- InChI
- InChI=1S/C4H9Cl/c1-2-3-4-5/h2-4H2,1H3
- InChI Key
- VFWCMGCRMGJXDK-UHFFFAOYSA-N
- Formula
- C4H9Cl
- SMILES
- CCCCCl
- Molecular Weight1
- 92.57
- CAS
- 109-69-3
- Other Names
-
- 1-Chlorobutane
- Butyl chloride
- Chlorure de butyle
- N-BUTYL CHLORIDE
- N-PROPYLCARBINYL CHLORIDE
- NBC wormer
- NCI-C06155
- NSC 8419
- Sure Shot
- n-C4H9Cl
- 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).
- μ : Dipole Moment (debye).
- 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).
- 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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Contents
- Physical Properties
- Temperature Dependent Properties
- Datasets
- Correlations
- Similar Compounds
- Mixtures
- Sources
Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.2180 | KDB | |
| ΔcH°liquid | [-2704.10; -2695.80] | kJ/mol |
|
| ΔcH°liquid | -2695.80 ± 1.10 | kJ/mol | NIST |
| ΔcH°liquid | -2704.10 ± 8.40 | kJ/mol | NIST |
| μ | 2.00 | debye | KDB |
| ΔfG° | -38.81 | kJ/mol | KDB |
| ΔfH°gas | [-154.60; -147.40] | kJ/mol |
|
| ΔfH°gas | -147.40 | kJ/mol | KDB |
| ΔfH°gas | -154.60 ± 1.20 | kJ/mol | NIST |
| ΔfH°liquid | -188.20 ± 1.20 | kJ/mol | NIST |
| ΔfusH° | 10.31 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 28.88 | kJ/mol | Joback Calculated Property |
| IE | [10.46; 10.94] | eV |
|
| IE | 10.64 ± 0.19 | eV | NIST |
| IE | 10.63 | eV | NIST |
| IE | 10.46 ± 0.05 | eV | NIST |
| IE | 10.94 | eV | NIST |
| IE | 10.50 ± 0.07 | eV | NIST |
| IE | 10.67 ± 0.03 | eV | NIST |
| IE | 10.84 | eV | NIST |
| log10WS | [-2.03; -2.03] |
|
|
| log10WS | -2.03 | Aq. Sol... | |
| log10WS | -2.03 | Estimat... | |
| logPoct/wat | 2.025 | Crippen Calculated Property | |
| McVol | 79.460 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 3 | KDB | |
| NFPA Health | 2 | KDB | |
| Pc | 3680.00 | kPa | KDB |
| Inp | [607.00; 659.61] |
|
|
| Inp | 646.10 | NIST | |
| Inp | 641.60 | NIST | |
| Inp | 647.30 | NIST | |
| Inp | 642.50 | NIST | |
| Inp | 639.60 | NIST | |
| Inp | 639.00 | NIST | |
| Inp | 638.30 | NIST | |
| Inp | Outlier 659.61 | NIST | |
| Inp | 639.00 | NIST | |
| Inp | 639.50 | NIST | |
| Inp | 640.00 | NIST | |
| Inp | 630.40 | NIST | |
| Inp | 654.00 | NIST | |
| Inp | 641.00 | NIST | |
| Inp | 631.00 | NIST | |
| Inp | 648.00 | NIST | |
| Inp | 644.00 | NIST | |
| Inp | 641.00 | NIST | |
| Inp | 641.00 | NIST | |
| Inp | 653.00 | NIST | |
| Inp | 644.00 | NIST | |
| Inp | 646.00 | NIST | |
| Inp | 648.00 | NIST | |
| Inp | 641.00 | NIST | |
| Inp | Outlier 607.00 | NIST | |
| Inp | Outlier 612.00 | NIST | |
| Inp | 638.00 | NIST | |
| Inp | 637.00 | NIST | |
| Inp | 637.00 | NIST | |
| Inp | 637.00 | NIST | |
| Inp | 637.00 | NIST | |
| Inp | 641.00 | NIST | |
| Inp | 637.00 | NIST | |
| Inp | 641.00 | NIST | |
| Inp | 642.00 | NIST | |
| Inp | 635.00 | NIST | |
| Inp | 642.00 | NIST | |
| Inp | 648.30 | NIST | |
| Inp | 639.10 | NIST | |
| Inp | 631.00 | NIST | |
| Inp | 637.00 | NIST | |
| Inp | 648.30 | NIST | |
| I | [832.00; 858.00] |
|
|
| I | 832.00 | NIST | |
| I | 842.00 | NIST | |
| I | 858.00 | NIST | |
| Tboil | [351.52; 351.60] | K |
|
| Tboil | 351.60 | K | KDB |
| Tboil | 351.52 | K | Study o... |
| Tboil | 351.53 | K | Isobari... |
| Tboil | 351.52 | K | Vapor-L... |
| Tc | [542.00; 542.00] | K |
|
| Tc | 542.00 | K | KDB |
| Tc | 542.00 | K | NIST |
| Tfus | [149.95; 150.12] | K |
|
| Tfus | 150.10 | K | KDB |
| Tfus | 150.12 | K | Aq. Sol... |
| Tfus | 150.05 | K | NIST |
| Tfus | 149.95 ± 0.05 | K | NIST |
| Tfus | 150.05 ± 0.20 | K | NIST |
| Vc | 0.312 | m3/kmol | KDB |
| Zc | 0.2547810 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [118.92; 159.72] | J/mol×K | [328.35; 500.65] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 120 130 140 150 160 350 400 450 500 | ||||
