- InChI
- InChI=1S/C8H8O2/c1-7(9)10-8-5-3-2-4-6-8/h2-6H,1H3
- InChI Key
- IPBVNPXQWQGGJP-UHFFFAOYSA-N
- Formula
- C8H8O2
- SMILES
- CC(=O)Oc1ccccc1
- Molecular Weight1
- 136.15
- CAS
- 122-79-2
- Other Names
-
- Acetic acid phenyl ester
- Fenylester kyseliny octove
- Phenol acetate
- Phenyl ester of acetic acid
- phenyl acetate
- phenyl ethanoate
- ω : Acentric Factor.
- ΔcH°liquid : Standard liquid enthalpy of combustion (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,liquid : Liquid phase heat capacity (J/mol×K).
- μ : Dipole Moment (debye).
- η : Dynamic viscosity (Pa×s).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- 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).
- ΔvapH : Enthalpy of vaporization at a given temperature (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).
- Ptriple : Triple Point Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- Ip : Polar retention indices.
- γ : Surface Tension (N/m).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- λgas : Gas thermal conductivity (W/m×K).
- λliquid : Liquid thermal conductivity (W/m×K).
- Tfus : Normal melting (fusion) point (K).
- Ttriple : Triple Point Temperature (K).
- UQi : UNIQUAC Qi Parameter.
- URi : UNIQUAC Ri Parameter.
- Vc : Critical Volume (m3/kmol).
- Zc : Critical Compressibility.
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | [0.4160; 0.4335] |
|
|
| ω | 0.4335 | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value | |
| ω | 0.4160 | ChemSep v8.3 pure component data Compiled value | |
| ΔcH°liquid | -3966.00 ± 0.84 | kJ/mol | NIST |
| μ | 1.72 | debye | ChemSep v8.3 pure component data Compiled value |
| ΔfG° | -177.30 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°gas | [-280.00; -279.70] | kJ/mol |
|
| ΔfH°gas | -279.70 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°gas | -279.70 ± 1.20 | kJ/mol | NIST |
| ΔfH°gas | -280.00 ± 2.00 | kJ/mol | NIST |
| ΔfH°liquid | [-334.80; -326.00] | kJ/mol |
|
| ΔfH°liquid | -326.00 ± 0.80 | kJ/mol | NIST |
| ΔfH°liquid | -334.80 ± 0.92 | kJ/mol | NIST |
| ΔfusH° | 14.89 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [46.30; 55.20] | kJ/mol |
|
| ΔvapH° | 53.30 | kJ/mol | NIST |
| ΔvapH° | 53.60 | kJ/mol | NIST |
| ΔvapH° | 53.10 | kJ/mol | NIST |
| ΔvapH° | 55.20 ± 0.80 | kJ/mol | NIST |
| ΔvapH° | Outlier 46.30 | kJ/mol | NIST |
| ΔvapH° | 54.00 ± 2.00 | kJ/mol | NIST |
| ΔvapH° | 54.80 | kJ/mol | NIST |
| IE | [8.60; 8.80] | eV |
|
| IE | 8.60 ± 0.05 | eV | NIST |
| IE | 8.80 ± 0.20 | eV | NIST |
| IE | 8.75 ± 0.03 | eV | NIST |
| log10WS | -1.63 | Relay (1.0) Calculated Property | |
| logPoct/wat | 1.612 | Crippen Calculated Property | |
| McVol | 107.260 | ml/mol | McGowan Calculated Property |
| Pc | [3587.00; 3590.00] | kPa |
|
| Pc | 3590.00 | kPa | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Pc | 3587.00 | kPa | ChemSep v8.3 pure component data Compiled value |
| Ptriple | 3.01e-04 | kPa | ChemSep v8.3 pure component data Compiled value |
| Inp | [1008.00; 1068.00] |
|
|
| Inp | 1008.00 | NIST | |
| Inp | 1025.00 | NIST | |
| Inp | 1008.00 | NIST | |
| Inp | 1025.00 | NIST | |
| Inp | 1033.00 | NIST | |
| Inp | 1033.00 | NIST | |
| Inp | 1068.00 | NIST | |
| Inp | 1050.00 | NIST | |
| Inp | 1065.00 | NIST | |
| Inp | 1068.00 | NIST | |
| Inp | 1033.00 | NIST | |
| Ip | [1633.00; 1660.00] |
|
|
| Ip | 1633.00 | NIST | |
| Ip | 1660.00 | NIST | |
| Tboil | [468.00; 469.90] | K |
|
| Tboil | 468.85 | K | ChemSep v8.3 pure component data Compiled value |
| Tboil | 469.20 | K | NIST |
