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Biogas reforming for hydrogen-rich syngas production over a Ni-K/Al2O3 catalyst using a temperature-controlled plasma reactor

机译:使用温控等离子体反应器在Ni-K/Al2O3催化剂上生产富氢合成气的沼气重整

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摘要

Plasma-enhanced catalytic biogas reforming for hydrogen-rich syngas production over a Ni-K/Al2O3 catalyst was investigated using a tabular dielectric barrier discharge non-thermal plasma reactor. To better understand the plasma catalysis synergy at elevated tempera-tures, we compared different reaction modes: plasma catalysis, plasma alone, and catal-ysis alone in a reaction temperature range of 160-400 degrees C. The combination of Ni-K/Al2O3 and plasma produced synergistic effects. Notably, the plasma-catalytic synergy was temperature-dependent and varied at different reaction temperatures. Using plasma catalysis, the maximum conversion of CH4 and CO2 (31.6 and 22.8, respectively) was attained over Ni-K/Al2O3 at 160 degrees C, while increasing the reaction temperature to 340 degrees C noticeably enhanced the H2/CO ratio to 2.71. Moreover, compared to plasma-catalytic biogas reforming at 160 degrees C, increasing the reaction temperature to 400 degrees C suppressed biogas conversion with dramatically reduced coke formation on the Ni-K/Al2O3 surface from 6.81 wt to 3.37 wt.(c) 2022 The Author(s). Published by Elsevier Ltd on behalf of Hydrogen Energy Publications LLC. This is an open access article under the CC BY license (http://creativecommons.org/ licenses/by/4.0/).
机译:采用板状介电阻挡放电非热等离子体反应器研究了Ni-K/Al2O3催化剂上等离子体增强催化沼气生产富氢合成气的方法.为了更好地了解在升高温度下的等离子体催化协同作用,我们比较了不同的反应模式:等离子体催化、单独等离子体和单独氧化氢,反应温度范围为160-400°C。Ni-K/Al2O3与等离子体的结合产生了协同效应。值得注意的是,等离子体-催化协同作用与温度有关,并且在不同的反应温度下会发生变化。在等离子体催化下,在160°C下,CH4和CO2的转化率分别为31.6%和22.8%,而将反应温度提高到340°C时,H2/CO比显著提高到2.71。此外,与160°C的等离子体催化沼气重整相比,将反应温度提高到400°C抑制了沼气转化,Ni-K/Al2O3表面的焦炭形成量从6.81 wt%大幅减少到3.37 wt%。(c) 2022 年作者。由Elsevier Ltd代表Hydrogen Energy Publications LLC出版。这是一篇采用 CC BY 许可(http://creativecommons.org/ licenses/by/4.0/)的开放获取文章。

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