Operational conditions:
| Mole fraction of Ethane, 1,2-dibromo- (1) - Liquid | Viscosity, Pa*s - Liquid |
|---|---|
| 0.0000 | 0.0053 |
| 0.0402 | 0.0049 |
| 0.0682 | 0.0047 |
| 0.1276 | 0.0043 |
| 0.2056 | 0.0038 |
| 0.2686 | 0.0034 |
| 0.3892 | 0.0029 |
| 0.4277 | 0.0027 |
| 0.5444 | 0.0023 |
| 0.6405 | 0.0021 |
| 0.7326 | 0.0019 |
| 0.8519 | 0.0017 |
| 0.9273 | 0.0017 |
| 0.9587 | 0.0017 |
| 0.9782 | 0.0017 |
| 1.0000 | 0.0017 |
Operational conditions:
| Mole fraction of Ethane, 1,2-dibromo- (1) - Liquid | Viscosity, Pa*s - Liquid |
|---|---|
| 0.0000 | 0.0053 |
| 0.0402 | 0.0049 |
| 0.0682 | 0.0047 |
| 0.1276 | 0.0043 |
| 0.2056 | 0.0038 |
| 0.2686 | 0.0034 |
| 0.3892 | 0.0029 |
| 0.4277 | 0.0027 |
| 0.5444 | 0.0023 |
| 0.6405 | 0.0021 |
| 0.7326 | 0.0019 |
| 0.8519 | 0.0017 |
| 0.9273 | 0.0017 |
| 0.9587 | 0.0017 |
| 0.9782 | 0.0017 |
| 1.0000 | 0.0017 |
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Ethane, 1,2-dibromo- (1) - Liquid | Mass density, kg/m3 - Liquid |
| 293.15 | 0.0000 | 818.856 |
| 293.15 | 0.0402 | 856.608 |
| 293.15 | 0.0682 | 883.413 |
| 293.15 | 0.1276 | 941.916 |
| 293.15 | 0.2056 | 1022.358 |
| 293.15 | 0.2686 | 1090.467 |
| 293.15 | 0.3892 | 1228.973 |
| 293.15 | 0.4277 | 1276.432 |
| 293.15 | 0.5444 | 1427.131 |
| 293.15 | 0.6405 | 1561.996 |
| 293.15 | 0.7326 | 1701.636 |
| 293.15 | 0.8519 | 1899.692 |
| 293.15 | 0.9273 | 2036.524 |
| 293.15 | 0.9587 | 2096.509 |
| 293.15 | 0.9782 | 2135.291 |
| 293.15 | 1.0000 | 2179.591 |
| 298.15 | 0.0000 | 815.281 |
| 298.15 | 0.0402 | 852.83 |
| 298.15 | 0.0682 | 879.495 |
| 298.15 | 0.1276 | 937.69 |
| 298.15 | 0.2056 | 1017.704 |
| 298.15 | 0.2686 | 1085.45 |
| 298.15 | 0.3892 | 1223.201 |
| 298.15 | 0.4277 | 1270.414 |
| 298.15 | 0.5444 | 1420.311 |
| 298.15 | 0.6405 | 1554.455 |
| 298.15 | 0.7326 | 1693.371 |
| 298.15 | 0.8519 | 1890.444 |
| 298.15 | 0.9273 | 2026.658 |
| 298.15 | 0.9587 | 2086.396 |
| 298.15 | 0.9782 | 2125.016 |
| 298.15 | 1.0000 | 2169.137 |
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Ethane, 1,2-dibromo- (1) - Liquid | Mass density, kg/m3 - Liquid |
| 308.15 | 0.0000 | 808.056 |
| 308.15 | 0.0402 | 845.2 |
| 308.15 | 0.0682 | 871.58 |
| 308.15 | 0.1276 | 929.152 |
| 308.15 | 0.2056 | 1008.302 |
| 308.15 | 0.2686 | 1075.321 |
| 308.15 | 0.3892 | 1211.591 |
| 308.15 | 0.4277 | 1258.283 |
| 308.15 | 0.5444 | 1406.533 |
| 308.15 | 0.6405 | 1539.272 |
| 308.15 | 0.7326 | 1676.75 |
| 308.15 | 0.8519 | 1871.877 |
| 308.15 | 0.9273 | 2006.874 |
| 308.15 | 0.9587 | 2066.136 |
| 308.15 | 0.9782 | 2104.454 |
| 308.15 | 1.0000 | 2148.196 |
| 313.15 | 0.0000 | 804.397 |
