US20020143283A1 - Material for removing beta-2 microglobulin from blood - Google Patents

Material for removing beta-2 microglobulin from blood Download PDF

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US20020143283A1
US20020143283A1 US10/139,822 US13982202A US2002143283A1 US 20020143283 A1 US20020143283 A1 US 20020143283A1 US 13982202 A US13982202 A US 13982202A US 2002143283 A1 US2002143283 A1 US 2002143283A1
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blood
microglobulin
beta
beads
polymer
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Andrew Braverman
Vadim Davankov
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    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61MDEVICES FOR INTRODUCING MEDIA INTO, OR ONTO, THE BODY; DEVICES FOR TRANSDUCING BODY MEDIA OR FOR TAKING MEDIA FROM THE BODY; DEVICES FOR PRODUCING OR ENDING SLEEP OR STUPOR
    • A61M1/00Suction or pumping devices for medical purposes; Devices for carrying-off, for treatment of, or for carrying-over, body-liquids; Drainage systems
    • A61M1/36Other treatment of blood in a by-pass of the natural circulatory system, e.g. temperature adaptation, irradiation ; Extra-corporeal blood circuits
    • A61M1/3679Other treatment of blood in a by-pass of the natural circulatory system, e.g. temperature adaptation, irradiation ; Extra-corporeal blood circuits by absorption
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/22Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising organic material
    • B01J20/26Synthetic macromolecular compounds
    • B01J20/261Synthetic macromolecular compounds obtained by reactions only involving carbon to carbon unsaturated bonds
    • BPERFORMING OPERATIONS; TRANSPORTING
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    • B01J20/22Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising organic material
    • B01J20/26Synthetic macromolecular compounds
    • B01J20/264Synthetic macromolecular compounds derived from different types of monomers, e.g. linear or branched copolymers, block copolymers, graft copolymers
    • BPERFORMING OPERATIONS; TRANSPORTING
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    • BPERFORMING OPERATIONS; TRANSPORTING
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    • B01J20/28Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
    • B01J20/28014Solid 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 form
    • B01J20/2805Sorbents inside a permeable or porous casing, e.g. inside a container, bag or membrane
    • BPERFORMING OPERATIONS; TRANSPORTING
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    • B01J20/28Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
    • B01J20/28054Solid 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 surface properties or porosity
    • B01J20/28078Pore diameter
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    • B01J20/30Processes for preparing, regenerating, or reactivating
    • B01J20/305Addition of material, later completely removed, e.g. as result of heat treatment, leaching or washing, e.g. for forming pores
    • B01J20/3064Addition of pore forming agents, e.g. pore inducing or porogenic agents
    • BPERFORMING OPERATIONS; TRANSPORTING
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    • B01J20/3092Packing of a container, e.g. packing a cartridge or column
    • BPERFORMING OPERATIONS; TRANSPORTING
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    • B01J20/30Processes for preparing, regenerating, or reactivating
    • B01J20/32Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating
    • B01J20/3202Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating characterised by the carrier, support or substrate used for impregnation or coating
    • B01J20/3206Organic carriers, supports or substrates
    • B01J20/3208Polymeric carriers, supports or substrates
    • B01J20/321Polymeric carriers, supports or substrates consisting of a polymer obtained by reactions involving only carbon to carbon unsaturated bonds
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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    • B01J20/30Processes for preparing, regenerating, or reactivating
    • B01J20/32Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating
    • B01J20/3231Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating characterised by the coating or impregnating layer
    • B01J20/3242Layers with a functional group, e.g. an affinity material, a ligand, a reactant or a complexing group
    • B01J20/3244Non-macromolecular compounds
    • B01J20/3246Non-macromolecular compounds having a well defined chemical structure
    • B01J20/3248Non-macromolecular compounds having a well defined chemical structure the functional group or the linking, spacer or anchoring group as a whole comprising at least one type of heteroatom selected from a nitrogen, oxygen or sulfur, these atoms not being part of the carrier as such
    • BPERFORMING OPERATIONS; TRANSPORTING
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    • B01J20/30Processes for preparing, regenerating, or reactivating
    • B01J20/32Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating
    • B01J20/3231Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating characterised by the coating or impregnating layer
    • B01J20/3242Layers with a functional group, e.g. an affinity material, a ligand, a reactant or a complexing group
    • B01J20/3244Non-macromolecular compounds
    • B01J20/3246Non-macromolecular compounds having a well defined chemical structure
