- InChI
- InChI=1S/C9H13N/c1-10(2)8-9-6-4-3-5-7-9/h3-7H,8H2,1-2H3
- InChI Key
- XXBDWLFCJWSEKW-UHFFFAOYSA-N
- Formula
- C9H13N
- SMILES
- CN(C)Cc1ccccc1
- Molecular Weight1
- 135.21
- CAS
- 103-83-3
- Other Names
-
- Araldite accelerator 062
- BDMA
- Benzenemethamine, N,N-dimethyl-
- Benzyl-N,N-dimethylamine
- Benzylamine, N,N-dimethyl-
- Benzyldimethylamine
- Dabco BDMA
- Dimethylbenzylamine
- N,N-Dimethyl-N-benzylamine
- N,N-Dimethylbenzenemethanamine
- N,N-Dimethylbenzylamine
- N-(Phenylmethyl)dimethylamine
- N-Benzyl-N,N-dimethylamine
- N-Benzyldimethylamine
- NSC 5342
- Sumine 2015
- UN 2619
- PAff : Proton affinity (kJ/mol).
- BasG : Gas basicity (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).
- 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).
- ρl : Liquid Density (kg/m3).
- 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 |
|---|---|---|---|
| PAff | 968.40 | kJ/mol | NIST |
| BasG | 937.40 | kJ/mol | NIST |
| ΔfG° | 248.09 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | 74.97 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 16.13 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [49.50; 50.10] | kJ/mol |
|
| ΔvapH° | 49.50 ± 0.40 | kJ/mol | NIST |
| ΔvapH° | 50.10 ± 0.90 | kJ/mol | NIST |
| IE | [7.69; 7.80] | eV |
|
| IE | 7.69 ± 0.05 | eV | NIST |
| IE | 7.69 ± 0.03 | eV | NIST |
| IE | 7.80 | eV | NIST |
| IE | 7.69 ± 0.05 | eV | NIST |
| log10WS | -1.76 | Crippen Calculated Property | |
| logPoct/wat | 1.748 | Crippen Calculated Property | |
| McVol | 123.890 | ml/mol | McGowan Calculated Property |
| Pc | 3254.14 | kPa | Joback Calculated Property |
| Inp | [1017.90; 1025.50] |
|
|
| Inp | 1017.90 | NIST | |
| Inp | 1025.50 | NIST | |
| I | 1350.00 | NIST | |
| Tboil | [454.00; 454.20] | K |
|
| Tboil | 454.20 | K | NIST |
| Tboil | 454.00 | K | NIST |
| Tc | 648.92 | K | Joback Calculated Property |
| Tfus | 250.08 | K | Joback Calculated Property |
| Vc | 0.450 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [245.34; 323.32] | J/mol×K | [444.44; 648.92] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 240 260 280 300 320 500 600 | ||||
| Cp,gas | 245.34 | J/mol×K | 444.44 | Joback Calculated Property |
| Cp,gas | 260.43 | J/mol×K | 478.52 | Joback Calculated Property |
| Cp,gas | 274.63 | J/mol×K | 512.60 | Joback Calculated Property |
| Cp,gas | 287.98 | J/mol×K | 546.68 | Joback Calculated Property |
| Cp,gas | 300.52 | J/mol×K | 580.76 | Joback Calculated Property |
| Cp,gas | 312.29 | J/mol×K | 614.84 | Joback Calculated Property |
| Cp,gas | 323.32 | J/mol×K | 648.92 | Joback Calculated Property |
| ΔvapH | 48.90 ± 0.40 | kJ/mol | 308.00 | NIST |
| ρl | [790.10; 907.60] | kg/m3 | [283.15; 418.15] |
|
|
T(K) Liquid Density (kg/m3) 780 800 820 840 860 880 900 300 350 400 | ||||
| ρl | 907.60 | kg/m3 | 283.15 | Measure... |
| ρl | 903.20 | kg/m3 | 288.15 | Measure... |
| ρl | 899.32 | kg/m3 | 293.15 | Measure... |
| ρl | 898.90 | kg/m3 | 293.15 | Measure... |
| ρl | 894.60 | kg/m3 | 298.15 | Measure... |
| ρl | 895.10 | kg/m3 | 298.15 | Measure... |
| ρl | 890.88 | kg/m3 | 303.15 | Measure... |
| ρl | 890.20 | kg/m3 | 303.15 | Measure... |
| ρl | 886.65 | kg/m3 | 308.15 | Measure... |
