Contents
Physical Properties
Temperature Dependent Properties
Pressure Dependent Properties
Datasets
Correlations
Similar Compounds
Mixtures
Sources
Physical Properties
Temperature Dependent Properties
Property
Value
Unit
Temperature (K)
Source
Cp,gas
[130.08; 171.46]
J/mol×K
[371.20; 500.20]
Cp,gas
130.08 ± 0.26
J/mol×K
371.20
NIST
Cp,gas
140.20
J/mol×K
390.00
NIST
Cp,gas
137.20 ± 1.30
J/mol×K
393.00
NIST
Cp,gas
138.87 ± 0.27
J/mol×K
396.20
NIST
Cp,gas
146.40
J/mol×K
410.00
NIST
Cp,gas
149.16 ± 0.30
J/mol×K
427.20
NIST
Cp,gas
149.40 ± 1.70
J/mol×K
428.00
NIST
Cp,gas
160.33 ± 0.32
J/mol×K
462.20
NIST
Cp,gas
159.00 ± 1.70
J/mol×K
463.00
NIST
Cp,gas
171.46 ± 0.34
J/mol×K
500.20
NIST
Cp,liquid
[138.39; 175.10]
J/mol×K
[228.15; 353.20]
Cp,liquid
139.13
J/mol×K
228.15
Isobari...
Cp,liquid
138.39
J/mol×K
228.15
Isobari...
Cp,liquid
140.79
J/mol×K
238.15
Isobari...
Cp,liquid
140.97
J/mol×K
238.15
Isobari...
Cp,liquid
157.65
J/mol×K
303.15
Isobari...
Cp,liquid
159.03
J/mol×K
303.15
Isobari...
Cp,liquid
159.10
J/mol×K
303.20
Heat ca...
Cp,liquid
160.40
J/mol×K
308.20
Heat ca...
Cp,liquid
162.35
J/mol×K
313.15
Isobari...
Cp,liquid
161.98
J/mol×K
313.15
Isobari...
Cp,liquid
161.60
J/mol×K
313.20
Heat ca...
Cp,liquid
163.00
J/mol×K
318.20
Heat ca...
Cp,liquid
164.10
J/mol×K
323.20
Heat ca...
Cp,liquid
165.50
J/mol×K
328.20
Heat ca...
Cp,liquid
167.00
J/mol×K
333.20
Heat ca...
Cp,liquid
168.60
J/mol×K
338.20
Heat ca...
Cp,liquid
170.40
J/mol×K
343.20
Heat ca...
Cp,liquid
172.80
J/mol×K
348.20
Heat ca...
Cp,liquid
175.10
J/mol×K
353.20
Heat ca...
η
[0.0002860; 0.0006657]
Pa×s
[283.15; 363.15]
η
0.0006657
Pa×s
283.15
Density...
η
0.0006300
Pa×s
288.15
Viscosi...
η
0.0005958
Pa×s
293.15
Density...
η
0.0005880
Pa×s
293.15
Viscosi...
η
0.0005530
Pa×s
298.15
Densiti...
η
0.0005540
Pa×s
298.15
Excess ...
η
0.0005500
Pa×s
298.15
Densiti...
η
0.0005540
Pa×s
298.15
Densiti...
η
0.0005635
Pa×s
298.15
Excess ...
η
0.0005531
Pa×s
298.15
Ultraso...
η
0.0005635
Pa×s
298.15
Density...
η
0.0005560
Pa×s
298.15
Viscosi...
η
0.0005530
Pa×s
298.15
Densiti...
η
0.0005635
Pa×s
298.15
Molecul...
η
0.0005580
Pa×s
298.15
Density...
η
0.0005220
Pa×s
303.15
Densiti...
η
0.0005250
Pa×s
303.15
Densiti...
η
0.0005344
Pa×s
303.15
Excess ...
η
0.0005344
Pa×s
303.15
Density...
η
0.0005230
Pa×s
303.15
Densiti...
η
0.0005344
Pa×s
303.15
Molecul...
η
0.0005368
Pa×s
303.15
Density...
η
0.0005250
Pa×s
303.15
Thermod...
η
0.0005250
Pa×s
303.15
Densiti...
η
0.0005253
Pa×s
303.15
Densiti...
η
0.0005251
Pa×s
303.15
Excess ...
η
0.0005230
Pa×s
303.15
Viscosi...
η
0.0005260
Pa×s
303.15
Density...
η
0.0005020
Pa×s
308.15
Ultraso...
η
0.0004960
Pa×s
308.15
Density...
η
0.0004980
Pa×s
308.15
Densiti...
η
0.0005091
Pa×s
308.15
Molecul...
η
0.0005091
Pa×s
308.15
Density...
η
0.0004933
Pa×s
308.15
Densiti...
η
0.0004990
Pa×s
308.15
Densiti...
η
0.0005091
Pa×s
308.15
Excess ...
η
0.0004940
Pa×s
308.15
Viscome...
η
0.0004755
Pa×s
313.15
Viscome...
η
0.0004676
Pa×s
313.15
Viscome...
η
0.0004859
Pa×s
313.15
Density...
η
0.0004700
Pa×s
313.15
Thermod...
η
0.0004700
Pa×s
313.15
Densiti...
η
0.0004700
Pa×s
313.15
Density...
η
0.0004710
Pa×s
313.15
Densiti...
η
0.0004717
Pa×s
313.15
Densiti...
η
0.0004710
Pa×s
313.15
Densiti...
η
0.0004670
Pa×s
313.15
Densiti...
η
0.0004491
Pa×s
318.15
Densiti...
η
0.0004460
Pa×s
318.15
Densiti...
η
0.0004379
Pa×s
318.15
Ultraso...
η
0.0004408
Pa×s
323.15
Density...
η
0.0004210
Pa×s
323.15
Densiti...
η
0.0004220
Pa×s
323.15
Densiti...
η
0.0004229
Pa×s
323.15
Excess ...
η
0.0004230
Pa×s
323.15
Thermod...
η
0.0004230
Pa×s
323.15
Densiti...
η
0.0004244
Pa×s
323.15
Densiti...
η
0.0004082
Pa×s
328.15
Densiti...
η
0.0003835
Pa×s
333.15
Densiti...
η
0.0003850
Pa×s
333.15
Thermod...
η
0.0003850
Pa×s
333.15
Densiti...
η
0.0003810
Pa×s
333.15
Densiti...
η
0.0003500
Pa×s
343.15
Thermod...
η
0.0003500
Pa×s
343.15
Densiti...
η
0.0003490
Pa×s
343.15
Densiti...
η
0.0003230
Pa×s
353.15
Thermod...
η
0.0003210
Pa×s
353.15
Densiti...
η
0.0003100
Pa×s
353.15
Densiti...
η
0.0002860
Pa×s
363.15
Densiti...
Δfus H
[6.55; 6.64]
kJ/mol
[177.95; 178.15]
Δfus H
6.62
kJ/mol
177.95
NIST
Δfus H
6.55
kJ/mol
178.00
NIST
Δfus H
6.61
kJ/mol
178.00
NIST
Δfus H
6.62
kJ/mol
178.00
NIST
Δfus H
6.64
kJ/mol
178.15
NIST
Δvap H
[24.00; 40.60]
kJ/mol
[244.50; 561.00]
Δvap H
40.60
kJ/mol
244.50
NIST
Δvap H
37.80
kJ/mol
251.50
NIST
Δvap H
38.90
kJ/mol
284.00
NIST
Δvap H
38.02
kJ/mol
298.00
Enthalp...
Δvap H
38.80
kJ/mol
298.00
NIST
Δvap H
36.90
kJ/mol
318.00
NIST
Δvap H
37.30
kJ/mol
323.00
NIST
Δvap H
37.80
kJ/mol
324.00
NIST
Δvap H
35.40
kJ/mol
333.00
NIST
Δvap H
35.65
kJ/mol
341.27
NIST
Δvap H
37.00
kJ/mol
346.00
NIST
Δvap H
37.00
kJ/mol
347.00
NIST
Δvap H
35.40
kJ/mol
363.00
NIST
Δvap H
33.40
kJ/mol
373.00
NIST
Δvap H
33.50 ± 0.10
kJ/mol
380.00
NIST
Δvap H
33.18
kJ/mol
383.70
KDB
Δvap H
33.18
kJ/mol
383.80
NIST
Δvap H
32.10 ± 0.10
kJ/mol
403.00
NIST
Δvap H
31.40
kJ/mol
413.00
NIST
Δvap H
35.70
kJ/mol
413.50
NIST
Δvap H
34.40
kJ/mol
414.00
NIST
Δvap H
29.40 ± 0.10
kJ/mol
441.00
NIST
Δvap H
28.40
kJ/mol
453.00
NIST
Δvap H
27.10 ± 0.10
kJ/mol
470.00
NIST
Δvap H
33.20
kJ/mol
485.50
NIST
Δvap H
24.00
kJ/mol
493.00
NIST
Δvap H
24.00 ± 0.10
kJ/mol
505.00
NIST
Δvap H
33.30
kJ/mol
561.00
NIST
Pvap
[0.24; 3280.00]
kPa
[253.83; 573.20]
Pvap
0.24
kPa
253.83
Isother...
Pvap
0.47
kPa
263.15
Isother...
Pvap
0.48
kPa
263.64
Isother...
Pvap
0.48
kPa
263.64
Isother...
Pvap
0.43
kPa
263.75
Vapour ...
Pvap
0.91
kPa
273.15
Isother...
Pvap
0.91
kPa
273.15
Isother...
Pvap
0.93
kPa
273.47
Isother...
Pvap
0.93
kPa
273.47
Isother...
Pvap
0.84
kPa
273.47
Vapour ...
Pvap
1.26
kPa
278.70
A milli...
Pvap
1.67
kPa
283.15
Isother...
Pvap
1.67
kPa
283.15
Isother...
Pvap
1.68
kPa
283.32
Isother...
Pvap
1.68
kPa
283.32
Isother...
Pvap
1.57
kPa
283.35
Vapour ...
Pvap
1.70
kPa
283.60
A milli...
Pvap
2.35
kPa
288.15
Experim...
Pvap
2.42
kPa
288.15
Experim...
Pvap
2.26
kPa
288.50
A milli...
Pvap
2.91
kPa
293.15
Isother...
Pvap
3.05
kPa
293.15
Experim...
Pvap
2.91
kPa
293.15
Isother...
Pvap
3.18
kPa
293.15
Experim...
Pvap
2.93
kPa
293.24
Isother...
Pvap
2.93
kPa
293.24
Isother...
Pvap
2.93
kPa
293.26
Isother...
Pvap
2.82
kPa
293.29
Vapour ...
Pvap
2.97
kPa
293.40
A milli...
Pvap
3.78
kPa
298.15
Isother...
Pvap
3.80
kPa
298.15
(Vapour...
Pvap
3.84
kPa
298.15
Experim...
Pvap
3.80
kPa
298.25
Isother...
Pvap
3.80
kPa
298.25
Isother...
Pvap
3.89
kPa
298.30
A milli...
Pvap
4.47
kPa
300.89
Thermog...
Pvap
4.90
kPa
303.15
Vapor-l...
Pvap
4.87
kPa
303.15
Isother...
Pvap
4.87
kPa
303.15
Isother...
Pvap
4.73
kPa
303.15
Experim...
Pvap
4.87
kPa
303.15
Measure...
Pvap
5.00
kPa
303.20
A milli...
Pvap
4.90
kPa
303.21
Isother...
Pvap
4.89
kPa
303.23
Isother...
Pvap
4.90
kPa
303.23
Isother...
Pvap
4.89
kPa
303.23
Isother...
Pvap
4.79
kPa
303.28
Vapour ...
Pvap
5.17
kPa
305.64
Thermog...
Pvap
5.23
kPa
305.68
Thermog...
Pvap
6.27
kPa
308.10
A milli...
Pvap
6.26
kPa
308.15
Vapor-l...
Pvap
6.32
kPa
308.15
Measure...
Pvap
7.99
kPa
313.10
A milli...
Pvap
7.88
kPa
313.15
Vapor L...
Pvap
7.78
kPa
313.15
Measure...
Pvap
7.88
kPa
313.15
Vapor-L...
Pvap
7.89
kPa
313.15
Phase e...
Pvap
7.88
kPa
313.15
Isother...
Pvap
7.85
kPa
313.15
Isother...
Pvap
7.96
kPa
313.15
Vapor-l...
Pvap
7.85
kPa
313.15
Isother...
Pvap
7.87
kPa
313.19
Isother...
Pvap
7.87
kPa
313.19
Isother...
Pvap
8.10
kPa
313.20
Isother...
Pvap
7.87
kPa
313.22
Isother...
Pvap
7.87
kPa
313.22
Isother...
Pvap
7.79
kPa
313.27
Vapour ...
Pvap
8.62
kPa
315.15
Vapour-...
Pvap
9.95
kPa
318.00
A milli...
Pvap
9.96
kPa
318.15
Vapor-l...
Pvap
9.89
kPa
318.15
Measure...
Pvap
10.77
kPa
320.15
Vapour-...
Pvap
12.26
kPa
323.00
A milli...
Pvap
12.31
kPa
323.15
Vapor-l...
Pvap
12.23
kPa
323.15
Isother...
Pvap
12.22
kPa
323.15
Isother...
Pvap
12.27
kPa
323.15
Measure...
Pvap
12.22
kPa
323.15
Isother...
Pvap
12.29
kPa
323.16
Vapor P...
Pvap
12.25
kPa
323.22
Isother...
Pvap
12.24
kPa
323.22
Isother...
Pvap
12.30
kPa
323.25
Vapour ...
Pvap
13.40
kPa
324.21
Thermog...
Pvap
13.34
kPa
325.15
Vapour-...
Pvap
13.37
kPa
325.16
Vapor P...
Pvap
14.53
kPa
327.15
Vapor P...
Pvap
14.90
kPa
327.60
Vapor p...
Pvap
15.00
kPa
327.90
A milli...
Pvap
14.96
kPa
328.15
Isother...
Pvap
15.14
kPa
328.15
Vapor-l...
Pvap
15.77
kPa
329.15
Vapor P...
Pvap
16.40
kPa
330.15
Vapour-...
Pvap
17.80
kPa
332.15
Vapor P...
Pvap
18.26
kPa
332.80
A milli...
Pvap
18.62
kPa
333.15
Vapor l...
Pvap
18.46
kPa
333.15
Isother...
Pvap
18.56
kPa
333.15
Activit...
Pvap
18.56
kPa
333.15
An equi...
Pvap
18.45
kPa
333.15
Isother...
Pvap
18.86
kPa
333.15
Vapor-l...
Pvap
18.57
kPa
333.20
Isother...
Pvap
18.57
kPa
333.20
Isother...
Pvap
18.93
kPa
333.22
Vapour ...
Pvap
19.35
kPa
334.25
Vapor P...
Pvap
20.02
kPa
335.15
Vapour-...
Pvap
20.00
kPa
335.25
Isobari...
Pvap
22.08
kPa
337.65
Vapor P...
Pvap
22.04
kPa
337.80
A milli...
Pvap
22.61
kPa
338.15
Vapor-l...
Pvap
23.83
kPa
339.65
Vapor P...
Pvap
26.32
kPa
342.30
Vapor P...
Pvap
26.47
kPa
342.45
Vapor P...
Pvap
26.66
kPa
342.65
Isobari...
Pvap
27.24
kPa
343.15
An equi...
Pvap
27.12
kPa
343.15
Isother...
Pvap
27.31
kPa
343.15
Vapor-l...
Pvap
27.10
kPa
343.15
Isother...
Pvap
27.20
kPa
343.16
Isother...
Pvap
27.20
kPa
343.16
Isother...
Pvap
27.76
kPa
343.18
Vapour ...
Pvap
29.21
kPa
345.25
Isobari...
Pvap
32.41
kPa
348.15
Isobari...
Pvap
32.72
kPa
348.15
Vapor-l...
Pvap
37.22
kPa
352.05
Isobari...
Pvap
37.61
kPa
352.25
Isobari...
Pvap
38.84
kPa
353.13
Isother...
Pvap
38.92
kPa
353.15
Vapor L...
Pvap
38.87
kPa
353.15
Isother...
Pvap
38.40
kPa
353.15
Vapor l...
Pvap
38.82
kPa
353.15
An equi...
Pvap
38.84
kPa
353.15
Isother...
Pvap
43.67
kPa
356.65
Isobari...
Pvap
45.96
kPa
357.90
Isobari...
Pvap
46.17
kPa
358.15
Vapor-l...
Pvap
49.60
kPa
360.70
Vapor p...
Pvap
51.35
kPa
361.30
Isobari...
Pvap
53.33
kPa
362.63
Isobari...
Pvap
53.30
kPa
362.64
Isobari...
Pvap
54.13
kPa
363.08
Isother...
Pvap
54.22
kPa
363.15
An equi...
Pvap
54.42
kPa
363.15
Isother...
Pvap
54.49
kPa
363.15
Activit...
Pvap
55.59
kPa
363.75
Isobari...
Pvap
63.84
kPa
368.15
Vapor-l...
Pvap
63.48
kPa
368.25
Isobari...
Pvap
70.12
kPa
371.40
Isobari...
Pvap
79.99
kPa
375.66
Isobari...
Pvap
80.00
kPa
375.66
Isobari...
Pvap
79.30
kPa
375.80
Vapor p...
Pvap
82.48
kPa
376.65
Isobari...
Pvap
86.25
kPa
378.15
Vapor-l...
Pvap
95.30
kPa
381.65
Vapor-l...
Pvap
99.89
kPa
383.25
Isobari...
Pvap
101.30
kPa
383.40
Isobari...
Pvap
100.66
kPa
383.50
Vapor p...
Pvap
101.30
kPa
383.55
Isobari...
Pvap
101.30
kPa
383.60
A new a...
Pvap
101.33
kPa
383.75
Vapor-L...
Pvap
101.30
kPa
383.76
Isobari...
Pvap
101.33
kPa
383.77
Isobari...
Pvap
101.30
kPa
383.80
Isobari...
Pvap
101.33
kPa
383.81
Isobari...
Pvap
101.33
kPa
383.82
Isobari...
Pvap
102.00
kPa
384.10
Isobari...
Pvap
102.73
kPa
384.30
Vapor p...
Pvap
121.30
kPa
390.25
Isobari...
Pvap
121.30
kPa
390.26
Isobari...
Pvap
161.30
kPa
400.75
Isobari...
Pvap
201.30
kPa
409.65
Isobari...
Pvap
498.30
kPa
451.00
Vapor p...
Pvap
499.90
kPa
451.50
Vapor p...
Pvap
760.00
kPa
473.30
A novel...
Pvap
760.00
kPa
473.30
A novel...
Pvap
760.00
kPa
473.30
A novel...
Pvap
1009.33
kPa
490.40
Vapor p...
Pvap
1150.00
kPa
498.30
A novel...
Pvap
1120.00
kPa
498.30
A novel...
Pvap
1140.00
kPa
498.30
A novel...
Pvap
1660.00
kPa
523.40
A novel...
Pvap
1660.00
kPa
523.40
A novel...
Pvap
1670.00
kPa
523.40
A novel...
Pvap
2350.00
kPa
548.30
A novel...
Pvap
2340.00
kPa
548.40
A novel...
Pvap
2340.00
kPa
548.40
A novel...
Pvap
3230.00
kPa
573.20
A novel...
Pvap
3250.00
kPa
573.20
A novel...
Pvap
3280.00
kPa
573.20
A novel...
n 0
[1.48260; 1.50278]
[283.15; 318.15]
n 0
1.50278
283.15
Density...
n 0
1.49960
288.15
Excess ...
n 0
1.49980
288.15
Densiti...
n 0
1.49980
288.15
Refract...
n 0
1.49600
293.00
Quatern...
n 0
1.49650
293.10
A study...
n 0
1.49650
293.10
Densiti...
n 0
1.48730
293.10
(Liquid...
n 0
1.49610
293.10
Vapor-L...
n 0
1.48730
293.10
Measure...
n 0
1.49600
293.15
Liquid-...
n 0
1.49650
293.15
Experim...
n 0
1.49650
293.15
A study...
n 0
1.49690
293.15
Liquid-...
n 0
1.49530
293.15
Isobari...
n 0
1.49600
293.15
Ternary...
n 0
1.49670
293.15
Solubil...
n 0
1.49620
293.15
Densiti...
n 0
1.49650
293.15
Vapor-L...
n 0
1.49600
293.15
Vapor l...
n 0
1.49620
293.15
Infinit...
n 0
1.49700
293.15
Excess ...
n 0
1.49687
293.15
Solubil...
n 0
1.49700
293.15
Refract...
n 0
1.49700
293.15
Densiti...
n 0
1.49670
293.15
Solubil...
n 0
1.49650
293.15
Effect ...
n 0
1.49300
293.15
Volumet...
n 0
1.49670
293.15
Solubil...
n 0
1.49670
293.15
Solubil...
n 0
1.49670
293.20
Liquid ...
n 0
1.49393
298.10
Liquid-...
n 0
1.49650
298.15
Densiti...
n 0
1.49399
298.15
Extract...
n 0
1.49410
298.15
Excess ...
n 0
1.49410
298.15
Physica...
n 0
1.49398
298.15
Applica...
n 0
1.49390
298.15
Densiti...
n 0
1.49393
298.15
Volumet...
n 0
1.49393
298.15
Volumet...
n 0
1.49440
298.15
Excess ...
n 0
1.49406
298.15
Solubil...
n 0
1.49399
298.15
Separat...
n 0
1.49400
298.15
Liquid-...
n 0
1.49413
298.15
KDB
n 0
1.49410
298.15
Solubil...
n 0
1.49410
298.15
Solubil...
n 0
1.49410
298.15
Excess ...
n 0
1.49399
298.15
Density...
n 0
1.49419
298.15
Vapor-L...
n 0
1.49399
298.15
Liquid-...
n 0
1.49310
298.15
Excess ...
n 0
1.49399
298.15
Effect ...
n 0
1.49380
298.15
Experim...
n 0
1.49390
298.15
Vapor-L...
n 0
1.49390
298.15
Vapor-L...
n 0
1.49390
298.15
Vapor-L...
n 0
1.49420
298.15
Solubil...
n 0
1.49390
298.15
Vapor-L...
n 0
1.49650
298.15
The vol...
n 0
1.49360
298.15
Experim...
n 0
1.49410
298.15
Excess ...
n 0
1.49397
298.15
Isother...
n 0
1.49400
298.15
Vapor l...
n 0
1.49420
298.15
Densiti...
n 0
1.49390
298.15
Vapor l...
n 0
1.49399
298.15
Effect ...
n 0
1.49397
298.15
Isother...
n 0
1.49410
298.15
Volumet...
n 0
1.49420
298.15
Refract...
n 0
1.49400
298.20
(Liquid...
n 0
1.49140
303.15
Densiti...
n 0
1.49180
303.15
Excess ...
n 0
1.49130
303.15
Refract...
n 0
1.49130
303.15
Densiti...
n 0
1.49124
303.15
Solubil...
n 0
1.49020
303.15
Excess ...
n 0
1.48850
308.15
Topolog...
n 0
1.48740
308.15
Excess ...
n 0
1.48840
308.15
Densiti...
n 0
1.48840
308.15
Refract...
n 0
1.48550
313.15
Refract...
n 0
1.48550
313.15
Densiti...
n 0
1.48260
318.15
Densiti...
n 0
1.48260
318.15
Refract...
ρl
[781.97; 876.19]
kg/m3
[283.15; 373.20]
ρl
876.19
kg/m3
283.15
Volumet...
ρl
871.00
kg/m3
288.15
Effect ...
ρl
871.79
kg/m3
288.15
Densiti...
ρl
871.44
kg/m3
288.15
Volumet...
ρl
871.50
kg/m3
288.15
Thermod...
ρl
871.92
kg/m3
288.20
The imp...
ρl
867.00
kg/m3
293.00
KDB
ρl
866.84
kg/m3
293.15
Thermod...
ρl
866.68
kg/m3
293.15
Isobari...
ρl
866.82
kg/m3
293.15
Density...
ρl
866.70
kg/m3
293.15
Densiti...
ρl
866.82
kg/m3
293.15
Density...
ρl
866.70
kg/m3
293.15
Densiti...
ρl
866.84
kg/m3
293.15
Density...
ρl
866.98
kg/m3
293.15
Thermod...
ρl
866.91
kg/m3
293.15
Volumet...
ρl
867.00
kg/m3
293.15
Effect ...
ρl
866.80
kg/m3
293.15
Densiti...
ρl
866.93
kg/m3
293.15
Partial...
ρl
866.92
kg/m3
293.15
Volumet...
ρl
868.00
kg/m3
293.15
Effect ...
ρl
867.08
kg/m3
293.15
Densiti...
ρl
866.78
kg/m3
293.15
Liquid-...
ρl
867.30
kg/m3
293.20
Measure...
ρl
866.81
kg/m3
293.20
Isobari...
ρl
866.51
kg/m3
293.20
Isother...
ρl
867.80
kg/m3
293.20
Measure...
ρl
867.61
kg/m3
293.20
Measure...
ρl
864.69
kg/m3
295.20
Isother...
ρl
862.86
kg/m3
297.20
Isother...
ρl
857.61
kg/m3
298.00
Removal...
ρl
862.21
kg/m3
298.15
Experim...
ρl
866.90
kg/m3
298.15
Liquid-...
ρl
862.18
kg/m3
298.15
Thermod...
ρl
862.11
kg/m3
298.15
Densiti...
ρl
862.34
kg/m3
298.15
Liquid ...
ρl
862.22
kg/m3
298.15
Excess ...
ρl
862.29
kg/m3
298.15
Thermod...
ρl
863.67
kg/m3
298.15
Phase b...
ρl
862.34
kg/m3
298.15
Evaluat...
ρl
866.90
kg/m3
298.15
Liquid-...
ρl
857.58
kg/m3
298.15
Experim...
ρl
863.67
kg/m3
298.15
Phase b...
ρl
862.19
kg/m3
298.15
Excess ...
ρl
861.81
kg/m3
298.15
Volumet...
ρl
862.27
kg/m3
298.15
Liquid-...
ρl
862.35
kg/m3
298.15
Thermod...
ρl
862.17
kg/m3
298.15
Evaluat...
ρl
862.17
kg/m3
298.15
Phase b...
ρl
862.17
kg/m3
298.15
(Liquid...
ρl
862.23
kg/m3
298.15
Excess ...
ρl
862.18
kg/m3
298.15
Heat ca...
ρl
862.35
kg/m3
298.15
Mutual ...
ρl
862.23
kg/m3
298.15
Quatern...
ρl
862.22
kg/m3
298.15
Measure...
ρl
862.23
kg/m3
298.15
(Liquid...
ρl
862.20
kg/m3
298.15
Fully a...
ρl
862.21
kg/m3
298.15
Conform...
ρl
862.18
kg/m3
298.15
Desulfu...
ρl
862.18
kg/m3
298.15
Hexyl d...
ρl
862.00
kg/m3
298.15
Effect ...
ρl
862.23
kg/m3
298.15
Isother...
ρl
862.19
kg/m3
298.15
Viscosi...
ρl
862.20
kg/m3
298.15
Thermod...
ρl
864.99
kg/m3
298.15
Liquid ...
ρl
862.21
kg/m3
298.15
Molar E...
ρl
862.18
kg/m3
298.15
Densiti...
ρl
862.19
kg/m3
298.15
Thermod...
ρl
862.27
kg/m3
298.15
Binary ...
ρl
862.18
kg/m3
298.15
Thermod...
ρl
862.00
kg/m3
298.15
Densiti...
ρl
862.10
kg/m3
298.15
Determi...
ρl
862.00
kg/m3
298.15
Densiti...
ρl
862.23
kg/m3
298.15
Topolog...
ρl
862.40
kg/m3
298.15
Thermo ...
ρl
862.10
kg/m3
298.15
Density...
ρl
862.23
kg/m3
298.15
Binary ...
ρl
862.17
kg/m3
298.15
Molar E...
ρl
862.36
kg/m3
298.15
Densiti...
ρl
862.21
kg/m3
298.15
Thermod...
ρl
861.74
kg/m3
298.15
Isobari...
ρl
862.27
kg/m3
298.15
Mutual ...
ρl
861.94
kg/m3
298.20
Isother...
ρl
862.49
kg/m3
298.20
The imp...
ρl
861.45
kg/m3
298.70
Isother...
ρl
858.00
kg/m3
303.15
Effect ...
ρl
857.61
kg/m3
303.15
Measure...
ρl
857.73
kg/m3
303.15
Thermod...
ρl
857.50
kg/m3
303.15
Volumet...
ρl
857.51
kg/m3
303.15
Thermod...
ρl
857.47
kg/m3
303.15
Vapor-L...
ρl
857.51
kg/m3
303.15
Thermod...
ρl
857.53
kg/m3
303.15
Density...
ρl
857.50
kg/m3
303.15
Density...
ρl
857.51
kg/m3
303.15
Heat ca...
ρl
857.58
kg/m3
303.15
Volumet...
ρl
857.50
kg/m3
303.15
Density...
ρl
857.50
kg/m3
303.15
Densiti...
ρl
857.39
kg/m3
303.15
Isobari...
ρl
857.64
kg/m3
303.15
Densiti...
ρl
857.50
kg/m3
303.15
Densiti...
ρl
855.63
kg/m3
303.20
Measure...
ρl
855.94
kg/m3
303.20
Measure...
ρl
856.12
kg/m3
303.20
Measure...
ρl
851.69
kg/m3
308.15
Isobari...
ρl
852.79
kg/m3
308.15
Densiti...
ρl
852.82
kg/m3
308.15
Thermod...
ρl
852.82
kg/m3
308.15
Heat ca...
