High-yield method of production of freeze-dried purified factor VIII by blood banks

Isolation of the factor VIII-von Willebrand factor complex directly from plasma by gel filtration

A high capacity gel filtration system was developed with the purpose of isolating factor VIII (FVIII) and von Willebrand factor (vWF) directly from plasma in significantly higher yields than obtained by cryoprecipitation, the technique most commonly used to recover FVIII-vWF from human plasma. After laboratory-scale gel filtration of plasma, a FVIII-containing fraction was collected containing about 90% of FVIII in the applied plasma and with almost tenfold higher purity than that obtained by cryoprecipitation. The gel filtration step has been scaled up for use as the initial step in the manufacturing process for a FVIII preparation (Nordiate).

Characterization of factors affecting the stability of frozen heparinized plasma

The use of heparin rather than citrate as primary anticoagulant has been shown to significantly improve the initial activity, stability and recovery of factor VIII:C from human plasma, cryoprecipitates or factor VIII concentrates if the plasma was initially frozen at -80 degrees C and subsequently stored at this temperature. If frozen and stored at progressively warmer temperatures however, increasing amounts of insoluble protein aggregates, termed storage precipitates (SPs), were recovered in the thawed plasma and cryoprecipitate fractions. Plasma recovery by centrifugation at 7,000 g for 7 min [Method I (MI)], 2 x 10 min (MII) or 15 min (MIII) had little effect on SP formation after 1 month at any storage temperature. After 4 months at -20 degrees C, more SP was recovered from MIII plasma whereas at -40 degrees C, more SP was recovered from MI plasma. Also, the preparation method had little or no effect on factor VIII:C activity at equivalent storage times or temperatures. A trend towards improved factor VIII recoveries was noted at lower freezing and storage temperatures however. SP formation was associated with reduced fibrinogen levels in the recovered plasma without loss of antithrombin-III or increased fibrinopeptide-A. Western blots showed polymerization of A alpha or gamma-chains of fibrinogen. SP formation was reduced or eliminated with factor XIII inhibitors, antibody to the active factor XIII a subunit or adjustment of heparinized plasma to 5-10 mM sodium citrate before initial freezing and storage. Although plasma factor VIII:C recoveries were only slightly affected at these citrate concentrations under most conditions, its recovery in cryoprecipitates was substantially improved owing to the reduction or absence of SPs.

Screening for ischaemic heart disease risk factors at a health fair: low attendance by those at highest risk

Among people attending a heart disease screening project at a Health Fair in Sheffield, only 22 of 425 (5.2%) lived in areas with more than 25% of the population belonging to social classes IV or V. The incidence of heart disease is known to be particularly high in these areas, where 15.1% of the total population live. By analysis of the attendance rates from districts other than those immediately adjacent to the site of the Health Fair, we found that the strength of this inverse correlation increased, suggesting that the problems of access are probably greater for people living in deprived areas than for others.

Studies on the stability of VIII:C during the manufacture of a factor VIII concentrate for clinical use

The stability of VIII:C was investigated by monitoring samples taken at different points from a routine process for the manufacture of factor VIII concentrate and by examining the stabilising influence of a number of product formulations. Loss of VIII:C over process-finishing procedures (formulation, 0.22 micron filtration, dispensing) was associated with a citrate-induced inactivation which could be prevented by controlling the ionised calcium concentration of the solution. These results were obtained using a one-stage clotting assay but were not observed using a two-stage assay. No evidence for activation was found in vitro (e.g. by FPA generation and VIII:C stability) and the yield increase suggested by the one-stage assay was supported by results from a controlled clinical evaluation.