    • B01J20/3248Non-macromolecular compounds having a well defined chemical structure the functional group or the linking, spacer or anchoring group as a whole comprising at least one type of heteroatom selected from a nitrogen, oxygen or sulfur, these atoms not being part of the carrier as such
    • B01J20/3251Non-macromolecular compounds having a well defined chemical structure the functional group or the linking, spacer or anchoring group as a whole comprising at least one type of heteroatom selected from a nitrogen, oxygen or sulfur, these atoms not being part of the carrier as such comprising at least two different types of heteroatoms selected from nitrogen, oxygen or sulphur
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/30Processes for preparing, regenerating, or reactivating
    • B01J20/32Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating
    • B01J20/3231Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating characterised by the coating or impregnating layer
    • B01J20/3242Layers with a functional group, e.g. an affinity material, a ligand, a reactant or a complexing group
    • B01J20/3244Non-macromolecular compounds
    • B01J20/3246Non-macromolecular compounds having a well defined chemical structure
    • B01J20/3248Non-macromolecular compounds having a well defined chemical structure the functional group or the linking, spacer or anchoring group as a whole comprising at least one type of heteroatom selected from a nitrogen, oxygen or sulfur, these atoms not being part of the carrier as such
    • B01J20/3255Non-macromolecular compounds having a well defined chemical structure the functional group or the linking, spacer or anchoring group as a whole comprising at least one type of heteroatom selected from a nitrogen, oxygen or sulfur, these atoms not being part of the carrier as such comprising a cyclic structure containing at least one of the heteroatoms nitrogen, oxygen or sulfur, e.g. heterocyclic or heteroaromatic structures
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
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    • B01J20/30Processes for preparing, regenerating, or reactivating
    • B01J20/32Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating
    • B01J20/3231Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating characterised by the coating or impregnating layer
    • B01J20/3242Layers with a functional group, e.g. an affinity material, a ligand, a reactant or a complexing group
    • B01J20/3268Macromolecular compounds
    • B01J20/327Polymers obtained by reactions involving only carbon to carbon unsaturated bonds
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/30Processes for preparing, regenerating, or reactivating
    • B01J20/32Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating
    • B01J20/3231Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating characterised by the coating or impregnating layer
    • B01J20/3242Layers with a functional group, e.g. an affinity material, a ligand, a reactant or a complexing group
    • B01J20/3268Macromolecular compounds
    • B01J20/3272Polymers obtained by reactions otherwise than involving only carbon to carbon unsaturated bonds
    • BPERFORMING OPERATIONS; TRANSPORTING
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    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/30Processes for preparing, regenerating, or reactivating
    • B01J20/32Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating
    • B01J20/3231Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating characterised by the coating or impregnating layer
    • B01J20/3242Layers with a functional group, e.g. an affinity material, a ligand, a reactant or a complexing group
    • B01J20/3268Macromolecular compounds
    • B01J20/3278Polymers being grafted on the carrier
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61MDEVICES FOR INTRODUCING MEDIA INTO, OR ONTO, THE BODY; DEVICES FOR TRANSDUCING BODY MEDIA OR FOR TAKING MEDIA FROM THE BODY; DEVICES FOR PRODUCING OR ENDING SLEEP OR STUPOR
    • A61M1/00Suction or pumping devices for medical purposes; Devices for carrying-off, for treatment of, or for carrying-over, body-liquids; Drainage systems
    • A61M1/14Dialysis systems; Artificial kidneys; Blood oxygenators ; Reciprocating systems for treatment of body fluids, e.g. single needle systems for hemofiltration or pheresis
    • A61M1/16Dialysis systems; Artificial kidneys; Blood oxygenators ; Reciprocating systems for treatment of body fluids, e.g. single needle systems for hemofiltration or pheresis with membranes
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61MDEVICES FOR INTRODUCING MEDIA INTO, OR ONTO, THE BODY; DEVICES FOR TRANSDUCING BODY MEDIA OR FOR TAKING MEDIA FROM THE BODY; DEVICES FOR PRODUCING OR ENDING SLEEP OR STUPOR
    • A61M2202/00Special media to be introduced, removed or treated
    • A61M2202/04Liquids
    • A61M2202/0413Blood
    • A61M2202/0415Plasma
    • A61M2202/0421Beta-2-microglobulin
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2220/00Aspects relating to sorbent materials
    • B01J2220/50Aspects relating to the use of sorbent or filter aid materials
    • B01J2220/58Use in a single column
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2220/00Aspects relating to sorbent materials
    • B01J2220/50Aspects relating to the use of sorbent or filter aid materials
    • B01J2220/62In a cartridge
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10STECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S210/00Liquid purification or separation
    • Y10S210/902Materials removed
    • Y10S210/903Nitrogenous
    • Y10S210/905Protein

Definitions

  • the present invention relates to a material for removing beta-2 microglobulin from blood.
