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Title: | Poly(DL-lactide)-degrading enzyme production by immobilized Actinomadura keratinilytica strain T16-1 in a 5-L fermenter under various fermentation processes |
Authors: | Panyachanakul T. Kitpreechavanich V. Tokuyama S. Krajangsang S. |
Keywords: | Bacteria Biodegradable polymers Biodegradation Bioreactors Cell immobilization Enzyme activity Enzymes Fermentation Fermenters Lactic acid Process control Productivity Radioactive waste vitrification Actinomycete Batch fermentation Continuous fermentation Depolymerase Fermentation process Optimized conditions Plastic wastes Poly(DL-lactic acid) Enzyme immobilization polylactide proteinase Actinomadura Actinomadura keratinilytica aeration Article biotechnological production continuous fermentation enzyme activity enzyme synthesis fermentation fermentation optimization immobilized cell nonhuman repeated batch fermentation scale up |
Issue Date: | 2017 |
Abstract: | Background Poly(DL-lactic acid), or PDLLA, is a biodegradable polymer that can be hydrolyzed by various types of enzymes. The protease produced by Actinomadura keratinilytica strain T16-1 was previously reported to have PDLLA depolymerase activity. However, few studies have reported on PDLLA-degrading enzyme production by bacteria. Therefore, the aims of this study were to determine a suitable immobilization material for PDLLA-degrading enzyme production and optimize PDLLA-degrading enzyme production by using immobilized A. keratinilytica strain T16-1 under various fermentation process conditions in a stirrer fermenter. Results Among the tested immobilization materials, a scrub pad was the best immobilizer, giving an enzyme activity of 30.03 U/mL in a shake-flask scale. The maximum enzyme activity was obtained at aeration 0.25 vvm, agitation 170 rpm, 45°C, and 48 h of cultivation time. Under these conditions, a PDLLA-degrading enzyme production of 766.33 U/mL with 15.97 U/mL·h productivity was observed using batch fermentation in a 5-L stirrer fermenter. Increased enzyme activity and productivity were observed in repeated-batch (942.67 U/mL and 19.64 U/mL·h) and continuous fermentation (796.43 U/mL and 16.58 U/mL·h) at a dilution rate of 0.013/h. Scaled-up production of the enzyme in a 10-L stirrer bioreactor using the optimized conditions showed a maximum enzyme activity of 578.67 U/mL and a productivity of 12.06 U/mL·h. Conclusions This research successfully scaled-up the enzyme production to 5 and 10 L in a stirrer fermenter and is helpful for many applications of poly(lactic acid). © 2017 |
URI: | https://ir.swu.ac.th/jspui/handle/123456789/12996 https://www.scopus.com/inward/record.uri?eid=2-s2.0-85034060952&doi=10.1016%2fj.ejbt.2017.09.001&partnerID=40&md5=75279251f68e214b50155d13e05211b9 |
ISSN: | 7173458 |
Appears in Collections: | Scopus 1983-2021 |
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