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Search for Optimum Substitutive Neutralizing Agent and pH Control Strategy in Fumaric Acid Fermentation by Rhizopus oryzae |
CHEN Chen, TAI Chao, LI Shuang |
State Key Laboratory of Materials-Oriented Chemical Engineering, College of Biotechnology and Pharmaceutical Engineering, Nanjing University of Technology, Nanjing 210009, China |
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Abstract Four different neutralizing agents (CaCO3, Na2CO3, NH3稨2O, NaOH) were chosen to examine the effects of neutralizing agents on fumaric acid fermentation by Rhizopus oryzae ME-F12 which is the mutant of R. oryzae ATCC 20344. It was found that fumaric acid yield and productivity in the fermentation using Na2CO3 as neutralizing agent were the closest to which in the traditional CaCO3 case. Then the effects of different pH values (3.5, 4.5, 5.5, and 6.5) on fumaric acid fermentation using Na2CO3 as neutralizing agent were investigated. Based on the analysis of three kinetic parameters, a two-stage pH control strategy, aimed at achieving high concentration, high yield and high productivity of fumaric acid simultaneously, was proposed. pH was controlled at 5.5 at the first 24 h, and then switched to 4.5 till the end of the fermentation. Finally, the maximum concentration of fumaric acid reached 40.5 g/L with the yield of 0.55 g/g and the productivity of 0.61 g/L/h, which were 8.3%, 10.0% and 17.3% higher than the best result of constant pH control process. Its productivity was even 3.4% higher than which in CaCO3 case. With the internal advantages of reducing power consumption and simplifying downstream processing, using Na2CO3 as neutralizing agent under two-stage pH control strategy successfully take place of CaCO3.
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Received: 13 December 2012
Published: 25 April 2013
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[1] Liao W, Liu Y, Frear C, et al. Co-production of fumaric acid and chitin from a nitrogen-rich lignocellulosic material-dairy manure-using a pelletized filamentous fungus Rhizopus oryzae ATCC 20344. Bioresource Technology, 2008, 99(13):5859-5866. [2] Tao W Y, Collier J R, Collier B J, et al. Fumaric acid as an adhesion promoter in rayon/nylon composite fibers. Textile Research Journal,1993, 63(3):162-170. [3] Cao N, Du J, Chen C, et al. Production of fumaric acid by immobilized Rhizopus using rotary biofilm contactor Applied Biochemistry and Biotechnology, 1997, 63(1):387-394. [4] Fu Y Q, Li S, Chen Y, et al. Enhancement of fumaric acid production by Rhizopus oryzae using a two-stage dissolved oxygen control strategy. Applied Biochemistry and Biotechnology, 2010, 162(4):1031-1038. [5] Cao N, Du J, Gong C, et al. Simultaneous production and recovery of fumaric acid from immobilized Rhizopus oryzae with a rotary biofilm contactor and an adsorption column. Applied and Environmental Microbiology, 1996, 62(8):2926-2931. [6] Gangl I, Weigand W, Keller F A. Economic comparison of calcium fumarate and codium fumarate production by Rhizopus arrhizus. Applied Biochemistry and Biotechnology, 1990, 24(1):663-677. [7] Xu Q, Li S, Fu Y Q, et al. Two-stage utilization of corn straw by Rhizopus oryzae for fumaric acid production. Bioresource Technology, 2010, 101(15):6262-6264. [8] Rhodes R, Lagoda A, Misenheimer T, et al. Production of fumaric acid in 20-liter fermentors. Applied Microbiology, 1962, 10(1):9-15. [9] Rhodes R, Moyer A, Smith M, et al. Production of fumaric acid by Rhizopus arrhizus. Applied Microbiology, 1959, 7(2):74-80. [10] Zhou Y, Du J, Tsao G. Mycelial pellet formation by Rhizopus oryzae ATCC 20344. Applied Biochemistry and Biotechnology, 2000, 84(1-9):779-789. [11] Du J, Cao N, Gong C, et al. Fumaric acid production in airlift loop reactor with porous sparger. Applied Biochemistry and Biotechnology, 1997, 63(1):541-556. [12] Fu Y Q, Xu Q, Li S, et al. A novel multi-stage preculture strategy of Rhizopus oryzae ME-F12 for fumaric acid production in a stirred-tank reactor. World Journal of Microbiology and Biotechnology, 2009, 25(10):1871-1876. [13] Zhou Y, Du J, Tsao G T. Comparison of fumaric acid production by Rhizopus oryzae using different neutralizing agents. Bioprocess and Biosystems Engineering, 2002, (25):179-181. [14] Riscaldati E, Moresi M, Federici F, et al. Direct ammonium fumarate production by Rhizopus arrhizus under phosphorous limitation. Biotechnology Letters, 2000, 22(13):1043-1047. [15] Luedeking R, Piret E. A kinetic study of the lactic acid fermentation. Batch process at controlled pH. Biotechnology and Bioengineering, 2000, 67(6):636-644. [16] Presser K, Ratkowsky D, Ross T. Modelling the growth rate of Escherichia coli as a function of pH and lactic acid concentration. Applied and Environmental Microbiology, 1997, 63(6):2355. [17] Jernejc K, Legisa M. A drop of intracellular pH stimulates citric acid accumulation by some strains of Aspergillus niger. Journal of Biotechnology, 2004,112(3):289-297. [18] Ji X J, Huang H, Du J, et al. Enhanced 2,3-butanediol production by Klebsiella oxytoca using a two-stage agitation speed control strategy. Bioresource Technology, 2009, 100(13):3410-3414. [19] Engel C A R, Straathof A J J, Zijlmans T W, et al. Fumaric acid production by fermentation. Applied Microbiology and Biotechnology, 2008, 78(3):379-389. |
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