2
0
2011
gue
gar
0
journal
Original
Guerrero, H.[Hernando]
Garcia-Mardones, M.[Monica]
Pera, G.[Gorka]
Bandres, I.[Isabel]
Lafuente, C.
J. Chem. Eng. Data
2011
2020-09-29
Experimental and Predicted Kinematic Viscosities for Alkane + Chloroalkane Mixtures
In this work, kinematic viscosities of binary mixtures formed by an alkane (3-methylpentane, 2,2-dimethylbutane, n-hexane, and n-heptane) and an isomeric chlorobutane (1-chlorobutane, 2-chlorobutane, 1-chloro-2-methylpropane, and 2-chloro-2-methylpropane) have been determined as a function of composition under atmospheric at three temperatures, T = (283.15, 298.15, and 313.15) K and correlated using the McAllister equation. Kinematic viscosities were measured using an Ubbelohde viscometer. Finally, we have used the Asfour method for predicting the dependence of viscosity with composition, and the predictions were compared with the experimental data.
10.1021/je200213h
7
56
3133-3141
1
InChI=1S/C4H9Cl/c1-2-3-4-5/h2-4H2,1H3
VFWCMGCRMGJXDK-UHFFFAOYSA-N
1-chlorobutane
butyl chloride
n-butyl chloride
C4H9Cl
1
Commercial source
1
99
2
Stated by supplier
2
InChI=1S/C4H9Cl/c1-3-4(2)5/h4H,3H2,1-2H3
BSPCSKHALVHRSR-UHFFFAOYSA-N
2-chlorobutane
1-methylpropyl chloride
sec-butyl chloride
C4H9Cl
1
Commercial source
1
99
2
Stated by supplier
3
InChI=1S/C4H9Cl/c1-4(2,3)5/h1-3H3
NBRKLOOSMBRFMH-UHFFFAOYSA-N
2-chloro-2-methylpropane
1,1-dimethylethyl chloride
1-chloro-1,1-dimethylethane
2-chloroisobutane
2-methyl-2-chloropropane
2-methyl-2-propyl chloride
chlorotrimethylmethane
tert-butyl chloride
trimethylchloromethane
C4H9Cl
1
Commercial source
1
99
2
Stated by supplier
4
InChI=1S/C6H14/c1-3-5-6-4-2/h3-6H2,1-2H3
VLKZOEOYAKHREP-UHFFFAOYSA-N
hexane
n-hexane
C6H14
1
Commercial source
1
99
2
Stated by supplier
5
InChI=1S/C7H16/c1-3-5-7-6-4-2/h3-7H2,1-2H3
IMNFDUFMRHMDMM-UHFFFAOYSA-N
heptane
n-heptane
C7H16
1
Commercial source
1
99
2
Stated by supplier
6
InChI=1S/C6H14/c1-4-6(3)5-2/h6H,4-5H2,1-3H3
PFEOZHBOMNWTJB-UHFFFAOYSA-N
3-methylpentane
C6H14
1
Commercial source
1
99
2
Stated by supplier
7
InChI=1S/C6H14/c1-5-6(2,3)4/h5H2,1-4H3
HNRMPXKDFBEGFZ-UHFFFAOYSA-N
2,2-dimethylbutane
neohexane
C6H14
1
Commercial source
1
99
2
Stated by supplier
8
InChI=1S/C4H9Cl/c1-4(2)3-5/h4H,3H2,1-2H3
QTBFPMKWQKYFLR-UHFFFAOYSA-N
1-chloro-2-methylpropane
isobutyl chloride
propane, 1-chloro-2-methyl-
C4H9Cl
1
Commercial source
1
99
2
Stated by supplier
1
1
1
Principal objective of the work
BEM
XXX
7/20/2011
1
Kinematic viscosity, m2/s
Capillary tube (Ostwald; Ubbelohde) method
Liquid
Direct value, X
1
Data file compiler
Propagation of evaluated standard uncertainties
95
Liquid
1
Pressure, kPa
Liquid
101.325
6
1
Temperature, K
Liquid
1
283.15
5
1
5.564e-07
4
1
4.7e-09
1
298.15
5
1
4.785e-07
4
1
4.1e-09
1
313.15
5
1
4.216e-07
4
1
3.7e-09
2
2
1
Principal objective of the work
BEM
XXX
7/20/2011
1
Kinematic viscosity, m2/s
Capillary tube (Ostwald; Ubbelohde) method
Liquid
Direct value, X
1
Data file compiler
Propagation of evaluated standard uncertainties
95
Liquid
1
Pressure, kPa
Liquid
101.325
6
1
Temperature, K
Liquid
1
283.15
5
1
5.237e-07
4
1
4.5e-09
1
298.15
5
1
4.603e-07
4
1
4e-09
1
313.15
5
1
4.049e-07
4
1
3.6e-09
3
3
1
Principal objective of the work
BEM
XXX
7/20/2011
1
Kinematic viscosity, m2/s
Capillary tube (Ostwald; Ubbelohde) method
Liquid
Direct value, X
1
Data file compiler
Propagation of evaluated standard uncertainties
95
Liquid
1
Pressure, kPa
Liquid
101.325
6
1
Temperature, K
Liquid
1
283.15
5
1
6.992e-07
4
1
5.7e-09
1
298.15
5
1
5.696e-07
4
1
4.8e-09
1
313.15
5
1
4.77e-07
4
1
4.1e-09
4
4
1
Principal objective of the work
BEM
XXX
7/20/2011
1
Kinematic viscosity, m2/s
Capillary tube (Ostwald; Ubbelohde) method
Liquid
Direct value, X
1
Data file compiler
Propagation of evaluated standard uncertainties
95
Liquid
1
Pressure, kPa
Liquid
101.325
6
1
Temperature, K
Liquid
1
283.15
5
1
5.125e-07
4
1
4.4e-09
1
298.15
5
1
4.493e-07
4
1
3.9e-09
1
313.15
5
1
4.039e-07
4
1
3.6e-09
5
5
1
Principal objective of the work
BEM
XXX
7/20/2011
1
Kinematic viscosity, m2/s
Capillary tube (Ostwald; Ubbelohde) method
Liquid
Direct value, X
1
Data file compiler
Propagation of evaluated standard uncertainties
95
Liquid
1
Pressure, kPa
Liquid
101.325
6
1
Temperature, K
Liquid
1
283.15
5
1
6.697e-07
4
1
5.5e-09
1
298.15
5
1
5.754e-07
4
1
4.8e-09
1
313.15
