- InChI
- InChI=1S/C19H26/c1-2-3-4-5-6-7-8-11-17-14-15-18-12-9-10-13-19(18)16-17/h9-10,12-16H,2-8,11H2,1H3
- InChI Key
- BVGNMQMWUMKSMK-UHFFFAOYSA-N
- Formula
- C19H26
- SMILES
- CCCCCCCCCc1ccc2ccccc2c1
- Molecular Weight1
- 254.41
- CAS
- 61886-67-7
- ω : Acentric Factor.
- 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).
- ΔfusH° : Enthalpy of fusion at standard conditions (kJ/mol).
- ΔvapH° : Enthalpy of vaporization at standard conditions (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).
- 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 | 0.7321 | Relay (1.0) Calculated Property | |
| ΔfG° | 318.53 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -30.33 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfusH° | 35.64 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 94.09 | kJ/mol | Relay (1.0) Calculated Property |
| IE | 8.02 | eV | Relay (1.0) Calculated Property |
| log10WS | -7.38 | Relay (1.0) Calculated Property | |
| logPoct/wat | 6.133 | Crippen Calculated Property | |
| McVol | 235.350 | ml/mol | McGowan Calculated Property |
| Pc | 1624.60 | kPa | Joback Calculated Property |
| Tboil | 623.00 ± 5.00 | K | NIST |
| Tc | 839.95 | K | Relay (1.0) Calculated Property |
| Tfus | [276.70; 276.80] | K |
|
| Tfus | 276.70 ± 3.00 | K | NIST |
| Tfus | 276.80 ± 1.50 | K | NIST |
| Vc | 0.910 | m3/kmol | Relay (1.0) Calculated Property |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [312.84; 787.21] | J/mol×K | [273.00; 1000.00] |
Joback Predicted correlation
|
| Equation | Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,gas in J/mol×K, T in K | |||
| Coefficient A | -6.54320e+01 | |||
| Coefficient B | 1.66672e+00 | |||
| Coefficient C | -1.11068e-03 | |||
| Coefficient D | 2.96600e-07 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 312.84 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 398.34 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 473.45 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 539.11 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 596.27 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 645.85 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 688.80 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 726.05 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 758.54 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 787.21 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0090455; 0.0002516] | Pa×s | [276.75; 622.88] |
Joback Predicted correlation
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K | |||
| Coefficient A | -1.11520e+01 | |||
| Coefficient B | 1.78408e+03 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Comment | Liquid phase. Joback/Reid (1987), valid from Tf to 0.7·Tc. | |||
| Temperature range, min. | 276.75 | |||
| Temperature range, max. | 622.88 | |||
| η | 0.0090455 | Pa×s | 276.75 | Calculated Property |
| η | 0.0041194 | Pa×s | 315.21 | Calculated Property |
| η | 0.0022260 | Pa×s | 353.67 | Calculated Property |
| η | 0.0013573 | Pa×s | 392.13 | Calculated Property |
| η | 0.0009040 | Pa×s | 430.59 | Calculated Property |
| η | 0.0006436 | Pa×s | 469.05 | Calculated Property |
| η | 0.0004824 | Pa×s | 507.51 | Calculated Property |
| η | 0.0003766 | Pa×s | 545.97 | Calculated Property |
| η | 0.0003037 | Pa×s | 584.43 | Calculated Property |
| η | 0.0002516 | Pa×s | 622.88 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.65] | kPa | [480.22; 680.77] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.43435e+01 | |||
| Coefficient B | -5.06789e+03 | |||
| Coefficient C | -1.19668e+02 | |||
| Temperature range, min. | 480.22 | |||
| Temperature range, max. | 680.77 | |||
| Pvap | 1.33 | kPa | 480.22 | Calculated Property |
| Pvap | 3.02 | kPa | 502.50 | Calculated Property |
| Pvap | 6.26 | kPa | 524.79 | Calculated Property |
| Pvap | 12.01 | kPa | 547.07 | Calculated Property |
| Pvap | 21.62 | kPa | 569.35 | Calculated Property |
| Pvap | 36.81 | kPa | 591.64 | Calculated Property |
| Pvap | 59.73 | kPa | 613.92 | Calculated Property |
| Pvap | 92.96 | kPa | 636.20 | Calculated Property |
| Pvap | 139.49 | kPa | 658.49 | Calculated Property |
| Pvap | 202.65 | kPa | 680.77 | Calculated Property |
Similar Compounds
Find more compounds similar to 2-nonylnaphthalene.
Sources
- Cheméo Relay (1.0)
- Crippen Method
- Crippen Method
- Joback Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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