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Solved Midterm Exam 2 for Thermodynamics and Statistical Mechanics | PHYS 4230, Exams of Physics

Material Type: Exam; Class: Thermodynamics and Statistical Mechanics; Subject: Physics; University: University of Colorado - Boulder; Term: Fall 2008;

Typology: Exams

2019/2020

Uploaded on 11/25/2020

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Physics 4230, Fall 2008, Midterm Exam 2, Solutions
1. (a) System B is at a higher temperature than system A (TB> TA). Recall the definition of temperature in
terms of entropy:
1
T=∂S
∂U N ,V = slope of S(U). (1)
Since system B has a smaller slope of S(U), it has a larger temperature.
(b) Here, Qis the heat flowing from the hotter system to the colder one. So, it’s the heat flowing from B to A.
We define QAto be the heat added to A, and QBthe heat added to B. We have QA=Q, and QB=Q.
The change in entropy of system A is
SA=h∂S
∂U iU=UA
QA=h∂S
∂U iU=UA
Q. (2)
The partial derivative is evaluated at constant Nand V(not explicitly written above), and it’s evaluated
at U=UA.
Similarly, the change in entropy of B is
SB=h∂S
∂U iU=UB
QB=h∂S
∂U iU=UB
(Q). (3)
So the total change in entropy is
S= SA+ SB= h∂S
∂U iU=UA
h∂S
∂U iU=UB!Q. (4)
2. (a) U= 0. To see this, first focus on the gas on the right of the wall. Its temperature before and after the
process is T, and its energy is U= (5/2)Nk T . So its energy doesn’t change. The same is true for the gas
on the left of the wall, and therefore the total energy of all the gas doesn’t change.
(b) Let’s start with the thermodynamic identity:
dU =T dS P dV . (5)
Now, since the temperature is held constant during this process, the energy Udoesn’t change, since the
energy of a diatomic ideal gas is just U= (5/2)N kT . Therefore we can set dU = 0. Since we’re interested
in the change in entropy, we can solve the thermodynamic identity for dS:
dS =P
TdV =1
T
NkT
VdV =Nk
VdV . (6)
In the second equality above, I used the ideal gas law to plug in P=N kT/V .
Let’s get the change in entropy for the gas on the left and right separately (∆SLand SR), and then add
them up to get the final answer.
We find the entropy change by integrating dS from the initial to the final volume. For the gas on the left,
the initial volume is Vand the final volume is 5V, so
SL=ZVf
Vi
dS =Z5V
V
Nk
VdV =N k Z5V
V
dV
V=N k ln(V)
5V
V(7)
=Nkhln(5V)ln(V)i=N k ln 5V
V=N k ln5. (8)
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Physics 4230, Fall 2008, Midterm Exam 2, Solutions

  1. (a) System B is at a higher temperature than system A (TB > TA). Recall the definition of temperature in terms of entropy:

1 T

( ∂S

∂U

N,V

= slope of S(U ). (1)

Since system B has a smaller slope of S(U ), it has a larger temperature. (b) Here, Q is the heat flowing from the hotter system to the colder one. So, it’s the heat flowing from B to A. We define QA to be the heat added to A, and QB the heat added to B. We have QA = Q, and QB = −Q. The change in entropy of system A is

∆SA =

[ ∂S

∂U

]

U=UA

QA =

[ ∂S

∂U

]

U=UA

Q. (2)

The partial derivative is evaluated at constant N and V (not explicitly written above), and it’s evaluated at U = UA. Similarly, the change in entropy of B is

∆SB =

[ ∂S

∂U

]

U=UB

QB =

[ ∂S

∂U

]

U=UB

(−Q). (3)

So the total change in entropy is

∆S = ∆SA + ∆SB =

([

∂S

∂U

]

U=UA

[ ∂S

∂U

]

U=UB

Q. (4)

  1. (a) ∆U = 0. To see this, first focus on the gas on the right of the wall. Its temperature before and after the process is T , and its energy is U = (5/2)N kT. So its energy doesn’t change. The same is true for the gas on the left of the wall, and therefore the total energy of all the gas doesn’t change. (b) Let’s start with the thermodynamic identity:

dU = T dS − P dV. (5)

Now, since the temperature is held constant during this process, the energy U doesn’t change, since the energy of a diatomic ideal gas is just U = (5/2)N kT. Therefore we can set dU = 0. Since we’re interested in the change in entropy, we can solve the thermodynamic identity for dS:

dS =

P

T

dV =

T

N kT V

dV =

N k V

dV. (6)

In the second equality above, I used the ideal gas law to plug in P = N kT /V. Let’s get the change in entropy for the gas on the left and right separately (∆SL and ∆SR), and then add them up to get the final answer. We find the entropy change by integrating dS from the initial to the final volume. For the gas on the left, the initial volume is V and the final volume is 5V , so

∆SL =

∫ (^) Vf

Vi

dS =

∫ 5 V

V

N k V

dV = N k

∫ 5 V

V

dV V

= N k ln(V )

5 V V

= N k

[

ln(5V ) − ln(V )

]

= N k ln

( 5 V

V

= N k ln 5. (8)

For the gas on the right, everything is the same, except now the initial volume is 9V and the final volume is 5V. So we have

∆SR = N k

∫ 5 V

9 V

dV V =^ N k

[

ln(5V ) − ln(9V )

]

= N k ln(5/9). (9)

The total change in entropy is

∆S = ∆SL + ∆SR = N k

ln 5 + ln(5/9)

= N k ln(25/9). (10)

(c) Since temperature is held constant, we have

∆F = ∆U − T ∆S. (11)

We already showed ∆U = 0 in part (a), and in part (b) we found ∆S = N k ln(25/9). Therefore we have

∆F = −N kT ln(25/9). (12)

(d) The change in entropy is the same as it was in part (b), ∆S = N k ln(25/9). The reason is that, here, the initial and final states of the gas are the same as they were in part (b). Since entropy only depends on the state of a system, the change in entropy only depends on the initial and final states, not on how one gets between them.

  1. We begin by making the guess that we can write the COP of the combined refrigerator in terms of the efficiency of the engine, and the COP of the small refrigerator. The physical insight behind this guess is that the combined refrigerator works by first getting some work W out of the heat engine, and then, in a second step, using that work to power the small refrigerator. Since the engine and the small refrigerator are running just as they were before we connected them, it’s reasonable to guess that their efficiency and COP tell us the COP of the combined refrigerator. Let’s call the efficiency of the engine e = W/Qh 1 , and the COP of the small refrigerator c = Qc 2 /W. Then we have

ec =

W

Qh 1

Qc 2 W =^

Qc 2 Qh 1 = COP,^ (13)

the COP of the combined refrigerator. Now, from the discussion in class and in Schroeder, we know

e ≤ emax = 1 −

Tc 1 Th 1

c ≤ cmax =

Tc 2 Th 2 − Tc 2

Therefore,

COP ≤ COPmax = emaxcmax =

1 − Tc^1 Th 1

) (^) Tc 2 Th 2 − Tc 2

  1. As we did in class, we want to express dSR in terms of quantities having to do with the system, not the reservoir. The thermodynamic identity for the reservoir is:

dUR = TRdSR − PRdVR + μRdNR = TRdSR + μRdNR. (17)

Because the reservoir does not exchange volume with the system, we took dVR = 0 in the second equality.