Physical Properties
Property
Value
Unit
Source
ω
0.4030
PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
εr
5.01
NCMS SOLV-DB
Tflash,cc
296.15
K
NCMS SOLV-DB
Δf H°gas
-526.26
kJ/mol
Relay (1.0) Calculated Property
Δfus H°
12.14
kJ/mol
Joback Calculated Property
Δvap H°
42.96
kJ/mol
Relay (1.0) Calculated Property
IE
[9.90; 9.97]
eV
IE
9.90
eV
NIST
IE
9.90
eV
NIST
IE
9.97 ± 0.05
eV
NIST
IE
9.91 ± 0.03
eV
NIST
log 10 WS
-0.99
Relay (1.0) Calculated Property
log Poct/wat
1.509
NCMS SOLV-DB
McVol
102.840
ml/mol
McGowan Calculated Property
NFPA Fire
3
NCMS SOLV-DB
NFPA Health
1
NCMS SOLV-DB
NFPA Safety
0
NCMS SOLV-DB
Pc
[3010.00; 3124.86]
kPa
Pc
3010.00
kPa
IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value
Pc
3124.86
kPa
PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Inp
[737.00; 758.00]
Inp
746.00
NIST
Inp
740.00
NIST
Inp
738.10
NIST
Inp
746.00
NIST
Inp
737.00
NIST
Inp
749.00
NIST
Inp
745.00
NIST
Inp
Outlier 758.00
NIST
Inp
738.00
NIST
Inp
746.00
NIST
Inp
744.00
NIST
Inp
749.00
NIST
Inp
746.00
NIST
Ip
[974.00; 993.00]
Ip
985.00
NIST
Ip
990.00
NIST
Ip
988.00
NIST
Ip
974.00
NIST
Ip
974.00
NIST
Ip
993.00
NIST
Ip
982.00
NIST
Ip
974.00
NIST
Ip
985.00
NIST
Tboil
[383.20; 389.65]
K
Tboil
385.33
K
Experimental isobaric vapour-liquid equilibrium data for the binary system (N, N-dimethyl acetamide + dimethyl sulfoxide) and the quaternary system (sec-butyl acetate + sec-butyl alcohol + N, N-dimethyl acetamide + dimethyl sulfoxide) at 101.3 kPa
Tboil
385.12
K
Isobaric Vapor Liquid Equilibrium for the Binary Systems of sec-Butyl Acetate + n-Butyl Alcohol, Isobutyl Alcohol, or tert-Butyl Alcohol at 101.3 kPa
Tboil
385.15
K
Isobaric Vapor-Liquid Equilibrium for Two Binary Systems of n-Heptane + sec-Butyl Acetate and Methylcyclohexane + sec-Butyl Acetate under Atmosphere
Tboil
385.15
K
Isobaric Vapor-Liquid Equilibrium for the Binary Systems of 1,2-Dichloroethane + sec-Butyl Acetate, n-Propyl Acetate, and tert-Butyl Acetate at 101.3 kPa
Tboil
385.25
K
Experimental Measurements of Vapor Liquid Equilibrium Data for the Binary Systems of Methanol + 2-Butyl Acetate, 2-Butyl Alcohol + 2-Butyl Acetate, and Methyl Acetate + 2-Butyl Acetate at 101.33 kPa
Tboil
385.20
K
Investigation on Isobaric Vapor Liquid Equilibrium for Water + Acetic Acid + sec-Butyl Acetate
Tboil
385.49
K
NCMS SOLV-DB
Tboil
385.40
K
NIST
Tboil
385.00
K
NIST
Tboil
384.00 ± 3.00
K
NIST
Tboil
383.20 ± 2.00
K
NIST
Tboil
385.00 ± 2.00
K
NIST
Tboil
Outlier 389.65 ± 1.00
K
NIST
Tboil
385.35 ± 1.00
K
NIST
Tc
[560.00; 571.00]
K
Tc
571.00
K
IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value
Tc
560.00
K
PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tfus
[174.15; 174.25]
K
Tfus
174.15
K
Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus
174.25
K
NCMS SOLV-DB
Vc
0.388
m3 /kmol
PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
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Temperature Dependent Properties
Property
Value
Unit
Temperature (K)
Source
η
0.0006500
Pa×s
298.15
NCMS SOLV-DB
Pvap
[2.96; 101.33]
kPa
[298.15; 385.25]
Pvap
2.96
kPa
298.15
NCMS SOLV-DB
Pvap
101.30
kPa
385.15
Isobaric Vapor-Liquid Equilibrium for Two Binary Systems of n-Heptane + sec-Butyl Acetate and Methylcyclohexane + sec-Butyl Acetate under Atmosphere
