GGSR Product Evacuation Project - WorleyParsons.com

ANNEXURE A 

TECHNICAL SPECIFICATION – MECHANICAL 

Doc. No. 0435-JH0902-00-PP-RFQ-0010

Guru Gobind Singh Refinery Products 

Evacuation Project (GGSRPEP) 

Raman Mandi- Bahadurgarh and Raman Mandi- 

Bhatinda Multiproduct Pipeline 

LIST OF ATTACHMENTS FOR COMPOSITE WORKS TENDER FOR TERMINALS 

AT RAMANMANDI & BATHINDA (MECHANICAL) 

435-JH0902-10-ME-LST-0015 

25-Aug-2009 

Sanghi Oxygen Compound 

1, Mahal Industrial Estate 

Mahakali Caves Road 

Andheri (East), Mumbai - 400 093 India 

Phone: +91-22-67818000 

Fax : +91-22-67818080 

www.worleyparsons.com 

© Copyright 2009 WorleyParsons 

Page 1 of 4

SYNOPSIS 

Disclaimer 

This report has been prepared on behalf of and for the exclusive use of Hindustan Petroleum 

Corporation Limited (HPCL), and is subject to and issued in accordance with the agreement 

between Hindustan Petroleum Corporation Limited (HPCL) and WorleyParsons. WorleyParsons 

accepts no liability or responsibility whatsoever for it in respect of any use of or HPCL upon this 

report by any third party. 

Copying this report without the permission of Hindustan Petroleum Corporation Limited (HPCL) or 

WorleyParsons is not permitted. 

PROJECT 435/JH0902- HPCL GURU GOBIND SINGH REFINERY PRODUCTS EVACUATION PROJECT 

(GGSRPEP) 

REV DESCRIPTION ORIG REVIEW WORLEY- 

PARSONS 

APPROVAL 

DATE 

CLIENT 

APPROVAL 

DATE 

A 

Issued for DIC / SQC 

Subramanyam 

.S 

Sameer 

Ishwad 

Jeremy 

Wallace 

08-July-09 

N/A 

B 

Issued for Review 

Subramanyam 

.S 

Sameer 

Ishwad 

Jeremy 

Wallace 

10-July-09 

N/A 

C 

Issued For Tender 

Subramanyam 

.S 

Sameer 

Ishwad 

KMN Pillai 

25-Aug-09 

Page 2 of 4

Sr. 

no. 

List of Attachments Document No. Revision No. 

1. Basis of Design (Mechanical) 0435-JH0902-00-ME-BOD-0001 Rev-2 

2. Scope of Work for Rotating 

Equipment & Packages (Part A & 

Part B) 

3. Technical Compliance for Rotating 

Equipment & Packages 

435-JH0902-00-ME-SOW-0001 

435-JH0902-00-ME-TEN-0001 

Rev-C 

Rev-C 

4. Specifications for Sump Pumps 435-JH0902-10-ME-SPC-0009 Rev-C 

5. Equipment Datasheet for 

Centrifugal Pumps (VS) at 

Bathinda 

6. Equipment Datasheet for 

Centrifugal Pumps (VS) at 

RamanMandi 

7. Inspection & Test Plan for Sump 

Pumps 

8. Experience Record Proforma for 

Vertical Submercible Pumps 

9. Experience Record Proforma for 

VSD’s & Motors 

10. Mandatory Spares for Vertical 

Submersible (VS4) Pumps 

0435-JH0902-10-ME-DAS-0016 

0435-JH0902-10-ME-DAS-0012 

435-JH0902-00-ME-ITP-0006 

435-JH0902-10-ME-LST-0014 

435-JH0902-10-ME-LST-0007 

435-JH0902-10-ME-SPL-0003 

Rev C 

Rev C 

Rev-C 

Rev-C 

Rev-C 

Rev-C 

11. 

Specification for EOT Crane 

435-JH0902-10-ME-SPC-008 

Rev C 

12. 

Specification for Corrosion Inhibitor 

Package 

435-JH0902-10-ME-SPC-0010 

Rev C 

13 Datasheet For Corrosion Inhibitor 

Package For Ramanmandi To 

Bahadurgarh Pipeline 

435-JH0902-10-ME-DAS-0011 

Rev C 

Page 3 of 4

14 Datasheet For Corrosion Inhibitor 

Package For Ramanmandi To 

Bathinda Pipeline 

15 Experience Record Proforma for 

Packages 

16 Inspection & Test Plan for Dosing 

Pump 

435-JH0902-10-ME-DAS-0013 

435-JH0902-10-ME-LST-0013 

435-JH0902-00-ME-ITP-0007 

Rev C 

Rev C 

Rev C 

17. Site & Utility Data 435-JH0902-10-ME-SPC-0007 Rev C 

18. Scope Of Work And Supply(Static 

Equipments Part A & B) 

19. General Specification For 

Pressure Vessels 

0435-JH0902-00-ME-SOW-002 

0435-JH0902-00-ME-SPC-0015 

Rev C 

Rev C 

20. ITP For Pressure Vessels 0435-JH0902-00-ME-ITP-008 Rev C 

21. Mandatory Spare Parts For Static 

Equipments. 

22. Specifications for Slop / Interface 

Pumps 

23. Mechanical Datasheets for Slop / 

Interface Pumps at Bhatinda 

24. Mechanical Datasheets for Slop / 

Interface Pumps at Bhatinda 

25. Mandatory Spares for Horizontal 

Centrifugal Pumps 

0435-JH0902-00-ME-SPL-004 

0435-JH0902-00-ME-SPC-0011 

0435-JH0902-20-ME-DAS-0022 

0435-JH0902-20-ME-DAS-0023 

0435-JH0902-00-ME-SPL-0005 

Rev C 

Rev C 

Rev C 

Rev C 

Rev C 

26. Inspection & Test Plan for 

Horizontal Centrifugal Pumps 

0435-JH0902-00-ME-ITP-0009 

Rev C 

27 Mechanical Datasheet for Sump 

Tank for Ramanmandi 

28 Mechanical Datasheet for Sump 

Tank for Bathinda 

0435-JH0902-10-ME-DAS-0009 

0435-JH0902-20-ME-DAS-0017 

Rev C 

Rev C 

Page 4 of 4

Hindustan Petroleum Corporation Ltd. 

(A Government of India Enterprise) 

GGSR Product Evacuation Project 

BASIS OF DESIGN 

MECHANICAL 

Document No.:0435-JH0902-00-ME-BOD-0001 

2 Reissued for Design SS SVI KMNP 27.08.09 

1 Issue for Design SS SVI AK 29/04/09 

0 Issue for client comment SS SVI AK 23/04/09 

rev Description Originated By Checked By Approved By Date 

Document No.:0435-JH-0902-ME-BOD-0001 Rev.1 Page 1 of 37

MECHANICAL DESIGN BASIS 

DESIGN PHILOSOPHY FOR 

PACKAGED, ROTARY& STATIC EQUIPMENT 


CONTENTS 

Sl.NO. 

DESCRIPTION 

1. Reference Publications 

2 Designed Philosophy / Criteria 


1.0 REFFERENCED PUBLICATIONS 

1.1 Codes & Standards (latest editions) published by the following bodies, including 

their latest addenda, shall be followed unless specified otherwise. 

ASTM : American Society for Testing and Materials 

ASHRE : American Society of Heating, Refrigerating and Air 

Conditioning Engineers. 

API : American Petroleum Institute 

ASME : American Society of Mechanical Engineers 

AGMA : American Gear Manufacturers’ Association 

NFPA : National Fire Protection Association 

OCIMF : Oil Companies International Marine Forum 

TEMA : Students of Tubular Exchanger Manufacturers’ Association 

OISD : Oil Industries Safety Directorate 

1.2 Statutory Provision 

National laws and statutory provisions, such as, Department of Explosives, 

Nagpur, India, together with any local by-laws for the State shall also the complied 

with. Static and Mobile Pressure Vessels (SMPV) Rules and Petroleum Rules, as 

applicable, shall be complied with. 

2.0 DESIGN PHILOSOPHY / CRITERIA 

2.1 SCOPE 

The Design basis defines the minimum criteria to be followed for the design of 

various mechanical Rotary and Static equipments/systems/packages. 

2.2 GENERAL DESIGN REQUIREMENTS 

While specific guidelines pertaining to individual rotary equipment/system/package 

are listed in subsequent sections, the following shall be considered for all items 

while formulating their specifications and also in their procurement engineering 

activities. 


- Reliability in service (assessed from vendor’s relevant track record and 

ensured by incorporating certain minimum design features or requirements 

in the specifications). 

- Compliance with applicable national or overseas codes and standards as 

well as application statutory regulations in existence for a specific item. 

- Ease of operation and maintenance including any necessary measures for 

ensuring safety of personal and equipment as well as a conducive working 

environment. 

- Standardization of components wherever feasible. 

- Adherence to any limitation of available space for the equipment and for its 

operation/maintenance. 

- Facility for any known future expansion of plant capacity. 

- Proven Track Record (PTR) of similar unit(s). 

2.3 DESIGN REQUIREMENTS FOR SPECIFIC APPLICATIONS 

I) Corrosion allowance for carbon steel and vessels shall be minimum 3mm, 

unless otherwise specified. 

ii) 

iii) 

iv) 

All components/equipment shall meet the requirements of respective area 

classification. 

Insulation shall be provided for personal protection for all surfaces at 

temperature higher than 70 0 C. 

All couplings, gears, and exposed rotating parts shall be provided with 

adequate protection guards 

001 AIR CONDITIONING SYSTEM 

1. Inside Design Conditions 

DBT, 0 C 

% RH 

ii) Computer Building with all 21 + 1 50 + 5 

associated rooms. 

Rev. 2 

iii) UPS & Battery charger 24 + 1 50 + 5 

Room/Variable Speed Drive 

panel Room/Operator Room. 

iv) Operation Staff/ 24 + 1 30 t0 70 


Administrative Building. 

2. All the areas as defined in Architectural details are to be air conditioned except 

Electric Room, Record Room and Toilets, which shall be force / induced ventilated 

only. 

3. Air conditioning system shall be through local Window and Split AC. 

4. For VFD Room, Instrument Calibration room, & HVAC room, Air conditioning shall 

Rev. 2 

be provided as per the Basis of Design HVAC 0435-JH0902-10-HV-BOD-0001 & 

Specification for HVAC 0435-JH0902-10-HV-SPC-0001 attached elsewhere with 

the tender 

002 BASKET FILTER 

1. Basket filters shall normally be used when particles of around 150 microns or 

larger size are to be filtered from a fluid stream. 

2. Filter shall be designed not to exceed the allowable pressure drop in clean and 

dirty conditions. 

Rev. 1 

3. In order to avoid the possibility of frequent basket cleaning the gross and free 

Rev. 1 areas shall be at least 20 and 16 times respectively of the filter inlet nozzle area. 

4. Rev. 1 Filter shall be Horizontal type with facility for removal of the basket from the side 

after opening the house cover (Quick Opening and Closing Type). 

5. Fluid flow shall be from inside to outside of the basket, unless specified otherwise. 

6. Fluid housing design shall be as per ASME Section VIII, Division 1. For steam 

jacketed housing, applicable IBR requirements shall also be complied with. 

7. Rev. 1 All the basket Filter shall be provided with Backwashing connection and provision 

for back washing of Basket Filter 

003 PRESSURISATION FOR SUBSTATIONS / VENTILATION SYSTEM 

1. Ventilation air requirement shall be calculated based on 3 0 C temperature rise of 

incoming air to room depending upon the suitability of electrical / equipment for the 

room temperature being maintained. 

2. Minimum air changes per hour shall be 12 in the room. 

3. Air intakes shall be located in non-hazardous and chemical fume-free areas at 

adequate elevation to protect against rains and dust. 

4. Pressurized areas shall have over pressure of 5 mm WG. 

5. Fire dampers shall be electric motorized type. 


004 Manual Hoists / Chain Pulley Blocks / EOT and HOT Crane 

Rev. 1 

1. Design and manufacture of chain pulley block with or without trolley shall be 

consistent with capacity, lift, head room and other parameters as specified in data 

sheets. 

2. In design of chain pulley blocks, care shall be taken for following features:- 

- Minimum effort to lift a specified load 

- Self breaking system for holding the load in any position 

- Even loading of bearings 

- Ease of installation and maintenance 

- Compact design 

3. For safe area application chain pulley blocks shall be as per IS: 3832 

4. For hazardous area application, the materials for non-lubricated rubbing parts shall 

be non-sparking type (non-ferrous) 

5. Rev. 1 EOT / HOT Crane 

5.1 These cranes are normally installed in main pump house for the primary 

purpose of handling equipment and components for maintenance or replacement. 

Other applications involving use of cranes during plant operation may also exist. 

5.2 The bridge structure of overhead traveling crane shall be made from box 

(double web) type, plate type, or fabricated from rolled sections. The structure can 

be single girder or double girder type. The use of single girder bridge is limited to 

lifting capacities up to 5 Ton and span and length upto 10 mtr. In case either of 

these values is exceeded, the double girder bridge shall be used. 

5.3 For cranes which are to operate in areas classified as hazardous besides 

ensuring that all electrical components are certified for use in specified hazardous 

areas materials of construction for rubbing non lubricated metallic parts should be 

specified in such a way that the possibility of sparking during operation is 

eliminated. This is done by having one part in every such pair made from a suitable 

non-ferrous material such as phosphor/aluminium or gun metal depending upon 

the application. 

5.4 Maintenance walkway shall be provided on both sides along the travel and 

minimum 750mm wide platform along traverse travel. 

5.5 Minimum capacity of the crane shall be max, weight of the equipment to be 

lifted plus 10% margin 

5.6 EOT CRANES: 

Unless otherwise stated the following hoisting and travel speeds shall be 

used: 


Hoisting : 2 m/min 

Cross travel : 10 m/min 

Long travel : 20 m/min 

Higher operating speeds may be considered for higher lifts and longer bay 

lengths. Suitable inching (creep) speed mechanism shall be provided to facilate 

accurate spotting of the load 

DC electromagnetic or thrustor brake shall be used for the hoisting motion. 

Electro hydraulic thrustor-operated brakes are used for the cross and long travel 

motions. 

Auxiliary hoist shall be provided in case of cranes having capacity 15T and above. 

Capacity of auxiliary hoist shall be 10% of crane capacity with min. 2MT. 

EOT crane shall be suitable for hazardous area application 


DESIGN BASIS 

FOR 

ROTATING EQUIPMENT 


CONTENTS 

Sl.No. Description Page No. 

1. REFERENCED PUBLICATIONS………………………………………………………………. 10 

2. DESIGN PHILOSOPHY………………………………………………………………… ……. 11 

2.1 SCOPE………………………………………………………………………………………….. 11 

2.2 CONFLICTING REQUIREMENTS……………………………………………………………… 11 

2.3 UNITISATION ………………………………………………………………………………… 11 

2.4 APPLICABLE CODES AND STANDARDS…………………………………………… ……. 11 

2.5 EQUIPMENT SELECTION AND SIZING CRITERIA……………………………………….. 11 

2.6 EQUIPMENT SPARING PHILOSPHY……………………………………………………….. 12 

2.7 EQUIPMENT QUALIFICATION 

CRITERIA……………………………………………………………………. 12 

2.8 EQUIPMENT SUPPLIERS 

2.9 ASSOCIATED ACCESSORIES AND AUXILIARY SYSTEMS……………………………. 12 

2.10 SEALING SYSTEM SELECTION CRITERIA……………………………………………….. 13 

2.11 COUPLINGS & COUPLING GUARDS………………………………………………………. 13 

2.12 ALLOWABLE NOISE LEVEL…………………………………………………………………. 13 

2.13 EQUIPMENT STORAGE………………………………………………………………………. 13 

2.14 INITIAL FILL…………………………………………………………………………………….. 13 

2.15 INSTALLATION CRITERIA……………………………………………………………………. 13 

2.16 SAFETY………………………………………………………………………………………… 14 

2.17 INSPECTION AND TESTING……………………………………………………………….. 14 

3. SPECIAL REQUIREMENTS………………………………………………………………… 14 

3.1 CENTRIFUGAL PUMPS (OTHER THAN WATER SERVICE)…………………………… 14 

3.2 CENTRIFUGAL PUMPS (WATER SERVICE)……………………………………………… 18 

4. SPARES & SPECIAL TOOLS……………………………………………………………….. 20 

4.1 COMMISSIONING SPARE PARTS…………………………………………………………. 20 

4.2 SPECIAL TOOLS/TACKLESS……………………………………………………………….. 21 

4.3 MANDATORY SPARES ………………………………………………………………………. 21 

4.4 SPARE PARTS FOR T WO YEARS NORMAL OPERATION…………………………….. 21 

5. DOCUMENT, DATA & DRAWING…………………………………………………………… 21 

5.1 GENERAL………………………………………………………………………………………. 21 

5.2 DRAWING AND DOCUMENTS REQUIRED ALONG WITH BID………………………… 21 

5.3 DRAWING AND DOCUMENTS REQUIRED DURING DET AILED ENGINEERING….. 21 


1. REFERENCED PUBLICATIONS 

The following codes are referred and applicable for the equipment as enlisted. 

Table 1: applicable/Referred Codes and Standards 

S.No. Description Standard / Codes Remarks 

1. PUMPS 

1.1 Centrifugal Pumps (Special Purpose Process Service) API Std.610 

(1) 

(10 th edn.) 

1.2 Centrifugal Pumps (General Purpose Process 

Rev. 1 

--- (2) 

Service) 

1.3 Centrifugal Pumps (General Water Service) ISO 5199, ASME B (3) 

73.1 

1.4 Centrifugal Pumps (Slurry & Liquor Service) --- 

1.5 Positive Displacement Pumps (Reciprocating) API Std. 674 

(2 nd edition) 

1.6 Positive Displacement Pumps (Controlled Volume) API Std. 675 


1.7 Positive Displacement Pumps (Rotary) API Std. 676 


2.0 AUXILIARIES 

2.1 Lubrication, shaft sealing and control-oil systems and API Std. 614 

auxiliaries 

(4 th edition) 

2.2 Shaft sealing for centrifugal & rotary pumps API Std. 682 


API Std 670 (4 th 

edition) 

2.3 Vibration, Axial Position & Bearing Temp. Monitoring 

Systems 

3. MISCELLANEOUS 

(For reference) 

3.1 Gear Units ANSI/AGMA 

3.2 Bearings ABMA 

3.3 Laboratory Methods of Testing Fans for Rating AMCA 

Purposes 

3.4 Mechanical Vibrations-Balancing quality requirements ISO 1940 

of rotating rigid rotors 

Remarks: 

(1) Centrifugal pumps for special purpose process service are classified as 

pumps which are meant for process service (both for on-site & offsite) but 

excluding the pumps covered either under general-purpose process service or 

general water service. 

(2) Centrifugal pumps for general purpose process service are classified as 

pumps for applications where maximum pressure by all consideration does not 

exceed 16.0 kg/cm 2 g. pumping temperature remains within -29 0 C to 205 0 C, 

specific gravity is not less than 0.7 at the specified operating conditions or when 

dual pressurized / un-pressurized mechanical seals are not required/specified. 

Typical areas of application are non-process services & utility services such as Demineralised 

Water (DMW) plans, /raw Water Treatment Plants (RWTP), Effluent 

Treatment Plants (ETO), Blow-down services etc. 


(3) Centrifugal pumps for general water service are classified as pumps for 

applications such as Large Capacity Cooling Water Pumps, Auxiliary Cooling 

Water Pumps & other centrifugal pumps handling clean & cold water. 

(6) General-purpose gear units (conforming to API Std. 677) shall be used in 

equipment trains that are usually spared, or are in non-critical serviced and up-to a 

maximum driver rating of 750 KW. all ID fan trains are to be considered as meant 

for non-critical service. 

(7) Special-purpose gear units (conforming to API Std. 613) shall be used in 

equipment trains that are usually not spared, or are in critical service. 

(8) Special-purpose couplings (conforming to API Std. 671) shall be used in 

equipment trains, as special in the EDB. 

2. DESIGN PHILOSOPHY 

2.1 SCOPE 

The specification covers the design criteria for the purpose of carrying out 

Engineering for Procurement of various rotating equipment required including 

requirements with regard to spare parts & special tools. This EDB shall be applied 

for project of GGSR Product Evacuation Project. 

Electrical items, Instrumentation & Controls, Piping, Pressure Vessels, Mechanical 

Equipment, etc. associated with rotating equipment shall comply with the design 

requirements as given in the respective specifications forming part of the bid 

package / inquiry. 

2.2 CONFLICTING REQUIREMENTS 

In case of conflict between this Engineering Design Basis and other attached and / 

or refereed specifications, the following order of precedence shall govern: 

(a) Process Package approved by HPCL/WP 

(b) P&ID’s (if any) 

(c) This Design Basis 

(d) Other specifications (if any) 

(e) Other referred codes and standards. 

2.3 UNITISATION 

Unitisation where specified shall be carried out manufacturer’s shop before 

dispatch. For other equipment the same may be done at site / shop, as preferred, 

under direct supervision of driven equipment manufacturer’s representatives. 

2.4 APPLICABLE CODES AND STANDARDS 

Equipment Process Data Sheets, P&IDs, Specification and Standards / Codes (as 

per the table 1) along with the requirements specified in this Design Basis shall be 

the basis of design, selection, manufacture, inspection/testing of the equipment. 

For design aspects not specifically covered herein, the design shall be based on 

good engineering practices. 


2.5 EQUIPMENT SELECTION AND SIZING CRITERIA 

2.5.1 Selection of Rotating Equipment shall be based upon the following considerations. 

- Suitability for the specified duty conditions 

- Standard Models under vendor’s regular range of manufacture 

- Proven Track record in similar service as specified under acceptance 

criteria. 

2.5.2 Allowable working pressure & temperature of the rotating equipment shall be 

greater than the higher of design pressure & temperature specified in:- 

- The equipment data sheet (if any) 

- Engineering specifications, codes & standards. 

2.5.3 All rotating equipment & drivers (including gear units and couplings if any) shall be 

designed to perform satisfactorily under specified start up conditions, part load 

operation, maximum differential pressure operation and relief valve set pressure 

and up to full speed/maximum conditions speed. 

2.6 EQUIPMENT SPARING PHILOSOPHY 

The equipment Sparing philosophy including warehouse spare requirement shall 

be as specified in the process package and or bid package. 

2.7 EQUIPMENT QUALIFICATION CRITERIA (EQC) 

All Rotating Equipment shall be field proven and meet the EQC as specified in the 

special requirements of the relevant rotating equipment, as applicable. Rotating 

Equipment Vendor/LSTK Contractor shall complete the Experience Record 

Performa’s enclosed with the inquiry document to amply prove that the offered 

Rotating Equipment meet the EQC for technical acceptance. In addition 

manufacturer’s catalogue and general reference list for Rotating Equipment shall 

also be furnished during detailed engineering by the Contractor. 

2.8 EQUIPMENT SUPPLIERS 

The equipment supplier shall be one from the approved list of vendors provided 

elsewhere in the bid package. 

2.9 ASSOCIATED ACCESSORIES AND AUXILIARY SYSTEMS 

2.9.1 The Vendor shall furnish all rotating equipment, drivers, auxiliary systems, 

instrumentation and control systems, all necessary electrical and safety devices as 

applicable or required for safe and reliable operation of the unit. 

The Vendor/ Contractor in his scope of supply and work shall also include the 

hardware required over and above what is specified, for safe and satisfactory 

operation of the equipment 

2.9.2 Motors, electrical/instrument components and electrical/instrument installations 

shall be suitable for the area classification specified by the purchaser, and shall 


meet the requirements as defined in the electrical/instrument specification attached 

with the relevant sections of the bid package / order. 

2.10 SEALING SYSTEM SELECTION CRITERIA 

2.10.1 Centrifugal Pumps 

2.10.1.1 All pumps shall be provided with mechanical seals (except. clean cold water 

service). 

2.10.1.2 Tank/Pit mounted vertical pumps (process service) shall be provided with dry 

running vapours seals. In case of handling Hazardous or toxic fluids this vapour 

seal shall be Nitrogen buffered. 

2.11 COUPLINGS & COUPLING GUARDS 

2.11.1 Unless otherwise specified, couplings shall be of metallic, non-lubricated, flexible 

element type (i.e. either diaphragm or discs) with spacer, for all equipment. All 

coupling models shall be selected for a minimum service factor of 1.5. 

2.11.2 Couplings for the following equipment shall conform to API Standard 671: 

- Multi-stage (greater than two stages) centrifugal pumps with driver rating 

greater than 160 kW. 

2.11.4 Universal type coupling (hook joint) shall be used for coupling diesel engine and 

the vertical water pumps. 

2.11.5 Removable coupling guard shall be provided which shall be fabricated from nonsparking 

material, and shall be open at the bottom to permit manual shaft rotation. 

The guard shall be sufficiently rigid to withstand deflections as a result of body 

contact of nominally 100 kgs. 

2.12 ALLOWABLE NOISE LEVEL 

2.12.1 Equipment noise level (Driver + Driven equipment train + auxiliaries) shall not 

exceed 85 when measured at One-meter distance from the equipment skid in any 

direction, 

2.13 EQUIPMENT STORAGE 

2.14 INITIAL FILL 

All rotating equipment shall be packed for an outside storage period of at least 12 

months. 

The initial fill of lubricants, sealing fluid & other consumables for start-up & 

commissioning shall be included in the scope of supply of the Vendor 

2.15 INSTALLATION CRITERIA 


2.15.1 Pumps 

2.16 SAFETY 

All pumps shall be suitable for outdoor installation. 

2.16.1 Equipment design and engineering shall incorporate adequate safety features (as 

per applicable specifications of respective equipment as well as Health. Safety 

and Environment Codes & Standards applicable for the subject project) to provide 

protection to operating personnel, equipment and environment 

2.16.2 Thermal relief valves shall be provided for components that may be blocked in by 

isolation valves (including any cooling water return circuit piping). 

2.16.3 All electrical components & installations, instruments shall be suitable for the 

electrical area classification and grouping in which the equipment is installed. 

2.17. INSPECTION AND TESTING 

2.17.1 Inspection and test specified in the bid package shall be carried out by the 

Equipment Vendor at his works. The Vendor shall conduct inspection and witness 

tests of all equipment at vendor’s works and furnish inspection and test reports to 

the owner. 

2.17.2 Owner and/or his consultant/ TPIA may participate along with the vendor’s 

inspection personnel in any inspection and tests. The vendor shall notify to owner/ 

consultant of all inspection and tests at least four weeks before the scheduled date 

of inspection and test and reconfirm the same at least one week before the date of 

inspection and testing. 

3.0 SPECIAL REQUIREMENTS 

3.1 CENTRIFUGAL PUMPS (OTHER THAN WATER SERVICE) 

3.1.1 EQUIPMENT QUALIFICATION CRITERIA 

3.1.1.1 The vendor shall be an established centrifugal pump manufacturer having 

adequate engineering, manufacturing and testing facilities for pumps conforming to 

API Standard. 

3.1.1.2 The pump model offered shall be from the existing regular manufacturing range of 

the vendor. The mechanical as well as hydraulic performance (including NPSHR) 

for the complete range of operation of the offered model shall have been 

established in the shop test. 

The offered pump model shall meet the following minimum service and 

manufacturing experience requirements: 


Rev.1 

Pumps shall be identical or validly similar in terms of Power rating, Hydraulic 

Performance (including NPSHR), Inlet flow, differential Head, Operating Pressure 

& Temperature, Pumping Liquid, Speed, Number & Type of Impellers, Mechanical 

Design, Materials, Bearing span (applicable for between bearing pumps), Column 

Length (applicable for vertically suspended pumps) etc. and compared to at least 

TWO UNITS of the proposed model designed, manufactured, tested and supplied 

from the proposed manufacturing plant in the last seven years and at least ONE of 

these units shall have successfully operated in the field for at least 8000 hours 

individually without any major problem as on the date of issue of inquiry. 

3.1.1.3 The vendor should have engineered, packaged, tested (performance test, string 

test etc.) and supplied at least TWO identical or validly similar pumping units in 

terms of construction (axially or radically split), size of pumps (flow, head and 

power), lubrication system, sealing system and type of drive from the proposed 

Rev.1 shop in the last seven years and at least ONE of these units shall have 

successfully operated in the field for at least 8000 hours individually without any 

major problem as on the date of issue of inquiry. 

3.1.2 Two stage pumps shall be of in-between bearing types. 

3.1.3 Inducers shall not be used except for Sundyne or equivalent type of pumps. 

3.1.4 Pumps for high head, low flow duties (falling outside the range of two stage pumps 

without continuous bypass) shall be Sundyne or equivalent type. 

3.1.5 Pumps where difference between NPSHA and NPSHR is less than 0.6 meter are 

not acceptable. The said NPSHR value shall correspond to the maximum value of 

NPSHR from rated flow down to the recommended minimum continuous stable 

flow specified by the vendor. 

3.1.6 The maximum permissible running clearances shall not be less than twice the 

running clearances as specified in API610. 

3.1.7 Impeller of multistage pumps shall also be positively locked against axial 

movement in the direction opposite to normal hydraulic thrust. 

3.1.8 Mechanical Seal for pumps shall conform to API-682. Mechanical Seals shall be 

imported either in fully assembled condition OR the critical components shall be 

imported by Indian seal manufacturers from their respective principals and the 

seals shall be assembled and tested in the indigenous of these seal 

manufacturers. Qualification test results of each seal shall be furnished during 

detail engineering for review. 

3.1.9 Pumps shall be provided with single mechanical seals (except for clean cold water 

service pumps where gland packing is acceptable). For services involving solid 

contaminants, hazardous/toxic services, light hydrocarbons such as LPG, NEL, 

Naphtha, liquid gasses and services involving liquids at or above auto ignition 

temp., duel mechanical seal shall be used. 

3.1.10 


(a) 

(b) 

(c) 

(d) 

Pumps handling non-congealing liquids at temperatures 200 0 C and above 

shall be provided with API seal flushing plan 23 or 32 where single 

mechanical seals are provided Plan 32 

Cooler shall not be provided in seal flushing system where seal is flushed 

by congealing liquid. 

For pumps provided with flushing Plan 21 and 23. Temperature Indicator 

shall be provided in the flushing line. 

Seal Plans 52 & 53 (for API-610 Pumps ) shall be as per sketches as per 

API 682. 

3.1.11 In case Multistage pumps require force feed lubrication, the same shall conform to 

flg .B.10 of API-610, 10 th edition. 

The instruments shall be suitable for the specified area classification and shall be 

from approved vendors (specified elsewhere in the bid package). 

3.1.12 The motor nameplate rating for pumps under parallel operation/auto start shall not 

be less than the max. BKW indicated on pump data sheet (Power at End of he 

curve for the rated impeller) and the pump motor shall be suitable for start-up 

under open discharge valve condition. 

3.1.13 The motor nameplate rating for application where the specific gravity of pumped 

fluid is less than 1.0 shall not be less than the BKW of pump at minimum 

continuous stable flow with clean cold water of sp. gravity 1.0. 

3.1.14 The coupling service factor shall not be less than 1.5 over the driver rating as a 

minimum. 

3.1.15 Coupling guard shall be perforated and of non-sparking material. The guard shall 

be open at the bottom to permit manual shaft rotation. The guard shall be 

sufficiently rigid to withstand deflections as a result of bodily contact of nominally 

100 kgs. The guard for pumps/motors should have proper and convenient 

arrangement for vibration readings. 

3.1.16 Hydraulic Power Recovery Turbines shall be optimized for best efficiency at 

Normal Flow. 

3.1.17 INTERCHANGEABLITY: As far as possible pumps & mechanical seals and 

couplings shall be of identical make so that minimum levels of inventory can be 

maintained and maximum interchangeability /standardization can b achieved. 

3.1.18 All pumps not open to sky with motor rating equal or higher than 75 kW shall be 

provided with monorails. No monorails should normally be provided for pumps 

outside the rack. Sufficient space below rack shall be available for pump 

maintenance. 

3.1.19 Whenever pumps capacity control is through LIC or LIC/FIC cascade or has a fail 

closed control valve on pump discharge or process minimum capacity is less than 

pump MCF, necessary flow instruments in pump discharge along with pump 

bypass back to suction vessel with control valve for pump protection shall be 


provided. However when continuous Bypass of pump MCF is envisaged bypass 

from pump discharge back to suction vessel with restriction orifice sized for pump 

MCF instead of control valve shall be provided. 

3.1.20 Equipments along with the drivers shall be procured from the respective driven 

equipment manufacturers as skid mounted units with all accessories, auxiliaries 

along with auxiliary piping. 

3.1.21 Magnetic drain plug shall be provided for all centrifugal pumps bearing housings. 

3.1.22 For seal flushing plans, piping material shall be of Stainless Steel. For cooling 

water plans, piping material shall be carbon steel. 

3.1.23 All pumps shall be provided with plugged connection for oil mist lubrication for 

future use. 

3.1.24 All pumps shall be provided with bearing isolators. 

3.1.25 Inspection and Testing (For Each Pump) : 

3.1.25.1 Material Certificates for the following are required. 

3.1.25.2 The material inspection requirement for pressure containing parts shall be as per 

the following inspection category. 

Category A: 

This category is applicable for carbon steel and cast iron for services with process 

design pressure upto 40 bar and design temperature from 0 to 150-0-C. 

Inspection requirement: As per vendor’s standard Quality/Assurance Plan. 

Category B: 

The category is applicable for services within the design pressure range of 0-70 

bar and temperature range of -29 0 C to 300 0 C. 

Inspection requirement includes visual inspection and magnetic particle or liquid 

penetrant inspection of following components as a minimum: 

- Nozzle weld 

- But t welds on pressure containing components. 

- Fillet welds on pressure containing components. 

- Shaft 

Liquid penetrant inspection shall be performed only when specified magnetic 

particle inspection is not feasible. 

Category C: 

This category is applicable for services with process design pressure above 70 bar 

or process design temperature below -29 0 C and above 300 0 C. Inspection includes 

all the requirements of Category B together with radiographic or ultrasonic 

inspection of 

- Nozzle weld 

- Butt welds on pressure containing components. 

Ultrasonic inspection shall be carried out when radiography is not feasible. 


3.1.25.3 Inspection shall also include dimensional check of pump, drier and auxiliaries (if 

any) duly mounted on the base plate, in accordance with certified general 

assembly drawing. This will include all main pump dimensions, base plate 

dimensions, location of foundation bolt holes, size /position/rating of flanges, 

coupling guard arrangement, verification of the required material certificates and 

their traceability to the respective components. In addition, following checks shall 

also be carried out: 

- A measurement of the actual running clearances throughout the pump. 

- A check of the hardness of wear rings. 

- A check for good workmanship and finish throughout. 

3.1.25.4 The following tests shall be witnessed by owner’s inspecting agency: 

- Hydrostatic (For all pressure containing parts including auxiliaries) 

- Performance 

- NPSH (In case difference between NPSHA and NPSHR is less than or 

equal to 1.0 m or when specified in the job specification) 

- Dismantling inspection and reassembly after the running test, which shall 

included examination of mechanical seals, close clearance parts and 

measurement of running clearances. In case of multistage pumps having 

hydrodynamic bearings, the bearing shall be removed inspected and 

reassembled. 

- Sound level Test (During Performance Test) 

3.2 CENTRIFUGAL PUMPS (WATER SERVICE) 

3.2.1 Equipment qualification criteria 

3.2.1.1 The pump vendor shall be an established centrifugal pump manufacturer having 

adequate engineering, manufacturing and testing facilities for Centrifugal Pumps 

(Water Service). 

3.2.1.2 The pump model offered shall be from the existing regular manufacturing range of 

the pump manufacturer. The mechanical as well as the hydraulic performance 

(including NPSHR) for the complete range of operation of the offered model shall 

have been established in the shop test. The offered pump model shall meet the 

following minimum service and manufacturing experiences requirements. 

Pumps shall be identical or validly similar in terms of Power rating, Hydraulic 

Performance (including NPSHR), Inlet flow, Different Head, Speed, Number & 

Type of impellers, Mechanical Design, Materials, Bearing span (applicable for 

between bearing pumps), Column Length (applicable for vertically suspended 

pumps) etc. as compared to a lest TWO UNIS of the proposed model 

manufacturer, tested and supplied from the proposed manufacturing plant in the 

Rev. 1 

last seven years and at least ONE of these units shall have successfully operated 

in the field for at least 8000 hours individually without any major overhaul as on the 

date of issue of invitation to bid. 

3.2.2 Pumps with constant speed drivers shall be capable of at least 5 percent head 

increase at rated condition and pump rated speed by replacing with a new impeller 


or impellers. Offered impeller shall in no case be less than the minimum diameter 

impeller. 

3.2.3 Horizontal pumps of the close-coupled, the two stage overhung, or the single stage 

double suction overhung, type shall not be furnished. 

3.2.4 Pumps where difference between NPSHA and NPSHR is 0.6 meter or less are not 

acceptable. The said NPSHR value shall correspond to the maximum value of 

NPSHR from rated flow down to the recommended minimum stable flow specified 

by the vendor. 

3.2.5 Pumps that have stable head/capacity curves (continuous head rise to shut-off) are 

preferred for all applications and are required when parallel operation is specified. 

When parallel operation is specified, the head rise shall be at least 10 percent of 

the head at rated capacity. 

3.2.6 Vertical pumps & motors that could be damaged due to reverse rotation shall be 

proved with non-reverse rated or suitable device to prevent reverse rotation. 

3.2.7 Impellers shall be cast as one piece. 

3.2.8 Shaft shall be provided with sleeves under the packaging/seal. Sleeves shall be 

locked to the shaft. The material of sleeve shall be 12 percent chrome steel 

(hardened). Where the size of pump makes the use of shaft impracticable, the 

shaft shall be constructed of 12 percent chrome steel (hardened). For vertical 

pumps, shaft material shall be 12 percent chrome steel. 

3.2.9 The following vibration limits shall be applied at rated speed and at flow of +10 

percent of rated flow. 

Rev. 1 

3.2.9.1 Horizontal pumps 

Unfiltered vibration velocity for horizontal pumps upto 3000 rpm with antifriction 

bearing or sleeve bearings when measured at the bearing housing in horizontal or 

vertical direction shall not exceed 7.6 mm/sec (0.3 inch/sec.). 

