- 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.
Cheméo is a service of Céondo GmbH, since 2007, we provide simulation, modelling and software development services for the industry.
Do not hesitate to contact us for your projects.
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] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 110 120 130 140 350 400 450 500 | ||||
| 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] |
|
|
T(K) Dynamic viscosity (Pa×s) 3.20e-4 3.40e-4 3.60e-4 3.80e-4 290 300 310 | ||||
| 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] |
|
|
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 29 29.5 30 30.5 31 31.5 315 320 325 | ||||
| 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] |
|
|
T(K) Liquid Density (kg/m3) 695 700 705 710 715 295 300 305 310 | ||||
| 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] |
|
|
T(K) Speed of sound in fluid (m/s) 1180 1200 1220 1240 1260 290 295 300 305 | ||||
| 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 | |||
|
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 5000 200 300 400 500 | ||||
| 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
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.
Outlier This icon means
that the value is more than 2 standard deviations away from the
property mean.