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改性介质的调变对NaY沸石后处理及其催化裂化性能的影响 被引量:2

Influence of modifying medium on treatment and catalytic performance of NaY zeolite
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摘要 Y型沸石作为FCC催化剂的主要活性组分,其酸性能和孔结构的改性效果直接决定了催化剂的性能优劣。选取酸性能为调变对象,分别采用两种不同的改性介质(Ce Y焙烧气氛和铵离子交换p H)对Na Y沸石进行后改性处理。将所得的改性Y沸石进行了红外(IR)、X光电子能谱(XPS)和低温氮气物理吸附等表征分析。最后,使用真实油品VGO在固定流化床反应评价装置ACE上对改性样品的催化性能进行了评价。研究发现,选取Ce离子作为改性介质时,可通过改变后处理过程中的焙烧气氛来调变沸石不同酸类型的分布(Br?nsted/Lewis acid,B/L),实现对应的USY沸石的催化性能的调控;选取铵离子作为改性介质时,适当地调节第1次铵离子交换p H的苛刻程度,能够在调变超稳Y沸石B酸量的同时提高Y型沸石的介孔体积。 Y zeolite, the main component responsible for the catalytic activity, selectivity, and stability of catalysts in fluid catalytic cracking(FCC), has long been used extensively in oil refining. The acidity and pore structure of Y zeolite determine its catalytic performance. To tune acidic property, post-synthesis treatment of Na Y was carried out with two different modifying media, i.e., the calcination atmosphere of Ce Y and the ammonium ion exchange with different p H value. The structures and physical properties of the modified Y zeolites were characterized by IR spectroscopy, X-ray photoelectron spectroscopy(XPS) and low temperature N2 physical adsorption; while their catalytic performance was evaluated on VGO oil in a fluidized bed reaction ACE unit. When Ce ion was chosen as the modifying medium, the distribution of various types of acids(Br?nsted/Lewis acid) and the catalytic performance of USY zeolites could be controlled by changing calcination atmosphere. When cationic ammonium was used, the amount of Br?nsted acid could be regulated and pore volume could be increased in the ultra stable Y zeolites by precisely adjusting p H value of the first ammonium ion exchange medium.
出处 《化工学报》 EI CAS CSCD 北大核心 2016年第8期3394-3399,共6页 CIESC Journal
基金 国家重点基础研究发展计划项目(2012CB215001) 国家自然科学基金项目(U1462202)~~
关键词 Y沸石改性 稀土 处理气氛 水热处理 变价 分子筛 催化剂 氧化 Y zeolite modification rare earth treatment atmosphere steam treatment valence transformation molecular sieves catalyst oxidation
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  • 1SCHERZER J.Chapter 5 Correlation between catalyst formulation and catalytic properties[J].Stud.Surf.Sci.Catal.,1993,76:145-182.
  • 2XU M,LIU X,MADON R J.Pathways for Y zeolite destruction:the role of sodium and vanadium[J].J.Catal.,2002,207(2):237-246.
  • 3何鸣元.催化裂化催化剂中Y型分子筛制造的水热化学[J].大自然探索,1996,15(4):12-13. 被引量:15
  • 4SATO K,NISHIMURA Y,MATSUBAYASHI N.Structural changes of zeolites during ion exchange treatment:effects of Si/Al ratio of the starting NaY[J].Microporous Mesoporous Mater.,2003,59:133-146.
  • 5SANDOVAL-DíAZ L,RUíZ-CARDONA Y,TRUJILLO C.Amorphization of USY zeolite induced by sodium chloride and high temperature steaming[J].Microporous Mesoporous Mater.,2016,224:168-175.
  • 6SCHüBLER F,SCHALLMOSER S,SHI H,et al.Enhancement of dehydrogenation and hydride transfer by La3+ cations in zeolites during acid catalyzed alkane reactions[J].ACS Catalysis,2014,4(6):1743-1752.
  • 7NERY J G,MASCARENHAS Y P,BONAGAMBA T J,et al.Location of cerium and lanthanum cations in CeNaY and LaNaY after calcination[J].Zeolites,1997,18(1):44-49.
  • 8BAUGIS G L,BRITO H F,OLIVEIRA W D,et al.The luminescent behavior of the steamed EuY zeolite incorporated with vanadium and rare earth passivators[J].Microporous Mesoporous Mater.,2001,49(1/2/3):179-187.
  • 9LI J C,ZENG P H,ZHAO L,et al.Tuning of acidity in CeY catalytic cracking catalysts by controlling the migration of Ce in the ion exchange step through valence changes[J].J.Catal.,2015,329:441-448.
  • 10GAO X H,QIN Z H,WANG B J,et al.High silica REHY zeolite with low rare earth loading as high-performance catalyst for heavy oil conversion[J].Applied Catalyst A:General.,2012,(413/414):254-260.

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