Find the critical ratio from specific heat ratio. Evaluate back pressure limits for stable operation. Save tables, download files, and verify engineering decisions fast.
For isentropic flow of an ideal gas, choking occurs when the Mach number at the minimum area reaches 1. The corresponding critical pressure ratio between the throat and stagnation state is:
P*/P0 = ( 2 / (k + 1) )^( k / (k − 1) )
Here k is the specific heat ratio. If your provided back-pressure ratio Pb/P0
is less than or equal to P*/P0, the flow is considered choked.
| k | Critical ratio (P*/P0) | P0 | Pb | Pb/P0 | Status |
|---|---|---|---|---|---|
| 1.400 | 0.528282 | 300 kPa | 120 kPa | 0.4000 | Choked |
| 1.330 | 0.540364 | 500 kPa | 260 kPa | 0.5200 | Choked |
| 1.660 | 0.488084 | 200 kPa | 70 kPa | 0.3500 | Choked |
| 1.289 | 0.547724 | 10 bar | 7 bar | 0.7000 | Not choked |
The choked flow pressure ratio compares downstream static pressure at the throat to the upstream stagnation state. For compressible gases, this ratio controls whether the flow can accelerate to Mach 1 at the minimum area. When the ratio drops below a critical value, the nozzle becomes “sonic-limited” at the throat.
Choking is a safety and performance boundary. It limits mass flow through orifices, control valves, nozzles, and leaks. Many relief and vent calculations assume choking to estimate worst‑case discharge. If choking occurs, reducing back pressure further often increases noise and jet velocity more than it increases flow rate.
This calculator uses the standard isentropic relationship for an ideal gas with constant specific heats. The condition Mach = 1 at the throat produces a unique critical pressure ratio that depends only on the specific heat ratio, k = Cp/Cv. No temperatures are required for the ratio itself.
Typical k values are about 1.40 for air and nitrogen near room temperature, about 1.33 for water vapor, about 1.289 for carbon dioxide, and about 1.66 for helium. Lower k generally increases the critical ratio, meaning choking is reached at a higher downstream pressure for the same upstream pressure.
Designers often prefer a pressure limit instead of a dimensionless ratio. The tool computes P* = P0 × (P*/P0), giving the maximum back pressure that still permits choking for the chosen upstream pressure. This is useful for setting downstream constraints and checking operating envelopes quickly.
If you provide Pb, the calculator evaluates Pb/P0 and compares it to the critical ratio. When Pb/P0 is less than or equal to the critical value, the status reads “Choked.” A margin is also reported as (critical − actual), indicating how far below the boundary you operate.
Pressures must be positive and use the same unit selection to keep ratios consistent. The calculator supports Pa, kPa, MPa, bar, and psi with internal conversion to pascals. The ratio is unitless, so changing units does not change the critical ratio, only the displayed pressures.
For high-pressure real-gas behavior, large temperature shifts, two-phase flow, strong shocks, or non‑isentropic losses, the ideal choking ratio can deviate from reality. Use the output as an initial screening tool and pair it with vendor data, discharge coefficients, and standards-based sizing when accuracy is critical.
The critical ratio is P*/P0, the downstream-to-upstream limit where the throat reaches Mach 1. Below this ratio, the flow becomes choked and is no longer controlled by downstream pressure.
No. The critical ratio depends only on k for the ideal isentropic model. Temperature is needed for mass-flow rate calculations, but not for the choking pressure ratio itself.
The calculator still returns the critical ratio and the critical pressure P*. Add Pb to get a clear choked/not‑choked decision and the operating margin.
Presets are representative near common conditions. If your gas composition or temperature differs, enter a custom k. Even small k changes can shift the boundary in sensitive designs.
It means downstream pressure no longer controls the throat condition. Mass flow can still change with upstream pressure, temperature, throat area, and losses, but not primarily with further Pb reductions.
No. This is a compressible-gas choking model. Liquid “choking” involves cavitation and different criteria. Use a dedicated liquid valve/cavitation sizing method instead.
Real-gas effects, friction, heat transfer, upstream turbulence, and discharge coefficients change effective behavior. Treat this result as a first-pass check and validate with standards or manufacturer data.
Important Note: All the Calculators listed in this site are for educational purpose only and we do not guarentee the accuracy of results. Please do consult with other sources as well.