2
0
2010
zaf
sar
0
journal
Original
Zafarani-Moattar, M. T.[Mohammed Taghi]
Sarmad, S.[Shokat]
J. Chem. Eng. Data
2010
2020-09-29
Osmotic and Activity Coefficient of 1-Ethyl-3-methylimidazolium Bromide in Aqueous Solutions of Potassium Dihydrogen Phosphate, Dipotassium Hydrogen Phosphate, and Tripotassium Phosphate at T = 298.15 K
Vapor-liquid equilibrium data (water activity, vapor pressure, osmotic coefficient, and activity coefficient) of the mixed electrolyte aqueous solution, 1-ethyl-3-methylimidazolium bromide, [Emim][Br], + tripotassium phosphate, [Emim][Br], + dipotassium hydrogen phosphate, [Emim][Br], + potassium dihydrogen phosphate, and their corresponding binary aqueous solutions have been measured by the isopiestic method at temperature 298.15 K. The osmotic coefficients for binary aqueous solutions were correlated to the Pitzer and modified Pitzer models. From these data, the corresponding mean molal activity coefficients, ?+-, have been calculated. The activity coefficients of mixed electrolytes were calculated by Scatchard s neutral-electrolyte method. The activity results were also satisfactorily fitted to the semiempirical equation.
10.1021/je100720x
11
55
5182-5190
1
InChI=1S/3K.H3O4P/c;;;1-5(2,3)4/h;;;(H3,1,2,3,4)/q3*+1;/p-3
LWIHDJKSTIGBAC-UHFFFAOYSA-K
tripotassium phosphate
phosphoric acid, potassium salt (1:3)
potassium phosphate
K3O4P
1
Commercial source
1
98
2
Stated by supplier
2
InChI=1S/C6H11N2.BrH/c1-3-8-5-4-7(2)6-8;/h4-6H,3H2,1-2H3;1H/q+1;/p-1
GWQYPLXGJIXMMV-UHFFFAOYSA-M
1-ethyl-3-methylimidazolium bromide
C6H11BrN2
1
Commercial source
1
98
2
Stated by supplier
2
0.29
2
Karl Fischer titration
3
InChI=1S/2K.H3O4P/c;;1-5(2,3)4/h;;(H3,1,2,3,4)/q2*+1;/p-2
ZPWVASYFFYYZEW-UHFFFAOYSA-L
dipotassium hydrogen phosphate
conclyte P
dibasic potassium phosphate
dipotassium hydrogen phosphate (K2HPO4)
dipotassium monohydrogen phosphate
dipotassium monophosphate
dipotassium orthophosphate
dipotassium phosphate
dipotassium phosphate (K2HPO4)
hydrogen dipotassium phosphate
phosphoric acid, dipotassium salt
potassium monohydrogen phosphate
HK2O4P
1
Commercial source
1
99
2
Stated by supplier
4
InChI=1S/K.H3O4P/c;1-5(2,3)4/h;(H3,1,2,3,4)/q+1;/p-1
GNSKLFRGEWLPPA-UHFFFAOYSA-M
monopotassium phosphate
monobasic potassium phosphate
monopotassium dihydrogen phosphate
monopotassium orthophosphate
phosphoric acid, monopotassium salt
potassium dihydrogen phosphate
potassium dihydrogen phosphate (KH2PO4)
H2KO4P
1
Commercial source
1
99
2
Stated by supplier
5
InChI=1S/H2O/h1H2
XLYOFNOQVPJJNP-UHFFFAOYSA-N
water
H2O
1
Commercial source
1
99.9
3
Estimated by the compiler
