WO2007099374A1 - Adsorbents for protein purification - Google Patents
Adsorbents for protein purification Download PDFInfo
- Publication number
- WO2007099374A1 WO2007099374A1 PCT/GB2007/050095 GB2007050095W WO2007099374A1 WO 2007099374 A1 WO2007099374 A1 WO 2007099374A1 GB 2007050095 W GB2007050095 W GB 2007050095W WO 2007099374 A1 WO2007099374 A1 WO 2007099374A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- use according
- adsorbent
- formula
- aryl
- halogen
- Prior art date
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07D—HETEROCYCLIC COMPOUNDS
- C07D251/00—Heterocyclic compounds containing 1,3,5-triazine rings
- C07D251/02—Heterocyclic compounds containing 1,3,5-triazine rings not condensed with other rings
- C07D251/12—Heterocyclic compounds containing 1,3,5-triazine rings not condensed with other rings having three double bonds between ring members or between ring members and non-ring members
- C07D251/26—Heterocyclic compounds containing 1,3,5-triazine rings not condensed with other rings having three double bonds between ring members or between ring members and non-ring members with only hetero atoms directly attached to ring carbon atoms
- C07D251/40—Nitrogen atoms
- C07D251/48—Two nitrogen atoms
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D15/00—Separating processes involving the treatment of liquids with solid sorbents; Apparatus therefor
- B01D15/08—Selective adsorption, e.g. chromatography
- B01D15/26—Selective adsorption, e.g. chromatography characterised by the separation mechanism
- B01D15/38—Selective adsorption, e.g. chromatography characterised by the separation mechanism involving specific interaction not covered by one or more of groups B01D15/265 - B01D15/36
- B01D15/3804—Affinity chromatography
-
- 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
- B01J20/281—Sorbents specially adapted for preparative, analytical or investigative chromatography
- B01J20/286—Phases chemically bonded to a substrate, e.g. to silica or to polymers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/30—Processes for preparing, regenerating, or reactivating
- B01J20/32—Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating
- B01J20/3231—Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating characterised by the coating or impregnating layer
- B01J20/3242—Layers with a functional group, e.g. an affinity material, a ligand, a reactant or a complexing group
- B01J20/3244—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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/30—Processes for preparing, regenerating, or reactivating
- B01J20/32—Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating
- B01J20/3231—Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating characterised by the coating or impregnating layer
- B01J20/3242—Layers with a functional group, e.g. an affinity material, a ligand, a reactant or a complexing group
- B01J20/3244—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
-
- Y—GENERAL 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
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T436/00—Chemistry: analytical and immunological testing
- Y10T436/25—Chemistry: analytical and immunological testing including sample preparation
- Y10T436/25375—Liberation or purification of sample or separation of material from a sample [e.g., filtering, centrifuging, etc.]
-
- Y—GENERAL 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
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T436/00—Chemistry: analytical and immunological testing
- Y10T436/25—Chemistry: analytical and immunological testing including sample preparation
- Y10T436/25375—Liberation or purification of sample or separation of material from a sample [e.g., filtering, centrifuging, etc.]
- Y10T436/255—Liberation or purification of sample or separation of material from a sample [e.g., filtering, centrifuging, etc.] including use of a solid sorbent, semipermeable membrane, or liquid extraction
Definitions
- This invention relates to compounds and their use as affinity ligands for protein purification.
- Antibodies are immunoglobulin glycoproteins having a basic unit of a monomer structure.
- the monomer is a Y-shaped protein that consists of four polypeptide chains, two of which are identical heavy chains and two are identical light chains connected by disulphide bridges.
- IgG (a monomeric immunoglobulin approximately of 150 kD in size) provides antibody-based immunity against invading pathogens and, due to the high specificity that IgG has towards specific antigens within the body, it is the most commonly used reagent in immunological research and clinical diagnostics.
- Mabs Monoclonal antibodies
- Mabs Monoclonal antibodies
- Antibody fragments (parts of whole antibody molecules) offer several advantages over whole antibodies. They are easier and more cost effective to manufacture, they have fewer side-effects in patients, by reducing the risk of cytokine release and its associated toxicity, due to the absence of the Fc (heavy chain) region, and they can be modified to include therapeutic payloads.
- Protein L 5 a protein with a molecular weight of 35000 Daltons derived from a bacterial species of Peptostreptococcus magn ⁇ s, is known to bind to antibody light chains and has been investigated for the purification of some antibody fragments but is not considered to be cost- effective and is not available in commercia! quantities.
