Operational condition: Pressure, kPa = 100 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of 1,4-Dioxane (2) - Liquid | Molar heat capacity at constant pressure, J/K/mol - Liquid |
293.15 | 0.0799 | 173.61 |
293.15 | 0.1351 | 171.94 |
293.15 | 0.1965 | 170.17 |
293.15 | 0.2378 | 169.01 |
293.15 | 0.2874 | 167.66 |
293.15 | 0.3258 | 166.66 |
293.15 | 0.3642 | 165.66 |
293.15 | 0.4195 | 164.26 |
293.15 | 0.4625 | 163.21 |
293.15 | 0.5061 | 162.15 |
293.15 | 0.5543 | 161.01 |
293.15 | 0.6023 | 159.90 |
293.15 | 0.6487 | 158.83 |
293.15 | 0.6946 | 157.82 |
293.15 | 0.7412 | 156.79 |
293.15 | 0.7845 | 155.87 |
293.15 | 0.8398 | 154.71 |
293.15 | 0.8975 | 153.56 |
298.15 | 0.0799 | 175.65 |
298.15 | 0.1351 | 173.94 |
298.15 | 0.1965 | 172.12 |
298.15 | 0.2378 | 170.93 |
298.15 | 0.2874 | 169.54 |
298.15 | 0.3258 | 168.49 |
298.15 | 0.3642 | 167.46 |
298.15 | 0.4195 | 166.02 |
298.15 | 0.4625 | 164.92 |
298.15 | 0.5061 | 163.82 |
298.15 | 0.5543 | 162.63 |
298.15 | 0.6023 | 161.47 |
298.15 | 0.6487 | 160.36 |
298.15 | 0.6946 | 159.29 |
298.15 | 0.7412 | 158.22 |
298.15 | 0.7845 | 157.25 |
298.15 | 0.8398 | 156.04 |
298.15 | 0.8975 | 154.82 |
303.15 | 0.0799 | 177.71 |
303.15 | 0.1351 | 175.96 |
303.15 | 0.1965 | 174.08 |
303.15 | 0.2378 | 172.86 |
303.15 | 0.2874 | 171.43 |
303.15 | 0.3258 | 170.34 |
303.15 | 0.3642 | 169.27 |
303.15 | 0.4195 | 167.78 |
303.15 | 0.4625 | 166.62 |
303.15 | 0.5061 | 165.49 |
303.15 | 0.5543 | 164.25 |
303.15 | 0.6023 | 163.05 |
303.15 | 0.6487 | 161.90 |
303.15 | 0.6946 | 160.78 |
303.15 | 0.7412 | 159.66 |
303.15 | 0.7845 | 158.66 |
303.15 | 0.8398 | 157.39 |
303.15 | 0.8975 | 156.10 |
308.15 | 0.0799 | 179.75 |
308.15 | 0.1351 | 177.96 |
308.15 | 0.1965 | 176.03 |
308.15 | 0.2378 | 174.77 |
308.15 | 0.2874 | 173.28 |
308.15 | 0.3258 | 172.17 |
308.15 | 0.3642 | 171.07 |
308.15 | 0.4195 | 169.52 |
308.15 | 0.4625 | 168.33 |
308.15 | 0.5061 | 167.15 |
308.15 | 0.5543 | 165.88 |
308.15 | 0.6023 | 164.62 |
308.15 | 0.6487 | 163.44 |
308.15 | 0.6946 | 162.27 |
308.15 | 0.7412 | 161.12 |
308.15 | 0.7845 | 160.06 |
308.15 | 0.8398 | 158.74 |
308.15 | 0.8975 | 157.39 |
Operational condition: Pressure, kPa = 100 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of 1,4-Dioxane (2) - Liquid | Molar heat capacity at constant pressure, J/K/mol - Liquid |
293.15 | 0.0799 | 173.61 |
293.15 | 0.1351 | 171.94 |
293.15 | 0.1965 | 170.17 |
293.15 | 0.2378 | 169.01 |
293.15 | 0.2874 | 167.66 |
293.15 | 0.3258 | 166.66 |
