WO2002041989A1 - Metal-chelating adsorbents and their use - Google Patents

Metal-chelating adsorbents and their use Download PDF

Info

Publication number
WO2002041989A1
WO2002041989A1 PCT/GB2001/005231 GB0105231W WO0241989A1 WO 2002041989 A1 WO2002041989 A1 WO 2002041989A1 GB 0105231 W GB0105231 W GB 0105231W WO 0241989 A1 WO0241989 A1 WO 0241989A1
Authority
WO
WIPO (PCT)
Prior art keywords
conjugate according
conjugate
ligand
formula
support matrix
Prior art date
Application number
PCT/GB2001/005231
Other languages
French (fr)
Inventor
Mark Burton
Original Assignee
Prometic Biosciences Ltd.
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Prometic Biosciences Ltd. filed Critical Prometic Biosciences Ltd.
Priority to AU2002220830A priority Critical patent/AU2002220830A1/en
Publication of WO2002041989A1 publication Critical patent/WO2002041989A1/en
Priority to AU2002343100A priority patent/AU2002343100A1/en
Priority to PCT/GB2002/005326 priority patent/WO2003045546A1/en

Links

Classifications

    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K51/00Preparations containing radioactive substances for use in therapy or testing in vivo
    • A61K51/02Preparations containing radioactive substances for use in therapy or testing in vivo characterised by the carrier, i.e. characterised by the agent or material covalently linked or complexing the radioactive nucleus
    • A61K51/04Organic compounds
    • A61K51/06Macromolecular compounds, carriers being organic macromolecular compounds, i.e. organic oligomeric, polymeric, dendrimeric molecules
    • A61K51/065Macromolecular compounds, carriers being organic macromolecular compounds, i.e. organic oligomeric, polymeric, dendrimeric molecules conjugates with carriers being macromolecules
    • 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
    • B01J20/223Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising organic material containing metals, e.g. organo-metallic compounds, coordination complexes
    • 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
    • B01J20/281Sorbents specially adapted for preparative, analytical or investigative chromatography
    • B01J20/286Phases chemically bonded to a substrate, e.g. to silica or to polymers
    • 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
    • B01J20/3092Packing of a container, e.g. packing a cartridge or 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
    • 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
    • B01J20/3202Impregnating 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
    • B01J20/3212Polymeric carriers, supports or substrates consisting of a polymer obtained by reactions otherwise than 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
    • B01J20/3214Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating characterised by the method for obtaining this coating or impregnating
    • B01J20/3217Resulting in a chemical bond between the coating or impregnating layer and the carrier, support or substrate, e.g. a covalent bond
    • 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
    • B01J20/3214Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating characterised by the method for obtaining this coating or impregnating
    • B01J20/3217Resulting in a chemical bond between the coating or impregnating layer and the carrier, support or substrate, e.g. a covalent bond
    • B01J20/3219Resulting in a chemical bond between the coating or impregnating layer and the carrier, support or substrate, e.g. a covalent bond involving a particular spacer or linking group, e.g. for attaching an active group
    • 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
    • B01J20/3251Non-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
    • 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
    • B01J20/3265Non-macromolecular compounds with an organic functional group containing a metal, e.g. a metal affinity ligand
    • 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
    • B01J20/34Regenerating or reactivating
    • B01J20/3425Regenerating or reactivating of sorbents or filter aids comprising organic materials
    • 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
    • B01J20/34Regenerating or reactivating
    • B01J20/345Regenerating or reactivating using a particular desorbing compound or mixture
    • B01J20/3475Regenerating or reactivating using a particular desorbing compound or mixture in the liquid phase
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J45/00Ion-exchange in which a complex or a chelate is formed; Use of material as complex or chelate forming ion-exchangers; Treatment of material for improving the complex or chelate forming ion-exchange properties
    • GPHYSICS
    • G21NUCLEAR PHYSICS; NUCLEAR ENGINEERING
    • G21FPROTECTION AGAINST X-RADIATION, GAMMA RADIATION, CORPUSCULAR RADIATION OR PARTICLE BOMBARDMENT; TREATING RADIOACTIVELY CONTAMINATED MATERIAL; DECONTAMINATION ARRANGEMENTS THEREFOR
    • G21F9/00Treating radioactively contaminated material; Decontamination arrangements therefor
    • G21F9/04Treating liquids
    • G21F9/06Processing
    • G21F9/12Processing by absorption; by adsorption; by ion-exchange
    • 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
    • B01J2220/54Sorbents specially adapted for analytical or investigative chromatography
    • 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

