- InChI
- InChI=1S/C13H12/c1-3-7-12(8-4-1)11-13-9-5-2-6-10-13/h1-10H,11H2
- InChI Key
- CZZYITDELCSZES-UHFFFAOYSA-N
- Formula
- C13H12
- SMILES
- c1ccc(Cc2ccccc2)cc1
- Molecular Weight1
- 168.23
- CAS
- 101-81-5
- Other Names
-
- 1,1'-Dimethylenebis(benzene)
- ALPHA-PHENYLTOLUENE
- BENZYLBENZENE
- Benzene, (phenylmethyl)-
- Benzene, 1,1'-methylenebis-
- Benzene, benzyl-
- DITAN
- Ditane
- Methane, diphenyl-
- NSC 4708
- Toluene, «alpha»-phenyl-
- Toluene, «alpha»-phenyl-
- phenylmethylbenzene
- ω : Acentric Factor.
- PAff : Proton affinity (kJ/mol).
- BasG : Gas basicity (kJ/mol).
- ΔcH°liquid : Standard liquid enthalpy of combustion (kJ/mol).
- 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).
- μ : Dipole Moment (debye).
- 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°liquid : Liquid phase 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).
- 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).
- NFPA Fire : NFPA Fire Rating.
- NFPA Health : NFPA Health Rating.
- Pc : Critical Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- ρc : Critical density (kg/m3).
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- I : Polar retention indices.
- ΔfusS : Entropy of fusion at a given temperature (J/mol×K).
- S°gas : Molar entropy at standard conditions (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).
- Vc : Critical Volume (m3/kmol).
- Zc : Critical Compressibility.
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.4420 | KDB | |
| PAff | 802.00 | kJ/mol | NIST |
| BasG | 769.50 | kJ/mol | NIST |
| ΔcH°liquid | [-6927.20; -6919.60] | kJ/mol |
|
| ΔcH°liquid | -6927.20 ± 1.40 | kJ/mol | NIST |
| ΔcH°liquid | -6919.60 ± 1.30 | kJ/mol | NIST |
| ΔcH°solid | [-6945.00; -6673.00] | kJ/mol |
|
| ΔcH°solid | -6673.00 | kJ/mol | NIST |
| ΔcH°solid | -6931.20 | kJ/mol | NIST |
| ΔcH°solid | -6929.54 ± 0.84 | kJ/mol | NIST |
| ΔcH°solid | -6945.00 | kJ/mol | NIST |
| μ | 0.40 | debye | KDB |
| EA | 0.16 ± 0.04 | eV | NIST |
| ΔfG° | 283.40 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | [156.60; 165.00] | kJ/mol |
|
| ΔfH°gas | 165.00 ± 2.20 | kJ/mol | NIST |
| ΔfH°gas | 162.30 ± 2.30 | kJ/mol | NIST |
| ΔfH°gas | 164.80 ± 1.60 | kJ/mol | NIST |
| ΔfH°gas | 156.60 | kJ/mol | NIST |
| ΔfH°liquid | [88.91; 97.10] | kJ/mol |
|
| ΔfH°liquid | 97.10 ± 2.20 | kJ/mol | NIST |
| ΔfH°liquid | 97.10 ± 1.40 | kJ/mol | NIST |
| ΔfH°liquid | 88.91 | kJ/mol | NIST |
| ΔfH°solid | [75.10; 114.00] | kJ/mol |
|
| ΔfH°solid | 75.10 ± 2.20 | kJ/mol | NIST |
| ΔfH°solid | 114.00 | kJ/mol | NIST |
| ΔfusH° | 19.01 | kJ/mol | Thermod... |
| ΔsubH° | [87.20; 87.60] | kJ/mol |
|
| ΔsubH° | 87.20 ± 0.70 | kJ/mol | NIST |
