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Biomedical subjects

B Mattiasson

Publications and source records attributed to B Mattiasson.

At least 19 recordsLinked to original sources

Process monitoring by flow-injection immunoassay. Evaluation of a sequential competitive binding assay.

A new variation on the theme of flow-injection binding assays is presented, namely the sequential competitive binding assay, in which the sample containing the native antigen is first introduced into the flow system followed by a pulse of labelled antigen. The flow-injection binding assay was used in monitoring the effluent from column chromatographic separations of proteins. By applying a computer-based evaluation system, concentrations are automatically read and compensation is made for denaturation in the affinity sorbent.

Binding, Competitive

Maximizing the expression of a recombinant gene in Escherichia coli by manipulation of induction time using lactose as inducer.

The use of isopropyl-beta-D-thiogalactoside (IPTG) for induction of the lac-promoter in small-scale cultivations is well established. However, for large-scale microbiological processes the cost of this inducer is a severe limitation. Here is described a method by which lactose is used as inducer of the lac promoter with the same efficiency as that of IPTG. It was found that after growth on glucose the time of the addition of lactose is important for the quality of induction. The resulting yield of the recombinant protein increased when lactose was added to the culture if the glucose concentration was rather low. By careful monitoring of the glucose level in the fermentation, using a biosensor, it was possible to add the inducer when the carbon source was nearly depleted. Using Escherichia coli BL21 (pET3), in which was cloned the main antigen coat protein of the foot and mouth disease virus, induction of the gene led to expression of the target protein at a level exceeding 20% of the total cell protein.

Aphthovirus

Immunochemically based assays for process control.

Immunoanalysis for process control is reviewed. The development of non-equilibrium immunoassays from a manually operated flow injection system to a completely computerized system for sample analysis as well as calibration and data evaluation is discussed. Several other approaches in using immunochemistry in biosensors for process control are discussed. The fact that reuse of antibodies raises specific demands on their properties is discussed. Even if the area is young, much progress has been achieved and one can foresee an interesting future development of the area.

Biomedical Engineering

Evaluation of displacement chromatography for the recovery of lactate dehydrogenase from beef heart under scale-up conditions.

A complex mixture of proteins was subjected to displacement development from a Tris Acryl DEAE anion-exchange column. Lactate dehydrogenase was used as the target protein in the evaluation of the resolution and separation under scale-up conditions. The conditions of operation were scaled up in terms of column size and protein load. Column length was found to play an important role in resolving the mixture. The performance of the displacement mode run was compared with a conventional ion-exchange elution run in terms of fraction purity and specific activities. In general, displacement chromatography of the complex mixture yielded better results.

Animals

The cDNA sequence of a neutral horseradish peroxidase.

A cDNA clone encoding a horseradish (Armoracia rusticana) peroxidase has been isolated and characterized. The cDNA contains 1378 nucleotides excluding the poly(A) tail and the deduced protein contains 327 amino acids which includes a 28 amino acid leader sequence. The predicted amino acid sequence is nine amino acids shorter than the major isoenzyme belonging to the horseradish peroxidase C group (HRP-C) and the sequence shows 53.7% identity with this isoenzyme. The described clone encodes nine cysteines of which eight correspond well with the cysteines found in HRP-C. Five potential N-glycosylation sites with the general sequence Asn-X-Thr/Ser are present in the deduced sequence. Compared to the earlier described HRP-C this is three glycosylation sites less. The shorter sequence and fewer N-glycosylation sites give the native isoenzyme a molecular weight of several thousands less than the horseradish peroxidase C isoenzymes. Comparison with the net charge value of HRP-C indicates that the described cDNA clone encodes a peroxidase which has either the same or a slightly less basic pI value, depending on whether the encoded protein is N-terminally blocked or not. This excludes the possibility that HRP-n could belong to either the HRP-A, -D or -E groups. The low sequence identity (53.7%) with HRP-C indicates that the described clone does not belong to the HRP-C isoenzyme group and comparison of the total amino acid composition with the HRP-B group does not place the described clone within this isoenzyme group. Our conclusion is that the described cDNA clone encodes a neutral horseradish peroxidase which belongs to a new, not earlier described, horseradish peroxidase group.

Amino Acid Sequence

Tailoring the microenvironment of enzymes in water-poor systems.

Biocatalytic systems using enzymes in organic solvents open up the possibility of performing a whole range of reactions which would not normally occur under physiological conditions. The ability to perform reverse hydrolysis, or to convert substances relatively insoluble in aqueous environments on a scale of practical value in commercial applications are among those reactions for which water-poor systems are appropriate.

Emulsions

Continuous monitoring of urea in blood during dialysis.

