- InChI
- InChI=1S/C5H14N2/c1-7(2)5-3-4-6/h3-6H2,1-2H3
- InChI Key
- IUNMPGNGSSIWFP-UHFFFAOYSA-N
- Formula
- C5H14N2
- SMILES
- CN(C)CCCN
- Molecular Weight1
- 102.18
- CAS
- 109-55-7
- Other Names
-
- 1,3-Propanediamine, N1,N1-dimethyl-
- 1-(Dimethylamino)-3-aminopropane
- 1-Amino-3-(dimethylamino)propane
- 3-(Dimethylamino)-1-aminopropane
- 3-(Dimethylamino)-1-propanamine
- 3-(Dimethylamino)-1-propylamine
- 3-(dimethylamino)propylamine
- 3-Amino-1-(dimethylamino)propane
- 3-Dimethylamino-n-propylamine
- 3-aminopropyldimethylamine
- 3-dimethylamino-1-propylamine
- 3-dimethylaminopropylamine
- H2N(CH2)3N(CH3)2
- N,N-Dimethyl-1,3-diaminopropane
- N,N-Dimethyl-1,3-propylenediamine
- N,N-Dimethyl-N-(3-aminopropyl)amine
- N,N-Dimethylpropylene-1,3-diamine
- N,N-Dimethylpropylenediamine
- N,N-Dimethyltrimethylenediamine
- N,N-dimethyl-1,3-propanediamine
- N-(3-aminopropyl)dimethylamine
- NSC 1067
- Propylamine, 3-(N,N-dimethylamino)-
- «gamma»-(Dimethylamino)propylamine
- PAff : Proton affinity (kJ/mol).
- BasG : Gas basicity (kJ/mol).
- 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).
- ΔfusH : Enthalpy of fusion 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).
- 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).
- ΔfusS : Entropy of fusion at a given temperature (J/mol×K).
- S°liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Ttriple : Triple Point Temperature (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 | 1025.00 | kJ/mol | NIST |
| BasG | 975.30 | kJ/mol | NIST |
| ΔcH°liquid | [-3891.50; -3876.00] | kJ/mol |
|
| ΔcH°liquid | -3891.50 ± 4.00 | kJ/mol | NIST |
| ΔcH°liquid | -3891.10 ± 0.50 | kJ/mol | NIST |
| ΔcH°liquid | -3876.00 ± 2.00 | kJ/mol | NIST |
| ΔfG° | 168.45 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | [-44.80; -34.70] | kJ/mol |
|
| ΔfH°gas | -34.70 ± 4.00 | kJ/mol | NIST |
| ΔfH°gas | -35.10 | kJ/mol | NIST |
| ΔfH°gas | -44.80 | kJ/mol | NIST |
| ΔfH°liquid | [-77.30; -76.90] | kJ/mol |
|
| ΔfH°liquid | -76.90 ± 4.00 | kJ/mol | NIST |
| ΔfH°liquid | -77.30 ± 0.50 | kJ/mol | NIST |
| ΔfusH° | 16.92 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [42.20; 47.28] | kJ/mol |
|
| ΔvapH° | 42.24 ± 0.09 | kJ/mol | NIST |
| ΔvapH° | 42.20 | kJ/mol | NIST |
| ΔvapH° | 47.28 | kJ/mol | NIST |
| log10WS | 0.08 | Crippen Calculated Property | |
| logPoct/wat | -0.103 | Crippen Calculated Property | |
| McVol | 101.270 | ml/mol | McGowan Calculated Property |
| Pc | 3704.46 | kPa | Joback Calculated Property |
