ISSN: 0256-1115 (print version) ISSN: 1975-7220 (electronic version)
Copyright © 2024 KICHE. All rights reserved

Articles & Issues

Language
English
Conflict of Interest
In relation to this article, we declare that there is no conflict of interest.
Publication history
Received September 29, 2009
Accepted November 23, 2009
articles This is an Open-Access article distributed under the terms of the Creative Commons Attribution Non-Commercial License (http://creativecommons.org/licenses/bync/3.0) which permits unrestricted non-commercial use, distribution, and reproduction in any medium, provided the original work is properly cited.
Copyright © KIChE. All rights reserved.

All issues

A novel strategy on the high-cell-density cultivation of Candida utilis for the enhanced production of glutathione

School of Basic Medicine and Biological Science, College of Medicine, Soochow University, Suzhou 215123, P. R. China
Korean Journal of Chemical Engineering, July 2010, 27(4), 1246-1251(6), 10.1007/s11814-010-0190-y
downloadDownload PDF

Abstract

Efficient glutathione production by high-cell-density cultivation of Candida utilis was investigated. A series of batch glutathione fermentations were carried out and the optimal initial glucose concentration was found to be about 26 g/L. Then, fed-batch fermentation under diverse feeding strategies was used to enhance glutathione production with a total glucose concentration of 150 g/L. Constant glucose feeding strategy cannot meet the requirement of cells at the late period of feeding, while exponential glucose feeding strategy cannot satisfy the needs of cells at the beginning of feeding. Based on the results above, a polynomial glucose feeding strategy was developed to provide enough glucose for cells along with the cultivation, under which both the cell and glutathione productivity were satisfactorily improved. Furthermore, fed-batch fermentation under this strategy with a total glucose concentration of 200 g/L was successfully performed, the dry cell weight and glutathione concentration reached 91.2 g/L and 825 mg/L, respectively.

References

Stephen DW, Jamieson DJ, FEMS Microbiol. Lett., 141, 207 (1996)
Sies H, Free Radical Biol. Med., 27, 916 (1999)
Li Y, Wei GY, Chen J, Appl. Microbiol. Biotechnol., 66(3), 233 (2004)
Riesenberg D, Guthke R, Appl. Microbiol. Biotechnol., 51(4), 422 (1999)
Doran PM, Bioprocess engineering principles., Academic Press Ltd. (1997)
Lee SY, Trends Biotechnol., 14, 98 (1996)
Ordaz L, Lopez R, Melchy O, de la Torre M, Appl. Microbiol. Biotechnol., 57(3), 374 (2001)
Lee J, Lee SY, Park S, Middelberg APJ, Biotechnol. Adv., 17, 29 (1999)
Sakato K, Tanaka H, Biotechnol. Bioeng., 40, 904 (1992)
Alfafara CG, Miura K, Shimizu H, Shioya S, Suga KI, Suzuki K, Biotechnol. Bioeng., 41, 493 (1993)
Wang Z, Tan T, Song J, Process Biochem., 42, 108 (2007)
van Urk H, Voll WSL, Sheffers WA, van Dijken JP, Appl.Environ. Microbiol., 56, 281 (1990)
Castrillo JI, Kaliterna J, Weusthuis RA, Vandijken JP, Pronk JT, Biotechnol. Bioeng., 49(6), 621 (1996)
Liang G, Liao X, Du G, Chen J, J. Appl. Microbiol., 105(5), 1432 (2008)
Wei G, Wang D, Chen J, J. Chem. Ind. Eng., China, 58, 2329 (2007)
Miller G, Anal. Chem., 31, 426 (1959)
Tietze F, Anal. Chem., 27, 502 (1969)
Cui JD, Li Y, Korean J. Chem. Eng., 26(2), 444 (2009)
Li Y, Chen J, Song Q, Lun S, Katakura Y, Chin. J. Pharm., 30, 1 (1997)
Yamane T, Shimizu S, Adv. Biochem. Eng. Biotechnol., 30, 147 (1984)
Vanags J, Rychtera M, Ferzik S, Vishkins M, Viesturs U, Eng.Life. Sci., 7, 247 (2007)
Alfafara CG, Miura K, Shimizu H, Shioya S, Suga K, Appl.Microbiol. Biotechnol., 37, 141 (1992)

The Korean Institute of Chemical Engineers. F5, 119, Anam-ro, Seongbuk-gu, 233 Spring Street Seoul 02856, South Korea.
TEL. No. +82-2-458-3078FAX No. +82-507-804-0669E-mail : kiche@kiche.or.kr

Copyright (C) KICHE.all rights reserved.

- Korean Journal of Chemical Engineering 상단으로