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通过自蔓延高温合成法制备用于NH3选择性催化还原NO的粉末状和预制MnO₂-CeO₂-Al₂O₃催化剂

Synthesis of Both Powdered and Preformed MnO -CeO-AlO Catalysts by Self-Propagating High-Temperature Synthesis for the Selective Catalytic Reduction of NO with NH.

作者信息

Wang Chao, Yu Feng, Zhu Mingyuan, Tang Changjin, Dong Lin, Dai Bin

机构信息

Key Laboratory for Green Processing of Chemical Engineering of Xinjiang Bingtuan, School of Chemistry and Chemical Engineering, Key Laboratory of Materials-Oriented Chemical Engineering of Xinjiang Uygur Autonomous Region, and Engineering Research Center of Materials-Oriented Chemical Engineering of Xinjiang Production and Construction Corps, Shihezi University, Shihezi 832003, P. R. China.

Key Laboratory of Mesoscopic Chemistry of Ministry of Education, School of Chemistry and Chemical Engineering, Nanjing University, Nanjing 210093, P. R. China.

出版信息

ACS Omega. 2018 May 28;3(5):5692-5703. doi: 10.1021/acsomega.7b01286. eCollection 2018 May 31.

DOI:10.1021/acsomega.7b01286
PMID:31458769
原文链接:https://pmc.ncbi.nlm.nih.gov/articles/PMC6641950/
Abstract

MnO -CeO-AlO powdered and preformed catalysts were prepared through self-propagating high-temperature synthesis (SHS) and impregnation methods. Compared to the traditional impregnation method, the SHS method has a shorter catalyst preparation cycle and simpler preparation process. The characterization results showed that mixed crystals of cerium, aluminum, and manganese oxides were formed through the SHS method, the binding energy of Mn increased, and the active components were distributed uniformly. The MnO -CeO-AlO powdered catalyst had an extensive pore structure, with a Brunauer-Emmett-Teller surface area of approximately 136 m/g, a pore volume of approximately 0.17 cm/g, and an average pore diameter of approximately 5.1 nm. Furthermore, the MnO -CeO-AlO powdered catalyst achieved a NO conversion higher than 80% at 100-250 °C. Coating liquids with identical metal-ion concentrations were prepared using the catalysts, and the preformed catalyst obtained through the SHS method had a higher loading capacity after one coating. The MnO -CeO-AlO preformed catalyst achieved a NO conversion higher than 70% at 200-350 °C.

摘要

通过自蔓延高温合成(SHS)法和浸渍法制备了MnO₂ -CeO₂-Al₂O₃粉末催化剂和预制催化剂。与传统浸渍法相比,SHS法的催化剂制备周期更短,制备过程更简单。表征结果表明,通过SHS法形成了铈、铝和锰氧化物的混合晶体,Mn的结合能增加,活性组分分布均匀。MnO₂ -CeO₂-Al₂O₃粉末催化剂具有广泛的孔结构,比表面积约为136 m²/g,孔容约为0.17 cm³/g,平均孔径约为5.1 nm。此外,MnO₂ -CeO₂-Al₂O₃粉末催化剂在100-250℃时的NO转化率高于80%。使用这些催化剂制备了金属离子浓度相同的涂层液,通过SHS法得到的预制催化剂在一次涂层后具有更高的负载量。MnO₂ -CeO₂-Al₂O₃预制催化剂在200-

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