Definitions

  • This invention relates to the preparation and use of novel affinity ligands for the removal of contaminant metal ions from diagnostic and therapeutic formulations.
  • Radioimmunotherapy relies on the targeted delivery of conjugates of monoclonal antibodies with radioactive metal ions to specific tumour sites, the specificity being a function of the antibody chosen.
  • the active agent is prepared by incubating a metal chelate-antibody conjugate with an excess of the radioisotopic metal ion for 0.5 - 1.0 hr. This is often followed by a series of time-consuming purification procedures to remove unbound or non-specifically bound metal ions.
  • Typical purification protocols include dialysis and combinations of ion-exchange chromatography and gel filtration chromatography. Lengthy purification procedures lead to significant decreases in effective doses of radiation, particularly for conjugates comprising nuclides with short half-lives. Additionally, multi-step purification procedures lead to undesirable dilution effects.
  • metal chelates Representative examples of metal chelates, methods of preparation of metal chelate-protein conjugates, and the use of such conjugates in diagnostic and therapeutic applications, have been disclosed in several publications. See, for example, rejcarek et al., Biochem. Biophys. Res. Commun., 1977, p.581, vol. 77; Brechbiel et al., Inorg. Chem., 1986, p.5783, vol. 25; Meares et al, Jou. Prot. Chem., 1984, p.215, vol. 3; Hnatowichet ⁇ /., Science, 1983a, p.613, vol.220;Khawet ⁇ /., Science., 1980, p.295, vol.
  • a commonly used reagent for the covalent modification of proteins is the cyclic dianhydride of diethylenetriaminepentaacetic acid (DPTA), whereby an amide bond is formed between the protein and the chelator:
  • DPTA diethylenetriaminepentaacetic acid
  • the use of bifbnctional chelating reagents such as the dianhydride of DPTA results in cross-linking of the protein.
  • the amide linkage between the protein and chelator is both acid- and base-labile.
  • the ligand comprises coordination groups selected from COOH, PO 3 H and SO 3 H
  • the ligand backbone is linked, optionally by means of a spacer, to a support matrix
  • the ligand backbone/spacer is free of ester and amide bonds.
  • Such a conjugate can be used for the capture of metal ions from water, aqueous solutions, blood, plasma, and pharmaceutical and therapeutic products and proteins.
  • Metal-chelating ligand-matrix conjugates embodying the present invention can be represented by formula (1)
  • A represents a C,. 6 saturated hydrocarbon chain; each X is COOH, PO 3 H or SO 3 H; n is 2 or more;
  • M is an optional spacer arm; and Z is a support matrix.
  • A maybe linear or branched alkylene such as divalent methyl, ethyl, n-propyl, isopropyl, n-butyl, sec-butyl, isobutyl ortert-butyl.
  • X is preferably COOH.
  • n is preferably 2, so that the conjugate has 4 coordination groups, and usually no more than 3, 4 or 5.
  • the support matrix may be any compound or material, particulate or non- particulate, soluble or insoluble, porous or non-porous, which may be used for the immobilization of metal-chelating ligands, to form a metal-chelating ligand-matrix conjugate, thereby providing a convenient means of binding metal ions from solution.
  • particulate support matrices include natural polymers such as agarose, dextran, cellulose or starch, synthetic polymers and co-polymers such as perfluorocarbons, polystyrene, polyacrylamide, polyvinyl alcohol and polymethyl methacrylate, and inorganic compounds such as silica, glass, alumina and metal oxides.
  • soluble carriers include polymers of dextran, polyvinyl alcohol, polyethylene glycol and hydrolysed starch.
  • the support matrix may be in the form of packed columns or cartridges, or of membranes or sheets comprising such polymers.
  • Covalent attachment of ligand structures as represented by formula (1) to the support matrix Z may be achieved by use of a variety of activation agents including, but not limited to, cyanogen bromide, epichlorohydrin, 1,4-butanediol diglycidyl ether, tosyl chloride, tresyl chloride, and cyanuric chloride.
  • the spacer group M may be absent, although it will be understood by those skilled in the art that the non-functional part of any functional groups used to conjugate Z and the coordination groups may be present in the product. If present, M may be any group which is conveniently capable of holding the ligand at a distance from the support matrix.
  • spacer groups include diaminoalkanes and polyvinyl alcohol (PNA).
  • a preferred spacer M comprises a group of the formula -T- L- wherein T is O, S or ⁇ R, R is H or C, ⁇ alkyl, and L is an optionally substituted C 2 . 20 alkylene chain optionally including one or more ether or thioether linkages.
  • a further aspect of this invention is a facile method for the preparation of conjugates represented by formula (1) with a stable C- ⁇ bond formed between the ligand and the support matrix Z. A variety of methods is available, which avoid introducing an ester or amide bond.
  • the method comprises the reaction of a polyamine of the formul H-[ ⁇ H-A] n - ⁇ H 2 , with an activated support matrix Z-Y, wherein Y is a reactive group, optionally in the presence of or after reaction of either component with a compound introducing M; and reaction of the product with a compound of the formula Q-CH 2 -X, wherein Q is a group reactive with NH.
  • a diamine such as diethylenetriamine is coupled to an activated support matrix followed by reaction with a halogenoacetic acid such as bromoacetic acid or chloroacetic acid to give a conjugate embodying the invention, by the method shown in the following scheme
  • a desirable key feature of metal-chelating ligand-matrix conjugates prepared according to this invention is the ultrastable C-N linkage between the support matrix and the metal-chelating ligand, thereby enabling the use of such conjugates for sequestering metal ions at extremes of pH, ionic strength and temperature, without the risk of potentially toxic metal ion leachates.
