2
0
2010
cio
teo
1
journal
Original
Ciocirlan, O.[Oana]
Teodorescu, M.[Mariana]
Dragoescu, D.[Dana]
Iulian, O.[Olga]
Barhala, A.[Alexandru]
J. Chem. Eng. Data
2010
2020-09-29
Densities and Excess Molar Volumes of the Binary Mixtures of Cyclopentanone with Chloroalkanes at T = (288.15, 298.15, 308.15, and 318.15) K
The experimental densities of binary mixtures of cyclopentanone with 1,1,2,2-tetrachloroethane, 1,1,1-trichloroethane, trichloromethane, 1,2-dichloroethane, 1,3-dichloropropane, 1,4-dichlorobutane, and 1-chlorobutane have been measured at T = (288.15, 298.15, 308.15, and 318.15) K and atmospheric pressure, over the whole composition range. From these results, excess molar volumes, VE, have been calculated and fitted to the Redlich-Kister polynomial equation. The excess molar volumes are negative for the cyclopentanone + 1,1,2,2-tetrachloroethane, 1,1,1-trichloroethane, trichloromethane, and 1-chlorobutane systems and positive for the other three systems over almost the whole mole fraction range and temperatures studied. The variation of these properties with composition of the binary mixtures is discussed in terms of molecular interactions between components and structural effects.
10.1021/je901052w
9
55
3891-3895
1
InChI=1S/C2H2Cl4/c3-1(4)2(5)6/h1-2H
QPFMBZIOSGYJDE-UHFFFAOYSA-N
1,1,2,2-tetrachloroethane
Freon 130
R-130
acetylene tetrachloride
sym-tetrachloroethane
C2H2Cl4
1
Commercial source
1
99.8
3
Gas chromatography
2
Dried by oven heating
Molecular sieve treatment
Dried by oven heating
Molecular sieve treatment
2
InChI=1S/C2H3Cl3/c1-2(3,4)5/h1H3
UOCLXMDMGBRAIB-UHFFFAOYSA-N
1,1,1-trichloroethane
Freon 140a
R-140a
chlorotene
methylchloroform
C2H3Cl3
1
Commercial source
1
99.8
3
Gas chromatography
2
Dried by oven heating
Molecular sieve treatment
Dried by oven heating
Molecular sieve treatment
3
InChI=1S/CHCl3/c2-1(3)4/h1H
HEDRZPFGACZZDS-UHFFFAOYSA-N
trichloromethane
R-20
chloroform
freon 20
CHCl3
1
Commercial source
1
99.8
3
Gas chromatography
2
Dried by oven heating
Molecular sieve treatment
Dried by oven heating
Molecular sieve treatment
4
InChI=1S/C2H4Cl2/c3-1-2-4/h1-2H2
WSLDOOZREJYCGB-UHFFFAOYSA-N
1,2-dichloroethane
1,2-ethylene dichloride
Freon 150
R-150
C2H4Cl2
1
Commercial source
1
99.8
3
Gas chromatography
2
Dried by oven heating
Molecular sieve treatment
Dried by oven heating
Molecular sieve treatment
