- InChI
- InChI=1S/C4H12N2/c1-6-4-2-3-5/h6H,2-5H2,1H3
- InChI Key
- QHJABUZHRJTCAR-UHFFFAOYSA-N
- Formula
- C4H12N2
- SMILES
- CNCCCN
- Molecular Weight1
- 88.15
- CAS
- 6291-84-5
- Other Names
-
- (3-Aminopropyl)methylamine
- 1,3-Propanediamine, N1-methyl-
- 1-Amino-3-(methylamino)propane
- 3-Methylaminopropylamine
- 3-amino-1-(methylamino)propane
- N-Methyl-1,3-propanediamine
- N-methyl-1,3-diaminopropane
- N-methyl-1,3-propylenediamine
- N-methyltrimethylenediamine
- NSC 8160
- ΔcH°liquid : Standard liquid enthalpy of combustion (kJ/mol).
- 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).
- ΔfH°liquid : Liquid phase 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).
- ρl : Liquid Density (kg/m3).
- 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 | -3208.90 ± 1.70 | kJ/mol | NIST |
| ΔfG° | 138.64 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -38.63 | kJ/mol | Joback Calculated Property |
| ΔfH°liquid | -80.20 ± 1.70 | kJ/mol | NIST |
| ΔfusH° | 16.41 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 41.58 | kJ/mol | Joback Calculated Property |
| log10WS | -0.12 | Crippen Calculated Property | |
| logPoct/wat | -0.445 | Crippen Calculated Property | |
| McVol | 87.180 | ml/mol | McGowan Calculated Property |
| Pc | 4260.71 | kPa | Joback Calculated Property |
| Tboil | 413.20 | K | NIST |
| Tc | 600.57 | K | Joback Calculated Property |
| Tfus | 270.76 | K | Joback Calculated Property |
| Vc | 0.324 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [175.61; 227.44] | J/mol×K | [413.62; 600.57] | 
|
|
T(K) Ideal gas heat capacity (J/mol×K) 180 190 200 210 220 230 450 500 550 600 | ||||
| Cp,gas | 175.61 | J/mol×K | 413.62 | Joback Calculated Property |
| Cp,gas | 185.23 | J/mol×K | 444.78 | Joback Calculated Property |
| Cp,gas | 194.44 | J/mol×K | 475.94 | Joback Calculated Property |
| Cp,gas | 203.25 | J/mol×K | 507.09 | Joback Calculated Property |
| Cp,gas | 211.69 | J/mol×K | 538.25 | Joback Calculated Property |
| Cp,gas | 219.74 | J/mol×K | 569.41 | Joback Calculated Property |
| Cp,gas | 227.44 | J/mol×K | 600.57 | Joback Calculated Property |
| Cp,liquid | [243.50; 250.20] | J/mol×K | [303.15; 353.15] |
|
|
