INGENIA

CHE-41

Ergun packed bed

Packed-bed pressure drop.

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GoverningErgun packed bed

Governing equation

ΔP/L=150μ(1−ϵ)2u/(ϵ3d2)+1.75ρ(1−ϵ)u2/(ϵ3d)\Delta P/L=150\mu(1-\epsilon)^2 u/(\epsilon^3 d^2)+1.75\rho(1-\epsilon)u^2/(\epsilon^3 d)

u∈[0.001,0.2]u \in \left[0.001, 0.2\right]

where

mu
mu (Pa·s)
eps
eps (—)
u
u (m/s)
d
d (mm)
rho
rho (kg/m³)
dP
Ergun packed bed (Pa/m)

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.

CHE-41 · pipe
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①

Governing law — red

ΔP/L=150μ(1−ϵ)2u/(ϵ3d2)+1.75ρ(1−ϵ)u2/(ϵ3d)\Delta P/L=150\mu(1-\epsilon)^2 u/(\epsilon^3 d^2)+1.75\rho(1-\epsilon)u^2/(\epsilon^3 d)

u∈[0.001,0.2]u \in \left[0.001, 0.2\right]

u=0.001u = 0.001dP=99.22dP = 99.22

②

Domain of the variable — blue

umin⁡=0.001,umax⁡=0.2u_{\min} = 0.001,\quad u_{\max} = 0.2

u∈[0.001,0.2]u \in \left[0.001, 0.2\right]

u=0.001u = 0.001u=0.001u = 0.001

③

Response curve — green

ΔP/L=150μ(1−ϵ)2u/(ϵ3d2)+1.75ρ(1−ϵ)u2/(ϵ3d)\Delta P/L=150\mu(1-\epsilon)^2 u/(\epsilon^3 d^2)+1.75\rho(1-\epsilon)u^2/(\epsilon^3 d)

u∈[0.001,0.2]u \in \left[0.001, 0.2\right]

u=0.001u = 0.001dP=99.22dP = 99.22

④

Rate of change — amber

ddPdu\frac{\mathrm{d}dP}{\mathrm{d}u}

u∈[0.001,0.2]u \in \left[0.001, 0.2\right]

u=0.002u = 0.002dP′=1.18×105dP^{\prime} = 1.18\times 10^{5}

Lecture brief

Historical brief

From CSTR/PFR mole balances and Arrhenius rates to McCabe–Thiele stages and NTU exchangers, chemical engineering is conservation plus equilibrium. The lab is that design arithmetic. This sheet (CHE-41 — Ergun packed bed) is the form associated with Ergun packed bed. Working symbols: mumu, epseps, uu, dd, rhorho →\rightarrow dPdP. Packed-bed pressure drop. Pedagogical SI sheet with a live model and a swept parameter.

Purpose

Purpose: compute dPdP from mumu, epseps, uu, dd, rhorho in Chemical engineering via ΔP/L=150μ(1−ϵ)2u/(ϵ3d2)+1.75ρ(1−ϵ)u2/(ϵ3d)\Delta P/L=150\mu(1-\epsilon)^2 u/(\epsilon^3 d^2)+1.75\rho(1-\epsilon)u^2/(\epsilon^3 d) Packed-bed pressure drop. Use it when a real chemical engineering question must be answered in SI before a code check.

Live realistic example

In symbols

Live case. Given mu=0.001 Pa⋅smu = 0.001\,\mathrm{Pa·s}, eps=0.400 —eps = 0.400\,\mathrm{—}, u=0.020 m/su = 0.020\,\mathrm{m/s}, d=3.000 mmd = 3.000\,\mathrm{mm}, rho=1000.000 kg/m3rho = 1000.000\,\mathrm{kg/m^{3}}, the governing relation ΔP/L=150μ(1−ϵ)2u/(ϵ3d2)+1.75ρ(1−ϵ)u2/(ϵ3d)\Delta P/L=150\mu(1-\epsilon)^2 u/(\epsilon^3 d^2)+1.75\rho(1-\epsilon)u^2/(\epsilon^3 d) yields dP=4062.500 Pa/mdP = 4062.500\,\mathrm{Pa/m}. One governing identity, SI units, a single sweep on the sheet. Move a slider: the numbers are this situation, not a canned story.

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Outputs

  • Ergun packed bed dP4062.500 Pa/m
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Narration of this film

One governing identity, SI units, a single sweep on the sheet.

Packed-bed pressure drop. Pedagogical SI sheet with a live model and a swept parameter.

Reading speed

Watch on YouTube