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Note: the following studies show that ISG is safe IF all other processes for preparation are sterile. That was not the case until the 90's. The products were not pasteurized until the eighties. Prior to this, the Fractionation process, at all four plants, including Connaught in Canada, were constantly sited by the FDA for violations of Good Manufacturing procedures for sanitary processes and equipment.
Three
generations of immunoglobulin G preparations for clinical use. McCue JP, Hein RH, Tenold R Rev
Infect Dis 1986 Jul-Aug;8 Suppl 4:S374-81 The
first purified human immunoglobulin G (IgG) preparation used clinically was
immune serum globulin (ISG), which was prepared in the 1940s by E. J. Cohn's
group. It was originally formulated in water with 0.3 M glycine at pH 6.8 and
was 70%-80% monomeric. ISG was safe when given intramuscularly and efficacious
for measles and hepatitis prophylaxis. The next generation of purified IgG began
in the 1960s with chemically modified preparations suitable for intravenous
administration. The first such IgG intravenous preparation (IGIV) in the United
States was IGIV pH 6.8 (Gamimune, Cutter Biological), in which the
anticomplement activity found in ISG was removed by reduction and alkylation of
disulfide bridges. This product was originally formulated as a 5% IgG solution
in water (pH 6.8) with 0.2 M glycine in 10% maltose for stabilization. It
remained stable for at least 2.5 years at 5 degrees C, was 80%-90% monomeric,
had virtually no anticomplement activity, was safe given intravenously, and was
efficacious for prophylaxis in agammaglobulinemic patients. A third generation
of purified IgG has since been developed; IGIV pH 4.25, (Gamimune N, Cutter
Biological), which was isolated by the Cohn method from human plasma and is safe
for intravenous use, is a 5% solution of IgG in water (pH 4.25) with 10%
maltose. The product is greater than 99%
IgG, greater than 95% monomeric, and has greater than 90% less anticomplement
activity than ISG. PMID:
3092303, UI: 86315374
FDA/ORA Compliance Program Guidance 7342.006 CHAPTER 42 - BLOOD AND BLOOD PRODUCTS Plasma Fractionation Blood plasma contains a mixture of hundreds of different kinds of proteins, only a few of which are of therapeutic interest. To make plasma derivative products, plasma can be treated with a variety of substances to separate the desired proteins from others, in a process called fractionation. Fractionation of plasma, from pools often derived from thousands of donors, was developed during World War II by Cohn and co-workers at Harvard Medical School. Today, most plasma derivative manufacturers use a modified Cohn method developed by Oncley (Cohn-Oncley fractionation process) or further variants of this method, that permit manufacture of additional products. Fractionation by the Cohn-Oncley method relies on precipitation of plasma proteins by a combination of cold alcohol (usually ethanol)-water mixtures and adjustments of pH, ionic strength, temperature, and protein concentration. Alternatively, some manufacturers separate plasma derivatives by column chromatography using ion exchange, gel filtration, or affinity methods, without alcohol. In all cases, fractions of plasma are separated sequentially, with the product from one step, such as the precipitate and/or supernatant, becoming the starting material for the next step in the fractionation process. If each step is not done properly, subsequent fractions can be adversely affected. Thus, the integrity of each final product is dependent on all of the preceding steps in the process. After fractionation, derivatives undergo further processing to purify and concentrate proteins and to inactivate or remove (clearance) any bacterial or viral contaminants. While early steps in the manufacturing process are not performed aseptically, all final products are sterile. Types of viral clearance include those steps that are part of the fractionation process itself, e.g., pH4/pepsin or polyethylene glycol (PEG) fractionation, or those steps that are deliberately added, e.g., solvent/detergent treatment or viral filtration. In some instances more than one viral clearance step is used for a given product. Plasma derivatives are similar to other biological products in that they are protein-based and subject to denaturization at high temperatures. These products are usually filled by using aseptic processing techniques, and cannot be terminally sterilized, although in some instances they can be heat-treated in the final container to effect viral or bacterial inactivation. A few plasma proteins may also be manufactured by recombinant DNA methods. Fractionation Products Each plasma fraction is enriched in specific protein components and is used for a different purpose. In the Cohn-Oncley method, Fraction I contains mostly fibrinogen (not a licensed product), the main protein component of blood clots. Fraction II+III has a high concentration of immunoglobulins (antibodies). Some manufacturers use Fraction IV to prepare licensed products; others consider it a by-product. Fraction IV-1 is the