2
0
2010
fat
ilo
0
journal
Original
Fattahi, M.
Iloukhani, H.
J. Chem. Thermodyn.
2010
2020-09-29
Excess molar volume, viscosity, and refractive index study for the ternary mixture {2-methyl-2-butanol (1) + tetrahydrofuran (2) + propylamine (3)} at different temperatures. Application of the ERAS-model and Peng Robinson Stryjek Vera equation of state
Densities, viscosities, and refractive indices of the ternary mixture consist of {2-methyl-2-butanol (1) + tetrahydrofuran (THF) (2) + propylamine (3)} at a temperature of 298.15 K and related binary mixtures were measured at temperatures of (288.15, 298.15, and 308.15) K at ambient pressure. Data were used to calculate the excess molar volumes and the deviations of the viscosity and refractive index. The Redlich Kister and the Cibulka equations were used for correlating binary and ternary properties, respectively. The ERAS-model has been applied for describing the binary and ternary excess molar volumes and also Peng Robinson Stryjek Vera (PRSV) equation of state (EOS) has been used to predict the binary and ternary excess molar volumes and viscosities.
Density
Viscosity
Refractive index
ERAS-model
PRSV EOS
10.1016/j.jct.2010.05.009
11
42
1335-1345
1
InChI=1S/C3H9N/c1-2-3-4/h2-4H2,1H3
WGYKZJWCGVVSQN-UHFFFAOYSA-N
propan-1-amine
1-aminopropane
1-propanamine
n-propylamine
propylamine
C3H9N
1
Commercial source
1
99
2
Stated by supplier
2
InChI=1S/C4H8O/c1-2-4-5-3-1/h1-4H2
WYURNTSHIVDZCO-UHFFFAOYSA-N
tetrahydrofuran
1,4-epoxybutane
THF
oxacyclopentane
oxolane
tetramethylene oxide
C4H8O
1
Commercial source
1
99
2
Stated by supplier
3
InChI=1S/C5H12O/c1-4-5(2,3)6/h6H,4H2,1-3H3
MSXVEPNJUHWQHW-UHFFFAOYSA-N
2-methylbutan-2-ol
2-methyl-2-butanol
tert-amyl alcohol
tert-pentyl alcohol
C5H12O
1
Commercial source
1
99
2
Stated by supplier
1
1
1
Principal objective of the work
VVD
TRC
7/17/2019
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
Pressure, kPa
Liquid
101
3
1
Temperature, K
Liquid
1
288.15
5
1
0.0003851
4
1
3.4e-06
1
298.15
5
1
0.0003585
4
1
3.3e-06
1
308.15
5
1
0.0003222
4
1
3e-06
2
1
1
Principal objective of the work
VVD
TRC
7/17/2019
1
Mass density, kg/m3
Vibrating tube 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
1
288.15
5
1
721.57
5
1
0.25
1
298.15
5
1
711.08
5
1
0.25
1
308.15
5
1
700.4
5
1
0.25
3
1
1
Principal objective of the work
KNA
TRC
1/22/2010
1
Refractive index (Na D-line)
Standard Abbe refractometry
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
288.15
5
1
1.3899
5
1
0.0004
1
298.15
5
1
1.3844
5
1
0.0004
1
308.15
5
1
1.3784
5
1
0.0004
4
2
1
Principal objective of the work
VVD
TRC
7/17/2019
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
Pressure, kPa
Liquid
101
3
1
Temperature, K
Liquid
1
288.15
5
1
0.0004991
4
1
4.3e-06
1
298.15
5
1
0.000454
4
1
4e-06
1
308.15
5
1
0.0004172
4
1
3.7e-06
5
2
1
Principal objective of the work
VVD
TRC
7/17/2019
1
Mass density, kg/m3
Vibrating tube 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
1
288.15
5
1
892.92
5
1
0.23
1
298.15
5
1
882.03
5
1
0.24
1
308.15
5
1
871.01
5
1
0.24
6
2
1
Principal objective of the work
KNA
TRC
1/22/2010
1
Refractive index (Na D-line)
Standard Abbe refractometry
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