| S°liquid | 323.00 | J/mol×K | NIST |
| Tboil | [405.20; 408.05] | K |
|
| Tboil | 406.00 | K | NIST |
| Tboil | 405.20 | K | NIST |
| Tboil | 408.05 | K | NIST |
| Tc | 578.11 | K | Joback Calculated Property |
| Tfus | 261.84 | K | Joback Calculated Property |
| Ttriple | 194.43 ± 0.02 | K | NIST |
| Vc | 0.362 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [201.04; 261.97] | J/mol×K | [398.77; 578.11] |
|
| Cp,gas | 201.04 | J/mol×K | 398.77 | Joback Calculated Property |
| Cp,gas | 212.39 | J/mol×K | 428.66 | Joback Calculated Property |
| Cp,gas | 223.25 | J/mol×K | 458.55 | Joback Calculated Property |
| Cp,gas | 233.62 | J/mol×K | 488.44 | Joback Calculated Property |
| Cp,gas | 243.52 | J/mol×K | 518.33 | Joback Calculated Property |
| Cp,gas | 252.96 | J/mol×K | 548.22 | Joback Calculated Property |
| Cp,gas | 261.97 | J/mol×K | 578.11 | Joback Calculated Property |
| Cp,liquid | [248.71; 255.70] | J/mol×K | [295.96; 298.15] |
|
| Cp,liquid | 249.00 | J/mol×K | 295.96 | NIST |
| Cp,liquid | 248.71 | J/mol×K | 298.00 | NIST |
| Cp,liquid | 255.70 | J/mol×K | 298.15 | NIST |
| ΔfusH | [12.38; 12.38] | kJ/mol | [194.40; 194.43] |
|
| ΔfusH | 12.38 | kJ/mol | 194.40 | NIST |
| ΔfusH | 12.38 | kJ/mol | 194.43 | NIST |
| ΔvapH | [44.10; 46.00] | kJ/mol | [290.00; 298.15] |
|
| ΔvapH | 44.10 ± 0.20 | kJ/mol | 290.00 | NIST |
| ΔvapH | 46.00 | kJ/mol | 298.15 | Vapor p... |
| Pvap | [0.18; 24.10] | kPa | [273.04; 363.44] |
|
| Pvap | 0.18 | kPa | 273.04 | Phase e... |
| Pvap | 0.38 | kPa | 283.06 | Phase e... |
| Pvap | 0.38 | kPa | 283.15 | Phase e... |
| Pvap | 0.75 | kPa | 293.13 | Phase e... |
| Pvap | 0.75 | kPa | 293.15 | Phase e... |
| Pvap | 1.40 | kPa | 303.15 | Phase e... |
| Pvap | 1.40 | kPa | 303.16 | Phase e... |
| Pvap | 2.46 | kPa | 313.15 | Phase e... |
| Pvap | 2.48 | kPa | 313.21 | Phase e... |
| Pvap | 4.16 | kPa | 323.15 | Phase e... |
| Pvap | 4.19 | kPa | 323.27 | Phase e... |
| Pvap | 6.76 | kPa | 333.15 | Phase e... |
| Pvap | 6.83 | kPa | 333.32 | Phase e... |
| Pvap | 10.61 | kPa | 343.15 | Phase e... |
| Pvap | 10.73 | kPa | 343.37 | Phase e... |
| Pvap | 10.72 | kPa | 343.37 | Phase e... |
| Pvap | 16.15 | kPa | 353.15 | Phase e... |
| Pvap | 16.31 | kPa | 353.41 | Phase e... |
| Pvap | 23.90 | kPa | 363.15 | Phase e... |
| Pvap | 24.10 | kPa | 363.44 | Phase e... |
| ρl | [753.82; 830.37] | kg/m3 | [278.15; 363.15] |
|
| ρl | 830.37 | kg/m3 | 278.15 | Volumet... |
| ρl | 829.93 | kg/m3 | 278.65 | Volumet... |
