Experimental and modeling of fixed-bed reactor for yellow phosphorous tail gas purification over impregnated activated carbon

Chemical Engineering Journal

Volumn 137, Issue 3, 2008, Pages 471-479

  Ma, Liping ^a   Ning, Ping ^a   Zhang, Yuanyuan ^a   Wang, XueQian ^a  

^a KUNMING UNIVERSITY OF SCIENCE AND TECHNOLOGY   (China)

Author keywords

Catalytic oxidation; Fixed bed; Impregnated activated carbon; Modeling; Yellow phosphorous tail gas

Indexed keywords

ACTIVATED CARBON; ADSORPTION; BINARY MIXTURES; CATALYTIC OXIDATION; GAS FUEL PURIFICATION; IMPREGNATION; METHANOL; PILOT PLANTS; RAW MATERIALS; REACTION KINETICS;

FIXED BED; IMPREGNATED ACTIVATED CARBON; YELLOW PHOSPHOROUS TAIL GAS;

PHOSPHORUS;

ACTIVATED CARBON; ADSORPTION; BINARY MIXTURES; CATALYTIC OXIDATION; GAS FUEL PURIFICATION; IMPREGNATION; METHANOL; PHOSPHORUS; PILOT PLANTS; RAW MATERIALS; REACTION KINETICS;

EID: 39749101756     PISSN: 13858947     EISSN: None     Source Type: Journal    
DOI: 10.1016/j.cej.2007.04.032     Document Type: Article

References (32)

1. Ning P., Xie Y.Ch., and Yi H.H. Study on a four-bed PSA process for the manufacture of pure CO. Proceedings of Seventh International Conference of Fundamentals of Adsorption. Nagasaki, Japan (2001) 613-617
2. Xie Y.-Ch., and Zhang J.P. Adsorption isotherms for PU1 and its application in industry. Proceedings of Seventh International Conference of Fundamentals of Adsorption. Nagasaki, Japan (2001) 561-563
3. B.S. Shakirv, St. Prom, Pretreatment and purification of yellow phosphoric tail gas, Moscow, vol. 148, 1993, pp. 3-4.
4. Zhantasov K.T. Impurities remove from yellow phosphoric tail gas. Vestn. Minist. Nauki-Akak. Nauk Res. Kaz. 5 (1997) 52
5. Westmoreland P.R., and Harrison D.P. Evaluation of candidate solids for high temperature desulfurization of low BTU gases. Environ. Sci. Technol. 10 (1976) 659-663
6. 2S from coal gas using limestone: kinetic consideration. Ind. Eng. Chem. Res. 33 2 (1994) 265-272
7. 2S sorption by calcined limestone. Ind. Eng. Chem. Res. 34 7 (1995) 2334-2342
8. Chauk S.S., Agnihotri R., and Jadhav R.A. Kinetic of high-pressure removal of hydrogen sulfide using calcium oxide powder. Am. Ind. Chem. Eng. J. 46 6 (2000) 1157-1167
9. 2 concentrations. Chem. Eng. Sci. 57 13 (2002) 2381-2393
10. 2S removal from coal gases. Ind. Eng. Chem. Res. 37 (1998) 2775-2782
11. Suvar E., Radamson H., and Grahn J.V. Phosphorus profile control in low-temperature silicon epitaxy by reduced pressure chemical vapor deposition. Mater. Sci. Eng. B 89 (2002) 314-323
12. Sun Y., Law D.C., and Hicks R.F. Kinetics of phosphine adsorption and phosphorus desorption from gallium and indium phosphide (0 0 1). Surf. Sci. 540 (2003) 12-22
13. 2 on Bigadiç Clinoptilolite. Sep. Sci. Technol. 30 (1995) 2747-2756
14. 2S catalytic oxidation on impregnated activated carbon: experiment and modeling. Chem. Eng. J. 118 (2006) 133-139
15. 2S and sulfur recovery with heteropoly compound. Sep. Purif. Technol. 31 (2003) 111-121
16. 2S. Ind. Eng. Chem. Res. 34 (1995) 1102-1109
17. 3 catalyst under flow and pressure conditions: a thermodynamic and modelization study. Thermochim. Acta 379 (2001) 241-254
18. Bansal R.C., Donnet J.B., and Stoeckli F. Activated Carbon (1988), Dekker, New York
19. 2S concentrations by chemical adsorption and biological oxidation process. Environ. Eng. Sci. 23 6 (2006) 942-953
20. Kaliva A.N., and Smith J.W. Oxidization of low concentration of hydrogen sulfide by air on a fixed activated carbon. Can. J. Chem. Eng. 61 (1983) 208-212
21. Yang R.T. Gas Separation by Adsorption Process (1987), Butterworths, London
22. Suwanprasop S., Eftaxias A., Stuber F., Polaert I., Lebigue C.J., and Delmas H. Scale-up and modeling of fixed-bed reactors for catalytic phenol oxidation over adsorptive active carbon. Ind. Eng. Chem. Res. 44 (2005) 9513-9523
23. 2. Chem. Eng. Sci. 51 (1996) 2523-2533
24. Konttinen J.T., Zevenhoven C.A.P., and Hupa M.M. Hot gas desulfurization with zinc titanate sorbents in a fluidized bed 2. Reactor model. Ind. Eng. Chem. Res. 36 (1997) 2340-2349
25. Konttinen J.T., Zevenhoven C.A.P., and Hupa M.M. Determination of sorbent particle conversion rate model parameters. Ind. Eng. Chem. Res. 36 (1997) 2336-2345
26. Bart H.J., Ning P., and Germerdonk R. Two-dimensional non-isothermal model for toluene adsorprion in a fixed bed adsorber. Chem. Eng. Process. 35 (1996) 57-63
27. Bart H.J. Numerical simulation of toluene adsorption on activated carbon in a technical column in low concentration range. Chem. Eng. Technol. 19 4 (1996) 296-303
28. Zhang H.P., and Cheng D.Y. Mathematical model for a fixed bed adsorptive reactor. Carbon 38 (2000) 877-880
29. Gu J.J., and Bart H.J. Heat and mass transfer in steam desorption of an activated carbon adsorber. Inter. Commun. Heat Mass Trans. 32 (2005) 296-304
30. Huang H.J., Wu G.B., Yang J., and Dai Y.C. Modeling of gas-solid chemisorption in chemical heat pumps. Sep. Purif. Technol. 34 (2004) 191-200
31. 2S catalytic oxidation on impregnated activated carbon: experiment and modelling. Chem. Eng. J. 118 (2006) 133-139
32. Ning P. Numerische simulation des sorptionsverhaltnisses der schadstoffe in kleintechnischen aktivkohlekolonnen im umweltrelevanten konzentrationsbereich unter berucksichtigung von warmeeffekten und maldistribution (1996), Shaker Verlag, Aachen