Isentropic Efficiency

Compressor and turbine efficiencies are defined inversely — ideal ÷ actual for a compressor, actual ÷ ideal for a turbine — precisely so that both land below 1. Swapping them produces a plausible number above unity and nothing downstream complains. The loss shows up as temperature: a real compressor discharges hotter than ideal, a real turbine exhausts hotter too.

Ideal outlet temperature
Actual outlet temperature
Temperature penalty
Ideal specific work
Actual specific work
Actual power
Lost power
Definition used

Constant specific heats are assumed, which is good for moderate temperature ranges and optimistic across a gas turbine’s full span — a real machine uses temperature-dependent properties or a polytropic (small-stage) efficiency instead. Polytropic efficiency is always slightly higher than isentropic for a compressor because of the reheat effect, so check which one a vendor is quoting before comparing machines. Typical values: 0.70–0.85 for reciprocating and screw compressors, 0.80–0.90 for centrifugal, 0.85–0.92 for large turbines.

A helper, not a substitute for engineering judgment. Verify against the governing standard and your own hand calculations.