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Cultivation strategies for production of (R)-3-hydroxybutyric acid from simultaneous consumption of glucose, xylose and arabinose by Escherichia coli

Jarmander, Johan (författare)
KTH,Industriell bioteknologi
Belotserkovsky, Jaroslav (författare)
KTH,Industriell bioteknologi
Sjöberg, Gustav (författare)
KTH,Industriell bioteknologi
visa fler...
Guevara-Martínez, Mónica (författare)
KTH,Industriell bioteknologi,Universidad Mayor de San Simón, Bolivia
Zabaleta, Mariel Perez (författare)
KTH,Industriell bioteknologi,Universidad Mayor de San Simón, Bolivia
Quillaguaman, Jorge (författare)
Universidad Mayor de San Simón, Bolivia
Larsson, Gen (författare)
KTH,Industriell bioteknologi
visa färre...
 (creator_code:org_t)
2015-04-11
2015
Engelska.
Ingår i: Microbial Cell Factories. - : BioMed Central. - 1475-2859. ; 14:1, s. 51-
  • Tidskriftsartikel (refereegranskat)
Abstract Ämnesord
Stäng  
  • 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 lead 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 the strain 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 by E. coli reported here from glucose, xylose and arabinose is further comparable to the current state of the art for production of 3HB from glucose sources.

Ämnesord

NATURVETENSKAP  -- Biologi (hsv//swe)
NATURAL SCIENCES  -- Biological Sciences (hsv//eng)

Nyckelord

Escherichia coli
3-Hydroxybutyric acid
3HB
simultaneous uptake
lignocellulose
production process
nitrogen limitation
Bioteknologi
Biotechnology

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