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A Study On The Dynamic Behavior Of A Sulfur Trioxide Decomposer For A Nuclear Hydrogen Production

机译:三氧化硫分解器用于制氢的动力学行为研究

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The sulfur-iodine thermochemical water-splitting cycle (S-I cycle) is one of the most promising technologies for mass H_2 production. The S-I cycle is generally divided into three sections, one of which involves a H_2SO_4 concentration and decomposition. In the sulfuric acid processing section (Section 2), H_2SO_4 is decomposed into H_2O and SO_3, and then the produced SO_3 is further decomposed into SO_2 and O_2, which takes place in a H_2SO_4 decomposer and a SO_3 decomposer, respectively. The SO_3 decomposition requires heat of a high temperature and this suggests a heat-exchanger type reactor. To understand the temperature profiles and chemical reactions through a SO_3 decomposer, a dynamic model was developed by considering the heat and material balances in partial differential forms. A model was used to size the decomposer to a proposed design basis and it was also applied to simulate the responses corresponding to the changes of the operation conditions such as increased or decreased flow rates.
机译:硫碘热化学水分解循环(S-1循环)是大规模生产H_2的最有希望的技术之一。 S-1循环通常分为三个部分,其中一个涉及H_2SO_4的浓度和分解。在硫酸处理段(第2节)中,H_2SO_4分解为H_2O和SO_3,然后将生成的SO_3进一步分解为SO_2和O_2,这分别在H_2SO_4分解器和SO_3分解器中进行。 SO_3分解需要高温的热,这表明是热交换器型反应器。为了了解通过SO_3分解器的温度曲线和化学反应,通过考虑偏微分形式的热量和物料平衡来建立动态模型。使用一个模型将分解器的大小调整到建议的设计基础,并且还将其用于模拟与操作条件的变化(例如增加或减少的流量)相对应的响应。

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