Efficient production of propylene and gasoline from methanol in multi-regime riser

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• 作者：Xiaojing Meng ; Huiwen Huang ; Qiang Zhang…
• 关键词：Gasoline ; Methanol ; Multi ; regime Reactor ; PGFM Process ; Propylene
• 刊名：Korean Journal of Chemical Engineering
• 出版年：2016
• 出版时间：April 2016
• 年：2016
• 卷：33
• 期：4
• 页码：1239-1246
• 全文大小：631 KB
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• 作者单位：Xiaojing Meng (1)
  Huiwen Huang (1)
  Qiang Zhang (1)
  Chunyi Li (1)
  Qiukai Cui (2)
  
  1. State Key Laboratory of Heavy Oil Processing, China University of Petroleum (East China), Qingdao, 266555, Shandong, China
  2. Dagang Petrochemical Company, Petro China Corporation, Tianjin, 300280, China
  
• 刊物类别：Chemistry and Materials Science
• 刊物主题：Chemistry
  Industrial Chemistry and Chemical Engineering
  Catalysis
  Materials Science
  Biotechnology
  
• 出版者：Springer New York
• ISSN：1975-7220

文摘

High gas-solid contact efficiency and low solid back-mixing are necessary to both promote methanol conversion and inhibit side reactions. Thus, a novel multi-regime reactor with dense-phase reaction section and dilute-phase conveying region was designed. The reactor promoted stable reaction activity during a 300 h pilot-scale evaluation with high yields of propylene and gasoline. A process for maximum propylene and gasoline production from methanol (PGFM) characterized by moderate operating severity, application of ZSM-11 catalyst and novel reactor, and stratified reprocessing or etherification of light gasoline and C<sub>4sub> olefins was proposed. The PGFM process can be implemented in the existing FCC process and is considered to be more economic and flexible.