2
0
2010
red
swa
1
journal
Original
Reddy, K. S.
Swamy, A. V. N.
Prasad, T. E. V.[T. E. Vittal]
Prasad, D. H. L.
Fluid Phase Equilib.
2010
2020-09-29
Bubble point measurements of binary mixtures formed by 1-hexanol with selected nitro-compounds and substituted benzenes at 95.6 kPa
Bubble point measurements (at 95.6 kPa) over the entire composition range are carried out for the binary mixtures formed by 1-hexanol with the: nitro-compounds (acetonitrile, acrylonitrile N,N-dimethyl formamide and aniline) and substituted benzenes (o-xylene, chlorobenzene, and nitrobenzene), employing a Swietoslawski type ebulliometer. Wilson model is found to represent the measured liquid phase composition versus bubble point temperature data well. Computed values of the vapor phase mole fractions and liquid phase activity coefficients are tabulated and briefly discussed.
Vapor liquid equilibria
Activity coefficients
1-Hexanol
Nitro-compounds
Substituted benzenes
10.1016/j.fluid.2010.08.010
2
298
276-279
1
InChI=1S/C6H14O/c1-2-3-4-5-6-7/h7H,2-6H2,1H3
ZSIAUFGUXNUGDI-UHFFFAOYSA-N
hexan-1-ol
1-hexanol
1-hydroxyhexane
amylcarbinol
hexyl alcohol
n-hexanol
n-hexyl alcohol
pentylcarbinol
C6H14O
1
Commercial source
1
98
2
Estimated by the compiler
2
InChI=1S/C2H3N/c1-2-3/h1H3
WEVYAHXRMPXWCK-UHFFFAOYSA-N
acetonitrile
cyanomethane
ethanenitrile
ethanonitrile
methanecarbonitrile
methyl cyanide
C2H3N
1
Commercial source
1
98
2
Estimated by the compiler
3
InChI=1S/C3H3N/c1-2-3-4/h2H,1H2
NLHHRLWOUZZQLW-UHFFFAOYSA-N
acrylonitrile
2-propenenitrile
cyanoethylene
propenenitrile
vinyl cyanide
C3H3N
1
Commercial source
1
98
2
Estimated by the compiler
4
InChI=1S/C3H7NO/c1-4(2)3-5/h3H,1-2H3
ZMXDDKWLCZADIW-UHFFFAOYSA-N
dimethylformamide
DMF
DMFA
N,N-dimethylformamide
N,N-dimethylmethanamide
dimethylformamide (DMF)
C3H7NO
1
Commercial source
1
98
2
Estimated by the compiler
5
InChI=1S/C6H7N/c7-6-4-2-1-3-5-6/h1-5H,7H2
PAYRUJLWNCNPSJ-UHFFFAOYSA-N
aniline
aminobenzene
benzeneamine
phenylamine
C6H7N
1
Commercial source
1
98
2
Estimated by the compiler
6
InChI=1S/C6H5Cl/c7-6-4-2-1-3-5-6/h1-5H
MVPPADPHJFYWMZ-UHFFFAOYSA-N
chlorobenzene
monochlorobenzene
phenyl chloride
C6H5Cl
1
Commercial source
1
98
2
Estimated by the compiler
7
InChI=1S/C6H5NO2/c8-7(9)6-4-2-1-3-5-6/h1-5H
LQNUZADURLCDLV-UHFFFAOYSA-N
nitrobenzene
C6H5NO2
1
Commercial source
1
98
2
Estimated by the compiler
8
InChI=1S/C8H10/c1-7-5-3-4-6-8(7)2/h3-6H,1-2H3
CTQNGGLPUBDAKN-UHFFFAOYSA-N
1,2-dimethylbenzene
1,2-xylene
o-xylene
ortho-xylene
C8H10
1
Commercial source
1
98
