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首页> 外文期刊>Desalination: The International Journal on the Science and Technology of Desalting and Water Purification >Hydrodynamics and mass transfer simulation of wastewater treatment in membrane reactors
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Hydrodynamics and mass transfer simulation of wastewater treatment in membrane reactors

机译:膜反应器废水处理的流体力学和传质模拟

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摘要

This work presents CFD simulation of hollow-fiber membrane reactors (HFMRs) for separation of ammonia from aqueous solutions. Simulations are carried out to predict ammonia transport in a membrane reactor. Mass transfer and hydrodynamics of the system were investigated through solving conservation equations. The conservation equations solved here were the Navier-Stokes and continuity equations. Finite element analysis was applied for numerical solution of the system equations. UMFPACK was chosen as linear solver and showed good convergence. The influence of effective parameters on the mass transfer and hydrodynamics of the ammonia removal was investigated. Simulation results showed that total flux of ammonia decreases sharply in the region near the membrane inlet. Hydrodynamic investigations also revealed that velocity reached fully developed after a short distance from the reactor entrance. The results of this work confirmed that feed and solvent velocities are the most important parameters in the removal of ammonia. It is also indicated that the numerical procedure is useful and capable to predict the performance of hollow-fiber membrane reactors for separation of ammonia from aqueous solutions.
机译:这项工作提出了用于从水溶液中分离氨的中空纤维膜反应器(HFMR)的CFD模拟。进行模拟以预测膜反应器中氨的迁移。通过求解守恒方程,研究了系统的传质和流体动力学。在这里求解的守恒方程是Navier-Stokes和连续性方程。将有限元分析用于系统方程的数值解。选择UMFPACK作为线性求解器,并显示出良好的收敛性。研究了有效参数对脱氨传质和流体动力学的影响。模拟结果表明,氨气总通量在膜入口附近区域急剧下降。水动力研究还表明,在距反应堆入口一小段距离后,速度就完全达到了极限。这项工作的结果证实,进料速度和溶剂速度是去除氨气中最重要的参数。还表明,该数值程序是有用的,并且能够预测中空纤维膜反应器从水溶液中分离氨的性能。

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