T(K) Liquid phase heat capacity (J/mol×K) 243 244 245 246 247 248 249 250 320 340 | ||||
| Cp,liquid | 243.50 | J/mol×K | 303.15 | Molar h... |
| Cp,liquid | 244.30 | J/mol×K | 308.15 | Molar h... |
| Cp,liquid | 244.40 | J/mol×K | 313.15 | Molar h... |
| Cp,liquid | 244.60 | J/mol×K | 318.15 | Molar h... |
| Cp,liquid | 245.10 | J/mol×K | 323.15 | Molar h... |
| Cp,liquid | 245.40 | J/mol×K | 328.15 | Molar h... |
| Cp,liquid | 246.00 | J/mol×K | 333.15 | Molar h... |
| Cp,liquid | 246.60 | J/mol×K | 338.15 | Molar h... |
| Cp,liquid | 247.70 | J/mol×K | 343.15 | Molar h... |
| Cp,liquid | 248.50 | J/mol×K | 348.15 | Molar h... |
| Cp,liquid | 250.20 | J/mol×K | 353.15 | Molar h... |
| ΔvapH | [45.90; 53.10] | kJ/mol | [298.15; 370.00] |
|
| ΔvapH | 53.10 | kJ/mol | 298.15 | Vapor p... |
| ΔvapH | 45.90 | kJ/mol | 370.00 | NIST |
| Pvap | [0.09; 170.02] | kPa | [273.00; 432.40] |
|
|
T(K) Vapor pressure (kPa) 0 50 100 150 300 350 400 | ||||
| Pvap | 0.09 | kPa | 273.00 | Phase e... |
| Pvap | 0.09 | kPa | 273.15 | Phase e... |
| Pvap | 0.20 | kPa | 283.15 | Phase e... |
| Pvap | 0.20 | kPa | 283.37 | Phase e... |
| Pvap | 0.43 | kPa | 293.15 | Phase e... |
| Pvap | 0.43 | kPa | 293.47 | Phase e... |
| Pvap | 0.86 | kPa | 303.11 | Phase e... |
| Pvap | 0.85 | kPa | 303.15 | Phase e... |
| Pvap | 1.59 | kPa | 313.15 | Phase e... |
| Pvap | 1.61 | kPa | 313.18 | Phase e... |
| Pvap | 2.81 | kPa | 323.15 | Phase e... |
| Pvap | 2.83 | kPa | 323.26 | Phase e... |
| Pvap | 2.83 | kPa | 323.26 | Phase e... |
| Pvap | 3.46 | kPa | 326.81 | Ebullio... |
| Pvap | 4.47 | kPa | 331.62 | Ebullio... |
| Pvap | 4.75 | kPa | 333.15 | Phase e... |
| Pvap | 4.76 | kPa | 333.23 | Phase e... |
| Pvap | 4.76 | kPa | 333.25 | Phase e... |
| Pvap | 5.97 | kPa | 337.36 | Ebullio... |
| Pvap | 7.72 | kPa | 343.15 | Phase e... |
| Pvap | 7.75 | kPa | 343.26 | Phase e... |
| Pvap | 7.74 | kPa | 343.28 | Phase e... |
| Pvap | 7.74 | kPa | 343.30 | Phase e... |
| Pvap | 7.97 | kPa | 343.91 | Ebullio... |
| Pvap | 11.85 | kPa | 352.54 | Phase e... |
| Pvap | 11.85 | kPa | 352.54 | Phase e... |
| Pvap | 12.08 | kPa | 353.15 | Phase e... |
| Pvap | 12.14 | kPa | 353.24 | Phase e... |