| Tboil | Outlier 468.00 | K | NIST |
| Tboil | 468.85 | K | NIST |
| Tboil | 468.85 ± 0.40 | K | NIST |
| Tboil | 468.90 ± 0.50 | K | NIST |
| Tboil | 468.90 ± 0.50 | K | NIST |
| Tboil | 468.70 ± 0.50 | K | NIST |
| Tboil | 469.00 ± 4.00 | K | NIST |
| Tboil | Outlier 469.90 ± 1.00 | K | NIST |
| Tc | [685.70; 687.10] | K |
|
| Tc | 685.70 | K | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Tc | 687.10 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | [243.15; 267.05] | K |
|
| Tfus | 266.00 | K | Melting Point, Enthalpy of Fusion, and Heat Capacity Measurements of Several Polyfunctional, Industrially Important Compounds by Differential Scanning Calorimetry |
| Tfus | 243.15 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Tfus | 251.30 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | 267.05 | K | NIST |
| Ttriple | 251.30 | K | ChemSep v8.3 pure component data Compiled value |
| UQi | 3.85 | ChemSep v8.3 pure component data Compiled value | |
| URi | 4.92 | ChemSep v8.3 pure component data Compiled value | |
| Vc | [0.397; 0.406] | m3/kmol |
|
| Vc | 0.397 | m3/kmol | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Vc | 0.406 | m3/kmol | ChemSep v8.3 pure component data Compiled value |
| Zc | 0.2550000 | ChemSep v8.3 pure component data Compiled value |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | 51.70 | kJ/mol | 390.00 | NIST |
| Pvap | [3.50; 66.10] | kPa | [373.20; 453.20] |
|
| Pvap | 3.50 | kPa | 373.20 | Isothermal (vapour + liquid) equilibrium (VLE) for binary mixtures containing diethyl carbonate, phenyl acetate, diphenyl carbonate, or ethyl acetate |
| Pvap | 18.20 | kPa | 413.20 | Isothermal (vapour + liquid) equilibrium (VLE) for binary mixtures containing diethyl carbonate, phenyl acetate, diphenyl carbonate, or ethyl acetate |
| Pvap | 66.10 | kPa | 453.20 | Isothermal (vapour + liquid) equilibrium (VLE) for binary mixtures containing diethyl carbonate, phenyl acetate, diphenyl carbonate, or ethyl acetate |
| ρl | [1073.00; 1073.30] | kg/m3 | [298.15; 298.20] |
|
| ρl | 1073.30 | kg/m3 | 298.15 | Revision of the volumetric method for measurements of liquid liquid equilibria in binary systems |
| ρl | 1073.00 | kg/m3 | 298.20 | Investigation of Ternary Phase Diagrams of (Water + Butyric Acid + Phenyl Acetate) at Different Temperatures |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [132.19; 368.79] | J/mol×K | [255.00; 1500.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,gas in J/mol×K, T in K | |||
| Coefficient A | 7.43501e+01 | |||
| Coefficient B | -5.00000e+02 | |||
| Coefficient C | 6.01842e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 255.00 | |||
| Temperature range, max. | 1500.00 | |||
| Cp,gas | 132.19 | J/mol×K | 255.00 | Calculated Property |
| Cp,gas | 189.62 | J/mol×K | 393.33 | Calculated Property |
| Cp,gas | 234.80 | J/mol×K | 531.67 | Calculated Property |
| Cp,gas | 269.19 | J/mol×K | 670.00 | Calculated Property |
| Cp,gas | 295.73 | J/mol×K | 808.33 | Calculated Property |
| Cp,gas | 316.67 | J/mol×K | 946.67 | Calculated Property |
| Cp,gas | 333.55 | J/mol×K | 1085.00 | Calculated Property |
| Cp,gas | 347.41 | J/mol×K | 1223.33 | Calculated Property |
| Cp,gas | 358.99 | J/mol×K | 1361.67 | Calculated Property |
| Cp,gas | 368.79 | J/mol×K | 1500.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | [219.98; 332.80] | J/mol×K | [251.30; 687.10] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,liquid in J/mol×K, T in K | |||
| Coefficient A | 1.82030e+02 | |||
