{"title":"Submerged Cultivation of Ganoderma lucidum Biomass in Stirred Tank Reactor","authors":"M. Berovič, M. Popović","doi":"10.15255/CABEQ.2018.1371","DOIUrl":null,"url":null,"abstract":"European isolated strain Ganoderma lucidum, its biomass formation, intracellular and extracellular polysaccharide production in batch and repeated fedbatch cultivation, were studied. The best fed batch results were obtained in the first feeding at 141 h at productivity of biomass Px = 0.016 g g–1 h–1, intracellular Pi = 0.010 g g–1 h–1, extracellular polysaccharides Pe = 0.007 g g–1 h–1, and percent value of polysaccharides per cell dry weight Pi/x = 5.0 % and Pe/x = 3.0 %. Although four feedings increased the amount of fungal biomass by 42.66 %, productivities of fungal polysaccharides Pi = 0.010 g g–1 L–1 and Pe = 0.011 g g–1 L–1 showed that at the fourth feeding, the biomass was already exhausted and polysaccharide production was reduced. Therefore, 210 h batch cultivation with Px = 0.095 g g–1 L–1, Pi = 0.078 g g–1 L–1 at Pi/x = 33 % and extracellular polysaccharides Pe = 0.095 g g–1 L–1 at Pe/x = 6.8 %, was found to be the best mode for G. lucidum fungal biomass and polysaccharides production. Non-Newtonian cultivation broth rheology was found to be influenced entirely by the concentration and morphology of the biomass.","PeriodicalId":9765,"journal":{"name":"Chemical and Biochemical Engineering Quarterly","volume":" ","pages":""},"PeriodicalIF":1.6000,"publicationDate":"2019-01-16","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"3","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"Chemical and Biochemical Engineering Quarterly","FirstCategoryId":"5","ListUrlMain":"https://doi.org/10.15255/CABEQ.2018.1371","RegionNum":4,"RegionCategory":"生物学","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q4","JCRName":"BIOTECHNOLOGY & APPLIED MICROBIOLOGY","Score":null,"Total":0}
引用次数: 3
Abstract
European isolated strain Ganoderma lucidum, its biomass formation, intracellular and extracellular polysaccharide production in batch and repeated fedbatch cultivation, were studied. The best fed batch results were obtained in the first feeding at 141 h at productivity of biomass Px = 0.016 g g–1 h–1, intracellular Pi = 0.010 g g–1 h–1, extracellular polysaccharides Pe = 0.007 g g–1 h–1, and percent value of polysaccharides per cell dry weight Pi/x = 5.0 % and Pe/x = 3.0 %. Although four feedings increased the amount of fungal biomass by 42.66 %, productivities of fungal polysaccharides Pi = 0.010 g g–1 L–1 and Pe = 0.011 g g–1 L–1 showed that at the fourth feeding, the biomass was already exhausted and polysaccharide production was reduced. Therefore, 210 h batch cultivation with Px = 0.095 g g–1 L–1, Pi = 0.078 g g–1 L–1 at Pi/x = 33 % and extracellular polysaccharides Pe = 0.095 g g–1 L–1 at Pe/x = 6.8 %, was found to be the best mode for G. lucidum fungal biomass and polysaccharides production. Non-Newtonian cultivation broth rheology was found to be influenced entirely by the concentration and morphology of the biomass.
研究了欧洲分离菌株灵芝的生物量形成、细胞内和细胞外多糖的分批培养和重复补料培养。在141小时的第一次进料中获得了最佳的补料分批结果,生产力为生物质Px=0.016 g g–1 h–1,细胞内Pi=0.010 g g–2 h–1、细胞外多糖Pe=0.007 g g–3 h–1以及每细胞干重多糖百分比Pi/x=5.0%和Pe/x=3.0%。尽管四次饲养使真菌生物量增加了42.66%,但真菌多糖的产量Pi=0.010 g g–1 L–1和Pe=0.011 g g–L L–1表明,在第四次饲养时,生物量已经耗尽,多糖产量减少。因此,发现210小时分批培养是灵芝真菌生物量和多糖生产的最佳模式,其中Px=0.095 g g–1 L–1,Pi/x=33%时Pi=0.078 g g–1L–1,Pe/x=6.8%时胞外多糖Pe=0.095 g g–1l–1。发现非牛顿培养基的流变性完全受生物质的浓度和形态的影响。
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