ρl
852.93
kg/m3
308.15
Densiti...
ρl
852.80
kg/m3
308.15
Densiti...
ρl
852.83
kg/m3
308.15
Thermod...
ρl
848.00
kg/m3
313.15
Effect ...
ρl
848.80
kg/m3
313.15
Densiti...
ρl
848.07
kg/m3
313.15
Vapor-L...
ρl
847.82
kg/m3
313.15
Isobari...
ρl
848.14
kg/m3
313.15
Density...
ρl
848.15
kg/m3
313.15
Thermod...
ρl
848.20
kg/m3
313.15
Volumet...
ρl
848.11
kg/m3
313.15
Density...
ρl
848.00
kg/m3
313.15
Densiti...
ρl
848.21
kg/m3
313.15
Densiti...
ρl
848.11
kg/m3
313.15
Density...
ρl
848.23
kg/m3
313.20
The imp...
ρl
844.27
kg/m3
313.20
Measure...
ρl
844.75
kg/m3
313.20
Measure...
ρl
844.57
kg/m3
313.20
Measure...
ρl
843.49
kg/m3
318.15
Densiti...
ρl
842.88
kg/m3
318.15
Isobari...
ρl
843.44
kg/m3
318.15
Thermod...
ρl
843.30
kg/m3
318.15
Densiti...
ρl
838.66
kg/m3
323.15
Density...
ρl
838.90
kg/m3
323.15
Densiti...
ρl
838.50
kg/m3
323.15
Densiti...
ρl
838.73
kg/m3
323.15
Thermod...
ρl
838.42
kg/m3
323.15
Isobari...
ρl
838.70
kg/m3
323.15
Density...
ρl
838.66
kg/m3
323.15
Density...
ρl
840.00
kg/m3
323.15
Effect ...
ρl
833.68
kg/m3
323.20
Measure...
ρl
833.51
kg/m3
323.20
Measure...
ρl
833.21
kg/m3
323.20
Measure...
ρl
834.00
kg/m3
328.15
Thermod...
ρl
829.13
kg/m3
333.15
Density...
ρl
829.16
kg/m3
333.15
Density...
ρl
829.60
kg/m3
333.15
Densiti...
ρl
829.25
kg/m3
333.15
Thermod...
ρl
828.94
kg/m3
333.15
Isobari...
ρl
829.12
kg/m3
333.15
Density...
ρl
831.00
kg/m3
333.15
Effect ...
ρl
822.43
kg/m3
333.20
Measure...
ρl
822.73
kg/m3
333.20
Measure...
ρl
822.90
kg/m3
333.20
Measure...
ρl
821.00
kg/m3
343.15
Effect ...
ρl
819.51
kg/m3
343.15
Density...
ρl
819.60
kg/m3
343.15
Density...
ρl
820.20
kg/m3
343.15
Densiti...
ρl
812.39
kg/m3
343.20
Measure...
ρl
811.93
kg/m3
343.20
Measure...
ρl
812.22
kg/m3
343.20
Measure...
ρl
809.70
kg/m3
353.15
Density...
ρl
802.15
kg/m3
353.20
Measure...
ρl
801.98
kg/m3
353.20
Measure...
ρl
801.69
kg/m3
353.20
Measure...
ρl
799.70
kg/m3
363.15
Density...
ρl
792.16
kg/m3
363.20
Measure...
ρl
792.00
kg/m3
363.20
Measure...
ρl
791.71
kg/m3
363.20
Measure...
ρl
781.97
kg/m3
373.20
Measure...
ρl
782.26
kg/m3
373.20
Measure...
ρl
782.42
kg/m3
373.20
Measure...
D* i
[0.00; 0.00]
m2 /s
[239.09; 343.45]
D* i
0.00
m2 /s
239.09
Viscous...
D* i
0.00
m2 /s
240.94
Viscous...
D* i
0.00
m2 /s
248.57
Viscous...
D* i
0.00
m2 /s
251.71
Viscous...
D* i
0.00
m2 /s
253.27
Viscous...
D* i
0.00
m2 /s
253.28
Viscous...
D* i
0.00
m2 /s
258.16
Viscous...
D* i
0.00
m2 /s
258.23
Viscous...
D* i
0.00
m2 /s
263.51
Viscous...
D* i
0.00
m2 /s
268.32
Viscous...
D* i
0.00
m2 /s
273.43
Viscous...
D* i
0.00
m2 /s
273.54
Viscous...
D* i
0.00
m2 /s
278.07
Viscous...
D* i
0.00
m2 /s
278.15
Viscous...
D* i
0.00
m2 /s
288.05
Viscous...
D* i
0.00
m2 /s
293.08
Viscous...
D* i
0.00
m2 /s
298.00
Viscous...
D* i
0.00
m2 /s
298.18
Viscous...
D* i
0.00
m2 /s
298.20
Viscous...
D* i
0.00
m2 /s
298.21
Viscous...
D* i
0.00
m2 /s
298.21
Viscous...
D* i
0.00
m2 /s
298.21
Viscous...
D* i
0.00
m2 /s
308.07
Viscous...
D* i
0.00
m2 /s
322.69
Viscous...
D* i
0.00
m2 /s
323.16
Viscous...
D* i
0.00
m2 /s
323.18
Viscous...
D* i
0.00
m2 /s
332.93
Viscous...
D* i
0.00
m2 /s
333.16
Viscous...
D* i
0.00
m2 /s
343.45
Viscous...
Δfus S
[36.79; 37.25]
J/mol×K
[177.95; 178.15]
Δfus S
37.20
J/mol×K
177.95
NIST
Δfus S
36.79
J/mol×K
178.00
NIST
Δfus S
37.25
J/mol×K
178.15
NIST
csound,fluid
[425.50; 1394.10]
m/s
[278.15; 523.15]
csound,fluid
1394.10
m/s
278.15
Advance...
csound,fluid
1371.50
m/s
283.15
Advance...
csound,fluid
1347.50
m/s
288.15
Tempera...
csound,fluid
1349.10
m/s
288.15
Advance...
csound,fluid
1347.50
m/s
288.15
Influen...
csound,fluid
1336.32
m/s
290.65
Influen...
csound,fluid
1325.34
m/s
293.15
Influen...
csound,fluid
1326.90
m/s
293.15
Advance...
csound,fluid
1328.60
m/s
293.15
Physico...
csound,fluid
1314.33
m/s
295.65
Influen...
csound,fluid
1307.30
m/s
298.15
Physico...
csound,fluid
1304.00
m/s
298.15
Densiti...
csound,fluid
1304.00
m/s
298.15
Densiti...
csound,fluid
1303.00
m/s
298.15
Thermod...
csound,fluid
1303.44
m/s
298.15
Influen...
csound,fluid
1303.00
m/s
298.15
Isentro...
csound,fluid
1305.10
m/s
298.15
Advance...
csound,fluid
1303.44
m/s
298.15
Tempera...
csound,fluid
1292.64
m/s
300.65
Influen...
csound,fluid
1283.60
m/s
303.15
Advance...
csound,fluid
1285.50
m/s
303.15
Physico...
csound,fluid
1281.88
m/s
303.15
Influen...
csound,fluid
1271.16
m/s
305.65
Influen...
csound,fluid
1264.20
m/s
308.15
Physico...
csound,fluid
1262.00
m/s
308.15
Densiti...
csound,fluid
1262.00
m/s
308.15
Thermod...
csound,fluid
1262.00
m/s
308.15
Densiti...
csound,fluid
1260.49
m/s
308.15
Influen...
csound,fluid
1262.20
m/s
308.15
Advance...
csound,fluid
1249.83
m/s
310.65
Influen...
csound,fluid
1240.90
m/s
313.15
Advance...
csound,fluid
1242.40
m/s
313.15
Physico...
csound,fluid
1239.22
m/s
313.15
Influen...
csound,fluid
1228.62
m/s
315.65
Influen...
csound,fluid
1219.90
m/s
318.15
Advance...
csound,fluid
1220.70
m/s
318.15
Physico...
csound,fluid
1218.01
m/s
318.15
Influen...
csound,fluid
1207.31
m/s
320.65
Influen...
csound,fluid
1200.80
m/s
323.15
Speed o...
csound,fluid
1200.80
m/s
323.15
Measure...
csound,fluid
1196.60
m/s
323.15
Tempera...
csound,fluid
1196.60
m/s
323.15
Influen...
csound,fluid
1198.90
m/s
323.15
Advance...
csound,fluid
1178.20
m/s
328.15
Advance...
csound,fluid
1157.70
m/s
333.15
Advance...
csound,fluid
1137.20
m/s
338.15
Advance...
csound,fluid
1117.00
m/s
343.15
Advance...
csound,fluid
1000.00
m/s
373.15
Speed o...
csound,fluid
806.00
m/s
423.15
Measure...
csound,fluid
806.00
m/s
423.15
Speed o...
csound,fluid
616.20
m/s
473.15
Speed o...
csound,fluid
425.50
m/s
523.15
Measure...
csound,fluid
425.50
m/s
523.15
Speed o...
γ
[0.02; 0.03]
N/m
[277.85; 368.14]
γ
0.03
N/m
277.85
Surface...
γ
0.03
N/m
278.15
Thermod...
γ
0.03
N/m
283.15
Thermod...
γ
0.03
N/m
287.81
Surface...
γ
0.03
N/m
288.15
Surface...
γ
0.03
N/m
293.00
Density...
γ
0.03
N/m
293.15
Thermod...
γ
0.03
N/m
293.20
KDB
γ
0.03
N/m
297.82
Surface...
γ
0.03
N/m
298.15
Surface...
γ
0.03
N/m
302.83
Surface...
γ
0.03
N/m
303.16
Surface...
γ
0.03
N/m
307.86
Surface...
γ
0.03
N/m
308.15
Surface...
γ
0.03
N/m
308.15
Surface...
γ
0.03
N/m
312.87
Surface...
γ
0.03
N/m
313.15
Surface...
γ
0.03
N/m
317.86
Surface...
γ
0.03
N/m
318.13
Surface...
γ
0.03
N/m
318.15
Surface...
γ
0.02
N/m
323.15
Surface...
γ
0.02
N/m
327.88
Surface...
γ
0.02
N/m
328.15
Surface...
γ
0.02
N/m
328.16
Surface...
γ
0.02
N/m
333.14
Surface...
γ
0.02
N/m
337.88
Surface...
γ
0.02
N/m
338.16
Surface...
γ
0.02
N/m
343.16
Surface...
γ
0.02
N/m
348.16
Surface...
γ
0.02
N/m
353.15
Surface...
γ
0.02
N/m
358.15
Surface...
γ
0.02
N/m
363.16
Surface...
γ
0.02
N/m
368.14
Surface...
λ
[0.11; 0.15]
W/m×K
[234.60; 375.71]
λ
0.15
W/m×K
234.60
Thermal...
λ
0.14
W/m×K
254.58
Thermal...
λ
0.14
W/m×K
272.64
Thermal...
λ
0.14
W/m×K
273.17
Thermal...
λ
0.14
W/m×K
273.45
Thermal...
λ
0.14
W/m×K
274.65
Thermal...
λ
0.14
W/m×K
275.40
Thermal...
λ
0.14
W/m×K
275.95
Thermal...
λ
0.14
W/m×K
276.19
Thermal...
λ
0.14
W/m×K
276.31
Thermal...
λ
0.13
W/m×K
278.42
Thermal...
λ
0.13
W/m×K
281.25
Thermal...
λ
0.13
W/m×K
281.25
Thermal...
λ
0.13
W/m×K
287.33
Thermal...
λ
0.13
W/m×K
288.72
Thermal...
λ
0.13
W/m×K
289.65
Thermal...
λ
0.13
W/m×K
293.23
Thermal...
λ
0.13
W/m×K
294.45
Thermal...
λ
0.13
W/m×K
294.69
Thermal...
λ
0.13
W/m×K
295.01
Thermal...
λ
0.13
W/m×K
295.07
Thermal...
λ
0.13
W/m×K
295.08
Thermal...
λ
0.13
W/m×K
295.47
Thermal...
λ
0.13
W/m×K
295.79
Thermal...
λ
0.13
W/m×K
297.45
Thermal...
λ
0.13
W/m×K
298.60
Thermal...
λ
0.13
W/m×K
300.43
Thermal...
λ
0.13
W/m×K
302.05
Thermal...
λ
0.13
W/m×K
304.59
Thermal...
λ
0.13
W/m×K
307.66
Thermal...
λ
0.13
W/m×K
308.62
Thermal...
λ
0.13
W/m×K
310.22
Thermal...
λ
0.13
W/m×K
314.68
Thermal...
λ
0.13
W/m×K
314.69
Thermal...
λ
0.13
W/m×K
314.74
Thermal...
λ
0.13
W/m×K
315.55
Thermal...
λ
0.13
W/m×K
315.85
Thermal...
λ
0.13
W/m×K
316.70
Thermal...
λ
0.13
W/m×K
316.82
Thermal...
λ
0.13
W/m×K
317.94
Thermal...
λ
0.12
W/m×K
318.80
Thermal...
λ
0.12
W/m×K
318.84
Thermal...
λ
0.12
W/m×K
319.32
Thermal...
λ
0.12
W/m×K
319.96
Thermal...
λ
0.12
W/m×K
321.21
Thermal...
λ
0.12
W/m×K
327.65
Thermal...
λ
0.12
W/m×K
328.48
Thermal...
λ
0.12
W/m×K
329.50
Thermal...
λ
0.12
W/m×K
329.65
Thermal...
λ
0.12
W/m×K
330.77
Thermal...
λ
0.12
W/m×K
331.24
Thermal...
λ
0.12
W/m×K
333.34
Thermal...
λ
0.12
W/m×K
334.99
Thermal...
λ
0.12
W/m×K
335.27
Thermal...
λ
0.12
W/m×K
337.36
Thermal...
λ
0.12
W/m×K
337.63
Thermal...
λ
0.12
W/m×K
338.23
Thermal...
λ
0.12
W/m×K
338.39
Thermal...
λ
0.12
W/m×K
339.65
Thermal...
λ
0.12
W/m×K
339.77
Thermal...
λ
0.12
W/m×K
339.85
Thermal...
λ
0.12
W/m×K
340.17
Thermal...
λ
0.12
W/m×K
340.62
Thermal...
λ
0.12
W/m×K
341.16
Thermal...
λ
0.12
W/m×K
343.09
Thermal...
λ
0.12
W/m×K
346.01
Thermal...
λ
0.12
W/m×K
347.00
Thermal...
λ
0.11
W/m×K
350.87
Thermal...
λ
0.12
W/m×K
351.33
Thermal...
λ
0.12
W/m×K
351.55
Thermal...
λ
0.12
W/m×K
352.25
Thermal...
λ
0.11
W/m×K
354.89
Thermal...
λ
0.11
W/m×K
355.63
Thermal...
λ
0.12
W/m×K
355.71
Thermal...
λ
0.11
W/m×K
355.95
Thermal...
λ
0.11
W/m×K
357.02
Thermal...
λ
0.11
W/m×K
365.42
Thermal...
λ
0.11
W/m×K
370.29
Thermal...
λ
0.11
W/m×K
373.92
Thermal...
λ
0.11
W/m×K
375.26
Thermal...
λ
0.11
W/m×K
375.26
Thermal...
λ
0.11
W/m×K
375.71
Thermal...
αdiff
[4.66e-08; 8.63e-08]
m2 /s
[302.90; 523.38]
αdiff
8.63e-08
m2 /s
302.90
Thermal...
αdiff
8.33e-08
m2 /s
312.45
Thermal...
αdiff
8.03e-08
m2 /s
323.07
Thermal...
αdiff
7.77e-08
m2 /s
333.27
Thermal...
αdiff
7.52e-08
m2 /s
343.52
Thermal...
αdiff
7.30e-08
m2 /s
353.73
Thermal...
αdiff
7.09e-08
m2 /s
363.73
Thermal...
αdiff
6.90e-08
m2 /s
373.04
Thermal...
αdiff
6.71e-08
m2 /s
382.94
Thermal...
αdiff
6.52e-08
m2 /s
392.88
Thermal...
αdiff
6.33e-08
m2 /s
402.93
Thermal...
αdiff
6.15e-08
m2 /s
413.06
Thermal...
αdiff
5.98e-08
m2 /s
422.73
Thermal...
αdiff
5.81e-08
m2 /s
432.67
Thermal...
αdiff
5.64e-08
m2 /s
442.68
Thermal...
αdiff
5.48e-08
m2 /s
452.96
Thermal...
αdiff
5.33e-08
m2 /s
462.99
Thermal...
αdiff
5.19e-08
m2 /s
473.20
Thermal...
αdiff
5.06e-08
m2 /s
482.98
Thermal...
αdiff
4.94e-08
m2 /s
493.05
Thermal...
αdiff
4.84e-08
m2 /s
503.17
Thermal...
αdiff
4.74e-08
m2 /s
513.41
Thermal...
αdiff
4.66e-08
m2 /s
523.38
Thermal...
Pressure Dependent Properties
Datasets
Viscosity, Pa*s (11)
Refractive index (Na D-line) (1)
Mass density, kg/m3 (14)
Speed of sound, m/s (4)
Thermal conductivity, W/m/K (2)
Viscosity, Pa*s
Fixed
Measured
Temperature, K - Liquid
Pressure, kPa - Liquid
Viscosity, Pa*s - Liquid
273.13
1000.00
0.0008
273.13
5000.00
0.0008
273.13
10000.00
0.0008
273.13
20000.00
0.0009
273.13
30000.00
0.0010
298.15
1000.00
0.0006
298.15
5000.00
0.0006
298.15
10000.00
0.0006
298.15
20000.00
0.0006
298.15
30000.00
0.0007
323.16
1000.00
0.0004
323.16
5000.00
0.0004
323.16
10000.00
0.0005
323.16
20000.00
0.0005
323.16
30000.00
0.0005
343.16
1000.00
0.0003
343.16
5000.00
0.0004
343.16
10000.00
0.0004
343.16
20000.00
0.0004
343.16
30000.00
0.0004
363.16
1000.00
0.0003
363.16
5000.00
0.0003
363.16
10000.00
0.0003
363.16
20000.00
0.0003
363.16
30000.00
0.0004
Reference
Fixed
Measured
Temperature, K - Liquid
Pressure, kPa - Liquid
Viscosity, Pa*s - Liquid
293.15
100.00
0.0006
293.15
1000.00
0.0006
293.15
5000.00
0.0006
293.15
10000.00
0.0006
293.15
20000.00
0.0007
293.15
30000.00
0.0007
293.15
40000.00
0.0008
293.15
50000.00
0.0009
293.15
60000.00
0.0009
293.15
70000.00
0.0010
293.15
80000.00
0.0010
293.15
100000.00
0.0011
293.15
120000.00
0.0013
293.15
140000.00
0.0015
298.15
100.00
0.0006
298.15
1000.00
0.0006
298.15
5000.00
0.0006
298.15
10000.00
0.0006
298.15
20000.00
0.0006
298.15
30000.00
0.0007
298.15
40000.00
0.0007
298.15
50000.00
0.0008
298.15
60000.00
0.0008
298.15
70000.00
0.0009
298.15
80000.00
0.0010
298.15
100000.00
0.0011
298.15
120000.00
0.0012
298.15
140000.00
0.0013
313.15
100.00
0.0005
313.15
1000.00
0.0005
313.15
5000.00
0.0005
313.15
10000.00
0.0005
313.15
20000.00
0.0005
313.15
30000.00
0.0006
313.15
40000.00
0.0006
313.15
50000.00
0.0007
313.15
60000.00
0.0007
313.15
70000.00
0.0008
313.15
80000.00
0.0008
313.15
100000.00
0.0009
313.15
120000.00
0.0010
313.15
140000.00
0.0011
323.15
100.00
0.0004
323.15
1000.00
0.0004
323.15
5000.00
0.0004
323.15
10000.00
0.0005
323.15
20000.00
0.0005
323.15
30000.00
0.0005
323.15
40000.00
0.0006
323.15
50000.00
0.0006
323.15
60000.00
0.0006
323.15
70000.00
0.0007
323.15
80000.00
0.0007
323.15
100000.00
0.0008
323.15
120000.00
0.0009
323.15
140000.00
0.0010
333.15
100.00
0.0004
333.15
1000.00
0.0004
333.15
5000.00
0.0004
333.15
10000.00
0.0004
333.15
20000.00
0.0004
333.15
30000.00
0.0005
333.15
40000.00
0.0005
333.15
50000.00
0.0005
333.15
60000.00
0.0006
333.15
70000.00
0.0006
333.15
80000.00
0.0007
333.15
100000.00
0.0007
333.15
120000.00
0.0008
333.15
140000.00
0.0009
348.15
100.00
0.0003
348.15
1000.00
0.0003
348.15
5000.00
0.0003
348.15
10000.00
0.0004
348.15
20000.00
0.0004
348.15
30000.00
0.0004
348.15
40000.00
0.0004
348.15
50000.00
0.0005
348.15
60000.00
0.0005
348.15
70000.00
0.0005
348.15
80000.00
0.0006
348.15
100000.00
0.0006
348.15
120000.00
0.0007
348.15
140000.00
0.0008
353.15
100.00
0.0003
353.15
1000.00
0.0003
353.15
5000.00
0.0003
353.15
10000.00
0.0003
353.15
20000.00
0.0004
353.15
30000.00
0.0004
353.15
40000.00
0.0004
353.15
50000.00
0.0005
353.15
60000.00
0.0005
353.15
70000.00
0.0005
353.15
80000.00
0.0005
353.15
100000.00
0.0006
353.15
120000.00
0.0007
353.15
140000.00
0.0008
373.15
100.00
0.0003
373.15
1000.00
0.0003
373.15
5000.00
0.0003
373.15
10000.00
0.0003
373.15
20000.00
0.0003
373.15
30000.00
0.0003
373.15
40000.00
0.0004
373.15
50000.00
0.0004
373.15
60000.00
0.0004
373.15
70000.00
0.0004
373.15
80000.00
0.0005
373.15
100000.00
0.0005
Reference
Fixed
Measured
Temperature, K - Liquid
Pressure, kPa - Liquid
Viscosity, Pa*s - Liquid
303.15
101.30
0.0005
Reference
Fixed
Measured
Temperature, K - Liquid
Pressure, kPa - Liquid
Viscosity, Pa*s - Liquid
298.15
100.00
0.0006
298.15
2110.00
0.0006
298.15
4100.00
0.0006
298.15
6100.00
0.0006
298.15
8110.00
0.0006
298.15
10110.00
0.0006
323.15
100.00
0.0004
323.15
2080.00
0.0004
323.15
4110.00
0.0004
323.15
6000.00
0.0004
323.15
8120.00
0.0004
323.15
10050.00
0.0005
323.15
12210.00
0.0005
323.15
15000.00
0.0005
348.15
100.00
0.0003
348.15
2120.00
0.0003
348.15
12110.00
0.0004
348.15
15210.00
0.0004
Reference
Fixed
Measured
Temperature, K - Liquid
Pressure, kPa - Liquid
Viscosity, Pa*s - Liquid
303.15
100.00
0.0005
303.15
1000.00
0.0005
303.15
5000.00
0.0005
303.15
10000.00
0.0006
303.15
15000.00
0.0006
303.15
20000.00
0.0006
303.15
25000.00
0.0006
303.15
30000.00
0.0007
303.15
35000.00
0.0007
303.15
40000.00
0.0007
303.15
45000.00
0.0007
303.15
50000.00
0.0008
303.15
55000.00
0.0008
303.15
60000.00
0.0008
313.15
100.00
0.0005
313.15
1000.00
0.0005
313.15
5000.00
0.0005
313.15
10000.00
0.0005
313.15
15000.00
0.0005
313.15
20000.00
0.0006
313.15
25000.00
0.0006
313.15
30000.00
0.0006
313.15
35000.00
0.0006
313.15
40000.00
0.0006
313.15
45000.00
0.0007
313.15
50000.00
0.0007
313.15
55000.00
0.0007
313.15
60000.00
0.0007
323.15
100.00
0.0004
323.15
1000.00
0.0004
323.15
5000.00
0.0004
323.15
10000.00
0.0005
323.15
15000.00
0.0005
323.15
20000.00
0.0005
323.15
25000.00
0.0005
323.15
30000.00
0.0005
323.15
35000.00
0.0006
323.15
40000.00
0.0006
323.15
45000.00
0.0006
323.15
50000.00
0.0006
323.15
55000.00
0.0006
323.15
60000.00
0.0007
333.15
100.00
0.0004
333.15
1000.00
0.0004
333.15
5000.00
0.0004
333.15
10000.00
0.0004
333.15
15000.00
0.0004
333.15
20000.00
0.0004
333.15
25000.00
0.0005
333.15
30000.00
0.0005
333.15
35000.00
0.0005
333.15
40000.00
0.0005
333.15
45000.00
0.0005
333.15
50000.00
0.0006
333.15
55000.00
0.0006
333.15
60000.00
0.0006
343.15
100.00
0.0003
343.15
1000.00
0.0004
343.15
5000.00
0.0004
343.15
10000.00
0.0004
343.15
15000.00
0.0004
343.15
20000.00
0.0004
343.15
25000.00
0.0004
343.15
30000.00
0.0004
343.15
35000.00
0.0005
343.15
40000.00
0.0005
343.15
45000.00
0.0005
343.15
50000.00
0.0005
343.15
55000.00
0.0005
343.15
60000.00
0.0005
353.15
100.00
0.0003
353.15
1000.00
0.0003
353.15
5000.00
0.0003
353.15
10000.00
0.0003
353.15
15000.00
0.0004
353.15
20000.00
0.0004
353.15
25000.00
0.0004
353.15
30000.00
0.0004
353.15
35000.00
0.0004
353.15
40000.00
0.0004
353.15
45000.00
0.0004
353.15
50000.00
0.0005
353.15
55000.00
0.0005
353.15
60000.00
0.0005
Reference
Fixed
Measured
Temperature, K - Liquid
Pressure, kPa - Liquid
Viscosity, Pa*s - Liquid
323.15
100.00
0.0004
323.15
13940.00
0.0005
323.15
27338.00
0.0005
323.15
41055.00
0.0006
323.15
54593.00
0.0006
323.15
68135.00
0.0007
373.11
13270.00
0.0003
373.11
26975.00
0.0003
373.11
40789.00
0.0004
373.11
54631.00
0.0004
373.11
68196.00
0.0004
Reference
Fixed
Measured
Temperature, K - Liquid
Pressure, kPa - Liquid
Viscosity, Pa*s - Liquid
248.16
1000.00
0.0012
248.16
10000.00
0.0013
248.16
20000.00
0.0014
248.16
30000.00
0.0015
273.15
1000.00
0.0008
273.15
10000.00
0.0008
273.15
20000.00
0.0009
273.15
30000.00
0.0010
273.15
40000.00
0.0010
298.14
1000.00
0.0006
298.14
10000.00
0.0006
298.14
20000.00
0.0006
298.14
30000.00
0.0007
298.14
40000.00
0.0007
323.13
1000.00
0.0004
323.13
10000.00
0.0005
323.13
20000.00
0.0005
323.13
30000.00
0.0005
323.13
40000.00
0.0006
348.13
1000.00
0.0003
348.13
10000.00
0.0004
348.13
20000.00
0.0004
348.13
30000.00
0.0004
348.13
40000.00
0.0004
Reference
Fixed
Measured
Pressure, kPa - Liquid
Temperature, K - Liquid
Viscosity, Pa*s - Liquid
101.00
293.31
0.0006
101.00
303.04
0.0005
101.00
312.90
0.0005
101.00
322.79
0.0004
101.00
332.41
0.0004
2230.00
332.42
0.0004
4430.00
332.36
0.0004
6420.00
332.32
0.0004
8310.00
332.30
0.0004
10060.00
332.32
0.0004
11850.00
332.34
0.0004
14200.00
332.58
0.0004
15730.00
332.37
0.0004
17830.00
332.67
0.0004
1240.00
303.02
0.0005
2110.00
302.82
0.0005
3960.00
302.73
0.0005
5660.00
302.76
0.0006
7840.00
302.77
0.0006
9860.00
302.68
0.0006
12320.00
302.92
0.0006
14080.00
302.92
0.0006
15900.00
302.94
0.0006
17780.00
302.97
0.0006
Reference
Fixed
Measured
Temperature, K - Liquid
Pressure, kPa - Liquid
Viscosity, Pa*s - Liquid
298.15
100.00
0.0006
298.15
2300.00
0.0006
298.15
4400.00
0.0006
298.15
7430.00
0.0006
298.15
10400.00
0.0006
298.15
12470.00
0.0006
298.15
14490.00
0.0006
323.15
120.00
0.0004
323.15
3340.00
0.0004
323.15
6340.00
0.0004
323.15
9600.00
0.0005
323.15
12750.00
0.0005
323.15
14770.00
0.0005
Reference
Fixed
Measured
Temperature, K - Liquid
Pressure, kPa - Liquid
Viscosity, Pa*s - Liquid
313.15
100.00
0.0005
323.15
100.00
0.0004
333.15
100.00
0.0004
333.15
800.00
0.0004
333.15
1600.00
0.0004
333.15
2400.00
0.0004
333.15
3200.00
0.0004
343.15
100.00
0.0003
353.15
100.00
0.0003
363.15
100.00
0.0003
373.15
100.00
0.0003
373.15
800.00
0.0003
373.15
1600.00
0.0003
373.15
2400.00
0.0003
373.15
3200.00
0.0003
393.15
1600.00
0.0002
413.15
1600.00
0.0002
433.15
1600.00
0.0002
453.15
1600.00
0.0002
473.15
1600.00
0.0001
Reference
Fixed
Measured
Pressure, kPa - Liquid
Temperature, K - Liquid
Viscosity, Pa*s - Liquid
100.00
293.15
0.0006
100.00
313.15
0.0005
100.00
333.15
0.0004
100.00
353.15
0.0003
20000.00
293.15
0.0007
20000.00
313.15
0.0005
20000.00
333.15
0.0004
20000.00
353.15
0.0004
40000.00
293.15
0.0008
40000.00
313.15
0.0006
40000.00
333.15
0.0005
40000.00
353.15
0.0004
60000.00
293.15
0.0009
60000.00
313.15
0.0007
60000.00
333.15
0.0006
60000.00
353.15
0.0005
80000.00
293.15
0.0010
80000.00
313.15
0.0008
80000.00
333.15
0.0007
80000.00
353.15
0.0005
100000.00
293.15
0.0012
100000.00
313.15
0.0009
100000.00
333.15
0.0007
100000.00
353.15
0.0006
Reference
Refractive index (Na D-line)
Fixed
Measured
Pressure, kPa - Liquid
Temperature, K - Liquid
Refractive index (Na D-line) - Liquid
100.00
293.15
1.4966
Reference
Mass density, kg/m3
Fixed
Measured
Temperature, K - Liquid
Pressure, kPa - Liquid
Mass density, kg/m3 - Liquid
323.20
5240.00
843.3
323.20
10200.00
847.8
333.10
2090.00
830.7
333.10
4220.00
832.7
333.10
6360.00
834.8
333.10
10200.00
838.2
Reference
Fixed
Measured
Temperature, K - Liquid
Pressure, kPa - Liquid
Mass density, kg/m3 - Liquid
283.15
100.00
876.1
283.15
5000.00
879.5
283.15
10000.00
882.9
283.15
15000.00
886.1
283.15
20000.00
889.3
283.15
25000.00
892.4
283.15
30000.00
895.3
283.15
35000.00
898.2
283.15
40000.00
901.0
283.15
45000.00
903.7
293.15
100.00
866.8
293.15
5000.00
870.5
293.15
10000.00
874.1
293.15
15000.00
877.5
293.15
20000.00
880.8
293.15
25000.00
884.0
293.15
30000.00
887.1
293.15
35000.00
890.1
293.15
40000.00
893.0
293.15
45000.00
895.9
303.15
100.00
857.5
303.15
5000.00
861.4
303.15
10000.00
865.2
303.15
15000.00
868.8
303.15
20000.00
872.3
303.15
25000.00
875.7
303.15
30000.00
879.0
303.15
35000.00
882.1
303.15
40000.00
885.2
303.15
45000.00
888.1
313.15
100.00
848.1
313.15
5000.00
852.2
313.15
10000.00
856.2
313.15
15000.00
860.0
313.15
20000.00
863.7
313.15
25000.00
867.3
313.15
30000.00
870.7
313.15
35000.00
874.0
313.15
40000.00
877.2
313.15
45000.00
880.3
323.15
100.00
838.6
323.15