  • Another aspect of this invention is a one-step chromatographic method for the removal of contaminant metal ions from diagnostic and therapeutic products.
  • unbound and/or loosely bound metal ions are scavenged from a pharmaceutical product by passing the preparation through a terminally sterilized column containing a conjugate represented by formula (1), e.g. using an inert support matrix such as polytetrafluoroethylene (PTFE).
  • PTFE polytetrafluoroethylene
  • This invention may be applied to the removal of any suitable metal ion including radioactive and non-radioactive metal ions.
  • PTFE as a chromatographic support in this invention has specific advantages over other commercially available support matrices, including chemical and biological inertness, compatibility with gamma-irradiation and minimal swelling upon wetting which minimizes any sample dilution effects during use.
  • Another aspect of the present invention is the provision of an expeditious procedure for the removal of contaminant metal ions from pharmaceutical and other therapeutic formulations and comprises a terminally sterilized single-use disposable cartridge or element containing a metal-chelating adsorbent of formula (1).
  • the conjugate is used as the adsorbent for a radiactive component in a liquid sample.
  • Such a method comprises using a syringe mounted at the outlet of a chamber to draw the sample through the chamber, wherein the chamber is housed within a radiation-absorbing shroud and contains an adsorbent for the component, and wherein the chamber also has an inlet and means for mounting a syringe thereon.
  • FIG. 1 Apparatus suitable for use in this embodiment is illustrated schematically in the accompanying drawing.
  • the drawing shows a chamber 1 having a syringe needle 2 mounted at its inlet, connected via a Luer fitting 3, and a seal 4.
  • the combination is adapted to receive liquid sample 5 in a container 6.
  • the chamber also has a syringe 7 mounted at its outlet and connected via a Luer fitting 8.
  • the chamber includes an adsorbent 9.
  • the combination of these components is surrounded by a radiation-absorbing shroud 10. In use, raising the syringe piston 11 draws liquid through the adsorbent 9. The sryinge 7, containing less contaminated liquid, can then be removed.
  • novel conjugate may also be reused, if necessary or desired; its robustness means that NaOH can be used for sterilisation.
  • DETATA is diethylenetriaminetetraacetic acid.
  • Example 1 DETATA-agarose
  • Epoxy-activated Sepharose CL-6B (94g settled weight) from stage 1 was mixed with 0.2M sodium bicarbonate solution (225ml) and diethylenetriamine (150ml) and the ⁇ reaction mixture stirred for 23 hours at 50 °C. The resulting amino gel was washed with RO water (10 x 100ml portions), 0. IM acetic acid (10 x 100ml portions) and finally with RO water (10 x 100ml portions). This gel was used in stage 3 of the reaction. Stage 3 - Preparation of DETATA-Agarose
  • the diethylenetriamine-agarose (stage 2) was mixed with bromoacetic acid (16g), 2M sodium hydroxide (50ml) and IM sodium bicarbonate (50ml). The resulting reaction mixture was adjusted to pH 7.0 with sodium hydroxide and left to react at room temperature for 16 hours. The gel was then washed with RO water (10 x 100ml portions) to remove excess reactants. , Yttrium-binding capacity DETATA-agarose (5g) was washed sequentially with RO water (10 x 5ml portions), IM sodium hydroxide (10 x 5ml portions) and RO water (10 x 5ml portions). The gel was then mixed with 5 ml RO water and the slurry gravity packed into a 10ml column.
  • the settled gel from stage 2 was suspended in IM sodium hydrogen carbonate (25ml) and 2M sodium hydroxide solution (25ml). Bromoacetic acid (8g) was added and the pH of the suspension adjusted to pH 7.0 by the drop-wise addition of 2M sodium hydroxide. The reaction mixture was stirred for 16 hours at room temperature. The final chelate adsorbent was washed with an excess of RO water at the end of the reaction. Copper-binding capacity
  • DETATA-PTFE adsorbent (1.2g dry weight) was dry packed to a bed height of 20mm into a cartridge (40mm height x 8mm i.d.) containing a leur fitting at the inlet port and a 0.45mm filter connected to a leur fitting at the outlet port.
  • the packed cartridge was housed within a radiation shield to minimize exposure to radiation during use.
  • a preparation of antibody immunoconjugate labelled with 90 yttrium was prepared by incubating 90 yttrium chloride (37Mbq, 200 ⁇ l in 0. IM acetate buffer pH 5.5) with antibody immunoconjugate (5 ⁇ l, 30 ⁇ g) for 30 minutes.
  • the radiolabelled reaction mixture was passed through the cartridge and immunoconjugate eluted with sodium acetate (3 x lml, 0. IM pH 5.5).
  • the radiochemical purity of the conjugate prior to purification was 96% and increased to 98% after purification using the cartridge.
  • An aqueous slurry of DETATA-PTFE was packed into a glass chromatography column (10mm i.d.) to a bed height of 49mm (3.85ml column volume) and washed sequentially with sodium hydroxide (IM, 10ml) and RO water (10ml) at a flow rate of lml/min. Copper was loaded onto the adsorbent by passing an aqueous solution of copper sulphate (10ml, 16mg/ml) through the column. The column was then washed with RO water (10ml) to remove excess copper sulphate and equilibrated with loading buffer (0. IM sodium acetate, 0.5M sodium chloride pH 7.7, 10ml).
  • albumin binding capacity 22.1 ⁇ g/ml of adsorbent.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Analytical Chemistry (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Health & Medical Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Physics & Mathematics (AREA)
  • Proteomics, Peptides & Aminoacids (AREA)
  • Pharmacology & Pharmacy (AREA)
  • General Engineering & Computer Science (AREA)
  • Engineering & Computer Science (AREA)
  • Inorganic Chemistry (AREA)
  • Medicinal Chemistry (AREA)
  • Optics & Photonics (AREA)
  • High Energy & Nuclear Physics (AREA)
  • Epidemiology (AREA)
  • Animal Behavior & Ethology (AREA)
  • General Health & Medical Sciences (AREA)
  • Public Health (AREA)
  • Veterinary Medicine (AREA)
  • External Artificial Organs (AREA)

