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32<br />

II Standards, conventions and contents <strong>of</strong> the tables<br />

gation <strong>of</strong> errors. In practice the parameters affected by the change between these two<br />

standard state pressures are the Gibbs energy and entropy changes <strong>of</strong> all processes that<br />

involve gaseous species. Consequently, changes occur also in the Gibbs energies <strong>of</strong><br />

formation <strong>of</strong> species that consist <strong>of</strong> elements whose reference state is gaseous (H, O, F,<br />

Cl, N, and the noble gases). No other thermodynamic quantities are affected significantly.<br />

A large part <strong>of</strong> the following discussion has been taken from the NBS tables <strong>of</strong><br />

chemical thermodynamic properties [1982WAG/EVA], see also Freeman [1984FRE].<br />

The following expressions define the effect <strong>of</strong> pressure on the properties <strong>of</strong> all<br />

substances:<br />

⎛∂H<br />

⎞ ⎛∂V<br />

⎞<br />

⎜ ⎟ = V − T⎜ ⎟ =<br />

⎝ ∂p<br />

⎠<br />

T<br />

T ⎝∂<br />

⎠p<br />

V(1 −αT)<br />

(II.39)<br />

2<br />

⎛∂C<br />

p ⎞ ⎛∂<br />

V ⎞<br />

⎜ ⎟ = −T<br />

⎜ 2 ⎟<br />

⎝ ∂p<br />

⎠ ∂T<br />

T ⎝ ⎠p<br />

(II.40)<br />

⎛∂S<br />

⎞<br />

⎛∂V<br />

⎞<br />

⎜ ⎟ = −V<br />

α = −⎜ ⎟<br />

⎝∂p⎠<br />

∂T<br />

T<br />

⎝ ⎠p<br />

(II.41)<br />

⎛∂G<br />

⎞<br />

⎜ ⎟<br />

⎝ ∂p<br />

⎠T<br />

= V<br />

(II.42)<br />

where α ≡<br />

1 ⎛∂V<br />

⎞<br />

⎜ ⎟<br />

V ⎝∂T<br />

⎠p<br />

(II.43)<br />

For ideal gases, V = RT / p and α = R / pV = 1 /T. The conversion equations<br />

listed below (Eqs. (II.44) to (II.51)) apply to the small pressure change from 1 atm to 1<br />

bar (0.1 MPa). The quantities that refer to the old standard state pressure <strong>of</strong> 1 atm are<br />

assigned the superscript (atm) , and those that refer to the new standard state pressure <strong>of</strong><br />

1 bar are assigned the superscript (bar) .<br />

For all substances the changes in the enthalpy <strong>of</strong> formation and heat capacity<br />

are much smaller than the experimental accuracy and can be disregarded. This is exactly<br />

true for ideal gases.<br />

(bar)<br />

(atm)<br />

ΔfH ( T) − ΔfH ( T) = 0<br />

(II.44)<br />

(bar)<br />

(atm)<br />

C ( T) − C ( T) = 0<br />

(II.45)<br />

For gaseous substances, the entropy difference is:<br />

p<br />

(atm)<br />

(bar)<br />

(atm)<br />

S T − S T R ⎜ R<br />

(bar) ⎟<br />

p<br />

⎛ p ⎞<br />

( ) ( ) = ln = ln1.01325<br />

⎝ p ⎠<br />

= 0.1094 J·K –1·mol –1 (II.46)<br />

This is exactly true for ideal gases, as follows from Eq. (II.41) with α = R / pV .<br />

The entropy change <strong>of</strong> a reaction or process is thus dependent on the number <strong>of</strong> moles<br />

<strong>of</strong> gases involved:<br />

CHEMICAL THERMODYNAMICS OF TIN, ISBN 978-92-64-99206-1, © <strong>OECD</strong> 20<strong>12</strong>

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