Hans-Jörg Bart , Ping Ning , Peishi Sun , Wenpiao Song
{"title":"Chemisorptive catalytic oxidation process for SO2 from smelting waste gases by Fe(II)","authors":"Hans-Jörg Bart , Ping Ning , Peishi Sun , Wenpiao Song","doi":"10.1016/S0956-9618(96)00158-0","DOIUrl":null,"url":null,"abstract":"<div><p>Chemisorption of SO<sub>2</sub> from smelting plant exhaust gases in a single sieve plate column was investigated. Main parameters were SO<sub>2</sub> and O<sub>2</sub> gas and H<sub>2</sub>SO<sub>4</sub>, FeSO<sub>4</sub> and Al<sub>2</sub>(SO<sub>4</sub>)<sub>3</sub> liquid concentrations on reaction rate and equilibrium in FeII-EDTA solutions. Absence of inhibitors with this kind of flue gases promote fast kinetics. Optimal process conditions with 3% wt. FeSO<sub>4</sub> catalyst up to 2000 PPM SO<sub>2</sub>. Maximum yield of 16% H<sub>2</sub>SO<sub>4</sub> could be achieved considering optimal liquid/vapor ratio, oxygen surplus and insert salt concentrations.</p></div>","PeriodicalId":101160,"journal":{"name":"Separations Technology","volume":"6 4","pages":"Pages 253-260"},"PeriodicalIF":0.0000,"publicationDate":"1996-10-01","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"https://sci-hub-pdf.com/10.1016/S0956-9618(96)00158-0","citationCount":"2","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"Separations Technology","FirstCategoryId":"1085","ListUrlMain":"https://www.sciencedirect.com/science/article/pii/S0956961896001580","RegionNum":0,"RegionCategory":null,"ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"","JCRName":"","Score":null,"Total":0}
引用次数: 2
Abstract
Chemisorption of SO2 from smelting plant exhaust gases in a single sieve plate column was investigated. Main parameters were SO2 and O2 gas and H2SO4, FeSO4 and Al2(SO4)3 liquid concentrations on reaction rate and equilibrium in FeII-EDTA solutions. Absence of inhibitors with this kind of flue gases promote fast kinetics. Optimal process conditions with 3% wt. FeSO4 catalyst up to 2000 PPM SO2. Maximum yield of 16% H2SO4 could be achieved considering optimal liquid/vapor ratio, oxygen surplus and insert salt concentrations.