Thermodynamics

 
Thermodynamics
University of Diyala
College of Engineering
Mechanical Engineering Department
Class: Second Year
Second Semester
ME210 : Thermodynamics
M
E
2
1
0
-
 
C
H
A
P
T
E
R
 
8
R
E
F
R
I
G
E
R
A
T
I
O
N
 
C
Y
C
L
E
S
B
y
L
e
c
t
u
r
e
r
S
a
m
e
e
r
 
D
.
 
A
l
i
L
a
y
t
h
 
A
b
e
d
 
H
a
s
s
n
a
w
e
2
R
E
F
R
I
G
E
R
A
T
O
R
S
 
A
N
D
H
E
A
T
 
P
U
M
P
S
for 
f
i
x
ed
 
va
l
u
e
s
 
of
Q
 
an
d
 
Q
L
H
T
he
 
o
b
j
e
ctive
 
of a refri
g
er
a
tor
 
is to rem
o
ve 
h
e
a
t
(
Q
L
)
 
from
 
the
 
cold
 
me
d
i
u
m;
 
the
 
o
b
j
e
ctive
 
of a h
e
at
p
u
mp
 
is to
 
su
p
p
l
y
 
h
e
at
 
(
Q
H
)
 
to a 
w
arm
 
me
d
i
u
m.
T
her
m
od
y
na
m
ic
s
-
CH
11
T
h
e
 
t
r
a
n
s
f
e
r
 
o
f
 
h
e
a
t
 
f
r
o
m
 
a
 
l
o
w
-
t
e
m
p
e
r
a
t
u
r
e
r
e
g
i
o
n
 
t
o
 
a
 
h
i
g
h
-
t
e
m
p
e
r
a
t
u
r
e
 
o
n
e
 
r
e
q
u
i
r
e
s
s
p
e
c
i
a
l
 
d
e
v
i
c
e
s
 
c
a
l
l
e
d
 
r
e
f
r
i
g
e
r
a
t
o
r
s
.
A
n
o
t
h
e
r
 
d
e
v
i
c
e
 
t
h
a
t
 
t
r
a
n
s
f
e
r
s
 
h
e
a
t
 
f
r
o
m
 
a
l
o
w
-
t
e
m
p
e
r
a
t
u
r
e
 
m
e
d
i
u
m
 
t
o
 
a
 
h
i
g
h
-
t
e
m
p
e
r
a
t
u
r
e
 
o
n
e
 
i
s
 
t
h
e
 
h
e
a
t
 
p
u
m
p
.
R
e
frig
e
rat
o
rs
 
a
n
d
 
h
e
at p
u
mps
 
are
 
ess
e
nti
a
l
l
y
the
 
same
 
d
e
vic
e
s;
 
th
e
y d
i
f
fer in
 
th
e
ir
ob
j
e
ctiv
e
s
 
on
l
y
.
3
T
H
E
 
R
E
V
E
R
S
E
D
 
C
A
R
N
O
T
 
C
Y
C
L
E
Sc
he
m
a
tic
 
o
f
 
a
C
a
rn
o
t
 
refri
g
er
a
tor
an
d
 
T
-
s
 
d
i
a
g
ram
of the
 
rev
e
rsed
C
a
rn
o
t
 
c
y
cl
e
.
The
 
reversed
 
Carnot
 
c
y
cle
 
is the
 
m
ost
 
efficient
 
refrig.
 
