- Name
- 1-Propanol
- InChI
- InChI=1S/C3H8O/c1-2-3-4/h4H,2-3H2,1H3
- InChI Key
- BDERNNFJNOPAEC-UHFFFAOYSA-N
- Formula
- C3H8O
- SMILES
- CCCO
- Mol. Weight (g/mol)
- 60.09
- CAS
- 71-23-8
- Name
- Ethane, 1,2-dichloro-
- InChI
- InChI=1S/C2H4Cl2/c3-1-2-4/h1-2H2
- InChI Key
- WSLDOOZREJYCGB-UHFFFAOYSA-N
- Formula
- C2H4Cl2
- SMILES
- ClCCCl
- Mol. Weight (g/mol)
- 98.96
- CAS
- 107-06-2
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Datasets
- Mole fraction (2)
- η - Viscosity, Pa*s (2)
- ρl - Mass density, kg/m3 (4)
- Vapor or sublimation pressure, kPa (2)
Mole fraction of Ethane, 1,2-dichloro- (2) [ref]
Operational condition: Temperature, K = 313.15 (Liquid)
| Mole fraction of Ethane, 1,2-dichloro- (2) - Liquid | Mole fraction of Ethane, 1,2-dichloro- (2) - Gas |
|---|---|
| 0.0000 | 0.0000 |
| 0.0992 | 0.4950 |
| 0.1477 | 0.5739 |
| 0.1770 | 0.6017 |
| 0.2514 | 0.6747 |
| 0.3030 | 0.6888 |
| 0.5214 | 0.7740 |
| 0.5622 | 0.7813 |
| 0.6494 | 0.7991 |
| 0.6710 | 0.7979 |
| 0.7590 | 0.8220 |
| 0.8289 | 0.8429 |
| 1.0000 | 1.0000 |
Mole fraction of Ethane, 1,2-dichloro- (2) [ref]
Operational condition: Temperature, K = 313.15 (Liquid)
| Mole fraction of Ethane, 1,2-dichloro- (2) - Liquid | Mole fraction of Ethane, 1,2-dichloro- (2) - Gas |
|---|---|
| 0.0000 | 0.0000 |
| 0.0992 | 0.4950 |
| 0.1477 | 0.5739 |
| 0.1770 | 0.6017 |
| 0.2514 | 0.6747 |
| 0.3030 | 0.6888 |
| 0.5214 | 0.7740 |
| 0.5622 | 0.7813 |
| 0.6494 | 0.7991 |
| 0.6710 | 0.7979 |
| 0.7590 | 0.8220 |
| 0.8289 | 0.8429 |
| 1.0000 | 1.0000 |
Viscosity, Pa*s [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 1-Propanol (1) - Liquid | Viscosity, Pa*s - Liquid |
| 288.15 | 0.1054 | 0.0008 |
| 288.15 | 0.2095 | 0.0009 |
| 288.15 | 0.3124 | 0.0009 |
| 288.15 | 0.4141 | 0.0010 |
| 288.15 | 0.5146 | 0.0011 |
| 288.15 | 0.6139 | 0.0013 |
| 288.15 | 0.7121 | 0.0015 |
| 288.15 | 0.8092 | 0.0017 |
| 288.15 | 0.9051 | 0.0020 |
| 293.15 | 0.1054 | 0.0008 |
| 293.15 | 0.2096 | 0.0008 |
| 293.15 | 0.3126 | 0.0009 |
| 293.15 | 0.4143 | 0.0009 |
| 293.15 | 0.5148 | 0.0010 |
| 293.15 | 0.6141 | 0.0011 |
| 293.15 | 0.7123 | 0.0013 |
| 293.15 | 0.8093 | 0.0015 |
| 293.15 | 0.9052 | 0.0018 |
| 298.15 | 0.1054 | 0.0007 |
| 298.15 | 0.2095 | 0.0007 |
| 298.15 | 0.3124 | 0.0008 |
| 298.15 | 0.4141 | 0.0008 |
| 298.15 | 0.5146 | 0.0009 |
| 298.15 | 0.6140 | 0.0010 |
| 298.15 | 0.7122 | 0.0012 |
| 298.15 | 0.8092 | 0.0014 |
