2
0
2019
dom
kro
0
journal
Original
Domaska, U.[Urszula]
Krolikowska, M.[Marta]
Pobudkowska, A.[Aneta]
Krolikowski, M.[Marek]
Wickowski, M.[Mikoaj]
Fluid Phase Equilib.
2019
2020-09-29
Physico-chemical properties of ionic liquids: density, viscosity, density at high pressure, surface tension, octan-1-ol/water partition coefficients and thermodynamic models
Ionic liquids (ILs) are an important new media and one of the most attractive solvents used in extraction and separation processes. This work presents some important physico-chemical properties and topics related to ILs, which were found by us as good extractive solvents for the desulfurization of fuels and for the separation of water/biobutan-1-ol. It consists of the most important series of experimental measurements of density and viscosity of pure ILs and in binary systems with thiophene and butan-1-ol: (N-hydroxyethylpyridinium tricyanomethanide, [C2OHPy][TCM] + thiophene), or (N-hydroxypropylpyridinium tricyanomethanide, [C3OHPy][TCM] + thiophene) or (N-benzyl-N-dodecyl-N,Ndimethylammonium bis(trifluoromethyl-sulfonyl)imide, [N1,1,12,Bz][NTf2] + butan-1-ol). These systems exhibit mainly negative molar excess volumes, V^E in systems with thiophene and slightly positive and negative in the system with butan-1-ol. The Redlich Kister equation was used for correlation of the liquid density, excess molar volumes and dynamic viscosity deviations as a function of temperature and composition, whereas Vogel-Fulcher-Tammann, VFT was used for describing the temperature dependence of dynamic viscosities. Very often, the high pressure is proposed for new technologies of separation and that is why we present the influence of pressure on the density of [C2OHPy][TCM], [C3OHPy][TCM] and [N1,1,12,Bz][NTf2] in a wide range of temperature from T = (298.15 to 348.15) K and pressure from p = (0.1 to 40) MPa. The Tait equation was used for the correlation of density as a function of mole fraction, temperature, and pressure. The influence of pressure for ILs, is as usual, not significant. The thermal expansion coefficient and isothermal compressibility coefficient as a function of temperature T, and pressure p are presented. Herein, surface tension of new ILs was measured for the collection of physico-chemical properties of the ILs used in this work. Also, the octan-1-ol/water, K_ow partition coefficients in ternary liquid-liquid phase equilibrium were determined for the systems {[C2OHPy][TCM], or [C3OHPy][TCM](1) + octan-1-ol (2) + water (3)} at temperature T = 298.15 K and the discussion of the biocompatibility of the used ILs is presented.
Ionic liquids
Density
Viscosity
Density at high pressure
Surface tension
Octan-1-ol/water partition coefficient
Thermodynamic description.
10.1016/j.fluid.2019.112304
502
112304
1
InChI=1S/C4H4S/c1-2-4-5-3-1/h1-4H
YTPLMLYBLZKORZ-UHFFFAOYSA-N
thiophene
C4H4S
1
Commercial source
1
99
3
Stated by supplier
2
Molecular sieve treatment
3
99.88
4
Gas chromatography
4
0.0095
2
Karl Fischer titration
2
InChI=1S/C4H10O/c1-2-3-4-5/h5H,2-4H2,1H3
LRHPLDYGYMQRHN-UHFFFAOYSA-N
butan-1-ol
1-butanol
n-butanol
n-butyl alcohol
C4H10O
1
Commercial source
1
99.9
3
Stated by supplier
2
Molecular sieve treatment
3
0.0035
2
Karl Fischer titration
3
InChI=1S/C8H18O/c1-2-3-4-5-6-7-8-9/h9H,2-8H2,1H3
KBPLFHHGFOOTCA-UHFFFAOYSA-N
octan-1-ol
1-octanol
capryl alcohol
caprylic alcohol
n-octyl alcohol
octanol
octyl alcohol
C8H18O
1
Commercial source
1
99
2
Stated by supplier
2
Molecular sieve treatment
3
99.65
4
Gas chromatography
4
0.006
2
Karl Fischer titration
4
InChI=1S/H2O/h1H2
XLYOFNOQVPJJNP-UHFFFAOYSA-N
water
H2O
1
Commercial source
1
99.8
3
Estimated by the compiler
2
Fractional distillation
5
InChI=1S/C7H10NO.C4N3/c9-7-6-8-4-2-1-3-5-8;5-1-4(2-6)3-7/h1-5,9H,6-7H2;/q+1;-1
KQZWPPHTIVSMRA-UHFFFAOYSA-N
1-(2-hydroxyethyl)pyridinium tricyanomethanide
C11H10N4O
1
Commercial source
1
De-gassed by evacuation
2
97
2
NMR (proton)
3
0.0576
3
Karl Fischer titration
6
InChI=1S/C8H12NO.C4N3/c10-8-4-7-9-5-2-1-3-6-9;5-1-4(2-6)3-7/h1-3,5-6,10H,4,7-8H2;/q+1;-1
FSOHROIKZGMUMN-UHFFFAOYSA-N
1-(3-hydroxypropyl)pyridinium tricyanomethanide
C12H12N4O
1
Commercial source
1
De-gassed by evacuation
2
97
2
NMR (proton)
3
0.0406
3
Karl Fischer titration
7
InChI=1S/C21H38N.C2F6NO4S2/c1-4-5-6-7-8-9-10-11-12-16-19-22(2,3)20-21-17-14-13-15-18-21;3-1(4,5)14(10,11)9-15(12,13)2(6,7)8/h13-15,17-18H,4-12,16,19-20H2,1-3H3;/q+1;-1
HBXKXGIJMCROMT-UHFFFAOYSA-N
benzyldimethyldodecylammonium bis(trifluoromethylsulfonyl)imide
benzyldimethyldodecylammonium bis(trifluoromethylsulfonyl)imide [N1,1,12,Bz][NTf2]
C23H38F6N2O4S2
1
Commercial source
1
De-gassed by evacuation
2
98
2
NMR (proton)
3
0.032
3
Karl Fischer titration
1
1
1
Principal objective of the work
VVD
TRC
1/9/2020
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
293.15
5
1
1064.42
6
1
0.12
1
298.15
5
1
1058.53
6
1
0.12
1
303.15
5
1
1052.67
6
1
0.11
1
308.15
5
1
1046.69
6
1
0.11
1
313.15
5
1
1040.71
6
1
0.11
1
318.15
5
1
1034.78
6
1
0.11
1
323.15
5
1
1028.69
6
1
0.11
1
328.15
5
1
1022.51
6
1
0.11
1
333.15
5
1
1016.4
6
1
0.11
1
338.15
5
1
1010.15
6
1
0.11
1
343.15
5
1
1003.94
6
1
0.11
1
348.15
5
1
997.65
5
1
0.11
2
1
1
Principal objective of the work
VVD
TRC
1/9/2020
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
293.15
5
1
0.000653
3
1
6.5e-05
1
298.15
5
1
0.000615
3
1
6.2e-05
1
303.15
5
1
0.00058
3
1
5.8e-05
1
308.15
5
1
0.000545
3
1
5.5e-05
1
313.15
5
1
0.000518
3
1
5.2e-05
1
318.15
5
1
0.000491
3
1
4.9e-05
1
323.15
5
1
0.000464
3
1
