Property
Value
Unit
Source
ω
0.3519
Relay (1.0) Calculated Property
Δf G°
-25.94
kJ/mol
Joback Calculated Property
Δf H°gas
-168.25
kJ/mol
Relay (1.0) Calculated Property
Δfus H°
8.61
kJ/mol
Joback Calculated Property
Δvap H°
26.62
kJ/mol
Relay (1.0) Calculated Property
IE
8.85
eV
Relay (1.0) Calculated Property
log 10 WS
-1.33
Relay (1.0) Calculated Property
log Poct/wat
1.556
Crippen Calculated Property
McVol
82.880
ml/mol
McGowan Calculated Property
Pc
3572.80
kPa
Joback Calculated Property
Tboil
338.48
K
Relay (1.0) Calculated Property
Tc
490.95
K
Relay (1.0) Calculated Property
Tfus
157.15
K
Relay (1.0) Calculated Property
Vc
0.306
m3 /kmol
Relay (1.0) Calculated Property
Property
Value
Unit
Temperature (K)
Source
Cp,gas
[135.21; 180.14]
J/mol×K
[332.90; 500.59]
Cp,gas
135.21
J/mol×K
332.90
Joback Calculated Property
Cp,gas
143.28
J/mol×K
360.85
Joback Calculated Property
Cp,gas
151.11
J/mol×K
388.80
Joback Calculated Property
Cp,gas
158.71
J/mol×K
416.74
Joback Calculated Property
Cp,gas
166.08
J/mol×K
444.69
Joback Calculated Property
Cp,gas
173.22
J/mol×K
472.64
Joback Calculated Property
Cp,gas
180.14
J/mol×K
500.59
Joback Calculated Property
η
[0.0002010; 0.0024826]
Pa×s
[166.58; 332.90]
η
0.0024826
Pa×s
166.58
Joback Calculated Property
η
0.0012110
Pa×s
194.30
Joback Calculated Property
η
0.0007067
Pa×s
222.02
Joback Calculated Property
η
0.0004648
Pa×s
249.74
Joback Calculated Property
η
0.0003324
Pa×s
277.46
Joback Calculated Property
η
0.0002526
Pa×s
305.18
Joback Calculated Property
η
0.0002010
Pa×s
332.90
Joback Calculated Property
Pvap
[20.00; 101.70]
kPa
[296.02; 337.90]
Pvap
20.00
kPa
296.02
Isothermal Binary and Ternary VLE for the Mixtures of Propyl Vinyl Ether + Ethanol + Isooctane at 323.15 K and VE at 293.15 K
Pvap
25.00
kPa
301.62
Isothermal Binary and Ternary VLE for the Mixtures of Propyl Vinyl Ether + Ethanol + Isooctane at 323.15 K and VE at 293.15 K
Pvap
30.00
kPa
305.44
Isothermal Binary and Ternary VLE for the Mixtures of Propyl Vinyl Ether + Ethanol + Isooctane at 323.15 K and VE at 293.15 K
Pvap
35.00
kPa
309.37
Isothermal Binary and Ternary VLE for the Mixtures of Propyl Vinyl Ether + Ethanol + Isooctane at 323.15 K and VE at 293.15 K
Pvap
40.00
kPa
312.65
Isothermal Binary and Ternary VLE for the Mixtures of Propyl Vinyl Ether + Ethanol + Isooctane at 323.15 K and VE at 293.15 K
Pvap
45.00
kPa
315.13
Isothermal Binary and Ternary VLE for the Mixtures of Propyl Vinyl Ether + Ethanol + Isooctane at 323.15 K and VE at 293.15 K
Pvap
50.00
kPa
317.88
Isothermal Binary and Ternary VLE for the Mixtures of Propyl Vinyl Ether + Ethanol + Isooctane at 323.15 K and VE at 293.15 K
Pvap
55.00
kPa
320.29
Isothermal Binary and Ternary VLE for the Mixtures of Propyl Vinyl Ether + Ethanol + Isooctane at 323.15 K and VE at 293.15 K
Pvap
60.00
kPa
322.72
Isothermal Binary and Ternary VLE for the Mixtures of Propyl Vinyl Ether + Ethanol + Isooctane at 323.15 K and VE at 293.15 K
Pvap
65.00
kPa
324.90
Isothermal Binary and Ternary VLE for the Mixtures of Propyl Vinyl Ether + Ethanol + Isooctane at 323.15 K and VE at 293.15 K
Pvap
70.00
kPa
326.95
Isothermal Binary and Ternary VLE for the Mixtures of Propyl Vinyl Ether + Ethanol + Isooctane at 323.15 K and VE at 293.15 K
Pvap
75.00
kPa
328.89
Isothermal Binary and Ternary VLE for the Mixtures of Propyl Vinyl Ether + Ethanol + Isooctane at 323.15 K and VE at 293.15 K
Pvap
80.00
kPa
330.76
Isothermal Binary and Ternary VLE for the Mixtures of Propyl Vinyl Ether + Ethanol + Isooctane at 323.15 K and VE at 293.15 K
Pvap
85.00
kPa
332.86
Isothermal Binary and Ternary VLE for the Mixtures of Propyl Vinyl Ether + Ethanol + Isooctane at 323.15 K and VE at 293.15 K
Pvap
90.00
kPa
334.22
Isothermal Binary and Ternary VLE for the Mixtures of Propyl Vinyl Ether + Ethanol + Isooctane at 323.15 K and VE at 293.15 K
Pvap
95.00
kPa
336.28
Isothermal Binary and Ternary VLE for the Mixtures of Propyl Vinyl Ether + Ethanol + Isooctane at 323.15 K and VE at 293.15 K
Pvap
100.00
kPa
337.38
Isothermal Binary and Ternary VLE for the Mixtures of Propyl Vinyl Ether + Ethanol + Isooctane at 323.15 K and VE at 293.15 K
Pvap
101.70
kPa
337.90
Isothermal Binary and Ternary VLE for the Mixtures of Propyl Vinyl Ether + Ethanol + Isooctane at 323.15 K and VE at 293.15 K
n 0
1.39094 ± 0.00005
298.15
Binary LLE for Propyl Vinyl Ether (PVE) + Water, Ternary LLE for PVE + Methanol or Ethanol + Water at 298.15 K, and VE and centsR at 293.15 K for the Mixture of PVE + Ethanol + 2,2,4-Trimethylpentane
ρl
[762.69; 768.97]
kg/m3
[293.15; 298.15]
ρl
768.97 ± 0.01
kg/m3
293.15
Isothermal Binary and Ternary VLE for the Mixtures of Propyl Vinyl Ether + Ethanol + Isooctane at 323.15 K and VE at 293.15 K
ρl
762.98 ± 0.01
kg/m3
298.15
Binary LLE for Propyl Vinyl Ether (PVE) + Water, Ternary LLE for PVE + Methanol or Ethanol + Water at 298.15 K, and VE and centsR at 293.15 K for the Mixture of PVE + Ethanol + 2,2,4-Trimethylpentane
ρl
762.96
kg/m3
298.15
Liquid Liquid Equilibrium for Ternary Systems of Propyl Vinyl Ether + C3 or C4 Alcohols + Water at 298.15 K and Excess Molar Enthalpies for Ternary and Constituent Binary Systems of Propyl Vinyl Ether + Ethanol + Isooctane at 303.15 K
ρl
762.69 ± 0.01
kg/m3
298.15
Binary and Ternary Vapor-Liquid Equilibrium at 323.15 K and Excess Molar Volumes at 298.15 K for the Mixtures of Propyl Vinyl Ether + 1-Propanol + Toluene