2
0
2009
lom
baw
0
journal
Original
Lomte, S. B.[Shama B.]
Bawa, M. J.[Madhuri J.]
Lande, M. K. K.[Machhindra K.]
Arbad, B. R. R.[Balasaheb R.]
J. Chem. Eng. Data
2009
2020-09-29
Densities and Viscosities of Binary Liquid Mixtures of 2-Butanone with Branched Alcohols at (293.15 to 313.15) K
Densities and viscosities of the binary mixtures of 2-butanone with 2-propanol, 2-methyl-1-propanol, 2-butanol, and 2-methyl-2-butanol were measured over the entire mole fractions at (293.15, 298.15, 303.15, 308.15, and 313.15) K. Using the experimental values of densities, excess molar volumes VE were calculated. The results were discussed in terms of molecular interactions.
10.1021/je800571y
1
54
127-130
1
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
Fractional distillation
Molecular sieve treatment
Fractional distillation
Molecular sieve treatment
2
99
2
Estimated by the compiler
2
InChI=1S/C4H10O/c1-4(2)3-5/h4-5H,3H2,1-2H3
ZXEKIIBDNHEJCQ-UHFFFAOYSA-N
2-methyl-1-propanol
2-methylpropan-1-ol
isobutanol
isobutyl alcohol
C4H10O
1
Commercial source
1
Fractional distillation
Molecular sieve treatment
Fractional distillation
Molecular sieve treatment
2
99
2
Estimated by the compiler
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
Fractional distillation
Molecular sieve treatment
Fractional distillation
Molecular sieve treatment
2
99
2
Estimated by the compiler
4
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
Fractional distillation
Molecular sieve treatment
Fractional distillation
Molecular sieve treatment
2
99
2
Estimated by the compiler
5
InChI=1S/C4H8O/c1-3-4(2)5/h3H2,1-2H3
ZWEHNKRNPOVVGH-UHFFFAOYSA-N
butanone
2-butanone
butan-2-one
ethyl methyl ketone
methyl ethyl ketone
C4H8O
1
Commercial source
1
98
2
Stated by supplier
2
Fractional distillation
3
99
2
Estimated by the compiler
1
1
1
Principal objective of the work
RDC
TRC
2/24/2009
1
Viscosity, Pa*s
CAPTUB::UFactor:32
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
293.15
5
1
0.0022256
5
1
0.0004062
1
298.15
5
1
0.0019102
5
1
0.0003527
1
303.15
5
1
0.001737
5
1
0.0003233
1
308.15
5
1
0.0015242
5
1
0.0002871
1
313.15
5
1
0.0013472
5
1
0.0002568
2
1
1
Principal objective of the work
RDC
TRC
2/24/2009
1
Mass density, kg/m3
PYCNOM::UFactor:4
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
293.15
5
1
785.45
5
1
0.99
1
298.15
5
1
781.26
5
1
0.98
1
303.15
5
1
777.97
5
1
1.06
1
308.15
5
1
772.59
5
1
1.13
1
313.15
5
1
768.32
5
1
1.12
3
2
1
Principal objective of the work
RDC
TRC
2/24/2009
1
Viscosity, Pa*s
CAPTUB::UFactor:32
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
293.15
5
1
0.0040366
5
1
0.0007093
1
298.15
5
1
0.0033297
5
1
0.0005918
1
303.15
5
1
0.0028752
5
1
0.0005157
1
308.15
5
1
0.0024207
5
1
0.0004392
1
313.15
5
1
0.0019666
5
1
0.0003623
4
2
1
Principal objective of the work
RDC
TRC
2/24/2009
1
Mass density, kg/m3
PYCNOM::UFactor:4
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
293.15
5
1
801.68
5
1
0.98
1
298.15
5
1
797.8
5
1
1
1
303.15
5
1
794.16
5
1
1.05
1
308.15
5
1
790.06
5
1
1.07
1
313.15
5
1
786.7
5
1
1.08
5
3
1
Principal objective of the work
RDC
TRC
2/24/2009
1
Viscosity, Pa*s
CAPTUB::UFactor:32
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
293.15
5
1
0.0036316
5
1
0.0006421
1
298.15
5
1
0.0029975
5
1
0.0005362
1
303.15
5
1
0.0024978
5
1
0.0004522
1
308.15
5
1
0.0020542
5
1
0.0003772
1
313.15
5
1
0.0017989
5
1
0.0003338
6
3
1
Principal objective of the work
RDC
TRC
2/24/2009
1
Mass density, kg/m3
PYCNOM::UFactor:4
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
293.15
5
1
806.48
5
1
1.01
1
298.15
5
1
802.35
5
1
1.01
1
303.15
5
1
798.96
5
1
1.07
1
308.15
5
1
794.18
5
1
1.13
1
313.15
5
1
790.07
5
1
1.14
7
4
1
Principal objective of the work
RDC
TRC
2/24/2009
1
Viscosity, Pa*s
CAPTUB::UFactor:32
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
293.15
5
1
0.005108
5
1
0.0008813
1
298.15
5
1
0.004474
5
1
0.0007816
1
303.15
5
1
0.0039086
5
1
0.0006881
1
308.15
5
1
0.0033871
5
1
0.0006014
1
313.15
5
1
0.0029086
5
1
0.0005213
8
4
1
Principal objective of the work
RDC
TRC
2/24/2009
1
Mass density, kg/m3
PYCNOM::UFactor:4
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
293.15
5
1
809.61
5
1
1.05
1
298.15