c
y
cle
 
operating
 
bet
w
een
 
T
L
 
and
 
T
H
.
It
 
is not
 
a
 
suitab
l
e
 
model
 
for
 
ref
r
igeration
 
c
y
cles since
 
proce
s
ses
 
2
-
3
 
and 4
-
1
 
are
 
not
 
pract
i
cal
be
c
au
s
e 
Process
 
2
-
3
 
involves
 
the
 
compression
 
of
 
a
 
liqui
d
–vapor
 m
i
x
ture,
 
w
hich
 
requires
 
a
compressor
 
that
 
w
ill
 hand
l
e
 
t
w
o
 
pha
s
es,
 
and
 
process
 
4
-
1
 
involves
 
the
 
expans
i
on
 
of
 
hig
h
-
moistu
r
e
-
content
 
r
e
frige
r
ant
 
in
 
a
 
tu
r
bine.
Both C
O
Ps increase as
t
he
 
d
i
f
f
erence
 
bet
w
een
 
t
he
t
w
o
 
t
empe
r
a
t
ures
dec
r
eases,
 
t
hat
 
is,
 
as 
T
L
rises or
 
T
H 
 
f
a
l
ls.
T
H
E
 
I
D
E
A
L
 
V
A
P
O
R
-
C
O
M
P
R
E
S
S
I
O
N
R
E
F
R
I
G
E
R
A
T
I
O
N
 
C
Y
C
L
E
T
h
e
 
v
a
p
o
r
-
c
o
m
p
r
e
s
s
i
o
n
 
r
e
f
r
i
g
e
r
a
t
i
o
n
 
c
y
c
l
e
 
i
s
 
t
h
e
 
i
d
e
a
l
 
m
o
d
e
l
 
f
o
r
 
r
e
f
r
i
g
e
r
a
t
i
o
n
s
y
s
t
e
m
s
.
 
U
n
l
i
k
e
 
t
h
e
 
r
e
v
e
r
s
e
d
 
C
a
r
n
o
t
 
c
y
c
l
e
,
 
t
h
e
 
r
e
f
r
i
g
e
r
a
n
t
 
i
s
 
v
a
p
o
r
i
z
e
d
 
c
o
m
p
l
e
t
e
l
y
b
e
f
o
r
e
 
i
t
 
i
s
 
c
o
m
p
r
e
s
s
e
d
 
a
n
d
 
t
h
e
 
t
u
r
b
i
n
e
 
i
s
 
r
e
p
l
a
c
e
d
 
w
i
t
h
 
a
 
t
h
r
o
t
t
l
i
n
g
 
d
e
v
i
c
e
.
T
h
i
s
 
is the
 
most
w
i
d
ely
 
us
e
d
 
c
y
cle
for refri
g
er
a
tors,
A
-C s
y
stems,
 
a
n
d
hea
t 
pu
m
p
s.
Schematic
 
and
 
T
-
s
d
i
agr
a
m
 
for 
t
he i
d
eal
vap
o
r
-compress
i
on
refri
g
er
a
tion
 
c
y
cl
e
.
4
An
 
or
d
i
n
ary
hou
s
eho
ld
refri
g
er
a
to
r
.
T
he
 
P
-
h
 
d
i
a
g
ram
 
of an
 
id
e
al
 
va
p
or-
com
p
ress
i
on
 
refri
g
er
a
tion
 
c
y
cl
e
.
T
he
 
ideal vapo
r
-
comp
r
ess
i
on 
r
e
f
rigera
t
ion
 
c
y
cle
 
invo
l
ves
 
an
 
ir
r
eversib
l
e
 
(
t
hro
tt
ling)
process
 t
o
 
make
 
it a
 
mo
r
e
 
real
i
s
t
ic
 
model 
f
or the ac
t
ual
 
s
y
s
t
ems.
Rep
l
ac
i
ng
 
t
he
 
e
x
pans
i
on
 
va
l
ve
 
by
 
a
 
t
urbine
 
is
 
not prac
t
ical since 
t
he
added benefits cannot
 
jus
t
i
f
y
 t
he
 
added
 
cost and
 
comple
x
i
t
y
.
Stead
y
-
flow
energy
 
balan
c
e
5
6
A
C
T
U
A
L
 
V
A
P
O
R
-
C
O
M
P
R
E
S
S
I
O
N
R
E
F
R
I
G
E
R
A
T
I
O
N
 
C
Y
C
L
E
An
 
ac
t
ual vapor
-
comp
r
ess
i
on 
r
e
f
rigera
t
ion
 
c
y
cle
 
d
i
f
f
ers f
r
om the ideal one
 
o
w
ing
mos
t
ly
 t
o
 
t
he
 
ir
r
eversib
i
l
it
ies
 
t
hat
 
occur 
i
n
 
various componen
t
s,
 
main
l
y
 
due
 
t
o
 
f
lu
i
d
f
riction 
(causes pressu
r
e
 
drops) and
 
heat
 
t
rans
f
er
 
t
o
 
or f
r
om the sur
r
ound
i
ng
s
.
Sc
he
m
a
tic
 
an
d
T
-
s
 
d
i
a
g
ram
 
for
the
 
actu
a
l
va
p
o
r
-
com
p
ress
i
on
r
e
fri
ge
r
a
ti
o
n
c
y
cl
e
.
D
I
F
F
E
R
E
N
C
E
S
N
o
n
-is
e
ntr
o
p
i
c
 
