Mixture of Trichloromethane + Methyl Alcohol

Datasets

1. Mole fraction (4)
2. η - Viscosity, Pa*s (4)
3. n₀ - Refractive index (Na D-line) (2)
4. ρ_l - Mass density, kg/m3 (6)
5. c_sound,fluid - Speed of Sound, m/s (2)
6. T_boil - Boiling temperature at pressure P, K (4)
7. Vapor Liquid Equilibrium at Constant Temperature (2)

Mole fraction of Trichloromethane (1) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Trichloromethane (1) - Liquid	Mole fraction of Trichloromethane (1) - Gas
0.0000	0.0000
0.0460	0.1200
0.0890	0.2040
0.1390	0.3060
0.1880	0.3630
0.2370	0.4300
0.2810	0.4670
0.3240	0.5080
0.3830	0.5500
0.4330	0.5750
0.4910	0.5990
0.5660	0.6160
0.5890	0.6290
0.6310	0.6500
0.7020	0.6620
0.7420	0.6800
0.7900	0.7000
0.8370	0.7170
0.9040	0.7650
0.9350	0.8200
1.0000	1.0000

Mole fraction of Trichloromethane (1) [ref]

Operational condition: Pressure, kPa = 100 (Gas)

Mole fraction of Trichloromethane (1) - Liquid	Mole fraction of Trichloromethane (1) - Gas
0.0000	0.0000
0.0231	0.0629
0.0413	0.1078
0.0584	0.1431
0.0805	0.1916
0.1081	0.2463
0.1382	0.2991
0.1767	0.3558
0.2218	0.4127
0.2702	0.4647
0.3218	0.5066
0.3685	0.5374
0.4203	0.5648
0.4642	0.5861
0.5092	0.6059
0.5521	0.6231
0.5977	0.6354
0.6347	0.6454
0.6685	0.6544
0.7128	0.6656
0.7452	0.6769
0.7821	0.6893
0.8178	0.7060
0.8562	0.7268
0.8857	0.7453
0.9131	0.7688
0.9407	0.8012
0.9629	0.8408
0.9805	0.9123
1.0000	1.0000

Mole fraction of Trichloromethane (1) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Trichloromethane (1) - Liquid	Mole fraction of Trichloromethane (1) - Gas
0.0000	0.0000
0.0460	0.1200
0.0890	0.2040
0.1390	0.3060
0.1880	0.3630
0.2370	0.4300
0.2810	0.4670
0.3240	0.5080
0.3830	0.5500
0.4330	0.5750
0.4910	0.5990
0.5660	0.6160
0.5890	0.6290
0.6310	0.6500
0.7020	0.6620
0.7420	0.6800
0.7900	0.7000
0.8370	0.7170
0.9040	0.7650
0.9350	0.8200
1.0000	1.0000

Mole fraction of Trichloromethane (1) [ref]

Operational condition: Pressure, kPa = 100 (Gas)

Mole fraction of Trichloromethane (1) - Liquid	Mole fraction of Trichloromethane (1) - Gas
0.0000	0.0000
0.0231	0.0629
0.0413	0.1078
0.0584	0.1431
0.0805	0.1916
0.1081	0.2463
0.1382	0.2991
0.1767	0.3558
0.2218	0.4127
0.2702	0.4647
0.3218	0.5066
0.3685	0.5374
0.4203	0.5648
0.4642	0.5861
0.5092	0.6059
0.5521	0.6231
0.5977	0.6354
0.6347	0.6454
0.6685	0.6544
0.7128	0.6656
0.7452	0.6769
0.7821	0.6893
0.8178	0.7060
0.8562	0.7268
0.8857	0.7453
0.9131	0.7688
0.9407	0.8012
0.9629	0.8408
0.9805	0.9123
1.0000	1.0000

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Methyl Alcohol (2) - Liquid	Viscosity, Pa*s - Liquid
298.15	0.0000	0.0006
298.15	0.0999	0.0006
298.15	0.2012	0.0006
298.15	0.3015	0.0007
298.15	0.3991	0.0007
298.15	0.5020	0.0007
298.15	0.5998	0.0007
298.15	0.7012	0.0006
298.15	0.7998	0.0006
298.15	0.9001	0.0006
298.15	1.0000	0.0005
303.15	0.0000	0.0006
303.15	0.0999	0.0006
303.15	0.2012	0.0006
303.15	0.3015	0.0006
303.15	0.3991	0.0006
303.15	0.5020	0.0006
303.15	0.5998	0.0006
303.15	0.7012	0.0006
303.15	0.7998	0.0006
303.15	0.9001	0.0005
303.15	1.0000	0.0005
308.15	0.0000	0.0005
308.15	0.0999	0.0006
308.15	0.2012	0.0006
308.15	0.3015	0.0006
308.15	0.3991	0.0006
308.15	0.5020	0.0006
308.15	0.5998	0.0006
308.15	0.7012	0.0005
308.15	0.7998	0.0005
308.15	0.9001	0.0005
308.15	1.0000	0.0005
313.15	0.0000	0.0005
313.15	0.0999	0.0005
313.15	0.2012	0.0005
313.15	0.3015	0.0005
313.15	0.3991	0.0005
313.15	0.5020	0.0005
313.15	0.5998	0.0005
313.15	0.7012	0.0005
313.15	0.7998	0.0005
313.15	0.9001	0.0005
313.15	1.0000	0.0004
318.15	0.0000	0.0005
318.15	0.0999	0.0005
318.15	0.2012	0.0005
318.15	0.3015	0.0005
318.15	0.3991	0.0005
318.15	0.5020	0.0005
318.15	0.5998	0.0005
318.15	0.7012	0.0005
318.15	0.7998	0.0005
318.15	0.9001	0.0004
318.15	1.0000	0.0004

