Contents
Physical Properties
Temperature Dependent Properties
Datasets
Correlations
Similar Compounds
Mixtures
Sources
Physical Properties
Property
Value
Unit
Source
PAff
856.00
kJ/mol
NIST
BasG
826.90
kJ/mol
NIST
Δf G°
-102.52
kJ/mol
Joback Calculated Property
Δf H°gas
[-317.80; -314.00]
kJ/mol
Δf H°gas
-317.80
kJ/mol
NIST
Δf H°gas
-314.00 ± 2.00
kJ/mol
NIST
Δf H°liquid
-350.80 ± 2.60
kJ/mol
NIST
Δfus H°
5.07
kJ/mol
Joback Calculated Property
Δvap H°
[32.97; 33.10]
kJ/mol
Δvap H°
32.97
kJ/mol
NIST
Δvap H°
33.10 ± 0.40
kJ/mol
NIST
IE
9.39 ± 0.01
eV
NIST
log 10 WS
-1.53
Crippen Calculated Property
log Poct/wat
1.821
Crippen Calculated Property
McVol
101.270
ml/mol
McGowan Calculated Property
Pc
3114.04
kPa
Joback Calculated Property
Inp
[586.00; 637.00]
Inp
612.70
NIST
Inp
612.00
NIST
Inp
Outlier 586.00
NIST
Inp
Outlier 587.00
NIST
Inp
620.00
NIST
Inp
624.00
NIST
Inp
620.00
NIST
Inp
637.00
NIST
Inp
616.00
NIST
Inp
615.40
NIST
Inp
620.00
NIST
Inp
621.00
NIST
Inp
620.00
NIST
Inp
612.70
NIST
I
[710.00; 710.00]
I
710.00
NIST
I
710.00
NIST
Tboil
[345.60; 346.30]
K
Tboil
346.10 ± 0.50
K
NIST
Tboil
346.30
K
NIST
Tboil
345.60
K
NIST
Tboil
345.90 ± 0.30
K
NIST
Tc
531.48
K
Joback Calculated Property
Tfus
179.15 ± 0.20
K
NIST
Vc
0.379
m3 /kmol
Joback Calculated Property
Temperature Dependent Properties
Property
Value
Unit
Temperature (K)
Source
Cp,gas
[182.43; 245.69]
J/mol×K
[355.87; 531.48]
Cp,gas
182.43
J/mol×K
355.87
Joback Calculated Property
Cp,gas
194.11
J/mol×K
385.14
Joback Calculated Property
Cp,gas
205.32
J/mol×K
414.41
Joback Calculated Property
Cp,gas
216.07
J/mol×K
443.68
Joback Calculated Property
Cp,gas
226.37
J/mol×K
472.94
Joback Calculated Property
Cp,gas
236.25
J/mol×K
502.21
Joback Calculated Property
Cp,gas
245.69
J/mol×K
531.48
Joback Calculated Property
Cp,liquid
218.00
J/mol×K
298.00
NIST
η
[0.0004780; 0.0005320]
Pa×s
[293.15; 303.15]
η
0.0005320
Pa×s
293.15
Viscosi...
η
0.0005040
Pa×s
298.15
Viscosi...
η
0.0004780
Pa×s
303.15
Viscosi...
Δvap H
[29.76; 35.30]
kJ/mol
[299.00; 373.50]
Δvap H
35.30
kJ/mol
299.00
NIST
Δvap H
33.50
kJ/mol
315.00
NIST
Δvap H
32.20
kJ/mol
325.50
NIST
Δvap H
32.10
kJ/mol
326.50
NIST
Δvap H
31.90
kJ/mol
329.00
NIST
Δvap H
32.10
kJ/mol
329.50
NIST
Δvap H
29.76
kJ/mol
345.60
NIST
Δvap H
31.20
kJ/mol
373.50
NIST
Pvap
[16.83; 147.90]
kPa
[298.25; 358.31]
Pvap
16.83
kPa
298.25
The the...