Abstract

A metal-chelating ligand-support conjugate comprises coordination groups selected from COOH, PO3H and SO3H bound to a ligand backbone, the ligand backbone is linked, optionally by means of a spacer, to a support matrix, and the ligand backbone/spacer is free of ester and amide bonds. Such a conjugate may be prepared by the reaction of a polyamine of the formula H-[NH-A]n-NH2 with an activated support matrix Z-Y, wherein Y is a reactive group, optionally in the presence of or after reaction of either component with a compound introducing M; and reaction of the product with a compound of the formula Q-CH2-X, wherein Q is a group reactive with NH.

Description

METAL-CHELATING ADSORBENTS AND THEIR USE Field of the Invention
This invention relates to the preparation and use of novel affinity ligands for the removal of contaminant metal ions from diagnostic and therapeutic formulations. Background of the Invention
In recent years, significant advances have been made in the use of diagnostic radioimaging (radioimmunoscintigraphy) and of in vivo cytotoxic radiotherapy for the diagnosis and treatment of conditions such as cancer. Radioimmunotherapy relies on the targeted delivery of conjugates of monoclonal antibodies with radioactive metal ions to specific tumour sites, the specificity being a function of the antibody chosen. In typical radiotherapy protocols, the active agent is prepared by incubating a metal chelate-antibody conjugate with an excess of the radioisotopic metal ion for 0.5 - 1.0 hr. This is often followed by a series of time-consuming purification procedures to remove unbound or non-specifically bound metal ions. Typical purification protocols include dialysis and combinations of ion-exchange chromatography and gel filtration chromatography. Lengthy purification procedures lead to significant decreases in effective doses of radiation, particularly for conjugates comprising nuclides with short half-lives. Additionally, multi-step purification procedures lead to undesirable dilution effects.
Representative examples of metal chelates, methods of preparation of metal chelate-protein conjugates, and the use of such conjugates in diagnostic and therapeutic applications, have been disclosed in several publications. See, for example, rejcarek et al., Biochem. Biophys. Res. Commun., 1977, p.581, vol. 77; Brechbiel et al., Inorg. Chem., 1986, p.5783, vol. 25; Meares et al, Jou. Prot. Chem., 1984, p.215, vol. 3; Hnatowichetα/., Science, 1983a, p.613, vol.220;Khawetα/., Science., 1980, p.295, vol. 209; Scheinberg etβ/., Science, 1982, pJ511, vol. 215; US-A-4479930; US-A-4472509; US-A-5130118; EP-A-0484989; EP-A-0345723; and WO-A-96/15816.
A commonly used reagent for the covalent modification of proteins is the cyclic dianhydride of diethylenetriaminepentaacetic acid (DPTA), whereby an amide bond is formed between the protein and the chelator: The use of bifbnctional chelating reagents such as the dianhydride of DPTA results in cross-linking of the protein. Furthermore, the amide linkage between the protein and chelator is both acid- and base-labile. Thus, there remains the need for efficient and robust methods for the removal of contaminating metal ions from pharmaceutical preparations, including radiolabelled antibody conjugates, whilst overcoming the drawbacks of current procedures. Summary of the Invention
According to the present invention, in a metal-chelating ligand-support conjugate, the ligand comprises coordination groups selected from COOH, PO3H and SO3H, the ligand backbone is linked, optionally by means of a spacer, to a support matrix, and the ligand backbone/spacer is free of ester and amide bonds. Such a conjugate can be used for the capture of metal ions from water, aqueous solutions, blood, plasma, and pharmaceutical and therapeutic products and proteins.
Metal-chelating ligand-matrix conjugates embodying the present invention can be represented by formula (1)
Figure imgf000004_0001
CH X
(1)
wherein A represents a C,.6 saturated hydrocarbon chain; each X is COOH, PO3H or SO3H; n is 2 or more;
M is an optional spacer arm; and Z is a support matrix. Description of the Invention
In compounds of formula 1, A maybe linear or branched alkylene such as divalent methyl, ethyl, n-propyl, isopropyl, n-butyl, sec-butyl, isobutyl ortert-butyl. X is preferably COOH. n is preferably 2, so that the conjugate has 4 coordination groups, and usually no more than 3, 4 or 5. The support matrix may be any compound or material, particulate or non- particulate, soluble or insoluble, porous or non-porous, which may be used for the immobilization of metal-chelating ligands, to form a metal-chelating ligand-matrix conjugate, thereby providing a convenient means of binding metal ions from solution. Examples of particulate support matrices include natural polymers such as agarose, dextran, cellulose or starch, synthetic polymers and co-polymers such as perfluorocarbons, polystyrene, polyacrylamide, polyvinyl alcohol and polymethyl methacrylate, and inorganic compounds such as silica, glass, alumina and metal oxides. Examples of soluble carriers include polymers of dextran, polyvinyl alcohol, polyethylene glycol and hydrolysed starch. The support matrix may be in the form of packed columns or cartridges, or of membranes or sheets comprising such polymers.
