Use of CS instead of KCS
Posted: 19 Dec 2010, 19:21
Consider the following situation:
Working Fluid: Ammonia
Operating Temperature= 33 degrees Celcius
Recommended material= Killed Carbon Steel (can withstand up to -45 degrees Celcius)
At some points Carbon Steel has been used (cannot go below -10 degrees Celcius).
It is realistic to expect that temperatures in the range of -20 and below would be scaled during start-ups and shut-downs.
It is worthy to operate the line for around 45 days with some CS spools?
Please advise.
Kamran
Working Fluid: Ammonia
Operating Temperature= 33 degrees Celcius
Recommended material= Killed Carbon Steel (can withstand up to -45 degrees Celcius)
At some points Carbon Steel has been used (cannot go below -10 degrees Celcius).
It is realistic to expect that temperatures in the range of -20 and below would be scaled during start-ups and shut-downs.
It is worthy to operate the line for around 45 days with some CS spools?
Please advise.
Kamran