5000.00
843.0
323.15
10000.00
847.2
323.15
15000.00
851.3
323.15
20000.00
855.2
323.15
25000.00
858.9
323.15
30000.00
862.5
323.15
35000.00
866.0
323.15
40000.00
869.4
323.15
45000.00
872.6
333.15
100.00
828.8
333.15
5000.00
833.5
333.15
10000.00
838.0
333.15
15000.00
842.3
333.15
20000.00
846.4
333.15
25000.00
850.4
333.15
30000.00
854.2
333.15
35000.00
857.9
333.15
40000.00
861.4
333.15
45000.00
864.8
343.15
100.00
819.2
343.15
5000.00
824.1
343.15
10000.00
829.0
343.15
15000.00
833.5
343.15
20000.00
837.9
343.15
25000.00
842.1
343.15
30000.00
846.0
343.15
35000.00
849.9
343.15
40000.00
853.5
343.15
45000.00
857.0
353.15
100.00
809.4
353.15
5000.00
814.7
353.15
10000.00
819.9
353.15
15000.00
824.7
353.15
20000.00
829.3
353.15
25000.00
833.7
353.15
30000.00
837.9
353.15
35000.00
841.9
353.15
40000.00
845.7
353.15
45000.00
849.4
Reference
Fixed
Measured
Pressure, kPa - Liquid
Temperature, K - Liquid
Mass density, kg/m3 - Liquid
100.00
293.15
867.1
100.00
303.15
857.5
100.00
313.15
847.8
100.00
323.15
838.4
100.00
333.15
828.8
100.00
343.15
819.4
100.00
353.15
809.7
5000.00
293.15
870.6
5000.00
303.15
861.4
5000.00
313.15
852.0
5000.00
323.15
842.7
5000.00
333.15
833.5
5000.00
343.15
824.5
5000.00
353.15
815.1
10000.00
293.15
874.2
10000.00
303.15
865.1
10000.00
313.15
856.1
10000.00
323.15
847.0
10000.00
333.15
838.2
10000.00
343.15
829.3
10000.00
353.15
820.3
15000.00
293.15
877.6
15000.00
303.15
869.0
15000.00
313.15
859.9
15000.00
323.15
851.1
15000.00
333.15
842.6
15000.00
343.15
833.9
15000.00
353.15
825.3
20000.00
293.15
881.1
20000.00
303.15
872.4
20000.00
313.15
863.5
20000.00
323.15
855.0
20000.00
333.15
846.6
20000.00
343.15
838.1
20000.00
353.15
829.9
25000.00
293.15
884.2
25000.00
303.15
875.8
25000.00
313.15
867.1
25000.00
323.15
858.9
25000.00
333.15
850.5
25000.00
343.15
842.3
25000.00
353.15
834.0
30000.00
293.15
887.3
30000.00
303.15
879.0
30000.00
313.15
870.5
30000.00
323.15
862.5
30000.00
333.15
854.3
30000.00
343.15
846.2
30000.00
353.15
838.2
35000.00
293.15
890.3
35000.00
303.15
882.1
35000.00
313.15
873.8
35000.00
323.15
866.0
35000.00
333.15
857.9
35000.00
343.15
850.1
35000.00
353.15
842.2
40000.00
293.15
893.3
40000.00
303.15
885.2
40000.00
313.15
877.0
40000.00
323.15
869.4
40000.00
333.15
861.4
40000.00
343.15
853.7
40000.00
353.15
846.1
45000.00
293.15
896.1
45000.00
303.15
888.2
45000.00
313.15
880.2
45000.00
323.15
872.5
45000.00
333.15
864.8
45000.00
343.15
857.4
45000.00
353.15
849.8
50000.00
293.15
898.9
50000.00
303.15
891.1
50000.00
313.15
883.3
50000.00
323.15
875.7
50000.00
333.15
868.1
50000.00
343.15
860.8
50000.00
353.15
853.3
55000.00
293.15
901.6
55000.00
303.15
894.0
55000.00
313.15
886.2
55000.00
323.15
878.7
55000.00
333.15
871.4
55000.00
343.15
864.2
55000.00
353.15
856.7
60000.00
293.15
904.2
60000.00
303.15
896.7
60000.00
313.15
889.0
60000.00
323.15
881.7
60000.00
333.15
874.5
60000.00
343.15
867.4
60000.00
353.15
860.1
65000.00
293.15
906.7
65000.00
303.15
899.2
65000.00
313.15
891.8
65000.00
323.15
884.6
65000.00
333.15
877.5
65000.00
343.15
870.3
65000.00
353.15
863.5
Reference
Fixed
Measured
Temperature, K - Liquid
Pressure, kPa - Liquid
Mass density, kg/m3 - Liquid
293.00
2000.00
871.2
293.00
3000.00
871.9
293.00
4000.00
872.6
293.00
5000.00
873.2
293.00
10000.00
876.8
293.00
20000.00
883.4
293.00
30000.00
889.3
293.00
40000.00
895.1
293.00
50000.00
900.5
293.00
60000.00
905.8
293.00
70000.00
910.8
293.00
80000.00
915.8
293.00
90000.00
920.4
293.00
100000.00
924.8
293.00
110000.00
929.4
293.00
120000.00
933.6
293.00
130000.00
938.0
293.00
135000.00
939.9
293.00
137500.00
940.9
313.00
2000.00
852.2
313.00
3000.00
853.0
313.00
4000.00
853.9
313.00
5000.00
854.6
313.00
10000.00
858.6
313.00
20000.00
866.1
313.00
30000.00
872.9
313.00
40000.00
879.0
313.00
50000.00
884.8
313.00
60000.00
890.4
313.00
70000.00
896.0
313.00
80000.00
901.2
313.00
90000.00
906.3
313.00
100000.00
911.0
313.00
110000.00
915.7
313.00
120000.00
920.3
313.00
130000.00
924.8
313.00
135000.00
927.0
313.00
137500.00
927.9
333.00
2000.00
833.0
333.00
3000.00
834.0
333.00
4000.00
834.9
333.00
5000.00
835.8
333.00
10000.00
840.2
333.00
20000.00
848.2
333.00
30000.00
855.9
333.00
40000.00
863.0
333.00
50000.00
869.2
333.00
60000.00
875.6
333.00
70000.00
881.5
333.00
80000.00
887.1
333.00
90000.00
892.3
333.00
100000.00
897.6
333.00
110000.00
902.5
333.00
120000.00
907.3
333.00
130000.00
912.0
333.00
135000.00
914.2
333.00
137500.00
915.4
353.00
2000.00
814.2
353.00
3000.00
815.2
353.00
4000.00
816.3
353.00
5000.00
817.3
353.00
10000.00
822.4
353.00
20000.00
831.5
353.00
30000.00
840.1
353.00
40000.00
847.6
353.00
50000.00
854.7
353.00
60000.00
861.5
353.00
70000.00
867.7
353.00
80000.00
873.8
353.00
90000.00
879.6
353.00
100000.00
884.9
353.00
110000.00
890.3
353.00
120000.00
895.4
353.00
130000.00
900.3
353.00
135000.00
902.6
353.00
137500.00
903.7
373.00
2000.00
794.2
373.00
3000.00
795.4
373.00
4000.00
796.6
373.00
5000.00
797.8
373.00
10000.00
803.8
373.00
20000.00
814.0
373.00
30000.00
823.5
373.00
40000.00
832.0
373.00
50000.00
840.2
373.00
60000.00
847.2
373.00
70000.00
853.9
373.00
80000.00
860.3
373.00
90000.00
866.6
373.00
100000.00
872.2
373.00
110000.00
877.8
373.00
120000.00
883.3
373.00
130000.00
888.5
373.00
135000.00
890.8
373.00
137500.00
892.0
393.00
2000.00
774.2
393.00
3000.00
775.7
393.00
4000.00
777.2
393.00
5000.00
778.5
393.00
10000.00
785.1
393.00
20000.00
797.0
393.00
30000.00
807.5
393.00
40000.00
816.9
393.00
50000.00
825.2
393.00
60000.00
833.3
393.00
70000.00
840.6
393.00
80000.00
847.3
393.00
90000.00
854.0
393.00
100000.00
860.1
393.00
110000.00
866.0
393.00
120000.00
871.6
393.00
130000.00
877.2
393.00
135000.00
879.8
393.00
137500.00
881.0
413.00
2000.00
753.1
413.00
3000.00
754.9
413.00
4000.00
756.5
413.00
5000.00
758.3
413.00
10000.00
766.1
413.00
20000.00
779.5
413.00
30000.00
791.3
413.00
40000.00
801.6
413.00
50000.00
810.8
413.00
60000.00
819.2
413.00
70000.00
827.3
413.00
80000.00
834.6
413.00
90000.00
841.3
413.00
100000.00
848.0
413.00
110000.00
854.2
413.00
120000.00
860.2
413.00
130000.00
865.8
413.00
135000.00
868.5
413.00
137500.00
869.7
433.00
2000.00
731.6
433.00
3000.00
733.6
433.00
4000.00
735.6
433.00
5000.00
737.5
433.00
10000.00
746.9
433.00
20000.00
762.1
433.00
30000.00
774.9
433.00
40000.00
786.5
433.00
50000.00
796.7
433.00
60000.00
805.8
433.00
70000.00
814.3
433.00
80000.00
822.0
433.00
90000.00
829.2
433.00
100000.00
836.0
433.00
110000.00
842.6
433.00
120000.00
848.7
433.00
130000.00
854.9
433.00
135000.00
857.7
433.00
137500.00
859.0
448.00
2000.00
714.3
448.00
3000.00
716.6
448.00
4000.00
718.9
448.00
5000.00
721.1
448.00
10000.00
731.4
448.00
20000.00
748.5
448.00
30000.00
762.6
448.00
40000.00
774.7
448.00
50000.00
785.5
448.00
60000.00
795.1
448.00
70000.00
804.1
448.00
80000.00
812.3
448.00
90000.00
820.0
448.00
100000.00
827.2
448.00
110000.00
833.9
448.00
120000.00
840.2
448.00
130000.00
846.6
448.00
135000.00
849.6
448.00
137500.00
850.9
468.00
2000.00
689.9
468.00
3000.00
692.7
468.00
4000.00
695.5
468.00
5000.00
698.2
468.00
10000.00
710.6
468.00
20000.00
730.4
468.00
30000.00
745.9
468.00
40000.00
759.3
468.00
50000.00
771.1
468.00
60000.00
781.7
468.00
70000.00
790.9
468.00
80000.00
799.8
468.00
90000.00
808.0
468.00
100000.00
815.5
468.00
110000.00
822.8
468.00
120000.00
829.5
468.00
130000.00
836.0
468.00
135000.00
838.9
468.00
137500.00
840.4
Reference
Fixed
Measured
Temperature, K - Liquid
Pressure, kPa - Liquid
Mass density, kg/m3 - Liquid
298.15
100.00
862.1
298.15
2130.00
863.6
298.15
4150.00
865.2
298.15
6180.00
866.7
298.15
8210.00
868.2
298.15
10230.00
869.6
298.15
11250.00
870.4
298.15
12260.00
871.1
298.15
14290.00
872.5
298.15
16310.00
873.9
298.15
18340.00
875.3
298.15
20370.00
876.7
298.15
22390.00
878.0
298.15
24420.00
879.3
298.15
26450.00
880.6
298.15
28470.00
881.9
298.15
29490.00
882.5
298.15
30500.00
883.2
298.15
32530.00
884.4
298.15
34550.00
885.6
298.15
36580.00
886.8
298.15
38600.00
888.0
298.15
39620.00
888.6
308.15
100.00
853.0
308.15
2130.00
854.5
308.15
4150.00
856.2
308.15
6180.00
857.8
308.15
8210.00
859.3
308.15
10230.00
860.9
308.15
11250.00
861.7
308.15
12260.00
862.4
308.15
14290.00
863.9
308.15
16310.00
865.4
308.15
18340.00
866.8
308.15
20370.00
868.2
308.15
22390.00
869.6
308.15
24420.00
871.0
308.15
26450.00
872.4
308.15
28470.00
873.8
308.15
29490.00
874.4
308.15
30500.00
875.0
308.15
32530.00
876.3
308.15
34550.00
877.6
308.15
36580.00
878.9
308.15
38600.00
880.1
308.15
39620.00
880.7
318.15
100.00
843.8
318.15
2130.00
845.6
318.15
4150.00
847.3
318.15
6180.00
849.0
318.15
8210.00
850.6
318.15
10230.00
852.3
318.15
11250.00
853.1
318.15
12260.00
853.9
318.15
14290.00
855.4
318.15
16310.00
857.0
318.15
18340.00
858.5
318.15
20370.00
860.0
318.15
22390.00
861.5
318.15
24420.00
862.9
318.15
26450.00
864.4
318.15
28470.00
865.8
318.15
29490.00
866.5
318.15
30500.00
867.2
318.15
32530.00
868.5
318.15
34550.00
869.9
318.15
36580.00
871.2
318.15
38600.00
872.5
318.15
39620.00
873.2
328.15
100.00
834.5
328.15
2130.00
836.5
328.15
4150.00
838.3
328.15
6180.00
840.1
328.15
8210.00
841.8
328.15
10230.00
843.5
328.15
11250.00
844.4
328.15
12260.00
845.2
328.15
14290.00
846.9
328.15
16310.00
848.6
328.15
18340.00
850.1
328.15
20370.00
851.7
328.15
22390.00
853.3
328.15
24420.00
854.8
328.15
26450.00
856.3
328.15
28470.00
857.8
328.15
29490.00
858.5
328.15
30500.00
859.3
328.15
32530.00
860.7
328.15
34550.00
862.1
328.15
36580.00
863.5
328.15
38600.00
864.9
328.15
39620.00
865.5
Reference
Fixed
Measured
Temperature, K - Liquid
Pressure, kPa - Liquid
Mass density, kg/m3 - Liquid
283.15
100.00
876.0
283.15
1000.00
876.6
283.15
5000.00
879.5
283.15
10000.00
882.9
283.15
30000.00
895.3
283.15
50000.00
906.4
283.15
70000.00
916.4
298.15
100.00
862.5
298.15
1000.00
863.0
298.15
5000.00
866.1
298.15
10000.00
869.7
298.15
30000.00
883.1
298.15
50000.00
894.9
298.15
70000.00
905.5
323.15
100.00
839.1
323.15
1000.00
839.7
323.15
5000.00
843.2
323.15
10000.00
847.5
323.15
30000.00
862.8
323.15
50000.00
876.0
323.15
70000.00
887.6
333.15
100.00
829.6
333.15
1000.00
830.2
333.15
5000.00
834.0
333.15
10000.00
838.5
333.15
30000.00
854.6
333.15
50000.00
868.4
333.15
70000.00
880.6
348.15
100.00
815.1
348.15
1000.00
815.8
348.15
5000.00
820.0
348.15
10000.00
825.0
348.15
30000.00
842.4
348.15
50000.00
857.2
348.15
70000.00
870.1
373.15
100.00
789.5
373.15
1000.00
791.4
373.15
5000.00
796.4
373.15
10000.00
802.3
373.15
30000.00
822.4
373.15
50000.00
838.9
373.15
70000.00
853.1
398.15
1000.00
765.1
398.15
5000.00
771.0
398.15
10000.00
777.9
398.15
30000.00
801.1
398.15
50000.00
819.6
398.15
70000.00
835.1
Reference
Fixed
Measured
Pressure, kPa - Liquid
Temperature, K - Liquid
Mass density, kg/m3 - Liquid
100.00
298.15
862.0
1000.00
298.15
862.7
5000.00
298.15
865.7
10000.00
298.15
869.4
15000.00
298.15
873.0
20000.00
298.15
876.4
30000.00
298.15
882.9
40000.00
298.15
889.0
45000.00
298.15
891.9
50000.00
298.15
894.7
60000.00
298.15
900.2
100.00
323.15
838.7
1000.00
323.15
839.5
5000.00
323.15
843.1
10000.00
323.15
847.4
15000.00
323.15
851.5
20000.00
323.15
855.4
30000.00
323.15
862.7
40000.00
323.15
869.5
45000.00
323.15
872.7
50000.00
323.15
875.9
60000.00
323.15
881.9
100.00
348.15
814.6
1000.00
348.15
815.6
5000.00
348.15
819.8
10000.00
348.15
824.7
15000.00
348.15
829.5
20000.00
348.15
834.0
30000.00
348.15
842.4
40000.00
348.15
850.0
45000.00
348.15
853.6
50000.00
348.15
857.1
60000.00
348.15
863.8
1000.00
373.15
791.1
5000.00
373.15
796.0
10000.00
373.15
801.8
15000.00
373.15
807.3
20000.00
373.15
812.5
30000.00
373.15
822.0
40000.00
373.15
830.6
45000.00
373.15
834.6
50000.00
373.15
838.4
60000.00
373.15
845.8
1000.00
398.15
765.3
5000.00
398.15
771.3
10000.00
398.15
778.3
15000.00
398.15
784.7
20000.00
398.15
790.8
30000.00
398.15
801.6
40000.00
398.15
811.2
45000.00
398.15
815.7
50000.00
398.15
819.9
60000.00
398.15
828.0
Reference
Fixed
Measured
Temperature, K - Liquid
Pressure, kPa - Liquid
Mass density, kg/m3 - Liquid
233.15
101.25
922.207
233.15
1055.60
922.722
233.15
1861.30
923.156
233.15
3871.07
924.223
233.15
5873.94
925.287
233.15
8031.15
926.415
233.15
9906.49
927.392
233.15
11972.80
928.445
233.15
13947.10
929.451
233.15
15970.80
930.461
233.15
18028.60
931.487
233.15
19921.10
932.422
233.15
22000.00
933.432
233.15
24028.70
934.411
233.15
25833.40
935.279
233.15
27875.90
936.25
233.15
29775.60
937.146
253.15
102.01
903.705
253.15
1102.59
904.316
253.15
1837.13
904.762
253.15
3915.79
906.0
253.15
6024.32
907.237
253.15
7905.75
908.333
253.15
9884.50
909.467
253.15
11994.60
910.665
253.15
13974.90
911.777
253.15
15950.90
912.877
253.15
17977.80
913.989
253.15
20022.00
915.098
253.15
21921.00
916.119
253.15
24088.40
917.274
253.15
25989.80
918.275
253.15
27826.70
919.23
253.15
29745.90
920.223
273.15
97.87
885.25
273.15
1027.82
885.881
273.15
1996.92
886.534
273.15
4081.70
887.926
273.15
5913.44
889.129
273.15
8004.24
890.482
273.15
9932.36
891.714
273.15
11879.80
892.948
273.15
13887.70
894.195
273.15
16098.50
895.56
273.15
18098.90
896.771
273.15
19969.20
897.897
273.15
21859.80
899.011
273.15
23914.00
900.215
273.15
25979.60
901.41
273.15
28069.50
902.607
273.15
30122.70
903.766
293.15
99.87
866.733
293.15
1127.75
867.518
293.15
2021.41
868.196
293.15
3955.95
869.643
293.15
6107.05
871.23
293.15
8032.84
872.623
293.15
9984.75
874.014
293.15
12114.30
875.512
293.15
13946.90
876.779
293.15
15848.70
878.081
293.15
17969.10
879.506
293.15
19990.50
880.848
293.15
22236.40
882.319
293.15
23980.90
883.441
293.15
25908.50
884.671
293.15
27990.50
885.976
293.15
30011.00
887.242
313.15
100.25
848.035
313.15
1103.10
848.903
313.15
2030.62
849.693
313.15
3897.28
851.277
313.15
6141.83
853.137
313.15
7925.24
854.59
313.15
9859.02
856.142
313.15
11934.70
857.774
313.15
13950.30
859.327
313.15
16069.10
860.941
313.15
17874.10
862.289
313.15
19838.40
863.738
313.15
22114.30
865.383
313.15
24096.90
866.799
313.15
25913.10
868.068
313.15
28004.70
869.523
313.15
29965.50
870.863
333.15
98.96
829.055
333.15
1101.01
830.042
333.15
2134.31
831.05
333.15
4003.84
832.841
333.15
6105.69
834.814
333.15
8004.97
836.556
333.15
9960.27
838.314
333.15
12120.50
840.218
333.15
14111.20
841.938
333.15
15856.90
843.417
333.15
18129.10
845.312
333.15
19859.70
846.724
333.15
22144.00
848.558
333.15
24050.50
850.059
333.15
25886.50
851.479
333.15
28037.10
853.128
333.15
29895.00
854.529
353.15
100.22
809.674
353.15
1169.90
810.881
353.15
2003.60
811.814
353.15
4142.50
814.153
353.15
6005.54
816.142
353.15
8141.30
818.365
353.15
10003.50
820.255
353.15
12008.20
822.24
353.15
14198.40
824.368
353.15
16142.20
826.212
353.15
18101.40
828.027
353.15
19916.80
829.683
353.15
22137.50
831.662
353.15
24034.00
833.323
353.15
26059.00
835.06
353.15
28105.10
836.785
353.15
29954.10
838.316
373.15
1259.86
791.299
373.15
2065.80
792.34
373.15
3870.71
794.611
373.15
6198.30
797.456
373.15
8095.93
799.709
373.15
9917.32
801.809
373.15
12114.50
804.274
373.15
13933.50
806.263
373.15
16020.00
808.493
373.15
18023.10
810.573
373.15
19927.20
812.508
373.15
22108.00
814.677
373.15
23970.20
816.486
373.15
25950.10
818.372
373.15
27873.70
820.167
373.15
29906.80
822.029
393.15
1097.43
770.672
393.15
1998.69
772.03
393.15
4084.58
775.078
393.15
6214.76
778.084
393.15
8059.27
780.589
393.15
9988.38
783.137
393.15
12133.60
785.871
393.15
14051.30
788.257
393.15
16078.00
790.683
393.15
18011.70
792.945
393.15
19811.10
794.994
393.15
22109.50
797.55
393.15
23923.10
799.514
393.15
25870.20
801.576
393.15
27974.20
803.747
393.15
29891.10
805.692
413.15
1099.07
749.389
413.15
1960.79
750.924
413.15
4038.31
754.503
413.15
6026.64
757.773
413.15
8189.08
761.18
413.15
9852.03
763.702
413.15
12116.70
767.016
413.15
14167.50
769.904
413.15
16108.40
772.544
413.15
18095.40
775.165
413.15
20103.80
777.733
413.15
22151.60
780.275
413.15
24008.60
782.518
413.15
25995.60
784.857
413.15
27793.40
786.922
413.15
29814.70
789.193
433.15
1101.78
726.984
433.15
1976.67
728.858
433.15
4084.44
733.177
433.15
6154.50
737.18
433.15
8078.74
740.731
433.15
9952.57
744.032
433.15
11979.80
747.451
433.15
13969.10
750.677
433.15
16091.10
753.964
433.15
17960.70
756.765
433.15
19890.30
759.561
433.15
22082.30
762.624
433.15
24002.20
765.215
433.15
26048.90
767.899
433.15
27835.50
770.185
433.15
29992.70
772.844
453.15
1107.48
703.102
453.15
2037.85
705.548
453.15
4185.27
710.874
453.15
6060.45
715.218
453.15
8005.22
719.474
453.15
9870.31
723.328
453.15
12115.30
727.721
453.15
14139.10
731.482
453.15
16026.60
734.835
453.15
17927.80
738.09
453.15
20153.00
741.727
453.15
22071.10
744.756
453.15
24056.90
747.767
453.15
26028.80
750.661
453.15
27966.30
753.404
453.15
29817.00
755.955
473.15
1104.44
677.2
473.15
2031.33
680.289
473.15
4033.85
686.456
473.15
6024.42
692.111
473.15
7930.82
697.122
473.15
10106.60
702.459
473.15
11931.20
706.639
473.15
13958.70
711.045
473.15
16004.30
715.254
473.15
17878.30
718.918
473.15
19844.40
722.599
473.15
22087.70
726.587
473.15
24074.30
729.989
473.15
26037.60
733.203
473.15
27839.80
736.071
473.15
29805.80
739.091
Reference
Fixed
Measured
Temperature, K - Liquid
Pressure, kPa - Liquid
Mass density, kg/m3 - Liquid
295.90
15300.00
873.9
295.90
15300.00
873.9
295.90
36900.00
888.3
295.90
37000.00
888.3
295.90
56300.00
899.5
295.90
56300.00
899.5
295.90
77100.00
910.8
295.90
77100.00
910.8
295.90
92300.00
918.5
295.90
92300.00
918.5
295.90
112400.00
927.8
295.90
112500.00
927.9
295.90
113100.00
928.0
295.90
113100.00
927.9
295.90
132800.00
936.5
295.90
132800.00
936.5
295.90
154900.00
945.5
295.90
155000.00
945.5
305.10
8800.00
860.1
305.10
8800.00
860.1
305.10
71100.00
900.3
305.10
71100.00
900.3
305.10
71100.00
900.3
305.10
71100.00
900.3
305.10
125700.00
926.6
305.10
125700.00
926.6
305.10
174300.00
946.6
305.10
174500.00
946.6
323.40
21600.00
852.5
323.40
21700.00
852.5
323.40
31600.00
860.3
323.40
56700.00
877.1
323.40
56700.00
877.1
323.40
56700.00
877.1
323.40
77500.00
889.3
323.40
77600.00
889.4
323.40
110300.00
906.5
323.40
110400.00
906.5
323.40
133100.00
919.1
323.40
133100.00
919.2
323.40
149000.00
926.0
323.40
149100.00
926.0
323.40
153800.00
926.0
323.40
153900.00
926.0
323.40
153900.00
926.0
323.40
154000.00
926.0
323.40
182500.00
939.6
323.40
182500.00
939.5
323.40
202800.00
947.3
323.40
202900.00
947.4
323.40
219900.00
953.2
323.40
220100.00
953.3
323.40
223000.00
952.9
323.40
223300.00
952.9
347.30
9200.00
821.2
347.30
9200.00
821.3
347.30
35500.00
845.5
347.30
35600.00
845.6
347.30
82100.00
877.4
347.30
82200.00
877.4
347.30
106400.00
891.1
347.30
106500.00
891.1
347.30
140400.00
907.9
347.30
140400.00
907.9
347.30
140600.00
907.9
347.30
140700.00
907.9
347.30
160800.00
917.1
347.30
160800.00
917.1
347.30
182500.00
926.1
347.30
182500.00
926.1
347.30
182500.00
926.2
347.30
182600.00
926.2
347.30
204500.00
934.8
347.30
204800.00
934.8
392.50
16800.00
789.6
392.50
16800.00
789.7
392.50
35200.00
810.6
392.50
35200.00
810.6
392.50
35200.00
810.6
392.50
35300.00
810.6
392.50
48400.00
822.9
392.50
48500.00
822.9
392.50
64700.00
831.8
392.50
64800.00
832.6
392.50
78400.00
846.1
392.50
78500.00
846.2
392.50
90500.00
849.8
392.50
90600.00
850.6
392.50
113000.00
865.4
392.50
113100.00
866.2
392.50
133600.00
875.1
392.50
133700.00
875.9
392.50
154300.00
886.5
392.50
154400.00
886.6
392.50
174900.00
895.6
392.50
195100.00
904.6
392.50
195200.00
904.6
392.50
195200.00
905.4
392.50
216900.00
913.6
392.50
217100.00
914.4
392.50
238700.00
923.8
392.50
238900.00
924.7
392.50
258600.00
929.8
392.50
258900.00
930.7
392.50
279100.00
938.4
392.50
279700.00
939.3
421.50
10200.00
755.6
421.50
10300.00
755.7
421.50
21700.00
771.9
421.50
21900.00
772.0
421.50
36200.00
788.7
421.50
36200.00
788.8
421.50
49700.00
802.4
421.50
49800.00
802.5
421.50
70900.00
818.3
421.50
70900.00
818.7
421.50
87800.00
832.8
421.50
87800.00
832.4
421.50
106200.00
841.8
421.50
106200.00
842.1
421.50
121800.00
852.0
421.50
121800.00
851.6
421.50
133100.00
862.0
421.50
133200.00
862.1
421.50
139800.00
862.1
421.50
139900.00
865.9
421.50
160700.00
873.2
421.50
160700.00
873.3
421.50
175700.00
881.8
421.50
177600.00
881.7
421.50
188500.00
890.6
421.50
188700.00
890.5
421.50
196400.00
890.5
421.50
196500.00
890.4
421.50
216100.00
899.2
421.50
216200.00
899.2
421.50
237800.00
912.0
421.50
237900.00
911.7
421.50
258000.00
916.4
421.50
258400.00
916.5
421.50
274100.00
925.5
421.50
274400.00
925.6
421.50
296000.00
932.5
421.50
297900.00
932.7
451.80
18700.00
738.4
451.80
18800.00
738.7
451.80
43000.00
772.1
451.80
43100.00
772.1
451.80
43200.00
772.4
451.80
70500.00
799.4
451.80
70600.00
799.6
451.80
85500.00
812.0
451.80
85500.00
812.2
451.80
99500.00
822.4
451.80
99600.00
822.4
451.80
99600.00
822.7
451.80
112800.00
827.6
451.80
113000.00
827.0
451.80
116500.00
833.9
451.80
116600.00
834.2
451.80
133600.00
842.0
451.80
133600.00
842.0
451.80
133700.00
