2
0
2009
bha
bha
1
journal
Original
Bhatia, S. C.[Subhash C.]
Bhatia, R.[Rachna]
Dubey, G. P.[Gyan P.]
J. Chem. Eng. Data
2009
2020-09-29
Studies on Transport and Thermodynamic Properties of Binary Mixtures of Hexan-1-ol with Halogenated Compounds at 293.15 K
Viscosities (?) of binary mixtures of hexan-1-ol with 1,2-dichloroethane, 1,2-dibromoethane, and 1,1,2,2-tetrachloroethene have been determined at 293.15 K and at the atmospheric pressure for the whole composition range. Deviations in viscosity (??) from the mole fraction average have been derived from the experimental data. The viscosity data have been correlated using Kendall-Monroe, Lobe, Grunberg-Nissan, Tamura-Kurata, Hind-Mclaughlin-Ubbelohde, and Katti-Chaudhary viscosity models and McAllister s three-body interaction model.
10.1021/je900278v
12
54
3303-3306
1
InChI=1S/C2H4Cl2/c3-1-2-4/h1-2H2
WSLDOOZREJYCGB-UHFFFAOYSA-N
1,2-dichloroethane
1,2-ethylene dichloride
Freon 150
R-150
C2H4Cl2
1
Commercial source
1
99.7
3
Stated by supplier
2
De-gassed by evacuation
Molecular sieve treatment
De-gassed by evacuation
Molecular sieve treatment
3
99.5
3
Gas chromatography
2
InChI=1S/C2H4Br2/c3-1-2-4/h1-2H2
PAAZPARNPHGIKF-UHFFFAOYSA-N
1,2-dibromoethane
alpha,omega-dibromoethane
ethylene bromide
ethylene dibromide
glycol dibromide
C2H4Br2
1
Commercial source
1
99.5
3
Stated by supplier
2
De-gassed by evacuation
3
99.5
3
Gas chromatography
3
InChI=1S/C2Cl4/c3-1(4)2(5)6
CYTYCFOTNPOANT-UHFFFAOYSA-N
tetrachloroethene
perchloroethylene
tetrachloroethylene
C2Cl4
1
Commercial source
1
99.4
3
Stated by supplier
2
De-gassed by evacuation
Molecular sieve treatment
De-gassed by evacuation
Molecular sieve treatment
3
99.5
3
Gas chromatography
4
InChI=1S/C6H14O/c1-2-3-4-5-6-7/h7H,2-6H2,1H3
ZSIAUFGUXNUGDI-UHFFFAOYSA-N
hexan-1-ol
1-hexanol
1-hydroxyhexane
amylcarbinol
hexyl alcohol
n-hexanol
n-hexyl alcohol
pentylcarbinol
C6H14O
1
Commercial source
1
99.7
3
Stated by supplier
1
1
1
Principal objective of the work
RDC
TRC
12/17/2009
1
Viscosity, Pa*s
Capillary tube (Ostwald; Ubbelohde) method
Liquid
Direct value, X
1
Data file compiler
Propagation of evaluated standard uncertainties
95
Liquid
1
Temperature, K
Liquid
2
Pressure, kPa
Liquid
1
293.15
5
2
101
3
1
0.000827
3
1
7e-06
2
1
1
Principal objective of the work
RDC
TRC
12/17/2009
1
Mass density, kg/m3
VIBTUB::UFactor:4
Liquid
Direct value, X
1
Data file compiler
Propagation of evaluated standard uncertainties
95
Liquid
1
Temperature, K
Liquid
2
Pressure, kPa
Liquid
1
298.15
5
2
101
3
1
1252.766
7
1
0.596
3
2
1
Principal objective of the work
RDC
TRC
12/17/2009
1
Viscosity, Pa*s
Capillary tube (Ostwald; Ubbelohde) method
Liquid
Direct value, X
1
Data file compiler
Propagation of evaluated standard uncertainties
95
Liquid
1
Temperature, K
Liquid
2
Pressure, kPa
Liquid
1
293.15
5
2
101
3
1
0.001733
4
1
1.1e-05
4
2
1
Principal objective of the work
RDC
TRC
12/17/2009
1
Mass density, kg/m3
VIBTUB:UFactor:4
Liquid
Direct value, X
1
Data file compiler
Propagation of evaluated standard uncertainties
95
Liquid
1
