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Biomedical subjects

P Dhulster

Publications and source records attributed to P Dhulster.

12 recordsLinked to original sources

Real time in situ microscopy for animal cell-concentration monitoring during high density culture in bioreactor.

An in situ microscope (ISM) device is utilised in this study to monitor hybridoma cells concentration in a stirred bioreactor. It generates images by using pulsed illumination of the liquid broth synchronised with the camera frame generation to avoid blur from the cell's motion. An appropriate image processing isolates the sharp objects from the blurred ones that are far from the focal plane. As image processing involves several parameters, this paper focuses on the robustness of the results of the cells counting. This stage determines the applicability of the measuring device and has seldom been tackled in the presentations of ISM devices. Calibration is secondly performed for assessing the cell-concentration from the cell automated numeration provided by the ISM. Flow cytometry and hemacytometer chamber were used as reference analytical methods. These measures and the output of the image processing allow estimating a single calibration parameter: the reference volume per image equal to 1.08 x 10(-6) mL. In these conditions, the correlation coefficient between both reference and ISM data sets becomes equal to 0.99. A saturation of this system during an ultrasonic wave perfusion phase that deeply changes the culture conditions is observed and discussed. Principal component analysis (PCA) is used to undergo the robustness study and the ISM calibration step.

Algorithms↗

Antibacterial activity of a pepsin-derived bovine hemoglobin fragment.

Peptic digestion of bovine hemoglobin yields a fragment with antibacterial activity. This peptide was purified to homogeneity by a two-step procedure including anion exchange chromatography and preparative reversed-phase HPLC. Mass determination and fragmentation indicated that this peptide corresponded to the 1-23 fragment of the alpha chain of hemoglobin. The minimum inhibitory concentration and mode of action of this peptide towards Micrococcus luteus strain A270 were determined. Hemolytic assay, interaction with liposomes, and study of its structure in solution were also performed.

Amino Acid Sequence↗

A simple method for the two-step preparation of two pure haemorphins from a total haemoglobin peptic hydrolysate by conventional low-pressure chromatographies.

The development of a simple purification method for two haemorphins, VV-haemorphin-7 (Val-Val-Tyr-Pro-Trp-Thr-Gln-Arg-Phe) and VV-haemorphin-4 (Val-Val-Tyr-Pro-Trp-Thr), from a total peptic haemoglobin hydrolysate is described. Cation-exchange chromatography on CM-Sephadex was used as a pre-fractionation step for the hydrolysate. VV-haemorphin-7 and VV-haemorphin-4 were eluted in two different fractions. The second and final purification step was hydrophobic-interaction chromatography on phenyl-Sepharose, which allowed the isolation of the two pure haemorphins. Haemoglobin and globin hydrolysates were compared as starting materials. For easy recovery of haemorphins and easy adjustment of conditions for final purification, a volatile buffer, ammonium acetate buffer, pH 6.5, was employed. This process, which allowed the preparation of pure haemorphins from a total protein hydrolysate, could be scaled up and used in the food industry.

Animals↗

Molecular weight characteristics of alginate produced by Azotobacter vinelandii in a membrane bioreactor.

A membrane bioreactor which combines a continuous fermentor and a cross-flow microfiltration module enabling continuous cell recycling and removal of the fermentation products freed of microbial cells was tested for the production of alginate by Azotobacter vinelandii. The molecular weight characteristics of the polysaccharide produced were investigated. The macromolecular characteristics of alginate recovered by first filtering batch fermentation broths through different microporous ceramic membranes with pore sizes varying from 0.45 to 1.4 microm seemed to be independent of the MPS. The 0.8-microm membrane pore size (MPS) was selected for continuous alginate production in the membrane bioreactor. A mean yield value of 0.21 g alginate g(-1) saccharose was obtained and an increase in alginate polydispersity as incubation proceeded was observed, probably due to enzymatic degradation of the polysaccharide.

Alginates↗

Hydrolysis and large scale ultrafiltration study of alfalfa protein concentrate enzymatic hydrolysate.

Batch enzymatic hydrolysis of insoluble Alfalfa Protein Concentrate by Delvolase was carried out at laboratory and at pilot-plant scale coupled to an ultrafiltration reactor with a mineral tubular membrane. Parametric studies were carried out on the batch system to determine the biochemical and hydrodynamical optimum conditions. The hydrolysis conditions selected were 40 degrees C, pH 9.5, initial substrate level 3 g protein/100 g and the enzyme substrate ratio 152 U/g protein. After 5 h of hydrolysis, 96% of the total amount of initial nitrogen was solubilized. The ultrafiltration conditions selected were a 10 000 Nominal Molecular Weight Cut-Off, a transmembrane pressure of 1.5 bar, a flux velocity of 0.8 m/s. Fifty percent of the initial nitrogen appeared in the permeate.

Journal Article↗

Comparison of the IgE titers to bovine colostral G immunoglobulins and their F(ab')2 fragments in sera of patients allergic to milk.

