Xi Chen , Wenqi Zhong , Shuguang Liu , Theodore J. Heindel
{"title":"流化床喷射的 X 射线计算机断层扫描 (XCT) 研究:测量方法开发和单组分流化","authors":"Xi Chen , Wenqi Zhong , Shuguang Liu , Theodore J. Heindel","doi":"10.1016/j.apt.2024.104681","DOIUrl":null,"url":null,"abstract":"<div><div>Air injected into a fluidized bed through a perforated plate distributor may form individual jets above the distributor plate, which can have a significant impact on the gas–solid flow and heat/mass transfer in the dense phase region. Therefore, it is important to study the jetting characteristics in a fluidized bed, but the measurement of such jets is extremely challenging because of the opaque dense phase region. In this paper, an X-ray computed tomography (XCT) measurement system was constructed, and three-dimensional reconstruction software based on the cone beam filtered back projection algorithm (FDK) was implemented. A jet recognition and quantification algorithm was also developed and tested. Based on these methods, the influence of the jet velocity (<em>U</em><sub>j</sub>) and bed material size (<em>d</em><sub>p</sub>) on the structure and shape of the jets was studied. The results show that when the jet velocity increases, the average jet length (<em>L</em>), jet maximum diameter (<em>D</em>), and jet volume (<em>V</em>) increase, while the average jet half angle (<em>θ</em>) fluctuates around a constant value. Under the same jet velocity (<em>U</em><sub>j</sub>), the average jet length (<em>L</em>), jet maximum diameter (<em>D</em>), and jet volume (<em>V</em>) are inversely proportional to the bed material size (<em>d</em><sub>p</sub>), while the average jet half angle (<em>θ</em>) is directly proportional to the bed material size (<em>d</em><sub>p</sub>). Finally, a correlation for jet length (<em>L</em>) in a fluidized bed is proposed. This study provides a new characterization method for jetting in a fluidized bed, and offers unique experimental data for CFD model validation in fluidized bed simulations.</div></div>","PeriodicalId":7232,"journal":{"name":"Advanced Powder Technology","volume":"35 11","pages":"Article 104681"},"PeriodicalIF":4.2000,"publicationDate":"2024-10-01","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":"{\"title\":\"X-ray computed tomography (XCT) study of jetting in a fluidized bed: Measurement method development and single component fluidization\",\"authors\":\"Xi Chen , Wenqi Zhong , Shuguang Liu , Theodore J. Heindel\",\"doi\":\"10.1016/j.apt.2024.104681\",\"DOIUrl\":null,\"url\":null,\"abstract\":\"<div><div>Air injected into a fluidized bed through a perforated plate distributor may form individual jets above the distributor plate, which can have a significant impact on the gas–solid flow and heat/mass transfer in the dense phase region. Therefore, it is important to study the jetting characteristics in a fluidized bed, but the measurement of such jets is extremely challenging because of the opaque dense phase region. In this paper, an X-ray computed tomography (XCT) measurement system was constructed, and three-dimensional reconstruction software based on the cone beam filtered back projection algorithm (FDK) was implemented. A jet recognition and quantification algorithm was also developed and tested. Based on these methods, the influence of the jet velocity (<em>U</em><sub>j</sub>) and bed material size (<em>d</em><sub>p</sub>) on the structure and shape of the jets was studied. The results show that when the jet velocity increases, the average jet length (<em>L</em>), jet maximum diameter (<em>D</em>), and jet volume (<em>V</em>) increase, while the average jet half angle (<em>θ</em>) fluctuates around a constant value. Under the same jet velocity (<em>U</em><sub>j</sub>), the average jet length (<em>L</em>), jet maximum diameter (<em>D</em>), and jet volume (<em>V</em>) are inversely proportional to the bed material size (<em>d</em><sub>p</sub>), while the average jet half angle (<em>θ</em>) is directly proportional to the bed material size (<em>d</em><sub>p</sub>). Finally, a correlation for jet length (<em>L</em>) in a fluidized bed is proposed. This study provides a new characterization method for jetting in a fluidized bed, and offers unique experimental data for CFD model validation in fluidized bed simulations.</div></div>\",\"PeriodicalId\":7232,\"journal\":{\"name\":\"Advanced Powder Technology\",\"volume\":\"35 11\",\"pages\":\"Article 104681\"},\"PeriodicalIF\":4.2000,\"publicationDate\":\"2024-10-01\",\"publicationTypes\":\"Journal Article\",\"fieldsOfStudy\":null,\"isOpenAccess\":false,\"openAccessPdf\":\"\",\"citationCount\":\"0\",\"resultStr\":null,\"platform\":\"Semanticscholar\",\"paperid\":null,\"PeriodicalName\":\"Advanced Powder Technology\",\"FirstCategoryId\":\"5\",\"ListUrlMain\":\"https://www.sciencedirect.com/science/article/pii/S0921883124003571\",\"RegionNum\":2,\"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":"Advanced Powder Technology","FirstCategoryId":"5","ListUrlMain":"https://www.sciencedirect.com/science/article/pii/S0921883124003571","RegionNum":2,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q2","JCRName":"ENGINEERING, CHEMICAL","Score":null,"Total":0}
X-ray computed tomography (XCT) study of jetting in a fluidized bed: Measurement method development and single component fluidization
Air injected into a fluidized bed through a perforated plate distributor may form individual jets above the distributor plate, which can have a significant impact on the gas–solid flow and heat/mass transfer in the dense phase region. Therefore, it is important to study the jetting characteristics in a fluidized bed, but the measurement of such jets is extremely challenging because of the opaque dense phase region. In this paper, an X-ray computed tomography (XCT) measurement system was constructed, and three-dimensional reconstruction software based on the cone beam filtered back projection algorithm (FDK) was implemented. A jet recognition and quantification algorithm was also developed and tested. Based on these methods, the influence of the jet velocity (Uj) and bed material size (dp) on the structure and shape of the jets was studied. The results show that when the jet velocity increases, the average jet length (L), jet maximum diameter (D), and jet volume (V) increase, while the average jet half angle (θ) fluctuates around a constant value. Under the same jet velocity (Uj), the average jet length (L), jet maximum diameter (D), and jet volume (V) are inversely proportional to the bed material size (dp), while the average jet half angle (θ) is directly proportional to the bed material size (dp). Finally, a correlation for jet length (L) in a fluidized bed is proposed. This study provides a new characterization method for jetting in a fluidized bed, and offers unique experimental data for CFD model validation in fluidized bed simulations.
期刊介绍:
The aim of Advanced Powder Technology is to meet the demand for an international journal that integrates all aspects of science and technology research on powder and particulate materials. The journal fulfills this purpose by publishing original research papers, rapid communications, reviews, and translated articles by prominent researchers worldwide.
The editorial work of Advanced Powder Technology, which was founded as the International Journal of the Society of Powder Technology, Japan, is now shared by distinguished board members, who operate in a unique framework designed to respond to the increasing global demand for articles on not only powder and particles, but also on various materials produced from them.
Advanced Powder Technology covers various areas, but a discussion of powder and particles is required in articles. Topics include: Production of powder and particulate materials in gases and liquids(nanoparticles, fine ceramics, pharmaceuticals, novel functional materials, etc.); Aerosol and colloidal processing; Powder and particle characterization; Dynamics and phenomena; Calculation and simulation (CFD, DEM, Monte Carlo method, population balance, etc.); Measurement and control of powder processes; Particle modification; Comminution; Powder handling and operations (storage, transport, granulation, separation, fluidization, etc.)