Refrigeration Graphic (Coolpack)

27
Enthalpy [kJ/kg] 0 100 200 300 400 500 600 700 800 900 1000 1100 1200 1300 1400 1500 1600 1700 1800 1900 2000 Pressure [Bar] 0.50 0.60 0.70 0.80 0.90 1.00 2.00 3.00 4.00 5.00 6.00 7.00 8.00 9.00 10.00 20.00 30.00 40.00 50.00 60.00 70.00 80.00 90.00 100.00 200.00 s = 3.75 s = 4.00 s = 4.25 s = 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 40 50 60 60 70 80 80 90 100 100 110 120 120 130 140 160 180 200 220 0.0030 0.0040 0.0050 0.0060 0.0070 0.0080 0.0090 0.010 0.015 0.020 0.030 0.040 0.050 0.060 0.070 0.080 0.090 0.10 0.15 0.20 0.30 0.40 0.50 0.60 0.70 0.80 0.90 1.0 1.5 2.0 3.0 4.0 -40 -30 -20 -10 0 10 20 30 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 0.90 s = 1.00 2.00 3.00 4.00 5.00 6.00 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 v= 0.80 v= 1.0 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. 12-04-23 R717 Ref :R.Döring. Klima+Kälte ingenieur Ki-Extra 5, 1978

description

Coolpack graphic

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