Operational condition: Pressure, kPa = 101.3 (Liquid)
| Mole fraction of Ethanone, 1-cyclopropyl- (2) - Liquid | Mole fraction of Ethanone, 1-cyclopropyl- (2) - Gas |
|---|---|
| 1.0000 | 1.0000 |
| 0.9278 | 0.9947 |
| 0.8100 | 0.9881 |
| 0.5145 | 0.9757 |
| 0.5042 | 0.9695 |
| 0.4197 | 0.9645 |
| 0.3267 | 0.9597 |
| 0.2410 | 0.9266 |
| 0.1968 | 0.8894 |
| 0.1178 | 0.7781 |
| 0.1137 | 0.7502 |
| 0.1054 | 0.7257 |
| 0.0998 | 0.7171 |
| 0.0698 | 0.6500 |
| 0.0365 | 0.4500 |
| 0.0000 | 0.0000 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Mole fraction of Ethanone, 1-cyclopropyl- (2) - Liquid | Mole fraction of Ethanone, 1-cyclopropyl- (2) - Gas |
|---|---|
| 1.0000 | 1.0000 |
| 0.9278 | 0.9947 |
| 0.8100 | 0.9881 |
| 0.5145 | 0.9757 |
| 0.5042 | 0.9695 |
| 0.4197 | 0.9645 |
| 0.3267 | 0.9597 |
| 0.2410 | 0.9266 |
| 0.1968 | 0.8894 |
| 0.1178 | 0.7781 |
| 0.1137 | 0.7502 |
| 0.1054 | 0.7257 |
| 0.0998 | 0.7171 |
| 0.0698 | 0.6500 |
| 0.0365 | 0.4500 |
| 0.0000 | 0.0000 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Mole fraction of Ethanone, 1-cyclopropyl- (2) - Liquid | Temperature, K - Liquid | Viscosity, Pa*s - Liquid |
| 1.0000 | 303.15 | 0.0006 |
| 0.8999 | 303.15 | 0.0007 |
| 0.7999 | 303.15 | 0.0008 |
| 0.6999 | 303.15 | 0.0010 |
| 0.5999 | 303.15 | 0.0012 |
| 0.4999 | 303.15 | 0.0015 |
| 0.4002 | 303.15 | 0.0018 |
| 0.3004 | 303.15 | 0.0022 |
| 0.2009 | 303.15 | 0.0026 |
| 0.0998 | 303.15 | 0.0032 |
| 0.0000 | 303.15 | 0.0038 |
| 1.0000 | 313.15 | 0.0005 |
| 0.8999 | 313.15 | 0.0006 |
| 0.7999 | 313.15 | 0.0007 |
| 0.6999 | 313.15 | 0.0009 |
| 0.5999 | 313.15 | 0.0011 |
| 0.4999 | 313.15 | 0.0013 |
| 0.4002 | 313.15 | 0.0016 |
| 0.3004 | 313.15 | 0.0019 |
| 0.2009 | 313.15 | 0.0024 |
| 0.0998 | 313.15 | 0.0029 |
| 0.0000 | 313.15 | 0.0034 |
| 1.0000 | 323.15 | 0.0005 |
| 0.8999 | 323.15 | 0.0005 |
| 0.7999 | 323.15 | 0.0006 |
| 0.6999 | 323.15 | 0.0008 |
| 0.5999 | 323.15 | 0.0009 |
| 0.4999 | 323.15 | 0.0012 |
| 0.4002 | 323.15 | 0.0014 |
| 0.3004 | 323.15 | 0.0017 |
| 0.2009 | 323.15 | 0.0021 |
| 0.0998 | 323.15 | 0.0026 |
| 0.0000 | 323.15 | 0.0031 |
| 1.0000 | 333.15 | 0.0004 |
| 0.8999 | 333.15 | 0.0005 |
| 0.7999 | 333.15 | 0.0006 |
| 0.6999 | 333.15 | 0.0007 |
| 0.5999 | 333.15 | 0.0008 |
| 0.4999 | 333.15 | 0.0010 |
| 0.4002 | 333.15 | 0.0013 |
| 0.3004 | 333.15 | 0.0016 |
| 0.2009 | 333.15 | 0.0019 |
| 0.0998 | 333.15 | 0.0023 |
| 0.0000 | 333.15 | 0.0027 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Mole fraction of Ethanone, 1-cyclopropyl- (2) - Liquid | Temperature, K - Liquid | Viscosity, Pa*s - Liquid |
