2
0
2009
dom
nev
0
journal
Original
Domanska, U.[Urszula]
Nevines, A.[Ashley]
Laskowska, M.[Marta]
Thermochim. Acta
2009
2020-09-29
Temperature and composition dependence of the density and viscosity of binary mixtures of (1-decanol + fragrance material)
Density and viscosity were determined for binary mixtures containing 1-decanol and three fragrance raw materials based on cyclohexane: cyclohexyl carboxylic acid (CCA), or cyclohexyl acetate (CA), or 2-cyclohexyl ethyl acetate (2CEA) in wide range of temperatures from 300 to 340K and atmospheric pressure. Excess molar volumes were calculated and correlated by the Redlich Kister polynomial expansions involving parameters dependent on temperature for the mixtures. The polynomial correlations describe the variation of density and viscosity with composition. The coefficient of thermal expansion, ^2 was described for all pure fragrance rawmaterials and their mixtures and related excess property has been calculated. The temperature dependence of density and viscosity for these systems can be described by an empirical second-order polynomial and by the Vogel Fulcher Tammann equation, respectively. Comparison of the results for three binary systems elucidates the influence of the substituent at the cyclohexane ring on their physical and volumetric properties.
1-Decanol
Fragrance materials
Physico-chemical properties
Experimental densities and viscosities
Excess molar volumes
Volume expansivities
Excess volume expansivities
Correlation
10.1016/j.tca.2009.02.013
1-2
491
10-19
1
InChI=1S/C7H12O2/c8-7(9)6-4-2-1-3-5-6/h6H,1-5H2,(H,8,9)
NZNMSOFKMUBTKW-UHFFFAOYSA-N
cyclohexanecarboxylic acid
C7H12O2
1
Commercial source
1
98
2
Stated by supplier
2
InChI=1S/C8H14O2/c1-7(9)10-8-5-3-2-4-6-8/h8H,2-6H2,1H3
YYLLIJHXUHJATK-UHFFFAOYSA-N
cyclohexyl ethanoate
acetic acid, cyclohexyl ester
cyclohexyl acetate
ethanoic acid, cyclohexyl ester
C8H14O2
1
Commercial source
1
98
2
Stated by supplier
3
InChI=1S/C10H18O2/c1-9(11)12-8-7-10-5-3-2-4-6-10/h10H,2-8H2,1H3
NOTFZGFABLVTIG-UHFFFAOYSA-N
cyclohexylethyl acetate
C10H18O2
1
Commercial source
1
98
2
Stated by supplier
4
InChI=1S/C10H22O/c1-2-3-4-5-6-7-8-9-10-11/h11H,2-10H2,1H3
MWKFXSUHUHTGQN-UHFFFAOYSA-N
decan-1-ol
1-decanol
decyl alcohol
n-decyl alcohol
C10H22O
1
Commercial source
1
99.8
3
Stated by supplier
2
Fractional distillation
1
1
1
Principal objective of the work
TRC
VVD
7/15/2009
1
Viscosity, Pa*s
Falling or rolling sphere viscometry
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
