50,00 40,00
3 0 0 0 0,
R600
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. 05-09-18
4 0 , 0 0 0 0
150
90 80
10,00 9,00 8,00 ] 7,00 r a B 6,00
[ e r u s s e r P
70 v =
60
110
6 0 , 0 0 0 0 0 v = 0 0 ,0 0 8 v = 0 0 0 , 0 1 0 v =
100
0 0 0 2 0 0 0, 0, 0
120
110
3 0 0 0 3 0 0, 0, 0
100 0 0 0 4 0 0 0, 0, 0 4
90
0 ,0 1 5 0 0 v = 0 0 , 0 2 0 0
0 0 05 0 0 0, 0, 05
80
0 0 0 6 0 0 0, 0, 0 6 0 0 0 7 0 0 0, 0, 0 7 0 0 08 0 0 0, 0, 08 0 0 0 9 0 0 0, 0, 0 9 0 0 0, 0,1 0 0 0
70 60
50 v =
5,00 40
4,00
v =
0 ,0 3 0 0 0
0 ,0 4 0 0 0
3,00
40 30
8 0 0 0, 00 v = 0 1 0 0 0, 1 v =
20
2,00
0 7 , 2 = s
0 6 , 2 = s
50
0 ,0 6 0 0 0 v =
30
0 8 , 2 = s
0 5 , 2 = s
1,00 0,90 0,80 0,70 0,60
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 0 4 0 0 0 0, 0, 4 0 0 0 0, 0,5 0 0 0 0 2 , 3 = s
0
0 3 0 0 , 3 v = 0
x = 0,10
0 0 3 0 0 0 0, 0, 3 0 0 1 , 3 = s
10
4 0 0 0 , 4 v = 0
0 0 2 0 0 0 0, 0, 2 0
0 0 , 3 = s
20
0 0 , 1 5 0 1 v = 0 2 0 0 0, 2 v =
-10
0,50
0 0 0, 0,15 0 0
0 9 , 2 = s
10
0
0 0 8 0 0, 0 , 0 0 9 0 0 0 0 1 0 0 0, 0 01 5 0 0, 0
130
120
20,00
0 , 0 0 7 0 0
140
130
30,00
0 , 0 0 6 0 0
0 5 , 2 = s
150 140
5 0 , 0 0 0 0
-10
0,90
0
20
40
60
80
100
120
0 0 0, 0,6 0 0 0 0 0 7 0 0 0 0, 0, 7 0 0 0 0, 0,8 0 0 0 0 0 9 0 0 0 0, 0, 9 0 0 0 0 0 0 0 1, 0 0
140
2,20
480
520
Enthalpy [kJ/kg]
560
600
640
680
720
760
800
840
880
200,00
5 1 0 0 0 ,
R744
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. 05-09-18 0 4 , 1 = s
5 3, 1 = s
100,00 90,00 80,00
0 5 , 1 = s
5 5 , 1 = s
5 6 , 1 = s
0 7 , 1 = s
5 7 , 1 = s
30
60,00
10
5
40,00
3 0 0 0 0, v = 4 0 , 0 0 0 v =
-5 -10
30,00
-20
20,00
0 -5 -10
6 0 , 0 0 0 v = 8 0 , 0 0 0 0 v = 0 0 , 0 1 0 0 v =
-15
-25 -30
-15 -20 -25
1 5 0 0, 00 v =
-35
10,00 9,00 8,00
-30
0 0 , 0 2 0 0 v =
-40
-35
-50
7,00 6,00
x = 0,10
0,20 s = 0,80
80
100
120
140
0,30 1,00
160
180
0,40
0,50
1,20
200
220
240
0,60 1,40
260
280
0,70
0,80
1,60
300
320
0,90
1,80
340
360
Enthalpy [kJ/kg]
,0 2 0 0 0 0
,0 3 0 0 0 0
,0 4 0 0 0 0 ,0 5 0 0 0 0
4 2 , = s 0 5 2 , = 5 s 5 2 , = 0 6 s 2 , = s
-45
0 0 , 0 4 0 v = 0
-50
, 0 1 5 0 0 0
-40
0 0 3 0 , 0 v = 0
-45
5 0 , 2 = s 0 1 , 2 = s 5 1 , 2 = s 0 2 , 2 = s 5 2 , 2 = s 0 3 , 2 = s 5 3 , 2 = s 0 4 2 , = s 5
5
0
,0 0 7 0 0 0 ,0 0 8 0 0 0 ,0 0 9 0 0 0 0 0 0 0 ,0 1
5 8 , 1 0 = 9 , s 1 5 = 9 , s 1 = 0 0 s ,
15
10
50,00
0 8 , 1 = s
20
15
,0 0 4 0 0 0
,0 0 6 0 0 0
2 = s
25
20
0 , 0 0 3 0 0
0 , 0 0 5 0 0 0 6 , 1 = s
30 25
70,00
] r a B [ e r u s s e r P
5 4 , 1 = s
2 0 , 0 0 0
,0 6 0 0 0 0 ,0 7 0 0 0 0 , 0 8 0 0 0 0 , 0 9 0 0 0 0 0 1 0, 1 0 0
-50 -40 -30-20 -10 0 10 20 30 40 50 60 70 80 90100 90100110 110120 120130 130
2,00
380
400
420
440
460
480
500
520
540
560
580
600
0 3 0 0 , 0
R170
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. 05-09-18
10 6 0 8 0 0 , 0 0 0 0 0, = v v = 0 0 , 1 0 0 v = 5 0 , 1 0 0 v = 0 0 0 , 2 0 0 = v
-10 -20 -30
10,00 ] 9,00 r a 8,00 B [ 7,00 e r 6,00 u
-40
5,00
-60
-70
3,00
2,00
0 0 05 0 0 0, 0, 05
0 6 , 2 = s
-30
0 8 , 2 = s
-40
0 0 0 6 0 0 0, 0, 0 6 0 0 0 7 0 0 0, 0, 0 7 0 0 0 8 0 0 0, 0, 0 8 0 0 0 9 0 0 0, 0, 0 9 0 0 0, 0,1 0 0 0 0 0 3 , = s
-50
0 0 0, 0,15 0 0 0 0 2 0 0 0 0, 0, 2 0
0 2 3 , = s
0 0 3 0 0 0 0, 0, 3 0
-60 0 4 3 , = s
0 0 4 0 0 0 0, 0, 4 0
-70
0 0 0,5 0 0 0
0 6 3 , = s
-80
0 3 0 0 0, 3 v = 0 4 0 0 , 4 v = 0
-90
0 0 0 4 0 0 0, 0, 0 4
-20
0 0 ,1 5 0 1 v = 0 2 0 0 0, 2 v =
-80
0 3 0 0 0, 0, 0
0 4 , 2 = s
-10
0 0 ,0 6 0 0 = v 0 0 , 0 8 0 0 v = 0 ,1 0 0 0 1 v =
4,00
0 2 0 0 0, 0, 0 2
0
0 0 , 3 0 0 0 v = 0 0 ,0 4 0 0 v =
-50
01 5 0 0, 0, 01
0 2 , 2 = s
0
20,00
0 0 6 0 0 0 0, 0, 6 0 0 0 7 0 0 0 0, 0, 7 0 0 0 8 0 0 0 0, 0, 8 0 0 0 9 0 0 0 0, 0, 9 0 0 0 0 0 0 0 1, 0 0
0 8 3 , = s
0 0 4, = s
-90
0 0 1,5 0 0 0
6 ,6 0 0 0 v = 0
-100
0 0 0 0 0 0 2, 2, 0 0
-100 x = 0,10
0,20
s = 0,00 0, 0 ,20
-100
20
10
30,00
0,50
6 0 0 7 0 0 8 0 0 0 9 0 ,0 0 0 0 0 0 , 00 , 0, 0 0 0 0 , 0 1 0 0 0
0 0 , 2 = s
30
20
40,00
1,00 0,90 0,80 0,70 0,60
5 0 , 0 0 0
30
50,00
s s e r P
0 0 4 0 0 ,
-50
0
0,30
0,40
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
350
-100 -80
-60
-40
-20
0
20
40
60
80
100
120
140
160
850
900
2,40
400
450
Enthalpy [kJ/kg]
500
550
600
650
700
750
800
0 3 0 0 , 0
R1150
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. 05-09-18
50,00
0 0 4 0 0,
5 0 , 0 0 0 0 6 , 1 = s
0
0 6 0 0 0 ,0 0 7 0, 0 , 0 0 0 0 8 0, 0 0 0 9 0 0 0 0 0 0 ,0 1 0 0
0 7 , 1 = s
0
40,00
-10 -10 -20
30,00
20,00 -40
s s e r P
-60
-70
5,00
3,00 -90
0,50
0 0 0 5 0 0 0, 0, 0 5 0 0 0 6 0 0 0, 0, 0 0 0 0 7 0 0 0, 0, 0 0 8 0 0 0, 0, 0 0 9 0 0 0, 0 9 0,1 0 0 0
-80
-90
-100
4 0 0 0 , 4 v = 0
-110
-110
6 ,6 0 0 0 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
250
2 0 0 0 0, 0, 2 0
3 0 0 0 0, 0, 3 4 0 0 0 0, 0, 4 0 5 0 0 0 0, 0, 5 0 6 0 0 0 0, 0, 6 0 7 0 0 0 0, 0, 7 0 8 0 0 0 0, 0, 8 0 9 0 0 0 0, 9 0 0 0 0 0 1, 0 0
5 0 0 0 1, 5 0 0 0 0 0 2, 2, 0 0
0,80
1,80
0,1 5 0 0
3 3, = 0 s 4 3 , = s 0 5 3 , = 0 s 6 3, = s 7 0 3, = s
0 3 , 3 0 0 v = 0
s = -0,20 0 ,00
-150
-70
0 , 2 0 0 0 2 v =
-100
0 0 0 4 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 1 3 , = 0 s 2 3, = s 0
-60
0 ,1 5 0 0 1 v =
2,00
1,00 0,90 0,80 0,70 0,60
-50
0 ,0 6 0 0 0 v = 0 0 8 0 0, 0 v = 0 1 0 0 0, 1 v =
-80
4,00
0 3 0 0 0, 0, 0 3
2 , 2 = 0 s 3 , 2 = 0 4 s 2 , = s 0 5 2 , = s
