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Exergy analysis for the Na-O-H (sodium-oxygen-hydrogen) thermochemical water splitting cycle

机译:Na-O-H(钠-氧-氢)热化学水分解循环的火用分析

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Thermochemical water splitting cycles are considered an attractive option to produce H-2, a substance with many important applications for society such as ammonia production because they do not require fossil fuels. In contrast, they obtain H-2 decomposing water by means of cyclic chemical reactions. There are a wide variety of thermochemical ones under research, including the relatively new Na-O-H (sodium-oxygen-hydrogen) cycle proposed in 2012 by a research group. Despite introducing a new potential thermochemical cycle, those previous researchers do not investigate the thermal performance of it. Such task can be done through an exergy analysis. So, the aim of the paper is to evaluate the exergy performance of the Na-O-H cycle and its chemical reactions. This goal is accomplished by implementing in EES (Engineering Equation Solver) software exergy efficiency (epsilon(1)) and exergy destroyed (E-D_1) balances for the cycle and their reactions considering specific conditions of pressure (p) and temperature (T). This approach allows understanding how these two variables influence the system performance, which could compromise its actual implementation and economic feasibility if it has low thermal efficiency. According to the results: reaction 1 (hydrogen production step) has mean epsilon(1) - 96% and E-D_1 = 8.5 kJ under 100-300 degrees C at 0-1 bar; reaction 2 (metal separation step) has E-D_2 = 280 kJ and epsilon(2) = 56% at 450 degrees C considering vacuum condition; hydrolysis step (reaction 3) has average epsilon(3) = 87% and E-D_3 = 18 kJ at 25-200 degrees C under 0-1 bar. Then, the Na-O-H cycle has overall epsilon = 82% and E-D = 306 kJ to produce 1 mol of H-2. These values of and ED are theoretical and maximized ones. In practical situations, such amounts probably will reduce in function of unavoidable irreversibility present in actual systems such as pressure drop and heat loss that were neglected in the work to facilitate its development. Finally, it concludes the Na-O-H cycle has relatively high exergy efficiency, making it a potential hydrogen production method. However, its practical implementation in the future must overcome some of its drawbacks, by means of more research, like the low thermal efficiency of reaction 2 when compared to reactions 1 and 3 beyond the low pressure needed to perform such step. (C) 2020 Hydrogen Energy Publications LLC. Published by Elsevier Ltd. All rights reserved.
机译:热化学分水循环被认为是生产H-2的一种有吸引力的选择,H-2是一种对社会具有许多重要应用的物质,例如氨生产,因为它们不需要化石燃料。相反,它们通过循环化学反应获得分解水的H-2。有多种热化学方法正在研究中,包括一个研究小组在2012年提出的相对较新的Na-O-H(钠-氧-氢)循环。尽管引入了新的潜在热化学循环,但那些先前的研究人员并未研究其热性能。这样的任务可以通过火用分析来完成。因此,本文的目的是评估Na-O-H循环的火用性能及其化学反应。该目标是通过在EES(工程方程求解器)软件中实施循环的本能效率(epsilon(1))和本能破坏的(E-D_1)平衡以及考虑到特定压力条件(p)和温度(T)的反应而实现的。这种方法可以了解这两个变量如何影响系统性能,如果热效率低,则可能会损害其实际实施和经济可行性。根据结果​​:反应1(制氢步骤)在0-1 bar和100-300摄氏度下的平均ε(96)和E-D_1 = 8.5 kJ;考虑到真空条件,在450℃下,反应2(金属分离步骤)的E-D_2 = 280 kJ,ε(2)= 56%;水解步骤(反应3)在0-1 bar和25-200摄氏度下的平均ε(3)= 87%,E-D_3 = 18 kJ。然后,Na-O-H循环的总ε= 82%,E-D = 306 kJ,以产生1 mol H-2。和ED的这些值是理论值和最大值。在实际情况下,这种量可能会降低实际系统中不可避免的不可逆性,例如为了促进其发展而在工作中忽略的压降和热损失。最后,得出结论,Na-O-H循环具有较高的火用效率,使其成为潜在的制氢方法。但是,其未来的实际实施必须通过更多的研究来克服其某些缺点,例如与反应1和3相比,反应2的热效率低,超出了执行此步骤所需的低压。 (C)2020 Hydrogen Energy Publications LLC。由Elsevier Ltd.出版。保留所有权利。

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