| Cp,gas | 118.92 | J/mol×K | 328.35 | Joback Calculated Property |
| Cp,gas | 126.38 | J/mol×K | 357.07 | Joback Calculated Property |
| Cp,gas | 133.57 | J/mol×K | 385.78 | Joback Calculated Property |
| Cp,gas | 140.49 | J/mol×K | 414.50 | Joback Calculated Property |
| Cp,gas | 147.15 | J/mol×K | 443.22 | Joback Calculated Property |
| Cp,gas | 153.56 | J/mol×K | 471.93 | Joback Calculated Property |
| Cp,gas | 159.72 | J/mol×K | 500.65 | Joback Calculated Property |
| Cp,liquid | [156.22; 173.09] | J/mol×K | [284.15; 353.15] |
|
|
T(K) Liquid phase heat capacity (J/mol×K) 155 160 165 170 300 320 340 | ||||
| Cp,liquid | 156.22 | J/mol×K | 284.15 | Heat Ca... |
| Cp,liquid | 156.75 | J/mol×K | 286.65 | Heat Ca... |
| Cp,liquid | 157.28 | J/mol×K | 289.15 | Heat Ca... |
| Cp,liquid | 157.70 | J/mol×K | 291.65 | Heat Ca... |
| Cp,liquid | 158.27 | J/mol×K | 294.15 | Heat Ca... |
| Cp,liquid | 158.86 | J/mol×K | 296.65 | Heat Ca... |
| Cp,liquid | 158.90 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 159.53 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 159.64 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 159.48 | J/mol×K | 299.15 | Heat Ca... |
| Cp,liquid | 160.05 | J/mol×K | 301.65 | Heat Ca... |
| Cp,liquid | 160.50 | J/mol×K | 304.15 | Heat Ca... |
| Cp,liquid | 161.06 | J/mol×K | 306.65 | Heat Ca... |
| Cp,liquid | 161.59 | J/mol×K | 309.15 | Heat Ca... |
| Cp,liquid | 162.24 | J/mol×K | 311.65 | Heat Ca... |
| Cp,liquid | 162.92 | J/mol×K | 314.15 | Heat Ca... |
| Cp,liquid | 163.42 | J/mol×K | 316.65 | Heat Ca... |
| Cp,liquid | 164.11 | J/mol×K | 319.15 | Heat Ca... |
| Cp,liquid | 164.82 | J/mol×K | 321.65 | Heat Ca... |
| Cp,liquid | 165.00 | J/mol×K | 324.15 | Heat Ca... |
| Cp,liquid | 165.97 | J/mol×K | 326.65 | Heat Ca... |
| Cp,liquid | 166.72 | J/mol×K | 329.15 | Heat Ca... |
| Cp,liquid | 167.29 | J/mol×K | 331.65 | Heat Ca... |
| Cp,liquid | 167.78 | J/mol×K | 334.15 | Heat Ca... |
| Cp,liquid | 168.53 | J/mol×K | 336.65 | Heat Ca... |
| Cp,liquid | 169.12 | J/mol×K | 339.15 | Heat Ca... |
| Cp,liquid | 170.01 | J/mol×K | 341.65 | Heat Ca... |
| Cp,liquid | 170.43 | J/mol×K | 344.15 | Heat Ca... |
| Cp,liquid | 170.49 | J/mol×K | 346.65 | Heat Ca... |
| Cp,liquid | 171.50 | J/mol×K | 349.15 | Heat Ca... |
| Cp,liquid | 173.02 | J/mol×K | 351.65 | Heat Ca... |
| Cp,liquid | 173.09 | J/mol×K | 353.15 | Heat Ca... |
| η | [0.0003540; 0.0004993] | Pa×s | [283.15; 318.15] |
|
|
T(K) Dynamic viscosity (Pa×s) 3.50e-4 4.00e-4 4.50e-4 5.00e-4 290 300 310 | ||||
| η | 0.0004993 | Pa×s | 283.15 | Experim... |
| η | 0.0004993 | Pa×s | 283.15 | Viscosi... |
| η | 0.0004701 | Pa×s | 288.15 | Viscosi... |
| η | 0.0004701 | Pa×s | 288.15 | Experim... |
| η | 0.0004770 | Pa×s | 288.15 | Densiti... |
| η | 0.0004433 | Pa×s | 293.15 | Viscosi... |
| η | 0.0004433 | Pa×s | 293.15 | Experim... |
| η | 0.0004214 | Pa×s | 298.15 | Viscosi... |
| η | 0.0004214 | Pa×s | 298.15 | Experim... |
| η | 0.0004212 | Pa×s | 298.15 | Densiti... |
| η | 0.0004273 | Pa×s | 298.15 | Measure... |
| η | 0.0004290 | Pa×s | 298.15 | Densiti... |
| η | 0.0004050 | Pa×s | 303.15 | Experim... |
| η | 0.0004050 | Pa×s | 303.15 | Viscosi... |
| η | 0.0004090 | Pa×s | 303.15 | Densiti... |
| η | 0.0003885 | Pa×s | 308.15 | Viscosi... |
| η | 0.0003900 | Pa×s | 308.15 | Densiti... |
| η | 0.0003885 | Pa×s | 308.15 | Experim... |
| η | 0.0003645 | Pa×s | 313.15 | Measure... |
| η | 0.0003642 | Pa×s | 313.15 | Experim... |
| η | 0.0003720 | Pa×s | 313.15 | Densiti... |
| η | 0.0003642 | Pa×s | 313.15 | Viscosi... |
| η | 0.0003640 | Pa×s | 313.15 | Densiti... |
| η | 0.0003540 | Pa×s | 318.15 | Densiti... |
| ΔvapH | [29.40; 37.20] | kJ/mol | [304.00; 358.00] |
|
|
