- InChI
- InChI=1S/C9H21N/c1-4-7-10(8-5-2)9-6-3/h4-9H2,1-3H3
- InChI Key
- YFTHZRPMJXBUME-UHFFFAOYSA-N
- Formula
- C9H21N
- SMILES
- CCCN(CCC)CCC
- Molecular Weight1
- 143.27
- CAS
- 102-69-2
- Other Names
-
- (n-C3H7)3N
- N,N-DIPROPYL-1-PROPYLAMINE
- N,N-Dipropyl-1-propanamine
- N,N-dipropylpropanamine
- Propyldi-n-propylamine
- TRIPROPYLAMINE
- Tri-n-propylamine
- UN 2260
- propanamine, N,N-dipropyl-
- 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).
- 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).
- Pc : Critical Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- I : Polar retention indices.
- 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 | 991.00 | kJ/mol | NIST |
| BasG | 960.10 | kJ/mol | NIST |
| ΔcH°liquid | -6335.66 ± 0.79 | kJ/mol | NIST |
| ΔfG° | 135.68 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -160.80 ± 0.80 | kJ/mol | NIST |
| ΔfH°liquid | -206.90 ± 0.79 | kJ/mol | NIST |
| ΔfusH° | 22.09 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [46.15; 46.20] | kJ/mol |
|
| ΔvapH° | 46.17 | kJ/mol | NIST |
| ΔvapH° | 46.20 ± 0.10 | kJ/mol | NIST |
| ΔvapH° | 46.15 ± 0.07 | kJ/mol | NIST |
| IE | [7.00; 8.00] | eV |
|
| IE | 7.40 | eV | NIST |
| IE | 7.00 ± 0.10 | eV | NIST |
| IE | 7.03 ± 0.09 | eV | NIST |
| IE | 7.23 | eV | NIST |
| IE | 8.00 ± 0.30 | eV | NIST |
| log10WS | -2.28 | Aq. Sol... | |
| logPoct/wat | 2.518 | Crippen Calculated Property | |
| McVol | 147.650 | ml/mol | McGowan Calculated Property |
| Pc | 2302.53 | kPa | Joback Calculated Property |
| Inp | [915.00; 964.00] |
|
|
| Inp | 918.00 | NIST | |
| Inp | 917.00 | NIST | |
| Inp | 915.00 | NIST | |
| Inp | 915.00 | NIST | |
| Inp | 964.00 | NIST | |
| Inp | 964.00 | NIST | |
| Inp | 962.00 | NIST | |
| Inp | 917.00 | NIST | |
| Inp | 917.00 | NIST | |
| Inp | 937.00 | NIST | |
| Inp | 937.00 | NIST | |
| Inp | 927.00 | NIST | |
| Inp | 927.00 | NIST | |
| I | [958.00; 978.00] |
|
|
| I | 978.00 | NIST | |
| I | 970.00 | NIST | |
| I | 974.00 | NIST | |
| I | 965.00 | NIST | |
| I | 968.00 | NIST | |
| I | 958.00 | NIST | |
| Tboil | [427.40; 430.00] | K |
|
| Tboil | 429.65 | K | KDB |
| Tboil | 429.20 | K | NIST |
| Tboil | 427.40 ± 0.50 | K | NIST |
| Tboil | 429.15 ± 2.00 | K | NIST |
| Tboil | 429.15 ± 2.00 | K | NIST |
| Tboil | 429.65 ± 1.00 | K | NIST |
| Tboil | 429.15 ± 1.50 | K | NIST |
| Tboil | 427.65 ± 3.00 | K | NIST |
| Tboil | 427.65 ± 3.00 | K | NIST |
| Tboil | 429.15 ± 0.50 | K | NIST |
| Tboil | 429.15 ± 3.00 | K | NIST |
| Tboil | 429.15 ± 2.00 | K | NIST |
| Tboil | 430.00 ± 4.00 | K | NIST |
| Tc | 579.60 | K | Joback Calculated Property |
| Tfus | [172.65; 179.65] | K |
|
| Tfus | 179.65 | K | Aq. Sol... |
| Tfus | 172.65 ± 0.50 | K | NIST |
| Tfus | 179.65 ± 0.50 | K | NIST |
| Vc | 0.557 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [303.35; 385.27] | J/mol×K | [417.76; 579.60] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 300 320 340 360 380 450 500 550 | ||||
| Cp,gas | 303.35 | J/mol×K | 417.76 | Joback Calculated Property |
| Cp,gas | 318.41 | J/mol×K | 444.73 | Joback Calculated Property |
| Cp,gas | 332.88 | J/mol×K | 471.71 | Joback Calculated Property |
| Cp,gas | 346.79 | J/mol×K | 498.68 | Joback Calculated Property |
| Cp,gas | 360.15 | J/mol×K | 525.66 | Joback Calculated Property |
| Cp,gas | 372.97 | J/mol×K | 552.63 | Joback Calculated Property |
| Cp,gas | 385.27 | J/mol×K | 579.60 | Joback Calculated Property |
| η | [0.0005380; 0.0005980] | Pa×s | [303.15; 313.15] |
|
| η | 0.0005980 | Pa×s | 303.15 | Studies... |
| η | 0.0005380 | Pa×s | 313.15 | Studies... |
| ΔvapH | 45.60 | kJ/mol | 408.00 | NIST |
| Pvap | [0.20; 1.26] | kPa | [283.15; 313.15] |
|
|
T(K) Vapor pressure (kPa) 0.2 0.4 0.6 0.8 1 1.2 290 300 310 | ||||
