- InChI
- InChI=1S/C3H6Br2/c4-2-1-3-5/h1-3H2
- InChI Key
- VEFLKXRACNJHOV-UHFFFAOYSA-N
- Formula
- C3H6Br2
- SMILES
- BrCCCBr
- Molecular Weight1
- 201.89
- CAS
- 109-64-8
- Other Names
-
- 1,3-Dibromopropane
- CH2BrCH2CH2Br
- Dibromo-1,3 propane
- TRIMETHYLENE DIBROMIDE
- Trimethylene bromide
- «alpha»,«gamma»-Dibromopropane
- «omega»,«omega»'-Dibromopropane
- «alpha»,«gamma»-Dibromopropane
- «omega»,«omega»'-Dibromopropane
- 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).
- 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).
- n0 : Refractive Index.
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- I : Polar retention indices.
- ΔfusS : Entropy of fusion at a given temperature (J/mol×K).
- γ : Surface Tension (N/m).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Ttriple : Triple Point Temperature (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° | 3.02 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -52.59 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 14.10 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [45.30; 47.60] | kJ/mol |
|
| ΔvapH° | 47.46 | kJ/mol | NIST |
| ΔvapH° | 47.60 | kJ/mol | NIST |
| ΔvapH° | 47.45 ± 0.10 | kJ/mol | NIST |
| ΔvapH° | 45.30 | kJ/mol | NIST |
| IE | [10.07; 10.26] | eV |
|
| IE | 10.07 ± 0.02 | eV | NIST |
| IE | 10.10 | eV | NIST |
| IE | 10.26 | eV | NIST |
| log10WS | -2.08 | Aq. Sol... | |
| logPoct/wat | 2.166 | Crippen Calculated Property | |
| McVol | 88.130 | ml/mol | McGowan Calculated Property |
| Pc | 5343.52 | kPa | Joback Calculated Property |
| Inp | [919.00; 989.00] |
|
|
| Inp | 971.00 | NIST | |
| Inp | 989.00 | NIST | |
| Inp | 936.00 | NIST | |
| Inp | 955.00 | NIST | |
| Inp | 919.00 | NIST | |
| Inp | 963.70 | NIST | |
| Inp | 937.70 | NIST | |
| I | [1419.00; 1460.00] |
|
|
| I | 1419.00 | NIST | |
| I | 1422.00 | NIST | |
| I | 1460.00 | NIST | |
| Tboil | 440.05 | K | KDB |
| Tc | 608.96 | K | Joback Calculated Property |
| Tfus | [237.00; 239.10] | K |
|
| Tfus | 238.65 | K | KDB |
| Tfus | 239.10 | K | Aq. Sol... |
| Tfus | 238.95 ± 0.60 | K | NIST |
| Tfus | 237.00 ± 0.40 | K | NIST |
| Tfus | 238.85 ± 0.50 | K | NIST |
| Ttriple | 238.60 ± 0.20 | K | NIST |
| Vc | 0.328 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [123.47; 155.22] | J/mol×K | [400.36; 608.96] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 125 130 135 140 145 150 155 400 500 600 | ||||
| Cp,gas | 123.47 | J/mol×K | 400.36 | Joback Calculated Property |
| Cp,gas | 129.66 | J/mol×K | 435.13 | Joback Calculated Property |
| Cp,gas | 135.46 | J/mol×K | 469.89 | Joback Calculated Property |
| Cp,gas | 140.89 | J/mol×K | 504.66 | Joback Calculated Property |
| Cp,gas | 145.98 | J/mol×K | 539.43 | Joback Calculated Property |
| Cp,gas | 150.75 | J/mol×K | 574.20 | Joback Calculated Property |
| Cp,gas | 155.22 | J/mol×K | 608.96 | Joback Calculated Property |