5
1
4.986e-07
4
1
4.3e-09
6
6
1
Principal objective of the work
BEM
XXX
7/20/2011
1
Kinematic viscosity, m2/s
Capillary tube (Ostwald; Ubbelohde) method
Liquid
Direct value, X
1
Data file compiler
Propagation of evaluated standard uncertainties
95
Liquid
1
Pressure, kPa
Liquid
101.325
6
1
Temperature, K
Liquid
1
283.15
5
1
4.928e-07
4
1
4.2e-09
1
298.15
5
1
4.366e-07
4
1
3.8e-09
1
313.15
5
1
3.881e-07
4
1
3.5e-09
7
7
1
Principal objective of the work
BEM
XXX
7/20/2011
1
Kinematic viscosity, m2/s
Capillary tube (Ostwald; Ubbelohde) method
Liquid
Direct value, X
1
Data file compiler
Propagation of evaluated standard uncertainties
95
Liquid
1
Pressure, kPa
Liquid
101.325
6
1
Temperature, K
Liquid
1
283.15
5
1
6.234e-07
4
1
5.2e-09
1
298.15
5
1
5.206e-07
4
1
4.4e-09
1
313.15
5
1
4.579e-07
4
1
4e-09
8
8
1
Principal objective of the work
BEM
XXX
7/20/2011
1
Kinematic viscosity, m2/s
Capillary tube (Ostwald; Ubbelohde) method
Liquid
Direct value, X
1
Data file compiler
Propagation of evaluated standard uncertainties
95
Liquid
1
Pressure, kPa
Liquid
101.325
6
1
Temperature, K
Liquid
1
283.15
5
1
5.8e-07
4
1
4.9e-09
1
298.15
5
1
4.929e-07
4
1
4.2e-09
1
313.15
5
1
4.363e-07
4
1
3.8e-09
9
6
1
1
1
Principal objective of the work
BEM
XXX
7/20/2011
1
Kinematic viscosity, m2/s
Capillary tube (Ostwald; Ubbelohde) method
Liquid
Direct value, X
1
Data file compiler
Propagation of evaluated standard uncertainties
95
Liquid
1
Pressure, kPa
Liquid
101
3
1
Temperature, K
Liquid
2
Mole fraction
6
Liquid
1
283.15
5
2
0.0518
3
1
5.496e-07
4
1
4.6e-09
1
283.15
5
2
0.094
3
1
5.448e-07
4
1
4.6e-09
1
283.15
5
2
0.2038
4
1
5.326e-07
4
1
4.5e-09
1
283.15
5
2
0.304
4
1
5.228e-07
4
1
4.5e-09
1
283.15
5
2
0.4059
4
1
5.143e-07
4
1
4.4e-09
1
283.15
5
2
0.5021
4
1
5.075e-07
4
1
4.3e-09
1
283.15
5
2
0.5999
4
1
5.017e-07
4
1
4.3e-09
1
283.15
5
2
0.7043
4
1
4.97e-07
4
1
4.3e-09
1
283.15
5
2
0.8049
4
1
4.945e-07
4
1
4.2e-09
1
283.15
5
2
0.9038
4
1
4.928e-07
4
1
4.2e-09
1
283.15
5
2
0.9492
4
1
4.928e-07
4
1
4.2e-09
1
298.15
5
2
0.0518
3
1
4.734e-07
4
1
4.1e-09
1
298.15
5
2
0.094
3
1
4.704e-07
4
1
4.1e-09
1
298.15
5
2
0.2038
4
1
4.622e-07
4
1
4e-09
1
298.15
5
2
0.304
4
1
4.553e-07
4
1
4e-09
1
298.15
5
2
0.4059
4
1
4.5e-07
4
1
3.9e-09
1
298.15
5
2
0.5021
4
1
4.453e-07
4
1
3.9e-09
1
298.15
5
2
0.5999
4
1
4.411e-07
4
1
3.9e-09
1
298.15
5
2
0.7043
4
1
4.382e-07
4
1
3.8e-09
1
298.15
5
2
0.8049
4
1
4.365e-07
4
1
3.8e-09
1
298.15
5
2
0.9038
4
1
4.351e-07
4
1
3.8e-09
1
298.15
5
2
0.9492
4
1
4.355e-07
4
1
3.8e-09
1
313.15
5
2
0.0518
3
1
4.175e-07
4
1
3.7e-09
1
313.15
5
2
0.094
3
1
4.155e-07
4
1
3.7e-09
1
313.15
5
2
0.2038
4
1
4.088e-07
4
1
3.6e-09
1
313.15
5
2
0.304
4
1
4.036e-07
4
1
3.6e-09
1
313.15
5
2
0.4059
4
1
3.988e-07
4
1
3.5e-09
1
313.15
5
2
0.5021
4
1
3.952e-07
4
1
3.5e-09
1
313.15
5
2
0.5999
4
1
3.921e-07
4
1
3.5e-09
1
313.15
5
2
0.7043
4
1
3.896e-07
4
1
3.5e-09
1
313.15
5
2
0.8049
4
1
3.884e-07
4
1
3.5e-09
1
313.15
5
2
0.9038
4
1
3.879e-07
4
1
3.5e-09
1
313.15
5
2
0.9492
4
1
3.877e-07
4
1
3.5e-09
10
2
1
6
1
Principal objective of the work
BEM
XXX
7/20/2011
1
Kinematic viscosity, m2/s
Capillary tube (Ostwald; Ubbelohde) method
Liquid
Direct value, X
1
Data file compiler
Propagation of evaluated standard uncertainties
95
Liquid
1
Pressure, kPa
Liquid
101
3
1
Temperature, K
Liquid
2
Mole fraction
6
Liquid
1
283.15
5
2
0.0518
3
1
5.193e-07
4
1
4.4e-09
1
283.15
5
2
0.101
4
1
5.142e-07
4
1
4.4e-09
1
283.15
5
2
0.2014
4
1
5.066e-07
4
1
4.3e-09
1
283.15
5
2
0.3025
4
1
4.995e-07
4
1
4.3e-09
1
283.15
5
2
0.4027
4
1
4.943e-07
4
1
4.2e-09
1
283.15
5
2
0.4998
4
1
4.906e-07
4
1
4.2e-09
1
283.15
5
2
0.6043
4
1
4.881e-07
4
1
4.2e-09
1
283.15
5
2
0.7008
4
1
4.87e-07
4
1
4.2e-09
1
283.15
5
2
0.8004
4
1
4.874e-07
4
1
4.2e-09
1
283.15
5
2
0.8981
4
1
4.897e-07
4
1
4.2e-09
1
283.15
5
2
0.9481
4
1
4.911e-07
4
1
4.2e-09
1
298.15
5
2
0.0518
3
1
4.574e-07
4
1
4e-09
1
298.15
5
2
0.101
4
1
4.542e-07
4
1
4e-09
1
298.15
5
2
0.2014
4
1
4.483e-07
4
1
3.9e-09
1
298.15
5
2
0.3025
4
1
4.431e-07
4
1
3.9e-09
1
298.15
5
2
0.4027
4
1
4.39e-07
4
1
3.8e-09
1
298.15
5
2
0.4998
4
1
4.362e-07
4
1
3.8e-09
1
298.15
5
2
0.6043
4
1
4.345e-07
4
1
3.8e-09
1
298.15
5
2
0.7008
4
1
4.34e-07
4
1
3.8e-09
1
298.15
5
2
0.8004
4
1
4.337e-07
4
1
3.8e-09
1
298.15
5
2
0.8981
4
1
4.344e-07
4
1
3.8e-09
1
298.15
5
2
0.9481
4
1
4.356e-07
4
1