1
5
1
2
1
Principal objective of the work
GPC
XXX
11/24/2010
1
Osmotic coefficient
ISOPIE
Liquid
Direct value, X
5
1
Data file compiler
Propagation of evaluated standard uncertainties
95
Liquid
Gas
1
Temperature, K
Liquid
298.15
5
1
Molality, mol/kg
2
Liquid
1
0.5514
4
1
0.811
3
1
0.011
1
0.6588
4
1
0.801
3
1
0.011
1
0.6883
4
1
0.799
3
1
0.011
1
0.7764
4
1
0.795
3
1
0.011
1
0.9367
4
1
0.787
3
1
0.011
1
1.0405
5
1
0.786
3
1
0.011
1
1.9432
5
1
0.763
3
1
0.011
1
2.3076
5
1
0.757
3
1
0.011
1
2.5419
5
1
0.759
3
1
0.011
1
3.1886
5
1
0.763
3
1
0.011
1
4.3588
5
1
0.786
3
1
0.011
1
5.4096
5
1
0.821
3
1
0.01
1
7.1696
5
1
0.883
3
1
0.01
2
5
1
2
1
Principal objective of the work
RDC
XXX
11/24/2010
1
(Relative) activity
Isopiestic method
5
Liquid
Direct value, X
Pure compound
1
Data file compiler
Propagation of evaluated standard uncertainties
95
Liquid
Gas
1
Temperature, K
Liquid
298.15
5
1
Mass fraction
2
Liquid
1
0.1058
4
1
0.9821
4
1
0.0004
1
0.1264
4
1
0.9787
4
1
0.0004
1
0.1449
4
1
0.9753
4
1
0.0004
1
0.1471
4
1
0.9745
4
1
0.0004
1
0.1523
4
1
0.974
4
1
0.0004
1
0.1658
4
1
0.9715
4
1
0.0004
1
0.1671
4
1
0.9711
4
1
0.0004
1
0.1788
4
1
0.9688
4
1
0.0004
1
0.1809
4
1
0.9683
4
1
0.0004
1
0.1888
4
1
0.9678
4
1
0.0004
1
0.1992
4
1
0.9645
4
1
0.0004
1
0.2073
4
1
0.9629
4
1
0.0004
1
0.2136
4
1
0.9621
4
1
0.0004
1
0.2245
4
1
0.9594
4
1
0.0004
1
0.2258
4
1
0.959
4
1
0.0004
1
0.2281
4
1
0.9589
4
1
0.0004
1
0.2471
4
1
0.9544
4
1
0.0004
1
0.2736
4
1
0.9477
4
1
0.0004
1
0.2752
4
1
0.9471
4
1
0.0004
1
0.2778
4
1
0.948
4
1
0.0004
1
0.2956
4
1
0.942
4
1
0.0004
1
0.3106
4
1
0.9379
4
1
0.0004
1
0.3268
4
1
0.9328
4
1
0.0004
1
0.3417
4
1
0.9287
4
1
0.0004
1
0.3655
4
1
0.9204
4
1
0.0004
1
0.3939
4
1
0.9098
4
1
0.0004
1
0.4176
4
1
0.8996
4
1
0.0004
1
0.4427
4
1
0.8889
4
1
0.0004
3
5
1
2
1
Principal objective of the work
RDC
XXX
11/24/2010
1
Vapor or sublimation pressure, kPa
Isopiestic method
Liquid
Direct value, X
1
Data file compiler
Propagation of evaluated standard uncertainties
95
Liquid
Gas
1
Temperature, K
Liquid
298.15
5
1
Mass fraction
2
Liquid
1
0.1058
4
1
3.118
4
1
0.004
1
0.1264
4
1
3.107
4
1
0.004
1
0.1449
4
1
3.097
4
1
0.004
1
0.1471
4
1
3.094
4
1
0.004
1
0.1523
4
1
3.092
4
1
0.004
1
0.1658
4
1
3.084
4
1
0.004
1
0.1671
4
1
3.083
4
1
0.004
1
0.1788
4
1
3.076
4
1
0.004
1
0.1809
4
1
3.074
4
1
0.004
1
0.1888
4
1
3.073
4
1
0.004
1
0.1992
4
1
3.062
4
1
0.004
1
0.2073
4
1
3.057
4
1
0.004
1
0.2136
4
1
3.054
4
1
0.004
1
0.2245
4
1
3.046
4
1
0.004
1
0.2258
4
1
3.045
4
1
0.004
1
0.2281
4
1
3.044
4
1
0.004
1
0.2471
4
1
3.03
4
1
0.005
1
0.2736
4
1
3.009
4
1
0.005
1
0.2752
4
1