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	0.0006
298.15	0.0501	0.0006
298.15	0.0959	0.0006
298.15	0.1501	0.0006
298.15	0.2007	0.0007
298.15	0.2499	0.0007
298.15	0.3015	0.0007
298.15	0.3502	0.0007
298.15	0.3966	0.0007
298.15	0.4498	0.0007
298.15	0.5047	0.0006
298.15	0.5506	0.0006
298.15	0.6033	0.0006
298.15	0.6515	0.0006
298.15	0.7032	0.0006
298.15	0.7510	0.0006
298.15	0.7987	0.0006
298.15	0.8500	0.0006
298.15	0.9020	0.0006
298.15	0.9505	0.0006
298.15	1.0000	0.0006
308.15	0.0000	0.0005
308.15	0.0501	0.0005
308.15	0.0959	0.0005
308.15	0.1501	0.0006
308.15	0.2007	0.0006
308.15	0.2499	0.0006
308.15	0.3015	0.0006
308.15	0.3502	0.0006
308.15	0.3966	0.0006
308.15	0.4498	0.0006
308.15	0.5047	0.0006
308.15	0.5506	0.0006
308.15	0.6033	0.0006
308.15	0.6515	0.0006
308.15	0.7032	0.0006
308.15	0.7510	0.0005
308.15	0.7987	0.0005
308.15	0.8500	0.0005
308.15	0.9020	0.0005
308.15	0.9505	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 Methyl Alcohol (2) - Liquid	Viscosity, Pa*s - Liquid
298.15	0.0000	0.0006
298.15	0.0999	0.0006
298.15	0.2012	0.0006
298.15	0.3015	0.0007
298.15	0.3991	0.0007
298.15	0.5020	0.0007
298.15	0.5998	0.0007
298.15	0.7012	0.0006
298.15	0.7998	0.0006
298.15	0.9001	0.0006
298.15	1.0000	0.0005
303.15	0.0000	0.0006
303.15	0.0999	0.0006
303.15	0.2012	0.0006
303.15	0.3015	0.0006
303.15	0.3991	0.0006
303.15	0.5020	0.0006
303.15	0.5998	0.0006
303.15	0.7012	0.0006
303.15	0.7998	0.0006
303.15	0.9001	0.0005
303.15	1.0000	0.0005
308.15	0.0000	0.0005
308.15	0.0999	0.0006
308.15	0.2012	0.0006
308.15	0.3015	0.0006
308.15	0.3991	0.0006
308.15	0.5020	0.0006
308.15	0.5998	0.0006
308.15	0.7012	0.0005
308.15	0.7998	0.0005
308.15	0.9001	0.0005
308.15	1.0000	0.0005
313.15	0.0000	0.0005
313.15	0.0999	0.0005
313.15	0.2012	0.0005
313.15	0.3015	0.0005
313.15	0.3991	0.0005
313.15	0.5020	0.0005
313.15	0.5998	0.0005
313.15	0.7012	0.0005
313.15	0.7998	0.0005
313.15	0.9001	0.0005
313.15	1.0000	0.0004
318.15	0.0000	0.0005
318.15	0.0999	0.0005
318.15	0.2012	0.0005
318.15	0.3015	0.0005
318.15	0.3991	0.0005
318.15	0.5020	0.0005
318.15	0.5998	0.0005
318.15	0.7012	0.0005
318.15	0.7998	0.0005
318.15	0.9001	0.0004
318.15	1.0000	0.0004

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	0.0006
298.15	0.0501	0.0006
298.15	0.0959	0.0006
298.15	0.1501	0.0006
298.15	0.2007	0.0007
298.15	0.2499	0.0007
298.15	0.3015	0.0007
298.15	0.3502	0.0007
298.15	0.3966	0.0007
298.15	0.4498	0.0007
298.15	0.5047	0.0006
298.15	0.5506	0.0006
298.15	0.6033	0.0006
298.15	0.6515	0.0006
298.15	0.7032	0.0006
298.15	0.7510	0.0006
298.15	0.7987	0.0006
298.15	0.8500	0.0006
298.15	0.9020	0.0006
298.15	0.9505	0.0006
298.15	1.0000	0.0006
308.15	0.0000	0.0005
308.15	0.0501	0.0005
308.15	0.0959	0.0005
308.15	0.1501	0.0006
308.15	0.2007	0.0006
308.15	0.2499	0.0006
308.15	0.3015	0.0006
308.15	0.3502	0.0006
308.15	0.3966	0.0006
308.15	0.4498	0.0006
308.15	0.5047	0.0006
308.15	0.5506	0.0006
308.15	0.6033	0.0006
308.15	0.6515	0.0006
308.15	0.7032	0.0006
308.15	0.7510	0.0005
308.15	0.7987	0.0005
308.15	0.8500	0.0005
308.15	0.9020	0.0005
308.15	0.9505	0.0005
308.15	1.0000	0.0005

