- InChI
- InChI=1S/C24H18/c1-3-7-19(8-4-1)21-11-15-23(16-12-21)24-17-13-22(14-18-24)20-9-5-2-6-10-20/h1-18H
- InChI Key
- GPRIERYVMZVKTC-UHFFFAOYSA-N
- Formula
- C24H18
- SMILES
-
c1ccc(-c2ccc(-c3ccc(-c4ccccc4)
cc3)cc2)cc1 - Molecular Weight1
- 306.40
- CAS
- 135-70-6
- Other Names
-
- 1,1'-biphenyl, 4,4'-diphenyl-
- 4,4'-diphenylbiphenyl
- Quadriphenyl
- benzerythrene
- p,p'-Quaterphenyl
- p-quaterphenyl
- p-tetraphenyl
- ΔcH°solid : Standard solid enthalpy of combustion (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,solid : Solid phase heat capacity (J/mol×K).
- η : Dynamic viscosity (Pa×s).
- EA : Electron affinity (eV).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- ΔfH°gas : Enthalpy of formation at standard conditions (kJ/mol).
- ΔfH°solid : Solid 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).
- ΔsubH° : Enthalpy of sublimation 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.
- ΔfusS : Entropy of fusion at a given temperature (J/mol×K).
- S°solid,1 bar : Solid phase molar entropy at standard conditions (J/mol×K).
- Tboil : Normal Boiling Point Temperature (K).
- Tboilr : Boiling point at reduced pressure (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.
Cheméo is a service of Céondo GmbH, since 2007, we provide simulation, modelling and software development services for the industry.
Do not hesitate to contact us for your projects.
Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ΔcH°solid | -12244.00 ± 6.30 | kJ/mol | NIST |
| EA | 0.66 ± 0.02 | eV | NIST |
| ΔfG° | 581.58 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | [382.00; 400.00] | kJ/mol |
|
| ΔfH°gas | 400.00 ± 11.00 | kJ/mol | NIST |
| ΔfH°gas | 382.00 ± 7.50 | kJ/mol | NIST |
| ΔfH°solid | [227.00; 227.00] | kJ/mol |
|
| ΔfH°solid | 227.00 ± 7.00 | kJ/mol | NIST |
| ΔfH°solid | 227.00 ± 6.30 | kJ/mol | NIST |
| ΔfusH° | 33.30 | kJ/mol | Joback Calculated Property |
| ΔsubH° | [155.00; 172.50] | kJ/mol |
|
| ΔsubH° | 172.50 ± 8.40 | kJ/mol | NIST |
| ΔsubH° | 156.00 ± 1.00 | kJ/mol | NIST |
| ΔsubH° | 155.00 | kJ/mol | NIST |
| ΔvapH° | 136.10 ± 1.60 | kJ/mol | NIST |
| IE | 8.08 ± 0.05 | eV | NIST |
| log10WS | -9.28 | Crippen Calculated Property | |
| logPoct/wat | 6.688 | Crippen Calculated Property | |
| McVol | 253.980 | ml/mol | McGowan Calculated Property |
| Pc | 2014.51 | kPa | Joback Calculated Property |
| Inp | [472.80; 488.18] |
|
|
| Inp | 472.80 | NIST | |
| Inp | 488.18 | NIST | |
| Inp | 472.81 | NIST | |
| Inp | 488.18 | NIST | |
| S°solid,1 bar | 363.64 | J/mol×K | NIST |
| Tboil | 865.20 | K | Joback Calculated Property |
| Tc | 1146.33 | K | Joback Calculated Property |
| Tfus | [576.00; 591.00] | K |
|
| Tfus | 586.70 ± 0.50 | K | NIST |
| Tfus | 587.20 ± 0.50 | K | NIST |
| Tfus | 576.00 ± 2.00 | K | NIST |
| Tfus | 581.60 ± 4.00 | K | NIST |
| Tfus | 591.00 ± 4.00 | K | NIST |
| Ttriple | 594.40 | K | Isomeri... |
| Vc | 0.948 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [732.93; 813.64] | J/mol×K | [865.20; 1146.33] |
|
| Cp,gas | 732.93 | J/mol×K | 865.20 | Joback Calculated Property |
| Cp,gas | 749.87 | J/mol×K | 912.06 | Joback Calculated Property |
| Cp,gas | 765.15 | J/mol×K | 958.91 | Joback Calculated Property |
