分解
等离子体
核工程
材料科学
环境科学
化学
物理
工程类
核物理学
有机化学
作者
Lin He,Xiao-Ting Yue,xiaoping liu,Zhengwei Wu
标识
DOI:10.1088/1361-6463/ada2f9
摘要
Abstract Low-temperature plasma is recognized as a CO 2 decomposition technology with substantial sustainable potential. Enhancing energy efficiency remains a critical challenge for plasma technology to achieve broader industrial adoption. This study developed two water electrode reactors—one with a stationary water electrode and the other with a flowing water electrode—designed to enhance energy efficiency in the CO 2 decomposition process. A systematic performance comparison was subsequently made with a conventional aluminum mesh electrode reactor. The findings revealed that water electrode reactors significantly enhanced both heat transfer efficiency and power factor, thereby improving CO 2 conversion performance. The stationary water reactor achieved a peak energy efficiency of 20.64%. The effects of input power, inlet flow rate, and N 2 content on DBD plasma performance under high flow rate conditions were also explored in this study. The results indicated that as the input power increased, discharge intensity in all three reactors were intensified, leading to higher CO 2 conversion. However, a portion of the energy was dissipated as heat, which gradually diminished overall energy efficiency. When the feed flow rate increased from 150 sccm to 600 sccm, the shorter residence time resulted in decreased CO 2 conversion, while overall energy efficiency improved significantly. Increasing the N 2 content caused an exponential rise in CO 2 conversion, while the effective conversion rate and energy efficiency did not improve accordingly. Compared to previous studies, this research demonstrates a clear advantage in energy efficiency, offering useful insights for the industrial application of plasma technology in CO 2 decomposition.
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