{"title":"利用流化微载体固定化酿酒酵母从葡萄糖连续生产乙醇","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":"{\"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}","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
摘要
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。
Continuous ethanol production from glucose using Saccharomyces cerevisiae immobilized on fluidized microcarriers
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.