Refrigeration Graphic (Coolpack)
November 23, 2022 | Author: Anonymous | Category: N/A
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Description
0 3 0 0 0.
Ref :R.Döring. Klima+Kälte ingenieur Ki-Extra 5, 1978 200.00 R717 DTU, Department of Energy Engineering s in [kJ/(kg K)]. v in [m^3/kg]. T in [ºC] M.J. Skovrup & H.J.H Knudsen. 12-04-23
5 7 . 3 = s 0 3 1
0
4 0 0 0 0 0.
2
100.00 1 0 0
6 0 8 0 0 0 .0 0 0 0 0 0. 0 0 v = 0 v = 1 0 0
0 8
0 0 v =
0 7
5 0 4
]
0 0 v =
0
r
0 0 v = 3
a [B 0
P
r
e
s
s
u
2
10.00 9.00 8.00 7.00 6.00 5.00
0 0 v =
0
0 0 v = 0
1 -
50
0 3 0 . 0
0 2
2.00
0 5 . 0 = s
0 3 3 0 0 0. 0
5 2 . 5 = s
20
3 -
0 5 0 0 5 0. 0 0. 0 6 0 0. 0 6 0 7 0 0. 0 7 0. 0 8 0 9 0 0 9 0.. 0 0 0..1 0 0
0
0. 4 0 0. 5 0
0 5 . 6 = s
-10
0.. 6 0 0 0 7 0 0. 7 0. 8 0 0. 9 0 1. 0
5 7 . 6 = s
0 0 7. = s =
-20
. 6 0 0 6 v = 0
0.. 2 0 2 0 0
5 2 . 6 = s
10
1 5 . 1
0..1 5 0
0 3 0 0. 3 0.
4 0 0. 4 v = 0. 0
0 4 0 0 4 0.. 0 0
0 . 0 6 = s
30
0 .0 6 0
3 0 0. 3 v = 0 -
0.. 0 2 0 0
5 7 . 5 = s
40
0 4 0 . 0
.2 0 0 2 v = 0
3.00
-30
0 1. 0 v = 1
-40
1. 5
2 5 7. = s
2.. 0 2
5 0 7. = s
8 0 0. 8 v = 0
1.00 0.90 0.80 0.70 0.60 0.50
0 0. 0 1
60
1 0 . 1
0 v = 0 0
0 0 9 0 0. 0
0 5 . 5 = s
70
0 . 0 8 0 0 0 v = 1
4.00
5 7 . 4 = s
80
.0 2 0 0 0 0 v = 0
20.00
.
0 . 0 0 8 0 0
0.. 01 5 0
90
5 . 0 1 0 0 0 v =
6
30.00
0 5 . 4 = s
0 0 0 7 0. 0
100 9
0
e
5 2 . 4 = s
110 1
40.00
0 .0 0 6 0 0
120 1
90.00 80.00 70.00 60.00 50.00
r
0 0 . 4 = s
130 1
0
5 0 . 0 0 0
7 5 7. = s
-40
3. 0 4. 0
x = 0.10
0.20
s = 1.00
0
100
200
0.30
0.40
2.00
300
400
0.50
0.60
3.00
500
600
0.70
4.00
700
800
0.80
0.90
5.00
900 1000 1100 Enthalpy [kJ/kg]
-40 -20 0
20 40 60 80 100 120 140 160 180 200 220
6.00
1200
1300
1400
1500
1600
1700
1800
1900
2000
1 5 . 0 0 0
Ref :R.C.Downing. ASHRAE Transactions 1974. Paper No. 2313. 60.00 R11 DTU, Department of Energy Engineering s in [kJ/(kg K)]. v in [m^3/kg]. T in [ºC] 50.00 M.J. Skovrup & H.J.H Knudsen. 12-04-23 40.00
0
1 1
0 1 0 1 1 0 0 9 0 8 0
0 0 v =
7 6 0
[B
4
2.00 r
e
0 0 v =
0
u 3
s e P
r 0 2
1.00 0.90 0.80 0.70 0.60 0.50 0.40
0 1 5 . 0
80 70
0 1
0 30 0.0 3 0 40 0.0 4
0 4 0 . 0
0 8 . 1 = s
40
5 8 . 1 = s
30
0 0 v =
0 1
2 0 . 2
0 20 0. 2
0 0 v = 20
0
0.20
3 0 . 3
0.5 0
-10
6 0 0. 6 v = 0 0 3 -
0 .6 0 0 70 0 . 7 0 .8 0 0 90 0 . 9 1 .0
5 0 . 2 = s
0 4 . 4 0 v = 0. -
1 . 0 2 = s
-20
1 .5 2..0 2
5 1 . 2 = s
8 0 0. 8 v = 0
.0 1 0 v = 1
0.10 0.09 0.08 0.07 0.06 0.05
0 40 0. 4
0 0 . 2 = s
-
0.30
0 30 0. 3
5 9 . 1 = s
20
. 1 5 0 0 1 v =
0.1 5
0 9 . 1 = s
10 0
0. 050 0. 060 0 70 0.0 7 0. 080 0 90 0.0 9 0. 10
0 7 . 1 = s 5 7 . 1 = s
50
0 . 0 6 0 0 0 v = 0 8 . 0 0 0 0 v = 1 . 1 0 0 0 v =
s
0 20 0.0 2
90
0 . 0 3 0 0 0 v =
0
15 01 0.. 0 0
110
60 5
5 0 05 0 0 0.. 0 0 6 0 06 0. 0 0 0. 0 7 0 0 7 0 0 0.. 0 0 8 0 08 0 0 0.. 0 0 9 0 0 9 0 0 0 0.. 0 0 1 0 01 0.. 0 0
100
0 2 0 0. 0 0 v = 0
0. 0 0 4 0
150 140 130 120
0 .0 0 8 0 0 0 v = 0 0 . 0 1 0 0 v = 1
0
a
2 0 . 0 0 0 0 v = = 0 3 0 . 0 0 0 0 v = 4 0
. 0 0 0 0 0 v = 6 0 . 0 0 0 0 0 v =
2
3 0 0. 0 0
180 170 160
1 1
4
3.00
1 6
5 0
30
20.00
r
1 7
0
30.00
]
8 0
0
10.00 9.00 8.00 7.00 6.00 5.00 4.00
1 0
2 0 . 0 0 0 0
5 6 . 1 190 = s 9
-30
3..0 3 4..0 4
. 5 1 5 v = 1 0 4 -
5 .0 6 .0
-40 x = 0.10
0.20
0.30
s = 1.00
160
180
200
0.40
0.50
0.60
1.20
220
240
0.70
0.80
1.40
260
280
0.90
-40 -20
0
20
40
60
80
100
120
140
160
180
200
220
240
260
1.60
300
320
340 360 380 Enthalpy [kJ/kg]
400
420
440
460
480
500
520
540
560
70.00 60.00
5 1 0 0 0.
R12
Ref :R.C.Downing. ASHRAE Transactions 1974. Paper No. 2313. DTU, Department of Energy Engineering s in [kJ/(kg K)]. v in [m^3/kg]. T in [ºC] M.J. Skovrup & H.J.H Knudsen. 12-04-23 1 1 0 0
40.00 9
0
5
4
u e
5.00
]
P
r
s
s
r
e
[B
a
60
0 3
0 2
15 01 0.. 0 0
5 5 . 1 = s
0 2 0 0 2 0.. 0 0
50
6 0 . 0 0 0 0 0 v = 8 0 0 0 0. 0 0 v = 0 0. 0 0. 0 1 v = 0
r
70
3 0 . 0 0 v = 4 0 0 . 0 0 0 0 v = 6
0
10.00 9.00 8.00 7.00 6.00
80
0 2 0 0 0 . 0 v =
7
0 8 0 0 0 8 0.. 0 0 0.. 0 0 9 0 0 1 0 01 0.. 0 0
90 0 8
20.00
0 5 0 0 5 0 0 0. 0
0.. 0 0 6 0 0 7 0 0 7 0 0 0.. 0 0
100 0
0
0 3 0 0 3 0.. 0 0
40 0 6 . 1 = s
30
0 7 . 1 = s
5 6 . 1 = s s
5 7 . 1 = s s
20 0
5 0 1 0. 0 0 v = 0 0 2 0 0 0. v = 1
4.00 0
0
0 0 v = 1 -
10
0 2 -
0 0 v = 0
0 4
1 0 . 1
0. 0 9 0 0. 0..1 0 0
0 9 . 1 = s
0..15 0
3 0 0. 3 0 0.
0 0 . 2 = s
-30 1 5 . 1 .2 0 0 2 v = 0
0.. 2 0 0
5 9 . 1 = = s
-20
0 0 v = -
0.. 0 7 0 0 8 0 08 0.. 0 0
0 8 0 . 0
0 0 v =
1.00 0.90 0.80 0.70 0.60
6 0 06 0.. 0 0
-10
0 6 0 . 0
0 0 v = 3 -
5 0 05 0.. 0 0
5 8 . 1 = s
0 0 3 . 0
0 0 4 0 0 0. v =
2.00
0 4 0 0 4 0.. 0 0
0 8 . 1 = s
0
3.00
0 0. 0 0 4
110 1
30.00
3 0 0 . 0 0
0 5 . 1 = s
0
50.00
2 0 . 0 0 0
4 0 0. 4 0 0. 0.5 0 0.
-40
0.6 0 0.
0.50
x = 0.10
0.20
0.30
0.40
s = 1.00
140
160
180
200
0.50
0.60
1.20
220
240
0.70
0.80
0.90
-40
-20
0
20
40
60
80
100
120
140
160
180
200
1.40
260
280
300 320 340 Enthalpy [kJ/kg]
360
380
400
420
440
460
480
500
50.00 40.00
1 5 0 0 0.
