Chemical Properties of 2-Butanol, 2-methyl-, acetate (CAS 625-16-1)

2-Butanol, 2-methyl-, acetate

InChI
InChI=1S/C7H14O2/c1-5-7(3,4)9-6(2)8/h5H2,1-4H3
InChI Key
JCCIFDCPHCKATH-UHFFFAOYSA-N
Formula
C7H14O2
SMILES
CCC(C)(C)OC(C)=O
Molecular Weight1
130.18
CAS
625-16-1
Other Names
  • 1,1-dimethylpropyl acetate
  • 1,1-dimethylpropyl ethanoate
  • 2-methyl-2-butyl acetate
  • CH3C(O)OC(CH3)2CH2CH3
  • acetic acid, 1,1-dimethylpropyl ester
  • ethanoic acid, 1,1-dimethylpropyl ester
  • tert-Amyl ethanoate
  • tert-Pentyl Alcohol, acetate
  • tert-amyl acetate
  • tert-pentyl acetate
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Physical Properties

Property Value Unit Source
ΔcH°liquid -4173.60 ± 1.50 kJ/mol NIST
ΔfH°gas -539.00 ± 1.50 kJ/mol NIST
ΔfH°liquid -581.80 ± 1.50 kJ/mol NIST
ΔfusH° 10.84 kJ/mol Joback Calculated Property
ΔvapH° [40.30; 42.80] kJ/mol Show Hide
ΔvapH° 40.30 kJ/mol NIST
ΔvapH° 42.80 ± 0.34 kJ/mol NIST
ΔvapH° 42.80 kJ/mol NIST
ΔvapH° 42.80 ± 0.30 kJ/mol NIST
IE 9.76 eV Relay (1.0) Calculated Property
log10WS -1.26 Relay (1.0) Calculated Property
logPoct/wat 1.738 Crippen Calculated Property
McVol 116.930 ml/mol McGowan Calculated Property
Pc 2871.95 kPa Joback Calculated Property
Inp [753.00; 793.00]   Show Hide
Inp 753.00 NIST
Inp 764.00 NIST
Inp 793.00 NIST
Inp 793.00 NIST
I [917.00; 1003.00]   Show Hide
I 917.00 NIST
I 1003.00 NIST
I 1003.00 NIST
Tboil [393.15; 397.65] K Show Hide
Tboil 396.65 ± 0.60 K NIST
Tboil 393.15 ± 1.00 K NIST
Tboil 397.65 ± 1.00 K NIST
Tfus 200.58 K Relay (1.0) Calculated Property

Cheméo can also estimate Critical Temperature, Critical Volume, Standard Gibbs free energy of formation, Acentric Factor for this compound, but they fall outside the models' validated range, so they are not shown here. Open the prediction tool to compute them on demand.

Temperature Dependent Properties

Property Value Unit Temperature (K) Source
ΔvapH 42.80 kJ/mol 209.00 NIST
Pvap [0.39; 2.99] kPa [273.70; 308.40] Show Hide
Pvap 0.39 kPa 273.70 Transpiration method: Vapor pressures and enthalpies of vaporization of some low-boiling esters
Pvap 0.40 kPa 274.00 Transpiration method: Vapor pressures and enthalpies of vaporization of some low-boiling esters
Pvap 0.44 kPa 275.50 Transpiration method: Vapor pressures and enthalpies of vaporization of some low-boiling esters
Pvap 0.51 kPa 277.50 Transpiration method: Vapor pressures and enthalpies of vaporization of some low-boiling esters
Pvap 0.52 kPa 278.60 Transpiration method: Vapor pressures and enthalpies of vaporization of some low-boiling esters
Pvap 0.57 kPa 279.50 Transpiration method: Vapor pressures and enthalpies of vaporization of some low-boiling esters
Pvap 0.64 kPa 281.60 Transpiration method: Vapor pressures and enthalpies of vaporization of some low-boiling esters
Pvap 0.72 kPa 283.50 Transpiration method: Vapor pressures and enthalpies of vaporization of some low-boiling esters
Pvap 0.74 kPa 283.60 Transpiration method: Vapor pressures and enthalpies of vaporization of some low-boiling esters
Pvap 0.88 kPa 286.60 Transpiration method: Vapor pressures and enthalpies of vaporization of some low-boiling esters
Pvap 0.95 kPa 288.40 Transpiration method: Vapor pressures and enthalpies of vaporization of some low-boiling esters
Pvap 1.05 kPa 289.70 Transpiration method: Vapor pressures and enthalpies of vaporization of some low-boiling esters
Pvap 1.22 kPa 292.70 Transpiration method: Vapor pressures and enthalpies of vaporization of some low-boiling esters
Pvap 1.34 kPa 293.50 Transpiration method: Vapor pressures and enthalpies of vaporization of some low-boiling esters
Pvap 1.49 kPa 295.80 Transpiration method: Vapor pressures and enthalpies of vaporization of some low-boiling esters
Pvap 1.70 kPa 298.40 Transpiration method: Vapor pressures and enthalpies of vaporization of some low-boiling esters
Pvap 1.79 kPa 298.80 Transpiration method: Vapor pressures and enthalpies of vaporization of some low-boiling esters
Pvap 2.08 kPa 301.90 Transpiration method: Vapor pressures and enthalpies of vaporization of some low-boiling esters
Pvap 2.33 kPa 303.40 Transpiration method: Vapor pressures and enthalpies of vaporization of some low-boiling esters
Pvap 2.42 kPa 304.90 Transpiration method: Vapor pressures and enthalpies of vaporization of some low-boiling esters
Pvap 2.83 kPa 307.90 Transpiration method: Vapor pressures and enthalpies of vaporization of some low-boiling esters
Pvap 2.99 kPa 308.40 Transpiration method: Vapor pressures and enthalpies of vaporization of some low-boiling esters