841.4
451.80
174900.00
865.2
451.80
175000.00
864.5
451.80
216400.00
885.3
451.80
216600.00
884.6
451.80
238400.00
896.6
451.80
259000.00
906.0
451.80
259300.00
905.4
451.80
279400.00
912.7
451.80
280100.00
913.6
451.80
280100.00
912.9
500.30
23600.00
700.8
500.30
23700.00
700.7
500.30
56400.00
751.7
500.30
56600.00
751.6
500.30
84300.00
780.6
500.30
84400.00
780.4
500.30
105100.00
797.7
500.30
105200.00
797.6
500.30
129700.00
810.6
500.30
129800.00
810.7
500.30
168300.00
836.2
500.30
168500.00
836.3
500.30
188400.00
847.4
500.30
188500.00
847.5
500.30
215100.00
860.8
500.30
215300.00
860.9
500.30
235700.00
871.9
500.30
235900.00
872.0
500.30
238600.00
871.9
500.30
238800.00
872.0
500.30
258100.00
881.8
500.30
258300.00
881.9
500.30
279600.00
890.2
500.30
280200.00
890.3
534.90
38300.00
697.6
534.90
38300.00
696.9
534.90
52600.00
721.7
534.90
52800.00
721.0
534.90
69500.00
743.2
534.90
69600.00
742.5
534.90
89900.00
764.7
534.90
89900.00
764.7
534.90
90000.00
764.0
534.90
90000.00
764.0
534.90
105800.00
778.7
534.90
105900.00
778.0
534.90
125700.00
794.4
534.90
125800.00
793.6
534.90
171000.00
819.0
534.90
171100.00
819.0
534.90
171300.00
820.8
534.90
211800.00
843.1
534.90
212000.00
844.9
534.90
237300.00
859.2
534.90
257400.00
865.2
534.90
257700.00
867.1
534.90
279600.00
876.8
534.90
280800.00
878.1
Reference
Fixed
Measured
Temperature, K - Liquid
Pressure, kPa - Liquid
Mass density, kg/m3 - Liquid
283.16
1020.00
876.55
283.16
5010.00
879.36
283.16
10030.00
882.78
283.16
15050.00
886.11
283.16
20080.00
889.23
283.16
25060.00
892.35
283.16
30040.00
895.27
283.16
35080.00
898.24
283.16
40060.00
901.05
283.16
45050.00
903.77
283.16
50010.00
906.43
283.16
55060.00
909.09
283.16
60030.00
911.65
283.16
65050.00
914.15
298.15
1040.00
862.88
298.15
5040.00
865.93
298.15
10030.00
869.6
298.15
15050.00
873.21
298.15
20040.00
876.63
298.15
25050.00
879.93
298.15
30060.00
883.14
298.15
35020.00
886.25
298.15
40040.00
889.26
298.15
45070.00
892.2
298.15
50040.00
895.06
298.15
55040.00
897.86
298.15
60030.00
900.56
298.15
65020.00
903.2
323.15
1050.00
839.46
323.15
5050.00
843.04
323.15
10030.00
847.29
323.15
15010.00
851.38
323.15
20010.00
855.27
323.15
25060.00
859.05
323.15
30080.00
862.69
323.15
35020.00
866.13
323.15
40010.00
869.52
323.15
45060.00
872.84
323.15
50010.00
875.93
323.15
55010.00
879.01
323.15
60050.00
882.04
323.15
65030.00
884.91
348.15
1060.00
815.55
348.15
5070.00
819.75
348.15
10010.00
824.67
348.15
15030.00
829.43
348.15
20030.00
833.88
348.15
25020.00
838.2
348.15
30080.00
842.3
348.15
35050.00
846.21
348.15
40050.00
849.97
348.15
45070.00
853.63
348.15
50020.00
857.09
348.15
55060.00
860.49
348.15
60040.00
863.8
348.15
65070.00
867.0
373.15
1050.00
790.86
373.15
5020.00
795.87
373.15
10040.00
801.74
373.15
15040.00
807.26
373.15
20030.00
812.38
373.15
25080.00
817.35
373.15
30070.00
821.93
373.15
35040.00
826.36
373.15
40040.00
830.59
373.15
45030.00
834.57
373.15
50040.00
838.5
373.15
55040.00
842.23
373.15
60010.00
845.81
398.15
1070.00
765.25
398.15
5030.00
771.26
398.15
10040.00
778.22
398.15
15080.00
784.74
398.15
20010.00
790.62
398.15
25050.00
796.25
398.15
30040.00
801.49
398.15
35040.00
806.48
398.15
40020.00
811.17
398.15
45040.00
815.71
398.15
50020.00
819.96
398.15
55040.00
824.15
398.15
60020.00
828.11
398.15
65080.00
831.99
423.15
1050.00
738.06
423.15
5030.00
745.45
423.15
10060.00
753.93
423.15
15030.00
761.54
423.15
20000.00
768.41
423.15
25020.00
774.89
423.15
30020.00
780.87
423.15
35060.00
786.56
423.15
40020.00
791.82
423.15
45040.00
796.87
423.15
50040.00
801.63
423.15
55060.00
806.24
423.15
60040.00
810.55
423.15
65050.00
814.77
448.15
1040.00
708.96
448.15
5070.00
718.48
448.15
10040.00
728.71
448.15
15070.00
737.86
448.15
20050.00
745.94
448.15
25050.00
753.39
448.15
30040.00
760.21
448.15
35040.00
766.59
448.15
40020.00
772.48
448.15
45030.00
778.13
448.15
50030.00
783.39
448.15
55060.00
788.44
448.15
60010.00
793.17
448.15
65060.00
797.83
473.15
1030.00
676.8
473.15
5050.00
689.34
473.15
10050.00
702.19
473.15
15060.00
713.2
473.15
20020.00
722.73
473.15
25040.00
731.39
473.15
30010.00
739.18
473.15
35040.00
746.42
473.15
40050.00
753.09
473.15
45060.00
759.38
473.15
50050.00
765.18
473.15
55020.00
770.69
473.15
60030.00
775.95
473.15
65020.00
780.92
Reference
Fixed
Measured
Pressure, kPa - Liquid
Temperature, K - Liquid
Mass density, kg/m3 - Liquid
101.30
293.15
867.1
2000.00
293.15
868.3
4000.00
293.15
869.8
6000.00
293.15
871.2
10000.00
293.15
874.1
20000.00
293.15
880.9
30000.00
293.15
887.2
40000.00
293.15
893.2
50000.00
293.15
898.8
60000.00
293.15
904.1
70000.00
293.15
909.2
80000.00
293.15
914.1
90000.00
293.15
918.7
94000.00
293.15
920.5
96000.00
293.15
921.4
98000.00
293.15
922.3
100000.00
293.15
923.2
101.30
323.15
838.8
2000.00
323.15
840.3
4000.00
323.15
842.1
6000.00
323.15
843.8
10000.00
323.15
847.3
20000.00
323.15
855.2
30000.00
323.15
862.6
40000.00
323.15
869.4
50000.00
323.15
875.8
60000.00
323.15
881.8
70000.00
323.15
887.5
80000.00
323.15
893.0
90000.00
323.15
898.1
94000.00
323.15
900.1
96000.00
323.15
901.0
98000.00
323.15
902.0
100000.00
323.15
902.9
101.30
303.15
857.7
2000.00
303.15
858.8
4000.00
303.15
860.4
6000.00
303.15
861.9
10000.00
303.15
865.1
20000.00
303.15
872.3
30000.00
303.15
879.0
40000.00
303.15
885.2
50000.00
303.15
891.0
60000.00
303.15
896.7
70000.00
303.15
901.9
80000.00
303.15
907.0
90000.00
303.15
911.8
94000.00
303.15
913.6
96000.00
303.15
914.4
98000.00
303.15
915.3
100000.00
303.15
916.5
101.30
333.15
829.0
2000.00
333.15
830.9
4000.00
333.15
832.8
6000.00
333.15
834.7
10000.00
333.15
838.3
20000.00
333.15
846.8
30000.00
333.15
854.4
40000.00
333.15
861.6
50000.00
333.15
868.2
60000.00
333.15
874.5
70000.00
333.15
880.4
80000.00
333.15
885.9
90000.00
333.15
891.3
94000.00
333.15
893.3
96000.00
333.15
894.4
98000.00
333.15
895.4
100000.00
333.15
896.3
101.30
313.15
848.1
2000.00
313.15
849.4
4000.00
313.15
851.1
6000.00
313.15
852.8
10000.00
313.15
856.3
20000.00
313.15
863.8
30000.00
313.15
870.8
40000.00
313.15
877.5
50000.00
313.15
883.4
60000.00
313.15
889.2
70000.00
313.15
894.7
80000.00
313.15
899.9
90000.00
313.15
904.9
94000.00
313.15
906.6
96000.00
313.15
907.5
98000.00
313.15
908.5
100000.00
313.15
909.7
101.30
343.15
819.4
2000.00
343.15
821.4
4000.00
343.15
823.4
6000.00
343.15
825.4
10000.00
343.15
829.2
20000.00
343.15
838.2
30000.00
343.15
846.3
40000.00
343.15
853.8
50000.00
343.15
860.7
60000.00
343.15
867.2
70000.00
343.15
873.4
80000.00
343.15
879.2
90000.00
343.15
884.7
94000.00
343.15
886.7
96000.00
343.15
887.8
98000.00
343.15
888.8
100000.00
343.15
889.8
8000.00
298.15
872.6
12000.00
298.15
875.5
14000.00
298.15
876.9
16000.00
298.15
878.2
18000.00
298.15
879.6
22000.00
298.15
882.2
24000.00
298.15
883.5
26000.00
298.15
884.7
28000.00
298.15
886.0
32000.00
298.15
888.5
34000.00
298.15
889.6
36000.00
298.15
890.8
38000.00
298.15
892.0
42000.00
298.15
894.3
44000.00
298.15
895.4
46000.00
298.15
896.5
48000.00
298.15
897.7
52000.00
298.15
899.8
54000.00
298.15
900.9
56000.00
298.15
902.0
58000.00
298.15
903.1
62000.00
298.15
905.2
64000.00
298.15
906.2
66000.00
298.15
907.2
68000.00
298.15
908.2
72000.00
298.15
910.2
74000.00
298.15
911.2
76000.00
298.15
912.2
78000.00
298.15
913.1
82000.00
298.15
915.0
84000.00
298.15
915.9
86000.00
298.15
916.9
88000.00
298.15
917.8
92000.00
298.15
919.6
Reference
Fixed
Measured
Temperature, K - Liquid
Pressure, kPa - Liquid
Mass density, kg/m3 - Liquid
303.15
100.00
857.4
303.15
5000.00
861.3
303.15
10000.00
865.1
303.15
15000.00
868.7
303.15
20000.00
872.3
303.15
25000.00
875.6
303.15
30000.00
878.9
313.15
100.00
848.1
313.15
5000.00
852.1
313.15
10000.00
856.2
313.15
15000.00
860.0
313.15
20000.00
863.7
313.15
25000.00
867.2
313.15
30000.00
870.7
323.15
100.00
838.6
323.15
5000.00
842.9
323.15
10000.00
847.2
323.15
15000.00
851.2
323.15
20000.00
855.1
323.15
25000.00
858.9
323.15
30000.00
862.5
333.15
100.00
829.2
333.15
5000.00
833.7
333.15
10000.00
838.2
333.15
15000.00
842.5
333.15
20000.00
846.6
333.15
25000.00
850.5
333.15
30000.00
854.3
Reference
Fixed
Measured
Pressure, kPa - Liquid
Temperature, K - Liquid
Mass density, kg/m3 - Liquid
100.00
283.15
875.7
100.00
288.15
871.3
100.00
293.15
866.7
100.00
298.15
862.3
100.00
303.15
857.4
100.00
308.15
852.8
100.00
313.15
848.2
100.00
318.15
843.4
100.00
323.15
838.7
5000.00
283.15
879.4
5000.00
288.15
874.9
5000.00
293.15
870.4
5000.00
298.15
865.8
5000.00
303.15
861.3
5000.00
308.15
856.8
5000.00
313.15
852.2
5000.00
318.15
847.7
5000.00
323.15
843.0
10000.00
283.15
882.8
10000.00
288.15
878.4
10000.00
293.15
874.0
10000.00
298.15
869.5
10000.00
303.15
865.1
10000.00
308.15
860.7
10000.00
313.15
856.3
10000.00
318.15
851.8
10000.00
323.15
847.3
20000.00
283.15
889.3
20000.00
288.15
885.0
20000.00
293.15
880.8
20000.00
298.15
876.5
20000.00
303.15
872.3
20000.00
308.15
868.1
20000.00
313.15
863.8
20000.00
318.15
859.5
20000.00
323.15
855.2
30000.00
283.15
895.4
30000.00
288.15
891.3
30000.00
293.15
887.2
30000.00
298.15
883.0
30000.00
303.15
879.0
30000.00
308.15
875.0
30000.00
313.15
870.8
30000.00
318.15
866.8
30000.00
323.15
862.6
40000.00
283.15
901.1
40000.00
288.15
897.1
40000.00
293.15
893.2
40000.00
298.15
889.2
40000.00
303.15
885.2
40000.00
308.15
881.4
40000.00
313.15
877.4
40000.00
318.15
873.5
40000.00
323.15
869.5
50000.00
283.15
906.6
50000.00
288.15
902.7
50000.00
293.15
898.9
50000.00
298.15
895.0
50000.00
303.15
891.2
50000.00
308.15
887.4
50000.00
313.15
883.5
50000.00
318.15
879.7
50000.00
323.15
875.9
60000.00
283.15
911.7
60000.00
288.15
908.0
60000.00
293.15
904.3
60000.00
298.15
900.5
60000.00
303.15
896.8
60000.00
308.15
893.1
60000.00
313.15
889.4
60000.00
318.15
885.7
60000.00
323.15
881.9
Reference
Fixed
Measured
Temperature, K - Liquid
Pressure, kPa - Liquid
Mass density, kg/m3 - Liquid
293.14
580.00
867.3
293.14
2080.00
868.44
293.14
2100.00
868.49
293.14
4080.00
869.92
293.14
6080.00
871.41
293.14
8080.00
872.84
293.14
10080.00
874.27
293.14
10110.00
874.35
293.14
15090.00
877.74
293.14
15110.00
877.83
293.14
20090.00
881.09
293.14
20110.00
881.18
293.14
25090.00
884.33
293.14
25120.00
884.42
293.14
30090.00
887.47
293.14
30120.00
887.56
293.15
2080.00
868.48
293.15
4080.00
869.98
293.15
6080.00
871.45
293.15
8080.00
872.9
293.15
10080.00
874.33
293.15
15080.00
877.8
293.15
20080.00
881.15
293.15
25080.00
884.39
313.14
590.00
848.73
313.14
2090.00
850.02
313.14
4090.00
851.7
313.14
6090.00
853.35
313.14
8090.00
854.98
313.14
10090.00
856.57
313.14
15090.00
860.44
313.14
20090.00
864.16
313.14
25090.00
867.74
333.14
590.00
829.86
333.14
2090.00
831.32
333.14
4090.00
833.23
333.14
6090.00
835.1
333.14
8090.00
836.93
333.14
10090.00
838.73
333.14
15090.00
843.06
333.14
20090.00
847.2
333.14
25090.00
851.15
333.14
30090.00
854.96
353.14
2090.00
812.26
353.14
4090.00
814.44
353.14
6090.00
816.57
353.14
8090.00
818.63
353.14
10090.00
820.66
353.14
15090.00
825.54
353.14
20090.00
830.16
353.14
25090.00
834.54
353.14
30090.00
838.72
373.15
590.00
790.76
373.15
2090.00
792.7
373.15
4090.00
795.21
373.15
6090.00
797.64
373.15
8090.00
800.0
373.15
10090.00
802.3
373.15
15080.00
807.86
373.15
15090.00
807.78
373.15
20080.00
813.03
373.15
25080.00
817.91
373.15
30080.00
822.54
373.15
2090.00
792.76
373.15
4090.00
795.27
373.15
6090.00
797.7
373.15
8090.00
800.07
373.15
10090.00
802.37
373.49
2100.00
792.38
373.49
10110.00
802.04
373.49
15110.00
807.56
373.49
20120.00
812.74
373.49
25120.00
817.63
373.49
30120.00
822.28
Reference
Speed of sound, m/s
Fixed
Measured
Temperature, K - Liquid
Pressure, kPa - Liquid
Frequency, MHz - Liquid
Speed of sound, m/s - Liquid
303.15
101.33
2.0
1271.9
Reference
Fixed
Measured
Temperature, K - Liquid
Pressure, kPa - Liquid
Frequency, MHz - Liquid
Speed of sound, m/s - Liquid
303.15
100.00
2.0
1282.6
Reference
Operational condition: Frequency, MHz =
5 (Liquid)
Fixed
Measured
Temperature, K - Liquid
Pressure, kPa - Liquid
Speed of sound, m/s - Liquid
323.29
10200.00
1253.17
323.32
20600.00
1305.92
323.32
20480.00
1305.37
323.34
31540.00
1356.69
323.37
44870.00
1413.48
323.39
60820.00
1475.53
323.38
60790.00
1475.45
373.85
35520.00
1209.33
373.83
21270.00
1132.5
373.82
7570.00
1046.51
373.83
2170.00
1007.88
373.90
50350.00
1279.95
373.87
64470.00
1340.7
422.93
6580.00
863.73
422.98
20740.00
974.49
423.01
36450.00
1073.37
423.04
56200.00
1176.92
Reference
Fixed
Measured
Temperature, K - Liquid
Pressure, kPa - Liquid
Speed of sound, m/s - Liquid
240.00
103.32
1571.05
240.00
1104.21
1574.99
240.00
2104.94
1578.9
240.00
3105.74
1582.79
240.00
4106.28
1586.66
240.00
5107.43
1590.51
240.00
6107.67
1594.31
240.00
7108.38
1598.11
240.00
8109.15
1601.89
240.00
9109.83
1605.65
240.00
10110.50
1609.38
240.00
12612.20
1618.62
240.00
15113.80
1627.73
240.00
17615.50
1636.72
240.00
20117.10
1645.58
240.00
25120.60
1662.98
240.00
30124.00
1679.95
240.00
35127.40
1696.5
240.00
40130.80
1712.69
240.00
45134.20
1728.51
240.00
50137.60
1743.99
240.00
60144.40
1774.01
240.00
70151.40
1802.89
240.00
80158.20
1830.74
240.00
90165.20
1857.63
240.00
100172.00
1883.64
260.00
102.53
1476.76
260.00
1103.38
1481.1
260.00
2103.99
1485.39
260.00
3104.83
1489.66
260.00
4105.61
1493.9
260.00
5106.49
1498.11
260.00
6106.82
1502.29
260.00
7107.53
1506.45
260.00
8108.28
1510.58
260.00
9109.01
1514.67
260.00
10109.80
1518.75
260.00
12611.80
1528.82
260.00
17615.40
1548.49
260.00
20117.20
1558.1
260.00
25120.70
1576.92
260.00
30124.10
1595.21
260.00
35127.60
1613.03
260.00
40131.00
1630.39
260.00
45134.50
1647.33
260.00
50138.20
1663.87
260.00
60145.40
1695.85
260.00
70152.50
1726.52
260.00
80159.50
1755.96
260.00
90166.50
1784.35
260.00
15113.60
1538.73
260.00
100174.00
1811.73
280.00
103.62
1385.49
280.00
1104.53
1390.25
280.00
2105.31
1394.98
280.00
3106.24
1399.66
280.00
4107.05
1404.31
280.00
5107.65
1408.92
280.00
6108.14
1413.5
280.00
7108.79
1418.04
280.00
8109.45
1422.55
280.00
9110.12
1427.02
280.00
10110.80
1431.46
280.00
12612.50
1442.42
280.00
15114.20
1453.19
280.00
17616.00
1463.78
280.00
20118.00
1474.18
280.00
25121.50
1494.49
280.00
30125.00
1514.18
280.00
35128.50
1533.29
280.00
40132.00
1551.88
280.00
45135.00
1569.95
280.00
50138.50
1587.57
280.00
60145.30
1621.55
280.00
70152.30
1653.99
280.00
80159.10
1685.08
280.00
90165.80
1714.93
280.00
100173.00
1743.69
300.00
102.33
1297.15
300.00
1103.24
1302.4
300.00
2104.05
1307.6
300.00
3104.69
1312.74
300.00
103.33
1297.13
300.01
1104.24
1302.37
300.01
2104.88
1307.56
300.01
3105.58
1312.7
300.01
4106.36
1317.8
300.01
5107.04
1322.86
300.01
6107.45
1327.87
300.01
7108.08
1332.83
300.01
8108.73
1337.75
300.01
9109.36
1342.63
300.01
10110.00
1347.47
300.01
12611.70
1359.39
300.01
15113.40
1371.09
300.01
17615.20
1382.55
300.01
20116.90
1393.79
300.01
25120.30
1415.68
300.01
30123.60
1436.82
300.01
35126.90
1457.3
300.01
40130.10
1477.14
300.01
45133.30
1496.4
300.01
50136.50
1515.12
300.01
60143.10
1551.11
300.01
70150.40
1585.36
300.01
80158.50
1618.06
300.01
90165.60
1649.39
300.01
100172.00
1679.48
320.00
102.82
1211.56
320.00
102.83
1211.57
320.00
1103.61
1217.34
320.00
2104.26
1223.07
320.00
3105.03
1228.73
320.00
4105.82
1234.33
320.00
5106.65
1239.88
320.00
6107.07
1245.37
320.00
7107.78
1250.8
320.00
8108.51
1256.17
320.00
9109.16
1261.5
320.00
10109.80
1266.77
320.00
12611.50
1279.74
320.00
15113.20
1292.43
320.00
17614.90
1304.82
320.00
20116.60
1316.97
320.00
25120.10
1340.53
320.00
30123.50
1363.2
320.00
35127.10
1385.08
320.00
40130.90
1406.22
320.00
50137.90
1446.53
320.00
45134.40
1426.68
320.00
60144.90
1484.55
320.00
70152.00
1520.59
320.00
80158.90
1554.89
320.00
90165.90
1587.66
320.00
100173.00
1619.07
340.00
102.94
1128.51
340.00
1103.68
1134.9
340.00
2104.32
1141.21
340.00
3105.04
1147.45
340.00
4105.83
1153.61
340.00
103.20
1128.51
340.00
1104.11
1134.9
340.00
2104.92
1141.22
340.00
3105.78
1147.45
340.00
4106.59
1153.62
340.00
5107.25
1159.71
340.00
6107.67
1165.72
340.00
7108.35
1171.67
340.00
8109.05
1177.55
340.00
9109.73
1183.36
340.00
10110.30
1189.11
340.00
12612.00
1203.23
340.00
15113.70
1216.98
340.00
17615.40
1230.4
340.00
20117.10
1243.5
340.00
25120.50
1268.83
340.00
30124.00
1293.1
340.00
35127.60
1316.43
340.00
40131.20
1338.91
340.00
45134.90
1360.61
340.00
50138.80
1381.6
340.00
60145.70
1421.66
340.00
70152.60
1459.49
340.00
80159.50
1495.39
340.00
90166.50
1529.58
340.00
100174.00
1562.28
360.00
103.40
1047.63
360.00
1104.11
1054.73
360.00
2104.83
1061.73
360.00
3105.45
1068.62
360.00
4106.44
1075.42
360.00
5107.02
1082.11
360.00
6107.39
1088.72
360.00
7108.04
1095.24
360.00
8108.72
1101.68
360.00
9109.46
1108.04
360.00
10110.10
1114.32
359.99
10111.10
1114.35
360.00
12611.90
1129.68
359.99
12612.60
1129.71
359.99
15114.00
1144.62
359.99
17615.60
1159.13
359.99
20117.30
1173.26
359.99
25120.80
1200.47
359.99
30124.20
1226.42
359.99
35127.60
1251.26
359.99
40131.10
1275.12
359.99
45134.50
1298.07
359.99
50137.90
1320.21
359.99
60144.90
1362.33
359.99
70152.00
1401.95
359.99
80159.00
1439.41
359.99
90166.00
1474.99
359.99
100173.00
1508.93
380.00
101.06
968.429
380.00
1102.50
976.366
380.00
2103.36
984.155
380.00
3104.10
991.809
380.00
4104.99
999.336
380.00
5105.71
1006.74
380.00
6106.12
1014.03
380.00
7106.84
1021.2
380.00
8107.59
1028.27
380.00
9108.31
1035.23
380.00
10109.00
1042.09
380.00
12610.80
1058.83
380.00
15113.40
1075.03
380.00
17615.20
1090.72
380.00
20116.90
1105.95
380.00
25120.40
1135.15
380.00
30123.90
1162.87
380.00
35127.30
1189.28
380.00
40130.80
1214.55
380.00
45134.00
1238.78
380.00
50137.50
1262.09
380.00
60144.50
1306.28
380.00
70151.60
1347.66
380.00
80158.60
1386.66
380.00
90165.60
1423.62
380.00
100173.00
1458.77
400.00
603.01
894.984
400.00
1104.15
899.421
400.00
2104.60
908.149
400.00
3105.31
916.697
400.00
4106.00
925.074
400.00
5106.69
933.288
400.00
6107.36
941.35
400.00
7108.01
949.265
400.00
8108.66
957.044
400.00
9109.32
964.687
400.00
10109.90
972.207
400.00
12611.60
990.479
400.00
15113.30
1008.07
400.00
17615.10
1025.05
400.00
20116.80
1041.47
400.00
25120.20
1072.79
400.00
608.94
895.044
400.00
4105.08
925.079
400.00
15112.70
1008.09
400.00
30123.20
1102.36
400.00
35126.70
1130.4
400.00
40130.40
1157.11
400.00
45134.00
1182.65
400.00
50137.50
1207.15
400.00
60144.50
1253.4
400.00
70151.50
1296.54
400.00
80158.50
1337.05
400.00
90165.60
1375.32
400.00
100173.00
1411.65
420.00
1102.46
823.404
420.00
2103.16
833.269
420.00
3103.88
842.891
420.00
4104.56
852.281
420.00
5105.25
861.453
420.00
6105.94
870.42
420.00
7106.62
879.196
420.00
8107.32
887.789
420.00
9108.03
896.213
420.00
10108.70
904.476
420.00
12610.50
924.47
420.00
15112.30
943.614
420.00
17614.10
961.991
420.00
20115.90
979.684
420.00
25119.40
1013.26
420.00
30122.80
1044.75
420.00
35126.30
1074.47
420.00
40129.80
1102.67
420.00
45133.20
1129.52
420.00
50136.70
1155.2
420.00
60143.90
1203.5
420.00
70151.00
1248.37
420.00
80158.00
1290.36
420.00
90165.10
1329.92
420.00
100172.00
1367.39
Reference
Thermal conductivity, W/m/K
Fixed
Measured
Temperature, K - Liquid
Pressure, kPa - Liquid
Thermal conductivity, W/m/K - Liquid
294.20
100.00
0.1320
294.20
10000.00
0.1360
294.20
20000.00
0.1390
314.10
100.00
0.1270
314.10
10000.00
0.1310
314.10
20000.00
0.1350
334.40
100.00
0.1220
334.40
10000.00
0.1260
334.40
20000.00
0.1290
Reference
Fixed
Measured
Temperature, K - Liquid
Pressure, kPa - Liquid
Thermal conductivity, W/m/K - Liquid
317.52
20330.00
0.1330
317.46
15330.00
0.1292
317.42
10550.00
0.1277
317.39
5130.00
0.1266
317.42
1050.00
0.1251
336.30
20300.00
0.1267
336.34
15140.00
0.1245
336.32
10150.00
0.1229
336.39
5020.00
0.1205
336.42
1030.00
0.1194
356.27
20040.00
0.1218
356.27
15170.00
0.1205
356.36
10440.00
0.1184
356.43
5170.00
0.1166
356.41
1160.00
0.1131
376.88
20030.00
0.1185
376.95
15270.00
0.1147
376.95
10160.00
0.1124
376.95
5200.00
0.1108
377.07
1080.00
0.1096
396.26
20010.00
0.1141
395.96
15140.00
0.1121
396.23
10180.00
0.1091
396.28
5150.00
0.1072
396.32
1030.00
0.1059
416.29
20250.00
0.1104
416.33
15150.00
0.1066
416.72
10280.00
0.1054
416.68
5290.00
0.1033
416.75
1040.00
0.1013
436.23
20100.00
0.1051
436.34
15130.00
0.1036
436.48
10230.00
0.1026
436.52
5170.00
0.0992
436.37
1020.00
0.0972
456.02
20030.00
0.1029
456.22
15290.00
0.1003
456.24
10330.00
0.0990
456.04
5400.00
0.0956
456.26
1140.00
0.0928
476.38
20260.00
0.0994
476.75
15330.00
0.0965
476.35
10170.00
0.0941
476.73
5010.00
0.0914
476.61
1110.00
0.0901
496.03
20300.00
0.0962
496.27
15290.00
0.0945
496.31
10420.00
0.0928
496.49
5210.00
0.0870
496.15
2850.00
0.0875
516.06
20190.00
0.0940
516.20
15360.00
0.0916
516.21
10220.00
0.0906
516.40
5090.00
0.0862
536.56
20330.00
0.0921
536.39
15400.00
0.0897
536.30
10150.00
0.0873
556.59
20100.00
0.0927
556.53
15430.00
0.0908
556.68
10050.00
0.0869
576.72
20150.00
0.0885
Reference
Correlations
Similar Compounds
Find more compounds similar to Toluene .
