Computational Fluid Dynamics–Discrete Element Method Investigation of Pressure Signals and Solid Back-Mixing in a Full-Loop Circulating Fluidized Bed

详细信息    查看全文

• 作者：Kun Luo ; Shuai Wang ; Shiliang Yang ; Chenshu Hu ; Jianren Fan
• 刊名：Industrial & Engineering Chemistry Research
• 出版年：2017
• 出版时间：January 25, 2017
• 年：2017
• 卷：56
• 期：3
• 页码：799-813
• 全文大小：1089K
• ISSN：1520-5045

文摘

Computational fluid dynamics combined with discrete element method is employed to investigate the pressure signals and solid back-mixing behavior in a three-dimensional full-loop circulating fluidized bed operating in fast fluidization (FF) and dilute phase transport (DPT) regimes. The minimum fluidization velocity is successfully predicted after model validation. The gas–solid full-loop hydrodynamics is accurately captured. Pressure signals under different fluidization regimes shed light on the flow dynamics. The wider solid residence time distribution (RTD) curve with a longer tail in the FF regime indicates that solid flow closes to perfect mixing flow, and more severe solid back-mixing is due to solid internal circulation existing in the riser. The smaller solid RTD curve with a short tail in the DPT regime suggests that the solid flow deviates a little from plug flow, and a small-scale solid back-mixing is due to geometry restraint and recirculating gas–solid flow occurring in the lower and upper regions of the riser.