293.15 | 0.3642 | 165.66 |
293.15 | 0.4195 | 164.26 |
293.15 | 0.4625 | 163.21 |
293.15 | 0.5061 | 162.15 |
293.15 | 0.5543 | 161.01 |
293.15 | 0.6023 | 159.90 |
293.15 | 0.6487 | 158.83 |
293.15 | 0.6946 | 157.82 |
293.15 | 0.7412 | 156.79 |
293.15 | 0.7845 | 155.87 |
293.15 | 0.8398 | 154.71 |
293.15 | 0.8975 | 153.56 |
298.15 | 0.0799 | 175.65 |
298.15 | 0.1351 | 173.94 |
298.15 | 0.1965 | 172.12 |
298.15 | 0.2378 | 170.93 |
298.15 | 0.2874 | 169.54 |
298.15 | 0.3258 | 168.49 |
298.15 | 0.3642 | 167.46 |
298.15 | 0.4195 | 166.02 |
298.15 | 0.4625 | 164.92 |
298.15 | 0.5061 | 163.82 |
298.15 | 0.5543 | 162.63 |
298.15 | 0.6023 | 161.47 |
298.15 | 0.6487 | 160.36 |
298.15 | 0.6946 | 159.29 |
298.15 | 0.7412 | 158.22 |
298.15 | 0.7845 | 157.25 |
298.15 | 0.8398 | 156.04 |
298.15 | 0.8975 | 154.82 |
303.15 | 0.0799 | 177.71 |
303.15 | 0.1351 | 175.96 |
303.15 | 0.1965 | 174.08 |
303.15 | 0.2378 | 172.86 |
303.15 | 0.2874 | 171.43 |
303.15 | 0.3258 | 170.34 |
303.15 | 0.3642 | 169.27 |
303.15 | 0.4195 | 167.78 |
303.15 | 0.4625 | 166.62 |
303.15 | 0.5061 | 165.49 |
303.15 | 0.5543 | 164.25 |
303.15 | 0.6023 | 163.05 |
303.15 | 0.6487 | 161.90 |
303.15 | 0.6946 | 160.78 |
303.15 | 0.7412 | 159.66 |
303.15 | 0.7845 | 158.66 |
303.15 | 0.8398 | 157.39 |
303.15 | 0.8975 | 156.10 |
308.15 | 0.0799 | 179.75 |
308.15 | 0.1351 | 177.96 |
308.15 | 0.1965 | 176.03 |
308.15 | 0.2378 | 174.77 |
308.15 | 0.2874 | 173.28 |
308.15 | 0.3258 | 172.17 |
308.15 | 0.3642 | 171.07 |
308.15 | 0.4195 | 169.52 |
308.15 | 0.4625 | 168.33 |
308.15 | 0.5061 | 167.15 |
308.15 | 0.5543 | 165.88 |
308.15 | 0.6023 | 164.62 |
308.15 | 0.6487 | 163.44 |
308.15 | 0.6946 | 162.27 |
308.15 | 0.7412 | 161.12 |
308.15 | 0.7845 | 160.06 |
308.15 | 0.8398 | 158.74 |
308.15 | 0.8975 | 157.39 |
Operational condition: Pressure, kPa = 101 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of Cyclohexanone (1) - Liquid | Viscosity, Pa*s - Liquid |
288.15 | 0.0990 | 0.0014 |
288.15 | 0.2022 | 0.0015 |
288.15 | 0.3100 | 0.0015 |
288.15 | 0.4227 | 0.0016 |
288.15 | 0.5406 | 0.0017 |
288.15 | 0.6641 | 0.0019 |
288.15 | 0.7280 | 0.0020 |
288.15 | 0.8607 | 0.0022 |
288.15 | 0.9295 | 0.0024 |
293.15 | 0.0990 | 0.0013 |
293.15 | 0.2022 | 0.0014 |
293.15 | 0.3100 | 0.0014 |
293.15 | 0.4227 | 0.0015 |
293.15 | 0.5406 | 0.0016 |
293.15 | 0.6641 | 0.0017 |
293.15 | 0.7280 | 0.0018 |
293.15 | 0.8607 | 0.0020 |
293.15 | 0.9295 | 0.0021 |
298.15 | 0.0990 | 0.0012 |
298.15 | 0.2022 | 0.0012 |