Pvap
20.88
kPa
303.13
The the...
Pvap
25.07
kPa
307.44
The the...
Pvap
29.66
kPa
311.54
Vapor L...
Pvap
31.70
kPa
312.49
Vapor L...
Pvap
30.91
kPa
312.55
The the...
Pvap
31.90
kPa
312.84
Phase e...
Pvap
37.26
kPa
317.29
The the...
Pvap
40.20
kPa
318.55
Vapor L...
Pvap
40.71
kPa
319.61
Vapor L...
Pvap
45.18
kPa
322.38
Vapor L...
Pvap
45.83
kPa
322.74
The the...
Pvap
47.20
kPa
323.25
Vapor L...
Pvap
49.34
kPa
324.77
Vapor L...
Pvap
51.40
kPa
325.18
Vapor L...
Pvap
54.10
kPa
326.60
Vapor L...
Pvap
55.57
kPa
328.05
Vapor L...
Pvap
56.12
kPa
328.30
The the...
Pvap
59.00
kPa
329.02
Vapor L...
Pvap
60.07
kPa
330.26
Vapor L...
Pvap
65.30
kPa
331.96
Vapor L...
Pvap
64.24
kPa
332.17
Vapor L...
Pvap
64.28
kPa
332.26
Vapor L...
Pvap
67.40
kPa
333.28
Vapor L...
Pvap
67.49
kPa
333.56
The the...
Pvap
68.91
kPa
334.21
Vapor L...
Pvap
74.80
kPa
335.92
Vapor L...
Pvap
74.94
kPa
336.69
Vapor L...
Pvap
80.50
kPa
338.08
Vapor L...
Pvap
79.89
kPa
338.60
Vapor L...
Pvap
81.57
kPa
339.17
The the...
Pvap
85.80
kPa
340.01
Vapor L...
Pvap
84.63
kPa
340.37
Vapor L...
Pvap
90.10
kPa
341.49
Vapor L...
Pvap
91.51
kPa
342.76
Vapor L...
Pvap
94.30
kPa
342.88
Vapor L...
Pvap
93.18
kPa
343.23
The the...
Pvap
97.00
kPa
343.86
Vapor L...
Pvap
95.31
kPa
343.89
The the...
Pvap
97.44
kPa
344.57
The the...
Pvap
99.60
kPa
345.25
The the...
Pvap
102.80
kPa
345.77
Vapor L...
Pvap
101.69
kPa
345.92
The the...
Pvap
101.42
kPa
345.99
Vapor L...
Pvap
147.90
kPa
358.31
Phase e...
n 0
[1.37300; 1.37468]
[298.00; 298.15]
n 0
1.37300
298.00
Vapor-L...
n 0
1.37300
298.15
Vapor l...
n 0
1.37319
298.15
Vapor l...
n 0
1.37300
298.15
Vapor l...
n 0
1.37468
298.15
Atmosph...
ρl
[720.69; 741.11]
kg/m3
[293.15; 313.15]
ρl
741.11
kg/m3
293.15
Volumet...
ρl
735.85
kg/m3
298.15
Azeotro...
ρl
735.59
kg/m3
298.15
Volumet...
ρl
730.85
kg/m3
303.15
Volumet...
ρl
725.98
kg/m3
308.15
Volumet...
