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Reaction Equilibrium and Chemical Potential
Criteria for chemical equilibrium are:
i
i i 0
13.8
(G T )
0
T , P
These criteria are not in a useable form.
Recall our definition of fugacity which applies to any species
in any phase (vapour, liquid, solid)
ˆ
i Gi (T ) RT ln fi
Recall that Gi(T) is a temperature-dependent constant.
Also recall that enthalpy, internal energy and Gibb’s energy are
always specified an tabulated using a reference state.
CHEE 311 1
Standard States
For reaction equilibrium calculations, the Gibbs energy at standard
conditions is the usual reference state.
Gio Gi (T ) RT ln fio
These standard conditions are:
pure component i
at the reaction temperature
in a user-defined phase (gas, liquid or solid)
at a user-defined pressure (often 1 bar)
A great deal of thermodynamic data are published as the standard
properties of formation at STP (Table C.4 of the text)
DGfo is standard Gibbs energy of formation per mole of the
compound when formed from its elements in its standard
state at 25oC.
» Gases: pure, ideal gas at 1 bar
» Liquids: pure substance at 1 bar
CHEE 311 2
Chemical Potential and Activity
Subtracting this expression for the standard Gibbs energy (Gio) gets
rid of Gi(T):
ˆ
fi
i Gio RT ln o 13.9
fi
We define a new parameter, activity, to simplify this expression:
i Gio RT ln ai
ˆ
where,
a ˆ
ˆ i fi fio
The activity of a component is the ratio of its mixture fugacity to its
pure component fugacity at the standard state.
CHEE 311 3
Reaction Equilibrium and Activity
When a reactive system reaches an equilibrium state, we know that
the equilibrium criterion is satisfied:
ii 0
i
where i is the stoichiometric coefficient of component i and i is
the chemical potential of component i at the given P,T, and
composition.
Substituting for i in terms of activity gives:
i
ii i Gi RT ln ai 0
i
o
ˆ
Or,
iiGio
i ln ai
ˆ
i RT
CHEE 311 4
The Equilibrium Constant
Our equilibrium expression for reactive systems can be expressed
concisely in the form:
i i iGio
ˆ
ln ai 13.10
i RT
How does the sum turn in to a product P ?
The right hand side of equation 13.10 is a function of pure
component properties alone, and is therefore constant at a given
temperature.
The equilibrium constant, K, for the reaction is defined as:
i iGio
K exp ˆ
ai i 13.11
RT i
K is calculated from the standard Gibbs energies of the pure
components and the stoichiometric coefficients of the reaction.
CHEE 311 5
Standard Gibbs Energy Change of Reaction
The conventional means of writing the equilibrium constant uses DGo,
the standard Gibbs energy change the reaction.
DGo ii Gio
Using this notation, our equilibrium constant assumes the usual form:
DGo 13.11
K exp
RT
When calculating an equilibrium constant (or interpreting a literature
value), pay attention to standard state conditions.
Each Gio must represent the pure component at the
temperature of interest and in the state of interest.
DGo
ln K
RT
CHEE 311 6
Temp. Dependence of Reaction Equilibrium
DGo
ln K
RT
K depends on temperature because DG/RT depends on T
d (DG o / RT ) DH o
Gibbs-Helmholtz eqn.
dT RT 2
From which we can derive the temperature dependence of K:
d ln K DHo 13.14
dT RT2
If we assume that DHo is independent of temperature, we can integrate
13.14 directly to yield:
13.15
K DHo 1 1
ln
K1 R T T1
CHEE 311 7
K vs Temperature
Equation 12.15 predicts that ln K
versus 1/T is linear. This is based on
the assumption that DHo is only a
weak function of temperature over the
range of interest.
This is true for the
reactions, in Figure13.2
Why is DHo a function of T?
What do we do if we are
worried about DHo(T) when
computing K?
CHEE 311 8
Equilibrium State of a Reactive System
Let’s use the equilibrium constant to determine concentrations at
eq’m.
i iGio
exp ˆ
K ai i
RT i
Consider the gas phase reaction:
CH4 H2O CO 3H2
The equilibrium constant gives us:
ˆ ˆ3
aCOaH2
K
ˆ ˆ
aCH4 aH2O
Or
ˆ o ˆ o
( fCO / fCO )( fH2 / fH2 )3
K
ˆ o ˆ o
( fCH / fCH )( fH O / fH O )
4 4 2 2
CHEE 311 9
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