2
0
2010
alm
ilo
0
journal
Original
Almasi, M.[Mohammad]
Iloukhani, H.[Hossein]
J. Chem. Eng. Data
2010
2020-09-29
Densities, Viscosities, and Refractive Indices of Binary Mixtures of Acetophenone and 2-Alkanols
Densities, viscosities, and refractive indices of mixing of acetophenone with 2-alkanols, namely, 2-propanol, 2-butanol, 2-pentanol, 2-hexanol, and 2-heptanol, have been measured as a function of composition range at T = 298.15 K and ambient pressure. Excess molar volumes VmE, viscosity deviations ??, and refractive index deviations ?nD were calculated and correlated by the Redlich-Kister type function to derive the coefficients and estimate the standard error. For mixtures of acetophenone with used 2-alkanols, VmE is positive, except with 2-propanol over the entire range of the composition. ?? is negative, and ?nD is positive over the entire range of mole fraction. The effect of chain length of the 2-alkanols on the excess molar volumes, viscosity, and refractive index deviations of its mixtures with acetophenone is discussed. The experimental results have been used to test the applicability of the Prigogine-Flory-Patterson (PFP) theory. The agreement between theoretical and experimental results is satisfactory for acetophenone + 2-alkanol systems.
10.1021/je9005823
3
55
1416-1420
1
InChI=1S/C8H8O/c1-7(9)8-5-3-2-4-6-8/h2-6H,1H3
KWOLFJPFCHCOCG-UHFFFAOYSA-N
acetophenone
1-phenyl-1-ethanone
1-phenylethanone
methyl phenyl ketone
phenyl methyl ketone
C8H8O
1
Commercial source
1
99
2
Stated by supplier
2
InChI=1S/C3H8O/c1-3(2)4/h3-4H,1-2H3
KFZMGEQAYNKOFK-UHFFFAOYSA-N
propan-2-ol
2-propanol
isopropanol
isopropyl alcohol
sec-propyl alcohol
C3H8O
1
Commercial source
1
99
2
Stated by supplier
3
InChI=1S/C4H10O/c1-3-4(2)5/h4-5H,3H2,1-2H3
BTANRVKWQNVYAZ-UHFFFAOYSA-N
butan-2-ol
(RS)-2-butanol
2-butanol
DL-2-butanol
dl-2-butanol
dl-sec-butyl alcohol
sec-butanol
sec-butyl alcohol
C4H10O
1
Commercial source
1
99
2
Stated by supplier
4
InChI=1S/C5H12O/c1-3-4-5(2)6/h5-6H,3-4H2,1-2H3
JYVLIDXNZAXMDK-UHFFFAOYSA-N
pentan-2-ol
(R,S)-2-pentanol
2-pentanol
dl-2-pentanol
C5H12O
1
Commercial source
1
99
2
Stated by supplier
5
InChI=1S/C6H14O/c1-3-4-5-6(2)7/h6-7H,3-5H2,1-2H3
QNVRIHYSUZMSGM-UHFFFAOYSA-N
2-hexanol
2-hydroxyhexane
butylmethylcarbinol
methyl butyl carbinol
C6H14O
1
Commercial source
1
99
2
Stated by supplier
6
InChI=1S/C7H16O/c1-3-4-5-6-7(2)8/h7-8H,3-6H2,1-2H3
CETWDUZRCINIHU-UHFFFAOYSA-N
2-heptanol
2-hydroxyheptane
amylmethylcarbinol
methyl amyl carbinol
methylpentylcarbinol
C7H16O
1
Commercial source
1
99
2
Stated by supplier
1
1
1
Principal objective of the work
RDC
TRC
3/17/2010
1
Refractive index (Na D-line)
ABBE::UFactor:2
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