Mixtures
Find more mixtures with Toluene .
Sources
KDB Pure (Korean Thermophysical Properties Databank)
KDB Vapor Pressure Data
Crippen Method
High-Pressure Viscosity Measurements for the Ethanol + Toluene Binary System
Effect of Temperature on the Change of Refractive Index on Mixing for Butyl Acetate + Aromatic Hydrocarbons
Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
Thermal Conductivities of [bmim][PF6], [hmim][PF6], and [omim][PF6] from 294 to 335 K at Pressures up to 20 MPa.
A Digital Variable-Angle Rolling-Ball Viscometer for Measurement of Viscosity, Density, and Bubble-Point Pressure of CO2 and Organic Liquid Mixtures
Thermal Conductivity of Liquid Dimethoxyethane from 243 to 353K at Pressures up to 30 MPa
Viscometric and Volumetric Properties of 10 Regular Binary Systems at 308.15 K and 313.15 K
Thermodynamic Properties of Ternary Liquid Mixtures of 2-Pyrrolidinone with Aromatic Hydrocarbons
Densities and Volumetric Properties of Binary Mixtures of Butyl Acrylate with Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Mesitylene at Temperatures from 288.15 K to 318.15 K
Topological Investigations of Excess Molar Volumes and Excess Isentropic Compressibilities of Ternary Mixtures Containing Pyrrolidin-2-one at 308.15 K
Isentropic Compressibilities Changes of Mixing of Tetrahydropyran and Aromatic Hydrocarbons Ternary Mixtures at 308.15 K
Densities and Kinematic Viscosities of One Quinary Regular Liquid System and Its Five Quaternary Sub-Systems at Temperatures (293.15 and 298.15) K
Study of Acoustic Parameters in Binary Mixture at Variable Frequencies
Densities and Kinematic Viscosities of a Quinary Regular Liquid System and Its Five Quaternary Subsystems at 293.15A K and 298.15A K
Thermal Conductivity of n-Pentadecane (C15H32)
Hydrogen solubility in a chemical hydrogen storage medium, aromatic hydrocarbon, cyclic hydrocarbon, and their mixture for fuel cell systems
Experimental solubility data of various n-alkane waxes: effects of alkane chain length, alkane odd versus even carbon number structures, and solvent chemistry on solubility
The experiments and correlations of the solubility of ethylene in toluene solvent
An equipment for dynamic measurements of vapour liquid equilibria and results in binary systems containing cyclohexylamine
Volumetric properties under pressure for the binary system ethanol + toluene
Topological and thermodynamic investigations of molecular interactions in binary mixtures: Molar excess volumes and molar excess enthalpies
Isothermal vapour pressures and excess functions of 3,5- and 2,6-dimethylpyridine with toluene measurement and prediction
Experimental investigation of the vapour-liquid equilibrium of binary and ternary mixtures containing dibutyl ether (DBE), cyclohexane and toluene at 313.15 K
Vapor liquid liquid equilibria of perfluorohexane +CO2 + methanol, +toluene, and +acetone at 313K
Solubility of hydrogen in toluene for the ternary system H2 +CO2 + toluene from 305 to 343K and 1.2 to 10.5MPa
Isobaric vapor liquid equilibria for binary systems of butyl chlorides with heptane, toluene and cyclohexane at 101.3, 80.0 and 53.3 kPa
Infinite dilution activity coefficient measurements by inert gas stripping method
Volumetric and derivative properties under pressure for the system 1-propanol + toluene: A discussion of PC-SAFT and SAFT-VR
Ternary liquid liquid equilibria for mixtures of toluene + n-heptane + an ionic liquid
Infinite dilution activity coefficients, specific retention volumes and solvation thermodynamics of hydrocarbons in C78H158 branched alkane solvent
Binary liquid liquid equilibrium in the systems containing monofunctional benzene derivates and 1,2-ethanediol
Thermodynamic study of 1,1,2,2-tetrachloroethane + hydrocarbon mixtures I. Excess and solvation enthalpies
Vapor liquid equilibrium for binary system of diethyl sulfide + cyclohexane at 353.15 and 343.15 K and diethyl sulfide + 2-ethoxy-2-methylpropane at 343.15 and 333.15 K
Densities, viscosities and ultrasonic velocities of binary mixtures of methylbenzene with hexan-2-ol, heptan-2-ol and octan-2-ol at T = 298.15 and 308.15K
Vapour liquid equilibria, enthalpy of mixing of binary mixtures containing diisopropylether DIPE and monoaromatic hydrocarbons Experimental results and modelling
A simple apparatus for data solubility determination
Measurement of vapor.liquid equilibria (VLE) and excess enthalpies (HE) of binary systems with 1-alkyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide and prediction of these properties and A using modified UNIFAC (Dortmund)
Vapor liquid equilibrium for binary system of thiophene + 2,2,4-trimethylpentane at 343.15 and 353.15K and thiophene + 2-ethoxy-2-methylpropane at 333.15 and 343.15K
Ultrasonic and viscometric study of molecular interactions in binary mixtures of aniline with 1-propanol, 2-propanol, 2-methyl-1-propanol, and 2-methyl-2-propanol at different temperatures
Vapor liquid equilibria in ternary systems of associating components (water, aniline, cyclohexylamine) and hydrocarbons (octane or toluene)
Hydrogen solubility of mixed naphthenes and aromatics for a new hydrogen storage medium in fuel cell system
Vapor-liquid equilibrium for the binary mixtures of dimethylsulfoxide with substituted benzenes
Isothermal vapor liquid equilibrium at 333.15K and excess volumes and molar refractivity deviation at 298.15K for the ternary system di-butyl ether (1) + ethanol (2) + toluene (3) and its binary subsystems
Measurements of the isochoric heat capacity, the critical point (TC, nC) and vapor liquid coexistence curve (TS, nS) of high-purity toluene near the critical point*
Excess enthalpies of dimethylsulfoxide with substituted benzenes at 298.15K
Liquid liquid equilibrium of ternary systems 1-butyl-3-methylimidazolium hexafluorophosphate + aromatic + aliphatic
Homogeneity of the water + ethanol + toluene azeotrope at 101.3 kPa
Experimental and predicted phase equilibria and excess properties for systems with ionic liquids
A new high-pressure vapour liquid equilibrium apparatus
Isothermal vapor liquid equilibrium at 333.15K and excess molar volumes at 298.15K for the ternary system di-isopropyl ether + n-propyl alcohol + toluene and its binary subsystems
Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium trifluoromethanesulfonate using GLC
Isothermal vapor liquid equilibria for binary mixtures of benzene, toluene, m-xylene, and N-methylformamide at 333.15K and 353.15K
Activity coefficients at infinite dilution measurements for organic solutes and water in the 1-hexyloxymethyl-3-methyl-imidazolium and 1,3-dihexyloxymethyl-imidazolium bis(trifluoromethylsulfonyl)-imide ionic liquids The cation influence
Liquid phase equilibria for mixtures of (an aliphatic hydrocarbon + toluene + gamma-butyrolactone)
Vapor liquid equilibria and density measurement for binary mixtures of toluene, benzene, o-xylene, m-xylene, sulfolane and nonane at 333.15K and 353.15K
Vapor liquid equilibrium for the binary systems tetrahydrothiophene + toluene and tetrahydrothiophene + o-xylene at 368.15 K and 383.15 K
Measurement and correlation of liquid liquid equilibria for ternary systems {cyclooctane + aromatic hydrocarbon + 1-ethyl-3-methylpyridinium ethylsulfate} at T = 298.15 K and atmospheric pressure
(Solid + liquid) and (liquid + liquid) phase equilibria study and correlation of the binary systems {N-butyl-3-methylpyridinium tosylate + water, or + an alcohol, or + a hydrocarbon}
Liquid liquid equilibrium of ternary systems 1-octyl-3-methylimidazolium hexafluorophosphate + aromatic + aliphatic hydrocarbons
Phase equilibria on five binary systems containing 1-butanethiol and 3-methylthiophene in hydrocarbons
Phase equilibria for systems containing dimethyl disulfide and diethyl disulfide with hydrocarbons at 368.15 K
Liquid-liquid equilibria for ternary systems of {cyclohexane + aromatic compounds + 1-ethyl-3-methylpyridinium ethylsulfate}
Gas-liquid chromatography measurements of activity coefficients at infinite dilution of hydrocarbons and alkanols in 1-alkyl-3-methylimidazolium bis(oxalato)borate
Prediction of phase equilibria and excess properties for systems with ionic liquids using modified UNIFAC: Typical results and present status of the modified UNIFAC matrix for ionic liquids
Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-ethyl-3-methylimidazolium methanesulfonate
N-butylpyridinium bis-(trifluoromethylsulfonyl)imide ionic liquids as solvents for the liquid-liquid extraction of aromatics from their mixtures with alkanes: isomeric effect of the cation
Isothermal vapor-liquid equilibrium at T = 333.15 K and excess volumes and molar refractivity deviation at T = 298.15 K for the ternary mixtures {di-methyl carbonate (DMC) + ethanol + benzene} and {DMC+ ethanol + toluene}
Application of [EMim][ESO4] ionic liquid as solvent in the extraction of toluene from cycloalkanes: Study of liquid-liquid equilibria at T = 298.15 K
Influence of anion structure on the liquid-liquid equilibria of 1-(3-hydroxypropyl)pyridinium cation based ionic liquid-hydrocarbon binary systems
Physical properties of 3-methyl-N-butylpyridinium tricyanomethanide and ternary LLE data with an aromatic and an aliphatic hydrocarbon at T = (303.2 and 328.2) K and p = 0.1 MPa
Liquid-liquid equilibria of {n-heptane + toluene + aniline} ternary system: Experimental data and correlation
Vapor liquid liquid equilibrium and vapor liquid equilibrium for the quaternary system water ethanol cyclohexane toluene and the ternary system water cyclohexane toluene. Isobaric experimental determination at 101.3 kPa
Solubility of elemental sulfur in pure organic solvents and organic solvent-ionic liquid mixtures from 293.15 to 353.15 K
Isobaric vapor-liquid equilibrium for the binary mixtures of nonane with cyclohexane, toluene, m-xylene, or p-xylene at 101.3 kPa
Hexyl dimethylpyridinium ionic liquids for desulfurization of fuels. Effect of the position of the alkyl side chains
Ether + alcohol + hydrocarbon mixtures in fuels and bio-fuels: Excess enthalpies of binary mixtures containing dibutyl ether (DBE) or 1-butanol and 1-hexene or methylcyclohexane or toluene or cyclohexane or 2,2,4-trimethylpentane at 298.15K and 313.15K
Capacity of ionic liquids [EMim][NTf2] and [EMpy][NTf2] for extraction of toluene from mixtures with alkanes: Comparative study of the effect of the cation
Effect of temperature on the solubility of 3-aminopyridine in binary ethanol + toluene solvent mixtures
Thermodynamic characterization of second generation biofuels: Vapour-liquid equilibria and excess enthalpies of the binary mixtures 1-pentanol and cyclohexane or toluene
Phase equilibrium properties of the ternary mixture dibutyl ether + toluene + heptane at 313.15 K
Determination of the solubility, dissolution enthalpy and entropy of pyrene in different solvents
Isobaric vapor-liquid equilibrium for four binary systems of 3-methylthiophene
Activity coefficients at infinite dilution of organic solutes in the ionic liquid ethyl(2-hydroxyethyl)dimethyl-ammonium diethylphosphate using gas liquid chromatography
Activity coefficients at infinite dilution of organic solutes in 1-octyl-3-methylimidazolium nitrate using gas-liquid chromatography
Effect of 1-methyl 3-octylimidazolium thiocyanate on vapor-liquid equilibria of binary mixtures of hydrocarbons
Vapour-liquid equilibrium (VLE) for the systems furan + n-hexane and furan + toluene. Measurements, data treatment and modeling using molecular models
Solubility of hydrofluorocarbons in aromatic solvents and alcohols: Experimental data and modeling with CPA EoS
Isobaric vapor-liquid equilibrium of binary systems of decane with p-, o-, m-xylene at 20 kPa
Liquid-liquid equilibria of imidazolium ionic liquids having bistriflamide or triflate anions with aromatic non-polar and polar compounds
Separation of toluene from n-heptane using monocationic and dicationic ionic liquids
Solubility of ethylene in toluene, norbornene, and toluene + norbornene mixture
Phase behaviour of ionic liquid 1-butyl-1-methylpyrrolidinium tris(pentafluoroethyl)trifluorophosphate with alcohols, water and aromatic hydrocarbons
Isobaric vapor-liquid equilibrium for binary systemsof toluene + o-xylene, benzene + o-xylene, nonane + benzene and nonane + heptane at 101.3 kPa
Using binary mixtures of dicationic ionic liquids for determination ofactivity coefficients at infinite dilution by gas-liquid chromatography
A novel continuous flow apparatus with a video camera system for high pressure phase equilibrium measurements
Desulfurization of fuels by liquid-liquid extraction with1-ethyl-3-methylimidazolium ionic liquids
Solubility of 1, 3, 2-dioxaphosphorinane-5,5-dimethyl -2- (2,4,6-tribromophenoxy)-2-oxide in selected solvents
Phase equilibria of binary mixtures (ionic liquid + aromatic hydrocarbon): Effect of the structure of the components on the solubility
Measurements of activity coefficients at infinite dilution in vegetable oils and capric acid using the dilutor technique
Towards automated characterisation of liquid-liquid equilibria
Extraction of toluene from alkane using [Bmim][NO3] or [Omim][NO3] ionic liquid at 298.15 K and atmospheric pressure
Prediction and measurement of phase equilibria for the extraction of BTX from naphtha reformate using BMIMPF6 ionic liquid
Isobaric vapor-liquid equilibrium for binary system of cinnamaldehyde + benzaldehyde at 10, 20 and 30 kPa
Liquid-liquid extraction of toluene from n-heptane by {[emim][TCM] + [emim][DCA]} binary ionic liquid mixtures
Isobaric vapour + liquid equilibria for three binary systems (toluene + anisole, nbutylbenzene + anisole, and guaiacol + anisole) at 101.33 kPa
Vapor-liquid equilibrium for the binary mixtures of dipropylene glycol with aromatic hydrocarbons: Experimental and regression
Isobaric vapor-liquid equilibrium for binary and ternary systems with toluene, 2-methoxyethanol and dimethyl sulfoxide at 101.3 kPa
Thermodynamics of risperidone and solubility in pure organic solvents
Thermal conductivity of ethyl fluoride (HFC161)
Study of critical and maximum temperatures of coexistence of liquid and gas phase in hydrocarbons binary mixtures of aromatic hydrocarbons with alkanes and cycloalkanes
Experimental and theoretical study of interaction between organic compounds and 1- (4-sulfobutyl)-3-methylimidazolium based ionic liquids
Heat capacities of binary and ternary mixtures containing o-chlorotoluene, cyclic ether and aromatic hydrocarbons
Liquid-liquid equilibria for multicomponent mixtures of 2,2-dimethyl-1,3-dioxolane with n-heptane, toluene, ethanol and water
A modified continuous flow apparatus for gas solubility measurements at high pressure and temperature with camera system
Measurement and correlation of the solubility of N-(phosphonomethyl)iminodiacetic acid in different organic solvents
Liquid-liquid equilibria for ternary system water + toluene+ benzaldehyde at (303.2 to 343.2) K
Phase equilibria of the water + 1-butanol + toluene ternary system at 101.3 kPa
Isothermal vapor liquid equilibrium and molar excess Gibbs energies of two ternary systems containing either 1-butanol or 2-butanol + 1- hexene + methylbenzene at 313.15 K
Liquid-liquid equilibrium data for binary systems containing o-dichlorobenzene and nitrobenzene
Study of interaction between organic compounds and mono or dicationic oxygenated ionic liquids using gas chromatography
Phase behaviour of tricyanomethanide-based ionic liquids with alcohols and hydrocarbons
Vapor liquid equilibria of {n-heptane + toluene + [emim][DCA]} system by headspace gas chromatography
Removal of aromatic hydrocarbons from hydrocarbon mixture using glycols at 303.15 K and 333.15 K and atmospheric pressure: Experimental and calculated data by NRTL and UNIQUAC models
Solubilities of phosphoric acid, P,P0-1,4-phenylene P,P,P0,P0-tetraphenyl ester in the organic solvents
Liquid liquid equilibria in the ternary systems {hexadecane + BTX aromatics + 2-methoxyethanol or acetonitrile} at 298.15 K
Isothermal vapor- liquid equilibria and excess molar enthalpy of 2-methylpyrazine (2MP) containing binary mixtures. Comparison with DISQUAC predictions
Solid-liquid equilibrium of diphenyl anilinophosphonate in the different organic solvents
Experimental measurements and modelling of volumetric properties, refractive index and viscosity of binary systems of ethyl lactate with methyl ethyl ketone, toluene and n-methyl-2-pirrolidone at 288.15 323.15 K and atmospheric pressure. New UNIFAC VISCO and ASOG VISCO interaction parameters
Measurement of phase equilibria data for the extraction of toluene from alkane using different solvents
The ionic liquid 1-ethyl-3-methylimidazolium tris(pentafluoroethyl) trifluorophosphate as alternative extractant for BTEX separation
Liquid-liquid equilibria for ternary mixtures of 2,2-dimethyl-1,3-dioxolane-4-methanol with n-heptane, toluene, ethanol and water
Liquid-liquid phase diagrams of poly(ethylene glycol) and aromatic hydrocarbons
Solubility correlation and thermodynamic analysis of two forms of Metaxalone in different pure solvents
Non-random two-liquid modelling of switchable-hydrophilicity solvent systems: N,N-Dimethylcyclohexanamine, water, and toluene
Thermodynamics properties, VLE and HE, of the systems 2-pentanol and cyclohexane or methylbenzene for contributing to the knowledge of new biofuels
Speed of sound measurement in ethyl tert-butyl ether and tert-amyl methyl ether by Brillouin light scattering
Liquid-liquid equilibria in the ternary and multicomponent systems involving hydrocarbons, thiophene or pyridine and ionic liquid (1-benzyl-3-metylimidazolium bis(trifluorometylsulfonyl)imide)
Activity coefficients at infinite dilution of organic solvents and water in 1-butyl-3-methylimidazolium dicyanamide. A literature review of hexane/hex-1-ene separation
Vapor-liquid equilibria for n-heptane + (benzene, toluene, pxylene, or ethylbenzene) + {[4empy][Tf2N] (0.3) + [emim][DCA] (0.7)} binary ionic liquid mixture
Solubility of D-phenylglycine methyl ester hydrochloride in water and in organic individual or mixed solvents: Experimental data and results of thermodynamic modeling
Phase-equilibrium measurements with a novel multi-purpose high-pressure view cell: CO2 + n-decane and CO2 + toluene
Vapour-liquid equilibrium for tripropylene glycol + aromatic hydrocarbons binary systems: Experimental data and regression
Liquid-liquid equilibria for the extraction of furfural from aqueous solution using different solvents
Phase equilibria of phenol + toluene + quaternary ammonium salts for the separation of phenols from oil with forming deep eutectic solvents
Determination of solubility parameters from density measurements for non-polar hydrocarbons at temperatures from (298 to 433) K and pressures up to 137 MPa
Measurement and prediction of liquid-liquid equilibria in ternary systems containing water, an organic component, and cyclohexanol
Measurement of the solubility of the salt of 2- mercaptobenzothiazole with cyclohexylamine and tert-butylamine in various solvents at low temperatures: Models and thermodynamic parameters
In situ measurement of liquid-liquid equilibria by medium field nuclear magnetic resonance
Separation of the mixture pyridine + methylbenzene via several acidic ionic liquids: Phase equilibrium measurement and correlation
A milliliter-scale setup for the efficient characterization of isothermal vapor-liquid equilibria using Raman spectroscopy
Ternary phase behavior of phenol + toluene + zwitterionic alkaloids for separating phenols from oil mixtures via forming deep eutectic solvents
High selective water/butan-1-ol separation on investigation of limiting activity coefficients with [P8,8,8,8][[NTf2] ionic liquid
Phase behavior and densities of propylene + toluene and ethylene + toluene systems to 580 K and 70 MPa
The solubility of maleic acid in various inorganic salts and organic solvents: Thermodynamics model and parameters
Surface tension of four oxygenated fuels: experiment and correlation
Separation of binary mixtures based on limiting activity coefficients data using specific ammonium-based ionic liquid and modelling of thermodynamic functions
Measurements of activity coefficient at infinite dilution for organic solutes in tetramethylammonium chloride + ethylene glycol deep eutectic solvent using gas-liquid chromatography
Plotting of phase (vapor-liquid) transition surface near the critical point out of data from isochoric experiment. Experimental procedure
Determination and correlation of solubility of 2,2',4,4',6,6 '-hexanitro-1,1'-biphenyl and 2,2',2" ,4,4',4" ,6,6',6" -Nonanitro-1,1 ':3',1"-terphenyl in six pure solvents
Liquid-liquid equilibria of water + solutes (acetic acid/ acetol/furfural/guaiacol/methanol/phenol/propanal) + solvents (isopropyl acetate/toluene) ternary systems for pyrolysis oil fractionation
Solubility of 1-methyl-4-nitropyrazole in seventeen pure solvents at temperatures from 283.15 K to 323.15 K
Tetramethylammonium chloride + glycerol deep eutectic solvent as separation agent for organic liquid mixtures: Assessment from experimental limiting activity coefficients
Thermodynamics and activity coefficients at infinite dilution for organic solutes in the ionic liquid 1-butyl-1-methylpyrrolidinium dicyanamide
New ionic liquid [P4,4,4,4][NTf2] in bio-butanol extraction on investigation of limiting activity coefficients
High temperature and pressure water/oil interfacial tension benchmark data for the Ninth Industrial Fluid Properties Simulation Challenge
Solubility of citalopram hydrobromide in(ethanol + toluene) and (ethanol + ethyl acetate) at 283.15-318.15 K and its correlation with the Jouyban-Acree and CNIBS/R-K models
Ammonium ionic liquids in extraction of bio-butan-1-ol from water phase using activity coefficients at infinite dilution
Phase equilibria of 1-hexyl-3-methylimidazolium acetate with water and oil
Thermal conductivity and thermal diffusivity of pyrrolidinium- based ionic liquids at atmospheric pressure
Dissolution behavior and thermodynamic properties of lapatinib ditosylate in pure and mixed organic solvents from T = (283.15-323.15) K
Measurement and modeling of infinite dilution activity coefficients of organic compounds in an equimolar ionic liquid mixture of [Bmim]Cl and [Bmim][Tf2N]
Application of trihexyltetradecylphosphonium dicyanamide ionic liquid for various types of separations problems: Activity coefficients at infinite dilution measurements utilizing GLC method
Solubility measurements and thermodynamic modeling of pyrazinamide in five different solvent-antisolvent mixtures
Mixture densities and viscosities of toluene with ethylene or propylene at temperatures to 530 K and pressures to 70 MPa
(Liquid + liquid) phase behavior for systems containing (aromatic + TBA + methylcyclohexane)
(Vapour + liquid) equilibria of (1-butanol + benzene, or toluene, or o-, or m-, or p-xylene) at T = 308.15 K
Effect of temperature on the volumetric properties of (cyclohexanone + an aromatic hydrocarbon)
Experimental densities and excess volumes for binary mixtures of (dimethyl sulfoxide + an aromatic hydrocarbon) at temperatures from (293.15 to 353.15) K at atmospheric pressure
(P, Vm, T) Measurements of (toluene + propiophenone) at temperatures from 298.15 K to 328.15 K and at pressures up to 40 MPa
Excess molar volumes of (acetophenone + benzene, or toluene, or 1,3-xylene, or 1,3,5-trimethylbenzene) at temperatures (298.15 and 328.15) K
Studies on thermo-acoustic parameters in binary liquid mixtures of phosphinic acid (Cyanex 272) with different diluents at temperature 303.15 K: an ultrasonic study
A study of densities and volumetric properties of binary mixtures containing nitrobenzene at T = (293.15 to 353.15) K
Excess Molar Volumes of (propiophenone + benzene, or toluene, or ethylbenzene, or butylbenzene) at temperatures 298.15 K and 328.15 K
Activity coefficients at infinite dilution measurements for organic solutes in the ionic liquid 1-butyl-3-methyl-imidazolium 2-(2-methoxyethoxy) ethyl sulfate using g.l.c. at T = (298.15, 303.15, and 308.15) K
Liquid + liquid equilibria for ternary mixtures of (solvent + aromatic hydrocarbon + alkane)
Liquid phase behaviour of 1-hexyloxymethyl-3-methyl-imidazolium-based ionic liquids with hydrocarbons: The influence of anion
Partial molar volume of paracetamol in water, 0.1 M HCl and 0.154 M NaCl at T = (298.15, 303.15, 308.15 and 310.65) K and at 101.325 kPa
The volumetric properties of (1,2-propanediol carbonate + benzene, or toluene, or styrene) binary mixtures at temperatures from T = 293.15 K to T = 353.15 K
(Liquid + liquid) equilibria for ternary mixtures of (methanol or ethanol + toluene or m-xylene + n-dodecane)
Systems with ionic liquids: Measurement of VLE and c1 data and prediction of their thermodynamic behavior using original UNIFAC, mod. UNIFAC(Do) and COSMO-RS(Ol)
Tailor-made ionic liquids
Experimental and predicted volumetric and refractive index properties of ternary mixtures of iodoethane with toluene and alcohols at temperature 298.15 K and pressure 101 kPa
Thermodynamic investigation of N,N-dimethylformamide/toluene binary mixtures in the temperature range from 278.15 to 293.15 K
Excess and deviation properties for the binary mixtures of methylcyclohexane with benzene, toluene, p-xylene, mesitylene, and anisole at T = (298.15, 303.15, and 308.15) K
Excess molar volumes of (propiophenone + toluene) and estimated density of liquid propiophenone below its melting temperature
Excess molar volumes and refractive indices of (methoxybenzene + benzene, or toluene, or o-xylene, or m-xylene, or p-xylene, or mesitylene) binary mixtures between T = (288.15 to 303.15) K
Densities and volumetric properties of N-methyl-2-pyrrolidone with aromatic hydrocarbon at different temperature
Densities and volumes of mixing of the ternary system toluene + butyl acrylate + methyl methacrylate and its binaries at 298.15 K
Thermodynamic properties of binary mixtures of N-methyl-2-pyrrolidinone with cyclohexane, benzene, toluene at (303.15 to 353.15) K and atmospheric pressure
Densities, speeds of sound, and refractive indices of the ternary mixtures (toluene + methyl acetate + butyl acetate) and (toluene + methyl acetate + methyl heptanoate) at 298.15 K
Densities and excess volumes of binary mixtures of N,N-dimethylformamide with aromatic hydrocarbon at different temperature
Solubility data for toluene in various aqueous alkanolamine solutions
Physical properties of (propyl propanoate + hexane + toluene) at 298.15 K
A study on densities and excess volumes in the (c-butyrolactone + aromatic hydrocarbon) system at various temperatures
Phase equilibria of didecyldimethylammonium nitrate ionic liquid with water and organic solvents
Isobaric (vapour + liquid) equilibria data for the binary systems {1,2-dichloroethane (1) + toluene (2)} and {1,2-dichloroethane (1) + acetic acid (2)} at atmospheric pressure
(Liquid + liquid) equilibria of three ternary systems: (heptane + benzene + N-formylmorpholine), (heptane + toluene + N-formylmorpholine), (heptane + xylene + N-formylmorpholine) from T = (298.15 to 353.15) K
(Liquid + liquid) equilibria of ternary and quaternary systems containing n-hexane, toluene, m-xylene, propanol, sulfolane, and water at T = 303.15 K
Measurement of activity coefficients at infinite dilution in 1-hexadecyl-3-methylimidazolium tetrafluoroborate ionic liquid
Temperature influence on mixing properties of {ethyl tert-butyl ether (ETBE) + gasoline additives}
Excess molar volumes of (octane + benzene, or toluene, or 1,3-xylene, or 1,3,5-trimethylbenzene) at temperatures between (298.15 and 328.15) K
Densities, viscosities, and excess properties of (N-methylmorpholine + cyclohexane, + benzene, and + toluene) at T = (298.15, 303.15, 313.15, 323.15) K
Measurements of activity coefficients at infinite dilution of aromatic and aliphatic hydrocarbons, alcohols, and water in the new ionic liquid [EMIM][SCN] using GLC
Development of a Henry s constant correlation and solubility measurements of n-pentane, i-pentane, cyclopentane, n-hexane, and toluene in water
(Liquid + liquid) equilibria for ternary mixtures of (ethylene glycol + toluene + n-octane)
Densities and volumetric properties of (N-acetylmorpholine + aromatic hydrocarbon) binary mixtures from T = (293.15 to 343.15) K
Activity coefficients at infinite dilution of hydrocarbons, alkylbenzenes, and alcohols in the paramagnetic ionic liquid 1-butyl-3-methyl-imidazolium tetrachloridoferrate(III) using gas liquid chromatography
Thermodynamics of fuels with a bio-synthetic component (IV): (Vapor + liquid) equilibrium data for the ternary mixture (ethyl 1,1-dimethylethyl ether + 1-hexene + toluene) at T = 313.15 K
Experimental and theoretical study of surface tension of binary mixtures of (n-alkyl acetates + heptane, benzene, and toluene)
Thermodynamics of biofuels: Excess enthalpies for binary mixtures involving ethyl 1,1-dimethylethyl ether and hydrocarbons at different temperatures using a new flow calorimeter
Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid triethylsulphonium bis(trifluoromethylsulfonyl)imide
Measurements of activity coefficients at infinite dilution of aliphatic and aromatic hydrocarbons, alcohols, thiophene, tetrahydrofuran, MTBE, and water in ionic liquid [BMIM][SCN] using GLC
Automated densimetric system: Measurements and uncertainties for compressed fluids
Volumetric behaviour of binary liquid systems composed of toluene, isooctane, and methyl tert-butyl ether at temperatures from (298.15 to 328.15) K
Experimental densities, refractive indices, and speeds of sound of 12 binary mixtures containing alkanes and aromatic compounds at T = 313.15 K
Volumetric properties of binary liquid mixtures: Application of the Prigogine Flory Patterson theory to excess molar volumes of dichloromethane with benzene or toluene
Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 4-methyl-N-butyl-pyridinium bis(trifluoromethylsulfonyl)-imide
Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-ethyl-3-methylimidazolium trifluoromethanesulfonate using gas liquid chromatography at T = (313.15, 323.15, and 333.15) K
Temperature and pressure dependences of volumetric properties of two poly(propylene glycol) dimethyl ether lubricants
(Liquid + liquid) equilibria in the binary systems (aliphatic, or aromatic hydrocarbons + 1-ethyl-3-methylimidazolium ethylsulfate, or 1-butyl-3-methylimidazolium methylsulfate ionic liquids)
Activity coefficients at infinite dilution for solutes in the trioctylmethylammonium bis(trifluoromethylsulfonyl)imide ionic liquid using gas liquid chromatography
(Liquid + liquid) equilibria for ternary mixtures of (water + propionic acid + organic solvent) at T = 303.2 K
(Liquid + liquid) equilibria of (heptane, or hexane, or cyclohexane + toluene + 1,3- dimethyl-2-imidazolidinone) ternary systems at T = 298.15 K
Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-octyl-3-methylimidazolium hexafluorophosphate using gas liquid chromatography at T = (313.15, 323.15, and 333.15) K
Excess parameter studies on the binary mixtures of toluene with ketones at different temperatures
Gas liquid chromatography measurements of activity coefficients at infinite dilution of various organic solutes and water in tri-iso-butylmethylphosphonium tosylate ionic liquid
Evaluation of the polysubstituted pyridinium ionic liquid [hmmpy][Ntf2] as a suitable solvent for desulfurization: Phase equilibria
Thermochemistry of ionic liquid-catalysed reactions. Isomerisation and transalkylation of tert-alkyl-benzenes. Are these systems ideal?
