Operational condition: Pressure, kPa = 100 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of Ethanol (1) - Liquid | Viscosity, Pa*s - Liquid |
293.15 | 0.0000 | 0.0053 |
293.15 | 0.1001 | 0.0047 |
293.15 | 0.2003 | 0.0042 |
293.15 | 0.3004 | 0.0037 |
293.15 | 0.4006 | 0.0032 |
293.15 | 0.4998 | 0.0028 |
293.15 | 0.6009 | 0.0024 |
293.15 | 0.7001 | 0.0020 |
293.15 | 0.7995 | 0.0017 |
293.15 | 0.9001 | 0.0014 |
293.15 | 1.0000 | 0.0011 |
298.15 | 0.0000 | 0.0046 |
298.15 | 0.1001 | 0.0040 |
298.15 | 0.2003 | 0.0036 |
298.15 | 0.3004 | 0.0032 |
298.15 | 0.4006 | 0.0028 |
298.15 | 0.4998 | 0.0024 |
298.15 | 0.6009 | 0.0021 |
298.15 | 0.7001 | 0.0018 |
298.15 | 0.7995 | 0.0015 |
298.15 | 0.9001 | 0.0013 |
298.15 | 1.0000 | 0.0011 |
303.15 | 0.0000 | 0.0039 |
303.15 | 0.1001 | 0.0035 |
303.15 | 0.2003 | 0.0031 |
303.15 | 0.3004 | 0.0028 |
303.15 | 0.4006 | 0.0025 |
303.15 | 0.4998 | 0.0022 |
303.15 | 0.6009 | 0.0019 |
303.15 | 0.7001 | 0.0016 |
303.15 | 0.7995 | 0.0014 |
303.15 | 0.9001 | 0.0012 |
303.15 | 1.0000 | 0.0010 |
308.15 | 0.0000 | 0.0034 |
308.15 | 0.1001 | 0.0030 |
308.15 | 0.2003 | 0.0027 |
308.15 | 0.3004 | 0.0025 |
308.15 | 0.4006 | 0.0022 |
308.15 | 0.4998 | 0.0019 |
308.15 | 0.6009 | 0.0017 |
308.15 | 0.7001 | 0.0015 |
308.15 | 0.7995 | 0.0013 |
308.15 | 0.9001 | 0.0011 |
308.15 | 1.0000 | 0.0009 |
313.15 | 0.0000 | 0.0029 |
313.15 | 0.1001 | 0.0027 |
313.15 | 0.2003 | 0.0024 |
313.15 | 0.3004 | 0.0022 |
313.15 | 0.4006 | 0.0019 |
313.15 | 0.4998 | 0.0017 |
313.15 | 0.6009 | 0.0015 |
313.15 | 0.7001 | 0.0013 |
313.15 | 0.7995 | 0.0011 |
313.15 | 0.9001 | 0.0010 |
313.15 | 1.0000 | 0.0008 |
318.15 | 0.0000 | 0.0025 |
318.15 | 0.1001 | 0.0023 |
318.15 | 0.2003 | 0.0021 |
318.15 | 0.3004 | 0.0019 |
318.15 | 0.4006 | 0.0017 |
318.15 | 0.4998 | 0.0015 |
318.15 | 0.6009 | 0.0014 |
318.15 | 0.7001 | 0.0012 |
318.15 | 0.7995 | 0.0010 |
318.15 | 0.9001 | 0.0009 |
318.15 | 1.0000 | 0.0008 |
323.15 | 0.0000 | 0.0022 |
323.15 | 0.1001 | 0.0021 |
323.15 | 0.2003 | 0.0019 |
323.15 | 0.3004 | 0.0017 |
323.15 | 0.4006 | 0.0015 |
323.15 | 0.4998 | 0.0014 |
323.15 | 0.6009 | 0.0013 |
323.15 | 0.7001 | 0.0011 |
323.15 | 0.7995 | 0.0009 |
323.15 | 0.9001 | 0.0008 |
323.15 | 1.0000 | 0.0007 |
328.15 | 0.0000 | 0.0020 |
328.15 | 0.1001 | 0.0018 |
328.15 | 0.2003 | 0.0017 |
328.15 | 0.3004 | 0.0015 |
328.15 | 0.4006 | 0.0014 |
328.15 | 0.4998 | 0.0013 |
328.15 | 0.6009 | 0.0011 |
328.15 | 0.7001 | 0.0010 |
328.15 | 0.7995 | 0.0009 |