Refractive index (Na D-line) [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Methyl Alcohol (2) - Liquid	Refractive index (Na D-line) - Liquid
298.15	0.0000	1.4422
298.15	0.0999	1.4379
298.15	0.2012	1.4312
298.15	0.3015	1.4217
298.15	0.3991	1.4115
298.15	0.5020	1.4018
298.15	0.5998	1.3903
298.15	0.7012	1.3789
298.15	0.7998	1.3649
298.15	0.9001	1.3485
298.15	1.0000	1.3271
303.15	0.0000	1.4397
303.15	0.0999	1.4327
303.15	0.2012	1.4257
303.15	0.3015	1.4171
303.15	0.3991	1.4084
303.15	0.5020	1.3979
303.15	0.5998	1.3881
303.15	0.7012	1.377
303.15	0.7998	1.3633
303.15	0.9001	1.3467
303.15	1.0000	1.3245
308.15	0.0000	1.4356
308.15	0.0999	1.4289
308.15	0.2012	1.4212
308.15	0.3015	1.4116
308.15	0.3991	1.4031
308.15	0.5020	1.3953
308.15	0.5998	1.3856
308.15	0.7012	1.3729
308.15	0.7998	1.3592
308.15	0.9001	1.3443
308.15	1.0000	1.323
313.15	0.0000	1.4338
313.15	0.0999	1.427
313.15	0.2012	1.4211
313.15	0.3015	1.4127
313.15	0.3991	1.4049
313.15	0.5020	1.3943
313.15	0.5998	1.3839
313.15	0.7012	1.3722
313.15	0.7998	1.3592
313.15	0.9001	1.3461
313.15	1.0000	1.3208
318.15	0.0000	1.4297
318.15	0.0999	1.4201
318.15	0.2012	1.4174
318.15	0.3015	1.4093
318.15	0.3991	1.4023
318.15	0.5020	1.3927
318.15	0.5998	1.3817
318.15	0.7012	1.3719
318.15	0.7998	1.3576
318.15	0.9001	1.3406
318.15	1.0000	1.3184

Refractive index (Na D-line) [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Methyl Alcohol (2) - Liquid	Refractive index (Na D-line) - Liquid
298.15	0.0000	1.4422
298.15	0.0999	1.4379
298.15	0.2012	1.4312
298.15	0.3015	1.4217
298.15	0.3991	1.4115
298.15	0.5020	1.4018
298.15	0.5998	1.3903
298.15	0.7012	1.3789
298.15	0.7998	1.3649
298.15	0.9001	1.3485
298.15	1.0000	1.3271
303.15	0.0000	1.4397
303.15	0.0999	1.4327
303.15	0.2012	1.4257
303.15	0.3015	1.4171
303.15	0.3991	1.4084
303.15	0.5020	1.3979
303.15	0.5998	1.3881
303.15	0.7012	1.377
303.15	0.7998	1.3633
303.15	0.9001	1.3467
303.15	1.0000	1.3245
308.15	0.0000	1.4356
308.15	0.0999	1.4289
308.15	0.2012	1.4212
308.15	0.3015	1.4116
308.15	0.3991	1.4031
308.15	0.5020	1.3953
308.15	0.5998	1.3856
308.15	0.7012	1.3729
308.15	0.7998	1.3592
308.15	0.9001	1.3443
308.15	1.0000	1.323
313.15	0.0000	1.4338
313.15	0.0999	1.427
313.15	0.2012	1.4211
313.15	0.3015	1.4127
313.15	0.3991	1.4049
313.15	0.5020	1.3943
313.15	0.5998	1.3839
313.15	0.7012	1.3722
313.15	0.7998	1.3592
313.15	0.9001	1.3461
313.15	1.0000	1.3208
318.15	0.0000	1.4297
318.15	0.0999	1.4201
318.15	0.2012	1.4174
318.15	0.3015	1.4093
318.15	0.3991	1.4023
318.15	0.5020	1.3927
318.15	0.5998	1.3817
318.15	0.7012	1.3719
318.15	0.7998	1.3576
318.15	0.9001	1.3406
318.15	1.0000	1.3184

