MODELLING DEVELOPMENT OF A RECEIVER-REACTOR OF TYPE R2Mx FOR THERMOCHEMICAL WATER SPLITTING

Estefania Vega Puga, S. Brendelberger, Anika Weber, Christian Sattler
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Abstract

This work reports on the development of a transient heat transfer model for a prototype reactor of type R2Mx for thermochemical water splitting by temperature and pressure swing of ceria. Key aspects of the R2Mx concept, which are also incorporated in the prototype design, include a movable monolithic redox structure combined with a linear transport system, a reduction reactor as well as a dedicated oxidation reactor. With the model, the operation of the prototype is simulated for consecutive water splitting cycles, in which ceria is reduced in a continuously heated reactor, oxidized in a separate oxidation reactor and transported in between the reaction zones. A 2D axisymmetric numerical model of the prototype reactor was developed in ANSYS Mechanical. The model includes heat transfer calculations in combination with an approximated simulation of the transport of the redox material during cyclic operation. It incorporates the chemical reaction by means of a modified heat capacity for ceria and accounts for internal radiation heat transfer inside the porous redox material by applying effective heat transfer properties. A parametric analysis has been undertaken to evaluate different modes of operation of the oxidation reactor. Model results are used to size the power demand of the reduction reactor and vacuum pump, to define durations of the process steps as well as to assess operational parameters with respect to achieved temperatures. Findings suggest that suitable operation of the prototype reactor involves reduction durations ranging from 8 to 10 minutes and oxidations of 6 to 10 minutes.
用于热化学分水的 R2Mx 型接收器-反应器的模型开发
本研究报告介绍了为 R2Mx 型原型反应器开发瞬态传热模型的情况,该反应器用于通过铈的温度和压力变化进行热化学水分离。R2Mx 概念的主要方面也被纳入了原型设计中,包括一个与线性传输系统相结合的可移动整体氧化还原结构、一个还原反应器以及一个专用氧化反应器。利用该模型模拟了原型在连续水分离循环中的运行情况,其中铈在连续加热的反应器中被还原,在单独的氧化反应器中被氧化,并在反应区之间进行传输。在 ANSYS Mechanical 中开发了原型反应器的二维轴对称数值模型。该模型包括传热计算和循环运行期间氧化还原材料运输的近似模拟。该模型通过修改铈的热容量来计算化学反应,并通过应用有效传热特性来计算多孔氧化还原材料内部的辐射传热。通过参数分析,对氧化反应器的不同运行模式进行了评估。模型结果用于确定还原反应器和真空泵的功率需求,确定工艺步骤的持续时间,以及评估与达到的温度有关的运行参数。研究结果表明,原型反应器的适当操作包括 8 至 10 分钟的还原持续时间和 6 至 10 分钟的氧化持续时间。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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