- Name
- Trichloromethane
- InChI
- InChI=1S/CHCl3/c2-1(3)4/h1H
- InChI Key
- HEDRZPFGACZZDS-UHFFFAOYSA-N
- Formula
- CHCl3
- SMILES
- ClC(Cl)Cl
- Mol. Weight (g/mol)
- 119.38
- CAS
- 67-66-3
- Name
- 1-Butanol
- InChI
- InChI=1S/C4H10O/c1-2-3-4-5/h5H,2-4H2,1H3
- InChI Key
- LRHPLDYGYMQRHN-UHFFFAOYSA-N
- Formula
- C4H10O
- SMILES
- CCCCO
- Mol. Weight (g/mol)
- 74.12
- CAS
- 71-36-3
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Datasets
- η - Viscosity, Pa*s (4)
- ρl - Mass density, kg/m3 (6)
- csound,fluid - Speed of Sound, m/s (4)
- Vapor Liquid Equilibrium at Constant Pressure (3)
Viscosity, Pa*s [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Trichloromethane (1) - Liquid | Viscosity, Pa*s - Liquid |
| 298.15 | 0.0000 | 0.0026 |
| 298.15 | 0.0512 | 0.0024 |
| 298.15 | 0.1000 | 0.0022 |
| 298.15 | 0.1490 | 0.0021 |
| 298.15 | 0.2009 | 0.0019 |
| 298.15 | 0.2506 | 0.0017 |
| 298.15 | 0.2999 | 0.0015 |
| 298.15 | 0.3659 | 0.0014 |
| 298.15 | 0.4070 | 0.0012 |
| 298.15 | 0.4515 | 0.0011 |
| 298.15 | 0.4997 | 0.0010 |
| 298.15 | 0.5502 | 0.0009 |
| 298.15 | 0.6012 | 0.0009 |
| 298.15 | 0.6527 | 0.0008 |
| 298.15 | 0.7021 | 0.0008 |
| 298.15 | 0.7519 | 0.0007 |
| 298.15 | 0.8021 | 0.0007 |
| 298.15 | 0.8518 | 0.0007 |
| 298.15 | 0.9024 | 0.0006 |
| 298.15 | 0.9510 | 0.0006 |
| 298.15 | 1.0000 | 0.0006 |
| 308.15 | 0.0000 | 0.0020 |
| 308.15 | 0.0512 | 0.0019 |
| 308.15 | 0.1000 | 0.0018 |
| 308.15 | 0.1490 | 0.0016 |
| 308.15 | 0.2009 | 0.0015 |
| 308.15 | 0.2506 | 0.0014 |
| 308.15 | 0.2999 | 0.0013 |
| 308.15 | 0.3659 | 0.0011 |
| 308.15 | 0.4070 | 0.0010 |
| 308.15 | 0.4515 | 0.0010 |
| 308.15 | 0.4997 | 0.0009 |
| 308.15 | 0.5502 | 0.0008 |
| 308.15 | 0.6012 | 0.0008 |
| 308.15 | 0.6527 | 0.0007 |
| 308.15 | 0.7021 | 0.0007 |
| 308.15 | 0.7519 | 0.0006 |
| 308.15 | 0.8021 | 0.0006 |
| 308.15 | 0.8518 | 0.0006 |
| 308.15 | 0.9024 | 0.0006 |
| 308.15 | 0.9510 | 0.0005 |
| 308.15 | 1.0000 | 0.0005 |
Viscosity, Pa*s [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Trichloromethane (1) - Liquid | Viscosity, Pa*s - Liquid |
| 303.15 | 0.0000 | 0.0023 |
| 303.15 | 0.0513 | 0.0021 |
| 303.15 | 0.0999 | 0.0020 |
| 303.15 | 0.1490 | 0.0018 |
| 303.15 | 0.2009 | 0.0017 |
| 303.15 | 0.2506 | 0.0015 |
| 303.15 | 0.2999 | 0.0014 |
| 303.15 | 0.3659 | 0.0012 |
| 303.15 | 0.4070 | 0.0011 |
| 303.15 | 0.4515 | 0.0010 |
| 303.15 | 0.4997 | 0.0010 |
| 303.15 | 0.5502 | 0.0009 |
| 303.15 | 0.6011 | 0.0008 |
| 303.15 | 0.6527 | 0.0008 |
| 303.15 | 0.7020 | 0.0007 |
| 303.15 | 0.7519 | 0.0007 |
| 303.15 | 0.8020 | 0.0006 |
| 303.15 | 0.8517 | 0.0006 |
| 303.15 | 0.9023 | 0.0006 |
| 303.15 | 0.9509 | 0.0006 |
| 303.15 | 1.0000 | 0.0005 |
| 313.15 | 0.0000 | 0.0018 |
| 313.15 | 0.0512 | 0.0017 |
| 313.15 | 0.1000 | 0.0016 |
| 313.15 | 0.1490 | 0.0014 |
| 313.15 | 0.2009 | 0.0013 |
| 313.15 | 0.2506 | 0.0012 |
| 313.15 | 0.2999 | 0.0011 |
| 313.15 | 0.3659 | 0.0010 |
| 313.15 | 0.4070 | 0.0009 |
| 313.15 | 0.4515 | 0.0009 |
| 313.15 | 0.4997 | 0.0008 |
| 313.15 | 0.5502 | 0.0008 |
| 313.15 | 0.6012 | 0.0007 |
| 313.15 | 0.6527 | 0.0007 |
| 313.15 | 0.7021 | 0.0006 |
| 313.15 | 0.7519 | 0.0006 |
| 313.15 | 0.8021 | 0.0006 |
| 313.15 | 0.8518 | 0.0006 |
| 313.15 | 0.9024 | 0.0005 |
| 313.15 | 0.9510 | 0.0005 |
| 313.15 | 1.0000 | 0.0005 |
Viscosity, Pa*s [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Trichloromethane (1) - Liquid | Viscosity, Pa*s - Liquid |
| 298.15 | 0.0000 | 0.0026 |
| 298.15 | 0.0512 | 0.0024 |
| 298.15 | 0.1000 | 0.0022 |
