US3686395A - Process for preparation of storage stable hepatitis-free serum - Google Patents
Process for preparation of storage stable hepatitis-free serum Download PDFInfo
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- US3686395A US3686395A US78949A US3686395DA US3686395A US 3686395 A US3686395 A US 3686395A US 78949 A US78949 A US 78949A US 3686395D A US3686395D A US 3686395DA US 3686395 A US3686395 A US 3686395A
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- 210000002966 serum Anatomy 0.000 title claims abstract description 41
- 238000000034 method Methods 0.000 title claims description 26
- 238000002360 preparation method Methods 0.000 title abstract description 8
- 208000006454 hepatitis Diseases 0.000 title description 10
- RMAQACBXLXPBSY-UHFFFAOYSA-N silicic acid Chemical compound O[Si](O)(O)O RMAQACBXLXPBSY-UHFFFAOYSA-N 0.000 claims abstract description 38
- 235000012239 silicon dioxide Nutrition 0.000 claims abstract description 38
- 238000011146 sterile filtration Methods 0.000 claims abstract description 12
- 238000009281 ultraviolet germicidal irradiation Methods 0.000 claims description 17
- 210000004369 blood Anatomy 0.000 claims description 6
- 239000008280 blood Substances 0.000 claims description 6
- 238000001914 filtration Methods 0.000 claims description 6
- 238000002156 mixing Methods 0.000 claims description 6
- 210000002381 plasma Anatomy 0.000 abstract description 36
- 102000004895 Lipoproteins Human genes 0.000 abstract description 15
- 108090001030 Lipoproteins Proteins 0.000 abstract description 15
- 102000004169 proteins and genes Human genes 0.000 abstract description 9
- 108090000623 proteins and genes Proteins 0.000 abstract description 9
- 239000003153 chemical reaction reagent Substances 0.000 abstract description 3
- 238000010828 elution Methods 0.000 abstract description 3
- 230000000984 immunochemical effect Effects 0.000 abstract description 3
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 23
- 239000002244 precipitate Substances 0.000 description 15
- 241000700605 Viruses Species 0.000 description 13
- 229910002012 Aerosil® Inorganic materials 0.000 description 10
- 239000000047 product Substances 0.000 description 8
- 235000018102 proteins Nutrition 0.000 description 8
- 238000001179 sorption measurement Methods 0.000 description 8
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 7
- 108010017384 Blood Proteins Proteins 0.000 description 6
- 102000004506 Blood Proteins Human genes 0.000 description 6
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 6
- 231100000283 hepatitis Toxicity 0.000 description 6
- 239000000243 solution Substances 0.000 description 6
- 241000894006 Bacteria Species 0.000 description 5
- 238000001816 cooling Methods 0.000 description 5
- 239000007788 liquid Substances 0.000 description 5
- 239000000463 material Substances 0.000 description 5
- 108010049003 Fibrinogen Proteins 0.000 description 4
- 102000008946 Fibrinogen Human genes 0.000 description 4
- 239000003463 adsorbent Substances 0.000 description 4
- 238000004925 denaturation Methods 0.000 description 4
- 230000036425 denaturation Effects 0.000 description 4
- 229940012952 fibrinogen Drugs 0.000 description 4
- 239000000203 mixture Substances 0.000 description 4
- 239000011148 porous material Substances 0.000 description 4
- 241000125205 Anethum Species 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 3
- 101000929940 Homo sapiens Adrenocortical dysplasia protein homolog Proteins 0.000 description 3
- 239000000440 bentonite Substances 0.000 description 3
- 229910000278 bentonite Inorganic materials 0.000 description 3
- SVPXDRXYRYOSEX-UHFFFAOYSA-N bentoquatam Chemical compound O.O=[Si]=O.O=[Al]O[Al]=O SVPXDRXYRYOSEX-UHFFFAOYSA-N 0.000 description 3
- 230000006866 deterioration Effects 0.000 description 3
- 102000054726 human ACD Human genes 0.000 description 3
- 239000011164 primary particle Substances 0.000 description 3
- 239000012460 protein solution Substances 0.000 description 3
- 239000002510 pyrogen Substances 0.000 description 3
- 239000011780 sodium chloride Substances 0.000 description 3
- 238000003756 stirring Methods 0.000 description 3
- 229910002016 Aerosil® 200 Inorganic materials 0.000 description 2
- 241001465754 Metazoa Species 0.000 description 2
- 239000000654 additive Substances 0.000 description 2
- 239000010425 asbestos Substances 0.000 description 2
