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

机译:非负支持的镍催化剂由镍泡沫制备用于甲烷分解并回收碳沉积的废催化剂

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摘要

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 degrees C. 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.commentSuperscript/Subscript Available/comment
机译:催化甲烷分解(CMD)接受不断提高COX - 无氢和有价值的碳副产物的关注,并且催化剂对甲烷转化和产品特征起到至关重要的作用。通过温和的预处理制备从商业镍泡沫(NF)的不支持镍催化剂。在固定床反应器中的NF形态和CMD反应性探索了预处理方法(酸处理,热处理,酸热处理和氢气还原)和反应温度的影响。发现NF基催化剂的催化性能高度依赖于预处理和反应温度。热和酸热处理可以大大促进催化活性(分别高达74.6%和91.8%)在850℃下促进催化活性。为了充分释放催化剂的潜在能力,将碳沉积的废催化剂再循环为a新鲜催化剂在CMD试验中通过几种策略。通过模拟流化床反应器中的操作模型,可以实现高且稳定的甲烷转化(高达约90%-93%)以进行连续的CMD工艺。此外,碳沉积的废催化剂可以作为超级电容器电极材料的有希望的候选物。 (c)2021氢能出版物LLC。由elestvier有限公司出版。保留所有权利。&评论&上标/下标可用& /评论

著录项

  • 来源
    《International journal of hydrogen energy》 |2021年第42期|21853-21865|共13页
  • 作者单位

    Northwest Univ Sch Chem Engn Minist Educ Adv Use Technol Shanbei Energy Chem Engn Res Ctr Xian 710069 Peoples R China;

    Northwest Univ Sch Chem Engn Minist Educ Adv Use Technol Shanbei Energy Chem Engn Res Ctr Xian 710069 Peoples R China|Ningxia Univ State Key Lab High Efficiency Utilizat Coal & Gre Yinchuan 750021 Ningxia Peoples R China;

    Ningxia Univ State Key Lab High Efficiency Utilizat Coal & Gre Yinchuan 750021 Ningxia Peoples R China;

    Ningxia Univ State Key Lab High Efficiency Utilizat Coal & Gre Yinchuan 750021 Ningxia Peoples R China;

    Northwest Univ Sch Chem Engn Minist Educ Adv Use Technol Shanbei Energy Chem Engn Res Ctr Xian 710069 Peoples R China;

    Northwest Univ Sch Chem Engn Minist Educ Adv Use Technol Shanbei Energy Chem Engn Res Ctr Xian 710069 Peoples R China;

    Northwest Univ Sch Chem Engn Minist Educ Adv Use Technol Shanbei Energy Chem Engn Res Ctr Xian 710069 Peoples R China;

  • 收录信息 美国《科学引文索引》(SCI);美国《工程索引》(EI);美国《生物学医学文摘》(MEDLINE);
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

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

    机译:甲烷分解;镍泡沫;催化剂再循环;超级电容器电极;氢气生产;

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