- InChI
- InChI=1S/C3H9NO/c4-2-1-3-5/h5H,1-4H2
- InChI Key
- WUGQZFFCHPXWKQ-UHFFFAOYSA-N
- Formula
- C3H9NO
- SMILES
- NCCCO
- Molecular Weight1
- 75.11
- CAS
- 156-87-6
- Other Names
-
- 1,3-Propanolamine
- 1-Amino-3-hydroxypropane
- 1-Amino-3-propanol
- 3-Amino-1-propanol
- 3-Aminopropanol
- 3-Aminopropanol-(1)
- 3-Aminopropyl alcohol
- 3-Hydroxy-1-aminopropane
- 3-Hydroxy-1-propylamine
- 3-Hydroxypropylamine
- 3-Propanolamine
- 3-aminopropan-1-ol
- NH2(CH2)3OH
- NSC 7766
- Propanolamine
- «beta»-Alaninol
- «gamma»-Aminopropanol
- «beta»-Alaninol
- «gamma»-Aminopropanol
- PAff : Proton affinity (kJ/mol).
- BasG : Gas basicity (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,liquid : Liquid phase heat capacity (J/mol×K).
- η : Dynamic viscosity (Pa×s).
- 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).
- ΔfusH : Enthalpy of fusion at a given temperature (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).
- Inp : Non-polar retention indices.
- I : Polar retention indices.
- csound,fluid : Speed of sound in fluid (m/s).
- γ : Surface Tension (N/m).
- 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 |
|---|---|---|---|
| PAff | [936.00; 962.50] | kJ/mol |
|
| PAff | 962.50 | kJ/mol | NIST |
| PAff | 945.30 | kJ/mol | NIST |
| PAff | 936.00 | kJ/mol | NIST |
| PAff | 953.50 ± 1.60 | kJ/mol | NIST |
| BasG | [903.80; 921.30] | kJ/mol |
|
| BasG | 917.30 | kJ/mol | NIST |
| BasG | 912.50 | kJ/mol | NIST |
| BasG | 903.80 | kJ/mol | NIST |
| BasG | 921.30 ± 1.20 | kJ/mol | NIST |
| ΔfG° | -95.99 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -223.69 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 12.81 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 49.59 | kJ/mol | Joback Calculated Property |
| IE | [9.00; 9.77] | eV |
|
| IE | 9.00 | eV | NIST |
| IE | 9.77 ± 0.20 | eV | NIST |
| log10WS | 0.22 | Crippen Calculated Property | |
| logPoct/wat | -0.672 | Crippen Calculated Property | |
| McVol | 68.980 | ml/mol | McGowan Calculated Property |
| Pc | 5430.51 | kPa | Joback Calculated Property |
| Inp | [740.00; 826.00] |
|
|
| Inp | 773.00 | NIST | |
| Inp | 770.00 | NIST | |
| Inp | 740.00 | NIST | |
| Inp | 785.00 | NIST | |
| Inp | 826.00 | NIST | |
| Inp | 785.00 | NIST | |
| Inp | 826.00 | NIST | |
| Inp | 773.00 | NIST | |
| I | [1534.00; 1577.00] |
|
|
| I | 1534.00 | NIST | |
| I | 1577.00 | NIST | |
| I | 1570.00 | NIST | |
| I | 1548.00 | NIST | |
| I | 1548.00 | NIST | |
| I | 1555.00 | NIST | |
| I | 1555.00 | NIST | |
| I | 1555.00 | NIST | |
| Tboil | [460.70; 461.00] | K |
|
| Tboil | 460.70 | K | NIST |
| Tboil | 461.00 | K | NIST |
| Tc | 609.84 | K | Joback Calculated Property |
| Tfus | [284.70; 285.55] | K |
|
| Tfus | 284.70 ± 0.35 | K | NIST |
| Tfus | 285.55 ± 0.20 | K | NIST |
| Vc | 0.252 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [142.17; 177.53] | J/mol×K | [432.75; 609.84] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 140 150 160 170 180 450 500 550 600 | ||||
| Cp,gas | 142.17 | J/mol×K | 432.75 | Joback Calculated Property |
