用于高粘度聚合物混合的射孔静态混合器的混合性能研究

IF 1.6 4区 工程技术 Q3 ENGINEERING, CHEMICAL
Chenyang Wang, Jiankang Wang, Zhijun Li, Zuliang Yang, Lijun Hao, Yiwen Zheng
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引用次数: 0

摘要

为了研究穿孔结构对混合器混合性能的影响,采用径向布置、轴向布置和对角布置三种穿孔布置方式对Kenics静态混合器进行了改进。构建了相应的改进静态混合器,命名为PSM-R、PSM-A和PSM-D。利用Polyflow软件模拟了聚合物熔体在其中的流动。通过单因素实验分析了射孔布置、射孔直径(d)和射孔间距(δ)对分离尺度(S)和压降(Δp)的影响。结果表明,孔洞结构有利于提高混合效果。d对S和Δp的影响更为显著。随着psm d的增加,S先减小后增大。而Δp单调下降。δ对S和Δp的影响较小。通过拟合得到雷诺数(Re)与Δp的关系模型,Re对Δp的影响显著。在所有的psm中,d为3 mm和δ为7 mm的PSM-A的S最小,与标准的Kenics静态混合器相比降低了26.2%。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Study on mixing performance of perforation static mixers applied to high viscosity polymer mixing

To investigate the effect of perforation structure on the mixing performance, three kinds of perforation arrangement were used to modify Kenics static mixer, which were radial arrangement, axial arrangement, and diagonal arrangement. The corresponding modified static mixers were constructed and named PSM-R, PSM-A, and PSM-D. The flow of polymer melts inside them were simulated using Polyflow software. The effects of perforation arrangement, perforation diameter (d), and perforation spacing distance (δ) on segregation scale (S) and pressure drop (Δp) were analyzed using single-factor experiment. The results showed that the perforation structure was helpful to improve the mixing effect. The impact of d on S and Δp was more significant. While increasing d of PSMs, S firstly decreased and then increased. However, Δp monotonously decreased. The impact of δ on S and Δp was smaller. The model of Reynolds number (Re) versus Δp was obtained by fitting and the effect of Re on Δp was significant. In all PSMs, PSM-A with d of 3 mm and δ of 7 mm has the smallest S, that was reduced by 26.2%, compared to the standard Kenics static mixer.

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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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