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DC Field | Value | Language |
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dc.contributor.author | Panyachanakul T. | |
dc.contributor.author | Kitpreechavanich V. | |
dc.contributor.author | Tokuyama S. | |
dc.contributor.author | Krajangsang S. | |
dc.date.accessioned | 2021-04-05T03:21:59Z | - |
dc.date.available | 2021-04-05T03:21:59Z | - |
dc.date.issued | 2017 | |
dc.identifier.issn | 7173458 | |
dc.identifier.other | 2-s2.0-85034060952 | |
dc.identifier.uri | https://ir.swu.ac.th/jspui/handle/123456789/12996 | - |
dc.identifier.uri | https://www.scopus.com/inward/record.uri?eid=2-s2.0-85034060952&doi=10.1016%2fj.ejbt.2017.09.001&partnerID=40&md5=75279251f68e214b50155d13e05211b9 | |
dc.description.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 | |
dc.subject | Bacteria | |
dc.subject | Biodegradable polymers | |
dc.subject | Biodegradation | |
dc.subject | Bioreactors | |
dc.subject | Cell immobilization | |
dc.subject | Enzyme activity | |
dc.subject | Enzymes | |
dc.subject | Fermentation | |
dc.subject | Fermenters | |
dc.subject | Lactic acid | |
dc.subject | Process control | |
dc.subject | Productivity | |
dc.subject | Radioactive waste vitrification | |
dc.subject | Actinomycete | |
dc.subject | Batch fermentation | |
dc.subject | Continuous fermentation | |
dc.subject | Depolymerase | |
dc.subject | Fermentation process | |
dc.subject | Optimized conditions | |
dc.subject | Plastic wastes | |
dc.subject | Poly(DL-lactic acid) | |
dc.subject | Enzyme immobilization | |
dc.subject | polylactide | |
dc.subject | proteinase | |
dc.subject | Actinomadura | |
dc.subject | Actinomadura keratinilytica | |
dc.subject | aeration | |
dc.subject | Article | |
dc.subject | biotechnological production | |
dc.subject | continuous fermentation | |
dc.subject | enzyme activity | |
dc.subject | enzyme synthesis | |
dc.subject | fermentation | |
dc.subject | fermentation optimization | |
dc.subject | immobilized cell | |
dc.subject | nonhuman | |
dc.subject | repeated batch fermentation | |
dc.subject | scale up | |
dc.title | Poly(DL-lactide)-degrading enzyme production by immobilized Actinomadura keratinilytica strain T16-1 in a 5-L fermenter under various fermentation processes | |
dc.type | Article | |
dc.rights.holder | Scopus | |
dc.identifier.bibliograpycitation | Electronic Journal of Biotechnology. Vol 30, (2017), p.71-76 | |
dc.identifier.doi | 10.1016/j.ejbt.2017.09.001 | |
Appears in Collections: | Scopus 1983-2021 |
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