Operational condition: Pressure, kPa = 101 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of Eucalyptol (2) - Liquid | Molar heat capacity at constant pressure, J/K/mol - Liquid |
278.15 | 0.0000 | 246.17 |
278.15 | 0.1046 | 246.20 |
278.15 | 0.1990 | 246.45 |
278.15 | 0.2987 | 246.89 |
278.15 | 0.4008 | 247.59 |
278.15 | 0.4955 | 248.46 |
278.15 | 0.5939 | 249.62 |
278.15 | 0.6971 | 250.95 |
278.15 | 0.7985 | 252.64 |
278.15 | 0.8939 | 254.30 |
278.15 | 1.0000 | 256.14 |
298.15 | 0.0000 | 253.89 |
298.15 | 0.1046 | 254.53 |
298.15 | 0.1990 | 255.32 |
298.15 | 0.2987 | 256.22 |
298.15 | 0.4008 | 257.36 |
298.15 | 0.4955 | 258.59 |
298.15 | 0.5939 | 260.07 |
298.15 | 0.6971 | 261.75 |
298.15 | 0.7985 | 263.66 |
298.15 | 0.8939 | 265.57 |
298.15 | 1.0000 | 267.69 |
318.15 | 0.0000 | 262.16 |
318.15 | 0.1046 | 263.19 |
318.15 | 0.1990 | 264.31 |
318.15 | 0.2987 | 265.53 |
318.15 | 0.4008 | 267.00 |
318.15 | 0.4955 | 268.51 |
318.15 | 0.5939 | 270.26 |
318.15 | 0.6971 | 272.14 |
318.15 | 0.7985 | 274.24 |
318.15 | 0.8939 | 276.39 |
318.15 | 1.0000 | 278.65 |
338.15 | 0.0000 | 270.96 |
338.15 | 0.1046 | 272.35 |
338.15 | 0.1990 | 273.81 |
338.15 | 0.2987 | 275.37 |
338.15 | 0.4008 | 277.18 |
338.15 | 0.4955 | 278.93 |
338.15 | 0.5939 | 280.96 |
338.15 | 0.6971 | 283.13 |
338.15 | 0.7985 | 285.45 |
338.15 | 0.8939 | 287.81 |
338.15 | 1.0000 | 290.33 |
Operational condition: Pressure, kPa = 101 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of Eucalyptol (2) - Liquid | Molar heat capacity at constant pressure, J/K/mol - Liquid |
278.15 | 0.0000 | 246.17 |
278.15 | 0.1046 | 246.20 |
278.15 | 0.1990 | 246.45 |
278.15 | 0.2987 | 246.89 |
278.15 | 0.4008 | 247.59 |
278.15 | 0.4955 | 248.46 |
278.15 | 0.5939 | 249.62 |
278.15 | 0.6971 | 250.95 |
278.15 | 0.7985 | 252.64 |
278.15 | 0.8939 | 254.30 |
278.15 | 1.0000 | 256.14 |
298.15 | 0.0000 | 253.89 |
298.15 | 0.1046 | 254.53 |
298.15 | 0.1990 | 255.32 |
298.15 | 0.2987 | 256.22 |
298.15 | 0.4008 | 257.36 |
298.15 | 0.4955 | 258.59 |
298.15 | 0.5939 | 260.07 |
298.15 | 0.6971 | 261.75 |
298.15 | 0.7985 | 263.66 |
298.15 | 0.8939 | 265.57 |
298.15 | 1.0000 | 267.69 |
318.15 | 0.0000 | 262.16 |
318.15 | 0.1046 | 263.19 |
318.15 | 0.1990 | 264.31 |
318.15 | 0.2987 | 265.53 |
318.15 | 0.4008 | 267.00 |
318.15 | 0.4955 | 268.51 |
318.15 | 0.5939 | 270.26 |
318.15 | 0.6971 | 272.14 |
318.15 | 0.7985 | 274.24 |
318.15 | 0.8939 | 276.39 |
318.15 | 1.0000 | 278.65 |
338.15 | 0.0000 | 270.96 |
338.15 | 0.1046 | 272.35 |
338.15 | 0.1990 | 273.81 |
338.15 | 0.2987 | 275.37 |
338.15 | 0.4008 | 277.18 |
338.15 | 0.4955 | 278.93 |
338.15 | 0.5939 | 280.96 |
338.15 | 0.6971 | 283.13 |
338.15 | 0.7985 | 285.45 |
338.15 | 0.8939 | 287.81 |