Pvap
101.30
kPa
385.15
Isobaric Vapor-Liquid Equilibrium for the Binary Systems of 1,2-Dichloroethane + sec-Butyl Acetate, n-Propyl Acetate, and tert-Butyl Acetate at 101.3 kPa
Pvap
101.33
kPa
385.25
Experimental Measurements of Vapor Liquid Equilibrium Data for the Binary Systems of Methanol + 2-Butyl Acetate, 2-Butyl Alcohol + 2-Butyl Acetate, and Methyl Acetate + 2-Butyl Acetate at 101.33 kPa
n 0
[1.38700; 1.38700]
[298.15; 298.15]
n 0
1.38700
298.15
Liquid-Liquid Equilibria for the System 1-Methyl Propyl Ethanoate (1) + Acetic Acid (2) + Water (3) at (283.15 and 323.15) K
n 0
1.38700
298.15
NCMS SOLV-DB
ρl
[863.80; 871.00]
kg/m3
[293.15; 298.15]
ρl
871.00
kg/m3
293.15
Liquid - liquid equilibrium for the quaternary reaction system water p sec-butyl alcohol p sec-butyl acetate p acetic acid
ρl
866.40
kg/m3
298.15
Isobaric vapor-liquid equilibrium of the binary system sec-butyl acetate + para-xylene and the quaternary system methyl acetate + para-xylene + sec-butyl acetate + acetic acid at 101.3 kPa
ρl
863.80
kg/m3
298.15
Isobaric Vapor Liquid Equilibrium for the Binary Systems of sec-Butyl Acetate + Methyl Ethyl Ketone, 2-Methoxyethanol, or 1,2-Dimethoxyethane at 101.3 kPa
ρl
867.00
kg/m3
298.15
Isobaric Vapor-Liquid Equilibrium for the Binary Systems of Sec-butyl Acetate and Ethanol, 1-Propanol, or 2-Propanol at 101.3 kPa
γ
0.03
N/m
298.15
NCMS SOLV-DB
Datasets
Mass density, kg/m3
Fixed
Measured
Temperature, K - Liquid
Pressure, kPa - Liquid
Mass density, kg/m3 - Liquid
298.15
100.00
865.5
Reference
Correlations
Property
Value
Unit
Temperature (K)
Source
Cp,gas
[148.79; 337.52]
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 2.11610e+01
Coefficient B 5.24960e-01
Coefficient C -2.11200e-04
Coefficient D 2.60000e-09
Coefficient E 0.00000e+00
Temperature range, min. 273.00
Temperature range, max. 1000.00
Cp,gas
148.79
J/mol×K
273.00
Calculated Property
Cp,gas
180.56
J/mol×K
353.78
Calculated Property
Cp,gas
209.62
J/mol×K
434.56
Calculated Property
Cp,gas
235.96
J/mol×K
515.33
Calculated Property
Cp,gas
259.60
J/mol×K
596.11
Calculated Property
Cp,gas
280.54
J/mol×K
676.89
Calculated Property
Cp,gas
298.80
J/mol×K
757.67
Calculated Property
Cp,gas
314.37
J/mol×K
838.44
Calculated Property
Cp,gas
327.28
J/mol×K
919.22
Calculated Property
Cp,gas
337.52
J/mol×K
1000.00
Calculated Property
Property
Value
Unit
Temperature (K)
Source
Pvap
[6.56; 1893.93]
kPa
[313.15; 523.15]
KDB Vapor Pressure Data
Equation ln(Y) = A + B/T + C·ln(T) + D·T² + E/T² Y is Pvap in kPa, T in K
Coefficient A 1.94870e+01
Coefficient B -5.11855e+03
Coefficient C -1.39214e-01
Coefficient D -4.69511e-06
Coefficient E 0.00000e+00
Temperature range, min. 313.15
Temperature range, max. 523.15
Pvap
6.56
kPa
313.15
Calculated Property
Pvap
18.79
kPa
336.48
Calculated Property
Pvap
46.26
kPa
359.82
Calculated Property
Pvap
100.53
kPa
383.15
Calculated Property
Pvap
196.88
kPa
406.48
Calculated Property
Pvap
353.11
kPa
429.82
Calculated Property
Pvap
587.51
kPa
453.15
Calculated Property
Pvap
916.16
kPa
476.48
Calculated Property
Pvap
1350.29
kPa
499.82
Calculated Property
Pvap
1893.93
kPa
523.15
Calculated Property
Similar Compounds
Find more compounds similar to sec-Butyl acetate .
Mixtures
Find more mixtures with sec-Butyl acetate .
