- InChI
- InChI=1S/C8H11NO/c1-2-10-8-5-3-7(9)4-6-8/h3-6H,2,9H2,1H3
- InChI Key
- IMPPGHMHELILKG-UHFFFAOYSA-N
- Formula
- C8H11NO
- SMILES
- CCOc1ccc(N)cc1
- Molecular Weight1
- 137.18
- CAS
- 156-43-4
- Other Names
-
- 1-Amino-4-ethoxybenzene
- 4-Aminoethoxybenzene
- 4-Aminophenetole
- 4-ETHOXYBENZENAMINE
- 4-Ethoxyaniline
- 4-Ethoxybenzeneamine
- 4-Phenetidine
- Aniline, p-ethoxy-
- NSC 3116
- P-AMINOPHENETOLE
- P-ETHOXYANILINE
- Para-aminoethoxybenzene
- Phenethidine
- Phenetidine
- p-Aminofenetol
- p-Fenetidin
- p-Phenetidin
- p-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).
- 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.
- 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 |
|---|---|---|---|
| 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 |
| IE | [7.40; 7.67] | eV |
|
| IE | 7.67 ± 0.15 | eV | NIST |
| IE | 7.40 ± 0.10 | eV | NIST |
| 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 | [1253.50; 1277.00] |
|
|
| Inp | 1277.00 | NIST | |
| Inp | 1277.00 | NIST | |
| Inp | 1253.50 | NIST | |
| Inp | 1277.00 | NIST | |
| Tboil | [523.20; 527.20] | K |
|
| Tboil | 523.20 | K | NIST |
| Tboil | 527.20 | K | NIST |
| Tc | 730.98 | K | Joback Calculated Property |
| Tfus | 278.00 ± 0.02 | K | NIST |
| 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 | 61.20 | kJ/mol | 472.00 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.64] | kPa | [397.71; 555.61] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.55338e+01 | |||
| Coefficient B | -4.89850e+03 | |||
| Coefficient C | -7.64150e+01 | |||
| Temperature range, min. | 397.71 | |||
| Temperature range, max. | 555.61 | |||
| Pvap | 1.33 | kPa | 397.71 | Calculated Property |
| Pvap | 2.94 | kPa | 415.25 | Calculated Property |
| Pvap | 5.98 | kPa | 432.80 | Calculated Property |
| Pvap | 11.40 | kPa | 450.34 | Calculated Property |
| Pvap | 20.51 | kPa | 467.89 | Calculated Property |
| Pvap | 35.08 | kPa | 485.43 | Calculated Property |
| Pvap | 57.40 | kPa | 502.98 | Calculated Property |
| Pvap | 90.36 | kPa | 520.52 | Calculated Property |
| Pvap | 137.41 | kPa | 538.07 | Calculated Property |
| Pvap | 202.64 | kPa | 555.61 | Calculated Property |
| Pvap | [1.47e-04; 3367.86] | kPa | [277.00; 754.00] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 1.03358e+02 | |||
| Coefficient B | -1.20839e+04 | |||
| Coefficient C | -1.22350e+01 | |||
| Coefficient D | 3.25762e-06 | |||
| Temperature range, min. | 277.00 | |||
| Temperature range, max. | 754.00 | |||
| Pvap | 1.47e-04 | kPa | 277.00 | Calculated Property |
| Pvap | 0.02 | kPa | 330.00 | Calculated Property |
| Pvap | 0.61 | kPa | 383.00 | Calculated Property |
| Pvap | 6.70 | kPa | 436.00 | Calculated Property |
| Pvap | 38.94 | kPa | 489.00 | Calculated Property |
| Pvap | 148.04 | kPa | 542.00 | Calculated Property |
| Pvap | 419.16 | kPa | 595.00 | Calculated Property |
| Pvap | 962.88 | kPa | 648.00 | Calculated Property |
| Pvap | 1902.39 | kPa | 701.00 | Calculated Property |
| Pvap | 3367.86 | kPa | 754.00 | Calculated Property |
Similar Compounds
Find more compounds similar to Benzenamine, 4-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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