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Simulation of micro- and macro-transport in a packed bed of porous adsorbents by lattice Boltzmann methods

机译:格子Boltzmann方法模拟多孔吸附剂填充床中的微观和宏观迁移

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In this study we report 3D simulation of concentration profiles in a fixed bed packed with spherical porous adsorbents using lattice Boltzmann methods (LBMs). The lattice models have been developed to investigate evolution of concentration profiles due to inter- and intra-particle mass transport in an adsorber having small tube-to-sphere diameter (d(t)/d(p)) ratios. The multi-scaling feature of LBMs permits full 3D simulation of concentration profiles both in the bed voids and within the pores of the adsorbents without using any empirical correlations or without making 1D or 2D approximations that are usually made in traditional numerical methods. The model simulation is carried out for varying packing arrangements and small to large pore diffusivities. The simulation results show significant concentration gradients for small pore diffusivities and large particle size, which must be considered in predicting breakthrough and adsorption times for a tubular adsorber having d(t)/d(p) < 10. The model predicted breakthrough curves are validated with the experimental data obtained by tomography technique in a tubular adsorber packed with zeolite particles. (c) 2007 Elsevier Ltd. All rights reserved.
机译:在这项研究中,我们报告了使用格子Boltzmann方法(LBM)在装有球形多孔吸附剂的固定床中进行浓度分布的3D模拟。已经开发出晶格模型以研究由于在具有小管与球直径(d(t)/ d(p))之比的吸附器中由于颗粒间和颗粒内质量传输而引起的浓度分布的演变。 LBM的多标度功能允许对床层空隙和吸附剂孔隙内的浓度分布进行完整的3D模拟,而无需使用任何经验相关性,也无需进行通常采用传统数值方法得出的1D或2D近似值。对不同的填料布置以及小到大的孔扩散率进行了模型仿真。模拟结果表明,对于较小的孔扩散率和较大的粒径,存在明显的浓度梯度,在预测d(t)/ d(p)<10的管状吸附器的穿透时间和吸附时间时必须考虑该浓度梯度。验证了模型预测的穿透曲线层析成像技术在装有沸石颗粒的管状吸附器中获得的实验数据。 (c)2007 Elsevier Ltd.保留所有权利。

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