3.007
4
1
0.005
1
0.2778
4
1
3.01
4
1
0.005
1
0.2956
4
1
2.991
4
1
0.005
1
0.3106
4
1
2.978
4
1
0.005
1
0.3268
4
1
2.961
4
1
0.005
1
0.3417
4
1
2.948
4
1
0.005
1
0.3655
4
1
2.922
4
1
0.006
1
0.3939
4
1
2.888
4
1
0.006
1
0.4176
4
1
2.856
4
1
0.006
1
0.4427
4
1
2.822
4
1
0.006
4
5
1
1
1
Principal objective of the work
GPC
XXX
11/24/2010
1
Osmotic coefficient
ISOPIE
Liquid
Direct value, X
5
1
Data file compiler
Propagation of evaluated standard uncertainties
95
Liquid
Gas
1
Temperature, K
Liquid
298.15
5
1
Molality, mol/kg
1
Liquid
1
0.4308
4
1
0.694
3
1
0.013
1
0.5142
4
1
0.698
3
1
0.013
1
0.6347
4
1
0.705
3
1
0.013
1
0.7575
4
1
0.708
3
1
0.013
1
0.8132
4
1
0.716
3
1
0.012
1
1.0023
5
1
0.744
3
1
0.012
1
1.0119
5
1
0.745
3
1
0.012
1
1.2412
5
1
0.778
3
1
0.011
1
1.6947
5
1
0.866
3
1
0.01
1
1.8303
5
1
0.893
3
1
0.01
5
5
1
1
1
Principal objective of the work
RDC
XXX
11/24/2010
1
(Relative) activity
Isopiestic method
5
Liquid
Direct value, X
Pure compound
1
Data file compiler
Propagation of evaluated standard uncertainties
95
Liquid
Gas
1
Temperature, K
Liquid
298.15
5
1
Mass fraction
1
Liquid
1
0.0838
3
1
0.9787
4
1
0.0004
1
0.0984
3
1
0.9745
4
1
0.0004
1
0.1187
4
1
0.9683
4
1
0.0004
1
0.1385
4
1
0.9621
4
1
0.0004
1
0.1472
4
1
0.9589
4
1
0.0004
1
0.1754
4
1
0.9477
4
1
0.0004
1
0.1768
4
1
0.9471
4
1
0.0004
1
0.2085
4
1
0.9328
4
1
0.0004
1
0.2469
4
1
0.9098
4
1
0.0004
1
0.2646
4
1
0.8996
4
1
0.0004
1
0.2798
4
1
0.8889
4
1
0.0004
6
5
1
1
1
Principal objective of the work
RDC
XXX
11/24/2010
1
Vapor or sublimation pressure, kPa
Isopiestic method
Liquid
Direct value, X
1
Data file compiler
Propagation of evaluated standard uncertainties
95
Liquid
Gas
1
Temperature, K
Liquid
298.15
5
1
Mass fraction
1
Liquid
1
0.0838
3
1
3.107
4
1
0.004
1
0.0984
3
1
3.094
4
1
0.004
1
0.1187
4
1
3.074
4
1
0.004
1
0.1385
4
1
3.054
4
1
0.004
1
0.1472
4
1
3.044
4
1
0.004
1
0.1754
4
1
3.009
4
1
0.004
1
0.1768
4
1
3.007
4
1
0.004
1
0.2085
4
1
2.961
4
1
0.004
1
0.2469
4
1
2.888
4
1
0.004
1
0.2646
4
1
2.856
4
1
0.005
1
0.2798
4
1
2.822
4
1
0.005
7
5
1
3
1
Principal objective of the work
GPC
XXX
11/24/2010
1
Osmotic coefficient
ISOPIE
Liquid
Direct value, X
5
1
Data file compiler
Propagation of evaluated standard uncertainties
95
Liquid
Gas
1
Temperature, K
Liquid
298.15
5
1
Molality, mol/kg
3
Liquid
1
0.6496
4
1
0.711
3
1
0.012
1
0.7592
4
1
0.704
3
1
0.013
1
1.1118
5
1
0.69
3
1
0.013
1
1.2506
5
1
0.69
3
1
0.013
1
1.6042
5
1
0.689
3
1
0.013
1
1.7119
5
1
0.694
3
1
0.013
1
1.9646
5
1
0.696
3
1
0.013
1
2.1627
5
1
0.709
3
1
0.013
8
5
1
3
1
Principal objective of the work
RDC
XXX
11/24/2010
1
