- InChI
- InChI=1S/C12H25Br/c1-2-3-4-5-6-7-8-9-10-11-12-13/h2-12H2,1H3
- InChI Key
- PBLNBZIONSLZBU-UHFFFAOYSA-N
- Formula
- C12H25Br
- SMILES
- CCCCCCCCCCCCBr
- Molecular Weight1
- 249.23
- CAS
- 143-15-7
- Other Names
-
- 1-Bromododecane
- Dodecyl bromide
- LAURYL BROMIDE
- N-DODECYL BROMIDE
- 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).
- 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).
- 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).
- Tboilr : Boiling point at reduced pressure (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 |
|---|---|---|---|
| ΔcH°liquid | -7950.30 ± 2.00 | kJ/mol | NIST |
| ΔfG° | 64.48 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -269.90 ± 2.60 | kJ/mol | NIST |
| ΔfH°liquid | -344.70 ± 2.60 | kJ/mol | NIST |
| ΔfusH° | 32.12 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [74.77; 74.80] | kJ/mol |
|
| ΔvapH° | 74.77 | kJ/mol | NIST |
| ΔvapH° | 74.77 ± 0.38 | kJ/mol | NIST |
| ΔvapH° | 74.77 ± 0.38 | kJ/mol | NIST |
| ΔvapH° | 74.80 ± 0.40 | kJ/mol | NIST |
| log10WS | -5.28 | Crippen Calculated Property | |
| logPoct/wat | 5.302 | Crippen Calculated Property | |
| McVol | 197.440 | ml/mol | McGowan Calculated Property |
| Pc | 1888.72 | kPa | Joback Calculated Property |
| Inp | [1549.00; 1552.00] |
|
|
| Inp | 1552.00 | NIST | |
| Inp | 1549.00 | NIST | |
| Inp | 1552.00 | NIST | |
| I | [1793.00; 1818.00] |
|
|
| I | 1800.00 | NIST | |
| I | 1793.00 | NIST | |
| I | 1818.00 | NIST | |
| Tboil | 549.20 | K | NIST |
| Tc | 714.73 | K | Joback Calculated Property |
| Tfus | 284.80 | K | Joback Calculated Property |
| Vc | 0.769 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [460.39; 547.70] | J/mol×K | [540.12; 714.73] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 460 480 500 520 540 550 600 650 700 | ||||
| Cp,gas | 460.39 | J/mol×K | 540.12 | Joback Calculated Property |
| Cp,gas | 476.62 | J/mol×K | 569.22 | Joback Calculated Property |
| Cp,gas | 492.16 | J/mol×K | 598.32 | Joback Calculated Property |
| Cp,gas | 507.01 | J/mol×K | 627.42 | Joback Calculated Property |
| Cp,gas | 521.20 | J/mol×K | 656.53 | Joback Calculated Property |
| Cp,gas | 534.75 | J/mol×K | 685.63 | Joback Calculated Property |
| Cp,gas | 547.70 | J/mol×K | 714.73 | Joback Calculated Property |
| Cp,liquid | [399.29; 476.50] | J/mol×K | [298.15; 423.15] |
|
|
T(K) Liquid phase heat capacity (J/mol×K) 400 420 440 460 480 300 350 400 | ||||
| Cp,liquid | 399.29 | J/mol×K | 298.15 | Isobari... |
| Cp,liquid | 402.38 | J/mol×K | 303.15 | Isobari... |
| Cp,liquid | 405.47 | J/mol×K | 308.15 | Isobari... |
| Cp,liquid | 408.56 | J/mol×K | 313.15 | Isobari... |
| Cp,liquid | 411.65 | J/mol×K | 318.15 | Isobari... |
| Cp,liquid | 414.75 | J/mol×K | 323.15 | Isobari... |
| Cp,liquid | 417.84 | J/mol×K | 328.15 | Isobari... |
| Cp,liquid | 420.93 | J/mol×K | 333.15 | Isobari... |
| Cp,liquid | 424.02 | J/mol×K | 338.15 | Isobari... |
| Cp,liquid | 427.11 | J/mol×K | 343.15 | Isobari... |
| Cp,liquid | 430.20 | J/mol×K | 348.15 | Isobari... |
| Cp,liquid | 433.26 | J/mol×K | 353.15 | Isobari... |
| Cp,liquid | 436.35 | J/mol×K | 358.15 | Isobari... |
| Cp,liquid | 439.44 | J/mol×K | 363.15 | Isobari... |
| Cp,liquid | 442.53 | J/mol×K | 368.15 | Isobari... |
| Cp,liquid | 445.62 | J/mol×K | 373.15 | Isobari... |
| Cp,liquid | 448.72 | J/mol×K | 378.15 | Isobari... |
| Cp,liquid | 451.81 | J/mol×K | 383.15 | Isobari... |
| Cp,liquid | 454.90 | J/mol×K | 388.15 | Isobari... |
| Cp,liquid | 457.99 | J/mol×K | 393.15 | Isobari... |
| Cp,liquid | 461.08 | J/mol×K | 398.15 | Isobari... |
| Cp,liquid | 464.14 | J/mol×K | 403.15 | Isobari... |
| Cp,liquid | 467.23 | J/mol×K | 408.15 | Isobari... |
| Cp,liquid | 470.32 | J/mol×K | 413.15 | Isobari... |
| Cp,liquid | 473.41 | J/mol×K | 418.15 | Isobari... |
| Cp,liquid | 476.50 | J/mol×K | 423.15 | Isobari... |
| η | [0.0002170; 0.0038020] | Pa×s | [284.80; 540.12] |
|
|
T(K) Dynamic viscosity (Pa×s) 0 5.00e-4 1.00e-3 1.50e-3 2.00e-3 2.50e-3 3.00e-3 3.50e-3 4.00e-3 300 400 500 | ||||