Correlations

Property Value Unit Temperature (K) Source
Cp,gas [168.86; 390.04] J/mol×K [273.00; 1000.00] Joback Predicted correlation Show Hide
EquationY = A + B·T + C·T² + D·T³ + E·T⁴
Y is Cp,gas in J/mol×K, T in K
Coefficient A-2.53900e+00
Coefficient B7.39880e-01
Coefficient C-4.34200e-04
Coefficient D8.69000e-08
Coefficient E0.00000e+00
Temperature range, min.273.00
Temperature range, max.1000.00
Cp,gas 168.86 J/mol×K 273.00 Calculated Property
Cp,gas 208.72 J/mol×K 353.78 Calculated Property
Cp,gas 244.12 J/mol×K 434.56 Calculated Property
Cp,gas 275.33 J/mol×K 515.33 Calculated Property
Cp,gas 302.63 J/mol×K 596.11 Calculated Property
Cp,gas 326.29 J/mol×K 676.89 Calculated Property
Cp,gas 346.58 J/mol×K 757.67 Calculated Property
Cp,gas 363.79 J/mol×K 838.44 Calculated Property
Cp,gas 378.19 J/mol×K 919.22 Calculated Property
Cp,gas 390.04 J/mol×K 1000.00 Calculated Property
Property Value Unit Temperature (K) Source
η [0.0103557; 0.0002612] Pa×s [213.40; 419.17] Joback Predicted correlation Show Hide
EquationY = exp(A + B/T + C·ln(T) + D·T^E)
Y is η in Pa×s, T in K
Coefficient A-1.20670e+01
Coefficient B1.59982e+03
Coefficient C0.00000e+00
Coefficient D0.00000e+00
Coefficient E0.00000e+00
CommentLiquid phase. Joback/Reid (1987), valid from Tf to 0.7·Tc.
Temperature range, min.213.40
Temperature range, max.419.17
η 0.0103557 Pa×s 213.40 Calculated Property
η 0.0050132 Pa×s 236.26 Calculated Property
η 0.0027583 Pa×s 259.13 Calculated Property
η 0.0016721 Pa×s 281.99 Calculated Property
η 0.0010926 Pa×s 304.85 Calculated Property
η 0.0007576 Pa×s 327.72 Calculated Property
η 0.0005511 Pa×s 350.58 Calculated Property
η 0.0004167 Pa×s 373.44 Calculated Property
η 0.0003255 Pa×s 396.31 Calculated Property
η 0.0002612 Pa×s 419.17 Calculated Property
Property Value Unit Temperature (K) Source
Pvap [1.33; 202.66] kPa [296.82; 420.70] The Yaws Handbook of Vapor Pressure Show Hide
Equationln(Y) = A + B/(T + C)
Y is Pvap in kPa, T in K
Coefficient A1.52581e+01
Coefficient B-3.67169e+03
Coefficient C-5.15580e+01
Temperature range, min.296.82
Temperature range, max.420.70
Pvap 1.33 kPa 296.82 Calculated Property
Pvap 2.95 kPa 310.58 Calculated Property
Pvap 6.04 kPa 324.35 Calculated Property
Pvap 11.53 kPa 338.11 Calculated Property
Pvap 20.74 kPa 351.88 Calculated Property
Pvap 35.44 kPa 365.64 Calculated Property
Pvap 57.90 kPa 379.41 Calculated Property
Pvap 90.92 kPa 393.17 Calculated Property
Pvap 137.87 kPa 406.94 Calculated Property
Pvap 202.66 kPa 420.70 Calculated Property

Similar Compounds

Propanoic acid, 1,1-dimethylpropyl ester. Acetic acid, chloro, 1,1-dimethylpropyl ester. Acetic acid, bromo, 1,1-dimethylpropyl ester. Acetic acid, dibromo, 1,1-dimethylpropyl ester. Acetic acid, dichloro, 1,1-dimethylpropyl ester. Acetic acid, 3-ethylpent-3-yl ester. Acetic acid, trichloro, 1,1-dimethylpropyl ester. Acetic acid, tribromo, 1,1-dimethylpropyl ester. Propanoic acid, 3-chloro, 1,1-dimethylpropyl ester. Butyric acid, neopentyl ester. Propanoic acid, 2-chloro, 1,1-dimethylpropyl ester. 2-Methylpentan-2-yl acetate. 3-Methyl-3-pentanol, trifluoroacetate. Isopropyl tert-pentyl ether. Butane, 2-ethoxy-2-methyl-.

Find more compounds similar to 2-Butanol, 2-methyl-, acetate.

Sources

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