  • Beta-2 microglobulin a protein, is found in very high concentrations in patients with chronic renal failure and on chronic dialysis. Beta-2 microglobulin is removed by the kidneys in the proximal tubes by endocytosis in a healthy individual. The molecule is the co-dimer in the dimeric structure of Class-1 HLA antigens. These antigens are found in high concentration on lymphocytes and are found on all nucleated mammalian cells. In patients will malfunctioning kidney, beta-2 microglobulin accumulates to 40 to 60 multiples of normal. The accumulation of beta-2 microglobulin is basis of the initiation of Dialysis-Associated Amyloidosis. This is a clinical entity that causes arthropathy and neuropathy.
  • a material for removing beta-2 microglobulin from blood by passing the blood through the material which are hydrophilic and biocompatible a size and a structure selected so as to remove beta-2 microglobulin from the blood wherein said material is a porous beaded polydivinylbenzene or polystyrene-co-polydivinylbenzene polymer with a surface of [the] beads and of pores modified so as to prevent adsorption of large proteins and platelets and to minimize activation of blood complement system without affecting noticeably accessibility of an inner absorption space of the beads for beta-2 microglobulin and middle-sized toxicant molecules, in which polymer surface exposed vinyl groups are chemically modified so as to form different surface exposed functional groups which are hydrophilic and biocompatible.
  • a material is proposed for removing beta-2 microglobulin from blood is proposed.
  • a patient's blood is withdrawn from an arterial blood circulatory access point, and passed through an adsorbent material-polymer.
  • the adsorbent material through which the blood passes can be a porous polydivinylbenzene or polystyrene-co-polydivinylbenzene polymer with an enhanced proportion of mesopores.
  • the adsorbent material can be a porous polydivinylbenzene or polystyrene-co-polydivinylbenzene polymer with an enhanced proportion of mesopores and with a surface of the beads and of macropores modified so as to prevent adsorption of large proteins and platelets and to minimize activation of blood complement system without affecting noticeably accessibility of an inner adsorption space of the beads for beta-2 microglobulin and middle-sized toxicant molecules.
  • sorbents prepared in accordance with the invention are charged to a column or cartridge for service.
  • the column should preferably be provided with an inlet and an outlet designed to allow easy connection with the blood circuit, and with two porous filters set between the inlet and the sorbent layer, and between the sorbent layer and the outlet.
  • the column may be made of a biocompatible material, glass, polyethylene, polypropylene, polycarbonate, polystyrene. Of these, polypropylene and polycarbonate are preferred materials, because the column packed with the sorbent can be sterilized (e.g., autoclave and gamma-ray sterilization) before use.
  • the column or cartridge is then filled with a 1% solution of human serum albumin in normal saline and stored at 4° C.
  • a suitable anticoagulant such as ACD-A containing heparin in an effective amount.
  • ACD-A containing heparin in an effective amount.
  • this is approximately 11 of the sodium chloride solution to which 150 ml of ACD-A containing 6,000 units of heparin has been added.
  • the preparation of the adsorbent material can be performed as follows:
  • a solution of 130 g p-ethylstyrene, 132 g divinylbenzene (a mixture of para and metha-isomers of about 1:1) and 2.62 g benzoyl peroxide in a mixture of 600 ml toluene and 100 ml iso-amyl alcohol was suspended in 4 liters of pure water containing 1% cellulose stabilizer. After 39 min stirring at room temperature, the mixture was heated at 40° C. for 1 hours, 60° C. for 2 hours, 80° C. for 5 hours and 96° C. for 2 hours. After cooling the mixture to room temperature, the beads obtained were filtered and washed with hot water, methanol and water. The polymer was dried in oven for 7 hours at 80° C.
  • the reaction is carried out at 80° C. for 8 hours and 90-92° C. for additional 2 hours.
