- InChI
- InChI=1S/C3H6Cl2/c4-2-1-3-5/h1-3H2
- InChI Key
- YHRUOJUYPBUZOS-UHFFFAOYSA-N
- Formula
- C3H6Cl2
- SMILES
- ClCCCCl
- Molecular Weight1
- 112.99
- CAS
- 142-28-9
- Other Names
-
- 1,3-dichloropropane
- CH2ClCH2CH2Cl
- R 270fa
- trimethylene dichloride
- 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).
- Csat : Molar heat capacity at saturation pressure (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).
- NFPA Fire : NFPA Fire Rating.
- NFPA Health : NFPA Health Rating.
- Pc : Critical Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- n0 : Refractive Index.
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- I : Polar retention indices.
- csound,fluid : Speed of sound in fluid (m/s).
- γ : Surface Tension (N/m).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (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 | 0.2880 | KDB | |
| ΔcH°liquid | -1885.30 ± 8.40 | kJ/mol | NIST |
| ΔfG° | -49.48 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -142.84 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfusH° | 11.92 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [40.60; 41.00] | kJ/mol |
|
| ΔvapH° | 40.79 | kJ/mol | NIST |
| ΔvapH° | 41.00 | kJ/mol | NIST |
| ΔvapH° | 40.60 ± 0.10 | kJ/mol | NIST |
| ΔvapH° | 41.00 | kJ/mol | NIST |
| ΔvapH° | 40.75 ± 0.04 | kJ/mol | NIST |
| IE | [10.85; 10.93] | eV |
|
| IE | 10.89 ± 0.04 | eV | NIST |
| IE | 10.93 | eV | NIST |
| IE | 10.93 | eV | NIST |
| IE | 10.85 ± 0.05 | eV | NIST |
| log10WS | [-1.62; -1.62] |
|
|
| log10WS | -1.62 | Aq. Solubility Prediction | |
| log10WS | -1.62 | Estimated Solubility | |
| logPoct/wat | 1.854 | Crippen Calculated Property | |
| McVol | 77.610 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 3 | KDB | |
| NFPA Health | 2 | KDB | |
| Pc | 4010.00 | kPa | KDB |
| Inp | [747.20; 787.00] |
|
|
| Inp | 747.20 | NIST | |
| Inp | 751.00 | NIST | |
| Inp | 786.00 | NIST | |
| Inp | 760.00 | NIST | |
| Inp | 760.00 | NIST | |
| Inp | 760.00 | NIST | |
| Inp | 765.00 | NIST | |
| Inp | 756.00 | NIST | |
| Inp | 787.00 | NIST | |
| Inp | 765.00 | NIST | |
| Inp | 757.00 | NIST | |
| Inp | 774.80 | NIST | |
| Inp | 763.00 | NIST | |
| I | 1188.00 | NIST | |
| Tboil | [393.15; 398.15] | K |
|
| Tboil | 393.60 | K | KDB |
| Tboil | 394.00 ± 1.00 | K | NIST |
| Tboil | 393.60 | K | NIST |
| Tboil | 394.00 | K | NIST |
| Tboil | 393.15 ± 1.00 | K | NIST |
| Tboil | 393.15 ± 1.50 | K | NIST |
| Tboil | 394.35 ± 0.50 | K | NIST |
| Tboil | 393.95 ± 0.50 | K | NIST |
| Tboil | Outlier 398.15 ± 3.00 | K | NIST |
| Tboil | 393.55 ± 0.50 | K | NIST |
| Tboil | 396.15 ± 2.50 | K | NIST |
| Tboil | 393.55 ± 0.60 | K | NIST |
| Tboil | 393.70 ± 0.25 | K | NIST |
| Tboil | 393.55 ± 0.40 | K | NIST |
| Tboil | 393.70 ± 0.50 | K | NIST |
| Tboil | 393.70 ± 0.50 | K | NIST |
| Tboil | Outlier 397.15 ± 2.00 | K | NIST |
| Tc | 602.70 | K | KDB |
| Tfus | [173.40; 239.00] | K |
|
| Tfus | 174.00 | K | KDB |
| Tfus | 173.40 | K | Aq. Solubility Prediction |
| Tfus | 239.00 ± 0.02 | K | NIST |
| Vc | 0.301 | m3/kmol | KDB |
| Zc | 0.2412650 | KDB |
Temperature Dependent Properties
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.63] | kPa | [287.47; 420.41] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.44611e+01 | |||
| Coefficient B | -3.43171e+03 | |||
| Coefficient C | -4.53460e+01 | |||
| Temperature range, min. | 287.47 | |||
| Temperature range, max. | 420.41 | |||
| Pvap | 1.33 | kPa | 287.47 | Calculated Property |
| Pvap | 3.01 | kPa | 302.24 | Calculated Property |
| Pvap | 6.23 | kPa | 317.01 | Calculated Property |
| Pvap | 11.95 | kPa | 331.78 | Calculated Property |
| Pvap | 21.50 | kPa | 346.55 | Calculated Property |
| Pvap | 36.62 | kPa | 361.33 | Calculated Property |
| Pvap | 59.47 | kPa | 376.10 | Calculated Property |
| Pvap | 92.68 | kPa | 390.87 | Calculated Property |
| Pvap | 139.25 | kPa | 405.64 | Calculated Property |
| Pvap | 202.63 | kPa | 420.41 | Calculated Property |
| Pvap | [4.46e-06; 4145.08] | kPa | [173.65; 603.00] |
KDB Vapor Pressure Data
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 9.24683e+01 | |||
| Coefficient B | -7.89152e+03 | |||
| Coefficient C | -1.15542e+01 | |||
| Coefficient D | 8.02366e-06 | |||
| Temperature range, min. | 173.65 | |||
| Temperature range, max. | 603.00 | |||
| Pvap | 4.46e-06 | kPa | 173.65 | Calculated Property |
| Pvap | 5.63e-03 | kPa | 221.36 | Calculated Property |
| Pvap | 0.40 | kPa | 269.06 | Calculated Property |
| Pvap | 6.23 | kPa | 316.77 | Calculated Property |
| Pvap | 41.70 | kPa | 364.47 | Calculated Property |
| Pvap | 166.08 | kPa | 412.18 | Calculated Property |
| Pvap | 476.73 | kPa | 459.88 | Calculated Property |
| Pvap | 1107.27 | kPa | 507.59 | Calculated Property |
| Pvap | 2240.10 | kPa | 555.29 | Calculated Property |
| Pvap | 4145.08 | kPa | 603.00 | Calculated Property |
Similar Compounds
Find more compounds similar to Propane, 1,3-dichloro-.