328.15 | 0.9001 | 0.0008 |
328.15 | 1.0000 | 0.0006 |
Operational condition: Pressure, kPa = 100 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of Ethanol (1) - Liquid | Viscosity, Pa*s - Liquid |
293.15 | 0.0000 | 0.0053 |
293.15 | 0.1001 | 0.0047 |
293.15 | 0.2003 | 0.0042 |
293.15 | 0.3004 | 0.0037 |
293.15 | 0.4006 | 0.0032 |
293.15 | 0.4998 | 0.0028 |
293.15 | 0.6009 | 0.0024 |
293.15 | 0.7001 | 0.0020 |
293.15 | 0.7995 | 0.0017 |
293.15 | 0.9001 | 0.0014 |
293.15 | 1.0000 | 0.0011 |
298.15 | 0.0000 | 0.0046 |
298.15 | 0.1001 | 0.0040 |
298.15 | 0.2003 | 0.0036 |
298.15 | 0.3004 | 0.0032 |
298.15 | 0.4006 | 0.0028 |
298.15 | 0.4998 | 0.0024 |
298.15 | 0.6009 | 0.0021 |
298.15 | 0.7001 | 0.0018 |
298.15 | 0.7995 | 0.0015 |
298.15 | 0.9001 | 0.0013 |
298.15 | 1.0000 | 0.0011 |
303.15 | 0.0000 | 0.0039 |
303.15 | 0.1001 | 0.0035 |
303.15 | 0.2003 | 0.0031 |
303.15 | 0.3004 | 0.0028 |
303.15 | 0.4006 | 0.0025 |
303.15 | 0.4998 | 0.0022 |
303.15 | 0.6009 | 0.0019 |
303.15 | 0.7001 | 0.0016 |
303.15 | 0.7995 | 0.0014 |
303.15 | 0.9001 | 0.0012 |
303.15 | 1.0000 | 0.0010 |
308.15 | 0.0000 | 0.0034 |
308.15 | 0.1001 | 0.0030 |
308.15 | 0.2003 | 0.0027 |
308.15 | 0.3004 | 0.0025 |
308.15 | 0.4006 | 0.0022 |
308.15 | 0.4998 | 0.0019 |
308.15 | 0.6009 | 0.0017 |
308.15 | 0.7001 | 0.0015 |
308.15 | 0.7995 | 0.0013 |
308.15 | 0.9001 | 0.0011 |
308.15 | 1.0000 | 0.0009 |
313.15 | 0.0000 | 0.0029 |
313.15 | 0.1001 | 0.0027 |
313.15 | 0.2003 | 0.0024 |
313.15 | 0.3004 | 0.0022 |
313.15 | 0.4006 | 0.0019 |
313.15 | 0.4998 | 0.0017 |
313.15 | 0.6009 | 0.0015 |
313.15 | 0.7001 | 0.0013 |
313.15 | 0.7995 | 0.0011 |
313.15 | 0.9001 | 0.0010 |
313.15 | 1.0000 | 0.0008 |
318.15 | 0.0000 | 0.0025 |
318.15 | 0.1001 | 0.0023 |
318.15 | 0.2003 | 0.0021 |
318.15 | 0.3004 | 0.0019 |
318.15 | 0.4006 | 0.0017 |
318.15 | 0.4998 | 0.0015 |
318.15 | 0.6009 | 0.0014 |
318.15 | 0.7001 | 0.0012 |
318.15 | 0.7995 | 0.0010 |
318.15 | 0.9001 | 0.0009 |
318.15 | 1.0000 | 0.0008 |
323.15 | 0.0000 | 0.0022 |
323.15 | 0.1001 | 0.0021 |
323.15 | 0.2003 | 0.0019 |
323.15 | 0.3004 | 0.0017 |
323.15 | 0.4006 | 0.0015 |
323.15 | 0.4998 | 0.0014 |
323.15 | 0.6009 | 0.0013 |
323.15 | 0.7001 | 0.0011 |
323.15 | 0.7995 | 0.0009 |
323.15 | 0.9001 | 0.0008 |
323.15 | 1.0000 | 0.0007 |
328.15 | 0.0000 | 0.0020 |
328.15 | 0.1001 | 0.0018 |
328.15 | 0.2003 | 0.0017 |
328.15 | 0.3004 | 0.0015 |
328.15 | 0.4006 | 0.0014 |
328.15 | 0.4998 | 0.0013 |
328.15 | 0.6009 | 0.0011 |
328.15 | 0.7001 | 0.0010 |