298.15 | 0.3100 | 0.0013 |
298.15 | 0.4227 | 0.0013 |
298.15 | 0.5406 | 0.0014 |
298.15 | 0.6641 | 0.0015 |
298.15 | 0.7280 | 0.0016 |
298.15 | 0.8607 | 0.0018 |
298.15 | 0.9295 | 0.0019 |
303.15 | 0.0990 | 0.0011 |
303.15 | 0.2022 | 0.0011 |
303.15 | 0.3100 | 0.0012 |
303.15 | 0.4227 | 0.0012 |
303.15 | 0.5406 | 0.0013 |
303.15 | 0.6641 | 0.0014 |
303.15 | 0.7280 | 0.0015 |
303.15 | 0.8607 | 0.0017 |
303.15 | 0.9295 | 0.0018 |
308.15 | 0.0990 | 0.0010 |
308.15 | 0.2022 | 0.0011 |
308.15 | 0.3100 | 0.0011 |
308.15 | 0.4227 | 0.0011 |
308.15 | 0.5406 | 0.0012 |
308.15 | 0.6641 | 0.0013 |
308.15 | 0.7280 | 0.0014 |
308.15 | 0.8607 | 0.0015 |
308.15 | 0.9295 | 0.0016 |
313.15 | 0.0990 | 0.0010 |
313.15 | 0.2022 | 0.0010 |
313.15 | 0.3100 | 0.0010 |
313.15 | 0.4227 | 0.0011 |
313.15 | 0.5406 | 0.0011 |
313.15 | 0.6641 | 0.0012 |
313.15 | 0.7280 | 0.0013 |
313.15 | 0.8607 | 0.0014 |
313.15 | 0.9295 | 0.0015 |
Operational condition: Pressure, kPa = 101 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of Cyclohexanone (1) - Liquid | Viscosity, Pa*s - Liquid |
288.15 | 0.0990 | 0.0014 |
288.15 | 0.2022 | 0.0015 |
288.15 | 0.3100 | 0.0015 |
288.15 | 0.4227 | 0.0016 |
288.15 | 0.5406 | 0.0017 |
288.15 | 0.6641 | 0.0019 |
288.15 | 0.7280 | 0.0020 |
288.15 | 0.8607 | 0.0022 |
288.15 | 0.9295 | 0.0024 |
293.15 | 0.0990 | 0.0013 |
293.15 | 0.2022 | 0.0014 |
293.15 | 0.3100 | 0.0014 |
293.15 | 0.4227 | 0.0015 |
293.15 | 0.5406 | 0.0016 |
293.15 | 0.6641 | 0.0017 |
293.15 | 0.7280 | 0.0018 |
293.15 | 0.8607 | 0.0020 |
293.15 | 0.9295 | 0.0021 |
298.15 | 0.0990 | 0.0012 |
298.15 | 0.2022 | 0.0012 |
298.15 | 0.3100 | 0.0013 |
298.15 | 0.4227 | 0.0013 |
298.15 | 0.5406 | 0.0014 |
298.15 | 0.6641 | 0.0015 |
298.15 | 0.7280 | 0.0016 |
298.15 | 0.8607 | 0.0018 |
298.15 | 0.9295 | 0.0019 |
303.15 | 0.0990 | 0.0011 |
303.15 | 0.2022 | 0.0011 |
303.15 | 0.3100 | 0.0012 |
303.15 | 0.4227 | 0.0012 |
303.15 | 0.5406 | 0.0013 |
303.15 | 0.6641 | 0.0014 |
303.15 | 0.7280 | 0.0015 |
303.15 | 0.8607 | 0.0017 |
303.15 | 0.9295 | 0.0018 |
308.15 | 0.0990 | 0.0010 |
308.15 | 0.2022 | 0.0011 |
308.15 | 0.3100 | 0.0011 |
308.15 | 0.4227 | 0.0011 |
308.15 | 0.5406 | 0.0012 |
308.15 | 0.6641 | 0.0013 |
308.15 | 0.7280 | 0.0014 |
308.15 | 0.8607 | 0.0015 |
308.15 | 0.9295 | 0.0016 |
313.15 | 0.0990 | 0.0010 |
313.15 | 0.2022 | 0.0010 |
313.15 | 0.3100 | 0.0010 |
313.15 | 0.4227 | 0.0011 |
313.15 | 0.5406 | 0.0011 |
313.15 | 0.6641 | 0.0012 |
313.15 | 0.7280 | 0.0013 |
