Contents
Physical Properties
Temperature Dependent Properties
Pressure Dependent Properties
Datasets
Correlations
Similar Compounds
Mixtures
Sources
Physical Properties
Property
Value
Unit
Source
ω
0.3490
KDB
Tig
495.93
K
KDB
AP
342.850
K
KDB
Δc H°liquid
[-4830.00; -4810.30]
kJ/mol
Δc H°liquid
Outlier -4830.00 ± 120.00
kJ/mol
NIST
Δc H°liquid
-4818.70
kJ/mol
NIST
Δc H°liquid
-4816.91 ± 0.63
kJ/mol
NIST
Δc H°liquid
-4817.16 ± 0.88
kJ/mol
NIST
Δc H°liquid
-4815.00 ± 1.00
kJ/mol
NIST
Δc H°liquid
-4810.30
kJ/mol
NIST
Δc H°liquid
-4817.00 ± 1.50
kJ/mol
NIST
Cp,liquid
223.91
J/mol×K
THERMOD...
μ
0.00
debye
KDB
LFL
1.00
% in Air
KDB
UFL
7.00
% in Air
KDB
Tflash,oc
269.26
K
KDB
Δf G°
8.00
kJ/mol
KDB
Rg
4.2670
KDB
Δc,gross H
4816.91
kJ/mol
KDB
Δc,net H
4464.788
kJ/mol
KDB
Δf H°gas
[-189.30; -187.80]
kJ/mol
Δf H°gas
-187.90
kJ/mol
KDB
Δf H°gas
-187.80 ± 0.79
kJ/mol
NIST
Δf H°gas
-189.30
kJ/mol
NIST
Δf H°liquid
[-225.90; -224.40]
kJ/mol
Δf H°liquid
-224.40 ± 0.79
kJ/mol
NIST
Δf H°liquid
-225.90 ± 1.30
kJ/mol
NIST
Δfus H°
14.06
kJ/mol
Measure...
Δvap H°
[32.00; 36.90]
kJ/mol
Δvap H°
36.66
kJ/mol
NIST
Δvap H°
36.60
kJ/mol
NIST
Δvap H°
36.90
kJ/mol
NIST
Δvap H°
36.60 ± 0.10
kJ/mol
NIST
Δvap H°
36.55
kJ/mol
NIST
Δvap H°
36.54
kJ/mol
NIST
Δvap H°
Outlier 32.00 ± 0.20
kJ/mol
NIST
IE
[9.83; 10.16]
eV
IE
9.93 ± 0.10
eV
NIST
IE
10.15
eV
NIST
IE
9.93 ± 0.10
eV
NIST
IE
9.83 ± 0.15
eV
NIST
IE
9.91
eV
NIST
IE
9.90 ± 0.05
eV
NIST
IE
10.16
eV
NIST
IE
10.08
eV
NIST
log 10 WS
[-4.53; -4.53]
log 10 WS
-4.53
Aq. Sol...
log 10 WS
-4.53
Estimat...
log Poct/wat
2.977
Crippen Calculated Property
McVol
109.490
ml/mol
McGowan Calculated Property
Pc
[2723.80; 2801.64]
kPa
Pc
2740.00
kPa
KDB
Pc
2740.00 ± 30.00
kPa
NIST
Pc
2730.00 ± 40.00
kPa
NIST
Pc
2730.00 ± 30.00
kPa
NIST
Pc
2730.00 ± 10.00
kPa
NIST
Pc
2734.00 ± 20.00
kPa
NIST
Pc
2736.00
kPa
NIST
Pc
2734.00 ± 5.00
kPa
NIST
Pc
2775.00 ± 5.00
kPa
NIST
Pc
2760.00 ± 50.66
kPa
NIST
Pc
2736.52 ± 17.23
kPa
NIST
Pc
2736.00 ± 40.53
kPa
NIST
Pc
2770.00 ± 50.66
kPa
NIST
Pc
2750.00 ± 34.50
kPa
NIST
Pc
2730.31 ± 20.68
kPa
NIST
Pc
2730.00 ± 103.42
kPa
NIST
Pc
2735.77 ± 4.05
kPa
NIST
Pc
2735.77 ± 5.06
kPa
NIST
Pc
Outlier 2801.64 ± 20.26
kPa
NIST
Pc
2723.80 ± 26.70
kPa
NIST
ρc
[232.47; 241.49]
kg/m3
ρc
234.47 ± 3.01
kg/m3
NIST
ρc
232.47 ± 10.02
kg/m3
NIST
ρc
233.47 ± 6.01
kg/m3
NIST
ρc
232.47
kg/m3
NIST
ρc
234.47 ± 5.01
kg/m3
NIST
ρc
232.47 ± 5.01
kg/m3
NIST
ρc
241.49 ± 15.03
kg/m3
NIST
ρc
234.67 ± 1.60
kg/m3
NIST
ρc
234.71 ± 1.60
kg/m3
NIST
ρc
241.49 ± 2.00
kg/m3
NIST
ρc
241.49 ± 5.01
kg/m3
NIST
ρc
234.07 ± 3.01
kg/m3
NIST
S°liquid
[326.40; 330.10]
J/mol×K
S°liquid
328.57
J/mol×K
NIST
S°liquid
327.98
J/mol×K
NIST
S°liquid
328.86
J/mol×K
NIST
S°liquid
330.10
J/mol×K
NIST
S°liquid
326.40
J/mol×K
NIST
Tboil
[370.30; 372.00]
K
Tboil
371.60
K
KDB
Tboil
371.47
K
Isobari...
Tboil
371.35
K
Measure...
Tboil
371.64
K
Isobari...
Tboil
371.64
K
Isobari...
Tboil
371.40
K
Isobari...
Tboil
371.64
K
Isobari...
Tboil
371.56
K
Solutio...
Tboil
371.50
K
Excess ...
Tboil
371.53
K
Isobari...
Tboil
371.35
K
Excess ...
Tboil
371.28
K
Vapor L...
Tboil
Outlier 370.97
K
A New T...
Tboil
371.35
K
Isobari...
Tboil
371.18
K
Densiti...
Tboil
371.56
K
Measure...
Tboil
371.50
K
Vapor-L...
Tboil
371.65
K
Isobari...
Tboil
371.50 ± 0.20
K
NIST
Tboil
371.46 ± 0.10
K
NIST
Tboil
371.55 ± 0.10
K
NIST
Tboil
371.80 ± 0.30
K
NIST
Tboil
371.35 ± 0.40
K
NIST
Tboil
371.60
K
NIST
Tboil
371.46 ± 0.10
K
NIST
Tboil
371.55 ± 0.50
K
NIST
Tboil
371.60
K
NIST
Tboil
371.54 ± 0.01
K
NIST
Tboil
371.53 ± 0.30
K
NIST
Tboil
371.60 ± 0.20
K
NIST
Tboil
371.50 ± 0.50
K
NIST
Tboil
371.35 ± 0.30
K
NIST
Tboil
371.64 ± 0.08
K
NIST
Tboil
371.53 ± 0.10
K
NIST
Tboil
Outlier 372.00 ± 2.00
K
NIST
Tboil
371.60 ± 0.30
K
NIST
Tboil
371.60 ± 0.40
K
NIST
Tboil
371.55 ± 0.20
K
NIST
Tboil
371.50 ± 0.50
K
NIST
Tboil
371.55 ± 0.20
K
NIST
Tboil
371.57 ± 0.20
K
NIST
Tboil
371.55 ± 0.10
K
NIST
Tboil
371.55 ± 0.30
K
NIST
Tboil
371.25 ± 0.30
K
NIST
Tboil
371.55 ± 0.20
K
NIST
Tboil
Outlier 371.00 ± 0.30
K
NIST
Tboil
371.45 ± 0.40
K
NIST
Tboil
371.60 ± 0.40
K
NIST
Tboil
371.59 ± 0.10
K
NIST
Tboil
371.55 ± 0.20
K
NIST
Tboil
371.70 ± 0.30
K
NIST
Tboil
371.77 ± 0.15
K
NIST
Tboil
371.46 ± 0.05
K
NIST
Tboil
Outlier 370.65 ± 1.50
K
NIST
Tboil
Outlier 371.00 ± 3.00
K
NIST
Tboil
371.60 ± 0.20
K
NIST
Tboil
371.68 ± 0.20
K
NIST
Tboil
371.65 ± 0.70
K
NIST
Tboil
371.55 ± 0.50
K
NIST
Tboil
371.55 ± 0.50
K
NIST
Tboil
371.58 ± 0.20
K
NIST
Tboil
371.55 ± 0.50
K
NIST
Tboil
371.55 ± 0.50
K
NIST
Tboil
371.55 ± 0.30
K
NIST
Tboil
371.55 ± 0.40
K
NIST
Tboil
371.55 ± 0.50
K
NIST
Tboil
371.65 ± 0.30
K
NIST
Tboil
371.45 ± 0.15
K
NIST
Tboil
371.55 ± 0.50
K
NIST
Tboil
371.60 ± 0.20
K
NIST
Tboil
371.45 ± 0.30
K
NIST
Tboil
371.58 ± 0.08
K
NIST
Tboil
371.60 ± 0.20
K
NIST
Tboil
371.57 ± 0.02
K
NIST
Tboil
371.58 ± 0.20
K
NIST
Tboil
371.55 ± 0.10
K
NIST
Tboil
371.50 ± 0.15
K
NIST
Tboil
371.60 ± 0.30
K
NIST
Tboil
Outlier 370.30 ± 1.00
K
NIST
Tboil
371.55 ± 0.30
K
NIST
Tboil
371.57 ± 0.30
K
NIST
Tboil
371.55 ± 0.20
K
NIST
Tboil
371.57 ± 0.30
K
NIST
Tboil
371.57 ± 0.03
K
NIST
Tboil
371.68 ± 0.15
K
NIST
Tboil
371.55 ± 0.30
K
NIST
Tboil
371.55 ± 0.30
K
NIST
Tboil
371.45 ± 0.50
K
NIST
Tboil
371.40 ± 0.50
K
NIST
Tboil
371.65 ± 0.50
K
NIST
Tboil
371.59 ± 0.30
K
NIST
Tboil
371.54 ± 0.20
K
NIST
Tboil
371.55 ± 0.30
K
NIST
Tboil
371.60 ± 0.30
K
NIST
Tboil
371.56 ± 0.15
K
NIST
Tboil
371.55 ± 0.30
K
NIST
Tboil
371.60 ± 0.20
K
NIST
Tboil
371.10 ± 0.70
K
NIST
Tboil
371.55 ± 0.50
K
NIST
Tboil
371.55 ± 0.30
K
NIST
Tboil
371.55 ± 0.30
K
NIST
Tboil
371.60 ± 0.40
K
NIST
Tboil
371.60 ± 0.30
K
NIST
Tboil
371.55 ± 0.70
K
NIST
Tboil
371.55 ± 0.60
K
NIST
Tboil
371.40 ± 1.00
K
NIST
Tboil
371.54 ± 0.10
K
NIST
Tboil
371.55 ± 0.50
K
NIST
Tboil
371.57 ± 0.01
K
NIST
Tboil
371.57 ± 0.30
K
NIST
Tboil
371.55 ± 0.30
K
NIST
Tboil
371.55 ± 0.30
K
NIST
Tboil
371.55 ± 0.50
K
NIST
Tboil
371.57 ± 0.30
K
NIST
Tboil
371.70 ± 0.20
K
NIST
Tboil
371.55 ± 0.50
K
NIST
Tboil
371.55 ± 0.30
K
NIST
Tboil
371.20 ± 0.70
K
NIST
Tboil
371.54 ± 0.15
K
NIST
Tboil
Outlier 372.00 ± 1.50
K
NIST
Tboil
371.55 ± 0.50
K
NIST
Tboil
371.58 ± 0.05
K
NIST
Tboil
371.15 ± 1.00
K
NIST
Tboil
371.55 ± 0.20
K
NIST
Tboil
371.70 ± 0.20
K
NIST
Tboil
371.15 ± 2.00
K
NIST
Tboil
371.55 ± 0.25
K
NIST
Tboil
371.75 ± 0.40
K
NIST
Tboil
371.55 ± 1.00
K
NIST
Tboil
371.60 ± 0.30
K
NIST
Tboil
371.35 ± 1.00
K
NIST
Tboil
371.58 ± 0.03
K
NIST
Tboil
371.40 ± 0.50
K
NIST
Tboil
371.55 ± 0.50
K
NIST
Tboil
371.65 ± 0.30
K
NIST
Tboil
371.57 ± 0.30
K
NIST
Tboil
371.65 ± 0.50
K
NIST
Tboil
371.65 ± 0.30
K
NIST
Tboil
Outlier 371.00 ± 1.00
K
NIST
Tboil
371.15 ± 1.00
K
NIST
Tboil
371.60 ± 0.20
K
NIST
Tboil
371.57 ± 0.10
K
NIST
Tboil
371.56 ± 0.20
K
NIST
Tboil
371.55 ± 0.30
K
NIST
Tboil
371.55 ± 1.00
K
NIST
Tboil
371.57 ± 0.03
K
NIST
Tboil
371.55 ± 0.50
K
NIST
Tboil
371.55 ± 0.50
K
NIST
Tboil
371.15 ± 1.00
K
NIST
Tboil
371.55 ± 0.50
K
NIST
Tboil
371.40 ± 0.40
K
NIST
Tboil
371.73 ± 0.20
K
NIST
Tboil
371.55 ± 0.20
K
NIST
Tboil
371.56 ± 0.15
K
NIST
Tboil
371.55 ± 0.50
K
NIST
Tboil
371.57 ± 0.02
K
NIST
Tboil
371.65 ± 1.50
K
NIST
Tboil
371.54 ± 0.15
K
NIST
Tboil
371.40 ± 1.00
K
NIST
Tboil
371.55 ± 0.30
K
NIST
Tboil
371.56 ± 0.02
K
NIST
Tboil
371.65 ± 1.50
K
NIST
Tboil
371.67 ± 0.03
K
NIST
Tboil
371.55 ± 0.50
K
NIST
Tboil
371.67 ± 0.05
K
NIST
Tboil
371.55 ± 0.50
K
NIST
Tboil
371.30 ± 0.50
K
NIST
Tboil
371.45 ± 0.50
K
NIST
Tboil
371.15 ± 0.60
K
NIST
Tboil
Outlier 370.65 ± 0.60
K
NIST
Tboil
Outlier 370.40 ± 0.50
K
NIST
Tboil
371.50 ± 0.20
K
NIST
Tboil
371.10 ± 0.60
K
NIST
Tboil
371.51 ± 0.05
K
NIST
Tboil
371.51 ± 0.04
K
NIST
Tboil
371.65 ± 1.50
K
NIST
Tboil
371.70 ± 0.50
K
NIST
Tboil
371.55 ± 0.50
K
NIST
Tboil
371.40 ± 1.00
K
NIST
Tboil
Outlier 371.00 ± 1.00
K
NIST
Tboil
371.55 ± 0.30
K
NIST
Tboil
371.50 ± 0.20
K
NIST
Tboil
371.55 ± 0.30
K
NIST
Tboil
371.15 ± 1.00
K
NIST
Tboil
371.60 ± 0.30
K
NIST
Tboil
371.30 ± 1.00
K
NIST
Tboil
371.65 ± 1.00
K
NIST
Tboil
371.45 ± 0.15
K
NIST
Tboil
371.55 ± 0.30
K
NIST
Tboil
371.55 ± 0.50
K
NIST
Tboil
371.15 ± 0.50
K
NIST
Tboil
371.55 ± 0.30
K
NIST
Tboil
371.55 ± 0.20
K
NIST
Tboil
371.55 ± 0.20
K
NIST
Tboil
371.53 ± 0.10
K
NIST
Tboil
371.50 ± 0.15
K
NIST
Tboil
371.55 ± 0.30
K
NIST
Tboil
371.55 ± 0.30
K
NIST
Tboil
371.55 ± 0.50
K
NIST
Tboil
371.53 ± 0.10
K
NIST
Tboil
371.60 ± 0.20
K
NIST
Tboil
371.55 ± 0.30
K
NIST
Tboil
371.55 ± 0.30
K
NIST
Tboil
371.55 ± 0.30
K
NIST
Tboil
371.55 ± 0.30
K
NIST
Tboil
371.55 ± 0.20
K
NIST
Tboil
371.55 ± 0.30
K
NIST
Tboil
371.55 ± 0.50
K
NIST
Tboil
371.45 ± 0.30
K
NIST
Tboil
371.65 ± 0.60
K
NIST
Tboil
371.45 ± 0.30
K
NIST
Tboil
371.15 ± 0.30
K
NIST
Tboil
371.55 ± 0.50
K
NIST
Tboil
371.60 ± 0.50
K
NIST
Tboil
371.60 ± 0.20
K
NIST
Tboil
371.55 ± 0.30
K
NIST
Tboil
371.60 ± 0.50
K
NIST
Tboil
371.60 ± 0.20
K
NIST
Tboil
371.71 ± 0.20
K
NIST
Tboil
371.35 ± 0.50
K
NIST
Tboil
371.90 ± 1.50
K
NIST
Tboil
371.46 ± 0.25
K
NIST
Tboil
371.65 ± 0.50
K
NIST
Tboil
371.70 ± 5.00
K
NIST
Tboil
371.55 ± 0.20
K
NIST
Tboil
371.55 ± 0.50
K
NIST
Tboil
371.49 ± 0.30
K
NIST
Tboil
371.30 ± 0.80
K
NIST
Tboil
371.30 ± 1.00
K
NIST
Tboil
371.65 ± 1.50
K
NIST
Tboil
371.45 ± 1.50
K
NIST
Tboil
371.15 ± 1.00
K
NIST
Tboil
371.15 ± 2.00
K
NIST
Tboil
371.90 ± 1.50
K
NIST
Tboil
371.60 ± 0.30
K
NIST
Tboil
371.50 ± 0.40
K
NIST
Tboil
371.59 ± 0.50
K
NIST
Tboil
371.55 ± 1.00
K
NIST
Tboil
371.55 ± 1.00
K
NIST
Tboil
371.58 ± 1.00
K
NIST
Tboil
371.57 ± 1.00
K
NIST
Tboil
371.15 ± 2.00
K
NIST
Tboil
371.65 ± 2.00
K
NIST
Tboil
371.65 ± 2.00
K
NIST
Tboil
371.15 ± 2.00
K
NIST
Tc
[536.70; 542.70]
K
Tc
540.20
K
KDB
Tc
540.10
K
Measure...
Tc
540.00
K
Measure...
Tc
540.00
K
Measure...
Tc
540.14
K
Experim...
Tc
540.60
K
The Cri...
Tc
540.10
K
Measure...
Tc
540.14
K
Determi...
Tc
540.20 ± 0.30
K
NIST
Tc
Outlier 536.80 ± 2.00
K
NIST
Tc
Outlier 536.70 ± 4.00
K
NIST
Tc
540.00 ± 1.00
K
NIST
Tc
540.40 ± 0.40
K
NIST
Tc
539.80 ± 0.30
K
NIST
Tc
540.30
K
NIST
Tc
540.10
K
NIST
Tc
540.17 ± 0.10
K
NIST
Tc
540.20
K
NIST
Tc
540.68 ± 0.08
K
NIST
Tc
540.20 ± 0.30
K
NIST
Tc
539.86 ± 0.07
K
NIST
Tc
539.90 ± 0.30
K
NIST
Tc
Outlier 542.70 ± 0.70
K
NIST
Tc
541.00 ± 0.50
K
NIST
Tc
540.00 ± 0.30
K
NIST
Tc
540.00 ± 0.40
K
NIST
Tc
540.60 ± 0.40
K
NIST
Tc
540.28 ± 0.20
K
NIST
Tc
540.30 ± 0.33
K
NIST
Tc
540.53 ± 0.27
K
NIST
Tc
540.50 ± 0.55
K
NIST
Tc
540.16 ± 0.05
K
NIST
Tc
540.16 ± 0.06
K
NIST
Tc
Outlier 542.65 ± 0.50
K
NIST
Tc
540.00 ± 1.00
K
NIST
Tfus
[176.05; 183.15]
K
Tfus
182.31
K
Aq. Sol...
Tfus
182.50
K
KDB
Tfus
182.55 ± 0.20
K
NIST
Tfus
182.55 ± 0.20
K
NIST
Tfus
182.55 ± 0.20
K
NIST
Tfus
182.55 ± 0.20
K
NIST
Tfus
182.57 ± 0.10
K
NIST
Tfus
182.58 ± 0.05
K
NIST
Tfus
182.55 ± 0.02
K
NIST
Tfus
182.56 ± 0.05
K
NIST
Tfus
183.15 ± 2.00
K
NIST
Tfus
182.12 ± 0.20
K
NIST
Tfus
182.54 ± 0.03
K
NIST
Tfus
182.54 ± 0.02
K
NIST
Tfus
182.65 ± 0.40
K
NIST
Tfus
182.54 ± 0.05
K
NIST
Tfus
182.54 ± 0.03
K
NIST
Tfus
182.50 ± 0.06
K
NIST
Tfus
182.54 ± 0.03
K
NIST
Tfus
182.49 ± 0.08
K
NIST
Tfus
182.45 ± 0.20
K
NIST
Tfus
182.53 ± 0.02
K
NIST
Tfus
182.54 ± 0.01
K
NIST
Tfus
182.45 ± 0.15
K
NIST
Tfus
182.45 ± 0.30
K
NIST
Tfus
182.50 ± 0.15
K
NIST
Tfus
182.55 ± 0.20
K
NIST
Tfus
182.54 ± 0.01
K
NIST
Tfus
182.54 ± 0.03
K
NIST
Tfus
182.54 ± 0.02
K
NIST
Tfus
182.49 ± 0.15
K
NIST
Tfus
182.51 ± 0.20
K
NIST
Tfus
182.55 ± 0.20
K
NIST
Tfus
183.15 ± 1.50
K
NIST
Tfus
182.47 ± 0.20
K
NIST
Tfus
182.55 ± 0.07
K
NIST
Tfus
182.35 ± 0.30
K
NIST
Tfus
182.57 ± 0.08
K
NIST
Tfus
182.35 ± 0.40
K
NIST
Tfus
183.15 ± 2.00
K
NIST
Tfus
183.15 ± 1.50
K
NIST
Tfus
182.34 ± 0.30
K
NIST
Tfus
182.53 ± 0.15
K
NIST
Tfus
182.49 ± 0.20
K
NIST
Tfus
182.53 ± 0.10
K
NIST
Tfus
181.95 ± 1.00
K
NIST
Tfus
182.45 ± 0.50
K
NIST
Tfus
182.55 ± 0.40
K
NIST
Tfus
182.50 ± 0.08
K
NIST
Tfus
182.65 ± 0.50
K
NIST
Tfus
182.65 ± 0.50
K
NIST
Tfus
182.65 ± 0.40
K
NIST
Tfus
183.15 ± 0.30
K
NIST
Tfus
Outlier 176.05 ± 1.00
K
NIST
Ttriple
[182.20; 187.57]
K
Ttriple
182.55
K
KDB
Ttriple
183.20 ± 0.10
K
NIST
Ttriple
182.57 ± 0.05
K
NIST
Ttriple
182.59 ± 0.06
K
NIST
Ttriple
182.59 ± 0.02
K
NIST
Ttriple
182.70 ± 0.20
K
NIST
Ttriple
182.56 ± 0.05
K
NIST
Ttriple
182.55 ± 0.03
K
NIST
Ttriple
182.55 ± 0.05
K
NIST
Ttriple
182.55 ± 0.03
K
NIST
Ttriple
182.56 ± 0.04
K
NIST
Ttriple
182.56 ± 0.04
K
NIST
Ttriple
182.55 ± 0.04
K
NIST
Ttriple
182.55 ± 0.02
K
NIST
Ttriple
182.55 ± 0.01
K
NIST
Ttriple
182.53 ± 0.04
K
NIST
Ttriple
182.53 ± 0.02
K
NIST
Ttriple
182.56 ± 0.00
K
NIST
Ttriple
182.56 ± 0.01
K
NIST
Ttriple
182.56 ± 0.01
K
NIST
Ttriple
182.55 ± 0.02
K
NIST
Ttriple
182.56 ± 0.02
K
NIST
Ttriple
182.55 ± 0.04
K
NIST
Ttriple
182.55 ± 0.02
K
NIST
Ttriple
182.56 ± 0.20
K
NIST
Ttriple
182.56 ± 0.20
K
NIST
Ttriple
182.56 ± 0.05
K
NIST
Ttriple
182.56 ± 0.03
K
NIST
Ttriple
183.56 ± 0.06
K
NIST
Ttriple
Outlier 187.57 ± 0.03
K
NIST
Ttriple
182.20 ± 0.20
K
NIST
Ttriple
182.60 ± 0.20
K
NIST
Vc
[0.425; 0.428]
m3 /kmol
Vc
0.428
m3 /kmol
KDB
Vc
0.428
m3 /kmol
NIST
Vc
0.425 ± 0.001
m3 /kmol
NIST
Vm
[1.47e-04; 1.47e-04]
m3 /mol
Vm
1.47e-04
m3 /mol
Thermod...
Vm
1.47e-04
m3 /mol
Thermod...
Zc
0.2610980
KDB
Zra
0.26
KDB
Temperature Dependent Properties
Property
Value
Unit
Temperature (K)
Source
Cp,gas
[191.50; 238.49]
J/mol×K
[357.10; 466.10]
Cp,gas
191.50 ± 0.19
J/mol×K
357.10
NIST
Cp,gas
198.78 ± 0.20
J/mol×K
373.15
NIST
Cp,gas
210.75 ± 0.21
J/mol×K
400.40
NIST
Cp,gas
225.31 ± 0.23
J/mol×K
434.35
NIST
Cp,gas
238.49 ± 0.24
J/mol×K
466.10
NIST
Cp,liquid
[201.51; 328.61]
J/mol×K
[228.15; 333.15]
Cp,liquid
202.31
J/mol×K
228.15
Isobari...
