- InChI
- InChI=1S/C14H29Cl/c1-2-3-4-5-6-7-8-9-10-11-12-13-14-15/h2-14H2,1H3
- InChI Key
- RNHWYOLIEJIAMV-UHFFFAOYSA-N
- Formula
- C14H29Cl
- SMILES
- CCCCCCCCCCCCCCCl
- Molecular Weight1
- 232.83
- CAS
- 2425-54-9
- Other Names
-
- 1-Chlorotetradecane
- Myristyl chloride
- Tetradecyl chloride
- n-Tetradecyl chloride
- 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).
- 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.
- I : Polar retention indices.
- Tboil : Normal Boiling Point Temperature (K).
- Tboilr : Boiling point at reduced pressure (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 |
|---|---|---|---|
| ΔfG° | 55.07 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -348.03 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 36.21 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 86.60 | kJ/mol | NIST |
| log10WS | -5.84 | Crippen Calculated Property | |
| logPoct/wat | 5.926 | Crippen Calculated Property | |
| McVol | 220.360 | ml/mol | McGowan Calculated Property |
| Pc | 1480.43 | kPa | Joback Calculated Property |
| Inp | [1659.80; 1674.00] |
|
|
| Inp | 1659.80 | NIST | |
| Inp | 1668.00 | NIST | |
| Inp | 1666.00 | NIST | |
| Inp | 1662.00 | NIST | |
| Inp | 1674.00 | NIST | |
| Inp | 1659.80 | NIST | |
| Inp | 1668.00 | NIST | |
| Inp | 1662.00 | NIST | |
| I | [1873.00; 1890.00] |
|
|
| I | 1890.00 | NIST | |
| I | 1886.00 | NIST | |
| I | 1873.00 | NIST | |
| I | 1889.00 | NIST | |
| I | 1889.00 | NIST | |
| Tboil | 557.15 | K | Joback Calculated Property |
| Tc | 721.91 | K | Joback Calculated Property |
| Tfus | 277.46 | K | Joback Calculated Property |
| Vc | 0.869 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [543.05; 637.57] | J/mol×K | [557.15; 721.91] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 540 560 580 600 620 640 600 650 700 | ||||
| Cp,gas | 543.05 | J/mol×K | 557.15 | Joback Calculated Property |
| Cp,gas | 560.51 | J/mol×K | 584.61 | Joback Calculated Property |
| Cp,gas | 577.26 | J/mol×K | 612.07 | Joback Calculated Property |
| Cp,gas | 593.32 | J/mol×K | 639.53 | Joback Calculated Property |
| Cp,gas | 608.71 | J/mol×K | 666.99 | Joback Calculated Property |
| Cp,gas | 623.45 | J/mol×K | 694.45 | Joback Calculated Property |
| Cp,gas | 637.57 | J/mol×K | 721.91 | Joback Calculated Property |
| η | [0.0001767; 0.0045884] | Pa×s | [277.46; 557.15] |
|
|
T(K) Dynamic viscosity (Pa×s) 0 1.00e-3 2.00e-3 3.00e-3 4.00e-3 5.00e-3 300 400 500 | ||||
| η | 0.0045884 | Pa×s | 277.46 | Joback Calculated Property |
| η | 0.0018047 | Pa×s | 324.08 | Joback Calculated Property |
| η | 0.0008975 | Pa×s | 370.69 | Joback Calculated Property |
| η | 0.0005218 | Pa×s | 417.31 | Joback Calculated Property |
| η | 0.0003383 | Pa×s | 463.92 | Joback Calculated Property |
| η | 0.0002374 | Pa×s | 510.53 | Joback Calculated Property |
| η | 0.0001767 | Pa×s | 557.15 | Joback Calculated Property |
| ΔvapH | [68.70; 80.20] | kJ/mol | [343.00; 492.00] |
|
|
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 68 70 72 74 76 78 80 350 400 450 | ||||
| ΔvapH | 80.20 | kJ/mol | 343.00 | NIST |
| ΔvapH | 78.00 | kJ/mol | 343.00 | NIST |
| ΔvapH | 74.40 | kJ/mol | 343.00 | NIST |
| ΔvapH | 72.90 | kJ/mol | 343.00 | NIST |
| ΔvapH | 68.70 | kJ/mol | 492.00 | NIST |
| ρl | [770.10; 868.50] | kg/m3 | [288.15; 423.15] |
|
|
T(K) Liquid Density (kg/m3) 780 800 820 840 860 300 350 400 | ||||
| ρl | 868.50 | kg/m3 | 288.15 | Density... |
| ρl | 864.90 | kg/m3 | 293.15 | Density... |
| ρl | 861.00 | kg/m3 | 298.15 | Density... |
| ρl | 857.50 | kg/m3 | 303.15 | Density... |
| ρl | 843.30 | kg/m3 | 323.15 | Density... |
| ρl | 829.00 | kg/m3 | 343.15 | Density... |
| ρl | 814.30 | kg/m3 | 363.15 | Density... |
| ρl | 792.50 | kg/m3 | 393.15 | Density... |
| ρl | 770.10 | kg/m3 | 423.15 | Density... |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | 413.70 | K | 0.50 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.63] | kPa | [437.00; 602.17] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.55734e+01 | |||
| Coefficient B | -5.15727e+03 | |||
| Coefficient C | -9.96100e+01 | |||
| Temperature range, min. | 437.00 | |||
| Temperature range, max. | 602.17 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 450 500 550 600 | ||||
| Pvap | 1.33 | kPa | 437.00 | Calculated Property |
| Pvap | 2.93 | kPa | 455.35 | Calculated Property |
| Pvap | 5.97 | kPa | 473.70 | Calculated Property |
| Pvap | 11.38 | kPa | 492.06 | Calculated Property |
| Pvap | 20.47 | kPa | 510.41 | Calculated Property |
| Pvap | 35.02 | kPa | 528.76 | Calculated Property |
| Pvap | 57.33 | kPa | 547.11 | Calculated Property |
| Pvap | 90.27 | kPa | 565.47 | Calculated Property |
| Pvap | 137.34 | kPa | 583.82 | Calculated Property |
| Pvap | 202.63 | kPa | 602.17 | Calculated Property |
Similar Compounds
Find more compounds similar to Tetradecane, 1-chloro-.
Sources
- Crippen Method
- Crippen Method
- Density of Some 1-Chloroalkanes within the Temperature Range from (253.15 to 423.15) K
- Joback Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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