{"title":"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","authors":"Chenyang Wang, Jiankang Wang, Zhijun Li, Zuliang Yang, Lijun Hao, Yiwen Zheng","doi":"10.1002/cjce.25546","DOIUrl":null,"url":null,"abstract":"<p>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 (<i>d</i>), and perforation spacing distance (<i>δ</i>) on segregation scale (<i>S</i>) and pressure drop (<i>Δp</i>) were analyzed using single-factor experiment. The results showed that the perforation structure was helpful to improve the mixing effect. The impact of <i>d</i> on <i>S</i> and <i>Δp</i> was more significant. While increasing <i>d</i> of PSMs, <i>S</i> firstly decreased and then increased. However, <i>Δp</i> monotonously decreased. The impact of <i>δ</i> on <i>S</i> and <i>Δp</i> was smaller. The model of Reynolds number (Re) versus <i>Δp</i> was obtained by fitting and the effect of Re on <i>Δp</i> was significant. In all PSMs, PSM-A with <i>d</i> of 3 mm and <i>δ</i> of 7 mm has the smallest <i>S</i>, that was reduced by 26.2%, compared to the standard Kenics static mixer.</p>","PeriodicalId":9400,"journal":{"name":"Canadian Journal of Chemical Engineering","volume":"103 6","pages":"2953-2964"},"PeriodicalIF":1.6000,"publicationDate":"2024-11-19","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":"{\"title\":\"Study on mixing performance of perforation static mixers applied to high viscosity polymer mixing\",\"authors\":\"Chenyang Wang, Jiankang Wang, Zhijun Li, Zuliang Yang, Lijun Hao, Yiwen Zheng\",\"doi\":\"10.1002/cjce.25546\",\"DOIUrl\":null,\"url\":null,\"abstract\":\"<p>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 (<i>d</i>), and perforation spacing distance (<i>δ</i>) on segregation scale (<i>S</i>) and pressure drop (<i>Δp</i>) were analyzed using single-factor experiment. The results showed that the perforation structure was helpful to improve the mixing effect. The impact of <i>d</i> on <i>S</i> and <i>Δp</i> was more significant. While increasing <i>d</i> of PSMs, <i>S</i> firstly decreased and then increased. However, <i>Δp</i> monotonously decreased. The impact of <i>δ</i> on <i>S</i> and <i>Δp</i> was smaller. The model of Reynolds number (Re) versus <i>Δp</i> was obtained by fitting and the effect of Re on <i>Δp</i> was significant. In all PSMs, PSM-A with <i>d</i> of 3 mm and <i>δ</i> of 7 mm has the smallest <i>S</i>, that was reduced by 26.2%, compared to the standard Kenics static mixer.</p>\",\"PeriodicalId\":9400,\"journal\":{\"name\":\"Canadian Journal of Chemical Engineering\",\"volume\":\"103 6\",\"pages\":\"2953-2964\"},\"PeriodicalIF\":1.6000,\"publicationDate\":\"2024-11-19\",\"publicationTypes\":\"Journal Article\",\"fieldsOfStudy\":null,\"isOpenAccess\":false,\"openAccessPdf\":\"\",\"citationCount\":\"0\",\"resultStr\":null,\"platform\":\"Semanticscholar\",\"paperid\":null,\"PeriodicalName\":\"Canadian Journal of Chemical Engineering\",\"FirstCategoryId\":\"5\",\"ListUrlMain\":\"https://onlinelibrary.wiley.com/doi/10.1002/cjce.25546\",\"RegionNum\":4,\"RegionCategory\":\"工程技术\",\"ArticlePicture\":[],\"TitleCN\":null,\"AbstractTextCN\":null,\"PMCID\":null,\"EPubDate\":\"\",\"PubModel\":\"\",\"JCR\":\"Q3\",\"JCRName\":\"ENGINEERING, CHEMICAL\",\"Score\":null,\"Total\":0}","platform":"Semanticscholar","paperid":null,"PeriodicalName":"Canadian Journal of Chemical Engineering","FirstCategoryId":"5","ListUrlMain":"https://onlinelibrary.wiley.com/doi/10.1002/cjce.25546","RegionNum":4,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q3","JCRName":"ENGINEERING, CHEMICAL","Score":null,"Total":0}
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.
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.