- InChI
- InChI=1S/C10H20Br2/c1-2-3-4-5-6-7-8-10(12)9-11/h10H,2-9H2,1H3
- InChI Key
- XBRBOTTWTQOCJH-UHFFFAOYSA-N
- Formula
- C10H20Br2
- SMILES
- CCCCCCCCC(Br)CBr
- Molecular Weight1
- 300.08
- CAS
- 28467-71-2
- Other Names
-
- 1,2-Dibromodecane
- ω : Acentric Factor.
- 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).
- 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).
- 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).
- 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 |
|---|---|---|---|
| ω | 0.6574 | Relay (1.0) Calculated Property | |
| ΔfG° | 59.52 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -225.92 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfusH° | 28.70 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 70.14 | kJ/mol | Relay (1.0) Calculated Property |
| IE | 9.93 | eV | Relay (1.0) Calculated Property |
| log10WS | -5.93 | Relay (1.0) Calculated Property | |
| logPoct/wat | 4.895 | Crippen Calculated Property | |
| McVol | 186.760 | ml/mol | McGowan Calculated Property |
| Pc | 2421.88 | kPa | Joback Calculated Property |
| Tboil | 530.92 | K | Relay (1.0) Calculated Property |
| Tc | 736.83 | K | Relay (1.0) Calculated Property |
| Tfus | 301.15 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Vc | 0.688 | m3/kmol | Relay (1.0) Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | 67.00 | kJ/mol | 446.00 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [245.28; 553.92] | J/mol×K | [273.00; 1000.00] |
Joback Predicted correlation
|
| Equation | Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,gas in J/mol×K, T in K | |||
| Coefficient A | 8.49800e+00 | |||
| Coefficient B | 1.03612e+00 | |||
| Coefficient C | -6.66200e-04 | |||
| Coefficient D | 1.75500e-07 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 245.28 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 299.44 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 347.35 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 389.54 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 426.58 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 459.03 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 487.43 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 512.34 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 534.32 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 553.92 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0039916; 0.0002797] | Pa×s | [301.15; 528.84] |
Joback Predicted correlation
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K | |||
| Coefficient A | -1.16980e+01 | |||
| Coefficient B | 1.85942e+03 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Comment | Liquid phase. Joback/Reid (1987), valid from Tf to 0.7·Tc. | |||
| Temperature range, min. | 301.15 | |||
| Temperature range, max. | 528.84 | |||
| η | 0.0039916 | Pa×s | 301.15 | Calculated Property |
| η | 0.0024737 | Pa×s | 326.45 | Calculated Property |
| η | 0.0016422 | Pa×s | 351.75 | Calculated Property |
| η | 0.0011518 | Pa×s | 377.05 | Calculated Property |
| η | 0.0008447 | Pa×s | 402.34 | Calculated Property |
| η | 0.0006427 | Pa×s | 427.64 | Calculated Property |
| η | 0.0005041 | Pa×s | 452.94 | Calculated Property |
| η | 0.0004057 | Pa×s | 478.24 | Calculated Property |
| η | 0.0003337 | Pa×s | 503.54 | Calculated Property |
| η | 0.0002797 | Pa×s | 528.84 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.63] | kPa | [399.03; 553.74] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.54516e+01 | |||
| Coefficient B | -4.73524e+03 | |||
| Coefficient C | -8.67640e+01 | |||
| Temperature range, min. | 399.03 | |||
| Temperature range, max. | 553.74 | |||
| Pvap | 1.33 | kPa | 399.03 | Calculated Property |
| Pvap | 2.94 | kPa | 416.22 | Calculated Property |
| Pvap | 6.00 | kPa | 433.41 | Calculated Property |
| Pvap | 11.44 | kPa | 450.60 | Calculated Property |
| Pvap | 20.57 | kPa | 467.79 | Calculated Property |
| Pvap | 35.18 | kPa | 484.98 | Calculated Property |
| Pvap | 57.54 | kPa | 502.17 | Calculated Property |
| Pvap | 90.51 | kPa | 519.36 | Calculated Property |
| Pvap | 137.53 | kPa | 536.55 | Calculated Property |
| Pvap | 202.63 | kPa | 553.74 | Calculated Property |
| Pvap | [0.13; 100.51] | kPa | [368.80; 523.60] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.92171e+01 | |||
| Coefficient B | -7.24755e+03 | |||
| Coefficient C | -2.74250e+01 | |||
| Reference | Stull, 1947 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 368.80 | |||
| Temperature range, max. | 523.60 | |||
| Pvap | 0.13 | kPa | 368.80 | Calculated Property |
| Pvap | 0.37 | kPa | 386.00 | Calculated Property |
| Pvap | 0.93 | kPa | 403.20 | Calculated Property |
| Pvap | 2.17 | kPa | 420.40 | Calculated Property |
| Pvap | 4.70 | kPa | 437.60 | Calculated Property |
| Pvap | 9.57 | kPa | 454.80 | Calculated Property |
| Pvap | 18.45 | kPa | 472.00 | Calculated Property |
| Pvap | 33.86 | kPa | 489.20 | Calculated Property |
| Pvap | 59.49 | kPa | 506.40 | Calculated Property |
| Pvap | 100.51 | kPa | 523.60 | Calculated Property |
Similar Compounds
Find more compounds similar to DECANE, 1,2-DIBROMO-.
Sources
- Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) ChEDL chemicals 1.5.2, from Bradley, J.-C.; Williams, A.; Lang, A. Jean-Claude Bradley Open Melting Point Dataset. Figshare, 2014 (CC0).
- Cheméo Relay (1.0)
- Crippen Method
- Crippen Method
- Joback Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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