Mixture of Methyl Isobutyl Ketone + Trichloromethane

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Methyl Isobutyl Ketone

Name
Methyl Isobutyl Ketone
InChI
InChI=1S/C6H12O/c1-5(2)4-6(3)7/h5H,4H2,1-3H3
InChI Key
NTIZESTWPVYFNL-UHFFFAOYSA-N
Formula
C6H12O
SMILES
CC(=O)CC(C)C
Mol. Weight (g/mol)
100.16
CAS
108-10-1

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
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Datasets

  1. Mole fraction (2)
  2. η - Viscosity, Pa*s (2)
  3. Pvap - Vapor or sublimation pressure, kPa (2)
  4. ρl - Mass density, kg/m3 (2)

Mole fraction of Trichloromethane (2) [ref]

Operational condition: Temperature, K = 303.15 (Gas)

Mole fraction of Trichloromethane (2) - Liquid Mole fraction of Trichloromethane (2) - Gas
0.0000 0.0000
0.0959 0.2872
0.1852 0.4873
0.2468 0.6183
0.3514 0.7758
0.4459 0.8747
0.5575 0.9280
0.6019 0.9530
0.6279 0.9599
0.6603 0.9670
0.6989 0.9744
0.7328 0.9853
0.7538 0.9868
0.8285 0.9952
0.9402 0.9994
1.0000 1.0000

Mole fraction of Trichloromethane (2) [ref]

Operational condition: Temperature, K = 303.15 (Gas)

Mole fraction of Trichloromethane (2) - Liquid Mole fraction of Trichloromethane (2) - Gas
0.0000 0.0000
0.0959 0.2872
0.1852 0.4873
0.2468 0.6183
0.3514 0.7758
0.4459 0.8747
0.5575 0.9280
0.6019 0.9530
0.6279 0.9599
0.6603 0.9670
0.6989 0.9744
0.7328 0.9853
0.7538 0.9868
0.8285 0.9952
0.9402 0.9994
1.0000 1.0000

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Trichloromethane (2) - Liquid Viscosity, Pa*s - Liquid
283.15 0.0000 0.0007
283.15 0.0847 0.0007
283.15 0.1841 0.0007
283.15 0.2760 0.0008
283.15 0.3529 0.0008
283.15 0.4467 0.0008
283.15 0.5060 0.0008
283.15 0.6079 0.0008
283.15 0.6959 0.0008
283.15 0.8213 0.0007
283.15 0.9067 0.0007
283.15 1.0000 0.0006
293.15 0.0000 0.0006
293.15 0.0847 0.0006
293.15 0.1841 0.0006
293.15 0.2760 0.0007
293.15 0.3529 0.0007
293.15 0.4467 0.0007
293.15 0.5060 0.0007
293.15 0.6079 0.0007
293.15 0.6959 0.0007
293.15 0.8213 0.0007
293.15 0.9067 0.0006
293.15 1.0000 0.0006
303.15 0.0000 0.0005
303.15 0.0847 0.0005
303.15 0.1841 0.0006
303.15 0.2760 0.0006
303.15 0.3529 0.0006
303.15 0.4467 0.0006
303.15 0.5060 0.0006
303.15 0.6079 0.0006
303.15 0.6959 0.0006
303.15 0.8213 0.0006
303.15 0.9067 0.0006
303.15 1.0000 0.0005
313.15 0.0000 0.0005
313.15 0.0847 0.0005
313.15 0.1841 0.0005
313.15 0.2760 0.0005
313.15 0.3529 0.0005
313.15 0.4467 0.0005
313.15 0.5060 0.0006
313.15 0.6079 0.0006
313.15 0.6959 0.0006
313.15 0.8213 0.0005
313.15 0.9067 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 (2) - Liquid Viscosity, Pa*s - Liquid
283.15 0.0000 0.0007
283.15 0.0847 0.0007
283.15 0.1841 0.0007
283.15 0.2760 0.0008
283.15 0.3529 0.0008
283.15 0.4467 0.0008
283.15 0.5060 0.0008
283.15 0.6079 0.0008
283.15 0.6959 0.0008
283.15 0.8213 0.0007
283.15 0.9067 0.0007
283.15 1.0000 0.0006
293.15 0.0000 0.0006
293.15 0.0847 0.0006
293.15 0.1841 0.0006
293.15 0.2760 0.0007
293.15 0.3529 0.0007
293.15 0.4467 0.0007
293.15 0.5060 0.0007
293.15 0.6079 0.0007
293.15 0.6959 0.0007
293.15 0.8213 0.0007
293.15 0.9067 0.0006
293.15 1.0000 0.0006
303.15 0.0000 0.0005
303.15 0.0847 0.0005
303.15 0.1841 0.0006
303.15 0.2760 0.0006
303.15 0.3529 0.0006
303.15 0.4467 0.0006
303.15 0.5060 0.0006
303.15 0.6079 0.0006
303.15 0.6959 0.0006
303.15 0.8213 0.0006
303.15 0.9067 0.0006
303.15 1.0000 0.0005
313.15 0.0000 0.0005
313.15 0.0847 0.0005
313.15 0.1841 0.0005
313.15 0.2760 0.0005
313.15 0.3529 0.0005
313.15 0.4467 0.0005
313.15 0.5060 0.0006
313.15 0.6079 0.0006
313.15 0.6959 0.0006
313.15 0.8213 0.0005
313.15 0.9067 0.0005
313.15 1.0000 0.0005

