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Pipes Series Parallel

Reference data and engineering information about pipes series parallel for fluid mechanics applications.

pipesseriesparallel

Overview

Engineering reference data for Pipes Series Parallel 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

Series and Parallel Pipe Networks

Understanding the configuration of pipe networks is crucial for calculating system pressure drop and flow distribution.

Pipes in Series

For pipes connected in series, the mass flow rate remains constant through each pipe segment, while the total pressure loss is the cumulative sum of individual losses.

Pressure Loss Relationship: Δptotal=Δp1+Δp2++Δpn\Delta p_{total} = \Delta p_1 + \Delta p_2 + \dots + \Delta p_n

Mass Flow Relationship: m˙total=m˙1=m˙2==m˙n\dot{m}_{total} = \dot{m}_1 = \dot{m}_2 = \dots = \dot{m}_n

Pipes in Parallel

For pipes connected in parallel, the pressure loss is identical across all parallel branches, while the total mass flow rate is the sum of flows through each branch.

Pressure Loss Relationship: Δptotal=Δp1=Δp2==Δpn\Delta p_{total} = \Delta p_1 = \Delta p_2 = \dots = \Delta p_n

Mass Flow Relationship: m˙total=m˙1+m˙2++m˙n\dot{m}_{total} = \dot{m}_1 + \dot{m}_2 + \dots + \dot{m}_n

Application Notes

  1. The individual pressure losses (Δp1,Δp2,...\Delta p_1, \Delta p_2, ...) can be calculated using appropriate pressure drop correlations such as the Darcy-Weisbach equation.
  2. These relationships apply to incompressible flow and assume no significant changes in kinetic or potential energy between junction points.
  3. For compressible flows or systems with significant elevation changes, energy balance equations must be used instead.

References