3.2.9.2 Vertical Pumps 

Unfiltered vibration velocity for vertical pumps with antifriction and or sleeve 

bearings when measured at the top bearing housing of pump or top bearing 

housing of motor or mounting flange for measuring points upto 3 meters above the 

mounting base shall not exceed the following limit: 

Pumps greater than 1500 rpm (Peak to Peak) = 10.1 mm/sec. 

(0.4 inch/sec) 

Pumps upto & including 1500 rpm (Peak to Peak) = 8.9 mm/sec. 

(035 inch/sec.) 

3.2.10 Pumps for Fire Water Application shall also meet the following additional 

requirements: 


- Pumps shall be direct-coupled except in the case of engine-driven vertical 

turbine pumps wherein gear drives shall be used. 

- Pumps shall be capable of furnishing not less than 150 percent of rated 

capacity at a head not less than 65 percent of the rated head. Shut off 

head shall not exceed 120 percent of rated head in horizontal pumps and 

140 percent in the case of vertical turbine pumps. 

- Difference between NPSHA and NPSHR at 150 percent of the duty point 

shall not be less than 0.5 meters. 

- For Diesel engine drivers, the net continuous site power available after 

considering the duration due to site condition and power losses, due to 

other parasitic loads and engine driven auxiliaries shall of the following two 

values: 

(a) 20 percent in excess of the maximum BKW (including + 4% 

tolerance) required to drive the pump at rated condition. 

(b) Maximum BKW rated impeller as indicated by the manufacturer in 

the pump data sheets. 

3.2.11 Electrical motor drivers as per (IEC/IS) shall be rated for continuous duty (Duty 

type S1) whereas motor as per American Standards shall be designed to operate 

at a service factor of 1.0 Rating shall not be less than the following unless higher 

rating is dictated by the Note-1. 

Motor Name plate rating 

Less than 22 KW. 

22kW – 55 kW 

Higher than 55kW 

Motor MCR (%of Pump Rated BKW inclusive of 

+4% tolerance) 

To suit maximum BKW indicated on pump data 

sheet or 125% of rated pump BKW, whichever is 

higher. 

115% of rated pump BKW 

110% for rated pump BKW 

Note: 

1. The motor nameplate rating for pumps under parallel operation shall not be 

less than the max. BKW indicated on pump data sheet (the power at End of 

the Curve for the rated impeller) or shall have the specified margin as per 

this clause whichever is greater. The pump motors shall also be suitable 

for start-up under open discharge valve condition, 

3.2.11.1 INSPECTION AND TESTING 

Refer Centrifugal Pumps (Other than water service). 

4. SPARES & SPECIAL TOOLS 

4.1 COMMISSIONING SPARE PARTS 

Rev. 1 

Commissioning Spare Parts should be supplied free of cost by the equipment 

vendors. Vendor to supply mandatory spares and provide list of recommended 

spares for two years normal operation. 

4.2 SPECIAL TOOLS/TRACKLES 


Special Tools/Tackles shall be procured along with the main equipment as per 

equipment manufacturer’s recommendations. The list of such recommended shall 

be provided by vendor 

Rev. 1 

4.3 MANDATORY SPARES 

Mandatory spares, as specified in the bid package shall be procured along with the 

main equipment. Spare rotors where supplied shall be boxed in a metal containers 

for vertical storage. 

4.4 SPARE PARTS FOR TWO YEARS NORMAL OPERATION 

As per rotating equipment manufacturer’s recommendations, a quotation for spare 

parts for two-year normal operation along with unit price shall be furnished with the 

proposal for customer to order the same separately. Customer shall indicate, in 

case these spares are required to be order along with the equipment or to be 

ordered separately. 

5. DOCUMENTS, DATA & DRAWINGS 

5.1 GENERAL 

The Consultant shall develop detailed specifications for vendor data requirements 

pertaining to each type of Rotating Equipment as applicable in accordance with the 

owner’s requirements specified in the enquiry document. This specification shall 

form part of the Consultant’s / Owner’s purchase requisition for the type of Rotating 

Equipment. 

The Consultant shall be responsible for the review & approval of all Vendor Data & 

Drawing submitted by the Equipment manufacturer. Owner’s / Consultant’s review 

/ approval shall be limited to the vendor drawing and other documents as specified 

in the document entitled “Vendor Data, Document & Drawing for Owner / 

Consultant’s review” 

5.2 DRAWING AND DOCUMENTS REQUIRD ALONG WITH BID 

The Vendor shall furnish the following along with the bid: 

(a) Technical Compliance Pro-forma, duly completed. 

(b) List of deviations if any, to the applicable specifications. 

5.3 DRAWING AND DOCUMENTS REQUIRED DURING DETAILED ENGINEERING. 

The vendor shall submit all the documents and drawings pertaining to design, 

engineering and procurement of all Rotating Equipment as specified in Vendor 

Data. 

Requirements for Owner’ review and record. Number of prints to be submitted 

shall be as specified in the Contract. 


DESIGN BASIS 

DESIGN PHILOSOPHY 

STATIC EQUIPMENT 


CONTENTS 

Sl.No. 

DESCRIPTION 

1.0 Referenced Publications 

2.0 Design Philosophy/Criteria 

2.1 Equipment sizing 

2.2 Minimum shell / head thickness 

2.3 Equipment end closures 

2.4 Design pressure 

2.5 Test pressure 

2.6 Design temperature 

2.7 Corrosion allowance 

2.8 Wind consideration 

2.9 Earthquake consideration 

2.10 Capacity 

2.11 Supports 

2.12 Manholes 

2.13 Floating roof 

2.14 Nozzle size 

2.15 Flanges 

2.16 Internals 

2.17 Pipe davit 

2.18 Vent/drain/ventilation nozzle connections 

2.19 Spares 

2.20 MP connections for PG/TI 

2.21 Important considerations 

2.22 Heat exchangers 

2.23 Air coolers 

2.24 Bought out suppliers 

3.0 Design criteria/requirements – specific applications 

3.1 Storage spheres 

3.2 Tall columns 

3.3 Storage tanks 

3.4 Mounted bullet 

3.5 Reactors 

3.6 Double walled storage tank 

4.0 Project specific requirements 

Table-I 

Table-II 

Annexure-I 

Detail & wt. of column attachment 

Allowable stress for combined loading 

Material selection 


1.0 REFERENCED PUBLICATIONS 

a) The following codes and standards in their latest edition including latest addenda 

as on the date of first issue of this design basis shall be followed unless otherwise 

specified in the requisition for the design, fabrication, inspection and testing of 

Vessels, columns, Reactors, Spheres, Storage Tanks, Steel Silos, Bins, Hoppers, 

Steel Flare/Vents Stacks & heat exchangers. 

ASME SEC. VIII DIV.1 

API 650/IS:803 

API 2000 

OISD-118 

ASME SEC.II 

ASTM/IS 

IS: 875/SITE DATA 

IS: 1893/SITE DATA 

ASME SEC.IX 

ASME B 16.5 

ASME B 16.20 

For Pressure Vessels, 

For Atmospheric Storage Tanks 

Venting Atmospheric Storage Tanks 

for Oil and Gas Installation 

For material specification 

For material specification 

For wind load consideration 

For seismic design consideration 

For welding 

For flanges 

For gaskets 

b) Statutory Provisions: 

National laws and statutory provisions such as Indian Boiler Regulation and 

Department of Explosives, Nagpur, India together with any local by-laws for 

the state shall be complied with. Static and Mobile Pressure Vessel 

(SMPV) rules and Petroleum rules as applicable shall also be complied 

with. 

c) Publications 

ISO 15156 

. 

WRC Bulletlin#107 

WRC Bulletin#297 

Containing environments in oil and gas production 

Local Stresses in Spherical & Cylindrical Shells due 

to External Loadings. 

Local Stresses in Cylindrical Shells due to External 

Loadings on Nozzles 


2.0 DESIGN PHILOSOPHY / GENERAL CRITERIA 

Equipment shall be designed in compliance with the latest design code 

requirements and applicable standards/specifications. All design calculations shall 

be performed considering all applicable loads for erection, operating and hydro test 

conditions. 

2.1 Equipment Sizing 

c) Vessels (Thickness 50mm) Based on inside diameter 

d) Tanks Based on API 650 

Rev. 1 

2.2 Minimum Shell/Head Thickness 

Minimum thickness of equipment wall/components shall be as given below: 

a) For carbon and low alloy steel vessels – 6 mm (including corrosion allowance not 

exceeding 3.0), but not less than that calculated as per following: 

For diameters less than 2400 mm 

Wall thickness = Dia + 1.5 + Corrosion Allowance 

1000 

For diameters 2400 mm and above 

Wall thickness = Dia + 2.5 + Corrosion Allowance 

1000 

(if any) 

(if any) 

All dimensions are in mm. 

b) For stainless steel vessels and high alloy vessels – 3 mm, but not less than that 

calculated as per following for diameter n\more than 1500 mm. 

Wall thickness (mm)= Dia + 2.5 + Corrosion Allowance (if any) 

1000 

2.3 Equipment End Closures: 

- Unless specified otherwise Deep Torispherical Dished end with 80% crown radius 

and 15% knuckle radius of alternatively 2:1 semi Ellipsoidal Dished End shall be 

used for pressure vessels 

- Hemispherical Ends shall be considered when the thickness of shell exceeds 70 

mm. 

- Flat Covers may be used for atmospheric vessels. 

- Flanged Covers (consisting of standard forged WN flanges and blind flange as per 

ASME B 16.5 shall be used for Vessels of diameter < 900 mm having internals. 


- All columns 900 mm and below shall be provided with intermediate body flanges. 

Numbers of intermediate flanges shall be decided based on column height and 

type of internals. 

2.4 Design Pressure 

Unless specified otherwise elsewhere design pressure shall be calculated as per 

the following 

a) When operating pressure is up to and including 70 Kg/cm 2 g. 

Design pressure shall be equal to operating pressure plus 10% (minimum 2 

Kg/cm 2 g). 

b) When operating pressure is over 70 Kg./cm 2 g. 

Design pressure shall be equal to operating pressure plus 10% (minimum 7 

Kg/cm 2 g). 

Rev. 1 

c) Design pressure calculated above or specified in data sheet shall be at the top of 

vertical equipment or at the highest point of horizontal equipment. 

d) The design pressure at any lower point is to be determined by adding the 

maximum operating liquid head and any pressure gradient within the equipment 

(differential pressure as mentioned in Process Data Sheet). 

e) Equipment operating under vacuum/Partial vacuum shall be designed for an 

external pressure of 1.055 Kg./cm 2 g. 

f) Equipment shall be designed for steam out conditions as specified by process data 

sheet/piping. 

2.5 Test Pressure 

a) Equipment shall be hydrostatically tested in the fabricator’s shop as per design 

code. 

b) Equipment open to atmosphere shall be tested by filling with water to the top. 

Coils shall be tested separately to code test pressure. 

Rev. 1 

d) Unless others\wise specified in applicable design code allowable stress during 

hydro test in tension shall not exceed 90% of yield point. 

e) Storage tanks shall be tested as per applicable code. 

2.6 Design Temperature 

Unless otherwise specified elsewhere, design temperature shall be as per the following: 

a) For vessels operating at 0 0 C and over: 


Design temperature shall be equal to maximum operating temperature plus 

15 0 C subject to a minimum of 65 0 C. 

b) Minimum Metal design Temperature (MDMT) shall be lower of minimum 

atmospheric temperature and minimum temperature envisaged during operation. 

2.7 Corrosion Allowance: 

Unless otherwise specified elsewhere, minimum corrosion allowance shall be considered 

as follows: 

- Carbon Steel equipment : 3.0 mm* 

- Stainless steel equipment : Nil 

- CS Storage Tank bottom most shell : 1.5 mm 

course and bottom plate 

Rev. 1 

- CS Storage Tank shell (other : 1.5 mm 

course) 

- Storage tank Fixed roof/floating : Nil 

Roof 

- CS Buried Vessels (External) : 1.5 mm 

Corrosion allowance for nozzles and manholes neck shall be at lest equal to that 

specified for the equipment. No corrosion allowance is required for gasket sealing face of 

flanges. However, for non-standard blind flanges of channel covers the corrosion 

allowance will be applied. 

2.8 Wind consideration 

Wind load shall be calculated on the basis of IS 875/site data for skirtsupported 

equipment, storage flanks spheres, flare stacks and air coolers. 

a) Drag coefficient for cylindrical vessels shall be 0.7 minimum. 

b) Drag coefficient for spherical vessels shall be 0.6 minimum. 

c) Basis wind speed as per zone and area specified in IS 875 part 3. 

d) Of the factors shall be s below- 

K1=1.0 

K2 shall be based on Category 3 for units and 2 for offsite. 

K3=1.0 

A contingency fact or of 1.1 shall be applied to wind pressure. 

Rev. 1 

2.9 Earthquake Consideration: 

Earthquake loads for equipment shall be calculated in accordance with site specific 

acceleration spectra specified in the project specification. 


2.10 Capacity 

2.10.1 Tank 

- Nominal capacity for fixed roof tanks shall be volume of cylindrical shell. 

- Stored capacity for fixed roof tanks shall be equal to nominal capacity 

minus free board volume (equivalent to 500mm of shell height) 

- Nominal capacity (also stored capacity) for floating roof tanks shall be 

volume of cylindrical shell minus free board volume (equivalent to 1500 mm 

of shell height). 

- Nominal capacity (also the stored capacity) for fixed cum floating 

roof tanks shall be volume of cylindrical shell free board volume (equivalent 

to 2500 mm to 3000 mm of shell height for tanks with vent / overflow slot in 

shell). 

2.10.2 Buried vessels shall be suit ably anchored to prevent the uplift due to under ground 

water. Anchor bolts shall have corrosion allowance of 6 mm on diameter. Buried 

vessels shall be rest ed on concrete saddles with anchoring bracket at the bottom 

of the vessel. 

2.11 Manholes: 

a) Vessels with diameter greater than 900 mm and up to 1500 mm shall be 

provided with 500 NB manholes. However, if required, vessels and 

columns with diameter 1500 mm and above may be provided with 600 NB 

manholes. 

b) High pressure reactor manholes shall be on I.D. basis/. Size shall be as 

per licensor drawing. 

c) For storage tanks minimum number of manholes (Size 600mm) shall be as 

follows:- 

TANK DIAMETER SHELL FLUSH TYPE ROOF* 

MANHOLE CLEAN OUT DOORS MANHOLES 

Diameter. #12m 2 Nil 2 

Rev. 1 Rev. 1 

12 m

2.12 Floating roof: 

a) Clean out doors shall be provided as per client’s / process requirements 

and size of clean out doors fittings for tank shall be 36” (900mm) x 48” 

(1200m), 

2.12.1 Unless otherwise specified floating roof shall be of following construction 

TANK DIAMETER (D) 

TYPE OF FLOATING ROOF 

(a) 

(b) 

External 

Internal 

D # 12 m Double Deck Type Double Deck 

12 m < D # 60m Pontoon Type Pontoon Type @ 

D > 60m Double Deck Type Double Deck 

2.13 Nozzle Size: 

- Minimum Nozzle Size ; 40 NB 

- Safety Valve Nozzle : Based on I.D. 

_ Self Reinforced Nozzle neck : Based on I.D. 

2.14 Flanges 

2.14.1 Nozzle flanges up to 600 NB shall be as per ASME B16.5 and above 600 NB shall 

be as per ASME B 16.47 (SERIES’B’) except that for high pressure heat 

exchanger. Non-standard flanges shall be designed as per ASME Sec. VIII Div.1. 

2.14.2 Unless otherwise specified, W.N. Flanges shall be used for all classes. 

2.14.3 Unless otherwise specified, all girth flanges and intermediate body flanges shall be 

of weld neck type only. 

2.14.4 Flanges rating shall be established based on design pressure, design temperature 

and considering all external loads (moments and axial force). 

2.15 Internals: 

Unless otherwise specified removable internals shall be bolted type and material of 

bolting shall be stainless steel TP 304. For shell & tube heat exchangers, floating 


2.16 Pipe Davit: 

head bolting shall be compatible to shell material and SA 193 Gr. B7M/2HM shall 

be used as a minimum. 

(i) 

Vertical Vessels having safety valve size 80 NB and above and or having 

internals, shall be provided with pipe davit. 

2.17 Vent/Drain/Ventilation Nozzle connections: 

i) Vessels shall be provided with one number vent/drain connection as per 

following unless otherwise specified in process data sheet: 

Vessel Length of Vent Drain Ventilation 

Volume (Horizontal Vessel) Nozzle Nozzle Nozzle 

(V),m 3 (L),mm 

V # 6.0 - 40 NB 40 NB - 

6.0 < V # 15 - 50 NB 40 NB - 

V > 15 - 50 NB 80 NB - 

- 300mm< L< 4500 mm - 100 NB 

- 4500nn< L< 7500mm - 150 NB 

- L> 7500 mm - 200 NB 

Vertical vessel not having any nozzle on the top shall be provided with 50NB 

nozzle for conducting hydro test in vertical condition. 

2.18 Spares: 

i) Vessels 

Gaskets 

Fasteners 

Sight/Light Glass 

: Two sets for each installed gasket 

: 10% (Minimum two in each size) of 

installed fasteners. 

: 4 sets for each installed glass. 

2.19 Important considerations 

- Vessels shall be designed considering maximum operating liquid in addition 

to design pressure. 


- All vessels shall be capable of withstanding water full condition during 

system testing. 

- In addition, all vertical vessels, and horizontal vessels shall be designed so 

as to permit site testing of the equipment with water at the test pressure on 

the top of the equipment considering 33% of design wind load. The design 

shall base on fully corroded condition. 

- All equipment foundation shall be designed and constructed for water full 

condition when equipment is new with 33% of design wind load. 

- Vessels shall be tested at shop hydrostatically at pressure calculated as per 

applicable code 

- Seismic design shall be carried out based on site spectra instead of IS: 

1893, if furnished. 

- All nozzle necks, all nozzle flanges and blind flanges shall be of weld 

deposit construction for clad equipment. Loose liners are not permitted. 

- All vertical equipment shall be provided with two lifting lugs. Lifting lugs 

shall be designed with impact factor or two. 

- Material of various parts of equipment shall be selected as per Table given 

in Annexure-I unless otherwise stated on process data sheet. 

3.0 DESIGN CRITERIA / REQUIREMENTS – SPECIFIC APPLICATIONS 

3.1 Storage Tanks 

3.1.1 All storage tanks shall be designed as per code considering liquid height up to top curbangle 

of shell. 

3.1.2 Tanks shell thickness calculation shall be carried out by the one (1) – foot method as per 

API 650 for tank diameters less than and equal to 60m (200 feet). For tanks greater than 

60 m variable design point method shall be used. 

3.1.3 Maximum height of unstiffened shell shall be calculated based on the corroded thickness 

of shell courses. Section modulus of wind girders shall also base on corroded thickness of 

shell courses. 

3.1.4 Seismic design as per API 650 (Appendix-E) is mandatory for storage tanks. 


3.1.5 Annular bottom plates shall be provided for all storage tanks 12 meter diameter and 

above. 

3.1.6 Anchor bolts shall be provided based on design considering wind/seismic loads, uplift due 

to internal pressure etc. However, tanks having diameter # 10 meters shall be provided 

with anchor bolts and shall be spaced at approximately 1.8M of circumference. 

3.2 Loading 

Because of critical relationship between the foundation and vessel design, construction of 

sand-bed/ foundation and settlement shall be strictly monitored during various stages of 

construction, vessel hydro test etc. Following loading shall be considered for design: 

a) Operating Conditions: 

Self-weight of vessel (but corroded thickness), mound load, foundation/sand bed 

reaction, liquid weight, earth quake loading, differential settlement, design 

pressure, longitudinal frictional load due to thermal and pressure expansion, 

explosion pressure on mound (if specified). 

b) Hydro Test condition: 

Self-weight of vessel, mound load (in case of health check-up), foundation/ sandbed 

reaction, water weight, differential settlement, test pressure, longitudinal 

frictional load due to thermal and pressure expansion. 

3.3 Cathodic Protection 

Impressed current cathodic protection system shall be designed and installed as per WP’S 

specification. 

3.3.1 External Coating 

Applied protection shall be fully tested for absence of holidays using high voltage spark 

tester. 

3.4 Location / Spacing of Vessels 

Minimum spacing of vessels and other safety regulation shall be as per OISD-STD-118. 

3.5 Load due to Uneven Settlement 

a) To make allowance in the design for effect of tolerances in alignment of shell 

section. Unevenness in sand-bed, etc. a maximum/minimum reaction may be 

assumed as given below. 

b) Based on soil investigation along with vessel axis, sub grade modules of soil / bed 

shall be calculated. Value of Pmax/Pmin may be reduced to 1.30 provided 

foundation is constructed and differential settlement is ensured by the contractor 

and demonstrated hydro test. 


c) Sand-bed should be properly prepared and compacted to obtain effective angle of 

support at least 120 0 and differential settlement should not be ore than 40 mm 

between mid-point of vessel and end-point of vessel. 

d) During initial hydro test condition sand bed contact angel may be taken as 60 0 

without mound over vessel if such condition arises during construction and hydro 

testing of vessel. 

4.0 PROJECT SPECIFIC REQUIREMENTS 

GASKETS 

- All RTJ gaskets should have proper marketing stamped with metallurgical 

certificate available. 

- Only octagonal section ring should be used in case of RTJ joint. 

- CAF gasket shall not be used. 

BOLTING 

- The length of the studs/bolts should be such that minimum two threads should be 

out of the nut on either side. 

- All studs/bolts should have metallurgical certificates in case of alloy/SS metallurgy 

with identified colour marketing at the stud ends/bolt side face. 

- Torque wrench /hydraulic bolt tensioners to be used for fasteners as specified in 

Piping design basis. 

- All fasteners 2” & above shall be procured with 2 nuts. 

MISCELLANEOUS REQUIREMENTS 

- Temperature recorders used in stress relieving should be calibrated and related 

certificate should be available for verification. 

- Calibrated pressure gauges shall be used for hydro testing. Minimum two pressure 

gauges to be used – one at the pressurizing point and other at highest / fart hest 

point. 

- Welding of alloy butt joints should be completed in continuation from start to finish. 

- Electrical resistance coils should be used for preheating/post heating of alloy steel 

welding. 

- Permanent slopping monkey ladder should be provided inside the skirt of the 

column and vertical vessels to approach the bottom head for inspection purposes. 

- Only SS shims shall be used for equipment alignment / leveling. 

- Shell internal surface of floating roof tanks should be made smooth by grinding 

after fabrication so that no protrusion and sharp edges are left over. This is 

required to avoid damage to the foam seal during the movement o the floating 

roofs. 

- All vessels columns should have utility and instrument connections from the side 

and not from the bottom except drain point. 

- Tanks shell insulation should have continuity in insulation cladding even at 

stiffener/retainer ring locations on shell. 

- Inspection windows in insulation for inspection / thickness survey are to be 

provided in insulated equipment. 


TABLE-I 

(ALLOWABLE STRESSES FOR COMBINED LOADING) 

VESSEL CONDITION/TEMP.TYPE 

OF STRESSES 

CONDITIONS 

ERECTION OPERATING TEST 

NEW OR CORRODED NEW CORRODED CORRODED 

TEMPERATURE AMBIENT DESIGN AMBIENT 

LONGITUDINAL KxSxK KxSxK 0.90 x Y,PxE 

LONGITUDINAL COMPRESSIVE 

STRESS 

KxB KxB B 

Where 

S= Basic allowable Tensile Stress as per Clause UG 23(a) of ASME Code Sec.,VIII 

Div.1 

B= ‘B’ value calculated as per Clause UG-23(b) 

E= Weld joint efficiency of circumferential weld, depending on extent of radiography. 

K= Factor for increasing basic allowable value when wind or seismic load is present. 

Note: Allowable stress in skit to shell joint shall be as per following: 

a) 0.45S, if joint is shear type. 

b) 0.70S, if joint is compression type. 


ANNEXURE-I 

MATERIAL SELECTION 

The following table gives general guidelines for material selection for various Pressure Parts / Non Pressure 

Parts of the equipment based on design temperature wherever material of construction is not specified by 

the Owner/WP. 

PRESSUR PARTS 

NON PRESSURE PARTS 

DESIGN 

TEM 0 c 

PLATE 

PIPE 

(SEE NOTE 

8) 

TUBES 

SPACERS 

(SE NOTE 

11) 

FORGING 

(SEE NOTE 

12) 

BOLTS/ 

STUDS/ 

NUTS 

EXTERNAL 

(SEE NOTE 

13) 

CRYOGENIC 

STRUCTURAL 

ATTACHMENT 

WELDED TO 

PRESSURE 

PARTS,BAFFELS, 

SUPPORTS,TIE 

RODS,SEALING, 

SLIDING STRIPS 

ETC. 

INTERNAL 

PIPES 

STUDS 

BOLTS 

NUTS 

INTERNAL 

TIE RODS 

FROM 

-254 

UPTO-196 

ABOVE 

-196 

UPTO -80 

SA 240 

GR.304L,304 

316,316L 

347(IMPACT 

TESTED 

SA 240 

S 

GR.304L,304, 

316,316L, 

321, 347 

SA 353/553 

GR.A 

SA 312 

TYPE-304 

304L,316 

316L.,347 

DA 312 

TYPE 304 

304L,316, 

316L.,321 

347 

SA333 GR.8 

SA 213 

TYPE 304 

304L,316 

316L,347 

SA 312 

TYPE 304 

304L.,316, 

316L.,321 

SA 334 

GR.8 

SA 182,GR.F 

304,304L,316 

347,316L. 

SA 182,GR.F 

304,F304L, 

F316L,316 

321,347 

SA 522 

SA 320 

GR.B8,8C,8T 

STRAIN 

HARDENED 

SA 194 GR.S. 

8C,8T 

LOW TEMPERATURE 

SAMPLE AS PRESSURE PARTS 

SS GRADE 

SAME AS 

TUBES 

ABOVE 

-80 

UPTO -60 

SA 203 GR.E 

IMPACT 

TESTED (SEE 

NOTE-1) 

SA 333 GE.3 SA 334 GR.3 SA 350 

GR. LF3 

SA 320 L7 

SA 194 GR.4 

PR GR.7 

SA 203 GR E SA 333 

GR.3 

SA 193GR.B8 

SA 194 GR.8 

CS KILLED 

ABOVE 

-60 

UPTO -45 

SA 537 CL.1 

IMPACT 

TESTED (SEE 

BOTE.1) 

SA 333 GR.3 SA 334 GR.3 SA 350 

GR. LF3 

SA 320 L7 

SA 194 GR.4 

PR GR.7 

SA 537 CL.1 SA 333 

GR.3 

SA 193GR.B8 

SA 194 GR.8 

CS KILLED 

ABOVE 

-45 

UPTO 

-29 

Sa,516(ALL 

GRADES) 

IMPACT 

TESTED 

NOTE.1) 

SA 333 GR.6 

OR GR.1 

SA 334 GR.6 

OR.GR.1 

SA 350 

GR. LF3 

SA 320 GRL.7 

SA 194 GR.4 

OR GR.7 

SA 516 (IN ALL 

GRADES) 

SA 333 GR.6 

SA 193 GR.B8 

SA 194 GR.8 

CS KILLED 

ABOVE 

-29 

UPTO 

0 

SA 516 (ALL 

GRADES) 

(SEE NOTE.3( 

SA 106 GR.b 

(SEE NOTE.3) 

SA 334 GR.6 

OR.1 

(SEE NOTE 

.1) 

SA 105/ 

SA 266 

(SEE 

NOTE.3) 

SA 193 (IN ALL 

GRADES) 

INTERMEDIATE TEMPERALTURE 

SA-516(IN ALL 

GRADES) 

SA 106 G.B 

SA-193 GR.B8 

SA-194 G.8 

CS KILLED 

ABOVE 0 

UPTO 343 

ABOVE 343 

UPTO 427 

ABOVE 427 

UPTO 38 

SA 516(ALL 

GRADES 

SA240 TYPE 

304L,316,321 

(SEE OTE.4) 

SA 204 GR.B 

SA 387 GR.11 

CL.1/CL.2 

SA 240 TYPE 

304L,316L,321 

(SEE NOTE 4) 

SA 387 GR.11 

CL.1/CL.2 

SA 387 GR.12 

CL.1/CL.2 

SA 106 GR.B 

SA 312 

TP.304L 

316L,321,SA- 

376 

TP321 

SA 335 GR.P1 

SA 335GR 

GR.P11 

SA 312 

TYPE 

304L,316L 

321 

SA 376 

TYPOE 321 

SA 335 P11 

SA 335 P12 

SA-179 

SA -213 

TP 304L 

316L,321 

SA 209 GR T1 

SA 213 

GR.T 

SA 213 

GR.T11 

SA213 TYPE 

304L,316L,321 

SA 213 T11 

SA 213 T12 

SA-105 

SA-266 

SA 182F 

304L,316L.,321 

SA 182 G.F1 

SA 182 

GR.F11 

SA 182 F 

304L,316L 

321 

SA 182 GR 

F11 

SA 182 

GR.F12 

SA-193 B7 

SA-194GR.2H 

SA-193 B7 

SA0194GR2H 

SA 193 GR.B7 

SA 194 GR.4 

SA 193 B7 

SA 194 GR.4 

SA 193 GR.B7 

SA 194, GR.4 

LEVATED TEMPERATURE 

Sa193 

Gr.b16 

Sa 194 gr.4 

IS-2062 

(PLATES) 

SAME AS 

PRESSURE PARTS 

SAME AS 


SAME AS 


SAME AS 


SAME AS 


SA 106 GR.B 

SA 106 GR.B 

SAME AS 

PRESSURE 

PARTS 

SAME AS 

PRESSURE 

PARTS 

SAME AS 

PRESSURE 

PARTS 

SAME AS 

PRESSURE 

PARTS 

SA-193 GRB8 

SA-194 GR.4 

SA-193GRB8 

SA-194 GR8 

SA-193 GR.B8 

SA-194 GR.8 

SA-193 GR.B8 

SA-194 GR.8 

SA-193 GR.B8 

SA-194 GR.8 

SA-193 GR.B8 

SA 194 G.8 

IS-2062 

(WELDABLE 

QUALITY) 

SAME AS 

GRADE AS 

PRESSURE 

PARTS 

C-1/2 Mo 

(COMML.QLTY) 

1¼Cl.1/2 mO 

(comml 

Qlty) 

Sa 479 

Gr.304l 

316,321 

1¼Cl.1/2 mO 

(comml 

Qlty) 

ABOVE 427 

UPTO 500 

above 538 

upto 593 

SA 240 TYPE 

304,321 

(SEE 

NOTE.4)sa 

312/sa 376 

type 

304,316,321 

sa 387 gr.22 

cl.1/cl.2 

sa 387,gr.21 

cl.1/cl.2 

sa 312/ 

sa 376 

type 

304,316,321 

Sa 213 tp 

304,316,321 

Sa 182f 304 

316,321 

Sa 335 p22 Sa 213 t22 SA 182 GR 

F22 

SA 336 GR 

F22 

Sa 193 

Gr.b16 

Sa 194 gr.4 

SA 193 GR.B5 

SA 194 GE3 

SAME AS 


SAME AS 


SAME AS 

PRESSURE 

PARTS 

SAME AS 

PRESSURE 

PARTS 

SA-193 GR.B8 

SA 194 G.8 Sa 479 

gr.304l,316l.,321 

SAME AS 

PRESSURE 

PARTS 

2¼c.1 Mo 

(COMML.QLTY.) 


ABOVE 500 

UPTO 815 

SA 240 

G.304H, 

316H,321H 

SA312/ 

SA376 

TYOE 304H, 

316H, 311H 

SA213 

TYPE 304H, 

316H, 321H 

SA 182 

GRADES 

304HM 

316H,321H 

SA 193 GRB8 

SA 194 GR.8 

(STRAIN 

HARDENED) 

SAME AS 


SAME AS 

PRESSURE 

PARTS 

SAME AS 

PRESSURE 

PARTS 

SA 479 

GR.304H, 

316H, 321H 

Notes: 

1. Selection of Carbon Steel and stainless steel material shall be based on process 

recommendation. 

2. This table is not applicable for atmospheric storage tanks. Materials shall be selected 

as per API 650 as applicable. 

3. Internal bolting shall be selected on the basis of shell side material as follows: 

SHELL MATERIAL STUD NUTS 

Carbon steel & upto 1% Cr. ASTM A 193 Gr B-7M ASTM A-194 Gr 2HM 

5% Chrome A 193 Gr B5 A 194 Gr 3 

13% Chrome A 193 Gr B6X A 194 Gr 6 

Stainless Steel A 193 Gr* A 194 Gr* 

For low temperatures, min, quality of bolting material shall be as specified for external 

bolting and shall be improved if shell side materials are better. 

*Compatible / same grade of SS. 


HINDUSTAN PETROLEUM CORPORATION LIMITED (HPCL) 





PART A 

SCOPE OF WORK FOR ROTATING EQUIPMENT & PACKAGES 

(AT RAMANMANDI TERMINAL) 

435-JH0902-00-ME-SOW-0001 

25-Aug-2009 





Phone: +91-22-67818000 

Fax : +91-22-67818080 



Page 1 of 7


HPCL GURU GOBIND SINGH REFINERY PRODUCTS EVACUATION PROJECT (GGSRPEP) 

SCOPE OF WORK FOR (ROTATING EQUIPMENT & PACKAGES) – PART A (RAMANMANDI TERMINAL ) 

. 

SYNOPSIS 

Disclaimer 











PARSONS 

APPROVAL 

DATE 

CLIENT 

APPROVAL 

DATE 

A 


Subramanyam 

.S 

Sameer 

Ishwad 

Jeremy 

Wallace 

08-July-09 

N/A 

B 


Subramanyam 

.S 

Sameer 

Ishwad 

Jeremy 

Wallace 

16-July-09 

N/A 

C 

Issued for Tender 

Subramanyam 

.S 

Sameer 

Ishwad 

KMN Pillai 

25-Aug-09 

Page 2 of 7



SCOPE OF WORK FOR (ROTATING EQUIPMENT & PACKAGES (AT RAMANMANDI TERMINAL) 

. 

1.0 Projects Details in Brief 

RamanMandi to Bahadurgarh Pipeline. 

As a part of Guru Gobind Singh Refinery (GGSR) Product Evacuation project, Hindustan 

Petroleum Co-corporation Ltd (HPCL) Proposes to lay a cross country multiproduct pipeline 

from the upcoming Guru Gobind Singh Refinery at Raman Mandi to HPCL’s existing terminal in 

Bahadurgarh. The length of the pipeline is approximately 243 Km. The pipeline is planned to 

transfer EURO-III MS,EURO-IV MS,EURO III HSD EURO IV HSD,SKO, Naphtha & ATF 

products from Raman Mandi to Bahadurgarh. The pipeline throughput shall be as follows: 

Pipeline Section Year / Phase Throughput in MMTPA 

Raman Mandi to 

Bahadurgarh 

2011-2012 / Phase-I 3.96 

2021-2022 / Phase – II 4.71 

The pipeline from Raman Mandi to Bahadurgarh is designed to cater the phase II 

throughputs.However to cater to phase-I throughput, the pumps have to run at lower speed 

through Variable Frequency Drives (VFD). 

Raman Mandi to Bhatinda: 

One Multi product Pipeline from GGSR Raman Mandi is proposed to be laid to HPCL’s 

existing depot in Bhatinda (approximately 29.6 Km) with a future provision to extend the 

pipeline from Bhatinda to Sangrur (approx.86 Km). Products to be transported via Raman 

Mandi to Bathinda pipeline are follows: 

(1) EURO-III grade of Motor Sprit (MS) 

(2) EURO-III grade of High Speed Diesel (HSD) 

(3) Superior Kerosene Oil (SKO) 

The project requirement for the Raman Mandi to Bathinda pipeline is to transport 0.929 Million 

Metric Tones Per Annum (MMTPA) of EURO – III MS, EURO – III HSD and SKO in the Year 

2011-12 (Phase-I) and 1.375 MMTPA of the products in the Year 2021-22 (Phase-II) Suitable 

tap off facility shall be provided at Bathinda for extension of the pipeline to Sangrur in future. 

The pipeline throughput shall be as follows: 

Page 3 of 7




. 

Pipeline Section Year / Phase Throughput in Million Metric Tons 

per Annum (MMTPA) 

Raman Mandi – Bathinda 

(incl. Sangrur) 

Bathinda - Sangur 

2011 – 2012 / Phase - I 0.929 

2021 – 2022 / Phase - II 1.375 

2011 – 2012 / Phase - I 0.470 

2021 – 2022 / Phase - II 0.697 

Pipeline from Raman Mandi to Bathinda and the Stations are designed for the projected throughput of 

1.375 MMTPA (Phase - II). However, the pump/driver will be designed such that presently it shall cater 

to the requirement of Phase-I throughput of Bathinda alone. Space provision shall be made for 

additional pumps to be installed at a later date to cater the requirement of Phase – II throughput for the 

volumes upto Sangrur. To cater for more than one flowrate and different densities / viscosities pumps 

have to run at lower speed through Variable Frequency Drives (VFD). 

2.0 Scope of Work: 

Contractor’s scope of work under the Composite works for terminals at RamanMandi shall be as 

described under: 

2.1 Procurement of Rotating Equipment & Packages (excluding FREE issue materials), refer Table 

-1 listed in this scope of work below) from the Approved Vendors attached with the Tender 

documents. The scope of supply shall be as per the relevant Specifications, datasheets, process 

documents and all other relevant documents attached elsewhere in the Tender. 

2.2 To follow the specifications like Engineering Design Basis, relevant specifications, Data Sheets 

(wherever attached) and Process package etc. attached with the Bid Document for the purpose 

of detail engineering execution for rotating equipments & Packages. 

2.3 Contractor’s scope shall include the following: 

2.3.1 Preparing enquiry specifications/ documents for each Rotating Equipment & Package item 

(Excluding Free issue materials) and materials to be purchased including spare parts for 

erection & commissioning, mandatory spare parts, special tools & tackles (as applicable) and 

spare parts for two-year normal operation. 

2.3.2 Specifications/Datasheets indicating technical requirements are attached in the Tender 

document for Rotating Equipments & Packages (Excluding Free issue materials) such as Sump 

Pumps, EOT Cranes, and Corrosion Inhibitor Package. Contractor shall use these data sheets 

for these equipments for enquiry / purchase and Owner/WP’s approvals. The contractor shall 

Page 4 of 7




. 

use the above specifications in conjunction with the process documents, which shall be referred 

for Operating Conditions, Material selection, Operational philosophy, instrumentation 

requirements and scope of supply etc. 

