- InChI
- InChI=1S/C6H13Cl/c1-2-3-4-5-6-7/h2-6H2,1H3
- InChI Key
- MLRVZFYXUZQSRU-UHFFFAOYSA-N
- Formula
- C6H13Cl
- SMILES
- CCCCCCCl
- Molecular Weight1
- 120.62
- CAS
- 544-10-5
- Other Names
-
- 1-Chlorohexane
- 1-Hexyl chloride
- Hexyl chloride
- N-HEXYL CHLORIDE
- 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).
- 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.
- 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).
- Tboil : Normal Boiling Point Temperature (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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Contents
- Physical Properties
- Temperature Dependent Properties
- Datasets
- Correlations
- Similar Compounds
- Mixtures
- Sources
Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ΔfG° | -12.29 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -182.91 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 15.49 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [42.00; 42.86] | kJ/mol |
|
| ΔvapH° | 42.86 | kJ/mol | NIST |
| ΔvapH° | Outlier 42.00 | kJ/mol | NIST |
| ΔvapH° | 42.83 | kJ/mol | NIST |
| ΔvapH° | 42.80 ± 0.10 | kJ/mol | NIST |
| ΔvapH° | 42.80 ± 0.10 | kJ/mol | NIST |
| ΔvapH° | 42.82 ± 0.06 | kJ/mol | NIST |
| IE | [10.28; 10.31] | eV |
|
| IE | 10.31 | eV | NIST |
| IE | 10.28 ± 0.05 | eV | NIST |
| log10WS | [-3.12; -3.12] |
|
|
| log10WS | -3.12 | Aq. Sol... | |
| log10WS | -3.12 | Estimat... | |
| logPoct/wat | 2.805 | Crippen Calculated Property | |
| McVol | 107.640 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 3 | KDB | |
| Pc | 2982.79 | kPa | Joback Calculated Property |
| Inp | [833.30; 859.70] |
|
|
| Inp | 840.10 | NIST | |
| Inp | 838.80 | NIST | |
| Inp | 839.50 | NIST | |
| Inp | 837.40 | NIST | |
| Inp | 835.00 | NIST | |
| Inp | 833.70 | NIST | |
| Inp | 836.70 | NIST | |
| Inp | 840.90 | NIST | |
| Inp | 843.70 | NIST | |
| Inp | 842.90 | NIST | |
| Inp | 844.00 | NIST | |
| Inp | 842.90 | NIST | |
| Inp | 844.60 | NIST | |
| Inp | 858.20 | NIST | |
| Inp | 859.70 | NIST | |
| Inp | 857.00 | NIST | |
| Inp | 833.30 | NIST | |
| Inp | 838.30 | NIST | |
| Inp | 835.00 | NIST | |
| Inp | 858.00 | NIST | |
| Inp | 835.90 | NIST | |
| Inp | 857.10 | NIST | |
| Inp | 840.00 | NIST | |
| Inp | 858.00 | NIST | |
| Inp | 844.00 | NIST | |
| Inp | 848.00 | NIST | |
| Inp | 844.00 | NIST | |
| Inp | 846.00 | NIST | |
| Inp | 857.00 | NIST | |
| Inp | 847.00 | NIST | |
| Inp | 850.00 | NIST | |
| Inp | 853.00 | NIST | |
| Inp | 845.00 | NIST | |
| Inp | 845.00 | NIST | |