-40
0 0 , 0 3 0 0 v = 0 0 , 0 4 0 0 v =
0 2 0 0 0, 0, 0
0 9 , 1 = 0 0 s , 2 = 0 s 1 , 2 = s 0
-30
0 ,0 1 5 0 0 v = 0 0 , 0 2 0 0 v =
-50
10,00 ] 9,00 r a 8,00 B [ 7,00 e r 6,00 u
-20
6 0 8 0 0 , 0 0 0 0 0 ,0 0 = v 0 v = 0 , 0 1 0 v =
-30
0 8 , 1 = s
01 5 0 0, 0
0,90 2,20
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
0,100 0,090
2 0
R718
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] 0 , M.J. Skovrup & H.J.H Knudsen. 05-09-18 1
40
0,080
= v
0,070
0 , 2 = v
0,060 0,050
0 , 4 = v
30
0 , 6 = v
0 8 , v =
0 , 8 0 1 = s
0 , 1 0 v =
30
0,040
0,030
6 0
0 , 1 1 1 = s
0 4 , 1 1 = s
0 , 2 0 v =
] r a B [ e r u s s 0,020 e r P
4 0
40
20
8 0
0 0 , 2 1 = s
20
, 0 0 4 v = 10
0 3 , 2 1 = s
0 ,0 6 0 v =
0 6 , 2 1 = s
0 ,0 1 0 0 v =
0,009 0,008 0,007
0 9 , 2 1 = s
0 , 0 0 0 0 v = 2
0,006 0,005
x = 0,10 s = 2,40
0
200
400
600
0,20 3,00
800
0,30 3,60
4,20
1000
0,40 4,80
1200
5,40
1400
0,50 6,00
1600
0,60 6,60
7,20
1800
0,70 7,80
2000
Enthalpy [kJ/kg]
0 2 0
10
0 ,0 8 0 v =
0,010
0 1 0
0 7 , 1 1 = s
8,40
2200
0,80 9,00
2400
0,90
9,60
10,20
2600
0
0
0 4 0
50 100 150 200 250 300 350
10,80
2800
3000
3200
3400
3600
3800
5,000 4,000
R718
, 4 0 0 4
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. 05-09-18
140
3,000
120
0 0 4 0 , 6 0 , 8 0 0 v = 0 0 0 , 1 0 v = 0 0 ,
v = v =
2,000
0 , 2 0 0 2 v =
4 , 4 0 0 v = 0
120
6 , 6 0 0 v = 0
100
8 , 8 0 0 v = 0 0 , 0 0 0 v = 1
1,000 0,900 0,800 0,700 0,600 0,500 0,400
100
80 0 0 0 , 0 v = 2
0,300
60
0 , 0 0 0 v = 8 , 0 0 0 0 0 v = 1
40
0,030
s = 2,40
0
200
400
600
0,20 3,00
800
0,30 3,60
4,20
1000
0,40 4,80
1200
5,40
1400
0,50 6,00
1600
0,60 6,60
,0 0 8 0 , 0 0 0 1 0
, 0 0 2 0 0
7,20
1800
2000
Enthalpy [kJ/kg]
8,40
2200
, 0 0 8 0 0 ,0 0 1 0 0 0
,0 0 2 0 0 0
0 6 2 , 1 = s
0,70 7,80
, 0 0 6 0 0
0 3 2 , 1 = s
0 9 2 , 1 = s
0 x = 0,10
,0 0 6 0
0 0 2 , 1 = s
,0 0 0 0 0 v = 6 0 ,0 0 0 v = 8 0 ,0 0 0 0 0 v = 1 0
0
,0 0 4 0
0 4 , 1 1 = 0 s 7 , 1 1 = s
0 , 0 0 0 v = 4 0
0,010 0,009 0,008 0,007 0,006 0,005
0 2 , 0 1 = s
, 0 0 4 0 0
20
0,020
,0 0 2 0
40
,0 0 0 0 0 v = 2
20
0 9 , 9 = s
0 1 , 1 1 = s
0 , 0 0 0 v = 6
0,090 0,080 0,070 0,060 0,050 0,040
0 6 , 9 = s
0 8 0 , 1 = s
60 0 , 0 0 0 v = 4
,8 0 0 8 ,0 0 1 0
0 5 , 0 1 = s
80
] r a B0,200 [ e r u s s e r P0,100
, 6 0 0 6
0 140 3 , 9 = s
0,80 9,00
2400
0,90
9,60
10,20
2600
0
100
200
300
3000
3200
3400
3600
,0 0 4 0 0 0
10,80
2800
3800
50,00 40,00
4 0 ,0 0 0 0
R600a
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. 05-09-18
130
90
20,00 80 70 60
10,00 9,00 8,00 7,00 6,00 5,00
40
20
0
-10
1,00 0,90 0,80 0,70 0,60 0,50
0,30
0 0 05 0 0 0, 0, 05 0 0 06 0 0 0, 0, 06 0 0 0 7 0 0 0, 0, 0 7 0 0 08 0 0 0, 0, 08 0 0 0 9 0 0 0, 0, 0 9 0 0 0 1 0, 0, 0 0
50 40 30
0 7 , 2 = s
0 6 , 2 = s
0 5 , 2 = s
0 4 , 2 = s
20
0 0 0, 0,15 0 0 0 0 2 0 0 0 0, 0, 2 0
0 8 , 2 = s
10
0 0 3 0 0 0 0, 0, 3 0
0 9 , 2 = s
0
0 0 4 0 0 0 0, 0, 4 0
0 0 , 3 = s
-10
-20
0 0 0, 0,5 0 0 0 0 0 0, 0,6 0 0 0 0 0 7 0 0 0 0, 0, 7 0 0 0 0, 0,8 0 0 0 0 0 0 9 0 0 0, 0, 9 0 0 0 0 0 0 1, 0
0 1 , 3 = s 0 2 , 3 = s
-30
0 6 , 6 0 0 v = 0 8 ,8 0 0 0 v = 0 0 0 , 0 0 0 v = 1
-40
0 0 0 4 0 0 0, 0, 0 4
60
0 , 3 0 0 0 3 v = 0 4 0 0 , 4 v = 0
-30
0,40
80 70
0 1 5 0 0, 1 v = 0 0 , 2 0 0 2 v =
-20
0 0 0 3 0 0 0, 0, 0 3
90
0 ,0 6 0 0 0 v = 0 0 8 0 0, 0 v = 0 0 0 0, 11 v =
10
2,00
6 0 ,0 0 8 0 0 0 v = 0 0 ,0 0 v = 1 0 0 , 0 0 0 v =
3 0 0 0 , 00 v = 0 0 , 0 4 0 0 v =
30
3,00
100
1 5 0 0, 00 v = 0 0 2 0 0, 0 v =
50
0 0 0 2 0 0 0, 0, 0 2
110
100
0 0 8 0 9 0 0, 0 0 0 0, 0 0 01 0 0 0, 0 5 0 01 5 0 0, 0, 01
120
110
4,00
0 , 0 0 6 , 0 0 7 0 0 0 0 0
130 120
30,00
] r a B [ e r u s s e r P
0 , 0 0 5 0 0
0 0 0 1,5 0 0 0 0 0 0 0 0 2, 2, 0
-40
0 0 0 0 0 0 3, 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
Enthalpy [kJ/kg]
500
550
600
650
700
750
800
850
0 4 0 0 , 0
R50
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. 05-09-18
0 5 0 0 0,
0 6 0 0 9 0 0 0 7 0 0 8 0 0 , ,0 0 0 0 ,0 1 0 0, 0 0 0, 0 0 5 7 , 3 = s
50,00
0 0 , 4 = s
-90
40,00
-90
-100 -110
20,00 -120
10,00 ] 9,00 r a 8,00 B [ 7,00 e r 6,00 u
s s e r P
8 0 0 0 1 , 0 0 0 0 0, = v v = 5 0 , 1 0 0 = v 0 0 , 2 0 0 0 v =
-140
5,00
3,00
-150
-160
5 2 5 , = s
0,1 5 0 0
0 5 5 , = s
2 0 0 0 0, 2
3 0 0 0 0, 0, 3
0 0 6, = s
-140
4 0 0 0 0, 4 0
2 5 6 , = s
-150
5 0 0 0 0, 5 6 0 0 0 0, 6 7 , 0 7 0 0 0 8 0 0 0 0, 8 9 0 0 0 0, 9 0 0 0 0 1, 0
0 5 6 , = s
7 5 6, s = 0 0 7, s =
-160
6 0 0 0 , 6 v = 0
2 5 7, s =
5 0 0 0 1, 5 0 5 0 7, s =
0 0 0 0 2, 0
0 0 0 0 3, 0
0,50
x = 0,10
0,20
s = 1,00
100
0 0 0 6 0 0 0, 0 0 7 0 0 0, 0, 0 0 8 0 0 0, 0 0 9 0 0 0, 0 0,1 0 0 0
5 7 5, = s
0 3 0 0 0, 3 v = 0 4 0 0 , 4 v = 0
1,00 0,90 0,80 0,70 0,60
0 0 5 , = s
-130
0 1 5 0 0, 1 v = 0 0 , 2 0 0 2 v =
2,00
0 5 0 0 0, 0 5 5 7 4 , = s
-120
0 0 , 0 6 0 0 v = 0 0 , 0 8 0 0 v = 0 ,1 0 0 0 1 v =
4,00
0 4 0 0 0, 0, 0 0 5 , 4 = s
-110
0 0 0 , 3 0 0 v = 0 0 , 0 4 0 0 v =
-130
0 2 0 0 0, 0 0 0 0 3 0 0 0, 0
5 2 , 4 = s
-100
30,00
0 1 5 0 0, 0
150
200
0,30
0,40
2,00
250
300
0,50
0,60
3,00
350
400
0,70
0,80
4,00
450
500
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
50,00 40,00
Ref :R.Döring. Klima+Kälte ingenieur Ki-Extra 5, 1978 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. 05-09-18
80
50
20,00
80
70
60
30,00