5
InChI=1S/C3H6Cl2/c4-2-1-3-5/h1-3H2
YHRUOJUYPBUZOS-UHFFFAOYSA-N
1,3-dichloropropane
R 270fa
propane, 1,3-dichloro-
trimethylene dichloride
C3H6Cl2
1
Commercial source
1
99.8
3
Gas chromatography
2
Dried by oven heating
Molecular sieve treatment
Dried by oven heating
Molecular sieve treatment
6
InChI=1S/C4H8Cl2/c5-3-1-2-4-6/h1-4H2
KJDRSWPQXHESDQ-UHFFFAOYSA-N
1,4-dichlorobutane
butane, 1,4-dichloro-
tetramethylene chloride
C4H8Cl2
1
Commercial source
1
99.8
3
Gas chromatography
2
Dried by oven heating
Molecular sieve treatment
Dried by oven heating
Molecular sieve treatment
7
InChI=1S/C4H9Cl/c1-2-3-4-5/h2-4H2,1H3
VFWCMGCRMGJXDK-UHFFFAOYSA-N
1-chlorobutane
butyl chloride
n-butyl chloride
C4H9Cl
1
Commercial source
1
99.8
3
Gas chromatography
2
Dried by oven heating
Molecular sieve treatment
Dried by oven heating
Molecular sieve treatment
8
InChI=1S/C5H8O/c6-5-3-1-2-4-5/h1-4H2
BGTOWKSIORTVQH-UHFFFAOYSA-N
cyclopentanone
C5H8O
1
Commercial source
1
99.8
3
Gas chromatography
2
Dried by oven heating
Molecular sieve treatment
Dried by oven heating
Molecular sieve treatment
1
1
1
Principal objective of the work
RDC
XXX
9/27/2010
1
Mass density, kg/m3
VIBTUB:UFactor:2
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
288.15
5
1
1604.78
6
1
0.56
1
298.15
5
1
1589.19
6
1
0.54
1
308.15
5
1
1573.59
6
1
0.53
1
318.15
5
1
1557.95
6
1
0.52
2
2
1
Principal objective of the work
RDC
XXX
9/27/2010
1
Mass density, kg/m3
VIBTUB:UFactor:2
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
288.15
5
1
1346.17
6
1
0.38
1
298.15
5
1
1329.49
6
1
0.37
1
308.15
5
1
1312.65
6
1
0.36
1
318.15
5
1
1295.66
6
1
0.35
3
3
1
Principal objective of the work
RDC
XXX
9/27/2010
1
Mass density, kg/m3
VIBTUB:UFactor:2
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
288.15
5
1
1492.31
6
1
0.47
1
298.15
5
1
1473.43
6
1
0.46
1
308.15
5
1
1454.33
6
1
0.45
1
318.15
5
1
1434.97
6
1
0.43
4
4
1
Principal objective of the work
RDC
XXX
9/27/2010
1
Mass density, kg/m3
VIBTUB:UFactor:2
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
288.15
5
1
1260.33
6
1
0.32
1
298.15
5
1
1245.8
6
1
0.32
1
308.15
5
1
1231.15
6
1
0.31
1
318.15
5
1
1216.35
6
1
0.3
5
5
1
Principal objective of the work
RDC
XXX
9/27/2010
1
Mass density, kg/m3
VIBTUB:UFactor:2
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
288.15
5
1
1191.92
6
1
0.29
1
298.15
5
1
1179.56
