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Biomedical subjects

H Suomela

Publications and source records attributed to H Suomela.

10 recordsLinked to original sources

Virus inactivation during intravenous immunoglobulin production.

Effects of time, temperature, pH and stabilizers (i.e. medium) on inactivation of lipid-enveloped model viruses, Semliki Forest and vesicular stomatitis viruses in the production process of intravenous immunoglobulin were investigated on a laboratory scale. The lowering of pH, the raising of temperature and the increasing of incubation time improved the inactivation effect. However, small changes in pH and stabilizer concentrations did not influence the results. Inactivation was not linear and a clear tailing off could be seen. Therefore, for complete virus inactivation incubation times longer than 20 h are necessary. Inactivation took place much more rapidly in intravenous immunoglobulin solution than in intramuscular immunoglobulin solution. Processing steps such as freeze-dying in the presence of ethanol or storage of intramuscular immunoglobulin in the liquid state at pH7 only partially inactivated these viruses.

Blood Transfusion

Stability of European anti-D immunoglobulin preparations.

The stability of 18 batches of anti-D immunoglobulin preparations from 7 European manufacturers was studied over 28-day incubation at +37 degrees C and 3-year storage at +4 degrees C. The mean loss of activity after 28 days at +37 degrees C was 12.3 +/- 8.2%, and after 3 years at +4 degrees C 15.2 +/- 9.5%. The correlation coefficient of the loss of activity between these two storages was r = 0.61, p less than 0.05 indicating that short-term incubation can be used to evaluate the shelf life stability of anti-D activity. In general, measurements of IgG fragments or activities of plasmin, plasminogen, or prekallikrein activator were not valuable in predicting the stability of anti-D activity due to the fact that the preparation of each manufacturer has its own unique pattern of enzymes and inhibitors. The anti-D immunoglobulin preparations contained up to at least 7 plasma proteins in addition to IgG. All preparations contained factor B, most of them alpha 2-macroglobulin, alpha 1-antitrypsin, albumin, and alpha 2-HS glycoprotein, alpha-Lysozyme was present in 7, and ceruloplasmin in 2 preparations. Neither purity nor impurity correlated with stability.

Chromatography, High Pressure Liquid

Stability of IgG solutions, especially anti-D gammaglobulin, with special reference to measured proteolytic activity and degradation.

The stability of IgG solutions during the dating period can be predicted by measuring the degree of degradation after elevated storage conditions at +37 degrees C with added streptokinase. The measurement of proteolytic activity with a synthetic substrate correlates with the results obtained by SDS-disc gel electrophoresis and gel filtration. IgG molecules having Anti-D activity were observed to be essentially more sensitive to proteolytic degradation by plasmin than IgG molecules in general. It seems, therefore, that the methods which are suitable for the study of the stability of normal IgG preparations are not sufficient to predict the stability of anti-D gammaglobulin preparations.

Drug Stability

Preparation and properties of a therapeutic factor IX concentrate.

A method for the large-scale preparation of a coagulation factor IX concentrate from human plasma is described. The method includes absorption of the coagulation factors from cryosupernatant plasma to DEAE-Sephadex, extensive washing of the gel and elution of the coagulation factors with 0.5 M phosphate buffer at 6.85, followed by desalting of the eluate in a column of Sephadex G-25, then by lyophilization, dissolving and sterile filtration, and finally by freeze-drying of the final product. Experiments performed with HBsAg-positive plasma demonstrated a decrease in the HBsAg content by a factor of 10(-5) during the process. The product is inactive in a Na-PTT assay. The process yields an about 100-fold purified factor IX concentrate containing also factors II, VII, and X, but in relatively smaller amounts. The average yield relative to factor IX is 60%. The batch size has been from 16 to 150 litres of plasma and about 300 batches of the concentrate have been prepared. About 5,100 bottle (about 4.0 X 10(6) U of factor IX) of the concentrate have been used in the treatment of patients with haemophilia B. The clinical effect has always been good and the in vivo response to factor IX was 1.15 +/- 0.30%/U/kg body weight. Two cases of HBsAg-negative hepatitis that may have been caused by the concentrate, were detected. No thrombotic complications were found.

Factor IX

Purification of human factor IX by chromatography of a coagulation factor concentrate.

A purification procedure for, and some properties of, coagulation factor IX are described. The coagulation factor concentrate used for the treatment of hemophilia B patients was employed as the starting material. The isolation procedure consists of chromatography in DEAE-cellulose, two chromatographies in hydroxyapatite gel and two gel filtrations in Sephadex G-200. Only trace amounts of factors II, VII and X were present in the final preparation and the specific activity of factor IX was 159 corresponding 10,300 times purification from plasma. The molecular weight was estimated to be 76,000 in gel filtration and 86,000 in sodium dodecyl sulfate disc gel electrophoresis. Three activity peaks with pIs 4.15, 4.25 and 4.40 were obtained by isoelectric focusing.

Chromatography, DEAE-Cellulose

Human coagulation factor IX. Isolation and characterization.

Human coagulation factor IX was purified by two ion-exchange chromatographies on DEAE-Sephadex A-50, heparin-Sepharose chromatography, hydroxyapatite chromatography and immunoadsorbent technique. Factor IX was homogeneous by ordinary and sodium dodecylsulphate disc electrophoresis, N-terminal amino acid analyses and ultracentrifugation and by immunological criteria. The following molecular data were observed: 1. Sedimentation equilibrium indicated a molecular weight of 66100 and sedimentation velocity gave S20,W = 3.97 S. A partial specific volume of -v = 0.712 ml/g was calculated from the amino acid and carbohydrate composition. 2. Sodium dodecylsulphate disc gel electrophoresis suggested a molecular weight of 65000. 3. Gel filtration indicated a Stokes radius of 4.08 nm, and 'a molecular weight' of 72000, as well as a diffusion coefficient D20,W = 5.15 X 10(-7) cm2 s-1 and a frictional ratio f/fo = 1.54. 4. Tyrosine was the N-terminal amino acid. The amino acid composition is described. Factor IX contained approximately 17.5% carbohydrate, which includes 4.7% hexose, 6.8% N-acetylhexosamine and 6% sialic acid. 5. Microheterogeneity of pure factor IX was demonstrated by isoelectric focusing. The isoelectric points of the major components lay within range of pH 4.0 to 4.6. 6. The antibody raised in rabbits against the pure factor IX did not react with the other vitamin-K-dependent coagulation factors measured by coagulation factor assays or immunodiffusion in gels.

Amino Acids