288.15
5
1
1.4086
5
1
0.0004
1
298.15
5
1
1.4037
5
1
0.0004
1
308.15
5
1
1.3987
5
1
0.0004
7
3
1
Principal objective of the work
VVD
TRC
7/17/2019
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
Pressure, kPa
Liquid
101
3
1
Temperature, K
Liquid
1
288.15
5
1
0.0058667
5
1
4.34e-05
1
298.15
5
1
0.0034781
5
1
2.68e-05
1
308.15
5
1
0.0025042
5
1
1.93e-05
8
3
1
Principal objective of the work
VVD
TRC
7/17/2019
1
Mass density, kg/m3
Vibrating tube 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
1
288.15
5
1
814.01
5
1
0.24
1
298.15
5
1
804.88
5
1
0.24
1
308.15
5
1
795.52
5
1
0.24
9
3
1
Principal objective of the work
KNA
TRC
1/22/2010
1
Refractive index (Na D-line)
Standard Abbe refractometry
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
288.15
5
1
1.4062
5
1
0.0004
1
298.15
5
1
1.4015
5
1
0.0004
1
308.15
5
1
1.3968
5
1
0.0004
10
1
1
2
1
Principal objective of the work
RDC
TRC
11/30/2010
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
Pressure, kPa
Liquid
101
3
1
Temperature, K
Liquid
2
Mole fraction
2
Liquid
1
288.15
5
2
0
2
1
0.0003851
4
1
3.4e-06
1
288.15
5
2
0.0542
3
1
0.0003898
4
1
3.5e-06
1
288.15
5
2
0.1599
4
1
0.0003991
4
1
3.6e-06
1
288.15
5
2
0.1934
4
1
0.0004021
4
1
3.6e-06
1
288.15
5
2
0.3199
4
1
0.0004138
4
1
3.7e-06
1
288.15
5
2
0.4
4
1
0.0004211
4
1
3.7e-06
1
288.15
5
2
0.4789
4
1
0.0004289
4
1
3.8e-06
1
288.15
5
2
0.56
4
1
0.0004371
4
1
3.8e-06
1
288.15
5
2
0.6402
4
1
0.0004455
4
1
3.9e-06
1
288.15
5
2
0.7201
4
1
0.0004546
4
1
4e-06
1
288.15
5
2
0.8791
4
1
0.0004765
4
1
4.1e-06
1
288.15
5
2
0.9585
4
1
0.0004902
4
1
4.2e-06
1
288.15
5
2
1
5
1
0.0004991
4
1
4.3e-06
1
298.15
5
2
0
2
1
0.0003585
4
1
3.3e-06
1
298.15
5
2
0.0542
3
1
0.0003632
4
1
3.3e-06
1
298.15
5
2
0.1599
4
1
0.000372
4
1
3.4e-06
1
298.15
5
2
0.1934
4
1
0.0003747
4
1
3.4e-06
1
298.15
5
2
0.3199
4
1
0.0003856
4
1
3.5e-06
1
298.15
5
2
0.4
4
1
0.0003926
4
1
3.5e-06
1
298.15
5
2
0.4789
4
1
0.0003996
4
1
3.6e-06
1
298.15
5
2
0.56
4
1
0.0004071
4
1
3.6e-06
1
298.15
5
2
0.651
4
1
0.0004149
4
1
3.7e-06
1
298.15
5
2
0.7201
4
1
0.0004229
4
1
3.7e-06
1
298.15
5
2
0.8791
4
1
0.0004396
4
1
3.8e-06
1
298.15
5
2
0.9585
4
1
0.0004489
4
1
3.9e-06
1
298.15
5
2
1
5
1
0.000454
4
1
4e-06
1
308.15
5
2
0
2
1
0.0003222
4
1
3e-06
1
308.15
5
2
0.0542
3
1
0.0003269
4
1
3e-06
1
308.15
5
2
0.1599
4
1
0.0003363
4
1
3.1e-06
1
308.15
5
2
0.1934
4
1
0.0003393
4
1
3.1e-06
1
308.15
5
2
0.3199
4
1
0.0003509
4
1
3.2e-06
1
308.15
5
2
0.4
4
1
0.0003584
4
1
3.3e-06
1
308.15
5
2
0.4789
4
1
0.0003659
4
1
3.3e-06
1
308.15
5
2
0.56
4
1
0.0003736
4
1
3.4e-06
1
308.15
5
2
0.651
4
1
0.0003813
4
1
3.4e-06
1
308.15
5
2
0.7201
4
1
0.0003891
4
1
3.5e-06
1
308.15
5
2
0.8791
4
1
0.0004049
4
1
3.6e-06
1
308.15
5
2
0.9585
4
1
0.0004129
4
1
3.7e-06
1
308.15
5
2
1
5
1
0.0004172
4
1
3.7e-06
11
1
1
2
1
Principal objective of the work
VVD
TRC
11/23/2019
1
Mass density, kg/m3
Vibrating tube 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
288.15
5
2
0
2
1
721.57
5
1
0.25
1
288.15
5
2
0.0542
3
1
730.55
5
1
0.25
1
288.15
5
2
0.1599
4
1
748.15
5
1
0.25
1
288.15
5
2
0.1934
4
1
753.76
5
1
0.25
1
288.15
5
2
0.3199
4
1
775.03
5
1
0.24
1
288.15
5
2
0.4
4
1
788.58
5
1
0.24
1
288.15
5
2