338.15 | 1.0000 | 290.33 |
Operational condition: Pressure, kPa = 101 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of Eucalyptol (2) - Liquid | Viscosity, Pa*s - Liquid |
278.15 | 0.0000 | 0.0007 |
278.15 | 0.1046 | 0.0008 |
278.15 | 0.1990 | 0.0009 |
278.15 | 0.2987 | 0.0010 |
278.15 | 0.4008 | 0.0012 |
278.15 | 0.4955 | 0.0014 |
278.15 | 0.5939 | 0.0016 |
278.15 | 0.6971 | 0.0020 |
278.15 | 0.7985 | 0.0025 |
278.15 | 0.8939 | 0.0031 |
278.15 | 1.0000 | 0.0042 |
298.15 | 0.0000 | 0.0005 |
298.15 | 0.1046 | 0.0006 |
298.15 | 0.1990 | 0.0007 |
298.15 | 0.2987 | 0.0008 |
298.15 | 0.4008 | 0.0009 |
298.15 | 0.4955 | 0.0010 |
298.15 | 0.5939 | 0.0011 |
298.15 | 0.6971 | 0.0014 |
298.15 | 0.7985 | 0.0016 |
298.15 | 0.8939 | 0.0020 |
298.15 | 1.0000 | 0.0026 |
318.15 | 0.0000 | 0.0004 |
318.15 | 0.1046 | 0.0005 |
318.15 | 0.1990 | 0.0005 |
318.15 | 0.2987 | 0.0006 |
318.15 | 0.4008 | 0.0007 |
318.15 | 0.4955 | 0.0007 |
318.15 | 0.5939 | 0.0008 |
318.15 | 0.6971 | 0.0010 |
318.15 | 0.7985 | 0.0012 |
318.15 | 0.8939 | 0.0014 |
318.15 | 1.0000 | 0.0017 |
338.15 | 0.0000 | 0.0004 |
338.15 | 0.1046 | 0.0004 |
338.15 | 0.1990 | 0.0004 |
338.15 | 0.2987 | 0.0005 |
338.15 | 0.4008 | 0.0005 |
338.15 | 0.4955 | 0.0006 |
338.15 | 0.5939 | 0.0007 |
338.15 | 0.6971 | 0.0008 |
338.15 | 0.7985 | 0.0009 |
338.15 | 0.8939 | 0.0010 |
338.15 | 1.0000 | 0.0013 |
Operational condition: Pressure, kPa = 101 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of Eucalyptol (2) - Liquid | Viscosity, Pa*s - Liquid |
278.15 | 0.0000 | 0.0007 |
278.15 | 0.1046 | 0.0008 |
278.15 | 0.1990 | 0.0009 |
278.15 | 0.2987 | 0.0010 |
278.15 | 0.4008 | 0.0012 |
278.15 | 0.4955 | 0.0014 |
278.15 | 0.5939 | 0.0016 |
278.15 | 0.6971 | 0.0020 |
278.15 | 0.7985 | 0.0025 |
278.15 | 0.8939 | 0.0031 |
278.15 | 1.0000 | 0.0042 |
298.15 | 0.0000 | 0.0005 |
298.15 | 0.1046 | 0.0006 |
298.15 | 0.1990 | 0.0007 |
298.15 | 0.2987 | 0.0008 |
298.15 | 0.4008 | 0.0009 |
298.15 | 0.4955 | 0.0010 |
298.15 | 0.5939 | 0.0011 |
298.15 | 0.6971 | 0.0014 |
298.15 | 0.7985 | 0.0016 |
298.15 | 0.8939 | 0.0020 |
298.15 | 1.0000 | 0.0026 |
318.15 | 0.0000 | 0.0004 |
318.15 | 0.1046 | 0.0005 |
318.15 | 0.1990 | 0.0005 |
318.15 | 0.2987 | 0.0006 |
318.15 | 0.4008 | 0.0007 |
318.15 | 0.4955 | 0.0007 |
318.15 | 0.5939 | 0.0008 |
318.15 | 0.6971 | 0.0010 |
318.15 | 0.7985 | 0.0012 |
318.15 | 0.8939 | 0.0014 |
318.15 | 1.0000 | 0.0017 |
338.15 | 0.0000 | 0.0004 |
338.15 | 0.1046 | 0.0004 |
338.15 | 0.1990 | 0.0004 |
338.15 | 0.2987 | 0.0005 |
338.15 | 0.4008 | 0.0005 |
338.15 | 0.4955 | 0.0006 |
338.15 | 0.5939 | 0.0007 |
338.15 | 0.6971 | 0.0008 |
338.15 | 0.7985 | 0.0009 |
338.15 | 0.8939 | 0.0010 |
338.15 | 1.0000 | 0.0013 |
