1 |
Shima, S., S. Oshima, and H. Sakai. 1983. Biosynthesis of - poly-L-lysine by washed mycelium of Streptomyces albulus no. 346. Nippon Nogei Kagaku Kaishi 57: 221-226.
DOI
|
2 |
Shuler, M. and F. Kargi. 2002. Bioprocess Engineering, Basic Concepts, pp. 155-184. 2nd Ed. Prentice-Hall of India, New Delhi.
|
3 |
Yoshida, T. and T. Nagasawa. 2003.-Poly-L-lysine: Microbial production, biodegradation and application potential. Appl. Microbiol. Biotechnol. 62: 21-26.
DOI
ScienceOn
|
4 |
Zhang, Y., X. Feng, H. Xu, Z. Yao, and P. Ouyang. 2010. - Poly-L-lysine production by immobilized cells of Kitasatospora sp. MY 5-36 in repeated fed-batch cultures. Bioresour. Technol. 101: 5523-5527.
DOI
ScienceOn
|
5 |
Zou, X., H. Hang, J. Chu, Y. Zhuang, and S. Zhang. 2009. Oxygen uptake rate optimization with nitrogen regulation for erythromycin production and scale-up from 50 L to 372 scale. Bioresour. Technol. 100: 1406-1412.
DOI
ScienceOn
|
6 |
Luedeking, R. and E. Piret. 1959. A kinetic study of the lactic acid fermentation. J. Biochem. Microbiol. Technol. Eng. 1: 393-412.
DOI
|
7 |
Monod, J. 1949. The growth of bacterial cultures. A Review. Microbiology 3: 371-394.
DOI
ScienceOn
|
8 |
Palomares, L. A. and O. Ramirez. 1996. The effect of dissolved oxygen tension and the utility of oxygen uptake rate in insect cell culture. Cytotechnology 22: 225-237.
DOI
|
9 |
Pinches, A. and L. Pallent. 1986. Rate and yield relationships in the production of xanthan gum by batch fermentations using complex and chemically defined growth media. Biotechnol. Bioeng. 28: 1484-1496.
DOI
ScienceOn
|
10 |
Rowe, G. E., A. Margaritis, and N. Wei. 2003. Specific oxygen uptake rate variations during batch fermentation of Bacillus thuringiensis subspecies kurstaki HD-1. Biotechnol. Progr. 19: 1439-1443.
DOI
ScienceOn
|
11 |
Saimura, M., M. Takehara, S. Mizukami, K. Kataoka, and H. Hirohara. 2008. Biosynthesis of nearly monodispersed poly(-Llysine) in Streptomyces species. Biotechnol. Lett. 30: 377-385.
DOI
ScienceOn
|
12 |
Shih, I. L., T. C. Wang, S. Z. Chou, and G. D. Lee. 2010. Sequential production of two biopolymers levan and poly-- lysine by microbial fermentation. Bioresour. Technol. 102: 3966- 3969.
|
13 |
Sampaio, F. C., P. Torre, F. L. Passos, P. Perego, F. V. Passos, and A. Converti. 2004. Xylose metabolism in Debaromyces hansenii UFV-170. Effect of the specific oxygen uptake rate. Biotechnol. Progr. 20: 1641-1650.
DOI
ScienceOn
|
14 |
Shen, W. C., D. Yang, and H. J. Ryser. 1984. Calorimetric determination of microgram quantities of polylysine by trypan blue precipitation. Anal. Biochem. 142: 521-524.
DOI
ScienceOn
|
15 |
Shih, I. L., M. H. Shen, and Y. T. Van. 2006. Microbial synthesis of poly(-lysine) and its various applications. Bioresour. Technol. 97: 1148-1159.
DOI
ScienceOn
|
16 |
Shima, S. and H. Sakai. 1981. Poly-L-lysine produced by Streptomyces. Part II. Taxonomy and fermentation studies. Agric. Biol. Chem. 45: 2497-2502.
DOI
|
17 |
Shima, S., H. Matsuoka, T. Iwamoto, and H. Sakai. 1984. Antimicrobial action of -poly-L-lysine. J. Antibiot. 37: 1449- 1455.