- 239000011324 bead Substances 0.000 description 2
- 239000013060 biological fluid Substances 0.000 description 2
- GUJOJGAPFQRJSV-UHFFFAOYSA-N dialuminum;dioxosilane;oxygen(2-);hydrate Chemical compound O.[O-2].[O-2].[O-2].[Al+3].[Al+3].O=[Si]=O.O=[Si]=O.O=[Si]=O.O=[Si]=O GUJOJGAPFQRJSV-UHFFFAOYSA-N 0.000 description 2
- 238000001962 electrophoresis Methods 0.000 description 2
- 238000002474 experimental method Methods 0.000 description 2
- 239000000706 filtrate Substances 0.000 description 2
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- 239000011521 glass Substances 0.000 description 2
- 238000000760 immunoelectrophoresis Methods 0.000 description 2
- 238000000338 in vitro Methods 0.000 description 2
- 238000001802 infusion Methods 0.000 description 2
- 229910052901 montmorillonite Inorganic materials 0.000 description 2
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- 239000012266 salt solution Substances 0.000 description 2
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- HMUNWXXNJPVALC-UHFFFAOYSA-N 1-[4-[2-(2,3-dihydro-1H-inden-2-ylamino)pyrimidin-5-yl]piperazin-1-yl]-2-(2,4,6,7-tetrahydrotriazolo[4,5-c]pyridin-5-yl)ethanone Chemical compound C1C(CC2=CC=CC=C12)NC1=NC=C(C=N1)N1CCN(CC1)C(CN1CC2=C(CC1)NN=N2)=O HMUNWXXNJPVALC-UHFFFAOYSA-N 0.000 description 1
- VZSRBBMJRBPUNF-UHFFFAOYSA-N 2-(2,3-dihydro-1H-inden-2-ylamino)-N-[3-oxo-3-(2,4,6,7-tetrahydrotriazolo[4,5-c]pyridin-5-yl)propyl]pyrimidine-5-carboxamide Chemical compound C1C(CC2=CC=CC=C12)NC1=NC=C(C=N1)C(=O)NCCC(N1CC2=C(CC1)NN=N2)=O VZSRBBMJRBPUNF-UHFFFAOYSA-N 0.000 description 1
- SXAMGRAIZSSWIH-UHFFFAOYSA-N 2-[3-[2-(2,3-dihydro-1H-inden-2-ylamino)pyrimidin-5-yl]-1,2,4-oxadiazol-5-yl]-1-(2,4,6,7-tetrahydrotriazolo[4,5-c]pyridin-5-yl)ethanone Chemical compound C1C(CC2=CC=CC=C12)NC1=NC=C(C=N1)C1=NOC(=N1)CC(=O)N1CC2=C(CC1)NN=N2 SXAMGRAIZSSWIH-UHFFFAOYSA-N 0.000 description 1
- ZRPAUEVGEGEPFQ-UHFFFAOYSA-N 2-[4-[2-(2,3-dihydro-1H-inden-2-ylamino)pyrimidin-5-yl]pyrazol-1-yl]-1-(2,4,6,7-tetrahydrotriazolo[4,5-c]pyridin-5-yl)ethanone Chemical compound C1C(CC2=CC=CC=C12)NC1=NC=C(C=N1)C=1C=NN(C=1)CC(=O)N1CC2=C(CC1)NN=N2 ZRPAUEVGEGEPFQ-UHFFFAOYSA-N 0.000 description 1
- YJLUBHOZZTYQIP-UHFFFAOYSA-N 2-[5-[2-(2,3-dihydro-1H-inden-2-ylamino)pyrimidin-5-yl]-1,3,4-oxadiazol-2-yl]-1-(2,4,6,7-tetrahydrotriazolo[4,5-c]pyridin-5-yl)ethanone Chemical compound C1C(CC2=CC=CC=C12)NC1=NC=C(C=N1)C1=NN=C(O1)CC(=O)N1CC2=C(CC1)NN=N2 YJLUBHOZZTYQIP-UHFFFAOYSA-N 0.000 description 1
- 229910002018 Aerosil® 300 Inorganic materials 0.000 description 1
- 229910002019 Aerosil® 380 Inorganic materials 0.000 description 1
- 229910002020 Aerosil® OX 50 Inorganic materials 0.000 description 1
- 102000015081 Blood Coagulation Factors Human genes 0.000 description 1
- 108010039209 Blood Coagulation Factors Proteins 0.000 description 1
- 108010075016 Ceruloplasmin Proteins 0.000 description 1
- 102100023321 Ceruloplasmin Human genes 0.000 description 1
- 102000015779 HDL Lipoproteins Human genes 0.000 description 1
- 108010010234 HDL Lipoproteins Proteins 0.000 description 1
- 239000004677 Nylon Substances 0.000 description 1
- 241001417495 Serranidae Species 0.000 description 1
- 229920002472 Starch Polymers 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- VEZXCJBBBCKRPI-UHFFFAOYSA-N beta-propiolactone Chemical compound O=C1CCO1 VEZXCJBBBCKRPI-UHFFFAOYSA-N 0.000 description 1
- 239000003114 blood coagulation factor Substances 0.000 description 1
- 238000005119 centrifugation Methods 0.000 description 1
- FOCAUTSVDIKZOP-UHFFFAOYSA-M chloroacetate Chemical compound [O-]C(=O)CCl FOCAUTSVDIKZOP-UHFFFAOYSA-M 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
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- 238000011109 contamination Methods 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- 238000003745 diagnosis Methods 0.000 description 1
- 238000000502 dialysis Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000001727 in vivo Methods 0.000 description 1
- 230000002779 inactivation Effects 0.000 description 1
- 230000002452 interceptive effect Effects 0.000 description 1
- 238000011835 investigation Methods 0.000 description 1
- 238000002955 isolation Methods 0.000 description 1
- 150000002632 lipids Chemical class 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 229920001778 nylon Polymers 0.000 description 1
- 238000009928 pasteurization Methods 0.000 description 1