| 298.15 | 0.1490 | 0.0021 |
| 298.15 | 0.2009 | 0.0019 |
| 298.15 | 0.2506 | 0.0017 |
| 298.15 | 0.2999 | 0.0015 |
| 298.15 | 0.3659 | 0.0014 |
| 298.15 | 0.4070 | 0.0012 |
| 298.15 | 0.4515 | 0.0011 |
| 298.15 | 0.4997 | 0.0010 |
| 298.15 | 0.5502 | 0.0009 |
| 298.15 | 0.6012 | 0.0009 |
| 298.15 | 0.6527 | 0.0008 |
| 298.15 | 0.7021 | 0.0008 |
| 298.15 | 0.7519 | 0.0007 |
| 298.15 | 0.8021 | 0.0007 |
| 298.15 | 0.8518 | 0.0007 |
| 298.15 | 0.9024 | 0.0006 |
| 298.15 | 0.9510 | 0.0006 |
| 298.15 | 1.0000 | 0.0006 |
| 308.15 | 0.0000 | 0.0020 |
| 308.15 | 0.0512 | 0.0019 |
| 308.15 | 0.1000 | 0.0018 |
| 308.15 | 0.1490 | 0.0016 |
| 308.15 | 0.2009 | 0.0015 |
| 308.15 | 0.2506 | 0.0014 |
| 308.15 | 0.2999 | 0.0013 |
| 308.15 | 0.3659 | 0.0011 |
| 308.15 | 0.4070 | 0.0010 |
| 308.15 | 0.4515 | 0.0010 |
| 308.15 | 0.4997 | 0.0009 |
| 308.15 | 0.5502 | 0.0008 |
| 308.15 | 0.6012 | 0.0008 |
| 308.15 | 0.6527 | 0.0007 |
| 308.15 | 0.7021 | 0.0007 |
| 308.15 | 0.7519 | 0.0006 |
| 308.15 | 0.8021 | 0.0006 |
| 308.15 | 0.8518 | 0.0006 |
| 308.15 | 0.9024 | 0.0006 |
| 308.15 | 0.9510 | 0.0005 |
| 308.15 | 1.0000 | 0.0005 |
Viscosity, Pa*s [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Trichloromethane (1) - Liquid | Viscosity, Pa*s - Liquid |
| 303.15 | 0.0000 | 0.0023 |
| 303.15 | 0.0513 | 0.0021 |
| 303.15 | 0.0999 | 0.0020 |
| 303.15 | 0.1490 | 0.0018 |
| 303.15 | 0.2009 | 0.0017 |
| 303.15 | 0.2506 | 0.0015 |
| 303.15 | 0.2999 | 0.0014 |
| 303.15 | 0.3659 | 0.0012 |
| 303.15 | 0.4070 | 0.0011 |
| 303.15 | 0.4515 | 0.0010 |
| 303.15 | 0.4997 | 0.0010 |
| 303.15 | 0.5502 | 0.0009 |
| 303.15 | 0.6011 | 0.0008 |
| 303.15 | 0.6527 | 0.0008 |
| 303.15 | 0.7020 | 0.0007 |
| 303.15 | 0.7519 | 0.0007 |
| 303.15 | 0.8020 | 0.0006 |
| 303.15 | 0.8517 | 0.0006 |
| 303.15 | 0.9023 | 0.0006 |
| 303.15 | 0.9509 | 0.0006 |
| 303.15 | 1.0000 | 0.0005 |
| 313.15 | 0.0000 | 0.0018 |
| 313.15 | 0.0512 | 0.0017 |
| 313.15 | 0.1000 | 0.0016 |
| 313.15 | 0.1490 | 0.0014 |
| 313.15 | 0.2009 | 0.0013 |
| 313.15 | 0.2506 | 0.0012 |
| 313.15 | 0.2999 | 0.0011 |
| 313.15 | 0.3659 | 0.0010 |
| 313.15 | 0.4070 | 0.0009 |
| 313.15 | 0.4515 | 0.0009 |
| 313.15 | 0.4997 | 0.0008 |
| 313.15 | 0.5502 | 0.0008 |
| 313.15 | 0.6012 | 0.0007 |
| 313.15 | 0.6527 | 0.0007 |
| 313.15 | 0.7021 | 0.0006 |
| 313.15 | 0.7519 | 0.0006 |
| 313.15 | 0.8021 | 0.0006 |
| 313.15 | 0.8518 | 0.0006 |
| 313.15 | 0.9024 | 0.0005 |
| 313.15 | 0.9510 | 0.0005 |
| 313.15 | 1.0000 | 0.0005 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 1-Butanol (2) - Liquid | Mass density, kg/m3 - Liquid |
| 288.15 | 0.0000 | 1498.077 |
| 288.15 | 0.0493 | 1458.967 |
| 288.15 | 0.0994 | 1420.117 |
| 288.15 | 0.1499 | 1381.858 |
| 288.15 | 0.2003 | 1344.302 |
| 288.15 | 0.2476 | 1309.654 |
| 288.15 | 0.2790 | 1286.969 |
| 288.15 | 0.3474 | 1238.343 |
| 288.15 | 0.4003 | 1201.44 |
| 288.15 | 0.4610 | 1159.744 |
| 288.15 | 0.4993 | 1133.81 |
| 288.15 | 0.5517 | 1098.6 |
| 288.15 | 0.5989 | 1067.377 |
| 288.15 | 0.6510 | 1033.234 |
| 288.15 | 0.7008 | 1001.03 |
| 288.15 | 0.7485 | 970.42 |
| 288.15 | 0.7987 | 938.452 |
| 288.15 | 0.8495 | 906.492 |
| 288.15 | 0.8953 | 877.854 |
| 288.15 | 0.9475 | 845.53 |
| 288.15 | 1.0000 | 813.373 |
| 293.15 | 0.0000 | 1488.638 |
| 293.15 | 0.0493 | 1449.824 |
| 293.15 | 0.0994 | 1411.277 |
| 293.15 | 0.1499 | 1373.34 |
| 293.15 | 0.2003 | 1336.11 |
| 293.15 | 0.2476 | 1301.761 |
| 293.15 | 0.2790 | 1279.278 |
| 293.15 | 0.3474 | 1231.07 |
| 293.15 | 0.4003 | 1194.482 |