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 30 32 34 36 320 340 | ||||
| ΔvapH | 35.60 | kJ/mol | 304.00 | NIST |
| ΔvapH | 32.70 ± 0.10 | kJ/mol | 313.00 | NIST |
| ΔvapH | 37.20 | kJ/mol | 318.00 | NIST |
| ΔvapH | 35.00 | kJ/mol | 323.00 | NIST |
| ΔvapH | 31.80 ± 0.10 | kJ/mol | 328.00 | NIST |
| ΔvapH | 30.90 ± 0.10 | kJ/mol | 343.00 | NIST |
| ΔvapH | 30.90 | kJ/mol | 349.50 | NIST |
| ΔvapH | 30.00 | kJ/mol | 351.60 | KDB |
| ΔvapH | 30.39 | kJ/mol | 351.70 | NIST |
| ΔvapH | 30.00 ± 0.10 | kJ/mol | 358.00 | NIST |
| ΔvapH | 29.40 ± 0.10 | kJ/mol | 358.00 | NIST |
| ν | [0.0000004; 0.0000006] | m2/s | [283.15; 313.15] |
|
|
T(K) Kinematic viscosity (m2/s) 4.20e-7 4.40e-7 4.60e-7 4.80e-7 5.00e-7 5.20e-7 5.40e-7 5.60e-7 290 300 310 | ||||
| ν | 0.0000006 | m2/s | 283.15 | Experim... |
| ν | 0.0000005 | m2/s | 298.15 | Thermop... |
| ν | 0.0000005 | m2/s | 298.15 | Viscosi... |
| ν | 0.0000005 | m2/s | 298.15 | Experim... |
| ν | 0.0000004 | m2/s | 313.15 | Thermop... |
| ν | 0.0000004 | m2/s | 313.15 | Viscosi... |
| ν | 0.0000004 | m2/s | 313.15 | Experim... |
| Pvap | [4.98; 101.40] | kPa | [278.15; 351.61] |
|
|
T(K) Vapor pressure (kPa) 0 20 40 60 80 100 280 300 320 340 | ||||
| Pvap | 4.98 | kPa | 278.15 | Isother... |
| Pvap | 6.51 | kPa | 283.15 | Isother... |
| Pvap | 8.40 | kPa | 288.15 | Experim... |
| Pvap | 8.40 | kPa | 288.15 | Experim... |
| Pvap | 8.40 | kPa | 288.15 | Isother... |
| Pvap | 8.38 | kPa | 288.15 | Isother... |
| Pvap | 10.69 | kPa | 293.15 | Isother... |
| Pvap | 13.52 | kPa | 298.15 | Experim... |
| Pvap | 13.52 | kPa | 298.15 | Experim... |
| Pvap | 13.50 | kPa | 298.15 | Isother... |
| Pvap | 13.72 | kPa | 298.15 | (Vapour... |
| Pvap | 13.52 | kPa | 298.15 | (Vapour... |
| Pvap | 13.52 | kPa | 298.15 | Isother... |
| Pvap | 16.97 | kPa | 303.15 | Isother... |
| Pvap | 21.04 | kPa | 308.15 | Experim... |
| Pvap | 21.05 | kPa | 308.15 | Isother... |
| Pvap | 20.66 | kPa | 308.15 | (Vapour... |
| Pvap | 21.04 | kPa | 308.15 | Isother... |
| Pvap | 21.04 | kPa | 308.15 | Experim... |
| Pvap | 25.72 | kPa | 313.15 | Excess ... |
| Pvap | 25.72 | kPa | 313.15 | (Vapour... |
| Pvap | 25.88 | kPa | 313.15 | Isother... |
| Pvap | 31.59 | kPa | 318.15 | Isother... |
| Pvap | 31.46 | kPa | 318.15 | (Vapour... |
| Pvap | 38.26 | kPa | 323.15 | Isother... |
| Pvap | 40.87 | kPa | 325.00 | Isobari... |
| Pvap | 44.16 | kPa | 327.14 | Isobari... |
| Pvap | 46.87 | kPa | 328.66 | Isobari... |
| Pvap | 48.37 | kPa | 329.60 | Isobari... |
| Pvap | 48.83 | kPa | 329.78 | Isobari... |
| Pvap | 51.33 | kPa | 331.28 | Isobari... |
| Pvap | 53.30 | kPa | 332.28 | Isobari... |
| Pvap | 54.07 | kPa | 332.68 | Isobari... |
| Pvap | 59.61 | kPa | 335.44 | Isobari... |
| Pvap | 65.42 | kPa | 338.11 | Isobari... |
| Pvap | 72.23 | kPa | 341.04 | Isobari... |
| Pvap | 80.00 | kPa | 344.14 | Isobari... |
| Pvap | 87.52 | kPa | 346.84 | Isobari... |
| Pvap | 92.35 | kPa | 348.63 | Isobari... |
| Pvap | 101.30 | kPa | 351.53 | Isobari... |
| Pvap | 101.40 | kPa | 351.61 | Isobari... |
| n0 | [1.39131; 1.40750] | [283.15; 313.15] |
|
|
|
T(K) Refractive Index 1.39 1.4 1.4 1.41 290 300 310 | ||||
| n0 | 1.40750 | 283.15 | Volumet... | |
| n0 | 1.40481 | 288.15 | Volumet... | |
| n0 | 1.40450 | 288.15 | Excess ... | |
| n0 | 1.40212 | 293.15 | Volumet... | |
| n0 | 1.39950 | 298.15 | Volumet... | |
| n0 | 1.39910 | 298.15 | Isother... | |
| n0 | 1.39930 | 298.15 | Excess ... | |
| n0 | 1.39953 | 298.15 | Isother... | |
| n0 | 1.39950 | 298.15 | Volumet... | |
| n0 | 1.39960 | 298.15 | Densiti... | |
| n0 | 1.39953 | 298.15 | Isother... | |
| n0 | 1.39672 | 303.15 | Volumet... | |
| n0 | 1.39410 | 308.15 | Excess ... | |
| n0 | 1.39395 | 308.15 | Volumet... | |
| n0 | 1.39133 | 313.15 | Volumet... | |
