2
0
2010
raj
che
1
journal
Original
Rajagopal, K.[Krishnaswamy]
Chenthilnath, S.[Subramonian]
J. Chem. Eng. Data
2010
2020-09-29
Density and Viscosity of Ketones with Toluene at Different Temperatures and at Atmospheric Pressure
Densities and viscosities of binary mixtures of toluene with acetone, ethyl methyl ketone, and acetophenone including those of pure liquids are measured over the entire composition range at temperatures (298.15, 303.15, and 308.15) K, respectively, at atmospheric pressure. From these experimental data, the values of excess molar volume VmE and the deviations in viscosity ?? are calculated and fitted to the Redlich-Kister polynomial equation. The variation of these properties shows strong interaction between the molecules of the mixtures.
10.1021/je900523k
2
55
1060-1063
1
InChI=1S/C7H8/c1-7-5-3-2-4-6-7/h2-6H,1H3
YXFVVABEGXRONW-UHFFFAOYSA-N
toluene
methylbenzene
C7H8
1
Not stated in the document
1
Fractional distillation
Unspecified
Fractional distillation
Unspecified
2
98
2
Estimation
2
InChI=1S/C3H6O/c1-3(2)4/h1-2H3
CSCPPACGZOOCGX-UHFFFAOYSA-N
acetone
2-propanone
dimethyl ketone
propan-2-one
propanone
pyroacetic ether
C3H6O
1
Not stated in the document
1
Fractional distillation
2
98
2
Estimation
3
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
Not stated in the document
1
Fractional distillation
2
98
2
Estimation
4
InChI=1S/C8H8O/c1-7(9)8-5-3-2-4-6-8/h2-6H,1H3
KWOLFJPFCHCOCG-UHFFFAOYSA-N
acetophenone
1-phenyl-1-ethanone
1-phenylethanone
methyl phenyl ketone
phenyl methyl ketone
C8H8O
1
Not stated in the document
1
Fractional distillation
2
98
2
Estimation
1
1
1
Principal objective of the work
RDC
TRC
3/5/2010
1
Viscosity, Pa*s
Capillary tube (Ostwald; Ubbelohde) method
Liquid
Direct value, X
1
Data file compiler
Propagation of evaluated standard uncertainties
95
Liquid
1
Pressure, kPa
Liquid
101
3
1
Temperature, K
Liquid
1
298.15
5
1
0.0005635
4
1
7.3e-06
1
303.15
5
1
0.0005344
4
1
7e-06
1
308.15
5
1
0.0005091
4
1
6.7e-06
2
1
1
Principal objective of the work
RDC
TRC
3/5/2010
1
Speed of sound, m/s
Pulse-echo 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
298.15
5
1
1299.8
5
1
2.2
1
303.15
5
1
1279.5
5
1
2.2
1
308.15
5
1
1260.7
5
1
2.2
3
1
1
Principal objective of the work
RDC
TRC
3/5/2010
1
Mass density, kg/m3