4.7e-05
1
328.15
5
1
0.000441
3
1
4.4e-05
1
333.15
5
1
0.00042
3
1
4.2e-05
1
338.15
5
1
0.0004
3
1
4e-05
1
343.15
5
1
0.000382
3
1
3.8e-05
1
348.15
5
1
0.000364
3
1
3.7e-05
3
2
1
Principal objective of the work
VVD
TRC
1/9/2020
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
293.15
5
1
810.15
5
1
0.14
1
298.15
5
1
805.78
5
1
0.14
1
303.15
5
1
802.07
5
1
0.14
1
308.15
5
1
798.06
5
1
0.14
1
313.15
5
1
793.98
5
1
0.14
1
318.15
5
1
790.21
5
1
0.15
1
323.15
5
1
785.9
5
1
0.15
1
328.15
5
1
782.16
5
1
0.15
1
333.15
5
1
777.82
5
1
0.15
1
338.15
5
1
773.88
5
1
0.15
1
343.15
5
1
769.74
5
1
0.15
1
348.15
5
1
765.32
5
1
0.15
4
2
1
Principal objective of the work
VVD
TRC
1/9/2020
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
298.15
5
1
0.00252
4
1
0.000253
1
303.15
5
1
0.00223
4
1
0.000224
1
308.15
5
1
0.00198
4
1
0.000199
1
313.15
5
1
0.00175
4
1
0.000175
1
318.15
5
1
0.00156
4
1
0.000156
1
323.15
5
1
0.00142
4
1
0.000142
1
328.15
5
1
0.00127
4
1
0.000127
1
333.15
5
1
0.00111
4
1
0.000111
1
338.15
5
1
0.00101
4
1
0.000101
1
343.15
5
1
0.00092
3
1
9.2e-05
1
348.15
5
1
0.000845
3
1
8.5e-05
5
5
1
Principal objective of the work
JWM
JWM
1/8/2020
1
Mass density, kg/m3
Vibrating tube 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
100
1
1
1170.4
5
1
3.4
1
298.15
5
2
1000
1
1
1171.1
5
1
3.4
1
298.15
5
2
5000
1
1
1173.1
5
1
3.4
1
298.15
5
2
10000
1
1
1175.3
5
1
3.4
1
298.15
5
2
15000
2
1
1177.6
5
1
3.5
1
298.15
5
2
20000
1
1
1179.5
5
1
3.5
1
298.15
5
2
25000
2
1
1181.7
5
1
3.5
1
298.15
5
2
30000
1
1
1184
5
1
3.6
1
298.15
5
2
35000
2
1
1185.9
5
1
3.6
1
298.15
5
2
40000
1
1
1187.8
5
1
3.6
1
308.15
5
2
100
1
1
1163.5
5
1
3.3
1
308.15
5
2
1000
1
1
1164.4
5
1
3.3
1
308.15
5
2
5000
1
1
1166.1
5
1
3.4
1
308.15
5
2
10000
1
1
1168.4
5
1
3.4
1
308.15
5
2
15000
2
1
1170.5
5
1
3.4
1
308.15
5
2
20000
1
1
1172.9
5
1
3.5
1
308.15
5
2
25000
2
1
1175
5
1
3.5
1
308.15
5
2
30000
1
1
1177.2
5
1
3.5
1
308.15
5
2
35000
2
1
1179.5
5
1
3.6
1
308.15
5
2
40000
1
1
1181.2
5
1
3.6
1
318.15
5
2
100
1
1
1156.8
5
1
3.3
1
318.15
5
2
1000
1
1
1157.4
5
1
3.3
1
318.15
5
2
5000
1
1
1159.3
5
1
3.3
1
318.15
5
2
10000
1
1
1161.7
5
1
3.4
1
318.15
5
2
15000
2
1
1164.1
5
1
3.4
1
318.15
5
2
20000
1
1
1166.2
5
1
3.4
1
318.15
5
2
25000
2
1
1168.3
5
1
3.5
1
318.15
5
2
30000
1
1
1170.6
5
1
3.5
1
318.15
5
2
35000
2
1
1172.7
5
1
3.5
1
318.15
5
2
40000
1
1
1174.6
5
1
3.6
1
328.15
5
2
100
1
1
1150.1
5
1
3.3
1
328.15
5
2
1000
1
1
1150.7
5
1
3.3
1
328.15
5
2
5000
1
1
1152.7
5
1
3.3
1
328.15
5
2
10000
1
1
1155.1
5
1
3.3
1
328.15
5
2
15000
2
1
1157.5
5
1
3.4
1
328.15
5
2
20000
1
1
1159.8
5
1
3.4
1
328.15
5
2
25000
2
1
1162.1
5
1
3.4
1
328.15
5
2
30000
1
1
1164.2
5
1
3.5
1
328.15
5
2
35000
2
1
1166.2
5
1
3.5
1
328.15
5
2
40000
1
1
1168.1
5
1
3.5
1
338.15
5
2
100
1
1
1143.4
5
1
3.2
1
338.15
5
2
1000
1
1
1144.1
5
1
3.2
1
338.15
5
2
5000
1
1
1146.2
5
1
3.3
1
338.15
5
2
10000
1
1
1148.7
5
1
3.3
1
338.15
5
2
15000
2
1
1151.1
5
1
3.3
1
338.15
5
2
20000
1
1
1153.3
5
1
3.4
1
338.15
5
2
25000
2
1
1155.6
5
1
3.4
1
338.15
5
2
30000
1
1
1157.8
5
1
3.4
1
338.15
5
2
35000
2
1
1160
5
1
3.5
1
338.15
5
2
40000
1
1
1162.2
5
1
3.5
1
348.15
5
2
100
1
1
1136.8
5
1
3.2
1
348.15
5
2
1000
1
1
1137.3
5
1
3.2
1
348.15
5
2
5000
1
1
1139.5
5
1
3.2
1
348.15
5
2
10000
1
1
1142.1
5
1
3.3
1
348.15
5
2
15000
2
1
1144.5
5
1
3.3
1
348.15
5
2
20000
1
1
1146.9
5
1
3.3
1
348.15
5
2
25000
2
1
1149.1
5
1
3.4
1
348.15
5
2
30000
1
1
1151.4
5
1
3.4
1
348.15
5
2
35000
2
1
1153.4
5
1
3.4
1
348.15
5
2
40000
1
1
1155.7
5
1
3.5
1
293.15
5
2
101
3
1
1173.87
6
1
2.65
1
298.15
5
2
101
3
1
1170.41
6
1
2.64
1
303.15
5
2
101
3
1
1166.96
6
1
2.62
1
308.15
5
2
101
3
1
1163.54
6
1
2.6
1
313.15
5
2
101
3
1
1160.14
6
1
2.59
1
318.15
5
2
101
3
1
1156.75
6
1
2.57
1
323.15
5
2
101
3
1
1153.39
6
1
2.56
1
328.15
5
2
101
3
1
1150.05
6
1
2.54
1
333.15
5
2
101
3
1
1146.72
6
1
2.52
1
338.15
5
2
101
3
1
1143.41
6
1
2.51
1
343.15
5
2
101
3
1
1140.12
6
1
2.49
1
348.15
5
2
101
3
1
1136.84
6
1
2.48
6
5
1
Principal objective of the work
JWM
JWM
8/15/2019
1
Surface tension liquid-gas, N/m
Ring tensiometer
Liquid
Direct value, X
1
Data file compiler
Propagation of evaluated standard uncertainties
95
Liquid
Gas
1
Temperature, K
Liquid
1
298.15
5
1
0.05967
5
1
0.001182
1
303.15
5
1
0.05841
5
1
0.001158
1
308.15
5
1
0.05734
5
1
0.001138
1
313.15
5
1
0.056298
5
1
0.001118
1
318.15
5
1
0.055158
5
1
0.001097
1
323.15
5
1
0.05395
5
1
0.001074
1
328.15
5
1
0.05279
5
1
0.001052
7
5
1
Principal objective of the work
VVD
TRC
1/9/2020
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
293.15
5
1
0.13658
5
1
0.01444
1
298.15
5
1
0.097484
5
1
0.010059
1
303.15
5
1
0.071784
5
1
0.007303
1
308.15
5
1
0.054574
5
1
0.005521
1
313.15
5
1
0.042306
5
1
0.004289
1
318.15
5
1
0.033963
5
1
0.003443
1
323.15
5
1
0.027779
5
1
0.002816
1
328.15
5
1
0.022933
5
1
0.002325
1
333.15
5
1
0.019321
5
1
0.001959
1
338.15
5
1
0.0164
5
1
0.001662
1
343.15
5
1
0.01398
5
1
0.001417
1
348.15
5
1
0.0123
5
1
0.001247
8
6
1
Principal objective of the work
JWM
JWM
8/15/2019
1
Mass density, kg/m3
Vibrating tube method
Liquid
Direct value, X
1
Data file compiler
Propagation of evaluated standard uncertainties
95
Liquid
1
Temperature, K
Liquid
2
Pressure, kPa
Liquid
1
298.15
5
2
100
1
1
1149.6
5
1
3.3
1
298.15
5
2
1000
1
1
1150.3
5
1
3.3
1
298.15
5
2
5000
1
1
1152.3
5
1
3.3
1
298.15
5
2
10000
1
1
1154.3
5
1
3.3
1
298.15
5
2
15000
2
1
1156.7
5
1
3.4
1
298.15
5
2
20000
1
1
1158.7
5
1
3.4
1
298.15
5
2
25000
2
1
1160.9
5
1
3.4
1
298.15
5
2
30000
1
1
1162.9
5
1
3.4
1
298.15
5
2
35000
2
1