| n0 | 1.39131 | 313.15 | Volumet... | |
| ρl | [835.30; 925.80] | kg/m3 | [253.15; 338.15] |
|
|
T(K) Liquid Density (kg/m3) 840 860 880 900 920 300 | ||||
| ρl | 925.80 | kg/m3 | 253.15 | Density... |
| ρl | 917.40 | kg/m3 | 263.15 | Density... |
| ρl | 907.30 | kg/m3 | 273.15 | Density... |
| ρl | 896.60 | kg/m3 | 283.15 | Density... |
| ρl | 892.18 | kg/m3 | 288.15 | Densiti... |
| ρl | 892.10 | kg/m3 | 288.15 | Densiti... |
| ρl | 891.75 | kg/m3 | 288.15 | Excess ... |
| ρl | 886.00 | kg/m3 | 293.00 | KDB |
| ρl | 885.90 | kg/m3 | 293.15 | Density... |
| ρl | 880.69 | kg/m3 | 298.15 | Surface... |
| ρl | 881.17 | kg/m3 | 298.15 | Volumet... |
| ρl | 880.69 | kg/m3 | 298.15 | Densiti... |
| ρl | 880.69 | kg/m3 | 298.15 | Surface... |
| ρl | 881.12 | kg/m3 | 298.15 | Densiti... |
| ρl | 880.86 | kg/m3 | 298.15 | Volumet... |
| ρl | 880.69 | kg/m3 | 298.15 | Thermod... |
| ρl | 880.69 | kg/m3 | 298.15 | Surface... |
| ρl | 880.40 | kg/m3 | 298.15 | Density... |
| ρl | 881.05 | kg/m3 | 298.15 | Densiti... |
| ρl | 874.90 | kg/m3 | 303.15 | Density... |
| ρl | 875.10 | kg/m3 | 303.15 | Excess ... |
| ρl | 869.93 | kg/m3 | 308.15 | Densiti... |
| ρl | 870.00 | kg/m3 | 308.15 | Volumet... |
| ρl | 869.86 | kg/m3 | 308.15 | Densiti... |
| ρl | 863.83 | kg/m3 | 313.15 | Excess ... |
| ρl | 863.90 | kg/m3 | 313.15 | Density... |
| ρl | 858.52 | kg/m3 | 318.15 | Densiti... |
| ρl | 858.67 | kg/m3 | 318.15 | Volumet... |
| ρl | 858.58 | kg/m3 | 318.15 | Densiti... |
| ρl | 852.10 | kg/m3 | 323.15 | Density... |
| ρl | 835.30 | kg/m3 | 338.15 | Density... |
| csound,fluid | [1037.26; 1119.00] | m/s | [298.15; 318.15] |
|
| csound,fluid | 1119.00 | m/s | 298.15 | Speeds ... |
| csound,fluid | 1078.01 | m/s | 308.15 | Speeds ... |
| csound,fluid | 1037.26 | m/s | 318.15 | Speeds ... |
| γ | [0.02; 0.02] | N/m | [283.15; 313.15] |
|
|
T(K) Surface Tension (N/m) 0.02 0.02 0.02 0.02 0.02 0.02 0.02 0.03 290 300 310 | ||||
| γ | 0.02 | N/m | 283.15 | Surface... |
| γ | 0.02 | N/m | 288.15 | Surface... |
| γ | 0.02 | N/m | 293.15 | Surface... |
| γ | 0.02 | N/m | 293.20 | KDB |
| 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... |
Datasets
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Pressure, kPa - Liquid | Temperature, K - Liquid | Mass density, kg/m3 - Liquid |
| 100.00 | 283.15 | 897.36 |
| 100.00 | 288.15 | 892.04 |
| 100.00 | 293.15 | 886.36 |
| 100.00 | 298.15 | 880.82 |
| 100.00 | 303.15 | 875.21 |
| 100.00 | 308.15 | 869.76 |
| 100.00 | 313.15 | 863.9 |
| 100.00 | 318.15 | 858.39 |
| 100.00 | 323.15 | 852.47 |
| 100.00 | 328.15 | 846.87 |
| 2000.00 | 283.15 | 899.21 |
| 2000.00 | 288.15 | 893.99 |
| 2000.00 | 293.15 | 888.35 |
| 2000.00 | 298.15 | 882.9 |
| 2000.00 | 303.15 | 877.35 |
| 2000.00 | 308.15 | 871.94 |
| 2000.00 | 313.15 | 866.24 |
| 2000.00 | 318.15 | 860.79 |
| 2000.00 | 323.15 | 854.85 |
| 2000.00 | 328.15 | 849.38 |
| 5000.00 | 283.15 | 902.05 |
| 5000.00 | 288.15 | 896.87 |
| 5000.00 | 293.15 | 891.37 |
| 5000.00 | 298.15 | 886.01 |
| 5000.00 | 303.15 | 880.6 |
| 5000.00 | 308.15 | 875.3 |
| 5000.00 | 313.15 | 869.77 |
| 5000.00 | 318.15 | 864.38 |
| 5000.00 | 323.15 | 858.68 |
| 5000.00 | 328.15 | 853.41 |
| 7000.00 | 283.15 | 903.87 |
| 7000.00 | 288.15 | 898.76 |
| 7000.00 | 293.15 | 893.36 |
| 7000.00 | 298.15 | 888.03 |
| 7000.00 | 303.15 | 882.68 |
| 7000.00 | 308.15 | 877.49 |
| 7000.00 | 313.15 | 871.92 |
| 7000.00 | 318.15 | 866.7 |
| 7000.00 | 323.15 | 861.15 |
| 7000.00 | 328.15 | 855.89 |
| 10000.00 | 283.15 | 906.6 |
| 10000.00 | 288.15 | 901.58 |
| 10000.00 | 293.15 | 896.28 |
| 10000.00 | 298.15 | 890.99 |
| 10000.00 | 303.15 | 885.78 |
| 10000.00 | 308.15 | 880.77 |
| 10000.00 | 313.15 | 875.27 |
| 10000.00 | 318.15 | 870.14 |
| 10000.00 | 323.15 | 864.65 |