Cp,liquid
201.51
J/mol×K
228.15
Isobari...
Cp,liquid
206.22
J/mol×K
238.15
Isobari...
Cp,liquid
205.11
J/mol×K
238.15
Isobari...
Cp,liquid
209.60
J/mol×K
250.00
NIST
Cp,liquid
220.00
J/mol×K
285.00
NIST
Cp,liquid
222.88
J/mol×K
293.15
NIST
Cp,liquid
222.87
J/mol×K
293.15
Heat Ca...
Cp,liquid
223.23
J/mol×K
294.15
Heat Ca...
Cp,liquid
223.60
J/mol×K
295.15
Heat Ca...
Cp,liquid
223.97
J/mol×K
296.15
Heat Ca...
Cp,liquid
224.60
J/mol×K
296.50
NIST
Cp,liquid
224.35
J/mol×K
297.15
Heat Ca...
Cp,liquid
224.62
J/mol×K
297.86
NIST
Cp,liquid
223.40
J/mol×K
298.00
NIST
Cp,liquid
211.30
J/mol×K
298.00
NIST
Cp,liquid
223.00
J/mol×K
298.00
NIST
Cp,liquid
224.00
J/mol×K
298.00
NIST
Cp,liquid
224.30
J/mol×K
298.10
NIST
Cp,liquid
224.71
J/mol×K
298.15
NIST
Cp,liquid
224.93
J/mol×K
298.15
NIST
Cp,liquid
224.19
J/mol×K
298.15
NIST
Cp,liquid
224.74
J/mol×K
298.15
NIST
Cp,liquid
224.74
J/mol×K
298.15
NIST
Cp,liquid
224.85
J/mol×K
298.15
NIST
Cp,liquid
224.93
J/mol×K
298.15
NIST
Cp,liquid
328.61
J/mol×K
298.15
NIST
Cp,liquid
224.66
J/mol×K
298.15
NIST
Cp,liquid
226.53
J/mol×K
298.15
NIST
Cp,liquid
224.78
J/mol×K
298.15
NIST
Cp,liquid
225.30
J/mol×K
298.15
NIST
Cp,liquid
224.64
J/mol×K
298.15
NIST
Cp,liquid
224.72
J/mol×K
298.15
NIST
Cp,liquid
224.73
J/mol×K
298.15
NIST
Cp,liquid
224.60
J/mol×K
298.15
NIST
Cp,liquid
224.72
J/mol×K
298.15
NIST
Cp,liquid
224.72
J/mol×K
298.15
Heat Ca...
Cp,liquid
224.71
J/mol×K
298.15
NIST
Cp,liquid
224.69
J/mol×K
298.15
NIST
Cp,liquid
224.78
J/mol×K
298.15
NIST
Cp,liquid
224.73
J/mol×K
298.15
NIST
Cp,liquid
224.71
J/mol×K
298.15
NIST
Cp,liquid
224.78
J/mol×K
298.15
NIST
Cp,liquid
224.76
J/mol×K
298.15
NIST
Cp,liquid
224.80
J/mol×K
298.15
NIST
Cp,liquid
255.00
J/mol×K
298.15
NIST
Cp,liquid
225.10
J/mol×K
299.15
Heat Ca...
Cp,liquid
222.20
J/mol×K
299.20
NIST
Cp,liquid
233.13
J/mol×K
299.80
NIST
Cp,liquid
225.14
J/mol×K
300.00
NIST
Cp,liquid
225.33
J/mol×K
300.00
NIST
Cp,liquid
225.60
J/mol×K
300.00
NIST
Cp,liquid
225.47
J/mol×K
300.15
Heat Ca...
Cp,liquid
210.90
J/mol×K
300.80
NIST
Cp,liquid
225.87
J/mol×K
301.15
Heat Ca...
Cp,liquid
226.22
J/mol×K
302.15
Heat Ca...
Cp,liquid
217.00
J/mol×K
303.00
NIST
Cp,liquid
226.61
J/mol×K
303.15
Heat Ca...
Cp,liquid
226.53
J/mol×K
303.15
NIST
Cp,liquid
225.25
J/mol×K
303.15
Isobari...
Cp,liquid
225.96
J/mol×K
303.15
Isobari...
Cp,liquid
227.00
J/mol×K
304.15
Heat Ca...
Cp,liquid
227.40
J/mol×K
305.15
Heat Ca...
Cp,liquid
227.75
J/mol×K
306.15
Heat Ca...
Cp,liquid
228.14
J/mol×K
307.15
Heat Ca...
Cp,liquid
228.54
J/mol×K
308.15
Heat Ca...
Cp,liquid
228.95
J/mol×K
309.15
Heat Ca...
Cp,liquid
229.30
J/mol×K
310.15
Heat Ca...
Cp,liquid
229.71
J/mol×K
311.15
Heat Ca...
Cp,liquid
230.11
J/mol×K
312.15
Heat Ca...
Cp,liquid
230.51
J/mol×K
313.15
Heat Ca...
Cp,liquid
229.16
J/mol×K
313.15
Isobari...
Cp,liquid
230.87
J/mol×K
313.15
Isobari...
Cp,liquid
230.37
J/mol×K
313.15
Heat Ca...
Cp,liquid
247.30
J/mol×K
332.00
NIST
Cp,liquid
240.03
J/mol×K
333.15
Heat Ca...
Cp,liquid
226.50
J/mol×K
333.15
NIST
η
[0.0000745; 0.0005260]
Pa×s
[273.15; 503.20]
η
0.0005260
Pa×s
273.15
Densiti...
η
0.0004950
Pa×s
278.15
Densiti...
η
0.0004650
Pa×s
283.15
Densiti...
η
0.0004380
Pa×s
288.15
Densiti...
η
0.0004410
Pa×s
288.15
Densiti...
η
0.0004170
Pa×s
293.15
Densiti...
η
0.0004038
Pa×s
293.15
Excess ...
η
0.0004142
Pa×s
293.15
Densiti...
η
0.0004150
Pa×s
293.15
Densiti...
η
0.0003960
Pa×s
298.15
Densiti...
η
0.0004009
Pa×s
298.15
Thermod...
η
0.0004040
Pa×s
298.15
Volumet...
η
0.0003920
Pa×s
298.15
Densiti...
η
0.0003928
Pa×s
298.15
Densiti...
η
0.0003831
Pa×s
298.15
Excess ...
η
0.0003720
Pa×s
303.15
Densiti...
η
0.0003728
Pa×s
303.15
Densiti...
η
0.0003629
Pa×s
303.15
Excess ...
η
0.0003750
Pa×s
303.15
Density...
η
0.0003830
Pa×s
303.15
Volumet...
η
0.0003750
Pa×s
303.15
Thermod...
η
0.0003750
Pa×s
303.15
Densiti...
η
0.0003848
Pa×s
303.20
Viscosi...
η
0.0003541
Pa×s
308.15
Densiti...
η
0.0003497
Pa×s
308.15
Viscome...
η
0.0003560
Pa×s
308.15
Densiti...
η
0.0003540
Pa×s
308.15
Densiti...
η
0.0003500
Pa×s
308.15
Density...
η
0.0003329
Pa×s
313.15
Viscome...
η
0.0003420
Pa×s
313.15
Volumet...
η
0.0003250
Pa×s
313.15
Density...
η
0.0003373
Pa×s
313.15
Thermod...
η
0.0003274
Pa×s
313.15
Excess ...
η
0.0003360
Pa×s
313.15
Densiti...
η
0.0003374
Pa×s
313.15
Densiti...
η
0.0003422
Pa×s
313.20
Viscosi...
η
0.0003097
Pa×s
323.00
Viscosi...
η
0.0002980
Pa×s
323.15
Excess ...
η
0.0003074
Pa×s
323.15
Thermod...
η
0.0002834
Pa×s
333.10
Viscosi...
η
0.0002793
Pa×s
333.15
Thermod...
η
0.0002704
Pa×s
333.15
Excess ...
η
0.0002541
Pa×s
343.15
Thermod...
η
0.0002487
Pa×s
343.15
Excess ...
η
0.0002562
Pa×s
343.30
Viscosi...
η
0.0002382
Pa×s
353.30
Viscosi...
η
0.0002207
Pa×s
363.20
Viscosi...
η
0.0002027
Pa×s
373.30
Viscosi...
η
0.0001853
Pa×s
383.20
Viscosi...
η
0.0001717
Pa×s
393.20
Viscosi...
η
0.0001590
Pa×s
403.20
Viscosi...
η
0.0001488
Pa×s
413.20
Viscosi...
η
0.0001392
Pa×s
423.20
Viscosi...
η
0.0001308
Pa×s
433.20
Viscosi...
η
0.0001193
Pa×s
443.40
Viscosi...
η
0.0001135
Pa×s
453.10
Viscosi...
η
0.0001047
Pa×s
463.20
Viscosi...
η
0.0000978
Pa×s
473.20
Viscosi...
η
0.0000896
Pa×s
483.10
Viscosi...
η
0.0000817
Pa×s
493.20
Viscosi...
η
0.0000745
Pa×s
503.20
Viscosi...
Δfus H
[13.99; 14.16]
kJ/mol
[182.20; 182.70]
Δfus H
14.16
kJ/mol
182.20
NIST
Δfus H
14.16
kJ/mol
182.20
NIST
Δfus H
14.04
kJ/mol
182.52
NIST
Δfus H
14.04
kJ/mol
182.55
NIST
Δfus H
14.04
kJ/mol
182.55
NIST
Δfus H
14.02
kJ/mol
182.56
NIST
Δfus H
14.02
kJ/mol
182.56
NIST
Δfus H
14.03
kJ/mol
182.56
NIST
Δfus H
14.06
kJ/mol
182.56
NIST
Δfus H
13.99
kJ/mol
182.57
NIST
Δfus H
14.05
kJ/mol
182.59
NIST
Δfus H
14.04
kJ/mol
182.60
NIST
Δfus H
14.04
kJ/mol
182.60
NIST
Δfus H
14.06
kJ/mol
182.70
NIST
Δsub H
57.90
kJ/mol
183.00
NIST
Δvap H
[31.70; 36.72]
kJ/mol
[298.00; 371.60]
Δvap H
36.72
kJ/mol
298.00
Enthalp...
Δvap H
35.60 ± 0.10
kJ/mol
313.00
NIST
Δvap H
36.10
kJ/mol
318.00
NIST
Δvap H
36.40
kJ/mol
318.00
NIST
Δvap H
36.10
kJ/mol
330.50
NIST
Δvap H
34.50 ± 0.10
kJ/mol
331.00
NIST
Δvap H
34.40 ± 0.10
kJ/mol
333.00
NIST
Δvap H
36.00
kJ/mol
335.50
NIST
Δvap H
36.10
kJ/mol
336.00
NIST
Δvap H
33.20 ± 0.10
kJ/mol
350.00
NIST
Δvap H
34.70
kJ/mol
350.50
NIST
Δvap H
33.10 ± 0.10
kJ/mol
353.00
NIST
Δvap H
35.50
kJ/mol
353.50
NIST
Δvap H
35.40
kJ/mol
355.50
NIST
Δvap H
35.20
kJ/mol
360.50
NIST
Δvap H
32.00
kJ/mol
371.00
NIST
Δvap H
31.77
kJ/mol
371.60
NIST
Δvap H
31.70
kJ/mol
371.60
KDB
ν
[0.0000005; 0.0000007]
m2 /s
[283.15; 313.15]
ν
0.0000007
m2 /s
283.15
Kinemat...
ν
0.0000007
m2 /s
283.15
Experim...
ν
0.0000006
m2 /s
298.15
Kinemat...
ν
0.0000006
m2 /s
298.15
Experim...
ν
0.0000005
m2 /s
313.15
Kinemat...
ν
0.0000005
m2 /s
313.15
Experim...
Pvap
[0.82; 2621.76]
kPa
[263.45; 537.20]
Pvap
0.82
kPa
263.45
Isother...
Pvap
1.54
kPa
273.15
Excess ...
Pvap
1.53
kPa
273.15
Isother...
Pvap
1.55
kPa
273.27
Isother...
Pvap
2.76
kPa
283.15
Isother...
Pvap
2.77
kPa
283.21
Isother...
Pvap
3.63
kPa
288.15
Experim...
Pvap
4.76
kPa
293.15
Excess ...
Pvap
4.74
kPa
293.15
Isother...
Pvap
4.77
kPa
293.25
Isother...
Pvap
6.14
kPa
298.15
Excess ...
Pvap
6.09
kPa
298.15
Experim...
Pvap
6.10
kPa
298.15
Thermop...
Pvap
6.10
kPa
298.15
Isother...
Pvap
7.81
kPa
303.15
Isother...
Pvap
7.90
kPa
303.15
Bubble ...
Pvap
7.83
kPa
303.15
Excess ...
Pvap
7.92
kPa
303.15
Measure...
Pvap
7.79
kPa
303.15
Excess ...
Pvap
7.79
kPa
303.15
Isother...
Pvap
7.79
kPa
303.15
Measure...
Pvap
7.87
kPa
303.15
Phase e...
Pvap
8.32
kPa
305.26
Measure...
Pvap
9.85
kPa
308.15
Measure...
Pvap
9.87
kPa
308.15
Experim...
Pvap
10.55
kPa
310.22
Measure...
Pvap
12.41
kPa
313.12
Isother...
Pvap
12.39
kPa
313.15
Excess ...
Pvap
12.40
kPa
313.15
Bubble ...
Pvap
12.33
kPa
313.15
Vapor-L...
Pvap
12.24
kPa
313.15
Measure...
Pvap
12.33
kPa
313.15
Vapor L...
Pvap
12.33
kPa
313.15
Phase e...
Pvap
12.34
kPa
313.15
Measure...
Pvap
12.32
kPa
313.15
Excess ...
Pvap
12.34
kPa
313.15
Phase e...
Pvap
12.31
kPa
313.15
Thermod...
Pvap
12.32
kPa
313.15
Isother...
Pvap
13.09
kPa
314.93
Measure...
Pvap
14.07
kPa
316.50
Measure...
Pvap
15.33
kPa
318.15
Measure...
Pvap
16.19
kPa
319.71
Measure...
Pvap
18.98
kPa
323.10
Isother...
Pvap
18.85
kPa
323.15
Excess ...
Pvap
18.90
kPa
323.15
Measure...
Pvap
19.00
kPa
323.15
Bubble ...
Pvap
18.95
kPa
323.15
Phase e...
Pvap
18.91
kPa
323.15
Measure...
Pvap
18.85
kPa
323.15
Isother...
Pvap
18.96
kPa
323.15
Excess ...
Pvap
19.10
kPa
323.62
Measure...
Pvap
20.00
kPa
324.56
Measure...
Pvap
21.45
kPa
326.44
Measure...
Pvap
23.04
kPa
328.15
Isother...
Pvap
23.79
kPa
329.04
Measure...
Pvap
26.15
kPa
331.39
Vapor L...
Pvap
26.14
kPa
331.48
Measure...
Pvap
26.49
kPa
331.82
Isobari...
Pvap
28.13
kPa
333.07
Isother...
Pvap
28.14
kPa
333.15
Excess ...
Pvap
27.98
kPa
333.15
Excess ...
Pvap
28.20
kPa
333.15
Bubble ...
Pvap
27.99
kPa
333.15
Isother...
Pvap
27.97
kPa
333.21
Measure...
Pvap
29.69
kPa
334.81
Isobari...
Pvap
30.59
kPa
335.45
Vapor L...
Pvap
30.51
kPa
335.50
Measure...
Pvap
32.24
kPa
336.95
Isobari...
Pvap
32.84
kPa
337.48
Measure...
Pvap
35.53
kPa
339.56
Measure...
Pvap
35.66
kPa
339.70
Isobari...
Pvap
37.87
kPa
341.35
Measure...
Pvap
38.89
kPa
341.94
Vapor L...
Pvap
40.00
kPa
342.77
Determi...
Pvap
40.12
kPa
342.96
Measure...
Pvap
40.62
kPa
343.04
Isother...
Pvap
40.64
kPa
343.15
Excess ...
Pvap
40.43
kPa
343.15
Isother...
Pvap
40.43
kPa
343.15
Excess ...
Pvap
40.60
kPa
343.15
Bubble ...
Pvap
42.35
kPa
344.47
Measure...
Pvap
42.88
kPa
344.76
Isobari...
Pvap
44.75
kPa
346.04
Measure...
Pvap
46.80
kPa
347.16
Vapor L...
Pvap
46.71
kPa
347.28
Measure...
Pvap
47.80
kPa
347.85
Isobari...
Pvap
49.09
kPa
348.72
Measure...
Pvap
50.62
kPa
349.53
Isobari...
Pvap
50.97
kPa
349.68
Vapor L...
Pvap
51.49
kPa
350.12
Measure...
Pvap
53.33
kPa
351.08
Determi...
Pvap
53.30
kPa
351.14
Isobari...
Pvap
53.41
kPa
351.21
Measure...
Pvap
55.76
kPa
352.49
Measure...
Pvap
56.20
kPa
352.58
Vapor L...
Pvap
57.56
kPa
353.01
Isother...
Pvap
57.10
kPa
353.15
Bubble ...
Pvap
56.99
kPa
353.15
Isother...
Pvap
57.09
kPa
353.15
Vapor L...
Pvap
57.27
kPa
353.15
Excess ...
Pvap
57.88
kPa
353.62
Measure...
Pvap
58.57
kPa
353.90
Isobari...
Pvap
60.00
kPa
354.63
Vapor L...
Pvap
60.00
kPa
354.72
Isobari...
Pvap
60.18
kPa
354.79
Measure...
Pvap
63.11
kPa
356.25
Measure...
Pvap
63.98
kPa
356.61
Isobari...
Pvap
64.60
kPa
356.78
Vapor L...
Pvap
66.42
kPa
357.84
Measure...
Pvap
66.66
kPa
357.85
Determi...
Pvap
67.99
kPa
358.49
Isobari...
Pvap
68.27
kPa
358.68
Measure...
Pvap
70.24
kPa
359.38
Vapor L...
Pvap
71.15
kPa
359.98
Measure...
Pvap
74.25
kPa
361.33
Measure...
Pvap
75.87
kPa
362.03
Isobari...
Pvap
76.47
kPa
362.11
Vapor L...
Pvap
76.55
kPa
362.30
Measure...
Pvap
78.94
kPa
363.15
Excess ...
Pvap
78.59
kPa
363.15
Isother...
Pvap
79.00
kPa
363.32
Measure...
Pvap
79.55
kPa
363.44
Isobari...
Pvap
79.99
kPa
363.64
Determi...
Pvap
80.00
kPa
363.67
Isobari...
Pvap
80.00
kPa
363.74
Isobari...
Pvap
81.28
kPa
364.24
Measure...
Pvap
81.76
kPa
364.36
Isobari...
Pvap
83.45
kPa
364.95
Vapor L...
Pvap
84.05
kPa
365.32
Measure...
Pvap
85.00
kPa
365.65
Experim...
Pvap
86.30
kPa
366.20
Measure...
Pvap
86.56
kPa
366.23
Isobari...
Pvap
88.10
kPa
366.87
Measure...
Pvap
88.40
kPa
366.87
Vapor L...
Pvap
91.09
kPa
367.97
Measure...
Pvap
93.32
kPa
368.70
Determi...
Pvap
93.46
kPa
368.83
Measure...
Pvap
94.00
kPa
368.85
Vapor L...
Pvap
96.33
kPa
369.84
Measure...
Pvap
98.98
kPa
370.85
Measure...
Pvap
101.30
kPa
370.97
A New T...
Pvap
100.00
kPa
371.11
Measure...
Pvap
100.00
kPa
371.20
Isobari...
Pvap
101.30
kPa
371.28
Vapor L...
Pvap
100.68
kPa
371.35
Measure...
Pvap
101.30
kPa
371.35
Measure...
Pvap
101.30
kPa
371.47
Isobari...
Pvap
101.30
kPa
371.53
Isobari...
Pvap
101.32
kPa
371.56
Measure...
Pvap
100.00
kPa
371.58
Isobari...
Pvap
101.46
kPa
371.66
Isobari...
Pvap
102.90
kPa
372.08
Vapor P...
Pvap
103.92
kPa
372.42
Measure...
Pvap
106.48
kPa
373.25
Measure...
Pvap
108.71
kPa
373.98
Measure...
Pvap
110.39
kPa
374.50
Vapor P...
Pvap
111.77
kPa
374.93
Measure...
Pvap
113.35
kPa
375.41
Measure...
Pvap
116.21
kPa
376.29
Measure...
Pvap
119.14
kPa
377.17
Measure...
Pvap
120.32
kPa
377.51
Measure...
Pvap
120.89
kPa
377.68
Vapor P...
Pvap
123.70
kPa
378.49
Measure...
Pvap
126.80
kPa
379.37
Measure...
Pvap
130.00
kPa
380.26
Measure...
Pvap
132.04
kPa
380.83
Measure...
Pvap
145.56
kPa
384.39
Vapor P...
Pvap
166.41
kPa
389.41
Vapor P...
Pvap
182.39
kPa
392.89
Measure...
Pvap
185.50
kPa
393.58
Vapor P...
Pvap
186.60
kPa
393.79
Measure...
Pvap
189.67
kPa
394.43
Measure...
Pvap
192.97
kPa
395.10
Measure...
Pvap
196.04
kPa
395.73
Measure...
Pvap
197.85
kPa
396.09
Measure...
Pvap
199.97
kPa
396.50
Measure...
Pvap
200.79
kPa
396.70
Vapor P...
Pvap
224.89
kPa
401.26
Vapor P...
Pvap
248.92
kPa
405.44
Vapor P...
Pvap
275.09
kPa
409.66
Vapor P...
Pvap
302.76
kPa
413.80
Vapor P...
Pvap
341.76
kPa
419.17
Vapor P...
Pvap
378.80
kPa
423.85
Vapor P...
Pvap
420.15
kPa
428.69
Vapor P...
Pvap
477.00
kPa
433.15
In Situ...
Pvap
467.65
kPa
433.81
Vapor P...
Pvap
518.27
kPa
438.86
Vapor P...
Pvap
587.00
kPa
443.15
In Situ...
Pvap
568.27
kPa
443.50
Vapor P...
Pvap
619.76
kPa
447.95
Vapor P...
Pvap
666.97
kPa
451.80
Vapor P...
Pvap
703.00
kPa
453.15
In Situ...
Pvap
726.16
kPa
456.35
Vapor P...
Pvap
773.29
kPa
459.78
Vapor P...
Pvap
850.62
kPa
465.07
Vapor P...
Pvap
925.23
kPa
469.84
Vapor P...
Pvap
980.00
kPa
473.10
A novel...
Pvap
980.00
kPa
473.20
A novel...
Pvap
960.00
kPa
473.30
A novel...
Pvap
983.90
kPa
473.39
Vapor P...
Pvap
1030.55
kPa
476.11
Vapor P...
Pvap
1092.41
kPa
479.57
Vapor P...
Pvap
1169.38
kPa
483.67
Vapor P...
Pvap
1242.28
kPa
487.36
Vapor P...
Pvap
1313.39
kPa
490.81
Vapor P...
Pvap
1384.19
kPa
494.11
Vapor P...
Pvap
1443.40
kPa
496.77
Vapor P...
Pvap
1460.00
kPa
498.20
A novel...
Pvap
1490.00
kPa
498.20
A novel...
Pvap
1470.00
kPa
498.20
A novel...
Pvap
1518.18
kPa
500.01
Vapor P...
Pvap
1604.13
kPa
503.59
Vapor P...
Pvap
1699.51
kPa
507.39
Vapor P...
Pvap
1793.01
kPa
510.95
Vapor P...
Pvap
1911.60
kPa
515.27
Vapor P...
Pvap
2019.09
kPa
518.99
Vapor P...
Pvap
2116.11
kPa
522.22
Vapor P...
Pvap
2170.00
kPa
523.20
A novel...
Pvap
2190.00
kPa
523.20
A novel...
Pvap
2180.00
kPa
523.20
A novel...
Pvap
2219.70
kPa
525.53
Vapor P...
Pvap
2309.81
kPa
528.30
Vapor P...
Pvap
2416.50
kPa
531.47
Vapor P...
Pvap
2525.68
kPa
534.57
Vapor P...
Pvap
2621.76
kPa
537.20
Vapor P...
n 0
[1.37197; 1.53800]
[293.10; 323.15]
n 0
1.38820
293.10
(Liquid...
n 0
1.50240
293.10
(Liquid...
n 0
1.38760
293.15
Limitin...
n 0
1.38760
293.15
Bubble ...
n 0
1.38780
293.15
Infinit...
n 0
1.38780
293.15
Isother...
n 0
1.38780
293.15
A novel...
n 0
1.38720
293.15
Physica...
n 0
1.38776
293.15
Mixing ...
n 0
1.38770
293.15
Vapor L...
n 0
1.38730
293.20
Liquid ...
n 0
1.38850
298.10
Excess ...
n 0
1.38530
298.15
Liquid-...
n 0
1.38520
298.15
Multipr...
n 0
1.38530
298.15
Measure...
n 0
1.38600
298.15
Excess ...
n 0
1.38550
298.15
Physica...
n 0
1.38517
298.15
Mixing ...
n 0
1.38530
298.15
Improve...
n 0
1.38517
298.15
Thiophe...
n 0
1.38530
298.15
Thermod...
n 0
1.38520
298.15
Molar h...
n 0
1.38515
298.15
Extract...
n 0
1.38529
298.15
Applica...
n 0
1.38529
298.15
1-Alkyl...
n 0
1.38515
298.15
Separat...
n 0
1.38510
298.15
Bubble-...
n 0
1.38517
298.15
A study...
n 0
1.38520
298.15
Isother...
n 0
1.38527
298.15
Measure...
n 0
1.38517
298.15
Phase b...
n 0
1.38510
298.15
Bubble ...
n 0
1.38530
298.15
Vapor-L...
n 0
1.53800
298.15
Thermod...
n 0
1.38540
298.15
Solubil...
n 0
1.38530
298.15
Activit...
n 0
1.38511
298.15
KDB
n 0
1.38515
298.15
Extract...
n 0
1.38510
298.20
(Liquid...
n 0
1.38500
298.20
Liquid-...
n 0
1.38259
303.15
Experim...
n 0
1.38360
303.15
Excess ...
n 0
1.38270
303.15
Physica...
n 0
1.38440
303.15
(Liquid...
n 0
1.38258
303.15
Mixing ...
n 0
1.38100
308.15
Excess ...
n 0
1.37995
308.15
Experim...
n 0
1.37731
313.15
Experim...
n 0
1.37480
318.15
Multipr...
n 0
1.37463
318.15
Experim...
n 0
1.37480
318.15
Thermod...
n 0
1.37197
323.15
Experim...
