{"title":"Influence of organic loading rate on the anaerobic treatment of high strength semisynthetic waste waters in a biological fluidized bed","authors":"A. Converti, M. Del Borghi, G. Ferraiolo","doi":"10.1016/0300-9467(93)80046-Q","DOIUrl":null,"url":null,"abstract":"<div><p>The results of anaerobic digestion in a fluidized bed reactor fed with municipal waste waters enriched with glucose are presented. Several process conditions have been tested by varying the influent chemical oxygen demand (COD) from 4 to 13 kg m<sup>−3</sup> and the residence time from 5.0 to 68.2 h. The degradation efficiency and methane production rate are substantially affected by an increase in organic loading rate from 4 to 24 kgCOD<sub>i</sub> m<sup>−3</sup> day<sup>−1</sup>, suggesting a maximum operational value for this parameter. Using a Monod-type kinetic model, a maximum theoretical specific degradation rate of 1.76 kgCOD<sub>r</sub> kgVSS<sup>−1</sup> day<sup>−1</sup> has been calculated, which is very similar to values calculated for other effluents from food industry activities.</p></div>","PeriodicalId":101225,"journal":{"name":"The Chemical Engineering Journal","volume":"52 1","pages":"Pages B21-B28"},"PeriodicalIF":0.0000,"publicationDate":"1993-08-01","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"https://sci-hub-pdf.com/10.1016/0300-9467(93)80046-Q","citationCount":"23","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"The Chemical Engineering Journal","FirstCategoryId":"1085","ListUrlMain":"https://www.sciencedirect.com/science/article/pii/030094679380046Q","RegionNum":0,"RegionCategory":null,"ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"","JCRName":"","Score":null,"Total":0}
引用次数: 23
Abstract
The results of anaerobic digestion in a fluidized bed reactor fed with municipal waste waters enriched with glucose are presented. Several process conditions have been tested by varying the influent chemical oxygen demand (COD) from 4 to 13 kg m−3 and the residence time from 5.0 to 68.2 h. The degradation efficiency and methane production rate are substantially affected by an increase in organic loading rate from 4 to 24 kgCODi m−3 day−1, suggesting a maximum operational value for this parameter. Using a Monod-type kinetic model, a maximum theoretical specific degradation rate of 1.76 kgCODr kgVSS−1 day−1 has been calculated, which is very similar to values calculated for other effluents from food industry activities.