313.15 | 0.8607 | 0.0014 |
313.15 | 0.9295 | 0.0015 |
Operational conditions:
Mole fraction of 1,4-Dioxane (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
---|---|
0.0792 | 0.0817 |
0.1286 | 0.1245 |
0.1749 | 0.1595 |
0.2236 | 0.1916 |
0.2743 | 0.2201 |
0.3289 | 0.2455 |
0.3729 | 0.2622 |
0.4298 | 0.2787 |
0.4715 | 0.2871 |
0.5242 | 0.2930 |
0.5735 | 0.2935 |
0.6199 | 0.2892 |
0.7182 | 0.2624 |
0.7628 | 0.2412 |
0.8193 | 0.2048 |
0.8672 | 0.1647 |
0.9173 | 0.1125 |
Operational conditions:
Mole fraction of 1,4-Dioxane (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
---|---|
0.0792 | 0.0817 |
0.1286 | 0.1245 |
0.1749 | 0.1595 |
0.2236 | 0.1916 |
0.2743 | 0.2201 |
0.3289 | 0.2455 |
0.3729 | 0.2622 |
0.4298 | 0.2787 |
0.4715 | 0.2871 |
0.5242 | 0.2930 |
0.5735 | 0.2935 |
0.6199 | 0.2892 |
0.7182 | 0.2624 |
0.7628 | 0.2412 |
0.8193 | 0.2048 |
0.8672 | 0.1647 |
0.9173 | 0.1125 |
Operational condition: Pressure, kPa = 101 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of Cyclohexanone (1) - Liquid | Mass density, kg/m3 - Liquid |
288.15 | 0.0990 | 1027.6 |
288.15 | 0.2022 | 1016.9 |
288.15 | 0.3100 | 1006.5 |
288.15 | 0.4227 | 996.8 |
288.15 | 0.5406 | 986.5 |
288.15 | 0.6641 | 976.8 |
288.15 | 0.7280 | 971.2 |
288.15 | 0.8607 | 962.7 |
288.15 | 0.9295 | 957.7 |
293.15 | 0.0990 | 1021.8 |
293.15 | 0.2022 | 1011.3 |
293.15 | 0.3100 | 1000.8 |
293.15 | 0.4227 | 991.4 |
293.15 | 0.5406 | 981.7 |
293.15 | 0.6641 | 972.0 |
293.15 | 0.7280 | 966.1 |
293.15 | 0.8607 | 958.1 |
293.15 | 0.9295 | 953.1 |
298.15 | 0.0990 | 1016.5 |
298.15 | 0.2022 | 1006.2 |
298.15 | 0.3100 | 996.0 |
298.15 | 0.4227 | 986.4 |
298.15 | 0.5406 | 976.2 |
298.15 | 0.6641 | 966.8 |
298.15 | 0.7280 | 961.4 |
298.15 | 0.8607 | 953.2 |
298.15 | 0.9295 | 948.5 |
303.15 | 0.0990 | 1011.1 |
303.15 | 0.2022 | 1000.9 |
303.15 | 0.3100 | 990.8 |
303.15 | 0.4227 | 981.1 |
303.15 | 0.5406 | 971.5 |
303.15 | 0.6641 | 962.2 |
303.15 | 0.7280 | 956.9 |
303.15 | 0.8607 | 948.8 |
303.15 | 0.9295 | 943.8 |
308.15 | 0.0990 | 1005.5 |
308.15 | 0.2022 | 995.4 |
308.15 | 0.3100 | 985.5 |
308.15 | 0.4227 | 975.2 |
308.15 | 0.5406 | 966.5 |
308.15 | 0.6641 | 957.5 |
308.15 | 0.7280 | 952.4 |
308.15 | 0.8607 | 944.3 |
308.15 | 0.9295 | 939.1 |
313.15 | 0.0990 | 999.9 |
313.15 | 0.2022 | 989.7 |
313.15 | 0.3100 | 979.5 |
313.15 | 0.4227 | 970.7 |
313.15 | 0.5406 | 961.4 |
313.15 | 0.6641 | 952.5 |
313.15 | 0.7280 | 947.2 |
313.15 | 0.8607 | 939.4 |
313.15 | 0.9295 | 934.3 |
