中国科学院机构知识库网格
Chinese Academy of Sciences Institutional Repositories Grid
The simultaneous removal of NO and SO2 over MnO2 material via the multi-stage fluidized bed process at low temperatures

文献类型:期刊论文

作者Li, Changming2; Zhang, Xiaoling1; Li, Yunjia1; Sun, Lixin1; Huangfu, Lin3; Li, Jianling1; Gao, Shiqiu1; Yu, Jian1
刊名FUEL
出版日期2023-02-15
卷号334页码:9
关键词Multi-stage fluidized bed MnO2 Denitrification Desulfuration
ISSN号0016-2361
DOI10.1016/j.fuel.2022.126590
英文摘要To overcome the easy poisoning and deactivation of denitrification catalysts by SO2 at low temperatures, the bench-scale multi-stage fluidized bed (MSFB) process with the active MnO2 medium (feeding rate of 0.3-1.2 kg/ h) is designed and applied to simultaneously remove the NO and SO2 from flue gas of medium/small industrial boilers in the low-temperature range of 100 - 200 degrees C, which demonstrates excellent and stable removal efficiency of both NO and SO2 even in the presence of 10 vol% water. In the MSFB system, the fluidized MnO2 particles in different layers flow against the simulated flue gas stage by stage, and the deactivated MnO2 will be continuously discharged and replaced with fresh MnO2 to keep the system effective and steady. The MnO2 medium acts as both denitrification (DeNOx) catalyst and desulfurizer, and the limited backmixing and layered arrangement of the MSFB system ensure the high removal capacity and sufficient utilization of MnO2 material. The multiple structural characterizations further reveal that the active MnO2 is gradually consumed by SO2 to form MnSO4 stage by stage with decreased specific surface and pore volume, accounting for its gradually decreased removal efficiency of both NO and SO2 stage by stage. And the deactivated MnO2 can be easily regenerated by aqueous ammonia with the conversion of MnSO4 to active MnO2. The demonstrated advantages of the MSFB system with MnO2 will provide a promising technical route for the simultaneous removal of NO and SO2 from low-temperature flue gas in industry.
WOS关键词SELECTIVE CATALYTIC-REDUCTION ; FLUE-GAS ; MANGANESE OXIDE ; SULFUR-DIOXIDE ; SCR ; NH3 ; PERFORMANCE ; NH3-SCR ; DESULFURIZATION ; TOLERANCE
资助项目National Natural Science Foundation of China ; Natural Science Foundation of Beijing Municipality ; [21601192] ; [8222042]
WOS研究方向Energy & Fuels ; Engineering
语种英语
WOS记录号WOS:000891442200005
出版者ELSEVIER SCI LTD
资助机构National Natural Science Foundation of China ; Natural Science Foundation of Beijing Municipality
源URL[http://ir.ipe.ac.cn/handle/122111/56012]  
专题中国科学院过程工程研究所
通讯作者Yu, Jian
作者单位1.Chinese Acad Sci, Inst Proc Engn, State Key Lab Multiphase Complex Syst, Beijing 100190, Peoples R China
2.Beijing Technol & Business Univ, Sch Ecol & Environm, State Environm Protect Key Lab Food Chain Pollut C, Beijing 100048, Peoples R China
3.Pangang Grp Res Inst Co Ltd, State Key Lab Vanadium & Titanium Resources Compre, Panzhihua 617000, Peoples R China
推荐引用方式
GB/T 7714
Li, Changming,Zhang, Xiaoling,Li, Yunjia,et al. The simultaneous removal of NO and SO2 over MnO2 material via the multi-stage fluidized bed process at low temperatures[J]. FUEL,2023,334:9.
APA Li, Changming.,Zhang, Xiaoling.,Li, Yunjia.,Sun, Lixin.,Huangfu, Lin.,...&Yu, Jian.(2023).The simultaneous removal of NO and SO2 over MnO2 material via the multi-stage fluidized bed process at low temperatures.FUEL,334,9.
MLA Li, Changming,et al."The simultaneous removal of NO and SO2 over MnO2 material via the multi-stage fluidized bed process at low temperatures".FUEL 334(2023):9.

入库方式: OAI收割

来源:过程工程研究所

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