(Relative) activity
OTHER::sMethod:Isopiestic method
5
Liquid
Direct value, X
Pure compound
1
Data file compiler
Propagation of evaluated standard uncertainties
95
Liquid
Gas
1
Temperature, K
Liquid
298.15
5
1
Mass fraction
3
Liquid
1
0.1017
4
1
0.9753
4
1
0.0004
1
0.1168
4
1
0.9715
4
1
0.0004
1
0.1622
4
1
0.9594
4
1
0.0004
1
0.1789
4
1
0.9544
4
1
0.0004
1
0.2032
4
1
0.948
4
1
0.0004
1
0.2184
4
1
0.942
4
1
0.0004
1
0.2297
4
1
0.9379
4
1
0.0004
1
0.255
4
1
0.9287
4
1
0.0004
1
0.2736
4
1
0.9204
4
1
0.0004
9
5
1
3
1
Principal objective of the work
RDC
XXX
11/24/2010
1
Vapor or sublimation pressure, kPa
OTHER::sMethod:Isopiestic method
Liquid
Direct value, X
1
Data file compiler
Propagation of evaluated standard uncertainties
95
Liquid
Gas
1
Temperature, K
Liquid
298.15
5
1
Mass fraction
3
Liquid
1
0.1017
4
1
3.097
4
1
0.003
1
0.1168
4
1
3.084
4
1
0.003
1
0.1622
4
1
3.046
4
1
0.003
1
0.1789
4
1
3.03
4
1
0.003
1
0.2032
4
1
3.01
4
1
0.004
1
0.2184
4
1
2.991
4
1
0.004
1
0.2297
4
1
2.978
4
1
0.004
1
0.255
4
1
2.948
4
1
0.004
1
0.2736
4
1
2.922
4
1
0.004
10
5
1
4
1
Principal objective of the work
GPC
XXX
11/24/2010
1
Osmotic coefficient
ISOPIE
Liquid
Direct value, X
5
1
Data file compiler
Propagation of evaluated standard uncertainties
95
Liquid
Gas
1
Temperature, K
Liquid
298.15
5
1
Molality, mol/kg
4
Liquid
1
0.6269
4
1
0.8
3
1
0.011
1
0.9843
4
1
0.744
3
1
0.012
1
1.1131
5
1
0.731
3
1
0.012
1
1.2275
5
1
0.717
3
1
0.012
1
1.2705
5
1
0.715
3
1
0.012
1
1.5077
5
1
0.696
3
1
0.013
1
1.7071
5
1
0.68
3
1
0.013
11
5
1
4
1
Principal objective of the work
RDC
XXX
11/24/2010
1
(Relative) activity
OTHER::sMethod:Isopiestic method
5
Liquid
Direct value, X
Pure compound
1
Data file compiler
Propagation of evaluated standard uncertainties
95
Liquid
Gas
1
Temperature, K
Liquid
298.15
5
1
Mass fraction
4
Liquid
1
0.0786
3
1
0.9821
4
1
0.0004
1
0.1181
4
1
0.974
4
1
0.0004
1
0.1316
4
1
0.9711
4
1
0.0004
1
0.1431
4
1
0.9688
4
1
0.0004
1
0.1484
4
1
0.9678
4
1
0.0004
1
0.1603
4
1
0.9645
4
1
0.0004
1
0.1702
4
1
0.9629
4
1
0.0004
1
0.1885
4
1
0.959
4
1
0.0004
12
5
1
4
1
Principal objective of the work
RDC
XXX
11/24/2010
1
Vapor or sublimation pressure, kPa
OTHER::sMethod:Isopiestic method
Liquid
Direct value, X
1
Data file compiler
Propagation of evaluated standard uncertainties
95
Liquid
Gas
1
Temperature, K
Liquid
298.15
5
1
Mass fraction
4
Liquid
1
0.0786
3
1
3.118
4
1
0.003
1
0.1181
4
1
3.092
4
1
0.003
1
0.1316
4
1
3.083
4
1
0.003
1
0.1431
4
1
3.076
4
1
0.003
1
0.1484
4
1
3.073
4
1
0.003
1
0.1603
4
1
3.062
4
1
0.003
1
0.1702
4
1
3.057
4
1
0.003
1
0.1885
4
1
3.045
4
1
0.004
13
5
1
1
1
2
1