| ΔsubH° | 87.60 ± 0.80 | kJ/mol | NIST |
| ΔvapH° | [50.12; 67.90] | kJ/mol |
|
| ΔvapH° | 67.90 ± 0.40 | kJ/mol | NIST |
| ΔvapH° | 64.70 ± 0.20 | kJ/mol | NIST |
| ΔvapH° | 67.60 ± 0.20 | kJ/mol | NIST |
| ΔvapH° | 65.70 | kJ/mol | NIST |
| ΔvapH° | 67.90 ± 0.50 | kJ/mol | NIST |
| ΔvapH° | 67.70 ± 0.60 | kJ/mol | NIST |
| ΔvapH° | 67.70 | kJ/mol | NIST |
| ΔvapH° | 67.50 ± 0.30 | kJ/mol | NIST |
| ΔvapH° | 66.60 ± 0.10 | kJ/mol | NIST |
| ΔvapH° | Outlier 50.12 | kJ/mol | NIST |
| IE | [8.55; 9.40] | eV |
|
| IE | Outlier 9.40 | eV | NIST |
| IE | 8.70 ± 0.10 | eV | NIST |
| IE | 8.55 ± 0.03 | eV | NIST |
| IE | 9.00 ± 0.05 | eV | NIST |
| IE | 8.67 ± 0.05 | eV | NIST |
| IE | 8.80 | eV | NIST |
| IE | 8.80 ± 0.02 | eV | NIST |
| IE | 9.10 | eV | NIST |
| log10WS | [-4.12; -4.08] |
|
|
| log10WS | -4.12 | Aq. Sol... | |
| log10WS | -4.08 | Estimat... | |
| logPoct/wat | 3.277 | Crippen Calculated Property | |
| McVol | 146.510 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 1 | KDB | |
| NFPA Health | 1 | KDB | |
| Pc | [2700.00; 5978.17] | kPa |
|
| Pc | 2710.00 | kPa | KDB |
| Pc | 2700.00 ± 300.00 | kPa | NIST |
| Pc | 2710.00 ± 300.00 | kPa | NIST |
| Pc | Outlier 5978.17 ± 303.98 | kPa | NIST |
| Pc | 2857.36 ± 101.32 | kPa | NIST |
| Pc | 2857.36 ± 101.32 | kPa | NIST |
| ρc | [299.46; 302.82] | kg/m3 |
|
| ρc | 302.82 ± 50.47 | kg/m3 | NIST |
| ρc | 299.46 ± 20.19 | kg/m3 | NIST |
| Inp | [241.60; 1461.00] |
|
|
| Inp | 1448.70 | NIST | |
| Inp | 1414.60 | NIST | |
| Inp | 1423.50 | NIST | |
| Inp | 1429.80 | NIST | |
| Inp | 1412.40 | NIST | |
| Inp | 1429.40 | NIST | |
| Inp | 1415.00 | NIST | |
| Inp | 1449.00 | NIST | |
| Inp | 1458.00 | NIST | |
| Inp | 1405.20 | NIST | |
| Inp | 1418.10 | NIST | |
| Inp | 1403.90 | NIST | |
| Inp | 1380.10 | NIST | |
| Inp | 1389.60 | NIST | |
| Inp | 1412.00 | NIST | |
| Inp | 1401.00 | NIST | |
| Inp | 1406.00 | NIST | |
| Inp | 1400.00 | NIST | |
| Inp | 1393.00 | NIST | |
| Inp | 1424.00 | NIST | |
| Inp | 1380.10 | NIST | |
| Inp | 1416.00 | NIST | |
| Inp | 1403.00 | NIST | |
| Inp | 1461.00 | NIST | |
| Inp | 247.00 | NIST | |
| Inp | 241.60 | NIST | |
| Inp | 249.09 | NIST | |
| Inp | 249.09 | NIST | |
| Inp | 245.77 | NIST | |
| Inp | 243.40 | NIST | |
| Inp | 245.60 | NIST | |
| Inp | 245.56 | NIST | |
| Inp | 243.35 | NIST | |
| Inp | 245.60 | NIST | |
| Inp | 1400.00 | NIST | |
| Inp | 245.60 | NIST | |
| Inp | 1448.70 | NIST | |
| Inp | 1429.40 | NIST | |
| Inp | 1424.00 | NIST | |
| Inp | 1405.20 | NIST | |
| Inp | 1412.00 | NIST | |
| Inp | 247.00 | NIST | |
| Inp | 243.40 | NIST | |
| I | [1980.00; 1994.00] |
|
|
| I | 1980.00 | NIST | |
| I | 1984.00 | NIST | |
