WO1993009869A1 - Adsorbent for blood coagulation factor viii - Google Patents
Adsorbent for blood coagulation factor viii Download PDFInfo
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- WO1993009869A1 WO1993009869A1 PCT/JP1992/001480 JP9201480W WO9309869A1 WO 1993009869 A1 WO1993009869 A1 WO 1993009869A1 JP 9201480 W JP9201480 W JP 9201480W WO 9309869 A1 WO9309869 A1 WO 9309869A1
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- adsorbent
- factor viii
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07K—PEPTIDES
- C07K14/00—Peptides having more than 20 amino acids; Gastrins; Somatostatins; Melanotropins; Derivatives thereof
- C07K14/435—Peptides having more than 20 amino acids; Gastrins; Somatostatins; Melanotropins; Derivatives thereof from animals; from humans
- C07K14/745—Blood coagulation or fibrinolysis factors
- C07K14/755—Factors VIII, e.g. factor VIII C (AHF), factor VIII Ag (VWF)
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- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61P—SPECIFIC THERAPEUTIC ACTIVITY OF CHEMICAL COMPOUNDS OR MEDICINAL PREPARATIONS
- A61P7/00—Drugs for disorders of the blood or the extracellular fluid
- A61P7/04—Antihaemorrhagics; Procoagulants; Haemostatic agents; Antifibrinolytic agents
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/22—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising organic material
- B01J20/24—Naturally occurring macromolecular compounds, e.g. humic acids or their derivatives
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/22—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising organic material
- B01J20/26—Synthetic macromolecular compounds
- B01J20/261—Synthetic macromolecular compounds obtained by reactions only involving carbon to carbon unsaturated bonds
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/22—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising organic material
- B01J20/26—Synthetic macromolecular compounds
- B01J20/264—Synthetic macromolecular compounds derived from different types of monomers, e.g. linear or branched copolymers, block copolymers, graft copolymers
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/28—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
- B01J20/28002—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their physical properties
- B01J20/28004—Sorbent size or size distribution, e.g. particle size
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/30—Processes for preparing, regenerating, or reactivating
- B01J20/32—Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating
- B01J20/3202—Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating characterised by the carrier, support or substrate used for impregnation or coating
- B01J20/3206—Organic carriers, supports or substrates
- B01J20/3208—Polymeric carriers, supports or substrates
- B01J20/321—Polymeric carriers, supports or substrates consisting of a polymer obtained by reactions involving only carbon to carbon unsaturated bonds
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/30—Processes for preparing, regenerating, or reactivating
- B01J20/32—Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating
- B01J20/3231—Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating characterised by the coating or impregnating layer
- B01J20/3242—Layers with a functional group, e.g. an affinity material, a ligand, a reactant or a complexing group
- B01J20/3268—Macromolecular compounds
- B01J20/327—Polymers obtained by reactions involving only carbon to carbon unsaturated bonds
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/30—Processes for preparing, regenerating, or reactivating
- B01J20/32—Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating
- B01J20/3231—Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating characterised by the coating or impregnating layer
- B01J20/3242—Layers with a functional group, e.g. an affinity material, a ligand, a reactant or a complexing group
- B01J20/3268—Macromolecular compounds
- B01J20/3276—Copolymers
Definitions
- the present invention relates to an adsorbent for blood coagulation factor VIII (hereinafter often simply referred to as "factor VIII"). More specifically, molecules having a polycation suitable for efficiently adsorbing and recovering factor VIII from a solution containing various plasma proteins including factor VIII are bound and immobilized on a water-insoluble carrier. And an adsorbent made of a composite.
- Hemophilia A is an example of a congenital bleeding disorder. Hemophilia A is caused by a deficiency of a protein called factor VIII.In order for a person with hemophilia A to live as a healthy person, it is necessary to replace the lacking factor VIII. is there.
- Factor V II concentrates are usually prepared by using a precipitate from plasma called cryoprecipitate as a raw material and removing contaminating proteins such as fibrinogen and fibronectin.
- the recipe recipe can be obtained by centrifuging the precipitate generated by thawing fresh frozen plasma at a low temperature.
- the factor V III contained in plasma is 100%
- the recovery of factor V III in cryoprecipitate is as low as 40 to 50%.
- cryoprecipitate contains a large amount of contaminating proteins, it is necessary to remove those contaminating proteins.
- adsorption is performed by immobilizing a low-molecular-weight ligand such as a getylaminoethyl group on a water-insoluble carrier. Michalskieta 1.: Vox Sang, Vo 1.55, pp.
- factor IX blood coagulation factor IX
- factor VIII blood coagulation factor IX
- Factor VIII is a protein with a molecular weight of about 300,000. It is known from the amino acid sequence analysis that there is a region rich in acidic amino acids [G.A.V ehareta 1.: Natur'e, Vol. 3.12, pp. 3 3 7-3 4 2 (1 998 4)]. Furthermore, it is known to exist in blood as a complex with a von Willebrand factor having a multimeric structure with a molecular weight of 1,000,000 to 2,000,000 (Z.M. R uggerieta 1.: Blood, Vol. 57, PP. 114-11 4 3 (1 98 1)).
- the present inventors have found that in order to efficiently adsorb such a protein having a huge molecular weight, it has a large number of anion-exchange groups and a sufficient length.
- an adsorbent having a substance capable of firmly adsorbing by interacting with the complex at a plurality of points is suitable.
- the adsorbent consisting of a complex in which a molecule having a polycation is bonded to and immobilized on a water-insoluble carrier has an extremely specific adsorption to factor VIII. — It showed that it was able to adsorb and recover Factor VIII with high selectivity and high yield from solutions containing various plasma proteins including Factor VIII.
- the present invention has been completed based on these findings.
- one and primary object of the present invention is to provide a solution containing various plasma proteins, including factor VIII, from a solution containing factor VIII.
- An adsorbent forest capable of directly and specifically adsorbing factor I, and capable of easily desorbing and recovering adsorbed factor VIII.
- the molecular weight of a polycation-containing molecule is at least 15,500, unlike a complex formed by binding and immobilizing a molecule having a polycation to a water-insoluble carrier.
- an adsorbent for blood coagulation factor VIII wherein the positive charge density of the complex of 1 milliliter is from leq to 200 eq.
- the molecule having a polycation immobilized on the adsorbent of the present invention refers to a molecule having a molecular weight of at least 150000 and having a large number of anion exchange groups in the molecule.
- the anion exchange group include a primary amino group, a secondary amino group, a tertiary amino group, a primary ammonium base and the like.
- One of these anion exchange groups may be present alone in the molecule having a polycation, or two or more may be present.
- Examples of such a molecule include a homopolymer of a basic vinyl monomer having an anion exchange group in a side chain, or a vinyl copolymer which can be copolymerized with the basic vinyl monomer. Copolymer with monomer Can be mentioned. Further, instead of the basic vinyl monomer, a vinyl monomer having a side chain to which an anion exchange group can be added after polymerization may be used. Further, there may be mentioned polypeptides containing basic amino acids such as lysine and arginine.
- Examples of the basic vinyl monomer having an anion exchange group in the side chain include a vinyl monomer having a primary amino group, a secondary amino group, a tertiary amino group, and a quaternary ammonium base. Body included.
- Examples of such a biel monomer include acrylic acid derivatives, methacrylic acid derivatives, acrylic acid amide derivatives, and metaacrylic acid amines each having an amino group.
- Examples thereof include vinyl derivatives having a nitrogen-containing aromatic ring group such as a pyridyl group and an imidazolyl group in the side chain, and styrene derivatives substituted with an amino group.
- dimethylaminoethyl acrylate dimethylaminoethyl acrylate, dimethylaminoethyl acrylate, dimethylaminopropyl acrylate, 3-dimethylaminopropyl 2—hydroxypropylamine Rate, 3—Jethylamino2—Hydroxypropylacrylate, N—Dimethylaminoethylacrylate, N—Nethylethylaminoethylacrylate, Dimethylaminoethylmethacrylate Rate, getylaminoethyl methacrylate, getylaminopropyl methacrylate, 3—dimethylamine 2—hydroxypropyl propylmethacrylate, 3—getylamine 1—2— histamine Dro kiss Mouth pill methacrylate, N-dimethylamino methacrylate amide, N-ethylaminoethyl methacrylate, and the following formula:
- R is one CH 3 or one C 2 H 5 , X is (CH 2 ) n is an integer of 3)
- CHz -CH Such a vinyl monomer having a side chain that can be aminated after polymerization can also be used.
- Specific preferred examples of such a vinyl monomer include hydroxyxethyl acrylate and hydroxypropynoleacrylate. And hydroxypropyl methacrylate, and hydroxypropyl methacrylate.
- the basic butyl monomer may be an acrylic acid derivative, a metaacrylic acid derivative, an acrylic acid amide derivative or a methacrylic acid derivative having an amino group.
- vinyl acrylamide derivatives vinyl monomers that can be copolymerized with basic vinyl monomers include acrylic esters, metaacrylic esters, and N-alkylacrylic acids. Copolymers obtained using amides or N-alkyl methacrylates are preferred.
- the molecular weight of the molecule having a polycation of the present invention is at least 15,000. When the molecular weight is smaller than this, sometimes factor VIII is an extremely large protein, so that it is difficult to expect a sufficient interaction between the molecule and factor VIII.
- the positive charge density of the complex (1 mil / liter) composed of a molecule having a polycation and a water-insoluble carrier constituting the adsorbent is leq to 200 eq. .
- the positive charge density of the composite constituting the adsorbent of the present invention is determined by the following method. Swollen with water Put 1 milliliter of adsorbed material into a plastic column, wash with 1N hydrochloric acid, water, and 1N aqueous sodium hydroxide in that order, and adjust the pH of the liquid falling from the cam to 6.5.
- any of a hydrophilic carrier and a hydrophobic carrier can be used, but the hydrophobic carrier causes non-specific adsorption of proteins other than factor VIII to the carrier. Gives better results.
- the water-insoluble carrier is not particularly limited as long as it has a functional group that can be used for immobilizing a molecule having a polycation by chemical bonding.
- the chemical bond is preferably a covalent bond. Even when the water-insoluble carrier itself does not have such a functional group, one that can generate a functional group that can be used for immobilizing a molecule having a rebolication by appropriate chemical modification is used in the present invention. be able to.