5
1
805.01
5
1
1.08
1
303.15
5
1
800.41
5
1
1.11
1
308.15
5
1
795.81
5
1
1.15
1
313.15
5
1
791.21
5
1
1.18
9
5
1
Principal objective of the work
RDC
TRC
2/24/2009
1
Viscosity, Pa*s
CAPTUB::UFactor:32
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
293.15
5
1
0.0003956
4
1
9.33e-05
1
298.15
5
1
0.0002828
4
1
7.38e-05
1
303.15
5
1
0.0002666
4
1
7.1e-05
1
308.15
5
1
0.0002601
4
1
6.99e-05
1
313.15
5
1
0.0002545
4
1
6.89e-05
10
5
1
Principal objective of the work
RDC
TRC
2/24/2009
1
Mass density, kg/m3
PYCNOM::UFactor:4
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
293.15
5
1
804.92
5
1
1.1
1
298.15
5
1
799.7
5
1
1.11
1
303.15
5
1
794.81
5
1
1.14
1
308.15
5
1
789.78
5
1
1.19
1
313.15
5
1
784.32
5
1
1.24
11
1
1
5
1
Principal objective of the work
JFK
TRC
2/24/2009
1
Viscosity, Pa*s
CAPTUB:UFactor:32
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
293.15
5
2
0
2
1
0.0022256
5
1
0.0004062
1
293.15
5
2
0.0595
3
1
0.0018161
5
1
0.0003368
1
293.15
5
2
0.1282
4
1
0.0015044
5
1
0.0002837
1
293.15
5
2
0.1724
4
1
0.0012939
5
1
0.0002477
1
293.15
5
2
0.2326
4
1
0.0011026
5
1
0.000215
1
293.15
5
2
0.2941
4
1
0.0009668
4
1
0.0001917
1
293.15
5
2
0.3572
4
1
0.000852
4
1
0.000172
1
293.15
5
2
0.4217
4
1
0.0007693
4
1
0.0001577
1
293.15
5
2
0.4878
4
1
0.0007113
4
1
0.0001477
1
293.15
5
2
0.5556
4
1
0.0006609
4
1
0.0001391
1
293.15
5
2
0.625
4
1
0.0006072
4
1
0.0001298
1
293.15
5
2
0.6962
4
1
0.0005511
4
1
0.0001201
1
293.15
5
2
0.7693
4
1
0.0005144
4
1
0.0001138
1
293.15
5
2
0.8442
4
1
0.0004675
4
1
0.0001057
1
293.15
5
2
0.9211
4
1
0.0004293
4
1
9.91e-05
1
293.15
5
2
1
5
1
0.0003956
4
1
9.33e-05
1
298.15
5
2
0
2
1
0.0019102
5
1
0.0003527
1
298.15
5
2
0.0595
3
1
0.0015957
5
1
0.0002992
1
298.15
5
2
0.1282
4
1
0.0013616
5
1
0.0002593
1
298.15
5
2
0.1724
4
1
0.0011845
5
1
0.000229
1
298.15
5
2
0.2326
4
1
0.0009992
4
1
0.0001972
1
298.15
5
2
0.2941
4
1
0.0008812
4
1
0.000177
1
298.15
5
2
0.3572
4
1
0.0007675
4
1
0.0001574
1
298.15
5
2
0.4217
4
1
0.0006949
4
1
0.0001449
1
298.15
5
2
0.4878
4
1
0.0006289
4
1
0.0001336
1
298.15
5
2
0.5556
4
1
0.0005801
4
1
0.0001251
1
298.15
5
2
0.625
4
1
0.0005071
4
1
0.0001125
1
298.15
5
2
0.6962
4
1
0.0004516
4
1
0.000103
1
298.15
5
2
0.7693
4
1
0.0003852
4
1
9.15e-05
1
298.15
5
2
0.8442
4
1
0.000353
4
1
8.59e-05
1
298.15
5
2
0.9211
4
1
0.0003262
4
1
8.13e-05
1
298.15
5
2
1
5
1
0.0002828
4
1
7.38e-05
1
303.15
5
2
0
2
1
0.001737
5
1
0.0003233
1
303.15
5
2
0.0595
3
1
0.0014133
5
1
0.0002681
1
303.15
5
2
0.1282
4
1
0.0012067
5
1
0.0002328
1
303.15
5
2
0.1724
4
1
0.0010456
5
1
0.0002052
1
303.15
5
2
0.2326
4
1
0.0009083
4
1
0.0001816
1
303.15
5
2
0.2941
4
1
0.0008021
4
1
0.0001634
1
303.15
5
2
0.3572
4
1
0.0007154
4
1
0.0001485
1
303.15
5
2
0.4217
4
1
0.0006406
4
1
0.0001356
1
303.15
5
2
0.4878
4
1
0.0005816
4
1
0.0001254
1
303.15
5
2
0.5556
4
1
0.0005303
4
1
0.0001166
1
303.15
5
2
0.625
4
1
0.0004848
4
1
0.0001087
1
303.15
5
2
0.6962
4
1
0.0004355
4
1
0.0001002
1
303.15
5
2
0.7693
4
1
0.0003866
4
1
9.17e-05
1
303.15
5
2
0.8442
4
1
0.0003359
4
1
8.3e-05
1
303.15
5
2
0.9211
4
1
0.0002972
4
1
7.63e-05
1
303.15
5
2
1
5
1
0.0002666
4
1
7.1e-05
1
308.15
5
2
0
2
1
0.0015242
5
1
0.0002871
1
308.15
5
2
0.0595
3
1
0.0012715
5
1
0.0002439
1
308.15
5
2
0.1282
4
1
0.0010948
5
1
0.0002136
1
308.15
5
2
0.1724
4
1
0.0009637
4
1
0.0001911
1
308.15
5
2
0.2326
4
1
0.0008366
4
1
0.0001693
1
308.15
5
2
0.2941
4
1
0.0007488
4
1
0.0001542
1
308.15
5
2
0.3572
4
1
0.0006663
4
1
0.00014
1
308.15
5
2
0.4217
4
1
0.0005987
4
1
0.0001283
1
308.15
5
2
0.4878
4
1
0.0005428
4
1
0.0001187
1
308.15
5
2
0.5556
4
1
0.0004834
4
1
0.0001085
1
308.15
5
2
0.625
4
1
0.0004314
4
1
9.95e-05
1
308.15
5
2
0.6962
4
1
0.0003751
4
1
8.98e-05
1
308.15
5
2
0.7693
4
1
0.0003345
4
1
8.27e-05
1
308.15
5
2
0.8442
4
1
0.000306
4
1
7.78e-05
1
308.15
5
2
0.9211
4
1
0.0002758
4
1
7.26e-05
1
308.15
5
2
1
5
1
0.0002601
4
1
6.99e-05
1
313.15
5
2
0
2
1
0.0013472
5
1
0.0002568
1
313.15
5
2
0.0595
3
1
0.0011649
5
1
0.0002256
1
313.15
5
2
0.1282
4
1
0.0010029
5
1
0.0001979
1
313.15
5
2
0.1724
4
1
0.0008693
4
1
0.0001749
1
313.15
5
2
0.2326
4
1
0.000774
4
1
0.0001585
1
313.15
5
2
0.2941
4
1
0.0006929
4
1
0.0001446
1
313.15
5
2
0.3572
4
1
0.0006169
4
1
