- InChI
- InChI=1S/C6H15N/c1-3-5-7-6-4-2/h7H,3-6H2,1-2H3
- InChI Key
- WEHWNAOGRSTTBQ-UHFFFAOYSA-N
- Formula
- C6H15N
- SMILES
- CCCNCCC
- Molecular Weight1
- 101.19
- CAS
- 142-84-7
- Other Names
-
- (n-C3H7)2NH
- DIPROPYLAMINE
- Di-n-propylamine
- N-DIPROPYLAMINE
- N-Propyl-1-propanamine
- N-Propyl-propylamine
- Rcra waste number U110
- UN 2383
- 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).
- 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).
- 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.
- csound,fluid : Speed of sound in fluid (m/s).
- 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 |
|---|---|---|---|
| ω | 0.4710 | KDB | |
| PAff | 962.30 | kJ/mol | NIST |
| BasG | 929.30 | kJ/mol | NIST |
| ΔcH°liquid | [-4350.20; -4348.68] | kJ/mol |
|
| ΔcH°liquid | -4350.20 ± 1.30 | kJ/mol | NIST |
| ΔcH°liquid | -4348.68 ± 0.42 | kJ/mol | NIST |
| μ | 1.00 | debye | KDB |
| ΔfG° | 89.03 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | [-118.10; -116.50] | kJ/mol |
|
| ΔfH°gas | -116.50 ± 1.60 | kJ/mol | NIST |
| ΔfH°gas | -118.10 | kJ/mol | NIST |
| ΔfH°liquid | [-156.20; -154.60] | kJ/mol |
|
| ΔfH°liquid | -154.60 ± 1.50 | kJ/mol | NIST |
| ΔfH°liquid | -156.20 ± 0.42 | kJ/mol | NIST |
| ΔfusH° | 16.39 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [38.10; 41.50] | kJ/mol |
|
| ΔvapH° | 40.10 | kJ/mol | NIST |
| ΔvapH° | 38.10 | kJ/mol | NIST |
| ΔvapH° | 41.50 | kJ/mol | NIST |
| ΔvapH° | 40.20 ± 0.30 | kJ/mol | NIST |
| ΔvapH° | 40.00 ± 0.10 | kJ/mol | NIST |
| ΔvapH° | 40.04 ± 0.06 | kJ/mol | NIST |
| IE | [7.80; 8.60] | eV |
|
| IE | 7.80 ± 0.10 | eV | NIST |
| IE | 7.84 ± 0.02 | eV | NIST |
| IE | 8.60 ± 0.30 | eV | NIST |
| log10WS | -0.46 | Aq. Sol... | |
| logPoct/wat | 1.396 | Crippen Calculated Property | |
| McVol | 105.380 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 3 | KDB | |
| NFPA Health | 3 | KDB | |
| Pc | [3630.00; 3630.00] | kPa |
|
| Pc | 3630.00 | kPa | KDB |
| Pc | 3630.00 ± 36.27 | kPa | NIST |
| Inp | [742.60; 752.00] |
|
|
| Inp | 742.60 | NIST | |
| Inp | 742.60 | NIST | |
| Inp | 744.00 | NIST | |
| Inp | 746.00 | NIST | |
| Inp | 746.00 | NIST | |
| Inp | 752.00 | NIST | |
| Inp | 752.00 | NIST | |
| Inp | 750.00 | NIST | |
| Inp | 748.00 | NIST | |
| Inp | 746.00 | NIST | |
| Inp | 748.00 | NIST | |
| Inp | 745.00 | NIST | |
| Inp | 748.00 | NIST | |
| I | [894.00; 910.00] |
|
|
| I | 901.00 | NIST | |
| I | 904.00 | NIST | |
| I | 905.00 | NIST | |
| I | 900.00 | NIST | |
| I | 910.00 | NIST | |
| I | 894.00 | NIST | |
| Tboil | [380.70; 383.85] | K |
|
| Tboil | 382.40 | K | KDB |
| Tboil | Outlier 380.70 | K | NIST |
| Tboil | 382.56 ± 0.30 | K | NIST |
| Tboil | 382.70 | K | NIST |
| Tboil | 382.40 | K | NIST |
| Tboil | 381.55 ± 0.40 | K | NIST |
| Tboil | 382.45 | K | NIST |
| Tboil | 382.20 ± 1.50 | K | NIST |
| Tboil | 383.15 ± 2.00 | K | NIST |
| Tboil | 382.15 ± 3.00 | K | NIST |
| Tboil | 382.35 ± 0.40 | K | NIST |
| Tboil | 383.85 ± 0.40 | K | NIST |
| Tboil | 382.15 ± 3.00 | K | NIST |
| Tboil | 383.15 ± 3.00 | K | NIST |
| Tboil | 383.05 ± 0.80 | K | NIST |
| Tc | [555.80; 555.80] | K |
|
| Tc | 555.80 | K | KDB |
| Tc | 555.80 | K | Gas-Liq... |
| Tc | 555.80 ± 0.55 | K | NIST |
| Tfus | [209.60; 233.55] | K |
|
| Tfus | 210.00 | K | KDB |
| Tfus | 215.90 | K | Aq. Sol... |
| Tfus | 210.15 | K | NIST |
| Tfus | 209.60 ± 0.60 | K | NIST |
| Tfus | 210.15 ± 0.50 | K | NIST |
| Tfus | Outlier 233.55 ± 0.50 | K | NIST |
| Vc | 0.406 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [199.23; 261.47] | J/mol×K | [386.85; 556.73] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 200 210 220 230 240 250 260 400 450 500 550 | ||||
