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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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 |
work_keys_str_mv |
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