Urease was immobilized to porous glass and used in combination with a conductivity meter for determining urea in standard solutions as well as in blood from a patient undergoing dialysis. The sampling unit involves a possibility for heparinization at the sampling point and a dialysis step prior to exposure to the enzyme column. The unit operates in a linear mode in the concentration range 5-50 mM. Monitoring of dialysis process gave good correlation with off-line analyses.

Biosensing Techniques

Purification, characterization, and structure of pseudobactin 589 A, a siderophore from a plant growth promoting Pseudomonas.

Under conditions of low-iron stress the plant growth promoting bacterium Pseudomonas putida 589 (DSM 50202) produced a yellow-green fluorescent iron-binding peptide siderophore, which was designated pseudobactin 589 A and had an affinity constant toward Fe3+ of 10(25) at pH 7. Protonated pseudobactin 589 A had the molecular formula C54H78O26N15 and a nominal mass spectral molecular mass of 1353 g/mol. Its structure was determined by a combination of nuclear magnetic resonance, fast atom bombardment mass spectrometry, and Edman degradation. Pseudobactin 589 A consisted of a nonapeptide with the amino acid sequence L-Asp-L-Lys-(D)-beta-OH-Asp-D(L)-Ser-L-Thr-D-Ala-D-Glu-L(D)-Ser-L-N delta-OH- Orn, in which lysine was amide bonded via the carboxy and the N epsilon-amino groups. A quinoline-derived chromophore was connected via an amide bond to the alpha-amino nitrogen of aspartic acid and an L-malamide residue was attached to the chromophore. The three bidentate Fe3+ binding ligands consisted of an o-dihydroxy aromatic group from the quinoline derivative, beta-hydroxyaspartic acid, and an internally cyclized N delta-hydroxyornithine. The structure of pseudobactin 589 A is unique but strikingly similar to that of other pseudobactin-type siderophores from other plant growth promoting and plant deleterious pseudomonads.

Amino Acid Sequence

Interesterification of phosphatidylcholine with lipases in organic media.

Lipases were investigated with respect to their ability to catalyse the incorporation of fatty acids into phosphatidylcholine (PC) by interesterification reactions. The enzymes were dried onto solid support materials and the conversions were carried out in water-saturated toluene. Three lipases (two fungal and one plant enzyme) had the desired activity; immobilized lipase from Mucor miehei (Lipozyme) was the most active enzyme. The Lipozyme-catalysed interesterification was selective for the sn-1 position of PC and during 48 h of reaction around 50% of the fatty acids in this position were replaced with heptadecanoic acid, a fatty acid which was practically absent in the original phospholipid. Due to adsorption on the support material and the competing hydrolysis reaction the total amount of PC in the reaction solution decreased to about 40% of the original amount. Higher interesterification rates were obtained with free fatty acids as acyl donors than with fatty acid esters.

Chromatography, Gas

A dual streaming potential device used as an affinity sensor for monitoring hybridoma cell cultivations.

A dual streaming potential device was used for determining the content of monoclonal antibodies in cultivation medium for hybridoma cells. Samples of culture medium were analyzed as discrete pulses, as a continuous flow of constant concentration as well as with fluctuating concentrations. Tests were done with two subclasses of IgG as well as with IgM. Finally, the analytical device was applied to the registration of production of monoclonal antibodies in a cultivation.

Animals

Enzymatic peptide synthesis in organic media: a comparative study of water-miscible and water-immiscible solvent systems.

Peptide synthesis was carried out in a variety of organic solvents with low contents of water. The enzyme was deposited on the support material, celite, from an aqueous buffer solution. After evaporation of the water the biocatalyst was suspended in the reaction mixtures. The chymotrypsin-catalyzed reaction between Z-Phe-OMe and Leu-NH2 was used as a model reaction. Under the conditions used ([Z-Phe-OMe]0 less than or equal to 40 mM, [Leu-NH2]0/([Z-Phe-OMe]0 = 1.5) the reaction was first order with respect to Z-Phe-OMe. Tris buffer, pH 7.8, was the best buffer to use in the preparation of the biocatalyst. In water-miscible solvents the reaction rate increased with increasing water content, but the final yield of peptide decreased due to the competing hydrolysis of Z-Phe-OMe. Among the water-miscible solvents, acetonitrile was the most suitable, giving 91% yield with 4% (by vol.) water. In water-immiscible solvents the reaction rate and the product distribution were little affected by water additions in the range between 0% and 2% (vol. %) in excess of water saturation. The reaction rates correlated well with the log P values of the solvent. The highest yield (93%) was obtained in ethyl acetate; in this solvent the reaction was also fast. Under most reaction conditions used the reaction product was stable; secondary hydrolysis of the peptide formed was normally negligible. The method presented is a combination of kinetically controlled peptide synthesis (giving high reaction rates) and thermodynamically controlled peptide synthesis (giving stable reaction products).

Chromatography, High Pressure Liquid