| Inp | 844.00 | NIST | |
| Inp | 844.00 | NIST | |
| Inp | 844.00 | NIST | |
| Inp | 848.00 | NIST | |
| Inp | 850.00 | NIST | |
| I | [1034.00; 1050.00] |
|
|
| I | Outlier 1034.00 | NIST | |
| I | 1041.00 | NIST | |
| I | 1041.00 | NIST | |
| I | 1050.00 | NIST | |
| I | 1047.00 | NIST | |
| I | 1049.00 | NIST | |
| I | 1050.00 | NIST | |
| I | 1050.00 | NIST | |
| Tboil | [407.45; 408.22] | K |
|
| Tboil | 407.45 | K | KDB |
| Tboil | 407.70 | K | NIST |
| Tboil | 408.22 ± 0.08 | K | NIST |
| Tboil | 408.10 | K | NIST |
| Tboil | 407.45 ± 0.30 | K | NIST |
| Tc | 594.60 | K | NIST |
| Tfus | 179.15 ± 1.20 | K | NIST |
| Vc | 0.420 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [185.96; 242.42] | J/mol×K | [374.11; 546.35] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 190 200 210 220 230 240 400 450 500 550 | ||||
| Cp,gas | 185.96 | J/mol×K | 374.11 | Joback Calculated Property |
| Cp,gas | 196.32 | J/mol×K | 402.82 | Joback Calculated Property |
| Cp,gas | 206.29 | J/mol×K | 431.52 | Joback Calculated Property |
| Cp,gas | 215.87 | J/mol×K | 460.23 | Joback Calculated Property |
| Cp,gas | 225.08 | J/mol×K | 488.94 | Joback Calculated Property |
| Cp,gas | 233.93 | J/mol×K | 517.64 | Joback Calculated Property |
| Cp,gas | 242.42 | J/mol×K | 546.35 | Joback Calculated Property |
| Cp,liquid | [202.64; 235.17] | J/mol×K | [284.15; 373.15] |
|
|
T(K) Liquid phase heat capacity (J/mol×K) 200 205 210 215 220 225 230 235 300 320 340 360 | ||||
| Cp,liquid | 212.36 | J/mol×K | 284.15 | Heat Ca... |
| Cp,liquid | 213.23 | J/mol×K | 286.65 | Heat Ca... |
| Cp,liquid | 213.91 | J/mol×K | 289.15 | Heat Ca... |
| Cp,liquid | 214.63 | J/mol×K | 291.65 | Heat Ca... |
| Cp,liquid | 202.64 | J/mol×K | 293.15 | Tempera... |
| Cp,liquid | 215.40 | J/mol×K | 294.15 | Heat Ca... |
| Cp,liquid | 216.12 | J/mol×K | 296.65 | Heat Ca... |
| Cp,liquid | 216.20 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 204.33 | J/mol×K | 298.15 | Tempera... |
| Cp,liquid | 216.95 | J/mol×K | 299.15 | Heat Ca... |
| Cp,liquid | 217.75 | J/mol×K | 301.65 | Heat Ca... |
| Cp,liquid | 205.90 | J/mol×K | 303.15 | Tempera... |
| Cp,liquid | 218.44 | J/mol×K | 304.15 | Heat Ca... |
| Cp,liquid | 219.22 | J/mol×K | 306.65 | Heat Ca... |
| Cp,liquid | 207.47 | J/mol×K | 308.15 | Tempera... |
| Cp,liquid | 219.99 | J/mol×K | 309.15 | Heat Ca... |
| Cp,liquid | 221.00 | J/mol×K | 311.65 | Heat Ca... |
| Cp,liquid | 208.91 | J/mol×K | 313.15 | Tempera... |
| Cp,liquid | 221.78 | J/mol×K | 314.15 | Heat Ca... |
