- InChI
- InChI=1S/C12H11N/c1-3-7-11(8-4-1)13-12-9-5-2-6-10-12/h1-10,13H
- InChI Key
- DMBHHRLKUKUOEG-UHFFFAOYSA-N
- Formula
- C12H11N
- SMILES
- c1ccc(Nc2ccccc2)cc1
- Molecular Weight1
- 169.22
- CAS
- 122-39-4
- Other Names
-
- ANILINOBENZENE
- Aniline, N-phenyl-
- Benzenamine, N-phenyl-
- Benzene, (phenylamino)-
- Benzene, anilino-
- Big Dipper
- C.I. 10355
- DFA
- DPA
- Deccoscald 282
- Difenylamin
- N,N-Diphenylamine
- N-Fenylanilin
- N-PHENYL-BENZENAMINE
- N-Phenylaniline
- N-Phenylbenzenamine
- N-Phenylbenzeneamine
- NSC 215210
- Naugalube 428L
- No-Scald
- No-Scald dpa 283
- Phenylaniline
- Scaldip
- ΔcH°liquid : Standard liquid enthalpy of combustion (kJ/mol).
- 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).
- ΔfH°liquid : Liquid phase enthalpy of formation at standard conditions (kJ/mol).
- ΔfH°solid : Solid phase enthalpy of formation at standard conditions (kJ/mol).
- ΔfusH° : Enthalpy of fusion at standard conditions (kJ/mol).
- ΔfusH : Enthalpy of fusion at a given temperature (kJ/mol).
- ΔsubH° : Enthalpy of sublimation at standard conditions (kJ/mol).
- ΔsubH : Enthalpy of sublimation at a given temperature (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).
- NFPA Fire : NFPA Fire Rating.
- NFPA Health : NFPA Health Rating.
- Pc : Critical Pressure (kPa).
- Psub : Sublimation pressure (kPa).
- Pvap : Vapor pressure (kPa).
- Inp : Non-polar retention indices.
- I : 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 |
|---|---|---|---|
| ΔcH°liquid | -6426.20 | kJ/mol | NIST |
| ΔfG° | 364.37 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | 202.00 | kJ/mol | NIST |
| ΔfH°liquid | 132.00 | kJ/mol | NIST |
| ΔfH°solid | [109.00; 142.50] | kJ/mol |
|
| ΔfH°solid | 130.00 ± 1.50 | kJ/mol | NIST |
| ΔfH°solid | 142.50 | kJ/mol | NIST |
| ΔfH°solid | 117.40 ± 2.10 | kJ/mol | NIST |
| ΔfH°solid | 131.00 | kJ/mol | NIST |
| ΔfH°solid | 109.00 | kJ/mol | NIST |
| ΔfusH° | 19.68 | kJ/mol | Measure... |
| ΔsubH° | 110.00 | kJ/mol | NIST |
| ΔvapH° | [55.23; 70.00] | kJ/mol |
|
| ΔvapH° | 55.23 | kJ/mol | NIST |
| ΔvapH° | 69.90 | kJ/mol | NIST |
| ΔvapH° | 70.00 | kJ/mol | NIST |
| IE | [7.14; 7.44] | eV |
|
| IE | 7.19 ± 0.05 | eV | NIST |
| IE | 7.18 ± 0.01 | eV | NIST |
| IE | 7.14 ± 0.03 | eV | NIST |
| IE | 7.25 ± 0.03 | eV | NIST |
| IE | 7.44 | eV | NIST |
| log10WS | [-3.51; -3.50] |
|
|
| log10WS | -3.51 | Aq. Sol... | |
| log10WS | -3.50 | Estimat... | |
| logPoct/wat | 3.430 | Crippen Calculated Property | |
| McVol | 142.400 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 1 | KDB | |
| NFPA Health | 3 | KDB | |
| Pc | 8409.97 ± 405.30 | kPa | NIST |
| Inp | [274.57; 1637.00] |
|
|
| Inp | 1619.00 | NIST | |
| Inp | 1567.00 | NIST | |
| Inp | 1621.00 | NIST | |
| Inp | 1625.00 | NIST | |
| Inp | 1622.00 | NIST | |
| Inp | 1637.00 | NIST | |
| Inp | 1588.00 | NIST | |
| Inp | 1602.00 | NIST | |
| Inp | 1637.00 | NIST | |
| Inp | 1568.00 | NIST | |
