u du w q - solid state chemistry - solid state chemistryfor all ellements in their reference states...
TRANSCRIPT
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1
Summary Lecture 1 (glossery: see App. B, SG)
- First law: conservation of energy
function state a is
0
U
dU
QWdUU
dQdWdU
- Perfect gas nRTPV Equation of state
- Perfect atomic gas PVnRTU2
3
2
3
- Mechanical work dVPdVPW ext
Reversible process
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2
Summary Lecture 2 (second law and entropy)
Second law: for any spontaneous process
0surtot dSdSdST
dQdS
rev
S is a state function, so independent of path
Alternative form: Clausius inequality:
TdSdQ
TdSdQ rev
TdSdQ irr
Reversible process
Irreversible process
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3
Summary Lecture 2 (alternative energy functions)
PVUH
TSHG
TSUA
V
VT
UC
P
PT
HC
UInternal energy
Enthalpy
Helmholtz free energy
Gibbs free energy
State functions
Heat capacities
PdVTdSdU TdSdUV
VdPTdSdH TdSdHP
PdVSdTdA 0,
VTdA
VdPSdTdG 0,
PTdG
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4
Summary Lecture 3 (chemical equilibria)
Second law→ 0,
TPGd
QRTGG lnrr
RT
GK rexp
i
i
i GG ,mfr
Equ
ilib
riu
m s
tate
Energy minimum
T,P 0r G
0r G
Reaction progression ξ 0 1 ξeq
0r G
0r G
0r G
0r G
reaction ΔrG
Equilibrium constant bar1P
i
iiaQ
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5
Summary Lecture 3 (formation energies)
0,mf
iGFor all ellements in their reference states at T
For all ellements in their reference states at T
iii STHG ,mf,mf,mf
At constant, chosen T
Partial pressure
PxP ii
Mole fraction
j
j
iii
n
n
n
nx
For gaseous mixtures For perfect gas mixtures
i
i
i
P
PQ
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6
Summary Lecture 4 (activity)
For perfect gas mixtures
P
Pa i
i
For pure liquids
For pure solids
1la
1sa
iii aRT ln
c
ca ic
ii
)(
b
ba ib
ii
)( i
x
ii xa )(
mol/L1c mol/kg1b
H -logpH a
For general systems:
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7
Summary Lecture 4 (electrochemistry)
QRTGG rr ln QF
RTEE ln
Nernst equation
)(Fe3 aq)(MnO4 aq
)(Fe2 aq)(Mn 2 aq
)(H aq
)(OH2 l)(OH2 l
Pt Pt
Equ
ilib
riu
m s
tate
Energy minimum
T,P 0r G
0r G
Reaction progression ξ 0 1 ξeq
0r G
E + -
0r G
0r G
0r G
reaction
0E
0E
0E
FEGr
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8
Summary Lecture 5: solutions or mixtures
Equilibrium between phases of component i in mixtures
,, ii in equilibrium:
phase α
phase β
i
iiTPG n
,
lglglglg
lg axaxnRTG ,B,,B,,A,,A,
,
mix lnln
BBAAmix lnln xxxxnRS
0mix H
Real phase mixing
lglglglg
lg xxxxnRTG ,B,,B,,A,,A,
,
mix lnln Perfect gas mixing
Ideal solution (Raoult)
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9
Summary Lecture 5: colligative properties
Osmosis
P,T
h
Al
Al+
B
B*
Am,fus
*2
fusA,x
H
RTT
B*
Am,vap
*2
vapA,x
H
RTT
Freezing point depression Boiling point elevation
A*ln
mA,
aV
RTΠgh
BRTΠgh
A*
Am,fus
*2
fusA,ln a
H
RTT
A*
Am,vap
*2
vapA,ln a
H
RTT
Ideal solution: Ideal solution:
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10
Lecture 6: Efficiency of processes
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1690/1698
1784
1803/1824
1854/1862
Heat Work
Steam engine
Theory of efficiency
Definition Entropy
11
Lecture 6: Efficiency of processes: History
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Thomas Savery 1650-1715
1698
vacuum Steam-Water
pump
12
Lecture 6: History: Convert heat to work
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Denis Papin 1647-1712 1690
Steam-Water pump Using a Piston
13
Lecture 6: History: Convert heat to work
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Thomas Newcomen 1664-1729
+ (Thomas Savery)
The Proprietors of the Invention for Raising Water by Fire
Efficiency: 2-5 %
14
Lecture 6: History: Convert heat to work
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James Watt 1736-1819
1784 Steam engine
efficiency: 25 %
15
Lecture 6: History: Convert heat to work
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Sadi Carnot 1796-1832
Thermodynamical model system: heat engine
Is the amount of (useful) work limited? Is there an alternative medium for steam?