| I | 1994.00 | NIST | |
| I | 1994.00 | NIST | |
| I | 1980.00 | NIST | |
| I | 1994.00 | NIST | |
| S°gas | 436.00 | J/mol×K | NIST |
| S°solid,1 bar | 239.30 | J/mol×K | NIST |
| Tboil | [529.00; 538.80] | K |
|
| Tboil | 538.20 | K | KDB |
| Tboil | 537.00 | K | NIST |
| Tboil | 537.50 | K | NIST |
| Tboil | 534.00 ± 3.00 | K | NIST |
| Tboil | 537.42 ± 0.20 | K | NIST |
| Tboil | 536.00 ± 0.50 | K | NIST |
| Tboil | 537.42 ± 0.30 | K | NIST |
| Tboil | 536.00 ± 3.00 | K | NIST |
| Tboil | 537.00 ± 3.00 | K | NIST |
| Tboil | 535.00 ± 2.00 | K | NIST |
| Tboil | 535.65 ± 4.00 | K | NIST |
| Tboil | 534.00 ± 1.00 | K | NIST |
| Tboil | 534.00 ± 2.00 | K | NIST |
| Tboil | 532.00 ± 3.00 | K | NIST |
| Tboil | 533.00 ± 3.00 | K | NIST |
| Tboil | 534.00 ± 3.00 | K | NIST |
| Tboil | 534.65 ± 1.50 | K | NIST |
| Tboil | 537.00 ± 3.00 | K | NIST |
| Tboil | 538.00 ± 3.00 | K | NIST |
| Tboil | Outlier 529.00 ± 4.00 | K | NIST |
| Tboil | Outlier 529.00 ± 5.00 | K | NIST |
| Tboil | 538.80 ± 1.50 | K | NIST |
| Tboil | 533.00 ± 3.00 | K | NIST |
| Tboil | 534.00 ± 3.00 | K | NIST |
| Tboil | 533.00 ± 4.00 | K | NIST |
| Tboil | 534.00 ± 2.50 | K | NIST |
| Tboil | 532.00 ± 3.00 | K | NIST |
| Tboil | 534.00 ± 3.00 | K | NIST |
| Tboil | 533.00 ± 3.00 | K | NIST |
| Tboil | 534.70 ± 2.00 | K | NIST |
| Tboil | 536.00 ± 3.00 | K | NIST |
| Tboil | 538.00 ± 3.00 | K | NIST |
| Tboil | 534.00 ± 3.00 | K | NIST |
| Tboil | 538.00 ± 3.00 | K | NIST |
| Tboil | 534.00 ± 3.00 | K | NIST |
| Tboil | 534.15 ± 3.00 | K | NIST |
| Tboil | 535.00 ± 3.00 | K | NIST |
| Tboil | 535.00 ± 3.00 | K | NIST |
| Tboil | 532.00 ± 3.00 | K | NIST |
| Tboil | 535.00 ± 3.00 | K | NIST |
| Tboil | 532.00 ± 3.00 | K | NIST |
| Tboil | 533.00 ± 5.00 | K | NIST |
| Tboil | 534.00 ± 4.00 | K | NIST |
| Tboil | 536.00 ± 4.00 | K | NIST |
| Tboil | 534.00 ± 3.00 | K | NIST |
| Tboil | 536.00 ± 6.00 | K | NIST |
| Tboil | 537.85 ± 1.00 | K | NIST |
| Tboil | 533.00 ± 4.00 | K | NIST |
| Tboil | 533.00 ± 4.00 | K | NIST |
| Tboil | 534.00 ± 5.00 | K | NIST |
| Tboil | 536.00 ± 4.00 | K | NIST |
| Tboil | 535.00 ± 5.00 | K | NIST |
| Tc | [760.00; 845.65] | K |
|
| Tc | 760.00 | K | KDB |
| Tc | 760.00 ± 8.00 | K | NIST |
| Tc | 760.00 ± 8.00 | K | NIST |
| Tc | 767.00 ± 10.00 | K | NIST |
| Tc | 760.00 ± 8.00 | K | NIST |
| Tc | Outlier 845.65 ± 3.00 | K | NIST |
| Tc | 770.15 ± 2.00 | K | NIST |
| Tc | 770.20 ± 10.00 | K | NIST |
| Tfus | [25.20; 571.40] | K |
|
| Tfus | 298.39 | K | KDB |
| Tfus | 314.32 | K | Aq. Sol... |
| Tfus | Outlier 571.40 ± 0.30 | K | NIST |
| Tfus | 298.21 ± 0.15 | K | NIST |
| Tfus | 298.17 ± 0.10 | K | NIST |
| Tfus | 300.20 ± 0.70 | K | NIST |