| 293.15 | 0.4610 | 1153.143 |
| 293.15 | 0.4993 | 1127.428 |
| 293.15 | 0.5517 | 1092.6 |
| 293.15 | 0.5989 | 1061.553 |
| 293.15 | 0.6510 | 1027.696 |
| 293.15 | 0.7008 | 995.76 |
| 293.15 | 0.7485 | 965.404 |
| 293.15 | 0.7987 | 933.697 |
| 293.15 | 0.8495 | 901.999 |
| 293.15 | 0.8953 | 873.588 |
| 293.15 | 0.9475 | 841.51 |
| 293.15 | 1.0000 | 809.573 |
| 298.15 | 0.0000 | 1479.148 |
| 298.15 | 0.0493 | 1440.633 |
| 298.15 | 0.0994 | 1402.389 |
| 298.15 | 0.1499 | 1364.771 |
| 298.15 | 0.2003 | 1327.863 |
| 298.15 | 0.2476 | 1293.819 |
| 298.15 | 0.2790 | 1271.534 |
| 298.15 | 0.3474 | 1223.746 |
| 298.15 | 0.4003 | 1187.479 |
| 298.15 | 0.4610 | 1146.5 |
| 298.15 | 0.4993 | 1121.002 |
| 298.15 | 0.5517 | 1086.4 |
| 298.15 | 0.5989 | 1055.688 |
| 298.15 | 0.6510 | 1022.116 |
| 298.15 | 0.7008 | 990.45 |
| 298.15 | 0.7485 | 960.349 |
| 298.15 | 0.7987 | 928.907 |
| 298.15 | 0.8495 | 897.472 |
| 298.15 | 0.8953 | 869.292 |
| 298.15 | 0.9475 | 837.462 |
| 298.15 | 1.0000 | 805.762 |
| 303.15 | 0.0000 | 1469.612 |
| 303.15 | 0.0493 | 1431.398 |
| 303.15 | 0.0994 | 1393.449 |
| 303.15 | 0.1499 | 1356.152 |
| 303.15 | 0.2003 | 1319.568 |
| 303.15 | 0.2476 | 1285.822 |
| 303.15 | 0.2790 | 1263.746 |
| 303.15 | 0.3474 | 1216.374 |
| 303.15 | 0.4003 | 1180.425 |
| 303.15 | 0.4610 | 1139.809 |
| 303.15 | 0.4993 | 1114.527 |
| 303.15 | 0.5517 | 1080.3 |
| 303.15 | 0.5989 | 1049.776 |
| 303.15 | 0.6510 | 1016.495 |
| 303.15 | 0.7008 | 985.097 |
| 303.15 | 0.7485 | 955.255 |
| 303.15 | 0.7987 | 924.082 |
| 303.15 | 0.8495 | 892.91 |
| 303.15 | 0.8953 | 864.961 |
| 303.15 | 0.9475 | 833.386 |
| 303.15 | 1.0000 | 801.923 |
| 308.15 | 0.0000 | 1460.025 |
| 308.15 | 0.0493 | 1422.115 |
| 308.15 | 0.0994 | 1384.45 |
| 308.15 | 0.1499 | 1347.474 |
| 308.15 | 0.2003 | 1311.21 |
| 308.15 | 0.2476 | 1277.767 |
| 308.15 | 0.2790 | 1255.896 |
| 308.15 | 0.3474 | 1208.943 |
| 308.15 | 0.4003 | 1173.313 |
| 308.15 | 0.4610 | 1133.064 |
| 308.15 | 0.4993 | 1107.999 |
| 308.15 | 0.5517 | 1074.0 |
| 308.15 | 0.5989 | 1043.814 |
| 308.15 | 0.6510 | 1010.818 |
| 308.15 | 0.7008 | 979.698 |
| 308.15 | 0.7485 | 950.115 |
| 308.15 | 0.7987 | 919.208 |
| 308.15 | 0.8495 | 888.303 |
| 308.15 | 0.8953 | 860.59 |
| 308.15 | 0.9475 | 829.272 |
| 308.15 | 1.0000 | 798.053 |
| 313.15 | 0.0000 | 1450.413 |
| 313.15 | 0.0493 | 1412.816 |
| 313.15 | 0.0994 | 1375.41 |
| 313.15 | 0.1499 | 1338.756 |
| 313.15 | 0.2003 | 1302.801 |
| 313.15 | 0.2476 | 1269.664 |
| 313.15 | 0.2790 | 1248.018 |
| 313.15 | 0.3474 | 1201.478 |
| 313.15 | 0.4003 | 1166.161 |
| 313.15 | 0.4610 | 1126.294 |
| 313.15 | 0.4993 | 1101.418 |
| 313.15 | 0.5517 | 1067.8 |
| 313.15 | 0.5989 | 1037.803 |
| 313.15 | 0.6510 | 1005.107 |
| 313.15 | 0.7008 | 974.26 |
| 313.15 | 0.7485 | 944.94 |
| 313.15 | 0.7987 | 914.297 |
| 313.15 | 0.8495 | 883.67 |
| 313.15 | 0.8953 | 856.188 |
| 313.15 | 0.9475 | 825.138 |
| 313.15 | 1.0000 | 794.147 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Trichloromethane (1) - Liquid | Mass density, kg/m3 - Liquid |
| 298.15 | 0.0000 | 806.33 |
| 298.15 | 0.0512 | 836.7 |
| 298.15 | 0.1000 | 865.9 |
| 298.15 | 0.1490 | 895.66 |
| 298.15 | 0.2009 | 927.49 |
| 298.15 | 0.2506 | 958.3 |
| 298.15 | 0.2999 | 989.27 |
| 298.15 | 0.3659 | 1031.4 |
| 298.15 | 0.4070 | 1057.94 |
| 298.15 | 0.4515 | 1087.02 |
| 298.15 | 0.4997 | 1118.91 |
| 298.15 | 0.5502 | 1152.78 |
| 298.15 | 0.6012 | 1187.46 |
| 298.15 | 0.6527 | 1223.02 |
| 298.15 | 0.7021 | 1257.69 |
| 298.15 | 0.7519 | 1293.2 |