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Methyl Alcohol (2) - Liquid	Mass density, kg/m3 - Liquid
298.15	0.0000	1478.75
298.15	0.0999	1443.84
298.15	0.2012	1403.84
298.15	0.3015	1358.87
298.15	0.3991	1309.46
298.15	0.5020	1250.29
298.15	0.5998	1186.04
298.15	0.7012	1108.93
298.15	0.7998	1020.91
298.15	0.9001	914.54
298.15	1.0000	787.21
303.15	0.0000	1469.16
303.15	0.0999	1434.0
303.15	0.2012	1394.48
303.15	0.3015	1350.17
303.15	0.3991	1301.28
303.15	0.5020	1242.63
303.15	0.5998	1178.79
303.15	0.7012	1102.19
303.15	0.7998	1014.72
303.15	0.9001	909.0
303.15	1.0000	782.75
308.15	0.0000	1460.01
308.15	0.0999	1424.97
308.15	0.2012	1385.67
308.15	0.3015	1341.86
308.15	0.3991	1293.54
308.15	0.5020	1235.37
308.15	0.5998	1171.85
308.15	0.7012	1095.59
308.15	0.7998	1008.7
308.15	0.9001	903.73
308.15	1.0000	777.56
313.15	0.0000	1450.39
313.15	0.0999	1415.61
313.15	0.2012	1376.61
313.15	0.3015	1333.14
313.15	0.3991	1285.19
313.15	0.5020	1227.45
313.15	0.5998	1164.4
313.15	0.7012	1088.7
313.15	0.7998	1002.44
313.15	0.9001	898.23
313.15	1.0000	772.97
318.15	0.0000	1440.03
318.15	0.0999	1405.51
318.15	0.2012	1366.88
318.15	0.3015	1323.78
318.15	0.3991	1276.2
318.15	0.5020	1218.91
318.15	0.5998	1156.37
318.15	0.7012	1081.29
318.15	0.7998	995.73
318.15	0.9001	892.36
318.15	1.0000	768.03