0.4789
4
1
802.01
5
1
0.24
1
288.15
5
2
0.56
4
1
815.87
5
1
0.24
1
288.15
5
2
0.6402
4
1
829.71
5
1
0.24
1
288.15
5
2
0.7201
4
1
843.56
5
1
0.24
1
288.15
5
2
0.8791
4
1
871.41
5
1
0.24
1
288.15
5
2
0.9585
4
1
885.46
5
1
0.24
1
288.15
5
2
1
5
1
892.92
5
1
0.23
1
298.15
5
2
0
2
1
711.08
5
1
0.25
1
298.15
5
2
0.0542
3
1
719.96
5
1
0.25
1
298.15
5
2
0.1599
4
1
737.23
5
1
0.25
1
298.15
5
2
0.1934
4
1
742.73
5
1
0.25
1
298.15
5
2
0.3199
4
1
763.65
5
1
0.25
1
298.15
5
2
0.4
4
1
777.02
5
1
0.24
1
298.15
5
2
0.4789
4
1
790.28
5
1
0.24
1
298.15
5
2
0.56
4
1
804.04
5
1
0.24
1
298.15
5
2
0.651
4
1
819.66
5
1
0.24
1
298.15
5
2
0.7201
4
1
831.66
5
1
0.24
1
298.15
5
2
0.8791
4
1
859.85
5
1
0.24
1
298.15
5
2
0.9585
4
1
874.29
5
1
0.24
1
298.15
5
2
1
5
1
882.03
5
1
0.24
1
308.15
5
2
0
2
1
700.4
5
1
0.25
1
308.15
5
2
0.0542
3
1
709.15
5
1
0.25
1
308.15
5
2
0.1599
4
1
726.3
5
1
0.25
1
308.15
5
2
0.1934
4
1
731.73
5
1
0.25
1
308.15
5
2
0.3199
4
1
752.47
5
1
0.25
1
308.15
5
2
0.4
4
1
765.73
5
1
0.25
1
308.15
5
2
0.4789
4
1
778.88
5
1
0.24
1
308.15
5
2
0.56
4
1
792.57
5
1
0.24
1
308.15
5
2
0.651
4
1
806.31
5
1
0.24
1
308.15
5
2
0.7201
4
1
820.22
5
1
0.24
1
308.15
5
2
0.8791
4
1
848.66
5
1
0.24
1
308.15
5
2
0.9585
4
1
863.3
5
1
0.24
1
308.15
5
2
1
5
1
871.01
5
1
0.24
12
1
1
2
1
Principal objective of the work
KNA
TRC
1/22/2010
1
Refractive index (Na D-line)
Standard Abbe refractometry
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
288.15
5
2
0
5
1
1.3899
5
1
0.0004
1
288.15
5
2
0.0542
3
1
1.3908
5
1
0.0004
1
288.15
5
2
0.1599
4
1
1.3927
5
1
0.0004
1
288.15
5
2
0.1934
4
1
1.3933
5
1
0.0004
1
288.15
5
2
0.3199
4
1
1.3956
5
1
0.0004
1
288.15
5
2
0.4
4
1
1.397
5
1
0.0004
1
288.15
5
2
0.4789
4
1
1.3985
5
1
0.0004
1
288.15
5
2
0.56
4
1
1.4
5
1
0.0004
1
288.15
5
2
0.6402
4
1
1.4015
5
1
0.0004
1
288.15
5
2
0.7201
4
1
1.4031
5
1
0.0004
1
288.15
5
2
0.8791
4
1
1.4062
5
1
0.0004
1
288.15
5
2
0.9585
4
1
1.4078
5
1
0.0004
1
288.15
5
2
1
5
1
1.4086
5
1
0.0004
1
298.15
5
2
0
5
1
1.3844
5
1
0.0004
1
298.15
5
2
0.0542
3
1
1.3854
5
1
0.0004
1
298.15
5
2
0.1599
4
1
1.3873
5
1
0.0004
1
298.15
5
2
0.1934
4
1
1.3879
5
1
0.0004
1
298.15
5
2
0.3199
4
1
1.3902
5
1
0.0004
1
298.15
5
2
0.4
4
1
1.3917
5
1
0.0004
1
298.15
5
2
0.4789
4
1
1.3931
5
1
0.0004
1
298.15
5
2
0.56
4
1
1.3947
5
1
0.0004
1
298.15
5
2
0.6402
4
1
1.3965
5
1
0.0004
1
298.15
5
2
0.7201
4
1
1.3978
5
1
0.0004
1
298.15
5
2
0.8791
4
1
1.4011
5
1
0.0004
1
298.15
5
2
0.9585
4
1
1.4028
5
1
0.0004
1
298.15
5
2
1
5
1
1.4037
5
1
0.0004
1
308.15
5
2
0
5
1
1.3784
5
1
0.0004
1
308.15
5
2
0.0542
3
1
1.3793
5
1
0.0004
1
308.15
5
2
0.1599
4
1
1.3812
5
1
0.0004
1
308.15
5
2
0.1934
4
1
1.3818
5
1
0.0004
1
308.15
5
2
0.3199
4
1
1.3842
5
1
0.0004
1
308.15
5
2
0.4
4
1
1.3857
5
1
0.0004
1
308.15
5
2
0.4789
4
1
1.3873
5
1
0.0004
1
308.15
5
2
0.56
4
1
1.3889
5
1
0.0004
1
308.15
5
2
0.6402
4
1
1.3906
5
1
0.0004
1
308.15
5
2
0.7201
4
1
1.3923
5
1
0.0004
1
308.15
5
2
0.8791
4
1
1.3958
5
1
0.0004
1
308.15
5
2
0.9585
4
1
1.3977
5
1
0.0004
1
308.15
5
2
1
5
1
1.3987
5
1
0.0004
13
3
1
2
1
Principal objective of the work
RDC
TRC
11/30/2010
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
Pressure, kPa
Liquid
101
3
1
Temperature, K
Liquid
2
Mole fraction