3.8e-09
1
313.15
5
2
0.0518
3
1
4.031e-07
4
1
3.6e-09
1
313.15
5
2
0.101
4
1
4.004e-07
4
1
3.6e-09
1
313.15
5
2
0.2014
4
1
3.958e-07
4
1
3.5e-09
1
313.15
5
2
0.3025
4
1
3.919e-07
4
1
3.5e-09
1
313.15
5
2
0.4027
4
1
3.885e-07
4
1
3.5e-09
1
313.15
5
2
0.4998
4
1
3.865e-07
4
1
3.5e-09
1
313.15
5
2
0.6043
4
1
3.851e-07
4
1
3.4e-09
1
313.15
5
2
0.7008
4
1
3.844e-07
4
1
3.4e-09
1
313.15
5
2
0.8004
4
1
3.847e-07
4
1
3.4e-09
1
313.15
5
2
0.8981
4
1
3.858e-07
4
1
3.5e-09
1
313.15
5
2
0.9481
4
1
3.868e-07
4
1
3.5e-09
11
6
1
8
1
Principal objective of the work
BEM
XXX
7/20/2011
1
Kinematic viscosity, m2/s
Capillary tube (Ostwald; Ubbelohde) method
Liquid
Direct value, X
1
Data file compiler
Propagation of evaluated standard uncertainties
95
Liquid
1
Pressure, kPa
Liquid
101
3
1
Temperature, K
Liquid
2
Mole fraction
6
Liquid
1
283.15
5
2
0.0522
3
1
5.703e-07
4
1
4.8e-09
1
283.15
5
2
0.1013
4
1
5.618e-07
4
1
4.7e-09
1
283.15
5
2
0.2024
4
1
5.464e-07
4
1
4.6e-09
1
283.15
5
2
0.3032
4
1
5.324e-07
4
1
4.5e-09
1
283.15
5
2
0.4028
4
1
5.212e-07
4
1
4.4e-09
1
283.15
5
2
0.5056
4
1
5.115e-07
4
1
4.4e-09
1
283.15
5
2
0.604
4
1
5.043e-07
4
1
4.3e-09
1
283.15
5
2
0.7018
4
1
4.988e-07
4
1
4.3e-09
1
283.15
5
2
0.8002
4
1
4.949e-07
4
1
4.2e-09
1
283.15
5
2
0.898
4
1
4.93e-07
4
1
4.2e-09
1
283.15
5
2
0.9486
4
1
4.927e-07
4
1
4.2e-09
1
298.15
5
2
0.0522
3
1
4.87e-07
4
1
4.2e-09
1
298.15
5
2
0.1013
4
1
4.823e-07
4
1
4.2e-09
1
298.15
5
2
0.2024
4
1
4.717e-07
4
1
4.1e-09
1
298.15
5
2
0.3032
4
1
4.631e-07
4
1
4e-09
1
298.15
5
2
0.4028
4
1
4.55e-07
4
1
4e-09
1
298.15
5
2
0.5056
4
1
4.484e-07
4
1
3.9e-09
1
298.15
5
2
0.604
4
1
4.43e-07
4
1
3.9e-09
1
298.15
5
2
0.7018
4
1
4.396e-07
4
1
3.8e-09
1
298.15
5
2
0.8002
4
1
4.37e-07
4
1
3.8e-09
1
298.15
5
2
0.898
4
1
4.357e-07
4
1
3.8e-09
1
298.15
5
2
0.9486
4
1
4.355e-07
4
1
3.8e-09
1
313.15
5
2
0.0522
3
1
4.322e-07
4
1
3.8e-09
1
313.15
5
2
0.1013
4
1
4.275e-07
4
1
3.8e-09
1
313.15
5
2
0.2024
4
1
4.187e-07
4
1
3.7e-09
1
313.15
5
2
0.3032
4
1
4.113e-07
4
1
3.6e-09
1
313.15
5
2
0.4028
4
1
4.048e-07
4
1
3.6e-09
1
313.15
5
2
0.5056
4
1
3.994e-07
4
1
3.6e-09
1
313.15
5
2
0.604
4
1
3.951e-07
4
1
3.5e-09
1
313.15
5
2
0.7018
4
1
3.918e-07
4
1
3.5e-09
1
313.15
5
2
0.8002
4
1
3.896e-07
4
1
3.5e-09
1
313.15
5
2
0.898
4
1
3.881e-07
4
1
3.5e-09
1
313.15
5
2
0.9486
4
1
3.879e-07
4
1
3.5e-09
12
6
1
3
1
Principal objective of the work
BEM
XXX
7/20/2011
1
Kinematic viscosity, m2/s
Capillary tube (Ostwald; Ubbelohde) method
Liquid
Direct value, X
1
Data file compiler
Propagation of evaluated standard uncertainties
95
Liquid
1
Pressure, kPa
Liquid
101
3
1
Temperature, K
Liquid
2
Mole fraction
6
Liquid
1
283.15
5
2
0.0496
3
1
6.755e-07
4
1
5.6e-09
1
283.15
5
2
0.0995
3
1
6.538e-07
4
1
5.4e-09
1
283.15
5
2
0.2046
4
1
6.148e-07
4
1
5.1e-09
1
283.15
5
2
0.3023
4
1
5.848e-07
4
1
4.9e-09
1
283.15
5
2
0.405
4
1
5.592e-07
4
1
4.7e-09
1
283.15
5
2
0.5064
4
1
5.394e-07
4
1
4.6e-09
1
283.15
5
2
0.6033
4
1
5.235e-07
4
1
4.5e-09
1
283.15
5
2
0.7038
4
1
5.114e-07
4
1
4.4e-09
1
283.15
5
2
0.8012
4
1
5.026e-07
4
1
4.3e-09
1
283.15
5
2
0.9018
4
1
4.964e-07
4
1
4.3e-09
1
283.15
5
2
0.9514
4
1
4.946e-07
4
1
4.2e-09
1
298.15
5
2
0.0496
3
1
5.548e-07
4
1
4.7e-09
1
298.15
5
2
0.0995
3
1
5.4e-07
4
1
4.6e-09
1
298.15
5
2
0.2046
4
1
5.14e-07
4
1
4.4e-09
1
298.15
5
2
0.3023
4
1
4.937e-07
4
1
4.2e-09
1
298.15
5
2
0.405
4
1
4.767e-07
4
1
4.1e-09
1
298.15
5
2
0.5064
4
1
4.637e-07
4
1
4e-09
1
298.15
5
2
0.6033
4
1
4.536e-07
4
1
3.9e-09
1
298.15
5
2
0.7038
4
1
4.462e-07
4
1
3.9e-09
1
298.15
5
2
0.8012
4
1
4.41e-07
4
1
3.9e-09
1
298.15
5
2
0.9018
4
1
4.377e-07
4
1
3.8e-09
1
298.15
5
2
0.9514
4
1
4.372e-07
4
1
3.8e-09
1
313.15
5
2
0.0496
3
1
4.681e-07
4
1
4.1e-09
1
313.15
5
2
0.0995
3
1
4.576e-07
4
1
4e-09
1
313.15
5
2
0.2046
4
1
4.4e-07
4
1
3.8e-09
1
313.15
5
2
0.3023
4
1
4.256e-07
4
1
3.7e-09
1
313.15
5
2
0.405
4
1
4.14e-07
4
1
3.7e-09
1
313.15
5
2
0.5064
4
1
4.051e-07
4
1
3.6e-09
1
313.15
5
2
0.6033
4
1
3.984e-07
4
1
3.5e-09
1
313.15
5
2
0.7038
4
1
3.933e-07
4
1
3.5e-09
1
313.15
5
2
0.8012
4
1
3.9e-07
4
1
3.5e-09
1
313.15
5
2
0.9018
4
1
3.881e-07
4
1
3.5e-09
1
313.15
5
2
0.9514
4
1
3.88e-07
4
1
3.5e-09
13
7
1
1
1
Principal objective of the work
BEM
XXX
7/20/2011
1
Kinematic viscosity, m2/s
Capillary tube (Ostwald; Ubbelohde) method
Liquid
Direct value, X
1
Data file compiler