2
Estimated by the compiler
1
1
1
Principal objective of the work
DAS
TRC
12/30/2010
1
Mass density, kg/m3
Pycnometric 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
101.325
6
1
815.3
4
1
1.2
2
2
1
Principal objective of the work
DAS
TRC
12/30/2010
1
Mass density, kg/m3
Pycnometric 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
101.325
6
1
776.5
4
1
1.2
3
3
1
Principal objective of the work
DAS
TRC
12/30/2010
1
Mass density, kg/m3
Pycnometric 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
101.325
6
1
800.3
4
1
5.7
4
4
1
Principal objective of the work
DAS
TRC
12/30/2010
1
Mass density, kg/m3
Pycnometric 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
293.15
5
2
101.325
6
1
948.7
4
1
5.9
5
5
1
Principal objective of the work
DAS
TRC
12/30/2010
1
Mass density, kg/m3
Pycnometric 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
101.325
6
1
1017.3
5
1
6.1
6
6
1
Principal objective of the work
DAS
TRC
12/30/2010
1
Mass density, kg/m3
Pycnometric 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
293.15
5
2
101.325
6
1
1106
4
1
6.3
7
7
1
Principal objective of the work
DAS
TRC
12/30/2010
1
Mass density, kg/m3
Pycnometric 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
101.325
6
1
1198
4
1
6.5
8
8
1
Principal objective of the work
DAS
TRC
12/30/2010
1
Mass density, kg/m3
Pycnometric 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
101.325
6
1
875.9
4
1
5.8
9
2
1
1
1
Principal objective of the work
DAS
TRC
12/30/2010
1
Boiling temperature at pressure P, K
Ebulliometric method (Recirculating still)
Liquid
Direct value, X
1
Data file compiler
Propagation of evaluated standard uncertainties
95
Liquid
Gas
1
Pressure, kPa
Liquid
95.6
3
1
Mole fraction
2
Liquid
1
0
2
1
428.45
5
1
0.44
1
0.0846
3
1
376.35
5
1
0.75
1
0.1877
4
1
369.95
5
1
0.46
1
0.2502
4
1
368.25
5
1
0.45
1
0.2938
4
1
367.35
5
1
0.45
1
0.3563
4
1
366.05
5
1
0.45
1
0.4282
4
1
364.75
5
1
0.45
1
0.4907
4
1
363.55
5
1
0.45
1
0.5552
4
1
362.15
5
1
0.45
1
0.6177
4
1
361.15
5
1
0.45
1
0.7892
4
1
357.75
5
1
0.45
1
0.8517
4
1
356.15
5
1
0.45
1
0.9142
4
1
354.65
5
1
0.45
1
0.9767
4
1
353.15
5
1
0.45
1
1
5
1
352.55
5
1
0.44
10
2
1
1
1
Principal objective of the work
DAS
TRC
12/30/2010
1
Mole fraction
Chromatography
2
Gas
Direct value, X
1
Data file compiler
Propagation of evaluated standard uncertainties
95
Gas
Liquid
1
Mole fraction
2
Liquid
2
Temperature, K
Liquid
1
0
2
2
428.45
5
1
0
2
1
0.0846
3
2
376.35
5
1
0.8718
4
1
0.0044
1
0.1877
4
2
369.95
5
1
0.9071
4
1
0.0037
1
0.2502
4
2
368.25
5
1