- 229920006316 polyvinylpyrrolidine Polymers 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 235000004252 protein component Nutrition 0.000 description 1
- 238000005057 refrigeration Methods 0.000 description 1
- 235000019698 starch Nutrition 0.000 description 1
- 239000008107 starch Substances 0.000 description 1
- 230000001954 sterilising effect Effects 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
- 239000012258 stirred mixture Substances 0.000 description 1
Classifications
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K35/00—Medicinal preparations containing materials or reaction products thereof with undetermined constitution
- A61K35/12—Materials from mammals; Compositions comprising non-specified tissues or cells; Compositions comprising non-embryonic stem cells; Genetically modified cells
- A61K35/14—Blood; Artificial blood
- A61K35/16—Blood plasma; Blood serum
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61L—METHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
- A61L2/00—Methods or apparatus for disinfecting or sterilising materials or objects other than foodstuffs or contact lenses; Accessories therefor
- A61L2/0005—Methods or apparatus for disinfecting or sterilising materials or objects other than foodstuffs or contact lenses; Accessories therefor for pharmaceuticals, biologicals or living parts
- A61L2/0011—Methods or apparatus for disinfecting or sterilising materials or objects other than foodstuffs or contact lenses; Accessories therefor for pharmaceuticals, biologicals or living parts using physical methods
Definitions
- This invention relates to lipoprotein-free, stable serum and plasma and more particularly to stable hepatitis-free serum and plasma and to a process for making the same.
- Stabilized plasma protein solutions are generally prepared by fractionation. Adsorption on bentonite and treatment with monochloroacetate are also known (Donald Dawson et al. lSR Volume II, No. 1, January, 1962, 31). However, fractionation yields only plasma protein solutions which contain no therapeutically important fractions. With the other processes, it is not possible to achieve any stability.
- lt isstill another object to protect sera and plasma from deterioration caused by lipoproteins present therein without the use of chemical additives and without subsequent denaturation of the serum protein.
- colloidal silicic acid is capable under certain reaction conditions quantitatively to absorb not only alpha alpha and fi-lipoproteins but in addition the fibrinogen present in serum and plasma.
- serum and plasma are treated by intimately contacting the same with colloidal silicic acid, protein solutions are obtained which still contain all the therapeutically important constituents and which are substantially stable to storage due to the complete removal of fibrinogen which is unstable in solution as well as the complete removal of the lipoproteins, so that at a constant refrigeration temperature 4 to 6C) storage is possible for up to 2 years without any appearance of cloudiness and without any loss of therapeutic activity.
- the present invention is directed to a process for the preparation of lipoprotein-free, stable and sterile serum, which is characterized in that blood serum or blood plasma is intimately mixed with 250 to 500 mg. of colloidal silicic acid per gram of total protein and is thereafter purified, following removal of the silicic acid, by a combined treatment with UV irradiation (UV ultraviolet) and sterile filtration.
- blood serum or blood plasma is intimately mixed with 250 to 500 mg. of colloidal silicic acid per gram of total protein and is thereafter purified, following removal of the silicic acid, by a combined treatment with UV irradiation (UV ultraviolet) and sterile filtration.
- the sterile filtration is carried out first and UV-irradiation thereafter, although the sequence is not critical.
- the treatment of the plasma and serum according to the invention is preferably carried out at temperatures of up to 50C, in particular-between 20 and 50C.
- the preferred pH range during the processing lies between 6.5 and 8.
- the duration of the mixing process depends on the type of apparatus used for mixing.
- Mixing times as used in practice consist for example, of l to 8 hours treatment using mixers rotating at a suitable speed.
- the UV-irradiation is preferably carried out at an intensity of 1 mW/cm minute.
