- InChI
- InChI=1S/C19H16/c1-4-10-16(11-5-1)19(17-12-6-2-7-13-17)18-14-8-3-9-15-18/h1-15,19H
- InChI Key
- AAAQKTZKLRYKHR-UHFFFAOYSA-N
- Formula
- C19H16
- SMILES
- c1ccc(C(c2ccccc2)c2ccccc2)cc1
- Molecular Weight1
- 244.33
- CAS
- 519-73-3
- Other Names
-
- 1,1',1''-Methylidynetris[benzene]
- 1,1',1''-methylidynetrisbenzene
- Benzene,1,1',1"-methylidynetris-
- benzene, 1,1',1''-methylidynetris-
- methane, triphenyl-
- tritane
- 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).
- ΔfusH : Enthalpy of fusion at a given temperature (kJ/mol).
- ΔsubH° : Enthalpy of sublimation at standard conditions (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).
- 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°gas : 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).
- 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 |
|---|---|---|---|
| ΔfG° | 443.89 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | 276.10 ± 5.00 | kJ/mol | NIST |
| ΔfusH° | 23.57 | kJ/mol | Joback Calculated Property |
| ΔsubH° | [100.70; 112.00] | kJ/mol |
|
| ΔsubH° | 108.40 ± 2.80 | kJ/mol | NIST |
| ΔsubH° | 109.10 ± 0.60 | kJ/mol | NIST |
| ΔsubH° | 112.00 | kJ/mol | NIST |
| ΔsubH° | 100.70 | kJ/mol | NIST |
| ΔsubH° | 105.00 ± 0.80 | kJ/mol | NIST |
| ΔvapH° | [93.20; 95.00] | kJ/mol |
|
| ΔvapH° | 93.20 ± 2.20 | kJ/mol | NIST |
| ΔvapH° | 94.60 | kJ/mol | NIST |
| ΔvapH° | 95.00 | kJ/mol | NIST |
| IE | [8.34; 8.40] | eV |
|
| IE | 8.34 ± 0.03 | eV | NIST |
| IE | 8.34 ± 0.04 | eV | NIST |
| IE | 8.40 ± 0.05 | eV | NIST |
| log10WS | -5.25 | Crippen Calculated Property | |
| logPoct/wat | 4.867 | Crippen Calculated Property | |
| McVol | 207.290 | ml/mol | McGowan Calculated Property |
| Pc | 2400.57 | kPa | Joback Calculated Property |
| Inp | [327.80; 1997.00] |
|
|
| Inp | 1978.00 | NIST | |
| Inp | 1982.00 | NIST | |
| Inp | 1997.00 | NIST | |
| Inp | 327.80 | NIST | |
| Inp | 1982.00 | NIST | |
| Inp | 1997.00 | NIST | |
| Inp | 327.80 | NIST | |
| S°gas | 541.00 | J/mol×K | NIST |
| Tboil | [449.00; 632.00] | K |
|
| Tboil | 449.00 ± 2.00 | K | NIST |
| Tboil | 632.00 ± 1.00 | K | NIST |
| Tboil | 632.00 ± 6.00 | K | NIST |
| Tc | 982.16 | K | Joback Calculated Property |
| Tfus | [361.00; 367.80] | K |
|
| Tfus | 364.40 ± 3.00 | K | NIST |
| Tfus | 365.70 ± 3.00 | K | NIST |
| Tfus | 367.80 ± 3.00 | K | NIST |
| Tfus | 366.40 ± 1.00 | K | NIST |
| Tfus | 365.00 ± 6.00 | K | NIST |
| Tfus | Outlier 361.00 ± 6.00 | K | NIST |
| Tfus | Outlier 362.00 ± 7.00 | K | NIST |
| Tfus | 363.00 ± 4.00 | K | NIST |
| Tfus | 365.00 ± 4.00 | K | NIST |
| Tfus | 365.70 ± 1.50 | K | NIST |
| Tfus | 365.50 ± 1.00 | K | NIST |
| Tfus | 365.20 ± 1.00 | K | NIST |
| Tfus | 365.20 ± 0.50 | K | NIST |
| Tfus | 365.00 ± 3.00 | K | NIST |
| Tfus | 366.40 ± 1.50 | K | NIST |
| Tfus | 365.60 ± 0.20 | K | NIST |
| Tfus | 363.00 ± 2.00 | K | NIST |
| Tfus | 365.00 ± 4.00 | K | NIST |
| Tfus | 365.30 ± 0.20 | K | NIST |
| Tfus | 366.00 ± 2.00 | K | NIST |
| Tfus | 365.30 ± 1.00 | K | NIST |
| Tfus | 366.85 ± 0.30 | K | NIST |
| Tfus | 366.25 ± 0.20 | K | NIST |
| Tfus | 365.50 ± 0.60 | K | NIST |
| Tfus | 365.00 ± 0.10 | K | NIST |
| Tfus | 365.99 ± 0.50 | K | NIST |
| Vc | 0.769 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [550.53; 640.21] | J/mol×K | [713.72; 982.16] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 560 580 600 620 640 800 900 | ||||
| Cp,gas | 550.53 | J/mol×K | 713.72 | Joback Calculated Property |
| Cp,gas | 569.41 | J/mol×K | 758.46 | Joback Calculated Property |
| Cp,gas | 586.50 | J/mol×K | 803.20 | Joback Calculated Property |
| Cp,gas | 601.97 | J/mol×K | 847.94 | Joback Calculated Property |