| Cp,liquid | 222.49 | J/mol×K | 316.65 | Heat Ca... |
| Cp,liquid | 210.48 | J/mol×K | 318.15 | Tempera... |
| Cp,liquid | 223.43 | J/mol×K | 319.15 | Heat Ca... |
| Cp,liquid | 224.31 | J/mol×K | 321.65 | Heat Ca... |
| Cp,liquid | 212.05 | J/mol×K | 323.15 | Tempera... |
| Cp,liquid | 224.70 | J/mol×K | 324.15 | Heat Ca... |
| Cp,liquid | 226.02 | J/mol×K | 326.65 | Heat Ca... |
| Cp,liquid | 213.62 | J/mol×K | 328.15 | Tempera... |
| Cp,liquid | 227.13 | J/mol×K | 329.15 | Heat Ca... |
| Cp,liquid | 228.86 | J/mol×K | 331.65 | Heat Ca... |
| Cp,liquid | 215.07 | J/mol×K | 333.15 | Tempera... |
| Cp,liquid | 228.99 | J/mol×K | 334.15 | Heat Ca... |
| Cp,liquid | 229.44 | J/mol×K | 336.65 | Heat Ca... |
| Cp,liquid | 216.63 | J/mol×K | 338.15 | Tempera... |
| Cp,liquid | 230.06 | J/mol×K | 339.15 | Heat Ca... |
| Cp,liquid | 231.22 | J/mol×K | 341.65 | Heat Ca... |
| Cp,liquid | 217.96 | J/mol×K | 343.15 | Tempera... |
| Cp,liquid | 231.83 | J/mol×K | 344.15 | Heat Ca... |
| Cp,liquid | 232.32 | J/mol×K | 346.65 | Heat Ca... |
| Cp,liquid | 219.05 | J/mol×K | 348.15 | Tempera... |
| Cp,liquid | 233.18 | J/mol×K | 349.15 | Heat Ca... |
| Cp,liquid | 234.56 | J/mol×K | 351.65 | Heat Ca... |
| Cp,liquid | 235.17 | J/mol×K | 353.15 | Heat Ca... |
| Cp,liquid | 220.98 | J/mol×K | 353.15 | Tempera... |
| Cp,liquid | 222.42 | J/mol×K | 358.15 | Tempera... |
| Cp,liquid | 223.87 | J/mol×K | 363.15 | Tempera... |
| Cp,liquid | 225.32 | J/mol×K | 368.15 | Tempera... |
| Cp,liquid | 226.65 | J/mol×K | 373.15 | Tempera... |
| η | [0.0004778; 0.0007704] | Pa×s | [293.15; 333.15] |
|
|
T(K) Dynamic viscosity (Pa×s) 4.50e-4 5.00e-4 5.50e-4 6.00e-4 6.50e-4 7.00e-4 7.50e-4 300 310 320 330 | ||||
| η | 0.0007704 | Pa×s | 293.15 | Viscosi... |
| η | 0.0007173 | Pa×s | 298.15 | Viscosi... |
| η | 0.0006702 | Pa×s | 303.15 | Viscosi... |
| η | 0.0006283 | Pa×s | 308.15 | Viscosi... |
| η | 0.0005910 | Pa×s | 313.15 | Viscosi... |
| η | 0.0005580 | Pa×s | 318.15 | Viscosi... |
| η | 0.0005285 | Pa×s | 323.15 | Viscosi... |
| η | 0.0005019 | Pa×s | 328.15 | Viscosi... |
| η | 0.0004778 | Pa×s | 333.15 | Viscosi... |
| ΔvapH | [35.67; 43.50] | kJ/mol | [328.00; 408.10] |
|
|
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 36 38 40 42 44 340 360 380 400 | ||||
| ΔvapH | 40.50 ± 0.10 | kJ/mol | 328.00 | NIST |
| ΔvapH | 40.00 ± 0.10 | kJ/mol | 343.00 | NIST |
| ΔvapH | 41.10 | kJ/mol | 347.50 | NIST |
| ΔvapH | 43.50 | kJ/mol | 348.50 | NIST |
| ΔvapH | 39.00 ± 0.10 | kJ/mol | 358.00 | NIST |
| ΔvapH | 38.40 ± 0.10 | kJ/mol | 368.00 | NIST |