R13 Ref :R.C.Downing. ASHRAE Transactions 1974. Paper No. 2313. DTU, Department of Energy Engineering s in [kJ/(kg K)]. v in [m^3/kg]. T in [ºC] M.J. Skovrup & H.J.H Knudsen. 12-05-06
2 0 . 0 0 0
2 0
20 1
30.00
2 0 0 0 0. 0 0 0 v = 0 3 0 0 . 0 0 v = 0 0 4 0 0 . 0 0 v = 0 6 0 0 0 . 0 0 v = 0 8 . 0 0 0 0 0 v = 0 1 0 0. 0 0 v = 0 1
20.00 0 2 0 3 -
10.00 9.00 8.00 7.00 6.00 5.00 4.00
0 4 0 5 -
v =
0 6 -
v =
3.00 0
]r -
B
2.00 [ e r 0
u 8 -
s s e P
r
v =
1.00 0.90 0.80 0.70 0.60 0.50 0.40
9 -
0 1 -
0 40 0.0 4
5 5 . 1 = s
-60
0 6 . 1 s s =
5 6 . 1 = s
-70
0 . 0 6 0 0 0
0. 050 0. 060 0 70 0.0 7 0. 080 0 90 0.0 9 0. 10
0 5 . 1 = s
-50
0 .0 2 0 0 0
0 30 0.0 3
5 4 . 1 = s
-40
5 . 0 1 0 0 0
0 20 0.0 2 0 4 . 1 = s
-30
0. 15 0 20 0. 2
0 7 . 1 = s
-80
0 30 0. 3
5 7 . 1 = s
0 40 0. 4
0 8 . 1 = s
-90
.2 0 0 2 v = 0
0.30 10
v = 4 0 0 0 . 4 v = -
0. 50
-100
0 9 . 1 s = s
0 1. 0 v = 1
-120
2..0 2
0 0 2. = s
8 0 0. 8 v = 0
0.10 0.09 0.08 0.07 0.06 0.05
1. 5
9 5 1. = s
-110
. 6 0 0 6 v = 0
0. 60 0 70 0. 7 0. 80 90 9 . 0 0 1. 0
5 8 . 1 = s
. 3 0 0 0 3
1
6 0 06 0 0 0. 0 0. 0 7 0 0 7 0 0 0.. 0 0 8 0 08 0 0 0.. 0 0 0 9 0 0 9 0 0 0 0.. 0 1 0 01 . 0 0 0. 01 5
1 5 0 . 1 v = 0 0
5 0 05 0 0 0. 0 0.
-10 -20
. 0 8 0 0 0 0 v = 0 . 1 0 0 1 v = 0
0.20
0
0 . 0 3 0 0 0 v = 0 4 0 0 0. 0 v = 7
a
0 0 4 0 0. 0
5 3 . 1 = s
10 0
0 . 0 0 3 0 0
0 3 . 1 = s
0
0 5 2. = s
-120
3..0 3 4..0 4 5. 0
x = 0.10
0.20
s = 0.60
80
100
0.30
0.40
0.80
120
140
0.50
0.60
1.00
160
0.70 1.20
180
200
0.80
0.90
-120 -100 -80
-60
-40
-20
0
20
40
60
80
100
120
1.40
220
240 260 Enthalpy [kJ/kg]
280
300
320
340
360
380
400
50.00 40.00
1 5 0 0 0.
R14
Ref :R.C.Downing. ASHRAE Transactions 1974. Paper No. 2313. DTU, Department of Energy Engineering s in [kJ/(kg K)]. v in [m^3/kg]. T in [ºC] M.J. Skovrup & H.J.H Knudsen. 12-05-06
2 0 . 0 0 0
0 -
-50 0 6 -
30.00
-60 0 7 -
20.00
2 0 .0 0 0 0 0 3 0 v = 0 0 0. 0 0 4 0 v = 0 0 0 0 0. v = 6 0 0 0 0 0 0. v = 0 8 .0 0 0 0 0 v = 1 0 0 . 0 0 0 v =
0 8 0 9 -
10.00 9.00 8.00 7.00 6.00 5.00 4.00
0 0 1 0 1 -
3.00 02 1
B
a e r u s
0
s 3 1
P
r
e -
1.00 0.90 0.80 0.70 0.60 0.50 0.40
0 0 v = v =
0
v = 4 1
0 0 v = v =
0.30
5 0 05 0 0 0.. 0 0
-90
50
0 20 0.0 2
5 0 . 2 = s
0 30 0.0 3
0 1 . 2 = s
2 = s
-120
0.050 0.060 0 70 0.0 7 0.080 0 90 0.0 9 0.10
5 2 . 2 = s 0 2 . 3 = s 5 3 . 2 = s
0.15 0 20 0. 2
0 4 . 2 = s 5 4 . 2 = s
-130
1 5 . 1
0 40 0.0 4
5 1 . 2 = 0 s 2 .
-110
0 8 0 0 0. 0
-
-140
. 2 0 0 0 2
.4 0 0 4 v = 0
0 30 0. 3 0 40 0. 4
0 6 . 2 = s 6 5 5 2. = s
1.5
7 0 2. = s
-150
2.0 2.
7 5 2. = s
. 6 0 0 6 v = 0
. 8 0 0 8 v = 0 0 1. 0 v = 1
0.10 0.09 0.08 0.07 0.06 0.05
0.50 0.60 0 70 0. 7 0.80 0 90 0. 9 1.0
0 5 . 2 = s 5 5 2 . = s
3 0 0. 0. 3 v = 1
0 7 0 0 7 0 0 0.. 0 0 8 0 08 0 0 0.. 0 0 0 9 0 0 9 0 0 0 . 0 0. 1 0 01 0.. 0 0 0 .01 5
0 0 . 2 = s
-100
0 6 0 . 0
6 0 0 06 0. 0 0 0.
5 9 . 1 = s
1 0 0 0. 1
-
0.20
-80
0 . 0 3 0 0 0 v = 0 4 0 0 0. 0 v = -
2.00 [
0 0 4 0 0. 0
0 9 . 1 = s
-70
5 . 0 1 0 0 0 v = 0 2 0 0 0. 0 v = 1
r]
3 0 . 0 0 0 0
5
3.0 3.
8 0 2. = s
4.0 4. 5.0 6.0
x = 0.10
0.20 s = 1.20
180
200
220
0.30
0.40
0.50
1.40
240
0.60
1.60
260
0.70 1.80
280
0.80
0.90
-140 -120 -100
-80
360
380
-60
-40
-20
0
20
40
60
2.00
300
320 340 Enthalpy [kJ/kg]
400
420
440
460
480
Ref :R.C.Downing. ASHRAE Transactions 1974. Paper No. 2313. 30.00 R113 DTU, Department of Energy Engineering s in [kJ/(kg K)]. v in [m^3/kg]. T in [ºC] M.J. Skovrup & H.J.H Knudsen. 12-05-06
7 6
1 1
3
10.00 9.00 8.00 7.00 6.00 5.00 4.00
0 2 1 0 1 1 0 0 1 0 0 8
v = 0 7
2.00 a B 0
[ 5
e
P
r
e
s
s
u
r 4 0 3
2
0 0 v = 1
0.20
-
0. 060 0 70 0.0 7 0. 080 9 0. 0 0 0.10
70 5 7 . 1 = s
0 7 . 1 = s
60
0 8 . 1 = s
50 40 30
5 6 . 1 = s
0.15 0. 20 5 8 . 1 = s
2 0 . 2
0. 30 0 40 0. 4 0. 50
0 9 . 1 = s
20 0 6 . 1 = s
10
0. 60 0 70 0. 7 0. 80 0. 90
5 9 1 . 1 . = s
1. 0
0
1. 5 0 0 . 2 = s
-10
0 1. 0 v = 1
2. 0
3. 0 4..0 4
-20
-20 x = 0.10
0.20
0.30
0.40
0.50
0.60
s = 1.20
180
0. 050
80
6 0 0. 6 v = 0 .8 0 0 8 v = 0
0 1
0 40 0.0 4
90
3 0 0. 3 = 0 v . 4 0 0 0 4 v = 0
0.10 0.09 0.08 0.07 0.06 0.05
v = 2 0 0 0 . 0 0
. 1 5 0 0 1 v =
0
0.30
0 .0 30
100
1 0 0 0. 1 v =
0
0 20 0.0 2
120
0 . 0 6 0 0 0 v = 0 . 0 8 0 0 0 v =
0
1.00 0.90 0.80 0.70 0.60 0.50 0.40
0. 01 5
110
0 0 . 0 3 v = = 0 0 0 . 0 4 0 0 0 v = 60
6 0 06 0. 0 0 0. 0 7 0 0 7 0 0 0.. 0 0 08 0 08 0 0.. 0 0 0 9 0 0 9 0 0 0.. 0 0 1 0 0.. 0 0
130
0 1 5 0 0. 0
9
3.00 r]
v = 0 .0 0 6 0 0 0 = v 0 8 0 . 0 0 0 0 v = 0 . 0 1 0 0 0 v = 1
0 0. 0 0 5
170 160 150 140
0 0 0 2 0 0 0 . 0 3 v = 0 . 0 0 0 4 0 0 0 0 v = 0 0. 0
4 0
200 190 180
1 5
0
2
0
1 0
20.00
0 1
9 8
0
0
0 1
.0 0 4 0 0 0
0
200
220
240
260
0.70
0.80
0.90
-20
0
20
40
60
80
100
120
140
160
180
200
220
1.40
280
300
320
340 360 Enthalpy [kJ/kg]
380
400
420
440
460
480
500
520
40.00 30.00
Ref :R.C.Downing. ASHRAE Transactions 1974. Paper No. 2313. DTU, Department of Energy Engineering s in [kJ/(kg K)]. v in [m^3/kg]. T in [ºC] M.J. Skovrup & H.J.H Knudsen. 12-05-06 1 1 0 1
2 0 . 0 0 0 0 0 v = 0 3 0
0 9
. 0 0 0 0 v = 0 4 0 . 0 0 0 0 v = 6 0 . 0 0 0 0 0 v = 0 8 . 0 0 0 0 0 v = 0 1 0 0 0. 0 v = 0 8
0 7 0 6 0 5 0 4 3
0 0 v =
0
a
2
2.00 B e r u s P
r
e
s
0
1.00 0.90 0.80 0.70 0.60 0.50 0.40
v = 0 -
0 2 -
v = 3 -
0 4 -
0. 050 0. 060 0 70 0.0 7 0. 080 0. 090 0 .10 0.1
30
10
0 . 0 6 0 0 0
0
5 6 . 1 = s
0 6 . 1 = s
20
0 7 . 1 = s
0.15 0 20 0. 2
5 7 . 1 = s
5 5 . 1 = s
-10
0. 30 0 8 . 1 = s
-20
3 .3 0
v =
5 -
0 40 0. 4 0. 50 0. 60 0 70 0. 7 0. 80
5 8 . 1 = s
-30
0..9 0 10 0 9 . 1 = s
4 0 0 0 . 4
-40
6 0 0. 6 v = 0 8 0 0. 8 v = 0 0
0.10 0.09 0.08 0.07 0.06 0.05
0 0 .0 2
. 1 5 0 0 1
0 0 v =
0.20
0 40 0.0 4
50
2 0 0 0. 2 v =
0
0.30
0 .0 30
60
40
0 . 0 8 0 0 0 v = . 1 0 0 1 0 v = 1
0 20 0.0 2
70
v = 0 . 0 4 0 0 0 v = 1
0. 015
90
0 .0 3 0 0 0
0
[
0 4 0 0 4 0 0 0.. 0 0 5 0 05 0 0 0.. 0 0 6 0 06 0.. 0 0 0 0 0... 0 0 0 0 0 0 7 7 8 0 08 0 0 0. 0 0 9 0 0 9 0 0 0.. 0 0 1 0 01 0.. 0 0
80
5 . 0 1 0 0 0 v =
0
0 0. 0 0 3
140 130 120 110 100
1 0
3.00
1 2
2 0 . 0 0 0 0
4 1 3
0
20.00
10.00 9.00 8.00 7.00 6.00 5.00 4.00
0 0
0
r]
1 5 . 0 0 0
R114
1. 5 2. 0
.0 1 0 v = 1
-50
3. 0 4.0 4.