Separation of toluene from alkanes using 1-ethyl-3-methylpyridinium ethylsulfate ionic liquid at T = 298.15 K and atmospheric pressure
Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate [EMIM][TCB] using gas liquid chromatography
Volumetric behaviour of the ternary liquid system composed of methyl tert-butyl ether, toluene, and isooctane at temperatures from (298.15 to 328.15) K: Experimental data and correlation
Separation of toluene and heptane by liquid liquid extraction using z-methyl-N-butylpyridinium tetrafluoroborate isomers (z = 2, 3, or 4) at T = 313.2 K
Separation of aromatic hydrocarbons (toluene or benzene) from aliphatic hydrocarbon (n-heptane) by extraction with ethylene carbonate
Measurements of activity coefficients at infinite dilution of organic solutes and water in 1-propyl-1-methylpiperidinium bis{(trifluoromethyl)sulfonyl}imide ionic liquid using g.l.c.
Activity coefficients at infinite dilution of organic solutes in N-alkylpyridinium bis(trifluoromethylsulfonyl)imide ([CnPY][NTf2], n = 2, 4, 5) using gas liquid chromatography
Excess molar volumes, excess molar enthalpies, and excess isentropic compressibilities of tetrahydropyran with aromatic hydrocarbons
Measurement and correlation of the (p, rho, T) relation of liquid cyclohexane, toluene, and ethanol in the temperature range from 233.15 K to 473.15 K at pressures up to 30 MPa for use as density reference liquids
Measurements of activity coefficients at infinite dilution of organic compounds and water in isoquinolinium-based ionic liquid [C8iQuin][NTf2] using GLC
Extraction of toluene from aliphatic compounds using an ionic liquid as solvent: Influence of the alkane on the (liquid + liquid) equilibrium
Activity coefficients at infinite dilution of organic solutes in the ionic liquid trihexyl(tetradecyl)phosphonium tetrafluoroborate using gas liquid chromatography at T = (313.15, 333.15, 353.15, and 373.15) K
Separation of toluene from cyclic hydrocarbons using 1-butyl-3-methylimidazolium methylsulfate ionic liquid at T = 298.15 K and atmospheric pressure
Thermodynamic and topological investigations of molecular interactions in binary and ternary mixtures containing 1-methyl pyrrolidin-2-one at T = 308.15 K
Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-butyl-3-methylimidazolium hexafluoroantimonate using gas liquid chromatography at T = (313.15, 323.15, and 333.15) K
Activity coefficients at infinite dilution of organic solutes in the ionic liquid, methyl(trioctyl)ammonium thiosalicylate, [N1888][TS] by gas liquid chromatography at T = (303.15, 313.15, and 323.15) K
Thermophysical properties and phase equilibria study of the binary systems {N-hexylquinolinium bis(trifluoromethylsulfonyl)imide + aromatic hydrocarbons, or an alcohol}
Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate
Densities, viscosities, speed of sound, and IR spectroscopic studies of binary mixtures of tert-butyl acetate with benzene, methylbenzene, and ethylbenzene at T = (298.15 and 308.15) K
Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(3-hydroxypropyl)pyridinium bis(trifluoromethylsulfonyl)-amide
(Liquid + liquid) equilibrium for ternary mixtures of {heptane + aromatic compounds + [EMpy][ESO4]} at T = 298.15 K
Physical properties of 3-methyl-N-butylpyridinium tetracyanoborate and 1-butyl-1-methylpyrrolidinium tetracyanoborate and ternary LLE data of [3-mebupy]B(CN)4 with an aromatic and an aliphatic hydrocarbon at T = 303.2 K and 328.2 K and p = 0.1 MPa
(Liquid + liquid) equilibrium for the ternary systems {heptane + toluene + 1-allyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide} and {heptane + toluene + 1-methyl-3-propylimidazolium bis(trifluoromethylsulfonyl)imide} ionic liquids
Binary and ternary (liquid + liquid) equilibrium for {methylcyclohexane (1) + toluene (2) + 1-hexyl-3-methylimidazolium tetracyanoborate (3)/1-butyl-3-methylimidazolium tetracyanoborate (3)}
Thermodynamics and activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium tetracyanoborate
Isobaric (vapour + liquid) equilibria for sulfolane with toluene, ethylbenzene, and isopropylbenzene at 101.33 kPa
Thermodynamic properties of biofuels: Heat capacities of binary mixtures containing ethanol and hydrocarbons up to 20 MPa and the pure compounds using a new flow calorimeter
Volumetric behaviour of binary and ternary liquid systems composed of ethanol, isooctane, and toluene at temperatures from (298.15 to 328.15) K. Experimental data and correlation
Alkylsulfate-based ionic liquids in the liquid-liquid extraction of aromatic hydrocarbons
Interactions of volatile organic compounds with the ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate
Volumetric properties of binary mixtures of tributylamine with benzene derivatives and comparison with ERAS model results at temperatures from (293.15 to 333.15) K
Solubilities of some organic solutes in 1-ethyl-3-methylimidazolium acetate. Chromatographic measurements and predictions from COSMO-RS
Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(2-methoxyethyl)-4-methylmorpholinium bis(trifluoromethylsulfonyl)-amide
Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-hexyl-3-methylimidazolium tetracyanoborate
(Liquid + liquid) equilibria for the ternary mixtures (alkane + toluene + ionic liquid) at T = 298.15 K: Influence of the anion on the phase equilibria
Tar removal from biosyngas in the biomass gasification process. (Liquid + liquid) equilibrium {water + solvent (paraxylene and methyl hexadecanoate) + model molecules of tar (benzene, toluene, phenol)}
Activity coefficients at infinite dilution of organic solutes in the ionic liquid trihexyltetradecylphosphonium hexafluorophosphate using gas liquid chromatography at T = (313.15, 333.15, 353.15, and 363.15) K
Determination of infinite dilution activity coefficients using HS-SPME/GC/FID for hydrocarbons in furfural at temperatures of (298.15, 308.15, and 318.15) K
Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)-1-methylpiperidinium bis(trifluoromethylsulfonyl)-amide
The potential of head-space gas chromatography for VLE measurements
Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-ethyl-3-methylimidazolium methanesulfonate
Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)-1-methylpyrrolidinium bis(trifluoromethylsulfonyl)-amide
Application of [HMim][NTf2], [HMim][TfO] and [BMim][TfO] ionic liquids on the extraction of toluene from alkanes: Effect of the anion and the alkyl chain length of the cation on the LLE
Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(2-methoxyethyl)-4-methylmorpholinium trifluorotris(perfluoroethyl)phosphate
Measurement and correlation of the solubility of 2,3,4,5-tetrabromothiophene in different solvents
Activity coefficient at infinite dilution measurements for organic solutes (polar and non-polar) in fatty compounds: Saturated fatty acids
Thermodynamics of mixtures containing amines. XI. Liquid + liquid equilibria and molar excess enthalpies at 298.15 K for N-methylaniline + hydrocarbon systems. Characterization in terms of DISQUAC and ERAS models
Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)- 1-methylpiperidinium trifluorotris(perfluoroethyl)phosphate
(Liquid + liquid) equilibria for the ternary (water + acetic acid + toluene) system at different temperatures: Experimental data and correlation
Henry s constants and activity coefficients of some organic solutes in 1-butyl,3-methylimidazolium hydrogen sulfate and in 1-methyl,3-trimethylsilylmethylimidazolium chloride
(Liquid + liquid) equilibria of aqueous solutions of butyric acid with n-heptane and toluene at T = (298.2, 308.2, and 318.2) K
Desulfurization of fuel-oils with [C2mim][NTf2]: A comparative study
Advanced calibration, adjustment, and operation of a density and sound speed analyzer
Interactions of volatile organic compounds with the ionic liquids 1-butyl-1-methylpyrrolidinium tetracyanoborate and 1-butyl-1-methylpyrrolidinium bis(oxalato)borate
Physicochemical properties and activity coefficients at infinite dilution for organic solutes and water in a novel bicyclic guanidinium superbase-derived protic ionic liquid
Activity coefficient at infinite dilution measurements for organic solutes (polar and non-polar) in fatty compounds Part II: C18 fatty acids
Liquid liquid equilibria for ternary systems of (ethylene glycol + toluene + heptane) at temperatures (303.15, 308.15, and 313.15) K and atmospheric pressure: Experimental results and correlation with UNIQUAC and NRTL models
Experimental and theoretical study on infinite dilution activity coefficients of various solutes in piperidinium ionic liquids
Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)- 1-methylpyrrolidinium trifluorotris(perfluoroethyl)phosphate
Measurements of activity coefficients at infinite dilution for organic solutes and water in N-hexylisoquinolinium thiocyanate, [HiQuin][SCN] using GLC
Activity coefficients at infinite dilution of organic solutes in N-formylmorpholine and N-methylpyrrolidone from gas-liquid chromatography
Interface adsorption and micelle formation of ionic liquid 1-hexyl-3-methylimidazolium chloride in the toluene + water system
Viscosity measurements for 2,3,3,3-tetrafluoroprop-1-ene (R1234yf) and trans-1,3,3,3-tetrafluoropropene (R1234ze(E))
Phase equilibria study of the (N-octylisoquinolinium thiocyanate ionic liquid + aliphatic and aromatic hydrocarbon, or thiophene) binary systems
Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-hydroxyethyl)- 3-methylimidazolium trifluorotris(perfluoroethyl)phosphate
Volumetric behaviour of the (2,2,4-trimethylpentane + methylbenzene + butan-1-ol) ternary system and its binary sub-systems within the temperature range (298.15-328.15) K
Activity coefficients at infinite dilution of organic solutes in diethylene glycol and triethylene glycol from gas-liquid chromatography
Activity coefficients at infinite dilution of organic solutes in the ionic liquid trihexyltetradecylphosphonium bis(trifluoromethylsulfonyl)imide using gas-liquid chromatography at T = (313.15, 333.15, 353.15 and 373.15) K
Infinite dilution activity coefficients of volatile organic compounds in two ionic liquids composed of the tris(pentafluoroethyl) trifluorophosphate ([FAP]) anion and a functionalized cation
Thermodynamics of fenoxycarb in solution
Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium tricyanomethanide
Evaluation of ionic liquids as solvent for aromatic extraction: Experimental, correlation and COSMO-RS predictions
Thermodynamics and activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-butyl-1-methylmorpholinium tricyanomethanide
The study of activity coefficients at infinite dilution for organic solutes and water in 1-butyl-4-methylpyridinium dicyanamide, [B4MPy][DCA] using GLC
Measurement of activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-ethyl-3-methylimidazolium 2-(2-methoxyethoxy) ethylsulfate at T = (308.15, 313.15, 323.15 and 333.15) K using gas + liquid chromatography
Measurement of activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-hexyl-1,4-diaza[2.2.2]bicyclooctanium bis(trifluoromethylsulfonyl)imide using gas-liquid chromatography
Activity coefficients at infinite dilution of organic solutes in 1-hexyl-3- methylimidazolium trifluoroacetate and influence of interfacial adsorption using gas liquid chromatography
Selective extraction of toluene from n-heptane using [emim][SCN] and [bmim][SCN] ionic liquids as solvents
Phase behavior of ternary mixtures {aliphatic hydrocarbon + aromatic hydrocarbon + ionic liquid}: Experimental LLE data and their modeling by COSMO-RS
(Liquid + liquid) equilibrium at T = 298.15 K for ternary mixtures of alkane + aromatic compounds + imidazolium-based ionic liquids
The impact of uni-univalent electrolytes on (water + acetic acid + toluene) equilibria: Representation with electrolyte-NRTL model
Quaternary (liquid + liquid) equilibrium data for the extraction of toluene from alkanes using the ionic liquid [EMim][MSO4]
Application of 1-pentyl-3-methylimidazolium bis(trifluoromethylsulfonyl) imide for desulfurization, denitrification and dearomatization of FCC gasoline
Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-butyl-3-methylimidazolium methyl sulfate
Thermodynamics and activity coefficients at infinite dilution for organic solutes, water and diols in the ionic liquid choline bis(trifluoromethylsulfonyl)imide
Thermodynamics of solvation in propylene glycol and methyl cellosolve
Measurement and correlation of solubility of 4-chloro-2,5-dimethoxynitrobenzene and 4-chloro-2,5- dimethoxyaniline in methanol, ethanol, xylene and toluene
Phase equilibria study of binary systems comprising an (ionic liquid + hydrocarbon)
Solvation parameter model and thermodynamic parameters in a dicationic ionic liquid based on pyrrolidinium
Experimental and theoretically study of interaction between organic compounds and tricyanomethanide based ionic liquids
Phase equilibrium measurements of (methane + benzene) and (methane + methylbenzene) at temperatures from (188 to 348) K and pressures to 13 MPa
Excess enthalpies of ternary mixtures of (oxygenated additives + aromatic hydrocarbon) mixtures in fuels and bio-fuels: (Dibutyl-ether + 1-propanol + benzene), or toluene, at T = (298.15 and 313.15) K
Activity coefficients at infinite dilution of organic solutes in methylphosphonate based ionic liquids using gas-liquid chromatography
Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(3-hydroxypropyl)-4-methylmorpholinium bis(trifluoromethylsulfonyl)-amide
Activity coefficients at infinite dilution for organic solutes and water in 1-ethyl-1-methylpyrrolidinium lactate
Activity coefficients at infinite dilution, physicochemical and thermodynamic properties for organic solutes and water in the ionic liquid ethyl-dimethyl-(2-methoxyethyl)ammonium trifluorotris-(perfluoroethyl)phosphate
Measurement and correlation of the solubility of 3,4-bis(3-nitrofurazan-4-yl)furoxan (DNTF) in different solvents
Measurements and equation-of-state modelling of thermodynamic properties of binary mixtures of 1-butyl-1-methylpyrrolidinium tetracyanoborate ionic liquid with molecular compounds
Volumetric behavior of the ternary system (methyl tert-butyl ether + methylbenzene + butan-1-ol) and its binary sub-system (methyl tert-butyl ether + butan-1-ol) within the temperature range (298.15 to 328.15) K
(Vapour + liquid) equilibria, (VLE) excess molar enthalpies and infinite dilution activity coefficients of selected binary systems involving n-hexyl pyridinium bis(trifluoromethylsulphonyl)imide ionic liquid: Experimental and predictions using modified UNIFAC (Dortmund)
Solubility measurement and modelling of 1,8-dinitronaphthalene in nine organic solvents from T = (273.15 to 308.15) K and mixing properties of solutions
Use of selective ionic liquids and ionic liquid/salt mixtures as entrainer in a (vapor + liquid) system to separate n-heptane from toluene
Activity coefficients at infinite dilution of alkanes, alkenes, alkyl benzenes in dimethylphosphate based ionic liquids using gas liquid chromatography
Screening of environmental friendly ionic liquid as a solvent for the different types of separations problem: Insight from activity coefficients at infinite dilution measurement using (gas + liquid) chromatography technique
Ultrasonic and 31P NMR investigations of an acidic nuclear extractant with some monosubstituted benzenes
Solubility determination and correlation for 1,8-dinitronaphthalene in (acetone + methanol), (toluene + methanol) and (acetonitrile + methanol) mixed solvents
(Liquid + liquid) equilibrium of ternary and quaternary systems containing heptane, cyclohexane, toluene and the ionic liquid [EMim][N(CN)2]. Experimental data and correlation
Solubility modelling and thermodynamic dissolution functions of phthalimide in ten organic solvents
Solubility and solution thermodynamics of ethyl 5-amino-4-cyano-3-(2-ethoxy-2-oxoethyl)-2-thiophenecarboxylate in nine organic solvents at evaluated temperatures
Contributing to accurate high pressure viscosity measurements: Vibrating wire viscometer and falling body viscometer techniques
Selective recovery of aliphatics from aromatics in the presence of the {[4empy][Tf2N] + [emim][DCA]} ionic liquid mixture
A 1-alkylcyanopyridinium-based ionic liquid in the separation processes
Determination and thermodynamic modeling of solid-liquid phase equilibrium for 3,5-dichloroaniline in pure solvents and ternary 3,5-dichloroaniline + 1,3,5-trichlorobenzene + toluene system
Solubility determination and thermodynamic dissolution functions of 1,3-diphenylguanidine in nine organic solvents at evaluated temperatures
Measurement and correlation of solubility of pronamide in five organic solvents at (278.15-323.15) K
Solubility determination and thermodynamic modeling of 5-nitro-8- hydroxyquinoline in ten organic solvents from T = (278.15 to 313.15) K and mixing properties of solutions
Solubility and solution thermodynamics of 2-methyl-6-nitroaniline in ten organic solvents at elevated temperatures
Solubility determination and thermodynamic models for dehydroepiandrosterone acetate in mixed solvents of (ethyl acetate + methanol), (ethyl acetate + ethanol) and (ethyl acetate + isopropanol)
Thermodynamics and selectivity of separation based on activity coefficients at infinite dilution of various solutes in 1-allyl-3-methylimidazolium bis{(trifluoromethyl)sulfonyl}imide ionic liquid
Solubility determination and thermodynamic modeling of 2,4-dinitroaniline in nine organic solvents from T = (278.15 to 318.15) K and mixing properties of solutions
Separation of aliphatic from aromatic hydrocarbons and sulphur compounds from fuel based on measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid N,N-diethyl-N-methyl-N-(2-methoxy-ethyl)ammonium bis(trifluoromethylsulfonyl)imide
Thermodynamics and activity coefficients at infinite dilution for organic solutes in the ionic liquid 1-hexyl-2,3-dimethylimidazolium bis(trifluoromethylsulfonyl)imide
Solubility determination and thermodynamic modeling of 3-methyl-4- nitrobenzoic acid in twelve organic solvents from T = (283.15-318.15) K and mixing properties of solutions
Liquid-liquid extraction of toluene from alkane with pyridinium based ionic liquid ([BPy][NO3] and [HPy][NO3]) at 298.15 K and atmospheric pressure
Heat capacities of aqueous binary and ternary mixtures (with piperazine) of N-(2-aminoethyl)-piperazine and N,N,N'-trimethylethylenediamine at temperatures (303.2-353.2) K
Solubility determination and thermodynamic modelling of 2,4-dihydro-5-methyl-2-(4-methylphenyl)-3H-pyrazol-3-one in twelve organic solvents from T = (278.15 to 313.15) K and mixing properties of solutions
Thermodynamics and limiting activity coefficients measurements for organic solutes and water in the ionic liquid 1-dodecyl-3-methylimidzolium bis(trifluoromethylsulfonyl) imide
Solubility of N-phenylanthranilic acid in nine organic solvents from T = (283.15 to 318.15) K: Determination and modelling
Thermodynamic modelling for solubility of 4-nitrobenzaldehyde in different solvents at temperature range from (273.15 to 313.15) K and mixing properties of solutions
Fully automatized apparatus for determining speed of sound for liquids in the temperature and pressure interval (283.15-343.15) K and (0.1-95) MPa
Solubility determination and thermodynamic modeling of paclobutrazol in nine organic solvents from T = (278.15 to 318.15) K and mixing properties of solutions
Thermodynamic modelling for solubility of 5-chloro-1-methyl-4-nitroimidazole in eleven organic solvents from T = (283.15 to 318.15) K
Measurement and correlation of solubility of ciclesonide in seven pure organic solvents
Thermodynamic study of solubility for 2-amino-4-chloro-6-methoxypyrimidine in twelve organic solvents at temperatures from 273.15 K to 323.15 K
Solubility and solution thermodynamics of 2-methyl-4-nitroaniline in eleven organic solvents at elevated temperatures
Solubility measurement and thermodynamic functions of 3-nitrobenzaldehyde in different solvents at elevated temperatures
Solubility determination and modelling of 4-nitro-1,2-phenylenediamine in eleven organic solvents from T = (283.15 to 318.15) K and thermodynamic properties of solutions
Solubility determination and thermodynamic modelling for 2-amino-4-chlorobenzoic acid in eleven organic solvents from T = (278.15 to 313.15) K and mixing properties of solutions
Solubility and thermodynamic functions of tebuconazole in nine organic solvents from T = (278.15 to 313.15) K and mixing properties of solutions
Solubility of 2-isopropylimidazole in nine pure organic solvents and liquid mixture of (methanol + ethyl acetate) from T = (278.15 to 313.15) K: Experimental measurement and thermodynamic modelling
Solubility of 2-nitro-p-phenylenediamine in nine pure solvents and mixture of (methanol + N-methyl-2-pyrrolidone) from T = (283.15 to 318.15) K: Determination and modelling
Physicochemical study of intermolecular interactions in 1,4-dioxane + aromatic hydrocarbons binary mixtures at different temperatures by using ultrasonic and viscometric methods
Solubility of 4-methyl-2-nitroaniline in fourteen organic solvents from T = (278.15 to 313.15) K and mixing properties of solutions
Solubility determination and thermodynamic modelling of 3,5-dimethylpyrazole in nine organic solvents from T = (283.15 to 313.15) K and mixing properties of solutions
Solubility of commercial octacosanol in organic solvents and their correlation by thermodynamic models at different temperatures
Separation of binary mixtures hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on limiting activity coefficients
Solubility modelling and dissolution properties of 5-phenyltetrazole in thirteen mono-solvents and liquid mixtures of (methanol + ethyl acetate) at elevated temperatures
Thermodynamic functions for solubility of 2-mercaptobenzothiazole in eleven pure organic solvents at temperatures from 273.15 K to 318.15 K and mixing properties of solutions
Thermodynamics and activity coefficients at infinite dilution for organic compounds and water in the ionic liquid 1-butyl-3-methylimidazolium perchlorate
High-temperature, high-pressure viscosities and densities of toluene
Conformational analysis of branched alkanes using limiting partial molar volumes
Liquid-liquid equilibria for toluene/heptane + phenol/cresols + ethylene glycol system
Effect of temperature on intermolecular interactions between the organic solvents: Insights from density and excess volume
Separation of water/butan-1-ol based on activity coefficients at infinite dilution in 1,3-didecyl-2-methylimidazolium dicyanamide ionic liquid
Separation of binary mixtures hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on gamma infinity data measurements
Separation of binary mixtures based on gamma infinity data using [OMMIM][NTf2] ionic liquid and modelling of thermodynamic functions
Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid trihexyl-tetradecyl-phosphonium tricyanomethanide
Thermodynamic study of molecular interaction-selectivity in separation processes based on limiting activity coefficients
Density, sound speed and derived thermophysical properties of n-nonane at temperatures between (283.15 and 473.15)K and at pressures up to 390MPa
Abraham model correlations for describing the thermodynamic properties of solute transfer into pentyl acetate based on headspace chromatographic and solubility measurements
Thermodynamics and selectivity of separation based on activity coefficients at infinite dilution of various solutes in ionic liquid [HMMIM][BF4]
The use of ionic liquids for separation of binary hydrocarbons mixtures based on gamma infinity data measurements
Thermodynamics and activity coefficients at infinite dilution for organic compounds in the ionic liquid 1-hexyl-3-methylimidazolium chloride
Separation of binary mixtures based on gamma infinity data using [OMMIM][BF4] ionic liquid and modelling of thermodynamic functions
Solvent screening and liquid-liquid measurement for extraction of phenols from aromatic hydrocarbon mixtures
Determination of the thermodynamic parameters of ionic liquid 1-propyl-3-methylimidazolium bromide by gas-liquid chromatography
Thermodynamic characterization of binary mixtures of poly(propylene glycol) 425 with toluene and o-, m- and p-xylenes
Ternary phase diagram of phenanthrene and carbazole in different solvents and its application in the separation of them
Solubility parameter of lenalidomide for predicting the type of solubility profile and application of thermodynamic model
Thermal conductivity data for refrigerant mixtures containing R1234yf and R1234ze(E)
Speed of sound and derived thermodynamic properties of para-xylene at temperatures between (306 and 448) K and at pressures up to 66 MPa
Separation of (water/butan-1-ol) binary systems based on activity coefficients at infinite dilution with phosphonium ionic liquid
The dissolution behaviour and apparent thermodynamic analysis of diprophylline in pure and mixed solvents
Co-solvence phenomenon and thermodynamic properties of edaravone in pure and mixed solvents
Volumetric and viscometric studies of molecular interaction of the ternary system toluene (1) + cyclohexane (2) + n-hexane (3) at 298.15K
Molecular interactions in binary mixtures containing o-toluidine
Excess molar volumes and excess isentropic compressibilities of 2-pyrrolidinone at 308.15K
Molecular interaction studies and theoretical estimation of ultrasonic speeds using scaled particle theory in binary mixtures of toluene with homologous nitriles at different temperatures
Excess Molar Enthalpies for Binary and Ternary Mixtures containing Cyclic Ether, 2-Methylaniline and Aromatic Hydrocarbons
Excess molar enthalpies of ternary mixtures containing o-toluidine + tetrahydropyran with pyridine or isomeric picolines or benzene or toluene at 308.15K
Determination of the solubility, dissolution enthalpy and entropy of 3-pentadecylphenyl acrylate in different organic solvents
