Hydrostatically balanced gradient-formers: programming of gradients.

A novel in situ product recovery (ISPR) approach for the (fully) integrated separation of L-phenylalanine (L-phe) from a 20 l fed-batch process with the recombinant L-tyrosine auxotrophic strain E. coli F-4/pF81 is presented. The strain was rationally constructed for the production of the aromatic amino acid. Glucose and tyrosine control is used. A reactive extraction system consisting of kerosene, the cation-selective carrier D(2)EHPA and sulphuric acid, all circulating in liquid-liquid centrifuges, is applied for the on-line L-phe separation from cell- and protein-free permeate. Permeate is drained off from the bioreactor bypass. Using the novel ISPR approach, a significantly extended product formation period at 0.25 mmol/(g*h) together with a reduced by-product formation and a 28% relative glucose/L-phe yield increase is observed. Thus, the ISPR approach is superior to the reference non-ISPR process and even offers extraction rates approximately three times higher than the published membrane-based process.

Centrifugation, Density Gradient↗

PubMed2004

A model for sedimentation in inhomogeneous media. II. Compressibility of aqueous and organic solvents.

The effects of solvent compressibility on the sedimentation behavior of macromolecules as observed in analytical ultracentrifugation are examined. Expressions for the density and pressure distributions in the solution column are derived and combined with the finite element solution of the Lamm equation in inhomogeneous media to predict the macromolecular concentration distributions under different conditions. Independently, analytical expressions are derived for the sedimentation of non-diffusing particles in the limit of low compressibility. Both models are quantitatively consistent and predict solvent compressibility to result in a reduction of the sedimentation rate along the solution column and a continuous accumulation of solutes in the plateau region. For both organic and aqueous solvents, the calculated deviations from the sedimentation in incompressible media can be very large and substantially above the measurement error. Assuming conventional configurations used for sedimentation velocity experiments in analytical ultracentrifugation, neglect of the compressibility of water leads to systematic errors underestimating sedimentation coefficients by approximately 1% at a rotor speeds of 45000 rpm, but increasing to 2-5% with increasing rotor speeds and decreasing macromolecular size. The proposed finite element solution of the Lamm equation can be used to take solvent compressibility quantitatively into account in direct boundary models for discrete species, sedimentation coefficient distributions or molar mass distributions. Using the analytical expressions for the sedimentation of non-diffusing particles, the ls-g*(s) distribution of apparent sedimentation coefficients is extended to the analysis of sedimentation in compressible solvents. The consideration of solvent compressibility is highly relevant not only when using organic solvents, but also in aqueous solvents when precise sedimentation coefficients are needed, for example, for hydrodynamic modeling.

Centrifugation, Density Gradient↗

PubMed2004

Discontinuous Percoll gradient centrifugation combined with immunomagnetic separation obviates the need for erythrocyte lysis and yields isolated eosinophils with minimal granule abnormalities.

Isolated blood eosinophils are routinely used to study eosinophil activation mechanisms. However, as revealed by ultrastructural analysis, different isolation protocols may yield purified eosinophils with marked variability in granule electron density. In this study, using eosinophil peroxidase (EPO) histochemistry and transmission electron microscopy (TEM), we have compared the morphology of eosinophils in immediately fixed whole blood (to represent a morphological baseline) with isolated eosinophils purified by a number of protocols. Eosinophils in whole blood contained intact specific secondary granules of which a few exhibited marginal coarsening of matrix electron density (4% (95% CI: 2 to 7) altered granules per eosinophil). By contrast, eosinophils purified according to standard protocols, which included erythrocyte lysis with either ammonium chloride or distilled water, showed moderate to extensive loss in density of secondary granule core and/or matrix (NH4Cl: 62% (95% CI: 58 to 66); dH2O: 37% (95% CI: 30 to 44) altered granules). Stepwise analysis of eosinophils during the cell separation processes indicated that the granule abnormalities seen following erythrocyte lysis were further increased following immunomagnetic separation. However, when erythrocyte lysis was omitted, by use of a two-layered Percoll gradient (1.076 g/ml/1.088 g/ml) to which diluted whole blood was applied directly, eosinophils with minimal granule abnormalities (11% (95%CI: 9 to 13) altered granules) could be obtained after immunomagnetic separation. In conclusion, to obtain eosinophils with granule morphology more closely resembling the whole blood baseline phenotype, erythrocyte lysis should be avoided when separating eosinophils from human blood. Thus it will be possible to study in vitro the early transformation of resting eosinophils into the degranulating phenotype found in diseased tissues.

Centrifugation, Density Gradient↗