| 10000.00 | 328.15 | 859.47 |
| 20000.00 | 283.15 | 915.16 |
| 20000.00 | 288.15 | 910.38 |
| 20000.00 | 293.15 | 905.24 |
| 20000.00 | 298.15 | 900.33 |
| 20000.00 | 303.15 | 895.41 |
| 20000.00 | 308.15 | 890.56 |
| 20000.00 | 313.15 | 885.35 |
| 20000.00 | 318.15 | 880.62 |
| 20000.00 | 323.15 | 875.43 |
| 20000.00 | 328.15 | 870.67 |
| 30000.00 | 283.15 | 923.05 |
| 30000.00 | 288.15 | 918.48 |
| 30000.00 | 293.15 | 913.5 |
| 30000.00 | 298.15 | 908.81 |
| 30000.00 | 303.15 | 904.1 |
| 30000.00 | 308.15 | 899.63 |
| 30000.00 | 313.15 | 894.59 |
| 30000.00 | 318.15 | 890.1 |
| 30000.00 | 323.15 | 885.16 |
| 30000.00 | 328.15 | 880.58 |
| 40000.00 | 283.15 | 930.41 |
| 40000.00 | 288.15 | 925.97 |
| 40000.00 | 293.15 | 921.24 |
| 40000.00 | 298.15 | 916.74 |
| 40000.00 | 303.15 | 912.24 |
| 40000.00 | 308.15 | 907.72 |
| 40000.00 | 313.15 | 903.08 |
| 40000.00 | 318.15 | 898.75 |
| 40000.00 | 323.15 | 894.16 |
| 40000.00 | 328.15 | 889.73 |
| 50000.00 | 283.15 | 937.2 |
| 50000.00 | 288.15 | 932.96 |
| 50000.00 | 293.15 | 928.33 |
| 50000.00 | 298.15 | 924.0 |
| 50000.00 | 303.15 | 919.76 |
| 50000.00 | 308.15 | 915.48 |
| 50000.00 | 313.15 | 910.86 |
| 50000.00 | 318.15 | 906.72 |
| 50000.00 | 323.15 | 902.27 |
| 50000.00 | 328.15 | 897.97 |
| 60000.00 | 283.15 | 943.68 |
| 60000.00 | 288.15 | 939.57 |
| 60000.00 | 293.15 | 935.0 |
| 60000.00 | 298.15 | 930.86 |
| 60000.00 | 303.15 | 926.77 |
| 60000.00 | 308.15 | 922.6 |
| 60000.00 | 313.15 | 918.16 |
| 60000.00 | 318.15 | 914.22 |
| 60000.00 | 323.15 | 910.0 |
| 60000.00 | 328.15 | 905.8 |
| 65000.00 | 283.15 | 946.75 |
| 65000.00 | 288.15 | 942.66 |
| 65000.00 | 293.15 | 938.38 |
| 65000.00 | 298.15 | 934.15 |
| 65000.00 | 303.15 | 930.08 |
| 65000.00 | 308.15 | 925.91 |
| 65000.00 | 313.15 | 921.77 |
| 65000.00 | 318.15 | 917.73 |
| 65000.00 | 323.15 | 913.54 |
| 65000.00 | 328.15 | 909.45 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 288.15 | 100.00 | 891.8 |
| 288.15 | 2000.00 | 893.6 |
| 288.15 | 4100.00 | 895.6 |
| 288.15 | 6100.00 | 897.5 |
| 288.15 | 8100.00 | 899.4 |
| 288.15 | 10100.00 | 901.3 |
| 288.15 | 12100.00 | 903.0 |
| 288.15 | 14100.00 | 904.9 |
| 288.15 | 16300.00 | 906.7 |
| 288.15 | 18400.00 | 908.5 |
| 288.15 | 20200.00 | 910.3 |
| 298.15 | 100.00 | 880.6 |
| 298.15 | 2000.00 | 882.6 |
| 298.15 | 4100.00 | 884.9 |
| 298.15 | 6100.00 | 886.8 |
| 298.15 | 8100.00 | 888.7 |
| 298.15 | 10100.00 | 890.9 |
| 298.15 | 12100.00 | 892.8 |
| 298.15 | 14200.00 | 894.7 |
| 298.15 | 16200.00 | 896.5 |
| 298.15 | 18300.00 | 898.5 |
| 298.15 | 20400.00 | 900.2 |
| 308.15 | 100.00 | 870.0 |
| 308.15 | 2000.00 | 872.1 |
| 308.15 | 4100.00 | 874.4 |
| 308.15 | 6100.00 | 876.5 |
| 308.15 | 8100.00 | 878.6 |
| 308.15 | 10100.00 | 880.8 |
| 308.15 | 12100.00 | 882.9 |
| 308.15 | 14200.00 | 884.9 |
| 308.15 | 16200.00 | 886.8 |
| 308.15 | 18300.00 | 888.8 |
| 308.15 | 20200.00 | 890.6 |
| 318.15 | 100.00 | 859.1 |
| 318.15 | 2000.00 | 861.5 |
| 318.15 | 4000.00 | 863.8 |
| 318.15 | 6100.00 | 866.3 |
| 318.15 | 8100.00 | 868.7 |
| 318.15 | 10100.00 | 870.9 |
| 318.15 | 12100.00 | 873.1 |
| 318.15 | 14100.00 | 875.1 |
| 318.15 | 16200.00 | 877.2 |
| 318.15 | 18400.00 | 879.3 |
| 318.15 | 20200.00 | 881.2 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 298.15 | 100.00 | 880.6 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 283.15 | 100.00 | 897.21 |
| 283.15 | 2500.00 | 899.51 |
| 283.15 | 5000.00 | 901.82 |
| 283.15 | 10000.00 | 906.3 |
| 283.15 | 15000.00 | 910.57 |
| 283.15 | 20000.00 | 914.69 |
| 283.15 | 25000.00 | 918.63 |
| 283.15 | 30000.00 | 922.33 |
| 283.15 | 35000.00 | 926.05 |
| 293.15 | 100.00 | 886.18 |
| 293.15 | 2500.00 | 888.63 |
| 293.15 | 5000.00 | 891.13 |
| 293.15 | 10000.00 | 895.89 |
