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ME334 Introduction to Statistical Mechanics Wei Cai Stanford University Winter 2008
7. Thermodynamics Worked Examples
Problem 7.1 Consider a gas tank of volume V containing N gas molecules with total energyE. For all 7 thermodynamic potentials,
E(S,V,N) (1)
A(T , V , N ) (2)H(S,p,N) (3)
G(T ,p ,N ) (4)
I(S,V,) (5)
J(S,p,) (6)
K(T , V , ) (7)
write down the corresponding 3 conjugate variables. For example, for E(S,V,N), they arethe definitions of T, p, and . Also write down 3 Maxwell relations for each thermodynamicpotential. There should be 7 (3 + 3) = 42 equations in total.
Solution
Energy: E(S,V,N)
dE = T dSpdV + dN
T
E
S
V,N
, p
E
V
S,N
,
E
N
S,V
T
V
S,N
=
p
S
V,N
,
T
N
S,V
=
S
V,N
,
p
N
S,V
=
V
S,N
Helmoltz Free Energy: A(T,V,N)
A = E T S
dA = dE T dS SdT = SdTpdV + dN
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S =
A
T
V,N
, p =
A
V
T,N
, =
A
N
T,V
S
V
T,N
=
p
T
V,N
,
S
N
T,V
=
T
V,N
,
p
N
T,V
=
V
T,N
Enthalpy: H(S,p,N)
H = E+pV
dH = dE+pdV + V dp = T dS+ V dp + dN
T =
HS
p,N
, V =
Hp
S,N
, =
HN
S,p
T
p
S,N
=
V
S
p,N
,
T
N
S,p
=
S
p,N
,
V
N
S,p
=
p
S,N
Gibbs Free Energy: G(T,p,N)
G = A +pV
dG = dA +pdV + V dp =
SdT + V dp + dN
S =
G
T
p,N
, V =
G
p
T,N
, =
G
N
T,p
S
p
T,N
=
V
T
p,N
,
S
N
T,p
=
T
p,N
,
V
N
T,p
=
p
T,N
I(S,V,)
I = E N
dI = dE dNNd = T dSpdVNd
T =
I
S
V,
, p =
I
V
S,
, N =
I
S,V
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T
V
S,
=
p
S
V,
,
T
S,V
=
N
S
V,
,
p
S,V
=
N
V
S,
J(S,p,)
J = H N
dJ = dH dNNd = T dS+ V dpNd
T =
J
S
p,
, V =
J
p
S,
, N =
J
S,p
Tp
S,
=
VS
p,
,
T
S,p
=
NS
p,
,
V
S,p
=
Np
S,
K(T,V,)
K = A N
dK = dA dNNd = SdTpdVNd
S =K
TV, , p =
KV
T, , N =
K
T,V
S
V
T,
=
p
T
V,
,
S
T,V
=
N
T
V,
,
p
T,V
=
N
V
T,
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Problem 7.2 The Sackur-Tetrode equation gives the analytic expression for the entropy ofan ideal gas,
S = kBN
ln
V
N
4mE
3Nh2
3/2+
5
2
(8)
(a) Invert this equation to obtain E(S,V,N). Derive the expression for T, p, and . Verifythe ideal gas law pV = N kBT.
(b) Obtain A(T , V , N ) and recompute S from A(T , V , N ).
(c) Obtain G(T ,p ,N ) and compare it with N.
(d) Compute the heat capacity at constant volume CV, heat capacity at constant pressureCp, coefficient of thermal expansion and compressibility , which are defined as follows
CV =
dQdT
V,N
(9)
Cp =
dQ
dT
p,N
(10)
=1
V
V
T
p,N
(11)
= 1
V
V
p
T,N
(12)
Verify that CpCV = 2V T / (this relation is valid for arbitrary thermodynamic system).
Solution
(a) At fixed S, V, N, the property thermodynamic potential is E(S,V,N).
E(S,V,N) =3Nh2
4m
N
V
2/3exp
2S
3N kB
5
3
T =E
SV,N = E
2
3NkB E =
3NkBT
2
p =
E
V
S,N
= E2
3V=
N kBT
V pV = NkBT
=
E
N
S,V
=E
N
5
3
2S
3NkB
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(b) At fixed T, V, N, the property thermodynamic potential is A(T , V , N ). Recall thatA = E T S. But we need to be careful about rewriting everything in terms of T, V, Nnow.
E =
3
2NkBT
S = NkB
ln
V
N
2mkBT
h2
3/2 + 5
2
(13)
A(T , V , N ) = E T S =3N kBT
2NkBT
ln
V
N
2mkBT
h2
3/2 + 5
2
= N kBT
ln
V
N
2mkBT
h2
3/2 + 1
S =A
TV,N =
A
T + NkBT
3
2 T =
A
T +
3NkB
2
= NkB
ln
V
N
2mkBT
h2
3/2 + 5
2
which reproduces Eq. (13).
(c) At fixed T, p, N, the property thermodynamic potential is G(T ,p ,N ). Recall thatG = A +p V. But we need to be careful about rewriting everything in terms ofT, p, N now.