3
Liquid
1
288.15
5
2
0
2
1
0.0004991
4
1
4.3e-06
1
288.15
5
2
0.1028
4
1
0.0007142
4
1
5.9e-06
1
288.15
5
2
0.1791
4
1
0.000895
4
1
7.3e-06
1
288.15
5
2
0.2676
4
1
0.0011302
5
1
9.1e-06
1
288.15
5
2
0.3601
4
1
0.0013647
5
1
1.09e-05
1
288.15
5
2
0.45
4
1
0.0016303
5
1
1.29e-05
1
288.15
5
2
0.5402
4
1
0.0019684
5
1
1.55e-05
1
288.15
5
2
0.6295
4
1
0.0023986
5
1
1.87e-05
1
288.15
5
2
0.7058
4
1
0.0028495
5
1
2.21e-05
1
288.15
5
2
0.8097
4
1
0.0036232
5
1
2.79e-05
1
288.15
5
2
0.8903
4
1
0.0043808
5
1
3.34e-05
1
288.15
5
2
0.9629
4
1
0.0052449
5
1
3.96e-05
1
288.15
5
2
1
5
1
0.0058667
5
1
4.34e-05
1
298.15
5
2
0
2
1
0.000454
4
1
4e-06
1
298.15
5
2
0.1028
4
1
0.0005079
4
1
4.4e-06
1
298.15
5
2
0.1791
4
1
0.0005724
4
1
4.9e-06
1
298.15
5
2
0.2676
4
1
0.0006232
4
1
5.3e-06
1
298.15
5
2
0.3601
4
1
0.0007532
4
1
6.3e-06
1
298.15
5
2
0.45
4
1
0.0008859
4
1
7.3e-06
1
298.15
5
2
0.5402
4
1
0.0010636
5
1
8.7e-06
1
298.15
5
2
0.6295
4
1
0.0012881
5
1
1.04e-05
1
298.15
5
2
0.7058
4
1
0.0015484
5
1
1.24e-05
1
298.15
5
2
0.8097
4
1
0.0020076
5
1
1.59e-05
1
298.15
5
2
0.8903
4
1
0.0025174
5
1
1.97e-05
1
298.15
5
2
0.9629
4
1
0.0030519
5
1
2.37e-05
1
298.15
5
2
1
5
1
0.0034781
5
1
2.68e-05
1
308.15
5
2
0
2
1
0.0004172
4
1
3.7e-06
1
308.15
5
2
0.1028
4
1
0.0004359
4
1
3.8e-06
1
308.15
5
2
0.1791
4
1
0.0004592
4
1
4e-06
1
308.15
5
2
0.2676
4
1
0.0005449
4
1
4.6e-06
1
308.15
5
2
0.3601
4
1
0.0006428
4
1
5.3e-06
1
308.15
5
2
0.45
4
1
0.000747
4
1
6.1e-06
1
308.15
5
2
0.5402
4
1
0.0008887
4
1
7.2e-06
1
308.15
5
2
0.6295
4
1
0.0010546
5
1
8.4e-06
1
308.15
5
2
0.7058
4
1
0.0012315
5
1
9.7e-06
1
308.15
5
2
0.8097
4
1
0.0015477
5
1
1.21e-05
1
308.15
5
2
0.8903
4
1
0.0019075
5
1
1.48e-05
1
308.15
5
2
0.9629
4
1
0.0022341
5
1
1.73e-05
1
308.15
5
2
1
5
1
0.0025042
5
1
1.93e-05
14
3
1
2
1
Principal objective of the work
RDC
TRC
11/30/2010
1
Mass density, kg/m3
Vibrating tube 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
3
Liquid
1
288.15
5
2
0
2
1
892.92
5
1
0.23
1
288.15
5
2
0.1028
4
1
881.2
5
1
0.24
1
288.15
5
2
0.1791
4
1
873.29
5
1
0.24
1
288.15
5
2
0.2676
4
1
865.01
5
1
0.24
1
288.15
5
2
0.3601
4
1
857.15
5
1
0.24
1
288.15
5
2
0.45
4
1
850.2
5
1
0.24
1
288.15
5
2
0.5402
4
1
843.79
5
1
0.24
1
288.15
5
2
0.6295
4
1
837.94
5
1
0.24
1
288.15
5
2
0.7058
4
1
833.16
5
1
0.24
1
288.15
5
2
0.8097
4
1
826.96
5
1
0.24
1
288.15
5
2
0.8903
4
1
821.89
5
1
0.24
1
288.15
5
2
0.9629
4
1
816.9
5
1
0.24
1
288.15
5
2
1
5
1
814.01
5
1
0.24
1
298.15
5
2
0
2
1
882.03
5
1
0.24
1
298.15
5
2
0.1028
4
1
870.63
5
1
0.24
1
298.15
5
2
0.1791
4
1
862.93
5
1
0.24
1
298.15
5
2
0.2676
4
1
854.87
5
1
0.24
1
298.15
5
2
0.3601
4
1
847.22
5
1
0.24
1
298.15
5
2
0.45
4
1
840.46
5
1
0.24
1
298.15
5
2
0.5402
4
1
834.19
5
1
0.24
1
298.15
5
2
0.6295
4
1
828.48
5
1
0.24
1
298.15
5
2
0.7058
4
1
823.78
5
1
0.24
1
298.15
5
2
0.8097
4
1
817.62
5
1
0.24
1
298.15
5
2
0.8903
4
1
812.56
5
1
0.24
1
298.15
5
2
0.9629
4
1
807.57
5
1
0.24
1
298.15
5
2
1
5
1
804.88
5
1
0.24
1
308.15
5
2
0
2
1
871.01
5
1
0.24
1
308.15
5
2
0.1028
4
1
859.92
5
1
0.24
1
308.15
5
2
0.1791
4
1
852.42
5
1
0.24
1
308.15
5
2
0.2676
4
1
844.57
5
1
0.24
1
308.15
5
2
0.3601
4
1
837.11
5
1
0.24
1
308.15
5
2
0.45
4
1
830.51
5
1
0.24
1
308.15
5
