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Fed-batch production of MCL-PHA with elevated 3-hydroxynonanoate content

With no inhibition of β-oxidation, Pseudomonas putida KT2440 produces medium-chain-length poly(3-hydroxyalkanoate) (MCL-PHA) with approximately 65 mol% 3-hydroxynonanoate (HN) from nonanoic acid. Production of PHA with higher HN content and an adjustable monomeric composition was obtained using acry...

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Detalles Bibliográficos
Autores principales: Jiang, Xuan Jade, Sun, Zhiyong, Ramsay, Juliana A, Ramsay, Bruce A
Formato: Online Artículo Texto
Lenguaje:English
Publicado: Springer 2013
Materias:
Acceso en línea:https://www.ncbi.nlm.nih.gov/pmc/articles/PMC3846598/
https://www.ncbi.nlm.nih.gov/pubmed/23987136
http://dx.doi.org/10.1186/2191-0855-3-50
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author Jiang, Xuan Jade
Sun, Zhiyong
Ramsay, Juliana A
Ramsay, Bruce A
author_facet Jiang, Xuan Jade
Sun, Zhiyong
Ramsay, Juliana A
Ramsay, Bruce A
author_sort Jiang, Xuan Jade
collection PubMed
description With no inhibition of β-oxidation, Pseudomonas putida KT2440 produces medium-chain-length poly(3-hydroxyalkanoate) (MCL-PHA) with approximately 65 mol% 3-hydroxynonanoate (HN) from nonanoic acid. Production of PHA with higher HN content and an adjustable monomeric composition was obtained using acrylic acid, a fatty acid β-oxidation inhibitor, together with nonanoic acid and glucose as co-substrates in fed-batch fermentations. Different monomeric compositions were obtained by varying the feeding conditions to impose different specific growth rates and inhibitor feed concentrations. At a nonanoic acid: glucose: acrylic acid feed mass ratio of 1.25: 1: 0.05 and a specific growth rate of 0.15 h(-1), 71.4 g L(-1) biomass was produced containing 75.5% PHA with 89 mol% HN at a cumulative PHA productivity of 1.8 g L(-1) h(-1).
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spelling pubmed-38465982013-12-06 Fed-batch production of MCL-PHA with elevated 3-hydroxynonanoate content Jiang, Xuan Jade Sun, Zhiyong Ramsay, Juliana A Ramsay, Bruce A AMB Express Original Article With no inhibition of β-oxidation, Pseudomonas putida KT2440 produces medium-chain-length poly(3-hydroxyalkanoate) (MCL-PHA) with approximately 65 mol% 3-hydroxynonanoate (HN) from nonanoic acid. Production of PHA with higher HN content and an adjustable monomeric composition was obtained using acrylic acid, a fatty acid β-oxidation inhibitor, together with nonanoic acid and glucose as co-substrates in fed-batch fermentations. Different monomeric compositions were obtained by varying the feeding conditions to impose different specific growth rates and inhibitor feed concentrations. At a nonanoic acid: glucose: acrylic acid feed mass ratio of 1.25: 1: 0.05 and a specific growth rate of 0.15 h(-1), 71.4 g L(-1) biomass was produced containing 75.5% PHA with 89 mol% HN at a cumulative PHA productivity of 1.8 g L(-1) h(-1). Springer 2013-08-29 /pmc/articles/PMC3846598/ /pubmed/23987136 http://dx.doi.org/10.1186/2191-0855-3-50 Text en Copyright © 2013 Jiang et al.; licensee Springer. http://creativecommons.org/licenses/by/2.0 This is an Open Access article distributed under the terms of the Creative Commons Attribution License (http://creativecommons.org/licenses/by/2.0), which permits unrestricted use, distribution, and reproduction in any medium, provided the original work is properly cited.
spellingShingle Original Article
Jiang, Xuan Jade
Sun, Zhiyong
Ramsay, Juliana A
Ramsay, Bruce A
Fed-batch production of MCL-PHA with elevated 3-hydroxynonanoate content
title Fed-batch production of MCL-PHA with elevated 3-hydroxynonanoate content
title_full Fed-batch production of MCL-PHA with elevated 3-hydroxynonanoate content
title_fullStr Fed-batch production of MCL-PHA with elevated 3-hydroxynonanoate content
title_full_unstemmed Fed-batch production of MCL-PHA with elevated 3-hydroxynonanoate content
title_short Fed-batch production of MCL-PHA with elevated 3-hydroxynonanoate content
title_sort fed-batch production of mcl-pha with elevated 3-hydroxynonanoate content
topic Original Article
url https://www.ncbi.nlm.nih.gov/pmc/articles/PMC3846598/
https://www.ncbi.nlm.nih.gov/pubmed/23987136
http://dx.doi.org/10.1186/2191-0855-3-50
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