| ΔvapH | 35.67 | kJ/mol | 408.10 | NIST |
| ν | [0.0000007; 0.0000009] | m2/s | [283.15; 313.15] |
|
| ν | 0.0000009 | m2/s | 283.15 | Experim... |
| ν | 0.0000008 | m2/s | 298.15 | Experim... |
| ν | 0.0000007 | m2/s | 313.15 | Experim... |
| Pvap | [1.25; 5.96] | kPa | [298.15; 328.15] |
|
| Pvap | 1.25 | kPa | 298.15 | Isother... |
| Pvap | 2.86 | kPa | 313.15 | (Vapour... |
| Pvap | 2.86 | kPa | 313.15 | Excess ... |
| Pvap | 5.96 | kPa | 328.15 | Isother... |
| n0 | [1.41680; 1.41720] | [298.15; 303.15] |
|
|
| n0 | 1.41710 | 298.15 | Densiti... | |
| n0 | 1.41720 | 298.15 | (P,Vm,T... | |
| n0 | 1.41680 | 303.15 | Densiti... | |
| ρl | [873.38; 873.50] | kg/m3 | [298.15; 298.15] |
|
| ρl | 873.50 | kg/m3 | 298.15 | Vapour ... |
| ρl | 873.38 | kg/m3 | 298.15 | Experim... |
| csound,fluid | [922.90; 1219.10] | m/s | [293.15; 373.15] |
|
|
T(K) Speed of sound in fluid (m/s) 900 950 1000 1050 1100 1150 1200 300 320 340 360 | ||||
| csound,fluid | 1219.10 | m/s | 293.15 | Speed o... |
| csound,fluid | 1200.10 | m/s | 298.15 | Speed o... |
| csound,fluid | 1181.90 | m/s | 303.15 | Speed o... |
| csound,fluid | 1165.20 | m/s | 308.15 | Speed o... |
| csound,fluid | 1143.70 | m/s | 313.15 | Speed o... |
| csound,fluid | 1128.10 | m/s | 318.15 | Speed o... |
| csound,fluid | 1106.00 | m/s | 323.15 | Speed o... |
| csound,fluid | 1087.00 | m/s | 328.15 | Speed o... |
| csound,fluid | 1068.80 | m/s | 333.15 | Speed o... |
| csound,fluid | 1050.20 | m/s | 338.15 | Speed o... |
| csound,fluid | 1031.70 | m/s | 343.15 | Speed o... |
| csound,fluid | 1013.30 | m/s | 348.15 | Speed o... |
| csound,fluid | 995.00 | m/s | 353.15 | Speed o... |
| csound,fluid | 976.90 | m/s | 358.15 | Speed o... |
| csound,fluid | 958.90 | m/s | 363.15 | Speed o... |
| csound,fluid | 940.60 | m/s | 368.15 | Speed o... |
| csound,fluid | 922.90 | m/s | 373.15 | Speed o... |
Datasets
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 288.15 | 100.00 | 882.7 |
| 288.15 | 2000.00 | 884.4 |
| 288.15 | 4100.00 | 886.0 |
| 288.15 | 5900.00 | 887.5 |
| 288.15 | 8100.00 | 889.2 |
| 288.15 | 10100.00 | 890.7 |
| 288.15 | 12200.00 | 892.3 |
| 288.15 | 14200.00 | 893.8 |
| 288.15 | 16200.00 | 895.2 |
| 288.15 | 18200.00 | 896.7 |
| 288.15 | 20200.00 | 898.3 |
| 298.15 | 100.00 | 873.1 |
| 298.15 | 2000.00 | 874.8 |
| 298.15 | 4100.00 | 876.6 |
| 298.15 | 6100.00 | 878.3 |
| 298.15 | 8100.00 | 879.9 |
| 298.15 | 10200.00 | 881.7 |
| 298.15 | 12100.00 | 883.3 |
| 298.15 | 14200.00 | 885.0 |
| 298.15 | 16400.00 | 886.6 |
