Could someone help me calculate the relieving temperature of PSV.
PSV is on an acid KOD. OP-0.7 Kg/cm2g & OT=46 deg C. its mentioned in API that Relieving temp for gases is calculated as Tr=(Pr/P1)*T1.
but this law applies only for constant volume of gas. and in KOD considering Blocked outlet contigency we cant apply this law as no of moles of gas entering vessel inc with time.
|
Relieving Temperature
Started by , Apr 17 2007 04:26 AM
4 replies to this topic
Share this topic:
#1
Posted 17 April 2007 - 04:26 AM
#2
Posted 09 October 2008 - 12:48 PM
hello Puja,
i uses aspen hysys to overcome the same situation.. i was digging this issue for some times long back.. but one of my cleint solved it using the aspen hysys software.
I think you can do with aspen hysys..
If u r stuckup pls contact me..
i uses aspen hysys to overcome the same situation.. i was digging this issue for some times long back.. but one of my cleint solved it using the aspen hysys software.
I think you can do with aspen hysys..
If u r stuckup pls contact me..
#3
Posted 09 October 2008 - 06:45 PM
This equation is ONLY for vessel contain GAS/VAPOR only. DO NOT USED for other scenario.
#4
Posted 10 October 2008 - 04:18 PM
QUOTE (JoeWong @ Oct 10 2008, 01:45 AM) <{POST_SNAPBACK}>
This equation is ONLY for vessel contain GAS/VAPOR only. DO NOT USED for other scenario.
Small addition, it's valid for the fire scenario of vessels containing gas/vapour.
What is the high pressure source in this case?
#5
Posted 11 October 2008 - 12:49 PM
QUOTE (puja @ Apr 17 2007, 11:26 AM) <{POST_SNAPBACK}>
Could someone help me calculate the relieving temperature of PSV.
PSV is on an acid KOD. OP-0.7 Kg/cm2g & OT=46 deg C. its mentioned in API that Relieving temp for gases is calculated as Tr=(Pr/P1)*T1.
but this law applies only for constant volume of gas. and in KOD considering Blocked outlet contigency we cant apply this law as no of moles of gas entering vessel inc with time.
PSV is on an acid KOD. OP-0.7 Kg/cm2g & OT=46 deg C. its mentioned in API that Relieving temp for gases is calculated as Tr=(Pr/P1)*T1.
but this law applies only for constant volume of gas. and in KOD considering Blocked outlet contigency we cant apply this law as no of moles of gas entering vessel inc with time.
To determine the relieving temperature during a blocked gas outlet scenario, i would use the polytropic compression temperature (or, to simplify, the adiabatic compression temperature).
Similar Topics
Caloric Temperature CalculationStarted by Guest_bckesim_* , 10 Apr 2024 |
|
|
||
Heat Exchanger Temperature CrossStarted by Guest_kaidlut_* , 20 Dec 2022 |
|
|
||
Temperature Cross Heat ExchangerStarted by Guest_Priolo_* , 12 Aug 2019 |
|
|
||
Cross Temperature In Heater Exchanger (Lng)Started by Guest_Yogan_* , 21 Feb 2024 |
|
|
||
Propane Product Temperature Correction FactorStarted by Guest_loggrrr_* , 20 Nov 2023 |
|
|