Covalent attachment of ligand structures as represented by formula (1) to the support matrix Z may be achieved by use of a variety of activation agents including, but not limited to, cyanogen bromide, epichlorohydrin, 1,4-butanediol diglycidyl ether, tosyl chloride, tresyl chloride, and cyanuric chloride. The spacer group M may be absent, although it will be understood by those skilled in the art that the non-functional part of any functional groups used to conjugate Z and the coordination groups may be present in the product. If present, M may be any group which is conveniently capable of holding the ligand at a distance from the support matrix. Such spacer groups include diaminoalkanes and polyvinyl alcohol (PNA). A preferred spacer M comprises a group of the formula -T- L- wherein T is O, S or ΝR, R is H or C,^ alkyl, and L is an optionally substituted C2.20 alkylene chain optionally including one or more ether or thioether linkages. A further aspect of this invention is a facile method for the preparation of conjugates represented by formula (1) with a stable C-Ν bond formed between the ligand and the support matrix Z. A variety of methods is available, which avoid introducing an ester or amide bond. For examle, the method comprises the reaction of a polyamine of the formul H-[ΝH-A]n-ΝH2, with an activated support matrix Z-Y, wherein Y is a reactive group, optionally in the presence of or after reaction of either component with a compound introducing M; and reaction of the product with a compound of the formula Q-CH2-X, wherein Q is a group reactive with NH.
In one embodiment of the invention, a diamine such as diethylenetriamine is coupled to an activated support matrix followed by reaction with a halogenoacetic acid such as bromoacetic acid or chloroacetic acid to give a conjugate embodying the invention, by the method shown in the following scheme
Figure imgf000006_0001
H2N—(CH2)2— H—(CH2)2— H2
Figure imgf000006_0002
Z-O CH,—CH- CH2—NH—(CH,)2— H—(CH2)2—NH
2 I OH
Br—CH2—COOH
CH,—COOH
I 2 CH2—COOH
/
Z-O—CH2—CH—CH2—N —(CH2)2—N —(CH2)2—N
OH I CH,—COOH
CH,—COOH 2
The method shown above can be adapted, as will be apparent to those skilled in the art, to produce any other embodiment of the invention.
A desirable key feature of metal-chelating ligand-matrix conjugates prepared according to this invention is the ultrastable C-N linkage between the support matrix and the metal-chelating ligand, thereby enabling the use of such conjugates for sequestering metal ions at extremes of pH, ionic strength and temperature, without the risk of potentially toxic metal ion leachates.
Another aspect of this invention is a one-step chromatographic method for the removal of contaminant metal ions from diagnostic and therapeutic products. In a preferred embodiment of the invention, unbound and/or loosely bound metal ions are scavenged from a pharmaceutical product by passing the preparation through a terminally sterilized column containing a conjugate represented by formula (1), e.g. using an inert support matrix such as polytetrafluoroethylene (PTFE). Such adsorbents have a high affinity for heavy metals, and the method yields a therapeutic product that is substantially free of unbound metal ions and is suitable for administration to humans in vivo.
This invention may be applied to the removal of any suitable metal ion including radioactive and non-radioactive metal ions. The use of PTFE as a chromatographic support in this invention has specific advantages over other commercially available support matrices, including chemical and biological inertness, compatibility with gamma-irradiation and minimal swelling upon wetting which minimizes any sample dilution effects during use.
Another aspect of the present invention is the provision of an expeditious procedure for the removal of contaminant metal ions from pharmaceutical and other therapeutic formulations and comprises a terminally sterilized single-use disposable cartridge or element containing a metal-chelating adsorbent of formula (1). In one embodiment of the invention, the conjugate is used as the adsorbent for a radiactive component in a liquid sample. Such a method comprises using a syringe mounted at the outlet of a chamber to draw the sample through the chamber, wherein the chamber is housed within a radiation-absorbing shroud and contains an adsorbent for the component, and wherein the chamber also has an inlet and means for mounting a syringe thereon.
Apparatus suitable for use in this embodiment is illustrated schematically in the accompanying drawing. The drawing shows a chamber 1 having a syringe needle 2 mounted at its inlet, connected via a Luer fitting 3, and a seal 4. The combination is adapted to receive liquid sample 5 in a container 6. The chamber also has a syringe 7 mounted at its outlet and connected via a Luer fitting 8. The chamber includes an adsorbent 9. The combination of these components is surrounded by a radiation-absorbing shroud 10. In use, raising the syringe piston 11 draws liquid through the adsorbent 9. The sryinge 7, containing less contaminated liquid, can then be removed.
The novel conjugate may also be reused, if necessary or desired; its robustness means that NaOH can be used for sterilisation.
The following Examples illustrate the invention. DETATA is diethylenetriaminetetraacetic acid. Example 1 DETATA-agarose
Stage 1 - Preparation of epichlorohydrin-activated agarose
A slurry of Sepharose CL-6B (200g settled weight), RO water (128ml) and 10M sodium hydroxide (16ml) was reacted with epichlorohydrin (14.4ml) at 40°C for 3.5 hours. The epoxy activated Sepharose CL-6B was washed exhaustively with RO water (10 x 200ml portions) to remove excess reactants and used immediately in stage 2. Stage 2 - Preparation of diethylenetriamine-agarose
Epoxy-activated Sepharose CL-6B (94g settled weight) from stage 1 was mixed with 0.2M sodium bicarbonate solution (225ml) and diethylenetriamine (150ml) and the ■ reaction mixture stirred for 23 hours at 50 °C. The resulting amino gel was washed with RO water (10 x 100ml portions), 0. IM acetic acid (10 x 100ml portions) and finally with RO water (10 x 100ml portions). This gel was used in stage 3 of the reaction. Stage 3 - Preparation of DETATA-Agarose
The diethylenetriamine-agarose (stage 2) was mixed with bromoacetic acid (16g), 2M sodium hydroxide (50ml) and IM sodium bicarbonate (50ml). The resulting reaction mixture was adjusted to pH 7.0 with sodium hydroxide and left to react at room temperature for 16 hours. The gel was then washed with RO water (10 x 100ml portions) to remove excess reactants. , Yttrium-binding capacity DETATA-agarose (5g) was washed sequentially with RO water (10 x 5ml portions), IM sodium hydroxide (10 x 5ml portions) and RO water (10 x 5ml portions). The gel was then mixed with 5 ml RO water and the slurry gravity packed into a 10ml column.
