Hello All,
As discussed earlier, [please refer this thread: http://www.cheresour...ressure-query/] the reactor is having an independent bursting disc installed [without any relief valve] on it. And as per the discussion earlier the back pressure should be less than 50% of set pressure. I have now re-estimated the pressure drop across the bursting disc discharge line and it is more than 50% of the set pressure i.e. set pressure is 1barg and pressure drop is 0.6bar. However, I think we can get away with this restriction [50% of set pressure] as the bursting disc is reverse acting [i.e. the bursting disc manual says : [i]Due to the reverse acting compression mode of the disc it is also totally immune to backpressures and vacuum]. [/i]Any comment/help?
Please note that it is a low pressure reactor and has bursting disc set at 1barg. As this is the case, how such discharge line [with pressure drop of 0.6bar] will be affected if we install a relief valve in combination i.e. relief valve at the downstream of the existing bursting disc? I think it will cause more problem as the set pressure [1barg] is too low [?]. Any comment?
Thanks in advance.
KS
|
|
Maximum Allowable Back Pressure When Bd & Prv In Combination
Started by chemks2012, Oct 04 2012 10:07 AM
2 replies to this topic
Share this topic:
#1
Posted 04 October 2012 - 10:07 AM
#2
Posted 04 October 2012 - 03:06 PM
I know of no limiting built-up backpressure for a rupture disk. You calculate flow through the piping and disk with conventional fitting and line k values. The disk manufacturer labels k for the ruptured disk and provides them to you in the literature.
Bobby
Bobby
Edited by Bobby Strain, 06 October 2012 - 07:47 PM.
#3
Posted 06 October 2012 - 01:38 AM
KS,
Please upload a simple sketch of the RD/PRV combination. Are they configured in closed couple? Anyway you have to consider 3% rule of pressure drop limitation in PSV inlet line during fluid relieving.
Fallah
Please upload a simple sketch of the RD/PRV combination. Are they configured in closed couple? Anyway you have to consider 3% rule of pressure drop limitation in PSV inlet line during fluid relieving.
Fallah
Similar Topics
Pressure BuildupStarted by Guest_Yankee_* , 31 Mar 2026 |
|
|
||
Spray Dryer Nozzle Issue – Pressure Increase And Fines IncreaseStarted by Guest_Ella2365_* , 24 Mar 2026 |
|
|
||
The Basis Of Calculation To 3% Pressure Loss At The Inlet Of PressureStarted by Guest_phoenixmoca_* , 14 Mar 2026 |
|
|
||
Mdmt Basis For Gas Let-Down From High-Pressure Storage (Non-Blowdown CStarted by Guest_naghizad_* , 27 Feb 2026 |
|
|
||
Steam Pots Cyclic Pressure Pulsation And Water HammeringStarted by Guest_Abdelilah_* , 07 Dec 2025 |
|
|

FB