| 313.15 | 0.0402 | 841.335 |
| 313.15 | 0.0682 | 867.573 |
| 313.15 | 0.1276 | 924.828 |
| 313.15 | 0.2056 | 1003.545 |
| 313.15 | 0.2686 | 1070.191 |
| 313.15 | 0.3892 | 1205.721 |
| 313.15 | 0.4277 | 1252.152 |
| 313.15 | 0.5444 | 1399.601 |
| 313.15 | 0.6405 | 1531.625 |
| 313.15 | 0.7326 | 1668.382 |
| 313.15 | 0.8519 | 1862.549 |
| 313.15 | 0.9273 | 1996.951 |
| 313.15 | 0.9587 | 2055.976 |
| 313.15 | 0.9782 | 2094.137 |
| 313.15 | 1.0000 | 2137.692 |
Operational conditions:
| Mole fraction of Ethane, 1,2-dibromo- (1) - Liquid | Mass density, kg/m3 - Liquid |
|---|---|
| 0.0000 | 818.856 |
| 0.0402 | 856.608 |
| 0.0682 | 883.413 |
| 0.1276 | 941.916 |
| 0.2056 | 1022.358 |
| 0.2686 | 1090.467 |
| 0.3892 | 1228.973 |
| 0.4277 | 1276.432 |
| 0.5444 | 1427.131 |
| 0.6405 | 1561.996 |
| 0.7326 | 1701.636 |
| 0.8519 | 1899.692 |
| 0.9273 | 2036.524 |
| 0.9587 | 2096.509 |
| 0.9782 | 2135.291 |
| 1.0000 | 2179.591 |
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Ethane, 1,2-dibromo- (1) - Liquid | Mass density, kg/m3 - Liquid |
| 293.15 | 0.0000 | 818.856 |
| 293.15 | 0.0402 | 856.608 |
| 293.15 | 0.0682 | 883.413 |
| 293.15 | 0.1276 | 941.916 |
| 293.15 | 0.2056 | 1022.358 |
| 293.15 | 0.2686 | 1090.467 |
| 293.15 | 0.3892 | 1228.973 |
| 293.15 | 0.4277 | 1276.432 |
| 293.15 | 0.5444 | 1427.131 |
| 293.15 | 0.6405 | 1561.996 |
| 293.15 | 0.7326 | 1701.636 |
| 293.15 | 0.8519 | 1899.692 |
| 293.15 | 0.9273 | 2036.524 |
| 293.15 | 0.9587 | 2096.509 |
| 293.15 | 0.9782 | 2135.291 |
| 293.15 | 1.0000 | 2179.591 |
| 298.15 | 0.0000 | 815.281 |
| 298.15 | 0.0402 | 852.83 |
| 298.15 | 0.0682 | 879.495 |
| 298.15 | 0.1276 | 937.69 |
| 298.15 | 0.2056 | 1017.704 |
| 298.15 | 0.2686 | 1085.45 |
| 298.15 | 0.3892 | 1223.201 |
| 298.15 | 0.4277 | 1270.414 |
| 298.15 | 0.5444 | 1420.311 |
| 298.15 | 0.6405 | 1554.455 |
| 298.15 | 0.7326 | 1693.371 |
| 298.15 | 0.8519 | 1890.444 |
| 298.15 | 0.9273 | 2026.658 |
| 298.15 | 0.9587 | 2086.396 |
| 298.15 | 0.9782 | 2125.016 |
| 298.15 | 1.0000 | 2169.137 |
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Ethane, 1,2-dibromo- (1) - Liquid | Mass density, kg/m3 - Liquid |
| 308.15 | 0.0000 | 808.056 |
| 308.15 | 0.0402 | 845.2 |
| 308.15 | 0.0682 | 871.58 |
| 308.15 | 0.1276 | 929.152 |
| 308.15 | 0.2056 | 1008.302 |
| 308.15 | 0.2686 | 1075.321 |
| 308.15 | 0.3892 | 1211.591 |
| 308.15 | 0.4277 | 1258.283 |
| 308.15 | 0.5444 | 1406.533 |
| 308.15 | 0.6405 | 1539.272 |
| 308.15 | 0.7326 | 1676.75 |
| 308.15 | 0.8519 | 1871.877 |
| 308.15 | 0.9273 | 2006.874 |
| 308.15 | 0.9587 | 2066.136 |
| 308.15 | 0.9782 | 2104.454 |
| 308.15 | 1.0000 | 2148.196 |
