- InChI
- InChI=1S/C12H10/c1-3-7-11(8-4-1)12-9-5-2-6-10-12/h1-10H
- InChI Key
- ZUOUZKKEUPVFJK-UHFFFAOYSA-N
- Formula
- C12H10
- SMILES
- c1ccc(-c2ccccc2)cc1
- Molecular Weight1
- 154.21
- CAS
- 92-52-4
- Other Names
-
- 1,1'-Biphenyl
- 1,1'-Diphenyl
- 1,1-Biphenyl
- Bibenzene
- Carolid AL
- Diphenyl
- Lemonene
- NSC 14916
- PhPh
- Phenador-X
- Phenylbenzene
- Tetrosin LY
- Xenene
- ω : Acentric Factor.
- PAff : Proton affinity (kJ/mol).
- BasG : Gas basicity (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,liquid : Liquid phase 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 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).
- γ : Surface Tension (N/m).
- S°solid,1 bar : Solid phase molar entropy at standard conditions (J/mol×K).
- ΔsubS : Entropy of sublimation at a given temperature (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).
- vspec : Specific Volume (m3/kg).
- Zc : Critical Compressibility.
- Zra : Rackett Parameter.
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.3720 | KDB | |
| PAff | [808.80; 813.60] | kJ/mol |
|
| PAff | 813.60 | kJ/mol | NIST |
| PAff | 808.80 | kJ/mol | NIST |
| BasG | [780.70; 782.90] | kJ/mol |
|
| BasG | 782.90 | kJ/mol | NIST |
| BasG | 780.70 | kJ/mol | NIST |
| EA | 0.13 ± 0.04 | eV | NIST |
| ΔfG° | 280.30 | kJ/mol | KDB |
| ΔfH°gas | 182.20 | kJ/mol | KDB |
| ΔfH°solid | [96.70; 100.50] | kJ/mol |
|
| ΔfH°solid | 98.20 ± 2.50 | kJ/mol | NIST |
| ΔfH°solid | 96.70 ± 2.60 | kJ/mol | NIST |
| ΔfH°solid | 100.50 ± 1.50 | kJ/mol | NIST |
| ΔfH°solid | 96.80 ± 4.00 | kJ/mol | NIST |
| ΔfH°solid | 97.20 ± 1.60 | kJ/mol | NIST |
| ΔfusH° | 19.30 | kJ/mol | Synthesis and characterization of novel binary organic monotectic and eutectic alloys |
| ΔvapH° | 67.63 | kJ/mol | Relay (1.0) Calculated Property |
| IE | [7.95; 8.90] | eV |
|
| IE | 8.16 ± 0.13 | eV | NIST |
| IE | 8.80 ± 0.05 | eV | NIST |
| IE | Outlier 8.90 | eV | NIST |
| IE | 7.95 ± 0.02 | eV | NIST |
| IE | 8.23 ± 0.01 | eV | NIST |
| IE | 8.20 ± 0.05 | eV | NIST |
| IE | 8.46 | eV | NIST |
| IE | 8.22 ± 0.15 | eV | NIST |
| IE | 8.27 ± 0.01 | eV | NIST |
| IE | 8.64 | eV | NIST |
| IE | 8.35 | eV | NIST |
| IE | 8.40 | eV | NIST |
| IE | 8.39 | eV | NIST |
| IE | 8.34 | eV | NIST |
| log10WS | [-4.38; -4.34] |
|
|
| log10WS | -4.38 | Aq. Solubility Prediction | |
| log10WS | -4.34 | Estimated Solubility | |
| logPoct/wat | 3.354 | Crippen Calculated Property | |
| McVol | 132.420 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 1 | KDB | |
| NFPA Health | 2 | KDB | |
| Pc | [3120.00; 4084.00] | kPa |
|
| Pc | 3380.00 | kPa | KDB |
| Pc | 3400.00 ± 100.00 | kPa | NIST |
| Pc | 3346.00 ± 103.42 | kPa | NIST |
| Pc | 3500.00 ± 101.33 | kPa | NIST |
| Pc | 3800.00 ± 689.50 | kPa | NIST |
| Pc | 3120.00 ± 202.65 | kPa | NIST |
| Pc | Outlier 4084.00 ± 137.89 | kPa | NIST |