| 298.15 | 18400.00 | 888.1 |
| 298.15 | 20200.00 | 889.6 |
| 308.15 | 100.00 | 864.3 |
| 308.15 | 2000.00 | 866.1 |
| 308.15 | 4100.00 | 868.0 |
| 308.15 | 6100.00 | 869.7 |
| 308.15 | 8100.00 | 871.5 |
| 308.15 | 10200.00 | 873.3 |
| 308.15 | 12100.00 | 875.0 |
| 308.15 | 14200.00 | 876.7 |
| 308.15 | 16200.00 | 878.3 |
| 308.15 | 18300.00 | 879.9 |
| 308.15 | 20200.00 | 881.5 |
| 318.15 | 100.00 | 855.1 |
| 318.15 | 2000.00 | 857.0 |
| 318.15 | 4000.00 | 858.9 |
| 318.15 | 6100.00 | 860.9 |
| 318.15 | 8100.00 | 862.7 |
| 318.15 | 10100.00 | 864.6 |
| 318.15 | 11900.00 | 866.1 |
| 318.15 | 14100.00 | 868.1 |
| 318.15 | 16100.00 | 869.9 |
| 318.15 | 18000.00 | 871.4 |
| 318.15 | 20000.00 | 872.8 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 298.15 | 100.00 | 873.1 |
| Reference | ||
Speed of sound, m/s
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Speed of sound, m/s - Liquid |
| 293.15 | 100.00 | 1219.1 |
| 293.15 | 5000.00 | 1240.5 |
| 293.15 | 9910.00 | 1264.5 |
| 293.15 | 19720.00 | 1310.0 |
| 293.15 | 29530.00 | 1352.6 |
| 293.15 | 39340.00 | 1392.6 |
| 293.15 | 49150.00 | 1430.1 |
| 293.15 | 58960.00 | 1465.7 |
| 293.15 | 68770.00 | 1499.3 |
| 293.15 | 78580.00 | 1531.5 |
| 293.15 | 88390.00 | 1562.3 |
| 293.15 | 98200.00 | 1591.9 |
| 293.15 | 108000.00 | 1620.6 |
| 293.15 | 117800.00 | 1648.2 |
| 293.15 | 127600.00 | 1675.2 |
| 293.15 | 137400.00 | 1701.5 |
| 293.15 | 147200.00 | 1727.1 |
| 293.15 | 157100.00 | 1752.2 |
| 293.15 | 166900.00 | 1776.7 |
| 293.15 | 176700.00 | 1800.6 |
| 293.15 | 186500.00 | 1824.0 |
| 293.15 | 196300.00 | 1846.5 |
| 313.15 | 100.00 | 1140.7 |
| 313.15 | 5000.00 | 1166.4 |
| 313.15 | 9910.00 | 1191.8 |
| 313.15 | 19720.00 | 1240.1 |
| 313.15 | 29530.00 | 1285.3 |
| 313.15 | 39340.00 | 1327.6 |
| 313.15 | 49150.00 | 1367.4 |
| 313.15 | 58960.00 | 1405.0 |
| 313.15 | 68770.00 | 1440.6 |
| 313.15 | 78580.00 | 1474.6 |
| 313.15 | 88390.00 | 1507.0 |
| 313.15 | 98200.00 | 1538.0 |
| 313.15 | 108000.00 | 1567.9 |
| 313.15 | 117800.00 | 1596.7 |
| 313.15 | 127600.00 | 1624.5 |
| 313.15 | 137400.00 | 1651.4 |
| 313.15 | 147200.00 | 1677.5 |
| 313.15 | 157100.00 | 1702.6 |
| 313.15 | 166900.00 | 1726.9 |
| 313.15 | 176700.00 | 1750.3 |
| 313.15 | 186500.00 | 1772.6 |
| 313.15 | 196300.00 | 1793.6 |
| 333.15 | 100.00 | 1068.8 |
| 333.15 | 5000.00 | 1097.1 |
| 333.15 | 9910.00 | 1124.4 |
| 333.15 | 19720.00 | 1176.0 |
| 333.15 | 29530.00 | 1224.0 |
| 333.15 | 39340.00 | 1268.8 |
| 333.15 | 49150.00 | 1310.8 |
| 333.15 | 58960.00 | 1350.4 |