DOI
|
18 |
Dorresteijn, R. C., C. D. Gooijer, J. Tramper, and E. C. Beuvery. 1994. A simple dynamic method for on-line and off-line determination of a during cultivation of animal cells. Biotechnol. Tech. 8: 675-680.
|
19 |
Felse, P. A. and T. Panda. 2000. Submerged culture production of chitinase by Trichoderma harzianum in stirred-tank bioreactors: The influence of agitator speed. Biochem. Eng. J. 4: 115-120.
DOI
ScienceOn
|
20 |
Galaction, A. I., D. Cascaval, C. Onisco, and M. Turnea. 2004. Prediction of oxygen mass transfer coefficients in stirred bioreactors for bacteria, yeast and fungus broths. Biochem. Eng. J. 20: 85-94.
DOI
ScienceOn
|
21 |
Garcia-Ochoa, F. and E. Gomez. 2009. Bioreactor scale-up and oxygen transfer rate in microbial processes: An overview. Biotechnol. Adv. 27: 153-176.
DOI
|
22 |
Garcia-Ochoa, F., V. Santos, J. Casas, and E. Gomez. 2000. Xanthan gum: Production, recovery, and properties. Biotechnol. Adv. 18: 549-579.
DOI
ScienceOn
|
23 |
Hiraki, J., T. Ichikawa, S. I. Ninomiya, H. Seki, K. Uohama, H. S. Seki, Kimura, Y. Yanagimoto, and J. W. Barnett. 2003. Use of ADME studies to confirm the safety of -polylysine as a preservative in food. Regul. Toxicol. Pharm. 37: 328-340.
DOI
ScienceOn
|
24 |
Garcia-Ochoaa, F., E. Gomeza, V. E. Santosa, and J. C. Merchukb. 2010. Oxygen uptake rate in microbial processes: An overview. Biochem. Eng. J. 49: 289-307.
DOI
ScienceOn
|
25 |
Gomez, E., V. E. Santos, A. Alcon, and F. Garcia-Ochoa. 2006. Oxygen transport rate on Rhodococcus erythropolis cultures: Effect on growth and BDS capability. Chem. Eng. Sci. 61: 4595-4604.
DOI
ScienceOn
|
26 |
Hiraki, J. and E. Suzuki. 1999. Process for producing -poly-Llysine with immobilized Streptomyces albulus. US Patent 5900363.
|
27 |
Hirohara, H., M. Takehara, M. Saimura, A. Masayuki, and M. Miyamoto. 2006. Biosynthesis of poly(-L-lysine)s in two newly isolated strains of Streptomyces sp. Appl. Microbiol. Biotechnol. 73: 321-331.
DOI
ScienceOn
|
28 |
Kahar, P., T. Iwata, J. Hiraki, Y. E. Park, and M. Okabe. 2001. Enhancement of -polylysine production by Streptomyces albulus strain 410 using pH control. J. Biosci. Bioeng. 91: 190-194.
|
29 |
Kawase, Y., B. Halard, and M. Moo-Young. 1992. Liquid-phase mass transfer coefficients in bioreactors. Biotechnol. Bioeng. 39: 1133-1140.
DOI
|
30 |
Bankar, S. B. and R. S. Singhal. 2010. Optimization of poly-- lysine production by Streptomyces noursei NRRL 5126. Bioresour. Technol. 101: 8370-8375.
DOI
ScienceOn
|
31 |
Bankar, S. B. and R. S. Singhal. 2011. Metabolic precursors enhance the production of poly--lysine by Streptomyces noursei NRRL 5126. Eng. Life Sci. DOI: 10.1002/elsc.201000127.
|
32 |
Bok, S. H. and A. L. Demain. 1977. An improved calorimetric assay for polyols. Anal. Biochem. 81: 18-20.
DOI
ScienceOn
|
33 |
Calik, P., P. Yilgor, P. Ayhan, and A. Demir. 2004. Oxygen transfer effects on recombinant benzaldehyde lyase production. Chem. Eng. Sci. 59: 5075-5083.
DOI
ScienceOn
|