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Frontiers of Chemical Science and Engineering

ISSN 2095-0179

ISSN 2095-0187(Online)

CN 11-5981/TQ

邮发代号 80-969

2019 Impact Factor: 3.552

Frontiers of Chemical Science and Engineering  2011, Vol. 5 Issue (1): 79-88   https://doi.org/10.1007/s11705-010-0550-5
  RESEARCH ARTICLE 本期目录
Effect of SiO2/Al2O3 ratio on the conversion of methanol to olefins over molecular sieve catalysts
Effect of SiO2/Al2O3 ratio on the conversion of methanol to olefins over molecular sieve catalysts
Qian WANG1, Lei WANG2, Hui WANG1, Zengxi LI1(), Xiangping ZHANG2, Suojiang ZHANG2(), Kebin ZHOU1
1. Graduate University of Chinese Academy of Sciences, Beijing 100049, China; 2. State Key Laboratory of Multiphase Complex System, Institute of Process Engineering, Chinese Academy of Sciences, Beijing 100190, China
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Abstract

A series of SAPO-34 molecular sieves with different SiO2/Al2O3 ratios have been synthesized for the methanol-to-olefin (MTO) reaction. Their physico-chemical properties are characterized by various techniques such as X-ray diffraction (XRD), scanning electron microscopy (SEM), energy dispersive spectroscopy (EDS), Fourier transform infrared spectroscopy (FT-IR) and N2 adsorption-desorption. The results are compared with those of the commercial HZSM-5, which show that the crystallinity and particle diameter of SAPO-34 as well as HZSM-5 increase with SiO2/Al2O3 ratio. The variation of BET surface area of SAPO-34 is different from that of HZSM-5 and the sample with SiO2/Al2O3 ratio of 0.4 exhibits the highest BET surface area. FT-IR spectra indicate that HZSM-5 has both Br?nsted and Lewis acid sites and Br?nsted acid sites are stronger, whereas SAPO-34 samples are dominated only by Lewis acid sites. When the SiO2/Al2O3 ratio increases, propylene and butylenes become the predominant product of the MTO reaction over HZSM-5. In contrast, the main products of this reaction catalyzed by SAPO-34 are ethylene and propylene. According to the product distribution, the reaction mechanism over HZSM-5 catalysts is proposed.

Key wordsHZSM-5    SAPO-34    methanol-to-olefin (MTO)    SiO2/Al2O3 ratio
收稿日期: 2010-03-28      出版日期: 2011-03-05
Corresponding Author(s): LI Zengxi,Email:zxli@home.ipe.ac.cn; ZHANG Suojiang,Email:sjzhang@home.ipe.ac.cn   
 引用本文:   
. Effect of SiO2/Al2O3 ratio on the conversion of methanol to olefins over molecular sieve catalysts[J]. Frontiers of Chemical Science and Engineering, 2011, 5(1): 79-88.
Qian WANG, Lei WANG, Hui WANG, Zengxi LI, Xiangping ZHANG, Suojiang ZHANG, Kebin ZHOU. Effect of SiO2/Al2O3 ratio on the conversion of methanol to olefins over molecular sieve catalysts. Front Chem Sci Eng, 2011, 5(1): 79-88.
 链接本文:  
https://academic.hep.com.cn/fcse/CN/10.1007/s11705-010-0550-5
https://academic.hep.com.cn/fcse/CN/Y2011/V5/I1/79
Fig.1  
Fig.2  
SiO2/Al2O3 ratio in initial gelSiO2/Al2O3 ratio in product a)BET surface area /(m2·g-1)crystallinity /%crystal size /μm
259.246-65~1
5013.99324275~2
10061.00024690~3
30097.167296100~5
Tab.1  
SiO2/Al2O3 ratio in initial gelproduct composition a)crystallinity /%crystal size /μm
AlSiPSiO2/Al2O3
0.10.5870.0370.3760.03262~2
0.40.5840.0870.3290.07470~4
0.70.5910.0810.3270.06994~5
1.00.6180.0700.3120.057100~7
Tab.2  
Fig.3  
Fig.4  
SiO2/Al2O3 ratiosBET surface area /(m2·g-1)pore volume /(cm3·g-1)pore diameter /nm (BJH method)
0.13390.404.7
0.43530.384.2
0.73210.354.4
1.02800.334.7
Tab.3  
Fig.5  
Fig.6  
Fig.7  
Fig.8  
Fig.9  
Fig.10  
Fig.11  
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