| ρl | 829.49 | kg/m3 | 279.15 | Volumet... |
| ρl | 829.05 | kg/m3 | 279.65 | Volumet... |
| ρl | 828.61 | kg/m3 | 280.15 | Volumet... |
| ρl | 828.17 | kg/m3 | 280.65 | Volumet... |
| ρl | 827.73 | kg/m3 | 281.15 | Volumet... |
| ρl | 827.29 | kg/m3 | 281.65 | Volumet... |
| ρl | 826.84 | kg/m3 | 282.15 | Volumet... |
| ρl | 826.40 | kg/m3 | 282.65 | Volumet... |
| ρl | 825.96 | kg/m3 | 283.15 | Volumet... |
| ρl | 825.52 | kg/m3 | 283.65 | Volumet... |
| ρl | 825.08 | kg/m3 | 284.15 | Volumet... |
| ρl | 824.64 | kg/m3 | 284.65 | Volumet... |
| ρl | 824.20 | kg/m3 | 285.15 | Volumet... |
| ρl | 823.76 | kg/m3 | 285.65 | Volumet... |
| ρl | 823.32 | kg/m3 | 286.15 | Volumet... |
| ρl | 822.88 | kg/m3 | 286.65 | Volumet... |
| ρl | 822.44 | kg/m3 | 287.15 | Volumet... |
| ρl | 822.00 | kg/m3 | 287.65 | Volumet... |
| ρl | 821.56 | kg/m3 | 288.15 | Volumet... |
| ρl | 821.12 | kg/m3 | 288.65 | Volumet... |
| ρl | 820.67 | kg/m3 | 289.15 | Volumet... |
| ρl | 820.23 | kg/m3 | 289.65 | Volumet... |
| ρl | 819.79 | kg/m3 | 290.15 | Volumet... |
| ρl | 819.35 | kg/m3 | 290.65 | Volumet... |
| ρl | 818.91 | kg/m3 | 291.15 | Volumet... |
| ρl | 818.47 | kg/m3 | 291.65 | Volumet... |
| ρl | 818.03 | kg/m3 | 292.15 | Volumet... |
| ρl | 817.58 | kg/m3 | 292.65 | Volumet... |
| ρl | 817.14 | kg/m3 | 293.15 | Volumet... |
| ρl | 816.70 | kg/m3 | 293.65 | Volumet... |
| ρl | 816.26 | kg/m3 | 294.15 | Volumet... |
| ρl | 815.82 | kg/m3 | 294.65 | Volumet... |
| ρl | 815.37 | kg/m3 | 295.15 | Volumet... |
| ρl | 814.93 | kg/m3 | 295.65 | Volumet... |
| ρl | 814.49 | kg/m3 | 296.15 | Volumet... |
| ρl | 814.05 | kg/m3 | 296.65 | Volumet... |
| ρl | 813.60 | kg/m3 | 297.15 | Volumet... |
| ρl | 813.16 | kg/m3 | 297.65 | Volumet... |
| ρl | 812.78 | kg/m3 | 298.15 | Density... |
| ρl | 812.72 | kg/m3 | 298.15 | Volumet... |
| ρl | 812.27 | kg/m3 | 298.65 | Volumet... |
| ρl | 811.83 | kg/m3 | 299.15 | Volumet... |
| ρl | 811.39 | kg/m3 | 299.65 | Volumet... |
| ρl | 810.94 | kg/m3 | 300.15 | Volumet... |
| ρl | 810.50 | kg/m3 | 300.65 | Volumet... |
| ρl | 810.06 | kg/m3 | 301.15 | Volumet... |
| ρl | 809.61 | kg/m3 | 301.65 | Volumet... |
| ρl | 809.17 | kg/m3 | 302.15 | Volumet... |
| ρl | 808.72 | kg/m3 | 302.65 | Volumet... |
| ρl | 808.28 | kg/m3 | 303.15 | Volumet... |
| ρl | 807.84 | kg/m3 | 303.65 | Volumet... |
| ρl | 807.39 | kg/m3 | 304.15 | Volumet... |
| ρl | 806.95 | kg/m3 | 304.65 | Volumet... |
| ρl | 806.50 | kg/m3 | 305.15 | Volumet... |
| ρl | 806.06 | kg/m3 | 305.65 | Volumet... |