| 298.15 | 0.9052 | 0.0016 |
| 303.15 | 0.1056 | 0.0007 |
| 303.15 | 0.2099 | 0.0007 |
| 303.15 | 0.3129 | 0.0007 |
| 303.15 | 0.4146 | 0.0008 |
| 303.15 | 0.5151 | 0.0008 |
| 303.15 | 0.6144 | 0.0009 |
| 303.15 | 0.7125 | 0.0011 |
| 303.15 | 0.8095 | 0.0012 |
| 303.15 | 0.9053 | 0.0014 |
| 308.15 | 0.1057 | 0.0006 |
| 308.15 | 0.2100 | 0.0007 |
| 308.15 | 0.3131 | 0.0007 |
| 308.15 | 0.4149 | 0.0007 |
| 308.15 | 0.5154 | 0.0008 |
| 308.15 | 0.6147 | 0.0009 |
| 308.15 | 0.7128 | 0.0010 |
| 308.15 | 0.8097 | 0.0011 |
| 308.15 | 0.9054 | 0.0013 |
| 313.15 | 0.1058 | 0.0006 |
| 313.15 | 0.2103 | 0.0006 |
| 313.15 | 0.3134 | 0.0006 |
| 313.15 | 0.4152 | 0.0007 |
| 313.15 | 0.5158 | 0.0007 |
| 313.15 | 0.6150 | 0.0008 |
| 313.15 | 0.7131 | 0.0009 |
| 313.15 | 0.8099 | 0.0010 |
| 313.15 | 0.9055 | 0.0012 |
Viscosity, Pa*s [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 1-Propanol (1) - Liquid | Viscosity, Pa*s - Liquid |
| 288.15 | 0.1054 | 0.0008 |
| 288.15 | 0.2095 | 0.0009 |
| 288.15 | 0.3124 | 0.0009 |
| 288.15 | 0.4141 | 0.0010 |
| 288.15 | 0.5146 | 0.0011 |
| 288.15 | 0.6139 | 0.0013 |
| 288.15 | 0.7121 | 0.0015 |
| 288.15 | 0.8092 | 0.0017 |
| 288.15 | 0.9051 | 0.0020 |
| 293.15 | 0.1054 | 0.0008 |
| 293.15 | 0.2096 | 0.0008 |
| 293.15 | 0.3126 | 0.0009 |
| 293.15 | 0.4143 | 0.0009 |
| 293.15 | 0.5148 | 0.0010 |
| 293.15 | 0.6141 | 0.0011 |
| 293.15 | 0.7123 | 0.0013 |
| 293.15 | 0.8093 | 0.0015 |
| 293.15 | 0.9052 | 0.0018 |
| 298.15 | 0.1054 | 0.0007 |
| 298.15 | 0.2095 | 0.0007 |
| 298.15 | 0.3124 | 0.0008 |
| 298.15 | 0.4141 | 0.0008 |
| 298.15 | 0.5146 | 0.0009 |
| 298.15 | 0.6140 | 0.0010 |
| 298.15 | 0.7122 | 0.0012 |
| 298.15 | 0.8092 | 0.0014 |
| 298.15 | 0.9052 | 0.0016 |
| 303.15 | 0.1056 | 0.0007 |
| 303.15 | 0.2099 | 0.0007 |
| 303.15 | 0.3129 | 0.0007 |
| 303.15 | 0.4146 | 0.0008 |
| 303.15 | 0.5151 | 0.0008 |
| 303.15 | 0.6144 | 0.0009 |
| 303.15 | 0.7125 | 0.0011 |
| 303.15 | 0.8095 | 0.0012 |
| 303.15 | 0.9053 | 0.0014 |
| 308.15 | 0.1057 | 0.0006 |
| 308.15 | 0.2100 | 0.0007 |
| 308.15 | 0.3131 | 0.0007 |
| 308.15 | 0.4149 | 0.0007 |
| 308.15 | 0.5154 | 0.0008 |
| 308.15 | 0.6147 | 0.0009 |
| 308.15 | 0.7128 | 0.0010 |
| 308.15 | 0.8097 | 0.0011 |
| 308.15 | 0.9054 | 0.0013 |
| 313.15 | 0.1058 | 0.0006 |
| 313.15 | 0.2103 | 0.0006 |
| 313.15 | 0.3134 | 0.0006 |
| 313.15 | 0.4152 | 0.0007 |
| 313.15 | 0.5158 | 0.0007 |
| 313.15 | 0.6150 | 0.0008 |