Principal objective of the work
GPC
XXX
11/24/2010
1
(Relative) activity
Isopiestic method
5
Liquid
Direct value, X
Pure compound
1
Data file compiler
Propagation of evaluated standard uncertainties
95
Liquid
Gas
1
Temperature, K
Liquid
298.15
5
1
Mass fraction
2
Liquid
2
Mass fraction
1
Liquid
1
0
2
2
0.0838
3
1
0.9787
4
1
0.0004
1
0
2
2
0.0984
3
1
0.9745
4
1
0.0004
1
0
2
2
0.1187
4
1
0.9683
4
1
0.0004
1
0
2
2
0.1385
4
1
0.9621
4
1
0.0004
1
0
2
2
0.1472
4
1
0.9589
4
1
0.0004
1
0
2
2
0.1754
4
1
0.9477
4
1
0.0004
1
0
2
2
0.1768
4
1
0.9471
4
1
0.0004
1
0
2
2
0.2085
4
1
0.9328
4
1
0.0004
1
0
2
2
0.2469
4
1
0.9098
4
1
0.0004
1
0
2
2
0.2646
4
1
0.8996
4
1
0.0004
1
0
2
2
0.2798
4
1
0.8889
4
1
0.0004
1
0.0508
3
2
0.0678
3
1
0.9683
4
1
0.0004
1
0.0614
3
2
0.0434
3
1
0.9745
4
1
0.0004
1
0.0657
3
2
0.0744
3
1
0.9621
4
1
0.0004
1
0.0664
3
2
0.0807
3
1
0.9589
4
1
0.0004
1
0.0704
3
2
0.0261
3
1
0.9787
4
1
0.0004
1
0.0788
3
2
0.0984
3
1
0.9471
4
1
0.0004
1
0.0832
3
2
0.0187
3
1
0.9787
4
1
0.0004
1
0.0925
3
2
0.0245
3
1
0.9745
4
1
0.0004
1
0.094
3
2
0.085
3
1
0.9477
4
1
0.0004
1
0.0988
3
2
0.111
4
1
0.9328
4
1
0.0004
1
0.1134
4
2
0.0277
3
1
0.9683
4
1
0.0004
1
0.1173
4
2
0.1508
4
1
0.8996
4
1
0.0004
1
0.1184
4
2
0.0393
3
1
0.9621
4
1
0.0004
1
0.1187
4
2
0.1349
4
1
0.9098
4
1
0.0004
1
0.1264
4
2
0
2
1
0.9787
4
1
0.0004
1
0.1277
4
2
0.0411
3
1
0.9589
4
1
0.0004
1
0.1446
4
2
0.0538
3
1
0.9471
4
1
0.0004
1
0.1471
4
2
0
2
1
0.9745
4
1
0.0004
1
0.1546
4
2
0.1392
4
1
0.8889
4
1
0.0004
1
0.1557
4
2
0.047
3
1
0.9477
4
1
0.0004
1
0.1809
4
2
0
2
1
0.9683
4
1
0.0004
1
0.1957
4
2
0.0512
3
1
0.9328
4
1
0.0004
1
0.2136
4
2
0
2
1
0.9621
4
1
0.0004
1
0.2281
4
2
0
2
1
0.9589
4
1
0.0004
1
0.2464
4
2
0.0574
3
1
0.9098
4
1
0.0004
1
0.2564
4
2
0.0642
3
1
0.8996
4
1
0.0004
1
0.2654
4
2
0.0726
3
1
0.8889
4
1
0.0004
1
0.2736
4
2
0
2
1
0.9477
4
1
0.0004
1
0.2752
4
2
0
2
1
0.9471
4
1
0.0004
1
0.3268
4
2
0
2
1
0.9328
4
1
0.0004
1
0.3939
4
2
0
2
1
0.9098
4
1
0.0004
1
0.4176
4
2
0
2
1
0.8996
4
1
0.0004
1
0.4427
4
2
0
2
1
0.8889
4
1
0.0004
14
5
1
1
1
2
1
Principal objective of the work
GPC
XXX
11/24/2010
1
Vapor or sublimation pressure, kPa
Isopiestic method
Liquid
Direct value, X
1
Data file compiler
Propagation of evaluated standard uncertainties
95
Liquid
Gas
1
Temperature, K
Liquid
298.15
5
1
Mass fraction
2
Liquid
2
Mass fraction
1
Liquid
1
0
2
2
0.0838
3
1
3.107
4
1
0.004
1
0
2
2
0.0984
3
1
3.094
4
1
0.004
1
0
2
2
0.1187
4
1
3.074
4
1
0.004
1
0
2
2
0.1385
4
1
3.054
4
1
0.004
1
0
2
2
0.1472
4
1
3.044
4
1
0.004
1
0
2
2
0.1754
4
1
3.009
4
1
0.004
1
0
2
2
0.1768
4
1
3.007
4
1
0.004
1
0
2
2
0.2085
4
1
2.961