40 30
0
-10
30
-20
5 0 0 0, 5 6 0 0 0, 6 7 0 0 0, 7 8 0 0 0, 8 9 0 0 0, 9 0 0 0 1, 0 0
5 7 , 6 = s
-20
0 0 7 , = s
-30
5 0 0 1, 5
0 5 7 , = s
-40
0,30
x = 0,10
0,20
0,30
s = 1,00
0
100
200
0,40
2,00
300
400
0,50 3,00
500
600
0,60
0,70
4,00
700
800
0,80
0,90
1000
0 0 0 4, 0
0 0 8, = s
-50
5,00
900
0 0 0 3, 0
5 7 7, = s
0 0 0 0 0 v = 2,
-50
0 0 0 2, 0
5 2 7 , = s
5 5 0 0 0 v = 1,
0,50 0,40
4 0 0 0, 4 0
0 5 , 6 = s
-10
0 8 , 8 0 0 v = 0 0 0 , 0 0 0 v = 1
-40
2 0 0 0, 2
0
0 6 , 6 0 0 v = 0
1,00 0,90 0,80 0,70 0,60
1 5 0 0, 1
5 2 6 , = s
0 4 0 0 , 4 v = 0
-30
5 7 5 , = s
3 0 0 0, 3
10
0 3 0 0 , 3 v = 0
2,00
0 6 0 0, 0 0 7 0 0, 0 0 8 0 0, 0 0 9 0 0, 0 1 0 0 0, 1
0 0 6 , = s
20
0 2 0 0 0, 2 v =
3,00
0 5 5 , = s
40
0 , 1 5 0 0 1 v =
4,00
0 5 0 0, 0
5 2 , 5 = s
50
0 , 0 8 0 0 0 v = 0 0 , 1 0 0 1 v =
, 0 4 0 0 0
0 0 , 5 = s
60
0 0 , 0 6 0 0 v =
10
5,00
70
6 0 0 0 0, 0 8 0 = 0 , v 0 1 0 0 , v = 0 0 5 0 0 0 , 1 0 0 v = , 0 2 0 0 v = v = 0 0 , 0 3 0 0 v = 0 0 , 0 4 0 0 v =
20
10,00 9,00 8,00 7,00 6,00
] r a B [ e r u s s e r P
0 3 0 0, 0
R717
-40 -20 0
0 0 0 5, 0 0 0 0 0 6, 0 0 0 0 7, 0
20 40 60 80 1 00 00 1 20 20 1 40 40 1 60 60 1 80 80 20 0 2 20 20
6,00
1100
Enthalpy [kJ/kg]
1200
1300
1400
1500
1600
1700
1800
1900
2000
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. 05-09-18
5 0 6 0 0 7 0 8 0 0 1 0 0 , 0 0 0 ,0 0 0 0 ,0 0 0 0 0 , 0 0 0, 0 0 0 9 0 0 ,0
90
80
80
70
30,00
40 30
[ e r u s s e r P
10 0
-10
4,00 3,00
2,00
30
0 0 06 0 0 0, 0, 06 0 0 0 7 0 0 0, 0, 0 7 0 0 08 0 0 0, 0, 08 0 0 0 9 0 0 0, 0, 0 9 0 0 0, 0,1 0 0 0
0 4 , 2 = s
20 0 5 , 2 = s
10
0 6 , 2 = s
0 7 , 2 = s
0 8 , 2 = s
0 9 , 2 = s
0 0 , 3 = s
0 1 , 3 = s
0 0 0, 0,15 0 0
0 2 , 3 = s
0
0 0 , 0 6 0 0 v = 0 0 ,0 8 0 0 v = 0 0 , 1 0 0 1 v =
-20
0 0 05 0 0 0, 0, 05
40
0 0 , 3 0 0 = v 0 0 , 4 0 0 v =
5,00
0 0 0 4 0 0 0, 0, 0 4
50
5 0 , 1 0 0 v = 0 0 , 2 0 0 v =
20
0 0 0 3 0 0 0, 0, 0 3
60
6 0 , 0 8 0 0 0 0 = 0 v 0, v = 0 1 0 0 0, v =
50
20,00
0 0 0 2 0 0 0, 0, 0
0 3 , 2 = s
70
60
10,00 9,00 8,00 ] 7,00 r a B 6,00
01 5 0 0, 0, 01
90
0 3 , 3 = s
-10
-30
-40
-30
0 0 0, 0,5 0 0 0 0 0 0, 0,6 0 0 0
0 6 , 3 = s
0 0 7 0 0 0 0, 0, 7 0 0 0 0, 0,8 0 0 0 0 0 9 0 0 0 0, 0, 9 0 0 0 0 0 0 0 1, 0 0
0 7 , 3 = s
-40
0 4 , 4 0 0 v = 0
-50
0 0 4 0 0 0 0, 0, 4 0
0 5 , 3 = s
0 3 0 0 0, 3 v =
1,00 0,90 0,80 0,70 0,60
0 0 3 0 0 0 0, 0, 3 0
0 4 , 3 = s
-20
0 0 , 1 5 0 1 v = 0 0 , 2 0 0 2 v =
0 0 2 0 0 0 0, 0, 2 0
-50 0 0 1,5 0 0 0
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 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. 05-09-18
4 0 , 0 0 0
90
80
40,00
80
70
70
60
30,00
6 0 , 0 0 8 0 0 0 0 v = = 0, 0 0 v 0 , 1 0 v = 5 0 , 0 1 0 0 v = 0 0 , 2 0 0 0 v =
40 30 20
10,00 9,00 8,00 7,00 6,00
] r a B [ e r u s s e r P
10
-10
5,00 4,00
40
3,00 -30
2,00
-50
0 0 9 0 0, 0
01 0 0 0, 0 015 0 0, 0, 01 0 0 0 2 0 0 0, 0, 0 2
0 3 , 2 = s
0 0 0 3 0 0 0, 0, 0 3 0 0 0 4 0 0 0, 0, 0 4
0 4 , 2 = s
0 0 05 0 0 0, 0, 05
0 5 , 2 = s
20
0 6 , 2 = s
10
0 7 , 2 = s
0 8 , 2 = s
0 9 , 2 = s
0 0 06 0 0 0, 0, 06 0 0 0 7 0 0 0, 0, 0 7 0 0 08 0 0 0, 0, 08 0 0 0 9 0 0 0, 0, 0 9 0 0 0, 0,1 0 0 0
0 0 , 3 = s
0 1 , 3 = s
0
0 0 0, 0,15 0 0
0 2 3 , = s
-10
0 0 2 0 0 0 0, 0, 2 0
0 3 3 , = s
-20
0 0 4 0 0 0 0, 0, 4 0
0 5 3 , = s
-50
x = 0,10
50
100
0 8 3 , = s
0 6 , 6 0 0 v = 0 -60
-60
s = 0,60
0 0 0, 0,6 0 0 0 0 0 7 0 0 0 0, 0, 7 0
0 7 3 , = s
0 4 0 0 , 4 v = 0
0,50
0 0 0, 0,5 0 0 0
0 6 3 , = s
-40
0 , 3 0 0 0 3 v =
0 0 3 0 0 0 0, 0, 3 0
0 4 3 , = s
-30
5 0 0 0, 11 v = 0 0 , 2 0 0 2 v =
-40
, 0 0 8 0 0 0
30
0 0 , 0 6 0 0 v = 0 0 , 0 8 0 0 v = 0 0 ,1 0 0 1 v =
-20
1,00 0,90 0,80 0,70 0,60
50
0 0 0 , 3 0 0 v = 0 0 , 0 4 0 0 v =
0
0 , 0 0 7 0 0
60
50
20,00
0 , 0 0 6 0 0
0 2 , 2 = s
90
50,00
5 0 , 0 0 0 0
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 0 0, 0,8 0 0 0 0 0 9 0 0 0 0, 0, 9 0 0 0 0 0 0 0 1, 0 0
0 0 1,5 0 0 0
-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
60,00 50,00 40,00
1 5 , 0 0 0
R11
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. 05-09-18
190 180 170 160
30,00
10,00 9,00 8,00 7,00 6,00 5,00 4,00 ] r a B [ e r u s s e r P
80
0 0 0 2 140 0, 0 v = 3 0 130 0 0 0, 0 v = 0 0 4 0 120 0, 0 = v 110 6 0 , 0 0 0 0 100 = v 0 8 0 0 0, 0 v = 0 0 90 1 0 0 , v = 0
60 50
3,00
30
10
-10
0,30
0 0 3 0 0 0,0 0,0 3 0 0 4 0 0 0,0 0,0 4 0 0 05 0 0 0, 0, 05 0 0 6 0 0 0,0 0,06 0 0 0 7 0 0 0, 0, 0 7 0 0 08 0 0 0, 0, 08 0 0 0 9 0 0 0, 0, 0 9 0 0 0 1 0, 0, 0 0
0 7 , 1 = s
5 7 , 1 = s
0 8 , 1 = s
5 8 1 , = s
0 0 0, 0,15 0 0
0 9 1 , = s
30
0 0 0 2 0 0 0, 0, 2 0 0 0 3 0 0 0, 0, 3
5 9 1 , = s
20 10
0 0 0 4 0 0 0, 0, 4 0 0 0 0, 0,5 0 0 0 0 0 0, 0,6 0 0 0 0 0 7 0 0 0, 0, 7 0 0 8 0, 0, 0 0 0 0 0 0 9 0 0 0, 0, 9 0 0 0 0 0 0 1, 0
0 0 2 , = s
0
5 0 2 , = s
-10
0 1 2 , = s
-20
0 0 0 1,5 0 0 0 0 0 0 0 0 2, 2, 0
5 1 2 , = s
-30
0 0 0 0 0 0 3, 3, 0 0 0 0 0 0 0 4, 4, 0
5 5 0 0 0 v = 1,
-40
0 0 0 0 0 0 5, 0 0 0 0 0 0 0 6, 0
-40 x = 0,10
0,20
0,30
s = 1,00
160
0 0 0 2 0 0 0, 0, 0 2
40
6 0 0 0 , 6 v = 0 8 8 0 0 0 v = 0, 0 ,0 0 0 0 v = 1
-30
0,10 0,09 0,08 0,07 0,06 0,05
60 50
0 3 0 0 , 3 v = 0 0 0 4 0 , 4 v = 0
-20
0,20
80 70
0 , 1 5 0 0 1 v = 0 0 0 2 2 , v = 0
0
015 0 0, 0, 01
90
0 0 6 0 0, 0 v = 0 0 8 0 , 0 v = 0 0 0 1 , 1 0 v = 0
20
1,00 0,90 0,80 0,70 0,60 0,50 0,40
