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Biomedical subjects

D Josic

Publications and source records attributed to D Josic.

13 recordsLinked to original sources

Peptide affinity chromatography of human clotting factor VIII. Screening of the vWF-binding domain.

The region of von Willebrand factor, which is involved in the complex formation with factor VIII, was used to generate a panel of octapeptides. A peptide ladder was generated from the von Willebrand factor region aa40 to aa100 and was synthesized on cellulose membranes by spot technology. Four peptides with affinity for factor VIII were identified by incubation with plasma derived factor VIII and recombinant factor VIII. The peptides denoted as 010 (LCPPGMVRHE), 011 (RCPCFHQGK), 014 (CFHQGKEYA) and 015 (RDRKWNCTDHVC) were further characterized by real-time interaction analysis and small scale affinity chromatography. Biotinylated peptides were used for blotting assays. These experiments showed that the peptides are directed against the light chain of FVIII. We consider these peptides as valuable tools for in situ labeling and also as ligands suitable for affinity chromatography.

Amino Acid Sequence

High-performance capillary electrophoresis for in-process control in the production of antithrombin III and human clotting factor IX.

Antithrombin III (ATIII) and factor IX (FIX), two proteins from the clotting cascade, were investigated in parallel experiments, using capillary gel electrophoresis and capillary isoelectric focusing. The results from these experiments were compared with the results obtained from sodium dodecyl sulfate-polyacrylamide gel electrophoresis (SDS-PAGE) and slab gel isoelectric focusing. In the case of ATIII, capillary gel sieving showed comparable results to SDS-PAGE with the added advantage of the shorter time required for analysis. By optimizing capillary isoelectric focusing (cIEF), a separation of the ATIII isoforms was achieved. In the case of FIX, capillary gel electrophoresis (SDS-CE) of a FIX preparation gave similar results to those obtained by size-exclusion high-performance liquid chromatography and SDS-PAGE, but turned out to be less sensitive in detecting protein impurities at low concentrations. The microheterogeneity of this protein was shown by using cIEF.

Antithrombin III

Pharmacokinetic behaviour of R-(+)- and S-(-)-amlodipine after single enantiomer administration.

Amlodipine, 3-ethyl 5-methyl-2-[(2-aminoethoxymethyl]-4-(2-chlorophenyl)-1,4-dihydro-6-methy l-3,5-pyridinedicarboxylate, is a chiral calcium antagonist, currently on the market and in therapeutic use as a racemate. The pharmacokinetic behaviour of R-(+)- and S-(-)-amlodipine after single enantiomer administration to healthy male human volunteers together with comparative administration of the racemic mixture of both enantiomers were studied. Plasma levels were studied as a function of time and assayed using an enantioselective chromatographic method (coupled chiral and achiral HPLC) with on-line solid-phase extraction and UV absorbance detection. The method was validated separately for the R-(+)- and S-(-)-enantiomer, respectively. Results of the study indicate that the pharmacokinetic behaviour of R-(+)- and S-(-)-amlodipine after single enantiomer administration is comparable to that of each enantiomer after administration of the racemate. No racemization occurs in vivo in human plasma after single enantiomer administration.

Administration, Oral

Improved virus safety and purity of a chromatographically produced factor IX concentrate by nanofiltration.

A virus removal system based on tangential flow filtration was introduced into a Factor IX production process. Beside the intended virus reduction potency of filter membranes, an additional purification effect could be achieved. This purification effect was evaluated in detail by means of sodium dodecyl sulphate-polyacrylamide gel electrophoresis and size-exclusion HPLC. High-molecular-mass impurities were retained by the membrane, thus increasing the specific activity of the product.

Blood-Borne Pathogens

Development and biochemical characterization of a double-virus-inactivated factor VIII preparation.