| Pvap | 12.48 | kPa | 353.78 | Ebullio... |
| Pvap | 18.10 | kPa | 362.82 | Phase e... |
| Pvap | 18.11 | kPa | 362.84 | Phase e... |
| Pvap | 18.31 | kPa | 363.15 | Phase e... |
| Pvap | 20.47 | kPa | 365.76 | Ebullio... |
| Pvap | 26.61 | kPa | 372.74 | Phase e... |
| Pvap | 26.61 | kPa | 372.76 | Phase e... |
| Pvap | 27.96 | kPa | 372.77 | Ebullio... |
| Pvap | 38.34 | kPa | 382.84 | Phase e... |
| Pvap | 38.35 | kPa | 382.87 | Phase e... |
| Pvap | 39.97 | kPa | 383.53 | Ebullio... |
| Pvap | 53.96 | kPa | 392.92 | Phase e... |
| Pvap | 53.96 | kPa | 392.95 | Phase e... |
| Pvap | 64.98 | kPa | 397.99 | Ebullio... |
| Pvap | 73.40 | kPa | 402.59 | Phase e... |
| Pvap | 73.40 | kPa | 402.59 | Phase e... |
| Pvap | 73.41 | kPa | 402.61 | Phase e... |
| Pvap | 79.98 | kPa | 404.70 | Ebullio... |
| Pvap | 101.27 | kPa | 412.50 | Ebullio... |
| Pvap | 129.80 | kPa | 422.46 | Phase e... |
| Pvap | 129.79 | kPa | 422.46 | Phase e... |
| Pvap | 129.84 | kPa | 422.51 | Phase e... |
| Pvap | 170.02 | kPa | 432.40 | Phase e... |
| Pvap | 169.97 | kPa | 432.40 | Phase e... |
| ρl | [787.72; 860.46] | kg/m3 | [283.15; 363.15] |
|
|
T(K) Liquid Density (kg/m3) 790 800 810 820 830 840 850 860 300 320 340 360 | ||||
| ρl | 860.46 | kg/m3 | 283.15 | Volumet... |
| ρl | 851.61 | kg/m3 | 293.15 | Volumet... |
| ρl | 848.00 | kg/m3 | 298.15 | Study o... |
| ρl | 842.69 | kg/m3 | 303.15 | Volumet... |
| ρl | 849.10 | kg/m3 | 303.15 | Mutual ... |
| ρl | 844.70 | kg/m3 | 308.15 | Mutual ... |
| ρl | 840.30 | kg/m3 | 313.15 | Mutual ... |
| ρl | 833.72 | kg/m3 | 313.15 | Volumet... |
| ρl | 835.90 | kg/m3 | 318.15 | Mutual ... |
| ρl | 831.50 | kg/m3 | 323.15 | Mutual ... |
| ρl | 824.67 | kg/m3 | 323.15 | Volumet... |
| ρl | 815.56 | kg/m3 | 333.15 | Volumet... |
| ρl | 806.37 | kg/m3 | 343.15 | Volumet... |
| ρl | 797.09 | kg/m3 | 353.15 | Volumet... |
| ρl | 787.72 | kg/m3 | 363.15 | Volumet... |
Similar Compounds
