Physical Properties
Property
Value
Unit
Source
Δc H°liquid
[-3394.20; -3389.00]
kJ/mol
Δc H°liquid
-3394.20 ± 2.60
kJ/mol
NIST
Δc H°liquid
-3389.00
kJ/mol
NIST
Δc H°liquid
-3390.00 ± 2.00
kJ/mol
NIST
Δf G°
-249.69
kJ/mol
Joback Calculated Property
Δf H°gas
-636.00 ± 3.00
kJ/mol
NIST
Δf H°liquid
-681.80 ± 2.60
kJ/mol
NIST
Δfus H°
29.21
kJ/mol
Joback Calculated Property
Δvap H°
[41.00; 45.80]
kJ/mol
Δvap H°
45.80
kJ/mol
NIST
Δvap H°
41.00 ± 0.40
kJ/mol
NIST
log 10 WS
-1.31
Crippen Calculated Property
log Poct/wat
1.088
Crippen Calculated Property
McVol
102.150
ml/mol
McGowan Calculated Property
Pc
3534.66
kPa
Joback Calculated Property
Inp
[729.00; 786.00]
Inp
755.00
NIST
Inp
729.00
NIST
Inp
734.00
NIST
Inp
786.00
NIST
Inp
781.00
NIST
Inp
776.00
NIST
Inp
763.00
NIST
Inp
767.00
NIST
Inp
767.00
NIST
Inp
771.00
NIST
Inp
786.00
NIST
I
[1069.00; 1070.00]
I
1070.00
NIST
I
1069.00
NIST
I
1069.00
NIST
I
1069.00
NIST
I
1070.00
NIST
S°gas
374.40 ± 5.00
J/mol×K
NIST
S°liquid
289.40
J/mol×K
NIST
Tboil
[395.00; 401.15]
K
Tboil
397.15
K
NIST
Tboil
Outlier 401.15 ± 0.50
K
NIST
Tboil
397.15 ± 1.00
K
NIST
Tboil
395.00 ± 1.00
K
NIST
Tboil
397.20 ± 1.50
K
NIST
Tboil
396.50 ± 1.00
K
NIST
Tc
563.00 ± 4.00
K
NIST
Tfus
[284.15; 286.00]
K
Tfus
285.75
K
NIST
Tfus
284.15 ± 1.00
K
NIST
Tfus
285.65 ± 0.20
K
NIST
Tfus
286.00 ± 0.50
K
NIST
Tfus
285.70 ± 0.10
K
NIST
Ttriple
285.70 ± 0.10
K
NIST
Vc
0.365
m3 /kmol
Joback Calculated Property
Temperature Dependent Properties
Property
Value
Unit
Temperature (K)
Source
Cp,gas
[223.56; 300.83]
J/mol×K
[427.74; 632.02]
Cp,gas
223.56
J/mol×K
427.74
Joback Calculated Property
Cp,gas
237.89
J/mol×K
461.79
Joback Calculated Property
Cp,gas
251.64
J/mol×K
495.83
Joback Calculated Property
Cp,gas
264.82
J/mol×K
529.88
Joback Calculated Property
Cp,gas
277.41
J/mol×K
563.93
Joback Calculated Property
Cp,gas
289.41
J/mol×K
597.97
Joback Calculated Property
Cp,gas
300.83
J/mol×K
632.02
Joback Calculated Property
Cp,liquid
[250.20; 257.30]
J/mol×K
[298.00; 306.60]
Cp,liquid
250.20
J/mol×K
298.00
NIST
Cp,liquid
257.30
J/mol×K
298.15
NIST
Cp,liquid
254.00
J/mol×K
306.60
NIST
η
[0.0009070; 0.0013740]
Pa×s
[288.15; 308.15]
η
0.0013740
Pa×s
288.15
Densiti...
η
0.0012240
Pa×s
293.15
Densiti...
η
0.0011070
Pa×s
298.15
Densiti...
η
0.0011070
Pa×s
298.15
Excess ...
η
0.0011070
Pa×s
298.15
Molecul...
η
0.0010010
Pa×s
303.15
Excess ...
η
0.0010010
Pa×s
303.15
Molecul...
η
0.0010010
Pa×s
303.15
Densiti...
η
0.0009070
Pa×s
308.15
Excess ...
η
0.0009070
Pa×s
308.15
Molecul...
η
0.0009070
Pa×s
308.15
Densiti...
Δfus H
[0.26; 13.52]
kJ/mol
[142.70; 285.70]
Δfus H
0.26
kJ/mol
142.70
NIST
Δfus H
0.77
kJ/mol
147.50
NIST
Δfus H
13.52
kJ/mol
285.70
NIST
Δfus H
13.52
kJ/mol
285.70
NIST
Δvap H
41.50
kJ/mol
359.50
NIST
n 0
1.40290
298.15
Viscosi...
Δfus S
[1.81; 47.32]
J/mol×K
[142.70; 285.70]
Δfus S
1.81
J/mol×K
142.70
NIST
Δfus S
5.24
J/mol×K
147.50
NIST
Δfus S
47.32
J/mol×K
285.70
NIST
Correlations
Property
Value
Unit
Temperature (K)
Source
Pvap
[0.68; 202.63]
kPa
[285.75; 421.91]
The Yaw...
Equation ln(Pvp) = A + B/(T + C) Coefficient A 1.47084e+01 Coefficient B -3.38746e+03 Coefficient C -6.14290e+01 Temperature range, min. 285.75
Temperature range, max. 421.91
Pvap
0.68
kPa
285.75
Calculated Property
Pvap
1.75
kPa
300.88
Calculated Property
Pvap
4.06
kPa
316.01
Calculated Property
Pvap
8.57
kPa
331.14
Calculated Property
Pvap
16.71
kPa
346.27
Calculated Property
Pvap
30.44
kPa
361.39
Calculated Property
Pvap
52.34
kPa
376.52
Calculated Property
Pvap
85.66
kPa
391.65
Calculated Property
Pvap
134.25
kPa
406.78
Calculated Property
Pvap
202.63
kPa
421.91
Calculated Property
Similar Compounds
Find more compounds similar to Paraldehyde .
Mixtures
Sources
Crippen Method
Crippen Method
Molecular interactions in (2,4,6-trimethyl-1,3,5-trioxane + n-alkyl acetates) at T=(298.15, 303.15, and 308.15) K
Excess Molar Volumes and Viscosity Deviations of Binary Mixtures of 2,4,6-Trimethyl-1,3,5-trioxane + Ethanol, 1-Propanol, and 1-Butanol at (298.15, 303.15, and 308.15) K
Densities and Viscosities of Binary Mixtures of Paraldehyde + Propylene Carbonate at (288.15, 293.15, 298.15, 303.15, and 308.15) K
Viscosities, Ultrasonic Velocities at (288.15 and 298.15) K, and Refractive Indices at (298.15) K of Binary Mixtures of 2,4,6-Trimethyl-1,3,5-trioxane with Dimethyl Carbonate, Diethyl Carbonate, and Propylene Carbonate
Joback Method
McGowan Method
NIST Webbook
The Yaws Handbook of Vapor Pressure
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that the value is more than 2 standard deviations away from the
property mean.