| Pc | 3218.08 ± 81.06 | kPa | NIST |
| Pc | 3226.19 ± 81.06 | kPa | NIST |
| ρc | [306.87; 322.29] | kg/m3 |
|
| ρc | 308.42 ± 15.42 | kg/m3 | NIST |
| ρc | 309.96 ± 10.02 | kg/m3 | NIST |
| ρc | 322.29 ± 10.02 | kg/m3 | NIST |
| ρc | 306.87 ± 14.96 | kg/m3 | NIST |
| Inp | [229.21; 1408.00] |
|
|
| Inp | 1369.00 | NIST | |
| Inp | 1369.00 | NIST | |
| Inp | 1370.00 | NIST | |
| Inp | 1378.00 | NIST | |
| Inp | 1353.00 | NIST | |
| Inp | 1340.00 | NIST | |
| Inp | 1340.00 | NIST | |
| Inp | 1382.00 | NIST | |
| Inp | 1351.00 | NIST | |
| Inp | 1351.00 | NIST | |
| Inp | 1351.00 | NIST | |
| Inp | 1352.00 | NIST | |
| Inp | 1352.00 | NIST | |
| Inp | 1352.00 | NIST | |
| Inp | 1352.00 | NIST | |
| Inp | 1352.00 | NIST | |
| Inp | 1352.00 | NIST | |
| Inp | 1352.00 | NIST | |
| Inp | 1354.00 | NIST | |
| Inp | 1387.00 | NIST | |
| Inp | 1359.00 | NIST | |
| Inp | 1366.30 | NIST | |
| Inp | 1377.90 | NIST | |
| Inp | 1396.00 | NIST | |
| Inp | 1373.00 | NIST | |
| Inp | 1405.00 | NIST | |
| Inp | 1398.70 | NIST | |
| Inp | 1354.00 | NIST | |
| Inp | 1380.00 | NIST | |
| Inp | 1399.00 | NIST | |
| Inp | 1354.00 | NIST | |
| Inp | 1345.00 | NIST | |
| Inp | 1346.00 | NIST | |
| Inp | 1349.00 | NIST | |
| Inp | 1350.00 | NIST | |
| Inp | 1389.00 | NIST | |
| Inp | 1377.30 | NIST | |
| Inp | 1375.40 | NIST | |
| Inp | 1368.50 | NIST | |
| Inp | 1377.30 | NIST | |
| Inp | 1381.80 | NIST | |
| Inp | 1338.40 | NIST | |
| Inp | 1392.20 | NIST | |
| Inp | 1387.00 | NIST | |
| Inp | 1368.50 | NIST | |
| Inp | 1377.30 | NIST | |
| Inp | 1381.80 | NIST | |
| Inp | 1375.40 | NIST | |
| Inp | 1381.00 | NIST | |
| Inp | 1375.78 | NIST | |
| Inp | 1377.20 | NIST | |
| Inp | 1377.91 | NIST | |
| Inp | 1396.81 | NIST | |
| Inp | 1392.00 | NIST | |
| Inp | 1392.64 | NIST | |
| Inp | 1390.72 | NIST | |
| Inp | 1384.00 | NIST | |
| Inp | 1374.00 | NIST | |
| Inp | 1378.00 | NIST | |
| Inp | 1349.00 | NIST | |
| Inp | 1350.00 | NIST | |
| Inp | 1364.00 | NIST | |
| Inp | 1373.00 | NIST | |
| Inp | 1362.00 | NIST | |
| Inp | 1397.00 | NIST | |
| Inp | 1371.00 | NIST | |
| Inp | 1375.00 | NIST | |
| Inp | 1366.00 | NIST | |
| Inp | 1360.00 | NIST | |
| Inp | 1360.00 | NIST | |
| Inp | 1408.00 | NIST | |
| Inp | 1368.00 | NIST | |
| Inp | 1396.00 | NIST | |
| Inp | 1384.00 | NIST | |
| Inp | 1385.30 | NIST | |
| Inp | 1379.00 | NIST | |
| Inp | 1388.00 | NIST | |
| Inp | 1380.00 | NIST | |
| Inp | 1380.00 | NIST | |
| Inp | 1381.00 | NIST | |
| Inp | 1381.00 | NIST | |
| Inp | 1381.00 | NIST | |
| Inp | 1382.00 | NIST | |
| Inp | 1385.00 | NIST | |
| Inp | 1385.00 | NIST | |
| Inp | 1354.00 | NIST | |
| Inp | 1356.00 | NIST | |
| Inp | 1356.00 | NIST | |
| Inp | 1342.00 | NIST | |
| Inp | 1358.00 | NIST | |
| Inp | 1366.00 | NIST | |
| Inp | 1345.00 | NIST | |
| Inp | 1380.00 | NIST | |
| Inp | 1391.00 | NIST | |
| Inp | 1385.00 | NIST | |
| Inp | 1394.00 | NIST | |