| Cp,gas | 199.23 | J/mol×K | 386.85 | Joback Calculated Property |
| Cp,gas | 210.62 | J/mol×K | 415.16 | Joback Calculated Property |
| Cp,gas | 221.60 | J/mol×K | 443.48 | Joback Calculated Property |
| Cp,gas | 232.16 | J/mol×K | 471.79 | Joback Calculated Property |
| Cp,gas | 242.32 | J/mol×K | 500.10 | Joback Calculated Property |
| Cp,gas | 252.08 | J/mol×K | 528.41 | Joback Calculated Property |
| Cp,gas | 261.47 | J/mol×K | 556.73 | Joback Calculated Property |
| η | [0.0004230; 0.0005120] | Pa×s | [303.15; 313.15] |
|
| η | 0.0005120 | Pa×s | 303.15 | Studies... |
| η | 0.0004230 | Pa×s | 313.15 | Studies... |
| ΔvapH | [33.47; 41.00] | kJ/mol | [291.00; 382.40] |
|
| ΔvapH | 41.00 | kJ/mol | 291.00 | NIST |
| ΔvapH | 40.00 | kJ/mol | 351.50 | NIST |
| ΔvapH | 39.80 | kJ/mol | 362.00 | NIST |
| ΔvapH | 33.47 | kJ/mol | 382.40 | NIST |
| Pvap | [2.72; 9.89] | kPa | [293.15; 318.15] |
|
|
T(K) Vapor pressure (kPa) 3 4 5 6 7 8 9 10 300 310 | ||||
| Pvap | 2.72 | kPa | 293.15 | Thermod... |
| Pvap | 3.60 | kPa | 298.15 | Thermod... |
| Pvap | 4.71 | kPa | 303.15 | Thermod... |
| Pvap | 6.12 | kPa | 308.15 | Thermod... |
| Pvap | 7.80 | kPa | 313.15 | Thermod... |
| Pvap | 9.89 | kPa | 318.15 | Thermod... |
| ρl | [723.64; 738.47] | kg/m3 | [291.15; 313.15] |
|
|
T(K) Liquid Density (kg/m3) 724 726 728 730 732 734 736 738 295 300 305 310 | ||||
| ρl | 738.47 | kg/m3 | 291.15 | Density... |
| ρl | 738.00 | kg/m3 | 293.00 | KDB |
| ρl | 737.20 | kg/m3 | 293.15 | Density... |
| ρl | 738.19 | kg/m3 | 293.15 | Thermod... |
| ρl | 738.18 | kg/m3 | 293.15 | Volumet... |
| ρl | 733.72 | kg/m3 | 298.15 | Thermod... |
| ρl | 733.37 | kg/m3 | 298.15 | Thermod... |
| ρl | 733.64 | kg/m3 | 298.15 | Volumet... |
| ρl | 733.62 | kg/m3 | 298.15 | Thermod... |
| ρl | 732.56 | kg/m3 | 298.15 | Density... |
| ρl | 731.21 | kg/m3 | 303.15 | Studies... |
| ρl | 731.21 | kg/m3 | 303.15 | Studies... |
| ρl | 729.10 | kg/m3 | 303.15 | Thermod... |
| ρl | 728.20 | kg/m3 | 303.15 | Density... |
| ρl | 729.07 | kg/m3 | 303.15 | Volumet... |
| ρl | 724.48 | kg/m3 | 308.15 | Volumet... |
| ρl | 723.64 | kg/m3 | 308.15 | Density... |
| ρl | 726.15 | kg/m3 | 313.15 | Studies... |
| csound,fluid | [1149.03; 1235.06] | m/s | [288.15; 308.15] |
|
|
T(K) Speed of sound in fluid (m/s) 1160 1180 1200 1220 1240 290 295 300 305 | ||||
| csound,fluid | 1235.06 | m/s | 288.15 | Mixing ... |
| csound,fluid | 1213.41 | m/s | 293.15 | Mixing ... |
| csound,fluid | 1209.20 | m/s | 293.15 | Thermod... |
| csound,fluid | 1209.38 | m/s | 293.15 | Thermod... |
| csound,fluid | 1191.86 | m/s | 298.15 | Mixing ... |
| csound,fluid | 1187.70 | m/s | 298.15 | Thermod... |
| csound,fluid | 1188.00 | m/s | 298.15 | Thermod... |
| csound,fluid | 1167.10 | m/s | 303.15 | Thermod... |
| csound,fluid | 1167.57 | m/s | 303.15 | Thermod... |
| csound,fluid | 1170.43 | m/s | 303.15 | Mixing ... |
| csound,fluid | 1149.03 | m/s | 308.15 | Mixing ... |
Datasets
Viscosity, Pa*s
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Viscosity, Pa*s - Liquid |
| 303.15 | 101.33 | 0.0005 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.01e-03; 3694.84] | kPa | [210.15; 555.80] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 1.45365e+02 | |||
| Coefficient B | -1.01337e+04 | |||
| Coefficient C | -1.95845e+01 | |||
| Coefficient D | 1.57470e-05 | |||
| Temperature range, min. | 210.15 | |||
| Temperature range, max. | 555.80 | |||
|
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 3500 4000 300 400 500 | ||||
| Pvap | 1.01e-03 | kPa | 210.15 | Calculated Property |