| 293.15 | 20000.00 | 904.73 |
| 293.15 | 25000.00 | 908.9 |
| 293.15 | 30000.00 | 912.88 |
| 293.15 | 35000.00 | 916.77 |
| 298.15 | 100.00 | 880.63 |
| 298.15 | 2500.00 | 883.17 |
| 298.15 | 5000.00 | 885.72 |
| 298.15 | 10000.00 | 890.65 |
| 298.15 | 15000.00 | 895.36 |
| 298.15 | 20000.00 | 899.79 |
| 298.15 | 25000.00 | 904.09 |
| 298.15 | 30000.00 | 908.22 |
| 298.15 | 35000.00 | 912.17 |
| 303.15 | 100.00 | 874.92 |
| 303.15 | 2500.00 | 877.59 |
| 303.15 | 5000.00 | 880.23 |
| 303.15 | 10000.00 | 885.43 |
| 303.15 | 15000.00 | 890.24 |
| 303.15 | 20000.00 | 894.84 |
| 303.15 | 25000.00 | 899.24 |
| 303.15 | 30000.00 | 903.46 |
| 303.15 | 35000.00 | 907.47 |
| 313.15 | 100.00 | 863.82 |
| 313.15 | 2500.00 | 866.65 |
| 313.15 | 5000.00 | 869.49 |
| 313.15 | 10000.00 | 874.93 |
| 313.15 | 15000.00 | 880.07 |
| 313.15 | 20000.00 | 884.94 |
| 313.15 | 25000.00 | 889.61 |
| 313.15 | 30000.00 | 894.04 |
| 313.15 | 35000.00 | 898.33 |
| 323.15 | 100.00 | 852.43 |
| 323.15 | 2500.00 | 855.47 |
| 323.15 | 5000.00 | 858.54 |
| 323.15 | 10000.00 | 864.35 |
| 323.15 | 15000.00 | 869.85 |
| 323.15 | 20000.00 | 875.03 |
| 323.15 | 25000.00 | 879.94 |
| 323.15 | 30000.00 | 884.62 |
| 323.15 | 35000.00 | 889.1 |
| 333.15 | 100.00 | 840.79 |
| 333.15 | 2500.00 | 844.06 |
| 333.15 | 5000.00 | 847.37 |
| 333.15 | 10000.00 | 853.61 |
| 333.15 | 15000.00 | 859.47 |
| 333.15 | 20000.00 | 864.97 |
| 333.15 | 25000.00 | 870.17 |
| 333.15 | 30000.00 | 875.12 |
| 333.15 | 35000.00 | 879.82 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 298.15 | 13.52 | 880.805 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.66] | kPa | [255.28; 373.41] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.45467e+01 | |||
| Coefficient B | -3.09635e+03 | |||
| Coefficient C | -3.81330e+01 | |||
| Temperature range, min. | 255.28 | |||
| Temperature range, max. | 373.41 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 300 350 | ||||
| Pvap | 1.33 | kPa | 255.28 | Calculated Property |
| Pvap | 3.01 | kPa | 268.41 | Calculated Property |
| Pvap | 6.21 | kPa | 281.53 | Calculated Property |
| Pvap | 11.90 | kPa | 294.66 | Calculated Property |
| Pvap | 21.41 | kPa | 307.78 | Calculated Property |
| Pvap | 36.48 | kPa | 320.91 | Calculated Property |
| Pvap | 59.30 | kPa | 334.03 | Calculated Property |
| Pvap | 92.48 | kPa | 347.16 | Calculated Property |
| Pvap | 139.11 | kPa | 360.28 | Calculated Property |
| Pvap | 202.66 | kPa | 373.41 | Calculated Property |
| Pvap | [2.33e-06; 3601.12] | kPa | [150.05; 537.00] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 7.92413e+01 | |||
| Coefficient B | -6.56700e+03 | |||
| Coefficient C | -9.70121e+00 | |||
| Coefficient D | 7.48517e-06 | |||
| Temperature range, min. | 150.05 | |||
| Temperature range, max. | 537.00 | |||
|
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 3500 200 300 400 500 | ||||
| Pvap | 2.33e-06 | kPa | 150.05 | Calculated Property |
| Pvap | 3.87e-03 | kPa | 193.04 | Calculated Property |
| Pvap | 0.31 | kPa | 236.04 | Calculated Property |
| Pvap | 5.25 | kPa | 279.03 | Calculated Property |
| Pvap | 36.74 | kPa | 322.03 | Calculated Property |
| Pvap | 150.09 | kPa | 365.02 | Calculated Property |
| Pvap | 435.10 | kPa | 408.02 | Calculated Property |
| Pvap | 1006.70 | kPa | 451.01 | Calculated Property |
| Pvap | 2003.11 | kPa | 494.01 | Calculated Property |
| Pvap | 3601.12 | kPa | 537.00 | Calculated Property |
Similar Compounds
Find more compounds similar to Butane, 1-chloro-.
Mixtures
- Tetrahydropyran + Butane, 1-chloro-
- Butane, 1-chloro- + Tetrahydrofuran
- Diisopropyl ether + Butane, 1-chloro-
- Butane, 1-chloro- + Acetic acid, butyl ester
- Butane, 1-ethoxy- + Butane, 1-chloro-
- Butane, 1-chloro- + Propane, 2-methoxy-2-methyl-