| Pvap | 0.20 | kPa | 283.15 | Evaluat... |
| Pvap | 0.28 | kPa | 288.15 | Evaluat... |
| Pvap | 0.38 | kPa | 293.15 | Evaluat... |
| Pvap | 0.52 | kPa | 298.15 | Evaluat... |
| Pvap | 0.71 | kPa | 303.15 | Evaluat... |
| Pvap | 0.95 | kPa | 308.15 | Evaluat... |
| Pvap | 1.26 | kPa | 313.15 | Evaluat... |
| ρl | [740.41; 752.10] | kg/m3 | [298.15; 313.15] |
|
| ρl | 752.10 | kg/m3 | 298.15 | Partial... |
| ρl | 749.15 | kg/m3 | 303.15 | Studies... |
| ρl | 749.15 | kg/m3 | 303.15 | Studies... |
| ρl | 740.41 | kg/m3 | 313.15 | Studies... |
Datasets
Viscosity, Pa*s
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Viscosity, Pa*s - Liquid |
| 303.15 | 101.33 | 0.0006 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.66] | kPa | [325.72; 453.50] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.57356e+01 | |||
| Coefficient B | -4.09570e+03 | |||
| Coefficient C | -6.05930e+01 | |||
| Temperature range, min. | 325.72 | |||
| Temperature range, max. | 453.50 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 350 400 450 | ||||
| Pvap | 1.33 | kPa | 325.72 | Calculated Property |
| Pvap | 2.92 | kPa | 339.92 | Calculated Property |
| Pvap | 5.94 | kPa | 354.12 | Calculated Property |
| Pvap | 11.31 | kPa | 368.31 | Calculated Property |
| Pvap | 20.35 | kPa | 382.51 | Calculated Property |
| Pvap | 34.82 | kPa | 396.71 | Calculated Property |
| Pvap | 57.06 | kPa | 410.91 | Calculated Property |
| Pvap | 89.97 | kPa | 425.10 | Calculated Property |
| Pvap | 137.11 | kPa | 439.30 | Calculated Property |
| Pvap | 202.66 | kPa | 453.50 | Calculated Property |
| Pvap | [2.00e-08; 2115.04] | kPa | [179.65; 577.50] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 1.04659e+02 | |||
| Coefficient B | -1.01020e+04 | |||
| Coefficient C | -1.27761e+01 | |||
| Coefficient D | 5.18581e-06 | |||
| Temperature range, min. | 179.65 | |||
| Temperature range, max. | 577.50 | |||
|
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 200 300 400 500 | ||||
| Pvap | 2.00e-08 | kPa | 179.65 | Calculated Property |
| Pvap | 8.79e-05 | kPa | 223.86 | Calculated Property |
| Pvap | 0.02 | kPa | 268.06 | Calculated Property |
| Pvap | 0.57 | kPa | 312.27 | Calculated Property |
| Pvap | 6.71 | kPa | 356.47 | Calculated Property |
| Pvap | 40.88 | kPa | 400.68 | Calculated Property |
| Pvap | 159.57 | kPa | 444.88 | Calculated Property |
| Pvap | 458.82 | kPa | 489.09 | Calculated Property |
| Pvap | 1063.82 | kPa | 533.29 | Calculated Property |
| Pvap | 2115.04 | kPa | 577.50 | Calculated Property |
Similar Compounds
Find more compounds similar to 1-Propanamine, N,N-dipropyl-.
Mixtures
- 1-Propanamine, N,N-dipropyl- + Methyl Alcohol
- 1-Propanamine, N,N-dipropyl- + Carbon Tetrachloride
- Trichloromethane + 1-Propanamine, N,N-dipropyl-
- 1-Propanamine, N,N-dipropyl- + Cyclohexane
- Benzene + 1-Propanamine, N,N-dipropyl-
- 1-Propanamine, N,N-dipropyl- + 1-Butanol
- 1-Propanamine, N,N-dipropyl- + 1,4-Dioxane
- 1-Propanamine, N,N-dipropyl- + Tetrahydrofuran
- 1-Propanamine, N,N-dipropyl- + Heptane
Sources
- KDB Vapor Pressure Data
- Crippen Method
- Thermodynamic study of (heptane + amine) mixtures. III: Excess and partial molar volumes in mixtures with secondary, tertiary, and cyclic amines at 298.15 K
- Partial molar volume of tertiary amines in methanol at T = 298.15 K. Solvation, shape and specific interactions
- 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
- Evaluation of the Vaporization Enthalpies and Liquid Vapor Pressures of (R)-Deprenyl, (S)-Benzphetamine, Alverine, and a Series of Aliphatic Tertiary Amines by Correlation Gas Chromatography at T/K = 298.15
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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