- InChI
- InChI=1S/C9H19Br/c1-2-3-4-5-6-7-8-9-10/h2-9H2,1H3
- InChI Key
- AYMUQTNXKPEMLM-UHFFFAOYSA-N
- Formula
- C9H19Br
- SMILES
- CCCCCCCCCBr
- Molecular Weight1
- 207.15
- CAS
- 693-58-3
- Other Names
-
- 1-Bromononane
- 1-NONYL BROMIDE
- 1-n-Nonyl bromide
- N-NONYL BROMIDE
- Nonyl bromide
- n-Nonyl-1-bromide
- 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).
- ΔfusH : Enthalpy of fusion at a given temperature (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).
- 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° | 39.22 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -202.76 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 24.35 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 42.06 | kJ/mol | Joback Calculated Property |
| log10WS | -4.02 | Crippen Calculated Property | |
| logPoct/wat | 4.132 | Crippen Calculated Property | |
| McVol | 155.170 | ml/mol | McGowan Calculated Property |
| Pc | 2467.81 | kPa | Joback Calculated Property |
| Inp | [1220.00; 1244.00] |
|
|
| Inp | 1220.00 | NIST | |
| Inp | 1240.00 | NIST | |
| Inp | 1244.00 | NIST | |
| Inp | 1231.00 | NIST | |
| Inp | 1238.00 | NIST | |
| Inp | 1220.00 | NIST | |
| Inp | 1231.00 | NIST | |
| I | [1476.00; 1496.00] |
|
|
| I | 1478.00 | NIST | |
| I | 1476.00 | NIST | |
| I | 1496.00 | NIST | |
| I | 1496.00 | NIST | |
| Tboil | [474.00; 474.20] | K |
|
| Tboil | 474.20 | K | NIST |
| Tboil | 474.00 | K | NIST |
| Tc | 650.81 | K | Joback Calculated Property |
| Tfus | [242.40; 244.20] | K |
|
| Tfus | 244.15 | K | KDB |
| Tfus | 244.20 ± 0.20 | K | NIST |
| Tfus | 242.40 ± 0.20 | K | NIST |
| Tfus | 244.09 ± 0.25 | K | NIST |
| Tfus | 242.44 ± 0.15 | K | NIST |
| Vc | 0.602 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [320.03; 394.99] | J/mol×K | [471.48; 650.81] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 320 340 360 380 400 500 550 600 650 | ||||
| Cp,gas | 320.03 | J/mol×K | 471.48 | Joback Calculated Property |
| Cp,gas | 333.98 | J/mol×K | 501.37 | Joback Calculated Property |
| Cp,gas | 347.32 | J/mol×K | 531.26 | Joback Calculated Property |
| Cp,gas | 360.07 | J/mol×K | 561.15 | Joback Calculated Property |
| Cp,gas | 372.25 | J/mol×K | 591.03 | Joback Calculated Property |
| Cp,gas | 383.88 | J/mol×K | 620.92 | Joback Calculated Property |
| Cp,gas | 394.99 | J/mol×K | 650.81 | Joback Calculated Property |
| Cp,liquid | [302.55; 364.88] | J/mol×K | [284.15; 423.15] |
|
|
T(K) Liquid phase heat capacity (J/mol×K) 300 310 320 330 340 350 360 370 300 350 400 | ||||
| Cp,liquid | 302.55 | J/mol×K | 284.15 | Heat Ca... |
| Cp,liquid | 303.54 | J/mol×K | 286.65 | Heat Ca... |
| Cp,liquid | 304.62 | J/mol×K | 289.15 | Heat Ca... |
| Cp,liquid | 305.57 | J/mol×K | 291.65 | Heat Ca... |
| Cp,liquid | 306.69 | J/mol×K | 294.15 | Heat Ca... |
| Cp,liquid | 307.68 | J/mol×K | 296.65 | Heat Ca... |
| Cp,liquid | 308.30 | J/mol×K | 298.15 | Isobari... |
| Cp,liquid | 308.80 | J/mol×K | 299.15 | Heat Ca... |
| Cp,liquid | 309.82 | J/mol×K | 301.65 | Heat Ca... |
| Cp,liquid | 310.56 | J/mol×K | 303.15 | Isobari... |
| Cp,liquid | 310.95 | J/mol×K | 304.15 | Heat Ca... |
| Cp,liquid | 311.91 | J/mol×K | 306.65 | Heat Ca... |
