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Crossover Main Replacement - Coke Oven Managers Association

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Matthew John<br />

<strong>Crossover</strong> <strong>Main</strong> <strong>Replacement</strong> Project


Introduction<br />

• Morfa <strong>Coke</strong> Making plant is an Otto Simon Carves’ Twin<br />

Flue Underjet Compound design with twin collector<br />

mains.<br />

• The <strong>Oven</strong>s were comissioned in 1981 and consists of 84<br />

ovens (2 batteries of 42 ovens).<br />

• As part of the coke making process, volatile gases<br />

released from the coal during the carbonisation process<br />

are exhausted from the ovens to a By-Product plant, via a<br />

gas recovery pipe work system referred to as “crossover<br />

mains” There are four crossover mains in total, two per<br />

battery.<br />

2


Introduction<br />

After 33 years of uninterrupted service, each crossover has<br />

typically seen in the region of 1.45 billion m 3 of coke oven gas.<br />

The system has already surpassed its original design life by<br />

some 8 years and the pipe work was in poor condition.<br />

3


Introduction<br />

Due to the poor condition of the pipe work and the losses of<br />

containment, we were faced with three options.<br />

1. Repair the current pipe work by “over plating”.<br />

2. Remove the <strong>Coke</strong> side Gas Collecting <strong>Main</strong> and<br />

“<strong>Crossover</strong> mains” altogether and operate the plant on a<br />

single Gas Collecting <strong>Main</strong>.<br />

3. Remove the <strong>Crossover</strong> mains and replace with new.<br />

4


Introduction<br />

The first two options were not viable, firstly each of the<br />

crossover mains had previously been “over-plated”, and this<br />

would only prove to be a short-term repair.<br />

Secondly even though it was possible to operate the plant on<br />

a single Gas Collecting <strong>Main</strong> the operating tolerances were<br />

