Syngas production from cellulose solid waste by enhanced chemical looping gasification using Ca-Fe bimetallic oxygen carrier with porous structure
文献类型:期刊论文
作者 | Tang, Genyang1,2,3; Gu, Jing1,2; Wei, Guoqiang1,2; Huang, Zhen2; Wu, Jiahuan2,4,5; Yuan, Haoran1,2,3; Chen, Yong1,2,3 |
刊名 | FUEL |
出版日期 | 2022-08-15 |
卷号 | 322页码:12 |
ISSN号 | 0016-2361 |
关键词 | Chemical looping gasification Cellulose solid waste Ca-Fe oxygen carrier Synthesis gas |
DOI | 10.1016/j.fuel.2022.124106 |
通讯作者 | Yuan, Haoran(yuanhr@ms.giec.ac.cn) |
英文摘要 | Chemical looping gasification (CLG) is a promising and innovative technology used to produce synthesis gases without the preparation of gasifying agents, which exhibits advantages in synthesis gas heating value, tar inhibition and production cost Metal Oxide as oxygen carrier (OC) transfers the oxygen and heat in CLG process to avoid product syngas to be mixed with nitrogen, which decides the efficiency and feasibility of CLG system. Ca-Fe bimetallic OCs are considered as the potential available OC for its excellent selectivity on CO and H-2 and char conversion activity. However, the low activity presents great challenges in further application for Ca-Fe OCs. To improve the performance of OCs, Ca-Fe OC with porous structure were prepared with simple method and investigated in a fixed bed with cellulose as fuel combined with various analytical methods. The results reveal that the pore area and pore volume increased significantly with increasing sol pH. The OCs with pH adjustment improved the syngas yield by over 28% and the carbon conversion efficiency by over 10%. Using the sample with pH = 6 as OC, from 800 degrees C to 950 degrees C, the carbon conversion efficiency increased more than 25%, and O/B = 0.5 and S/B = 1.2 should be the most property conditions for cellulose CLG. After 10 redox cycles, the performance of OCs with pH adjustment was better than that without adjustment in steam atmosphere. The improvement of OCs might be due to the higher pore surface area increasing the efficiency of steam reforming and the inner redox cycle of OCs. Therefore, Ca-Fe bimetallic OCs with large surface areas could potentially be used as good candidate oxygen carriers for CLG of cellulose solid waste. |
WOS关键词 | TAR MODEL-COMPOUND ; CALCIUM FERRITE ; BARIUM FERRITE ; REDOX REACTION ; GAS-PRODUCTION ; PYROLYSIS ; OXIDE ; OXIDATION ; REACTIVITY ; CONVERSION |
资助项目 | National Key Research and Development Program of China[2019YFC1906803] ; Key Special Project for Introduced Talents Team of Southern Marine Science and Engineering Guangdong Laboratory (Guangzhou)[GML2019ZD0101] |
WOS研究方向 | Energy & Fuels ; Engineering |
语种 | 英语 |
出版者 | ELSEVIER SCI LTD |
WOS记录号 | WOS:000807712100006 |
资助机构 | National Key Research and Development Program of China ; Key Special Project for Introduced Talents Team of Southern Marine Science and Engineering Guangdong Laboratory (Guangzhou) |
源URL | [http://ir.giec.ac.cn/handle/344007/36781] |
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.Southern Marine Sci & Engn Guangdong Lab Guangzho, Guangzhou 511458, Peoples R China 2.Chinese Acad Sci, Guangzhou Inst Energy Convers, Guangzhou 510640, Peoples R China 3.Univ Chinese Acad Sci, Beijing 100049, Peoples R China 4.Guangdong Prov Key Lab New & Renewable Energy Res, Guangzhou 510640, Peoples R China 5.Shenzhen Gas Corp Ltd, Shenzhen 518000, Peoples R China |
推荐引用方式 GB/T 7714 | Tang, Genyang,Gu, Jing,Wei, Guoqiang,et al. Syngas production from cellulose solid waste by enhanced chemical looping gasification using Ca-Fe bimetallic oxygen carrier with porous structure[J]. FUEL,2022,322:12. |
APA | Tang, Genyang.,Gu, Jing.,Wei, Guoqiang.,Huang, Zhen.,Wu, Jiahuan.,...&Chen, Yong.(2022).Syngas production from cellulose solid waste by enhanced chemical looping gasification using Ca-Fe bimetallic oxygen carrier with porous structure.FUEL,322,12. |
MLA | Tang, Genyang,et al."Syngas production from cellulose solid waste by enhanced chemical looping gasification using Ca-Fe bimetallic oxygen carrier with porous structure".FUEL 322(2022):12. |
入库方式: OAI收割
来源:广州能源研究所
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