Refrigeration Graphic (Coolpack)
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Transcript of Refrigeration Graphic (Coolpack)
-
Enthalpy [kJ/kg]0 100 200 300 400 500 600 700 800 900 1000 1100 1200 1300 1400 1500 1600 1700 1800 1900 2000
Pressu
re [Ba
r]
0.500.600.700.800.901.001.00
2.00
3.004.005.006.007.008.009.0010.00
20.00
30.0040.0050.0060.0070.0080.0090.00100.00
200.00
s = 3.7
5
s = 4.0
0
s = 4.2
5s =
4.50
s = 4.75
s = 5.00
s = 5.25
s = 5.50
s = 5.75
s = 6.00
s = 6.25
s = 6.50
s = 6.75
s = 7.00
s = 7.25
s = 7.50
s = 7.75
-40
-40
-30
-20
-20
-10
0
0
10
20
20
30
40
4050
60
6070
80
8090
100
100110
120
120130
140 160 180 200 220
0.0030
0.0040
0.0050 0.0060 0.0070 0.0080 0.0090 0.0100.015
0.020
0.030
0.0400.0500.0600.0700.0800.0900.10
0.15
0.20
0.30
0.400.500.600.700.800.901.0
1.52.0
3.04.0
-40
-30-20
-100
1020
3040
5060
7080
90
100
110
120
130
x = 0.10 0.20 0.30 0.40 0.50 0.60 0.70 0.80 0.90s = 1.00 2.00 3.00 4.00 5.00 6.00
v= 0.0060v= 0.00
80
v= 0.010
v= 0.015
v= 0.020
v= 0.030
v= 0.040
v= 0.060
v= 0.080
v= 0.10
v= 0.15
v= 0.20
v= 0.30
v= 0.40
v= 0.60
v= 0.80v= 1.0
DTU, Department of Energy Engineerings in [kJ/(kg K)]. v in [m^3/kg]. T in [C]M.J. Skovrup & H.J.H Knudsen. 12-04-23
R717 Ref :R.Dring. Klima+Klte ingenieur Ki-Extra 5, 1978
-
Enthalpy [kJ/kg]160 180 200 220 240 260 280 300 320 340 360 380 400 420 440 460 480 500 520 540 560
Pressu
re [Ba
r]
0.050.060.070.080.090.100.10
0.200.300.400.500.600.700.800.901.00
2.003.004.005.006.007.008.009.00
10.00
20.0030.0040.0050.0060.00
s = 1.6
5
s = 1.7
0s =
1.75
s = 1.80
s = 1.85
s = 1.90
s = 1.95
s = 2.00
s = 2.05
s = 2.10
s = 2.15
-40-40
-30
-20
-20
-10
0
0
10
20
2030
40
4050
60
6070
80
8090
100
100110
120
120130
140
140150
160
160170
180
180190
200 220 240 260
0.0015
0.0020 0.0030 0.0040 0.00500.00600.00700.00800.00900.010
0.0150.020
0.0300.0400.0500.0600.0700.0800.0900.10
0.150.20
0.300.400.500.600.700.800.901.0
1.52.0
3.04.05.06.0
-40-30
-20-10
010
2030
4050
6070
8090
100110
120130
140150
160
170
180 190
x = 0.10 0.20 0.30 0.40 0.50 0.60 0.70 0.80 0.90s = 1.00 1.20 1.40 1.60
v= 0.0020
v= 0.0030
v= 0.0040
v= 0.0060
v= 0.0080
v= 0.010
v= 0.015
v= 0.020
v= 0.030
v= 0.040
v= 0.060
v= 0.080
v= 0.10
v= 0.15v= 0.20
v= 0.30v= 0.40
v= 0.60 v= 0.80v= 1.0
v= 1.5
DTU, Department of Energy Engineerings in [kJ/(kg K)]. v in [m^3/kg]. T in [C]M.J. Skovrup & H.J.H Knudsen. 12-04-23
R11 Ref :R.C.Downing. ASHRAE Transactions 1974. Paper No. 2313.
-
Enthalpy [kJ/kg]140 160 180 200 220 240 260 280 300 320 340 360 380 400 420 440 460 480 500
Pressu
re [Ba
r]
0.500.600.700.800.901.001.00
2.00
3.004.005.006.007.008.009.00
10.00
20.00
30.0040.0050.0060.0070.00
s = 1.5
0s =
1.55
s = 1.6
0
s = 1.6
5
s = 1.7
0
s = 1.7
5s =
1.80
s = 1.85
s = 1.90
s = 1.95
s = 2.00
-40
-40
-30
-20
-20
-10
0
0
10
20
20
30
40
4050
60
6070
80
8090
100
100110
120 140 160 180 200
0.0015
0.0020 0.0030 0.00400.00500.00600.00700.00800.00900.010
0.015
0.020
0.030
0.0400.0500.0600.0700.0800.0900.10
0.15
0.20
0.30
0.400.500.60
-40-30
-20-10
010
2030
4050
60
70
80
90
100
110
x = 0.10 0.20 0.30 0.40 0.50 0.60 0.70 0.80 0.90s = 1.00 1.20 1.40
v= 0.0020
v= 0.0030
v= 0.0040
v= 0.0060
v= 0.0080
v= 0.010
v= 0.015
v= 0.020
v= 0.030
v= 0.040
v= 0.060
v= 0.080
v= 0.10
v= 0.15v= 0.20
DTU, Department of Energy Engineerings in [kJ/(kg K)]. v in [m^3/kg]. T in [C]M.J. Skovrup & H.J.H Knudsen. 12-04-23
R12 Ref :R.C.Downing. ASHRAE Transactions 1974. Paper No. 2313.