| ρl | 885.90 | kg/m3 | 308.15 | Measure... |
| ρl | 881.70 | kg/m3 | 313.15 | Measure... |
| ρl | 882.42 | kg/m3 | 313.15 | Measure... |
| ρl | 877.40 | kg/m3 | 318.15 | Measure... |
| ρl | 878.18 | kg/m3 | 318.15 | Measure... |
| ρl | 873.20 | kg/m3 | 323.15 | Measure... |
| ρl | 873.94 | kg/m3 | 323.15 | Measure... |
| ρl | 868.90 | kg/m3 | 328.15 | Measure... |
| ρl | 869.68 | kg/m3 | 328.15 | Measure... |
| ρl | 865.43 | kg/m3 | 333.15 | Measure... |
| ρl | 864.60 | kg/m3 | 333.15 | Measure... |
| ρl | 861.16 | kg/m3 | 338.15 | Measure... |
| ρl | 860.40 | kg/m3 | 338.15 | Measure... |
| ρl | 856.00 | kg/m3 | 343.15 | Measure... |
| ρl | 856.89 | kg/m3 | 343.15 | Measure... |
| ρl | 851.80 | kg/m3 | 348.15 | Measure... |
| ρl | 847.50 | kg/m3 | 353.15 | Measure... |
| ρl | 843.20 | kg/m3 | 358.15 | Measure... |
| ρl | 838.90 | kg/m3 | 363.15 | Measure... |
| ρl | 834.60 | kg/m3 | 368.15 | Measure... |
| ρl | 830.20 | kg/m3 | 373.15 | Measure... |
| ρl | 825.90 | kg/m3 | 378.15 | Measure... |
| ρl | 821.50 | kg/m3 | 383.15 | Measure... |
| ρl | 817.10 | kg/m3 | 388.15 | Measure... |
| ρl | 812.70 | kg/m3 | 393.15 | Measure... |
| ρl | 808.20 | kg/m3 | 398.15 | Measure... |
| ρl | 803.70 | kg/m3 | 403.15 | Measure... |
| ρl | 799.20 | kg/m3 | 408.15 | Measure... |
| ρl | 794.70 | kg/m3 | 413.15 | Measure... |
| ρl | 790.10 | kg/m3 | 418.15 | Measure... |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | [339.50; 456.70] | K | [2.00; 102.00] |
|
| Tboilr | 339.50 ± 0.50 | K | 2.00 | NIST |
| Tboilr | 456.70 | K | 102.00 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.64] | kPa | [335.41; 487.10] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.41873e+01 | |||
| Coefficient B | -3.72516e+03 | |||
| Coefficient C | -6.74040e+01 | |||
| Temperature range, min. | 335.41 | |||
| Temperature range, max. | 487.10 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 350 400 450 | ||||
| Pvap | 1.33 | kPa | 335.41 | Calculated Property |
| Pvap | 3.03 | kPa | 352.26 | Calculated Property |
| Pvap | 6.30 | kPa | 369.12 | Calculated Property |
| Pvap | 12.11 | kPa | 385.97 | Calculated Property |
| Pvap | 21.79 | kPa | 402.83 | Calculated Property |
| Pvap | 37.07 | kPa | 419.68 | Calculated Property |
| Pvap | 60.08 | kPa | 436.54 | Calculated Property |
| Pvap | 93.35 | kPa | 453.39 | Calculated Property |
| Pvap | 139.78 | kPa | 470.25 | Calculated Property |
| Pvap | 202.64 | kPa | 487.10 | Calculated Property |
Similar Compounds
Find more compounds similar to Benzenemethanamine, N,N-dimethyl-.
Mixtures
Sources
- Crippen Method
- Crippen Method
- Density, viscosity, refractive index and conductivity of switchable hydrophilicity solvent systems: N,N-Dimethylbenzylamine, water and carbon dioxide
- Measurement and Correlation for Acoustic, Transport, Refractive, and High-Temperature Volumetric Data of Substituted Benzylamines
- Joback Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
Note: Cheméo is only indexing the data, follow the source links to retrieve the latest data. The source is also providing more information like the publication year, authors and more. Take the time to validate and double check the source of the data.