Mixture of Ethanol + Propane, 2-methoxy-2-methyl-

Excel

Ethanol

Name
Ethanol
InChI
InChI=1S/C2H6O/c1-2-3/h3H,2H2,1H3
InChI Key
LFQSCWFLJHTTHZ-UHFFFAOYSA-N
Formula
C2H6O
SMILES
CCO
Mol. Weight (g/mol)
46.07
CAS
64-17-5

Propane, 2-methoxy-2-methyl-

Name
Propane, 2-methoxy-2-methyl-
InChI
InChI=1S/C5H12O/c1-5(2,3)6-4/h1-4H3
InChI Key
BZLVMXJERCGZMT-UHFFFAOYSA-N
Formula
C5H12O
SMILES
COC(C)(C)C
Mol. Weight (g/mol)
88.15
CAS
1634-04-4
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Datasets

  1. Azeotropic composition: mole fraction (4)
  2. η - Viscosity, Pa*s (2)
  3. Pc - Critical pressure, kPa (2)
  4. ρl - Mass density, kg/m3 (2)
  5. γ - Surface tension liquid-gas, N/m (2)
  6. Tboil - Boiling temperature at pressure P, K (2)
  7. Tc - Critical temperature, K (2)
  8. Azeotropic temperature, K (2)

Azeotropic composition: mole fraction of Ethanol (1) [ref]

Pressure, kPa - Liquid Azeotropic composition: mole fraction of Ethanol (1) - Liquid
75.00 0.0370
94.00 0.0620

Mole fraction of Ethanol (1) [ref]

Fixed Measured
Mole fraction of Ethanol (1) - Liquid Pressure, kPa - Liquid Mole fraction of Ethanol (1) - Gas
0.0000 50.00 0.0000
0.0000 75.00 0.0000
0.0000 94.00 0.0000
0.0450 94.00 0.0450
0.0460 50.00 0.0390
0.0460 75.00 0.0430
0.0820 94.00 0.0740
0.0830 50.00 0.0630
0.0830 75.00 0.0700
0.1450 50.00 0.0940
0.1530 75.00 0.1090
0.1530 94.00 0.1170
0.2130 50.00 0.1210
0.2160 75.00 0.1370
0.2160 94.00 0.1470
0.2680 50.00 0.1410
0.2710 75.00 0.1590
0.2720 94.00 0.1710
0.3140 50.00 0.1540
0.3140 75.00 0.1740
0.3180 94.00 0.1900
0.3680 50.00 0.1710
0.3680 75.00 0.1910
0.3680 94.00 0.2070
0.4130 50.00 0.1830
0.4160 75.00 0.2080
0.4160 94.00 0.2250
0.4640 50.00 0.2050
0.4710 94.00 0.2450
0.4720 75.00 0.2310
0.5150 50.00 0.2240
0.5160 94.00 0.2630
0.5170 75.00 0.2490
0.5600 50.00 0.2400
0.5610 94.00 0.2860
0.5620 75.00 0.2710
0.6080 50.00 0.2620
0.6080 75.00 0.2910
0.6080 94.00 0.3150
0.6550 50.00 0.2900
0.6590 75.00 0.3230
0.6590 94.00 0.3430
0.7100 50.00 0.3270
0.7140 75.00 0.3620
0.7150 94.00 0.3860
0.7830 50.00 0.3980
0.7940 75.00 0.4430
0.7970 94.00 0.4730
0.8340 50.00 0.4710
0.8380 75.00 0.5120
0.8470 94.00 0.5420
0.8850 50.00 0.5630
0.8890 75.00 0.6090
0.8910 94.00 0.6280
0.9280 94.00 0.7210
0.9290 75.00 0.7080
0.9300 50.00 0.6820
0.9570 75.00 0.7970
0.9570 94.00 0.8100
0.9600 50.00 0.7970
1.0000 50.00 1.0000
1.0000 75.00 1.0000
1.0000 94.00 1.0000

Azeotropic composition: mole fraction of Ethanol (1) [ref]

Pressure, kPa - Liquid Azeotropic composition: mole fraction of Ethanol (1) - Liquid
75.00 0.0370
94.00 0.0620

