{"title":"结构参数对间接流化床颗粒太阳能接收器中气固流动和气泡特性的影响","authors":"Ziang Zhu , Liyun Zhu , Anjun Li , Zhenbo Wang","doi":"10.1016/j.cherd.2024.10.032","DOIUrl":null,"url":null,"abstract":"<div><div>The two-phase flow and bubble characteristics in Fluidized Bed Particle Solar Receivers (FBPSRs) with varying receiver diameters were numerically investigated by employing the Eulerian-Eulerian framework. Comparisons of solid volume fraction were made between experimental measurements and numerical simulations to validate the accuracy of the numerical model. Subsequently, the effects of receiver diameter on fluidization behavior were studied by considering particle volume fraction, slip velocity, bubbling frequency, bubble size, and bubble dynamics. The results show that a significant reduction was observed in solid holdup at <em>z</em> = 950 mm within narrower tubes. Besides, a consistent pattern of fluidization was evident, characterized by the formation of larger bubbles or slugs in <em>D</em> = 28 mm and 34 mm receivers. The larger diameter receiver restricted the size of the bubbles, leading to increased solid holdup and thus improving the contact between gas and particles. With the decrease of receiver diameter, the dominant frequency became clear. For the bubble dynamics, the bubble time fraction increased with tube diameter, but this trend became less consistent at higher elevations. Additionally, the overall bubble duration time increased with receiver diameter due to lower gas-solid slip velocity. However, a significantly higher bubble duration time was observed at <em>z</em> = 950 mm.</div></div>","PeriodicalId":10019,"journal":{"name":"Chemical Engineering Research & Design","volume":null,"pages":null},"PeriodicalIF":3.7000,"publicationDate":"2024-10-28","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":"{\"title\":\"Effects of structural parameters on gas-solid flow and bubble characteristics in indirect fluidized bed particle solar receivers\",\"authors\":\"Ziang Zhu , Liyun Zhu , Anjun Li , Zhenbo Wang\",\"doi\":\"10.1016/j.cherd.2024.10.032\",\"DOIUrl\":null,\"url\":null,\"abstract\":\"<div><div>The two-phase flow and bubble characteristics in Fluidized Bed Particle Solar Receivers (FBPSRs) with varying receiver diameters were numerically investigated by employing the Eulerian-Eulerian framework. Comparisons of solid volume fraction were made between experimental measurements and numerical simulations to validate the accuracy of the numerical model. Subsequently, the effects of receiver diameter on fluidization behavior were studied by considering particle volume fraction, slip velocity, bubbling frequency, bubble size, and bubble dynamics. The results show that a significant reduction was observed in solid holdup at <em>z</em> = 950 mm within narrower tubes. Besides, a consistent pattern of fluidization was evident, characterized by the formation of larger bubbles or slugs in <em>D</em> = 28 mm and 34 mm receivers. The larger diameter receiver restricted the size of the bubbles, leading to increased solid holdup and thus improving the contact between gas and particles. With the decrease of receiver diameter, the dominant frequency became clear. For the bubble dynamics, the bubble time fraction increased with tube diameter, but this trend became less consistent at higher elevations. Additionally, the overall bubble duration time increased with receiver diameter due to lower gas-solid slip velocity. However, a significantly higher bubble duration time was observed at <em>z</em> = 950 mm.</div></div>\",\"PeriodicalId\":10019,\"journal\":{\"name\":\"Chemical Engineering Research & Design\",\"volume\":null,\"pages\":null},\"PeriodicalIF\":3.7000,\"publicationDate\":\"2024-10-28\",\"publicationTypes\":\"Journal Article\",\"fieldsOfStudy\":null,\"isOpenAccess\":false,\"openAccessPdf\":\"\",\"citationCount\":\"0\",\"resultStr\":null,\"platform\":\"Semanticscholar\",\"paperid\":null,\"PeriodicalName\":\"Chemical Engineering Research & Design\",\"FirstCategoryId\":\"5\",\"ListUrlMain\":\"https://www.sciencedirect.com/science/article/pii/S0263876224006178\",\"RegionNum\":3,\"RegionCategory\":\"工程技术\",\"ArticlePicture\":[],\"TitleCN\":null,\"AbstractTextCN\":null,\"PMCID\":null,\"EPubDate\":\"\",\"PubModel\":\"\",\"JCR\":\"Q2\",\"JCRName\":\"ENGINEERING, CHEMICAL\",\"Score\":null,\"Total\":0}","platform":"Semanticscholar","paperid":null,"PeriodicalName":"Chemical Engineering Research & Design","FirstCategoryId":"5","ListUrlMain":"https://www.sciencedirect.com/science/article/pii/S0263876224006178","RegionNum":3,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q2","JCRName":"ENGINEERING, CHEMICAL","Score":null,"Total":0}
引用次数: 0
摘要
采用欧拉-欧拉框架对不同接收器直径的流化床粒子太阳能接收器(FBPSR)中的两相流和气泡特性进行了数值研究。比较了实验测量和数值模拟的固体体积分数,以验证数值模型的准确性。随后,通过考虑颗粒体积分数、滑移速度、起泡频率、气泡大小和气泡动力学,研究了接收器直径对流化行为的影响。结果表明,在较窄的管道内,z = 950 毫米处的固体截留量明显减少。此外,流化模式也很明显,其特点是在 D = 28 毫米和 34 毫米的接收器中形成较大的气泡或蛞蝓。直径较大的接收器限制了气泡的大小,从而增加了固体吸附力,改善了气体和颗粒之间的接触。随着接收器直径的减小,主导频率逐渐清晰。在气泡动力学方面,气泡时间分数随管道直径的增加而增加,但在海拔较高时,这一趋势变得不那么一致。此外,由于气固滑移速度较低,整体气泡持续时间随接收器直径的增加而增加。不过,在 z = 950 毫米处观察到的气泡持续时间明显较长。
Effects of structural parameters on gas-solid flow and bubble characteristics in indirect fluidized bed particle solar receivers
The two-phase flow and bubble characteristics in Fluidized Bed Particle Solar Receivers (FBPSRs) with varying receiver diameters were numerically investigated by employing the Eulerian-Eulerian framework. Comparisons of solid volume fraction were made between experimental measurements and numerical simulations to validate the accuracy of the numerical model. Subsequently, the effects of receiver diameter on fluidization behavior were studied by considering particle volume fraction, slip velocity, bubbling frequency, bubble size, and bubble dynamics. The results show that a significant reduction was observed in solid holdup at z = 950 mm within narrower tubes. Besides, a consistent pattern of fluidization was evident, characterized by the formation of larger bubbles or slugs in D = 28 mm and 34 mm receivers. The larger diameter receiver restricted the size of the bubbles, leading to increased solid holdup and thus improving the contact between gas and particles. With the decrease of receiver diameter, the dominant frequency became clear. For the bubble dynamics, the bubble time fraction increased with tube diameter, but this trend became less consistent at higher elevations. Additionally, the overall bubble duration time increased with receiver diameter due to lower gas-solid slip velocity. However, a significantly higher bubble duration time was observed at z = 950 mm.
期刊介绍:
ChERD aims to be the principal international journal for publication of high quality, original papers in chemical engineering.
Papers showing how research results can be used in chemical engineering design, and accounts of experimental or theoretical research work bringing new perspectives to established principles, highlighting unsolved problems or indicating directions for future research, are particularly welcome. Contributions that deal with new developments in plant or processes and that can be given quantitative expression are encouraged. The journal is especially interested in papers that extend the boundaries of traditional chemical engineering.