Propagation of evaluated standard uncertainties
95
Liquid
1
Pressure, kPa
Liquid
101
3
1
Temperature, K
Liquid
2
Mole fraction
7
Liquid
1
283.15
5
2
0.0524
3
1
5.594e-07
4
1
4.7e-09
1
283.15
5
2
0.101
4
1
5.603e-07
4
1
4.7e-09
1
283.15
5
2
0.1995
4
1
5.627e-07
4
1
4.7e-09
1
283.15
5
2
0.3081
4
1
5.663e-07
4
1
4.8e-09
1
283.15
5
2
0.3985
4
1
5.705e-07
4
1
4.8e-09
1
283.15
5
2
0.499
4
1
5.76e-07
4
1
4.8e-09
1
283.15
5
2
0.5984
4
1
5.822e-07
4
1
4.9e-09
1
283.15
5
2
0.7015
4
1
5.899e-07
4
1
4.9e-09
1
283.15
5
2
0.7986
4
1
5.992e-07
4
1
5e-09
1
283.15
5
2
0.9002
4
1
6.098e-07
4
1
5.1e-09
1
283.15
5
2
0.9487
4
1
6.16e-07
4
1
5.1e-09
1
298.15
5
2
0.0524
3
1
4.802e-07
4
1
4.1e-09
1
298.15
5
2
0.101
4
1
4.809e-07
4
1
4.1e-09
1
298.15
5
2
0.1995
4
1
4.822e-07
4
1
4.2e-09
1
298.15
5
2
0.3081
4
1
4.846e-07
4
1
4.2e-09
1
298.15
5
2
0.3985
4
1
4.867e-07
4
1
4.2e-09
1
298.15
5
2
0.499
4
1
4.898e-07
4
1
4.2e-09
1
298.15
5
2
0.5984
4
1
4.943e-07
4
1
4.2e-09
1
298.15
5
2
0.7015
4
1
5e-07
4
1
4.3e-09
1
298.15
5
2
0.7986
4
1
5.063e-07
4
1
4.3e-09
1
298.15
5
2
0.9002
4
1
5.133e-07
4
1
4.4e-09
1
298.15
5
2
0.9487
4
1
5.17e-07
4
1
4.4e-09
1
313.15
5
2
0.0524
3
1
4.231e-07
4
1
3.7e-09
1
313.15
5
2
0.101
4
1
4.239e-07
4
1
3.7e-09
1
313.15
5
2
0.1995
4
1
4.253e-07
4
1
3.7e-09
1
313.15
5
2
0.3081
4
1
4.275e-07
4
1
3.8e-09
1
313.15
5
2
0.3985
4
1
4.294e-07
4
1
3.8e-09
1
313.15
5
2
0.499
4
1
4.322e-07
4
1
3.8e-09
1
313.15
5
2
0.5984
4
1
4.362e-07
4
1
3.8e-09
1
313.15
5
2
0.7015
4
1
4.409e-07
4
1
3.9e-09
1
313.15
5
2
0.7986
4
1
4.463e-07
4
1
3.9e-09
1
313.15
5
2
0.9002
4
1
4.52e-07
4
1
3.9e-09
1
313.15
5
2
0.9487
4
1
4.55e-07
4
1
4e-09
14
7
1
2
1
Principal objective of the work
BEM
XXX
7/20/2011
1
Kinematic viscosity, m2/s
Capillary tube (Ostwald; Ubbelohde) method
Liquid
Direct value, X
1
Data file compiler
Propagation of evaluated standard uncertainties
95
Liquid
1
Pressure, kPa
Liquid
101
3
1
Temperature, K
Liquid
2
Mole fraction
7
Liquid
1
283.15
5
2
0.0448
3
1
5.266e-07
4
1
4.5e-09
1
283.15
5
2
0.0993
3
1
5.3e-07
4
1
4.5e-09
1
283.15
5
2
0.2003
4
1
5.356e-07
4
1
4.5e-09
1
283.15
5
2
0.301
4
1
5.421e-07
4
1
4.6e-09
1
283.15
5
2
0.3993
4
1
5.494e-07
4
1
4.6e-09
1
283.15
5
2
0.4989
4
1
5.579e-07
4
1
4.7e-09
1
283.15
5
2
0.6039
4
1
5.683e-07
4
1
4.8e-09
1
283.15
5
2
0.7002
4
1
5.793e-07
4
1
4.9e-09
1
283.15
5
2
0.8033
4
1
5.935e-07
4
1
5e-09
1
283.15
5
2
0.9028
4
1
6.07e-07
4
1
5.1e-09
1
283.15
5
2
0.9518
4
1
6.147e-07
4
1
5.1e-09
1
298.15
5
2
0.0448
3
1
4.621e-07
4
1
4e-09
1
298.15
5
2
0.0993
3
1
4.64e-07
4
1
4e-09
1
298.15
5
2
0.2003
4
1
4.679e-07
4
1
4.1e-09
1
298.15
5
2
0.301
4
1
4.719e-07
4
1
4.1e-09
1
298.15
5
2
0.3993
4
1
4.761e-07
4
1
4.1e-09
1
298.15
5
2
0.4989
4
1
4.815e-07
4
1
4.1e-09
1
298.15
5
2
0.6039
4
1
4.88e-07
4
1
4.2e-09
1
298.15
5
2
0.7002
4
1
4.949e-07
4
1
4.2e-09
1
298.15
5
2
0.8033
4
1
5.036e-07
4
1
4.3e-09
1
298.15
5
2
0.9028
4
1
5.122e-07
4
1
4.4e-09
1
298.15
5
2
0.9518
4
1
5.165e-07
4
1
4.4e-09
1
313.15
5
2
0.0448
3
1
4.07e-07
4
1
3.6e-09
1
313.15
5
2
0.0993
3
1
4.086e-07
4
1
3.6e-09
1
313.15
5
2
0.2003
4
1
4.12e-07
4
1
3.6e-09
1
313.15
5
2
0.301
4
1
4.157e-07
4
1
3.7e-09
1
313.15
5
2
0.3993
4
1
4.2e-07
4
1
3.7e-09
1
313.15
5
2
0.4989
4
1
4.251e-07
4
1
3.7e-09
1
313.15
5
2
0.6039
4
1
4.309e-07
4
1
3.8e-09
1
313.15
5
2
0.7002
4
1
4.368e-07
4
1
3.8e-09
1
313.15
5
2
0.8033
4
1
4.438e-07
4
1
3.9e-09
1
313.15
5
2
0.9028
4
1
4.508e-07
4
1
3.9e-09
1
313.15
5
2
0.9518
4
1
4.546e-07
4
1
4e-09
15
7
1
8
1
Principal objective of the work
BEM
XXX
7/20/2011
1
Kinematic viscosity, m2/s
Capillary tube (Ostwald; Ubbelohde) method
Liquid
Direct value, X
1
Data file compiler
Propagation of evaluated standard uncertainties
95
Liquid
1
Pressure, kPa
Liquid
101
3
1
Temperature, K
Liquid
2
Mole fraction
7
Liquid
1
283.15
5
2
0.0487
3
1
5.82e-07
4
1
4.9e-09
1
283.15
5
2
0.0994
3
1
5.816e-07
4
1
4.9e-09
1
283.15
5
2
0.1995
4
1
5.814e-07
4
1
4.9e-09
1
283.15
5
2
0.2985
4
1
5.821e-07
4
1
4.9e-09
1
283.15
5
2
0.3993
4
1
5.834e-07
4
1
4.9e-09
1
283.15
5
2
0.5018
4
1
5.866e-07
4
1
4.9e-09
1
283.15
5
2
0.6011
4
1
5.899e-07
4
1
4.9e-09
1
283.15
5
2
0.6985
4
1
5.953e-07
4
1
5e-09
1
283.15
5
2
0.7995
4
1
6.024e-07
4
1
5e-09
1
283.15
5
2
0.8988
4
1
6.115e-07
4
1
5.1e-09
1
283.15
5
2
0.9479
4
1
6.158e-07
4
1
5.1e-09
1
298.15
5
2
0.0487
3
1
4.94e-07
4
1
4.2e-09
1
298.15
5
2
0.0994
3
1
4.941e-07
