- InChI
- InChI=1S/C5H11Cl/c1-2-3-4-5-6/h2-5H2,1H3
- InChI Key
- SQCZQTSHSZLZIQ-UHFFFAOYSA-N
- Formula
- C5H11Cl
- SMILES
- CCCCCCl
- Molecular Weight1
- 106.59
- CAS
- 543-59-9
- Other Names
-
- 1-Chloropentane
- Amyl chloride
- N-AMYL CHLORIDE
- N-PENTYL CHLORIDE
- Pentyl chloride
- UN 1107
- 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).
- ΔvapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
- ΔvapH : Enthalpy of vaporization at a given temperature (kJ/mol).
- IE : Ionization energy (eV).
- ν : Kinematic viscosity (m2/s).
- 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).
- Tboilr : Boiling point at reduced pressure (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 | 0.4370 | KDB | |
| ΔcH°liquid | [-3352.00; -3344.60] | kJ/mol |
|
| ΔcH°liquid | -3349.90 ± 1.20 | kJ/mol | NIST |
| ΔcH°liquid | -3352.00 ± 3.00 | kJ/mol | NIST |
| ΔcH°liquid | -3344.60 | kJ/mol | NIST |
| ΔfG° | -20.71 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -175.20 ± 1.30 | kJ/mol | NIST |
| ΔfH°liquid | [-213.40; -212.00] | kJ/mol |
|
| ΔfH°liquid | -213.40 ± 1.30 | kJ/mol | NIST |
| ΔfH°liquid | -212.00 ± 3.00 | kJ/mol | NIST |
| ΔfusH° | 12.90 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [38.20; 38.80] | kJ/mol |
|
| ΔvapH° | 38.30 | kJ/mol | NIST |
| ΔvapH° | Outlier 38.80 | kJ/mol | NIST |
| ΔvapH° | 38.21 | kJ/mol | NIST |
| ΔvapH° | 38.20 | kJ/mol | NIST |
| ΔvapH° | 38.20 ± 0.10 | kJ/mol | NIST |
| ΔvapH° | 38.24 ± 0.02 | kJ/mol | NIST |
| IE | 10.47 | eV | NIST |
| log10WS | [-2.73; -2.73] |
|
|
| log10WS | -2.73 | Aq. Sol... | |
| log10WS | -2.73 | Estimat... | |
| logPoct/wat | 2.415 | Crippen Calculated Property | |
| McVol | 93.550 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 3 | KDB | |
| NFPA Health | 1 | KDB | |
| Pc | 3320.00 | kPa | KDB |
| Inp | [722.00; 762.00] |
|
|
| Inp | 742.20 | NIST | |
| Inp | 741.70 | NIST | |
| Inp | 742.00 | NIST | |
| Inp | 762.00 | NIST | |
| Inp | 732.20 | NIST | |
| Inp | Outlier 722.00 | NIST | |
| Inp | 725.00 | NIST | |
| Inp | 729.00 | NIST | |
| Inp | 730.00 | NIST | |
| Inp | 754.00 | NIST | |
| Inp | 756.00 | NIST | |
| Inp | 754.20 | NIST | |
| Inp | 736.00 | NIST | |
| Inp | 739.00 | NIST | |
| Inp | 747.00 | NIST | |
| Inp | 743.00 | NIST | |
| Inp | 744.00 | NIST | |
| Inp | 762.00 | NIST | |
| Inp | 746.00 | NIST | |
| Inp | 748.00 | NIST | |
| Inp | 751.00 | NIST | |
| Inp | 744.00 | NIST | |
| Inp | 742.00 | NIST | |
| Inp | 740.00 | NIST | |
| Inp | 751.10 | NIST | |
| Inp | 743.40 | NIST | |
| Inp | 742.00 | NIST | |
| Inp | 747.00 | NIST | |
| Inp | 748.00 | NIST | |
| Inp | 742.20 | NIST | |
| Inp | Outlier 722.00 | NIST | |
| Inp | 756.00 | NIST | |
| I | [938.00; 953.00] |
|
|
| I | 938.00 | NIST | |
| I | 945.00 | NIST | |
| I | 943.00 | NIST | |
| I | Outlier 953.00 | NIST | |
| I | 946.00 | NIST | |
| I | 941.00 | NIST | |
| I | 945.00 | NIST | |
| I | 945.00 | NIST | |
| I | 938.00 | NIST | |
| Tboil | 380.20 | K | KDB |
| Tc | [552.00; 568.50] | K |
|
| Tc | 552.00 | K | KDB |
| Tc | 568.50 | K | NIST |
| Tfus | 174.00 | K | KDB |
| Vc | 0.364 | m3/kmol | KDB |