  • the stabilizer is rigorously washed out with hot water (60 to 80° C.) and the above organic solvents are removed by steam distillation.
  • the beads obtained are filtered, washed with 1 l dioxane and with deionized water. Finally, the beads are dried in oven at 60° C. overnight.
  • Example 1 The polymer obtained in Example 1 displayed apparent inner surface area of 1200 sq.m/g and total pore volume of 0.8 ml/g, increased its volume in ethanol by a factor of 1.3, adsorbed Cytochrome C from a phosphate buffer solution in an amount of 32-34 mg per 1 g of the polymer, efficiently removed beta2-microglobuline from blood of patients on permanent dialysis treatment, did pass successfully the hemocompatibility test (recalcification of plasma within the allowed 126-144 sec time limits) without any chemical modification or additional treatment of the surface of polymeric beads.
  • Example 2 As in Example 1, taking 220 ml divinylbenzene, 180 ml ethylvinylbenzene, 150 ml toluene, 150 ml n-octane and 3.0 g benzene peroxide as the organic phase. Inner surface area of the product obtained amounts to 1000 sq.m/g, Volume swelling with ethanol amounts to 1.25.
  • Example 1 As in Example 1, taking organic phase consisting of 320 ml divinylbenzene, 80 ml ethylvynylbenzene, 600 ml toluene, 600 ml n-octane and 2.94 g bis-azoisobuthyric nitrile. Inner surface area of the product obtained amounts to 1150 sq.m/g, Volume swelling with ethanol amounts to 1.5.
  • Example 2 As in Example 1, taking 250 ml benzene and 250 ml methanol, instead of toluene and n-octane, as the porogen for the preparation of organic phase. Inner surface area of the product obtained amounts to 800 sq.m/g. Volume swelling with ethanol amounts to 1.3
  • Example 2 As in Example 1, taking 200 ml ethylene dichloride and 120 ml n-hexane as the porogen. Inner surface area of the product obtained amounts to 1000 sq.m/g. Volume swelling with ethanol amounts to 1.3.
  • Example 2 As in Example 1, taking the mixture of 400 ml cyclohexane and 100 ml methanol as the porogen. Inner surface area of the product obtained amounts to 800 sq.m/g. Volume swelling with ethanol amounts to 1.2.
  • the surface of the beads of the polymer can be modified.
  • the modification of the copolymers can be performed in accordance with the following three principal directions. grafting hydrophilic polymer chains by a radial polymerization of 2-hydroxyethyl methacrylate, N-vinylpyrrolidone, N-vinylcaprolactame, or other water soluble monomers, oxidation of the vinyl groups to epoxy groups with the subsequent reaction of the epoxy groups with water, ethylene glycol, amines or 2-amonoethanol molecules, and depositing high-molecular-weight hemocompatible polymer, in particular poly(trifluorethyoxy) phosphazene onto the surface of the polymeric beads.
  • Example 1 To 1.5 g dry polymer of Example 1 suspended in 5 ml methanol at 40° C. were added 0.04 g layroxyl peroxide in 2 ml methanol and 0.01 ml tetramethyl ethylenediamine in 1 ml methanol. The mixture was heated to 50° C. for 1 hr, supplied with 0.01 ml N-vinylpyrrolidone in 1 ml ethanol and heated further to 60° C. for 3 hours. The polymer was washed with methanol and dried.
  • the medium which is used for modification of the polymers can be purely organic; however, it can be for example aqueous-organic and contain at least 20 vol. % of the organic substance.

Abstract

A material for removing beta-2 microglobulin from blood by passing the blood through the material which are hydrophilic and biocompatible a size and a structure selected so as to remove beta-2 microglobulin from the blood, wherein said material is a porous beaded polydivinylbenzene or polystyrene-co-polydivinylbenzene polymer with a surface of [the] beads and of pores modified so as to prevent adsorption of large proteins and platelets and to minimize activation of blood complement system without affecting noticeably accessibility of an inner absorption space of the beads for beta-2 microglobulin and middle-sized toxicant molecules, in which polymer surface exposed vinyl groups are chemically modified so as to form different surface exposed functional groups which are hydrophilic and biocompatible.

