- InChI
- InChI=1S/C9H19Cl/c1-2-3-4-5-6-7-8-9-10/h2-9H2,1H3
- InChI Key
- RKAMCQVGHFRILV-UHFFFAOYSA-N
- Formula
- C9H19Cl
- SMILES
- CCCCCCCCCCl
- Molecular Weight1
- 162.70
- CAS
- 2473-01-0
- Other Names
-
- 1-Chlorononane
- Nonyl chloride
- n-Nonyl 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).
- 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).
- Pc : Critical Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- 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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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ΔfG° | 12.97 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -244.83 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 23.26 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 55.90 | kJ/mol | NIST |
| log10WS | -3.74 | Crippen Calculated Property | |
| logPoct/wat | 3.976 | Crippen Calculated Property | |
| McVol | 149.910 | ml/mol | McGowan Calculated Property |
| Pc | 2227.09 | kPa | Joback Calculated Property |
| Inp | [1150.00; 1167.00] |
|
|
| Inp | 1159.00 | NIST | |
| Inp | Outlier 1167.00 | NIST | |
| Inp | 1150.00 | NIST | |
| Inp | 1154.00 | NIST | |
| Inp | 1159.00 | NIST | |
| Inp | 1152.00 | NIST | |
| Inp | 1159.00 | NIST | |
| Inp | 1154.00 | NIST | |
| Inp | 1152.00 | NIST | |
| I | [1350.00; 1364.00] |
|
|
| I | 1350.00 | NIST | |
| I | 1363.00 | NIST | |
| I | 1364.00 | NIST | |
| I | 1364.00 | NIST | |
| I | 1363.00 | NIST | |
| Tboil | [475.15; 476.70] | K |
|
| Tboil | 476.70 | K | NIST |
| Tboil | 475.15 ± 1.50 | K | NIST |
| Tc | 612.60 | K | Joback Calculated Property |
| Tfus | 221.11 | K | Joback Calculated Property |
| Vc | 0.589 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [304.65; 379.53] | J/mol×K | [442.75; 612.60] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 300 320 340 360 380 450 500 550 600 | ||||
| Cp,gas | 304.65 | J/mol×K | 442.75 | Joback Calculated Property |
| Cp,gas | 318.43 | J/mol×K | 471.06 | Joback Calculated Property |
| Cp,gas | 331.68 | J/mol×K | 499.37 | Joback Calculated Property |
| Cp,gas | 344.40 | J/mol×K | 527.67 | Joback Calculated Property |
| Cp,gas | 356.60 | J/mol×K | 555.98 | Joback Calculated Property |
| Cp,gas | 368.31 | J/mol×K | 584.29 | Joback Calculated Property |
| Cp,gas | 379.53 | J/mol×K | 612.60 | Joback Calculated Property |
| Cp,liquid | [294.32; 329.63] | J/mol×K | [293.15; 373.15] |
|
|
T(K) Liquid phase heat capacity (J/mol×K) 295 300 305 310 315 320 325 330 300 320 340 360 | ||||
| Cp,liquid | 294.32 | J/mol×K | 293.15 | Tempera... |
| Cp,liquid | 296.44 | J/mol×K | 298.15 | Tempera... |
| Cp,liquid | 298.55 | J/mol×K | 303.15 | Tempera... |
| Cp,liquid | 300.67 | J/mol×K | 308.15 | Tempera... |
| Cp,liquid | 302.78 | J/mol×K | 313.15 | Tempera... |
| Cp,liquid | 304.90 | J/mol×K | 318.15 | Tempera... |
| Cp,liquid | 307.18 | J/mol×K | 323.15 | Tempera... |
| Cp,liquid | 309.46 | J/mol×K | 328.15 | Tempera... |
| Cp,liquid | 311.57 | J/mol×K | 333.15 | Tempera... |
| Cp,liquid | 313.85 | J/mol×K | 338.15 | Tempera... |
| Cp,liquid | 315.96 | J/mol×K | 343.15 | Tempera... |
| Cp,liquid | 318.24 | J/mol×K | 348.15 | Tempera... |
| Cp,liquid | 320.52 | J/mol×K | 353.15 | Tempera... |
| Cp,liquid | 322.80 | J/mol×K | 358.15 | Tempera... |
| Cp,liquid | 325.07 | J/mol×K | 363.15 | Tempera... |
| Cp,liquid | 327.35 | J/mol×K | 368.15 | Tempera... |
| Cp,liquid | 329.63 | J/mol×K | 373.15 | Tempera... |
| η | [0.0002658; 0.0053880] | Pa×s | [221.11; 442.75] |
|
|
T(K) Dynamic viscosity (Pa×s) 0 1.00e-3 2.00e-3 3.00e-3 4.00e-3 5.00e-3 250 300 350 400 | ||||
| η | 0.0053880 | Pa×s | 221.11 | Joback Calculated Property |
| η | 0.0022788 | Pa×s | 258.05 | Joback Calculated Property |
| η | 0.0011955 | Pa×s | 294.99 | Joback Calculated Property |
| η | 0.0007241 | Pa×s | 331.93 | Joback Calculated Property |
| η | 0.0004849 | Pa×s | 368.87 | Joback Calculated Property |
| η | 0.0003493 | Pa×s | 405.81 | Joback Calculated Property |
| η | 0.0002658 | Pa×s | 442.75 | Joback Calculated Property |
| ΔvapH | [51.50; 53.40] | kJ/mol | [410.00; 436.00] |
|
| ΔvapH | 53.40 | kJ/mol | 410.00 | NIST |
| ΔvapH | 51.50 | kJ/mol | 436.00 | NIST |
| ν | [0.0000005; 0.0000017] | m2/s | [296.21; 413.15] |
|
|