Operational condition: Pressure, kPa = 101 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of Eucalyptol (2) - Liquid | Mass density, kg/m3 - Liquid |
278.15 | 0.0000 | 714.55 |
278.15 | 0.1046 | 738.47 |
278.15 | 0.1990 | 759.76 |
278.15 | 0.2987 | 782.16 |
278.15 | 0.4008 | 805.03 |
278.15 | 0.4955 | 826.13 |
278.15 | 0.5939 | 847.98 |
278.15 | 0.6971 | 870.82 |
278.15 | 0.7985 | 893.16 |
278.15 | 0.8939 | 914.06 |
278.15 | 1.0000 | 937.25 |
298.15 | 0.0000 | 698.51 |
298.15 | 0.1046 | 722.35 |
298.15 | 0.1990 | 743.56 |
298.15 | 0.2987 | 765.86 |
298.15 | 0.4008 | 788.62 |
298.15 | 0.4955 | 809.62 |
298.15 | 0.5939 | 831.35 |
298.15 | 0.6971 | 854.05 |
298.15 | 0.7985 | 876.24 |
298.15 | 0.8939 | 897.03 |
298.15 | 1.0000 | 920.04 |
318.15 | 0.0000 | 682.19 |
318.15 | 0.1046 | 705.93 |
318.15 | 0.1990 | 727.08 |
318.15 | 0.2987 | 749.32 |
318.15 | 0.4008 | 772.01 |
318.15 | 0.4955 | 792.93 |
318.15 | 0.5939 | 814.56 |
318.15 | 0.6971 | 837.17 |
318.15 | 0.7985 | 859.26 |
318.15 | 0.8939 | 879.92 |
318.15 | 1.0000 | 902.84 |
338.15 | 0.0000 | 665.43 |
338.15 | 0.1046 | 689.16 |
338.15 | 0.1990 | 710.27 |
338.15 | 0.2987 | 732.46 |
338.15 | 0.4008 | 755.1 |
338.15 | 0.4955 | 775.96 |
338.15 | 0.5939 | 797.55 |
338.15 | 0.6971 | 820.1 |
338.15 | 0.7985 | 842.12 |
338.15 | 0.8939 | 862.72 |
338.15 | 1.0000 | 885.57 |
Operational condition: Pressure, kPa = 101 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of Eucalyptol (2) - Liquid | Mass density, kg/m3 - Liquid |
278.15 | 0.0000 | 714.55 |
278.15 | 0.1046 | 738.47 |
278.15 | 0.1990 | 759.76 |
278.15 | 0.2987 | 782.16 |
278.15 | 0.4008 | 805.03 |
278.15 | 0.4955 | 826.13 |
278.15 | 0.5939 | 847.98 |
278.15 | 0.6971 | 870.82 |
278.15 | 0.7985 | 893.16 |
278.15 | 0.8939 | 914.06 |
278.15 | 1.0000 | 937.25 |
298.15 | 0.0000 | 698.51 |
298.15 | 0.1046 | 722.35 |
298.15 | 0.1990 | 743.56 |
298.15 | 0.2987 | 765.86 |
298.15 | 0.4008 | 788.62 |
298.15 | 0.4955 | 809.62 |
298.15 | 0.5939 | 831.35 |
298.15 | 0.6971 | 854.05 |
298.15 | 0.7985 | 876.24 |
298.15 | 0.8939 | 897.03 |
298.15 | 1.0000 | 920.04 |
318.15 | 0.0000 | 682.19 |
318.15 | 0.1046 | 705.93 |
318.15 | 0.1990 | 727.08 |
318.15 | 0.2987 | 749.32 |
318.15 | 0.4008 | 772.01 |
318.15 | 0.4955 | 792.93 |
318.15 | 0.5939 | 814.56 |
318.15 | 0.6971 | 837.17 |
318.15 | 0.7985 | 859.26 |
318.15 | 0.8939 | 879.92 |
318.15 | 1.0000 | 902.84 |
338.15 | 0.0000 | 665.43 |
338.15 | 0.1046 | 689.16 |
338.15 | 0.1990 | 710.27 |
338.15 | 0.2987 | 732.46 |
338.15 | 0.4008 | 755.1 |
338.15 | 0.4955 | 775.96 |
338.15 | 0.5939 | 797.55 |
338.15 | 0.6971 | 820.1 |
338.15 | 0.7985 | 842.12 |
338.15 | 0.8939 | 862.72 |
338.15 | 1.0000 | 885.57 |