310
2
1
0.0132
3
1
0.0002
1
320
2
1
0.00926
3
1
0.00015
1
330
2
1
0.00676
3
1
0.00011
1
340
2
1
0.00507
3
1
8e-05
2
1
1
Principal objective of the work
TRC
VVD
7/15/2009
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
310
2
1
1017.17
6
1
0.87
1
320
2
1
1008.77
6
1
0.86
1
330
2
1
1000.4
6
1
0.84
1
340
2
1
992.03
5
1
0.83
3
2
1
Principal objective of the work
TRC
VVD
7/15/2009
1
Viscosity, Pa*s
Falling or rolling sphere viscometry
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
300
1
1
0.00195
3
1
3e-05
1
310
2
1
0.00161
3
1
3e-05
1
320
2
1
0.00136
3
1
2e-05
1
330
2
1
0.00116
3
1
2e-05
1
340
2
1
0.00101
3
1
2e-05
4
2
1
Principal objective of the work
TRC
VVD
7/15/2009
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
300
1
1
963.57
5
1
0.79
1
310
2
1
953.9
5
1
0.78
1
320
2
1
944.17
5
1
0.77
1
330
2
1
934.41
5
1
0.76
1
340
2
1
924.64
5
1
0.75
5
3
1
Principal objective of the work
TRC
VVD
7/15/2009
1
Viscosity, Pa*s
Falling or rolling sphere viscometry
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
300
1
1
0.00254
3
1
4e-05
1
310
2
1
0.00207
3
1
3e-05
1
320
2
1
0.00172
3
1
3e-05
1
330
2
1
0.00146
3
1
2e-05
1
340
2
1
0.00126
3
1
2e-05
6
3
1
Principal objective of the work
TRC
VVD
7/15/2009
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
300
1
1
943.64
5
1
0.77
1
310
2
1
935.03
5
1
0.76
1
320
2
1
926.43
5
1
0.75
1
330
2
1
917.82
5
1
0.74
1
340
2
1
909.17
5
1
0.73
7
4
1
Principal objective of the work
TRC
VVD
7/15/2009
1
Viscosity, Pa*s
Falling or rolling sphere viscometry
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
300
1
1
0.0103
4
1
0.00013
1
310
2
1
0.00709
3
1
9e-05
1
320
2
1
0.005
3
1
6e-05
1
330
2
1
0.00367
3
1
5e-05
1
340
2
1
0.00274
3
1
3e-05
8
4
1
Principal objective of the work
TRC
VVD
7/15/2009
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
300
1
1
825.13
5
1
0.14
1
310
2
1
818.26
5
1
0.14
1
320
2
1
811.33
5
1
0.14
1
330
2
1
804.31
5
1
0.14
1
340
2
1
797.15
5
1
0.15
9
1
1
4
1
Principal objective of the work
RJB
TRC
7/15/2009
1
Viscosity, Pa*s
Falling or rolling sphere viscometry
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
310
2
2
0
2
1
0.0132
3
1
0.0002
1
310
2
2
0.0377
3
1
0.0121
3
1
0.0002
1
310
2
2
0.0625
3
1
0.0118
3
1
0.0002
1
310
2
2
0.1776
4
1
0.0106
3
1
0.0002
1
310
2
2
0.2753
4
1
0.00961
3
1
0.00014
1
310
2
2
0.4103
4
1
0.00879
3
1
0.00012
1
310
2
2
0.4952
4
1
0.00845
3
1
0.00011
1
310
2
2
0.5659
4
1
0.00815
3
1
0.00011
1
310
2
2
0.6678
4
1
0.00786
3
1