2.3.3 Detailed Purchase Requisition / Specifications for each Rotating Equipments & Packages 

(Excluding Free issue materials) and shall obtain the approval/review of Purchase Requisition 

by Owner / WP. 

2.3.4 Detailed review, checking and approval of equipment engineering and fabrication drawings 

and technical data from Vendors for equipment and materials (Excluding Free issue materials), to 

ensure adequacy and consistency with the design, safety and operability requirements. 

2.3.5 All inspection and tests are conducted for Rotating Equipments & Packages (Excluding Free 

issue materials) at Vendor’s shops/site as specified in Tender document, Engineering 

Design Basis, Data Sheets, Specifications, Codes and Standards etc. Contractor shall also 

submit the schedule of witnessed tests of all rotating equipment well in advance. 

2.3.6 Supply spare parts for Two-year normal operation for Rotating Equipments & Packages 

(Excluding Free issue materials), if ordered by the Owner, from equipment vendor. 

2.3.7 Supply commissioning spares for Rotating Equipments & Packages (Excluding Free issue 

materials) as required in the equipment Vendor’s scope. Contractor shall procure the same 

from the equipment vendors and make it available well before commissioning of 

Plant/Equipment. In case, any additional spares are consumed during commissioning then the 

same to be provided by the contractor at no additional cost to the Owner/WP. 

2.3.8 Supply all special tools and tackles required for Rotating Equipments & Packages 

(Excluding Free issue materials) Assembly/maintenance of the Rotating Equipment in 

the scope of supply. 

Page 5 of 7




. 

2.3.10 Contractor’s scope for Rotating Equipments & Packages (Excluding Free issue 

materials) shall include complete Design, Engineering, Procurement of bought out items, 

testing supply, transportation from vendor’s shop to site, Receipt of material at site, 

Handling at site and arrange for storage at site as per Tender Document. 

2.3.11 For Rotating Equipments & Packages (Excluding from Free issue materials) which are 

transported by sea shall have sea-worthy packing. The Contractor shall strictly follow the 

recommended preservation procedures during the period of storage for all equipment. 

2.4 Contractor shall carry out the Erection of all Rotating Equipments and Packages coming 

at RamanMandi (including Free issue materials) at the specified location on the properly 

designed & cast foundation as per Tender Document. 

2.5 Contractor shall carry out the inter-connections piping at all interface points such as 

Main Process and all utility connections. 

2.6 Contractor shall note that consumables, lubricants etc. required during erection, 

commissioning and performance guarantee run for Rotating Equipments & Packages (Excluding 

Free issue materials) such as first fill of lubricants etc shall be Contractor’s scope. A 

consolidated list for all rotating equipment / package shall be provided indicating type of 

lubricant, grease, oil etc. giving specifications, quantities, brand name and their Indian 

equivalent. Lubricants for the FREE issue material shall be provided by the purchaser. 

2.7 Contractor shall supply & install EOT Cranes for the following Pump houses: 

• Mainline Pumps sheds 

• Booster Pumps sheds 

The cranes shall be sized for handling the heaviest single piece of equipment for 

maintenance. The maintenance facilities (EOT Cranes) shall be as per Engineering Design 

Basis – Package Equipment and specifications & datasheets for EOT Crane attached. 

2.8 Pre-commissioning and commissioning of all Rotating Equipment & Packages at 

RamanMandi is in the scope of the contractor. Representative of Original Equipment 

Manufacturer (OEM) of critical rotating equipment such as Mainline & Booster Pumps will 

supervise the Pre-commissioning, testing & Commissioning activities. However, the contractor 

shall provide all assistance including manpower, tools and tackles in the Pre-commissioning, 

testing & Commissioning activities of these critical equipments also. 

Page 6 of 7




. 

Scope of Work for Free Issue Material & Scope of work for Rotating Equipment & Package, to 

be procured by Contractor: Table -1 

Sr 

no. 

FREE ISSUE Rotating 


Rotating Equipment & Packages to be supplied by the 

Contractor 

1. Scope of work shall include 

Receipt of material at site, 

Handling at site and arrange 

for storage at site for Rotating 

Equipments & Packages, 

Erection, Precommissioning, 

testing, and Commissioning 

along with interface piping 

with other systems / piping. 

2. - P-10-11 A/B/C- Booster 

Pumps at RamanMandi for 


-P-10-12 A/B/C Mainline 

Pumps at RamanMandi for 


- F-10-14 Filter Water 

Separator at RamanMandi 

- F-10-11 A/B Basket Filter at 

RamanMandi 

Scope of work shall include Design, Engineering, 

Procurement of materials & bought out items, packaging of 

the equipment / Package, inspection & testing at equipment / 

package vendor’s works, transportation to site, Receipt of 

material at site, Handling at site and arrange for storage at 

site, Erection, Precommissioning, testing & 

Commissioning along with interface piping with other 

systems/ piping. 

- P-10-03 / P-10-04 Sump Pumps at RamanMandi 

- EOT Crane at RamanMandi for Mainline Pump house 

- EOT Crane Booster Pump house 

- ZZ-10-0001, Corrosion Inhibitor Package at 

RamanMandi.for Bathinda Pipeline, 

- ZZ-10-0002, Corrosion Inhibitor Package at RamanMandi 

for Bahadurgarh Pipeline 

- Supply of 3 Ton chain pulley block. 

- P-10-02 A/B Mainline Pumps 

at RamanMandi for Bathinda 

Pipeline. 

- P-10-01 A/B Booster Pumps 

at RamanMandi for Bathinda 

Pipeline. 

- F-10-01 A/B, Basket Filter at 

RamanMandi 

Page 7 of 7






PART B 

SCOPE OF WORK FOR ROTATING EQUIPMENT & PACKAGES 

(AT BATHINDA TERMINAL) 

435-JH0902-00-ME-SOW-0001 

25-Aug-2009 





Phone: +91-22-67818000 

Fax : +91-22-67818080 



Page 1 of 7



SCOPE OF WORK FOR (ROTATING EQUIPMENT & PACKAGES) – PART B (BATHINDA TERMINAL) 

. 

SYNOPSIS 

Disclaimer 











PARSONS 

APPROVAL 

DATE 

CLIENT 

APPROVAL 

DATE 

A 


Subramanyam 

.S 

Sameer 

Ishwad 

Jeremy 

Wallace 

08-July-09 

N/A 

B 


Subramanyam 

.S 

Sameer 

Ishwad 

Jeremy 

Wallace 

16-July-09 

N/A 

C 


Subramanyam 

.S 

Sameer 

Ishwad 

KMN Pillai 

25-Aug-09 

Page 2 of 7



SCOPE OF WORK FOR (ROTATING EQUIPMENT & PACKAGES (BATHINDA TERMINAL) 

. 


RamanMandi to Bahadurgarh Pipeline. 



from the upcoming Guru Gobind Singh Refinery at Raman Mandi to HPCL’s existing terminal in 

Bahadurgarh. The length of the pipeline is approximately 243 Km. The pipeline is planned to 

transfer EURO-III MS,EURO-IV MS,EURO III HSD EURO IV HSD,SKO, Naphtha & ATF 




Bahadurgarh 

2011-2012 / Phase-I 3.96 

2021-2022 / Phase – II 4.71 



through Variable Frequency Drives (VFD). 


One Multi product Pipeline from GGSR Raman Mandi is proposed to be laid to HPCL’s 







The project requirement for the Raman Mandi to Bathinda pipeline is to transport 0.929 Million 

Metric Tones Per Annum (MMTPA) of EURO – III MS, EURO – III HSD and SKO in the Year 

2011-12 (Phase-I) and 1.375 MMTPA of the products in the Year 2021-22 (Phase-II) Suitable 

tap off facility shall be provided at Bathinda for extension of the pipeline to Sangrur in future. 

The pipeline throughput shall be as follows: 

Page 3 of 7




. 

Pipeline Section Year / Phase Throughput in Million Metric Tons 

per Annum (MMTPA) 




2011 – 2012 / Phase - I 0.929 

2021 – 2022 / Phase - II 1.375 

2011 – 2012 / Phase - I 0.470 

2021 – 2022 / Phase - II 0.697 


1.375 MMTPA (Phase - II). However, the pump/driver will be designed such that presently it shall cater 

to the requirement of Phase-I throughput of Bathinda alone. Space provision shall be made for 

additional pumps to be installed at a later date to cater the requirement of Phase – II throughput for the 

volumes upto Sangrur. To cater for more than one flowrate and different densities / viscosities pumps 

have to run at lower speed through Variable Frequency Drives (VFD). 

2.0 Scope of Work: 

Contractor’s scope of work under the Composite works for terminals at Bathinda shall be as 

described under: 

2.1 Procurement of Rotating Equipment & Packages (excluding FREE issue materials), refer Table 

-1 listed in this scope of work below) from the Approved Vendors attached with the Tender 

documents. The scope of supply shall be as per the relevant Specifications, datasheets, process 

documents and all other relevant documents attached elsewhere in the Tender. 

2.2 To follow the specifications like Engineering Design Basis, relevant specifications, Data Sheets 

(wherever attached) and Process package etc. attached with the Bid Document for the purpose 

of detail engineering execution for rotating equipments & Packages. 

2.3 Contractor’s scope shall include the following: 

2.3.1 Preparing enquiry specifications/ documents for each Rotating Equipment & Package item 

(Excluding Free issue materials) and materials to be purchased including spare parts for 

erection & commissioning, mandatory spare parts, special tools & tackles (as applicable) and 

spare parts for two-year normal operation. 

2.3.2 Specifications/Datasheets indicating technical requirements are attached in the Tender 

document for Rotating Equipments & Packages (Excluding Free issue materials) such as Sump 

Pumps, Slop/Interface transfer pumps. Contractor shall use these data sheets for these 

equipments for enquiry / purchase and Owner/WP’s approvals. The contractor shall use the 

Page 4 of 7




. 

above specifications in conjunction with the process documents, which shall be referred for 

Operating Conditions, Material selection, Operational philosophy, instrumentation requirements 

and scope of supply etc. 

2.3.3 Detailed Purchase Requisition / Specifications for each Rotating Equipments & Packages 

(Excluding Free issue materials) and shall obtain the approval/review of Purchase Requisition 

by Owner / WP. 

2.3.4 Detailed review, checking and approval of equipment engineering and fabrication drawings 

and technical data from Vendors for equipment and materials (Excluding Free issue materials), to 

ensure adequacy and consistency with the design, safety and operability requirements. 

2.3.5 All inspection and tests are conducted for Rotating Equipments & Packages (Excluding Free 

issue materials) at Vendor’s shops/site as specified in Tender document, Engineering 

Design Basis, Data Sheets, Specifications, Codes and Standards etc. Contractor shall also 

submit the schedule of witnessed tests of all rotating equipment well in advance. 

2.3.6 Supply spare parts for Two-year normal operation for Rotating Equipments & Packages 

(Excluding Free issue materials), if ordered by the Owner, from equipment vendor. 

2.3.7 Supply commissioning spares for Rotating Equipments & Packages (Excluding Free issue 

materials) as required in the equipment Vendor’s scope. Contractor shall procure the same 

from the equipment vendors and make it available well before commissioning of 

Plant/Equipment. In case, any additional spares are consumed during commissioning then the 

same to be provided by the contractor at no additional cost to the Owner/WP. 

2.3.8 Supply all special tools and tackles required for Rotating Equipments & Packages 

(Excluding Free issue materials) Assembly/maintenance of the Rotating Equipment in 

the scope of supply. 

Page 5 of 7




. 

2.3.9 Contractor’s scope for Rotating Equipments & Packages (Excluding Free issue 

materials) shall include complete Design, Engineering, Procurement of bought out items, 

testing supply, transportation from vendor’s shop to site, Receipt of material at site, 

Handling at site and arrange for storage at site as per Tender Document. 

2.4 Contractor shall carry out the Erection of all Rotating Equipments and Packages coming 

at Bathinda (including Free issue materials) at the specified location on the properly 

designed & cast foundation as per Tender Document. 

2.5 Contractor shall carry out the inter-connections piping at all interface points such as 

Main Process and all utility connections. 

2.6 Contractor shall note that consumables, lubricants etc. required during erection, 

commissioning and performance guarantee run for Rotating Equipments & Packages (Excluding 

Free issue materials) such as first fill of lubricants etc shall be Contractor’s scope. A 

consolidated list for all rotating equipment / package shall be provided indicating type of 

lubricant, grease, oil etc. giving specifications, quantities, brand name and their Indian 

equivalent. Lubricants for the FREE issue material shall be provided by the purchaser. 

2.7 Pre-commissioning and commissioning of all Rotating Equipment & Packages at Bathinda isin 

the scope of the contractor. 

Page 6 of 7




. 

Scope of Work for Free Issue Material & Scope of work for Rotating Equipment & Package, to 

be procured by Contractor: Table -1 

Sr 

no. 

FREE ISSUE Rotating 


Rotating Equipment & Packages to be supplied by the 

Contractor 

1. Scope of work shall include 

Receipt of material at site, 

Handling at site and arrange 

for storage at site for Rotating 

Equipments & Packages, 

Erection, Precommissioning, 

testing, and Commissioning 

along with interface piping 

with other systems / piping. 

Scope of work shall include Design, Engineering, 

Procurement of materials & bought out items, packaging of 

the equipment / Package, inspection & testing at equipment / 

package vendor’s works, transportation to site, Receipt of 

material at site, Handling at site and arrange for storage at 

site, Erection, Precommissioning, testing & 

Commissioning along with interface piping with other 

systems/ piping. 

2. - (ZZ-20-001) Oil Water 

Separator Package at 

Bathinda 

- F-20-01 A/B Basket Filter at 

Bathinda 

- P-20-01 / P-20-02, Sump Pumps at Bathinda. 

- P-20-03 & P-20-04: Slop and interface transfer pumps at 

Bathinda 

- 3 Ton chain pulley block. 

Page 7 of 7



TECHNICAL COMPLIANCE FOR ROTATING & PACKAGES 





TECHNICAL COMPLIANCE FOR ROTATING EQUIPMENT & PACKAGES 

435-JH0902-00-ME-TEN-0001 

16-July-2009 





Phone: +91-22-67818000 

Fax : +91-22-67818080 


© Copyright 2009 WorleyParsons




SYNOPSIS 

Disclaimer 











PARSONS 

APPROVAL 

DATE 

CLIENT 

APPROVAL 

DATE 

A 


Subramanyam 

.S 

Sameer 

Ishwad 

Jeremy 

Wallace 

08-July-09 

N/A 

B 


Subramanyam 

.S 

Sameer 

Ishwad 

KMN Pillai 

16-July-09 

N/A




Sr. 

No 

COMPLIANCE STATEMENT / QUERY 

BIDDER’S CONFIRMATION / ANSWER 

1 BIDDER IS INFORMED THAT THE DETAILED OFFER 

FOR ANY ROTATING EQUIPMENT / PACKAGE 

EQUIPMENT (EXCLUDED FROM FREE MATERIAL) , 

i.e. FILLED-IN EQUIPMENT DATA SHEETS, 

PERFORMANCE CURVES, VENDOR'S SELECTED 

EQUIPMENT MODELS ETC. IS NOT REQUIRED AT 

THE STAGE OF BIDDING AND SHALL NOT BE 

REVIEWED OR TAKEN COGNIZANCE OF AT THIS 

STAGE. ACORDINGLY, THE BIDDER SHALL 

FURNISH ONLY THE FOLLOWING DOCUMENTS 

ALONGWITH THE BID: 

a) This Technical Compliance with categorical 

Confirmation against each of the clauses 

b) Deviations, if any against the equipment data sheets, 

Specification shall be duly consolidated at one place 

(under exceptions/ deviation list). In case no deviations 

are furnished, it shall be construed that bidder’s 

Proposal is in total compliance to bid document 

requirements. 

Bidder shall note that vendor specific deviations to design 

codes (ISO/IS/BS/API etc.) shall not be considered at this 

stage and shall be subject to review and approval of 

Owner/WP during detail engineering. However bidder shall 

note that deviations to only those requirements of design 

codes, which are technically infeasible to meet, shall be 

permitted provided suitable justification for the same is 

furnished. Deviations, which can be withdrawn with extra 

cost and or time implication, shall not be permitted. 

Page 3 of 5




2 Any deviations/deletions/corrections made elsewhere in 

the body of the bid (on equipment data sheet, specs etc.) 

will not be taken cognizance of and all such deviations 

shall be deemed to have been withdrawn by the bidder. 

Confirm compliance. 

3 Confirm that the equipment supplied shall be from 

one of the approved vendors given in the 

APPROVED VENDOR LIST attached elsewhere in 

4. Confirm that all equipment shall be ordered on the Vendors 

only after: 

a) Approval/Review of the Purchase Requisition by 

HPCL/WP as specified. 

b) Ensuring equipment meeting the acceptance criteria 

specified in the bid document by furnishing duly filled in 

EXPERIENCE RECORD FORMAT attached with the 

bid document which shall be subject to HPCL/WP’s 

approval/review. 

5. Duly filled in equipment data sheets, characteristic 

curves for the selected vendor/equipment model shall be 

subject to HPCL/WP’s approval/review to ensure 

compliance to bid specification during detailed 

engineering stage. Confirm compliance 

6. Confirm that the Scope of supply and work 

considered in the Bid proposal is in total compliance to the 

Bid specification requirement including Scope of 

Work/Supply, Data Sheet, Job specs. and attatched 

specification with respect to all Rotating equipment. 

7. Confirm that wherever the Material Of Construction 

of equipment components have been specified in the Bid 

specification, same or superior MOC shall be offered 

Page 4 of 5




8. Confirm that all Inspection & Tests as required for 

each equipment, as per the Data sheets, Job specs and 

as per specification and Codes attached and referred to 

have been included by the bidder in his proposal 

9. Bidder shall obtain and submit a list of Operation and 

Maintenance spares required for Two Year Normal 

Operation (indicating the price against each spare) as 

recommended by the equipment manufacturer / bidder. 

This price shall remain valid till six months after the 

completion of complete tender work. 

10. Confirm that Erection & Commissioning Spares as 

required for each equipment have been included by 

the bidder in his proposal. Further in case any spare 

is consumed over and above the quoted 

commissioning spares during startup/commissioning, the 

same shall be supplied free of cost. 

11. Confirm that Special Tools & Tackles, as required 

for each Equipment, have been included by the Bidder in 

his proposal. 

12. Confirm that all consumables, chemicals, lubricants etc. for 

initial charge and for commissioning and site performance 

guarantee run have been included in the Bidder’s proposal. 

13. Confirm that all Drawings / Data requirements as per 

specifications and codes attached and referred to has been 

included in the bidder’s proposal. 

Page 5 of 5






SPECIFICATION FOR SUMP PUMPS 

435-JH0902-10-ME-SPC-0009 

31-July-2009 





Phone: +91-22-67818000 

Fax : +91-22-67818080 






SYNOPSIS 

Disclaimer 











PARSONS 

APPROVAL 

DATE 

CLIENT 

APPROVAL 

DATE 

A 


Subramanyam 

.S 

Sameer 

Ishwad 

Jeremy 

Wallace 

08-July-09 

N/A 

B 


Subramanyam 

.S 

Sameer 

Ishwad 

Jeremy 

Wallace 

10-July-09 

N/A 

C 


Subramanyam 

.S 

Sameer 

Ishwad 

KMN Pillai 

25-July-09




CONTENTS 

1. INTRODUCTION ................................................................................................................6 

1.1 Scope of Work ...................................................................................................................6 

1.2 Sump Pumps at Raman Mandi & Bhatinda Pump Station ................................................7 

1.3 Work Included .........................................................................................................................8 

1.3 Design Basis ......................................................................................................................9 

1.3.1 Design Life, Availability and Reliability.................................................................................9 

1.3.2 Noise Limitation .........................................................................................................9 

1.4 Material Certification ..........................................................................................................9 

1.5 Reference Documents .....................................................................................................10 

1.5.1 British Standards (BS) .........................................................................................10 

1.5.2 American Standard Institute (ANSI).....................................................................10 

1.5.3 American Society and Mechanical Engineers (ASME)........................................11 

1.5.4 American Society for Testing and Materials (ASTM)...........................................11 

1.5.5 American Petroleum Institute (API)......................................................................11 

1.5.6 The Institute of Petroleum (IP) .............................................................................12 

1.5.7 ISO Standards (ISO)............................................................................................13 

1.5.8 Manufacturers Standardisation Society (MSS)....................................................13 

1.5.9 International Electrotechnical Commission (IEC) ................................................13 

1.5.10 National Fire Protection Association (NFPA).......................................................14 

1.5.11 Tubular Exchanger Manufacturers Association (TEMA)......................................14 

1.5.12 Occupational Safety and Health Administration (OSHA).....................................14 

1.5.13 Oil Industries Safety Directorate (OISD)..............................................................14 

1.5.14 Petroleum and Explosives Safety Organisation (PESO) .....................................15 

1.5.15 Referenced Standard Specifications....................................................................15 

1.6 Conflicts, Deviations, and Amendments ..........................................................................15 

1.7 Vendor Exceptions...........................................................................................................15




2. TECHNICAL REQUIREMENTS .......................................................................................16 

2.1 General ............................................................................................................................16 

2.2 Process and Operating Criteria........................................................................................17 

2.3 Amendments, Supplements and Choices to API 610......................................................17 

2.4 Auxiliary Equipment and Connections .............................................................................23 

2.5 Bearings and Bearing Housings ......................................................................................24 

2.6 Lubrication........................................................................................................................24 

2.7 Electric Motors .................................................................................................................24 

2.8 Machinery Protection System ..........................................................................................24 

2.9 General..................................................................................................................................25 

2.10 Pump Skid Instrument Installation ...................................................................................25 

2.11 Civil.....................................................................................................................................25 

3. PROTECTIVE COATING .................................................................................................26 

4. SPARE PARTS AND SPECIAL TOOLS ..........................................................................27 

4.1 Spare Parts ......................................................................................................................27 

4.1.1 Spare Parts Required ..........................................................................................27 

4.1.2 Information Required ...........................................................................................27 

4.1.3 Contents...............................................................................................................27 

4.2 Special Tools....................................................................................................................28 

5. MARKING .........................................................................................................................29 

6. TESTING ..........................................................................................................................30 

6.1 General ............................................................................................................................30 

6.2 Welds ...............................................................................................................................30 

6.3 Castings ...........................................................................................................................30 

6.4 Hydrostatic Tests .............................................................................................................31 

6.5 Performance Test ............................................................................................................31 

6.6 NPSHR Test.....................................................................................................................31 

6.7 Unit Test...........................................................................................................................32




6.8 Mechanical Run Test .......................................................................................................32 

7. MATERIAL SOURCING TRACEABILITY AND CERTIFICATION ...................................33 

8. PACKING, SHIPPING AND HANDLING ..........................................................................34 

9. INSPECTION, QUALITY ASSURANCE AND QUALITY CONTROL REQUIREMENTS.35 

10. SITE ERECTION, TESTING AND COMMISSIONING ASISTANCE ...............................37 

11. PERFORMANCE GUARANTEE ......................................................................................38 

13. VENDOR SUPPLIED DOCUMENTS.........................................................................................39 

APPENDIX-A: SPECIFICATIONS & DATASHEETS.......................................................................40 

APPENDIX-B: VENDOR DATA REQUIREMENT LIST ...................................................................41




1. INTRODUCTION 

1.1 Scope of Work 

The scope of work under this document shall include supply of Sump pumps for Sump tanks 

This specification details the general requirements for the pump sets (API 610 10 th edition Centrifugal 

Pump) and is to be used in conjunction with the data sheets, and specifications enclosed. 

The Contractor / Vendor shall be responsible for the design, manufacturing, fabrication, assembly, 

painting, inspection and testing, certification (as applicable), preparation for shipment, supply of 

documentation for the complete package, and site erection, testing and commissioning as described 

in this specification and attachments. 

This specification does not dictate the detailed equipment design requirements. It is intended that this 

responsibility be retained fully by the Contractor / Vendor so that Contractor’s / Vendor’s warranty 

remains fully in force and is not affected by statements herein. 

The API 610 Centrifugal Pump Sets shall be complete including all ancillary equipment/items required 

to meet the design and environmental conditions as stated herein. Any additional part, equipment, 

material, etc., which are not specifically mentioned in this specification, but are required to make the 

supplied equipment/item complete in all respect in accordance with the intent of this specification, 

statutory requirements, applicable codes/standards, good engineering practices, and for safe and 

trouble-free operation, shall be deemed to be covered under the scope of this specification. 

If national and/or local regulations exist in which some of the requirements may be more stringent 

than in this specification, the Contractor / vendor shall determine by careful scrutiny which of the 

requirements are the more stringent and which combination of requirements will be acceptable as 

regards to safety, environmental, economic and legal aspects, in all cases the contractor / Vendor 

shall inform the Purchaser of any deviation from the requirements of this specification which is 

considered to be necessary in order to comply with national and/or local regulations. The Purchaser 

may then decide to negotiate with the Authorities concerned with the object of obtaining agreement to 

follow this specification as closely as possible. 

This specification also includes in the scope of Contractor / Vendor, tagging and preparation for 

shipment of all equipment furnished. 

6




1.2 Sump Pumps at Raman Mandi & Bhatinda Pump Station 

Item Equipment No. Equipment Title Data Sheet No. 

1 P-10-03 Sump Pump (at Ramanmandi) 0435-JH0902-10-ME-DAS-0012 

2 P-10-04 Sump Pump (at Ramanmandi) 0435-JH0902-10-ME-DAS-0012 

3 P-20-01 Sump Pump (at Bhatinda) 0435-JH0902-10-ME-DAS-0016 

4 P-20-02 Sump Pump (at Bhatinda) 0435-JH0902-10-ME-DAS-0016 

7




1.3 Work Included 

The Contractor / Vendor shall furnish all components and ancillary equipment necessary to make the 

equipment complete, safe, maintainable and ready for trouble free operation. The equipment scope 

shall include but not be limited to: 

• Pump assemblies; 

• Drive couplings; 

• Mechanical seal assemblies and flushing / cooling plans as may be necessary; 

• Mounting arrangement for pump assemblies and drives; 

• Guarding around exposed rotating surfaces, of non-sparking material; 

• Strainer 

• Package and equipment lifting lugs; 

• Earthing lugs; 

• Pump bearing lubrication systems (as applicable) 

• Machinery protection system (instruments/controls) as may be necessary safe & trouble free 

operation, along with necessary cabling. (as applicable) 

• Local controls stations (with remote/manual switch). 

• Interface with supervisory control systems; 

• Inspection and performance testing; 

• Disassembly and reassembly of unit test pumps after completion of test work; 

• Surface preparation, painting, protective coating and preservation; 

• Foundation / holding down bolts with nuts; 

• Special tools for installation / operation / maintenance; 

• Mandatory Spares as listed in the attachments elsewhere in the bid package 

• Spare parts for start up and commissioning (with list); 

• Spares for 2 years operation and maintenance (if required – optional), however list with price 

shall be provided; 

• Packing & shipping of equipment to site; 

• Unloading & storage at site; 

• Erection & commissioning assistance for the package 

• Supply of power cabling between switchgears, and between packages and driven motors 

• Power supplies as may be required for the package; 

• Cabling between panel and pump skid. 

• Pressure gauges and pressure transmitters on the pump suction and discharge. 

8




• Equipment performance guarantee; 

• Operating and maintenance manuals; and 

• Information and data as indicated in Vendor Data Requirement List. 

1.3 Design Basis 

1.3.1 Design Life, Availability and Reliability 

The overall availability and reliability of the complete package shall be demonstrated by the 

Contractor / Vendor. Unless otherwise stated, the package design life shall be 20 years, with an 

uninterrupted period of operation of 3 years. 

The Contractor / Vendor shall identify any aspects of its standard components or packages that do 

not meet this requirement and submit descriptions to the Purchaser for consideration during the 

tendering process. 

1.3.2 Noise Limitation 

Noise levels of all equipment under normal operation shall not exceed an eight-hour equivalent 

continuous A-weighted sound pressure level, LAeq,8h, of 85 dB(A) at 1 metre in all directions. Sound 

level tests shall be performed to verify the same. In case noise test certificate shows a sound level 

exceeding 85 dB (A), necessary rectification/modification shall be done at Contractor / Vendor ’s own 

cost and the pump set shall be re-tested to bring down the sound level to the specified limit. 

Predicted noise levels shall be subject to approval by Purchaser. 

The specified noise level should be attained without the use of orifices, mufflers, diffusers and/or 

credit for thermal or acoustic insulation where practical. 

Noise attenuating enclosure is generally not preferred and shall be avoided. However, if used (subject 

to approval of Purchaser) shall be designed to provide full access to the equipment for maintenance 

and operation. 

1.4 Material Certification 

Pressure containing parts and shafting shall have material certification in compliance with BS EN 

10204 type 3.1 and include original mill certificates or certified copies. Components shall be fully 

traceable back to the certificate. 

Other parts shall be provided with certification to BS EN 10204 type 2.2. 

9




1.5 Reference Documents 

The design, fabrication and supply of pump sets shall comply with the applicable sections of the latest 

edition of the following codes and standards including their addenda 

1.5.1 British Standards (BS) 

Standard No. 

BS 1041 

BS 2765 

BS 3463 

BS 3693 

BS 5308-1 

BS EN 10204 

BS EN 13190 

BS EN 60073 

BS EN 60079 – 0 to 11 

BS EN 60584 

BS EN 60751 

BS EN 837-1 

PD 5304 

Standard Title 

Code for temperature measurement. 

Specification for dimensions of temperature detecting elements and 

corresponding pockets 

Specification for observation and gauge glasses for pressure vessels 

Recommendations for design of scales and indexes on analogue 

indicating instruments 

Instrumentation cables. Specification for polyethylene insulated cables 

Metallic materials. Types of inspection documents 

Dial thermometers 

Basic and safety principles for man-machine interface, marking and 

identification. Coding principles for indicators and actuators 

Electrical apparatus for potentially explosive atmospheres. General 

requirements 

Thermocouples. Reference tables 

Industrial platinum resistance thermometer sensors 

Pressure gauges. Bourdon tube pressure gauges. Dimensions, 

metrology, requirements and testing 

Guidance on safe use of machinery 

1.5.2 American Standard Institute (ANSI) 

Standard No. 

ANSI B40.1 


Gauges - Pressure Indicating Dial Type - Elastic Element 

10




ANSI MC 96.1 

Temperature Measurement Thermocouples 

1.5.3 American Society and Mechanical Engineers (ASME) 

Standard No. 

ASME B16.11 

ASME B16.34 

ASME B16.5 

ASME B18.2.2 

ASME B31.3 

ASME B46.1 

ASME BPVC Section II 

ASME BPVC Section V 


Forged Fittings, Socket-Welding and Threaded 

Valves—Flanged, Threaded, and Welding End 

Pipe Flanges and Flanged Fittings 

Square and Hex Nuts 

Process Piping 

Surface Texture (Surface Roughness, Waviness and Lay) 

Materials 

Non-destructive Examination 

ASME BPVC Section VIII Rules for Construction of Pressure Vessels - Division 1 

ASME BPVC Section IX 

ASME PTC 19.3 

Welding and Brazing Qualifications 

Temperature Measurement 

1.5.4 American Society for Testing and Materials (ASTM) 

Standard No. 

ASTM A194 

ASTM A36 


Standard Specification for Carbon and Alloy Steel Nuts for Bolts for 

High Pressure or High Temperature Service, or Both 

Standard Specification for Carbon Structural Steel 

1.5.5 American Petroleum Institute (API) 

Standard No. 

API 520 


Sizing Selection and Installation of Pressure Relieving Devices in 

11




Standard No. 

API 526 

API 541 


Refineries 

Flanged Steel Pressure Relief valves 

Form-wound Squirrel-Cage Induction Motors - 500 Horsepower and 

Larger 

API 547 General-purpose Form-wound Squirrel Cage Induction Motors - 250 

Horsepower and Larger 

API 550 

API 610 

API 614 

API 670 

API 671 

API 677 

API 682 

API RP 505 

API RP 551 

API RP 686 

Installation of Refinery Instruments and Control Systems 

Centrifugal Pumps for Petroleum, Petrochemical and Natural Gas 

Industries 

Lubrication, Shaft-sealing and Oil-control Systems and Auxiliaries 

Machinery Protection Systems 

Special Purpose Couplings for Petroleum, Chemical and Gas Industry 

Services 

General-Purpose Gear Units for Petroleum, Chemical and Gas 

Industry Services 

Pumps—Shaft Sealing Systems for Centrifugal and Rotary Pumps 

Recommended Practice for Classification of Locations for Electrical 

Installations at Petroleum Facilities as Class I, Zone 0, Zone 1 and 

Zone 2 

Process Measurement Instrumentation 

Recommended Practices for Machinery Installation and Installation 

Design 

1.5.6 The Institute of Petroleum (IP) 

Standard No. 

IP 205/71 


Petroleum Measurement Manual Part V, Automatic Tank Gauging 

12




1.5.7 ISO Standards (ISO) 

Standard No. 

ISO 1940 

ISO 8310 


Mechanical vibration -- Balance quality requirements for rotors in a 

constant (rigid) state 

Refrigerated Light Hydrocarbon Fluids – Measurement of Temperature 

in Tanks Containing Liquefied Gases – Resistance Thermometers and 

Thermocouples. 

1.5.8 Manufacturers Standardisation Society (MSS) 

Standard No. 

MSS SP-55 


Quality Standard for Steel Castings for Valves, Flanges and Fittings 

and Other Piping Components - Visual Method for Evaluation of 

Surface Irregularities 

1.5.9 International Electrotechnical Commission (IEC) 

Standard No. 

IEC 73 

IEC 529 

IEC 60584-1 


Specification for The Colour of Indicator Lights, Push Buttons, 

Annunciators and Digital Readouts 

Degrees of Protection Provided by Enclosures (IP Code) 

Thermocouples – Part 1 : Reference 

IEC 60584-3 Thermocouples – Part 3: Extension and Compensating Cables – 

Tolerances and Identification system 

IEC 60751 

IEC 60034 

IEC 60060 

IEC 60072 

IEC 60079 

Industrial Platinum Resistance Thermometers and Thermometers and 

Platinum Temperature Sensors 

Rotating Electrical Machines 

High Voltage Test Techniques 

Dimensions and Output Series for Rotating Electrical Machines 

Electrical Apparatus for Explosive Gas Atmospheres 

13




IEC 60085 

IEC 61972 

IEC 61986 

Thermal Evaluation and Designation of Electrical Insulation 

Method for Determining Losses and Efficiency of Three-phase Cage 

Induction Motors 

Rotating Electrical Machines – Equivalent Loading and Super-position 

Techniques – Indirect Testing to Determine Temperature Rise 

1.5.10 National Fire Protection Association (NFPA) 

Standard No. 

NFPA 77 


Recommended Practice on Static Electricity 

1.5.11 Tubular Exchanger Manufacturers Association (TEMA) 

1.5.12 Occupational Safety and Health Administration (OSHA) 

1.5.13 Oil Industries Safety Directorate (OISD) 

Standard No. 

OISD-RP-110 

OISD-STD-119 

OISD-STD-123 

OISD-STD-122 

OISD-STD-125 

OISD-RP-126 

OISD-STD-171 


Recommended Practices on Static Electricity 

Selection, Operation and Maintenance of Pumps 

Selection, Operation and Maintenance of Rotary Equipment 

Components 

Selection, Operation and Maintenance of Fans, Blowers, Gear Boxes, 

Agitators & Mixers 

Inspection and Maintenance of Mechanical Seals 

Specific practices for installations and maintenance of rotating 

equipment 

Preservation of Idle Static & Rotary Mechanical Equipments 

14




1.5.14 Petroleum and Explosives Safety Organisation (PESO) 

1.5.15 Referenced Standard Specifications 

Document No. 

0435-JH0902-00-PI-SPC-003 

435-JH0902-00-EL-SPC-0002 

435-JH0902-00-EL-DAS-0085 

Document Title 

Specification for Painting / Coating Requirements 

Specification for Low Voltage Induction Motors 

Datasheet for Low Voltage induction Motors. 

1.6 Conflicts, Deviations, and Amendments 

Contractor’s / Vendor’s bid shall clearly state and list exceptions to this specification and all 

referenced documents. In the event of any conflict arising between this specification and other 

documents listed herein, refer comments to Purchaser for clarification before design or fabrication 

commences. 

The order of precedence that applies is generally as follows: 

• Data Sheets 

• This Specification 

• Referenced Drawings 

• Project Specifications 

• General Specifications 

• Referenced Codes and Standards 

1.7 Vendor Exceptions 

Contractor’s / Vendor’s Bid shall clearly state and list exceptions/deviations under a separate section 

“exceptions/deviations” and all referenced codes and standards and all documents referred in this 

specification. Exceptions mentioned elsewhere in the Bid or implied in the Bid shall be invalid. 

15




2. TECHNICAL REQUIREMENTS 

The pumps including mounting plate, driver and all other ancillary equipment shall be in accordance 

with the latest edition (10 th edition) of the API 610 edition / ISO 13079 “Centrifugal Pumps for 

Petroleum, Heavy Duty Chemical and Gas Industry Service” plus as amended by the comments on 

the subsequent Sections this specification including referenced standards, specifications, datasheets 

and drawings enclosed. 

The Contractor / Vendor shall comply with applicable Indian Federal, State or Local codes, 

regulations, ordinances, and rules. 

2.1 General 

The pumps shall be of manufacturer’s standard proven design and be suitable for service as 

mentioned in the datasheet attached elsewhere in the bid package. 

The pumps and their component parts shall be manufactured to controlled tolerances to assure 

complete inter-changeability with similar pumps in the station. 

The Contractor / Vendor shall offer pumps from an existing manufacturing range which shall be a unit 

of the same size and design which has a successful record of proven field service at operating 

conditions similar in terms of power rating, hydraulic performance including NPSHR, inlet flow, 

differential head, operating pressure and temperature, pumping liquid, speed, number and type of 

impellers, mechanical design and materials of construction. At least one pumps similar to those 

proposed shall have demonstrated successful continuous operation in the field for at least three years 

individually without any major overhaul. 

The site environmental conditions for the Sump pump are detailed in the enclosures. 

