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Novel phenomenological discrete bubble model of freely bubbling dense gas–solid fluidized beds: Application to two-dimensional beds

机译:自由鼓泡致密气固流化床的新型现象学离散气泡模型:在二维床中的应用

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摘要

A phenomenological discrete bubble model has been developed for freely bubbling dense gas–solid fluidized beds and validated for a pseudo-two-dimensional fluidized bed. In this model, bubbles are treated as distinct elements and their trajectories are tracked by integrating Newton's equation of motion. The effect of bubble–bubble interactions was taken into account via a modification of the bubble velocity. The emulsion phase velocity was obtained as a superposition of the motion induced by individual bubbles, taking into account bubble–bubble interaction. This novel model predicts the bubble size evolution and the pattern of emulsion phase circulation satisfactorily. Moreover, the effects of the superficial gas velocity, bubble–bubble interactions, initial bubble diameter, and the bed aspect ratio have been carefully investigated. The simulation results indicate that bubble–bubble interactions have profound influence on both the bubble and emulsion phase characteristics. Furthermore, this novel model may become a valuable tool in the design and optimization of fluidized-bed reactors. ? 2012 American Institute of Chemical Engineers AIChE J, 2012
机译:已开发出一种现象学离散气泡模型,用于自由鼓泡致密的气固流化床,并已针对伪二维流化床进行了验证。在此模型中,气泡被视为不同的元素,并且通过整合牛顿运动方程来跟踪其轨迹。通过修改气泡速度考虑了气泡与气泡相互作用的影响。考虑到气泡与气泡的相互作用,乳液相速度是由单个气泡引起的运动的叠加而获得的。这个新颖的模型可以令人满意地预测气泡尺寸的演变和乳液相循环的模式。此外,已经仔细研究了表观气体速度,气泡-气泡相互作用,初始气泡直径和床长宽比的影响。模拟结果表明,气泡与气泡的相互作用对气泡和乳剂相的特性都具有深远的影响。此外,这种新颖的模型可能成为流化床反应器设计和优化中的重要工具。 ? 2012美国化学工程师学会AIChE J,2012

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