| Cp,liquid | 312.82 | J/mol×K | 308.15 | Isobari... |
| Cp,liquid | 313.01 | J/mol×K | 309.15 | Heat Ca... |
| Cp,liquid | 314.10 | J/mol×K | 311.65 | Heat Ca... |
| Cp,liquid | 315.10 | J/mol×K | 313.15 | Isobari... |
| Cp,liquid | 315.18 | J/mol×K | 314.15 | Heat Ca... |
| Cp,liquid | 316.32 | J/mol×K | 316.65 | Heat Ca... |
| Cp,liquid | 317.36 | J/mol×K | 318.15 | Isobari... |
| Cp,liquid | 317.44 | J/mol×K | 319.15 | Heat Ca... |
| Cp,liquid | 318.70 | J/mol×K | 321.65 | Heat Ca... |
| Cp,liquid | 319.61 | J/mol×K | 323.15 | Isobari... |
| Cp,liquid | 319.80 | J/mol×K | 324.15 | Heat Ca... |
| Cp,liquid | 320.96 | J/mol×K | 326.65 | Heat Ca... |
| Cp,liquid | 321.87 | J/mol×K | 328.15 | Isobari... |
| Cp,liquid | 322.16 | J/mol×K | 329.15 | Heat Ca... |
| Cp,liquid | 323.32 | J/mol×K | 331.65 | Heat Ca... |
| Cp,liquid | 324.15 | J/mol×K | 333.15 | Isobari... |
| Cp,liquid | 324.63 | J/mol×K | 334.15 | Heat Ca... |
| Cp,liquid | 325.00 | J/mol×K | 336.65 | Heat Ca... |
| Cp,liquid | 326.41 | J/mol×K | 338.15 | Isobari... |
| Cp,liquid | 326.99 | J/mol×K | 339.15 | Heat Ca... |
| Cp,liquid | 328.13 | J/mol×K | 341.65 | Heat Ca... |
| Cp,liquid | 328.67 | J/mol×K | 343.15 | Isobari... |
| Cp,liquid | 329.39 | J/mol×K | 344.15 | Heat Ca... |
| Cp,liquid | 330.49 | J/mol×K | 346.65 | Heat Ca... |
| Cp,liquid | 330.92 | J/mol×K | 348.15 | Isobari... |
| Cp,liquid | 331.79 | J/mol×K | 349.15 | Heat Ca... |
| Cp,liquid | 333.04 | J/mol×K | 351.65 | Heat Ca... |
| Cp,liquid | 333.20 | J/mol×K | 353.15 | Isobari... |
| Cp,liquid | 333.74 | J/mol×K | 353.15 | Heat Ca... |
| Cp,liquid | 335.46 | J/mol×K | 358.15 | Isobari... |
| Cp,liquid | 337.72 | J/mol×K | 363.15 | Isobari... |
| Cp,liquid | 339.98 | J/mol×K | 368.15 | Isobari... |
| Cp,liquid | 342.26 | J/mol×K | 373.15 | Isobari... |
| Cp,liquid | 344.51 | J/mol×K | 378.15 | Isobari... |
| Cp,liquid | 346.77 | J/mol×K | 383.15 | Isobari... |
| Cp,liquid | 349.03 | J/mol×K | 388.15 | Isobari... |
| Cp,liquid | 351.31 | J/mol×K | 393.15 | Isobari... |
| Cp,liquid | 353.57 | J/mol×K | 398.15 | Isobari... |
| Cp,liquid | 355.82 | J/mol×K | 403.15 | Isobari... |
| Cp,liquid | 358.08 | J/mol×K | 408.15 | Isobari... |
| Cp,liquid | 360.36 | J/mol×K | 413.15 | Isobari... |
| Cp,liquid | 362.62 | J/mol×K | 418.15 | Isobari... |
| Cp,liquid | 364.88 | J/mol×K | 423.15 | Isobari... |
| η | [0.0002865; 0.0042127] | Pa×s | [250.99; 471.48] |
|
|
T(K) Dynamic viscosity (Pa×s) 0 1.00e-3 2.00e-3 3.00e-3 4.00e-3 300 400 | ||||
| η | 0.0042127 | Pa×s | 250.99 | Joback Calculated Property |
| η | 0.0020219 | Pa×s | 287.74 | Joback Calculated Property |
| η | 0.0011459 | Pa×s | 324.49 | Joback Calculated Property |
| η | 0.0007290 | Pa×s | 361.24 | Joback Calculated Property |
| η | 0.0005042 | Pa×s | 397.98 | Joback Calculated Property |
| η | 0.0003711 | Pa×s | 434.73 | Joback Calculated Property |
| η | 0.0002865 | Pa×s | 471.48 | Joback Calculated Property |
| ΔfusH | [30.12; 30.12] | kJ/mol | [243.20; 243.20] |
|
| ΔfusH | 30.12 | kJ/mol | 243.20 | NIST |
| ΔfusH | 30.12 | kJ/mol | 243.20 | NIST |
| ΔvapH | [52.20; 53.10] | kJ/mol | [450.50; 470.00] |
|
| ΔvapH | 53.10 | kJ/mol | 450.50 | NIST |
