Dear All,
I have used Hysys dynamics for depressurisation with an isentropic expansion efficiency of 90% and a vessel U value of 5W/m2K. The minimum fluid temperatures calculated dowstream of the valve are around -80C. I've been told these are the temperatures that can be achieved during this type of process which involves isentropic expansion + isenthalpic expansion.
I've been told that usually mean metal temperature is substantially less severe than the fluid temperature and that the flare piping design should be based on the mean metal temperature, not on the temperature of the fluid contacting the metal.
Please could you advice how to calculate the mean metal temperature?
Thanks in advance,
Ann
|
|
Flare Piping Design
Started by Antonieta, Nov 21 2007 06:10 AM
1 reply to this topic
Share this topic:
#1
Posted 21 November 2007 - 06:10 AM
#2
Posted 23 November 2007 - 10:06 PM
QUOTE (Antonieta @ Nov 21 2007, 06:10 AM) <{POST_SNAPBACK}>
Dear All,
I have used Hysys dynamics for depressurisation with an isentropic expansion efficiency of 90% and a vessel U value of 5W/m2K. The minimum fluid temperatures calculated dowstream of the valve are around -80C. I've been told these are the temperatures that can be achieved during this type of process which involves isentropic expansion + isenthalpic expansion.
I've been told that usually mean metal temperature is substantially less severe than the fluid temperature and that the flare piping design should be based on the mean metal temperature, not on the temperature of the fluid contacting the metal.
Please could you advice how to calculate the mean metal temperature?
Thanks in advance,
Ann
I have used Hysys dynamics for depressurisation with an isentropic expansion efficiency of 90% and a vessel U value of 5W/m2K. The minimum fluid temperatures calculated dowstream of the valve are around -80C. I've been told these are the temperatures that can be achieved during this type of process which involves isentropic expansion + isenthalpic expansion.
I've been told that usually mean metal temperature is substantially less severe than the fluid temperature and that the flare piping design should be based on the mean metal temperature, not on the temperature of the fluid contacting the metal.
Please could you advice how to calculate the mean metal temperature?
Thanks in advance,
Ann
See some responses HERE
Suggest no double posting...it may leads to suspension...
Good luck.
JoeWong
Similar Topics
Rupture Disk Tail/lateral Piping Design BasisStarted by Guest_Karthikram_* , 19 Aug 2025 |
|
|
||
Wet Scrubber Design For Low Flow Rate Of GasStarted by Guest_SIVAMOORTHY_* , 17 Apr 2018 |
|
|
||
Design Of Direct Contact After Cooler (Dcac) For Air Separation UnitStarted by Guest_Paulogeorge_* , 29 Jul 2025 |
|
|
||
Flare Header Reverse FlowStarted by Guest_Ahmadhamzahperta_* , 04 Apr 2025 |
|
|
||
Design Capacity Of Hydrogen Pullet During Hydroprocessing Units UpsetStarted by Guest_Divid Kelin_* , 18 Jun 2025 |
|
|

FB





