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8/13/2019 More On Entropy
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Lecture 8: Thermo and Entropy
Reading: Zumdahl 10.2, 10.3
Outline
Answers to yesterdays questions
Isothermal processes
Isothermal gas expansion and work Reversible and Irreversible processes
Thermodynamic definition of entropy
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Answers
Not terribly satisfying but
Heat death is only a hypothesisIf the expansion of theuniverse is slowing, then the increase in the entropydensity of the universe is also slowing.
Gravity leads to heavier objects. Eventually this leads to
black holes. Steven Hawkings originally proposed blackholes as maximum entropy per unit mass.
But now he recants
A simpler explanation will become apparent todaythat is that raising and releasing a body with regard to PEis not perfect hence an increase in entropy.
Entropy is also seen as the reason time flows forward
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AnswersBoltzmann distributions
0
1
2
3
4
5
6
7
0 2 4 6 8 10
Weighted Average Energy
Count
s
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Isothermal Processes
Recall: Isothermal means T = 0. Since E = nCvT, then E = 0 for an
isothermal process.
Since E = q + w:
q = -w (isothermal process)
We will use isothermal processes to
illustrate what is meant by reversible and
irreversible processes.
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Isothermal Expansion (cont.)
Initially, V = V1
P = P1
Pressure of gas is equal to that
created by mass:
P1
= force/area = M1
g/A
where A = piston area
g = gravitational acceleration (9.8 m/s2)
kg m-1 s-2 = 1 Pa
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Isothermal Expansion (cont.) One-Step Expansion. We change the
weight to M1/4, then
Pext = (M1/4)g/A = P1/4
The mass will be lifted until the internalpressure equals the external pressure. In
this case Vfinal = 4V1
w = -PextV = -P1/4 (4V1 - V1) = -3/4 P1V1
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Two Step Expansion
In this expansion we go in two steps:Step 1: M1 to M1/2
Step 2: M1/2 to M1/4
In first step:
Pext = P1/2, Vfinal = 2V1
w1 = -PextV = -P1/2 (2V1 - V1) = -1/2 P1V1
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Two Step Expansion (cont.)
In Step 2 (M1/2 to M1/4 ):
Pext = P1/4, Vfinal = 4V1
w2 = -PextV = - P1/4 (4V1 - 2V1) = -1/2 P1V1
wtotal = w1 + w2 = -P1V1/2 - P1V1/2 = -P1V1
wtotal,2 step > wtotal,1 step
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Two Step Expansion (cont.) Graphically, we can envision this two-step processon a PV diagram:
Work is given by the area under the PV curve.
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Two Step Compression Now we will do the opposite.take the gas and
compress:
Vinit = 4V1
Pinit = P1/4
Compression in two steps:
first place on mass = M1/2
second, replace mass with one = M1
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Compression/Expansion
We have undergonea cycle where thesystem returns to
the starting state.
In two step example:wexpan. = -P1V1
wcomp. = 2P1V1
wcycle
= P1V
1
qcycle = -P1V1
Now, E = 0 (state fcn)
But, q = -w 0
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Irreversible Processes Since q and w for this cycle are not zero, the
surroundings of the system have changed.
Though the system has been restored to its
starting state, the universe has changed. When it is not possible to restore a system to
its original state without leaving a change inthe universe we call the process irreversible.
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Infinite Step Expansion
Imagine that we perform a process in which we change
the weight infinitesimally between expansions.
(Perhaps we use very fine grains of sand.)
Instead of determining the sum of work performed ateach step to get wtotal, we integrate:
w = PexdVVinitial
Vfinal
= PdVVinitial
Vfinal
= nRT
VdV
Vinitial
Vfinal
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Infinite Step Expansion (cont.) Grapically:
Infinitely Many Steps
(reversible)Six Steps
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Infinite Step Expansion (cont.)
If we perform theintegration from V1 to
V2:
2 22
11 1
expan 2
1
(ln( )) ln|V V
V
totalVV V
VnRTw PdV dV nRT V nRT
V V
= = = =
expan expan2
1
lnrev rev
Vw nRT q
V
= =
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Infinite Step Compression
If we perform the
integration in the
backwards direction,
from V2 to V1 :
1 11
22 2
comp 1
2
(ln( )) ln|rev
V VV
VV V
VnRTw PdV dV nRT V nRT
V V
= = = =
comp comp 1
2
lnrev rev
Vw q nRT
V
= =
2
1
ln V
nRT
V
=
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Reversible Processes
Comparing the results for the expansionand the compression
So this cycle can in principle be performed
without changing the surroundings.
These types of processes are called
reversible.
comp expan comp expanandrev rev rev rev
q q w w= =
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Reversible and Irreversible
Processes
After a reversible process both the systemand its surroundings can be restored to
their original state.
After an irreversible process this is not
possible. It is not possible to restore the
system to its original state withoutchanging the surroundings.
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Reversible and Irreversible
Processes (cont.)