| 313.15 | 0.7131 | 0.0009 |
| 313.15 | 0.8099 | 0.0010 |
| 313.15 | 0.9055 | 0.0012 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 1-Propanol (1) - Liquid | Mass density, kg/m3 - Liquid |
| 288.15 | 0.0000 | 1260.35 |
| 288.15 | 0.0260 | 1248.39 |
| 288.15 | 0.0500 | 1237.53 |
| 288.15 | 0.0500 | 1237.37 |
| 288.15 | 0.1000 | 1215.38 |
| 288.15 | 0.1220 | 1205.69 |
| 288.15 | 0.1490 | 1193.33 |
| 288.15 | 0.2500 | 1149.08 |
| 288.15 | 0.3500 | 1104.87 |
| 288.15 | 0.4500 | 1060.3 |
| 288.15 | 0.5500 | 1015.43 |
| 288.15 | 0.6450 | 972.3 |
| 288.15 | 0.7500 | 924.58 |
| 288.15 | 0.8500 | 878.59 |
| 288.15 | 0.8990 | 855.66 |
| 288.15 | 0.9500 | 831.69 |
| 288.15 | 0.9740 | 820.39 |
| 288.15 | 0.9750 | 819.73 |
| 288.15 | 1.0000 | 807.86 |
| 298.15 | 0.0000 | 1245.75 |
| 298.15 | 0.0260 | 1234.01 |
| 298.15 | 0.0500 | 1223.22 |
| 298.15 | 0.0500 | 1223.08 |
| 298.15 | 0.1000 | 1201.26 |
| 298.15 | 0.1220 | 1191.67 |
| 298.15 | 0.1490 | 1179.47 |
| 298.15 | 0.2500 | 1135.78 |
| 298.15 | 0.3500 | 1092.18 |
| 298.15 | 0.4500 | 1048.27 |
| 298.15 | 0.5500 | 1004.09 |
| 298.15 | 0.6450 | 961.66 |
| 298.15 | 0.7500 | 914.71 |
| 298.15 | 0.8500 | 869.49 |
| 298.15 | 0.8990 | 846.93 |
| 298.15 | 0.9500 | 823.36 |
| 298.15 | 0.9740 | 812.24 |
| 298.15 | 0.9750 | 811.6 |
| 298.15 | 1.0000 | 799.78 |
| 308.15 | 0.0000 | 1231.16 |
| 308.15 | 0.0260 | 1219.5 |
| 308.15 | 0.0500 | 1208.79 |
| 308.15 | 0.0500 | 1208.64 |
| 308.15 | 0.1000 | 1187.01 |
| 308.15 | 0.1220 | 1177.5 |
| 308.15 | 0.1490 | 1165.44 |
| 308.15 | 0.2500 | 1122.28 |
| 308.15 | 0.3500 | 1079.29 |
| 308.15 | 0.4500 | 1036.04 |
| 308.15 | 0.5500 | 992.55 |
| 308.15 | 0.6450 | 950.81 |
| 308.15 | 0.7500 | 904.65 |
| 308.15 | 0.8500 | 860.21 |
| 308.15 | 0.8990 | 838.05 |
| 308.15 | 0.9500 | 814.89 |
| 308.15 | 0.9740 | 803.95 |
| 308.15 | 0.9750 | 803.33 |
| 308.15 | 1.0000 | 791.71 |
| 318.15 | 0.0000 | 1216.56 |
| 318.15 | 0.0260 | 1204.86 |
| 318.15 | 0.0500 | 1194.22 |
| 318.15 | 0.0500 | 1194.08 |
| 318.15 | 0.1000 | 1172.6 |
| 318.15 | 0.1220 | 1163.18 |
| 318.15 | 0.1490 | 1151.24 |
| 318.15 | 0.2500 | 1108.59 |
| 318.15 | 0.3500 | 1066.19 |
| 318.15 | 0.4500 | 1023.57 |
| 318.15 | 0.5500 | 980.78 |
| 318.15 | 0.6450 | 939.73 |
| 318.15 | 0.7500 | 894.38 |
| 318.15 | 0.8500 | 850.73 |
| 318.15 | 0.8990 | 828.97 |
| 318.15 | 0.9500 | 806.24 |
| 318.15 | 0.9740 | 795.49 |
| 318.15 | 0.9750 | 794.89 |