0.0001315
1
313.15
5
2
0.4217
4
1
0.0005567
4
1
0.0001211
1
313.15
5
2
0.4878
4
1
0.0004753
4
1
0.0001071
1
313.15
5
2
0.5556
4
1
0.0004406
4
1
0.0001011
1
313.15
5
2
0.625
4
1
0.0003846
4
1
9.14e-05
1
313.15
5
2
0.6962
4
1
0.0003302
4
1
8.2e-05
1
313.15
5
2
0.7693
4
1
0.000316
4
1
7.95e-05
1
313.15
5
2
0.8442
4
1
0.000286
4
1
7.43e-05
1
313.15
5
2
0.9211
4
1
0.0002706
4
1
7.17e-05
1
313.15
5
2
1
5
1
0.0002545
4
1
6.89e-05
12
1
1
5
1
Principal objective of the work
JFK
TRC
2/24/2009
1
Mass density, kg/m3
PYCNOM:UFactor:4
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
293.15
5
2
0
2
1
785.45
5
1
0.99
1
293.15
5
2
0.0562
3
1
786.4
5
1
0.98
1
293.15
5
2
0.1136
4
1
787.47
5
1
0.98
1
293.15
5
2
0.1724
4
1
788.54
5
1
0.99
1
293.15
5
2
0.2326
4
1
789.67
5
1
0.99
1
293.15
5
2
0.2941
4
1
790.83
5
1
1
1
293.15
5
2
0.3571
4
1
792.05
5
1
1
1
293.15
5
2
0.4217
4
1
793.29
5
1
1.01
1
293.15
5
2
0.4878
4
1
794.6
5
1
1.02
1
293.15
5
2
0.5555
4
1
795.96
5
1
1.03
1
293.15
5
2
0.625
4
1
797.35
5
1
1.04
1
293.15
5
2
0.6962
4
1
798.79
5
1
1.05
1
293.15
5
2
0.7692
4
1
800.26
5
1
1.05
1
293.15
5
2
0.8442
4
1
801.6
5
1
1.06
1
293.15
5
2
0.9211
4
1
803.3
5
1
1.07
1
293.15
5
2
1
5
1
804.92
5
1
1.1
1
298.15
5
2
0
2
1
781.26
5
1
0.98
1
298.15
5
2
0.0562
3
1
782.34
5
1
0.98
1
298.15
5
2
0.1136
4
1
783.31
5
1
0.99
1
298.15
5
2
0.1724
4
1
784.36
5
1
1
1
298.15
5
2
0.2326
4
1
785.46
5
1
1
1
298.15
5
2
0.2941
4
1
786.59
5
1
1.01
1
298.15
5
2
0.3571
4
1
787.74
5
1
1.02
1
298.15
5
2
0.4217
4
1
788.95
5
1
1.02
1
298.15
5
2
0.4878
4
1
790.18
5
1
1.03
1
298.15
5
2
0.5555
4
1
791.44
5
1
1.04
1
298.15
5
2
0.625
4
1
792.74
5
1
1.05
1
298.15
5
2
0.6962
4
1
794.08
5
1
1.06
1
298.15
5
2
0.7692
4
1
795.45
5
1
1.07
1
298.15
5
2
0.8442
4
1
796.86
5
1
1.08
1
298.15
5
2
0.9211
4
1
798.3
5
1
1.1
1
298.15
5
2
1
5
1
799.7
5
1
1.11
1
303.15
5
2
0
2
1
777.97
5
1
1.06
1
303.15
5
2
0.0562
3
1
778.9
5
1
1.07
1
303.15
5
2
0.1136
4
1
779.85
5
1
1.07
1
303.15
5
2
0.1724
4
1
780.81
5
1
1.07
1
303.15
5
2
0.2326
4
1
781.82
5
1
1.07
1
303.15
5
2
0.2941
4
1
782.85
5
1
1.08
1
303.15
5
2
0.3571
4
1
783.91
5
1
1.08
1
303.15
5
2
0.4217
4
1
785.01
5
1
1.09
1
303.15
5
2
0.4878
4
1
786.14
5
1
1.09
1
303.15
5
2
0.5555
4
1
787.29
5
1
1.1
1
303.15
5
2
0.625
4
1
788.49
5
1
1.1
1
303.15
5
2
0.6962
4
1
789.7
5
1
1.11
1
303.15
5
2
0.7692
4
1
790.95
5
1
1.12
1
303.15
5
2
0.8442
4
1
792.21
5
1
1.12
1
303.15
5
2
0.9211
4
1
793.51
5
1
1.13
1
303.15
5
2
1
5
1
794.81
5
1
1.14
1
308.15
5
2
0
2
1
772.59
5
1
1.13
1
308.15
5
2
0.0562
3
1
773.52
5
1
1.14
1
308.15
5
2
0.1136
4
1
774.58
5
1
1.14
1
308.15
5
2
0.1724
4
1
775.58
5
1
1.14
1
308.15
5
2
0.2326
4
1
776.64
5
1
1.14
1
308.15
5
2
0.2941
4
1
777.7
5
1
1.14
1
308.15
5
2
0.3571
4
1
778.8
5
1
1.15
1
308.15
5
2
0.4217
4
1
779.92
5
1
1.15
1
308.15
5
2
0.4878
4
1
781.07
5
1
1.15
1
308.15
5
2
0.5555
4
1
782.24
5
1
1.16
1
308.15
5
2
0.625
4
1
783.44
5
1
1.16
1
308.15
5
2
0.6962
4
1
784.66
5
1
1.17
1
308.15
5
2
0.7692
4
1
785.91
5
1
1.17
1
308.15
5
2
0.8442
4
1
787.18
5
1
1.18
1
308.15
5
2
0.9211
4
1
788.48
5
1
1.19
1
308.15
5
2
1
5
1
789.78
5
1
1.19
1
313.15
5
2
0
2
1
768.32
5
1
1.12
1
313.15
5
2
0.0562
3
1
769.21
5
1
1.13
1
313.15
5
2
0.1136
4
1
770.17
5
1
1.14
1
313.15
5
2
0.1724
4
1
771.13
5
1
1.14
1
313.15
5
2
0.2326
4
1
772.12
5
1
1.15
1
313.15
5
2
0.2941
4
1
773.13
5
1
1.15
1
313.15
5
2
0.3571
4
1
774.16
5
1
1.16
1
313.15
5
2
0.4217
4
1
775.21
5
1
1.17
1
313.15
5
2
0.4878
4
1
776.27
5
1
1.17
1
313.15
5
2
0.5555
4
1
777.37
5
1
1.18
1
313.15
5
2
0.625
4
1
778.48
5
1
1.19
1
313.15
5
2
0.6962
4
1
779.61
5
1
1.2
1
313.15
5
2
0.7692
4
1
780.76
5
1
1.21
1
313.15
5
2
0.8442
4
1
781.93
5
1
1.22
1
313.15
5
2
0.9211
4
1
783.12
5
1
1.23
1
313.15
5
2
1
5
1
784.32
5
1
1.24
13
2
1
5
1
Principal objective of the work
JFK
TRC
2/24/2009
1
Viscosity, Pa*s
CAPTUB:UFactor:32
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
293.15
5
2
0
2
1
0.0040366
5
1
0.0007093
1
293.15
5
2
0.0684
3
1
0.0031376
5
1
0.0005597
1
293.15
5
2
0.1365
4
1
0.0024294
5
1
0.0004406
1
293.15
5
2
0.2044
4
1
0.0018623
5
1
0.0003446
1
293.15
5
2
0.2721
4
1
0.001426
5
1
0.0002703
1
293.15
5
2
0.3395
4
1
0.0011106
5
1
0.0002163
1
293.15
5
2
0.4066
4
1
0.0008561
4
1
0.0001727
1
293.15
5
2
0.4735
4