ρl
720.69
kg/m3
313.15
Volumet...
csound,fluid
[920.73; 1078.87]
m/s
[288.15; 323.15]
csound,fluid
1078.87
m/s
288.15
Tempera...
csound,fluid
1076.43
m/s
288.15
Influen...
csound,fluid
1076.43
m/s
288.15
Tempera...
csound,fluid
1065.09
m/s
290.65
Influen...
csound,fluid
1053.72
m/s
293.15
Influen...
csound,fluid
1042.23
m/s
295.65
Influen...
csound,fluid
1031.01
m/s
298.15
Influen...
csound,fluid
1031.01
m/s
298.15
Tempera...
csound,fluid
1033.23
m/s
298.15
Tempera...
csound,fluid
1019.76
m/s
300.65
Influen...
csound,fluid
1008.62
m/s
303.15
Influen...
csound,fluid
1010.23
m/s
303.15
Tempera...
csound,fluid
997.52
m/s
305.65
Influen...
csound,fluid
986.39
m/s
308.15
Influen...
csound,fluid
975.42
m/s
310.65
Influen...
csound,fluid
965.87
m/s
313.15
Tempera...
csound,fluid
964.53
m/s
313.15
Influen...
csound,fluid
953.54
m/s
315.65
Influen...
csound,fluid
942.67
m/s
318.15
Influen...
csound,fluid
931.73
m/s
320.65
Influen...
csound,fluid
920.73
m/s
323.15
Influen...
csound,fluid
922.48
m/s
323.15
Tempera...
csound,fluid
920.73
m/s
323.15
Tempera...
csound,fluid
922.08
m/s
323.15
Tempera...
αdiff
[2.27e-08; 5.67e-08]
m2 /s
[293.13; 496.24]
αdiff
5.67e-08
m2 /s
293.13
Thermal...
αdiff
5.45e-08
m2 /s
303.09
Thermal...
αdiff
5.16e-08
m2 /s
313.21
Thermal...
αdiff
4.96e-08
m2 /s
323.18
Thermal...
αdiff
4.79e-08
m2 /s
333.18
Thermal...
αdiff
4.70e-08
m2 /s
338.25
Thermal...
αdiff
4.64e-08
m2 /s
343.17
Thermal...
αdiff
4.55e-08
m2 /s
348.15
Thermal...
αdiff
4.49e-08
m2 /s
353.08
Thermal...
αdiff
4.43e-08
m2 /s
358.19
Thermal...
αdiff
4.38e-08
m2 /s
363.10
Thermal...
αdiff
4.33e-08
m2 /s
368.12
Thermal...
αdiff
4.30e-08
m2 /s
373.11
Thermal...
αdiff
4.26e-08
m2 /s
378.18
Thermal...
αdiff
4.20e-08
m2 /s
383.14
Thermal...
αdiff
4.17e-08
m2 /s
388.07
Thermal...
αdiff
4.15e-08
m2 /s
393.06
Thermal...
αdiff
4.10e-08
m2 /s
398.17
Thermal...
αdiff
4.08e-08
m2 /s
403.22
Thermal...
αdiff
4.02e-08
m2 /s
408.16
Thermal...
αdiff
4.00e-08
m2 /s
413.10
Thermal...
αdiff
3.97e-08
m2 /s
418.18
Thermal...
αdiff
3.95e-08
m2 /s
423.09
Thermal...
αdiff
3.90e-08
m2 /s
428.08
Thermal...
αdiff
3.85e-08
m2 /s
433.18
Thermal...
αdiff
3.82e-08
m2 /s
438.17
Thermal...
αdiff
3.77e-08
m2 /s
443.06
Thermal...
αdiff
3.74e-08
m2 /s
448.18
Thermal...
αdiff
3.68e-08
m2 /s
453.18
Thermal...
αdiff
3.61e-08
m2 /s
458.10
Thermal...
αdiff
3.53e-08
m2 /s
463.19
Thermal...
αdiff
3.50e-08
m2 /s
466.12
Thermal...
αdiff
3.45e-08
m2 /s
469.18
Thermal...
αdiff
3.39e-08
m2 /s
472.09
Thermal...
αdiff
3.33e-08
m2 /s
475.06
Thermal...
αdiff
3.25e-08
m2 /s
478.15
Thermal...
αdiff
3.16e-08
m2 /s
481.24
Thermal...
αdiff
3.05e-08
m2 /s
484.23
Thermal...
