Property
Value
Unit
Source
ω
0.7958
Relay (1.0) Calculated Property
Δf G°
-466.06
kJ/mol
Joback Calculated Property
Δf H°gas
-839.60
kJ/mol
Relay (1.0) Calculated Property
Δfus H°
19.05
kJ/mol
Joback Calculated Property
Δvap H°
84.10
kJ/mol
Relay (1.0) Calculated Property
IE
9.52
eV
Relay (1.0) Calculated Property
log 10 WS
0.07
Relay (1.0) Calculated Property
log Poct/wat
0.170
Crippen Calculated Property
McVol
161.150
ml/mol
McGowan Calculated Property
Pc
2746.90
kPa
Joback Calculated Property
Tboil
540.78
K
Relay (1.0) Calculated Property
Tc
697.31
K
Relay (1.0) Calculated Property
Tfus
258.58
K
Relay (1.0) Calculated Property
Vc
0.617
m3 /kmol
Relay (1.0) Calculated Property
Property
Value
Unit
Temperature (K)
Source
Cp,gas
[444.44; 506.27]
J/mol×K
[633.20; 797.93]
Cp,gas
444.44
J/mol×K
633.20
Joback Calculated Property
Cp,gas
455.90
J/mol×K
660.66
Joback Calculated Property
Cp,gas
466.89
J/mol×K
688.11
Joback Calculated Property
Cp,gas
477.42
J/mol×K
715.57
Joback Calculated Property
Cp,gas
487.49
J/mol×K
743.02
Joback Calculated Property
Cp,gas
497.11
J/mol×K
770.48
Joback Calculated Property
Cp,gas
506.27
J/mol×K
797.93
Joback Calculated Property
Cp,liquid
440.60
J/mol×K
298.00
NIST
η
[0.0000137; 0.0425755]
Pa×s
[312.29; 633.20]
η
0.0425755
Pa×s
312.29
Joback Calculated Property
η
0.0041843
Pa×s
365.78
Joback Calculated Property
η
0.0007433
Pa×s
419.26
Joback Calculated Property
η
0.0001952
Pa×s
472.75
Joback Calculated Property
η
0.0000673
Pa×s
526.23
Joback Calculated Property
η
0.0000282
Pa×s
579.72
Joback Calculated Property
η
0.0000137
Pa×s
633.20
Joback Calculated Property
Pvap
[0.04; 0.22]
kPa
[350.15; 378.15]
Pvap
0.04
kPa
350.15
Vapour-liquid equilibrium for tripropylene glycol + aromatic hydrocarbons binary systems: Experimental data and regression
Pvap
0.06
kPa
357.15
Vapour-liquid equilibrium for tripropylene glycol + aromatic hydrocarbons binary systems: Experimental data and regression
Pvap
0.10
kPa
364.15
Vapour-liquid equilibrium for tripropylene glycol + aromatic hydrocarbons binary systems: Experimental data and regression
Pvap
0.15
kPa
371.15
Vapour-liquid equilibrium for tripropylene glycol + aromatic hydrocarbons binary systems: Experimental data and regression
Pvap
0.22
kPa
378.15
Vapour-liquid equilibrium for tripropylene glycol + aromatic hydrocarbons binary systems: Experimental data and regression
ρl
[976.90; 1017.50]
kg/m3
[293.15; 343.15]
ρl
1017.50
kg/m3
293.15
Density and vapour pressure of mixed-solvent desiccant systems (propylene glycol or dipropylene glycol or tripropylene glycol + magnesium chloride + water)
ρl
1009.50
kg/m3
303.15
Density and vapour pressure of mixed-solvent desiccant systems (propylene glycol or dipropylene glycol or tripropylene glycol + magnesium chloride + water)
ρl
1001.50
kg/m3
313.15
Density and vapour pressure of mixed-solvent desiccant systems (propylene glycol or dipropylene glycol or tripropylene glycol + magnesium chloride + water)
ρl
993.40
kg/m3
323.15
Density and vapour pressure of mixed-solvent desiccant systems (propylene glycol or dipropylene glycol or tripropylene glycol + magnesium chloride + water)
ρl
985.20
kg/m3
333.15
Density and vapour pressure of mixed-solvent desiccant systems (propylene glycol or dipropylene glycol or tripropylene glycol + magnesium chloride + water)
ρl
976.90
kg/m3
343.15
Density and vapour pressure of mixed-solvent desiccant systems (propylene glycol or dipropylene glycol or tripropylene glycol + magnesium chloride + water)
λ
[0.14; 0.15]
W/m×K
[298.10; 449.60]
λ
0.15
W/m×K
298.10
Density, Viscosity and Thermal Conductivity of Aqueous Solutions of Propylene Glycol, Dipropylene Glycol, and Tripropylene Glycol between 290 K and 460 K
λ
0.15
W/m×K
326.10
Density, Viscosity and Thermal Conductivity of Aqueous Solutions of Propylene Glycol, Dipropylene Glycol, and Tripropylene Glycol between 290 K and 460 K
λ
0.15
W/m×K
351.10
Density, Viscosity and Thermal Conductivity of Aqueous Solutions of Propylene Glycol, Dipropylene Glycol, and Tripropylene Glycol between 290 K and 460 K
λ
0.15
W/m×K
376.20
Density, Viscosity and Thermal Conductivity of Aqueous Solutions of Propylene Glycol, Dipropylene Glycol, and Tripropylene Glycol between 290 K and 460 K
λ
0.14
W/m×K
399.40
Density, Viscosity and Thermal Conductivity of Aqueous Solutions of Propylene Glycol, Dipropylene Glycol, and Tripropylene Glycol between 290 K and 460 K
λ
0.14
W/m×K
424.90
Density, Viscosity and Thermal Conductivity of Aqueous Solutions of Propylene Glycol, Dipropylene Glycol, and Tripropylene Glycol between 290 K and 460 K
λ
0.14
W/m×K
449.60
Density, Viscosity and Thermal Conductivity of Aqueous Solutions of Propylene Glycol, Dipropylene Glycol, and Tripropylene Glycol between 290 K and 460 K