Optimization of process parameters and fermentation strategy for xylanase production in a stirred tank reactor using a mutant Aspergillus nidulans strain

The present work studied the optimization of aeration rate, agitation rate and oxygen transfer and the use of various batch fermentation strategies for xylanase production from a recombinant Aspergillus nidulans strain in a 3 L stirred tank reactor. Maximum xylanase production of 1250 U/mL with prod...

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Main Authors: Asmaa Abdella, Fernando Segato, Mark R. Wilkins
Format: Article
Language:English
Published: Elsevier 2020-06-01
Series:Biotechnology Reports
Subjects:
Online Access:http://www.sciencedirect.com/science/article/pii/S2215017X20300576
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spelling doaj-ca82c9d55aff445890de9c8bf3dc7a572020-11-25T03:41:25ZengElsevierBiotechnology Reports2215-017X2020-06-0126e00457Optimization of process parameters and fermentation strategy for xylanase production in a stirred tank reactor using a mutant Aspergillus nidulans strainAsmaa Abdella0Fernando Segato1Mark R. Wilkins2Department of Industrial Biotechnology, Genetic Engineering and Biotechnology Research Institute, University of Sadat City, PO Box 79, Sadat City, 22857 Egypt; Department of Biological Systems Engineering, University of Nebraska-Lincoln, 3605 Fair Street, Lincoln, NE, 68583-0726 USA; Industrial Agricultural Products Center, University of Nebraska-Lincoln, 3605 Fair Street, Lincoln, NE, 68583-0730 USASynthetic and Molecular Biology Laboratory, Department of Biotechnology, Lorena School of Engineering, University of São Paulo, Estrada Municipal do Campinho, s/n, Lorena, SP, BrazilDepartment of Biological Systems Engineering, University of Nebraska-Lincoln, 3605 Fair Street, Lincoln, NE, 68583-0726 USA; Industrial Agricultural Products Center, University of Nebraska-Lincoln, 3605 Fair Street, Lincoln, NE, 68583-0730 USA; Department of Food Science and Technology, 1901 N 21stSt. University of Nebraska-Lincoln, Lincoln, NE, 68588-6205 USA; Corresponding author at: University of Nebraska-Lincoln, 211 Chase Hall, PO Box 830726, Lincoln, NE, 68583-0726 USA.The present work studied the optimization of aeration rate, agitation rate and oxygen transfer and the use of various batch fermentation strategies for xylanase production from a recombinant Aspergillus nidulans strain in a 3 L stirred tank reactor. Maximum xylanase production of 1250 U/mL with productivity of 313 U/mL/day was obtained under an aeration rate of 2 vvm and an agitation rate of 400 rpm using batch fermentation. The optimum volumetric oxygen transfer coefficient (kLa) for efficient xylanase production was found to be 38.6 h−1. Fed batch mode and repeated batch fermentation was also performed with kLa was 38.6 h−1. Xylanase enzyme productivity increased to 327 with fed batch fermentation and 373 U/mL/day with repeated batch fermentation. Also, maximum xylanase activity increased to 1410 U/mL with fed batch fermentation and 1572 U/mL with repeated batch fermentation.http://www.sciencedirect.com/science/article/pii/S2215017X20300576XylanaseEnzymeFed batchRepeated batchOptimization
collection DOAJ
language English
format Article
sources DOAJ
author Asmaa Abdella
Fernando Segato
Mark R. Wilkins
spellingShingle Asmaa Abdella
Fernando Segato
Mark R. Wilkins
Optimization of process parameters and fermentation strategy for xylanase production in a stirred tank reactor using a mutant Aspergillus nidulans strain
Biotechnology Reports
Xylanase
Enzyme
Fed batch
Repeated batch
Optimization
author_facet Asmaa Abdella
Fernando Segato
Mark R. Wilkins
author_sort Asmaa Abdella
title Optimization of process parameters and fermentation strategy for xylanase production in a stirred tank reactor using a mutant Aspergillus nidulans strain
title_short Optimization of process parameters and fermentation strategy for xylanase production in a stirred tank reactor using a mutant Aspergillus nidulans strain
title_full Optimization of process parameters and fermentation strategy for xylanase production in a stirred tank reactor using a mutant Aspergillus nidulans strain
title_fullStr Optimization of process parameters and fermentation strategy for xylanase production in a stirred tank reactor using a mutant Aspergillus nidulans strain
title_full_unstemmed Optimization of process parameters and fermentation strategy for xylanase production in a stirred tank reactor using a mutant Aspergillus nidulans strain
title_sort optimization of process parameters and fermentation strategy for xylanase production in a stirred tank reactor using a mutant aspergillus nidulans strain
publisher Elsevier
series Biotechnology Reports
issn 2215-017X
publishDate 2020-06-01
description The present work studied the optimization of aeration rate, agitation rate and oxygen transfer and the use of various batch fermentation strategies for xylanase production from a recombinant Aspergillus nidulans strain in a 3 L stirred tank reactor. Maximum xylanase production of 1250 U/mL with productivity of 313 U/mL/day was obtained under an aeration rate of 2 vvm and an agitation rate of 400 rpm using batch fermentation. The optimum volumetric oxygen transfer coefficient (kLa) for efficient xylanase production was found to be 38.6 h−1. Fed batch mode and repeated batch fermentation was also performed with kLa was 38.6 h−1. Xylanase enzyme productivity increased to 327 with fed batch fermentation and 373 U/mL/day with repeated batch fermentation. Also, maximum xylanase activity increased to 1410 U/mL with fed batch fermentation and 1572 U/mL with repeated batch fermentation.
topic Xylanase
Enzyme
Fed batch
Repeated batch
Optimization
url http://www.sciencedirect.com/science/article/pii/S2215017X20300576
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