| Cp,liquid | [156.10; 171.51] | J/mol×K | [245.70; 355.15] |
|
|
T(K) Liquid phase heat capacity (J/mol×K) 155 160 165 170 250 300 350 | ||||
| Cp,liquid | 156.10 | J/mol×K | 245.70 | NIST |
| Cp,liquid | 162.24 | J/mol×K | 285.15 | Heat Ca... |
| Cp,liquid | 162.41 | J/mol×K | 286.65 | Heat Ca... |
| Cp,liquid | 162.57 | J/mol×K | 288.15 | Heat Ca... |
| Cp,liquid | 162.74 | J/mol×K | 289.65 | Heat Ca... |
| Cp,liquid | 162.92 | J/mol×K | 291.15 | Heat Ca... |
| Cp,liquid | 163.09 | J/mol×K | 292.65 | Heat Ca... |
| Cp,liquid | 163.26 | J/mol×K | 294.15 | Heat Ca... |
| Cp,liquid | 163.44 | J/mol×K | 295.65 | Heat Ca... |
| Cp,liquid | 163.62 | J/mol×K | 297.15 | Heat Ca... |
| Cp,liquid | 159.00 | J/mol×K | 298.00 | NIST |
| Cp,liquid | 163.73 | J/mol×K | 298.15 | Heat Ca... |
| Cp,liquid | 163.70 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 163.79 | J/mol×K | 298.65 | Heat Ca... |
| Cp,liquid | 163.97 | J/mol×K | 300.15 | Heat Ca... |
| Cp,liquid | 164.15 | J/mol×K | 301.65 | Heat Ca... |
| Cp,liquid | 164.34 | J/mol×K | 303.15 | Heat Ca... |
| Cp,liquid | 164.52 | J/mol×K | 304.65 | Heat Ca... |
| Cp,liquid | 164.71 | J/mol×K | 306.15 | Heat Ca... |
| Cp,liquid | 164.89 | J/mol×K | 307.65 | Heat Ca... |
| Cp,liquid | 165.08 | J/mol×K | 309.15 | Heat Ca... |
| Cp,liquid | 165.27 | J/mol×K | 310.65 | Heat Ca... |
| Cp,liquid | 165.46 | J/mol×K | 312.15 | Heat Ca... |
| Cp,liquid | 165.65 | J/mol×K | 313.65 | Heat Ca... |
| Cp,liquid | 165.85 | J/mol×K | 315.15 | Heat Ca... |
| Cp,liquid | 166.04 | J/mol×K | 316.65 | Heat Ca... |
| Cp,liquid | 166.24 | J/mol×K | 318.15 | Heat Ca... |
| Cp,liquid | 166.43 | J/mol×K | 319.65 | Heat Ca... |
| Cp,liquid | 166.63 | J/mol×K | 321.15 | Heat Ca... |
| Cp,liquid | 166.83 | J/mol×K | 322.65 | Heat Ca... |
| Cp,liquid | 167.04 | J/mol×K | 324.15 | Heat Ca... |
| Cp,liquid | 167.24 | J/mol×K | 325.65 | Heat Ca... |
| Cp,liquid | 167.44 | J/mol×K | 327.15 | Heat Ca... |
| Cp,liquid | 167.65 | J/mol×K | 328.65 | Heat Ca... |
| Cp,liquid | 167.86 | J/mol×K | 330.15 | Heat Ca... |
| Cp,liquid | 168.06 | J/mol×K | 331.65 | Heat Ca... |
| Cp,liquid | 168.27 | J/mol×K | 333.15 | Heat Ca... |
| Cp,liquid | 168.49 | J/mol×K | 334.65 | Heat Ca... |
| Cp,liquid | 168.70 | J/mol×K | 336.15 | Heat Ca... |
| Cp,liquid | 168.91 | J/mol×K | 337.65 | Heat Ca... |
| Cp,liquid | 169.13 | J/mol×K | 339.15 | Heat Ca... |
| Cp,liquid | 169.35 | J/mol×K | 340.65 | Heat Ca... |
| Cp,liquid | 169.56 | J/mol×K | 342.15 | Heat Ca... |
| Cp,liquid | 169.78 | J/mol×K | 343.65 | Heat Ca... |
| Cp,liquid | 170.00 | J/mol×K | 345.15 | Heat Ca... |
| Cp,liquid | 170.23 | J/mol×K | 346.65 | Heat Ca... |
| Cp,liquid | 170.45 | J/mol×K | 348.15 | Heat Ca... |
| Cp,liquid | 170.68 | J/mol×K | 349.65 | Heat Ca... |
| Cp,liquid | 170.90 | J/mol×K | 351.15 | Heat Ca... |
| Cp,liquid | 171.13 | J/mol×K | 352.65 | Heat Ca... |
| Cp,liquid | 171.36 | J/mol×K | 354.15 | Heat Ca... |