0.0001
1
310
2
2
0.7657
4
1
0.0077
3
1
0.0001
1
310
2
2
0.8462
4
1
0.00748
3
1
9e-05
1
310
2
2
0.9063
4
1
0.00743
3
1
9e-05
1
310
2
2
0.9593
4
1
0.00741
3
1
9e-05
1
310
2
2
1
5
1
0.00709
3
1
9e-05
1
320
2
2
0
2
1
0.00926
3
1
0.00015
1
320
2
2
0.0377
3
1
0.00854
3
1
0.00013
1
320
2
2
0.0625
3
1
0.00832
3
1
0.00013
1
320
2
2
0.1776
4
1
0.00757
3
1
0.00011
1
320
2
2
0.2753
4
1
0.00694
3
1
0.0001
1
320
2
2
0.4103
4
1
0.00639
3
1
9e-05
1
320
2
2
0.4952
4
1
0.00615
3
1
8e-05
1
320
2
2
0.5659
4
1
0.00594
3
1
8e-05
1
320
2
2
0.6678
4
1
0.00572
3
1
7e-05
1
320
2
2
0.7657
4
1
0.0056
3
1
7e-05
1
320
2
2
0.8462
4
1
0.00548
3
1
7e-05
1
320
2
2
0.9063
4
1
0.00536
3
1
7e-05
1
320
2
2
0.9593
4
1
0.0053
3
1
7e-05
1
320
2
2
1
5
1
0.005
3
1
6e-05
1
330
2
2
0
2
1
0.00676
3
1
0.00011
1
330
2
2
0.0377
3
1
0.00629
3
1
0.0001
1
330
2
2
0.0625
3
1
0.00613
3
1
0.0001
1
330
2
2
0.1776
4
1
0.00565
3
1
8e-05
1
330
2
2
0.2753
4
1
0.00519
3
1
7e-05
1
330
2
2
0.4103
4
1
0.0048
3
1
7e-05
1
330
2
2
0.4952
4
1
0.00463
3
1
6e-05
1
330
2
2
0.5659
4
1
0.00447
3
1
6e-05
1
330
2
2
0.6678
4
1
0.0043
3
1
6e-05
1
330
2
2
0.7657
4
1
0.0042
3
1
5e-05
1
330
2
2
0.8462
4
1
0.00412
3
1
5e-05
1
330
2
2
0.9063
4
1
0.004
3
1
5e-05
1
330
2
2
0.9593
4
1
0.00399
3
1
5e-05
1
330
2
2
1
5
1
0.00367
3
1
5e-05
1
340
2
2
0
2
1
0.00507
3
1
8e-05
1
340
2
2
0.0377
3
1
0.00481
3
1
8e-05
1
340
2
2
0.0625
3
1
0.0047
3
1
7e-05
1
340
2
2
0.1776
4
1
0.00435
3
1
6e-05
1
340
2
2
0.2753
4
1
0.00404
3
1
6e-05
1
340
2
2
0.4103
4
1
0.00372
3
1
5e-05
1
340
2
2
0.4952
4
1
0.00358
3
1
5e-05
1
340
2
2
0.5659
4
1
0.00345
3
1
5e-05
1
340
2
2
0.6678
4
1
0.00332
3
1
4e-05
1
340
2
2
0.7657
4
1
0.00323
3
1
4e-05
1
340
2
2
0.8462
4
1
0.00317
3
1
4e-05
1
340
2
2
0.9063
4
1
0.00307
3
1
4e-05
1
340
2
2
0.9593
4
1
0.00306
3
1
4e-05
1
340
2
2
1
5
1
0.00274
3
1
3e-05
10
1
1
4
1
Principal objective of the work
RJB
TRC
7/15/2009
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
4
Liquid
1
310
2
2
0
2
1
1017.17
6
1
0.87
1
310
2
2
0.0377
3
1
1005.93
6
1
0.79
1
310
2
2
0.0625
3
1
998.87
5
1
0.75
1
310
2
2
0.1776
4
1
968.18
5
1
0.58
1
310
2
2
0.2753
4
1
944.78
5
1
0.46
1
310
2
2
0.4103
4
1
915.49
5
1
0.34
1
310
2
2
0.4952
4
1
898.67
5
1
0.28
1
310
2
2
0.5659
4
1
885.48
5
1
0.24
1
310
2
2
0.6678
4
1
867.76
5
1
0.2
1
310
2
2
0.7657
4
1
851.98
5
1
0.17
1
310
2
2
0.8462
4
1
839.8
5
1
0.15
1
310
2
2
0.9063
4
1
831.11
5
1
0.15
1
310
2
2
0.9593
4
1
823.73
5
1
0.14
1
310
2
2
1
5
1
818.26
5
1
0.14
1
320
2
2
0
2
1
1008.77
6
1
0.86
1
320
2
2
0.0377