- viruses analogous to the hepatitis virus are largely removed from the plasma or serum. It has already been indicated above thatwith the present state of the art, it is not possible to carry out experiments with the hepatitis virus on the animal. (in vivo) or in vitro. Therefore, it is necessary to rely on tests carried out with analogous viruses, the presence of which can be scientifically proved.
- the coli-phage has been described by LoGrippo as a particularly suitable analog for the hepatitis virus (lnvestigations of the Use of ,B-Propiolactones in Virus Inactivation; G.A.
- preserved plasma or serum is obtained which is stable in storage and free from hepatitis virus.
- Quantitative removal of viruses may be achieved especially if a filtration step using layer filters of a suitable nature and pore size, and preferably if asbestoscontaining filters impervious to bacteria, are employed in a filtration step carried out between the adsorption operation and UV-irradiation.
- the model viruses used were coli-T-phages.
- the adsorbed lipoproteins can be eluted from the silicic acid precipitate'which is obtained by the process of the invention, largely without denaturation, by utilizing concentrated salt solutions in the alkaline pH range. Concentration of the lipoproteins thus recovered can be effected by a preceding elution of other adsorbed proteins by means of salt solutions of low concentratlon.
- the lipoprotein solution is suitable for use as a biochemical and immunochemical reagent, in particular for medical diagnosis.
- the storage stable lipoprotein-free sera and plasma canbe used as infusion liquids as for any of the other conventional uses for which such materials are conventionally employed.
- the colloidal silicic acid used in the practice of the invention can be any of those commercially available, especially those sold as Aerosil silica by DEGUSSA of Germany or as Cab-O-Sil by Cabot in the United States. Since the products are ultimately intended for human administration, the only requirement is that the adsorbent not contain any interfering contaminants. Thus, for example, the whole Aerosil silica line is suitable except for those which contain substantial amounts of starch, e. g. Aerosil compositum, or hydrophobic-imparting radicals, e.g. Aerosil R. 972, and their Cab-O- Sil counterparts.
- the surface area and particle size of the colloidal silicic acid may vary widely embracing, for example, the entire spread of commercial products which have primary particle sizes of about 3 to 50 m,u. and densities ranging from about 2.5 up to as high as 7.8 pounds per cubic foot, achieved by compression.
- the standard products are known as Aerosil 200 or Cab-O-Sil M-5 which have medium range surface areas of about 200 square meters per gram. Because of their higher surfaces Cab-O-Sil H-S or Aerosil 300, having 300 square meters of surface per gram, are even more effective on a weight basis; the extra high surface products such as Cab-O-Sil EH-S and Aerosil 380 have 380 square meters of surface per gram and are most effective.
- the surface area could be as low as square meters per gram, e.g Aerosil MOX 80, or even as low as 50 square meters per gram, e.g. Aerosil OX 50, although somewhat larger quantities would be required for a given result.
- the surfaces are all so large, however, that the indicated range of about 250 to 500 mg. of colloidal silicic acid per gram of total protein covers the practical operations; if materials of lower surface area are used, the upper part of the weight range will be required and/or possibly longer contact times, higher surface area materials performing their role in lesser amounts and/0r shorter times.
- EXAMPLE 1 A 1 liter flask was filled with 20 g of colloidal silicic acid. (The exact product employed was the silicic acid marketed by the firm DEGUSSA under the Trade Name Aerosil.) Thereafter 200g of glass beads (0.4 cm diameter), were introduced into the flask and it was closed with muslin and sterilized in hot air for 2 hours at l80C. The serum which was to be treated (pH 7.5) was then introduced into the flask under sterile conditions. After the flask had been sealed, it was rotated for 4 hours at a rate of 40 to 50 revolutions per minute overhead.
- the adsorption efiect is in the main directly dependent on the speed of rotation.
- the contents of the flask were then heated for 4 hours at 45C in a water bath without stirring or shaking, and thereafter centrifuged after cooling for 30 minutes at 5,000 revolutions per minute.
- the flask contents were then subjected to UV irradiation in a Dill apparatus.
- the liquid was then filtered off under sterile conditions. After 4 weeks storage at +5C, the liquid if necessary could be filtered off from the slight precipitate which sometimes forms.
- the silicic acid precipitate was worked up as follows:
- the voluminous precipitate was frozen at 20C, thawed at room temperature, and centrifuged for 15 minutes at 5,000 revolutions per minute.
- the upper layer which demonstrated on paper electrophoresis and immunoelectrophoresis substantially the same composition as the main portion of adsorbed serum or plasma, was filtered under sterile conditions after UV irradiation, and thereafter filtered again, if necessary, after 4 weeks storage at 5C.
- Sera prepared in this manner were found to be both acutely and chronically toxicologically compatible and entirely free from pyrogens.