| Cp,gas | 615.98 | J/mol×K | 892.68 | Joback Calculated Property |
| Cp,gas | 628.67 | J/mol×K | 937.42 | Joback Calculated Property |
| Cp,gas | 640.21 | J/mol×K | 982.16 | Joback Calculated Property |
| η | [0.0001036; 0.0019643] | Pa×s | [368.15; 713.72] |
|
|
T(K) Dynamic viscosity (Pa×s) 0 5.00e-4 1.00e-3 1.50e-3 2.00e-3 400 500 600 700 | ||||
| η | 0.0019643 | Pa×s | 368.15 | Joback Calculated Property |
| η | 0.0008632 | Pa×s | 425.75 | Joback Calculated Property |
| η | 0.0004615 | Pa×s | 483.34 | Joback Calculated Property |
| η | 0.0002819 | Pa×s | 540.94 | Joback Calculated Property |
| η | 0.0001893 | Pa×s | 598.53 | Joback Calculated Property |
| η | 0.0001364 | Pa×s | 656.12 | Joback Calculated Property |
| η | 0.0001036 | Pa×s | 713.72 | Joback Calculated Property |
| ΔfusH | [18.20; 21.98] | kJ/mol | [365.30; 367.20] |
|
|
T(K) Enthalpy of fusion at a given temperature (kJ/mol) 18 19 20 21 22 365.5 366 366.5 367 | ||||
| ΔfusH | 21.98 | kJ/mol | 365.30 | NIST |
| ΔfusH | 21.97 | kJ/mol | 365.30 | NIST |
| ΔfusH | 21.97 | kJ/mol | 365.30 | NIST |
| ΔfusH | 18.20 | kJ/mol | 365.50 | NIST |
| ΔfusH | 20.92 | kJ/mol | 365.60 | NIST |
| ΔfusH | 20.70 | kJ/mol | 367.20 | NIST |
| ΔsubH | [100.00; 113.90] | kJ/mol | [330.50; 367.00] |
|
|
T(K) Enthalpy of sublimation at a given temperature (kJ/mol) 100 102 104 106 108 110 112 114 330 340 350 360 | ||||
| ΔsubH | 106.80 | kJ/mol | 330.50 | NIST |
| ΔsubH | 100.00 ± 0.40 | kJ/mol | 337.00 | NIST |
| ΔsubH | 106.70 ± 0.60 | kJ/mol | 338.00 | NIST |
| ΔsubH | 113.90 | kJ/mol | 353.00 | NIST |
| ΔsubH | 100.10 ± 0.59 | kJ/mol | 367.00 | NIST |
| ΔvapH | [58.60; 82.00] | kJ/mol | [402.50; 577.50] |
|
| ΔvapH | 82.00 | kJ/mol | 402.50 | NIST |
| ΔvapH | 58.60 | kJ/mol | 577.50 | NIST |
| Pvap | [1.30e-07; 0.92] | kPa | [298.15; 510.00] |
|
|
T(K) Vapor pressure (kPa) 0 0.2 0.4 0.6 0.8 1 300 400 500 | ||||
| Pvap | 1.30e-07 | kPa | 298.15 | Hypothe... |
| Pvap | 1.69e-07 | kPa | 300.00 | Hypothe... |
| Pvap | 6.70e-07 | kPa | 310.00 | Hypothe... |
| Pvap | 2.39e-06 | kPa | 320.00 | Hypothe... |
| Pvap | 7.76e-06 | kPa | 330.00 | Hypothe... |
| Pvap | 2.31e-05 | kPa | 340.00 | Hypothe... |
| Pvap | 6.36e-05 | kPa | 350.00 | Hypothe... |
| Pvap | 1.63e-04 | kPa | 360.00 | Hypothe... |
| Pvap | 3.91e-04 | kPa | 370.00 | Hypothe... |
| Pvap | 8.85e-04 | kPa | 380.00 | Hypothe... |
| Pvap | 1.90e-03 | kPa | 390.00 | Hypothe... |
| Pvap | 3.87e-03 | kPa | 400.00 | Hypothe... |
| Pvap | 7.52e-03 | kPa | 410.00 | Hypothe... |
| Pvap | 0.01 | kPa | 420.00 | Hypothe... |
| Pvap | 0.03 | kPa | 430.00 | Hypothe... |
| Pvap | 0.04 | kPa | 440.00 | Hypothe... |
| Pvap | 0.07 | kPa | 450.00 | Hypothe... |
| Pvap | 0.12 | kPa | 460.00 | Hypothe... |
| Pvap | 0.19 | kPa | 470.00 | Hypothe... |
| Pvap | 0.29 | kPa | 480.00 | Hypothe... |
| Pvap | 0.44 | kPa | 490.00 | Hypothe... |
| Pvap | 0.64 | kPa | 500.00 | Hypothe... |
| Pvap | 0.92 | kPa | 510.00 | Hypothe... |
| ΔfusS | [49.80; 60.20] | J/mol×K | [365.30; 365.60] |
|
| ΔfusS | 60.20 | J/mol×K | 365.30 | NIST |
| ΔfusS | 49.80 | J/mol×K | 365.50 | NIST |
| ΔfusS | 57.20 | J/mol×K | 365.60 | NIST |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | 631.70 | K | 101.00 | NIST |
Similar Compounds
![9,10[1',2']-Benzenoanthracene, 9,10-dihydro-.](data:image/png;base64,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)
Find more compounds similar to Triphenylmethane.
Sources
- Crippen Method
- Crippen Method
- 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.
Outlier This icon means
that the value is more than 2 standard deviations away from the
property mean.