-
Enthalpy [kJ/kg]80 100 120 140 160 180 200 220 240 260 280 300 320 340 360 380 400
Pressu
re [Ba
r]
0.050.060.070.080.090.100.10
0.200.300.400.500.600.700.800.901.00
2.003.004.005.006.007.008.009.00
10.00
20.0030.0040.0050.00
s = 1.3
0s =
1.35
s = 1.40
s = 1.45
s = 1.50
s = 1.55
s = 1.60
s = 1.65
s = 1.70
s = 1.75
s = 1.80
s = 1.85
s = 1.90
s = 1.95
s = 2.00
s = 2.05
-120
-120
-110
-100
-100
-90
-80
-80
-70
-60
-60
-50
-40
-40-30
-20
-20-10
0
010
20
20
40 60 80 100 120
0.0015
0.0020 0.0030 0.0040 0.0050 0.00600.00700.00800.00900.010
0.0150.020
0.0300.0400.0500.0600.0700.0800.0900.10
0.150.20
0.300.400.500.600.700.800.901.0
1.52.0
3.04.05.0
-120
-110
-100
-90-80
-70-60
-50-40
-30
-20
-10
0
10
20
x = 0.10 0.20 0.30 0.40 0.50 0.60 0.70 0.80 0.90s = 0.60 0.80 1.00 1.20 1.40
v= 0.0020
v= 0.0030
v= 0.0040
v= 0.0060
v= 0.0080
v= 0.010
v= 0.015
v= 0.020
v= 0.030
v= 0.040
v= 0.060
v= 0.080
v= 0.10
v= 0.15
v= 0.20
v= 0.30
v= 0.40v= 0.60
v= 0.80v= 1.0
DTU, Department of Energy Engineerings in [kJ/(kg K)]. v in [m^3/kg]. T in [C]M.J. Skovrup & H.J.H Knudsen. 12-05-06
R13 Ref :R.C.Downing. ASHRAE Transactions 1974. Paper No. 2313.
-
Enthalpy [kJ/kg]180 200 220 240 260 280 300 320 340 360 380 400 420 440 460 480
Pressu
re [Ba
r]
0.050.060.070.080.090.100.10
0.200.300.400.500.600.700.800.901.00
2.003.004.005.006.007.008.009.00
10.00
20.0030.0040.0050.00
s = 1.9
0s =
1.95
s = 2.00
s = 2.05
s = 2.10
s = 2.15
s = 2.20
s = 2.25
s = 2.30
s = 2.35
s = 2.40
s = 2.45
s = 2.50
s = 2.55
s = 2.60
s = 2.65
s = 2.70
s = 2.75
s = 2.80
-150
-140
-140
-130
-120
-120
-110
-100
-100
-90
-80
-80-70
-60
-60-50
-40 -20 0 20 40 60
0.0015
0.0020 0.0030 0.0040 0.0050 0.0060 0.00700.00800.00900.010
0.0150.020
0.0300.0400.0500.0600.0700.0800.0900.10
0.150.20
0.300.400.500.600.700.800.901.0
1.52.0
3.04.05.06.0
-150
-140
-130
-120
-110
-100
-90
-80
-70
-60
-50
x = 0.10 0.20 0.30 0.40 0.50 0.60 0.70 0.80 0.90s = 1.20 1.40 1.60 1.80 2.00
v= 0.0020
v= 0.0030
v= 0.0040
v= 0.0060
v= 0.0080
v= 0.010
v= 0.015
v= 0.020
v= 0.030
v= 0.040
v= 0.060
v= 0.080
v= 0.10
v= 0.15
v= 0.20
v= 0.30v= 0.40
v= 0.60v= 0.80v= 1.0
DTU, Department of Energy Engineerings in [kJ/(kg K)]. v in [m^3/kg]. T in [C]M.J. Skovrup & H.J.H Knudsen. 12-05-06
R14 Ref :R.C.Downing. ASHRAE Transactions 1974. Paper No. 2313.
-
Enthalpy [kJ/kg]180 200 220 240 260 280 300 320 340 360 380 400 420 440 460 480 500 520
Pressu
re [Ba
r]
0.050.060.070.080.090.100.10
0.200.300.400.500.600.700.800.901.00
2.003.004.005.006.007.008.009.00
10.00
20.0030.00
s = 1.7
0
s = 1.7
5
s = 1.8
0s =
1.85
s = 1.9
0s =
1.95s =
2.00
s = 1.6
5
s = 1.6
0
-20-20
-10
0
0
10
20
20
30
40
40
50
60
6070
80
8090
100
100110
120
120130
140
140150
160
160170
180
180190
200
200
220
0.0040 0.0050 0.00600.00700.00800.00900.010
0.0150.020
0.0300.0400.0500.0600.0700.0800.0900.10
0.150.20
0.300.400.500.600.700.800.901.0
1.52.0
3.04.0-20
-100
1020
3040
5060
7080
90100
110120
130140
150160
170180 19
0 200
x = 0.10 0.20 0.30 0.40 0.50 0.60 0.70 0.80 0.90s = 1.20 1.40
v= 0.0020
v= 0.0030
v= 0.0040
v= 0.0060
v= 0.0080
v= 0.010
v= 0.015
v= 0.020
v= 0.030
v= 0.040
v= 0.060
v= 0.080
v= 0.10
v= 0.15
v= 0.20
v= 0.30
v= 0.40v= 0.60
v= 0.80v= 1.0
DTU, Department of Energy Engineerings in [kJ/(kg K)]. v in [m^3/kg]. T in [C]M.J. Skovrup & H.J.H Knudsen. 12-05-06
R113 Ref :R.C.Downing. ASHRAE Transactions 1974. Paper No. 2313.