- EXAMPLE 2 1 liter of human serum and 20g of colloidal silicic acid sterilized using hot air were thoroughly stirred at pH 7.5 (physiological pH) for 4 hours at 45C, and after cooling, centrifuged for 30 minutes at 5,000 revolutions per minute and irradiated with UV light. Thereafter the contents were filtered under sterile conditions. After 4 weeks of storage at 5C, any precipitate which had formed was filtered off.
- EXAMPLE 3 1 liter of human ACD plasma was adjusted to a 5.5 percent protein content, and at a pH of 6.5 thoroughly stirred for 4 hours at 45C with 30g of colloidal silicic acid which had been sterilized with hot air. The stirred mixture was then centrifuged, irradiated with UV light and filtered under sterile conditions. After 4 weeks of storage at 5C, the liquid was filtered to remove any precipitate which had formed.
- EXAMPLE 4 A 1 liter flask was filled with 20g of colloidal silicic acid, preferably the silicic acid product sold by the firm DEGUSSA under the Trade Name Aerosil was used. 200g of glass beads having a diameter of 0.4 cm were introduced and the flask closed with muslin and sterilized with hot air for 2 hours at 180C. The serum to be treated (having a pH of 7.5) was introduced into the flask under sterile conditions. After the flask had been sealed, it was rotated for 4 hours at 40 to 50 revolutions per minute overhead. The adsorption as previously noted directly depends on the speed of rotation used.
- the contents of the flask were then heated for 4 hours at 45C in a water bath without stirring or shaking, and after cooling they were centrifuged for 30 minutes at 5,000 revolutions per minute following filtration using filter layers of suitable nature and pore size, the filtrate was irradiated with UV light using therefor a DILL apparatus. After 4 weeks of storage at +5C, the precipitate, if any had formed, was filtered off.
- the silicic acid precipitate remaining was worked up as follows: The voluminous precipitate was frozen at 20C, thawed at room temperature, and centrifuged for minutes at 5,000 revolutions per minute. The upper layer, which was analyzed by paper electrophoresis and immunoelectrophoresis had substantially the same composition as the main portion of adsorbed serum of plasma, was filtered, prior to UV irradiation, using therefor suitable filter layers and preferably asbestoscontaining filters which are impervious to bacteria.
- Sera prepared in this manner were both acutely and chronically toxicologically compatible and free from pyrogens.
- EXAMPLE 6 1 liter of human serum was thoroughly stirred at pH 7.5 (physiological pH) in admixture with g of hot-air sterilized colloidal silicic acid for 4 hours at 45C. After cooling, the contents were centrifuged for minutes at 5,000 revolutions per minute and were then filtered through asbestoscontaining filters constructed so they were impervious to bacteria. The filtrate was then irradiated with UV light. After 4 weeks of storage at 5C, the precipitate, if any had formed, was filtered off.
- the product thereby obtained had the same desirable properties as the product described in Example 5.
- EXAMPLE 7 1 liter of human ACD plasma was adjusted so as to have a 5 .5 percent protein content, and at a pH of 6.5 thoroughly stirred for 4 hours at 45C together with 30g of colloidal silicic acid which had been sterilized by hot air. The plasma-silicic acid batch was then centrifuged, filtered through asbestos-containing filters impervious to bacteria, and irradiated with UV light. After 4 hours of storage at 5C, the precipitate, if any had formed, was filtered off.
- the serum obtained was both acutely and chronically toxicologically compatible and entirely free from pyrogen.
- the recoveredprecipitate was suspended in 1 liter of H 0, and 450g of solid NaCl were then added thereto. The mixture was then stirred for 1 hour at pH 9.0, the pH being kept constant by the addition of NaOH. After centrifuging, the top layer was dialyzed for 24 hours against 20 liters of 0.7% NaCl solution at 5C, followed by dialysis against 1 liter of 10 percent polyvinyl pyrrolidone K 90. It was thereby concentrated to about 2 percent protein.
- the solution was then filtered under sterile conditions, the filter comprising multiple layers of filter material of pore sizes smaller than the solids to be removed.
- the colloidal silicic acid was the standard Aerosil material, i.e. that identified either as Aerosil or Aerosil 200 and having 200 square meters of surface per gram and a primary particle size of about 16 mp.
- Aerosil material i.e. that identified either as Aerosil or Aerosil 200 and having 200 square meters of surface per gram and a primary particle size of about 16 mp.
- a set of side-by-side runs were made with the same silicic acid as well as with others, as follows:
- Adsorbent In an identical run using montmorillonite, obtained from Carl Roth OHG, Düsseldorf, Germany, of undefined particle size and surface area and of 80 percent I purity, less than 5 percent of the lipoproteins were adsorbed.
- EXAMPLE 1 1 and examples are set forth by way of illustration and not limitation and that various modifications and changes may be made without departing from the spirit and scope of the present invention.