| Inp | 1369.00 | NIST | |
| Inp | 1375.00 | NIST | |
| Inp | 1356.00 | NIST | |
| Inp | 1384.00 | NIST | |
| Inp | 1384.00 | NIST | |
| Inp | 1368.00 | NIST | |
| Inp | 1369.00 | NIST | |
| Inp | 1362.00 | NIST | |
| Inp | 1362.00 | NIST | |
| Inp | 1348.00 | NIST | |
| Inp | 1342.00 | NIST | |
| Inp | 1343.00 | NIST | |
| Inp | 1349.00 | NIST | |
| Inp | 1350.00 | NIST | |
| Inp | 1389.00 | NIST | |
| Inp | 1389.00 | NIST | |
| Inp | 245.80 | NIST | |
| Inp | 237.70 | NIST | |
| Inp | 236.39 | NIST | |
| Inp | 236.39 | NIST | |
| Inp | 236.34 | NIST | |
| Inp | 235.88 | NIST | |
| Inp | 236.15 | NIST | |
| Inp | 236.19 | NIST | |
| Inp | 236.26 | NIST | |
| Inp | 236.32 | NIST | |
| Inp | 236.87 | NIST | |
| Inp | 236.92 | NIST | |
| Inp | 237.02 | NIST | |
| Inp | 237.04 | NIST | |
| Inp | 236.28 | NIST | |
| Inp | 236.48 | NIST | |
| Inp | 231.10 | NIST | |
| Inp | 235.60 | NIST | |
| Inp | 233.57 | NIST | |
| Inp | 234.13 | NIST | |
| Inp | 235.55 | NIST | |
| Inp | 233.78 | NIST | |
| Inp | 233.46 | NIST | |
| Inp | 236.40 | NIST | |
| Inp | 236.20 | NIST | |
| Inp | 236.00 | NIST | |
| Inp | 235.63 | NIST | |
| Inp | 232.74 | NIST | |
| Inp | 236.39 | NIST | |
| Inp | 233.96 | NIST | |
| Inp | 236.59 | NIST | |
| Inp | 234.05 | NIST | |
| Inp | 230.79 | NIST | |
| Inp | 229.80 | NIST | |
| Inp | 236.44 | NIST | |
| Inp | 233.96 | NIST | |
| Inp | 236.60 | NIST | |
| Inp | 236.56 | NIST | |
| Inp | 236.39 | NIST | |
| Inp | 236.56 | NIST | |
| Inp | 235.50 | NIST | |
| Inp | 240.35 | NIST | |
| Inp | 229.33 | NIST | |
| Inp | 235.00 | NIST | |
| Inp | 235.00 | NIST | |
| Inp | 229.21 | NIST | |
| Inp | 235.74 | NIST | |
| Inp | 233.96 | NIST | |
| Inp | 233.96 | NIST | |
| Inp | 235.51 | NIST | |
| Inp | 237.30 | NIST | |
| Inp | 235.60 | NIST | |
| Inp | 236.40 | NIST | |
| Inp | 232.86 | NIST | |
| Inp | 232.96 | NIST | |
| Inp | 236.20 | NIST | |
| Inp | 233.96 | NIST | |
| Inp | 245.80 | NIST | |
| Inp | 235.88 | NIST | |
| Inp | 236.87 | NIST | |
| Inp | 236.48 | NIST | |
| Inp | 235.55 | NIST | |
| Inp | 236.00 | NIST | |
| Inp | 236.59 | NIST | |
| Inp | 233.96 | NIST | |
| I | [228.73; 2030.00] |
|
|
| I | 2029.00 | NIST | |
| I | 1996.00 | NIST | |
| I | 2016.00 | NIST | |
| I | 1996.00 | NIST | |
| I | 2030.00 | NIST | |
| I | 1981.00 | NIST | |
| I | 1967.00 | NIST | |
| I | 2012.00 | NIST | |
| I | 1981.00 | NIST | |
| I | 1974.00 | NIST | |
| I | 1974.00 | NIST | |
| I | 1981.00 | NIST | |
| I | Outlier 228.73 | NIST | |
| I | 2029.00 | NIST | |
| I | 2012.00 | NIST | |
| S°solid,1 bar | [205.90; 209.38] | J/mol×K |
|
| S°solid,1 bar | 209.38 | J/mol×K | NIST |
| S°solid,1 bar | 209.00 | J/mol×K | NIST |
| S°solid,1 bar | 205.90 | J/mol×K | NIST |
| Tboil | 529.20 | K | KDB |
| Tc | [768.75; 800.00] | K |
|
| Tc | 773.00 | K | KDB |
| Tc | 773.00 ± 3.00 | K | NIST |
| Tc | 773.00 ± 3.00 | K | NIST |
