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Relief Temperature For Gas Expansion Case
Started by Sevail, May 31 2009 02:17 AM
8 replies to this topic
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#1
Posted 31 May 2009 - 02:17 AM
it seems that there are two way for calculation of reliefing temperature in gas expansion
1- considering a compressor to increase pressure from operating to relief pressure with 100% effi.
(By Hysys)
2-using API-521 formula for gas expansion(T2=(P2/P1)*T1)
But the result of above items are different while real situation is compression of gas in constant volume.
1- considering a compressor to increase pressure from operating to relief pressure with 100% effi.
(By Hysys)
2-using API-521 formula for gas expansion(T2=(P2/P1)*T1)
But the result of above items are different while real situation is compression of gas in constant volume.
#2
Posted 01 June 2009 - 07:23 AM
So what is your question?
#3
Posted 01 June 2009 - 07:24 AM
Sevail,
Please supply a better indication of what you seek. I read your posting and don't know if you're interested in a compressor or a releif valve. The quality of the responses is directly proportional to the quality of the question.
Please supply a better indication of what you seek. I read your posting and don't know if you're interested in a compressor or a releif valve. The quality of the responses is directly proportional to the quality of the question.
#4
Posted 02 June 2009 - 02:27 AM
QUOTE (Sevail @ May 31 2009, 03:17 AM) <{POST_SNAPBACK}>
it seems that there are two way for calculation of reliefing temperature in gas expansion
1- considering a compressor to increase pressure from operating to relief pressure with 100% effi.
(By Hysys)
2-using API-521 formula for gas expansion(T2=(P2/P1)*T1)
But the result of above items are different while real situation is compression of gas in constant volume.
1- considering a compressor to increase pressure from operating to relief pressure with 100% effi.
(By Hysys)
2-using API-521 formula for gas expansion(T2=(P2/P1)*T1)
But the result of above items are different while real situation is compression of gas in constant volume.
Second way (API-521 FORMULA) is nearly the same as what you mentioned as real situation.
#5
Posted 02 June 2009 - 08:25 AM
QUOTE (Sevail @ May 31 2009, 01:17 AM) <{POST_SNAPBACK}>
2-using API-521 formula for gas expansion(T2=(P2/P1)*T1)
You might as well credit Joseph Louis Gay-Lussac (1802) with that equation.
#6
Posted 17 June 2009 - 03:28 AM
You need to caculate with your experience also. Knowledge is just a basic and in the ideal situation.The results are alway something differ.
#7
Posted 17 June 2009 - 12:25 PM
Item 1/
I usually use that method to determine the relieving temperature in a blocked gas outlet case (so gas compression not expansion).
Item 2/
Applicable for a gas-filled vessel in external fire case (with the assumption that inlets and outlets are all closed => constant volume).
#8
Posted 20 June 2009 - 06:51 PM
I always use HYsys to get the relief temperature.
The formula of (T2=(P2/P1)*T1) is valid for gases.
THen for liquid case, hysys's help is needed to know the temperature when liquid became gas at the reliving pressure
The formula of (T2=(P2/P1)*T1) is valid for gases.
THen for liquid case, hysys's help is needed to know the temperature when liquid became gas at the reliving pressure
#9
Posted 16 July 2009 - 09:23 AM
An ancient rule of thumb for natural gas says "-1°C every 2 bars" in depressurisation.....
not for official documents but not too bad for simply evaluation
in any case hysys depressuring utility...........
bye
diego
not for official documents but not too bad for simply evaluation
in any case hysys depressuring utility...........
bye
diego
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