Mixtures
- Methyl formate + Propane, 1,3-dichloro-
- Ethyl formate + Propane, 1,3-dichloro-
- Formic acid, propyl ester + Propane, 1,3-dichloro-
- Formic acid, butyl ester + Propane, 1,3-dichloro-
- Formic acid, pentyl ester + Propane, 1,3-dichloro-
- Methane, nitro- + Propane, 1,3-dichloro-
- Propanoic acid, butyl ester + Propane, 1,3-dichloro-
- Acetic acid, butyl ester + Propane, 1,3-dichloro-
- Butanoic acid, butyl ester + Propane, 1,3-dichloro-
- Butanoic acid, ethyl ester + Propane, 1,3-dichloro-
- Pentanoic acid, ethyl ester + Propane, 1,3-dichloro-
- Ethyl Acetate + Propane, 1,3-dichloro-
- Propanoic acid, ethyl ester + Propane, 1,3-dichloro-
- Cyclopentanone + Propane, 1,3-dichloro-
- 2-Butanone + Propane, 1,3-dichloro-
- Acetic acid, propyl ester + Propane, 1,3-dichloro-
- Propanoic acid, propyl ester + Propane, 1,3-dichloro-
- Butanoic acid, propyl ester + Propane, 1,3-dichloro-
- Ethane, nitro- + Propane, 1,3-dichloro-
- Propane, 1,3-dichloro- + Water
Find more mixtures with Propane, 1,3-dichloro-.
Sources
- KDB Vapor Pressure Data
- Cheméo Relay (1.0)
- Crippen Method
- Speeds of sound, isentropic compressibilities and refractive indices for some binary mixtures of nitromethane with chloroalkane at temperatures from 298.15 to 318.15 K. Comparison with theories
- Thermodynamic study of (alkyl esters + a,x-alkyl dihalides) I: HE and V E for 25 binary mixtures {xCu-1H2u-1CO2C2H5 + (1-x)a,x-ClCH2(CH2)v-2CH2Cl}, where u = 1 to 5, a = 1 and v = x = 2 to 6
- Thermodynamic study of (alkyl esters + a,x-alkyl dihalides)III. HE m and V E m for 20 binary mixtures {xCu-1H2u-1CO2C4H9 + (1 - x)a,x-ClCH2(CH2)v-2CH2Cl}, where u = 1 to 4, a = 1 and v = x = 2 to 6
- Thermodynamic study of (alkyl esters + a,x-alkyl dihalides) V. Hex and Vex for 25 binary mixtures {xCu-1H2u-1CO2CH3 + (1-x)a,x-ClCH2(CH2)v-2CH2Cl}, where u = 1 to 5, a = 1 and v = x = 2 to 6
- Isothermal (vapour + liquid) equilibria and excess Gibbs free energies in some binary (cyclopentanone + chloroalkane) mixtures at temperatures from 298.15 K to 318.15 K
- Density and refractive index in mixtures of ionic liquids and organic solvents: Correlations and predictions
- Thermodynamic study of (alkyl esters + a,x-alkyl dihalides) VII. HE m and VE m for 20 binary mixtures {xCu 1H2u 1CO2C3H7 + (1 x)a,x-ClCH2(CH2)v 2CH2Cl}, where u = 1 to 4, a = 1 and v = x = 2 to 6. An analysis of behavior using the COSMO-RS methodology
- Volumetric and optical properties for some (2-butanone + chloroalkane) binary mixtures at T = 298.15 K
- Speed of sound as a function of temperature and pressure for propane derivatives
- The additivity of surface and volumetric properties of alpha,omega-dihalogenoalkanes
- The Critical Temperatures of a Number of (i) (Chloroalkane (C3 C4) + Hydrocarbon (C6 C7)) Binary Mixtures and (ii) (Aromatic Halocarbon (Chlorobenzene, Fluorobenzene, 1,2-Dichlorobenzene, or 1,3-Dichlorobenzene) + Alkane (C8)) Binary Mixtures
- Heat Capacities of alpha,omega-Dichloroalkanes at Temperatures from 284.15 K to 353.15 K and a Group Additivity Analysis
- Isothermal Vapor Liquid Equilibria for Nitromethane and Nitroethane + 1,3-Dichloropropane Binary Systems at Temperatures between (343.15 and 363.15) K
- Determination of Henry's Law Constants Using Internal Standards with Benchmark Values
- Volumetric Study for the Binary Nitromethane with Chloroalkane Mixtures at Temperatures in the Range (298.15 to 318.15) K
- Densities and Excess Molar Volumes of the Binary Mixtures of Cyclohexanone with Chloroalkanes at Temperatures between (288.15 and 318.15) K
- Densities and Excess Molar Volumes of the Binary Mixtures of Cyclopentanone with Chloroalkanes at T = (288.15, 298.15, 308.15, and 318.15) K
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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