Pycnometric 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
298.15
5
1
860.9
4
1
0.8
1
303.15
5
1
856
4
1
0.8
1
308.15
5
1
851.6
4
1
0.8
4
2
1
Principal objective of the work
RDC
TRC
3/5/2010
1
Viscosity, Pa*s
Capillary tube (Ostwald; Ubbelohde) method
Liquid
Direct value, X
1
Data file compiler
Propagation of evaluated standard uncertainties
95
Liquid
1
Pressure, kPa
Liquid
101
3
1
Temperature, K
Liquid
1
298.15
5
1
0.0003027
4
1
4.8e-06
1
303.15
5
1
0.0002918
4
1
4.7e-06
1
308.15
5
1
0.0002809
4
1
4.6e-06
5
2
1
Principal objective of the work
RDC
TRC
3/5/2010
1
Speed of sound, m/s
Pulse-echo 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
298.15
5
1
1162
5
1
2.2
1
303.15
5
1
1141.2
5
1
2.2
1
308.15
5
1
1121.4
5
1
2.2
6
2
1
Principal objective of the work
RDC
TRC
3/5/2010
1
Mass density, kg/m3
Pycnometric 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
298.15
5
1
784.3
4
1
0.7
1
303.15
5
1
779
4
1
0.7
1
308.15
5
1
773.5
4
1
0.7
7
3
1
Principal objective of the work
RDC
TRC
3/5/2010
1
Viscosity, Pa*s
Capillary tube (Ostwald; Ubbelohde) method
Liquid
Direct value, X
1
Data file compiler
Propagation of evaluated standard uncertainties
95
Liquid
1
Pressure, kPa
Liquid
101
3
1
Temperature, K
Liquid
1
298.15
5
1
0.0003856
4
1
5.3e-06
1
303.15
5
1
0.0003653
4
1
5.1e-06
1
308.15
5
1
0.000344
4
1
4.8e-06
8
3
1
Principal objective of the work
RDC
TRC
3/5/2010
1
Speed of sound, m/s
Pulse-echo 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
298.15
5
1
1191.6
5
1
2.2
1
303.15
5
1
1173.5
5
1
2.2
1
308.15
5
1
1153.8
5
1
2.2
9
3
1
Principal objective of the work
RDC
TRC
3/5/2010
1
Mass density, kg/m3
Pycnometric 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
298.15
5
1
798.2
4
1
0.7
1
303.15
5
1
794.7
4
1
0.7
1
308.15
5
1
788.5
4
1
0.7
10
4
1
Principal objective of the work
RDC
TRC
3/5/2010
1
Viscosity, Pa*s
Capillary tube (Ostwald; Ubbelohde) method
Liquid
Direct value, X
1
Data file compiler
Propagation of evaluated standard uncertainties
95
Liquid
1
Pressure, kPa
Liquid
101
3
1
Temperature, K
Liquid
1
298.15
5
1
0.0016788
5
1
1.94e-05
1
303.15
5
1
0.0015328
5
1
1.78e-05
1
308.15
5
1
0.0014073
5
1
1.64e-05
11
4
1
Principal objective of the work
RDC
TRC
3/5/2010
1
Speed of sound, m/s
Pulse-echo 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
298.15
5
1
1476.2
5
1
2.3
1
303.15
5
1
