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4 General Technical Specification of Bhilai Steel Plant, SAIL ...

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© 2007 MECON Limited<br />

All rights reserved<br />

<strong>General</strong> <strong>Technical</strong> <strong>Specification</strong><br />

v) Separate seal pots shall be provided for different gasses.<br />

vi) Removal <strong>of</strong> condensate from branch line from inter shop gas pipe and inshop<br />

gas pipe should be carried out in separate condensate seal pots.<br />

vii) Minimum height <strong>of</strong> the water seal in the condensate seal pot shall exceed the<br />

maximum working pressure <strong>of</strong> gas by 500 mm, but this height in no case shall<br />

be lower than 2000 mm.<br />

If necessary, the height <strong>of</strong> water seal can be increased by adding more than one<br />

seal pot in series. However, number <strong>of</strong> such seal pots shall not exceed three.<br />

Further base plate <strong>of</strong> seal pot shall have minimum thickness <strong>of</strong> 16 mm.<br />

While installing common seal pot for a number <strong>of</strong> gas pipe, height <strong>of</strong> water seal<br />

should exceed by 500 mm the maximum working pressure in any <strong>of</strong> the<br />

connected gas pipe.<br />

viii) Design <strong>of</strong> condensate seal pots should ensure protection against leakage <strong>of</strong><br />

harmful gases into building by providing vent <strong>of</strong> adequate height on the seal pot.<br />

ix) Condensate seal pot shall be provided with purging facilities.<br />

x) Installation <strong>of</strong> condensate seal pot for in shop gas network is allowed inside the<br />

buildings.<br />

Condensate Drain Arrangement for Medium pressure High pressures gas<br />

i) Condensate disposal for gases having higher line pressure have to be done by<br />

using adequate pressure seal pots.<br />

ii) In a high pressure seal pot the metallic float is utilized for disposal <strong>of</strong> condensate<br />

and prevent leakage <strong>of</strong> gas from the pot.<br />

iii) The seal pot should be air tight and wall thickness should be decided on the line<br />

test pressure.<br />

iv) Condensate coming out <strong>of</strong> seal pot should be discharged into phenolic sewerage<br />

line or in a reservoir provided locally.<br />

02.08. STEAM TRAPS / MOISTURE TRAPS-<br />

At low points in steam & compressed air pipeline steam traps / moisture traps with<br />

strainer assembly will be provided to drain out the condensate. Selection <strong>of</strong> steam trap<br />

shall be as per IPSS: 1-06-039 – 02. Installation <strong>of</strong> steam traps shall be as per IPSS: 1-<br />

06-037<br />

02.09. PURGING SYSTEM<br />

System for feeding purge gas and venting <strong>of</strong> gas/ air from the piping system shall be<br />

provided for all fuel gas piping.<br />

Purging<br />

i) Gas pipelines <strong>of</strong> blast furnace gas, coke oven gas, converter gas and mixed gas<br />

shall be equipped with nitrogen or steam pipe connection with isolation valve.<br />

The connection <strong>of</strong> nitrogen or steam pipeline to the gas pipeline shall be done by<br />

means <strong>of</strong> flexible hose which shall be connected only during the period <strong>of</strong><br />

purging.<br />

Gases & Liquid Fluids<br />

Page 10 <strong>of</strong> 51<br />

GS-02

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