- InChI
- InChI=1S/C5H13NO/c1-6(2)4-3-5-7/h7H,3-5H2,1-2H3
- InChI Key
- PYSGFFTXMUWEOT-UHFFFAOYSA-N
- Formula
- C5H13NO
- SMILES
- CN(C)CCCO
- Molecular Weight1
- 103.16
- CAS
- 3179-63-3
- Other Names
-
- 1-(Dimethylamino)propan-3-ol
- 1-Dimethylamino-3-propanol
- 3-(Dimethlyamino)propanol
- 3-(Dimethylamino)-1-propanol
- 3-(Dimethylamino)propanol
- 3-(N,N-Dimethylamino)-1-propanol
- 3-(N,N-Dimethylamino)propanol
- 3-(dimethylamino)propan-1-ol
- 3-dimethylamino-1-propanol
- 3-dimethylaminopropan-1-ol
- Dimethylaminopropanol
- Dimethylpropanolamine
- N,N-Dimethyl-3-hydroxypropylamine
- N,N-Dimethyl-«gamma»-aminopropanol
- N,N-Dimethyl-«gamma»-aminopropanol
- N,N-Dimethylaminopropanol
- N,N-Dimethylpropanolamine
- NSC 62086
- «gamma»-(Dimethylamino)propanol
- «gamma»-(Dimethylamino)propanol
- 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).
- 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).
- γ : Surface Tension (N/m).
- Tboil : Normal Boiling Point Temperature (K).
- Tboil : Boiling point at given pressure (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 |
|---|---|---|---|
| ΔfG° | -34.82 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -231.23 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 15.81 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 45.45 | kJ/mol | Joback Calculated Property |
| IE | 8.74 ± 0.04 | eV | NIST |
| log10WS | 0.25 | Crippen Calculated Property | |
| logPoct/wat | -0.070 | Crippen Calculated Property | |
| McVol | 97.160 | ml/mol | McGowan Calculated Property |
| Pc | 3867.48 | kPa | Joback Calculated Property |
| Tboil | [436.50; 436.70] | K |
|
| Tboil | 436.70 | K | NIST |
| Tboil | 436.50 ± 0.50 | K | NIST |
| Tc | 578.89 | K | Joback Calculated Property |
| Tfus | 239.40 | K | Joback Calculated Property |
| Vc | 0.352 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [197.87; 248.97] | J/mol×K | [418.42; 578.89] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 200 210 220 230 240 250 450 500 550 | ||||
| Cp,gas | 197.87 | J/mol×K | 418.42 | Joback Calculated Property |
| Cp,gas | 207.30 | J/mol×K | 445.16 | Joback Calculated Property |
| Cp,gas | 216.34 | J/mol×K | 471.91 | Joback Calculated Property |
| Cp,gas | 225.02 | J/mol×K | 498.65 | Joback Calculated Property |
| Cp,gas | 233.35 | J/mol×K | 525.40 | Joback Calculated Property |
| Cp,gas | 241.33 | J/mol×K | 552.14 | Joback Calculated Property |
| Cp,gas | 248.97 | J/mol×K | 578.89 | Joback Calculated Property |
| Pvap | [7.00e-03; 2.31] | kPa | [283.15; 373.10] |
|
|
T(K) Vapor pressure (kPa) 0 0.5 1 1.5 2 2.5 300 320 340 360 | ||||
| Pvap | 7.00e-03 | kPa | 283.15 | Investi... |
| Pvap | 0.02 | kPa | 293.14 | Investi... |
| Pvap | 0.03 | kPa | 303.09 | Investi... |
| Pvap | 0.07 | kPa | 313.08 | Investi... |
| Pvap | 0.14 | kPa | 323.28 | Investi... |
| Pvap | 0.26 | kPa | 333.12 | Investi... |
| Pvap | 0.47 | kPa | 343.12 | Investi... |
| Pvap | 1.42 | kPa | 363.17 | Investi... |
| Pvap | 2.31 | kPa | 373.10 | Investi... |
| ρl | [846.70; 886.70] | kg/m3 | [293.15; 343.15] |
|
|
T(K) Liquid Density (kg/m3) 850 860 870 880 890 300 320 340 | ||||
| ρl | 886.70 | kg/m3 | 293.15 | Densiti... |
| ρl | 885.00 | kg/m3 | 293.15 | Volumet... |
| ρl | 883.00 | kg/m3 | 298.15 | Densiti... |
| ρl | 881.00 | kg/m3 | 298.15 | Volumet... |
| ρl | 880.82 | kg/m3 | 298.15 | Density... |
| ρl | 877.00 | kg/m3 | 303.15 | Volumet... |
| ρl | 879.10 | kg/m3 | 303.15 | Densiti... |
| ρl | 875.10 | kg/m3 | 308.15 | Densiti... |
| ρl | 869.00 | kg/m3 | 313.15 | Volumet... |
| ρl | 871.20 | kg/m3 | 313.15 | Densiti... |
| ρl | 867.20 | kg/m3 | 318.15 | Densiti... |
| ρl | 863.10 | kg/m3 | 323.15 | Densiti... |
| ρl | 860.00 | kg/m3 | 323.15 | Volumet... |
| ρl | 859.10 | kg/m3 | 328.15 | Densiti... |
| ρl | 855.00 | kg/m3 | 333.15 | Densiti... |
| ρl | 850.80 | kg/m3 | 338.15 | Densiti... |
| ρl | 846.70 | kg/m3 | 343.15 | Densiti... |
| γ | [0.03; 0.03] | N/m | [298.15; 333.15] |
|
|
