Mixture of Trichloromethane + Ethanol

Excel

Trichloromethane

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

Ethanol

Name
Ethanol
InChI
InChI=1S/C2H6O/c1-2-3/h3H,2H2,1H3
InChI Key
LFQSCWFLJHTTHZ-UHFFFAOYSA-N
Formula
C2H6O
SMILES
CCO
Mol. Weight (g/mol)
46.07
CAS
64-17-5
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Datasets

  1. Mole fraction (4)
  2. η - Viscosity, Pa*s (2)
  3. ρl - Mass density, kg/m3 (4)
  4. csound,fluid - Speed of Sound, m/s (2)
  5. Tboil - Boiling temperature at pressure P, K (4)
  6. Vapor Liquid Equilibrium at Constant Temperature (2)

Mole fraction of Trichloromethane (1) [ref]

Operational condition: Pressure, kPa = 101.3 (Gas)

Mole fraction of Trichloromethane (1) - Liquid Mole fraction of Trichloromethane (1) - Gas
0.0850 0.2290
0.1830 0.4150
0.2800 0.5430
0.3620 0.6240
0.4720 0.6950
0.5670 0.7380
0.6790 0.7840
0.7760 0.8190
0.8810 0.8700
0.9510 0.9260

Mole fraction of Trichloromethane (1) [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Mole fraction of Trichloromethane (1) - Gas Mole fraction of Trichloromethane (1) - Liquid
0.0000 0.0000
0.0490 0.0160
0.0890 0.0290
0.1510 0.0530
0.2080 0.0740
0.2680 0.1020
0.3460 0.1380
0.4150 0.1780
0.4880 0.2260
0.5530 0.2840
0.6090 0.3470
0.6460 0.3980
0.6840 0.4570
0.7110 0.5050
0.7320 0.5500
0.7490 0.5910
0.7650 0.6320
0.7820 0.6740
0.7940 0.7090
0.8030 0.7350
0.8150 0.7690
0.8280 0.8010
0.8400 0.8300
0.8540 0.8600
0.8690 0.8890
0.8850 0.9110
0.9020 0.9320
0.9260 0.9510
0.9480 0.9700
0.9710 0.9850
1.0000 1.0000

Mole fraction of Trichloromethane (1) [ref]

Operational condition: Pressure, kPa = 101.3 (Gas)

Mole fraction of Trichloromethane (1) - Liquid Mole fraction of Trichloromethane (1) - Gas
0.0850 0.2290
0.1830 0.4150
0.2800 0.5430
0.3620 0.6240
0.4720 0.6950
0.5670 0.7380
0.6790 0.7840
0.7760 0.8190
0.8810 0.8700
0.9510 0.9260

Mole fraction of Trichloromethane (1) [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Mole fraction of Trichloromethane (1) - Gas Mole fraction of Trichloromethane (1) - Liquid
0.0000 0.0000
0.0490 0.0160
0.0890 0.0290
0.1510 0.0530
0.2080 0.0740
0.2680 0.1020
0.3460 0.1380
0.4150 0.1780
0.4880 0.2260
0.5530 0.2840
0.6090 0.3470
0.6460 0.3980
0.6840 0.4570
0.7110 0.5050
0.7320 0.5500
0.7490 0.5910
0.7650 0.6320
0.7820 0.6740
0.7940 0.7090
0.8030 0.7350
0.8150 0.7690
0.8280 0.8010
0.8400 0.8300
0.8540 0.8600
0.8690 0.8890
0.8850 0.9110
0.9020 0.9320
0.9260 0.9510
0.9480 0.9700
0.9710 0.9850
1.0000 1.0000