Mole fraction of Ethanol (1) [ref]

Fixed Measured
Mole fraction of Ethanol (1) - Liquid Pressure, kPa - Liquid Mole fraction of Ethanol (1) - Gas
0.0000 50.00 0.0000
0.0000 75.00 0.0000
0.0000 94.00 0.0000
0.0450 94.00 0.0450
0.0460 50.00 0.0390
0.0460 75.00 0.0430
0.0820 94.00 0.0740
0.0830 50.00 0.0630
0.0830 75.00 0.0700
0.1450 50.00 0.0940
0.1530 75.00 0.1090
0.1530 94.00 0.1170
0.2130 50.00 0.1210
0.2160 75.00 0.1370
0.2160 94.00 0.1470
0.2680 50.00 0.1410
0.2710 75.00 0.1590
0.2720 94.00 0.1710
0.3140 50.00 0.1540
0.3140 75.00 0.1740
0.3180 94.00 0.1900
0.3680 50.00 0.1710
0.3680 75.00 0.1910
0.3680 94.00 0.2070
0.4130 50.00 0.1830
0.4160 75.00 0.2080
0.4160 94.00 0.2250
0.4640 50.00 0.2050
0.4710 94.00 0.2450
0.4720 75.00 0.2310
0.5150 50.00 0.2240
0.5160 94.00 0.2630
0.5170 75.00 0.2490
0.5600 50.00 0.2400
0.5610 94.00 0.2860
0.5620 75.00 0.2710
0.6080 50.00 0.2620
0.6080 75.00 0.2910
0.6080 94.00 0.3150
0.6550 50.00 0.2900
0.6590 75.00 0.3230
0.6590 94.00 0.3430
0.7100 50.00 0.3270
0.7140 75.00 0.3620
0.7150 94.00 0.3860
0.7830 50.00 0.3980
0.7940 75.00 0.4430
0.7970 94.00 0.4730
0.8340 50.00 0.4710
0.8380 75.00 0.5120
0.8470 94.00 0.5420
0.8850 50.00 0.5630
0.8890 75.00 0.6090
0.8910 94.00 0.6280
0.9280 94.00 0.7210
0.9290 75.00 0.7080
0.9300 50.00 0.6820
0.9570 75.00 0.7970
0.9570 94.00 0.8100
0.9600 50.00 0.7970
1.0000 50.00 1.0000
1.0000 75.00 1.0000
1.0000 94.00 1.0000

