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Received June 11, 2008
Accepted September 18, 2008
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Optimization of citric acid production by Aspergillus niger NRRL 567 grown in a column bioreactor
1Department of Bioresource Engineering, Faculty of Agricultural and Environmental Sciences, McGill University, 21,111 Lakeshore, Ste Anne de Bellevue, Quebec, H9K 3V9, Canada 2Samsung Advanced Institute of Technology, Mt. 14-1 Nongseo-dong Giheung-gu, Youngin-si, Gyeonggi-do 446-712, Korea 3Department of Chemical Engineering, Kyonggi University, 94-6, Iui-dong, Yeongtong-gu, Suwon 443-760, Korea 4Faculty of Environmental and Biological Engineering, Shenyang Institute of Chemical Technology, Shenyang 110000, China
jw1028.kim@samsung.com
Korean Journal of Chemical Engineering, March 2009, 26(2), 422-427(6), 10.1007/s11814-009-0071-4
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Abstract
Citric acid production using Aspergillus niger NRRL 567 grown on peat moss has been optimized in a column bioreactor using a statistically based method. A 2^(3) full factorial design with eight fermentation conditions was applied to evaluate significance on citric acid production and their interactions between variables, where the three independent variables evaluated were aeration rate, bed depth and temperature. Aeration rate and fermentation temperature were identified to be significant variables. Citric acid production markedly increases with aeration rate and fermentation temperature; however, the bed depth of solid substrate showed an insignificant effect on citric acid production. The optimum fermentation condition for citric acid production in a column bioreactor consisted of aeration rate of 0.84 vvm, bed depth of 22 cm and fermentation temperature of 32 ℃. Under a given condition, a maximum citric acid production of 120.6 g/l was predicted and matched well with the experimental value of 123.9 g/kg.
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Nandakumar MP, Thakur MS, Raghavarao KS, Ghildyal NP, Process Biochem., 29(7), 545 (1994)
Ghildyal NP, Gowthaman MK, Rao KS, Karanth NG, Enzyme Microb. Technol., 16(3), 253 (1994)
Pintado J, Torrado A, Gonzalez MP, Murado MA, Enzyme Microb. Technol., 23(1-2), 149 (1998)
Goes AP, Sheppard JD, J. Chem. Technol. Biotechnol., 73, 709 (1999)
Kokitkar PB, Tanner RD, Enz. Microbiol. Technol., 12, 552 (1990)
Omori T, Takeshima N, Shimoda M, J. Ferment. Bioeng., 78(1), 27 (1994)
Smits JP, Rinzema A, Tramper J, van Sonsbeek HM, Hage JC, Kaynak A, Knol W, Enzyme Microb. Technol., 22(1), 50 (1998)
Favela-Torres E, Cordova-Lopez J, Garcia-Rivero M, Gutierrez-Rojas M, Process Biochem., 33(2), 103 (1998)
Romero-Gomez SJ, Augur C, Viniegra-Gonzalez G, Biotechnol. Lett., 22(15), 1255 (2000)
Wasay SA, Barrington SF, Tokunaga S, Bioremed. J., 2, 184 (1998)
Kim JW, Suzelle S, Sheppard J, Lee B, Process Biochem., 41, 1253 (2006)
Barrington S, Kim JW, Bioresour. Technol., 99(2), 368 (2008)
Xu DB, Kubicek CP, Roch M, Appl. Microbiol. Biotechnol., 30, 444 (1989)
Marier JR, Boulet M, J. Dairy Sci., 41, 1683 (1958)
Miller GL, Anal. Chem., 31, 426 (1959)
Berthouex PM, Brown LC, Statistics for environmental engineers (2nd Ed.), CRC press, Boca Raton, FL (1994)
Panda T, Naidu GSN, Sinha J, Process Biochem., 35(1), 187 (1999)
de Medeiros SF, Avery MA, Avery B, Leite SGF, Freitas ACC, Williamson JS, Biotechnol. Lett., 24(11), 937 (2002)
Abou-Zeid AA, Ashy MA, Agr. Wasters, 9, 51 (1984)
Elliott HA, Shastri NL, Water Air Soil Poll., 110, 335 (1999)
Sayer JA, Gadd GM, Mycol. Res., 105, 1261 (2001)
Barrington S, Choiniere D, Trigui M, Knight W, Bioresour. Technol., 83(3), 189 (2002)