Kinetic model for hydroisomerization reaction of C8-aromatics

Frontiers of Chemical Engineering in China

Volumn 2, Issue 1, 2008, Pages 10-16

  Xu, Ouguan ^a,b   Su, Hongye ^b   Jin, Xiaoming ^b   Chu, Jian ^b  

^a ZHEJIANG UNIVERSITY OF TECHNOLOGY   (China)

^b STATE KEY LABORATORY OF INDUSTRIAL CONTROL TECHNOLOGY   (China)

Author keywords

C8 aromatics; Catalyst deactivation function; Hydroisomerization; Kinetic model; Parameter estimation; Reaction network

Indexed keywords

EID: 41249100174     PISSN: 16737369     EISSN: 16737474     Source Type: Journal    
DOI: 10.1007/s11705-008-0015-2     Document Type: Article

References (21)

1. Zhao R D, Jin Z L. Aromatics Industry. Beijing: Chemical Industry Press, 2001 (in Chinese)
2. Collins D J, Medina R J, Davis B H. Xylene isomerization by ZSM-5 zeolite catalyst. The Can J of Chem Eng, 1983, 61: 29-35
3. Li Y G, Chang X D and Zeng Z H. Kinetics study of the isomerization of xylene on HZSM-5. 1: Kinetics model and reaction mechanism. Ind Eng Chem Res, 1992, 31(1): 187-192
4. Iliyas A, Al-Khattaf S. Xylene transformation over USY zeolite: An experimental and kinetic study. Appl Catal Gen A, 2004, 269: 225-236
5. Iliyas A, Al-Khattaf S. Xylene isomerization over USY zeolite in a Riser Simulator: A comprehensive kinetic model. Ind Eng Chem Res, 2004, 43(6): 1349-1358
6. Iliyas A and Al-Khattaf S. Gas-phase isomerization of meta -xylene over USY zeolite in aRiser Simulator: A simplified kinetic model. Chemical Engineering Journal, 2005, 107: 127-132
7. 8-aromatics. The Cana J of Chem Eng, 1980, 58: 517-520
8. Hsu Y S, Lee T Y and Hu H C. Isomerization of ethylebenzene and m -xylene on zeolite. Ind Eng Chem Res, 1988, 27(6): 942-947
9. 8 -aromatics. I: Modeling and estimation of relative rate constants by the Wei-Prater method. Journal of Chemical Industry and Engineering (China), 1985, 3(3): 257-267 (in Chinese)
10. 8 -aromatics. II: Mathematical expression of ray vector and its application. Journal of Chemical Industry and Engineering (China), 1985, 3(3): 268-277 (in Chinese)
11. 8-aromatics. Journal of Chemical Industry and Engineering (China), 1989, 3(3): 323-330 (in Chinese)
12. Ramage M P, Graziani K R and Krambeck F J. Development of Mobil's kinetic reforming model. Chem Eng Sci, 1980, 35(1): 41-48
13. Zheng Y, Wei F, Jin Y. CFD simulation of FCC process in Downer reactor. Journal of Chemical Industry and Engineering (China), 2003, 54(8): 1087-1086 (in Chinese)
14. Jacob S M, Gross B and Weekman J R V W. A lumping and reaction scheme for catalytic cracking. AIChE J, 1976, 22(4): 701-713
15. 3 catalyst. Ind Eng Chem Res, 1988, 27(1): 51-57
16. Song X Q, Wang Z W, Jin Y. Hydrodynamics of radial flow moving-bed reactor. Journal of Chemical Industry and Engineering (China), 1992, 43(3): 268-274 (in Chinese)
17. Wang J F, Jing S, Wang T F, Jin Y, Ma X Q, Gao L P. Mathematical modeling and flow field characteristics of radial flow moving-bed reactors. Journal of Chemical Engineering of Chinese Universites, 1999, 13(5): 435-441 (in Chinese)
18. Huang H J. Practical computer simulation of chemical processes-MATLAB's application in chemical engineering. Beijing: Chemical Industry press, 2004 (in Chinese)
19. Zhang C F. The optimum temperature conditions for deactivating catalysts - an analysis of irreversible first-order reaction. Journal of East China Institute of Chemical Technology, 1983, 9(3): 339-344 (in Chinese)
20. Szépe S, Levenspie O. Optimal temperature policies for reactors subject to catalyst deactivation - I Batch reactor. Chemical Engineering Science, 1968, 23: 881-894
21. Hu Y Y, Su H Y, Chu J. Modeling and simulation of commercial catalytic reformers. Journal of Chemical Engineering of Chinese Universites, 2003, 17(4): 418-424 (in Chinese)