ρl
[626.26; 700.67]
kg/m3
[273.15; 358.15]
ρl
700.67
kg/m3
273.15
Experim...
ρl
696.57
kg/m3
278.15
Experim...
ρl
692.44
kg/m3
283.15
Density...
ρl
692.40
kg/m3
283.15
Experim...
ρl
688.59
kg/m3
288.15
Excess ...
ρl
688.13
kg/m3
288.15
Densiti...
ρl
688.25
kg/m3
288.15
Excess ...
ρl
689.00
kg/m3
288.15
Effect ...
ρl
688.20
kg/m3
288.15
Experim...
ρl
687.95
kg/m3
288.15
Experim...
ρl
687.95
kg/m3
288.15
Densiti...
ρl
684.00
kg/m3
293.00
KDB
ρl
683.85
kg/m3
293.15
Density...
ρl
683.78
kg/m3
293.15
Surface...
ρl
683.93
kg/m3
293.15
Densiti...
ρl
683.67
kg/m3
293.15
Density...
ρl
683.91
kg/m3
293.15
Excess ...
ρl
683.73
kg/m3
293.15
Densiti...
ρl
683.85
kg/m3
293.15
Thermod...
ρl
683.99
kg/m3
293.15
Experim...
ρl
684.05
kg/m3
293.15
Density...
ρl
685.00
kg/m3
293.15
Effect ...
ρl
683.89
kg/m3
293.15
Density...
ρl
683.73
kg/m3
293.15
Experim...
ρl
684.00
kg/m3
293.15
Densiti...
ρl
683.99
kg/m3
293.15
Excess ...
ρl
683.82
kg/m3
293.15
Thermop...
ρl
683.53
kg/m3
293.20
Isobari...
ρl
683.82
kg/m3
293.22
Thermod...
ρl
679.74
kg/m3
298.15
Excess ...
ρl
679.60
kg/m3
298.15
Thermod...
ρl
679.66
kg/m3
298.15
Thermod...
ρl
690.60
kg/m3
298.15
Ternary...
ρl
681.48
kg/m3
298.15
Quatern...
ρl
679.61
kg/m3
298.15
Density...
ρl
680.02
kg/m3
298.15
Binary ...
ρl
679.75
kg/m3
298.15
Experim...
ρl
680.00
kg/m3
298.15
Liquid-...
ρl
679.71
kg/m3
298.15
Thermod...
ρl
679.43
kg/m3
298.15
Liquid-...
ρl
679.59
kg/m3
298.15
Thermop...
ρl
683.80
kg/m3
298.15
Liquid-...
ρl
679.63
kg/m3
298.15
Thermod...
ρl
679.50
kg/m3
298.15
Vapor-L...
ρl
679.54
kg/m3
298.15
Thermod...
ρl
679.50
kg/m3
298.15
Vapor-L...
ρl
680.17
kg/m3
298.15
Excess ...
ρl
679.48
kg/m3
298.15
Separat...
ρl
679.40
kg/m3
298.15
Viscosi...
ρl
679.47
kg/m3
298.15
Solvent...
ρl
679.54
kg/m3
298.15
Experim...
ρl
680.00
kg/m3
298.15
Phase d...
ρl
679.71
kg/m3
298.15
Thermod...
ρl
679.91
kg/m3
298.15
Volumet...
ρl
679.00
kg/m3
298.15
Liquid-...
ρl
679.60
kg/m3
298.15
Vapour ...
ρl
679.71
kg/m3
298.15
Densiti...
ρl
679.55
kg/m3
298.15
Phase b...
ρl
683.80
kg/m3
298.15
Liquid-...
ρl
679.57
kg/m3
298.15
Applica...
ρl
679.60
kg/m3
298.15
Cation ...
ρl
679.57
kg/m3
298.15
Capacit...
ρl
679.49
kg/m3
298.15
Topolog...
ρl
679.64
kg/m3
298.15
Density...
ρl
679.78
kg/m3
298.15
Density...
ρl
679.48
kg/m3
298.15
Separat...
ρl
679.54
kg/m3
298.15
Effect ...
ρl
679.57
kg/m3
298.15
Quatern...
ρl
679.54
kg/m3
298.15
Extract...
ρl
679.57
kg/m3
298.15
(Liquid...
ρl
679.50
kg/m3
298.15
Fully a...
ρl
680.00
kg/m3
298.15
Effect ...
ρl
679.49
kg/m3
298.15
Densiti...
ρl
679.79
kg/m3
298.15
Excess ...
ρl
679.63
kg/m3
298.15
Thermod...
ρl
680.00
kg/m3
298.15
Effect ...
ρl
679.54
kg/m3
298.15
Thermod...
ρl
679.54
kg/m3
298.15
Excess ...
ρl
679.49
kg/m3
298.15
Excess ...
ρl
679.49
kg/m3
298.15
Experim...
ρl
679.70
kg/m3
298.15
Densiti...
ρl
679.71
kg/m3
298.15
Liquid-...
ρl
679.46
kg/m3
298.15
Conform...
ρl
679.63
kg/m3
298.15
Thermod...
ρl
679.75
kg/m3
298.16
Thermod...
ρl
682.30
kg/m3
298.20
Ternary...
ρl
679.86
kg/m3
298.20
Apparen...
ρl
675.75
kg/m3
301.62
Density...
ρl
675.84
kg/m3
303.15
Excess ...
ρl
675.63
kg/m3
303.15
Volumet...
ρl
675.54
kg/m3
303.15
Density...
ρl
675.23
kg/m3
303.15
Densiti...
ρl
675.41
kg/m3
303.15
Excess ...
ρl
675.53
kg/m3
303.15
Thermod...
ρl
675.23
kg/m3
303.15
Experim...
ρl
676.00
kg/m3
303.15
Effect ...
ρl
675.47
kg/m3
303.15
Densiti...
ρl
675.37
kg/m3
303.15
Density...
ρl
675.35
kg/m3
303.15
Density...
ρl
675.40
kg/m3
303.15
Effect ...
ρl
675.31
kg/m3
303.15
Thermop...
ρl
675.49
kg/m3
303.15
Experim...
ρl
675.51
kg/m3
303.17
Thermod...
ρl
671.07
kg/m3
308.15
Density...
ρl
671.19
kg/m3
308.15
Experim...
ρl
671.33
kg/m3
308.15
Volumet...
ρl
671.20
kg/m3
308.15
Densiti...
ρl
671.12
kg/m3
308.15
Excess ...
ρl
670.94
kg/m3
308.15
Densiti...
ρl
670.94
kg/m3
308.15
Experim...
ρl
671.02
kg/m3
308.15
Thermop...
ρl
671.05
kg/m3
308.15
Density...
ρl
671.21
kg/m3
308.17
Thermod...
ρl
667.37
kg/m3
310.71
Density...
ρl
666.73
kg/m3
313.15
Density...
ρl
666.92
kg/m3
313.15
Excess ...
ρl
666.80
kg/m3
313.15
Effect ...
ρl
666.89
kg/m3
313.15
Densiti...
ρl
666.89
kg/m3
313.15
Excess ...
ρl
666.87
kg/m3
313.15
Experim...
ρl
665.84
kg/m3
313.15
Excess ...
ρl
668.00
kg/m3
313.15
Effect ...
ρl
666.62
kg/m3
313.15
Experim...
ρl
667.01
kg/m3
313.15
Volumet...
ρl
666.74
kg/m3
313.15
Density...
ρl
666.62
kg/m3
313.15
Densiti...
ρl
666.68
kg/m3
313.15
Thermop...
ρl
666.97
kg/m3
313.17
Thermod...
ρl
662.27
kg/m3
318.15
Experim...
ρl
662.38
kg/m3
318.15
Density...
ρl
662.65
kg/m3
318.15
Volumet...
ρl
662.38
kg/m3
318.15
Density...
ρl
662.52
kg/m3
318.15
Experim...
ρl
662.27
kg/m3
318.15
Densiti...
ρl
662.55
kg/m3
318.15
Densiti...
ρl
662.67
kg/m3
318.18
Thermod...
ρl
659.85
kg/m3
319.85
Density...
ρl
658.26
kg/m3
323.15
Volumet...
ρl
658.13
kg/m3
323.15
Experim...
ρl
657.90
kg/m3
323.15
Densiti...
ρl
657.90
kg/m3
323.15
Experim...
ρl
660.00
kg/m3
323.15
Effect ...
ρl
657.98
kg/m3
323.15
Density...
ρl
658.19
kg/m3
323.15
Densiti...
ρl
657.99
kg/m3
323.15
Density...
ρl
657.70
kg/m3
323.15
Effect ...
ρl
653.71
kg/m3
328.15
Experim...
ρl
653.72
kg/m3
328.15
Excess ...
ρl
653.57
kg/m3
328.15
Density...
ρl
653.79
kg/m3
328.15
Densiti...
ρl
651.92
kg/m3
329.04
Density...
ρl
648.40
kg/m3
333.15
Effect ...
ρl
651.00
kg/m3
333.15
Effect ...
ρl
649.33
kg/m3
333.15
Densiti...
ρl
649.11
kg/m3
333.15
Density...
ρl
649.24
kg/m3
333.15
Experim...
ρl
644.74
kg/m3
338.15
Experim...
ρl
644.60
kg/m3
338.15
Density...
ρl
644.84
kg/m3
338.15
Densiti...
ρl
644.77
kg/m3
338.15
Excess ...
ρl
644.32
kg/m3
338.26
Density...
ρl
642.00
kg/m3
343.15
Effect ...
ρl
640.29
kg/m3
343.15
Densiti...
ρl
640.19
kg/m3
343.15
Experim...
ρl
635.91
kg/m3
347.53
Density...
ρl
635.60
kg/m3
348.15
Experim...
ρl
635.63
kg/m3
348.15
Excess ...
ρl
630.95
kg/m3
353.15
Experim...
ρl
627.85
kg/m3
356.84
Density...
ρl
626.26
kg/m3
358.15
Experim...
Δfus S
[76.81; 78.81]
J/mol×K
[182.20; 182.70]
Δfus S
77.73
J/mol×K
182.20
NIST
Δfus S
77.73
J/mol×K
182.20
NIST
Δfus S
76.93
J/mol×K
182.52
NIST
Δfus S
76.89
J/mol×K
182.55
NIST
Δfus S
76.89
J/mol×K
182.55
NIST
Δfus S
77.02
J/mol×K
182.56
NIST
Δfus S
76.81
J/mol×K
182.56
NIST
Δfus S
78.81
J/mol×K
182.56
NIST
Δfus S
76.81
J/mol×K
182.56
NIST
Δfus S
76.96
J/mol×K
182.59
NIST
Δfus S
77.00
J/mol×K
182.70
NIST
csound,fluid
[111.10; 1154.11]
m/s
[292.70; 536.15]
csound,fluid
1154.11
m/s
292.70
Thermod...
csound,fluid
1151.92
m/s
293.13
Excess ...
csound,fluid
1152.60
m/s
293.15
Excess ...
csound,fluid
1152.20
m/s
293.15
Excess ...
csound,fluid
1131.06
m/s
298.00
Thermod...
csound,fluid
1130.26
m/s
298.12
Excess ...
csound,fluid
1130.90
m/s
298.15
Excess ...
csound,fluid
1131.00
m/s
298.15
Excess ...
csound,fluid
1108.00
m/s
302.15
Measure...
csound,fluid
1109.45
m/s
302.98
Thermod...
csound,fluid
1108.78
m/s
303.10
Excess ...
csound,fluid
1109.60
m/s
303.15
Excess ...
csound,fluid
1109.10
m/s
303.15
Excess ...
csound,fluid
1087.42
m/s
308.06
Thermod...
csound,fluid
1087.47
m/s
308.07
Excess ...
csound,fluid
1088.10
m/s
308.15
Excess ...
csound,fluid
1088.20
m/s
308.15
Excess ...
csound,fluid
1066.28
m/s
313.03
Excess ...
csound,fluid
1067.10
m/s
313.15
Excess ...
csound,fluid
1066.90
m/s
313.15
Excess ...
csound,fluid
1064.29
m/s
313.45
Thermod...
csound,fluid
1042.00
m/s
318.15
Measure...
csound,fluid
1043.90
m/s
318.33
Excess ...
csound,fluid
981.50
m/s
333.15
Measure...
csound,fluid
921.10
m/s
348.15
Measure...
csound,fluid
861.20
m/s
363.15
Measure...
csound,fluid
801.60
m/s
378.15
Measure...
csound,fluid
742.30
m/s
393.15
Measure...
csound,fluid
683.10
m/s
408.15
Measure...
csound,fluid
643.50
m/s
418.15
Measure...
csound,fluid
603.90
m/s
428.15
Measure...
csound,fluid
564.00
m/s
438.15
Measure...
csound,fluid
523.90
m/s
448.15
Measure...
csound,fluid
503.60
m/s
453.15
Measure...
csound,fluid
483.30
m/s
458.15
Measure...
csound,fluid
462.80
m/s
463.15
Measure...
csound,fluid
442.20
m/s
468.15
Measure...
csound,fluid
421.30
m/s
473.15
Measure...
csound,fluid
400.30
m/s
478.15
Measure...
csound,fluid
379.00
m/s
483.15
Measure...
csound,fluid
357.40
m/s
488.15
Measure...
csound,fluid
335.40
m/s
493.15
Measure...
csound,fluid
313.00
m/s
498.15
Measure...
csound,fluid
290.10
m/s
503.15
Measure...
csound,fluid
266.60
m/s
508.15
Measure...
csound,fluid
242.40
m/s
513.15
Measure...
csound,fluid
217.30
m/s
518.15
Measure...
csound,fluid
190.90
m/s
523.15
Measure...
csound,fluid
162.70
m/s
528.15
Measure...
csound,fluid
131.90
m/s
533.15
Measure...
csound,fluid
111.10
m/s
536.15
Measure...
γ
[0.01; 0.02]
N/m
[277.93; 358.12]
γ
0.02
N/m
277.93
Surface...
γ
0.02
N/m
282.83
Surface...
γ
0.02
N/m
283.15
Experim...
γ
0.02
N/m
287.81
Surface...
γ
0.02
N/m
288.15
Interfa...
γ
0.02
N/m
288.15
Density...
γ
0.02
N/m
292.81
Surface...
γ
0.02
N/m
293.15
Surface...
γ
0.02
N/m
293.15
Density...
γ
0.02
N/m
293.15
Experim...
γ
0.02
N/m
293.15
Surface...
γ
0.02
N/m
293.15
Surface...
γ
0.02
N/m
293.20
KDB
γ
0.02
N/m
297.82
Surface...
γ
0.02
N/m
298.13
Surface...
γ
0.02
N/m
298.15
Density...
γ
0.02
N/m
298.15
Surface...
γ
0.02
N/m
298.15
Interfa...
γ
0.02
N/m
298.15
Surface...
γ
0.02
N/m
298.15
Surface...
γ
0.02
N/m
302.83
Surface...
γ
0.02
N/m
303.15
Density...
γ
0.02
N/m
303.15
Surface...
γ
0.02
N/m
303.15
Surface...
γ
0.02
N/m
303.15
Experim...
γ
0.02
N/m
303.15
Surface...
γ
0.02
N/m
303.18
Surface...
γ
0.02
N/m
303.49
Surface...
γ
0.02
N/m
307.86
Surface...
γ
0.02
N/m
308.12
Surface...
γ
0.02
N/m
308.15
Interfa...
γ
0.02
N/m
308.15
Surface...
γ
0.02
N/m
308.15
Surface...
γ
0.02
N/m
308.15
Surface...
γ
0.02
N/m
308.15
Density...
γ
0.02
N/m
312.86
Surface...
γ
0.02
N/m
313.13
Surface...
γ
0.02
N/m
313.15
Surface...
γ
0.02
N/m
313.15
Experim...
γ
0.02
N/m
313.15
Surface...
γ
0.02
N/m
313.15
Surface...
γ
0.02
N/m
313.18
Surface...
γ
0.02
N/m
317.86
Surface...
γ
0.02
N/m
318.15
Surface...
γ
0.02
N/m
318.15
Surface...
γ
0.02
N/m
318.15
Surface...
γ
0.02
N/m
318.15
Interfa...
γ
0.02
N/m
318.17
Surface...
γ
0.02
N/m
318.49
Surface...
γ
0.02
N/m
322.86
Surface...
γ
0.02
N/m
323.15
Surface...
γ
0.02
N/m
323.15
Surface...
γ
0.02
N/m
323.15
Experim...
γ
0.02
N/m
323.15
Surface...
γ
0.02
N/m
323.20
Surface...
γ
0.02
N/m
327.88
Surface...
γ
0.02
N/m
328.12
Surface...
γ
0.02
N/m
328.15
Interfa...
γ
0.02
N/m
328.15
Surface...
γ
0.02
N/m
332.91
Surface...
γ
0.02
N/m
333.13
Surface...
γ
0.02
N/m
337.88
Surface...
γ
0.02
N/m
338.14
Surface...
γ
0.02
N/m
342.92
Surface...
γ
0.02
N/m
343.12
Surface...
γ
0.01
N/m
348.13
Surface...
γ
0.01
N/m
358.12
Surface...
Pressure Dependent Properties
Datasets
Molar heat capacity at constant pressure, J/K/mol (1)
Viscosity, Pa*s (6)
Mass density, kg/m3 (13)
Speed of sound, m/s (2)
Molar heat capacity at constant pressure, J/K/mol
Fixed
Measured
Temperature, K - Liquid
Pressure, kPa - Liquid
Molar heat capacity at constant pressure, J/K/mol - Liquid
273.15
100.00
216.20
273.15
5000.00
213.10
273.15
10000.00
210.90
273.15
15000.00
208.10
273.15
20000.00
207.20
293.15
100.00
224.10
293.15
5000.00
223.00
293.15
10000.00
218.20
293.15
15000.00
216.80
293.15
20000.00
214.40
313.15
100.00
233.80
313.15
5000.00
230.30
313.15
10000.00
226.20
313.15
15000.00
223.10
313.15
20000.00
221.60
333.15
100.00
241.90
333.15
5000.00
238.70
333.15
10000.00
235.00
333.15
15000.00
232.00
333.15
20000.00
229.30
Reference
Viscosity, Pa*s
Fixed
Measured
Temperature, K - Liquid
Pressure, kPa - Liquid
Viscosity, Pa*s - Liquid
298.15
98.00
0.0004
298.15
24510.00
0.0005
298.15
49030.00
0.0006
298.15
98060.00
0.0008
298.15
147100.00
0.0011
298.15
196130.00
0.0015
298.15
245160.00
0.0019
303.15
98.00
0.0004
303.15
24510.00
0.0005
303.15
49030.00
0.0006
303.15
98060.00
0.0008
303.15
147100.00
0.0011
303.15
196130.00
0.0014
303.15
245160.00
0.0017
323.11
49030.00
0.0005
323.13
24510.00
0.0004
323.20
98060.00
0.0007
323.20
147100.00
0.0009
323.21
196130.00
0.0011
323.25
98.00
0.0003
323.25
245160.00
0.0014
362.80
147100.00
0.0006
362.83
98060.00
0.0005
362.85
49030.00
0.0004
362.87
196130.00
0.0008
362.92
98.00
0.0002
362.98
245160.00
0.0010
363.07
24510.00
0.0003
391.93
147100.00
0.0005
392.00
196130.00
0.0007
392.00
245160.00
0.0008
392.04
98060.00
0.0004
393.01
24510.00
0.0002
393.14
49030.00
0.0003
422.17
196130.00
0.0006
422.24
98060.00
0.0003
422.26
147100.00
0.0004
422.58
24510.00
0.0002
422.60
49030.00
0.0002
423.04
245160.00
0.0007
452.91
245160.00
0.0006
453.04
196130.00
0.0005
453.10
147100.00
0.0004
453.16
98060.00
0.0003
453.24
49030.00
0.0002
453.40
24510.00
0.0002
470.10
49030.00
0.0002
470.19
24510.00
0.0002
470.19
98060.00
0.0003
470.19
147100.00
0.0004
470.57
196130.00
0.0005
470.61
245160.00
0.0005
Reference
Fixed
Measured
Temperature, K - Liquid
Pressure, kPa - Liquid
Viscosity, Pa*s - Liquid
293.15
20000.00
0.0005
293.15
40000.00
0.0006
293.15
60000.00
0.0007
293.15
80000.00
0.0008
293.15
100000.00
0.0009
313.15
20000.00
0.0004
313.15
40000.00
0.0005
313.15
60000.00
0.0006
313.15
80000.00
0.0007
313.15
100000.00
0.0008
333.15
20000.00
0.0003
333.15
40000.00
0.0004
333.15
60000.00
0.0005
333.15
80000.00
0.0005
333.15
100000.00
0.0006
353.15
20000.00
0.0003
353.15
40000.00
0.0003
353.15
60000.00
0.0004
353.15
80000.00
0.0005
353.15
100000.00
0.0005
Reference
Fixed
Measured
Temperature, K - Liquid
Pressure, kPa - Liquid
Viscosity, Pa*s - Liquid
303.15
101.33
0.0004
Reference
Fixed
Measured
Temperature, K - Liquid
Pressure, kPa - Liquid
Viscosity, Pa*s - Liquid
298.24
100.00
0.0004
306.79
5000.00
0.0004
306.79
10000.00
0.0004
323.93
100.00
0.0003
337.54
5000.00
0.0003
337.54
10000.00
0.0003
348.64
100.00
0.0002
369.35
5000.00
0.0002
369.35
10000.00
0.0002
407.85
5000.00
0.0002
407.85
10000.00
0.0002
449.64
5000.00
0.0001
449.64
10000.00
0.0001
473.54
5000.00
0.0001
473.54
10000.00
0.0001
Reference
Fixed
Measured
Temperature, K - Liquid
Pressure, kPa - Liquid
Viscosity, Pa*s - Liquid
293.15
5000.00
0.0004
293.15
10000.00
0.0005
293.15
20000.00
0.0005
293.15
30000.00
0.0006
293.15
40000.00
0.0006
293.15
60000.00
0.0007
293.15
80000.00
0.0008
293.15
100000.00
0.0009
293.15
120000.00
0.0010
313.15
5000.00
0.0004
313.15
10000.00
0.0004
313.15
20000.00
0.0004
313.15
30000.00
0.0005
313.15
40000.00
0.0005
313.15
60000.00
0.0006
313.15
80000.00
0.0006
313.15
100000.00
0.0007
313.15
120000.00
0.0008
Reference
Fixed
Measured
Temperature, K - Liquid
Pressure, kPa - Liquid
Viscosity, Pa*s - Liquid
303.15
100.00
0.0004
303.15
1000.00
0.0004
303.15
5000.00
0.0004
303.15
10000.00
0.0004
303.15
15000.00
0.0004
303.15
20000.00
0.0004
303.15
25000.00
0.0005
303.15
30000.00
0.0005
303.15
35000.00
0.0005
303.15
40000.00
0.0005
303.15
45000.00
0.0006
303.15
50000.00
0.0006
303.15
55000.00
0.0006
303.15
60000.00
0.0006
313.15
100.00
0.0003
313.15
1000.00
0.0003
313.15
5000.00
0.0003
313.15
10000.00
0.0004
313.15
15000.00
0.0004
313.15
20000.00
0.0004
313.15
25000.00
0.0004
313.15
30000.00
0.0004
313.15
35000.00
0.0005
313.15
40000.00
0.0005
313.15
45000.00
0.0005
313.15
50000.00
0.0005
313.15
55000.00
0.0005
313.15
60000.00
0.0006
323.15
100.00
0.0003
323.15
1000.00
0.0003
323.15
5000.00
0.0003
323.15
10000.00
0.0003
323.15
15000.00
0.0004
323.15
20000.00
0.0004
323.15
25000.00
0.0004
323.15
30000.00
0.0004
323.15
35000.00
0.0004
323.15
40000.00
0.0004
323.15
45000.00
0.0005
323.15
50000.00
0.0005
323.15
55000.00
0.0005
323.15
60000.00
0.0005
333.15
100.00
0.0003
333.15
1000.00
0.0003
333.15
5000.00
0.0003
333.15
10000.00
0.0003
333.15
15000.00
0.0003
333.15
20000.00
0.0003
333.15
25000.00
0.0004
333.15
30000.00
0.0004
333.15
35000.00
0.0004
333.15
40000.00
0.0004
333.15
45000.00
0.0004
333.15
50000.00
0.0004
333.15
55000.00
0.0005
333.15
60000.00
0.0005
343.15
100.00
0.0002
343.15
1000.00
0.0002
343.15
5000.00
0.0003
343.15
10000.00
0.0003
343.15
15000.00
0.0003
343.15
20000.00
0.0003
343.15
25000.00
0.0003
343.15
30000.00
0.0003
343.15
35000.00
0.0004
343.15
40000.00
0.0004
343.15
45000.00
0.0004
343.15
50000.00
0.0004
343.15
55000.00
0.0004
343.15
60000.00
0.0004
353.15
100.00
0.0002
353.15
1000.00
0.0002
353.15
5000.00
0.0002
353.15
10000.00
0.0003
353.15
15000.00
0.0003
353.15
20000.00
0.0003
353.15
25000.00
0.0003
353.15
30000.00
0.0003
353.15
35000.00
0.0003
353.15
40000.00
0.0003
353.15
45000.00
0.0004
353.15
50000.00
0.0004
353.15
55000.00
0.0004
353.15
60000.00
0.0004
Reference
Mass density, kg/m3
Fixed
Measured
Temperature, K - Liquid
Pressure, kPa - Liquid
Mass density, kg/m3 - Liquid
293.00
2100.00
687.2
293.00
3000.00
688.1
293.00
4000.00
688.9
293.00
5000.00
689.8
293.00
10000.00
694.0
293.00
20000.00
701.8
293.00
30000.00
708.7
293.00
40000.00
714.8
293.00
49900.00
720.8
293.00
59900.00
726.4
293.00
69900.00
731.6
293.00
79900.00
736.8
293.00
89900.00
741.5
293.00
99900.00
746.1
293.00
109900.00
750.6
293.00
119900.00
754.9
293.00
129900.00
759.2
293.00
134900.00
761.2
293.00
137400.00
762.2
313.00
2100.00
671.9
313.00
3000.00
672.9
313.00
4000.00
673.9
313.00
5000.00
674.8
313.00
10000.00
679.4
313.00
20000.00
688.0
313.00
30000.00
695.4
313.00
40000.00
702.2
313.00
49900.00
708.5
313.00
59900.00
714.3
313.00
69900.00
720.0
313.00
79900.00
725.2
313.00
89900.00
730.3
313.00
99900.00
735.1
313.00
109900.00
739.9
313.00
119900.00
744.3
313.00
129900.00
748.7
313.00
134900.00
751.0
313.00
137400.00
751.9
333.00
2100.00
654.8
333.00
3000.00
656.0
333.00
4000.00
657.7
333.00
5000.00
658.4
333.00
10000.00
663.9
333.00
20000.00
673.8
333.00
30000.00
682.3
333.00
40000.00
689.5
333.00
49900.00
696.5
333.00
59900.00
703.1
333.00
69900.00
708.9
333.00
79900.00
714.5
333.00
89900.00
720.0
333.00
99900.00
725.2
333.00
109900.00
729.8
333.00
119900.00
734.7
333.00
129900.00
739.3
333.00
134900.00
741.4
333.00
137400.00
742.6
353.00
2100.00
636.1
353.00
3000.00
637.6
353.00
4000.00
639.1
353.00
5000.00
640.4
353.00
10000.00
647.1
353.00
20000.00
658.5
353.00
30000.00
668.0
353.00
40000.00
676.7
353.00
49900.00
684.5
353.00
59900.00
691.3
353.00
69900.00
697.9
353.00
79900.00
703.8
353.00
89900.00
709.7
353.00
99900.00
715.0
353.00
109900.00
720.3
353.00
119900.00
725.3
353.00
129900.00
730.1
353.00
134900.00
732.4
353.00
137400.00
733.5
373.00
2100.00
616.9
373.00
3000.00
618.6
373.00
4000.00
620.3
373.00
5000.00
622.0
373.00
10000.00
629.9
373.00
20000.00
643.2
373.00
30000.00
654.1
373.00
40000.00
663.6
373.00
49900.00
672.0
373.00
59900.00
679.6
373.00
69900.00
686.7
373.00
79900.00
693.3
373.00
89900.00
699.4
373.00
99900.00
705.2
373.00
109900.00
710.7
373.00
119900.00
716.0
373.00
129900.00
720.9
373.00
134900.00
723.3
373.00
137400.00
724.5
393.00
2100.00
596.5
393.00
3000.00
598.7
393.00
4000.00
600.8
393.00
5000.00
602.8
393.00
10000.00
612.2
393.00
20000.00
627.8
393.00
30000.00
640.2
393.00
40000.00
650.8
393.00
49900.00
659.9
393.00
59900.00
668.3
393.00
69900.00
675.9
393.00
79900.00
682.9
393.00
89900.00
689.5
393.00
99900.00
695.7
393.00
109900.00
701.4
393.00
119900.00
706.8
393.00
129900.00
712.1
393.00
134900.00
714.7
393.00
137400.00
715.8
413.00
2100.00
574.1
413.00
3000.00
577.0
413.00
4000.00
579.6
413.00
5000.00
582.1
413.00
10000.00
593.6
413.00
20000.00
611.9
413.00
30000.00
626.0
413.00
40000.00
637.6
413.00
49900.00
647.8
413.00
59900.00
656.9
413.00
69900.00
664.7
413.00
79900.00
672.4
413.00
89900.00
679.3
413.00
99900.00
685.8
413.00
109900.00
692.2
413.00
119900.00
698.0
413.00
129900.00
703.6
413.00
134900.00
706.2
413.00
137400.00
707.4
433.00
2100.00
550.1
433.00
3000.00
553.9
433.00
4000.00
557.5
433.00
5000.00
560.7
433.00
10000.00
574.6
433.00
20000.00
595.4
433.00
30000.00
611.5
433.00
40000.00
624.3
433.00
49900.00
635.2
433.00
59900.00
644.7
433.00
69900.00