-
Enthalpy [kJ/kg]140 160 180 200 220 240 260 280 300 320 340 360 380 400 420 440 460
Pressu
re [Ba
r]
0.050.060.070.080.090.100.10
0.200.300.400.500.600.700.800.901.00
2.003.004.005.006.007.008.009.00
10.00
20.0030.0040.00
s = 1.6
0
s = 1.6
5s =
1.70
s = 1.75
s = 1.80
s = 1.85
s = 1.90
s = 1.5
5
-50
-40
-40
-30
-20
-20
-10
0
0
10
20
2030
40
4050
60
6070
80
8090
100
100110
120
120130
140
1400.001
50.0020 0.0030 0.0040
0.00500.00600.00700.00800.00900.010
0.0150.020
0.0300.0400.0500.0600.0700.0800.0900.10
0.150.20
0.300.400.500.600.700.800.901.0
1.52.0
3.04.0
-50-40
-30-20
-100
1020
30
40
50
60
70
80
90
100
110
120
130 140
x = 0.10 0.20 0.30 0.40 0.50 0.60 0.70 0.80 0.90s = 1.00 1.20 1.40
v= 0.0020
v= 0.0030
v= 0.0040
v= 0.0060
v= 0.0080
v= 0.010
v= 0.015
v= 0.020
v= 0.030
v= 0.040
v= 0.060
v= 0.080
v= 0.10
v= 0.15v= 0.20
v= 0.30v= 0.40
v= 0.60v= 0.80v= 1.0
DTU, Department of Energy Engineerings in [kJ/(kg K)]. v in [m^3/kg]. T in [C]M.J. Skovrup & H.J.H Knudsen. 12-05-06
R114 Ref :R.C.Downing. ASHRAE Transactions 1974. Paper No. 2313.
-
Enthalpy [kJ/kg]160 180 200 220 240 260 280 300 320 340 360 380 400 420 440 460 480 500 520 540
Pressu
re [Ba
r]
0.050.060.070.080.090.100.10
0.200.300.400.500.600.700.800.901.00
2.003.004.005.006.007.008.009.00
10.00
20.0030.00
s = 1.7
0s =
1.75
s = 1.8
0
s = 1.8
5s =
1.90
s = 1.95
s = 2.00
s = 2.05
s = 2.10
-30
-20
-20
-10
0
0
10
20
20
30
40
4050
60
6070
80
8090
100
100110
120
120130
140
140150
160
160170
180 200
0.0050 0.0060 0.0070 0.00800.00900.010
0.0150.020
0.0300.0400.0500.0600.0700.0800.0900.10
0.150.20
0.300.400.500.600.700.800.901.0
1.52.0
3.04.05.0
-30-20
-100
1020
3040
5060
7080
90100
110120
130
140 150 160 170
x = 0.10 0.20 0.30 0.40 0.50 0.60 0.70 0.80 0.90s = 1.00 1.20 1.40 1.60
v= 0.0020
v= 0.0030
v= 0.0040
v= 0.0060
v= 0.0080
v= 0.010
v= 0.015
v= 0.020
v= 0.030
v= 0.040
v= 0.060
v= 0.080
v= 0.10
v= 0.15
v= 0.20
v= 0.30
v= 0.40
v= 0.60v= 0.80v= 1.0
v= 1.5
DTU, Department of Energy Engineerings in [kJ/(kg K)]. v in [m^3/kg]. T in [C]M.J. Skovrup & H.J.H Knudsen. 12-05-06
R123 Ref :DuPont SUVA 123
-
Enthalpy [kJ/kg]140 160 180 200 220 240 260 280 300 320 340 360 380 400 420 440 460 480 500 520 540 560
Pressu
re [Ba
r]
0.500.600.700.800.901.001.00
2.00
3.00
4.005.006.007.008.009.0010.00
20.00
30.00
40.0050.00
s = 1.7
0
s = 1.7
5s =
1.80
s = 1.8
5s =
1.90
s = 1.9
5s =
2.00
s = 2.0
5s =
2.10
s = 2.1
5s =
2.20
s = 2.2
5
-40-40
-30
-20
-20
-10
0
0
10
20
20
30
40
40
50
60
60
70
80
8090
100
100
120 140 160
0.0015
0.0020
0.0030 0.0040 0.0050 0.00600.00700.00800.00900.010
0.015
0.020
0.030
0.040
0.0500.0600.0700.0800.0900.10
0.15
0.20
0.30
0.40
0.500.60-4
0-30
-20-10
0
10
20
30
40
50
60
70
80
90
100
x = 0.10 0.20 0.30 0.40 0.50 0.60 0.70 0.80 0.90s = 1.00 1.20 1.40 1.60
v= 0.0020
v= 0.0030
v= 0.0040
v= 0.0060
v= 0.0080
v= 0.010
v= 0.015
v= 0.020
v= 0.030
v= 0.040
v= 0.060
v= 0.080
v= 0.10
v= 0.15v= 0.20
DTU, Department of Energy Engineerings in [kJ/(kg K)]. v in [m^3/kg]. T in [C]M.J. Skovrup & H.J.H Knudsen. 12-04-23
R134a Ref :D.P.Wilson & R.S.Basu, ASHRAE Transactions 1988, Vol. 94 part 2.
-
Enthalpy [kJ/kg]125 150 175 200 225 250 275 300 325 350 375 400 425 450 475 500 525 550 575 600 625 650 675 700 725 750 775
Pressu
re [Ba
r]
0.500.600.700.800.901.001.00
2.00
3.00
4.005.006.007.008.009.0010.00
20.00
30.00
s = 2.1
0s =
2.20
s = 2.3
0
s = 2.4
0
s = 2.5
0s =
2.60
s = 2.7
0s =
2.80
s = 2.9
0
-40-40
-30
-20
-20
-10
0
0
10
20
20
30
40
40
50
60
60
70
80
8090
100 120 140 160 180 200
0.00900.010 0.015 0.020
0.030
0.040
0.0500.0600.0700.0800.0900.10
0.15
0.20
0.30
0.40
0.500.600.700.800.901.0-40
-30-20
-100
1020
3040
5060
70
80 90
x = 0.10 0.20 0.30 0.40 0.50 0.60 0.70 0.80 0.90s = 1.00 1.20 1.40 1.60 1.80 2.00
v= 0.003
0
v= 0.004
0
v= 0.0060v= 0.
