- InChI
- InChI=1S/C24H49Cl/c1-2-3-4-5-6-7-8-9-10-11-12-13-14-15-16-17-18-19-20-21-22-23-24-25/h2-24H2,1H3
- InChI Key
- SUSHJBUUCQMSOK-UHFFFAOYSA-N
- Formula
- C24H49Cl
- SMILES
- CCCCCCCCCCCCCCCCCCCCCCCCCl
- Molecular Weight1
- 373.10
- CAS
- 6422-18-0
- 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).
- 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).
- 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 | 1.0504 | Relay (1.0) Calculated Property | |
| ΔfG° | 139.27 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -584.63 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfusH° | 62.11 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 136.29 | kJ/mol | Relay (1.0) Calculated Property |
| IE | 10.45 | eV | Relay (1.0) Calculated Property |
| log10WS | -9.76 | Relay (1.0) Calculated Property | |
| logPoct/wat | 9.827 | Crippen Calculated Property | |
| McVol | 361.260 | ml/mol | McGowan Calculated Property |
| Pc | 789.49 | kPa | Joback Calculated Property |
| Tboil | 612.02 | K | Relay (1.0) Calculated Property |
| Tc | 807.68 | K | Relay (1.0) Calculated Property |
| Tfus | 322.88 | K | Relay (1.0) Calculated Property |
| Vc | 1.447 | m3/kmol | Relay (1.0) Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | 72.40 | kJ/mol | 658.50 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [528.02; 1265.78] | 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 | -6.03700e+00 | |||
| Coefficient B | 2.29062e+00 | |||
| Coefficient C | -1.30220e-03 | |||
| Coefficient D | 2.83400e-07 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 528.02 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 653.90 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 766.72 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 867.36 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 956.72 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 1035.71 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 1105.21 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 1166.13 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 1219.35 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 1265.78 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0017237; 0.0000893] | Pa×s | [390.16; 674.17] |
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 | -1.33901e+01 | |||
| Coefficient B | 2.74160e+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. | 390.16 | |||
| Temperature range, max. | 674.17 | |||
| η | 0.0017237 | Pa×s | 390.16 | Calculated Property |
| η | 0.0010188 | Pa×s | 421.72 | Calculated Property |
| η | 0.0006480 | Pa×s | 453.27 | Calculated Property |
| η | 0.0004371 | Pa×s | 484.83 | Calculated Property |
| η | 0.0003094 | Pa×s | 516.39 | Calculated Property |
| η | 0.0002279 | Pa×s | 547.94 | Calculated Property |
| η | 0.0001735 | Pa×s | 579.50 | Calculated Property |
| η | 0.0001359 | Pa×s | 611.06 | Calculated Property |
| η | 0.0001090 | Pa×s | 642.62 | Calculated Property |
| η | 0.0000893 | Pa×s | 674.17 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.64] | kPa | [531.52; 791.15] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.30333e+01 | |||
| Coefficient B | -5.08636e+03 | |||
| Coefficient C | -1.32456e+02 | |||
| Temperature range, min. | 531.52 | |||
| Temperature range, max. | 791.15 | |||
| Pvap | 1.33 | kPa | 531.52 | Calculated Property |
| Pvap | 3.15 | kPa | 560.37 | Calculated Property |
| Pvap | 6.67 | kPa | 589.22 | Calculated Property |
| Pvap | 12.92 | kPa | 618.06 | Calculated Property |
| Pvap | 23.25 | kPa | 646.91 | Calculated Property |
| Pvap | 39.31 | kPa | 675.76 | Calculated Property |
| Pvap | 63.02 | kPa | 704.61 | Calculated Property |
| Pvap | 96.56 | kPa | 733.45 | Calculated Property |
| Pvap | 142.27 | kPa | 762.30 | Calculated Property |
| Pvap | 202.64 | kPa | 791.15 | Calculated Property |
Similar Compounds
Find more compounds similar to 1-Chlorotetracosane.
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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