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Hydrodynamics and flow structure, gas and solids mixing behavior, and choking phenomena in gas-solid fluidization.

机译:气固流化过程中的流体动力学和流动结构,气固混合行为以及窒息现象。

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摘要

In this study, the dynamic flow behavior and gas and solids mixing behavior in the turbulent fluidized beds are investigated by using Electrical Capacitance Tomography (ECT) technique and tracer technique.; The ECT study reveals that the time-averaged solids holdup distribution exhibits radial symmetry in the turbulent regime, which is not the case for the bubbling regime. The standard deviations of the fluctuations of the cross-sectional averaged bubble/void phase fraction, and the cross-sectional averaged solids holdups in the bubble/void phase and in the emulsion phase, all peak at the transition velocity from the bubbling to the turbulent regimes, U c. The addition of 10% fine particles decreases the solids concentration in the emulsion phase due to the breakup of the large bubbles. The bubble/void phase fraction does not vary with bed temperature up to 400°C; the emulsion phase voidage is observed to increase as the bed temperature increases. More than one spiral motion of bubble swarms is observed in the bubbling regime for the 0.3 m ID fluidized bed. The transition velocity, Uc, decreases with increasing bed diameter. The gas and solids mixing behavior varies significantly with the flow regimes. The temperature and pressure are found to have little effect on the gas and solids mixing behavior. A small quantity of fine particles is noted to drastically affect the gas and solids mixing behavior in the turbulent fluidized bed.; The term "choking" commonly refers to a gas-solid fluidization phenomenon in which a small change in gas or solids flow rate prompts a large change in the hydrodynamic behavior such as the pressure drop or solids holdup during the gas-solid flow. In this study, the flow structure variations during the regime transition and the choking phenomenon in a 0.05 m ID pneumatic conveying system and a 0.1 m ID circulating fluidized bed for both Group A and Group B particles are examined by utilizing the Electric Capacitance Tomography (ECT). The criterion for the occurrence of choking transition in a circulating fluidized bed for both Group A and Group B particles is given.; In summary, a systematic study has been conducted to investigate the dynamic flow behavior and gas and solids mixing behavior in the turbulent fluidized beds under different operating conditions. The choking phenomenon and the regime transition in the circulating fluidized beds are discerned from the viewpoints of flow structure variations obtained by the ECT technique. It establishes a comprehensive database and provides profound understanding on the dynamic flow behavior of the complex gas-solid two-phase flow systems. (Abstract shortened by UMI.)
机译:在这项研究中,利用电容层析成像(ECT)技术和示踪技术研究了湍流化床中的动态流动行为以及气体和固体的混合行为。 ECT研究表明,在湍流状态下,时间平均固体滞留率分布呈现出径向对称性,而在鼓泡状态下则并非如此。气泡/空隙相和乳液相中的横截面平均气泡/空隙相分数的波动的标准偏差以及横截面平均固体含量的标准偏差均在从鼓泡到湍流的转变速度处达到峰值政权由于大气泡的破裂,添加10%的细颗粒降低了乳液相中的固体浓度。气泡/空隙相分数不会随床温升高至400°C而变化;观察到乳液相空隙率随着床温的升高而增加。对于0.3 m ID的流化床,在鼓泡状态下观察到了多个气泡群的螺旋运动。过渡速度Uc随着床层直径的增加而减小。气体和固体的混合行为随流动方式而显着变化。发现温度和压力对气体和固体的混合行为几乎没有影响。注意到少量细颗粒会极大地影响湍流床中气体和固体的混合行为。术语“窒息”通常是指一种气固流化现象,其中气体或固体流速的微小变化会促使流体力学行为发生较大变化,例如在气固流动期间的压降或固体滞留。在这项研究中,通过使用电容层析成像技术(ECT)检查了0.05 m ID的气动输送系统和0.1 m ID的A组和B组颗粒的循环流化床中状态过渡期间的流动结构变化和窒息现象。 )。给出了A组和B组颗粒在循环流化床中发生窒息转变的标准。总之,已经进行了系统的研究,以研究在不同操作条件下在湍流化床中的动态流动行为以及气体和固体的混合行为。从通过ECT技术获得的流动结构变化的观点,识别出循环流化床中的窒息现象和状态转变。它建立了一个全面的数据库,并对复杂的气固两相流系统的动态流动行为提供了深刻的了解。 (摘要由UMI缩短。)

著录项

  • 作者

    Du, Bing.;

  • 作者单位

    The Ohio State University.;

  • 授予单位 The Ohio State University.;
  • 学科 Engineering Chemical.
  • 学位 Ph.D.
  • 年度 2005
  • 页码 361 p.
  • 总页数 361
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类 化工过程(物理过程及物理化学过程);
  • 关键词

  • 入库时间 2022-08-17 11:41:50

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