- any known shape such as a particle shape, a fibrous shape, a hollow fiber shape, and a membrane shape can be used, but handling as an adsorbent In view of the above, particles and fibrous materials are preferred.
- examples of the particulate carrier include agarose ⁇ , dextran-based, cellulose-based and other natural polymer-based carriers, polyacrylamide-based, polyamide-based, and poly- amide-based carriers. Synthetic polymer-based carriers such as ester-based, polyurethane-based, and vinyl compound polymers can be mentioned.
- a carrier having a porous structure the surface area of the carrier is increased, so that the molecule having immobilized polythione and the factor VIII can be easily brought into contact with each other. It gives good results with increased volume.
- a polymer of a vinyl compound hydrophilized by one unit of a hydrophilic monomer can easily form a carrier having a porous structure, and can easily obtain a carrier having high physical strength.
- a crosslinked copolymer having a bul alcohol unit often reduces the non-specific adsorption of a protein to a carrier, and gives a favorable result in many cases.
- the fibrous carrier known fibers such as a cellulose-based fiber and a polyester-based fiber can be used.
- the fiber diameter is preferably in the range of 0.02 denier or 10 denier.
- the particulate support having a porous structure has an exclusion limit molecular weight in the range of 1,000 to 100,000,000, and an average particle size of 5 to 1,000 ⁇ m. ⁇ is preferred.
- Binding and immobilization of polycation-containing molecules to water-insoluble carriers It is better to use a chemical bond, especially a covalent bond, for the conversion.
- a known method for activating a water-insoluble carrier and a method for immobilizing a molecule having a polycation which are generally used in immobilized enzymes and affinity chromatography, can be used [Kenichi Kasai et al .: “Affinity mouth mouth one”, published by Tokyo Chemical Industry Co., Ltd. (1991):].
- a molecule (spacer) having an arbitrary length can be introduced between the water-insoluble carrier and the molecule having a polycation.
- the active group generated by activating the water-insoluble carrier is a group capable of reacting with a nucleophilic reactive group having an active hydrogen such as an amino group, a carboxyl group, a hydroxyl group, or a thiol group of a molecule having a polycation.
- a nucleophilic reactive group having an active hydrogen such as an amino group, a carboxyl group, a hydroxyl group, or a thiol group of a molecule having a polycation.
- epoxy group tresil group (tresy 1 gr)
- the adsorbent of the present invention can be obtained by contacting a solution containing various plasma proteins containing Factor VII
- Adsorb factor II Adsorb factor II.
- the solution containing various plasma proteins including factor VIII at this time may be plasma or a product from plasma.
- the products from plasma include the above-mentioned cryoprecipitate, The supernatant after separation and removal of the pithate, plasma from which some or all of the contaminant components have been removed by appropriate treatment with an ion exchange resin or the like can be mentioned.
- the adsorbent of the present invention is capable of adsorbing factor VIII in plasma under various conditions, but usually adsorbs at normal temperature and normal pressure. It is preferred in terms of sex.
- the temperature should be within the stable range of Factor V I I I, but is usually between 0 and 50 ° C.
- the adsorption time is not particularly limited, it is usually in the range of 10 minutes to 2 hours, and an appropriate time can be selected depending on the temperature and the method of adsorption.
- either a batch method or a column method can be used, but when a large amount of plasma is to be treated, the batch method is often preferred because it can be processed in a shorter time.
- a crosslinked copolymer having a vinyl alcohol unit was synthesized as shown below.
- 8 g and Yo Li becomes homogeneous mixture of polyvinyl alcohol 1 wt 0/0, V phosphate 2 hydrogen isocyanatomethyl Li um dihydrate 0.0 5 wt.
- the water-insoluble carrier obtained in the above step was used as a water-insoluble carrier (swelled with acetate). 3 Milliliters were suspended in acetonitrile 2.1 milliliters. To the suspension, add Tresyl Mouth Ride 45 microliters and pyridine 135 microliters and shake at room temperature for 10 minutes to obtain the active group. An activated carrier having a tresyl group was obtained. (1) above, 2-copolymer of hydroxyethyl methyl acrylate and methylaminoethyl methacrylate 30 Omg 5
- blood coagulation factor VIII was used.
- a commercial kit (Aceracrom FVIIIR: Ag, manufactured by Boehringer Mannheim Yamanouchi Co., Ltd., Japan)
- the amount of blood coagulation factor VIII antigen in the plasma before and after the above adsorption experiment was measured.
- the amount of factor VIII antigen after the adsorption experiment was 10% before the adsorption experiment.
- the adsorbent after the adsorption experiment was transferred to a plastic column, and washed three times with 2 milliliters of a 10 mM aqueous sodium citrate solution (pH 7.4). Then, an aqueous solution containing 2 OmM sodium phosphate, 1% lysine, 1 M sodium chloride, 20% ethylene glycol, and 1% triton X100 ( Factor VIII was eluted using two PH 6.0) 2 milliliters. When the factor VIII activity contained in the eluate was measured, 69% of the factor VIII in the plasma used in the adsorption experiment was recovered.
- Example 2 (1) 10 milliliters of the water-insoluble carrier obtained in Example 1 was suspended in 12 milliliters of dimethyl sulfoxide, and 8 milliliters of the suspension was added to the suspension. Add a little epichlorohydrin and 1 milliliter of 50% aqueous sodium hydroxide solution and shake at 30 ° C for 5 hours to activate the active group. As a result, an activated carrier having an epoxy group was obtained.
- Molecule having polycation synthesized in Example 1 135 mg was dissolved in 50% aqueous solution of dimethylformamide in 13.5 milliliters of aqueous solution, and 9 milliliters of the activated carrier obtained as described above was added thereto. Adjust the pH to 12 with, shake for 20 hours at 45 ° C, and fix the copolymer of 2-hydroxymethyl methacrylate and getylaminoethyl methacrylate. Thus, a modified adsorbent was obtained. The positive charge density per milliliter of the adsorbent determined by titration with an aqueous sodium hydroxide solution was 110 / eq.
- Sepharose which is an agarose-based carrier, was used as the water-insoluble carrier.
- an activating carrier having a tresyl group as an active group commercially available tresyl-activated Sepharose 4B (Pharmacia, Sweden) 3 milliliters
- the pH was adjusted to 8 with an aqueous sodium hydroxide solution, and the mixture was shaken at room temperature for 24 hours to obtain an adsorbent.
- the positive charge density of the adsorbent per milliliter determined by titration with an aqueous solution of sodium hydroxide was 12 ⁇ eq. I got it.
- Example 1 when an adsorption experiment was performed using plasma from a healthy subject, the factor VII I activity in the plasma after the adsorption experiment was 10% of that before the adsorption experiment.
- Example 1 As a water-insoluble carrier, Toray Pearl (Tosoichi Japan, Ltd.), a hydrophilic bullpolymer carrier, was used.
- an activating carrier having a tresyl group as an active group commercially available AF-tresyl toyopearl 6.50 (manufactured by Tosoh Corporation B, Japan) 3 milliliters was used in Example 1. 30 mg of a copolymer of 2-hydroxyhydroxymethyl methacrylate and getylaminoethyl methacrylate, which was synthesized in step 2, was dissolved in 6 milliliter of 50% aqueous dimethylformamide solution.
- Example 2 Using a crosslinked copolymer having a butyl alcohol unit synthesized in Example 1 as a water-insoluble carrier, in the same manner as in Example 1, An activated carrier having an epoxy group as an active group was obtained using epichlorohydrin.
- poly-L-lysine molecular weight: 20,000, ICN Immunobiological, America
- PH10 aqueous solution of sodium phosphate
- Example 1 when an adsorption experiment was performed using plasma from a healthy individual, the factor VIII activity in the plasma after the adsorption experiment was 28% of that before the adsorption experiment.
- the adsorption rates of factor VIII and factor IX were determined by measuring the respective activities remaining in plasma after the adsorption experiment. The measurement of the factor VIII activity was carried out in the same manner as in Example 1.
- the activity of Factor IX is determined by the Hard i sty—step method [R.M.Had i s t y e a 1.: Thro m b os D a he s.H a e m o h., V o
- the adsorption rates of factor VIII and factor IX were determined by the respective activities remaining in the plasma after the adsorption experiment, as in Example 6. It was determined by measuring.
- the activated carrier 3 was added to a solution prepared by dissolving 150 mg of the copolymer synthesized in Example 1 in 6% of a 75% aqueous dimethyl sulfoxide solution. Milliliter was added, the pH was adjusted to 8 with an aqueous solution of sodium hydroxide, and the mixture was shaken at room temperature for 24 hours to obtain an adsorbent.
- the positive charge density of 1 milliliter of the adsorbent determined by titration with an aqueous sodium hydroxide solution was 43 ⁇ eq.
- Example 1 As in Example 1, an adsorption experiment was carried out using plasma from a healthy subject. As a result, the factor VIII activity in the plasma after the adsorption experiment was 26% of that before the adsorption experiment. Further, factor VIII was eluted using the same eluate as in Example 1, and the activity of factor V factory II contained in the eluate was measured. Factor VIII had been recovered.
- Example 8 In order to examine the multi-molecular structure of the von Willebrand factor in the eluate in Example 1, SDS electrophoresis using a 2% agarose gel was performed. The existence of multimers was recognized up to the same high molecular weight region. Industrial applicability
- the blood coagulation factor VIII adsorbent of the present invention has a molecule having a polycation, it can be compared with a conventional adsorbent using a low-molecular-weight compound as a ligand. Interaction becomes more specific, and plasma can be used as it is without using the conventional method via cryoprecipitate.
- the VI I I factor can be adsorbed at a high rate.
- the adsorbent for blood coagulation factor VIII of the present invention makes a remarkable contribution to the production of a blood coagulation factor VIII preparation.
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Abstract
Description
明細書 Specification
血液凝固第 V I I I 因子の吸着材 技術分野 Adsorbent for blood coagulation factor V II I
本発明は、 血液凝固第 V I I I 因子 (以後、 屡々 、 単に "第 V I I I 因子" と称す) の吸着材に関する。 更に詳しく は、 第 V I I I 因子を含む種々 の血漿蛋白質を含有する溶液 から第 V I I I 因子を効率的に吸着、 回収するのに適した、 ポリ カチオンを有する分子が水不溶性担体に結合 · 固定化さ れた複合体よ リ なる吸着材に関する。 The present invention relates to an adsorbent for blood coagulation factor VIII (hereinafter often simply referred to as "factor VIII"). More specifically, molecules having a polycation suitable for efficiently adsorbing and recovering factor VIII from a solution containing various plasma proteins including factor VIII are bound and immobilized on a water-insoluble carrier. And an adsorbent made of a composite.
