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India's largest coal handling agency - Mjunction

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Expert Speak<br />

Refractory lining work for lower oven doors in progress in COP<br />

body was replaced with insulating castable Insulite-15. Top<br />

surface was finished with 70 mm LC-45 dense castable. About<br />

78 upper oven doors have been replaced with the new lining<br />

since September 31, 2009. None of these freshly lined doors<br />

have failed so far.<br />

There is a proposal to use ceramic fibre modules for upper<br />

door lining. Orders have already been placed for imported<br />

and indigenous modules, particularly for the upper door<br />

lining, the results of which can be seen only after installation.<br />

Lower Oven Doors<br />

The first instance of damage of lower oven door commenced<br />

almost within two to three months of the first start-up of coke<br />

oven battery nos. 7 and 8. Similar to the upper door lining,<br />

changes were made in the lower door lining also, mainly<br />

the peripherals, which receive maximum external abrasions.<br />

These were lined with dense LC-45 castable on top of Hysil<br />

boards. A pictorial representation of the extent of repairs done<br />

almost over a year after September 31, 2009 is given herewith.<br />

None of these freshly lined doors have failed till date.<br />

Bridge Pipes<br />

It was observed that the ceramic fibre lining of the bridge<br />

pipes was failing repeatedly and fallen refractory material<br />

was blocking the suction ports. It was also observed initially<br />

that the temperature inside the bridge pipes was shooting up<br />

as high as 1450°C leading to fusion and melting down of not<br />

only the refractory material, but also the mild steel body of the<br />

bridge pipes, thereby creating gaping holes.<br />

It was also observed that certain amounts of combustibles<br />

were being carried over to the bridge pipe region. The<br />

operating procedure being followed at that point of time<br />

(before September 31, 2009) had a flaw, although it was as<br />

per the instructions given by the Chinese suppliers. The two<br />

primary air windows provided in the upper oven doors were<br />

completely closed for the initial three hours after charging of<br />

ovens. Since the plant was being operated almost at full load,<br />

one oven was being pushed and charged every 45 minutes. As<br />

a result, unburnt volatiles escaped continuously to the bridge<br />

pipe and branch headers. Another mistake which further<br />

aggravated the problem was that a tertiary hole was made by<br />

some <strong>agency</strong> at the bottom of the uptake just after the fourlinked<br />

arch, which provided additional combustion air to the<br />

unburnt volatiles.<br />

A third observation was that when bridge pipes were<br />

being changed, flue hole cleaning was overlooked at times and<br />

bridge pipes were also being changed only on one side, that is,<br />

either the coke side or the pusher side, ignoring the condition<br />

of the other side. This resulted in more flow of gas through<br />

one of the bridge pipes leading to higher temperature and<br />

meltdown. The following steps were undertaken to overcome<br />

the problem of bridge pipe failure:<br />

a) Immediate plugging of tertiary holes with strict instructions<br />

to never open them in future.<br />

b) Keeping the primary air windows open right from the<br />

time after charging, closing it fully only when the oven<br />

is ready and regulating it in between as per combustion<br />

requirement.<br />

c) Keeping the levels of the combustibles in flue gas, particularly<br />

carbon monoxide and hydrogen at trace levels.<br />

d) To take up bridge pipe replacement either simultaneously<br />

on both the coke side and the pusher side or at a small gap<br />

of maximum one week.<br />

e) Use of dense castable LC-45 in the top layer in contact with<br />

the hot gas.<br />

f) To do compulsory suction port cleaning with every bridge<br />

pipe replacement.<br />

The above mentioned steps have brought in drastic<br />

improvements in the condition and life of the bridge pipes<br />

and their lining. Over the last one year, more than 100 out of<br />

a total of 192 bridge pipes have been replaced, none of which<br />

have failed as yet. With full load operation at 36 pushing per<br />

day, some damages temporarily resurfaced but were quickly<br />

controlled. The key to the solution to the problem was basically<br />

lowering the temperature of the flue gas to about 1100°C to<br />

1150°C which is as per the design and the liner material can<br />

withstand the same.<br />

The author is working as Vice President in the coke manufacturing<br />

unit of Bhushan Power and Steel Limited, Jharsuguda, Orissa.<br />

Right from its inception in 2007, the plant has been facing problems<br />

of massive failure of refractory lining of bridge pipes, upper oven<br />

doors, lower oven doors and branch headers. Many trial and error<br />

processes were carried out with different material and massive<br />

maintenance work was taken up to combat the failures, but fruitful<br />

results were not coming up. Finally after doing an in-depth study<br />

of various operational and maintenance aspects, a viable solution to<br />

this endemic problem could be found with the combined efforts of all<br />

related disciplines.<br />

The author is grateful to M/s K. Vijayan, S. Mukherjee, Sanjeev<br />

Srivastav, Sanjit Kumar and the entire coke oven team for their<br />

relentless efforts in bringing about the improvements in the operation<br />

and maintenance of the coke oven plant.<br />

COAL INSIGHTS 57 October 2010

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