- InChI
- InChI=1S/C3H4Cl2/c1-3(5)2-4/h1-2H2
- InChI Key
- FALCMQXTWHPRIH-UHFFFAOYSA-N
- Formula
- C3H4Cl2
- SMILES
- C=C(Cl)CCl
- Molecular Weight1
- 110.97
- CAS
- 78-88-6
- Other Names
-
- 1,2-Dichloro-2-propene
- 2,3-DICHLOROPROPYLENE
- 2,3-Dichloro-1-propene
- 2,3-Dichloropropene
- 2,3-Dichloropropene-(1)
- 2-CHLOROALLYL CHLORIDE
- Propene, 2,3-dichloro-
- ΔcH°liquid : Standard liquid enthalpy of combustion (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- 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).
- Inp : Non-polar retention indices.
- I : Polar retention indices.
- 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 |
|---|---|---|---|
| ΔcH°liquid | -1726.20 | kJ/mol | NIST |
| ΔfG° | 29.81 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -21.09 | kJ/mol | Joback Calculated Property |
| ΔfH°liquid | -73.47 | kJ/mol | NIST |
| ΔfusH° | 9.33 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 30.45 | kJ/mol | Joback Calculated Property |
| IE | 9.82 ± 0.03 | eV | NIST |
| log10WS | -1.73 | Crippen Calculated Property | |
| logPoct/wat | 1.978 | Crippen Calculated Property | |
| McVol | 73.310 | ml/mol | McGowan Calculated Property |
| Pc | 4255.16 | kPa | Joback Calculated Property |
| Inp | [684.00; 707.00] |
|
|
| Inp | 705.00 | NIST | |
| Inp | 686.00 | NIST | |
| Inp | 707.00 | NIST | |
| Inp | 684.00 | NIST | |
| I | [1066.00; 1066.00] |
|
|
| I | 1066.00 | NIST | |
| I | 1066.00 | NIST | |
| Tboil | 367.20 | K | NIST |
| Tc | 529.79 | K | Joback Calculated Property |
| Tfus | 167.69 | K | Joback Calculated Property |
| Vc | 0.283 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [97.84; 124.34] | J/mol×K | [339.46; 529.79] |
|
| Cp,gas | 97.84 | J/mol×K | 339.46 | Joback Calculated Property |
| Cp,gas | 102.90 | J/mol×K | 371.18 | Joback Calculated Property |
| Cp,gas | 107.69 | J/mol×K | 402.90 | Joback Calculated Property |
| Cp,gas | 112.22 | J/mol×K | 434.63 | Joback Calculated Property |
| Cp,gas | 116.50 | J/mol×K | 466.35 | Joback Calculated Property |
| Cp,gas | 120.54 | J/mol×K | 498.07 | Joback Calculated Property |
| Cp,gas | 124.34 | J/mol×K | 529.79 | Joback Calculated Property |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.67] | kPa | [272.20; 390.24] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.50651e+01 | |||
| Coefficient B | -3.38646e+03 | |||
| Coefficient C | -4.30370e+01 | |||
| Temperature range, min. | 272.20 | |||
| Temperature range, max. | 390.24 | |||
| Pvap | 1.33 | kPa | 272.20 | Calculated Property |
| Pvap | 2.97 | kPa | 285.32 | Calculated Property |
| Pvap | 6.08 | kPa | 298.43 | Calculated Property |
| Pvap | 11.62 | kPa | 311.55 | Calculated Property |
| Pvap | 20.91 | kPa | 324.66 | Calculated Property |
| Pvap | 35.71 | kPa | 337.78 | Calculated Property |
| Pvap | 58.26 | kPa | 350.89 | Calculated Property |
| Pvap | 91.33 | kPa | 364.01 | Calculated Property |
| Pvap | 138.19 | kPa | 377.12 | Calculated Property |
| Pvap | 202.67 | kPa | 390.24 | Calculated Property |
| Pvap | [2.19e-03; 4352.68] | kPa | [191.50; 577.00] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 5.21947e+01 | |||
| Coefficient B | -5.61113e+03 | |||
| Coefficient C | -5.54617e+00 | |||
| Coefficient D | 3.51475e-06 | |||
| Temperature range, min. | 191.50 | |||
| Temperature range, max. | 577.00 | |||
| Pvap | 2.19e-03 | kPa | 191.50 | Calculated Property |
| Pvap | 0.16 | kPa | 234.33 | Calculated Property |
| Pvap | 2.79 | kPa | 277.17 | Calculated Property |
| Pvap | 20.65 | kPa | 320.00 | Calculated Property |
| Pvap | 90.37 | kPa | 362.83 | Calculated Property |
| Pvap | 279.65 | kPa | 405.67 | Calculated Property |
| Pvap | 682.96 | kPa | 448.50 | Calculated Property |
| Pvap | 1411.92 | kPa | 491.33 | Calculated Property |
| Pvap | 2589.63 | kPa | 534.17 | Calculated Property |
| Pvap | 4352.68 | kPa | 577.00 | Calculated Property |
Similar Compounds
Find more compounds similar to 1-Propene, 2,3-dichloro-.
Sources
- KDB Vapor Pressure Data
- Crippen Method
- Crippen Method
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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