Design and economics of industrial production of fructooligosaccharides

2008 ◽  
Vol 62 (4) ◽  
Author(s):  
Katarína Vaňková ◽  
Zdenka Onderková ◽  
Monika Antošová ◽  
Milan Polakovič

AbstractA process for industrial production of fructooligosaccharides (FOS’s) based on the conversion of sucrose by immobilized fructosyltransferase (FTase) from the cells of Aureobasidium pullulans CCY 27-1-94 was developed. Particular process operations and conditions were designed employing results of laboratory and semi-pilot scale experiments. The process flowsheet comprised three sections: FTase production, which included fermentation, isolation and purification of the enzyme, FTase immobilization and FOS’s production where a product with a high content of FOS’s was prepared by the removal of glucose, fructose and unreacted sucrose from the reaction mixture using simulated moving-bed chromatography. Two alternative process flowsheets were proposed for the annual production of 10 000 t of FOS’s: one for a powdery product and the second one for syrup. The economic analysis provided the costs for the production of immobilized FTase and FOS’s using two different price estimates for sucrose.

Author(s):  
Ainoa Morillas-España ◽  
Tomás Lafarga ◽  
Francisco Gabriel Acién-Fernández ◽  
Cintia Gómez-Serrano ◽  
Cynthia Victoria González-López

1997 ◽  
Vol 45 (1) ◽  
pp. 109-115 ◽  
Author(s):  
G. Zhong ◽  
T. Yun ◽  
S. Khattabi ◽  
G. Guiochon

2020 ◽  
Vol 15 (10) ◽  
pp. 1934578X2096467
Author(s):  
Tai Thi Ngoc Dong ◽  
Chih-Hsiung Lin ◽  
Ming-Tsai Liang

In this study, the separation of ginsenosides from the crude extract of Sanchi ginseng and American ginseng, obtained by aqueous ethanol extraction, was conducted in a simulated moving bed (SMB) with cleaning in place (CIP) design. Concentrated products with 86.2%, w/w, and 91.5%, w/w, of ginsenosides were obtained by the utilization of CIP-SMB for Sanchi and American ginseng, respectively. This study reveals that CIP-SMB could enrich ginsenosides by removing the retained impurities, which were initially extracted by aqueous ethanol and not removed by either the antisolvent precipitation for Sanchi ginseng or the ethyl acetate extraction for American ginseng. Although the ginsenosides in both ginsengs are similar, the difficulty in applying chromatography to the crude extract differs. A natural crude extract normally contains compounds with significant difference in retention. A traditional SMB with 4 sections will be, consequently, unable to continuously separate the natural products. This study develops methods for pretreating the crude extract and demonstrates the feasibility of continuously separating ginsenosides by using SMB. SMB is an effective technology for large-scale chromatography and can generally resolve solvent and energy consumption problems. This is expected to promote the industrial use of SMB for the production of concentrated ginsenosides as active pharmaceutical ingredients.


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