Performance analyses of a pH-shift and DOT-shift integrated fed-batch fermentation process for the production of ganoderic acid and Ganoderma polysaccharides by medicinal mushroom Ganoderma lucidum

被引:104
作者
Tang, Ya-Jie [1 ,2 ]
Zhang, Wei [1 ]
Zhong, Jian-Jiang [3 ]
机构
[1] Hubei Univ Technol, Coll Bioengn, Hubei Prov Key Lab Ind Microbiol, Wuhan 430068, Peoples R China
[2] Chinese Acad Sci, Inst Proc Engn, Natl Key Lab Biochem Engn, Beijing 100080, Peoples R China
[3] Shanghai Jiao Tong Univ, Coll Life Sci & Biotechnol, Minist Educ, Key Lab Microbial Metab, Shanghai 200240, Peoples R China
基金
中国国家自然科学基金;
关键词
Ganoderma lucidum; pH-shift culture; DOT-shift culture; Fed-batch culture; Integrated strategy; EXOPOLYSACCHARIDE PRODUCTION; SUBMERGED FERMENTATION; CONTROL STRATEGY; CULTURE PROCESS; CULTIVATION; HYPERPRODUCTION; BIOREACTORS; MYCELIA; CELLS;
D O I
10.1016/j.biortech.2008.10.005
中图分类号
S2 [农业工程];
学科分类号
0828 ;
摘要
Investigations on Ganoderma lucidum fermentation suggested that the responses of the cell growth and metabolites biosynthesis to pH and dissolved oxygen tension (DOT) were different. The ganoderic acid (GA) production of 321.6 mg/L was obtained in the pH-shift culture by combining a 4-day culture at pH 3.0 with the following 6-day culture at pH 4.5, which was higher by 45% and 300% compared with the culture at pH 3.0 and 4.5, respectively. The CA production of 487.1 mg/L was achieved in the DOT-shift culture by combining a 6-day culture at 25% of DOT with a following 6-day culture at 10% of DOT, which was higher by 43% and 230% compared with the culture at 25% and 10% of DOT, respectively. A fed-batch fermentation process by combining the above-mentioned pH-shift and DOT-shift strategies resulted in a significant synergistic enhancement of CA accumulation up to 754.6 mg/L, which is the highest reported in the submerged fermentation of G. lucidum in stirred-tank bioreactor. (C) 2008 Elsevier Ltd. All rights reserved.
引用
收藏
页码:1852 / 1859
页数:8
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