Abstract
The modified rotating simplex method has been successfully used to determine the best combination of agitation rate and aeration rate for maximum production of extracellular proteases by Staphylococcus aureus mutant RC128, in a stirred tank bioreactor operated in a discontinuous way. This mutant has shown altered exoprotein production, specially enhanced protease production. Maximum production of proteases (15.28 UP/ml), measured using azocasein as a substrate, was obtained at exponential growth phase when the bioreactor was operated at 300 rpm and at 2 vvm with a volumetric oxygen transfer coefficient (K L a) of 175.75 h−1. These conditions were found to be more suitable for protease production.
Similar content being viewed by others
References
Milavec P, Podornik A, Stravs R, Koloini T (2002) Effect of experimental error on the efficiency of different optimization methods for bioprocess media optimization. Bioprocess Biosyst Eng 25:68–78
Xu CP, Sinha J, Bae JT, Kim SW, Yun JW (2006) Optimization of physical parameters for exo-biopolymer production in submeged mycelial cultures of two entomopathogenic fungi Paecilomyces japonica and Paecilomyces tenuipes. Lett Appl Microbiol 42:501–506
Kolossváry GJ (1996) Optimization of lipase activity from Rhizopus sp. in triglyceride hydrolisis using a modified simplex method. Process Biochem 6:595–600
Tinoi J, Rakariyatham N, Deming RL (2005) Simplex optimization of carotenoid production by Rhodotorula glutinis using hydrolyzed mung bean waste flour as substrate. Process Biochem 40:2551–2557
Panda T, Naidu GSN, Sinha J (1999) Multiresponse analysis of microbiological parameters affecting the production of of pectolytic enzymes by Aspergillus niger: a statistical review. Pcocess Biochem 35:187–195
Felse AP, Panda T (1999) Self-directing optimization of parameters for extracellular chitinase production by Trichoderma harzianum in batch mode. Bioprocess Eng 34:563–566
Gupta R, Beg QK, Lorenz P (2002) Bacterial alkaline proteases: molecular approaches and industrial applications. Appl Microbiol Biotechnol 59:15–32
Çalik P, Çalik G, Özdamar T (1998) Oxygen transfer effects in serine alkaline protease fermentation by Bacillus licheniformis: Use of citric acid as the carbon source. Enzyme Microb Technol 23:451–461
Hwang YB, Lee AC, Chang HN, Chang YK (1991) Dissolved oxygen concentration regulations using auto tunning proportional integral derivative controller in fermentation process. Biotechnol Tech 5:85–90
Arvidson S, Holme T, Wadström T (1970) Formation of Bacteriolytic Enzymes in Batch and Continuous Culture of Staphylococcus aureus. J Bacteriol 104:227–233
Carpenter D, Silverman G (1976) Synthesis of staphylococcal enterotoxin A and nuclease under controlled fermentor conditions. Appl Environ Microbiol 31:243–248
Vadehra DA, Harmon LG (1969) Factors affecting production of staphylococcal lipase. J Appl Bacteriol 32:147–150
Drapeau GR, Boily Y, Hourmard J (1972) Purification and propierties of an extracellular protease of Staphylococcus aureus. J Biol Chem 247:6720–6726
Kim S, Park KS, Byun SM, Pan JG, Shin YC (1995) Overproduction of Serratia marcescens metalloprotease (SMP) from the recombinant Serratia marcescens strains. Microb Lett 17:497–502
Giraudo A, Martínez G, Calzolari A, Nagel R (1994) Characterization of a Tn925-induced mutant of Staphylococcus aureus alterd in exoprotein production. J Basic Microbiol 34:317–322
Takeuchi S, Kinoshita T, Kaidoh T, Hashizume N (1999) Purifiction and caracterization of protease produced by Staphylococcus aureus isolated from a diseased chicken. Vet Microbiol 67:195–202
Bailey J, Ollis D (1986) Biochemical engineering fundamentals. Mc Graw-Hill, New York
Bradford M (1976) A rapid and sensitive method for quantification of microgram quantities of protein utilizing the principle of protein-dye binding. Anal Biochem 72:248–254
Nelder JA, Mead RA (1965) A simplex method for function minimization. Comput J 7:308–313
Bandyopadhyay B, Humphrey A, Taguchi H (1967) Dynamic measurement of volumetric oxygen transfer coefficient in fermentation systems. Biotechnol Bioeng 9:533–544
Ruchti G, Dunn IJ, Bourne JR (1981) Comparison of dynamic oxygen electrode methods for the measurement of KLa. Biotechnol Bioeng 23:277–290
Dang NDP, Karrer DA, Dunn IJ (1977) Oxygen transfer coefficients by dynamic model moment analysis. Biotechnol Bioeng 19:853–865
Märkl H, Bronnenmeier R (1985) Mechanical stress and microbial production. In: Rehm HJ, Reed G (eds) Biotechnology. Fundamentals of biochemical engineering, vol 2. H. Brauer, VCH Weinheim, Germany, pp 369–392
Thomas CR (1990) Problems of shear in biotechnology. In: Winkler MA (ed) Chemical engineering problems in biotechnology. Elsevier Applied Science, London, pp 23–92
Van’t Riet K (1979) Review of measuring methods and results in nonviscous gas-liquid mass transfer in stirred vessels. Nid Eng Chem Process Des Dev 18:357–364
Ustáriz F, Laca A, García L, Díaz M (2004) Fermentation of individual proteins for protease production by Serratia marcescens. Biochem Eng J 19:147–153
Beg Q, Sahai V, Gupta R (2003) Statistical media optimization and alkaline protease production from Bacillus mojavensis in a bioreactor. Process Biochem 39:203–209
Genckal H, Tari C (2006) Alkaline protease production from alkalophilic Bacillus sp. isolated from natural habitats. Enzyme Microb Technol 39:703–710
Acknowledgments
The authors wish to thank the support given by the Secretaría de Ciencia y Técnica Universidad Nacional de Río Cuarto (UNRC), Argentina.
Author information
Authors and Affiliations
Corresponding author
Rights and permissions
About this article
Cite this article
Ducros, E., Ferrari, M., Pellegrino, M. et al. Effect of aeration and agitation on the protease production by Staphylococcus aureus mutant RC128 in a stirred tank bioreactor. Bioprocess Biosyst Eng 32, 143–148 (2009). https://doi.org/10.1007/s00449-008-0233-5
Received:
Accepted:
Published:
Issue Date:
DOI: https://doi.org/10.1007/s00449-008-0233-5