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Free Fick's law calculator for diffusion flux, mass transfer rate, and concentration gradient calculations with step-by-step solutionsfor chemistry and physics. Perfect for students learning molecular transport phenomena.
Last updated: February 2, 2026
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Diffusion Flux:
-1.000e-7 mol/(m²⋅s)
Diffusion Flux
Formula: J = -D × (dC/dx)
Diffusion Flux:
-1.000e-7 mol/(m²⋅s)
Mass Transfer Rate:
-1.000e-9 mol/s
Concentration Difference:
1.000e+0 mol/m³
Formula
J = -D × (dC/dx)
Mass transfer rate per unit area
Formula
ṁ = -D × A × (dC/dx)
Total mass transfer rate
Formula
dC/dx = -J / D
Rate of concentration change
Example
Controlled release from polymer matrix
D = 10⁻¹² m²/s, gradient = 1000 mol/m⁴
Example
Water purification through membrane
D = 10⁻⁹ m²/s, A = 1 m², gradient = 10 mol/m⁴
Example
Contaminant diffusion in groundwater
D = 10⁻¹⁰ m²/s, gradient = 0.1 mol/m⁴
Fick's law with D = 1.0 × 10⁻⁹ m²/s, dC/dx = 100 mol/m⁴, A = 0.01 m²:
Diffusion Flux
-1.0 × 10⁻⁷ mol/(m²⋅s)
Mass Transfer Rate
-1.0 × 10⁻⁹ mol/s
Concentration Difference
0.001 mol/m³
Fick's law is a fundamental principle in mass transfer that describes how particles diffuse from regions of high concentration to regions of low concentration. Understanding this law is essential for chemistry, chemical engineering, and materials sciencewhere molecular transport phenomena are important.
This systematic approach ensures accurate Fick's law calculations for any mass transfer problem.
The three main formulas are: J = -D × (dC/dx) for diffusion flux, ṁ = J × A = -D × A × (dC/dx) for mass transfer rate, and dC/dx = -J / D for concentration gradient. The negative sign indicates that flux is opposite to the concentration gradient direction. The diffusion coefficient depends on temperature, pressure, and molecular properties.
Need help with other chemistry topics? Check out our free fall calculator and derivative calculator.
Get Custom Calculator for Your PlatformDiffusion coefficient (D) = 1.0 × 10⁻⁹ m²/s
Concentration gradient (dC/dx) = 100 mol/m⁴
Area (A) = 0.01 m²
Calculation type = Diffusion flux
Final Results:
Diffusion Flux
-1.000e-7 mol/(m²⋅s)
Mass Transfer Rate
-1.000e-9 mol/s
Concentration Difference
1.000e+0 mol/m³
Diffusion Coefficient
1.0 × 10⁻⁹ m²/s
D = 10⁻¹² m²/s, dC/dx = 1000 mol/m⁴, A = 0.001 m²
J = -1.0 × 10⁻⁹ mol/(m²⋅s)
D = 10⁻⁹ m²/s, dC/dx = 10 mol/m⁴, A = 1 m²
ṁ = -1.0 × 10⁻⁸ mol/s
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