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 303.15 (Gas)

Mole fraction of Trichloromethane (2) - Liquid Vapor or sublimation pressure, kPa - Liquid
0.0000 3.89
0.0959 4.68
0.1852 5.68
0.2468 6.56
0.3514 8.54
0.4459 11.00
0.5575 14.89
0.6019 16.74
0.6279 17.70
0.6603 19.03
0.6989 20.70
0.7328 22.39
0.7538 23.33
0.8285 26.52
0.9402 30.87
1.0000 32.19

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 303.15 (Gas)

Mole fraction of Trichloromethane (2) - Liquid Vapor or sublimation pressure, kPa - Liquid
0.0000 3.89
0.0959 4.68
0.1852 5.68
0.2468 6.56
0.3514 8.54
0.4459 11.00
0.5575 14.89
0.6019 16.74
0.6279 17.70
0.6603 19.03
0.6989 20.70
0.7328 22.39
0.7538 23.33
0.8285 26.52
0.9402 30.87
1.0000 32.19

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Trichloromethane (2) - Liquid Mass density, kg/m3 - Liquid
283.15 0.0000 809.8
283.15 0.0847 849.0
283.15 0.1841 898.2
283.15 0.2760 947.2
283.15 0.3529 991.1
283.15 0.4467 1048.8
283.15 0.5060 1087.7
283.15 0.6079 1159.3
283.15 0.6959 1226.7
283.15 0.8213 1332.6
283.15 0.9067 1412.3
283.15 1.0000 1507.3
293.15 0.0000 800.7
293.15 0.0847 839.4
293.15 0.1841 888.1
293.15 0.2760 936.6
293.15 0.3529 980.1
293.15 0.4467 1037.0
293.15 0.5060 1075.3
293.15 0.6079 1146.0
293.15 0.6959 1212.4
293.15 0.8213 1316.7
293.15 0.9067 1395.0
293.15 1.0000 1488.4
303.15 0.0000 791.6
303.15 0.0847 829.9
303.15 0.1841 878.0
303.15 0.2760 925.8
303.15 0.3529 968.7
303.15 0.4467 1025.0
303.15 0.5060 1062.8
303.15 0.6079 1132.5
303.15 0.6959 1197.9
303.15 0.8213 1300.6
303.15 0.9067 1377.7
303.15 1.0000 1469.4
313.15 0.0000 782.2
313.15 0.0847 820.0
313.15 0.1841 867.5
313.15 0.2760 914.9
313.15 0.3529 957.1
313.15 0.4467 1012.6
313.15 0.5060 1050.0
313.15 0.6079 1118.7
313.15 0.6959 1183.2
313.15 0.8213 1284.1
313.15 0.9067 1359.8
313.15 1.0000 1450.0

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Trichloromethane (2) - Liquid Mass density, kg/m3 - Liquid
283.15 0.0000 809.8
283.15 0.0847 849.0
283.15 0.1841 898.2
283.15 0.2760 947.2
283.15 0.3529 991.1
283.15 0.4467 1048.8
283.15 0.5060 1087.7
283.15 0.6079 1159.3
283.15 0.6959 1226.7
283.15 0.8213 1332.6
283.15 0.9067 1412.3
283.15 1.0000 1507.3
293.15 0.0000 800.7
293.15 0.0847 839.4
293.15 0.1841 888.1
293.15 0.2760 936.6
293.15 0.3529 980.1
293.15 0.4467 1037.0
293.15 0.5060 1075.3
293.15 0.6079 1146.0
293.15 0.6959 1212.4
293.15 0.8213 1316.7
293.15 0.9067 1395.0
293.15 1.0000 1488.4
303.15 0.0000 791.6
303.15 0.0847 829.9
303.15 0.1841 878.0
303.15 0.2760 925.8
303.15 0.3529 968.7
303.15 0.4467 1025.0
303.15 0.5060 1062.8
303.15 0.6079 1132.5
303.15 0.6959 1197.9
303.15 0.8213 1300.6
303.15 0.9067 1377.7
303.15 1.0000 1469.4
313.15 0.0000 782.2
313.15 0.0847 820.0
313.15 0.1841 867.5
313.15 0.2760 914.9
313.15 0.3529 957.1
313.15 0.4467 1012.6
313.15 0.5060 1050.0
313.15 0.6079 1118.7
313.15 0.6959 1183.2
313.15 0.8213 1284.1
313.15 0.9067 1359.8
313.15 1.0000 1450.0

Sources