- InChI
- InChI=1S/C9H12O/c1-2-10-8-9-6-4-3-5-7-9/h3-7H,2,8H2,1H3
- InChI Key
- AXPZDYVDTMMLNB-UHFFFAOYSA-N
- Formula
- C9H12O
- SMILES
- CCOCc1ccccc1
- Molecular Weight1
- 136.19
- CAS
- 539-30-0
- Other Names
-
- (ethoxymethyl)benzene
- Benzyl ethyl ether
- Benzyl ethyl oxide
- Ether, benzyl ethyl
- Ethyl benzyl ether
- ω : Acentric Factor.
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- η : Dynamic viscosity (Pa×s).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- ΔfH°gas : 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).
- Pvap : Vapor pressure (kPa).
- Inp : Non-polar retention indices.
- I : Polar retention indices.
- Tboil : Normal Boiling Point Temperature (K).
- Tboilr : Boiling point at reduced pressure (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 | 0.3986 | Relay (1.0) Calculated Property | |
| ΔfG° | 32.31 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -114.72 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfusH° | 14.29 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 53.50 ± 0.40 | kJ/mol | NIST |
| IE | 8.42 | eV | NIST |
| log10WS | -1.60 | Relay (1.0) Calculated Property | |
| logPoct/wat | 2.223 | Crippen Calculated Property | |
| McVol | 119.780 | ml/mol | McGowan Calculated Property |
| Pc | 3199.16 | kPa | Joback Calculated Property |
| Inp | [1039.50; 1047.90] |
|
|
| Inp | 1047.90 | NIST | |
| Inp | 1039.50 | NIST | |
| Inp | 1046.00 | NIST | |
| I | [1421.00; 1439.00] |
|
|
| I | 1421.00 | NIST | |
| I | 1424.00 | NIST | |
| I | 1421.00 | NIST | |
| I | 1421.00 | NIST | |
| I | 1428.00 | NIST | |
| I | 1439.00 | NIST | |
| I | 1438.00 | NIST | |
| I | 1439.00 | NIST | |
| I | 1421.00 | NIST | |
| Tboil | [458.20; 462.00] | K |
|
| Tboil | 458.20 | K | NIST |
| Tboil | 462.00 | K | NIST |
| Tboil | 458.20 ± 0.60 | K | NIST |
| Tboil | 458.35 ± 0.40 | K | NIST |
| Tc | 658.03 | K | Relay (1.0) Calculated Property |
| Tfus | 207.03 | K | Relay (1.0) Calculated Property |
| Vc | 0.435 | m3/kmol | Relay (1.0) Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | 48.00 | kJ/mol | 379.50 | NIST |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | 351.00 | K | 2.40 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [154.55; 383.62] | 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 | -1.36980e+01 | |||
| Coefficient B | 7.16720e-01 | |||
| Coefficient C | -3.86000e-04 | |||
| Coefficient D | 6.66000e-08 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 154.55 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 194.50 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 230.33 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 262.26 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 290.49 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 315.24 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 336.72 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 355.13 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 370.70 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 383.62 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0027046; 0.0001939] | Pa×s | [239.84; 462.36] |
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 | -1.13889e+01 | |||
| Coefficient B | 1.31339e+03 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Comment | Liquid phase. Joback/Reid (1987), valid from Tf to 0.7·Tc. | |||
| Temperature range, min. | 239.84 | |||
| Temperature range, max. | 462.36 | |||
| η | 0.0027046 | Pa×s | 239.84 | Calculated Property |