| 1.0000 | 303.15 | 0.0006 |
| 0.8999 | 303.15 | 0.0007 |
| 0.7999 | 303.15 | 0.0008 |
| 0.6999 | 303.15 | 0.0010 |
| 0.5999 | 303.15 | 0.0012 |
| 0.4999 | 303.15 | 0.0015 |
| 0.4002 | 303.15 | 0.0018 |
| 0.3004 | 303.15 | 0.0022 |
| 0.2009 | 303.15 | 0.0026 |
| 0.0998 | 303.15 | 0.0032 |
| 0.0000 | 303.15 | 0.0038 |
| 1.0000 | 313.15 | 0.0005 |
| 0.8999 | 313.15 | 0.0006 |
| 0.7999 | 313.15 | 0.0007 |
| 0.6999 | 313.15 | 0.0009 |
| 0.5999 | 313.15 | 0.0011 |
| 0.4999 | 313.15 | 0.0013 |
| 0.4002 | 313.15 | 0.0016 |
| 0.3004 | 313.15 | 0.0019 |
| 0.2009 | 313.15 | 0.0024 |
| 0.0998 | 313.15 | 0.0029 |
| 0.0000 | 313.15 | 0.0034 |
| 1.0000 | 323.15 | 0.0005 |
| 0.8999 | 323.15 | 0.0005 |
| 0.7999 | 323.15 | 0.0006 |
| 0.6999 | 323.15 | 0.0008 |
| 0.5999 | 323.15 | 0.0009 |
| 0.4999 | 323.15 | 0.0012 |
| 0.4002 | 323.15 | 0.0014 |
| 0.3004 | 323.15 | 0.0017 |
| 0.2009 | 323.15 | 0.0021 |
| 0.0998 | 323.15 | 0.0026 |
| 0.0000 | 323.15 | 0.0031 |
| 1.0000 | 333.15 | 0.0004 |
| 0.8999 | 333.15 | 0.0005 |
| 0.7999 | 333.15 | 0.0006 |
| 0.6999 | 333.15 | 0.0007 |
| 0.5999 | 333.15 | 0.0008 |
| 0.4999 | 333.15 | 0.0010 |
| 0.4002 | 333.15 | 0.0013 |
| 0.3004 | 333.15 | 0.0016 |
| 0.2009 | 333.15 | 0.0019 |
| 0.0998 | 333.15 | 0.0023 |
| 0.0000 | 333.15 | 0.0027 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Mole fraction of Ethanone, 1-cyclopropyl- (2) - Liquid | Temperature, K - Liquid | Mass density, kg/m3 - Liquid |
| 1.0000 | 303.15 | 889.8 |
| 0.8999 | 303.15 | 924.5 |
| 0.7999 | 303.15 | 958.3 |
| 0.6999 | 303.15 | 991.1 |
| 0.5999 | 303.15 | 1022.5 |
| 0.4999 | 303.15 | 1052.8 |
| 0.4002 | 303.15 | 1081.9 |
| 0.3004 | 303.15 | 1109.7 |
| 0.2009 | 303.15 | 1136.2 |
| 0.0998 | 303.15 | 1161.9 |
| 0.0000 | 303.15 | 1185.7 |
| 1.0000 | 313.15 | 880.3 |
| 0.8999 | 313.15 | 915.5 |
| 0.7999 | 313.15 | 949.2 |
| 0.6999 | 313.15 | 982.1 |
| 0.5999 | 313.15 | 1013.8 |
| 0.4999 | 313.15 | 1044.3 |
| 0.4002 | 313.15 | 1073.7 |
| 0.3004 | 313.15 | 1101.8 |
| 0.2009 | 313.15 | 1128.5 |
| 0.0998 | 313.15 | 1154.3 |
| 0.0000 | 313.15 | 1178.3 |
| 1.0000 | 323.15 | 870.6 |
| 0.8999 | 323.15 | 905.9 |
| 0.7999 | 323.15 | 939.6 |
| 0.6999 | 323.15 | 972.4 |
| 0.5999 | 323.15 | 1004.2 |
| 0.4999 | 323.15 | 1034.8 |
| 0.4002 | 323.15 | 1064.2 |
| 0.3004 | 323.15 | 1092.3 |
| 0.2009 | 323.15 | 1119.1 |
| 0.0998 | 323.15 | 1144.9 |
| 0.0000 | 323.15 | 1168.9 |
| 1.0000 | 333.15 | 861.2 |
| 0.8999 | 333.15 | 896.5 |
| 0.7999 | 333.15 | 930.2 |
| 0.6999 | 333.15 | 963.1 |
| 0.5999 | 333.15 | 994.8 |
