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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  2013, Vol. 7 Issue (2): 202-209   https://doi.org/10.1007/s11705-013-1328-3
  RESEARCH ARTICLE 本期目录
Deactivation and regeneration of TS-1/SiO2 catalyst for epoxidation of propylene with hydrogen peroxide in a fixed-bed reactor
Deactivation and regeneration of TS-1/SiO2 catalyst for epoxidation of propylene with hydrogen peroxide in a fixed-bed reactor
Hainan SHI, Yaquan WANG(), Guoqiang WU, Wenping FENG, Yi Lin, Teng ZHANG, Xing JIN, Shuhai WANG, Xiaoxue WU, Pengxu YAO
Key Laboratory for Green Chemical Technology of the Ministry of Education, School of Chemical Engineering & Technology, Tianjin University, Tianjin 300072, China
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Abstract

TS-1/SiO2 catalyst for the epoxidation of propylene with hydrogen peroxide in a fixed-bed reactor has been investigated. The catalyst activity decreases gradually with the online reaction time, but the selectivity of propylene epoxide is kept at about 93%. The fresh, deactivated and regenerated catalysts were characterized with X-ray diffraction, Fourier transform infrared spectroscopy, ultra-violet-visible diffuse reflectance, Brunner-Emmett-Teller method and thermogravimetric analysis, and the deactivated catalyst was regenerated with H2O2/methanol solution. Compared with the fresh catalyst, both the framework structure and the content of titanium in the framework of the deactivated and regenerated TS-1/SiO2 catalysts were not changed. The major reason of the catalyst deactivation was the blockage of the channels of the catalyst by bulky organic by-products, which covered the active centers of titanium in TS-1. The deposited materials on the deactivated TS-1/SiO2 catalyst could be removed by treatment with hydrogen peroxide/methanol solution or pure methanol; the higher the treatment temperature and the higher the concentration of H2O2 in methanol, the higher the extent of the regeneration. The regeneration treatment did not influence the product selectivity in the propylene epoxidation.

Key wordsTS-1/SiO2, epoxidation of propylene, fixed-bed reactor, deactivation    regeneration
收稿日期: 2012-12-05      出版日期: 2013-06-05
Corresponding Author(s): WANG Yaquan,Email:yqwang@tju.edu.cn   
 引用本文:   
. Deactivation and regeneration of TS-1/SiO2 catalyst for epoxidation of propylene with hydrogen peroxide in a fixed-bed reactor[J]. Frontiers of Chemical Science and Engineering, 2013, 7(2): 202-209.
Hainan SHI, Yaquan WANG, Guoqiang WU, Wenping FENG, Yi Lin, Teng ZHANG, Xing JIN, Shuhai WANG, Xiaoxue WU, Pengxu YAO. Deactivation and regeneration of TS-1/SiO2 catalyst for epoxidation of propylene with hydrogen peroxide in a fixed-bed reactor. Front Chem Sci Eng, 2013, 7(2): 202-209.
 链接本文:  
https://academic.hep.com.cn/fcse/CN/10.1007/s11705-013-1328-3
https://academic.hep.com.cn/fcse/CN/Y2013/V7/I2/202
Fig.1  
Fig.2  
Catalyst sampleRelative crystallinity/%I960/I550
Fresh1000.48
Deactivated670.41
Regenerated920.46
Tab.1  
Fig.3  
Fig.4  
CatalystSBET/(m2?g-1)SMicropore/(m2?g-1)Vtatol/(cm3?g-1)VMicropore/(cm3?g-1)
Fresh3212720.4150.353
Deactivated145870.2440.123
Regenerated3022540.4040.342
Tab.2  
Fig.5  
Fig.6  
Fig.7  
Fig.8  
Fig.9  
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