Operational condition: Pressure, kPa = 101 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of Eucalyptol (2) - Liquid | Speed of sound, m/s - Liquid |
278.15 | 0.0000 | 1256.65 |
278.15 | 0.1046 | 1263.76 |
278.15 | 0.1990 | 1270.81 |
278.15 | 0.2987 | 1279.14 |
278.15 | 0.4008 | 1288.48 |
278.15 | 0.4955 | 1297.82 |
278.15 | 0.5939 | 1308.36 |
278.15 | 0.6971 | 1320.12 |
278.15 | 0.7985 | 1332.5 |
278.15 | 0.8939 | 1344.94 |
278.15 | 1.0000 | 1359.61 |
298.15 | 0.0000 | 1172.69 |
298.15 | 0.1046 | 1180.9 |
298.15 | 0.1990 | 1188.55 |
298.15 | 0.2987 | 1197.5 |
298.15 | 0.4008 | 1207.27 |
298.15 | 0.4955 | 1216.87 |
298.15 | 0.5939 | 1227.66 |
298.15 | 0.6971 | 1239.84 |
298.15 | 0.7985 | 1252.37 |
298.15 | 0.8939 | 1264.88 |
298.15 | 1.0000 | 1278.39 |
318.15 | 0.0000 | 1090.71 |
318.15 | 0.1046 | 1099.65 |
318.15 | 0.1990 | 1108.14 |
318.15 | 0.2987 | 1117.88 |
318.15 | 0.4008 | 1128.3 |
318.15 | 0.4955 | 1138.35 |
318.15 | 0.5939 | 1149.5 |
318.15 | 0.6971 | 1162.28 |
318.15 | 0.7985 | 1175.57 |
318.15 | 0.8939 | 1188.32 |
318.15 | 1.0000 | 1200.99 |
338.15 | 0.0000 | 1010.72 |
338.15 | 0.1046 | 1020.2 |
338.15 | 0.1990 | 1029.62 |
338.15 | 0.2987 | 1040.27 |
338.15 | 0.4008 | 1051.6 |
338.15 | 0.4955 | 1062.26 |
338.15 | 0.5939 | 1073.84 |
338.15 | 0.6971 | 1087.43 |
338.15 | 0.7985 | 1101.37 |
338.15 | 0.8939 | 1114.47 |
338.15 | 1.0000 | 1126.65 |
Operational condition: Pressure, kPa = 101 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of Eucalyptol (2) - Liquid | Speed of sound, m/s - Liquid |
278.15 | 0.0000 | 1256.65 |
278.15 | 0.1046 | 1263.76 |
278.15 | 0.1990 | 1270.81 |
278.15 | 0.2987 | 1279.14 |
278.15 | 0.4008 | 1288.48 |
278.15 | 0.4955 | 1297.82 |
278.15 | 0.5939 | 1308.36 |
278.15 | 0.6971 | 1320.12 |
278.15 | 0.7985 | 1332.5 |
278.15 | 0.8939 | 1344.94 |
278.15 | 1.0000 | 1359.61 |
298.15 | 0.0000 | 1172.69 |
298.15 | 0.1046 | 1180.9 |
298.15 | 0.1990 | 1188.55 |
298.15 | 0.2987 | 1197.5 |
298.15 | 0.4008 | 1207.27 |
298.15 | 0.4955 | 1216.87 |
298.15 | 0.5939 | 1227.66 |
298.15 | 0.6971 | 1239.84 |
298.15 | 0.7985 | 1252.37 |
298.15 | 0.8939 | 1264.88 |
298.15 | 1.0000 | 1278.39 |
318.15 | 0.0000 | 1090.71 |
318.15 | 0.1046 | 1099.65 |
318.15 | 0.1990 | 1108.14 |
318.15 | 0.2987 | 1117.88 |
318.15 | 0.4008 | 1128.3 |
318.15 | 0.4955 | 1138.35 |
318.15 | 0.5939 | 1149.5 |
318.15 | 0.6971 | 1162.28 |
318.15 | 0.7985 | 1175.57 |
318.15 | 0.8939 | 1188.32 |
318.15 | 1.0000 | 1200.99 |
338.15 | 0.0000 | 1010.72 |
338.15 | 0.1046 | 1020.2 |
338.15 | 0.1990 | 1029.62 |
338.15 | 0.2987 | 1040.27 |
338.15 | 0.4008 | 1051.6 |
338.15 | 0.4955 | 1062.26 |
338.15 | 0.5939 | 1073.84 |
338.15 | 0.6971 | 1087.43 |
338.15 | 0.7985 | 1101.37 |
338.15 | 0.8939 | 1114.47 |
338.15 | 1.0000 | 1126.65 |