Innovative fermentation strategies for the production of extremophilic enzymes

• Published in: Extremophiles (Tokyo. Print) 2001-06, Vol.5 (3), p.193-198
• Main Authors: SCHIRALDI, Chiara, ACONE, Margherita, GIULIANO, Mariateresa, CARTENI, Maria, DE ROSA, Mario
• Format: Article
• Language: English
• Subjects: Biological and medical sciences; Bioreactors; Biotechnology; Dextrins - biosynthesis; Enzyme engineering; Enzymes - biosynthesis; Enzymes - genetics; Enzymes - isolation & purification; Escherichia coli - enzymology; Escherichia coli - genetics; Escherichia coli - growth & development; Fermentation; Filtration; Fundamental and applied biological sciences. Psychology; Genetic Engineering; Glucosyltransferases - biosynthesis; Glucosyltransferases - genetics; Glucosyltransferases - isolation & purification; Methods. Procedures. Technologies; Production of selected enzymes; Space life sciences; Sulfolobus - enzymology; Sulfolobus - genetics; Trehalose - biosynthesis
• ISSN: 1431-0651; 1433-4909
• DOI: 10.1007/s007920100194

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.