- InChI
- InChI=1S/C3H6Cl2/c1-3(2,4)5/h1-2H3
- InChI Key
- ZEOVXNVKXIPWMS-UHFFFAOYSA-N
- Formula
- C3H6Cl2
- SMILES
- CC(C)(Cl)Cl
- Molecular Weight1
- 112.99
- CAS
- 594-20-7
- Other Names
-
- 2,2-Dichloropropane
- DIMETHYLDICHLOROMETHANE
- dichlorodimethylmethane
- isopropylidene chloride
- ω : Acentric Factor.
- ΔcH°liquid : Standard liquid enthalpy of combustion (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,liquid : Liquid phase 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).
- ΔfusH : Enthalpy of fusion at a given temperature (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).
- Inp : Non-polar retention indices.
- ΔfusS : Entropy of fusion at a given temperature (J/mol×K).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Ttriple : Triple Point Temperature (K).
- Vc : Critical Volume (m3/kmol).
- Zc : Critical Compressibility.
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.1980 | KDB | |
| ΔcH°liquid | -1879.50 ± 8.40 | kJ/mol | NIST |
| ΔfG° | -46.64 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | [-176.70; -173.00] | kJ/mol |
|
| ΔfH°gas | -176.70 | kJ/mol | NIST |
| ΔfH°gas | -173.00 ± 8.80 | kJ/mol | NIST |
| ΔfH°liquid | -206.00 ± 8.40 | kJ/mol | NIST |
| ΔfusH° | 4.51 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [32.10; 33.00] | kJ/mol |
|
| ΔvapH° | 32.10 | kJ/mol | NIST |
| ΔvapH° | 33.00 ± 1.00 | kJ/mol | NIST |
| log10WS | -1.99 | Crippen Calculated Property | |
| logPoct/wat | 2.200 | Crippen Calculated Property | |
| McVol | 77.610 | ml/mol | McGowan Calculated Property |
| Pc | 4100.00 | kPa | KDB |
| Inp | [584.00; 619.00] |
|
|
| Inp | 602.00 | NIST | |
| Inp | 619.00 | NIST | |
| Inp | 605.00 | NIST | |
| Inp | Outlier 584.00 | NIST | |
| Inp | 605.00 | NIST | |
| Inp | 605.00 | NIST | |
| Inp | 598.00 | NIST | |
| Inp | 608.00 | NIST | |
| Inp | 604.00 | NIST | |
| Inp | 605.00 | NIST | |
| Inp | 602.00 | NIST | |
| Inp | 619.00 | NIST | |
| Tboil | [342.01; 342.85] | K |
|
| Tboil | 342.50 | K | KDB |
| Tboil | 342.50 | K | NIST |
| Tboil | 342.50 ± 0.30 | K | NIST |
| Tboil | 342.35 ± 0.50 | K | NIST |
| Tboil | 342.01 ± 0.40 | K | NIST |
| Tboil | 342.45 ± 0.40 | K | NIST |
| Tboil | 342.85 ± 0.60 | K | NIST |
| Tboil | 342.25 ± 0.70 | K | NIST |
| Tc | 539.50 | K | KDB |
| Tfus | [238.50; 240.20] | K |
|
| Tfus | 239.00 | K | KDB |
| Tfus | 240.20 ± 1.00 | K | NIST |
| Tfus | 238.80 ± 0.40 | K | NIST |
| Tfus | 238.50 ± 0.60 | K | NIST |
| Ttriple | 239.25 ± 0.05 | K | NIST |
| Vc | 0.290 | m3/kmol | KDB |
| Zc | 0.2655230 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [110.80; 147.36] | J/mol×K | [339.67; 535.07] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 110 120 130 140 150 350 400 450 500 | ||||
| Cp,gas | 110.80 | J/mol×K | 339.67 | Joback Calculated Property |
| Cp,gas | 118.00 | J/mol×K | 372.24 | Joback Calculated Property |
| Cp,gas | 124.73 | J/mol×K | 404.80 | Joback Calculated Property |
| Cp,gas | 131.01 | J/mol×K | 437.37 | Joback Calculated Property |
| Cp,gas | 136.85 | J/mol×K | 469.93 | Joback Calculated Property |
| Cp,gas | 142.29 | J/mol×K | 502.50 | Joback Calculated Property |
| Cp,gas | 147.36 | J/mol×K | 535.07 | Joback Calculated Property |
| Cp,liquid | [150.24; 161.13] | J/mol×K | [260.64; 329.56] |
|
|
T(K) Liquid phase heat capacity (J/mol×K) 150 152 154 156 158 160 162 260 280 300 320 | ||||
| Cp,liquid | 150.33 | J/mol×K | 260.64 | Heat ca... |
| Cp,liquid | 150.49 | J/mol×K | 260.64 | Heat ca... |
| Cp,liquid | 150.24 | J/mol×K | 260.64 | Heat ca... |
| Cp,liquid | 151.41 | J/mol×K | 268.30 | Heat ca... |
| Cp,liquid | 151.24 | J/mol×K | 268.30 | Heat ca... |
| Cp,liquid | 150.99 | J/mol×K | 268.30 | Heat ca... |
| Cp,liquid | 151.40 | J/mol×K | 270.00 | NIST |
| Cp,liquid | 152.32 | J/mol×K | 278.52 | Heat ca... |
| Cp,liquid | 152.24 | J/mol×K | 278.52 | Heat ca... |
| Cp,liquid | 152.32 | J/mol×K | 278.52 | Heat ca... |
| Cp,liquid | 154.07 | J/mol×K | 288.72 | Heat ca... |
| Cp,liquid | 153.98 | J/mol×K | 288.72 | Heat ca... |
| Cp,liquid | 153.82 | J/mol×K | 288.72 | Heat ca... |