- a process for the preparation of lipoprotein-free, stable and sterile serum or plasma which comprises intimately admixing, at temperatures of up to about 50C, a blood member selected from the group consisting of serum and plasma with 250 to 500 mg of colloidal silicic acid per gram of total protein, whereinthe colloidal silicic acid has a primary particle size of about 3 to 50 m, a bulk density of about 2.5 to 7.8 pounds per cubic foot and 'a surface area of about 50 to 380 square meters per gram, and thereafter separating the silicic acid having the adsorbed lipoproteins from the blood member thereon.
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- Health & Medical Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Public Health (AREA)
- Hematology (AREA)
- Biomedical Technology (AREA)
- Medicinal Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Epidemiology (AREA)
- Animal Behavior & Ethology (AREA)
- General Health & Medical Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Veterinary Medicine (AREA)
- Cell Biology (AREA)
- Molecular Biology (AREA)
- Biotechnology (AREA)
- Developmental Biology & Embryology (AREA)
- Immunology (AREA)
- Virology (AREA)
- Zoology (AREA)
- Pharmacology & Pharmacy (AREA)
- Medicines Containing Material From Animals Or Micro-Organisms (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
- Peptides Or Proteins (AREA)
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DEB0086560 | 1966-04-06 | ||
DE1966B0089704 DE1617335B2 (de) | 1966-11-05 | 1966-11-05 | Verfahren zur herstellung von lipoproteinfreiem, stabilem und sterilem serum |
DEB0091011 | 1967-02-02 |
Publications (1)
Publication Number | Publication Date |
---|---|
US3686395A true US3686395A (en) | 1972-08-22 |
Family
ID=27209344
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US78949A Expired - Lifetime US3686395A (en) | 1966-04-06 | 1970-10-07 | Process for preparation of storage stable hepatitis-free serum |
Country Status (8)
Country | Link |
---|---|
US (1) | US3686395A (enrdf_load_stackoverflow) |
AT (1) | AT270868B (enrdf_load_stackoverflow) |
BE (1) | BE696020A (enrdf_load_stackoverflow) |
FR (1) | FR7395M (enrdf_load_stackoverflow) |
GB (1) | GB1115849A (enrdf_load_stackoverflow) |
NL (1) | NL6702923A (enrdf_load_stackoverflow) |
SE (1) | SE328089B (enrdf_load_stackoverflow) |
SU (1) | SU477580A3 (enrdf_load_stackoverflow) |
Cited By (25)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3822095A (en) * | 1972-08-14 | 1974-07-02 | Block Engineering | System for differentiating particles |
US3972858A (en) * | 1973-12-22 | 1976-08-03 | Behringwerke Aktiengesellschaft | Process for the preparation of choleragen |
US4136094A (en) * | 1977-08-31 | 1979-01-23 | The Regents Of The University Of Minnesota | Preparation of intravenous human and animal gamma globulins and isolation of albumin |
JPS5446813A (en) * | 1977-09-22 | 1979-04-13 | Toyo Soda Mfg Co Ltd | Separation of plasmaprotein |
US4164495A (en) * | 1976-04-06 | 1979-08-14 | Nordisk Insulinlaboratorium | Method of recovering immunoglobulin using a polyol and an alkanoic acid |
US4228154A (en) * | 1979-02-26 | 1980-10-14 | Armour Pharmaceutical Company | Purification of plasma albumin by ion exchange chromatography |
US4251510A (en) * | 1979-08-15 | 1981-02-17 | Cutter Laboratories, Inc. | Intravenously injectable solution of plasma protein fraction free from bradykinin, kininogen and prekallikrein activators and processes for its production |
WO1982002900A1 (en) * | 1981-02-27 | 1982-09-02 | Inc Amf | Tissue culture medium |
US4378346A (en) * | 1979-08-15 | 1983-03-29 | Tankersley Donald L | Intravenously injectable solution of plasma protein fraction free from bradykinin, kininogen and prekallikrein activators and processes for its production |
USRE31268E (en) * | 1976-04-06 | 1983-06-07 | Nordisk Insulinlaboratorium | Method of recovering immunoglobulin using a polyol and an alkanoic acid |
WO1984000569A1 (en) * | 1982-07-23 | 1984-02-16 | Amf Inc | Fibrous media containing millimicron sized particulates |
WO1984002916A1 (en) * | 1983-01-26 | 1984-08-02 | Amf Inc | Tissue culture medium |
US4480029A (en) * | 1981-04-27 | 1984-10-30 | Baxter Travenol Laboratories, Inc. | Biological indicators and their use |