4
1
0.004
1
0
2
2
0.2469
4
1
2.888
4
1
0.004
1
0
2
2
0.2646
4
1
2.856
4
1
0.005
1
0
2
2
0.2798
4
1
2.822
4
1
0.005
1
0.0508
3
2
0.0678
3
1
3.074
4
1
0.004
1
0.0614
3
2
0.0434
3
1
3.094
4
1
0.004
1
0.0657
3
2
0.0744
3
1
3.054
4
1
0.004
1
0.0664
3
2
0.0807
3
1
3.044
4
1
0.004
1
0.0704
3
2
0.0261
3
1
3.107
4
1
0.004
1
0.0788
3
2
0.0984
3
1
3.007
4
1
0.004
1
0.0832
3
2
0.0187
3
1
3.107
4
1
0.004
1
0.0925
3
2
0.0245
3
1
3.094
4
1
0.004
1
0.094
3
2
0.085
3
1
3.009
4
1
0.004
1
0.0988
3
2
0.111
4
1
2.961
4
1
0.004
1
0.1134
4
2
0.0277
3
1
3.074
4
1
0.004
1
0.1173
4
2
0.1508
4
1
2.856
4
1
0.005
1
0.1184
4
2
0.0393
3
1
3.054
4
1
0.004
1
0.1187
4
2
0.1349
4
1
2.888
4
1
0.004
1
0.1264
4
2
0
2
1
3.107
4
1
0.004
1
0.1277
4
2
0.0411
3
1
3.044
4
1
0.004
1
0.1446
4
2
0.0538
3
1
3.007
4
1
0.004
1
0.1471
4
2
0
2
1
3.094
4
1
0.004
1
0.1546
4
2
0.1392
4
1
2.822
4
1
0.005
1
0.1557
4
2
0.047
3
1
3.009
4
1
0.004
1
0.1809
4
2
0
2
1
3.074
4
1
0.004
1
0.1957
4
2
0.0512
3
1
2.961
4
1
0.005
1
0.2136
4
2
0
2
1
3.054
4
1
0.004
1
0.2281
4
2
0
2
1
3.044
4
1
0.004
1
0.2464
4
2
0.0574
3
1
2.888
4
1
0.005
1
0.2564
4
2
0.0642
3
1
2.856
4
1
0.005
1
0.2654
4
2
0.0726
3
1
2.822
4
1
0.005
1
0.2736
4
2
0
2
1
3.009
4
1
0.005
1
0.2752
4
2
0
2
1
3.007
4
1
0.005
1
0.3268
4
2
0
2
1
2.961
4
1
0.005
1
0.3939
4
2
0
2
1
2.888
4
1
0.006
1
0.4176
4
2
0
2
1
2.856
4
1
0.006
1
0.4427
4
2
0
2
1
2.822
4
1
0.006
15
5
1
3
1
2
1
Principal objective of the work
GPC
XXX
11/24/2010
1
(Relative) activity
Isopiestic method
5
Liquid
Direct value, X
Pure compound
1
Data file compiler
Propagation of evaluated standard uncertainties
95
Liquid
Gas
1
Temperature, K
Liquid
298.15
5
1
Mass fraction
2
Liquid
2
Mass fraction
3
Liquid
1
0
2
2
0.1017
4
1
0.9753
4
1
0.0004
1
0
2
2
0.1168
4
1
0.9715
4
1
0.0004
1
0
2
2
0.1622
4
1
0.9594
4
1
0.0004
1
0
2
2
0.1789
4
1
0.9544
4
1
0.0004
1
0
2
2
0.2032
4
1
0.948
4
1
0.0004
1
0
2
2
0.2184
4
1
0.942
4
1
0.0004
1
0
2
2
0.2297
4
1
0.9379
4
1
0.0004
1
0
2
2
0.255
4
1
0.9287
4
1
0.0004
1
0
2
2
0.2736
4
1
0.9204
4
1
0.0004
1
0.042
3
2
0.0583
3
1
0.9753
4
1
0.0004
1
0.0569
3
2
0.0581
3
1
0.9715
4
1
0.0004
1
0.0608
3
2
0.0913
3
1
0.9594
4
1
0.0004
1
0.0699
3
2
0.0972
3
1
0.9544
4
1
0.0004
1
0.0824
3
2
0.119
4
1
0.942
4
1
0.0004
1
0.0882
3
2
0.1013
4
1
0.948
4
1
0.0004
1
0.0898
3
2
0.1423
4
1
0.9287
4
1
0.0004
1
0.0919
3
2
0.0344
3
1
0.9715
4
1
0.0004
1
0.0921
3
2
0.1193
4
1
0.9379
4
1
0.0004
1
0.0955
3
2
0.0223
3
1
0.9753
4
1
0.0004
1
0.11
4
2
0.1409
4
1
0.9204
4
1
0.0004
1
0.1302
4
2
0.0411
3
1
0.9594
4
1
0.0004
1
0.1357
4
2
0.0496
3
1
0.9544
4
1
0.0004
1
0.1449
4
2
0
2
1
0.9753
4
1
0.0004
1
0.1457