Colostral G immunoglobulins (IgGs) are described in many recent studies as having a beneficial effect for the treatment of viral, bacterial and parasitic diarrhea in animals and humans. The specific IgE titers to bovine colostral IgG, to bovine serum IgG, and to F(ab')2 fragments of IgG were immunoenzymatically quantified in sera of patients allergic to milk, to statistically evaluate and compare their relative immunoreactivity towards these purified antigens. The results clearly indicated that 36% of the population tested was potentially allergic to colostral IgG, and serum IgG globally elicited significantly lower IgE titers. The F(ab')2 fragments lead to a significantly decreased immunoreactivity as compared to colostral IgG. This study shows the interesting use of peptic hydrolysis of IgG in producing fragments with preserved therapeutic immunoactivity and reduced potential allergenicity.

Animals↗

Agitation rate effects on plasmid stability in immobilized and free-cell continuous cultures of recombinant E. coli.

Escherichia coli B/pTG201 recombinant cells were immobilized by entrapment in a carrageenan gel and cultivated in nonselective media to investigate the effect of agitation rate on plasmid stability, biomass concentration, and enzyme productivity. These parameters were studied in continuous cultures for free and immobilized cells, respectively. Immobilized recombinant cells exhibit an increase in the stability of the plasmid pTG201 compared to free cells, even under conditions where the tendency of plasmid stability for free cells decreased generally more rapidly under a higher agitation rate. Intensive agitation, resulting also in a strong shear stress, greatly reduced cell concentration within gel beads throughout the course of growth. Higher enzyme expression of catechol 2-3, dioxygenase was also obtained in leaked cells due to better maintenance of plasmid stability and higher plasmid copy number with regard to free cells. Enzyme productivity of leaked and free cells in minimal medium decreased with the increase in agitation rate, due to decreased plasmid stability; however, in LB medium, it increased in the presence of higher agitation rate related to important cell concentration.

Catechol 2,3-Dioxygenase↗

Influence of immobilization on the stability of pTG201 recombinant plasmid in some strains of Escherichia coli.

The stability of pTG201 plasmid was examined by continuous culture in three genetically different Escherichia coli hosts. Two types of experiment were carried out, one with free cells and one with immobilized cells. When cells were cultivated in free continuous culture in the absence of antibiotic selection, the plasmid was maintained with various degrees of stability in the three host organisms. By contrast, in continuous culture with immobilized cells, plasmid pTG201 was stably maintained in the three strains. We showed that the increase in pTG201 stability in immobilized cells is due neither to plasmid transfer between immobilized cells nor to an increase of the plasmid copy number of immobilized cells. We also showed that plasmid-free cells, when coimmobilized and grown in competition with plasmid-containing cells, cannot overrun the culture.

Ampicillin↗

Plasmid inheritability and biomass production: comparison between free and immobilized cell cultures of Escherichia coli BZ18(pTG201) without selection pressure.

Maintenance of the plasmid pTG201 in Escherichia coli BZ18 was studied for both free and immobilized cells during chemostat culture, in the absence of the antibiotic against which resistance was plasmid encoded. Electron microscopic observations of immobilized proliferant cells within carrageenan gel beads showed high cell concentrations and growth into distinct cavities. The plasmid which coded for the catechol 2,3-dioxygenase activity was stably maintained during 80 generations in the case of immobilized cells. A theoretical analysis founded on the compartmentalization resulting from the immobilized growth conditions was described. However, the model still showed a plasmid stability inferior to that determined experimentally. Hypotheses dealing with physiological changes of immobilized cells were presented. In addition, the high cell concentrations obtained in the outer 50 microns of the carrageenan gel beads gave a biomass productivity within this useful volume which was 20 times higher than in free-cell cultures.

Bacteriological Techniques↗

Steroid modifications with immobilized biocatalysts--use of immobilized enzyme-requiring cofactor regeneration and of immobilized mycelium.

Two biological approaches have been investigated for specific modifications of steroids. The first one uses the purified enzyme for the specific dehydrogenation of androsterone to androstanedione. The enzyme used is 3 alpha-hydroxysteroid dehydrogenase which requires a cofactor (NAD). A cofactor regeneration is needed so that the process could work continuously. The conjugation of two points (immobilization of the enzyme and optimization of the ratio methanol-water) allows a continuous work of the enzyme during 25 days. Moreover, we propose a chemical regeneration of the cofactor using methoxy derivative of phenazine methosulphate. Right now it is the limiting step of the process. The second approach of steroid modification uses a whole mycelium of Aspergillus phoenicis for the specific hydroxylation of progesterone to 11 alpha-hydroxy progesterone. The transformation of 90% of the progesterone is obtained with calcium alginate immobilization and the lowest number of products is obtained at pH lower than 2.5 with carrageenan and polyurethane immobilization. It seems promising to apply immobilized biocatalysts to the bioconversion of hydrophobic compounds in organic solvents system.

3-Hydroxysteroid Dehydrogenases↗