Dear Sir
Greetings !
Sir ,
At our facility we have two screw compressor running together,feeding the same plant air header .
Each compressor is designed to discharge 1100 Nm3/ hr compressed air @10 barg
Total plant consumpton is 1800Nm3 / hr , to counter the gap b/w supply and consumption , One compessor is kept running always and the other kept in auto . The later one loads and unloads B/w 100 and 0 % load very frequently . which affacts parameter of Downstream equipments like air seperation unit.
So we have to open the Plant air header drain to reduce the frequency of loading and unloading of the compressor which in turn increase the power loss.
Can somebody suggest me some ways or modification or optional ways to reduce this drainage of Compressed air or to use it some how,some where.
\
regards,
Shin
|

Using Screw Compressor Efficiantly
Started by shin29, Nov 07 2012 12:56 AM
3 replies to this topic
Share this topic:
#1
Posted 07 November 2012 - 12:56 AM
#2
Posted 07 November 2012 - 07:10 AM
Shin 29 ,
Did you talk to your vendor about your problem ? They may help you .
Breizh
Did you talk to your vendor about your problem ? They may help you .
Breizh
#3
Posted 08 November 2012 - 01:25 AM
Dear Breizh,
Thanks for your reaponse.
Sir i have talked with the vendor about the problem, they ruled out the possibility of installing a variable speed drive or a circulation valve . further they stopped responding . Now we are finding some innovative solution for 2 years . As after that plant air cinsumption is supposed to rise .
That's why i post this problem on the blog . to get something from other's experiances .
warm regards,
Sharad Bhardwaj
Thanks for your reaponse.
Sir i have talked with the vendor about the problem, they ruled out the possibility of installing a variable speed drive or a circulation valve . further they stopped responding . Now we are finding some innovative solution for 2 years . As after that plant air cinsumption is supposed to rise .
That's why i post this problem on the blog . to get something from other's experiances .
warm regards,
Sharad Bhardwaj
#4
Posted 08 November 2012 - 01:55 AM
Shin,
When I answered to your post my thought was : why not using a VSD !
I guess you have one or multiples air storage after the discharge of the compressor with Pressure switches ( High , low ) to start /stop the compressors and at least to operate at minimum load .
I cannot help more.
Breizh
When I answered to your post my thought was : why not using a VSD !
I guess you have one or multiples air storage after the discharge of the compressor with Pressure switches ( High , low ) to start /stop the compressors and at least to operate at minimum load .
I cannot help more.
Breizh
Similar Topics
![]() Lng Boil Off Gas Compressor Suction DrumStarted by Guest_Lyne_* , 04 Jun 2025 |
|
![]() |
||
Parallel Compressor Setup With Uneven CapacitiesStarted by Guest_sinrem_* , 13 May 2025 |
|
![]() |
||
![]() Hysys Expander/compressor Input Using Dimensionless CurveStarted by Guest_Alfreedo_* , 21 Apr 2025 |
|
![]() |
||
Centriugal CompressorStarted by Guest_Rahimzadeh_* , 02 Mar 2025 |
|
![]() |
||
Pulsation Device In Reciprocating CompressorStarted by Guest_zaidanamir_* , 17 Feb 2025 |
|
![]() |