Measurement and prediction of oxygen solubility in toluene at temperatures from 298.45 K to 393.15 K and pressures up to 1.0 MPa

Journal of Chemical and Engineering Data

Volumn 52, Issue 6, 2007, Pages 2339-2344

  Li, Airong ^a   Tang, Shengwei ^a   Tan, Pinghua ^a   Liu, Changjun ^a   Liang, Bin ^a  

^a SICHUAN UNIVERSITY   (China)

Author keywords

[No Author keywords available]

Indexed keywords

MIXING; PHASE EQUILIBRIA; PRESSURE EFFECTS; SOLUBILITY; THERMOANALYSIS; TOLUENE;

MODIFIED-HURON VIDAL (MHV1) MIXING RULE; OXYGEN SOLUBILITY; PREDICTIVE SOAVE-REDILICH-KWONG (PSRK) EQUATION; TOTAL PRESSURE METHOD;

DISSOLVED OXYGEN;

EID: 36849095577     PISSN: 00219568     EISSN: None     Source Type: Journal    
DOI: 10.1021/je700330c     Document Type: Article

References (30)

1. Kantm, M. L.; Sreekanth, P.; Rao, K. K. et al. An improved process for selective liquid-phase air oxidation of toluene. Catal. Lett. 2002, 81, 223-232.
2. Borgaonkar, H. V.; Raverkar, S. R.; Chandalla, S. B. Liquid phase oxidation of toluene to benzaldehyde by air. Ind. Eng. Prod. Res. Dev. 1984, 23, 455-458.
3. Hoom, J. A. A.; Van Soolingen, J.; Versteeg, G. F. Modeling toluene oxidation incorporation of mass transfer phenomena. Chem. Eng. Res. Des. 2005, 52, 187-195.
4. 4 in methylcyclohexane and toluene at 283 K to 313 K. J. Chem. Thermodyn. 1974, 6, 237-243.
5. Fischer, K.; Wilken, M. Experimental determination of oxygen and nitrogen solubility in organic solvents up to 10 MPa at temperatures between 298 K and 398 K. J. Chem. Thermodyn. 2001, 33, 1285-1308.
6. Holderbaum, T.; Gmehling, J. PSRK: A group contribution equation of state based on UNIFAC. Fluid Phase Equilib. 1991, 70, 251-265.
7. Fischer, K.; Gmehling, J. Further development status and results of the PSRK method for the prediction of vapor-liquid equilibrium and gas solubilities. Fluid Phase Equilib. 1996, 121, 185-206.
8. Gmehling, J.; Li, J.; Fischer, K. Further development of the PSRK model for the prediction of gas solubilities and vapor-liquid-equilibria at low and high pressures II. Fluid Phase Equilib. 1997, 141, 113-127.
9. Horstmann, S.; Fischer. K.; Gmehling, J. PSRK group contribution equation of state: revision and extension III. Fluid Phase Equilib. 2000, 167, 173-186.
10. Li, J.; Topphoff, M.; Fischer, K.; Gmehling, J. Prediction of gas solubilities in aquesous electrolyte systems using the predictive Soave-Redlich-Kwong model. Ind. Eng. Chem. Res. 2001, 40, 3703-3710.
11. Fredenslund, A.; Jones, R. L.; Prausnitz, J. M. Group-contribution estimation of activity coefficients in nonideal liquid mixtures. AIChE J. 1975, 21 6, 1086-1099.
12. Abrams, D. S.; Prausnitz, J. M. Statistical thermodynamics of liquid mixture: a new expression for the excess Gibbs energy of partly or completely miscible systems. AIChE J. 1975, 21 1, 116-128.
13. Cukor, P. M.; Prausnitz, J. M. Solubilities in liquids at elevated temperatures. Henry's constant for hydrogen, methane, and ethane in hexadecane, bicyclohexyl, and diphenylmethane. J. Phys. Chem. 1972, 76, 598-601.
14. Olson, J. D. Solubility of nitrogen, argon, methane, and ethane in ethylene oxide. J. Chem. Eng. Data. 1977, 22, 326-329.
15. Graaf, G. H.; Smit, H. J.; Stamhuis, E. J.; Beenackers, A. A. C. M. Gas-Liquid solubilities of the methanol synthesis components in various solvents. J. Chem. Eng. Data. 1992, 37, 146-158.
16. d'Angelo, J. V. H.; Francescon, A. Z. Gas-liquid solubility of hydrogen in n-Alcohols (1 ≤n ≤4) at pressure from 3.6 MPa to 10 MPa and temperatures from 298.15 K to 525.15 K. J. Chem. Eng. Data. 2001, 46, 671-674.
17. Breman, B. B.; Beenackers, A. A. C. M.; Rietjens, E. W. J.; Stege, J. H. Gas-liquid solubilities of carbon monoxide, carbon dioxide, hydrogen, water, 1-alcohols (2 ≤ n ≤6) in hexadecane, octacosane, 1-hexandecanol, phenantrene; tetraethylene glycol at pressure up to 5.5 MPa and temperatures from 293 K to 553 K. J. Chem. Eng. Data. 1994, 39, 647-666.
18. Jacquemin, J.; Costa Gomes, M. F. et al. Solubility of carbon dioxide, ethane, methane, oxygen, nitrogen, hydrogen, argon, and carbon monoxide in 1-butyl-3-methylimidazolium tetrafluoroborate between temperatures 283 K and 343 K and at pressures close to atmospheric. J. Chem. Thermodyn. 2006, 38, 490-502.
19. Mainar, A. M.; Pardo, J. I. et al. Solubility of gases in binary liquid mixtures: an experimental and theoretical study of the system noble gas + trifluoroethanol + water. Ind. Eng. Chem. Res. 2003, 42, 1439-1450.
20. Gibanel, F.; Lopez, M. C.; Royo, F. M.; Rodriguez, V.; Vrieta, J. S. Solubility of nonpolar gases in tetrahydropyran at 0°C to 30°C and 101.33 KPa partial pressure of gas. J. Solution Chem. 1994, 23, 1247.
21. Clever, H. L.; Battino, R. Techniques of chemistry. Solutions and Solubilities Part I; Wiley: New York, 1975; Vol. 8.
22. Wilhem, E. Precision Methods for the Determination of the Solubility of gases in liquids. Crit. Rev. Anal. Chem. 1985, 16, 129.
23. Weast, R. C., Astle, M. J., Eds. CRC Handbook of data on organic compounds; CRC Press: Boca Raton, FL, 1987.
24. Zhang, L. H. Handbook of Petrochemical Datum; Chemical Industry Press: Beijing, 1983.
25. Stephenson, R. M.; Malanowski, S. Handbook of the thermodynamics of organic compounds; Elsevier Science Publishing Co. Inc: New York, 1987.
26. Stefoglo, E. F.; Kuchin, I. V.; Kravtsov, A. V. Study of gas-liquid stirred reactor stability taking into account the temperature influence on gas solubility. Chem. Eng. Science 2004, 59, 4137-4147.
27. Jobbagy, M. M.; Rarey-nies, J.; Gmehling, J. Gas solubility data for further development of phase equilibrium models. Fluid Phase Equilib. 1988, 42, 185-194.
28. Atiqullah, M.; Hammawa, H.; Hamid, H. Modeling the solubility of ethylene and propylene in a typical polymerization diluent: some selected situations. Eur. Polym. J. 1998, 34, 1522-1520.
29. E-EOS model in phase equilibrium calculation and prediction. Petrochem. Technol. 2005, 34, 694-698.
30. Bondi, A. Physical Properties of Molecular Crystals; Wiley: New York, 1968.