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 0.0011
298.15 0.0522 0.0011
298.15 0.1007 0.0011
298.15 0.1468 0.0010
298.15 0.2014 0.0010
298.15 0.2505 0.0010
298.15 0.3005 0.0009
298.15 0.3491 0.0009
298.15 0.3999 0.0008
298.15 0.4505 0.0008
298.15 0.5045 0.0007
298.15 0.5509 0.0007
298.15 0.6007 0.0007
298.15 0.6492 0.0006
298.15 0.7008 0.0006
298.15 0.7496 0.0006
298.15 0.8059 0.0006
298.15 0.8544 0.0006
298.15 0.8994 0.0006
298.15 0.9498 0.0006
298.15 1.0000 0.0006
308.15 0.0000 0.0009
308.15 0.0522 0.0009
308.15 0.1007 0.0009
308.15 0.1468 0.0009
308.15 0.2014 0.0008
308.15 0.2505 0.0008
308.15 0.3005 0.0008
308.15 0.3491 0.0007
308.15 0.3999 0.0007
308.15 0.4505 0.0007
308.15 0.5045 0.0006
308.15 0.5509 0.0006
308.15 0.6007 0.0006
308.15 0.6492 0.0006
308.15 0.7008 0.0006
308.15 0.7496 0.0006
308.15 0.8059 0.0006
308.15 0.8544 0.0005
308.15 0.8994 0.0005
308.15 0.9498 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
298.15 0.0000 0.0011
298.15 0.0522 0.0011
298.15 0.1007 0.0011
298.15 0.1468 0.0010
298.15 0.2014 0.0010
298.15 0.2505 0.0010
298.15 0.3005 0.0009
298.15 0.3491 0.0009
298.15 0.3999 0.0008
298.15 0.4505 0.0008
298.15 0.5045 0.0007
298.15 0.5509 0.0007
298.15 0.6007 0.0007
298.15 0.6492 0.0006
298.15 0.7008 0.0006
298.15 0.7496 0.0006
298.15 0.8059 0.0006
298.15 0.8544 0.0006
298.15 0.8994 0.0006
298.15 0.9498 0.0006
298.15 1.0000 0.0006
308.15 0.0000 0.0009
308.15 0.0522 0.0009
308.15 0.1007 0.0009
308.15 0.1468 0.0009
308.15 0.2014 0.0008
308.15 0.2505 0.0008
308.15 0.3005 0.0008
308.15 0.3491 0.0007
308.15 0.3999 0.0007
308.15 0.4505 0.0007
308.15 0.5045 0.0006
308.15 0.5509 0.0006
308.15 0.6007 0.0006
308.15 0.6492 0.0006
308.15 0.7008 0.0006
308.15 0.7496 0.0006
308.15 0.8059 0.0006
308.15 0.8544 0.0005
308.15 0.8994 0.0005
308.15 0.9498 0.0005
308.15 1.0000 0.0005

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.33 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Ethanol (2) - Liquid Mass density, kg/m3 - Liquid
288.15 0.0000 1498.077
288.15 0.0485 1472.168
288.15 0.0997 1444.687
288.15 0.1993 1389.445
288.15 0.2999 1331.013
288.15 0.4002 1269.36
288.15 0.4984 1204.895
288.15 0.5504 1168.927
288.15 0.6001 1133.489
288.15 0.6949 1062.09
288.15 0.7940 981.537
288.15 0.8503 933.183
288.15 0.9001 888.356
288.15 1.0000 793.721
293.15 0.0000 1488.638
293.15 0.0485 1462.839
293.15 0.0997 1435.551
293.15 0.1993 1380.636
293.15 0.2999 1322.638
293.15 0.4002 1261.463
293.15 0.4984 1197.515
293.15 0.5504 1161.838
293.15 0.6001 1126.688
293.15 0.6949 1055.876
293.15 0.7940 976.02
293.15 0.8503 927.998
293.15 0.9001 883.494
293.15 1.0000 789.454
298.15 0.0000 1479.148
298.15 0.0485 1453.461
298.15 0.0997 1426.279
298.15 0.1993 1371.766
298.15 0.2999 1314.202
298.15 0.4002 1253.502
298.15 0.4984 1190.075
298.15 0.5504 1154.688
298.15 0.6001 1119.829
298.15 0.6949 1049.609
298.15 0.7940 970.455
298.15 0.8503 922.772
298.15 0.9001 878.595
298.15 1.0000 785.164
303.15 0.0000 1469.612
303.15 0.0485 1444.03
303.15 0.0997 1416.991
303.15 0.1993 1362.834
303.15 0.2999 1305.697
303.15 0.4002 1245.473
303.15 0.4984 1182.569
303.15 0.5504 1147.436
303.15 0.6001 1112.902
303.15 0.6949 1043.282
303.15 0.7940 964.839
303.15 0.8503 917.5
303.15 0.9001 873.653
303.15 1.0000 780.853
308.15 0.0000 1460.025
308.15 0.0485 1434.548
308.15 0.0997 1407.645
308.15 0.1993 1353.833
308.15 0.2999 1297.125
308.15 0.4002 1237.37
308.15 0.4984 1174.989
308.15 0.5504 1140.19
308.15 0.6001 1105.903
308.15 0.6949 1036.887
308.15 0.7940 959.165
308.15 0.8503 912.175
308.15 0.9001 868.659
308.15 1.0000 776.51
313.15 0.0000 1450.413
313.15 0.0485 1425.025
313.15 0.0997 1398.251
313.15 0.1993 1344.778
313.15 0.2999 1288.501
313.15 0.4002 1229.177
313.15 0.4984 1167.344
313.15 0.5504 1132.843
313.15 0.6001 1098.846
313.15 0.6949 1030.436
313.15 0.7940 953.436
313.15 0.8503 906.798
313.15 0.9001 863.612
313.15 1.0000 772.138