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	786.3
298.15	0.0501	852.42
298.15	0.0959	907.6
298.15	0.1501	967.31
298.15	0.2007	1018.13
298.15	0.2499	1063.89
298.15	0.3015	1107.99
298.15	0.3502	1146.56
298.15	0.3966	1180.85
298.15	0.4498	1217.39
298.15	0.5047	1252.37
298.15	0.5506	1279.51
298.15	0.6033	1308.68
298.15	0.6515	1333.97
298.15	0.7032	1359.31
298.15	0.7510	1381.31
298.15	0.7987	1402.09
298.15	0.8500	1423.32
298.15	0.9020	1443.49
298.15	0.9505	1461.44
298.15	1.0000	1478.82
308.15	0.0000	776.6
308.15	0.0501	842.0
308.15	0.0959	896.56
308.15	0.1501	955.55
308.15	0.2007	1005.77
308.15	0.2499	1050.91
308.15	0.3015	1094.32
308.15	0.3502	1132.48
308.15	0.3966	1166.26
308.15	0.4498	1202.34
308.15	0.5047	1236.78
308.15	0.5506	1263.63
308.15	0.6033	1292.64
308.15	0.6515	1317.33
308.15	0.7032	1342.39
308.15	0.7510	1363.96
308.15	0.7987	1384.31
308.15	0.8500	1405.26
308.15	0.9020	1425.07
308.15	0.9505	1442.54
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 Methyl Alcohol (2) - Liquid	Mass density, kg/m3 - Liquid
288.15	0.0000	1498.077
288.15	0.0298	1487.346
288.15	0.0492	1480.267
288.15	0.0724	1471.759
288.15	0.0942	1463.439
288.15	0.1282	1450.192
288.15	0.1586	1437.963
288.15	0.2444	1401.121
288.15	0.2956	1377.441
288.15	0.3383	1356.507
288.15	0.3980	1325.255
288.15	0.4393	1302.229
288.15	0.4983	1267.1
288.15	0.5505	1233.392
288.15	0.6022	1197.323
288.15	0.6352	1172.938
288.15	0.6999	1121.29
288.15	0.7500	1077.545
288.15	0.7996	1030.616
288.15	0.8193	1011.238
288.15	0.8534	975.44
288.15	0.9100	911.539
288.15	0.9300	887.399
288.15	0.9542	857.083
288.15	1.0000	796.093
293.15	0.0000	1488.638
293.15	0.0298	1477.931
293.15	0.0492	1470.881
293.15	0.0724	1462.414
293.15	0.0942	1454.141
293.15	0.1282	1440.98
293.15	0.1586	1428.829
293.15	0.2444	1392.244
293.15	0.2956	1368.733
293.15	0.3383	1347.953
293.15	0.3980	1316.934
293.15	0.4393	1294.082
293.15	0.4983	1259.218
293.15	0.5505	1225.765
293.15	0.6022	1190.011
293.15	0.6352	1165.776
293.15	0.6999	1114.52
293.15	0.7500	1071.098
293.15	0.7996	1024.5
293.15	0.8193	1005.113
293.15	0.8534	969.692
293.15	0.9100	906.188
293.15	0.9300	882.191
293.15	0.9542	852.051
293.15	1.0000	791.4
298.15	0.0000	1479.148
298.15	0.0298	1468.465
298.15	0.0492	1461.441
298.15	0.0724	1453.013
298.15	0.0942	1444.789
298.15	0.1282	1431.705
298.15	0.1586	1419.634
298.15	0.2444	1383.302
298.15	0.2956	1359.967
298.15	0.3383	1339.334
298.15	0.3980	1308.55
298.15	0.4393	1285.874
298.15	0.4983	1251.28
298.15	0.5505	1218.088
298.15	0.6022	1182.624
298.15	0.6352	1158.565
298.15	0.6999	1107.707
298.15	0.7500	1064.609
298.15	0.7996	1018.344
298.15	0.8193	998.988
298.15	0.8534	963.915
298.15	0.9100	900.813
298.15	0.9300	876.963
298.15	0.9542	847.0
298.15	1.0000	786.694
303.15	0.0000	1469.612
303.15	0.0298	1458.953
303.15	0.0492	1451.95
303.15	0.0724	1443.554
303.15	0.0942	1435.375
303.15	0.1282	1422.367
303.15	0.1586	1410.374
303.15	0.2444	1374.295
303.15	0.2956	1351.137
303.15	0.3383	1330.656
303.15	0.3980	1300.105
303.15	0.4393	1277.602
303.15	0.4983	1243.281
303.15	0.5505	1210.35
303.15	0.6022	1175.169
303.15	0.6352	1151.299
303.15	0.6999	1100.844
303.15	0.7500	1058.072
303.15	0.7996	1012.148
303.15	0.8193	992.86
303.15	0.8534	958.1
303.15	0.9100	895.41
303.15	0.9300	871.71
303.15	0.9542	841.927
303.15	1.0000	781.966
308.15	0.0000	1460.025
308.15	0.0298	1449.385
308.15	0.0492	1442.4
308.15	0.0724	1434.035
308.15	0.0942	1425.891
308.15	0.1282	1412.964
308.15	0.1586	1401.043
308.15	0.2444	1365.219
308.15	0.2956	1342.24
308.15	0.3383	1321.902
308.15	0.3980	1291.589
308.15	0.4393	1269.262
308.15	0.4983	1235.216
308.15	0.5505	1202.554
308.15	0.6022	1167.65
308.15	0.6352	1143.978
308.15	0.6999	1093.926
308.15	0.7500	1051.484
308.15	0.7996	1005.907
308.15	0.8193	986.761
308.15	0.8534	952.24
308.15	0.9100	889.975
308.15	0.9300	866.422
308.15	0.9542	836.829
308.15	1.0000	777.213
313.15	0.0000	1450.413
313.15	0.0298	1439.804
313.15	0.0492	1432.835
313.15	0.0724	1424.49
313.15	0.0942	1416.399
313.15	0.1282	1403.524
313.15	0.1586	1391.678
313.15	0.2444	1356.097
313.15	0.2956	1333.29
313.15	0.3383	1313.094
313.15	0.3980	1283.024
313.15	0.4393	1260.885
313.15	0.4983	1227.126
313.15	0.5505	1194.712
313.15	0.6022	1160.084
313.15	0.6352	1136.625
313.15	0.6999	1086.962
313.15	0.7500	1044.851
313.15	0.7996	999.622
313.15	0.8193	980.633
313.15	0.8534	946.342
313.15	0.9100	884.513
313.15	0.9300	861.11
313.15	0.9542	831.705
313.15	1.0000	772.443

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Methyl Alcohol (2) - Liquid	Mass density, kg/m3 - Liquid
298.15	0.0000	1478.75
298.15	0.0999	1443.84
298.15	0.2012	1403.84
298.15	0.3015	1358.87
298.15	0.3991	1309.46
298.15	0.5020	1250.29
298.15	0.5998	1186.04
298.15	0.7012	1108.93
298.15	0.7998	1020.91
298.15	0.9001	914.54
298.15	1.0000	787.21
303.15	0.0000	1469.16
303.15	0.0999	1434.0
303.15	0.2012	1394.48
303.15	0.3015	1350.17
303.15	0.3991	1301.28
303.15	0.5020	1242.63
303.15	0.5998	1178.79
303.15	0.7012	1102.19
303.15	0.7998	1014.72
303.15	0.9001	909.0
303.15	1.0000	782.75
308.15	0.0000	1460.01
308.15	0.0999	1424.97
308.15	0.2012	1385.67
308.15	0.3015	1341.86
308.15	0.3991	1293.54
308.15	0.5020	1235.37
308.15	0.5998	1171.85
308.15	0.7012	1095.59
308.15	0.7998	1008.7
308.15	0.9001	903.73
308.15	1.0000	777.56
313.15	0.0000	1450.39
313.15	0.0999	1415.61
313.15	0.2012	1376.61
313.15	0.3015	1333.14
313.15	0.3991	1285.19
313.15	0.5020	1227.45
313.15	0.5998	1164.4
313.15	0.7012	1088.7
313.15	0.7998	1002.44
313.15	0.9001	898.23
313.15	1.0000	772.97
318.15	0.0000	1440.03
318.15	0.0999	1405.51
318.15	0.2012	1366.88
318.15	0.3015	1323.78
318.15	0.3991	1276.2
318.15	0.5020	1218.91
318.15	0.5998	1156.37
318.15	0.7012	1081.29
318.15	0.7998	995.73
318.15	0.9001	892.36
318.15	1.0000	768.03

