- InChI
- InChI=1S/C3H9N/c1-2-3-4/h2-4H2,1H3
- InChI Key
- WGYKZJWCGVVSQN-UHFFFAOYSA-N
- Formula
- C3H9N
- SMILES
- CCCN
- Molecular Weight1
- 59.11
- CAS
- 107-10-8
- Other Names
-
- 1-AMINOPROPANE
- 1-Propanamine
- 1-Propylamine
- MONOPROPYLAMINE
- Mono-n-propylamine
- NSC 7490
- PROPANAMINE
- Rcra waste number U194
- UN 1277
- n-C3H7NH2
- n-Propylamine
- propan-1-amine
- ω : Acentric Factor.
- 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).
- μ : Dipole Moment (debye).
- η : Dynamic viscosity (Pa×s).
- 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).
- 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).
- NFPA Fire : NFPA Fire Rating.
- NFPA Health : NFPA Health Rating.
- Pc : Critical Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- I : Polar retention indices.
- ΔfusS : Entropy of fusion at a given temperature (J/mol×K).
- S°liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
- 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).
- Ttriple : Triple Point Temperature (K).
- Vc : Critical Volume (m3/kmol).
- Vm : Molar Volume (m3/mol).
- Zc : Critical Compressibility.
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.3030 | KDB | |
| PAff | [907.10; 917.80] | kJ/mol |
|
| PAff | 917.80 | kJ/mol | NIST |
| PAff | 907.50 | kJ/mol | NIST |
| PAff | 907.10 | kJ/mol | NIST |
| BasG | 883.90 | kJ/mol | NIST |
| ΔcH°liquid | [-2365.00; -2344.00] | kJ/mol |
|
| ΔcH°liquid | -2365.00 ± 3.00 | kJ/mol | NIST |
| ΔcH°liquid | -2344.00 | kJ/mol | NIST |
| μ | 1.30 | debye | KDB |
| ΔfG° | 39.82 | kJ/mol | KDB |
| ΔfH°gas | [-106.70; -69.90] | kJ/mol |
|
| ΔfH°gas | -72.43 | kJ/mol | KDB |
| ΔfH°gas | -69.90 ± 0.80 | kJ/mol | NIST |
| ΔfH°gas | -70.17 ± 0.54 | kJ/mol | NIST |
| ΔfH°gas | -106.70 | kJ/mol | NIST |
| ΔfH°liquid | [-138.00; -101.50] | kJ/mol |
|
| ΔfH°liquid | -101.50 ± 0.40 | kJ/mol | NIST |
| ΔfH°liquid | -138.00 | kJ/mol | NIST |
| ΔfusH° | 8.72 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [29.20; 31.43] | kJ/mol |
|
| ΔvapH° | 31.43 | kJ/mol | NIST |
| ΔvapH° | 31.30 | kJ/mol | NIST |
| ΔvapH° | 31.30 ± 0.20 | kJ/mol | NIST |
| ΔvapH° | 31.30 | kJ/mol | NIST |
| ΔvapH° | 29.20 | kJ/mol | NIST |
| IE | [8.50; 9.44] | eV |
|
| IE | 8.50 ± 0.10 | eV | NIST |
| IE | 8.78 ± 0.02 | eV | NIST |
| IE | 9.40 ± 0.30 | eV | NIST |
| IE | 9.44 | eV | NIST |
| log10WS | -0.51 | Crippen Calculated Property | |
| logPoct/wat | 0.355 | Crippen Calculated Property | |
| McVol | 63.110 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 3 | KDB | |
| NFPA Health | 3 | KDB | |
| Pc | [4720.00; 4737.96] | kPa |
|
| Pc | 4720.00 | kPa | KDB |
| Pc | 4737.96 ± 101.32 | kPa | NIST |
| Pc | 4737.96 ± 40.53 | kPa | NIST |
| Inp | [472.00; 542.00] |
|
|
| Inp | 521.00 | NIST | |
| Inp | 521.00 | NIST | |
| Inp | Outlier 472.00 | NIST | |
| Inp | 542.00 | NIST | |
| Inp | 518.00 | NIST | |
| Inp | 515.00 | NIST | |
| Inp | 515.00 | NIST | |
| Inp | 527.00 | NIST | |
| Inp | 528.00 | NIST | |
| Inp | 524.00 | NIST | |
| Inp | 526.00 | NIST | |
| Inp | 510.00 | NIST | |
| Inp | 542.00 | NIST | |
| Inp | 518.00 | NIST | |
| Inp | 518.00 | NIST | |
| Inp | 527.00 | NIST | |
| I | [783.00; 817.00] |
|
|
| I | 787.00 | NIST | |
| I | 785.00 | NIST | |
| I | 817.00 | NIST | |
| I | 815.00 | NIST | |
| I | 783.00 | NIST | |
| I | 800.00 | NIST | |
| I | 816.00 | NIST | |
| I | 816.00 | NIST | |
| S°liquid | [227.44; 228.20] | J/mol×K |
|
| S°liquid | 227.44 | J/mol×K | NIST |
| S°liquid | 228.20 | J/mol×K | NIST |