| 333.15 | 68770.00 | 1387.7 |
| 333.15 | 78580.00 | 1423.2 |
| 333.15 | 88390.00 | 1457.0 |
| 333.15 | 98200.00 | 1489.4 |
| 333.15 | 108000.00 | 1520.4 |
| 333.15 | 117800.00 | 1550.3 |
| 333.15 | 127600.00 | 1579.1 |
| 333.15 | 137400.00 | 1607.0 |
| 333.15 | 147200.00 | 1633.9 |
| 333.15 | 157100.00 | 1659.9 |
| 333.15 | 166900.00 | 1684.9 |
| 333.15 | 176700.00 | 1708.9 |
| 333.15 | 186500.00 | 1731.8 |
| 333.15 | 196300.00 | 1753.5 |
| 353.15 | 100.00 | 995.0 |
| 353.15 | 5000.00 | 1026.2 |
| 353.15 | 9910.00 | 1055.4 |
| 353.15 | 19720.00 | 1110.7 |
| 353.15 | 29530.00 | 1162.0 |
| 353.15 | 39340.00 | 1209.8 |
| 353.15 | 49150.00 | 1254.5 |
| 353.15 | 58960.00 | 1296.3 |
| 353.15 | 68770.00 | 1335.8 |
| 353.15 | 78580.00 | 1373.0 |
| 353.15 | 88390.00 | 1408.3 |
| 353.15 | 98200.00 | 1441.9 |
| 353.15 | 108000.00 | 1474.0 |
| 353.15 | 117800.00 | 1504.7 |
| 353.15 | 127600.00 | 1534.3 |
| 353.15 | 137400.00 | 1562.7 |
| 353.15 | 147200.00 | 1590.1 |
| 353.15 | 157100.00 | 1616.4 |
| 353.15 | 166900.00 | 1641.8 |
| 353.15 | 176700.00 | 1666.1 |
| 353.15 | 186500.00 | 1689.4 |
| 353.15 | 196300.00 | 1711.4 |
| 373.15 | 100.00 | 922.9 |
| 373.15 | 5000.00 | 957.0 |
| 373.15 | 9910.00 | 989.6 |
| 373.15 | 19720.00 | 1050.4 |
| 373.15 | 29530.00 | 1105.8 |
| 373.15 | 39340.00 | 1156.5 |
| 373.15 | 49150.00 | 1203.2 |
| 373.15 | 58960.00 | 1246.3 |
| 373.15 | 68770.00 | 1286.9 |
| 373.15 | 78580.00 | 1324.8 |
| 373.15 | 88390.00 | 1360.8 |
| 373.15 | 98200.00 | 1395.1 |
| 373.15 | 108000.00 | 1427.9 |
| 373.15 | 117800.00 | 1459.6 |
| 373.15 | 127600.00 | 1490.1 |
| 373.15 | 137400.00 | 1519.6 |
| 373.15 | 147200.00 | 1548.1 |
| 373.15 | 157100.00 | 1575.5 |
| 373.15 | 166900.00 | 1601.7 |
| 373.15 | 176700.00 | 1626.5 |
| 373.15 | 186500.00 | 1649.5 |
| 373.15 | 196300.00 | 1670.6 |
| 393.15 | 100.00 | 853.3 |
| 393.15 | 5000.00 | 893.8 |
| 393.15 | 9910.00 | 928.6 |
| 393.15 | 19720.00 | 993.2 |
| 393.15 | 29530.00 | 1051.8 |
| 393.15 | 39340.00 | 1105.2 |
| 393.15 | 49150.00 | 1154.2 |
| 393.15 | 58960.00 | 1199.4 |
| 393.15 | 68770.00 | 1241.4 |
| 393.15 | 78580.00 | 1280.8 |
| 393.15 | 88390.00 | 1318.0 |
| 393.15 | 98200.00 | 1353.3 |
| 393.15 | 108000.00 | 1387.2 |
| 393.15 | 117800.00 | 1419.7 |
| 393.15 | 127600.00 | 1451.2 |
| 393.15 | 137400.00 | 1481.6 |
| 393.15 | 147200.00 | 1511.1 |
| 393.15 | 157100.00 | 1539.5 |
| 393.15 | 166900.00 | 1566.9 |
| 393.15 | 176700.00 | 1592.8 |
| 393.15 | 186500.00 | 1617.2 |
| 393.15 | 196300.00 | 1639.7 |
| 413.15 | 100.00 | 784.0 |