Temperature, K
Liquid
2
Pressure, kPa
Liquid
1
298.15
5
2
101
3
1
2179.591
7
1
2.202
5
3
1
Principal objective of the work
RDC
TRC
12/17/2009
1
Viscosity, Pa*s
Capillary tube (Ostwald; Ubbelohde) method
Liquid
Direct value, X
1
Data file compiler
Propagation of evaluated standard uncertainties
95
Liquid
1
Temperature, K
Liquid
2
Pressure, kPa
Liquid
1
293.15
5
2
101
3
1
0.00089
3
1
7e-06
6
3
1
Principal objective of the work
RDC
TRC
12/17/2009
1
Mass density, kg/m3
VIBTUB::UFactor:4
Liquid
Direct value, X
1
Data file compiler
Propagation of evaluated standard uncertainties
95
Liquid
1
Temperature, K
Liquid
2
Pressure, kPa
Liquid
1
298.15
5
2
101
3
1
1622.745
7
1
1.227
7
4
1
Principal objective of the work
RDC
TRC
12/17/2009
1
Viscosity, Pa*s
Capillary tube (Ostwald; Ubbelohde) method
Liquid
Direct value, X
1
Data file compiler
Propagation of evaluated standard uncertainties
95
Liquid
1
Temperature, K
Liquid
2
Pressure, kPa
Liquid
1
293.15
5
2
101
3
1
0.005291
4
1
3e-05
8
4
1
Principal objective of the work
RDC
TRC
12/17/2009
1
Mass density, kg/m3
VIBTUB:UFactor:4
Liquid
Direct value, X
1
Data file compiler
Propagation of evaluated standard uncertainties
95
Liquid
1
Temperature, K
Liquid
2
Pressure, kPa
Liquid
1
298.15
5
2
101
3
1
818.856
6
1
0.419
9
1
1
4
1
Principal objective of the work
VN
TRC
12/17/2009
1
Viscosity, Pa*s
Capillary tube (Ostwald; Ubbelohde) method
Liquid
Direct value, X
1
Data file compiler
Propagation of evaluated standard uncertainties
95
Liquid
1
Temperature, K
Liquid
293.15
5
2
Pressure, kPa
Liquid
101
3
1
Mole fraction
1
Liquid
1
0
2
1
0.005291
4
1
3e-05
1
0.037
3
1
0.005008
4
1
3.2e-05
1
0.0769
3
1
0.004696
4
1
3e-05
1
0.1499
4
1
0.004191
4
1
2.7e-05
1
0.2147
4
1
0.003787
4
1
2.5e-05
1
0.2935
4
1
0.003292
4
1
2.3e-05
1
0.3952
4
1
0.002726
4
1
2e-05
1
0.4532
4
1
0.002405
4
1
1.8e-05
1
0.5596
4
1
0.001894
4
1
1.5e-05
1
0.6113
4
1
0.001677
4
1
1.3e-05
1
0.6971
4
1
0.001372
4
1
1.1e-05
1
0.7791
4
1
0.001137
4
1
9e-06
1
0.8563
4
1
0.000977
3
1
8e-06
1
0.9335
4
1
0.000873
3
1
7e-06
1
0.979
4
1
0.000833
3
1
7e-06
1
1
5
1
0.000827
3
1
7e-06
10
1
1
4
1
Principal objective of the work
VN
TRC
12/17/2009
1
Mass density, kg/m3
VIBTUB:UFactor:4
Liquid
Direct value, X
1
Data file compiler
Propagation of evaluated standard uncertainties
95
Liquid
1
Temperature, K
Liquid
298.15
5
2
Pressure, kPa
Liquid
101
3
1
Mole fraction
1
Liquid
1
0
2
1
818.856
6
1
0.419
1
0.037
3
1
828.769
6
1
0.68
1
0.0769
3
1
839.847
6
1
0.685
1
0.1499
4
1
860.583
6
1
0.68
1
0.2147
4
1
879.725
6
1
0.701
1
0.2935
4
1
904.954
6
1
0.735
1
0.3952
4
1
940.475
6
1
0.754
1
0.4532
4
1
962.107
6
1
0.816
1
0.5596
4
1
1005.05
7
1
0.841
1
0.6113
4
1
1027.551
7
1
0.94
1
0.6971
4
1
1067.981
7
1
1.032
1
0.7791
4
1
1111.055
7
1
1.149
1
0.8563
4
1
1155.161
7
1
1.294
1
0.9335
4
1
1205.426
7
1
1.426
1
0.979
4
1
1236.986
7
1
1.528
1
1
5
1
1252.766
7
1
0.596
11
2
1
4
1
Principal objective of the work
VN
TRC
12/17/2009
1
Viscosity, Pa*s
Capillary tube (Ostwald; Ubbelohde) method
Liquid
Direct value, X
1
Data file compiler
