- 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).
- 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.
Cheméo is a service of Céondo GmbH, since 2007, we provide simulation, modelling and software development services for the industry.
Do not hesitate to contact us for your projects.
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 | -136.73 | kJ/mol | Joback 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. Sol... | |
| log10WS | -1.62 | Estimat... | |
| 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 | 393.60 | K | KDB |
| Tc | 602.70 | K | KDB |
| Tfus | [173.40; 239.00] | K |
|
| Tfus | 174.00 | K | KDB |
| Tfus | 173.40 | K | Aq. Sol... |
| Tfus | 239.00 ± 0.02 | K | NIST |
| Vc | 0.301 | m3/kmol | KDB |
| Zc | 0.2412650 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [110.16; 141.21] | J/mol×K | [342.90; 525.16] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 110 115 120 125 130 135 140 350 400 450 500 | ||||
| Cp,gas | 110.16 | J/mol×K | 342.90 | Joback Calculated Property |
| Cp,gas | 115.92 | J/mol×K | 373.28 | Joback Calculated Property |
| Cp,gas | 121.44 | J/mol×K | 403.65 | Joback Calculated Property |
| Cp,gas | 126.72 | J/mol×K | 434.03 | Joback Calculated Property |
| Cp,gas | 131.77 | J/mol×K | 464.41 | Joback Calculated Property |
| Cp,gas | 136.60 | J/mol×K | 494.78 | Joback Calculated Property |
| Cp,gas | 141.21 | J/mol×K | 525.16 | Joback Calculated Property |
| Cp,liquid | 157.00 | J/mol×K | 298.15 | NIST |
| η | [0.0003452; 0.0037023] | Pa×s | [183.41; 342.90] |
|
|
T(K) Dynamic viscosity (Pa×s) 5.00e-4 1.00e-3 1.50e-3 2.00e-3 2.50e-3 3.00e-3 3.50e-3 4.00e-3 200 250 300 | ||||
| η | 0.0037023 | Pa×s | 183.41 | Joback Calculated Property |
| η | 0.0019411 | Pa×s | 209.99 | Joback Calculated Property |
| η | 0.0011766 | Pa×s | 236.57 | Joback Calculated Property |
| η | 0.0007891 | Pa×s | 263.15 | Joback Calculated Property |
| η | 0.0005695 | Pa×s | 289.74 | Joback Calculated Property |
| η | 0.0004342 | Pa×s | 316.32 | Joback Calculated Property |
| η | 0.0003452 | Pa×s | 342.90 | Joback Calculated Property |
| ΔvapH | [33.89; 39.00] | kJ/mol | [371.00; 394.00] |
|
| ΔvapH | 39.00 | kJ/mol | 371.00 | NIST |
| ΔvapH | 33.89 | kJ/mol | 393.60 | KDB |
| ΔvapH | 35.18 | kJ/mol | 394.00 | NIST |
| n0 | [1.44550; 1.44620] | [298.15; 298.15] |
|
|
| n0 | 1.44550 | 298.15 | Thermod... | |
| n0 | 1.44590 | 298.15 | Isother... | |
| n0 | 1.44600 | 298.15 | Density... | |
| n0 | 1.44620 | 298.15 | Isother... | |
| ρl | [1154.65; 1191.93] | kg/m3 | [288.15; 318.15] |
|
|
T(K) Liquid Density (kg/m3) 1160 1170 1180 1190 290 300 310 | ||||
| ρl | 1191.92 | kg/m3 | 288.15 | Densiti... |
| ρl | 1191.93 | kg/m3 | 288.15 | Densiti... |
| ρl | 1179.58 | kg/m3 | 298.15 | Densiti... |
| ρl | 1179.20 | kg/m3 | 298.15 | Speed o... |
| ρl | 1180.10 | kg/m3 | 298.15 | Volumet... |
| ρl | 1179.56 | kg/m3 | 298.15 | Densiti... |
| ρl | 1180.50 | kg/m3 | 298.15 | Volumet... |
| ρl | 1167.16 | kg/m3 | 308.15 | Densiti... |
| ρl | 1167.70 | kg/m3 | 308.15 | Volumet... |
| ρl | 1167.14 | kg/m3 | 308.15 | Densiti... |
| ρl | 1154.67 | kg/m3 | 318.15 | Densiti... |
| ρl | 1155.21 | kg/m3 | 318.15 | Volumet... |
| ρl | 1154.65 | kg/m3 | 318.15 | Densiti... |
| csound,fluid | [1163.22; 1236.45] | m/s | [298.15; 318.15] |
|
| csound,fluid | 1236.45 | m/s | 298.15 | Speeds ... |
| csound,fluid | 1199.72 | m/s | 308.15 | Speeds ... |
| csound,fluid | 1163.22 | m/s | 318.15 | Speeds ... |
| γ | [0.03; 0.03] | N/m | [293.15; 313.15] |
|
|
T(K) Surface Tension (N/m) 0.03 0.03 0.03 0.03 0.03 0.03 295 300 305 310 | ||||
| γ | 0.03 | N/m | 293.15 | The add... |
| γ | 0.03 | N/m | 298.15 | The add... |
| γ | 0.03 | N/m | 303.15 | The add... |
| γ | 0.03 | N/m | 308.15 | The add... |
| γ | 0.03 | N/m | 313.15 | The add... |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.63] | kPa | [287.47; 420.41] |
The Yaw...
|
| 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 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 300 350 400 | ||||
| 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 Vap...
|
| 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 | |||
|
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 200 400 600 | ||||
| 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
- Methane, nitro- + Propane, 1,3-dichloro-
- Butanoic acid, ethyl ester + Propane, 1,3-dichloro-
- Pentanoic acid, ethyl ester + Propane, 1,3-dichloro-
- Ethyl formate + Propane, 1,3-dichloro-
- Ethyl Acetate + Propane, 1,3-dichloro-
- Propanoic acid, ethyl ester + Propane, 1,3-dichloro-
- Formic acid, butyl ester + 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-
- Cyclopentanone + Propane, 1,3-dichloro-
- Formic acid, propyl ester + Propane, 1,3-dichloro-
- n-Propyl acetate + Propane, 1,3-dichloro-
- Propanoic acid, propyl ester + Propane, 1,3-dichloro-
- Butanoic acid, propyl ester + Propane, 1,3-dichloro-
- 2-Butanone + Propane, 1,3-dichloro-
- Benzene + Propane, 1,3-dichloro-
- Propane, 1,3-dichloro- + Cyclohexane
- Butane, 2,2-dimethyl- + Propane, 1,3-dichloro-
- n-Hexane + Propane, 1,3-dichloro-
Find more mixtures with Propane, 1,3-dichloro-.
Sources
- KDB Pure (Korean Thermophysical Properties Databank)
- KDB Vapor Pressure Data
- 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
Note: Cheméo is only indexing the data, follow the source links to retrieve the latest data. The source is also providing more information like the publication year, authors and more. Take the time to validate and double check the source of the data.