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 784.32
298.15 0.0522 834.86
298.15 0.1007 879.76
298.15 0.1468 920.98
298.15 0.2014 968.01
298.15 0.2505 1008.24
298.15 0.3005 1047.8
298.15 0.3491 1084.58
298.15 0.3999 1121.8
298.15 0.4505 1157.08
298.15 0.5045 1193.09
298.15 0.5509 1223.51
298.15 0.6007 1254.55
298.15 0.6492 1284.3
298.15 0.7008 1314.71
298.15 0.7496 1342.79
298.15 0.8059 1374.26
298.15 0.8544 1400.99
298.15 0.8994 1425.35
298.15 0.9498 1452.14
298.15 1.0000 1478.82
308.15 0.0000 775.51
308.15 0.0522 824.87
308.15 0.1007 868.7
308.15 0.1468 909.11
308.15 0.2014 955.3
308.15 0.2505 994.85
308.15 0.3005 1033.7
308.15 0.3491 1069.92
308.15 0.3999 1106.5
308.15 0.4505 1141.59
308.15 0.5045 1177.49
308.15 0.5509 1207.46
308.15 0.6007 1238.37
308.15 0.6492 1267.81
308.15 0.7008 1297.8
308.15 0.7496 1325.84
308.15 0.8059 1357.1
308.15 0.8544 1383.35
308.15 0.8994 1407.35
308.15 0.9498 1433.5
308.15 1.0000 1459.45

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.33 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Ethanol (2) - Liquid Mass density, kg/m3 - Liquid
288.15 0.0000 1498.077
288.15 0.0485 1472.168
288.15 0.0997 1444.687
288.15 0.1993 1389.445
288.15 0.2999 1331.013
288.15 0.4002 1269.36
288.15 0.4984 1204.895
288.15 0.5504 1168.927
288.15 0.6001 1133.489
288.15 0.6949 1062.09
288.15 0.7940 981.537
288.15 0.8503 933.183
288.15 0.9001 888.356
288.15 1.0000 793.721
293.15 0.0000 1488.638
293.15 0.0485 1462.839
293.15 0.0997 1435.551
293.15 0.1993 1380.636
293.15 0.2999 1322.638
293.15 0.4002 1261.463
293.15 0.4984 1197.515
293.15 0.5504 1161.838
293.15 0.6001 1126.688
293.15 0.6949 1055.876
293.15 0.7940 976.02
293.15 0.8503 927.998
293.15 0.9001 883.494
293.15 1.0000 789.454
298.15 0.0000 1479.148
298.15 0.0485 1453.461
298.15 0.0997 1426.279
298.15 0.1993 1371.766
298.15 0.2999 1314.202
298.15 0.4002 1253.502
298.15 0.4984 1190.075
298.15 0.5504 1154.688
298.15 0.6001 1119.829
298.15 0.6949 1049.609
298.15 0.7940 970.455
298.15 0.8503 922.772
298.15 0.9001 878.595
298.15 1.0000 785.164
303.15 0.0000 1469.612
303.15 0.0485 1444.03
303.15 0.0997 1416.991
303.15 0.1993 1362.834
303.15 0.2999 1305.697
303.15 0.4002 1245.473
303.15 0.4984 1182.569
303.15 0.5504 1147.436
303.15 0.6001 1112.902
303.15 0.6949 1043.282
303.15 0.7940 964.839
303.15 0.8503 917.5
303.15 0.9001 873.653
303.15 1.0000 780.853
308.15 0.0000 1460.025
308.15 0.0485 1434.548
308.15 0.0997 1407.645
308.15 0.1993 1353.833
308.15 0.2999 1297.125
308.15 0.4002 1237.37
308.15 0.4984 1174.989
308.15 0.5504 1140.19
308.15 0.6001 1105.903
308.15 0.6949 1036.887
308.15 0.7940 959.165
308.15 0.8503 912.175
308.15 0.9001 868.659
308.15 1.0000 776.51
313.15 0.0000 1450.413
313.15 0.0485 1425.025
313.15 0.0997 1398.251
313.15 0.1993 1344.778
313.15 0.2999 1288.501
313.15 0.4002 1229.177
313.15 0.4984 1167.344
313.15 0.5504 1132.843
313.15 0.6001 1098.846
313.15 0.6949 1030.436
313.15 0.7940 953.436
313.15 0.8503 906.798
313.15 0.9001 863.612
313.15 1.0000 772.138

