Ammonia autothermal reformer with air side-stream distribution for hydrogen production

制氢 吸热过程 氨生产 工艺工程 产量(工程) 甲烷转化炉 分解 水煤气变换反应 化学 核工程 热力学 材料科学 蒸汽重整 工程类 物理化学 物理 有机化学 吸附
作者
Jinseong Jang,Myungwan Han
出处
期刊:International Journal of Hydrogen Energy [Elsevier BV]
卷期号:49: 1468-1481 被引量:28
标识
DOI:10.1016/j.ijhydene.2023.09.157
摘要

Recently, there has been growing interest in utilizing ammonia through its decomposition process for on-site hydrogen production, primarily due to technical problems in hydrogen generation and storage. As ammonia decomposition is an endothermic reaction, an external heat source is required to facilitate the reaction. To address this, an ammonia autothermal reforming process that directly integrates ammonia decomposition and oxidation using air as the source of oxygen within a single reactor vessel was proposed. This process eliminates the need for additional external heat sources and simplifies the process. The design of the reactor incorporates an air distribution structure that allows for achieving a specified temperature range for the desired reaction. Thermodynamic analysis of the autothermal system revealed that high feed temperature, high reaction temperature, and low pressure are the most beneficial conditions for generating a high yield of hydrogen. The proposed process was simulated to assess its feasibility using kinetic parameters obtained from experimental data in the literature [27]. An optimization problem to minimize the reactor length in designing the proposed reactor was developed. The reactor design produces a high yield of hydrogen while maintaining the reaction temperature within the desired range. Adjusting the air flow rate at distribution points along the reactor to maintain peak temperatures at predetermined levels was shown to provide good load flexibility for variations in ammonia flow rate.
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