We are in the process of designing a new flare system and need guidance on acceptable operating pressure to be used as design basis, this would be the constant superimposed backpressure (on a normal day) behind any PSVs that tie into the flare header. From reading a related discussion on this forum, I noticed a reference to API-521 which specifies a minimum design pressure (or MAWP) of 50psig for the flare header system (including the flare knockout pot). The operating pressure would really be dependent on the amount of flaring in the process, but is there any recommended operating pressure range so we can make adjusments to the pipe sizing in order to stay within this range? Thanks!
|

Flare System Operating Pressure (Superimposed Backpressure)
#1
Posted 23 September 2014 - 07:50 PM
#2
Posted 23 September 2014 - 08:00 PM
The sizing and pressure are determined by the maximum relief load. That is where you start.
Bobby
#3
Posted 23 September 2014 - 08:15 PM
Thanks for your response Bobby. Just to check if I understand your guidance correctly: So assuming the maximum relief load is pool fire scenario (global), I'd calculate the built up pressure for this load, and check how much margin I have between this value and the system MAWP, this will tell how much room I have for the normal operating pressure?
#4
Posted 23 September 2014 - 10:35 PM
Almost. Then ascertain that the selected size is OK for some low set pressure valves.
Bobby
#5
Posted 24 September 2014 - 04:13 AM
Thanks Bobby, this helps a lot.
Similar Topics
Steam Pressure In Heat ExchangerStarted by Guest_mvanrijnbach_* , 15 Apr 2025 |
|
![]() |
||
Critical Pressure For Choke Valve SizingStarted by Guest_Sherif Morsi_* , 07 Nov 2017 |
|
![]() |
||
![]() Flare Header Reverse FlowStarted by Guest_Ahmadhamzahperta_* , 04 Apr 2025 |
|
![]() |
||
Psv Backpressure TestingStarted by Guest_sam1111_* , 17 Mar 2025 |
|
![]() |
||
![]() Valve Cavity - Pressure Relief ValveStarted by Guest_CS10_* , 20 Feb 2025 |
|
![]() |