T(K) Kinematic viscosity (m2/s) 4.00e-7 6.00e-7 8.00e-7 1.00e-6 1.20e-6 1.40e-6 1.60e-6 1.80e-6 300 350 400 | ||||
| ν | 0.0000017 | m2/s | 296.21 | Kinemat... |
| ν | 0.0000016 | m2/s | 300.65 | Kinemat... |
| ν | 0.0000013 | m2/s | 313.15 | Kinemat... |
| ν | 0.0000012 | m2/s | 318.15 | Kinemat... |
| ν | 0.0000011 | m2/s | 323.15 | Kinemat... |
| ν | 0.0000011 | m2/s | 328.15 | Kinemat... |
| ν | 0.0000010 | m2/s | 333.15 | Kinemat... |
| ν | 0.0000009 | m2/s | 338.15 | Kinemat... |
| ν | 0.0000009 | m2/s | 343.15 | Kinemat... |
| ν | 0.0000009 | m2/s | 348.15 | Kinemat... |
| ν | 0.0000008 | m2/s | 353.15 | Kinemat... |
| ν | 0.0000008 | m2/s | 358.15 | Kinemat... |
| ν | 0.0000007 | m2/s | 363.15 | Kinemat... |
| ν | 0.0000007 | m2/s | 368.15 | Kinemat... |
| ν | 0.0000007 | m2/s | 373.15 | Kinemat... |
| ν | 0.0000006 | m2/s | 383.15 | Kinemat... |
| ν | 0.0000006 | m2/s | 393.15 | Kinemat... |
| ν | 0.0000005 | m2/s | 403.15 | Kinemat... |
| ν | 0.0000005 | m2/s | 413.15 | Kinemat... |
| csound,fluid | [856.00; 1297.20] | m/s | [293.15; 423.15] |
|
|
T(K) Speed of sound in fluid (m/s) 900 1000 1100 1200 1300 300 350 400 | ||||
| csound,fluid | 1297.20 | m/s | 293.15 | Tempera... |
| csound,fluid | 1278.20 | m/s | 298.15 | Tempera... |
| csound,fluid | 1259.50 | m/s | 303.15 | Tempera... |
| csound,fluid | 1240.90 | m/s | 308.15 | Tempera... |
| csound,fluid | 1222.50 | m/s | 313.15 | Tempera... |
| csound,fluid | 1204.30 | m/s | 318.15 | Tempera... |
| csound,fluid | 1186.30 | m/s | 323.15 | Tempera... |
| csound,fluid | 1168.40 | m/s | 328.15 | Tempera... |
| csound,fluid | 1150.70 | m/s | 333.15 | Tempera... |
| csound,fluid | 1133.20 | m/s | 338.15 | Tempera... |
| csound,fluid | 1115.90 | m/s | 343.15 | Tempera... |
| csound,fluid | 1098.80 | m/s | 348.15 | Tempera... |
| csound,fluid | 1081.90 | m/s | 353.15 | Tempera... |
| csound,fluid | 1065.10 | m/s | 358.15 | Tempera... |
| csound,fluid | 1048.50 | m/s | 363.15 | Tempera... |
| csound,fluid | 1032.20 | m/s | 368.15 | Tempera... |
| csound,fluid | 1015.90 | m/s | 373.15 | Tempera... |
| csound,fluid | 999.10 | m/s | 378.15 | Tempera... |
| csound,fluid | 982.70 | m/s | 383.15 | Tempera... |
| csound,fluid | 966.40 | m/s | 388.15 | Tempera... |
| csound,fluid | 950.30 | m/s | 393.15 | Tempera... |
| csound,fluid | 934.30 | m/s | 398.15 | Tempera... |
| csound,fluid | 918.40 | m/s | 403.15 | Tempera... |
| csound,fluid | 902.60 | m/s | 408.15 | Tempera... |
| csound,fluid | 887.00 | m/s | 413.15 | Tempera... |
| csound,fluid | 871.40 | m/s | 418.15 | Tempera... |
| csound,fluid | 856.00 | m/s | 423.15 | Tempera... |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.65] | kPa | [363.70; 503.52] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.57153e+01 | |||
| Coefficient B | -4.46724e+03 | |||
| Coefficient C | -7.41370e+01 | |||
| Temperature range, min. | 363.70 | |||
| Temperature range, max. | 503.52 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 400 450 500 | ||||
| Pvap | 1.33 | kPa | 363.70 | Calculated Property |
| Pvap | 2.93 | kPa | 379.24 | Calculated Property |
| Pvap | 5.95 | kPa | 394.77 | Calculated Property |
| Pvap | 11.32 | kPa | 410.31 | Calculated Property |
| Pvap | 20.36 | kPa | 425.84 | Calculated Property |
| Pvap | 34.85 | kPa | 441.38 | Calculated Property |
| Pvap | 57.09 | kPa | 456.91 | Calculated Property |
| Pvap | 90.01 | kPa | 472.45 | Calculated Property |
| Pvap | 137.13 | kPa | 487.98 | Calculated Property |
| Pvap | 202.65 | kPa | 503.52 | Calculated Property |
Similar Compounds
Find more compounds similar to Nonane, 1-chloro-.
Mixtures
Sources
- Crippen Method
- Crippen Method
- Temperature Dependence of the Thermophysical Properties of 1-Chlorohexane, 1-Iodohexane, 1-Iodoheptane, and 1-Chlorononane at Saturation Condition
- Kinematic Viscosity of 1-Iodohexane, 1-Iodoheptane, and 1-Chlorononane at Temperatures from (293.15 to 423.15) K
- Temperature Dependence of the Speed of Sound of Nonane + 1-Chlorononane in the Range of (293.15 to 423.15) K
- Joback Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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Outlier This icon means
that the value is more than 2 standard deviations away from the
property mean.