3
1
997.64
5
1
0.78
1
320
2
2
0.0625
3
1
990.64
5
1
0.74
1
320
2
2
0.1776
4
1
960.23
5
1
0.57
1
320
2
2
0.2753
4
1
937.02
5
1
0.46
1
320
2
2
0.4103
4
1
907.93
5
1
0.34
1
320
2
2
0.4952
4
1
891.24
5
1
0.28
1
320
2
2
0.5659
4
1
878.13
5
1
0.24
1
320
2
2
0.6678
4
1
860.52
5
1
0.2
1
320
2
2
0.7657
4
1
844.86
5
1
0.17
1
320
2
2
0.8462
4
1
832.74
5
1
0.16
1
320
2
2
0.9063
4
1
824.11
5
1
0.15
1
320
2
2
0.9593
4
1
816.78
5
1
0.14
1
320
2
2
1
5
1
811.33
5
1
0.14
1
330
2
2
0
2
1
1000.4
6
1
0.84
1
330
2
2
0.0377
3
1
989.37
5
1
0.77
1
330
2
2
0.0625
3
1
982.42
5
1
0.73
1
330
2
2
0.1776
4
1
952.28
5
1
0.56
1
330
2
2
0.2753
4
1
929.25
5
1
0.45
1
330
2
2
0.4103
4
1
900.36
5
1
0.34
1
330
2
2
0.4952
4
1
883.77
5
1
0.28
1
330
2
2
0.5659
4
1
870.74
5
1
0.24
1
330
2
2
0.6678
4
1
853.23
5
1
0.2
1
330
2
2
0.7657
4
1
837.65
5
1
0.17
1
330
2
2
0.8462
4
1
825.61
5
1
0.16
1
330
2
2
0.9063
4
1
817.02
5
1
0.15
1
330
2
2
0.9593
4
1
809.74
5
1
0.15
1
330
2
2
1
5
1
804.31
5
1
0.14
1
340
2
2
0
2
1
992.03
5
1
0.83
1
340
2
2
0.0377
3
1
981.1
5
1
0.76
1
340
2
2
0.0625
3
1
974.22
5
1
0.72
1
340
2
2
0.1776
4
1
944.31
5
1
0.56
1
340
2
2
0.2753
4
1
921.45
5
1
0.45
1
340
2
2
0.4103
4
1
892.75
5
1
0.34
1
340
2
2
0.4952
4
1
876.25
5
1
0.28
1
340
2
2
0.5659
4
1
863.29
5
1
0.24
1
340
2
2
0.6678
4
1
845.89
5
1
0.2
1
340
2
2
0.7657
4
1
830.36
5
1
0.17
1
340
2
2
0.8462
4
1
818.36
5
1
0.16
1
340
2
2
0.9063
4
1
809.82
5
1
0.15
1
340
2
2
0.9593
4
1
802.6
5
1
0.15
1
340
2
2
1
5
1
797.15
5
1
0.15
11
4
1
2
1
Principal objective of the work
RJB
TRC
7/15/2009
1
Viscosity, Pa*s
Falling or rolling sphere viscometry
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
300
1
2
0
2
1
0.00195
3
1
3e-05
1
300
1
2
0.0746
3
1
0.00201
3
1
3e-05
1
300
1
2
0.1275
4
1
0.00211
3
1
3e-05
1
300
1
2
0.184
4
1
0.00226
3
1
3e-05
1
300
1
2
0.2015
4
1
0.0023
3
1
3e-05
1
300
1
2
0.2425
4
1
0.00242
3
1
4e-05
1
300
1
2
0.2741
4
1
0.00254
3
1
4e-05
1
300
1
2
0.4169
4
1
0.00315
3
1
4e-05
1
300
1
2
0.4886
4
1
0.00361
3
1
5e-05
1
300
1
2
0.6055
4
1
0.00441
3
1
6e-05
1
300
1
2
0.6993
4
1
0.00527
3
1
7e-05
1
300
1
2
0.8435
4
1
0.00756
3
1
9e-05
1
300
1
2
0.8806
4
1
0.00817
3
1
0.0001
1
300
1
2
1
5
1
0.0103
4
1
0.00013
1
310
2
2
0
2
1
0.00161
3
1
3e-05
1
310
2
2
0.0746
3
1
0.00165
3
1
3e-05
1
310
2
2
0.1275
4
1
0.00172
3
1
3e-05
1
310
2
2
0.184
4
1
0.00182
3
1
3e-05
1
310
2
2
0.2015
4
1
0.00186
3
1
3e-05
1
310
2
2
0.2425
4
1
0.00195
3
1
3e-05
1
310
2
2
0.2741
4
1
0.00203
3
1
3e-05
1
310
2
2
0.4169
4
1
0.00247
3
1
3e-05
1
310