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Propane, 2-methoxy-2-methyl- (2) - Liquid Viscosity, Pa*s - Liquid
293.15 0.0097 0.0012
293.15 0.0198 0.0011
293.15 0.0301 0.0011
293.15 0.0402 0.0011
293.15 0.0502 0.0011
293.15 0.0583 0.0010
293.15 0.0700 0.0010
293.15 0.0801 0.0010
293.15 0.0861 0.0010
293.15 0.1009 0.0010
293.15 0.1540 0.0009
293.15 0.2006 0.0008
293.15 0.2471 0.0007
293.15 0.2975 0.0007
293.15 0.3487 0.0006
293.15 0.3976 0.0006
293.15 0.4532 0.0005
293.15 0.5007 0.0005
293.15 0.5505 0.0005
293.15 0.5998 0.0005
293.15 0.6484 0.0004
293.15 0.6995 0.0004
293.15 0.7490 0.0004
293.15 0.7995 0.0004
293.15 0.8496 0.0004
293.15 0.9009 0.0004
293.15 0.9093 0.0004
293.15 0.9166 0.0004
293.15 0.9299 0.0004
293.15 0.9398 0.0003
293.15 0.9501 0.0003
293.15 0.9597 0.0003
293.15 0.9680 0.0003
293.15 0.9802 0.0003
293.15 0.9868 0.0003
298.15 0.0097 0.0011
298.15 0.0198 0.0010
298.15 0.0301 0.0010
298.15 0.0402 0.0010
298.15 0.0502 0.0010
298.15 0.0583 0.0010
298.15 0.0700 0.0009
298.15 0.0801 0.0009
298.15 0.0861 0.0009
298.15 0.1009 0.0009
298.15 0.1540 0.0008
298.15 0.2006 0.0007
298.15 0.2471 0.0007
298.15 0.2975 0.0006
298.15 0.3487 0.0006
298.15 0.3976 0.0005
298.15 0.4532 0.0005
298.15 0.5007 0.0005
298.15 0.5505 0.0004
298.15 0.5998 0.0004
298.15 0.6484 0.0004
298.15 0.6995 0.0004
298.15 0.7490 0.0004
298.15 0.7995 0.0004
298.15 0.8496 0.0003
298.15 0.9009 0.0003
298.15 0.9093 0.0003
298.15 0.9166 0.0003
298.15 0.9299 0.0003
298.15 0.9398 0.0003
298.15 0.9501 0.0003
298.15 0.9597 0.0003
298.15 0.9680 0.0003
298.15 0.9802 0.0003
298.15 0.9868 0.0003
303.15 0.0097 0.0010
303.15 0.0198 0.0010
303.15 0.0301 0.0009
303.15 0.0402 0.0009
303.15 0.0502 0.0009
303.15 0.0583 0.0009
303.15 0.0700 0.0009
303.15 0.0801 0.0008
303.15 0.0861 0.0008
303.15 0.1009 0.0008
303.15 0.1540 0.0007
303.15 0.2006 0.0007
303.15 0.2471 0.0006
303.15 0.2975 0.0006
303.15 0.3487 0.0005
303.15 0.3976 0.0005
303.15 0.4532 0.0005
303.15 0.5007 0.0004
303.15 0.5505 0.0004
303.15 0.5998 0.0004
303.15 0.6484 0.0004
303.15 0.6995 0.0004
303.15 0.7490 0.0003
303.15 0.7995 0.0003
303.15 0.8496 0.0003
303.15 0.9009 0.0003
303.15 0.9093 0.0003
303.15 0.9166 0.0003
303.15 0.9299 0.0003
303.15 0.9398 0.0003
303.15 0.9501 0.0003
303.15 0.9597 0.0003
303.15 0.9680 0.0003
303.15 0.9802 0.0003
303.15 0.9868 0.0003
308.15 0.0097 0.0009
308.15 0.0198 0.0009
308.15 0.0301 0.0008
308.15 0.0402 0.0008
308.15 0.0502 0.0008
308.15 0.0583 0.0008
308.15 0.0700 0.0008
308.15 0.0801 0.0008
308.15 0.0861 0.0008
308.15 0.1009 0.0007
308.15 0.1540 0.0007
308.15 0.2006 0.0006
308.15 0.2471 0.0006
308.15 0.2975 0.0005
308.15 0.3487 0.0005
308.15 0.3976 0.0005
308.15 0.4532 0.0004
308.15 0.5007 0.0004
308.15 0.5505 0.0004
308.15 0.5998 0.0004
308.15 0.6484 0.0003
308.15 0.6995 0.0003
308.15 0.7490 0.0003
308.15 0.7995 0.0003
308.15 0.8496 0.0003
308.15 0.9009 0.0003
308.15 0.9093 0.0003
308.15 0.9166 0.0003
308.15 0.9299 0.0003
308.15 0.9398 0.0003
308.15 0.9501 0.0003
308.15 0.9597 0.0003
308.15 0.9680 0.0003
308.15 0.9802 0.0003
308.15 0.9868 0.0003