too fine, due to the size of our oven design and size of out<br />

Ascension pipes.<br />

Stopping the coke making process to replace these crossover<br />

mains was not an option, so plans were put together to<br />

change all four mains on a “live gas” system.<br />

This is believed to be a first for Tata Steel Europe if not<br />

worldwide.<br />

5


Planning Phase<br />

The planning phase was key to the success of this project.<br />

A project team was formed which was collaboration between<br />

both Process and Engineering personnel from the <strong>Coke</strong> oven<br />

department, Process Safety personnel and personnel from<br />

the Project department.<br />

A master schedule was produced and a weekly status review<br />

plan was used to provide an easy to read breakdown of the<br />

imminent tasks.<br />

6


Planning Phase<br />

Health and Safety<br />

Safety was the main priority of this project and to ensure<br />

there weren’t any accidents, there were a number of safety<br />

measures taken.<br />

The project was carried out in accordance with CDM<br />

regulations and F10 notification was issued to the HSE.<br />

The project team were nominated as both CDM Co-ordinator<br />

and Principal Contractor.<br />

7


Planning Phase<br />

Health and Safety<br />

Due to the hazards involved with this project a huge amount<br />

of time and effort was invested in Hazard Identification and<br />

Process Hazard Analysis.<br />

Event trees were constructed to provide good clear<br />

visualisation of the events requiring mitigation, this helped to<br />

develop a comprehensive Process Hazard Analysis.<br />

8


Planning Phase<br />

Assembly Drawings<br />

An assembly drawing was constructed covering the entire<br />

scope of the installation including over-plating, temporary<br />

platforms and the interconnection pipe work<br />

9


Planning Phase<br />

‘Mock-up’ trial<br />

Another crucial part of the planning phase was the<br />

construction of a ‘mock-up’, simulating the blanking spade<br />

insertion and removal process.<br />

The mock-up included:<br />

•The blanking spade<br />

•Clamping ring concept<br />

•Jacking steel work<br />

•Guide cradle<br />

•and protective curtain.<br />

10


Preparation Phase<br />

Jacking Steelwork & Over plating<br />

Before any work could be started a substantial amount of<br />

preparation was required.<br />

Large areas of the collector mains required over plating to<br />

ensure there was enough “mechanical strength” to carry out<br />

the replacement task.<br />

Additional steelwork was erected to provide “jacking points”<br />

for splitting the flanges with hydraulic jacks.<br />

Pressure control and purging operations<br />

Nitrogen purge points and re-circulating gas stabbings were “hottapped”<br />

into the crossover mains to facilitate pressure control and<br />

purging operations.<br />

11


Preparation Phase<br />

Ground preparation of surrounding areas<br />

Calculations made during the planning phase of the project<br />

considered the weight of each crossover main assuming they<br />

were totally blocked with heavy tar deposits.<br />

“Gas flow” testing was also conducted as part of the planning<br />

phase; this indicated that each of the crossover mains was<br />

substantially blocked.<br />

The weight of each main was calculated to be approximately<br />

40 tonnes, which resulted in the requirement for an 800T<br />

crane.<br />

Ground surveys were performed in the two crane location<br />

areas and the ground was prepared in readiness for the<br />

arrival of the crane.<br />

12


Preparation Phase<br />

Spreader beam<br />

Due to the visibly poor condition of the existing crossover<br />

mains, there was real concern that the horizontal section of<br />

the main could collapse under it’s own weight during the<br />

removal process.<br />

Therefore a bespoke “spreader beam” was designed and<br />

manufactured, that supported the pipe at one-metre pitches to<br />

mitigate this problem.<br />

13


Preparation Phase<br />

<strong>Coke</strong> “Dump Wharf”<br />

The crane location for the work carried out on number two<br />

battery, prevented the use of the existing <strong>Coke</strong> “dump wharf”.<br />

This was recognised during the planning phase and a new<br />

“emergency coke dump wharf” was constructed.<br />

14


Preparation Phase<br />

Interconnecting pipe work<br />

Preparation had to be made for each battery to operate on a<br />

single crossover main while one was being replaced.<br />

This was achieved by the installation of interconnection pipe<br />

work and valves, which enabled the gas make to be re-routed<br />

to the adjacent Gas collecting main.<br />

A pipe work arrangement was “hot tapped” into the ram side<br />

gas collector main and a duplex arrangement was “hot<br />

tapped” into the coke side gas collector main.<br />

15


Preparation Phase<br />

Welding inspection & Pressure testing<br />

All the new pipe work, including the service pipe work was<br />

manufactured and tested at Fairwood Fabrications Ltd<br />

workshop.<br />

Before leaving the workshop every weld was 100% MPI<br />

tested and each pipe section pressure tested with<br />

compressed air to one and a half times the maximum working<br />

pressure.<br />

A quality assurance (QA) file complied throughout the<br />

manufacturing process was produced and formed part of the<br />

Health and Safety file.<br />

16


Preparation Phase<br />

Expansion Joint<br />

The only design change from the original crossover design was the<br />

inclusion of an expansion bellows.<br />

This was to allow for any thermal expansion likely to have taken place<br />

when the new crossover at ambient temperature is connected to the<br />

working gas system with temperatures around 80° C.<br />

17


<strong>Crossover</strong> <strong>Main</strong> <strong>Replacement</strong><br />

Isolating the first <strong>Crossover</strong> main<br />

Insertion of the first blanking plate was the first real test of all<br />

the months of preparation and planning.<br />

For each crossover the Ram side leg was blanked off first<br />

followed by the <strong>Coke</strong> side.<br />

As an output from the Management of change and risk<br />

assessment exercises, a comprehensive checklist was<br />

written to ensure all tasks were listed and signed off when<br />

completed.<br />

A crane and hydraulic jacks were used to split the flanges.<br />

18


<strong>Crossover</strong> <strong>Main</strong> <strong>Replacement</strong><br />

Isolating the first <strong>Crossover</strong> main<br />

The most critical part of this process was the control of the<br />

gas pressure while splitting the flanges.<br />

To ensure the precise control required for this task, the<br />

system was controlled manually using pressure gauges and<br />

vent pipes to provide a visual indication to the controller.<br />

While inserting the blanking plate the sight of coke oven gas<br />

emerging from the split flange was a good indication that<br />

there was a slight positive gas pressure preventing air ingress<br />

and the threat of explosion.<br />

19


<strong>Crossover</strong> <strong>Main</strong> <strong>Replacement</strong><br />

