- InChI
- InChI=1S/C24H18/c1-4-10-19(11-5-1)22-16-23(20-12-6-2-7-13-20)18-24(17-22)21-14-8-3-9-15-21/h1-18H
- InChI Key
- SXWIAEOZZQADEY-UHFFFAOYSA-N
- Formula
- C24H18
- SMILES
-
c1ccc(-c2cc(-c3ccccc3)cc(-c3cc
ccc3)c2)cc1 - Molecular Weight1
- 306.40
- CAS
- 612-71-5
- Other Names
-
- 1,1'-Biphenyl, 3,5-diphenyl-
- 1,3,5-triphenylbenzene
- 5'-Phenyl-1,1':3',1''-terphenyl
- 5'-Phenyl-m-terphenyl
- NSC 17358
- Symmetrical triphenylbenzene
- Triphenylbenzene
- benzene, 1,3,5-triphenyl-
- m-Terphenyl, 5'-phenyl-
- s-Triphenylbenzene
- 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).
- 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 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).
- Psub : Sublimation 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).
- 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 |
|---|---|---|---|
| ΔcH°solid | -12241.30 ± 5.30 | kJ/mol | NIST |
| ΔfG° | 581.58 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | 371.80 ± 3.80 | kJ/mol | NIST |
| ΔfH°solid | [222.00; 224.60] | kJ/mol |
|
| ΔfH°solid | 222.00 ± 3.40 | kJ/mol | NIST |
| ΔfH°solid | 224.60 ± 5.40 | kJ/mol | NIST |
| ΔfusH° | [31.10; 149.50] | kJ/mol |
|
| ΔfusH° | 147.70 | kJ/mol | New Knu... |
| ΔfusH° | 147.90 | kJ/mol | New Knu... |
| ΔfusH° | 148.40 | kJ/mol | New Knu... |
| ΔfusH° | 149.50 | kJ/mol | New Knu... |
| ΔfusH° | 31.10 | kJ/mol | Vapor P... |
| ΔvapH° | [133.40; 140.00] | kJ/mol |
|
| ΔvapH° | 133.40 ± 2.00 | kJ/mol | NIST |
| ΔvapH° | 140.00 | kJ/mol | 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 | [469.48; 2891.00] |
|
|
| Inp | 2891.00 | NIST | |
| Inp | 469.48 | NIST | |
| S°solid,1 bar | [367.40; 375.50] | J/mol×K |
|
| S°solid,1 bar | 375.50 | J/mol×K | NIST |
| S°solid,1 bar | 367.40 | J/mol×K | NIST |
| Tboil | 733.20 | K | NIST |
| Tc | 1146.33 | K | Joback Calculated Property |
| Tfus | [444.00; 450.10] | K |
|
| Tfus | 450.10 ± 4.00 | K | NIST |
| Tfus | 448.00 ± 0.30 | K | NIST |
| Tfus | 444.00 ± 1.50 | K | NIST |
| Tfus | 446.00 ± 3.00 | K | NIST |
| Ttriple | 446.00 ± 1.00 | K | NIST |
| 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] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 740 760 780 800 820 900 1000 1100 | ||||
| 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 | [357.96; 361.00] | J/mol×K | [298.10; 298.15] |
|
| Cp,solid | 358.32 | J/mol×K | 298.10 | NIST |
| Cp,solid | 357.96 | J/mol×K | 298.15 | Reassem... |
| Cp,solid | 361.00 | J/mol×K | 298.15 | NIST |
| η | [0.0000654; 0.0006475] | Pa×s | [490.96; 865.20] |
|
|
T(K) Dynamic viscosity (Pa×s) 1.00e-4 2.00e-4 3.00e-4 4.00e-4 5.00e-4 6.00e-4 7.00e-4 500 600 700 800 | ||||
| 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 | [32.60; 33.40] | kJ/mol | [445.20; 446.00] |
|
