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Reciprocating Compressor Performance Testing
Started by iplan, Feb 24 2010 09:37 AM
2 replies to this topic
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#1
Posted 24 February 2010 - 09:37 AM
I am required to evaluate the performance of a battery of reciprocating compressors working in parallel. Since the flow meter is a common one installed at the common discharge of all the compressors, individual flow can only be estimated by stopping individual compressors and computing the flow by the differences in total flow. To avoid this, I would like to know whether it is possible to estimate compressor efficiency ( polytropic or volumetric) without the flow component.
Many thanks in advance.
iplan
Many thanks in advance.
iplan
#2
Posted 05 April 2010 - 10:53 AM
iplan,
Do you at least know the pressure ratio of the compressors? You could use the constant heat capacity method for isentropic efficiency of a gas turbine compressor from the following formula:
Eff= (C-1)/(T2/T1-1)
Where C= Pr^((Gamma-1)/Gamma)
Eff = isentropic efficiency
Pr = compressor pressure ratio
T2/T1 = compressor temperature ratio
Gamma = cp/cv for air (~1.4)
kahlil
Do you at least know the pressure ratio of the compressors? You could use the constant heat capacity method for isentropic efficiency of a gas turbine compressor from the following formula:
Eff= (C-1)/(T2/T1-1)
Where C= Pr^((Gamma-1)/Gamma)
Eff = isentropic efficiency
Pr = compressor pressure ratio
T2/T1 = compressor temperature ratio
Gamma = cp/cv for air (~1.4)
kahlil
I am required to evaluate the performance of a battery of reciprocating compressors working in parallel. Since the flow meter is a common one installed at the common discharge of all the compressors, individual flow can only be estimated by stopping individual compressors and computing the flow by the differences in total flow. To avoid this, I would like to know whether it is possible to estimate compressor efficiency ( polytropic or volumetric) without the flow component.
Many thanks in advance.
iplan
#3
Posted 09 April 2010 - 10:20 AM
Hi,
Many thanks.The pressure ratios are known for each stage. I also estimated the polytropic efficiency through HYSYS. But I believe, the polytropic efficiency is mostly used for the centrifugal machines.
My understanding is that the volumetric efficiency in reciprocating compressors is hampered by passing suction valves, bad piston rings etc. If these components pass, they will also increase the suction temperature of the stage and in turn increasing discharge temperature also of the stage. Hence I request the forum experts to clarify whether it is correct if we correlate that a poor polytropic efficiency indicates a poor volumetric efficiency.
thanks again,
iplan
Many thanks.The pressure ratios are known for each stage. I also estimated the polytropic efficiency through HYSYS. But I believe, the polytropic efficiency is mostly used for the centrifugal machines.
My understanding is that the volumetric efficiency in reciprocating compressors is hampered by passing suction valves, bad piston rings etc. If these components pass, they will also increase the suction temperature of the stage and in turn increasing discharge temperature also of the stage. Hence I request the forum experts to clarify whether it is correct if we correlate that a poor polytropic efficiency indicates a poor volumetric efficiency.
thanks again,
iplan
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