com
p
ress
i
on
S
u
p
e
rh
e
at
e
d
 
va
p
or
 
at
 
ev
a
p
o
rat
o
r
 
e
x
it
S
u
bc
o
o
l
ed
 
l
i
q
u
id
 
at
 
co
n
d
e
ns
e
r
 
e
x
it
Pr
e
ss
u
re
 
d
r
op
s in c
onden
s
e
r
 
an
d
 
e
v
apo
r
a
tor
T
he
 
COP
 
dec
r
eases as
 
a result
of ir
r
eversib
i
l
it
ies.
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Refrigeration cycles involving refrigerators and heat pumps are explored, including the ideal vapor-compression cycle and the reversed Carnot cycle. Learn about the efficiency and practicality of different cycles in transferring heat between temperature regions.

  • Thermodynamics
  • Refrigeration Cycles
  • Heat Pumps
  • Vapor-Compression
  • Efficiency

Uploaded on Feb 19, 2025 | 0 Views


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  1. University of Diyala College of Engineering Mechanical Engineering Department Class: Second Year Second Semester ME210 : Thermodynamics ME210- CHAPTER 8 REFRIGERATION CYCLES By Lecturer Sameer D. Ali Layth Abed Hassnawe Thermodynamics

  2. REFRIGERATORSAND HEAT PUMPS The transfer of heat from a low-temperature region to a high-temperature one requires special devices called refrigerators. Another device that transfers heat from a low-temperature medium to a high- temperature one is the heat pump. Refrigerators and heat pumps are essentially the same devices; they differ in their objectives only. The objective of a refrigerator is to remove heat (QL) from the cold medium; the objective of a heat pump is to supply heat (QH) to a warm medium. for fixed values of Q and Q L H 2 Thermodynamics-CH11

  3. THE REVERSED CARNOT CYCLE The reversed Carnot cycle is the most efficient refrig. cycle operating between TLand TH. It is not a suitable model for refrigeration cycles since processes 2-3 and 4-1 are not practical because Process 2-3 involves the compression of a liquid vapor mixture, which requires a compressor that will handle two phases, and process 4-1 involves the expansion of high- moisture-content refrigerant in a turbine. Both COPs increase as the difference between the two temperatures decreases, that is, as TL rises or TH falls. Schematic of a Carnot refrigerator and T-s diagram of the reversed Carnot cycle. 3

  4. THE IDEAL VAPOR-COMPRESSION REFRIGERATION CYCLE The vapor-compression refrigeration cycle is the ideal model for refrigeration systems. Unlike the reversed Carnot cycle, the refrigerant is vaporized completely before it is compressed and the turbine is replaced with a throttling device. This is the most widely used cycle for refrigerators, A-C systems, and heat pumps. Schematic and T-s diagram for the ideal vapor-compression refrigeration cycle. 4

  5. The ideal vapor-compression refrigeration cycle involves an irreversible (throttling) process to make it a more realistic model for the actual systems. Replacing the expansion valve by a turbine is not practical since the added benefits cannot justify the added cost and complexity. Steady-flow energy balance An ordinary household refrigerator. The P-h diagram of an ideal vapor- compression refrigeration cycle. 5

  6. ACTUAL VAPOR-COMPRESSION REFRIGERATION CYCLE An actual vapor-compression refrigeration cycle differs from the ideal one owing mostly to the irreversibilities that occur in various components, mainly due to fluid friction (causes pressure drops) and heat transfer to or from the surroundings. The COP decreases as a result of irreversibilities. DIFFERENCES Non-isentropic compression Superheated vapor at evaporator exit Subcooled liquid at condenser exit Pressure drops in condenser and evaporator Schematic and T-s diagram for the actual vapor- compression refrigeration cycle. 6

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