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Thermodynamics I Chapter 6 Entropy. Mohsin Mohd Sies Fakulti Kejuruteraan Mekanikal , Universiti Teknologi Malaysia. Entropy (Motivation). The preferred direction implied by the 2 nd Law can be better understood and quantified by the concept of entropy. - PowerPoint PPT Presentation
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Thermodynamics IChapter 6Entropy
Mohsin Mohd SiesFakulti Kejuruteraan Mekanikal, Universiti Teknologi Malaysia
Entropy (Motivation)
The preferred direction implied by the 2nd Law can be better understood and quantified by the concept of entropy.Entropy quantifies the 2nd Law and imposes the direction of processes.Here we will study entropy and how processes will proceed only in the direction of increasing entropy.
Clausius Inequality
Erev Eirrev
QH QH
QL QL,irrev
W Wirrev
TH
TL
Consider two heat engines between the same temperatures
Consider of the whole cycleTQ
(a) Erev
0
0
11
rev
L
L
H
H
LL
HH
L
L
H
H
rev
TQ
TQ
TQ
QT
QT
TQ
TQ
TQ
(b) Eirrev
ΔQ+Q=QQ>Q
LirrevL,
LirrevL,
Combined to be:
= 0 if reversible< 0 if irreversible> 0 impossible
ENTROPY
1
2B
A
2
1
1
2
2
1
1
2
2
1
0
B
BA
BArev
TQ
TQ
TQ
TQ
TQ
TQ
Does not depend on path; thermodynamic property!
Let's call this property entropy, S [kJ/K]
revTQdS
Entropy , S = extensive property [kJ/K]
Specific entropy, s = intensive property [kJ/kg.K]
2
112
2
1revT
QSSdS
We have actually defined entropy change
From statistical thermodynamics, entropy ~ measure of molecular disorderWork is an ordered form of energy (High quality)
No entropy transfer along with work transferHeat is a disordered form of energy (Low quality)
Entropy is transferred along with heat transfer
“Entropy = zero for pure crystal at 0 K”Third Law of Thermodynamics
Entropy with a 0 K reference is called absolute entropy
T-ds Relations
To find the relationship between Q and T so that the integration of Q/T can be performed
- From the 1st Law (neglecting KE & PE)
pdvduTdspdVdUTdSdUpdVTdS
(a)
dU=δWδQU=WQ
revrev
pdV=δWTdS=δQ
rev
rev
- From the definition of enthalpy
vdppdvdhduvdppdvdudh
pvuh
From (a)
vdpdhTdspdvvdppdvdh
pdvduTds
(b)
Tvdp
Tdhds
Tpdv
Tduds
&
vdpdhTdspdvduTds
Can be used for S of any process (rev. & irrev.)Can be used for open & closed system
T-ds Relations
Entropy Change of Pure Substances
Can be obtained from Tds Relations in conjunction with other thermodynamic relationsFor 2 phase substances like water and R-134a, use property tables
S = S2 – S1
For ideal gas, from Tds relations
1
2
1
212 lnln
vvR
TTCsss
vdvR
TdTCds
vdvR
TdTCds
Tpdv
Tduds
v
v
v
vR
TpRTpv
dTCdu v
Assume Cv=constant& integrate
1
2
1
212 lnln
ppR
TTCsss
pdpR
TdTCds
pdpR
TdTCds
Tvdp
Tdhds
p
p
p
Another relation,
pR
TvRTpv
dTCdh p
Assume Cp =constant& integrate
1
2
1
212
1
2
1
212
lnln
lnln
ppR
TTCsss
vvR
TTCsss
p
v
Both equations give the same resultChoose according to available data..
