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Study on Deactivation and Cracking Performance of Catalysts Containing Y and MFI Zeolites

Study on Deactivation and Cracking Performance of Catalysts Containing Y and MFI Zeolites
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摘要 This article investigated the deactivation caused by hydrothermal treatment and metal contamination of two cracking catalysts containing the Y and ZRP- 1 zeolites aimed at maximization of light olefin yield.Test results had shown that the hydrothermal stability and resistance to metal contamination of the ZRP-1zeolite were apparently better than those of the Y zeolite. Hydrothermal treatment and metal contamination had not only changed the catalytic cracking performance of respective zeolites, but at the same time had also modified to a definite degree of the relative proportions of effective components in these two zeolites and affected the synergistic effects between them, resulting in a relative enhancement of secondary cracking ability of the catalyst and increased olefin selectivity in the FCC products. In the course of application of catalyst for maximization of light olefins yield appropriate adjustment of the relative proportion of two active components can help to alleviate the products distribution and selectivity changes caused by deactivationof FCC catalysts. This article investigated the deactivation caused by hydrothermal treatmentand metal contamination of two cracking catalysts containing the Y and ZRP-1 zeolites aimed atmaximization of light olefin yield.Test results had shown that the hydrothermal stability andresistance to metal contamination of the ZRP-1 zeolite were apparently better than those of the Yzeolite.Hydrothermal treatment and metal contamination had not only changed the catalytic crackingperformance of respective zeolites,but at the same time had also modified to a definite degree ofthe relative proportions of effective components in these two zeolites and affected the synergisticeffects between them,resulting in a relative enhancement of secondary cracking ability of thecatalyst and increased olefin selectivity in the FCC products.In the course of application ofcatalyst for maximization of light olefins yield appropriate adjustment of the relative proportionof two active components can help to alleviate the products distribution and selectivity changescaused by deactivation of FCC catalysts.
出处 《China Petroleum Processing & Petrochemical Technology》 SCIE CAS 2004年第1期29-35,共7页 中国炼油与石油化工(英文版)
关键词 catalytic cracking ZEOLITE CATALYST DEACTIVATION MFI 沸石 钝化作用 裂化性能 催化剂 炼油行业 石油
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  • 1[1]Madon R J. Role of ZSM-5 and ultrastable Y zeolites for increasing gasoline octane number. J Catal, 199 l, 129(1): 275-287
  • 2[2]Buchanan J S. Reactions of model compounds over steamed ZSM-5 at simulated FCC reaction conditions. Appl Catal, 1991,74(1): 83-94
  • 3[3]Adewuyi Y G. Compositional changes in FCC gasoline products resulting from high-level additions of ZSM-5 zeolite to RE-USY catalyst. Appl Catal, A: General, 1997, 163(1-2): 15-29
  • 4[4]Rajagopalan K, Young G W. Hydrocarbon cracking selectivities with dual-function zeolite catalysts. In: Occelli M L.Fluid catalytic cracking: Role in modem refining, Washington,DC: American Chemical Society, 1988:34-48
  • 5[5]Hsing L H, Pratt R E. Fluid cracking catalyst ZSM-5 additive performance at overcracking mode. In: Occelli M L,O'Connor P. Fluid catalytic cracking III: Materials and processes. Washington, DC: American Chemical Society, 1994:241-270
  • 6[6]McDaniel C V, Maher P K. Zeolite stability and ultrastable zeolites. In: Rabo J A. Zeolite chemistry and catalysis.Washington, DC: American Chemical Society, 1976: 285-331
  • 7[7]Chen Junwu, Cao Hanchang, Catalytic Cracking Engineering and Process. Beijing: China Petrochemical Press, 1995
  • 8[8]Mitchell B R. Metal Contamination of Cracking Catalysts 1: Synthetic Metals Deposition on Fresh Catalysts. Ind Eng Chem Prod Res Dev, 1980, 1 9(2): 209-213

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