Antonello A. Barresi, Stephen L. Hung ∗, Lisa D. Pfefferle
{"title":"Methane combustion in a catalytically stabilized thermal burner","authors":"Antonello A. Barresi, Stephen L. Hung ∗, Lisa D. Pfefferle","doi":"10.1016/0300-9467(92)80019-7","DOIUrl":null,"url":null,"abstract":"<div><p>The chemical role of the catalyst in the catalytically stabilized thermal combustion of methane is investigated; platinum and manganese oxide catalysts were tested. Comparison of the performances of an externally heated catalytic wall tubular reactor and a non-catalytic alumina wall tubular reactor shows that complete conversion of methane is obtained at a slightly higher temperature in the catalytic flow reactor as a consequence of reactant depletion close to the wall due to heterogeneous reactions. However, a highly active catalyst such as platinum changes the selectivity dramatically, almost preventing the production of intermediate compounds and giving high combustion efficiencies.</p></div>","PeriodicalId":101225,"journal":{"name":"The Chemical Engineering Journal","volume":"50 3","pages":"Pages 123-131"},"PeriodicalIF":0.0000,"publicationDate":"1992-12-01","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"https://sci-hub-pdf.com/10.1016/0300-9467(92)80019-7","citationCount":"10","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"The Chemical Engineering Journal","FirstCategoryId":"1085","ListUrlMain":"https://www.sciencedirect.com/science/article/pii/0300946792800197","RegionNum":0,"RegionCategory":null,"ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"","JCRName":"","Score":null,"Total":0}
引用次数: 10
Abstract
The chemical role of the catalyst in the catalytically stabilized thermal combustion of methane is investigated; platinum and manganese oxide catalysts were tested. Comparison of the performances of an externally heated catalytic wall tubular reactor and a non-catalytic alumina wall tubular reactor shows that complete conversion of methane is obtained at a slightly higher temperature in the catalytic flow reactor as a consequence of reactant depletion close to the wall due to heterogeneous reactions. However, a highly active catalyst such as platinum changes the selectivity dramatically, almost preventing the production of intermediate compounds and giving high combustion efficiencies.