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Fed-Batch Production of Saccharomyces cerevisiae L-Asparaginase II by Recombinant Pichia pastoris MUT(s) Strain

L-Asparaginase (ASNase) is used in the treatment of acute lymphoblastic leukemia, being produced and commercialized only from bacterial sources. Alternative Saccharomyces cerevisiae ASNase II coded by the ASP3 gene was biosynthesized by recombinant Pichia pastoris MUT(s) under the control of the AOX...

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Detalles Bibliográficos
Autores principales: Rodrigues, David, Pillaca-Pullo, Omar, Torres-Obreque, Karin, Flores-Santos, Juan, Sánchez-Moguel, Ignacio, Pimenta, Marcela V., Basi, Tajindar, Converti, Attilio, Lopes, André M., Monteiro, Gisele, Fonseca, Luís P., Pessoa, Adalberto Jr.
Formato: Online Artículo Texto
Lenguaje:English
Publicado: Frontiers Media S.A. 2019
Materias:
Acceso en línea:https://www.ncbi.nlm.nih.gov/pmc/articles/PMC6375902/
https://www.ncbi.nlm.nih.gov/pubmed/30800657
http://dx.doi.org/10.3389/fbioe.2019.00016
Descripción
Sumario:L-Asparaginase (ASNase) is used in the treatment of acute lymphoblastic leukemia, being produced and commercialized only from bacterial sources. Alternative Saccharomyces cerevisiae ASNase II coded by the ASP3 gene was biosynthesized by recombinant Pichia pastoris MUT(s) under the control of the AOX1 promoter, using different cultivation strategies. In particular, we applied multistage fed-batch cultivation divided in four distinct phases to produce ASNase II and determine the fermentation parameters, namely specific growth rate, biomass yield, and enzyme activity. Cultivation of recombinant P. pastoris under favorable conditions in a modified defined medium ensured a dry biomass concentration of 31 g(dcw).L(−1) during glycerol batch phase, corresponding to a biomass yield of 0.77 g(dcw.)g [Formula: see text] and a specific growth rate of 0.21 h(−1). After 12 h of glycerol feeding under limiting conditions, cell concentration achieved 65 g(dcw.)L(−1) while ethanol concentration was very low. During the phase of methanol induction, biomass concentration achieved 91 g(dcw.)L(−1), periplasmic specific enzyme activity 37.1 U.g [Formula: see text] , volumetric enzyme activity 3,315 U.L(−1), overall enzyme volumetric productivity 31 U.L(−1).h(−1), while the specific growth rate fell to 0.039 h(−1). Our results showed that the best strategy employed for the ASNase II production was using glycerol fed-batch phase with pseudo exponential feeding plus induction with continuous methanol feeding.