1
0.0007002
4
1
0.0001458
1
293.15
5
2
0.5402
4
1
0.0006142
4
1
0.000131
1
293.15
5
2
0.6066
4
1
0.000538
4
1
0.0001179
1
293.15
5
2
0.6727
4
1
0.0005271
4
1
0.000116
1
293.15
5
2
0.7387
4
1
0.0005071
4
1
0.0001125
1
293.15
5
2
0.8044
4
1
0.0005079
4
1
0.0001127
1
293.15
5
2
0.8698
4
1
0.0004996
4
1
0.0001113
1
293.15
5
2
0.935
4
1
0.0004722
4
1
0.0001065
1
293.15
5
2
1
5
1
0.0003956
4
1
9.33e-05
1
298.15
5
2
0
2
1
0.0033297
5
1
0.0005918
1
298.15
5
2
0.0684
3
1
0.0026113
5
1
0.0004713
1
298.15
5
2
0.1365
4
1
0.0020537
5
1
0.0003771
1
298.15
5
2
0.2044
4
1
0.001566
5
1
0.0002942
1
298.15
5
2
0.2721
4
1
0.0012057
5
1
0.0002326
1
298.15
5
2
0.3395
4
1
0.0009449
4
1
0.0001879
1
298.15
5
2
0.4066
4
1
0.0007513
4
1
0.0001546
1
298.15
5
2
0.4735
4
1
0.000607
4
1
0.0001298
1
298.15
5
2
0.5402
4
1
0.0005305
4
1
0.0001166
1
298.15
5
2
0.6066
4
1
0.0004883
4
1
0.0001093
1
298.15
5
2
0.6727
4
1
0.0004556
4
1
0.0001037
1
298.15
5
2
0.7387
4
1
0.0004444
4
1
0.0001017
1
298.15
5
2
0.8044
4
1
0.0004189
4
1
9.73e-05
1
298.15
5
2
0.8698
4
1
0.0004217
4
1
9.78e-05
1
298.15
5
2
0.935
4
1
0.0003617
4
1
8.74e-05
1
298.15
5
2
1
5
1
0.0002828
4
1
7.38e-05
1
303.15
5
2
0
2
1
0.0028752
5
1
0.0005157
1
303.15
5
2
0.0684
3
1
0.0022402
5
1
0.0004087
1
303.15
5
2
0.1365
4
1
0.0017799
5
1
0.0003306
1
303.15
5
2
0.2044
4
1
0.0014042
5
1
0.0002666
1
303.15
5
2
0.2721
4
1
0.0011041
5
1
0.0002152
1
303.15
5
2
0.3395
4
1
0.0008637
4
1
0.000174
1
303.15
5
2
0.4066
4
1
0.000676
4
1
0.0001417
1
303.15
5
2
0.4735
4
1
0.0005418
4
1
0.0001185
1
303.15
5
2
0.5402
4
1
0.0004663
4
1
0.0001055
1
303.15
5
2
0.6066
4
1
0.0004135
4
1
9.64e-05
1
303.15
5
2
0.6727
4
1
0.0003743
4
1
8.96e-05
1
303.15
5
2
0.7387
4
1
0.0003713
4
1
8.91e-05
1
303.15
5
2
0.8044
4
1
0.0003607
4
1
8.73e-05
1
303.15
5
2
0.8698
4
1
0.0003443
4
1
8.44e-05
1
303.15
5
2
0.935
4
1
0.0003135
4
1
7.91e-05
1
303.15
5
2
1
5
1
0.0002666
4
1
7.1e-05
1
308.15
5
2
0
2
1
0.0024207
5
1
0.0004392
1
308.15
5
2
0.0684
3
1
0.0019129
5
1
0.0003532
1
308.15
5
2
0.1365
4
1
0.0015337
5
1
0.0002887
1
308.15
5
2
0.2044
4
1
0.0011932
5
1
0.0002305
1
308.15
5
2
0.2721
4
1
0.0009579
4
1
0.0001901
1
308.15
5
2
0.3395
4
1
0.0007612
4
1
0.0001563
1
308.15
5
2
0.4066
4
1
0.0006222
4
1
0.0001324
1
308.15
5
2
0.4735
4
1
0.0005176
4
1
0.0001144
1
308.15
5
2
0.5402
4
1
0.0004456
4
1
0.0001019
1
308.15
5
2
0.6066
4
1
0.0004102
4
1
9.58e-05
1
308.15
5
2
0.6727
4
1
0.0003752
4
1
8.98e-05
1
308.15
5
2
0.7387
4
1
0.0003573
4
1
8.67e-05
1
308.15
5
2
0.8044
4
1
0.0003498
4
1
8.54e-05
1
308.15
5
2
0.8698
4
1
0.0003334
4
1
8.25e-05
1
308.15
5
2
0.935
4
1
0.0003005
4
1
7.69e-05
1
308.15
5
2
1
5
1
0.0002601
4
1
6.99e-05
1
313.15
5
2
0
2
1
0.0019666
5
1
0.0003623
1
313.15
5
2
0.0684
3
1
0.0016255
5
1
0.0003043
1
313.15
5
2
0.1365
4
1
0.00133
5
1
0.0002539
1
313.15
5
2
0.2044
4
1
0.0010736
5
1
0.00021
1
313.15
5
2
0.2721
4
1
0.0008538
4
1
0.0001723
1
313.15
5
2
0.3395
4
1
0.0006894
4
1
0.000144
1
313.15
5
2
0.4066
4
1
0.0005674
4
1
0.000123
1
313.15
5
2
0.4735
4
1
0.00046
4
1
0.0001044
1
313.15
5
2
0.5402
4
1
0.0003948
4
1
9.32e-05
1
313.15
5
2
0.6066
4
1
0.00034
4
1
8.37e-05
1
313.15
5
2
0.6727
4
1
0.0003138
4
1
7.92e-05
1
313.15
5
2
0.7387
4
1
0.0002909
4
1
7.52e-05
1
313.15
5
2
0.8044
4
1
0.0002754
4
1
7.25e-05
1
313.15
5
2
0.8698
4
1
0.00028
4
1
7.33e-05
1
313.15
5
2
0.935
4
1
0.0002769
4
1
7.28e-05
1
313.15
5
2
1
5
1
0.0002545
4
1
6.89e-05
14
2
1
5
1
Principal objective of the work
JFK
TRC
2/24/2009
1
Mass density, kg/m3
PYCNOM:UFactor:4
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
293.15
5
2
0
2
1
801.68
5
1
0.98
1
293.15
5
2
0.0684
3
1
801.9
5
1
0.99
1
293.15
5
2
0.1365
4
1
802.11
5
1
0.99
1
293.15
5
2
0.2044
4
1
802.32
5
1
1
1
293.15
5
2
0.2721
4
1
802.52
5
1
1.01
1
293.15
5
2
0.3395
4
1
802.72
5
1
1.02
1
293.15
5
2
0.4066
4
1
802.92
5
1
1.02
1
293.15
5
2
0.4735
4
1
803.13
5
1
1.03
1
293.15
5
2
0.5402
4
1
803.33
5
1
1.04
1
293.15
5
2
0.6066
4
1
803.54
5
1
1.05
1
293.15
5
2
0.6727
4
1
803.75
5
1
1.06
1
293.15
5
2
0.7387
4
1
803.97
5
1
1.07
1
293.15
5
2
0.8044
4
1
804.2
5
1
1.08
1
293.15
5
2
0.8698
4
1
804.43
5
1
1.08
1
293.15
5
2
0.935
4
1
804.67
5
1
1.09
1
293.15
5
2
1
5
1
804.92
5
1
1.1
1
298.15
5
2
0
2
1
797.8
5
1
1
1
