大a族粉体直径0.6 m流化床一级旋流器双孔内固体流动研究

IF 1.9 4区 工程技术 Q3 ENGINEERING, CHEMICAL
Jessica Godin, Francisco Sanchez Careaga, Dominic Pjontek, Cedric Briens, Jennifer McMillan
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引用次数: 0

摘要

在大多数工业流化床中,内旋流器使用双填料将固体回收到密集流化床。不良的双重操作会大大增加旋风的颗粒损失。采用直径为0.6 m的大a组颗粒柱进行的实验表明,在流化床内气体流速较低时,气塞通过双孔上升,产生固体脉冲发射;这个问题通过在双腿的底部添加肘部终止来解决。在高气速下,双叠体后退。一个新的模型表明,双管回流是由靠近双管底部的流化床压力波动过大引起的。瞬间,局部床层压力高于双孔内压力,流态化固体从床层流入双孔。因此,对双肘进行了改进:增加了双肘直径和高度,并在双肘上增加了通气和肘端。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Study of solids flow in the dipleg of the primary cyclone of a 0.6 m diameter fluidized bed of a large group A powder

Internal cyclones use diplegs to recycle solids to the dense fluidized bed in most industrial fluidized beds. Poor dipleg operation can greatly increase particle losses from cyclones. Experiments with a 0.6 m diameter column and large group A particles showed that at low gas velocities in the fluidized bed, gas slugs rose through the dipleg, causing the emission of solids pulses; this issue was resolved by adding an elbow termination at the bottom of the dipleg. At high gas velocities, the dipleg backed up. A new model showed that dipleg backup resulted from large pressure fluctuations in the fluidized bed near the bottom of the dipleg. Momentarily, the local bed pressure became higher than the pressure in the dipleg, and fluidized solids flowed from the bed into the dipleg. Consequently, the dipleg was modified: the dipleg diameter and height were increased, and aeration and an elbow termination were added to the dipleg.

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来源期刊
Canadian Journal of Chemical Engineering
Canadian Journal of Chemical Engineering 工程技术-工程:化工
CiteScore
3.60
自引率
14.30%
发文量
448
审稿时长
3.2 months
期刊介绍: The Canadian Journal of Chemical Engineering (CJChE) publishes original research articles, new theoretical interpretation or experimental findings and critical reviews in the science or industrial practice of chemical and biochemical processes. Preference is given to papers having a clearly indicated scope and applicability in any of the following areas: Fluid mechanics, heat and mass transfer, multiphase flows, separations processes, thermodynamics, process systems engineering, reactors and reaction kinetics, catalysis, interfacial phenomena, electrochemical phenomena, bioengineering, minerals processing and natural products and environmental and energy engineering. Papers that merely describe or present a conventional or routine analysis of existing processes will not be considered.
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