Simultaneous saccharification and fermentation by co-cultures of Fusarium oxysporum and Saccharomyces cerevisiae enhances ethanol production from liquefied wheat straw at high solid content

被引:44
作者
Paschos, Thomas [1 ]
Xiros, Charilaos [2 ]
Christakopoulos, Paul [3 ]
机构
[1] Natl Tech Univ Athens, Sch Chem Engn, Biotechnol Lab, Athens 5780, Greece
[2] Bern Univ Appl Sci, Sch Agr Forestry & Food Sci, Div Agr, CH-3052 Zollikofen, Switzerland
[3] Lulea Univ Technol, Dept Civil Environm & Nat Resources Engn, Div Chem Engn, Biochem Proc Engn, SE-97187 Lulea, Sweden
关键词
Consolidated bioprocess; Liquefaction; High-gravity fermentation; Wheat straw; Solid-state culture; BREWERS SPENT GRAIN; LIGNOCELLULOSIC ETHANOL; CO-FERMENTATION; PRETREATMENT; PERFORMANCE; HYDROLYSIS; BIOETHANOL; ENZYME;
D O I
10.1016/j.indcrop.2015.07.061
中图分类号
S2 [农业工程];
学科分类号
0828 ;
摘要
A co-fermentation process involving Saccharomyces cerevisiae and Fusarium oxysporum was studied, using hydrothermally pretreated wheat straw as substrate. In the first step of the study, we examined liquefaction of the material in a free-fall reactor. Both the enzyme loading and the dry matter content affected severely the liquefaction efficiency. In the second step (simultaneous saccharification and fermentation (SSF) experiments), we found that the enzymatic system of F. oxysporum contributed significantly to substrate hydrolysis, while its metabolic system played a secondary role in fermentation. SSF in the presence of F. oxysporum cells and enzymes gave 62 g L-1 ethanol. In the third step of the study, a semi-consolidated bioprocess was designed in which F. oxysporum culture (submerged or solid-state) was added at the SSF stage along with S. cerevisiae. The addition of solid F. oxysporum culture increased ethanol production by 19%, leading to a final ethanol concentration of 58 g L-1. The present study proposes a semi-consolidated process combining two microorganisms for the fermentation at high solids concentration of a liquefied material using an in house free fall mixing reactor. The semi-consolidated process proposed not only increased the ethanol yields significantly, but could also lead to lower overall cost of the process by incorporating in-situ enzyme production. (C) 2015 The Authors. Published by Elsevier B.V. This is an open access article under the CC BY-NC-ND license (http://creativecommons.org/licenses/by-nc-nd/4.0/).
引用
收藏
页码:793 / 802
页数:10
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