![1,3-Propanediamine, N'-[3-(dimethylamino)propyl]-N,N-dimethyl-.](data:image/png;base64,iVBORw0KGgoAAAANSUhEUgAAAPoAAAD6CAIAAAAHjs1qAAANoklEQVR4nO3dXUyT5xvH8au8FyYCIiBQFFARtfVlU6Z7IcLWBabBxOESE9yJIR7VGEzYlhgSj5CZQLJkCbpk6bLEhMTE4X8LGeLiohN1AmYovkwdKIogMMfbWqDX/+CuxQnYAu3Tmev3OWLp0z53y5f7vvsUmY6ZCUCGAH8PAEA7yB0EQe4gCHIHQZA7CILcQRDkDoIgdxAEuYMgyB0EQe4gCHIHQZA7CILcQRDkDoIgdxAEuYMgyB0EQe4gCHIHQZA7CILcQRDkDoIgdxAEuYMgyB0EQe4gCHIHQZA7CILcQRDkDoIgdxAEuYMgyB0EQe4gCHIHQZA7CILcQRDkDoIgdxAEuYMgyB0EQe4gCHIHQZA7CILcQRDkDoIgdxAEuYMgyB0EQe4gCHIHQZA7CILcQRDkDoIgdxAEuYMgyB0EQe4gCHIHQZA7CILcQRDkDoIgdxAEuYMgyB0EQe4gCHIHQZA7CILcQRDkDoIgdxAEuYMgyB0EQe4gCHIHQZA7CILcQRDkDoIgdxAEuYMgyB0EQe4gCHIHQZA7CILcQRDkDoIgdxAEuYMgyB0EQe4gCHIHQZA7CILcQRDkDoIgdxAEuYMgyB0EQe4gCHIHQZA7CILcQRDkDoIEuT3ixo0bIyMj69at02A00+no6Ojo6Ojq6iooKAgODvbXMBwOx4kTJ1JTU+fNm5eRkeGvYRDRzZs3BwYG7t27t2PHjoAAv81Zo6Oj33//fUJCQkpKSkpKir+GQUTNzc16vX7FihVujmN33n///YCAgKKioq6uLrcHe93w8HB5eflrr70WGxtLRMuWLaupqdF+GMzc2Nj45ptvElFycnJwcLDFYunv79d+GAMDA2VlZaGhoYmJiUS0bt26s2fPaj8MZq6vr1+1ahURxcXF6fX60tLSgYEB7Yfx5MkTi8USGBi4ZcsWtwe7yd1ut5eUlISEhBDR/Pnzjxw5YrPZvDRONxwOx/Hjxw0GAxHpdLqcnJylS5eqH9G8vLy2tjZthsHM7e3tO3fu1Ol0RGQwGMxms5pQ4+Lijh49Oj4+rs0wxsfHjx49GhcXR0QBAQFms9n14uzcubO9vV2bYTBzW1tbXl6e+l4sXbo0JyfH9eIcP37c4XBoMwybzXbkyJH58+cTUUhISElJid1uf/ld3M/uzHzr1q3CwkL19LSZX69cufLOO++oM65fv/6XX35hZrvdXl1drab54ODg4uLinp4enw5jaGhIrS1EFB4e7prAmpub3333XTW8tWvXajC/NjY2ZmVlqTNmZWU1Njbys6Vv3rx5RKTm17///tunw+jv7y8tLQ0NDSWiqKio8vLyf/75h5kvXryolj4i2rhx44ULF3w6DH5ubSGi9957r7W11ZN7eZS7cvr06dWrV6sT5Obm/v7777Md6su41iYiWrBgQVVV1djY2PMH9Pb2ug6IiYmZfIC31NbWLlmyRD3frVu33rt3b/IBqamprgPu3r3ri2Hcv3+/qKhITZ/JyclWq/WF6fPBgweuA5KSkiYf4BXj4+NWq9W1tkze3DocDqvVmpCQoBacoqKiR48eeX0YzHzz5s0PP/xQvezLly8/deqU5/edQe7MbLfbKysro6Ki1Py6b9++vr7+mQ12ejabvaKiIjIyUq1NBw4cePr06XQHX79+/YMPPlDPOTMzs66uzlvDYOYrV668/fbbL6wtUxoeHj506FB4eLiaXw8ePDg4OOStYQwODh08eFCv16u15dChQ8PDw9MdfOnSpU2bNqkxb9iw4ddff/XWMJj5559/XrNmjXrw7Ozs5ubm6Y58+vTpgQMH1O43MjKyoqLCZnOzwfBcX1//vn371LWKqKioyspKt7uXF8wsd8U1v+r1MStX2qqqeHR0Fg/zL/X1vGaNbcmS5Wptunbtmif3qq2tTUtLc82vd+7cmeMwenp6XEtHbGysh0tHZ2enml9jY1dmZIxVV/Mc9/MOB9fU8KpVT+PiEtRT+/PPPz24l/fnV7dry5Ru376tdr8pKVtWrnTMffM7Ps5WKxuNDyIiItTa8vjx41k8zmxyV1paWvbsaSRiIjaZ+MyZWT7OtWtsNrN6nO3bT890nrbZbFVVVWr/GhISYrFYXrImvITdbq+qqlJri7rwMtPHOX/+/K5d19UT2byZL12axSiYmS9d4s2bnS/Irl0nz58/P6O7Dw4OlpWVhYWFEVFERERZWdnIyMgshjE0NOR6nPDw8LKyspesLVOqq6vbvv2+eiJmM3s2g03hzBk2mZwvyJ4937W0tMzygeaSu1Jby2lpzqFs3cozml77+ri0lENCmIijo