377367 Benzene Methylation Catalysed By Hierarchically Porous Zeolite: An Effective Way to Promote Xylene Selectivity and Catalyst Lifetime for Large Scale Commercial Use

Monday, November 17, 2014: 2:30 PM
304 (Hilton Atlanta)
Xuan He1, Kake Zhu1 and Xuedong Zhu2, (1)College of Chemical Engineering, East China University of Science and Technology, Shanghai, China, (2)Engineering Research Centre of Large Scale Reactor Engineering and Technology, East China University of Science and Technology, Shanghai, China

Benzene Methylation Catalysed by Hierarchically Porous Zeolite: An Effective Way to Promote Xylene Selectivity and Catalyst Lifetime for Large Scale Commercial Use

Xuan He1, Kake Zhu1, Xuedong Zhu*2

1 College of Chemical Engineering, East China University of Science and Technology, Shanghai, China, 2 Engineering Research Centre of Large Scale Reactor Engineering and Technology, East China University of Science and Technology, Shanghai, China

Abstract

Methylation of benzene is an alternative low-cost route to produce xylenes, but selectivity to xylene remains low over conventional zeolitic catalysts. In this work, a combined dry-gel-conversion and steam-assisted-crystallization method is used to synthesize hierarchically porous zeolite ZSM-5 with varied Si/Al ratios. N2 physisorption, NH3- TPD, SEM and FT-IR are employed to characterize the texture and acidity of both hierarchically porous zeolites and their conventional counterparts. The method is found to be applicable to ZSM-5 with Si/Al ratios from 20 to 180. Catalytic properties are test on benzene methylation at 460 oC to investigate the effect of additional porosity and Si/Al ratios. At low Si/Al ratios, the benzene conversions over conventional and hierarchical ZSM-5 are close, and selectivity to toluene is high over hierarchical ZSM-5. It is found that hierarchical porosity markedly enhances the utility of zeolite and selectivity towards xylenes via improved mass transport at higher Si/Al ratios. Under optimized hierarchical ZSM-5 catalyst, xylene selectivity reaches 34.9 % at Si/Al ratio of 180, and a remarkable lifetime of 3000 h is accomplished in industrial sideline evaluation.

Key words: benzene methylation, hierarchical porous zeolite, process intensification

 

 

References

[1]Van der Mynsbrugge, J., Visur, M., Olsbye, et al. Methylation of benzene by methanol: Single-site kinetics over H-ZSM-5 and H-beta zeolite catalysts[J]J. Catal., 2008, 292: 201-212

[2]Mirth, G., Lercher, J.A.. In Situ IR spectroscopic study of the surface species during methylation of toluene over HZSM-5[J]J. Catal., 1991, 132: 244-252

[3]Odedairo, T., Al-Khattaf, S.. Comparative study of zeolite catalyzed alkylation of benzene with alcohols of different chain length: H-ZSM-5 versus mordenite[J]Catal. Today, 2013, 204: 73-84

Fig.1 Crystallization mechanism on hierarchical porous ZSM-5 in this work

Fig.2 MFI topology and para-xylene

Fig.3 Mechanism on benzene alkylation with methanol

Fig.4 SEM image of conventional ZSM-5 (a, c, d) and hierarchically porous (b, e, f) ZSM-5-HTS with Si/Al ratios of 20 (a, b) and 180 (c-f)

 


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