This paper describes the development of a double-virus-inactivated preparation. The original goal was to inactivate and/or remove parvovirus from plasma-derived factor VIII. More recently, attention has also been focused on the controversial issue of transmission of the non-lipid-coated hepatitis A virus by preparations of factor VIII which have been solvent/detergent-treated and purified by ion-exchange chromatography.

Antiviral Agents

Purification of factor VIII and von Willebrand factor from human plasma by anion-exchange chromatography.

Factor VIII (anti-hemophilia A factor) is isolated from human plasma. Purification is carried out by a combination of precipitation and chromatographic procedures. After precipitation, the first step in virus inactivation is achieved through the effect of a non-ionic detergent such as Tween 80, and a solvent, e.g. tri-n-butylphosphate (TnBP). By subsequent anion-exchange chromatography, a highly enriched product is isolated, consisting of a complex formed by factor VIII and von Willebrand factor (FVIII-vWF). This treatment also removes the virus-inactivating reagents to quantities in the low ppm range. The second step in virus inactivation is aimed specifically at the non-enveloped viruses and consists of pasteurization at temperatures higher than 60 degrees C for 10 h. Through the addition of stabilizers, between 80% and 90% of the initial activity of FVIII is preserved during the modified pasteurisation. Along with the possibly denatured proteins the stabilizers, such as sugars, amino acids and bivalent cations, are subsequently removed by ion-exchange chromatography. The two-fold virus inactivation, by solvent/detergent treatment and subsequent pasteurisation, allows the destruction of both lipid-enveloped and non-enveloped viruses. During the procedure FVIII is stabilized through the high content of vWF. The complex consisting of FVIII and vWF can be dissociated by adding calcium ions. Subsequently both glycoproteins from this complex are separated from one another by further anion-exchange chromatography.

Biocompatible Materials

Application of high-performance membrane chromatography for separation of annexins from the plasma membranes of liver and isolation of monospecific polyclonal antibodies.

The separation of annexins, calcium-binding plasma membrane-associated proteins from rat liver and Morris hepatoma 7777 by high-performance membrane chromatography (HPMC) is described. The annexins with low molecular masses, CBP 33 and CBP 35, and the annexin with a high molecular mass, CBP 65/67, can be separated within 10 min from one another by anion-exchange HPMC under non-denaturing conditions. The separation devices used consist of compact, porous disks (QuickDisk) on the one hand and of bundled membranes made of cellulose fibers (MemSep) on the other. Both have been found to be equally well suited for this separation. The annexins obtained in this way are subsequently bound to epoxy-activated porons disks and used for the separation of monospecific polyclonal antibodies against the annexin CBP 65/67.

Animals

Purification of human tumour necrosis factor by membrane chromatography.

The recombinant human tumour necrosis factor alpha from an extract of Escherichia coli was enriched to homogeneity according to specific activity and sodium dodecyl sulphate-polyacrylamide gel electrophoresis by purification using anion-exchange HPLC and hydrophobic interaction HPLC. Parallel experiments with the same separation methods, but carried out with membrane chromatography on compact discs, gave similar results in terms of yield and purity of the product. The active form of the protein is a trimer. The second isolation step, hydrophobic interaction chromatography, causes dissociation of the trimer into monomers and a partial loss of the biological activity of the protein. The phenomenon occurs on both the column and the disc. This in turn indicates strongly that the dissociation of the protein is a consequence of interaction between the samples and the hydrophobic ligand, and is not caused by non-specific interaction with the matrix.

Blotting, Western

Extraction of Triton X-100 and its determination in virus-inactivated human plasma by the solvent--detergent method.