1164.9
5
1
3.5
1
298.15
5
2
40000
1
1
1167.1
5
1
3.5
1
308.15
5
2
100
1
1
1142.9
5
1
3.2
1
308.15
5
2
1000
1
1
1143.6
5
1
3.2
1
308.15
5
2
5000
1
1
1145.5
5
1
3.3
1
308.15
5
2
10000
1
1
1147.8
5
1
3.3
1
308.15
5
2
15000
2
1
1150
5
1
3.3
1
308.15
5
2
20000
1
1
1152.3
5
1
3.4
1
308.15
5
2
25000
2
1
1154.6
5
1
3.4
1
308.15
5
2
30000
1
1
1156.6
5
1
3.4
1
308.15
5
2
35000
2
1
1158.6
5
1
3.4
1
308.15
5
2
40000
1
1
1160.7
5
1
3.5
1
318.15
5
2
100
1
1
1136.3
5
1
3.2
1
318.15
5
2
1000
1
1
1136.4
5
1
3.2
1
318.15
5
2
5000
1
1
1138.2
5
1
3.2
1
318.15
5
2
10000
1
1
1140.5
5
1
3.3
1
318.15
5
2
15000
2
1
1143
5
1
3.3
1
318.15
5
2
20000
1
1
1145.2
5
1
3.3
1
318.15
5
2
25000
2
1
1147.6
5
1
3.3
1
318.15
5
2
30000
1
1
1149.7
5
1
3.4
1
318.15
5
2
35000
2
1
1151.8
5
1
3.4
1
318.15
5
2
40000
1
1
1154
5
1
3.4
1
328.15
5
2
100
1
1
1129.7
5
1
3.2
1
328.15
5
2
1000
1
1
1130.2
5
1
3.2
1
328.15
5
2
5000
1
1
1132.2
5
1
3.2
1
328.15
5
2
10000
1
1
1134.5
5
1
3.2
1
328.15
5
2
15000
2
1
1136.6
5
1
3.3
1
328.15
5
2
20000
1
1
1138.8
5
1
3.3
1
328.15
5
2
25000
2
1
1140.8
5
1
3.3
1
328.15
5
2
30000
1
1
1143
5
1
3.3
1
328.15
5
2
35000
2
1
1144.9
5
1
3.4
1
328.15
5
2
40000
1
1
1146.7
5
1
3.4
1
338.15
5
2
100
1
1
1123.3
5
1
3.1
1
338.15
5
2
1000
1
1
1123.8
5
1
3.2
1
338.15
5
2
5000
1
1
1125.8
5
1
3.2
1
338.15
5
2
10000
1
1
1128
5
1
3.2
1
338.15
5
2
15000
2
1
1130
5
1
3.2
1
338.15
5
2
20000
1
1
1132
5
1
3.3
1
338.15
5
2
25000
2
1
1134
5
1
3.3
1
338.15
5
2
30000
1
1
1136
5
1
3.3
1
338.15
5
2
35000
2
1
1137.9
5
1
3.3
1
338.15
5
2
40000
1
1
1140.1
5
1
3.4
1
348.15
5
2
100
1
1
1116.9
5
1
3.1
1
348.15
5
2
1000
1
1
1117.2
5
1
3.1
1
348.15
5
2
5000
1
1
1118.9
5
1
3.1
1
348.15
5
2
10000
1
1
1121.2
5
1
3.2
1
348.15
5
2
15000
2
1
1123.4
5
1
3.2
1
348.15
5
2
20000
1
1
1125.7
5
1
3.2
1
348.15
5
2
25000
2
1
1127.8
5
1
3.2
1
348.15
5
2
30000
1
1
1130
5
1
3.3
1
348.15
5
2
35000
2
1
1132
5
1
3.3
1
348.15
5
2
40000
1
1
1133.9
5
1
3.3
1
293.15
5
2
101
3
1
1152.99
6
1
2.55
1
298.15
5
2
101
3
1
1149.62
6
1
2.54
1
303.15
5
2
101
3
1
1146.25
6
1
2.52
1
308.15
5
2
101
3
1
1142.91
6
1
2.51
1
313.15
5
2
101
3
1
1139.58
6
1
2.49
1
318.15
5
2
101
3
1
1136.28
6
1
2.48
1
323.15
5
2
101
3
1
1133
6
1
2.46
1
328.15
5
2
101
3
1
1129.74
6
1
2.45
1
333.15
5
2
101
3
1
1126.49
6
1
2.43
1
338.15
5
2
101
3
1
1123.27
6
1
2.42
1
343.15
5
2
101
3
1
1120.06
6
1
2.4
1
348.15
5
2
101
3
1
1116.86
6
1
2.39
9
6
1
Principal objective of the work
JWM
JWM
8/15/2019
1
Surface tension liquid-gas, N/m
Ring tensiometer
Liquid
Direct value, X
1
Data file compiler
Propagation of evaluated standard uncertainties
95
Liquid
Gas
1
Temperature, K
Liquid
1
298.15
5
1
0.05664
5
1
0.001125
1
303.15
5
1
0.055628
5
1
0.001106
1
308.15
5
1
0.054404
5
1
0.001082
1
313.15
5
1
0.05321
5
1
0.00106
1
318.15
5
1
0.052156
5
1
0.00104
1
323.15
5
1
0.05096
5
1
0.001017
1
328.15
5
1
0.04986
5
1
0.000996
10
6
1
Principal objective of the work
VVD
TRC
1/9/2020
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
293.15
5
1
0.126256
6
1
0.013263
1
298.15
5
1
0.092543
5
1
0.009521
1
303.15
5
1
0.069515
5
1
0.007065
1
308.15
5
1
0.053839
5
1
0.005446
1
313.15
5
1
0.042526
5
1
0.004311
1
318.15
5
1
0.034643
5
1
0.003512
1
323.15
5
1
0.028096
5
1
0.002848
1
328.15
5
1
0.023407
5
1
0.002373
1
333.15
5
1
0.01984
5
1
0.002011
1
338.15
5
1
0.016936
5
1
0.001717
1
343.15
5
1
0.014535
5
1
0.001473
1
348.15
5
1
0.01305
5
1
0.001323
11
7
1
Principal objective of the work
JWM
JWM
8/15/2019
1
Mass density, kg/m3
Vibrating tube method
Liquid
Direct value, X
1
Data file compiler
Propagation of evaluated standard uncertainties
95
Liquid
1
Temperature, K
Liquid
2
Pressure, kPa
Liquid
1
298.15
5
2
100
1
1
1212.9
5
1
2.7
1
298.15
5
2
1000
1
1
1213.5
5
1
2.7
1
298.15
5
2
5000
1
1
1216.3
5
1
2.7
1
298.15
5
2
10000
1
1
1219.5
5
1
2.8
1
298.15
5
2
15000
2
1
1222.8
5
1
2.8
1
298.15
5
2
20000
1
1
1226
5
1
2.8
1
298.15
5
2
25000
2
1
1228.8
5
1
2.8
1
298.15
5
2
30000
1
1
1231.8
5
1
2.9
1
298.15
5
2
35000
2
1
1234.5
5
1
2.9
1
298.15
5
2
40000
1
1
1237.3
5
1
2.9
1
308.15
5
2
100
1
1
1204.9
5
1
2.7
1
308.15
5
2
1000
1
1
1205.7
5
1
2.7
1
308.15
5
2
5000
1
1
1208.6
5
1
2.7
1
308.15
5
2
10000
1
1
1211.9
5
1
2.7
1
308.15
5
2
15000
2
1
1215.2
5
1
2.8
1
308.15
5
2
20000
1
1
1218.4
5
1
2.8
1
308.15
5
2
25000
2
1
1221.6
5
1
2.8
1
308.15
5
2
30000
1
1
1224.4
5
1
2.8
1
308.15
5
2
35000
2
1
1227.5
5
1
2.9
1
308.15
5
2
40000
1
1
1230.5
5
1
2.9
1
318.15
5
2
100
1
1
1197.1
5
1
2.7
1
318.15
5
2
1000
1
1
1197.9
5
1
2.7
1
318.15
5
2
5000
1
1
1200.9
5
1
2.7
1
318.15
5
2
10000
1
1
1204.6
5
1
2.7
1
318.15
5
2
15000
2
1
1207.7
5
1
2.7
1
318.15
5
2
20000
1
1
1211.1
5
1
2.8
1
318.15
5
2
25000
2
1
1214.5
5
1
2.8
1
318.15
5
2
30000
1
1
1217.6
5
1
2.8
1
318.15
5
2
35000
2
1
1220.7
5
1
2.9
1
318.15
5
2
40000
1
1
1223.4
5
1
2.9
1
328.15
5
2
100
1
1
1189.3
5
1
2.6
1
328.15
5
2
1000
1
1
1190
5
1
2.6
1
328.15
5
2
5000
1
1
1193.1
5
1
2.7
1
328.15
5
2
10000
1
1
1196.9
5
1
2.7
1
328.15
5
2
15000
2
1
1200.3
5
1
2.7
1
328.15
5
2
20000
1
1
1203.7
5
1
2.7
1
328.15
5
2
25000
2
1
1207.3
5
1
2.8
1
328.15
5
2
30000
1
1
1210.4
5
1
2.8
1
328.15
5
2
35000
2
1
1213.6
5
1
2.8
1
328.15
5
2
40000
1
1
1216.2
5
1
2.9
1
338.15
5
2
100
1
1
1181.4
5
1
2.6
1
338.15
5
2
1000
1
1
1182.1
5
1
2.6
1
338.15
5
2
5000
1
1
1185.3
5
1
2.6
1
338.15
5
2
10000
1
1
1189.2
5
1
2.7
1
338.15
5
2
15000
2
1
1192.9
5
1
2.7
1
338.15
5
2
20000
1
1
1196.5
5
1
2.7
1
338.15
5
2
25000
2
1
1199.8
5
1
2.7
1
338.15
5
2
30000
1
1
1203.1
5
1
2.8
1
338.15
5
2
35000
2
1
1206.4
5
1
2.8
1
338.15
5
2
40000
1
1
1209.2
5
1
2.8
1
348.15
5
2
100
1
1