背景技術 Background art
血液凝固は、 多種類の因子が複雑に関与する現象でぁ リ 、 これらの因子の質的或いは量的な欠損は出血性疾患と して観 察される。 先天的な出血性疾患の例と して血友病 Aを挙げる こ とができる。 血友病 Aは、 第 V I I I 因子と呼ばれる蛋白 質の欠損によるもので、 血友病 A患者が健常者と変わらない 生活を営むためには、 不足している第 V I I I 因子を補充ず る必要がある。 Blood coagulation is a phenomenon in which various types of factors are involved in a complex manner. The qualitative or quantitative deficiency of these factors is observed as a hemorrhagic disease. Hemophilia A is an example of a congenital bleeding disorder. Hemophilia A is caused by a deficiency of a protein called factor VIII.In order for a person with hemophilia A to live as a healthy person, it is necessary to replace the lacking factor VIII. is there.
第 V I I I 因子を補充するために、 第 V I I I 因子濃縮製 剤と呼ばれる血漿分画製剤が広く 用いられている。 第 V Ϊ I I 因子濃縮製剤は通常、 ク リ オプレシピテー ト と呼ばれる血 漿からの沈澱物を原料と し、 フイブリ ノ ゲンゃフイブロネク チン等の夾雑蛋白質を除去するこ とによ り調製されている In order to supplement factor VIII, a plasma fractionation product called factor VIII concentrate is widely used. Factor V II concentrates are usually prepared by using a precipitate from plasma called cryoprecipitate as a raw material and removing contaminating proteins such as fibrinogen and fibronectin.
[ S . J . S l i c h t e r e t a 1 . : T r a n s f u s i o n , V o l . 1 6 , P P . 6 1 6 - 6 2 6 ( 1 9 7 6 ) ] 。 [S.J.S lichtereta 1.: T ransf usion, Vol. 16, PP. 6 16-62 (1976)]].
ク リ ^プレシピテ一 トは、 新鮮凍結血漿を低温下で融解す ることによ リ生じる沈澱を遠心分離して得ることができる。 しかし、 血漿に含まれる第 V I I I 因子を 1 0 0 %とすると、 ク リオプレシピテー トでの第 V I I I 因子の回収率は 4 0〜 5 0 %と低値である。 さらに、 ク リオプレシピテー ト中には 夾雜蛋白質が多く含まれているため、 それらの夾雑蛋白質を 除去する必要があリ、 一般にジェチルァミ ノェチル基のよ う な低分子リガンドを水不溶性担体に固定化した吸着材 [ C . M i c h a l s k i e t a 1 . : V o x S a n g , V o 1 . 5 5 , p p . 2 0 2 - 2 1 0 ( 1 9 8 8 ) ] が使われ ることが多いが、 この吸着材は、 血液凝固第 I X因子 (以後、 屡々 、 単に "第 I X因子" と称す) が第 V I I I 因子と共存 する場合には、 第 I X因子の方をよ リ多く吸着するため、 第 V I I I 因子濃縮製剤を調製するまでには更に複雑な精製 X 程が必要となリ、 最終的な製剤における第 V I I I 因子の回 収率は約 2 0 %にまで低下するという問題点がある。 The recipe recipe can be obtained by centrifuging the precipitate generated by thawing fresh frozen plasma at a low temperature. However, assuming that the factor V III contained in plasma is 100%, the recovery of factor V III in cryoprecipitate is as low as 40 to 50%. Furthermore, since cryoprecipitate contains a large amount of contaminating proteins, it is necessary to remove those contaminating proteins.In general, adsorption is performed by immobilizing a low-molecular-weight ligand such as a getylaminoethyl group on a water-insoluble carrier. Michalskieta 1.: Vox Sang, Vo 1.55, pp. 202-210 (19988) is often used, but this adsorbent is However, when blood coagulation factor IX (hereinafter often simply referred to as “factor IX”) coexists with factor VIII, the factor VIII-enriched preparation is adsorbed because more factor IX is adsorbed. A more complicated purification process is required before preparation, and the factor VIII recovery in the final preparation is reduced to about 20%.
以上のよう な問題点を解決するため、 血漿から直接、 或い は、 ク リオプレシピテー ト分取後の上清から効率よ く第 V I I I 因子を吸着、 回収するこ とのできる吸着材の開発が望ま れていた。 In order to solve the above problems, it is desirable to develop an adsorbent capable of efficiently adsorbing and recovering factor VIII directly from plasma or from the supernatant after fractionation of cryoprecipitate. Had been.
第 V I I I 因子は分子量約 3 0万の蛋白質でぁリ 、 そのァ ミ ノ酸配列解析から、 酸性アミ ノ酸に富む領域の存在するこ とが知られてレヽる [ G . A . V e h a r e t a 1 . : N a t u r' e , V o l . 3 1 2, p p . 3 3 7 - 3 4 2 ( 1 9 8 4 ) ] 。 さ らに、 血液中では分子量 1 0 0万〜 2, 0 0 0 万のマルチマー構造を有するフォンヴィルブラン ド因子との 複合体と して存在するこ とが知られている ( Z . M . R u g g e r i e t a 1 . : B l o o d , V o l . 5 7, P P . 1 1 4 0 - 1 1 4 3 ( 1 9 8 1 ) ) 。 Factor VIII is a protein with a molecular weight of about 300,000. It is known from the amino acid sequence analysis that there is a region rich in acidic amino acids [G.A.V ehareta 1.: Natur'e, Vol. 3.12, pp. 3 3 7-3 4 2 (1 998 4)]. Furthermore, it is known to exist in blood as a complex with a von Willebrand factor having a multimeric structure with a molecular weight of 1,000,000 to 2,000,000 (Z.M. R uggerieta 1.: Blood, Vol. 57, PP. 114-11 4 3 (1 98 1)).
本発明者らは、 鋭意研究の結果、 このよ う な巨大な分子量 を有する蛋白質を効率良く 吸着するためには、 陰イ オン交換 基を多数個有し且つ十分な長さを有していて、 該複合体と複 数点で相互作用するこ とによ リ強固に吸着する こ とが可能な 物質を有する吸着材が好適であるこ とを知見した。 更にこの よ うな吸着材を開発すべく鋭意検討の結果、 ポリ カチオンを 有する分子が水不溶性担体に結合 , 固定化してなる複合体よ リ なる吸着材が第 V I I I 因子に対して極めて特異的な吸着— 挙動を示し、 第 V I I I 因子を含む種々 の血漿蛋白質を含有 する溶液から第 V I I I 因子を高い選択率と高い収率で吸着、 回収することができ るこ とを知見した。 本発明は、 これらの 知見に基づいて完成したものである。 As a result of intensive studies, the present inventors have found that in order to efficiently adsorb such a protein having a huge molecular weight, it has a large number of anion-exchange groups and a sufficient length. However, they have found that an adsorbent having a substance capable of firmly adsorbing by interacting with the complex at a plurality of points is suitable. Furthermore, as a result of intensive studies to develop such an adsorbent, the adsorbent consisting of a complex in which a molecule having a polycation is bonded to and immobilized on a water-insoluble carrier has an extremely specific adsorption to factor VIII. — It showed that it was able to adsorb and recover Factor VIII with high selectivity and high yield from solutions containing various plasma proteins including Factor VIII. The present invention has been completed based on these findings.
発明の開示 Disclosure of the invention
したがって、 本発明の 1 つの且つ主たる 目的は、 第 V I I I 因子を含む種々 の血漿蛋白質を含有する溶液から第 V I I I 因子を直接、 特異的且つ効率的に吸着することのでき、 し かも吸着された第 V I I I 因子の脱着 · 回収が容易にできる 吸着林 提供することである。 Accordingly, one and primary object of the present invention is to provide a solution containing various plasma proteins, including factor VIII, from a solution containing factor VIII. An adsorbent forest capable of directly and specifically adsorbing factor I, and capable of easily desorbing and recovering adsorbed factor VIII.
本発明の上記及び他の諸目的、 諸特徴、 諸利益は、 次に述 ベる本発明の詳細な説明及び添付の請求範囲の記載から明ら かになろう。 The above and other objects, features, and advantages of the present invention will become apparent from the following detailed description of the present invention and the appended claims.
本発明によれば、 ポリカチオンを有する分子が水不溶性担 体に結合 · 固定化されてなる複合体よ リなリ、 ポリカチオン を有する分子の分子量が少く とも 1 5, 0 0 0であリ、 該複 合体 1 ミ リ リ ッ トルあたリ の正電荷密度が l e q〜 2 0 0 e qであることを特徴とする血液凝固第 V I I I 因子の吸 着材が提供される。 According to the present invention, the molecular weight of a polycation-containing molecule is at least 15,500, unlike a complex formed by binding and immobilizing a molecule having a polycation to a water-insoluble carrier. Further, there is provided an adsorbent for blood coagulation factor VIII, wherein the positive charge density of the complex of 1 milliliter is from leq to 200 eq.
本発明の吸着材に固定化されたボリカチオンを有する分子 は、 1分子の分子量が少く とも 1 5, 0 0 0であリ、 分子中 に陰イオン交換基を多数個持つものをいう。 陰イオン交換基 と しては、 一級ァミノ基、 二級アミノ基、 三級アミノ基、 ΕΓ 級アンモニゥム塩基等をあげることができる。 これらの陰ィ オン交換基の 1種類が単独でポリ カチオンを有する分子の中 に存在してもよく、 また、 2種類以上が存在してもかまわな レゝ The molecule having a polycation immobilized on the adsorbent of the present invention refers to a molecule having a molecular weight of at least 150000 and having a large number of anion exchange groups in the molecule. Examples of the anion exchange group include a primary amino group, a secondary amino group, a tertiary amino group, a primary ammonium base and the like. One of these anion exchange groups may be present alone in the molecule having a polycation, or two or more may be present.
