The engineering effects of fluids flow on freely suspended biological macro-materials and macromolecules

Shear-induced changes in membrane fluidity during culture of a fragile dinoflagellate microalga

The commonly used shear protective agent Pluronic F68 (PF68) was toxic to the marine dinoflagellate microalga Protoceratium reticulatum, but had a shear-protective effect on it at concentrations of ≤ 0.5 g L(-1) . Supplementation of P. reticulatum cultures with PF68 actually increased the fluidity of the cell membrane; therefore, the shear protective effect of PF68 could not be ascribed to reduced membrane fluidity, an explanation that has been commonly used in relation to its shear protective effect on animal cells. Data are reported on the membrane fluidity of P. reticulatum and its response to the presence of PF68 under sublethal and lethal turbulence regimens. The membrane fluidity was found to depend strongly on the level of lipoperoxides in the cells produced under lethal agitation.

Entrapment in E. coli improves the operational stability of recombinant β-glycosidase CelB from Pyrococcus furiosus and facilitates biocatalyst recovery

beta-Glycosidase CelB from the hyperthermophilic archaeon Pyrococcus furiosus is a versatile biocatalyst that has been used for the hydrolysis and synthesis of beta-d-glycosidic compounds at high temperatures and in non-conventional solvents. In spite of its outstanding thermal stability, CelB is prone to inactivation in the presence of reducing sugars and through recirculation in loop enzyme reactors. Entrapment into E. coli cells was used here to improve the stability of recombinant CelB under conditions promoting strong inactivation. Glutardialdehyde-mediated protein cross-linking or rigidification of the cell membrane by adding magnesium ions was required to prevent release of CelB from within the cell into the bulk solution. In the presence of 1M glucose or when applying recirculation rates of 2.6 min(-1), the entrapped enzyme was around two-fold more stable at 80 degrees C than free CelB. The significance of the stabilisation was attenuated by the decrease in CelB initial activity which was due to cross-linking and glutardialdehyde concentration-dependent. Entrapment facilitated downstream processing of CelB and biocatalyst recovery in repeated batchwise conversions of lactose at elevated temperatures.

Impact of engineering flow conditions on plasmid DNA yield and purity in chemical cell lysis operations

Chemical lysis of bacterial cells using an alkaline solution containing a detergent may provide an efficient scalable means for selectively removing covalently closed circular plasmid DNA from high-molecular-weight contaminating cellular components including chromosomal DNA. In this article we assess the chemical lysis of E. coli cells by SDS in a NaOH solution and determine the impact of pH environment and shear on the supercoiled plasmid and chromosomal DNA obtained. Experiments using a range of plasmids from 6 kb to 113 kb determined that in an unfavorable alkaline environment, where the NaOH concentration during lysis is greater than 0.15 +/- 0.03 M (pH 12.9 +/- 0.2), irreversible denaturation of the supercoiled plasmid DNA occurs. The extent of denaturation is shown to increase with time of exposure and NaOH concentration. Experiments using stirred vessels show that, depending on NaOH concentration, moderate to high mixing rates are necessary to maximize plasmid yield. While NaOH concentration does not significantly affect chromosomal DNA contamination, a high NaOH concentration is necessary to ensure complete conversion of chromosomal DNA to single-stranded form. In a mechanically agitated lysis reactor the correct mixing strategy must balance the need for sufficient mixing to eliminate potential regions of high NaOH concentrations and the need to avoid excessive breakage of the shear sensitive chromosomal DNA. The effect of shear on chromosomal DNA is examined over a wide range of shear rates (10(1)-10(5) s(-1)) demonstrating that, while increasing shear leads to fragmentation of chromosomal DNA to smaller sizes, it does not lead to significantly increased chromosomal DNA contamination except at very high shear rates (about 10(4)-10(5) s(-1)). The consequences of these effects on the choice of lysis reactor and scale-up are discussed.