- InChI
- InChI=1S/C10H20Cl2/c11-9-7-5-3-1-2-4-6-8-10-12/h1-10H2
- InChI Key
- RBBNTRDPSVZESY-UHFFFAOYSA-N
- Formula
- C10H20Cl2
- SMILES
- ClCCCCCCCCCCCl
- Molecular Weight1
- 211.17
- CAS
- 2162-98-3
- Other Names
-
- Decamethylene dichloride
- Decane, 1,10-dichloro-
- 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).
- Inp : Non-polar retention indices.
- Ip : 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 |
|---|---|---|---|
| ω | 0.5783 | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value | |
| ΔfG° | 9.46 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -305.25 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfusH° | 30.05 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 73.10 | kJ/mol | NIST |
| IE | 10.19 | eV | Relay (1.0) Calculated Property |
| log10WS | -5.85 | Relay (1.0) Calculated Property | |
| logPoct/wat | 4.585 | Crippen Calculated Property | |
| McVol | 176.240 | ml/mol | McGowan Calculated Property |
| Pc | 2072.10 | kPa | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Inp | 1526.00 | NIST | |
| Ip | [1916.00; 1918.00] |
|
|
| Ip | 1918.00 | NIST | |
| Ip | 1916.00 | NIST | |
| Ip | 1916.00 | NIST | |
| Tboil | 522.38 | K | Relay (1.0) Calculated Property |
| Tc | 752.50 | K | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Tfus | [288.75; 288.75] | K |
|
| Tfus | 288.75 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Tfus | 288.75 ± 0.50 | K | NIST |
| Vc | 0.681 | m3/kmol | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | 61.10 | kJ/mol | 480.50 | NIST |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | 440.70 | K | 3.70 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [244.43; 551.78] | 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 | 1.95800e+01 | |||
| Coefficient B | 9.67400e-01 | |||
| Coefficient C | -5.61000e-04 | |||
| Coefficient D | 1.25800e-07 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 244.43 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 297.18 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 344.35 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 386.35 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 423.56 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 456.38 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 485.22 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 510.46 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 532.52 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 551.78 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0026199; 0.0002161] | Pa×s | [288.75; 526.75] |
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 | -1.14673e+01 | |||
| Coefficient B | 1.59468e+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. | 288.75 | |||
| Temperature range, max. | 526.75 | |||
| η | 0.0026199 | Pa×s | 288.75 | Calculated Property |
| η | 0.0016484 | Pa×s | 315.19 | Calculated Property |
| η | 0.0011143 | Pa×s | 341.64 | Calculated Property |
| η | 0.0007968 | Pa×s | 368.08 | Calculated Property |
| η | 0.0005960 | Pa×s | 394.53 | Calculated Property |
| η | 0.0004623 | Pa×s | 420.97 | Calculated Property |
| η | 0.0003696 | Pa×s | 447.42 | Calculated Property |
| η | 0.0003029 | Pa×s | 473.86 | Calculated Property |
| η | 0.0002536 | Pa×s | 500.31 | Calculated Property |
| η | 0.0002161 | Pa×s | 526.75 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.66] | kPa | [403.32; 568.86] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.48734e+01 | |||
| Coefficient B | -4.59549e+03 | |||
| Coefficient C | -8.82540e+01 | |||
| Temperature range, min. | 403.32 | |||
| Temperature range, max. | 568.86 | |||
| Pvap | 1.33 | kPa | 403.32 | Calculated Property |
| Pvap | 2.98 | kPa | 421.71 | Calculated Property |
| Pvap | 6.13 | kPa | 440.11 | Calculated Property |
| Pvap | 11.72 | kPa | 458.50 | Calculated Property |
| Pvap | 21.09 | kPa | 476.89 | Calculated Property |
| Pvap | 35.99 | kPa | 495.29 | Calculated Property |
| Pvap | 58.63 | kPa | 513.68 | Calculated Property |
| Pvap | 91.74 | kPa | 532.07 | Calculated Property |
| Pvap | 138.52 | kPa | 550.47 | Calculated Property |
| Pvap | 202.66 | kPa | 568.86 | Calculated Property |
Similar Compounds
Find more compounds similar to 1,10-Dichlorodecane.
Sources
- Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) ChEDL chemicals 1.5.2, from Bradley, J.-C.; Williams, A.; Lang, A. Jean-Claude Bradley Open Melting Point Dataset. Figshare, 2014 (CC0).
- PSRK revision IV (2005), critical constants and acentric factors of 1000 components ChEDL chemicals 1.5.2, from Horstmann, S.; Jabłoniec, A.; Krafczyk, J.; Fischer, K.; Gmehling, J. PSRK Group Contribution Equation of State: Comprehensive Revision and Extension IV, Including Critical Constants and α-Function Parameters for 1000 Components. Fluid Phase Equilib. 2005, 227, 157-164.
- Cheméo Relay (1.0)
- Crippen Method
- Crippen Method
- Joback Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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