| Cp,liquid | 171.51 | J/mol×K | 355.15 | Heat Ca... |
| η | [0.0004696; 0.0030679] | Pa×s | [243.17; 400.36] |
|
|
T(K) Dynamic viscosity (Pa×s) 5.00e-4 1.00e-3 1.50e-3 2.00e-3 2.50e-3 3.00e-3 250 300 350 400 | ||||
| η | 0.0030679 | Pa×s | 243.17 | Joback Calculated Property |
| η | 0.0019272 | Pa×s | 269.37 | Joback Calculated Property |
| η | 0.0013146 | Pa×s | 295.57 | Joback Calculated Property |
| η | 0.0009544 | Pa×s | 321.76 | Joback Calculated Property |
| η | 0.0007271 | Pa×s | 347.96 | Joback Calculated Property |
| η | 0.0005754 | Pa×s | 374.16 | Joback Calculated Property |
| η | 0.0004696 | Pa×s | 400.36 | Joback Calculated Property |
| ΔfusH | [14.64; 14.64] | kJ/mol | [238.60; 238.60] |
|
| ΔfusH | 14.64 | kJ/mol | 238.60 | NIST |
| ΔfusH | 14.64 | kJ/mol | 238.60 | NIST |
| ΔfusH | 14.64 | kJ/mol | 238.60 | NIST |
| ΔvapH | [44.80; 47.89] | kJ/mol | [308.00; 439.40] |
|
|
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 44.5 45 45.5 46 46.5 47 47.5 48 350 400 | ||||
| ΔvapH | 47.30 ± 0.10 | kJ/mol | 308.00 | NIST |
| ΔvapH | 46.70 ± 0.10 | kJ/mol | 315.00 | NIST |
| ΔvapH | 46.10 ± 0.10 | kJ/mol | 323.00 | NIST |
| ΔvapH | 45.50 ± 0.10 | kJ/mol | 330.00 | NIST |
| ΔvapH | 44.80 ± 0.10 | kJ/mol | 338.00 | NIST |
| ΔvapH | 46.60 | kJ/mol | 372.00 | NIST |
| ΔvapH | 47.80 | kJ/mol | 419.00 | NIST |
| ΔvapH | 47.89 | kJ/mol | 439.40 | NIST |
| n0 | 1.52040 | 298.15 | Thermod... | |
| ρl | [1941.18; 1980.22] | kg/m3 | [292.55; 314.58] |
|
|
T(K) Liquid Density (kg/m3) 1940 1950 1960 1970 1980 300 310 | ||||
| ρl | 1980.22 | kg/m3 | 292.55 | Thermod... |
| ρl | 1970.22 | kg/m3 | 297.98 | Thermod... |
| ρl | 1961.58 | kg/m3 | 303.07 | Thermod... |
| ρl | 1952.84 | kg/m3 | 308.02 | Thermod... |
| ρl | 1941.18 | kg/m3 | 314.58 | Thermod... |
| ΔfusS | 61.40 | J/mol×K | 238.60 | NIST |
| γ | [0.04; 0.04] | N/m | [293.15; 313.15] |
|
|
T(K) Surface Tension (N/m) 0.04 0.04 0.04 0.04 0.04 0.04 295 300 305 310 | ||||
| γ | 0.04 | N/m | 293.15 | The add... |
| γ | 0.04 | N/m | 298.15 | The add... |
| γ | 0.04 | N/m | 303.15 | The add... |
| γ | 0.04 | N/m | 308.15 | The add... |
| γ | 0.04 | N/m | 313.15 | The add... |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 294.08] | kPa | [330.28; 467.14] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.61869e+01 | |||
| Coefficient B | -4.23517e+03 | |||
| Coefficient C | -6.39080e+01 | |||
| Temperature range, min. | 330.28 | |||
| Temperature range, max. | 467.14 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 250 300 350 400 450 | ||||
| Pvap | 1.33 | kPa | 330.28 | Calculated Property |
| Pvap | 3.15 | kPa | 345.49 | Calculated Property |
| Pvap | 6.80 | kPa | 360.69 | Calculated Property |
| Pvap | 13.63 | kPa | 375.90 | Calculated Property |
| Pvap | 25.62 | kPa | 391.11 | Calculated Property |
| Pvap | 45.51 | kPa | 406.31 | Calculated Property |
| Pvap | 77.01 | kPa | 421.52 | Calculated Property |