| Inp | 1617.00 | NIST | |
| Inp | 1634.00 | NIST | |
| Inp | 1575.00 | NIST | |
| Inp | 1575.00 | NIST | |
| Inp | 1601.00 | NIST | |
| Inp | 274.57 | NIST | |
| Inp | 276.00 | NIST | |
| Inp | 279.32 | NIST | |
| Inp | 275.74 | NIST | |
| Inp | 279.27 | NIST | |
| I | [2517.00; 2521.00] |
|
|
| I | 2517.00 | NIST | |
| I | 2517.00 | NIST | |
| I | 2521.00 | NIST | |
| I | 2521.00 | NIST | |
| Tboil | [575.15; 582.15] | K |
|
| Tboil | 575.15 | K | KDB |
| Tboil | 575.20 | K | NIST |
| Tboil | 582.15 ± 2.00 | K | NIST |
| Tc | 931.15 ± 3.00 | K | NIST |
| Tfus | [325.60; 326.65] | K |
|
| Tfus | 325.85 | K | KDB |
| Tfus | 326.23 | K | Aq. Sol... |
| Tfus | 325.60 | K | Experim... |
| Tfus | 326.65 | K | DSC mea... |
| Vc | 0.526 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [326.77; 404.16] | J/mol×K | [577.49; 825.49] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 320 340 360 380 400 600 700 800 | ||||
| Cp,gas | 326.77 | J/mol×K | 577.49 | Joback Calculated Property |
| Cp,gas | 342.66 | J/mol×K | 618.82 | Joback Calculated Property |
| Cp,gas | 357.24 | J/mol×K | 660.16 | Joback Calculated Property |
| Cp,gas | 370.60 | J/mol×K | 701.49 | Joback Calculated Property |
| Cp,gas | 382.81 | J/mol×K | 742.83 | Joback Calculated Property |
| Cp,gas | 393.97 | J/mol×K | 784.16 | Joback Calculated Property |
| Cp,gas | 404.16 | J/mol×K | 825.49 | Joback Calculated Property |
| ΔfusH | [17.86; 19.90] | kJ/mol | [326.10; 326.20] |
|
| ΔfusH | 19.90 | kJ/mol | 326.10 | NIST |
| ΔfusH | 17.86 | kJ/mol | 326.20 | NIST |
| ΔfusH | 17.86 | kJ/mol | 326.20 | NIST |
| ΔsubH | [96.70; 110.00] | kJ/mol | [310.50; 311.00] |
|
| ΔsubH | 96.70 ± 2.50 | kJ/mol | 310.50 | NIST |
| ΔsubH | 110.00 ± 1.00 | kJ/mol | 311.00 | NIST |
| ΔvapH | [54.20; 64.10] | kJ/mol | [478.00; 623.00] |
|
| ΔvapH | 64.10 | kJ/mol | 478.00 | NIST |
| ΔvapH | 54.20 | kJ/mol | 623.00 | NIST |
| Psub | [4.00e-05; 2.03e-03] | kPa | [293.10; 326.70] |
|
|
T(K) Sublimation pressure (kPa) 0 5.00e-4 1.00e-3 1.50e-3 2.00e-3 300 310 320 | ||||
| Psub | 4.00e-05 | kPa | 293.10 | Thermoc... |
| Psub | 4.00e-05 | kPa | 293.70 | Thermoc... |
| Psub | 6.00e-05 | kPa | 296.20 | Thermoc... |
| Psub | 7.00e-05 | kPa | 298.20 | Thermoc... |
| Psub | 8.00e-05 | kPa | 298.40 | Thermoc... |
| Psub | 1.00e-04 | kPa | 300.20 | Thermoc... |
| Psub | 1.20e-04 | kPa | 301.00 | Thermoc... |
| Psub | 1.30e-04 | kPa | 302.10 | Thermoc... |
| Psub | 1.50e-04 | kPa | 302.70 | Thermoc... |
| Psub | 1.40e-04 | kPa | 303.20 | Thermoc... |
| Psub | 1.70e-04 | kPa | 305.20 | Thermoc... |
| Psub | 2.00e-04 | kPa | 305.50 | Thermoc... |
| Psub | 2.40e-04 | kPa | 308.00 | Thermoc... |
| Psub | 2.50e-04 | kPa | 308.00 | Thermoc... |
| Psub | 2.60e-04 | kPa | 308.20 | Thermoc... |
| Psub | 2.90e-04 | kPa | 309.10 | Thermoc... |
| Psub | 3.00e-04 | kPa | 309.30 | Thermoc... |
| Psub | 3.40e-04 | kPa | 310.70 | Thermoc... |
| Psub | 4.20e-04 | kPa | 312.30 | Thermoc... |
