INGENIA

ENV-38

Fick diffusive flux

J = −D (C2−C1)/Δx. Steady one-dimensional diffusion.

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Water qualityFick 1855

Governing equation

J=−DC2−C1ΔxJ=-D\dfrac{C_2-C_1}{\Delta x}

Δx∈[0.001,2]\Delta x \in \left[0.001, 2\right]

where

D
Diffusivity (m²/s)
C_1
Conc. 1 (mg/L)
C_2
Conc. 2 (mg/L)
\Delta x
Distance (m)
J
Flux toward 2 (mg/(m²·s))

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.

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①

Governing law — red

J=−DC2−C1ΔxJ=-D\dfrac{C_2-C_1}{\Delta x}

Δx∈[0.001,2]\Delta x \in \left[0.001, 2\right]

Δx=0.001\Delta x = 0.001J=0.008J = 0.008

②

Domain of the variable — blue

Δxmin⁡=0.001,Δxmax⁡=2\Delta x_{\min} = 0.001,\quad \Delta x_{\max} = 2

Δx∈[0.001,2]\Delta x \in \left[0.001, 2\right]

Δx=0.001\Delta x = 0.001Δx=0.001\Delta x = 0.001

③

Response curve — green

J=−DC2−C1ΔxJ=-D\dfrac{C_2-C_1}{\Delta x}

Δx∈[0.001,2]\Delta x \in \left[0.001, 2\right]

Δx=0.001\Delta x = 0.001J=0.008J = 0.008

④

Rate of change — amber

dJdΔx\frac{\mathrm{d}J}{\mathrm{d}\Delta x}

Δx∈[0.001,2]\Delta x \in \left[0.001, 2\right]

Δx=0.014\Delta x = 0.014J′=−0.306J^{\prime} = -0.306

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-38 — Fick diffusive flux) is the form associated with Fick 1855. Working symbols: DD, C1C_1, C2C_2, Δx\Delta x →\rightarrow JJ. Fick's first law: flux is minus diffusivity times the concentration gradient. The start of mixing models.

Purpose

Purpose: compute JJ from DD, C1C_1, C2C_2, Δx\Delta x in Environmental via J=−DC2−C1ΔxJ=-D\dfrac{C_2-C_1}{\Delta x} J = −D (C2−C1)/Δx. Steady one-dimensional diffusion. Use it when a real environmental question must be answered in SI before a code check.

Live realistic example

In symbols

Live case. Given D=1.000e−9 m2/sD = 1.000e-9\,\mathrm{m^{2}/s}, C1=10.000 mg/LC_1 = 10.000\,\mathrm{mg/L}, C2=2.000 mg/LC_2 = 2.000\,\mathrm{mg/L}, Δx=0.050 m\Delta x = 0.050\,\mathrm{m}, the governing relation J=−DC2−C1ΔxJ=-D\dfrac{C_2-C_1}{\Delta x} yields J=1.600e−4 mg/(m2⋅s)J = 1.600e-4\,\mathrm{mg/(m^{2}·s)}. Two wells, a gradient, a flux arrow. Move a slider: the numbers are this situation, not a canned story.

Calculator

Inputs

Outputs

  • Flux toward 2 J0.000160 mg/(m²·s)
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Narration of this film

Two wells, a gradient, a flux arrow.

Fick's first law: flux is minus diffusivity times the concentration gradient. The start of mixing models.

Reading speed

Watch on YouTube