653.5
433.00
79900.00
661.6
433.00
89900.00
669.0
433.00
99900.00
676.0
433.00
109900.00
682.3
433.00
119900.00
688.5
433.00
129900.00
694.3
433.00
134900.00
697.2
433.00
137400.00
698.6
448.00
2100.00
531.1
448.00
3000.00
535.6
448.00
4000.00
539.8
448.00
5000.00
543.6
448.00
10000.00
560.0
448.00
20000.00
583.0
448.00
30000.00
600.3
448.00
40000.00
614.4
448.00
49900.00
626.2
448.00
59900.00
636.6
448.00
69900.00
646.2
448.00
79900.00
654.4
448.00
89900.00
661.8
448.00
99900.00
669.2
448.00
109900.00
675.8
448.00
119900.00
682.3
448.00
129900.00
688.4
448.00
134900.00
691.4
448.00
137400.00
692.6
468.00
2100.00
501.1
468.00
3000.00
507.8
468.00
4000.00
513.4
468.00
5000.00
518.6
468.00
10000.00
539.1
468.00
20000.00
566.5
468.00
30000.00
586.2
468.00
40000.00
601.3
468.00
49900.00
614.2
468.00
59900.00
625.3
468.00
69900.00
635.2
468.00
79900.00
644.1
468.00
89900.00
652.3
468.00
99900.00
659.9
468.00
109900.00
667.2
468.00
119900.00
673.9
468.00
129900.00
679.9
468.00
134900.00
682.8
468.00
137400.00
684.3
Reference
Fixed
Measured
Temperature, K - Liquid
Pressure, kPa - Liquid
Mass density, kg/m3 - Liquid
233.15
101.68
733.289
233.15
1104.14
733.918
233.15
2003.32
734.481
233.15
4006.02
735.714
233.15
6004.84
736.928
233.15
8009.54
738.125
233.15
9956.83
739.277
233.15
11864.20
740.377
233.15
13984.20
741.588
233.15
15994.70
742.722
233.15
17888.30
743.774
233.15
20074.10
744.977
233.15
22023.80
746.029
233.15
24017.60
747.094
233.15
25954.00
748.113
233.15
27944.50
749.147
233.15
29979.30
750.192
253.15
98.99
717.086
253.15
1101.50
717.807
253.15
2000.52
718.446
253.15
4006.34
719.85
253.15
6005.44
721.223
253.15
8147.76
722.669
253.15
10096.20
723.959
253.15
11827.30
725.088
253.15
13955.10
726.459
253.15
16060.20
727.785
253.15
18039.50
729.014
253.15
20020.00
730.22
253.15
22093.30
731.465
253.15
23827.70
732.495
253.15
25891.20
733.701
253.15
27738.70
734.762
253.15
29899.80
735.987
273.15
102.15
700.687
273.15
1101.26
701.507
273.15
2006.30
702.244
273.15
4005.43
703.841
273.15
6005.46
705.403
273.15
8197.47
707.077
273.15
10109.30
708.507
273.15
12113.70
709.976
273.15
14092.30
711.403
273.15
16115.70
712.831
273.15
18076.00
714.19
273.15
20096.30
715.565
273.15
22068.90
716.883
273.15
24101.50
718.226
273.15
25917.60
719.397
273.15
27991.30
720.718
273.15
29444.50
721.633
293.15
98.89
683.986
293.15
1104.28
684.937
293.15
2003.35
685.779
293.15
4003.02
687.611
293.15
6003.71
689.394
293.15
8007.44
691.14
293.15
10027.90
692.854
293.15
12138.70
694.603
293.15
14007.80
696.118
293.15
16160.30
697.827
293.15
18149.30
699.368
293.15
19992.10
700.756
293.15
22123.00
702.362
293.15
24036.20
703.766
293.15
25999.00
705.175
293.15
27982.80
706.576
293.15
29985.70
707.965
313.15
101.45
666.898
313.15
1102.20
667.995
313.15
2005.49
668.973
313.15
4004.53
671.086
313.15
6106.94
673.238
313.15
7941.18
675.062
313.15
9944.39
676.997
313.15
11841.20
678.793
313.15
13782.40
680.575
313.15
16032.40
682.588
313.15
17876.00
684.2
313.15
19748.40
685.804
313.15
21802.90
687.518
313.15
23828.70
689.172
313.15
25813.90
690.765
313.15
27801.40
692.324
313.15
29818.40
693.872
333.15
103.00
649.298
333.15
1105.97
650.588
333.15
2004.12
651.723
333.15
4003.59
654.18
333.15
6004.59
656.549
333.15
8005.55
658.837
333.15
9901.48
660.933
333.15
12083.40
663.274
333.15
14040.10
665.309
333.15
16005.20
667.293
333.15
17854.30
669.109
333.15
19984.70
671.149
333.15
21966.60
672.997
333.15
23925.50
674.778
333.15
25823.40
676.467
333.15
27822.80
678.205
333.15
30009.20
680.058
353.15
99.37
631.037
353.15
1182.85
632.68
353.15
2156.26
634.131
353.15
4140.73
636.982
353.15
6175.55
639.78
353.15
8138.91
642.37
353.15
10095.00
644.851
353.15
12083.30
647.284
353.15
14039.80
649.596
353.15
16039.20
651.883
353.15
18008.20
654.064
353.15
19996.30
656.201
353.15
21955.50
658.247
353.15
23925.40
660.247
353.15
25887.20
662.188
353.15
27855.00
664.084
353.15
29976.00
666.077
373.15
1164.33
613.877
373.15
2149.21
615.631
373.15
4123.49
618.999
373.15
5987.02
622.014
373.15
8094.82
625.262
373.15
10059.80
628.151
373.15
12066.30
630.972
373.15
14017.80
633.61
373.15
16044.40
636.241
373.15
18058.00
638.765
373.15
19975.60
641.085
373.15
21959.60
643.408
373.15
23948.00
645.665
373.15
25804.80
647.712
373.15
27898.40
649.952
373.15
29818.70
651.952
393.15
1101.93
593.952
393.15
2001.51
595.905
393.15
4002.83
600.027
393.15
6004.29
603.884
393.15
8005.48
607.511
393.15
10007.10
610.942
393.15
12110.90
614.361
393.15
14116.50
617.466
393.15
16097.20
620.399
393.15
18029.00
623.142
393.15
20054.00
625.904
393.15
22015.90
628.483
393.15
24005.50
631.008
393.15
25986.10
633.434
393.15
27951.60
635.769
393.15
29842.80
638.037
Reference
Fixed
Measured
Temperature, K - Liquid
Pressure, kPa - Liquid
Mass density, kg/m3 - Liquid
313.18
1000.00
668.09
313.18
2000.00
669.03
313.18
3000.00
669.97
313.18
4000.00
670.93
313.18
5010.00
671.9
313.18
6000.00
672.87
313.18
7000.00
673.86
313.18
8000.00
674.87
313.18
9000.00
675.87
313.18
10000.00
676.86
313.18
11000.00
677.85
313.18
12000.00
678.83
313.18
13000.00
679.81
313.18
14000.00
680.76
313.18
15000.00
681.7
313.18
16000.00
682.62
313.18
17000.00
683.53
313.18
18000.00
684.41
313.18
19000.00
685.26
313.18
20000.00
686.11
313.18
21000.00
686.92
313.18
22000.00
687.67
313.18
23000.00
688.42
313.18
23910.00
689.07
313.18
25000.00
689.85
333.04
1000.00
650.66
333.04
2000.00
651.8
333.04
3000.00
652.94
333.04
4000.00
654.08
333.04
5000.00
655.23
333.04
6000.00
656.38
333.04
7000.00
657.54
333.04
8000.00
658.65
333.04
9000.00
659.81
333.04
10000.00
660.92
333.04
11000.00
662.03
333.04
12000.00
663.1
333.04
13000.00
664.2
333.04
14000.00
665.25
333.04
15000.00
666.31
333.04
16000.00
667.33
333.04
17000.00
668.33
333.04
18030.00
669.34
333.04
19000.00
670.26
333.04
20000.00
671.2
333.04
22000.00
673.01
333.04
23000.00
673.86
333.04
24000.00
674.7
333.04
25000.00
675.52
333.04
23000.00
673.86
353.06
1010.00
632.6
353.06
2000.00
634.02
353.06
3000.00
635.41
353.06
4000.00
636.78
353.06
5000.00
638.15
353.06
6000.00
639.47
353.06
7000.00
640.8
353.06
8000.00
642.1
353.06
9010.00
643.4
353.06
10000.00
644.66
353.06
11000.00
645.92
353.06
12000.00
647.13
353.06
13000.00
648.37
353.06
14000.00
649.56
353.06
15000.00
650.72
353.06
16000.00
651.88
353.06
17000.00
653.0
353.06
18030.00
654.12
353.06
19000.00
655.16
353.06
20000.00
656.22
353.06
21000.00
657.27
353.06
22000.00
658.25
353.06
23000.00
659.24
353.06
24000.00
660.2
353.06
25000.00
661.14
Reference
Fixed
Measured
Temperature, K - Liquid
Pressure, kPa - Liquid
Mass density, kg/m3 - Liquid
298.15
100.00
679.5
298.15
1000.00
680.4
298.15
5000.00
684.2
298.15
10000.00
688.6
298.15
15000.00
692.8
298.15
20000.00
696.7
298.15
25000.00
700.4
298.15
30000.00
704.0
298.15
35000.00
707.4
298.15
40000.00
710.7
298.15
45000.00
713.8
298.15
50000.00
716.8
298.15
55000.00
719.7
298.15
60000.00
722.5
298.15
65000.00
725.2
298.15
70000.00
727.9
298.15
80000.00
732.9
298.15
90000.00
737.7
298.15
100000.00
742.3
298.15
110000.00
746.6
298.15
120000.00
750.7
298.15
130000.00
754.6
298.15
140000.00
758.4
313.15
100.00
666.6
313.15
1000.00
667.6
313.15
5000.00
671.8
313.15
10000.00
676.7
313.15
15000.00
681.3
313.15
20000.00
685.6
313.15
25000.00
689.5
313.15
30000.00
693.5
313.15
35000.00
697.1
313.15
40000.00
700.5
313.15
45000.00
703.9
313.15
50000.00
707.2
313.15
55000.00
710.3
313.15
60000.00
713.3
313.15
65000.00
716.1
313.15
70000.00
718.9
313.15
80000.00
724.2
313.15
90000.00
729.3
313.15
100000.00
734.0
313.15
110000.00
738.6
313.15
120000.00
742.8
313.15
130000.00
747.0
313.15
140000.00
751.1
333.15
100.00
648.9
333.15
1000.00
650.0
333.15
5000.00
655.0
333.15
10000.00
660.6
333.15
15000.00
665.8
333.15
20000.00
670.6
333.15
25000.00
675.1
333.15
30000.00
679.4
333.15
35000.00
683.4
333.15
40000.00
687.3
333.15
45000.00
690.9
333.15
50000.00
694.4
333.15
55000.00
697.7
333.15
60000.00
701.0
333.15
65000.00
704.1
333.15
70000.00
707.1
333.15
80000.00
712.8
333.15
90000.00
718.2
333.15
100000.00
723.2
333.15
110000.00
728.1
333.15
120000.00
732.6
333.15
130000.00
737.0
333.15
140000.00
741.1
353.15
100.00
631.2
353.15
1000.00
632.1
353.15
5000.00
637.8
353.15
10000.00
644.3
353.15
15000.00
650.3
353.15
20000.00
655.7
353.15
25000.00
660.8
353.15
30000.00
665.5
353.15
35000.00
670.0
353.15
40000.00
674.1
353.15
45000.00
678.1
353.15
50000.00
682.0
353.15
55000.00
685.5
353.15
60000.00
689.1
353.15
65000.00
692.4
353.15
70000.00
695.7
353.15
80000.00
701.7
353.15
90000.00
707.5
353.15
100000.00
712.8
353.15
110000.00
717.9
353.15
120000.00
722.7
353.15
130000.00
727.3
353.15
140000.00
731.6
373.15
1000.00
613.3
373.15
5000.00
620.1
373.15
10000.00
627.7
373.15
15000.00
634.5
373.15
20000.00
640.7
373.15
25000.00
646.3
373.15
30000.00
651.6
373.15
35000.00
656.5
373.15
40000.00
661.1
373.15
45000.00
665.5
373.15
50000.00
669.6
373.15
55000.00
673.5
373.15
60000.00
677.3
373.15
65000.00
680.8
373.15
70000.00
684.3
373.15
80000.00
690.8
373.15
90000.00
696.9
373.15
100000.00
702.6
373.15
110000.00
708.0
373.15
120000.00
713.0
373.15
130000.00
717.9
373.15
140000.00
722.3
393.15
1000.00
593.5
393.15
5000.00
601.7
393.15
10000.00
610.6
393.15
15000.00
618.4
393.15
20000.00
625.4
393.15
25000.00
631.7
393.15
30000.00
637.5
393.15
35000.00
643.0
393.15
40000.00
648.0
393.15
45000.00
652.8
393.15
50000.00
657.2
393.15
55000.00
661.5
393.15
60000.00
665.5
393.15
65000.00
669.3
393.15
70000.00
673.1
393.15
80000.00
680.1
393.15
90000.00
686.5
393.15
100000.00
692.5
393.15
110000.00
698.2
393.15
120000.00
703.4
393.15
130000.00
708.5
393.15
140000.00
713.4
Reference
Fixed
Measured
Temperature, K - Liquid
Pressure, kPa - Liquid
Mass density, kg/m3 - Liquid
288.15
101.00
688.33
293.15
101.00
684.11
298.15
101.00
679.87
303.15
101.00
675.6
308.15
101.00
671.31
313.15
101.00
667.0
288.15
100.00
688.4
288.15
1000.00
689.2
288.15
5000.00
692.5
288.15
10000.00
696.5
288.15
15000.00
700.4
288.15
20000.00
704.1
288.15
25000.00
707.7
288.15
30000.00
711.1
288.15
35000.00
714.3
288.15
40000.00
717.4
288.15
45000.00
720.3
288.15
50000.00
723.1
288.15
55000.00
725.8
288.15
60000.00
728.2
293.15
100.00
684.2
293.15
1000.00
685.0
293.15
5000.00
688.4
293.15
10000.00
692.6
293.15
15000.00
696.5
293.15
20000.00
700.4
293.15
25000.00
704.0
293.15
30000.00
707.5
293.15
35000.00
710.9
293.15
40000.00
714.0
293.15
45000.00
717.0
293.15
50000.00
719.9
293.15
55000.00
722.5
293.15
60000.00
725.1
298.15
100.00
679.9
298.15
1000.00
680.7
298.15
5000.00
684.3
298.15
10000.00
688.6
298.15
15000.00
692.7
298.15
20000.00
696.6
298.15
25000.00
700.4
298.15
30000.00
704.0
298.15
35000.00
707.4
298.15
40000.00
710.7
298.15
45000.00
713.8
298.15
50000.00
716.7
298.15
55000.00
719.4
298.15
60000.00
721.9
303.15
100.00
675.7
303.15
1000.00
676.5
303.15
5000.00
680.2
303.15
10000.00
684.6
303.15
15000.00
688.9
303.15
20000.00
693.0
303.15
25000.00
696.8
303.15
30000.00
700.5
303.15
35000.00
704.0
303.15
40000.00
707.4
303.15
45000.00
710.5
303.15
50000.00
713.5
303.15
55000.00
716.2
303.15
60000.00
718.8
308.15
100.00
671.4
308.15
1000.00
672.2
308.15
5000.00
676.0
308.15
10000.00
680.6
308.15
15000.00
685.0
308.15
20000.00
689.2
308.15
25000.00
693.2
308.15
30000.00
697.0
308.15
35000.00
700.6
308.15
40000.00
704.0
308.15
45000.00
707.2
308.15
50000.00
710.3
308.15
55000.00
713.1
308.15
60000.00
715.7
313.15
100.00
667.1
313.15
1000.00
668.0
313.15
5000.00
672.0
313.15
10000.00
676.7
313.15
15000.00
681.2
313.15
20000.00
685.5
313.15
25000.00
689.6
313.15
30000.00
693.5
313.15
35000.00
697.2
313.15
40000.00
700.7
313.15
45000.00
704.0
313.15
50000.00
707.1
313.15
55000.00
709.9
313.15
60000.00
712.6
318.15
100.00
662.7
318.15
1000.00
663.6
318.15
5000.00
667.7
318.15
10000.00
672.6
318.15
15000.00
677.3
318.15
20000.00
681.8
318.15
25000.00
686.0
318.15
30000.00
690.0
318.15
35000.00
693.8
318.15
40000.00
697.4
318.15
45000.00
700.7
318.15
50000.00
703.9
318.15
55000.00
706.8
318.15
60000.00
709.5
323.15
100.00
658.3
323.15
1000.00
659.3
323.15
5000.00
663.5
323.15
10000.00
668.6
323.15
15000.00
673.4
323.15
20000.00
678.0
323.15
25000.00
682.4
323.15
30000.00
686.5
323.15
35000.00
690.4
323.15
40000.00
694.1
323.15
45000.00
697.5
323.15
50000.00
700.7
323.15
55000.00
703.7
323.15
60000.00
706.4
328.15
100.00
653.9
328.15
1000.00
654.9
328.15
5000.00
659.3
328.15
10000.00
664.5
328.15
15000.00
669.5
328.15
20000.00
674.3
328.15
25000.00
678.8
328.15
30000.00
683.0
328.15
35000.00
687.0
328.15
40000.00
690.8
328.15
45000.00
694.3
328.15
50000.00
697.6
328.15
55000.00
700.6
328.15
60000.00
703.3
333.15
100.00
649.5
333.15
1000.00
650.6
333.15
5000.00
655.1
333.15
10000.00
660.5
333.15
15000.00
665.7
333.15
20000.00
670.6
333.15
25000.00
675.2
333.15
30000.00
679.6
333.15
35000.00
683.7
333.15
40000.00
687.5
333.15
45000.00
691.1
333.15
50000.00
694.4
333.15
55000.00
697.4
333.15
60000.00
700.2
343.15
100.00
640.5
343.15
1000.00
641.6
343.15
5000.00
646.5
343.15
10000.00
652.3
343.15
15000.00
657.8
343.15
20000.00
663.1
343.15
25000.00
668.0
343.15
30000.00
672.6
343.15
35000.00
676.9
343.15
40000.00
681.0
343.15
45000.00
684.7
343.15
50000.00
688.1
343.15
55000.00
691.3
343.15
60000.00
694.1
353.15
100.00
631.3
353.15
1000.00
632.5
353.15
5000.00
637.8
353.15
10000.00
644.0
353.15
15000.00
649.9
353.15
20000.00
655.5
353.15
25000.00
660.7
353.15
30000.00
665.6
353.15
35000.00
670.2
353.15
40000.00
674.4
353.15
45000.00
678.3
353.15
50000.00
681.9
353.15
55000.00
685.1
353.15
60000.00
688.0
363.15
100.00
621.9
363.15
1000.00
623.2
363.15
5000.00
628.9
363.15
10000.00
635.6
363.15
15000.00
641.9
363.15
20000.00
647.9
363.15
25000.00
653.4
363.15
30000.00
658.6
363.15
35000.00
663.5
363.15
40000.00
667.9
363.15
45000.00
672.0
363.15
50000.00
675.7
363.15
55000.00
679.0
363.15
60000.00
681.9
373.15
1000.00
614.2
373.15
5000.00
620.2
373.15
10000.00
627.4
373.15
15000.00
634.1
373.15
20000.00
640.4
373.15
25000.00
646.3
373.15
30000.00
651.8
373.15
35000.00
656.9
373.15
40000.00
661.5
373.15
45000.00
665.8
373.15
50000.00
669.6
373.15
55000.00
673.1
373.15
60000.00
676.1
393.15
1000.00
594.6
393.15
5000.00
601.7
393.15
10000.00
610.0
393.15
15000.00
617.8
393.15
20000.00
625.0
393.15
25000.00
631.7
393.15
30000.00
637.9
393.15
35000.00
643.6
393.15
40000.00
648.7
393.15
45000.00
653.3
393.15
50000.00
657.4
393.15
55000.00
660.9
393.15
60000.00
663.9
413.15
1000.00
574.1
413.15
5000.00
582.3
413.15
10000.00
592.0
413.15
15000.00
600.9
413.15
20000.00
609.2
413.15
25000.00
616.9
413.15
30000.00
623.9
413.15
35000.00
630.2
413.15
40000.00
635.9
413.15
45000.00
640.9
413.15
50000.00
645.2
413.15
55000.00
648.9
413.15
60000.00
651.9
Reference
Fixed
Measured
Pressure, kPa - Liquid
Temperature, K - Liquid
Mass density, kg/m3 - Liquid
100.00
298.15
679.71
Reference
Fixed
Measured
Temperature, K - Liquid
Pressure, kPa - Liquid
Mass density, kg/m3 - Liquid
283.15
100.00
692.57
288.15
100.00
688.55
293.15
100.00
684.19
298.15
100.00
679.95
303.15
100.00
675.68
308.15
100.00
671.39
313.15
100.00
667.06
318.15
100.00
662.54
323.15
100.00
658.32
328.15
100.00
653.81
283.15
2000.00
694.49
288.15
2000.00
690.28
293.15
2000.00
686.15
298.15
2000.00
682.02
303.15
2000.00
677.75
308.15
2000.00
673.45
313.15
2000.00
669.26
318.15
2000.00
664.87
323.15
2000.00
660.53
328.15
2000.00
656.27
283.15
5000.00
697.06
288.15
5000.00
693.01
293.15
5000.00
688.99
298.15
5000.00
684.8
303.15
5000.00
680.76
308.15
5000.00
676.49
313.15
5000.00
672.35
318.15
5000.00
668.35
323.15
5000.00
664.05
328.15
5000.00
659.84
283.15
7000.00
698.8
288.15
7000.00
694.77
293.15
7000.00
690.74
298.15
7000.00
686.68
303.15
7000.00
682.65
308.15
7000.00
678.48
313.15
7000.00
674.51
318.15
7000.00
670.32
323.15
7000.00
666.33
328.15
7000.00
661.99
283.15
10000.00
701.2
288.15
10000.00
697.23
293.15
10000.00
693.41
298.15
10000.00
689.23
303.15
10000.00
685.52
308.15
10000.00
681.37
313.15
10000.00
677.42
318.15
10000.00
673.52
323.15
10000.00
669.41
328.15
10000.00
665.25
283.15
20000.00
709.08
288.15
20000.00
705.18
293.15
20000.00
701.57
298.15
20000.00
697.65
303.15
20000.00
694.07
308.15
20000.00
690.12
313.15
20000.00
686.53
318.15
20000.00
682.85
323.15
20000.00
679.17
328.15
20000.00
675.25
283.15
30000.00
716.12
288.15
30000.00
712.38
293.15
30000.00
708.99
298.15
30000.00
705.17
303.15
30000.00
701.86
308.15
30000.00
698.22
313.15
30000.00
694.65
318.15
30000.00
691.31
323.15
30000.00
687.64
328.15
30000.00
684.02
283.15
40000.00
722.63
288.15
40000.00
719.01
293.15
40000.00
715.7
298.15
40000.00
712.11
303.15
40000.00
708.87
308.15
40000.00
705.32
313.15
40000.00
702.08
318.15
40000.00
698.89
323.15
40000.00
695.38
328.15
40000.00
691.84
283.15
50000.00
728.63
288.15
50000.00
725.2
293.15
50000.00
722.03
298.15
50000.00
718.54
303.15
50000.00
715.5
308.15
50000.00
712.12
313.15
50000.00
708.98
318.15
50000.00
705.82
323.15
50000.00
702.5
328.15
50000.00
699.13
283.15
60000.00
734.33
288.15
60000.00
731.01
293.15
60000.00
728.02
298.15
60000.00
724.73
303.15
60000.00
721.67
308.15
60000.00
718.41
313.15
60000.00
715.39
318.15
60000.00
712.36
323.15
60000.00
709.15
328.15
60000.00
706.05
283.15
65000.00
736.99
288.15
65000.00
733.73
293.15
65000.00
730.72
298.15
65000.00
727.65
303.15
65000.00
724.56
308.15
65000.00
721.43
313.15
65000.00
718.32
318.15
65000.00
715.32
323.15
65000.00
712.32
328.15
65000.00
709.3
Reference
Fixed
Measured
Temperature, K - Liquid
Pressure, kPa - Liquid
Mass density, kg/m3 - Liquid
298.15
100.00
680.0
298.15
3000.00
683.0
298.15
6000.00
686.0
298.15
9000.00
689.0
298.15
12000.00
691.0
298.15
15000.00
694.0
308.15
100.00
670.0
308.15
3000.00
674.0
308.15
6000.00
677.0
308.15
9000.00
680.0
308.15
12000.00
683.0
308.15
15000.00
685.0
318.15
100.00
662.0
318.15
3000.00
666.0
318.15
6000.00
669.0
318.15
9000.00
672.0
318.15
12000.00
675.0
318.15
15000.00
678.0
Reference
Fixed
Measured
Temperature, K - Liquid
Pressure, kPa - Liquid
Mass density, kg/m3 - Liquid
293.25
2103.00
685.58
293.25
3666.00
687.27
293.25
6195.00
689.52
293.25
10385.00
693.22
293.25
14421.00
696.48
293.25
17447.00
698.88
293.25
20472.00
701.01
293.25
23543.00
703.3
293.25
26611.00
705.5
313.08
2050.00
669.15
313.08
4083.00
671.15
313.08
6733.00
673.77
313.07
11204.00
678.28
313.08
14195.00
681.03
313.07
17225.00
683.61
313.07
20247.00
686.13
313.08
23266.00
688.54
313.08
26286.00
691.26
313.07
29805.00
693.98
332.78
2084.00
652.25
332.77
4091.00
654.57
332.78
7031.00
658.26
332.78
11151.00
662.67
332.78
14177.00
665.56
332.78
17172.00
668.79
332.78
20193.00
671.47
332.78
23214.00
674.57
332.78
26231.00
677.28
352.39
2184.00
635.33
352.39
4102.00
637.96
352.40
7146.00
641.83
352.39
11159.00
646.85
352.39
14169.00
650.4
352.39
17199.00
653.84
352.40
20204.00
657.05
352.40
23212.00
660.04
352.40
26228.00
663.06
352.39
29758.00
666.6
Reference
Fixed
Measured
Pressure, kPa - Liquid
Temperature, K - Liquid
Mass density, kg/m3 - Liquid
100.00
278.15
696.3
100.00
283.15
692.1
100.00
293.15
683.7
100.00
303.15
675.3
100.00
313.15
666.6
100.00
323.15
657.6
100.00
333.15
648.9
100.00
343.15
639.8
100.00
353.15
630.6
1000.00
278.15
697.0
1000.00
283.15
692.9
1000.00
293.15
684.6
1000.00
303.15
676.2
1000.00
313.15
667.6
1000.00
323.15
658.7
1000.00
333.15
650.0
1000.00
343.15
641.1
1000.00
353.15
632.0
2500.00
278.15
698.3
2500.00
283.15
694.2
2500.00
293.15
685.9
2500.00
303.15
677.7
2500.00
313.15
669.1
2500.00
323.15
660.4
2500.00
333.15
651.8
2500.00
343.15
643.1
2500.00
353.15
634.2
5000.00
278.15
700.3
5000.00
283.15
696.3