| 313.15 | 0.0000 | 804.397 |
| 313.15 | 0.0402 | 841.335 |
| 313.15 | 0.0682 | 867.573 |
| 313.15 | 0.1276 | 924.828 |
| 313.15 | 0.2056 | 1003.545 |
| 313.15 | 0.2686 | 1070.191 |
| 313.15 | 0.3892 | 1205.721 |
| 313.15 | 0.4277 | 1252.152 |
| 313.15 | 0.5444 | 1399.601 |
| 313.15 | 0.6405 | 1531.625 |
| 313.15 | 0.7326 | 1668.382 |
| 313.15 | 0.8519 | 1862.549 |
| 313.15 | 0.9273 | 1996.951 |
| 313.15 | 0.9587 | 2055.976 |
| 313.15 | 0.9782 | 2094.137 |
| 313.15 | 1.0000 | 2137.692 |
Operational conditions:
| Mole fraction of Ethane, 1,2-dibromo- (1) - Liquid | Mass density, kg/m3 - Liquid |
|---|---|
| 0.0000 | 818.856 |
| 0.0402 | 856.608 |
| 0.0682 | 883.413 |
| 0.1276 | 941.916 |
| 0.2056 | 1022.358 |
| 0.2686 | 1090.467 |
| 0.3892 | 1228.973 |
| 0.4277 | 1276.432 |
| 0.5444 | 1427.131 |
| 0.6405 | 1561.996 |
| 0.7326 | 1701.636 |
| 0.8519 | 1899.692 |
| 0.9273 | 2036.524 |
| 0.9587 | 2096.509 |
| 0.9782 | 2135.291 |
| 1.0000 | 2179.591 |
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Ethane, 1,2-dibromo- (1) - Liquid | Speed of sound, m/s - Liquid |
| 293.15 | 0.0000 | 1320.11 |
| 293.15 | 0.0402 | 1296.69 |
| 293.15 | 0.0682 | 1280.96 |
| 293.15 | 0.1276 | 1249.37 |
| 293.15 | 0.2056 | 1211.19 |
| 293.15 | 0.2686 | 1182.94 |
| 293.15 | 0.3892 | 1135.24 |
| 293.15 | 0.4277 | 1121.2 |
| 293.15 | 0.5444 | 1083.57 |
| 293.15 | 0.6405 | 1057.41 |
| 293.15 | 0.7326 | 1036.51 |
| 293.15 | 0.8519 | 1016.83 |
| 293.15 | 0.9273 | 1009.94 |
| 293.15 | 0.9587 | 1008.3 |
| 293.15 | 0.9782 | 1007.43 |
| 293.15 | 1.0000 | 1007.04 |
| 298.15 | 0.0000 | 1303.19 |
| 298.15 | 0.0402 | 1279.95 |
| 298.15 | 0.0682 | 1264.36 |
| 298.15 | 0.1276 | 1233.06 |
| 298.15 | 0.2056 | 1195.28 |
| 298.15 | 0.2686 | 1167.33 |
| 298.15 | 0.3892 | 1120.21 |
| 298.15 | 0.4277 | 1106.34 |
| 298.15 | 0.5444 | 1069.22 |
| 298.15 | 0.6405 | 1043.59 |
| 298.15 | 0.7326 | 1023.12 |
| 298.15 | 0.8519 | 1003.95 |
| 298.15 | 0.9273 | 997.38 |
| 298.15 | 0.9587 | 995.92 |
| 298.15 | 0.9782 | 994.76 |
| 298.15 | 1.0000 | 994.27 |
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Ethane, 1,2-dibromo- (1) - Liquid | Speed of sound, m/s - Liquid |
| 308.15 | 0.0000 | 1270.16 |
| 308.15 | 0.0402 | 1246.83 |
| 308.15 | 0.0682 | 1231.5 |
| 308.15 | 0.1276 | 1200.8 |
| 308.15 | 0.2056 | 1163.78 |
| 308.15 | 0.2686 | 1136.45 |
| 308.15 | 0.3892 | 1090.37 |
| 308.15 | 0.4277 | 1076.97 |
| 308.15 | 0.5444 | 1041.17 |
| 308.15 | 0.6405 | 1016.47 |
| 308.15 | 0.7326 | 996.88 |
| 308.15 | 0.8519 | 978.58 |
| 308.15 | 0.9273 | 971.93 |
| 308.15 | 0.9587 | 970.13 |
| 308.15 | 0.9782 | 969.05 |
| 308.15 | 1.0000 | 968.69 |