Each pump shall be mounted on a base plate complete with the following ancillary equipment: 

• Drive motor; 

• API mechanical seal 

• Junction boxes for machinery protection; 

The lube oil system for each pump unit shall be individual ring oil lubricated and with constant level 

oiler. 

Materials of construction shall be suitable for the chemical and physical properties of the hydrocarbon 

fluids to be pumped. The physical properties of the fluids are detailed in the data sheets. 

The pump drive train including shaft shall be adequately sized and shall be designed for a minimum 

design factor of 1.5 at maximum load. 

Where possible lifting lugs shall be provided to facilitate disassembly of the pumps. 

16




Materials for pump parts shall be in accordance with API 610 Table-H and shall be as specified in the 

data sheets. For pump parts not designed as full compliance materials in Table-H, Supplier/ Vendors 

shall get Purchaser’s prior approval. 

The pumps may be subject to dead head conditions (zero flow, maximum head), due to accidental 

closure of the discharge valves or any other reason. The Contractor / Vendor shall indicate in the bid 

documentation the maximum time period that the pumps can operate under dead head conditions. 

2.2 Process and Operating Criteria 

The design should be based on the most severe operating condition specified on the Project Data 

Sheets. 

The pumps shall be selected such that: 

• Over the “Normal Operating Flow Range” the duty point is close to the best efficiency point as 

far as practicable. 

• Curves shall rise continuously to shut off from the rated flow duty point. The head rise shall not 

exceed the percentage specified in API 610 

The pumps shall operate such that difference between NPSHA and NPSHR shall be at least 2.0 m 

across the entire operating range. The NPSHR shall be lower than the NPSHA over the full operating 

range of the pump. 

The suction specific speed (N ss ), calculated at the best efficiency point (BEP) for the maximum 

impeller diameter of the casing, shall not exceed 12800 SI Units (11000 US Units). Pumps offered 

with suction specific speed > 12800 SI Units (11000 US Units) may be accepted subject to 

Purchaser’s written approval. Pumps with N ss < 10,000 SI Units will be preferred. Pumps fitted with 

inducers are not acceptable. 

2.3 Amendments, Supplements and Choices to API 610 

The amendments, supplements and choices to API 610 / ISO13709 given in this Section are directly 

related to equivalent sections and paragraphs in API 610. For clarity, the section and paragraph 

numbering of API 610 has been used as far as possible. 

Only amendments, supplements and choices have been stated hereafter. All other paragraphs and 

clauses which have not been mentioned shall be considered unchanged and shall be applied as 

stated in API 610 and references mentioned therein. 

API 610 Paragraph no.: 

3 Terms and definitions 

3.60 (New) 

17




‘Supplement' adds the requirement following this term to the referenced API Standard requirement. A 

supplement does not change the API Standards requirement. 

3.61 (New) 

‘Amendment' changes the API Standard requirement to that which follows the term. All parts of the 

API Standard requirement, which are not addressed, remain applicable. 

3.62 (New) 

'Choice' provides direction for choices, which are specified by the API Standard paragraph. Parts of 

bulleted paragraphs, which do not require decisions, are fully applicable. 

5.1.3 (Amendment) 

Contractor / Vendor to note there is no cooling water available in the plant. Contractor / Vendor to 

consider air cooling for any cooling requirement. 

5.1.10 (Supplement) 

The Net Positive Suction Head Available (NPSHA) shall exceed the Net Positive Suction Head 

Required (NPSHR) by at least 2 m (6 ft) throughout the range from minimum continuous stable flow 

up to and including the rated capacity, and by 0.5 m (2 ft) at 120% of rated flow. 

5.1.13 (Choice / Supplement) 

Paragraph 5.1.13 shall apply. 

Pumps on non-parallel operation shall have stable head/capacity curves, which continuously rise by 

at least 5% from rated capacity to shut-off. Pumps in parallel operation shall have a head rise from 

the rated point to shut-off not less than 10% and preferably not greater than 20% depending on 

system requirements. 

5.1.16 (Choice / Supplement) 

Paragraph 5.1.16 shall apply. 

The maximum sound pressure level shall be as specified under Section ‘Noise Limitation’ elsewhere 

in this specification. 


The numbers of vanes in impellers shall be different to the numbers of vanes in diffusers. On pumps 

with two or more stages impellers/diffuser configuration shall be staggered to avoid coincidence of 

pressure pulses. 


Contractor / Vendor to note there is no cooling water available in the plant. Any cooling system shall 

be air cooled. 

18




5.1.32 (New) 

The Contractor / Vendor shall advise the minimum and maximum allowable safe flows for all 

proposed pumps for continuous operation, considering temperature rise, vibration limits and NPSH 

limits. Contractor / Vendor shall indicate “preferred operating range” and “allowable operating range” 

on the pump characteristic curve for rated speed and lowest operating speed corresponding to the 

low flow-low head operating point. 

5.1.33 (New) 

For balancing axial thrust in multi-stage pumps, only the following arrangements shall be used, either 

alone or in combination: 

- Individually-balanced impellers or opposed arrangements of impellers; 

- A balancing piston (considering the subject service fluid is non-abrasive); 

Balance disk or combinations with a balance disk shall not be used. 

5.3.6 (Choice) 

All parts referred to in the definition of pressure casing (3.42) shall have the same MAWP. 

5.4.2.1 (Amendment) 

All pumps shall have flanged suction and discharge nozzles of equal ASME pressure/temperature 

ratings. 


Threaded connections to the pressure casing shall not be used, except that the seal gland connection 

may be threaded. 


All auxiliary connections to the pressure casing shall be fitted with flanged stubs. Integral flanges may 

be used. If the pump nozzles are Class 900 or above, or the pumping temperature is 0°C (32°F) or 

below, or if the pump is for hazardous service, or if ISO 15156 or NACE MR0103 is applicable, then 

socket welded connections shall not be used. In these cases full penetration butt welded connections 

are required. 

5.4.3.6 (Supplement) 

Valves shall not be welded to the pump. 


Openings shall not be furnished unless they are essential, in which case they shall be located away 

from high-velocity areas. The provision and location of openings shall be identified in the Contractor / 

Contractor’s / Vendor ’s proposal and shall be subject to the approval of the Purchaser. All openings 

19




furnished and not connected to piping shall be closed with a flange in accordance with (5.4.3.4). 

Balance leak off lines and their connections shall be flanged. Unions shall not be used. 


Pumps shall preferably be self-venting. If this is not possible, then external vent connections in 

volute(s) and, if necessary, in seal areas shall be provided. Both drain and vent connections shall be 

welded and provided with flanged connection and valve. In case of multiple vents/drains, each shall 

be manifold to single-flanged and valved connection. Piping shall terminate in ANSI flanges, of the 

same rating as the pump discharge nozzle at the baseplate edge. 

5.5.1 (Amendment) 

Allowable Nozzle loads and moments shall be 2 times of the figures given in API 610 / ISO 13709 

Table 4. Supplier shall ensure that base plates are also suitable for withstanding above loads. 

5.6.16 (New) 

Preferably the pump selection shall be such that their rated impeller diameters not greater than 90% 

of the maximum diameter impeller and not less than 110% of the minimum impeller diameter that the 

casing will take. 

5.7.2 (Amendment / Supplement) 

The pump casing wear rings shall be manufactured from material which ideally has a Brinell hardness 

preferably 100BHN (but not less than 50BHN) greater than the impeller wear rings in their finished 

state. For wear ring materials with higher galling tendencies, if increased running clearances are 

considered necessary, efficiencies quoted shall be based on the higher running clearances. 

5.7.3 (Amendment / Supplement) 

The pump casing and impeller wear rings shall be held in place by setscrews. Tack welding is not 

acceptable. 


Pumps shall be equipped with mechanical seals conforming to API 682. Mechanical seals shall be 

offered and supplied from one of the following makes viz. Flowserve / Eagle Industries / John 

Crane / Burgmann. 

The seal manufacturer shall formally approve for each pump the following: 

• The seal selection 

• The seal flush plans 

• The seal metallurgy 

• The seal system 

20




• The seal installation 

• Special features (such as multi point injection) 

• The proposed method of operation 

The Contractor / pump Vendor shall be responsible for obtaining this approval from the seal 

manufacturer and submitting to Purchaser for review. 

The Contractor / Vendor shall furnish the seal manufacturer with the pump data sheet and also the 

project and pump identification numbers for each pump, in order that the seal manufacturer may 

prepare for the Purchaser a complete seal schedule and interchangeability chart. 

Compatible buffer / barrier fluid (if applicable) for the intended service and the characteristics shall be 

specified by seal manufacturer. Combined heat load (heat soak and seal face generated heat) 

calculation shall be furnished by seal manufacturer. Cooling requirements / seal flush rates for 

restricting to the maximum allowable rise in temperature of 5°C shall be specified by Contractor / 

Vendor based on heat load calculation. Contractor / Vendor shall quote closed loop seal cooling 

system with finned coil with air cooling. 

Contractor / Vendor to note there is no cooling water available in the plant. Any cooling system shall 

be air cooled. 

All components of seals and seal systems shall withstand the maximum discharge pressure and the 

maximum allowable temperature. The Contractor / Vendor shall advise in his Bid of the maximum 

dynamic and static sealing pressure and temperature if these requirements cannot be met. 

The pump Vendor shall supply and install all mechanical seal piping and appurtenances to make a 

complete operational seal system. 


Contractor / Vendor shall perform a transient (as well as steady state) torsional critical speed analysis 

for sub-sections (c) and (d) of the clause. 

5.9.2.6 (Choice) 

Paragraph 5.9.2.6 will apply when specified on the data sheet. 

When a torsional analysis is performed the Vendor shall furnish a detailed report. 


For vertical, close-coupled, in-line pumps vibration readings shall be taken on both bearings for the 

electric motor driver in the horizontal plane at 90° to each other. For vertical pumps with a flexible 

coupling additional readings shall be taken at the pump top bearing. 


21




When hydrodynamic thrust bearings are proposed, the pump hydraulic design shall be such that the 

axial loads are unidirectional under all operating conditions. Contractor / Vendor shall submit with bid, 

curves showing the variation of axial load with capacity (zero flow to 120% BEP) for design internal 

clearances and two times design internal clearances. For variable speed units, similar curve for 

maximum speed and minimum speed shall be submitted. 


Contractor / Vendor to note that there is no cooling water available in the plant. In case of any Lube 

oil cooling requirement, vendor shall achieve the same using air cooling. 

5.12.2.5 (Choice/Supplement) 

For casting repairs made in the Contractor’s / vendor's shop, repair procedures including weld maps 

shall be submitted for approval to Purchaser. The Purchaser's approval is required before proceeding 

with repair. Repairs made at the foundry level shall be controlled by the casting material specification. 


Pump couplings shall be supplied by the pump Vendor. Flexible all-steel couplings shall be provided 

for all pumps. Rigid all-steel, axially adjustable, couplings shall be supplied for vertical pumps with 

bearings integral with driver. The complete pump coupling shall be supplied fully machined by the 

pump Vendor and shipped with the pump. Couplings shall be rated for the maximum transient torque 

which can be expected in the case of a short circuit at the motor terminals and rapid automatic 

reconnection of the motor with full opposite residual voltage, under full load conditions. 


Coupling guards shall be of non-sparking material and shall conform to BS PD 5304. Aluminium is not 

accepted as a non-sparking material. 


The datasheet shall specify whether pipe or tubing shall be used for auxiliary systems. Seamless pipe 

of ASTM A 312, Type 316L shall be used if maximum pumping temperature is above 260 °C (500 °F) 

or if the auxiliary system contains erosive fluid. 

If piping is specified on the datasheet, then pipe shall be used for all auxiliary systems, except for 

air/water coolers and barrier/buffer gas systems, which may be made using stainless steel seamless 

tubing. 

If tubing is specified on the data sheet then stainless steel (SS 316L) seamless tubing shall be used 

for all auxiliary systems unless higher alloys are required to conform to pump metallurgy. 

Insulation or guarding shall be provided as an integral part of the auxiliary piping system to provide 

personnel protection if the non-insulated metal temperature exceeds 70 °C (160 °F) and the auxiliary 

piping system is in an area where it can be touched during normal operation and maintenance 

activities. 

22




6.5.1.6 (Choice) 

Each piping system shall be manifolded to one purchaser's connection (inlet or outlet); these 

connections shall be terminated with proper rated flange at the end of baseplate/skid, and within the 

confines of the baseplate/skid. 


Flanges shall be used instead of socket-welded unions. 


If a spare rotor or complete inner assembly for multistage pumps is supplied with the pump, it shall be 

subject to the same running/performance tests in the pump casing as the main rotor. 

7.3.3.4b) 

(Supplement) 

Bearing housing temperature shall be measured at all five points of the performance test, except 

closed valve. For pump powers greater or equal to 100 kW, pump shall be run until oil temperature 

stabilizes at rated condition. 


An NPSH test shall be performed in the following cases: 

(i) For pumps, if the difference between NPSHA and NPSHR is less than 2 m (6 ft); 

(ii) For pumps handling liquids containing dissolved gas; 

(iii) For pumps with a suction specific speed above 12800 SI Units (11000 US Units); 

(iv) If the NPSHA at 120% of rated flow exceeds the NPSHR by 0.5 m (1.5 ft), or less 

2.4 Auxiliary Equipment and Connections 

Where required or when specified on the equipment data sheets, lube oil and auxiliary process piping 

systems including accessories such as gauges and valves, shall be supplied fully assembled and 

installed. 

All flushing piping and accessories shall be provided. All parts of the flushing system shall be equal 

to or better than the pump casing material, and shall be suitable for maximum discharge pressure and 

temperature. 

The following connections and auxiliary equipment shall be supplied as a minimum: 

• Pump casing drains and piping; 

• Pump venting points and piping; 

• Bearing temperature connections. 

23




All pump vents and drains shall be provided with an isolating valve piped to the base plate edge and 

terminated with a blind flange. All terminating flanges shall be in accordance with ASME B16.5 and 

shall be of the same rating as the pump discharge nozzle flange. 

2.5 Bearings and Bearing Housings 

Steel bearing housings shall be provided. 

Bearing type and arrangement shall be in accordance with API 610 along with the limitations given in 

Table 9 of API 610. 

Bearings without pressure lubrication shall be ring oil lubricated and have constant level oilers. 

2.6 Lubrication 

Where the bearing housing acts as an oil chamber, an oil level sight glass with the recommended 

level clearly marked shall be fitted. Topping up of the bearing housing oil chamber shall be possible 

without dismantling the pump set assembly or any of it’s auxiliaries. 

The Contractor’s / Vendor’s recommendations for lubrication will be submitted in the form of 

Lubrication Schedule. 

2.7 Electric Motors 

Rating of the electric motors shall be sized considering margin required as per API 610 on the 

maximum pump duty point. The motor rating shall also be crosschecked to satisfy the maximum 

(usually end-of-curve) power requirement of pump with reasonable margin so that the motor is 

capable enough to cater to any un-intended run-out case. All the motors shall be flameproof Ex (d) 

type, suitable for Zone 2, Gas group IIA, IIB, and temp. class.T3. Type test certificates for explosion 

protection class from the recognised testing authority shall be submitted. As per the statutory 

requirement in India the approval from the chief controller of explosives (CCOE) for flameproof 

motors, Ex (d) must be submitted. CCOE Certificates for the Flameproof motors shall be submitted 

along with the final MDR / OMM. 

Where sleeve bearing motors are offered, a limited end float type of coupling shall be applied to 

prevent damage to the motor due to axial movement of the rotor during start-up or shutdown. 

Vertical and horizontal adjustment alignment screws shall be provided for all drivers having a mass of 

over 250 kg. 

2.8 Machinery Protection System 

The instrumentation (as applicable) shall be designed for hazardous area Zone1, Gr. IIA, IIB, T3. The 

enclosure protection shall be minimum IP65. 

24




The MOC for instrumentation shall be suitable for the process and environment. 

The instrumentation process and pneumatic / hydraulic tubing shall be SS316. 

All pumps shall be offered with an included primary protection system for safe operation of pump and 

driver. 

The description of each protective device of the pump shall be in accordance with API 610 and API 

682 as required for relevant seal flushing plans 

Apart from the protections outlined, the Contractor / vendor may include other protections deemed 

necessary for operation of the package as a whole. 

2.9 General 

Contractor / Vendor to furnish datasheets for total instrumentation employed 

Any additional protection devices if recommended by the pump manufacturer shall be considered. 

Set points for pressure, temperature, vibration and seal leakage level parameters for the pump and 

motor towards alarm and trip conditions shall have to be specified by the Contractor / Vendor. 

Pump and drive protection signals shall be interfaced with the Plant Control System. 

2.10 Pump Skid Instrument Installation 

The installation and wiring of skid-mounted equipment shall be in accordance with the applicable 

Standards, Codes and Statutory Regulations. 

Pump skid instrument equipment and cabling layout drawings, together with junction box termination 

drawings, shall be submitted for approval by the Purchaser. 

2.11 Civil 

Contractor / Vendor Shall furnish all the relevant information for carrying out foundation designs. As a 

minimum following values shall be provided. 

- Skid dimensions including General arrangement. 

- Loads / Forces acting on top of foundation / Vessel 

- Anchor bolts or foundation bolt details 

25




3. PROTECTIVE COATING 

The equipment base plate and skid structure and support shall be painted as per the project 

Specification for Painting / Coating Requirements 0435-JH0902-00-PI-SPC-003. Pump and the 

Motors shall be painted as per manufacturer standard. Manufacturer painting standard shall be 

furnished with the Bid for review during bid evaluation. 

26




4. SPARE PARTS AND SPECIAL TOOLS 

4.1 Spare Parts 

4.1.1 Spare Parts Required 

a) Mandatory Spares: The Check list for Mandatory spares for the pump packages are 

attached in bid package. Cost of Mandatory spares shall be included to arrive at the total cost 

of package for a particular item. 

b) Spares for two years Normal operation: Contractor / Vendor shall furnish an 

itemised list of recommended spares with unit prices for two years normal & continuous 

operation of the complete pumping unit (including Mechanical, Electrical, Instrumentation 

spares) required. These spares shall be over and above the specified mandatory spares. 

c) Erection & Commissioning spares: Contractor / Vendor shall include in his 

scope of supply for each pump package, the spares required for erection & commissioning of 

the pump, motor, Instruments etc .of that package. List for the same (separately for each 

pump to be furnished by the bidder along with the bid. 

If however, any additional spare is consumed during erection & commissioning over and 

above the included erection & commissioning spares, the same shall be provided by the 

contractor/ vendor at no extra cost to purchaser at the time of erection & commissioning. 

4.1.2 Information Required 

The parts list shall specify the source of manufacture and model number of each component part. 

4.1.3 Contents 

The spare parts list shall also identify the quantity of spare parts held, or the nearest major service 

centre, relative to the equipment being offered to the Purchaser. 

Should the Purchaser exercise its option to purchase any or all of the spare parts, it shall be the 

responsibility of the Contractor / Vendor to provide the following at no extra cost to facilitate 

identification and classification of spare parts: 

• Every item shall have a tag or legend bearing the drawing and part number reference; 

• The shipping advice note shall cross reference to the tag number; and 

• A list giving the following information for each spare part: 

− Handbook number; 

− Handbook drawing number; 

27




− Handbook drawing part number; 

− Spare parts list and item number description; 

− Manufacturing drawing number; 

− Manufacturing drawing part number; and 

− The Purchaser’s specification number and/or purchase order number under which parts 

were supplied. 

Where the same pump part number is used for a component in differing pumps additional identifiers 

must be used. 

Spare parts shall be traceable to a pump by size, type and, if unique, pump equipment number. 

4.2 Special Tools 

The Contractor / Vendor shall supply one (1) set of special tools & tackles required for the erection 

and/or maintenance of the package including all ancillary equipment. 

Special Tools & Tackles means all such tools / tackles those are specific to the erection and/or 

maintenance of the supplied equipment/package, and are normally not expected to be available in a 

plant workshop, but without which it would be difficult or time-consuming to do erection and/or 

maintenance of the supplied equipment/package. 

The Contractor / Vendor shall identify the special tools required with Bid. 

Special tools shall be itemised and submitted for review. 

28




5. MARKING 

Pumps shall have a nameplate made out of 1 mm thick grade 316 stainless steel plate firmly attached 

to the pump pedestal by means of stainless steel screws or rivets. 

The information stamped on the nameplate shall be as indicated in Clause 5.13.2 of API 610. 

Lettering shall be 5 mm high with 3 mm spacing between lines. 

Pumps shall have a direction of rotation arrow cast into pump casings or indicated on a stainless steel 

plate mounted on the bearing housing or pump pedestal close to the drive end. 

Prominent warning signs shall be affixed to the pump for removal of anti-brinelling devices and 

lubrication requirements. 

29




6. TESTING 

6.1 General 

As a minimum, inspection, testing and QA shall be conducted according to this specification and the 

attached data sheets. 

The Contractor / Vendor shall operate a quality management system to ensure the technical 

requirements of this project are met. The QA requirements specified herein shall apply to all 

materials and equipment in the Contractor’s / Vendor’s scope of supply. Shop inspection by the 

purchaser’s nominated inspector will be required and the extent of inspection shall be approved by 

the Purchaser. 

Test requirements will be as specified here in and as noted on the pump data sheet. Contractor’s / 

Vendor’s standard QA/QC procedures are acceptable except if modified herein. 

Materials mill test certification (chemical and mechanical data) as noted on the data sheet, for 

pressure containing parts, impeller and shaft are required. 

The Contractor / Vendor shall supply calculations to show the conversion of data acquired with tests 

carried out using water to that applicable for the fluids proposed for operation of the pumps. 

The Contractor / Vendor shall include a description of shop pump test set-ups including 

instrumentation to be used and specific step by step test program. 

6.2 Welds 

Testing of welds on the pump sets and associated equipment shall be in accordance with Table-13 of 

API 610. 

Contractor / Vendor to follow the Basis of Design document: 0435-JH-0902-ME-BOD-0001 for the 

extent of inspection & testing criteria. 

6.3 Castings 

All major weld repairs to pressure containing castings shall be subject to approval by the Purchaser. 

Weld procedures and weld maps shall be furnished that show the dimension and locations of these 

defects. Material inspection shall be in accordance with Table-13 of API 610. 

Major defects are: 

• Repairs to leaks that develop during hydrostatic tests; 

• Repairs where the depth exceeds 20% of the wall thickness or 25 mm, which ever is less; and 

• Repairs where one defect surface area exceed 65 cm². 

30




Weld repairs shall be inspected by dye penetrant/magnetic particle examination. Castings shall be 

re-hydrotested after repairs have been carried out. 

6.4 Hydrostatic Tests 

Hydrostatic testing shall be carried out in accordance with API 610. 

Gaskets used during hydrostatic test shall be identical to those supplied with the pump for operational 

service. 

Leaks past any gasketed areas or any joint connections are unacceptable. 

6.5 Performance Test 

The pumps shall performance tested as per Section 7.3.3 of API 610. 

The pumps shall be tested at the following duty points: 

• Shutoff wherever practical, otherwise at minimum thermal flow; 

• Minimum Continuous Stable Flow; 

• Rated flow; 

• Guarantee point (if guarantee point is the rated point, then shall normal operating point) 

• Best efficiency point (BEP); 

• Maximum Allowable Flow (at least 120% of the rated flow or BEP whichever is more); and 

• Additional points may be required if more than 30% of the curve is having no measured point. 

The following parameters shall be measured during the tests at all test points: 

• Pump hydraulic power; 

• Flow rate; 

• Pump head; 

• All bearing vibration amplitudes; 

• Bearing temperatures; 

When supplied with the pump, the spare rotor and inner casing assemblies shall be performance 

tested in the corresponding pressure casing. 

6.6 NPSHR Test 

NPSHR test if required as per the conditions specified in this specification or if specified in the data 

sheet shall be conducted. NPSHR test shall be of the vacuum suppression type. A throttle valve 

NPSHR test may be accepted subject to Purchasers approval. 

31




NPSHR tests shall be carried out on all pumps in accordance with Section 7.3.4.2 of API 610. 

6.7 Unit Test 

Each pump set, shall be subject to a complete unit test as per Section 7.3.4.3 of API 610 but with the 

flow rates and pump speeds corresponding to the performance tests defined in Section 6.5 of this 

specification. 

Complete unit test shall be conducted in the same manner as mechanical run test specified under 

section 6.8 except that job driver and all job auxiliaries shall be used during this test. Due to use of job 

driver, difference in specific gravity between the test liquid and actual pumped liquid may sometimes 

not permit running the pump at rated capacity during this test, in such cases, test shall be performed 

at the maximum permissible capacity. 

6.8 Mechanical Run Test 

After the performance test has been completed, the Contractor / Vendor shall operate the pump in a 

stable condition for at least 4 hours at rated capacity and for 2 hours at minimum continuous flow, 

during which pump mechanical behaviour shall be demonstrated to meet the requirements of this 

specification. Counting of test duration shall start after stabilization of bearing temperature. The test 

shall be run at maximum continuous speed. 

Each pump shall be stripped down after completion of the test and shall undergo a thorough visual 

inspection. Special emphasis shall be placed on the following items: 

• Pump casing and impeller wear rings; and 

• Shaft bearings. 

If there is evidence of internal rubbing or sleeve bearing damage on disassembly following the unit 

test, the cause of the problem must be corrected and the pump shall be rerun, again dismantled and 

re-inspected. This process will be continued until there is no measurable dimensional change or metal 

transfer in the bearings or close-clearance parts. Pumps need not be run again if no evidence of 

rubbing or other defects is found on disassembly. The cost of subsequent testing plus 

disassembly/reassembly (following detection of internal pump damage) shall be at the Contractor’s / 

Vendor’s cost. 

32




7. MATERIAL SOURCING TRACEABILITY AND CERTIFICATION 

The Contractor / Vendor shall submit a Manufacturers Data Report (MDR) which will allow 

identification and certification of all pressure retaining parts and key rotational parts of the pumps 

which shall include mechanical properties and chemical composition analysis, mill certificates, heat 

numbers and certificates of conformance. Each certificate shall be reviewed and signed by the 

manufacturer’s authorised personnel as detailed in the Inspection and Test Plan. 

Pressure retaining parts shall be clearly marked to ensure that full traceability is maintained. 

Pressure-retaining parts shall include body forgings and castings. 

Key rotational parts include the impeller and impeller shaft. 

Certificates shall be available at final inspection in the manufacturer’s works. 

Certificates of compliance shall be provided for bolting used in pressure retaining parts. 

33




8. PACKING, SHIPPING AND HANDLING 

Preparation for shipment shall be as per Section 7.4 of API 610. 

The components of the pump set shall be shop assembled to the maximum extent practical, such that 

field assembly is both minimized and simplified, and matching of components is assured. The parts 

that cannot be shop assembled prior to shipment shall be shop fitted, identified and match marked. 

The equipment items that are shipped in a “knocked down” condition shall be individually tagged with 

the assigned tag/part number. Contractor’s / Vendor’s philosophy for the same shall be reviewed and 

approved by Purchaser. 

Adequate provisions shall be made to prevent damage to the bearings from brinelling during 

transport. Rotors on equipment shall be strapped down to wooden blocks for transport, and 

appropriate shaft locks shall be provided and fitted. Appropriate high visibility label tags shall be fitted 

to all blocked or locked rotor equipment. 

All spare parts shall be packed separately from the main pump set assemblies. 

All parts and equipment including spares shall be packed suitable for long term storage in a tropical 

climate. 

The spare rotor shall be crated in a metal container for transportation and storage; the crating method 

shall be suitable for at least 4 years storage in both horizontal and vertically suspended position. The 

container shall be equipped for nitrogen blanketing. 

34




9. INSPECTION, QUALITY ASSURANCE AND QUALITY CONTROL 

REQUIREMENTS 

The Contractor / Vendor shall conform to the requirements of this specification in the performance of 

the work under the Contract. 

The Purchaser reserves the right to inspect the manufacture of the pumps at the Contractor / Vendor 

or Sub-Vendor’s premises at any time. The Purchaser may also appoint a third party inspector to act 

on his behalf. 

The Contractor / Vendor shall submit an Inspection and Test Plan (ITP) for approval prior to 

commencement of manufacture. The Purchaser will advise the Contractor / Vendor, by marking up 

the Inspection and Test Plan, of the specific inspection review, witness and hold points required. The 

Contractor / Vendor shall give ten working days prior notice to the Purchaser of such item or hold 

point being reached. 

Contractor / Vendor shall submit quality plans, test procedures for all tests, for approval of Purchaser, 

and testing shall be done only after such documents have been duly approved. 

As a minimum the following stages will be subject to witness/ 

/review by the Purchaser or third party inspector: 

• Visual inspection of all parts prior to assembly of pump; 

• Visual inspection of the assembled pump with accessories; 

• Surface finish and profile verification at each phase of surface preparation and coating; 

• Name plate checks; 

• Material certification checks; 

• Radiography of impeller tip and panoramic shot of impeller; 

• Ultrasonic testing of shaft; 

• Dynamic balancing of rotor assembly; 

• Heat sample of each casing with test results; 

• Sound level and vibration tests; 

• Review of all documents prior to shipping; 

• Full dimensional checks; and 

• Pump tests. 

The Contractor / Vendor shall obtain Purchaser approval of the following prior to any fabrication 

taking place: 

• Weld procedures; and 

35




• All drawings associated with the pump sets. 

The Contractor / Vendor shall afford the Purchaser the use of telephone, facsimile and office facilities 

for the purpose of completing reports during inspections. 

Where inspection or testing is performed by certified testing laboratories, they shall be registered by 

an internationally recognized testing organization. 

The appropriate inspection equipment and the Contractor’s / Vendor’s personnel shall be readily 

available to complete the inspection at the time agreed. 

The appropriate test procedure and acceptance criteria shall be available to the Purchaser for 

immediate analysis of the inspection results. 

The final inspection, before issue of a release note for the pump sets, shall include material 

certificates, test certificates, surface treatment, dimensional conformity, tagging and packing 

conformity. 

Specimen crating and packaging may also be inspected. 

36




10. SITE ERECTION, TESTING AND COMMISSIONING ASISTANCE 

The Contractor / Vendor shall provide site erection, pre-commissioning and commissioning 

assistance of pump sets. After the completion of the precommissioning activities (including 

mechanical, electrical, instrumentation) each pump package shall be subjected to a site trial run / 

operation (Duration for the same shall be finalised after award). During this trial run, satisfactory 

operation of pump package unit (including pump, driver, contractor / vendor / supplied electrical 

equipment and all auxiliary equipment) shall be established. Operating point shall be within pump 

operating Flow range. Site trail run shall form the part of commissioning. 

The Contractor / Vendor shall be responsible for witnessing and signing off all activities associated 

with commissioning and that testing of pumps are carried out in accordance with Pump vendor’s 

requirements. 

On completion of Site acceptance testing & Commissioning, the Vendor shall submit a report to the 

Purchasers detailing all activities associated with precommissioning, commissioning and testing of 

pumps. 

. 

37




11. PERFORMANCE GUARANTEE 

The Contractor / Vendor shall guarantee that the pump sets supplied shall the meet the performance 

requirements set down in this specification (including referenced documents). 

Special emphasis is placed on the following criteria: 

• The ability to meet duty point at the normal flow range and rated flow rate; 

• Powers draw at normal and rated flow rates; 

• NPSH requirements at normal and rated flow rates; 

• Drive motor efficiencies at normal and rated flow rates; 

• Equipment noise level under all operating conditions. 

The Contractor / Vendor will guarantee the pump performance as witnessed in factory tests. The 

Contractor / Vendor shall nominate the performance of the pump at the rated test point in terms of 

total dynamic head, and power at a nominated flow rate and pump speed. The hydraulic power at the 

test point shall be advised by the Contractor / Vendor in the form of a positive and negative 

percentage tolerance. No negative tolerance on flow or total dynamic head at the rated speed will be 

accepted. 

38




13. VENDOR SUPPLIED DOCUMENTS 

The Contractor/ Vendor shall supply documentation in accordance with the Vendor Document 

Requirements List (VDRL) indicated under Appendix B of this specification. 

39




APPENDIX-A: SPECIFICATIONS & DATASHEETS 

Document No. 

0435-JH0902-00-PI-SPC-0003 

0435-JH0902-00-EL-SPC-0002 

0435-JH0902-00-EL-DAS-0085 

0435-JH0902-10-ME-DAS-0012 

0435-JH0902-10-ME-DAS-0016 




Datasheet for Low Voltage Induction Motors 

Mechanical Datasheets for Sump Pumps at RamanMandi 

Mechanical Datasheets for Sump Pumps at Bhatinda 

40




APPENDIX-B: VENDOR DATA REQUIREMENT LIST 

Sr. 

No. 

Document / Drawings For Purchaser’s approval For Purchaser’s Information 

1. Pump GA Drawings Yes - 

2. Pump C/s Drawings Yes 

3. Filled in Mechanical 

Datasheets 

Yes 

4. Performance Curves Yes 

5. Filled in Motor Datasheets Yes 

6. GA Drawings for the Motors 

indicating Terminal box 

details and cable sizes 

Yes 

7. Characteristic curves for 

Motors 

Yes 

8.. Instruments Datasheets Yes 

9. Quality Procedures: 

Yes 

- Hydro test 

procedures 

- WPS/PQR 

- ITP 

- FAT Procedures 

- SAT Procedures 

10. MDR / IOM manuals Yes (1 copy) 3 Hard copies & 1 Soft Copy CD. 

41

Equipment Data Sheet for Centrifugal Pump (VS) 

Tag No. : P-20-01 & P-20-02 Client: 

Service: Sump Pumps for Transfer of Drain Oil (Hydrocarbon) Plant Location: 

P & ID No. : 435-JH0902-20-PR-PID-2003 Supplier: 

Calculation Ref. : 

Purchase Order No.: 

No. of Units: 

Service Description: 

Transfer of Drain Oil (Hydrocarbon) 

Centrifugal Pump Data Sheet to API 610, 10th Edition 

1 NOTES: INFORMATION BELOW TO BE COMPLETED: BY PURCHASER BY MANUFACTURER BY MANUFACTURER OR PURCHASER 

2 DATA SHEETS (6.1.1) 

REVISIONS 

3 ITEM NO. ATTACHED ITEM NO. ATTACHED ITEM NO. ATTACHED NO. DATE BY 

4 PUMP 

P-20-01 / P-20-02 

5 MOTOR M-20-01 / M-P-20-02 

6 GEAR 

7 TURBINE 

8 APPLICABLE OVERLAY STANDARD(S): 

9 OPERATING CONDITIONS (5.1.3) LIQUID (5.1.3) 

10 FLOW, NORMAL 10 (m 3 /h) RATED 11 (m³/h) LIQUID TYPE OR NAME Refer service description & process data (Sheet 2 of 5) 

11 OTHER Refer Sheet 2 of 5 HAZARDOUS FLAMMABLE (5.1.5) 

12 

13 SUCTION PRESSURE MAX./RATED Refer Sheet 2 of 5 / (kg/cm 2 a) (Refer Sheet 2 of 5) 

14 DISCHARGE PRESSURE Refer Sheet 2 of 5 (kg/cm 2 a) PUMPING TEMP (°C) 

15 DIFFERENTIAL PRESSURE Refer Sheet 2 of 5 

(kg/cm 2 ) VAPOR PRESS. (kg/cm 2 a) 

16 DIFF. HEAD Refer Sheet 2 of 5 (mlc) NPSHA Sht 2/5 (m) Remark 1 RELATIVE DENSITY (SG): 

17 PROCESS VARIATIONS (5.1.4) VISCOSITY (cP) 

18 STARTING CONDITIONS (5.1.4) SPECIFIC HEAT, Cp (kJ/kg °C) 

19 SERVICE: CONT. INTERMITTENT (STARTS/DAY) CHLORIDE CONCENTRATION (PPM) 

20 PARALLEL OPERATION REQ'D (5.1.13) H 2 S CONCENTRATION (6.5.2.4) (PPM) WET (5.2.1.12c) 

21 SITE DATA (5.1.3) CORROSIVE / EROSIVE AGENT Due to Water (5.12.1.9) 

22 

23 LOCATION: (5.1.30) MATERIALS (5.12.1.1) 

24 INDOOR (covered location) HEATED OUTDOOR UNHEATED ANNEX H CLASS (5.12.1.1) S6 

25 ELECTRICAL AREA CLASSIFICATION (5.1.24 / 6.1.4) MIN DESIGN METAL TEMP (5.12.4.1) 0 (°C) 

26 CL 1 ZONE 2 GR IIA, IIB DIV T3 REDUCED HARDNESS MATERIALS REQ'D. (5.12.1.11) Yes 

27 WINTERIZATION REQ'D TROPICALIZATION REQ'D. BARREL/CASE IMPELLER 

28 SITE DATA (5.1.30) CASE/IMPELLER WEAR RINGS 

29 ALTITUDE 203.5 (m) BAROMETER (bara) SHAFT 

30 RANGE OF AMBIENT TEMPS: MIN/MAX. 0 / 50 (°C) DIFFUSERS 

31 RELATIVE HUMIDITY: MIN / MAX 5 / 90 (%) BOLTING PTFE …………………………………………………………………………………………… 

coated A193 Gr. B7 

32 UNUSUAL CONDITIONS: (5.1.30) DUST FUMES PERFORMANCE: 

33 OTHER PROPOSAL CURVE NO. RPM 

34 IMPELLER DIA. RATED MAX. MIN. (mm) 

35 IMPELLER TYPE 

36 DRIVER TYPE RATED POWER (kW) EFFICIENCY (%) 

37 INDUCTION MOTOR STEAM TURBINE GEAR MINIMUM CONTINUOUS FLOW: 

38 OTHER THERMAL (m 3 /h) STABLE (m 3 /h) 

39 Refer motor specification/ Datasheet respectively PREFERRED OPER. REGION TO (m 3 /h) 

40 MOTOR DRIVER (6.1.1 / 6.1.4) ALLOWABLE OPER. REGION TO (m 3 /h) 

41 MANUFACTURER MAX HEAD @ RATED IMPELLER (m) 

42 (kW) (RPM) MAX POWER @ RATED IMPELLER (kW) 

43 FRAME ENCLOSURE NPSHR AT RATED CAPACITY (m) (5.1.10) 

44 HORIZONTAL VERTICAL SERVICE FACTOR MAX SUCTION SPECIFIC SPEED: 12,800 SI Units (5.1.11) 

45 VOLTS/PHASE/HERTZ 415 / 3 / 50 MAX. SOUND PRESS. LEVEL REQ'D Max. 85 @ 1.0 m (dBA) (5.1.16) 

46 TYPE EST MAX SOUND PRESS. LEVEL (dBA) (5.1.16) 

47 MINIMUM STARTING VOLTAGE (6.1.5) EST MAX SOUND POWER LEVEL (dBA) (5.1.16) 

48 INSULATION TEMP. RISE UTILITY CONDITIONS (5.1.3) 

49 FULL LOAD AMPS ELECTRICITY 

50 LOCKED ROTOR AMPS DRIVERS 

51 STARTING METHOD HEATING 

52 LUBE SYSTEM VOLTAGE DIP 80% OTHER (6.1.5) 

53 

54 BEARINGS (TYPE/NUMBER): STEAM MAX. PRESS. MAX. TEMP. MIN. PRESS. MIN. TEMP. 

55 RADIAL / DRIVERS 

N/A 

56 THRUST / HEATING 

N/A 

57 VERTICAL THRUST CAPACITY COOLING WATER: (5.1.19) SOURCE NOT APPLICABLE 

58 UP (N) DOWN (N) SUPPLY TEMP. (°C) MAX. RETURN TEMP. (°C) 

59 NORM. PRESS. (barg) DESIGN PRESS. (barg) 

60 REFER MOTOR DATA SHEET MIN. RET. PRESS. (barg) MAX. ALLOW. D.P. (barg) 

61 CHLORIDE CONCENTRATION: (PPM) 

66 

D 

C 

B 

A 

Rev. 