4
1
4.2e-09
1
298.15
5
2
0.1995
4
1
4.939e-07
4
1
4.2e-09
1
298.15
5
2
0.2985
4
1
4.939e-07
4
1
4.2e-09
1
298.15
5
2
0.3993
4
1
4.942e-07
4
1
4.2e-09
1
298.15
5
2
0.5018
4
1
4.958e-07
4
1
4.3e-09
1
298.15
5
2
0.6011
4
1
4.986e-07
4
1
4.3e-09
1
298.15
5
2
0.6985
4
1
5.025e-07
4
1
4.3e-09
1
298.15
5
2
0.7995
4
1
5.071e-07
4
1
4.3e-09
1
298.15
5
2
0.8988
4
1
5.13e-07
4
1
4.4e-09
1
298.15
5
2
0.9479
4
1
5.163e-07
4
1
4.4e-09
1
313.15
5
2
0.0487
3
1
4.366e-07
4
1
3.8e-09
1
313.15
5
2
0.0994
3
1
4.365e-07
4
1
3.8e-09
1
313.15
5
2
0.1995
4
1
4.362e-07
4
1
3.8e-09
1
313.15
5
2
0.2985
4
1
4.363e-07
4
1
3.8e-09
1
313.15
5
2
0.3993
4
1
4.366e-07
4
1
3.8e-09
1
313.15
5
2
0.5018
4
1
4.38e-07
4
1
3.8e-09
1
313.15
5
2
0.6011
4
1
4.402e-07
4
1
3.8e-09
1
313.15
5
2
0.6985
4
1
4.439e-07
4
1
3.9e-09
1
313.15
5
2
0.7995
4
1
4.476e-07
4
1
3.9e-09
1
313.15
5
2
0.8988
4
1
4.524e-07
4
1
3.9e-09
1
313.15
5
2
0.9479
4
1
4.542e-07
4
1
4e-09
16
7
1
3
1
Principal objective of the work
BEM
XXX
7/20/2011
1
Kinematic viscosity, m2/s
Capillary tube (Ostwald; Ubbelohde) method
Liquid
Direct value, X
1
Data file compiler
Propagation of evaluated standard uncertainties
95
Liquid
1
Pressure, kPa
Liquid
101
3
1
Temperature, K
Liquid
2
Mole fraction
7
Liquid
1
283.15
5
2
0.0499
3
1
6.937e-07
4
1
5.7e-09
1
283.15
5
2
0.1017
4
1
6.864e-07
4
1
5.6e-09
1
283.15
5
2
0.1983
4
1
6.729e-07
4
1
5.5e-09
1
283.15
5
2
0.3004
4
1
6.6e-07
4
1
5.5e-09
1
283.15
5
2
0.399
4
1
6.491e-07
4
1
5.4e-09
1
283.15
5
2
0.4989
4
1
6.399e-07
4
1
5.3e-09
1
283.15
5
2
0.6017
4
1
6.32e-07
4
1
5.2e-09
1
283.15
5
2
0.7034
4
1
6.27e-07
4
1
5.2e-09
1
283.15
5
2
0.8
4
1
6.228e-07
4
1
5.2e-09
1
283.15
5
2
0.8967
4
1
6.221e-07
4
1
5.2e-09
1
283.15
5
2
0.9504
4
1
6.224e-07
4
1
5.2e-09
1
298.15
5
2
0.0499
3
1
5.657e-07
4
1
4.8e-09
1
298.15
5
2
0.1017
4
1
5.592e-07
4
1
4.7e-09
1
298.15
5
2
0.1983
4
1
5.493e-07
4
1
4.6e-09
1
298.15
5
2
0.3004
4
1
5.405e-07
4
1
4.6e-09
1
298.15
5
2
0.399
4
1
5.333e-07
4
1
4.5e-09
1
298.15
5
2
0.4989
4
1
5.275e-07
4
1
4.5e-09
1
298.15
5
2
0.6017
4
1
5.225e-07
4
1
4.4e-09
1
298.15
5
2
0.7034
4
1
5.2e-07
4
1
4.4e-09
1
298.15
5
2
0.8
4
1
5.18e-07
4
1
4.4e-09
1
298.15
5
2
0.8967
4
1
5.184e-07
4
1
4.4e-09
1
298.15
5
2
0.9504
4
1
5.19e-07
4
1
4.4e-09
1
313.15
5
2
0.0499
3
1
4.748e-07
4
1
4.1e-09
1
313.15
5
2
0.1017
4
1
4.715e-07
4
1
4.1e-09
1
313.15
5
2
0.1983
4
1
4.664e-07
4
1
4e-09
1
313.15
5
2
0.3004
4
1
4.607e-07
4
1
4e-09
1
313.15
5
2
0.399
4
1
4.568e-07
4
1
4e-09
1
313.15
5
2
0.4989
4
1
4.538e-07
4
1
3.9e-09
1
313.15
5
2
0.6017
4
1
4.522e-07
4
1
3.9e-09
1
313.15
5
2
0.7034
4
1
4.518e-07
4
1
3.9e-09
1
313.15
5
2
0.8
4
1
4.519e-07
4
1
3.9e-09
1
313.15
5
2
0.8967
4
1
4.541e-07
4
1
3.9e-09
1
313.15
5
2
0.9504
4
1
4.556e-07
4
1
4e-09
17
1
1
4
1
Principal objective of the work
BEM
XXX
7/20/2011
1
Kinematic viscosity, m2/s
Capillary tube (Ostwald; Ubbelohde) method
Liquid
Direct value, X
1
Data file compiler
Propagation of evaluated standard uncertainties
95
Liquid
1
Pressure, kPa
Liquid
101
3
1
Temperature, K
Liquid
2
Mole fraction
1
Liquid
1
283.15
5
2
0.0508
3
1
5.501e-07
4
1
4.7e-09
1
283.15
5
2
0.0992
3
1
5.449e-07
4
1
4.6e-09
1
283.15
5
2
0.1972
4
1
5.351e-07
4
1
4.5e-09
1
283.15
5
2
0.2966
4
1
5.269e-07
4
1
4.5e-09
1
283.15
5
2
0.3976
4
1
5.198e-07
4
1
4.4e-09
1
283.15
5
2
0.5009
4
1
5.145e-07
4
1
4.4e-09
1
283.15
5
2
0.6006
4
1
5.112e-07
4
1
4.4e-09
1
283.15
5
2
0.6982
4
1
5.092e-07
4
1
4.4e-09
1
283.15
5
2
0.7972
4
1
5.082e-07
4
1
4.3e-09
1
283.15
5
2
0.8979
4
1
5.094e-07
4
1
4.4e-09
1
283.15
5
2
0.9472
4
1
5.103e-07
4
1
4.4e-09
1
298.15
5
2
0.0508
3
1
4.74e-07
4
1
4.1e-09
1
298.15
5
2
0.0992
3
1
4.701e-07
4
1
4.1e-09
1
298.15
5
2
0.1972
4
1
4.634e-07
4
1
4e-09
1
298.15
5
2
0.2966
4
1
4.577e-07
4
1
4e-09
1
298.15
5
2
0.3976
4
1
4.531e-07
4
1
3.9e-09
1
298.15
5
2
0.5009
4
1
4.495e-07
4
1
3.9e-09
1
298.15
5
2
0.6006
4
1
4.467e-07
4
1
3.9e-09
1
298.15
5
2
0.6982
4
1
4.451e-07
4
1
3.9e-09
1
298.15
5
2
0.7972
4
1
4.455e-07
4
1
3.9e-09
1
298.15
5
2
0.8979
4
1
4.464e-07
4
1
3.9e-09
1
298.15
5
2
0.9472
4
1
4.474e-07
4
1
3.9e-09
1
313.15
5
2
0.0508
3
1
4.182e-07
4
1
3.7e-09
1
313.15
5
2
0.0992
3
1
4.169e-07
4
1
3.7e-09
1
313.15
5
2
0.1972
4
1
4.118e-07
4
1
3.6e-09
1
313.15
5
2
0.2966
4
1
4.08e-07
4
1
3.6e-09
1
313.15
5
2
0.3976
4
1
4.048e-07
4
1
3.6e-09
1
313.15
5
2
0.5009
4
1
4.027e-07
4
1
