Mixture of Isopropyl Alcohol + Tetrachloroethylene

Excel

Isopropyl Alcohol

Name
Isopropyl Alcohol
InChI
InChI=1S/C3H8O/c1-3(2)4/h3-4H,1-2H3
InChI Key
KFZMGEQAYNKOFK-UHFFFAOYSA-N
Formula
C3H8O
SMILES
CC(C)O
Mol. Weight (g/mol)
60.09
CAS
67-63-0

Tetrachloroethylene

Name
Tetrachloroethylene
InChI
InChI=1S/C2Cl4/c3-1(4)2(5)6
InChI Key
CYTYCFOTNPOANT-UHFFFAOYSA-N
Formula
C2Cl4
SMILES
ClC(Cl)=C(Cl)Cl
Mol. Weight (g/mol)
165.83
CAS
127-18-4
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Datasets

  1. η - Viscosity, Pa*s (2)
  2. ρl - Mass density, kg/m3 (2)

Viscosity, Pa*s [ref]

Operational conditions:

Mole fraction of Tetrachloroethylene (2) - Liquid Viscosity, Pa*s - Liquid
0.0000 0.0020
0.0763 0.0019
0.1567 0.0017
0.2417 0.0015
0.3313 0.0014
0.4266 0.0012
0.5276 0.0011
0.6349 0.0010
0.7486 0.0009
0.8705 0.0009
1.0000 0.0008
Mole fraction of Tetrachloroethylene (2)
Viscosity, Pa*s
8.00e-4
1.00e-3
1.20e-3
1.40e-3
1.60e-3
1.80e-3
2.00e-3
0
0.5
1

Viscosity, Pa*s [ref]

Operational conditions:

Mole fraction of Tetrachloroethylene (2) - Liquid Viscosity, Pa*s - Liquid
0.0000 0.0020
0.0763 0.0019
0.1567 0.0017
0.2417 0.0015
0.3313 0.0014
0.4266 0.0012
0.5276 0.0011
0.6349 0.0010
0.7486 0.0009
0.8705 0.0009
1.0000 0.0008
Mole fraction of Tetrachloroethylene (2)
Viscosity, Pa*s
8.00e-4
1.00e-3
1.20e-3
1.40e-3
1.60e-3
1.80e-3
2.00e-3
0
0.5
1

Mass density, kg/m3 [ref]

Operational conditions:

Mole fraction of Tetrachloroethylene (2) - Liquid Mass density, kg/m3 - Liquid
0.0000 784.3
0.0763 864.9
0.1567 946.4
0.2417 1026.7
0.3313 1107.5
0.4266 1189.3
0.5276 1271.6
0.6349 1355.4
0.7486 1437.6
0.8705 1523.6
1.0000 1610.2
Mole fraction of Tetrachloroethylene (2)
Mass density, kg/m3
800
1000
1200
1400
1600
0
0.5
1

Mass density, kg/m3 [ref]

Operational conditions:

Mole fraction of Tetrachloroethylene (2) - Liquid Mass density, kg/m3 - Liquid
0.0000 784.3
0.0763 864.9
0.1567 946.4
0.2417 1026.7
0.3313 1107.5
0.4266 1189.3
0.5276 1271.6
0.6349 1355.4
0.7486 1437.6
0.8705 1523.6
1.0000 1610.2
Mole fraction of Tetrachloroethylene (2)
Mass density, kg/m3
800
1000
1200
1400
1600
0
0.5
1

Sources