1173.4
5
1
2.6
1
348.15
5
2
1000
1
1
1174.3
5
1
2.6
1
348.15
5
2
5000
1
1
1177.2
5
1
2.6
1
348.15
5
2
10000
1
1
1181.5
5
1
2.6
1
348.15
5
2
15000
2
1
1185.4
5
1
2.7
1
348.15
5
2
20000
1
1
1189.2
5
1
2.7
1
348.15
5
2
25000
2
1
1192.7
5
1
2.7
1
348.15
5
2
30000
1
1
1195.9
5
1
2.8
1
348.15
5
2
35000
2
1
1199.3
5
1
2.8
1
348.15
5
2
40000
1
1
1202.4
5
1
2.8
1
293.15
5
2
101
3
1
1216.82
6
1
1.31
1
298.15
5
2
101
3
1
1212.86
6
1
1.3
1
303.15
5
2
101
3
1
1208.91
6
1
1.29
1
308.15
5
2
101
3
1
1204.88
6
1
1.28
1
313.15
5
2
101
3
1
1200.97
6
1
1.27
1
318.15
5
2
101
3
1
1197.07
6
1
1.26
1
323.15
5
2
101
3
1
1193.16
6
1
1.25
1
328.15
5
2
101
3
1
1189.25
6
1
1.25
1
333.15
5
2
101
3
1
1185.32
6
1
1.24
1
338.15
5
2
101
3
1
1181.37
6
1
1.23
1
343.15
5
2
101
3
1
1177.39
6
1
1.22
1
348.15
5
2
101
3
1
1173.37
6
1
1.21
12
7
1
Principal objective of the work
JWM
JWM
8/15/2019
1
Surface tension liquid-gas, N/m
Ring tensiometer
Liquid
Direct value, X
1
Data file compiler
Propagation of evaluated standard uncertainties
95
Liquid
Gas
1
Temperature, K
Liquid
1
298.15
5
1
0.032575
5
1
0.000561
1
303.15
5
1
0.032183
5
1
0.000555
1
308.15
5
1
0.03178
5
1
0.000548
1
313.15
5
1
0.031403
5
1
0.000543
1
318.15
5
1
0.031025
5
1
0.000537
1
323.15
5
1
0.030603
5
1
0.000531
1
328.15
5
1
0.030177
5
1
0.000524
13
7
1
Principal objective of the work
VVD
TRC
1/9/2020
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
298.15
5
1
1.42465
6
1
0.20489
1
303.15
5
1
0.97432
5
1
0.13223
1
308.15
5
1
0.68267
5
1
0.08781
1
313.15
5
1
0.4848
5
1
0.05931
1
318.15
5
1
0.35107
5
1
0.04107
1
323.15
5
1
0.26057
5
1
0.02933
1
328.15
5
1
0.19722
5
1
0.02149
1
333.15
5
1
0.15175
5
1
0.01611
1
338.15
5
1
0.11819
5
1
0.01228
1
343.15
5
1
0.09183
5
1
0.009387
1
348.15
5
1
0.077509
5
1
0.007859
14
5
1
1
1
Principal objective of the work
JWM
JWM
9/26/2019
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
Mole fraction
5
Liquid
2
Temperature, K
Liquid
1
1
5
2
293.15
5
1
1173.87
6
1
2.65
1
1
5
2
298.15
5
1
1170.41
6
1
2.64
1
1
5
2
303.15
5
1
1166.96
6
1
2.62
1
1
5
2
308.15
5
1
1163.54
6
1
2.6
1
1
5
2
313.15
5
1
1160.14
6
1
2.59
1
1
5
2
318.15
5
1
1156.75
6
1
2.57
1
1
5
2
323.15
5
1
1153.39
6
1
2.56
1
1
5
2
328.15
5
1
1150.05
6
1
2.54
1
1
5
2
333.15
5
1
1146.72
6
1
2.52
1
1
5
2
338.15
5
1
1143.41
6
1
2.51
1
1
5
2
343.15
5
1
1140.12
6
1
2.49
1
1
5
2
348.15
5
1
1136.84
6
1
2.48
1
0.901
4
2
293.15
5
1
1170.05
6
1
2.16
1
0.901
4
2
298.15
5
1
1166.55
6
1
2.15
1
0.901
4
2
303.15
5
1
1163.05
6
1
2.13
1
0.901
4
2
308.15
5
1
1159.57
6
1
2.12
1
0.901
4
2
313.15
5
1
1156.11
6
1
2.11
1
0.901
4
2
318.15
5
1
1152.67
6
1
2.09
1
0.901
4
2
323.15
5
1
1149.25
6
1
2.08
1
0.901
4
2
328.15
5
1
1145.86
6
1
2.07
1
0.901
4
2
333.15
5
1
1142.48
6
1
2.06
1
0.901
4
2
338.15
5
1
1139.11
6
1
2.04
1
0.901
4
2
343.15
5
1
1135.76
6
1
2.03
1
0.901
4
2
348.15
5
1
1132.43
6
1
2.02
1
0.8044
4
2
293.15
5
1
1167.35
6
1
1.74
1
0.8044
4
2
298.15
5
1
1163.8
6
1
1.73
1
0.8044
4
2
303.15
5
1
1160.25
6
1
1.72
1
0.8044
4
2
308.15
5
1
1156.73
6
1
1.71
1
0.8044
4
2
313.15
5
1
1153.22
6
1
1.7
1
0.8044
4
2
318.15
5
1
1149.74
6
1
1.69
1
0.8044
4
2
323.15
5
1
1146.27
6
1
1.68
1
0.8044
4
2
328.15
5
1
1142.82
6
1
1.66
1
0.8044
4
2
333.15
5
1
1139.38
6
1
1.65
1
0.8044
4
2
338.15
5
1
1135.97
6
1
1.64
1
0.8044
4
2
343.15
5
1
1132.57
6
1
1.63
1
0.8044
4
2
348.15
5
1
1129.18
6
1
1.62
1
0.7041
4
2
293.15
5
1
1164.1
6
1
1.36
1
0.7041
4
2
298.15
5
1
1160.5
6
1
1.35
1
0.7041
4
2
303.15
5
1
1156.9
6
1
1.34
1
0.7041
4
2
308.15
5
1
1153.32
6
1
1.33
1
0.7041
4
2
313.15
5
1
1149.76
6
1
1.32
1
0.7041
4
2
318.15
5
1
1146.21
6
1
1.31
1
0.7041
4
2
323.15
5
1
1142.69
6
1
1.31
1
0.7041
4
2
328.15
5
1
1139.18
6
1
1.3
1
0.7041
4
2
333.15
5
1
1135.69
6
1
1.29
1
0.7041
4
2
338.15
5
1
1132.22
6
1
1.28
1
0.7041
4
2
343.15
5
1
1128.75
6
1
1.27
1
0.7041
4
2
348.15
5
1
1125.31
6
1
1.26
1
0.6
4
2
293.15
5
1
1160.03
6
1
1.02
1
0.6
4
2
298.15
5
1
1156.36
6
1
1.01
1
0.6
4
2
303.15
5
1
1152.69
6
1
1
1
0.6
4
2
308.15
5
1
1149.04
6
1
1
1
0.6
4
2
313.15
5
1
1145.4
6
1
0.99
1
0.6
4
2
318.15
5
1
1141.79
6
1
0.98
1
0.6
4
2
323.15
5
1
1138.19
6
1
0.97
1
0.6
4
2
328.15
5
1
1134.6
6
1
0.97
1
0.6
4
2
333.15
5
1
1131.02
6
1
0.96
1
0.6
4
2
338.15
5
1
1127.47
6
1
0.95
1
0.6
4
2
343.15
5
1
1123.92
6
1
0.95
1
0.6
4
2
348.15
5
1
1120.38
6
1
0.94
1
0.4996
4
2
293.15
5
1
1155.23
6
1
0.74
1
0.4996
4
2
298.15
5
1
1151.47
6
1
0.73
1
0.4996
4
2
303.15
5
1
1147.71
6
1
0.73
1
0.4996
4
2
308.15
5
1
1143.97
6
1
0.72
1
0.4996
4
2
313.15
5
1
1140.21
6
1
0.72
1
0.4996
4
2
318.15
5
1
1136.54
6
1
0.71
1
0.4996
4
2
323.15
5
1
1132.84
6
1
0.71
1
0.4996
4
2
328.15
5
1
1129.11
6
1
0.7
1
0.4996
4
2
333.15
5
1
1125.32
6
1
0.7
1
0.4996
4
2
338.15
5
1
1121.39
6
1
0.69
1
0.4996
4
2
343.15
5
1
1117.91
6
1
0.68
1
0.4996
4
2
348.15
5
1
1114.16
6
1
0.68
1
0.4042
4
2
293.15
5
1
1149.03
6
1
0.52
1
0.4042
4
2
298.15
5
1
1145
6
1
0.52
1
0.4042
4
2
303.15
5
1
1141.37
6
1
0.51
1
0.4042
4
2
308.15
5
1
1137.58
6
1
0.51
1
0.4042
4
2
313.15
5
1
1133.79
6
1
0.5
1
0.4042
4
2
318.15
5
1
1130
6
1
0.5
1
0.4042
4
2
323.15
5
1
1126.21
6
1
0.5
1
0.4042
4
2
328.15
5
1
1122.45
6
1
0.49
1
0.4042
4
2
333.15
5
1
1118.65
6
1
0.49
1
0.4042
4
2
338.15
5
1
1114.84
6
1
0.48
1
0.4042
4
2
343.15
5
1
1111.04
6
1
0.48
1
0.4042
4
2
348.15
5
1
1107.25
6
1
0.48
1
0
5
2
293.15
5
1
1064.42
6
1
0.12
1
0
5
2
298.15
5
1
1058.53
6
1
0.12
1
0
5
2
303.15
5
1
1052.67
6
1
0.11
1
0
5
2
308.15
5
1
1046.69
6
1
0.11
1
0
5
2
313.15
5
1
1040.71
6
1
0.11
1
0
5
2
318.15
5
1
1034.78
6
1
0.11
1
0
5
2
323.15
5
1
1028.69
6
1
0.11
1
0
5
2
328.15
5
1