1457.2
5
1
2.3
1
308.15
5
1
1441.2
5
1
2.3
12
4
1
Principal objective of the work
RDC
TRC
3/5/2010
1
Mass density, kg/m3
Pycnometric 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
298.15
5
1
1022.4
5
1
1.1
1
303.15
5
1
1017.9
5
1
1.1
1
308.15
5
1
1013.5
5
1
1.1
13
2
1
1
1
Principal objective of the work
TKK
TRC
3/5/2010
1
Viscosity, Pa*s
Capillary tube (Ostwald; Ubbelohde) method
Liquid
Direct value, X
1
Data file compiler
Propagation of evaluated standard uncertainties
95
Liquid
1
Pressure, kPa
Liquid
101
3
1
Temperature, K
Liquid
2
Mole fraction
1
Liquid
1
298.15
5
2
0
2
1
0.0003027
4
1
4.8e-06
1
298.15
5
2
0.0702
3
1
0.0003418
4
1
5.1e-06
1
298.15
5
2
0.1468
4
1
0.0003759
4
1
5.5e-06
1
298.15
5
2
0.2269
4
1
0.0004076
4
1
5.7e-06
1
298.15
5
2
0.3135
4
1
0.0004383
4
1
6e-06
1
298.15
5
2
0.4051
4
1
0.0004662
4
1
6.3e-06
1
298.15
5
2
0.5072
4
1
0.0004893
4
1
6.5e-06
1
298.15
5
2
0.616
4
1
0.0005092
4
1
6.7e-06
1
298.15
5
2
0.7355
4
1
0.0005293
4
1
6.9e-06
1
298.15
5
2
0.8629
4
1
0.0005462
4
1
7.1e-06
1
298.15
5
2
1
5
1
0.0005635
4
1
7.3e-06
1
303.15
5
2
0
2
1
0.0002918
4
1
4.7e-06
1
303.15
5
2
0.0702
3
1
0.0003218
4
1
5e-06
1
303.15
5
2
0.1468
4
1
0.0003527
4
1
5.2e-06
1
303.15
5
2
0.2269
4
1
0.000381
4
1
5.5e-06
1
303.15
5
2
0.3135
4
1
0.0004098
4
1
5.8e-06
1
303.15
5
2
0.4051
4
1
0.0004358
4
1
6e-06
1
303.15
5
2
0.5072
4
1
0.0004553
4
1
6.2e-06
1
303.15
5
2
0.616
4
1
0.000475
4
1
6.4e-06
1
303.15
5
2
0.7355
4
1
0.0004947
4
1
6.6e-06
1
303.15
5
2
0.8629
4
1
0.0005144
4
1
6.8e-06
1
303.15
5
2
1
5
1
0.0005344
4
1
7e-06
1
308.15
5
2
0
2
1
0.0002809
4
1
4.6e-06
1
308.15
5
2
0.0702
3
1
0.0003021
4
1
4.8e-06
1
308.15
5
2
0.1468
4
1
0.0003267
4
1
5e-06
1
308.15
5
2
0.2269
4
1
0.0003517
4
1
5.2e-06
1
308.15
5
2
0.3135
4
1
0.0003785
4
1
5.5e-06
1
308.15
5
2
0.4051
4
1
0.000404
4
1
5.7e-06
1
308.15
5
2
0.5072
4
1
0.000425
4
1
5.9e-06
1
308.15
5
2
0.616
4
1
0.0004443
4
1
6.1e-06
1
308.15
5
2
0.7355
4
1
0.0004638
4
1
6.3e-06
1
308.15
5
2
0.8629
4
1
0.0004848
4
1
6.5e-06
1
308.15
5
2
1
5
1
0.0005091
4
1
6.7e-06
14
2
1
1
1
Principal objective of the work
TKK
TRC
3/5/2010
1
Speed of sound, m/s
Pulse-echo 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
1
Liquid
1
298.15
5
2
0
2
1
1162
5
1
2.2
1
298.15
5
2
0.0702
3
1
1174.8
5
1
2.2
1
298.15
5
2
0.1468
4
1
1188.7
5
1
2.2
1
298.15
5
2