| 298.15 | 0.8021 | 1329.4 |
| 298.15 | 0.8518 | 1365.91 |
| 298.15 | 0.9024 | 1403.63 |
| 298.15 | 0.9510 | 1440.79 |
| 298.15 | 1.0000 | 1478.82 |
| 308.15 | 0.0000 | 798.38 |
| 308.15 | 0.0512 | 828.27 |
| 308.15 | 0.1000 | 857.0 |
| 308.15 | 0.1490 | 886.25 |
| 308.15 | 0.2009 | 917.55 |
| 308.15 | 0.2506 | 947.84 |
| 308.15 | 0.2999 | 978.3 |
| 308.15 | 0.3659 | 1019.75 |
| 308.15 | 0.4070 | 1045.83 |
| 308.15 | 0.4515 | 1074.42 |
| 308.15 | 0.4997 | 1105.67 |
| 308.15 | 0.5502 | 1138.99 |
| 308.15 | 0.6012 | 1173.05 |
| 308.15 | 0.6527 | 1207.99 |
| 308.15 | 0.7021 | 1241.99 |
| 308.15 | 0.7519 | 1276.84 |
| 308.15 | 0.8021 | 1312.4 |
| 308.15 | 0.8518 | 1348.31 |
| 308.15 | 0.9024 | 1385.4 |
| 308.15 | 0.9510 | 1421.97 |
| 308.15 | 1.0000 | 1459.45 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Trichloromethane (1) - Liquid | Mass density, kg/m3 - Liquid |
| 303.15 | 0.0000 | 802.31 |
| 303.15 | 0.0513 | 832.44 |
| 303.15 | 0.0999 | 861.44 |
| 303.15 | 0.1490 | 890.91 |
| 303.15 | 0.2009 | 922.47 |
| 303.15 | 0.2506 | 953.06 |
| 303.15 | 0.2999 | 983.75 |
| 303.15 | 0.3659 | 1025.5 |
| 303.15 | 0.4070 | 1051.86 |
| 303.15 | 0.4515 | 1080.69 |
| 303.15 | 0.4997 | 1112.25 |
| 303.15 | 0.5502 | 1145.88 |
| 303.15 | 0.6011 | 1180.26 |
| 303.15 | 0.6527 | 1215.51 |
| 303.15 | 0.7020 | 1249.87 |
| 303.15 | 0.7519 | 1285.1 |
| 303.15 | 0.8020 | 1320.98 |
| 303.15 | 0.8517 | 1357.17 |
| 303.15 | 0.9023 | 1394.7 |
| 303.15 | 0.9509 | 1431.43 |
| 303.15 | 1.0000 | 1469.21 |
| 313.15 | 0.0000 | 794.37 |
| 313.15 | 0.0512 | 823.95 |
| 313.15 | 0.1000 | 852.45 |
| 313.15 | 0.1490 | 881.47 |
| 313.15 | 0.2009 | 912.53 |
| 313.15 | 0.2506 | 942.58 |
| 313.15 | 0.2999 | 972.85 |
| 313.15 | 0.3659 | 1013.85 |
| 313.15 | 0.4070 | 1039.75 |
| 313.15 | 0.4515 | 1067.95 |
| 313.15 | 0.4997 | 1099.0 |
| 313.15 | 0.5502 | 1132.03 |
| 313.15 | 0.6012 | 1165.78 |
| 313.15 | 0.6527 | 1200.35 |
| 313.15 | 0.7021 | 1234.0 |
| 313.15 | 0.7519 | 1268.52 |
| 313.15 | 0.8021 | 1303.85 |
| 313.15 | 0.8518 | 1339.4 |
| 313.15 | 0.9024 | 1376.18 |
| 313.15 | 0.9510 | 1412.42 |
| 313.15 | 1.0000 | 1449.74 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 1-Butanol (2) - Liquid | Mass density, kg/m3 - Liquid |
| 288.15 | 0.0000 | 1498.077 |
| 288.15 | 0.0493 | 1458.967 |
| 288.15 | 0.0994 | 1420.117 |
| 288.15 | 0.1499 | 1381.858 |
| 288.15 | 0.2003 | 1344.302 |
| 288.15 | 0.2476 | 1309.654 |
| 288.15 | 0.2790 | 1286.969 |
| 288.15 | 0.3474 | 1238.343 |
| 288.15 | 0.4003 | 1201.44 |
| 288.15 | 0.4610 | 1159.744 |
| 288.15 | 0.4993 | 1133.81 |
| 288.15 | 0.5517 | 1098.6 |
| 288.15 | 0.5989 | 1067.377 |
| 288.15 | 0.6510 | 1033.234 |
| 288.15 | 0.7008 | 1001.03 |
| 288.15 | 0.7485 | 970.42 |
| 288.15 | 0.7987 | 938.452 |
| 288.15 | 0.8495 | 906.492 |
| 288.15 | 0.8953 | 877.854 |
| 288.15 | 0.9475 | 845.53 |
| 288.15 | 1.0000 | 813.373 |
| 293.15 | 0.0000 | 1488.638 |
| 293.15 | 0.0493 | 1449.824 |
| 293.15 | 0.0994 | 1411.277 |
| 293.15 | 0.1499 | 1373.34 |
| 293.15 | 0.2003 | 1336.11 |
| 293.15 | 0.2476 | 1301.761 |
| 293.15 | 0.2790 | 1279.278 |
| 293.15 | 0.3474 | 1231.07 |
| 293.15 | 0.4003 | 1194.482 |
| 293.15 | 0.4610 | 1153.143 |
| 293.15 | 0.4993 | 1127.428 |
| 293.15 | 0.5517 | 1092.6 |
| 293.15 | 0.5989 | 1061.553 |
| 293.15 | 0.6510 | 1027.696 |
| 293.15 | 0.7008 | 995.76 |
| 293.15 | 0.7485 | 965.404 |
| 293.15 | 0.7987 | 933.697 |
| 293.15 | 0.8495 | 901.999 |
| 293.15 | 0.8953 | 873.588 |
| 293.15 | 0.9475 | 841.51 |
| 293.15 | 1.0000 | 809.573 |