25-Aug-09 Issued for Tender SS SVI 

10-Jul-09 Issued For Review SS SVI 

07-Jul-09 ISSUED FOR DIC & SQC SS SVI JW 

Date 

2 Nos. ( 1 per tag no.) 

Issue Description 

Hindustan Petroleum Corporation Limited 

Bhatinda 

MIN. 

VOLTAGE PHASE HERTZ 

415 V 3 ph 50 

KMNP 

Originated Checked Approved 

Client 


HPCL Guru Gobind Singh Refinery Products Evacuation Project (GGSRPEP) 

Project No: 435/JH0902 SHEET 

Datasheet No: 0435-JH0902-10-ME-DAS-0016 1 of 5 

JW 

NORMAL 

MAX. 

O:\HPCL-GGSR\10-Engineering\8.04-ME-Mechanical\Mechanical docs. for comp. tender\Final Composite Tender\Sump Pumps\435-JH0902-10-ME-DAS-0016 8/26/2009







No. of Units: 





1 PROCESS DATA 

2 1. The rated and the operating parameters for the pump are as follows : 

3 

4 

5 

6 

7 

8 

9 

10 

11 

12 

Fluid 

Viscosity (cP) 

Vapour Pressure (kPaa) : 

Specific Gravity: Solids/Liquid/Mixture 

Operation 

No. of Units 

Connected in Series / Parallel 

Corrosive/Erosive 

Hazardous Service 

MIXED HYDROCARBON 

0.52 TO 6.72 @ 20 O C 

9.8 TO 59.8 @ 38 O C 

0.72 TO 0.86 

INTERMITTENT 

1 NO PER PUMP TAG NO. 

- 

YES / DUE TO WATER 

YES / DUE TO HYDROCARBON 

13 

14 

15 

16 

17 

Total Flow Rate (Min/Nor./Max.) 

Conc. by Mass % 

Conc. by Volume % 

Temperature O C 

B.P. Elevation (m) 

-' / 10 / 11 

- 

- 

25 

m3/h 

18 

Min Submerge Req. 

19 

20 

21 

22 

23 

24 

25 

26 

27 

28 

29 

30 

31 

32 

33 

34 

35 

36 

37 

38 

39 

40 

41 

42 

43 

44 

45 

46 

47 

48 

49 

50 

51 

52 

53 

54 

55 

56 

57 

58 

59 

60 

61 

62 

SUCTION CONDITIONS 

Source Pressure (kPaa) 101.325 

Static Head (kPa) 

0.82 

Line Losses (piping) (kPa) 3.4 

strainer, filter, etc (kPa) - 

Total suction pressure (kPaa) 99.00 

Total suction head (m) 12 

DISCHARGE CONDITIONS 

End of Line Pressure (kPaa) 

1801 

Static Head (kPa) 35 

Line Losses (kPa) 10 

Losses through fittings & eqmt. '- kPa 

Total discharge pressure (kPaa) 1846 

Total discharge head (m) 226 

NPSH & DIFF. PRESSURE 

NPSHA 4.74 

Design differential pressure (kPa) 1922 

Design differential head (m) 235.0 

Hydraulic power Kw 

5.87 

DESIGN CONDITIONS 

Pump casing pressure (kPag) 

VTC 

Pump casing temperature (Max/Min) o C 

VTC 

Ambient temperature (Norm/Min) o C 25 / 0 


Bhatinda 












No. of Units: 


CONSTRUCTION 

1 



SURFACE PREPARATION AND PAINT 

2 ROTATION: (VIEWED FROM CPLG END) CW CCW MANUFACTURER'S STANDARD OTHER (SEE BELOW) 

3 PUMP TYPE: (1.3) PUMP: Contractor / Vendor shall furinsh manufacturer painting std 

4 VS1 VS2 VS3 VS4 VS5 VS6 VS7 with the bid for review during bid evaluation. 

5 CASING MOUNTING: SUMP COVER PLATE PUMP SURFACE PREPARARTION 

6 INLINE SEPARATE MOUNTING PLATE (8.3.8.3.1) PRIMER 

7 SEPARATE SOLE PLATE (8.3.8.3.3) FINISH COAT 

8 CASING SPLIT: BASEPLATE/COLUMN : (6.3.17) 

9 AXIAL RADIAL BASEPLATE SURFACE PREPARATION 

10 CASING TYPE: PRIMER 

11 SINGLE VOLUTE MULTIPLE VOLUTE DIFFUSER FINISH COAT 

12 CASE PRESSURE RATING: SHIPMENT: (7.4.1) 

13 MAX ALLOWABLE WORKING PRESSURE (MPa) DOMESTIC EXPORT EXPORT BOXING REQUIRED 

14 @ (°C) OUTDOOR STORAGE MORE THAN 6 MONTHS 

15 HYDROTEST PRESSURE (MPa) SPARE ROTOR ASSEMBLY PACKAGED FOR: 

16 SUCTION PRESSURE REGIONS MUST BE DESIGNED HORIZONTAL STORAGE VERTICAL STORAGE 

17 FOR MAWP (5.3.6) TYPE OF SHIPPING PREPARATION 

18 

19 NOZZLE CONNECTIONS: (5.4.2) HEATING AND COOLING 

20 SIZE (DN) FLANGE FACING POSITION 

HEATING JACKET REQ'D. (5.8.9) COOLING REQ'D. 

21 RATING COOLING WATER PIPING PLAN (6.5.3.1) 

22 SUCTION 300# RF 

C.W. PIPING: 

23 DISCHARGE 300# RF 

PIPE TUBING; FITTINGS 

24 BALANCE DRUM C.W. PIPING MATERIALS: 

25 S. STEEL C. STEEL GALVANIZED 

26 PRESSURE CASING AUX. CONNECTIONS: (5.4.3) COOLING WATER REQUIREMENTS: 

27 NO. SIZE (DN) TYPE 

BEARING HOUSING (m 3 /h) @ (MPa) 

28 DRAIN HEAT EXCHANGER (m 3 /h) @ (MPa) 

29 VENT STEAM PIPING: TUBING PIPE 

30 WARM-UP BEARINGS AND LUBRICATION 

31 BALANCE / LEAK-OFF BEARING (TYPE/NUMBER): 

32 MACHINED AND STUDDED CONNECTIONS (5.4.3.8) RADIAL 

33 CYLINDRICAL THREADS REQUIRED (5.4.3.3) THRUST 

34 ROTOR: LUBRICATION (5.11.3, 5.11.4): 

35 COMPONENT BALANCE TO ISO 1940 G1.0 (5.9.4.4) GREASE FLOOD PURGE OIL MIST 

36 SHRINK FIT - LIMITED MOVEMENT IMPELLERS (8.2.2.3) FLINGER PURE OIL MIST 

37 COUPLINGS: CONSTANT LEVEL OILER PREFERENCE (5.10.2.2): 

38 MANUFACTURER MODEL OIL VISC. ISO GRADE 

39 RATING (kW per 100 r/min) REVIEW AND APPROVE THRUST BEARING SIZE 

40 SPACER LENGTH (mm) SERVICE FACT. 1.5 OIL HEATER REQUIRED: STEAM ELECTRIC 

41 RIGID 

42 THROUGH COUPLINGS: INSTRUMENTATION (6.4.2) 

43 MANUFACTURER MODEL ACCELEROMETER (6.4.2.1) 

44 RATING (kW per 100 r/min) LUBE PROVISION FOR MOUNTING ONLY (5.10.2.11) 

45 SPACER LENGTH (mm) SERVICE FACT. FLAT SURFACE REQUIRED (5.10.2.12) 

46 RIGID PRESSURE GAUGE TYPE 

47 DRIVER HALF-COUPLING MOUNTED BY: 

48 PUMP MFR. DRIVER MFR. PURCHASER 

49 COUPLING BALANCED TO ISO 1940-1 G.6.3 (6.2.3) REMARKS: Vendor to recommend instrumentation required for safe and 

50 COUPLING PER ISO 14691 (6.2.4) trouble free operation of the pumps in their bid. 

51 COUPLING PER ISO 10441 (6.2.4) 

52 COUPLING PER API 671 (6.2.4) MASSES (kg) 

53 NON SPARK COUPLING GUARD (6.2.14c) PUMP 

54 COUPLING GUARD STANDARD PER (6.2.14a) DRIVER 

55 MECHANICAL SEAL: REQUIRED (Remark- 3) GEAR 

56 SEE ATTACHED ISO 21049/API 682 DATA SHEET SOLE PLATE / MOUNTING FLANGE 

57 COUPLING 

58 MOTOR STOOL 

59 TOTAL 

60 

61 

62 

63 

64 

65 

66 



Bhatinda 







Tag No. : P-20-01 & P-20-02 

Client: 


Service: Sump Pumps for Transfer of Drain Oil (Hydrocarbon) Plant Location: Bhatinda 




No. of Units: 





1 SPARE PARTS (TABLE 18) VERTICAL PUMPS (CONT.) 

2 START-UP NORMAL MAINTENANCE Supply start-up spares PUMP AND STRUCTURE DYNAMIC ANALYSIS (8.3.5) 

3 SPECIFY Two years of operation spares parts DRAIN PIPED TO SURFACE (8.3.13.5) 

4 

5 OTHER PURCHASER REQUIREMENTS QA INSPECTION AND TESTING 

6 COORDINATION MEETING REQUIRED (9.1.3) SHOP INSPECTION (7.1.4) PERF. CURVE APPROVAL 

7 MAXIMUM DISCHARGE PRESSURE TO INCLUDE (5.3.2) TEST WITH SUBSTITUTE SEAL (7.3.3.2b) 

8 MAX RELATIVE DENSITY TEST NON-WIT WIT OBSERVE 

9 MAX DIA. IMPELLERS AND/OR NO OF STAGES HYDROSTATIC TEST OF BOWLS 

10 OPERATION TO TRIP SPEED AND COLUMN (8.3.13.2) 

11 CONNECTION DESIGN APPROVAL (5.12.3.4) HYDROSTATIC (7.3.2) 

12 TORSIONAL ANALYSIS REQUIRED (5.9.2.1) PERFORMANCE (7.3.3) 

13 TORSIONAL ANALYSIS REPORT (5.9.2.6) RETEST ON SEAL LKGE (7.3.3.2d) 

14 PROGRESS REPORTS (9.3.3) NPSH (7.3.4.2) 

15 OUTLINE OF PROCEDURES FOR OPTIONAL TESTS (9.2.5) COMPLETE UNIT TEST (7.3.4.3) 

16 ADDITIONAL DATA REQUIRING 20 YEARS RETENTION (7.2.2.1f) SOUND LEVEL TEST (7.3.4.4) 

17 MANIFOLD PIPING TO SINGLE CONNECTION (6.5.1.6) CLEANLINESS PRIOR TO 

18 DRAIN VENT COOLING WATER FINAL ASSEMBLY (7.2.2.2) 

19 MOUNT SEAL RESERVOIR OFF BASEPLATE (6.5.1.4) NOZZLE LOAD TEST (6.3.6) 

20 FLANGES REQD IN PLACE OF SOCKET WELD UNIONS (6.5.2.8) 4 h MECH RUN TEST(7.3.4.7.2) 

21 CONNECTION BOLTING PTFE COATING SS MECHANICAL RUN UNTIL OIL 

22 PAINTED ASTM A153 GALVANISED TEMP. STABLE (7.3.4.7.1) 

23 INSTALLATION LIST IN PROPOSAL (9.2.3L) 4 h MECHANICAL RUN AFTER 

24 VERTICAL PUMPS 

OIL TEMP. STABLE (7.3.4.7.3) 

25 PUMP THRUST: (+) UP (-) DOWN TRUE PEAK VELOCITY 

26 AT MIN. FLOW (N) (N) DATA (7.3.3.4d) 

27 AT RATED FLOW (N) (N) RESONANCE TEST (8.3.9.2) 

28 MAX. THRUST (N) (N) AUXILIARY EQUIPMENT TEST 

29 SOLEPLATE REQ'D (8.3.8.3.3) (m) X (m) (7.3.4.5) 

30 SEPARATE MOUNTING PLATE REQUIRED (8.3.8.3.1) IMPACT TESTING (5.12.4.3) 

31 SOLEPLATE THICKNESS (mm) PER EN 13445 

32 COLUMN PIPE: FLANGED THREADED PER ASME VIII 

33 DIAMETER (mm) LENGTH (m) VENDOR KEEP REPAIR AND HT RECORDS (7.2.1.1c) (copy provided to Purchaser) 

34 GUIDE BUSHINGS VENDOR SUBMIT TEST PROCEDURES (7.3.1.2 / 9.2.5) 

35 NUMBER VENDOR SUBMIT TEST DATA WITHIN 24 HOURS (7.3.3.3e) 

36 LINE SHAFT BEARING SPACING (mm) INCLUDE PLOTTED VIBRATION SPECTRA (5.9.3.3) 

37 GUIDE BUSHINGS LUBE: RECORD FINAL ASSEMBLY RUNNING CLEARANCES 

38 WATER OIL COMPLETION OF INSPECTION CHECK LIST (7.1..6) 

39 GREASE PUMPAGE MATERAIL CERTIFICATION REQUIRED (5.12.1.8) 

40 LINESHAFT: OPEN ENCLOSED CASING IMPELLER SHAFT 

41 LINE SHAFT DIAMETER: (mm) OTHER Wetted parts 

42 TUBE DIAMETER: (mm) CASTING REPAIR PROCEDURE APPROVAL REQ'D (5.12.2.5) 

43 LINESHAFT COUPLING: INSPECTION REQUIRED FOR CONNECTION 

44 LINE SHAFT DIAMETER: SLEEVE & KEY THREADED WELDS (5.12.3.4) 

45 SUCTION CAN THCKNESS (mm) MAG. PARTICLE LIQUID PENETRANT 

46 LENGTH (m) RADIOGRAP[HIC ULTRASONIC 

47 DIAMETER (m) INSPECTION REQUIRED FOR CASTINGS (7.2.1.3) (5.12.1.5) 

48 SUCTION STRAINER TYPE SUITABLE FOR THE PUMP MAG. PARTICLE LIQUID PENETRANT 

49 FLOAT & ROD FLOAT SWITCH RADIOGRAP[HIC ULTRASONIC 

50 IMPELLER COLLETS ACCEPTABLE (5.6.3) HARDNESS TEST REQUIRED (7.2.2.3) 

51 HARDENED SLEEVES UNDER BEARINGS (8.3.10.5) ADDITIONAL SUBSURFACE EXAMINATION (7.2.1.3) 

52 FOR 

53 METHOD 

54 

Pit arrangment 

55 Key 3 2 1 

56 1 grade 

57 2 low liquid level 

58 3 centreline of discharge 

59 l 1 sump depth 

60 l 2 pump length 

61 l 2 

62 l 3 centreline discharge height 

63 l 4 height of grade above low liquid level 

64 l 5 datum elevation, first-stage impeller 

65 l 6 submergence required 

66 Ø d sump diameter 

67 

Ø d 

68 Refer to hydraulic institute standards for definitions 

69 l 1 m l 2 m 

70 Ø d m l 6 m 

71 l 4 m l 3 m VENDOR SHALL FILL-IN THE DIMENSIONS WITH THE TENDER 

72 l 5 m 

73 

l 1 

l 2 

l 5 

l 3 





l 4 

l 6 


Tag No. : P-20-01 & P-20-02 


Client: 


P & ID No. : 435-JH0902-20-PR-PID-2003 

Supplier: 



No. of Units: 




1 APPLICABLE TO: PROPOSALS PURCHASE AS BUILT 

2 FOR HPCL's GURU GOBIND SINGH REFINERY PRODUCT EVACUATION PROJECT UNIT Raman Mandi Pumping Station - Bathinda pipeline 

3 SITE RAMAN MANDI PUMPING STATION SERVICE Transfer of Drain Oil 

4 

5 NOTES: INFORMATION BELOW TO BE COMPLETED: BY PURCHASER BY MANUFACTURER BY MANUFACTURER OR PURCHASER 

6 

7 PRESSURE VESSEL DESIGN CODE REFERENCES. 

8 THESE REFERENCES MUST BE LISTED BY THE MANUFACTURER 

9 PRESSURE VESSEL DESIGN STANDARD USED TO DESIGN PRESSURE CASING(5.3.4) 

10 CASTING FACTORS USED IN DESIGN( 5.3.2)(TABLE 2) 

11 SOURCE OF MATERIAL PROPERTIES 

12 

13 WELDING AND REPAIRS (5.12.3.1) 

14 THESE REFERENCES MUST BE LISTED BY THE PURCHASER. (DEFAULT TO TABLE 10 IF NO PURCHASER PREFERENCE IS STATED) 

15 ALTERNATE WELDING CODES AND STANDARDS (5.12.3.1) 

16 Welding Requirement (Applicable Code or Standard) Purchaser defined Default per Table 10 

17 Welder/operator qualification 

18 Welding procedure qualification 

19 Non-pressure retaining structural welding such as baseplates or supports 

20 Magnetic particle or liquid penetrant examination of the plate edges 

21 Postweld heat treatment 

22 Postweld heat treatment of casing fabrication welds 

23 

24 MATERIAL INSPECTION (7.2.2.1)(7.2.1.3) 

25 THESE REFERENCES MUST BE LISTED BY THE PURCHASER (DEFAULT TO TABLE 13 IF NO PURCHASER PREFERENCE IS STATED) 

26 ALTERNATIVE MATERIAL INSPECTIONS AND ACCEPTANCE CRITERIA (SEE TABLE 13) Vendor shall indicate any alternative codes here 

27 Type of inspection Methods For fabrications Castings 

28 Radiography 

29 Ultrasonic inspection 

30 Magnetic particle inspection 

31 Liquid penetrant inspection 

32 

33 1. The Net Positive Suction Head Available (NPSHA) shall exceed the Net Positive Suction Head Required (NPSHR) by at least 2 m (6 ft) throughout the range from minimum 

34 continuous stable flow up to and including the rated capacity, and by 0.5 m (2 ft) at 120 % of rated flow. 

35 2. Contractor / Vendor to Consider Mechanical Seal (As per API 682) in his scope of supply, Appropriate Seal flushing plan shall be selected for the said service. 

36 3 Contractor / Vendor to note that there is no cooling water vailable in the plant. Hence any cooling requirement shall be met by air cooling 

37 4 Contractor/ Vendor shall consider instrumentation as may be necessary for the safe and trouble free operation of the pumps. Transmitters are preffered over switches 

38 as per Project instrumentation philosophy. 

39 

40 

41 

42 

43 

44 

45 

46 

47 

48 

49 

50 

51 

52 

53 

54 

55 

56 

57 

58 

59 

60 

61 

62 

63 

64 

65 

66 


REMARKS 


Bhatinda 






The drawing, design and details given on this format are the property of WorleyParsons Engineering Pvt. Ltd. They are merely loaned on the borrower’s express agreement 

that they will not be reproduced, copied, exhibited or used, except in the limited way permitted by a written consent given by the tender to the borrower for the intended use. 

Sr. 

No. 

1. Incoming 

Material 

(Castings) 

Stage Component Characteristics Method of check Quantum 

of check 

Casing 

Stuffing Box 

Impeller 

Bearing Housing 

Reference 

documents 

Surface Quality Visual 100% ASME Material 

specification 

Acceptance 

norms 

ASME Sec-VIII, 

Div 1, Appendix 7 

Record 

Inspection 

report 

Sub 

Vend 

or 

Vend 

or 

WP 

W W - 

- 


Material 

Do Dimensions Measurement 100% As per vendors 

approved 

drawing 

As per vendor 

approved 

drawings 

Inspection 

report 

W W - 


Material 

Do Chemical / 

Physical 

properties 

Review of 

manufacturers TC 

All heats 

As per relevant 

material 

specification 


material 

specification 

Manufacturers 

TC 

W R R 


Material 

All castings 

materials 

Heat treatment 

Review of HT 

charts 

All heats 


material 

specification 


material 

specification 

HT chart or 

TC 

W R R 


material (Bar 

stock) 

Shaft material 

Chemical 

properties / 

Physical 

properties 

Review of 

manufacturers TC / 

Lab check 

All heats 


material 

specification 


material 

specification 

Manufacturers 

TC or Lab 

report 

W R R 

ITP FOR SUMP PUMP 


435-JH0902-00-ME-ITP-0006 

Page 1 of 5 

Rev. 

C



Sr. 

No. 

6. Hard ware 

items 


of check 

Gaskets, 

Fasteners, Gland 

packings, valves 

Suitability Test 

certificates 

Visual review or 

Test reports or 

certificates 

7. Accessories Mechanical seal Leakage test Hydotest 

Air test 

Measurement of 

leakage 

8. Accessories Barrier/Buffer 

liquid reservoir 


liquid Coolers 

1. WPS / 

PQR/WPQ 

2. Leakage check 

3. Dimensional 

check 

4. Materials TC 

1. WPS /PQR/ 

WPQ 


3. Dimensional 

check 


1. Qualification 

2. Hydro test 

3. Measurement 

4. Review of TC 

1. Qualification. 

2. Hydrotest 

3. Measurement 


As per 

sampling 

plan 

Reference 

documents 

Approved 

drawings and 

datasheets & 

Relevant stds 

Acceptance 

norms 

Approved 

drawings and 

datasheets & 

Relevant stds 

Type test As per API 682 API 682 and seal 

manufacturers 

drawing 

100% As per approved 

drawings. ASME 

Section II / Sec- 

VIII, div-1 / IX 


drawings. ASMe 



As per approved 








Record 

Inspection 

report 

Manufacturers 

inspection / 

Test report 

As per 

Manufacturers 

test record & 

Inspection 

record 

As per 

Manufacturers 

test record & 

Inspection 

record 

Sub 

Vend 

or 

Vend 

or 

WP 

W R R 

W R R 

W W W/R 

W W W/R 

10. Accessories Coupling 1. Dimensions 

2. Dynamic 

balancing 

11. In Process Casing 

Impeller 

Stuffing Box 

Defects open to 

surface 

1. Measurement 100% 1. As Per 

approved 

drawings 

2. ISO 1940& 

API 610 

D.P examination 100% of 

Machined ASTM E 105 

surfaces 

1. As Per 

approved 

drawings 

2. ISO 1940& 

API 610 

ASME Sec VIII 

Div-1, Appendix - 

7 

Manufacturers 

inspection & 

test records 

Manufacturers 

inspection & 

test records 

W W R 

- W R 

12. In process Butt Weld joint (if Weld defects Radiography On Nozzle ASME Sec V ASME Sec VIII Manufacturers - W R 



435-JH0902-00-ME-ITP-0006 

Page 2 of 5 

Rev. 

C



Sr. 

No. 


of check 

Reference 

documents 

Acceptance 

norms 

applicable) 

to casing 

joint 

Article 2 Div -1 UW 51 inspection & 

test records 

14. In Process Shaft Internal Defects Ultrasonic Test 100% 1. ASTM A 

388/ 

Written 

approved 

procedure 

Approved 

procedures 

Manufacturers 

inspection & 

test records 

15. WPS,PQR,W Wear rings Thickness of Visual Hardness 100% Specifications, Specifications, Manufacturers 

PQ previous 

overlay, Hardness Measurement 

WPS,PQR,WPQ WPS,PQR,WPQ WPS,PQR,W 

qualifications 

PQ Records 

for overlay 

16. Test before 

assembly 

Rotor Assembly 

with coupling Half 

Dynamic 

balancing 

17. Testing Assembled Pump 1. Performance 

2. NPSHR 

3. Vibration 

4. Sound 

5. Bearing 

temperature 

rise 

6. Mech. 

Running 

Record 

Measurement Each rotor ISO 1940 ISO 1940 GR.2.5 Manufacturers 

inspection & 

test records 

Measurement 

18. Testing Dismantled pump Strip examination Visual check 

Wear Ring 

Clearance 

measurement 

19. Testing Unitised Pump, 

Job Motor, Jack 

Screws, Base 

String test 


sound, temperature 

rise, Vibrations 

Each 

pump 

Each 

pump 

Each set 

API 610 API 610 Manufacturers 

inspection & 

test records 


inspection & 

test records 

Approved GA & 

API 610 

Approved GA & 

API 610 

Manufacturers 

inspection & 

test records 

Sub 

Vend 

or 

Vend 

or 

WP 

- W W/R 

- W R 

- W O 

- W W 

- W W 

- W W 



435-JH0902-00-ME-ITP-0006 

Page 3 of 5 

Rev. 

C



Sr. 

No. 


of check 

Reference 

documents 

Acceptance 

norms 

plate, instruments 

20. Testing Auxiliary piping Leak tightness Hydro test Each set No leakage No Leakage Manufacturers 

inspection & 

test records 

21. Testing Base plate Dimensions Measurement Each plate Approved GA 

drgs. 

22. Testing Instruments Doc. Review Review Each test 

report 

Approved 

Datasheet 

Approved GA 

drgs. 

Approved 

Datasheet 

Record 

Manufacturers 

inspection & 

test records 

Manufacturers 

TC 

Sub 

Vend 

or 

Vend 

or 

- W W 

- W W 

W W/R R 

WP 



435-JH0902-00-ME-ITP-0006 

Page 4 of 5 

Rev. 

C



Legends: 

WPS- WELDING PROCEDURE SPECIFICATION 

PQR- PROCEDURE QUALIFICATION RECORD 

WPQ- WELDER PERFORMANCE QUALIFICATION 

W- WITNESS 

O- OBSERVED 

R- REVIEW 

H- HOLD 

NOTES: 

1. WELD REPAIR IF ANY TO BE DONE AFTER THE APPROVAL OF THE PURCHASER / AUTHORISED REPRESENTATIVE OF PURCHASER AS PER APPLICABLE CODE AND 

QUALIFIED WPS AND WELDER. 

2. MATERIAL FOR LOW TERMPERATURE SERVICE TO BE IMPACT TESTED AS PER APPLICABLE SPECIFICATION 

3. FOR AUSTENITIC STAINLESS STEEL MICRO STRUCTURE AND IGC TESTS TO BE CONDUCTED AS PER APPLICABLE CODE & PURCHASE REQUISITION 

4. HARDFACING OF WEARRINGS SHALL BE AS PER APPROVED CROSS SECTIONAL DRAWINGS / DATASHEET. 

5. MECHANICAL RUN TEST SHALL BE AS DESCRIBED IN THE SPECIFICATION FOR SUMP PUMPS 

6. PUMP DRIVER SHALL BE INSPECTED AT DRIVER MANUFACTURERS SHOP AS PER RELEVANT INSPECTION & TEST PLAN 

7. PERFORMANCE TOLERANCES SHALL BE AS PER API 610 10 TH EDITION & SPECIFICATION FOR SUMP PUMPS. 



435-JH0902-00-ME-ITP-0006 

Page 5 of 5 

Rev. 

C

The drawing, design and details given on this format are the property of WorleyParsons Engineering Pvt. Ltd. They are merely loaned on the 

borrower’s express agreement that they will not be reproduced, copied, exhibited or used, except in the limited way permitted by a written 

consent given by the tender to the borrower for the intended use. 

ITEM : VERTICAL CENTRIFUGAL PUMPS 

ITEM NUMBER : 

VENDOR : 

INSTRUCTIONS TO VENDORS : 

EXPERIENCE RECORD – CENTRIFUGAL PUMP (VERTICAL) 

1. This proforma duly filled in shall be submitted for each item separately, alongwith the bid. 

2. Since the information requested in this proforma will be utilized to assess provenness of offered model, it is in the interest of the 

equipment manufacturer to pick up those cases out of total list of references which most closely match with the offered mode. The 

equipment manufacturer shall also ensure that each & every information asked for is furnished and the same is correct and 

complete in all respects. 

Incorrect information furnished in this proforma shall render the bid liable for rejection. 

3. While furnishing the materials, where asked for, the equipment manufacturer shall furnish ASTM equivalents also. 

4. For the referred installations, the equipment manufacturer shall indicate the name of the person (alongwith his address, telephone 

no., fax no. / email-id etc.) who may be contacted by the Purchaser/ his representative, if felt necessary. 

5. The equipment manufacturer shall also furnish along with the bid his standard reference list for the offered equipment model 

manufactured and supplied by him. 

6. The equipment manufacturer shall clarify the meaning of each letter/ digit used in the model designation below : 

Description of Model designation system : 

EXPERIENCE RECORD PROFORMA 

CENTRIFUGAL (VERTICAL SUBMERSIBLE 

PUMPS) 

EXPERIENCE RECORD 

PROFORMA NO. 

435-JH0902-10-ME-LST-0014 

Page 1 of 6 

Rev 

C




SL. 

NO. 

PARAMETER 

INFORMATION ON 

PROPOSED 

MODEL 

INFORMATION ON REFERRED EXISTING 

INSTALLATIONS 

Ref – 1 Ref – 2 Ref – 3 

REMARKS 

1 2 3 4 5 6 7 

1 GENERAL 

1.1 

Cross reference to manufacturer’s Standard 

Reference list 

1.2 Make 

1.3 Model Number 

1.4 Number of units supplied 

1.5 

Type of driver 

(Electric Motor / VSDs) 

1.6 Driver rated kW / Speed (rpm) 

1.7 

1.8 

1.9 

Edition of API Std – 610 to which the pump 

conforms (10th) 

Drive 

(Fixed Speed / Variable Frequency) 

Shop where pump is designed, manufactured, 

packaged, tested & supplied with address 



PUMPS) 


PROFORMA NO. 

435-JH0902-10-ME-LST-0014 

Page 2 of 6 

Rev 

C




SL. 

NO. 

PARAMETER 


PROPOSED 

MODEL 


INSTALLATIONS 

Ref – 1 Ref – 2 Ref – 3 

REMARKS 

2 OPERATING CONDITIONS 

2.1 Fluid handled 

2.2 Fluid temperature (Min / Max) °C 

2.3 Capacity (m 3 /hr) 

2.4 Maximum Suction pressure (kg/cm 2 ,a) 

2.5 Differential Head, Rated (m) 

2.6 Differential Pressure, Rated (kg/c m 2 ) 

2.7 Minimum Submergence Required (mm) 

2.8 

Setting depth (mm) 

(distance between bottom face of the 

mounting flange and first stage impeller 

suction eye) 

2.9 Efficiency 

2.10 BKW, Rated 

2.11 Minimum Continuous Stable Flow, (m 3 /hr) 



PUMPS) 


PROFORMA NO. 

435-JH0902-10-ME-LST-0014 

Page 3 of 6 

Rev 

C




SL. 

NO. 

PARAMETER 


PROPOSED 

MODEL 


INSTALLATIONS 

Ref – 1 Ref – 2 Ref – 3 

REMARKS 

2.12 Rated Speed 

2.13 

MAWP casing (kg/c m 2 G) 

@15°C 

@ pumping temperature 

3 CONSTRUCTION 

3.1 

Type of Pump Discharge (WITH Separate 

Discharge) : VS4 

3.2 Type of line shaft (open / close) 

3.3 

Line shaft lubrication (pumping medium / 

separate lubricant) 

3.4 Startup prelubrication required (yes / no) 

3.5 No. of stages 

3.6 

Impeller diameter – rated/ Maximum/ Minimum 

(mm) 



PUMPS) 


PROFORMA NO. 

435-JH0902-10-ME-LST-0014 

Page 4 of 6 

Rev 

C




SL. 

NO. 

PARAMETER 


PROPOSED 

MODEL 


INSTALLATIONS 

Ref – 1 Ref – 2 Ref – 3 

REMARKS 

3.7 

Whether the proposed model and reference 

models have identical hydraulic design (for 

impeller / diffuser / volute) 

3.8 Sealing Element ( mechanical seal) 

3.9 Type of mechanical seal (Single / Double) 

3.10 API Sealing Plan No. 

3.11 API Cooling Plan 

4 MATERIAL OF CONSTRUCTION 

4.1 API – 610 Material Code 

4.2 Casing 

4.3 Impellers 

4.4 Line Shaft 

4.5 Column 

4.6 Line Shaft bearing 



PUMPS) 


PROFORMA NO. 

435-JH0902-10-ME-LST-0014 

Page 5 of 6 

Rev 

C




SL. 

NO. 

PARAMETER 


PROPOSED 

MODEL 


INSTALLATIONS 

Ref – 1 Ref – 2 Ref – 3 

REMARKS 

5 

OTHER INFORMATION ON 

INSTALLATIONS 

5.1 Date of supply of entire unit 

5.2 Date of commissioning of entire unit 

5.3 

No. of operating hours completed as on the 

date of issue of material requisition 

5.4 Major problems encountered 

5.5 Purchaser’s Name and Address 

Name (Company / Organization ) 

Name of Contract Person 

Address 

Telephone No. 

Fax No. 

Email-id 



PUMPS) 


PROFORMA NO. 

435-JH0902-10-ME-LST-0014 

Page 6 of 6 

Rev 

C




ITEM : 

ITEM NUMBER : 

VENDOR : 

INSTRUCTIONS TO VENDORS : 

EXPERIENCE RECORD – MOTOR / VSDs 

1. This proforma duly filled in shall be submitted for each item separately, alongwith the bid. 

2. Since the information requested in this proforma will be utilized to assess provenness of offered model, it is in the interest of the 

equipment manufacturer to pick up those cases out of total list of references which most closely match with the offered mode. The 

equipment manufacturer shall also ensure that each & every information asked for is furnished and the same is correct and 

complete in all respects. 

Incorrect information furnished in this proforma shall render the bid liable for rejection. 

3. While furnishing the materials, where asked for, the equipment manufacturer shall furnish ASTM equivalents also. 

4. For the referred installations, the equipment manufacturer shall indicate the name of the person (alongwith his address, telephone 

no., fax no. / email-id etc.) who may be contacted by the Purchaser/ his representative, if felt necessary. 

5. The equipment manufacturer shall also furnish along with the bid his standard reference list for the offered equipment model 

manufactured and supplied by him. 

6. For pumps with VSD drives, Vendors are cautioned to cite only those pump references where VSDs have been used. 

7. The equipment manufacturer shall clarify the meaning of each letter/ digit used in the model designation below : 

Description of Model designation system : 


MOTORS/VSD’S 


PROFORMA NO. 

435-JH0902-10-ME-LST-007 

Page 1 of 6 

Rev 

C




SL. 

NO. 

PARAMETER 


PROPOSED 

MODEL 


INSTALLATIONS 

Ref – 1 Ref – 2 Ref – 3 

REMARKS 

1 2 3 4 5 6 7 

For Electric Motors 

1 

1.1 

GENERAL (For design, manufacture, 

testing and supply of motor) 



1.2 Make 


1.4 

Enclosure Type (Whether Type-n/ Type Ex(e)/ 

Type Ex(d)) 

1.5 Rated Kw of motors / No. of poles 

1.6 Rated voltage of motor 

1.7 Whether Fixed speed/ Variable speed drive 

1.8 Speed variation range (through VSDs) 

1.9 Model/ Type of driving/ non drive end bearings 




PROFORMA NO. 

435-JH0902-10-ME-LST-007 

Page 2 of 6 

Rev 

C




SL. 

NO. 

PARAMETER 


PROPOSED 

MODEL 


INSTALLATIONS 

Ref – 1 Ref – 2 Ref – 3 

REMARKS 

1.10 

Shop where motor is designed, manufactured, 

packaged, tested & supplied with address 

2 


INSTALLATIONS 

2.1 Date of supply 

2.2 Date of commissioning 

2.3 







Address 

Telephone No. 

Fax No. 




PROFORMA NO. 

435-JH0902-10-ME-LST-007 

Page 3 of 6 

Rev 

C




SL. 

NO. 

PARAMETER 


PROPOSED 

MODEL 


INSTALLATIONS 

Ref – 1 Ref – 2 Ref – 3 

REMARKS 

Email-id 




PROFORMA NO. 

435-JH0902-10-ME-LST-007 

Page 4 of 6 

Rev 

C




1 

1.1 

1.2 Make 

For Variable Speed Drive Panel 

GENERAL (For design, manufacture, 

testing and supply of Variable speed drive 

(VSD) panels) 




1.4 Power rating 

1.5 Voltage rating 

1.6 Speed variation range 

1.7 

1.8 

1.9 

2 

Shop where variable speed drive panel is 

designed, manufactured, packaged, tested & 

supplied with address 

Experience record for carrying out harmonic 

analysis (for both harmonic currents & 

voltages) and calculations of harmonics 

injected into the AC system 

Experience record for design, engineering and 

supply of requisite harmonic filters to reduce 

harmonics within limits recommended in IEC 


INSTALLATIONS 

2.1 Date of supply 




PROFORMA NO. 

435-JH0902-10-ME-LST-007 

Page 5 of 6 

Rev 

C




2.2 Date of commissioning 

2.3 







Address 

Telephone No. 

Fax No. 

Email-id 




PROFORMA NO. 

