Physical Properties
Property
Value
Unit
Source
ω
0.3932
Relay (1.0) Calculated Property
Δc H°liquid
-4948.16 ± 0.47
kJ/mol
NIST
Δf G°
-75.13
kJ/mol
Joback Calculated Property
Δf H°gas
-248.94 ± 0.88
kJ/mol
NIST
Δf H°liquid
-308.40 ± 0.52
kJ/mol
NIST
Δfus H°
11.96
kJ/mol
Joback Calculated Property
Δvap H°
[59.46; 60.90]
kJ/mol
Δvap H°
60.90 ± 0.50
kJ/mol
NIST
Δvap H°
59.46 ± 0.71
kJ/mol
NIST
Δvap H°
59.50
kJ/mol
NIST
IE
8.96
eV
Relay (1.0) Calculated Property
log 10 WS
-1.14
Relay (1.0) Calculated Property
log Poct/wat
1.978
Crippen Calculated Property
McVol
125.650
ml/mol
McGowan Calculated Property
Pc
3166.83
kPa
Joback Calculated Property
Inp
1200.00
NIST
I
1665.00
NIST
Tboil
[469.00; 480.00]
K
Tboil
469.00
K
NIST
Tboil
480.00 ± 5.00
K
NIST
Tc
674.63
K
Relay (1.0) Calculated Property
Tfus
256.46
K
Relay (1.0) Calculated Property
Vc
0.458
m3 /kmol
Relay (1.0) Calculated Property
Temperature Dependent Properties
Property
Value
Unit
Temperature (K)
Source
Δvap H
56.50 ± 0.70
kJ/mol
300.50
NIST
Pressure Dependent Properties
Property
Value
Unit
Pressure (kPa)
Source
Tboilr
361.20
K
2.40
NIST
Correlations
Property
Value
Unit
Temperature (K)
Source
Cp,gas
[169.64; 402.66]
J/mol×K
[273.00; 1000.00]
Joback Predicted correlation
Equation Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,gas in J/mol×K, T in K
Coefficient A 1.01200e+01
Coefficient B 6.59440e-01
Coefficient C -2.78200e-04
Coefficient D 1.13000e-08
Coefficient E 0.00000e+00
Temperature range, min. 273.00
Temperature range, max. 1000.00
Cp,gas
169.64
J/mol×K
273.00
Calculated Property
Cp,gas
209.10
J/mol×K
353.78
Calculated Property
Cp,gas
245.08
J/mol×K
434.56
Calculated Property
Cp,gas
277.62
J/mol×K
515.33
Calculated Property
Cp,gas
306.76
J/mol×K
596.11
Calculated Property
Cp,gas
332.53
J/mol×K
676.89
Calculated Property
Cp,gas
354.97
J/mol×K
757.67
Calculated Property
Cp,gas
374.11
J/mol×K
838.44
Calculated Property
Cp,gas
390.00
J/mol×K
919.22
Calculated Property
Cp,gas
402.66
J/mol×K
1000.00
Calculated Property
Property
Value
Unit
Temperature (K)
Source
η
[0.0029241; 0.0001619]
Pa×s
[247.07; 480.03]
Joback Predicted correlation
Equation Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K
Coefficient A -1.17979e+01
Coefficient B 1.47330e+03
Coefficient C 0.00000e+00
Coefficient D 0.00000e+00
Coefficient E 0.00000e+00
Comment Liquid phase. Joback/Reid (1987), valid from Tf to 0.7·Tc.
Temperature range, min. 247.07
Temperature range, max. 480.03
η
0.0029241
Pa×s
247.07
Calculated Property
η
0.0016612
Pa×s
272.95
Calculated Property
η
0.0010408
Pa×s
298.84
Calculated Property
η
0.0007026
Pa×s
324.72
Calculated Property
η
0.0005026
Pa×s
350.61
Calculated Property
η
0.0003765
Pa×s
376.49
Calculated Property
η
0.0002927
Pa×s
402.37
Calculated Property
η
0.0002346
Pa×s
428.26
Calculated Property
η
0.0001928
Pa×s
454.14
Calculated Property
η
0.0001619
Pa×s
480.03
Calculated Property
Similar Compounds
Find more compounds similar to Benzaldehyde dimethyl acetal .
Sources
Note: Cheméo is only indexing the data, follow the source links to retrieve the latest data. The source is also providing more information like the publication year, authors and more.
Take the time to validate and double check the source of the data.
These property values are available through the Cheméo API . A free account gives you an access key.