| 413.15 | 5000.00 | 829.4 |
| 413.15 | 9910.00 | 867.7 |
| 413.15 | 19720.00 | 938.1 |
| 413.15 | 29530.00 | 1001.1 |
| 413.15 | 39340.00 | 1057.7 |
| 413.15 | 49150.00 | 1109.0 |
| 413.15 | 58960.00 | 1155.8 |
| 413.15 | 68770.00 | 1198.9 |
| 413.15 | 78580.00 | 1239.1 |
| 413.15 | 88390.00 | 1276.9 |
| 413.15 | 98200.00 | 1312.8 |
| 413.15 | 108000.00 | 1347.4 |
| 413.15 | 117800.00 | 1380.6 |
| 413.15 | 127600.00 | 1413.0 |
| 413.15 | 137400.00 | 1444.5 |
| 413.15 | 147200.00 | 1475.2 |
| 413.15 | 157100.00 | 1504.9 |
| 413.15 | 166900.00 | 1533.7 |
| 413.15 | 176700.00 | 1560.9 |
| 413.15 | 186500.00 | 1586.4 |
| 413.15 | 196300.00 | 1609.7 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.67] | kPa | [307.59; 431.58] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.55612e+01 | |||
| Coefficient B | -3.86347e+03 | |||
| Coefficient C | -5.46410e+01 | |||
| Temperature range, min. | 307.59 | |||
| Temperature range, max. | 431.58 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 350 400 | ||||
| Pvap | 1.33 | kPa | 307.59 | Calculated Property |
| Pvap | 2.93 | kPa | 321.37 | Calculated Property |
| Pvap | 5.98 | kPa | 335.14 | Calculated Property |
| Pvap | 11.39 | kPa | 348.92 | Calculated Property |
| Pvap | 20.49 | kPa | 362.70 | Calculated Property |
| Pvap | 35.04 | kPa | 376.47 | Calculated Property |
| Pvap | 57.36 | kPa | 390.25 | Calculated Property |
| Pvap | 90.31 | kPa | 404.03 | Calculated Property |
| Pvap | 137.38 | kPa | 417.80 | Calculated Property |
| Pvap | 202.67 | kPa | 431.58 | Calculated Property |
| Pvap | [0.69; 104.41] | kPa | [288.15; 409.15] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 1.03644e+02 | |||
| Coefficient B | -8.56728e+03 | |||
| Coefficient C | -1.32703e+01 | |||
| Coefficient D | 1.04706e-05 | |||
| Temperature range, min. | 288.15 | |||
| Temperature range, max. | 409.15 | |||
|
T(K) Vapor pressure (kPa) 0 20 40 60 80 100 300 350 400 | ||||
| Pvap | 0.69 | kPa | 288.15 | Calculated Property |
| Pvap | 1.53 | kPa | 301.59 | Calculated Property |
| Pvap | 3.15 | kPa | 315.04 | Calculated Property |
| Pvap | 6.03 | kPa | 328.48 | Calculated Property |
| Pvap | 10.86 | kPa | 341.93 | Calculated Property |
| Pvap | 18.53 | kPa | 355.37 | Calculated Property |
| Pvap | 30.18 | kPa | 368.82 | Calculated Property |
| Pvap | 47.22 | kPa | 382.26 | Calculated Property |
| Pvap | 71.31 | kPa | 395.71 | Calculated Property |
| Pvap | 104.41 | kPa | 409.15 | Calculated Property |
Similar Compounds
Find more compounds similar to Hexane, 1-chloro-.
