Diffusion:
Fick’s laws
Principle
Fick's first law
Fick's first law is used in steady-state diffusion (see Diffusion:
general), i.e., when the concentration within the diffusion volume does not
change with respect to time (Jin = Jout).
, (1)
where
J is the
diffusion flux in dimensions of (mol m-2 s-1);
D is the diffusion coefficient or diffusivity, (m2 s-1);
φ is the
concentration (mol m-3);
x is the position (m).
D is
proportional to the velocity of the diffusing particles, which depends on the
temperature, viscosity of the fluid and the size of the particles according to
the Stokes-Einstein relation. For the biological molecules the diffusion coefficient
normally ranges from 10-11 to 10-
Fick's second law is used in non-steady or continually
changing state diffusion, i.e., when the concentration within the diffusion
volume changes with respect to time.
, (2)
Where:
φ is the concentration (mol m-3);
t is time (s);
D is the constant
diffusion coefficient (m2 s-1);
x is the position (m).
With some calculation, it can be derived from the First Fick's
law and the mass balance.
Application
Equations based on Fick's law have been commonly used to
model transport processes in foods, porous soils, semiconductor doping process,
etc.. In biomedicine, transport of biopolymers, pharmaceuticals, in neurons,
etc. are modeled with the Fick equations.
Typically, a compound's D is ~10,000x greater in air than
in water. CO2 in air has a diffusion coefficient of 16 mm˛/s, and in
water, its coefficient is 0.0016 mm˛/s.
Physiological examples
For example for the steady states, when concentration
does not change by time, the left part of the above equation will be zero and
therefore in one dimension and when D is
constant, the equation (2) becomes 0 = D dφ/dx2. The solution
for the concentration φ will be the linear change of concentrations along x. This is what by
approximation happens in the alveolar-capillary membrane and with diffusion of
particles from the liquid to liquid phase in the wall of capillaries in the
tissues.
Biological perspective
The first law gives rise to the following formula:
Rate of diffusion
= KA(P2 – P1)
It states that the rate of diffusion of a gas across a
membrane is:
· Constant
for a given gas at a given temperature by an experimentally determined factor, K
· Proportional
to the surface area over which diffusion is taking place, A
· Proportional
to the difference in partial pressures of the gas across the membrane, P2
− P1
It is also inversely proportional to the distance over
which diffusion must take place, or in other words the thickness of the
membrane. The factor K comprises this thickness.
The exchange rate of a gas across a fluid membrane can be
determined by using this law together with Graham's
law.
More Info
Temperature
dependence of the diffusion coefficient
The diffusion coefficient at different temperatures is
often found to be well predicted by
, (5)
where:
D0 is
the maximum diffusion coefficient at infinite temperature,
EA is
the activation energy for diffusion (J/mol),
T is absolute temperature
(K),
R is the gas
constant in dimensions of (J/(K∙mol)).
3D diffusion
For the case of 3-dimensional diffusion the Second Fick's
Law looks like:
(3)
where
is the
,
where i, j and k are the unit-vectors in the direction of
the respective coordinate (the standard basis in R3).
Finally if the diffusion coefficient is not a constant,
but depends upon the coordinate and/or concentration, the Second Fick's Law
looks like:
. (4)