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3.8 Fick's Law of Diffusion<br />

Analogous to Fourier's law of heat conduction (Equation 3.1) and the equation for shear<br />

stress in shear flow, the diffusion rate in mass transfer is given by Fick's law. This can be<br />

written as [16]<br />

where<br />

mA = mass flux per unit time<br />

A - Area<br />

D^B = diffusion coefficient of the constituent A in constituent B<br />

cA = mass concentration of component A per unit volume<br />

x = distance.<br />

The governing expression for the transient rate of diffusion is [2]<br />

where<br />

t = time<br />

x = distance<br />

(3.72)<br />

(3.73)<br />

The desorption of volatile or gaseous components from a molten polymer in an extruder<br />

can be calculated from [17] using Equation 3.73<br />

where<br />

^1 = rate of desorption (g/s)<br />

Ac = area of desorption (cm 2 )<br />

C0 = initial concentration of the volatile component (g/cm 3 ) in the polymer<br />

D = diffusion coefficient (cm 2 /s)<br />

t - time of exposure (s) of the polymer to the surrounding atmosphere<br />

3.8.1 Permeability<br />

(3.74)<br />

Plastics are permeable by gases, vapors and liquids to a certain extent. The dififiisional<br />

characteristics of polymers can be described in terms of a quantity known as permeability.

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