| η | 0.0016212 | Pa×s | 264.56 | Calculated Property |
| η | 0.0010607 | Pa×s | 289.29 | Calculated Property |
| η | 0.0007419 | Pa×s | 314.01 | Calculated Property |
| η | 0.0005467 | Pa×s | 338.74 | Calculated Property |
| η | 0.0004200 | Pa×s | 363.46 | Calculated Property |
| η | 0.0003336 | Pa×s | 388.19 | Calculated Property |
| η | 0.0002724 | Pa×s | 412.91 | Calculated Property |
| η | 0.0002276 | Pa×s | 437.63 | Calculated Property |
| η | 0.0001939 | Pa×s | 462.36 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.66] | kPa | [336.28; 487.70] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.50689e+01 | |||
| Coefficient B | -4.34681e+03 | |||
| Coefficient C | -4.22100e+01 | |||
| Temperature range, min. | 336.28 | |||
| Temperature range, max. | 487.70 | |||
| Pvap | 1.33 | kPa | 336.28 | Calculated Property |
| Pvap | 2.97 | kPa | 353.10 | Calculated Property |
| Pvap | 6.08 | kPa | 369.93 | Calculated Property |
| Pvap | 11.62 | kPa | 386.75 | Calculated Property |
| Pvap | 20.91 | kPa | 403.58 | Calculated Property |
| Pvap | 35.70 | kPa | 420.40 | Calculated Property |
| Pvap | 58.25 | kPa | 437.23 | Calculated Property |
| Pvap | 91.32 | kPa | 454.05 | Calculated Property |
| Pvap | 138.18 | kPa | 470.88 | Calculated Property |
| Pvap | 202.66 | kPa | 487.70 | Calculated Property |
| Pvap | [0.02; 3121.33] | kPa | [275.65; 662.00] |
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 | 5.98020e+01 | |||
| Coefficient B | -7.77928e+03 | |||
| Coefficient C | -6.31706e+00 | |||
| Coefficient D | 2.34148e-06 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 275.65 | |||
| Temperature range, max. | 662.00 | |||
| Pvap | 0.02 | kPa | 275.65 | Calculated Property |
| Pvap | 0.45 | kPa | 318.58 | Calculated Property |
| Pvap | 3.97 | kPa | 361.51 | Calculated Property |
| Pvap | 20.74 | kPa | 404.43 | Calculated Property |
| Pvap | 75.64 | kPa | 447.36 | Calculated Property |
| Pvap | 213.58 | kPa | 490.29 | Calculated Property |
| Pvap | 499.73 | kPa | 533.22 | Calculated Property |
| Pvap | 1015.83 | kPa | 576.14 | Calculated Property |
| Pvap | 1855.51 | kPa | 619.07 | Calculated Property |
| Pvap | 3121.33 | kPa | 662.00 | Calculated Property |
| Pvap | [0.13; 100.38] | kPa | [299.00; 458.00] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.53589e+01 | |||
| Coefficient B | -4.48367e+03 | |||
| Coefficient C | -4.09100e+01 | |||
| Reference | Stull, 1947 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 299.00 | |||
| Temperature range, max. | 458.00 | |||
| Pvap | 0.13 | kPa | 299.00 | Calculated Property |
| Pvap | 0.41 | kPa | 316.67 | Calculated Property |
| Pvap | 1.08 | kPa | 334.33 | Calculated Property |
| Pvap | 2.58 | kPa | 352.00 | Calculated Property |
| Pvap | 5.59 | kPa | 369.67 | Calculated Property |
| Pvap | 11.20 | kPa | 387.33 | Calculated Property |
| Pvap | 20.99 | kPa | 405.00 | Calculated Property |
| Pvap | 37.12 | kPa | 422.67 | Calculated Property |
| Pvap | 62.40 | kPa | 440.33 | Calculated Property |
| Pvap | 100.38 | kPa | 458.00 | Calculated Property |
Similar Compounds
![Benzene, 1,1'-[1,2-ethanediylbis(oxymethylene)]bis-.](data:image/png;base64,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)
Find more compounds similar to Benzene, (ethoxymethyl)-.
Sources
- KDB Vapor Pressure Data
- Cheméo Relay (1.0)
- Crippen Method
- Crippen Method
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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