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Modeling and numerical simulation of coupled reactive fluidized beds in a Chemical Looping Combustion system

机译:化学循环燃烧系统中耦合反应流化床的建模与数值模拟

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摘要

In this work, reactive unsteady three-dimensional numerical simulations of a Chemical Looping Combustion (CLC) plant are performed. The plant is a 120 kWth pilot working with Ca-Mn-based material as selected oxygen carrier. Numerical simulations are performed by NEPTUNE_CFD code using an Euler-Euler approach which computes both the gas and the solid phases in an Eulerian fashion accounting for specific closures in order to model interphase mass, momentum and energy transfers. Reduction and oxidation heterogeneous (i.e. gas-solid) reactions are modeled by means of a grain model (shrinking core model in the grain) accounting for both the competing mechanisms of chemical reaction at the particle internal surface and gaseous diffusion through the product layer. Results from numerical simulations are validated against experimental measurements and analyzed in order to gain insight in the local behaviour of the reactive gas-particle flow in the CLC system. The theoretical/numerical tool developed in this work will be used for design upgrade recommendation in the stage of scaling-up from pilot to industrial facilities.
机译:在这项工作中,进行了化学循环燃烧(CLC)工厂的反应性非稳态三维数值模拟。该工厂是一个120 kWth的中试工厂,采用Ca-Mn基材料作为选定的氧气载体。通过NEPTUNE_CFD代码使用Euler-Euler方法执行数值模拟,该方法以欧拉方式计算出气相和固相,并考虑了特定的封闭情况,从而为相间质量,动量和能量传递建模。还原和氧化非均相(即气固)反应是通过颗粒模型(颗粒中的收缩核模型)建模的,该模型考虑了颗粒内表面化学反应的竞争机制以及通过产物层的气体扩散。数值模拟的结果针对实验测量值进行了验证,并进行了分析,以了解CLC系统中反应性气体颗粒流的局部行为。这项工作中开发的理论/数值工具将用于从试点规模扩大到工业设施阶段的设计升级建议。

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    Hamidouche Ziad;

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  • 年度 2017
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