0080
v= 0.010
v= 0.015
v= 0.020
v= 0.030
v= 0.040
v= 0.060
v= 0.080
v= 0.10
v= 0.15
v= 0.20
v= 0.30
v= 0.40
DTU, Department of Energy Engineerings in [kJ/(kg K)]. v in [m^3/kg]. T in [C]M.J. Skovrup & H.J.H Knudsen. 12-05-06
R152a Ref :ASHRAE Thermodynamic properties of Refrigerants 1986
-
Enthalpy [kJ/kg]-100 -50 0 50 100 150 200 250 300 350 400 450 500 550 600 650 700 750 800 850 900
Pressu
re [Ba
r]
0.500.600.700.800.901.001.00
2.00
3.004.005.006.007.008.009.00
10.00
20.00
30.0040.0050.0060.0070.00
s = 2.0
0s =
2.20
s = 2.4
0s =
2.60
s = 2.80
s = 3.00
s = 3.20
s = 3.40
s = 3.60
s = 3.80
s = 4.00
-100-100
-90
-80
-80
-70
-60
-60
-50
-40
-40
-30
-20
-20
-10
0
010
20
2030
40 60 80 100 120 140 160
0.0030
0.0040
0.0050
0.0060 0.0070 0.0080 0.0090 0.010 0.015
0.020
0.030
0.0400.0500.0600.0700.0800.0900.10
0.15
0.20
0.30
0.400.500.600.700.800.901.0
1.5
2.0-100
-90-80
-70-60
-50-40
-30-20
-10
0
10
20
30
x = 0.10 0.20 0.30 0.40 0.50 0.60 0.70 0.80 0.90s = 0.00 0.20 0.40 0.60 0.80 1.00 1.20 1.40 1.60 1.80 2.00 2.20 2.40
v= 0.0060v= 0.
0080
v= 0.010
v= 0.015
v= 0.020
v= 0.030
v= 0.040
v= 0.060
v= 0.080
v= 0.10
v= 0.15
v= 0.20
v= 0.30
v= 0.40
v= 0.60
DTU, Department of Energy Engineerings in [kJ/(kg K)]. v in [m^3/kg]. T in [C]M.J. Skovrup & H.J.H Knudsen. 12-05-06
R170 Ref :W.C.Reynolds: Thermodynamic properties in SI
-
Enthalpy [kJ/kg]-150 -100 -50 0 50 100 150 200 250 300 350 400 450 500 550 600 650 700
Pressu
re [Ba
r]
0.500.600.700.800.901.001.00
2.00
3.004.005.006.007.008.009.00
10.00
20.00
30.0040.0050.0060.0070.00
s = 1.6
0s =
1.70
s = 1.8
0s =
1.90
s = 2.0
0s =
2.10s =
2.20s =
2.30s =
2.40s =
2.50s =
2.60s =
2.70s =
2.80s =
2.90s =
3.00s =
3.10
s = 3.20
s = 3.30
s = 3.40
s = 3.50
s = 3.60
s = 3.70
-110
-100
-100
-90
-80
-80
-70
-60
-60
-50
-40
-40
-30
-20
-20-10
0
0
20 40 60 80 100
0.0030
0.0040
0.0050
0.0060
0.0070 0.0080 0.0090 0.010 0.015
0.020
0.030
0.0400.0500.0600.0700.0800.0900.10
0.15
0.20
0.30
0.400.500.600.700.800.901.0
1.5
2.0
-110
-100
-90-80
-70-60
-50
-40
-30
-20
-10
0
x = 0.10 0.20 0.30 0.40 0.50 0.60 0.70 0.80 0.90s = -0.20 0.00 0.20 0.40 0.60 0.80 1.00 1.20 1.40 1.60 1.80 2.00 2.20 2.40
v= 0.0060v= 0.0
080
v= 0.010
v= 0.015
v= 0.020
v= 0.030
v= 0.040
v= 0.060
v= 0.080
v= 0.10
v= 0.15
v= 0.20
v= 0.30
v= 0.40
v= 0.60
DTU, Department of Energy Engineerings in [kJ/(kg K)]. v in [m^3/kg]. T in [C]M.J. Skovrup & H.J.H Knudsen. 12-05-06
R1150 Ref :W.C.Reynolds: Thermodynamic properties in SI
-
Enthalpy [kJ/kg]50 100 150 200 250 300 350 400 450 500 550 600 650 700 750 800 850 900 950 1000
Pressu
re [Ba
r]
0.500.600.700.800.901.001.00
2.00
3.004.005.006.007.008.009.00
10.00
20.00
30.0040.0050.0060.0070.00
s = 2.2
0s =
2.30
s = 2.4
0s =
2.50
s = 2.6
0s =
2.70
s = 2.8
0s =
2.90s =
3.00s =
3.10s =
3.20s =
3.30s =
3.40s =
3.50s =
3.60s =
3.70s =
3.80
-60
-60
-50
-40
-40
-30
-20
-20
-10
0
0
10
20
2030
40
4050
60
6070
80
8090
100 120 140 160 180 200
0.0030
0.0040
0.0050 0.0060 0.0070 0.0080 0.0090 0.0100.015
0.020
0.030
0.0400.0500.0600.0700.0800.0900.10
0.15
0.20
0.30
0.400.500.600.700.800.901.0
1.5-60
-50-40
-30-20
-100
1020
3040
50
60
70
80
90
x = 0.10 0.20 0.30 0.40 0.50 0.60 0.70 0.80 0.90s = 0.60 0.80 1.00 1.20 1.40 1.60 1.80 2.00 2.20 2.40
v= 0.0060
v= 0.0080
v= 0.010
v= 0.015
v= 0.020
v= 0.030
v= 0.040
v= 0.060
v= 0.080
v= 0.10
v= 0.15
v= 0.20
v= 0.30
v= 0.40
v= 0.60
DTU, Department of Energy Engineerings in [kJ/(kg K)]. v in [m^3/kg]. T in [C]M.J. Skovrup & H.J.H Knudsen. 12-05-06
R1270 Ref :W.C.Reynolds: Thermodynamic properties in SI
-
Enthalpy [kJ/kg]140 160 180 200 220 240 260 280 300 320 340 360 380 400 420 440 460 480 500 520 540 560 580 600 620
Pressu
re [Ba
r]
0.050.060.070.080.090.100.10
0.200.300.400.500.600.700.800.901.00
2.003.004.005.006.007.008.009.00
10.00
20.00
s = 1.8
5s =
1.90
s = 1.9
5s =
2.00s =
2.05s =
2.10s =
2.15s =
2.20s =
2.25s =
2.30s =
2.35s =
2.40s =
2.45
-40
-40
-30
-20
-20
-10
0
0
10
20
20
30
40
4050
60
6070
80
8090
100
100110
120
120130
140 160 180 200 220 240
0.010 0.0150.020
0.0300.0400.0500.0600.0700.0800.0900.10
0.150.20
0.300.400.500.600.700.800.901.0
1.52.0
3.04.05.06.07.08.0
-40-30
-20-10
010
2030
4050
6070
8090
100110 12
0 130
x = 0.10 0.20 0.30 0.40 0.50 0.60 0.70 0.80 0.90s = 1.00 1.20 1.40 1.60 1.80
v= 0.0020
v= 0.0030
v= 0.0040
v= 0.0060v= 0.00
80v= 0.01
0
v= 0.015
v= 0.020
v= 0.030
v= 0.040
v= 0.060
v= 0.080
v= 0.10
v= 0.15
v= 0.20
v= 0.30
v= 0.40
v= 0.60v= 0.80v= 1.0
v= 1.5v= 2.0
DTU, Department of Energy Engineerings in [kJ/(kg K)]. v in [m^3/kg]. T in [C]M.J. Skovrup & H.J.H Knudsen. 12-05-06
R21 Ref :R.C.Downing. ASHRAE Transactions 1974. Paper No. 2313.