6
1
0.28
1
308.15
5
1
1167.14
6
1
0.27
1
318.15
5
1
1154.65
6
1
0.27
6
6
1
Principal objective of the work
RDC
XXX
9/27/2010
1
Mass density, kg/m3
VIBTUB:UFactor:2
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
288.15
5
1
1143.43
6
1
0.26
1
298.15
5
1
1132.5
6
1
0.26
1
308.15
5
1
1121.54
6
1
0.25
1
318.15
5
1
1110.54
6
1
0.25
7
7
1
Principal objective of the work
RDC
XXX
9/27/2010
1
Mass density, kg/m3
VIBTUB:UFactor:2
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
288.15
5
1
892.18
5
1
0.24
1
298.15
5
1
881.12
5
1
0.25
1
308.15
5
1
869.93
5
1
0.25
1
318.15
5
1
858.58
5
1
0.26
8
8
1
Principal objective of the work
RDC
XXX
9/27/2010
1
Mass density, kg/m3
VIBTUB:UFactor:2
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
288.15
5
1
953.99
5
1
0.22
1
298.15
5
1
944.35
5
1
0.23
1
308.15
5
1
934.69
5
1
0.23
1
318.15
5
1
924.99
5
1
0.23
9
1
1
8
1
Principal objective of the work
GPC
TRC
9/27/2010
1
Mass density, kg/m3
VIBTUB:UFactor:2
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
288.15
5
2
0
2
1
953.99
5
1
0.22
1
288.15
5
2
0.1209
4
1
1047.22
6
1
0.38
1
288.15
5
2
0.2041
4
1
1109.07
6
1
0.38
1
288.15
5
2
0.3218
4
1
1193.26
6
1
0.4
1
288.15
5
2
0.4139
4
1
1256.69
6
1
0.42
1
288.15
5
2
0.512
4
1
1321.38
6
1
0.44
1
288.15
5
2
0.6132
4
1
1385.46
6
1
0.47
1
288.15
5
2
0.7097
4
1
1443.91
6
1
0.5
1
288.15
5
2
0.7901
4
1
1490.55
6
1
0.52
1
288.15
5
2
0.9004
4
1
1551.95
6
1
0.56
1
288.15
5
2
1
5
1
1604.78
6
1
0.56
1
298.15
5
2
0
2
1
944.35
5
1
0.23
1
298.15
5
2
0.1209
4
1
1036.91
6
1
0.37
1
298.15
5
2
0.2041
4
1
1098.28
6
1
0.38
1
298.15
5
2
0.3218
4
1
1181.79
6
1
0.4
1
298.15
5
2
0.4139
4
1
1244.71
6
1
0.41
1
298.15
5
2
0.512
4
1
1308.82
6
1
0.44
1
298.15
5
2
0.6132
4
1
1372.29
6
1
0.46
1
298.15
5
2
0.7097
4
1
1430.16
6
1
0.49
1
298.15
5
2
0.7901
4
1
1476.32
6
1
0.51
1
298.15
5
2
0.9004
4
1
1537.02
6
1
0.55
1
298.15
5
2
1
5
1
1589.19
6
1
0.54
1
308.15
5
2
0
2
1
934.69
5
1
0.23
1
308.15
5
2
0.1209
4
1
1026.54
6
1
0.37
1
308.15
5
2
0.2041
4
1
1087.44
6
1
0.37
1
308.15
5
2
0.3218
4
1
1170.29
6
1
0.39
1
308.15
5
2
0.4139
4
1
1232.66
6
1
0.41
1
308.15
5
2
0.512
4
1
1296.19
6
1
0.43
1
308.15
5
2
0.6132
4
1
1359.06
6
1
0.45
1
308.15
5
2
0.7097
4
1
1416.37
6
1
0.48
1
308.15
5
2
0.7901
4
1
1462.03
6
1
0.5
1
308.15
5
2
0.9004
4
1
1522.06
6
1
0.53
1
308.15
5
2
1
5
1
1573.59
6
1
0.53
1
318.15
5
2
0
2
1
924.99