source material for Alpha-1-proteinase Inhibitor (Human); Fraction IV-4+V is the source of Plasma Protein Fraction (Human). Fraction V is the source of Albumin (Human). Most of these products, but not all are intravenously administered. A description of some of the major plasma derivatives follows: Antihemophilic Factor (Human) (AHF, Factor VIII). AHF protein, one component of the cryoprecipitate fraction of plasma, is used to treat classical hemophilia (hemophilia A). Cryoprecipitate is the solid material that remains after frozen plasma is thawed at a near freezing temperature; it serves as the source of AHF. After the cryoprecipitate dissolves upon warming, the AHF in it can be purified to a high degree, subjected to various viral clearance procedures, and prepared as a lyophilized concentrate. AHF is administered intravenously. NOTE: Even though the clinically active ingredient is the same, AHF is not the same product as Cryoprecipitated AHF, a single donor product prepared in blood banks. Factor IX Complex (Human) is adsorbed from the plasma fraction remaining after cryoprecipitate removal. It is a heat- or solvent/detergent-treated, lyophilized preparation containing factors II, VII, IX, and X. It is administered intravenously for the prevention and control of bleeding caused by Factor IX deficiency (hemophilia B), and other coagulation disorders. Coagulation Factor IX (Human) is a highly purified factor IX product that contains negligible amounts of other coagulation factors, and is used to treat hemophilia B. Immune Globulin (Human) (IG) is a solution of immunoglobulin G (IgG) indicated for prophylaxis of hepatitis A, prevention or modification of measles (Rubeola), and for immunoglobulin deficiency. It is administered intramuscularly. Additional specific immune globulins for intramuscular administration are obtained from donors whose plasma contains selected high titer antibodies. Products are available for use in the passive prophylaxis of varicella-zoster, tetanus, hepatitis B, rabies, and other infections. Another product, Rho(D) Immune Globulin (Human), is for the prevention of sensitization to the Rho(D) antigen and hemolytic disease of the newborn. Some of the intramuscular immunoglobulin products have been subjected to heat- or solvent/detergent-treatment. Immune Globulin Intravenous (Human) (IGIV) is a lyophilized preparation that contains intact, unmodified, immunoglobulin. It is often stabilized with monosaccharide (sucrose, glucose, or mannose) and/or Albumin (Human) or glycine. It is indicated for patients with primary immunodeficiency, immune thrombocytopenia and Kawasaki's disease. Additional specific IGIV products are also available and used for such indications as prevention of hemolytic disease of the newborn, or passive prophylaxis of cytomegalovirus or respiratory syncytial virus. All IGIV products have been subjected to viral inactivation/removal procedures by either fortuitous or deliberate methods. http://www.fda.gov/ora/cpgm/42_006.html
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| Transfusion 1992 Nov-Dec;32(9):824-8 |
Vox Sang 1974;27(4):302-9
Berg JV, Berntsen KO, Bjorling H, Holmstrom B, Vyas GN
PMID: 4213354, UI: 75014376
Low Frequency of Cirrhosis in a Hepatitis C (Genotype 1b) Single-Source Outbreak in Germany: A 20-Year Multicenter Study.
Hepatology 2000 Jul;32(1):91-96
Wiese M, Berr F, Lafrenz M, Porst H, Oesen U
University Affiliated Hospital St. Georg of Leipzig, Departments of Medicine
of the Universities, Germany.
>From August 1978 until March 1979, 14 batches of anti-D immune globulin contaminated with hepatitis C virus (HCV) genotype 1b (20,000-480,000
copies/dose) from a single erythrocyte donor had been administered for prophylaxis of rhesus isoimmunization throughout East Germany.
All 2,867 women involved had been recalled after January 12, 1979 for repeated screening of alanine transaminase (ALT). They were prospectively
followed in regional centers. We have reexamined a cohort of 1,018 women (median age 24, range 16-38 years at infection) on follow-up for 20 years in
9 representative centers. Within 6 months after anti-D administration, 10% of these women had no evidence of disease and 90% had acute hepatitis C (n =
917) including 49% with symptomatic and 22% with icteric course. After 20 years, 85% of the 917 affected women still tested positive for HCV
antibodies (among them 3% responded to interferon treatment) and 55% were positive for HCV RNA (among them 7% were nonresponders to interferon and 3%
were apparent HCV carriers). Only 4 (0.4%) had overt cirrhosis. Two (0.2%)
died of superinfected fulminant hepatitis B or alcoholism and cirrhosis, respectively. Histology obtained in 44% of the viremic women showed
hepatitis of minimal to moderate grade in 96%, portal fibrosis in 47%, and septal fibrosis in 3% of the cases.
In conclusion, formerly healthy young women, without hepatic comorbidity, may clear HCV (1b) infection in half of the cases or develop mild chronic
hepatitis C with low risk of progression to cirrhosis within 20 years.
PMID: 10869294
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