4.7 Article

Unsupported nickel catalyst prepared from nickel foam for methane decomposition and recycling the carbon deposited spent catalyst

期刊

INTERNATIONAL JOURNAL OF HYDROGEN ENERGY
卷 46, 期 42, 页码 21853-21865

出版社

PERGAMON-ELSEVIER SCIENCE LTD
DOI: 10.1016/j.ijhydene.2021.04.026

关键词

Methane decomposition; Nickel foam; Catalyst recycle; Supercapacitor electrode; Hydrogen production

资金

  1. National Natural Science Foundation of China [21878248]
  2. Young Scitech Nova Project of Shaanxi Province [2020KJXX012]
  3. Natural Science Foundation of Shaanxi Province [2021JLM-22]
  4. Foundation of State Key Laboratory of Highefficiency Utilization of Coal and Green Chemical Engineering [2021K11]

向作者/读者索取更多资源

Catalytic methane decomposition using unsupported nickel catalysts derived from commercial nickel foam shows highly dependent catalytic performance on pre-treatment and reaction temperature. Thermal and acid-thermal treatments can greatly enhance catalytic activity, with methane conversion rates reaching up to 74.6% and 91.8% at 850 degrees Celsius. Recycling carbon deposited spent catalysts can achieve high and stable methane conversion rates, while the spent catalysts can also serve as promising candidates for supercapacitor electrode materials.
Catalytic methane decomposition (CMD) receives increasing attention for co-production of COx-free hydrogen and valuable carbon by-product, and the catalyst plays a crucial role on methane conversion and the product features. Unsupported nickel catalysts derived from commercial nickel foam (NF) were prepared for CMD by mild pre-treatment. Effects of the pre-treatment method (acid treatment, thermal treatment, acid-thermal treatment and hydrogen reduction) and reaction temperature were explored on the NF morphology and CMD reactivity in a fixed-bed reactor. It is found that catalytic performance of the NF-based catalyst is highly dependent on the pre-treatment and reaction temperature. The thermal and acid-thermal treatments could greatly promote the catalytic activity (with methane conversion up to 74.6% and 91.8%, respectively) at 850 C-circle. To fully release potential abilities of the catalyst, the carbon deposited spent catalyst was recycled as a fresh catalyst in the CMD test by several strategies. High and stable methane conversion (up to around 90%-93%) can be achieved by simulating the operation model in a fluidized-bed reactor for a continuous CMD process. Besides, the carbon deposited spent catalyst could serve as a promising candidate of supercapacitor electrode material. (c) 2021 Hydrogen Energy Publications LLC. Published by Elsevier Ltd. All rights reserved.

作者

我是这篇论文的作者
点击您的名字以认领此论文并将其添加到您的个人资料中。

评论

主要评分

4.7
评分不足

次要评分

新颖性
-
重要性
-
科学严谨性
-
评价这篇论文

推荐

暂无数据
暂无数据