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Propane, 2-methoxy-2-methyl- (2) - Liquid Viscosity, Pa*s - Liquid
293.15 0.0097 0.0012
293.15 0.0198 0.0011
293.15 0.0301 0.0011
293.15 0.0402 0.0011
293.15 0.0502 0.0011
293.15 0.0583 0.0010
293.15 0.0700 0.0010
293.15 0.0801 0.0010
293.15 0.0861 0.0010
293.15 0.1009 0.0010
293.15 0.1540 0.0009
293.15 0.2006 0.0008
293.15 0.2471 0.0007
293.15 0.2975 0.0007
293.15 0.3487 0.0006
293.15 0.3976 0.0006
293.15 0.4532 0.0005
293.15 0.5007 0.0005
293.15 0.5505 0.0005
293.15 0.5998 0.0005
293.15 0.6484 0.0004
293.15 0.6995 0.0004
293.15 0.7490 0.0004
293.15 0.7995 0.0004
293.15 0.8496 0.0004
293.15 0.9009 0.0004
293.15 0.9093 0.0004
293.15 0.9166 0.0004
293.15 0.9299 0.0004
293.15 0.9398 0.0003
293.15 0.9501 0.0003
293.15 0.9597 0.0003
293.15 0.9680 0.0003
293.15 0.9802 0.0003
293.15 0.9868 0.0003
298.15 0.0097 0.0011
298.15 0.0198 0.0010
298.15 0.0301 0.0010
298.15 0.0402 0.0010
298.15 0.0502 0.0010
298.15 0.0583 0.0010
298.15 0.0700 0.0009
298.15 0.0801 0.0009
298.15 0.0861 0.0009
298.15 0.1009 0.0009
298.15 0.1540 0.0008
298.15 0.2006 0.0007
298.15 0.2471 0.0007
298.15 0.2975 0.0006
298.15 0.3487 0.0006
298.15 0.3976 0.0005
298.15 0.4532 0.0005
298.15 0.5007 0.0005
298.15 0.5505 0.0004
298.15 0.5998 0.0004
298.15 0.6484 0.0004
298.15 0.6995 0.0004
298.15 0.7490 0.0004
298.15 0.7995 0.0004
298.15 0.8496 0.0003
298.15 0.9009 0.0003
298.15 0.9093 0.0003
298.15 0.9166 0.0003
298.15 0.9299 0.0003
298.15 0.9398 0.0003
298.15 0.9501 0.0003
298.15 0.9597 0.0003
298.15 0.9680 0.0003
298.15 0.9802 0.0003
298.15 0.9868 0.0003
303.15 0.0097 0.0010
303.15 0.0198 0.0010
303.15 0.0301 0.0009
303.15 0.0402 0.0009
303.15 0.0502 0.0009
303.15 0.0583 0.0009
303.15 0.0700 0.0009
303.15 0.0801 0.0008
303.15 0.0861 0.0008
303.15 0.1009 0.0008
303.15 0.1540 0.0007
303.15 0.2006 0.0007
303.15 0.2471 0.0006
303.15 0.2975 0.0006
303.15 0.3487 0.0005
303.15 0.3976 0.0005
303.15 0.4532 0.0005
303.15 0.5007 0.0004
303.15 0.5505 0.0004
303.15 0.5998 0.0004
303.15 0.6484 0.0004
303.15 0.6995 0.0004
303.15 0.7490 0.0003
303.15 0.7995 0.0003
303.15 0.8496 0.0003
303.15 0.9009 0.0003
303.15 0.9093 0.0003
303.15 0.9166 0.0003
303.15 0.9299 0.0003
303.15 0.9398 0.0003
303.15 0.9501 0.0003
303.15 0.9597 0.0003
303.15 0.9680 0.0003
303.15 0.9802 0.0003
303.15 0.9868 0.0003
308.15 0.0097 0.0009
308.15 0.0198 0.0009
308.15 0.0301 0.0008
308.15 0.0402 0.0008
308.15 0.0502 0.0008
308.15 0.0583 0.0008
308.15 0.0700 0.0008
308.15 0.0801 0.0008
308.15 0.0861 0.0008
308.15 0.1009 0.0007
308.15 0.1540 0.0007
308.15 0.2006 0.0006
308.15 0.2471 0.0006
308.15 0.2975 0.0005
308.15 0.3487 0.0005
308.15 0.3976 0.0005
308.15 0.4532 0.0004
308.15 0.5007 0.0004
308.15 0.5505 0.0004
308.15 0.5998 0.0004
308.15 0.6484 0.0003
308.15 0.6995 0.0003
308.15 0.7490 0.0003
308.15 0.7995 0.0003
308.15 0.8496 0.0003
308.15 0.9009 0.0003
308.15 0.9093 0.0003
308.15 0.9166 0.0003
308.15 0.9299 0.0003
308.15 0.9398 0.0003
308.15 0.9501 0.0003
308.15 0.9597 0.0003
308.15 0.9680 0.0003
308.15 0.9802 0.0003
308.15 0.9868 0.0003

Critical pressure, kPa [ref]