| ρl | 805.61 | kg/m3 | 306.15 | Volumet... |
| ρl | 805.17 | kg/m3 | 306.65 | Volumet... |
| ρl | 804.72 | kg/m3 | 307.15 | Volumet... |
| ρl | 804.28 | kg/m3 | 307.65 | Volumet... |
| ρl | 803.83 | kg/m3 | 308.15 | Volumet... |
| ρl | 803.39 | kg/m3 | 308.65 | Volumet... |
| ρl | 802.94 | kg/m3 | 309.15 | Volumet... |
| ρl | 802.50 | kg/m3 | 309.65 | Volumet... |
| ρl | 802.05 | kg/m3 | 310.15 | Volumet... |
| ρl | 801.61 | kg/m3 | 310.65 | Volumet... |
| ρl | 801.16 | kg/m3 | 311.15 | Volumet... |
| ρl | 800.72 | kg/m3 | 311.65 | Volumet... |
| ρl | 800.27 | kg/m3 | 312.15 | Volumet... |
| ρl | 799.82 | kg/m3 | 312.65 | Volumet... |
| ρl | 799.38 | kg/m3 | 313.15 | Volumet... |
| ρl | 798.93 | kg/m3 | 313.65 | Volumet... |
| ρl | 798.48 | kg/m3 | 314.15 | Volumet... |
| ρl | 798.04 | kg/m3 | 314.65 | Volumet... |
| ρl | 797.59 | kg/m3 | 315.15 | Volumet... |
| ρl | 797.14 | kg/m3 | 315.65 | Volumet... |
| ρl | 796.69 | kg/m3 | 316.15 | Volumet... |
| ρl | 796.25 | kg/m3 | 316.65 | Volumet... |
| ρl | 795.80 | kg/m3 | 317.15 | Volumet... |
| ρl | 795.35 | kg/m3 | 317.65 | Volumet... |
| ρl | 794.90 | kg/m3 | 318.15 | Volumet... |
| ρl | 794.45 | kg/m3 | 318.65 | Volumet... |
| ρl | 794.01 | kg/m3 | 319.15 | Volumet... |
| ρl | 793.56 | kg/m3 | 319.65 | Volumet... |
| ρl | 793.11 | kg/m3 | 320.15 | Volumet... |
| ρl | 792.66 | kg/m3 | 320.65 | Volumet... |
| ρl | 792.21 | kg/m3 | 321.15 | Volumet... |
| ρl | 791.76 | kg/m3 | 321.65 | Volumet... |
| ρl | 791.31 | kg/m3 | 322.15 | Volumet... |
| ρl | 790.86 | kg/m3 | 322.65 | Volumet... |
| ρl | 790.41 | kg/m3 | 323.15 | Volumet... |
| ρl | 789.96 | kg/m3 | 323.65 | Volumet... |
| ρl | 789.52 | kg/m3 | 324.15 | Volumet... |
| ρl | 789.06 | kg/m3 | 324.65 | Volumet... |
| ρl | 788.62 | kg/m3 | 325.15 | Volumet... |
| ρl | 788.17 | kg/m3 | 325.65 | Volumet... |
| ρl | 787.72 | kg/m3 | 326.15 | Volumet... |
| ρl | 787.26 | kg/m3 | 326.65 | Volumet... |
| ρl | 786.81 | kg/m3 | 327.15 | Volumet... |
| ρl | 786.36 | kg/m3 | 327.65 | Volumet... |
| ρl | 785.91 | kg/m3 | 328.15 | Volumet... |
| ρl | 785.46 | kg/m3 | 328.65 | Volumet... |
| ρl | 785.01 | kg/m3 | 329.15 | Volumet... |
| ρl | 784.56 | kg/m3 | 329.65 | Volumet... |
| ρl | 784.11 | kg/m3 | 330.15 | Volumet... |
| ρl | 783.65 | kg/m3 | 330.65 | Volumet... |
| ρl | 783.20 | kg/m3 | 331.15 | Volumet... |
| ρl | 782.75 | kg/m3 | 331.65 | Volumet... |
| ρl | 782.30 | kg/m3 | 332.15 | Volumet... |
| ρl | 781.84 | kg/m3 | 332.65 | Volumet... |