| Tc | 777.00 ± 6.00 | K | NIST |
| Tc | 789.00 ± 5.60 | K | NIST |
| Tc | 769.00 ± 3.00 | K | NIST |
| Tc | Outlier 800.00 ± 11.11 | K | NIST |
| Tc | 768.75 ± 2.00 | K | NIST |
| Tfus | [341.10; 342.84] | K |
|
| Tfus | 342.84 | K | Aq. Solubility Prediction |
| Tfus | 342.00 | K | KDB |
| Tfus | 341.10 | K | Solid-liquid equilibria of eicosane, tetracosane or biphenyl + 1- octadecanol, or + 1-eicosanol mixtures |
| Tfus | 342.10 | K | The use of organic calibration standards in the enthalpy calibration of differential scanning calorimeters |
| Tfus | 342.08 | K | Investigation of the melting behavior of the reference materials biphenyl and phenyl salicylate by a new type adiabatic scanning calorimeter |
| Ttriple | [341.80; 342.09] | K |
|
| Ttriple | 342.09 ± 0.01 | K | NIST |
| Ttriple | 341.80 ± 0.30 | K | NIST |
| Vc | [0.497; 0.497] | m3/kmol |
|
| Vc | 0.497 | m3/kmol | KDB |
| Vc | 0.497 | m3/kmol | NIST |
| Zc | 0.2613710 | KDB | |
| Zra | 0.27 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [278.63; 358.58] | J/mol×K | [527.32; 777.19] |
|
| Cp,gas | 278.63 | J/mol×K | 527.32 | Joback Calculated Property |
| Cp,gas | 294.98 | J/mol×K | 568.96 | Joback Calculated Property |
| Cp,gas | 310.02 | J/mol×K | 610.61 | Joback Calculated Property |
| Cp,gas | 323.82 | J/mol×K | 652.25 | Joback Calculated Property |
| Cp,gas | 336.46 | J/mol×K | 693.90 | Joback Calculated Property |
| Cp,gas | 348.02 | J/mol×K | 735.54 | Joback Calculated Property |
| Cp,gas | 358.58 | J/mol×K | 777.19 | Joback Calculated Property |
| Cp,liquid | [259.54; 301.20] | J/mol×K | [298.00; 422.00] |
|
| Cp,liquid | 259.54 | J/mol×K | 298.00 | NIST |
| Cp,liquid | 263.20 | J/mol×K | 350.80 | NIST |
| Cp,liquid | 285.30 | J/mol×K | 370.00 | NIST |
| Cp,liquid | 300.00 | J/mol×K | 370.00 | NIST |
| Cp,liquid | 301.20 | J/mol×K | 422.00 | NIST |
| Cp,solid | [190.00; 198.39] | J/mol×K | [294.40; 303.00] |
|
| Cp,solid | 194.10 | J/mol×K | 294.40 | NIST |
| Cp,solid | 197.90 | J/mol×K | 298.10 | NIST |
| Cp,solid | 198.39 | J/mol×K | 298.15 | NIST |
| Cp,solid | 198.17 | J/mol×K | 298.15 | NIST |
| Cp,solid | 197.70 | J/mol×K | 298.15 | NIST |
| Cp,solid | 190.80 | J/mol×K | 298.15 | NIST |
| Cp,solid | 190.00 | J/mol×K | 300.00 | NIST |
| Cp,solid | 197.90 | J/mol×K | 303.00 | NIST |
| η | [0.0002032; 0.0026453] | Pa×s | [277.84; 527.32] |
|
| η | 0.0026453 | Pa×s | 277.84 | Joback Calculated Property |
| η | 0.0013056 | Pa×s | 319.42 | Joback Calculated Property |
| η | 0.0007582 | Pa×s | 361.00 | Joback Calculated Property |
| η | 0.0004926 | Pa×s | 402.58 | Joback Calculated Property |
| η | 0.0003470 | Pa×s | 444.16 | Joback Calculated Property |
| η | 0.0002595 | Pa×s | 485.74 | Joback Calculated Property |
| η | 0.0002032 | Pa×s | 527.32 | Joback Calculated Property |
| ΔfusH | [18.57; 19.70] | kJ/mol | [314.30; 344.34] |
|
