- InChI
- InChI=1S/C24H51N/c1-4-7-10-13-16-19-22-25(23-20-17-14-11-8-5-2)24-21-18-15-12-9-6-3/h4-24H2,1-3H3
- InChI Key
- XTAZYLNFDRKIHJ-UHFFFAOYSA-N
- Formula
- C24H51N
- SMILES
- CCCCCCCCN(CCCCCCCC)CCCCCCCC
- Molecular Weight1
- 353.67
- CAS
- 1116-76-3
- Other Names
-
- 336S
- Alamine 308
- Alamine 336
- Alamine 3365
- Alamine 336S
- Farmin 08
- N,N-dioctyl-1-octanamine
- NSC 11034
- TOA
- Tri-N-caprylylamine
- Tri-n-octylamine
- Tricaprylamine
- Tricaprylylamine
- Trioctylamine
- 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).
- 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).
- 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.
- 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.
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 |
|---|---|---|---|
| ΔcH°liquid | [-16147.90; -16145.40] | kJ/mol |
|
| ΔcH°liquid | -16145.40 ± 3.60 | kJ/mol | NIST |
| ΔcH°liquid | -16147.90 ± 2.10 | kJ/mol | NIST |
| ΔfG° | 261.98 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | [-477.00; -474.80] | kJ/mol |
|
| ΔfH°gas | -477.00 ± 15.00 | kJ/mol | NIST |
| ΔfH°gas | -474.80 | kJ/mol | NIST |
| ΔfH°liquid | [-587.50; -585.30] | kJ/mol |
|
| ΔfH°liquid | -587.50 ± 3.80 | kJ/mol | NIST |
| ΔfH°liquid | -585.30 ± 2.10 | kJ/mol | NIST |
| ΔfusH° | 60.94 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [110.00; 110.50] | kJ/mol |
|
| ΔvapH° | 110.00 ± 15.00 | kJ/mol | NIST |
| ΔvapH° | 110.50 | kJ/mol | NIST |
| ΔvapH° | 110.40 ± 1.50 | kJ/mol | NIST |
| log10WS | -8.44 | Crippen Calculated Property | |
| logPoct/wat | 8.370 | Crippen Calculated Property | |
| McVol | 359.000 | ml/mol | McGowan Calculated Property |
| Pc | 805.25 | kPa | Joback Calculated Property |
| Inp | [2290.00; 2297.00] |
|
|
| Inp | 2297.00 | NIST | |
| Inp | 2297.00 | NIST | |
| Inp | 2290.00 | NIST | |
| Inp | 2290.00 | NIST | |
| Inp | 2297.00 | NIST | |
| Tboil | [630.15; 639.20] | K |
|
| Tboil | 639.20 | K | NIST |
| Tboil | 630.15 ± 4.00 | K | NIST |
| Tc | 932.42 | K | Joback Calculated Property |
| Tfus | [238.55; 238.73] | K |
|
| Tfus | 238.73 | K | Solid-L... |
| Tfus | 238.55 ± 1.00 | K | NIST |
| Vc | 1.397 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [1132.54; 1255.89] | J/mol×K | [760.96; 932.42] |
|
| Cp,gas | 1132.54 | J/mol×K | 760.96 | Joback Calculated Property |
| Cp,gas | 1155.63 | J/mol×K | 789.54 | Joback Calculated Property |
| Cp,gas | 1177.65 | J/mol×K | 818.11 | Joback Calculated Property |
| Cp,gas | 1198.64 | J/mol×K | 846.69 | Joback Calculated Property |
| Cp,gas | 1218.65 | J/mol×K | 875.27 | Joback Calculated Property |
| Cp,gas | 1237.72 | J/mol×K | 903.85 | Joback Calculated Property |
| Cp,gas | 1255.89 | J/mol×K | 932.42 | Joback Calculated Property |
| Cp,liquid | 750.80 | J/mol×K | 298.15 | NIST |
| ΔvapH | [70.60; 100.10] | kJ/mol | [298.00; 603.50] |
|
| ΔvapH | 100.10 | kJ/mol | 298.00 | Evaluat... |
| ΔvapH | 71.85 | kJ/mol | 505.00 | Thermod... |
| ΔvapH | 70.60 | kJ/mol | 603.50 | NIST |
| ρl | [803.88; 817.08] | kg/m3 | [283.15; 303.15] |
|
| ρl | 817.08 | kg/m3 | 283.15 | Density... |
| ρl | 810.48 | kg/m3 | 293.15 | Density... |
| ρl | 807.90 | kg/m3 | 298.15 | Liquid-... |
| ρl | 807.46 | kg/m3 | 298.15 | Liquid-... |
