Published: CABEQ 32 (2) (2018) 267–274
Paper type: Original Scientific Paper
T. Chysirichote
Abstract
Solid-state fermentation (SSF) has been used to produce value-added products from
agricultural and food processing wastes, but the majority of SSF production has been
conducted on a small scale due to the limitations of heat and mass transfer. This research
aimed to reduce the temperature changes in packed-bed bioreactor during the cellulase
fermentation of Aspergillus niger ATCC 16888 on copra waste from coconut milk process. The three configurations of bioreactor used in this study consisted of one- (control), two- and three-layered packed-bed bioreactors. Total volumes of packed-bed bioreactor and bed material were 127 and 57 L, respectively. The sterilized air 30 °C was forced from the bottom of bioreactor at 0.20 vvm. The highest cellulase production (5.0 ± 0.4 FPU g–1DS) was obtained from the bottom zone of the three-layered bioreactor after fermenting for 1 d. However, the greatest growth was found at the top one, in which a large amount of aerial mycelium was detected.
(This work is licensed under a Creative Commons Attribution 4.0 International License.)
This work is licensed under a Creative Commons Attribution 4.0 International License
Keywords
cellulase, solid-state fermentation, packed-bed bioreactor, Aspergillus niger