2
2
0.4886
4
1
0.00281
3
1
4e-05
1
310
2
2
0.6055
4
1
0.00335
3
1
4e-05
1
310
2
2
0.6993
4
1
0.00395
3
1
5e-05
1
310
2
2
0.8435
4
1
0.00549
3
1
7e-05
1
310
2
2
0.8806
4
1
0.00585
3
1
7e-05
1
310
2
2
1
5
1
0.00709
3
1
9e-05
1
320
2
2
0
2
1
0.00136
3
1
2e-05
1
320
2
2
0.0746
3
1
0.00138
3
1
2e-05
1
320
2
2
0.1275
4
1
0.00143
3
1
2e-05
1
320
2
2
0.184
4
1
0.00151
3
1
2e-05
1
320
2
2
0.2015
4
1
0.00155
3
1
2e-05
1
320
2
2
0.2425
4
1
0.0016
3
1
2e-05
1
320
2
2
0.2741
4
1
0.00166
3
1
2e-05
1
320
2
2
0.4169
4
1
0.00198
3
1
3e-05
1
320
2
2
0.4886
4
1
0.00223
3
1
3e-05
1
320
2
2
0.6055
4
1
0.00262
3
1
3e-05
1
320
2
2
0.6993
4
1
0.00304
3
1
4e-05
1
320
2
2
0.8435
4
1
0.0041
3
1
5e-05
1
320
2
2
0.8806
4
1
0.00437
3
1
5e-05
1
320
2
2
1
5
1
0.005
3
1
6e-05
1
330
2
2
0
2
1
0.00116
3
1
2e-05
1
330
2
2
0.0746
3
1
0.00117
3
1
2e-05
1
330
2
2
0.1275
4
1
0.00121
3
1
2e-05
1
330
2
2
0.184
4
1
0.00127
3
1
2e-05
1
330
2
2
0.2015
4
1
0.0013
3
1
2e-05
1
330
2
2
0.2425
4
1
0.00134
3
1
2e-05
1
330
2
2
0.2741
4
1
0.00139
3
1
2e-05
1
330
2
2
0.4169
4
1
0.00163
3
1
2e-05
1
330
2
2
0.4886
4
1
0.00181
3
1
3e-05
1
330
2
2
0.6055
4
1
0.00209
3
1
3e-05
1
330
2
2
0.6993
4
1
0.00239
3
1
3e-05
1
330
2
2
0.8435
4
1
0.00314
3
1
4e-05
1
330
2
2
0.8806
4
1
0.00334
3
1
4e-05
1
330
2
2
1
5
1
0.00367
3
1
5e-05
1
340
2
2
0
2
1
0.00101
3
1
2e-05
1
340
2
2
0.0746
3
1
0.00102
3
1
2e-05
1
340
2
2
0.1275
4
1
0.00105
3
1
2e-05
1
340
2
2
0.184
4
1
0.00109
3
1
2e-05
1
340
2
2
0.2015
4
1
0.0011
3
1
2e-05
1
340
2
2
0.2425
4
1
0.00114
3
1
2e-05
1
340
2
2
0.2741
4
1
0.00118
3
1
2e-05
1
340
2
2
0.4169
4
1
0.00136
3
1
2e-05
1
340
2
2
0.4886
4
1
0.00149
3
1
2e-05
1
340
2
2
0.6055
4
1
0.0017
3
1
2e-05
1
340
2
2
0.6993
4
1
0.00192
3
1
3e-05
1
340
2
2
0.8435
4
1
0.00247
3
1
3e-05
1
340
2
2
0.8806
4
1
0.00261
3
1
3e-05
1
340
2
2
1
5
1
0.00274
3
1
3e-05
12
4
1
2
1
Principal objective of the work
RJB
TRC
7/15/2009
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
4
Liquid
1
300
1
2
0
2
1
963.57
5
1
0.79
1
300
1
2
0.0746
3
1
949.18
5
1
0.68
1
300
1
2
0.1275
4
1
939.64
5
1
0.61
1
300
1
2
0.184
4
1
929.88
5
1
0.54
1
300
1
2
0.2015
4
1
926.89
5
1
0.52
1
300
1
2
0.2425
4
1
920.06
5
1
0.48
1
300
1
2
0.2741
4
1
915.03
5
1
0.45
1
300
1
2
0.4169
4
1
893.64
5
1
0.33
1
300
1
2
0.4886
4
1
883.66
5
1
0.28
1
300
1
2
0.6055
4
1
868.47
5
1
0.22
1
300
1
2
0.6993
4
1
857.06
5
1
0.19
1
300
1
2
0.8435
4
1
840.97
5
1
0.15
1
300
1
2
0.8806
4
1
837.03
5
1
0.15
1
300
1
2
1
5
1
825.13
5
1
0.14
1
310
2
2
0
2
1
953.9
5
1
0.78
1
