Catalytic performance of CuO/HZSM-5 in aromatic synthesis from CH3Br

被引:0
|
作者
Chen T. [1 ]
Chen H. [2 ]
Fu J. [2 ]
Chen K. [1 ]
Ouyang P. [1 ,2 ]
机构
[1] Biotechnology and Pharmaceutical Engineering, Nanjing Tech University, Nanjing, 211800, Jiangsu
[2] Key Laboratory of Biomass Chemical Engineering of Ministry of Education, College of Chemical and Biological Engineering, Zhejiang University, Hangzhou, 310027, Zhejiang
来源
Fu, Jie (iefu@zju.edu.cn) | 1600年 / Materials China卷 / 68期
基金
中国国家自然科学基金;
关键词
Aromatic; Catalysis; CH[!sub]3[!/sub]Br; CuO/HZSM-5; Fixed-bed; Stability;
D O I
10.11949/j.issn.0438-1157.20161659
中图分类号
学科分类号
摘要
CuO/HZSM-5 catalysts with 1%-7% CuO loading, which were prepared by incipient wetness impregnation, were used to study catalytic performance in the conversion of CH3Br to aromatic compounds in a fixed-bed reactor by changing temperature, CH3Br flow rate and CuO loading. Fresh and used catalysts were characterized by SEM, TEM, XRD, XPS, TG, DSC, N2 adsorption and desorption, and NH3-TPD. XRD results showed that CuO was highly dispersed on HZSM-5 and structure of CuO crystals did not change during reaction. NH3-TPD results showed that 3% (mass) CuO loading increased strong acidity of catalyst. XPS results showed that coke deposition on used CuO/HZSM-5 catalyst was mainly graphite. The highest aromatic yield of 22.3% was achieved at condition of 3% (mass) CuO loading, 360℃ temperature and 240 ml·g-1·h-1 GHSV. The 3% (mass) CuO/HZSM-5 maintained stable catalytic activity within 40 h reaction time. © All Right Reserved.
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页码:2344 / 2351
页数:7
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共 30 条
  • [1] Zhang D.Z., Wei Y.X., Shen J.H., Et al., Chloromethane conversion over Mg modified ZSM-5 zeolite catalysts, Natural Gas Chemical Industry, 31, 3, pp. 14-17, (2006)
  • [2] Chen Q.L., Qian B.Z., Current situation of nature gas chemical industry, Modern Chemical Industry, 22, 5, pp. 1-4, (2002)
  • [3] Sousa-Aguiar E.F., Appel L.G., Mota C., Natural gas chemical transformations: the path to refining in the future, Catalysis Today, 101, 1, pp. 3-7, (2005)
  • [4] Holmen A., Olsvik O., Rokstad O.A., Pyrolysis of nature gas: chemistry and process concepts, Fuel Processing Technology, 42, 2-3, pp. 249-267, (1995)
  • [5] Holmen A., Rokstad O.A., Solbakken A., High-temperature pyrolysis of hydrocarbons(I): Methane to acetylene, Industrial & Engineering Chemistry Process Design & Development, 15, 3, pp. 439-444, (1976)
  • [6] Liu R.S., Iwamoto M., Lunsford J.H., Partial oxidation of methane by nitrous oxide over molybdenum oxide supported on silica, Journal of the Chemical Society, Chemical Communications, 1, 1, pp. 78-79, (1982)
  • [7] Yong R.S., Tan B., Wang K., Progress in the technologies for production of chemicals from natural gas and development opportunity, Natural Gas Chemical Industry, 34, 4, pp. 70-75, (2009)
  • [8] Bai E.Z., Economics and prospects of FT synfuels, Chemical Industry and Engineering Progress, 23, 4, pp. 370-374, (2004)
  • [9] Chen J.G., Xiang H.W., Li Y.W., Et al., Advance in key techniques of Fischer-Tropsch synthesis for liquid fuel production, Journal of Chemical Industry and Engineering(China), 54, 4, pp. 516-523, (2003)
  • [10] Xia X.R., Bi Y.L., Wu T.H., Et al., An infrared spectroscopic study of the mechanism of chloromethane conversion to higher hydrocarbons on HZSM-5 catalyst, Catalysis Letters, 33, 1, pp. 75-90, (1995)