| Tboil | 320.37 | K | KDB |
| Tc | [496.95; 499.20] | K |
|
| Tc | 497.00 | K | KDB |
| Tc | 499.20 | K | Gas-Liq... |
| Tc | 497.00 | K | NIST |
| Tc | 496.95 ± 1.50 | K | NIST |
| Tc | 496.95 ± 0.50 | K | NIST |
| Tfus | [190.00; 190.15] | K |
|
| Tfus | 190.00 | K | KDB |
| Tfus | 190.15 | K | NIST |
| Tfus | 190.00 ± 0.60 | K | NIST |
| Tfus | 190.15 ± 0.50 | K | NIST |
| Ttriple | [188.36; 188.38] | K |
|
| Ttriple | 188.36 | K | KDB |
| Ttriple | 188.38 ± 0.01 | K | NIST |
| Ttriple | 188.36 ± 0.07 | K | NIST |
| Vc | 0.233 | m3/kmol | KDB |
| Vm | 8.32e-05 | m3/mol | Thermod... |
| Zc | 0.2661370 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [106.30; 145.07] | J/mol×K | [340.57; 522.57] |
|
| Cp,gas | 106.30 | J/mol×K | 340.57 | Joback Calculated Property |
| Cp,gas | 113.40 | J/mol×K | 370.90 | Joback Calculated Property |
| Cp,gas | 120.24 | J/mol×K | 401.24 | Joback Calculated Property |
| Cp,gas | 126.82 | J/mol×K | 431.57 | Joback Calculated Property |
| Cp,gas | 133.15 | J/mol×K | 461.90 | Joback Calculated Property |
| Cp,gas | 139.23 | J/mol×K | 492.23 | Joback Calculated Property |
| Cp,gas | 145.07 | J/mol×K | 522.57 | Joback Calculated Property |
| Cp,liquid | [160.00; 166.40] | J/mol×K | [298.15; 298.15] |
|
| Cp,liquid | 162.51 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 160.00 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 166.40 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 162.30 | J/mol×K | 298.15 | NIST |
| η | [0.0003130; 0.0003851] | Pa×s | [288.15; 313.15] |
|
| η | 0.0003851 | Pa×s | 288.15 | Excess ... |
| η | 0.0003585 | Pa×s | 298.15 | Excess ... |
| η | 0.0003530 | Pa×s | 303.15 | Studies... |
| η | 0.0003222 | Pa×s | 308.15 | Excess ... |
| η | 0.0003130 | Pa×s | 313.15 | Studies... |
| ΔfusH | [10.62; 10.97] | kJ/mol | [188.36; 188.40] |
|
| ΔfusH | 10.97 | kJ/mol | 188.36 | NIST |
| ΔfusH | 10.62 | kJ/mol | 188.36 | NIST |
| ΔfusH | 10.97 | kJ/mol | 188.40 | NIST |
| ΔvapH | [28.90; 31.30] | kJ/mol | [313.00; 328.00] |
|
| ΔvapH | 30.10 | kJ/mol | 313.00 | NIST |
| ΔvapH | 29.55 | kJ/mol | 320.40 | NIST |
| ΔvapH | 29.71 | kJ/mol | 322.20 | KDB |
| ΔvapH | 31.30 | kJ/mol | 323.00 | NIST |
| ΔvapH | 28.90 | kJ/mol | 328.00 | NIST |
| ρl | [696.04; 717.00] | kg/m3 | [293.00; 313.15] |
|
| ρl | 717.00 | kg/m3 | 293.00 | KDB |
| ρl | 716.48 | kg/m3 | 293.15 | Volumet... |
| ρl | 712.25 | kg/m3 | 298.15 | Speeds ... |
| ρl | 711.21 | kg/m3 | 298.15 | Volumet... |
| ρl | 711.80 | kg/m3 | 298.15 | Speed o... |
| ρl | 712.76 | kg/m3 | 298.15 | Excess ... |
| ρl | 705.88 | kg/m3 | 303.15 | Volumet... |
| ρl | 706.10 | kg/m3 | 303.15 | Studies... |
| ρl | 706.10 | kg/m3 | 303.15 | Studies... |
| ρl | 700.62 | kg/m3 | 308.15 | Volumet... |
| ρl | 696.04 | kg/m3 | 313.15 | Studies... |
| ΔfusS | [56.40; 58.26] | J/mol×K | [188.36; 188.36] |
|
| ΔfusS | 58.26 | J/mol×K | 188.36 | NIST |
| ΔfusS | 56.40 | J/mol×K | 188.36 | NIST |
| csound,fluid | [1169.93; 1266.07] | m/s | [288.15; 308.15] |
|
| csound,fluid | 1266.07 | m/s | 288.15 | Mixing ... |
| csound,fluid | 1242.02 | m/s | 293.15 | Mixing ... |
| csound,fluid | 1217.97 | m/s | 298.15 | Mixing ... |
| csound,fluid | 1193.96 | m/s | 303.15 | Mixing ... |
| csound,fluid | 1169.93 | m/s | 308.15 | Mixing ... |
| γ | 0.02 | N/m | 293.20 | KDB |
Datasets
Viscosity, Pa*s
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Viscosity, Pa*s - Liquid |