5000.00
293.15
688.2
5000.00
303.15
680.1
5000.00
313.15
671.7
5000.00
323.15
663.1
5000.00
333.15
654.8
5000.00
343.15
646.3
5000.00
353.15
637.8
7500.00
278.15
702.3
7500.00
283.15
698.3
7500.00
293.15
690.4
7500.00
303.15
682.4
7500.00
313.15
674.2
7500.00
323.15
665.8
7500.00
333.15
657.6
7500.00
343.15
649.4
7500.00
353.15
641.1
10000.00
278.15
704.2
10000.00
283.15
700.2
10000.00
293.15
692.5
10000.00
303.15
684.7
10000.00
313.15
676.6
10000.00
323.15
668.4
10000.00
333.15
660.4
10000.00
343.15
652.4
10000.00
353.15
644.3
15000.00
278.15
707.9
15000.00
283.15
704.0
15000.00
293.15
696.6
15000.00
303.15
689.0
15000.00
313.15
681.2
15000.00
323.15
673.3
15000.00
333.15
665.6
15000.00
343.15
658.0
15000.00
353.15
650.3
20000.00
278.15
711.4
20000.00
283.15
707.6
20000.00
293.15
700.4
20000.00
303.15
693.0
20000.00
313.15
685.5
20000.00
323.15
677.9
20000.00
333.15
670.4
20000.00
343.15
663.1
20000.00
353.15
655.7
25000.00
278.15
714.7
25000.00
283.15
711.1
25000.00
293.15
703.9
25000.00
303.15
696.9
25000.00
313.15
689.5
25000.00
323.15
682.1
25000.00
333.15
674.9
25000.00
343.15
667.9
25000.00
353.15
660.8
Reference
Fixed
Measured
Temperature, K - Liquid
Pressure, kPa - Liquid
Mass density, kg/m3 - Liquid
278.15
100.00
696.36
278.15
1000.00
697.01
278.15
5000.00
700.47
278.15
10000.00
704.35
278.15
15000.00
708.03
278.15
20000.00
711.54
278.15
25000.00
714.88
278.15
30000.00
718.17
278.15
35000.00
721.23
278.15
40000.00
724.19
278.15
45000.00
727.05
283.15
100.00
692.23
283.15
1000.00
693.01
283.15
5000.00
696.39
283.15
10000.00
700.44
283.15
15000.00
704.24
283.15
20000.00
707.85
283.15
25000.00
711.27
283.15
30000.00
714.56
283.15
35000.00
717.81
283.15
40000.00
720.8
283.15
45000.00
723.72
293.15
100.00
683.79
293.15
1000.00
684.6
293.15
5000.00
688.22
293.15
10000.00
692.49
293.15
15000.00
696.52
293.15
20000.00
700.34
293.15
25000.00
703.98
293.15
30000.00
707.62
293.15
35000.00
710.9
293.15
40000.00
714.1
293.15
45000.00
717.14
303.15
100.00
675.35
303.15
1000.00
676.16
303.15
5000.00
680.06
303.15
10000.00
684.63
303.15
15000.00
688.92
303.15
20000.00
692.96
303.15
25000.00
696.8
303.15
30000.00
700.52
303.15
35000.00
704.0
303.15
40000.00
707.3
303.15
45000.00
710.51
313.15
100.00
666.86
313.15
1000.00
667.7
313.15
5000.00
671.91
313.15
10000.00
676.8
313.15
15000.00
681.35
313.15
20000.00
685.63
313.15
25000.00
689.69
313.15
30000.00
693.53
313.15
35000.00
697.19
313.15
40000.00
700.67
313.15
45000.00
704.02
323.15
100.00
657.9
323.15
1000.00
658.85
323.15
5000.00
663.24
323.15
10000.00
668.53
323.15
15000.00
673.44
323.15
20000.00
677.94
323.15
25000.00
682.25
323.15
30000.00
686.3
323.15
35000.00
690.15
323.15
40000.00
693.83
323.15
45000.00
697.33
333.15
100.00
648.77
333.15
1000.00
649.92
333.15
5000.00
654.8
333.15
10000.00
660.46
333.15
15000.00
665.66
333.15
20000.00
670.49
333.15
25000.00
675.03
333.15
30000.00
679.3
333.15
35000.00
683.35
333.15
40000.00
687.19
333.15
45000.00
690.85
343.15
100.00
639.69
343.15
1000.00
640.93
343.15
5000.00
646.23
343.15
10000.00
652.33
343.15
15000.00
657.9
343.15
20000.00
663.04
343.15
25000.00
667.86
343.15
30000.00
672.37
343.15
35000.00
676.61
343.15
40000.00
680.63
343.15
45000.00
684.47
353.15
100.00
630.49
353.15
1000.00
631.83
353.15
5000.00
637.6
353.15
10000.00
644.13
353.15
15000.00
650.11
353.15
20000.00
655.53
353.15
25000.00
660.64
353.15
30000.00
665.38
353.15
35000.00
669.83
353.15
40000.00
674.08
353.15
45000.00
678.04
Reference
Fixed
Measured
Temperature, K - Liquid
Pressure, kPa - Liquid
Mass density, kg/m3 - Liquid
313.15
340.00
667.1
313.15
690.00
667.5
313.15
1030.00
667.8
313.15
1380.00
668.2
313.15
1720.00
668.64
313.15
2070.00
669.0
313.15
2410.00
669.3
313.15
2760.00
669.8
313.15
3100.00
670.1
313.15
3450.00
670.4
313.15
3800.00
670.8
313.15
4140.00
671.2
313.15
4480.00
671.6
313.15
4830.00
671.9
313.15
5170.00
672.2
313.15
5510.00
672.6
313.15
5860.00
672.9
313.15
6200.00
673.3
313.15
6550.00
673.6
313.15
6890.00
674.0
313.15
7240.00
674.3
333.15
340.00
649.7
333.15
690.00
650.2
333.15
1030.00
650.6
333.15
1380.00
651.0
333.15
1720.00
651.4
333.15
2070.00
651.9
333.15
2410.00
652.3
333.15
2760.00
652.7
333.15
3100.00
653.2
333.15
3450.00
653.6
333.15
3800.00
654.0
333.15
4140.00
654.4
333.15
4480.00
654.8
333.15
4830.00
655.2
333.15
5170.00
655.6
333.15
5510.00
656.0
333.15
5860.00
656.4
333.15
6200.00
656.8
333.15
6550.00
657.2
333.15
6890.00
657.6
333.15
7240.00
658.0
333.15
7580.00
658.4
333.15
7930.00
658.8
333.15
8270.00
659.2
353.15
340.00
631.8
353.15
690.00
632.3
353.15
1030.00
632.8
353.15
1380.00
633.3
353.15
1720.00
633.9
353.15
2070.00
634.4
353.15
2410.00
634.9
353.15
2760.00
635.3
353.15
3100.00
635.8
353.15
3450.00
636.3
353.15
3800.00
636.8
353.15
4140.00
637.3
353.15
4480.00
637.7
353.15
4830.00
638.2
353.15
5170.00
638.7
353.15
5510.00
639.2
353.15
5860.00
639.6
353.15
6200.00
640.1
353.15
6550.00
640.6
353.15
6890.00
641.0
353.15
7240.00
641.5
353.15
7580.00
641.9
353.15
7930.00
642.3
353.15
8270.00
642.8
353.15
8620.00
643.2
353.15
8960.00
643.9
353.15
9310.00
644.1
353.15
9650.00
644.5
373.15
340.00
613.1
373.15
690.00
613.7
373.15
1030.00
614.3
373.15
1380.00
614.9
373.15
1720.00
615.5
373.15
2070.00
616.1
373.15
2410.00
616.7
373.15
2760.00
617.3
373.15
3100.00
618.2
373.15
3450.00
618.5
373.15
3800.00
619.0
373.15
4140.00
619.6
373.15
4480.00
620.2
373.15
4830.00
620.7
373.15
5170.00
621.2
373.15
5510.00
621.8
373.15
5860.00
622.3
373.15
6200.00
622.9
373.15
6550.00
623.4
373.15
6890.00
623.9
373.15
7240.00
624.4
373.15
7580.00
625.0
373.15
7930.00
625.5
373.15
8270.00
626.0
373.15
8620.00
626.5
373.15
8960.00
627.0
373.15
9310.00
627.5
373.15
9650.00
628.0
393.15
340.00
593.4
393.15
690.00
594.1
393.15
1030.00
594.9
393.15
1380.00
595.6
393.15
1720.00
596.3
393.15
2070.00
597.0
393.15
2410.00
597.8
393.15
2760.00
598.5
393.15
3100.00
599.2
393.15
3450.00
599.9
393.15
3800.00
600.5
393.15
4140.00
601.2
393.15
4480.00
601.9
393.15
4830.00
602.5
393.15
5170.00
603.2
393.15
5510.00
603.8
393.15
5860.00
604.4
393.15
6200.00
605.1
393.15
6550.00
605.7
393.15
6890.00
606.3
393.15
7240.00
606.9
393.15
7580.00
607.5
393.15
7930.00
608.1
393.15
8270.00
608.7
393.15
8620.00
609.3
393.15
8960.00
609.9
393.15
9310.00
610.8
393.15
9650.00
611.1
Reference
Fixed
Measured
Temperature, K - Liquid
Pressure, kPa - Liquid
Mass density, kg/m3 - Liquid
283.15
101.00
692.398
283.15
267.60
692.646
283.15
550.80
692.799
283.15
878.60
693.177
283.15
991.30
693.192
283.15
2020.20
694.161
283.15
2914.80
694.997
283.15
4946.50
696.597
283.15
7034.80
698.638
283.15
9021.60
700.052
283.15
9991.90
700.869
283.15
11958.70
702.48
283.15
15011.20
704.783
283.15
18047.40
706.965
283.15
20045.40
708.637
283.15
22056.50
709.841
283.15
25044.10
712.0
283.15
28046.30
714.05
283.15
30051.70
715.435
283.15
32054.80
716.688
283.15
32971.30
717.342
283.15
32999.60
717.432
283.15
34016.50
718.012
283.15
34959.50
718.734
283.15
37943.00
720.455
283.15
40004.00
721.755
283.15
42057.90
723.102
283.15
44939.90
724.839
283.15
48022.40
726.526
283.15
49996.40
727.851
283.15
51981.80
728.904
283.15
54965.00
730.736
283.15
57949.30
732.407
283.15
59996.40
733.467
283.15
62025.40
734.345
283.15
64997.50
735.98
283.16
65971.00
736.499
288.15
102.00
688.224
288.15
391.30
688.682
288.15
554.40
688.232
288.15
882.70
689.214
288.15
989.10
688.618
288.15
2057.50
689.559
288.15
2917.80
690.931
288.15
5041.40
692.738
288.15
7088.80
693.96
288.15
9018.60
695.614
288.15
10039.90
696.278
288.15
12071.60
698.584
288.15
15001.40
700.836
288.15
17968.20
703.23
288.15
20067.60
704.758
288.15
22019.60
705.649
288.15
25001.50
707.645
288.15
28025.70
709.735
288.15
30034.70
711.006
288.15
32084.00
712.959
288.15
33050.00
713.818
288.15
33096.20
713.93
288.15
34035.60
714.067
288.15
35077.00
714.575
288.15
37992.90
716.378
288.15
40040.80
717.608
288.15
42022.80
718.735
288.15
44979.30
720.398
288.15
48045.10
723.18
288.15
50067.60
724.245
288.15
52032.00
724.841
288.15
55076.90
726.211
288.15
58004.00
729.214
288.15
59987.50
729.723
288.15
61973.60
731.101
288.15
64941.60
731.745
288.15
66025.40
732.751
293.15
100.50
683.714
293.16
305.20
684.504
293.16
476.40
684.708
293.15
825.10
684.796
293.16
1045.20
685.167
293.15
1971.70
685.978
293.15
3060.60
686.787
293.15
5011.00
688.859
293.16
7096.80
690.796
293.15
9042.10
692.394
293.15
10035.70
693.252
293.15
11946.50
694.459
293.15
14940.60
697.266
293.16
17888.60
698.789
293.16
19991.60
701.345
293.15
21987.10
701.769
293.16
24983.20
704.2
293.15
27986.00
706.659
293.16
29975.80
708.599
293.16
32232.40
710.098
293.15
33150.80
710.425
293.15
33149.70
710.401
293.15
34098.90
710.557
293.15
34999.60
711.53
293.16
38026.50
712.948
293.15
40081.00
714.898
293.15
42099.20
716.347
293.15
45068.20
718.234
293.16
48021.50
720.258
293.16
50084.50
721.322
293.16
52032.40
722.789
293.15
54965.50
724.479
293.15
58071.90
726.215
293.16
60018.30
727.31
293.16
61962.20
728.261
293.16
64991.00
729.973
293.15
66045.20
730.5
298.15
102.30
679.807
298.15
305.40
680.336
298.16
493.70
680.581
298.15
854.50
680.896
298.16
1012.60
680.891
298.15
1980.90
681.933
298.15
3167.80
682.97
298.15
5067.60
684.841
298.15
7065.30
686.383
298.16
9120.90
688.48
298.15
10106.60
689.119
298.16
11970.20
689.977
298.16
15219.70
693.294
298.16
17984.10
694.869
298.15
20127.80
696.696
298.15
22004.20
699.062
298.15
25080.50
701.29
298.16
28040.20
703.578
298.16
30089.10
704.725
298.16
32033.90
706.093
298.15
33112.80
707.026
298.16
33092.70
706.936
298.15
33924.30
706.971
298.16
35216.60
707.884
298.15
38096.90
709.948
298.15
40161.30
711.975
298.15
42028.50
713.324
298.15
45020.90
715.087
298.15
48106.60
717.001
298.15
50068.10
718.317
298.16
52019.70
719.461
298.15
55016.00
721.123
298.15
57930.90
723.027
298.15
59914.40
724.031
298.15
62036.30
725.393
298.15
65017.50
726.954
298.16
66118.40
727.501
303.15
100.70
675.559
303.15
304.10
675.598
303.15
498.90
675.77
303.15
900.60
675.904
303.15
979.10
676.053
303.15
1977.60
677.27
303.16
2964.90
678.337
303.15
4930.40
680.06
303.16
7045.60
682.343
303.16
8858.20
683.448
303.16
10013.90
684.334
303.15
11975.10
686.61
303.15
15043.60
689.15
303.16
18021.30
692.198
303.15
19974.40
693.813
303.15
21919.60
695.403
303.15
24991.70
697.736
303.16
27933.40
699.906
303.16
29990.40
701.007
303.15
31957.80
702.727
303.15
32862.10
703.514
303.15
33111.70
703.9
303.15
34080.70
704.468
303.15
34979.90
705.109
303.15
37951.00
707.216
303.15
39903.50
708.418
303.15
42013.80
709.635
303.15
44896.20
711.236
303.15
47951.40
713.224
303.15
50065.30
714.711
303.15
52072.60
715.915
303.15
55074.50
717.452
303.15
57989.30
719.654
303.15
59978.60
720.537
303.15
62052.40
721.855
303.15
64988.20
723.925
303.15
66029.70
724.328
308.15
105.00
671.006
308.15
274.30
671.143
308.15
494.10
671.318
308.15
803.30
671.687
308.15
1039.50
672.093
308.15
1916.70
672.909
308.15
2980.70
674.097
308.15
4990.20
676.132
308.15
6964.90
678.143
308.15
8864.30
679.887
308.15
9863.10
680.761
308.15
12008.60
682.857
308.16
15068.70
685.368
308.15
17849.80
687.815
308.15
19930.20
689.488
308.15
21988.30
691.177
308.15
25012.20
693.658
308.15
27955.20
695.718
308.15
29906.20
696.905
308.15
31928.70
698.302
308.15
32941.40
698.96
308.15
32885.90
699.002
308.15
34010.80
700.438
308.16
34949.30
701.078
308.15
37971.20
703.176
308.15
40011.40
704.309
308.15
41998.10
705.614
308.15
45016.60
707.854
308.15
48033.40
709.906
308.15
50043.60
711.265
308.15
51977.40
712.584
308.15
54981.90
714.563
308.15
58008.90
716.265
308.15
60030.00
717.688
308.15
61984.80
718.959
308.15
64980.50
720.569
308.16
66087.80
721.543
313.15
100.80
666.87
313.15
316.00
667.185
313.15
569.60
667.234
313.16
860.70
667.671
313.15
1088.80
668.002
313.15
2109.70
669.053
313.15
3137.00
670.192
313.15
5111.80
672.198
313.15
6921.80
674.169
313.15
9210.70
676.379
313.15
10209.30
677.309
313.15
12019.70
679.079
313.15
15058.60
681.665
313.15
17921.10
684.308
313.15
19931.90
686.1
313.15
22058.20
687.733
313.15
24861.60
690.068
313.15
27868.70
692.385
313.15
29956.80
693.806
313.15
32107.10
695.43
313.15
32980.30
696.141
313.15
33002.20
696.147
313.15
33981.20
697.086
313.15
35045.40
697.948
313.15
38126.60
700.098
313.16
39996.90
701.327
313.15
41978.40
702.778
313.15
44946.30
704.758
313.15
47879.70
706.851
313.16
50020.80
708.33
313.15
52097.40
709.812
313.15
54924.00
711.549
313.15
58081.50
713.474
313.15
59932.20
714.707
313.15
62004.00
716.103
313.15
64954.10
717.814
313.15
66113.10
718.367
318.15
100.70
662.812
318.15
336.30
663.228
318.16
590.90
663.443
318.16
891.00
663.766
318.15
1105.70
663.94
318.15
1929.10
664.905
318.15
2933.20
665.972
318.16
5020.80
668.355
318.16
6926.70
670.309
318.15
8989.00
672.331
318.15
10074.50
673.533
318.15
11896.00
675.253
318.16
14800.10
678.075
318.15
18102.40
681.046
318.15
19985.10
682.727
318.15
22093.70
684.679
318.16
24872.80
686.865
318.16
27909.40
689.38
318.15
29997.50
691.196
318.16
31957.10
692.414
318.15
33015.60
693.259
318.15
33179.60
693.331
318.16
34110.30
694.119
318.16
35047.60
694.934
318.15
37838.40
697.046
318.15
40092.50
698.439
318.16
41996.00
699.6
318.15
44884.00
701.561
318.15
47944.40
703.663
318.16
49950.20
705.2
318.16
52037.30
706.412
318.15
54944.20
708.215
318.15
57972.30
710.506
318.15
59922.50
711.605
318.16
61930.00
712.85
318.15
65021.80
714.898
318.15
66027.50
715.438
323.15
102.30
658.378
323.15
296.10
658.71
323.15
528.40
658.782
323.16
920.70
659.343
323.15
994.20
659.429
323.15
2006.90
660.61
323.15
2966.60
661.806
323.15
4996.20
663.968
323.15
7042.10
666.276
323.15
9029.90
667.858
323.15
10089.70
669.742
323.15
11913.70
670.973
323.15
15110.70
674.373
323.15
17980.70
677.251
323.15
20037.80
678.71
323.15
21994.90
680.737
323.15
24993.40
683.213
323.16
27958.40
685.975
323.16
30054.60
687.083
323.15
32079.20
689.177
323.16
33067.40
689.946
323.15
33103.20
689.972
323.15
34080.80
690.434
323.15
35113.00
691.624
323.15
37952.80
693.659
323.16
40047.00
695.097
323.15
42011.10
696.516
323.16
44936.90
698.783
323.15
48025.40
700.814
323.15
49933.50
702.105
323.15
52114.30
703.681
323.15
54963.50
705.509
323.15
58044.90
707.475
323.15
60049.80
708.827
323.15
62131.00
710.008
323.15
64998.70
711.842
323.16
66131.20
712.551
328.15
100.80
653.868
328.15
289.90
654.182
328.16
501.00
654.211
328.15
897.50
654.815
328.15
994.10
655.012
328.15
1988.80
656.162
328.15
2996.70
657.408
328.15
5013.40
659.794
328.15
6974.90
662.023
328.15
9017.00
664.204
328.15
10040.00
665.257
328.16
12209.60
667.562
328.16
15054.80
670.204
328.16
18061.30
673.216
328.16
20279.00
675.247
328.16
22012.90
676.775
328.15
24924.10
679.489
328.15
27979.20
682.036
328.15
29958.30
683.395
328.15
32059.50
685.102
328.15
33065.50
685.969
328.15
33107.20
685.992
328.15
34013.40
687.01
328.15
35029.60
687.796
328.15
38009.80
690.025
328.15
39969.00
691.415
328.15
41958.80
692.865
328.15
44952.60
695.094
328.15
47977.50
697.371
328.15
49926.50
698.804
328.15
51996.90
700.259
328.15
54946.60
702.284
328.15
57938.70
704.221
328.15
59990.90
705.64
328.15
61981.50
707.057
328.15
65031.60
708.835
328.15
66046.20
709.499
333.15
100.40
649.302
333.16
303.50
649.622
333.15
532.60
649.653
333.15
897.80
650.259
333.16
1003.00
650.554
333.15
1987.20
651.687
333.15
3023.40
653.063
333.15
4997.40
655.338
333.15
7002.40
657.844
333.15
9032.00
660.047
333.15
10209.50
661.268
333.16
12011.10
663.322
333.15
15008.40
666.206
333.16
17991.90
669.217
333.16
20035.90
671.108
333.15
22033.60
672.882
333.16
25027.10
675.678
333.15
28039.90
678.188
333.15
30015.60
679.579
333.15
32067.10
681.185
333.15
32976.90
681.946
333.16
33072.70
682.004
333.15
34085.90
683.474
333.15
35075.40
684.235
333.15
37893.70
686.324
333.15
40110.90
687.848
333.15
41946.80
689.191
333.15
44974.00
691.567
333.15
47935.60
693.899
333.15
49919.60
695.372
333.15
51953.30
696.893
333.15
54875.90
699.008
333.15
58057.20
700.988
333.15
59992.70
702.482
333.15
62048.60
703.927
333.15
64970.40
705.65
333.15
66005.00
706.481
338.15
100.40
644.915
338.15
309.80
645.161
338.15
561.60
645.341
338.15
898.50
645.924
338.15
1014.10
646.212
338.16
2000.20
647.409
338.15
2936.10
648.694
338.15
5018.60
651.205
338.16
6917.30
653.552
338.16
9046.90
656.063
338.15
10033.60
657.126
338.16
11959.40
659.361
338.15
14884.90
662.203
338.15
17955.80
665.481
338.15
19927.00
667.369
338.15
22041.10
669.319
338.15
25026.20
672.169
338.16
27975.50
674.704
338.15
29993.70
676.134
338.16
31948.90
677.899
338.15
32881.50
678.515
338.16
32881.50
678.499
338.15
33937.40
679.921
338.15
35012.40
680.879
338.16
37962.10
683.24
338.15
39986.90
684.582
338.15
41989.90
686.092
338.15
44978.20
688.463
338.15
47971.40
690.744
338.15
49998.60
692.38
338.15
52127.20
693.976
338.16
54992.20
696.066
338.15
57939.90
697.82
338.15
60013.80
699.459
338.16
62073.50
700.918
338.15
65011.90
702.688
338.15
66056.80
703.55
343.15
105.10
640.758
343.15
297.30
640.918
343.15
520.30
641.218
343.15
911.70
641.765
343.15
1017.70
641.938
343.15
1994.60
643.242
343.15
2968.30
644.553
343.15
4994.80
647.152
343.15
6976.60
649.726
343.15
9002.60
652.141
343.15
10060.40
653.267
343.15
12024.50
655.625
343.15
14927.50
658.769
343.15
17975.20
661.975
343.15
19985.00
664.0
343.15
22032.80
666.001
343.15
25090.50
668.93
343.15
28044.70
671.724
343.15
30082.00
673.379
343.15
32169.60
675.296
343.15
33053.30
676.043
343.15
33096.80
676.076
343.16
34034.10
676.976
343.15
35030.10
677.808
343.15
37943.20
680.185
343.15
40012.30
681.817
343.15
41972.20
683.353
343.15
44927.30
685.751
343.15
47907.90
688.0
343.15
50058.90
689.668
343.15
52026.20
691.103
343.16
54918.50
693.158
343.16
57986.20
695.23
343.15
59944.40
696.69
343.15
61966.50
697.921
343.15
65069.90
699.939
343.15
66059.20
700.533
348.15
100.30
636.109
348.16
291.70
636.475
348.15
462.20
636.505
348.15
859.80
637.192
348.15
974.20
637.393
348.15
1974.90
638.781
348.15
3051.10
640.295
348.15
5094.00
643.002
348.16
7050.20
645.632
348.16
9003.20
648.038
348.15
10025.40
649.256
348.16
12186.90
651.83
348.15
14792.00
654.622
348.16
17899.00
658.098
348.15
20111.40
660.386
348.15
22163.40
662.539
348.16
25099.80
665.329
348.15
28080.10
668.108
348.15
30148.90
670.002
348.15
32161.30
671.799
348.16
32941.60
672.463
348.15
32935.20
672.452
348.15
33958.60
673.504
348.15
35044.60
674.428
348.15
37937.40
676.834
348.15
40025.60
678.502
348.16
42065.80
680.23
348.15
45050.60
682.511
348.15
47914.70
684.825
348.15
49949.80
686.336
348.15
52166.80
688.088
348.15
55021.90
690.168
348.15
57945.30
692.261
348.16
60030.00
693.748
348.15
62063.30
695.106
348.15
64941.60
696.91
348.15
66153.40
697.788
353.15
100.50
631.649
353.15
336.00
631.995
353.15
572.60
632.233
353.15
926.00
632.774
353.15
1016.40
632.95
353.16
2113.40
634.631
353.15
2992.10
635.919
353.15
4963.90
638.644
353.15
7000.90
641.284
353.15
9062.30
643.911
353.15
10005.00
645.176
353.15
12127.50
647.788
353.15
14954.20
651.028
353.15
17977.40
654.406
353.15
19937.00
656.492
353.15
21893.60
658.507
353.15
24908.20
661.562
353.15
27850.30
664.482
353.15
29936.20
666.345
353.15
31876.00
668.022
353.15
32911.00
668.934
353.15
32960.80
669.075
353.16
33963.70
670.126
353.15
34945.40
670.985
353.15
37913.10
673.509
353.15
40142.80
675.336
353.15
42067.30
677.003
353.15
45001.70
679.292
353.15
48029.20
681.775
353.15
50145.10
683.478
353.15
52082.20
685.052
353.15
55132.20
687.213
353.15
57980.30
689.013
353.15
60098.40
690.731
353.16
62042.50
692.223
353.15
65062.70
694.154
353.16
66024.30
694.802
358.15
100.40
626.935
358.15