- Butane, 1-chloro- + Heptane
- Butane, 1-chloro- + Cyclohexane
- Toluene + Butane, 1-chloro-
- Butane, 1-chloro- + Ethane, nitro-
- Butane, 1-chloro- + Methane, nitro-
- Butane, 1-chloro- + 1-Octanol
- Butane, 1-chloro- + 1-Decanol
- Butane, 1-chloro- + 1,4-Dioxane
- 1,3-Dioxolane + Butane, 1-chloro-
- Formamide, N,N-dimethyl- + Butane, 1-chloro-
- Butane, 1-chloro- + N,N-Dimethylacetamide
- Butane, 1-chloro- + Cyclopentanone
- 2-Pyrrolidinone, 1-methyl- + Butane, 1-chloro-
- n-Hexane + Butane, 1-chloro-
Find more mixtures with Butane, 1-chloro-.
Sources
- KDB Pure (Korean Thermophysical Properties Databank)
- KDB Vapor Pressure Data
- Crippen Method
- Thermophysical Properties of Mixtures of Tetrahydropyran with Chlorobutanes
- Surface Tension of Mixtures of Tetrahydrofuran or Tetrahydropyran with Isomeric Chlorobutanes
- Viscosities of Binary Mixtures Containing Isomeric Chlorobutanes and Diisopropylether: Experimental and Predicted Values
- Densities, Excess Molar Volumes, Viscosities, and Refractive Indices of Binary Mixtures of n-Butyl Acetate with 1-Chloroalkanes (C4 C8) at 298.15 K
- Experimental and Predicted Viscosities of Binary Mixtures Containing Chlorinated and Oxygenated Compounds
- Study of tetrahydropyran-chlorobutane VLE using the a o and o o approaches
- Solubility of chlorobutane, ethyl methacrylate and trifluoroethyl acrylate in supercritical carbon dioxide
- Excess molar volume and viscosity study for the ternary system tetrahydrofuran (1) + 1-chlorobutane (2) + 2-butanol (3) at 283.15, 298.15 and 313.15 K
- Isobaric vapor liquid equilibria for binary systems of butyl chlorides with heptane, toluene and cyclohexane at 101.3, 80.0 and 53.3 kPa
- Measurement and prediction of multicomponent diffusion coefficients in four ternary liquid systems
- Limiting activity coefficients of 1-chlorobutane in water and in aqueous solutions of substances involved in synthesis of ionic liquids
- Isothermal vapour-liquid equilibria and excess enthalpies for the binary mixtures containing an isomeric chlorobutane and diisopropyl ether
- 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
- Experimental and predicted vapour-liquid equilibrium of the binary mixtures n-heptane + chlorobutane isomers
- Abraham model linear free energy relationships for describing the partitioning and solubility behavior of nonelectrolyte organic solutes dissolved in pyridine at 298.15 K
- Isothermal (vapour + liquid) equilibrium at several temperatures of (1-chlorobutane + 1-octanol, or 1-decanol)
- Volumetric and refractive properties of binary mixtures containing 1,4-dioxane and chloroalkanes
- Surface study of mixtures containing cyclic ethers and isomeric chlorobutanes
- (Vapour + liquid) equilibria and excess molar enthalpies for binary mixtures containing N,N-dialkylamides and 1-chloroalkanes
- 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
- Excess enthalpies and isothermal (vapour + liquid) equilibria of (1-methyl-2-pyrrolidone + 1-chloroalkane or +,?-dichloroalkane) mixtures
- Surface and bulk behaviour of some (n-hexane + chloroalkane) mixtures
- (Vapour + liquid) equilibrium and excess Gibbs functions of ternary mixtures containing 1-butanol or 2-butanol, n-hexane, and 1-chlorobutane at T = 298.15 K
- (Vapour + liquid) equilibria and excess Gibbs free energies of (cyclohexanone + 1- chlorobutane and + 1,1,1-trichloroethane) binary mixtures at temperatures from (298.15 to 318.15) K
- Volumetric and acoustic behaviour of systems containing n-hexane, or n-heptane and isomeric chlorobutanes
- Experimental and predicted properties of the binary mixtures containing an isomeric chlorobutane and butyl ethyl ether
- Abraham model correlations for describing the thermodynamic properties of solute transfer into pentyl acetate based on headspace chromatographic and solubility measurements
