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ABSORPTION PROCESS IN MgCl_2-NH_3 THERMOCHEMICAL BATTERIES WITH CONSTANT MASS FLOW RATE

机译:恒定流量的MgCl_2-NH_3热化学电池的吸收过程

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The working principle and performance of thermochemical batteries have been studied before [1-3]. In this paper, the performance of a thermochemical battery based on magnesium chloride and ammonia pair with a constant mass flow rate of ammonia gas is studied. It is shown that controlling the mass flow rate lowers the temperature of the reactive complex and increases the duration of the absorption process. However, it was observed that the reaction becomes mass transfer limited which slows the absorption rate and takes control of the reaction away from the mass flow controller. The progress of the reaction inside the reactor is studied in a single-cell reactor to understand the performance of these thermal batteries. It was shown that a reaction zone starts at the inlet and moves toward the end of the reactor. The mass transfer limited reaction zone movement reduces the absorption rate and temperature in the reaction zone.
机译:在[1-3]之前已经研究了热化学电池的工作原理和性能。本文研究了在氨气质量流量恒定的情况下,基于氯化镁和氨对的热化学电池的性能。结果表明,控制质量流量降低了反应性络合物的温度并增加了吸收过程的持续时间。但是,观察到反应受到传质的限制,这减慢了吸收速率并使反应的控制远离质量流量控制器。在单电池反应器中研究了反应器内部反应的进程,以了解这些热电池的性能。结果表明,反应区始于入口,并向反应器末端移动。传质受限的反应区移动降低了反应区的吸收速率和温度。

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