| 298.15 | 0.0000 | 1479.148 |
| 298.15 | 0.0493 | 1440.633 |
| 298.15 | 0.0994 | 1402.389 |
| 298.15 | 0.1499 | 1364.771 |
| 298.15 | 0.2003 | 1327.863 |
| 298.15 | 0.2476 | 1293.819 |
| 298.15 | 0.2790 | 1271.534 |
| 298.15 | 0.3474 | 1223.746 |
| 298.15 | 0.4003 | 1187.479 |
| 298.15 | 0.4610 | 1146.5 |
| 298.15 | 0.4993 | 1121.002 |
| 298.15 | 0.5517 | 1086.4 |
| 298.15 | 0.5989 | 1055.688 |
| 298.15 | 0.6510 | 1022.116 |
| 298.15 | 0.7008 | 990.45 |
| 298.15 | 0.7485 | 960.349 |
| 298.15 | 0.7987 | 928.907 |
| 298.15 | 0.8495 | 897.472 |
| 298.15 | 0.8953 | 869.292 |
| 298.15 | 0.9475 | 837.462 |
| 298.15 | 1.0000 | 805.762 |
| 303.15 | 0.0000 | 1469.612 |
| 303.15 | 0.0493 | 1431.398 |
| 303.15 | 0.0994 | 1393.449 |
| 303.15 | 0.1499 | 1356.152 |
| 303.15 | 0.2003 | 1319.568 |
| 303.15 | 0.2476 | 1285.822 |
| 303.15 | 0.2790 | 1263.746 |
| 303.15 | 0.3474 | 1216.374 |
| 303.15 | 0.4003 | 1180.425 |
| 303.15 | 0.4610 | 1139.809 |
| 303.15 | 0.4993 | 1114.527 |
| 303.15 | 0.5517 | 1080.3 |
| 303.15 | 0.5989 | 1049.776 |
| 303.15 | 0.6510 | 1016.495 |
| 303.15 | 0.7008 | 985.097 |
| 303.15 | 0.7485 | 955.255 |
| 303.15 | 0.7987 | 924.082 |
| 303.15 | 0.8495 | 892.91 |
| 303.15 | 0.8953 | 864.961 |
| 303.15 | 0.9475 | 833.386 |
| 303.15 | 1.0000 | 801.923 |
| 308.15 | 0.0000 | 1460.025 |
| 308.15 | 0.0493 | 1422.115 |
| 308.15 | 0.0994 | 1384.45 |
| 308.15 | 0.1499 | 1347.474 |
| 308.15 | 0.2003 | 1311.21 |
| 308.15 | 0.2476 | 1277.767 |
| 308.15 | 0.2790 | 1255.896 |
| 308.15 | 0.3474 | 1208.943 |
| 308.15 | 0.4003 | 1173.313 |
| 308.15 | 0.4610 | 1133.064 |
| 308.15 | 0.4993 | 1107.999 |
| 308.15 | 0.5517 | 1074.0 |
| 308.15 | 0.5989 | 1043.814 |
| 308.15 | 0.6510 | 1010.818 |
| 308.15 | 0.7008 | 979.698 |
| 308.15 | 0.7485 | 950.115 |
| 308.15 | 0.7987 | 919.208 |
| 308.15 | 0.8495 | 888.303 |
| 308.15 | 0.8953 | 860.59 |
| 308.15 | 0.9475 | 829.272 |
| 308.15 | 1.0000 | 798.053 |
| 313.15 | 0.0000 | 1450.413 |
| 313.15 | 0.0493 | 1412.816 |
| 313.15 | 0.0994 | 1375.41 |
| 313.15 | 0.1499 | 1338.756 |
| 313.15 | 0.2003 | 1302.801 |
| 313.15 | 0.2476 | 1269.664 |
| 313.15 | 0.2790 | 1248.018 |
| 313.15 | 0.3474 | 1201.478 |
| 313.15 | 0.4003 | 1166.161 |
| 313.15 | 0.4610 | 1126.294 |
| 313.15 | 0.4993 | 1101.418 |
| 313.15 | 0.5517 | 1067.8 |
| 313.15 | 0.5989 | 1037.803 |
| 313.15 | 0.6510 | 1005.107 |
| 313.15 | 0.7008 | 974.26 |
| 313.15 | 0.7485 | 944.94 |
| 313.15 | 0.7987 | 914.297 |
| 313.15 | 0.8495 | 883.67 |
| 313.15 | 0.8953 | 856.188 |
| 313.15 | 0.9475 | 825.138 |
| 313.15 | 1.0000 | 794.147 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Trichloromethane (1) - Liquid | Mass density, kg/m3 - Liquid |
| 298.15 | 0.0000 | 806.33 |
| 298.15 | 0.0512 | 836.7 |
| 298.15 | 0.1000 | 865.9 |
| 298.15 | 0.1490 | 895.66 |
| 298.15 | 0.2009 | 927.49 |
| 298.15 | 0.2506 | 958.3 |
| 298.15 | 0.2999 | 989.27 |
| 298.15 | 0.3659 | 1031.4 |
| 298.15 | 0.4070 | 1057.94 |
| 298.15 | 0.4515 | 1087.02 |
| 298.15 | 0.4997 | 1118.91 |
| 298.15 | 0.5502 | 1152.78 |
| 298.15 | 0.6012 | 1187.46 |
| 298.15 | 0.6527 | 1223.02 |
| 298.15 | 0.7021 | 1257.69 |
| 298.15 | 0.7519 | 1293.2 |
| 298.15 | 0.8021 | 1329.4 |
| 298.15 | 0.8518 | 1365.91 |
| 298.15 | 0.9024 | 1403.63 |
| 298.15 | 0.9510 | 1440.79 |
| 298.15 | 1.0000 | 1478.82 |
| 308.15 | 0.0000 | 798.38 |
| 308.15 | 0.0512 | 828.27 |
| 308.15 | 0.1000 | 857.0 |
| 308.15 | 0.1490 | 886.25 |
| 308.15 | 0.2009 | 917.55 |
| 308.15 | 0.2506 | 947.84 |
| 308.15 | 0.2999 | 978.3 |