Propagation of evaluated standard uncertainties
95
Liquid
1
Temperature, K
Liquid
293.15
5
2
Pressure, kPa
Liquid
101
3
1
Mole fraction
2
Liquid
1
0
2
1
0.005291
4
1
3e-05
1
0.0402
3
1
0.004925
4
1
3.3e-05
1
0.0682
3
1
0.004703
4
1
3.1e-05
1
0.1276
4
1
0.004275
4
1
2.8e-05
1
0.2056
4
1
0.003781
4
1
2.5e-05
1
0.2686
4
1
0.003412
4
1
2.2e-05
1
0.3892
4
1
0.002862
4
1
1.9e-05
1
0.4277
4
1
0.002711
4
1
1.8e-05
1
0.5444
4
1
0.002325
4
1
1.5e-05
1
0.6405
4
1
0.00207
4
1
1.4e-05
1
0.7326
4
1
0.001877
4
1
1.2e-05
1
0.8519
4
1
0.001726
4
1
1.1e-05
1
0.9273
4
1
0.00169
4
1
1.1e-05
1
0.9587
4
1
0.001692
4
1
1.1e-05
1
0.9782
4
1
0.00171
4
1
1.1e-05
1
1
5
1
0.001733
4
1
1.1e-05
12
2
1
4
1
Principal objective of the work
VN
TRC
12/17/2009
1
Mass density, kg/m3
VIBTUB:UFactor:4
Liquid
Direct value, X
1
Data file compiler
Propagation of evaluated standard uncertainties
95
Liquid
1
Temperature, K
Liquid
298.15
5
2
Pressure, kPa
Liquid
101
3
1
Mole fraction
2
Liquid
1
0
2
1
818.856
6
1
0.419
1
0.0402
3
1
856.608
6
1
0.408
1
0.0682
3
1
883.413
6
1
0.376
1
0.1276
4
1
941.916
6
1
0.309
1
0.2056
4
1
1022.358
7
1
0.279
1
0.2686
4
1
1090.467
7
1
0.371
1
0.3892
4
1
1228.973
7
1
0.574
1
0.4277
4
1
1276.432
7
1
0.656
1
0.5444
4
1
1427.131
7
1
0.9
1
0.6405
4
1
1561.996
7
1
1.129
1
0.7326
4
1
1701.636
7
1
1.373
1
0.8519
4
1
1899.692
7
1
1.722
1
0.9273
4
1
2036.524
7
1
1.972
1
0.9587
4
1
2096.509
7
1
2.084
1
0.9782
4
1
2135.291
7
1
2.157
1
1
5
1
2179.591
7
1
2.202
13
4
1
3
1
Principal objective of the work
VN
TRC
12/17/2009
1
Viscosity, Pa*s
Capillary tube (Ostwald; Ubbelohde) method
Liquid
Direct value, X
1
Data file compiler
Propagation of evaluated standard uncertainties
95
Liquid
1
Temperature, K
Liquid
293.15
5
2
Pressure, kPa
Liquid
101
3
1
Mole fraction
3
Liquid
1
0
2
1
0.005291
4
1
3e-05
1
0.0688
3
1
0.004756
4
1
3.1e-05
1
0.123
4
1
0.004351
4
1
2.9e-05
1
0.2457
4
1
0.003493
4
1
2.4e-05
1
0.3618
4
1
0.002772
4
1
2e-05
1
0.4502
4
1
0.002308
4
1
1.7e-05
1
0.5583
4
1
0.001853
4
1
1.4e-05
1
0.6518
4
1
0.001534
4
1
1.2e-05
1
0.7068
4
1
0.001382
4
1
1e-05
1
0.7419
4
1
0.001297
4
1
1e-05
1
0.7797
4
1
0.001213
4
1
9e-06
1
0.8315
4
1
0.001116
4
1
9e-06
1
0.8718
4
1
0.001051
4
1
8e-06
1
0.9179
4
1
0.000982
3
1
8e-06
1
0.9504
4
1
0.000942
3
1
7e-06
1
1
5
1
0.00089
3
1
7e-06
14
4
1
3
1
Principal objective of the work
VN
TRC
12/17/2009
1
Mass density, kg/m3
VIBTUB:UFactor:4
Liquid
Direct value, X
1
Data file compiler
Propagation of evaluated standard uncertainties
95
Liquid
1
Temperature, K
Liquid
298.15
5
2
Pressure, kPa
Liquid
101
3
1
Mole fraction
3
Liquid
1
0
2
1
818.856
6
1
0.419
1
0.0688
3
1
864.637
6
1
0.375
1
0.123
4
1
901.521
6
1
0.326
1
0.2457
4
1
987.759
6
1
0.22
1
0.3618
4
1
1072.992
7
1
0.308
1
0.4502
4
1
1140.457
7
1
0.413
1
0.5583
4
1
1226.302
7
1
0.552
1
0.6518
4
1
1303.622
7
1
0.681
1
0.7068
4
1
1350.534
7
1
0.762
1
0.7419
4
1
1381.185
7
1
0.815
1
0.7797
4
1
1414.647
7
1
0.873
1
0.8315
4
1
1461.437
7
1
0.954
1
0.8718
4
1
1498.8
7
1
1.021
1
0.9179
4
1
1542.246
7
1
1.098
1
0.9504
4
1
1573.609
7
1
1.155
1
1
5
1
1622.745
7
1
1.227