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(Reference retrieved automatically from Web of Science through information on FAPESP grant and its corresponding number as mentioned in the publication by the authors.)

Extractive Fermentation of Clavulanic Acid by Streptomyces DAUFPE 3060 Using Aqueous Two-Phase System

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Author(s):
Viana Marques, D. A. [1] ; Pessoa-Junior, A. [1] ; Lima-Filho, J. L. [2] ; Converti, A. [3] ; Perego, P. [3] ; Porto, A. L. F. [4]
Total Authors: 6
Affiliation:
[1] Univ Sao Paulo, Dept Pharmaceut Technol & Biochem, BR-05508000 Sao Paulo - Brazil
[2] Univ Fed Pernambuco, Dept Biochem, BR-50670901 Recife, PE - Brazil
[3] Univ Genoa, Dept Chem & Proc Engn, I-16145 Genoa - Italy
[4] Univ Fed Rural Pernambuco, Dept Anim Morphol & Physiol, BR-52171900 Dois Irmaos, PE - Brazil
Total Affiliations: 4
Document type: Journal article
Source: BIOTECHNOLOGY PROGRESS; v. 27, n. 1, p. 95-103, JAN-FEB 2011.
Web of Science Citations: 16
Abstract

The influence of four variables, specifically PEG molar mass (400, 1,000, and 8,000 g/mol), concentrations of PEG and phosphate salts (15, 20, and 25% for both), and agitation intensity (110, 150, and 200 rpm), on clavulanic acid (CA) extraction by extractive fermentation with PEG/phosphate salts aqueous two-phase system was investigated in shaken flasks using a 2(4-1)-fractional factorial design. After selection of the two most significant variables (agitation intensity and PEG molar mass), an optimization study conducted according to a 2(2)-central composite design revealed that 25% PEG 8,000 g/mol and phosphate salts at 240 rpm (run 6) were the best conditions for the extractive fermentation, leading to the best results in terms of partition coefficient (k = 8.2), yield of CA in the PEG-rich phase (eta(T) = 93%) and productivity (P = 5.3 mg/Lh). As a first attempt to make a scale-up of these results, the effectiveness of the extractive fermentation was then checked in a bench-scale bioreactor under conditions as close as possible to the optimum ones determined in flasks. The highest CA concentration obtained in the PEG-rich phase (691 mg/L) was 30% higher than in flasks, thus demonstrating the potential of such a new process, integrating the production and extraction steps, as a promising, low-cost tool to obtain high yields of this and similar products. (C) 2010 American Institute of Chemical Engineers Biotechnol. Prog., 27: 95-103, 2011 (AU)