Mole fraction of Ethanol (1) - Liquid Critical pressure, kPa - Liquid
0.0000 3448.00
0.0620 3586.00
0.1005 3712.00
0.2007 3890.00
0.3011 4110.00
0.4005 4338.00
0.5003 4572.00
0.5997 4820.00
0.7005 5101.00
0.7999 5412.00
0.9000 5774.00
1.0000 6135.00

Critical pressure, kPa [ref]

Mole fraction of Ethanol (1) - Liquid Critical pressure, kPa - Liquid
0.0000 3448.00
0.0620 3586.00
0.1005 3712.00
0.2007 3890.00
0.3011 4110.00
0.4005 4338.00
0.5003 4572.00
0.5997 4820.00
0.7005 5101.00
0.7999 5412.00
0.9000 5774.00
1.0000 6135.00

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Propane, 2-methoxy-2-methyl- (2) - Liquid Mass density, kg/m3 - Liquid
293.15 0.0097 789.03
293.15 0.0198 788.28
293.15 0.0301 787.54
293.15 0.0402 786.85
293.15 0.0502 786.37
293.15 0.0583 785.66
293.15 0.0700 784.87
293.15 0.0801 784.2
293.15 0.0861 783.96
293.15 0.1009 782.99
293.15 0.1540 779.59
293.15 0.2006 776.77
293.15 0.2471 774.06
293.15 0.2975 771.22
293.15 0.3487 768.46
293.15 0.3976 765.94
293.15 0.4532 763.17
293.15 0.5007 760.96
293.15 0.5505 758.76
293.15 0.5998 756.62
293.15 0.6484 754.48
293.15 0.6995 752.35
293.15 0.7490 750.35
293.15 0.7995 748.36
293.15 0.8496 746.44
293.15 0.9009 744.51
293.15 0.9093 744.2
293.15 0.9166 743.9
293.15 0.9299 743.35
293.15 0.9398 742.96
293.15 0.9501 742.54
293.15 0.9597 742.15
293.15 0.9680 741.84
293.15 0.9802 741.35
293.15 0.9868 741.1
298.15 0.0097 784.78
298.15 0.0198 783.99
298.15 0.0301 783.23
298.15 0.0402 782.54
298.15 0.0502 782.01
298.15 0.0583 781.32
298.15 0.0700 780.51
298.15 0.0801 779.82
298.15 0.0861 779.52
298.15 0.1009 778.56
298.15 0.1540 775.08
298.15 0.2006 772.21
298.15 0.2471 769.46
298.15 0.2975 766.56
298.15 0.3487 763.75
298.15 0.3976 761.16
298.15 0.4532 758.36
298.15 0.5007 756.08
298.15 0.5505 753.83
298.15 0.5998 751.67
298.15 0.6484 749.51
298.15 0.6995 747.32
298.15 0.7490 745.3
298.15 0.7995 743.27
298.15 0.8496 741.31
298.15 0.9009 739.34
298.15 0.9093 739.04
298.15 0.9166 738.72
298.15 0.9299 738.18
298.15 0.9398 737.79
298.15 0.9501 737.38
298.15 0.9597 736.97
298.15 0.9680 736.66
298.15 0.9802 736.15
298.15 0.9868 735.92
303.15 0.0097 780.44
303.15 0.0198 779.64
303.15 0.0301 778.87
303.15 0.0402 778.16
303.15 0.0502 777.63
303.15 0.0583 776.91
303.15 0.0700 776.08
303.15 0.0801 775.37
303.15 0.0861 775.09
303.15 0.1009 774.11
303.15 0.1540 770.56
303.15 0.2006 767.62
303.15 0.2471 764.79
303.15 0.2975 761.83
303.15 0.3487 758.96
303.15 0.3976 756.32
303.15 0.4532 753.45
303.15 0.5007 751.15
303.15 0.5505 748.85
303.15 0.5998 746.63
303.15 0.6484 744.43
303.15 0.6995 742.19
303.15 0.7490 740.14
303.15 0.7995 738.06
303.15 0.8496 736.08
303.15 0.9009 734.07
303.15 0.9093 733.77
303.15 0.9166 733.47
303.15 0.9299 732.9
303.15 0.9398 732.51
303.15 0.9501 732.09
303.15 0.9597 731.71
303.15 0.9680 731.37
303.15 0.9802 730.87
303.15 0.9868 730.61
308.15 0.0097 776.08
308.15 0.0198 775.26
308.15 0.0301 774.47
308.15 0.0402 773.74
308.15 0.0502 773.2
308.15 0.0583 772.46
308.15 0.0700 771.61
308.15 0.0801 770.89
308.15 0.0861 770.6
308.15 0.1009 769.6
308.15 0.1540 765.97
308.15 0.2006 762.96
308.15 0.2471 760.08
308.15 0.2975 757.06
308.15 0.3487 754.12
308.15 0.3976 751.43
308.15 0.4532 748.5
308.15 0.5007 746.15
308.15 0.5505 743.8
308.15 0.5998 741.53
308.15 0.6484 739.29
308.15 0.6995 737.0
308.15 0.7490 734.91
308.15 0.7995 732.8
308.15 0.8496 730.78
308.15 0.9009 728.75
308.15 0.9093 728.45
308.15 0.9166 728.14
308.15 0.9299 727.57
308.15 0.9398 727.17
308.15 0.9501 726.76
308.15 0.9597 726.36
308.15 0.9680 726.03
308.15 0.9802 725.52
308.15 0.9868 725.26

