{"title":"槽式电解槽叶栅性能及优化研究","authors":"Thomas Z. Fahidy","doi":"10.1016/0300-9467(92)80014-2","DOIUrl":null,"url":null,"abstract":"<div><p>The effect of the imposed cell voltage policy on reactant-to-product conversion and the optimal number of elements in a CSTER cascade was analysed in terms of various costs associated with its operation. Optimal operation may be feasible with a single tank or with several tanks in series, according to the relative magnitude of governing costs. Operation with the same voltage imposition on each element is also compared with operation with a non-uniform voltage distribution.</p></div>","PeriodicalId":101225,"journal":{"name":"The Chemical Engineering Journal","volume":"50 2","pages":"Pages 109-113"},"PeriodicalIF":0.0000,"publicationDate":"1992-11-01","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"https://sci-hub-pdf.com/10.1016/0300-9467(92)80014-2","citationCount":"0","resultStr":"{\"title\":\"A study of performance and optimization of tank-electrolyser cascades\",\"authors\":\"Thomas Z. Fahidy\",\"doi\":\"10.1016/0300-9467(92)80014-2\",\"DOIUrl\":null,\"url\":null,\"abstract\":\"<div><p>The effect of the imposed cell voltage policy on reactant-to-product conversion and the optimal number of elements in a CSTER cascade was analysed in terms of various costs associated with its operation. Optimal operation may be feasible with a single tank or with several tanks in series, according to the relative magnitude of governing costs. Operation with the same voltage imposition on each element is also compared with operation with a non-uniform voltage distribution.</p></div>\",\"PeriodicalId\":101225,\"journal\":{\"name\":\"The Chemical Engineering Journal\",\"volume\":\"50 2\",\"pages\":\"Pages 109-113\"},\"PeriodicalIF\":0.0000,\"publicationDate\":\"1992-11-01\",\"publicationTypes\":\"Journal Article\",\"fieldsOfStudy\":null,\"isOpenAccess\":false,\"openAccessPdf\":\"https://sci-hub-pdf.com/10.1016/0300-9467(92)80014-2\",\"citationCount\":\"0\",\"resultStr\":null,\"platform\":\"Semanticscholar\",\"paperid\":null,\"PeriodicalName\":\"The Chemical Engineering Journal\",\"FirstCategoryId\":\"1085\",\"ListUrlMain\":\"https://www.sciencedirect.com/science/article/pii/0300946792800142\",\"RegionNum\":0,\"RegionCategory\":null,\"ArticlePicture\":[],\"TitleCN\":null,\"AbstractTextCN\":null,\"PMCID\":null,\"EPubDate\":\"\",\"PubModel\":\"\",\"JCR\":\"\",\"JCRName\":\"\",\"Score\":null,\"Total\":0}","platform":"Semanticscholar","paperid":null,"PeriodicalName":"The Chemical Engineering Journal","FirstCategoryId":"1085","ListUrlMain":"https://www.sciencedirect.com/science/article/pii/0300946792800142","RegionNum":0,"RegionCategory":null,"ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"","JCRName":"","Score":null,"Total":0}
A study of performance and optimization of tank-electrolyser cascades
The effect of the imposed cell voltage policy on reactant-to-product conversion and the optimal number of elements in a CSTER cascade was analysed in terms of various costs associated with its operation. Optimal operation may be feasible with a single tank or with several tanks in series, according to the relative magnitude of governing costs. Operation with the same voltage imposition on each element is also compared with operation with a non-uniform voltage distribution.
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