CHAPTER 6
Tds Equations
Entropy and Available Energy
Consider two identical bodies, each of mass m, and
heat capacity cP, but one at temperature T1, and the other at temperature T2. When placed in contact,
heat flows from the hotter to the cooler, until they come to a common temperature,
2
2 1 T
T Tf
Entropy Change
3
1 2
1 2
2 ln
2
P
T T
S mc
T T
1 2
1 2
ln ln
f f
T T f f
P P
T T
T T
dT dT
S mc mc
T T T T
2 2
1 2 1 2 1 2
ln f ln f 2 ln f
P P P
T T T
mc mc mc
T T T T T T
Entropy Increased
4
1 2
2
1 2T
T
TT
2 1 2
(
T
T
)
0
2 2
1 2
2
1 20
T
T
TT
2 2
1 2
2
1 24
1 2“Lost” Work
5
2 2
1 2
2 1 2 1
ln Tf 0 Tf 1 Tf T T
T T T T
Run a Carnot engine between the two bodies.
2 1 2 1
2 1 2 1
0 P
dQ dQ dT dT
mc
T T T T
2 1
2 1
2 1 2 1
ln ln 0
f f
T T
f f
T T
T T
dT dT
T T T T
Amount of Work
6
1 2
1 2
2
2
P
T T
W mc T T
2 1
W Q Q
2 1
( ) ( )
P f f
W mc T T T T
1 2 2
P f
W mc T T T
1 2 2 1 2
P
Tds Equations
7
v P
P v
P v
c c
T T
Tds c dv c dP dv dP
v P v
v v
v
P T
Tds c dT T dv c dT dv T
P P
P
v
Tds c dT T dP c dT Tv dP
T
Internal Energy
8
v
T
u
du
c dT
dv
v
v T
u
u
du
dT
dv
T
v
Thermo & Stat Mech - Spring 2006 Class 7
9
v
T
u
Tds
c dT
P dv
v
Internal Energy
Tds
du
Pdv
v
T
u
du
c dT
dv
v
First Tds Equation 10 v v c s T T v T u
Tds c dT P dv
v 1 v T c u
ds dT P dv
T T v
v T s s
ds dT dv
T v 1 T T s u P v T v
First Tds Equation (cont.)
11
1
v
T
T v
c u
P
v T T T v
v
v
c s
T T
1
T T
s u
P
v T v
2 2
s s
v T T v
First Tds Equation (cont.) 12 2 1 1 v v T T
c u u
v T v T T T v T
2 2 2
1 1 1
v T
u u P u
P
T v T T T v T T v
2 2
1 1 1
T v v T
u u P u
P P
T T v T T v T T v
2 1 1 v T P u P
T T T v
13
First Tds Equation (cont.)
v T
P u
T P
T v
2
1 1
v T
P u
P
T T T v
v
T
u
Tds c dT P dv
v
v
v
P
Tds c dT T dv
T
The First Tds Equation (cont.)
14
v
v
P
Tds
c dT
T
dv
T
cP – cv
15
p v
T
u
c c P v
v
p v
T
u
c c P v
v
v
T
u
dq c dT P dv v
cP – cv
16
2
p v
Tv c c
p v
v T P
P P v
c c T v Tv
T v T
p v
T
u
c c P v
v
1 ,
T P
P v
v
v v T
Enthalpy
17
P
T
h
Tds dh vdP c dT v dP
P
P
P T T
h h h
dh dT dP c dT dP
T P P
, so
h
u
Pv
2nd Tds Equation 18 P P c s T T p T h
Tds c dT v dP
P 1 p T c h
ds dT v dP
T T P
P T s s
ds dT dP
T P 1 T T s h v P T P
2nd Tds Equation (cont.)
19
1
P
T
T P
c h
v
P T T T P
P
P
c s
T T
1
T T
s h
v
P T P
2 2
s s
P T T P
2nd Tds Equation (cont.) 20 P T v h T v T P 2 1 1 P P T T
c h h
P T P T T T P T
2 2
1 1 1
T P P T
h h v h
v v
T T P T T P T T p
2 1 1 P T v h v
T T T P
2nd Tds Equation (cont.)
21
p
P
v
Tds
c dT
T
dP
T
P
T
h
Tds c dT v dP P
Third Tds Equation
v
v v
c
s T
P T P
22
Consider s s P v( , )
v P
s s
ds dP dv
P v
1
v v v v v
s s T T s T
P T P T T P
Third Tds Equation
23
P
P P
c
s T
v T v
v P
s s
ds dP dv
P v
1
P P P P p
s s T T s T
v T v T T v
Third Tds Equation
24
v P
v P
T T
Tds c dP c dv
P v
v P
s s
ds dP dv
P v
v P
v P
c T c T
ds dP dv
T P T v
THE 3 Tds EQUATION
25
P v
P v
T T
Tds c dv c dP
v P
v
v
P
Tds c dT T dv
T
P
P
v
Tds c dT T dP
T
Joule Coefficient
26
v
T
u c
v
v T
P u
T P
T v
v
v
P
c
T
P
T
Joule Thomson Coefficient
27
P
T
h c
P
P T
v h
T v
T P
P
P
v
c
v T
T
Various thermodynamic relation from the TdS Eq
28
v
v
P
Tds c dT T dv
T
,
v v
c s
T T
T v
s P
v T
29
Various thermodynamic relation from the TdS Eq cont…
P
P
v
Tds c dT T dP
T
,
P P
c s
T T
T P
s V
P T
30
Various thermodynamic relation from the TdS Eq cont…
P v
P v
T T
Tds c dv c dP
v P
P
P P
c
s T
v T v
v
v v
c
s V
P T P