5
1
0.23
1
318.15
5
2
0.1209
4
1
1016.11
6
1
0.37
1
318.15
5
2
0.2041
4
1
1076.53
6
1
0.37
1
318.15
5
2
0.3218
4
1
1158.7
6
1
0.39
1
318.15
5
2
0.4139
4
1
1220.54
6
1
0.4
1
318.15
5
2
0.512
4
1
1283.5
6
1
0.42
1
318.15
5
2
0.6132
4
1
1345.77
6
1
0.45
1
318.15
5
2
0.7097
4
1
1402.5
6
1
0.47
1
318.15
5
2
0.7901
4
1
1447.69
6
1
0.49
1
318.15
5
2
0.9004
4
1
1507.05
6
1
0.52
1
318.15
5
2
1
5
1
1557.95
6
1
0.52
10
2
1
8
1
Principal objective of the work
GPC
TRC
9/27/2010
1
Mass density, kg/m3
VIBTUB:UFactor:2
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
2
Liquid
1
288.15
5
2
0
2
1
953.99
5
1
0.22
1
288.15
5
2
0.1165
4
1
1006.37
6
1
0.28
1
288.15
5
2
0.2125
4
1
1048.24
6
1
0.28
1
288.15
5
2
0.3002
4
1
1085.47
6
1
0.29
1
288.15
5
2
0.4003
4
1
1126.73
6
1
0.3
1
288.15
5
2
0.4938
4
1
1164.1
6
1
0.31
1
288.15
5
2
0.5938
4
1
1202.79
6
1
0.33
1
288.15
5
2
0.6952
4
1
1240.7
6
1
0.35
1
288.15
5
2
0.7988
4
1
1277.98
6
1
0.36
1
288.15
5
2
0.911
4
1
1316.7
6
1
0.38
1
288.15
5
2
1
5
1
1346.17
6
1
0.38
1
298.15
5
2
0
2
1
944.35
5
1
0.23
1
298.15
5
2
0.1165
4
1
995.99
5
1
0.27
1
298.15
5
2
0.2125
4
1
1037.23
6
1
0.28
1
298.15
5
2
0.3002
4
1
1073.88
6
1
0.29
1
298.15
5
2
0.4003
4
1
1114.46
6
1
0.3
1
298.15
5
2
0.4938
4
1
1151.18
6
1
0.31
1
298.15
5
2
0.5938
4
1
1189.17
6
1
0.32
1
298.15
5
2
0.6952
4
1
1226.35
6
1
0.34
1
298.15
5
2
0.7988
4
1
1262.86
6
1
0.35
1
298.15
5
2
0.911
4
1
1300.71
6
1
0.37
1
298.15
5
2
1
5
1
1329.49
6
1
0.37
1
308.15
5
2
0
2
1
934.69
5
1
0.23
1
308.15
5
2
0.1165
4
1
985.56
5
1
0.27
1
308.15
5
2
0.2125
4
1
1026.17
6
1
0.27
1
308.15
5
2
0.3002
4
1
1062.22
6
1
0.28
1
308.15
5
2
0.4003
4
1
1102.11
6
1
0.29
1
308.15
5
2
0.4938
4
1
1138.19
6
1
0.3
1
308.15
5
2
0.5938
4
1
1175.46
6
1
0.31
1
308.15
5
2
0.6952
4
1
1211.89
6
1
0.33
1
308.15
5
2
0.7988
4
1
1247.62
6
1
0.34
1
308.15
5
2
0.911
4
1
1284.6
6
1
0.36
1
308.15
5
2
1
5
1
1312.65
6
1
0.36
1
318.15
5
2
0
2
1
924.99
5
1
0.23
1
318.15
5
2
0.1165
4
1
975.08
5
1
0.28
1
318.15
5
2
0.2125
4
1
1015.04
6
1
0.27
1
318.15
5
2
0.3002
4
1
1050.49
6
1
0.28
1
318.15
5
2
0.4003
4
1
1089.7
6
1
0.28
1
318.15
5
2
0.4938
4
1
1125.09
6
1
0.29
1
318.15
5
2
0.5938
4
1
1161.64
6
1
0.31
1
318.15
5
2
0.6952
4
1
1197.32
6
1
0.32
1
318.15
5
2
0.7988
4
1
1232.24
6
1
0.34
1
318.15
5
2
0.911
4
1
1268.34
6
1
0.35
1
318.15
5
2
1
5
1
1295.66
6
1
0.35
11
3
1
8
1
Principal objective of the work