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Propane, 2-methoxy-2-methyl- (2) - Liquid Mass density, kg/m3 - Liquid
293.15 0.0097 789.03
293.15 0.0198 788.28
293.15 0.0301 787.54
293.15 0.0402 786.85
293.15 0.0502 786.37
293.15 0.0583 785.66
293.15 0.0700 784.87
293.15 0.0801 784.2
293.15 0.0861 783.96
293.15 0.1009 782.99
293.15 0.1540 779.59
293.15 0.2006 776.77
293.15 0.2471 774.06
293.15 0.2975 771.22
293.15 0.3487 768.46
293.15 0.3976 765.94
293.15 0.4532 763.17
293.15 0.5007 760.96
293.15 0.5505 758.76
293.15 0.5998 756.62
293.15 0.6484 754.48
293.15 0.6995 752.35
293.15 0.7490 750.35
293.15 0.7995 748.36
293.15 0.8496 746.44
293.15 0.9009 744.51
293.15 0.9093 744.2
293.15 0.9166 743.9
293.15 0.9299 743.35
293.15 0.9398 742.96
293.15 0.9501 742.54
293.15 0.9597 742.15
293.15 0.9680 741.84
293.15 0.9802 741.35
293.15 0.9868 741.1
298.15 0.0097 784.78
298.15 0.0198 783.99
298.15 0.0301 783.23
298.15 0.0402 782.54
298.15 0.0502 782.01
298.15 0.0583 781.32
298.15 0.0700 780.51
298.15 0.0801 779.82
298.15 0.0861 779.52
298.15 0.1009 778.56
298.15 0.1540 775.08
298.15 0.2006 772.21
298.15 0.2471 769.46
298.15 0.2975 766.56
298.15 0.3487 763.75
298.15 0.3976 761.16
298.15 0.4532 758.36
298.15 0.5007 756.08
298.15 0.5505 753.83
298.15 0.5998 751.67
298.15 0.6484 749.51
298.15 0.6995 747.32
298.15 0.7490 745.3
298.15 0.7995 743.27
298.15 0.8496 741.31
298.15 0.9009 739.34
298.15 0.9093 739.04
298.15 0.9166 738.72
298.15 0.9299 738.18
298.15 0.9398 737.79
298.15 0.9501 737.38
298.15 0.9597 736.97
298.15 0.9680 736.66
298.15 0.9802 736.15
298.15 0.9868 735.92
303.15 0.0097 780.44
303.15 0.0198 779.64
303.15 0.0301 778.87
303.15 0.0402 778.16
303.15 0.0502 777.63
303.15 0.0583 776.91
303.15 0.0700 776.08
303.15 0.0801 775.37
303.15 0.0861 775.09
303.15 0.1009 774.11
303.15 0.1540 770.56
303.15 0.2006 767.62
303.15 0.2471 764.79
303.15 0.2975 761.83
303.15 0.3487 758.96
303.15 0.3976 756.32
303.15 0.4532 753.45
303.15 0.5007 751.15
303.15 0.5505 748.85
303.15 0.5998 746.63
303.15 0.6484 744.43
303.15 0.6995 742.19
303.15 0.7490 740.14
303.15 0.7995 738.06
303.15 0.8496 736.08
303.15 0.9009 734.07
303.15 0.9093 733.77
303.15 0.9166 733.47
303.15 0.9299 732.9
303.15 0.9398 732.51
303.15 0.9501 732.09
303.15 0.9597 731.71
303.15 0.9680 731.37
303.15 0.9802 730.87
303.15 0.9868 730.61
308.15 0.0097 776.08
308.15 0.0198 775.26
308.15 0.0301 774.47
308.15 0.0402 773.74
308.15 0.0502 773.2
308.15 0.0583 772.46
308.15 0.0700 771.61
308.15 0.0801 770.89
308.15 0.0861 770.6
308.15 0.1009 769.6
308.15 0.1540 765.97
308.15 0.2006 762.96
308.15 0.2471 760.08
308.15 0.2975 757.06
308.15 0.3487 754.12
308.15 0.3976 751.43
308.15 0.4532 748.5
308.15 0.5007 746.15
308.15 0.5505 743.8
308.15 0.5998 741.53
308.15 0.6484 739.29
308.15 0.6995 737.0
308.15 0.7490 734.91
308.15 0.7995 732.8
308.15 0.8496 730.78
308.15 0.9009 728.75
308.15 0.9093 728.45
308.15 0.9166 728.14
308.15 0.9299 727.57
308.15 0.9398 727.17
308.15 0.9501 726.76
308.15 0.9597 726.36
308.15 0.9680 726.03
308.15 0.9802 725.52
308.15 0.9868 725.26