1022.51
6
1
0.11
1
0
5
2
333.15
5
1
1016.4
6
1
0.11
1
0
5
2
338.15
5
1
1010.15
6
1
0.11
1
0
5
2
343.15
5
1
1003.94
6
1
0.11
1
0
5
2
348.15
5
1
997.65
5
1
0.11
15
5
1
1
1
Principal objective of the work
JWM
JWM
8/15/2019
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
Mole fraction
5
Liquid
2
Temperature, K
Liquid
1
1
5
2
293.15
5
1
0.13658
5
1
0.01444
1
1
5
2
298.15
5
1
0.097484
5
1
0.010059
1
1
5
2
303.15
5
1
0.071784
5
1
0.007303
1
1
5
2
308.15
5
1
0.054574
5
1
0.005521
1
1
5
2
313.15
5
1
0.042306
5
1
0.004289
1
1
5
2
318.15
5
1
0.033963
5
1
0.003443
1
1
5
2
323.15
5
1
0.027779
5
1
0.002816
1
1
5
2
328.15
5
1
0.022933
5
1
0.002325
1
1
5
2
333.15
5
1
0.019321
5
1
0.001959
1
1
5
2
338.15
5
1
0.0164
5
1
0.001662
1
1
5
2
343.15
5
1
0.01398
5
1
0.001417
1
1
5
2
348.15
5
1
0.0123
5
1
0.001247
1
0.901
4
2
293.15
5
1
0.091196
5
1
0.009357
1
0.901
4
2
298.15
5
1
0.067117
5
1
0.006801
1
0.901
4
2
303.15
5
1
0.050912
5
1
0.005138
1
0.901
4
2
308.15
5
1
0.039605
5
1
0.004007
1
0.901
4
2
313.15
5
1
0.031582
5
1
0.003195
1
0.901
4
2
318.15
5
1
0.025727
5
1
0.002603
1
0.901
4
2
323.15
5
1
0.021302
5
1
0.002155
1
0.901
4
2
328.15
5
1
0.017915
5
1
0.001812
1
0.901
4
2
333.15
5
1
0.015203
5
1
0.001538
1
0.901
4
2
338.15
5
1
0.013071
5
1
0.001322
1
0.901
4
2
343.15
5
1
0.01151
5
1
0.001164
1
0.901
4
2
348.15
5
1
0.01034
5
1
0.001046
1
0.8044
4
2
293.15
5
1
0.067047
5
1
0.006782
1
0.8044
4
2
298.15
5
1
0.051636
5
1
0.005202
1
0.8044
4
2
303.15
5
1
0.040134
5
1
0.004053
1
0.8044
4
2
308.15
5
1
0.031552
5
1
0.003187
1
0.8044
4
2
313.15
5
1
0.025587
5
1
0.002584
1
0.8044
4
2
318.15
5
1
0.021136
5
1
0.002135
1
0.8044
4
2
323.15
5
1
0.017621
5
1
0.00178
1
0.8044
4
2
328.15
5
1
0.014845
5
1
0.001499
1
0.8044
4
2
333.15
5
1
0.012808
5
1
0.001293
1
0.8044
4
2
338.15
5
1
0.011135
5
1
0.001125
1
0.8044
4
2
343.15
5
1
0.009901
4
1
0.001
1
0.8044
4
2
348.15
5
1
0.00889
4
1
0.000898
1
0.7041
4
2
293.15
5
1
0.052214
5
1
0.005252
1
0.7041
4
2
298.15
5
1
0.041197
5
1
0.004154
1
0.7041
4
2
303.15
5
1
0.03268
5
1
0.003295
1
0.7041
4
2
308.15
5
1
0.026102
5
1
0.002632
1
0.7041
4
2
313.15
5
1
0.021168
5
1
0.002134
1
0.7041
4
2
318.15
5
1
0.017677
5
1
0.001782
1
0.7041
4
2
323.15
5
1
0.014783
5
1
0.001491
1
0.7041
4
2
328.15
5
1
0.01263
5
1
0.001273
1
0.7041
4
2
333.15
5
1
0.010949
5
1
0.001104
1
0.7041
4
2
338.15
5
1
0.009432
4
1
0.000951
1
0.7041
4
2
343.15
5
1
0.0084
4
1
0.000847
1
0.7041
4
2
348.15
5
1
0.0075
4
1
0.000756
1
0.6
4
2
293.15
5
1
0.040174
5
1
0.004045
1
0.6
4
2
298.15
5
1
0.031753
5
1
0.003197
1
0.6
4
2
303.15
5
1
0.025534
5
1
0.002571
1
0.6
4
2
308.15
5
1
0.020704
5
1
0.002084
1
0.6
4
2
313.15
5
1
0.017186
5
1
0.00173
1
0.6
4
2
318.15
5
1
0.014417
5
1
0.001451
1
0.6
4
2
323.15
5
1
0.012161
5
1
0.001224
1
0.6
4
2
328.15
5
1
0.010556
5
1
0.001063
1
0.6
4
2
333.15
5
1
0.009125
4
1
0.000919
1
0.6
4
2
338.15
5
1
0.007864
4
1
0.000792
1
0.6
4
2
343.15
5
1
0.006994
4
1
0.000704
1
0.6
4
2
348.15
5
1
0.0062
4
1
0.000624
1
0.4996
4
2
293.15
5
1
0.029539
5
1
0.00297
1
0.4996
4
2
298.15
5
1
0.023551
5
1
0.002368
1
0.4996
4
2
303.15
5
1
0.019106
5
1
0.001921
1
0.4996
4
2
308.15
5
1
0.015835
5
1
0.001592
1
0.4996
4
2
313.15
5
1
0.013358
5
1
0.001343
1
0.4996
4
2
318.15
5
1
0.011402
5
1
0.001147
1
0.4996
4
2
323.15
5
1
0.00987
4
1
0.000992
1
0.4996
4
2
328.15
5
1
0.008668
4
1
0.000872
1
0.4996
4
2
333.15
5
1
0.007573
4
1
0.000762
1
0.4996
4
2
338.15
5
1
0.00654
4
1
0.000658
1
0.4996
4
2
343.15
5
1
0.00574
4
1
0.000577
1
0.4996
4
2
348.15
5
1
0.00512
4
1
0.000515
1
0.4042
4
2
293.15
5
1
0.019881
5
1
0.001997
1
0.4042
4
2
298.15
5
1
0.016286
5
1
0.001636
1
0.4042
4
2
303.15
5
1
0.013581
5
1
0.001364
1
0.4042
4
2
308.15
5
1
0.011502
5
1
0.001155
1
0.4042
4
2
313.15
5
1
0.00996
4
1
0.001001
1
0.4042
4
2
318.15
5
1
0.008777
4
1
0.000882
1
0.4042
4
2
323.15
5
1
0.007813
4
1
0.000785
1
0.4042
4
2
328.15
5
1
0.007011
4
1
0.000704
1
0.4042
4
2
333.15
5
1
0.006149
4
1
0.000618
1
0.4042
4
2
338.15
5
1
0.0054
4
1
0.000542
1
0.4042
4
2
343.15
5
1
0.00468
4
1
0.00047
1
0.4042
4
2
348.15
5
1
0.00417
4
1
0.000419
1
0
5
2
293.15
5
1
0.000653
3
1
6.5e-05
1
0
5
2
298.15
5
1
0.000615
3
1
6.2e-05
1
0
5
2
303.15
5
1
0.00058
3
1
5.8e-05
1
0
5
2
308.15
5
1
0.000545
3
1
5.5e-05
1
0
5
2
313.15
5
1
0.000518
3
1
5.2e-05
1
0
5
2
318.15
5
1
0.000491
3
1
4.9e-05
1
0
5
2
323.15
5
1
0.000464
3
1
4.7e-05
1
0
5
2
328.15
5
1
0.000441
3
1
4.4e-05
1
0
5
2
333.15
5
1
0.00042
3
1
4.2e-05
1
0
5
2
338.15
5
1
0.0004
3
1
4e-05
1
0
5
2
343.15
5
1
0.000382
3
1
3.8e-05
1
0
5
2
348.15
5
1
0.000364
3
1
3.7e-05
16
6
1
1
1
Principal objective of the work
JWM
JWM
9/26/2019
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
Mole fraction
6
Liquid
2
Temperature, K
Liquid
1
1
5
2
293.15
5
1
1152.99
6
1
2.55
1
1
5
2
298.15
5
1
1149.62
6
1
2.54
1
1
5
2
303.15
5
1
1146.25
6
1
2.52
1
1
5
2
308.15
5
1
1142.91
6
1
2.51
1
1
5
2
313.15
5
1
1139.58
6
1
2.49
1
1
5
2
318.15
5
1
1136.28
6
1
2.48
1
1
5
2
323.15
5
1
1133
6
1
2.46
1
1
5
2
328.15
5
1
1129.74
6
1
2.45
1
1
5
2
333.15
5
1
1126.49
6
1
2.43
1
1
5
2
338.15
5
1
1123.27
6
1
2.42
1
1
5
2
343.15
5
1
1120.06
6
1
2.4
1
1
5
2
348.15
5
1
1116.86
6
1
2.39
1
0.9377
4
2
293.15
5
1
1152.07
6
1
2.26
1
0.9377
4
2
298.15
5
1
1148.67
6
1
2.24
1
0.9377
4
2
303.15
5
1
1145.29
6
1
2.23
1
0.9377
4
2
308.15
5
1
1141.92
6
1
2.21
1
0.9377
4
2
313.15
5
1
1138.58
6
1
2.2
1
0.9377
4
2
318.15
5
1
1135.25
6
1
2.19
1
0.9377
4
2
323.15
5
1
1131.95
6
1
2.17
1
0.9377
4
2
328.15
5
1
1128.66
6
1
2.16
1
0.9377
4
2
333.15
5
1
1125.39
6
1
2.15
1
0.9377
4
2
338.15
5
1
1122.14
6
1
