Concise Physical Chemistry

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c06 JWBS043-Rogers September 13, 2010 11:25 Printer Name: Yet to Come


88 THE GIBBS FREE ENERGY

4
2 2

2 3
1
1 bar 1 bar

(, ) (, )

(, ) (, )

G
AgpBgp

GG
G
AgpBgp

Δ

ΔΔ
Δ

↑↑


FIGURE 6.1 A reaction diagram forG 4.

Integrating to findG 2 , we obtain

G 2 =


∫Gp
2
G1bar

dG=RT

∫Gp
2
G1bar

dp
p

=RTln

p 2
1

where the pressure at the lower limit of integration is 1 bar. A similar equation
describesG 3. Combination ofG 1 ,G 2 , andG 3 with attention to the sign
differences givesG 4 , the desired change in the Gibbs function for reaction at the
new pressurep 2. One way of getting the signs straight is to set up the diagram as a
cyclic process, and remember that the sum of changes in any thermodynamic function
must be zero around a cycle.

6.5.1 The Equilibrium Constant as a Quotient of Quotients
In writing equilibrium constant expressions such asKeq=pB/pAfor a reaction
A → B in the gas phase, it should be remembered that the pressures are quotients
relative to a pressure in the standard statep/p 0 , hence they are unitless and so isKeq.
If the gas is not ideal, the fugacityfis used in place of the pressure or in the case
of liquids and solutions, the activityamay be used. Fugacities or activities are also
ratiosf/f 0 ora/a 0 relative to a standard state soKeqis still unitless, as it must be for
some of the mathematical manipulations to come. Changes toKeqexpressed in terms
of fugacities or activities bring about complication in the mathematical expression
and in the experimental determination of the quantities involved; but once again, the
principles are the same as in the ideal case.

6.6 THE TEMPERATURE DEPENDENCE OF THE FREE ENERGY


From the usual expression for the derivative of a quotient,

d

(u
v

)


dx

=


v

du
dx

−u

dv
dx
v^2

,


and stipulating constant pressure, we get

d

(


G


T


)


dT

=


T


(


dG
dT

)


−G


(


dT
dT

)


T^2


=


−TS−G


T^2

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