Physical Properties
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
Temperature Dependent Properties
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
n 0
1.39793
298.15
Isothermal vapor liquid equilibrium at 323.15K and excess molar volumes and refractive indices at 298.15K for the ternary system propyl vinyl ether + 1-propanol + benzene and its binary sub-systems
ρl
[762.69; 768.97]
kg/m3
[293.15; 298.15]
ρl
768.97
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
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
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
Correlations
Property
Value
Unit
Temperature (K)
Source
Pvap
[1.33; 202.64]
kPa
[251.52; 363.99]
The Yaws Handbook of Vapor Pressure
Equation ln(Pvp) = A + B/(T + C) Coefficient A 1.49761e+01 Coefficient B -3.17806e+03 Coefficient C -3.51560e+01 Temperature range, min. 251.52
Temperature range, max. 363.99
Pvap
1.33
kPa
251.52
Calculated Property
Pvap
2.97
kPa
264.02
Calculated Property
Pvap
6.10
kPa
276.51
Calculated Property
Pvap
11.67
kPa
289.01
Calculated Property
Pvap
20.99
kPa
301.51
Calculated Property
Pvap
35.84
kPa
314.00
Calculated Property
Pvap
58.43
kPa
326.50
Calculated Property
Pvap
91.51
kPa
339.00
Calculated Property
Pvap
138.33
kPa
351.49
Calculated Property
Pvap
202.64
kPa
363.99
Calculated Property
Similar Compounds
Find more compounds similar to Propyl vinyl ether .
Mixtures
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