| ΔfusH | 32.60 | kJ/mol | 445.20 | NIST |
| ΔfusH | 33.40 | kJ/mol | 446.00 | NIST |
| ΔfusH | 33.40 | kJ/mol | 446.00 | NIST |
| ΔfusH | 33.40 | kJ/mol | 446.00 | NIST |
| ΔsubH | [141.20; 164.40] | kJ/mol | [363.00; 427.00] |
|
|
T(K) Enthalpy of sublimation at a given temperature (kJ/mol) 140 145 150 155 160 165 380 400 420 | ||||
| ΔsubH | 164.40 ± 4.20 | kJ/mol | 363.00 | NIST |
| ΔsubH | 145.60 ± 0.90 | kJ/mol | 376.00 | NIST |
| ΔsubH | 142.20 | kJ/mol | 392.00 | NIST |
| ΔsubH | 141.20 ± 0.70 | kJ/mol | 418.00 | NIST |
| ΔsubH | 142.00 | kJ/mol | 427.00 | NIST |
| ΔvapH | [77.50; 118.00] | kJ/mol | [477.00; 617.50] |
|
| ΔvapH | 118.00 | kJ/mol | 477.00 | NIST |
| ΔvapH | 77.50 | kJ/mol | 617.50 | NIST |
| Psub | [1.39e-04; 1.20e-03] | kPa | [407.36; 429.29] |
|
|
T(K) Sublimation pressure (kPa) 2.00e-4 4.00e-4 6.00e-4 8.00e-4 1.00e-3 1.20e-3 410 415 420 425 | ||||
| Psub | 1.40e-04 | kPa | 407.36 | The des... |
| Psub | 1.41e-04 | kPa | 407.36 | The des... |
| Psub | 1.39e-04 | kPa | 407.36 | The des... |
| Psub | 1.44e-04 | kPa | 408.04 | Develop... |
| Psub | 1.49e-04 | kPa | 408.05 | Develop... |
| Psub | 1.54e-04 | kPa | 408.16 | Develop... |
| Psub | 1.73e-04 | kPa | 409.30 | The des... |
| Psub | 1.66e-04 | kPa | 409.30 | The des... |
| Psub | 1.64e-04 | kPa | 409.30 | The des... |
| Psub | 2.10e-04 | kPa | 411.30 | The des... |
| Psub | 2.06e-04 | kPa | 411.30 | The des... |
| Psub | 2.15e-04 | kPa | 411.30 | The des... |
| Psub | 2.38e-04 | kPa | 413.04 | Develop... |
| Psub | 2.47e-04 | kPa | 413.05 | Develop... |
| Psub | 2.53e-04 | kPa | 413.16 | Develop... |
| Psub | 2.56e-04 | kPa | 413.23 | The des... |
| Psub | 2.51e-04 | kPa | 413.23 | The des... |
| Psub | 2.51e-04 | kPa | 413.23 | The des... |
| Psub | 3.16e-04 | kPa | 415.35 | The des... |
| Psub | 3.16e-04 | kPa | 415.35 | The des... |
| Psub | 3.17e-04 | kPa | 415.35 | The des... |
| Psub | 3.48e-04 | kPa | 416.86 | The des... |
| Psub | 3.61e-04 | kPa | 416.86 | The des... |
| Psub | 3.70e-04 | kPa | 417.22 | The des... |
| Psub | 3.71e-04 | kPa | 417.22 | The des... |
| Psub | 3.88e-04 | kPa | 418.03 | Develop... |
| Psub | 4.03e-04 | kPa | 418.05 | Develop... |
| Psub | 4.16e-04 | kPa | 418.15 | Develop... |
| Psub | 4.54e-04 | kPa | 419.24 | The des... |
| Psub | 4.70e-04 | kPa | 419.24 | The des... |
| Psub | 5.68e-04 | kPa | 421.36 | The des... |
| Psub | 5.42e-04 | kPa | 421.36 | The des... |
| Psub | 5.63e-04 | kPa | 421.36 | The des... |
| Psub | 6.22e-04 | kPa | 423.03 | Develop... |
| Psub | 6.34e-04 | kPa | 423.03 | Develop... |
| Psub | 6.48e-04 | kPa | 423.04 | Develop... |
| Psub | 6.72e-04 | kPa | 423.16 | Develop... |
| Psub | 6.68e-04 | kPa | 423.29 | The des... |
| Psub | 6.72e-04 | kPa | 423.29 | The des... |