αdiff
2.95e-08
m2 /s
487.17
Thermal...
αdiff
2.77e-08
m2 /s
490.09
Thermal...
αdiff
2.63e-08
m2 /s
493.14
Thermal...
αdiff
2.27e-08
m2 /s
496.24
Thermal...
Datasets
Mass density, kg/m3 (1)
Speed of sound, m/s (1)
Mass density, kg/m3
Fixed
Measured
Temperature, K - Liquid
Pressure, kPa - Liquid
Mass density, kg/m3 - Liquid
283.15
100.00
751.23
288.15
100.00
746.2
293.15
100.00
741.05
298.15
100.00
735.9
303.15
100.00
730.67
308.15
100.00
725.44
313.15
100.00
720.14
318.15
100.00
714.82
323.15
100.00
709.43
328.15
100.00
703.95
333.15
100.00
698.45
283.15
5000.00
756.42
288.15
5000.00
751.53
293.15
5000.00
746.6
298.15
5000.00
741.67
303.15
5000.00
736.68
308.15
5000.00
731.69
313.15
5000.00
726.68
318.15
5000.00
721.59
323.15
5000.00
716.51
328.15
5000.00
711.38
333.15
5000.00
706.19
283.15
10000.00
761.33
288.15
10000.00
756.63
293.15
10000.00
751.89
298.15
10000.00
747.14
303.15
10000.00
742.38
308.15
10000.00
737.6
313.15
10000.00
732.78
318.15
10000.00
727.94
323.15
10000.00
723.13
328.15
10000.00
718.21
333.15
10000.00
713.35
283.15
15000.00
765.98
288.15
15000.00
761.42
293.15
15000.00
756.83
298.15
15000.00
752.27
303.15
15000.00
747.69
308.15
15000.00
743.07
313.15
15000.00
738.45
318.15
15000.00
733.82
323.15
15000.00
729.2
328.15
15000.00
724.52
333.15
15000.00
719.84
283.15
20000.00
770.36
288.15
20000.00
765.93
293.15
20000.00
761.5
298.15
20000.00
757.08
303.15
20000.00
752.63
308.15
20000.00
748.18
313.15
20000.00
743.71
318.15
20000.00
739.27
323.15
20000.00
734.81
328.15
20000.00
730.3
333.15
20000.00
725.83
283.15
25000.00
774.54
288.15
25000.00
770.23
293.15
25000.00
765.92
298.15
25000.00
761.61
303.15
25000.00
757.33
308.15
25000.00
753.01
313.15
25000.00
748.69
318.15
25000.00
744.39
323.15
25000.00
740.06
328.15
25000.00
735.75
333.15
25000.00
731.42
283.15
30000.00
778.52
288.15
30000.00
774.31
293.15
30000.00
770.13
298.15
30000.00
765.96
303.15
30000.00
761.74
308.15
30000.00
757.57
313.15
30000.00
753.36
318.15
30000.00
749.2
323.15
30000.00
745.02
328.15
30000.00
740.83
333.15
30000.00
736.64
283.15
35000.00
782.33
288.15
35000.00
778.21
293.15
35000.00
774.13
298.15
35000.00
770.04
303.15
35000.00
765.95
308.15
35000.00
761.9
313.15
35000.00
757.81
318.15
35000.00
753.76
323.15
35000.00
749.69
328.15
35000.00
745.64
333.15
35000.00
741.54
283.15
40000.00
785.98
288.15
40000.00
781.97
293.15
40000.00
777.97
298.15
40000.00
773.96
303.15
40000.00
769.98
308.15
40000.00
766.03
313.15
40000.00
762.03
318.15
40000.00
758.08
323.15
40000.00
754.13
328.15
40000.00
750.18
333.15
40000.00
746.21
283.15
45000.00
789.49
288.15
45000.00