2
0.5402
4
1
824.37
5
1
0.24
1
308.15
5
2
0.6295
4
1
818.76
5
1
0.24
1
308.15
5
2
0.7058
4
1
814.12
5
1
0.24
1
308.15
5
2
0.8097
4
1
808.01
5
1
0.24
1
308.15
5
2
0.8903
4
1
802.98
5
1
0.24
1
308.15
5
2
0.9629
4
1
798.22
5
1
0.24
1
308.15
5
2
1
5
1
795.52
5
1
0.24
15
3
1
2
1
Principal objective of the work
KNA
TRC
1/22/2010
1
Refractive index (Na D-line)
Standard Abbe refractometry
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
3
Liquid
1
288.15
5
2
0
5
1
1.4086
5
1
0.0004
1
288.15
5
2
0.1028
4
1
1.4076
5
1
0.0004
1
288.15
5
2
0.1791
4
1
1.4069
5
1
0.0004
1
288.15
5
2
0.2676
4
1
1.4065
5
1
0.0004
1
288.15
5
2
0.3601
4
1
1.4064
5
1
0.0004
1
288.15
5
2
0.45
4
1
1.4066
5
1
0.0004
1
288.15
5
2
0.5402
4
1
1.4068
5
1
0.0004
1
288.15
5
2
0.6295
4
1
1.407
5
1
0.0004
1
288.15
5
2
0.7058
4
1
1.4071
5
1
0.0004
1
288.15
5
2
0.8097
4
1
1.4071
5
1
0.0004
1
288.15
5
2
0.8903
4
1
1.4069
5
1
0.0004
1
288.15
5
2
0.9629
4
1
1.4065
5
1
0.0004
1
288.15
5
2
1
5
1
1.4062
5
1
0.0004
1
298.15
5
2
0
5
1
1.4037
5
1
0.0004
1
298.15
5
2
0.1028
4
1
1.4027
5
1
0.0004
1
298.15
5
2
0.1791
4
1
1.4022
5
1
0.0004
1
298.15
5
2
0.2676
4
1
1.4018
5
1
0.0004
1
298.15
5
2
0.3601
4
1
1.4018
5
1
0.0004
1
298.15
5
2
0.45
4
1
1.402
5
1
0.0004
1
298.15
5
2
0.5402
4
1
1.4022
5
1
0.0004
1
298.15
5
2
0.6295
4
1
1.4023
5
1
0.0004
1
298.15
5
2
0.7058
4
1
1.4024
5
1
0.0004
1
298.15
5
2
0.8097
4
1
1.4024
5
1
0.0004
1
298.15
5
2
0.8903
4
1
1.4022
5
1
0.0004
1
298.15
5
2
0.9629
4
1
1.4018
5
1
0.0004
1
298.15
5
2
1
5
1
1.4015
5
1
0.0004
1
308.15
5
2
0
5
1
1.3987
5
1
0.0004
1
308.15
5
2
0.1028
4
1
1.3979
5
1
0.0004
1
308.15
5
2
0.1791
4
1
1.3974
5
1
0.0004
1
308.15
5
2
0.2676
4
1
1.3972
5
1
0.0004
1
308.15
5
2
0.3601
4
1
1.3971
5
1
0.0004
1
308.15
5
2
0.45
4
1
1.3972
5
1
0.0004
1
308.15
5
2
0.5402
4
1
1.3974
5
1
0.0004
1
308.15
5
2
0.6295
4
1
1.3976
5
1
0.0004
1
308.15
5
2
0.7058
4
1
1.3977
5
1
0.0004
1
308.15
5
2
0.8097
4
1
1.3977
5
1
0.0004
1
308.15
5
2
0.8903
4
1
1.3975
5
1
0.0004
1
308.15
5
2
0.9629
4
1
1.3972
5
1
0.0004
1
308.15
5
2
1
5
1
1.3968
5
1
0.0004
16
3
1
1
1
Principal objective of the work
RDC
TRC
11/30/2010
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
Pressure, kPa
Liquid
101
3
1
Temperature, K
Liquid
2
Mole fraction
3
Liquid
1
288.15
5
2
0
2
1
0.0003851
4
1
3.4e-06
1
288.15
5
2
0.0733
3
1
0.0004625
4
1
4e-06
1
288.15
5
2
0.1528
4
1
0.0005521
4
1
4.7e-06
1
288.15
5
2
0.2327
4
1
0.0006938
4
1
5.8e-06
1
288.15
5
2
0.3155
4
1
0.0008513
4
1
6.9e-06
1
288.15
5
2
0.398
4
1
0.0010408
5
1
8.4e-06
1
288.15
5
2
0.4888
4
1
0.0013541
5
1
1.08e-05
1
288.15
5
2
0.5804
4
1
0.001827
5
1
1.43e-05
1
288.15
5
2
0.6697
4
1
0.0023898
5
1
1.86e-05
1
288.15
5
2
0.7769
4
1
0.0032881
5
1
2.52e-05
1
288.15
5
2
0.8741
4
1
0.004258
5
1
3.24e-05
1
288.15
5
2
0.9498
4
1
0.00517
5
1
3.9e-05
1
288.15
5
2
1
5
1
0.0058667
5
1
4.34e-05
1
298.15
5
2
0
2
1
0.0003585
4
1
3.3e-06
1
298.15
5
2
0.0733
3
1
0.0004161
4
1
3.7e-06
1
298.15
5
2
0.1528
4
1
0.0004813
4
1
4.2e-06
1
298.15
5
2
0.2327
4
1
0.0005258
4
1
4.5e-06
1
298.15
5
2
0.3155
4
1
0.0006157
4
1
5.2e-06
1
298.15
5
2
0.398
4
1
0.0007142
4
1
5.9e-06
1
298.15
5
2
0.4888
4
1
0.0008835
4
1
7.2e-06
1
298.15
5
2
0.5804
4
1
0.0011291
5
1
9e-06
1
298.15
5
2
