Continuous production of oligosaccharides from whey using a membrane reactor

被引:52
作者
Foda, MI [1 ]
Lopez-Leiva, M [1 ]
机构
[1] Univ Lund, Dept Food Engn, S-22100 Lund, Sweden
关键词
oligosaccarides; membrane reactor; milk whey; hydrolysis; UF-permeate;
D O I
10.1016/S0032-9592(99)00108-9
中图分类号
Q5 [生物化学]; Q7 [分子生物学];
学科分类号
071010 ; 081704 ;
摘要
Whey permeate (containing 14, 20 or 23% lactose) was used in the continuous production of oligosaccharides (OS) by hydrolysis from Maxilact 2000 L (Kluyveromyces lactis beta-D-galacosidase). Two types of membrane reactors were used: a laboratory scale, Amicon stirred cell, using a flat membrane (41.8 cm(2)) and a pilot plant-scale membrane reactor using a Romicon hollow fiber cartridge (0.5 m(2)). Batch experiments were run to determine the optimal reaction time (when the largest amount of OS are produced). This optimal reaction time was then used in the experiments in continuous mode as the mean residence time of the whey permeate in the reactor, which could be controlled by adjusting the rate of permeate and or the volume of the substrate in the system. (C) 2000 Elsevier Science Ltd. All rights reserved.
引用
收藏
页码:581 / 587
页数:7
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