0.2269
4
1
1202.5
5
1
2.2
1
298.15
5
2
0.3135
4
1
1216.6
5
1
2.2
1
298.15
5
2
0.4051
4
1
1230.8
5
1
2.2
1
298.15
5
2
0.5072
4
1
1244.7
5
1
2.2
1
298.15
5
2
0.616
4
1
1258
5
1
2.2
1
298.15
5
2
0.7355
4
1
1271.8
5
1
2.2
1
298.15
5
2
0.8629
4
1
1285.8
5
1
2.2
1
298.15
5
2
1
5
1
1299.8
5
1
2.2
1
303.15
5
2
0
2
1
1141.2
5
1
2.2
1
303.15
5
2
0.0702
3
1
1152.9
5
1
2.2
1
303.15
5
2
0.1468
4
1
1166.1
5
1
2.2
1
303.15
5
2
0.2269
4
1
1179.5
5
1
2.2
1
303.15
5
2
0.3135
4
1
1193.4
5
1
2.2
1
303.15
5
2
0.4051
4
1
1207.4
5
1
2.2
1
303.15
5
2
0.5072
4
1
1221
5
1
2.2
1
303.15
5
2
0.616
4
1
1234.7
5
1
2.2
1
303.15
5
2
0.7355
4
1
1249.2
5
1
2.2
1
303.15
5
2
0.8629
4
1
1264.2
5
1
2.2
1
303.15
5
2
1
5
1
1279.5
5
1
2.2
1
308.15
5
2
0
2
1
1121.4
5
1
2.2
1
308.15
5
2
0.0702
3
1
1132.7
5
1
2.2
1
308.15
5
2
0.1468
4
1
1145.3
5
1
2.2
1
308.15
5
2
0.2269
4
1
1158.5
5
1
2.2
1
308.15
5
2
0.3135
4
1
1172.4
5
1
2.2
1
308.15
5
2
0.4051
4
1
1186.4
5
1
2.2
1
308.15
5
2
0.5072
4
1
1200
5
1
2.2
1
308.15
5
2
0.616
4
1
1214
5
1
2.2
1
308.15
5
2
0.7355
4
1
1228.8
5
1
2.2
1
308.15
5
2
0.8629
4
1
1244.3
5
1
2.2
1
308.15
5
2
1
5
1
1260.7
5
1
2.2
15
2
1
1
1
Principal objective of the work
TKK
TRC
3/5/2010
1
Mass density, kg/m3
Pycnometric 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
1
Liquid
2
Temperature, K
Liquid
1
0
2
2
298.15
5
1
784.3
4
1
0.7
1
0
2
2
303.15
5
1
779
4
1
0.7
1
0
2
2
308.15
5
1
773.5
4
1
0.7
1
0.0702
3
2
298.15
5
1
792.5
4
1
0.7
1
0.0702
3
2
303.15
5
1
787.6
4
1
0.7
1
0.0702
3
2
308.15
5
1
782.8
4
1
0.7
1
0.1468
4
2
298.15
5
1
801.3
4
1
0.7
1
0.1468
4
2
303.15
5
1
796.7
4
1
0.7
1
0.1468
4
2
308.15
5
1
792.2
4
1
0.7
1
0.2269
4
2
298.15
5
1
810
4
1
0.7
1
0.2269
4
2
303.15
5
1
805.7
4
1
0.7
1
0.2269
4
2
308.15
5
1
801.3
4
1
0.7
1
0.3135
4
2
298.15
5
1
818.7
4
1
0.7
1
0.3135
4
2
303.15
5
1
814.4
4
1
0.7
1
0.3135
4
2
308.15
5
1
810.1
4
1
0.7
1
0.4051
4
2
298.15
5
1
827
4
1
0.7
1
0.4051
4
2
303.15
5
1
822.7
4
1
0.8
1
0.4051
4
2
308.15
5
1
818.3
4
1
0.8
1
0.5072
4
2
298.15
5
1
834.4
4
1
0.8
1
0.5072
4
2
303.15
5
1
830
4
1
0.8
1
0.5072
4
2
308.15
5
1
825.9
4
1
0.8
1
0.616
4
2
298.15
5
1
841.2
4
1
0.8
1
0.616
4
2
303.15
5
1
836.9
4
1
0.8
1
0.616
4
2
308.15
5
1
832.9
4
1
0.8
1
0.7355
4
2
298.15
5
1
847.9
4
1
0.8
1
0.7355
4
2
303.15
5
1
843.6
4
1
0.8
1
0.7355
4
2
308.15
5
1
839.6
4
1
0.8
1
0.8629
4
2
298.15