310
2
2
0.0746
3
1
939.8
5
1
0.67
1
310
2
2
0.1275
4
1
930.43
5
1
0.6
1
310
2
2
0.184
4
1
920.86
5
1
0.54
1
310
2
2
0.2015
4
1
917.91
5
1
0.52
1
310
2
2
0.2425
4
1
911.24
5
1
0.47
1
310
2
2
0.2741
4
1
906.31
5
1
0.44
1
310
2
2
0.4169
4
1
885.38
5
1
0.32
1
310
2
2
0.4886
4
1
875.61
5
1
0.28
1
310
2
2
0.6055
4
1
860.73
5
1
0.22
1
310
2
2
0.6993
4
1
849.55
5
1
0.19
1
310
2
2
0.8435
4
1
833.83
5
1
0.16
1
310
2
2
0.8806
4
1
829.95
5
1
0.15
1
310
2
2
1
5
1
818.26
5
1
0.14
1
320
2
2
0
2
1
944.17
5
1
0.77
1
320
2
2
0.0746
3
1
930.36
5
1
0.66
1
320
2
2
0.1275
4
1
921.2
5
1
0.6
1
320
2
2
0.184
4
1
911.8
5
1
0.53
1
320
2
2
0.2015
4
1
908.94
5
1
0.51
1
320
2
2
0.2425
4
1
902.38
5
1
0.47
1
320
2
2
0.2741
4
1
897.62
5
1
0.44
1
320
2
2
0.4169
4
1
877.06
5
1
0.32
1
320
2
2
0.4886
4
1
867.5
5
1
0.28
1
320
2
2
0.6055
4
1
852.93
5
1
0.22
1
320
2
2
0.6993
4
1
841.99
5
1
0.19
1
320
2
2
0.8435
4
1
826.58
5
1
0.16
1
320
2
2
0.8806
4
1
822.79
5
1
0.15
1
320
2
2
1
5
1
811.33
5
1
0.14
1
330
2
2
0
2
1
934.41
5
1
0.76
1
330
2
2
0.0746
3
1
920.89
5
1
0.66
1
330
2
2
0.1275
4
1
911.92
5
1
0.59
1
330
2
2
0.184
4
1
902.71
5
1
0.52
1
330
2
2
0.2015
4
1
899.91
5
1
0.51
1
330
2
2
0.2425
4
1
893.48
5
1
0.46
1
330
2
2
0.2741
4
1
888.82
5
1
0.43
1
330
2
2
0.4169
4
1
868.7
5
1
0.32
1
330
2
2
0.4886
4
1
859.33
5
1
0.28
1
330
2
2
0.6055
4
1
845.1
5
1
0.22
1
330
2
2
0.6993
4
1
834.37
5
1
0.19
1
330
2
2
0.8435
4
1
819.26
5
1
0.16
1
330
2
2
0.8806
4
1
815.55
5
1
0.15
1
330
2
2
1
5
1
804.31
5
1
0.14
1
340
2
2
0
2
1
924.64
5
1
0.75
1
340
2
2
0.0746
3
1
911.39
5
1
0.65
1
340
2
2
0.1275
4
1
902.57
5
1
0.58
1
340
2
2
0.184
4
1
893.57
5
1
0.52
1
340
2
2
0.2015
4
1
890.81
5
1
0.5
1
340
2
2
0.2425
4
1
884.52
5
1
0.46
1
340
2
2
0.2741
4
1
879.96
5
1
0.43
1
340
2
2
0.4169
4
1
860.25
5
1
0.32
1
340
2
2
0.4886
4
1
851.09
5
1
0.28
1
340
2
2
0.6055
4
1
837.14
5
1
0.22
1
340
2
2
0.6993
4
1
826.63
5
1
0.19
1
340
2
2
0.8435
4
1
811.81
5
1
0.16
1
340
2
2
0.8806
4
1
808.17
5
1
0.16
1
340
2
2
1
5
1
797.15
5
1
0.15
13
4
1
3
1
Principal objective of the work
RJB
TRC
7/15/2009
1
Viscosity, Pa*s
Falling or rolling sphere viscometry
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
300
1
2
0
2
1
0.00254
3
1
4e-05
1
300
1
2
0.1066
4
1
0.00265
3
1
4e-05
1
300
1
2
0.1534
4
1
0.00274
3
1
4e-05
1
300
1
2
0.2863
4
1
0.00294
3
1
4e-05
1
300
1
2
0.337
4
1
0.00314
3
1
4e-05
1
300
1
2
0.4105
4
1
0.00347
3
1
5e-05
1
300
1
2
0.4983
4
1
0.00391
3
1
5e-05
1
300
1
2
0.5476
4
1
0.00425
3
1
6e-05
1
300
1
2
0.6306
4
1
0.00492