298.15
5
2
0.0684
3
1
797.93
5
1
1.01
1
298.15
5
2
0.1365
4
1
798.06
5
1
1.02
1
298.15
5
2
0.2044
4
1
798.18
5
1
1.02
1
298.15
5
2
0.2721
4
1
798.29
5
1
1.03
1
298.15
5
2
0.3395
4
1
798.41
5
1
1.04
1
298.15
5
2
0.4066
4
1
798.52
5
1
1.05
1
298.15
5
2
0.4735
4
1
798.63
5
1
1.05
1
298.15
5
2
0.5402
4
1
798.75
5
1
1.06
1
298.15
5
2
0.6066
4
1
798.87
5
1
1.07
1
298.15
5
2
0.6727
4
1
798.99
5
1
1.07
1
298.15
5
2
0.7387
4
1
799.12
5
1
1.08
1
298.15
5
2
0.8044
4
1
799.25
5
1
1.09
1
298.15
5
2
0.8698
4
1
799.4
5
1
1.1
1
298.15
5
2
0.935
4
1
799.54
5
1
1.11
1
298.15
5
2
1
5
1
799.7
5
1
1.11
1
303.15
5
2
0
2
1
794.16
5
1
1.05
1
303.15
5
2
0.0684
3
1
794.21
5
1
1.05
1
303.15
5
2
0.1365
4
1
794.25
5
1
1.06
1
303.15
5
2
0.2044
4
1
794.29
5
1
1.06
1
303.15
5
2
0.2721
4
1
794.32
5
1
1.07
1
303.15
5
2
0.3395
4
1
794.36
5
1
1.08
1
303.15
5
2
0.4066
4
1
794.39
5
1
1.08
1
303.15
5
2
0.4735
4
1
794.42
5
1
1.09
1
303.15
5
2
0.5402
4
1
794.46
5
1
1.09
1
303.15
5
2
0.6066
4
1
794.49
5
1
1.1
1
303.15
5
2
0.6727
4
1
794.53
5
1
1.1
1
303.15
5
2
0.7387
4
1
794.58
5
1
1.11
1
303.15
5
2
0.8044
4
1
794.63
5
1
1.12
1
303.15
5
2
0.8698
4
1
794.68
5
1
1.12
1
303.15
5
2
0.935
4
1
794.74
5
1
1.13
1
303.15
5
2
1
5
1
794.81
5
1
1.14
1
308.15
5
2
0
2
1
790.06
5
1
1.07
1
308.15
5
2
0.0684
3
1
790.04
5
1
1.08
1
308.15
5
2
0.1365
4
1
790.03
5
1
1.09
1
308.15
5
2
0.2044
4
1
790
5
1
1.09
1
308.15
5
2
0.2721
4
1
789.98
5
1
1.1
1
308.15
5
2
0.3395
4
1
789.95
5
1
1.11
1
308.15
5
2
0.4066
4
1
789.92
5
1
1.12
1
308.15
5
2
0.4735
4
1
789.89
5
1
1.12
1
308.15
5
2
0.5402
4
1
789.87
5
1
1.13
1
308.15
5
2
0.6066
4
1
789.85
5
1
1.14
1
308.15
5
2
0.6727
4
1
789.83
5
1
1.15
1
308.15
5
2
0.7387
4
1
789.82
5
1
1.16
1
308.15
5
2
0.8044
4
1
789.81
5
1
1.16
1
308.15
5
2
0.8698
4
1
789.8
5
1
1.17
1
308.15
5
2
0.935
4
1
789.79
5
1
1.18
1
308.15
5
2
1
5
1
789.78
5
1
1.19
1
313.15
5
2
0
2
1
786.7
5
1
1.08
1
313.15
5
2
0.0684
3
1
786.54
5
1
1.09
1
313.15
5
2
0.1365
4
1
786.39
5
1
1.1
1
313.15
5
2
0.2044
4
1
786.22
5
1
1.11
1
313.15
5
2
0.2721
4
1
786.06
5
1
1.12
1
313.15
5
2
0.3395
4
1
785.89
5
1
1.13
1
313.15
5
2
0.4066
4
1
785.73
5
1
1.14
1
313.15
5
2
0.4735
4
1
785.56
5
1
1.15
1
313.15
5
2
0.5402
4
1
785.4
5
1
1.16
1
313.15
5
2
0.6066
4
1
785.23
5
1
1.17
1
313.15
5
2
0.6727
4
1
785.08
5
1
1.18
1
313.15
5
2
0.7387
4
1
784.92
5
1
1.19
1
313.15
5
2
0.8044
4
1
784.77
5
1
1.21
1
313.15
5
2
0.8698
4
1
784.62
5
1
1.22
1
313.15
5
2
0.935
4
1
784.47
5
1
1.23
1
313.15
5
2
1
5
1
784.32
5
1
1.24
15
3
1
5
1
Principal objective of the work
JFK
TRC
2/24/2009
1
Viscosity, Pa*s
CAPTUB:UFactor:32
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
293.15
5
2
0
2
1
0.0036316
5
1
0.0006421
1
293.15
5
2
0.0684
3
1
0.0029103
5
1
0.0005216
1
293.15
5
2
0.1365
4
1
0.0023397
5
1
0.0004255
1
293.15
5
2
0.2044
4
1
0.00187
5
1
0.0003459
1
293.15
5
2
0.2721
4
1
0.0014911
5
1
0.0002814
1
293.15
5
2
0.3395
4
1
0.0011831
5
1
0.0002288
1
293.15
5
2
0.4066
4
1
0.0009558
4
1
0.0001898
1
293.15
5
2
0.4735
4
1
0.0007693
4
1
0.0001577
1
293.15
5
2
0.5402
4
1
0.0006236
4
1
0.0001326
1
293.15
5
2
0.6066
4
1
0.0005287
4
1
0.0001163
1
293.15
5
2
0.6727
4
1
0.0004645
4
1
0.0001052
1
293.15
5
2
0.7387
4
1
0.0004412
4
1
0.0001012
1
293.15
5
2
0.8044
4
1
0.0004486
4
1
0.0001025
1
293.15
5
2
0.8698
4
1
0.0004468
4
1
0.0001021
1
293.15
5
2
0.935
4
1
0.00042
4
1
9.75e-05
1
293.15
5
2
1
5
1
0.0003956
4
1
9.33e-05
1
298.15
5
2
0
2
1
0.0029975
5
1
0.0005362
1
298.15
5
2
0.0684
3
1
0.0024289
5
1
0.0004406
1
298.15
5
2
0.1365
4
1
0.0020069
5
1
0.0003692
1
298.15
5
2
0.2044
4
1
0.0016125
5
1
0.0003021
1
298.15
5
2
0.2721
4
1
0.0012989
5
1
0.0002486
1
298.15
5
2
0.3395
4
1
0.0010509
5
1
0.0002061
1
298.15
5
2
0.4066
4
1
0.0008537
4
1
0.0001722
1
298.15
5
2
0.4735
4
1
0.000687
4
1
0.0001436
1
298.15
5
2
0.5402
4
1
0.00056
4
1
0.0001217
1
298.15
5
2
0.6066
4
1
0.00048
4
1
0.0001079
1
298.15
5
2
0.6727
4
1
0.0004282
4
1
9.89e-05
1
298.15
5
2
0.7387
4
1
0.0003922
4
1
9.27e-05
1
298.15
5
2
0.8044
4
1
0.000362
4
1
8.75e-05
1
298.15
5
2
0.8698
4
1
0.0003482
4
1
8.51e-05
1
298.15
5
2
0.935
4
1
0.0003
4
1
7.68e-05
1
298.15
5
2
1
5
1
0.0002828
4
1
7.38e-05
1
303.15
5
2
0
2
1
0.0024978
5
1
0.0004522
1
303.15
5
2
0.0684
3
1
0.0020372
5
1
0.0003743