Sources
KDB Vapor Pressure Data
Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) ChEDL chemicals 1.5.2, from Bradley, J.-C.; Williams, A.; Lang, A. Jean-Claude Bradley Open Melting Point Dataset. Figshare, 2014 (CC0).
IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 ChEDL chemicals 1.5.2, from Kudchadker, A. P.; Ambrose, D.; Tsonopoulos, C. Vapor-Liquid Critical Properties of Elements and Compounds. 7. Oxygen Compounds Other Than Alkanols and Cycloalkanols. J. Chem. Eng. Data 2001, 46, 457-479.
PSRK revision IV (2005), critical constants and acentric factors of 1000 components ChEDL chemicals 1.5.2, from Horstmann, S.; Jabłoniec, A.; Krafczyk, J.; Fischer, K.; Gmehling, J. PSRK Group Contribution Equation of State: Comprehensive Revision and Extension IV, Including Critical Constants and α-Function Parameters for 1000 Components. Fluid Phase Equilib. 2005, 227, 157-164.
Cheméo Relay (1.0)
Crippen Method
Solubility and limiting activity coefficient of simvastatin in different organic solvents
Liquid liquid equilibrium of the ternary system water + acetic acid + sec-butyl acetate
Experimental isobaric vapor-liquid equilibrium for ternary system of sec-butyl alcohol + sec-butyl acetate + N,N-dimethyl formamide at 101.3 kPa
Isobaric vapor-liquid equilibrium for ternary system of sec-butyl alcohol + sec-butyl acetate + N,N- dimethyl acetamide at 101.3 kPa
Isobaric vapor-liquid equilibrium of the binary system sec-butyl acetate + para-xylene and the quaternary system methyl acetate + para-xylene + sec-butyl acetate + acetic acid at 101.3 kPa
Experimental isobaric vapor-liquid equilibrium for the ternary system of sec-butyl alcohol + sec-butyl acetate + dimethyl sulfoxide at 101.3 kPa
Liquid - liquid equilibrium for the quaternary reaction system water p sec-butyl alcohol p sec-butyl acetate p acetic acid
Experimental isobaric vapour-liquid equilibrium data for the binary system (N, N-dimethyl acetamide + dimethyl sulfoxide) and the quaternary system (sec-butyl acetate + sec-butyl alcohol + N, N-dimethyl acetamide + dimethyl sulfoxide) at 101.3 kPa
Isobaric Vapor Liquid Equilibrium for the Binary Systems of sec-Butyl Acetate + Methyl Ethyl Ketone, 2-Methoxyethanol, or 1,2-Dimethoxyethane at 101.3 kPa
Isobaric Vapor Liquid Equilibrium for the Binary Systems of sec-Butyl Acetate + n-Butyl Alcohol, Isobutyl Alcohol, or tert-Butyl Alcohol at 101.3 kPa
Isobaric Vapor-Liquid Equilibrium for the Binary Systems of Sec-butyl Acetate and Ethanol, 1-Propanol, or 2-Propanol at 101.3 kPa
Isobaric Vapor-Liquid Equilibrium for Two Binary Systems of n-Heptane + sec-Butyl Acetate and Methylcyclohexane + sec-Butyl Acetate under Atmosphere
Isobaric Vapor-Liquid Equilibrium for the Binary Systems of 1,2-Dichloroethane + sec-Butyl Acetate, n-Propyl Acetate, and tert-Butyl Acetate at 101.3 kPa
Liquid-Liquid Equilibrium of the Ternary System sec-Butyl Acetate + sec-Butyl Alcohol + Ethylene Glycol at 298.2, 308.2, and 318.2 K
Isobaric Vapor-Liquid Equilibria of Binary Mixtures of Diethyl Carbonate with Isopropyl Acetate, sec-Butyl Acetate, or Isoamyl Acetate at 101.3 kPa
Experimental Measurements of Vapor Liquid Equilibrium Data for the Binary Systems of Methanol + 2-Butyl Acetate, 2-Butyl Alcohol + 2-Butyl Acetate, and Methyl Acetate + 2-Butyl Acetate at 101.33 kPa
Investigation on Isobaric Vapor Liquid Equilibrium for Water + Acetic Acid + sec-Butyl Acetate
Solubility of Lovastatin in Ethyl Acetate, Propyl Acetate, Isopropyl Acetate, Butyl Acetate, sec-Butyl Acetate, Isobutyl Acetate, tert-Butyl Acetate, and 2-Butanone, between (285 and 313) K
Liquid-Liquid Equilibria for the System 1-Methyl Propyl Ethanoate (1) + Acetic Acid (2) + Water (3) at (283.15 and 323.15) K
Joback Method
McGowan Method
NIST Webbook
NCMS SOLV-DB
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