Physical Properties
Property
Value
Unit
Source
PAff
840.10
kJ/mol
NIST
BasG
[808.20; 810.00]
kJ/mol
BasG
808.20
kJ/mol
NIST
BasG
810.00 ± 0.40
kJ/mol
NIST
BasG
809.60
kJ/mol
NIST
Δc H°liquid
-3747.49 ± 0.81
kJ/mol
NIST
Δf G°
-126.44
kJ/mol
Joback Calculated Property
Δf H°gas
-290.67 ± 0.88
kJ/mol
NIST
Δf H°liquid
-328.54 ± 0.28
kJ/mol
NIST
Δfus H°
5.48
kJ/mol
Joback Calculated Property
Δvap H°
[37.87; 38.30]
kJ/mol
Δvap H°
38.00
kJ/mol
NIST
Δvap H°
38.30
kJ/mol
NIST
Δvap H°
37.87 ± 0.08
kJ/mol
NIST
Δvap H°
37.90 ± 0.10
kJ/mol
NIST
IE
[8.88; 9.40]
eV
IE
9.14 ± 0.03
eV
NIST
IE
Outlier 9.40
eV
NIST
IE
9.12 ± 0.01
eV
NIST
IE
9.17 ± 0.06
eV
NIST
IE
9.11 ± 0.01
eV
NIST
IE
9.24
eV
NIST
IE
Outlier 8.88 ± 0.04
eV
NIST
IE
9.14 ± 0.01
eV
NIST
IE
9.17 ± 0.03
eV
NIST
IE
9.18 ± 0.03
eV
NIST
IE
9.21
eV
NIST
log 10 WS
[-0.72; -0.72]
log 10 WS
-0.72
Aq. Sol...
log 10 WS
-0.72
Estimat...
log Poct/wat
1.621
Crippen Calculated Property
McVol
96.970
ml/mol
McGowan Calculated Property
Pc
3411.87
kPa
Joback Calculated Property
Inp
[665.00; 705.00]
Inp
693.10
NIST
Inp
697.44
NIST
Inp
690.48
NIST
Inp
691.81
NIST
Inp
693.30
NIST
Inp
695.47
NIST
Inp
697.00
NIST
Inp
692.00
NIST
Inp
693.00
NIST
Inp
696.00
NIST
Inp
698.00
NIST
Inp
675.00
NIST
Inp
685.00
NIST
Inp
672.00
NIST
Inp
Outlier 665.00
NIST
Inp
692.00
NIST
Inp
692.00
NIST
Inp
681.00
NIST
Inp
705.00
NIST
Inp
Outlier 665.00
NIST
Inp
693.00
NIST
Inp
692.00
NIST
Inp
695.00
NIST
Inp
692.00
NIST
Inp
692.00
NIST
Inp
693.00
NIST
Inp
705.00
NIST
Inp
698.00
NIST
Inp
Outlier 665.00
NIST
Inp
692.00
NIST
Inp
693.10
NIST
Inp
695.47
NIST
Inp
698.00
NIST
I
[949.00; 986.30]
I
986.30
NIST
I
968.50
NIST
I
974.30
NIST
I
980.20
NIST
I
978.00
NIST
I
978.00
NIST
I
949.00
NIST
I
978.00
NIST
I
968.00
NIST
I
960.00
NIST
I
986.30
NIST
I
949.00
NIST
I
978.00
NIST
S°liquid
282.40
J/mol×K
NIST
Tboil
[363.15; 447.50]
K
Tboil
379.20
K
NIST
Tboil
379.30
K
NIST
Tboil
378.63 ± 0.20
K
NIST
Tboil
379.20 ± 0.50
K
NIST
Tboil
379.40 ± 0.50
K
NIST
Tboil
379.00 ± 0.30
K
NIST
Tboil
378.35 ± 0.50
K
NIST
Tboil
378.65 ± 0.50
K
NIST
Tboil
377.00 ± 2.00
K
NIST
Tboil
363.15
K
NIST
Tboil
399.15 ± 0.50
K
NIST
Tboil
383.40 ± 5.00
K
NIST
Tboil
378.90 ± 0.50
K
NIST
Tboil
378.15 ± 1.00
K
NIST
Tboil
379.35 ± 0.50
K
NIST
Tboil
378.15 ± 2.00
K
NIST
Tboil
378.15 ± 1.00
K
NIST
Tboil
379.35 ± 0.50
K
NIST
Tboil
379.65 ± 0.50
K
NIST
Tboil
378.75 ± 1.00
K
NIST
Tboil
378.65 ± 0.50
K
NIST
Tboil
379.20 ± 0.50
K
NIST
Tboil
379.15 ± 1.50
K
NIST
Tboil
379.65 ± 0.30
K
NIST
Tboil
378.65 ± 2.00
K
NIST
Tboil
378.85 ± 1.00