| ΔfusH | 18.95 | kJ/mol | 314.30 | NIST |
| ΔfusH | 18.65 | kJ/mol | 341.50 | NIST |
| ΔfusH | 18.66 | kJ/mol | 341.50 | NIST |
| ΔfusH | 18.66 | kJ/mol | 341.50 | NIST |
| ΔfusH | 18.59 | kJ/mol | 342.00 | NIST |
| ΔfusH | 18.58 | kJ/mol | 342.10 | NIST |
| ΔfusH | 18.58 | kJ/mol | 342.20 | NIST |
| ΔfusH | 19.70 | kJ/mol | 342.30 | NIST |
| ΔfusH | 18.57 | kJ/mol | 343.00 | NIST |
| ΔfusH | 18.80 | kJ/mol | 344.10 | NIST |
| ΔfusH | 19.27 | kJ/mol | 344.34 | NIST |
| ΔsubH | [68.60; 83.60] | kJ/mol | [283.00; 383.00] |
|
| ΔsubH | 83.60 ± 2.50 | kJ/mol | 283.00 | NIST |
| ΔsubH | 81.59 | kJ/mol | 288.05 | NIST |
| ΔsubH | 75.80 ± 0.60 | kJ/mol | 289.00 | NIST |
| ΔsubH | 68.60 ± 0.80 | kJ/mol | 292.00 | NIST |
| ΔsubH | 76.00 ± 4.00 | kJ/mol | 293.00 | NIST |
| ΔsubH | 68.60 ± 0.80 | kJ/mol | 295.00 | NIST |
| ΔsubH | 75.10 ± 1.70 | kJ/mol | 297.00 | NIST |
| ΔsubH | 81.52 | kJ/mol | 298.15 | NIST |
| ΔsubH | 81.60 ± 1.70 | kJ/mol | 301.00 | NIST |
| ΔsubH | 75.20 | kJ/mol | 308.00 | NIST |
| ΔsubH | 83.40 | kJ/mol | 310.50 | NIST |
| ΔsubH | 80.40 ± 1.60 | kJ/mol | 319.00 | NIST |
| ΔsubH | 75.81 ± 0.59 | kJ/mol | 342.50 | NIST |
| ΔsubH | 81.80 | kJ/mol | 383.00 | NIST |
| ΔvapH | [45.61; 64.95] | kJ/mol | [298.00; 647.00] |
|
| ΔvapH | 64.95 | kJ/mol | 298.00 | Enthalpies of Vaporization and Vapor Pressures of Some Deuterated Hydrocarbons. Liquid-Vapor Pressure Isotope Effects |
| ΔvapH | 60.40 | kJ/mol | 363.00 | NIST |
| ΔvapH | 59.60 | kJ/mol | 400.50 | NIST |
| ΔvapH | 54.90 | kJ/mol | 416.50 | NIST |
| ΔvapH | 59.40 | kJ/mol | 443.00 | NIST |
| ΔvapH | 57.40 | kJ/mol | 464.00 | NIST |
| ΔvapH | 60.30 | kJ/mol | 464.00 | NIST |
| ΔvapH | 50.40 | kJ/mol | 464.00 | NIST |
| ΔvapH | 57.30 | kJ/mol | 476.50 | NIST |
| ΔvapH | 45.61 | kJ/mol | 528.20 | KDB |
| ΔvapH | 51.20 | kJ/mol | 591.50 | NIST |
| ΔvapH | 48.00 | kJ/mol | 647.00 | NIST |
| Pvap | [0.10; 0.57] | kPa | [345.70; 376.20] |
|
| Pvap | 0.10 | kPa | 345.70 | Benchmark properties of biphenyl as a liquid organic hydrogen carrier: Evaluation of thermochemical data with complementary experimental and computational methods |
| Pvap | 0.12 | kPa | 347.70 | Benchmark properties of biphenyl as a liquid organic hydrogen carrier: Evaluation of thermochemical data with complementary experimental and computational methods |
| Pvap | 0.12 | kPa | 348.30 | Benchmark properties of biphenyl as a liquid organic hydrogen carrier: Evaluation of thermochemical data with complementary experimental and computational methods |
| Pvap | 0.14 | kPa | 350.40 | Benchmark properties of biphenyl as a liquid organic hydrogen carrier: Evaluation of thermochemical data with complementary experimental and computational methods |
| Pvap | 0.16 | kPa | 353.30 | Benchmark properties of biphenyl as a liquid organic hydrogen carrier: Evaluation of thermochemical data with complementary experimental and computational methods |