785.55
293.15
45000.00
781.65
298.15
45000.00
777.75
303.15
45000.00
773.86
308.15
45000.00
769.97
313.15
45000.00
766.08
318.15
45000.00
762.23
323.15
45000.00
758.36
328.15
45000.00
754.48
333.15
45000.00
750.65
283.15
50000.00
792.89
288.15
50000.00
789.02
293.15
50000.00
785.19
298.15
50000.00
781.37
303.15
50000.00
777.57
308.15
50000.00
773.76
313.15
50000.00
769.94
318.15
50000.00
766.19
323.15
50000.00
762.39
328.15
50000.00
758.63
333.15
50000.00
754.86
283.15
55000.00
796.17
288.15
55000.00
792.37
293.15
55000.00
788.63
298.15
55000.00
784.85
303.15
55000.00
781.12
308.15
55000.00
777.4
313.15
55000.00
773.66
318.15
55000.00
769.98
323.15
55000.00
766.26
328.15
55000.00
762.55
333.15
55000.00
758.88
283.15
60000.00
799.33
288.15
60000.00
795.56
293.15
60000.00
791.91
298.15
60000.00
788.21
303.15
60000.00
784.56
308.15
60000.00
780.9
313.15
60000.00
777.23
318.15
60000.00
773.61
323.15
60000.00
770.0
328.15
60000.00
766.37
333.15
60000.00
762.77
283.15
65000.00
802.42
288.15
65000.00
798.71
293.15
65000.00
795.1
298.15
65000.00
791.48
303.15
65000.00
787.89
308.15
65000.00
784.29
313.15
65000.00
780.69
318.15
65000.00
777.13
323.15
65000.00
773.58
328.15
65000.00
770.52
333.15
65000.00
766.51
Reference
Speed of sound, m/s
Fixed
Measured
Temperature, K - Liquid
Pressure, kPa - Liquid
Speed of sound, m/s - Liquid
293.15
10.00
1059.15
303.15
10.00
1012.95
313.15
10.00
967.71
323.15
20.00
923.32
333.15
40.00
879.69
343.15
60.00
836.71
353.15
90.00
794.25
363.15
130.00
752.18
373.15
180.00
710.37
383.15
250.00
668.66
393.15
340.00
626.87
403.15
440.00
584.83
413.15
570.00
542.3
423.15
730.00
499.06
433.15
920.00
454.82
443.15
1150.00
409.25
453.15
1420.00
361.97
463.15
1750.00
312.51
473.15
2130.00
260.24
483.15
2570.00
204.36
488.15
2820.00
174.7
493.15
3090.00
143.64
Reference
Correlations
Property
Value
Unit
Temperature (K)
Source
Pvap
[1.33; 202.66]
kPa
[257.16; 367.48]
The Yaw...
Equation ln(Pvp) = A + B/(T + C) Coefficient A 1.53227e+01 Coefficient B -3.30527e+03 Coefficient C -3.73240e+01 Temperature range, min. 257.16
Temperature range, max. 367.48
Pvap
1.33
kPa
257.16
Calculated Property
Pvap
2.95
kPa
269.42
Calculated Property
Pvap
6.03
kPa
281.68
Calculated Property
Pvap
11.50
kPa
293.93
Calculated Property
Pvap
20.69
kPa
306.19
Calculated Property
Pvap
35.36
kPa
318.45
Calculated Property
Pvap
57.78
kPa
330.71
Calculated Property
Pvap
90.79
kPa
342.96
Calculated Property
Pvap
137.76
kPa
355.22
Calculated Property
Pvap
202.66
kPa
367.48
Calculated Property
Similar Compounds
Find more compounds similar to Propane, 2-ethoxy-2-methyl- .