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	786.3
298.15	0.0501	852.42
298.15	0.0959	907.6
298.15	0.1501	967.31
298.15	0.2007	1018.13
298.15	0.2499	1063.89
298.15	0.3015	1107.99
298.15	0.3502	1146.56
298.15	0.3966	1180.85
298.15	0.4498	1217.39
298.15	0.5047	1252.37
298.15	0.5506	1279.51
298.15	0.6033	1308.68
298.15	0.6515	1333.97
298.15	0.7032	1359.31
298.15	0.7510	1381.31
298.15	0.7987	1402.09
298.15	0.8500	1423.32
298.15	0.9020	1443.49
298.15	0.9505	1461.44
298.15	1.0000	1478.82
308.15	0.0000	776.6
308.15	0.0501	842.0
308.15	0.0959	896.56
308.15	0.1501	955.55
308.15	0.2007	1005.77
308.15	0.2499	1050.91
308.15	0.3015	1094.32
308.15	0.3502	1132.48
308.15	0.3966	1166.26
308.15	0.4498	1202.34
308.15	0.5047	1236.78
308.15	0.5506	1263.63
308.15	0.6033	1292.64
308.15	0.6515	1317.33
308.15	0.7032	1342.39
308.15	0.7510	1363.96
308.15	0.7987	1384.31
308.15	0.8500	1405.26
308.15	0.9020	1425.07
308.15	0.9505	1442.54
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 Methyl Alcohol (2) - Liquid	Mass density, kg/m3 - Liquid
288.15	0.0000	1498.077
288.15	0.0298	1487.346
288.15	0.0492	1480.267
288.15	0.0724	1471.759
288.15	0.0942	1463.439
288.15	0.1282	1450.192
288.15	0.1586	1437.963
288.15	0.2444	1401.121
288.15	0.2956	1377.441
288.15	0.3383	1356.507
288.15	0.3980	1325.255
288.15	0.4393	1302.229
288.15	0.4983	1267.1
288.15	0.5505	1233.392
288.15	0.6022	1197.323
288.15	0.6352	1172.938
288.15	0.6999	1121.29
288.15	0.7500	1077.545
288.15	0.7996	1030.616
288.15	0.8193	1011.238
288.15	0.8534	975.44
288.15	0.9100	911.539
288.15	0.9300	887.399
288.15	0.9542	857.083
288.15	1.0000	796.093
293.15	0.0000	1488.638
293.15	0.0298	1477.931
293.15	0.0492	1470.881
293.15	0.0724	1462.414
293.15	0.0942	1454.141
293.15	0.1282	1440.98
293.15	0.1586	1428.829
293.15	0.2444	1392.244
293.15	0.2956	1368.733
293.15	0.3383	1347.953
293.15	0.3980	1316.934
293.15	0.4393	1294.082
293.15	0.4983	1259.218
293.15	0.5505	1225.765
293.15	0.6022	1190.011
293.15	0.6352	1165.776
293.15	0.6999	1114.52
293.15	0.7500	1071.098
293.15	0.7996	1024.5
293.15	0.8193	1005.113
293.15	0.8534	969.692
293.15	0.9100	906.188
293.15	0.9300	882.191
293.15	0.9542	852.051
293.15	1.0000	791.4
298.15	0.0000	1479.148
298.15	0.0298	1468.465
298.15	0.0492	1461.441
298.15	0.0724	1453.013
298.15	0.0942	1444.789
298.15	0.1282	1431.705
298.15	0.1586	1419.634
298.15	0.2444	1383.302
298.15	0.2956	1359.967
298.15	0.3383	1339.334
298.15	0.3980	1308.55
298.15	0.4393	1285.874
298.15	0.4983	1251.28
298.15	0.5505	1218.088
298.15	0.6022	1182.624
298.15	0.6352	1158.565
298.15	0.6999	1107.707
298.15	0.7500	1064.609
298.15	0.7996	1018.344
298.15	0.8193	998.988
298.15	0.8534	963.915
298.15	0.9100	900.813
298.15	0.9300	876.963
298.15	0.9542	847.0
298.15	1.0000	786.694
303.15	0.0000	1469.612
303.15	0.0298	1458.953
303.15	0.0492	1451.95
303.15	0.0724	1443.554
303.15	0.0942	1435.375
303.15	0.1282	1422.367
303.15	0.1586	1410.374
303.15	0.2444	1374.295
303.15	0.2956	1351.137
303.15	0.3383	1330.656
303.15	0.3980	1300.105
303.15	0.4393	1277.602
303.15	0.4983	1243.281
303.15	0.5505	1210.35
303.15	0.6022	1175.169
303.15	0.6352	1151.299
303.15	0.6999	1100.844
303.15	0.7500	1058.072
303.15	0.7996	1012.148
303.15	0.8193	992.86
303.15	0.8534	958.1
303.15	0.9100	895.41
303.15	0.9300	871.71
303.15	0.9542	841.927
303.15	1.0000	781.966
308.15	0.0000	1460.025
308.15	0.0298	1449.385
308.15	0.0492	1442.4
308.15	0.0724	1434.035
308.15	0.0942	1425.891
308.15	0.1282	1412.964
308.15	0.1586	1401.043
308.15	0.2444	1365.219
308.15	0.2956	1342.24
308.15	0.3383	1321.902
308.15	0.3980	1291.589
308.15	0.4393	1269.262
308.15	0.4983	1235.216
308.15	0.5505	1202.554
308.15	0.6022	1167.65
308.15	0.6352	1143.978
308.15	0.6999	1093.926
308.15	0.7500	1051.484
308.15	0.7996	1005.907
308.15	0.8193	986.761
308.15	0.8534	952.24
308.15	0.9100	889.975
308.15	0.9300	866.422
308.15	0.9542	836.829
308.15	1.0000	777.213
313.15	0.0000	1450.413
313.15	0.0298	1439.804
313.15	0.0492	1432.835
313.15	0.0724	1424.49
313.15	0.0942	1416.399
313.15	0.1282	1403.524
313.15	0.1586	1391.678
313.15	0.2444	1356.097
313.15	0.2956	1333.29
313.15	0.3383	1313.094
313.15	0.3980	1283.024
313.15	0.4393	1260.885
313.15	0.4983	1227.126
313.15	0.5505	1194.712
313.15	0.6022	1160.084
313.15	0.6352	1136.625
313.15	0.6999	1086.962
313.15	0.7500	1044.851
313.15	0.7996	999.622
313.15	0.8193	980.633
313.15	0.8534	946.342
313.15	0.9100	884.513
313.15	0.9300	861.11
313.15	0.9542	831.705
313.15	1.0000	772.443