- Thermodynamic study of 2-methyl-tetrahydrofuran with isomeric chlorobutanes
- Volumetric properties for binary and ternary systems consist of 1-chlorobutane, n-butylamine and isobutanol at 298.15 K with application of the Prigogine-Flory-Patterson theory and ERAS-Model
- Excess molar volumes of (1-chlorobutane +heptane + 2-butanone or 2-pentanone) at 288.15 , 303.15 and 313.15 K . Measurements and correlations.
- Excess properties from p.rho.T data for n-heptane + isomeric chlorobutane mixtures
- 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
- Measurements, Correlations, and Predictions of Viscosities for the Ternary Mixture (2-Butanol + Hexane + 1-Chlorobutane) at 298.15 K and 313.15 K
- Vapor-Liquid Equilibrium and Volumetric Measurements for Binary Mixtures of 1,4-Dioxane with Isomeric Chlorobutanes
- Viscosities of Binary Mixtures of Isomeric Butanols or Isomeric Chlorobutanes with 2-Methyltetrahydrofuran
- Solubilities of Some Long-Chain n-Alkanes in Dipropyl Ether, Dibutyl Ether, 1-Chlorobutane, and 1-Chlorooctane as Functions of Temperature
- Excess Molar Volumes, Viscosities, and Refractive Indexes for Binary Mixtures of 1-Chlorobutane with Four Alcohols at T = (288.15, 298.15 and 308.15) K
- Densities and Viscosities of Binary Mixtures of 1-Chlorobutane with Butanol Isomers at Several Temperatures
- 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
- Solubility of Imidazoles, Benzimidazoles, and Phenylimidazoles in Dichloromethane, 1-Chlorobutane, Toluene, and 2-Nitrotoluene
- Densities and Viscosities of the Binary Mixtures of Tetrahydrofuran with Isomeric Chlorobutanes at 298.15 K and 313.15 K
- Surface Tensions of the Ternary Mixtures Containing an Isomeric Butanol + n-Hexane + 1-Chlorobutane at 298.15 K
- Activity Coefficients at Infinite Dilution for Hydrocarbons in Fatty Alcohols Determined by Gas-Liquid Chromatography
- Volumetric, Acoustic, and Refractive Properties of Isomeric Chlorobutanes with Diisopropyl Ether
- Experimental and Predicted Kinematic Viscosities for Alkane + Chloroalkane Mixtures
- Activity Coefficients at Infinite Dilution by GLC in Alkanediamines as Stationary Phases
- Volumetric Properties of Short-Chain Chloroalkanes
- Volumetric Study for the Binary Nitromethane with Chloroalkane Mixtures at Temperatures in the Range (298.15 to 318.15) K
- Densities and Isothermal Compressibilities at Pressures up to 20 MPa of the Systems N,N-Dimethylformamide or N,N-Dimethylacetamide + 1-Chloroalkane
- Density of Some 1-Chloroalkanes within the Temperature Range from (253.15 to 423.15) K
- Densities and Isothermal Compressibilities at Pressures up to 20 MPa of the Systems 1-Methyl-2-pyrrolidone + 1-Chloroalkane or + r,u-Dichloroalkane
- Densities and Excess Volumes of the 1-Chlorobutane + n-Hexane System at Temperatures from (283.15 to 333.15) K and Pressures from (0.1 to 35) MPa
- Densities and Viscosities of the Ternary Mixtures 2-Methyl-1-propanol (or 2-Methyl-2-propanol) + N-Hexane + 1-Chlorobutane at 298.15 K
- Isothermal Vapor-Liquid Equilibrium of Binary Mixtures Containing 1-Chlorobutane, Ethanol, or Acetonitrile
- Phase Behavior, Densities, and Isothermal Compressibility of Carbon Dioxide + 1-Bromobutane, Carbon Dioxide + 1-Chlorobutane, and Carbon Dioxide + 1-Methylimidazole
- Densities and Excess Molar Volumes of the Binary Mixtures of Cyclohexanone with Chloroalkanes at Temperatures between (288.15 and 318.15) K
- Isothermal Vapor-Liquid Equilibrium of Ternary Mixtures Containing 2-Methyl-1-propanol or 2-Methyl-2-propanol, n-Hexane, and 1-Chlorobutane at 298.15 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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