0.6697
4
1
0.0014676
5
1
1.16e-05
1
298.15
5
2
0.7769
4
1
0.001974
5
1
1.54e-05
1
298.15
5
2
0.8741
4
1
0.0025654
5
1
1.99e-05
1
298.15
5
2
0.9498
4
1
0.0030678
5
1
2.37e-05
1
298.15
5
2
1
5
1
0.0034781
5
1
2.68e-05
1
308.15
5
2
0
2
1
0.0003222
4
1
3e-06
1
308.15
5
2
0.0733
3
1
0.0003822
4
1
3.4e-06
1
308.15
5
2
0.1528
4
1
0.0004437
4
1
3.9e-06
1
308.15
5
2
0.2327
4
1
0.000501
4
1
4.3e-06
1
308.15
5
2
0.3155
4
1
0.0005725
4
1
4.8e-06
1
308.15
5
2
0.398
4
1
0.0006756
4
1
5.6e-06
1
308.15
5
2
0.4888
4
1
0.0008338
4
1
6.7e-06
1
308.15
5
2
0.5804
4
1
0.0010295
5
1
8.2e-06
1
308.15
5
2
0.6697
4
1
0.0012835
5
1
1.01e-05
1
308.15
5
2
0.7769
4
1
0.0016645
5
1
1.29e-05
1
308.15
5
2
0.8741
4
1
0.0020295
5
1
1.56e-05
1
308.15
5
2
0.9498
4
1
0.0023045
5
1
1.77e-05
1
308.15
5
2
1
5
1
0.0025042
5
1
1.93e-05
17
3
1
1
1
Principal objective of the work
RDC
TRC
11/30/2010
1
Mass density, kg/m3
Vibrating tube 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
3
Liquid
1
288.15
5
2
0
2
1
721.57
5
1
0.25
1
288.15
5
2
0.0733
3
1
731.65
5
1
0.25
1
288.15
5
2
0.1528
4
1
742.12
5
1
0.25
1
288.15
5
2
0.2327
4
1
752
5
1
0.24
1
288.15
5
2
0.3155
4
1
761.54
5
1
0.24
1
288.15
5
2
0.398
4
1
770.38
5
1
0.24
1
288.15
5
2
0.4888
4
1
779.41
5
1
0.24
1
288.15
5
2
0.5804
4
1
787.76
5
1
0.24
1
288.15
5
2
0.6697
4
1
795.11
5
1
0.24
1
288.15
5
2
0.7769
4
1
802.69
5
1
0.24
1
288.15
5
2
0.8741
4
1
808.3
5
1
0.24
1
288.15
5
2
0.9498
4
1
811.88
5
1
0.24
1
288.15
5
2
1
5
1
814.01
5
1
0.24
1
298.15
5
2
0
2
1
711.08
5
1
0.25
1
298.15
5
2
0.0733
3
1
721.43
5
1
0.25
1
298.15
5
2
0.1528
4
1
732.03
5
1
0.25
1
298.15
5
2
0.2327
4
1
742.1
5
1
0.25
1
298.15
5
2
0.3155
4
1
751.82
5
1
0.24
1
298.15
5
2
0.398
4
1
760.84
5
1
0.24
1
298.15
5
2
0.4888
4
1
770.02
5
1
0.24
1
298.15
5
2
0.5804
4
1
778.45
5
1
0.24
1
298.15
5
2
0.6697
4
1
785.88
5
1
0.24
1
298.15
5
2
0.7769
4
1
793.82
5
1
0.24
1
298.15
5
2
0.8741
4
1
799.58
5
1
0.24
1
298.15
5
2
0.9498
4
1
803.1
5
1
0.24
1
298.15
5
2
1
5
1
804.88
5
1
0.24
1
308.15
5
2
0
2
1
700.4
5
1
0.25
1
308.15
5
2
0.0733
3
1
710.97
5
1
0.25
1
308.15
5
2
0.1528
4
1
721.79
5
1
0.25
1
308.15
5
2
0.2327
4
1
732.07
5
1
0.25
1
308.15
5
2
0.3155
4
1
741.93
5
1
0.25
1
308.15
5
2
0.398
4
1
751.09
5
1
0.24
1
308.15
5
2
0.4888
4
1
760.39
5
1
0.24
1
308.15
5
2
0.5804
4
1
768.97
5
1
0.24
1
308.15
5
2
0.6697
4
1
776.64
5
1
0.24
1
308.15
5
2
0.7769
4
1
784.6
5
1
0.24
1
308.15
5
2
0.8741
4
1
790.43
5
1
0.24
1
308.15
5
2
0.9498
4
1
793.93
5
1
0.24
1
308.15
5
2
1
5
1
795.52
5
1
0.24
18
3
1
1
1
Principal objective of the work
KNA
TRC
1/22/2010
1
Refractive index (Na D-line)
Standard Abbe refractometry
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
3
Liquid
1
288.15
5
2
0
5
1
1.3899
5
1
0.0004
1
288.15
5
2
0.0733
3
1
1.392
5
1
0.0004
1
288.15
5
2
0.1528
4
1
1.3944
5
1
0.0004
1
288.15
5
2
0.2327
4
1
1.3968
5
1
0.0004
1
288.15
5
2
0.3155
4
1
1.3989
5
1
0.0004
1
288.15
5
2
0.398
4
1
1.4009
5
1
0.0004
1
288.15
5
2
0.4888
4
1
1.4028
5
1
0.0004
1
288.15
5
2
0.5804
4
1
1.4043
5
1
0.0004
1
288.15
5
2
0.6697
4
1
1.4053
5
1
0.0004
1
288.15
5
2
0.7769
4
1
1.4058
5
1
0.0004
1
288.15
5
2
0.8741
4
1
1.406
5
1
0.0004
1
288.15
5
2
0.9498
4
1
1.4061
5
1
0.0004
1
288.15
5
2
1
5
1
1.4062
5
1
0.0004
1