1
303.15
5
2
0.1365
4
1
0.0016491
5
1
0.0003083
1
303.15
5
2
0.2044
4
1
0.0013517
5
1
0.0002576
1
303.15
5
2
0.2721
4
1
0.0010737
5
1
0.00021
1
303.15
5
2
0.3395
4
1
0.0008484
4
1
0.0001713
1
303.15
5
2
0.4066
4
1
0.0006826
4
1
0.0001428
1
303.15
5
2
0.4735
4
1
0.0005613
4
1
0.0001219
1
303.15
5
2
0.5402
4
1
0.0004526
4
1
0.0001031
1
303.15
5
2
0.6066
4
1
0.0003944
4
1
9.31e-05
1
303.15
5
2
0.6727
4
1
0.0003468
4
1
8.49e-05
1
303.15
5
2
0.7387
4
1
0.0003077
4
1
7.81e-05
1
303.15
5
2
0.8044
4
1
0.0003031
4
1
7.73e-05
1
303.15
5
2
0.8698
4
1
0.0003071
4
1
7.8e-05
1
303.15
5
2
0.935
4
1
0.0002786
4
1
7.31e-05
1
303.15
5
2
1
5
1
0.0002666
4
1
7.1e-05
1
308.15
5
2
0
2
1
0.0020542
5
1
0.0003772
1
308.15
5
2
0.0684
3
1
0.0016915
5
1
0.0003156
1
308.15
5
2
0.1365
4
1
0.0013391
5
1
0.0002554
1
308.15
5
2
0.2044
4
1
0.0010543
5
1
0.0002067
1
308.15
5
2
0.2721
4
1
0.0008161
4
1
0.0001658
1
308.15
5
2
0.3395
4
1
0.0006282
4
1
0.0001334
1
308.15
5
2
0.4066
4
1
0.0005076
4
1
0.0001126
1
308.15
5
2
0.4735
4
1
0.0004126
4
1
9.62e-05
1
308.15
5
2
0.5402
4
1
0.0003601
4
1
8.72e-05
1
308.15
5
2
0.6066
4
1
0.000326
4
1
8.13e-05
1
308.15
5
2
0.6727
4
1
0.0003051
4
1
7.76e-05
1
308.15
5
2
0.7387
4
1
0.000309
4
1
7.83e-05
1
308.15
5
2
0.8044
4
1
0.0003112
4
1
7.87e-05
1
308.15
5
2
0.8698
4
1
0.0003186
4
1
8e-05
1
308.15
5
2
0.935
4
1
0.0002966
4
1
7.62e-05
1
308.15
5
2
1
5
1
0.0002601
4
1
6.99e-05
1
313.15
5
2
0
2
1
0.0017989
5
1
0.0003338
1
313.15
5
2
0.0684
3
1
0.0014993
5
1
0.0002828
1
313.15
5
2
0.1365
4
1
0.001228
5
1
0.0002364
1
313.15
5
2
0.2044
4
1
0.0010032
5
1
0.0001979
1
313.15
5
2
0.2721
4
1
0.0008187
4
1
0.0001662
1
313.15
5
2
0.3395
4
1
0.0006806
4
1
0.0001425
1
313.15
5
2
0.4066
4
1
0.0005709
4
1
0.0001236
1
313.15
5
2
0.4735
4
1
0.0004786
4
1
0.0001076
1
313.15
5
2
0.5402
4
1
0.0004206
4
1
9.76e-05
1
313.15
5
2
0.6066
4
1
0.0003681
4
1
8.85e-05
1
313.15
5
2
0.6727
4
1
0.0003429
4
1
8.42e-05
1
313.15
5
2
0.7387
4
1
0.0003191
4
1
8.01e-05
1
313.15
5
2
0.8044
4
1
0.0002915
4
1
7.53e-05
1
313.15
5
2
0.8698
4
1
0.0002805
4
1
7.34e-05
1
313.15
5
2
0.935
4
1
0.0002718
4
1
7.19e-05
1
313.15
5
2
1
5
1
0.0002545
4
1
6.89e-05
16
3
1
5
1
Principal objective of the work
JFK
TRC
2/24/2009
1
Mass density, kg/m3
PYCNOM:UFactor:4
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
293.15
5
2
0
2
1
806.48
5
1
1.01
1
293.15
5
2
0.0684
3
1
806.36
5
1
1.01
1
293.15
5
2
0.1365
4
1
806.25
5
1
1.02
1
293.15
5
2
0.2044
4
1
806.14
5
1
1.02
1
293.15
5
2
0.2721
4
1
806.03
5
1
1.03
1
293.15
5
2
0.3395
4
1
805.92
5
1
1.04
1
293.15
5
2
0.4066
4
1
805.81
5
1
1.04
1
293.15
5
2
0.4735
4
1
805.71
5
1
1.05
1
293.15
5
2
0.5402
4
1
805.61
5
1
1.05
1
293.15
5
2
0.6066
4
1
805.5
5
1
1.06
1
293.15
5
2
0.6727
4
1
805.4
5
1
1.07
1
293.15
5
2
0.7387
4
1
805.3
5
1
1.07
1
293.15
5
2
0.8044
4
1
805.21
5
1
1.09
1
293.15
5
2
0.8698
4
1
805.11
5
1
1.09
1
293.15
5
2
0.935
4
1
805.01
5
1
1.09
1
293.15
5
2
1
5
1
804.92
5
1
1.1
1
298.15
5
2
0
2
1
802.35
5
1
1.01
1
298.15
5
2
0.0684
3
1
802.16
5
1
1.02
1
298.15
5
2
0.1365
4
1
801.98
5
1
1.02
1
298.15
5
2
0.2044
4
1
801.79
5
1
1.03
1
298.15
5
2
0.2721
4
1
801.61
5
1
1.04
1
298.15
5
2
0.3395
4
1
801.43
5
1
1.04
1
298.15
5
2
0.4066
4
1
801.25
5
1
1.05
1
298.15
5
2
0.4735
4
1
801.07
5
1
1.06
1
298.15
5
2
0.5402
4
1
800.9
5
1
1.06
1
298.15
5
2
0.6066
4
1
800.72
5
1
1.07
1
298.15
5
2
0.6727
4
1
800.55
5
1
1.08
1
298.15
5
2
0.7387
4
1
800.38
5
1
1.08
1
298.15
5
2
0.8044
4
1
800.1
5
1
1.09
1
298.15
5
2
0.8698
4
1
800.04
5
1
1.1
1
298.15
5
2
0.935
4
1
799.87
5
1
1.11
1
298.15
5
2
1
5
1
799.7
5
1
1.11
1
303.15
5
2
0
2
1
798.96
5
1
1.07
1
303.15
5
2
0.0684
3
1
798.67
5
1
1.07
1
303.15
5
2
0.1365
4
1
798.39
5
1
1.08
1
303.15
5
2
0.2044
4
1
798.1
5
1
1.08
1
303.15
5
2
0.2721
4
1
797.82
5
1
1.09
1
303.15
5
2
0.3395
4
1
797.54
5
1
1.09
1
303.15
5
2
0.4066
4
1
797.26
5
1
1.1
1
303.15
5
2
0.4735
4
1
796.98
5
1
1.1
1
303.15
5
2
0.5402
4
1
796.71
5
1
1.1
1
303.15
5
2
0.6066
4
1
796.43
5
1
1.11
1
303.15
5
2
0.6727
4
1
796.16
5
1
1.11
1
303.15
5
2
0.7387
4
1
795.89
5
1
1.12
1
303.15
5
2
0.8044
4
1
795.62
5
1
1.12
1
303.15
5
2
0.8698
4
1
795.35
5
1
1.13
1
303.15
5
2
0.935
4
1
795.08
5
1
1.13
1
303.15
5
2
1
5
1
794.81
5
1
1.14
1
308.15
5
2
0
2
1