US4503039A (en) * | 1982-12-21 | 1985-03-05 | Biotest-Serum-Institut Gmbh | Coagulant plasma-protein solution |
US4511473A (en) * | 1982-02-09 | 1985-04-16 | Amf Incorporated | Fibrous media containing millimicron-sized particulates |
EP0139975A1 (de) * | 1983-08-26 | 1985-05-08 | BEHRINGWERKE Aktiengesellschaft | Verfahren zur Pasteurisierung von Humanplasma |
EP0124363A3 (en) * | 1983-05-02 | 1985-07-03 | Advanced Genetics Research Institute | Photochemical decontamination treatment of whole blood or blood components |
US4533634A (en) * | 1983-01-26 | 1985-08-06 | Amf Inc. | Tissue culture medium |
US4639513A (en) * | 1984-02-02 | 1987-01-27 | Cuno Inc. | Intravenously injectable immunoglobulin G (IGG) and method for producing same |
US4764369A (en) * | 1983-07-14 | 1988-08-16 | New York Blood Center Inc. | Undenatured virus-free biologically active protein derivatives |
US4820805A (en) * | 1983-07-14 | 1989-04-11 | New York Blood Center, Inc. | Undenatured virus-free trialkyl phosphate treated biologically active protein derivatives |
US5418130A (en) * | 1990-04-16 | 1995-05-23 | Cryopharm Corporation | Method of inactivation of viral and bacterial blood contaminants |
WO1996009371A1 (en) * | 1994-09-21 | 1996-03-28 | Stichting Scheikundig Onderzoek In Nederland | Protein mixture prepared from serum for use as component in media for in vitro culture of animal cells |
US6187572B1 (en) | 1990-04-16 | 2001-02-13 | Baxter International Inc. | Method of inactivation of viral and bacterial blood contaminants |
US20060110399A1 (en) * | 2004-11-18 | 2006-05-25 | Van Holten Robert W | Optimal placement of a robust solvent/detergent process post viral ultrafiltration of an immune gamma globulin |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE2837168A1 (de) * | 1978-08-25 | 1980-03-06 | Blutspendedienst Dt Rote Kreuz | Verfahren zur herstellung einer fuer die intravenoese anwendung geeigneten immunglobulinloesung |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
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US2469193A (en) * | 1942-02-09 | 1949-05-03 | Research Corp | Protein fractionation |
US3284434A (en) * | 1960-08-29 | 1966-11-08 | Univ Kansas State | Protein isolation and preparations |
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1967
- 1967-02-24 NL NL6702923A patent/NL6702923A/xx unknown
- 1967-03-07 GB GB10621/66D patent/GB1115849A/en not_active Expired
- 1967-03-17 AT AT258467A patent/AT270868B/de active
- 1967-03-23 BE BE696020D patent/BE696020A/xx unknown
- 1967-03-31 SE SE04492/67A patent/SE328089B/xx unknown
- 1967-04-05 FR FR101581A patent/FR7395M/fr not_active Expired
- 1967-09-29 SU SU1186878A patent/SU477580A3/ru active
-
1970
- 1970-10-07 US US78949A patent/US3686395A/en not_active Expired - Lifetime
Patent Citations (2)
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US2469193A (en) * | 1942-02-09 | 1949-05-03 | Research Corp | Protein fractionation |
US3284434A (en) * | 1960-08-29 | 1966-11-08 | Univ Kansas State | Protein isolation and preparations |
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Title |
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Clausen et al., Isolation of Ceruloplasmin, Protides of the Biological Fluids, 9th Colloquim, pp. 269 275, 1962. * |
Journal of the American Medical Association (JAMA), Vol. 138, No. 3, p. 255, 1948. * |
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Cited By (29)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3822095A (en) * | 1972-08-14 | 1974-07-02 | Block Engineering | System for differentiating particles |
US3972858A (en) * | 1973-12-22 | 1976-08-03 | Behringwerke Aktiengesellschaft | Process for the preparation of choleragen |
USRE31268E (en) * | 1976-04-06 | 1983-06-07 | Nordisk Insulinlaboratorium | Method of recovering immunoglobulin using a polyol and an alkanoic acid |
US4164495A (en) * | 1976-04-06 | 1979-08-14 | Nordisk Insulinlaboratorium | Method of recovering immunoglobulin using a polyol and an alkanoic acid |
US4136094A (en) * | 1977-08-31 | 1979-01-23 | The Regents Of The University Of Minnesota | Preparation of intravenous human and animal gamma globulins and isolation of albumin |
JPS5446813A (en) * | 1977-09-22 | 1979-04-13 | Toyo Soda Mfg Co Ltd | Separation of plasmaprotein |