4
2
0.0599
3
1
0.948
4
1
0.0004
1
0.1658
4
2
0
2
1
0.9715
4
1
0.0004
1
0.1714
4
2
0.0535
3
1
0.942
4
1
0.0004
1
0.1798
4
2
0.0583
3
1
0.9379
4
1
0.0004
1
0.1967
4
2
0.0633
3
1
0.9287
4
1
0.0004
1
0.204
4
2
0.0723
3
1
0.9204
4
1
0.0004
1
0.2245
4
2
0
2
1
0.9594
4
1
0.0004
1
0.2471
4
2
0
2
1
0.9544
4
1
0.0004
1
0.2778
4
2
0
2
1
0.948
4
1
0.0004
1
0.2956
4
2
0
2
1
0.942
4
1
0.0004
1
0.3106
4
2
0
2
1
0.9379
4
1
0.0004
1
0.3417
4
2
0
2
1
0.9287
4
1
0.0004
1
0.3655
4
2
0
2
1
0.9204
4
1
0.0004
16
5
1
3
1
2
1
Principal objective of the work
GPC
XXX
11/24/2010
1
Vapor or sublimation pressure, kPa
Isopiestic method
Liquid
Direct value, X
1
Data file compiler
Propagation of evaluated standard uncertainties
95
Liquid
Gas
1
Temperature, K
Liquid
298.15
5
1
Mass fraction
2
Liquid
2
Mass fraction
3
Liquid
1
0
2
2
0.1017
4
1
3.097
4
1
0.003
1
0
2
2
0.1168
4
1
3.084
4
1
0.003
1
0
2
2
0.1622
4
1
3.046
4
1
0.003
1
0
2
2
0.1789
4
1
3.03
4
1
0.003
1
0
2
2
0.2032
4
1
3.01
4
1
0.004
1
0
2
2
0.2184
4
1
2.991
4
1
0.004
1
0
2
2
0.2297
4
1
2.978
4
1
0.004
1
0
2
2
0.255
4
1
2.948
4
1
0.004
1
0
2
2
0.2736
4
1
2.922
4
1
0.004
1
0.042
3
2
0.0583
3
1
3.097
4
1
0.003
1
0.0569
3
2
0.0581
3
1
3.084
4
1
0.004
1
0.0608
3
2
0.0913
3
1
3.046
4
1
0.004
1
0.0699
3
2
0.0972
3
1
3.03
4
1
0.004
1
0.0824
3
2
0.119
4
1
2.991
4
1
0.004
1
0.0882
3
2
0.1013
4
1
3.01
4
1
0.004
1
0.0898
3
2
0.1423
4
1
2.948
4
1
0.004
1
0.0919
3
2
0.0344
3
1
3.084
4
1
0.004
1
0.0921
3
2
0.1193
4
1
2.978
4
1
0.004
1
0.0955
3
2
0.0223
3
1
3.097
4
1
0.004
1
0.11
4
2
0.1409
4
1
2.922
4
1
0.004
1
0.1302
4
2
0.0411
3
1
3.046
4
1
0.004
1
0.1357
4
2
0.0496
3
1
3.03
4
1
0.004
1
0.1449
4
2
0
2
1
3.097
4
1
0.004
1
0.1457
4
2
0.0599
3
1
3.01
4
1
0.004
1
0.1658
4
2
0
2
1
3.084
4
1
0.004
1
0.1714
4
2
0.0535
3
1
2.991
4
1
0.004
1
0.1798
4
2
0.0583
3
1
2.978
4
1
0.004
1
0.1967
4
2
0.0633
3
1
2.948
4
1
0.004
1
0.204
4
2
0.0723
3
1
2.922
4
1
0.004
1
0.2245
4
2
0
2
1
3.046
4
1
0.004
1
0.2471
4
2
0
2
1
3.03
4
1
0.005
1
0.2778
4
2
0
2
1
3.01
4
1
0.005
1
0.2956
4
2
0
2
1
2.991
4
1
0.005
1
0.3106
4
2
0
2
1
2.978
4
1
0.005
1
0.3417
4
2
0
2
1
2.948
4
1
0.005
1
0.3655
4
2
0
2
1
2.922
4
1
0.006
17
5
1
4
1
2
1
Principal objective of the work
GPC
XXX
11/24/2010
1
(Relative) activity
Isopiestic method
5
Liquid
Direct value, X
Pure compound
1
Data file compiler
Propagation of evaluated standard uncertainties
95
Liquid
Gas
1
Temperature, K
Liquid
298.15
5
1
Mass fraction
2
Liquid
2
Mass fraction
4
Liquid
1
0
2
2
0.0786
3
1
0.9821
4
1
0.0004
1
0
2
2
0.1181
4
1
0.974
4
1
0.0004
1
0
2
2
0.1316
4
1
0.9711
4
1
0.0004
1
0
2
2
0.1431
4
1
0.9688
4
1
0.0004
1
0
2
2