Isolating the first <strong>Crossover</strong> main<br />

Guided slots at the front edge of the blanking plate located<br />

around the few loosened flange bolts at the rear of the flange;<br />

to facilitate bolthole alignment.<br />

When all the new flange bolts were loosely fitted, the<br />

crossover main leg supported by the crane was lowered until<br />

the flanges fitted onto the new gasket.<br />

20


<strong>Crossover</strong> <strong>Main</strong> <strong>Replacement</strong><br />

Removal of “Bend Section”<br />

The bend section of the crossover was disconnected form the<br />

horizontal section to prevent slewing as the horizontal section<br />

was lifted out.<br />

An 80 tonne crane set-up on the Ram track side of the<br />

Battery was used to execute the lift.<br />

After disconnection of the flanges and breaking up of the<br />

heavy tar deposit at the flange, the bend was lowered to the<br />

floor.<br />

21


<strong>Crossover</strong> <strong>Main</strong> <strong>Replacement</strong><br />

Removal of “Bend Section”<br />

22


<strong>Crossover</strong> <strong>Main</strong> <strong>Replacement</strong><br />

Horizontal Section Removal<br />

After disconnection of all service pipe work and the flanges<br />

connecting the horizontal section to the verticals, the fully<br />

supported the horizontal section was ready for removal.<br />

23


<strong>Crossover</strong> <strong>Main</strong> <strong>Replacement</strong><br />

Horizontal Section Removal<br />

When the pipe work was lowered to the floor level, it was<br />

clear to see it’s poor condition and the necessity to support<br />

the pipe at one-metre intervals.<br />

Also as the “gas flow” tests performed prior to the work<br />

starting indicated, the pipe cross sectional area was<br />

substantially reduced by deposits effecting gas flow through<br />

the pipe.<br />

24


Installing the new <strong>Crossover</strong> <strong>Main</strong>s<br />

Installation of the new horizontal section<br />

Prior to the installation of each new horizontal section all the<br />

support steelwork was upgraded to ensure good mechanical<br />

integrity and extend the life expectancy.<br />

The installation process was simply the reverse of the<br />

removal process.<br />

The new vertical legs were lifted and secured into place, and<br />

then the horizontal sections complete with all new service<br />

pipe work and expansion joint was lifted into place.<br />

<strong>Main</strong>taining good visual and radio contact with the crane<br />

operator was essential throughout the lift.<br />

25


Installing the new <strong>Crossover</strong> <strong>Main</strong>s<br />

Installation of the new horizontal section<br />

Scaffolding towers erected on either end of the crossover<br />

proved a safe working area for the installation team to<br />

carefully guide the new pipe into place and install the new<br />

gaskets.<br />

26


Installing the new <strong>Crossover</strong> <strong>Main</strong>s<br />

Installation of Bend Section<br />

The final section to be fitted is the bend.<br />

The bend section was cut to suit, allowing for the difference in<br />

the new installation fitting to the existing pipe work that is still<br />

operational and carrying hot gas.<br />

The bend was measured and tacked on site then removed<br />

backed to a workshop for completion.<br />

27


Installing the new <strong>Crossover</strong> <strong>Main</strong>s<br />

Removing the Blanking plates<br />

With the installation of the new pipe work complete the next<br />

phase of the installation was the removal of the spade that<br />

was preventing the gas flow over the new pipe.<br />

Again the pressure control was critical to the success of this<br />

phase, so to ensure the precise control required for this task,<br />

the system was controlled manually using pressure gauges<br />

and vent pipes to provide a visual indication to the controller.<br />

The coke side spade was removed first followed by the ram<br />

side.<br />

28


Installing the new <strong>Crossover</strong> <strong>Main</strong>s<br />

Removing the Blanking plates<br />

Again the 800 tonne crane was used to split the flanges via<br />

the bespoke spreader beam.<br />

Slowly the spade was removed and the gas pressure was<br />

adjusted as required.<br />

When the blanking spade was fully removed, the bolts were<br />

replaced and the main was lowered back onto the new gasket<br />

and the joint was secured.<br />

At this point coke oven gas was flowing through the new<br />

crossover pipe work and the new main was “live”.<br />

29


Summary<br />

The project took 40 weeks to complete from start to finish.<br />

Thousands of man-hours were utilised.<br />

Four new crossover mains were successfully installed.<br />

The project was completed on time, within budget and without<br />

any accidents.<br />

30

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