5
1
854.3
4
1
0.8
1
0.8629
4
2
303.15
5
1
849.8
4
1
0.8
1
0.8629
4
2
308.15
5
1
845.8
4
1
0.8
1
1
5
2
298.15
5
1
860.9
4
1
0.8
1
1
5
2
303.15
5
1
856
4
1
0.8
1
1
5
2
308.15
5
1
851.6
4
1
0.8
16
3
1
1
1
Principal objective of the work
TKK
TRC
3/5/2010
1
Viscosity, Pa*s
Capillary tube (Ostwald; Ubbelohde) method
Liquid
Direct value, X
1
Data file compiler
Propagation of evaluated standard uncertainties
95
Liquid
1
Pressure, kPa
Liquid
101
3
1
Temperature, K
Liquid
2
Mole fraction
1
Liquid
1
298.15
5
2
0
2
1
0.0003856
4
1
5.3e-06
1
298.15
5
2
0.0856
3
1
0.0004052
4
1
5.6e-06
1
298.15
5
2
0.1724
4
1
0.0004244
4
1
5.8e-06
1
298.15
5
2
0.2624
4
1
0.0004439
4
1
6e-06
1
298.15
5
2
0.337
4
1
0.0004594
4
1
6.2e-06
1
298.15
5
2
0.433
4
1
0.0004781
4
1
6.5e-06
1
298.15
5
2
0.5555
4
1
0.0004987
4
1
6.7e-06
1
298.15
5
2
0.66
4
1
0.0005145
4
1
6.9e-06
1
298.15
5
2
0.769
4
1
0.0005308
4
1
7.1e-06
1
298.15
5
2
0.8831
4
1
0.0005472
4
1
7.3e-06
1
298.15
5
2
1
5
1
0.0005635
4
1
7.5e-06
1
303.15
5
2
0
2
1
0.0003653
4
1
5.1e-06
1
303.15
5
2
0.0856
3
1
0.0003822
4
1
5.3e-06
1
303.15
5
2
0.1724
4
1
0.0003996
4
1
5.5e-06
1
303.15
5
2
0.2624
4
1
0.0004176
4
1
5.7e-06
1
303.15
5
2
0.337
4
1
0.000432
4
1
5.9e-06
1
303.15
5
2
0.433
4
1
0.0004494
4
1
6.1e-06
1
303.15
5
2
0.5555
4
1
0.0004688
4
1
6.3e-06
1
303.15
5
2
0.66
4
1
0.0004844
4
1
6.5e-06
1
303.15
5
2
0.769
4
1
0.0005002
4
1
6.7e-06
1
303.15
5
2
0.8831
4
1
0.0005168
4
1
6.9e-06
1
303.15
5
2
1
5
1
0.0005344
4
1
7.1e-06
1
308.15
5
2
0
2
1
0.000344
4
1
4.8e-06
1
308.15
5
2
0.0856
3
1
0.0003593
4
1
5e-06
1
308.15
5
2
0.1724
4
1
0.0003756
4
1
5.2e-06
1
308.15
5
2
0.2624
4
1
0.0003922
4
1
5.4e-06
1
308.15
5
2
0.337
4
1
0.0004061
4
1
5.6e-06
1
308.15
5
2
0.433
4
1
0.000423
4
1
5.8e-06
1
308.15
5
2
0.5555
4
1
0.0004417
4
1
6e-06
1
308.15
5
2
0.66
4
1
0.0004575
4
1
6.2e-06
1
308.15
5
2
0.769
4
1
0.0004738
4
1
6.4e-06
1
308.15
5
2
0.8831
4
1
0.0004909
4
1
6.6e-06
1
308.15
5
2
1
5
1
0.0005091
4
1
6.8e-06
17
3
1
1
1
Principal objective of the work
TKK
TRC
3/5/2010
1
Speed of sound, m/s
Pulse-echo 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
1
Liquid
1
298.15
5
2
0
2
1
1191.6
5
1
2.2
1
298.15
5
2
0.0856
3
1
1205.5
5
1
2.2
1
298.15
5
2
0.1724
4
1
1218.5
5
1
2.2
1
298.15
5
2
0.2624
4
1
1231.6
5
1
2.2
1
298.15
5
2
0.337
4
1
1241.7
5
1
2.2
1
298.15
5
2