x = 0.10
0.20
0.30
0.40
0.50
s = 1.00
140
160
180
200
0.60
0.70
1.20
220
240
0.80
0.90
-40
-20
0
20
40
60
80
100
120
140
1.40
260
280
300 320 Enthalpy [kJ/kg]
340
360
380
400
420
440
460
Ref :DuPont SUVA 123 30.00 R123 DTU, Department of Energy Engineering 4
1 0 0
10.00 9.00 8.00 7.00 6.00 5.00 4.00
1 0 9 0 8 0 7 0 0 5
0 0 v =
0
2.00 4
B [ 3
e r e P
r
1.00 0.90 0.80 0.70 0.60 0.50 0.40
0 1
0 0 v = 0
0.30
0 0 v =
0.20 0 2 -
0.10 0.09 0.08 0.07 0.06 0.05 -
0. 050 0. 060 0 70 0.0 7 0. 080 90 9 0 0. 0 0. 10
70 60
0 0 .0 3
50 0 7 . 1 = s
40
5 7 . 1 = s
0 8 . 1 = s
8 5 . 1 = s
0. 15
20
0 .3 0
5 9 . 1 = s
10
0 40 0 . 4 0 .5 0 0 .6 0 0 70 0 . 7 0 .8 0 0 90 0 . 9 1 .0
0 0 . 2 = s
0 3 0 . 3
4 . 4 0
0 20 0. 2
0 9 . 1 = s
30
5 0 2 . 2 . = s
-10
1 .5 0 1 . 2 = s
-20
8 0 0. 8 v = 0 0 . 0 1 1 = v
3
0 40 0.0 4
80
5 0 . 0 1
.6 0 0 6 v = 0
0
0 30 0.0 3
100
1 5 . 1
0 0 v = 1 -
0 2 0 0 2 0.. 0 0
90
. 2 0 0 0 2 v =
0
0 8 0 0 8 0 0 0 . 0 0. 0 9 0 0 9 0 0 0.. 0 0 1 0 01 0.. 0 0 15 01 0.. 0 0
120
0 . 0 8 0 0 0 v = 0 1 1 0 0. v = 2
0 7 0 0 7 0 0 0. 0
110
0 . 0 6 0 0 0 v =
0
0 6 0 0 0 6 0. 0
140 130
. 0 4 0 0 0 0 v =
0
s
1
. 0 0 2 0 0 0 0 v = 3 0 0 0 4 0 . 0 0 0 . 0 0 v = 0 0 0 v = 0 6 0 0 0 . 0 0 v = 8 0 . 0 0 0 0 0 = v 0 0 1 0 0. 0 v =
0 0 v = 0 2 0 0 0. 0 v =
6
3.00
s
1
0 . 0 0 5 0 0
170 160 150
1
2 1 1
u
1
7
3
0 0
a
0 6
1 0
20.00
r]
0 5
0
s in [kJ/(kg K)]. v in [m^3/kg]. T in [ºC] M.J. Skovrup & H.J.H Knudsen. 12-05-06
0
2..0 2
3 .0
. 5 1 5 v = 1
-30
4..0 4 5 .0
x = 0.10
0.20
0.30
s = 1.00
160
180
200
0.40
0.50
0.60
1.20
220
240
0.70
0.80
1.40
260
280
300
0.90
-20
0
20
40
60
80
100
120
140
160
180
200
1.60
320
340 360 Enthalpy [kJ/kg]
380
400
420
440
460
480
500
520
540
50.00 40.00
5 1 0 0 0.
R134a
Ref :D.P.Wilson & R.S.Basu, ASHRAE Transactions 1988, Vol. 94 part 2. DTU, Department of Energy Engineering s in [kJ/(kg K)]. v in [m^3/kg]. T in [ºC] M.J. Skovrup & H.J.H Knudsen. 12-04-23
0
8
0 6
4
10.00 9.00 8.00 7.00
0 3
0
6.00 5.00 P
r
e
s
0 0 v = 0 1
0
15 01 0.. 0 0 0 2 0 0 2 0.. 0 0
50 0 3 0 0 3 0. 0 0.
40 0 4 0 0 4 0.. 0 0
30
. 0 1 5 0
20
5 7 . 1 = s s
0 8 1 . 1 . = s
5 8 . 1 = = s
5 9 . 1 = = s
0 9 . 1 = s
10
0 0 3 0. 0 0 v =
3.00
0 7 . 1 = s s
60
0 0 2 0. 0 0 v =
4.00
0 9 0 0 9 0 0 0 . 0 0.. 01 0 0
70
2
a
s
80
0 2 0 . 0 0 = v 0 3 0 0 . 0 v = 4 0 . 0 0 0 0 0 v =
6 0 0 0 0 0. 0 v = 8 0 0 0 0 0 0. v = 0 0 1 0 0 0. v = 0
u
8 0 0 8 0 0 0.. 0 0
90 0
5
r
0 0 6 0 0. 0 0. 0 0 7 0
9
0
e
0 0. 0 0 5
100 0
20.00
B[
4 0 0. 0 0
0
70
]
3 0 . 0 0 0 0
1
30.00
r
0 2 0 0 0.
5 0 05 0. 0 0.
1 -
2.00
0
0 2 -
8 0 08 0. 0 0. 0 9 0 0 9 0.. 0 0 0..1 0 0
0 1 . 2 = s
-10
0 . 0 6 0 0 0 v =
0 7 0 0 7 0.. 0 0
5 0 . 2 = s
0 . 0 4 0 0 0 v = 0
0.. 0 0 06 6 0
0 0 . 2 = s
0..15 0 5 1 . 2 = s
0 . 0 8 0 0 0 v = . 1 0 0 0 1 v =
-20
0 3
1.00 0.90 0.80 0.70 0.60
-
0 0 v =
1 5 . 1
0 2 2 . 2 . = s
0. 3 0 0.
5 2 . 2 = s
-30 v =
0 2 0 0.. 2 0
2 0 0 0. 2
0. 4 0 0. 0.5 0 0.
0 4 -
0.6 0 0.
-40
0.50
x = 0.10
0.20
0.30
s = 1.00
140
160
180
200
0.40
0.50
0.60
1.20
220
240
0.70
0.80
1.40
260
280
0.90
-40
-20
0
20
400
420
40
60
440
460
80
100
120
140
160
1.60
300
320
340 360 380 Enthalpy [kJ/kg]
480
500
520
540
560
Ref :ASHRAE Thermodynamic properties of Refrigerants 1986 30.00 R152a DTU, Department of Energy Engineering 0
9 8
s in [kJ/(kg K)]. v in [m^3/kg]. T in [ºC] M.J. Skovrup & H.J.H Knudsen. 12-05-06
9 0 1 0 . 0 0 0 0 .0 0 0 0
7 0 6 0
0 0 3 0 . 0 0 4 = 0 v 0 0. 0 = 6 v 0
10.00 9.00 8.00 7.00 3
0
]r
6.00
0 0 v = 0
[
B 1
e s P
r
e
s
0 0 v = 1 -
2.00
0.. 0 7 0 0 0.. 0 8 0 0 0.. 0 9 0 0 0 2 2 . 2 . = s
20
0 3 2 . 2 . = s
0
0 5 . 2 = s
4 . 2 = s
0 0 6 . 0
0..15 0
0 6 . 2 = s
10
2 0 0.. 2 0
0
0 0 8 0 0. 0 v = 1 0 0. 1 0 v = 0
6 0 06 0.. 0 0
0..1 0 0
3 0 0 . 0
0
3.00
5 0 05 0 . 0
30
0 0 4 0. 0 0 v =
4.00 u
r
0 1 . 2 = s
40
2
5.00 a
50
5 . 1 0 0 = v 0 2 0 0 . v = 0
0 4 0 0 4 0. 0 0.