16
Lecture 6: Steam engines: Convert heat to work
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Sadi Carnot 1796-1832
Thermodynamical model system: heat engine
(useful) work
Heat (flow)
Heat (flow)
Is the amount of (useful) work limited? Is there an alternative medium for steam?
17
Lecture 6: Steam engines: Convert heat to work
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Sadi Carnot 1796-1832
(useful) work
Heat (flow)
Heat (flow)
TH and TC separated: no internal losses Process steps: isotherms and adiabats Idealized cycle: reversible process Arbitrary medium: perfect gas
Is the amount of (useful) work limited? Is there an alternative medium for steam?
18
Lecture 6: Steam engines: Carnot cycle
Qin
Qout
Win
Wout
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Sadi Carnot 1796-1832
(useful) work
Heat (flow)
Heat (flow)
TH and TC separated: no internal losses Process steps: isotherms and adiabats Idealized cycle: reversible process Arbitrary medium: perfect gas
Is the amount of (useful) work limited? Is there an alternative medium for steam?
19
Lecture 6: Steam engines: Carnot cycle
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Sadi Carnot 1796-1832
(useful) work
Heat (flow)
Heat (flow)
Maximal efficiency depends on
(TH -TC)
Transformation of heat into work always
involves losses (QC)
1824
20
Lecture 6: Steam engines: Carnot cycle
TH and TC separated: no internal losses Process steps: isotherms and adiabats Idealized cycle: reversible process Arbitrary medium: perfect gas
Is the amount of (useful) work limited? Is there an alternative medium for steam?
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Rudolf Clausius 1822-1888
WQU ddd
Äquivalenzwert der Verwandlung R. Clausius Philosophical Magazine, 12 (1856) p.81
1854
First law: conservation of energy U
Second law: transformations
(processes)
21
Lecture 6: Fundamentals of thermodynamics
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Rudolf Clausius 1822-1888
WQU ddd
0d
T
QS
1824
Sadi Carnot 1796-1832
1850
(useful) work
Heat (flow)
Heat (flow)
1865
First law: conservation of energy U
Second law: transformations
For all reversible cyclic processes
Maximal efficiency depends on
(TH -TC)
Transformation of heat into work always
involves losses (QC)
22
Lecture 6: Fundamentals of thermodynamics
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The entropy (spontaneously) always increases until thermodynamic equilibrium is reached
23
Lecture 6: Modern classical thermodynamics
WQU
0surtot SSS
T
dQdS
rev
T
QS
sur
ENTROPY ║
Heat +
Temperature
First law: conservation of energy U
Second law: processes
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24
Lecture 6: Modern classical thermodynamics
WQU
0surtot SSS
T
dQdS
rev
T
QS
sur
0tot T
dQdSdS dQTdS
for any spontaneous process:
TdSdQ Clausius inequality
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25
Lecture 6: Modern classical thermodynamics
TdSdQ
Clausius inequality
TdSdQ rev
TdSdQ irr
PdVTdSdVPdQdWdQdU ext
irr
rev. Process (mech. Work)
irr. Process (mech. Work)
any process
U is a state function, so independent of the path
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Hermann von Helmholtz 1821-1894
An isothermal reversible process delivers maximal (volume) work
dWdQdU
TSUA
26
Lecture 6: Fundamentals of thermodynamics
TSddUdA
dWdAT
Helmholtz free energy
SdTdWTdSSdTdWdQdA
TdSdQ
0dWfor work done by the
system on surroundings TAW max
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Josiah Gibbs 1839-1903
27
Lecture 6: Fundamentals of thermodynamics
dWdQdU
TSHG
TSddHdG
(Study guide: p.12)
TdSdQ
edWSdTdGP
e,dWdG
TP
TPGW
,
max
e
edWSdTTdSdQdGP
Isothermal isobaric reversible process delivers maximal (electric) work
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28
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Qh
Qc
Win
Wout
Sadi Carnot (1796-1832)
Carnot cycle
Reversible processes
29
Lecture 6: Energy conversion: Carnot cycle
Machine model: → cyclic process
Q→W for a steam engine
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Qh
Qc
Win
Wout
Carnot cycle
Reversible processes
30
Machine model: → cyclic process
Q→W for a steam engine or power station
Heat engine
Lecture 6: Energy conversion: Carnot cycle
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Qh
Qc
Win
Wout
Carnot cycle
Reversible processes
31
Machine model: → cyclic process