05 0 0 05 0, 0, 0 6 0 0 0 6 0 0, 0, 0 0 7 0 0 0 7 0 0, 0, 0 0 8 0 0 0 8 0 0, 0, 0 0 0 9 0 0 0 0 0 , 0, 0 9 0 0 01 0 0 0, 0, 01
110
0 0 3 0 0, 0 v = 0 0 4 0 , 0 v = 0
40
2,00
0 0 4 0 0, 0, 0
100
0 , 0 1 5 0 0 v = 0 , 0 2 0 0 0 v =
70
,0 0 3 0 0 0
170 160 150 140 130 120
150
20,00
0 , 0 0 2 0 0
5 6 , 1 190 = s 180
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
40,00 30,00
1 5 ,0 0 0 0
R114
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. 05-09-18
140
130 120 100
2 0 , 0 0 0 0 v = 0 0 3 0 0 , 0 v = 0 4 0 , 0 0 0 v = 0 0 0 6 0, 0 v = 0 8 0 0 , 0 0 v = 0 0 1 0 , 0 v = 0
10,00 9,00 8,00 7,00 6,00 5,00 4,00
70 60 50 40
3,00 ] r a B [ e r u s s e r P
20 10 0
1,00 0,90 0,80 0,70 0,60 0,50 0,40
-20
0,30
-40
0,10 0,09 0,08 0,07 0,06 0,05
05 0 0 0, 0, 05 06 0 0 0, 0, 06 0 0 0 7 0 0 0, 0, 0 7 0 0 08 0 0 0, 0, 08 0 0 9 0 0 0,0 0,0 9 0 0 0, 0,1 0 0 0
5 6 , 1 = s
0 6 , 1 = s
0 7 , 1 = s
0 0 2 0 0 0 0, 0, 2 0
5 7 , 1 = s
5 5 , 1 = s
-10
0 0 0, 0,15 0 0
0 0 0, 0,3 0 0 0 0 8 , 1 = s
-20
0 0 4 0 0 0 0, 0, 4 0 0 0 0, 0,5 0 0 0 0 0 0 0 0 0,6 0,6 0 0 0 7 0 0 0 0, 0, 7 0 0 0 0, 0,8 0 0 0 0 0 0 , 9 0 9 0, 0 0 0 0 0 0 0 0 0 1, 0 0
5 8 , 1 = s
-30
0 9 , 1 = s
-40
0 0 ,5 0 0 0 1,5 0 0 0 0 0 0 2,0 2,0 0
-50
0 0 0 0 0 0 3, 0 0 0 0 0 0 0 0 4, 4, 0 0
x = 0,10
0,20
0,30
0,40
0,50
s = 1,00
140
0
6 0 0 0 , 6 v = 0 8 ,8 0 0 0 v = 0 0 0 0 0 0 v = 1,
-50
4 0 0 0 4 0 0, 0, 0
50
10
0 3 0 0 , 3 v = 0 0 4 , 4 0 0 v = 0
0,20
3 0 0 0 3 0 0, 0, 0
60
20
0 , 1 5 0 0 1 v = 0 0 0 2 2 , v = 0
-30
0 0 0 2 0 0 0, 0, 0 2
70
30
0 , 0 6 0 0 0 v = 0 , 0 8 0 0 0 v = 0 ,1 0 0 0 1 v =
-10
80
40
0 0 , 0 3 0 0 v = 0 0 , 0 4 0 0 v =
2,00
015 0 0, 0, 01
90
0 0 , 0 1 5 v = 0 0 0 2 0 0, 0 v =
30
0 0 4 0 0, 0, 0 0 5 0 0 0 5 0 0, 0 0 6 0 0 0 6 0 0, 0, 0 0 0 0 7 0 0, 0, 0 0 8 0 0 0 8 0 0, 0, 0 0 9 0 0 0 9 0 0, 0, 0 0 0 0 01 0 0 0, 0, 01
100
90
80
0 0 3 0 0, 0
140 130 120 110
110
20,00
0 , 0 0 2 0 0
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
Enthalpy [kJ/kg]
320
340
360
380
400
420
440
460
1 5 , 0 0 0
R12
70,00 60,00
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. 05-09-18
50,00
110
40
10,00 ] 9,00 r a 8,00 B [ 7,00 e r 6,00 u
s s e r P
30 20
80
2 0 , 0 0 0 = v 3 0 60 , 0 0 0 v = 0 4 0 ,0 0 0 v = 6 0 ,0 0 0 0 v = 8 0 ,0 0 0 0 v = 1 0 0 , 0 0 0 v =
4,00
0
3,00
-20
0 0 0 3 0 0 0, 0, 0 3
40 0 6 , 1 = s
30
0 7 , 1 = s
5 6 , 1 = s
5 7 , 1 = s
20
0 0 0 4 0 0 0, 0, 0 4 0 0 05 0 0 0, 0, 05
0 8 , 1 = s
0 0 0 6 0 0 0, 0, 0 6 0 0 0 7 0 0 0, 0, 0 7 0 0 0 8 0 0 0, 0, 0 8 0 0 0 9 0 0 0, 0, 0 9 0 0 0, 0,1 0 0 0
5 8 , 1 = s
0
0 9 , 1 = s
-10
0 0 0, 0,15 0 0
0 0 2 , = s
-30
0 2 , 2 0 0 v = 0
0 0 2 0 0 0 0, 0, 2 0
5 9 1 , = s
-20
0 0 3 0 0 0 0, 3 0 0 0 4 0 0 0 0, 0, 4 0 0 0 0,5 0 0 0
-40
0 0 6 0 0 0 0, 0, 6 0
0,50
x = 0,10
0,20
0,30
0,40
s = 1,00
140
0 0 0 2 0 0 0, 0, 0
10
0 1 5 0 , 1 v = 0
-40
015 0 0, 0, 01
5 5 , 1 = s
50
0 0 , 0 6 0 0 v = 0 0 , 0 8 0 0 v = 0 ,1 0 0 0 1 v =
-30
1,00 0,90 0,80 0,70 0,60
60
0 0 , 0 3 0 0 v = 0 ,0 4 0 0 0 v =
-10
2,00
70
5 0 ,0 1 0 0 v = 0 0 , 0 2 0 0 v =
10
5,00
0 0 7 0 0, 0 0 8 0 0 0 8 0 0, 0, 0 0 0 0 9 0 0, 0, 0 0 01 0 0 0, 0, 01
90
70
50
0 0 5 0 0, 0 0 6 0 0 0 6 0 0, 0
100
80
20,00
4 0 0 0 4 0 0, 0
110
90
30,00
,0 0 3 0 0 0
0 5 , 1 = s
100
40,00
0 2 0 0 , 00
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
30,00
R123
Ref :DuPont SUVA 123 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. 05-09-18
140
20,00
2 0 , 0 0 0 0 v = 0 3 0 ,0 0 4 0 0 0 110 , 0 v = = 0 0 v 6 0 0 0 0 0, v = 0 8 0 , 0 0 0 v = 0 0 1 0 0 , 0 v = 0 ,0 1 5 0 0 v = 0 0 , 0 2 0 0 v =
90 80 70
4,00
60
3,00 ] r a B [ e r u s s e r P
50
2,00 30
1,00 0,90 0,80 0,70 0,60 0,50
10
0 ,1 5 0 0 1 v = 0 2 , 2 0 0 v = 0 0 3 ,3 0 0 v = 0 0 4 0 0 , 4 v = 0 0 6 , 6 0 0 v = 0 0 8 , 8 0 0 v = 0 0 0 , 0 0 0 v = 1
0
0,40 0,30
-10
0,20 -20
0,10 0,09 0,08 0,07 0,06 0,05
-30
0 0 0 3 0 0 0, 0, 0 3
100 90
0 0 0 4 0 0 0, 0, 0 4
80
0 0 05 0 0 0, 0, 05 0 0 06 0 0 0, 0, 06 0 0 0 7 0 0 0, 0, 0 7 0 0 8 0 0 0,0 0,08 0 0 9 0 9 0 , 0, 0 0 0 0 0 0, 0,1 0 0 0
70 60 50 0 7 , 1 = s
40
5 7 , 1 = s
5 8 , 1 = s
0 8 , 1 = s
0 0 0, 0,15 0 0 0 0 0 2 0 0 0, 0, 2
0 9 , 1 = s
30 20
0 0 0 3 0 0 0, 0, 3 0 0 0 4 0 0 0, 0, 4
5 9 , 1 = s
10
0 0 0 0, 0,5 0 0 0 0 0 0, 0,6 0 0 0 0 0 7 0 0 0, 0, 7 0 0 0 0, 0,8 0 0 0 0 0 9 0 0 0, 0, 9 0 0 0 0 0 0 1, 0
0 0 , 2 = s
0
5 0 , 2 = s
-10
0 0 0 1,5 0 0 0 1 2 , = s
-20
0 0 0 0 0 0 2, 2, 0 0 0 0 0 0 0 3, 3, 0
5 5 0 0 0 v = 1,
-30
0 0 0 0 0 0 4, 4, 0 0 0 0 0 0 0 5, 0
x = 0,10
0,20
0,30
s = 1,00
160
0 0 0 2 0 0 0, 0, 0 2
110
0 , 0 6 0 0 0 v = 0 , 0 8 0 0 0 v = 0 0 , 1 0 0 1 v =
20
015 0 0, 0, 01
120
0 0 3 0 , 0 v = 0 0 ,0 4 0 0 0 v =
40
0 0 7 0 0 0 0, 0, 0 0 8 0 0, 0, 0 0 8 0 9 0 0 0 9 0 0, 0, 0 0 0 01 0 0 0, 0, 01
130
120
100
0 0 6 0 0, 0
140
130
10,00 9,00 8,00 7,00 6,00 5,00
,0 0 5 0 0 0
170 160 150
160 170
150
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. 05-09-18
100
2 0 , 0 0 0
90 80 80 70
20,00
60 50 40
10,00 9,00 8,00 ] 7,00 r a B 6,00
[ e r u s s e r P
30 20
5,00 4,00 0
-10
2,00
0,50
-30
0 7 , 1 = s
015 0 0, 0, 0 0 2 0 0 0, 0, 0
50 0 0 0 3 0 0 0, 0, 0 3
40
0 0 0 4 0 0 0, 0, 0 4
30 20
5 7 , 1 = s
0 8 , 1 = s
5 8 , 1 = s
5 9 , 1 = s
0 9 , 1 = s
10
0 0 05 0 0 0, 0, 05 0 0 0 6 0 0 0, 0, 0 6
0 0 , 2 = s