| Coefficient B | 1.11570e-01 | |||
| Coefficient C | 1.56980e-04 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 251.30 | |||
| Temperature range, max. | 687.10 | |||
| Cp,liquid | 219.98 | J/mol×K | 251.30 | Calculated Property |
| Cp,liquid | 229.57 | J/mol×K | 299.72 | Calculated Property |
| Cp,liquid | 239.90 | J/mol×K | 348.14 | Calculated Property |
| Cp,liquid | 250.96 | J/mol×K | 396.57 | Calculated Property |
| Cp,liquid | 262.76 | J/mol×K | 444.99 | Calculated Property |
| Cp,liquid | 275.30 | J/mol×K | 493.41 | Calculated Property |
| Cp,liquid | 288.57 | J/mol×K | 541.83 | Calculated Property |
| Cp,liquid | 302.58 | J/mol×K | 590.26 | Calculated Property |
| Cp,liquid | 317.32 | J/mol×K | 638.68 | Calculated Property |
| Cp,liquid | 332.80 | J/mol×K | 687.10 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0061705; 0.0004506] | Pa×s | [251.30; 468.85] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K | |||
| Coefficient A | -1.67860e+01 | |||
| Coefficient B | 1.71510e+03 | |||
| Coefficient C | 8.81750e-01 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 251.30 | |||
| Temperature range, max. | 468.85 | |||
| η | 0.0061705 | Pa×s | 251.30 | Calculated Property |
| η | 0.0036762 | Pa×s | 275.47 | Calculated Property |
| η | 0.0023960 | Pa×s | 299.64 | Calculated Property |
| η | 0.0016735 | Pa×s | 323.82 | Calculated Property |
| η | 0.0012343 | Pa×s | 347.99 | Calculated Property |
| η | 0.0009509 | Pa×s | 372.16 | Calculated Property |
| η | 0.0007588 | Pa×s | 396.33 | Calculated Property |
| η | 0.0006234 | Pa×s | 420.51 | Calculated Property |
| η | 0.0005247 | Pa×s | 444.68 | Calculated Property |
| η | 0.0004506 | Pa×s | 468.85 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [63.79; 0.00] | kJ/mol | [251.30; 687.10] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A·(1 − Tr)^(B + C·Tr + D·Tr² + E·Tr³), Tr = T/Tc Y is ΔvapH in kJ/mol, T in K | |||
| Coefficient A | 7.71980e+01 | |||
| Coefficient B | 3.11090e-01 | |||
| Coefficient C | 3.91890e-01 | |||
| Coefficient D | -2.65060e-01 | |||
| Coefficient E | 0.00000e+00 | |||
| Critical temperature, Tc (K) | 6.87100e+02 | |||
| Temperature range, min. | 251.30 | |||
| Temperature range, max. | 687.10 | |||
| ΔvapH | 63.79 | kJ/mol | 251.30 | Calculated Property |
| ΔvapH | 60.28 | kJ/mol | 299.72 | Calculated Property |
| ΔvapH | 56.51 | kJ/mol | 348.14 | Calculated Property |
| ΔvapH | 52.45 | kJ/mol | 396.57 | Calculated Property |
| ΔvapH | 48.09 | kJ/mol | 444.99 | Calculated Property |
| ΔvapH | 43.35 | kJ/mol | 493.41 | Calculated Property |
| ΔvapH | 38.05 | kJ/mol | 541.83 | Calculated Property |
| ΔvapH | 31.83 | kJ/mol | 590.26 | Calculated Property |
| ΔvapH | 23.63 | kJ/mol | 638.68 | Calculated Property |
| ΔvapH | 0.00 | kJ/mol | 687.10 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.64] | kPa | [350.99; 496.64] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.63860e+01 | |||
| Coefficient B | -5.16870e+03 | |||
| Coefficient C | -2.99210e+01 | |||
| Temperature range, min. | 350.99 | |||
| Temperature range, max. | 496.64 | |||
| Pvap | 1.33 | kPa | 350.99 | Calculated Property |
| Pvap | 2.89 | kPa | 367.17 | Calculated Property |
| Pvap | 5.82 | kPa | 383.36 | Calculated Property |
| Pvap | 11.05 | kPa | 399.54 | Calculated Property |
| Pvap | 19.86 | kPa | 415.72 | Calculated Property |
| Pvap | 34.06 | kPa | 431.91 | Calculated Property |
| Pvap | 56.02 | kPa | 448.09 | Calculated Property |
| Pvap | 88.78 | kPa | 464.27 | Calculated Property |