A = NkBTlnkBTp
2mkBTh2
3/2
+ 1p V = N kBT
G = A +pV
= NkBT
ln
kBT
p
2mkBT
h2
3/2 (14)
At the same time, Eq. (13) leads to
N = E
5
3
2S
3NkB
=
5N kBT
2 T S
= 5NkBT
2NkBT
lnkBTp
2mkBT
h2
3/2 + 52
= NkBT
ln
kBT
p
2mkBT
h2
3/2 (15)
Comparing Eqs. (14) and (15), we have
G = N
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(d) To compute heat capacity at constant volume, CV, the proper thermodynamic potentialto consider is A(T , V , N ), with
S = A
TV,N
CV =
dQ
dT
V,N
= T
S
T
V,N
= T
2A
T2
V,N
Recall that
S(T , V , N ) = NkB
ln
V
N
2mkBT
h2
3/2 + 5
2
we have
CV = T
STV,N
= 32NkB
To compute heat capacity at constant pressure, Cp, the proper thermodynamic potential toconsider is G(T ,p ,N ), with
S =
G
T
p,N
Cp =
dQ
dT
p,N
= T
S
T
p,N
= T
2G
T2
p,N
From
S(T ,p ,N ) = NkB
ln
kBT
p
2mkBT
h2
3/2 + 5
2
we have
Cp = T
S
T
p,N
=5
2NkB
Cp CV = NkB
To compute coefficient of thermal expansion, , the proper thermodynamic potential toconsider is G(T ,p ,N ), with
V =
G
p
T,N
=NkBT
p
=1
V
V
T
p,N
=1
V
2G
p T
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Therefore
=p
NkBT
NkBp
=1
T
To compute compressibility, , the proper thermodynamic potential to consider is alsoG(T ,p ,N ), with
= 1
V
V
p
T,n
= 1
V
2G
p2
Therefore
= p
NkBT
NkBT
p2=
1
p
2V T
=
1
T2
V T p = N kB = Cp CV
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Problem 7.3 Consider an insulated container of volume V2. N idea gas molecules areinitially confined within volume V1 by a piston and the remaining volume V2V1 is in vacuum.Let T1, p1, E1, S1 A1, H1, G1 be the temperature, pressure, energy, entropy, Helmholtz freeenergy, enthalpy, and Gibbs free energy of the ideal gas at this state, respectively.
V1 V2 - V1
(a) Imagine that the piston is suddenly removed so that the gas has volume V2. After sometime the system settles down to equilibrium again. What are the temperature T2, pressure
p2, energy E2, entropy S2, Helmholtz free energy A2, enthalpy H2, and Gibbs free energy G2in the new equilibrium state? Mark the initial and final states in the p-V plot and the T-S
plot.
(b) Suppose we move the piston infinitely slowly (a reversible process) to let the gas expandto the full volume V2. The gas container is thermally insulated during this process. What isthe work done W to the system? What are T2, p2, E2, A2, H2, G2 in the final equilibriumstate? Express them in terms of the thermodynamic functions of state 1 and V2/V1. Markthe initial and final states in the p-V plot and the T-S plot.
Solution:
(a) Because there is no heat flow or work done to the system during the free expansion, the
change of total energy is zero,
E2 = E1
From the Sackur-Tetrode equation for the entropy of ideal gas
S = kBN
ln
V
N
4mE
3Nh2
3/2+
5
2
(16)
Hence
S2 = S1 + kBNlnV2V1
Because temperature is defined as
T =
S
E
1
V,N
=2 E
3NkB
we have,
T2 = T1 =2E1
3NkB
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Because p V = N kB T, we have
p2 =NkBT2
V2=
p1 V1V2
Change of Helmholtz free energy,
A2 A1 = (E2 T2S2) (E1 T1S1)
= T1(S2 S1)
A2 = A1 N kB T1 lnV2V1
Enthalpy,
H2 = E2 +p2V2 =5
2NkBT1 = H1
Change of Gibbs free energy,
G2 G1 = (H2 T2S2) (H1 T1S1)
= T1(S2 S1)
G2 = G1 N kB T1 lnV2V1
Table 1: Change of thermodynamic properties if the piston suddenly disappears and the gassettle down to the new equilibrium state with volume V2.
T2 T1 0p2 p1 p1(V1/V2 1)E2 E1 0S2 S1 N kB ln(V2/V1)A2 A1 N kB T ln(V2/V1)H2 H1 0G2 G1 N kB T ln(V2/V1)
(b) Here the piston expansion is a reversible and adiabatic (no heat flow) process. Hence
the entropy change should be zero,
S2 = S1
From Eq. (16),
V1 E3/21 = V2 E
3/22
E2 =
V1V2
2/3E1
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Because E = 32
NkBT,
T2 =
V1V2
2/3T1 (17)
Eq. (17) can also be obtained from the ideal gas law, p V = N kBT. Duringthe expansion process, the energy change corresponding to a differentialchange of volume dV is,
dE = dW = p dV = NkBT
VdV
At the same time, E = 32
NkBT, therefore dE =3
2NkBdT, so that,
3
2NkBdT =
N kBT
VdV
3
2
dT
T =
dV
V3
2
T2T1
dT
T=
V2V1
dV
V3
2ln
T2T1
= lnV2V1
T2 =
V1V2
2/3T1
Because
p2 V2 = N kB T2 =
V1V2
2/3p1 V1
p2 =
V1V2
5/3p1
Helmholtz free energy, enthalpy and Gibbs free energy,
A2 = E2 T2S2 =
V1V2
2/3E1
V1V2
2/3T1S1
= V1
V2
2/3
A1
H2 = E2 +p2V2 =3
2NkBT2 + NkBT2
=5
2NkBT2 =
V1V2
2/3 52
NkBT1
=
V1V2
2/3H1
G2 = A2 +p2(V1 + V2) = A2 + N kBT2
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=
V1V2
2/3(A1 + NkBT1)
=
V1V2
2/3G1
Table 2: Change of thermodynamic properties if the piston moves very slowly and adiabat-ically expand the volume to V2.
T2/T1 (V1/V2)2/3
p2/p1 (V1/V2)5/3
E2/E1 (V1/V2)2/3
S2/S1 1A2/A1 (V1/V2)
2/3
H2/H1 (V1/V2)2/3
G2/G1 (V1/V2)2/3
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