Description

    CROSS-REFERENCE TO A RELATED APPLICATION
  • This application is a division of patent application Ser. No. 09/294,224 which is a continuation of patent application Ser. No. 08/902,727 filed on Jul. 30, 1997.[0001]
  • BACKGROUND OF THE INVENTION
  • The present invention relates to a material for removing beta-2 microglobulin from blood. [0002]
  • Beta-2 microglobulin, a protein, is found in very high concentrations in patients with chronic renal failure and on chronic dialysis. Beta-2 microglobulin is removed by the kidneys in the proximal tubes by endocytosis in a healthy individual. The molecule is the co-dimer in the dimeric structure of Class-1 HLA antigens. These antigens are found in high concentration on lymphocytes and are found on all nucleated mammalian cells. In patients will malfunctioning kidney, beta-2 microglobulin accumulates to 40 to 60 multiples of normal. The accumulation of beta-2 microglobulin is basis of the initiation of Dialysis-Associated Amyloidosis. This is a clinical entity that causes arthropathy and neuropathy. The primary effect is severe joint destruction and pain. Many patients require corrective surgery such as Carpal-Tunnel Laminectomies and Cervical Spine Laminectomy. In addition, they require use of analgesics and anti-inflammatory medications to treat the symptoms of DRA. [0003]
  • Attempts to remove beta-2 microglobulin have been made, as disclosed for example in A New Therapeutic Approach to Dialysis Amyloidosis: Intensive Removal of β[0004] 2-Microglobulin with Adsorbent Column by Fumitake Geijyo, Noriyuki Homma, Shin Hasegawa, and Massaaki Arakawa published in Department of Internal Medicine (II), Niigata University School of Medicine, Niigata, Japan. A method of removing beta-2 microglobulin from blood is also disclosed in our U.S. patent application Ser. No. 08/902,727 filed on Jul. 30, 1997. This method can be further amplified and improved.
  • SUMMARY OF THE INVENTION
  • Accordingly, it is an object of present invention to provide a material for removal of beta-2 microglobulin, which is a further improvement of existing methods. [0005]
  • In keeping with these objects and with others which will become apparent hereinafter, one feature of present invention resides, briefly stated, in a material for removing beta-2 microglobulin from blood by passing the blood through the material which are hydrophilic and biocompatible a size and a structure selected so as to remove beta-2 microglobulin from the blood, wherein said material is a porous beaded polydivinylbenzene or polystyrene-co-polydivinylbenzene polymer with a surface of [the] beads and of pores modified so as to prevent adsorption of large proteins and platelets and to minimize activation of blood complement system without affecting noticeably accessibility of an inner absorption space of the beads for beta-2 microglobulin and middle-sized toxicant molecules, in which polymer surface exposed vinyl groups are chemically modified so as to form different surface exposed functional groups which are hydrophilic and biocompatible. [0006]
  • The novel features which are considered as characteristic for the present invention are set forth in particular in the appended claims. The invention itself, however, both as to its construction and its method of operation, together with additional objects and advantages thereof, will be best understood from the following description of specific embodiments when read in connection with the accompanying drawings. [0007]
  • DESCRIPTION OF PREFERRED EMBODIMENTS
  • In accordance with present invention, a material is proposed for removing beta-2 microglobulin from blood is proposed. A patient's blood is withdrawn from an arterial blood circulatory access point, and passed through an adsorbent material-polymer. [0008]
  • The adsorbent material through which the blood passes can be a porous polydivinylbenzene or polystyrene-co-polydivinylbenzene polymer with an enhanced proportion of mesopores. [0009]
  • Also, the adsorbent material can be a porous polydivinylbenzene or polystyrene-co-polydivinylbenzene polymer with an enhanced proportion of mesopores and with a surface of the beads and of macropores modified so as to prevent adsorption of large proteins and platelets and to minimize activation of blood complement system without affecting noticeably accessibility of an inner adsorption space of the beads for beta-2 microglobulin and middle-sized toxicant molecules. [0010]