60
0
0 = v
0 4
0 3 0 0. 0 3
70
8 0 0 0 0. . 0 = = 0 1 v 0 v .
5
2 0 0 2 0. 0
80 0
20.00
0 1 5 0. 0
90
0 7 . 2 = s
-10
0 8 . 2 = s
0 2 -
1 5 v = = 0. 0.
-20
. 2 0 0 0 2 v = 0
1.00 0.90 0.80 0.70 3 -
4 0 0.. 4 0 0..5 0 0 0 9 . 2 = s
-30
. 3 0 0 0 3 v =
0..6 0 0 7 0 0.. 7 0 8 0 0.. 8 0 9 0 0.. 9 0 0 1 . 0
. 4 0 0 0 4 v = 0 4
0.60
3 0 0.. 3 0
-
-40
0.50
x = 0.10
0.20
s = 1.00
125
150
175
200
0.30 1.20
225
250
0.40
0.50
1.40
275
300
0.60 1.60
325
0.70
0.80
1.80
350
375
0.90
-40
-20
0
20
40
60
550
575
80
100
120
140
160
180
200
700
725
750
2.00
400
425 450 475 Enthalpy [kJ/kg]
500
525
600
625
650
675
775
70.00 60.00
0 3 0 0 . 0
R170 Ref :W.C.Reynolds: Thermodynamic properties in SI DTU, Department of Energy Engineering s in [kJ/(kg K)]. v in [m^3/kg]. T in [ºC] M.J. Skovrup & H.J.H Knudsen. 12-05-06 2 1
10 0 0 0 6 0 8 0 . 0 0 0. = = 0 v v 1 -
20.00 2 0
v =
3 -
u e
5.00 P
r
s
s
r
e
[
4 -
5 0 1 0. 0 0
5 -
6 -
0 0 v = 7 -
0 8 . 2 = s
-40
0. 0 7 0 0. 8 0 08 0.. 0 0 0 9 0 0 9 0.. 0 0 0..1 0 0 0 0 3 . = s
8 -
v =
0..15 0 0 2 0 0.. 2 0
0 2 . 3 = s
-50
0 0 6 . 0
0
2.00
-60
9 -
0 0 v =
0. 4 0 0. 0 6 . 3 = s
. 1 5 0 1 0
0
0.. 3 0 0
0 4 . 3 = s
-70
0 2 . 2 0 v = 0.
0..5 0 0 0..6 0 0
3 0 . 3
0 0 . 4 = s
-90
0
0.. 7 0 0 0..8 0 0 0.. 9 0 0 1. 0
0 8 . 3 = s
-80
. 4 0 0 0 4 v =
1. 5
6 0 0. 6 v = 0 0 1 -
2.. 0 2
-100 x = 0.10
0.20
s = 0 .00 0 .20
-100
0 6 . 2 = s
-30
0 0 8 0. 0 0 v = 1 0 0. 1 0 v =
0
3.00
0.50
6 0 06 0. 0 0.
0
4.00
1.00 0.90 0.80 0.70 0.60
0 4 0 0 4 0.. 0 0
5 0 05 0. 0 0.
-20
3 0 . 0 0 0 0 v = 0 0 4 0 0 0. v = 0
0 3 0 0 3 0.. 0 0
0 4 . 2 = s
-10
2 0 0 0. 0 0 v =
0
0 2 0 0 2 0.. 0 0
0
1 0 0. = v
0
15 01 0.. 0 0
0 2 . 2 = s
0 0
B
20 0
30.00
a
30 0
6 0 7 0 .0 0 0 8 0 . 0 0 0 0 . 0 0 0 0 9 0 . 0 1 0 0 0 0 0 0 . 0
0 0 . 2 = = s
3
40.00
r]
5 0 0 0 0.
0
50.00
10.00 9.00 8.00 7.00 6.00
0 0 4 0 0.
-50
0
0.40
0.30 0.60
50
0.40 0.80
100
0.50
1.00
1.20
150
0.60 1.40
200
0.70
1.60
250
1.80
0.80 2.00
300
0.90
2.20
-100 -80
-60
-40
-20
0
20
40
60
80
100
120
140
160
850
900
2.40
350 400 450 Enthalpy [kJ/kg]
500
550
600
650
700
750
800
70.00 60.00
0 3 0 0 . 0
R1150 Ref :W.C.Reynolds: Thermodynamic properties in SI DTU, Department of Energy Engineering s in [kJ/(kg K)]. v in [m^3/kg]. T in [ºC] M.J. Skovrup & H.J.H Knudsen. 12-05-06
50.00
0 0 4 0 0.
0 6 . 1 = s 0
0 7 . 1 = s
1
-
20.00 0 4
0 0 v = 0 5 -
u e
5.00
B
P
r
s
s
r
e
[
0 0 v = 0 -6
0 0 2 . 0
7 -
v = 0
-70
-80
0 . 0 8 0 0 0 v =
3.00 0
-90 . 1 5 0 0 1 v =
2.00 0 -10
1.00 0.90 0.80 0.70 0.60 0.50
0 0 v =
0..15 0 0.. 2 0 0
0.. 3 0 0 0. 4 0 0. 0..5 0 0
-100
0 6 . 3 = s 7 0 3. = s
4 0 0. 4 v = 0 1 -
-110
. 6 0 0 6 v = 0
x = 0.10
0.20
-100
-50
0.20
0.30 0.40
0
0.40 0.60
50
0.80
0.50 1.00
100
0.60 1.20
150
1.40
0.70 1.60
200
2.00
1. 5 2.. 0 2
0.80
1.80
0. 7 0 0. 0.. 8 0 0 0.. 9 0 0 1. 0
3. = s
3 0 0 0. 3 v = 1
0..6 0 0
0 3 3. = 0 s = 4 . 3 = s 0 5
2 .2 0
0
s = --0 0.20 0 .00
-150
0.. 0 7 0 0 0.. 0 8 0 0 0.. 0 9 0 0 0..1 0 0
0 0 . 3 = s 0 1 . 3 = 0 s 2 . 3 = s
1 0 1 0 0. v = 9 -
06 0 0.. 06 0
0 6 2 . 2 . = s 0 7 . 2 = 0 s 8 . 2 = s 0 9 . 2 = s
-60
0 0 4 0 0 0 .
05 0 0.. 0 0
0 5 . 2 = s
-50
0 . 0 6 0 0 0 v = 8 -
0 4 0 0.. 0 0
2 = s
-40
0 0 3 0. 0 0 v =
0
4.00
5 0 1 . 0
0 3 0 0 3 0.. 0 0
0 3 . 2 = 0 4 s .
-30
0 0 0. 0 v =
-
a
-20
0 6 8 0 . 0 0 0 . 0 0 0 0 0 = v v = 1 0 0 3
r]
0 0 . 2 = 0 1 s . 2 = s 0 2 . 2 = s
-
30.00
0 2 0 0. 0 2 0.
0 9 . 1 = s
-10 2
15 01 0.. 0 0
0 8 . 1 = s
0
10.00 9.00 8.00 7.00 6.00
6 0 7 0 8 0 0 0 0 . 0 0. 0 . 0 0 0 0 9 0 0 0 0 0 0 . 0 1 0 0 . 0
0 0
40.00
5 0 0 0 0.