0 0 0 7 0 0 0, 0, 0 7 0 0 0 8 0 0 0, 0, 0 8 0 0 0 9 0 0 0, 0, 0 9 0 0 0,1 0 0 0
5 0 , 2 = s
0
0 1 , 2 = s
-10
0 0 0, 0,15 0 0
5 1 , 2 = s
0 0 2 0 0 0 0, 0, 2 0 0 2 , 2 = s
-20
0 1 5 0 , 1 v = 0
0 0 3 0 0 0 0, 0, 3 0
5 2 , 2 = s
-30 0 2 , 2 0 0 v = 0
0 0 4 0 0 0 0, 0, 4 0 0 0 0, 0,5 0 0 0
-40
0 0 6 0 0 0 0, 0, 6 0
-40 x = 0,10
0,20
0,30
s = 1,00
140
0 0 6 0 0, 0 0 0 0 7 0 0, 0, 0 8 0 0 0 8 0 0, 0, 0 0 9 0 0 0 9 0 0, 0, 0 0 0 0 01 0 0 0, 0, 0
60
0 0 , 0 6 0 0 v = 0 ,0 8 0 0 0 v = 0 0 , 1 0 0 1 v =
-20
0 0 5 0 0, 0
70
0 0 , 0 3 0 0 v = 0 ,0 4 0 0 0 v =
3,00
1,00 0,90 0,80 0,70 0,60
2 0 , 0 0 0 v = 0 3 , 0 0 0 v = 4 0 , 0 0 0 0 v = 6 0 , 0 0 0 0 v = 8 0 ,0 0 0 0 v = 0 0 , 0 1 0 0 v =
5 0 , 0 1 0 0 v = 0 0 ,0 2 0 0 v =
10
0 , 0 0 4 0 0
100
90
30,00
3 0 , 0 0 0 0
160
180
200
0,40
0,50
1,20
220
240
0,60
0,70
0,80
1,40
260
280
0,90
-40
-20
0
20
40
60
400
420
440
460
80
100
120
140
160
1,60
300
320
340
360
Enthalpy [kJ/kg]
380
480
500
520
540
560
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. 05-09-18
-50
-60
-80 -90
10,00 9,00 8,00 7,00 6,00 5,00 4,00
-100
-110
3,00
-140
-80
0 5 0 0 0 5 0, 0, 0
0 0 6 0 0, 0, 0 0
7 0 0 0 7 0 0, 0, 0 0 8 0 0 08 0, 0, 0 0 9 0 0 0 9 0 0, 0, 0 0 0 0 0 1 0 0 0, 0, 01 015 0 0, 0, 01 0 0 0 2 0 0 0, 0, 0 2
5 0 , 2 = s 0 1 2 , 5 = 1 s 2 , = 0 s 2 ,
-100
0 0 0 3 0 0 0, 0, 0 3 0 0 0 4 0 0 0, 0, 0 4 0 0 05 0 0 0, 0, 05 0 0 06 0 0 0, 0, 06 0 0 0 7 0 0 0, 0, 0 7 0 0 08 0 0 0, 0, 08 0 0 0 9 0 0 0, 0, 0 9 0 0 0, 0,1 0 0 0
2 = s
5 2 2 , = s 0 3 2 , = s 5 3 2, = s 0 4 2 , = s 5 4 2 , = s
-110
-120
-130
0 0 0, 0,15 0 0 0 0 2 0 0 0 0, 0, 2 0 0 0 3 0 0 0 0, 0, 3 0 0 0 0 0 0 0,4 0,4 0 0 0 0, 0,5 0 0 0 0 0 0, 0,6 0 0 0 0 0 7 0 0 0 0, 0, 7 0 0 0 0, 0,8 0 0 0 0 0 9 0 0 0 0, 0, 9 0 0 0 0 0 0 0 1, 0 0
0 5 2 , = s 5 5 2, = s
-140
0 3 0 0 , 3 v = 0 4 4 0 0 0 , v = 0
-150
,0 0 4 0 0 0
5 9 , 1 = s 0 0 , 2 = s
-90
0 , 1 5 0 0 1 v = 0 , 2 0 0 0 2 v =
0,30
6 0 2, s = 6 5 2, = s
0 0 1,5 0 0 0
7 0 2, s =
-150
0 0 0 0 0 2,0 2,0 0
7 5 2, s =
0 6 , 6 0 0 v = 0 8 ,8 0 0 0 v = 0 0 , 0 0 0 0 v = 1
8 0 2, = s
0 0 0 0 0 3,0 3,0 0 0 0 0 0 0 0 4, 4, 0 0 0 0 ,0 0 0 0 5,0 0 0 0 0 0 0 0 6, 0 0
x = 0,10
0,20 s = 1,20
180
-70
0 ,0 6 0 0 0 v = 0 0 8 0 , 0 v = 0 0 0 , 1 0 0 1 v =
-130
1,00 0,90 0,80 0,70 0,60 0,50 0,40
2 0 , 0 3 0 0 0 ,0 0 v = 0 0 v = 0 0 4 0 0, 0 = v 0 ,0 0 6 0 0 v = 0 ,0 0 8 0 0 v = 0 0 1 0 0 , 0 v = 5 0 , 0 1 0 0 v = 0 0 , 0 2 0 0 v =
0 0 3 0 0, 0 v = 0 0 4 0 0, 0 v =
-120
2,00
0,10 0,09 0,08 0,07 0,06 0,05
= s
-70
20,00
0,20
0 0 0 3 0, 0 0 9 , 1
-50
-60
30,00
] r a B [ e r u s s e r P
2 0 ,0 0 0 0
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
30,00
9 0 1 0 0 ,0 , 0 0 0 0 0 0
R152a
Ref :ASHRAE Thermodynamic properties of Refrigerants 1986 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. 05-09-18
90
80
,0 1 5 0 0 0
90
0 2 0 0 0, 0
80 70 3 0 0 0 0, 0 = v 0 4 0 0, 0 6 0 , v = 0 0 8 0 0 0 0 v = = 0, 0 v 0 1
20,00 60 50
10,00 9,00 8,00 7,00 20
10
4,00 0
0 v =
1,00 0,90 0,80 0,70 0,60
0 0 0 6 0 0 0, 0, 0 6
0 9 0 0 0, 0, 0 0, 0,1 0 0 0 0 2 , 2 = s
0 3 , 2 = s
0 5 , 2 = s
0 4 , 2 = s
0 0 0, 0,1 5 0 0
0 6 , 2 = s
10
0 0 2 0 0 0 0, 0, 2 0
0 0 7 , 2 = s
-10
0 1 ,1 5 0
0 0 3 0 0 0 0, 0, 3 0 0 8 , 2 = s
-20
0 0 , 2 0 0 2 v =
-30
4 0 0 0 0, 0, 4 0 0 0 0, 0,5 0 0 0 0 9 , 2 = s
-30
0 0 , 3 0 0 3 v =
0 0 0 6 0 0 0, 0, 6 0 0 0 7 0 0 0, 0, 7 0 0 8 8 , 0, 0 0 0 0 0 0 0 9 0 0 0, 0, 9 0 0 0 0 0 0 1, 0
0 4 0 0 , 4 v = 0
-40
-40
0,50
x = 0,10
0,20
s = 1,00
125
0 0 0 5 0 0 0, 0, 0
0 1 , 2 = s
0 7 0 0 0, 0, 0 7 0 8 , 0, 0 0 8 0 0
20
0 0 , 0 8 0 0 v = 0 0 ,1 0 0 1 v =
-20
0 4 0 0 0, 0, 0 4
30
0 0 ,0 6 0 0 v =
-10
2,00
40
0 0 , 3 0 0 v = 0 0 0 4 0, 0 v =
5,00
3,00
50
5 0 , 1 0 0 v = 0 0 , 2 0 0 v =
30
6,00 ] r a B [ e r u s s e r P
60
0, v =
40
0 3 0 0 0, 0
70
150
175
200
0,30 1,20
225
250
0,40
0,50
1,40
275
300
0,60 1,60
325
350
0,70
0,80
1,80
375
0,90
-40
-20
0
20
40
60
80
100
120
140
160
180
200
675
700
725
750
2,00
400
425
450
475
Enthalpy [kJ/kg]
500
525
550
575
600
625
650
775
80,00 70,00 60,00
1 5 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. 05-09-18
2 0 , 0 0 0 0 6 , 1 = s
90
50,00
60 50
20,00
40 30 20
10,00 ] 9,00 r a 8,00 B [ 7,00 e r u 6,00 s
s e r P
10
-10
4,00 3,00
-40
0,50
30
0 7 , 1 = s
01 5 0 0, 01 0 0 0 2 0 0 0, 0, 0 2
3 0 0 0 3 0 0, 0, 0
5 8 , 1 = s
20
0 0 0 4 0 0 0, 0, 0
0 9 , 1 = s
0 0 05 0 0 0, 0, 0
5 9 , 1 = s
10
0 6 0 0 0, 0, 0 6 0 0 0 7 0 0 0, 0, 0 7 0 0 0 8 0 0 0, 0, 0 0 0 0 9 0 0 0, 0, 0 9 0 0 0, 0,1 0 0 0
0 0 , 2 = s
0
5 0 2 , = s
-10
0 1 2 , = s
-20
0 0 0, 0,15 0 0
5 1 2 , = s
0 0 2 0 0 0 0, 0, 2 0
0 2 2 , = s
-30
-50
3 3 0 0 0 v = 0, 0,20
0,30
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 0 4 0 0 0 0, 0, 4 0
0 3 2 , = s
2 ,2 0 0 0 v = 0
x = 0,10
0 0 3 0 0 0 0, 0, 3 0
5 2 2 , = s
-40
0 1 , 1 5 0 v = 0
s = 1,00
140
7 0 0 0 7 0 0, 0, 0 0 0 8 0 0, 0, 0 0 9 0 0 0 9 0 0, 0 01 0 0 0, 0, 0
0 8 , 1 = s
40
0 0 6 0 0, 0 v = 0 0 , 0 8 0 v = 0 0 1 0 0 , 1 v = 0
0 0 5 0 0, 0 0 0 6 0 0, 0
= s
50
0 0 , 0 4 0 0 v =
-30
, 0 0 4 0 0 0
5 7 , 1
60
0 0 3 0 0, 0 v =
-20
2,00
70
2 0 , 0 0 0 = v 3 0 , 0 0 0 0 = v 0 4 0 , 0 0 0 v = 6 0 ,0 0 0 0 v = 0 ,0 0 8 0 0 v = 0 0 , 0 1 0 0 v =
0 ,0 1 5 0 0 v = 0 ,0 2 0 0 0 v =
0
5,00
1,00 0,90 0,80 0,70 0,60
