- InChI
- InChI=1S/C14H14/c1-11-8-9-14(10-12(11)2)13-6-4-3-5-7-13/h3-10H,1-2H3
- InChI Key
- CKENDVLIAVMNDW-UHFFFAOYSA-N
- Formula
- C14H14
- SMILES
- Cc1ccc(-c2ccccc2)cc1C
- Molecular Weight1
- 182.26
- CAS
- 4433-11-8
- Other Names
-
- 3,4-dimethylbiphenyl
- biphenyl, 3,4-dimethyl-
- 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).
- 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 |
|---|---|---|---|
| ω | 0.4298 | Relay (1.0) Calculated Property | |
| ΔfG° | 272.56 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | 145.20 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfusH° | 19.32 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 76.04 | kJ/mol | Relay (1.0) Calculated Property |
| IE | 7.94 | eV | Relay (1.0) Calculated Property |
| log10WS | -5.26 | Relay (1.0) Calculated Property | |
| logPoct/wat | 3.970 | Crippen Calculated Property | |
| McVol | 160.600 | ml/mol | McGowan Calculated Property |
| Pc | 2684.64 | kPa | Joback Calculated Property |
| Inp | [1683.00; 1697.00] |
|
|
| Inp | 1683.00 | NIST | |
| Inp | 1697.00 | NIST | |
| I | [2279.00; 2324.00] |
|
|
| I | 2324.00 | NIST | |
| I | 2279.00 | NIST | |
| Tboil | [555.00; 555.00] | K |
|
| Tboil | 555.00 ± 4.00 | K | NIST |
| Tboil | 555.00 ± 4.00 | K | NIST |
| Tc | 791.13 | K | Relay (1.0) Calculated Property |
| Tfus | 302.60 ± 1.50 | K | NIST |
| Vc | 0.604 | m3/kmol | Relay (1.0) Calculated Property |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [193.06; 498.47] | 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 | -4.90500e+01 | |||
| Coefficient B | 1.05704e+00 | |||
| Coefficient C | -6.66120e-04 | |||
| Coefficient D | 1.56600e-07 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 193.06 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 248.47 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 297.35 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 340.21 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 377.53 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 409.81 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 437.55 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 461.25 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 481.39 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 498.47 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0021589; 0.0001761] | Pa×s | [302.60; 577.54] |
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 | -1.14025e+01 | |||
| Coefficient B | 1.59300e+03 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 302.60 | |||
| Temperature range, max. | 577.54 | |||
| η | 0.0021589 | Pa×s | 302.60 | Calculated Property |
| η | 0.0013323 | Pa×s | 333.15 | Calculated Property |
| η | 0.0008916 | Pa×s | 363.70 | Calculated Property |
| η | 0.0006350 | Pa×s | 394.25 | Calculated Property |
| η | 0.0004749 | Pa×s | 424.79 | Calculated Property |
| η | 0.0003692 | Pa×s | 455.34 | Calculated Property |
| η | 0.0002963 | Pa×s | 485.89 | Calculated Property |
| η | 0.0002441 | Pa×s | 516.44 | Calculated Property |
| η | 0.0002055 | Pa×s | 546.99 | Calculated Property |
| η | 0.0001761 | Pa×s | 577.54 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.63] | kPa | [414.12; 589.99] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.44135e+01 | |||
| Coefficient B | -4.50104e+03 | |||
| Coefficient C | -9.54820e+01 | |||
| Temperature range, min. | 414.12 | |||
| Temperature range, max. | 589.99 | |||
| Pvap | 1.33 | kPa | 414.12 | Calculated Property |
| Pvap | 3.02 | kPa | 433.66 | Calculated Property |
| Pvap | 6.24 | kPa | 453.20 | Calculated Property |
| Pvap | 11.97 | kPa | 472.74 | Calculated Property |
| Pvap | 21.55 | kPa | 492.28 | Calculated Property |
| Pvap | 36.69 | kPa | 511.83 | Calculated Property |
| Pvap | 59.57 | kPa | 531.37 | Calculated Property |
| Pvap | 92.79 | kPa | 550.91 | Calculated Property |
| Pvap | 139.34 | kPa | 570.45 | Calculated Property |
| Pvap | 202.63 | kPa | 589.99 | Calculated Property |
Similar Compounds
Find more compounds similar to 1,1'-Biphenyl, 3,4-dimethyl-.
Sources
- Cheméo Relay (1.0)
- Crippen Method
- Crippen Method
- Joback Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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