Hi,
As per API guidelines, Relief valve downstream of a CV is to be sized for the max. Cv (for CV failure case).
However what fluid properties are to be referred to for rated flow calculation i.e. fluid properties at relieving condition or at normal condition.
looking for valuable inputs.
regards
|

Relieving Rate For Control Valve Failure
Started by chemdk, Dec 21 2011 09:00 AM
3 replies to this topic
Share this topic:
#1
Posted 21 December 2011 - 09:00 AM
#2
Posted 21 December 2011 - 10:25 AM
chemdk,
The relief valve capacity will be the maximum flow rate through the control valve in the fail open condition. However, the fluid properties will be corresponding to the relieving condition i.e. the relief valve set pressure plus the allowable overpressure (10% over the set pressure for a single relief device and non-fire case as per API STD 520).
Hope this helps.
Regards,
Ankur.
The relief valve capacity will be the maximum flow rate through the control valve in the fail open condition. However, the fluid properties will be corresponding to the relieving condition i.e. the relief valve set pressure plus the allowable overpressure (10% over the set pressure for a single relief device and non-fire case as per API STD 520).
Hope this helps.
Regards,
Ankur.
#3
Posted 22 December 2011 - 06:13 AM
Ankur,
Thank you for ur reply.
Maximum flow rate thru a CV is when CV is wide open (Max Cv value). However to arrive at max flow rate thru a control valve, shall one use relieving condition properties (density) Or maximum flow is calculated assuming fluid "standard" condition properties.
Thank you for ur reply.
Maximum flow rate thru a CV is when CV is wide open (Max Cv value). However to arrive at max flow rate thru a control valve, shall one use relieving condition properties (density) Or maximum flow is calculated assuming fluid "standard" condition properties.
#4
Posted 22 December 2011 - 08:55 AM
chemdk,
Maximum flow rate occurs due to valve fail open. This could happen even before the line downstream of the control valve gets overpressurized. Overpressure would be a consequence of maximum flow and not vice-versa. Hence maximum flow rate should be calculated at the operating conditions of flow. If the maximum flow rate due to valve fail open is defined as mass flow and you need to report the flow as volume flow then consider the lowest density of the fluid at the operating conditions (temperature / pressure) to arrive at volume flow @operating conditions.
Regards,
Ankur.
Maximum flow rate occurs due to valve fail open. This could happen even before the line downstream of the control valve gets overpressurized. Overpressure would be a consequence of maximum flow and not vice-versa. Hence maximum flow rate should be calculated at the operating conditions of flow. If the maximum flow rate due to valve fail open is defined as mass flow and you need to report the flow as volume flow then consider the lowest density of the fluid at the operating conditions (temperature / pressure) to arrive at volume flow @operating conditions.
Regards,
Ankur.
Similar Topics
Check Valve FailureStarted by Guest_Falah_* , 26 Mar 2025 |
|
![]() |
||
Multiport Selector Valve (Msv)Started by Guest__1angelia23_* , 12 Mar 2025 |
|
![]() |
||
![]() Valve Cavity - Pressure Relief ValveStarted by Guest_CS10_* , 20 Feb 2025 |
|
![]() |
||
![]() Psvs Relieving To Closed Drain SystemStarted by Guest__1angelia23_* , 12 Jan 2025 |
|
![]() |
||
![]() Valve Cv InputsStarted by Guest_QuantumEng_* , 01 Apr 2024 |
|
![]() |