| Psub | 4.50e-04 | kPa | 313.00 | Thermoc... |
| Psub | 5.00e-04 | kPa | 313.70 | Thermoc... |
| Psub | 5.40e-04 | kPa | 315.00 | Thermoc... |
| Psub | 5.50e-04 | kPa | 315.00 | Thermoc... |
| Psub | 6.10e-04 | kPa | 315.40 | Thermoc... |
| Psub | 6.00e-04 | kPa | 315.70 | Thermoc... |
| Psub | 6.50e-04 | kPa | 316.00 | Thermoc... |
| Psub | 7.00e-04 | kPa | 316.70 | Thermoc... |
| Psub | 7.50e-04 | kPa | 317.20 | Thermoc... |
| Psub | 8.30e-04 | kPa | 318.00 | Thermoc... |
| Psub | 8.60e-04 | kPa | 318.20 | Thermoc... |
| Psub | 8.50e-04 | kPa | 318.30 | Thermoc... |
| Psub | 8.50e-04 | kPa | 318.70 | Thermoc... |
| Psub | 1.11e-03 | kPa | 320.30 | Thermoc... |
| Psub | 1.10e-03 | kPa | 320.70 | Thermoc... |
| Psub | 1.38e-03 | kPa | 322.30 | Thermoc... |
| Psub | 1.43e-03 | kPa | 323.20 | Thermoc... |
| Psub | 1.53e-03 | kPa | 323.20 | Thermoc... |
| Psub | 1.69e-03 | kPa | 324.10 | Thermoc... |
| Psub | 1.64e-03 | kPa | 324.70 | Thermoc... |
| Psub | 1.86e-03 | kPa | 325.20 | Thermoc... |
| Psub | 2.03e-03 | kPa | 326.70 | Thermoc... |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.66] | kPa | [428.54; 610.47] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.53095e+01 | |||
| Coefficient B | -5.43887e+03 | |||
| Coefficient C | -6.64740e+01 | |||
| Temperature range, min. | 428.54 | |||
| Temperature range, max. | 610.47 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 450 500 550 600 | ||||
| Pvap | 1.33 | kPa | 428.54 | Calculated Property |
| Pvap | 2.95 | kPa | 448.75 | Calculated Property |
| Pvap | 6.03 | kPa | 468.97 | Calculated Property |
| Pvap | 11.51 | kPa | 489.18 | Calculated Property |
| Pvap | 20.70 | kPa | 509.40 | Calculated Property |
| Pvap | 35.37 | kPa | 529.61 | Calculated Property |
| Pvap | 57.81 | kPa | 549.83 | Calculated Property |
| Pvap | 90.81 | kPa | 570.04 | Calculated Property |
| Pvap | 137.78 | kPa | 590.26 | Calculated Property |
| Pvap | 202.66 | kPa | 610.47 | Calculated Property |
Similar Compounds
![[1,1'-Biphenyl]-4,4'-diamine, N,N'-diphenyl-.](data:image/png;base64,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)
Find more compounds similar to Diphenylamine.
Mixtures
Sources
- Crippen Method
- Solubility of three natural compounds with insecticidal activity in supercritical carbon dioxide: Experimental measurements and predictive modeling with the GC-EoS
- Experimental and modeling studies of binary organic eutectic systems to be used as stabilizers for nitrate esters-based energetic materials
- Measurement and prediction of (solid + liquid) equilibria of gun powder's and propellant's stabilizers mixtures
- DSC measurement and prediction of phase diagrams for binary mixtures of energetic materials' stabilizers
- Thermochemistry of Drugs. Experimental and First-Principles Study of Fenamates
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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