2.13
1
0.9377
4
2
343.15
5
1
1119.05
6
1
2.12
1
0.9377
4
2
348.15
5
1
1115.67
6
1
2.11
1
0.8231
4
2
293.15
5
1
1150.15
6
1
1.76
1
0.8231
4
2
298.15
5
1
1146.71
6
1
1.75
1
0.8231
4
2
303.15
5
1
1143.28
6
1
1.74
1
0.8231
4
2
308.15
5
1
1139.86
6
1
1.73
1
0.8231
4
2
313.15
5
1
1136.46
6
1
1.72
1
0.8231
4
2
318.15
5
1
1133.08
6
1
1.71
1
0.8231
4
2
323.15
5
1
1129.72
6
1
1.69
1
0.8231
4
2
328.15
5
1
1126.38
6
1
1.68
1
0.8231
4
2
333.15
5
1
1123.06
6
1
1.67
1
0.8231
4
2
338.15
5
1
1119.76
6
1
1.66
1
0.8231
4
2
343.15
5
1
1116.47
6
1
1.65
1
0.8231
4
2
348.15
5
1
1113.19
6
1
1.64
1
0.7045
4
2
293.15
5
1
1147.36
6
1
1.32
1
0.7045
4
2
298.15
5
1
1144.04
6
1
1.31
1
0.7045
4
2
303.15
5
1
1140.55
6
1
1.3
1
0.7045
4
2
308.15
5
1
1137.07
6
1
1.29
1
0.7045
4
2
313.15
5
1
1133.61
6
1
1.28
1
0.7045
4
2
318.15
5
1
1130.07
6
1
1.27
1
0.7045
4
2
323.15
5
1
1126.85
6
1
1.27
1
0.7045
4
2
328.15
5
1
1123.35
6
1
1.26
1
0.7045
4
2
333.15
5
1
1119.77
6
1
1.25
1
0.7045
4
2
338.15
5
1
1116.29
6
1
1.24
1
0.7045
4
2
343.15
5
1
1112.94
6
1
1.23
1
0.7045
4
2
348.15
5
1
1109.46
6
1
1.22
1
0.5955
4
2
293.15
5
1
1144.39
6
1
0.97
1
0.5955
4
2
298.15
5
1
1140.98
6
1
0.97
1
0.5955
4
2
303.15
5
1
1137.35
6
1
0.96
1
0.5955
4
2
308.15
5
1
1133.77
6
1
0.95
1
0.5955
4
2
313.15
5
1
1130.19
6
1
0.95
1
0.5955
4
2
318.15
5
1
1126.69
6
1
0.94
1
0.5955
4
2
323.15
5
1
1123.23
6
1
0.93
1
0.5955
4
2
328.15
5
1
1119.67
6
1
0.93
1
0.5955
4
2
333.15
5
1
1115.78
6
1
0.92
1
0.5955
4
2
338.15
5
1
1112.46
6
1
0.91
1
0.5955
4
2
343.15
5
1
1108.99
6
1
0.91
1
0.5955
4
2
348.15
5
1
1105.72
6
1
0.9
1
0.505
4
2
293.15
5
1
1141.66
6
1
0.73
1
0.505
4
2
298.15
5
1
1137.83
6
1
0.73
1
0.505
4
2
303.15
5
1
1134.43
6
1
0.72
1
0.505
4
2
308.15
5
1
1130.79
6
1
0.72
1
0.505
4
2
313.15
5
1
1127.05
6
1
0.71
1
0.505
4
2
318.15
5
1
1123.63
6
1
0.71
1
0.505
4
2
323.15
5
1
1120.03
6
1
0.7
1
0.505
4
2
328.15
5
1
1116.34
6
1
0.69
1
0.505
4
2
333.15
5
1
1112.55
6
1
0.69
1
0.505
4
2
338.15
5
1
1109.07
6
1
0.68
1
0.505
4
2
343.15
5
1
1105.39
6
1
0.68
1
0.505
4
2
348.15
5
1
1101.97
6
1
0.67
1
0.4088
4
2
293.15
5
1
1137.42
6
1
0.52
1
0.4088
4
2
298.15
5
1
1133.63
6
1
0.51
1
0.4088
4
2
303.15
5
1
1129.84
6
1
0.51
1
0.4088
4
2
308.15
5
1
1126.06
6
1
0.5
1
0.4088
4
2
313.15
5
1
1122.3
6
1
0.5
1
0.4088
4
2
318.15
5
1
1118.55
6
1
0.5
1
0.4088
4
2
323.15
5
1
1114.81
6
1
0.49
1
0.4088
4
2
328.15
5
1
1111.08
6
1
0.49
1
0.4088
4
2
333.15
5
1
1107.37
6
1
0.48
1
0.4088
4
2
338.15
5
1
1103.66
6
1
0.48
1
0.4088
4
2
343.15
5
1
1099.97
6
1
0.48
1
0.4088
4
2
348.15
5
1
1096.28
6
1
0.47
1
0
5
2
293.15
5
1
1064.42
6
1
0.12
1
0
5
2
298.15
5
1
1058.53
6
1
0.12
1
0
5
2
303.15
5
1
1052.67
6
1
0.11
1
0
5
2
308.15
5
1
1046.69
6
1
0.11
1
0
5
2
313.15
5
1
1040.71
6
1
0.11
1
0
5
2
318.15
5
1
1034.78
6
1
0.11
1
0
5
2
323.15
5
1
1028.69
6
1
0.11
1
0
5
2
328.15
5
1
1022.51
6
1
0.11
1
0
5
2
333.15
5
1
1016.4
6
1
0.11
1
0
5
2
338.15
5
1
1010.15
6
1
0.11
1
0
5
2
343.15
5
1
1003.94
6
1
0.11
1
0
5
2
348.15
5
1
997.65
5
1
0.11
17
6
1
1
1
Principal objective of the work
JWM
JWM
8/15/2019
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
Mole fraction
6
Liquid
2
Temperature, K
Liquid
1
1
5
2
293.15
5
1
0.126256
6
1
0.013263
1
1
5
2
298.15
5
1
0.092543
5
1
0.009521
1
1
5
2
303.15
5
1
0.069515
5
1
0.007065
1
1
5
2
308.15
5
1
0.053839
5
1
0.005446
1
1
5
2
313.15
5
1
0.042526
5
1
0.004311
1
1
5
2
318.15
5
1
0.034643
5
1
0.003512
1
1
5
2
323.15
5
1
0.028096
5
1
0.002848
1
1
5
2
328.15
5
1
0.023407
5
1
0.002373
1
1
5
2
333.15
5
1
0.01984
5
1
0.002011
1
1
5
2
338.15
5
1
0.016936
5
1
0.001717
1
1
5
2
343.15
5
1
0.014535
5
1
0.001473
1
1
5
2
348.15
5
1
0.01305
5
1
0.001323
1
0.9377
4
2
293.15
5
1
0.114978
6
1
0.011979
1
0.9377
4
2
298.15
5
1
0.085366
5
1
0.008735
1
0.9377
4
2
303.15
5
1
0.064369
5
1
0.00652
1
0.9377
4
2
308.15
5
1
0.049857
5
1
0.005048
1
0.9377
4
2
313.15
5
1
0.039547
5
1
0.004004
1
0.9377
4
2
318.15
5
1
0.032203
5
1
0.00326
1
0.9377
4
2
323.15
5
1
0.026199
5
1
0.002652
1
0.9377
4
2
328.15
5
1
0.021805
5
1
0.002208
1
0.9377
4
2
333.15
5
1
0.018527
5
1
0.001876
1
0.9377
4
2
338.15
5
1
0.015852
5
1
0.001605
1
0.9377
4
2
343.15
5
1
0.013608
5
1
0.001378
1
0.9377
4
2
348.15
5
1
0.012251
5
1
0.00124
1
0.8231
4
2
293.15
5
1
0.094111
5
1
0.009659
1
0.8231
4
2
298.15
5
1
0.068895
5
1
0.006976
1
0.8231
4
2
303.15
5
1
0.05269
5
1
0.005311
1
0.8231
4
2
308.15
5
1
0.042091
5
1
0.004252
1
0.8231
4
2
313.15
5
1
0.033474
5
1
0.003382
1
0.8231
4
2
318.15
5
1
0.027386
5
1
0.002767
1
0.8231
4
2
323.15
5
1
0.02242
5
1
0.002265
1
0.8231
4
2
328.15
5
1
0.018811
5
1
0.0019
1
0.8231
4
2
333.15
5
1
0.016105
5
1
0.001627
1
0.8231
4
2
338.15
5
1
0.013797
5
1
0.001394
1
0.8231
4
2
343.15
5
1
0.011927
5
1
0.001205
1
0.8231
4
2
348.15
5
1
0.010736
5
1
0.001085
1
0.7045
4
2
293.15
5
1
0.069311
5
1
0.007006
1
0.7045
4
2
298.15
5
1
0.052011
5
1
0.005232
1
0.7045
4
2
303.15
5
1
0.039989
5
1
0.004032
1
0.7045
4
2
308.15
5
1
0.032445
5
1
0.003271
1
0.7045
4
2
313.15
5
1
0.026372
5
1
0.002659
1
0.7045
4
2
318.15
5
1
0.022131
5
1
0.002231
1
0.7045
4
2
323.15
5
1
0.018271
5
1
0.001842
1
0.7045
4
2
328.15
5
1
0.015444
5
1
0.001557
1
0.7045
4
2
333.15
5
1
0.013335
5
1
0.001345
1
0.7045
4
2
338.15
5
1
0.011539
5
1
0.001163
1
0.7045
4
2
343.15
5
1
0.010015
5
1
0.00101
1
0.7045
4
2
348.15
5
1
0.009056
4
1
0.000913
1
0.5955
4
2
293.15
5
1
0.048646
5
1
0.004898
1
0.5955
4
2
298.15
5
1
0.036555
5
1
0.00368
1
0.5955
4
2
303.15
5
1
0.029271
5
1
0.002947
1
0.5955
4
2
308.15
5
1
0.024106
5
1
0.002427
1
0.5955
4
2
313.15
5
1
0.019816
5
1
0.001995
1
0.5955
4
2
318.15
5
1