0.1484
4
1
0.9678
4
1
0.0004
1
0
2
2
0.1603
4
1
0.9645
4
1
0.0004
1
0
2
2
0.1702
4
1
0.9629
4
1
0.0004
1
0
2
2
0.1885
4
1
0.959
4
1
0.0004
1
0.0388
3
2
0.0424
3
1
0.9821
4
1
0.0004
1
0.0464
3
2
0.0788
3
1
0.9711
4
1
0.0004
1
0.0501
3
2
0.0812
3
1
0.9678
4
1
0.0004
1
0.0517
3
2
0.0639
3
1
0.974
4
1
0.0004
1
0.0558
3
2
0.0792
3
1
0.9688
4
1
0.0004
1
0.0648
3
2
0.0919
3
1
0.9629
4
1
0.0004
1
0.0705
3
2
0.0802
3
1
0.9645
4
1
0.0004
1
0.0722
3
2
0.019
3
1
0.9821
4
1
0.0004
1
0.078
3
2
0.0932
3
1
0.959
4
1
0.0004
1
0.0922
3
2
0.0332
3
1
0.974
4
1
0.0004
1
0.101
4
2
0.0362
3
1
0.9711
4
1
0.0004
1
0.1032
4
2
0.0407
3
1
0.9688
4
1
0.0004
1
0.1058
4
2
0
2
1
0.9821
4
1
0.0004
1
0.1171
4
2
0.0387
3
1
0.9678
4
1
0.0004
1
0.1217
4
2
0.0419
3
1
0.9645
4
1
0.0004
1
0.1329
4
2
0.0392
3
1
0.9629
4
1
0.0004
1
0.1374
4
2
0.0473
3
1
0.959
4
1
0.0004
1
0.1523
4
2
0
2
1
0.974
4
1
0.0004
1
0.1671
4
2
0
2
1
0.9711
4
1
0.0004
1
0.1788
4
2
0
2
1
0.9688
4
1
0.0004
1
0.1888
4
2
0
2
1
0.9678
4
1
0.0004
1
0.1992
4
2
0
2
1
0.9645
4
1
0.0004
1
0.2073
4
2
0
2
1
0.9629
4
1
0.0004
1
0.2258
4
2
0
2
1
0.959
4
1
0.0004
18
5
1
4
1
2
1
Principal objective of the work
GPC
XXX
11/24/2010
1
Vapor or sublimation pressure, kPa
Isopiestic method
Liquid
Direct value, X
1
Data file compiler
Propagation of evaluated standard uncertainties
95
Liquid
Gas
1
Temperature, K
Liquid
298.15
5
1
Mass fraction
2
Liquid
2
Mass fraction
4
Liquid
1
0
2
2
0.0786
3
1
3.118
4
1
0.003
1
0
2
2
0.1181
4
1
3.092
4
1
0.003
1
0
2
2
0.1316
4
1
3.083
4
1
0.003
1
0
2
2
0.1431
4
1
3.076
4
1
0.003
1
0
2
2
0.1484
4
1
3.073
4
1
0.003
1
0
2
2
0.1603
4
1
3.062
4
1
0.003
1
0
2
2
0.1702
4
1
3.057
4
1
0.003
1
0
2
2
0.1885
4
1
3.045
4
1
0.004
1
0.0388
3
2
0.0424
3
1
3.118
4
1
0.003
1
0.0464
3
2
0.0788
3
1
3.083
4
1
0.004
1
0.0501
3
2
0.0812
3
1
3.073
4
1
0.004
1
0.0517
3
2
0.0639
3
1
3.092
4
1
0.004
1
0.0558
3
2
0.0792
3
1
3.076
4
1
0.004
1
0.0648
3
2
0.0919
3
1
3.057
4
1
0.004
1
0.0705
3
2
0.0802
3
1
3.062
4
1
0.004
1
0.0722
3
2
0.019
3
1
3.118
4
1
0.004
1
0.078
3
2
0.0932
3
1
3.045
4
1
0.004
1
0.0922
3
2
0.0332
3
1
3.092
4
1
0.004
1
0.101
4
2
0.0362
3
1
3.083
4
1
0.004
1
0.1032
4
2
0.0407
3
1
3.076
4
1
0.004
1
0.1058
4
2
0
2
1
3.118
4
1
0.004
1
0.1171
4
2
0.0387
3
1
3.073
4
1
0.004
1
0.1217
4
2
0.0419
3
1
3.062
4
1
0.004
1
0.1329
4
2
0.0392
3
1
3.057
4
1
0.004
1
0.1374
4
2
0.0473
3
1
3.045
4
1
0.004
1
0.1523
4
2
0
2
1
3.092
4
1
0.004
1
0.1671
4
2
0
2
1
3.083
4
1
0.004
1
0.1788
4
2
0
2
1
3.076
4
1
0.004
1
0.1888
4
2
0
2
1
3.073
4
1
0.004
1
0.1992
4
2
0
2
1
3.062
4
1
0.004
1
0.2073
4
2
0
2
1
3.057
4
1
0.004
1
0.2258
4
2
0
2
1
3.045
4
1
0.004