| Zc | 0.2636690 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [151.15; 200.12] | J/mol×K | [351.23; 523.71] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 150 160 170 180 190 200 350 400 450 500 | ||||
| Cp,gas | 151.15 | J/mol×K | 351.23 | Joback Calculated Property |
| Cp,gas | 160.12 | J/mol×K | 379.98 | Joback Calculated Property |
| Cp,gas | 168.76 | J/mol×K | 408.72 | Joback Calculated Property |
| Cp,gas | 177.07 | J/mol×K | 437.47 | Joback Calculated Property |
| Cp,gas | 185.06 | J/mol×K | 466.22 | Joback Calculated Property |
| Cp,gas | 192.74 | J/mol×K | 494.97 | Joback Calculated Property |
| Cp,gas | 200.12 | J/mol×K | 523.71 | Joback Calculated Property |
| Cp,liquid | [184.57; 204.24] | J/mol×K | [284.15; 353.15] |
|
|
T(K) Liquid phase heat capacity (J/mol×K) 185 190 195 200 205 300 320 340 | ||||
| Cp,liquid | 184.57 | J/mol×K | 284.15 | Heat Ca... |
| Cp,liquid | 185.29 | J/mol×K | 286.65 | Heat Ca... |
| Cp,liquid | 185.95 | J/mol×K | 289.15 | Heat Ca... |
| Cp,liquid | 186.52 | J/mol×K | 291.65 | Heat Ca... |
| Cp,liquid | 187.16 | J/mol×K | 294.15 | Heat Ca... |
| Cp,liquid | 187.66 | J/mol×K | 296.65 | Heat Ca... |
| Cp,liquid | 187.70 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 188.46 | J/mol×K | 299.15 | Heat Ca... |
| Cp,liquid | 189.19 | J/mol×K | 301.65 | Heat Ca... |
| Cp,liquid | 189.81 | J/mol×K | 304.15 | Heat Ca... |
| Cp,liquid | 190.32 | J/mol×K | 306.65 | Heat Ca... |
| Cp,liquid | 190.99 | J/mol×K | 309.15 | Heat Ca... |
| Cp,liquid | 191.89 | J/mol×K | 311.65 | Heat Ca... |
| Cp,liquid | 192.65 | J/mol×K | 314.15 | Heat Ca... |
| Cp,liquid | 193.22 | J/mol×K | 316.65 | Heat Ca... |
| Cp,liquid | 194.09 | J/mol×K | 319.15 | Heat Ca... |
| Cp,liquid | 194.69 | J/mol×K | 321.65 | Heat Ca... |
| Cp,liquid | 195.06 | J/mol×K | 324.15 | Heat Ca... |
| Cp,liquid | 196.14 | J/mol×K | 326.65 | Heat Ca... |
| Cp,liquid | 196.99 | J/mol×K | 329.15 | Heat Ca... |
| Cp,liquid | 197.64 | J/mol×K | 331.65 | Heat Ca... |
| Cp,liquid | 198.46 | J/mol×K | 334.15 | Heat Ca... |
| Cp,liquid | 199.23 | J/mol×K | 336.65 | Heat Ca... |
| Cp,liquid | 199.92 | J/mol×K | 339.15 | Heat Ca... |
| Cp,liquid | 200.41 | J/mol×K | 341.65 | Heat Ca... |
| Cp,liquid | 201.19 | J/mol×K | 344.15 | Heat Ca... |
| Cp,liquid | 201.73 | J/mol×K | 346.65 | Heat Ca... |
| Cp,liquid | 202.54 | J/mol×K | 349.15 | Heat Ca... |
| Cp,liquid | 203.57 | J/mol×K | 351.65 | Heat Ca... |
| Cp,liquid | 204.24 | J/mol×K | 353.15 | Heat Ca... |
| η | [0.0002888; 0.0042937] | Pa×s | [176.03; 351.23] |
|
|
T(K) Dynamic viscosity (Pa×s) 0 1.00e-3 2.00e-3 3.00e-3 4.00e-3 200 250 300 350 | ||||
| η | 0.0042937 | Pa×s | 176.03 | Joback Calculated Property |
| η | 0.0019882 | Pa×s | 205.23 | Joback Calculated Property |
| η | 0.0011153 | Pa×s | 234.43 | Joback Calculated Property |
| η | 0.0007111 | Pa×s | 263.63 | Joback Calculated Property |
| η | 0.0004960 | Pa×s | 292.83 | Joback Calculated Property |
| η | 0.0003693 | Pa×s | 322.03 | Joback Calculated Property |
| η | 0.0002888 | Pa×s | 351.23 | Joback Calculated Property |
| ΔvapH | [33.15; 38.70] | kJ/mol | [303.00; 380.90] |
|
|
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 33 34 35 36 37 38 39 320 340 360 380 | ||||
