Isotherm
Consider a surface:
Definition:q0, q1, ..., qn = Surface area (cm-2) covered by 0, 1, ..., n layers of adsorbed molecules.
At Equilibrium:q0 must remain constant. . Rate of Evaporation Rate of Condensation . . = from First Layer onto Bare Surface
Similarly, at equilibrium q1 must remain constant. . Rate of Condensation Rate of Condensation . . on the Bare Surface on the 1st Layer + = + Rate of Evaporation Rate of Evaporation from the second layer from the second layer . . . k1Pq0 + k-2q2 = k2Pq1 + k-1q1
Substituting into (I) gives
k-2q2 = k2Pq1
Extending this argument to other layers,
Definitions:
Total surface area of the catalyst,
Total volume of gas adsorbed on surface
where v0 is the volume of gas adsorbed on one square centimeter of surface when it is covered with a complete layer. . . .
where vm is the volume of gas adsorbed when the entire surface is covered with a complete monolayer.
From (I),
If we assume that the properties of the 1st, 2nd, ... layers are equivalent, then,
Similarly,q3 =xq2 =x2q1
Generally,qi =xqi-1 =xi-1q1 =xi-1yq0 =cxiq0 {c=x/y}
Substituting into (V),
Now,
Also, . . .
At saturation pressure of gas P0, an infinite number of adsorbate layers must build up on the surface. From equation VII, for this to be possible,
must be infinite. This means that at P0, x must equal 1. . . . g = P0(From definition of x) . . . x = P/P0
Substituting into VII, we arrive at the recognized form of the BET isotherm,
This can be rearranged to give,
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There is no such equation. The main reason is that there is no relationship between current and frequency.
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