0.90 2.20
250 300 Enthalpy [kJ/kg]
-100 -80
-60
-40
-20
0
20
40
60
80
100
2.40
350
400
450
500
550
600
650
700
0 3 0 0 . 0
R1270
70.00 60.00
Ref :W.C.Reynolds: Thermodynamic properties in SI DTU, Department of Energy Engineering s in [kJ/(kg K)]. v in [m^3/kg]. T in [ºC] M.J. Skovrup & H.J.H Knudsen. 12-05-06
0 0 4 . 0 0 0 2 . 2 = s s
0
50.00
9 0
90
8
40.00
80 0 7
6 5
0 0 6 0 0 8 0. 0 . 0 = 0 v
0 4 3
2
u e
5.00 P
r
s
s
r
e
[
B
a
0 1 0
0 0 v =
0 0
0 3 -
2.00 0 4 -
v =
8 0 0. 0 0
0 0 9 0 0. 0
1 0 01 0. 0 15 01 0.. 0 0
0 3 . 2 = s
0 2 0 0 2 0.. 0 0
0 3 0 0 3 0. 0 0. 0 4 0 0 4 0.. 0 0 0 4 . 2 = s
5 0 05 0.. 0 0
06 0 0.. 06 0
0 5 . 2 = s
0 6 2 . = s
10
3 0 0 .0
0 7 . 2 = s
0 8 2 . 2 . = s
0 9 2 . 2 . = s
0 7 0 0.. 0 7 0 08 0 0.. 08 0 0 9 0 0.. 0 9 0 0..1 0 0
0 0 3 . = s
0 1 . 3 = s
0
0 .15
0 2 . 3 = s
-10
0 20 0. 2
0 3 . 3 = s
-20
-30
5 -
v =
3 0 0 0. 3
0 40 0. 4
0 5 . 3 = s
-50
6 0 0. 6 v = 0
0.50
x = 0.10 s = 0.60
50
100
0.20 0.80
150
0.30 1.00
200
0.40 1.20
0.50 1.40
250
0.60 1.60
300
1.80
350
0.70
0.80
2.00
400
0.90
2.20
450
0.60 0 70 0. 7
0 7 . 3 = s
. 4 0 0 0 4 v =
-60
0.50
6 . 0 3 = s
-40
2 0 . 2
0 30 0. 3
0 4 . 3 = s
. 1 5 0 0 1
0 0 v = 0
1.00 0.90 0.80 0.70 0.60
20
0 0 6 0. 0 0 v = 0 0 8 0 0 0 . v = 1 0 1 0 0 . v = 2 -
3.00
30
0 .0 4 0 0 0 v = 1
4.00
40
5 . 0 1 0 0 0 v = 0 2 0 0. 0 v = = 0
r]
50
1 0 v = . 0 0 0 0 v =
0
10.00 9.00 8.00 7.00 6.00
0 0 0 7 0 . 0
60 0
20.00
0 .0 0 6 0 0
70 0
30.00
5 0 0 0 0. 0
0.80 0 90 0. 9 1.0
0 8 . 3 = s
1.5
-60 -60 -40
-20
0
20
40
60
80
100
120
140
160
180
200
2.40
500 550 Enthalpy [kJ/kg]
600
650
700
750
800
850
900
950
1000
R21
20.00
Ref :R.C.Downing. ASHRAE Transactions 1974. Paper No. 2313. DTU, Department of Energy Engineering s in [kJ/(kg K)]. v in [m^3/kg]. T in [ºC] M.J. Skovrup & H.J.H Knudsen. 12-05-06
0 1
1
1
3
0 0 9 0 8 0 7
0 6 0
v = 5
0 4
3.00
0 0 v =
0
0 0 v = 3
2
a B
1
P
r
e
s
s
u
r
e
1.00 0.90 0.80 0.70 0.60 0.50 0.40
v = 0
80
5 . 0 1 0 0 0 v = 0 2 0 0 0. 0
0 -
0 0 v =
0 2
0 4 0 0 4 0.. 0 0 5 0 05 0.. 0 0
06 0 0. 06 0. 0 7 0 0.. 0 7 0 08 0 0.. 08 0 0 9 0 . 0. 0 9 0 0..1 0 0
0 9 . 1 = s
60 50
0 3 0 . 0
5 9 . 1 = s
40
0 0 .0 4
0 0 . 2 = s
30 20
0..15 0 5 0 . 2 s s =
10
1 0 0 0. 1
2 0 0.. 2 0 0
0 1 . 2 = s
3 0 0.. 3 0 0
5 1 . 2 = s
0..5 0 0
0 3 . 2 = s
-20
4 0 0 0. 4
-3
0 v = 0
6 0 . 6 v =
0 1. 0 v = 1
0 4 -
0.10 0.09 0.08 0.07 0.06 0.05
0 3.. 0 3
5 4 . 2 = s
-40
. 5 1 5 v = 1
2.. 0 2 0
0 4 . 2 = s
-30
. 8 0 0 0 8
1.5
5 3 . 2 = = s
0
0.20
0..6 0 0 7 0 0.. 7 0 0 0..8 0 0 9 0 0.. 9 0 0 0 1. 0
5 2 . 2 = s
-10
3 0 0 0. 3
v =
4 0 0.. 4 0 0
0 2 . 2 = s
0
2 0 . 2
v = -
0.30
5 8 . 1 = s
70
. 1 5 0 0 1 v = 1
0 3 0 0 3 0.. 0 0
100 90
0 0 . 0 6 0 v = 0. 0 . 0 8 0 0 0 v =
0
[
0 2 0 0 2 0.. 0 0
110
0
2.00 r]
15 01 0 . 0 0.
130 120
0 2 0 . 0 v = 0 = 3 0 0 . 0 4 0 0 0 0 = 0 v 0 0 .0 0 6 0 8 0 .0 0 v = 0 . 0 0 0 0 0 0 0 . 0 1 v = = 0 0 0 v = v 0 1
10.00 9.00 8.00 7.00 6.00 5.00 4.00
0
. 0 1 0 0 0
0 2 1
0 4.. 0 4 0 5. 0
0 2. 0 v = 2
x = 0.10
0.20
0.30
s = 1.00
140
160
180
200
0.40
1.20
220
240
0.50
0.60
1.40
260
280
0.70 1.60
300
320
0 6. 0 0 7. 0 7. 0 8. 0
0.80
0.90
-40 -20 0
20
40
60
80 100 120 140 160
180
200
220
240
1.80
340
360 380 400 Enthalpy [kJ/kg]
420
440
460
480
500
520
540
560
580
600
620
80.00 70.00 60.00
5 1 0 0 0 .
R22
Ref :R.C.Downing. ASHRAE Transactions 1974. Paper No. 2313. DTU, Department of Energy Engineering s in [kJ/(kg K)]. v in [m^3/kg]. T in [ºC] M.J. Skovrup & H.J.H Knudsen. 12-04-23
0 2 . 0 0 0 0 6 . 1 = s
0 9
50.00 8
40.00
0 5
20.00 0 4 0 3
0 0 v =
2
a
r
]
P
r
e
s
s
u
0 8 . 1 = s
40
6 0 0 0 . 0
0 2 0 0 2 0. 0 0.
30
0 3 0 0 3 0.. 0 0
5 8 . 1 = s
20
1
8.00 7.00 6.00 r
e
B[
15 01 0.. 0 0
50
0 0 1 0. 0 0 v =
0
0 8 0 0 8 0. 0 0 9 0 0 9 0 0 0.. 0 0 1 0 01 0 . 0
5 7 . 1 = s
60
8 0 0 0 0. 0 0 v =
0
10.00 9.00
70
0 2 0 . 0 0 v = 3 0 0 0 0. 0 0 v = 4 0 . 0 0 0 0 0 v = 6
0. 0 0 6 0 0 7 0 0 7 0 0 0.. 0 0
0
7 0
0 0 v = 0
0 0 v =
5.00 0 1 -
4.00 2 -
0 0 v =
3 -
0.. 0 7 0 0 0.. 0 8 0 0
4 -
0. 0 9 0 0. 0..1 0 0
5 0 . 2 = s
-10
0 1 . 2 = s
-20
0 . 0 8 0 0 = 0 v . 1 0 0 0 1 v = 0
0..15 0
5 1 . 2 = s
-30
0.. 2 0 0 0 2 . 2
s = s
0.50
x = 0.10
0.30
s = 1.00
140
160
180
200
0.40
0.50
1.20
220
240
0.60
0.70
1.40
260
280
0.80 1.60
300
320
0..5 0 0 0..6 0 0
-50
. 3 0 0 3 v = 0
0.20
0.. 4 0 0
0 3 . 2 = s
.2 0 0 2 v = 0
-50
0.. 3 0 0
5 2 . 2 = s
-40
.1 5 0 0 1 v =
1.00 0.90 0.80 0.70 0.60
0.. 0 0 06 6 0
0 0 . 2 = s
0
0 0 .0 4
5 0 05 0.. 0 0
5 9 . 1 = s
0 . 0 6 0 0 0 v = 0
2.00
0 0 2 . 0
0.. 0 4 0 0
0 9 . 1 = s
10
0 3 0 0 0 0 . v =
0
3.00
5 0 1 . 0
5 0 0 5 0. 0 0
7 . 1 = s
80 0
30.00
0 0 4 0 0. 0
5 6 . 1 = s
90 0
3 0 . 0 0 0 0
0.. 7 0 0 0.. 8 0 0 0.. 9 0 0
0.90
-40
-20
0
20
40
60
80
100
120
140
160
180
200
1.80
340 360 380 Enthalpy [kJ/kg]
400
420
440
460
480
500
520
540
560
60.00 50.00
5 1 0 0 . 0
R23 Ref :R.C.Downing. ASHRAE Transactions 1974. Paper No. 2313. DTU, Department of Energy Engineering s in [kJ/(kg K)]. v in [m^3/kg]. T in [ºC] M.J. Skovrup & H.J.H Knudsen. 12-05-06
0 2 0 0 0.
3 0 0 0 0. 0
0 2
0 . 0 0 5 0 0
0 0 6 0 0. 0
0 0 7 0 0. 0 0 0 8 0 0. 0 0 0. 0 0 9
0
1 0 0 0 1 0. 0
5 . 1 = s
20
40.00
4 0 . 0 0 0 0
0 1
10
30.00
0 0 2 0 . 0 = v 0 3 0 0 0. = 0 v 0 4 0 0. = v 0
0 1 -
20.00 0 2 -
-
s P
6.00
r
e
s
u
r
e
[
B
a
10.00 9.00 8.00 7.00 0 4
0 7 . 1 = s
-20
8 0 0 0 0 0 0. v = 0 . 0 1 0 0 0 v = 3
]r
0.. 0 2 0 0
-10
6 0 0 0 0 0. 0 v =
0
0. 0 1 5
0 6 . 1 = s
0
0 3 0 0. 0 3 0 8 1 . = s
-30
0 4 0 0.. 0 0 5 0 0. 0 5
-
0 0 v = -
5.00 0 -
v =
3.00
-50
0 0 v = 7 -
2.00
0 0 .0 6 0 0 . 0 8
0 0 v =
1 5 0. 1 v = 0 -
80
100
0.30
0.80
120
140
0.40
0.50
1.00
160
180
0.60
0.70
1.20
200
220
1.40
240
0. 2 0
1 0 . 1
8
0.20
0.1 5
0 1 . 2 = s
-70
0
x = 0.10
0 0 . 2 = s
-60
0 0 v =
s = 0.60
0 8 0 0.. 0 8 0 0 9 0 0.. 0 9 0 0..1 0 0
0 4 0 0 0. 0
0
7 0 0 7 0. 0
0 9 . 1 = s
0 0 3 0 0 0. v = 6
1.00
0. 0 6 0
-40
0 0 2 0. 0 0 v = 0 5
4.00
5 0 1 . 0
0.80
0 2 . 2 = s
-80 0.90
-80
0.. 4 0 0
-60
-40
-20
0
20
40
60
80
100
1.60
260 280 Enthalpy [kJ/kg]
300
320
0. 3 0
340
360
380
400
420
440
460
50.00 40.00
0 0 4 0 0.