| Pvap | 0.22 | kPa | 358.30 | Benchmark properties of biphenyl as a liquid organic hydrogen carrier: Evaluation of thermochemical data with complementary experimental and computational methods |
| Pvap | 0.28 | kPa | 363.30 | Benchmark properties of biphenyl as a liquid organic hydrogen carrier: Evaluation of thermochemical data with complementary experimental and computational methods |
| Pvap | 0.35 | kPa | 368.20 | Benchmark properties of biphenyl as a liquid organic hydrogen carrier: Evaluation of thermochemical data with complementary experimental and computational methods |
| Pvap | 0.37 | kPa | 368.20 | Benchmark properties of biphenyl as a liquid organic hydrogen carrier: Evaluation of thermochemical data with complementary experimental and computational methods |
| Pvap | 0.48 | kPa | 373.10 | Benchmark properties of biphenyl as a liquid organic hydrogen carrier: Evaluation of thermochemical data with complementary experimental and computational methods |
| Pvap | 0.54 | kPa | 375.40 | Benchmark properties of biphenyl as a liquid organic hydrogen carrier: Evaluation of thermochemical data with complementary experimental and computational methods |
| Pvap | 0.57 | kPa | 376.20 | Benchmark properties of biphenyl as a liquid organic hydrogen carrier: Evaluation of thermochemical data with complementary experimental and computational methods |
| ρl | 990.00 | kg/m3 | 347.00 | KDB |
| ΔfusS | [54.20; 60.30] | J/mol×K | [314.30; 344.10] |
|
| ΔfusS | 60.30 | J/mol×K | 314.30 | NIST |
| ΔfusS | 54.60 | J/mol×K | 341.50 | NIST |
| ΔfusS | 54.81 | J/mol×K | 341.50 | NIST |
| ΔfusS | 54.40 | J/mol×K | 342.00 | NIST |
| ΔfusS | 54.30 | J/mol×K | 342.10 | NIST |
| ΔfusS | 54.30 | J/mol×K | 342.20 | NIST |
| ΔfusS | 54.20 | J/mol×K | 343.00 | NIST |
| ΔfusS | 54.60 | J/mol×K | 344.10 | NIST |
| γ | 0.03 | N/m | 393.20 | KDB |
| ΔsubS | 273.42 | J/mol×K | 298.15 | NIST |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | [347.00; 418.20] | K | [0.03; 2.90] |
|
| Tboilr | 347.00 ± 4.00 | K | 0.03 | NIST |
| Tboilr | 418.20 | K | 2.90 | NIST |
| Tboilr | 418.00 | K | 2.90 | NIST |
Datasets
Specific volume, m3/kg
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Specific volume, m3/kg - Liquid |
| 333.15 | 100.00 | 0.0010 |
| 343.15 | 100.00 | 0.0010 |
| 353.15 | 100.00 | 0.0010 |
| 353.15 | 10000.00 | 0.0010 |
| 353.15 | 20000.00 | 0.0010 |
| 353.15 | 30000.00 | 0.0010 |
| 363.15 | 100.00 | 0.0010 |
| 363.16 | 100.00 | 0.0010 |
| 363.16 | 10000.00 | 0.0010 |
| 363.16 | 20000.00 | 0.0010 |
| 363.16 | 30000.00 | 0.0010 |
| 363.16 | 40000.00 | 0.0010 |
| 363.16 | 50000.00 | 0.0010 |
| 363.16 | 60000.00 | 0.0010 |
| 363.16 | 70000.00 | 0.0010 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [0.11; 3838.88] | kPa | [342.00; 789.26] |
KDB Vapor Pressure Data
