Publications by authors named "M H Szczesna-Antczak"

Chitin is one of the most abundant biopolymers. Due to its recalcitrant nature and insolubility in accessible solvents, it is often considered waste and not a bioresource. The products of chitin modification such as chitosan and chitooligosaccharides are highly sought, but their preparation is a challenging process, typically performed with thermochemical methods that lack specificities and generate hazardous waste.

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The fungus Mucor circinelloides exhibits high potential for green chemistry and technological applications. Recently M. circinelloides, which so far was considered mainly as a platform for biodiesel production, was found to exhibit high ene-reductase activity.

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Chitin and its N-deacetylated derivative chitosan are two biological polymers that have found numerous applications in recent years, but their further deployment suffers from limitations in obtaining a defined structure of the polymers using traditional conversion methods. The disadvantages of the currently used industrial methods of chitosan manufacturing and the increasing demand for a broad range of novel chitosan oligosaccharides (COS) with a fully defined architecture increase interest in chitin and chitosan-modifying enzymes. Enzymes such as chitinases, chitosanases, chitin deacetylases, and recently discovered lytic polysaccharide monooxygenases had attracted considerable interest in recent years.

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The goal of this study was to increase the cost-effectiveness of oil production by an oleaginous and lipolytic strain M. circinelloides IBT-83, by optimizing both lipids accumulation in the mycelium containing intracellular lipases, and a one-step process coupling lipids extraction and enzymatic trans/esterification. In optimal conditions (culture medium composed of corn steep solids, plant oil, glucose and NO) over 50g/dm of biomass containing over 60% of lipids was produced.

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Mucor circinelloides IBT-83 mycelium that exhibits both lipolytic (A) and chitosanolytic (A) activities was immobilized into polyurethane foam in a 30 L laboratory fermenter. The process of immobilization was investigated in terms of the carrier porosity, its type, amount, and shape, location inside the fermenter, mixing, and aeration parameters during the culture, as well as downstream processing operations. The selected conditions allowed for immobilization of approximately 7 g of defatted and dried mycelium in 1 g of carrier, i.

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