Developments in the understanding of gas-solid contact efficiency in the circulating fluidized bed riser reactor: A review

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• 作者：Chengxiu Wang¹ ; Jesse Zhu¹ ; ² ; ^{jzhu@uwo.ca" class="auth_mail" title="E-mail the corresponding author}
• 关键词：Circulating fluidized bed ; Riser ; High density ; Gas&ndash ; solid contacting ; Heat transfer ; Ozone decomposition
• 刊名：Chinese Journal of Chemical Engineering
• 出版年：2016
• 出版时间：January 2016
• 年：2016
• 卷：24
• 期：1
• 页码：53-62
• 全文大小：1408 K

文摘

In the last several decades, circulating fluidized bed reactors have been studied in many aspects including hydrodynamics, heat and mass transfer and gas–solid two phase contacting. However, despite the abundance of review papers on hydrodynamics, there is no summary paper on gas–solid contact efficiency to date, especially on high density circulating fluidized beds (CFBs). This paper gives an introduction to, and a review of the measurement of contact efficiency in circulating fluidized bed riser. Firstly, the popular testing method of contact efficiency including the method of heating transfer experiment and hot model reaction are discussed, then previous published papers are reviewed based on the discussed methods. Some key results of the experimental work are described and discussed. Gas–solid contact efficiency is affected by the operating conditions as well as the particle size distribution. The result of the contact efficiency shows that the CFB riser is far away from an ideal plug flow reactor due to the characteristics of hydrodynamics in the riser. Lacunae in the available literature have been delineated and recommendations have been made for further work.