80
70
30,00
5 6 , 1 = s
90
80
40,00
0 0 0 3 0, 0
0 0 0, 0,5 0 0 0 0 0 6 0 0 0 0, 0, 6 0 0 0 7 0 0 0 0, 0, 7 0 0 0 8 0 0 0 0, 0, 8 0 0 0 9 0 0 0 0, 0, 9 0
-50
0,90
-40
-20
0
20
40
60
80
100
120
140
160
180
200
1,80
340
360
Enthalpy [kJ/kg]
380
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. 05-09-18
2 0 0 0 0,
3 0 , 0 0 0 0
20 10 10
30,00
0
2 0 , 0 0 0 = v 3 0 , 0 0 0 = v 4 0 ,0 0 0 0 v = 6 0 , 0 0 0 0 v = 8 0 , 0 0 0 0 v = 0 ,0 1 0 0 0 v =
-10
20,00 -20
-30
10,00 9,00 8,00 ] r a 7,00 B [ 6,00 e
r u s s e r P
-40
-50
4,00
-70
0 3 0 0 0, 0 0 4 0 0 0, 0 0 8 , 1 = s
-40
0 5 0 0 0, 0, 0 0 6 0 0 0, 0, 0 0 7 0 0 0, 0 7 0 0 0 8 0 0 0, 0 0 9 0 0 0, 0, 0 0 0 0,1 0 0 0
0 9 1 , = s
-50
-60
0 0 0,1 5 0 0
0 0 2 , = s
0 , 0 6 0 0 0 v =
0 0 2 0 0 0 0, 2 0
-70 0 1 2 , = s
0 0 8 0 0, 0 v = 0 1 0 0 , 1 v = 0
-80
0 2 0 0 0, 0 2
-30
0 0 4 0 0, 0 v =
2,00
01 5 0 0, 0
0 7 , 1 = s
-20
0 0 , 0 3 0 0 v =
3,00
3 3 0 0 0 v = 0,
0,50
x = 0,10
0,20
s = 0,60
60
80
100
0,30
0,40
0,80
120
140
1,00
160
180
0,50
0,60 1,20
200
0,70
0,80
1,40
220
240
0 0 4 0 0 0 0, 4
0 2 2 , = s
2 ,2 0 0 0 v = 0
-90
3 0 0 0 0, 0, 3
-80
0 1 5 0 , 1 v = 0
1,00 0,90 0,80 0,70 0,60
0 0 7 0 0, 0 0 0 0 8 0 0, 0 0 0 9 0 0, 0 01 0 0 0, 0
-10
0 ,0 2 0 0 0 v =
-60
,0 0 6 0 0 0
0 6 , 1 = s
0
5 0 , 0 1 0 0 v =
5,00
0 0 5 0 0, 0
0 5 , 1 = s
20
40,00
0 0 0 4 0, 0
0 0 5 0 0 0 0, 0, 5 0 0 0 6 0 0 0 0, 0, 6 0 7 0 0 0 0, 0, 7
-90
0 0 8 0 0 0 0, 8 0
0,90
-80
-60
-40
-20
0
20
40
60
80
100
1,60
260
280
Enthalpy [kJ/kg]
300
320
340
360
380
400
420
440
460
40,00
0 2 0 0 0 ,
R404A
Ref :DuPont SUVA HP62 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. 05-09-18
30,00
3 0 0 0 0,
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 6 , 1 = s
60 50
20,00
4 0 , 0 0 0 0
0 0 9 0 0, 0 01 0 0 0, 0, 01
5 0 01 5 0 0, 0, 0
40
0 0 0 2 0 0 0, 0, 0 2
30
0 0 0 3 0 0 0, 0, 0 3
20
10,00 9,00 8,00 7,00 ] r a B [ e r u s s e r P
0 0 0 4 0 0 0, 0, 0 4
10
0 0 05 0 0 0, 0, 05 5 6 , 1 = s
0
6,00 5,00
= s
-10
0 8 , 1 = s
5 7 , 1 = s
0 7 , 1
5 8 , 1 = s
0 9 , 1 = s
0 0 0 7 0 0 0, 0, 0 7 0 0 0 8 0 0 0, 0, 0 8 0 0 0 9 0 0 0, 0, 0 9 0 0 0, 0,1 0 0 0
0 0 , 2 = s
4,00 -20
3,00
0 0 0 6 0 0 0, 0, 0 6
5 9 , 1 = s
5 0 , 2 = s
0 0 0, 0,15 0 0 0 1 , 2
-30
2,00
0 0 2 0 0 0 0, 0, 2 0
= s
5 1 , 2 = s
-40
0 0 3 0 0 0 0, 3 0
0 2 , 2 = s
1,00 0,90 0,80 0,70
0 0 4 0 0 0 0, 4 0
-50 -50
0 0 0, 0,5 0 0 0 0 0 6 0 0 0 0, 0, 6 0
0,60 0,50
0 0 7 0 0 0 0, 0, 7 0
x = 0,10
0,20
0,30
0,40
0,50
s = 1,00
120
140
160
180
200
0,60
0,70
1,20
220
240
0,80
0,90
1,40
260
280
-40
-20
0
20
40
60
80
100
120
140
160
1,60
300
320
340
Enthalpy [kJ/kg]
360
380
400
420
440
460
480
500
520
540
50,00 40,00
0 2 0 0 0 ,
R407C
Ref :DuPont SUVA AC9000 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. 05-09-18
30,00
3 0 , 0 0 0
0 ,0 0 4 0 0
0 0 5 0 0, 0
,0 0 6 0 0 0
0 0 7 0 0, 0
5 7 , 1 = s
60
8 0 0 0 8 0 0, 0, 0 0 0 0 9 0 0, 0, 0 0 01 0 0 0, 0, 01
01 5 0 0, 0, 01
50
0 0 0 2 0 0 0, 0, 0 2
20,00 40 0 8 , 1 = s
30
10,00 9,00 8,00 ] 7,00 r a B 6,00
[ e r u s s e r P
0 3 0 0 0, 0, 0 3 0 0 0 4 0 0 0, 0, 0
20 5 8 , 1 = s
10
0
5,00 4,00
0 0 05 0 0 0, 0, 05 0 9 , 1 = s
5 9 , 1 = s
0 0 , 2 = s
0 0 0 6 0 0 0, 0, 0 6 0 0 0 7 0 0 0, 0, 0 7
5 0 , 2 = s
0 0 0 8 0 0 0, 0, 0 8 0 0 0 9 0 0 0, 0, 0 9 0 0 0, 0,1 0 0 0
0 1 , 2 = s
5 1 , 2 = s
-10 -10
3,00
0 0 0, 0,15 0 0
0 2 , 2 = s
-20
0 0 2 0 0 0 0, 0, 2 0
5 2 , 2 = s
2,00 -30
0 3 , 2 = s
0,50
0 0 4 0 0 0 0, 0, 4 0
0 4 , 2 = s
0 0 0, 0,5 0 0 0 0 0 6 0 0 0 0, 6 0
-5 0 0
x = 0,10
0,20
0,30
0,40
s = 1,00
120
5 3 , 2 = s
-40
1,00 0,90 0,80 0,70 0,60
0 0 3 0 0 0 0, 0, 3 0
140
160
180
200
0,50
1,20
220
240
0 0 7 0 0 0 0, 7 0 0 0 8 0 0 0 0, 0, 8 0
0,60
0,70
1,40
260
280
0,80
0,90
1,60
300
320
-40
-20
0
20
40
60
80
100
120
140
160
1,80
340
360
Enthalpy [kJ/kg]
380
400
420
440
460
480
500
520
540
560
580
40,00
R410A
Ref :Patel-Teja equation and DuPont SUVA 9100 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. 05-09-18
60
30
5 0 01 5 0 0, 0
10
] r a B [ e r u s s e r P
0 2 0 0 0, 0, 0
0 3 0 0 0, 0, 0 0 0 0 4 0 0 0, 0 4
0 9 , 1
0 0 0 5 0 0 0, 0, 0 5
= s
0
6,00
5 9 , 1 0 = 0 , s 2 = s
-10
5,00
0 6 0 0 0, 0, 0 6 5 0 , 2 = s
3,00
0 1 , 2 = s
0 2 , 2 = s
-30
2,00
0 7 0 0 0, 0, 0 7 0 8 0 0 0, 0 0 0 0 9 0 0 0, 0, 0 9 0, 0,1 0 0 0
5 1 , 2 = s
-20
4,00
,0 1 0 0 0 0
5 8 , 1 = s
20
10,00 9,00 8,00 7,00
0 , 0 0 9 0 0
0 8 , 1 = s
40
20,00
0 , 0 0 8 0 0
5 7 , 1 = s
50
30,00
5 0 6 0 0 , 0 , 0 0 0 0 7 0 0 0 0 0, 0
0 0 0, 0,1 5 0 0
5 2 , 2 = s
2 0 0 0 0, 0, 2 0
0 3 , 2 = s
-40
0 0 3 0 0 0 0, 0, 3 0
5 3 , 2 = s
0 4 , 2 = s
-50
0 0 4 0 0 0 0, 0, 4
5 4 , 2 = s
1,00 0,90 0,80 0,70
0 0 5 0 0 0 0, 0, 5 0 0 6 0 0 0 0, 0, 6
0 5 , 2 = s
-60
7 0 0 0 0, 0, 7 8 , 0, 0 8 0 0 0 0 0 9 0 0 0 0, 0, 9
0,60 0,50
x = 0,10
0,20
s = 0,80
100
120
140
160
0,30 1,00
180
0,40
0,50
1,20
200
220
0,60
0,70
1,40
240
260
280
0,80
1,60
300
320
0,90
-60
-40
-20
0
20
40
60
80
100
120
140
500
520
540
560
1,80
340
360
Enthalpy [kJ/kg]
380
400
420
440
460
480
580
0 , 0 0 4 0 0
R507
30,00
Ref :Allied Signal, Genetron AZ 50 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. 05-09-18
60
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 9 0 0, 0, 0 01 0 0 0, 0
60
50 50 2 0 , 0 0 0 v = 3 0 , 0 0 4 0 0 0 ,0 v = = 0 0 v