Surface tension liquid-gas, N/m [ref]

Operational condition: Temperature, K = 303.15 (Liquid)

Mole fraction of Ethanol (1) - Liquid Surface tension liquid-gas, N/m - Liquid
0.1020 0.0184
0.2120 0.0184
0.3100 0.0185
0.4080 0.0188
0.5270 0.0190
0.6230 0.0192
0.7210 0.0196
0.8260 0.0200

Surface tension liquid-gas, N/m [ref]

Operational condition: Temperature, K = 303.15 (Liquid)

Mole fraction of Ethanol (1) - Liquid Surface tension liquid-gas, N/m - Liquid
0.1020 0.0184
0.2120 0.0184
0.3100 0.0185
0.4080 0.0188
0.5270 0.0190
0.6230 0.0192
0.7210 0.0196
0.8260 0.0200

Boiling temperature at pressure P, K [ref]

Fixed Measured
Mole fraction of Ethanol (1) - Liquid Pressure, kPa - Liquid Boiling temperature at pressure P, K - Liquid
0.0000 50.00 308.30
0.0000 75.00 319.39
0.0000 94.00 325.98
0.0450 94.00 325.88
0.0460 50.00 308.40
0.0460 75.00 319.37
0.0820 94.00 325.92
0.0830 50.00 308.58
0.0830 75.00 319.47
0.1450 50.00 308.96
0.1530 75.00 319.79
0.1530 94.00 326.16
0.2130 50.00 309.47
0.2160 75.00 320.18
0.2160 94.00 326.53
0.2680 50.00 309.94
0.2710 75.00 320.66
0.2720 94.00 326.86
0.3140 50.00 310.41
0.3140 75.00 320.64
0.3180 94.00 327.15
0.3680 50.00 310.93
0.3680 75.00 320.92
0.3680 94.00 327.25
0.4130 50.00 311.26
0.4160 75.00 321.40
0.4160 94.00 328.29
0.4640 50.00 312.14
0.4710 94.00 328.70
0.4720 75.00 322.80
0.5150 50.00 312.90
0.5160 94.00 329.42
0.5170 75.00 323.42
0.5600 50.00 313.62
0.5610 94.00 329.90
0.5620 75.00 324.14
0.6080 50.00 314.44
0.6080 75.00 324.53
0.6080 94.00 331.27
0.6550 50.00 315.54
0.6590 75.00 326.14
0.6590 94.00 332.32
0.7100 50.00 316.99
0.7140 75.00 327.54
0.7150 94.00 333.75
0.7830 50.00 319.54
0.7940 75.00 329.79
0.7970 94.00 336.14
0.8340 50.00 321.92
0.8380 75.00 332.22
0.8470 94.00 338.76
0.8850 50.00 324.74
0.8890 75.00 334.68
0.8910 94.00 340.65
0.9280 94.00 343.32
0.9290 75.00 337.38
0.9300 50.00 327.90
0.9570 75.00 339.48
0.9570 94.00 345.39
0.9600 50.00 330.45
1.0000 50.00 334.57
1.0000 75.00 344.02
1.0000 94.00 349.56