Any process taking place quickly in thereal world will be irreversible.
To be reversible, the changes in the system
must be slow and the system must be at
equilibrium at all times.
Real processes can approach beingreversible if they are performed slowly
enough.
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Thermodynamic Definition of Entropy
For a reversible isothermal process, the change
in the entropy of a system is
If the temperature changes during the process
In both cases, the qrev is the heat transferred in a
reversible process which converts the initial state
into the final state.
finalrev
initial
dqS
T =
r e vqST
=
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Irreversible process
S for a process is defined in terms of the heat for areversible process between those two states.
For an irreversible isothermal process
If the temperature changes during the irreversible
process
In both cases, the qirr is the heat transferred in an
irreversibleprocess.
final
irr
initial
dq
S T >
irrqST
>
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Change in Entropy for an Isothermal
Volume Change of an Ideal Gas
Initial State (T, Vinitial
)
Final State (T. Vfinal)
Now T = 0; therefore, E = 0 and q = -w
Do expansion reversibly.
ln
ln
finalrev rev
initial
finalrev
initial
Vq w nRT
VVq
S nR
T V
= =
= =
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Connecting with Lecture 6 From this lecture:
RTln R ln
T T
final finalrev
initial initial
V Vq nS n
V V
= = =
Exactly the same as derived in the previous lecture!
N ln R lninal final
initial initial
V VS k nV V
= =
The number of atoms, N = nNa.
F th i h i h ti f id l hi h t t t i t ?
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For the isochoric heating of an ideal gas, which statement is true?
Initial Final
V = 0
C. w = 0A. E = 0
D. q = 0B. H = 0
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Entropy Change for Isochoric
Temperature Change of an Ideal Gas
Initial State (Tinitial, V) Final State (Tfinal. V)
Now
V = 0; therefore, w = 0 qrev = E = nCvT
S (ln( ))
ln
|
final finalinal
initial
initial initial
T TT
rev V V T
T T
finalV
initial
dq nC dT nC TT T
T
nC T
= = =
=
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Calculating EntropyS=
dqrev
Tinitial
final
S= dqrev
Tinitial
final
=nR lnVfinal
Vinitial
dqrev =nRT
dV
VT = 0
S= dqrev
Tinitial
final
=nCv lnTfinal
Tinitial
V = 0 dqrev =nCvdT
S= dqrev
Tinitial
final
=nCp lnTfinal
Tinitial
P = 0 dqrev =nCPdT
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Calculating Entropy Example: What is S for the heating of a mole of a monatomic
gas isochorically from 298 K to 350 K?
ln
finalfinalrev
vinitialinitial
TdqS nC
T T
= =
3/2R
( ) 3503(1 ) ln2 298K
S mol RK
=
2JSK
=
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Four-step Cycle
Lets consider a four-step cycle: 1: Isothermal expansion (TH)
2: Isochoric cooling (V2)
3: Isothermal compression (TL)
4: Isochoric heating (V1)
Volume
V1 V2
1
2
3
4
Since the entropy is a state function, S for the cycle must be 0.
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Scycle 1. Isothermal Expansion at T = TH from V1 to V2
2. Isochoric Cooling at V = V2 from TH to TL
3. Isothermal Compression at T = TL from V2 to V1
4. Isochoric Heating at V = V1 from TL to TH
2 L Hln( )vS nC T T =
( )1 2 1lnS nR V V =
( ) ( )3 1 2 2 1 1ln lnS nR V V nR V V S = = =
4 H L L H 2ln ln( ) ( )v vS nC T T nC T T S = = =
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ScycleSum up the four entropy changes
As expected, S for a cycle is zero.
cycle 1 2 3 4
0
S S S S S = + + +
=
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Four-step Cycle
Lets consider a four-step cycle: 1: Isothermal expansion (TH)
2: Isochoric cooling (V2)
3: Isothermal compression (TL)
4: Isochoric heating (V1)
Volume
V1 V2
1
2
3
4
q and w are path dependent and are not zero when
summed around this cycle.
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q and w are not state functions
1. Isothermal Expansion at T = TH from V1 to V2
2. Isochoric Cooling at V = V2 from TH to TL
3. Isothermal Compression at T = TL from V2 to V1
4. Isochoric Heating at V = V1 from TL to TH
( )1 H 1 H 2 1T S T lnq nR V V = =
( ) ( )3 L 1 L 1 2 L 2 1T S T ln T lnq nR V V nR V V = = =
2 2 2 2 L HE E C (T T )vq w n= = =
4 4 4 4 H L 2E E C (T T )vq w n q= = = =
d f i
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q and w are not state functions
So heat transferred to system during this cycle
is
Since E = 0
This cycle can be thought of as a very simple
engine. Run in reverse it is a refrigerator.
1 2 3 4
H L 2 1(T T )ln( ) 0q q q q q
nR V V = + + += >
H L 2 1(T T )ln( )
0
w q nR V V = =