- 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.
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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] |
|
| 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] |
|
| 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] |
|
| 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] |
|
| 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] |
|
| 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
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Outlier This icon means
that the value is more than 2 standard deviations away from the
property mean.