| 303.15 | 101.33 | 0.0004 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [0.02; 4633.74] | kPa | [190.15; 496.95] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 5.49672e+01 | |||
| Coefficient B | -5.34711e+03 | |||
| Coefficient C | -5.90378e+00 | |||
| Coefficient D | 3.59300e-06 | |||
| Temperature range, min. | 190.15 | |||
| Temperature range, max. | 496.95 | |||
| Pvap | 0.02 | kPa | 190.15 | Calculated Property |
| Pvap | 0.52 | kPa | 224.24 | Calculated Property |
| Pvap | 5.57 | kPa | 258.33 | Calculated Property |
| Pvap | 32.00 | kPa | 292.42 | Calculated Property |
| Pvap | 121.48 | kPa | 326.51 | Calculated Property |
| Pvap | 345.78 | kPa | 360.59 | Calculated Property |
| Pvap | 800.92 | kPa | 394.68 | Calculated Property |
| Pvap | 1595.02 | kPa | 428.77 | Calculated Property |
| Pvap | 2837.43 | kPa | 462.86 | Calculated Property |
| Pvap | 4633.74 | kPa | 496.95 | Calculated Property |
Similar Compounds
Find more compounds similar to Propylamine.
Mixtures
- Propylamine + Ethanol, 2-methoxy-
- Propylamine + Ethanol, 2-(2-methoxyethoxy)-
- Propylamine + Ethanol, 2-[2-(2-methoxyethoxy)ethoxy]-
- Ethanol, 2-(2-ethoxyethoxy)- + Propylamine
- Propylamine + Ethanol, 2-(2-butoxyethoxy)-
- Propylamine + Diethyl carbitol
- Propylamine + Butane, 1,1'-[oxybis(2,1-ethanediyloxy)]bis-
- Propylamine + Tetrahydrofuran
- Propylamine + Amylene hydrate
- Propylamine + Amylene hydrate + Tetrahydrofuran
- Propylamine + Heptane
- Acetonitrile + Propylamine
- Propylamine + Carbon Tetrachloride
- Trichloromethane + Propylamine
- Propylamine + Cyclohexane
- Benzene + Propylamine
- Propylene Glycol + Propylamine
- 1,3-Propanediol + Propylamine
- Propylamine + 1-Butanol
- Propylamine + 1,4-Dioxane
Find more mixtures with Propylamine.
Sources
- KDB Vapor Pressure Data
- Crippen Method
- Crippen Method
- Speeds of Sound and Isentropic Compressibilities of n-Alkoxyethanols and Polyethers with Propylamine at 298.15K
- Thermodynamic study of heptane + amine mixtures. V. Excess and solvation Gibbs energies
- Excess molar volume, viscosity, and refractive index study for the ternary mixture {2-methyl-2-butanol (1) + tetrahydrofuran (2) + propylamine (3)} at different temperatures. Application of the ERAS-model and Peng Robinson Stryjek Vera equation of state
- Thermodynamic study of (heptane + amine) mixtures. II. Excess and partial molar volumes at 298.15 K
- Volumetric properties of binary mixtures of (acetonitrile + amines) at several temperatures with application of the ERAS model
- Speed of sound as a function of temperature and pressure for propane derivatives
- Studies of viscosities of dilute solutions of alkylamine in non-electrolyte solvents. II. Haloalkanes and other polar solvents
- Studies of partial molar volumes of alkylamine in non-electrolyte solvents I. Alkylamines in hydrocarbons at 303.15 and 313.15K
- Excess enthalpies of binary mixtures of some propylamines + some propanols at 298.15K
- Studies of viscosities of dilute solutions of alkylamines in non-electrolyte solvents III. Alkylamines in butanols 303.15K
- Studies of viscosities of dilute solutions of alkylamines in non-electrolyte solvents: IV. Alkylamines in 1,4-dioxane and oxolane at 303.15K
- Gas-Liquid Critical Temperatures of Some Alkenes, Amines, and Cyclic Hydrocarbons
- Mixing Properties for Binary Liquid Mixtures of Methyl tert-Butyl Ether with Propylamine and Dipropylamine at Temperatures from (288.15 to 308.15) K
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
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