| ΔvapH | 36.20 | kJ/mol | 303.00 | NIST |
| ΔvapH | 37.30 | kJ/mol | 313.00 | NIST |
| ΔvapH | 36.50 | kJ/mol | 328.00 | NIST |
| ΔvapH | 35.60 | kJ/mol | 343.00 | NIST |
| ΔvapH | 38.70 | kJ/mol | 349.00 | NIST |
| ΔvapH | 34.60 | kJ/mol | 358.00 | NIST |
| ΔvapH | 34.00 | kJ/mol | 363.00 | NIST |
| ΔvapH | 33.20 | kJ/mol | 378.00 | NIST |
| ΔvapH | 33.18 | kJ/mol | 380.20 | KDB |
| ΔvapH | 33.15 | kJ/mol | 380.90 | NIST |
| ν | [0.0000005; 0.0000007] | m2/s | [283.15; 313.15] |
|
| ν | 0.0000007 | m2/s | 283.15 | Experim... |
| ν | 0.0000006 | m2/s | 298.15 | Experim... |
| ν | 0.0000005 | m2/s | 313.15 | Experim... |
| Pvap | [4.05; 16.40] | kPa | [298.15; 328.15] |
|
| Pvap | 4.05 | kPa | 298.15 | Isother... |
| Pvap | 8.45 | kPa | 313.15 | Isother... |
| Pvap | 16.40 | kPa | 328.15 | Isother... |
| n0 | [1.40970; 1.41015] | [298.15; 298.15] |
|
|
| n0 | 1.40970 | 298.15 | Densiti... | |
| n0 | 1.41015 | 298.15 | Isother... | |
| ρl | [809.10; 917.50] | kg/m3 | [253.15; 363.15] |
|
|
T(K) Liquid Density (kg/m3) 800 820 840 860 880 900 920 300 350 | ||||
| ρl | 917.50 | kg/m3 | 253.15 | Density... |
| ρl | 910.20 | kg/m3 | 263.15 | Density... |
| ρl | 900.70 | kg/m3 | 273.15 | Density... |
| ρl | 891.00 | kg/m3 | 283.15 | Density... |
| ρl | 881.30 | kg/m3 | 293.15 | Density... |
| ρl | 877.09 | kg/m3 | 298.15 | Volumet... |
| ρl | 876.20 | kg/m3 | 298.15 | Density... |
| ρl | 879.80 | kg/m3 | 298.15 | Volumet... |
| ρl | 866.97 | kg/m3 | 308.15 | Volumet... |
| ρl | 856.73 | kg/m3 | 318.15 | Volumet... |
| ρl | 851.30 | kg/m3 | 323.15 | Density... |
| ρl | 830.60 | kg/m3 | 343.15 | Density... |
| ρl | 809.10 | kg/m3 | 363.15 | Density... |
| csound,fluid | [1085.84; 1164.24] | m/s | [298.15; 318.15] |
|
| csound,fluid | 1164.24 | m/s | 298.15 | Speeds ... |
| csound,fluid | 1124.94 | m/s | 308.15 | Speeds ... |
| csound,fluid | 1085.84 | m/s | 318.15 | Speeds ... |
| γ | [0.02; 0.03] | N/m | [283.15; 313.15] |
|
|
T(K) Surface Tension (N/m) 0.02 0.02 0.02 0.02 0.03 0.03 0.03 290 300 310 | ||||
| γ | 0.03 | N/m | 283.15 | Surface... |
| γ | 0.03 | N/m | 288.15 | Surface... |
| γ | 0.03 | N/m | 293.15 | Surface... |
| γ | 0.02 | N/m | 298.15 | Surface... |
| γ | 0.02 | N/m | 303.15 | Surface... |
| γ | 0.02 | N/m | 308.15 | Surface... |
| γ | 0.02 | N/m | 313.15 | Surface... |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | 278.20 | K | 1.30 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.63] | kPa | [277.05; 406.59] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.46439e+01 | |||
| Coefficient B | -3.45471e+03 | |||
| Coefficient C | -3.64100e+01 | |||
| Temperature range, min. | 277.05 | |||
| Temperature range, max. | 406.59 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 300 350 400 | ||||
| Pvap | 1.33 | kPa | 277.05 | Calculated Property |
| Pvap | 3.00 | kPa | 291.44 | Calculated Property |
| Pvap | 6.18 | kPa | 305.84 | Calculated Property |
| Pvap | 11.84 | kPa | 320.23 | Calculated Property |
| Pvap | 21.31 | kPa | 334.62 | Calculated Property |
| Pvap | 36.33 | kPa | 349.02 | Calculated Property |
| Pvap | 59.09 | kPa | 363.41 | Calculated Property |