328.15 | 0.7995 | 0.0009 |
328.15 | 0.9001 | 0.0008 |
328.15 | 1.0000 | 0.0006 |
Operational condition: Pressure, kPa = 100 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of Ethanol (1) - Liquid | Mass density, kg/m3 - Liquid |
293.15 | 0.0000 | 818.9 |
293.15 | 0.1001 | 816.7 |
293.15 | 0.2003 | 815.1 |
293.15 | 0.3004 | 813.3 |
293.15 | 0.4006 | 811.6 |
293.15 | 0.4998 | 808.7 |
293.15 | 0.6009 | 806.0 |
293.15 | 0.7001 | 802.9 |
293.15 | 0.7995 | 799.2 |
293.15 | 0.9001 | 794.9 |
293.15 | 1.0000 | 790.1 |
298.15 | 0.0000 | 815.3 |
298.15 | 0.1001 | 813.1 |
298.15 | 0.2003 | 811.5 |
298.15 | 0.3004 | 809.7 |
298.15 | 0.4006 | 807.9 |
298.15 | 0.4998 | 805.0 |
298.15 | 0.6009 | 802.2 |
298.15 | 0.7001 | 798.9 |
298.15 | 0.7995 | 795.2 |
298.15 | 0.9001 | 790.8 |
298.15 | 1.0000 | 785.9 |
303.15 | 0.0000 | 811.7 |
303.15 | 0.1001 | 809.5 |
303.15 | 0.2003 | 807.8 |
303.15 | 0.3004 | 806.0 |
303.15 | 0.4006 | 804.1 |
303.15 | 0.4998 | 801.2 |
303.15 | 0.6009 | 798.4 |
303.15 | 0.7001 | 795.0 |
303.15 | 0.7995 | 791.2 |
303.15 | 0.9001 | 786.6 |
303.15 | 1.0000 | 781.6 |
308.15 | 0.0000 | 808.1 |
308.15 | 0.1001 | 805.9 |
308.15 | 0.2003 | 804.2 |
308.15 | 0.3004 | 802.3 |
308.15 | 0.4006 | 800.4 |
308.15 | 0.4998 | 797.4 |
308.15 | 0.6009 | 794.5 |
308.15 | 0.7001 | 791.1 |
308.15 | 0.7995 | 787.1 |
308.15 | 0.9001 | 782.5 |
308.15 | 1.0000 | 777.2 |
313.15 | 0.0000 | 804.5 |
313.15 | 0.1001 | 802.2 |
313.15 | 0.2003 | 800.5 |
313.15 | 0.3004 | 798.5 |
313.15 | 0.4006 | 796.6 |
313.15 | 0.4998 | 793.6 |
313.15 | 0.6009 | 790.6 |
313.15 | 0.7001 | 787.1 |
313.15 | 0.7995 | 783.0 |
313.15 | 0.9001 | 778.2 |
313.15 | 1.0000 | 772.9 |
318.15 | 0.0000 | 800.8 |
318.15 | 0.1001 | 798.5 |
318.15 | 0.2003 | 796.7 |
318.15 | 0.3004 | 794.8 |
318.15 | 0.4006 | 792.7 |
318.15 | 0.4998 | 789.7 |
318.15 | 0.6009 | 786.6 |
318.15 | 0.7001 | 783.0 |
318.15 | 0.7995 | 778.9 |
318.15 | 0.9001 | 774.0 |
318.15 | 1.0000 | 768.4 |
323.15 | 0.0000 | 797.1 |
323.15 | 0.1001 | 794.8 |
323.15 | 0.2003 | 793.0 |
323.15 | 0.3004 | 790.9 |
323.15 | 0.4006 | 788.9 |
323.15 | 0.4998 | 785.7 |
323.15 | 0.6009 | 782.6 |
323.15 | 0.7001 | 779.0 |
323.15 | 0.7995 | 774.7 |
323.15 | 0.9001 | 769.7 |
323.15 | 1.0000 | 764.0 |
328.15 | 0.0000 | 793.4 |
328.15 | 0.1001 | 791.0 |
328.15 | 0.2003 | 789.2 |
328.15 | 0.3004 | 787.1 |
328.15 | 0.4006 | 784.9 |
328.15 | 0.4998 | 781.8 |
328.15 | 0.6009 | 778.6 |
328.15 | 0.7001 | 774.8 |
328.15 | 0.7995 | 770.4 |
