- InChI
- InChI=1S/C10H7Br/c11-10-7-3-5-8-4-1-2-6-9(8)10/h1-7H
- InChI Key
- DLKQHBOKULLWDQ-UHFFFAOYSA-N
- Formula
- C10H7Br
- SMILES
- Brc1cccc2ccccc12
- Molecular Weight1
- 207.07
- CAS
- 90-11-9
- Other Names
-
- .alpha.-bromonaphthalene
- 1-Bromonaphthalene
- 1-Bromonapthalene
- 1-NAPHTHYL BROMIDE
- ALPHA-BROMONAPHTHALENE
- «alpha»-Bromonaphthalene
- «alpha»-Naphthyl bromide
- «alpha»-Bromonaphthalene
- «alpha»-Naphthyl bromide
- ΔcH°liquid : Standard liquid enthalpy of combustion (kJ/mol).
- Cp,gas : Ideal gas 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).
- 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).
- IE : Ionization energy (eV).
- 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.
- 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 |
|---|---|---|---|
| ΔcH°liquid | [-5047.10; -5024.90] | kJ/mol |
|
| ΔcH°liquid | -5047.10 ± 2.20 | kJ/mol | NIST |
| ΔcH°liquid | -5024.90 ± 0.80 | kJ/mol | NIST |
| ΔfG° | 257.07 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | 174.30 ± 5.60 | kJ/mol | NIST |
| ΔfH°liquid | 111.60 ± 2.60 | kJ/mol | NIST |
| ΔfusH° | 17.61 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [62.70; 63.90] | kJ/mol |
|
| ΔvapH° | 63.90 ± 0.40 | kJ/mol | NIST |
| ΔvapH° | 62.70 ± 5.00 | kJ/mol | NIST |
| IE | [8.08; 8.09] | eV |
|
| IE | 8.08 ± 0.03 | eV | NIST |
| IE | 8.08 ± 0.03 | eV | NIST |
| IE | 8.09 | eV | NIST |
| log10WS | [-4.35; -4.35] |
|
|
| log10WS | -4.35 | Aq. Sol... | |
| log10WS | -4.35 | Estimat... | |
| logPoct/wat | 3.602 | Crippen Calculated Property | |
| McVol | 126.040 | ml/mol | McGowan Calculated Property |
| Pc | 4173.09 | kPa | Joback Calculated Property |
| Inp | [1434.00; 1434.00] |
|
|
| Inp | 1434.00 | NIST | |
| Inp | 1434.00 | NIST | |
| Inp | 1434.00 | NIST | |
| I | 2157.00 | NIST | |
| Tboil | [554.20; 554.35] | K |
|
| Tboil | 554.35 | K | KDB |
| Tboil | 554.20 | K | NIST |
| Tboil | 554.25 ± 0.70 | K | NIST |
| Tc | 800.62 | K | Joback Calculated Property |
| Tfus | [271.88; 279.25] | K |
|
| Tfus | 279.25 | K | KDB |
| Tfus | 271.88 | K | Aq. Sol... |
| Tfus | 275.00 ± 1.00 | K | NIST |
| Tfus | 279.25 ± 0.20 | K | NIST |
| Tfus | 279.25 ± 0.30 | K | NIST |
| Vc | 0.471 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [244.65; 302.26] | J/mol×K | [545.00; 800.62] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 240 250 260 270 280 290 300 600 700 800 | ||||
| Cp,gas | 244.65 | J/mol×K | 545.00 | Joback Calculated Property |
| Cp,gas | 256.61 | J/mol×K | 587.60 | Joback Calculated Property |
| Cp,gas | 267.49 | J/mol×K | 630.21 | Joback Calculated Property |
| Cp,gas | 277.39 | J/mol×K | 672.81 | Joback Calculated Property |
| Cp,gas | 286.42 | J/mol×K | 715.42 | Joback Calculated Property |
| Cp,gas | 294.68 | J/mol×K | 758.02 | Joback Calculated Property |
| Cp,gas | 302.26 | J/mol×K | 800.62 | Joback Calculated Property |
| η | [0.0003922; 0.0016175] | Pa×s | [333.90; 545.00] |
|
|
T(K) Dynamic viscosity (Pa×s) 4.00e-4 6.00e-4 8.00e-4 1.00e-3 1.20e-3 1.40e-3 1.60e-3 400 500 | ||||
| η | 0.0016175 | Pa×s | 333.90 | Joback Calculated Property |