| 0.4999 | 333.15 | 1025.4 |
| 0.4002 | 333.15 | 1054.8 |
| 0.3004 | 333.15 | 1082.9 |
| 0.2009 | 333.15 | 1109.7 |
| 0.0998 | 333.15 | 1135.6 |
| 0.0000 | 333.15 | 1159.4 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Mole fraction of Ethanone, 1-cyclopropyl- (2) - Liquid | Temperature, K - Liquid | Mass density, kg/m3 - Liquid |
| 1.0000 | 303.15 | 889.8 |
| 0.8999 | 303.15 | 924.5 |
| 0.7999 | 303.15 | 958.3 |
| 0.6999 | 303.15 | 991.1 |
| 0.5999 | 303.15 | 1022.5 |
| 0.4999 | 303.15 | 1052.8 |
| 0.4002 | 303.15 | 1081.9 |
| 0.3004 | 303.15 | 1109.7 |
| 0.2009 | 303.15 | 1136.2 |
| 0.0998 | 303.15 | 1161.9 |
| 0.0000 | 303.15 | 1185.7 |
| 1.0000 | 313.15 | 880.3 |
| 0.8999 | 313.15 | 915.5 |
| 0.7999 | 313.15 | 949.2 |
| 0.6999 | 313.15 | 982.1 |
| 0.5999 | 313.15 | 1013.8 |
| 0.4999 | 313.15 | 1044.3 |
| 0.4002 | 313.15 | 1073.7 |
| 0.3004 | 313.15 | 1101.8 |
| 0.2009 | 313.15 | 1128.5 |
| 0.0998 | 313.15 | 1154.3 |
| 0.0000 | 313.15 | 1178.3 |
| 1.0000 | 323.15 | 870.6 |
| 0.8999 | 323.15 | 905.9 |
| 0.7999 | 323.15 | 939.6 |
| 0.6999 | 323.15 | 972.4 |
| 0.5999 | 323.15 | 1004.2 |
| 0.4999 | 323.15 | 1034.8 |
| 0.4002 | 323.15 | 1064.2 |
| 0.3004 | 323.15 | 1092.3 |
| 0.2009 | 323.15 | 1119.1 |
| 0.0998 | 323.15 | 1144.9 |
| 0.0000 | 323.15 | 1168.9 |
| 1.0000 | 333.15 | 861.2 |
| 0.8999 | 333.15 | 896.5 |
| 0.7999 | 333.15 | 930.2 |
| 0.6999 | 333.15 | 963.1 |
| 0.5999 | 333.15 | 994.8 |
| 0.4999 | 333.15 | 1025.4 |
| 0.4002 | 333.15 | 1054.8 |
| 0.3004 | 333.15 | 1082.9 |
| 0.2009 | 333.15 | 1109.7 |
| 0.0998 | 333.15 | 1135.6 |
| 0.0000 | 333.15 | 1159.4 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Mole fraction of Ethanone, 1-cyclopropyl- (2) - Liquid | Boiling temperature at pressure P, K - Liquid |
|---|---|
| 1.0000 | 384.80 |
| 0.9278 | 387.40 |
| 0.8100 | 392.40 |
| 0.5145 | 411.30 |
| 0.5042 | 412.20 |
| 0.4197 | 420.40 |
| 0.3267 | 431.90 |
| 0.2410 | 445.80 |
| 0.1968 | 454.70 |
| 0.1178 | 475.50 |
| 0.1137 | 476.80 |
| 0.1054 | 479.60 |
| 0.0998 | 481.50 |
| 0.0698 | 490.20 |
| 0.0365 | 508.20 |
| 0.0000 | 530.90 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Mole fraction of Ethanone, 1-cyclopropyl- (2) - Liquid | Boiling temperature at pressure P, K - Liquid |
|---|---|
| 1.0000 | 384.80 |
| 0.9278 | 387.40 |
| 0.8100 | 392.40 |
| 0.5145 | 411.30 |
| 0.5042 | 412.20 |
| 0.4197 | 420.40 |
| 0.3267 | 431.90 |
| 0.2410 | 445.80 |
| 0.1968 | 454.70 |
| 0.1178 | 475.50 |
| 0.1137 | 476.80 |
| 0.1054 | 479.60 |
| 0.0998 | 481.50 |
| 0.0698 | 490.20 |
| 0.0365 | 508.20 |
| 0.0000 | 530.90 |