264.10
627.168
358.15
508.40
627.316
358.15
926.80
628.098
358.15
1013.90
628.327
358.16
2083.90
629.903
358.15
3021.20
631.365
358.15
4930.00
634.077
358.16
6993.50
637.086
358.16
9030.20
639.755
358.15
10072.70
641.066
358.15
12136.80
643.735
358.15
14904.90
646.944
358.15
17965.40
650.491
358.16
20162.00
652.87
358.15
22174.60
654.965
358.15
25059.40
657.993
358.15
28035.20
660.974
358.15
30001.90
662.532
358.15
31977.70
664.488
358.15
32792.60
665.093
358.15
33039.30
665.404
358.15
33850.00
666.525
358.15
35026.50
667.567
358.15
37872.30
669.996
358.15
40037.40
671.748
358.15
42100.10
673.454
358.16
45054.00
675.954
358.15
47958.10
678.424
358.15
50037.90
680.129
358.15
52080.70
681.85
358.15
55073.40
684.059
358.15
57918.40
685.685
358.15
60042.70
687.68
358.15
62066.50
689.111
358.15
64986.10
691.283
358.15
66108.60
692.023
363.15
104.10
622.138
363.15
334.00
622.474
363.15
601.70
622.649
363.15
892.90
623.267
363.15
1034.70
623.668
363.15
1986.00
625.081
363.15
2940.40
626.678
363.15
4979.20
629.757
363.16
6920.20
632.642
363.16
8964.80
635.395
363.15
9959.50
636.563
363.15
11970.70
639.421
363.15
14935.50
642.887
363.15
17973.30
646.544
363.15
19939.90
648.708
363.16
21932.90
650.806
363.15
24872.20
654.024
363.15
27992.70
657.078
363.15
30062.30
659.006
363.15
31961.10
660.63
363.15
33053.30
661.633
363.15
33032.60
661.606
363.15
33999.50
663.017
363.15
35028.30
664.03
363.15
37919.20
666.495
363.15
39916.00
668.059
363.15
42015.50
669.917
363.16
44986.80
672.551
363.15
47947.20
675.063
363.15
50050.30
676.807
363.15
52022.60
678.457
363.15
54940.40
680.815
363.15
57916.50
682.78
363.15
59980.00
684.625
363.15
62042.90
686.168
363.15
64924.10
688.267
363.15
66088.40
689.169
Reference
Speed of sound, m/s
Fixed
Measured
Temperature, K - Fluid (supercritical or subcritical phases)
Pressure, kPa - Fluid (supercritical or subcritical phases)
Speed of sound, m/s - Fluid (supercritical or subcritical phases)
513.92
2500.00
266.66
525.23
2500.00
196.31
528.93
2500.00
167.01
534.12
2500.00
121.38
538.13
2500.00
101.28
544.09
2500.00
100.71
547.02
2500.00
107.6
552.59
2500.00
118.66
559.91
2500.00
129.19
564.02
2500.00
135.46
572.57
2500.00
144.47
584.19
2500.00
156.26
590.48
2500.00
161.58
601.60
2500.00
170.4
612.58
2500.00
179.23
620.87
2500.00
183.77
632.18
2500.00
189.44
640.72
2500.00
192.85
650.07
2500.00
195.77
513.59
3000.00
293.56
523.83
3000.00
242.56
528.41
3000.00
218.56
532.76
3000.00
193.81
538.36
3000.00
152.7
544.95
3000.00
115.6
549.04
3000.00
105.27
553.93
3000.00
110.64
574.87
5000.00
160.49
577.04
5000.00
154.18
582.31
5000.00
142.67
588.17
5000.00
139.88
592.28
5000.00
136.41
597.48
5000.00
135.43
602.30
5000.00
135.26
607.65
5000.00
136.72
615.11
5000.00
142.58
623.25
5000.00
150.58
632.29
5000.00
156.55
643.51
5000.00
165.41
513.58
6000.00
394.15
524.62
6000.00
357.73
529.10
6000.00
344.17
533.77
6000.00
331.99
539.09
6000.00
316.72
543.60
6000.00
300.59
548.98
6000.00
283.97
553.05
6000.00
270.32
557.86
6000.00
255.8
563.84
6000.00
236.54
574.85
6000.00
211.93
583.18
6000.00
191.45
592.57
6000.00
176.14
604.10
6000.00
161.83
613.73
6000.00
158.49
559.74
3000.00
116.03
563.09
3000.00
119.84
574.33
3000.00
134.46
582.39
3000.00
142.99
591.77
3000.00
152.87
602.84
3000.00
161.38
612.37
3000.00
167.57
623.42
3000.00
174.58
632.04
3000.00
179.96
641.53
3000.00
186.21
650.90
3000.00
189.41
513.65
4000.00
333.84
524.25
4000.00
291.43
528.90
4000.00
269.01
533.55
4000.00
252.16
537.58
4000.00
231.06
541.47
4000.00
208.26
549.16
4000.00
178.39
553.43
4000.00
160.12
560.41
4000.00
132.63
563.94
4000.00
124.51
575.28
4000.00
113.58
584.60
4000.00
122.55
591.62
4000.00
127.84
603.68
4000.00
143.88
612.08
4000.00
149.82
621.22
4000.00
157.32
631.85
4000.00
163.15
641.95
4000.00
173.32
622.48
6000.00
158.77
632.41
6000.00
159.42
643.04
6000.00
164.74
513.40
8000.00
451.65
524.62
8000.00
417.84
528.95
8000.00
403.55
533.57
8000.00
391.25
538.84
8000.00
376.34
542.55
8000.00
364.39
548.66
8000.00
346.4
553.19
8000.00
335.76
557.81
8000.00
325.48
563.58
8000.00
312.82
574.41
8000.00
287.41
583.10
8000.00
270.69
593.19
8000.00
249.19
604.67
8000.00
226.0
613.93
8000.00
218.01
620.20
8000.00
211.6
632.86
8000.00
201.03
642.59
8000.00
195.65
515.30
10000.00
481.16
523.19
10000.00
459.31
533.40
10000.00
437.12
543.16
10000.00
413.25
553.20
10000.00
388.87
563.03
10000.00
363.89
573.39
10000.00
345.21
579.18
10000.00
331.94
515.23
5000.00
363.89
521.41
5000.00
337.01
534.45
5000.00
293.97
543.50
5000.00
262.34
553.42
5000.00
225.17
565.65
5000.00
187.87
582.86
10000.00
325.02
587.85
10000.00
315.79
592.71
10000.00
307.49
603.51
10000.00
291.2
614.03
10000.00
272.94
623.13
10000.00
260.67
Reference
Fixed
Measured
Pressure, kPa - Liquid
Temperature, K - Liquid
Speed of sound, m/s - Liquid
100.00
293.15
1151.69
100.00
298.16
1129.87
100.00
303.06
1108.88
100.00
308.08
1087.42
100.00
313.10
1066.12
100.00
318.18
1044.54
15200.00
293.20
1256.33
15200.00
303.17
1218.64
15200.00
308.08
1200.43
15200.00
313.10
1182.05
15200.00
318.18
1163.39
30400.00
293.18
1341.5
30400.00
303.13
1306.98
30400.00
308.07
1290.28
30400.00
313.12
1273.35
30400.00
318.18
1256.47
45590.00
293.19
1416.6
45590.00
298.18
1400.09
45590.00
303.07
1384.42
45590.00
308.07
1368.71
45590.00
313.12
1352.98
45590.00
318.17
1337.39
60790.00
293.20
1484.48
60790.00
298.19
1468.69
60790.00
303.18
1453.68
60790.00
308.12
1438.95
60790.00
313.12
1424.3
60790.00
318.17
1409.63
75990.00
293.20
1546.46
75990.00
298.11
1531.64
75990.00
303.17
1517.17
75990.00
308.12
1503.23
75990.00
313.10
1489.21
75990.00
318.09
1475.54
91190.00
293.20
1603.69
91190.00
298.15
1589.43
91190.00
303.18
1575.68
91190.00
308.11
1562.39
91190.00
313.13
1549.03
91190.00
318.15
1535.72
101320.00
293.20
1639.7
101320.00
298.16
1625.72
101320.00
303.10
1612.63
101320.00
308.24
1599.12
101320.00
313.21
1586.17
101320.00
318.18
1573.59
111450.00
293.10
1674.29
111450.00
298.13
1660.46
111450.00
298.16
1660.43
111450.00
303.15
1647.6
111450.00
308.21
1634.64
111450.00
313.20
1622.05
111450.00
318.18
1609.77
121580.00
293.16
1707.09
121580.00
298.14
1692.38
121580.00
303.10
1681.25
121580.00
308.17
1668.58
121580.00
313.13
1656.4
121580.00
318.17
1644.27
Reference
Correlations
Similar Compounds
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Mixtures
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Sources
KDB Pure (Korean Thermophysical Properties Databank)
KDB Vapor Pressure Data
Crippen Method
Kinematic Viscosities for Ether + Alkane Mixtures: Experimental Results and UNIFAC-VISCO Parameters
Viscometric and Volumetric Properties of 10 Regular Binary Systems at 308.15 K and 313.15 K
Thermodynamic and Acoustic Properties of Mixtures of Dibromomethane + Heptane
Experimental Study of the Density and Viscosity of n-Heptane at Temperatures from 298 K to 470 K and Pressure up to 245 MPa
Densities and Kinematic Viscosities of a Quinary Regular Liquid System and Its Five Quaternary Subsystems at 293.15A K and 298.15A K
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
Activity coefficient at infinite dilution, azeotropic data, excess enthalpies and solid liquid-equilibria for binary systems of alkanes and aromatics with esters
Liquid-liquid equilibrium data of water with neohexane, methylcyclohexane, tert-butyl methyl ether, n-heptane and vapor -liquid-liquid equilibrium with methane
Vapour pressures and excess functions of (3,5; 2,6)dimethylpyridine + n-hexane, n-heptane and n-octane measurement and prediction
Establishing benchmarks for the Second Industrial Fluids Simulation Challenge
Determination of activity coefficients at infinite dilution of organic solutes in the ionic liquid, trihexyl(tetradecyl)-phosphonium tris(pentafluoroethyl) trifluorophosphate, by gas liquid chromatography
Bubble points of some binary mixtures formed by o-cresol at 95.75 kPa
Solubility of CO2 in branched alkanes in order to extend the PPR78 model (predictive 1978, Peng Robinson EOS with temperature-dependent kij calculated through a group contribution method) to such systems
Isobaric vapour liquid equilibria for binary mixtures of n-heptane with bromobenzene, chlorobenzene and fluorobenzene at atmospheric pressure
Comparative experimental and modeling studies of the viscosity behavior of ethanol +C7 hydrocarbon mixtures versus pressure and temperature
Liquid liquid equilibrium of (perfluoroalkane + alkane) binary mixtures
Isobaric vapor liquid equilibria for binary systems of butyl chlorides with heptane, toluene and cyclohexane at 101.3, 80.0 and 53.3 kPa
Determination of activity coefficients at infinite dilution of organic solutes in the ionic liquid, tributylmethylphosphonium methylsulphate by gas liquid chromatography
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
Vapour liquid liquid and vapour liquid equilibrium of the system water + ethanol + heptane at 101.3 kPa
Vapour liquid equilibrium data for the hydrogen sulphide + n-heptane system at temperatures from 293.25 to 373.22K and pressures up to about 6.9MPa
Thermodynamic study of 1,1,2,2-tetrachloroethane + hydrocarbon mixtures I. Excess and solvation enthalpies
Thermodynamics of mixtures containing amines VI. Liquid liquid equilibria for mixtures of o-toluidine + selected alkanes
Determination and correlation of vapor liquid equilibrium for binary systems consisting of close-boiling components
Determination and correlation of liquid liquid equilibria for four binary N,N-dimethylformamide + hydrocarbon systems
Determination of partial molar excess enthalpies at infinite dilution for the systems four alcohols + [bmim]PF6 at different temperatures by isothermal titration calorimeter
Phase behaviour of 1-methyl-3-octylimidazolium bis[trifluoromethylsulfonyl]imide with thiophene and aliphatic hydrocarbons: The influence of n-alkane chain length
Thermodynamics of fuels with a biosynthetic component (III): Vapor liquid equilibrium data for the ternary mixture ethyl 1, 1-dimethylethyl ether, n-heptane and 1-hexene at T = 313.15K
Determination and correlation of molar excess enthalpies of binary systems 2,4-pentanedione + (1-butanol, + 2-methyl-1-propanol, + 1-pentanol, + 1-heptane, + ethyl acetate, and + water)
A study on the liquid liquid equilibria of 1-alkyl-3-methylimidazolium hexafluorophosphate with ethanol and alkanes
Thiophene separation from aliphatic hydrocarbons using the 1-ethyl-3-methylimidazolium ethylsulfate ionic liquid
Isobaric vapor liquid equilibria for the n-hexane + 2-isopropoxyethanol and n-heptane + 2-isopropoxyethanol systems
Activity coefficients at infinite dilution measurements for organic solutes in the ionic liquid N-butyl-4-methylpyridinium tosylate using GLC at T = (328.15, 333.15, 338.15, and 343.15)K
Measurement and prediction of activity coefficients at infinite dilution ( ), vapor.liquid equilibria (VLE) and excess enthalpies (HE) of binary systems with 1,1-dialkyl-pyrrolidinium bis(trifluoromethylsulfonyl)imide using mod. UNIFAC (Dortmund)
Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium trifluoromethanesulfonate using GLC
(Solid + liquid) and (liquid + liquid) phase equilibria measurements and correlation of the binary systems {tri-iso-butyl(methyl)phosphonium tosylate + alcohol, or +hydrocarbon}
Activity coefficients at infinite dilution of alkanes and alkenes in 1-alkyl-3-methylimidazolium tetrafluoroborate
Binary, ternary and quaternary liquid liquid equilibria in 1-butanol, oleic acid, water and n-heptane mixtures
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)
Phase equilibrium for the systems diisopropyl ether, isopropyl alcohol + 2,2,4-trimethylpentane and + n-heptane at 101.3 kPa
Excess molar enthalpies of diethyl malonate+ (1-butanol, 2-methyl-1-propanol, 1-pentanol, n-heptane, and ethyl acetate) at T= (288.2, 298.2, 313.2, 328.2, 338.2, and 348.2 K) and p = 101.3 kPa
Alkylsulfate-based ionic liquids to separate azeotropic mixtures
(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}
Measurements of different thermodynamic properties of systems containing ionic liquids and correlation of these properties using modified UNIFAC (Dortmund)
Alkylsulfate-based ionic liquids to separate azeotropic mixtures
1-Butanol + hexylamine + n-heptane at temperature range (288.15 323.15 K): Experimental density data, excess molar volumes determination and modeling with cubic EOS
Isobaric vapor-liquid equilibria for the n-heptane + ethylene glycol monopropyl ether and n-octane + ethylene glycol monopropyl ether systems
Liquid-liquid equilibrium and interfacial tension of the ternary system heptane + thiophene + 1-ethyl-3-methylimidazolium bis(trifluoromethanesulfonyl)imide
Gas-liquid chromatography measurements of activity coefficients at infinite dilution of hydrocarbons and alkanols in 1-alkyl-3-methylimidazolium bis(oxalato)borate
Experimental and predicted excess molar enthalpies of binary mixtures containing 2,2'-oxybis[propane], benzene, butan-1-ol, 2-methylpropan-1-ol, 2-methyl-2-ene-1-propanol at 303.15 K
Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-ethyl-3-methylimidazolium methanesulfonate
Viscosity of the binary systems 2-methyl-2-propanol with n-alkanes at T = (303.15, 308.15, 313.15, 318.15 and 323.15) K: Prediction and correlation - New UNIFAC-VISCO interaction parameters
Liquid densities of acetone and n-heptane and excess volumes of the binary system in a wide temperature and pressure range
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
Influence of anion structure on the liquid-liquid equilibria of 1-(3-hydroxypropyl)pyridinium cation based ionic liquid-hydrocarbon binary systems
Solubility of decanedioic acid in binary solvent mixtures
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
Measurements and correlation of vapour liquid equilibria of 2-butanone and hydrocarbons binary systems at two different pressures
Experimental determination and calculation of the critical curves for the binary systems of CO2 containing ketone, alkane, ester and alcohol, respectively
Liquid-liquid equilibria of {n-heptane + toluene + aniline} ternary system: Experimental data and correlation
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
Isobaric vapor-liquid equilibrium for four binary systems of thiophene
Phase equilibrium properties of the ternary mixture dibutyl ether + toluene + heptane at 313.15 K
Ternary liquid-liquid equilibria of bis(trifluoromethylsulfonyl)-amide based ionic liquids + methanol + heptane
Liquid-liquid equilibria of mixtures with ethyl lactate and various hydrocarbons
Isobaric vapor-liquid equilibrium for four binary systems of 3-methylthiophene
Ternary liquid-liquid equilibria of bis(trifluoromethylsulfonyl)-amide based ionic liquids + thiophene + n-heptane. The influence of cation structure
Activity coefficients at infinite dilution of organic solutes in the ionic liquid ethyl(2-hydroxyethyl)dimethyl-ammonium diethylphosphate using gas liquid chromatography
Validation of a new apparatus using the dynamic method for determining the critical properties of binary mixtures containing CO2 and a n-alkane
Activity coefficients at infinite dilution of organic solutes in 1-octyl-3-methylimidazolium nitrate using gas-liquid chromatography
Liquid-liquid equilibrium (LLE) data for ternary mixtures of {aliphatic + p-xylene + [EMpy][ESO4]} at T = 313.15 K
Vapour liquid equilibria and excess enthalpies of the binary mixtures 1-pentanol with 2,2,4-trimethylpentane or n-heptane
A novel static analytical apparatus for phase equilibrium measurements
Ternary liquid liquid equilibria of trifluorotris(perfluoroethyl)phosphate based ionic liquids + methanol + heptane
Ternary (liquid liquid) equilibria of nitrate based ionic liquid + alkane + benzene at 298.15 K: Experiments and correlation
Separation of toluene from n-heptane using monocationic and dicationic ionic liquids
Liquid-liquid equilibria containing fluorous solvents as environmentally benign solvent
(Liquid-liquid) equilibria for ternary and quaternary systems of representative compounds of gasoline + methanol at 293.15 K: Experimental data and correlation
Isobaric vapor-liquid equilibrium for binary systemsof toluene + o-xylene, benzene + o-xylene, nonane + benzene and nonane + heptane at 101.3 kPa
Isobaric vapor-liquid equilibrium for systems containing sulfur compounds
Using binary mixtures of dicationic ionic liquids for determination ofactivity coefficients at infinite dilution by gas-liquid chromatography
Capacity of two 1-butyl-1-methylpyrrolidinium-based ionic liquidsfor the extraction of ethanol from its mixtures with heptane and hexane
A novel continuous flow apparatus with a video camera system for high pressure phase equilibrium measurements
Liquid-liquid equilibrium in binary systems of isomeric C8 aliphatic monoethers with nitromethane
A novel dynamic recirculating apparatus for vapour-liquid equilibrium measurements at moderate pressures and temperatures
Interfacial tension of binary mixtures exhibiting azeotropic behavior: Measurement and modeling with PCP-SAFT combined with Density Gradient Theory
Ternary liquid-liquid equilibria of trifluorotris(perfluoroethyl)phosphate based ionic liquids + benzothiophene + heptane
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
Liquid-liquid extraction of toluene from n-heptane by {[emim][TCM] + [emim][DCA]} binary ionic liquid mixtures
Extraction of benzene, ethylbenzene, and xylenes from n-heptane using binary mixtures of [4empy][Tf2N] and [emim][DCA] ionic liquids
Liquid-liquid equilibria for multicomponent mixtures of 2,2-dimethyl-1,3-dioxolane with n-heptane, toluene, ethanol and water
Thermodynamic behaviour of second generation biofuels: Vapour liquid equilibria and excess enthalpies of the binary mixtures 2-pentanol and n-heptane or 2,2,4-trimethylpentane
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
Liquid liquid equilibria for ternary systems ethanol + heptane + phosphoric-based ionic liquids
Thermodynamic study of heptane + amine mixtures. V. Excess and solvation Gibbs energies
Vapor liquid equilibria of {n-heptane + toluene + [emim][DCA]} system by headspace gas chromatography
Separation of azeotropic mixtures using high ionicity ionic liquid based on 1-ethyl-3- methylimidazolium thiocyanate
Vapour liquid equilibrium at T = 308.15 K for binary systems: Dibromomethane + n-heptane, bromotrichloromethane + n-heptane, bromotrichloromethane + dibromomethane, bromotrichloromethane + bromochloromethane and dibromomethane + bromochloromethane. Experimental data and modelling
Separation of pyridine from heptane with tricyanomethanide-based ionic liquids
Isothermal vapor- liquid equilibria and excess molar enthalpy of 2-methylpyrazine (2MP) containing binary mixtures. Comparison with DISQUAC predictions
Extraction of aromatic nitrogen compounds from heptane quinolinium and isoquinolinium based ionic liquids
Phase equilibrium for ternary liquid systems of water + di-(2- ethylhexyl)phosphoric acid + organic diluents: Thermodynamic study
Solutions of alkyl methanoates and alkanes: Simultaneous modeling of phase equilibria and mixing properties. Estimation of behavior by UNIFAC with recalculation of parameters
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
Vapour-liquid equilibria of the ternary mixture (1-pentanol + 2,2,4-trimethylpentane + heptane) and the binary mixture (2,2,4-trimethylpentane + heptane) at T = 313.15 K for the characterization of second generation biofuels.