0.016874
5
1
0.001699
1
0.5955
4
2
323.15
5
1
0.014219
5
1
0.001431
1
0.5955
4
2
328.15
5
1
0.012002
5
1
0.001208
1
0.5955
4
2
333.15
5
1
0.010501
5
1
0.001057
1
0.5955
4
2
338.15
5
1
0.009243
4
1
0.000931
1
0.5955
4
2
343.15
5
1
0.008114
4
1
0.000817
1
0.5955
4
2
348.15
5
1
0.0074
4
1
0.000745
1
0.505
4
2
293.15
5
1
0.03151
5
1
0.003169
1
0.505
4
2
298.15
5
1
0.02507
5
1
0.002521
1
0.505
4
2
303.15
5
1
0.020407
5
1
0.002052
1
0.505
4
2
308.15
5
1
0.01693
5
1
0.001703
1
0.505
4
2
313.15
5
1
0.014259
5
1
0.001434
1
0.505
4
2
318.15
5
1
0.012185
5
1
0.001225
1
0.505
4
2
323.15
5
1
0.010509
5
1
0.001057
1
0.505
4
2
328.15
5
1
0.009025
4
1
0.000908
1
0.505
4
2
333.15
5
1
0.007958
4
1
0.0008
1
0.505
4
2
338.15
5
1
0.007119
4
1
0.000716
1
0.505
4
2
343.15
5
1
0.006334
4
1
0.000637
1
0.505
4
2
348.15
5
1
0.005887
4
1
0.000592
1
0.4088
4
2
293.15
5
1
0.017491
5
1
0.001757
1
0.4088
4
2
298.15
5
1
0.014374
5
1
0.001444
1
0.4088
4
2
303.15
5
1
0.012013
5
1
0.001207
1
0.4088
4
2
308.15
5
1
0.010166
5
1
0.001021
1
0.4088
4
2
313.15
5
1
0.008691
4
1
0.000873
1
0.4088
4
2
318.15
5
1
0.007529
4
1
0.000756
1
0.4088
4
2
323.15
5
1
0.006577
4
1
0.000661
1
0.4088
4
2
328.15
5
1
0.005804
4
1
0.000583
1
0.4088
4
2
333.15
5
1
0.005145
4
1
0.000517
1
0.4088
4
2
338.15
5
1
0.004618
4
1
0.000464
1
0.4088
4
2
343.15
5
1
0.004158
4
1
0.000418
1
0.4088
4
2
348.15
5
1
0.003965
4
1
0.000398
1
0
5
2
293.15
5
1
0.000653
3
1
6.5e-05
1
0
5
2
298.15
5
1
0.000615
3
1
6.2e-05
1
0
5
2
303.15
5
1
0.00058
3
1
5.8e-05
1
0
5
2
308.15
5
1
0.000545
3
1
5.5e-05
1
0
5
2
313.15
5
1
0.000518
3
1
5.2e-05
1
0
5
2
318.15
5
1
0.000491
3
1
4.9e-05
1
0
5
2
323.15
5
1
0.000464
3
1
4.7e-05
1
0
5
2
328.15
5
1
0.000441
3
1
4.4e-05
1
0
5
2
333.15
5
1
0.00042
3
1
4.2e-05
1
0
5
2
338.15
5
1
0.0004
3
1
4e-05
1
0
5
2
343.15
5
1
0.000382
3
1
3.8e-05
1
0
5
2
348.15
5
1
0.000364
3
1
3.7e-05
18
7
1
2
1
Principal objective of the work
JWM
JWM
9/26/2019
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
Mole fraction
7
Liquid
2
Temperature, K
Liquid
1
1
5
2
293.15
5
1
1216.82
6
1
1.31
1
1
5
2
298.15
5
1
1212.86
6
1
1.3
1
1
5
2
303.15
5
1
1208.91
6
1
1.29
1
1
5
2
308.15
5
1
1204.88
6
1
1.28
1
1
5
2
313.15
5
1
1200.97
6
1
1.27
1
1
5
2
318.15
5
1
1197.07
6
1
1.26
1
1
5
2
323.15
5
1
1193.16
6
1
1.25
1
1
5
2
328.15
5
1
1189.25
6
1
1.25
1
1
5
2
333.15
5
1
1185.32
6
1
1.24
1
1
5
2
338.15
5
1
1181.37
6
1
1.23
1
1
5
2
343.15
5
1
1177.39
6
1
1.22
1
1
5
2
348.15
5
1
1173.37
6
1
1.21
1
0.9164
4
2
293.15
5
1
1208.93
6
1
1.11
1
0.9164
4
2
298.15
5
1
1204.97
6
1
1.1
1
0.9164
4
2
303.15
5
1
1201.04
6
1
1.09
1
0.9164
4
2
308.15
5
1
1197.01
6
1
1.08
1
0.9164
4
2
313.15
5
1
1193.1
6
1
1.08
1
0.9164
4
2
318.15
5
1
1189.2
6
1
1.07
1
0.9164
4
2
323.15
5
1
1185.29
6
1
1.06
1
0.9164
4
2
328.15
5
1
1181.39
6
1
1.05
1
0.9164
4
2
333.15
5
1
1177.5
6
1
1.05
1
0.9164
4
2
338.15
5
1
1173.61
6
1
1.04
1
0.9164
4
2
343.15
5
1
1169.74
6
1
1.03
1
0.9164
4
2
348.15
5
1
1165.68
6
1
1.02
1
0.7485
4
2
293.15
5
1
1191.18
6
1
0.76
1
0.7485
4
2
298.15
5
1
1187.21
6
1
0.76
1
0.7485
4
2
303.15
5
1
1183.24
6
1
0.75
1
0.7485
4
2
308.15
5
1
1179.28
6
1
0.75
1
0.7485
4
2
313.15
5
1
1175.32
6
1
0.74
1
0.7485
4
2
318.15
5
1
1171.36
6
1
0.73
1
0.7485
4
2
323.15
5
1
1167.41
6
1
0.73
1
0.7485
4
2
328.15
5
1
1163.47
6
1
0.72
1
0.7485
4
2
333.15
5
1
1159.55
6
1
0.72
1
0.7485
4
2
338.15
5
1
1155.64
6
1
0.71
1
0.7485
4
2
343.15
5
1
1151.72
6
1
0.7
1
0.7485
4
2
348.15
5
1
1147.75
6
1
0.7
1
0.594
4
2
293.15
5
1
1169.15
6
1
0.51
1
0.594
4
2
298.15
5
1
1165.03
6
1
0.5
1
0.594
4
2
303.15
5
1
1161.15
6
1
0.5
1
0.594
4
2
308.15
5
1
1157.98
6
1
0.5
1
0.594
4
2
313.15
5
1
1153.12
6
1
0.49
1
0.594
4
2
318.15
5
1
1149.07
6
1
0.49
1
0.594
4
2
323.15
5
1
1145.19
6
1
0.48
1
0.594
4
2
328.15
5
1
1141.22
6
1
0.48
1
0.594
4
2
333.15
5
1
1137.25
6
1
0.47
1
0.594
4
2
338.15
5
1
1133.39
6
1
0.47
1
0.594
4
2
343.15
5
1
1129.38
6
1
0.47
1
0.594
4
2
348.15
5
1
1125.35
6
1
0.46
1
0.4494
4
2
293.15
5
1
1139.41
6
1
0.32
1
0.4494
4
2
298.15
5
1
1135.48
6
1
0.32
1
0.4494
4
2
303.15
5
1
1131.42
6
1
0.32
1
0.4494
4
2
308.15
5
1
1127.1
6
1
0.31
1
0.4494
4
2
313.15
5
1
1123.31
6
1
0.31
1
0.4494
4
2
318.15
5
1
1119.29
6
1
0.31
1
0.4494
4
2
323.15
5
1
1115.27
6
1
0.3
1
0.4494
4
2
328.15
5
1
1111.29
6
1
0.3
1
0.4494
4
2
333.15
5
1
1107.27
6
1
0.3
1
0.4494
4
2
338.15
5
1
1103.32
6
1
0.3
1
0.4494
4
2
343.15
5
1
1099.25
6
1
0.29
1
0.4494
4
2
348.15
5
1
1095.19
6
1
0.29
1
0.3015
4
2
293.15
5
1
1092.4
6
1
0.21
1
0.3015
4
2
298.15
5
1
1088.35
6
1
0.21
1
0.3015
4
2
303.15
5
1
1084.27
6
1
0.2
1
0.3015
4
2
308.15
5
1
1080.2
6
1
0.2
1
0.3015
4
2
313.15
5
1
1076.12
6
1
0.2
1
0.3015
4
2
318.15
5
1
1072.05
6
1
0.2
1
0.3015
4
2
323.15
5
1
1067.97
6
1
0.2
1
0.3015
4
2
328.15
5
1
1063.88
6
1
0.2
1
0.3015
4
2
333.15
5
1
1059.79
6
1
0.2
1
0.3015
4
2
338.15
5
1
1055.68
6
1
0.19
1
0.3015
4
2
343.15
5
1
1051.58
6
1
0.19
1
0.3015
4
2
348.15
5
1
1047.47
6
1
0.2
1
0.1507
4
2
293.15
5
1
1006.82
6
1
0.26
1
0.1507
4
2
298.15
5
1
1002.81
6
1
0.22
1
0.1507
4
2
303.15
5
1
998.76
5
1
0.22
1
0.1507
4
2
308.15
5
1
994.7
5
1
0.22
1
0.1507
4
2
313.15
5
1
990.63
5
1
0.22
1
0.1507
4
2
318.15
5
1
986.54
5
1
0.22
1
0.1507
4
2
323.15
5
1
982.44
5
1
0.22
1
0.1507
4
2
328.15
5
1
978.31
5
1
0.22
1
0.1507
4
2
333.15
5
1
974.17
5
1
0.22
1
0.1507
4
2
338.15
5
1
970.01
5
1
0.22
1
0.1507
4
2
343.15
5
1
965.82
5
1
0.22
1
0.1507
4
2
348.15
5
1
961.61
5
1
0.28
1
0
5
2
293.15
5
1
810.15
5
1
0.14
1
0
5
2
298.15
5
1
805.78
5
1
0.14
1
0
5
2
303.15
5
1
802.07
5
1
0.14
1
0
5
2
308.15
5
1
798.06
5
1
0.14
1
0
5
2
313.15
5