Operational condition: Pressure, kPa = 100 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of 1,4-Dioxane (2) - Liquid | Mass density, kg/m3 - Liquid |
293.15 | 0.0999 | 953.66 |
293.15 | 0.1548 | 957.29 |
293.15 | 0.2064 | 960.83 |
293.15 | 0.2523 | 964.08 |
293.15 | 0.3087 | 968.21 |
293.15 | 0.3412 | 970.67 |
293.15 | 0.3952 | 974.86 |
293.15 | 0.4315 | 977.76 |
293.15 | 0.4875 | 982.38 |
293.15 | 0.5348 | 986.41 |
293.15 | 0.5798 | 990.36 |
293.15 | 0.6145 | 993.49 |
293.15 | 0.6698 | 998.63 |
293.15 | 0.7148 | 1002.9 |
293.15 | 0.7682 | 1008.2 |
293.15 | 0.8015 | 1011.6 |
293.15 | 0.8542 | 1017.2 |
293.15 | 0.9054 | 1022.7 |
298.15 | 0.0999 | 949.13 |
298.15 | 0.1548 | 952.73 |
298.15 | 0.2064 | 956.23 |
298.15 | 0.2523 | 959.45 |
298.15 | 0.3087 | 963.55 |
298.15 | 0.3412 | 965.97 |
298.15 | 0.3952 | 970.12 |
298.15 | 0.4315 | 972.99 |
298.15 | 0.4875 | 977.54 |
298.15 | 0.5348 | 981.52 |
298.15 | 0.5798 | 985.42 |
298.15 | 0.6145 | 988.51 |
298.15 | 0.6698 | 993.56 |
298.15 | 0.7148 | 997.82 |
298.15 | 0.7682 | 1003.0 |
298.15 | 0.8015 | 1006.4 |
298.15 | 0.8542 | 1011.8 |
298.15 | 0.9054 | 1017.3 |
303.15 | 0.0999 | 944.25 |
303.15 | 0.1548 | 947.83 |
303.15 | 0.2064 | 951.32 |
303.15 | 0.2523 | 954.52 |
303.15 | 0.3087 | 958.59 |
303.15 | 0.3412 | 960.99 |
303.15 | 0.3952 | 965.11 |
303.15 | 0.4315 | 967.96 |
303.15 | 0.4875 | 972.47 |
303.15 | 0.5348 | 976.42 |
303.15 | 0.5798 | 980.28 |
303.15 | 0.6145 | 983.33 |
303.15 | 0.6698 | 988.34 |
303.15 | 0.7148 | 992.55 |
303.15 | 0.7682 | 997.69 |
303.15 | 0.8015 | 1001.0 |
303.15 | 0.8542 | 1006.4 |
303.15 | 0.9054 | 1011.7 |
308.15 | 0.0999 | 939.34 |
308.15 | 0.1548 | 942.9 |
308.15 | 0.2064 | 946.37 |
308.15 | 0.2523 | 949.56 |
308.15 | 0.3087 | 953.6 |
308.15 | 0.3412 | 955.99 |
308.15 | 0.3952 | 960.08 |
308.15 | 0.4315 | 962.9 |
308.15 | 0.4875 | 967.38 |
308.15 | 0.5348 | 971.29 |
308.15 | 0.5798 | 975.11 |
308.15 | 0.6145 | 978.13 |
308.15 | 0.6698 | 983.08 |
308.15 | 0.7148 | 987.23 |
308.15 | 0.7682 | 992.32 |
308.15 | 0.8015 | 995.58 |
308.15 | 0.8542 | 1000.8 |
308.15 | 0.9054 | 1006.2 |
Operational condition: Pressure, kPa = 101 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of Cyclohexanone (1) - Liquid | Mass density, kg/m3 - Liquid |
288.15 | 0.0990 | 1027.6 |
288.15 | 0.2022 | 1016.9 |
288.15 | 0.3100 | 1006.5 |
288.15 | 0.4227 | 996.8 |
288.15 | 0.5406 | 986.5 |
288.15 | 0.6641 | 976.8 |
288.15 | 0.7280 | 971.2 |
288.15 | 0.8607 | 962.7 |
288.15 | 0.9295 | 957.7 |