298.15
5
2
0
5
1
1.3844
5
1
0.0004
1
298.15
5
2
0.0733
3
1
1.3868
5
1
0.0004
1
298.15
5
2
0.1528
4
1
1.3893
5
1
0.0004
1
298.15
5
2
0.2327
4
1
1.3917
5
1
0.0004
1
298.15
5
2
0.3155
4
1
1.394
5
1
0.0004
1
298.15
5
2
0.398
4
1
1.3961
5
1
0.0004
1
298.15
5
2
0.4888
4
1
1.398
5
1
0.0004
1
298.15
5
2
0.5804
4
1
1.3996
5
1
0.0004
1
298.15
5
2
0.6697
4
1
1.4005
5
1
0.0004
1
298.15
5
2
0.7769
4
1
1.4012
5
1
0.0004
1
298.15
5
2
0.8741
4
1
1.4013
5
1
0.0004
1
298.15
5
2
0.9498
4
1
1.4014
5
1
0.0004
1
298.15
5
2
1
5
1
1.4015
5
1
0.0004
1
308.15
5
2
0
5
1
1.3784
5
1
0.0004
1
308.15
5
2
0.0733
3
1
1.3809
5
1
0.0004
1
308.15
5
2
0.1528
4
1
1.3835
5
1
0.0004
1
308.15
5
2
0.2327
4
1
1.386
5
1
0.0004
1
308.15
5
2
0.3155
4
1
1.3884
5
1
0.0004
1
308.15
5
2
0.398
4
1
1.3906
5
1
0.0004
1
308.15
5
2
0.4888
4
1
1.3926
5
1
0.0004
1
308.15
5
2
0.5804
4
1
1.3944
5
1
0.0004
1
308.15
5
2
0.6697
4
1
1.3954
5
1
0.0004
1
308.15
5
2
0.7769
4
1
1.3962
5
1
0.0004
1
308.15
5
2
0.8741
4
1
1.3964
5
1
0.0004
1
308.15
5
2
0.9498
4
1
1.3966
5
1
0.0004
1
308.15
5
2
1
5
1
1.3968
5
1
0.0004
19
3
1
1
1
2
1
Principal objective of the work
RDC
TRC
11/30/2010
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
Pressure, kPa
Liquid
101
3
2
Temperature, K
Liquid
298.15
5
1
Mole fraction
3
Liquid
2
Mole fraction
2
Liquid
1
0.0913
3
2
0.1819
4
1
0.0004805
4
1
4.1e-06
1
0.1003
4
2
0.5994
4
1
0.0005218
4
1
4.5e-06
1
0.1004
4
2
0.5001
4
1
0.0005099
4
1
4.4e-06
1
0.1008
4
2
0.4001
4
1
0.0005411
4
1
4.6e-06
1
0.1022
4
2
0.6982
4
1
0.0005321
4
1
4.5e-06
1
0.1033
4
2
0.7953
4
1
0.0005439
4
1
4.6e-06
1
0.1235
4
2
0.1254
4
1
0.0004804
4
1
4.2e-06
1
0.1262
4
2
0.1233
4
1
0.0004757
4
1
4.1e-06
1
0.1676
4
2
0.2572
4
1
0.0005521
4
1
4.7e-06
1
0.1984
4
2
0.5947
4
1
0.0005862
4
1
4.9e-06
1
0.1995
4
2
0.6991
4
1
0.0005849
4
1
4.9e-06
1
0.1999
4
2
0.1985
4
1
0.0005462
4
1
4.6e-06
1
0.2
4
2
0.3006
4
1
0.0005567
4
1
4.7e-06
1
0.2003
4
2
0.3996
4
1
0.000565
4
1
4.8e-06
1
0.2004
4
2
0.4994
4
1
0.000576
4
1
4.8e-06
1
0.2991
4
2
0.0996
3
1
0.0006871
4
1
5.7e-06
1
0.2991
4
2
0.5996
4
1
0.0007152
4
1
5.9e-06
1
0.2998
4
2
0.2998
4
1
0.0007049
4
1
5.8e-06
1
0.3005
4
2
0.2003
4
1
0.0006968
4
1
5.7e-06
1
0.3007
4
2
0.4002
4
1
0.0007129
4
1
5.9e-06
1
0.3007
4
2
0.4992
4
1
0.0007153
4
1
5.9e-06
1
0.3994
4
2
0.3005
4
1
0.0008709
4
1
7e-06
1
0.3996
4
2
0.2003
4
1
0.0008662
4
1
7e-06
1
0.4001
4
2
0.1001
4
1
0.0008946
4
1
7.2e-06
1
0.4006
4
2
0.3992
4
1
0.0008692
4
1
7e-06
1
0.4062
4
2
0.4953
4
1
0.0008711
4
1
7e-06
1
0.4692
4
2
0.1559
4
1
0.0010205
5
1
8.1e-06
1
0.4998
4
2
0.2002
4
1
0.0010634
5
1
8.4e-06
1
0.4998
4
2
0.2998
4
1
0.0010578
5
1
8.4e-06
1
0.5002
4
2
0.3992
4
1
0.0010427
5
1
8.3e-06
1
0.5911
4
2
0.1024
4
1
0.0013313
5
1
1.04e-05
1
0.5969
4
2
0.3037
4
1
0.0012622
5
1
9.9e-06
1
0.5993
4
2
0.1997
4
1
0.0013576
5
1
1.06e-05
1
0.6705
4
2
0.2344
4
1
0.0015478
5
1
1.2e-05
1
0.6968
4
2
0.1008
4
1
0.0017282
5
1
1.33e-05
1
0.7689
4
2
0.1341
4
1
0.0020403
5
1
1.56e-05
20
3
1
1
1
2
1
Principal objective of the work
RDC
TRC
11/30/2010
1
Mass density, kg/m3
Vibrating tube method
Liquid
Direct value, X
1
Data file compiler
Propagation of evaluated standard uncertainties
95
Liquid
1
Pressure, kPa
Liquid
101
3
2
Temperature, K
Liquid