US4228154A (en) * | 1979-02-26 | 1980-10-14 | Armour Pharmaceutical Company | Purification of plasma albumin by ion exchange chromatography |
US4251510A (en) * | 1979-08-15 | 1981-02-17 | Cutter Laboratories, Inc. | Intravenously injectable solution of plasma protein fraction free from bradykinin, kininogen and prekallikrein activators and processes for its production |
US4378346A (en) * | 1979-08-15 | 1983-03-29 | Tankersley Donald L | Intravenously injectable solution of plasma protein fraction free from bradykinin, kininogen and prekallikrein activators and processes for its production |
WO1982002900A1 (en) * | 1981-02-27 | 1982-09-02 | Inc Amf | Tissue culture medium |
US4473647A (en) * | 1981-02-27 | 1984-09-25 | Amf Inc. | Tissue culture medium |
US4480029A (en) * | 1981-04-27 | 1984-10-30 | Baxter Travenol Laboratories, Inc. | Biological indicators and their use |
US4511473A (en) * | 1982-02-09 | 1985-04-16 | Amf Incorporated | Fibrous media containing millimicron-sized particulates |
WO1984000569A1 (en) * | 1982-07-23 | 1984-02-16 | Amf Inc | Fibrous media containing millimicron sized particulates |
US4503039A (en) * | 1982-12-21 | 1985-03-05 | Biotest-Serum-Institut Gmbh | Coagulant plasma-protein solution |
US4533634A (en) * | 1983-01-26 | 1985-08-06 | Amf Inc. | Tissue culture medium |
WO1984002916A1 (en) * | 1983-01-26 | 1984-08-02 | Amf Inc | Tissue culture medium |
EP0124363A3 (en) * | 1983-05-02 | 1985-07-03 | Advanced Genetics Research Institute | Photochemical decontamination treatment of whole blood or blood components |
US4820805A (en) * | 1983-07-14 | 1989-04-11 | New York Blood Center, Inc. | Undenatured virus-free trialkyl phosphate treated biologically active protein derivatives |
US4764369A (en) * | 1983-07-14 | 1988-08-16 | New York Blood Center Inc. | Undenatured virus-free biologically active protein derivatives |
EP0139975A1 (de) * | 1983-08-26 | 1985-05-08 | BEHRINGWERKE Aktiengesellschaft | Verfahren zur Pasteurisierung von Humanplasma |
US4639513A (en) * | 1984-02-02 | 1987-01-27 | Cuno Inc. | Intravenously injectable immunoglobulin G (IGG) and method for producing same |
US5418130A (en) * | 1990-04-16 | 1995-05-23 | Cryopharm Corporation | Method of inactivation of viral and bacterial blood contaminants |
US6187572B1 (en) | 1990-04-16 | 2001-02-13 | Baxter International Inc. | Method of inactivation of viral and bacterial blood contaminants |
WO1996009371A1 (en) * | 1994-09-21 | 1996-03-28 | Stichting Scheikundig Onderzoek In Nederland | Protein mixture prepared from serum for use as component in media for in vitro culture of animal cells |
NL9401535A (nl) * | 1994-09-21 | 1996-05-01 | Stichting Scheikundig Onderzoe | Uit serum bereid eiwitmengsel voor het gebruik als component in media voor het in vitro kweken van dierlijke cellen. |
US20060110399A1 (en) * | 2004-11-18 | 2006-05-25 | Van Holten Robert W | Optimal placement of a robust solvent/detergent process post viral ultrafiltration of an immune gamma globulin |
US7655233B2 (en) | 2004-11-18 | 2010-02-02 | Ortho-Clinical Diagnostics, Inc. | Optimal placement of a robust solvent/detergent process post viral ultrafiltration of an immune gamma globulin |
US20100129893A1 (en) * | 2004-11-18 | 2010-05-27 | Van Holten Robert W | Optimal placement of a robust solvent/detergent process post viral ultrafiltration of an immune gamma globulin |
Also Published As
Publication number | Publication date |
---|---|
BE696020A (enrdf_load_stackoverflow) | 1967-09-25 |
SU477580A3 (ru) | 1975-07-15 |
GB1115849A (en) | 1968-05-29 |
SE328089B (enrdf_load_stackoverflow) | 1970-09-07 |
NL6702923A (enrdf_load_stackoverflow) | 1967-10-09 |
FR7395M (enrdf_load_stackoverflow) | 1969-11-03 |
AT270868B (de) | 1969-05-12 |
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Owner name: BIOTEST A.G., GERMANY Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNOR:BIOTEST SERUM-INSTITUT G.M.B.H., A LIMITED LIABILITY COMPANY OF GERMANY;REEL/FRAME:004893/0230 Effective date: 19871120 Owner name: BIOTEST A.G., A JOINT STOCK COMPANY OF GERMANY Free format text: ASSIGNMENT OF ASSIGNORS INTEREST.;ASSIGNOR:BIOTEST SERUM-INSTITUT G.M.B.H., A LIMITED LIABILITY COMPANY OF GERMANY;REEL/FRAME:004893/0230 Effective date: 19871120 |