3.6e-09
1
313.15
5
2
0.6006
4
1
4.011e-07
4
1
3.6e-09
1
313.15
5
2
0.6982
4
1
4.005e-07
4
1
3.6e-09
1
313.15
5
2
0.7972
4
1
4.01e-07
4
1
3.6e-09
1
313.15
5
2
0.8979
4
1
4.023e-07
4
1
3.6e-09
1
313.15
5
2
0.9472
4
1
4.027e-07
4
1
3.6e-09
18
2
1
4
1
Principal objective of the work
BEM
XXX
7/20/2011
1
Kinematic viscosity, m2/s
Capillary tube (Ostwald; Ubbelohde) method
Liquid
Direct value, X
1
Data file compiler
Propagation of evaluated standard uncertainties
95
Liquid
1
Pressure, kPa
Liquid
101
3
1
Temperature, K
Liquid
2
Mole fraction
2
Liquid
1
283.15
5
2
0.0509
3
1
5.186e-07
4
1
4.4e-09
1
283.15
5
2
0.1002
4
1
5.147e-07
4
1
4.4e-09
1
283.15
5
2
0.1802
4
1
5.09e-07
4
1
4.3e-09
1
283.15
5
2
0.3029
4
1
5.025e-07
4
1
4.3e-09
1
283.15
5
2
0.4045
4
1
4.989e-07
4
1
4.3e-09
1
283.15
5
2
0.4991
4
1
4.975e-07
4
1
4.3e-09
1
283.15
5
2
0.5974
4
1
4.968e-07
4
1
4.3e-09
1
283.15
5
2
0.6992
4
1
4.982e-07
4
1
4.3e-09
1
283.15
5
2
0.7996
4
1
5.007e-07
4
1
4.3e-09
1
283.15
5
2
0.8981
4
1
5.055e-07
4
1
4.3e-09
1
283.15
5
2
0.9477
4
1
5.086e-07
4
1
4.3e-09
1
298.15
5
2
0.0509
3
1
4.579e-07
4
1
4e-09
1
298.15
5
2
0.1002
4
1
4.548e-07
4
1
4e-09
1
298.15
5
2
0.1802
4
1
4.501e-07
4
1
3.9e-09
1
298.15
5
2
0.3029
4
1
4.448e-07
4
1
3.9e-09
1
298.15
5
2
0.4045
4
1
4.42e-07
4
1
3.9e-09
1
298.15
5
2
0.4991
4
1
4.408e-07
4
1
3.9e-09
1
298.15
5
2
0.5974
4
1
4.401e-07
4
1
3.8e-09
1
298.15
5
2
0.6992
4
1
4.406e-07
4
1
3.9e-09
1
298.15
5
2
0.7996
4
1
4.419e-07
4
1
3.9e-09
1
298.15
5
2
0.8981
4
1
4.447e-07
4
1
3.9e-09
1
298.15
5
2
0.9477
4
1
4.465e-07
4
1
3.9e-09
1
313.15
5
2
0.0509
3
1
4.034e-07
4
1
3.6e-09
1
313.15
5
2
0.1002
4
1
4.012e-07
4
1
3.6e-09
1
313.15
5
2
0.1802
4
1
3.98e-07
4
1
3.5e-09
1
313.15
5
2
0.3029
4
1
3.948e-07
4
1
3.5e-09
1
313.15
5
2
0.4045
4
1
3.932e-07
4
1
3.5e-09
1
313.15
5
2
0.4991
4
1
3.926e-07
4
1
3.5e-09
1
313.15
5
2
0.5974
4
1
3.926e-07
4
1
3.5e-09
1
313.15
5
2
0.6992
4
1
3.939e-07
4
1
3.5e-09
1
313.15
5
2
0.7996
4
1
3.961e-07
4
1
3.5e-09
1
313.15
5
2
0.8981
4
1
3.993e-07
4
1
3.6e-09
1
313.15
5
2
0.9477
4
1
4.015e-07
4
1
3.6e-09
19
4
1
8
1
Principal objective of the work
BEM
XXX
7/20/2011
1
Kinematic viscosity, m2/s
Capillary tube (Ostwald; Ubbelohde) method
Liquid
Direct value, X
1
Data file compiler
Propagation of evaluated standard uncertainties
95
Liquid
1
Pressure, kPa
Liquid
101
3
1
Temperature, K
Liquid
2
Mole fraction
4
Liquid
1
283.15
5
2
0.0512
3
1
5.712e-07
4
1
4.8e-09
1
283.15
5
2
0.0999
3
1
5.631e-07
4
1
4.7e-09
1
283.15
5
2
0.2003
4
1
5.468e-07
4
1
4.6e-09
1
283.15
5
2
0.2993
4
1
5.339e-07
4
1
4.5e-09
1
283.15
5
2
0.4005
4
1
5.239e-07
4
1
4.5e-09
1
283.15
5
2
0.4977
4
1
5.171e-07
4
1
4.4e-09
1
283.15
5
2
0.598
4
1
5.12e-07
4
1
4.4e-09
1
283.15
5
2
0.6993
4
1
5.089e-07
4
1
4.3e-09
1
283.15
5
2
0.799
4
1
5.077e-07
4
1
4.3e-09
1
283.15
5
2
0.8967
4
1
5.092e-07
4
1
4.4e-09
1
283.15
5
2
0.9472
4
1
5.103e-07
4
1
4.4e-09
1
298.15
5
2
0.0512
3
1
4.863e-07
4
1
4.2e-09
1
298.15
5
2
0.0999
3
1
4.817e-07
4
1
4.2e-09
1
298.15
5
2
0.2003
4
1
4.711e-07
4
1
4.1e-09
1
298.15
5
2
0.2993
4
1
4.633e-07
4
1
4e-09
1
298.15
5
2
0.4005
4
1
4.566e-07
4
1
4e-09
1
298.15
5
2
0.4977
4
1
4.517e-07
4
1
3.9e-09
1
298.15
5
2
0.598
4
1
4.478e-07
4
1
3.9e-09
1
298.15
5
2
0.6993
4
1
4.462e-07
4
1
3.9e-09
1
298.15
5
2
0.799
4
1
4.455e-07
4
1
3.9e-09
1
298.15
5
2
0.8967
4
1
4.457e-07
4
1
3.9e-09
1
298.15
5
2
0.9472
4
1
4.474e-07
4
1
3.9e-09
1
313.15
5
2
0.0512
3
1
4.32e-07
4
1
3.8e-09
1
313.15
5
2
0.0999
3
1
4.282e-07
4
1
3.8e-09
1
313.15
5
2
0.2003
4
1
4.196e-07
4
1
3.7e-09
1
313.15
5
2
0.2993
4
1
4.128e-07
4
1
3.6e-09
1
313.15
5
2
0.4005
4
1
4.077e-07
4
1
3.6e-09
1
313.15
5
2
0.4977
4
1
4.041e-07
4
1
3.6e-09
1
313.15
5
2
0.598
4
1
4.017e-07
4
1
3.6e-09
1
313.15
5
2
0.6993
4
1
4.01e-07
4
1
3.6e-09
1
313.15
5
2
0.799
4
1
4.002e-07
4
1
3.6e-09
1
313.15
5
2
0.8967
4
1
4.006e-07
4
1
3.6e-09
1
313.15
5
2
0.9472
4
1
4.023e-07
4
1
3.6e-09
20
4
1
3
1
Principal objective of the work
BEM
XXX
7/20/2011
1
Kinematic viscosity, m2/s
Capillary tube (Ostwald; Ubbelohde) method
Liquid
Direct value, X
1
Data file compiler
Propagation of evaluated standard uncertainties
95
Liquid
1
Pressure, kPa
Liquid
101
3
1
Temperature, K
Liquid
2
Mole fraction
4
Liquid
1
283.15
5
2
0.0495
3
1
6.722e-07
4
1
5.5e-09
1
283.15
5
2
0.0989
3
1
6.489e-07
4
1
5.4e-09
1
283.15
5
2
0.2019
4
1
6.091e-07
4
1
5.1e-09
