YungPlantEng
Chemical
- Jan 19, 2022
- 82
Condensate piping used to heat 6 coils for a sulfur tank is undersized to where startup heating loads hammer and destroy smaller sections of the pipe. It’s currently cost prohibitive to replace everything - are there any effective stop gaps that we could try after shutdown or during startup to mitigate this issue?
During cold weather startups we try and open bypass manual valves to atmosphere until we see steam. This sounds degenerate but would it suffice to put up some small automated valves so light shifts aren’t running around in the dead of winter trying to manually open steam valves while the boiler is down?
The piping is also plumbed in a way that condensate lines move up vertically before going into the main steam header. Not sure how much condensate sitting in the tank coils and blowing through on startup are affecting the hammer we see.
During cold weather startups we try and open bypass manual valves to atmosphere until we see steam. This sounds degenerate but would it suffice to put up some small automated valves so light shifts aren’t running around in the dead of winter trying to manually open steam valves while the boiler is down?
The piping is also plumbed in a way that condensate lines move up vertically before going into the main steam header. Not sure how much condensate sitting in the tank coils and blowing through on startup are affecting the hammer we see.