期刊文献+

Comparative lipidomic analysis of S. cerevisiae cells during industrial bioethanol fermentation

Comparative lipidomic analysis of S. cerevisiae cells during industrial bioethanol fermentation
原文传递
导出
摘要 Variations in the composition and level of phospholipids (PLs) in yeast cells during industrial ethanol fermentation processes were analyzed. A comparative lipidomic method was used to investigate the changes in total cellular PLs during continuous and fed-batch/batch processes. The phospholipid metabolism in yeast changed during both processes, mainly due to the presence of longchain poly unsaturated fatty acids (PUFA) that contained phosphatidyglycerol (PG), phosphatidylethanolamine (PE) and phosphatidylserine (PS). The complexity of the media affected the growth of the yeast and the membrane composition. Yeast incorporated lots of exogenous saturated and PUFAs from the feedstock during the fermentations. During the continuous fermentation, there was an increase in PLs with shorter chains as the fermentation progressed and early in process there were more longchains. During the fed-batch/batch process, the PG species increased as the fermentation progressed. This is probably due to an inositol deficiency in the earlier part of the fermentation. Variations in the composition and level of phospholipids (PLs) in yeast cells during industrial ethanol fermentation processes were analyzed. A comparative lipidomic method was used to investigate the changes in total cellular PLs during continuous and fed-batch/batch processes. The phospholipid metabolism in yeast changed during both processes, mainly due to the presence of longchain poly unsaturated fatty acids (PUFA) that contained phosphatidyglycerol (PG), phosphatidylethanolamine (PE) and phosphatidylserine (PS). The complexity of the media affected the growth of the yeast and the membrane composition. Yeast incorporated lots of exogenous saturated and PUFAs from the feedstock during the fermentations. During the continuous fermentation, there was an increase in PLs with shorter chains as the fermentation progressed and early in process there were more longchains. During the fed-batch/batch process, the PG species increased as the fermentation progressed. This is probably due to an inositol deficiency in the earlier part of the fermentation.
出处 《Frontiers of Chemical Science and Engineering》 CAS CSCD 2012年第4期461-469,共9页 化学科学与工程前沿(英文版)
关键词 LIPIDOMICS systems biology phospholipids stirred-tank saccharomyces cerevisiae biorefinery engi-neering lipidomics, systems biology, phospholipids,stirred-tank, saccharomyces cerevisiae, biorefinery engi-neering
  • 相关文献

参考文献43

  • 1Ikner A, Shiozaki K.Yeast signaling pathways in the oxidative stress response mutation research/fundamental and molecular mechanisms of mutagenesis, 2005, 569(1-2): 13-27.
  • 2Yamaji K, Ham S, Mizoguchi H. Influence of Ras function on ethanol stress response of sake yeast. Journal of Bioscience and Bioengineering, 2003, 96(5): 474-480.
  • 3Gasch A P, Spellman P T, Kao C M, Carmel-harel O, Eisen M B, Storz G, Botstein D, Brown P O. Genomic expression programs in the response of yeast cells to environmental changes. Molecular Biology of the Cell, 2000, 11 : 4241-4257.
  • 4Puig S, Perez-Ortin J E. Expression levels and patterns ofglycolytic yeast genes during wine fermentation. Original Research Article Systematic and Applied Microbiology, 2000, 23(2): 300-303.
  • 5Beltran G, Novo M, Guillamon J M, Mas A, Rozes N. Effect of fermentation temperature and culture media on the yeast lipid composition and wine volatile compounds. International Journal of Food Microbiology, 2008, 121(2): 169-177.
  • 6Torija M J, Beltran G, Novo M, Poblet M, Guillamon J M, Mas A, Rozes N. Effects of fermentation temperature and Saccharomyces species on the cell fatty acid composition and presence of volatile compounds in wine. International Journal of Food Microbiology, 2003, 85(1-2): 127-136.
  • 7Xu T J, Zhao X Q, Bai F W. Continuous ethanol production using self-flocculating yeast in a cascade of fermentors. Enzyme and Microbial Technology, 2005, 37(6): 634-640.
  • 8Tang Y Q, An M Z, Zhong Y L, Shigem M, Wu X L, Kida K. Continuous ethanol fermentation from non-sulfuric acid-washed molasses using traditional stirred tank reactors and the flocculating yeast strain KF-7. Original Journal of Bioscience and Bioengineer- ing, 2010, 109(1): 41-46.
  • 9Alfenore S, Cameleyre X, Benbadis L, Bideaux C, Uribelarrea J L, Goma G, Molina-Jouve C, Guillouet S E. Aeration strategy: a need for very high ethanol performance in saccharomyces cerevisiae fed- batch process. Applied Microbiology and Biotechnology, 2004, 63 (5): 537-542.
  • 10Laluce C, Souza C S, Abud C L, Gattas E A L, Walker G M. Continuous ethanol production in a nonconventional five-stage system operating with yeast cell recycling at elevated temperatures. Journal of Industrial Microbiology & Biotechnology, 2002, 29(3): 140-144.

相关作者

内容加载中请稍等...

相关机构

内容加载中请稍等...

相关主题

内容加载中请稍等...

浏览历史

内容加载中请稍等...
;
使用帮助 返回顶部