| ρl | 781.39 | kg/m3 | 333.15 | Volumet... |
| ρl | 780.94 | kg/m3 | 333.65 | Volumet... |
| ρl | 780.49 | kg/m3 | 334.15 | Volumet... |
| ρl | 780.03 | kg/m3 | 334.65 | Volumet... |
| ρl | 779.58 | kg/m3 | 335.15 | Volumet... |
| ρl | 779.12 | kg/m3 | 335.65 | Volumet... |
| ρl | 778.67 | kg/m3 | 336.15 | Volumet... |
| ρl | 778.22 | kg/m3 | 336.65 | Volumet... |
| ρl | 777.76 | kg/m3 | 337.15 | Volumet... |
| ρl | 777.31 | kg/m3 | 337.65 | Volumet... |
| ρl | 776.85 | kg/m3 | 338.15 | Volumet... |
| ρl | 776.40 | kg/m3 | 338.65 | Volumet... |
| ρl | 775.94 | kg/m3 | 339.15 | Volumet... |
| ρl | 775.49 | kg/m3 | 339.65 | Volumet... |
| ρl | 775.03 | kg/m3 | 340.15 | Volumet... |
| ρl | 774.57 | kg/m3 | 340.65 | Volumet... |
| ρl | 774.11 | kg/m3 | 341.15 | Volumet... |
| ρl | 773.66 | kg/m3 | 341.65 | Volumet... |
| ρl | 773.20 | kg/m3 | 342.15 | Volumet... |
| ρl | 772.74 | kg/m3 | 342.65 | Volumet... |
| ρl | 772.29 | kg/m3 | 343.15 | Volumet... |
| ρl | 771.83 | kg/m3 | 343.65 | Volumet... |
| ρl | 771.37 | kg/m3 | 344.15 | Volumet... |
| ρl | 770.91 | kg/m3 | 344.65 | Volumet... |
| ρl | 770.45 | kg/m3 | 345.15 | Volumet... |
| ρl | 769.99 | kg/m3 | 345.65 | Volumet... |
| ρl | 769.53 | kg/m3 | 346.15 | Volumet... |
| ρl | 769.08 | kg/m3 | 346.65 | Volumet... |
| ρl | 768.62 | kg/m3 | 347.15 | Volumet... |
| ρl | 768.16 | kg/m3 | 347.65 | Volumet... |
| ρl | 767.70 | kg/m3 | 348.15 | Volumet... |
| ρl | 767.24 | kg/m3 | 348.65 | Volumet... |
| ρl | 766.78 | kg/m3 | 349.15 | Volumet... |
| ρl | 766.32 | kg/m3 | 349.65 | Volumet... |
| ρl | 765.86 | kg/m3 | 350.15 | Volumet... |
| ρl | 765.40 | kg/m3 | 350.65 | Volumet... |
| ρl | 764.94 | kg/m3 | 351.15 | Volumet... |
| ρl | 764.48 | kg/m3 | 351.65 | Volumet... |
| ρl | 764.02 | kg/m3 | 352.15 | Volumet... |
| ρl | 763.56 | kg/m3 | 352.65 | Volumet... |
| ρl | 763.10 | kg/m3 | 353.15 | Volumet... |
| ρl | 762.64 | kg/m3 | 353.65 | Volumet... |
| ρl | 762.17 | kg/m3 | 354.15 | Volumet... |
| ρl | 761.71 | kg/m3 | 354.65 | Volumet... |
| ρl | 761.25 | kg/m3 | 355.15 | Volumet... |
| ρl | 760.79 | kg/m3 | 355.65 | Volumet... |
| ρl | 760.33 | kg/m3 | 356.15 | Volumet... |
| ρl | 759.86 | kg/m3 | 356.65 | Volumet... |
| ρl | 759.40 | kg/m3 | 357.15 | Volumet... |
| ρl | 758.94 | kg/m3 | 357.65 | Volumet... |
| ρl | 758.48 | kg/m3 | 358.15 | Volumet... |
| ρl | 758.01 | kg/m3 | 358.65 | Volumet... |
| ρl | 757.55 | kg/m3 | 359.15 | Volumet... |
| ρl | 757.08 | kg/m3 | 359.65 | Volumet... |
