- InChI
- InChI=1S/C7H12O3/c1-2-3-7(8)10-5-6-4-9-6/h6H,2-5H2,1H3
- InChI Key
- YLNSNVGRSIOCEU-UHFFFAOYSA-N
- Formula
- C7H12O3
- SMILES
- CCCC(=O)OCC1CO1
- Molecular Weight1
- 144.17
- ω : Acentric Factor.
- ΔcH°liquid : Standard liquid enthalpy of combustion (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- η : Dynamic viscosity (Pa×s).
- ΔfH°gas : Enthalpy of formation at standard conditions (kJ/mol).
- ΔfH°liquid : Liquid phase enthalpy of formation at standard conditions (kJ/mol).
- ΔfusH° : Enthalpy of fusion at standard conditions (kJ/mol).
- ΔvapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
- IE : Ionization energy (eV).
- log10WS : Log10 of Water solubility in mol/l.
- logPoct/wat : Octanol/Water partition coefficient.
- McVol : McGowan's characteristic volume (ml/mol).
- Pc : Critical Pressure (kPa).
- n0 : Refractive Index.
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Vc : Critical Volume (m3/kmol).
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.5146 | Relay (1.0) Calculated Property | |
| ΔcH°liquid | -3909.20 ± 4.20 | kJ/mol | NIST |
| ΔfH°gas | -501.70 ± 2.80 | kJ/mol | NIST |
| ΔfH°liquid | -560.40 ± 4.20 | kJ/mol | NIST |
| ΔfusH° | 24.37 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [58.00; 58.70] | kJ/mol |
|
| ΔvapH° | 58.70 ± 0.40 | kJ/mol | NIST |
| ΔvapH° | 58.67 ± 0.35 | kJ/mol | NIST |
| ΔvapH° | 58.00 ± 0.42 | kJ/mol | NIST |
| ΔvapH° | 58.00 ± 0.40 | kJ/mol | NIST |
| ΔvapH° | 58.70 ± 0.40 | kJ/mol | NIST |
| ΔvapH° | 58.67 ± 0.35 | kJ/mol | NIST |
| IE | 10.03 | eV | Relay (1.0) Calculated Property |
| log10WS | -0.75 | Relay (1.0) Calculated Property | |
| logPoct/wat | 0.729 | Crippen Calculated Property | |
| McVol | 111.940 | ml/mol | McGowan Calculated Property |
| Pc | 3213.68 | kPa | Joback Calculated Property |
| Tboil | 461.76 | K | Relay (1.0) Calculated Property |
| Tc | 639.99 | K | Relay (1.0) Calculated Property |
| Tfus | 199.07 | K | Relay (1.0) Calculated Property |
| Vc | 0.452 | m3/kmol | Relay (1.0) Calculated Property |
Cheméo can also estimate Standard Gibbs free energy of formation for this compound, but it falls outside the models' validated range, so it is not shown here. Open the prediction tool to compute it on demand.
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| n0 | 1.42900 | 298.15 | Isobaric (vapour-liquid) equilibria data for the binary system of glycidyl butyrate (1) and epichlorohydrin (2) at 100 kPa,88.66 kPa,56 kPa |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [164.23; 387.83] | 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 | -1.09870e+01 | |||
| Coefficient B | 7.61920e-01 | |||
| Coefficient C | -4.68700e-04 | |||
| Coefficient D | 1.05600e-07 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 164.23 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 204.58 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 240.27 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 271.64 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 299.02 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 322.75 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 343.16 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 360.59 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 375.37 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 387.83 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0029565; 0.0004905] | Pa×s | [255.49; 447.29] |
Joback Predicted correlation
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K | |||
| Coefficient A | -1.00130e+01 | |||
| Coefficient B | 1.07031e+03 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 255.49 | |||
| Temperature range, max. | 447.29 | |||
| η | 0.0029565 | Pa×s | 255.49 | Calculated Property |
| η | 0.0021414 | Pa×s | 276.80 | Calculated Property |
| η | 0.0016242 | Pa×s | 298.11 | Calculated Property |
| η | 0.0012782 | Pa×s | 319.42 | Calculated Property |
| η | 0.0010366 | Pa×s | 340.74 | Calculated Property |
| η | 0.0008616 | Pa×s | 362.05 | Calculated Property |
| η | 0.0007310 | Pa×s | 383.36 | Calculated Property |
| η | 0.0006311 | Pa×s | 404.67 | Calculated Property |
| η | 0.0005528 | Pa×s | 425.98 | Calculated Property |
| η | 0.0004905 | Pa×s | 447.29 | Calculated Property |
Similar Compounds
Find more compounds similar to Glycidyl butyrate.
Sources
- Cheméo Relay (1.0)
- Crippen Method
- Crippen Method
- Isobaric (vapour-liquid) equilibria data for the binary system of glycidyl butyrate (1) and epichlorohydrin (2) at 100 kPa,88.66 kPa,56 kPa
- Joback Method
- McGowan Method
- NIST Webbook
Note: Cheméo is only indexing the data, follow the source links to retrieve the latest data. The source is also providing more information like the publication year, authors and more.
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