| Cp,gas | 148.69 | J/mol×K | 462.26 | Joback Calculated Property |
| Cp,gas | 154.96 | J/mol×K | 491.78 | Joback Calculated Property |
| Cp,gas | 160.97 | J/mol×K | 521.29 | Joback Calculated Property |
| Cp,gas | 166.73 | J/mol×K | 550.81 | Joback Calculated Property |
| Cp,gas | 172.25 | J/mol×K | 580.32 | Joback Calculated Property |
| Cp,gas | 177.53 | J/mol×K | 609.84 | Joback Calculated Property |
| Cp,liquid | [204.00; 217.00] | J/mol×K | [303.15; 353.15] |
|
|
T(K) Liquid phase heat capacity (J/mol×K) 204 206 208 210 212 214 216 218 320 340 | ||||
| Cp,liquid | 204.00 | J/mol×K | 303.15 | Molar H... |
| Cp,liquid | 207.00 | J/mol×K | 308.15 | Molar H... |
| Cp,liquid | 208.00 | J/mol×K | 313.15 | Molar H... |
| Cp,liquid | 208.00 | J/mol×K | 318.15 | Molar H... |
| Cp,liquid | 209.00 | J/mol×K | 323.15 | Molar H... |
| Cp,liquid | 210.00 | J/mol×K | 328.15 | Molar H... |
| Cp,liquid | 211.00 | J/mol×K | 333.15 | Molar H... |
| Cp,liquid | 213.00 | J/mol×K | 338.15 | Molar H... |
| Cp,liquid | 214.00 | J/mol×K | 343.15 | Molar H... |
| Cp,liquid | 216.00 | J/mol×K | 348.15 | Molar H... |
| Cp,liquid | 217.00 | J/mol×K | 353.15 | Molar H... |
| η | [0.0022500; 0.0404200] | Pa×s | [293.15; 373.15] |
|
|
T(K) Dynamic viscosity (Pa×s) 0 5.00e-3 0.01 0.02 0.02 0.03 0.03 0.04 0.04 300 320 340 360 | ||||
| η | 0.0404200 | Pa×s | 293.15 | Experim... |
| η | 0.0392895 | Pa×s | 293.15 | Measure... |
| η | 0.0304336 | Pa×s | 298.15 | Measure... |
| η | 0.0304300 | Pa×s | 298.15 | Viscosi... |
| η | 0.0238680 | Pa×s | 303.15 | Experim... |
| η | 0.0238700 | Pa×s | 303.15 | Viscosi... |
| η | 0.0238679 | Pa×s | 303.15 | Measure... |
| η | 0.0190700 | Pa×s | 308.15 | Viscosi... |
| η | 0.0190712 | Pa×s | 308.15 | Measure... |
| η | 0.0152700 | Pa×s | 313.15 | Viscosi... |
| η | 0.0152660 | Pa×s | 313.15 | Experim... |
| η | 0.0152664 | Pa×s | 313.15 | Measure... |
| η | 0.0123545 | Pa×s | 318.15 | Measure... |
| η | 0.0123600 | Pa×s | 318.15 | Viscosi... |
| η | 0.0102200 | Pa×s | 323.15 | Viscosi... |
| η | 0.0102191 | Pa×s | 323.15 | Measure... |
| η | 0.0102190 | Pa×s | 323.15 | Experim... |
| η | 0.0085400 | Pa×s | 328.15 | Viscosi... |
| η | 0.0085347 | Pa×s | 328.15 | Measure... |
| η | 0.0071230 | Pa×s | 333.15 | Experim... |
| η | 0.0071234 | Pa×s | 333.15 | Measure... |
| η | 0.0071200 | Pa×s | 333.15 | Viscosi... |
| η | 0.0060500 | Pa×s | 338.15 | Viscosi... |
| η | 0.0060452 | Pa×s | 338.15 | Measure... |
| η | 0.0048400 | Pa×s | 343.15 | Viscosi... |
| η | 0.0041700 | Pa×s | 348.15 | Viscosi... |
| η | 0.0036300 | Pa×s | 353.15 | Viscosi... |
| η | 0.0031900 | Pa×s | 358.15 | Viscosi... |
| η | 0.0027300 | Pa×s | 363.15 | Viscosi... |
| η | 0.0025200 | Pa×s | 368.15 | Viscosi... |
| η | 0.0022500 | Pa×s | 373.15 | Viscosi... |
| ΔfusH | 16.90 | kJ/mol | 284.10 | NIST |
| ρl | [939.30; 987.80] | kg/m3 | [293.15; 353.15] |
|
|
T(K) Liquid Density (kg/m3) 940 950 960 970 980 990 300 320 340 | ||||
| ρl | 987.80 | kg/m3 | 293.15 | Density... |
| ρl | 987.50 | kg/m3 | 293.15 | Density... |
| ρl | 987.50 | kg/m3 | 293.15 | Volumet... |
| ρl | 987.65 | kg/m3 | 293.15 | Density... |