| 308.15 | 0.3659 | 1019.75 |
| 308.15 | 0.4070 | 1045.83 |
| 308.15 | 0.4515 | 1074.42 |
| 308.15 | 0.4997 | 1105.67 |
| 308.15 | 0.5502 | 1138.99 |
| 308.15 | 0.6012 | 1173.05 |
| 308.15 | 0.6527 | 1207.99 |
| 308.15 | 0.7021 | 1241.99 |
| 308.15 | 0.7519 | 1276.84 |
| 308.15 | 0.8021 | 1312.4 |
| 308.15 | 0.8518 | 1348.31 |
| 308.15 | 0.9024 | 1385.4 |
| 308.15 | 0.9510 | 1421.97 |
| 308.15 | 1.0000 | 1459.45 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Trichloromethane (1) - Liquid | Mass density, kg/m3 - Liquid |
| 303.15 | 0.0000 | 802.31 |
| 303.15 | 0.0513 | 832.44 |
| 303.15 | 0.0999 | 861.44 |
| 303.15 | 0.1490 | 890.91 |
| 303.15 | 0.2009 | 922.47 |
| 303.15 | 0.2506 | 953.06 |
| 303.15 | 0.2999 | 983.75 |
| 303.15 | 0.3659 | 1025.5 |
| 303.15 | 0.4070 | 1051.86 |
| 303.15 | 0.4515 | 1080.69 |
| 303.15 | 0.4997 | 1112.25 |
| 303.15 | 0.5502 | 1145.88 |
| 303.15 | 0.6011 | 1180.26 |
| 303.15 | 0.6527 | 1215.51 |
| 303.15 | 0.7020 | 1249.87 |
| 303.15 | 0.7519 | 1285.1 |
| 303.15 | 0.8020 | 1320.98 |
| 303.15 | 0.8517 | 1357.17 |
| 303.15 | 0.9023 | 1394.7 |
| 303.15 | 0.9509 | 1431.43 |
| 303.15 | 1.0000 | 1469.21 |
| 313.15 | 0.0000 | 794.37 |
| 313.15 | 0.0512 | 823.95 |
| 313.15 | 0.1000 | 852.45 |
| 313.15 | 0.1490 | 881.47 |
| 313.15 | 0.2009 | 912.53 |
| 313.15 | 0.2506 | 942.58 |
| 313.15 | 0.2999 | 972.85 |
| 313.15 | 0.3659 | 1013.85 |
| 313.15 | 0.4070 | 1039.75 |
| 313.15 | 0.4515 | 1067.95 |
| 313.15 | 0.4997 | 1099.0 |
| 313.15 | 0.5502 | 1132.03 |
| 313.15 | 0.6012 | 1165.78 |
| 313.15 | 0.6527 | 1200.35 |
| 313.15 | 0.7021 | 1234.0 |
| 313.15 | 0.7519 | 1268.52 |
| 313.15 | 0.8021 | 1303.85 |
| 313.15 | 0.8518 | 1339.4 |
| 313.15 | 0.9024 | 1376.18 |
| 313.15 | 0.9510 | 1412.42 |
| 313.15 | 1.0000 | 1449.74 |
Speed of sound, m/s [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Trichloromethane (1) - Liquid | Speed of sound, m/s - Liquid |
| 298.15 | 0.0000 | 1235.0 |
| 298.15 | 0.0512 | 1215.0 |
| 298.15 | 0.1000 | 1198.0 |
| 298.15 | 0.1490 | 1180.0 |
| 298.15 | 0.2009 | 1163.0 |
| 298.15 | 0.2506 | 1146.0 |
| 298.15 | 0.2999 | 1130.0 |
| 298.15 | 0.3659 | 1110.0 |
| 298.15 | 0.4070 | 1097.0 |
| 298.15 | 0.4515 | 1085.0 |
| 298.15 | 0.4997 | 1071.0 |
| 298.15 | 0.5502 | 1058.0 |
| 298.15 | 0.6012 | 1045.0 |
| 298.15 | 0.6527 | 1033.0 |
| 298.15 | 0.7021 | 1022.0 |
| 298.15 | 0.7519 | 1013.0 |
| 298.15 | 0.8021 | 1004.0 |
| 298.15 | 0.8518 | 997.0 |
| 298.15 | 0.9024 | 992.0 |
| 298.15 | 0.9510 | 987.0 |
| 298.15 | 1.0000 | 985.0 |
| 308.15 | 0.0000 | 1210.0 |
| 308.15 | 0.0512 | 1190.0 |
| 308.15 | 0.1000 | 1171.0 |
| 308.15 | 0.1490 | 1153.0 |
| 308.15 | 0.2009 | 1134.0 |
| 308.15 | 0.2506 | 1116.0 |
| 308.15 | 0.2999 | 1099.0 |
| 308.15 | 0.3659 | 1078.0 |
| 308.15 | 0.4070 | 1065.0 |
| 308.15 | 0.4515 | 1051.0 |
| 308.15 | 0.4997 | 1037.0 |
| 308.15 | 0.5502 | 1024.0 |
| 308.15 | 0.6012 | 1011.0 |
| 308.15 | 0.6527 | 998.0 |
| 308.15 | 0.7021 | 987.0 |
| 308.15 | 0.7519 | 978.0 |
| 308.15 | 0.8021 | 969.0 |
| 308.15 | 0.8518 | 962.0 |
| 308.15 | 0.9024 | 956.0 |
| 308.15 | 0.9510 | 952.0 |
| 308.15 | 1.0000 | 950.0 |
Speed of sound, m/s [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Trichloromethane (1) - Liquid | Speed of sound, m/s - Liquid |
| 303.15 | 0.0000 | 1227.0 |
| 303.15 | 0.0513 | 1207.0 |
| 303.15 | 0.0999 | 1189.0 |
| 303.15 | 0.1490 | 1170.0 |
| 303.15 | 0.2009 | 1152.0 |
| 303.15 | 0.2506 | 1134.0 |
| 303.15 | 0.2999 | 1118.0 |
| 303.15 | 0.3659 | 1097.0 |