0.9156
4
1
0.0034
1
0.2938
4
2
367.35
5
1
0.9293
4
1
0.0032
1
0.3563
4
2
366.05
5
1
0.9264
4
1
0.0034
1
0.4282
4
2
364.75
5
1
0.933
4
1
0.0027
1
0.4907
4
2
363.55
5
1
0.9388
4
1
0.0026
1
0.5552
4
2
362.15
5
1
0.9449
4
1
0.0025
1
0.6177
4
2
361.15
5
1
0.9512
4
1
0.0024
1
0.7892
4
2
357.75
5
1
0.9703
4
1
0.0022
1
0.8517
4
2
356.15
5
1
0.9783
4
1
0.0021
1
0.9142
4
2
354.65
5
1
0.9869
4
1
0.0021
1
0.9767
4
2
353.15
5
1
0.9963
4
1
0.002
1
1
5
2
352.55
5
1
1
5
11
3
1
1
1
Principal objective of the work
DAS
TRC
12/30/2010
1
Boiling temperature at pressure P, K
Ebulliometric method (Recirculating still)
Liquid
Direct value, X
1
Data file compiler
Propagation of evaluated standard uncertainties
95
Liquid
Gas
1
Pressure, kPa
Liquid
95.6
3
1
Mole fraction
3
Liquid
1
0
2
1
428.45
5
1
0.44
1
0.0625
3
1
406.45
5
1
0.68
1
0.125
4
1
396.45
5
1
0.52
1
0.1746
4
1
391.35
5
1
0.48
1
0.2974
4
1
381.45
5
1
0.47
1
0.3599
4
1
377.35
5
1
0.46
1
0.4585
4
1
371.45
5
1
0.46
1
0.5595
4
1
366.15
5
1
0.46
1
0.622
4
1
363.05
5
1
0.45
1
0.6819
4
1
360.45
5
1
0.45
1
0.7444
4
1
357.75
5
1
0.45
1
0.8109
4
1
355.35
5
1
0.45
1
0.8734
4
1
352.35
5
1
0.45
1
0.9449
4
1
350.55
5
1
0.45
1
1
5
1
348.95
5
1
0.44
12
3
1
1
1
Principal objective of the work
DAS
TRC
12/30/2010
1
Mole fraction
Chromatography
3
Gas
Direct value, X
1
Data file compiler
Propagation of evaluated standard uncertainties
95
Gas
Liquid
1
Mole fraction
3
Liquid
2
Temperature, K
Liquid
1
0
2
2
428.45
5
1
0
2
1
0.0625
3
2
406.45
5
1
0.5616
4
1
0.0091
1
0.125
4
2
396.45
5
1
0.7126
4
1
0.0073
1
0.1746
4
2
391.35
5
1
0.7759
4
1
0.0067
1
0.2974
4
2
381.45
5
1
0.8672
4
1
0.0046
1
0.3599
4
2
377.35
5
1
0.897
4
1
0.0035
1
0.4585
4
2
371.45
5
1
0.9313
4
1
0.0033
1
0.5595
4
2
366.15
5
1
0.9555
4
1
0.0032
1
0.622
4
2
363.05
5
1
0.9667
4
1
0.0026
1
0.6819
4
2
360.45
5
1
0.9752
4
1
0.0026
1
0.7444
4
2
357.75
5
1
0.9825
4
1
0.0021
1
0.8109
4
2
355.35
5
1
0.9886
4
1
0.0021
1
0.8734
4
2
352.35
5
1
0.9932
4
1
0.002
1
0.9449
4
2
350.55
5
1
0.9974
4
1
0.002
1
1
5
2
348.95
5
1
1
5
13
4
1
1
1
Principal objective of the work
DAS
TRC
12/30/2010
1
Boiling temperature at pressure P, K
Ebulliometric method (Recirculating still)
Liquid
Direct value, X
1
Data file compiler
Propagation of evaluated standard uncertainties
95
Liquid
Gas
1
Pressure, kPa
Liquid
95.6
3
1
Mole fraction
4
Liquid
1
0
2
1
428.45
5
1
0.44
1
0.0625
3
1
427.65
5
1
0.45
1
0.1528
4
1
426.55
5
1
0.45
1
0.2651
4
1
425.45
5
1
0.44
1
0.3276
4
1
424.95
5
1
0.45
1
0.4191
4
1
423.75
5
1
0.44
1
0.4816
4
1
423.45
5
1
0.44
1
0.5198
4
1
423.05
5
1
0.44
1
0.5823
4
1
422.75
5
1
0.44
1
0.6448
4
1
423.05
5
1
0.44
1
0.7089
4
1
422.75
5
1
0.44
1
0.7714
4
1
422.05
5
1
0.44
1
0.8297
4
1
421.75
5
1
0.44
1
0.8922
4
1
421.55
5
1
0.44
1
0.936
4
1
421.34
5
1
0.44
1
1
5
1
421.05
5
1
0.44
14
4
1
1
1
Principal objective of the work
DAS
TRC
12/30/2010
1
Mole fraction
Chromatography
4
Gas
Direct value, X
1
Data file compiler
Propagation of evaluated standard uncertainties
95
Gas
Liquid
1
Mole fraction
4
Liquid
2
Temperature, K
Liquid
1
0
2
2
428.45
5
1
0
2
1
0.0625
3
2
427.65
5
1
0.0874
3
1
0.0117
1
0.1528
4
2
426.55
5
1
0.2005
4
1
0.0066
1
0.2651
4
2
425.45
5
1
0.3254
4
1
0.005
1
0.3276
4
2
424.95
5
1
0.3897
4
1
0.0064
1
0.4191
4
2
423.75
5
1
0.479
4
1
0.0086
1
0.4816
4
2
423.45
5
1
0.5376
4
1
0.009
1
0.5198
4
2
423.05
5
1
0.5727
4
1
0.0087
1
0.5823
4
2
422.75
5
1
0.6293
4
1
0.0082
1
0.6448
4
2
423.05
5
1
0.6851
4
1
0.0075
1
0.7089
4
2
422.75
5
1
0.7418
4
1
0.0066
1
0.7714
4
2
422.05
5
1
0.7979
4
1
0.0056
1
0.8297
4
2
421.75
5
1
0.8483
4
1
0.0047
1
0.8922
4
2
421.55
5
1
0.9036
4
1
0.0037
1
0.936
4
2
421.34
5
1
0.9426
4
1
0.0032
1
1
5
2
421.05
5
1
1
5
15
5
1
1
1
Principal objective of the work
DAS
TRC
12/30/2010
1
Boiling temperature at pressure P, K
Ebulliometric method (Recirculating still)
Liquid
Direct value, X
1
Data file compiler
Propagation of evaluated standard uncertainties
95
Liquid
Gas
1
Pressure, kPa
Liquid
95.6
3
1
Mole fraction
1
Liquid
1
0
2
1
455.25
5
1
0.44
1
0.0746
3
1
451.95
5
1
0.45
1
0.195
4
1
447.25
5
1
0.45
1
0.2574
4
1
445.05
5
1
0.45
1
0.3264
4
1
442.75
5
1
0.45
1
0.3889
4
1
440.85
5
1
0.45
1
0.4468
4
1
439.25
5
1
0.45
1
0.5093
4
1
437.55
5
1
0.45
1
0.5655
4
1
436.15
5
1
0.45
1
0.628
4
1
434.65
5
1
0.45
1
0.6845
4
1
433.65
5
1
0.45
1
0.747
4
1
432.25
5
1
0.45
1
0.8668
4
1
430.15
5
1
0.45
1
0.9293
4
1
429.35
5
1
0.45
1
1
5
1
428.45
5
1
0.44
16
5
1
1
1
Principal objective of the work
DAS
TRC
12/30/2010
1
Mole fraction
Chromatography
1
Gas
Direct value, X
1
Data file compiler
Propagation of evaluated standard uncertainties
95
Gas
Liquid
1
Mole fraction
1
Liquid
2
Temperature, K
Liquid
1
0
2
2
455.25
5
1
0
2
1
0.0746
3
2
451.95
5
1
0.1534
4
1
0.0084
1
0.195
4
2
447.25
5
1
0.3537
4
1
0.0064
1
0.2574
4
2
445.05
5
1
0.4402
4
1
0.0115
1
0.3264
4
2
442.75
5
1
0.5247
4
1
0.01
1
0.3889
4
2
440.85
5
1
0.5928
4
1
0.0093
1
0.4468
4
2
439.25
5
1
0.6496
4
1
0.008
1
0.5093
4
2
437.55
5
1
0.705
4
1
0.008
1
0.5655
4
2
436.15
5
1
0.7499
4
1
0.0107
1
0.628
4
2
434.65
5
1
0.7951
4
1
0.0056
1
0.6845
4
2
433.65
5
1