A solution of non-radioactive 89yttιium chloride (2.191mg/ml in RO water; 25ml) was loaded onto the column under gravity followed by RO water (5ml) to wash out any unbound metal ion. Elution of bound yttrium was achieved by passing 1 OmM hydrochloric acid (25ml) through the column. The flow-through, eluted fractions and the stock yttrium solutions were analysed for elemental yttrium by Inductively Coupled Plasma Atomic Emission Spectrometry. Results are shown in Table 1. Table 1
Figure imgf000009_0001
Thus, Total Load 24.625mg Flow through 21.540mg Amount bound 3.085mg Capacity 0.617mg 89Y3Jg gel
6.9μmol 89Y3Jg gel
Eluted 0.9675mg
Example 2 DETATA-PTFE Stage 1 - Preparation of 1,4-butanediol diglycidyl ether-activated PTFE
A suspension of polyvinyl alcohol-coated PTFE particles (20g wet PTFE), RO water (47ml), 10M sodium hydroxide solution (2ml) and 1 OOmg sodium borohydride was reacted with 1,4-butanediol diglycidyl ether (30ml) for 7 hours at room temperature. The epoxy-activated PTFE material was washed with excess RO water to remove reactants. Stage 2 - Preparation of diethylenetriamine-PTFE
The activated, settled product was mixed with an equal volume of diethylenetriamine and allowed to react for 24 hours at 50° C. Diethylenetriamine was removed at the end of the reaction by washing the gel with excess RO water. Stage 3 - Preparation of DETATA-PTFE
The settled gel from stage 2 was suspended in IM sodium hydrogen carbonate (25ml) and 2M sodium hydroxide solution (25ml). Bromoacetic acid (8g) was added and the pH of the suspension adjusted to pH 7.0 by the drop-wise addition of 2M sodium hydroxide. The reaction mixture was stirred for 16 hours at room temperature. The final chelate adsorbent was washed with an excess of RO water at the end of the reaction. Copper-binding capacity
An aqueous slurry of DETATA-PTFE (1.02g) was loaded into a 1ml glass column connected up to a Gilson peristaltic pump and washed sequentially with IM sodium hydroxide (10ml) and RO water (10ml) at a flow rate of 0.5ml/min. A stock solution of copper sulphate (16mg/ml in RO water; 11.35ml) was loaded onto the column at a flow rate of 0.5ml/min and the flow through collected (10ml). The column was rinsed withRO water ( 10ml) to remove any unbound copper sulphate. Bound copper sulphate was eluted from the column using nitric acid (OJM; 3.5ml). All fractions were assayed for copper sulphate spectrophotometrically. The results are shown in Table 2.
Table 2
Figure imgf000010_0001
Thus, Total Load 176.13mg
Flow through + RO rinse = 174.43mg
Eluted 0.401mg
Capacity = 2.512μmol Cu2Jg gel
Yttrium-binding capacity
A20%,(v/v) ethano water slurry of gamma-irradiated DETATA-PTFE (3.975g) was loaded into a 10ml glass column connected up to a peristaltic pump and washed with RO water (10ml), IM sodium hydroxide (10ml) and RO water (10ml) at a flow rate of 0.5ml/min. A stock solution of non-radioactive89yttrium chloride (1. Img/ml in RO water; 10ml) was loaded onto the column, washed with RO water (20ml) and the bound yttrium was eluted with nitric acid (0. IM; lOrnl). All fractions were assayed for yttrium by ICP- MS. The results are shown in Table 3.
Table 3
Figure imgf000010_0002
Thus, Total Load = 4923 μg
Flow through = 3014μg
RO rinse = 1681μg
Eluted = 221μg Capacity = 58.2μg 89Y3+/g gel
0.654μmol 89Y37g gel Radioactive Yttrium-Binding Efficiency
DETATA-PTFE adsorbent (1.2g dry weight) was dry packed to a bed height of 20mm into a cartridge (40mm height x 8mm i.d.) containing a leur fitting at the inlet port and a 0.45mm filter connected to a leur fitting at the outlet port. The packed cartridge was housed within a radiation shield to minimize exposure to radiation during use.
As a control, in the absence of immunoconjugate, a syringe was connected to the outlet port of the cartridge and sodium acetate buffer (5ml, OJM pH 5.5) was pulled through the cartridge. A solution of radioactive 90yttrium chloride (0.5ml) made up in sodium acetate buffer (0. IM, pH 5.5) containing 37MBq of radioactivity units was loaded onto the cartridge followed by acetate buffer (5 x 1ml, 0. IM pH 5.5). Measurement of radioactivity in the wash fractions showed that 99.1% of the radioactivity was retained by the cartridge. The cartridge was regenerated by sequentially washing with nitric acid (OJM,
5ml), RO water (5ml), sodium hydroxide (IM, 5ml) and finally with RO water (10ml). A preparation of antibody immunoconjugate labelled with 90yttrium was prepared by incubating 90yttrium chloride (37Mbq, 200μl in 0. IM acetate buffer pH 5.5) with antibody immunoconjugate (5μl, 30μg) for 30 minutes. The radiolabelled reaction mixture was passed through the cartridge and immunoconjugate eluted with sodium acetate (3 x lml, 0. IM pH 5.5). The radiochemical purity of the conjugate prior to purification was 96% and increased to 98% after purification using the cartridge. Human Serum Albumin Binding Capacity
An aqueous slurry of DETATA-PTFE was packed into a glass chromatography column (10mm i.d.) to a bed height of 49mm (3.85ml column volume) and washed sequentially with sodium hydroxide (IM, 10ml) and RO water (10ml) at a flow rate of lml/min. Copper was loaded onto the adsorbent by passing an aqueous solution of copper sulphate (10ml, 16mg/ml) through the column. The column was then washed with RO water (10ml) to remove excess copper sulphate and equilibrated with loading buffer (0. IM sodium acetate, 0.5M sodium chloride pH 7.7, 10ml). A sample of human serum albumin (2ml, lmg/ml) prepared in loading buffer was loaded onto the column at a flow rate of lml/min and the column was washed with loading buffer (10ml) to remove all unbound protein. Bound serum albumin was eluted from the column by applying 50mM tris/HCl, 0.15M ammonium chloride pH 8.0 (4.0ml). All fractions were assayed for albumin using the Coomassie protein assay. The results are summarized below.
Total serum albumin loaded = 2000 μg
Total serum albumin in flow through = 1870 μg
Total serum albumin in elution = 84.9 μg
Thus albumin binding capacity = 22.1 μg/ml of adsorbent.