Mixtures
Propane, 2-ethoxy-2-methyl- + Diethyl sulfide
1-Propanol + Propane, 2-ethoxy-2-methyl-
Thiophene + Propane, 2-ethoxy-2-methyl-
Propane, 2-ethoxy-2-methyl- + Heptane
1-Hexene + Propane, 2-ethoxy-2-methyl-
1-Hexene + Propane, 2-ethoxy-2-methyl- + Heptane
Propane, 2-ethoxy-2-methyl- + o-Xylene
Benzene, 1,3-dimethyl- + Propane, 2-ethoxy-2-methyl-
p-Xylene + Propane, 2-ethoxy-2-methyl-
Propanenitrile + Propane, 2-ethoxy-2-methyl-
Propane, 2-ethoxy-2-methyl- + Water
Ethanol, 2-methoxy- + Propane, 2-ethoxy-2-methyl-
Ethanol, 2-(2-methoxyethoxy)- + Propane, 2-ethoxy-2-methyl-
Propane, 2-ethoxy-2-methyl- + Ethanol, 2-[2-(2-methoxyethoxy)ethoxy]-
Propane, 2-ethoxy-2-methyl- + Ethanol, 2-ethoxy-
Ethanol, 2-(2-ethoxyethoxy)- + Propane, 2-ethoxy-2-methyl-
Propane, 2-ethoxy-2-methyl- + Ethanol, 2-[2-(2-ethoxyethoxy)ethoxy]-
Benzene + Propane, 2-ethoxy-2-methyl-
Toluene + Propane, 2-ethoxy-2-methyl-
Propane, 2-ethoxy-2-methyl- + Ethylbenzene
Find more mixtures with Propane, 2-ethoxy-2-methyl- .
Sources
Crippen Method
Crippen Method
Infinite dilution activity coefficient measurements by inert gas stripping method
Vapor liquid equilibrium for binary system of diethyl sulfide + cyclohexane at 353.15 and 343.15 K and diethyl sulfide + 2-ethoxy-2-methylpropane at 343.15 and 333.15 K
Vapor liquid equilibrium, densities, and interfacial tensions for the system ethyl 1,1-dimethylethyl ether (ETBE) + propan-1-ol
Vapor liquid equilibrium for binary system of thiophene + 2,2,4-trimethylpentane at 343.15 and 353.15K and thiophene + 2-ethoxy-2-methylpropane at 333.15 and 343.15K
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
Influence of temperature on thermodynamics of ethers + xylenes
Phase equilibrium measurements for systems containing propanenitrile with tert-butyl ethyl ether and C4-hydrocarbons
Azeotrope breaking for the system ethyl tert-butyl ether (ETBE) + ethanol at 313.15 K and excess properties at 298.15 K for mixtures of ETBE and ethanol with phosphonium-based ionic liquids
Atmospheric densities and interfacial tensions for 1- alkanol (1-butanol to 1-octanol) + water and ether (MTBE, ETBE, DIPE, TAME and THP) + water demixed mixtures.
Speed of sound measurement in ethyl tert-butyl ether and tert-amyl methyl ether by Brillouin light scattering
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
Experimental and modeled volumetric behavior of linear and branched ethers
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
Thermodynamics and activity coefficients at infinite dilution for organic solutes in the ionic liquid 1-butyl-1-methylpyrrolidinium dicyanamide
New ionic liquid [P4,4,4,4][NTf2] in bio-butanol extraction on investigation of limiting activity coefficients
Ammonium ionic liquids in extraction of bio-butan-1-ol from water phase using activity coefficients at infinite dilution
Volumetric properties of binary mixtures of alkoxyethanols with ethyl tert-butyl ether at various temperatures
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)
The thermodynamics of vaporization of ethyl tert-butyl ether, isobutyl tert-butyl ether, and di-isopropyl ether
Viscosities of binary mixtures of some n-ethoxyethanols with ethyl tert-butyl ether at T = (293.15, 298.15, and 303.15) K
Temperature influence on mixing properties of {ethyl tert-butyl ether (ETBE) + gasoline additives}
Thermodynamics of fuels with a bio-synthetic component (IV): (Vapor + liquid) equilibrium data for the ternary mixture (ethyl 1,1-dimethylethyl ether + 1-hexene + toluene) at T = 313.15 K
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 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
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
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