0.832
4
1
0.0051
1
0.747
4
2
432.25
5
1
0.869
4
1
0.0043
1
0.8668
4
2
430.15
5
1
0.9309
4
1
0.003
1
0.9293
4
2
429.35
5
1
0.961
4
1
0.0029
1
1
5
2
428.45
5
1
1
5
17
6
1
1
1
Principal objective of the work
DAS
TRC
12/30/2010
1
Boiling temperature at pressure P, K
Ebulliometric method (Recirculating still)
Liquid
Direct value, X
1
Data file compiler
Propagation of evaluated standard uncertainties
95
Liquid
Gas
1
Pressure, kPa
Liquid
95.6
3
1
Mole fraction
6
Liquid
1
0
2
1
428.45
5
1
0.44
1
0.0625
3
1
425.35
5
1
0.45
1
0.1204
4
1
422.75
5
1
0.45
1
0.1829
4
1
420.25
5
1
0.45
1
0.2912
4
1
416.65
5
1
0.45
1
0.3537
4
1
414.85
5
1
0.45
1
0.4065
4
1
413.55
5
1
0.45
1
0.469
4
1
412.05
5
1
0.45
1
0.5228
4
1
410.85
5
1
0.45
1
0.5853
4
1
409.45
5
1
0.45
1
0.649
4
1
408.45
5
1
0.45
1
0.7115
4
1
407.35
5
1
0.45
1
0.7871
4
1
406.05
5
1
0.45
1
0.8496
4
1
405.05
5
1
0.45
1
0.9171
4
1
404.05
5
1
0.45
1
1
5
1
402.85
5
1
0.44
18
6
1
1
1
Principal objective of the work
DAS
TRC
12/30/2010
1
Mole fraction
Chromatography
6
Gas
Direct value, X
1
Data file compiler
Propagation of evaluated standard uncertainties
95
Gas
Liquid
1
Mole fraction
6
Liquid
2
Temperature, K
Liquid
1
0
2
2
428.45
5
1
0
2
1
0.0625
3
2
425.35
5
1
0.1547
4
1
0.0081
1
0.1204
4
2
422.75
5
1
0.2701
4
1
0.0076
1
0.1829
4
2
420.25
5
1
0.3722
4
1
0.0077
1
0.2912
4
2
416.65
5
1
0.5102
4
1
0.0092
1
0.3537
4
2
414.85
5
1
0.5741
4
1
0.009
1
0.4065
4
2
413.55
5
1
0.6216
4
1
0.0083
1
0.469
4
2
412.05
5
1
0.672
4
1
0.0087
1
0.5228
4
2
410.85
5
1
0.7114
4
1
0.0071
1
0.5853
4
2
409.45
5
1
0.7537
4
1
0.0063
1
0.649
4
2
408.45
5
1
0.7939
4
1
0.0059
1
0.7115
4
2
407.35
5
1
0.8314
4
1
0.0048
1
0.7871
4
2
406.05
5
1
0.8753
4
1
0.0044
1
0.8496
4
2
405.05
5
1
0.9112
4
1
0.0034
1
0.9171
4
2
404.05
5
1
0.9503
4
1
0.0029
1
1
5
2
402.85
5
1
1
5
19
7
1
1
1
Principal objective of the work
DAS
TRC
12/30/2010
1
Boiling temperature at pressure P, K
Ebulliometric method (Recirculating still)
Liquid
Direct value, X
1
Data file compiler
Propagation of evaluated standard uncertainties
95
Liquid
Gas
1
Pressure, kPa
Liquid
95.6
3
1
Mole fraction
1
Liquid
1
0
2
1
481.45
5
1
0.44
1
0.0625
3
1
474.25
5
1
0.49
1
0.1192
4
1
468.75
5
1
0.47
1
0.1817
4
1
465.55
5
1
0.47
1
0.2889
4
1
456.15
5
1
0.47
1
0.3514
4
1
452.45
5
1
0.46
1
0.4037
4
1
449.75
5
1
0.46
1
0.4662
4
1
446.65
5
1
0.45
1
0.52
4
1
444.45
5
1
0.45
1
0.5825
4
1
441.65
5
1
0.45
1
0.6464
4
1
439.15
5
1
0.45
1
0.709
4
1
436.95
5
1
0.45
1
0.7852
4
1
434.45
5
1
0.45
1
0.8477
4
1
432.45
5
1
0.45
1
0.9164
4
1
430.65
5
1