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 784.32
298.15 0.0522 834.86
298.15 0.1007 879.76
298.15 0.1468 920.98
298.15 0.2014 968.01
298.15 0.2505 1008.24
298.15 0.3005 1047.8
298.15 0.3491 1084.58
298.15 0.3999 1121.8
298.15 0.4505 1157.08
298.15 0.5045 1193.09
298.15 0.5509 1223.51
298.15 0.6007 1254.55
298.15 0.6492 1284.3
298.15 0.7008 1314.71
298.15 0.7496 1342.79
298.15 0.8059 1374.26
298.15 0.8544 1400.99
298.15 0.8994 1425.35
298.15 0.9498 1452.14
298.15 1.0000 1478.82
308.15 0.0000 775.51
308.15 0.0522 824.87
308.15 0.1007 868.7
308.15 0.1468 909.11
308.15 0.2014 955.3
308.15 0.2505 994.85
308.15 0.3005 1033.7
308.15 0.3491 1069.92
308.15 0.3999 1106.5
308.15 0.4505 1141.59
308.15 0.5045 1177.49
308.15 0.5509 1207.46
308.15 0.6007 1238.37
308.15 0.6492 1267.81
308.15 0.7008 1297.8
308.15 0.7496 1325.84
308.15 0.8059 1357.1
308.15 0.8544 1383.35
308.15 0.8994 1407.35
308.15 0.9498 1433.5
308.15 1.0000 1459.45

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 1144.0
298.15 0.0522 1129.0
298.15 0.1007 1114.0
298.15 0.1468 1101.0
298.15 0.2014 1085.0
298.15 0.2505 1071.0
298.15 0.3005 1057.0
298.15 0.3491 1045.0
298.15 0.3999 1033.0
298.15 0.4505 1021.0
298.15 0.5045 1011.0
298.15 0.5509 1003.0
298.15 0.6007 996.0
298.15 0.6492 990.0
298.15 0.7008 985.0
298.15 0.7496 982.0
298.15 0.8059 981.0
298.15 0.8544 980.0
298.15 0.8994 981.0
298.15 0.9498 983.0
298.15 1.0000 985.0
308.15 0.0000 1111.0
308.15 0.0522 1092.0
308.15 0.1007 1076.0
308.15 0.1468 1062.0
308.15 0.2014 1046.0
308.15 0.2505 1034.0
308.15 0.3005 1022.0
308.15 0.3491 1011.0
308.15 0.3999 1000.0
308.15 0.4505 991.0
308.15 0.5045 982.0
308.15 0.5509 975.0
308.15 0.6007 967.0
308.15 0.6492 962.0
308.15 0.7008 957.0
308.15 0.7496 953.0
308.15 0.8059 950.0
308.15 0.8544 949.0
308.15 0.8994 949.0
308.15 0.9498 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 1144.0
298.15 0.0522 1129.0
298.15 0.1007 1114.0
298.15 0.1468 1101.0
298.15 0.2014 1085.0
298.15 0.2505 1071.0
298.15 0.3005 1057.0
298.15 0.3491 1045.0
298.15 0.3999 1033.0
298.15 0.4505 1021.0
298.15 0.5045 1011.0
298.15 0.5509 1003.0
298.15 0.6007 996.0
298.15 0.6492 990.0
298.15 0.7008 985.0
298.15 0.7496 982.0
298.15 0.8059 981.0
298.15 0.8544 980.0
298.15 0.8994 981.0
298.15 0.9498 983.0
298.15 1.0000 985.0
308.15 0.0000 1111.0
308.15 0.0522 1092.0
308.15 0.1007 1076.0
308.15 0.1468 1062.0
308.15 0.2014 1046.0
308.15 0.2505 1034.0
308.15 0.3005 1022.0
308.15 0.3491 1011.0
308.15 0.3999 1000.0
308.15 0.4505 991.0
308.15 0.5045 982.0
308.15 0.5509 975.0
308.15 0.6007 967.0
308.15 0.6492 962.0
308.15 0.7008 957.0
308.15 0.7496 953.0
308.15 0.8059 950.0
308.15 0.8544 949.0
308.15 0.8994 949.0
308.15 0.9498 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
0.0850 346.40
0.1830 341.95
0.2800 338.65
0.3620 336.15
0.4720 334.35
0.5670 333.15
0.6790 332.55
0.7760 332.25
0.8810 332.25
0.9510 332.65