101.325
6
1
1.5308
5
1
0.0007
2
1
1
Principal objective of the work
RDC
TRC
3/17/2010
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
Temperature, K
Liquid
2
Pressure, kPa
Liquid
1
298.15
5
2
101
3
1
0.001678
5
1
1.29e-05
3
1
1
Principal objective of the work
RDC
TRC
3/17/2010
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
1023.3
6
1
0.37
4
2
1
Principal objective of the work
RDC
TRC
3/17/2010
1
Refractive index (Na D-line)
ABBE::UFactor:2
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
101.325
6
1
1.3745
5
1
0.0007
5
2
1
Principal objective of the work
RDC
TRC
3/17/2010
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
Temperature, K
Liquid
2
Pressure, kPa
Liquid
1
298.15
5
2
101
3
1
0.0020439
5
1
1.56e-05
6
2
1
Principal objective of the work
RDC
TRC
3/17/2010
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
780.98
5
1
0.59
7
3
1
Principal objective of the work
RDC
TRC
3/17/2010
1
Refractive index (Na D-line)
ABBE::UFactor:2
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
101.325
6
1
1.3946
5
1
0.0007
8
3
1
Principal objective of the work
RDC
TRC
3/17/2010
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
Temperature, K
Liquid
2
Pressure, kPa
Liquid
1
298.15
5
2
101
3
1
0.0031318
5
1
2.35e-05
9
3
1
Principal objective of the work
RDC
TRC
3/17/2010
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
802.56
5
1
0.56
10
4
1
Principal objective of the work
RDC
TRC
3/17/2010
1
Refractive index (Na D-line)
ABBE::UFactor:2
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
101.325
6
1
1.4045
5
1
0.0007
11
4
1
Principal objective of the work
RDC
TRC
3/17/2010
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
Temperature, K
Liquid
2
Pressure, kPa
Liquid
1
298.15
5
2
101
3
1
0.0034785
5
1
2.6e-05
12
4
1
Principal objective of the work
RDC
TRC
3/17/2010
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
805.24
5
1
0.56
13
5
1
Principal objective of the work
RDC
TRC
3/17/2010
1
Refractive index (Na D-line)
ABBE::UFactor:2
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
101.325
6
1
1.4116
5
1
0.0007
14
5
1
Principal objective of the work
RDC
TRC
3/17/2010
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
Temperature, K
Liquid
2
Pressure, kPa
Liquid
1
298.15
5
2
101
3
1
0.0041
4
1
3.1e-05
15
5
1
Principal objective of the work
RDC
TRC
3/17/2010
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
810.14
5
1
0.55
16
6
1
Principal objective of the work
RDC
TRC
3/17/2010
1
Refractive index (Na D-line)
ABBE::UFactor:2
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
101.325
6
1
1.4188
5
1
0.0007
17
6
1
Principal objective of the work
RDC
TRC
3/17/2010
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