0.433
4
1
1253.4
5
1
2.2
1
298.15
5
2
0.5555
4
1
1264.8
5
1
2.2
1
298.15
5
2
0.66
4
1
1273.5
5
1
2.2
1
298.15
5
2
0.769
4
1
1282.2
5
1
2.2
1
298.15
5
2
0.8831
4
1
1291.2
5
1
2.2
1
298.15
5
2
1
5
1
1299.8
5
1
2.2
1
303.15
5
2
0
2
1
1173.5
5
1
2.2
1
303.15
5
2
0.0856
3
1
1185.9
5
1
2.2
1
303.15
5
2
0.1724
4
1
1198.2
5
1
2.2
1
303.15
5
2
0.2624
4
1
1210.5
5
1
2.2
1
303.15
5
2
0.337
4
1
1220.3
5
1
2.2
1
303.15
5
2
0.433
4
1
1231.5
5
1
2.2
1
303.15
5
2
0.5555
4
1
1242.9
5
1
2.2
1
303.15
5
2
0.66
4
1
1251.8
5
1
2.2
1
303.15
5
2
0.769
4
1
1260.7
5
1
2.2
1
303.15
5
2
0.8831
4
1
1269.8
5
1
2.2
1
303.15
5
2
1
5
1
1279.5
5
1
2.2
1
308.15
5
2
0
2
1
1153.8
5
1
2.2
1
308.15
5
2
0.0856
3
1
1165.1
5
1
2.2
1
308.15
5
2
0.1724
4
1
1176.8
5
1
2.2
1
308.15
5
2
0.2624
4
1
1188.9
5
1
2.2
1
308.15
5
2
0.337
4
1
1198.7
5
1
2.2
1
308.15
5
2
0.433
4
1
1210.3
5
1
2.2
1
308.15
5
2
0.5555
4
1
1221.9
5
1
2.2
1
308.15
5
2
0.66
4
1
1231.1
5
1
2.2
1
308.15
5
2
0.769
4
1
1240.3
5
1
2.2
1
308.15
5
2
0.8831
4
1
1250.2
5
1
2.2
1
308.15
5
2
1
5
1
1260.7
5
1
2.2
18
3
1
1
1
Principal objective of the work
TKK
TRC
3/5/2010
1
Mass density, kg/m3
Pycnometric 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
1
Liquid
1
298.15
5
2
0
2
1
798.2
4
1
0.7
1
298.15
5
2
0.0856
3
1
805.3
4
1
0.7
1
298.15
5
2
0.1724
4
1
812.3
4
1
0.7
1
298.15
5
2
0.2624
4
1
819.3
4
1
0.7
1
298.15
5
2
0.337
4
1
824.8
4
1
0.7
1
298.15
5
2
0.433
4
1
831.4
4
1
0.8
1
298.15
5
2
0.5555
4
1
838.8
4
1
0.8
1
298.15
5
2
0.66
4
1
844.6
4
1
0.8
1
298.15
5
2
0.769
4
1
850.3
4
1
0.8
1
298.15
5
2
0.8831
4
1
855.8
4
1
0.8
1
298.15
5
2
1
5
1
860.9
4
1
0.8
1
303.15
5
2
0
2
1
794.7
4
1
0.7
1
303.15
5
2
0.0856
3
1
802
4
1
0.7
1
303.15
5
2
0.1724
4
1
809.1
4
1
0.7
1
303.15
5
2
0.2624
4
1
816
4
1
0.7
1
303.15
5
2
0.337
4
1
821.4
4
1
0.7
1
303.15
5
2
0.433
4
1
827.8
4
1
0.8
1
303.15
5
2
0.5555
4
1
835
4
1
0.8
1
303.15
5
2
0.66
4
1
840.7
4
1
0.8
1
303.15
5
2
0.769
4
1
846.2
4
1
0.8
1
303.15
5
2
0.8831
4
1
851.4
4
1
0.8
1
303.15
5
2
1
5
1
856
4
1
0.8
1
308.15
5
2
0
2
1
788.5
4
1
0.7
1
308.15
5
2
0.0856
3
1
796.3
4
1
0.7
1
308.15
5
2
0.1724
4
1
803.8
4
1
0.7
1
308.15
5
2
0.2624
4
1
810.9
4
1
0.7
1
308.15
5
2
0.337
4
1
816.5
4
1
0.8
1
308.15
5
2
0.433
4
1
823
4
1
0.8
1
308.15
5
2
0.5555
4
1
830.4
4
1
0.8
1
308.15
5
2
0.66
4
1
836.2
4
1
0.8
1
308.15
5
2
0.769
4
1
841.9
4
1