435-JH0902-10-ME-LST-007 

Page 6 of 6 

Rev 

C






SPECIFICATION FOR EOT CRANE 

435-JH0902-10-ME-SPC-008 

16-July-2009 





Phone: +91-22-67818000 

Fax : +91-22-67818080 



Page 1 of 31




SYNOPSIS 

Disclaimer 











PARSONS 

APPROVAL 

DATE 

CLIENT 

APPROVAL 

DATE 

A 


Subramanyam 

.S 

Sameer 

Ishwad 

Jeremy 

Wallace 

29-June-09 

N/A 

B 

Issued For Review 

Subramanyam 

.S 

Sameer 

Ishwad 

Jeremy 

Wallace 

06-July-09 

N/A 

C 

Issued For Tender 

Subramanyam 

.S 

Sameer 

Ishwad 

Jeremy 

Wallace 

16-July-09 

Page 2 of 31




CONTENTS 

1. INTRODUCTION ................................................................................................................4 

1.1 Scope of Work ....................................................................................................................4 

1.2 Extent of Supply..................................................................................................................6 

2.0 CODES & STANDARDS ....................................................................................................8 

2.2 Order of Precedence: .........................................................................................................9 

3.0 QUALITY ASSURANCE, INSPECTION & TESTING.......................................................17 

4.0 SURFACE PREPARATION AND FINISH ........................................................................19 

5.0 NAMEPLATE DETAILS ....................................................................................................20 

6.0 PACKAGING, PRESERVATION AND PREPARATION FOR SHIPMENT ......................20 

7.0 SPARE PARTS AND SPECIAL TOOLS ..........................................................................21 

7.1 Spares ..............................................................................................................................21 

7.2 Special Tools ....................................................................................................................21 

8.0 DOCUMENTATION ..........................................................................................................21 

8.1 Tender Documentation .....................................................................................................21 

8.2 Post Order Documentation ...............................................................................................22 

9.0 PERFORMANCE GUARANTEE ......................................................................................23 

Page 3 of 31






The document specifies minimum requirements for the supply of EOT Crane required for HPCL- 

GGSRPEP, Project. 

This specification along with the relevant Codes & standards describes the minimum requirements for 

design, manufacture, testing, supply, supervision of erection and commissioning for EOT Crane. It is 

not the intent to completely specify all details of design and construction; nevertheless, the equipment 

shall conform to high standards of engineering, design and workmanship in all respects. 

The Contractor/ Vendor shall make all possible efforts to comply strictly to the requirements of this 

Specifications and other relevant Codes & Standards. In case, any deviations are considered 

essential by the Contactor/ Vendor after making all possible efforts, these shall be separately listed in 

the Contractor’s /Vendor’s offer under ‘LIST OF DEVIATIONS/ EXCEPTIONS TO THE TENDER 

Docs. for the purchaser’s considerations. In the event, of any deviation not listed under the ‘List of 

deviations / exceptions to the tender’, even though it is appearing in other part of the offer, shall not 

be considered applicable. Deviations accepted by the purchaser are the only exceptions acceptable. 

Hence all the requirements shall be binding on the Contractor /Vendor without any cost and schedule 

implications to the purchaser. 

The Contractor / Vendor shall be responsible for the co-ordination of all Sub-Suppliers and for the 

overall guarantee of furnished equipment. It is the specific responsibility of the Supplier to invoke all 

applicable referenced specifications to each Sub-Supplier Purchase Order. 

The offered equipment shall be sourced from a regular and established manufacturer having requisite 

design, manufacturing and testing facilities. The offered model shall be from the regular 

manufacturing range of the supplier and the design shall have had a minimum of two years 

successful field operation with the same model having the same design and materials of construction. 

Relevant information of the offered equipment like catalogues; references, user’s certificates etc. shall 

be furnished along with the offer. 

Page 4 of 31




The type of handling facilities provided for various buildings/areas are listed in table below 

Sr.No. Building / Area Type of Handling Facilities Number of 

Crane 

1 RamanMandi Mainline Pump 

House 

2 RamanMandi Booster Pump 

House 

EOT Crane (Double Girder) 1 

EOT Crane (Double Girder) 1 

For EOT cranes: 

• Load capacity (SWL) in Ton : 20 tonnes (Mainline Pumps) / 10 tonnes (Booster Pumps 

• Span in m.: 16 m (Mainline Pumps) / 12 m (Booster Pumps) 

• Lifting height in m. : (6.5m from FFL for Mainline Pumps) / (6m above the ground for Booster 

pumps) 

Description: 

• Lifting height: Distance between hook in upper position and lower position. 

• Load capacity (SWL): Safe working load; required maximum capacity of crane and hoist. 

The equipment shall be complete including all ancillary items required to meet the design and 

environmental conditions as stated herein. Any additional part, equipment, material, etc., 

which are not specifically mentioned in this specification, but are required to make the 

supplied equipment/item complete in all respect in accordance with the intent of this 

specification, statutory requirements, applicable codes/standards, good engineering 

practices, and for safe and trouble-free operation, shall be deemed to be covered under the 

scope of this specification. 

If national and/or local regulations exist in which some of the requirements may be more stringent 

than in this specification, the Contractor /Vendor shall determine by careful scrutiny which of the 

requirements are the more stringent and which combination of requirements will be acceptable as 

regards safety, environmental, economic and legal aspects, in all cases the Contractor /Vendor shall 

inform the Purchaser of any deviation from the requirements of this specification which is considered 

to be necessary in order to comply with national and/or local regulations. The Purchaser may then 

decide to negotiate with the authorities concerned with the object of obtaining agreement to follow this 

specification as closely as possible. 

Page 5 of 31




1.2 Extent of Supply 

The Contractor /Vendor shall furnish all components and ancillary equipment necessary to make the 



A) EOT Cranes 

Sheet metal casing to protect accessible mechanical parts 

Crane and hoist control (joystick type radio remote control pendant type ) 

Crane long travel rail, rail sections will be fixed by welding to runway beams 

Resilient bumpers and rubber buffer where necessary 

Inhibition of starting in high speed 

Inhibition in reverse at high speed (by additional timers) 

Chain guides and rope guides 

Hook with safety latch 

End stops 

Anti-derailment devices 

Lubricators 

Lube oil and grease supply for the first filling 

Fitting and bolts 

Flameproof (Exd) Electrical motors and instrumentation necessary for operation 

Hoist & Crane Controls 

Any other necessary parts/ items required for crane operation 

B) General 

Metal surface coating and painting in accordance with Project Specification: 0435-JH0902-00-PE- 

SPC-003 

Special tools for maintenance/ erection and installation (as applicable) 

Start-up and commissioning spare parts 

Name plate 

Page 6 of 31




Supervision of Erection & Commissioning (including supervision of full performance tests) at site. 

Inspection and Testing, including load tests at shop along with testing required for Controls & 

Electrical equipment. 

Packing for transportation to Job sites 

Necessary certification 

Documentation for approval. 

Page 7 of 31




2.0 CODES & STANDARDS 

2.1 The Following codes & Standards shall be followed : 

Standard No. 

IS : 807 

IS : 816 

IS:1030 

IS:1181 


Code of Practice for Design, Manufacturing, Erection and testing 

(Structural Portion) of cranes & hoists. 

Code of Practice for use of Metal Arc Welding for General Construction 

in Mild Steel. 

Specification for Carbon Steel Castings for General Engineering 

Purposes. 

Qualifying tests for Metal Arc Welders (Engaged in welding structures 

other than pipes 

IS: 1570 

Schedules for Wrought Steels (Part II- Carbon steel 

IS : 1823 

IS : 2048 

Code of Practise for Oxy-acetylene welding for structural work in Mild 

Steel 

Parallel Keys & Key ways 

IS:2062 

IS: 2266 

IS:3177 

Steel for general purposes 

Steel wire ropes for general engineering purposes 

Code of Practice for Electric Overhead travelling cranes and Gantry 

Cranes other than steel works Cranes 

IS:3443 

IS:3681 

IS:3815 

IS: 4460 

IS: 5749 

Specification for Crane Rail Sections 

General Plan for Spur & Helical Gears 

Point Hook with shanks for General Engineering Purpose 

Method of Rating of Machine Cut Spur & Helical Gears 

Forged Ramshorn hooks 

Page 8 of 31




Standard No. 

IS:8610 

IS 5572 

IEC 60034 

ISO 9001 

EN 10204 / ISO 10474 


Point Hooks with Shank Capacity upto 25 tonnes Trapezoidal section 

Classification of Hazardous areas having Flammable gases and 

Vapours for Electrical installation. 


Quality Management Systems – Requirements (2001 Ed.) 

Type of Inspection Documents (2004Ed.) 

Other International standards may be acceptable subject to their being equivalent or superior with 

prior approval of purchaser. 

All codes & Standards mentioned above and all other relevant codes and standards shall be of latest 

issue only. 

For Provisions not covered by the above codes & Standards, applicable engineering practices and 

norms shall govern. 

2.2 Order of Precedence: 

The precedence for application of Project Documents, Codes, Standards, Design Engineering 

Practices and regulatory requirements shall be as follows: 

• Data Sheets (attached as an Annexure to this specification) 





• Referenced Codes and Standards 

Page 9 of 31




2.3 Design Requirements 

2.3.1 General 

• The equipment shall meet the type, duty class, required load lifts and load lift height, long/cross 

travel requirements as specified in the specifications and/or drawing. 

• Each component shall be located in such a manner as to be easy to operate and maintain. 

• The Contractor /Vendor shall be fully responsible for the supply, selection and quality of all 

materials inclusive of all consumables, welding, testing, protection devices, machinery, tools, 

labour and all other necessary materials and services required to complete the supply of 

equipment whether or not they are specified in this Specification and datasheet 

• The Contractor /Vendor shall be fully responsible for the coordination with all his Sub 

Contractor /Vendors for materials and services provided by them. However, Contractor 

/Vendor shall be solely responsible to Purchaser for compliance with the specified 

requirements. Contractor /Vendor shall submit a list and experience summary of all his Sub 

Contractor /Vendors. 

• Should the Contractor /Vendor come across any discrepancy, deficiency, or lack of clarity in 

any part of this specification or attached documents, he shall notify the same to the Purchaser, 

along with his offer, with proposed alternative or additional item and prices for each category 

thus included. Any items so identified after Purchase Order award will not constitute a change 

and will not be the cause for cost or schedule alteration. 

• All equipment within the package shall be suitable for installation for outdoor, undershed. 

• Equipment Data Sheet shall be provided by Contractor / Vendor and should be submitted along 

with the bid. 

2.4 Design Life, Availability and Reliability 


Contractor /Vendor. Unless otherwise stated, the package design life shall be 35 years, with an 


The Contractor /Vendor shall identify any aspects of its standard components or packages that do not 

meet the requirement of this specification, the same shall be listed in a separate section under 

Exceptions & Deviations to tender specifications.” Exceptions & Deviations listed elsewhere shall not 

be considered and deemed to be accepted by the vendor. 

Page 10 of 31




2.5 Hazardous Area Classification 

The hazardous area rating of the equipment shall be specified in the datasheet (Annexure-1 of 

this specification). 

Building / Area 

RamanMandi Mainline Pump House 

RamanMandi Booster Pump House 

Hazardous Area Classified 

Ex’d’, Class 1, Zone 2, IIB, T3 

Ex’d’, Class 1, Zone 2, IIB, T3 


All load carrying structural girders and main hook shall have material certification in compliance with 

BS EN 10204 type 3.1 and include original mill certificates or certified copies. Components shall be 

fully traceable back to the certificate. 

Page 11 of 31




2.7 TECHNICAL REQUIREMENTS 

2.7.1 Mechanical Requirement 

2.7.1.1 EOT Crane 

General 

Overhead travelling bridge cranes shall be designed, manufactured, inspected, and tested 

in accordance with this specification, applicable data sheets, and relevant codes & 

Standards. 

All parts of the individual crane installation shall be designed to be suitable for installation in 

outdoor undershed environment as specified on the data sheet. Crane component material 

selection and coating for components shall be suitable for site condition, as per the Site & 

Utility data. 

The long travel rails for all overhead travelling bridge cranes shall be provided by Contractor 

/Vendor. These will be welded on the girder. The runway structure (Crane Girder) on which 

the long travel rail rest will be part of the building steel works package and will be provided 

by Purchaser. 

Installation and alignment of long travelling rails will be carried out by the Composite works 

contractor under the supervision of the Crane Contractor /Vendor. 

All EOT cranes shall be top running double-girder cranes as specified in data sheets with 

the crane crab / trolley running on the top of the crane girders. 

The design of the crane structure shall be such that no welding is required in the field. 

The type of the drives and controls of cranes and hoists shall be as per this specifications 

and relevant IS codes. 

All lifting equipment shall be clearly stamped and labelled for the Safe Working Load (SWL) 

in tonnes. 

The crane design and construction shall meet tolerances as per IS codes; particularly for: 

• Crane rail joints, wheel running and guidance surfaces 

• Tolerance on span 

• Crane rail straightness 

Page 12 of 31




• Misalignment of crane running surface in vertical plane 

Crane Bridges 

The crane bridges shall consist of two fabricated box girders and two fabricated box section 

type end carriages. Each girder end shall have end carriage bolted to it. 

All girders shall be designed to resist both vertical and horizontal stresses. 

The maximum deflection of crane girder at test load shall not exceed 1 / 600 of span. 

The cranes shall be fitted with facilities for safe and easy access for inspection and 

maintenance. Double girder cranes shall have a full-length walkway along one girder so that 

all parts are easily accessible. Access to the crane will be through a walkway that forms part 

of the building or directly by a caged ladder and provided by the Contractor. Access to the 

crane platform will be through a ladder secured with a gate (positive security). 

End Carriages 

The overhead bridge cranes shall consist of two independent drive units and four long travel 

wheels, two of which will be driven. The wheels shall be double flanged with crane rated 

hardness suitable for specified maximum wheel loading. The travel wheels shall be fitted 

with lifetime lubricated anti-friction bearings. 

The end carriages shall be of the welded box section design fabricated from structural steel 

and shall be equipped with rigidly mounted high impact resistant bumpers. The construction 

of end carriages shall be stable enough to keep the end carriages in alignment to the 

runway. 

End carriages shall be mounted to the crane girders by high-tensile bolts. 

Each end carriage of electrically driven crane shall have one driven travel wheel, so that the 

crane is travelling on four wheels with a drive on both crane runways. Each driven wheel 

shall be provided with independent electric motor driver. The crane drives shall be lowmaintenance 

units with gear motor directly driving the travel wheels. The motors shall be 

equipped with integrated sliding rotor brakes. Limit switches with all necessary strikers shall 

be provided to allow the crane to travel up to the bumper and stop from 80% speed after 

reducing from nominal speed without permanently deforming the end carriage or bridge 

structures. 

The crane long travelling brakes shall be to Contractor /Vendor standards (electromechanical 

disc type fail-safe circuit brakes are recommended). Brake linings shall be self- 

Page 13 of 31




cleaning for long life and reliable operation. Brake coils shall be epoxy impregnated and 

bonded to a cast iron body for long life in the roughest environment. 

The cranes shall be fitted with a proper safety device to prevent de-railment in the case of 

wheel breakage. 

The following safety features shall be provided for the cranes: 

• Dead man switch 

• Fail safe 

• Trolley stop 

• Rail sweep 

• Bridge bumpers 

• Travel limit switch 

Trolleys and Hoists 

The trolley of double girder cranes shall be designed as top running electric driven fourwheel 

crab. 

The crab assemblies shall be of rigid steel construction. 

Travel wheel assembly shall be capable of being removed as a complete assembly with 

wheel, axle, bearings and bearing cartridges without disassembly. 

Buffers shall be provided at the faces of the crabs. 

The trolley brakes should be of electro-mechanical disc type based on the fail-safe circuit 

principle. Brake linings shall be self-cleaning for long life and reliable operation. Brake coils 

shall be epoxy impregnated and bonded to a cast iron body for long life in the roughest 

environment. 

The hoist of the electrical cranes shall be electric rope hoist type with sliding rotor selfbraking 

motor, which safely holds the load even in case of power failure. Limit switches shall 

be provided to prevent load hook over travel in lifting and lowering directions. The hoist 

make shall be selected from Purchaser’s approved Contractor /Vendor list. 

Contractor /Vendor shall incorporate a feature to lower the load in case of power failure. 

Page 14 of 31




The hoist brakes shall be magnetic drum brakes, spring set, electrically released, drum type 

friction brakes with adequate torque to stop and hold over 125% of the hoist design load. 

Additional independent mechanical load brake shall be provided on the hoist drum. 

Electrically driven hoists and crabs shall be equipped with squirrel cage motors. An inching 

control shall be provided on electrically driven hoists and trolleys. 

To prevent over hoisting of the crane, the hook-lifting unit shall be fitted with an over 

hoisting-protecting device. 

Cranes shall be provided with Ramshorn type hook and shall be provided with ball thrust 

bearings for free swiveling. Suitable material shall be offered. 

Crane and Hoist Control 

Electrical overhead cranes, electrical hoists shall be controlled from the operating floor level 

by joystick type radio remote control pendant push button station. When operator cabin is 

not specified in data sheet then crane shall be controlled from ground / operating floor level 

by means of suspended pendant type push button control box. 

The pendant control box shall be fitted with rocker-type or push-button switches for the 

crane functions, with a key-operated switch and a mushroom master switch which, when 

struck by hand, disconnects the entire power supply to the equipment. All control buttons 

shall be recessed to prevent accidental activation. 

The pendant control shall be made of "non breakable" (high impact) antistatic plastic with a 

galvanised wire rope suspension system to eliminate any strain to the control cable. The 

suspension system shall have provision for height adjustment. 

The crane pendant control panel shall be movable separately along the girder, independent 

of the actual crab or trolley position. All crane operations shall be executed only as long as 

the operator is pressing the relevant push button. 

The crane control shall be capable of performing any two of three crane motions 

simultaneously. 

The inching operation shall be provided for electrical overhead bridge cranes to allow 

movement of the hook, trolley or bridge in a series of short, discontinuous increments by 

momentary operation of an electrical controller. 

A precision speed control shall be provided for all crane and lifting gears. 

Page 15 of 31




Stepless speed controls for hoisting and travelling providing smooth starts, fast acceleration, 

easy positioning and soft stops shall be provided. All motions shall be smoothly controllable 

between zero and maximum speed. 

Brakes shall be progressively applied so as not to induce shock to the crane system and 

shall be fail-safe in operation. Safe load indication shall be provided. 

All controls and associated equipment shall be clearly marked with legible and durable signs 

and etched to show the functions. 

Electrical Equipment / Controls : 

Cranes in pump house shall be suitable for outdoor use under shelter. 

All electrical equipment shall comply with requirements as indicated in the “Specification for 

Low Voltage Induction Motors” Doc. No. 0435-JH-0902-00-EL-SPC-0002, Electric motors 

and other electrical items shall be of Purchasers approved make (as per approved 

Contractor /Vendor list) for standardization. 

Single point power supply shall be available as 415V, 50Hz, 3ph, 4 wires (one feeder). If 

any other power is required, Contractor /Vendor shall derive it from this feeder. The 

Contractor’s scope limit will be up to cable termination to the main switch furnished by the 

crane Contractor /Vendor. 

Purchaser will provide Earthing at two points inside Mainline Pump house & Booster Pump 

house. Contractor / Vendor shall form an earthing grid for all his equipments and connect it 

to Purchaser’s earth grid at two points. 

The electrical terminal boxes, junction boxes, pendant control boxes, Electric Motors etc. 

shall be with Ingress Protection level of IP-65. and shall be Flameproof Ex’d’ type. 

The Control Panel provided by the Contractor / Vendor shall compose of necessary starters, 

push buttons and all associated auxiliaries including Flat cable festoon system , cable etc. 

All motors starters, control panel, bus bar system, flat cable festoon system and cables etc 

shall be supplied by the Vendor/ Contractor for Cranes. 

Contractor /Vendor shall provide the details of Power requirements. Considering max. 

Possible simultaneous operation of the crane. 

Page 16 of 31




3.0 QUALITY ASSURANCE, INSPECTION & TESTING 

Inspection, testing and certification of electric overhead traveling cranes shall be in 

accordance with the applied codes, and as further defined below. The inspection and test 

plan shall be submitted for Purchaser approval. The crane installation completeness 

certificate shall include verification of the tolerances meeting relevant IS codes. 

All load carrying structural girders and main hook shall be supplied with material certificates 

according to EN 10204 "Type 3.1". For other material "Type 2.1" certificate should be 

provided. 

Material selected for lifting hooks, hook blocks, hoist drums etc. shall be supplied with 

material certificates according to EN 10204 Type 2.2. 

All welds shall be subjected to 100% visual examination and according to the requirements 

of the applied codes and as per Manufacturer's approved Quality Control and Inspection 

Plan. 

Each crane shall be fully assembled in the factory and subjected to load tests with test loads 

125% of SWL (within the allowable deflection of girders) . A test-run covering all functions of 

the crane shall also be carried-out before shipment. 

The inspection and tests of equipment shall be in accordance with relevant quality 

procedure and International Standards. The Contractor /Vendor shall provide type test 

certificate and routine test results of all equipment. After final assembly and installation, the 

Contractor /Vendor shall undertake necessary inspection and tests to satisfy the 

requirements of quality procedure and international standards. The inspection and test plan 

shall be submitted to the Purchaser for approval. 

3.1 Test at Workshop 

All testing shall be carried out at the manufacturing facility. The workshop tests shall include 

visual examination, dimensional control, load testing with test load, checking of safety 

devices, checking/ verification of crane girder deflection (locating trolley in central position), 

performance test of hoists, electrical functional test and review of Contractor /Vendor data 

book including all Q/C Test Certificates. 

The testing shall be carried out in accordance with relevant IS codes & Standards and this 

specification 

Page 17 of 31




NDE: - To be per IS Codes. All load bearing fillet welds shall be checked at root runs and 

finished welds by 100% MP or DP. Lifting lug shall be designed for 150% of their design 

load and with 100% NDE 

3.2 Test at Site 

On completion of material handling equipment erection the following site tests / performance 

tests shall be performed as a minimum requirement: 

• Testing without load 

• Operation of drive machinery (electrically operated type) 

• Working range (clearances, lifting height, etc.) 

• Testing with test load, 125% of the SWL load 

• Operation testing; 

o 

Correct operation of switches, contactors, power collector, festoons, 

indicators, alarm and protection devices etc. 

• Brake testing: 

o 

Electrically operated type: during lowering the test load shall be stopped and 

shall be reliably held both on nominal operation of the control unit and on 

emergency stop device; 

• Test with SWL load (Test load will be arranged by Contractor) 

o 

o 

o 

o 

Operation of all gears/wheels; 

Testing of safety equipment; 

Functional operations and tests of all drive units at nominal speed (electrically 

operated type) and control devices; 

Inch positioning test where creep units are installed; 

• Inspection and tests of electrical items, as a minimum, shall include : 

o 

o 

Verification of completeness of the data on the labels and required degree of 

protection of enclosure (including degree of protection with regards to safety). 

Visual examination. 

Page 18 of 31




Marking of components and terminals and caution / danger / instruction 

plates, as applicable. 

Verification of proper mounting of components, 

Interchange ability of similar electrical equipment and components 

Correct wiring of main and auxiliary circuits, 

Suitability of clamping, earthing and terminating arrangement, 

Mechanical operation including correct operation of switches, contactors, 

power collectors, festoons etc. 

Correct operation of indications, alarms and protection, 

Insulation tests, 

Tests of each continuity 

Functional tests 

Performance tests for one lot of equipment shall be carried out. 

Note: Braking test report and other Test certificates shall be provided for performed tests. 

4.0 SURFACE PREPARATION AND FINISH 

All exposed steelwork and fabricated items and piping shall be prepared and painted in 

accordance with specification Painting and Coating 0435-JH0902-00-PE-SPC-003. Where 

operating conditions are not suitable for the specified system, Contractor /Vendor shall 

specify a suitable alternative. 

The colour of finish coat shall be Golden Yellow unless otherwise specified 

All Sub Contractor /Vendor supplied components such as instrumentation, junction boxes 

and like equipment shall be protected by the Sub Contractor /Vendors standard protective 

coating. Contractor /Vendor shall provide details of the Sub Contractor /Vendor’s protective 

coatings with his offer. 

Page 19 of 31




5.0 NAMEPLATE DETAILS 

All equipments shall be supplied with Tag plates. 

Each Crane shall have an easily visible SWL stamped and labelled on crane girder. 

All major crane items shall be identified by corrosion resistant tag plates. Stainless steel 316 

shall be used. A minimum of 6 mm text and numbering height shall be clearly engraved (not 

etched) and paint filled on tag plates. Tag plates shall be secured using stainless steel 

screws, stainless steel wire or stainless steel chain. 

Each assembly shall be fitted with a stainless steel nameplate providing, as a minimum, the 

following information: 

• Material handling equipment tag number 

• P.O. Number 

• Shop order number 

• Manufacturer's name 

• Manufacture serial number 

• Year of manufacture 

• Important design parameters crane classification with state of loading / class 

of utilization (of each mechanism). 

6.0 PACKAGING, PRESERVATION AND PREPARATION FOR 

SHIPMENT 

All packaging shall be done in such a manner as to reduce the volume. The Equipment shall 

be dismantled into major components suitable for shipment. All assemblies shall be properly 

match marked for site erection. 

Attachments, spare parts of the equipment and small items shall be packed separately in 

wooden boxes. Each item shall be appropriately tagged with identification of main 

equipment, item denomination and reference number of the respective assembly drawing. 

Page 20 of 31




Detailed Packing list in water proof envelope shall be inserted in the package together with 

equipment. 

Packaging shall be unless otherwise stated suitable for prolong storage at site to prevent 

undue corrosion and damage before erection and commissioning of the crane. 

7.0 SPARE PARTS AND SPECIAL TOOLS 

7.1 Spares 

Contractor /Vendor shall recommend & consider commissioning spares as may be required 

for the said package. 


The Contractor /Vendor shall supply one (1) set of tools required for the erection and/or 

maintenance of the package including all ancillary equipment. 

The Contractor /Vendor shall identify the special tools required with his offer. 

Special tools shall be itemised and list shall be furnished along with the bid.. 

8.0 DOCUMENTATION 

The Contractor /Vendor shall be responsible for providing all documentation / drawing as 

following. 

8.1 Tender Documentation 

Tender documentation shall include the following: 

• Contractor /Vendor Document List. 

Page 21 of 31




• Production Schedule. 

• Product Technical Literature. 

• Technical and Performance Data as requested within this Specification. 

• General Arrangement Drawing. 

• Preliminary Weight Data. 

• Schematics Wiring Diagram. 

• Paint Procedures. 

• Confirmation of material certification. 

• Electrical Power requirement. 

The Contractor /Vendor shall separately detail each proposed deviation from the 

specification or data sheets, and submit to the Purchaser for approval. 

8.2 Post Order Documentation 

Purchase order documentation shall include the following for approval as a minimum: 

• Contractor /Vendor Documentation List 

• Production Schedule 

• Inspection and Test Plan 

• Contractor /Vendor Datasheets including model numbers and materials 

• General Arrangement Drawing/ Assembly Drawing (crane weight and 

dimension) 

• Electrical Wiring Diagram 

• Material Certification 

• Test Procedures 

• Test Results 

• Installation, Operations and Maintenance Manual (per equipment type) 

Page 22 of 31




9.0 PERFORMANCE GUARANTEE 

The offered material handling equipment shall be guaranteed for satisfactory mechanical 

performance for the parameters and conditions stated in datasheets & this Specification. 

Page 23 of 31




ANNEXURE – 1 

Datasheets for EOT Cranes: 

EOT CRANES: 

Unless otherwise stated the following hoisting and travel speeds shall be 

Used: 

- Hoisting : 2 m/min 

- Cross travel : 10 m/min 

- Long travel : 20 m/min 

Page 24 of 31




1.0 PURCHASER’S REQUIREMENTS 

1.1 Location : RamanMandi Pumping Station 

1.2 Quantity : 1 per pump house 

1.3 Main/Aux. Hoist Capacity, Metric Tons : 10 tonnes(Booster Pumps) 20 tonnes 

(Mainline pumps) 

1.4 Span, m : 12 m (For Booster) & 16 m (Mainline 

Pumps) 

1.5 Type of crane (Single girder/ Double girder) : Double Girder 

1.6 Class of duty (as per IS 807 & 3177) : 

1.7 Height of lift (Main/ Aux. hoist), m : 

1.8 Operating speeds (loaded) : 

a) Main / Aux. hoist (MH) m/min. : 2m/min 

b) Bridge travel (LT), m/min. : 20m/min 

c) Trolley travel (CT), m/min. : 10m/min. 

d) Creep for Main Hoist, m/min. : 

1.9 Acceleration cm./sq.sec. : 

a) Cross travel : 

b) Long travel (main) : 

1.10 Bay length (m) : 70 m (Mainline Pumps) / 55 m(Booster 

Pumps) 

1.11 Location (Indoor / Outdoor) : Outdoor under shed 

1.12 Max bridge deflection : 

1.13 Type of control (cabin / pendant) : Pendant type 

1.14 Area classification : Zone 2, Gas Group IIA, IIB, Temp. cl. T3 

1.15 Type of power supply system : Single point, 3 phase AC power supply 

1.16 Electricity available : 415 V, 3 phase, 4 wire 50Hz, + 10% 

1.17 Gantry (Runway) rail size : 

Page 25 of 31




2.0 MANUFACTURER’S SPECIFICATIONS (Bidder to fill up completely for each crane 

separately & submit after order). 

2.1 Crane Performance Data 

2.1.1 Name of the Supplier : 

2.1.2 Class of Crane : 

2.1.3 Main Hoist Capacity, tonne : 

2.1.4 Auxiliary hoist capacity, tonne : 

2.1.5 Maximum Bridge travel speed, metre/min. : 

2.1.6. Maximum trolley travel speed, metre/min. : 

2.1.7. Maximum main hoist speed, metre/min. : 

2.1.8 Inching Speed (MH / LT) metre / min. : 

2.1.9 Maximum auxiliary hoist speed : 

2.1.10 Deflection with trolley positioned for : 

Maximum deflection : 

2.1.11 Maximum lift of main hook in meters : 

2.1.12 Maximum lift of auxiliary hook above : 

2.1.13 Highest position of main hook above : 

Operating floor level in meters : 

2.1.14 Nearest approach of main hook to runway : 

rails on each side, m 

2.1.15 Nearest approach of auxiliary hook to : 

runway rails on each side, m 

2.1.16 Span (m) : 

2.1.17 Class of Duty (as per IS : 807 & 3177) : 

2.1.18 Camber provided / amount mm : 

2.1.19 Factor of safety of ropes : 

2.2 Name of Manufacturers 

2.2.1 E.O.T. Crane Unit : 

2.2.2 Crane Motors : 

2.2.3 Control Equipment : 

2.2.4 Runway rail : 

2.2.5 Runway and cross conductors : 

2.2.6 Main hook : 

2.2.7 Auxiliary hook : 

2.3 Weight of Equipment (kg) : 

2.3.1 Bridge assembly (unladen) : 

2.3.2 Trolley assembly (unladen) : 

2.3.3 Hoisting assembly : 

2.3.4 Runway rail with accessories : 

2.3.5 Runway conductors with accessories : 

2.3.6 Total for equipment : 

2.3.7 Each end carriage : 

2.3.8 Max. wheel loads : 

a) With impact : 

b) Without impact : 

Page 26 of 31




2.4 Crane Design Data 

2.4.1 Crane Bridge 

i. Girder Particular 

a) Type of girder construction : 

b) Size : 

c) Number : 

d) Material : 

e) Weight, each girder, kg : 

ii. 

Platform 

a) Type of construction : 

b) Material : 

c) Width : 

d) Length : 

e) Location : 

f) Handrail : 

g) Mattress material : 

iii. Rails : trolley bridge 

a) Type and size : 

b) Length : 

c) Material : 

d) Buffer frame type : 

e) Fixing details : 

iv. Wheel axles : trolley bridge 

a) Type : 

b) Number : 

c) Material : 

d) Diameter : 

v. Bearings for wheel axles 

a) Type and make : 

b) Size : 

c) Number : 

d) Material : 

e) Lubrication : 

f) Type of dust sealing : 

vi. Wheels : trolley bridge 

i. Type : 

ii. Size : 

iii. Number per end carriage : 

iv. Hardness No. (BHN) : 

v. Material : 

vi. Diameter : 

vii. Wheel base : 

Page 27 of 31




vii. Buffers : trolley bridge 


b) Location : 

c) Material : 

d) Number : 

e) Type of stops to engage the buffers : 

viii. Rail Sweep : trolley bridge 


b) Location : 

c) Material : 

ix. End Truck 

a) Type : 

b) Size : 

c) Number : 

d) Material : 

e) Weight kg : 

f) Length : 

2.4.2 Operators Cabinet 

i. Cab. Particulars 


b) Size : 

c) Fan type, size and make : 

d) Illumination : 

ii. Operator’s Seat : 

a) Type of seat : 

b) Location : 

iii. Warning Gong : 


b) Location : 

iv. Ladder from cab to bridge : 

a) Fitting : 

v. Control Panel : 

a) Location 

b) Location of emergency switches : 

2.4.3 Pendant 

Type : 

Furnish list of Controls / buttons : 

2.4.4 Bridge Drive Machinery and Trolley Drive Machinery 

i. Type of Bridge Drive Unit : 

ii. Type of Trolley Drive Unit : 

Page 28 of 31




iii. Material 

a) Gear : 

b) Shafts : 

c) Other components : 

iv. Lubricant Particulars : 

v. Guards and Enclosures provided as necessary : 

vi. Bearings : 


b) Size : 

c) Other components : 

2.4.5 Hoisting Mechanism : Main Hoist 

i. Materials 

a) Gear : 

b) Shaft : 

c) Drums : 

d) Sheaves : 

ii. Winding Drum Type & Size (dia x length) : 

iii. Ratio of winding drums (diameter to wire rope) : 

iv. Bearing : 

a) Type : 

b) Diameter / No. of strands : 

c) Number of falls : 

d) Safe capacity tonnes / sq. cm : 

2.4.6 Particulars of Hook Block : Main Hoist 

a) Type of Hook 

b) Material of Hook : 

c) Type and size of bearing at hook support : 

d) Safety latches provided : 

2.4.7 Controls 

i. Hoisting : 

a) Type of control : 

b) Number of speeds : 

ii. Lowering : 

a) Type of control : 

b) Number of speeds : 

iii. Bridge Travel : 

iv. Trolley Travel : 

v. Creep speed : 

a) Arrangement during lowering : 

b) Arrangement during hoisting : 

2.4.8 Limit Switch : Long Travel Trolley travel 

i. Type / Make : 

ii. Construction : 

iii. Number : 

iv. Location : 

v. Voltage and current rating : 

vi. Hoist limit switch : 

a) Over hoist limit switch type / make : 

Page 29 of 31




b) Over hoist limit switch construction : 

c) Over hoist limit switch location : 

d) Under lowering limit switch type / make : 

e) Under lowering limit switch construction : 

f) Under lowering limit switch location : 

g) Back up limit switch type / make / construction : 

2.4.9 Illumination fitting on bridge 

i. Number : 

ii. Type : 

iii. Portable hand lamp with wiring : 

iv. Supply of transformers and other : 

accessories as necessary 

2.4.10 i) Runway Rail 

Type : Material : 

Size : Manufacturer : 

All fittings (including fish plates & bolts) and fixtures 

ii) Runway Rail End stops : 

Type : Number : 

Material : Construction : 

2.4.11 a) Motors : Bridge travel Trolley travel 

i. Number : 

ii. Type : 

iii. Manufacturer : 

iv. Voltage, phase, frequency : 

v. KW : 

vi. Temp. rise over 50°C ambient : 

vii. Insulation class : 

viii. Type of enclosure : 

ix. Rated speed (rpm) : 

b. Hoist Motors : Main Hoist 

i. Number : 

ii. Type : 

iii. Manufacturer : 

iv. Voltage, phase, frequency : 

v. KW : 

vi. Temp, rise over 50°C ambient : 

vii. Insulation class : 

viii. Type of enclosure : 

ix. Degree of protection : 

2.4.12 Brakes 

i. : Trolley Bridge 

a) Type and number : 

b) Make / Size : 

c) Braking capacity of full load torque : 

d) Designed distance for complete : 

stopping from full speed, mm 

Page 30 of 31




ii. Hoist Machinery Brake : Main hoist 

a) Type, number : 

b) Make / Size : 

c) Braking capacity at % of full load : 

torque 

2.4.13 Gear Boxes Ratio : Type Rating S.F. 

a) CT : 

b) LT : 

c) MH : 

d) AH : 

2.4.14 Load indication sign on Crane Bridge : 

2.4.15 Extent and type of Painting on equipment : 

Before shipment (as per specs.) 

