甲烷
催化作用
氢
等离子体
材料科学
制氢
产量(工程)
生物燃料
可再生能源
能量载体
下降(电信)
化学工程
非热等离子体
化学
废物管理
有机化学
冶金
工程类
物理
电气工程
电信
量子力学
计算机科学
作者
Hao‐Yu Lian,Zongshuai Sun,Yun Ru,Jinglin Liu,Xiao‐Song Li,Ai‐Min Zhu
标识
DOI:10.1002/ppap.202300062
摘要
Abstract Toward hydrogen production from renewable sources, coreforming of dilute bioethanol (5 mol% ethanol) and methane using gliding arc discharge warm plasma is reported. For warm plasma alone, increases in methane to ethanol ratio and specific energy input lead to improving hydrogen yield, but low energy efficiency (<60%). The warm plasma coupled with Ni/CeO 2 /Al 2 O 3 catalyst in a heat‐insulation reactor achieves an energy efficiency of 80%, but the large axial‐temperature drop of the catalyst bed causes low conversions. Therefore, additional heating is provided to maintain the catalyst bed temperature. Under optimal conditions, total carbon conversion of 97% and hydrogen yield of 78% are achieved with an energy cost of 1.16 kWh/Nm 3 and energy efficiency of 85%.
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