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

IF 4.2 2区 工程技术 Q2 ENGINEERING, CHEMICAL
Xi Chen , Wenqi Zhong , Shuguang Liu , Theodore J. Heindel
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引用次数: 0

摘要

通过穿孔板分配器注入流化床的空气可能会在分配器板上方形成单独的射流,这可能会对稠密相区的气固流动和热量/质量传递产生重大影响。因此,研究流化床中的喷射特性非常重要,但由于稠密相区域不透明,测量这种喷射极具挑战性。本文构建了一套 X 射线计算机断层扫描(XCT)测量系统,并实施了基于锥束滤波背投影算法(FDK)的三维重建软件。此外,还开发并测试了一种射流识别和量化算法。基于这些方法,研究了射流速度(Uj)和床层材料尺寸(dp)对射流结构和形状的影响。结果表明,当射流速度增加时,平均射流长度 (L)、射流最大直径 (D) 和射流体积 (V) 会增加,而平均射流半角 (θ)则围绕一个恒定值波动。在相同的射流速度(Uj)下,平均射流长度(L)、射流最大直径(D)和射流体积(V)与床层材料尺寸(dp)成反比,而平均射流半角(θ)与床层材料尺寸(dp)成正比。最后,还提出了流化床中射流长度(L)的相关性。这项研究为流化床中的喷射提供了一种新的表征方法,并为流化床模拟中的 CFD 模型验证提供了独特的实验数据。
本文章由计算机程序翻译,如有差异,请以英文原文为准。

X-ray computed tomography (XCT) study of jetting in a fluidized bed: Measurement method development and single component fluidization

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.
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来源期刊
Advanced Powder Technology
Advanced Powder Technology 工程技术-工程:化工
CiteScore
9.50
自引率
7.70%
发文量
424
审稿时长
55 days
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.)
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