794.18
5
1
1.13
1
308.15
5
2
0.0684
3
1
793.88
5
1
1.13
1
308.15
5
2
0.1365
4
1
793.58
5
1
1.14
1
308.15
5
2
0.2044
4
1
793.28
5
1
1.14
1
308.15
5
2
0.2721
4
1
792.98
5
1
1.15
1
308.15
5
2
0.3395
4
1
792.68
5
1
1.15
1
308.15
5
2
0.4066
4
1
792.39
5
1
1.15
1
308.15
5
2
0.4735
4
1
792.09
5
1
1.16
1
308.15
5
2
0.5402
4
1
791.8
5
1
1.16
1
308.15
5
2
0.6066
4
1
791.51
5
1
1.17
1
308.15
5
2
0.6727
4
1
791.22
5
1
1.17
1
308.15
5
2
0.7387
4
1
790.93
5
1
1.17
1
308.15
5
2
0.8044
4
1
790.64
5
1
1.18
1
308.15
5
2
0.8698
4
1
790.35
5
1
1.18
1
308.15
5
2
0.935
4
1
790.06
5
1
1.19
1
308.15
5
2
1
5
1
789.78
5
1
1.19
1
313.15
5
2
0
2
1
790.07
5
1
1.14
1
313.15
5
2
0.0684
3
1
789.68
5
1
1.15
1
313.15
5
2
0.1365
4
1
789.29
5
1
1.15
1
313.15
5
2
0.2044
4
1
788.9
5
1
1.16
1
313.15
5
2
0.2721
4
1
788.51
5
1
1.16
1
313.15
5
2
0.3395
4
1
788.13
5
1
1.17
1
313.15
5
2
0.4066
4
1
787.74
5
1
1.18
1
313.15
5
2
0.4735
4
1
787.36
5
1
1.18
1
313.15
5
2
0.5402
4
1
786.97
5
1
1.19
1
313.15
5
2
0.6066
4
1
786.59
5
1
1.2
1
313.15
5
2
0.6727
4
1
786.21
5
1
1.2
1
313.15
5
2
0.7387
4
1
785.83
5
1
1.21
1
313.15
5
2
0.8044
4
1
785.45
5
1
1.22
1
313.15
5
2
0.8698
4
1
785.07
5
1
1.23
1
313.15
5
2
0.935
4
1
784.7
5
1
1.23
1
313.15
5
2
1
5
1
784.32
5
1
1.24
17
4
1
5
1
Principal objective of the work
JFK
TRC
2/24/2009
1
Viscosity, Pa*s
CAPTUB:UFactor:32
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
293.15
5
2
0
2
1
0.005108
5
1
0.0008813
1
293.15
5
2
0.0803
3
1
0.0038096
5
1
0.0006717
1
293.15
5
2
0.1583
4
1
0.0028621
5
1
0.0005135
1
293.15
5
2
0.2341
4
1
0.0021049
5
1
0.0003858
1
293.15
5
2
0.3077
4
1
0.0015578
5
1
0.0002928
1
293.15
5
2
0.3794
4
1
0.0011503
5
1
0.0002231
1
293.15
5
2
0.449
4
1
0.000842
4
1
0.0001702
1
293.15
5
2
0.5168
4
1
0.0006725
4
1
0.0001411
1
293.15
5
2
0.5828
4
1
0.0005515
4
1
0.0001202
1
293.15
5
2
0.6471
4
1
0.0004986
4
1
0.0001111
1
293.15
5
2
0.7097
4
1
0.0004935
4
1
0.0001102
1
293.15
5
2
0.7707
4
1
0.0004482
4
1
0.0001024
1
293.15
5
2
0.8302
4
1
0.0004457
4
1
0.0001019
1
293.15
5
2
0.8882
4
1
0.0004464
4
1
0.0001021
1
293.15
5
2
0.9448
4
1
0.0004338
4
1
9.99e-05
1
293.15
5
2
1
5
1
0.0003956
4
1
9.33e-05
1
298.15
5
2
0
2
1
0.004474
5
1
0.0007816
1
298.15
5
2
0.0803
3
1
0.00335
5
1
0.0005952
1
298.15
5
2
0.1583
4
1
0.0025206
5
1
0.000456
1
298.15
5
2
0.2341
4
1
0.00185
5
1
0.0003425
1
298.15
5
2
0.3077
4
1
0.00137
5
1
0.0002607
1
298.15
5
2
0.3794
4
1
0.0010541
5
1
0.0002067
1
298.15
5
2
0.449
4
1
0.0008221
4
1
0.0001668
1
298.15
5
2
0.5168
4
1
0.0006579
4
1
0.0001385
1
298.15
5
2
0.5828
4
1
0.0005913
4
1
0.0001271
1
298.15
5
2
0.6471
4
1
0.0005219
4
1
0.0001151
1
298.15
5
2
0.7097
4
1
0.0004894
4
1
0.0001095
1
298.15
5
2
0.7707
4
1
0.0004437
4
1
0.0001016
1
298.15
5
2
0.8302
4
1
0.0004344
4
1
0.0001
1
298.15
5
2
0.8882
4
1
0.0003813
4
1
9.08e-05
1
298.15
5
2
0.9448
4
1
0.0003142
4
1
7.92e-05
1
298.15
5
2
1
5
1
0.0002828
4
1
7.38e-05
1
303.15
5
2
0
2
1
0.0039086
5
1
0.0006881
1
303.15
5
2
0.0803
3
1
0.0029001
5
1
0.0005199
1
303.15
5
2
0.1583
4
1
0.0021401
5
1
0.0003917
1
303.15
5
2
0.2341
4
1
0.0015301
5
1
0.0002881
1
303.15
5
2
0.3077
4
1
0.0010901
5
1
0.0002128
1
303.15
5
2
0.3794
4
1
0.0008501
4
1
0.0001716
1
303.15
5
2
0.449
4
1
0.0006863
4
1
0.0001434
1
303.15
5
2
0.5168
4
1
0.0005601
4
1
0.0001217
1
303.15
5
2
0.5828
4
1
0.0005201
4
1
0.0001148
1
303.15
5
2
0.6471
4
1
0.00052
4
1
0.0001148
1
303.15
5
2
0.7097
4
1
0.00048
4
1
0.0001079
1
303.15
5
2
0.7707
4
1
0.0004801
4
1
0.0001079
1
303.15
5
2
0.8302
4
1
0.0004802
4
1
0.0001079
1
303.15
5
2
0.8882
4
1
0.0004402
4
1
0.000101
1
303.15
5
2
0.9448
4
1
0.0003601
4
1
8.72e-05
1
303.15
5
2
1
5
1
0.0002666
4
1
7.1e-05
1
308.15
5
2
0
2
1
0.0033871
5
1
0.0006014
1
308.15
5
2
0.0803
3
1
0.0025207
5
1
0.000456
1
308.15
5
2
0.1583
4
1
0.001905
5
1
0.0003519
1
308.15
5
2
0.2341
4
1
0.0014208
5
1
0.0002694
1
308.15
5
2
0.3077
4
1
0.0011034
5
1
0.0002151
1
308.15
5
2
0.3794
4
1
0.00084
4
1
0.0001699
1
308.15
5
2
0.449
4
1
0.0007188
4
1
0.000149
1
308.15
5
2
0.5168
4
1
0.0005865
4
1
0.0001262
1
308.15
5
2
0.5828
4
1
0.0005202
4
1
0.0001148
1
308.15
5
2
0.6471
4
1
0.0004801
4
1
0.0001079
1
308.15
5
2
0.7097
4
1
0.0004507
4
1
0.0001028
1
308.15
5
2
0.7707
4
1
0.0004505
4
1
0.0001028
1