3
1
6e-05
1
300
1
2
0.702
4
1
0.00557
3
1
7e-05
1
300
1
2
0.7382
4
1
0.00593
3
1
8e-05
1
300
1
2
0.8402
4
1
0.00722
3
1
9e-05
1
300
1
2
0.9332
4
1
0.00892
3
1
0.00011
1
300
1
2
1
5
1
0.0103
4
1
0.00013
1
310
2
2
0
2
1
0.00207
3
1
3e-05
1
310
2
2
0.1066
4
1
0.00214
3
1
3e-05
1
310
2
2
0.1534
4
1
0.0022
3
1
3e-05
1
310
2
2
0.2863
4
1
0.00234
3
1
3e-05
1
310
2
2
0.337
4
1
0.00246
3
1
4e-05
1
310
2
2
0.4105
4
1
0.00272
3
1
4e-05
1
310
2
2
0.4983
4
1
0.00302
3
1
4e-05
1
310
2
2
0.5476
4
1
0.00326
3
1
4e-05
1
310
2
2
0.6306
4
1
0.00376
3
1
5e-05
1
310
2
2
0.702
4
1
0.00415
3
1
5e-05
1
310
2
2
0.7382
4
1
0.0044
3
1
6e-05
1
310
2
2
0.8402
4
1
0.00525
3
1
7e-05
1
310
2
2
0.9332
4
1
0.00635
3
1
8e-05
1
310
2
2
1
5
1
0.00709
3
1
9e-05
1
320
2
2
0
2
1
0.00172
3
1
3e-05
1
320
2
2
0.1066
4
1
0.00177
3
1
3e-05
1
320
2
2
0.1534
4
1
0.00182
3
1
3e-05
1
320
2
2
0.2863
4
1
0.00191
3
1
3e-05
1
320
2
2
0.337
4
1
0.00201
3
1
3e-05
1
320
2
2
0.4105
4
1
0.00215
3
1
3e-05
1
320
2
2
0.4983
4
1
0.00241
3
1
3e-05
1
320
2
2
0.5476
4
1
0.00256
3
1
3e-05
1
320
2
2
0.6306
4
1
0.00293
3
1
4e-05
1
320
2
2
0.702
4
1
0.00318
3
1
4e-05
1
320
2
2
0.7382
4
1
0.00337
3
1
4e-05
1
320
2
2
0.8402
4
1
0.00394
3
1
5e-05
1
320
2
2
0.9332
4
1
0.00467
3
1
6e-05
1
320
2
2
1
5
1
0.005
3
1
6e-05
1
330
2
2
0
2
1
0.00146
3
1
2e-05
1
330
2
2
0.1066
4
1
0.00149
3
1
2e-05
1
330
2
2
0.1534
4
1
0.00153
3
1
2e-05
1
330
2
2
0.2863
4
1
0.00159
3
1
2e-05
1
330
2
2
0.337
4
1
0.00165
3
1
2e-05
1
330
2
2
0.4105
4
1
0.00176
3
1
2e-05
1
330
2
2
0.4983
4
1
0.00194
3
1
3e-05
1
330
2
2
0.5476
4
1
0.00207
3
1
3e-05
1
330
2
2
0.6306
4
1
0.00232
3
1
3e-05
1
330
2
2
0.702
4
1
0.0025
3
1
3e-05
1
330
2
2
0.7382
4
1
0.00264
3
1
3e-05
1
330
2
2
0.8402
4
1
0.00302
3
1
4e-05
1
330
2
2
0.9332
4
1
0.00353
3
1
4e-05
1
330
2
2
1
5
1
0.00367
3
1
5e-05
1
340
2
2
0
2
1
0.00126
3
1
2e-05
1
340
2
2
0.1066
4
1
0.00128
3
1
2e-05
1
340
2
2
0.1534
4
1
0.00131
3
1
2e-05
1
340
2
2
0.2863
4
1
0.00134
3
1
2e-05
1
340
2
2
0.337
4
1
0.00139
3
1
2e-05
1
340
2
2
0.4105
4
1
0.00144
3
1
2e-05
1
340
2
2
0.4983
4
1
0.00161
3
1
2e-05
1
340
2
2
0.5476
4
1
0.0017
3
1
2e-05
1
340
2
2
0.6306
4
1
0.00188
3
1
3e-05
1
340
2
2
0.702
4
1
0.00201
3
1
3e-05
1
340
2
2
0.7382
4
1
0.00212
3
1
3e-05
1
340
2
2
0.8402
4
1
0.00238
3
1
3e-05
1
340
2
2
0.9332
4
1
0.00272
3
1
3e-05
1
340
2
2
1
5
1
0.00274
3
1
3e-05
14
4
1
3
1
Principal objective of the work
RJB
TRC
7/15/2009
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
4
Liquid
1
300
1
2
0
2
1
943.64
5
1
0.77