40
20,00 30 20
10,00 9,00 8,00 7,00 ] r a B [ e r u s s e r P
30
6 0 , 0 0 0 0 v = 8 0 , 0 0 0 0 v = 0 0 , 0 1 0 0 v =
10
0
20
4,00
-20
-30
0 4 0 0 0, 0, 0 4
5 6 , 1 = s
0 0 0 5 0 0 0, 0 5 0 7 , 1 = s
-10
5 7 , 1 = s
-20
0 ,0 3 0 0 0 v =
3,00
0 2 0 0 0, 0, 0
0 3 0 0 0, 0, 0 3
0 ,0 1 5 0 0 v = 0 0 , 0 2 0 0 v =
-10
5,00
0 6 , 1 = s
10
0
6,00
01 5 0 0, 0
40
-30
0 0 , 0 6 0 0 v = 0 1 , 1 0 0 v = 0
0,60 0,50
-50
3 0 0 0 0, 0, 3 0 4 0 0 0 0, 4 0
5 0 , 2 = s
2 0 0 0 , 2 v = 0
5 0 0 0 0, 5 0
-60
0 0 6 0 0 0 0, 0, 6 0
-60 x = 0,10
0,20
0,30
s = 0,80
120
0 0 , 2 = s
-50 0 1 , 1 5 0 v = 0
2 0 0 0 0, 0, 2 0
5 9 , 1 = s
-40
0 0 , 0 8 0 0 v =
0, 0,1 5 0 0
0 9 , 1 = s
2,00
1,00 0,90 0,80 0,70
0 0 0 7 0 0 0, 0, 0 0 8 0 8 0 0, 0, 0 0 9 0 0 0, 0, 0 9 0, 0,1 0 0 0
0 8 , 1 = s 5 8 , 1 = s
0 ,0 4 0 0 0 v =
-40
0 0 0 6 0 0 0, 0, 0 6
140
0,40
0,50
1,00
160
180
0,60
1,20
200
220
240
0,70
0,80
1,40
260
280
0,90
-60
-40
-20
0
20
40
60
80
100
1,60
300
Enthalpy [kJ/kg]
320
340
360
380
400
420
440
460
20,00
8 0 0 0 , 0 0 , 0 0 9 0 0 0 0 , 0 1 0 0 0
R508A
Ref :ICI Chemicals & Polymers 1996 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. 05-09-18
-20 -30
10,00 9,00 8,00
-40
7,00
2 0 0 0 0, v = 0 3 0 0 0, 0 4 0 v = 0 0 , 6 0 , 0 0 0 v = 0 = v 0 8
-50
5,00
5 3 , 1 = s
0 2 0 0 0, 0
0 3 0 0 0, 0, 0
-40 0 0 0 4 0 0 0, 0
-50
5 0 , 1 0 0 v = 0 0 , 2 0 0 = v
-60
4,00
-30
, 0 0 v = 0 0 , 1 0 0 v =
6,00
] r a B [ e r u s s e r P
0 1 5 0 0, 0
-20
0 5 0 0 0, 0 5 0 0 0 6 0 0 0, 0
-60
0 4 , 1 = s
5 4 , 1 = s
0 5 , 1 = s
0 6 , 1 = s
5 5 , 1 = s
0 0 0 , 3 0 0 v =
1,00 0,90 0,80
0 7 , 1 = s
0 ,0 6 0 0 0 v =
-80
2 0 0 0 0, 2 0 8 , 1 = s
3 0 0 0 0, 3 5 8 , 1 = s
-90
0 1 5 0 0, 1 v =
0,70
0,1 5 0 0 5 7 , 1 = s
-80
0 ,0 8 0 0 0 v = 0 0 0 0, 11 v =
-90
0,1 0 0 0
-70
0 0 ,0 4 0 0 v =
2,00
0 8 0 0 0, 0 0 9 0 0 0, 0
5 6 , 1 = s
3,00 -70
0 7 0 0 0, 0
4 0 0 0 0, 4
0 2 0 0 , 2 v = 0
0,60 0,50
x = 0,10
0,20
0,30
s = 0,60
20
40
60
0,40
0,50
0,80
80
0,60
0,70
1,00
100
120
0,80
5 0 0 0 0, 5 0
0,90
-80
-60
-40
-20
0
20
40
60
1,20
140
160
180
Enthalpy [kJ/kg]
200
220
240
260
280
300
320
40,00 30,00
1 5 , 0 0 0 0
RC318
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. 05-09-18
110 100
90
20,00
90
80 80
2 0 , 0 0 0 0 v = 0 3 60 ,0 0 0 0 v = 0 4 ,0 0 0 0 v = 70
10,00 9,00 8,00 7,00 6,00 5,00
50
30
4,00 20
3,00 10
2,00 0
-10
1,00 0,90 0,80 0,70 0,60
-20
0,50 -30
0,40 0,30 0,20
0 0 , 3 0 0 v = 4 0 0 , 0 0 0 v = 0 0 , 0 6 0 0 v = 0 0 , 0 8 0 0 v = 0 0 , 1 0 0 1 v = 0 0 , 1 5 0 1 0 v = ,2 0 0 -30 0 2 v = 0 0 3 0 0, 3 v =
x = 0,10 0,100,20 0,20 0,30 0,30 0,40 0,40 0,50 0,50 0,60 0,60 0,70 0,70 0,80 0,80 0,90 0,90 s = 1,00
100
120
140
160
180
200
70
0 0 0 2 0 0 0, 0, 0 2
0 0 03 0 0 0, 0, 03
40
0 4 0 0 0, 0, 0 4 0
30 20
10
0 5 5, 1 = s
-10
015 0 0, 0, 01
60 50
6 0 40 , 0 0 0 0 v = 0 8 , 0 0 0 0 v = 0 0 ,0 1 0 0 v =
5 0 , 0 1 0 0 v = 0 0 , 2 0 0 = v
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 05 0 0 0, 0, 05 0 0 , 2 = s
06 0 0 0, 0, 06 7 0 0 0 7 0 0, 0, 0 08 0 0 0, 0, 08 9 0 0 0 9 0 0, 0, 0 0 0 0 0, 0,1 0 0
5 0 , 2 = s
0, 0,15 0 0 0 1 , 2 = s
-20
240
0 0 4 0 0 0, 0, 4 0 0 0 0 0, 0,5 0 0 0 0 0 0, 0,6 0 0 0 0 7 0 0 0, 0, 7 0 0 0 0 0, 0,8 0 0
-20
260
0 0 2 0 0 0, 0, 2 0
0 0 0 0, 0,3 0 0
0
20
40
60
80
100
120
1,20
220
0 0 3 0 0, 0 4 0 0 0 4 0 0, 0, 0 05 0 0 0 , 0, 0 5 0 6 0 0 0 6 0 0, 0, 0 0 7 0 0 0 7 0 0, 0, 0 0 8 0 0 08 0, 0, 0 0 9 0 0 0 9 0 0, 0, 0 0 0 0 1 0 0 0,0 0,01
110 100
] r a B [ e r u s s e r P
,0 0 2 0 0 0
280
300
320
340
Enthalpy [kJ/kg]
360
380
400
420
440
460
480
500
520
540
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. 05-09-18
0 2 0 0 0 ,
3 0 0 0 0, 0 1 , 2 = s
-120 -120
50,00 40,00
4 0 , 0 0 0
-130
0 2 , 2 = s
-130
30,00 -140
20,00 -150
10,00 9,00 8,00 7,00 6,00
] r a B [ e r u s s e r P
3 0 0 0 0 , 0 4 0, 0 0 = v v = 6 0 , 0 0 0 = v 8 0 , 0 0 0 = 0 0 v , 1 0 0 = v
5,00 4,00 3,00
v =
2,00
, 0 0 9 0 0 0
2 = s
0 7 2 , 0 = 8 s 2, = s
0 4 0 0 0, 0 0 5 0 0 0, 0 0 6 0 0 0, 0 0 7 0 0 0, 0 0 8 0 0 0, 0 0 9 0 0 0, 0 1 0 0 0 0, 1
0 9 2, = s
0 0 3 , = s 0 1 3, = s 0 2 3, = s 0 3 3 , = s
-170
1 5 0 0 0, 1 2 0 0 0 0, 2
4 0 3, = s
3 0 0 0 0, 3
5 0 3, s =
4 0 0 0 0, 4 0
6 0 3, s =
-180
5 0 0 0 0, 5
7 0 3, s =
9 0 3, s =
0 0 4, s =
0 3 , 3 0 0 v = 0 0,20
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
6 0 0 0 0, 6 7 0 0 0 0, 7 8 0 0 0 0, 8 9 0 0 0 0, 9 0 0 0 0 1, 0
0 , 3 8 s =
0 , 2 0 0 0 2 v =
x = 0,10
0 1 0 0 0, 0
0 3 0 0 0, 0
0 0 , 1 5 0 1 v =
s = 0, 0,60 0,80
100
0 , 0 0 8 0 0
0 2 0 0 0, 0
0 0 , 0 6 0 0
1,00 0,90 0,80 0,70 0,60 0,50
0 4 , 2 = 0 s 5 , 2 = 0 s 6 ,
-160
0 ,0 8 0 0 0 v = 0 0 , 1 0 0 1 v =
-180
0 0 0 7 0, 0
0 1 5 0 0, 0
-150
0 0 , 3 0 0 0 v = 0 0 , 0 4 0 0 v =
-170
0 , 0 0 6 0 0
0 3 , 2 = s
-140
5 0 , 1 0 0 = v 0 0 0 , 2 0 0 v =
-160
0 ,0 0 5 0 0
0,80 2,40
300
0,90 2,60
-180
-160
-140
-120
-100
-80
-60
-40
-20
0
20
2,80
350
Enthalpy [kJ/kg]
400
450
500
550
0 2 0 0 , 0
R728
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. 05-09-18
3 0 0 0 0, 0 5 , 1 = s
50,00 40,00
0 6 , 1 = s
-150
0 ,0 0 5 0 0
s
-170
10,00 9,00 8,00 7,00 6,00
-160
-180
5,00 4,00
v =
-180
2,00
v =
0 ,0 6 0 0 0
0 2 0 0 0, 0
0 3 0 0 0, 0 0 4 0 0 0, 0 0 0 0 5 0 0 0, 0
-190
0 2 0 0 , 2 v = 0
-200
