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
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Flare Piping Design
Started by Antonieta, Nov 21 2007 06:10 AM
1 reply to this topic
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#1
Posted 21 November 2007 - 06:10 AM
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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
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