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甲醇制丙烯过程中ZSM-5催化剂的失活行为 被引量:32

DEACTIVATION OF ZSM-5 CATALYSTS DURING METHANOL-TO-PROPYLENE PROCESS
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摘要 采用IR、TG、低温N2-吸附等手段对用于甲醇制丙烯(MTP)反应的高硅小晶粒ZSM-5催化剂的结焦和失活过程进行研究。结果表明,ZSM-5催化剂具有良好的水热稳定性;分子筛孔道中的可溶性结焦物主要以三甲基苯为主,含量存在一个积累过程,并在48 h达到最大值,随后保持相对稳定;分子筛表面积炭堵塞孔道是导致催化剂失活的主要原因,即积炭量随反应时间延长而持续增加,当其外表面容纳不了更多的积炭时,形成的积炭物质将堵塞沸石孔口,从而使得催化剂在770 h后突然失活。 The coke formation and deactivation process of high silica ZSM-5 catalyst with small particle size used in the reaction of methanol to produce propylene were studied by IR, TG and N2-adsorption techniques. The results showed that the ZSM-5 catalyst was of good hydrothermal stability. The soluble coke in ZSM-5 channels was mainly consisted of three substituted benzenes, which accumulated sharply in the reaction initial period and reached its maximum at reaction time of 48 h and then remained nearly unchanged for the most reaction period. It was the carbon deposition that caused the deactivation of the ZSM-5 catalyst. As the ZSM-5 exterior surface could not accommodate any more carbon coke, the newly formed coke would block the pore of ZSM-5 and subsequently resulted in a sharp deactivation of the catalyst after a long run time of 770 h.
出处 《石油学报(石油加工)》 EI CAS CSCD 北大核心 2008年第4期446-450,共5页 Acta Petrolei Sinica(Petroleum Processing Section)
基金 国家重点基础研究规划"973"项目(2003CB615801)资助
关键词 甲醇 丙烯 ZSM-5 结焦 失活 methanol propylene ZSM-5 coke deactivation
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参考文献12

  • 1瞿勇,胡云光,林衍华.丙烯增产技术开发进展及前景分析[J].石油化工技术经济,2004,20(5):46-51. 被引量:24
  • 2HACK M, KOSS U, KONIG P, et al. Method for producing propylene from methanol: WO 01/92190 Al [P]. 2001-12-06.
  • 3陆铭,孙洪敏,郭燏,杨为民,朱子彬.ZSM-5沸石催化剂的失活历程和活性稳定性[J].石油学报(石油加工),2001,17(4):59-63. 被引量:35
  • 4蒋毅,梁娟,赵素琴.ZnHZSM-5芳构化催化剂积炭影响因素的研究[J].Chinese Journal of Catalysis,1994,15(6):463-467. 被引量:27
  • 5MCLELLAN D, HOWE R F, L PARKER M, et al. Effects of coke formation on the acidity of ZSM-5[J]. J Catal, 1986, 99(2): 486-491.
  • 6HAW J F, NICHOLAS J B, SONG W G, et al. Roles for cyclopentenyl cations in the synthesis of hydrocarbons from methanol on zeolite catalyst HZSM-5 [J]. J AmChemSoe, 2000, 122(19): 4763-4775.
  • 7HAWJ F, SONG W G, MARCUS D M, et al. The mechanism of methanol to hydrocarbon catalysis [J]. Ace Chem Rea, 2003, 36(5): 317-326.
  • 8STOCKER M. Methanol-to-hydrocarbons: Catalytic materials and their behavior[J]. Micropor Mesopor Mater, 1999, 29(1-2) : 3-48.
  • 9LI J, XIONG G, LI C, et al. Coke formation during the methanol conversion to olefins in zeolites studied by UV Raman spectroscopy [ J ]. Microporous Mesoporous Mater, 2000, 39(1-2): 275-280.
  • 10LANGNER B E. Reactions of methanol on zeolites with different pore structures [J]. Appl Catal, 1982, 2 (4-5): 289-302.

二级参考文献14

  • 1蒋毅,梁娟,赵素琴.ZnHZSM-5芳构化催化剂积炭影响因素的研究[J].Chinese Journal of Catalysis,1994,15(6):463-467. 被引量:27
  • 2刘中民,硕士学位论文,1985年
  • 3Schindler Goetz-Peter, Roeper Michael, Stephan Juergen. Method for the Production of Propene. EP 1 379 489 2004- 01- 14.
  • 4田中纯一郎.增产丙烯的Superflex工艺[J].化学工学,2004,67(6):349-349.
  • 5德Erdl Erdgas K6hle,2003,119(2):86.
  • 6Van Egmond Cor. Heat-integrated high pressure system for separation of byproducts from an olefin stream. USA,US 2004 019 246,2004-01- 29.
  • 7孙永生.增产工艺技术助推“丙烯中心”转化[J].中国化工信息,2004,(3).
  • 8Ma'adhad A. , Abul-Hamayel M. Redhwi H, et al. Intergrating Retlning and Petrochemicals Hydrocarbon Engineering, 2003,8(6) :49.
  • 9张婕,沈辉波,刘大壮,张雷,郭新闻,王祥生.GPLE失活模型中的稳态活性[J].高校化学工程学报,1999,13(1):78-81. 被引量:4
  • 10陈标华,林世雄,张吉瑞.β沸石催化剂上二异丙苯与苯反应机理及催化剂失活[J].石油学报(石油加工),1999,15(3):77-82. 被引量:6

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