| 318.15 | 1.0000 | 783.64 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 1-Propanol (1) - Liquid | Mass density, kg/m3 - Liquid |
| 288.15 | 0.1054 | 1211.0 |
| 288.15 | 0.2095 | 1166.4 |
| 288.15 | 0.3124 | 1121.8 |
| 288.15 | 0.4141 | 1078.4 |
| 288.15 | 0.5146 | 1032.4 |
| 288.15 | 0.6139 | 986.0 |
| 288.15 | 0.7121 | 942.8 |
| 288.15 | 0.8092 | 895.4 |
| 288.15 | 0.9051 | 843.5 |
| 293.15 | 0.1054 | 1205.0 |
| 293.15 | 0.2096 | 1159.7 |
| 293.15 | 0.3126 | 1116.2 |
| 293.15 | 0.4143 | 1072.1 |
| 293.15 | 0.5148 | 1026.6 |
| 293.15 | 0.6141 | 980.6 |
| 293.15 | 0.7123 | 938.6 |
| 293.15 | 0.8093 | 890.5 |
| 293.15 | 0.9052 | 839.4 |
| 298.15 | 0.1054 | 1199.2 |
| 298.15 | 0.2095 | 1154.4 |
| 298.15 | 0.3124 | 1109.3 |
| 298.15 | 0.4141 | 1067.1 |
| 298.15 | 0.5146 | 1021.3 |
| 298.15 | 0.6140 | 976.2 |
| 298.15 | 0.7122 | 934.0 |
| 298.15 | 0.8092 | 885.9 |
| 298.15 | 0.9052 | 836.3 |
| 303.15 | 0.1056 | 1192.6 |
| 303.15 | 0.2099 | 1147.7 |
| 303.15 | 0.3129 | 1104.2 |
| 303.15 | 0.4146 | 1061.1 |
| 303.15 | 0.5151 | 1016.0 |
| 303.15 | 0.6144 | 970.5 |
| 303.15 | 0.7125 | 929.7 |
| 303.15 | 0.8095 | 882.6 |
| 303.15 | 0.9053 | 832.8 |
| 308.15 | 0.1057 | 1183.4 |
| 308.15 | 0.2100 | 1140.7 |
| 308.15 | 0.3131 | 1097.2 |
| 308.15 | 0.4149 | 1054.9 |
| 308.15 | 0.5154 | 1009.5 |
| 308.15 | 0.6147 | 964.0 |
| 308.15 | 0.7128 | 924.3 |
| 308.15 | 0.8097 | 877.3 |
| 308.15 | 0.9054 | 827.5 |
| 313.15 | 0.1058 | 1174.9 |
| 313.15 | 0.2103 | 1133.5 |
| 313.15 | 0.3134 | 1089.0 |
| 313.15 | 0.4152 | 1047.4 |
| 313.15 | 0.5158 | 1004.0 |
| 313.15 | 0.6150 | 956.7 |
| 313.15 | 0.7131 | 918.9 |
| 313.15 | 0.8099 | 870.1 |
| 313.15 | 0.9055 | 821.5 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 1-Propanol (1) - Liquid | Mass density, kg/m3 - Liquid |
| 288.15 | 0.0000 | 1260.35 |
| 288.15 | 0.0260 | 1248.39 |
| 288.15 | 0.0500 | 1237.53 |
| 288.15 | 0.0500 | 1237.37 |
| 288.15 | 0.1000 | 1215.38 |
| 288.15 | 0.1220 | 1205.69 |
| 288.15 | 0.1490 | 1193.33 |
| 288.15 | 0.2500 | 1149.08 |
| 288.15 | 0.3500 | 1104.87 |
| 288.15 | 0.4500 | 1060.3 |
| 288.15 | 0.5500 | 1015.43 |
| 288.15 | 0.6450 | 972.3 |
| 288.15 | 0.7500 | 924.58 |
| 288.15 | 0.8500 | 878.59 |
| 288.15 | 0.8990 | 855.66 |
| 288.15 | 0.9500 | 831.69 |
| 288.15 | 0.9740 | 820.39 |
| 288.15 | 0.9750 | 819.73 |
| 288.15 | 1.0000 | 807.86 |
| 298.15 | 0.0000 | 1245.75 |
| 298.15 | 0.0260 | 1234.01 |
