Innovative fermentation strategies for the production of extremophilic enzymes.

A new type of microfiltration (MF) bioreactor, developed in our laboratory, was investigated for use in improving efficiency of the production of extremophilic enzymes. In spite of the difficulties in cultivating hyperthermophiles, we achieved, in 300 h fermentation, more than 38 g/l dry weight of Sulfolobus solfataricus using a MF technique, and we demonstrated that the activity of alcohol dehydrogenase (ADH), as the reporter enzyme, was not affected by cell density. However, hyperthermophile cultivation is difficult to scale up because of evaporation and the very low growth rate. Thus, to achieve high productivity we cultivated, in the MF bioreactor, recombinant mesophilic hosts engineered for the production of two thermophilic enzymes, namely, trehalosyldextrin-forming enzyme (SsTDFE) and trehalose-forming enzyme (SsTFE) from Sulfolobus solfataricus. The traditional Luria-Bertani broth used for recombinant Escherichia coli growth was replaced with a semidefined medium. The latter was used in both the batch and the MF experiments, and the ratio of complex components (e.g., yeast extract and tryptone) to a simple carbon source (glycerol) was decreased during the fed-batch phase to further decrease the medium cost in view of industrial applications. The bioprocess developed was able to improve productivity 500 fold for rSsTFE and 60 fold for rSsTDFE with respect to the wild type cultivated in MF mode. Comparisons with another recombinant enzyme, alpha-glucosidase (rSsalphagly), from Sulfolobus solfataricus produced in our MF bioreactor are reported.

Effective production of a thermostable alpha-glucosidase from Sulfolobus solfataricus in Escherichia coli exploiting a microfiltration bioreactor.

A microfiltration (MF) membrane bioreactor was developed for an efficient production of a recombinant thermostable alpha-glucosidase (rSsGA) from Sulfolobus solfataricus MT-4. The aim of the membrane bioreactor was to improve the control of the concentration of key components in the growth of genetic engineered microorganisms, such as Escherichia coli. The influence of medium composition was studied in relation to cell growth and alpha-glucosidase production. The addition of components such as yeast extract and tryptone resulted in a higher enzyme production. High cell density cultivation of E. coli BL21(DE3) on semidefined medium, exploiting a microfiltration bioreactor, was studied in order to optimize rSsGA production. In addition to medium composition, the inducer employed (either isopropyl beta-D-thiogalactopyranoside or lactose), the induction duration, and the cultivation mode influenced both the final biomass and the enzyme yield. The MF bioreactor allowed a cell concentration of 50 g/L dry weight and a corresponding alpha-glucosidase production of 11,500 U/L. The improvement obtained in the enzyme production combining genetic engineering and the microfiltration strategy was estimated to be 2,000-fold the wild-type strain.