| 313.15 | 0.0000 | 1253.6 |
| 313.15 | 0.0402 | 1230.66 |
| 313.15 | 0.0682 | 1215.27 |
| 313.15 | 0.1276 | 1184.83 |
| 313.15 | 0.2056 | 1148.2 |
| 313.15 | 0.2686 | 1121.19 |
| 313.15 | 0.3892 | 1075.62 |
| 313.15 | 0.4277 | 1062.5 |
| 313.15 | 0.5444 | 1027.06 |
| 313.15 | 0.6405 | 1003.01 |
| 313.15 | 0.7326 | 983.86 |
| 313.15 | 0.8519 | 966.15 |
| 313.15 | 0.9273 | 959.29 |
| 313.15 | 0.9587 | 957.92 |
| 313.15 | 0.9782 | 956.68 |
| 313.15 | 1.0000 | 956.08 |
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Ethane, 1,2-dibromo- (1) - Liquid | Speed of sound, m/s - Liquid |
| 293.15 | 0.0000 | 1320.11 |
| 293.15 | 0.0402 | 1296.69 |
| 293.15 | 0.0682 | 1280.96 |
| 293.15 | 0.1276 | 1249.37 |
| 293.15 | 0.2056 | 1211.19 |
| 293.15 | 0.2686 | 1182.94 |
| 293.15 | 0.3892 | 1135.24 |
| 293.15 | 0.4277 | 1121.2 |
| 293.15 | 0.5444 | 1083.57 |
| 293.15 | 0.6405 | 1057.41 |
| 293.15 | 0.7326 | 1036.51 |
| 293.15 | 0.8519 | 1016.83 |
| 293.15 | 0.9273 | 1009.94 |
| 293.15 | 0.9587 | 1008.3 |
| 293.15 | 0.9782 | 1007.43 |
| 293.15 | 1.0000 | 1007.04 |
| 298.15 | 0.0000 | 1303.19 |
| 298.15 | 0.0402 | 1279.95 |
| 298.15 | 0.0682 | 1264.36 |
| 298.15 | 0.1276 | 1233.06 |
| 298.15 | 0.2056 | 1195.28 |
| 298.15 | 0.2686 | 1167.33 |
| 298.15 | 0.3892 | 1120.21 |
| 298.15 | 0.4277 | 1106.34 |
| 298.15 | 0.5444 | 1069.22 |
| 298.15 | 0.6405 | 1043.59 |
| 298.15 | 0.7326 | 1023.12 |
| 298.15 | 0.8519 | 1003.95 |
| 298.15 | 0.9273 | 997.38 |
| 298.15 | 0.9587 | 995.92 |
| 298.15 | 0.9782 | 994.76 |
| 298.15 | 1.0000 | 994.27 |
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Ethane, 1,2-dibromo- (1) - Liquid | Speed of sound, m/s - Liquid |
| 308.15 | 0.0000 | 1270.16 |
| 308.15 | 0.0402 | 1246.83 |
| 308.15 | 0.0682 | 1231.5 |
| 308.15 | 0.1276 | 1200.8 |
| 308.15 | 0.2056 | 1163.78 |
| 308.15 | 0.2686 | 1136.45 |
| 308.15 | 0.3892 | 1090.37 |
| 308.15 | 0.4277 | 1076.97 |
| 308.15 | 0.5444 | 1041.17 |
| 308.15 | 0.6405 | 1016.47 |
| 308.15 | 0.7326 | 996.88 |
| 308.15 | 0.8519 | 978.58 |
| 308.15 | 0.9273 | 971.93 |
| 308.15 | 0.9587 | 970.13 |
| 308.15 | 0.9782 | 969.05 |
| 308.15 | 1.0000 | 968.69 |
| 313.15 | 0.0000 | 1253.6 |
| 313.15 | 0.0402 | 1230.66 |
| 313.15 | 0.0682 | 1215.27 |
| 313.15 | 0.1276 | 1184.83 |
| 313.15 | 0.2056 | 1148.2 |
| 313.15 | 0.2686 | 1121.19 |
| 313.15 | 0.3892 | 1075.62 |
| 313.15 | 0.4277 | 1062.5 |
| 313.15 | 0.5444 | 1027.06 |
| 313.15 | 0.6405 | 1003.01 |
| 313.15 | 0.7326 | 983.86 |
| 313.15 | 0.8519 | 966.15 |
| 313.15 | 0.9273 | 959.29 |
| 313.15 | 0.9587 | 957.92 |
| 313.15 | 0.9782 | 956.68 |
| 313.15 | 1.0000 | 956.08 |