| 298.15 | 0.0500 | 1223.22 |
| 298.15 | 0.0500 | 1223.08 |
| 298.15 | 0.1000 | 1201.26 |
| 298.15 | 0.1220 | 1191.67 |
| 298.15 | 0.1490 | 1179.47 |
| 298.15 | 0.2500 | 1135.78 |
| 298.15 | 0.3500 | 1092.18 |
| 298.15 | 0.4500 | 1048.27 |
| 298.15 | 0.5500 | 1004.09 |
| 298.15 | 0.6450 | 961.66 |
| 298.15 | 0.7500 | 914.71 |
| 298.15 | 0.8500 | 869.49 |
| 298.15 | 0.8990 | 846.93 |
| 298.15 | 0.9500 | 823.36 |
| 298.15 | 0.9740 | 812.24 |
| 298.15 | 0.9750 | 811.6 |
| 298.15 | 1.0000 | 799.78 |
| 308.15 | 0.0000 | 1231.16 |
| 308.15 | 0.0260 | 1219.5 |
| 308.15 | 0.0500 | 1208.79 |
| 308.15 | 0.0500 | 1208.64 |
| 308.15 | 0.1000 | 1187.01 |
| 308.15 | 0.1220 | 1177.5 |
| 308.15 | 0.1490 | 1165.44 |
| 308.15 | 0.2500 | 1122.28 |
| 308.15 | 0.3500 | 1079.29 |
| 308.15 | 0.4500 | 1036.04 |
| 308.15 | 0.5500 | 992.55 |
| 308.15 | 0.6450 | 950.81 |
| 308.15 | 0.7500 | 904.65 |
| 308.15 | 0.8500 | 860.21 |
| 308.15 | 0.8990 | 838.05 |
| 308.15 | 0.9500 | 814.89 |
| 308.15 | 0.9740 | 803.95 |
| 308.15 | 0.9750 | 803.33 |
| 308.15 | 1.0000 | 791.71 |
| 318.15 | 0.0000 | 1216.56 |
| 318.15 | 0.0260 | 1204.86 |
| 318.15 | 0.0500 | 1194.22 |
| 318.15 | 0.0500 | 1194.08 |
| 318.15 | 0.1000 | 1172.6 |
| 318.15 | 0.1220 | 1163.18 |
| 318.15 | 0.1490 | 1151.24 |
| 318.15 | 0.2500 | 1108.59 |
| 318.15 | 0.3500 | 1066.19 |
| 318.15 | 0.4500 | 1023.57 |
| 318.15 | 0.5500 | 980.78 |
| 318.15 | 0.6450 | 939.73 |
| 318.15 | 0.7500 | 894.38 |
| 318.15 | 0.8500 | 850.73 |
| 318.15 | 0.8990 | 828.97 |
| 318.15 | 0.9500 | 806.24 |
| 318.15 | 0.9740 | 795.49 |
| 318.15 | 0.9750 | 794.89 |
| 318.15 | 1.0000 | 783.64 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 1-Propanol (1) - Liquid | Mass density, kg/m3 - Liquid |
| 288.15 | 0.1054 | 1211.0 |
| 288.15 | 0.2095 | 1166.4 |
| 288.15 | 0.3124 | 1121.8 |
| 288.15 | 0.4141 | 1078.4 |
| 288.15 | 0.5146 | 1032.4 |
| 288.15 | 0.6139 | 986.0 |
| 288.15 | 0.7121 | 942.8 |
| 288.15 | 0.8092 | 895.4 |
| 288.15 | 0.9051 | 843.5 |
| 293.15 | 0.1054 | 1205.0 |
| 293.15 | 0.2096 | 1159.7 |
| 293.15 | 0.3126 | 1116.2 |
| 293.15 | 0.4143 | 1072.1 |
| 293.15 | 0.5148 | 1026.6 |
| 293.15 | 0.6141 | 980.6 |
| 293.15 | 0.7123 | 938.6 |
| 293.15 | 0.8093 | 890.5 |
| 293.15 | 0.9052 | 839.4 |
| 298.15 | 0.1054 | 1199.2 |
| 298.15 | 0.2095 | 1154.4 |
| 298.15 | 0.3124 | 1109.3 |
| 298.15 | 0.4141 | 1067.1 |
| 298.15 | 0.5146 | 1021.3 |
| 298.15 | 0.6140 | 976.2 |
