Enzymatic hydrolysis of inulin in a bioreactor coupled with an ultrafiltration membrane

被引:14
作者
Hang, Hua [1 ]
Mu, Wanmeng [1 ]
Jiang, Bo [1 ]
Zhao, Meng [1 ]
Zhou, Liuming [1 ,2 ]
Zhang, Tao [1 ]
Miao, Ming [1 ]
机构
[1] Jiangnan Univ, State Key Lab Food Sci & Technol, Wuxi 214122, Jiangsu, Peoples R China
[2] Roquette Amer, Keokuk, IA 52632 USA
关键词
Inulin; Arthrobacter aurescens SK 8.001; Ultrafiltration membrane bioreactor; IFTase; DFA III; SOY PROTEIN HYDROLYSATE; DFA-III; GALACTOSYL-OLIGOSACCHARIDES; REACTOR SYSTEM; FRUCTOTRANSFERASE; PURIFICATION;
D O I
10.1016/j.desal.2011.09.016
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The continuous enzymatic production of difructose anhydride III (DFA III) from inulin as a substrate using ultrafiltration membrane bioreactor (UFMB) system was investigated. DFA III is a non-digestible oligosaccharide and has recently attracted interest as prebiotics. In the paper presented below, native inulin fructotransferase (IFTase) from Arthrobacter aurescens SK 8.001 was used as enzyme to catalyze transfructosylation reaction to produce DFA III, competed against the hydrolysis of inulin. When the substrate concentration is 100 g/L, the largest amount of difructose anhydride III (DFA III) was produced by 6-h hydrolysis of inulin. To optimize DFA III yield, process conditions were obtained: E/S 30 U/g, temperature 60-70 degrees C, pH 5.0-7.0, and 1-h hydrolysis time. Compared with the batch reactor, IFTase could be reused and the productivity and purity of DFA III could attain about 2379 and 92% in the UFMB. An operation stability study showed that the UFMB system could maintain the steady production of DFA III for over 12 h, and periodic addition of fresh inulin solution and IFTase could be added to the bioreactor. (C) 2011 Elsevier B.V. All rights reserved.
引用
收藏
页码:309 / 315
页数:7
相关论文
共 17 条
[1]  
Anna G.-P., 2005, DESALINATION, V184, P105
[2]   SOY PROTEIN HYDROLYSIS IN MEMBRANE REACTORS [J].
CHERYAN, M ;
DEESLIE, WD .
JOURNAL OF THE AMERICAN OIL CHEMISTS SOCIETY, 1983, 60 (06) :1112-1115
[3]   Functional properties of soy protein hydrolysate produced from a continuous membrane reactor system [J].
Chiang, WD ;
Shih, CJ ;
Chu, YH .
FOOD CHEMISTRY, 1999, 65 (02) :189-194
[4]   Angiotensin I-converting enzyme inhibitor derived from soy protein hydrolysate and produced by using membrane reactor [J].
Chiang, WD ;
Tsou, MJ ;
Tsai, ZY ;
Tsai, TC .
FOOD CHEMISTRY, 2006, 98 (04) :725-732
[5]  
Cho CM, 1997, J MICROBIOL BIOTECHN, V7, P121
[6]   Membrane-assisted enzymatic production of galactosyl-oligosaccharides from lactose in a continuous process [J].
Czermak, P ;
Ebrahimi, M ;
Grau, K ;
Netz, S ;
Sawatzki, G ;
Pfromm, PH .
JOURNAL OF MEMBRANE SCIENCE, 2004, 232 (1-2) :85-91
[7]   A novel ceramic membrane reactor system for the continuous enzymatic synthesis of oligosaccharides [J].
Ebrahimi, M. ;
Placido, L. ;
Engel, L. ;
Ashaghi, K. Shams ;
Czermak, P. .
DESALINATION, 2010, 250 (03) :1105-1108
[8]  
Elena G.D., 2006, J MEMBRANE SCI, V273, P152
[9]   Membrane chromatography reactor system for the continuous synthesis of galactosyl-oligosaccharides [J].
Engela, Larisa ;
Ebrahimi, Mehrdad ;
Czermak, Peter .
DESALINATION, 2008, 224 (1-3) :46-51
[10]   Thermostable inulin fructotransferase (DFA III-producing) from Arthrobacter sp L68-1 [J].
Haraguchi, K ;
Yoshida, M ;
Ohtsubo, K .
CARBOHYDRATE POLYMERS, 2005, 59 (04) :411-416