Public BetaOpen test period: August 30–September 13, 2026. Preliminary engineering calculation—verify results before use.

Flow & control valves / Tools 01–02

Gas Valve Sizing

Calculate either the required control-valve Cv or the available standard gas flow through a valve with known Cv.

Standard-flow basis60°F · 14.696 psiaSCFM is converted internally to SCFH
01

Operating conditions

Enter gauge pressures; the tool converts them to absolute.

Gas & valve propertiesReview vendor xT
Gas presets are preliminary. Replace xT with the valve manufacturer’s value.

Calculation method

Transparent engineering basis

1

Normalize conditions

Convert psig to psia and °F to °R. Convert SCFM to SCFH.

2

Check flow regime

Compare actual pressure-drop ratio with Fk·xT to identify choking.

3

Solve Cv or flow

Apply the expansion factor and solve the compressible-flow equation for the selected output.

Required CvCv = q / [1360 · Fp · P1 · Y · √(xeff / (Gg · T1 · Z))]
Available flowq = 1360 · Fp · Cv · P1 · Y · √(xeff / (Gg · T1 · Z))

References, conventions, and revision

  • Calculation structure follows the compressible-fluid method described by ANSI/ISA-75.01.01 / IEC 60534-2-1. This beta omits several manufacturer-specific corrections.
  • Pressure conversions use 1 standard atmosphere = 14.6959 psi, consistent with the NIST pressure conversion reference.
  • Preset gas values are approximate ambient-condition screening values. Molecular and heat-capacity data can be checked through the NIST Chemistry WebBook. Natural-gas composition is project-specific.
  • Website standard-flow convention: 60°F and 14.696 psia. Confirm that this matches the project, contract, meter, and vendor basis.

Calculator version: 0.3.0 · Revision date: 2026-08-30

Preliminary engineering calculation only. Excludes Reynolds correction, derived xTP, valve travel, noise prediction, trim selection, and manufacturer-specific corrections. Confirm gas properties and valve coefficients with the selected manufacturer.