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Steam Pipe Pressure Drop

Reference data and engineering information about steam pipe pressure drop for fluid mechanics applications.

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Overview

Engineering reference data for Steam Pipe Pressure Drop 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

Symbol Description Unit
ReRe Reynolds number
ρ\rho Fluid density kg/m³
vv Flow velocity m/s
DD Characteristic dimension m
μ\mu Dynamic viscosity Pa·s
PP Pressure Pa
ff Darcy friction factor

Imperial Units Correction Factors

For steam pressures other than 100 psi, adjust the estimated pressure drop by the corresponding factor from the table below.

Metric Units Correction Factors

For steam pressures other than 7 bar, multiply the estimated pressure drop by the corresponding factor.

Unit Conversions

Key conversions between Imperial and SI units for steam system calculations.

Mass Flow Rate

  • 1 lbs/hr=1.26×104 kg/s1 \text{ lbs/hr} = 1.26 \times 10^{-4} \text{ kg/s}
  • 1 kg/h=2.778×104 kg/s=3.67×102 lb/min1 \text{ kg/h} = 2.778 \times 10^{-4} \text{ kg/s} = 3.67 \times 10^{-2} \text{ lb/min}

Pressure

  • 1 psi (lb/in2)=6,894.8 Pa (N/m2)=0.06895 atm=14.50 bar1 \text{ psi (lb/in}^2\text{)} = 6,894.8 \text{ Pa (N/m}^2\text{)} = 0.06895 \text{ atm} = 14.50 \text{ bar}
  • 1 bar=105 Pa=14.50 psi1 \text{ bar} = 10^5 \text{ Pa} = 14.50 \text{ psi}

Interactive Charts

References