| ρl | 983.59 | kg/m3 | 298.15 | Density... |
| ρl | 984.30 | kg/m3 | 298.15 | Density... |
| ρl | 983.60 | kg/m3 | 298.15 | Density... |
| ρl | 980.30 | kg/m3 | 303.15 | Density... |
| ρl | 979.60 | kg/m3 | 303.15 | Density... |
| ρl | 979.65 | kg/m3 | 303.15 | Density... |
| ρl | 979.45 | kg/m3 | 303.15 | Volumet... |
| ρl | 976.20 | kg/m3 | 308.15 | Density... |
| ρl | 975.50 | kg/m3 | 308.15 | Density... |
| ρl | 971.61 | kg/m3 | 313.15 | Density... |
| ρl | 971.50 | kg/m3 | 313.15 | Density... |
| ρl | 971.67 | kg/m3 | 313.15 | Volumet... |
| ρl | 972.30 | kg/m3 | 313.15 | Density... |
| ρl | 967.50 | kg/m3 | 318.15 | Density... |
| ρl | 968.50 | kg/m3 | 318.15 | Density... |
| ρl | 963.36 | kg/m3 | 323.15 | Volumet... |
| ρl | 963.40 | kg/m3 | 323.15 | Density... |
| ρl | 963.52 | kg/m3 | 323.15 | Density... |
| ρl | 964.90 | kg/m3 | 323.15 | Density... |
| ρl | 959.30 | kg/m3 | 328.15 | Density... |
| ρl | 955.38 | kg/m3 | 333.15 | Density... |
| ρl | 955.80 | kg/m3 | 333.15 | Density... |
| ρl | 951.70 | kg/m3 | 338.15 | Density... |
| ρl | 947.60 | kg/m3 | 343.15 | Density... |
| ρl | 943.50 | kg/m3 | 348.15 | Density... |
| ρl | 939.30 | kg/m3 | 353.15 | Density... |
| csound,fluid | [1632.43; 1727.44] | m/s | [293.15; 323.15] |
|
|
T(K) Speed of sound in fluid (m/s) 1640 1660 1680 1700 1720 300 310 320 | ||||
| csound,fluid | 1727.44 | m/s | 293.15 | Density... |
| csound,fluid | 1712.25 | m/s | 298.15 | Density... |
| csound,fluid | 1696.24 | m/s | 303.15 | Density... |
| csound,fluid | 1680.79 | m/s | 308.15 | Density... |
| csound,fluid | 1664.67 | m/s | 313.15 | Density... |
| csound,fluid | 1648.51 | m/s | 318.15 | Density... |
| csound,fluid | 1632.43 | m/s | 323.15 | Density... |
| γ | [0.04; 0.04] | N/m | [298.15; 323.15] |
|
|
T(K) Surface Tension (N/m) 0.04 0.04 0.04 0.04 0.04 0.04 0.04 300 310 320 | ||||
| γ | 0.04 | N/m | 298.15 | Surface... |
| γ | 0.04 | N/m | 303.15 | Surface... |
| γ | 0.04 | N/m | 308.15 | Surface... |
| γ | 0.04 | N/m | 313.15 | Surface... |
| γ | 0.04 | N/m | 318.15 | Surface... |
| γ | 0.04 | N/m | 323.15 | Surface... |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.67] | kPa | [360.86; 483.82] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.65620e+01 | |||
| Coefficient B | -4.48126e+03 | |||
| Coefficient C | -8.55000e+01 | |||
| Temperature range, min. | 360.86 | |||
| Temperature range, max. | 483.82 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 400 450 | ||||
| Pvap | 1.33 | kPa | 360.86 | Calculated Property |
| Pvap | 2.88 | kPa | 374.52 | Calculated Property |
| Pvap | 5.79 | kPa | 388.18 | Calculated Property |
| Pvap | 10.98 | kPa | 401.85 | Calculated Property |
| Pvap | 19.74 | kPa | 415.51 | Calculated Property |
| Pvap | 33.87 | kPa | 429.17 | Calculated Property |
| Pvap | 55.77 | kPa | 442.83 | Calculated Property |
| Pvap | 88.50 | kPa | 456.50 | Calculated Property |
| Pvap | 135.91 | kPa | 470.16 | Calculated Property |
| Pvap | 202.67 | kPa | 483.82 | Calculated Property |
Similar Compounds
Find more compounds similar to 1-Propanol, 3-amino-.