-
Enthalpy [kJ/kg]140 160 180 200 220 240 260 280 300 320 340 360 380 400 420 440 460 480 500 520 540 560
Pressu
re [Ba
r]
0.500.600.700.800.901.001.00
2.00
3.004.005.006.007.008.009.00
10.00
20.00
30.0040.0050.0060.0070.0080.00
s = 1.6
0s =
1.65
s = 1.7
0s =
1.75
s = 1.8
0s =
1.85
s = 1.90
s = 1.95
s = 2.00
s = 2.05
s = 2.10
s = 2.15
s = 2.20
s = 2.25
s = 2.30
-50
-40
-40
-30
-20
-20
-10
0
0
10
20
20
30
40
4050
60
6070
80
8090
100 120 140 160 180 200
0.0015
0.0020
0.0030 0.0040 0.00500.00600.00700.00800.00900.010
0.015
0.020
0.030
0.0400.0500.0600.0700.0800.0900.10
0.15
0.20
0.30
0.400.500.600.700.800.90
-50
-40-30
-20-10
010
2030
40
50
60
70
80
90
x = 0.10 0.20 0.30 0.40 0.50 0.60 0.70 0.80 0.90s = 1.00 1.20 1.40 1.60 1.80
v= 0.0020
v= 0.0030
v= 0.0040
v= 0.0060
v= 0.0080
v= 0.010
v= 0.015
v= 0.020
v= 0.030
v= 0.040
v= 0.060
v= 0.080
v= 0.10
v= 0.15
v= 0.20
v= 0.30
DTU, Department of Energy Engineerings in [kJ/(kg K)]. v in [m^3/kg]. T in [C]M.J. Skovrup & H.J.H Knudsen. 12-04-23
R22 Ref :R.C.Downing. ASHRAE Transactions 1974. Paper No. 2313.
-
Enthalpy [kJ/kg]80 100 120 140 160 180 200 220 240 260 280 300 320 340 360 380 400 420 440 460
Pressu
re [Ba
r]
1.00
2.00
3.00
4.005.006.007.008.009.0010.00
20.00
30.00
40.0050.0060.00
s = 1.5
0
s = 1.6
0s =
1.70
s = 1.8
0s =
1.90s =
2.00s =
2.10s =
2.20
-80
-80
-70
-60
-60
-50
-40
-40
-30
-20
-20
-10
0
0
10
20
20
40 60 80 100
0.0015
0.0020
0.0030
0.0040 0.0050 0.0060 0.00700.00800.00900.010
0.015
0.020
0.030
0.040
0.0500.0600.0700.0800.0900.10
0.15
0.20
0.30
0.40
-80
-70
-60
-50
-40
-30
-20
-10
0
10
20
x = 0.10 0.20 0.30 0.40 0.50 0.60 0.70 0.80 0.90s = 0.60 0.80 1.00 1.20 1.40 1.60
v= 0.0020
v= 0.0030
v= 0.0040
v= 0.0060
v= 0.0080
v= 0.010
v= 0.015
v= 0.020
v= 0.030
v= 0.040
v= 0.060
v= 0.080
v= 0.10
v= 0.15
DTU, Department of Energy Engineerings in [kJ/(kg K)]. v in [m^3/kg]. T in [C]M.J. Skovrup & H.J.H Knudsen. 12-05-06
R23 Ref :R.C.Downing. ASHRAE Transactions 1974. Paper No. 2313.