Solution thermodynamics of simvastatin in pure solvents and binary solvent mixtures
Experimental study on liquid - liquid equilibria of ionic liquids + alkane + ethyl benzene or p-xylene at 298.15 K
Experimental and predicted vapour-liquid equilibrium of the binary mixtures n-heptane + chlorobutane isomers
Extraction of benzene from heptane with pyridinium based ionic liquid at (298.15, 308.15 and 318.15) K
Liquid-liquid equilibria in the ternary and multicomponent systems involving hydrocarbons, thiophene or pyridine and ionic liquid (1-benzyl-3-metylimidazolium bis(trifluorometylsulfonyl)imide)
Solubility of heptane in aqueous solutions of methyldiethanolamine (MDEA)
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
Liquid-liquid equilibria for the extraction of phenols from alkane using ethylene glycol
Effect of cation alkyl chain length on liquid-liquid equilibria of {ionic liquids + thiophene + heptane}: COSMO-RS prediction and experimental verification
Quantitative comparison between predicted and experimental binary n-alkane p benzene phase behaviors using cubic and PC-SAFT EOS
Determination of solubility parameters from density measurements for non-polar hydrocarbons at temperatures from (298 to 433) K and pressures up to 137 MPa
Abraham model linear free energy relationships for describing the partitioning and solubility behavior of nonelectrolyte organic solutes dissolved in pyridine at 298.15 K
Effect of polarity and temperature on the binary interaction between D2EHPA extractant and organic solvents (kerosene, n-heptane, chlorobenzene and 1-octanol): Experimental and thermodynamics
Measurement and prediction of liquid-liquid equilibria in ternary systems containing water, an organic component, and cyclohexanol
Application of 1-hexyl-3-methylimidazolium trifluoromethanesulfonate to the removal of alcohol from mixtures with heptane
High selective water/butan-1-ol separation on investigation of limiting activity coefficients with [P8,8,8,8][[NTf2] ionic liquid
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
Quaternary isothermal vapor-liquid equilibrium of the model biofuel 2-butanone + n-heptane + tetrahydrofuran + cyclohexane using Raman spectroscopic characterization
Measurement of critical properties for binary and ternary mixtures containing potential gasoline additive diethyl carbonate (DEC)
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
Extraction of benzothiazole and thiophene from their mixtures with n-heptane using tetrahexylammonium bromide-based deep eutectic solvents as extractive denitrogenation and desulfurization agents
New ionic liquid [P4,4,4,4][NTf2] in bio-butanol extraction on investigation of limiting activity coefficients
Liquid-liquid equilibria of n-heptane, methanol and deep eutectic solvents composed of carboxylic acid and monocyclic terpenes
Ammonium ionic liquids in extraction of bio-butan-1-ol from water phase using activity coefficients at infinite dilution
Separation of thiophene, or benzothiophene from model fuel using glycols. Liquid-liquid phase equilibria and oxidative desulfurization study
Measurements of activity coefficients at infinite dilution for organic solutes in two quaternary ammonium-based ionic liquids [DDA][ClO4] and [DDA][BF4]
Density of biofuel mixtures (Dibutyl ether + Heptane) at temperatures from (298.15-393.15) K and at pressures up to 140 MPa: Experimental data and PC-SAFT modeling
Application of trihexyltetradecylphosphonium dicyanamide ionic liquid for various types of separations problems: Activity coefficients at infinite dilution measurements utilizing GLC method
The determination of activity coefficients at infinite dilution using g.l.c. for hydrocarbons in furfural at T = 278:15 K and T = 298:15 K
Thermodynamic properties of (an ester + an alkane). XVI. Experimental HEm and V Em values and a new correlation method for (an alkyl ethanoate + an n-alkane) at 318.15 K
Activity coefficients at infinite dilution for hydrocarbons in furfuryl alcohol at T=(278.15 and 298.15) K, determined by g.l.c.
Ternary (liquid + liquid) equilibria for mixtures of 1-hexyl-3-methylimidazolium (tetrafluoroborate or hexafluorophosphate) + benzene + an alkane at T = 298.2 K and p = 0.1 MPa
Physical properties of {anisole + n-alkanes} at temperatures between (293.15 and 303.15) K
Thermodynamic and acoustic properties of binary mixtures of alcohols and alkanes. I. Speed of sound in (ethanol + n-heptane) under elevated pressures
Thermodynamic and acoustic properties of binary mixtures of alcohols and alkanes. II. Density and heat capacity of (ethanol + n-heptane) under elevated pressures
Thermodynamic properties of (an ester + and alkane). XVII. Experimental He and Ve values for (an alkyl propanoate + an alkane) at 318.15K
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)
Excess molar volumes of the ternary system {methylcyclohexane (1) + cyclohexane (2) + n-alkanes (3)} at T = 298.15 K
Liquid phase behaviour of 1-hexyloxymethyl-3-methyl-imidazolium-based ionic liquids with hydrocarbons: The influence of anion
Activity coefficients at infinite dilution measurements for organic solutes in the ionic liquid hexyl-3-methyl-imidazolium bis(trifluoromethylsulfonyl)-imide using g.l.c. at T = (298.15, 313.15, and 333.15) K
Excess properties of the binary mixtures of methylcyclohexane + alkanes (C6 to C12) at T = 298.15 K to T = 308.15 K
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)
Experimental measurements and prediction of liquid densities for n-alkane mixtures
Measurement of activity coefficients at infinite dilution using polar and non-polar solutes in the ionic liquid 1-methyl-3-octyl-imidazolium diethyleneglycolmonomethylethersulfate at T = (288.15, 298.15, and 313.15) K
Excess molar heat capacities for (decan-1-ol + n-heptane) at temperatures from (290 to 318) K. Experimental results and theoretical description using the ERAS model
(p,rho,T,x) and viscosity measurements of {x1 n-heptane + (1 - x1) n-octane} mixtures at high temperatures and high pressures
High-pressure (vapor + liquid) equilibria in the (nitrogen + n-heptane) system
(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
Measurement of activity coefficients at infinite dilution in 1-hexadecyl-3-methylimidazolium tetrafluoroborate ionic liquid
Mixing properties of binary mixtures presenting azeotropes at several temperatures
Thermodynamic study of (perfluoroalkane + alkane) mixtures: Excess and solvation enthalpies
(Liquid + liquid) equilibria of {heptane + xylene + N-formylmorpholine} ternary system
Measurements of activity coefficients at infinite dilution of aromatic and aliphatic hydrocarbons, alcohols, and water in the new ionic liquid [EMIM][SCN] using GLC
Excess properties and vapour pressure of (3-diethylaminopropylamine + n-alkanes)
Solvent extraction of thiophene from n-alkanes (C7, C12, and C16) using the ionic liquid [C8mim][BF4]
Phase equilibria for mixtures containing nonionic surfactant systems: Modeling and experiments
Measurement and correlation of the (p, ?, T) relation of liquid n-heptane, n-nonane, 2,4-dichlorotoluene, and bromobenzene in the temperature range from (233.15 to 473.15) K at pressures up to 30 MPa for use as density reference liquids
Activity coefficients at infinite dilution measurements for organic solutes in the ionic liquid trihexyltetradecylphosphonium-bis-(2,4,4-trimethylpentyl)- phosphinate using g.l.c. at T = (303.15, 308.15, 313.15, and 318.15) K
Thermodynamic and acoustic properties of (heptane + dodecane) mixtures under elevated pressures
Measurement and correlation of (vapor + liquid) equilibria for the {2-propoxyethanol (C3E1) + n-hexane} and the {2-propoxyethanol (C3E1) + n-heptane} systems
Experimental and theoretical study of surface tension of binary mixtures of (n-alkyl acetates + heptane, benzene, and toluene)
Molar heat capacities for (2-methyl-2-butanol + heptane) mixtures and cyclopentanol at temperatures from (284 to 353) K
Phase diagrams of (hexane + methanol + 2,2,2-trifluoroethanol) at three temperatures: Measurement and correlation
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
Experimental densities, refractive indices, and speeds of sound of 12 binary mixtures containing alkanes and aromatic compounds at T = 313.15 K
(Liquid + liquid) equilibria for ternary mixtures of (alkane + benzene + [EMpy] [ESO4]) at several temperatures and atmospheric pressure
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
Excess enthalpies of binary and ternary mixtures containing dibutyl ether (DBE), 1-butanol, and heptane at T = 298.15 K and 313.15 K
Experimental and theoretical study of surface tension of n-pentane, n-heptane, and some of their mixtures at different temperatures
(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
Speed of sound, density, and heat capacity for (2-methyl-2-butanol + heptane) at pressures up to 100 MPa and temperatures from (293 to 318) K. Experimental results and theoretical investigations
(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
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
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
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 benzene from alkanes by solvent extraction with 1-ethylpyridinium ethylsulfate ionic liquid
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.
Volumetric and acoustic behaviour of systems containing n-hexane, or n-heptane and isomeric chlorobutanes
Activity coefficients at infinite dilution of organic solutes in N-alkylpyridinium bis(trifluoromethylsulfonyl)imide ([CnPY][NTf2], n = 2, 4, 5) using gas liquid chromatography
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
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
Thermodynamic study of (heptane + amine) mixtures. II. Excess and partial molar volumes at 298.15 K
Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate
Quaternary isobaric (vapor + liquid + liquid) equilibrium and (vapor + liquid) equilibrium for the system (water + ethanol + cyclohexane + heptane) at 101.3 kPa
Thermodynamic study of (heptane + amine) mixtures. III: Excess and partial molar volumes in mixtures with secondary, tertiary, and cyclic amines at 298.15 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
Thermodynamics and activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium tetracyanoborate
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
Compressed liquid densities for the (n-heptane + n-decane) and (n-octane + n-decane) systems from T = (313 to 363) K
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
(Liquid + liquid) equilibrium for binary systems of N-formylmorpholine with alkanes
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
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
Ternary (liquid + liquid) equilibria of {trifluorotris(perfluoroethyl)phosphate based ionic liquids + thiophene + heptane}
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
1-Alkyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide ionic liquids as solvents in the separation of azeotropic mixtures
Liquid-liquid extraction of aromatics from their mixtures with alkanes using 1-methyl 3-octylimidazolium thiocyanate ionic liquid
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
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 of aqueous solutions of butyric acid with n-heptane and toluene at T = (298.2, 308.2, and 318.2) K
Volumetric and acoustic properties of binary mixtures of tri-n-butyl phosphate with n-hexane, cyclohexane, and n-heptane from T = (298.15 to 323.15) K
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
Application of 1-alkyl-3-methylpyridinium bis(trifluoromethylsulfonyl)imide ionic liquids for the ethanol removal from its mixtures with alkanes
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
Separation of thiophene from heptane with ionic liquids
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
Measurement of critical temperatures and critical pressures for binary mixtures of methyl tert-butyl ether (MTBE) + alcohol and MTBE + alkane
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
Activity coefficients at infinite dilution of organic solutes in diethylene glycol and triethylene glycol from gas-liquid chromatography
Infinite dilution activity coefficients of volatile organic compounds in two ionic liquids composed of the tris(pentafluoroethyl) trifluorophosphate ([FAP]) anion and a functionalized cation
Solvent extraction of aromatic sulfur compounds from n-heptane using the 1-ethyl-3-methylimidazolium tricyanomethanide ionic liquid
Liquid density of biofuel mixtures: 1-Heptanol + heptane system at pressures up to 140 MPa and temperatures from 298.15 K to 393.15 K
Experimental and theoretical excess molar enthalpies of ternary and binary mixtures containing 2-Methoxy-2-Methylpropane, 1-propanol, heptane
Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium tricyanomethanide
Cation effect of ammonium imide based ionic liquids in alcohols extraction from alcohol-alkane azeotropic mixtures
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
Density, viscosity and excess molar volume of binary mixtures of tri-n-octylamine + diluents (n-heptane, n-octane, n-nonane, and n-decane) at various temperatures
Separation of sulfur compounds from alkanes with 1-alkylcyanopyridinium-based ionic liquids
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
Effect of the alkyl side chain of the 1-alkylpiperidinium-based ionic liquids on desulfurization of fuels
Measurement and correlation of critical properties for binary mixtures and ternary mixtures containing gasoline additives
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
Extraction desulfurization process of fuels with ionic liquids
Thermodynamics of solvation in propylene glycol and methyl cellosolve
Ternary (liquid + liquid) equilibria of {trifluorotris(perfluoroethyl) phosphate based ionic liquids + thiophene + heptane}: Part 2
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
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
(Liquid + liquid) extraction of methanol from alkanes using dialkylphosphate-based ionic liquids as solvents
Thermodynamic models for determination of the solubility of (-)-shikimic acid in different pure solvents and in (H2O + ethanol) binary solvent mixtures
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
Measurements and equation-of-state modelling of thermodynamic properties of binary mixtures of 1-butyl-1-methylpyrrolidinium tetracyanoborate ionic liquid with molecular compounds
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
(Liquid + liquid) equilibrium of ternary and quaternary systems containing heptane, cyclohexane, toluene and the ionic liquid [EMim][N(CN)2]. Experimental data and correlation
(Liquid + liquid) equilibria measurements for ternary systems (sulfolane + a carboxylic acid + n-heptane) at T = 303.15 K and at 0.1 MPa
Contributing to accurate high pressure viscosity measurements: Vibrating wire viscometer and falling body viscometer techniques
Mutual diffusion coefficients of isopropanol + n-heptane and isobutanol + n-heptane
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
Densities and derived thermodynamic properties for the (n-heptane + n-octane), (n-heptane + ethanol) and (n-octane + ethanol) systems at high pressures
Experimental determination of critical data of multi-component mixtures containing potential gasoline additives 2-butanol by a flow-type apparatus
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
Isothermal vapour-liquid equilibrium data for the binary systems of (CHF3 or C2F6) and n-heptane
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
Liquid-liquid extraction of toluene from alkane with pyridinium based ionic liquid ([BPy][NO3] and [HPy][NO3]) at 298.15 K and atmospheric pressure
Thermodynamics and limiting activity coefficients measurements for organic solutes and water in the ionic liquid 1-dodecyl-3-methylimidzolium bis(trifluoromethylsulfonyl) imide
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
Activity coefficients at infinite dilution of hydrocarbons in glycols: Experimental data and thermodynamic modeling with the GCA-EoS
High pressure densities and derived thermodynamic properties for the (n-heptane + n-octane + ethanol) ternary system
Surface tension and density of mixtures of m-xylene + n-alkane at 293.15 K: Analysis under the extended Langmuir and Shereshefsky models
Liquid-liquid equilibrium measurements and correlation for phase behaviors of alcohols + heptane + ILs ternary systems
Determination of melting temperatures in hydrocarbon mixtures by differential scanning calorimetry
Separation of binary mixtures hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on limiting activity coefficients
Mutual diffusion coefficients of n-butanol + n-heptane and n-pentanol + n-heptane from 288.15 K to 318.15 K
Thermodynamics and activity coefficients at infinite dilution for organic compounds and water in the ionic liquid 1-butyl-3-methylimidazolium perchlorate
Conformational analysis of branched alkanes using limiting partial molar volumes
Effect of temperature on intermolecular interactions between the organic solvents: Insights from density and excess volume
Thermodynamics of mixtures containing aromatic nitriles
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
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]
Removal of 2- and 3-methylthiophene from their mixtures with n-heptane using tetrahexylammonium bromide-based deep eutectic solvents as extractive desulfurization agents
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
Determination of the thermodynamic parameters of ionic liquid 1-propyl-3-methylimidazolium bromide by gas-liquid chromatography
Liquid-liquid extraction of sulfur compounds from heptane with tricyanomethanide based ionic liquids
Mutual diffusion coefficients of 3-methyl-1-butanol + n-heptane and 2-methyl-1-butanol + n-heptane from 288.15 K to 318.15 K
Isobaric vapor-liquid equilibrium of three binary systems containing dimethyl succinate, dimethyl glutarate and dimethyl adipate at 2, 5.2 and 8.3 kPa
Determination and correlation of solubility and solution thermodynamics of musk xylene in different pure solvents
Liquid-liquid equilibria for (2-hydroxy benzaldehyde + n-alkane) mixtures. Intermolecular and proximity effects in systems containing hydroxyl and aldehyde groups
Excess volumes, densities, speeds of sound and viscosities for the binary systems of diisopropyl ether with hydrocarbons at 303.15K
Thermophysical properties and thermodynamic phase behavior of ionic liquids
Topological and thermodynamic investigations of binary mixtures: Molar excess volumes, molar excess enthalpies and isentropic compressibility changes of mixing
Experimental determination and modelling of densities and excess molar volumes of ternary system (1-butanol + cyclohexylamine + n-heptane) and corresponding binaries from 288.15 to 323.15K
Excess molar volumes and isentropic compressibilities changes of mixing of tetrahydropyran + benzene + cyclo or n-alkanes ternary mixtures at 308.15 K
Thermodynamic properties of binary mixtures containing Tetrahydropyran: Excess molar volumes, Excess molar enthalpies and isentropic compressibilities changes of mixing
THERMODYNAMICS OF MIXTURES CONTAINING ALKOXYETHANOLS. XXVIII. LIQUID-LIQUID EQUILIBRIA FOR 2-PHENOXYETHANOL + SELECTED ALKANES
Thermophysical Study of the n-Hexane or n-Heptane with 1- Chloropropane Systems
Excess molar volumes of (1-chlorobutane +heptane + 2-butanone or 2-pentanone) at 288.15 , 303.15 and 313.15 K . Measurements and correlations.
Determination of the solubility, dissolution enthalpy and entropy of 3-pentadecylphenyl acrylate in different organic solvents
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
THERMODYNAMICS OF MIXTURES CONTAINING AMINES. XIV. CpEm OF BENZYLAMINE WITH HEPTANE AT 293.15 K OR WITH METHANOL, 1-PROPANOL OR 1-PENTANOL AT (293.15-308.15) K
Excess properties from p.rho.T data for n-heptane + isomeric chlorobutane mixtures
Viscosity measurements of hydrocarbon fuel at temperatures from (303.2 to 513.2) K and pressures up to 5.1 MPa using a two-capillary viscometer
Temperature and pressure dependence of densities and viscosities for binary mixtures of methyl decanoate plus n-heptane
Density and Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane + n-Heptane, 2,2,4-Trimethylpentane + n-Octane, Ethyl Acetate + Benzene, and Butanenitrile + Benzene from (293.15 to 323.15) K
Capillary Viscometer and Vibrating Tube Densimeter for Simultaneous Measurements up to 70 MPa and 423 K
Phase Equilibria in Systems of Morpholine, Acetonitrile, and n-Alkanes
Solubility Measurement and Correlation for 2- Naphthaldehyde in Pure Organic Solvents and Methanol + Ethanol Mixtures
Experimental and Computational Study on Liquid Liquid Equilibrium in Ternary Systems of -Valerolactone, Toluene, and Hydrocarbons
Experimental and Modeling Study of the Phase Behavior of (Heptane + Carbon Dioxide + Water) Mixtures
Vapor Liquid Equilibria of n-Heptane + Toluene +1-Ethyl-4-methylpyridinium Bis(trifluoromethylsulfonyl)imide Ionic Liquid
Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane +1-Alkanols from 298.15 to 323.15 K
Solubility of Ethene in n-Hexane and n-Heptane as Common Slurry-Phase Polymerization Solvents: Experimental Measurement and Modeling
Activity Coefficients at Infinite Dilution of Organic Solutes and Water in Tributylethylphosphonium Diethylphosphate Using Gas Liquid Chromatography: Thermodynamic Properties of Mixtures Containing Ionic Liquids
Vapor Liquid Equilibria Measurements for the Five Linear C6 Esters with n-Octane
Solubility of 2-Ethylanthraquinone in Binary Mixtures of Oligooxymethylene Dimethyl Ethers with Different Number of CH2O Groups of n = 2, 3, and 4 from 293.15 to 343.15 K
Viscosity Measurement of Endothermic Fuels at Temperatures from 303 K to 673 K and Pressures up to 5.00 MPa
Vapor Liquid Equilibria Measurements for Di-n-Propyl Ether and Butyl Ethyl Ether with n-Heptane
Diffusion Coefficients of Carbon Dioxide in Eight Hydrocarbon Liquids at Temperatures between (298.15 and 423.15) K at Pressures up to 69 MPa
Liquid Liquid Equilibria Data for Ethylbenzene or p-Xylene with Alkane and 1-Butylpyridinium Nitrate Ionic Liquid at 298.15 K
Measurement and Correlation of Liquid Liquid Equilibrium for Quaternary Systems of Water + Methanol or Ethanol + Ethyl Methyl Carbonate + Heptane at 25 deg C
L(+)-tartaric Acid Separations Using Aliquat 336 in n-Heptane, Kerosene, and 1-Octanol at 300 +- 1 K
Vapor Liquid Equilibrium and Excess Enthalpy Data for Systems Containing N,N-Dimethylacetamide
Densities and Viscosities of Corn Oil + n-Alkanes Blends from (288.15 to 343.15) K at 0.1 MPa
Phase Behavior of the System (Carbon Dioxide + n-Heptane + Methylbenzene): A Comparison between Experimental Data and SAFT-gamma-Mie Predictions
The Critical Temperatures of a Number of (i) (Chloroalkane (C3 C4) + Hydrocarbon (C6 C7)) Binary Mixtures and (ii) (Aromatic Halocarbon (Chlorobenzene, Fluorobenzene, 1,2-Dichlorobenzene, or 1,3-Dichlorobenzene) + Alkane (C8)) Binary Mixtures
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
Extraction of Low Concentration Aqueous Solution of Methylal: Liquid Liquid Equilibrium in Water + Methylal + (Cyclohexane and n-Heptane) Ternary Systems
Isothermal Vapor-Liquid Equilibria for Binary Mixtures of Methyl Nonafluorobutyl Ether + Acetone, Cyclopentyl Methyl Ether, Ethyl Acetate, n-Heptane, Methanol, and Toluene
Liquid-Liquid Extraction of Butanol from Heptane + Butanol Mixture by Ionic Liquids
Experimental Vapor-Liquid Equilibria and Thermodynamic Modeling of the Methanol + n-Heptane and 1-Butanol + Aniline Binary Systems
Isobaric Vapor-Liquid Equilibrium for Two Binary Systems of n-Heptane + sec-Butyl Acetate and Methylcyclohexane + sec-Butyl Acetate under Atmosphere
Density of Working Liquids for Diffusion Vacuum Pumps
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
Bubble Pressure Measurement and Prediction for n-Hexadecane and n-Eicosane + Cyclohexane, Methylcyclohexane, and Ethylcyclohexane Binary Mixtures from 303.15 to 393.15 K
Measurement of the Speed of Sound in Near-Critical and Supercritical n-Heptane at Temperatures from (513.40 to 650.90) K and Pressures from (2.5 to 10.0) MPa
Liquid Density of Mixtures of Methyl Nonafluorobutyl Ether (HFE-7100) + n-Heptane at Pressures up to 80 MPa and Temperatures from 298.15 to 393.15 K
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
Solubilities of Organic Semiconductors and Nonsteroidal Anti-inflammatory Drugs in Pure and Mixed Organic Solvents: Measurement and Modeling with Hansen Solubility Parameter
Measurement of Critical Properties for Binary and Ternary Mixtures Containing n-Butanol and n-Alkane
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
Determination of Activity Coefficients at Infinite Dilution of Solutes in N,N'-Di(2-ethylhexyl)isobutyramide Using Inverse Gas-Liquid Chromatography
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
A New Test System for Distillation Efficiency Experiments at Elevated Liquid Viscosities: Vapor-Liquid Equilibrium and Liquid Viscosity Data for Cyclopentanol + Cyclohexanol
Experimental Study on Reactive Extraction of Malonic Acid with Validation by Fourier Transform Infrared Spectroscopy
Solubility Determination and Correlation of Warfarin Sodium 2-Propanol Solvate in Pure, Binary, and Ternary Solvent Mixtures
Separation of Alkylbenzenes from n-Heptane Using Binary Mixtures of Ionic Solvents
Liquid Liquid Equilibrium Data for the Separation of Acetone from n-Heptane Using Four Imidazolium-Based Ionic Liquids
Solubilities of 2,6-Dimethylnaphthalene in Six Pure Solvents and Two Binary Solvent Systems
Effect of Diluents on Extraction Equilibrium of trans-Aconitic Acid
Measuring Activity Coefficient at Infinite Dilution of Hydrocarbons in Ionic Liquids and Evaluation of Other Thermodynamic Properties using Gas Chromatography
Liquid-Liquid Equilibrium for Ternary Systems of N-Methylformamide + Pyrrole/Indole + Alkanes at 298.15 K: Phase Equilibrium Measurement and Correlation
(r, VE, T) Measurements of the Ternary Mixture (Dibutyl Ether + 1-Heptanol + Heptane) at Temperatures up to 393.15 K and Pressures up to 140 MPa and Modeling Using the Peng-Robinson and PC-SAFT Equations of State
Assessment of Pyrrolidinium-Based Ionic Liquid for the Separation of Binary Mixtures Based on Activity Coefficients at Infinite Dilution
Liquid-Liquid Equilibrium Data for Ternary Systems Containing Alkanes (n-Pentane, n-Hexane, n-Heptane, and n-Octane) + Alcohol (Methanol and Ethanol) + Protic Ionic Liquid (2-HEAF)
Liquid-Liquid Equilibrium Measurements for the Extraction of Pyridine and Benzothiazole from n-Alkanes Using Deep Eutectic Solvents
Measurement of VLE Data by Using an Experimental Installation with Automatic Control: Modeling of Binary Systems of Methyl Acetate or Ethyl Acetate with n-Heptane or 2,2,4-Trimethylpentane at Both 0.1 and 1.5 MPa
Thermodynamic Properties of Mixtures Containing Precursors of Vitamin B5
Viscosities of Dimethyl Carbonate or Diethyl Carbonate with Alkanes at Four Temperatures. New UNIFAC-VISCO Parameters
Surface Tension of Pure Liquids and Binary Liquid Mixtures
Solubility of 1-Alkyl-3-methylimidazolium Hexafluorophosphate in Hydrocarbons
Excess Molar Enthalpies for Binary Mixtures of Ethanol + Acetone, + Octane, + Cyclohexane and 1-Propanol + Acetone, + Octane, + Heptane at 323.15
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
Ternary Liquid-Liquid Equilibria for Mixtures of 1-Methyl-3-octylimidazolium Chloride + an Alkanol + an Alkane at 298.2 K and 1 bar
Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Hexyl-3-methylimidazolium Hexafluorophosphate from Gas-Liquid Chromatography
Solubilities of n-Alkanes (C6 to C8) in Water from 30 0C to 180 0C.