Solubility in binary solvent mixtures: pyrene dissolved in alcohol + toluene mixtures
Correlation and prediction of the phase behavior and thermal properties of binary and ternary systems of 2,2 -oxybis[propane] + benzene, toluene, cyclohexane or n-heptane
Vapor pressure data of nicotine, anabasine and cotinine using differential scanning calorimetry
Thermogravimetric measurement of evaporation: Data analysis based on the Stefan tube
Volumetric and acoustic properties of binary systems (furfural or furfuryl alcohol + toluene) and (furfuryl alcohol + ethanol) at different temperatures
Application of a DSC based vapor pressure method for examining the extent of ideality in associating binary mixtures with narrow boiling range oil cuts as a mixture component
Experimental measurement and phase equilibria calculation for ternary systems of carbon dioxide+ toluene + naphthalene and carbon dioxide+ ethanol + acridine, applicable for fine particle production in GAS process
Isobaric phase equilibrium of morpholine + 1-decanol, volumetric properties and molar refractivity from 293.15 to 333.15 K of morpholine + 1-decanol and 1-octanol + toluene system with applications of Prigogine-Flory-Patterson theory
Low cost apparatus for rapid boiling point determination of small air sensitive samples under inert atmosphere
A new analysis method for improving collection of vapor-liquid equilibrium (VLE) data of binary mixtures using differential scanning calorimetry (DSC)
Isothermal vapor-liquid equilibrium of binary and ternary systems of anisole, hexane, and toluene and ternary system of methyl tert-butyl ether, hexane, and toluene
Solubilities of Phosphoramidic Acid, N-(phenylmethyl)-, Diphenyl Ester in Selected Solvents
Solid Forms, Crystal Habits, and Solubility of Danthron
Solubility, Thermodynamic Properties, and Derived Excess Properties of Benzoic Acid in (Acetic Acid + Water) and (Acetic Acid + Toluene) Binary Mixtures
Viscous Calibration Liquids for Self-diffusion Measurements
Solubility and Dissolution Thermodynamics for 1,3,5- Trichlorobenzene in Organic Solvents
Mass Diffusion Coefficient and Soret Coefficient of o-Dichlorobenzene Solutions of PCBM and [60]Fullerene by the Soret Forced Rayleigh Scattering Method
Experimental and Computational Study on Liquid Liquid Equilibrium in Ternary Systems of -Valerolactone, Toluene, and Hydrocarbons
Vapor Liquid Equilibria of n-Heptane + Toluene +1-Ethyl-4-methylpyridinium Bis(trifluoromethylsulfonyl)imide Ionic Liquid
Vapor Pressure Measurements for Binary Mixtures Containing Ionic Liquid and Predictions by the Conductor-like Screening Model for Real Solvents
Measurement of Hydrogen Solubility in Potential Liquid Organic Hydrogen Carriers
Density and Viscosity from 293.15 to 373.15 K, Speed of Sound and Bulk Modulus from 293.15 to 343.15 K, Surface Tension, and Flash Point of Binary Mixtures of Bicyclohexyl and 1,2,3,4-Tetrahydronaphthalene or Trans-decahydronaphthalene at 0.1 MPa
Solubility Measurement and Correlation of (+)-Biotin Intermediate Lactone in Different Organic Solvents from (287.15 to 323.75) K
Activity Coefficients at Infinite Dilution of Organic Solutes and Water in Tributylethylphosphonium Diethylphosphate Using Gas Liquid Chromatography: Thermodynamic Properties of Mixtures Containing Ionic Liquids
Solubility Modeling of 4-(Methylsulfonyl)benzaldehyde in Nine Organic Solvents at Elevated Temperatures
Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of 1,2,3,4-Tetrahydronaphthalene and Trans-decahydronaphthalene
Solubilities of Dihydroxylammonium 5,5'-Bistetrazole-1,1'-diolate in Various Pure Solvents at Temperatures Between 293.15 and 323.15 K
Vapor Liquid Equilibria for (n-Hexane, n-Octane, Cyclohexane, or 2,3-Dimethylpentane) + Toluene + {[4empy][Tf2N] (0.3) + [emim][DCA] (0.7)} Mixed Ionic Liquids
Solubility of Mercury in Liquid Hydrocarbons and Hydrocarbon Mixtures
Determination and Correlation of Solubility of 3,4-Dinitro-1H-pyrazole in Different Pure Solvents from 298.15 K to 338.15 K
Solubility Measurement and Thermodynamic Modeling of 4-Nitrophthalimide in Twelve Pure Solvents at Elevated Temperatures Ranging from (273.15 to 323.15) K
Isothermal Vapor Liquid Equilibrium Data for the Toluene + Methanol + N-Butylpyridinium Bromide System
Solubility of 3,7,9,11-Tetraoxo-2,4,6,8,10-pentaaza[3.3.3] Propellane (TOPAP) in Different Pure Solvents at Temperatures between 273.15 and 318.15 K
Thermal Diffusivity of 2-Ethoxy-2-methylpropane (ETBE) and 2-Methoxy-2-methylbutane (TAME) at Temperatures from (293 to 523) K and Pressure up to 10 MPa
Vapor Liquid Equilibrium Data for the Furan-Toluene Binary System between 313.02 and 352.99 K
Liquid Liquid Equilibria for the Ternary Systems Dodecane + Toluene or Thiophene or Pyridine + 1-Ethyl-3-methylimidazolium Methyl Sulfate
Measurement and Modeling of Solid Liquid Equilibrium of para-tert-Butylbenzoic Acid in Acetic Acid/Methanol + Water and Acetic Acid + para-tert-Butyltoluene Binary Systems at Various Temperatures
Liquid-Liquid Equilibrium Measurements for Model Systems Related to Catalytic Fast Pyrolysis of Biomass
Mutual solubility of aromatic hydrocarbons in pyrrolidinium and ammonium-based ionic liquids and its modeling using the Cubic-Plus-Association (CPA) Equation of State
Diffusion Coefficients of Carbon Dioxide in Eight Hydrocarbon Liquids at Temperatures between (298.15 and 423.15) K at Pressures up to 69 MPa
Isobaric Vapor Liquid Equilibrium for Binary and Ternary Systems of Isoamyl Alcohol + Isoamyl Acetate + Dimethyl Sulfoxide at 101.33 kPa
Measurement and Correlation of the Solubility of e-CL-20 in 12 Organic Solvents at Temperatures Ranging from 278.15 to 318.15 K
Solubility Measurement and the Correlation of 1-Naphthaleneacetic Acid in Pure and Methanol + Water Binary Solvents from T = (278.25 to 323.55) K
Isobaric Vapor Liquid Equilibrium for Binary Systems of Cyclohexanone + Benzene, Cyclohexanone + Toluene, and Cyclohexanone + p-Xylene at 101.3 kPa
Measurement and Modeling of Solubility of para-tert-Butylbenzoic Acid in Pure and Mixed Organic Solvents at Different Temperatures
Solvent Polarity Effect when Amberlite-LA2 Is Used in the Extraction of Picric Acid
Liquid Liquid Equilibria of Binary, Ternary, and Quaternary Systems Involving Monoethylene Glycol, Water, Toluene, p-Xylene, Hexane, and Octane
Measurement and Prediction of Vapor Liquid(-Liquid) Equilibria in Ternary Systems Containing Water, an Organic Component, and Cyclohexanol
Vapor Liquid Equilibrium and Excess Enthalpy Data for Systems Containing N,N-Dimethylacetamide
Phase Behavior Data of (CO2 + Toluene + Phenanthrene) and (CO2 + (Methanol + Phenanthrene) Systems at High Pressure
Phase Behavior of the System (Carbon Dioxide + n-Heptane + Methylbenzene): A Comparison between Experimental Data and SAFT-gamma-Mie Predictions
Solid Liquid Phase Equilibrium of N,N'-Piperazinebis(neopentylglycol)phosphoramidate in Selected Solvents from T = (293.15 to 333.15) K
Measurement and Correlation of Isothermal Binary Vapor Liquid Equilibrium for Diethyl Carbonate + Isooctane/n-Heptane/Toluene Systems
Determination of Infinite Dilution Activity Coefficients of Several Organic Solutes in N-Butylpyridinium Nitrate/N-Octylpyridinium Nitrate by Blend Inverse Gas Chromatography
Experimental Determination and Correlation of Liquid Liquid Equilibria for Water + Cyclohexanone + Solvents (Toluene or p-Xylene) Ternary Systems at 303.15 and 323.15 K under 101.3 kPa
Experimental and Modeling Studies on the Solubility of 2-Chloro-N-(4-methylphenyl)propanamide (S1) in Binary Ethyl Acetate + Hexane, Toluene + Hexane, Acetone + Hexane, and Butanone + Hexane Solvent Mixtures Using Polythermal Method
Thermodynamic Functions for Solubility of 1-Hydroxybenzotriazole in Sixteen Solvents at Temperatures from (278.15 to 313.15) K and Mixing Property of Mixtures
Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Selected Ternary Mixtures of n-Butylcyclohexane + a Linear Alkane (n-Hexadcane or n-Dodecane) + an Aromatic Compound (Toluene, n-Butylbenzene, or n-Hexylbenzene)
Liquid-Liquid Equilibrium Data, Density, Viscosity, and Interfacial Tension of Ternary System (Toluene-Acetic Acid-Water) at 298.15 K: Experiment and Correlation
Solubility Modeling and Mixing Thermodynamics of Thiamphenicol in Water and Twelve Neat Organic Solvents from T = (278.15 to 318.15) K
Liquid-Liquid Equilibrium Data and Correlation for the Quaternary Systems Water + Polyphenol (Hydroquinone, Catechol, and Resorcinol) + Methyl Isobutyl Ketone + Methylbenzene
Isothermal Vapor-Liquid Equilibria for Binary Mixtures of Methyl Nonafluorobutyl Ether + Acetone, Cyclopentyl Methyl Ether, Ethyl Acetate, n-Heptane, Methanol, and Toluene
Thermodynamic Functions for the Solubility of 3-Nitrobenzonitrile in 12 Organic Solvents from T/K = (278.15 to 318.15)
Determination and Correlation of Liquid-Liquid Equilibria Data for Water + Cyclohexanol + (Mesityl Oxide, Toluene, and p-Xylene) Ternary Systems at Different Temperatures
Measurement and Correlation of Solubility of Resorcinol Bis(cyclic 2,2-dimethyl-1,3-propanediol phosphate) in Selected Solvents from T = 293.15 to 333.15 K
Measurement and Correlation of the Solubilities of Sulfur S8 in 10 Solvents
Measurement and Prediction of Vapor-Liquid Equilibria in Ternary Systems Containing an Organic Component, Cyclohexylamine, and Cyclohexanol
Solubility Modeling and Mixing Properties for Benzoin in Different Monosolvents and Solvent Mixtures at the Temperature Range from 273.15 to 313.15 K
Separation of Protocatechuic Acid Using Di-(2-ethylhexyl)phosphoric Acid in Isobutyl Acetate, Toluene, and Petroleum Ether
Densities and Dynamic Viscosities of Alicyclic Cyclohexane with Toluene, o-Xylene, and Mesitylene at T = (303.15 to 323.15) K and Atmospheric Pressure
Solubility Measurement and Thermodynamic Modeling of N-(4-Methylphenyl-Z-3-chloro-2-(phenylthio)propenamide in 12 Pure Solvents at Temperatures Ranging from 278.15 to 318.15 K
Aniracetam Solubility in Pure and Binary Solvents: Effect of Molecular Interaction and Analysis of Crystallized Products
Determination of Activity Coefficients at Infinite Dilution of Organic Solutes in the Ionic Liquid 1-(2-Hydroxyethyl)-3-methylimidazolium Nonafluoro-1-butanesulfonate Using Gas-Liquid Chromatography
Isothermal Vapor-Liquid Equilibrium Data for Binary Systems of CHF3 or C2F6 with Methylcyclohexane or Toluene
Bubble Pressure Measurement and Prediction for n-Hexadecane and n-Eicosane + Cyclohexane, Methylcyclohexane, and Ethylcyclohexane Binary Mixtures from 303.15 to 393.15 K
Solubility of 2-Chlorophenylacetic Acid in 12 Pure Solvents from T = (273.15/283.15 to 318.15) K: Determination and Modeling
Computation of Liquid Isothermal Compressibility from Density Measurements: An Application to Toluene
Solid-Liquid Phase Equilibria of the Ternary System (2-Naphthaldehyde + 4-Methylphthalic Anhydride + Ethyl Acetate) at (288.15, 298.15, and 308.15) K
Solubility Measurement and Modeling of 1-(3-nitrophenyl)Ethanone and 1-(4-nitrophenyl)Ethenone in Nine Pure Organic Solvents from T = (278.15 to 318.15) K and Mixing Properties of Solutions
Solubility and Molecular Interactions of Trimetazidine Hydrochloride in 12 Monosolvents and Solvent Mixtures of Methanol + (Ethanol, N,N-Dimethylformamide or Ethyl Acetate)
Solubility Measurement, Modeling, and Thermodynamic Functions for para-Methoxyphenylacetic Acid in Pure and Mixed Organic and Aqueous Systems
Solubility Measurement and Modeling of 2-Amino-4,6-dichoropyrimidine in Ten Pure Solvents and (Ethyl Acetate + Ethanol) Solvent Mixtures
Experiment and Computation of Solubility and Dissolution Properties for Enalapril Maleate and Its Intermediate in Pure Solvents
Solubility Measurement and Correlation for epsilon-2,4,6,8,10,12-Hexanitro-2,4,6,8,10,12-hexaazaisowurtzitane in Different Alkanes/Aromatic Hydrocarbon + Ethyl Acetate Binary Solvents at Temperatures of between 283.15 and 323.15 K
Influence of Different Solvent Properties and Composition for the Solubility of Iopromide
Solubilities of Organic Semiconductors and Nonsteroidal Anti-inflammatory Drugs in Pure and Mixed Organic Solvents: Measurement and Modeling with Hansen Solubility Parameter
Solubility of Toltrazuril and the Effect of a Cosolvent
Activity Coefficients at Infinite Dilution of Various Solutes in Tetrapropylammonium Bromide + 1,6-Hexanediol Deep Eutectic Solvent
Thermodynamic Parameters of a New Synthesized Tricationic Ionic Liquid Stationary Phase by Inverse Gas Chromatography
Solubility of Diflufenican in Pure and Binary Solvent Systems
Determination of Activity Coefficients at Infinite Dilution of Solutes in N,N'-Di(2-ethylhexyl)isobutyramide Using Inverse Gas-Liquid Chromatography
Experimental Measurements and Modeling Study of Liquid-Liquid Equilibrium [(Water + Methyl Oleate + Model Molecules of Tar Issued from the Biomass Gasification Process (Benzene, Toluene, Phenol, Thiophene, and Pyridine)]
Liquid Extraction of Toluene from Heptane, Octane, or Nonane Using Mixed Ionic Solvents of 1-Ethyl-3-methylimidazolium Methylsulfate and 1-Hexyl-3-methylimidazolium Hexafluorophosphate
Solubility Measurement and Thermodynamic Properties of Levetiracetam in Pure and Mixed Solvents
Measurement and Correlation of Solubility of Gatifloxacin in 12 Pure Solvents from 273.15 K to 318.15 K
Solubility Measurement and Thermodynamic Model Correlation and Evaluation of 2-Chloro-5-nitroaniline in 12 Pure Solvents
Experiment and Application of the Solid-Liquid Phase Equilibrium for Ternary 2-Nitro-p-phenylenediamine + Ethyl Acetate + Isopropanol and 2-Nitro-p-phenylenediamine + 4-Nitro-o-phenylenediamine + N-Methyl-2-pyrrolidone systems
Solubility of N-tert-Butylbenzothiazole-2-sulfenamide in Several Pure and Binary Solvents
Effect of Solvent Properties and Composition on the Solubility of Ganciclovir Form I
Solubility Determination and Thermodynamic Modeling of Buprofezin in Different Solvents and Mixing Properties of Solutions
Solubility in Different Solvents, Correlation, and Solvent Effect in the Solvent Crystallization Process of Iohexol
Binary Solid-Liquid Solubility Determination and Model Correlation of Quizalofop-p-ethyl in Different Pure Solvents
Solid-Liquid Equilibrium of Azacyclotridecan-2-one in 15 Pure Solvents from T = 273.15 to 323.15 K: Experimental Determination and Thermodynamic Modeling
Solubility Determination of 1,5-Naphthalenediamine and 1,8-Naphthalenediamine in Different Solvents and Mixing Properties of Solutions
Solubility, Model Correlation, and Solvent Effect of 2-Amino-3-methylbenzoic Acid in 12 Pure Solvents
Solubility and Solution Thermodynamics of 3-Nitrophthalonitrile in 12 Neat Solvents at Temperatures from 278.15 to 323.15 K
Experimental Determination and Modeling of Liquid-Liquid Equilibrium for Ternary Mixtures of Ethylene Glycol + 1,2-Butanediol + 3-Heptanone or Anisole
Solid-Liquid Equilibrium of 5-Chloro-8-hydroxyquinoline and 5,7-Dichloro-8-hydroxyquinoline in Different Solvents and Mixing Properties of Solutions
Parametric Analysis of Mandelic Acid Separation from Aqueous Solutions by Using Secondary Amine Mixture (Amberlite LA-2) in Various Diluents
Measuring Activity Coefficient at Infinite Dilution of Hydrocarbons in Ionic Liquids and Evaluation of Other Thermodynamic Properties using Gas Chromatography
Solubility Determination and Thermodynamic Modeling of 2-Mercaptobenzimidazole in 12 Solvents from T = 278.15 K to T = 318.15 K
Reactive Extraction of Gallic Acid Using Tributyl Phosphate in Different Classes of Diluents
Solubility Measurement and Thermodynamic Model Correlation of 5-Nitrosalicylaldehyde in Different Solvents
o-Nitrophenylacetonitrile Solubility in Several Pure Solvents: Measurement, Correlation, and Solvent Effect Analysis
Solubility of Gastrodin in Pure and Mixed Solvents at 273.15-313.15 K and Its Correlation with Different Thermodynamic Models
Solubility Measurement and Correlation of 2-Oxindole in 12 Pure Organic Solvents
Assessment of Pyrrolidinium-Based Ionic Liquid for the Separation of Binary Mixtures Based on Activity Coefficients at Infinite Dilution
Measurement of the Solubility of Diclazuril and Discussion of the Effect of the Cosolvent
Ternary Liquid-Liquid Equilibrium of Toluene + Dimethyl Carbonate + ILs at 298.15 K and Atmospheric Pressure
Determination and Correlation of Solubilities of 1,3,5-Trifluoro-2,4,6-triiodobenzene in Different Solvents from 289.25 to 332.15 K
Solubility Determination, Correlation, and Solute-Solvent Molecular Interactions of 5-Aminotetrazole in Various Pure Solvents
Solubility Determination and Thermodynamic Mixing Properties of 5-Methyl-2-pyrazinecarboxylic Acid in Different Solvents
Solubility and Thermodynamic Modeling of Sulfanilamide in 12 Mono Solvents and 4 Binary Solvent Mixtures from 278.15 to 318.15 K
Solubility, Solubility Modeling, and Antisolvent Precipitation of 1,3-Bis(9-carbazolyl)benzene in Organic Solvents
Binary Equilibrium Solubility of Amidinothiourea in Monosolvents: Experimental Determination, Model Correlation, and Solvent Effect Analysis
Measurement and Correlation of Solubility of Marbofloxacin in 12 Pure Solvents from 283.15 to 328.15 K
Solubility Study and Mixing Property of 3,5-Dinitro-2-methylbenzoic Acid in 13 Pure Solvents from 288.15 to 333.15 K
Experimental and Correlated Liquid-Liquid Equilibrium Data for Ternary Systems (Water + Poly(oxymethylene) Dimethyl Ethers + Toluene) at T = 293.15 and 303.15 K and p = 101.3 kPa
Solubility Increment and Thermodynamic Analysis of Bioactive Antofloxacin Hydrochloride in Aqueous ChCl/PTS Deep Eutectic Solvent and Cosolvent Mixtures
Infinite Dilution Activity Coefficients in Ethylene Glycol and Ethylene Carbonate
Liquid-liquid equilibria for mixtures of (Furfural + an Aromatic hydrocarbon + an alkane) at T=298.15 K
Heat Capacities of alpha,omega-Dichloroalkanes at Temperatures from 284.15 K to 353.15 K and a Group Additivity Analysis
Thermodynamic Properties of Mixtures Containing Precursors of Vitamin B5
Surface Tension of Pure Liquids and Binary Liquid Mixtures
Solubility of 1-Alkyl-3-methylimidazolium Hexafluorophosphate in Hydrocarbons
Thermodynamics of Ternary Liquid Mixtures Containing Toluene, Ethylbenzene, and Chlorobenzene
Infinite Dilution Activity Coefficients of Hydrocarbons in Triethylene Glycol and Tetraethylene Glycol
Determination of Isobaric Thermal Expansivity of Organic Compounds from 0.1 to 30 MPa at 30 C with an Isothermal Pressure Scanning Microcalorimeter
Solubility of -Carotene in Binary Solvents Formed by Some Hydrocarbons with Dibutyl Ether and 1,2-Dimethoxyethane
Isobaric Vapor-Liquid Equilibria of the Ternary System Toluene + Ethylbenzene + Amyl Acetate
Densities, Excess Molar Volumes, Viscosities, Speeds of Sound, Excess Isentropic Compressibilities, and Relative Permittivities for CmH2m+1(OCH2CH2)nOH (m ) 1 or 2 or 4 andn ) 1) + Benzene, + Toluene, + (o-, m-, and p-) Xylenes, + Ethylbenzene, and + Cyclohexane
Densities, Excess Molar Volumes at T = (298.15 to 313.15) K, Speeds of Sound, Excess Isentropic Compressibilities, Relative Permittivities and Deviations in Molar Polarizations at T = (298.15 and 308.15) K for Methyl Methacrylate + 2-Butoxyethanol or + Dibutyl Ether + Benzene, + Toluene and + p-Xylene
Liquid-Liquid Equilibria for Binary Mixtures of Water + Benzene, + Toluene, and + p-Xylene from 273 K to 458 K
Surface Tension and Interfacial Tension of Binary Organic Liquid Mixtures
Excess Molar Volumes and Viscosities of Binary Mixtures of Sulfolane with Benzene, Toluene, Ethylbenzene, p-Xylene, o-Xylene, and m-Xylene at 303.15 and 323.15 K and Atmospheric Pressure
Densities and Viscosities of Binary Liquid Mixtures of Trichloroethylene and Tetrachloroethylene with Some Polar and Nonpolar Solvents
Density, Viscosity, and Excess Properties of Binary Liquid Mixtures of Propylene Carbonate with Polar and Nonpolar Solvents
Pressure-Density-Temperature Behavior of CO2/Acetone, CO2/Toluene, and CO2/Monochlorobenzene Mixtures in the Near-Critical Region
Density and Viscosity Studies of Binary Mixtures of N,N-Dimethylformamide with Toluene and Methyl Benzoate at (298.15, 303.15, 308.15, and 313.15) K
Solubility of a-Carotene in Binary Solvents Formed by Some Hydrocarbons with tert-Butyl Methyl Ether and with tert-Amyl Methyl Ether
Vibrating Wire Viscometer with Wire Diameters of (0.05 and 0.15) mm: Results for Methylbenzene and Two Fluids with Nominal Viscosities at T = 298 K and p = 0.01 MPa of (14 and 232) mPa*s at Temperatures between (298 and 373) K and Pressures below 40 MPa
Liquid-Liquid Equilibrium for the Quaternary System Toluene + Water + Propionic Acid + Ethyl Acetate at 25 deg C and Atmospheric Pressure
Experimental Dynamic Viscosities of 2,3-Dimethylpentane up to 60 MPa and from (303.15 to 353.15) K Using a Rolling-Ball Viscometer
Density Measurements under Pressure for the Binary System 1-Propanol + Toluene
Measurement of Diffusion Coefficients in Thermodynamically Nonideal Systems
Thermal Conductivity of Some Oxygenated Fuels and Additives in the Saturated Liquid Phase
Quaternary Liquid-Liquid Equilibrium of Water + Acetic Acid + Propionic Acid + Solvent (Amyl Alcohol, Cyclohexyl Acetate, or Toluene) Systems
High-Pressure Vapor-Liquid Equilbria of Some Carbon Dioxide + Organic Binary Systems
Vapor-Liquid Equilibrium Measurements of MTBE and TAME with Toluene
Measurement of Activity Coefficients at Infinite Dilution of Benzene, Toluene, Ethanol, Esters, Ketones, and Ethers at Various Temperatures in Water Using the Dilutor Technique
Vapor-Liquid Equilibrium and Density of the Binary System 1-Phenylethylamine + Toluene
Solubility of Imidazoles, Benzimidazoles, and Phenylimidazoles in Dichloromethane, 1-Chlorobutane, Toluene, and 2-Nitrotoluene
Surface and interfacial tension of the ternary system heptane + toluene + N,N-dimethylformamide
Determination of Activity Coefficients at Infinite Dilution of Solutes in the Ionic Liquid 1-Butyl-3-methylimidazolium Octyl Sulfate Using Gas-Liquid Chromatography at a Temperature of 298.15 K, 313.15 K, or 328.15 K
Viscosities and Excess Molar Volumes of the Ternary System Toluene (1) + Cyclohexane (2) + Pentane (3) at 298.15 K
Apparatus for the Determination of Water Solubility in Hydrocarbon: Toluene and Alkylcyclohexanes (C6 to C8) from 30 C to 180 C
Isobaric Vapor-Liquid Equilibria for Binary Mixtures of 1,2-Dibromoethane with Benzene, Toluene, Fluorobenzene, and Bromobenzene at Atmospheric Pressure
Mutual Solubilities of Terpene in Methanol and Water and Their Multicomponent Liquid-Liquid Equilibria
Densities, Viscosities, and Refractive Indices of Binary Mixtures of Anisole with Benzene, Methylbenzene, Ethylbenzene, Propylbenzene, and Butylbenzene at (293.15 and 303.15) K
Activity Coefficients at Infinite Dilution of Cylcohexylamine + Octane, Toluene, Ethylbenzene, or Aniline and Excess Molar Volumes in Binary Mixtures of Cyclohexylamine + Heptane, Octane, Nonane, Decane, Undecane, Aniline, or Water
A Vibrating Edge Supported Plate, Fabricated by the Methods of Micro Electro Mechanical System for the Simultaneous Measurement of Density and Viscosity: Results for Methylbenzene and Octane at Temperatures between (323 and 423) K and Pressures in the Range (0.1 to 68) MPa
Thermodynamic Properties of Mixtures Containing Ionic Liquids. 8. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in 1-Hexyl-3-methylimidazolium Bis(trifluoromethylsulfonyl) Imide Using Gas-Liquid Chromatography
Densities and Viscosities of Diethyl Carbonate + Toluene, + Methanol, and + 2-Propanol from (293.15 to 363.15) K
Thermodynamic Properties of Mixtures Containing Ionic Liquids. 9. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in Trimethyl-butylammonium Bis(trifluoromethylsulfonyl) Imide Using Gas-Liquid Chromatography and Static Method
Liquid-Liquid Equilibria for Binary and Ternary Systems Containing Glycols, Aromatic Hydrocarbons, and Water: Experimental Measurements and Modeling with the CPA EoS
Solubilities of 2-(6-Oxido-6H-dibenz[c,e][1,2]oxaphosphorin-6-yl)-methanol in the Selected Solvents
Determination and Study of the Solubility of Methane in Mixtures of Methanol plus Various Hydrocarbons at High Pressures
Liquid-Liquid(-Liquid) Equilibria in Ternary Systems of Water + Cyclohexylamine + Aromatic Hydrocarbon (Toluene or Propylbenzene) or Aliphatic Hydrocarbon (Heptane or Octane)
Solubilities at High Dilution of Toluene, Ethylbenzene, 1,2,4-Trimethylbenzene, and Hexane in Di-2-ethylhexyl, Diisoheptyl, and Diisononyl Phthalates
Ternary Liquid-Liquid(-Liquid) Equilibria of Aniline + Cyclohexylamine + Water, Aniline + Cyclohexylamine + Octane, Aniline + Water + Toluene, and Aniline + Water + Octane
Activity Coefficients at Infinite Dilution in 1-Alkyl-3-methylimidazolium Tetrafluoroborate Ionic Liquids
Vapor-Liquid Equilibrium of Ferrocene in Some Organic Solvents Using Spectroscopic Methods
Azeotropic and Heats of Mixing Data for Several Binary Organic Systems Containing 1-Methoxy-2-propanol and 2-Butoxy Ethanol
Thermodynamic Properties of Mixtures Containing Ionic Liquids: Activity Coefficients at Infinite Dilution of Organic Compounds in 1-Propyl Boronic Acid-3-Alkylimidazolium Bromide and 1-Propenyl-3-alkylimidazolium Bromide Using Inverse Gas Chromatography
Solubilities of Benzene, Toluene, and Xylene Isomers in 1-Butyl-3-methylimidazolium Tetrafluoroborate
Densities and Viscosities for the Ternary Systems of Methyl tert-Butyl Ether + Methanol + Benzene and Methyl tert-Butyl Ether + Methanol + Toluene and Their Sub-binary Systems at 298.15 K
Vapor-Liquid Equilibrium for Binary System of 1-Propanethiol, Thiophene, and Diethyl Sulfide with Toluene at 90.03 kPa
Phase Boundaries of CO2 + Toluene, CO2 + Acetone, and CO2 + Ethanol at High Temperatures and High Pressures
Ternary Liquid-Liquid Equilibria for Systems of (Sulfolane + Toluene or Chloronaphthalene + Octane)
Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Butyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
