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The maximum non-expansion work available from a reversible spontaneous process ( < 0) at constant T and p is equal to , that is
ΔGΔG
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The maximum non-expansion work available from a reversible spontaneous process ( < 0) at constant T and p is equal to , that is
ΔG
exp-nonwΔG
ΔG
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The maximum non-expansion work available from a reversible spontaneous process ( < 0) at constant T and p is equal to , that is
This is a second important application of .
ΔG
exp-nonwΔG
ΔG
ΔG
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The maximum non-expansion work available from a reversible spontaneous process ( < 0) at constant T and p is equal to , that is
This is a second important application of . The key constraints are indicated in blue type.
ΔG
exp-nonwΔG
ΔG
ΔG
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To prove that , start with a summary of
previous results:exp-nonwΔG
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To prove that , start with a summary of
previous results: G = H – T S (1)
exp-nonwΔG
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To prove that , start with a summary of
previous results: G = H – T S (1) H = E + pV (2)
exp-nonwΔG
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To prove that , start with a summary of
previous results: G = H – T S (1) H = E + pV (2) (3)
exp-nonwΔG
wqΔE
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To prove that , start with a summary of
previous results: G = H – T S (1) H = E + pV (2) (3) (4)
exp-nonwΔG
exp-nonexp www
wqΔE
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To prove that , start with a summary of
previous results: G = H – T S (1) H = E + pV (2) (3) (4) (5)
exp-nonwΔG
exp-nonexp www
TqΔS rev
wqΔE
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Plug Eq. (2) into Eq. (1) so that G = E + pV – TS (6)
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Plug Eq. (2) into Eq. (1) so that G = E + pV – TS (6) Now take a change in each variable
Δ(TS)Δ(pV)ΔEΔG
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Plug Eq. (2) into Eq. (1) so that G = E + pV – TS (6) Now take a change in each variable
(7)
Δ(TS)Δ(pV)ΔEΔG STΔTSΔpVΔΔVpΔE
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Plug Eq. (2) into Eq. (1) so that G = E + pV – TS (6) Now take a change in each variable
(7) Plug Eq. (4) into Eq. (3) and insert the result into Eq.
(7):
Δ(TS)Δ(pV)ΔEΔG STΔTSΔpVΔΔVpΔE
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Plug Eq. (2) into Eq. (1) so that G = E + pV – TS (6) Now take a change in each variable
(7) Plug Eq. (4) into Eq. (3) and insert the result into Eq.
(7): (8)
Δ(TS)Δ(pV)ΔEΔG
STΔTSΔpVΔΔVpwwqΔG exp-nonexp
STΔTSΔpVΔΔVpΔE
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Now fix the conditions:
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Now fix the conditions: (a) constant temperature, so that ,
0ΔT
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Now fix the conditions: (a) constant temperature, so that , (b) constant pressure, so that ,
0ΔT 0Δp
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Now fix the conditions: (a) constant temperature, so that , (b) constant pressure, so that , (c) and reversible process,
0ΔT 0Δp
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Now fix the conditions: (a) constant temperature, so that , (b) constant pressure, so that , (c) and reversible process, then Eq. (8) simplifies to (9)
STΔVpwwqΔG revexp,-nonrevexp,rev
0ΔT 0Δp
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Now fix the conditions: (a) constant temperature, so that , (b) constant pressure, so that , (c) and reversible process, then Eq. (8) simplifies to (9) which simplifies using Eq. (5) to yield
STΔVpwwqΔG revexp,-nonrevexp,rev
0ΔT 0Δp
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Now fix the conditions: (a) constant temperature, so that , (b) constant pressure, so that , (c) and reversible process, then Eq. (8) simplifies to (9) which simplifies using Eq. (5) to yield (10)
STΔVpwwqΔG revexp,-nonrevexp,rev
0ΔT 0Δp
ΔVpwwΔG revexp,-nonrevexp,
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Now fix the conditions: (a) constant temperature, so that , (b) constant pressure, so that , (c) and reversible process, then Eq. (8) simplifies to (9) which simplifies using Eq. (5) to yield (10) For a reversible change , hence
STΔVpwwqΔG revexp,-nonrevexp,rev
0ΔT 0Δp
ΔVpwwΔG revexp,-nonrevexp,
ΔVpw revexp,
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Now fix the conditions: (a) constant temperature, so that , (b) constant pressure, so that , (c) and reversible process, then Eq. (8) simplifies to (9) which simplifies using Eq. (5) to yield (10) For a reversible change , hence
STΔVpwwqΔG revexp,-nonrevexp,rev
0ΔT 0Δp
ΔVpwwΔG revexp,-nonrevexp,
ΔVpw revexp,
revexp,-nonwΔG
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A true reversible process takes an infinite amount of time to complete. Therefore we can never obtain in any process the amount of useful work predicted by the value of . ΔG
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The Gibbs Energy and Equilibrium
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The Gibbs Energy and Equilibrium When a system goes from an initial to a final state, a
indicates a spontaneous change left to right, a indicates a non-spontaneous process, the reaction is spontaneous right to left.
0ΔG 0ΔG
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The Gibbs Energy and Equilibrium When a system goes from an initial to a final state, a
indicates a spontaneous change left to right, a indicates a non-spontaneous process, the reaction is spontaneous right to left.
It is possible that , and hence
0ΔG 0ΔG
ΔSTΔH 0ΔG
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The Gibbs Energy and Equilibrium When a system goes from an initial to a final state, a
indicates a spontaneous change left to right, a indicates a non-spontaneous process, the reaction is spontaneous right to left.
It is possible that , and hence
When , the system is at equilibrium, there is no net change.