| Pvap | 92.24 | kPa | 377.80 | Calculated Property |
| Pvap | 138.91 | kPa | 392.20 | Calculated Property |
| Pvap | 202.63 | kPa | 406.59 | Calculated Property |
| Pvap | [3.00e-05; 4145.21] | kPa | [174.15; 588.00] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 7.39136e+01 | |||
| Coefficient B | -6.80056e+03 | |||
| Coefficient C | -8.81199e+00 | |||
| Coefficient D | 6.28593e-06 | |||
| Temperature range, min. | 174.15 | |||
| Temperature range, max. | 588.00 | |||
|
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 200 300 400 500 | ||||
| Pvap | 3.00e-05 | kPa | 174.15 | Calculated Property |
| Pvap | 0.01 | kPa | 220.13 | Calculated Property |
| Pvap | 0.67 | kPa | 266.12 | Calculated Property |
| Pvap | 8.38 | kPa | 312.10 | Calculated Property |
| Pvap | 49.74 | kPa | 358.08 | Calculated Property |
| Pvap | 185.63 | kPa | 404.07 | Calculated Property |
| Pvap | 513.13 | kPa | 450.05 | Calculated Property |
| Pvap | 1161.54 | kPa | 496.03 | Calculated Property |
| Pvap | 2297.20 | kPa | 542.02 | Calculated Property |
| Pvap | 4145.21 | kPa | 588.00 | Calculated Property |
Similar Compounds
Find more compounds similar to Pentane, 1-chloro-.
Mixtures
- Acetic acid, butyl ester + Pentane, 1-chloro-
- Pentane, 1-chloro- + Tetrahydrofuran
- Tetrahydropyran + Pentane, 1-chloro-
- 1,3-Dioxolane + Pentane, 1-chloro-
- Pentane, 1-chloro- + 1,4-Dioxane
- Pentane, 1-chloro- + Methane, nitro-
- Ethane, nitro- + Pentane, 1-chloro-
- n-Hexane + Pentane, 1-chloro-
- 2-Butanone + Pentane, 1-chloro-
- 1,8-Diaminooctane + Pentane, 1-chloro-
- Pentane, 1-chloro- + 1,10-Diaminodecane
- 1,12-Dodecanediamine + Pentane, 1-chloro-
Sources
- KDB Vapor Pressure Data
- Crippen Method
- Densities, Excess Molar Volumes, Viscosities, and Refractive Indices of Binary Mixtures of n-Butyl Acetate with 1-Chloroalkanes (C4 C8) at 298.15 K
- Isothermal vapour-liquid equilibrium for cyclic ethers with 1-chloropentane
- Isothermal vapor liquid equilibria and excess Gibbs free energies in some binary nitroalkane + chloroalkane mixtures at temperatures from 298.15 K to 318.15 K
- 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
- Surface and bulk behaviour of some (n-hexane + chloroalkane) mixtures
- Volumetric and optical properties for some (2-butanone + chloroalkane) binary mixtures at T = 298.15 K
- Experimental and predicted viscosities of binary mixtures of cyclic ethers with 1-chloropentane or 1-chlorohexane at 283.15, 298.15, and 313.15K
- Does Alkyl Chain Length Really Matter? Structure-Property Relationships in Thermochemistry of Ionic Liquids.
- Heat Capacities of 1-chloroalkanes and 1-bromoalkanes within the temperature range from 284.15 K to 353.15 K. A group additivity and molecular connectivity analysis
- Activity Coefficients at Infinite Dilution by GLC in Alkanediamines as Stationary Phases
- Volumetric Study for the Binary Nitromethane with Chloroalkane Mixtures at Temperatures in the Range (298.15 to 318.15) K
- Density of Some 1-Chloroalkanes within the Temperature Range from (253.15 to 423.15) 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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