GPC
TRC
9/27/2010
1
Mass density, kg/m3
VIBTUB:UFactor:2
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
3
Liquid
1
288.15
5
2
0
2
1
953.99
5
1
0.22
1
288.15
5
2
0.1249
4
1
1016.96
6
1
0.3
1
288.15
5
2
0.2266
4
1
1069.07
6
1
0.31
1
288.15
5
2
0.3255
4
1
1120.83
6
1
0.33
1
288.15
5
2
0.4011
4
1
1161.1
6
1
0.35
1
288.15
5
2
0.5001
4
1
1214.66
6
1
0.37
1
288.15
5
2
0.5919
4
1
1265
6
1
0.39
1
288.15
5
2
0.69
4
1
1319.45
6
1
0.42
1
288.15
5
2
0.807
4
1
1384.63
6
1
0.46
1
288.15
5
2
0.906
4
1
1439.89
6
1
0.49
1
288.15
5
2
1
5
1
1492.31
6
1
0.47
1
298.15
5
2
0
2
1
944.35
5
1
0.23
1
298.15
5
2
0.1249
4
1
1006.56
6
1
0.29
1
298.15
5
2
0.2266
4
1
1058.03
6
1
0.31
1
298.15
5
2
0.3255
4
1
1109.11
6
1
0.32
1
298.15
5
2
0.4011
4
1
1148.82
6
1
0.34
1
298.15
5
2
0.5001
4
1
1201.57
6
1
0.36
1
298.15
5
2
0.5919
4
1
1251.09
6
1
0.39
1
298.15
5
2
0.69
4
1
1304.53
6
1
0.41
1
298.15
5
2
0.807
4
1
1368.39
6
1
0.45
1
298.15
5
2
0.906
4
1
1422.36
6
1
0.48
1
298.15
5
2
1
5
1
1473.43
6
1
0.46
1
308.15
5
2
0
2
1
934.69
5
1
0.23
1
308.15
5
2
0.1249
4
1
996.12
5
1
0.29
1
308.15
5
2
0.2266
4
1
1046.93
6
1
0.3
1
308.15
5
2
0.3255
4
1
1097.32
6
1
0.32
1
308.15
5
2
0.4011
4
1
1136.46
6
1
0.33
1
308.15
5
2
0.5001
4
1
1188.38
6
1
0.35
1
308.15
5
2
0.5919
4
1
1237.05
6
1
0.38
1
308.15
5
2
0.69
4
1
1289.48
6
1
0.4
1
308.15
5
2
0.807
4
1
1351.97
6
1
0.44
1
308.15
5
2
0.906
4
1
1404.64
6
1
0.46
1
308.15
5
2
1
5
1
1454.33
6
1
0.45
1
318.15
5
2
0
2
1
924.99
5
1
0.23
1
318.15
5
2
0.1249
4
1
985.6
5
1
0.29
1
318.15
5
2
0.2266
4
1
1035.75
6
1
0.3
1
318.15
5
2
0.3255
4
1
1085.43
6
1
0.31
1
318.15
5
2
0.4011
4
1
1123.98
6
1
0.33
1
318.15
5
2
0.5001
4
1
1175.07
6
1
0.35
1
318.15
5
2
0.5919
4
1
1222.87
6
1
0.37
1
318.15
5
2
0.69
4
1
1274.26
6
1
0.39
1
318.15
5
2
0.807
4
1
1335.37
6
1
0.42
1
318.15
5
2
0.906
4
1
1387
6
1
0.45
1
318.15
5
2
1
5
1
1434.97
6
1
0.43
12
4
1
8
1
Principal objective of the work
GPC
TRC
9/27/2010
1
Mass density, kg/m3
VIBTUB:UFactor:2
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
288.15
5
2
0
2
1
953.99
5
1
0.22
1
288.15
5
2
0.1186
4
1
986.57
5
1
0.24
1
288.15
5
2
0.1945
4
1
1007.9
6
1
0.24
1
288.15
5
2
0.3015
4
1
1038.6
6
1
0.25
1
288.15
5
2
0.4044
4
1
1068.85
6
1
0.26
1
288.15
5
2
0.5004
4
1
1097.68
6
1
0.27
1
288.15
5
2
0.6009
4
1
1128.64
6
1
0.28
1
288.15
5
2
0.6915
4
1
1157.24
6
1
0.3
1
288.15
5
2
0.7932
4
1
