Continuous extraction of a recombinant cutinase from Escherichia coli disrupted cells with reversed micelles using a perforated rotating disc contactor

Continuous annular chromatography: General characterization and application for the isolation of recombinant protein drugs

Isolation of recombinant protein drugs from cell culture supernatant is usually performed in batch mode, even if the fermentation process itself is continuous. As a novel approach, continuous separation techniques like continuous annular chromatography (CAC) can be used for continuous isolation. The potential of CAC for industrial application is demonstrated by continuous isolation of rFVIII from cell culture supernatant in pilot scale (i.e., 144-288 l/day). Thirty-fold concentration can be achieved at 94% yield, while purity is increased 3-5-fold. For this a batch direct feed ion exchange chromatography method was adapted to a commercial preparative CAC system (P-CAC). A headspace loading technique was used to maximize the concentration factor, while buffer incompatibility problems were addressed by a specifically modified inlet geometry. To allow sterile on-line coupling to FVIII-producing perfusion fermenters, an autoclavable pilot scale P-CAC prototype was developed. General characterization of P-CAC revealed a current limitation of the technology, i.e., variations in the outlet flow rates of up to +/-20%. These flow variations are shown to be caused mainly by a nonuniform annular resin bed and in turn result in "peak wobbling," i.e., the slight variation of peak position (up to +/-4 degrees ) and shape (e.g., A(s) = 0.9-1.4) as a specific function of column position. Some additional peak broadening, although less significant, is caused by a "peak oscillation" effect that results from the necessary segmentation of flow into discrete outlets. Both effects are only measurable if peaks are either monitored continuously or at least measured at multiple column positions. For isolation processes, these nonideal flow phenomena mean that more outlet streams have to be collected in order to achieve maximum yield and thus the achievable concentration factor is somewhat lower than the theoretical maximum.

Enzymatic esterification of ethanol by an immobilised Rhizomucor miehei lipase in a perforated rotating disc bioreactor

A perforated rotating disc bioreactor was developed to perform the esterification of ethanol with oleic acid, catalyzed by a lipase from Rhizomucor miehei immobilized by adsorption on to a hydrophobic support-Accurel EP700. The bioreactor with total recirculation operated at an optimum agitation rate of 400 rev./min. The experimental results, in this condition, were predict by a kinetic model using the constants obtained in the batch (Erlenmeyer flasks) assays: a catalytic constant, k(cat) = 5.78 mmol/h. mg protein; a Michaelis constant for ethanol, K(m(Et)) = 1.20 M; a Michaelis constant for oleic acid, K(m(Ol)) = 1.16 x 10(-8) M, and a dissociation constant of the ethanol-lipase complex, K((Et)) = 9.46 x 10(7) M. The efficiency of conversion gradually decreased during continuous operation of the reactor. The enzymatic activity decayed according to a first order deactivation model and the integrated equations of a continuous stirred tank reactor (CSTR) and a plug flow reactor (PFR). A half-life time of the lipase of about 10 days and a deactivation constant of 0.003 h(-1) were obtained in the present system.

Cutinase: from molecular level to bioprocess development

This review analyzes the role of cutinases in nature and their potential biotechnological applications. The cloning and expression of a fungal cutinase, Fusarium solani f. pisi, in Escherichia coli and Saccharomyces cerevisiae hosts are described. The three-dimensional structure of this cutinase is also analyzed and its function as a lipase is discussed and compared with other lipases. The biocatalytic applications of cutinase are described taking into account the preparation of different cutinase forms and the media in which the different types of reactions have been performed, namely hydrolysis, esterification, transesterification, and resolution of racemic mixtures. The stability of cutinase preparations is discussed and, in particular, the cutinase stability in anionic reversed micelles is analyzed considering the role of hexanol as a substrate, a cosurfactant, and a stabilizer. Process development, based on the operation of cutinase reactors, is also reviewed.