1
283.15
5
2
0.2987
4
1
5.81e-07
4
1
4.9e-09
1
283.15
5
2
0.4043
4
1
5.575e-07
4
1
4.7e-09
1
283.15
5
2
0.4985
4
1
5.415e-07
4
1
4.6e-09
1
283.15
5
2
0.6024
4
1
5.287e-07
4
1
4.5e-09
1
283.15
5
2
0.7017
4
1
5.203e-07
4
1
4.4e-09
1
283.15
5
2
0.7996
4
1
5.151e-07
4
1
4.4e-09
1
283.15
5
2
0.9025
4
1
5.123e-07
4
1
4.4e-09
1
283.15
5
2
0.9498
4
1
5.119e-07
4
1
4.4e-09
1
298.15
5
2
0.0495
3
1
5.527e-07
4
1
4.7e-09
1
298.15
5
2
0.0989
3
1
5.369e-07
4
1
4.6e-09
1
298.15
5
2
0.2019
4
1
5.105e-07
4
1
4.4e-09
1
298.15
5
2
0.2987
4
1
4.916e-07
4
1
4.2e-09
1
298.15
5
2
0.4043
4
1
4.756e-07
4
1
4.1e-09
1
298.15
5
2
0.4985
4
1
4.651e-07
4
1
4e-09
1
298.15
5
2
0.6024
4
1
4.571e-07
4
1
4e-09
1
298.15
5
2
0.7017
4
1
4.516e-07
4
1
3.9e-09
1
298.15
5
2
0.7996
4
1
4.489e-07
4
1
3.9e-09
1
298.15
5
2
0.9025
4
1
4.478e-07
4
1
3.9e-09
1
298.15
5
2
0.9498
4
1
4.483e-07
4
1
3.9e-09
1
313.15
5
2
0.0495
3
1
4.671e-07
4
1
4e-09
1
313.15
5
2
0.0989
3
1
4.565e-07
4
1
4e-09
1
313.15
5
2
0.2019
4
1
4.391e-07
4
1
3.8e-09
1
313.15
5
2
0.2987
4
1
4.266e-07
4
1
3.7e-09
1
313.15
5
2
0.4043
4
1
4.162e-07
4
1
3.7e-09
1
313.15
5
2
0.4985
4
1
4.095e-07
4
1
3.6e-09
1
313.15
5
2
0.6024
4
1
4.048e-07
4
1
3.6e-09
1
313.15
5
2
0.7017
4
1
4.019e-07
4
1
3.6e-09
1
313.15
5
2
0.7996
4
1
4.009e-07
4
1
3.6e-09
1
313.15
5
2
0.9025
4
1
4.016e-07
4
1
3.6e-09
1
313.15
5
2
0.9498
4
1
4.023e-07
4
1
3.6e-09
21
1
1
5
1
Principal objective of the work
BEM
XXX
7/20/2011
1
Kinematic viscosity, m2/s
Capillary tube (Ostwald; Ubbelohde) method
Liquid
Direct value, X
1
Data file compiler
Propagation of evaluated standard uncertainties
95
Liquid
1
Pressure, kPa
Liquid
101
3
1
Temperature, K
Liquid
2
Mole fraction
1
Liquid
1
283.15
5
2
0.0508
3
1
5.595e-07
4
1
4.7e-09
1
283.15
5
2
0.1017
4
1
5.632e-07
4
1
4.7e-09
1
283.15
5
2
0.1981
4
1
5.703e-07
4
1
4.8e-09
1
283.15
5
2
0.2989
4
1
5.788e-07
4
1
4.9e-09
1
283.15
5
2
0.4022
4
1
5.882e-07
4
1
4.9e-09
1
283.15
5
2
0.4998
4
1
5.984e-07
4
1
5e-09
1
283.15
5
2
0.6008
4
1
6.102e-07
4
1
5.1e-09
1
283.15
5
2
0.6989
4
1
6.229e-07
4
1
5.2e-09
1
283.15
5
2
0.7985
4
1
6.367e-07
4
1
5.3e-09
1
283.15
5
2
0.898
4
1
6.52e-07
4
1
5.4e-09
1
283.15
5
2
0.9498
4
1
6.608e-07
4
1
5.5e-09
1
298.15
5
2
0.0508
3
1
4.824e-07
4
1
4.2e-09
1
298.15
5
2
0.1017
4
1
4.857e-07
4
1
4.2e-09
1
298.15
5
2
0.1981
4
1
4.927e-07
4
1
4.2e-09
1
298.15
5
2
0.2989
4
1
5e-07
4
1
4.3e-09
1
298.15
5
2
0.4022
4
1
5.088e-07
4
1
4.3e-09
1
298.15
5
2
0.4998
4
1
5.177e-07
4
1
4.4e-09
1
298.15
5
2
0.6008
4
1
5.278e-07
4
1
4.5e-09
1
298.15
5
2
0.6989
4
1
5.386e-07
4
1
4.6e-09
1
298.15
5
2
0.7985
4
1
5.501e-07
4
1
4.7e-09
1
298.15
5
2
0.898
4
1
5.626e-07
4
1
4.7e-09
1
298.15
5
2
0.9498
4
1
5.692e-07
4
1
4.8e-09
1
313.15
5
2
0.0508
3
1
4.248e-07
4
1
3.7e-09
1
313.15
5
2
0.1017
4
1
4.278e-07
4
1
3.8e-09
1
313.15
5
2
0.1981
4
1
4.335e-07
4
1
3.8e-09
1
313.15
5
2
0.2989
4
1
4.396e-07
4
1
3.8e-09
1
313.15
5
2
0.4022
4
1
4.471e-07
4
1
3.9e-09
1
313.15
5
2
0.4998
4
1
4.545e-07
4
1
4e-09
1
313.15
5
2
0.6008
4
1
4.624e-07
4
1
4e-09
1
313.15
5
2
0.6989
4
1
4.705e-07
4
1
4.1e-09
1
313.15
5
2
0.7985
4
1
4.792e-07
4
1
4.1e-09
1
313.15
5
2
0.898
4
1
4.882e-07
4
1
4.2e-09
1
313.15
5
2
0.9498
4
1
4.935e-07
4
1
4.2e-09
22
2
1
5
1
Principal objective of the work
BEM
XXX
7/20/2011
1
Kinematic viscosity, m2/s
Capillary tube (Ostwald; Ubbelohde) method
Liquid
Direct value, X
1
Data file compiler
Propagation of evaluated standard uncertainties
95
Liquid
1
Pressure, kPa
Liquid
101
3
1
Temperature, K
Liquid
2
Mole fraction
2
Liquid
1
283.15
5
2
0.0506
3
1
5.287e-07
4
1
4.5e-09
1
283.15
5
2
0.0989
3
1
5.334e-07
4
1
4.5e-09
1
283.15
5
2
0.2012
4
1
5.44e-07
4
1
4.6e-09
1
283.15
5
2
0.3016
4
1
5.558e-07
4
1
4.7e-09
1
283.15
5
2
0.3997
4
1
5.677e-07
4
1
4.8e-09
1
283.15
5
2
0.4984
4
1
5.812e-07
4
1
4.9e-09
1
283.15
5
2
0.5994
4
1
5.966e-07
4
1
5e-09
1
283.15
5
2
0.6994
4
1
6.128e-07
4
1
5.1e-09
1
283.15
5
2
0.7996
4
1
6.304e-07
4
1
5.2e-09
1
283.15
5
2
0.9006
4
1
6.496e-07
4
1
5.4e-09
1
283.15
5
2
0.9503
4
1
6.6e-07
4
1
5.5e-09
1
298.15
5
2
0.0506
3
1
4.649e-07
4
1
4e-09
1
298.15
5
2
0.0989
3
1
4.686e-07
4
1
4.1e-09
1
298.15
5
2
0.2012
4
1
4.78e-07
4
1
4.1e-09
1
298.15
5
2
0.3016
4
1
4.876e-07
4
1
4.2e-09
1
298.15
5
2
0.3997
4
1
4.978e-07
4
1
4.3e-09
1
298.15
5
2
0.4984
4
1
5.087e-07
4
1
4.3e-09
1
298.15
5
2
0.5994
4
1
5.206e-07
4
1
4.4e-09
1