| Cp,gas | 778.96 | J/mol×K | 1005.77 | Joback Calculated Property |
| Cp,gas | 791.51 | J/mol×K | 1052.62 | Joback Calculated Property |
| Cp,gas | 803.00 | J/mol×K | 1099.48 | Joback Calculated Property |
| Cp,gas | 813.64 | J/mol×K | 1146.33 | Joback Calculated Property |
| Cp,solid | [340.00; 363.45] | J/mol×K | [298.15; 300.00] |
|
| Cp,solid | 363.45 | J/mol×K | 298.15 | Reassem... |
| Cp,solid | 362.52 | J/mol×K | 298.15 | NIST |
| Cp,solid | 340.00 | J/mol×K | 300.00 | NIST |
| η | [0.0000654; 0.0006475] | Pa×s | [490.96; 865.20] |
|
| η | 0.0006475 | Pa×s | 490.96 | Joback Calculated Property |
| η | 0.0003563 | Pa×s | 553.33 | Joback Calculated Property |
| η | 0.0002213 | Pa×s | 615.71 | Joback Calculated Property |
| η | 0.0001500 | Pa×s | 678.08 | Joback Calculated Property |
| η | 0.0001086 | Pa×s | 740.45 | Joback Calculated Property |
| η | 0.0000827 | Pa×s | 802.83 | Joback Calculated Property |
| η | 0.0000654 | Pa×s | 865.20 | Joback Calculated Property |
| ΔfusH | [37.80; 57.60] | kJ/mol | [586.70; 587.20] |
|
| ΔfusH | 57.60 | kJ/mol | 586.70 | NIST |
| ΔfusH | 37.80 | kJ/mol | 587.20 | NIST |
| ΔfusH | 37.80 | kJ/mol | 587.20 | NIST |
| Pvap | [2.38e-10; 0.12] | kPa | [298.15; 510.00] |
|
| Pvap | 2.38e-10 | kPa | 298.15 | Hypothe... |
| Pvap | 3.35e-10 | kPa | 300.00 | Hypothe... |
| Pvap | 1.94e-09 | kPa | 310.00 | Hypothe... |
| Pvap | 9.84e-09 | kPa | 320.00 | Hypothe... |
| Pvap | 4.41e-08 | kPa | 330.00 | Hypothe... |
| Pvap | 1.77e-07 | kPa | 340.00 | Hypothe... |
| Pvap | 6.44e-07 | kPa | 350.00 | Hypothe... |
| Pvap | 2.13e-06 | kPa | 360.00 | Hypothe... |
| Pvap | 6.49e-06 | kPa | 370.00 | Hypothe... |
| Pvap | 1.83e-05 | kPa | 380.00 | Hypothe... |
| Pvap | 4.81e-05 | kPa | 390.00 | Hypothe... |
| Pvap | 1.19e-04 | kPa | 400.00 | Hypothe... |
| Pvap | 2.76e-04 | kPa | 410.00 | Hypothe... |
| Pvap | 6.07e-04 | kPa | 420.00 | Hypothe... |
| Pvap | 1.27e-03 | kPa | 430.00 | Hypothe... |
| Pvap | 2.54e-03 | kPa | 440.00 | Hypothe... |
| Pvap | 4.87e-03 | kPa | 450.00 | Hypothe... |
| Pvap | 8.99e-03 | kPa | 460.00 | Hypothe... |
| Pvap | 0.02 | kPa | 470.00 | Hypothe... |
| Pvap | 0.03 | kPa | 480.00 | Hypothe... |
| Pvap | 0.05 | kPa | 490.00 | Hypothe... |
| Pvap | 0.07 | kPa | 500.00 | Hypothe... |
| Pvap | 0.12 | kPa | 510.00 | Hypothe... |
| ΔfusS | [64.40; 98.20] | J/mol×K | [586.70; 587.20] |
|
| ΔfusS | 98.20 | J/mol×K | 586.70 | NIST |
| ΔfusS | 64.40 | J/mol×K | 587.20 | NIST |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | 701.20 | K | 2.40 | NIST |
Similar Compounds
![Bicyclo[6.2.0]decapentaene.](data:image/png;base64,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)
Find more compounds similar to 1,1':4',1'':4'',1'''-Quaterphenyl.
Sources
- Crippen Method
- Crippen Method
- Reassembling and testing of a high-precision heat capacity drop calorimeter. Heat capacity of some polyphenyls at T = 298.15 K
- Isomerization effect on the heat capacities and phase behavior of oligophenyls isomers series
- Hypothetical Thermodynamic Properties. Subcooled Vaporization Enthalpies and Vapor Pressures of Polyaromatic Hydrocarbons
- Joback Method
- McGowan Method
- NIST Webbook
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.