T(K) Surface Tension (N/m) 0.03 0.03 0.03 0.03 0.03 0.03 300 310 320 330 | ||||
| γ | 0.03 | N/m | 298.15 | Volumet... |
| γ | 0.03 | N/m | 303.15 | Volumet... |
| γ | 0.03 | N/m | 308.15 | Volumet... |
| γ | 0.03 | N/m | 313.15 | Volumet... |
| γ | 0.03 | N/m | 318.15 | Volumet... |
| γ | 0.03 | N/m | 323.15 | Volumet... |
| γ | 0.03 | N/m | 333.15 | Volumet... |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboil | [352.30; 433.70] | K | [4.80; 99.80] |
|
|
P(kPa) Boiling point at given pressure (K) 360 380 400 420 440 50 100 | ||||
| Tboil | 352.30 | K | 4.80 | Vapour-... |
| Tboil | 352.90 | K | 4.80 | Vapour-... |
| Tboil | 368.30 | K | 9.80 | Vapour-... |
| Tboil | 378.50 | K | 14.80 | Vapour-... |
| Tboil | 378.50 | K | 14.80 | Vapour-... |
| Tboil | 385.80 | K | 19.80 | Vapour-... |
| Tboil | 396.80 | K | 29.80 | Vapour-... |
| Tboil | 405.00 | K | 39.80 | Vapour-... |
| Tboil | 411.60 | K | 49.80 | Vapour-... |
| Tboil | 417.20 | K | 59.80 | Vapour-... |
| Tboil | 421.70 | K | 69.80 | Vapour-... |
| Tboil | 426.30 | K | 79.80 | Vapour-... |
| Tboil | 429.90 | K | 89.80 | Vapour-... |
| Tboil | 433.70 | K | 99.80 | Vapour-... |
| Tboilr | 347.50 ± 1.50 | K | 4.40 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [0.24; 202.66] | kPa | [302.99; 500.71] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.35176e+01 | |||
| Coefficient B | -3.59566e+03 | |||
| Coefficient C | -6.25390e+01 | |||
| Temperature range, min. | 302.99 | |||
| Temperature range, max. | 500.71 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 300 400 500 | ||||
| Pvap | 0.24 | kPa | 302.99 | Calculated Property |
| Pvap | 0.83 | kPa | 324.96 | Calculated Property |
| Pvap | 2.40 | kPa | 346.93 | Calculated Property |
| Pvap | 5.93 | kPa | 368.90 | Calculated Property |
| Pvap | 13.01 | kPa | 390.87 | Calculated Property |
| Pvap | 25.87 | kPa | 412.83 | Calculated Property |
| Pvap | 47.40 | kPa | 434.80 | Calculated Property |
| Pvap | 81.20 | kPa | 456.77 | Calculated Property |
| Pvap | 131.41 | kPa | 478.74 | Calculated Property |
| Pvap | 202.66 | kPa | 500.71 | Calculated Property |
Similar Compounds
Find more compounds similar to 1-Propanol, 3-(dimethylamino)-.
Mixtures
- 1-Propanol, 3-(dimethylamino)- + Water
- Carbon dioxide + 1-Propanol, 3-(dimethylamino)- + Water
- 1-Propanol, 3-(dimethylamino)- + Dimethyl Sulfoxide
- 1-Propanol, 3-(dimethylamino)- + 1,3-Propanediamine, N-methyl- + Water
- 1-Propanol, 3-(dimethylamino)- + 1-Propanol, 3-amino- + Water
- 1-Propanol, 3-(dimethylamino)- + 1-Propanol, 3-amino-
- Ethanol, 2-(ethylamino)- + 1-Propanol, 3-(dimethylamino)- + Water
Sources
- Crippen Method
- Crippen Method
- Investigation of the isothermal (vapour + liquid) equilibria of aqueous 2-amino-2-methyl-1-propanol (AMP), N-benzylethanolamine, or 3-dimethylamino-1-propanol solutions at several temperatures
- Excess molar enthalpies for binary mixtures of different amines with water
- Densities of unloaded and CO2-loaded 3-dimethylamino-1-propanol at temperatures (293.15 to 343.15) K
- Volumetric, acoustic and transport properties of mixtures containing dimethyl sulfoxide and some amines or alkanolamines: Measurement and correlation
- CO2 absorption with aqueous tertiary amine solutions: Equilibrium solubility and thermodynamic modeling
- Experiment and model for the viscosity of carbonated 3-(dimethylamino)propan-1-ol and 2-(ethylamino)ethanol blended aqueous solutions
- Vapour-liquid equilibrium study of tertiary amines, single and in blend with 3-(methylamino)propylamine, for post-combustion CO2 capture
- Absorption capacity and CO2 removal efficiency in tray tower by using 2-(ethylamino)ethanol activated 3-(dimethylamino)propan-1-ol aqueous solution
- Volumetric Properties, Viscosities, Refractive Indices and Surface Tensions for Aqueous N, ndimethylpropanolamine (DMPA) Solutions From 298.15 K to 343.15 K
- 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
- The Yaws Handbook of Vapor Pressure
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