Hippo
Chemical
- Feb 6, 2003
- 7
I have what I suppose is a basic question about the surge point of a centrifugal compressor.
If I'm given the estimated surge in ICFM of a machine, will the surge flow be different if the inlet conditions change?
I've always considered a centrifugal compressor as a volumetric device that is not really impacted by inlet composition, temperature or pressure. I thought I only needed actual volumetric flow (inlet) to get what I needed from a supplied curve. I have a vendor completed datasheet and compressor curves that indicate reasonably different surge flows for different inlet conditions as well as different polytropic head for the same ICFM. I'm baffled.
Thanks for any replies.
Mark
If I'm given the estimated surge in ICFM of a machine, will the surge flow be different if the inlet conditions change?
I've always considered a centrifugal compressor as a volumetric device that is not really impacted by inlet composition, temperature or pressure. I thought I only needed actual volumetric flow (inlet) to get what I needed from a supplied curve. I have a vendor completed datasheet and compressor curves that indicate reasonably different surge flows for different inlet conditions as well as different polytropic head for the same ICFM. I'm baffled.
Thanks for any replies.
Mark