Claims

1. A metal-chelating ligand-support conjugate in which the ligand comprises coordination groups selected from COOH, PO3H and SO3H bound to a ligand backbone, the ligand backbone is linked, optionally by means of a spacer; to a support matrix, and
! the ligand backbone/spacer is free of ester and amide bonds.
2. A conjugate according to claim 1, of the formula
Figure imgf000013_0001
(1)
wherein A represents a C,^ saturated hydrocarbon chain; each X is COOH, PO3H or SO3H; n is 2 or more;
M is an optional spacer arm; and Z is a support matrix.
3. A conjugate according to claim 2, wherein M is present and comprises a group of the formula -T-L- wherein T is O, S or NR, R is H or Cx_6 alkyl, and L is an optionally substituted C2.20 alkylene chain optionally including one or more ether or thioether linkages.
4. A conjugate according to claim 2, wherein M is absent.
5. A conjugate according to any of claims 2 to 4, wherein n is 2.
6. A conjugate according to any preceding claim, wherein the coordination group/X is COOH.
7. A conjugate according to any preceding claim, wherein the support matrix is a perfluorocarbon polymer or a perfluorocarbon copolymer, either of which is optionally coated with a hydrophilic polymer.
8. A conjugate according to any preceding claim, capable of chelating yttrium ions.
9. A method for the preparation of a conjugate according to any preceding claim, which comprises the reaction of a polyamine of the formula H-[NH-A]n-NH2 with an activated support matrix Z-Y, wherein Y is a reactive group, optionally in the presence of or after reaction of either component with a compound introducing M; and reaction of the product with a compound of the formula Q-CH2-X, wherein Q is a group reactive with NH.
10. A conjugate according to any of claims 1 to 8, obtainable by a method according to claim 9.
11. A complex of a conjugate according to any of claims 1 to 8 and 10, and chelated metal ions.
12. Use of a conjugate according to any of claims 1 to 8 and 10, for the removal of metal ions from a sample.
13. Use according to claim 12, wherein the metal ions are radioactive.
14. Use of a complex according to claim 11 , for the separation, isolation, purification, characterisation, identification or quantification of proteins or nucleic acids.
15. A method for the removal of a radioactive component from a liquid sample, which comprises using a syringe mounted at the outlet of a chamber to draw the sample through the chamber, wherein the chamber is housed within a radiation-absorbing shroud and contains an adsorbent for the said component, and wherein the chamber also has an inlet and means for mounting a syringe thereon.
16. A method according to claim 15, wherein the adsorbent.is a conjugate according to any of claims 1 to 8.
PCT/GB2001/005231 2000-11-27 2001-11-27 Metal-chelating adsorbents and their use WO2002041989A1 (en)

Priority Applications (3)

Application Number Priority Date Filing Date Title
AU2002220830A AU2002220830A1 (en) 2000-11-27 2001-11-27 Metal-chelating adsorbents and their use
AU2002343100A AU2002343100A1 (en) 2001-11-27 2002-11-27 The use of metal-chelating adsorbents
PCT/GB2002/005326 WO2003045546A1 (en) 2001-11-27 2002-11-27 The use of metal-chelating adsorbents

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
GB0028879A GB0028879D0 (en) 2000-11-27 2000-11-27 Adsorbents and their use
GB0028879.5 2000-11-27

Publications (1)

Publication Number Publication Date
WO2002041989A1 true WO2002041989A1 (en) 2002-05-30

Family

ID=9903944

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/GB2001/005231 WO2002041989A1 (en) 2000-11-27 2001-11-27 Metal-chelating adsorbents and their use

Country Status (3)

Country Link
AU (1) AU2002220830A1 (en)
GB (1) GB0028879D0 (en)
WO (1) WO2002041989A1 (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2003045546A1 (en) * 2001-11-27 2003-06-05 Prometic Biosciences Ltd. The use of metal-chelating adsorbents
WO2009013358A2 (en) * 2007-07-26 2009-01-29 Laboratoires Cyclopharma New compositions based on polysaccharides grafted by polyamine or polysulphurised compounds
WO2017046625A1 (en) * 2015-06-25 2017-03-23 Cube Biotech Gmbh New chelators for affinity purification of recombinant proteins
US9630165B2 (en) 2014-01-17 2017-04-25 Genzyme Corporation Sterile chromatography resin and use thereof in manufacturing processes
US9650413B2 (en) 2013-03-08 2017-05-16 Genzyme Corporation Integrated continuous manufacturing of therapeutic protein drug substances
US10087214B2 (en) 2014-01-17 2018-10-02 Genzyme Corporation Sterile chromatography and manufacturing processes
US11369703B2 (en) 2018-08-31 2022-06-28 Genzyme Corporation Sterile chromatography resin and use thereof in manufacturing processes

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4599175A (en) * 1983-09-30 1986-07-08 Asahi Kasei Kogyo Kabushiki Kaisha Process for separating and purifying metallic elements by displacement chromatography
US4877830A (en) * 1986-07-10 1989-10-31 Hoffmann-La Roche Inc. Metal chelate resins
WO1991006008A1 (en) * 1989-10-11 1991-05-02 Akzo N.V. Method for purifying chelator conjugated compounds
WO1992017403A1 (en) * 1991-04-05 1992-10-15 Brigham Young University Support bonded polyalkylene-polyamine-poly(carboxylic acid) and extraction of metal ions therewith
EP0621074A1 (en) * 1993-04-22 1994-10-26 E.I. Du Pont De Nemours And Company Hydrophilic polymer coated perfluorocarbon polymer-based matrices, their preparation and use in bioaffinity separations
EP0972566A2 (en) * 1998-07-13 2000-01-19 Minh Tran Quang Affinity immobilised metal resins

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4599175A (en) * 1983-09-30 1986-07-08 Asahi Kasei Kogyo Kabushiki Kaisha Process for separating and purifying metallic elements by displacement chromatography
US4877830A (en) * 1986-07-10 1989-10-31 Hoffmann-La Roche Inc. Metal chelate resins
WO1991006008A1 (en) * 1989-10-11 1991-05-02 Akzo N.V. Method for purifying chelator conjugated compounds
WO1992017403A1 (en) * 1991-04-05 1992-10-15 Brigham Young University Support bonded polyalkylene-polyamine-poly(carboxylic acid) and extraction of metal ions therewith
EP0621074A1 (en) * 1993-04-22 1994-10-26 E.I. Du Pont De Nemours And Company Hydrophilic polymer coated perfluorocarbon polymer-based matrices, their preparation and use in bioaffinity separations
EP0972566A2 (en) * 1998-07-13 2000-01-19 Minh Tran Quang Affinity immobilised metal resins