Mixtures
- Acetic acid, butyl ester + Hexane, 1-chloro-
- Hexane, 1-chloro- + Tetrahydrofuran
- Tetrahydropyran + Hexane, 1-chloro-
- 1,3-Dioxolane + Hexane, 1-chloro-
- Hexane, 1-chloro- + 1,4-Dioxane
- Octane + Hexane, 1-chloro-
- Formamide, N,N-dimethyl- + Hexane, 1-chloro-
- N,N-Dimethylacetamide + Hexane, 1-chloro-
- 2-Pyrrolidinone, 1-methyl- + Hexane, 1-chloro-
- Benzene + Benzene, 1,3-dichloro- + Hexane, 1-chloro-
- n-Hexane + Hexane, 1-chloro-
- Hexane, 1-iodo- + Hexane, 1-chloro-
- Benzene + Hexane, 1-chloro-
- Benzene + Benzene, 1,2-dichloro- + Hexane, 1-chloro-
- Hexane, 1-chloro- + 1,8-Diaminooctane
- Hexane, 1-chloro- + 1,10-Diaminodecane
- 1,12-Dodecanediamine + Hexane, 1-chloro-
Sources
- KDB Pure (Korean Thermophysical Properties Databank)
- 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
- Vapour liquid equilibrium of cyclic ethers with 1-chlorohexane: Experimental results and UNIFAC predictions
- (P,Vm,T) Measurements of (octane + 1-chlorohexane) at temperatures from 298.15 K to 328.15 K and at pressures up to 40 MPa
- (Vapour + liquid) equilibria and excess molar enthalpies for binary mixtures containing N,N-dialkylamides and 1-chloroalkanes
- Excess enthalpies and isothermal (vapour + liquid) equilibria of (1-methyl-2-pyrrolidone + 1-chloroalkane or +,?-dichloroalkane) mixtures
- Isothermal (vapour + liquid) equilibrium of (cyclic ethers + chlorohexane) mixtures: Experimental results and SAFT modelling
- Experimental and predicted data of excess molar enthalpies and excess molar volumes for the ternary system (1,3-dichlorobenzene + benzene + 1-chlorohexane) at T = 298.15 K
- Densities, speeds of sound, isentropic compressibilities, refractive indexes, and viscosities of tetrahydrofuran with haloalkane or alkyl ethanoate at T = 303.15 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.
- Speed of Sound of Hexane + 1-Chlorohexane, Hexane + 1-Iodohexane, and 1-Chlorohexane + 1-Iodohexane at Saturation Condition
- Excess Molar Enthalpies and Excess Molar Volumes of the Ternary System 1,2-Dichlorobenzene + Benzene +1-Chlorohexane at 298.15 K
- Viscosities and Densities of Binary Mixtures of Hexane with 1-Chlorohexane between 293.15 K and 333.15 K
- Temperature Dependence of the Thermophysical Properties of 1-Chlorohexane, 1-Iodohexane, 1-Iodoheptane, and 1-Chlorononane at Saturation Condition
- 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
- Speeds of Sound, Densities, and Isentropic Compressibilities of 1-Chlorohexane at Temperatures from (293.15 to 413.15) K and Pressures up to 200 MPa
- Activity Coefficients at Infinite Dilution by GLC in Alkanediamines as Stationary Phases
- Densities and Isothermal Compressibilities at Pressures up to 20 MPa of the Systems N,N-Dimethylformamide or N,N-Dimethylacetamide + 1-Chloroalkane
- Densities and Isothermal Compressibilities at Pressures up to 20 MPa of the Systems 1-Methyl-2-pyrrolidone + 1-Chloroalkane or + r,u-Dichloroalkane
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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