308.15
5
2
0.8302
4
1
0.0004503
4
1
0.0001027
1
308.15
5
2
0.8882
4
1
0.0004012
4
1
9.43e-05
1
308.15
5
2
0.9448
4
1
0.00032
4
1
8.02e-05
1
308.15
5
2
1
5
1
0.0002601
4
1
6.99e-05
1
313.15
5
2
0
2
1
0.0029086
5
1
0.0005213
1
313.15
5
2
0.0803
3
1
0.00226
5
1
0.000412
1
313.15
5
2
0.1583
4
1
0.0017
5
1
0.000317
1
313.15
5
2
0.2341
4
1
0.0012873
5
1
0.0002466
1
313.15
5
2
0.3077
4
1
0.0009819
4
1
0.0001943
1
313.15
5
2
0.3794
4
1
0.0007418
4
1
0.000153
1
313.15
5
2
0.449
4
1
0.0005869
4
1
0.0001263
1
313.15
5
2
0.5168
4
1
0.0004801
4
1
0.0001079
1
313.15
5
2
0.5828
4
1
0.0004017
4
1
9.44e-05
1
313.15
5
2
0.6471
4
1
0.0003511
4
1
8.56e-05
1
313.15
5
2
0.7097
4
1
0.0003307
4
1
8.21e-05
1
313.15
5
2
0.7707
4
1
0.000323
4
1
8.08e-05
1
313.15
5
2
0.8302
4
1
0.0003001
4
1
7.68e-05
1
313.15
5
2
0.8882
4
1
0.0002999
4
1
7.68e-05
1
313.15
5
2
0.9448
4
1
0.0002997
4
1
7.67e-05
1
313.15
5
2
1
5
1
0.0002545
4
1
6.89e-05
18
4
1
5
1
Principal objective of the work
JFK
TRC
2/24/2009
1
Mass density, kg/m3
PYCNOM:UFactor:4
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
293.15
5
2
0
2
1
809.61
5
1
1.05
1
293.15
5
2
0.0803
3
1
809.22
5
1
1.05
1
293.15
5
2
0.1583
4
1
808.84
5
1
1.06
1
293.15
5
2
0.2341
4
1
808.48
5
1
1.06
1
293.15
5
2
0.3077
4
1
808.13
5
1
1.06
1
293.15
5
2
0.3794
4
1
807.79
5
1
1.07
1
293.15
5
2
0.449
4
1
807.47
5
1
1.07
1
293.15
5
2
0.5168
4
1
807.16
5
1
1.08
1
293.15
5
2
0.5828
4
1
806.85
5
1
1.08
1
293.15
5
2
0.6471
4
1
806.56
5
1
1.08
1
293.15
5
2
0.7097
4
1
806.27
5
1
1.09
1
293.15
5
2
0.7707
4
1
805.99
5
1
1.09
1
293.15
5
2
0.8302
4
1
805.71
5
1
1.09
1
293.15
5
2
0.8882
4
1
805.45
5
1
1.1
1
293.15
5
2
0.9448
4
1
805.18
5
1
1.1
1
293.15
5
2
1
5
1
804.92
5
1
1.1
1
298.15
5
2
0
2
1
805.01
5
1
1.08
1
298.15
5
2
0.0803
3
1
804.57
5
1
1.08
1
298.15
5
2
0.1583
4
1
804.15
5
1
1.09
1
298.15
5
2
0.2341
4
1
803.74
5
1
1.09
1
298.15
5
2
0.3077
4
1
803.35
5
1
1.08
1
298.15
5
2
0.3794
4
1
802.97
5
1
1.09
1
298.15
5
2
0.449
4
1
802.6
5
1
1.1
1
298.15
5
2
0.5168
4
1
802.24
5
1
1.1
1
298.15
5
2
0.5828
4
1
801.89
5
1
1.15
1
298.15
5
2
0.6471
4
1
801.56
5
1
1.1
1
298.15
5
2
0.7097
4
1
801.23
5
1
1.1
1
298.15
5
2
0.7707
4
1
800.91
5
1
1.11
1
298.15
5
2
0.8302
4
1
800.6
5
1
1.11
1
298.15
5
2
0.8882
4
1
800.29
5
1
1.11
1
298.15
5
2
0.9448
4
1
799.99
5
1
1.11
1
298.15
5
2
1
5
1
799.7
5
1
1.11
1
303.15
5
2
0
2
1
800.41
5
1
1.11
1
303.15
5
2
0.0803
3
1
799.94
5
1
1.12
1
303.15
5
2
0.1583
4
1
799.49
5
1
1.12
1
303.15
5
2
0.2341
4
1
799.06
5
1
1.12
1
303.15
5
2
0.3077
4
1
798.85
5
1
1.12
1
303.15
5
2
0.3794
4
1
798.25
5
1
1.12
1
303.15
5
2
0.449
4
1
797.86
5
1
1.12
1
303.15
5
2
0.5168
4
1
797.48
5
1
1.12
1
303.15
5
2
0.5828
4
1
796.12
5
1
1.13
1
303.15
5
2
0.6471
4
1
796.77
5
1
1.13
1
303.15
5
2
0.7097
4
1
796.43
5
1
1.13
1
303.15
5
2
0.7707
4
1
796.08
5
1
1.13
1
303.15
5
2
0.8302
4
1
795.75
5
1
1.13
1
303.15
5
2
0.8882
4
1
795.42
5
1
1.13
1
303.15
5
2
0.9448
4
1
795.11
5
1
1.14
1
303.15
5
2
1
5
1
794.81
5
1
1.14
1
308.15
5
2
0
2
1
795.81
5
1
1.15
1
308.15
5
2
0.0803
3
1
795.3
5
1
1.15
1
308.15
5
2
0.1583
4
1
794.82
5
1
1.15
1
308.15
5
2
0.2341
4
1
794.36
5
1
1.16
1
308.15
5
2
0.3077
4
1
793.92
5
1
1.17
1
308.15
5
2
0.3794
4
1
793.49
5
1
1.16
1
308.15
5
2
0.449
4
1
793.07
5
1
1.17
1
308.15
5
2
0.5168
4
1
792.67
5
1
1.17
1
308.15
5
2
0.5828
4
1
792.27
5
1
1.13
1
308.15
5
2
0.6471
4
1
791.89
5
1
1.17
1
308.15
5
2
0.7097
4
1
791.52
5
1
1.18
1
308.15
5
2
0.7707
4
1
791.15
5
1
1.18
1
308.15
5
2
0.8302
4
1
790.79
5
1
1.18
1
308.15
5
2
0.8882
4
1
790.44
5
1
1.19
1
308.15
5
2
0.9448
4
1
790.1
5
1
1.19
1
308.15
5
2
1
5
1
789.78
5
1
1.19
1
313.15
5
2
0
2
1
791.21
5
1
1.18
1
313.15
5
2
0.0803
3
1
790.63
5
1
1.18
1
313.15
5
2
0.1583
4
1
790.09
5
1
1.19
1
313.15
5
2
0.2341
4
1
789.57
5
1
1.19
1
313.15
5
2
0.3077
4
1
789.06
5
1
1.2
1
313.15
5
2
0.3794
4
1
788.57
5
1
1.2
1
313.15
5
2
0.449
4
1
788.09
5
1
1.2
1
313.15
5
2
0.5168
4
1
787.63
5
1
1.21
1
313.15
5
2
0.5828
4
1
787.18
5
1
1.21
1
313.15
5
2
0.6471
4
1
786.74
5
1
1.22
1
313.15
5
2
0.7097
4
1
786.32
5
1
1.22
1
313.15
5
2
0.7707
4
1
785.9
5
1
1.22
1
313.15
5
2
0.8302
4
1
785.49
5
1
1.23
1
313.15
5
2
0.8882
4
1
785.09
5
1
1.23
1
313.15
5
2
0.9448
4
1
784.7
5
1
1.24
1
313.15
5
2
1
5
1
784.32
5
1
1.24