-
Enthalpy [kJ/kg]50 100 150 200 250 300 350 400 450 500 550 600 650 700 750 800 850 900 950 1000
Pressu
re [Ba
r]
0.500.600.700.800.901.001.00
2.00
3.004.005.006.007.008.009.00
10.00
20.00
30.0040.0050.00
s = 2.3
0s =
2.40
s = 2.5
0s =
2.60
s = 2.7
0s =
2.80
s = 2.9
0s =
3.00
s = 3.1
0s =
3.20
s = 3.30
s = 3.40
s = 3.50
s = 3.60
s = 3.70
-50
-40
-40
-30
-20
-20
-10
0
0
10
20
20
30
40
4050
60
6070
80
8090
100 120 140 160 180 200
0.0040
0.00500.006
00.00700.00800.0090 0.010 0.015
0.020
0.030
0.0400.0500.0600.0700.0800.0900.10
0.15
0.20
0.30
0.400.500.600.700.800.901.0
1.5
-50-40
-30-20
-100
1020
3040
50
60
70
80
90
x = 0.10 0.20 0.30 0.40 0.50 0.60 0.70 0.80 0.90s = 0.80 1.00 1.20 1.40 1.60 1.80 2.00 2.20 2.40
v= 0.0060
v= 0.0080
v= 0.010
v= 0.015
v= 0.020
v= 0.030
v= 0.040
v= 0.060
v= 0.080
v= 0.10
v= 0.15
v= 0.20
v= 0.30
v= 0.40
DTU, Department of Energy Engineerings in [kJ/(kg K)]. v in [m^3/kg]. T in [C]M.J. Skovrup & H.J.H Knudsen. 12-05-06
R290 Ref :W.C.Reynolds: Thermodynamic Properties in SI
-
Enthalpy [kJ/kg]100 150 200 250 300 350 400 450 500 550 600 650 700 750 800 850 900 950 1000 1050 1100
Pressu
re [Ba
r]
0.500.600.700.800.901.001.00
2.00
3.004.005.006.007.008.009.00
10.00
20.00
30.0040.0050.0060.0070.00
s = 3.7
5s =
4.00
s = 4.2
5s =
4.50s =
4.75s =
5.00s =
5.25s =
5.50
s = 5.75
s = 6.00
s = 6.25
s = 6.50
s = 6.75
s = 7.00
s = 7.25
s = 7.50
-160
-160
-150
-140
-140
-130
-120
-120
-110
-100
-100
-90
-80 -60 -40 -20 0 20
0.0040
0.0050
0.0060
0.00700.008
00.00900.010 0.015 0.020
0.030
0.0400.0500.0600.0700.0800.0900.10
0.15
0.20
0.30
0.400.500.600.700.800.901.0
1.5
2.0
3.0
-160
-150
-140
-130
-120
-110
-100
-90
x = 0.10 0.20 0.30 0.40 0.50 0.60 0.70 0.80 0.90s = 1.00 2.00 3.00 4.00 5.00
v= 0.0080v= 0.
010
v= 0.015
v= 0.020
v= 0.030
v= 0.040
v= 0.060
v= 0.080
v= 0.10
v= 0.15
v= 0.20
v= 0.30
v= 0.40
v= 0.60
DTU, Department of Energy Engineerings in [kJ/(kg K)]. v in [m^3/kg]. T in [C]M.J. Skovrup & H.J.H Knudsen. 12-05-06
R50 Ref :W.C.Reynolds: Thermodynamic properties in SI
-
Enthalpy [kJ/kg]120 160 200 240 280 320 360 400 440 480 520 560 600 640 680 720 760 800 840 880
Pressu
re [Ba
r]
0.500.600.700.800.901.001.00
2.00
3.004.005.006.007.008.009.00
10.00
20.00
30.0040.0050.00
s = 2.5
0
s = 2.6
0
s = 2.7
0s =
2.80
s = 2.9
0s =
3.00
s = 3.1
0s =
3.20
s = 2.5
0
-10
0
0
10
20
20
30
40
40
50
60
6070
80
8090
100
100110
120
120130
140
140150
0.0030
0.0040
0.0050 0.0060 0.0070 0.00800.00900.010
0.015
0.020
0.030
0.0400.0500.0600.0700.0800.0900.10
0.15
0.20
0.30
0.400.500.600.700.800.901.0
-100
1020
30
40
50
60
70
80
90
100
110
120
130
140
150
x = 0.10 0.20 0.30 0.40 0.50 0.60 0.70 0.80 0.90s = 1.00 1.20 1.40 1.60 1.80 2.00 2.20
v= 0.0060
v= 0.0080
v= 0.010
v= 0.015
v= 0.020
v= 0.030
v= 0.040
v= 0.060
v= 0.080
v= 0.10
v= 0.15
v= 0.20
v= 0.30
v= 0.40
DTU, Department of Energy Engineerings in [kJ/(kg K)]. v in [m^3/kg]. T in [C]M.J. Skovrup & H.J.H Knudsen. 12-05-06
R600 Ref :W.C.Reynolds: Thermodynamic Properties in SI
-
Enthalpy [kJ/kg]50 100 150 200 250 300 350 400 450 500 550 600 650 700 750 800 850
Pressu
re [Ba
r]
0.20
0.300.400.500.600.700.800.901.001.00
2.00
3.004.005.006.007.008.009.0010.00
20.00
30.0040.0050.00
s = 2.4
0s =
2.50
s = 2.6
0s =
2.70
s = 2.8
0s =
2.90
s = 3.0
0s =
3.10s =
3.20
-40
-40
-30
-20
-20
-10
0
0
10
20
2030
40
4050
60
6070
80
8090
100
100110
120
120130
140
0.0040 0.0050 0.0060 0.0070 0.00800.00900.010
0.0150.020
0.0300.0400.0500.0600.0700.0800.0900.10
0.150.20
0.300.400.500.600.700.800.901.0
1.52.0
3.0
-40-30
-20-10
010
2030
40
50
60
70
80
90
100
110
120
130
x = 0.10 0.20 0.30 0.40 0.50 0.60 0.70 0.80 0.90s = 0.80 1.00 1.20 1.40 1.60 1.80 2.00 2.20
v= 0.0060
v= 0.0080
v= 0.010
v= 0.015
v= 0.020
v= 0.030
v= 0.040
v= 0.060
v= 0.080
v= 0.10
v= 0.15
v= 0.20
v= 0.30
v= 0.40
v= 0.60v= 0.80
v= 1.0
DTU, Department of Energy Engineerings in [kJ/(kg K)]. v in [m^3/kg]. T in [C]M.J. Skovrup & H.J.H Knudsen. 12-05-06
R600a Ref :W.C.Reynolds: Thermodynamic Properties in SI
-
Enthalpy [kJ/kg]-200 0 200 400 600 800 1000 1200 1400 1600 1800 2000 2200 2400 2600 2800 3000 3200
Pressu
re [Ba
r]
0.0050.0060.0070.0080.0090.010
0.0200.0300.0400.0500.0600.0700.0800.0900.100
0.2000.3000.4000.5000.6000.7000.8000.9001.000
2.0003.0004.0005.000
s = 7.20
s = 7.50
s = 7.80
s = 8.10
s = 8.40
s = 8.70
s = 9.00
s = 9.30
s = 9.60
s = 9.90
s = 10.2
0s =
10.50
0
0
20
40
60
80
100
100
120
140
200 300
0.40 0.600.801.0
2.0
4.0
6.08.010
20
40
6080100
200
400
2040
6080
100120
140
x = 0.10 0.20 0.30 0.40 0.50 0.60 0.70 0.80 0.90s = 0.60 1.20 1.80 2.40 3.00 3.60 4.20 4.80 5.40 6.00 6.60 7.20 7.80 8.40
v= 0.040
v= 0.060
v= 0.080v= 0.