| Tfus | 298.20 ± 1.00 | K | NIST |
| Tfus | 298.35 ± 0.15 | K | NIST |
| Tfus | 298.80 ± 3.00 | K | NIST |
| Tfus | 299.20 ± 3.00 | K | NIST |
| Tfus | 299.65 ± 0.50 | K | NIST |
| Tfus | 298.30 ± 0.30 | K | NIST |
| Tfus | Outlier 25.20 ± 0.20 | K | NIST |
| Tfus | 299.00 ± 2.00 | K | NIST |
| Tfus | 299.80 ± 0.50 | K | NIST |
| Tfus | 298.25 ± 0.30 | K | NIST |
| Tfus | 298.00 ± 3.00 | K | NIST |
| Tfus | 300.15 ± 2.00 | K | NIST |
| Tfus | 298.40 ± 3.00 | K | NIST |
| Tfus | 301.00 ± 3.00 | K | NIST |
| Tfus | 298.00 ± 0.70 | K | NIST |
| Tfus | 299.00 ± 2.00 | K | NIST |
| Tfus | 298.24 ± 0.02 | K | NIST |
| Tfus | 297.70 ± 2.00 | K | NIST |
| Tfus | 299.00 ± 2.00 | K | NIST |
| Tfus | 299.00 ± 2.00 | K | NIST |
| Tfus | 299.00 ± 3.00 | K | NIST |
| Tfus | 299.00 ± 3.00 | K | NIST |
| Tfus | 298.70 ± 0.20 | K | NIST |
| Tfus | 299.00 ± 2.00 | K | NIST |
| Tfus | 300.00 ± 2.00 | K | NIST |
| Tfus | 298.00 ± 1.00 | K | NIST |
| Tfus | 298.40 ± 0.50 | K | NIST |
| Tfus | 298.20 ± 0.50 | K | NIST |
| Tfus | 298.30 ± 0.30 | K | NIST |
| Tfus | 297.00 ± 3.00 | K | NIST |
| Tfus | 297.70 ± 3.00 | K | NIST |
| Tfus | 300.00 ± 2.00 | K | NIST |
| Tfus | 298.40 ± 0.10 | K | NIST |
| Tfus | 299.70 ± 2.00 | K | NIST |
| Tfus | 300.15 ± 1.00 | K | NIST |
| Tfus | 297.00 ± 3.00 | K | NIST |
| Tfus | 297.00 ± 3.00 | K | NIST |
| Tfus | 298.00 ± 3.00 | K | NIST |
| Tfus | 298.70 ± 1.00 | K | NIST |
| Tfus | 299.00 ± 2.00 | K | NIST |
| Tfus | 297.70 ± 3.00 | K | NIST |
| Tfus | 298.70 ± 2.00 | K | NIST |
| Tfus | 298.70 ± 3.00 | K | NIST |
| Tfus | 299.00 ± 2.00 | K | NIST |
| Tfus | 297.40 ± 3.00 | K | NIST |
| Tfus | 297.00 ± 3.00 | K | NIST |
| Tfus | 299.30 ± 2.00 | K | NIST |
| Tfus | 299.70 ± 3.00 | K | NIST |
| Tfus | 297.10 ± 3.00 | K | NIST |
| Tfus | 297.00 ± 3.00 | K | NIST |
| Tfus | 297.00 ± 3.00 | K | NIST |
| Tfus | 299.00 ± 3.00 | K | NIST |
| Tfus | 299.00 ± 3.00 | K | NIST |
| Tfus | 300.00 ± 2.00 | K | NIST |
| Tfus | 300.00 ± 2.00 | K | NIST |
| Tfus | 298.70 ± 2.00 | K | NIST |
| Tfus | 300.00 ± 2.00 | K | NIST |
| Tfus | 299.30 ± 1.00 | K | NIST |
| Tfus | 300.19 ± 0.50 | K | NIST |
| Tfus | 300.00 ± 1.50 | K | NIST |
| Tfus | 299.15 ± 1.00 | K | NIST |
| Tfus | 299.00 ± 2.00 | K | NIST |
| Tfus | 300.00 ± 2.00 | K | NIST |
| Tfus | 299.00 ± 2.00 | K | NIST |
| Tfus | 299.40 ± 2.00 | K | NIST |
| Tfus | 299.00 ± 2.00 | K | NIST |
| Tfus | 299.50 ± 1.00 | K | NIST |
| Tfus | 299.70 ± 1.50 | K | NIST |
| Tfus | 297.60 ± 1.00 | K | NIST |
| Tfus | 299.60 ± 1.00 | K | NIST |
| Tfus | 298.80 ± 1.50 | K | NIST |
| Tfus | 299.50 ± 1.50 | K | NIST |
| Tfus | 299.80 ± 1.50 | K | NIST |
| Tfus | 298.00 ± 3.00 | K | NIST |
| Tfus | 299.00 ± 3.00 | K | NIST |
