Area · total pressure · temperature · Mach
Compressible mass flow
Inputs
User-entered flow area; nozzle, throat, and duct geometry are not derived.
User-entered absolute total pressure; pressure losses and state conversion are not derived.
User-entered absolute total temperature; heat transfer and temperature state are not derived.
User-entered Mach number; this workspace does not determine flow regime or choking.
User-entered ideal-gas specific-heat ratio; gas properties are not derived.
User-entered specific gas constant; gas composition and properties are not derived.
Results
Literal ideal compressible mass flow
3.4833
kg/sDeclared Mach number
0.5
—Declared flow areaA
0.01
Declared total pressure
200,000
ṁ = (A·pt/√Tt)·√(γ/R)·M·[1 + ((γ − 1)/2)·M²]^(−(γ + 1)/(2(γ − 1)))
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: Hydrostatic pressure · Flow continuity · Pipe mean velocity · Bernoulli equation
Method
Formula, when it applies, and when it does not
Apply NASA’s ideal isentropic mass-flow relation to gas-state and flow inputs without determining Mach number, choking, or nozzle geometry.
ṁ = (A·pt/√Tt)·√(γ/R)·M·[1 + ((γ − 1)/2)·M²]^(−(γ + 1)/(2(γ − 1)))
When
- Ideal-gas isentropic relation
- Declared total pressure and temperature
- User-entered Mach number and gas constants
- Single flow area
Don’t
- This applies NASA’s stated ideal isentropic mass-flow relation only to user-declared area, total state, Mach number, specific-heat ratio, and gas constant. It does not determine Mach number, gas properties, choking, nozzle or duct geometry, pressure losses, heat transfer, flow regime, capacity, safety, suitability, or approval.