| η | 0.0011413 | Pa×s | 369.08 | Joback Calculated Property |
| η | 0.0008557 | Pa×s | 404.27 | Joback Calculated Property |
| η | 0.0006718 | Pa×s | 439.45 | Joback Calculated Property |
| η | 0.0005467 | Pa×s | 474.63 | Joback Calculated Property |
| η | 0.0004578 | Pa×s | 509.82 | Joback Calculated Property |
| η | 0.0003922 | Pa×s | 545.00 | Joback Calculated Property |
| ΔfusH | [15.16; 15.16] | kJ/mol | [271.40; 271.40] |
|
| ΔfusH | 15.16 | kJ/mol | 271.40 | NIST |
| ΔfusH | 15.16 | kJ/mol | 271.40 | NIST |
| ΔvapH | [45.80; 58.50] | kJ/mol | [327.00; 514.00] |
|
| ΔvapH | 56.00 ± 6.00 | kJ/mol | 327.00 | NIST |
| ΔvapH | 58.50 | kJ/mol | 456.00 | NIST |
| ΔvapH | 45.80 | kJ/mol | 514.00 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.64] | kPa | [407.92; 532.96] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.90252e+01 | |||
| Coefficient B | -6.39560e+03 | |||
| Coefficient C | -6.65960e+01 | |||
| Temperature range, min. | 407.92 | |||
| Temperature range, max. | 532.96 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 450 500 | ||||
| Pvap | 1.33 | kPa | 407.92 | Calculated Property |
| Pvap | 2.77 | kPa | 421.81 | Calculated Property |
| Pvap | 5.46 | kPa | 435.71 | Calculated Property |
| Pvap | 10.24 | kPa | 449.60 | Calculated Property |
| Pvap | 18.38 | kPa | 463.49 | Calculated Property |
| Pvap | 31.70 | kPa | 477.39 | Calculated Property |
| Pvap | 52.75 | kPa | 491.28 | Calculated Property |
| Pvap | 84.99 | kPa | 505.17 | Calculated Property |
| Pvap | 133.00 | kPa | 519.07 | Calculated Property |
| Pvap | 202.64 | kPa | 532.96 | Calculated Property |
| Pvap | [2.09e-04; 3730.17] | kPa | [279.35; 824.00] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 9.46369e+01 | |||
| Coefficient B | -1.12075e+04 | |||
| Coefficient C | -1.12370e+01 | |||
| Coefficient D | 3.88225e-06 | |||
| Temperature range, min. | 279.35 | |||
| Temperature range, max. | 824.00 | |||
|
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 3500 4000 400 600 800 | ||||
| Pvap | 2.09e-04 | kPa | 279.35 | Calculated Property |
| Pvap | 0.03 | kPa | 339.87 | Calculated Property |
| Pvap | 0.93 | kPa | 400.38 | Calculated Property |
| Pvap | 9.27 | kPa | 460.90 | Calculated Property |
| Pvap | 49.06 | kPa | 521.42 | Calculated Property |
| Pvap | 173.06 | kPa | 581.93 | Calculated Property |
| Pvap | 465.78 | kPa | 642.45 | Calculated Property |
| Pvap | 1043.18 | kPa | 702.97 | Calculated Property |
| Pvap | 2059.67 | kPa | 763.48 | Calculated Property |
| Pvap | 3730.17 | kPa | 824.00 | Calculated Property |
Similar Compounds
Find more compounds similar to Naphthalene, 1-bromo-.
Mixtures
Sources
- KDB Vapor Pressure Data
- Crippen Method
- Solubility of Bromoderivatives C60Brn (n = 6, 8, 24) in 1-Chloronaphthalene and 1-Bromonaphthalene in the Temperature Range (10 to 60) deg C
- Temperature Dependence of Solubility of Individual Light Fullerenes and Industrial Fullerene Mixture in 1-Chloronaphthalene and 1-Bromonaphthalene
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- 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.