Mixtures
- 1-Propanol, 2-methyl- + 1-Propanol, 3-amino-
- Isopropyl Alcohol + 1-Propanol, 3-amino-
- 1-Propanol, 3-amino- + Water
- Carbon dioxide + 1-Propanol, 3-amino- + Water
- 1-Propanol, 3-(dimethylamino)- + 1-Propanol, 3-amino- + Water
- 1-Propanol, 3-(dimethylamino)- + 1-Propanol, 3-amino-
- Ethanol + 1-Propanol, 3-amino-
- Diethanolamine + 1-Propanol, 3-amino- + Water
- Triethanolamine + 1-Propanol, 3-amino- + Water
- 1-Propanol, 3-amino- + Water + 1-Propanol, 2-amino-2-methyl-
- 1-Propanol + 1-Propanol, 3-amino-
- 1-Propanol, 3-amino- + 1-Propanol, 2-amino-2-methyl-
- Diethanolamine + 1-Propanol, 3-amino-
- Triethanolamine + 1-Propanol, 3-amino-
Sources
- Crippen Method
- Crippen Method
- Molar excess enthalpy (HEm) for various {alkanolamine (1) + water (2)} systems at T = (298.15, 313.15, and 323.15) K
- Measurement and modeling the excess molar properties of binary mixtures of {[C6mim][BF4] + 3-amino-1-propanol} and {[C6mim][BF4] + isobutanol}: Application of Prigogine-Flory-Patterson theory
- Experimental excess molar properties of binary mixtures of (3-amino-1-propanol + isobutanol, 2-propanol) at T = (293.15 to 333.15) K and modelling the excess molar volume by Prigogine-Flory-Patterson theory
- Low-temperature thermal properties of the aqueous solutions of simple aminoalcohols: Finding of peculiarities in 1-amino-2-propanol solutions
- Density Measurements of Unloaded and CO2-Loaded 3-Amino-1-propanol Solutions at Temperatures (293.15 to 353.15) 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
- Volumetric and Viscometric Properties of Alcohol Amines + Ethanol Binary Mixtures
- Viscosity Measurement and Correlation of Unloaded and CO2-Loaded 3-Amino-1-propanol Solution
- Density and Viscosity of 2-Butanol + (1-Propanol, 2-Propanol, or 3-Amino-1-propanol) Mixtures at Temperatures of (293.15 to 323.15) K: Application of the ERAS Model
- Surface Tension of aqueous vinary mixtures of 1-amino-2-propanol and 3-amino-1-propanol, and aqueous ternary mixtures of these amines with diethanolamine, triethanolamine, and 2-amino-2-methyl-1-propanol from (298.15 to 323.15) K
- Molar Heat Capacity of Various Aqueous Alkanolamine Solutions from 303.15 K to 353.15 K
- Density and Viscosity Measurements of Binary Alkanol Mixtures from (293.15 to 333.15) K at Atmospheric Pressure
- Density, Speed of Sound, Isentropic Compressibility, and Excess Volume of Binary Mixtures of 1-Amino-2-propanol or 3-Amino-1-propanol with 2-Amino-2-methyl-1-propanol, Diethanolamine, or Triethanolamine from (293.15 to 323.15) K
- Joback Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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