Physical Properties
Property
Value
Unit
Source
ω
0.5062
Relay (1.0) Calculated Property
Δf G°
-138.15
kJ/mol
Joback Calculated Property
Δf H°gas
-411.26
kJ/mol
Relay (1.0) Calculated Property
Δf H°liquid
-413.10 ± 3.30
kJ/mol
NIST
Δfus H°
16.67
kJ/mol
Joback Calculated Property
Δvap H°
46.19
kJ/mol
Relay (1.0) Calculated Property
IE
9.81
eV
Relay (1.0) Calculated Property
log 10 WS
-2.06
Relay (1.0) Calculated Property
log Poct/wat
1.906
Crippen Calculated Property
McVol
126.720
ml/mol
McGowan Calculated Property
Pc
2790.61
kPa
Joback Calculated Property
Inp
[960.00; 989.00]
Inp
964.00
NIST
Inp
967.00
NIST
Inp
960.00
NIST
Inp
962.00
NIST
Inp
962.00
NIST
Inp
962.00
NIST
Inp
967.00
NIST
Inp
989.00
NIST
Inp
989.00
NIST
Inp
967.00
NIST
I
[1190.00; 1232.00]
I
1232.00
NIST
I
1220.00
NIST
I
1190.00
NIST
I
1190.00
NIST
Tboil
434.70
K
NIST
Tc
616.18
K
Relay (1.0) Calculated Property
Tfus
[196.80; 196.80]
K
Tfus
196.80
K
NIST
Tfus
196.80 ± 0.20
K
NIST
Ttriple
197.78 ± 0.01
K
NIST
Vc
0.478
m3 /kmol
Relay (1.0) Calculated Property
Temperature Dependent Properties
Property
Value
Unit
Temperature (K)
Source
Cp,gas
[262.99; 327.16]
J/mol×K
[455.29; 637.18]
Cp,gas
262.99
J/mol×K
455.29
Joback Calculated Property
Cp,gas
274.81
J/mol×K
485.61
Joback Calculated Property
Cp,gas
286.17
J/mol×K
515.92
Joback Calculated Property
Cp,gas
297.08
J/mol×K
546.24
Joback Calculated Property
Cp,gas
307.54
J/mol×K
576.55
Joback Calculated Property
Cp,gas
317.57
J/mol×K
606.87
Joback Calculated Property
Cp,gas
327.16
J/mol×K
637.18
Joback Calculated Property
Cp,liquid
273.80
J/mol×K
298.15
NIST
Δfus H
15.55
kJ/mol
197.80
NIST
Δvap H
[45.10; 47.40]
kJ/mol
[358.00; 390.50]
Δvap H
47.40
kJ/mol
358.00
NIST
Δvap H
45.10
kJ/mol
390.50
NIST
ρl
[871.64; 895.23]
kg/m3
[293.15; 318.15]
ρl
895.19
kg/m3
293.15
Densities, ultrasonic speeds, excess and partial molar properties of binary mixtures of acetonitrile with some alkyl methacrylates at temperatures from 293.15 K to 318.15 K
ρl
895.23
kg/m3
293.15
Density, excess volume, and excess coefficient of thermal expansion of the binary systems of dimethyl carbonate with butyl methacrylate, allyl methacrylate, styrene, and vinyl acetate at T = (293.15, 303.15, and 313.15) K
ρl
890.44
kg/m3
298.15
Densities, isobaric thermal compressibilities and derived thermodynamic properties of the binary systems of cyclohexane with allyl methacrylate, butyl methacrylate, methacrylic acid, and vinyl acetate at t = (298.15 and 308.15)K
ρl
890.44
kg/m3
298.15
Densities and derived thermodynamic properties of the binary systems of 1,1-dimethylethyl methyl ether with allyl methacrylate, butyl methacrylate, methacrylic acid, and vinyl acetate at T = (298.15 and 308.15) K
ρl
890.48
kg/m3
298.15
Densities, ultrasonic speeds, excess and partial molar properties of binary mixtures of acetonitrile with some alkyl methacrylates at temperatures from 293.15 K to 318.15 K
ρl
885.99
kg/m3
303.15
Density, excess volume, and excess coefficient of thermal expansion of the binary systems of dimethyl carbonate with butyl methacrylate, allyl methacrylate, styrene, and vinyl acetate at T = (293.15, 303.15, and 313.15) K
ρl
885.78
kg/m3
303.15
Densities, ultrasonic speeds, excess and partial molar properties of binary mixtures of acetonitrile with some alkyl methacrylates at temperatures from 293.15 K to 318.15 K