このよ うな分子の例と して、 側鎖に陰イオン交換基を有す る塩基性ビュル単量体の単独重合体、 または、 該塩基性ビニ ル単量体と、 それと共重合し得るビュル単量体との共重合体 を挙げるこ とができる。 また、 該塩基性ビニル単量体のかわ リ に、 重合後に陰イオン交換基をつける こ とのでき る側鎖を 有する ビニル単量体を用いるこ と もでき る。 さ らに、 リ ジン やアルギニン等の塩基性ア ミ ノ酸を含むポリべプチ ドを挙げ る こ とができ る。 Examples of such a molecule include a homopolymer of a basic vinyl monomer having an anion exchange group in a side chain, or a vinyl copolymer which can be copolymerized with the basic vinyl monomer. Copolymer with monomer Can be mentioned. Further, instead of the basic vinyl monomer, a vinyl monomer having a side chain to which an anion exchange group can be added after polymerization may be used. Further, there may be mentioned polypeptides containing basic amino acids such as lysine and arginine.
側鎖に陰イオン交換基を有する塩基性ビニル単量体と して は、 一級ァミ ノ基、 二級ア ミ ノ基、 三級アミ ノ基、 四級ア ン モニゥム塩基を有する ビニル単量体が含まれる。 このよ うな ビエル単量体の例と しては、 それぞれァ ミ ノ基を有するァク リ ル酸誘導体、 メ タアク リ ル酸誘導体、 アク リ ル酸ア ミ ド誘 導体およびメ タアク リル酸アミ ド誘導体、 更には側鎖にピリ ジル基、 イ ミ ダゾリル基等の含窒素芳香環基を有する ビニル 化合物、 およびアミ ノ基で置換されたス チ レ ン誘導体等が用 レヽられる。 具体的な例と して、 ジメ チルア ミ ノ エチルアタ リ レー ト 、 ジェチルア ミ ノ エチルアタ リ レー ト 、 ジメ チルア ミ ノ プロ ピルァク リ レー ト、 3 —ジメ チルァ ミ ノ 一 2 — ヒ ドロ- キシプロ ピルアタ リ レー ト 、 3 —ジェチルア ミ ノ ー 2 — ヒ ド ロキシプロ ピルァク リ レー ト、 N —ジメ チルア ミ ノ エチルァ ク リル酸ア ミ ド、 N —ジェチルア ミ ノエチルァク リ ノレ酸ア ミ ド、 ジメチルア ミ ノエチルメ タァク リ レー ト 、 ジェチルア ミ ノエチルメ タアタ リ レー ト 、 ジェチルァ ミ ノ プロ ピルメ タァ タ リ レー ト 、 3 —ジメ チルア ミ ノ ー 2 — ヒ ドロ キシプロ ピル メ タアタ リ レー ト、 3 —ジェチルァ ミ ノ 一 2 — ヒ ドロ キシプ 口 ピルメ タァク リ レー ト、 N—ジメ チルア ミ ノ エチノレメ タァ ク リル酸アミ ド、 N—ジェチルアミ ノエチルメ タアク リル酸 ァミ ド、'および次式 : Examples of the basic vinyl monomer having an anion exchange group in the side chain include a vinyl monomer having a primary amino group, a secondary amino group, a tertiary amino group, and a quaternary ammonium base. Body included. Examples of such a biel monomer include acrylic acid derivatives, methacrylic acid derivatives, acrylic acid amide derivatives, and metaacrylic acid amines each having an amino group. Examples thereof include vinyl derivatives having a nitrogen-containing aromatic ring group such as a pyridyl group and an imidazolyl group in the side chain, and styrene derivatives substituted with an amino group. Specific examples include dimethylaminoethyl acrylate, dimethylaminoethyl acrylate, dimethylaminopropyl acrylate, 3-dimethylaminopropyl 2—hydroxypropylamine Rate, 3—Jethylamino2—Hydroxypropylacrylate, N—Dimethylaminoethylacrylate, N—Nethylethylaminoethylacrylate, Dimethylaminoethylmethacrylate Rate, getylaminoethyl methacrylate, getylaminopropyl methacrylate, 3—dimethylamine 2—hydroxypropyl propylmethacrylate, 3—getylamine 1—2— histamine Dro kiss Mouth pill methacrylate, N-dimethylamino methacrylate amide, N-ethylaminoethyl methacrylate, and the following formula:
(但し、 Rは一 C H3または一 C 2H5、 Xは (C H2) n は 3の整数である) (However, R is one CH 3 or one C 2 H 5 , X is (CH 2 ) n is an integer of 3)
で示されるスチレン誘導体を挙げることができる Styrene derivatives represented by
また、 例えば、 CHz-CH のよ うな、 重合後にァミ ノ化のできる側鎖を有するビニル単— 量体を用いることもできる。 Also, for example, CHz -CH Such a vinyl monomer having a side chain that can be aminated after polymerization can also be used.
上述の塩基性ビニル単量体と共重合し得るビニル単量体の 例と しては、 N— ビエルピロ リ ドン、 アク リ ル酸エステル、 メ タアタ リ ル酸エステル、 N—アルキルァク リ ル酸ァ ミ ド、 N—アルキルメタァク リル酸アミ ド等を挙げることができる < このよ うなビニル単量体で好ましい具体的な例と しては、 ヒ ドロ キシェチルァク リ レー ト、 ヒ ドロ キシプロ ピノレアク リ レ ー ト、 ヒ ドロキシェチノレメ タァク リ レー ト 、 およびヒ ドロキ シプロ ピルメ タァク リ レー トを挙げるこ とができ る。 Examples of vinyl monomers that can be copolymerized with the basic vinyl monomers described above include N-bierpyrrolidone, acrylates, meta-atalylates, and N-alkyl acrylates. And amides of N-alkyl methacrylate. Specific preferred examples of such a vinyl monomer include hydroxyxethyl acrylate and hydroxypropynoleacrylate. And hydroxypropyl methacrylate, and hydroxypropyl methacrylate.
上に拳げた、 ポリ カチオンを有する分子の例の う ち、 塩基 性ビュル単量体と して、 アミ ノ基を有するアク リル酸誘導体、 メ タアク リル酸誘導体、 アク リル酸アミ ド誘導体またはメ タ アク リル酸アミ ド誘導体を用い、 塩基性ビニル単量体と共重 合し得るビニル単量体と して、 アク リル酸エステル、 メ タァ ク リ ル酸エステル、 N—アルキルアク リ ル酸ア ミ ドまたは N —アルキルメ タァク リル酸アミ ドを用いて得られる共重合体 が好ま しい。 ' Among the above examples of molecules having a polycation, the basic butyl monomer may be an acrylic acid derivative, a metaacrylic acid derivative, an acrylic acid amide derivative or a methacrylic acid derivative having an amino group. Using vinyl acrylamide derivatives, vinyl monomers that can be copolymerized with basic vinyl monomers include acrylic esters, metaacrylic esters, and N-alkylacrylic acids. Copolymers obtained using amides or N-alkyl methacrylates are preferred. '
本発明のポ リ カチオンを有する分子の分子量は、 少く と も 1 5, 0 0 0である。 分子量がこれよ リ小さレ、ときには、 第 V I I I 因子が極めて巨大な蛋白質であるために、 該分子と 第 V I I I 因子との十分な相互作用が期待しにく い。 また、 本発明の吸着材は、 それを構成するポリ カチオンを有する分 子および水不溶性担体よるなる複合体 1 ミ リ リ ッ トルあた リ' の正電荷密度が l e q〜 2 0 0 e qである。 該複合体 1 ミ リ リ ッ トルあたリ の正電荷密度が 1 μ e q未満の場合には、 第 V I I I 因子が十分に吸着されず、 また、 2 0 0 iu e q を 越える場合には、 第 V I I I 因子の吸着が強く な リ溶出が困 難になることや他の蛋白質の吸着も多く なる等の問題が生じ てく る。 なお、 本発明の吸着材を構成する複合体の正電荷密 度は、 以下に示す方法にょ リ求めたものをいう。 水で膨潤さ せた吸着材 1 ミ リ リ ッ トルをプラスチック製カラムに入れ 1 規定塩酸、 水、 1規定水酸化ナト リ ウム水溶液の順で洗った 後、 カ ムからの落下液の p Hが 6 . 5程度になるまで水で 洗う。 その後、 5 0 ミ リ リ ツ トルの試験管に吸着材を移して 0 . 0 1規定塩酸 2 0 ミ リ リ ッ トルを入れて 2 4時間ゆるや かに振と うする。 上清 5 ミ リ リ ッ トルを、 2 0 ミ リ リ ッ トル の三角フラスコに移し、 フエノールフタレイン水溶液を指示 薬と して入れ、 0 . 0 1規定水酸化ナ ト リ ウム水溶液で、 ビ ュレツ トを用いて滴定を行う ことによ リ測定し、 正電荷密度 を求める。 The molecular weight of the molecule having a polycation of the present invention is at least 15,000. When the molecular weight is smaller than this, sometimes factor VIII is an extremely large protein, so that it is difficult to expect a sufficient interaction between the molecule and factor VIII. In addition, in the adsorbent of the present invention, the positive charge density of the complex (1 mil / liter) composed of a molecule having a polycation and a water-insoluble carrier constituting the adsorbent is leq to 200 eq. . If the positive charge density of the complex per milliliter is less than 1 μeq, factor VIII is not sufficiently adsorbed, and if it exceeds 200 μeq, the factor Problems such as difficulty in elution due to strong adsorption of factor VIII and increase in adsorption of other proteins will arise. The positive charge density of the composite constituting the adsorbent of the present invention is determined by the following method. Swollen with water Put 1 milliliter of adsorbed material into a plastic column, wash with 1N hydrochloric acid, water, and 1N aqueous sodium hydroxide in that order, and adjust the pH of the liquid falling from the cam to 6.5. Wash with water until it is about Then, transfer the adsorbent to a test tube of 50 milliliters, add 20 milliliters of 0.01N hydrochloric acid, and shake gently for 24 hours. Transfer 5 milliliters of the supernatant to a 20 milliliter Erlenmeyer flask, add phenolphthalein aqueous solution as an indicator, and use a 0.01N aqueous sodium hydroxide solution to add Determine the positive charge density by performing titration using a pellet.
