{"title":"Characteristics of integral plasma-fluidized bed and preparation of Mo-based catalysts for sulfur-resistant methanation","authors":"Baowei Wang, Jiangzhou Kong, Xiaoyan Li","doi":"10.1007/s11144-024-02735-6","DOIUrl":null,"url":null,"abstract":"<div><p>Integral plasma fluidized bed reactors were designed for catalyst preparation. Fluidization characteristics and discharge performance were investigated. Results indicated that a bed height of 30 mm and a gas velocity of 0.10–0.18 m/s were obtained a better fluidization effect. Input power 8 W could make the discharge more stable in the double dielectric barrier discharge (DDBD) fluidized bed reactor. The preparation of 20% Mo/Al<sub>2</sub>O<sub>3</sub> sulfur-resistant methanation catalysts was treated with DDBD fluidized bed reactor. Plasma time treatment was investigated. The highest CO conversion was obtained for a plasma treatment time of 30 min. The highest methane yield was obtained for a 60 min catalyst. The catalyst components were found to be uniformly dispersed in the form of ammonium molybdate on an Al<sub>2</sub>O<sub>3</sub> carrier based on N<sub>2</sub> physisorption-desorption, XRD, TGA, Raman, TEM and TPR characterization. This suggests that the DBD fluidized bed may provide a novel route for catalyst preparation.</p></div>","PeriodicalId":750,"journal":{"name":"Reaction Kinetics, Mechanisms and Catalysis","volume":"138 1","pages":"285 - 302"},"PeriodicalIF":1.7000,"publicationDate":"2024-10-21","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"Reaction Kinetics, Mechanisms and Catalysis","FirstCategoryId":"92","ListUrlMain":"https://link.springer.com/article/10.1007/s11144-024-02735-6","RegionNum":4,"RegionCategory":"化学","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q4","JCRName":"CHEMISTRY, PHYSICAL","Score":null,"Total":0}
引用次数: 0
Abstract
Integral plasma fluidized bed reactors were designed for catalyst preparation. Fluidization characteristics and discharge performance were investigated. Results indicated that a bed height of 30 mm and a gas velocity of 0.10–0.18 m/s were obtained a better fluidization effect. Input power 8 W could make the discharge more stable in the double dielectric barrier discharge (DDBD) fluidized bed reactor. The preparation of 20% Mo/Al2O3 sulfur-resistant methanation catalysts was treated with DDBD fluidized bed reactor. Plasma time treatment was investigated. The highest CO conversion was obtained for a plasma treatment time of 30 min. The highest methane yield was obtained for a 60 min catalyst. The catalyst components were found to be uniformly dispersed in the form of ammonium molybdate on an Al2O3 carrier based on N2 physisorption-desorption, XRD, TGA, Raman, TEM and TPR characterization. This suggests that the DBD fluidized bed may provide a novel route for catalyst preparation.
期刊介绍:
Reaction Kinetics, Mechanisms and Catalysis is a medium for original contributions in the following fields:
-kinetics of homogeneous reactions in gas, liquid and solid phase;
-Homogeneous catalysis;
-Heterogeneous catalysis;
-Adsorption in heterogeneous catalysis;
-Transport processes related to reaction kinetics and catalysis;
-Preparation and study of catalysts;
-Reactors and apparatus.
Reaction Kinetics, Mechanisms and Catalysis was formerly published under the title Reaction Kinetics and Catalysis Letters.