Production and purification of fructo-oligosaccharides using an enzyme membrane bioreactor and subsequent fermentation with probiotic Bacillus coagulans

被引:26
作者
Fan, Rong [1 ,4 ]
Burghardt, Jan P. [1 ,2 ]
Prell, Florian [2 ,3 ]
Zorn, Holger [2 ,3 ,4 ]
Czermak, Peter [1 ,2 ,4 ]
机构
[1] Univ Appl Sci Mittelhessen, Inst Bioproc Engn & Pharmaceut Technol, D-35390 Giessen, Germany
[2] Justus Liebig Univ Giessen, Fac Biol & Chem, Heinreich Buff Ring 17-19, D-35392 Giessen, Germany
[3] Justus Liebig Univ Giessen, Inst Food Chem & Food Biotechnol, Heinreich Buff Ring 17-19, D-35392 Giessen, Germany
[4] Fraunhofer Inst Mol Biol & Appl Ecol IME, Inst Part Bioresources, Ohlebergsweg 12, D-35392 Giessen, Germany
关键词
Oligosaccharide; Ceramic membrane; Ultrafiltration; Enzyme membrane bioreactor; FOS purification; ULTRA SP-L; FLUX DECLINE; ULTRAFILTRATION; FRUCTOOLIGOSACCHARIDES; IMMOBILIZATION; FRUCTOSYLTRANSFERASE; COCULTURE; PROTEINS; ACID; PH;
D O I
10.1016/j.seppur.2020.117291
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Fructo-oligosaccharides (FOS) are low-calorie sweeteners that can be synthesized by the transfructosylation of sucrose using enzymes known as fructosyltransferases. However, enzymatic conversion is inhibited by the accumulation of glucose as a byproduct, which limits the conversion rate and yield. We therefore developed a semi-continuous production process in an enzyme membrane bioreactor (EMBR) system followed by fermentation with the probiotic bacterium Bacillus coagulans. Filtration experiments were conducted in total recycle mode to evaluate membrane fouling using the resistance-in-series model. We found that fouling was predominantly caused by the accumulation of proteins at the membrane surface, which accounted for 29.6-95.5% of the total filtration resistance depending on the conditions. Using these data, we were able to achieve a stable filtration flux that fulfilled the requirements of the EMBR system by regulating the filtration parameters. The average concentration of total FOS in the products of EMBR reached 270 g.L-1, which was 4.6% higher than the batch process. Subsequently, the crude FOS preparation was treated by fed-batch fermentation with B. coagulans. The monosaccharides in the reaction mix (glucose and fructose) were completely removed, increasing the concentration of FOS to 195.9 g.L-1 and the purity to 96.6%.
引用
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页数:9
相关论文
共 54 条
[1]   Ultrafiltration modeling of multiple solutes system for continuous cross-flow process [J].
Ahmad, A. L. ;
Chong, M. F. ;
Bhatia, S. .
CHEMICAL ENGINEERING SCIENCE, 2006, 61 (15) :5057-5069
[2]   Effect of pH on the fractionation of whey proteins with a ceramic ultrafiltration membrane [J].
Almecija, M. Carmen ;
Ibanez, Ruben ;
Guadix, Antonio ;
Guadix, Emilia M. .
JOURNAL OF MEMBRANE SCIENCE, 2007, 288 (1-2) :28-35
[3]  
[Anonymous], 2000, Curr Opin Endocrinol Diabetes Obes, DOI DOI 10.1097/00060793-200002000-00004
[4]   Immobilization of Pectinex Ultra SP-L to produce galactooligosaccharides [J].
Aslan, Yakup ;
Tanriseven, Aziz .
JOURNAL OF MOLECULAR CATALYSIS B-ENZYMATIC, 2007, 45 (3-4) :73-77
[5]   Fructo-oligosaccharides: Production, Purification and Potential Applications [J].
Bali, Vandana ;
Panesar, Parmjit S. ;
Bera, Manab B. ;
Panesar, Reeba .
CRITICAL REVIEWS IN FOOD SCIENCE AND NUTRITION, 2015, 55 (11) :1475-1490
[6]   Development and Characterization of an Enzyme Membrane Reactor for Fructo-Oligosaccharide Production [J].
Burghardt, Jan Philipp ;
Coletta, Luca Antonio ;
van der Bolt, Ramona ;
Ebrahimi, Mehrdad ;
Gerlach, Doreen ;
Czermak, Peter .
MEMBRANES, 2019, 9 (11)
[7]   Two-Step Production of Neofructo-Oligosaccharides Using Immobilized Heterologous Aspergillus terreus 1F-Fructosyltransferase Expressed in Kluyveromyces lactis and Native Xanthophyllomyces dendrorhous G6-Fructosyltransferase [J].
Burghardt, Jan Philipp ;
Baas, Markus ;
Gerlach, Doreen ;
Czermak, Peter .
CATALYSTS, 2019, 9 (08)
[8]  
Burghardt JP, 2018, IJPMBS, V7, P71, DOI [10.18178/ijpmbs.7.4.71-77, DOI 10.18178/IJPMBS.7.4.71-77]
[9]  
Burns DB, 1999, BIOTECHNOL BIOENG, V64, P27, DOI 10.1002/(SICI)1097-0290(19990705)64:1<27::AID-BIT3>3.0.CO
[10]  
2-E