多孔催化剂制氢氨裂解的数值分析

IF 0.7 Q4 ENGINEERING, MECHANICAL
Si-Hyun Cho, Gyeong-Min Kim, Yoon-Ho Bae, Yongsub Kim, Chung-Hwan Jeon
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引用次数: 0

摘要

氢社会的一个典型技术问题是难以确保氢储存和长途运输的经济效率。为了克服这个问题,需要一种能将氢转化为其他形式化合物的氢载体。特别是氨,在氢载体中具有许多实际优点,作为一种非常合适的物质而受到关注。因此,利用氨气裂解制高纯氢气是必要的。本文建立了氨裂解装置的数值CFD模型。通过数值模型分析了其流动和传热特性。温度分布不均匀会引起氨的局部裂化反应,对制氢过程产生不利影响。该研究可用于设计大型氨裂解装置和高效制氢工艺,为氢储存/运输/利用系统的氢基础设施建设做出贡献。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Numerical Analysis of Ammonia Cracker using Porous Catalyst for Hydrogen Production
A typical technical problem in a hydrogen society is the difficulty of securing the economic efficiency of hydrogen storage and long-distance transportation. To overcome this issue, a hydrogen carrier is needed that can convert hydrogen to other forms of compounds. Ammonia, in particular, has many practical advantages among hydrogen carriers and is drawing attention as a very suitable substance. Therefore, cracking technology using ammonia into high-purity hydrogen is necessary. In this research, a numerical CFD model of ammonia cracker was developed. Flow and heat transfer characteristics were analyzed by numerical model. Non-uniform temperature distribution causes local cracking reaction of ammonia, and adversely affects hydrogen production process. This research can be used to design large-scale ammonia cracker and efficient hydrogen production process and can contribute to build a hydrogen infrastructure for hydrogen storage/transport/utilization system.
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