Boiling temperature at pressure P, K [ref]

Fixed Measured
Mole fraction of Ethanol (1) - Liquid Pressure, kPa - Liquid Boiling temperature at pressure P, K - Liquid
0.0000 50.00 308.30
0.0000 75.00 319.39
0.0000 94.00 325.98
0.0450 94.00 325.88
0.0460 50.00 308.40
0.0460 75.00 319.37
0.0820 94.00 325.92
0.0830 50.00 308.58
0.0830 75.00 319.47
0.1450 50.00 308.96
0.1530 75.00 319.79
0.1530 94.00 326.16
0.2130 50.00 309.47
0.2160 75.00 320.18
0.2160 94.00 326.53
0.2680 50.00 309.94
0.2710 75.00 320.66
0.2720 94.00 326.86
0.3140 50.00 310.41
0.3140 75.00 320.64
0.3180 94.00 327.15
0.3680 50.00 310.93
0.3680 75.00 320.92
0.3680 94.00 327.25
0.4130 50.00 311.26
0.4160 75.00 321.40
0.4160 94.00 328.29
0.4640 50.00 312.14
0.4710 94.00 328.70
0.4720 75.00 322.80
0.5150 50.00 312.90
0.5160 94.00 329.42
0.5170 75.00 323.42
0.5600 50.00 313.62
0.5610 94.00 329.90
0.5620 75.00 324.14
0.6080 50.00 314.44
0.6080 75.00 324.53
0.6080 94.00 331.27
0.6550 50.00 315.54
0.6590 75.00 326.14
0.6590 94.00 332.32
0.7100 50.00 316.99
0.7140 75.00 327.54
0.7150 94.00 333.75
0.7830 50.00 319.54
0.7940 75.00 329.79
0.7970 94.00 336.14
0.8340 50.00 321.92
0.8380 75.00 332.22
0.8470 94.00 338.76
0.8850 50.00 324.74
0.8890 75.00 334.68
0.8910 94.00 340.65
0.9280 94.00 343.32
0.9290 75.00 337.38
0.9300 50.00 327.90
0.9570 75.00 339.48
0.9570 94.00 345.39
0.9600 50.00 330.45
1.0000 50.00 334.57
1.0000 75.00 344.02
1.0000 94.00 349.56

Critical temperature, K [ref]

Mole fraction of Ethanol (1) - Liquid Critical temperature, K - Liquid
0.0000 497.00
0.0620 495.00
0.1005 494.60
0.2007 493.80
0.3011 493.30
0.4005 493.90
0.5003 495.00
0.5997 497.10
0.7005 499.50
0.7999 503.50
0.9000 508.10
1.0000 514.20

Critical temperature, K [ref]

Mole fraction of Ethanol (1) - Liquid Critical temperature, K - Liquid
0.0000 497.00
0.0620 495.00
0.1005 494.60
0.2007 493.80
0.3011 493.30
0.4005 493.90
0.5003 495.00
0.5997 497.10
0.7005 499.50
0.7999 503.50
0.9000 508.10
1.0000 514.20

Azeotropic temperature, K [ref]

Pressure, kPa - Liquid Azeotropic temperature, K - Liquid
75.00 319.32
94.00 325.77

Azeotropic temperature, K [ref]

Pressure, kPa - Liquid Azeotropic temperature, K - Liquid
75.00 319.32
94.00 325.77

Sources