| 298.15 | 0.7122 | 934.0 |
| 298.15 | 0.8092 | 885.9 |
| 298.15 | 0.9052 | 836.3 |
| 303.15 | 0.1056 | 1192.6 |
| 303.15 | 0.2099 | 1147.7 |
| 303.15 | 0.3129 | 1104.2 |
| 303.15 | 0.4146 | 1061.1 |
| 303.15 | 0.5151 | 1016.0 |
| 303.15 | 0.6144 | 970.5 |
| 303.15 | 0.7125 | 929.7 |
| 303.15 | 0.8095 | 882.6 |
| 303.15 | 0.9053 | 832.8 |
| 308.15 | 0.1057 | 1183.4 |
| 308.15 | 0.2100 | 1140.7 |
| 308.15 | 0.3131 | 1097.2 |
| 308.15 | 0.4149 | 1054.9 |
| 308.15 | 0.5154 | 1009.5 |
| 308.15 | 0.6147 | 964.0 |
| 308.15 | 0.7128 | 924.3 |
| 308.15 | 0.8097 | 877.3 |
| 308.15 | 0.9054 | 827.5 |
| 313.15 | 0.1058 | 1174.9 |
| 313.15 | 0.2103 | 1133.5 |
| 313.15 | 0.3134 | 1089.0 |
| 313.15 | 0.4152 | 1047.4 |
| 313.15 | 0.5158 | 1004.0 |
| 313.15 | 0.6150 | 956.7 |
| 313.15 | 0.7131 | 918.9 |
| 313.15 | 0.8099 | 870.1 |
| 313.15 | 0.9055 | 821.5 |
Vapor or sublimation pressure, kPa [ref]
Operational condition: Temperature, K = 313.15 (Liquid)
| Mole fraction of Ethane, 1,2-dichloro- (2) - Liquid | Vapor or sublimation pressure, kPa - Gas |
|---|---|
| 0.0000 | 7.18 |
| 0.0992 | 12.62 |
| 0.1477 | 14.50 |
| 0.1770 | 15.51 |
| 0.2514 | 17.66 |
| 0.3030 | 18.75 |
| 0.5214 | 21.36 |
| 0.5622 | 21.63 |
| 0.6494 | 21.93 |
| 0.6710 | 21.99 |
| 0.7590 | 22.28 |
| 0.8289 | 22.30 |
| 1.0000 | 21.05 |
Vapor or sublimation pressure, kPa [ref]
Operational condition: Temperature, K = 313.15 (Liquid)
| Mole fraction of Ethane, 1,2-dichloro- (2) - Liquid | Vapor or sublimation pressure, kPa - Gas |
|---|---|
| 0.0000 | 7.18 |
| 0.0992 | 12.62 |
| 0.1477 | 14.50 |
| 0.1770 | 15.51 |
| 0.2514 | 17.66 |
| 0.3030 | 18.75 |
| 0.5214 | 21.36 |
| 0.5622 | 21.63 |
| 0.6494 | 21.93 |
| 0.6710 | 21.99 |
| 0.7590 | 22.28 |
| 0.8289 | 22.30 |
| 1.0000 | 21.05 |
Sources
- (Vapor + liquid) equilibria for the binary mixtures (1-propanol + dibromomethane, or + bromochloromethane, or + 1,2-dichloroethane or +1-bromo-2-chloroethane) at T = 313.15 K.
- Densities and Excess Molar Volumes for the Binary and Ternary Systems of (1,4-Dioxane, 1-Propanol or 2-Propanol, and 1,2-Dichloroethane) at T = (288.15 to 318.15) K. Experimental Measurements and Prigogine-Flory-Patterson Modeling
- Densities and Viscosities of (1-Propanol + 1,2-Dichloroethane), (1-Propanol + Benzaldehyde), (Benzaldehyde + 1,2-Dichloroethane), and (1-Propanol + 1,2-Dichloroethane + Benzaldehyde) Mixtures from T = 288.15 K to 313.15 K