本発明で用いられる水不溶性担体は、 親水性担体、 疎水性 '担体いずれも使用できるが、 疎水性担体では第 V I I I 因子 以外の蛋白質の該担体への非特異的吸着が生じるため、 親水 性担体の方が好ましい結果を与える。 As the water-insoluble carrier used in the present invention, any of a hydrophilic carrier and a hydrophobic carrier can be used, but the hydrophobic carrier causes non-specific adsorption of proteins other than factor VIII to the carrier. Gives better results.
又、 水不溶性担体はポリカチオンを有する分子を化学結合 によリ 固定化するのに利用できる官能基を有するものであれ一 ば特に限定されない。 化学結合は共有結合によるものが好ま しい。 該官能基を水不溶性担体自体が持たない場合でも、 適 当な化学的修飾によ リボリカチオンを有する分子の固定化に 利用し得る官能基を生じさせることができるものは、 本発明 に使用することができる。 The water-insoluble carrier is not particularly limited as long as it has a functional group that can be used for immobilizing a molecule having a polycation by chemical bonding. The chemical bond is preferably a covalent bond. Even when the water-insoluble carrier itself does not have such a functional group, one that can generate a functional group that can be used for immobilizing a molecule having a rebolication by appropriate chemical modification is used in the present invention. be able to.
水不溶性担体の形状は、 粒子状、 繊維状、 中空糸状、 膜状 等いずれの公知の形状も用い得るが、 吸着材と しての取扱い 等の点から、 粒子状、 繊維状のものが好ま しい。 As the shape of the water-insoluble carrier, any known shape such as a particle shape, a fibrous shape, a hollow fiber shape, and a membrane shape can be used, but handling as an adsorbent In view of the above, particles and fibrous materials are preferred.
このよ うな水不溶性担体の う ち粒子状担体と しては、 ァガ ロース ^、 デキス トラン系、 セルロース系等の天然高分子系 担体、 ポリ アク リ ルアミ ド系、 ポリ ア ミ ド系、 ポリ エステル 系、 ポリ ウレタン系、 ビニル化合物の重合体等の合成高分子 系担体を挙げるこ とができ る。 多孔性構造を有する担体を用 いる と、 担体の表面積が増大するため、 固定化されたポリ 力 チオンを有する分子と、 第 V I I I 因子との接触が容易にな リ 、 吸着される第 V I I I 因子の量が増すという良好な結果 を与える。 特に、 親水性モノマ一単位によ リ親水化されたビ ニル化合物の重合体が、 多孔性構造の担体を作リやすく 、 ま た、 物理的強度の大きい担体が得やすいため、 第 V I I I 因 子の精製工程に組入れる時に、 好ま しい結果を与える。 なか でも、 ビュルアルコール単位を有する架橋共重合体が蛋白質 の担体への非特異的吸着が少なく な り 、 好ま しい結果を与え るこ とが多い。 また、 繊維状担体と しては、 セルロース系、一 ポリエステル系等公知の繊維を用いるこ とができる。 繊維状 担体を用いる場合には、 その繊維径が 0 . 0 2デニールない し 1 0デニールの範囲にあるものが良い。 ' 多孔性構造を有する粒子状担体は、 排除限界分子量が 1 , 0 0 0ないし 1 0 0, 0 0 0, 0 0 0の範囲であり 、 平均粒 子径が 5ないし 1, 0 0 0 μ πιであるものが好ま しい。 Among such water-insoluble carriers, examples of the particulate carrier include agarose ^, dextran-based, cellulose-based and other natural polymer-based carriers, polyacrylamide-based, polyamide-based, and poly- amide-based carriers. Synthetic polymer-based carriers such as ester-based, polyurethane-based, and vinyl compound polymers can be mentioned. When a carrier having a porous structure is used, the surface area of the carrier is increased, so that the molecule having immobilized polythione and the factor VIII can be easily brought into contact with each other. It gives good results with increased volume. In particular, a polymer of a vinyl compound hydrophilized by one unit of a hydrophilic monomer can easily form a carrier having a porous structure, and can easily obtain a carrier having high physical strength. Gives favorable results when incorporated into the purification process of Among them, a crosslinked copolymer having a bul alcohol unit often reduces the non-specific adsorption of a protein to a carrier, and gives a favorable result in many cases. In addition, as the fibrous carrier, known fibers such as a cellulose-based fiber and a polyester-based fiber can be used. When a fibrous carrier is used, the fiber diameter is preferably in the range of 0.02 denier or 10 denier. '' The particulate support having a porous structure has an exclusion limit molecular weight in the range of 1,000 to 100,000,000, and an average particle size of 5 to 1,000 μm. πι is preferred.
ポリ カチオンを有する分子の水不溶性担体への結合 · 固定 化には、 化学結合、 特に共有結合による方法を用いるのがよ レ、。 そのためには、 通常、 固定化酵素やァフィ二テイクロマ トグラ ^ィ一で用いられる公知の水不溶性担体の活性化方法 およびポリカチオンを有する分子の固定化方法を用いること ができる [笠井献一ら : 「ァフィニティーク口マ トグラフィ 一」 日本囯、 (株) 東京化学同人発行 ( 1 9 9 1 ) :] 。 また、 必要に応じて水不溶性担体とボリカチオンを有する分子との 間に任意の長さの分子 (スぺーサ一) を導入して使用するこ ともできる。 Binding and immobilization of polycation-containing molecules to water-insoluble carriers It is better to use a chemical bond, especially a covalent bond, for the conversion. For this purpose, a known method for activating a water-insoluble carrier and a method for immobilizing a molecule having a polycation, which are generally used in immobilized enzymes and affinity chromatography, can be used [Kenichi Kasai et al .: “Affinity mouth mouth one”, published by Tokyo Chemical Industry Co., Ltd. (1991):]. Further, if necessary, a molecule (spacer) having an arbitrary length can be introduced between the water-insoluble carrier and the molecule having a polycation.
水不溶性担体を活性化して生じる活性基は、 ポリカチオン を有する分子のアミ ノ基、 カルボキシル基、 水酸基、 チォー ル基等の活性水素を有する求核反応基と反応し得る基であリ 、 具体的には、 エポキシ基、 トレシル基 ( t r e s y 1 g r The active group generated by activating the water-insoluble carrier is a group capable of reacting with a nucleophilic reactive group having an active hydrogen such as an amino group, a carboxyl group, a hydroxyl group, or a thiol group of a molecule having a polycation. Typically, epoxy group, tresil group (tresy 1 gr
0 u p ) (— O— S 0 2— C H 2— C F 3 ) 、 イ ミダゾリルカ ルバメー ト基、 イ ミ ドカーボネー ト基、 カーボネー ト基、 ホ ルミル基、 ブロモアセチル基、 ハロゲン化ト リ アジン基など を挙げることができる。 0 up) (— O— S 0 2 — CH 2 — CF 3 ), imidazolyl carbamate, imidcarbonate, carbonate, formyl, bromoacetyl, halogenated triazine, etc. Can be mentioned.
本発明の吸着材は、 第 V I I I 因子を含む種々の血漿蛋白 質を含有する溶液と接触させることによ リ、 該溶液中の第 V The adsorbent of the present invention can be obtained by contacting a solution containing various plasma proteins containing Factor VII
1 I I 因子を吸着する。 この時の第 V I I I 因子を含む種々 の血漿蛋白質を含有する溶液としては、 血漿、 あるいは血漿 からの生成物を挙げることができる。 血漿からの生成物と し ては、 前述のク リオプレシピテー ト、 血漿からク リオプレシ ピテー トを分離除去した後の上清、 イオン交換樹脂等による 適当な処理を施して夾雑成分の一部または全部を除去した血 漿などを挙げるこ とができ る。 1 Adsorb factor II. The solution containing various plasma proteins including factor VIII at this time may be plasma or a product from plasma. The products from plasma include the above-mentioned cryoprecipitate, The supernatant after separation and removal of the pithate, plasma from which some or all of the contaminant components have been removed by appropriate treatment with an ion exchange resin or the like can be mentioned.
本発明の吸着材は種々の条件下で、 血漿中の第 V I I I 因 子を吸着するこ とが可能であるが、 通常は、 常温、 常圧での 吸着を行う のが、 第 V I I I 因子の安定性の点から好ま しい。 温度は、 第 V I I I 因子の安定な範囲でおこなわれるが、 通 常、 0〜 5 0 °Cで行う。 吸着時間も特に限定はされないが、 通常は、 1 0分〜 2時間の範囲で行うが、 温度、 吸着の方法 によ リ 、 適当な時間を選択するこ とができ る。 The adsorbent of the present invention is capable of adsorbing factor VIII in plasma under various conditions, but usually adsorbs at normal temperature and normal pressure. It is preferred in terms of sex. The temperature should be within the stable range of Factor V I I I, but is usually between 0 and 50 ° C. Although the adsorption time is not particularly limited, it is usually in the range of 10 minutes to 2 hours, and an appropriate time can be selected depending on the temperature and the method of adsorption.
吸着の方法については、 回分式またはカラム式のどちらで も実施し得るが、 多量の血漿を処理する場合には回分式の方 が短時間で処理でき るため好ましいこ とが多い。 Regarding the method of adsorption, either a batch method or a column method can be used, but when a large amount of plasma is to be treated, the batch method is often preferred because it can be processed in a shorter time.
使用する吸着材の量については、 吸着材/血漿の比の値が 低いほど、 コス トの点から有利であるが、 本発明の吸着材で は、 吸着材/ 血漿の容量比の値が 1 Z 2 0 〜 1 1 0 0 の 囲で用いるこ とができる。 Regarding the amount of adsorbent to be used, the lower the value of the adsorbent / plasma ratio is, the more advantageous from the viewpoint of cost. It can be used in the range of Z20 to 110.
発明を実施するための最良の形態 BEST MODE FOR CARRYING OUT THE INVENTION
以下の実施例において、 本発明をさらに詳細に説明するが、 本発明ほ実施例に何ら限定されるものではない。 The present invention will be described in more detail in the following examples, but the present invention is not limited to the examples.