| ρl | 756.62 | kg/m3 | 360.15 | Volumet... |
| ρl | 756.15 | kg/m3 | 360.65 | Volumet... |
| ρl | 755.69 | kg/m3 | 361.15 | Volumet... |
| ρl | 755.22 | kg/m3 | 361.65 | Volumet... |
| ρl | 754.75 | kg/m3 | 362.15 | Volumet... |
| ρl | 754.28 | kg/m3 | 362.65 | Volumet... |
| ρl | 753.82 | kg/m3 | 363.15 | Volumet... |
| ΔfusS | 63.70 | J/mol×K | 194.43 | NIST |
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==)
![N,N-Bis[(hydroxyethyl)trimethylene]diamine.](data:image/png;base64,iVBORw0KGgoAAAANSUhEUgAAAPoAAAD6CAIAAAAHjs1qAAASgUlEQVR4nO3de1BU5x3G8YdLAM0qKhrximI0olis1mqKGmJo0lgadYyAGggmduM4RtOOk21tOvbiTFbTmGhq6qLGWG/VkASJxnS8UW8hRqyJN/CaBCEWCYJ44f7rH0cXQZbL7sLZ3ff5jP94XM6+znw9vufse/Z4iQiI1OCt9wCIWg9zJ4Uwd1IIcyeFMHdSCHMnhTB3UghzJ4Uwd1IIcyeFMHdSCHMnhTB3UghzJ4Uwd1IIcyeFMHdSCHMnhTB3UghzJ4Uwd1IIcyeFMHdSCHMnhTB3UghzJ4Uwd1IIcyeFMHdSCHMnhTB3UghzJ4Uwd1IIcyeFMHdSCHMnhTB3UghzJ4Uwd1IIcyeFMHdSCHMnhTB3UghzJ4Uwd1IIcyeFMHdSCHMnhTB3UghzJ4Uwd1IIcyeFMHdSCHMnhTB3UghzJ4Uwd1IIcyeFMHdSCHMnhTB3UghzJ4Uwd1IIcyeFMHdSCHOnBv3vf5g9GyEh6NQJjzyCBQtw8yYAvP46nn++1is3bsTjj+syxqbz1XsA5MKKizFmDDp0gMWCPn1w6hTmz8ehQ9izBwUFyM2t++JvvtFnnE3G3Mm2t99GURGOHYPBAAADByIiAmFh2LJF75HZiZMZsm3nTsTG3mld8/DDiIrCp5/qNyaH8OhOtuXkYPLkuhv79kV2NoKDkZGB8PCa7YWF8PdvzdHZgbmTbQ88gLKyuhtLS+HnBwADB2Lp0prtqan4+OPWG5tdmDvZNmAAsrLqbjxzBiNHAkCHDhg7tmb7yZOtNzB7ce5OtsXFISUFFy/WbNmzB0ePIj5evzE5hEd3si0pCR99hJEj8cor6NsXJ05g2TLMm4fRo11/3lIv5k62+fhg2zZs2IDt27FvH7p2xebNmDABAEaMQHBwrRcPHIhnn9VlmE3nJSJ6j4Fcm/bhUUgIvLx0HonDOHenxvzpT+jbF6tW6T0OJ2Du1Bjt4szAgXqPwwk4maHGdOyIoiLk56NLF72H4ige3alB33+PoiJ06uQBrYO5UyO0mUxYmN7jcA7mTg3yoIk7mDs1IjsbAB55RO9xOAdzpwadOQPw6E6K8KzJDC9Ekm23bqFdO/j64uZN+HrCehMe3cm2rCxUV6N/f89oHcydGuJZMxkwd2qIdlnGg3L3kP+kqCUkFxa2Hzv20aFDQ/QeibPw6E42rdi/f+r+/Vf79NF7IE7DKzNUv+rqaoPBUFpaWlRU1L59e72H4xw8ulP9vvnmm9u3b/fo0cNjWgdzJ1uysrIADPSg81Qwd7KFuZNCsrOzATziKYvDNMyd6sejOynEI3PnhUiqR2FhYVBQkMFguH79upf7f9+GFY/uVA/rod2TWgdzp3p55EwGzJ3q5ZGXZcAlYlRHXl7e+vXrV61aZTAYPO/oztwJAMrLy9PS0tasWbNr166qqioAb7755qRJk/Qel5PxyozqsrKy3n///bVr1+bn5wPw9/d/5plnEhISxo8f7+Pjo/fonIxHd0Vdv349NTV1/fr1u3fv1rYMGjQoMTHxhRde6OIRXxhWL+aunMzMzOTk5E2bNt24cQNAYGBgXFxcQkLC6NGj9R5ai2Puqrhy5cqWLVtWr1598u5DlIYPH240GqdPn/7ggw/qO7ZWw9w9XFVV1b59+5KTk1NTUysqKgB07949ISFh5syZDz/8sN6ja208VfVYZ8+e3bRp03vvvZeTkwPAx8fn8ccfNxqNkyZN8vWUL9JoLkX/2h6stLT0k08+SU5O3rNnj3YsGzhwYFJS0owZMx566CG9R6cz5u45tHPQzZs3l5SUAGjXrt3EiRMTExOfeOIJD1v6Yjfm7vauXbv2wQcfvPvuu1999ZW2RTsHnTZtmsFg0Hdsroa5u6vq6uq9e/cmJydv27atvLwcQHBwcGxs7MyZM4cMGaL36FwUT1XdVXp6+rhx40TEeg46ceLEBx54QO9xuTTm7pYKCgq6dOnSpk2bhQsXJiYmduvWTe8RuQdOZtySth59yJAhJpNJ77G4E653d0ueevtFS2PubslTb79oaczdLfHobh/m7paYu314Zcb9lJeXa2sYb9y44e/vr/dw3AmP7u7n7NmzlZWVoaGhbL25mLv74UzGbszd/TB3uzWe+6pVsFhqbUlNxV//WvdlmZl46SVkZNRsOXAAf/yj4yOkurTceRXSDo3nvn8//vOfWlv++1/s2FH3ZRcvIjkZzz+PsrI7W86cwb/+5ZRBUi08utvNmZOZrl3h54e//c2Ju6S6RISfMdnNmWtmfHzw1lt45hnEx6NfPyfumGrk5ZX/5CfzfHwuBwUF6T0W99Ok3L/8Ei+9VPPbzEybDw2PjsaTT2LOHOzc6YzR0X1On/ZPT180dqze43BPTcr9wQcRcs+TZM+fx82bNl+8bBkGDUJKisNDo/p43HPbW1WTch80CAsW1Py2rAz//rfNF4eE4A9/wPz5+O1vHR4d3Ud7bjvn7fZpkevu8+cjIAArVrTEvlXHo7sjHMr98GHExyM+HpmZtbb7+eHvf8fZswBQXY3Zs3H3pmFyFHN3ROO5BwcjOLjWlqAg9OoFEaxdizfewKJFmD4dBgN69655TXQ0fv1r9OoFiwX/+AciI7F1q7PHrp6SEuTlISCg1qkUNYM4Q2ioVFfX/0elpfLiiwKIl5eYTFJZ6ZQ3VNSRIwLIj36k9zjclhPm7h9+iDFjYOt7e/z9sXo1LBb4+mLxYsTE4No1x99TUZzJOMjR3Pftw/LlWLaskZcZjdizB1274rPP8NOf4tQpB99WUdplGeZuN/tzF8HSpXjtNSxfjh9+QEVFI68fMwZHj2LECJw/j1Gj8PHHdr+zc2RmZs6ePXv9+vUrV67UeShNph3deRXSfnZPg0pKxGis+ZWf36Sfun1bEhNrpvJVVXa/v52uXbtmsViGDRum/fU7duwIICEh4datW609lOYbPFgAyczUexxuyzmnqs1lsYivrwASEyNFRa3xjlVVVQcOHDAajW3btrWGbjQaly1bFhgYCGDo0KGXLl1qjaHYq7JS/P3Fy0tKSvQeitvSJ3cR2blTOnYUQAYPlgsXClvujS5fvmw2m0NDQ7XKvb29o6Oj161bZz2cZ2VlaYtpO3fuvHfv3pYbiYPOnhVAevfWexzuTLfcReT8eQkPl1GjUgIDA9PS0py789LS0q1bt8bExFgfH9ezZ0+TyVTvIfyHH3548sknAfj6+prNZueOxFkqKiQ7Ww4e1Hsc7kzP3EXk+nWJjZ0GwMfHZ8mSJU7Z56lTp0wmk/Xxcf7+/lOmTNm1a1e1rY8GRESksrLSZDJp34PuUlP5hQslKUlKS2u2zJ8v27frNyB3pnPuIlJdXW02m729vQHExcXdvHnTvv0UFRVZLJbIyEjrWfigQYPMZvPVq1ebvpPNmzdrk/tHH300Ly/PvpE4V1SUAPKXv9RsiYiQpUv1G5A70z93zY4dO7RTxoiIiIsXLzbrZ48ePWo0Gq2PjwsMDDQajZn2Xr84fvx4nz59AHTv3v3zzz+3bydOFBUlMTHSpo2cO3dnC3O3m6vkLiLZ2dlhYWEAgoKCdu/e3ejrc3NzzWaz9fFx3t7ekZGRFovF7v8frAoKCsaNG6dNhFavXu3g3hwUFSWLFsnUqfLzn9/Zwtzt5kK5i0hxcfGECRMaPmWsrKzctWvXlClTrI+P69Gjh8lkunDhghNHUlFRYf0uaaPRWF5e7sSdN4uWe06OGAyyaZMIc3eAa+Uud6fy2inj9OnT7z1lPHPmjMlksj4+zs/PLyYmZuvWrRUVFS00mA0bNrRp0wbAmDFjrly50kLvYov2GZyWu4i88YYEB8v168zdfi6Xu2bLli3aXHzYsGGnT59et25ddHS09fFxYWFhZrM5v4kf5DomMzOzd+/e2nXMI0eOtMI7isjJk2IySUiIFBfX5F5eLoMHi8nE3O3normLyPHjx/v27QvA+jloYGDgrFmzWq05q/z8/MceewxAQEDAunXrWu6NCgvlnXdk6FAB7vxKSanJXUTS0yUgQLp2Ze52ct3cReTq1atxcXGzZs0aPny4xWK5ceOGXiMpLS2dOXOmdSrv3OlTVZUcOCBGo7Rte6fyDh3EaJRjx0SkVu4i8txzAsjSpZKRIVOnckFB87h07pqq1l9HZoPFYvHz8wPw1FNPFRY6YeHD5ctiNkto6J3Kvb0lOlrWrZN7P+MyGmXNmprfXrkio0bJhg13louFh9dcoKRGuUHuLuXgwYPBwcEA+vXrd+LECft2UlYmaWkyZcqddXKA9OwpJpM06/OGc+ckPFwAad9enL0Cw2Mx92a7fPnyiBEjABgMhpSUlGb97Ndffz1v3rzo6GVa5QEBMnWq7Npl50LokhKZPFkA8fERs9nm/ZNkxdztcfv27aSkJABeXl4mk6nR6VZRUdHKlSu1fyQAfH0DoqLK3nlHHJ8QVVeL2Sze3gJIXJw4/Ambh2Pu9rNYLNpTqsePH3/t2rV6X1PvAocDBw44dyTbt0tgoAASEdG8GZHTFRQUvP3221FRUStWrPjiiy/0HEp9mLtD0tPTtY+9BgwYcPr0aev2vLw8s9ncv39/rXIvLy9tgUPLXVzKzpawMAEkKEiasALDyaqqqj777LPY2Fjr83O8vb0DAgLWrl3b2kNpEHN31HfffTd8+HAA7dq1++ijj7QFDtpRX1tnZjKZzp8/3wojKS6WCRMEEF9fabVF+zk5OWazWfuExHr3zObNm+fPn+8KSzDqYO5OUFJSMnnyZG1JmXWBw7PPPrtz587K1v1incpK+d3vxMtLAHn55fzSe5fJO9X9d8/06tWrzt0z69ev13EJRr2Yu3NUV1cvWrRoyZIl4eHhb731VrMW2Tvdli3SqdPtwYN/OmzYsG+//da5O9fununcubNWeUBAQAN3z9y7BOPLL7907kjswNw909dfX9BW7Xfr1u3w4cOO79DW3TMFBQUN/2Bubu6oUaNaYQlGUzB3j1VQUBAdHa3NrFatWmXfTu7/BocOHToYjcZj2gqHprl3CcbcuXNbeYJ3L+buybQbcK2njGVlZU3/We3umX53nzpk/QYHu++ecfoSDDswd8+3ceNG7dgcGRn5/fffN/zisrKytLS0+++eae4dlfVKT0/XbpmP+vGPq0+dcnyHzcXclXDs2LGQkBCtXVuf/pw+ffreu2e0b3BIS0tz7twjJyfn0ZEjr4wYIQaDNHMJhuOYuyquXr0aFRWlnTLe++lPcXGxdvdMnXPQlrt7purWLZk27c43Jy5c2JprfZi7QioqKubOnWudymdkZBiNRoPB0KILHGyyfnPiL3/ZSt+cyNwVtHLlSu2U0brAYdy4cRs2bNDhm6TS06VLFwFkwAC5ZwlGy/ESEZBiDh48uG/fvm3btj399NMzZsywfoGmDi5cwKRJOHEC7dvjn//EhAkt+m7MnfR24wZmzEBKCry88OqreP11m4+CcViLPGiSqBkMBmzdCrMZXl5YvBjx8Q09pdoxPLqTy/jkEzz3HK5fR0QEPv0U3bs7/R2YO7mSc+cwcSL8/HDoENq2RWEh3n0Xhw6hogKhoXjxRYwcCQCvvYaICEyZUvODy5fD2xtz5jS8e05myJX074/Dh7FjB9q2RW4uhg3Dhx9i/HgkJqKyEpGRWLsWAHbvxsmTtX4wIwNffNHo7n1bZtRE9goMRGAgALz6Ktq3R0YGtLsIEhPRrx/mzMGvfmX3vnl0J5dUUYHUVLz8Mu7eMQMAv/kNqqqwY4fde+XRnVxSbi5u3ar7TM22bdGzJy5cAIDUVFy6VPNHGRm4Zy2+LcydXJj3fbMPX19oF1e6dcPdp4UCaOKTqZk7uaTgYPj54dIljB5ds7GyEt99hz59AGDkSLzySs0fHTnSlL1y7k4uKSAA0dFYs6bWxo0bUVmJX/zC7r3y6E6uavFi/OxniI/HnDno0AF79+L3v8eCBejRw+5dMndyVeHh+Pxz/PnPiI1FWRkGDMCKFUhKAoD+/REcXOvFISH1TPTvw09VSSGcu5NCmDsphLmTQpg7KYS5k0KYOymEuZNCmDsphLmTQpg7KYS5k0KYOymEuZNCmDsphLmTQpg7KYS5k0KYOymEuZNCmDsphLmTQpg7KYS5k0KYOymEuZNCmDsphLmTQpg7KYS5k0KYOymEuZNCmDsphLmTQpg7KYS5k0KYOymEuZNCmDsphLmTQpg7KYS5k0KYOymEuZNCmDsphLmTQpg7KYS5k0KYOymEuZNCmDsphLmTQpg7KYS5k0KYOymEuZNCmDsphLmTQpg7KYS5k0KYOymEuZNCmDsphLmTQpg7KYS5k0L+D52Gu3fta0QRAAAAAElFTkSuQmCC)
Find more compounds similar to 1,3-Propanediamine, N,N-dimethyl-.
Mixtures
Sources
- Crippen Method
- Crippen Method
- 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
- Volumetric properties of the water + 3-(dimethylamino) propylamine (DMAPA) mixture at atmospheric pressure from 283.15 to 353.15K
- Density, Speed of Sound, Viscosity and Surface Tension of 3-Dimethylamino-1-propylamine + Water, 3-Amino-1-propanol + 3-Dimethylamino-1-propanol, and (3-Amino-1-propanol + 3-Dimethylamino-1-propanol) + Water from T = (293.15 to 323.15) K
- Joback Method
- McGowan Method
- NIST Webbook
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