R290 Ref :W.C.Reynolds: Thermodynamic Properties in SI DTU, Department of Energy Engineering s in [kJ/(kg K)]. v in [m^3/kg]. T in [ºC] M.J. Skovrup & H.J.H Knudsen. 12-05-06
5 0 6 0 7 0 0 8 0 0 0 0 . 0 0 0 0. . 0 0 0 0 0 0 . 0 0 0 9 0 . 0 1 0 0. 0
9
90 0 8
80 0 7
30.00 6 5 0 4 0
r
e
[
B
a
]r
2
1
P
r
30
0 4 . 2 = s
0 7 0 0. 0 7 0. 08 0 0.. 08 0 0 9 0 0. 0 9 0. 0..1 0 0
20
0 0 3 . = 0 v
0
1
0 5 . 2 = s
10
0 0 4 . = 0 v
0
e
s
5 0 05 0.. 0 0
06 0 0. 06 0.
0
5.00 u s
0 4 0 0 4 0.. 0 0
40
1 5 0 0 . v = 2 0 0 . = 0 v
0
0 3 0 0 3 0.. 0 0
50
0 = v
3
0 2 0 0 2 0.. 0 0
60
0 6 0 . 0 8 0 0 0 = v 0 0 . 0 = v 0 1 . 0
20.00
0 3 . 2 = = s
70 0
10.00 9.00 8.00 7.00 6.00
15 01 0.. 0 0
0
0 6 . 2 = s
0 7 . 2 = s
0 8 . 2 = s
0 9 . 2 = s
0 0 . 3 = s
0
0 0 v = 0
3.00 2 -
0 0 . 0 6
0 0 v =
-10
3
2.00 0
-30
.2 0 0 0 2 v = 4 -
1.00 0.90 0.80 0.70 0.60
1 .1 5
5 -
4 0 . 4
0.60 70 0. 70
0 7 . 3 = s
-40
0 0 v =
0.50
0 6 . 3 = s
. 3 0 0 0 3 v = 0
40 0. 40
0 5 . 3 = s
-
0 0 v =
30 0. 30
0 4 . 3 = s
-20
1 0 . 1
0 2 0 0.. 2 0
0 3 . 3 = s
0 0 . 0 8
0 0 v =
0
0..1 5 0
0 2 . 3 = s
-
4.00
0 1 . 3 = s
0.80 90 0. 90 1.0
-50 1.5
0.50
x = 0.10
0.20
s = 0.80
50
100
150
0.30 1.00
200
0.40 1.20
0.50 1.40
250
0.60 1.60
300
0.70 1.80
350
0.80 2.00
400
0.90 2.20
450
-40
-20
0
20
40
60
80
100
120
140
160
180
200
900
950
1000
2.40
500 550 Enthalpy [kJ/kg]
600
650
700
750
800
850
0 4 0 0 . 0
R50 Ref :W.C.Reynolds: Thermodynamic properties in SI
70.00 60.00
0 5 0 0 0 .
6 0 7 0 8 0 0 9 0 0 0 0 0 0 0 0 0 0. 0 1 . 0. 0. 0 0 0. 0
DTU, Department of Energy Engineering s in [kJ/(kg K)]. v in [m^3/kg]. T in [ºC] M.J. Skovrup & H.J.H Knudsen. 12-05-06
5 7 . 3
0 0 4 . 4 . = s
s = s
50.00 0 9 -
40.00
-90 0 0 1
-100 0 1
0 8 0 0 1 0 . 0. 0 = = 0 v v 1 -
20.00 2 1 -
u e
5.00 P
r
s
s
r
e
[
B
a
r
]
10.00 9.00 8.00 7.00 6.00
0 -1
0 0 v = 0
4 0 0 4 0. 0 0 5 . 4 = s
0 5 0 0. 0 5 5 7 . 4 = s
0 0 . 5 = s
-120
1
-130
0 0 4 . 0
5 1 -
-150
1 -
0 4 0 0. 4 0 5 0 0.. 5 0 0 6 0 0.. 6 0
5 0 6. = s
.2 0 0 2 = 0 v 0 6
0.. 3 0 0
5 2 . 6 = s
1 5 0 0 . 1 v =
2.00
0 2 0 0. 2
0 0 . 6 = s
-140
0 0 8 0. 0 0 v = 1 0 0. 1 0 v = 0
3.00
5 2 5 . = s
5 7 5 . = s
0 .0 6 0 0 0 v =
4.00
0 7 0 0 7 0.. 0 0 0 8 0 0 8 0.. 0 0 0 9 0 0. 0 9 0.1 0
0 5 5 . . = 5 s
4 -
0 6 0 0. 0 6
0..1 5 0
0 0. 0 0 . 0 3 v = 3
0
-110
5 0 1 0. 0 0 v = 0 2 0 0. 0 0 v =
0
0. 0 2 0
3 0 0 3 . 0 5 2 . 4 = s
-
30.00
. 0 1 5 0 0
5 7 . = = 6 s
3 0 0 0. 3 v =
1. 0
0 0 7. = s
-160
. 4 0 0 0 4 v =
1.00 0.90 0.80 0.70 0.60
0 7 0 0.. 7 0 0 8 0 0.. 8 0 0. 9 0
1. 5
5 2 . 7 s =
2.. 0 2
0 5 . 7 s =
.6 0 0 6 v = 0
3. 0
0.50
x = 0.10
0.20
s = 1.00
100
150
200
0.30
0.40
2.00
250
300
0.50
0.60
3.00
350
400
0.70 4.00
450
500
0.80
0.90
-160
-140
-120
-100
-80
800
850
-60
-40
-20
0
20
1000
1050
5.00
550 600 650 Enthalpy [kJ/kg]
700
750
900
950
1100
0 3 0 0 0.
Ref :W.C.Reynolds: Thermodynamic Properties in SI 50.00 R600 DTU, Department of Energy Engineering
40.00
4 0 . 0 0 0
0 5
s in [kJ/(kg K)]. v in [m^3/kg]. T in [ºC] M.J. Skovrup & H.J.H Knudsen. 12-05-06 4
150 1
0 3 0 1 0 1 0 1 0 9 0 8
r
e
[
B
a
r
]
10.00 9.00 8.00 7.00 6.00
7 0 6 0 5
0 0 v =
0
P
r
e
s
4.00 0 3
0 0 v =
3.00 2
2.00
5 0 05 0.. 0 0
80
0. 0 7 0 0.
60
0 0 . 0 3
0 7 . 2 = s
0 6 . 2 = s
50 40
0 6 0 . 0
30
0 0 v = .1 0 0 1 0 v =
0
6 0 06 0. 0 0.
70
0 0 . 0 8
0
0 4 0 0 4 0.. 0 0
90
0 . 0 4 0 0 0 v = 4
0 3 0 0 3 0. 0 0.
100
5 . 0 1 0 0 0 v = 0 . 0 2 0 0 = 0 v 0
5.00 s
u
110
6 0 0 0 0 0. 0 0 8 v = 0 . 0 0 0 0 v = 0 1 . 0 0 0 0 v = 0
0 2 0 0 2 0.. 0 0
120 1
0 0. 0 0 8 0 0. 0 0 9 0. 0 1 0 15 01 0.. 0 0
130 2
20.00
7 0 0. 0 0
140
1
30.00
0 0 0 6 0. 0
0 5 . 2 = s s
1 0
0 .0 0 5 0 0
0. 0 0. 08 8 0 0 9 0 0 9 0.. 0 0 0..1 0 0 0 8 . 2 = s
0 5 . 2 = s
0..1 5 0
0 9 . 2 = s
0 2 0 0.. 2 0
0 0 . 3 = s
20
1
30 0. 30 0
= 0. 0 1 . 1 5 v = 0 0 v = 0
1.00 0.90 0.80 0.70 0.60
2 0 . 2
-
4 0 0 . 4 v = 0
x = 0.10 s = 1.00
120
160
200
0.20
0.30
1.20
240
0.40 1.40
280
0.50 1.60
320
360
0.60 1.80
400
0.70
0.80 2.00
440
0. 40 40 0.50 0 2 . 3 = s
0
. 3 0 0 0 3 v = 0 1
0.50
. 3 . 3 1 = s
10
0.60 0 70 0. 7 0.80 0 90 0. 9 1.0
-10
0.90
0
20
40
60
80
100
120
140
2.20
480 520 Enthalpy [kJ/kg]
560
600
640
680
720
760
800
840
880
4 0 . 0 0 0
Ref :W.C.Reynolds: Thermodynamic Properties in SI 50.00 R600a DTU, Department of Energy Engineering
40.00
2 1 1 1 0 1 0 9
20.00 0 8 0 7 0 6
10.00 9.00 8.00 7.00 6.00
5 0
r
e
[
B
0 3
v = 0 2
3.00 s
s
u
0
0 0 v = 1
e r P
130 120
01 15 0 . 0 0.
110
0 2 0 0 2 0.. 0 0
0 .0 0 6 0 0 0 0 0 8 v = 0 0 0 .0 = v 1 0 .0 0 0 0 v =
0 3 0 0 3 0. 0 0.
90 80
0 4 0 0 4 0 . 0 0.