| Tfus | 299.00 ± 3.00 | K | NIST |
| Tfus | 299.00 ± 3.00 | K | NIST |
| Tfus | 297.70 ± 3.00 | K | NIST |
| Tfus | 299.70 ± 3.00 | K | NIST |
| Tfus | 298.00 ± 2.00 | K | NIST |
| Tfus | 299.60 ± 2.00 | K | NIST |
| Vc | [0.563; 0.563] | m3/kmol |
|
| Vc | 0.563 | m3/kmol | KDB |
| Vc | 0.563 | m3/kmol | NIST |
| Zc | 0.2414500 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [324.65; 408.98] | J/mol×K | [550.20; 794.86] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 320 340 360 380 400 600 700 800 | ||||
| Cp,gas | 324.65 | J/mol×K | 550.20 | Joback Calculated Property |
| Cp,gas | 341.78 | J/mol×K | 590.98 | Joback Calculated Property |
| Cp,gas | 357.57 | J/mol×K | 631.75 | Joback Calculated Property |
| Cp,gas | 372.11 | J/mol×K | 672.53 | Joback Calculated Property |
| Cp,gas | 385.47 | J/mol×K | 713.31 | Joback Calculated Property |
| Cp,gas | 397.73 | J/mol×K | 754.08 | Joback Calculated Property |
| Cp,gas | 408.98 | J/mol×K | 794.86 | Joback Calculated Property |
| Cp,solid | [223.80; 279.90] | J/mol×K | [282.50; 303.00] |
|
| Cp,solid | 223.80 | J/mol×K | 282.50 | NIST |
| Cp,solid | 233.50 | J/mol×K | 298.50 | NIST |
| Cp,solid | 279.90 | J/mol×K | 300.00 | NIST |
| Cp,solid | 266.10 | J/mol×K | 303.00 | NIST |
| η | [0.0001914; 0.0026514] | Pa×s | [289.11; 550.20] |
|
|
T(K) Dynamic viscosity (Pa×s) 0 5.00e-4 1.00e-3 1.50e-3 2.00e-3 2.50e-3 300 400 500 | ||||
| η | 0.0026514 | Pa×s | 289.11 | Joback Calculated Property |
| η | 0.0012846 | Pa×s | 332.62 | Joback Calculated Property |
| η | 0.0007360 | Pa×s | 376.14 | Joback Calculated Property |
| η | 0.0004733 | Pa×s | 419.66 | Joback Calculated Property |
| η | 0.0003307 | Pa×s | 463.17 | Joback Calculated Property |
| η | 0.0002458 | Pa×s | 506.69 | Joback Calculated Property |
| η | 0.0001914 | Pa×s | 550.20 | Joback Calculated Property |
| ΔfusH | [18.57; 19.05] | kJ/mol | [298.30; 299.40] |
|
|
T(K) Enthalpy of fusion at a given temperature (kJ/mol) 18.6 18.7 18.8 18.9 19 298.5 299 | ||||
| ΔfusH | 18.58 | kJ/mol | 298.30 | NIST |
| ΔfusH | 18.58 | kJ/mol | 298.30 | NIST |
| ΔfusH | 18.57 | kJ/mol | 298.30 | NIST |
| ΔfusH | 19.01 | kJ/mol | 298.40 | NIST |
| ΔfusH | 19.05 | kJ/mol | 299.40 | NIST |
| ΔsubH | [64.00; 88.50] | kJ/mol | [284.00; 299.80] |
|
|
T(K) Enthalpy of sublimation at a given temperature (kJ/mol) 65 70 75 80 85 90 285 290 295 300 | ||||
| ΔsubH | 88.50 ± 0.80 | kJ/mol | 284.00 | NIST |
| ΔsubH | 71.50 | kJ/mol | 285.50 | NIST |
| ΔsubH | 83.30 ± 3.30 | kJ/mol | 285.50 | NIST |
| ΔsubH | 64.00 | kJ/mol | 288.50 | NIST |
| ΔsubH | 72.00 ± 0.80 | kJ/mol | 297.00 | NIST |
| ΔsubH | 72.00 ± 0.80 | kJ/mol | 297.00 | NIST |