2.4.16 Shop tests conform to requirement of specification : 

Page 31 of 31





Bathinda Multiproduct Pipeline 

SPECIFICATION FOR CORROSION INHIBITOR PACKAGE 

435-JH0902-10-ME-SPC-0010 

27-Aug-09 





Phone: +91-22-67818000 

Fax : +91-22-67818080 






SYNOPSIS 

Disclaimer 











PARSONS 

APPROVAL 

DATE 

CLIENT 

APPROVAL 

DATE 

A 


Subramanyam 

.S 

Sameer 

Ishwad 

Jeremy 

Wallace 

06-July-09 

N/A 

B 


Subramanyam 

.S 

Sameer 

Ishwad 

Jeremy 

Wallace 

20-July-09 

N/A 

C 


Subramanyam 

.S 

Sameer 

Ishwad 

KMN Pillai 

27-Aug-09




CONTENTS 

1. INTRODUCTION ................................................................................................................5 

1.1 Scope of Work...............................................................................................................................5 

1.2 Corrosion Inhibitor Package at RamanMandi ...............................................................................6 

1.3 Work Included ..............................................................................................................................6 

1.3 Design Basis .................................................................................................................................8 

1.3.1 Design Life, Availability and Reliability......................................................................................8 

1.3.2 Noise Limitation ........................................................................................................................8 

1.4 Material Certification .....................................................................................................................8 

1.5 Reference Documents ..................................................................................................................9 

1.5.1 British Standards (BS) ..............................................................................................................9 

1.5.2 American Standard Institute (ANSI) .........................................................................................9 

1.5.3 American Society and Mechanical Engineers (ASME) ............................................................9 

1.5.4 American Society for Testing and Materials (ASTM) .............................................................10 

1.5.5 American Petroleum Institute (API) ........................................................................................10 

1.5.6 The Institute of Petroleum (IP) ...............................................................................................11 

1.5.7 ISO Standards (ISO) ..............................................................................................................11 

1.5.8 Manufacturers Standardisation Society (MSS) ......................................................................11 

1.5.9 International Electrotechnical Commission (IEC)...................................................................11 

1.5.10 Petroleum and Explosives Safety Organisation (PESO) ......................................................12 

1.5.11 Referenced Standard Specifications.....................................................................................12 

1.6 Conflicts, Deviations, and Amendments .....................................................................................12 

1.7 Contractor / Vendor Exceptions ..................................................................................................13 

2. TECHNICAL REQUIREMENTS ..............................................................................................14 

3 DESIGN REQUIREMENTS .....................................................................................................15 

4 QUALITY ASSURANCE INSPECTION, & SITE TESTING ......................................................25 

4.1 Quality Assurance ......................................................................................................................25




4.2 Factory Inspection and Site Acceptance Testing:.......................................................................25 

4.3 Material and Welding Inspection:...............................................................................................26 

4.4 Contractor / Vendor Requirements ............................................................................................27 

5 SURFACE PREPARATION AND FINISH .................................................................................27 

6 NAMEPLATE DETAILS ............................................................................................................28 

7 PACKAGING, PRESERVATION AND PREPARATION FOR SHIPMENT .............................28 

8 SPARE PARTS AND SPECIAL TOOLS .................................................................................29 

8.1 Spares .........................................................................................................................................29 

8.2 Special Tools...............................................................................................................................30 

9 DOCUMENTATION ..................................................................................................................30 

9.1 Bid Documentation....................................................................................................................30 

9.2 Post Order Documentation .......................................................................................................31






This Specification covers the minimum project requirements for the supply of Corrosion 

Inhibitor Package suitable for installation on the HPCL-GGSRPEP, Project at Raman 

Mandi. There shall be a dedicated Corrosion Inhibitor Package each for RamanMandi to 

Bhadurgarh Pipeline & one for RamanMandi to Bathinda Pipeline. The requirements for the 

same are as listed and given in this specification. 

This specification details the general requirements for the Package and is to be used in 

conjunction with the data sheets, drawings and specifications detailed and attached 


The Contractor / Vendor shall be responsible for the design, fabrication, assembly, painting, 

inspection, erection, testing and commissioning, certification, preparation for shipment and 

supply of documentation for the complete package as described in this specification and 

attachments in the bid package. 

This specification does not dictate the detailed equipment design requirements. It is intended 

that this responsibility be retained fully by the Contractor / Vendor so that Contractor’s / 

Vendor’s warranty remains fully in force and is not affected by statements herein. 

The Corrosion Inhibitor Package shall be complete including all ancillary equipment/items 

required to meet the design and environmental conditions as stated herein. Any additional 

part, equipment, material, etc., which are not specifically mentioned in this specification, but 

are required to make the supplied equipment/item complete in all respect in accordance with 

the intent of this specification, statutory requirements, applicable codes/standards, good 

engineering practices, and for safe and trouble-free operation, shall be deemed to be covered 

under the scope of this specification. 

If national and/or local regulations exist in which some of the requirements may be more 

stringent than in this specification, the Contractor / Vendor shall determine by careful scrutiny 

which of the requirements are the more stringent and which combination of requirements will 

be acceptable as regards safety, environmental, economic and legal aspects, in all cases the 

contractor / vendor shall inform the purchaser of any deviation from the requirements of this 

specification which is considered to be necessary in order to comply with national and/or local 

5




regulations. The purchaser may then decide to negotiate with the Authorities concerned with 

the object of obtaining agreement to follow this specification as closely as possible. 

This specification includes tagging and preparation for shipment of all equipment furnished. 

1.2 Corrosion Inhibitor Package at RamanMandi 

Item Equipment No. Equipment Title Data Sheet No. 

1 ZZ-10-002 Corrosion Inhibitor Package for 

RamanMandi to Bhadurgarh Pipeline 

2 ZZ-10-001 Corrosion Inhibitor Package for 

RamanMandi to Bathinda Pipeline 

435-JH0902-10-ME-DAS-0011 

435-JH0902-10-ME-DAS-0013 

1.3 Work Included 

The Contractor / Vendor shall furnish all components and ancillary equipment necessary to make the 



• Hydraulically actuated double diaphragm type positive displacement metering pumps 

complete with electrical motor and Variable Frequency Drives (For Control of Dosing 

Rate) 

• Chemical storage tank with access ladder and platforms as required. 

• Calibration column 

• Strainer 

• Pulsation dampener 

• Pressure relief valve 

• Pressure indicator 

• Check valve 

• Pressure Transmitter 

• Flow transmitter 

6




• All necessary instrumentation as shown on P&ID. 

• Signals to be carried to PLC (to be provided by Purchaser) 

• Local Control Stations for Equipments, with start/stop push buttons And Auto / 

Manual Selector Switch. 

• All interconnecting pipe work with necessary supports, valves and fittings in SS 316L 

• Common skid structure base plate to accommodate the Tank, pump, instrumentation 

and connecting piping incorporating integrated skid drip pan. 

• Cables, cable gland and cable tray within skid limit 

• Earthing lugs 

• Supply of power cabling between switchgears, and between package and driven 

motors & VFD. 

• Power supplies as may be required for the package. 

• Name plates for all equipments, instruments, valves, and tanks for the package. 

• Foundation / Holding down bolts for the package. 

• Inspection of the package at Contractor / vendor / sub vendors shop, 

• Complete Erection, Testing and Commissioning of the package. 

• Surface preparation and Painting as per Project Painting specifications attached 


• First fill of chemicals required for the package. 

• First fill of lubricants. 

• Packing for Transportation 

• Preparation for shipment of the package to site. 

• Unloading & storage at site. 

• Spares parts for start up & commissioning (with list) 

• Spares for 2 years operation and maintenance (if required – optional), however list 

with price shall be provided 

7




• Documentation for approval. 

• Package Performance Guarantees 

1.3 Design Basis 

1.3.1 Design Life, Availability and Reliability 


Contractor / Vendor. Unless otherwise stated, the package design life shall be 35 years, with an 


The Contractor / Vendor shall identify any aspects of its standard components or packages that do 

not meet this requirement and submit descriptions to the Purchaser for consideration during the 

tendering process. 

1.3.2 Noise Limitation 

Noise levels of all equipment (within the package) under normal operation shall not exceed an eighthour 

equivalent continuous A-weighted sound pressure level, LAeq,8h, of 85 dB(A) at 1 metre in all 

directions. Sound level tests shall be performed to verify the same. In case noise test certificate 

shows a sound level exceeding 85 dB (A), necessary rectification/modification shall be done at 

Contractor’s / Vendor ’s own cost and the equipments shall be re-tested to bring down the sound level 

to the specified limit. 

Predicted noise levels shall be subject to approval by Purchaser. 

The specified noise level should be attained without the use of orifices, mufflers, diffusers and/or 

credit for thermal or acoustic insulation where practical. 

Noise attenuating enclosure is generally not preferred and shall be avoided. However, if used (subject 

to approval of Purchaser) shall be designed to provide full access to the equipment for maintenance 

and operation. 


Pressure containing parts and shafting shall have material certification in compliance with BS EN 

10204 type 3.1 and include original mill certificates or certified copies. Components shall be fully 

traceable back to the certificate. 

Other parts shall be provided with certification to BS EN 10204 type 2.2. 

8




1.5 Reference Documents 

The design, fabrication and supply of Corrosion Inhibitor Package shall comply with the applicable 

sections of the latest edition of the following codes and standards including their addenda 

1.5.1 British Standards (BS) 

Standard No. 

BS 7244 


Specifications for Flame arrestors for General use 

1.5.2 American Standard Institute (ANSI) 

Standard No. 

ANSI B40.1 

ANSI MC 96.1 


Gauges - Pressure Indicating Dial Type - Elastic Element 

Temperature Measurement Thermocouples 

1.5.3 American Society and Mechanical Engineers (ASME) 

Standard No. 

ASME B16.25 

ASME B16.34 

ASME B16.5 

ASME B16.9 

ASME B18.2.2 

ASME B31.3 

ASME B46.1 

ASME BPVC Section II 

ASME BPVC Section V 


Butt welded ends for pipe,valves,flangesand fittings 

Valves—Flanged, Threaded, and Welding End 

Pipe Flanges and Flanged Fittings 

Factory-made Wrought Butt Welding Fittings 

Square and Hex Nuts 

Process Piping 

Surface Texture (Surface Roughness, Waviness and Lay) 

Materials (Parts A,B,C,D) 

Non-destructive Examination 

ASME BPVC Section VIII Rules for Construction of Pressure Vessels - Division 1 

ASME BPVC Section IX 

Welding and Brazing Qualifications 

9




1.5.4 American Society for Testing and Materials (ASTM) 

Standard No. 

ASTM A194 

ASTM A36 

AISC 

AWD D 1.1 


Standard Specification for Carbon and Alloy Steel Nuts for Bolts for 

High Pressure or High Temperature Service, or Both 

Standard Specification for Carbon Structural Steel 

American Institute for Steel Construction 

American Structural Welding Code 

1.5.5 American Petroleum Institute (API) 

Standard No. 

API 520 

API 526 

API 610 

API 675 

API 614 

API 670 

API 671 

API 677 

API 682 

API 650 

API 12F 

API RP 505 


Sizing Selection and Installation of Pressure Relieving Devices in 

Refineries 

Flanged Steel Pressure Relief valves 

Centrifugal Pumps for Petroleum, Petrochemical and Natural Gas 

Industries 

Positive Displacement Pumps- Controlled Volume 

Lubrication, Shaft-sealing and Oil-control Systems and Auxiliaries 

Machinery Protection Systems 

Special Purpose Couplings for Petroleum, Chemical and Gas Industry 

Services 

General-Purpose Gear Units for Petroleum, Chemical and Gas 

Industry Services 

Pumps—Shaft Sealing Systems for Centrifugal and Rotary Pumps 

Welded Storage Tank 

Specification for Shop weld tank for storage and production liquid. 

Recommended Practice for Classification of Locations for Electrical 

Installations at Petroleum Facilities as Class I, Zone 0, Zone 1 and 

Zone 2 

10




Standard No. 

API RP 521 


Guide for Pressure Relieving & Depressurising systems 

1.5.6 The Institute of Petroleum (IP) 

Standard No. 

IP 205/71 


Petroleum Measurement Manual Part V, Automatic Tank Gauging 

1.5.7 ISO Standards (ISO) 

Standard No. 

ISO 9001 


Quality Management Systems – Requirements (2001 Ed.) 

1.5.8 Manufacturers Standardisation Society (MSS) 

Standard No. 

MSS SP-55 


Quality Standard for Steel Castings for Valves, Flanges and Fittings 

and Other Piping Components - Visual Method for Evaluation of 

Surface Irregularities 

1.5.9 International Electrotechnical Commission (IEC) 

Standard No. 

IEC 60947-5-1 

IEC 60034-1 


Specification for The Colour of Indicator Lights, Push Buttons, 

Annunciators and Digital Readouts 


11




1.5.10 Petroleum and Explosives Safety Organisation (PESO) 

1.5.11 Referenced Standard Specifications 

Document No. 

0435-JH0902-00-PI-SPC-003 

435-JH0902-00-EL-SPC-0002 

435-JH0902-00-EL-SPC-0003 

435-JH0902-00-PE-SPC-0001 

435-JH0902-00-PE-SPC-0002 

435-JH0902-00-EL-DAS-0085 

435-JH0902-00-EL-DAS-0086 

0435-JH0902-00-IN-BOD-001 




Specification for Variable Frequency Drives 

Piping Material Specifications 

Valve Material Specifications 

Datasheets for Low Voltage Induction Motors 

Datasheets for Low Voltage Variable Frequency Drives 

Basis of Design for Instrumentation 

1.6 Conflicts, Deviations, and Amendments 

Contractor’s / Vendor’s bid shall clearly state and list exceptions to this specification and all 

referenced documents. In the event of any conflict arising between this specification and other 

documents listed herein, refer comments to Purchaser for clarification before design or fabrication 

commences. 

The order of precedence that applies is generally as follows: 

• Data Sheets 





• Referenced Codes and Standards. 

12




1.7 Contractor / Vendor Exceptions 

Contractor’s / Vendor’s Bid shall clearly state and list the exceptions/deviations under a separate 

section “exceptions/deviations” to Specifications, referenced codes and standards and all documents 

referred in this specification. Exceptions mentioned elsewhere in the Bid or implied in the Bid shall be 

invalid. 

13




2. TECHNICAL REQUIREMENTS 

The equipments and all the auxiliaries within the Corrosion Inhibitor Package shall conform to the 

minimum requirements mentioned in this specification along with the attached datasheets and 

technical requirements furnished elsewhere in the bid package. 

All the equipments, piping valves, electrical items, instrumentation and controls shall be properly 

mounted completely connected in accordance with the applicable project specifications. 

Each component shall be located in such a manner as to be easy to operate and maintain. All 

inline/offline instruments and piping valves shall be accessible. The skid layout shall be free from 

access obstructions. Layout of piping and cables shall avoid interference and obstructions to any 

junction box, instruments or valves. 

The design of the individual pieces of equipment forming the packaged unit(s) shall be strictly in 

accordance with the mechanical data and process service condition, as noted in this specification and 

the data sheets. 

The design shall ensure the satisfactory functioning of the complete package, i.e. tanks, chemical 

injection pumps, controls and other ancillaries. In cases where the Contractor / Vendor supplies 

equipment that he has not manufactured, the Contractor / Vendor shall ensure that the designs of 

these are compatible with each other and with his own equipment in all respects. The satisfactory 

functioning of the complete package shall form part of the Contractor / Vendor’s guarantee. 

The Contractor / Vendor shall be fully responsible for the supply, selection and quality of all materials 

inclusive of all consumables, welding, testing, protection devices, machinery, tools, labour and all 

other necessary materials and services required to complete the supply of equipment whether or not 

they are specified in this Specification and attachments. 

The Contractor / Vendor shall be fully responsible for the coordination with all his Sub-Vendors for 

materials and services provided by them. However, Contractor / Vendor shall be solely responsible to 

Purchaser for compliance with the specified requirements. Contractor / Vendor shall submit to the 

purchaser a list of experience for all his sub vendors for the items sub ordered within the package. 

Should the Contractor / Vendor come across any discrepancy, deficiency, or lack of clarity in any part 

of this specification or attached documents, he shall notify the same to the Purchaser, along with his 

offer, with a proposed alternative or additional item and prices for each category thus included. Any 

items so identified after Order award will not constitute a change and will not be the cause for cost or 

schedule alteration. 

14




All equipment within the skid shall be suitable for external outdoor undershed environment, suitable 

for the hazardous area classification mentioned in the datasheets. 

Contractor / Vendor shall complete all relevant sections of the data sheet, and submit the same with 

his bid / offer. 

As a minimum, the equipment shall be suitable for service in a Class 1, Zone 2, IIB, T3 hazardous 

area as defined by API RP 505. 

The Contractor / Vendor shall comply with applicable Indian Federal, State or Local codes, 

regulations, ordinances, and rules. 

3 DESIGN REQUIREMENTS 

The equipment shall be designed to handle chemicals as defined in the relevant datasheets. 

Contractor / Vendor shall comply with any requirements or recommendations as stated in the 

respective chemical manufacturer’s Material Safety Data Sheets (MSDS). 

Contractor / Vendor, shall comply to the requirements furnished below as a minimum, however any 

additional item/ equipment / controls, which are not specifically mentioned in this specification 

however deemed necessary by the contractor / vendor shall be included in the scope of supply: 

Chemical Injection Pump: 

a) The chemical injection pumps and accessories shall be designed for 35 years of trouble 

free, uninterrupted and safe operation and shall be as per API 675. 

b) For Recommended dosing rate please refer Process datasheet 435-JH0902-10-PR-DAS- 

0017 & 435-JH0902-10-PR-DAS-0017. Contractor to confirm the dosing rate required for 

the pump based on the injection rate required. 

c) Each pump shall be capable of 110% of the design capacity. 

d) The pump discharge shall be provided with an external relief valve for protection of the 

piping against a closed pump discharge. 

e) The external relief device shall be in addition to any internal pressure relieving device 

which may be supplied as an integral part of the pump. 

f) A rupture detection system shall be provided for the detection of the diaphragm failure and 

to trip the pump, when either of the diaphragms gets detected as ruptured. Diaphragms 

shall be designed in such a way that the stresses developed on the diaphragm during the 

deflection are the minimum. 

15




g) Contractor / Vendor shall supply fittings/tools for the nitrogen charging of the pulsation 

dampeners. 

h) All coupling components liable to rub as a result of failure of the flexible elements shall be 

of non-sparking materials. Coupling guard shall also be of non-sparking material. 

i) All vents and drains shall be terminated with a valve and blind flange. The outlets on valve 

vent and drains shall be piped down to the skid. 

Chemical Storage : 

Corrosion Inhibitor should be stored in a suitably sized tank based on the properties of 

inhibitor & dosing rate.The storage tank shall be cylindrical shape with dished end, as may 

be necessary for the chemical to be stored in the tank under the required pressure. 

If the tank is cylindrical in shape with dished end, it shall meet the following as minimum: 

• Design, fabrication, welding, inspection & testing shall be in accordance with ASME Sec 

VIII, Div 1. 

• It may be installed in vertical or horizontal position. 

• Full penetration welds shall be used for all nozzles, manholes etc. 

• For proper access & maintenance, adequate platforms and ladders shall be provided if 

required. 

Sr. 

no. 

Following are the recommended Corrosion inhibitor suppliers 

Suppliers Chemicals * 

1. Innospec Ltd DCI-4A 

2. Dorf Ketal Chemicals Pvt Ltd Unicor J 

3. CIBA Speciality chemicals Ciba ® SARKOSYL ® O 

4. Chemtreat India Pvt Ltd Remidol 

Note: *Contractor to confirm based on selected Inhibitor. Equivalent or Superior product needs to be 

supplied. 

16




Interconnecting Piping: 

a) All piping shall be designed, fabricated, inspected and test in accordance with ASME 

B31.3, this document and other relevant documents attached with the Bid package. 

b) Material of construction of all piping, valves shall be as per the Piping Material 

specifications & Valve material specifications and The material of tubing and tube fitting (as 

applicable for corrosion inhibitor package) shall be SS316L and shall be based on the 

projection piping class. 

c) The use of asbestos products is prohibited. 

d) All piping shall be neatly arranged and shall be terminated at the edge of the skid. 

e) Minimum piping / connection size shall be ½” NPT 

f) Equipment and valves shall be located to ensure it can be easily accessed, operated and 

maintained. Pipe works shall be routed to allow ease of access to valves and 

instrumentation. 

g) Equipment arrangement shall favour compactness but shall allow ample room for 

convenient operation, access and maintenance. The layout shall ensure access is 

available without the use of scaffolding or portable ladders. Access routes shall be 

provided into the areas of the package for equipment needing inspection, checking or 

servicing, of all pumps, valves, instruments etc. 

h) All valves and local read-out type instruments shall also be positioned in accessible 

locations. 

i) All piping systems shall be designed so that the loads and moments applied at the flanges 

of equipment shall not exceed the permissible reactions for the equipment as specified by 

the manufacturers of the equipment. 

j) All piping shall be terminated and anchored at the skid edge with an appropriately rated 

flange. Piping connections at the battery limits of package shall be flanged connections. 

Piping shall be arranged in such a manner as to avoid tripping or overhead problems. 

k) All piping shall be adequately supported for both service & shipment. Thermoplastic pads 

shall be installed between all pipes and their supports. Where u-bolts are used, same shall 

be of SS 316L. 

17




l) Suitably located vents & drains shall be provided for any testing, start-up, operations or 

maintenance of the skid. These shall be located on equipment or piping as necessary. 

m) As a minimum piping welds shall be subject to 100% DPT and as per clause 4.3 of this 

specification , piping shall be hydro tested. 

n) Isolation valves are required between the tank and the level instrument and gauges. 

Isolation valves are also required between instruments and piping. 

Electrical 

All Motors & Variable Frequency Drive shall conform to project specifications and data 

sheet referred in this specification and in the bid package. 

All the motors shall be flameproof Ex(d) type, suitable for Zone 2, Gas group IIA, IIB, 

and T3. Type test certificates for explosion protection class from the recognised testing 

authority shall be submitted. As per the statutory requirement in India the approval from 

the chief controller of explosives (CCOE) for flameproof motors, Ex(d) must be 

submitted. This test certificate for flameproof motor, Ex(d) must be tested for having 

tested the motor along with Variable Frequency Drive for all the offered type of the 

equipment as per the requirement of IEC. Otherwise details of compliance to IEC 

requirement for Variable speed flameproof motor shall be submitted. BIS license must 

have been possessed by the manufacturer for indigenously manufactured FLP motors; 

CCOE Certificates for the Flameproof motors shall be submitted along with the final 

MDR / OMM. 

Instrumentation: 

I) General : 

a) All the instrumentation furnished within the package shall meet the requirements 

mentioned in the basis of design for Instrumentation for GGSRPEP Project, attached 

elsewhere in the bid package. All the instruments furnished within the package shall be 

suitable for hazardous area classification of Zone1, Gr. IIA, IIB, and T3. The enclosure 

protection shall be suitable minimum IP 65. 

b) All materials of pressure housing and all wetted parts shall be compatible with the 

process fluid handled. As a minimum, material of construction shall be SS 316L. 

c) The cable entry connection to all instrumentations shall be ISO metric (M20). 

18




d) Tube fittings shall be of twin-ferrule double compression type. Seamless stainless steel 

tubing, fittings and valves shall be in accordance with applicable project specification. 

Connection on equipment and piping for instruments and test points shall comply with 

piping class specification. All tubes and fittings materials shall be SS 316L as minimum. 

The instrument tubing shall be PVC coated (2 mm). 

e) All instruments should be readable and easily accessible for maintenance. 

f) Transmitters shall have digital communication signal superimposed (HART) on the 

standard 4-20 mA DC signal through 600 ohms load. 

II) Level Instruments: 

a) Storage tank shall be provided with level gauge and level electronic transmitter (for 

level shut down low). Both the level instruments shall be mounted on the stand pipe 

provided on the tank. 

A) Level Gauge: 

Level gauges shall be magnetic type with the following features: 

• Continuous monitoring of liquid level over measuring length 

• Local display/ bar graph style flags in RED and WHITE colours 

• Robust, shock proof and completely sealed for safety 

• Suitable for high toxic fluids 

• Powerful Omni-direction magnet system – guide – free float 

• Rotate able display through 360° irrespective of float position 

• High pressure capability 

• Side or Top mounted options with appropriate flange rating 

• SS 316L scale with millimeter marking 

• Tank level gauges shall be graduated to indicate the volume of liquid in liters 

• Vent and drain connections with isolation valves and caps 

• Body material shall be SS 316L as a minimum and rating for level instruments shall 

conform to the applicable equipment/ process pipes specification 

19




• The protection for the instrument shall be IP65, as a minimum. 

B) Level Transmitter: 

• Level transmitter shall be external cage side mounted float type 

• Transmitter shall have two wire 4-20 mA @24V DC powered from the PLC panel (By 

purchaser). 

• External level instrument chambers shall be fabricated from seamless process piping. 

The chamber shall be self supporting from the primary process connection, without 

over stressing the gauge chamber or the vessel nozzles and without the need for 

intermediate chamber supports. 

• Level transmitter shall be provided with integral digital indicator to read level in 

Engineering units 

• Level transmitter shall be Intrinsically safe (EEx ‘ia’) certified type 

III) 

Pressure Instruments: 

• The pressure gauges shall be provided at upstream and downstream of each pump and 

a pressure transmitter shall be provided at the pump common discharge header (for 

pressure shut down high). 

A) Pressure Gauges 

• Pressure gauges shall be 150mm in diameter for general applications. 

• Differential Pressure Gauges shall be 150mm in diameter. 

• White laminated dials with black numerals shall be standard. 

• The dial shall be marked as follows :- 

o Manufacturers full name 

o Manufacturers model number 

o Element material specification and grade 

o Other key details, for example NACE MR 01-75 

• Casing material shall be 316 Stainless Steel. 

20




• For general use gauges shall use a bourdon tube measuring element. The accuracy shall be 

0.5% FSD or better. The movement shall be either rotary geared stainless steel or cam and 

roller type. 

• The element material for process gauges shall be 316 stainless steel as a minimum. 

• All gauges shall be full safety pattern fitted with shatterproof safety glass. Gauges below 25 

Kg/cm2 range shall have a safety blow-out disc in the back. Gauges for higher than 25 

Kg/cm2 service shall have a solid front and blow-out rear. 

• Gauges exposed to vibration or process pulsations shall be glycerine filled and shall be fitted 

with pulsation dampers to the same material as the element. 

• Gauges shall be able to withstand, without zero or calibration shift, over-range pressure of 1.3 

x calibrated range as standard. 

• Over-range protection such as gauge snubbers or savers shall be provided where the 

process pressures may exceed 1.3 x FSD. 

• Gauge connection shall be at the bottom (Panel mounted gauges shall have rear process 

connections). Standard connections shall be 1/2″NPT male for process gauges. 

• Gauges will be supplied with engraved labels stating tag no. 

• Gauges for pump service shall have pulsation dampeners where required and gauge savers 

in all applications. 

B) Pressure Transmitters: 

• The pressure transmitter shall be 2-wire, 4-20 mA @ 24 VDC output with ingress protection of 

IP65 and shall be intrinsically safe (EEx ‘ia’) certified type. The transmitter shall be provided 

with integral digital indicator for pressure (available close to the pump). It shall read in 

engineering units for the pressure measurement. The Transmitter shall be powered from PLC 

panel (By Purchaser). The accuracy of Pressure Transmitters shall be +/- 0.1% of full scale 

reading. 

IV) 

Pressure Relief Valves: 

• Pressure relief valve shall be full nozzle, full lift and self seating type and according to API- 

RP-520, 521, 526, 527 (with exception to that for low flow items-the dimensions of inlet, outlet 

flange and orifice will be smaller than the one specified in API 526 to avoid fluttering). 

Body/Bonnet, Nozzle/disc shall be of SS 316L. The spring shall be SS material or Inconel. 

• For variable back pressure, balance bellow type valve shall be used with bellow material as 

SS 316L. Design/engineering percentage over pressure and blow down shall be considered 

to arrive at the selection and calculation. 

21




V) Flow Instruments: 

• Flow transmitter and indicator shall be provided on pump common discharge. 

• The flow transmitter shall be 2-wire, 4-20 mA @ 24 VDC output with ingress protection of 

IP65 and shall be intrinsically safe (EEx ‘ia’) certified type. The transmitter shall be provided 

with integral digital indicator for flow (available close to the pump). It shall read in engineering 

units for the flow measurement. The Transmitter shall be powered from PLC panel (By 

Purchaser). The accuracy of flow transmitters shall be +/- 0.1% of full scale reading. 

VI) 

Local Control Stations 

The skid shall be provided with a Local Control Stations with the following requirements: 

o 

o 

o 

o 

o 

The panel shall be provided with local Start/Stop push buttons, auto manual 

selector switch for each of the chemical injection pumps. 

It shall be suitable for hazardous area of Zone 2, Gas group IIA, IIB, and temp. 

Class.T3. The enclosure class shall be IP-65. 

The pumps shall trip on low level in the corrosion inhibitor storage tank. 

The chemical Injection package logic shall be implemented in the PLC panel (By 

purchaser). 

Indication lamps shall be provided on the local control stations for pump/motor 

running, stopped, tripped, common fault etc. 

o The local control stations shall be provided with sunshade. Contractor / Vendor 

shall ensure that adequate protection is provided for all the electronic 

components mounted inside the panel. 

VII) PLC for the Corrosion Inhibitor Package (Provided by the Purchaser) 

• All the analogue signals from level transmitter, pressure transmitters etc. shall be wired to the 

interface junction box supplied by Contractor / Vendor. 

• The multi pair cable from the junction box up to the PLC panel for cable termination shall be 

provided Contractor / Vendor. The Corrosion Inhibitor Package Logic shall be implemented in 

the PLC Panel. Pumps shall be controlled through VFD for controlling the Dosing into the 

main pipeline. 

22




VIII) Junction Box on Skid 

• All field instrumentation within skid shall be terminated in skid edge mounted Junction Boxes 

for further cabling upto PLC. Connections shall be made at terminals in instruments or 

junction boxes. Splicing is not acceptable. Junction box terminal strips shall be fabricated of 

rail-mounted shoe terminal blocks and associated hardware. 

• Instrumentation cables shall be adequately separated from power cables and equipment to 

minimize interference. Cables shall be installed in cable trays. 

• All junction boxes shall be certified EEx’d’ (Flameproof) as a minimum. 

• The junction boxes shall be suitably sized for ease of access, and shall be equipped with 

sufficient terminals for termination of cable cores, including all spare cores. An additional 25% 

of terminals shall be fitted in excess of the above requirement. 

• All cables shall be XLPE/PVC insulated, single galvanized steel wire armour and PVC over 

sheathed. 

• The terminals in the junction boxes shall be suitably sized for the cable cores, 

• Each junction box shall have 20% spare entries for field cables and a spare entry for each 

size of multi core cable entering the box. All spare entries shall be fitted with certified sealing 

plugs. 

• All cable glands shall be certified EEx(d). 

Structural Base Plate: 

• Corrosion Inhibitor Package Skid shall accommodate the pump, interconnecting piping, 

necessary valve, instrumentation and LCS. 

• The skid shall be designed and built to ensure that all the equipment along with the 

accessories & piping are mounted suitably for convenient operation and maintenance. 

• The skid shall be rigid construction that cannot distort during lifting / hoisting and shipment. 

Anchor bolts shall be within the Corrosion Inhibitor Package scope of supply. 

• The Contractor / Vendor shall provide a common drip pan (with flanged drain outlet 

connection) to cover all sources of spillage and extending underneath the entire skid. The drip 

pan shall have sufficient strength, thickness to prevent sags, rises and out of level areas that 

may cause liquid trapping. The drain from the drip pan shall be terminated at skid edge. The 

drip pan shall be sloped towards the flanged drain outlet connection. 

23




• All equipment edges shall be within skid structural base plate, no part of equipment or 

terminal points shall project beyond the edge of the skid structural base plate. 

• Equipment shall be mounted on the skid such that equipment supports bear directly on and 

attach to primary structural members of the skid. 

• Spreader beam (if required) to facilitate lifting shall be provided by Contractor / Vendor 

together with slings and shackles. These lifting devices shall be certified by an approved third 

party agency for the required safe working load (SWL). 

• Lifting lugs shall be adequately designed and fully welded with 100% NDT and shall be load 

tested to minimum 150% of their design load. 

• 100% UT & 100% MPI/ DPI will be carried out on parent materials, lifting lugs & lifting aids 

material. All welds on lifting lugs & lifting aids shall be subject to a 100% MPI test both before 

/ after the load test. 

24




4 QUALITY ASSURANCE INSPECTION, & SITE TESTING 

4.1 Quality Assurance 

The Contractor / Vendor shall demonstrate that he operates a quality system in accordance with 

the ISO 9000 series of requirements. The effectiveness of the quality system and the 

Contractor’s / Vendor's compliance with it shall be subject to monitoring by Purchaser and in 

addition, may be audited following an agreed period of notice. 

The Contractor / Vendor shall submit a quality control program for Purchaser review at the time 

of offer. The Contractor / Vendor shall provide facilities for and cooperate with Purchaser and 

statutory authority inspectors during manufacturing, assembly and testing. 

4.2 Factory Inspection and Site Acceptance Testing: 

Contractor / Vendor shall submit for review and approval by the Purchaser an Inspection and 

Test Plan (ITP) covering all relevant components, completed equipment and systems. The 

Extent of witness, review and hold points shall be finalised post award. 

Contractor / Vendor shall allow Purchaser access to the fabrication premises for an inspection 

prior to order placement. 

A detailed test procedure of shop tests shall be submitted at least one (1) month in advance of 

any testing and shall be approved by the Purchaser. 

The entire unit shall be assembled and tested to functionally check the total system operation 

and ensure minimum commissioning and installation time on site. After assembly, Contractor / 

Vendor shall perform the following tests: 

o 

o 

o 

o 

Vendor's standard shop tests 

Hydro test of all pressure parts. 

Performance test for all the pumps at pump manufacturer’s shop with job 

drivers. The performance test shall include flow repeatability, accuracy, and line 

in accordance with API 675. 

Mechanical run test. 

25




o 

o 

o 

o 

o 

Electrical Motor test at manufacturer’s shop. 

Functionality check for VFD at manufacturer’s shop. 

Functional & routine testing of skid and all items / accessories including valves, 

cables etc. 

Skid overall dimensions. 

Noise tests. 

The complete unit shall be trial assembled and dimensionally checked prior to shipment. This 

activity shall be witnessed by the Purchaser and/or his representative. 

Site Acceptance Testing: 

The Contractor / Vendor shall provide site erection, pre-commissioning and commissioning of 

the package. Commissioning shall commence After the completion of the precommissioning 

activities (including civil, mechanical, electrical, instrumentation works) 

Purchaser's final acceptance of the equipment will be subject to a performance test once the 

equipment has been erected, installed and Pre- commissioned. Contractor / Vendor shall 

submit to the purchaser a Site acceptance testing procedure after order, SAT shall be 

conducted based on the approved Procedure by the purchaser. Such tests shall be held no 

later than one (1) year from initial startup. 

4.3 Material and Welding Inspection: 

Butt welds shall be 10% examined by radiography and pressure retaining fillet welds shall be 

100% examined by DP test. Should radiography prove impractical, 100% ultrasonic inspection 

shall be permitted with the approval of the Purchaser. 

Skid and vessel pad eyes shall require 100% DP test. 

26




Pressure retaining parts shall be hydrostatically tested to at least 1.5 times of the design pressure, in 

accordance with Section VIII, Division 1 of the ASME Code or ASME B31.3 / 31.4. 

Welders/welder operators shall be qualified in accordance with Section IX of the ASME code and 

approved by the Purchaser prior to welding on this contract. 

Weld procedures shall be qualified in accordance with Section IX of the ASME code and submitted 

for approval by the Purchaser before welding can commence 

4.4 Contractor / Vendor Requirements 

Contractor / Vendor shall provide Purchaser with at least 14 days notice to witness tests run in both 

his shop and his Sub-Vendor's shops. 

Contractor / Vendor shall provide Purchaser with reasonable access to its and its Sub-Vendor's plant 

facilities in order to verify that equipment is manufactured and tested as specified. 

Contractor / Vendor shall provide calibration certificates of testing instrumentation for review by the 

Purchaser prior to each test. 

Contractor / Vendor shall provide weekly reports during procurement and fabrication phases 

indicating progress status. 

Contractor / Vendor shall provide O&M training for HPCL Operations and Maintenance personnel. 

This training shall be provided for the Package supplied including any sub-vendor equipment 

included in the package. 

5 SURFACE PREPARATION AND FINISH 

All exposed steelwork and fabricated items and piping (Other than Stainless Steel) shall be prepared 

and painted in accordance with Specification for Painting / Coating Requirements 0435-JH0902-00- 

PI-SPC-003. All SS Piping & surfaces shall be pickled & passivated. 

All Sub Vendor supplied components such as piping valves, instrumentation, junction boxes and like 

equipment shall be protected by the Sub Vendors standard protective coating. Contractor / Vendor 

shall provide details of the Sub Vendor’s protective coatings with the bid. 

27




6 NAMEPLATE DETAILS 

All the Equipment, Tanks, instruments, Speciality items shall be supplied with tag plates. 

Tag plates shall be manufactured from 316 stainless steel. Text and numbering shall be clearly 

engraved, paint filled and a minimum of 6mm high. 

Tag plates for accessories shall be secured using stainless steel screws, stainless steel wire or 

stainless steel chain. 

All pressure regulators shall have a label identifying operating set pressure. 

Each valve and actuator assembly shall be fitted with a stainless steel nameplate providing, 

as a minimum, the following information: 

• Tag Number 

• Manufacturer's Name or Trademark 

• Serial Number 

• Flange Pressure Rating 

• Packing Type 

• Maximum Air or Hydraulic supply pressure 

7 PACKAGING, PRESERVATION AND PREPARATION FOR 

SHIPMENT 

The Contractor / Vendor shall prepare the equipment for shipment to RamanMandi site. 

Documents, including unloading, unpacking and lifting instructions, a description of the 

reassembly steps required for installation and pre-commissioning and start up instructions 

shall be included with the package. The number of copies of documents to be provided shall 

be as stated in the Bid Package. 

Contractor / Vendor shall ensure the equipment is suitably supported and braced for 

transport. 

Prior to shipment, all instrumentation and other equipment vulnerable to damage shall be 

disassembled and boxed separately for shipment. 

28




The Contractor / Vendor shall recommend preservation requirements for idle periods of nonoperation 

up to 1 year protection against rain, moisture, dirt, blasting grit etc. 

8 SPARE PARTS AND SPECIAL TOOLS 

8.1 Spares 

Erection & Commissioning spares 

Contractor / Vendor shall provide and include in his scope of supply the recommended spares 

parts for the equipments, instruments, valves etc. within his package to cover the 

commissioning and start-up for the Corrosion Inhibitor Package. 

If however, any additional spare is consumed during erection & commissioning over and 

above the included erection & commissioning spares, the same shall be provided by the 

Contractor / Vendor at no extra cost to purchaser at the time of erection & commissioning. 

Spares for two years Normal operation 

Contractor / Vendor shall furnish an itemised list of recommended spares with unit prices for 

two years normal & continuous operation of the complete Package (including Mechanical, 

Electrical, Instrumentation spares) required. 

Equipment manufacturer's recommendations shall be followed by the Contractor / Vendor in 

the preparation of recommended spare parts list. 

All spare parts furnished by Contractor / Vendor shall be wrapped and packaged to preserve 

original as-new condition under normal conditions of storage anticipated in RamanMandi. 

The same parts shall be tagged by stainless steel tags and coded so that later identification 

as to their intended equipment usage will be facilitated. All items supplied shall be packaged 

separately and clearly marked as "Spare Parts" and shipped with the equipment in 

accordance with the instructions from Purchaser. Packing lists shall be furnished complete 

and in detail so that parts can be handled without uncrating 

29





The Contractor / Vendor shall supply one (1) set of special tools & tackles required for the 

erection and/or maintenance of the package including all ancillary equipment. 

