- InChI
- InChI=1S/C5H10Cl2/c6-4-2-1-3-5-7/h1-5H2
- InChI Key
- LBKDGROORAKTLC-UHFFFAOYSA-N
- Formula
- C5H10Cl2
- SMILES
- ClCCCCCCl
- Molecular Weight1
- 141.04
- CAS
- 628-76-2
- Other Names
-
- 1,5-Dichloropentane
- AMYLENE CHLORIDE
- PENTAMETHYLENE CHLORIDE
- Pentamethylene dichloride
- 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).
- 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.
- Inp : Non-polar retention indices.
- I : Polar retention indices.
- γ : Surface Tension (N/m).
- 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 |
|---|---|---|---|
| ΔfG° | -32.64 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -178.01 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 17.10 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [50.71; 52.20] | kJ/mol |
|
| ΔvapH° | 50.71 | kJ/mol | NIST |
| ΔvapH° | 52.20 | kJ/mol | NIST |
| ΔvapH° | 51.30 ± 0.80 | kJ/mol | NIST |
| log10WS | -2.22 | Crippen Calculated Property | |
| logPoct/wat | 2.634 | Crippen Calculated Property | |
| McVol | 105.790 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 3 | KDB | |
| NFPA Health | 2 | KDB | |
| Pc | 3184.73 | kPa | Joback Calculated Property |
| Inp | [1002.00; 1028.00] |
|
|
| Inp | 1010.00 | NIST | |
| Inp | 1028.00 | NIST | |
| Inp | 1028.00 | NIST | |
| Inp | 1002.00 | NIST | |
| Inp | 1010.00 | NIST | |
| Inp | 1028.00 | NIST | |
| I | 1444.00 | NIST | |
| Tboil | [451.15; 455.15] | K |
|
| Tboil | 453.20 | K | NIST |
| Tboil | 451.15 ± 2.00 | K | NIST |
| Tboil | 455.15 ± 0.50 | K | NIST |
| Tboil | 453.15 ± 1.00 | K | NIST |
| Tc | 569.78 | K | Joback Calculated Property |
| Tfus | 205.95 | K | Joback Calculated Property |
| Vc | 0.413 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [175.74; 223.13] | J/mol×K | [388.66; 569.78] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 180 190 200 210 220 400 450 500 550 | ||||
| Cp,gas | 175.74 | J/mol×K | 388.66 | Joback Calculated Property |
| Cp,gas | 184.54 | J/mol×K | 418.85 | Joback Calculated Property |
| Cp,gas | 192.96 | J/mol×K | 449.03 | Joback Calculated Property |
| Cp,gas | 201.02 | J/mol×K | 479.22 | Joback Calculated Property |
| Cp,gas | 208.73 | J/mol×K | 509.41 | Joback Calculated Property |
| Cp,gas | 216.09 | J/mol×K | 539.60 | Joback Calculated Property |
| Cp,gas | 223.13 | J/mol×K | 569.78 | Joback Calculated Property |
| Cp,liquid | [209.65; 218.76] | J/mol×K | [283.15; 323.15] |
|
|
T(K) Liquid phase heat capacity (J/mol×K) 210 212 214 216 218 290 300 310 320 | ||||
| Cp,liquid | 209.65 | J/mol×K | 283.15 | Heat Ca... |
| Cp,liquid | 210.73 | J/mol×K | 288.15 | Heat Ca... |
| Cp,liquid | 211.89 | J/mol×K | 293.15 | Heat Ca... |
| Cp,liquid | 212.94 | J/mol×K | 298.15 | Heat Ca... |
| Cp,liquid | 213.40 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 214.06 | J/mol×K | 303.15 | Heat Ca... |
| Cp,liquid | 215.21 | J/mol×K | 308.15 | Heat Ca... |
| Cp,liquid | 216.38 | J/mol×K | 313.15 | Heat Ca... |
| Cp,liquid | 217.56 | J/mol×K | 318.15 | Heat Ca... |
| Cp,liquid | 218.76 | J/mol×K | 323.15 | Heat Ca... |
| η | [0.0003408; 0.0044320] | Pa×s | [205.95; 388.66] |
|
|
T(K) Dynamic viscosity (Pa×s) 0 1.00e-3 2.00e-3 3.00e-3 4.00e-3 250 300 350 | ||||
| η | 0.0044320 | Pa×s | 205.95 | Joback Calculated Property |
| η | 0.0021944 | Pa×s | 236.40 | Joback Calculated Property |
| η | 0.0012756 | Pa×s | 266.85 | Joback Calculated Property |
| η | 0.0008286 | Pa×s | 297.30 | Joback Calculated Property |
| η | 0.0005832 | Pa×s | 327.76 | Joback Calculated Property |
| η | 0.0004357 | Pa×s | 358.21 | Joback Calculated Property |
| η | 0.0003408 | Pa×s | 388.66 | Joback Calculated Property |
| ΔvapH | 47.20 | kJ/mol | 407.50 | NIST |
| n0 | 1.45400 | 298.15 | Thermod... | |