293.15 | 0.0990 | 1021.8 |
293.15 | 0.2022 | 1011.3 |
293.15 | 0.3100 | 1000.8 |
293.15 | 0.4227 | 991.4 |
293.15 | 0.5406 | 981.7 |
293.15 | 0.6641 | 972.0 |
293.15 | 0.7280 | 966.1 |
293.15 | 0.8607 | 958.1 |
293.15 | 0.9295 | 953.1 |
298.15 | 0.0990 | 1016.5 |
298.15 | 0.2022 | 1006.2 |
298.15 | 0.3100 | 996.0 |
298.15 | 0.4227 | 986.4 |
298.15 | 0.5406 | 976.2 |
298.15 | 0.6641 | 966.8 |
298.15 | 0.7280 | 961.4 |
298.15 | 0.8607 | 953.2 |
298.15 | 0.9295 | 948.5 |
303.15 | 0.0990 | 1011.1 |
303.15 | 0.2022 | 1000.9 |
303.15 | 0.3100 | 990.8 |
303.15 | 0.4227 | 981.1 |
303.15 | 0.5406 | 971.5 |
303.15 | 0.6641 | 962.2 |
303.15 | 0.7280 | 956.9 |
303.15 | 0.8607 | 948.8 |
303.15 | 0.9295 | 943.8 |
308.15 | 0.0990 | 1005.5 |
308.15 | 0.2022 | 995.4 |
308.15 | 0.3100 | 985.5 |
308.15 | 0.4227 | 975.2 |
308.15 | 0.5406 | 966.5 |
308.15 | 0.6641 | 957.5 |
308.15 | 0.7280 | 952.4 |
308.15 | 0.8607 | 944.3 |
308.15 | 0.9295 | 939.1 |
313.15 | 0.0990 | 999.9 |
313.15 | 0.2022 | 989.7 |
313.15 | 0.3100 | 979.5 |
313.15 | 0.4227 | 970.7 |
313.15 | 0.5406 | 961.4 |
313.15 | 0.6641 | 952.5 |
313.15 | 0.7280 | 947.2 |
313.15 | 0.8607 | 939.4 |
313.15 | 0.9295 | 934.3 |
Operational condition: Pressure, kPa = 100 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of 1,4-Dioxane (2) - Liquid | Mass density, kg/m3 - Liquid |
293.15 | 0.0999 | 953.66 |
293.15 | 0.1548 | 957.29 |
293.15 | 0.2064 | 960.83 |
293.15 | 0.2523 | 964.08 |
293.15 | 0.3087 | 968.21 |
293.15 | 0.3412 | 970.67 |
293.15 | 0.3952 | 974.86 |
293.15 | 0.4315 | 977.76 |
293.15 | 0.4875 | 982.38 |
293.15 | 0.5348 | 986.41 |
293.15 | 0.5798 | 990.36 |
293.15 | 0.6145 | 993.49 |
293.15 | 0.6698 | 998.63 |
293.15 | 0.7148 | 1002.9 |
293.15 | 0.7682 | 1008.2 |
293.15 | 0.8015 | 1011.6 |
293.15 | 0.8542 | 1017.2 |
293.15 | 0.9054 | 1022.7 |
298.15 | 0.0999 | 949.13 |
298.15 | 0.1548 | 952.73 |
298.15 | 0.2064 | 956.23 |
298.15 | 0.2523 | 959.45 |
298.15 | 0.3087 | 963.55 |
298.15 | 0.3412 | 965.97 |
298.15 | 0.3952 | 970.12 |
298.15 | 0.4315 | 972.99 |
298.15 | 0.4875 | 977.54 |
298.15 | 0.5348 | 981.52 |
298.15 | 0.5798 | 985.42 |
298.15 | 0.6145 | 988.51 |
298.15 | 0.6698 | 993.56 |
298.15 | 0.7148 | 997.82 |
298.15 | 0.7682 | 1003.0 |
298.15 | 0.8015 | 1006.4 |
298.15 | 0.8542 | 1011.8 |
298.15 | 0.9054 | 1017.3 |
303.15 | 0.0999 | 944.25 |
303.15 | 0.1548 | 947.83 |
303.15 | 0.2064 | 951.32 |
303.15 | 0.2523 | 954.52 |
303.15 | 0.3087 | 958.59 |
303.15 | 0.3412 | 960.99 |