1
300
1
2
0.1066
4
1
929.42
5
1
0.63
1
300
1
2
0.1534
4
1
923.37
5
1
0.57
1
300
1
2
0.2863
4
1
906.56
5
1
0.43
1
300
1
2
0.337
4
1
900.31
5
1
0.39
1
300
1
2
0.4105
4
1
891.39
5
1
0.33
1
300
1
2
0.4983
4
1
880.9
5
1
0.27
1
300
1
2
0.5476
4
1
875.09
5
1
0.24
1
300
1
2
0.6306
4
1
865.45
5
1
0.21
1
300
1
2
0.702
4
1
857.32
5
1
0.18
1
300
1
2
0.7382
4
1
853.32
5
1
0.17
1
300
1
2
0.8402
4
1
842.12
5
1
0.15
1
300
1
2
0.9332
4
1
832.17
5
1
0.14
1
300
1
2
1
5
1
825.13
5
1
0.14
1
310
2
2
0
2
1
935.03
5
1
0.76
1
310
2
2
0.1066
4
1
921
5
1
0.62
1
310
2
2
0.1534
4
1
915.03
5
1
0.56
1
310
2
2
0.2863
4
1
898.44
5
1
0.43
1
310
2
2
0.337
4
1
892.31
5
1
0.38
1
310
2
2
0.4105
4
1
883.51
5
1
0.33
1
310
2
2
0.4983
4
1
873.2
5
1
0.27
1
310
2
2
0.5476
4
1
867.47
5
1
0.24
1
310
2
2
0.6306
4
1
857.95
5
1
0.21
1
310
2
2
0.702
4
1
849.92
5
1
0.19
1
310
2
2
0.7382
4
1
846.02
5
1
0.18
1
310
2
2
0.8402
4
1
835
5
1
0.16
1
310
2
2
0.9332
4
1
825.2
5
1
0.14
1
310
2
2
1
5
1
818.26
5
1
0.14
1
320
2
2
0
2
1
926.43
5
1
0.75
1
320
2
2
0.1066
4
1
912.57
5
1
0.61
1
320
2
2
0.1534
4
1
906.67
5
1
0.56
1
320
2
2
0.2863
4
1
890.31
5
1
0.42
1
320
2
2
0.337
4
1
884.26
5
1
0.38
1
320
2
2
0.4105
4
1
875.59
5
1
0.33
1
320
2
2
0.4983
4
1
865.44
5
1
0.27
1
320
2
2
0.5476
4
1
859.81
5
1
0.24
1
320
2
2
0.6306
4
1
850.45
5
1
0.21
1
320
2
2
0.702
4
1
842.53
5
1
0.19
1
320
2
2
0.7382
4
1
838.68
5
1
0.18
1
320
2
2
0.8402
4
1
827.83
5
1
0.16
1
320
2
2
0.9332
4
1
818.17
5
1
0.15
1
320
2
2
1
5
1
811.33
5
1
0.14
1
330
2
2
0
2
1
917.82
5
1
0.74
1
330
2
2
0.1066
4
1
904.11
5
1
0.61
1
330
2
2
0.1534
4
1
898.29
5
1
0.55
1
330
2
2
0.2863
4
1
882.13
5
1
0.42
1
330
2
2
0.337
4
1
876.16
5
1
0.38
1
330
2
2
0.4105
4
1
867.62
5
1
0.32
1
330
2
2
0.4983
4
1
857.61
5
1
0.27
1
330
2
2
0.5476
4
1
852.05
5
1
0.24
1
330
2
2
0.6306
4
1
842.85
5
1
0.21
1
330
2
2
0.702
4
1
835.03
5
1
0.19
1
330
2
2
0.7382
4
1
831.25
5
1
0.18
1
330
2
2
0.8402
4
1
820.58
5
1
0.16
1
330
2
2
0.9332
4
1
811.05
5
1
0.15
1
330
2
2
1
5
1
804.31
5
1
0.14
1
340
2
2
0
2
1
909.17
5
1
0.73
1
340
2
2
0.1066
4
1
895.64
5
1
0.6
1
340
2
2
0.1534
4
1
889.87
5
1
0.55
1
340
2
2
0.2863
4
1
873.9
5
1
0.42
1
340
2
2
0.337
4
1
867.98
5
1
0.38
1
340
2
2
0.4105
4
1
859.59
5
1
0.32
1
340
2
2
0.4983
4
1
849.71
5
1
0.27
1
340
2
2
0.5476
4
1
844.24
5
1
0.24
1
340
2
2
0.6306
4
1
835.15
5
1
0.21
1
340
2
2
0.702
4
1
827.46
5
1
0.19
1
340
2
2
0.7382
4
1
823.73
5
1
0.18
1
340
2
2
0.8402
4
1
813.21
5
1
0.16
1
340
2
2
0.9332
4
1
803.8
5
1
0.15
1
340
2
2
1
5
1
797.15
5
1
0.15