Analyze compressible gas behavior using practical sizing inputs. Switch units, export results, and inspect trends. Built for engineers needing fast, transparent, data-driven valve checks.
| Scenario | P1 | P2 | Temp | Gg | Z | xT | Known Flow | Approx. Cv | Approx. Kv |
|---|---|---|---|---|---|---|---|---|---|
| Natural gas sizing | 8 bar(a) | 5 bar(a) | 25 °C | 0.60 | 0.98 | 0.72 | 1500 Nm³/h | 12.455 | 10.773 |
| Air service sizing | 6 bar(a) | 4.8 bar(a) | 20 °C | 1.00 | 1.00 | 0.70 | 850 Nm³/h | 11.270 | 9.748 |
| Flow prediction | 10 bar(a) | 6 bar(a) | 35 °C | 0.55 | 0.97 | 0.68 | Cv = 15.000 | 15.000 | 12.975 |
These entries are sample engineering cases for orientation. Actual valve sizing should still be checked against valve trim, noise, piping geometry, and manufacturer guidance.
This calculator uses a practical compressible-gas sizing relationship for valve-style flow coefficient work under standard volumetric flow conditions.
Where:
This method is excellent for quick design checks and screening studies. Final valve selection should use full manufacturer data and service-specific standards.
It represents a valve or restriction’s capacity to pass gas under a defined pressure drop and set of fluid conditions. Larger coefficients indicate higher flow capability.
Compressible-gas equations depend on true thermodynamic pressure. Gauge pressure omits atmospheric pressure, which changes the pressure ratio and can distort the calculated coefficient.
Choked flow occurs when the pressure drop ratio reaches the valve’s critical factor xT. Beyond that point, more downstream pressure reduction does not increase flow proportionally.
Use Cv when your sizing references U.S. customary practice. Use Kv when your project documentation or vendor data is based on metric valve coefficients.
Z corrects ideal-gas behavior. Real gases deviate from ideal predictions at many practical pressures and temperatures, so Z helps keep the result more realistic.
No. Both are standard volumetric flow units, but they reference different standard temperatures. This calculator converts between them for convenience.
Use it for strong preliminary engineering, checking, and comparison. Final procurement should still verify trim style, noise, cavitation risk, piping geometry, and manufacturer sizing methods.
The graph plots predicted standard flow against downstream pressure while holding the gas, temperature, upstream pressure, and coefficient fixed. It helps visualize sensitivity and choking behavior.
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.