Dears
We are having a steam turbine that is driving a centrifugal compressor with a configuration shown in the attached sketch case:1.
We are intending to reduce the extracted steam flow from HP case by almost 18 T/H due to non requirement of original amount in downstream processes. However, this reduction in extraction steam should not affect the power delivered to the compressor and hence the LP case inlet steam flow shall be increased by amount derived from turbine steam diagram.
Actually I am bit confused with second configuration of flow whether turbine shaft rpm in case: 2 will remain the same as case:1 if we know that the shaft power will remain the same?
Another confusion will isentropic efficincies of both LP and HP case remain the same in both cases?
Attached Files
Edited by Said Salim, 09 March 2022 - 11:21 PM.