70
0. 05 0 0. 06 0 0 70 0.0 7 0. 080 0 90 0.0 9 0. 10
60 50
4
5.00 4.00 a
0 0. 0 0 8 0 9 0 0 0.. 0 0 0. 01 0
100
.0 1 5 0 0 0 v = 0 2 .0 0 0 0 v =
0
7 0 0. 0 0
1 0
0 0
r
0 . 0 0 6 0 0
3
s in [kJ/(kg K)]. v in [m^3/kg]. T in [ºC] M.J. Skovrup & H.J.H Knudsen. 12-05-06
30.00
]
0 0 0 5 0. 0
0
2.00
0 0 v = 0 1 1 0 0 . v = 0
0 1 -
v =
1.00 0.90 0
0.80 0.70 0.60 0.50
30
0 6 0 . 0
0 40 0. 4
0 0 . 3 = s
-20
. 4 0 0 0 4
0 30 0. 3
0 9 . 2 = s
0 -10
v =
0 20 0. 2
0 8 . 2 = s
10
0 8 0 . 0
0. 15
2 0 0 0. 2
3 -
0 7 . 2 = s
0 6 . 2 = s
0 5 . 2 = s
0 4 . 2 = s
20
0. 0 3 . 3 0 v = 0
0.40
40
. 1 5 0 0 1
v = 2 -
0 .0 3 0 0 = 0 v .0 4 0 0 0 0
0. 50 0. 60 0 1 . 3 = s s
0 70 0. 7 0. 9 80 0 0. 90 1 .0
0 2 . 3 = s
-30
. 6 0 0 6 v = 0 0 4 -
1 .5
8 0 0. 8 v = 0 . 0 1 0 v = 1
0.30
2..0 2
-40
3 .0
0.20
x = 0.10 s = 0.80
50
100
150
0.20
0.30
1.00
200
0.40 1.20
250
0.50 1.40
0.60 1.60
300
0.70 1.80
350
0.80 2.00
400
0.90
-40
-20
0
20
40
60
80
100
120
140
2.20
450 500 Enthalpy [kJ/kg]
550
600
650
700
750
800
850
4 0 0 . 4
Ref :W.C.Reynolds: Thermodynamic properties in SI 5.000 R718 0 DTU, Department of Energy Engineering 4 1 s in [kJ/(kg K)]. v in [m^3/kg]. T in [ºC] 4.000 M.J. Skovrup & H.J.H Knudsen. 12-05-06
3.000
0 4 0 . 0 6 0 =
140
8 0 1 0 v 0. 0 0 . 0 0 . 8 . 0 v = = 0 = v v 0 2 1
2 0 2 0 0. v =
2.000
4 0 0. 4 v = 0
0
v = 0 1
0.300 B
0.200 [
a
r
80 . 0 2 0 v = 2 0
0 4. 0 v = 4
P
r
0.100 0.090 0.080 0.070 0.060 0.050 0.040 0
. 0 8 0 v = 8 4
2
8 0 v = 8
0.20 s = 0.60
-200
0
200
0.30 1.20
1.80
400
0.40 2.40
600
3.00
800
0.50 3.60
1000
0.60
4.20
1200
6 0
4.80
8 0 1 0 0
0 5 . 0 1 = s
0 v = 1 0
0.70 5.40
6.00
1400 1600 Enthalpy [kJ/kg]
2 0 0
0 2 . 0 1 = s
0 x = 0.10
4 0
0 9 . 9 = s
4 0 v = 4
6 0 v = 6
0.010 0.009 0.008 0.007 0.006 0.005
2 0
0 6 . 9 = = s
20
0.020
1 0
0 3 . 9 = s
2 0 v = 2 0
0 8. 0
0 0 . 9 = s
40
1 0 v = 1
0.030
0 6. 0
0 7 . 8 = s
. 0 6 0 v = 6 e
0 4. 0
60
r s
0 2. 0
0 4 . 8 s s =
6
s
0 8 . 7 = s
0 1 . 8 = s
8
u
1.. 0 1 0
0 5 . 7 = s
100
0
e
8 0 0. 8
0 2 . 7 = s
. 6 0 0 0 6
. 8 0 0 8 v = 0 0 1. 0 v = 1
1.000 0.900 0.800 0.700 0.600 0.500 0.400 ]
120
6 0 0. 6
0.80 6.60
1800
7.20
2000
0.90 7.80
0
100
200
300
8.40
2200
2400
2600
2800
3000
3200
4 0 0
70.00 60.00
0 2 0 0 . 0
R728 Ref :W.C.Reynolds: Thermodynamic Properties in SI DTU, Department of Energy Engineering s in [kJ/(kg K)]. v in [m^3/kg]. T in [ºC] M.J. Skovrup & H.J.H Knudsen. 12-05-06
3 0 0 0 0. 0 5 . 1 = s
50.00
4 0 0 0 0. 0
0 6 1 1 . . = s
0
40.00 5
7 0 . 1 = s
1 -
0 8 . 0 1 9 . = 1 s 0 = 0 . s 2 = s
0 6 1 -
20.00
7 1
0 . 0 0 0 = v 0 1 0. 0 v = =
-
u
10.00 9.00 8.00 7.00 6.00 e
5.00 P
r
s
s
r
e
[
B
a
r
]
8 1 -
0 0 v =
4.00
0 2 . 2 0 = 3 s . 2 = s
0 1
-180
0 0 . 0 3
.0 6 0 0 0 0 v =
2.00
0 4 0 0. 0 0 5 0 0. 0 0 6 0 0. 0 0 7 0 0. 0
2 0 0. 2
3 0 0. 3
0 2 3. = s
-190
0 0 v =
1 5 0. 1
0 0 . 3 = s 0 1 3 . = s
8 0 = 0. 0 0 . 0 v = . 1 0 0 1 0 v =
1.00 0.90 0.80 0.70 0.60
0. 0 8 0. 0 8 0 0 0 9 0 0. 0 1 0 0. 1
0 6 2. = s 0 7 . 2 = s 0 8 2. = s 0 9 2 . = s
9 -
4 0 0. 4
. 0 0 3 3 = s 0 4 3 . = s
0 2
. 3 0 0 3 v = 0
x = 0.10
0.20
s = 0.00 0.20
50
75
100
0.30
0.40
0.60
125
0.40 0.80
150
0.50 1.00
1.20
175
0.60 1.40
0.70 1.60
200
0.80
1.80
225
2.00
6 0 0. 6 7 0 0. 7 8 0 0. 8 9 0 0. 9 0 1. 0
0 6 . 3 s =
0 7 . 3 s =
-
0.50
5 0 0. 5
0 5 . 3 s =
1 .1 5 . 2 0 0 2 v = 0
0
-200
0.90 2.20
-200
-180
-160
-140
-120
-100
-80
-60
-40
2.40
250 275 Enthalpy [kJ/kg]
300
325
0. 0 1 0
0. 0 3 0
0 5 2. = s
0 0 0 4 0 0. v =
3.00
0 0 9 0 0. 0
0. 0 2 0
-170
2 0 0 . 0
0 0 v =
8 0 0 . 0 0
0. 0 1 5
5 . 0 1 0 0 0 v = 0
7 0 0. 0 0
0 4 . 2 = s
-160
0 0 4 0 . 0 0 = 0 6 v 0 0 . = v 0 8 0
6 0 . 0 0 0 0
0 1 . 2 = s
-150
30.00
5 0 . 0 0 0 0
350
375
400
425
450
0 2 0 0 . 0
R729
70.00 60.00
0 3 0 0 0.
Ref :W.C.Reynolds: Thermodynamic Properties in SI DTU, Department of Energy Engineering s in [kJ/(kg K)]. v in [m^3/kg]. T in [ºC] M.J. Skovrup & H.J.H Knudsen. 12-05-06
0 6 . 1 = s
50.00
0 7 1 . 1 . = s
40.00
4 0 0 0 0.
0 8 . 1 = s
0 9 . 1 = s
-145
30.00
0 0 . 2 = s
5 0 . 0 0 0
0 2 . 2 = s
0 4 . 2 = s
P
r
e
s
s
u
r
e
10.00 9.00 8.00 7.00 6.00
0 4 0 0. 0 0 5 0 0. 0
0 6 . 2 = s
0 6 0 0. 0 0 7 0 0. 0 0 8 0 0. 0
0 7 . 2 = s
-17 0
0 9 0 0. 0 1 0 0. 1
0 8 . 2 = s
- 175
0 9 . 2 = s
5.00 4.00
0 3 0 0. 0
0 5 . 2 = s
- 165
[
B
a
9 0 0. 0 0 0 1 0 . 0
0 2 0 0. 0 0 3 . 2 = s
-1 6 0
r
8 0 0. 0 0
0. 0 1 5
- 155
]
0 0 0 7 0. 0
0 1 . 2 = s
-150 -1 50
20.00
0 0 0 6 0. 0
1 5 0. 1
0 0 . 3 = s
- 180
0 1 . 3 = s 0 2 . 3 = s
3.00 -1 8 5
2 0 0. 2
0 3 . 3 = s
2.00
3 0 0. 3
0 4 . 3 = s
4 0 0. 4
0 5 . 3 = s
-1 9 0
5 0 0. 5 6 0 0. 6
1.00
75
100
x = 0.10
0.20
0.40
0.60
125
0.30 0.80
150
0.40 1.00
175
1.20
0.50 1.40
200
0.60 1.60
225
0.70 1.80
0.80 2.00
2.20
250 275 Enthalpy [kJ/kg]
0.90
-180
-160
-140
-120
-100
-80
-60
2.40
300
325
350
375
400
425
450
5 1 0 0 . 0
R732
70.00 60.00
Ref :W.C.Reynolds: Thermodynamic Properties in SI DTU, Department of Energy Engineering s in [kJ/(kg K)]. v in [m^3/kg]. T in [ºC] M.J. Skovrup & H.J.H Knudsen. 12-05-06
0 2 0 0 0 .
3 0 0 0 0.
