Optimization of inulinase production by solid-state fermentation in a packed-bed bioreactor

被引:30
作者
Mazutti, Marcio A. [1 ,2 ]
Zabot, Giovani [1 ]
Boni, Gabriela [1 ]
Skovronski, Aline [1 ]
de Oliveira, Debora [1 ]
Di Luccio, Marco [1 ]
Rodrigues, Maria Isabel [2 ]
Treichel, Helen [1 ]
Maugeri, Francisco [2 ]
机构
[1] Univ Reg Integrada Alto Uruguai & Missoes, Dept Food Engn, BR-99700000 Erechim, RS, Brazil
[2] Univ Estadual Campinas, Dept Food Engn, BR-13083862 Campinas, SP, Brazil
关键词
solid-state; packed-bed bioreactor; optimization; agroindustrial residues; SUGARCANE BAGASSE;
D O I
10.1002/jctb.2273
中图分类号
Q81 [生物工程学(生物技术)]; Q93 [微生物学];
学科分类号
071005 ; 0836 ; 090102 ; 100705 ;
摘要
BACKGROUND: This work is focused on inulinase production by solid-sate fermentation (SSF) using sugarcane bagasse, corn steep liquor (CSL), pre-treated cane molasses, and soybean bran as substrates in a 3-kg (dry basis) packed-bed bioreactor. SSF was carried out by the yeast Kluyveromyces marxianus NRRL Y-7571 and response surface methodology was used to optimize the temperature, air flow rate and initial mass of cells. RESULTS: The optimum inulinase activity (436.7 +/- 36.3 U g(-1) dry substrate) was obtained at 24 h at an inlet air temperature of 30 degrees C, air flow rate 2.2 m(3) h(-1) and 22 g of cells for fermentation. Inulinase productivity at these conditions was 18.2 U gds(-1) h(-1). Kinetic evaluation at the optimized conditions showed that the maximum inulinase production was verified at 24 h of fermentation. The carbon dioxide and the metabolic heat generation are directly associated with the consumption of total reducing sugars present in the medium. CONCLUSION: The high productivity achieved in this work shows the technical viability of inulinase production by SSF in a packed-bed bioreactor. (C) 2009 Society of Chemical Industry
引用
收藏
页码:109 / 114
页数:6
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