Continuous production of chitooligosaccharides by an immobilized enzyme in a dual-reactor system

[EN] A chitosanolytic activity found in a commercial α-amylase from Bacillus amylolyquefaciens (BAN) was covalently immobilized onto glyoxal agarose beads (25% recovery of activity) and assessed for the continuous production of chitooligosaccharides (COS). The immobilization did not change the react...

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Detalles Bibliográficos
Autores: Santos-Moriano, Paloma, Woodley, John M., Plou Gasca, Francisco José
Tipo de recurso: artículo
Fecha de publicación:2016
País:España
Institución:Consejo Superior de Investigaciones Científicas (CSIC)
Repositorio:DIGITAL.CSIC. Repositorio Institucional del CSIC
OAI Identifier:oai:digital.csic.es:10261/220641
Acceso en línea:http://hdl.handle.net/10261/220641
Access Level:acceso abierto
Palabra clave:Chitooligosaccharides
Chitosanolytic enzymes
Covalent immobilization
Packed-bead reactor
Glyoxal agarose
Process optimization
Descripción
Sumario:[EN] A chitosanolytic activity found in a commercial α-amylase from Bacillus amylolyquefaciens (BAN) was covalently immobilized onto glyoxal agarose beads (25% recovery of activity) and assessed for the continuous production of chitooligosaccharides (COS). The immobilization did not change the reaction profile (with chitotriose and chitobiose as major products, using chitosans of different polymerization and deacetylation degrees), but significantly increased the enzyme thermostability. A two-step process was proposed, in which chitosan was first hydrolyzed in a batch reactor to a viscosity that could flow through a packed-bead reactor (PBR), thus avoiding clogging of the column. The relationship between hydrolysis degree of chitosan (1% w/v) and viscosity of the solution was assessed in a batch reactor. A 50% hydrolyzed chitosan did not cause any clogging of the PBR. Under these conditions, the productivity of the PBR at the lowest dilution rate was 37 g L h, with a conversion yield of 73%. In contrast, at the highest dilution rate, the productivity was nearly 200 g L h, but the conversion yield dropped to around 40%.