| ΔsubH | 82.47 ± 0.63 | kJ/mol | 299.80 | NIST |
| ΔvapH | [48.90; 72.20] | kJ/mol | [323.00; 535.00] |
|
|
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 50 55 60 65 70 350 400 450 500 | ||||
| ΔvapH | 66.40 ± 0.50 | kJ/mol | 323.00 | NIST |
| ΔvapH | 72.20 | kJ/mol | 339.00 | NIST |
| ΔvapH | 63.70 | kJ/mol | 352.50 | NIST |
| ΔvapH | 61.80 | kJ/mol | 393.00 | NIST |
| ΔvapH | 55.80 | kJ/mol | 445.00 | NIST |
| ΔvapH | 64.10 ± 0.10 | kJ/mol | 459.00 | NIST |
| ΔvapH | 48.90 ± 0.30 | kJ/mol | 459.00 | NIST |
| ΔvapH | 52.00 ± 0.20 | kJ/mol | 459.00 | NIST |
| ΔvapH | 55.00 ± 0.10 | kJ/mol | 459.00 | NIST |
| ΔvapH | 57.90 ± 0.10 | kJ/mol | 459.00 | NIST |
| ΔvapH | 61.00 ± 0.10 | kJ/mol | 459.00 | NIST |
| ΔvapH | 56.70 | kJ/mol | 503.00 | NIST |
| ΔvapH | 54.20 | kJ/mol | 522.50 | NIST |
| ΔvapH | 49.00 | kJ/mol | 535.00 | NIST |
| Pvap | [2.02e-03; 520.00] | kPa | [298.15; 623.10] |
|
|
T(K) Vapor pressure (kPa) 0 100 200 300 400 500 300 400 500 600 | ||||
| Pvap | 2.02e-03 | kPa | 298.15 | Hypothe... |
| Pvap | 2.39e-03 | kPa | 300.00 | Hypothe... |
| Pvap | 5.64e-03 | kPa | 310.00 | Hypothe... |
| Pvap | 0.01 | kPa | 320.00 | Hypothe... |
| Pvap | 0.03 | kPa | 330.00 | Hypothe... |
| Pvap | 0.05 | kPa | 340.00 | Hypothe... |
| Pvap | 0.10 | kPa | 350.00 | Hypothe... |
| Pvap | 0.18 | kPa | 360.00 | Hypothe... |
| Pvap | 0.31 | kPa | 370.00 | Hypothe... |
| Pvap | 0.53 | kPa | 380.00 | Hypothe... |
| Pvap | 0.86 | kPa | 390.00 | Hypothe... |
| Pvap | 1.35 | kPa | 400.00 | Hypothe... |
| Pvap | 2.08 | kPa | 410.00 | Hypothe... |
| Pvap | 3.11 | kPa | 420.00 | Hypothe... |
| Pvap | 4.55 | kPa | 430.00 | Hypothe... |
| Pvap | 6.50 | kPa | 440.00 | Hypothe... |
| Pvap | 9.12 | kPa | 450.00 | Hypothe... |
| Pvap | 12.56 | kPa | 460.00 | Hypothe... |
| Pvap | 17.00 | kPa | 470.00 | Hypothe... |
| Pvap | 22.63 | kPa | 480.00 | Hypothe... |
| Pvap | 29.69 | kPa | 490.00 | Hypothe... |
| Pvap | 38.42 | kPa | 500.00 | Hypothe... |
| Pvap | 49.08 | kPa | 510.00 | Hypothe... |
| Pvap | 210.00 | kPa | 573.10 | A novel... |
| Pvap | 200.00 | kPa | 573.10 | A novel... |
| Pvap | 210.00 | kPa | 573.10 | A novel... |
| Pvap | 340.00 | kPa | 598.00 | A novel... |
| Pvap | 330.00 | kPa | 598.00 | A novel... |
| Pvap | 330.00 | kPa | 598.00 | A novel... |
| Pvap | 510.00 | kPa | 623.00 | A novel... |
| Pvap | 510.00 | kPa | 623.10 | A novel... |
| Pvap | 520.00 | kPa | 623.10 | A novel... |
| ρl | 1006.00 | kg/m3 | 293.00 | KDB |
| ΔfusS | [62.25; 62.34] | J/mol×K | [298.30; 298.30] |
|
| ΔfusS | 62.34 | J/mol×K | 298.30 | NIST |
| ΔfusS | 62.25 | J/mol×K | 298.30 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.64] | kPa | [398.83; 568.23] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.48830e+01 | |||