7m8nGd91aezs7O4uFhdMElMTKyurp7RBZP6+vrMzEzX+57r16/PbhgOB1utnJDARKzTcWEhd3TM4O4PH3JxMQcGMhHHxnJVFc/6XYlrfiWi9PT0GV1dcDgcNTU16jq6TqcrLCz0ZG2Z0ugoV1fzwoVMxEFBXFzM3d0zuHtHBxcVOesyGNhq5Tm+K5lr7sxss3FVFUdGMhGHhLDFwm6nRbU2xcUxEQcEcFERz2ppetHly5c3b96svsdvvPHGuXPn3N7lxo0b+fn56i4ZGRk//PDD3IcxOMhlZRwWxkQcEcFlZex2erXbJ17D4GCPXkNPNDQ0mEwm9exycnKuXr3q9i6XL19+66231F1ef/11T15Dt3p72WLhoCDnvObJ7ndoaOI1DA/36DX0hBdyVzo7ubiYAwKYiBctYrV/bWriW7ecB9jtrK7XPb82bdnCHnwLZmDyzDTdBem+vj6LxRIUFERE0dHR5eXl3v1IYfLMxMwXLrBrOIODrK7X1dZyevrECvnHH14cBY+OjlZXVy9cuNB1RaV7mgn24cOHrhVy0aJFM10h3Wpr47w859NcsYJ//JGZ+exZdr2/6O3lpibn+5aUlIkV0oufKHgtd6WxkbOyXPtONpvZYGD1WVtPD8fH8+HDzlvT0vjECe+efMLkfefz+9fnCwgKCiouLp6ugLmrr+fVq51Pef9+NpnYaGR1OaG1lU0m3r/feevq1Vxf76NRcF9fX2lpqbpgMvlnW73/cV0Tm/X7H0+cODGx+z18mOPjOTvbuUVpaGCzmXftct6alcWNjV4+u5dzZ5746fzf/9hs5txcLilhfpb7nTscE+O1tenlOjo6ioqK1LpsMBisViszNzQ0GI3GGa3vc6R2bvHxfPEim0ycm8tffMH8LPfffuMFCzxa3+duyp2b169uuaV2brGxfOsWx8dzbi5/+y3zs9xPnZrYHXid93NX1Jt4s5nr6jg1la9edebuukkzz/ednJzsevd28uRJLYehnrXJxOfOcXIyt7c7c2fNX5CTJ0+mp6e/8IIYjcaGhgYth6GedXw8NzWxwcC9vc7c2ZcviK9+mU6vd34RHk4VFbR3LzG/eJM2cnJyWlpa1CeCRqNRXZtrbW0tKCjQchiuZ71wIX36KVksU9ykjYKCgra2NrV7MRqN6pPppqamnJwcLYfhetbp6fTJJ/TZZ1Pc5HXufwF47j76iL7+mr77ToNTTS0gIGD37t3btm0LDAwcHh5WH8T40d699M039NNPfhuA+kT8448/Dg8PHx8fj46O9ttQiIjo88/JZKJly3x+Ii1yJ6Ivv6TsbG1ONS31TVVvyPwrMJC++ory8ykpyZ/D8PuPvYteT5WVtHs3bdjg2xNp9C8Dli2jPXu0OdWrYeNG2rHD34P4L9m6lZ79jqkP6di1p/aBR48oOprCwoiI7HZ69IgWL/bd2V4BLS2UmUmhoUREQ0N0+zatXevnIflXezsZDKT+PdbgIA0M0KJFPjydb3NXkpPp8WPq7KS4OF+f6r8uIYGamigxkYjo4UNav566uvw9Jn/r7qakJIqPpwcPfH4uLTYzo6M0Nka+/7GCVxIzjY3R6KgW58JfIgBBNLoyAy7Z2RQUREQ0NubvociD3LV29uy/9u6gJWxmQBDkDoIgd00dO0YxMc6vY2Lo2DG/jkYe7N01tW3bxNdhYf/6T9AAZncQRIvZPSnprl4/ptOlEwVqcDp4teh044sX34mJCSJK8/W5tMi9s3NTd3c3cxdRvAang1cL85P29oyRkTiix74+FzYzIAhyB0GQOwiC3EEQ5A6CIHcQBLmDIMgdBEHuIIgWn6rm5+f/9ddf6g+UArwgLCxs+/bt6v+A5Gta/CUCgP8IbGZAEOQOgiB3EAS5gyDIHQRB7iAIcgdBkDsIgtxBEOQOgiB3EAS5gyDIHQRB7iAIcgdBkDsIgtxBEOQOgiB3EAS5gyDIHQRB7iAIcgdBkDsIgtxBEOQOgiB3EAS5gyDIHQRB7iAIcgdBkDsIgtxBEOQOgiB3EAS5gyDIHQRB7iAIcgdBkDsIgtxBEOQOgiB3EAS5gyDIHQRB7iAIcgdBkDsIgtxBEOQOgiB3EAS5gyDIHQRB7iAIcgdBkDsIgtxBEOQOgiB3EAS5gyDIHQRB7iAIcgdBkDsIgtxBEOQOgiB3EAS5gyDIHQRB7iAIcgdBkDsIgtxBEOQOgiB3EAS5gyDIHQRB7iAIcgdBkDsIgtxBEOQOgiB3EAS5gyDIHQRB7iAIcgdBkDsIgtxBEOQOgiB3EAS5gyDIHQRB7iAIcgdBkDsIgtxBEOQOgiB3EAS5gyDIHQRB7iAIcgdBkDsI8n81H6Mj6yqEkgAAAABJRU5ErkJggg==)
