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Chemical

Steady diffusion flux through a plane layer

Molar flux of a species through a flat layer in steady one-dimensional diffusion with a straight concentration profile.

Ref
CHE-07
Rev
v1
Field
Chemical
Result
JA [mmol/(m² s)]

Fick’s first law says a species diffuses from high to low concentration at a rate proportional to the gradient. For steady one-dimensional diffusion through a plane layer of thickness L with concentrations C₁ and C₂ at the two faces, the profile is a straight line and the molar flux is J = D(C₁ − C₂)/L. The diffusion coefficient D is about 10⁻⁹ m²/s for a solute in liquid and about 10⁻⁵ m²/s for a gas in a gas. The flux is shown in mmol/(m² s).

Molar flux of a species through a flat layer in steady one-dimensional diffusion with a straight concentration profile. It points from the high-concentration face to the low-concentration face.

Calculator

Solve for
mmol/(m² s)
10⁻⁹ m²/s
0.01100
mol/m³
01,000
mol/m³
01,000
mm
0.0150
  • Flux in mol/(m² s)1.6×10−4 mol/(m² s)
  • Concentration gradient, (C₁ − C₂)/L80,000 mol/m⁴
  • Characteristic diffusion time, L²/D500 s

What drives the result

Each variable is moved across its typical range while the others stay at the values above. The longest bar is the key driver.

Molar flux (mmol/(m² s)) current value 0.16 mmol/(m² s)
LLayer thicknessKey driver
0.003216
DABDiffusion coefficient
8e-48
CA,1Concentration at face 1
−0.041.96
CA,2Concentration at face 2
−1.80.2
  • A concentration drop of 80 mol/m³ across 1 mm with D = 2 × 10⁻⁹ m²/s drives a flux of 0.16 mmol/(m² s).
  • The characteristic diffusion time L²/D is 500 s: halving the thickness cuts it by a factor of four, which is why thin membranes respond quickly while thick ones take a long time to reach steady state.
Chart data as tables

Ranked variables

VariableTypical rangeLowest resultHighest resultSwing (mmol/(m² s))Local stepChange in result
L Layer thickness0.01 to 50 mm0.00321616+10%−9.09 %
DAB Diffusion coefficient0.01 to 100 10⁻⁹ m²/s8e-487.999+10%+10 %
CA,1 Concentration at face 10 to 1,000 mol/m³−0.041.962+10%+12.5 %
CA,2 Concentration at face 20 to 1,000 mol/m³−1.80.22+10%−2.5 %

Sweep of Layer thickness

Layer thickness (mm)Molar flux (mmol/(m² s))
0.0116
0.0295.518
0.084091.903
0.24380.6562
0.70710.2263
2.050.07803
5.9460.02691
17.240.009279
500.0032

Sweep one variable

Molar flux (mmol/(m² s))Hover, touch, or use the arrow keys on the chart
051015 0.010.1110 Layer thickness (mm), log scale now 0.16

Variables and how each one contributes

JA

Molar flux

Result · mmol/(m² s)

What the equation gives you. Everything else feeds it.

DAB

Diffusion coefficient

10⁻⁹ m²/s · typical 0.01 to 100

The diffusion coefficient of the species in the layer, in units of 10⁻⁹ m²/s. Raises the flux in direct proportion. Raising it by 0.5 (to 2.5) moves the result by +25 %, from 0.16 to 0.2 mmol/(m² s).

CA,1

Concentration at face 1

mol/m³ · typical 0 to 1,000

The concentration of the species at face 1 (high side), in mol/m³. Raises the flux in direct proportion to the concentration drop. Raising it by 10 (to 110) moves the result by +12.5 %, from 0.16 to 0.18 mmol/(m² s).

CA,2

Concentration at face 2

mol/m³ · typical 0 to 1,000

The concentration at face 2 (low side), in mol/m³. Lowers the flux: the driving concentration difference becomes smaller. Raising it by 10 (to 30) moves the result by −12.5 %, from 0.16 to 0.14 mmol/(m² s).

L

Layer thickness

mm · typical 0.01 to 50

The thickness of the layer, in mm. Lowers the flux in inverse proportion: a thicker layer means a gentler gradient. Raising it by 0.25 mm (to 1.25 mm) moves the result by −20 %, from 0.16 to 0.128 mmol/(m² s).

Worked example with the values above

  1. Concentration drop: C₁ − C₂ = 100 − 20 = 80 mol/m³; thickness L = 0.001 m.
  2. Gradient: 80 / 0.001 = 80,000 mol/m⁴; D = 2×10−9 m²/s.
  3. J = 2×10−9 × 80,000 = 1.6×10−4 mol/(m² s) = 0.16 mmol/(m² s).

Assumptions and limits

  • Steady, one-dimensional diffusion through a uniform layer with constant D, and a linear concentration profile.
  • No reaction in the layer and negligible bulk flow.

Common mistakes

  • Using the bulk concentrations when the layer interface has a different (equilibrium) concentration.
  • Mixing mm and m, or mol/dm³ and mol/m³.

Statistics and uncertainty

Diffusion coefficients depend on temperature (they roughly double for every 20 to 30 K in liquids) and are known to ±10 % at best, so the flux is no better. For a membrane, the surface concentrations are set by solubility rather than the bulk concentrations, which can change the result greatly.

Where it is used

  • Gas or moisture permeation through a film, seal or wall, and the transfer rate in a membrane.
  • Estimating the rate of diffusion-limited processes in chemical engineering.

Maths you need

  • Concentration gradient: change of concentration over distance
  • Molar flux: moles per unit area per unit time

Related formulas

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