1
793.98
5
1
0.14
1
0
5
2
318.15
5
1
790.21
5
1
0.15
1
0
5
2
323.15
5
1
785.9
5
1
0.15
1
0
5
2
328.15
5
1
782.16
5
1
0.15
1
0
5
2
333.15
5
1
777.82
5
1
0.15
1
0
5
2
338.15
5
1
773.88
5
1
0.15
1
0
5
2
343.15
5
1
769.74
5
1
0.15
1
0
5
2
348.15
5
1
765.32
5
1
0.15
19
7
1
2
1
Principal objective of the work
JWM
JWM
8/15/2019
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
Mole fraction
7
Liquid
2
Temperature, K
Liquid
1
1
5
2
298.15
5
1
1.42465
6
1
0.20489
1
1
5
2
303.15
5
1
0.97432
5
1
0.13223
1
1
5
2
308.15
5
1
0.68267
5
1
0.08781
1
1
5
2
313.15
5
1
0.4848
5
1
0.05931
1
1
5
2
318.15
5
1
0.35107
5
1
0.04107
1
1
5
2
323.15
5
1
0.26057
5
1
0.02933
1
1
5
2
328.15
5
1
0.19722
5
1
0.02149
1
1
5
2
333.15
5
1
0.15175
5
1
0.01611
1
1
5
2
338.15
5
1
0.11819
5
1
0.01228
1
1
5
2
343.15
5
1
0.09183
5
1
0.009387
1
1
5
2
348.15
5
1
0.077509
5
1
0.007859
1
0.9164
4
2
298.15
5
1
1.066286
7
1
0.146656
1
0.9164
4
2
303.15
5
1
0.747853
6
1
0.097476
1
0.9164
4
2
308.15
5
1
0.531953
6
1
0.065928
1
0.9164
4
2
313.15
5
1
0.385642
6
1
0.045667
1
0.9164
4
2
318.15
5
1
0.28502
6
1
0.032427
1
0.9164
4
2
323.15
5
1
0.21017
6
1
0.023053
1
0.9164
4
2
328.15
5
1
0.159341
6
1
0.016978
1
0.9164
4
2
333.15
5
1
0.125
6
1
0.013037
1
0.9164
4
2
338.15
5
1
0.099341
5
1
0.010194
1
0.9164
4
2
343.15
5
1
0.079201
5
1
0.008032
1
0.9164
4
2
348.15
5
1
0.068
5
1
0.006859
1
0.7485
4
2
298.15
5
1
0.504708
6
1
0.062026
1
0.7485
4
2
303.15
5
1
0.361796
6
1
0.042431
1
0.7485
4
2
308.15
5
1
0.265552
6
1
0.029914
1
0.7485
4
2
313.15
5
1
0.197977
6
1
0.021548
1
0.7485
4
2
318.15
5
1
0.150427
6
1
0.015923
1
0.7485
4
2
323.15
5
1
0.116662
6
1
0.012088
1
0.7485
4
2
328.15
5
1
0.091629
5
1
0.009347
1
0.7485
4
2
333.15
5
1
0.076818
5
1
0.007771
1
0.7485
4
2
338.15
5
1
0.063
5
1
0.006334
1
0.7485
4
2
343.15
5
1
0.052414
5
1
0.005257
1
0.7485
4
2
348.15
5
1
0.046257
5
1
0.004651
1
0.594
4
2
298.15
5
1
0.208392
6
1
0.022796
1
0.594
4
2
303.15
5
1
0.153421
6
1
0.016256
1
0.594
4
2
308.15
5
1
0.11531
6
1
0.011927
1
0.594
4
2
313.15
5
1
0.086098
5
1
0.008746
1
0.594
4
2
318.15
5
1
0.069108
5
1
0.006958
1
0.594
4
2
323.15
5
1
0.057225
5
1
0.005739
1
0.594
4
2
328.15
5
1
0.046793
5
1
0.0047
1
0.594
4
2
333.15
5
1
0.040918
5
1
0.00411
1
0.594
4
2
338.15
5
1
0.033799
5
1
0.003395
1
0.594
4
2
343.15
5
1
0.029015
5
1
0.002914
1
0.594
4
2
348.15
5
1
0.025217
5
1
0.002533
1
0.4494
4
2
298.15
5
1
0.103077
6
1
0.010572
1
0.4494
4
2
303.15
5
1
0.078036
5
1
0.007886
1
0.4494
4
2
308.15
5
1
0.060141
5
1
0.006031
1
0.4494
4
2
313.15
5
1
0.047168
5
1
0.004734
1
0.4494
4
2
318.15
5
1
0.037624
5
1
0.003776
1
0.4494
4
2
323.15
5
1
0.030411
5
1
0.003052
1
0.4494
4
2
328.15
5
1
0.024876
5
1
0.002497
1
0.4494
4
2
333.15
5
1
0.0206
5
1
0.002068
1
0.4494
4
2
338.15
5
1
0.017243
5
1
0.001731
1
0.4494
4
2
343.15
5
1
0.014563
5
1
0.001462
1
0.4494
4
2
348.15
5
1
0.012161
5
1
0.001221
1
0.3015
4
2
298.15
5
1
0.043561
5
1
0.004371
1
0.3015
4
2
303.15
5
1
0.034116
5
1
0.003422
1
0.3015
4
2
308.15
5
1
0.027306
5
1
0.002739
1
0.3015
4
2
313.15
5
1
0.022036
5
1
0.002211
1
0.3015
4
2
318.15
5
1
0.01806
5
1
0.001812
1
0.3015
4
2
323.15
5
1
0.014933
5
1
0.001498
1
0.3015
4
2
328.15
5
1
0.012472
5
1
0.001251
1
0.3015
4
2
333.15
5
1
0.010476
5
1
0.001051
1
0.3015
4
2
338.15
5
1
0.008869
4
1
0.00089
1
0.3015
4
2
343.15
5
1
0.007583
4
1
0.000761
1
0.3015
4
2
348.15
5
1
0.006534
4
1
0.000655
1
0.1507
4
2
298.15
5
1
0.015273
5
1
0.001532
1
0.1507
4
2
303.15
5
1
0.012442
5
1
0.001248
1
0.1507
4
2
308.15
5
1
0.010371
5
1
0.00104
1
0.1507
4
2
313.15
5
1
0.008752
4
1
0.000878
1
0.1507
4
2
318.15
5
1
0.007451
4
1
0.000747
1
0.1507
4
2
323.15
5
1
0.006396
4
1
0.000641
1
0.1507
4
2
328.15
5
1
0.005537
4
1
0.000555
1
0.1507
4
2
333.15
5
1
0.004826
4
1
0.000484
1
0.1507
4
2
338.15
5
1
0.004237
4
1
0.000425
1
0.1507
4
2
343.15
5
1
0.003745
4
1
0.000376
1
0.1507
4
2
348.15
5
1
0.003429
4
1
0.000344
1
0
5
2
298.15
5
1
0.00252
4
1
0.000253
1
0
5
2
303.15
5
1
0.00223
4
1
0.000224
1
0
5
2
308.15
5
1
0.00198
4
1
0.000199
1
0
5
2
313.15
5
1
0.00175
4
1
0.000175
1
0
5
2
318.15
5
1
0.00156
4
1
0.000156
1
0
5
2
323.15
5
1
0.00142
4
1
0.000142
1
0
5
2
328.15
5
1
0.00127
4
1
0.000127
1
0
5
2
333.15
5
1
0.00111
4
1
0.000111
1
0
5
2
338.15
5
1
0.00101
4
1
0.000101
1
0
5
2
343.15
5
1
0.00092
3
1
9.2e-05
1
0
5
2
348.15
5
1
0.000845
3
1
8.5e-05
20
5
1
3
1
4
1
Principal objective of the work
JWM
JWM
8/15/2019
1
Amount concentration (molarity), mol/dm3
SPECTR
5
Liquid
Ratio with the reference state, X/X(REF)
Phase in equilibrium with primary phase at the same temperature and pressure
Liquid
1
Data file compiler
Propagation of evaluated standard uncertainties
95
Liquid
3
Liquid
4
1
Temperature, K
Liquid
3
298.15
5
2
Pressure, kPa
Liquid
3
101
3
1
Amount concentration (molarity), mol/dm3
5
Liquid
4
1
0.0127
3
1
0.24
2
1
0.02
1
0.0162
3
1
0.3
2
1
0.02
1
0.0224
3
1
0.36
2
1
0.02
1
0.0291
3
1
0.33
2
1
0.02
1
0.0321
3
1
0.36
2
1
0.02
1
0.0343
3
1
0.34
2
1
0.03
21
6
1
3
1
4
1
Principal objective of the work
JWM
JWM
1/8/2020
1
Amount concentration (molarity), mol/dm3
SPECTR
6
Liquid
Ratio with the reference state, X/X(REF)
Phase in equilibrium with primary phase at the same temperature and pressure
Liquid
1
Data file compiler
Propagation of evaluated standard uncertainties
95
Liquid
3
Liquid
4
1
Temperature, K
Liquid
3
298.15
5
2
Pressure, kPa
Liquid
3
101
3
1
Amount concentration (molarity), mol/dm3
6
Liquid
4
1
0.0087
2
1
0.04
1
1
0.02
1
0.0117
3
1
0.17
2
1
0.02
1
0.0202
3
1
0.31
2
1
0.02
1
0.0218
3
1
0.29
2
1
0.03
1
0.0245
3
1
0.38
2
1
0.05