0
0 1 . 2 = = s
2 1 -
50.00
0 4 . 0 0 0
-120 0 3
40.00 1 -
0 2 . 2 = s
-130
30.00 1 -
20.00
0 0 0 3 0 4 0 . 0 0 0. = v = v
0 5 1 -
u
10.00 9.00 8.00 7.00 6.00 e
5.00
]
P
r
s
s
r
e
[
B
a
r
06 1
0 7 1
4.00
0 0 v = -
3.00
0 6 . 2 = s
0
0 7 . 2 = s
v = = 0 0 -1
0 5 0 0. 0 0 6 0 0. 0 0 7 0 0. 0 0 8 0 0. 0 0 9 0 0.. 0 0 1 0 0. 1
0 . 0 3 = s
0 1 . 3 = s 0 2 . 3 = s 0 3 . 3 = s
-170
1 5 0. 1 2 0 0. 2
4 0 3. = s
0 0 8 . 0 0 0 v =
3 0 0. 3
5 0 3. = s
1 .1 0
0 0 v =
1.00 0.90 0.80 0.70 0.60
0 4 0 0. 0
0 8 . 2 = s
0 9 . 2 = s
3 0 0 . 0
8
4 0 0. 4
0 6 . = 3 s =
0.. 5 0 5 0
0 7 . 3 s =
-180
6 0 0. 6
1 .1 5
0 9 . 3 s =
0 0 4 . 4 s =
.3 0 0 3 v = 0
x = 0.10
0.20
s = 0.60 0.80
100
150
0.30 1.00
1.20
200
0.40 1.40
0.50 1.60
0.60 1.80
250
2.00
0.70 2.20
7 0 0. 7 8 0 0. 8 9 0 0. 9 0 1. 0
8 0 3. = s
.2 0 0 0 2 v =
0.50
0. 0 1 0
0 3 0 0. 0
0 6 0 0 0. 0 v =
2.00
0 0 9 0 0. 0
0 2 0 0. 0
-160
0 0 4 0. 0 0 v =
8 0 0. 0 0
0 4 . 2 = s
-150
5 . 0 1 0 0 0 v = 2 0 0 0 0 0. v = -
0 0 0 7 0. 0
0 3 . 2 = s
-140
0 6 0 . 0 0 v = 8 0 0 0 . = 0 0 v 1 0 0 . v =
0 0 0 6 0. 0
0 1 5 0.. 0
0 5 . 2 = s
0 4
5 0 0 0 0 . 0
0.80 2.40
0.90 2.60
-180
-160
-140
-120
-100
-80
-60
-40
-20
0
20
2.80
300 350 Enthalpy [kJ/kg]
400
450
500
550
5 1 0 0 . 0
R740
70.00 60.00
0 2 0 0 . 0
Ref :W.C.Reynolds: Thermodynamic Properties in SI DTU, Department of Energy Engineering s in [kJ/(kg K)]. v in [m^3/kg]. T in [ºC] M.J. Skovrup & H.J.H Knudsen. 12-05-06
3 0 0 0 0. 0 7 . 1 = s s
50.00 0 3 -
0 4
2 0 0 0 . 0 = 0 v 3 0 0 . 0 = v 0 4 1 -
20.00 5 1 -
] r
P
r
e
s
s
u
r
e
[
B
0 0 . 2 = s
6 1 -
0 0 v = 0 7
5.00
5 0 0 0. 0 5 0.
-160
0 0 2 . 0
3.00 v = 0 8 -
x = 0.10 s = 0.80
140
160
180
0.20
0.30
1.00
0.40
1.20
200
0.50 1.40
220
0.60 1.60
240
0 v = 0
260
2.00
0. 3 0 9 0 2 . = s
1 0 . 1
0.80
0. 2 0
0 8 2. = s
-180
0.70 1.80
0. 1 5
7 0 2 . = s s
. 0 8 0 0 0 0 v =
1.00
0 0. 0 7 0 0. 0 8 0 0. 0 9 0. 1 0
6 0 2. = s
0 . 0 4 0 0 0
0 6 0 0 0. 0 v = 1
0 0. 0 6
0 5 . 2 = s
0 0 3 0. 0 0 v =
2.00
0 0. 0 4
0 4 . 2 = s
-170
4.00
0 0. 0 2
2 0 2. = s
0 3 . 2 = s
-150
5 0 1 . 0
0 0 v = 1 -
0 0 8 0 0. 0 9 0 0. 0 0
0 0. 0 3
0 8 0 0 0. = v 0 0 . 0 1 0 0 v = 0
10.00 9.00 8.00 7.00 6.00
0 . 0 0 7 0 0
5 0. 0 1 0 1 . 2 = s
-140
0 0 6 0 0 . v = =
a
0 9 . 1 = s
0 . 0 0 = v
0
0 0 0 6 0. 0
0 0. 0 1
-130
30.00
0 0 0 5 0 . 0
0 1 8 . = s
1
40.00
4 0 . 0 0 0
0. 4 0 0 0 . 3 s =
0.90
-180
-160
-140
-120
-100
-80
-60
-40
-20
0. 5 0
0
2.20
280 300 Enthalpy [kJ/kg]
320
340
360
380
400
420
5 1 0 0 . 0
R744
0 2 0 0 . 0
0 3 0 0 . 0
Ref :W.C.Reynolds: Thermodynamic Properties in SI DTU, Department of Energy Engineering s in [kJ/(kg K)]. v in [m^3/kg]. T in [ºC] M.J. Skovrup & H.J.H Knudsen. 12-05-06 5 .4 1 = s
100.00
5 .5 1 = s
0 . 5 1 = s
90.00 80.00
5 .6 1 = s
5 7 . 1 = s
30
0 8 . 1 = s
5 2
25
9 0 . 0 0 0 5 8 . 1 = s
0 2
]
20 5
r
0 . 1 0 0
0 9 . 1 = s
1
a B [
15
50.00 u
r
e
6 0 . 0 0 0
8 0 . 0 0 0
0 .7 1 = s
3
60.00
5 0 . 0 0 0
. 0 7 0 0 0 0 .6 1 = s
0
70.00
4 0 0 0 0.
5 9 . 1 = s
0 0 . 2 = s
0
5 0 . 2 = s
0 1 . 2 = s
0 1 5 0. 0
1
s s
0 3 0 0 . 0 = v
e r P 5
40.00
0 0 4 0 . 0 = v
0
5 0 0 6 0 . 0 = v
5 -
30.00
5 1 . 2 = s
10
0
0 8 0 0 0. 0 . = v
0
0 2 . 2 = s
1 -
0 2 0 0. 0 5 2 . 2
s = s
-5 0 1 0 0. = v
0 3 . 2 = s
-10
5 1
5 3 . 2 = s
-
0 0 v =
20.00
x = 0.10
0.20
s = 1.00
140
160
180
200
0.30
0.40
0.50
1.20
220
240
0.60
1.40
260
280
300
0.70
0.80
1.60
320
340 360 380 Enthalpy [kJ/kg]
5 0 . 0 1
-15
0.90
-10
0
10 20 30 40 50 60 70 80 90 100 11 1 10
1.80
400
420
440
460
480
500
520
540
560
580
3 0 0 . 0
5 0 0 1 0. 0
Ref :R.C.Downing. ASHRAE Transactio ons ns 1974. Paper No. 2313. 40.00 RC318 DTU, Department of Energy Engineering s in [kJ/(kg K)]. v in [m^3/kg]. T in [ºC] M.J. Skovrup & H.J.H Knudsen. 12-05-06 0 1 00 1 9
90 8
7
0 6
10.00 9.00 8.00 7.00 6.00 5.00
0 5 0
0 0 v =
[
0 2
3.00 e u
r s s
0 1
P
r
e
2.00
0 1 -
1.00 0.90 0.80 0.70 0.60 0.50
0 0 v =
-
1 5 1 0 0. v = . 2 0 0 2 0 v = 0 3
0.40 -
0.30
0. 030 0 40 0 .0 4
20 10
0
0 0 . 0 6
0 20 .0 2 0.0
30
5 . 0 1 0 0 0 v = 0 2 0 0. 0 0 v =
5 .5 1 = s
-10
8 0 0. 0 0 v = 0. 1 0 1 0 0. v = 20
.
0 3 0 0 0. 0 v = 0 4 . 0 0 0 0 v = 0
0. 0 1 5
60
40
v = 0 0 1 0
3
B
70
50
8 . 0 0 0 0 0
0
80
2 0 0 0 . 0
6 0 0 0 0. 0 0 v = 0
4
4.00 a
r
0 0 v = 3 0 0 0 . 0 0 0 v = 0 4 . 0 0 0 0 0 v =
6 0 06 0 0 0. 0 0. 0 7 0 0 7 0 0 0.. 0 0 0 .00 80 90 9 0. 00 0 0. 010
100
0 0
5 0 05 0 0 0.. 0 0
110
0
20.00
0 6 . 1 = s
5 6 . 1 = s
0 7 . 1 = s
5 7 . 1 = s
5 8 . 1 = s
0 8 . 1 = s
0 9 . 1 = s
5 9 . 1 = s
0 .0 50 0 0 . 2 = s
0 .0 60 0 70 0 .0 7 0 .0 80 0 .0 90 0 .1 0
5 0 . 2 = s
0 .1 5 0 1 . 2 = s
0 40 0 . 4
-30
0. 50 0. 60 0. 70 0. 80
x=0 0.. 1 10 00 ..2 2 0 0 ..3 3 0 0 ..4 4 0 0 ..5 5 0 0 .6 .6 0 0 ..7 7 0 0 ..8 8 0 0 ..9 90 s = 1.00
100
120
140
160
180
200
-20
0
20
40
60
80
100
120
1.20
220
240
0 .2 0
0 .3 0
-20
. 3 0 0 0 3 v =
0.20
0 3 0 0. 0 0 3 0 4 0 0 4 0 0 0 . 0
1
30.00
]
0 0 2 0 0. 0
260
280
300 320 340 Enthalpy [kJ/kg]
360
380
400
420
440
460
480
500
520
540
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