実施例 1 Example 1
水不溶性担体と して、 ビニルアルコール単位を有する架橋 共重合体を下に示すよ うにして合成した。 酢酸ビニル 1 0 0 g、 ト リ ァリルイ ソシァヌ レー ト 6 4. 3 g、 酢酸ェチル 1 0 0 g、 ヘプタン 1 0 0 g、 ポリ酢酸ビニル (重合度 5 0 0 ) 7. 5 gおよぴ 2 , 2 ' —ァゾビスイ ソブチロニ ト リル 3. 8 gょ リなる均一混合液と、 ポリ ビニルアルコール 1重量0 /0、 V ン酸 2水素ナト リ ウム 2水和物 0. 0 5重量。 /0およびリ ン '酸水素 2ナト リ ウム 1 2水和物 1 . 5重量%を溶解した水 4 0 0 ミ リ リ ッ トルとを混合し、 +分撹拌したのち、 6 5でで 1 8時間、 さ らに 7 5 °Cで 5時間加熱撹拌して、 懸濁重合を 行い、 粒状架橋共重合体を得た。 この架橋共重合体を洗浄後、 水酸化ナ ト リ ウム 4 6 . 5 gを含むメ タノール 2 リ ッ トルど 共に 4 0 °Cで 1 8時間撹拌して、 架橋共重合体のケン化反応 を行い、 ビニルアルコール単位を有する架橋共重合体よ リな る水不溶性担体を得た。 この水不溶性担体の平均粒子径は、 1 0 0 m、 排除限界分子量は、 2 , 0 0 0, 0 0 0であつ た。 As a water-insoluble carrier, a crosslinked copolymer having a vinyl alcohol unit was synthesized as shown below. 100 g of vinyl acetate, 64.3 g of triarylsocyanate, 100 g of ethyl acetate, 100 g of heptane, 7.5 g of polyvinyl acetate (polymerization degree: 500) and 2 g , 2 '- Azobisui Sobuchironi DOO drill 3. 8 g and Yo Li becomes homogeneous mixture of polyvinyl alcohol 1 wt 0/0, V phosphate 2 hydrogen isocyanatomethyl Li um dihydrate 0.0 5 wt. / 0 and phosphoric acid dihydrogen sodium dihydrate 1 dihydrate 1.5 wt% dissolved in water 400 ml, mixed and stirred for + minutes, then 65 with 1 The suspension was heated and stirred at 75 ° C. for 8 hours and further at 75 ° C. for suspension polymerization to obtain a granular crosslinked copolymer. After washing the cross-linked copolymer, two liters of methanol containing 46.5 g of sodium hydroxide were stirred at 40 ° C for 18 hours to perform a saponification reaction of the cross-linked copolymer. Was carried out to obtain a water-insoluble carrier composed of a crosslinked copolymer having a vinyl alcohol unit. The average particle size of this water-insoluble carrier was 100 m, and the exclusion limit molecular weight was 2,000, 000.
次に、 ポリカチオンを有する分子と して、 次に示すよ うな 共重合体を合成した。 X 3 Next, the following copolymer was synthesized as a molecule having a polycation. X 3
2 — ヒ ドロ キシェチルメ タアタ リ レー ト 0 . 8 モルと ジェ チルア ミ ノエチルメ タァク リ レー ト 0 . 2 モルを含むエタ ノ ール溶液 1 リ ッ トルに、 重合開始剤と して 2 , 2 ' 一ァゾビ スイソプチロ ニ ト リ ノレ 0 . 0 0 5 モルを力 Qえて、 6 0 °Cで 8 時間、 ラジカル共重合反応を行った。 このよ う に して得たポ リ カチオンを有する分子の分子量を、 ジメ チルホルムア ミ ド を溶離液と したゲル浸透ク ロマ ト グラフィ ー (カラム : ショ ゥデッ ク ス A D - 8 0 M Z S , 日本国、 昭和電工 (株) 製) によ り 求めたと ころ、 1 8 万 (ポ リ エチレング リ コール換算) であった。 2 — 1 liter of an ethanol solution containing 0.8 mol of hydroxyethyl methyl acrylate and 0.2 mol of acetylaminoethyl methacrylate, 2, 2′-one as a polymerization initiator A radical copolymerization reaction was carried out at 60 ° C. for 8 hours by adding 0.05 mol of azobisisobutyronitrile. The molecular weight of the polycation-containing molecule obtained in this manner was determined by gel permeation chromatography using dimethylformamide as an eluent (column: Shodex AD-80 MZS, Japan, It was 180,000 (polyethylene glycol equivalent) as determined by Showa Denko KK.
上記で得た水不溶性担体と しての架橘共重合体 (アセ ト ン で膨潤したもの) 3 ミ リ リ ッ トルをアセ ト ン 2 . 1 ミ リ リ ツ トル中に懸濁して、 この懸濁液に、 ト レシルク 口 ライ ド 4 5 マイ ク ロ リ ツ トル、 ピリ ジン 1 3 5 マイ ク ロ リ ッ トノレを加え て、 室温で 1 0分間振と う して、 活性基と して ト レシル基を 有する活性化担体を得た。 一 上記の、 2 — ヒ ドロ キシェチルメ タァク リ レー ト と ジェチ ルア ミ ノエチルメ タァク リ レー トの共重合体 3 0 O m g を 5 The water-insoluble carrier obtained in the above step was used as a water-insoluble carrier (swelled with acetate). 3 Milliliters were suspended in acetonitrile 2.1 milliliters. To the suspension, add Tresyl Mouth Ride 45 microliters and pyridine 135 microliters and shake at room temperature for 10 minutes to obtain the active group. An activated carrier having a tresyl group was obtained. (1) above, 2-copolymer of hydroxyethyl methyl acrylate and methylaminoethyl methacrylate 30 Omg 5
0 %ジメ チルホルムア ミ ド水溶液 6 ミ リ リ ッ トルに溶解'した 溶液に、 上記の活性化担体 3 ミ リ リ ツ トルを加え、 水酸化ナ ト リ ウム水溶液で P Hを 8 に調整した後、 室温で 2 4 時間振 と う して、 上記のポ リ カチオンを有する分子が上記水不溶性 担体に結合 · 固定化されてなる複合体である吸着材を得た。 水酸化ナ ト リ ゥム水溶液による滴定から求めた該吸着材 1 ミ リ リ ツ トルあたリの正電荷密度は、 4 0 /^ e qであった。 このよ うにして得られた吸着材 0 . 2 ミ リ リ ッ トルと健常 者血漿 4 ミ リ リ ッ トルをプラスチック製試験管に入れ、 室温 で 1時間緩やかに回転しながら撹拌して吸着実験を行つた。 血液凝固第 V I I I 因子活性測定用の市販キッ ト (テス トチ ーム F V I I I 、 日本国、 第一化学薬品 (株) 製) を用いて、 吸着実験前後の血漿中の血液凝固第 V I I I 因子活性を測定 したところ、 吸着実験後の血漿中の第 V I I I 因子活性は、 吸着実験前の 7。/。であつた。 To the solution dissolved in 0% dimethylformamide aqueous solution in 6 milliliters was added 3 milliliters of the above-mentioned activated carrier, and the pH was adjusted to 8 with an aqueous sodium hydroxide solution. By shaking at room temperature for 24 hours, an adsorbent was obtained, which was a complex in which the above-mentioned polycation-containing molecule was bound and immobilized on the water-insoluble carrier. The positive charge density of the adsorbent, which was determined by titration with a sodium hydroxide aqueous solution, was 40 / ^ eq. 0.2 milliliters of the adsorbent thus obtained and 4 milliliters of plasma from a healthy subject were placed in a plastic test tube and stirred at room temperature with gentle rotation for 1 hour to perform an adsorption experiment. Went. Using a commercially available kit for measuring blood coagulation factor VIII activity (Test Team FVIII, manufactured by Daiichi Kagaku, Japan), measure blood coagulation factor VIII activity before and after the adsorption experiment As a result, the factor VIII activity in the plasma after the adsorption experiment was 7 before the adsorption experiment. /. It was.
この第 V I I I 因子活性測定の結果が、 第 V I I I 因子の '失活によるものではなく 、 本発明の吸着材に第 V I I I 因子 が吸着された結果であることを確認するために、 血液凝固第 V I I I 因子抗原測定用の市販キッ ト (アセラク ロム F V I I I R : A g 日本国、 ベーリ ンガーマンハイ ム山之内 (株) 製) を用いて、 上記の吸着実験前後の血漿中の血液凝固第 V I I I 因子抗原量を測定したところ、 吸着実験後の第 V I I I 因子抗原量は吸着実験前の 1 0 %であった。 In order to confirm that the result of the factor VIII activity measurement was not due to the inactivation of factor VIII but to the result of the factor VIII being adsorbed to the adsorbent of the present invention, blood coagulation factor VIII was used. Using a commercial kit (Aceracrom FVIIIR: Ag, manufactured by Boehringer Mannheim Yamanouchi Co., Ltd., Japan), the amount of blood coagulation factor VIII antigen in the plasma before and after the above adsorption experiment was measured. The amount of factor VIII antigen after the adsorption experiment was 10% before the adsorption experiment.
吸着実験後の第 V I I I 因子活性及び第 V I I I 因子抗原 量の減少が対応することから、 血漿中の第 V I I I 因子は、 本発明の吸着材に吸着されたことが確認された。 なお、 この 活性と抗原量との対応は、 以後の実施例においても同等であ つた。 次に、 第 V I I I 因子を取得するために本発明の吸着材を 用いる時の有用性を確認するために、 上記の吸着実験後の吸 着材からの第 V I I I 因子の溶出実験を行なった。 Since the decrease in the factor VIII activity and the amount of the factor VIII antigen after the adsorption experiment corresponded, it was confirmed that factor VIII in plasma was adsorbed by the adsorbent of the present invention. Incidentally, the correspondence between this activity and the amount of antigen was the same in the following Examples. Next, in order to confirm the usefulness of using the adsorbent of the present invention to obtain factor VIII, an elution experiment of factor VIII from the adsorbent after the above-mentioned adsorption experiment was performed.