1190.15
6
1
0.31
1
288.15
5
2
0.8997
4
1
1225.7
6
1
0.33
1
288.15
5
2
1
5
1
1260.33
6
1
0.32
1
298.15
5
2
0
2
1
944.35
5
1
0.23
1
298.15
5
2
0.1186
4
1
976.53
5
1
0.24
1
298.15
5
2
0.1945
4
1
997.59
5
1
0.24
1
298.15
5
2
0.3015
4
1
1027.87
6
1
0.25
1
298.15
5
2
0.4044
4
1
1057.69
6
1
0.26
1
298.15
5
2
0.5004
4
1
1086.09
6
1
0.27
1
298.15
5
2
0.6009
4
1
1116.55
6
1
0.28
1
298.15
5
2
0.6915
4
1
1144.68
6
1
0.29
1
298.15
5
2
0.7932
4
1
1177.01
6
1
0.31
1
298.15
5
2
0.8997
4
1
1211.87
6
1
0.33
1
298.15
5
2
1
5
1
1245.8
6
1
0.32
1
308.15
5
2
0
2
1
934.69
5
1
0.23
1
308.15
5
2
0.1186
4
1
966.45
5
1
0.24
1
308.15
5
2
0.1945
4
1
987.23
5
1
0.24
1
308.15
5
2
0.3015
4
1
1017.08
6
1
0.24
1
308.15
5
2
0.4044
4
1
1046.46
6
1
0.25
1
308.15
5
2
0.5004
4
1
1074.43
6
1
0.26
1
308.15
5
2
0.6009
4
1
1104.39
6
1
0.27
1
308.15
5
2
0.6915
4
1
1132.02
6
1
0.29
1
308.15
5
2
0.7932
4
1
1163.76
6
1
0.3
1
308.15
5
2
0.8997
4
1
1197.94
6
1
0.32
1
308.15
5
2
1
5
1
1231.15
6
1
0.31
1
318.15
5
2
0
2
1
924.99
5
1
0.23
1
318.15
5
2
0.1186
4
1
956.32
5
1
0.25
1
318.15
5
2
0.1945
4
1
976.81
5
1
0.24
1
318.15
5
2
0.3015
4
1
1006.23
6
1
0.24
1
318.15
5
2
0.4044
4
1
1035.16
6
1
0.25
1
318.15
5
2
0.5004
4
1
1062.67
6
1
0.26
1
318.15
5
2
0.6009
4
1
1092.12
6
1
0.27
1
318.15
5
2
0.6915
4
1
1119.26
6
1
0.28
1
318.15
5
2
0.7932
4
1
1150.4
6
1
0.29
1
318.15
5
2
0.8997
4
1
1183.89
6
1
0.31
1
318.15
5
2
1
5
1
1216.35
6
1
0.3
13
8
1
5
1
Principal objective of the work
GPC
TRC
9/27/2010
1
Mass density, kg/m3
VIBTUB:UFactor:2
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
288.15
5
2
0
2
1
953.99
5
1
0.22
1
288.15
5
2
0.1064
4
1
980.5
5
1
0.24
1
288.15
5
2
0.1972
4
1
1002.92
6
1
0.23
1
288.15
5
2
0.2925
4
1
1026.13
6
1
0.24
1
288.15
5
2
0.3865
4
1
1048.87
6
1
0.24
1
288.15
5
2
0.4831
4
1
1071.97
6
1
0.25
1
288.15
5
2
0.5793
4
1
1094.77
6
1
0.26
1
288.15
5
2
0.6743
4
1
1117.06
6
1
0.27
1
288.15
5
2
0.7804
4
1
1141.7
6
1
0.28
1
288.15
5
2
0.8756
4
1
1163.59
6
1
0.29
1
288.15
5
2
1
5
1
1191.92
6
1
0.29
1
298.15
5
2
0
2
1
944.35
5
1
0.23
1
298.15
5
2
0.1064
4
1
970.62
5
1
0.24
1
298.15
5
2
0.1972
4
1
992.8
5
1
0.23
1
298.15
5
2
0.2925
4
1
1015.76
6
1
0.24
1
298.15
5
2
0.3865
4
1
1038.26
6
1
0.24
1
298.15
5
2
0.4831
4
1
1061.1
6
1
0.25
1
298.15
5
2
0.5793
4
1
1083.63
6
1
0.25
1
298.15
5
2
0.6743
4
1
1105.64
6
1
0.26
1
298.15
5
2
0.7804
4
1
1129.98
6
1
0.27
1