| Pvap | 124.84 | kPa | 436.73 | Calculated Property |
| Pvap | 194.85 | kPa | 451.93 | Calculated Property |
| Pvap | 294.08 | kPa | 467.14 | Calculated Property |
| Pvap | [0.15; 102.57] | kPa | [283.15; 441.15] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 3.97029e+01 | |||
| Coefficient B | -6.17431e+03 | |||
| Coefficient C | -3.53806e+00 | |||
| Coefficient D | 2.40591e-06 | |||
| Temperature range, min. | 283.15 | |||
| Temperature range, max. | 441.15 | |||
|
T(K) Vapor pressure (kPa) 0 20 40 60 80 100 300 350 400 | ||||
| Pvap | 0.15 | kPa | 283.15 | Calculated Property |
| Pvap | 0.45 | kPa | 300.71 | Calculated Property |
| Pvap | 1.17 | kPa | 318.26 | Calculated Property |
| Pvap | 2.74 | kPa | 335.82 | Calculated Property |
| Pvap | 5.88 | kPa | 353.37 | Calculated Property |
| Pvap | 11.67 | kPa | 370.93 | Calculated Property |
| Pvap | 21.71 | kPa | 388.48 | Calculated Property |
| Pvap | 38.17 | kPa | 406.04 | Calculated Property |
| Pvap | 63.92 | kPa | 423.59 | Calculated Property |
| Pvap | 102.57 | kPa | 441.15 | Calculated Property |
Similar Compounds
Find more compounds similar to Propane, 1,3-dibromo-.
Mixtures
- Ethyl formate + Propane, 1,3-dibromo-
- Propane, 1,3-dibromo- + Ethyl Acetate
- Propanoic acid, ethyl ester + Propane, 1,3-dibromo-
- Propane, 1,3-dibromo- + Butanoic acid, ethyl ester
- Pentanoic acid, ethyl ester + Propane, 1,3-dibromo-
- Propane, 1,3-dibromo- + Methyl formate
- Propane, 1,3-dibromo- + Acetic acid, methyl ester
- Propane, 1,3-dibromo- + Methyl propionate
- Butanoic acid, methyl ester + Propane, 1,3-dibromo-
- Propane, 1,3-dibromo- + Methyl valerate
- Formic acid, butyl ester + Propane, 1,3-dibromo-
- Propane, 1,3-dibromo- + Acetic acid, butyl ester
- Propanoic acid, butyl ester + Propane, 1,3-dibromo-
- Butanoic acid, butyl ester + Propane, 1,3-dibromo-
Sources
- KDB Vapor Pressure Data
- Crippen Method
- Thermodynamic and Acoustic Properties of 1,3-Dibromopropane and 1,5-Dibromopentane within the Temperature Range From 293K to 313K at Pressures up to 100MPa
- Thermodynamic study of (alkyl esters + a,x-alkyl dihalides) II: HE m and V E m for 25 binary mixtures {xCu-1H2u-1CO2C2H5 + (1 - x)a,x-BrCH2(CH2)v-2CH2Br}, where u = 1 to 5, a = 1 and v = x = 2 to 6
- Thermodynamic study of (alkyl esters + alpha,omega-alkyl dihalides) IV: Hex and Vex for 25 binary mixtures {xC(u-1)H(2u-1)CO2CH3 + (1-x)alpha,omega-BrCH2(CH2)(v-2)CH2Br}, where u = 1 to 5, alpha = 1 and v = omega = 2 to 6
- Thermodynamic study of (alkyl esters + alpha,beta-alkyl dihalides) VI.H and V for 20 binary mixtures {xCu-1H2u-1CO2(CH2)3CH3 + (1 - x)alpha,omega-BrCH2(CH2)v-2CH2Br}, where u = 1 to 5, alpha = 1, and v = omega = 2 to 6
- The additivity of surface and volumetric properties of alpha,omega-dihalogenoalkanes
- Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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