- Design pressure <strong>for</strong> high ----------------------------------pressure portion, bar- Working pressure at superheater ----------------------------------outlet, bar- Working pressure at HRSG ----------------------------------steam drum, bar- Static head, drum water level to ----------------------------------economiser inlet, bar- Working pressure at economiser, bar ----------------------------------(2) at Partial Load(Gas Turbine output at Site Condition)100% 75% 50% 25%- Exhaust gas flow, kg/hr ------- ------- ------- -------- Exhaust gas temp., 0 C ------- ------- ------- -------- Steam Output, kg/hr ------- ------- ------- -------- Superheater exit pressure, bar ------- ------- ------- -------- Superheater exit temp., 0 C ------- ------- ------- -------- Feed Water temp. at ------- ------- ------- -------economiser inlet, 0 C- Pinch point temp., 0 C ------ ------- ------- -------- Approach temp., 0 C ------- ------- ------- -------Gas TemperatureSuperheater inlet, 0 C ------- ------- ------- -------Evaporator inlet, 0 C ------- ------- ------- -------Economiser outlet, 0 C ------- ------- ------- -------3.3 Operating Limit- Max. gas temperature atsuperheater inlet during start-up, 0 C ----------------------------------- Max. superheater metal temperature atduring start-up, 0 C ----------------------------------- Max. drum metal differentialtemperature during pressure raising, 0 C ----------------------------------- Max. rate <strong>of</strong> decrease insaturation temperature, 0 C ----------------------------------- Max. water temperature be<strong>for</strong>edraining HRSG, 0 C ----------------------------------- Max. superheater steam pressure, bar ---------------------------------<strong>Ghorasal</strong> <strong>300</strong>-<strong>450</strong> <strong>MW</strong> CCPP Project (Vol-2B <strong>of</strong> 2 ) 16
- Max. superheater steam temp., 0 C ----------------------------------- Min. load <strong>for</strong> superheater spray, % ----------------------------------- Max. casing design pressure, mm Aq. ----------------------------------3.4 Evaporator Section- Manufacturer, country ----------------------------------- Heating surface, m 2 ----------------------------------- Heat absorbing rate, kj/m 2 /hr ----------------------------------- Method <strong>of</strong> joining long tubes ----------------------------------- Method <strong>of</strong> fixing tubes to header oror drum ----------------------------------- Tube outside diameter, mm ----------------------------------- Tube thickness, mm ----------------------------------- Tube pitching, mm ----------------------------------- Casing thickness, mm ----------------------------------3.5 Drum- Manufacturer, country ----------------------------------- <strong>Construction</strong> ----------------------------------- Internal diameter, mm ----------------------------------- Thickness, mm ----------------------------------Length, mm ----------------------------------Steam purifier,Manufacturer, countryType- Design pressure, bar ----------------------------------Operating pressure, bar ----------------------------------3.6 Safety Valve- Manufacturer, country ----------------------------------1) <strong>for</strong> Drum- Type ----------------------------------Number ----------------------------------Size <strong>of</strong> valve, mm ----------------------------------Capacity, kg/hr ----------------------------------Design lifting pressure, bar ----------------------------------2) <strong>for</strong> superheater- Type ----------------------------------Number ----------------------------------<strong>Ghorasal</strong> <strong>300</strong>-<strong>450</strong> <strong>MW</strong> CCPP Project (Vol-2B <strong>of</strong> 2 ) 17
- Page 2: 1. Schedule PageSchedule-A Guarante
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- Page 8 and 9: Man-hours for :Minor inspectionNorm
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- Page 14 and 15: - Auxiliary relays ----------------
- Page 18 and 19: Size of valve, mm -----------------
- Page 20 and 21: Shaft -----------------------------
- Page 22 and 23: - Number of exhaust ---------------
- Page 24 and 25: - Scheme for turbine drainage andau
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-Manufacturer, Country ------------
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1) Grades of Steel ----------------
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B-23 Water Treatment Plant.The quan
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Sl.No.Description of the main desig
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12. ION EXCHANGER UNITS : CATION UN
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16. CAUSTIC SODA STORAGE TANK andME
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Name of items15. Centrifuging machi
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Name of the items28. Pot. metabisul
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HRSG- Feed water correction plant-
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SCHEDULE - ETOOLS AND APPLIANCESThe
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SCHEDULE-FSpares & consumables duri
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W.1.1.32 Cable Arrangment, Comb. Ch
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W.1.1.38 Piping Rack, RightSl No.It
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W.1.1.47.1 Seal Ring 8 PCW.1.1.47.2
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W.1.4.6.1 Tmg-Gasket 2 PCPriceW.1.4
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M.1.1.34.3 Disk 20 PCM.1.1.56 Exhau
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No.i) O’ Ringii) O’ Ringiii) O
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No.Item Quantity Unitprice(CIF)B. I
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Spares & Service during Long Term S
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SCHEDULE - HCIVIL AND BUILDING WORK
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SCHEDULE - ILIST OF SUBCONTRACTORST
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SCHEDULE - KMOBILISATION AND DEMOBI