INGENIA

ENV-28

Carman–Kozeny filter

ΔP/L = 180 μ (1−ε)² u /(dp² ε³). Laminar packed-bed headloss.

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FiltrationCarman–Kozeny

Governing equation

ΔPL=180μ(1ε)2udp2ε3\dfrac{\Delta P}{L}=180\dfrac{\mu(1-\varepsilon)^2 u}{d_p^2\varepsilon^3}

where

\mu
Viscosity (mPa·s)
\varepsilon
Porosity ()
u
Approach velocity (mm/s)
d_p
Grain diameter (mm)
L
Bed depth (m)
\Delta P
Pressure drop (kPa)

Lecture brief

Historical brief

Streeter–Phelps (1925) oxygen sag, settling theory and Guldberg–Waage kinetics made water and air quality a rate problem. The lab computes sag, overflow and a snapshot of reactor mass balance. This sheet (ENV-28 — Carman–Kozeny filter) is the form associated with Carman–Kozeny. Working symbols: μ\mu, ε\varepsilon, uu, dpd_p, LL \rightarrow ΔP\Delta P. Kozeny treated the bed as a bundle of hydraulic capillaries; Carman set the constant at 180 for spheres.

Purpose

Purpose: compute ΔP\Delta P from μ\mu, ε\varepsilon, uu, dpd_p, LL in Environmental via ΔPL=180μ(1ε)2udp2ε3\dfrac{\Delta P}{L}=180\dfrac{\mu(1-\varepsilon)^2 u}{d_p^2\varepsilon^3} ΔP/L = 180 μ (1−ε)² u /(dp² ε³). Laminar packed-bed headloss. Use it when a real environmental question must be answered in SI before a code check.

Live realistic example

In symbols

Live case. Given μ=1.000mPas\mu = 1.000\,\mathrm{mPa·s}, ε=0.400\varepsilon = 0.400\,\mathrm{—}, u=2.000mm/su = 2.000\,\mathrm{mm/s}, dp=0.600mmd_p = 0.600\,\mathrm{mm}, L=0.800mL = 0.800\,\mathrm{m}, the governing relation ΔPL=180μ(1ε)2udp2ε3\dfrac{\Delta P}{L}=180\dfrac{\mu(1-\varepsilon)^2 u}{d_p^2\varepsilon^3} yields ΔP=4.500kPa\Delta P = 4.500\,\mathrm{kPa}. A sand bed, a seepage arrow, a head drop. Move a slider: the numbers are this situation, not a canned story.

Calculator

Inputs

Outputs

  • Pressure drop \Delta P4.500 kPa
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ENV-28 · pipe
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Narration of this film

A sand bed, a seepage arrow, a head drop.

Kozeny treated the bed as a bundle of hydraulic capillaries; Carman set the constant at 180 for spheres.

Reading speed

Watch on YouTube