3 ,3 0 0 0 v = 0 x = 0,10
0,20
s = 0, 0 ,00 0,20
50
75
2 0 0 0 0, 2
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
2,00
225
3 0 0 0 0, 3 4 0 0 0 0, 4 5 0 0 0 0, 5 6 , 0 6 0 0 0
5 0 3, s = , 0 3 6 s =
0 1 5 0 0, 1 v =
0,50
1 5 0 0 0, 1
1 0 3, = s 2 0 3, s = 3 0 3, s = 4 0 3, s =
0 0 8 0 0, 0 v = 0 0 , 1 0 0 1 v =
1,00 0,90 0,80 0,70 0,60
0 6 0 0 0, 0 0 7 0 0 0, 0 0 8 0 0 0, 0 0 9 0 0 0, 0 1 0 0 0 0, 1
0 6 2 , = s 0 7 2 , = s 0 8 2 , = s 0 9 2, = s 0 0 3, s =
0 ,0 3 0 0 0
-190
0 1 0 0 0, 0
0 5 2 , = s
0 0 , 0 4 0 0 v =
3,00
,0 0 9 0 0 0
0 3 2, = 0 s 4 2 , = s
-170
5 0 , 0 1 0 0 v = 0 0 0 , 2 0 0 v =
,0 0 8 0 0 0
, 0 1 5 0 0 0
= s
0 0 4 , 0 0 6 0 = v , 0 0 0 = v 8 0 , 0 0 0 0 v = 0 1 0 0, v =
0 , 0 0 7 0 0
0 0 2 , 0 = 1 s 2 , 0 = 2 s 2 ,
-160
20,00
0 , 0 0 6 0 0
0 7 , 1 0 = 8 , s 0 1 9 , = 1 s =
-150
30,00
] r a B [ e r u s s e r P
4 0 , 0 0 0 0
7 0 3, s =
-200
0,90 2,20
-200
7 0 0 0 0, 7 8 0 0 0 0, 8 9 0 0 0 0, 9 0 0 0 0 1, 0
-180
-160
-140
-120
-100
-80
-60
-40
2,40
250
Enthalpy [kJ/kg]
275
300
325
350
375
400
425
450
5 1 0 0 , 0
R740
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. 05-09-18
0 2 0 0 0,
3 0 0 , 0 0 0 7 , 1 = s
50,00
0 8 , 1 = s
-130
40,00
4 0 ,0 0 0 0
0 9 1 , = s
0 0 2 , = s
-130
30,00
-140
20,00 -150
] 10,00 r a 9,00 B [ 8,00 e r u 7,00 s s e 6,00 r P
-180
,0 6 0 0 0 0 ,0 7 0 0 0 0 ,0 8 0 0 0 0 ,0 9 0 0 0 0 ,1 0 0 0 0 1
4 0 2, = s
-160
5 0 2, = s
-170
,1 5 0 0 0 1
6 0 2, = s
,2 0 0 0 0 2
7 0 2, s =
0 0 , 0 6 0 0 v =
8 0 2, s =
-180
,3 0 0 0 0 3
x = 0,10
0,20
160
180
0,30
1,00
0,40 1,20
200
0,50 1,40
220
0,60 1,60
240
0,70 1,80
260
,4 0 0 0 0 4
0 , 2 9 s =
0,80 2,00
,5 0 0 0 0 5
, 0 3 0 s =
1 5 0 0 , 1 v = 0
s = 0,80
140
,0 4 0 0 0 0 ,0 5 0 0 0 0
0 0 8 0 , 0 v = 0 0 1 0 0 , 1 v = 0
1,00 0,90 0,80 0,70
,0 2 0 0 0 0
2 0 2, s =
0 ,0 3 0 0 0 v = 0 0 , 0 4 0 0 v =
2,00
, 0 0 8 0 0 0 ,0 0 9 0 0 0 ,0 1 0 0 0 0
3 0 2, = s
-150
4,00 3,00
0 , 0 0 7 0 0
,0 3 0 0 0 0
5 0 , 0 1 0 0 v = 0 ,0 2 0 0 0 v =
-170
0 0 0 6 0, 0
,0 1 5 0 0 0 0 1 2, = s
-140
6 0 , 0 0 0 v = 8 0 , 0 0 0 0 v = 0 0 , 0 1 0 0 v =
-160
5,00
2 0 , 0 0 0 v = 3 0 , 0 0 0 = v 4 0 , 0 0 0 v =
5 0 , 0 0 0 0
0,90
-180
-160
-140
-120
-100
-80
-60
-40
-20
,6 0 0 0 0 6 ,7 0 0 0 0 7 ,8 0 0 0 0 8 0
2,20
280 Enthalpy [kJ/kg]
300
320
340
360
380
400
420
0 2 0 0 , 0
R729
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. 05-09-18
3 0 0 0 0, 0 6 , 1 = s
50,00
0 7 , 1 = s
40,00
4 0 ,0 0 0 0
0 8 , 1 = s
0 9 , 1 = s
-145
0 0 , 2 = s
5 0 , 0 0 0 0
-150
0 2 2 , 0 = 3 s 2 , = s
-175
5,00 -180
3,00
2,00
, 0 6 0 0 0 0 0 7 0 0 0, 0 0 8 0 0 0, 0 0 9 0 0 0, 0 1 0 0 0 0, 1
1 5 0 0 0, 1 2 0 0 0 0, 2
0,20 0,40
-200
0,60
-175
0,30 0,80
-150
0,40 1,00
1,20
-125
5 0 0 0 0, 5 6 0 0 0 0, 6 7 0 0 0 0, 7 8 0 0 0 0, 8 9 0 0 0 0, 9 0 0 0 0 1, 0
7 0 3, s =
0,50 1,40
4 0 0 0 0, 4
6 0 3, s =
-19 5
x = 0,10
3 0 0 0 0, 3
3 0 3, s = 4 0 3, s = 5 0 3, s =
-190
-225
, 0 5 0 0 0 0
1 0 3, s = 2 0 3, s =
-185
0,50
, 0 4 0 0 0 0
0 7 2 , = s 0 8 2 , = s 0 9 2, = s 0 0 3, = s
-170
1,00 0,90 0,80 0,70 0,60
, 0 3 0 0 0 0
0 6 2, = s
-165
4,00
0 0 9 0 0, 0 0 1 0 0 0, 0
0 2 0 0 0, 0
0 4 2, = s 0 5 2 , = s
-160
s s e r P
,0 0 8 0 0 0
0 1 5 0 0, 0
-155 155
10,00 ] 9,00 r a 8,00 B [ 7,00 e r 6,00 u
,0 0 7 0 0 0
0 1 , 2 = s
30,00
20,00
0 0 0 6 0, 0
0,60 1,60
-100
0,70 1,80
-75
0,80
2,00
2,20
-50
0,90
-180
-160
-140
-120
-100
-80
-60
2,40
-25
Enthalpy [kJ/kg]
0
25
50
75
100
125
150
2800
2800 T a u l li n i ie n n
2600
1 ,5 2
2400
g k / J k n i h
2600 3
4
6
8
1 0 1 5
2 0
1 0 ,5 0 ,2 0 ,1
H i l f s l i n i e n
2400
2200
2200 2 0 1 5 b a r 1 0 8 6 4
2000
e i p l a h t 1800 n E
2000
3 2
1 , 5
1 0 , 5
1800
0 , 2 2 0 , 1
1600
1600
1400
1400 NaßdampfGebiet
1200
1200
1000
1000
2 0 00 0
800 800
800
S i e d e l i n i e n
18 0 0 °C 17 0 0 16 0 0 15 0 0
600 600
14 0 0
1 5
12 0 0 110
400 400
600
2 0 b a r
13 0 0
8 6
10 0 0
1 0
400
4
9 0 0
3
8 0 0
2
7 0 0
1 ,5
6 0 0
1
200 200
200
5 0 0 4 0 0
0 ,5
3 0 0 2 0 0
0 ,2
10
0
0 E r s t - 10 a r l i n i r u e n g s -
0
g s u u n r r r a t s a E r s e e i n n l i -200
0 ,1
- 2 20 0
-200
-30 -40 -50 -60
- 7 0
-400 0,0
0,1
0,2
0,3
0,4
-400 0,5
0,6
0,7
0,8
Ammoniakkonzentration Ammoniakkonzentration ξ in kg/kg
0,9
1,0
2900
g k / J k2800 n i
2900
H i l f s l i n i e
2800
h
2 b a ar r
e i p2700 l a h t n E
1
2700
0 ,5 0 ,2 0 ,1 0 ,0 5 5
2600
2600
0 ,0 2 2 0 ,0 1
2500
2500
500 500
500 S i e d e l i n i e
400 400
400 0 , 2
2 b a r
0 ,5
° C 1 0 1 1 2 0
1
300 300
300 1 0 0
9 0
7 0
8 0
200 200
100 100
200
E r s t a r r u n l i n g i e s -
5 0 60
4 0
0,1
0 5 0, 0
100 30 2 0 0
10
0 2 0, 0, 0 ,01 0,01
0
0
0,3
0
0,4
0,5
0,6
0,7
0,8
0,9
Wasserkonzentration Wasserkonzentration ξ in kg/kg
1,0
350
3,0
3,5
4,0
4,5
5,0
5,5 0 2 1 0 0 2
K n i
0 8 1
0 0 1
6,0
0 8
0 6 0 5
5 2
0 4
0 2
0 3
0 6 1
r a b
300
0 0 3
6,5
6 1
4 1
2 1
8
6 5
4
0 1
7,0
3
2
5 , 1
350
1
420
8 1
K n i
410
0 4 1
400 390
T r u t a r e p m e T
380 370
5 , 0
360 350
250
300
T r u t a r e p m e T 250
330 320 310 300
200
200
290 280 270 15 0 0 14 0 0
260 250
150
150
240 230 1 6 0
1 3 0
220 210 200
100
100
190 180 - 1 0
3,0
0
1 0
3,5
2 0
3 0
4 0
4,0
5 0
6 0
7 0
8 0 0
4,5
9 0
1 0 0
1 1 0
1 2 0 0
5,0
T,s - Diagramm von Luft
h = 170 kJ/kg 5,5
6,0
Entropie s
6,5
in kJ/(kg K)
7,0
