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Relief Temperature For Gas Expansion Case


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#1 Sevail

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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.

#2 joerd

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Posted 01 June 2009 - 07:23 AM

So what is your question?

#3 djack77494

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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.

#4 fallah

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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.


Second way (API-521 FORMULA) is nearly the same as what you mentioned as real situation.


#5 joerd

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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 Zhejang Chenggao Valve Co.

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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. smile.gif

#7 sheiko

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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 demank

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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

#9 diego

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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




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