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 coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)- 1-methylpiperidinium trifluorotris(perfluoroethyl)phosphate
Physicochemical properties and activity coefficients at infinite dilution for organic solutes and water in a novel bicyclic guanidinium superbase-derived protic ionic liquid
Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)- 1-methylpyrrolidinium trifluorotris(perfluoroethyl)phosphate
Measurements of activity coefficients at infinite dilution for organic solutes and water in N-hexylisoquinolinium thiocyanate, [HiQuin][SCN] using GLC
Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-hydroxyethyl)- 3-methylimidazolium trifluorotris(perfluoroethyl)phosphate
Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium tricyanomethanide
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
Thermodynamics and activity coefficients at infinite dilution for organic solutes, water and diols in the ionic liquid choline bis(trifluoromethylsulfonyl)imide
Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(3-hydroxypropyl)-4-methylmorpholinium bis(trifluoromethylsulfonyl)-amide
Activity coefficients at infinite dilution for organic solutes and water in 1-ethyl-1-methylpyrrolidinium lactate
Activity coefficients at infinite dilution, physicochemical and thermodynamic properties for organic solutes and water in the ionic liquid ethyl-dimethyl-(2-methoxyethyl)ammonium trifluorotris-(perfluoroethyl)phosphate
A 1-alkylcyanopyridinium-based ionic liquid in the separation processes
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
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 limiting activity coefficients measurements for organic solutes and water in the ionic liquid 1-dodecyl-3-methylimidzolium bis(trifluoromethylsulfonyl) imide
Separation of binary mixtures hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on limiting activity coefficients
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
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
The use of ionic liquids for separation of binary hydrocarbons mixtures based on gamma infinity data measurements
Thermodynamic Analysis of the Experimental Equilibria for the Liquid-Phase Etherification of Isobutene with C1 to C4 Linear Primary Alcohols
Activity Coefficients at Infinite Dilution of Organic Solutes and Water in Tributylethylphosphonium Diethylphosphate Using Gas Liquid Chromatography: Thermodynamic Properties of Mixtures Containing Ionic Liquids
Thermal Diffusivity of 2-Ethoxy-2-methylpropane (ETBE) and 2-Methoxy-2-methylbutane (TAME) at Temperatures from (293 to 523) K and Pressure up to 10 MPa
Oxygenated Gasoline Additives: Saturated Heat Capacities between (277 and 355) K
Vapor Liquid Equilibrium for Binary System of 2-Propanol + 2-Ethoxy-2-methylpropane and Ethyl Ethanoate + 2-Ethoxy-2-methylpropane at 333 K and 2-Propanone + 2-Ethoxy-2-methylpropane at 323 K
Volumetric and Viscosity Study for the Mixtures of 2-Ethoxy-2-methylpropane, Ethanol, and 1-Ethyl-3-methylimidazolium Ethyl Sulfate Ionic Liquid
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
Vapor-Liquid Equilibrium for Dimethyl Disulfide + Butane, + trans-But-2-ene, + 2-Methylpropane, + 2-Methylpropene, + Ethanol, and 2-Ethoxy-2-methylpropane
Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing 2-Ethoxy-2-methylpropane or 2-Ethoxy-2-methylbutane and Acetonitrile or Propanenitrile
Thermodynamics of Fuels with a Biosynthetic Component. II. Vapor Liquid Equilibrium Data for Binary and Ternary Mixtures Containing Ethyl 1,1-Dimethylethyl Ether, 1-Hexene, and Cyclohexane at T = 313.15 K
Phase Equilibria of (1-Ethyl-3-methylimidazolium Ethylsulfate + Hydrocarbon, + Ketone, and + Ether) Binary Systems
Joback Method
McGowan Method
NIST Webbook
The Yaws Handbook of Vapor Pressure
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