298.15
5
1
Mole fraction
3
Liquid
2
Mole fraction
2
Liquid
1
0.0913
3
2
0.1819
4
1
756.93
5
1
0.24
1
0.1003
4
2
0.5994
4
1
822.2
5
1
0.24
1
0.1004
4
2
0.5001
4
1
806.09
5
1
0.24
1
0.1008
4
2
0.4001
4
1
789.83
5
1
0.24
1
0.1022
4
2
0.6982
4
1
838.37
5
1
0.24
1
0.1033
4
2
0.7953
4
1
854.19
5
1
0.24
1
0.1235
4
2
0.1254
4
1
751.39
5
1
0.24
1
0.1262
4
2
0.1233
4
1
751.09
5
1
0.25
1
0.1676
4
2
0.2572
4
1
776.61
5
1
0.24
1
0.1984
4
2
0.5947
4
1
830.2
5
1
0.24
1
0.1995
4
2
0.6991
4
1
845.91
5
1
0.24
1
0.1999
4
2
0.1985
4
1
768.97
5
1
0.24
1
0.2
4
2
0.3006
4
1
786.09
5
1
0.24
1
0.2003
4
2
0.3996
4
1
800.18
5
1
0.24
1
0.2004
4
2
0.4994
4
1
815.77
5
1
0.24
1
0.2991
4
2
0.0996
3
1
764.91
5
1
0.24
1
0.2991
4
2
0.5996
4
1
838.18
5
1
0.24
1
0.2998
4
2
0.2998
4
1
794.78
5
1
0.24
1
0.3005
4
2
0.2003
4
1
780.12
5
1
0.24
1
0.3007
4
2
0.4002
4
1
809.6
5
1
0.24
1
0.3007
4
2
0.4992
4
1
824.09
5
1
0.24
1
0.3994
4
2
0.3005
4
1
804.69
5
1
0.24
1
0.3996
4
2
0.2003
4
1
789.67
5
1
0.24
1
0.4001
4
2
0.1001
4
1
775.48
5
1
0.24
1
0.4006
4
2
0.3992
4
1
817.4
5
1
0.24
1
0.4062
4
2
0.4953
4
1
830.73
5
1
0.24
1
0.4692
4
2
0.1559
4
1
789.72
5
1
0.24
1
0.4998
4
2
0.2002
4
1
798.28
5
1
0.24
1
0.4998
4
2
0.2998
4
1
811.98
5
1
0.24
1
0.5002
4
2
0.3992
4
1
824.28
5
1
0.24
1
0.5911
4
2
0.1024
4
1
793.1
5
1
0.24
1
0.5969
4
2
0.3037
4
1
818.48
5
1
0.24
1
0.5993
4
2
0.1997
4
1
805.76
5
1
0.24
1
0.6705
4
2
0.2344
4
1
814.16
5
1
0.24
1
0.6968
4
2
0.1008
4
1
800.36
5
1
0.24
1
0.7689
4
2
0.1341
4
1
808.86
5
1
0.24
21
3
1
1
1
2
1
Principal objective of the work
KNA
TRC
1/22/2010
1
Refractive index (Na D-line)
Standard Abbe refractometry
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
2
Mole fraction
2
Liquid
1
0.7689
4
2
0.1341
4
1
1.4022
5
1
0.0004
1
0.6705
4
2
0.2344
4
1
1.402
4
1
0.001
1
0.5969
4
2
0.3037
4
1
1.4018
5
1
0.0004
1
0.5002
4
2
0.3992
4
1
1.4015
5
1
0.0004
1
0.4062
4
2
0.4953
4
1
1.4012
5
1
0.0004
1
0.2991
4
2
0.5996
4
1
1.4012
5
1
0.0004
1
0.1995
4
2
0.6991
4
1
1.4009
5
1
0.0004
1
0.1033
4
2
0.7953
4
1
1.4011
5
1
0.0004
1
0.6968
4
2
0.1008
4
1
1.4014
5
1
0.0004
1
0.5993
4
2
0.1997
4
1
1.4011
5
1
0.0004
1
0.4998
4
2
0.2998
4
1
1.4009
5
1
0.0004
1
0.4006
4
2
0.3992
4
1
1.4005
5
1
0.0004
1
0.3007
4
2
0.4992
4
1
1.3997
5
1
0.0004
1
0.1984
4
2
0.5947
4
1
1.3998
5
1
0.0004
1
0.1022
4
2
0.6982
4
1
1.3995
5
1
0.0004
1
0.5911
4
2
0.1024
4
1
1.4002
5
1
0.0004
1
0.4998
4
2
0.2002
4
1
1.4001
5
1
0.0004
1
0.3994
4
2
0.3005
4
1
1.3996
5
1
0.0004
1
0.3007
4
2
0.4002
4
1
1.3991
5
1
0.0004
1
0.2004
4
2
0.4994
4
1
1.3983
5
1
0.0004
1
0.1003
4
2
0.5994
4
1
1.3983
5
1
0.0004
1
0.4692
4
2
0.1559
4
1
1.3994
5
1
0.0004
1
0.3996
4
2
0.2003
4
1
1.3985
5
1
0.0004
1
0.2998
4
2
0.2998
4
1
1.3979
5
1
0.0004
1
0.2003
4
2
0.3996
4
1
1.3971
5
1
0.0004
1
0.1004
4
2
0.5001
4
1
1.3966
5
1
0.0004
1
0.4001
4
2
0.1001
4
1
1.3973
5
1
0.0004
1
0.3005
4
2
0.2003
4
1
1.3969
5
1
0.0004
1
0.2
4
2
0.3006
4
1
1.3956
5
1
0.0004
1
0.1008
4
2
0.4001
4
1
1.3954
5
1
0.0004
1
0.2991
4
2
0.0996
3
1
1.3974
5
1
0.0004
1
0.1999
4
2
0.1985
4
1
1.3941
5
1
0.0004
1
0.1262
4
2
0.1233
4
1
1.3932
5
1
0.0004
1
0.1676
4
2
0.2572
4
1
1.3925
5
1
0.0004
1
0.1235
4
2
0.1254
4
1
1.3924
5
1
0.0004
1
0.0913
3
2
0.1819
4
1
1.3895
5
1
0.0004