0.8
1
308.15
5
2
0.8831
4
1
847.2
4
1
0.8
1
308.15
5
2
1
5
1
851.6
4
1
0.8
19
4
1
1
1
Principal objective of the work
TKK
TRC
3/5/2010
1
Viscosity, Pa*s
Capillary tube (Ostwald; Ubbelohde) method
Liquid
Direct value, X
1
Data file compiler
Propagation of evaluated standard uncertainties
95
Liquid
1
Pressure, kPa
Liquid
101
3
1
Temperature, K
Liquid
2
Mole fraction
1
Liquid
1
298.15
5
2
0
2
1
0.0016788
5
1
1.94e-05
1
298.15
5
2
0.1093
4
1
0.0015606
5
1
1.81e-05
1
298.15
5
2
0.2145
4
1
0.0014457
5
1
1.68e-05
1
298.15
5
2
0.3206
4
1
0.0013292
5
1
1.55e-05
1
298.15
5
2
0.4281
4
1
0.0012105
5
1
1.42e-05
1
298.15
5
2
0.5229
4
1
0.0011055
5
1
1.3e-05
1
298.15
5
2
0.6213
4
1
0.0009949
4
1
1.18e-05
1
298.15
5
2
0.7157
4
1
0.0008879
4
1
1.07e-05
1
298.15
5
2
0.8392
4
1
0.0007472
4
1
9.2e-06
1
298.15
5
2
0.9074
4
1
0.0006694
4
1
8.4e-06
1
298.15
5
2
1
5
1
0.0005635
4
1
7.3e-06
1
303.15
5
2
0
2
1
0.0015328
5
1
1.78e-05
1
303.15
5
2
0.1093
4
1
0.0014257
5
1
1.66e-05
1
303.15
5
2
0.2145
4
1
0.0013225
5
1
1.54e-05
1
303.15
5
2
0.3206
4
1
0.001218
5
1
1.42e-05
1
303.15
5
2
0.4281
4
1
0.0011121
5
1
1.31e-05
1
303.15
5
2
0.5229
4
1
0.001018
5
1
1.21e-05
1
303.15
5
2
0.6213
4
1
0.0009188
4
1
1.1e-05
1
303.15
5
2
0.7157
4
1
0.0008233
4
1
1e-05
1
303.15
5
2
0.8392
4
1
0.0006978
4
1
8.7e-06
1
303.15
5
2
0.9074
4
1
0.0006286
4
1
7.9e-06
1
303.15
5
2
1
5
1
0.0005344
4
1
7e-06
1
308.15
5
2
0
2
1
0.0014073
5
1
1.64e-05
1
308.15
5
2
0.1093
4
1
0.0013102
5
1
1.53e-05
1
308.15
5
2
0.2145
4
1
0.001217
5
1
1.42e-05
1
308.15
5
2
0.3206
4
1
0.0011228
5
1
1.32e-05
1
308.15
5
2
0.4281
4
1
0.0010272
5
1
1.22e-05
1
308.15
5
2
0.5229
4
1
0.0009425
4
1
1.13e-05
1
308.15
5
2
0.6213
4
1
0.0008535
4
1
1.03e-05
1
308.15
5
2
0.7157
4
1
0.0007678
4
1
9.4e-06
1
308.15
5
2
0.8392
4
1
0.0006554
4
1
8.2e-06
1
308.15
5
2
0.9074
4
1
0.0005933
4
1
7.6e-06
1
308.15
5
2
1
5
1
0.0005091
4
1
6.7e-06
20
4
1
1
1
Principal objective of the work
TKK
TRC
3/5/2010
1
Speed of sound, m/s
Pulse-echo 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
1
Liquid
1
298.15
5
2
0
2
1
1476.2
5
1
2.3
1
298.15
5
2
0.1093
4
1
1463.8
5
1
2.3
1
298.15
5
2
0.2145
4
1
1449.6
5
1
2.3
1
298.15
5
2
0.3206
4
1
1434.7
5
1
2.3
1
298.15
5
2
0.4281
4
1
1417.5
5
1
2.3
1
298.15
5
2
0.5229
4
1
1401
5
1
2.3
1
298.15
5
2
0.6213
4
1
1381.9
5
1
2.3
1
298.15
5
2
0.7157
