- InChI
- InChI=1S/C7H18N2/c1-3-9(4-2)7-5-6-8/h3-8H2,1-2H3
- InChI Key
- QOHMWDJIBGVPIF-UHFFFAOYSA-N
- Formula
- C7H18N2
- SMILES
- CCN(CC)CCCN
- Molecular Weight1
- 130.23
- CAS
- 104-78-9
- Other Names
-
- (N,N-Diethylamino)propylamine
- 1,3-Propanediamine, N1,N1-diethyl-
- 1-(Diethylamino)propylamine-3
- 1-Amino-3-(diethylamino)propane
- 3-(Diethylamino)-1-propylamine
- 3-(Diethylamino)propylamine
- 3-(N,N-Diethylamino)-1-propylamine
- 3-Diethylamino-n-propylamine
- 3-aminopropyldiethylamine
- Diethylaminopropylamine
- Diethylaminotrimethylenamine
- N,N-Diethyl-1,3-diaminopropane
- N,N-Diethyl-1,3-propanediamine
- N,N-Diethylpropylenediamine
- N,N-Diethyltrimethylenediamine
- N,N-diethylpropane-1,3-diamine
- N-(3-Diethylaminopropyl)amine
- N-Diethyltrimethylenediamine
- NSC 7776
- UN 2684
- «gamma»-(Diethylamino)propylamine
- «gamma»-(Diethylamino)propylamine
- 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).
- 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° | 185.29 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -86.49 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 22.10 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 43.86 | kJ/mol | Joback Calculated Property |
| log10WS | -0.76 | Crippen Calculated Property | |
| logPoct/wat | 0.677 | Crippen Calculated Property | |
| McVol | 129.450 | ml/mol | McGowan Calculated Property |
| Pc | 2969.80 | kPa | Joback Calculated Property |
| Tboil | [432.20; 442.55] | K |
|
| Tboil | 432.20 | K | NIST |
| Tboil | 441.70 | K | NIST |
| Tboil | 442.55 | K | NIST |
| Tc | 621.46 | K | Joback Calculated Property |
| Tfus | 284.38 | K | Joback Calculated Property |
| Vc | 0.474 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [281.45; 354.24] | J/mol×K | [444.53; 621.46] |
|
| Cp,gas | 281.45 | J/mol×K | 444.53 | Joback Calculated Property |
| Cp,gas | 295.01 | J/mol×K | 474.02 | Joback Calculated Property |
| Cp,gas | 307.97 | J/mol×K | 503.51 | Joback Calculated Property |
| Cp,gas | 320.35 | J/mol×K | 532.99 | Joback Calculated Property |
| Cp,gas | 332.18 | J/mol×K | 562.48 | Joback Calculated Property |
| Cp,gas | 343.47 | J/mol×K | 591.97 | Joback Calculated Property |
| Cp,gas | 354.24 | J/mol×K | 621.46 | Joback Calculated Property |
| ΔvapH | [46.40; 52.40] | kJ/mol | [298.15; 386.00] |
|
| ΔvapH | 52.40 | kJ/mol | 298.15 | Vapor p... |
| ΔvapH | 46.40 | kJ/mol | 386.00 | NIST |
| Pvap | [0.01; 8.02] | kPa | [263.16; 363.25] |
|
| Pvap | 0.01 | kPa | 263.16 | Phase e... |
| Pvap | 0.03 | kPa | 273.05 | Phase e... |
| Pvap | 0.03 | kPa | 273.15 | Phase e... |
| Pvap | 0.03 | kPa | 273.15 | Excess ... |
| Pvap | 0.08 | kPa | 283.15 | Phase e... |
| Pvap | 0.07 | kPa | 283.15 | Excess ... |
| Pvap | 0.08 | kPa | 283.27 | Phase e... |
| Pvap | 0.08 | kPa | 283.27 | Phase e... |
| Pvap | 0.16 | kPa | 293.15 | Phase e... |
| Pvap | 0.15 | kPa | 293.15 | Excess ... |
| Pvap | 0.16 | kPa | 293.22 | Phase e... |
| Pvap | 0.33 | kPa | 303.14 | Phase e... |
| Pvap | 0.31 | kPa | 303.15 | Excess ... |
| Pvap | 0.33 | kPa | 303.15 | Phase e... |
| Pvap | 0.31 | kPa | 303.15 | Excess ... |
| Pvap | 0.33 | kPa | 303.16 | Phase e... |