| 303.15 | 0.4070 | 1084.0 |
| 303.15 | 0.4515 | 1071.0 |
| 303.15 | 0.4997 | 1056.0 |
| 303.15 | 0.5502 | 1043.0 |
| 303.15 | 0.6011 | 1030.0 |
| 303.15 | 0.6527 | 1018.0 |
| 303.15 | 0.7020 | 1007.0 |
| 303.15 | 0.7519 | 997.0 |
| 303.15 | 0.8020 | 989.0 |
| 303.15 | 0.8517 | 981.0 |
| 303.15 | 0.9023 | 975.0 |
| 303.15 | 0.9509 | 971.0 |
| 303.15 | 1.0000 | 969.0 |
| 313.15 | 0.0000 | 1193.0 |
| 313.15 | 0.0512 | 1172.0 |
| 313.15 | 0.1000 | 1154.0 |
| 313.15 | 0.1490 | 1135.0 |
| 313.15 | 0.2009 | 1116.0 |
| 313.15 | 0.2506 | 1098.0 |
| 313.15 | 0.2999 | 1081.0 |
| 313.15 | 0.3659 | 1060.0 |
| 313.15 | 0.4070 | 1047.0 |
| 313.15 | 0.4515 | 1034.0 |
| 313.15 | 0.4997 | 1019.0 |
| 313.15 | 0.5502 | 1006.0 |
| 313.15 | 0.6012 | 993.0 |
| 313.15 | 0.6527 | 981.0 |
| 313.15 | 0.7021 | 970.0 |
| 313.15 | 0.7519 | 961.0 |
| 313.15 | 0.8021 | 952.0 |
| 313.15 | 0.8518 | 945.0 |
| 313.15 | 0.9024 | 939.0 |
| 313.15 | 0.9510 | 936.0 |
| 313.15 | 1.0000 | 934.0 |
Speed of sound, m/s [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Trichloromethane (1) - Liquid | Speed of sound, m/s - Liquid |
| 298.15 | 0.0000 | 1235.0 |
| 298.15 | 0.0512 | 1215.0 |
| 298.15 | 0.1000 | 1198.0 |
| 298.15 | 0.1490 | 1180.0 |
| 298.15 | 0.2009 | 1163.0 |
| 298.15 | 0.2506 | 1146.0 |
| 298.15 | 0.2999 | 1130.0 |
| 298.15 | 0.3659 | 1110.0 |
| 298.15 | 0.4070 | 1097.0 |
| 298.15 | 0.4515 | 1085.0 |
| 298.15 | 0.4997 | 1071.0 |
| 298.15 | 0.5502 | 1058.0 |
| 298.15 | 0.6012 | 1045.0 |
| 298.15 | 0.6527 | 1033.0 |
| 298.15 | 0.7021 | 1022.0 |
| 298.15 | 0.7519 | 1013.0 |
| 298.15 | 0.8021 | 1004.0 |
| 298.15 | 0.8518 | 997.0 |
| 298.15 | 0.9024 | 992.0 |
| 298.15 | 0.9510 | 987.0 |
| 298.15 | 1.0000 | 985.0 |
| 308.15 | 0.0000 | 1210.0 |
| 308.15 | 0.0512 | 1190.0 |
| 308.15 | 0.1000 | 1171.0 |
| 308.15 | 0.1490 | 1153.0 |
| 308.15 | 0.2009 | 1134.0 |
| 308.15 | 0.2506 | 1116.0 |
| 308.15 | 0.2999 | 1099.0 |
| 308.15 | 0.3659 | 1078.0 |
| 308.15 | 0.4070 | 1065.0 |
| 308.15 | 0.4515 | 1051.0 |
| 308.15 | 0.4997 | 1037.0 |
| 308.15 | 0.5502 | 1024.0 |
| 308.15 | 0.6012 | 1011.0 |
| 308.15 | 0.6527 | 998.0 |
| 308.15 | 0.7021 | 987.0 |
| 308.15 | 0.7519 | 978.0 |
| 308.15 | 0.8021 | 969.0 |
| 308.15 | 0.8518 | 962.0 |
| 308.15 | 0.9024 | 956.0 |
| 308.15 | 0.9510 | 952.0 |
| 308.15 | 1.0000 | 950.0 |
Speed of sound, m/s [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Trichloromethane (1) - Liquid | Speed of sound, m/s - Liquid |
| 303.15 | 0.0000 | 1227.0 |
| 303.15 | 0.0513 | 1207.0 |
| 303.15 | 0.0999 | 1189.0 |
| 303.15 | 0.1490 | 1170.0 |
| 303.15 | 0.2009 | 1152.0 |
| 303.15 | 0.2506 | 1134.0 |
| 303.15 | 0.2999 | 1118.0 |
| 303.15 | 0.3659 | 1097.0 |
| 303.15 | 0.4070 | 1084.0 |
| 303.15 | 0.4515 | 1071.0 |
| 303.15 | 0.4997 | 1056.0 |
| 303.15 | 0.5502 | 1043.0 |
| 303.15 | 0.6011 | 1030.0 |
| 303.15 | 0.6527 | 1018.0 |
| 303.15 | 0.7020 | 1007.0 |
| 303.15 | 0.7519 | 997.0 |
| 303.15 | 0.8020 | 989.0 |
| 303.15 | 0.8517 | 981.0 |
| 303.15 | 0.9023 | 975.0 |
| 303.15 | 0.9509 | 971.0 |
| 303.15 | 1.0000 | 969.0 |
| 313.15 | 0.0000 | 1193.0 |
| 313.15 | 0.0512 | 1172.0 |
| 313.15 | 0.1000 | 1154.0 |
| 313.15 | 0.1490 | 1135.0 |
| 313.15 | 0.2009 | 1116.0 |
| 313.15 | 0.2506 | 1098.0 |
| 313.15 | 0.2999 | 1081.0 |
| 313.15 | 0.3659 | 1060.0 |
| 313.15 | 0.4070 | 1047.0 |
| 313.15 | 0.4515 | 1034.0 |
| 313.15 | 0.4997 | 1019.0 |
| 313.15 | 0.5502 | 1006.0 |
| 313.15 | 0.6012 | 993.0 |
| 313.15 | 0.6527 | 981.0 |
| 313.15 | 0.7021 | 970.0 |
| 313.15 | 0.7519 | 961.0 |