Entropy change
Isentropic Processes, S = 0
For ideal gases, with constant Cp & Cv
1
2
1
1
2
1
2
1
1
2
2
1
1
2
1
2
1
2
1
2
1
2
1
2
lnln
lnlnln
lnln
0lnln
k
k
CR
v
v
v
vv
TT
vv
TT
vv
vv
CR
TT
vvR
TTC
vvR
TTCs
v
1
kCR
CC
k
RCC
v
v
p
vp
kk
kk
CR
p
p
pp
TT
pp
pp
pp
CR
TT
ppR
TTCs
p
1
1
2
1
2
1
1
2
1
2
1
2
1
2
1
2
1
2
ln
ln
lnln
0lnln
Another one
kk
CR
kCC
CC
CR
RCC
p
p
v
p
p
p
vp
1
11
Combined to become
1
2
1
1
1
2
1
2
kk
k
vv
pp
TT Isentropic process
for ideal gas, constant Cp , Cv
dpv=w
vdp=δw
ped+ked+dh=δwvdpdh
ped+ked+dh=δwδq
rev
rev
rev
revrev
2
1
Work for Open Systems
Reversible boundary work for closed systems
pdvwB
Open system reversible work, from 1st Law (single inlet/outlet)
Reversible work for open system
neglecting ke & pe, & rearrange;vdpdh=δq
vdpdh=TdsTds=δq
rev
rev
Increase in Entropy Principle
• For reversible processes, entropy of universe (system surrounding) doesn't change, it is just transferred (along with heat transfer)
• In real processes, irreversibilities cause entropy of universe to increase• Heat reservoirs don't have irreversibility• To simplify analysis, assume irreversibilities to exist only inside the
system under study.• Inside the system, entropy transfer and generation occur.
irrev
1
2
rev
Irreversible cycle since one of the processes is irreversible
From Clausius Inequality;
gen
irrev
irrev
S+TδQ=SS
TδQSS
TδQ>SS
TδQ<SS
2
112
2
112
2
112
2
112
Rearrange
Generalize for all processes
= when rev> when irrev< impossible
Sgen=entropy generated = 0 when rev. > 0 when irrev. < 0 impossible
genb
STQSS
2
112
Change of system entropy
Transfer of entropy (T where Q is transferred, usually at boundary
Entropy generation
Entropy Generation for Closed System
Sgen is the measure of irreversibilities involved during process
S surrounding or system may decrease (-ve), but S total (surrounding + system) must be > 0
Entropy of universe always increases (Entropy increase principle)
No such thing as entropy conservation principle
For a process to occur, Sgen> 0
0 systemgsurroundinuniversetotal,gen ΔS+ΔS=ΔSS
Entropy Generation for Closed System
gen
n
j j
j
genb
genb
STQ
SS
STQSS
STQSSS
112
12
12
For multiple heat transfers at different temperatures
gen
n
j j
j
gen
n
j j
j
STQ
dS
STQ
dtdS
1
1
In rate form
In differential form
Sgen - depends on the process (friction, T etc.) - not a property
Entropy Generation for Closed System
Entropy Generation for Open Systems
Apart from heat, mass flows also carry entropy along with them
Qin
min
sin
mout
soutCV
genoutinj j
jCV
genoutinj j
jCV
SmsmsTQ
S
SSSTQ
S
1
1
genoutinj j
jCV SsmsmTQ
dtdS
1
Rate of change of system entropy
Rate of entropy transfer
Rate of entropy generation
Qin
min
sin
CV
Entropy Generation for Open Systems
Steady Flow Process
genooiij j
j
genooiij j
jCV
CV
outinCV
SsmsmTQ
SsmsmTQ
dtdS
dtdS
mmdt
dm
1
1
0
0
0
mS
Tm
Qss
SssmTQ
gen
j jio
genoij j
j
j
1
1
)(0
single inlet/outlet;
Steady Flow Process
Reversible adiabatic process = isentropic process
Isentropic is not necessarily reversible adiabatic
Reversible process Sgen = 0
Produces Wmax
Consumes Wmin
30
ISENTROPIC EFFICIENCIES OF STEADY-FLOW DEVICES
The isentropic process involves no irreversibilities and serves as the ideal
process for adiabatic devices.
The h-s diagram for the actual and isentropic processes of an adiabatic turbine.
Isentropic Efficiency of Turbines
Also known as Adiabatic Efficiency or 2nd Law Efficiency
31
Isentropic Efficiencies of Compressors and Pumps
The h-s diagram of the actual and isentropic processes of an
adiabatic compressor.
Compressors are sometimes intentionally cooled to minimize the work input.
When kinetic and potential energies are negligible
32
Isentropic Efficiency of Nozzles
The h-s diagram of the actual and
isentropic processes of an
adiabatic nozzle.
If the inlet velocity of the fluid is small relative to the exit velocity, the energy balance is
Then,
A substance leaves actual nozzles at a
higher temperature (thus a lower velocity) as a result of friction.