Reaction performance and mechanism of a NiO/Ca2Fe2O5 oxygen carrier in Chemical looping gasification of cellulose
文献类型:期刊论文
作者 | Tang, Genyang1,2,3; Gu, Jing2,3; Wei, Guoqiang2,3; Yuan, Haoran1,2,3![]() ![]() |
刊名 | CHEMICAL ENGINEERING JOURNAL
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出版日期 | 2023 |
卷号 | 451页码:16 |
关键词 | Biomass solid waste CLG Cellulose Oxygen carrier |
ISSN号 | 1385-8947 |
DOI | 10.1016/j.cej.2022.137516 |
通讯作者 | Yuan, Haoran(yuanhr@ms.giec.ac.cn) |
英文摘要 | Chemical looping gasification (CLG) is a novel technology created to realize the clean and efficient utilization of solid fuels, where the syngas product avoids dilution by N2 and the pollutants are inhibited by using metal oxide as oxygen carrier (OC) instead of molecular oxygen. Cellulose, as the main component of biomass-based solid waste, was evaluated in the CLG process with NiO/Ca2Fe2O5 prepared by the impregnation method. Reaction mechanism and morphology evolution of the OC as well as the influence of key reaction parameters were investigated by fixed-bed reactor and thermogravimetric analysis experiments coupled with various characterization techniques. The results indicated that the addition of Ni not only improved the oxygen release performance of Ca2Fe2O5 but also helped tar cracking and carbon conversion. On the other hand, the excellent activity in the solid-solid reaction of Ca2Fe2O5 promoted the performance of the Ni-based OC. The test results revealed that Ca2Fe2O5 was a better base than CaFe2O4, and the carbon conversion efficiency reached 98% with the OC sample at 850 degrees C. NiO markedly improved the reactivity of Ca2Fe2O5 after 10 cyclic reactions. The temperature notably affected activity below temperatures of 850 degrees C and slightly above. Due to the limited reduction of Ca2Fe2O5 below 800 degrees C and the redox behavior improvement being minor above 850 degrees C, the temperature of 850 degrees C was marked as the optimum for the studied process Addition of water inhibited OC inactivation in cyclic reactions, which was mainly attributed to the crystal separation and agglomeration of OC particles. However, water inhibited the deep reduction of metal on the surface, which reduced the activity on tar cracking and carbon conversion to a certain extent. |
WOS关键词 | TAR MODEL-COMPOUND ; CAO-BASED CATALYSTS ; BIOMASS TAR ; KINETIC-ANALYSIS ; CALCIUM FERRITE ; BARIUM FERRITE ; REDOX REACTION ; GAS-PRODUCTION ; NICKEL ; CHAR |
资助项目 | Key -Area Research and Develop- ment Program of GuangDong Province[2019B110209003] ; Natural Science Foundation of China[51976223] ; Key Special Project for Introduced Talents Team of Southern Marine Science and Engineering Guangdong Laboratory (Guangzhou)[GML2019ZD0101] ; Guangdong Basic and Applied Basic Research Foundation[2021B1515020068] |
WOS研究方向 | Engineering |
语种 | 英语 |
WOS记录号 | WOS:000862854800004 |
出版者 | ELSEVIER SCIENCE SA |
资助机构 | Key -Area Research and Develop- ment Program of GuangDong Province ; Natural Science Foundation of China ; Key Special Project for Introduced Talents Team of Southern Marine Science and Engineering Guangdong Laboratory (Guangzhou) ; Guangdong Basic and Applied Basic Research Foundation |
源URL | [http://ir.giec.ac.cn/handle/344007/37419] ![]() |
专题 | 中国科学院广州能源研究所 |
通讯作者 | Yuan, Haoran |
作者单位 | 1.Univ Chinese Acad Sci, Beijing 100049, Peoples R China 2.Southern Marine Sci & Engn Guangdong Lab Guangzhou, Guangzhou 511458, Peoples R China 3.Chinese Acad Sci, Guangzhou Inst Energy Convers, Guangzhou 510640, Peoples R China |
推荐引用方式 GB/T 7714 | Tang, Genyang,Gu, Jing,Wei, Guoqiang,et al. Reaction performance and mechanism of a NiO/Ca2Fe2O5 oxygen carrier in Chemical looping gasification of cellulose[J]. CHEMICAL ENGINEERING JOURNAL,2023,451:16. |
APA | Tang, Genyang,Gu, Jing,Wei, Guoqiang,Yuan, Haoran,&Chen, Yong.(2023).Reaction performance and mechanism of a NiO/Ca2Fe2O5 oxygen carrier in Chemical looping gasification of cellulose.CHEMICAL ENGINEERING JOURNAL,451,16. |
MLA | Tang, Genyang,et al."Reaction performance and mechanism of a NiO/Ca2Fe2O5 oxygen carrier in Chemical looping gasification of cellulose".CHEMICAL ENGINEERING JOURNAL 451(2023):16. |
入库方式: OAI收割
来源:广州能源研究所
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