  • In accordance with this invention sorbents prepared in accordance with the invention are charged to a column or cartridge for service. The column should preferably be provided with an inlet and an outlet designed to allow easy connection with the blood circuit, and with two porous filters set between the inlet and the sorbent layer, and between the sorbent layer and the outlet. The column may be made of a biocompatible material, glass, polyethylene, polypropylene, polycarbonate, polystyrene. Of these, polypropylene and polycarbonate are preferred materials, because the column packed with the sorbent can be sterilized (e.g., autoclave and gamma-ray sterilization) before use. [0011]
  • The column or cartridge is then filled with a 1% solution of human serum albumin in normal saline and stored at 4° C. When ready for use, the column is washed with 0.9% NaC1 solution to which has been added a suitable anticoagulant. such as ACD-A containing heparin in an effective amount. For a 250 ml cartridge, this is approximately 11 of the sodium chloride solution to which 150 ml of ACD-A containing 6,000 units of heparin has been added. [0012]
  • As usual the following two typical extracorporeal blood circulation systems can be employed: [0013]
  • (I) Blood taken from a blood vessel of a patient is forced to pass through a column packed with the sorbent of this invention, and the clarified blood is returned to the blood vessel of the patient. [0014]
  • (ii) Blood taken from a patient is first separated through a separation membrane, by centrifugation or the like into hemocytes and plasma, the plasma thus separated is then forced to pass through the column packed with the sorbent of this invention to remove toxicants from the plasma; then, the clarified plasma from the column is mixed with the hemocytes separated above, and the mixture is returned to the blood vessels of the patient. [0015]
  • Of these two methods, the latter is more practical because of the smaller loss of hemocytes, for example, by adhesion of platelets and erythrocytes. [0016]
  • Any other ways of performing hemoperfusion or plasma perfusion are appropriate with the modified sorbents of this invention. Especially promising seems to be the above mentioned suggestion of Bodden (U.S. Pat. No. 5,069,662, December 1991), by which high concentrations of anti-cancer agents are perfused through the liver or other body organ containing a tumor and then the effluent blood is subjected to the extracorporeal hemoperfusion to remove the excess of the drug before the blood is returned to the blood circulation system of the patient. Another perspective system is that by Shettigar, et al. (U.S. Pat. No. 5,211,850, 1993), where achieving both convective and diffusive transport of plasma across a hollow fiber membrane towards a closed chamber with a sorbent and back into the fiber channel was suggested. The chamber could be packed with the sorbent of this invention. [0017]
  • The preparation of the adsorbent material can be performed as follows: [0018]
  • EXAMPLE 1
  • A solution of 130 g p-ethylstyrene, 132 g divinylbenzene (a mixture of para and metha-isomers of about 1:1) and 2.62 g benzoyl peroxide in a mixture of 600 ml toluene and 100 ml iso-amyl alcohol was suspended in 4 liters of pure water containing 1% cellulose stabilizer. After 39 min stirring at room temperature, the mixture was heated at 40° C. for 1 hours, 60° C. for 2 hours, 80° C. for 5 hours and 96° C. for 2 hours. After cooling the mixture to room temperature, the beads obtained were filtered and washed with hot water, methanol and water. The polymer was dried in oven for 7 hours at 80° C. [0019]
  • EXAMPLE 2
  • Into a seven-liter four-necked round-bottom flask equipped with a stirrer, a thermometer and a reflux condenser, is placed the solution of 8.4 g polyvinyl alcohol-type technical grade emulsion stabilizer GM-14 in four liters of deionized water (aqueous phase). The solution of 260 ml divinylbenzene, 140 ml ethylvinylbenzene, 250 ml toluene, 250 ml n-octane and 2.94 g benzene peroxide (organic phase) is then added to the aqueous phase on stirring at room temperature. In 20 min, the temperature is raised to 80° C. The reaction is carried out at 80° C. for 8 hours and 90-92° C. for additional 2 hours. After accomplishing the copolymerization, the stabilizer is rigorously washed out with hot water (60 to 80° C.) and the above organic solvents are removed by steam distillation. The beads obtained are filtered, washed with 1 l dioxane and with deionized water. Finally, the beads are dried in oven at 60° C. overnight. [0020]
