- InChI
- InChI=1S/C5H14N2/c1-6-4-5-7(2)3/h6H,4-5H2,1-3H3
- InChI Key
- HVOYZOQVDYHUPF-UHFFFAOYSA-N
- Formula
- C5H14N2
- SMILES
- CNCCN(C)C
- Molecular Weight1
- 102.18
- CAS
- 142-25-6
- Other Names
-
- 1,2-Diaminoethane, N,N,N'-trimethyl-
- 1-(N,N-dimethylamino)-2-(N-methylamino)ethane
- 2-(Dimethylamino)-N-methylethylamine
- Ethylenediamine, N,N,N'-trimethyl-
- N,N,N'-Trimethyl-1,2-ethanediamine
- N,N,N'-Trimethyldiaminoethane
- N,N,N'-Trimethylethanediamine
- N,N,N'-Trimethylethylenediamine
- N-[2-(dimethylamino)ethyl]-N-methylamine
- N1,N1,N2-trimethylethane-1,2-diamine
- dimethyl(2-(methylamino)ethyl)amine
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,liquid : Liquid phase 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).
- 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).
- 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° | 191.39 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -25.53 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 16.83 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 35.20 | kJ/mol | Joback Calculated Property |
| log10WS | 0.33 | Crippen Calculated Property | |
| logPoct/wat | -0.233 | Crippen Calculated Property | |
| McVol | 101.270 | ml/mol | McGowan Calculated Property |
| Pc | 3513.74 | kPa | Joback Calculated Property |
| Tboil | 390.20 | K | NIST |
| Tc | 545.47 | K | Joback Calculated Property |
| Tfus | 231.24 | K | Joback Calculated Property |
| Vc | 0.368 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [189.13; 250.59] | J/mol×K | [376.41; 545.47] | 
|
| Cp,gas | 189.13 | J/mol×K | 376.41 | Joback Calculated Property |
| Cp,gas | 200.50 | J/mol×K | 404.59 | Joback Calculated Property |
| Cp,gas | 211.39 | J/mol×K | 432.76 | Joback Calculated Property |
| Cp,gas | 221.84 | J/mol×K | 460.94 | Joback Calculated Property |
| Cp,gas | 231.85 | J/mol×K | 489.11 | Joback Calculated Property |
| Cp,gas | 241.43 | J/mol×K | 517.29 | Joback Calculated Property |
| Cp,gas | 250.59 | J/mol×K | 545.47 | Joback Calculated Property |
| Cp,liquid | [258.30; 286.60] | J/mol×K | [303.20; 353.20] |
|
| Cp,liquid | 258.30 | J/mol×K | 303.20 | Heat ca... |
| Cp,liquid | 260.00 | J/mol×K | 308.20 | Heat ca... |
| Cp,liquid | 262.70 | J/mol×K | 313.20 | Heat ca... |
| Cp,liquid | 265.30 | J/mol×K | 318.20 | Heat ca... |
| Cp,liquid | 269.20 | J/mol×K | 323.20 | Heat ca... |
| Cp,liquid | 272.70 | J/mol×K | 328.20 | Heat ca... |
| Cp,liquid | 276.00 | J/mol×K | 333.20 | Heat ca... |
| Cp,liquid | 278.90 | J/mol×K | 338.20 | Heat ca... |
| Cp,liquid | 281.30 | J/mol×K | 343.20 | Heat ca... |
| Cp,liquid | 283.40 | J/mol×K | 348.20 | Heat ca... |
| Cp,liquid | 286.60 | J/mol×K | 353.20 | Heat ca... |
| Pvap | [0.50; 4.40] | kPa | [274.20; 305.40] |
|
| Pvap | 0.50 | kPa | 274.20 | Thermod... |
| Pvap | 0.60 | kPa | 276.70 | Thermod... |
| Pvap | 0.89 | kPa | 281.80 | Thermod... |
| Pvap | 1.27 | kPa | 286.80 | Thermod... |
| Pvap | 1.69 | kPa | 291.00 | Thermod... |
| Pvap | 2.40 | kPa | 296.30 | Thermod... |
| Pvap | 2.73 | kPa | 298.20 | Thermod... |
| Pvap | 3.26 | kPa | 301.00 | Thermod... |
| Pvap | 3.81 | kPa | 303.20 | Thermod... |
| Pvap | 4.07 | kPa | 304.10 | Thermod... |
| Pvap | 4.40 | kPa | 305.40 | Thermod... |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.66] | kPa | [294.12; 413.06] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.56393e+01 | |||
| Coefficient B | -3.75363e+03 | |||
| Coefficient C | -4.96120e+01 | |||
| Temperature range, min. | 294.12 | |||
| Temperature range, max. | 413.06 | |||
| Pvap | 1.33 | kPa | 294.12 | Calculated Property |
| Pvap | 2.93 | kPa | 307.34 | Calculated Property |
| Pvap | 5.96 | kPa | 320.55 | Calculated Property |
| Pvap | 11.35 | kPa | 333.77 | Calculated Property |
| Pvap | 20.42 | kPa | 346.98 | Calculated Property |
| Pvap | 34.94 | kPa | 360.20 | Calculated Property |
| Pvap | 57.22 | kPa | 373.41 | Calculated Property |
| Pvap | 90.16 | kPa | 386.63 | Calculated Property |
| Pvap | 137.25 | kPa | 399.84 | Calculated Property |
| Pvap | 202.66 | kPa | 413.06 | Calculated Property |
Similar Compounds
![N-[2-(1-piperazinyl)ethyl]ethylenediamine.](data:image/png;base64,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)
Find more compounds similar to 1,2-Ethanediamine, N,N,N'-trimethyl-.
Mixtures
- 1,2-Ethanediamine, N,N,N'-trimethyl- + Water
- 1,2-Ethanediamine, N,N,N'-trimethyl- + Piperazine + Water
Sources
- Crippen Method
- Crippen Method
- Heat capacities of aqueous binary and ternary mixtures (with piperazine) of N-(2-aminoethyl)-piperazine and N,N,N'-trimethylethylenediamine at temperatures (303.2-353.2) K
- Thermodynamic Properties of N-Methyl-Substituted Ethane-1,2-diamines: Experimental and Computational Study
- Joback Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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