Q→W Heat engine
Qh
Qc
Wout
Win
Carnot cycle
Reversible processes
Machine model: → cyclic process
W→Q for a refrigerator
or heat pump
Lecture 6: Energy conversion: Carnot cycle
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Qh
Qc
Win
Wout
Reversible model
32
0 dS
S is state function
A
D
C
B
C
B
rev
dS0T
dQdS
c
c
h
h
T
Q
T
Q
c
c
D
C
D
C c
rev
T
Q
T
dQdS
For a (reversible) Carnot cycle
h
h
B
A
B
A h
rev
T
Q
T
dQdS
Study Guide p. 19-22
Lecture 6: Energy conversion: Carnot cycle
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Cyclic process
33
0 dU
U is state function
ch QQdQdW
0chinout QQWWdWNet work is done by the system on surroundings
(cf. exercise 6a for gasses)
0ch QQ0,0 hc QQ and
Lecture 6: Energy conversion: Carnot cycle
Qh
Qc
Win
Wout
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Cyclic process
34
0 dU
U is state function
(cf. exercise 6a for gasses)
ch QQdQdW
0ch QQ0,0 hc QQ and
“equilibrium” process
0T
Q
T
Q
c
c
h
hsursurtot SSSS
Lecture 6: Energy conversion: Carnot cycle
Qh
Qc
Win
Wout
c
c
h
h
T
Q
T
Q
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Carnot cycle
Efficiency of the process:
35
hcostenergy
energyuseful
Q
W
c
c
h
h
T
Q
T
Q
h
ch
h
ch
Q
Q
)0( c Q
h
c1
Q
Q
h
c1T
T
%)100x (
Lecture 6: Conversion efficiency: Carnot cycle
Qh
Qc
Win
Wout
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Power station
Thermodynamic efficiency of a Carnot cycle
36
h
c1T
T hc TT
10cT
0hc TT
1h
T
(steam) C500h
T
(dumped) C100c
T%52
Lecture 6: Conversion efficiency: Carnot cycle
Qh
Qc
Win
Wout
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Qh
Qc
Win
Wout
Reversible process
Thermodynamic efficiency of a Carnot cycle
37
h
c1T
T hc TT
10cT
0hc TT
1h
T
Irreversible process: h
c1T
T
Lecture 6: Conversion efficiency: Carnot cycle
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Qh
Qc
Wout
Win
Inverse Carnot cycle
38
Machine model: → cyclic process
W→Q for a refrigerator
or heat pump
Reversible processes
Lecture 6: Conversion efficiency: Carnot cycle
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Qh
Qc
Wout
Win
Inverse Carnot cycle
39
0 dS
S is state function
B
C
D
A
D
A
rev
dS0T
dQdS
h
h
A
B
A
B h
rev
T
Q
T
dQdS
c
c
C
D
C
D c
rev
T
Q
T
dQdS
Reversible processes
c
c
h
h
T
Q
T
Q
Lecture 6: Conversion efficiency: Carnot cycle
Machine model: → cyclic process
W→Q for a refrigerator
or heat pump
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Qh
Qc
Wout
Win
Inverse Carnot cycle
40
Machine model: → cyclic process
W→Q for a refridegerator
or heat pump
Reversible processes
0ch QQ0,0 ch QQ and
0T
Q
T
Q
h
c
h
hsurtot SS
Lecture 6: Conversion efficiency: Carnot cycle
surroundings
system
Non-spontaneous process
Freezer
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Qh
Qc
Wout
Win
Inverse Carnot cycle
41
Machine model: → cyclic process
W→Q for a refridegerator
or heat pump
Reversible processes 0 dU
U is state function
ch QQdQdW
0ch QQ0,0 ch QQ and
0QQ ch W
Lecture 6: Conversion efficiency: Carnot cycle
Work has to be done to run the process
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Qh
Qc
Wout
Win
Inverse Carnot cycle
42
Machine model: → cyclic process
W→Q for a refridegerator
or heat pump
Reversible processes Non spontaneous (forced) process
c: performance
Lecture 6: Conversion efficiency: Carnot cycle
ch
c
ch
cc
TT
T
Wc
c
c
h
h
T
Q
T
Q
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43
QF
RTEE ln
Nernst equation
)(Fe3 aq)(MnO4 aq
)(Fe2 aq)(Mn 2 aq
)(H aq
)(OH2 l)(OH2 l
Pt Pt
Lecture 6: Conversion efficiency: Batteries
E - + 0I
E
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44
QF
RTEE ln
Nernst equation
)(Fe3 aq)(MnO4 aq
)(Fe2 aq)(Mn 2 aq
)(H aq
)(OH2 l)(OH2 l
Pt Pt
Lecture 6: Conversion efficiency: Batteries
)(Fe3 aq)(MnO4 aq
)(Fe2 aq)(Mn 2 aq
)(H aq
)(OH2 l)(OH2 l
Pt Pt
E - + 0I 0I R
E E
?E
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45
QF
RTEE ln
Nernst equation
)(Fe3 aq)(MnO4 aq
)(Fe2 aq)(Mn 2 aq
)(H aq
)(OH2 l)(OH2 l
Pt Pt
Lecture 6: Conversion efficiency: Batteries
)(Fe3 aq)(MnO4 aq
)(Fe2 aq)(Mn 2 aq
)(H aq
)(OH2 l)(OH2 l
Pt Pt
E - + 0I 0I R
E E
?E
Q
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46
QF
RTEE ln
Nernst equation
)(Fe3 aq)(MnO4 aq
)(Fe2 aq)(Mn 2 aq
)(H aq
)(OH2 l)(OH2 l
Pt Pt
Lecture 6: Conversion efficiency: Batteries
)(Fe3 aq)(MnO4 aq
)(Fe2 aq)(Mn 2 aq
)(H aq
)(OH2 l)(OH2 l
Pt Pt
E - + 0I 0I R
E E
?E
Q
?