| Pvap | 136.14 | kPa | 480.46 | Calculated Property |
| Pvap | 202.64 | kPa | 496.64 | Calculated Property |
| Pvap | [3.01e-04; 3589.35] | kPa | [251.30; 687.10] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is Pvap in kPa, T in K | |||
| Coefficient A | 8.43882e+01 | |||
| Coefficient B | -1.00740e+04 | |||
| Coefficient C | -9.48310e+00 | |||
| Coefficient D | 3.87040e-18 | |||
| Coefficient E | 6.00000e+00 | |||
| Temperature range, min. | 251.30 | |||
| Temperature range, max. | 687.10 | |||
| Pvap | 3.01e-04 | kPa | 251.30 | Calculated Property |
| Pvap | 0.04 | kPa | 299.72 | Calculated Property |
| Pvap | 0.96 | kPa | 348.14 | Calculated Property |
| Pvap | 9.62 | kPa | 396.57 | Calculated Property |
| Pvap | 51.99 | kPa | 444.99 | Calculated Property |
| Pvap | 184.77 | kPa | 493.41 | Calculated Property |
| Pvap | 491.78 | kPa | 541.83 | Calculated Property |
| Pvap | 1072.01 | kPa | 590.26 | Calculated Property |
| Pvap | 2043.84 | kPa | 638.68 | Calculated Property |
| Pvap | 3589.35 | kPa | 687.10 | Calculated Property |
| Pvap | [0.13; 100.95] | kPa | [311.40; 469.10] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.61776e+01 | |||
| Coefficient B | -5.00743e+03 | |||
| Coefficient C | -3.60450e+01 | |||
| Reference | Stull, 1947 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 311.40 | |||
| Temperature range, max. | 469.10 | |||
| Pvap | 0.13 | kPa | 311.40 | Calculated Property |
| Pvap | 0.40 | kPa | 328.92 | Calculated Property |
| Pvap | 1.05 | kPa | 346.44 | Calculated Property |
| Pvap | 2.48 | kPa | 363.97 | Calculated Property |
| Pvap | 5.38 | kPa | 381.49 | Calculated Property |
| Pvap | 10.82 | kPa | 399.01 | Calculated Property |
| Pvap | 20.43 | kPa | 416.53 | Calculated Property |
| Pvap | 36.47 | kPa | 434.06 | Calculated Property |
| Pvap | 61.99 | kPa | 451.58 | Calculated Property |
| Pvap | 100.95 | kPa | 469.10 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ρl | [1112.80; 335.23] | kg/m3 | [251.30; 687.10] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A / B^(1 + (1 − T/C)^D) Y is ρl in kg/m3, T in K | |||
| Coefficient A | 8.54846e+01 | |||
| Coefficient B | 2.55000e-01 | |||
| Coefficient C | 6.87100e+02 | |||
| Coefficient D | 2.85710e-01 | |||
| Temperature range, min. | 251.30 | |||
| Temperature range, max. | 687.10 | |||
| ρl | 1112.80 | kg/m3 | 251.30 | Calculated Property |
| ρl | 1069.49 | kg/m3 | 299.72 | Calculated Property |
| ρl | 1024.04 | kg/m3 | 348.14 | Calculated Property |
| ρl | 975.93 | kg/m3 | 396.57 | Calculated Property |
| ρl | 924.41 | kg/m3 | 444.99 | Calculated Property |
| ρl | 868.27 | kg/m3 | 493.41 | Calculated Property |
| ρl | 805.46 | kg/m3 | 541.83 | Calculated Property |
| ρl | 731.81 | kg/m3 | 590.26 | Calculated Property |
| ρl | 636.04 | kg/m3 | 638.68 | Calculated Property |
| ρl | 335.23 | kg/m3 | 687.10 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| γ | [0.04; 0.00] | N/m | [251.30; 687.10] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A·(1 − Tr)^(B + C·Tr + D·Tr² + E·Tr³), Tr = T/Tc Y is γ in N/m, T in K | |||
| Coefficient A | 7.87310e-02 | |||
| Coefficient B | 1.61980e+00 | |||
| Coefficient C | -3.94050e-01 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Critical temperature, Tc (K) | 6.87100e+02 | |||
| Temperature range, min. | 251.30 | |||
| Temperature range, max. | 687.10 | |||
| γ | 0.04 | N/m | 251.30 | Calculated Property |
| γ | 0.03 | N/m | 299.72 | Calculated Property |
| γ | 0.03 | N/m | 348.14 | Calculated Property |
