AutoEngCalc - Engineering Calculators

Safety Valve Capacity Calculator

ASME Section VIII compliant calculations for gas, liquid, and two-phase flow. Calculate required orifice area and capacity for pressure relief valves.

Safety Valve: P=150 psig, W=10000 lb/hr
A = 0.196 in²

Safety Valve Capacity Calculator

ASME Section VIII compliant calculations for gas, liquid, and two-phase flow

Gas Service

Calculate required orifice area for gas flow per ASME Section VIII

psig
Typical range: 50 - 1000 psig
psig
Typical range: 0 - 100 psig
°F
Typical range: -50 to 500 °F
kg/kmol
Air: 28.97, Steam: 18.02
Air: 1.4, Steam: 1.33
Typically 1.0 for ideal gases
lb/hr
Typical range: 1000 - 50000 lb/hr

Liquid Service

Calculate required orifice area for liquid flow per ASME Section VIII

psig
psig
°F
lb/ft³
cP
gpm

Two-Phase Flow

Calculate required orifice area for two-phase flow using HEM

psig
psig
°F
lb/ft³
lb/ft³
lb/hr

Safety Valve Results

Required Orifice Area

-

in²

Flow Type

-

Critical/Subcritical

Capacity Factor

-

Kb/Kw

Compliance

-

ASME Section VIII

Critical Flow Pressure

-

psig

Back Pressure Ratio

-

P2/P1

Reynolds Number

-

Dimensionless

Omega Parameter

-

Two-Phase Flow

Safety Valve Inlet Outlet
Safety Valve Diagram Visualization

Safety Valve Capacity Calculations

ASME Section VIII Compliance

ASME Boiler and Pressure Vessel Code, Section VIII specifies requirements for pressure relief devices. Calculations account for back pressure, fluid properties, and flow conditions.

A = W / (C × K × P × √(MW / (Z × T)))

Where A is orifice area (in²), W is flow rate (lb/hr), C is gas constant, K is capacity correction factor, P is relief pressure (psia), MW is molecular weight, Z is compressibility factor, and T is temperature (°R).

Flow Types & Corrections

Different flow regimes require specific calculation approaches:

  • Critical Flow: Occurs when downstream pressure ≤ critical flow pressure
  • Subcritical Flow: Requires back pressure correction factor
  • Two-Phase Flow: Uses Homogeneous Equilibrium Model (HEM)
  • Viscosity Effects: Reynolds number determines viscosity corrections

Additional Pressure Safety Resources

Pressure Vessel Design

Wall thickness and MAWP calculations

Piping System Analysis

Pressure drop and flow calculations

Thermal Relief

Thermal expansion calculations

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