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	1109.0
298.15	0.0501	1080.0
298.15	0.0959	1060.0
298.15	0.1501	1041.0
298.15	0.2007	1028.0
298.15	0.2499	1017.0
298.15	0.3015	1007.0
298.15	0.3502	1000.0
298.15	0.3966	994.0
298.15	0.4498	989.0
298.15	0.5047	984.0
298.15	0.5506	981.0
298.15	0.6033	979.0
298.15	0.6515	977.0
298.15	0.7032	976.0
298.15	0.7510	976.0
298.15	0.7987	976.0
298.15	0.8500	977.0
298.15	0.9020	979.0
298.15	0.9505	982.0
298.15	1.0000	985.0
308.15	0.0000	1076.0
308.15	0.0501	1048.0
308.15	0.0959	1029.0
308.15	0.1501	1010.0
308.15	0.2007	997.0
308.15	0.2499	986.0
308.15	0.3015	976.0
308.15	0.3502	969.0
308.15	0.3966	963.0
308.15	0.4498	958.0
308.15	0.5047	954.0
308.15	0.5506	950.0
308.15	0.6033	948.0
308.15	0.6515	946.0
308.15	0.7032	945.0
308.15	0.7510	944.0
308.15	0.7987	944.0
308.15	0.8500	945.0
308.15	0.9020	946.0
308.15	0.9505	948.0
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
298.15	0.0000	1109.0
298.15	0.0501	1080.0
298.15	0.0959	1060.0
298.15	0.1501	1041.0
298.15	0.2007	1028.0
298.15	0.2499	1017.0
298.15	0.3015	1007.0
298.15	0.3502	1000.0
298.15	0.3966	994.0
298.15	0.4498	989.0
298.15	0.5047	984.0
298.15	0.5506	981.0
298.15	0.6033	979.0
298.15	0.6515	977.0
298.15	0.7032	976.0
298.15	0.7510	976.0
298.15	0.7987	976.0
298.15	0.8500	977.0
298.15	0.9020	979.0
298.15	0.9505	982.0
298.15	1.0000	985.0
308.15	0.0000	1076.0
308.15	0.0501	1048.0
308.15	0.0959	1029.0
308.15	0.1501	1010.0
308.15	0.2007	997.0
308.15	0.2499	986.0
308.15	0.3015	976.0
308.15	0.3502	969.0
308.15	0.3966	963.0
308.15	0.4498	958.0
308.15	0.5047	954.0
308.15	0.5506	950.0
308.15	0.6033	948.0
308.15	0.6515	946.0
308.15	0.7032	945.0
308.15	0.7510	944.0
308.15	0.7987	944.0
308.15	0.8500	945.0
308.15	0.9020	946.0
308.15	0.9505	948.0
308.15	1.0000	950.0

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Trichloromethane (1) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	337.90
0.0460	335.90
0.0890	334.20
0.1390	332.50
0.1880	331.20
0.2370	329.90
0.2810	329.10
0.3240	328.30
0.3830	327.80
0.4330	327.30
0.4910	327.10
0.5660	326.90
0.5890	326.80
0.6310	326.70
0.7020	326.80
0.7420	327.00
0.7900	327.10
0.8370	327.40
0.9040	328.40
0.9350	329.60
1.0000	334.10

