Physical Properties
Property
Value
Unit
Source
ω
0.3730
KDB
PAff
798.40
kJ/mol
NIST
BasG
767.70
kJ/mol
NIST
Δc H°gas
-2568.70 ± 0.92
kJ/mol
NIST
Δc H°liquid
-2579.00
kJ/mol
NIST
μ
3.80
debye
KDB
EA
0.02 ± 0.00
eV
NIST
Δf G°
108.70
kJ/mol
KDB
Δf H°gas
[31.20; 34.10]
kJ/mol
Δf H°gas
34.10
kJ/mol
KDB
Δf H°gas
31.20
kJ/mol
NIST
Δf H°liquid
-5.80 ± 1.00
kJ/mol
NIST
Δfus H°
7.62
kJ/mol
Joback Calculated Property
Δvap H°
34.98
kJ/mol
Joback Calculated Property
IE
[11.20; 11.80]
eV
IE
11.20
eV
NIST
IE
11.80 ± 0.25
eV
NIST
IE
11.67 ± 0.05
eV
NIST
IE
11.74
eV
NIST
IE
11.74
eV
NIST
log 10 WS
-1.36
Crippen Calculated Property
log Poct/wat
1.310
Crippen Calculated Property
McVol
68.600
ml/mol
McGowan Calculated Property
NFPA Fire
3
KDB
NFPA Health
3
KDB
Pc
[3779.42; 3880.00]
kPa
Pc
3880.00
kPa
KDB
Pc
3880.00 ± 10.00
kPa
NIST
Pc
3790.00 ± 91.19
kPa
NIST
Pc
3779.42 ± 81.06
kPa
NIST
Pc
3779.42 ± 81.06
kPa
NIST
Pc
3789.55 ± 81.06
kPa
NIST
Pc
3799.69 ± 81.06
kPa
NIST
Inp
[619.00; 686.00]
Inp
638.86
NIST
Inp
639.74
NIST
Inp
640.72
NIST
Inp
641.67
NIST
Inp
642.74
NIST
Inp
643.90
NIST
Inp
645.19
NIST
Inp
646.43
NIST
Inp
647.77
NIST
Inp
649.23
NIST
Inp
635.94
NIST
Inp
635.87
NIST
Inp
635.97
NIST
Inp
636.14
NIST
Inp
636.54
NIST
Inp
636.93
NIST
Inp
637.50
NIST
Inp
638.14
NIST
Inp
Outlier 686.00
NIST
Inp
638.10
NIST
Inp
624.00
NIST
Inp
622.00
NIST
Inp
642.00
NIST
Inp
640.00
NIST
Inp
633.00
NIST
Inp
619.00
NIST
Inp
641.00
NIST
Inp
640.00
NIST
Inp
640.00
NIST
Inp
640.00
NIST
Inp
641.00
NIST
Inp
643.00
NIST
Inp
638.00
NIST
Inp
646.00
NIST
Inp
Outlier 680.00
NIST
Inp
642.00
NIST
Inp
642.00
NIST
Inp
641.00
NIST
Inp
643.00
NIST
Inp
638.86
NIST
Inp
643.90
NIST
Inp
635.94
NIST
Inp
636.93
NIST
Inp
624.00
NIST
Inp
619.00
NIST
Inp
Outlier 680.00
NIST
I
[1100.00; 1100.00]
I
1100.00
NIST
I
1100.00
NIST
Tboil
[390.55; 390.70]
K
Tboil
390.70
K
KDB
Tboil
390.55
K
Measure...
Tc
[582.10; 585.40]
K
Tc
585.40
K
KDB
Tc
585.40 ± 0.20
K
NIST
Tc
582.10 ± 2.00
K
NIST
Tc
582.25 ± 0.90
K
NIST
Tc
582.15 ± 0.90
K
NIST
Tfus
[160.00; 161.25]
K
Tfus
161.20
K
KDB
Tfus
161.25 ± 0.60
K
NIST
Tfus
161.15 ± 0.50
K
NIST
Tfus
Outlier 160.00 ± 2.00
K
NIST
Tfus
161.25 ± 0.50
K
NIST
Tfus
160.90 ± 0.50
K
NIST
Vc
0.285
m3 /kmol
KDB
Zc
0.2275880
KDB
Temperature Dependent Properties
Property
Value
Unit
Temperature (K)
Source
Cp,gas
[118.15; 152.98]
J/mol×K
[393.00; 585.13]
Cp,gas
118.15
J/mol×K
393.00
Joback Calculated Property
Cp,gas
124.57
J/mol×K
425.02
Joback Calculated Property
Cp,gas
130.74
J/mol×K
457.04
Joback Calculated Property
Cp,gas
136.66
J/mol×K
489.07
Joback Calculated Property
Cp,gas
142.33
J/mol×K
521.09
Joback Calculated Property
Cp,gas
147.77
J/mol×K
553.11
Joback Calculated Property
Cp,gas
152.98
J/mol×K
585.13
Joback Calculated Property
Cp,liquid
[134.20; 134.90]
J/mol×K
[298.15; 303.15]
Cp,liquid
134.20
J/mol×K
298.15
NIST
Cp,liquid
134.90
J/mol×K
303.15
NIST
η
[0.0005049; 0.0005463]
Pa×s
[298.15; 308.15]
η
0.0005463
Pa×s
298.15
Molecul...
η
0.0005255
Pa×s
303.15
Molecul...
η
0.0005049
Pa×s
308.15
Molecul...
Δvap H
[33.68; 38.80]
kJ/mol
[366.50; 398.00]
Δvap H
37.70
kJ/mol
366.50
NIST
Δvap H
34.39
kJ/mol
390.40
KDB
Δvap H
33.68
kJ/mol
390.80
NIST
Δvap H
38.80
kJ/mol
398.00
NIST
ρl
[762.93; 792.00]
kg/m3
[293.00; 323.15]
ρl
792.00
kg/m3
293.00
KDB
ρl
790.86
kg/m3
293.15
Density...
ρl
786.25
kg/m3
298.15
Density...
ρl
786.27
kg/m3
298.15
Calorim...
ρl
781.63
kg/m3
303.15
Density...
ρl
776.99
kg/m3
308.15
Density...
ρl
772.32
kg/m3
313.15
Density...
ρl
767.64
kg/m3
318.15
Density...
ρl
762.93
kg/m3
323.15
Density...
γ
0.03
N/m
293.20
KDB
Correlations
Similar Compounds
Find more compounds similar to Butanenitrile .
Mixtures
Sources
KDB Vapor Pressure Data
Crippen Method
Crippen Method
Molecular interaction studies and theoretical estimation of ultrasonic speeds using scaled particle theory in binary mixtures of toluene with homologous nitriles at different temperatures
Density and Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane + n-Heptane, 2,2,4-Trimethylpentane + n-Octane, Ethyl Acetate + Benzene, and Butanenitrile + Benzene from (293.15 to 323.15) K
Experimental (Solid + Liquid) and (Liquid + Liquid) Equilibria and Excess Molar Volume of Alkanol + Acetonitrile, Propanenitrile, and Butanenitrile Mixtures
Measurements of Quaternary Liquid-Liquid Equilibrium for Water + Acetic Acid + Propionic Acid + Solvent (Butyronitrile, Benzyl Acetate, or Methyl Isobutyl Ketone) at 298.15 K
Calorimetric Study of Nitrile Group-Solvent Interactions and Comparison with Dispersive Quasi-Chemical (DISQUAC) Predictions
Joback Method
KDB
McGowan Method
NIST Webbook
The Yaws Handbook of Vapor Pressure
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