298.15
5
2
0.6994
4
1
5.331e-07
4
1
4.5e-09
1
298.15
5
2
0.7996
4
1
5.467e-07
4
1
4.6e-09
1
298.15
5
2
0.9006
4
1
5.609e-07
4
1
4.7e-09
1
298.15
5
2
0.9503
4
1
5.684e-07
4
1
4.8e-09
1
313.15
5
2
0.0506
3
1
4.086e-07
4
1
3.6e-09
1
313.15
5
2
0.0989
3
1
4.121e-07
4
1
3.6e-09
1
313.15
5
2
0.2012
4
1
4.202e-07
4
1
3.7e-09
1
313.15
5
2
0.3016
4
1
4.283e-07
4
1
3.8e-09
1
313.15
5
2
0.3997
4
1
4.37e-07
4
1
3.8e-09
1
313.15
5
2
0.4984
4
1
4.461e-07
4
1
3.9e-09
1
313.15
5
2
0.5994
4
1
4.558e-07
4
1
4e-09
1
313.15
5
2
0.6994
4
1
4.652e-07
4
1
4e-09
1
313.15
5
2
0.7996
4
1
4.757e-07
4
1
4.1e-09
1
313.15
5
2
0.9006
4
1
4.866e-07
4
1
4.2e-09
1
313.15
5
2
0.9503
4
1
4.927e-07
4
1
4.2e-09
23
5
1
8
1
Principal objective of the work
BEM
XXX
7/20/2011
1
Kinematic viscosity, m2/s
Capillary tube (Ostwald; Ubbelohde) method
Liquid
Direct value, X
1
Data file compiler
Propagation of evaluated standard uncertainties
95
Liquid
1
Pressure, kPa
Liquid
101
3
1
Temperature, K
Liquid
2
Mole fraction
5
Liquid
1
283.15
5
2
0.0507
3
1
5.818e-07
4
1
4.9e-09
1
283.15
5
2
0.0979
3
1
5.817e-07
4
1
4.9e-09
1
283.15
5
2
0.2004
4
1
5.851e-07
4
1
4.9e-09
1
283.15
5
2
0.3008
4
1
5.905e-07
4
1
4.9e-09
1
283.15
5
2
0.3993
4
1
5.97e-07
4
1
5e-09
1
283.15
5
2
0.4999
4
1
6.054e-07
4
1
5.1e-09
1
283.15
5
2
0.5973
4
1
6.156e-07
4
1
5.1e-09
1
283.15
5
2
0.6994
4
1
6.268e-07
4
1
5.2e-09
1
283.15
5
2
0.8006
4
1
6.397e-07
4
1
5.3e-09
1
283.15
5
2
0.9002
4
1
6.538e-07
4
1
5.4e-09
1
283.15
5
2
0.9491
4
1
6.615e-07
4
1
5.5e-09
1
298.15
5
2
0.0507
3
1
4.95e-07
4
1
4.2e-09
1
298.15
5
2
0.0979
3
1
4.97e-07
4
1
4.3e-09
1
298.15
5
2
0.2004
4
1
5.015e-07
4
1
4.3e-09
1
298.15
5
2
0.3008
4
1
5.064e-07
4
1
4.3e-09
1
298.15
5
2
0.3993
4
1
5.134e-07
4
1
4.4e-09
1
298.15
5
2
0.4999
4
1
5.215e-07
4
1
4.4e-09
1
298.15
5
2
0.5973
4
1
5.306e-07
4
1
4.5e-09
1
298.15
5
2
0.6994
4
1
5.403e-07
4
1
4.6e-09
1
298.15
5
2
0.8006
4
1
5.516e-07
4
1
4.7e-09
1
298.15
5
2
0.9002
4
1
5.633e-07
4
1
4.7e-09
1
298.15
5
2
0.9491
4
1
5.692e-07
4
1
4.8e-09
1
313.15
5
2
0.0507
3
1
4.381e-07
4
1
3.8e-09
1
313.15
5
2
0.0979
3
1
4.396e-07
4
1
3.8e-09
1
313.15
5
2
0.2004
4
1
4.438e-07
4
1
3.9e-09
1
313.15
5
2
0.3008
4
1
4.483e-07
4
1
3.9e-09
1
313.15
5
2
0.3993
4
1
4.536e-07
4
1
3.9e-09
1
313.15
5
2
0.4999
4
1
4.599e-07
4
1
4e-09
1
313.15
5
2
0.5973
4
1
4.663e-07
4
1
4e-09
1
313.15
5
2
0.6994
4
1
4.733e-07
4
1
4.1e-09
1
313.15
5
2
0.8006
4
1
4.809e-07
4
1
4.1e-09
1
313.15
5
2
0.9002
4
1
4.894e-07
4
1
4.2e-09
1
313.15
5
2
0.9491
4
1
4.94e-07
4
1
4.2e-09
24
5
1
3
1
Principal objective of the work
BEM
XXX
7/20/2011
1
Kinematic viscosity, m2/s
Capillary tube (Ostwald; Ubbelohde) method
Liquid
Direct value, X
1
Data file compiler
Propagation of evaluated standard uncertainties
95
Liquid
1
Pressure, kPa
Liquid
101
3
1
Temperature, K
Liquid
2
Mole fraction
5
Liquid
1
283.15
5
2
0.0519
3
1
6.84e-07
4
1
5.6e-09
1
283.15
5
2
0.1021
4
1
6.722e-07
4
1
5.5e-09
1
283.15
5
2
0.2015
4
1
6.546e-07
4
1
5.4e-09
1
283.15
5
2
0.3006
4
1
6.44e-07
4
1
5.3e-09
1
283.15
5
2
0.3997
4
1
6.391e-07
4
1
5.3e-09
1
283.15
5
2
0.5027
4
1
6.376e-07
4
1
5.3e-09
1
283.15
5
2
0.6011
4
1
6.397e-07
4
1
5.3e-09
1
283.15
5
2
0.7014
4
1
6.441e-07
4
1
5.3e-09
1
283.15
5
2
0.8007
4
1
6.504e-07
4
1
5.4e-09
1
283.15
5
2
0.8966
4
1
6.591e-07
4
1
5.4e-09
1
283.15
5
2
0.9518
4
1
6.651e-07
4
1
5.5e-09
1
298.15
5
2
0.0519
3
1
5.603e-07
4
1
4.7e-09
1
298.15
5
2
0.1021
4
1
5.532e-07
4
1
4.7e-09
1
298.15
5
2
0.2015
4
1
5.438e-07
4
1
4.6e-09
1
298.15
5
2
0.3006
4
1
5.389e-07
4
1
4.6e-09
1
298.15
5
2
0.3997
4
1
5.38e-07
4
1
4.6e-09
1
298.15
5
2
0.5027
4
1
5.391e-07
4
1
4.6e-09
1
298.15
5
2
0.6011
4
1
5.434e-07
4
1
4.6e-09
1
298.15
5
2
0.7014
4
1
5.489e-07
4
1
4.6e-09
1
298.15
5
2
0.8007
4
1
5.572e-07
4
1
4.7e-09
1
298.15
5
2
0.8966
4
1
5.652e-07
4
1
4.8e-09
1
298.15
5
2
0.9518
4
1
5.706e-07
4
1
4.8e-09
1
313.15
5
2
0.0519
3
1
4.741e-07
4
1
4.1e-09
1
313.15
5
2
0.1021
4
1
4.711e-07
4
1
4.1e-09
1
313.15
5
2
0.2015
4
1
4.675e-07
4
1
4e-09
1
313.15
5
2
0.3006
4
1
4.666e-07
4
1
4e-09
1
313.15
5
2
0.3997
4
1
4.679e-07
4
1
4.1e-09
1
313.15
5
2
0.5027
4
1
4.699e-07
4
1
4.1e-09
1
313.15
5
2
0.6011
4
1
4.735e-07
4
1
4.1e-09
1
313.15
5
2
0.7014
4
1
4.78e-07
4
1
4.1e-09
1
313.15
5
2
0.8007
4
1
4.832e-07
4
1
4.2e-09
1
313.15
5
2
0.8966
4
1
4.894e-07
4
1
4.2e-09
1
313.15
5
2
0.9518
4
1
4.944e-07
4
1
4.2e-09