Double cryoprecipitated factor VIII concentrate from heparinised plasma and its heat treatment

In an attempt to implement the small pool concept in Factor VIII purification, cryoprecipitate derived from heparinised plasma was reprecipitated in the cold providing a factor VIII concentrate for freeze drying and heat treatment. There was considerable purification; only 1% of the original plasma proteins was left in the final product. Factor VIII:C concentration was about 19 IU/ml. Factor VIII related antigen (RAg) appeared heterogeneous, with a broad base and asymmetry on crossed immunoelectrophoresis. Fibrinogen content was 15 g/l. In contrast to high-purity commercial concentrates, fibronectin was considerably concentrated. Immunoglobulin contents were similar to a high-purity commercial product. The amount of other plasma proteins was very small, varying from less than 0.2% for C3 complement to 2.3% ceruloplasmin. In some respects the preparation may be considered as an intermediate-purity Factor VIII concentrate. Following addition of 2% sucrose before freeze drying, Factor VIII, total protein and fibrinogen remain virtually stable (less than 15% loss) during heating of the material to 60, 64 or 68 degrees C for 24 to 72 h without changes of protein spectrum following heating. The heated product when stored at 4 degrees C remains stable for at least 3 months. In two severe haemophiliacs receiving this heat treated product, in vivo Factor VIII recovery was 100% with a mean half life of 10.2 h.

Influence of the primary anticoagulant on the recovery of factor VIII in cryoprecipitate

The influence of anticoagulant on overall factor VIII-yield was measured by drawing blood from one donor simultaneously in three bags containing ACD, CPD and heparin, respectively. After parallel processing factor VIII:C and factor VIII:CAg were measured. It is concluded that, under the circumstances used in this experiment, CPD gives the highest yield of factor VIII.

Small-pool high-yield factor VIII production

Hemophilia care depends on several factors for the production of purified FVIII: plasma procurement, plasma logistics, production method, and efficacy. The latter two are restrictive factors, both for the supply and the safety of FVIII preparations. Conventional production methodology unavoidably recovers only 10 to 20% of usable protein, therefore requiring large pools of source plasma. Related to pool size is the transmission of diseases, which poses unnecessary risks for patients. The development of new technologies to better recover FVIII allows reduction of the pool size: crush-thaw, controlled pore-glass chromatography, and heparin double-cold precipitation techniques. This review will reflect on current production methods, pool size concept, small-pool approaches in FVIII production, and future developments.

Influence of heparin and calcium chloride on assay, stability, and recovery of factor VIII

The influence of heparin alone or in conjunction with calcium chloride on the coagulation assay for factor VIII, on the stability of factor VIII in blood and in plasma, and on the recovery of factor VIII in cryoprecipitate and in an intermediate purity concentrate was investigated. A stabilizing effect of heparin and calcium on factor VIII activity in blood and plasma could be confirmed. We were, however, unable to make use of the higher activity that can, under certain circumstances, be recovered in the cryoprecipitates; this was mainly due to the poor solubility of cryoprecipitates prepared from heparinized blood. Heparin (or the absence of a calcium chelator) also interferes with the recovery of plasma components other than factor VIII.

A process for preparation of 'high-purity' factor VIII by controlled pore glass treatment

A simple process for large-scale manufacture of 'high-purity' factor VIII is described in detail. A crude concentrate prepared from washed cryo is treated with controlled pore glass (CPG, 500 A pore diameter) in proportion of 20-30 ml of CPG to 1 g input of protein. The slurry is poured into a separation column and the effluent purified concentrate collected. The remaining factor VIII in the void volume is displaced by a wash solution. After passage through a 0.2 micron membrane filter the product is dispensed and lyophilized. Maintaining the operating pH at 6.5-6.7 and adding synthetic amino acids improved the yield and solubility. The current concentrate contains 1 unit of factor VIII per mg protein (10 units mg fibrinogen) with a recovery of 250 units/kg plasma. The CPG stage is non-destructive, yielding more than 90% of the input factor VIII. In 1980-1983, more than 3 X 10(6) units have been used in New South Wales, mostly for massive cover in surgical patients. In collaboration with the Commonwealth Serum Laboratories, it is intended to expand production for use in other Australian States.

Pilot study for large-scale plasma procurement using automated plasmapheresis

A pilot study for large-scale automated plasmapheresis using the Haemonetics Model 50 machine was undertaken in the Yorkshire Region of the United Kingdom to determine the viability of such a programme for national self-sufficiency in fresh plasma procurement for factor VIII concentrate production. The study was designed to resolve three areas of concern: donor safety and recruitment; a cost analysis, and the choice of anticoagulant for optimum factor VIII yields. The results show that large-scale automated plasmapheresis could safely and economically produce high-quality source plasma necessary for national self-sufficiency.