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Control Valves Steam

Reference data and engineering information about control valves steam for fluid mechanics applications.

controlvalvessteam

Overview

Engineering reference data for Control Valves Steam in fluid mechanics.

Key Formulas

Reynolds Number

Re=ρvDμRe = \frac{\rho v D}{\mu}

Ratio of inertial to viscous forces — determines flow regime.

Bernoulli's Equation

P+12ρv2+ρgh=constP + \frac{1}{2}\rho v^2 + \rho g h = \text{const}

Conservation of energy for steady, inviscid, incompressible flow.

Continuity Equation

A1v1=A2v2A_1 v_1 = A_2 v_2

Conservation of mass for incompressible flow.

Darcy-Weisbach

ΔP=fLDρv22\Delta P = f \frac{L}{D} \frac{\rho v^2}{2}

Pressure drop due to friction in a pipe.

Variables

SymbolDescriptionUnit
ReReReynolds number
ρ\rhoFluid densitykg/m³
vvFlow velocitym/s
DDCharacteristic dimensionm
μ\muDynamic viscosityPa·s
PPPressurePa
ffDarcy friction factor

Steam Control Valve Design Procedure

The proper sizing of steam control valves follows a two-step processType:

  1. Determine the Pressure Coefficient (Pcoef) from the absolute inlet pressure and allowable pressure drop
  2. Select the Flow Factor (Kv) using Pcoef and the required steam flow rate

Pressure Coefficient Formula

Pcoef=ΔPvP_{coef} = \frac{\Delta P}{v}

Where:

  • PcoefP_{coef} = pressure coefficient
  • ΔP\Delta P = pressure drop across the valve (bar)
  • vv = specific volume of steam at inlet conditions (m³/kg)

Critical Pressure Drop Limitation

Important: The pressure drop across a control valve cannot exceed the critical pressure drop, which is approximately 42% of the absolute inlet pressure. Attempting to exceed this limit will result in choked flow and loss of control capability.

Pressure Coefficient Reference Table

15 rows
Pressure Coefficient (Pcoef) values for saturated steam at various pressure drops
Absolute Pressure (bar)
Specific Volume (m³/kg)
ΔP = 0.5 bar
ΔP = 1 bar
ΔP = 1.5 bar
ΔP = 2 bar
ΔP = 2.5 bar
ΔP = 3 bar
ΔP = 3.5 bar
ΔP = 4 bar
ΔP = 4.5 bar
ΔP = 5 bar
ΔP = 5.5 bar
ΔP = 6 bar
ΔP = 6.5 bar
ΔP = 7 bar
ΔP = 7.5 bar
11.690.3
20.890.561.12
30.610.821.642.46
40.451.112.223.334.44
50.381.322.633.955.266.58
60.321.563.134.696.257.819.38
70.271.853.75.567.419.2611.113
80.242.084.176.258.3310.4212.514.616.7
90.212.384.767.149.5211.914.316.719.121.4
100.192.635.267.8910.5313.1615.818.421.123.726.3
110.182.785.568.3311.1113.8916.719.422.22527.830.6
120.163.136.259.3812.515.6318.721.92528.131.334.437.5
130.153.336.671013.3316.672023.326.73033.336.74043.3
140.143.577.1410.7114.2917.8621.42528.632.135.739.342.946.450
150.133.857.6911.5415.3819.2323.126.930.834.638.542.346.25053.957.7

Source: engineeringtoolbox.com

Flow Factor Reference Table

Interactive Charts

Control Valves - Adding Flow Coefficients for Valves in Series or Parallel

References