Dear all;
I want to fill the datasheet of temporary strainer of compressor suction line.
what is the common figure for this DP. which is usually used in start up.
Thanks for your guidance.
mm217
|
Posted 05 May 2013 - 06:29 AM
Dear all;
I want to fill the datasheet of temporary strainer of compressor suction line.
what is the common figure for this DP. which is usually used in start up.
Thanks for your guidance.
mm217
Posted 05 May 2013 - 08:30 AM
mm217,
Temporary strainers (most often conical type) are used during start-up of the system during a commissioning or re-commissioning exercise and are meant to capture line debris, weld spatters etc. that can damage the impeller. These gross temporary strainers are subsequently removed and replaced with fine strainers where the pressure drop needs to be specified considering long-term operation, availability and protection from fine particles and dust.
For temporary strainers it is important for them to be mechanically strong and robust to withstand high differential pressures when the strainer gets completely blocked due to line debris in a very short duration. I would recommend to specify a minimum differential pressure of 1 bar (15 psi) based on my experience and understanding. Finding any specific written guidelines on what value of differential pressure should be specified may be difficult. Individual companies may assign different values of DP for such strainers. I would also ensure that the temporary strainer design pressure is equal to or greater than the suction line shut-in pressure. Niormally the suction line shut-in pressure is equal to the relief valve set-point on the compressor suction drum.
I would also recommend to take the opinion of the compressor manufacturer on the design of the temporary strainer including design pressure, temperature and maximum allowable differential pressure.
Hope this helps.
Regards,
Ankur.
Posted 05 May 2013 - 10:22 PM
Ankur;
I agree with you to take opinion of the compressor manufacturer on the design of the temporary strainer. Your explanation is quite helpful. I appreciate it.
Regards;
mm217
Posted 07 May 2013 - 05:39 AM
Hi,
we keep 0.35 barg for reciprocating compressor and for centrifugal compressor 1.0 barg.
Toor
Parallel Compressor Setup With Uneven CapacitiesStarted by Guest_sinrem_* , 13 May 2025 |
|
![]() |
||
Steam Pressure In Heat ExchangerStarted by Guest_mvanrijnbach_* , 15 Apr 2025 |
|
![]() |
||
Critical Pressure For Choke Valve SizingStarted by Guest_Sherif Morsi_* , 07 Nov 2017 |
|
![]() |
||
![]() Hysys Expander/compressor Input Using Dimensionless CurveStarted by Guest_Alfreedo_* , 21 Apr 2025 |
|
![]() |
||
Centriugal CompressorStarted by Guest_Rahimzadeh_* , 02 Mar 2025 |
|
![]() |