| 313.15 | 0.8021 | 952.0 |
| 313.15 | 0.8518 | 945.0 |
| 313.15 | 0.9024 | 939.0 |
| 313.15 | 0.9510 | 936.0 |
| 313.15 | 1.0000 | 934.0 |
Vapor Liquid Equilibrium at Constant Pressure [ref]
Operational condition: Pressure, kPa = 101.33 (VLE)
| Fixed | Measured | |
|---|---|---|
| T [K] - VLE | x1[mol/mol] of Trichloromethane (1) - Liquid | y1[mol/mol] of Trichloromethane (1) - Vapour |
| 390.65 | 0.0000 | 0.0000 |
| 382.15 | 0.0645 | 0.5250 |
| 377.65 | 0.1000 | 0.6350 |
| 373.15 | 0.1342 | 0.7500 |
| 365.15 | 0.2000 | 0.8550 |
| 364.65 | 0.2100 | 0.9000 |
| 356.45 | 0.2924 | 0.9150 |
| 356.15 | 0.3000 | 0.8800 |
| 351.65 | 0.3815 | 0.9450 |
| 350.65 | 0.4000 | 0.9150 |
| 347.15 | 0.4810 | 0.9450 |
| 346.45 | 0.5000 | 0.9250 |
| 343.35 | 0.5900 | 0.9450 |
| 342.95 | 0.6000 | 0.9450 |
| 340.15 | 0.7000 | 0.9450 |
| 339.75 | 0.7125 | 0.9650 |
| 338.15 | 0.8000 | 0.9800 |
| 337.15 | 0.8475 | 0.9650 |
| 336.35 | 0.9000 | 0.9800 |
| 334.35 | 1.0000 | 1.0000 |
Vapor Liquid Equilibrium at Constant Pressure [ref]
Operational condition: Pressure, kPa = 101.33 (VLE)
| Fixed | Measured | |
|---|---|---|
| T [K] - VLE | x1[mol/mol] of Trichloromethane (1) - Liquid | y1[mol/mol] of Trichloromethane (1) - Vapour |
| 388.25 | 0.0180 | 0.1000 |
| 386.95 | 0.0300 | 0.1640 |
| 379.55 | 0.0764 | 0.3660 |
| 372.85 | 0.1388 | 0.5680 |
| 366.55 | 0.2016 | 0.6950 |
| 363.45 | 0.2272 | 0.7280 |
| 362.45 | 0.2484 | 0.7480 |
| 357.95 | 0.3036 | 0.8080 |
| 357.55 | 0.3156 | 0.8120 |
| 355.35 | 0.3452 | 0.8400 |
| 353.15 | 0.3838 | 0.8560 |
| 351.85 | 0.4060 | 0.8700 |
| 350.65 | 0.4244 | 0.8820 |
| 348.25 | 0.4798 | 0.8980 |
| 347.75 | 0.4940 | 0.9050 |
| 346.15 | 0.5300 | 0.9190 |
| 343.95 | 0.5980 | 0.9320 |
| 342.35 | 0.6524 | 0.9440 |
| 340.35 | 0.7220 | 0.9550 |
| 339.45 | 0.7698 | 0.9600 |
| 338.55 | 0.8084 | 0.9680 |
| 337.65 | 0.8528 | 0.9740 |
| 337.05 | 0.9032 | 0.9820 |
| 335.75 | 0.9536 | 0.9910 |
Vapor Liquid Equilibrium at Constant Pressure [ref]
Operational condition: Pressure, kPa = 105 (VLE)
| Fixed | Measured | |
|---|---|---|
| T [K] - VLE | x1[mol/mol] of Trichloromethane (1) - Liquid | y1[mol/mol] of Trichloromethane (1) - Vapour |
| 391.61 | 0.0000 | 0.0000 |
| 390.62 | 0.0091 | 0.0449 |
| 388.96 | 0.0213 | 0.1255 |
| 387.43 | 0.0357 | 0.1801 |
| 383.69 | 0.0612 | 0.3066 |
| 380.17 | 0.0865 | 0.3937 |
| 376.14 | 0.1195 | 0.4974 |
| 370.37 | 0.1707 | 0.6171 |
| 365.64 | 0.2203 | 0.6899 |
| 361.9 | 0.2644 | 0.7575 |
| 357.72 | 0.3247 | 0.8065 |
| 354.43 | 0.3773 | 0.8499 |
| 351.34 | 0.4278 | 0.8767 |
| 349.62 | 0.4624 | 0.8909 |
| 347.67 | 0.5091 | 0.9166 |
| 343.31 | 0.6386 | 0.9405 |
| 341.13 | 0.6967 | 0.9461 |
| 340.09 | 0.7445 | 0.9497 |
| 339.67 | 0.7798 | 0.9608 |
| 339.36 | 0.7981 | 0.9633 |
| 339.09 | 0.8113 | 0.9635 |
| 337.54 | 0.8755 | 0.9762 |
| 336.6 | 0.9400 | 0.9893 |
| 336.34 | 0.9661 | 0.9893 |
| 335.56 | 0.9804 | 0.9921 |
| 335.37 | 1.0000 | 1.0000 |
Sources
- Dortmund Data Bank Vapor-Liquid Equilibrium Data
- Temperature Dependence of Densities and Excess Molar Volumes of the Ternary Mixture (1-Butanol + Chloroform + Benzene) and its Binary Constituents (1-Butanol + Chloroform and 1-Butanol + Benzene)
- Densities, viscosities, and ultrasonic velocity studies of binary mixtures of trichloromethane with methanol, ethanol, propan-1-ol, and butan-1-ol at T=(298.15 and 308.15) K
- Densities, Viscosities, and Ultrasonic Velocity Studies of Binary Mixtures of Chloroform with Propan-1-ol and Butan-1-ol at (303.15 and 313.15) K