10v= 0.20 v= 0.40
v= 0.60
v= 0.80v= 1.0
v= 2.0
v= 4.0
v= 6.0
v= 8.0v= 10
v= 20
v= 40
v= 60v= 80 v= 100
DTU, Department of Energy Engineerings in [kJ/(kg K)]. v in [m^3/kg]. T in [C]M.J. Skovrup & H.J.H Knudsen. 12-05-06
R718 Ref :W.C.Reynolds: Thermodynamic properties in SI
-
Enthalpy [kJ/kg]50 75 100 125 150 175 200 225 250 275 300 325 350 375 400 425 450
Pressu
re [Ba
r]
0.500.600.700.800.901.001.00
2.00
3.004.005.006.007.008.009.00
10.00
20.00
30.0040.0050.0060.0070.00
s = 1.5
0s =
1.60
s = 1.7
0s =
1.80
s = 1.90
s = 2.00
s = 2.10
s = 2.20
s = 2.30
s = 2.40
s = 2.50
s = 2.60
s = 2.70
s = 2.80
s = 2.90
s = 3.00
s = 3.10
s = 3.20
s = 3.30
s = 3.40
s = 3.50
s = 3.60
s = 3.70
-200
-200
-190
-180
-180
-170
-160
-160
-150
-140 -120 -100 -80 -60 -40
0.0020
0.0030
0.0040
0.0050 0.0060 0.0070 0.0080 0.0090 0.010
0.015
0.020
0.030
0.0400.0500.0600.0700.0800.0900.10
0.15
0.20
0.30
0.400.500.600.700.800.901.0-20
0
-190
-180
-170
-160
-150
x = 0.10 0.20 0.30 0.40 0.50 0.60 0.70 0.80 0.90s = 0.00 0.20 0.40 0.60 0.80 1.00 1.20 1.40 1.60 1.80 2.00 2.20 2.40
v= 0.0040
v= 0.0060
v= 0.0080
v= 0.010
v= 0.015
v= 0.020
v= 0.030
v= 0.040
v= 0.060
v= 0.080
v= 0.10
v= 0.15
v= 0.20
v= 0.30
DTU, Department of Energy Engineerings in [kJ/(kg K)]. v in [m^3/kg]. T in [C]M.J. Skovrup & H.J.H Knudsen. 12-05-06
R728 Ref :W.C.Reynolds: Thermodynamic Properties in SI
-
Enthalpy [kJ/kg]75 100 125 150 175 200 225 250 275 300 325 350 375 400 425 450
Pressu
re [Ba
r]
1.00
2.00
3.00
4.005.006.007.008.009.0010.00
20.00
30.00
40.0050.0060.0070.00
s = 1.6
0s =
1.70
s = 1.8
0s =
1.90
s = 2.0
0s =
2.10s =
2.20s =
2.30s =
2.40s =
2.50s =
2.60s =
2.70s =
2.80s =
2.90
s = 3.00
s = 3.10
s = 3.20
s = 3.30
s = 3.40
s = 3.50
-180 -160 -140 -120 -100 -80 -60
0.0020
0.0030
0.0040
0.0050 0.0060 0.0070 0.0080 0.00900.010
0.015
0.020
0.030
0.040
0.0500.0600.0700.0800.0900.10
0.15
0.20
0.30
0.40
0.500.60
-190
-185
-180
-175
-170
-165
-160
-155
-150
-145
2.402.202.001.801.601.401.201.000.800.600.40x = 0.10 0.20 0.30 0.40 0.50 0.60 0.70 0.80 0.90
DTU, Department of Energy Engineerings in [kJ/(kg K)]. v in [m^3/kg]. T in [C]M.J. Skovrup & H.J.H Knudsen. 12-05-06
R729 Ref :W.C.Reynolds: Thermodynamic Properties in SI
-
Enthalpy [kJ/kg]100 150 200 250 300 350 400 450 500 550
Pressu
re [Ba
r]
0.500.600.700.800.901.001.00
2.00
3.004.005.006.007.008.009.00
10.00
20.00
30.0040.0050.0060.0070.00
s = 2.1
0s =
2.20
s = 2.3
0s =
2.40s =
2.50s =
2.60s =
2.70
s = 2.80
s = 2.90
s = 3.00
s = 3.10
s = 3.20
s = 3.30
s = 3.40
s = 3.50
s = 3.60
s = 3.70
s = 3.80
s = 3.90
s = 4.00
-180
-180
-170
-160
-160
-150
-140
-140
-130
-120
-120
-100 -80 -60 -40 -20 0 20
0.0015
0.0020
0.0030
0.0040
0.0050 0.0060 0.0070 0.0080 0.0090 0.010
0.015
0.020
0.030
0.0400.0500.0600.0700.0800.0900.10
0.15
0.20
0.30
0.400.500.600.700.800.901.0
-180
-170
-160
-150
-140
-130
-120
x = 0.10 0.20 0.30 0.40 0.50 0.60 0.70 0.80 0.90s = 0.60 0.80 1.00 1.20 1.40 1.60 1.80 2.00 2.20 2.40 2.60 2.80
v= 0.003
0v= 0.