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 9.40474e+01 | |||
| Coefficient B | -1.07952e+04 | |||
| Coefficient C | -1.11711e+01 | |||
| Coefficient D | 3.86310e-06 | |||
| Temperature range, min. | 342.00 | |||
| Temperature range, max. | 789.26 | |||
| Pvap | 0.11 | kPa | 342.00 | Calculated Property |
| Pvap | 1.47 | kPa | 391.70 | Calculated Property |
| Pvap | 10.09 | kPa | 441.39 | Calculated Property |
| Pvap | 43.55 | kPa | 491.09 | Calculated Property |
| Pvap | 136.35 | kPa | 540.78 | Calculated Property |
| Pvap | 340.48 | kPa | 590.48 | Calculated Property |
| Pvap | 722.79 | kPa | 640.17 | Calculated Property |
| Pvap | 1363.78 | kPa | 689.87 | Calculated Property |
| Pvap | 2361.05 | kPa | 739.56 | Calculated Property |
| Pvap | 3838.88 | kPa | 789.26 | Calculated Property |
Similar Compounds
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Find more compounds similar to Biphenyl.
Mixtures
- Indole + Biphenyl
- Carbon dioxide + Biphenyl + Naphthalene
- Biphenyl + 1-Octadecanol
- Biphenyl + 1-Eicosanol
- Carbon dioxide + Biphenyl
- Diphenyl ether + Biphenyl
- Biphenyl + Benzaldehyde, 3-hydroxy-
- Biphenyl + Water
Sources
- KDB Pure (Korean Thermophysical Properties Databank)
- KDB Vapor Pressure Data
- Cheméo Relay (1.0)
- Crippen Method
- PVT Relationships of Binary Mixtures of Indole with 2-Methylnaphthalene and Biphenyl at 333.15 K and Pressures up to 270 MPa
- Solid liquid gas equilibrium of the naphthalene biphenyl CO2 system: Measurement and modeling
- Solid-liquid equilibria of eicosane, tetracosane or biphenyl + 1- octadecanol, or + 1-eicosanol mixtures
- High-pressure phase diagram of the drug mitotane in compressed and/or supercritical CO2
- Thermophysical properties of diphenyl ether + biphenyl mixtures for their use as heat transfer fluids
- Isobaric heat capacity at high pressure, density, and viscosity of (diphenyl ether + biphenyl) mixtures
- Benchmark properties of biphenyl as a liquid organic hydrogen carrier: Evaluation of thermochemical data with complementary experimental and computational methods
- Synthesis and characterization of novel binary organic monotectic and eutectic alloys
- The use of organic calibration standards in the enthalpy calibration of differential scanning calorimeters
- Investigation of the melting behavior of the reference materials biphenyl and phenyl salicylate by a new type adiabatic scanning calorimeter
- The Effects of Temperature and Inorganic Salts on the Aqueous Solubility of Selected Chlorobenzenes
- Solubilities of 4-Phenyltoluene, Phenylboric Acid, Biphenyl, and Iodobenzene in Carbon Dioxide from Measurements of the Relative Permittivity
- Enthalpies of Vaporization and Vapor Pressures of Some Deuterated Hydrocarbons. Liquid-Vapor Pressure Isotope Effects
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
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