甲烷
镍
部分氧化
化学链燃烧
合成气
氧气
非阻塞I/O
化学反应
无机化学
甲烷厌氧氧化
催化作用
化学工程
化学
工程类
有机化学
作者
Rui Liu,Xianhua Zhang,Tao Liu,Yao Xian,Zhi‐Jian Zhao,Chunlei Pei,Jinlong Gong
标识
DOI:10.1016/j.apcatb.2023.122478
摘要
The oxygen species over oxygen carriers determine the reaction performance in chemical looping partial oxidation of methane (CLPOM). This paper describes the dynamic migration and reaction of oxygen species over ceria-supported NiO oxygen carrier for CLPOM. At initial reaction stage, Ni-O species could be consumed rapidly and cause the full oxidation of methane to CO2. Afterwards, the active Ni-O-Ce species dominates the methane partial oxidation to promote the syngas yield. It is found that CO formation rate is linearly related with the content of oxygen species over Ni-O-Ce. Furthermore, the lattice oxygen from CeO2 would migrate through the bulk to complement the consumed Ni-O-Ce oxygen species. Eventually, 5NiO/(40CeO2-Al2O3) exhibit nearly three times as high as methane reaction rate of CeO2/Al2O3 and two times as high as CO formation rate of 5NiO/Al2O3. This work provides the comprehensive understanding of transport and reaction mechanism of oxygen species for chemical looping processes.
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