Simultaneous isoquercitin and gallic acid production of <i>Aspergillus niger</i> on Triphala byproduct under solid state fermentation in packed-bed bioreactor

Author:

Pakaweerachat Pattarabhorn12,Klinthong Worasaung3,Ohtaguchi Kazuhisa4,Chysirichote Teerin1

Affiliation:

1. Department of Food Engineering, School of Engineering, King Mongkut's Institute of Technology Ladkrabang, 1, Chalongkrung 1 Road, Ladkrabang, Bangkok 10520, Thailand

2. Faculty of Home Economics Technology, Department of Food and Nutrition, Rajamangala University of Technology Krungthep, 2, Nanglinchi Road, Tungmahamek, Sathorn, Bangkok 10120, Thailand

3. Greenday Global Co., ltd. 829, Moo 2, Bangpoo Industrail Estate (North), Phraeksa Mai, Mueang Samutprakarn, Samutprakarn 10280, Thailand

4. Department of Chemical Engineering, Tokyo Institute of Technology, 2-12-1 Ookayama, Meguroku, Tokyo 152-8550, Japan

Abstract

<abstract> <p>Triphala byproduct from hot-water extraction (TPB), which was a traditional process, was valorized by solid state fermentation in this research. Since the leftovers from the extraction contain high rutin and tannin contents, they were hydrolysable to isoquercitin and gallic acid, which were their monomers, respectively. <italic>Aspergillus niger</italic>, a producer of α-L-rhamnosidase and β-glucosidase, was cultured on the TPB to produce both isoquercitin and gallic acid, which were powerful antioxidants used in medical applications. The solid-state fermentation (SSF) was conducted in the three-layered packed-bed bioreactor aerated with humid air at different rates (0.1, 0.2 and 0.3 L/L/min or vvm). The highest isoquercitin and gallic acid production rates were found in the SSF, with 0.1 vvm at 1.14/h and 0.3 vvm at 3.12/h, respectively. The interaction of aeration rate and fermentation time significantly affected the fungal growth and the production of gallic acid, while the isoquercitin production was affected only by the fermentation time. Moreover, the differences of their production yields in different positions of bed along the height of bioreactor found to be useful to design the harvesting period of the fermentation products including isoquercitin or gallic acid or simultaneous isoquercitin and gallic acid. The results clearly showed that aeration, harvesting time, and position of the bioreactor were crucial in designing the process for isoquercitin, gallic acid, or both.</p> </abstract>

Publisher

American Institute of Mathematical Sciences (AIMS)

Subject

Agricultural and Biological Sciences (miscellaneous),Food Science

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