{"title":"Continuous ethanol production from glucose using Saccharomyces cerevisiae immobilized on fluidized microcarriers","authors":"Esa Melin, Wen K. Shieh","doi":"10.1016/0300-9467(92)80015-3","DOIUrl":null,"url":null,"abstract":"<div><p>The feasibildty was explored of employing biofluidized bed (BFB) technology based on immobilized <em>Saccharomyces cerevisiae</em> for continuous ethanol production from glucose. Long-term, steady and effective performance of ethanol production and glucose utilization is achievable in the BFB reactor when porous microcarriers are used to immobilize and retain yeast cells. More than two- thirds of the total reactor yeast cell mass was immobilized. Zero-order kinetics for ethanol production and glucose utilization existed at bulk liquid glucose concentrations greater than 1 g L<sup>−1</sup>. Ethanol inhibition of yeast cells was absent at bulk liquid ethanol concentrations as high as 78 g L<sup>−1</sup>.</p></div>","PeriodicalId":101225,"journal":{"name":"The Chemical Engineering Journal","volume":"50 2","pages":"Pages B17-B22"},"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)80015-3","citationCount":"7","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"The Chemical Engineering Journal","FirstCategoryId":"1085","ListUrlMain":"https://www.sciencedirect.com/science/article/pii/0300946792800153","RegionNum":0,"RegionCategory":null,"ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"","JCRName":"","Score":null,"Total":0}
引用次数: 7
Abstract
The feasibildty was explored of employing biofluidized bed (BFB) technology based on immobilized Saccharomyces cerevisiae for continuous ethanol production from glucose. Long-term, steady and effective performance of ethanol production and glucose utilization is achievable in the BFB reactor when porous microcarriers are used to immobilize and retain yeast cells. More than two- thirds of the total reactor yeast cell mass was immobilized. Zero-order kinetics for ethanol production and glucose utilization existed at bulk liquid glucose concentrations greater than 1 g L−1. Ethanol inhibition of yeast cells was absent at bulk liquid ethanol concentrations as high as 78 g L−1.
探讨了固定化酿酒酵母菌生物流化床(BFB)技术连续生产葡萄糖乙醇的可行性。利用多孔微载体固定和保留酵母细胞,可以实现BFB反应器长期、稳定、有效的乙醇生产和葡萄糖利用性能。反应器中超过三分之二的酵母细胞被固定化。当散装液体葡萄糖浓度大于1 g L−1时,乙醇生产和葡萄糖利用存在零级动力学。乙醇对酵母细胞的抑制作用在体积乙醇浓度高达78 g L−1时不存在。