Liquid-Liquid Equilibria of Ternary and Six-Component Systems Including Cyclohexane, Benzene, Toluene, Ethylbenzene, Cumene, and Sulfolane at 303.15 K
Viscosities, Densities, and Speeds of Sound of Binary Mixtures of Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Mesitylene with Anisole at (288.15, 293.15, 298.15, and 303.15) K
Interfacial Tension of Toluene + Water + Sodium Dodecyl Sulfate from (20 to 50) degC and pH between 4 and 9
Thermodynamics of Fuels with a Biosynthetic Component: Vapor-Liquid Equilibrium Data for Binary and Ternary Mixtures Containing Ethyl 1,1-Dimethylethyl Ether, n-Heptane, and Toluene at T ) 313.15 K
Excess Molar Volumes at 298.15 K and Isothermal Vapor-Liquid Equilibria at 333.15 K for the Binary Mixtures of Dimethyl Carbonate with Benzene, Toluene, n-Heptane, and Isooctane
Densities, Viscosities, and Speed of Sound Studies of Binary Mixtures of Methylbenzene with Heptan-1-ol, Octan-1-ol, and Decan-1-ol at (303.15 and 313.15) K
Solubility of Ethylene in 2,2,4-Trimethylpentane at Various Temperatures and Pressures
Experimental Study of Thermodynamic Properties of Mixtures Containing Ionic Liquid 1-Ethyl-3-methylimidazolium Ethyl Sulfate Using Gas-Liquid Chromatography and Transpiration Method
Diffusion Coefficients of Aromatic Compounds at Infinite Dilution in Binary Mixtures at 298.15 K
Measurement and Correlation of CO2 Solubility in the Systems of CO2 + Toluene, CO2 + Benzene, and CO2 + n-Hexane at Near-Critical and Supercritical Conditions
Solubility of D-p-Hydroxyphenylglycine in Water, Methanol, Ethanol, Carbon Tetrachloride, Toluene, and N,N-Dimethylformamide between 278 K and 323 K
Vapor-Liquid Equilibrium for Binary System of Thiophene + n-Hexane at (338.15 and 323.15) K and Thiophene + 1-Hexene at (333.15 and 323.15) K
Vapor-Liquid Equilibrium for Carbon Dioxide + Isopropyl, Isobutyl, and Isoamyl Acetates
Solubility of 4-(3,4-Dichlorophenyl)-1-tetralone in Some Organic Solvents
Ternary and Quaternary Liquid + Liquid Equilibria for Systems of (Water + Toluene + m-Xylene + Phenol)
Solubility of Xylitol in Ethanol, Acetone, N,N-Dimethylformamide, 1-Butanol, 1-Pentanol, Toluene, 2-Propanol, and Water
Solubilities of Triphenylphosphine in Ethanol, 2-Propanol, Acetone, Benzene, and Toluene
Vapor-Liquid Equilibrium for Binary System of Diethyl Sulfide + n-Heptane and Diethyl Sulfide + 2,2,4-Trimethylpentane at (363.15 and 353.15) K
Solubility of a-Carotene in Binary Solvents Formed by Some Hydrocarbons with 2,5,8-Trioxanonane, 2-Propanone, and Cyclohexanone
Henry's Law Constants and Infinite Dilution Activity Coefficients of Propane, Propene, Butane, 2-Methylpropane, 1-Butene, 2-Methylpropene, trans-2-Butene, cis-2-Butene, 1,3-Butadiene, Dimethyl Ether, Chloroethane, and 1,1-Difluoroethane in Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Styrene
Viscosities and Interfacial Properties of I-Methyl-3-butylimidazolium Hexafluorophosphate and 1-Isobutenyl-3-methylimidazolium Tetrafluoroborate Ionic Liquids
Vapor-Liquid Equilibrium for Binary System of Diethyl Sulfide + n-Hexane at (338.15 and 323.15) K and Diethyl Sulfide + 1-Hexene at (333.15 and 323.15) K
Densities and Viscosities of N-Formylmorpholine + Benzene, + Toluene at Different Temperatures and Atmospheric Pressures
Activity Coefficients at Infinite Dilution Measurements for Organic Solutes and Water in the Ionic Liquid 1-Butyl-3-methyl-pyridinium Trifluoromethanesulfonate
Liquid-Liquid Equilibria in Ternary Systems of Aromatic Hydrocarbons (Toluene or Ethylbenzene) + Phenols + Water
Liquid-Liquid Equilibrium of Ternary and Quaternary Systems Including Methyl Acetate, Benzene, Toluene, and Water at 283.2 K under Atmosphere
Solubility of Artemisinin in Different Single and Binary Solvent Mixtures Between (284.15 and 323.15) K and NRTL Interaction Parameters
Solubility of Decabromodiphenyl Ether in Different Solvents at (283.0 to 323.0) K
Solubilities of Phosphorus-Containing Compounds in Selected Solvents
Determination of Activity Coefficients at Infinite Dilution of 35 Solutes in the Ionic Liquid, 1-Butyl-3-methylimidazolium Tosylate, Using Gas-Liquid Chromatography
Solvent Extraction of Toluene from Heptane with the Ionic Liquids N-Ethylpyridinium Bis(trifluoromethylsulfonyl)imide and z-Methyl-N-ethylpyridinium Bis(trifluoromethylsulfonyl)imide (z = 2, 3, or 4) at T = 313.2 K
Vapor-Liquid Equilibria and Density Measurement for Binary Mixtures of Benzene + Nonane, Methylbenzene + 1,2-Dimethylbenzene, 1,3-Dimethylbenzene + 2,3,4,5-Tetrahydrothiophene-1,1-dioxide (Sulfolane), 1,2-Dimethylbenzene + Sulfolane, 1,2-Dimethylbenzene + N-Methylformamide (NMF), 1,3-Dimethylbenzene + NMF, and 1,4-Dimethylbenzene + NMF from (333.15 to 353.15) K at Vacuum Conditions
Activity Coefficients at Infinite Dilution for Hydrocarbons in Fatty Alcohols Determined by Gas-Liquid Chromatography
Densities, Speeds of Sound, Excess Molar Volumes, and Excess Isentropic Compressibilities at T = (298.15 and 308.15) K for Methyl Methacrylate + 1-Alkanols (1-Butanol, 1-Pentanol, and 1-Heptanol) + Cyclohexane, + Benzene, + Toluene, + p-Xylene, and + Ethylbenzene
Solubility of Benzoic Acid in Pure Solvents and Binary Mixtures
Measuring the Aqueous Henry's Law Constant at Elevated Temperatures Using an Extended EPICS Technique
Vapor-Liquid Equilibria in Ternary Systems of Toluene or Octane + Phenols + Water
Liquid-Liquid Equilibria Measurement of Systems Involving Alkanes (Heptane and Dodecane), Aromatics (Benzene or Toluene), and Furfural
Liquid-Liquid Equilibrium in Ternary Systems Containing Ethylene Glycol, Monofunctional Benzene Derivative, and Ethyl Acetate
Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Decyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
Solubilities of Phenylphosphinic Acid, Methylphenylphosphinic Acid, Hexachlorocyclotriphosphazene, and Hexaphenoxycyclotriphosphazene in Selected Solvents
Liquid-Liquid Extraction of Toluene from Heptane Using 1-Alkyl-3-methylimidazolium Bis(trifluoromethylsulfonyl)imide Ionic Liquids
Activity Coefficients at Infinite Dilution in Methylimidazolium Nitrate Ionic Liquids
Solubilities of N-[(4-Bromo-3,5-difluorine)-phenyl]maleimide in Different Organic Solvents
Measurements of Activity Coefficients at Infinite Dilution for Organic Solutes and Water in the Ionic Liquid 1-Butyl-1-methylpiperydinium Thiocyanate
Influence of Anion Structure on the Liquid-Liquid Equilibria of 1-Ethyl-3-methyl-imidazolium Cation Based Ionic Liquid-Hydrocarbon Binary Systems
Ternary Liquid-Liquid Equilibria for the (Methanol + Methylbenzene + Decane) System at Different Temperatures
Solubilities of 3-Carboxy-3-hydroxypentanedioic Acid in Ethanol, Butan-1-ol, Water, Acetone, and Methylbenzene
Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Butyl-3-methylimidazolium Nitrate Using Gas-Liquid Chromatography
Solubilities of 1-Hexyl-3-methylimidazole Nitrate and 1-Octyl-3-methylimidazole Nitrate in Selected Solvents
Activity Coefficients at Infinite Dilution of Organic Compounds in Four New Imidazolium-Based Ionic Liquids
Experimental Determination of Quaternary and Ternary Isobaric Vapor Liquid Liquid Equilibrium and Vapor Liquid Equilibrium for the Systems Water Ethanol Hexane Toluene and Water Hexane Toluene at 101.3 kPa
Solubilities of Tris(o-phenylenedioxy)cyclotriphosphazene in Selected Solvents
Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Ethyl-3-methylimidazolium Diethylphosphate Using Gas Liquid Chromatography
Sulfonate-Based Ionic Liquids in the Liquid Liquid Extraction of Aromatic Hydrocarbons
1-Alkyl-2,3-dimethylimidazolium Bis(trifluoromethylsulfonyl)imide Ionic Liquids for the Liquid Liquid Extraction of Toluene from Heptane
Activity Coefficients at Infinite Dilution by GLC in Alkanediamines as Stationary Phases
Partition Coefficients of Organic Compounds in Four New Tetraalkylammonium Bis(trifluoromethylsulfonyl)imide Ionic Liquids Using Inverse Gas Chromatography
Isobaric Vapor Liquid Equilibrium for Binary Systems of Toluene + Acrylic Acid, Toluene + Acetic Acid, and Cyclohexane + Acrylic Acid at 20 kPa
Interactions of Volatile Organic Compounds with the Ionic Liquid 1-Butyl-1-methylpyrrolidinium Dicyanamide
Vapor-Liquid Equilibria of Binary Mixtures Containing 1-Butanol and Hydrocarbons at 313.15 K
Compressed Liquid Viscosity of 1,1,1,3,3-Pentafluoropropane (R245fa) and 1,1,1,3,3,3-Hexafluoropropane (R236fa)
Isobaric Vapor-Liquid Equilibrium for Binary Systems of Toluene + Ethanol, Toluene + Isopropanol at (101.3, 121.3, 161.3 and 201.3) kPa
Excess Molar Volumes of 2,4,6,8-Tetramethylcyclotetrasiloxane with Benzene, Toluene, and Xylene at T = (288.15, 298.15, and 308.15) K
Evaluation of the Performance of Trigeminal Tricationic Ionic Liquids for Separation Problems
Evaluation of the Performance of Four Solvents for the Liquid Liquid Extraction of Acrylic Acid from Water
Solid Liquid Phase Equilibrium and Solubility of Dibenzo[b,d]furan and 9H-Fluoren-9-one in Organic Solvents
Vapor Liquid Equilibria of Binary Mixtures Containing 2-Butanol and Hydrocarbons at 313.15 K
Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Butyl-3-methylimidazolium Dibutylphosphate Using Gas Liquid Chromatography
Determination of Gas Concentrations in Liquids by Nuclear Magnetic Resonance: Hydrogen in Organic Solvents
Solubility of 6-Chloropyridazin-3-amine in Different Solvents
Crystal Structures, Reaction Rates, and Selected Physical Properties of Halo-Boronsubphthalocyanines (Halo = Fluoride, Chloride, and Bromide)
Biomass-Derived Platform Chemicals: Thermodynamic Studies on the Extraction of 5-Hydroxymethylfurfural from Ionic Liquids
Ternary and Quaternary Liquid Liquid Equilibria for Systems of Water + Methanol + Methylanthranilate + Toluene at Different Temperatures
Measurements and Correlations of Liquid.Liquid Equilibria for Water + Ethanol + 1,1'-Oxybis(butane) + Methylbenzene or Heptane Mixtures at 298.15 K
Activity Coefficients at Infinite Dilution for Organic Compounds Dissolved in 1-Alkyl-1-methylpyrrolidinium Bis(trifluoromethylsulfonyl)imide Ionic Liquids Having Six-, Eight-, and Ten-Carbon Alkyl Chains
Isobaric Heat Capacity Measurements of Liquid Methane, Ethane, and Propane by Differential Scanning Calorimetry at High Pressures and Low Temperatures
Determination and Correlation of Solubility Data and Dissolution Thermodynamic Data of l-Lactide in Different Pure Solvents
Determination of Henry's Law Constants Using Internal Standards with Benchmark Values
Liquid - Liquid Equilibria for the Ternary Systems of Per fl uorohexane + Methyl Nona fl uorobutyl Ether + Toluene, + 1,4-Dioxane, or + Dimethylformamide at 298.15 K
Solubilities of 4,4'-Dichlorodiphenyl Disulfide in Six Organic Solvents between (303.15 and 333.15) K
A Novel Vibrating-Wire Viscometer for High-Viscosity Liquids at Moderate Pressures
Liquid Liquid Equilibrium Data for {Heptane + Aromatic + 1-(2-Hydroxyethyl)-3-methylimidazolium Bis(trifluoromethylsulfonyl)imide ([hemim][NTf2])} Ternary Systems
A Promising Ionic Liquid [BMIM][FeCl4] for the Extractive Separation of Aromatic and Aliphatic Hydrocarbons
Solubilities of 4-Amino-4?-nitrodiphenyl Sulfide in Six Organic Solvents from 287.45 K to 365.55 K
Thermodynamics of Mixtures Containing Amines. XII. Volumetric and Speed of Sound Data at (293.15, 298.15, and 303.15) K for N-Methylaniline + Hydrocarbon Systems
Measurements of the Speed of Sound in Liquid Toluene
Excess Enthalpy and Excess Volume for Pyridine + Methyldiethanolamine and Pyridine + Ethanolamine Mixtures
Activity Coefficients at Infinite Dilution for Organic Solutes Dissolved in Three 1-Alkyl-1-methylpyrrolidinium Bis(trifluoromethylsulfonyl)imide Ionic Liquids Bearing Short Linear Alkyl Side Chains of Three to Five Carbons
Solubility Measurement and Modeling for 2-Benzoyl-3-chlorobenzoic Acid and 1-Chloroanthraquinone in Organic Solvents
Solubility of Benzyl Disulfide in Five Organic Solvents between (283.45 and 333.15) K
Solubilities of Phosphonic Acid, P,P'-(1,4-Piperazinediyl)bis-,P,P,P',P'-tetraphenyl Ester in Selected Solvents
Experimental Measurement and Modeling of Phase Diagrams of Binary Systems Encountered in the Gasoline Desulfurization Process Using Ionic Liquids
Liquid Liquid Equilibria for the Ternary Systems of Perfluamine + Hydrofluoroether + Benzene, Toluene, or Xylene at 298.15 K or 313.15 K
Measurement and Correlation of Solubilities of Indole-2-carboxylic Acid in Ten Different Pure Solvents from (278.15 to 360.15) K
Solubility of 1-Fluoro-4-(methylsulfonyl)benzene in Five Pure Organic Solvents at Temperatures from (288.40 to 331.50) K
Solid Liquid Phase Equilibria of N,N'-[1,3-Phenylenebis(methylene)]bis(phosphoramidic acid) P,P,P',P'-Tetraphenyl Ester in 10 Pure Solvents
Experimental Measurements and Modeling of the Solubility of Aceclofenac in Six Pure Solvents from (293.35 to 338.25) K
Infinite Dilution Activity Coefficients of Solutes Dissolved in Two Trihexyl(tetradecyl)phosphonium Ionic Liquids
Liquid Liquid Extraction of Toluene from n-Alkanes using {[4empy][Tf2N] + [emim][DCA]} Ionic Liquid Mixtures
Liquid Liquid Equilibria for the Ternary System Water + Benzyl Alcohol + Methylbenzene at (303.2 to 343.2) K
Experimental and Modeling of the Propene Solubility in the Heptane and Methylbenzene Solvents
Solubility and Thermodynamic Functions of Isatin in Pure Solvents
Thermodynamic Properties of Ternary Liquid Mixtures Containing o-Chlorotoluene: Excess Molar Volumes and Excess Isentropic Compressibilities
Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of n-Hexadecane + Ethylbenzene or + Toluene at (293.15 to 373.15) K and 0.1 MPa
Liquid Liquid Equilibria for Quaternary Systems of Water + Ethanol + Diethyl Carbonate + Methylbenzene or Heptane
Solubilities of Benzoic Acid in Binary Methylbenzene + Benzyl Alcohol and Methylbenzene + Benzaldehyde Solvent Mixtures
Experimental Study: The Impact of Dissolved Water on the Viscosity of Reservoir Fluids at HPHT Conditions
Measuring and Modeling the Solubility and Density for CO2 Toluene and C2H6 Toluene Systems
Selective Separation of Aromatics from Paraffins and Cycloalkanes Using Morpholinium-Based Ionic Liquid
Determination and Correlation of Solubilities of 2-Isopropylthioxanthone (ITX) in Seven Different Solvents from (299.15 to 329.85) K
Solid Liquid Phase Equilibrium of Phosphoramidic acid, N,N'-1,2-Ethanediylbis-P,P,P',P'-tetraphenyl Ester in Selected Solvents
Experimental Study of Solubility of Water in Liquid Organic Hydrogen Carriers
Measurement of the Speed of Sound in Hexane and Heptane at Temperatures from (303.15 to 536.15) K and Pressures from (1.0 to 8.5) MPa
Measurement and Correlation of the Solubility for 4,4'-Diaminodiphenylmethane in Different Solvents
Deduction of Physicochemical Properties from Solubilities: 2,4-Dihydroxybenzophenone, Biotin, and Caprolactam as Examples
Dialkylphosphate-Based Ionic Liquids as Solvents to Extract Toluene from Heptane
Measurement and Correlation of Diffusion Coefficients of Aromatic Compounds at Infinite Dilution in Alkane and Cycloalkane Solvents
Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Propyl-2,3-dimethylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
Surface Tension of the Ternary System Water + Acetone + Toluene
Experimental Isobaric Vapor-Liquid Equilibria of Binary Mixtures of 2,2,2-Trifluoroethanol with Benzene or Toluene
Measurement and Correlation of Liquid-Liquid Equilibria of Methylcyclohexane + Toluene + N-Formylmorpholine at (293, 303, 313, and 323) K
Measurement of Activity Coefficient at Infinite Dilution of Hydrocarbons in Sulfolane Using Gas-Liquid Chromatography
Isothermal Phase Equilibria and Excess Molar Enthalpies for Binary Systems with Dimethyl Ether at 323.15 K
Solubility of Fluorene in Different Solvents from 278.98 K to 338.35 K
Isothermal Vapor-Liquid Equilibrium Data for the System Methanol + Toluene + Triphenylbenzylphosphonium Chloride
Solubility of 2,6-Diaminopyridine in Toluene, o-Xylene, Ethylbenzene, Methanol, Ethanol, 2-Propanol, and Sodium Hydroxide Solutions
Excess Enthalpies of Chloroalkylbenzene + Alkylbenzene Mixtures
Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Butyl-3-methylimidazolium Trifluoromethanesulfonate Using Gas-Liquid Chromatography
Liquid-Liquid Equilibrium for the Quaternary System Water + Tetrahydrofuran + Toluene + 1-Butanol Mixture at 25 deg C and Atmospheric Pressure
Molar Excess Volume of sec- and tert-Butyl Chloride with Aromatic Hydrocarbons at T = 298.15 K
Solubilities of the Gaseous and Liquid Solutes and Their Thermodynamics of Solubilization in the Novel Room-Temperature Ionic Liquids at Infinite Dilution by Gas Chromatography
Measurement and Prediction of Oxygen Solubility in Toluene at Temperatures from 298.45 K to 393.15 K and Pressures up to 1.0 MPa
Solubility of Acenaphthylene in Different Solvents between (278 and 323) K
Solubilities of Vitamin K3 in Benzene, Toluene, Ethylbenzene, o-Xylene, m-Xylene, and p-Xylene between (299.44 and 344.24) K
Excess Enthalpies of (N-Methylformamide or N-Methylacetamide) + Aromatic Compounds at 303.15 K
Mutual Solubility Measurements of Hydrocarbon-Water Systems Containing Benzene, Toluene, and 3-Methylpentane
Refractive Indices of Binary Mixtures of Tetrahydrofuran with Aromatic Hydrocarbon at Temperatures from (288.15 to 318.15) K
Vapor Liquid Equilibrium of N-Formylmorpholine with Toluene and Xylene at 101.33 kPa
Measuring Surface Tension of Liquids at High Temperature and Elevated Pressure
Phase Equilibria of (1-Ethyl-3-methylimidazolium Ethylsulfate + Hydrocarbon, + Ketone, and + Ether) Binary Systems
Influence of the Temperature on the Liquid Liquid Equilibria of Heptane + Toluene + Sulfolane and Heptane + m-Xylene + Sulfolane
Densities and Viscosities of Binary Mixtures of Vitamin K3 with Benzene, Toluene, Ethylbenzene, o-Xylene, m-Xylene, and p-Xylene from (303.15 to 333.15) K
Liquid-Liquid Equilibrium of Ternary Systems of Cyclohexane + (Benzene, + Toluene, + Ethylbenzene, or + o-Xylene) + 4-Methyl-N-butyl Pyridinium Tetrafluoroborate Ionic Liquid at 303.15 K
Density and Viscosity Measurements of Diethyl Adipate from (303 to 373) K and up to 20 MPa
Measurements and Correlation of Liquid Liquid Equilibria of (Water + Ethanol + Dimethyl Carbonate + 2,2,4-Trimethylpentane or n-Heptane) and (Water + Dimethyl Carbonate + n-Heptane + Toluene)
Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Hexyl-3-methylimidazolium Trifluoromethanesulfonate Using Gas-Liquid Chromatography
Solubilities of Diphenylphosphinic Acid in Selected Solvents
Liquid-Liquid Equilibria for [C8mim][NTf2] + Thiophene + 2,2,4-Trimethylpentane or + Toluene
Enthalpies of Vaporization and Vapor Pressures of Some Deuterated Hydrocarbons. Liquid-Vapor Pressure Isotope Effects
Molar Excess Volumes and Excess Isentropic Compressibilities of Ternary Mixtures of o-Toluidine
Vapor-Liquid Equilibrium Data for the System Methanol + Toluene + Tetrabutylammonium Tetraphenylborate
Vapor-Liquid Equilibria of Binary Systems Comprising 1-Chloro-2-ethylhexane and 2-Ethyl-1-hexanol
Diffusion of Benzonitrile in CO2-Expanded Ethanol
Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Ethyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
Measurement of Infinite Dilution Activity Coefficients of Alcohols, Ketones, and Aromatic Hydrocarbons in 4-Methyl-N-butylpyridinium Tetrafluoroborate and 1-Butyl-3-methylimidazolium Hexafluorophosphate by Gas-Liquid Chromatography
Thermo Physical Properties of 4-Hydroxy 4-Methyl Pentanone with Nitrobenzene or Ethyl Benzene at Temperatures of (303.15, 313.15, and 323.15) K and a Pressure of 0.1 MPa
Solubility of Diamantane, Trimantane, Tetramantane, and Their Derivatives in Organic Solvents
Solubilities of 1,4-Naphthoquinone in Acetone, Toluene, Xylene, Ethanol, and n-Butyl Alcohol
Solubility of Artemisinin in Seven Different Pure Solvents from (283.15 to 323.15) K
Solubility of Bis(benzoxazolyl-2-methyl) Sulfide in Different Pure Solvents and Ethanol + Water Binary Mixtures between (273.25 and 325.25) K
Densities, Refractive Indices, and Excess Properties of Binary Mixtures of 1,4-Dioxane with Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Mesitylene at Temperatures from (288.15 to 318.15) K
Phase Equilibria Study of the Binary Systems (N-Butyl-4-methylpyridinium Tosylate Ionic Liquid + Organic Solvent, or Water)
Viscosities of p-Xylene, Acetic Acid, and p-Xylene + Acetic Acid at (313.15 to 473.15) K and (0.10 to 3.20) MPa: Determined by the Rolling-Ball Method
Activity Coefficients at Infinite Dilution of Organic Compounds in 1-Butyl-3-methylimidazolium Tetrafluoroborate Using Inverse Gas Chromatography
Vapor-Liquid Equilibria of Water + Triethylene Glycol (TEG) and Water + TEG + Toluene at 85 kPa
Solubility of Fluorene in Benzene, Chloroform, Acetone, 1-Propanol, Isobutanol, and Methylbenzene from (283 to 323) K
Thermophysical Characterization of Liquids Using Precise Density and Isobaric Heat Capacity Measurements As a Function of Pressure
Solubility of Adipic Acid in Acetone, Chloroform, and Toluene
Activity Coefficients at Infinite Dilution of Organic Compounds in Trihexyl(tetradecyl)phosphonium Bis(trifluoromethylsulfonyl)imide Using Inverse Gas Chromatography
Solubility of Canthaxanthin in Pure Solvents from (293.15 to 343.15) K
Solubilities of Triphenylphosphine Oxide in Selected Solvents
Paramagnetic Ionic Liquid 1-Butyl-3-methylimidazolium Tetrabromidocobaltate(II): Activity Coefficients at Infinite Dilution of Organic Solutes and Crystal Structure
Isothermal Vapor-Liquid Equilibria and Excess Enthalpy Data for the Binary System (Butyric Acid + Toluene)
Density, Speed of Sound, and Refractive Index for Binary Mixtures Containing Cycloalkanes and Aromatic Compounds at T = 313.15 K
Density and Viscosity of Decalin, Cyclohexane, and Toluene Binary Mixtures at (283.15, 293.15, 303.15, 313.15, and 323.15) K
Binary and Ternary Vapor-Liquid Equilibrium at 323.15 K and Excess Molar Volumes at 298.15 K for the Mixtures of Propyl Vinyl Ether + 1-Propanol + Toluene
Determination of the Density of Toluene in the Range from (293 to 373) K and from (0.1 to 30) MPa
Densities and Viscosities of Binary Mixtures of Methyl 4-Chlorobutyrate with Aromatic Hydrocarbons at T ) (298.15 to 318.15) K
Solubility of Elemental Sulfur in Toluene between (267.15 and 313.15) K under Atmospheric Pressure
Molar Excess Volumes and Excess Isentropic Compressibilities of {2-Methylaniline (i) + Benzene (j) + Methylbenzene}, {2-Methylaniline (i) + Benzene (j) + 1,2-Dimethylbenzene (k)}, and {2-Methylaniline (i) + Benzene (j) + 1,4-Dimethylbenzene (k)} at T = 308.15 K
Dynamic Viscosity of the Binary System 1-Propanol + Toluene as a Function of Temperature and Pressure
Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-(2-Hydroxyethyl)-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
Solubilities of Methyldiphenylphosphine Oxide in Selected Solvents
Measurement and Correlation of Bubble Point Pressure in (CO2 + C6H6), (CO2 + CH3C6H5), (CO2 + C6H14), and (CO2 + C7H16) at Temperatures from (293.15 to 313.15) K
Partition Coefficients of Organic Compounds in New Imidazolium and Tetralkylammonium Based Ionic Liquids Using Inverse Gas Chromatography
Solubility of Penicillin Sulfoxide in Different Solvents
Solubilities of 3-Pentadecylphenol in Ethanol, 1-Butanol, Toluene, Acetone, Tetrachloromethane, and Ethyl Acetate
Pure Component and Binary Vapor-Liquid Equilibrium + Modeling for Hexafluoropropylene and Hexafluoropropylene Oxide with Toluene and Hexafluoroethane
Liquid-Liquid Equilibria for the Three Ternary Systems (3-Methyl-N-butylpyridinium Dicyanamide + Toluene + Heptane), (1-Butyl-3-methylimidazolium Dicyanamide + Toluene + Heptane) and (1-Butyl-3-methylimidazolium Thiocyanate + Toluene + Heptane) at T = (313.15 and 348.15) K and p = 0.1 MPa
Comparison of the Efficiencies of Amine Extractants on Lactic Acid with Different Organic Solvents
Phase Equilibria of (1-Hexyl-3-methylimidazolium Thiocyanate + Water, Alcohol, or Hydrocarbon) Binary Systems
Density, Speed of Sound, and Refractive Index of the Binary Systems Cyclohexane (1) or Methylcyclohexane (1) or Cyclo-octane (1) with Benzene (2), Toluene (2), and Ethylbenzene (2) at Two Temperatures
Density and Viscosity of Ketones with Toluene at Different Temperatures and at Atmospheric Pressure
Liquid-Liquid Equilibrium for Ternary Mixtures of Hexane + Aromatic Compounds + [EMpy][ESO4] at T = 298.15 K
Phase Equilibria for Liquid Mixtures of (an Alkane + Toluene + Dimethyl Phthalate)
Solubilities of N-[(4-Bromo-3,5-difluorine)phenyl]acrylamide in Benzene, Methanol, Pyridine, Ethanol, Acetonitrile, and Toluene at Temperatures between (284.65 and 348.95) K
Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in Glycerol Using Gas-Liquid Chromatography
Solubilities of (2,5-Dihydroxyphenyl)diphenyl Phosphine Oxide in Selected Solvents
Effect of the Chain Length on the Aromatic Ring in the Separation of Aromatic Compounds from Methylcyclohexane Using the Ionic Liquid 1-Ethyl-3-methylpyridinium Ethylsulfate
Study of Ether-, Alcohol-, or Cyano-Functionalized Ionic Liquids Using Inverse Gas Chromatography
Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Ethyl-3-methylimidazolium Tris(pentafluoroethyl)trifluorophosphate [EMIM][FAP] Using Gas-Liquid Chromatography
Activity Coefficients at Infinite Dilution Measurements for Organic Solutes and Water in the Ionic Liquid 1-Hexyl-3-methylimidazolium Thiocyanate
Solubility of Triadimefon in Organic Solvents at Temperatures between (288.15 and 333.15) K
Liquid-Liquid Equilibria for the Ternary Systems {Heptane + Toluene + N-Butylpyridinium Tetrafluoroborate or N-Hexylpyridinium Tetrafluoroborate} at T = 313.2 K
Mutual Solubility of Pyridinium-Based Tetrafluoroborates and Toluene
Joback Method
KDB
Aqueous Solubility Prediction Method
Estimated Solubility Method
McGowan Method
NIST Webbook
The Yaws Handbook of Vapor Pressure
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