- InChI
- InChI=1S/C7H15Cl/c1-6(2)5-7(3,4)8/h6H,5H2,1-4H3
- InChI Key
- DQOHPSPKVODKLV-UHFFFAOYSA-N
- Formula
- C7H15Cl
- SMILES
- CC(C)CC(C)(C)Cl
- Molecular Weight1
- 134.65
- CAS
- 35951-33-8
- 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).
- 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).
- 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 | 0.3062 | Relay (1.0) Calculated Property | |
| ΔfG° | -3.47 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -237.27 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfH°liquid | -277.00 ± 2.00 | kJ/mol | NIST |
| ΔfusH° | 7.15 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 40.23 | kJ/mol | Relay (1.0) Calculated Property |
| IE | 10.04 | eV | Relay (1.0) Calculated Property |
| log10WS | -3.82 | Relay (1.0) Calculated Property | |
| logPoct/wat | 3.050 | Crippen Calculated Property | |
| McVol | 121.730 | ml/mol | McGowan Calculated Property |
| Pc | 2770.08 | kPa | Joback Calculated Property |
| Tboil | 389.25 | K | Relay (1.0) Calculated Property |
| Tc | 594.03 | K | Relay (1.0) Calculated Property |
| Tfus | 194.33 | K | Relay (1.0) Calculated Property |
| Vc | 0.446 | m3/kmol | Relay (1.0) Calculated Property |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [165.61; 390.74] | 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 | -1.67390e+01 | |||
| Coefficient B | 8.07380e-01 | |||
| Coefficient C | -5.52400e-04 | |||
| Coefficient D | 1.52500e-07 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 165.61 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 206.51 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 242.31 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 273.50 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 300.56 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 323.97 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 344.20 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 361.76 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 377.11 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 390.74 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0171872; 0.0002733] | Pa×s | [185.99; 406.75] |
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 | -1.16943e+01 | |||
| Coefficient B | 1.41924e+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. | 185.99 | |||
| Temperature range, max. | 406.75 | |||
| η | 0.0171872 | Pa×s | 185.99 | Calculated Property |
| η | 0.0070643 | Pa×s | 210.52 | Calculated Property |
| η | 0.0034956 | Pa×s | 235.05 | Calculated Property |
| η | 0.0019757 | Pa×s | 259.58 | Calculated Property |
| η | 0.0012323 | Pa×s | 284.11 | Calculated Property |
| η | 0.0008285 | Pa×s | 308.64 | Calculated Property |
| η | 0.0005906 | Pa×s | 333.16 | Calculated Property |
| η | 0.0004410 | Pa×s | 357.69 | Calculated Property |
| η | 0.0003418 | Pa×s | 382.22 | Calculated Property |
| η | 0.0002733 | Pa×s | 406.75 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.66] | kPa | [301.92; 457.70] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.33500e+01 | |||
| Coefficient B | -3.25580e+03 | |||
| Coefficient C | -5.26700e+01 | |||
| Temperature range, min. | 301.92 | |||
| Temperature range, max. | 457.70 | |||
| Pvap | 1.33 | kPa | 301.92 | Calculated Property |
| Pvap | 3.11 | kPa | 319.23 | Calculated Property |
| Pvap | 6.56 | kPa | 336.54 | Calculated Property |
| Pvap | 12.68 | kPa | 353.85 | Calculated Property |
| Pvap | 22.81 | kPa | 371.16 | Calculated Property |
| Pvap | 38.63 | kPa | 388.46 | Calculated Property |
| Pvap | 62.14 | kPa | 405.77 | Calculated Property |
| Pvap | 95.61 | kPa | 423.08 | Calculated Property |
| Pvap | 141.55 | kPa | 440.39 | Calculated Property |
| Pvap | 202.66 | kPa | 457.70 | Calculated Property |
Similar Compounds
Find more compounds similar to 2-Chloro-2,4-dimethylpentane.
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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