303.15 | 0.3952 | 965.11 |
303.15 | 0.4315 | 967.96 |
303.15 | 0.4875 | 972.47 |
303.15 | 0.5348 | 976.42 |
303.15 | 0.5798 | 980.28 |
303.15 | 0.6145 | 983.33 |
303.15 | 0.6698 | 988.34 |
303.15 | 0.7148 | 992.55 |
303.15 | 0.7682 | 997.69 |
303.15 | 0.8015 | 1001.0 |
303.15 | 0.8542 | 1006.4 |
303.15 | 0.9054 | 1011.7 |
308.15 | 0.0999 | 939.34 |
308.15 | 0.1548 | 942.9 |
308.15 | 0.2064 | 946.37 |
308.15 | 0.2523 | 949.56 |
308.15 | 0.3087 | 953.6 |
308.15 | 0.3412 | 955.99 |
308.15 | 0.3952 | 960.08 |
308.15 | 0.4315 | 962.9 |
308.15 | 0.4875 | 967.38 |
308.15 | 0.5348 | 971.29 |
308.15 | 0.5798 | 975.11 |
308.15 | 0.6145 | 978.13 |
308.15 | 0.6698 | 983.08 |
308.15 | 0.7148 | 987.23 |
308.15 | 0.7682 | 992.32 |
308.15 | 0.8015 | 995.58 |
308.15 | 0.8542 | 1000.8 |
308.15 | 0.9054 | 1006.2 |
Operational conditions:
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of 1,4-Dioxane (2) - Liquid | Speed of sound, m/s - Liquid |
293.15 | 0.0999 | 1423.2 |
293.15 | 0.1548 | 1419.0 |
293.15 | 0.2064 | 1415.2 |
293.15 | 0.2523 | 1411.8 |
293.15 | 0.3087 | 1407.8 |
293.15 | 0.3412 | 1405.5 |
293.15 | 0.3952 | 1401.8 |
293.15 | 0.4315 | 1399.3 |
293.15 | 0.4875 | 1395.6 |
293.15 | 0.5348 | 1392.5 |
293.15 | 0.5798 | 1389.7 |
293.15 | 0.6145 | 1387.5 |
293.15 | 0.6698 | 1384.1 |
293.15 | 0.7148 | 1381.5 |
293.15 | 0.7682 | 1378.5 |
293.15 | 0.8015 | 1376.8 |
293.15 | 0.8542 | 1374.1 |
293.15 | 0.9054 | 1371.7 |
298.15 | 0.0999 | 1407.2 |
298.15 | 0.1548 | 1402.8 |
298.15 | 0.2064 | 1398.7 |
298.15 | 0.2523 | 1395.1 |
298.15 | 0.3087 | 1390.8 |
298.15 | 0.3412 | 1388.3 |
298.15 | 0.3952 | 1384.3 |
298.15 | 0.4315 | 1381.6 |
298.15 | 0.4875 | 1377.6 |
298.15 | 0.5348 | 1374.2 |
298.15 | 0.5798 | 1371.1 |
298.15 | 0.6145 | 1368.7 |
298.15 | 0.6698 | 1365.0 |
298.15 | 0.7148 | 1362.0 |
298.15 | 0.7682 | 1358.7 |
298.15 | 0.8015 | 1356.7 |
298.15 | 0.8542 | 1353.6 |
298.15 | 0.9054 | 1350.8 |
303.15 | 0.0999 | 1387.0 |
303.15 | 0.1548 | 1382.6 |
303.15 | 0.2064 | 1378.5 |
303.15 | 0.2523 | 1374.9 |
303.15 | 0.3087 | 1370.6 |
303.15 | 0.3412 | 1368.1 |
303.15 | 0.3952 | 1364.0 |
303.15 | 0.4315 | 1361.3 |
303.15 | 0.4875 | 1357.2 |
303.15 | 0.5348 | 1353.8 |
303.15 | 0.5798 | 1350.6 |
303.15 | 0.6145 | 1348.2 |
303.15 | 0.6698 | 1344.4 |
303.15 | 0.7148 | 1341.4 |
303.15 | 0.7682 | 1338.0 |
303.15 | 0.8015 | 1335.9 |
303.15 | 0.8542 | 1332.7 |
303.15 | 0.9054 | 1329.6 |
308.15 | 0.0999 | 1367.1 |
308.15 | 0.1548 | 1362.7 |
308.15 | 0.2064 | 1358.7 |