Find more compounds similar to 1,3-Propanediamine, N-methyl-.
Mixtures
- 1,3-Propanediamine, N-methyl- + Water
- 1-Propanol, 3-(dimethylamino)- + 1,3-Propanediamine, N-methyl- + Water
- 1,3-Propanediamine, N-methyl- + N-«beta»-Hydroxyethylpyrrolidine + Water
- 1-Propanol, 3-(diethylamino)- + 1,3-Propanediamine, N-methyl- + Water
- Piperazine + 1,3-Propanediamine, N-methyl- + Water
- 1,3-Propanediamine, N-methyl- + Methyldiethanolamine
- 1,3-Propanediamine, N-methyl- + N,N-Diethyl-2-aminoethanol
- 1,3-Propanediamine, N-methyl- + N,N-Dimethylaminoethanol
- 1,3-Propanediamine, N-methyl- + Methyldiethanolamine + Water
- 1,3-Propanediamine, N-methyl- + N-Methylglycine + Water
- 1,3-Propanediamine, N-methyl- + N,N-Diethyl-2-aminoethanol + Water
- Carbon dioxide + 1,3-Propanediamine, N-methyl- + Water
Sources
- Crippen Method
- Crippen Method
- Mutual diffusion coefficients, density, and viscosity of aqueoussolutions of new polyamine CO2absorbents
- Density, viscosity, and N2O solubility of aqueous amino acid salt and amine amino acid salt solutions
- 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
- Vapour-liquid equilibrium study of tertiary amines, single and in blend with 3-(methylamino)propylamine, for post-combustion CO2 capture
- Molar heat capacities of diethylenetriamine and 3-(methylamino)propylamine, their aqueous binaries, and aqueous ternaries with piperazine
- Study of CO2 Absorption into Phase Change Solvents MAPA and DEEA
- Freezing Point Depressions of Phase Change CO2 Solvents
- Volumetric Properties of Binary Mixtures of 3-(Methylamino)propylamine with Water, N-Methyldiethanolamine, N,N-Dimethylethanolamine, and N,N-Diethylethanolamine from (283.15 to 363.15) K
- Equilibrium Total Pressure and CO2 Solubility in Binary and Ternary Aqueous Solutions of 2-(Diethylamino)ethanol (DEEA) and 3-(Methylamino)propylamine (MAPA)
- Ebulliometric Determination of Vapor
- Joback Method
- McGowan Method
- NIST Webbook
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.