Cited By (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2003045546A1 (en) * 2001-11-27 2003-06-05 Prometic Biosciences Ltd. The use of metal-chelating adsorbents
WO2009013358A2 (en) * 2007-07-26 2009-01-29 Laboratoires Cyclopharma New compositions based on polysaccharides grafted by polyamine or polysulphurised compounds
FR2919189A1 (en) * 2007-07-26 2009-01-30 Cyclopharma Sa Lab NOVEL COMPOSITIONS BASED ON POLYOSIDES GRAFTED BY POLYAMINE OR POLYSOUFRE COMPOUNDS.
WO2009013358A3 (en) * 2007-07-26 2009-10-22 Laboratoires Cyclopharma Polysaccharides grafted by polyamines for the preparation of radiopharmaceutical compositions
US9023396B2 (en) 2007-07-26 2015-05-05 Laboratoires Cyclopharma Compositions based on polysaccharides grafted by polyamine or polysulphurised compounds
US9650412B2 (en) 2013-03-08 2017-05-16 Genzyme Corporation Integrated continuous manufacturing of therapeutic protein drug substances
US9650413B2 (en) 2013-03-08 2017-05-16 Genzyme Corporation Integrated continuous manufacturing of therapeutic protein drug substances
US9657056B2 (en) 2013-03-08 2017-05-23 Genzyme Corporation Integrated continuous manufacturing of therapeutic protein drug substances
US10711034B2 (en) 2013-03-08 2020-07-14 Genzyme Corporation Integrated continuous manufacturing of therapeutic protein drug substances
US9630165B2 (en) 2014-01-17 2017-04-25 Genzyme Corporation Sterile chromatography resin and use thereof in manufacturing processes
US10071364B2 (en) 2014-01-17 2018-09-11 Genzyme Corporation Sterile affinity chromatography resin
US10087214B2 (en) 2014-01-17 2018-10-02 Genzyme Corporation Sterile chromatography and manufacturing processes
US10919021B2 (en) 2014-01-17 2021-02-16 Genzyme Corporation Sterile chromatography resin and use thereof in manufacturing processes
US11839861B2 (en) 2014-01-17 2023-12-12 Genzyme Corporation Sterile chromatography resin and use thereof in manufacturing processes
US11912739B2 (en) 2014-01-17 2024-02-27 Genzyme Corporation Sterile chromatography and manufacturing processes
WO2017046625A1 (en) * 2015-06-25 2017-03-23 Cube Biotech Gmbh New chelators for affinity purification of recombinant proteins
US11369703B2 (en) 2018-08-31 2022-06-28 Genzyme Corporation Sterile chromatography resin and use thereof in manufacturing processes

Also Published As

Publication number Publication date
AU2002220830A1 (en) 2002-06-03
GB0028879D0 (en) 2001-01-10

Similar Documents

Publication Publication Date Title
DK172602B1 (en) Metal chelate resins, process for their preparation, use thereof for metal chelate chromatography, nitrilotriac vinegar
JPH05261280A (en) Metal-chelating hydrophilic polymer
JP5026648B2 (en) Method and equipment for removal of metal cations from liquids by polyazacycloalkane resins grafted on a support
JP3499869B2 (en) Activated support materials, their preparation and use
JPH0214325B2 (en)
JP2010133734A (en) Carboxylation carrier for affinity chromatography, and separating agent for affinity chromatography using the same
JPH0144725B2 (en)
Kugel et al. Microporous poly (caprolactam) hollow fibers for therapeutic affinity adsorption
WO2002041989A1 (en) Metal-chelating adsorbents and their use
ES2340032T3 (en) A METHOD FOR GENERATING METAL BURNING AFFINITY LINKS.
WO2003045546A1 (en) The use of metal-chelating adsorbents
EP1507563B1 (en) Endotoxin-binding ligands and their use
US20060189797A1 (en) Magnetic polymer particles
JP2928589B2 (en) Adsorbent for modified LDL and apparatus for removing modified LDL using the same
EP0057600B1 (en) Affinity resins and their use in isolating bacterial luciferase
JPH0337976B2 (en)
US5866387A (en) Method for immobilizing ligand or compound having ligand bonded thereto
WO1992011039A1 (en) Derivatized tris-catechol chelating agents
JP2732252B2 (en) Hemoglobin selective adsorbent
US7175767B2 (en) Preparation of a metal chelating separation medium
JP7114150B2 (en) A new chromatographic medium
JPS63197462A (en) Anti-human igm immune adsorbent and its production
JPS6187640A (en) Separation process
JPS6155415B2 (en)
JP2717666B2 (en) Blood purification adsorbent, method for producing the same, and blood purification apparatus using the same

Legal Events

Date Code Title Description
AK Designated states

Kind code of ref document: A1

Designated state(s): AE AG AL AM AT AU AZ BA BB BG BR BY BZ CA CH CN CO CR CU CZ DE DK DM DZ EC EE ES FI GB GD GE GH GM HR HU ID IL IN IS JP KE KG KP KR KZ LC LK LR LS LT LU LV MA MD MG MK MN MW MX MZ NO NZ OM PH PL PT RO RU SD SE SG SI SK SL TJ TM TR TT TZ UA UG US UZ VN YU ZA ZW

AL Designated countries for regional patents

Kind code of ref document: A1

Designated state(s): GH GM KE LS MW MZ SD SL SZ TZ UG ZM ZW AM AZ BY KG KZ MD RU TJ TM AT BE CH CY DE DK ES FI FR GB GR IE IT LU MC NL PT SE TR BF BJ CF CG CI CM GA GN GQ GW ML MR NE SN TD TG

121 Ep: the epo has been informed by wipo that ep was designated in this application
REG Reference to national code

Ref country code: DE

Ref legal event code: 8642

122 Ep: pct application non-entry in european phase
NENP Non-entry into the national phase

Ref country code: JP

WWW Wipo information: withdrawn in national office

Country of ref document: JP