328.15 | 0.9001 | 765.3 |
328.15 | 1.0000 | 759.4 |
Operational condition: Pressure, kPa = 100 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of Ethanol (1) - Liquid | Mass density, kg/m3 - Liquid |
293.15 | 0.0000 | 818.9 |
293.15 | 0.1001 | 816.7 |
293.15 | 0.2003 | 815.1 |
293.15 | 0.3004 | 813.3 |
293.15 | 0.4006 | 811.6 |
293.15 | 0.4998 | 808.7 |
293.15 | 0.6009 | 806.0 |
293.15 | 0.7001 | 802.9 |
293.15 | 0.7995 | 799.2 |
293.15 | 0.9001 | 794.9 |
293.15 | 1.0000 | 790.1 |
298.15 | 0.0000 | 815.3 |
298.15 | 0.1001 | 813.1 |
298.15 | 0.2003 | 811.5 |
298.15 | 0.3004 | 809.7 |
298.15 | 0.4006 | 807.9 |
298.15 | 0.4998 | 805.0 |
298.15 | 0.6009 | 802.2 |
298.15 | 0.7001 | 798.9 |
298.15 | 0.7995 | 795.2 |
298.15 | 0.9001 | 790.8 |
298.15 | 1.0000 | 785.9 |
303.15 | 0.0000 | 811.7 |
303.15 | 0.1001 | 809.5 |
303.15 | 0.2003 | 807.8 |
303.15 | 0.3004 | 806.0 |
303.15 | 0.4006 | 804.1 |
303.15 | 0.4998 | 801.2 |
303.15 | 0.6009 | 798.4 |
303.15 | 0.7001 | 795.0 |
303.15 | 0.7995 | 791.2 |
303.15 | 0.9001 | 786.6 |
303.15 | 1.0000 | 781.6 |
308.15 | 0.0000 | 808.1 |
308.15 | 0.1001 | 805.9 |
308.15 | 0.2003 | 804.2 |
308.15 | 0.3004 | 802.3 |
308.15 | 0.4006 | 800.4 |
308.15 | 0.4998 | 797.4 |
308.15 | 0.6009 | 794.5 |
308.15 | 0.7001 | 791.1 |
308.15 | 0.7995 | 787.1 |
308.15 | 0.9001 | 782.5 |
308.15 | 1.0000 | 777.2 |
313.15 | 0.0000 | 804.5 |
313.15 | 0.1001 | 802.2 |
313.15 | 0.2003 | 800.5 |
313.15 | 0.3004 | 798.5 |
313.15 | 0.4006 | 796.6 |
313.15 | 0.4998 | 793.6 |
313.15 | 0.6009 | 790.6 |
313.15 | 0.7001 | 787.1 |
313.15 | 0.7995 | 783.0 |
313.15 | 0.9001 | 778.2 |
313.15 | 1.0000 | 772.9 |
318.15 | 0.0000 | 800.8 |
318.15 | 0.1001 | 798.5 |
318.15 | 0.2003 | 796.7 |
318.15 | 0.3004 | 794.8 |
318.15 | 0.4006 | 792.7 |
318.15 | 0.4998 | 789.7 |
318.15 | 0.6009 | 786.6 |
318.15 | 0.7001 | 783.0 |
318.15 | 0.7995 | 778.9 |
318.15 | 0.9001 | 774.0 |
318.15 | 1.0000 | 768.4 |
323.15 | 0.0000 | 797.1 |
323.15 | 0.1001 | 794.8 |
323.15 | 0.2003 | 793.0 |
323.15 | 0.3004 | 790.9 |
323.15 | 0.4006 | 788.9 |
323.15 | 0.4998 | 785.7 |
323.15 | 0.6009 | 782.6 |
323.15 | 0.7001 | 779.0 |
323.15 | 0.7995 | 774.7 |
323.15 | 0.9001 | 769.7 |
323.15 | 1.0000 | 764.0 |
328.15 | 0.0000 | 793.4 |
328.15 | 0.1001 | 791.0 |
328.15 | 0.2003 | 789.2 |
328.15 | 0.3004 | 787.1 |
328.15 | 0.4006 | 784.9 |
328.15 | 0.4998 | 781.8 |
328.15 | 0.6009 | 778.6 |
328.15 | 0.7001 | 774.8 |
328.15 | 0.7995 | 770.4 |
328.15 | 0.9001 | 765.3 |
328.15 | 1.0000 | 759.4 |