Hydrogen production via two-stage plasma catalytic decomposition of ammonia over Fe/ZSM-5 catalyst

Next Energy Pub Date : 2026-04-01 Epub Date: 2026-03-31 DOI:10.1016/j.nxener.2026.100599
Avik Denra , Shirjana Saud , Duc Ba Nguyen , Quoc Oai Vu , Lan Nguyen , Adnan Ali , Young Sun Mok
{"title":"Hydrogen production via two-stage plasma catalytic decomposition of ammonia over Fe/ZSM-5 catalyst","authors":"Avik Denra ,&nbsp;Shirjana Saud ,&nbsp;Duc Ba Nguyen ,&nbsp;Quoc Oai Vu ,&nbsp;Lan Nguyen ,&nbsp;Adnan Ali ,&nbsp;Young Sun Mok","doi":"10.1016/j.nxener.2026.100599","DOIUrl":null,"url":null,"abstract":"<div><div>This study investigates a 2-stage ammonia (NH<sub>3</sub>) decomposition process using nonthermal gliding arc plasma followed by thermal catalytic cracking. A 2-step catalyst preparation method was implemented, which included the ion-exchange and impregnation methods to achieve more homogeneous deposition of metal species on the zeolite support relative to the single-step impregnation method. The gliding arc discharge was sustained by an alternating current power source at 400 Hz. Plasma process parameters such as flow rate and NH<sub>3</sub> concentration were systematically varied to evaluate their impact on NH<sub>3</sub> conversion and hydrogen (H<sub>2</sub>) production. Results indicated that the optimal conditions for plasma-based H<sub>2</sub> production were achieved at a flow rate of 4.5 L/min and an NH<sub>3</sub> concentration of 11% in nitrogen (N<sub>2</sub>), yielding an H<sub>2</sub> production of 14.5 g/kWh. Further, the thermal catalytic NH<sub>3</sub> decomposition revealed that the catalyst prepared using the combined ion-exchange and impregnation method was superior to those prepared via individual methods. It was observed that although a higher conversion was achieved with the combination of plasma, the energy required was high. Also, the catalyst itself was capable enough at higher temperatures, achieving around 92% conversion at 700 °C. Thus, additional energy used for plasma is not essential at high temperatures, suggesting that the plasma stage can be beneficial at low temperatures or as a preheating stage of the catalyst.</div></div>","PeriodicalId":100957,"journal":{"name":"Next Energy","volume":"11 ","pages":"Article 100599"},"PeriodicalIF":0.0000,"publicationDate":"2026-04-01","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"Next Energy","FirstCategoryId":"1085","ListUrlMain":"https://www.sciencedirect.com/science/article/pii/S2949821X2600089X","RegionNum":0,"RegionCategory":null,"ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"2026/3/31 0:00:00","PubModel":"Epub","JCR":"","JCRName":"","Score":null,"Total":0}
引用次数: 0

Abstract

This study investigates a 2-stage ammonia (NH3) decomposition process using nonthermal gliding arc plasma followed by thermal catalytic cracking. A 2-step catalyst preparation method was implemented, which included the ion-exchange and impregnation methods to achieve more homogeneous deposition of metal species on the zeolite support relative to the single-step impregnation method. The gliding arc discharge was sustained by an alternating current power source at 400 Hz. Plasma process parameters such as flow rate and NH3 concentration were systematically varied to evaluate their impact on NH3 conversion and hydrogen (H2) production. Results indicated that the optimal conditions for plasma-based H2 production were achieved at a flow rate of 4.5 L/min and an NH3 concentration of 11% in nitrogen (N2), yielding an H2 production of 14.5 g/kWh. Further, the thermal catalytic NH3 decomposition revealed that the catalyst prepared using the combined ion-exchange and impregnation method was superior to those prepared via individual methods. It was observed that although a higher conversion was achieved with the combination of plasma, the energy required was high. Also, the catalyst itself was capable enough at higher temperatures, achieving around 92% conversion at 700 °C. Thus, additional energy used for plasma is not essential at high temperatures, suggesting that the plasma stage can be beneficial at low temperatures or as a preheating stage of the catalyst.
Fe/ZSM-5催化剂上两段等离子体催化分解氨制氢
本研究采用非热滑动电弧等离子体进行两阶段氨分解,然后进行热催化裂化。采用离子交换法和浸渍法两步催化剂制备方法,相对于一步浸渍法,实现了金属物质在沸石载体上的均匀沉积。滑动电弧放电由400 Hz的交流电源维持。系统地改变等离子体工艺参数,如流速和NH3浓度,以评估它们对NH3转化和氢气(H2)生成的影响。结果表明,等离子体制氢的最佳条件为:流速为4.5 L/min, NH3浓度为氮气(N2)的11%,产氢量为14.5 g/kWh。此外,热催化NH3分解实验表明,离子交换-浸渍复合法制备的催化剂优于单独法制备的催化剂。据观察,虽然等离子体的组合实现了更高的转换,但所需的能量很高。此外,催化剂本身在更高的温度下也有足够的能力,在700 °C时达到约92%的转化率。因此,在高温下,用于等离子体的额外能量是不必要的,这表明等离子体阶段在低温下或作为催化剂的预热阶段是有益的。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
求助全文
约1分钟内获得全文 求助全文
来源期刊
自引率
0.00%
发文量
0
×
引用
GB/T 7714-2015
复制
MLA
复制
APA
复制
导出至
BibTeX EndNote RefMan NoteFirst NoteExpress
×
提示
您的信息不完整,为了账户安全,请先补充。
现在去补充
×
提示
您因"违规操作"
具体请查看互助需知
我知道了
×
提示
确定
请完成安全验证×
copy
已复制链接
快去分享给好友吧!
我知道了
右上角分享
点击右上角分享
0
联系我们:info@booksci.cn Book学术提供免费学术资源搜索服务,方便国内外学者检索中英文文献。致力于提供最便捷和优质的服务体验。 Copyright © 2023 布克学术 All rights reserved.
京ICP备2023020795号-1
ghs 京公网安备 11010802042870号
Book学术文献互助
Book学术文献互助群
群 号:604180095
Book学术官方微信
小红书