| γ | [0.03; 0.04] | N/m | [293.15; 313.15] |
|
|
T(K) Surface Tension (N/m) 0.03 0.03 0.03 0.03 0.04 295 300 305 310 | ||||
| γ | 0.04 | 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... |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | [336.00; 337.70] | K | [1.30; 1.30] |
|
| Tboilr | 337.70 | K | 1.30 | NIST |
| Tboilr | 336.00 | K | 1.30 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.66] | kPa | [332.08; 482.98] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.46842e+01 | |||
| Coefficient B | -4.05298e+03 | |||
| Coefficient C | -5.05550e+01 | |||
| Temperature range, min. | 332.08 | |||
| Temperature range, max. | 482.98 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 350 400 450 | ||||
| Pvap | 1.33 | kPa | 332.08 | Calculated Property |
| Pvap | 2.99 | kPa | 348.85 | Calculated Property |
| Pvap | 6.17 | kPa | 365.61 | Calculated Property |
| Pvap | 11.82 | kPa | 382.38 | Calculated Property |
| Pvap | 21.27 | kPa | 399.15 | Calculated Property |
| Pvap | 36.27 | kPa | 415.91 | Calculated Property |
| Pvap | 59.02 | kPa | 432.68 | Calculated Property |
| Pvap | 92.17 | kPa | 449.45 | Calculated Property |
| Pvap | 138.86 | kPa | 466.21 | Calculated Property |
| Pvap | 202.66 | kPa | 482.98 | Calculated Property |
| Pvap | [4.06e-06; 3077.75] | kPa | [200.35; 663.00] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 7.19870e+01 | |||
| Coefficient B | -8.32410e+03 | |||
| Coefficient C | -8.10746e+00 | |||
| Coefficient D | 2.89471e-06 | |||
| Temperature range, min. | 200.35 | |||
| Temperature range, max. | 663.00 | |||
|
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 200 400 600 | ||||
| Pvap | 4.06e-06 | kPa | 200.35 | Calculated Property |
| Pvap | 3.29e-03 | kPa | 251.76 | Calculated Property |
| Pvap | 0.22 | kPa | 303.16 | Calculated Property |
| Pvap | 3.58 | kPa | 354.57 | Calculated Property |
| Pvap | 26.16 | kPa | 405.97 | Calculated Property |
| Pvap | 113.37 | kPa | 457.38 | Calculated Property |
| Pvap | 347.14 | kPa | 508.78 | Calculated Property |
| Pvap | 836.97 | kPa | 560.19 | Calculated Property |
| Pvap | 1705.00 | kPa | 611.59 | Calculated Property |
| Pvap | 3077.75 | kPa | 663.00 | Calculated Property |
Similar Compounds
Find more compounds similar to Pentane, 1,5-dichloro-.
Mixtures
- Pentane, 1,5-dichloro- + Butanoic acid, ethyl ester
- Pentanoic acid, ethyl ester + Pentane, 1,5-dichloro-
- Ethyl formate + Pentane, 1,5-dichloro-
- Pentane, 1,5-dichloro- + Ethyl Acetate
- Propanoic acid, ethyl ester + Pentane, 1,5-dichloro-
- Formic acid, butyl ester + Pentane, 1,5-dichloro-
- Propanoic acid, butyl ester + Pentane, 1,5-dichloro-
- Pentane, 1,5-dichloro- + Acetic acid, butyl ester
- Butanoic acid, butyl ester + Pentane, 1,5-dichloro-
- Formic acid, propyl ester + Pentane, 1,5-dichloro-
- Pentane, 1,5-dichloro- + n-Propyl acetate
- Propanoic acid, propyl ester + Pentane, 1,5-dichloro-
- Pentane, 1,5-dichloro- + Butanoic acid, propyl ester
- Dodecane + Pentane, 1,5-dichloro-
- Methyl formate + Pentane, 1,5-dichloro-
- Formic acid, pentyl ester + Pentane, 1,5-dichloro-
Sources
- KDB Vapor Pressure Data
- Crippen Method
- Crippen Method
- 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
- 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
- The additivity of surface and volumetric properties of alpha,omega-dihalogenoalkanes
- Heat Capacities of alpha,omega-Dichloroalkanes at Temperatures from 284.15 K to 353.15 K and a Group Additivity Analysis
- Heat Capacities, Densities, and Speeds of Sound for {(1,5-Dichloropentane or 1,6-Dichlorohexane) + Dodecane}
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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