0040
v= 0.0060
v= 0.0080
v= 0.010
v= 0.015
v= 0.020
v= 0.030
v= 0.040
v= 0.060
v= 0.080
v= 0.10
v= 0.15
v= 0.20
v= 0.30
DTU, Department of Energy Engineerings in [kJ/(kg K)]. v in [m^3/kg]. T in [C]M.J. Skovrup & H.J.H Knudsen. 12-05-06
R732 Ref :W.C.Reynolds: Thermodynamic Properties in SI
-
Enthalpy [kJ/kg]140 160 180 200 220 240 260 280 300 320 340 360 380 400 420
Pressu
re [Ba
r]
1.00
2.00
3.00
4.005.006.007.008.009.0010.00
20.00
30.00
40.0050.0060.0070.00
s = 1.7
0
s = 1.8
0s =
1.90s =
2.00s =
2.10
s = 2.20
s = 2.30
s = 2.40
s = 2.50
s = 2.60
s = 2.70
s = 2.80
s = 2.90
s = 3.00
-180
-180
-170
-160
-160
-150
-140
-140
-130
-120 -100 -80 -60 -40 -20 0
0.0015
0.0020
0.0030
0.0040
0.0050 0.0060 0.0070 0.00800.00900.010
0.015
0.020
0.030
0.040
0.0500.0600.0700.0800.0900.10
0.15
0.20
0.30
0.40
0.50
-180
-170
-160
-150
-140
-130
x = 0.10 0.20 0.30 0.40 0.50 0.60 0.70 0.80 0.90s = 0.80 1.00 1.20 1.40 1.60 1.80 2.00 2.20
v= 0.002
0
v= 0.0030
v= 0.0040
v= 0.0060
v= 0.0080
v= 0.010
v= 0.015
v= 0.020
v= 0.030
v= 0.040
v= 0.060
v= 0.080v= 0.10
DTU, Department of Energy Engineerings in [kJ/(kg K)]. v in [m^3/kg]. T in [C]M.J. Skovrup & H.J.H Knudsen. 12-05-06
R740 Ref :W.C.Reynolds: Thermodynamic Properties in SI
-
Enthalpy [kJ/kg]140 160 180 200 220 240 260 280 300 320 340 360 380 400 420 440 460 480 500 520 540 560 580
Pressu
re [Ba
r]
20.00
30.00
40.00
50.00
60.00
70.00
80.0090.00
100.00 s = 1.4
5s =
1.50
s = 1.5
5s =
1.60
s = 1.6
5s =
1.70
s = 1.7
5s =
1.80
s = 1.8
5s =
1.90
s = 1.9
5s =
2.00
s = 2.0
5s =
2.10
s = 2.1
5s =
2.20
s = 2.2
5s =
2.30
s = 2.3
5
-15
-10
-10
-5
0
0
5
10
10
15
20
20
25
30
30
40 50 60 70 80 90 100 110
0.0015
0.0020
0.0030
0.0040
0.0050
0.0060
0.0070
0.0080
0.0090
0.010
0.015
0.020
0.030-15
-10-5
05
10
15
20
25
30
x = 0.10 0.20 0.30 0.40 0.50 0.60 0.70 0.80 0.90s = 1.00 1.20 1.40 1.60 1.80
v= 0.003
0
v= 0.004
0
v= 0.0060
v= 0.0080
v= 0.010
v= 0.015
DTU, Department of Energy Engineerings in [kJ/(kg K)]. v in [m^3/kg]. T in [C]M.J. Skovrup & H.J.H Knudsen. 12-05-06
R744 Ref :W.C.Reynolds: Thermodynamic Properties in SI
-
Enthalpy [kJ/kg]100 120 140 160 180 200 220 240 260 280 300 320 340 360 380 400 420 440 460 480 500 520 540
Pressu
re [Ba
r]
0.20
0.300.400.500.600.700.800.901.001.00
2.00
3.004.005.006.007.008.009.0010.00
20.00
30.0040.00
s = 1.8
0
s = 1.8
5
s = 1.9
0
s = 1.9
5s =
2.00
s = 2.0
5s =
2.10
s = 1.7
5
s = 1.7
0
s = 1.6
5
s = 1.6
0
s = 1.5
5-30
-20
-20
-10
0
0
10
20
20
30
40
4050
60
6070
80
8090
100
100110
120
0.0015 0.00200.00300.00400.00500.00600.00700.00800.00900.010
0.0150.020
0.0300.0400.0500.0600.0700.0800.0900.10
0.15
0.20
0.30
0.400.500.600.700.80
-30
-20
-10
0
10
20
30
40
50
60
70
80
90
100
110
x = 0.100.20 0.30 0.40 0.50 0.60 0.70 0.80 0.90s = 1.00 1.20
v= 0.0020
v= 0.0030
v= 0.0040
v= 0.0060
v= 0.0080
v= 0.010
v= 0.015
v= 0.020
v= 0.030
v= 0.040
v= 0.060
v= 0.080
v= 0.10
v= 0.15
v= 0.20
v= 0.30
DTU, Department of Energy Engineerings in [kJ/(kg K)]. v in [m^3/kg]. T in [C]M.J. Skovrup & H.J.H Knudsen. 12-05-06
RC318 Ref :R.C.Downing. ASHRAE Transactions 1974. Paper No. 2313.
nh3.pdfr11 trichlorofluoromethane.pdfr12.pdfr13.pdfr14.pdfr113.pdfr114.pdfr123.pdfr134a.pdfr152a.pdfr170.pdfr1150.pdfr1270.pdfr21.pdfr22.pdfr23.pdfr290.pdfr50 methane.pdfr600 butane.pdfr600a isobutane.pdfr718 water.pdfr728 nitrogen.pdfr729 air.pdfr732 oksigen.pdfr740 argon.pdfr744 carbon dioxide.pdfrc318 octafluorocyclobutane.pdf