| ρl | 810.03 | kg/m3 | 298.15 | Partial... |
| ρl | 807.26 | kg/m3 | 298.15 | Density... |
| ρl | 803.88 | kg/m3 | 303.15 | Density... |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.64] | kPa | [487.56; 675.79] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.52061e+01 | |||
| Coefficient B | -5.53069e+03 | |||
| Coefficient C | -1.16832e+02 | |||
| Temperature range, min. | 487.56 | |||
| Temperature range, max. | 675.79 | |||
| Pvap | 1.33 | kPa | 487.56 | Calculated Property |
| Pvap | 2.96 | kPa | 508.47 | Calculated Property |
| Pvap | 6.05 | kPa | 529.39 | Calculated Property |
| Pvap | 11.55 | kPa | 550.30 | Calculated Property |
| Pvap | 20.79 | kPa | 571.22 | Calculated Property |
| Pvap | 35.51 | kPa | 592.13 | Calculated Property |
| Pvap | 57.99 | kPa | 613.05 | Calculated Property |
| Pvap | 91.02 | kPa | 633.96 | Calculated Property |
| Pvap | 137.94 | kPa | 654.88 | Calculated Property |
| Pvap | 202.64 | kPa | 675.79 | Calculated Property |
Similar Compounds
Find more compounds similar to 1-Octanamine, N,N-dioctyl-.
Mixtures
- 1-Octanamine, N,N-dioctyl- + Decane + Water
- 1-Octanamine, N,N-dioctyl- + Water
- 1-Octanamine, N,N-dioctyl- + Dodecane
- 1-Dodecanol + 1-Octanamine, N,N-dioctyl-
- Undecane + 1-Octanamine, N,N-dioctyl-
- 1-Octanamine, N,N-dioctyl- + Methyl Alcohol
- 1-Octanamine, N,N-dioctyl- + Heptane
- 1-Octanamine, N,N-dioctyl- + Octane
- 1-Octanamine, N,N-dioctyl- + Nonane
- 1-Octanamine, N,N-dioctyl- + Decane
- 1-Octanamine, N,N-dioctyl- + 1-Octanol
- 1-Octanamine, N,N-dioctyl- + 1-Decanol
- 1-Octanamine, N,N-dioctyl- + Tributyl phosphate
- 1-Octanamine, N,N-dioctyl- + 1-Butanol
- n-Hexane + 1-Octanamine, N,N-dioctyl-
- n-Hexane + 1-Octanamine, N,N-dioctyl- + 1-Butanol
Sources
- Crippen Method
- Crippen Method
- SLE and LLE for tri-butylphosphate or tri-octylamine contained systems; extractive solvents of Molybdenum
- Liquid-liquid equilibria for aqueous sulfuric acid solutions with undecane, dodecane, or 1-dodecanol, trioctylamine or tributyl phosphate and excess and deviation properties for sub-binary systems at 298.15 K
- Liquid-liquid equilibria, excess molar volume and deviations of the refractive indices at 298.15 K for mixtures of solvents used in themolybdenum extraction process
- Excess molar volumes and excess molar enthalpies of binary and ternary mixtures of 1-butanol, a tertiary amine (tri-n-butylamine or tri-n-octylamine) and n-hexane: Experimental results and ERAS-model calculations
- Partial molar volume of tertiary amines in methanol at T = 298.15 K. Solvation, shape and specific interactions
- Density, viscosity and excess molar volume of binary mixtures of tri-n-octylamine + diluents (n-heptane, n-octane, n-nonane, and n-decane) at various temperatures
- Thermodynamics and kinetics analysis of thermal dissociation of tri-n-octylamine hydrochloride in open system: A DFT and TGA study
- 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
- Solid-Liquid Equilibria, Excess Molar Volumes, and Molar Refractivity Deviations for Extractive Solvents of Molybdenum
- Joback Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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.