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Mole fraction of Trichloromethane (1) - Gas Boiling temperature at pressure P, K - Liquid
0.0000 351.20
0.0490 350.29
0.0890 349.54
0.1510 348.30
0.2080 347.13
0.2680 345.70
0.3460 344.13
0.4150 342.39
0.4880 340.48
0.5530 338.66
0.6090 337.04
0.6460 335.84
0.6840 334.92
0.7110 334.29
0.7320 333.75
0.7490 333.35
0.7650 333.03
0.7820 332.78
0.7940 332.59
0.8030 332.49
0.8150 332.34
0.8280 332.24
0.8400 332.24
0.8540 332.20
0.8690 332.27
0.8850 332.37
0.9020 332.53
0.9260 332.77
0.9480 333.07
0.9710 333.44
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
0.0850 346.40
0.1830 341.95
0.2800 338.65
0.3620 336.15
0.4720 334.35
0.5670 333.15
0.6790 332.55
0.7760 332.25
0.8810 332.25
0.9510 332.65

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Mole fraction of Trichloromethane (1) - Gas Boiling temperature at pressure P, K - Liquid
0.0000 351.20
0.0490 350.29
0.0890 349.54
0.1510 348.30
0.2080 347.13
0.2680 345.70
0.3460 344.13
0.4150 342.39
0.4880 340.48
0.5530 338.66
0.6090 337.04
0.6460 335.84
0.6840 334.92
0.7110 334.29
0.7320 333.75
0.7490 333.35
0.7650 333.03
0.7820 332.78
0.7940 332.59
0.8030 332.49
0.8150 332.34
0.8280 332.24
0.8400 332.24
0.8540 332.20
0.8690 332.27
0.8850 332.37
0.9020 332.53
0.9260 332.77
0.9480 333.07
0.9710 333.44
1.0000 333.96

Vapor Liquid Equilibrium at Constant Temperature [ref]

Operational condition: Temperature, K = 318.15 (VLE)

Fixed Measured
P [kPa] - VLE x1[mol/mol] of Trichloromethane (1) - Liquid y1[mol/mol] of Trichloromethane (1) - Vapour
24.585 0.0210 0.0830
28.131 0.0650 0.2380
34.797 0.1580 0.4730
40.33 0.2130 0.5570
43.65 0.2590 0.6070
46.743 0.3060 0.6510
50.196 0.3450 0.6780
51.049 0.3860 0.7040

Vapor Liquid Equilibrium at Constant Temperature [ref]

Operational condition: Temperature, K = 328.15 (VLE)

Fixed Measured
P [kPa] - VLE x1[mol/mol] of Trichloromethane (1) - Liquid y1[mol/mol] of Trichloromethane (1) - Vapour
39.463 0.0210 0.0750
49.129 0.1060 0.3210
55.022 0.1600 0.4280
60.622 0.2110 0.5130
65.328 0.2590 0.5720
69.314 0.3030 0.6160
72.154 0.3430 0.6470
74.954 0.3850 0.6700

Sources