Bubble Temperature Measurements on the Binary Mixtures of n-Heptane or Nitrobenzene or Chlorobenzene with Some Chloroethanes and Chloroethylenes at (94.6 to 95.8) kPa
Isobaric Vapor-Liquid Equilibria and Excess Properties for the Binary Systems of Methyl Esters + Heptane
Measurement of Activity Coefficients of Solutes at Infinite Dilution in (Dimethyl Sulfoxide + Acetamide, or Formamide, or Urea) Using Gas Liquid Chromatography at the Temperature 298.15 K
Speed of Sound in Propan-1-ol + Heptane Mixtures under Elevated Pressures
Bubble-Temperature Measurements on Some Binary Mixtures Formed by Tetrahydrofuran or Amyl Alcohol with Hydrocarbons, Chlorohydrocarbons, or Butanols at (94.6 or 95.8) kPa
Densities and Excess Molar Properties of Dimethyl Carbonate with Alkanes (C6 to C10) and VLE of Dimethyl Carbonate with Alkanes (C9 to C10) at 101.3 kPa
Determination of Activity Coefficients at Infinite Dilution of Solutes in the Ionic Liquid 1-Hexyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography at the Temperatures 298.15 K and 323.15 K
Excess Enthalpies of Binary Mixtures of 1-Hexene with Some n-Alkanes at 298.15 K
Limiting Activity Coefficients by Comparative Tensimetry: 1-Propanol and 1-Butanol in Heptane and in Octane
Measurement and Correlation of Mutual Solubilities for High Viscosity Binary Systems: Aniline + Methylcyclohexane, Phenol + Heptane, Phenol + Octane, and Glycerol + 1-Pentanol
Solubility of Benzophenone in Binary Alkane + Carbon Tetrachloride Solvent Mixtures
Volumetric Properties of Binary Tetraethylene Glycol Dimethyl Ether + Heptane Mixtures between (278.15 and 353.15) K and up to 25 MPa
Surface Tension and Interfacial Tension of Binary Organic Liquid Mixtures
Isothermal Vapor-Liquid Equilibria for the 2-Propanol + n-Heptane System near the Critical Region
Analysis and Evaluation of the Liquid-Liquid Equilibrium Data of the Extraction of Aromatics from Hydrocarbons by Tetraethylene Glycol
Determination and Study on the Solubility of Methane in Heptane + Cyclohexane and Heptane + Ethanol at High Pressures
Solubilities of Bis (2,2,6,6-Tetramethyl-4-Piperidinyl) Maleate in Hexane, Heptane, Octane, m-Xylene and Tetrahydrofuran from (253.15 to 310.15) K
Liquid-Liquid Equilibria for Monoethylene Glycol + Water + Alkane Systems in the Range (273 to 313) K and Atmospheric Pressure
Vapor Pressures of n-Heptane Determined by Comparative Ebulliometry
Compressed Liquid Densities of Squalane and Pentaerythritol Tetra(2-ethylhexanoate)
Liquid-Liquid Equilibrium for the System Heptane + o-Xylene + Diethylene Glycol over the Temperature Range of 288.15 K to 318.15 K
Phase Separation in Binary Mixtures Containing Linear Perfluoroalkanes
Experimental Dynamic Viscosities of 2,3-Dimethylpentane up to 60 MPa and from (303.15 to 353.15) K Using a Rolling-Ball Viscometer
Vapor-Liquid Equilibrium Data for the Binary Decafluoropentane (HFC-43-10meec) + Heptane, Decafluoropentane + Butyl Ethyl Ether, Octafluorobutane (HFC-338pcc) + Butyl Ethyl Ether, and Heptafluoro Propyl Methyl Ether (HFE-347mcc) + HFC-338pcc Systems at 101.3 kPa
Thermodynamic Properties of Binary Mixtures of p-Xylene with Cyclohexane, Heptane, Octane, and N-Methyl-2-pyrrolidone at Several Temperatures
Excess Molar Volumes and Viscosities of Binary Mixtures of Dimethyl Carbonate with Chlorobenzene, Hexane, and Heptane from (293.15 to 353.15) K and at Atmospheric Pressure
Determination of Activity Coefficients at Infinite Dilution of Polar and Nonpolar Solutes in the Ionic Liquid 1-Ethyl-3-methyl- imidazolium Bis(trifluoromethylsulfonyl) Imidate Using Gas-Liquid Chromatography at the Temperature 303.15 K or 318.15 K
Thermodynamics of Mixtures Containing Ethers. Part III. Liquid-Liquid Equilibria for 2,5,8,11-Tetraoxadodecane or 2,5,8,11,14-Pentaoxapentadecane + Selected N-Alkanes
Surface and interfacial tension of the ternary system heptane + toluene + N,N-dimethylformamide
Vapor-Liquid Equilibria for the Ternary Systems of Methyl tert-Butyl Ether + Methanol + Methylcyclohexane and Methyl tert-Butyl Ether + Methanol + n-Heptane and Constituent Binary Systems at 313.15 K
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
Thermodynamic Properties of Mixtures Containing Ionic Liquids. 5. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in 1-Methyl-3-butyl-imidazolium Bis(trifluoromethyl-sulfonyl) Imide Using Gas-Liquid Chromatography
Thermodynamic Properties of Mixtures Containing Ionic Liquids. 6. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in 1-Methyl-3-octyl-imidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
Surface Properties of Dilute Solutions of Alkanes in Benzyl Alcohol
Ternary and Quaternary Liquid-Liquid Equilibria of Water + Methanol + Diisopropyl Ether and Water + Methanol + Diisopropyl Ether + Toluene Mixtures
High-Pressure Density Measurements for the Binary System Ethanol + Heptane
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
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
Thermodynamics of Mixtures Containing a Strongly Polar Compound. 8. Liquid-Liquid Equilibria for N,N-Dialkylamide + Selected N-Alkanes
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 Ternary Mixtures (an Ionic Liquid + Benzene +Heptane or Hexadecane) at T ) 298.2 K and Atmospheric Pressure
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)
Activity Coefficients at Infinite Dilution in 1-Alkyl-3-methylimidazolium Tetrafluoroborate Ionic Liquids
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
Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Butyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
Density and Surface Tension Variation with Temperature for Heptane + 1-Alkanol
Isothermal Vapor-Liquid Equilibria and Excess Enthalpies of (Propyl Ethanoate + Heptane), (Propyl Ethanoate + Cyclohexane), and (Propyl Ethanoate + 1-Hexene)
Heat Capacity, Speed of Ultrasound, and Density for 1,5-Dibromopentane + Heptane within the Temperature Range from 293.15 K to 313.15 K
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
Diffusion Coefficients of Aromatic Compounds at Infinite Dilution in Binary Mixtures at 298.15 K
Infinite Dilution Activity Coefficients for Trihexyltetradecyl Phosphonium Ionic Liquids: Measurements and COSMO-RS Prediction
Thermophysical and Acoustical Properties of the Binary Mixtures 1,2-Dibromoethane + Heptane within the Temperature Range from 293.15 K to 313.15 K
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 Anthracene in Binary Diisopropyl Ether + Alkane Solvent Mixtures at 298.15 K
Solubility of 5-(Dithiolan-3-yl)pentanoic Acid in the Mixed Solvents of Cyclohexane + Ethyl Acetate, Heptane + Ethyl Acetate, and Hexane + Ethyl Acetate
Activity Coefficients at Infinite Dilution Measurements for Organic Solutes and Water in the Ionic Liquid 1-Butyl-3-methyl-pyridinium Trifluoromethanesulfonate
Solubility of Artemisinin in Different Single and Binary Solvent Mixtures Between (284.15 and 323.15) K and NRTL Interaction Parameters
Separation of Benzene from Linear Alkanes (C6-C9) Using 1-Ethyl-3-Methylimidazolium Ethylsulfate at T = 298.15 K
Interfacial Tension of n-Alkane and Ionic Liquid Systems
Determination of Activity Coefficients at Infinite Dilution of 35 Solutes in the Ionic Liquid, 1-Butyl-3-methylimidazolium Tosylate, Using Gas-Liquid Chromatography
Experimental Determination of Densities and Refractive Indices of the Ternary Mixture 2-Methyl-2-propanol + Cyclohexylamine + n-Heptane at T = (303.15 to 323.15) K
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
Thermodynamic and Acoustic Properties of Mixtures of 1,6-Dichlorohexane with Heptane from (293 to 313) K
Measurement of Heat Capacity by Adiabatic Calorimetry and Calculation of Thermodynamic Functions of Standard Substances: Copper, Benzoic Acid, and Heptane (For Calibration of an Adiabatic Calorimeter)
Solubility of Benzoic Acid in Pure Solvents and Binary Mixtures
Liquid-Liquid(-Liquid) Equilibria in Ternary Systems of Aliphatic Hydrocarbons (Heptane or Octane) + Phenols + Water
Influence of Compressed Carbon Dioxide on the Capillarity of the Gas-Crude Oil-Reservoir Water System
Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Liquid-Liquid Equilibria Measurement of Systems Involving Alkanes (Heptane and Dodecane), Aromatics (Benzene or Toluene), and Furfural
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
Measurements of Activity Coefficients at Infinite Dilution for Organic Solutes and Water in the Ionic Liquid 1-Butyl-1-methylpiperydinium Thiocyanate
Measurement and Correlation for the Solubilities of Dihydrocapsaicin in n-Heptane, n-Hexane, n-Pentane, Ethyl Acetate, Acetone, Ethanol, and Water
Influence of Anion Structure on the Liquid-Liquid Equilibria of 1-Ethyl-3-methyl-imidazolium Cation Based Ionic Liquid-Hydrocarbon Binary Systems
Vapor-Liquid Equilibrium in the Binary Systems 2-Butanol + tert-Amyl Methyl Ether, 2-Butanol + Heptane, and Heptane + tert-Amyl Methyl Ether
Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Butyl-3-methylimidazolium Nitrate Using Gas-Liquid Chromatography
Solubility of 2-(2,4,6-Trichlorophenoxy)ethyl Bromide in Methanol, Ethanol, Propanol, Isopropanol, Acetonitrile, n-Heptane, and Acetone
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 and Predicted Kinematic Viscosities for Alkane + Chloroalkane Mixtures
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
Apparent and Partial Molar Volumes at Infinite Dilution and Solid Liquid Equilibria of Dibenzothiophene + Alkane Systems
Extraction of Benzene from Aliphatic Compounds Using Commercial Ionic Liquids as Solvents: Study of the Liquid Liquid Equilibrium at T = 298.15 K
Interfacial Tensions of Imidazolium-Based Ionic Liquids with N-Alkanes and Cyclohexane
Extraction of n-Alcohols from n-Heptane Using Ionic Liquids.
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
Thermodynamic Study of Heptane + Silicone Mixtures. Excess Volumes and Enthalpies at 298.15 K
Excess Properties and Vapor Pressure of 2-Diethylaminoethylamine + n-Heptane
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
Computer Aided Solvent scanning for the Separation of 2-methoxynaphthene and 2-acetyl-6-methoxynaphthalene
Evaluation of the Performance of Trigeminal Tricationic Ionic Liquids for Separation Problems
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
Thermodynamics of Mixtures Containing Aromatic Alcohols. 1. Liquid Liquid Equilibria for (Phenylmethanol + Alkane) Systems
Isobaric Vapor Liquid Equilibria of Tertiary Amine and n-Alkane/Alkanol Binary Mixtures: Experimental Measurements and Modeling with GC-PPC-SAFT
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
Excess Molar Volumes and Speed of Sound in Bromotrichloromethane + n-Heptane, Dibromomethane + n-Heptane, Bromotrichloromethane + Dibromomethane, and Bromotrichloromethane + Bromochloromethane at Temperatures from (293.15 to 313.15) K
Measurements and Correlations of the Isobaric Vapor Liquid Equilibria of Binary Mixtures and Excess Properties for Mixtures Containing an Alkyl (Methyl, Ethyl) Butanoate with an Alkane (Heptane, Nonane) at 101.3 kPa
Liquid Liquid Equilibria for Dipropylene Glycol Hydrocarbon Binary Systems: Experimental Data and Regression
Multiproperty Correlation of Experimental Data of the Binaries Propyl Ethanoate + Alkanes (Pentane to Decane). New Experimental Information for Vapor Liquid Equilibrium and Mixing Properties
Temperature and Composition Effect on CO2 Miscibility by Interfacial Tension Measurement
Densities of Cresols and Linear Alkane Mixtures at High Pressure
(p, rho, T) Behavior for the Binary Mixtures Carbon Dioxide + Heptane and Carbon Dioxide + Tridecane
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
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
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
Vapor Liquid Equilibrium Data for the Morpholine-4-carbaldehyde + n-Hexane or n-Heptane Binary Systems Using a Static-Synthetic Apparatus
Liquid Liquid Equilibria of Benzene + n-Heptane + N,N-Dimethylformamide and Benzene + n-Heptane + N,N-Dimethylformamide + Ammonium Thiocyanate
Solubility and Dissolution Thermodynamic Data of Mefenamic Acid Crystals in Different Classes of Organic Solvents
Excess Molar Volumes and Viscosities of Binary Systems of Butylcyclohexane with n-Alkanes (C7 to C14) at T = 293.15 K to 313.15 K
Improvements in the Experimentation and the Representation of Thermodynamic Properties (iso-p VLE and yE) of Alkyl Propanoate + Alkane Binaries
Solubility of Dichloronitrobenzene in Eight Organic Solvents from T = (278.15 to 303.15) K: Measurement and Thermodynamic Modeling
Infinite Dilution Activity Coefficients of Solutes Dissolved in Two Trihexyl(tetradecyl)phosphonium Ionic Liquids
Experimental and Modeling of the Propene Solubility in the Heptane and Methylbenzene Solvents
Design of a Gamma Densitometer for Hydrocarbon Fuel at High Temperature and Supercritical Pressure
Liquid Liquid Equilibria for the Systems: Heptane + Benzene + Solvent (Propylene carbonate, N,N-Dimethylformamide, or Mixtures) at Temperatures from (303.2 to 323.2) K
Comparison Study on Temperature Dependence of the Interfacial Tension of n-Alkane Water and n-Alcohol Water Two Binary Systems
Enhancing liquid-phase olefin-paraffin separations using novel silver-based ionic liquids
Oxygenated Compounds + Hydrocarbon Mixtures in Fuels and Biofuels: Excess Enthalpies of Ternary Mixtures Containing 1-Butoxybutane + Propan-1-ol +1-Hex-1-ene, or Heptane, or 2,2,4-Trimethylpentane at (298.15 and 313.15) K
Liquid Liquid Equilibria for Quaternary Systems of Water + Ethanol + Diethyl Carbonate + Methylbenzene or Heptane
Liquid Liquid Equilibrium in Mixtures Containing Propane-1,2,3-triol and Mixtures Containing Vegetable Oils at Atmospheric Pressure
Density, Viscosity, Speed of Sound, Bulk Modulus, and Surface Tension of Binary Mixtures of n-Heptane + 2,2,4-Trimethylpentane at (293.15 to 338.15) K and 0.1 MPa
Determination of the Critical Properties of C6 C10 n-Alkanes and Their Binary Systems Using a Flow Apparatus
Experimental Study: The Impact of Dissolved Water on the Viscosity of Reservoir Fluids at HPHT Conditions
Selective Separation of Aromatics from Paraffins and Cycloalkanes Using Morpholinium-Based Ionic Liquid
P ? T Data for 1-Butanol and Isobutyl Alcohol from (283.15 to 363.15) K at Pressures up to 66 MPa
Solubility Determination and Thermodynamic Models for 2-Methylnaphthalene in Different Solvents from T = (278.15 to 303.15) K
Binary Liquid Liquid Equilibria of ?-Valerolactone with Some Hydrocarbons
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 of the Critical Properties of the Ternary Systems Hexane + Heptane + Octane and Octane + Nonane + Decane Using a Flow Apparatus
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
Densities and Viscosities of MTBE + Heptane or Octane at p ) 0.1 MPa from (273.15 to 363.15) K
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
Measurement of Activity Coefficient at Infinite Dilution of Hydrocarbons in Sulfolane Using Gas-Liquid Chromatography
Liquid - Liquid Equilibria for the Binary Systems of Sulfolane with Alkanes
Densities and Viscosities of Ternary Mixtures of Heptane, Octane, Nonane, and Hexyl Benzene from 293.15 K to 313.15 K
Measurements and Calculation of Vapor-Liquid Equilibria for the Binary Mixtures of Fluorobenzene and Alkanes at a Pressure of 101.4 kPa
Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Butyl-3-methylimidazolium Trifluoromethanesulfonate Using Gas-Liquid Chromatography
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
Liquid Liquid Equilibria of Mixtures Containing Methyl Acetate + Methanol + Hexane or Heptane
Diffusion Coefficients of Organic Compounds at Infinite Dilution in Mixtures Involving Associating Compounds. Experimental Determination and Modeling by Group Contribution Methods
Influence of the Temperature on the Liquid Liquid Equilibria of Heptane + Toluene + Sulfolane and Heptane + m-Xylene + Sulfolane
Solubilities of Stearic Acid in Organic Solvents and in Azeotropic Solvent Mixtures
Liquid Liquid Equilibria for the Ternary Systems Water + n-Pentanoic Acid with n-Heptane or Dichloromethane at 298.2 K
Excess Enthalpies and Thermal Conductivity Coefficients for Binary Mixtures of Carbon Tetrachloride and Four Alkanes (C5 to C8) at a Temperature of 298.15 K
Phase Equilibrium Properties of Binary and Ternary Mixtures Containing Dibutyl Ether, Cyclohexane, and Heptane or 1-Hexene at T ) 313.15 K
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
Enthalpies of Vaporization and Vapor Pressures of Some Deuterated Hydrocarbons. Liquid-Vapor Pressure Isotope Effects
Determination of Activity Coefficients at Infinite Dilution of Solutes in the Ionic Liquid, Trihexyltetradecylphosphonium Bis(trifluoromethylsulfonyl) Imide, Using Gas-Liquid Chromatography at T ) (303.15, 308.15, 313.15, and 318.15) K
Liquid-Liquid Equilibrium of (Cyclohexane + 2,2,2-Trifluoroethanol) and (Cyclohexane + Methanol) from (278.15 to 318.15) K
Determination and Correlation of Excess Molar Enthalpies of Eight Binary Systems Containing Acetophenone at Different Temperatures
Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Ethyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
Solubility of Diamantane, Trimantane, Tetramantane, and Their Derivatives in Organic Solvents
Effect of Temperature on Phase Equilibrium of the Mixed-Solvent System of (2,2,2-Trifluoroethanol + Methanol + Cyclohexane)
Densities and Viscosities of Binary Mixtures of Tri-n-butyl Phosphate + Cyclohexane, + n-Heptane at T ) (288.15, 293.15, 298.15, 303.15, and 308.15) K
Surface Tension of Dilute Solutions of Alkanes in Cyclohexanol at Different Temperatures
Solubility of the Antimicrobial Agent Triclosan in Organic Solvents of Different Hydrogen Bonding Capabilities at Several Temperatures
Solubilities of Palmitic Acid in Pure Solvents and Its Mixtures
Phase Equilibria Study of the Binary Systems (N-Butyl-4-methylpyridinium Tosylate Ionic Liquid + Organic Solvent, or Water)
Activity Coefficients at Infinite Dilution of Organic Compounds in 1-Butyl-3-methylimidazolium Tetrafluoroborate Using Inverse Gas Chromatography
Activity Coefficients at Infinite Dilution of Organic Compounds in Trihexyl(tetradecyl)phosphonium Bis(trifluoromethylsulfonyl)imide Using Inverse Gas Chromatography
In Situ Determination of Phase Equilibria of Methyl Benzoate + Alkane Mixtures Using an Infrared Absorption Method. Comparison with Polar GC-SAFT Predictions
Surface Tension of 2,2-Dimethylbutane from (233 to 378) K
Mutual Diffusion Coefficients of Diethyl Carbonate and Diethyl Adipate in Heptane at T = (278.15 to 338.15) K under Atmospheric Pressure
Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-(2-Hydroxyethyl)-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
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
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
Phase Equilibria of (1-Hexyl-3-methylimidazolium Thiocyanate + Water, Alcohol, or Hydrocarbon) Binary Systems
Experimental Measurement and Correlation of the Solubilities of 2,4-Dichloro-5-methoxypyrimidine in Ethyl Ethanoate, Methanol, Ethanol, Acetone, Tetrachloromethane, and Heptane at Temperatures between (295 and 320) K
Phase Equilibria for Liquid Mixtures of (an Alkane + Toluene + Dimethyl Phthalate)
Heat Capacities of Binary Mixtures of Acetic Acid with Acetic Anhydride and Methenamine at Different Temperatures
Density, Viscosity, and Speed of Sound of (Methyl Benzoate + Cyclohexane), (Methyl Benzoate + n-Hexane), (Methyl Benzoate + Heptane), and (Methyl Benzoate + Octane) at Temperatures of (303.15, 308.15, and 313.15) K
Isobaric Vapor-Liquid Equilibria of Heptane + 1-Butanol and Heptane + 1-Pentanol Systems at (53.3 and 91.3) kPa
Surface Tension of Diethyl Ether, Diisopropyl Ether, and Dibutyl Ether
Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in Glycerol Using Gas-Liquid Chromatography
Densities and Excess Molar Volumes of 2-Butanol + Cyclohexanamine + Heptane and 2-Butanol + n-Heptane at Temperatures between (288.15 and 323.15) K
Thermodynamics of Mixtures Containing a Strongly Polar Compound. 9. Liquid-Liquid Equilibria for epsilon-Caprolactam + Selected Alkanes
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
Volumetric and Viscous Properties at Several Temperatures for Binary Mixtures of N-Methylpiperazine with Methylcyclohexane or n-Heptane
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
KDB
Aqueous Solubility Prediction Method
Estimated Solubility Method
McGowan Method
NIST Webbook
The Yaws Handbook of Vapor Pressure
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