Declared efficiency work arithmetic
Isentropic compressor / turbine
Inputs
Select compressor or turbine sign convention; this workspace does not select equipment.
User-entered absolute inlet temperature.
User-entered absolute inlet pressure.
User-entered absolute outlet pressure.
User-entered constant ratio for the stated ideal gas; property inference is excluded.
User-entered value for stated work arithmetic.
User-entered steady mass flow.
User-entered scalar efficiency used only for stated-work arithmetic.
Results
Declared pressure ratio p₂/p₁
5
—Isentropic outlet temperature
475.15
Declared-efficiency outlet temperature
518.93
Declared-efficiency compressor specific work input
220.03
kJ/kgDeclared-efficiency compressor shaft power inputP
110.01
T2s/T1 = (p2/p1)^((γ−1)/γ); wis = cp(T2s−T1); wactual = wis/ηis; P = ṁw
A first-pass number, not a code check, certification, or approval. Read the method and its limits below. What this is and is not.
Nearby: Sensible heat · Heat-exchanger ΔTlm · Plane-wall conduction · Thermal radiation exchange
Method
Formula, when it applies, and when it does not
Calculate ideal-gas isentropic outlet state and declared-efficiency specific work and power for a compressor or turbine pressure change.
T2s/T1 = (p2/p1)^((γ−1)/γ); wis = cp(T2s−T1); wactual = wis/ηis; P = ṁw
When
- Ideal-gas isentropic relation
- User-entered γ, cp, mass flow, and efficiency
- Declared absolute inlet/outlet pressures
- Compressor or turbine sign convention
Don’t
- This is ideal-gas isentropic state and user-entered-efficiency work arithmetic only. It does not select or rate equipment, use compressor maps, evaluate surge, choking, staging, cooling, losses beyond the declared efficiency, controls, mechanical design, safety, operability, or approval.