Combinatorial modification and catalytic performance of ZSM-5 zeolite by phosphorus and aluminum

被引:0
|
作者
Li X. [1 ]
Zheng Q. [1 ]
Mi S. [1 ]
Shen B. [1 ]
机构
[1] State Key Laboratory of Heavy Oil Processing, The Key Laboratory of Catalysis of CNPC, China University of Petroleum, Beijing
来源
Huagong Xuebao/CIESC Journal | 2016年 / 67卷 / 08期
基金
中国国家自然科学基金;
关键词
Acidity; Catalysis; Composites; Hydrothermal; Phosphorus and aluminum combined modification; ZSM-5; zeolite;
D O I
10.11949/j.issn.0438-1157.20160368
中图分类号
学科分类号
摘要
ZSM-5 zeolite, one of the important shape selective catalysts with high molar ratio of silica to alumina, possesses strong acidity and excellent thermal and hydrothermal stability. The acidity and pore structure of ZSM-5 zeolite were adjusted by combinatorially modifying ZSM-5 molecular sieves with phosphorus and aluminum. Results showed lamellar-structured phosphorus and aluminum deposits on the surface of ZSM-5 zeolite at greater than 10% (mass) load of phosphorus and aluminum, which increased its acidity and formed new mesopores about 10 nm in diameter. Such highly acidic porous structures significantly increased the conversion of n-octane and the propylene yield by more than 20%. When used in catalytic cracking of heavy oil, the yield of oil residual and coke was decreased but the yield of propylene was increased by 1%. © All Right Reserved.
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页码:3357 / 3362
页数:5
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  • [1] Corma A., Melo F., Sauvanaud L., Et al., Different process schemes for converting light straight run and fluid catalytic cracking naphthas in a FCC unit for maximum propylene production, Appl. Catal. A, 265, pp. 195-206, (2004)
  • [2] Buchanan J.S., The chemistry of olefins production by ZSM-5 addition to catalytic cracking units, Catalysis Today, 55, pp. 207-212, (2000)
  • [3] Selli E., Rossetti I., Meloni D., Et al., Effect of surface acidity on the behavior of Fe-MFI catalysts for benzene hydroxylation to phenol, Appl. Catal. A, 262, pp. 131-136, (2004)
  • [4] Groen J.C., Moulijin J.A., Perez-Ramirez J., Decoupling mesoporosity formation and acidity modification in ZSM-5 zeolites by sequential desilication-dealumination, Microporous Mesoporous Mater., 87, pp. 153-161, (2005)
  • [5] Gopalakrishnan S., Zampieri A., Schwieger W., Et al., Mesoporous ZSM-5 zeolites via alkali treatment for the direct hydroxylation of benzene to phenol with N<sub>2</sub>O, Journal of Catalysis, 260, pp. 193-197, (2008)
  • [6] Muller M., Harvey G., Prins R., Comparison of the dealumination of zeolites beta, mordenite, ZSM-5 and ferrierite by thermal treatment, leaching with oxalic acid and treatment with SiCl<sub>4</sub> by <sup>1</sup>H, <sup>29</sup>Si and <sup>27</sup>Al MAS NMR, Microporous Mesoporous Mater., 34, pp. 135-147, (2000)
  • [7] Ogura M., Shinomiya S., Tateno J., Et al., Alkali-treatment technique-new method for modification of structural and acid-catalytic properties of ZSM-5 zeolites, Appl. Catal. A, 219, pp. 33-43, (2001)
  • [8] Groen J.C., Peffer L.A.A., Moulijn J.A., Et al., Mechanism of hierarchical porosity development in MFI zeolites by desilication: the role of aluminium as a pore-directing agent, Chemistry A European Journal, 11, pp. 4983-4994, (2005)
  • [9] Zhu X., Liu S., Song Y., Et al., Butene catalytic cracking to propene and ethene over potassium modified ZSM-5 catalysts, Catalysis Letters, 103, 3-4, pp. 201-210, (2005)
  • [10] Zhang Y., Zhou Y., Qiu A., Et al., Propane dehydrogenation on PtSn/ZSM-5 catalyst: effect of tin as a promoter, Catalysis Communications, 7, pp. 860-866, (2006)