  • The polymer obtained in Example 1 displayed apparent inner surface area of 1200 sq.m/g and total pore volume of 0.8 ml/g, increased its volume in ethanol by a factor of 1.3, adsorbed Cytochrome C from a phosphate buffer solution in an amount of 32-34 mg per 1 g of the polymer, efficiently removed beta2-microglobuline from blood of patients on permanent dialysis treatment, did pass successfully the hemocompatibility test (recalcification of plasma within the allowed 126-144 sec time limits) without any chemical modification or additional treatment of the surface of polymeric beads. Individual spherical beads of the polymer of 0.4-0.63 mm in diameter were mechanically destroyed at a loading of 450+50 g, which is much better as compared to typical macroporous beads (about 120-150 g), but not as good as typical hypercrosslinked beads (up to 600 g) of a comparable diameter and total porous volume. [0021]
  • EXAMPLE 3
  • As in Example 1, taking 220 ml divinylbenzene, 180 ml ethylvinylbenzene, 150 ml toluene, 150 ml n-octane and 3.0 g benzene peroxide as the organic phase. Inner surface area of the product obtained amounts to 1000 sq.m/g, Volume swelling with ethanol amounts to 1.25. [0022]
  • EXAMPLE 4
  • As in Example 1, taking organic phase consisting of 320 ml divinylbenzene, 80 ml ethylvynylbenzene, 600 ml toluene, 600 ml n-octane and 2.94 g bis-azoisobuthyric nitrile. Inner surface area of the product obtained amounts to 1150 sq.m/g, Volume swelling with ethanol amounts to 1.5. [0023]
  • EXAMPLE 5
  • As in Example 1, taking 250 ml benzene and 250 ml methanol, instead of toluene and n-octane, as the porogen for the preparation of organic phase. Inner surface area of the product obtained amounts to 800 sq.m/g. Volume swelling with ethanol amounts to 1.3 [0024]
  • Example 6
  • As in Example 1, taking 200 ml ethylene dichloride and 120 ml n-hexane as the porogen. Inner surface area of the product obtained amounts to 1000 sq.m/g. Volume swelling with ethanol amounts to 1.3. [0025]
  • EXAMPLE 7
  • As in Example 1, taking the mixture of 400 ml cyclohexane and 100 ml methanol as the porogen. Inner surface area of the product obtained amounts to 800 sq.m/g. Volume swelling with ethanol amounts to 1.2. [0026]
  • In accordance with the present invention, as explained herein above, the surface of the beads of the polymer can be modified. [0027]
  • The modification of the copolymers can be performed in accordance with the following three principal directions. grafting hydrophilic polymer chains by a radial polymerization of 2-hydroxyethyl methacrylate, N-vinylpyrrolidone, N-vinylcaprolactame, or other water soluble monomers, oxidation of the vinyl groups to epoxy groups with the subsequent reaction of the epoxy groups with water, ethylene glycol, amines or 2-amonoethanol molecules, and depositing high-molecular-weight hemocompatible polymer, in particular poly(trifluorethyoxy) phosphazene onto the surface of the polymeric beads. [0028]
  • This was disclosed in detail in our patent application Ser. No. 09/019,583 which is incorporated here by reference. [0029]
  • Several examples of the modification procedure are presented herein below. [0030]
  • EXAMPLE 1
  • (Aqueous-Organic Medium) [0031]
  • 5.4 g of the water-washed polymer (dry weight 2.1 g), prepared by polymerization of technical grade 50%-divinylbenzene described in Example 1, were suspended in a mixture of 3 ml ethanol and 2 ml water and supplied with a solution of 0.05 g of ammonium persulfate in 2 ml water, a solution of 0.035 ml tetramethyl ethylenedlamine in 1 ml ethanol and finally with a solution of 0.03 ml N-vinylpyrrolidone in 1 ml ethanol. The mixture was stirred at 37° C. for 4 hours. Using spectrophotometry at 234 nm, 99% of the initial amount of vinylpyrrolidone were found to graft to the polymer in the above aqueous/ethanolic mixture of the appropriate composition of 7:5 (vol/vol). The final polymer was washed with ethanol and dried to constant weight. The dry polymer can be easily wetted with water, what indicates the presence of hydrophilic grafted polymer layer on the surface of the basically hydrophobic material. [0032]
  • EXAMPLE 2
  • (Organic Medium) [0033]
  • 68 g of dry polymer obtained by polymerization of technical-grade 50%-divinylbenzene according to the protocol described in the above Example 1, were suspended in 350 ml ethanol, supplied with a solution of 1.4 g azo-bis-isobutyro nitrile in 60 ml ethanol, and heated to 60° C. At that temperature the mixture was provided with a solution of 1.0 ml N-vinylpyrrolidone in 10 ml ethanol. After shaking the mixture at 60° C. for 3.5 hours, conversion of vinylpyrrolidone was found to reach 99%. The final polymer thus contained 1.5% polyvinylpyrrolidone. [0034]