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 100 (Gas)

Mole fraction of Trichloromethane (1) - Liquid	Boiling temperature at pressure P, K - Gas
0.0000	337.41
0.0231	336.29
0.0413	335.51
0.0584	334.80
0.0805	333.97
0.1081	332.99
0.1382	332.00
0.1767	330.86
0.2218	329.74
0.2702	328.73
0.3218	327.92
0.3685	327.30
0.4203	326.93
0.4642	326.64
0.5092	326.42
0.5521	326.29
0.5977	326.22
0.6347	326.17
0.6685	326.17
0.7128	326.21
0.7452	326.27
0.7821	326.41
0.8178	326.60
0.8562	326.91
0.8857	327.27
0.9131	327.85
0.9407	328.67
0.9629	329.77
0.9805	331.45
1.0000	333.96

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Trichloromethane (1) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	337.90
0.0460	335.90
0.0890	334.20
0.1390	332.50
0.1880	331.20
0.2370	329.90
0.2810	329.10
0.3240	328.30
0.3830	327.80
0.4330	327.30
0.4910	327.10
0.5660	326.90
0.5890	326.80
0.6310	326.70
0.7020	326.80
0.7420	327.00
0.7900	327.10
0.8370	327.40
0.9040	328.40
0.9350	329.60
1.0000	334.10

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 100 (Gas)

Mole fraction of Trichloromethane (1) - Liquid	Boiling temperature at pressure P, K - Gas
0.0000	337.41
0.0231	336.29
0.0413	335.51
0.0584	334.80
0.0805	333.97
0.1081	332.99
0.1382	332.00
0.1767	330.86
0.2218	329.74
0.2702	328.73
0.3218	327.92
0.3685	327.30
0.4203	326.93
0.4642	326.64
0.5092	326.42
0.5521	326.29
0.5977	326.22
0.6347	326.17
0.6685	326.17
0.7128	326.21
0.7452	326.27
0.7821	326.41
0.8178	326.60
0.8562	326.91
0.8857	327.27
0.9131	327.85
0.9407	328.67
0.9629	329.77
0.9805	331.45
1.0000	333.96

Vapor Liquid Equilibrium at Constant Temperature [ref]

Operational condition: Temperature, K = 308.15 (VLE)

Fixed	Measured
P [kPa] - VLE	x1[mol/mol] of Trichloromethane (1) - Liquid	y1[mol/mol] of Trichloromethane (1) - Vapour
30.704	0.0500	0.1430
33.771	0.1000	0.2630
36.637	0.1500	0.3570
39.41	0.2000	0.4310
41.757	0.2500	0.4900
43.85	0.3000	0.5390
45.383	0.3500	0.5800
46.743	0.4000	0.6100
47.676	0.4500	0.6350
48.329	0.5000	0.6540
48.649	0.5500	0.6680
48.889	0.6000	0.6840
49.049	0.6500	0.6920
49.183	0.7000	0.7040
49.103	0.7500	0.7140
48.863	0.8000	0.7240
48.529	0.8500	0.7440
47.356	0.9000	0.7760
45.33	0.9500	0.8450

Vapor Liquid Equilibrium at Constant Temperature [ref]

Operational condition: Temperature, K = 322.45 (VLE)

Fixed	Measured
P [kPa] - VLE	x1[mol/mol] of Trichloromethane (1) - Liquid	y1[mol/mol] of Trichloromethane (1) - Vapour
58.875	0.0500	0.1380
64.355	0.1000	0.2540
69.968	0.1500	0.3500
74.607	0.2000	0.4240
78.14	0.2500	0.4760
80.807	0.3000	0.5200
82.833	0.3500	0.5500
84.433	0.4000	0.5770
85.713	0.4500	0.5980
86.233	0.5000	0.6190
86.686	0.5500	0.6340
87.006	0.6000	0.6470
87.313	0.6500	0.6590
87.579	0.7000	0.6700
87.566	0.7500	0.6800
87.219	0.8000	0.6940
86.326	0.8500	0.7160
84.34	0.9000	0.7540
80.167	0.9500	0.8240

Sources

• Dortmund Data Bank Vapor-Liquid Equilibrium Data
• Densities, viscosities, and refractive indices of binary and ternary mixtures of methanol, acetone, and chloroform at temperatures from (298.15-318.15) K and ambient pressure
• 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
• Volumetric Properties of the Binary Methanol + Chloroform and Ternary Methanol + Chloroform + Benzene Mixtures at (288.15, 293.15, 298.15, 303.15, 308.15, and 313.15) K
• Isobaric Vapor Liquid Equilibrium for Chloroform + Methanol + 1,3-Dimethylimidazolium Dimethylphosphate at 101.3 kPa
• Isobaric Vapor-Liquid and Liquid-Liquid Equilibria for Chloroform + Methanol + 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate at 100 kPa