Special Tools & Tackles means all such tools / tackles those are specific to the erection 

and/or maintenance of the supplied equipment/package, and are normally not expected to be 

available in a plant workshop, but without which it would be difficult or time-consuming to do 

erection and/or maintenance of the supplied equipment/package. 

The Contractor / Vendor shall identify the special tools required with Bid. Special tools shall 

be itemised and submitted for review. Special tools shall be itemised and submitted for 

review. 

9 DOCUMENTATION 

The Contractor / Vendor shall be responsible for providing all documentation / drawing as 

following. 

9.1 Bid Documentation 

Bid documentation shall include the following: 

• Supplier Document List 

• Production schedule 

• Product technical literature. 

• Technical and performance data as requested within this specification. 

• General Arrangement Drawing. 

• Preliminary weight data 

• Schematics wiring diagram. 

• Paint procedures. 

• Confirmation of Material Certification. 

30




• The Contractor / Vendor shall separately detail each proposed deviation from the 

specification or data sheets, and submit to the Purchaser for approval. 

9.2 Post Order Documentation 

Purchase order documentation shall include the following for approval as a minimum: 

• Contractor / Vendor documentation list 

• Production schedule 

• Inspection and test plan 

• Control valve sizing calculations (including noise calculations) 

• Contractor / Vendor datasheets including model numbers and materials for all the 

equipments, Valves, Instruments, Piping specialty items 

• Dimensional drawings, including GA drawings for the equipments 

• Equipment Layouts 

• P&ID for the Package. 

• Actuator control system schematics 

• Wiring Drawing for the Local Controls Stations. 

• Wiring for the PLC Panel (By Purchaser). 

• Details of signals to be carried to the PLC panel(By Purchaser) 

• Weight data 

• Material Certification 

• Test Procedures 

• Test Results 

• Calibration Certificates 

• Installation, Operations & Maintenance Manual (Per Equipment Type) 

31




Notes: 

• MDR & IOM 1 copy shall be submitted for purchaser’s review, after which 3 hard 

copies and 1 soft copy shall be submitted to the purchaser. 

32




Vendor/ Manufacturer’s Experience Record for Fabrication/ Packaging/ Testing of Pump/ Motor/ VSD (as applicable) 

Package 

ITEM : 

ITEM NUMBER : 

VENDOR : 

(Vendor to clarify the meaning of each letter / digit in the model designation) 

SL. 

NO. 

PARAMETER 


PROPOSED 

MODEL 


INSTALLATIONS 

Ref – 1 Ref – 2 Ref – 3 

REMARKS 

1 2 3 4 5 6 7 

1 

Size (LxWxH) : Main skid (Pump/ Gear/ Motor/ 

Instruments, Panels) 

2 Weight of main skid 

3 No. of support points 

4 Pump Data 

4.1 Make/ Model 

EXPERIENCE RECORD PROFORMA PACKAGES 


PROFORMA NO. 

435-JH0902-10-ME-LST-0013 

Page 1 of 3 

Rev 

C




SL. 

NO. 

PARAMETER 


PROPOSED 

MODEL 


INSTALLATIONS 

Ref – 1 Ref – 2 Ref – 3 

REMARKS 

4.2 Rated Capacity (m3/hr.) 

4.3 Suction/ Discharge Pressure (kg/cm2G) 

4.4 Differential Head (m) 

4.5 Speed (RPM) / Ratted BKW 

5 Driver Data 

5.1 Type of driver 


5.3 Driver Rating (kW)/ Speed (RPM) 

6 VSD Data 

6.1 Type of VSD 


6.3 Driver Rating (kW)/ Speed Range (RPM) 



PROFORMA NO. 

435-JH0902-10-ME-LST-0013 

Page 2 of 3 

Rev 

C




SL. 

NO. 

PARAMETER 


PROPOSED 

MODEL 


INSTALLATIONS 

Ref – 1 Ref – 2 Ref – 3 

REMARKS 

7 Control Panel 

8 Lube Oil System included (Yes/ No) 

9 Engineering for the package done by 

10 Project Management by 

11 

Shop where entire unit is packaged & Tested 

as per purchaser’s requirements with 

complete address/ fax & telephone no. and 

name of the contact person 

12 Data of supply & commissioning of unit 

13 

14 

15 

No. of operating hours completed at specified 

operating conditions as on bid due date. 

Name of purchaser with complete address/ 

fax no./ telephone no. and name of the 

contact person of the purchaser 

Location of operating site (complete address/ 

fax no./ telephone no. and name of contact 

person) 

16 Major problems encountered if any. 



PROFORMA NO. 

435-JH0902-10-ME-LST-0013 

Page 3 of 3 

Rev 

C



Applicable code : API 675 

Sr. 

No. 

1.a Incoming 

Material 

(Castings 

Plates & 

Pipes Tubes) 


of check 

Frame, Cross 

Head, fluid End 

Stuffing Box 

Relief Valve Body 

Reference 

documents 


specification 

Acceptance 

norms 

ASME Sec-VIII, 

Div 1, Appendix 7 

Record 

Inspection 

report 

Sub 

Vend 

or 

Vend 

or 

WP 

W W - 

- 

1.b Incoming 

Material 


approved 

drawing 

As per vendor 

approved 

drawings 

Inspection 

report 

W W - 

1.c Incoming 

Material 

1.d. 

Incoming 

Material 

Do 

All castings 

materials 

Chemical 

Properties / 

Physical 

properties 

Hardness 


Review of 

manufacturers TC 

Review of HT 

charts 

All heats 

All heats 


material 

specification 


material 

specification 


material 

specification 


material 

specification 

Manufacturers 

TC 

HT chart or 

TC 

W R R 

W R R 

1.e Incoming 

material (Bar 

stock) 

Crank Shaft , 

Connecting & 

Extn. Rods, 

Plunger and Gear 

Blanks 

Chemical 

properties / 

Physical 

properties 

Review of 

manufacturers TC / 

Lab check 

All heats 


material 

specification 


material 

specification 

Manufacturers 

TC or Lab 

report 

W R R 

INSPECTION & TEST PLAN FOR DOSING PUMP 

ITP FOR DOSING PUMP 

435-JH0902-00-ME-ITP-0007 

Page 1 of 4 

Rev. 

C




Sr. 

No. 

1.f Hard ware 

items 


of check 

Gaskets, 

Fasteners, 

Bearing Gland - 

Packing 

2.a. Accessories Volume Bottles & 

Piping l 

Surface Defects Visual As per 

sampling 

plan 

Fabrication 

2.b Accessories Coupling 1. Dimensions 

2. Dynamic 

balancing 

3.a In Process Frame, St. Box 

Cross Head , 

Crank Shaft, 

Connecting Rod, 

Plunger 

Defects open to 

surface 

1) WPS /PQR 

/WPQ 

2) Hydro Test 

3) Radiography 

4) Dimensional 

Check 

5) Material TC 

Reference 

documents 

Approved 

drawings / 

Relevant stds 





1. Measurement 100% 1. As Per 

approved 

drawings 

2. ISO 1940& 

API 610 

D.P examination 

3.b In process Frame Through defects Kerosene Leak 

Test 

3.c In Process Crank Shaft , 

Connecting & 

Extn. Rods , 

Gear Blanks 

Plunger, Fluid 

End & St. Box 

Internal Defects 

Ultrasonic Test 

(Pre Machining 

Stage) 

100% of 

Machined 

surfaces 

100% Oil 

Sump 

ASTM E 165 

Manufacturers 

Drg 

100% ASTM A 388/ 

Written 

approved 

procedure 

Acceptance 

norms 

Approved 

drawings 

/Relevant stds 





1. As Per 

approved 

drawings 

2. ISO 1940 

ASME Sec VIII 

Div-1, Appendix - 

7 

No Leakage / 

Sweating 

Approved 

procedures 

Record 

Inspection 

report 

Manufacturers 

inspection / 

Test report 

Manufacturers 

inspection & 

test records 

Manufacturers 

inspection & 

test records 

Manufacturers 

inspection & 

test records 

Manufacturers 

inspection & 

test records 

Sub 

Vend 

or 

Vend 

or 

WP 

W R R 

W W W/R 

W W R 

- W R 

- W R 

- W W/R 



435-JH0902-00-ME-ITP-0007 

Page 2 of 4 

Rev. 

C




Sr. 

No. 

4.a Test before 

assembly 


of check 

Fluid End. St. 

Box 

1) Inside 

2) Jacket Side 

3) Volume Bottle 

4) Piping 

5.a Testing Assembled Pump 1. Performance 

2. NPSHR 

3. Vibration 

4. Sound 

5. Bearing 

temperature 

rise 

6. Mech. 

Running 

7. R /V Set. Pr. 

Function Test 

Reference 

documents 

Acceptance 

norms 

Record 

Leak Tightness Hydro test Each set API 675. No leakage Manufacturers 

inspection & 

test records 

Measurement 

5.b Testing Dismantled pump Strip examination Visual check of 

Valve Assembly 

& Exposed Portion 

of Plunger 

Each 

pump 

Each 

pump 


inspection & 

test records 


inspection & 

test records 

Sub 

Vend 

or 

Vend 

or 

- W W 

- W W 

- W W 

WP 

5.c Testing Unitised Pump, 

Job Driver, Base 

Frame and 

Instruments 

General 

Arrangement 

Visual & 

Measurement 

Each set 

5.d Testing Instruments Doc. Review Review Each test 

report 

Approved GA 

Drawings 

Approved 

Datasheet 

Approved GA 

Drawings 

Approved 

Datasheet 

Manufacturers 

inspection & 

test records 

Manufacturers 

TC 

- W W 

W W/R R 



435-JH0902-00-ME-ITP-0007 

Page 3 of 4 

Rev. 

C




LEGENDS: 




W- WITNESS 

O- OBSERVED 

R- REVIEW 

H- HOLD 

NOTES: 

1. WELD REPAIR IF ANY TO BE DONE AFTER THE APPROVAL OF THE PURCHASER / AUTHORISED REPRESENTATIVE OF PURCHASER AS PER APPLICABLE CODE AND 

QUALIFIED WPS AND WELDER. 

2. HARD FACING IF REQUIRED SHALL BE DONE THROUGH QUALIFIED WELDERS USING QUALIFIED WPS./PQR. 

3. IF REQUIRED BY PURCHASER FLOW REPEATABILITY AND LINEARITY TESTS SHALL ALSO BE CONDUCTED. 



435-JH0902-00-ME-ITP-0007 

Page 4 of 4 

Rev. 

C


HPCL Guru Gobind Singh Refinery 

Products Evacuation Project (GGSRPEP) 

Site & Utility Data 

435-JH0902-10-ME-SPC-0007 

25 May 2009 





Phone: +91-22-67818000 

Fax : +91-22-67818080 





GENERAL SITE & UTILITY DATA 

SYNOPSIS 

Disclaimer 











PARSONS 

APPROVAL 

DATE 

CLIENT 

APPROVAL 

A - N/A 

DATE 

B 


Subramanyam 

.S 

Sameer 

Ishwad 

Anil Kumar 

29-Apr-09 

N/A 

C 


Subramanyam 

.S 

Sameer 

Ishwad 

Jeremy 

Wallace 

16-July-09 

Page ii





Ramanmandi to Bahadurgarh Pipeline. 



from the upcoming Guru Gobind Singh Refinery at Raman Mandi to HPCL’s existing terminal 

in Bahadurgarh. The length of the pipeline is approximately 243 Km. The pipeline is planned 

to transfer EURO-III MS,EURO-IV MS,EURO III HSD EURO IV HSD,SKO, Naphtha & ATF 




Bahadurgarh 

2011-2012 / Phase-I 3.96 

2021-2022 / Phase – II 4.71 



through variable speeds. 


One Multi product Pipeline from GGSR Raman Mandi is proposed to be layed to HPCL’s 







The project requirement for the Raman Mandi to Bathinda pipeline is to transport 0.929 

Million Metric Tones Per Annum (MMTPA) of EURO – III MS, EURO – III HSD and SKO in 

the Year 2011-12 (Phase-I) and 1.375 MMTPA of the products in the Year 2021-22 (Phase-II) 

Suitable tap off facility shall be provided at Bathinda for extension of the pipeline to Sangrur in 

future. The pipeline throughput shall be as follows: 

Page iii of 8 

21 May2009




Pipeline Section Year / Phase Throughput in Million Metric 

Tons per Annum (MMTPA) 




2011 – 2012 / Phase - I 0.929 

2021 – 2022 / Phase - II 1.375 

2011 – 2012 / Phase - I 0.470 

2021 – 2022 / Phase - II 0.697 


1.375 MMTPA (Phase - II). However, the pump/driver will be designed such that presently it shall 

cater to the requirement of Phase-I throughput of Bathinda alone. Space provision shall be made for 

additional pumps to be installed at a later date to cater the requirement of Phase – II throughput for 

the volumes upto Sangrur. To cater for more than one flowrate and different densities / viscosities 

pumps have to run at lower speed through Variable Frequency Drives (VFD). 

Table 1. Salient features of the Raman Mandi- Bahadurgarh Pipeline Project 

S.No. Feature Details 

1 Total Length 250 km long 18’’ Dia 

2 Diameter of the pipeline 18” 

3 Pump Station 1 

4 Line fill 41060 KL 

5 Products to be transported Euro III MS, Euro III HSD, Euro IV 

6 Throughput (MMTPA 

2011-12 

MS ,Euro IV HSD, ATF& 

, SKO 

3.96 

2021-22 4.71 

7 Location Type 

originating Proposed Pumping Station 

Raman Mandi 

New 

Chainage 

0.0 Kms. 

Latitude 29°-55’-51” 

Longitude 74°-57’-22’’ 

Page iv of 8 

21 May2009




Elevation 

Bahadurgarh 

Temperature & Pressure: 

Average rainfall maximum shade temperature 

Maximum recorded shade temperature 

Average annual minimum shade temperature 

Minimum recorded shade temperature 

Maximum external surface temperature (Direct 

exposure to sun) 

Relative Humidity 

Annual average humidity 

Absolute maximum humidity 

Absolute minimum humidity 

203.53 Mts.MSL 

Existing 

35 deg. C 

41 deg. C 

12 deg.C 

6 deg.C 

45 deg.C 

70% 

90% 

5% 

Note- The maximum humidity of 90% is 

possible in any month throughout the year. 

Rainfall 

Average annual rainfall 

Maximum recorded annual rainfall 

Minimum recorded rainfall 

350 mm 

1250mm 

126mm 

8 Tap Off Station Raman Mandi No 

Existing Receiving Station & delivery to 

existing Marketing Terminal at 

Bahadurgarh 

Yes 

Chainage 

250 Kms. 

Latitude 28°-43’-37’’ 

Longitude 76°-51’-28’’ 

Elevation 

215.589 Mts. MSL 

Features of the Raman Mandi- Bahadurgarh route 

9 Canal crossings: Distributaries, 

22 

Main/Branch 

Canals/minors 26 

Page v of 8 

21 May2009




10 Forest Length Nil. However, ROU of roads and 

canals are protected forests. 

11 Drains & Nallahs 03 

12 Rail crossings 05( B.G.) 

13 River 1 

14 Highway / Road crossings 

Super Express 1 

NH 02 

SH 03 

MDR /ODR/ other 40 

15 Environmentally sensitive areas within project 

None 

area 

16 States Enroute Punjab & Haryana 

17 Districts Enroute Bathinda in Punjab; Sirsa, Mansa, 

Fatehabad, Jind, Rohtak & Jhajjar 

in Haryana 

Table 2. Salient features of the Raman Mandi- Bathinda Pipeline Project 

S.No. Feature Details 

1 Total Length 30 km 

2 Diameter of the pipeline 10” 

3 Pump Station 1 

4 Line fill 1520KL 

5 Products to be transported Euro III HSD , Euro IIIMS ,SKO. 

6 Throughput (MMTPA 

, 0.93 SKO 

2011-12 

2021-22 1.37 

7 Location Type : 

New ( Chainage0.0) 

Originating Proposed Pumping Station & 

Storage Terminal at Raman Mandi 

Page vi of 8 

21 May2009




Proposed Receiving Station& delivery to 

existing Marketing Terminal at Bathinda 

Existing (Chainage-30.0 Kms.) 

Latitude 29°55’51’’ 

Longitude 74°57’22’’ 

Elevation 

Temperature & Pressure: 

Average rainfall maximum shade temperature 

Maximum recorded shade temperature 

Average annual minimum shade temperature 

Minimum recorded shade temperature 

Maximum external surface temperature (Direct 

exposure to sun) 

Relative Humidity 

Annual average humidity 

Absolute maximum humidity 

Absolute minimum humidity 

203.53 Mts.MSL 

35 deg. C 

41 deg. C 

12 deg.C 

6 deg.C 

45 deg.C 

70% 

90% 

5% 

Note- The maximum humidity of 90% is 

possible in any month throughout the year. 

Rainfall 

Average annual rainfall 

Maximum recorded annual rainfall 

Minimum recorded rainfall 

350 mm 

1250mm 

126mm 

8 Tap Off Station Raman Mandi No 

Bathinda 

Yes 

Latitude 30°09’31’’ 

Longitude 74°59’04’’ 

Elevation 

206.15 Mts above MSL 

Features of the Raman Mandi- Bathinda route 

9 Canal crossings 6 

Page vii of 8 

21 May2009




10 Forest Length Nil. However, ROU of roads and 

canals are protected forests. 

11 Drains & Nallahs 01 

12 Rail crossings 01( B.G.) 

13 Highway / Road crossings 

NH 

Nil 

SH 01 

MDR /ODR/ other Pucca roads 08 

14 Environmentally sensitive areas within project None 

Table 3. Power Supply Arrangement at Ramanmandi 

Station Source Back up DG Set for Emergency Power (KVA) 

Ramanmandi 

33 KV, 6.6 KV & 

415 V 

250 KVA AT 415 V 

Bathinda 415 V, 3 PH 25 KVA at 415 V 

Bhadurgarh 

Sectionalizing 

valve station 

415 V, 3 PH 

230 V, 1 PH 25 KVA, 1 PH 

Page viii of 8 

21 May2009



MANDATORY SPARE PARTS FOR STATIC EQUIPMENT 






0435-JH0902-00-ME-SPL-004 

25-Aug-09 





Phone: +91-22-67818000 

Fax : +91-22-67818080 



0435-JH0902-00-ME-SPL-004 Rev C Page 1 of 3




SYNOPSIS 

Disclaimer 



between Hindustan Petroleum Corporation Limited (HPCL) and WorleyParsons. 

WorleyParsons accepts no liability or responsibility whatsoever for it in respect of any use of or 

reliance upon this report by any third party. 



PROJECT 435/JH0902 - HPCL GURU GOBIND SINGH REFINERY PRODUCTS EVACUATION PROJECT 


REV DESCRIPTION PREPARED 

BY 

CHECKED 

BY 

APPROVED 

BY 

DATE 

CLIENT 

APPROVAL 

DATE 

A Issued for IDC Harshal 

Sasthe 

S. Ishwad J. Wallace 

02 July 09 

B 

Issued for 

Review 

Harshal 

Sasthe 

S. Ishwad J. Wallace 

20 July 09 

C 

Issued for 

Tender H. Sasthe S. Ishwad KMN Pillai 

25-Aug-09 





1. MANDATORY SPARE PARTS FOR PRESSURE VESSELS 

Sr. No. Part Description Quantity Required 

1. Bolting for each nozzle with 

10% (Minimum 2 sets) 

blind/companion flange and for each 

pad nozzle 

2 Gasket for each nozzle with 

200% 

blind/companion flange and for each 

pad nozzle 

3. Bolting for Internal Flanges 10% (Minimum 2 sets) 

4. Gasket for each Internal Flange 200% 

5. Sight/Light glasses assembly complete 

with bolting and gasket 

Four Sets 


1 Tag No. : P-20-03 Client: HINDUSTAN PETROLEUM CORPORATION LTD 

2 Service: TRANSFER OF SLOP & INTERFACE 

Plant Location: BATHINDA, PUNJAB 

3 P & ID No. : 435-JH0902-10-PR-PID-2004 REV D Manufacturer: 

4 Calculation Ref.: 435-JH0902-20-PR-CAL-0001 REV A Purchase Order No. : 

5 No. of Units: 1 Criticality Rating: 

6 Service Description: TRANSFER OF SLOP & INTERFACE Service Category: (3.64) 

7 

8 

9 

10 PLEASE REFER THE PROCESS DATA GIVEN ON PAGE 1OF 4 

11 

12 

13 

14 

15 

16 

17 

18 

19 

20 

21 

22 

23 

24 

25 

26 

27 

28 

29 

30 

31 

32 

33 

34 

35 

36 

37 

38 

39 

40 

41 

42 

43 

44 

45 

46 

47 

48 

49 

50 

51 

52 

53 

54 

55 

56 

57 

58 

59 

60 

61 

62 

63 

64 

65 

66 

67 

c 

B 

Equipment Data Sheet for Centrifugal Pump 

25-Aug-09 Issued for Tender SS SVI KMNP 

13-Aug-09 

13-Aug-09 

ISSUED FOR REVIEW 

ISSUED FOR SQC / DIC 

REMARKS 

A 

Rev. Date Issue Description Originated Checked Approved Client 

SS 

SS 



Project Ref: 0435-JH0902 

SVI 

SVI 

Datasheet No:0435-JH0902-20-ME-DAS-0022 

KMNP 

KMN 

Sheet 

2 of 4 

DRIMS#: 2009558

The drawing, design and details given on this format are the property of WorleyParsons Engineering Pvt. Ltd. They are merely loaned on the borrower’s express agreement that 

they will not be reproduced, copied, exhibited or used, except in the limited way permitted by a written consent given by the tender to the borrower for the intended use. 

Sr. 

No. 

Stage Component Characteristics Method of 

check 

Quantum 

of check 

Reference 

documents 

1. Incoming Casing 


Material Stuffing Box 

specification 

(Castings) Impeller 

Bearing Housing 

Acceptance 

norms 

ASME Sec- 

VIII, Div 1, 

Appendix 7 

Record 

Inspectio 

n report 

Sub Vendor WP 

Vendor 

W W - 


Material 


approved 

drawing 

As per 

vendor 

approved 

drawings 

Inspectio 

n report 

W W - 


Material 


Material 

Do 

All castings 

materials & Forging 

materials 

Chemical / Physical 

properties 


Review of 

manufacturers 

TC 

Review of HT 

charts 

All heats 

All heats 


material 

specification 


material 

specification 

As per 

relevant 

material 

specification 

As per 

relevant 

material 

specification 

Manufact 

urers TC 

HT chart 

or TC 

W R R 

W R R 


material 

(Bar stock) 

Shaft material Chemical properties / 

Physical properties 

Review of 

manufacturers 

TC / Lab check 

All heats 


material 

specification 

As per 

relevant 

material 

specification 

Manufact 

urers TC 

or Lab 

report 

W R R 

ITP FOR HORIZONTAL CENTRIFUGAL PUMPS 

ITP FOR MAIN PUMP 

0435-JH0902 -00- ME-ITP-0009 

Page 1 of 8 

Rev. 

C



Sr. 

No. 


check 

5. Hard ware Gaskets, Fasteners, Suitability Test 

Visual review or 

items Gland packings, certificates 

Test reports or 

valves 

certificates 

Quantum 

of check 

As per 

sampling 

plan 

Reference 

documents 

Approved 

drawings and 

datasheets & 

Relevant stds 

Acceptance 

norms 

Approved 

drawings and 

datasheets & 

Relevant stds 

Record 

Inspectio 

n report 

Sub Vendor WP 

Vendor 

W R R 

6. Accessories Mechanical seal Hydrotest 

Leakage test 

Air test 


liquid reservoir (if 

applicable) 


liquid Coolers (if 

applicable) 

1. WPS / PQR/WPQ 


3. Dimensional check 


1. WPS / PQR/WPQ 


3. Dimensional check 


9. Accessories Coupling 1. Dimensions 

2. Dynamic balancing 

Hydotest 

Air test 


leakage 


2. Hydro test 

3. Measureme 

nt 



2. Hydro test 

3. Measureme 

nt 


1. Measureme 

nt 

Type test As per API 682 API 682 and 

seal 

manufacture 

rs drawing 






drawings. ASMe 



100% 1. As Per 

approve 

d 

As per 

approved 

drawings. 

ASME 

Section II / 

Sec-VIII, div- 

1 / IX 

As per 

approved 

drawings. 

ASMe 

Section II / 

Sec-VIII, div- 

1 / IX 

1. As Per 

approved 

drawings 

Manufact 

urers 

inspectio 

n / Test 

report 

As per 

Manufact 

urers test 

record & 

Inspectio 

n record 

As per 

Manufact 

urers test 

record & 

Inspectio 

n record 

Manufact 

urers 

inspectio 


W R R 

W W W/ 

R 

W W W/ 

R 

W W R 

Rev. 


0435-JH0902 -00- ME-ITP-0009 

Page 2 of 8 

C



Sr. 

No. 


check 

10. Accessories Bearing Lube oil 

console (if 

applicable) 

11. In Process Casing 

Impeller 

Stuffing Box 

12. In process Butt Weld joint (if 

applicable) 

Suitability 

1. Pressure 

test 

2. Cleanliness 

test 

3. Operational 

test 

4. Material TC 


for Lube oil 

Pump & 

motor 


for 

instruments 

Defects open to surface D.P examination 100% of 

Machined 

surfaces 

Internal defects Radiography On Nozzle 

to casing 

Quantum Reference 

of check documents 

drawing 

s 

2. ISO 

1940& 

API 610 

100% As Per approved 

drawings 

/datasheets & 

API 614 

ASTM E 105 

ASME Sec V 

Article 2 

Acceptance 

norms 

2. ISO 

1940& 

API 610 

As Per 

approved 

drawings 

/datasheets 

& API 614 

ASME Sec 

VIII Div-1, 

Appendix -7 

ASME Sec 

VIII Div -1 

Record 

n & test 

records 

Manufact 

urers 

inspectio 

n & test 

records 

Manufact 

urers 

inspectio 

n & test 

records 

Manufact 

urers 

Sub 

Vendor 

Vendor 

WP 

W W W 

- W R 

- W R 



0435-JH0902 -00- ME-ITP-0009 

Page 3 of 8 

Rev. 

C



Sr. 

No. 


check 

13. In Process Shaft 

Forged outer casing 

14. WPS,PQR, 

WPQ 

previous 

qualificatio 

ns for 

overlay 


assembly 


assembly 

Wear rings 

Pump Outer stage 

Casing & Stuffing 

box 

Shaft (as 

applicable) 

1.Internal Defects 

2. Surface defects 

Thickness of overlay, 

Hardness 

1. Ultrasonic 

Test. 

2. 2. Magnetic 

particle 

testing. 

3. 3. Liquid 

penetrant 

testing 

Visual & 

Hardness 

Measurement 

Quantum 

of check 

Reference 

documents 

Acceptance 

norms 

Record 

joint UW 51 inspectio 

n & test 

records 

100% 1. ASTM A Approved Manufact 

388/ procedures urers 

Written 

inspectio 

approved 

n & test 

procedure 

records 

2. ASTM E 709 

3. ASTM E 165 

100% Specifications, 

WPS,PQR,WPQ 

Leak Tightness Hydro test Each set API 610 & 

approved drgs. 

Demagnetisation & 

Measurement of Mech. 

& Elect. Runout 

Measurement Each set Approved drgs. 

& API 670 

Specification 

s, 

WPS,PQR,W 

PQ 

No leakage 

API 670 

Manufact 

urers 

WPS,PQR, 

WPQ 

Records 

Manufact 

urers 

inspectio 

n & test 

records 

Manufact 

urers 

inspectio 

n & test 

Sub 

Vendor 

Vendor 

WP 

W W/ 

R 

- W R 

- W W 

- W R 



0435-JH0902 -00- ME-ITP-0009 

Page 4 of 8 

Rev. 

C



Sr. 

No. 


assembly 


check 

Rotor Assembly 

with coupling Half 

(as applicable) 

Quantum 

of check 

Dynamic balancing Measurement Each 

rotor 

18. Testing Assembled Pump 1. Performance 

2. NPSHR 

3. Vibration 

4. Sound 

5. Bearing temperature 

rise 

6. Mech. Running 

Measurement 

19. Testing Dismantled pump Strip examination Visual check 

Wear Ring 

Clearance 

measurement 

20. Testing Unitised Pump, Job 

Motor, Jack 

Screws, Base 

frames, 

instruments along 

with lube oil 

console 

String test 


sound, 

temperature 

rise, Vibration 

Each 

pump 

Each 

pump 

Each set 

Reference 

documents 

Acceptance 

norms 

Record 

records 

ISO 1940 ISO 1940 Manufact 

GR.2.5 urers 

inspectio 

n & test 

records 

API 610 API 610 Manufact 

urers 

inspectio 

n & test 

records 

API 610 API 610 Manufact 

urers 

inspectio 

n & test 

records 

Approved GA & 

API 610 

Approved GA 

& API 610 

Manufact 

urers 

inspectio 

n & test 

records 

Sub 

Vendor 

Vendor 

- W O 

WP 

- W W 

- W W 

- W W 



0435-JH0902 -00- ME-ITP-0009 

Page 5 of 8 

Rev. 

C



Sr. 

No. 


check 

Quantum 

of check 

Reference 

documents 

Acceptance 

norms 

Record 

21. Testing Auxiliary piping Leak tightness Hydro test Each set No leakage No Leakage Manufact 

urers 

inspectio 

n & test 

records 

22. Testing Base plate Dimensions Measurement Each Approved GA Approved GA Manufact 

plate drgs. 

drgs. urers 

inspectio 

n & test 

records 

23. Testing Instruments Doc. Review Review Each test Approved Approved Manufact 

24. Testing Rotor assembly Torsional Analysis & 

Lateral analysis 

Computational 

analysis 

report Datasheet Datasheet urers TC 

Type test API 610 API 610 Computat 

ional 

analysis 

print outs 

Sub 

Vendor 

Vendor WP 

- W W 

- W W 

W W/R R 

- R R 



0435-JH0902 -00- ME-ITP-0009 

Page 6 of 8 

Rev. 

C



Legends: 




W- WITNESS 

O- OBSERVED 

R- REVIEW 

H- HOLD 

NOTES: 

1. WELD REPAIR IF ANY TO BE DONE AFTER THE APPROVAL OF THE PURCHASER / AUTHORISED REPRESENTATIVE OF PURCHASER AS PER APPLICABLE CODE AND QUALIFIED 

WPS AND WELDER. 

2. MATERIAL FOR LOW TERMPERATURE SERVICE TO BE IMPACT TESTED AS PER APPLICABLE SPECIFICATION 

3. FOR AUSTENITIC STAINLESS STEEL MICRO STRUCTURE AND IGC TESTS TO BE CONDUCTED AS PER APPLICABLE CODE & PURCHASE REQUISITION 

4. FOR DUPLEX STAINLESS STEEL MICROSTRUCTURE & HARDNESS TO BE EXAMINED AS PER APLICABLE CODE 

5. LUBE OIL CONSOLE IS APPLICABLE WHERE PRESSURE LUBRICATION IS REQUIRED FOR BEARINGS 

6. STRING TEST OF THE PUMPS ALONG WITH FUNCTIONAL TEST FOR ALL AUXILLIRES SHALL BE CONDUCTED IN THE SHOP USING JOB MOTOR & LUBE OIL CONSOLE & 

BASEFRAME 

7. OUTER CASING IS APPLICABLE ONLY IN CASE OF DOUBLE CASING BARREL TYPE PUMP. 

8. INCASE OF HORIZONTALLY SPLIT CASING MULTISTAGE PUMP. STAGE CASING IS NOT APPLICABLE. 



0435-JH0902 -00- ME-ITP-0009 

Page 7 of 8 

Rev. 

C



9. MECHANICAL RUN TEST SHALL BE AS DESCRIBED IN THE SPECIFICATION FOR SLOP/INTERFACE PUMPS. 

10. HARD FACING OF WEAR RINGS SHALL BE AS PER APPROVED CROSS SECTIONAL DRAWING/ DATASHEET 

11. PUMP DRIVER SHALL BE INSPECTED AT DRIVER MANUFACTURERS SHOP AS PER RELEVANT INSPECTION & TEST PLAN 

12. PERFORMANCE TOLERANCES SHALL BE AS PER API 610 10 TH EDITION & SPECIFICATION FOR SLOP/ INTERFACEPUMPS. 



0435-JH0902 -00- ME-ITP-0009 

Page 8 of 8 

Rev. 

C

PROJECT TITLE: 

GGSR PRODUCT EVACUATION PROJECT 

(HINDUSTAN PETROLEUM CORPORATION LTD.) 

DOCUMENT TITLE: 

Mechanical Datasheet for Sump Tanks- 

T-10-01 / T-10-02 

TAG NO. - T-10-01 / T-10-02 

DOCUMENT NO. : 

0435-JH0902-10-ME-DAS-0009 

C 

B 

A 

Rev. No 

ISSUED FOR TENDER 

ISSUED FOR REVIEW 

ISSUED FOR IDC 

Description 

HS 

SVI KMN P. 

01/09/09 

HS 

SVI 

JJW 

07/07/09 

HS SVI JJW 01/07/09 

Prepared By Checked By App. By 

Date 

DOC NO. : 0435-JH0902-10-ME-DAS-0009 REV NO. : C Sheet 01 of 03

DOC TITLE: Mechanical Datasheet for Sump Tanks-T-10-01/02 


Tag No. T-10-01 / T-10-02 

DOC NO. : 0435-JH0902-10-ME-DAS-0009 REV NO. : C (HINDUSTAN PETROLEUM CORPORATION LTD.) 

GENERAL DATA 

Date: 01/09/09 

1 Equipment 

Sump Tank 

2 Equipment tag no. 

T-10-01 / T-10-02 

3 Type / Position 

Horizontal Cylindrical 

4 Quantity 

2 

5 Location 

Outdoor 

6 Operation 

Intermittent 

7 

8 Fluid 

OPERATING CASE 

Hydrocarbon (Euro-III MS, Euro-IV MS, Euro-III HSD, Euro-IV HSD, SKO,ATF, Naptha) 

9 Capacity (Working) m 3 20 

10 Capacity (Actual) m 3 24.3 

11 Density kg/m 3 650-860 

12 Operating Pressure kg/cm 2 ATM 

13 Operating Temperature °C 25 

14 Viscosity: cP EURO-IV MS 

0.4 @ 37.8 ° C 0.54 @ 20° C 

15 

EURO-III MS 

0.4 @ 37.8 ° C 0.54 @ 20° C 

16 

EURO-III HSD 

1.7-4.3 @ 40° C / 7 @ 20° C 

17 

EURO-IV HSD 

1.7-4.3 @ 40° C / 7 @ 20° C 

18 

SKO 

0.75 @ 100 ° C / 1.34 @ 40 ° C 

19 

ATF 

1 @ 37.8 ° C / 41.3 @ 20° C 

20 

NAPTHA 

0.4 @ 37.8 ° C / 0.52 @ 20 ° C 

21 Flash Point ° C EURO-IV MS

DOC TITLE: Mechanical Datasheet for Sump Tanks-T-10-01/02 

DOC NO. : 0435-JH0902-10-ME-DAS-0009 

58 

59 

60 

61 

62 

63 

64 

65 

66 

67 

68 

69 

70 

71 

72 

73 

74 

75 

76 

77 

78 

79 

80 

81 

82 

83 

84 

85 

86 

87 

88 

89 

90 

91 

92 

93 

94 

95 

96 

97 

98 

99 NOTES: 

100 1. ALL DIMENSIONS ARE IN mm UNLESS OTHERWISE SPECIFIED. 

101 2. ALL NOZZLE FLANGE DIMENSIONS SHALL BE AS PER ANSI B-16.5,150#. 

102 3. VENDOR IS FREE TO USED BETTER MATERIAL OPTION. 

103 4. VTS - VENDOR TO SPECIFY. 

104 5. VENDER SHOULD SUPPLY BOOT DETAILS 

105 6. VENT TO BE PROVIDE WITH FLAME ARRESTOR. TO BE VENTED AT MIN 3M ABOVE THE NEAREST OPERATIONAL PLATFORM 

106 OR PIPERACK WHICHEVER IS HIGHER 

107 7. FOR PAINTING AND COATING SPECIFICATIONS REFER DOC. NO. 0435-JH0902-00-PI-SPC-0003 

108 

109 

110 

111 

112 

113 

114 

115 

116 

117 

118 

119 

REV NO. : C 


(HINDUSTAN PETROLEUM CORPORATION LTD.) 

NOZZLE SCHEDULE 

Flange 

NOZZLE 

Nozzle Nominal 

Service 

STANDARD 

QTY 

Size 

PROJECTION FROM 

Number Rating Type 

ELEVATION 

OUTSIDE OF 

ORIENTATION 

SHELL/HEAD PLATE 

B1 VTS 1 150# SO RF Pump Motor 

B 16.5 VTS 

VTS 

VTS 

B2 2" 1 150# SO RF Recirculation 

B 16.5 VTS 

VTS 

VTS 

B3 6" 1 150# SO RF Sampling Connection 

B 16.5 VTS 

VTS 

VTS 

B4 2" 1 150# SO RF Pressure relief 

B 16.5 VTS 

VTS 

VTS 

B5 4" 1 150# SO RF vent 

B 16.5 VTS 

VTS 

VTS 

Closed drain inlet 

B6 4" 1 150# SO RF (From Bahadurgarh Drain 

B 16.5 

VTS 

Header) 

VTS 

VTS 

B7 4" 1 150# SO RF 

Closed drain inlet 

B 16.5 

(From Bathinda Drain Header) 

VTS 

VTS 

VTS 

B8 2" 1 150# SO RF Level Transmitter B 16.5 VTS 

VTS 

VTS 

B9 3" 1 150# SO RF To Tank Truck Loading 

B 16.5 VTS 

VTS 

VTS 

M1 24" 1 150# PLATE Manhole 

B 16.5 VTS 

VTS 

VTS 

S1 2" 1 150# SO RF Spare With B/F 

B 16.5 VTS 

VTS 

VTS 

VESSEL SKETCH 

Tag No. T-10-01 / T-10-02 

Date: 01/09/09 

Remarks 

DOC NO. : 0435-JH0902-10-ME-DAS-0009 REV NO. : C Sheet 03 of 03

GGSR Product Evacuation Project - WorleyParsons.com

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