Temperature, K
Liquid
2
Pressure, kPa
Liquid
1
298.15
5
2
101
3
1
0.0053305
5
1
3.91e-05
18
6
1
Principal objective of the work
RDC
TRC
3/17/2010
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
813.33
5
1
0.55
19
2
1
1
1
Principal objective of the work
GPC
TRC
3/17/2010
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
Temperature, K
Liquid
298.15
5
2
Pressure, kPa
Liquid
101
3
1
Mole fraction
1
Liquid
1
0
2
1
0.0020439
5
1
1.56e-05
1
0.0892
3
1
0.0016779
5
1
1.29e-05
1
0.1658
4
1
0.0015027
5
1
1.16e-05
1
0.2517
4
1
0.0013986
5
1
1.09e-05
1
0.3432
4
1
0.0013538
5
1
1.05e-05
1
0.4297
4
1
0.0013523
5
1
1.05e-05
1
0.5345
4
1
0.0013667
5
1
1.06e-05
1
0.6466
4
1
0.0014213
5
1
1.1e-05
1
0.7561
4
1
0.0014844
5
1
1.15e-05
1
0.8635
4
1
0.0015558
5
1
1.2e-05
1
0.9568
4
1
0.0016263
5
1
1.25e-05
1
1
5
1
0.001678
5
1
1.29e-05
20
2
1
1
1
Principal objective of the work
GPC
TRC
3/17/2010
1
Refractive index (Na D-line)
ABBE:UFactor:2
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
1.3745
5
1
0.0007
1
0.0892
3
1
1.3971
5
1
0.0007
1
0.1658
4
1
1.4181
5
1
0.0007
1
0.2517
4
1
1.4393
5
1
0.0007
1
0.3432
4
1
1.4601
5
1
0.0007
1
0.4297
4
1
1.4775
5
1
0.0007
1
0.5345
4
1
1.4953
5
1
0.0007
1
0.6466
4
1
1.5099
5
1
0.0007
1
0.7561
4
1
1.5195
5
1
0.0007
1
0.8635
4
1
1.5255
5
1
0.0007
1
0.9568
4
1
1.5276
5
1
0.0007
1
1
5
1
1.5308
5
1
0.0007
21
2
1
1
1
Principal objective of the work
GPC
TRC
3/17/2010
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
780.98
5
1
0.59
1
0.0892
3
1
813.69
5
1
0.55
1
0.1658
4
1
839.2
5
1
0.52
1
0.2517
4
1
865.44
5
1
0.49
1
0.3432
4
1
890.91
5
1
0.46
1
0.4297
4
1
913.04
5
1
0.43
1
0.5345
4
1
937.56
5
1
0.4
1
0.6466
4
1
961.31
5
1
0.37
1
0.7561
4
1
982.35
5
1
0.35
1
0.8635
4
1
1001.26
6
1
0.33
1
0.9568
4
1
1016.5
6
1
0.36
1
1
5
1
1023.3
6
1
0.37
22
3
1
1
1
Principal objective of the work
GPC
TRC
3/17/2010
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
Temperature, K
Liquid
298.15
5
2
Pressure, kPa
Liquid
101
3
1
Mole fraction
1
Liquid
1
0
2
1
0.0031318
5
1
2.35e-05
1
0.1031
4
1
0.0023449
5
1
1.78e-05
1
0.1635
4
1
0.0020092
5
1
1.53e-05
1
0.2517
4
1
0.0017049
5
1
1.31e-05
1
0.3422
4
1
0.0015443
5
1
1.19e-05
1
0.4361
4
1
0.0014614
5
1
1.13e-05
1
0.533
4
1
0.0014601
5
1
1.13e-05
1
0.6461
4
1
0.0015063
5
1
1.17e-05
1
0.7517
4
1
0.0015616
5
1
1.21e-05
1
0.8675
4
1
0.0016167
5
1
1.25e-05
1
0.9462
4
1
0.0016497
5
1
1.27e-05
1
1
5
1
0.001678
5
1
1.29e-05
23
3
1
1
1
Principal objective of the work
GPC
TRC
3/17/2010
1
Refractive index (Na D-line)
ABBE:UFactor:2
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
1.3946
5
1
0.0007
1
0.1031
4
1
1.4255
5
1
0.0007
1
0.1635
4
1
1.4443
5
1
0.0007
1
0.2517
4
1
1.4669
5
1
