Mixture of Trichloroethylene + Benzene, 1,3-dimethyl-

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Trichloroethylene

Name
Trichloroethylene
InChI
InChI=1S/C2HCl3/c3-1-2(4)5/h1H
InChI Key
XSTXAVWGXDQKEL-UHFFFAOYSA-N
Formula
C2HCl3
SMILES
ClC=C(Cl)Cl
Mol. Weight (g/mol)
131.39
CAS
79-01-6

Benzene, 1,3-dimethyl-

Name
Benzene, 1,3-dimethyl-
InChI
InChI=1S/C8H10/c1-7-4-3-5-8(2)6-7/h3-6H,1-2H3
InChI Key
IVSZLXZYQVIEFR-UHFFFAOYSA-N
Formula
C8H10
SMILES
Cc1cccc(C)c1
Mol. Weight (g/mol)
106.17
CAS
108-38-3
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Datasets

  1. η - Viscosity, Pa*s (2)
  2. n0 - Refractive index (Na D-line) (2)
  3. ρl - Mass density, kg/m3 (2)

Viscosity, Pa*s [ref]

Operational conditions:

Mole fraction of Trichloroethylene (1) - Liquid Viscosity, Pa*s - Liquid
0.0768 0.0006
0.1465 0.0006
0.2415 0.0006
0.3204 0.0006
0.3935 0.0006
0.4960 0.0006
0.5613 0.0006
0.6423 0.0006
0.7204 0.0006
0.7639 0.0006
0.8774 0.0006
0.9596 0.0006

Viscosity, Pa*s [ref]

Operational conditions:

Mole fraction of Trichloroethylene (1) - Liquid Viscosity, Pa*s - Liquid
0.0768 0.0006
0.1465 0.0006
0.2415 0.0006
0.3204 0.0006
0.3935 0.0006
0.4960 0.0006
0.5613 0.0006
0.6423 0.0006
0.7204 0.0006
0.7639 0.0006
0.8774 0.0006
0.9596 0.0006

Refractive index (Na D-line) [ref]

Operational conditions:

Mole fraction of Trichloroethylene (1) - Liquid Refractive index (Na D-line) - Liquid
0.0850 1.4932
0.1622 1.4922
0.2415 1.4908
0.3204 1.4894
0.3935 1.488
0.4960 1.4859
0.5613 1.4845
0.6429 1.4825
0.7226 1.4807
0.8061 1.4789
0.8832 1.4773
0.9596 1.4756

Refractive index (Na D-line) [ref]

Operational conditions:

Mole fraction of Trichloroethylene (1) - Liquid Refractive index (Na D-line) - Liquid
0.0850 1.4932
0.1622 1.4922
0.2415 1.4908
0.3204 1.4894
0.3935 1.488
0.4960 1.4859
0.5613 1.4845
0.6429 1.4825
0.7226 1.4807
0.8061 1.4789
0.8832 1.4773
0.9596 1.4756

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Trichloroethylene (1) - Liquid Mass density, kg/m3 - Liquid
293.15 0.0494 886.2
293.15 0.0796 899.93
293.15 0.1531 934.34
293.15 0.2300 971.87
293.15 0.3097 1012.52
293.15 0.4065 1064.66
293.15 0.4841 1108.6
293.15 0.5561 1151.33
293.15 0.6453 1206.86
293.15 0.7090 1248.6
293.15 0.7989 1310.61
293.15 0.8937 1380.16
293.15 0.9740 1442.88
298.15 0.0494 881.77
298.15 0.0796 895.43
298.15 0.1531 929.62
298.15 0.2300 966.92
298.15 0.3097 1007.32
298.15 0.4065 1059.1
298.15 0.4841 1102.78
298.15 0.5561 1145.2
298.15 0.6453 1200.35
298.15 0.7090 1241.79
298.15 0.7989 1303.35
298.15 0.8937 1372.41
298.15 0.9740 1434.66
303.15 0.0494 877.34
303.15 0.0796 890.91
303.15 0.1531 924.88
303.15 0.2300 961.95
303.15 0.3097 1002.09
303.15 0.4065 1053.53
303.15 0.4841 1096.93
303.15 0.5561 1139.05
303.15 0.6453 1193.84
303.15 0.7090 1234.95
303.15 0.7989 1296.06
303.15 0.8937 1364.61
303.15 0.9740 1426.38

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Trichloroethylene (1) - Liquid Mass density, kg/m3 - Liquid
293.15 0.0494 886.2
293.15 0.0796 899.93
293.15 0.1531 934.34
293.15 0.2300 971.87
293.15 0.3097 1012.52
293.15 0.4065 1064.66
293.15 0.4841 1108.6
293.15 0.5561 1151.33
293.15 0.6453 1206.86
293.15 0.7090 1248.6
293.15 0.7989 1310.61
293.15 0.8937 1380.16
293.15 0.9740 1442.88
298.15 0.0494 881.77
298.15 0.0796 895.43
298.15 0.1531 929.62
298.15 0.2300 966.92
298.15 0.3097 1007.32
298.15 0.4065 1059.1
298.15 0.4841 1102.78
298.15 0.5561 1145.2
298.15 0.6453 1200.35
298.15 0.7090 1241.79
298.15 0.7989 1303.35
298.15 0.8937 1372.41
298.15 0.9740 1434.66
303.15 0.0494 877.34
303.15 0.0796 890.91
303.15 0.1531 924.88
303.15 0.2300 961.95
303.15 0.3097 1002.09
303.15 0.4065 1053.53
303.15 0.4841 1096.93
303.15 0.5561 1139.05
303.15 0.6453 1193.84
303.15 0.7090 1234.95
303.15 0.7989 1296.06
303.15 0.8937 1364.61
303.15 0.9740 1426.38

Sources