ρl
881.07
kg/m3
308.15
Densities, ultrasonic speeds, excess and partial molar properties of binary mixtures of acetonitrile with some alkyl methacrylates at temperatures from 293.15 K to 318.15 K
ρl
880.86
kg/m3
308.15
Densities and derived thermodynamic properties of the binary systems of 1,1-dimethylethyl methyl ether with allyl methacrylate, butyl methacrylate, methacrylic acid, and vinyl acetate at T = (298.15 and 308.15) K
ρl
880.86
kg/m3
308.15
Densities, isobaric thermal compressibilities and derived thermodynamic properties of the binary systems of cyclohexane with allyl methacrylate, butyl methacrylate, methacrylic acid, and vinyl acetate at t = (298.15 and 308.15)K
ρl
876.19
kg/m3
313.15
Density, excess volume, and excess coefficient of thermal expansion of the binary systems of dimethyl carbonate with butyl methacrylate, allyl methacrylate, styrene, and vinyl acetate at T = (293.15, 303.15, and 313.15) K
ρl
876.35
kg/m3
313.15
Densities, ultrasonic speeds, excess and partial molar properties of binary mixtures of acetonitrile with some alkyl methacrylates at temperatures from 293.15 K to 318.15 K
ρl
871.64
kg/m3
318.15
Densities, ultrasonic speeds, excess and partial molar properties of binary mixtures of acetonitrile with some alkyl methacrylates at temperatures from 293.15 K to 318.15 K
Correlations
Similar Compounds
Find more compounds similar to n-Butyl methacrylate .
Mixtures
Sources
KDB Vapor Pressure Data
Cheméo Relay (1.0)
Crippen Method
Crippen Method
Liquid liquid equilibria for the ternary systems water + 1-propanol + methyl methacrylate, +butyl methacrylate, and +isobutyl methacrylate
Liquid liquid equilibria of water + 1-butanol + methyl methacrylate or butyl methacrylate or isobutyl methacrylate at 288.15K and 318.15K
Densities and derived thermodynamic properties of the binary systems of 1,1-dimethylethyl methyl ether with allyl methacrylate, butyl methacrylate, methacrylic acid, and vinyl acetate at T = (298.15 and 308.15) K
Density, excess volume, and excess coefficient of thermal expansion of the binary systems of dimethyl carbonate with butyl methacrylate, allyl methacrylate, styrene, and vinyl acetate at T = (293.15, 303.15, and 313.15) K
Densities, ultrasonic speeds, excess and partial molar properties of binary mixtures of acetonitrile with some alkyl methacrylates at temperatures from 293.15 K to 318.15 K
Densities, speeds of sound and excess properties of (benzonitrile + methyl methacrylate, or + ethyl methacrylate, or + n-butyl methacrylate) binary mixtures at temperatures from 293.15 K to 318.15 K
Densities, isobaric thermal compressibilities and derived thermodynamic properties of the binary systems of cyclohexane with allyl methacrylate, butyl methacrylate, methacrylic acid, and vinyl acetate at t = (298.15 and 308.15)K
Liquid-Liquid Equilibria for the Ternary Systems Water + 2-Propanol + Methyl Methacrylate, + Butyl Methacrylate, and + Isobutyl Methacrylate
Liquid-Liquid Equilibria of Water + 2-Butanol + (Methyl Methacrylate or Butyl Methacrylate or Isobutyl Methacrylate) at (288.2 and 318.2) K
Joback Method
KDB
McGowan Method
NIST Webbook
The Yaws Handbook of Vapor Pressure
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