Abstract
Cyclodextrin-glycosyl-transferase (EC2.4.1.19), produced by Wacker (Munich, Germany), was purified by biospecific affinity chromatography with β-cyclodextrin (β-CD) as ligand, and immobilized into controlled pore silica particles (0.42 mm). This immobilized enzyme (IE) had 4.7 mg of protein/g of support and a specific activity of 8.6 μmol of β-CD/(min·gIF) at 50°C, pH 8.0. It was used in a fluidized-bed reactor (FBR) at the same conditions for producing cyclodextrins (CDs) with 10% (w/v) maltodextrin solution as substrate. Bed expansion was modeled by the Richardson and Zaki equation, giving a good fit in two distin ctranges of bed porosities. The minimum fluidization velocity was 0.045 cm/s, the bed expansion coefficient was 3.98, and the particle terminal velocity was 2.4 cm/s. The FBR achieved high productivity, reaching in only 4 min of residence time the same amount of CDs normally achieved in a batch reactor with free enzyme after 24h of reaction, namely, 10.4 mM β-CD and 2.3 mM γ-CD.
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Tardioli, P.W., Zanin, G.M. & de Moraes, F.F. Production of cyclodextrins in a fluidized-bed reactor using cyclodextrin-glycosyl-transferase. Appl Biochem Biotechnol 84, 1003–1019 (2000). https://doi.org/10.1385/ABAB:84-86:1-9:1003
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DOI: https://doi.org/10.1385/ABAB:84-86:1-9:1003