308.15 | 0.2523 | 1355.0 |
308.15 | 0.3087 | 1350.6 |
308.15 | 0.3412 | 1348.1 |
308.15 | 0.3952 | 1343.9 |
308.15 | 0.4315 | 1341.2 |
308.15 | 0.4875 | 1336.9 |
308.15 | 0.5348 | 1333.5 |
308.15 | 0.5798 | 1330.2 |
308.15 | 0.6145 | 1327.7 |
308.15 | 0.6698 | 1323.8 |
308.15 | 0.7148 | 1320.7 |
308.15 | 0.7682 | 1317.1 |
308.15 | 0.8015 | 1314.9 |
308.15 | 0.8542 | 1311.5 |
308.15 | 0.9054 | 1308.3 |
Operational conditions:
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of 1,4-Dioxane (2) - Liquid | Speed of sound, m/s - Liquid |
293.15 | 0.0999 | 1423.2 |
293.15 | 0.1548 | 1419.0 |
293.15 | 0.2064 | 1415.2 |
293.15 | 0.2523 | 1411.8 |
293.15 | 0.3087 | 1407.8 |
293.15 | 0.3412 | 1405.5 |
293.15 | 0.3952 | 1401.8 |
293.15 | 0.4315 | 1399.3 |
293.15 | 0.4875 | 1395.6 |
293.15 | 0.5348 | 1392.5 |
293.15 | 0.5798 | 1389.7 |
293.15 | 0.6145 | 1387.5 |
293.15 | 0.6698 | 1384.1 |
293.15 | 0.7148 | 1381.5 |
293.15 | 0.7682 | 1378.5 |
293.15 | 0.8015 | 1376.8 |
293.15 | 0.8542 | 1374.1 |
293.15 | 0.9054 | 1371.7 |
298.15 | 0.0999 | 1407.2 |
298.15 | 0.1548 | 1402.8 |
298.15 | 0.2064 | 1398.7 |
298.15 | 0.2523 | 1395.1 |
298.15 | 0.3087 | 1390.8 |
298.15 | 0.3412 | 1388.3 |
298.15 | 0.3952 | 1384.3 |
298.15 | 0.4315 | 1381.6 |
298.15 | 0.4875 | 1377.6 |
298.15 | 0.5348 | 1374.2 |
298.15 | 0.5798 | 1371.1 |
298.15 | 0.6145 | 1368.7 |
298.15 | 0.6698 | 1365.0 |
298.15 | 0.7148 | 1362.0 |
298.15 | 0.7682 | 1358.7 |
298.15 | 0.8015 | 1356.7 |
298.15 | 0.8542 | 1353.6 |
298.15 | 0.9054 | 1350.8 |
303.15 | 0.0999 | 1387.0 |
303.15 | 0.1548 | 1382.6 |
303.15 | 0.2064 | 1378.5 |
303.15 | 0.2523 | 1374.9 |
303.15 | 0.3087 | 1370.6 |
303.15 | 0.3412 | 1368.1 |
303.15 | 0.3952 | 1364.0 |
303.15 | 0.4315 | 1361.3 |
303.15 | 0.4875 | 1357.2 |
303.15 | 0.5348 | 1353.8 |
303.15 | 0.5798 | 1350.6 |
303.15 | 0.6145 | 1348.2 |
303.15 | 0.6698 | 1344.4 |
303.15 | 0.7148 | 1341.4 |
303.15 | 0.7682 | 1338.0 |
303.15 | 0.8015 | 1335.9 |
303.15 | 0.8542 | 1332.7 |
303.15 | 0.9054 | 1329.6 |
308.15 | 0.0999 | 1367.1 |
308.15 | 0.1548 | 1362.7 |
308.15 | 0.2064 | 1358.7 |
308.15 | 0.2523 | 1355.0 |
308.15 | 0.3087 | 1350.6 |
308.15 | 0.3412 | 1348.1 |
308.15 | 0.3952 | 1343.9 |
308.15 | 0.4315 | 1341.2 |
308.15 | 0.4875 | 1336.9 |
308.15 | 0.5348 | 1333.5 |
308.15 | 0.5798 | 1330.2 |
308.15 | 0.6145 | 1327.7 |
308.15 | 0.6698 | 1323.8 |
308.15 | 0.7148 | 1320.7 |
308.15 | 0.7682 | 1317.1 |
308.15 | 0.8015 | 1314.9 |
308.15 | 0.8542 | 1311.5 |
308.15 | 0.9054 | 1308.3 |