| Coefficient B | -4.71056e+03 | |||
| Coefficient C | -7.60920e+01 | |||
| Temperature range, min. | 398.83 | |||
| Temperature range, max. | 568.23 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 400 450 500 550 | ||||
| Pvap | 1.33 | kPa | 398.83 | Calculated Property |
| Pvap | 2.98 | kPa | 417.65 | Calculated Property |
| Pvap | 6.12 | kPa | 436.47 | Calculated Property |
| Pvap | 11.71 | kPa | 455.30 | Calculated Property |
| Pvap | 21.08 | kPa | 474.12 | Calculated Property |
| Pvap | 35.97 | kPa | 492.94 | Calculated Property |
| Pvap | 58.61 | kPa | 511.76 | Calculated Property |
| Pvap | 91.71 | kPa | 530.59 | Calculated Property |
| Pvap | 138.49 | kPa | 549.41 | Calculated Property |
| Pvap | 202.64 | kPa | 568.23 | Calculated Property |
| Pvap | [1.99e-03; 2930.49] | kPa | [298.39; 768.00] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 1.11780e+02 | |||
| Coefficient B | -1.19847e+04 | |||
| Coefficient C | -1.37414e+01 | |||
| Coefficient D | 5.26072e-06 | |||
| Temperature range, min. | 298.39 | |||
| Temperature range, max. | 768.00 | |||
|
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 400 600 | ||||
| Pvap | 1.99e-03 | kPa | 298.39 | Calculated Property |
| Pvap | 0.10 | kPa | 350.57 | Calculated Property |
| Pvap | 1.57 | kPa | 402.75 | Calculated Property |
| Pvap | 11.31 | kPa | 454.93 | Calculated Property |
| Pvap | 49.80 | kPa | 507.11 | Calculated Property |
| Pvap | 157.57 | kPa | 559.28 | Calculated Property |
| Pvap | 397.08 | kPa | 611.46 | Calculated Property |
| Pvap | 854.01 | kPa | 663.64 | Calculated Property |
| Pvap | 1644.09 | kPa | 715.82 | Calculated Property |
| Pvap | 2930.49 | kPa | 768.00 | Calculated Property |
Similar Compounds
![Benzene, 1-methyl-3-[(4-methylphenyl)methyl]-.](data:image/png;base64,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)
![Bicyclo[4.1.0]hepta-1,3,5-triene.](data:image/png;base64,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)
Find more compounds similar to Diphenylmethane.
Mixtures
Sources
- KDB Vapor Pressure Data
- Crippen Method
- A novel continuous flow apparatus with a video camera system for high pressure phase equilibrium measurements
- Thermodynamic Properties of Diphenylmethane
- Hypothetical Thermodynamic Properties. Subcooled Vaporization Enthalpies and Vapor Pressures of Polyaromatic Hydrocarbons
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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.
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Outlier This icon means
that the value is more than 2 standard deviations away from the
property mean.