- InChI
- InChI=1S/C8H11NO/c1-2-10-8-6-4-3-5-7(8)9/h3-6H,2,9H2,1H3
- InChI Key
- ULHFFAFDSSHFDA-UHFFFAOYSA-N
- Formula
- C8H11NO
- SMILES
- CCOc1ccccc1N
- Molecular Weight1
- 137.18
- CAS
- 94-70-2
- Other Names
-
- 2-AMINOPHENETOLE
- 2-ETHOXYBENZENAMINE
- 2-Ethoxyaniline
- 2-Phenetidine
- O-ETHOXYANILINE
- UN 2311
- o-Aminophenetole
- o-Phenetidine
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- 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).
- 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.
- 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 |
|---|---|---|---|
| ΔfG° | 80.71 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -81.82 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 16.51 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 49.39 | kJ/mol | Joback Calculated Property |
| log10WS | -1.64 | Crippen Calculated Property | |
| logPoct/wat | 1.667 | Crippen Calculated Property | |
| McVol | 115.670 | ml/mol | McGowan Calculated Property |
| Pc | 3763.78 | kPa | Joback Calculated Property |
| Inp | 1206.80 | NIST | |
| Tboil | [505.65; 505.70] | K |
|
| Tboil | 505.70 | K | NIST |
| Tboil | 505.65 ± 0.50 | K | NIST |
| Tc | 730.98 | K | Joback Calculated Property |
| Tfus | 324.35 | K | Joback Calculated Property |
| Vc | 0.422 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [251.29; 315.60] | J/mol×K | [509.05; 730.98] |
|
| Cp,gas | 251.29 | J/mol×K | 509.05 | Joback Calculated Property |
| Cp,gas | 263.62 | J/mol×K | 546.04 | Joback Calculated Property |
| Cp,gas | 275.28 | J/mol×K | 583.03 | Joback Calculated Property |
| Cp,gas | 286.30 | J/mol×K | 620.01 | Joback Calculated Property |
| Cp,gas | 296.69 | J/mol×K | 657.00 | Joback Calculated Property |
| Cp,gas | 306.45 | J/mol×K | 693.99 | Joback Calculated Property |
| Cp,gas | 315.60 | J/mol×K | 730.98 | Joback Calculated Property |
| ΔvapH | 57.30 | kJ/mol | 415.50 | NIST |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | 400.70 | K | 1.90 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.67] | kPa | [381.40; 533.92] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.73221e+01 | |||
| Coefficient B | -6.21092e+03 | |||
| Coefficient C | -1.67940e+01 | |||
| Temperature range, min. | 381.40 | |||
| Temperature range, max. | 533.92 | |||
| Pvap | 1.33 | kPa | 381.40 | Calculated Property |
| Pvap | 2.84 | kPa | 398.35 | Calculated Property |
| Pvap | 5.68 | kPa | 415.29 | Calculated Property |
| Pvap | 10.72 | kPa | 432.24 | Calculated Property |
| Pvap | 19.26 | kPa | 449.19 | Calculated Property |
| Pvap | 33.11 | kPa | 466.13 | Calculated Property |
| Pvap | 54.71 | kPa | 483.08 | Calculated Property |
| Pvap | 87.29 | kPa | 500.03 | Calculated Property |
| Pvap | 134.92 | kPa | 516.97 | Calculated Property |
| Pvap | 202.67 | kPa | 533.92 | Calculated Property |
| Pvap | [0.90; 27.55] | kPa | [373.15; 458.15] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 2.12495e+01 | |||
| Coefficient B | -7.03241e+03 | |||
| Coefficient C | -4.28858e-01 | |||
| Coefficient D | 2.09166e-07 | |||
| Temperature range, min. | 373.15 | |||
| Temperature range, max. | 458.15 | |||
| Pvap | 0.90 | kPa | 373.15 | Calculated Property |
| Pvap | 1.42 | kPa | 382.59 | Calculated Property |
| Pvap | 2.19 | kPa | 392.04 | Calculated Property |
| Pvap | 3.31 | kPa | 401.48 | Calculated Property |
| Pvap | 4.90 | kPa | 410.93 | Calculated Property |
| Pvap | 7.15 | kPa | 420.37 | Calculated Property |
| Pvap | 10.24 | kPa | 429.82 | Calculated Property |
| Pvap | 14.45 | kPa | 439.26 | Calculated Property |
| Pvap | 20.09 | kPa | 448.71 | Calculated Property |
| Pvap | 27.55 | kPa | 458.15 | Calculated Property |
Similar Compounds
Find more compounds similar to Benzenamine, 2-ethoxy-.
Sources
- KDB Vapor Pressure Data
- Crippen Method
- Crippen Method
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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