| γ | 0.02 | N/m | 396.57 | Calculated Property |
| γ | 0.02 | N/m | 444.99 | Calculated Property |
| γ | 0.01 | N/m | 493.41 | Calculated Property |
| γ | 0.01 | N/m | 541.83 | Calculated Property |
| γ | 0.01 | N/m | 590.26 | Calculated Property |
| γ | 0.00 | N/m | 638.68 | Calculated Property |
| γ | 0.00 | N/m | 687.10 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λgas | [0.02; 0.06] | W/m×K | [468.85; 1000.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A·T^B / (1 + C/T + D/T²) Y is λgas in W/m×K, T in K | |||
| Coefficient A | 2.64470e-06 | |||
| Coefficient B | 1.44500e+00 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Temperature range, min. | 468.85 | |||
| Temperature range, max. | 1000.00 | |||
| λgas | 0.02 | W/m×K | 468.85 | Calculated Property |
| λgas | 0.02 | W/m×K | 527.87 | Calculated Property |
| λgas | 0.03 | W/m×K | 586.88 | Calculated Property |
| λgas | 0.03 | W/m×K | 645.90 | Calculated Property |
| λgas | 0.03 | W/m×K | 704.92 | Calculated Property |
| λgas | 0.04 | W/m×K | 763.93 | Calculated Property |
| λgas | 0.04 | W/m×K | 822.95 | Calculated Property |
| λgas | 0.05 | W/m×K | 881.97 | Calculated Property |
| λgas | 0.05 | W/m×K | 940.98 | Calculated Property |
| λgas | 0.06 | W/m×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λliquid | [0.14; 0.09] | W/m×K | [251.30; 468.85] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is λliquid in W/m×K, T in K | |||
| Coefficient A | 1.83710e-01 | |||
| Coefficient B | -1.90470e-04 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 251.30 | |||
| Temperature range, max. | 468.85 | |||
| λliquid | 0.14 | W/m×K | 251.30 | Calculated Property |
| λliquid | 0.13 | W/m×K | 275.47 | Calculated Property |
| λliquid | 0.13 | W/m×K | 299.64 | Calculated Property |
| λliquid | 0.12 | W/m×K | 323.82 | Calculated Property |
| λliquid | 0.12 | W/m×K | 347.99 | Calculated Property |
| λliquid | 0.11 | W/m×K | 372.16 | Calculated Property |
| λliquid | 0.11 | W/m×K | 396.33 | Calculated Property |
| λliquid | 0.10 | W/m×K | 420.51 | Calculated Property |
| λliquid | 0.10 | W/m×K | 444.68 | Calculated Property |
| λliquid | 0.09 | W/m×K | 468.85 | Calculated Property |
Similar Compounds
Find more compounds similar to Acetic acid, phenyl ester.
Mixtures
- 1,2-Ethanediol + Acetic acid, phenyl ester
- Acetic acid, phenyl ester + Ethyl Acetate
- Diethyl carbonate + Acetic acid, phenyl ester
- Acetic acid, phenyl ester + Diphenyl carbonate
- Acetic acid, phenyl ester + Butanoic acid + Water
- Acetic acid, phenyl ester + Water
Sources
- 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).
- 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)
- ChemSep v8.3 pure component data Converted from ChemSep v8.3 pure component data, H. Kooijman and R. Taylor (2021, 2022), Artistic License 2.0; see how the values differ.
- Crippen Method
- Crippen Method
- Revision of the volumetric method for measurements of liquid liquid equilibria in binary systems
- Isothermal (vapour + liquid) equilibrium (VLE) for binary mixtures containing diethyl carbonate, phenyl acetate, diphenyl carbonate, or ethyl acetate
- Investigation of Ternary Phase Diagrams of (Water + Butyric Acid + Phenyl Acetate) at Different Temperatures
- Melting Point, Enthalpy of Fusion, and Heat Capacity Measurements of Several Polyfunctional, Industrially Important Compounds by Differential Scanning Calorimetry
- Joback Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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