ArticleMicrobial cell factories2015
Cultivation strategies for production of (R)-3-hydroxybutyric acid from simultaneous consumption of glucose, xylose and arabinose by Escherichia coli.
Article in Microbial cell factories, 2015. The graph could read no effect estimate from its abstract, so it casts no vote on the map. Cited by 11 papers.
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11 citing papers in PubMed, 28 citations in OpenAlex.
- Sampling-free investigation of microbial carbon source preferences on renewable feedstocks via online monitoring of oxygen transfer rate.Bioprocess and biosystems engineering · 2025Article
- Citrate synthase variants improve yield of acetyl-CoA derived 3-hydroxybutyrate in Escherichia coli.Microbial cell factories · 2024Article
- Engineering of thioesterase YciA from Haemophilus influenzae for production of carboxylic acids.Applied microbiology and biotechnology · 2023Article
- Active pharmaceutical ingredient (API) chemicals: a critical review of current biotechnological approaches.Bioengineered · 2022Review
- Transcriptional profiling of the stringent response mutant strain E. coli SR reveals enhanced robustness to large-scale conditions.Microbial biotechnology · 2021Article
- Beyond Intracellular Accumulation of Polyhydroxyalkanoates: Chiral Hydroxyalkanoic Acids and Polymer Secretion.Frontiers in bioengineering and biotechnology · 2020Review
- Comparison of engineered Escherichia coli AF1000 and BL21 strains for (R)-3-hydroxybutyrate production in fed-batch cultivation.Applied microbiology and biotechnology · 2019Article
- The role of the acyl-CoA thioesterase "YciA" in the production of (R)-3-hydroxybutyrate by recombinant Escherichia coli.Applied microbiology and biotechnology · 2019Article
- Increasing the production of (R)-3-hydroxybutyrate in recombinant Escherichia coli by improved cofactor supply.Microbial cell factories · 2016Article
- Engineering Escherichia coli for production of 4-hydroxymandelic acid using glucose-xylose mixture.Microbial cell factories · 2016Article
- Regulating the production of (R)-3-hydroxybutyrate in Escherichia coli by N or P limitation.Frontiers in microbiology · 2015Article
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7 authors at 2 institutions in 2 countries.
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No grant is acknowledged in the PubMed record.
Abstract
backgroundLignocellulosic waste is a desirable biomass for use in second generation biorefineries. Up to 40% of its sugar content consist of pentoses, which organisms either take up sequentially after glucose depletion, or not at all. A previously described Escherichia coli strain, PPA652ara, capable of simultaneous consumption of glucose, xylose and arabinose was in the present work utilized for production of (R)-3-hydroxybutyric acid (3HB) from a mixture of glucose, xylose and arabinose.
resultsThe Halomonas boliviensis genes for 3HB production were for the first time cloned into E. coli PPA652ara, leading to product secretion directly into the medium. Process design was based on comparisons of batch, fed-batch and continuous cultivation, where both excess and limitation of the carbon mixture was studied. Carbon limitation resulted in low specific productivity of 3HB (<2 mg g(-1) h(-1)) compared to carbon excess (25 mg g(-1) h(-1)), but the yield of 3HB/cell dry weight (Y3HB/CDW) was very low (0.06 g g(-1)) during excess. Nitrogen-exhausted conditions could be used to sustain a high specific productivity (31 mg g(-1) h(-1)) and to increase the yield of 3HB/cell dry weight to 1.38 g g(-1). Nitrogen-limited fed-batch process design led to further increased specific productivity (38 mg g(-1) h(-1)) but also to additional cell growth (Y3HB/CDW=0.16 g g(-1)). Strain PPA652ara did under all processing conditions simultaneously consume glucose, xylose and arabinose, which was not the case for a reference wild type E. coli, which also gave a higher carbon flux to acetic acid.
conclusionsIt was demonstrated that by using E. coli PPA652ara, it was possible to design a production process for 3HB from a mixture of glucose, xylose and arabinose where all sugars were consumed. An industrial 3HB production process is proposed to be divided into a growth and a production phase, and nitrogen depletion/limitation is a potential strategy to maximize the yield of 3HB/CDW in the latter. The specific productivity of 3HB reported here from glucose, xylose and arabinose by E. coli is further comparable to the current state of the art for production from glucose sources.
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