| η | 0.0038020 | Pa×s | 284.80 | Joback Calculated Property |
| η | 0.0017300 | Pa×s | 327.35 | Joback Calculated Property |
| η | 0.0009435 | Pa×s | 369.91 | Joback Calculated Property |
| η | 0.0005832 | Pa×s | 412.46 | Joback Calculated Property |
| η | 0.0003944 | Pa×s | 455.01 | Joback Calculated Property |
| η | 0.0002852 | Pa×s | 497.57 | Joback Calculated Property |
| η | 0.0002170 | Pa×s | 540.12 | Joback Calculated Property |
| ΔvapH | 62.20 | kJ/mol | 510.50 | NIST |
| ρl | [923.70; 1056.50] | kg/m3 | [273.15; 423.15] |
|
|
T(K) Liquid Density (kg/m3) 920 940 960 980 1000 1020 1040 1060 300 350 400 | ||||
| ρl | 1056.50 | kg/m3 | 273.15 | Density... |
| ρl | 1048.50 | kg/m3 | 283.15 | Density... |
| ρl | 1039.80 | kg/m3 | 293.15 | Density... |
| ρl | 1035.60 | kg/m3 | 298.15 | Density... |
| ρl | 1014.00 | kg/m3 | 323.15 | Density... |
| ρl | 996.20 | kg/m3 | 343.15 | Density... |
| ρl | 979.00 | kg/m3 | 363.15 | Density... |
| ρl | 952.40 | kg/m3 | 393.15 | Density... |
| ρl | 923.70 | kg/m3 | 423.15 | Density... |
| csound,fluid | [871.74; 1323.54] | m/s | [273.32; 423.14] |
|
|
T(K) Speed of sound in fluid (m/s) 900 1000 1100 1200 1300 300 350 400 | ||||
| csound,fluid | 1323.54 | m/s | 273.32 | Speed o... |
| csound,fluid | 1224.75 | m/s | 303.21 | Speed o... |
| csound,fluid | 1161.16 | m/s | 323.18 | Speed o... |
| csound,fluid | 1069.74 | m/s | 353.15 | Speed o... |
| csound,fluid | 982.95 | m/s | 383.17 | Speed o... |
| csound,fluid | 926.37 | m/s | 403.19 | Speed o... |
| csound,fluid | 871.74 | m/s | 423.14 | Speed o... |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | [365.50; 473.30] | K | [0.03; 13.30] |
|
| Tboilr | 365.50 ± 0.50 | K | 0.03 | NIST |
| Tboilr | 407.70 | K | 0.80 | NIST |
| Tboilr | 473.30 ± 0.70 | K | 13.30 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.63] | kPa | [419.24; 580.29] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.54636e+01 | |||
| Coefficient B | -4.93910e+03 | |||
| Coefficient C | -9.37860e+01 | |||
| Temperature range, min. | 419.24 | |||
| Temperature range, max. | 580.29 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 450 500 550 | ||||
| Pvap | 1.33 | kPa | 419.24 | Calculated Property |
| Pvap | 2.94 | kPa | 437.13 | Calculated Property |
| Pvap | 6.00 | kPa | 455.03 | Calculated Property |
| Pvap | 11.43 | kPa | 472.92 | Calculated Property |
| Pvap | 20.56 | kPa | 490.82 | Calculated Property |
| Pvap | 35.17 | kPa | 508.71 | Calculated Property |
| Pvap | 57.52 | kPa | 526.61 | Calculated Property |
| Pvap | 90.49 | kPa | 544.50 | Calculated Property |
| Pvap | 137.51 | kPa | 562.40 | Calculated Property |
| Pvap | 202.63 | kPa | 580.29 | Calculated Property |
| Pvap | [1.29; 335.91] | kPa | [411.15; 610.15] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 1.11805e+02 | |||
| Coefficient B | -1.24932e+04 | |||
| Coefficient C | -1.36262e+01 | |||
| Coefficient D | 5.05498e-06 | |||
| Temperature range, min. | 411.15 | |||
| Temperature range, max. | 610.15 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 250 300 350 450 500 550 600 | ||||
| Pvap | 1.29 | kPa | 411.15 | Calculated Property |
| Pvap | 3.28 | kPa | 433.26 | Calculated Property |
| Pvap | 7.47 | kPa | 455.37 | Calculated Property |
| Pvap | 15.47 | kPa | 477.48 | Calculated Property |
| Pvap | 29.65 | kPa | 499.59 | Calculated Property |
| Pvap | 53.17 | kPa | 521.71 | Calculated Property |
| Pvap | 90.07 | kPa | 543.82 | Calculated Property |
| Pvap | 145.35 | kPa | 565.93 | Calculated Property |
| Pvap | 224.97 | kPa | 588.04 | Calculated Property |
| Pvap | 335.91 | kPa | 610.15 | Calculated Property |
Similar Compounds
Find more compounds similar to Dodecane, 1-bromo-.
Sources
- KDB Vapor Pressure Data
- Crippen Method
- Crippen Method
- Isobaric heat capacity, isothermal compressibility and fluctuational properties of 1- bromoalkanes
- Density of Some 1-Bromoalkanes within the Temperature Range from (243.15 to 423.15) K
- 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.