吸着実験後の吸着材をプラスチック製カラムに移し、 1 0 mMクェン酸ナ ト リ ウム水溶液 ( P H 7 . 4 ) 2 ミ リ リ ッ ト ルで 3回洗浄した。 その後で、 2 O mMリ ン酸ナ ト リ ウム、 1 %リ ジン、 1 M塩化ナ ト リ ウム、 2 0 %エチ レ ングリ コー ル、 1 % ト リ ト ン X 1 0 0 を含む水溶液 ( P H 6 . 0 ) 2 ミ リ リ ッ トルを 2回用いて、 第 V I I I 因子を溶出させた。 溶 出液中に含まれる第 V I I I 因子活性を測定したと ころ、 吸 着実験に用いた血漿中の 6 9 %の第 V I I I 因子が回収され ていた。 The adsorbent after the adsorption experiment was transferred to a plastic column, and washed three times with 2 milliliters of a 10 mM aqueous sodium citrate solution (pH 7.4). Then, an aqueous solution containing 2 OmM sodium phosphate, 1% lysine, 1 M sodium chloride, 20% ethylene glycol, and 1% triton X100 ( Factor VIII was eluted using two PH 6.0) 2 milliliters. When the factor VIII activity contained in the eluate was measured, 69% of the factor VIII in the plasma used in the adsorption experiment was recovered.
以上のよ う に、 高い回収率で第 V I I I 因子が回収される こ とが確認された。 なお、 以後の実施例においても、 同様に 高い回収率が得られた。 As described above, it was confirmed that Factor VIII was recovered at a high recovery rate. In the following examples, similarly, a high recovery rate was obtained.
実施例 2 一 実施例 1 で得た水不溶性担体 1 0 ミ リ リ ッ トルを 1 2 ミ リ リ ッ トルのジメチルスルフォ キシ ド中に懸濁させ、 こ の懸濁 液に、 8 ミ リ リ ッ トルのェ ピク ロ ロ ヒ ド リ ン と 1 ミ リ リ ク ト ルの 5 0 %水酸化ナ ト リ ゥム水溶液を加え、 3 0 °Cで 5時間 振と う して、 活性基と してエポキシ基を有する活性化担体を 得た。 Example 2 (1) 10 milliliters of the water-insoluble carrier obtained in Example 1 was suspended in 12 milliliters of dimethyl sulfoxide, and 8 milliliters of the suspension was added to the suspension. Add a little epichlorohydrin and 1 milliliter of 50% aqueous sodium hydroxide solution and shake at 30 ° C for 5 hours to activate the active group. As a result, an activated carrier having an epoxy group was obtained.
実施例 1 で合成したポリ カチオンを有する分子 1 3 5 m g を 5 0 %ジメ チルホルムアミ ド水溶液 1 3 . 5 ミ リ リ ッ トノレ に溶解した溶液に、 上記のよ う にして得た活性化担体 9 ミ リ リ ッ トルを加え、 水酸化ナ ト リ ウム水溶液で p Hを 1 2 に調 整した後、 4 5 °Cで 2 0時間振と う して、 2 — ヒ ドロキシェ チルメ タァク リ レー ト とジェチルアミ ノエチルメ タアタ リ レ ー ト との共重合体を固定化した吸着材を得た。 水酸化ナ ト リ ゥム水溶液による滴定から求めた該吸着材 1 ミ リ リ ッ トルあ たリ の正電荷密度は、 1 1 0 / e qであった。 Molecule having polycation synthesized in Example 1 135 mg Was dissolved in 50% aqueous solution of dimethylformamide in 13.5 milliliters of aqueous solution, and 9 milliliters of the activated carrier obtained as described above was added thereto. Adjust the pH to 12 with, shake for 20 hours at 45 ° C, and fix the copolymer of 2-hydroxymethyl methacrylate and getylaminoethyl methacrylate. Thus, a modified adsorbent was obtained. The positive charge density per milliliter of the adsorbent determined by titration with an aqueous sodium hydroxide solution was 110 / eq.
実施例 1 と同様に、 健常者血漿を用いて吸着実験を行った と ころ、 吸着実験後の血漿中の第 V I I I 因子活性は吸着実 験前の 1 6 %であった。 In the same manner as in Example 1, when an adsorption experiment was performed using plasma of a healthy subject, the factor VII I activity in the plasma after the adsorption experiment was 16% of that before the adsorption experiment.
実施例 3 Example 3
水不溶性担体と してァガロース系担体であるセフ ァ ロース (フアルマシア社、 スウェーデン) を用いた。 実施例 1 で合 成した 2—ヒ ドロキシェチルメ タァク リ レー ト とジェチルァ ミ ノェチルメ タァク リ レー ト の共重合体 6 O m g を 5 0 %ジ メチルホルムアミ ド水溶液 6 ミ リ リ ッ トルに溶解した溶液に、 ト レシル基を活性基と して有する活性化担体と して、 市販の ト レシル活性化セフ ァ ロ ース 4 B (フ アルマシア社、 ス ゥ ェ 一デン) 3 ミ リ リ ッ トルを加えて、 水酸化ナ ト リ ウム水溶液 で p Hを 8 に調整した後、 室温で 2 4時間振と う して、 吸着 材を得た。 水酸化ナ ト リ ウム水溶液による滴定から求めた該 吸着材 1 ミ リ リ ッ トルあた リ の正電荷密度は 1 2 μ e qであ つた。 Sepharose (Pharmacia, Sweden), which is an agarose-based carrier, was used as the water-insoluble carrier. A solution prepared by dissolving 6 O mg of a copolymer of 2-hydroxylethylmethacrylate and getylaminoethylmethacrylate synthesized in Example 1 in 50% aqueous solution of 60% dimethylformamide in 6 milliliters In addition, as an activating carrier having a tresyl group as an active group, commercially available tresyl-activated Sepharose 4B (Pharmacia, Sweden) 3 milliliters In addition, the pH was adjusted to 8 with an aqueous sodium hydroxide solution, and the mixture was shaken at room temperature for 24 hours to obtain an adsorbent. The positive charge density of the adsorbent per milliliter determined by titration with an aqueous solution of sodium hydroxide was 12 μeq. I got it.
実施例 1 と同様に、 健常者血漿を用いて吸着実験を行った と ころ、' 吸着実験後の血漿中の第 V I I I 因子活性は吸着実 験前の 1 0 %であった。 As in Example 1, when an adsorption experiment was performed using plasma from a healthy subject, the factor VII I activity in the plasma after the adsorption experiment was 10% of that before the adsorption experiment.
実施例 4 Example 4
水不溶性担体と して親水性ビュルポリ マー系担体である ト ョパール (日本国、 東ソ一. (株) 製) を用いた。 ト レシル基 を活性基と して有する活性化担体と して、 市販の A F— ト レ シル ト ヨパール 6 5 0 ( B本国、 東ソー (株) 製) 3 ミ リ リ ッ トルを、 実施例 1 で合成した 2 —ヒ ドロキシェチルメ タァ タ リ レー ト とジェチルア ミ ノ エチルメ タ ァ ク リ レー ト と の共 重合体 3 0 O m g を 5 0 %ジメチルホルムアミ ド水溶液 6 ミ リ リ ッ トルに溶解した溶液に加えて、 水酸化ナ ト リ ゥム水溶 液で P Hを 8 に調整した後、 室温で 2 0時間振と う して、 吸 着材を得た。 水酸化ナ ト リ ウム水溶液による滴定から求めた 該吸着材 1 ミ リ リ ッ トルあた り の正電荷密度は 2 0 μ e qで あつ 7こ 0 As a water-insoluble carrier, Toray Pearl (Tosoichi Japan, Ltd.), a hydrophilic bullpolymer carrier, was used. As an activating carrier having a tresyl group as an active group, commercially available AF-tresyl toyopearl 6.50 (manufactured by Tosoh Corporation B, Japan) 3 milliliters was used in Example 1. 30 mg of a copolymer of 2-hydroxyhydroxymethyl methacrylate and getylaminoethyl methacrylate, which was synthesized in step 2, was dissolved in 6 milliliter of 50% aqueous dimethylformamide solution. In addition to the solution, the pH was adjusted to 8 with an aqueous solution of sodium hydroxide, followed by shaking at room temperature for 20 hours to obtain an adsorbent. Positive charge density of Ri per adsorber material 1 ml was determined from the titration by hydroxide Na Application Benefits um aqueous solution 2 0 mu mediation 7 this in eq 0
実施例 1 と同様に、 健常者血漿を用いて吸着実験を行った と ころ、 吸着実験後の血漿中の第 V I I I 因子活性は、 吸着 実験前の 2 8 %であった。 In the same manner as in Example 1, when an adsorption experiment was performed using plasma of a healthy individual, the factor VII I activity in the plasma after the adsorption experiment was 28% of that before the adsorption experiment.
実施例 5 Example 5
水不溶性担体と して実施例 1 で合成したビュルアルコール 単位を有する架橋共重合体を用い、 実施例 1 と同様にして、 ェピクロロヒ ドリ ンを用いてエポキシ基を活性基と して有す る活性化担体を得た。 ポリカチオンを有する分子と して、 ポ リー L一リ ジン (分子量 2万、 I C Nィムノバイオロジカル 社、 アメ リカ) を l O O m g Zミ リ リ ッ トルの濃度になるよ うに 0. 2 Mリ ン酸ナト リ ゥム水溶液 ( P H 1 0 ) に溶解し た溶液 6 ミ リ リ ツ トルに、 上記の活性化担体 3 ミ リ リ ッ トル を加え、 4 5 °Cで 2 0時間振と う して、 吸着材を得た。 水酸 化ナト リ ゥム水溶液による滴定から求めた該吸着材 ジ y ッ トルあたリの正電荷密度は 9 2 μ e qであった。 Using a crosslinked copolymer having a butyl alcohol unit synthesized in Example 1 as a water-insoluble carrier, in the same manner as in Example 1, An activated carrier having an epoxy group as an active group was obtained using epichlorohydrin. As a polycation-containing molecule, poly-L-lysine (molecular weight: 20,000, ICN Immunobiological, America) was added to a concentration of 0.2 mg / 100 mg Z-milliliter. To 6 milliliters of a solution of an aqueous solution of sodium phosphate (PH10), add 3 milliliters of the activated carrier described above, and shake at 45 ° C for 20 hours. Thus, an adsorbent was obtained. The positive charge density of the adsorbent, determined by titration with an aqueous sodium hydroxide solution, was 92 μeq.
実施例 1 と同様に、 健常者血漿を用いて吸着実験を行った ところ、 吸着実験後の血漿中の第 V I I I 因子活性は吸着実 験前の 2 8 %であった。 As in Example 1, when an adsorption experiment was performed using plasma from a healthy individual, the factor VIII activity in the plasma after the adsorption experiment was 28% of that before the adsorption experiment.
