Enhancing the efficiency of two-stage cyclones without increasing pressure drop by optimizing inlet and outlet dimensions

IF 1.6 4区 工程技术 Q3 ENGINEERING, CHEMICAL Canadian Journal of Chemical Engineering Pub Date : 2024-06-18 DOI:10.1002/cjce.25356
Jiongjie He, Zhenxing Zhu, Hongbin Niu, Zhihong Tian, Jingxuan Yang, Guogang Sun
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Abstract

Efforts to enhance cyclone separators aim to minimize gas energy consumption while improving separation efficiency. This study attempts to achieve this goal for cyclones arranged in series using straightforward methods. Experimental and numerical simulation analyses were performed to study the effect of matching inlet and outlet diameters on the performance of a two-stage tandem cyclone separator. The results show that the matching method, in which the inlet gas velocities of both stages are higher than the outlet gas velocity, has a better separation efficiency. The efficiency and pressure drop models of the two-stage cyclones in series were constructed using the response surface methodology (RSM) to obtain the optimal combination of inlet size and exhaust pipe diameter. Experimental tests showed that the accuracy of this model was reasonable. At different permitted pressure drops, the optimized structure revealed that: (1) The inlet area should be smaller than the outlet area for each cyclone stage. (2) The secondary inlet size (KA) should be as large as possible. (3) dr decreases while KA increases in each step.

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通过优化入口和出口尺寸,在不增加压降的情况下提高两级旋风分离器的效率
改进旋风分离器的努力旨在最大限度地减少气体能耗,同时提高分离效率。本研究试图通过简单的方法来实现串联旋风分离器的这一目标。通过实验和数值模拟分析,研究了入口和出口直径匹配对两级串联旋风分离器性能的影响。结果表明,两级旋风分离器的入口气流速度均高于出口气流速度的匹配方法具有更好的分离效率。利用响应面法(RSM)构建了串联双级旋风分离器的效率和压降模型,从而获得了进气口尺寸和排气管直径的最佳组合。实验测试表明,该模型的精度是合理的。在不同的允许压降条件下,优化结构表明(1) 每级旋风分离器的入口面积应小于出口面积。(2) 二级入口尺寸(KA)应尽可能大。(3) 每级 KA 增大,而 dr 减小。
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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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