4.7 Article

High efficient thermochemical energy storage of methane reforming with carbon dioxide in cavity reactor with novel catalyst bed under concentrated sun simulator

期刊

RENEWABLE ENERGY
卷 188, 期 -, 页码 361-371

出版社

PERGAMON-ELSEVIER SCIENCE LTD
DOI: 10.1016/j.renene.2022.02.037

关键词

Thermochemical energy storage; Methane reforming; Solar energy; Cavity reactor; Energy utilization efficiency

资金

  1. Natural Science Foundation of Guangdong Province [2017B030308004]
  2. National Natural Science Foundation of China [52036011]

向作者/读者索取更多资源

The thermochemical energy storage performance of methane reforming with carbon dioxide in a cavity reactor under a concentrated sun simulator has been studied both experimentally and numerically. A novel catalyst bed structure with Ni/Al2O3 particles and perforated quartz encapsulation is proposed, which allows for high bed temperature and greenhouse effect, resulting in high chemical energy storage efficiency and total energy utilization efficiency of up to 41.1% and 80.3%, respectively.
Thermochemical energy storage performance of methane reforming with carbon dioxide in cavity reactor under concentrated sun simulator has been experimentally and numerically studied. Novel catalyst bed with Ni/Al2O3 particles and perforated quartz encapsulation is proposed to perform high bed temperature for greenhouse effect, and then chemical energy storage efficiency and total energy utilization efficiency of experimental system can respectively reach as high as 41.1% and 80.3%. As concentrated heat flux increases or reactant flow rate decreases, methane conversion rises with bed temperature increasing, while chemical energy storage efficiency first rises and then falls for larger heat loss. As inlet mole fraction of methane increases, chemical energy storage efficiency firstly increases and then drops. Numerical model of cavity reactor under concentrated heat flux is established and validated. In catalyst bed, maximum reaction rate occurs near focal point, while reverse reaction occurs near its side. With the improvement of porosity in catalyst bed, methane conversion and thermochemical storage efficiency firstly increase and then decrease, while they gradually increase with heat conductivity of bed rising. In addition, optimal concentrated heat flux, flow rate, mole fraction of methane (0.5) and bed porosity (0.6) are derived for maximum chemical energy storage efficiency. (c) 2022 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