  • Example 3
  • (Organic Medium) [0035]
  • To 1.5 g dry polymer of Example 1 suspended in 5 ml methanol at 40° C. were added 0.04 g layroxyl peroxide in 2 ml methanol and 0.01 ml tetramethyl ethylenediamine in 1 ml methanol. The mixture was heated to 50° C. for 1 hr, supplied with 0.01 ml N-vinylpyrrolidone in 1 ml ethanol and heated further to 60° C. for 3 hours. The polymer was washed with methanol and dried. [0036]
  • EXAMPLE 4
  • (Organic Medium) [0037]
  • To 2 g dry polymer of Example 1 suspended in 10 ml dioxane a solution of 0.08 g lauroyl peroxide in 4 ml ethanol was added. The temperature of the mixture was increased to 60° C. within 10 min, before additional 2 ml dioxane which contained 0.02 ml N-vinylpyrrolidone were added. The reaction mixture was stirred for 3 hr at 60° C. and the polymer was filtered and washed with ethanol. [0038]
  • EXAMPLE 5
  • (Organic Medium) [0039]
  • 2 g of dry polymer described in Example 1 and suspended in 10 ml ethanol were added at 40° C. with 0.08 g lauroyl peroxide in 4 ml ethanol. In 5 minutes 0.02 ml of tetramethyl ethylenediamine in 2 ml ethanol, and, after another 5 minutes, 0.02 ml N-vinylpyrrolidone in 2 ml ethanol were added. [0040]
  • After shaking the mixture for 2.5 hours at 40° C., 80% of the initial vinylpyrrodone were found to be grafted to the polymer surface. [0041]
  • The medium which is used for modification of the polymers can be purely organic; however, it can be for example aqueous-organic and contain at least 20 vol. % of the organic substance. [0042]
  • It has been found that when modification procedure is performed in non-organic, for example purely aqueous medium, the polymer is contaminated with endotoxin, and animals whose blood was purified through the thusly produced material developed fever, which can be considered as indirect indication of the presence of endotoxican in the polymer. In contrast, numerous experiment conducted for purification of physiological liquids of organism with the use of materials modified with the utilization of the medium in accordance with the present invention showed that the polymers were not contaminated with endotoxicans. [0043]
  • Depositing Phosphazene: [0044]
  • EXAMPLE 6
  • A solution of 0.0009 g poly(trifluoroethoxy) phosphazene (molecular weight 107) in 8 ml ethyl acetate were added quickly to 3 g of dry POROUS polymer and agitated until the whole of the solvent was totally absorbed by the polymer beads. The material was then dried under reduced pressure and washed with ethanol. [0045]

Claims (7)

1. A material for removing beta-2 microglobulin from blood by passing the blood through the material which are hydrophilic and biocompatible a size and a structure selected so as to remove beta-2 microglobulin from the blood, wherein said material is a porous beaded polydivinylbenzene or polystyrene-co-polydivinylbenzene polymer with a surface of beads and of pores modified so as to prevent adsorption of large proteins and platelets and to minimize activation of blood complement system without affecting noticeably accessibility of an inner absorption space of the beads for beta-2 microglobulin and middle-sized toxicant molecules, in which polymer surface exposed vinyl groups are chemically modified so as to form different surface exposed functional groups which are hydrophilic and biocompatible.
2. A material for removing beta-2 microglobulin from blood as defined in claim 1, wherein the beads contain more than 50% of divinylenzene.
3. A material for removing beta-2 microglobulin from blood as defined in claim 1, wherein the beads contain more than 60% of divinylenzene.
4. A material for removing beta-2 microglobulin from blood as defined in claim 1, wherein the beads contain more than 75% of divinylenzene.
5. A material for removing beta-2 microglobulin from blood as defined in claim 1, wherein the beads contain 55% of divinylenzene.
6. A material for removing beta-2 microglobulin from blood as defined in claim 1, wherein the beads contain 65% of divinylenzene.
7. A material for removing beta-2 microglobulin from blood as defined in claim 1, wherein the beads contain 80% of divinylenzene.
US10/139,822 1997-07-30 2002-05-07 Material for removing beta-2 microglobulin from blood Abandoned US20020143283A1 (en)

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CA2334680A1 (en) 2000-10-26
US6416487B1 (en) 2002-07-09
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JP2002541928A (en) 2002-12-10
CN1344172A (en) 2002-04-10

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