| Literature DB >> 24889547 |
Devchand N Avhad1, Virendra K Rathod2.
Abstract
The present work illustrates ultrasound assisted production of a fibrinolytic enzyme at 1L bioreactor scale from Bacillus sphaericus MTCC 3672. To alleviate the shortcomings of one factor at a time method of optimization, central composite rotatable design of response surface methodology was employed for optimization of ultrasound assisted production. Different process parameters such as irradiation time, duty cycle and power of ultrasound were varied in 3 different levels in 11 experimental runs. For evaluating mass transfer enhancement effect of ultrasonication on production, control non sonicated fermentation was optimized by varying different agitation speed (300-500rpm) and aeration rate (8.33-33.33cc/s). Optimized ultrasonication protocol resulted in 1.48-fold increase in fibrinolytic enzyme yield as compared to non sonicated fermentation, which comprised of ultrasound irradiation at 25kHz for 10min with 40% duty cycle and 160W power on 12h of growth phase in 1L bioreactor operated at 400rpm agitation speed and 16.66cc/s aeration rate. Declined glucose concentration from 0.1% w/v (non sonicated control run) to 0.05% w/v and breakage of cells cluster emphasized on increased substrate utilization potential and enhanced convection of ultrasound assisted fermentation in a bioreactor. Deliverables of current studies will provide significant insights for enhancement of productivity of various enzymes at a bioreactor level.Entities:
Keywords: Aeration rates; Agitation speed; Bacillus sphaericus; Mass transfer enhancement; Response surface methodology; Ultrasound assisted fermentation
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Year: 2014 PMID: 24889547 DOI: 10.1016/j.ultsonch.2014.04.020
Source DB: PubMed Journal: Ultrason Sonochem ISSN: 1350-4177 Impact factor: 7.491