298.15
5
2
0.8756
4
1
1151.59
6
1
0.28
1
298.15
5
2
1
5
1
1179.56
6
1
0.28
1
308.15
5
2
0
2
1
934.69
5
1
0.23
1
308.15
5
2
0.1064
4
1
960.68
5
1
0.24
1
308.15
5
2
0.1972
4
1
982.63
5
1
0.24
1
308.15
5
2
0.2925
4
1
1005.35
6
1
0.23
1
308.15
5
2
0.3865
4
1
1027.59
6
1
0.24
1
308.15
5
2
0.4831
4
1
1050.16
6
1
0.24
1
308.15
5
2
0.5793
4
1
1072.43
6
1
0.25
1
308.15
5
2
0.6743
4
1
1094.17
6
1
0.26
1
308.15
5
2
0.7804
4
1
1118.21
6
1
0.27
1
308.15
5
2
0.8756
4
1
1139.54
6
1
0.28
1
308.15
5
2
1
5
1
1167.14
6
1
0.27
1
318.15
5
2
0
2
1
924.99
5
1
0.23
1
318.15
5
2
0.1064
4
1
950.7
5
1
0.24
1
318.15
5
2
0.1972
4
1
972.41
5
1
0.24
1
318.15
5
2
0.2925
4
1
994.87
5
1
0.23
1
318.15
5
2
0.3865
4
1
1016.86
6
1
0.23
1
318.15
5
2
0.4831
4
1
1039.17
6
1
0.24
1
318.15
5
2
0.5793
4
1
1061.16
6
1
0.25
1
318.15
5
2
0.6743
4
1
1082.63
6
1
0.25
1
318.15
5
2
0.7804
4
1
1106.36
6
1
0.26
1
318.15
5
2
0.8756
4
1
1127.41
6
1
0.27
1
318.15
5
2
1
5
1
1154.65
6
1
0.27
14
6
1
8
1
Principal objective of the work
GPC
TRC
9/27/2010
1
Mass density, kg/m3
VIBTUB:UFactor:2
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
6
Liquid
1
288.15
5
2
0
2
1
953.99
5
1
0.22
1
288.15
5
2
0.1103
4
1
979.25
5
1
0.23
1
288.15
5
2
0.2151
4
1
1002.02
6
1
0.23
1
288.15
5
2
0.3024
4
1
1020.17
6
1
0.23
1
288.15
5
2
0.3909
4
1
1037.87
6
1
0.23
1
288.15
5
2
0.49
4
1
1056.87
6
1
0.24
1
288.15
5
2
0.5868
4
1
1074.68
6
1
0.24
1
288.15
5
2
0.6976
4
1
1094.22
6
1
0.25
1
288.15
5
2
0.8036
4
1
1112.13
6
1
0.26
1
288.15
5
2
0.919
4
1
1130.8
6
1
0.26
1
288.15
5
2
1
5
1
1143.43
6
1
0.26
1
298.15
5
2
0
2
1
944.35
5
1
0.23
1
298.15
5
2
0.1103
4
1
969.45
5
1
0.24
1
298.15
5
2
0.2151
4
1
992.09
5
1
0.23
1
298.15
5
2
0.3024
4
1
1010.12
6
1
0.23
1
298.15
5
2
0.3909
4
1
1027.7
6
1
0.23
1
298.15
5
2
0.49
4
1
1046.56
6
1
0.24
1
298.15
5
2
0.5868
4
1
1064.25
6
1
0.24
1
298.15
5
2
0.6976
4
1
1083.64
6
1
0.25
1
298.15
5
2
0.8036
4
1
1101.43
6
1
0.25
1
298.15
5
2
0.919
4
1
1119.97
6
1
0.26
1
298.15
5
2
1
5
1
1132.5
6
1
0.26
1
308.15
5
2
0
2
1
934.69
5
1
0.23
1
308.15
5
2
0.1103
4
1
959.63
5
1
0.24
1
308.15
5
2
0.2151
4
1
982.11
5
1
0.23
1
308.15
5
2
0.3024
4
1
1000.02
6
1
0.23
1
308.15
5
2
0.3909
4
1
1017.48
6
1
0.23
1
308.15
5
2
0.49
4
1
1036.22
6
1
0.23
1
308.15
5
2
0.5868
4
1
1053.78
6
1
0.24
1
308.15
5
2
0.6976
4
1
1073.04
6
1
0.24
1
308.15
5
2
0.8036
4
1
1090.7
6
1
0.25
1
308.15
5
2
0.919