K
NIST
Tboil
376.15 ± 5.00
K
NIST
Tboil
379.00 ± 2.50
K
NIST
Tboil
Outlier 447.50 ± 0.30
K
NIST
Tboil
377.15 ± 2.00
K
NIST
Tboil
378.15 ± 3.00
K
NIST
Tboil
379.40 ± 1.00
K
NIST
Tboil
377.65 ± 1.00
K
NIST
Tboil
378.95 ± 1.00
K
NIST
Tboil
379.30 ± 1.00
K
NIST
Tboil
378.15 ± 1.00
K
NIST
Tboil
379.15 ± 0.50
K
NIST
Tboil
378.15 ± 1.00
K
NIST
Tc
562.90
K
NIST
Tfus
[220.65; 223.40]
K
Tfus
220.65
K
Aq. Sol...
Tfus
220.65 ± 0.50
K
NIST
Tfus
223.40 ± 2.00
K
NIST
Tfus
220.65 ± 0.50
K
NIST
Ttriple
221.74 ± 0.05
K
NIST
Vc
0.366
m3 /kmol
Joback Calculated Property
Temperature Dependent Properties
Correlations
Similar Compounds
Find more compounds similar to 2-Butanone, 3,3-dimethyl- .
Mixtures
1-Propanol, 2,2-dimethyl- + 2-Butanone, 3,3-dimethyl-
Propane, 2-methoxy-2-methyl- + 2-Butanone, 3,3-dimethyl-
1-Propanol, 2,2-dimethyl- + Propane, 2-methoxy-2-methyl- + 2-Butanone, 3,3-dimethyl-
2-Butanone, 3,3-dimethyl- + Water
2-Butanone, 3,3-dimethyl- + Phenol + Water
2-Butanone, 3,3-dimethyl- + Propanoic acid + Water
Butanoic acid + 2-Butanone, 3,3-dimethyl- + Water
Acetic acid + 2-Butanone, 3,3-dimethyl- + Water
Phenol, 2-methyl- + 2-Butanone, 3,3-dimethyl- + Water
Phenol, 3-methyl- + 2-Butanone, 3,3-dimethyl- + Water
p-Cresol + 2-Butanone, 3,3-dimethyl- + Water
Sources
KDB Vapor Pressure Data
Crippen Method
Isothermal vapour liquid equilibria in the binary and ternary systems composed of tert-butyl methyl ether, 3,3-dimethyl-2-butanone and 2,2-dimethyl-1-propanol
Screening solvents to extract phenol from aqueous solutions by the COSMO-SAC model and extraction process simulation
Liquid Phase Equilibria of the Water + Propionic or Butyric Acid + Methyl tert-Butyl Ketone Ternary Systems at (298.15 and 323.15) K
Liquid Liquid Phase Equilibria for the Ternary Water + Acetic Acid + 3,3-Dimethyl-2-butanone System at (298.15, 313.15 and 323.15) K
Liquid Liquid Equilibrium for the Ternary Systems Methyl tert-Butyl Ketone + o-, m-, p-Cresol + Water at (298.2, 313.2, and 323.2) K
Phase Equilibrium on Extraction Methylphenols from Aqueous Solution with 3,3-Dimethyl-2-butanone at 333.2 K and 353.2 K
Air-Water Partitioning of C5 and C6 Alkanones: Measurement, Critical Compilation, Correlation, and Recommended Data
Joback Method
KDB
Aqueous Solubility Prediction Method
Estimated Solubility Method
McGowan Method
NIST Webbook
The Yaws Handbook of Vapor Pressure
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Outlier This icon means
that the value is more than 2 standard deviations away from the
property mean.