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An Eulerian Approach to Computational Fluid Dynamics Simulation of a Chemical-Looping Combustion Reactor With Chemical Reactions

机译:具有化学反应的化学环燃烧反应器的计算流体动力学模拟的欧拉方法

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Chemical-looping combustion (CLC) is a next-generation combustion technology that shows great promise in addressing the need for high-efficiency low-cost carbon capture from fossil fueled power plants. Although there have been a number of experimental studies on CLC in recent years, computational fluid dynamics (CFD) simulations have been limited in the literature. In this paper, simulation of a CLC reactor is conducted using the Eulerian approach in the commercial CFD solver ansys fluent based on a laboratory-scale experiment with a dual fluidized bed CLC reactor. The solid phase consists of a Fe-based oxygen carrier while the gaseous fuel used is syngas. The salient features of the fluidization behavior in the air reactor and fuel reactor beds representing a riser and a bubbling bed, respectively, as well as the down-comer, are accurately captured in the simulation. This work is among the few CFD simulations of a complete circulating dual fluidized bed system for CLC in 3D in the literature. It highlights the importance of 3D simulation of CLC systems and the need for more accurate empirical reaction rate data for future CLC simulations.
机译:化学循环燃烧(CLC)是下一代燃烧技术,在满足从化石燃料发电厂中高效低成本捕集碳的需求方面显示出巨大的希望。尽管近年来已进行了许多有关CLC的实验研究,但文献中对计算流体动力学(CFD)的模拟却非常有限。在本文中,基于实验室规模的双流化床CLC反应器,在商用CFD求解器ansys fluent中使用欧拉方法对CLC反应器进行了仿真。固相由铁基氧气载体组成,而所使用的气态燃料为合成气。在模拟中准确地捕获了分别代表立管和鼓泡床的空气反应器和燃料反应器床中的流化行为的显着特征。这项工作是文献中针对3D CLC的完整循环双流化床系统的少数CFD模拟之一。它强调了CLC系统的3D仿真的重要性,以及对将来的CLC仿真需要更准确的经验反应速率数据的需求。

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