4
1
1362.6
5
1
2.3
1
298.15
5
2
0.8392
4
1
1336.6
5
1
2.2
1
298.15
5
2
0.9074
4
1
1321.1
5
1
2.2
1
298.15
5
2
1
5
1
1299.8
5
1
2.2
1
303.15
5
2
0
2
1
1457.2
5
1
2.3
1
303.15
5
2
0.1093
4
1
1440.8
5
1
2.3
1
303.15
5
2
0.2145
4
1
1425.8
5
1
2.3
1
303.15
5
2
0.3206
4
1
1410.6
5
1
2.3
1
303.15
5
2
0.4281
4
1
1394.6
5
1
2.3
1
303.15
5
2
0.5229
4
1
1379
5
1
2.3
1
303.15
5
2
0.6213
4
1
1359.6
5
1
2.3
1
303.15
5
2
0.7157
4
1
1339.8
5
1
2.2
1
303.15
5
2
0.8392
4
1
1313.9
5
1
2.2
1
303.15
5
2
0.9074
4
1
1299.4
5
1
2.2
1
303.15
5
2
1
5
1
1279.5
5
1
2.2
1
308.15
5
2
0
2
1
1441.2
5
1
2.3
1
308.15
5
2
0.1093
4
1
1423.3
5
1
2.3
1
308.15
5
2
0.2145
4
1
1407.6
5
1
2.3
1
308.15
5
2
0.3206
4
1
1391.3
5
1
2.3
1
308.15
5
2
0.4281
4
1
1374.8
5
1
2.3
1
308.15
5
2
0.5229
4
1
1358.9
5
1
2.3
1
308.15
5
2
0.6213
4
1
1339.4
5
1
2.2
1
308.15
5
2
0.7157
4
1
1319.7
5
1
2.2
1
308.15
5
2
0.8392
4
1
1294.2
5
1
2.2
1
308.15
5
2
0.9074
4
1
1279.4
5
1
2.2
1
308.15
5
2
1
5
1
1260.7
5
1
2.2
21
4
1
1
1
Principal objective of the work
TKK
TRC
3/5/2010
1
Mass density, kg/m3
Pycnometric 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
1
Liquid
1
298.15
5
2
0
2
1
1022.4
5
1
1.1
1
298.15
5
2
0.1093
4
1
1006.8
5
1
1.1
1
298.15
5
2
0.2145
4
1
991.7
4
1
1
1
298.15
5
2
0.3206
4
1
975.9
4
1
1
1
298.15
5
2
0.4281
4
1
959.5
4
1
1
1
298.15
5
2
0.5229
4
1
944.5
4
1
1
1
298.15
5
2
0.6213
4
1
928.2
4
1
0.9
1
298.15
5
2
0.7157
4
1
912.1
4
1
0.9
1
298.15
5
2
0.8392
4
1
890.4
4
1
0.9
1
298.15
5
2
0.9074
4
1
878
4
1
0.8
1
298.15
5
2
1
5
1
860.9
4
1
0.8
1
303.15
5
2
0
2
1
1017.9
5
1
1.1
1
303.15
5
2
0.1093
4
1
1002.7
5
1
1.1
1
303.15
5
2
0.2145
4
1
987.4
4
1
1
1
303.15
5
2
0.3206
4
1
971.7
4
1
1
1
303.15
5
2
0.4281
4
1
955.1
4
1
1
1
303.15
5
2
0.5229
4
1
940
4
1
1
1
303.15
5
2
0.6213
4
1
923.7
4
1
0.9
1
303.15
5
2
0.7157
4
1
907.6
4
1
0.9
1
303.15
5
2
0.8392
4
1
885.9
4
1
0.9
1
303.15
5
2
0.9074
4
1
873.5
4
1
0.8
1
303.15
5
2
1
5
1
856
4
1
0.8
1
308.15
5
2
0
2
1
1013.5
5
1
1.1
1
308.15
5
2
0.1093
4
1
998.7
4
1
1.1
1
308.15
5
2
0.2145
4
1
983.5
4
1
1
1
308.15
5
2
0.3206
4
1
967.8
4
1
1
1
308.15
5
2
0.4281
4
1
951
3
1
2
1
308.15
5
2
0.5229
4
1
936
4
1
1
1
308.15
5
2
0.6213
4
1
919.6
4
1
0.9
1
308.15
5
2
0.7157
4
1
903.5
4
1
0.9
1
308.15
5
2
0.8392
4
1
881.8
4
1
0.9
1
308.15
5
2
0.9074
4
1
869.5
4
1
0.8
1
308.15
5
2
1
5
1
851.6
4
1
0.8