For inactivation of lipid-enveloped viruses during the production of fresh frozen and lyophilized human plasma, the solvent-detergent method was applied. In this process, the solvent tri-n-butyl phosphate is removed by extraction with castor oil. The removal of the non-ionic detergent Triton X-100 is performed by solid-phase extraction using reversed-phase supports. For this purpose, different polymer- and silica-based supports were tested. The highest capacity for Triton X-100 was achieved with C18 silica gels. These supports can bind more than 0.1 ml of Triton X-100 per ml of support. None of the proteins, e.g., clotting factors, bind to the support and therefore they pass through the column and their biological activity is hardly affected. The determination of detergent during the production process was also studied. The application of special columns allowing direct sample injection was introduced. This is a simple method for the rapid in-process determination of Triton X-100 in human plasma by reversed-phase chromatography under isocratic conditions. Using the method developed here, less than 1.0 ppm of Triton X-100 can be detected in less than 12 min without any sample pretreatment.

Blood

A solvent I detergent treated, pasteurised and highly purified factor VIII concentrate.

In an assessment of the risks of virus transmission by clotting concentrates it is clear that the currently practised procedures for virus inactivation are not equally effective against all types of viruses; neither a pasteurisation nor the solvent detergent (SID) process alone are adequate enough to inactivate viruses that are strongly resistant to heat and organic solvents. In this context, human parvovirus B19 and hepatitis A virus (HAV) are of particular concern. In order to improve this situation which still poses a risk to the haemophiliac patients, a more effective pasteurisation process has been developed that could be easily applied to an already well established factor VIII (FVIII) process in addition to the SID-treatment. Experiments using temperatures above 60 degrees C were performed prompted by two recent publications, which demonstrate that HAV becomes instable at temperatures exceeding 62 degrees C. It is the purpose of this paper to present the following progress: achievement of a pasteurisation procedure for FVIII at 63 degrees C for 10 h with no discernible change in the structure of the factor VIII/von Willebrand factor (FVIII/VWF) complex owing to a newly developed composition of stabilizers; application of this pasteurisation procedure to a purified FVIII fraction that has already been submitted to a SID-treatment: Doing so, two independent virus inactivation steps are performed as previously recommended by the International Association of Biological Standardization (IABS). Introduction of a second purification step on an anion exchange resin, achieving an additional virus reduction over the presently manufactured FVIII preparation.(ABSTRACT TRUNCATED AT 250 WORDS)

Blood Protein Electrophoresis

Regulation of intracellular iron distribution in K562 human erythroleukemia cells.

Following a pulse with 59Fe-transferrin, K562 erythroleukemia cells incorporate a significant amount of 59Fe into ferritin. Conditions or manipulations which alter the supply of iron to cells result in changes in the rate of ferritin biosynthesis with consequent variations in the size of the ferritin pool. Overnight exposure to iron donors such as diferric transferrin or hemin increases the ferritin level 2-4- or 6-8-fold above that of the control, respectively. Treatment with the anti-human transferrin receptor antibody, OKT9 (which reduces the iron uptake by decreasing the number of transferrin receptors) lowers the ferritin level by approximately 70-80% with respect to the control. The fraction of total cell-associated 59Fe (given as a pulse via transferrin) that becomes ferritin bound is proportional to the actual ferritin level and is independent of the instantaneous amount of iron taken up. This has allowed us to establish a curve that correlates different levels of intracellular ferritin with corresponding percentages of incoming iron delivered to ferritin. Iron released from transferrin appears to distribute to ferritin according to a partition function; the entering load going into ferritin is set for a given ferritin level over a wide range of actual amounts of iron delivered.

Biological Transport

Quantitative determination of intracellular, ferritin-associated radioactive iron by high-performance liquid chromatography and immunoprecipitation.

Antibodies raised against ferritin preparations of diverse origin provide an uncertain reagent for quantitation of the ferritin present in specific cell lysates. Utilizing K562 cells, a human leukemic cell line, techniques are described to resolve and to quantitate the ferritin-bound cytosolic iron. Processing the cell lysates by HPLC employing an anion-exchange or hydrophobic interaction column resulted in recovery of a single, ferritin-containing radioactive peak widely separated from the bulk of the non-ferritin-bound iron. Comparison of the yield obtained by chromatography with that by immunoprecipitation confirmed both the specificity and the quantitation of the antibody technique.

Binding Sites