- InChI
- InChI=1S/C10H19N/c1-2-3-4-5-6-7-8-9-10-11/h2-9H2,1H3
- InChI Key
- HBZDPWBWBJMYRY-UHFFFAOYSA-N
- Formula
- C10H19N
- SMILES
- CCCCCCCCCC#N
- Molecular Weight1
- 153.26
- CAS
- 1975-78-6
- Other Names
-
- 1-Cyanononane
- 1-Decanenitrile
- Caprinitrile
- Decanonitrile
- N-CAPRINITRILE
- NSC 6085
- Nitrile 10 D
- Nonyl cyanide
- n-Decanenitrile
- n-Nonyl cyanide
- ΔcH°liquid : Standard liquid enthalpy of combustion (kJ/mol).
- Cp,gas : Ideal gas 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).
- 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 |
|---|---|---|---|
| ΔcH°liquid | -6492.10 ± 1.20 | kJ/mol | NIST |
| ΔfG° | 166.50 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -91.60 ± 1.80 | kJ/mol | NIST |
| ΔfH°liquid | -158.40 ± 1.80 | kJ/mol | NIST |
| ΔfusH° | 23.16 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [66.30; 66.84] | kJ/mol |
|
| ΔvapH° | 66.84 | kJ/mol | NIST |
| ΔvapH° | 66.30 ± 0.40 | kJ/mol | NIST |
| ΔvapH° | 66.84 ± 0.37 | kJ/mol | NIST |
| ΔvapH° | 66.80 | kJ/mol | NIST |
| ΔvapH° | 66.80 ± 0.40 | kJ/mol | NIST |
| log10WS | -3.88 | Crippen Calculated Property | |
| logPoct/wat | 3.651 | Crippen Calculated Property | |
| McVol | 153.140 | ml/mol | McGowan Calculated Property |
| Pc | 2060.49 | kPa | Joback Calculated Property |
| Inp | [219.15; 1286.00] |
|
|
| Inp | 219.15 | NIST | |
| Inp | 1276.00 | NIST | |
| Inp | 1286.00 | NIST | |
| Inp | 1276.00 | NIST | |
| Inp | 1286.00 | NIST | |
| Inp | 219.15 | NIST | |
| I | 1677.00 | NIST | |
| Tboil | 516.90 ± 1.50 | K | NIST |
| Tc | 711.60 | K | Joback Calculated Property |
| Tfus | [255.25; 258.69] | K |
|
| Tfus | 258.69 ± 0.30 | K | NIST |
| Tfus | 258.69 ± 0.30 | K | NIST |
| Tfus | 255.25 ± 2.00 | K | NIST |
| Vc | 0.622 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [359.59; 431.99] | J/mol×K | [530.28; 711.60] |
|
| Cp,gas | 359.59 | J/mol×K | 530.28 | Joback Calculated Property |
| Cp,gas | 373.05 | J/mol×K | 560.50 | Joback Calculated Property |
| Cp,gas | 385.94 | J/mol×K | 590.72 | Joback Calculated Property |
| Cp,gas | 398.26 | J/mol×K | 620.94 | Joback Calculated Property |
| Cp,gas | 410.03 | J/mol×K | 651.16 | Joback Calculated Property |
| Cp,gas | 421.27 | J/mol×K | 681.38 | Joback Calculated Property |
| Cp,gas | 431.99 | J/mol×K | 711.60 | Joback Calculated Property |
| ΔvapH | [54.40; 58.00] | kJ/mol | [406.00; 474.50] |
|
| ΔvapH | 57.80 | kJ/mol | 406.00 | NIST |
| ΔvapH | 58.00 | kJ/mol | 450.00 | NIST |
| ΔvapH | 54.40 | kJ/mol | 474.50 | NIST |
| Pvap | [3.59e-03; 0.05] | kPa | [295.20; 326.30] |
|
| Pvap | 3.59e-03 | kPa | 295.20 | Vapor P... |
| Pvap | 4.84e-03 | kPa | 298.30 | Vapor P... |
| Pvap | 6.92e-03 | kPa | 302.20 | Vapor P... |
| Pvap | 9.28e-03 | kPa | 305.60 | Vapor P... |
| Pvap | 0.01 | kPa | 308.70 | Vapor P... |
| Pvap | 0.02 | kPa | 311.70 | Vapor P... |
| Pvap | 0.02 | kPa | 313.10 | Vapor P... |
| Pvap | 0.02 | kPa | 315.20 | Vapor P... |
| Pvap | 0.02 | kPa | 316.20 | Vapor P... |
| Pvap | 0.03 | kPa | 319.20 | Vapor P... |
| Pvap | 0.03 | kPa | 322.20 | Vapor P... |
| Pvap | 0.05 | kPa | 326.30 | Vapor P... |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.66] | kPa | [386.42; 549.04] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.46347e+01 | |||
| Coefficient B | -4.32966e+03 | |||
| Coefficient C | -8.46400e+01 | |||
| Temperature range, min. | 386.42 | |||
| Temperature range, max. | 549.04 | |||
| Pvap | 1.33 | kPa | 386.42 | Calculated Property |
| Pvap | 3.00 | kPa | 404.49 | Calculated Property |
| Pvap | 6.18 | kPa | 422.56 | Calculated Property |
| Pvap | 11.85 | kPa | 440.63 | Calculated Property |
| Pvap | 21.32 | kPa | 458.70 | Calculated Property |
| Pvap | 36.35 | kPa | 476.76 | Calculated Property |
| Pvap | 59.12 | kPa | 494.83 | Calculated Property |
| Pvap | 92.28 | kPa | 512.90 | Calculated Property |
| Pvap | 138.95 | kPa | 530.97 | Calculated Property |
| Pvap | 202.66 | kPa | 549.04 | Calculated Property |
| Pvap | [0.13; 107.04] | kPa | [342.15; 518.15] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 1.47381e+02 | |||
| Coefficient B | -1.32453e+04 | |||
| Coefficient C | -1.91825e+01 | |||
| Coefficient D | 1.02455e-05 | |||
| Temperature range, min. | 342.15 | |||
| Temperature range, max. | 518.15 | |||
| Pvap | 0.13 | kPa | 342.15 | Calculated Property |
| Pvap | 0.41 | kPa | 361.71 | Calculated Property |
| Pvap | 1.13 | kPa | 381.26 | Calculated Property |
| Pvap | 2.75 | kPa | 400.82 | Calculated Property |
| Pvap | 6.04 | kPa | 420.37 | Calculated Property |
| Pvap | 12.18 | kPa | 439.93 | Calculated Property |
| Pvap | 22.80 | kPa | 459.48 | Calculated Property |
| Pvap | 40.13 | kPa | 479.04 | Calculated Property |
| Pvap | 67.01 | kPa | 498.59 | Calculated Property |
| Pvap | 107.04 | kPa | 518.15 | Calculated Property |
Similar Compounds
Find more compounds similar to Decanenitrile.
Mixtures
Sources
- KDB Vapor Pressure Data
- Crippen Method
- Crippen Method
- Vapor Pressures and Enthalpies of Vaporization of a Series of the Linear Aliphatic Nitriles.
- Excess Enthalpies of {CH3(CH2)nCN, n = 5 to 12} + Methyl Methylthiomethyl Sulfoxide or + Dimethyl Sulfoxide at 298.15 K
- Joback Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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