0ΔG 0ΔG
ΔSTΔH 0ΔG
0ΔG
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Example: Consider a mixture of ice and water at 0 oC and 1 bar.
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Example: Consider a mixture of ice and water at 0 oC and 1 bar. Neither freezing nor melting is
spontaneous, provided no heat is added or removed from the system.
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Example: Consider a mixture of ice and water at 0 oC and 1 bar. Neither freezing nor melting is
spontaneous, provided no heat is added or removed from the system. There is a dynamic equilibrium:
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Example: Consider a mixture of ice and water at 0 oC and 1 bar. Neither freezing nor melting is
spontaneous, provided no heat is added or removed from the system. There is a dynamic equilibrium:
ice water
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Example: Consider a mixture of ice and water at 0 oC and 1 bar. Neither freezing nor melting is
spontaneous, provided no heat is added or removed from the system. There is a dynamic equilibrium:
ice water The ice lattice is broken down to form liquid water
and water freezes to form ice at every instant.
At equilibrium , and therefore the amount of useful work that can be extracted from the system is zero.
0ΔG
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Predicting the Outcome of Chemical Reactions
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Predicting the Outcome of Chemical Reactions
Consider the “simple” reaction A B
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Predicting the Outcome of Chemical Reactions
Consider the “simple” reaction A B How do we tell which is the spontaneous direction:
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Predicting the Outcome of Chemical Reactions
Consider the “simple” reaction A B How do we tell which is the spontaneous direction: A B or B A ?
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Predicting the Outcome of Chemical Reactions
Consider the “simple” reaction A B How do we tell which is the spontaneous direction: A B or B A ?
Examination of for each reaction gives the answer.ΔG
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Predicting the Outcome of Chemical Reactions
Consider the “simple” reaction A B How do we tell which is the spontaneous direction: A B or B A ?
Examination of for each reaction gives the answer.Suppose A B is spontaneous
ΔG
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Predicting the Outcome of Chemical Reactions
Consider the “simple” reaction A B How do we tell which is the spontaneous direction: A B or B A ?
Examination of for each reaction gives the answer.Suppose A B is spontaneous – will the reaction B A take place to any extent?
ΔG
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All chemical reactions proceed so as to reach the minimum of the total Gibbs energy of the system.
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All chemical reactions proceed so as to reach the minimum of the total Gibbs energy of the system.
Always between the total Gibbs energy of the products and the total Gibbs energy of the reactants, there will be some point where the total Gibbs energy of a mixture of reactants and products has a minimum Gibbs energy.
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All chemical reactions proceed so as to reach the minimum of the total Gibbs energy of the system.
Always between the total Gibbs energy of the products and the total Gibbs energy of the reactants, there will be some point where the total Gibbs energy of a mixture of reactants and products has a minimum Gibbs energy.
The minimum indicates the composition at equilibrium, i.e. A B.
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It is necessary to keep in mind that all reactions for which is positive in the forward direction, take place to some extent. However the extent of the reaction may be extremely small (particularly for many typical inorganic reactions).
ΔG
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Standard Gibbs Energy and the Equilibrium Constant
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Standard Gibbs Energy and the Equilibrium Constant
The Gibbs energy for a species X which is not in its standard state is given by
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Standard Gibbs Energy and the Equilibrium Constant
The Gibbs energy for a species X which is not in its standard state is given by
X0XX alnRTGG
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Standard Gibbs Energy and the Equilibrium Constant
The Gibbs energy for a species X which is not in its standard state is given by
where aX is the activity of species X. X
0XX alnRTGG
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52
Standard Gibbs Energy and the Equilibrium Constant
The Gibbs energy for a species X which is not in its standard state is given by
where aX is the activity of species X. Recall that
.
X0XX alnRTGG
[X]a XX
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Standard Gibbs Energy and the Equilibrium Constant
The Gibbs energy for a species X which is not in its standard state is given by
where aX is the activity of species X. Recall that
. In a number of situations the activity coefficient
satisfies , so that ,
X0XX alnRTGG
[X]a XX
1X [X]aX
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Standard Gibbs Energy and the Equilibrium Constant
The Gibbs energy for a species X which is not in its standard state is given by
where aX is the activity of species X. Recall that
. In a number of situations the activity coefficient
satisfies , so that , so that the above result simplifies to
X0XX alnRTGG
[X]a XX
1X [X]aX
[X]lnRTGG 0XX
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Standard Gibbs Energy and the Equilibrium Constant
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Standard Gibbs Energy and the Equilibrium Constant
If a reaction is run under conditions such that all of the reactants and products are not in their standard states – then for a reaction ΔG
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Standard Gibbs Energy and the Equilibrium Constant
If a reaction is run under conditions such that all of the reactants and products are not in their standard states – then for a reaction
a A + b B c C + d D
ΔG
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Standard Gibbs Energy and the Equilibrium Constant
If a reaction is run under conditions such that all of the reactants and products are not in their standard states – then for a reaction
a A + b B c C + d D is given by = c GC + d GD – a GA – b GB
ΔG
ΔG
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Standard Gibbs Energy and the Equilibrium Constant
If a reaction is run under conditions such that all of the reactants and products are not in their standard states – then for a reaction
a A + b B c C + d D is given by = c GC + d GD – a GA – b GB
= + – –
ΔG
ΔG
[C]lnRTcGc 0C [D]lnRTdGd 0
D
[A]lnRTaGa 0A [B]lnRTbGb 0
B
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0B
0A
0D
0C GbGaGdGcΔG
badc [B]lnRT[A]lnRT[D]lnRT[C]lnRT