実施例 6 Example 6
実施例 1で用いた吸着材を用いて健常者血漿 3 ミ リ リ ッ ト ルに対して、 吸着材の量を 0. l gから 0. 6 gまで変えて 第 V I I I 因子と第 I X因子の吸着挙動を調べた。 - 第 V 因子と第 I X因子の吸着率は、 それぞれ下【;: すようになった Using the adsorbent used in Example 1, adsorption of factor VIII and factor IX on 3 milliliters of healthy human plasma by changing the amount of adsorbent from 0.6 lg to 0.6 g The behavior was investigated. -The adsorption rates of Factor V and Factor IX are as follows:
吸着材 0 gの時 3 % 6 % (第 V I 因子 第 I X因子の順。 以下同じ) 3% 6% at 0 g of adsorbent (factor VI, factor IX, and so on)
吸着材 0. 2 gの時 3 2 %、 2 9 % 32%, 29% at 0.2 g of adsorbent
吸着材 0. 3 gの時 6 8 %、 4 5 % 68%, 45% at 0.3 g of adsorbent
吸着材 0. 4 gの時 9 0 %、 5 2 % 吸着材 0 . 5 gの時 9 2 %、 6 0 % 90%, 52% at 0.4 g of adsorbent 0.5% of adsorbent 92%, 60%
吸着材 0 . 6 gの時 9 5。/。、 6 5 % 95 at 0.6 g of adsorbent. /. , 65%
なお、'第 V I I I 因子と第 I X因子の吸着率は吸着実験後 の血漿中に残存するそれぞれの活性を測定する こ とによ リ求 めた。 第 V I I I 因子の活性測定は、 実施例 1 と同様の方法 によ リ行った。 また、 第 I X因子の活性は、 H a r d i s t y—段法 [ R . M. H a d i s t y e a 1 . : T h r o m b o s D a h e s . H a e m o h . , V o In addition, the adsorption rates of factor VIII and factor IX were determined by measuring the respective activities remaining in plasma after the adsorption experiment. The measurement of the factor VIII activity was carried out in the same manner as in Example 1. The activity of Factor IX is determined by the Hard i sty—step method [R.M.Had i s t y e a 1.: Thro m b os D a he s.H a e m o h., V o
1 . 7 , p p . 2 1 5 ( 1 9 6 2 ) ] によ り測定した。 1.7, p.p. 2 15 (1962)].
比較例 1 Comparative Example 1
巿販の D E A E—セファ ローズ (フ ァノレマシア社、 スゥェ 一デン) を用いて実施例 6 と同様にして第 V I I I 因子と第 I X因子の吸着挙動を調べたと ころ、 第 V I I I 因子と第 I X因子の吸着率は、 それぞれ下に記すよ う になった。 The adsorption behavior of factor VIII and factor IX was examined using DEAE-Sepharose (Swedish), a commercial product, in the same manner as in Example 6, and the adsorption of factor VIII and factor IX was performed. The rates are listed below.
吸着材 0 gの時 3 %、 6 3 % (第 V I I I 因子、 第 3%, 63% at 0 g of adsorbent (factor V
I X因子の順。 以下同じ) 一 吸着材 0. 2 gの時 9 %、 8 9 % IX factor order. The same applies to the following.) 1 0.2% of adsorbent 9%, 89%
吸着材 0 . 3 gの時 2 9 %、 9 0 % 29%, 90% at 0.3 g of adsorbent
吸着材 0. 4 gの時 5 9 %、 9 0 % ' 吸着材 0 . 5 gの時 8 2 %、 9 0 % Adsorbent 0.4 g, 59%, 90% 'Adsorbent 0.5 g, 82%, 90%
吸着材 0. 6 gの時 9 5 %、 9 0 % 95%, 90% at 0.6 g of adsorbent
なお、 第 V I I I 因子と第 I X因子の吸着率は、 実施例 6 と同様に、 吸着実験後の血漿中に残存するそれぞれの活性を 測定することによ リ求めた。 The adsorption rates of factor VIII and factor IX were determined by the respective activities remaining in the plasma after the adsorption experiment, as in Example 6. It was determined by measuring.
実施例 7 Example 7
実施 1で合成したビュルアルコール単位を有する架橋共 重合体を、 実施例 2 と同様にしてエポキシ活性化して得られ た活性化担体を用いた。 An activated carrier obtained by epoxy-activating the crosslinked copolymer having a bul alcohol unit synthesized in Example 1 in the same manner as in Example 2 was used.
ポリカチオンを有する分子と して、 実施例 1 で合成した共 重合体 1 5 0 m gを 7 5 %ジメチルスルフォキシ ド水溶液 6 ミ リ リ ツ トルに溶解した溶液に、 上記の活性化担体 3 ミ リ リ ッ トルを加え、 水酸化ナト リ ゥム水溶液で p Hを 8に調整し た後、 室温で 2 4時間振と う して、 吸着材を得た。 水酸化ナ トリ ゥム水溶液による滴定から求めた該吸着材 1 ミ リ リ ッ ト ルあたリの正電荷密度は、 4 3 μ e qであった。 As a molecule having a polycation, the activated carrier 3 was added to a solution prepared by dissolving 150 mg of the copolymer synthesized in Example 1 in 6% of a 75% aqueous dimethyl sulfoxide solution. Milliliter was added, the pH was adjusted to 8 with an aqueous solution of sodium hydroxide, and the mixture was shaken at room temperature for 24 hours to obtain an adsorbent. The positive charge density of 1 milliliter of the adsorbent determined by titration with an aqueous sodium hydroxide solution was 43 μeq.
実施例 1 と同様に、 健常者血漿を用いて吸着実験を行った ところ、 吸着実験後の血漿中の第 V I I I 因子活性は吸着実 験前の 2 6 %であった。 また、 実施例 1 と同様の溶出液を用 いて第 V I I I 因子を溶出させ、 溶出液中に含まれる第 V 厂 I I 因子活性を測定したところ、 吸着実験に用いた血漿中の 7 3 %の第 V I I I 因子が回収されていた。 As in Example 1, an adsorption experiment was carried out using plasma from a healthy subject. As a result, the factor VIII activity in the plasma after the adsorption experiment was 26% of that before the adsorption experiment. Further, factor VIII was eluted using the same eluate as in Example 1, and the activity of factor V factory II contained in the eluate was measured. Factor VIII had been recovered.
実施例 8 ' 実施例 1での溶出液中のフォンヴィルブランド因子のマル チマ一構造を調べるために、 2 %ァガロースゲルを用いた S D S電気泳動を行ったところ、 吸着実験前の血漿中のものと 同程度の高分子領域までマルチマーの存在が認められた。 産業上の利用可能性 Example 8 'In order to examine the multi-molecular structure of the von Willebrand factor in the eluate in Example 1, SDS electrophoresis using a 2% agarose gel was performed. The existence of multimers was recognized up to the same high molecular weight region. Industrial applicability
本発明の血液凝固第 V I I I 因子の吸着材は、 ポリ カチォ ンを有する分子を有しているため、 低分子化合物を リ ガン ド と して用いた従来の吸着材と比べる と、 第 V I I I 因子との 相互作用がよ リ特異的にな り 、 ク リ オプレシピテー トを経由 する従来の方法によるこ となく 、 血漿をそのまま用いても第 Since the blood coagulation factor VIII adsorbent of the present invention has a molecule having a polycation, it can be compared with a conventional adsorbent using a low-molecular-weight compound as a ligand. Interaction becomes more specific, and plasma can be used as it is without using the conventional method via cryoprecipitate.
V I I I 因子を高率に吸着するこ とができる。 このよ う に、 本発明の血液凝固第 V I I I 因子の吸着材は、 血液凝固第 V I I I 因子製剤の製造における寄与が著しく 大きい。 The VI I I factor can be adsorbed at a high rate. As described above, the adsorbent for blood coagulation factor VIII of the present invention makes a remarkable contribution to the production of a blood coagulation factor VIII preparation.
Claims
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3/322353 | 1991-11-12 | ||
| JP32235391 | 1991-11-12 |
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| Publication Number | Publication Date |
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| WO1993009869A1 true WO1993009869A1 (en) | 1993-05-27 |
Family
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/JP1992/001480 Ceased WO1993009869A1 (en) | 1991-11-12 | 1992-11-12 | Adsorbent for blood coagulation factor viii |
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| Country | Link |
|---|---|
| JP (1) | JPH05262664A (en) |
| AU (1) | AU2932992A (en) |
| WO (1) | WO1993009869A1 (en) |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101010334B (en) * | 2004-08-30 | 2013-02-06 | 东丽株式会社 | Fractionation apparatus |
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| JP4509341B2 (en) * | 2000-09-21 | 2010-07-21 | シスメックス株式会社 | Coagulation factor-deficient plasma and method for producing the same |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5627090B2 (en) * | 1976-08-04 | 1981-06-23 | ||
| JPS6241212B2 (en) * | 1977-07-25 | 1987-09-02 | Monsanto Co | |
| JPH01157000A (en) * | 1987-08-14 | 1989-06-20 | Waander Riethorst | Clotting factor isolation method and suitable adsorbent |
| JPH0236199A (en) * | 1988-07-22 | 1990-02-06 | Asahi Medical Co Ltd | Method for purifying blood coagulation factor and adsorbent material for purification |
-
1992
- 1992-11-12 AU AU29329/92A patent/AU2932992A/en not_active Abandoned
- 1992-11-12 WO PCT/JP1992/001480 patent/WO1993009869A1/en not_active Ceased
- 1992-11-12 JP JP4302211A patent/JPH05262664A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5627090B2 (en) * | 1976-08-04 | 1981-06-23 | ||
| JPS6241212B2 (en) * | 1977-07-25 | 1987-09-02 | Monsanto Co | |
| JPH01157000A (en) * | 1987-08-14 | 1989-06-20 | Waander Riethorst | Clotting factor isolation method and suitable adsorbent |
| JPH0236199A (en) * | 1988-07-22 | 1990-02-06 | Asahi Medical Co Ltd | Method for purifying blood coagulation factor and adsorbent material for purification |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101010334B (en) * | 2004-08-30 | 2013-02-06 | 东丽株式会社 | Fractionation apparatus |
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| JPH05262664A (en) | 1993-10-12 |
| AU2932992A (en) | 1993-06-15 |
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