4
1
1109.1
6
1
0.25
1
308.15
5
2
1
5
1
1121.54
6
1
0.25
1
318.15
5
2
0
2
1
924.99
5
1
0.23
1
318.15
5
2
0.1103
4
1
949.76
5
1
0.24
1
318.15
5
2
0.2151
4
1
972.09
5
1
0.23
1
318.15
5
2
0.3024
4
1
989.87
5
1
0.23
1
318.15
5
2
0.3909
4
1
1007.21
6
1
0.23
1
318.15
5
2
0.49
4
1
1025.82
6
1
0.23
1
318.15
5
2
0.5868
4
1
1043.26
6
1
0.23
1
318.15
5
2
0.6976
4
1
1062.39
6
1
0.24
1
318.15
5
2
0.8036
4
1
1079.93
6
1
0.24
1
318.15
5
2
0.919
4
1
1098.19
6
1
0.25
1
318.15
5
2
1
5
1
1110.54
6
1
0.25
15
7
1
8
1
Principal objective of the work
GPC
TRC
9/27/2010
1
Mass density, kg/m3
VIBTUB:UFactor:2
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
7
Liquid
1
288.15
5
2
0
2
1
953.99
5
1
0.22
1
288.15
5
2
0.097
3
1
947.69
5
1
0.23
1
288.15
5
2
0.2041
4
1
940.85
5
1
0.23
1
288.15
5
2
0.3226
4
1
933.38
5
1
0.23
1
288.15
5
2
0.4106
4
1
928
5
1
0.23
1
288.15
5
2
0.4991
4
1
922.46
5
1
0.23
1
288.15
5
2
0.605
4
1
915.99
5
1
0.24
1
288.15
5
2
0.7051
4
1
910
5
1
0.24
1
288.15
5
2
0.7934
4
1
904.56
5
1
0.24
1
288.15
5
2
0.8965
4
1
898.44
5
1
0.24
1
288.15
5
2
1
5
1
892.18
5
1
0.24
1
298.15
5
2
0
2
1
944.35
5
1
0.23
1
298.15
5
2
0.097
3
1
937.94
5
1
0.23
1
298.15
5
2
0.2041
4
1
930.96
5
1
0.23
1
298.15
5
2
0.3226
4
1
923.32
5
1
0.23
1
298.15
5
2
0.4106
4
1
917.83
5
1
0.24
1
298.15
5
2
0.4991
4
1
912.15
5
1
0.24
1
298.15
5
2
0.605
4
1
905.53
5
1
0.24
1
298.15
5
2
0.7051
4
1
899.39
5
1
0.24
1
298.15
5
2
0.7934
4
1
893.82
5
1
0.25
1
298.15
5
2
0.8965
4
1
887.54
5
1
0.25
1
298.15
5
2
1
5
1
881.12
5
1
0.25
1
308.15
5
2
0
2
1
934.69
5
1
0.23
1
308.15
5
2
0.097
3
1
928.14
5
1
0.23
1
308.15
5
2
0.2041
4
1
921.02
5
1
0.24
1
308.15
5
2
0.3226
4
1
913.2
5
1
0.24
1
308.15
5
2
0.4106
4
1
907.58
5
1
0.24
1
308.15
5
2
0.4991
4
1
901.77
5
1
0.24
1
308.15
5
2
0.605
4
1
894.69
5
1
0.24
1
308.15
5
2
0.7051
4
1
888.68
5
1
0.25
1
308.15
5
2
0.7934
4
1
882.97
5
1
0.25
1
308.15
5
2
0.8965
4
1
876.52
5
1
0.25
1
308.15
5
2
1
5
1
869.93
5
1
0.25
1
318.15
5
2
0
2
1
924.99
5
1
0.23
1
318.15
5
2
0.097
3
1
918.29
5
1
0.24
1
318.15
5
2
0.2041
4
1
911
5
1
0.24
1
318.15
5
2
0.3226
4
1
903.01
5
1
0.24
1
318.15
5
2
0.4106
4
1
897.24
5
1
0.24
1
318.15
5
2
0.4991
4
1
891.29
5
1
0.25
1
318.15
5
2
0.605
4
1
884.33
5
1
0.25
1
318.15
5
2
0.7051
4
1
877.86
5
1
0.25
1
318.15
5
2
0.7934
4
1
871.98
5
1
0.25
1
318.15
5
2
0.8965
4
1
865.36
5
1
0.26
1
318.15
5
2
1
5
1
858.58
5
1
0.26