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.
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.