0.45
1
1
5
1
428.45
5
1
0.44
20
7
1
1
1
Principal objective of the work
DAS
TRC
12/30/2010
1
Mole fraction
Chromatography
1
Gas
Direct value, X
1
Data file compiler
Propagation of evaluated standard uncertainties
95
Gas
Liquid
1
Mole fraction
1
Liquid
2
Temperature, K
Liquid
1
0
2
2
481.45
5
1
0
2
1
0.0625
3
2
474.25
5
1
0.2139
4
1
0.0041
1
0.1192
4
2
468.75
5
1
0.3569
4
1
0.0059
1
0.1817
4
2
465.55
5
1
0.4782
4
1
0.01
1
0.2889
4
2
456.15
5
1
0.6296
4
1
0.0081
1
0.3514
4
2
452.45
5
1
0.6959
4
1
0.0075
1
0.4037
4
2
449.75
5
1
0.7425
4
1
0.0066
1
0.4662
4
2
446.65
5
1
0.79
4
1
0.0056
1
0.52
4
2
444.45
5
1
0.825
4
1
0.0061
1
0.5825
4
2
441.65
5
1
0.8602
4
1
0.0044
1
0.6464
4
2
439.15
5
1
0.891
4
1
0.0039
1
0.709
4
2
436.95
5
1
0.9171
4
1
0.0034
1
0.7852
4
2
434.45
5
1
0.9442
4
1
0.0037
1
0.8477
4
2
432.45
5
1
0.9632
4
1
0.0027
1
0.9164
4
2
430.65
5
1
0.9814
4
1
0.0186
1
1
5
2
428.45
5
1
1
5
21
8
1
1
1
Principal objective of the work
DAS
TRC
12/30/2010
1
Boiling temperature at pressure P, K
Ebulliometric method (Recirculating still)
Liquid
Direct value, X
1
Data file compiler
Propagation of evaluated standard uncertainties
95
Liquid
Gas
1
Pressure, kPa
Liquid
95.6
3
1
Mole fraction
8
Liquid
1
0
2
1
428.45
5
1
0.44
1
0.0625
3
1
427.45
5
1
0.45
1
0.1035
4
1
426.75
5
1
0.45
1
0.18
4
1
425.45
5
1
0.45
1
0.2597
4
1
424.15
5
1
0.45
1
0.3192
4
1
423.15
5
1
0.45
1
0.3654
4
1
422.45
5
1
0.45
1
0.4279
4
1
421.45
5
1
0.45
1
0.4795
4
1
420.65
5
1
0.45
1
0.556
4
1
419.55
5
1
0.45
1
0.65
4
1
418.35
5
1
0.45
1
0.7111
4
1
417.65
5
1
0.44
1
0.8233
4
1
416.55
5
1
0.44
1
0.8858
4
1
416.05
5
1
0.44
1
0.935
4
1
415.75
5
1
0.44
1
1
5
1
415.45
5
1
0.44
22
8
1
1
1
Principal objective of the work
DAS
TRC
12/30/2010
1
Mole fraction
Chromatography
8
Gas
Direct value, X
1
Data file compiler
Propagation of evaluated standard uncertainties
95
Gas
Liquid
1
Mole fraction
8
Liquid
2
Temperature, K
Liquid
1
0
2
2
428.45
5
1
0
2
1
0.0625
3
2
427.45
5
1
0.0948
3
1
0.0036
1
0.1035
4
2
426.75
5
1
0.154
4
1
0.0038
1
0.18
4
2
425.45
5
1
0.2583
4
1
0.0162
1
0.2597
4
2
424.15
5
1
0.3585
4
1
0.0057
1
0.3192
4
2
423.15
5
1
0.4279
4
1
0.0081
1
0.3654
4
2
422.45
5
1
0.4787
4
1
0.0087
1
0.4279
4
2
421.45
5
1
0.5434
4
1
0.009
1
0.4795
4
2
420.65
5
1
0.5934
4
1
0.0086
1
0.556
4
2
419.55
5
1
0.6623
4
1
0.0092
1
0.65
4
2
418.35
5
1
0.7392
4
1
0.0066
1
0.7111
4
2
417.65
5
1
0.7854
4
1
0.0058
1
0.8233
4
2
416.55
5
1
0.865
4
1
0.0043
1
0.8858
4
2
416.05
5
1
0.9087
4
1
0.0037
1
0.935
4
2
415.75
5
1
0.9449
4
1
0.0042
1
1
5
2
415.45
5
1
1
5