INGENIA

FLD-22

Darcy friction pressure drop

Δp = f (L/D) (ρ v² / 2). The Darcy–Weisbach pipe formula in pascals.

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FluidsDarcy

Governing equation

Δp=fLDρv22\Delta p=f\dfrac{L}{D}\dfrac{\rho v^2}{2}

v∈[0.1,12]v \in \left[0.1, 12\right]

where

f
Friction factor (—)
L
Length (m)
D
Diameter (m)
\rho
Density (kg/m³)
v
Speed (m/s)
\Delta p
Pressure drop (kPa)

The figure, part by part

Each numbered marker wears the color of its card. Hover a card to light the marker. Tap a marker to jump to that card. The slider walks a red point along the curve; Animate drawing traces it like a pen.

FLD-22 · pipe
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①

Governing law — red

Δp=fLDρv22\Delta p=f\dfrac{L}{D}\dfrac{\rho v^2}{2}

v∈[0.1,12]v \in \left[0.1, 12\right]

v=0.1v = 0.1Δp=0.04\Delta p = 0.04

②

Domain of the variable — blue

vmin⁡=0.1,vmax⁡=12v_{\min} = 0.1,\quad v_{\max} = 12

v∈[0.1,12]v \in \left[0.1, 12\right]

v=0.1v = 0.1v=0.1v = 0.1

③

Response curve — green

Δp=fLDρv22\Delta p=f\dfrac{L}{D}\dfrac{\rho v^2}{2}

v∈[0.1,12]v \in \left[0.1, 12\right]

v=0.1v = 0.1Δp=0.04\Delta p = 0.04

④

Rate of change — amber

dΔpdv\frac{\mathrm{d}\Delta p}{\mathrm{d}v}

v∈[0.1,12]v \in \left[0.1, 12\right]

v=0.175v = 0.175Δp′=1.399\Delta p^{\prime} = 1.399

Lecture brief

Historical brief

Bernoulli, Navier–Stokes, Reynolds (1883) and Stokes drag made continuum flow a dimensionless craft. The sheets compute head, drag, Re and a pedagogical NS snapshot. This sheet (FLD-22 — Darcy friction pressure drop) is the form associated with Darcy. Working symbols: ff, LL, DD, ρ\rho, vv →\rightarrow Δp\Delta p. Laminar f = 64/Re. Turbulent f from Moody, a function of Re and ε/D.

Purpose

Purpose: compute Δp\Delta p from ff, LL, DD, ρ\rho, vv in Fluid physics via Δp=fLDρv22\Delta p=f\dfrac{L}{D}\dfrac{\rho v^2}{2} Δp = f (L/D) (ρ v² / 2). The Darcy–Weisbach pipe formula in pascals. Use it when a real fluid physics question must be answered in SI before a code check.

Live realistic example

In symbols

Live case. Given f=0.020 —f = 0.020\,\mathrm{—}, L=80.000 mL = 80.000\,\mathrm{m}, D=0.200 mD = 0.200\,\mathrm{m}, ρ=1000.000 kg/m3\rho = 1000.000\,\mathrm{kg/m^{3}}, v=2.000 m/sv = 2.000\,\mathrm{m/s}, the governing relation Δp=fLDρv22\Delta p=f\dfrac{L}{D}\dfrac{\rho v^2}{2} yields Δp=16.00 kPa\Delta p = 16.00\,\mathrm{kPa}. A long pipe, wall roughness, a falling p. Move a slider: the numbers are this situation, not a canned story.

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Inputs

Outputs

  • Pressure drop \Delta p16.00 kPa
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FLD-22 · pipe
00:0 / 00:08

Narration of this film

A long pipe, wall roughness, a falling p.

Laminar f = 64/Re. Turbulent f from Moody, a function of Re and ε/D.

Reading speed

Watch on YouTube