WO2002041989A1 - Metal-chelating adsorbents and their use - Google Patents
Metal-chelating adsorbents and their use Download PDFInfo
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- 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
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- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K51/00—Preparations containing radioactive substances for use in therapy or testing in vivo
- A61K51/02—Preparations 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
- A61K51/04—Organic compounds
- A61K51/06—Macromolecular compounds, carriers being organic macromolecular compounds, i.e. organic oligomeric, polymeric, dendrimeric molecules
- A61K51/065—Macromolecular compounds, carriers being organic macromolecular compounds, i.e. organic oligomeric, polymeric, dendrimeric molecules conjugates with carriers being macromolecules
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- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/22—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising organic material
- B01J20/223—Solid 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
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- B01J20/281—Sorbents specially adapted for preparative, analytical or investigative chromatography
- B01J20/286—Phases chemically bonded to a substrate, e.g. to silica or to polymers
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- B01J20/3092—Packing of a container, e.g. packing a cartridge or column
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- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/30—Processes for preparing, regenerating, or reactivating
- B01J20/32—Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating
- B01J20/3202—Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating characterised by the carrier, support or substrate used for impregnation or coating
- B01J20/3206—Organic carriers, supports or substrates
- B01J20/3208—Polymeric carriers, supports or substrates
- B01J20/3212—Polymeric carriers, supports or substrates consisting of a polymer obtained by reactions otherwise than involving only carbon to carbon unsaturated bonds
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- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/30—Processes for preparing, regenerating, or reactivating
- B01J20/32—Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating
- B01J20/3214—Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating characterised by the method for obtaining this coating or impregnating
- B01J20/3217—Resulting in a chemical bond between the coating or impregnating layer and the carrier, support or substrate, e.g. a covalent bond
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/30—Processes for preparing, regenerating, or reactivating
- B01J20/32—Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating
- B01J20/3214—Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating characterised by the method for obtaining this coating or impregnating
- B01J20/3217—Resulting in a chemical bond between the coating or impregnating layer and the carrier, support or substrate, e.g. a covalent bond
- B01J20/3219—Resulting 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
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- B—PERFORMING OPERATIONS; TRANSPORTING
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- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/30—Processes for preparing, regenerating, or reactivating
- B01J20/32—Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating
- B01J20/3231—Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating characterised by the coating or impregnating layer
- B01J20/3242—Layers with a functional group, e.g. an affinity material, a ligand, a reactant or a complexing group
- B01J20/3244—Non-macromolecular compounds
- B01J20/3246—Non-macromolecular compounds having a well defined chemical structure
- B01J20/3248—Non-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
- B01J20/3251—Non-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
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- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/30—Processes for preparing, regenerating, or reactivating
- B01J20/32—Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating
- B01J20/3231—Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating characterised by the coating or impregnating layer
- B01J20/3242—Layers with a functional group, e.g. an affinity material, a ligand, a reactant or a complexing group
- B01J20/3244—Non-macromolecular compounds
- B01J20/3246—Non-macromolecular compounds having a well defined chemical structure
- B01J20/3248—Non-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
- B01J20/3255—Non-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
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- B—PERFORMING OPERATIONS; TRANSPORTING
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- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/30—Processes for preparing, regenerating, or reactivating
- B01J20/32—Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating
- B01J20/3231—Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating characterised by the coating or impregnating layer
- B01J20/3242—Layers with a functional group, e.g. an affinity material, a ligand, a reactant or a complexing group
- B01J20/3244—Non-macromolecular compounds
- B01J20/3265—Non-macromolecular compounds with an organic functional group containing a metal, e.g. a metal affinity ligand
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/30—Processes for preparing, regenerating, or reactivating
- B01J20/34—Regenerating or reactivating
- B01J20/3425—Regenerating or reactivating of sorbents or filter aids comprising organic materials
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/30—Processes for preparing, regenerating, or reactivating
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- B01J20/345—Regenerating or reactivating using a particular desorbing compound or mixture
- B01J20/3475—Regenerating or reactivating using a particular desorbing compound or mixture in the liquid phase
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J45/00—Ion-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
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- G—PHYSICS
- G21—NUCLEAR PHYSICS; NUCLEAR ENGINEERING
- G21F—PROTECTION AGAINST X-RADIATION, GAMMA RADIATION, CORPUSCULAR RADIATION OR PARTICLE BOMBARDMENT; TREATING RADIOACTIVELY CONTAMINATED MATERIAL; DECONTAMINATION ARRANGEMENTS THEREFOR
- G21F9/00—Treating radioactively contaminated material; Decontamination arrangements therefor
- G21F9/04—Treating liquids
- G21F9/06—Processing
- G21F9/12—Processing by absorption; by adsorption; by ion-exchange
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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- B01J2220/00—Aspects relating to sorbent materials
- B01J2220/50—Aspects relating to the use of sorbent or filter aid materials
- B01J2220/54—Sorbents specially adapted for analytical or investigative chromatography
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2220/00—Aspects relating to sorbent materials
- B01J2220/50—Aspects relating to the use of sorbent or filter aid materials
- B01J2220/58—Use in a single column
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2220/00—Aspects relating to sorbent materials
- B01J2220/50—Aspects relating to the use of sorbent or filter aid materials
- B01J2220/62—In 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.
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Abstract
Description
Claims
Priority Applications (3)
Application Number | Priority Date | Filing Date | Title |
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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 |
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GB0028879A GB0028879D0 (en) | 2000-11-27 | 2000-11-27 | Adsorbents and their use |
GB0028879.5 | 2000-11-27 |
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WO2002041989A1 true WO2002041989A1 (en) | 2002-05-30 |
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Cited By (7)
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 |
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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 |
-
2000
- 2000-11-27 GB GB0028879A patent/GB0028879D0/en not_active Ceased
-
2001
- 2001-11-27 WO PCT/GB2001/005231 patent/WO2002041989A1/en not_active Application Discontinuation
- 2001-11-27 AU AU2002220830A patent/AU2002220830A1/en not_active Abandoned
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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 |
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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 |
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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 |
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