- InChI
- InChI=1S/C9H18Cl2/c1-2-3-4-5-6-7-8-9(10)11/h9H,2-8H2,1H3
- InChI Key
- FBTKIMWGAQACHU-UHFFFAOYSA-N
- Formula
- C9H18Cl2
- SMILES
- CCCCCCCCC(Cl)Cl
- Molecular Weight1
- 197.15
- CAS
- 821-88-5
- 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 | 0.5087 | Relay (1.0) Calculated Property | |
| ΔfG° | -1.40 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -270.24 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfusH° | 23.94 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 62.30 | kJ/mol | NIST |
| IE | 10.32 | eV | Relay (1.0) Calculated Property |
| log10WS | -5.42 | Relay (1.0) Calculated Property | |
| logPoct/wat | 4.541 | Crippen Calculated Property | |
| McVol | 162.150 | ml/mol | McGowan Calculated Property |
| Pc | 2167.36 | kPa | Joback Calculated Property |
| Tboil | 493.09 | K | Relay (1.0) Calculated Property |
| Tc | 680.98 | K | Relay (1.0) Calculated Property |
| Tfus | 233.81 | K | Relay (1.0) Calculated Property |
| Vc | 0.624 | m3/kmol | Relay (1.0) Calculated Property |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [222.90; 500.73] | 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 | 1.88070e+01 | |||
| Coefficient B | 8.78320e-01 | |||
| Coefficient C | -5.09800e-04 | |||
| Coefficient D | 1.13400e-07 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 222.90 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 270.75 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 313.52 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 351.57 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 385.25 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 414.92 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 440.95 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 463.69 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 483.49 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 500.73 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0070588; 0.0002918] | Pa×s | [236.03; 461.74] |
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 | -1.14710e+01 | |||
| Coefficient B | 1.53834e+03 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 236.03 | |||
| Temperature range, max. | 461.74 | |||
| η | 0.0070588 | Pa×s | 236.03 | Calculated Property |
| η | 0.0037745 | Pa×s | 261.11 | Calculated Property |
| η | 0.0022524 | Pa×s | 286.19 | Calculated Property |
| η | 0.0014607 | Pa×s | 311.27 | Calculated Property |
| η | 0.0010104 | Pa×s | 336.35 | Calculated Property |
| η | 0.0007357 | Pa×s | 361.43 | Calculated Property |
| η | 0.0005581 | Pa×s | 386.51 | Calculated Property |
| η | 0.0004379 | Pa×s | 411.59 | Calculated Property |
| η | 0.0003533 | Pa×s | 436.66 | Calculated Property |
| η | 0.0002918 | Pa×s | 461.74 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.65] | kPa | [385.92; 547.91] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.47846e+01 | |||
| Coefficient B | -4.42812e+03 | |||
| Coefficient C | -8.04700e+01 | |||
| Temperature range, min. | 385.92 | |||
| Temperature range, max. | 547.91 | |||
| Pvap | 1.33 | kPa | 385.92 | Calculated Property |
| Pvap | 2.99 | kPa | 403.92 | Calculated Property |
| Pvap | 6.15 | kPa | 421.92 | Calculated Property |
| Pvap | 11.77 | kPa | 439.92 | Calculated Property |
| Pvap | 21.17 | kPa | 457.92 | Calculated Property |
| Pvap | 36.12 | kPa | 475.91 | Calculated Property |
| Pvap | 58.81 | kPa | 493.91 | Calculated Property |
| Pvap | 91.94 | kPa | 511.91 | Calculated Property |
| Pvap | 138.67 | kPa | 529.91 | Calculated Property |
| Pvap | 202.65 | kPa | 547.91 | Calculated Property |
Similar Compounds
Find more compounds similar to 1,1-Dichlorononane.
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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