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正己烷催化裂解制低碳烯烃:ZSM-5分子筛催化剂酸性的影响 被引量:2

Catalytic cracking of n-hexane to light olefins:effects of acidity of ZSM-5 catalyst
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摘要 在小型固定床装置上,以ZSM-5分子筛为催化剂,研究不同硅铝物质的量比对合成的ZSM-5分子筛织构性能以及酸性对正己烷催化裂解性能的影响。采用XRD、SEM、N2吸附-脱附和NH3-TPD等方法对不同硅铝物质的量比的ZSM-5分子筛进行表征,结果表明,硅铝物质的量比的改变对ZSM-5分子筛的形貌和结构没有影响;随着硅铝物质的量比的增加,分子筛的酸量减少,酸强度减弱,正己烷催化裂解活性逐渐降低。同时,随着酸量减少和酸强度减弱,高硅ZSM-5分子筛上氢转移反应得到明显抑制,丙烯选择性提高。 Effects of SiO2/Al2O3 molar ratio on textural characteristics and acidity of ZSM-5 zeolite on catalytic cracking of n-hexane to light olefins were investigated in a fixed bed reactor. ZSM-5 zeolites with different SiO2/Al2O3 molar ratio were characterized by XRD, SEM, BET and NH3-TPD. It was found that SiO2/Al2O3 molar ratio had little effect on morphology and structure of synthesized ZSM-5 zeolites. Acidity and strongly acidic sites decreased with increasing SiO2/Al2O3 molar ratio. Correspondingly, activity of the ZSM-5 catalysts for conversion of n-hexane to olefins declined. Hydrogen transfer reactions on the catalysts with higher SiO2/Al2O3 molar ratio were obviously restrained with the decreasing acidity and strongly acidic sites, resulting in high selectivity to propylene.
出处 《工业催化》 CAS 2012年第6期44-48,共5页 Industrial Catalysis
基金 科技部国际科技合作与交流项目(2010DFB40440)
关键词 催化化学 ZSM-5分子筛 己烷催化裂解 丙烯 硅铝比 catalytic chemistry ZSM-5 zeolite hexane catalytic cracking propylene SiO2/Al2O3 ratio
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  • 1徐强,陈丙珍,何小荣,张蕾.石脑油在SRT-IV型工业炉清洁辐射管中裂解的数学模拟[J].计算机与应用化学,2001,18(3):223-228. 被引量:35
  • 2Dancuart L P. Performance of the Sasol SPDTM naphtha as steam cracking feedstock [ J ]. American Chemical Society Division of Petroleum Chemistry,2003,48 (2) :132 -138.
  • 3Depeyre D. Modeling of thermal steam cracking of an atmos- pheric gas oil [ J ]. Industrial & Engineering Chemistry Research, 1989,28 (7) : 967 - 976.
  • 4何海军,韩金兰,王乃计,肖翠微,范玮,苗鹏.Lurgi MTP工艺的技术经济分析[J].煤质技术,2006,21(3):45-47. 被引量:22
  • 5Liebner Waldemar, Rothaemel Martin, Wagner Jens. Greating value from standard natural gas [ J ]. Petroleum technology quarterly ,2003,8(5 ) : 141 - 147.
  • 6Koempel H, Liebner W. Lurgi methanol to propylene (MTP) report on a successful commercialization [ J ]. Studies in Surface Science and Catalysis,2009,167:261 -267.
  • 7Keading W W, Butter S A. Production of chemicals from methanol I. Low molecular weight olefins [ J ]. J Catalysis, 1980,61:155 - 164.
  • 8Dehertog W J H, Froment G F. Production of light alkenes from methanol on ZSM-5 catalysts [ J ]. Applied Catalysis A: General, 1991,71 : 153 - 165.
  • 9Jolly S, Saussey J, Bettahar M M, et al. Reaction mecha- nisms and kinetics in the n-hexane cracking over zeolites [ J ]. Applied Catalysis A : General, 1997,156 ( 1 ) :71 - 96.
  • 10Corrna A, Orchill6s A V. Current views on the mechanism of catalytic cracking [ J ]. Microporous and Mesoporous Materials, 2000, ( 35/36 ) : 21 - 30.

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