| ΔvapH | 52.20 | kJ/mol | 470.00 | NIST |
| csound,fluid | [808.79; 1329.91] | m/s | [253.46; 422.72] |
|
|
T(K) Speed of sound in fluid (m/s) 800 900 1000 1100 1200 1300 250 300 350 400 | ||||
| csound,fluid | 1329.91 | m/s | 253.46 | Speed o... |
| csound,fluid | 1262.72 | m/s | 273.29 | Speed o... |
| csound,fluid | 1165.07 | m/s | 303.15 | Speed o... |
| csound,fluid | 1101.12 | m/s | 323.14 | Speed o... |
| csound,fluid | 1009.85 | m/s | 353.10 | Speed o... |
| csound,fluid | 921.46 | m/s | 383.05 | Speed o... |
| csound,fluid | 864.42 | m/s | 402.98 | Speed o... |
| csound,fluid | 808.79 | m/s | 422.72 | Speed o... |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.66] | kPa | [375.64; 496.39] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.76688e+01 | |||
| Coefficient B | -5.16229e+03 | |||
| Coefficient C | -7.86350e+01 | |||
| Temperature range, min. | 375.64 | |||
| Temperature range, max. | 496.39 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 400 450 | ||||
| Pvap | 1.33 | kPa | 375.64 | Calculated Property |
| Pvap | 2.83 | kPa | 389.06 | Calculated Property |
| Pvap | 5.63 | kPa | 402.47 | Calculated Property |
| Pvap | 10.61 | kPa | 415.89 | Calculated Property |
| Pvap | 19.06 | kPa | 429.31 | Calculated Property |
| Pvap | 32.79 | kPa | 442.72 | Calculated Property |
| Pvap | 54.27 | kPa | 456.14 | Calculated Property |
| Pvap | 86.77 | kPa | 469.56 | Calculated Property |
| Pvap | 134.49 | kPa | 482.97 | Calculated Property |
| Pvap | 202.66 | kPa | 496.39 | Calculated Property |
| Pvap | [3.94; 317.51] | kPa | [391.15; 549.15] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 9.69072e+01 | |||
| Coefficient B | -1.03437e+04 | |||
| Coefficient C | -1.17047e+01 | |||
| Coefficient D | 5.06259e-06 | |||
| Temperature range, min. | 391.15 | |||
| Temperature range, max. | 549.15 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 250 300 400 450 500 550 | ||||
| Pvap | 3.94 | kPa | 391.15 | Calculated Property |
| Pvap | 7.88 | kPa | 408.71 | Calculated Property |
| Pvap | 14.71 | kPa | 426.26 | Calculated Property |
| Pvap | 25.87 | kPa | 443.82 | Calculated Property |
| Pvap | 43.23 | kPa | 461.37 | Calculated Property |
| Pvap | 69.04 | kPa | 478.93 | Calculated Property |
| Pvap | 106.03 | kPa | 496.48 | Calculated Property |
| Pvap | 157.33 | kPa | 514.04 | Calculated Property |
| Pvap | 226.49 | kPa | 531.59 | Calculated Property |
| Pvap | 317.51 | kPa | 549.15 | Calculated Property |
Similar Compounds
Find more compounds similar to Nonane, 1-bromo-.
Sources
- KDB Vapor Pressure Data
- Crippen Method
- Crippen Method
- Isobaric heat capacity, isothermal compressibility and fluctuational properties of 1- bromoalkanes
- 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
- Speed of Sound, Densities, and Isentropic Compressibilities of Liquid 1-Bromoalkanes at Temperatures from (243.15 to 423.15) K
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
Note: Cheméo is only indexing the data, follow the source links to retrieve the latest data. The source is also providing more information like the publication year, authors and more. Take the time to validate and double check the source of the data.