0.0007
1
0.3422
4
1
1.4877
5
1
0.0007
1
0.4361
4
1
1.5044
5
1
0.0007
1
0.533
4
1
1.5189
5
1
0.0007
1
0.6461
4
1
1.5314
5
1
0.0007
1
0.7517
4
1
1.5367
5
1
0.0007
1
0.8675
4
1
1.5351
5
1
0.0007
1
0.9462
4
1
1.5336
5
1
0.0007
1
1
5
1
1.5308
5
1
0.0007
24
3
1
1
1
Principal objective of the work
GPC
TRC
3/17/2010
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
802.56
5
1
0.56
1
0.1031
4
1
830.43
5
1
0.53
1
0.1635
4
1
846.12
5
1
0.51
1
0.2517
4
1
868.13
5
1
0.48
1
0.3422
4
1
889.8
5
1
0.46
1
0.4361
4
1
911.31
5
1
0.43
1
0.533
4
1
932.56
5
1
0.4
1
0.6461
4
1
956.27
5
1
0.38
1
0.7517
4
1
977.34
5
1
0.35
1
0.8675
4
1
999.34
5
1
0.33
1
0.9462
4
1
1013.72
6
1
0.35
1
1
5
1
1023.3
6
1
0.37
25
1
1
4
1
Principal objective of the work
GPC
TRC
3/17/2010
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
Temperature, K
Liquid
298.15
5
2
Pressure, kPa
Liquid
101
3
1
Mole fraction
1
Liquid
1
0
2
1
0.0034785
5
1
2.6e-05
1
0.0917
3
1
0.0027668
5
1
2.09e-05
1
0.1629
4
1
0.002314
5
1
1.76e-05
1
0.2502
4
1
0.0018755
5
1
1.44e-05
1
0.3416
4
1
0.0016264
5
1
1.25e-05
1
0.4371
4
1
0.0015018
5
1
1.16e-05
1
0.5387
4
1
0.0014892
5
1
1.15e-05
1
0.6442
4
1
0.0015344
5
1
1.19e-05
1
0.7547
4
1
0.0016047
5
1
1.24e-05
1
0.8716
4
1
0.0016583
5
1
1.28e-05
1
0.949
4
1
0.001669
5
1
1.28e-05
1
1
5
1
0.001678
5
1
1.29e-05
26
1
1
4
1
Principal objective of the work
GPC
TRC
3/17/2010
1
Refractive index (Na D-line)
ABBE:UFactor:2
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
1.4045
5
1
0.0007
1
0.0917
3
1
1.4627
5
1
0.0007
1
0.1629
4
1
1.4972
5
1
0.0007
1
0.2502
4
1
1.5257
5
1
0.0007
1
0.3416
4
1
1.5487
5
1
0.0007
1
0.4371
4
1
1.5642
5
1
0.0007
1
0.5387
4
1
1.5695
5
1
0.0007
1
0.6442
4
1
1.5674
5
1
0.0007
1
0.7547
4
1
1.5605
5
1
0.0007
1
0.8716
4
1
1.547
5
1
0.0007
1
0.949
4
1
1.539
5
1
0.0007
1
1
5
1
1.5308
5
1
0.0007
27
1
1
4
1
Principal objective of the work
GPC
TRC
3/17/2010
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
805.24
5
1
0.56
1
0.0917
3
1
826.19
5
1
0.53
1
0.1629
4
1
842.36
5
1
0.51
1
0.2502
4
1
862.04
5
1
0.49
1
0.3416
4
1
882.41
5
1
0.46
1
0.4371
4
1
903.49
5
1
0.44
1
0.5387
4
1
925.71
5
1
0.41
1
0.6442
4
1
948.51
5
1
0.39
1
0.7547
4
1
972.08
5
1
0.36
1
0.8716
4
1
996.7
5
1
0.33
1
0.949
4
1
1012.77
6
1
0.35
1
1
5
1
1023.3
6
1
0.37
28
1
1
6
1
Principal objective of the work
GPC
TRC
3/17/2010
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
Temperature, K
Liquid
298.15
5
2
Pressure, kPa
Liquid
101
3
1
Mole fraction
1
Liquid
1
0
2
1
0.0053305
5
1
3.91e-05
1
0.0913
3
1
0.0042819
5
1
3.19e-05
1
0.1631
4
1
0.0035719
5
1
2.68e-05
1
0.2637
4
1
0.0027634
5
1
2.09e-05
1
0.3425
4
1
0.0022961
5
1
1.74e-05
1
0.4374
4
1
0.0019084
5
1
1.46e-05
1
0.5387
4
1
0.0016617
5
