- InChI
- InChI=1S/C3H5Br3/c4-1-3(6)2-5/h3H,1-2H2
- InChI Key
- FHCLGDLYRUPKAM-UHFFFAOYSA-N
- Formula
- C3H5Br3
- SMILES
- BrCC(Br)CBr
- Molecular Weight1
- 280.78
- CAS
- 96-11-7
- Other Names
-
- 1,2,3-Tribromopropane
- Glycerol tribromohydrin
- Glyceryl tribromohydrin
- s-Tribromopropane
- sym-Tribromopropane
- 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.
- 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° | 14.90 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -31.54 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 15.86 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 41.19 | kJ/mol | Joback Calculated Property |
| log10WS | -2.49 | Crippen Calculated Property | |
| logPoct/wat | 2.540 | Crippen Calculated Property | |
| McVol | 105.630 | ml/mol | McGowan Calculated Property |
| Pc | 5999.95 | kPa | Joback Calculated Property |
| Inp | 1148.00 | NIST | |
| Tboil | [493.20; 495.30] | K |
|
| Tboil | 493.20 | K | NIST |
| Tboil | 495.30 | K | NIST |
| Tc | 699.87 | K | Joback Calculated Property |
| Tfus | [285.41; 289.30] | K |
|
| Tfus | 289.30 ± 0.02 | K | NIST |
| Tfus | 285.41 ± 0.05 | K | NIST |
| Vc | 0.384 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [149.10; 178.04] | J/mol×K | [466.08; 699.87] |
|
| Cp,gas | 149.10 | J/mol×K | 466.08 | Joback Calculated Property |
| Cp,gas | 155.03 | J/mol×K | 505.05 | Joback Calculated Property |
| Cp,gas | 160.46 | J/mol×K | 544.01 | Joback Calculated Property |
| Cp,gas | 165.43 | J/mol×K | 582.98 | Joback Calculated Property |
| Cp,gas | 169.98 | J/mol×K | 621.94 | Joback Calculated Property |
| Cp,gas | 174.17 | J/mol×K | 660.91 | Joback Calculated Property |
| Cp,gas | 178.04 | J/mol×K | 699.87 | Joback Calculated Property |
| Cp,liquid | 166.50 | J/mol×K | 298.00 | NIST |
| η | [0.0004514; 0.0032395] | Pa×s | [287.97; 466.08] |
|
| η | 0.0032395 | Pa×s | 287.97 | Joback Calculated Property |
| η | 0.0020007 | Pa×s | 317.66 | Joback Calculated Property |
| η | 0.0013417 | Pa×s | 347.34 | Joback Calculated Property |
| η | 0.0009582 | Pa×s | 377.02 | Joback Calculated Property |
| η | 0.0007188 | Pa×s | 406.71 | Joback Calculated Property |
| η | 0.0005607 | Pa×s | 436.39 | Joback Calculated Property |
| η | 0.0004514 | Pa×s | 466.08 | Joback Calculated Property |
| ΔfusH | [23.78; 23.78] | kJ/mol | [289.40; 289.40] |
|
| ΔfusH | 23.78 | kJ/mol | 289.40 | NIST |
| ΔfusH | 23.78 | kJ/mol | 289.40 | NIST |
| ΔvapH | [50.20; 50.80] | kJ/mol | [439.00; 492.50] |
|
| ΔvapH | 50.20 | kJ/mol | 439.00 | NIST |
| ΔvapH | 50.80 | kJ/mol | 492.50 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 215.81] | kPa | [373.75; 524.73] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.53100e+01 | |||
| Coefficient B | -4.43013e+03 | |||
| Coefficient C | -7.88460e+01 | |||
| Temperature range, min. | 373.75 | |||
| Temperature range, max. | 524.73 | |||
| Pvap | 1.33 | kPa | 373.75 | Calculated Property |
| Pvap | 2.99 | kPa | 390.53 | Calculated Property |
| Pvap | 6.19 | kPa | 407.30 | Calculated Property |
| Pvap | 11.91 | kPa | 424.08 | Calculated Property |
| Pvap | 21.59 | kPa | 440.85 | Calculated Property |
| Pvap | 37.12 | kPa | 457.63 | Calculated Property |
| Pvap | 60.96 | kPa | 474.40 | Calculated Property |
| Pvap | 96.15 | kPa | 491.18 | Calculated Property |
| Pvap | 146.35 | kPa | 507.95 | Calculated Property |
| Pvap | 215.81 | kPa | 524.73 | Calculated Property |
Similar Compounds
Find more compounds similar to Propane, 1,2,3-tribromo-.
Sources
- Crippen Method
- Crippen Method
- Joback Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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