In sizing of pressure safety valve ulimately we are finding the orifice area .Orifice area was chosen as per the ASME section VIII guidance( D,E,L,M)
The orifice area for L = 2.853 SQ.Inches & size (in x out) = 3 x 4
dia of orifice from the above orifice area comes to 1.9 inches only (arriving dia from Pi/4*d2 = 2.853 in2)
i have following clarification
i)In safety valve orifice area represents what?
ii)Orifice dia comes only 1.9" whereas inlet safety valve flange size was 3"?
Kindly clarify
Regards,
Bhaskaran.r
|
|
Safety Valve Orifice
Started by bhaskaran, Dec 29 2008 12:39 AM
2 replies to this topic
Share this topic:
#1
Posted 29 December 2008 - 12:39 AM
#2
Posted 29 December 2008 - 08:48 AM
Bhaskaran,
First let me suggest that you choose more carefully which forum to post questions to. You would likely achieve a better response if this were posted to the relief valve forum where the experts in this sort of matter reside.
Refering to a safety valve orifice area is a bit of a misnomer since a PSV more closely resembles an isentropic nozzle rather than an isenthalpic orifice. Nonetheless, the term is widely used. It represents the minimum cross-sectional flow area available for flluid flow. Since "the orifice" is a restriction internal to the PSV, I don't understand why you are surprised that the orifice diameter is smaller than the flange. It takes some space to put all "the workings" of the PSV inside the valve body.
First let me suggest that you choose more carefully which forum to post questions to. You would likely achieve a better response if this were posted to the relief valve forum where the experts in this sort of matter reside.
Refering to a safety valve orifice area is a bit of a misnomer since a PSV more closely resembles an isentropic nozzle rather than an isenthalpic orifice. Nonetheless, the term is widely used. It represents the minimum cross-sectional flow area available for flluid flow. Since "the orifice" is a restriction internal to the PSV, I don't understand why you are surprised that the orifice diameter is smaller than the flange. It takes some space to put all "the workings" of the PSV inside the valve body.
#3
Posted 29 December 2008 - 10:05 PM
QUOTE (djack77494 @ Dec 29 2008, 09:48 AM) <{POST_SNAPBACK}>
Bhaskaran,
First let me suggest that you choose more carefully which forum to post questions to. You would likely achieve a better response if this were posted to the relief valve forum where the experts in this sort of matter reside.
Refering to a safety valve orifice area is a bit of a misnomer since a PSV more closely resembles an isentropic nozzle rather than an isenthalpic orifice. Nonetheless, the term is widely used. It represents the minimum cross-sectional flow area available for flluid flow. Since "the orifice" is a restriction internal to the PSV, I don't understand why you are surprised that the orifice diameter is smaller than the flange. It takes some space to put all "the workings" of the PSV inside the valve body.
First let me suggest that you choose more carefully which forum to post questions to. You would likely achieve a better response if this were posted to the relief valve forum where the experts in this sort of matter reside.
Refering to a safety valve orifice area is a bit of a misnomer since a PSV more closely resembles an isentropic nozzle rather than an isenthalpic orifice. Nonetheless, the term is widely used. It represents the minimum cross-sectional flow area available for flluid flow. Since "the orifice" is a restriction internal to the PSV, I don't understand why you are surprised that the orifice diameter is smaller than the flange. It takes some space to put all "the workings" of the PSV inside the valve body.
Thanks jack for your reply.Hereafter i will be careful in putting questions in right forum.Thanx for your advice
Similar Topics
Two Phase Reverse Flow -Psv Sizing For Check Valve Failure CaseStarted by Guest_namita.modak1_* , 01 Apr 2026 |
|
|
||
Surface Area Calculation For Blowdown Orifice Sizing Including FinnedStarted by Guest_victortheone_* , 17 Feb 2026 |
|
|
||
Help Needed –Valve Causing High Pressure In Downstream VesselStarted by Guest_Alaa55_* , 27 Nov 2025 |
|
|
||
Thermal Relief Valve For A Fire CaseStarted by Guest_QuantumEng_* , 19 Nov 2025 |
|
|
||
Real Or Ideal Cp/cv For Control Valve CalculationsStarted by Guest_sumwunrandom_* , 14 Oct 2025 |
|
|

FB