| Pvap | 0.09 | kPa | 248.56 | Calculated Property |
| Pvap | 1.67 | kPa | 286.96 | Calculated Property |
| Pvap | 13.34 | kPa | 325.37 | Calculated Property |
| Pvap | 61.00 | kPa | 363.77 | Calculated Property |
| Pvap | 194.16 | kPa | 402.18 | Calculated Property |
| Pvap | 487.15 | kPa | 440.58 | Calculated Property |
| Pvap | 1045.32 | kPa | 478.99 | Calculated Property |
| Pvap | 2027.53 | kPa | 517.39 | Calculated Property |
| Pvap | 3694.84 | kPa | 555.80 | Calculated Property |
Similar Compounds
Find more compounds similar to 1-Propanamine, N-propyl-.
Mixtures
- 1-Propanol + 1-Propanamine, N-propyl-
- Acetone + 1-Propanamine, N-propyl-
- 2-Butanone + 1-Propanamine, N-propyl-
- 2-Pentanone + 1-Propanamine, N-propyl-
- 1-Propanamine, N-propyl- + 2-Heptanone
- Formamide, N,N-dimethyl- + 1-Propanamine, N-propyl-
- N,N-Dimethylacetamide + 1-Propanamine, N-propyl-
- Acetonitrile + 1-Propanamine, N-propyl-
- Trichloromethane + 1-Propanamine, N-propyl-
- 1-Propanamine, N-propyl- + Cyclohexane
- Benzene + 1-Propanamine, N-propyl-
- 1-Butanol + 1-Propanamine, N-propyl-
- 1-Propanamine, N-propyl- + 1,4-Dioxane
- 1-Propanamine, N-propyl- + Tetrahydrofuran
- Ethanol, 2-methoxy- + 1-Propanamine, N-propyl-
- Propane, 2-methoxy-2-methyl- + 1-Propanamine, N-propyl-
- Heptane + 1-Propanamine, N-propyl-
Sources
- KDB Pure (Korean Thermophysical Properties Databank)
- KDB Vapor Pressure Data
- Crippen Method
- Thermodynamics of mixtures with strongly negative deviations from Raoult s law Part 9. Vapor liquid equilibria for the system 1-propanol + di-n-propylamine at six temperatures between 293.15 and 318.15K
- Thermodynamics of ketone + amine mixtures. Part IX. Excess molar enthalpies at 298.15K for dipropylamine, or dibutylamine + 2-alkanone systems and modeling of linear or aromatic amine + 2-alkanone mixtures in terms of DISQUAC and ERAS
- Thermodynamic study of heptane + amine mixtures. V. Excess and solvation Gibbs energies
- Thermodynamics of amide + amine mixtures. 5. Excess molar enthalpies of N,N-dimethylformamide or N,N-dimethylacetamide + N-propylpropan-1-amine, + N-butylbutan-1-amine, + butan-1-amine, or + hexan-1-amine systems at 298.15 K. Application of the ERAS model
- Thermodynamic study of (heptane + amine) mixtures. III: Excess and partial molar volumes in mixtures with secondary, tertiary, and cyclic amines at 298.15 K
- Thermodynamics of (ketone + amine) mixtures. Part VI. Volumetric and speed of sound data at (293.15, 298.15, and 303.15) K for (2-heptanone + dipropylamine, +dibutylamine, or +triethylamine) systems
- Volumetric properties of binary mixtures of (acetonitrile + amines) at several temperatures with application of the ERAS model
- 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
- 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
- Thermodynamics of ketone + amine mixtures Part IV. Volumetric and speed of sound data at (293.15; 298.15 and 303.15 K) for 2-butanone +dipropylamine, +dibutylamine or +triethylamine systems
- Thermodynamics of amide + amine mixtures. 1. Volumetric, speed of sound, and refractive index data for N,Ndimethylformamide + N-propylpropan-1-amine, + N-butylbutan-1-amine, + butan-1-amine, or + hexan-1-amine systems at several temperatures
- Gas-Liquid Critical Temperatures of Some Alkenes, Amines, and Cyclic Hydrocarbons
- Density and Relative Permittivity of 2-Methoxyethanol + Dipropylamine Mixtures at Various Temperatures
- 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
- Aqueous Solubility Prediction Method
- McGowan Method
- NIST Webbook
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