| Pvap | 0.62 | kPa | 313.15 | Phase e... |
| Pvap | 0.59 | kPa | 313.15 | Excess ... |
| Pvap | 0.59 | kPa | 313.15 | Excess ... |
| Pvap | 0.62 | kPa | 313.16 | Phase e... |
| Pvap | 0.62 | kPa | 313.18 | Phase e... |
| Pvap | 1.05 | kPa | 323.15 | Excess ... |
| Pvap | 1.11 | kPa | 323.15 | Phase e... |
| Pvap | 1.05 | kPa | 323.15 | Excess ... |
| Pvap | 1.11 | kPa | 323.16 | Phase e... |
| Pvap | 1.11 | kPa | 323.16 | Phase e... |
| Pvap | 1.92 | kPa | 333.15 | Phase e... |
| Pvap | 1.81 | kPa | 333.15 | Excess ... |
| Pvap | 1.81 | kPa | 333.15 | Excess ... |
| Pvap | 1.94 | kPa | 333.18 | Phase e... |
| Pvap | 2.99 | kPa | 343.15 | Excess ... |
| Pvap | 2.99 | kPa | 343.15 | Excess ... |
| Pvap | 3.20 | kPa | 343.15 | Phase e... |
| Pvap | 3.23 | kPa | 343.21 | Phase e... |
| Pvap | 5.14 | kPa | 353.15 | Phase e... |
| Pvap | 4.76 | kPa | 353.15 | Excess ... |
| Pvap | 5.16 | kPa | 353.19 | Phase e... |
| Pvap | 5.16 | kPa | 353.19 | Phase e... |
| Pvap | 7.35 | kPa | 363.15 | Excess ... |
| Pvap | 8.02 | kPa | 363.15 | Phase e... |
| Pvap | 7.96 | kPa | 363.25 | Phase e... |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [0.20; 202.63] | kPa | [302.05; 497.01] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.37437e+01 | |||
| Coefficient B | -3.65186e+03 | |||
| Coefficient C | -6.39290e+01 | |||
| Temperature range, min. | 302.05 | |||
| Temperature range, max. | 497.01 | |||
| Pvap | 0.20 | kPa | 302.05 | Calculated Property |
| Pvap | 0.73 | kPa | 323.71 | Calculated Property |
| Pvap | 2.16 | kPa | 345.37 | Calculated Property |
| Pvap | 5.45 | kPa | 367.04 | Calculated Property |
| Pvap | 12.17 | kPa | 388.70 | Calculated Property |
| Pvap | 24.59 | kPa | 410.36 | Calculated Property |
| Pvap | 45.73 | kPa | 432.02 | Calculated Property |
| Pvap | 79.37 | kPa | 453.69 | Calculated Property |
| Pvap | 129.98 | kPa | 475.35 | Calculated Property |
| Pvap | 202.63 | kPa | 497.01 | Calculated Property |
Similar Compounds
![N,N-Bis[(hydroxyethyl)trimethylene]diamine.](data:image/png;base64,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)
![1,3-Propanediamine, N'-[3-(dimethylamino)propyl]-N,N-dimethyl-.](data:image/png;base64,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)
Find more compounds similar to 1,3-Propanediamine, N,N-diethyl-.
Mixtures
- 1,3-Propanediamine, N,N-diethyl- + Heptane
- n-Hexane + 1,3-Propanediamine, N,N-diethyl-
- 1,3-Propanediamine, N,N-diethyl- + Dodecane
- 1,3-Propanediamine, N,N-diethyl- + Cyclohexane
- 1,3-Propanediamine, N,N-diethyl- + Water
Sources
- Crippen Method
- Crippen Method
- Excess properties and vapour pressure of (3-diethylaminopropylamine + n-alkanes)
- Excess properties and vapour pressure of {3-diethylaminopropylamine + cyclohexane}
- Vapor pressure and enthalpy of vaporization of aliphatic propanediamines
- Phase equilibrium measurements and thermodynamic modeling of aqueous solutions of polyamines CO2 absorbents: 3-aminopropylmethylamine, 3-aminopropyldimethylamine and N,N-diethyl 1,3-propanediamine at temperatures from 273 K to 363 K
- Joback Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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