| Cp,liquid | 155.65 | J/mol×K | 298.93 | Heat ca... |
| Cp,liquid | 154.98 | J/mol×K | 298.93 | Heat ca... |
| Cp,liquid | 155.65 | J/mol×K | 298.93 | Heat ca... |
| Cp,liquid | 157.39 | J/mol×K | 309.14 | Heat ca... |
| Cp,liquid | 156.98 | J/mol×K | 309.14 | Heat ca... |
| Cp,liquid | 157.14 | J/mol×K | 309.14 | Heat ca... |
| Cp,liquid | 158.81 | J/mol×K | 319.35 | Heat ca... |
| Cp,liquid | 158.89 | J/mol×K | 319.35 | Heat ca... |
| Cp,liquid | 159.22 | J/mol×K | 319.35 | Heat ca... |
| Cp,liquid | 161.13 | J/mol×K | 329.56 | Heat ca... |
| Cp,liquid | 160.22 | J/mol×K | 329.56 | Heat ca... |
| Cp,liquid | 160.22 | J/mol×K | 329.56 | Heat ca... |
| η | [0.0004217; 0.0074107] | Pa×s | [185.83; 339.67] |
|
|
T(K) Dynamic viscosity (Pa×s) 0 1.00e-3 2.00e-3 3.00e-3 4.00e-3 5.00e-3 6.00e-3 7.00e-3 8.00e-3 200 250 300 | ||||
| η | 0.0074107 | Pa×s | 185.83 | Joback Calculated Property |
| η | 0.0034404 | Pa×s | 211.47 | Joback Calculated Property |
| η | 0.0018855 | Pa×s | 237.11 | Joback Calculated Property |
| η | 0.0011620 | Pa×s | 262.75 | Joback Calculated Property |
| η | 0.0007805 | Pa×s | 288.39 | Joback Calculated Property |
| η | 0.0005595 | Pa×s | 314.03 | Joback Calculated Property |
| η | 0.0004217 | Pa×s | 339.67 | Joback Calculated Property |
| ΔfusH | [2.34; 10.00] | kJ/mol | [188.00; 239.60] |
|
| ΔfusH | 5.98 | kJ/mol | 188.00 | NIST |
| ΔfusH | 2.34 | kJ/mol | 239.30 | NIST |
| ΔfusH | 2.34 | kJ/mol | 239.30 | NIST |
| ΔfusH | 10.00 | kJ/mol | 239.60 | NIST |
| ΔvapH | [29.29; 33.20] | kJ/mol | [322.50; 342.50] |
|
| ΔvapH | 33.20 | kJ/mol | 322.50 | NIST |
| ΔvapH | 29.29 | kJ/mol | 342.50 | KDB |
| ΔfusS | [9.62; 31.80] | J/mol×K | [188.00; 239.30] |
|
| ΔfusS | 31.80 | J/mol×K | 188.00 | NIST |
| ΔfusS | 9.62 | J/mol×K | 239.30 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [0.65; 203.07] | kPa | [239.36; 366.23] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.37772e+01 | |||
| Coefficient B | -2.65703e+03 | |||
| Coefficient C | -5.22970e+01 | |||
| Temperature range, min. | 239.36 | |||
| Temperature range, max. | 366.23 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 250 300 350 | ||||
| Pvap | 0.65 | kPa | 239.36 | Calculated Property |
| Pvap | 1.77 | kPa | 253.46 | Calculated Property |
| Pvap | 4.19 | kPa | 267.55 | Calculated Property |
| Pvap | 8.96 | kPa | 281.65 | Calculated Property |
| Pvap | 17.52 | kPa | 295.75 | Calculated Property |
| Pvap | 31.83 | kPa | 309.84 | Calculated Property |
| Pvap | 54.38 | kPa | 323.94 | Calculated Property |
| Pvap | 88.10 | kPa | 338.04 | Calculated Property |
| Pvap | 136.41 | kPa | 352.13 | Calculated Property |
| Pvap | 203.07 | kPa | 366.23 | Calculated Property |
| Pvap | [4.07; 4046.37] | kPa | [267.15; 539.46] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 7.32592e+01 | |||
| Coefficient B | -6.22039e+03 | |||
| Coefficient C | -8.76861e+00 | |||
| Coefficient D | 5.96757e-06 | |||
| Temperature range, min. | 267.15 | |||
| Temperature range, max. | 539.46 | |||
|
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 3500 4000 300 400 500 | ||||
| Pvap | 4.07 | kPa | 267.15 | Calculated Property |
| Pvap | 18.79 | kPa | 297.41 | Calculated Property |
| Pvap | 62.06 | kPa | 327.66 | Calculated Property |
| Pvap | 161.14 | kPa | 357.92 | Calculated Property |
| Pvap | 350.75 | kPa | 388.18 | Calculated Property |
| Pvap | 669.34 | kPa | 418.43 | Calculated Property |
| Pvap | 1156.48 | kPa | 448.69 | Calculated Property |
| Pvap | 1852.37 | kPa | 478.95 | Calculated Property |
| Pvap | 2799.54 | kPa | 509.20 | Calculated Property |
| Pvap | 4046.37 | kPa | 539.46 | Calculated Property |
Similar Compounds
Find more compounds similar to Propane, 2,2-dichloro-.
Mixtures
Sources
- KDB Vapor Pressure Data
- Crippen Method
- Crippen Method
- Heat capacities of selected chlorohydrocarbons
- Determination of Henry's Law Constants Using Internal Standards with Benchmark Values
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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