1
1.28e-05
1
0.6446
4
1
0.0015504
5
1
1.2e-05
1
0.7571
4
1
0.0015484
5
1
1.2e-05
1
0.8733
4
1
0.0016058
5
1
1.24e-05
1
0.9542
4
1
0.0016512
5
1
1.27e-05
1
1
5
1
0.001678
5
1
1.29e-05
29
1
1
6
1
Principal objective of the work
GPC
TRC
3/17/2010
1
Refractive index (Na D-line)
ABBE:UFactor:2
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
1.4188
5
1
0.0007
1
0.0913
3
1
1.4489
5
1
0.0007
1
0.1631
4
1
1.4748
5
1
0.0007
1
0.2637
4
1
1.5079
5
1
0.0007
1
0.3425
4
1
1.5298
5
1
0.0007
1
0.4374
4
1
1.5535
5
1
0.0007
1
0.5387
4
1
1.5708
5
1
0.0007
1
0.6446
4
1
1.582
5
1
0.0007
1
0.7571
4
1
1.5816
5
1
0.0007
1
0.8733
4
1
1.5669
5
1
0.0007
1
0.9542
4
1
1.5486
5
1
0.0007
1
1
5
1
1.5308
5
1
0.0007
30
1
1
6
1
Principal objective of the work
GPC
TRC
3/17/2010
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
813.33
5
1
0.55
1
0.0913
3
1
829.12
5
1
0.53
1
0.1631
4
1
841.87
5
1
0.51
1
0.2637
4
1
860.39
5
1
0.49
1
0.3425
4
1
875.43
5
1
0.47
1
0.4374
4
1
894.2
5
1
0.45
1
0.5387
4
1
915.07
5
1
0.42
1
0.6446
4
1
937.92
5
1
0.4
1
0.7571
4
1
963.35
5
1
0.37
1
0.8733
4
1
991.14
5
1
0.34
1
0.9542
4
1
1011.38
6
1
0.35
1
1
5
1
1023.3
6
1
0.37
31
1
1
5
1
Principal objective of the work
GPC
TRC
3/17/2010
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
Temperature, K
Liquid
298.15
5
2
Pressure, kPa
Liquid
101
3
1
Mole fraction
1
Liquid
1
0
2
1
0.0041
4
1
3.1e-05
1
0.0902
3
1
0.0031929
5
1
2.4e-05
1
0.1678
4
1
0.0026581
5
1
2.01e-05
1
0.2536
4
1
0.0021599
5
1
1.65e-05
1
0.34
4
1
0.0018024
5
1
1.38e-05
1
0.4382
4
1
0.0015062
5
1
1.17e-05
1
0.5395
4
1
0.0013435
5
1
1.05e-05
1
0.6451
4
1
0.001273
5
1
9.9e-06
1
0.75
4
1
0.001313
5
1
1.02e-05
1
0.8628
4
1
0.0013995
5
1
1.09e-05
1
0.9511
4
1
0.0015564
5
1
1.2e-05
1
1
5
1
0.001678
5
1
1.29e-05
32
1
1
5
1
Principal objective of the work
GPC
TRC
3/17/2010
1
Refractive index (Na D-line)
ABBE:UFactor:2
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
1.4116
5
1
0.0007
1
0.0902
3
1
1.4485
5
1
0.0007
1
0.1678
4
1
1.4782
5
1
0.0007
1
0.2536
4
1
1.5037
5
1
0.0007
1
0.34
4
1
1.5247
5
1
0.0007
1
0.4382
4
1
1.5425
5
1
0.0007
1
0.5395
4
1
1.5556
5
1
0.0007
1
0.6451
4
1
1.5615
5
1
0.0007
1
0.75
4
1
1.5593
5
1
0.0007
1
0.8628
4
1
1.5505
5
1
0.0007
1
0.9511
4
1
1.5394
5
1
0.0007
1
1
5
1
1.5308
5
1
0.0007
33
1
1
5
1
Principal objective of the work
GPC
TRC
3/17/2010
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
810.14
5
1
0.55
1
0.0902
3
1
827.84
5
1
0.53
1
0.1678
4
1
843.27
5
1
0.51
1
0.2536
4
1
860.63
5
1
0.49
1
0.34
4
1
878.39
5
1
0.47
1
0.4382
4
1
898.86
5
1
0.44
1
0.5395
4
1
920.38
5
1
0.42
1
0.6451
4
1
943.23
5
1
0.39
1
0.75
4
1
966.34
5
1
0.36
1
0.8628
4
1
991.72
5
1
0.34
1
0.9511
4
1
1011.93
6
1
0.35
1
1
5
1
1023.3
6
1
0.37