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Experimental study and numerical simulation of baffled bubbling fluidized beds with Geldart A particles in three dimensions

机译:三维Geldart A颗粒挡板鼓泡流化床的实验研究与数值模拟。

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In this study, a new method was developed to simulate the flow characteristics of Geldart A particles in the bubbling fluidized beds with perforated plates by the modified structure-based drag model. In this approach, the baffle was considered as a gas distributor and the baffled bubbling fluidized bed was divided into several sections which were treated as a series of freely bubbling fluidized beds. These freely bubbling fluidized beds were simulated by the structure-based drag model. Due to the structure difference between the baffle and the distributor, the empirical correlation of the initial bubble diameter in the structure-based drag model was modified to adapt the simulation of these freely bubbling fluidized beds. By this modification, the bubbling fluidization behavior and the bed expansion in a bubbling fluidized bed with perforated plates can be correctly predicted. The simulation results showed good agreements with the experimental data of the radial and axial solid volume fraction distributions and the axial pressure distribution. The phenomenon that baffles restrained back-mixing of particles was captured in the solid circulation pattern as well.
机译:在这项研究中,通过改进的基于结构的阻力模型,开发了一种新方法来模拟Geldart A颗粒在带孔板的鼓泡流化床中的流动特性。在这种方法中,折流板被认为是气体分配器,折流板的鼓泡流化床被分成几个部分,被视为一系列的自由鼓泡的流化床。这些自由鼓泡的流化床是通过基于结构的阻力模型进行模拟的。由于挡板和分配器之间的结构差异,修改了基于结构的阻力模型中初始气泡直径的经验相关性,以适应这些自由鼓泡流化床的模拟。通过该修改,可以正确地预测具有穿孔板的鼓泡流化床中的鼓泡流化行为和床膨胀。模拟结果与径向和轴向固体体积分数分布以及轴向压力分布的实验数据吻合良好。挡板抑制颗粒回混的现象也以固体循环模式被捕获。

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