Trehalose production at high temperature exploiting an immobilized cell bioreactor.

Abstract

The enzymatic production of trehalose from dextrins was studied as a series reaction in a packed bed reactor containing immobilized recombinant Escherichia coli cells, expressing either the Sulfolobus solfataricus (strain MT4) trehalosyl-dextrin forming enzyme (TDFE) or the trehalose-forming enzyme (TFE). The cells, subjected to thermal treatments to increase cell permeability and to inactivate the unwanted host proteins, were entrapped separately or together in a calcium alginate polymeric matrix. The biocatalyst beads were used to pack a tubular glass reactor that was operated in a recycle mode. The performances of a bioreactor containing alternate layers of EcTFE and EcTDFE alginate beads were evaluated and compared with the performance of the co-immobilized biocatalysts. The latter showed a superior throughput, therefore the bioreactor packed with the co-entrapped biocatalysts was tested for the production of trehalose from concentrated dextrin solutions (10%-30% w/v) and a conversion up to 90% was obtained. This conversion corresponded to a production of 127 g trehalose h(-1) kg(-1) of biocatalyst. The results obtained suggest that the bioprocess described may be of interest in the development of a large-scale industrial process for trehalose production at high temperature.