期刊文献+

Fe-ZSM-5分子筛酸性和Fe离子对苯一步氧化制苯酚反应的影响(英文)

Effects of Acidity and Fe-ions for Benzene to Phenol Oxidation over Fe-ZSM-5 Zeolite
下载PDF
导出
摘要 离子交换法制备的Fe-ZSM-5和K-Fe-ZSM-5分子筛,经不同温度水热处理后作为催化剂应用于N2O为氧化剂的苯一步氧化制取苯酚反应中。实验中,采用XRD、N2-吸附仪、NH3-TPD、27Al MAS NMR、FT-IR、UV-vis和H2-TPR等方法对催化剂进行表征。结果显示:离子交换制备的Fe-ZSM-5分子筛,部分Fe离子以Fe2O3形式负载于分子筛的孔道中。经水热处理,分子筛骨架脱铝导致Brnsted酸性位减少,而Fe2O3离子发生迁移形成活性Fe离子位。在苯一步氧化制苯酚反应中,N2O分子吸附于Fe离子位生成α-O。活性评价结果显示,水热处理前后,催化剂分解N2O性能不变,但苯酚选择性随水热处理温度的升高而逐渐降低。此外,K离子的引入将导致催化剂选择性的降低。 Fe-ZSM-5 and K-Fe-ZSM-5 zeolites were prepared by ion-exchange, followed by hydrothermal treat- ment at different temperature. After characterization by means of XRD, nitrogen adsorption/desorption, NH3-TPD, 27 A1 MAS NMR, FT-IR, UV-vis and H2-TPR, the samples have been investigated as catalysts for the one step oxi- dation of benzene to phenol by N20 as oxidizing agent. The results show that part of Fe2O3 particles are loaded on the surface and the pore of the Fe-ZSM-5 zeolite by ion-exchange. After hydrothermal treatment, Fe-ZSM-5 zeoliteoccurs framework dealumination and Brφnsted acid sites is decreased; The amounts of Fe2O3 particles decrease and iron-ions can be migrates to form highly active Fe^3+ sites. These result in that N20 molecules can be adsorbed on these highly active Fe3^+ sites and decompound to α-O. Before and after hydrothermal treatment, N20 conversion is almost unchanged in one step oxidation of benzene to phenol. Phenol selectivity is gradually increased with increas- ing temperature of hydrothermal treatment. However, the phenol selectivity is decreased because kalium ion is in- troduced into Fe-ZSM-5 zeolite.
出处 《科学技术与工程》 北大核心 2013年第16期4607-4613,共7页 Science Technology and Engineering
关键词 N2O苯 苯酚 Fe-ZSM-5分子筛 水热处理 N20 benzene phenol Fe-ZSM-5 zeolite hydrothermal treatment
  • 相关文献

参考文献9

  • 1Kharitonov A S, Panov G I, Sheveleva G A, et al. Catalysts for pro- duction of phenol and its derivatives. US 5672777. 1997.
  • 2Panov G I. , Uriarte A K, Rodikin M A, et al. Generation of active oxygen species on solid surfaces, opportunity for novel oxidation tech- nologies over zeolites. Catal Today, 1998; 41 (4) : 365-385.
  • 3Burch R, Howitt C. Investigation of zeolite catalysts for the direct partial oxidation of benzene to phenol. Appl Catal A, 1993; 103 ( 1 ) : 135-162.
  • 4Sun K Q, Xia H, Fang Z C. Active sites in Fe/ZSM-5 for nitrous ox- ide decomposition and benzene hydroxylation with nitrous oxide. J Catal, 2008; 254(2): 383-396.
  • 5Piruko L V, Uriarte A K, Chernyavsky V S, et al. Preparation and catalytic study of metal modified TS-1 in the oxidation of benzene to phenol by N20. Micro Meso Mater, 2001; 48(1-3) : 345-353.
  • 6Bordiga S, Buzzoni R, Geobaldo F, et al. Structure and reactivity and reactivity of framework and extraframework iron in Fe-Silicalite as investigated by spectroscopic and physicoehemical methods. J Catal, 1996 ; 158 ( 1 ) : 486-501.
  • 7Schwidder M, Kumar M S, Klementiev K, et al. Selective reduction of NO with Fe-ZSM-5 catalysts of low Fe content : 1. relations between active site structure and catalytic performance. J Catal, 2005; 231 (2) : 314-330.
  • 8Meloni D, Monaci R, Solinas V, et al. Activity and deactivation of Fe-MFI catalysts for benzene hydroxylation to phenol by N20. J Catal, 2003; 214 (2) : 169-178.
  • 9Ivanov D P, Sobolev V I, Panov G I. Deactivation by coking and re- generation of zeolite catalysts for benzene-to-phenol oxidation. Appl Catal A, 2003; 241(1-2) : 113-121.

相关作者

内容加载中请稍等...

相关机构

内容加载中请稍等...

相关主题

内容加载中请稍等...

浏览历史

内容加载中请稍等...
;
使用帮助 返回顶部