| Psub | 6.49e-04 | kPa | 423.29 | The des... |
| Psub | 7.96e-04 | kPa | 425.26 | The des... |
| Psub | 7.84e-04 | kPa | 425.26 | The des... |
| Psub | 1.00e-03 | kPa | 427.36 | The des... |
| Psub | 9.84e-04 | kPa | 427.36 | The des... |
| Psub | 9.66e-04 | kPa | 427.36 | The des... |
| Psub | 9.83e-04 | kPa | 428.03 | Develop... |
| Psub | 1.03e-03 | kPa | 428.04 | Develop... |
| Psub | 1.08e-03 | kPa | 428.16 | Develop... |
| Psub | 1.17e-03 | kPa | 429.29 | The des... |
| Psub | 1.20e-03 | kPa | 429.29 | The des... |
| Psub | 1.20e-03 | kPa | 429.29 | The des... |
| Pvap | [5.47e-10; 0.19] | kPa | [298.15; 510.00] |
|
|
T(K) Vapor pressure (kPa) 0 0.05 0.1 0.15 0.2 300 400 500 | ||||
| Pvap | 5.47e-10 | kPa | 298.15 | Hypothe... |
| Pvap | 7.65e-10 | kPa | 300.00 | Hypothe... |
| Pvap | 4.30e-09 | kPa | 310.00 | Hypothe... |
| Pvap | 2.12e-08 | kPa | 320.00 | Hypothe... |
| Pvap | 9.25e-08 | kPa | 330.00 | Hypothe... |
| Pvap | 3.62e-07 | kPa | 340.00 | Hypothe... |
| Pvap | 1.28e-06 | kPa | 350.00 | Hypothe... |
| Pvap | 4.16e-06 | kPa | 360.00 | Hypothe... |
| Pvap | 1.24e-05 | kPa | 370.00 | Hypothe... |
| Pvap | 3.44e-05 | kPa | 380.00 | Hypothe... |
| Pvap | 8.89e-05 | kPa | 390.00 | Hypothe... |
| Pvap | 2.16e-04 | kPa | 400.00 | Hypothe... |
| Pvap | 4.94e-04 | kPa | 410.00 | Hypothe... |
| Pvap | 1.07e-03 | kPa | 420.00 | Hypothe... |
| Pvap | 2.22e-03 | kPa | 430.00 | Hypothe... |
| Pvap | 4.39e-03 | kPa | 440.00 | Hypothe... |
| Pvap | 8.31e-03 | kPa | 450.00 | Hypothe... |
| Pvap | 0.02 | kPa | 460.00 | Hypothe... |
| Pvap | 0.03 | kPa | 470.00 | Hypothe... |
| Pvap | 0.05 | kPa | 480.00 | Hypothe... |
| Pvap | 0.08 | kPa | 490.00 | Hypothe... |
| Pvap | 0.12 | kPa | 500.00 | Hypothe... |
| Pvap | 0.19 | kPa | 510.00 | Hypothe... |
| ΔfusS | 75.10 | J/mol×K | 446.00 | NIST |
Similar Compounds
Find more compounds similar to 1,1':3',1''-Terphenyl, 5'-phenyl-.
Sources
- Crippen Method
- Crippen Method
- The design, construction, and testing of a new Knudsen effusion apparatus
- New Knudsen effusion apparatus with simultaneous gravimetric and quartz crystal microbalance mass loss detection
- Reassembling and testing of a high-precision heat capacity drop calorimeter. Heat capacity of some polyphenyls at T = 298.15 K
- Development of the Knudsen effusion methodology for vapour pressure measurements of low volatile liquids and solids based on a quartz crystal microbalance
- Vapor Pressures and Vaporization Enthalpies of the n-Alkanes from C31 to C38 at T = 298.15 K by Correlation Gas Chromatography
- Hypothetical Thermodynamic Properties. Subcooled Vaporization Enthalpies and Vapor Pressures of Polyaromatic Hydrocarbons
- Joback Method
- McGowan Method
- NIST Webbook
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