蒸汽重整
制氢
热解
废物管理
催化作用
环境科学
农业
氢
化学
工程类
有机化学
生态学
生物
作者
Piyush Pratap Singh,Anurag Jaswal,Ajay Singh,Tarak Mondal
标识
DOI:10.1021/acssuschemeng.3c07519
摘要
Biomass holds significant promise as a renewable feedstock for H2 production. In this study, an integrated biomass pyrolysis and bio-oil catalytic steam reforming approach was explored for hydrogen production from biomass, focusing on a mixture of agricultural crop residues as the feed material. An optimal bio-oil yield of 40.6 wt % was achieved at 450 °C with a heating rate of 10 °C/min during pyrolysis. Using a LaNi0.5Co0.5O3 catalyst, time-on-stream experiments exhibited a stable bio-oil conversion (80%) and average H2 yield (60%) over a 12 h period. Furthermore, FESEM and Raman analysis of the spent catalyst revealed considerable coke formation, which contributed to reduced catalytic activity after 5 h. However, coke was predominantly graphitic in nature, which kept the catalyst active over the entire 12 h period despite significant coke coverage.
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