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47
QF
RTEE ln
Nernst equation
)(Fe3 aq)(MnO4 aq
)(Fe2 aq)(Mn 2 aq
)(H aq
)(OH2 l)(OH2 l
Pt Pt
Lecture 6: Conversion efficiency: Batteries
E - + 0I 0I R
E E
Q
dtR
EdtIEdtPdQ
2
e
1costenergy
energyuseful
e
dW
dQ
Joule heating: 100 % conversion
IRE
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48
QF
RTEE ln
Nernst equation
)(Fe3 aq)(MnO4 aq
)(Fe2 aq)(Mn 2 aq
)(H aq
)(OH2 l)(OH2 l
Pt Pt
Lecture 6: Conversion efficiency: Batteries
E - + 0I 0I R
E E
Q
dtR
EdtIEdtPdQ
2
e
1costenergy
energyuseful
e
dW
dQ
Joule heating: 100 % conversion
?E IRE
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49
EMF: ElectroMotive Force
Lecture 6: Conversion efficiency: Batteries
QRT
EE lnF
EMF
Nernst equation
LLterm IREE LiEMF EEE
Li
EMF
RR
EI
cellEMF EE
LiEMF IRIRE
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50
EMF: ElectroMotive Force
Lecture 6: Conversion efficiency: Batteries
LLterm IREE LiEMF EEE
Li
EMF
RR
EI
Li
LEMFL
RR
REE
LiEMF IRIRE QRT
EE lnF
EMF
Nernst equation
cellEMF EE
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51
Lecture 6: Conversion efficiency: Batteries
QRT
EE lnF
EMF
Nernst equation
cellEMF EE
Li
LEMFL
RR
REE
tR
Edt
R
EdQ
L
2
L
2
L
LL
constantL E
e
L
e
L
W
Q
dW
dQ
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52
Lecture 6: Conversion efficiency: Batteries
QRT
EE lnF
EMF
Nernst equation
cellEMF EE
Li
LEMFL
RR
REE
tR
Edt
R
EdQ
L
2
L
2
L
LL
constantL E
tGGdtdW rre
IFt /
e
L
e
L
W
Q
dW
dQ
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53
Lecture 6: Conversion efficiency: Batteries
QRT
EE lnF
EMF
Nernst equation
cellEMF EE
Li
LEMFL
RR
REE
tR
Edt
R
EdQ
L
2
L
2
L
LL
constantL E
tIEtWdW EMFeee
L
e
L
W
Q
dW
dQ
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54
Lecture 6: Conversion efficiency: Batteries
QRT
EE lnF
EMF
Nernst equation
cellEMF EE
Li
LEMFL
RR
REE
tR
Edt
R
EdQ
L
2
L
2
L
LL
constantL EEMFL
2
L
IER
E
e
L
e
L
W
Q
dW
dQ
tIEtWdW EMFee
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55
Lecture 6: Conversion efficiency: Batteries
QRT
EE lnF
EMF
Nernst equation
cellEMF EE
Li
L
EMF
L
EMF
L
EMFL
2
L
EMFL
2
L
/
/
RR
R
IE
IE
E
E
EE
E
IER
E
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56
Lecture 6: Conversion efficiency: Batteries
QRT
EE lnF
EMF
Nernst equation
cellEMF EE
Li
L
EMF
L
EMF
L
EMFL
2
L
EMFL
2
L
/
/
RR
R
IE
IE
E
E
EE
E
IER
E
Li
L
RR
R
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57
Summary Lecture 6: Efficiency of processes
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Qh
Qc
Wout
Win
Qh
Qc
Win
Wout
58
Summary Lecture 6: Energy conv.: Carnot cycle Carnot cycle
Reversible processes
Q→W
Carnot cycle
Reversible processes
W→Q c
c
h
h
T
Q
T
Q
h
c1T
T
ch
c
TT
T
c
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59
Summary Lecture 6: Energy convers.: Batteries
EMF: ElectroMotive Force
QRT
EE lnF
EMF
Nernst equation
cellEMF EE
e
L
dW
dQ
Li
LEMFL
RR
REE
Li
L
RR
R