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Fick's First Law of Diffusion

Relates the diffusive molar flux of a species to the concentration gradient driving it across a stagnant medium.

Chemical EngineeringMass TransferProcess Design

Fick's First Law CalculatorJ = −D · (dC/dx)

J = −D · (ΔC/Δx)
D = diffusion coefficient (m²/s)  ·  ΔC = concentration difference (mol/m³)  ·  Δx = distance (m)
⟹ JD, ΔC, Δx
m²/s
mol/m³
m
mol/m²·s
Common:
Solve for:
Flux (J)
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Flux Magnitude
Low (<1e-8) Medium (1e-8–1e-6) High (1e-6–1e-4) Very High (>1e-4)
J vs. ΔCfixed D, Δx
J = −D·(ΔC/Δx) Computed point
J = −D · (ΔC/Δx)  ·  Flux in mol/m²·s

Interpretation

Fick's first law (duplicate): J = −D·(dC/dx). Flux is proportional to concentration gradient. See id=30 for full explanation.

J = -D * (dC/dx)
Fick's First Law of Diffusion

Variables

SymbolQuantityUnit
JDiffusive molar fluxmol/m2.s
DDiffusion coefficientm2/s
dC/dxConcentration gradientmol/m3 per m

What it means

This is a duplicate entry of Fick’s first law (see id=30). For completeness, the law is repeated here. Fick’s first law is the fundamental equation for diffusive mass transfer. It states that the molar flux J of a species is proportional to the negative of the concentration gradient, with the diffusion coefficient D as the constant of proportionality. It is applicable to steady‑state diffusion and forms the basis of many mass transfer models. In practice, it is used to determine the rate of diffusion of gases through porous media, diffusion of solutes in liquids, and diffusion of atoms in solids. It is also used in the design of membrane separation processes and in understanding drug release from pharmaceutical formulations. The law is named after Adolf Fick, who first formulated it in 1855.

Worked example

Fick's First Law – Two Examples

Real‑World
Scenario: D = 1×10⁻⁹ m²/s, dC/dx = 1000 mol/m⁴. Compute molar flux J.
ParameterValue
D1×10⁻⁹ m²/s
dC/dx1000 mol/m⁴
1J = -1e-9 × 1000 = -1×10⁻⁶ mol/m²·s
Result J = -1×10⁻⁶ mol/m²·s ✓ Negative flux
Scenario: D = 1.5×10⁻⁵ m²/s, dC/dx = 200 mol/m⁴. Find J.
ParameterValue
D1.5×10⁻⁵ m²/s
dC/dx200 mol/m⁴
1J = -1.5e-5 × 200 = -0.003 mol/m²·s
Result J = -0.003 mol/m²·s ✓ Higher flux
Key insight: Flux goes from high to low concentration; negative sign indicates direction.

Common mistakes

  • Duplicate of ID 30 – see that entry.
  • Note: Ensure you update the correct ID if you intend to keep separate content; otherwise, use the same as ID 30.

Applications

Fick's first law (as noted) is fundamental for diffusion analysis. Its duplicate entry reinforces the importance of this law in chemical engineering. It remains a cornerstone for modelling mass transfer in membranes, porous catalysts, biological tissues, and environmental systems. By applying Fick's law, engineers can design gas separation membranes, predict the release of active ingredients in pharmaceuticals, and model the spread of pollutants in air and water. The law also underlies the design of diffusion‑limited reactors and the analysis of corrosion and oxidation processes. Despite its simplicity, it provides a reliable starting point for more complex transport phenomena.

  • Same applications as id=30: membrane separations, catalysis, drug delivery, corrosion, environmental transport

Frequently Asked Questions

Q01What is the physical meaning of Fick's first law?
A01

Fick's first law states that the diffusive flux is proportional to the concentration gradient: J = –D·(dC/dx). It describes the spontaneous movement of molecules from regions of higher concentration to lower concentration, driven by the gradient.

Q02What are the units of the diffusion coefficient D?
A02

In SI, D has units of m²/s. Other common units are cm²/s (1 cm²/s = 10⁻⁴ m²/s).

Q03How does the diffusion coefficient vary with temperature?
A03

D generally increases with temperature, following an Arrhenius‑type equation: D = D₀·exp(–E_d/(RT)). This is used to estimate D at different temperatures.

Q04What is the difference between molecular diffusion and eddy diffusion?
A04

Molecular diffusion occurs due to random thermal motion of molecules. Eddy diffusion (turbulent diffusion) occurs in turbulent flow and is much faster; it is described by an eddy diffusivity that is not a material property.

Q05What are the typical values of D for gases and liquids?
A05

In gases, D is of the order 10⁻⁵ m²/s; in liquids, about 10⁻⁹ m²/s; in solids, 10⁻¹² to 10⁻¹⁶ m²/s. The large difference is due to the closer packing and stronger interactions in condensed phases.

Q06How do you apply Fick's law to a steady‑state membrane permeation problem?
A06

For a membrane of thickness δ, with concentrations C₁ and C₂ on the two sides, the flux is J = –D·(C₂ – C₁)/δ (assuming linear gradient). This is used to calculate permeability.

Q07What are the common mistakes when using Fick's first law?
A07

  • Using the law in a transient situation without the time derivative.
  • Ignoring the effect of temperature on D.
  • Assuming D is constant when it depends on concentration (non‑Fickian diffusion).
  • Forgetting to include the negative sign, leading to a sign error in the flux direction.

Q08What is the relationship between Fick's law and the Einstein‑Smoluchowski equation?
A08

The diffusion coefficient is related to the mean squared displacement of particles: D = ⟨x²⟩/(2t) in one dimension (Einstein relation). This connects macroscopic diffusion to microscopic particle motion.