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  • 1
    Electronic Resource
    Electronic Resource
    Springer
    Applied microbiology and biotechnology 35 (1991), S. 144-148 
    ISSN: 1432-0614
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Summary Zymomonas mobilis is able to convert glucose and fructose to gluconic acid and sorbitol. The enzyme, glucose-fructose oxidoreductase, catalysing the intermolecular oxidation-reduction of glucose and fructose to gluconolactone and sorbitol, was formed in high amounts [1.4 units (U)·mg-1] when Z. mobilis was grown in chemostats with glucose as the only carbon source under non-carbon-limiting conditions. The activity of a gluconolactone-hydrolysing lactonase was constant at 0.2 U·mg-1. Using glucose-grown cells for the conversion of equimolar fructose and glucose mixtures up to 60% (w/v), a maximum product concentration of only 240 g·1-1 of sorbitol was found. The gluconic acid accumulated was further metabolized to ethanol. After permeabilizing the cells using cationic detergents, maximum sorbitol and gluconic acid concentrations of 295 g·1-1 each were reached; no ethanol production occurred. In a continuous process with κ-carrageenan-immobilized and polyethylenimin-hardened, permeabilized cells no significant decrease in the conversion yield was observed after 75 days. The specific production rates for a high yield conversion ( 〉 98%) in a continuous two-stage process were 0.19 g·g-1·h-1 for sorbitol and 0.21 g·g-1·h-1 for gluconic acid, respectively. For the sugar conversion of cetyltrimethylammonium bromide-treated κ-carrageenan-immobilized cells a V max of 1.7 g·g-1·h-1 for sorbitol production and a K m of 77.2 g·1-1 were determined
    Type of Medium: Electronic Resource
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  • 2
    ISSN: 1432-0614
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Summary Upon the addition of 2-hydroxybutyrate as precursor to strain DL4 of Corynebacterium glutamicum not only isoleucine is secreted, but also the biosynthetic intermediates 2-ketobutyrate (max. 3 mM) and 2-keto-3-methylvalerate (max. 5 mM). In addition, the decarboxylation products of several biosynthetic intermediates are formed. This decarboxylation occurs in part chemically. Due to the accumulation of 2-keto-3-methylvalerate and its decarboxylation product the following aminating reaction yielding isoleucine was assayed for limitation. The metabolite secretion of strains with a threefold increased transaminase activity obtained by genetic engineering was unaffected. The equilibrium constant of the transaminase reaction was determined as 0.5 with enriched enzyme, revealing that the reaction is nearly freely reversible and apparently not rate-limiting. From these facts it is concluded that the additional step of isoleucine secretion is most probably limiting and this has not been considered so far in any isoleucine production process.
    Type of Medium: Electronic Resource
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