- WO97/1G887 discloses triazine-based compounds, useful as affinity adsorbents, of formula I
- R 1 is H, alky!, hydroxyalkyl, cyclohexyl, NH 2 , phenyl, naphthyl, 1- ⁇ henylpyrazole, indazoie, benzthiazole, benzoxazole or benzimidazote, any of which aromatic groups can be substituted with one or more of aikyl, alkoxy, acytoxy, acylamino, amino, NH 2 , OH, CO 2 H, sulphonyl, carbamoyl, suiphamoyl, alkylsuIphonyS and halogen; one X is N and the other is N, C-CI or C-CN;
- Y is O, S or NR 2 ;
- Z is O, S or NR 3 ;
- R 2 and R 3 are each H 1 alkyi, hydroxyaikyl, benzyl or ⁇ -phenylethyl;
- Q is benzene, naphthalene, benzthiazole, benzoxazoie, 1 -phenylpyrazoie, indazoie or benzimidazole;
- R 4 , R 5 and R 6 are each H, OH, alky!, alkoxy, amino, NH 2 , acyloxy, acylamino, CO 2 H, sulphonic acid, carbamoyl, suiphamoyl, alkylsulphonyl or halogen; n is O to 6; p is O to 20; and A is a support matrix optionally linked to the X-containing ring by a spacer.
- Compounds of formula ! are disclosed as having affinity for proteins such as immunoglobulins, insulin. Factor VII or human growth hormone.
- Compounds such as II are able to remove immunoglobulins specifically from complex mixtures or feedstocks such as human plasma.
- Another type of commonly encountered feedstock is industrially produced cell culture supernatant, in which monoclonal antibodies are present at concentrations up to 5 g/i of supernatant.
- Compounds such as I! may also be useful for specific removal of monoclonal antibody from these mixtures, although their performance is known to be compromised by the presence of cell culture additives such as PIuronic F-68.
- Pluronic F-68 is an anti-foaming agent commonly used used in mammalian ce)! culture, it is a biock copolymer of poiyoxyethylene and polyoxypropytene, and has a molecular weight of approximately 8000 Da. Pluronic F-68 is used to protect cells from shear and air bubble damage, and is typically used in an amount of 1 g/L in cell culture supernatants. Its presence may reduce or abolish the ability of compounds such as S! to remove immunoglobulins from such feedstocks, which represents a considerable obstacle to the use of such ligands for direct capture of monoclonal antibodies from mammalian eel! culture media.
- R-. is H, alkyi, aryi, hydroxyaikyl, cyclohexyi amino or a heterocyclic group e.g naphthyS, 1-phenyipyrazole, indazole, benzthiazole, benzoxazole or benzimidazole, any of which aromatic groups may comprise a further fused ring And can be substituted with one or more of alkyi, aryl, alkoxy, aryloxy, acyloxy, acylamino, amino, OH, CO 2 H, sulphonyl, carbamoyl, suiphamoyi, alky!suiphony! and halogen, one X is N and the other is N, C-CI or C-CN,
- Y is O, S or NR 25
- Z is O, S or NR 3 ,
- R 2 and R 3 are each H, aikyi, hydroxyalkyi, benzyl or ⁇ -phenylethyi;
- Q is benzene, naphthalene, benzthiazole, benzoxazole, 1-phenyIpyrazoie, indazole or benzimidazole,
- R 4 , R 5 and R s are each H, OH, alkyi, aryi, heterocyclic alkoxy, aryloxy, amino, acyloxy, acySamsno, CO 2 H, sulphonic acsd, carbamoyl, suiphamoyi, alkylsuSpnonyi or halogen, or two or more of R 4 , R 5 and R 6 are linked to form a cyclic structure, U and V are the same or different C-i 10 straight-chain a ⁇ kyiene groups optionally substituted by one or more of hydroxy!, alky!, aryl, hydroxyaikyl, ⁇ -phenylethyl and halogen such as CHOH, and
- A is a support matrix optionally linked to the X-containing ring by a spacer
- WO97/10887, WO00/67900 and WO003/097112 disclose how combinatorial libraries of iigands can be haul on a solid support.
- Thesr disclosures, including examples of embodiments and procedures common to the present invention, are incorporated herein by reference During the screening of a set of these combinatorial libraries with a feedstock containing albumin, immunoglobulins and PIuronic F-68, a number of ligands were identified as being capable of selectively binding and eluting immunoglobulins, Compounds of formula III, for use in the invention, can be prepared by procedures known to those skilled tn the art Such procedures are described in the 3 PCT publications identified above, they can be readily adapted to the preparation of new compounds
- R and/or QR 4 R 5 R 6 is or includes a cyclic structure, erther or each cyclic structure preferably has a OH or SO 3 H substituenf
- each X ss N is substituted, e g ss CHOH
- Such substituted compounds are novel Preferred immunoglobuling-binding ligands or adsorbents of the invention are of formulae IV-XISl:
- T he immunoglobulin-binding ligands described herein are useful for the purification immunoglobulins from complex mixtures including, but not limited to, human plasma and recombinant fermentation supematants. This utility is demonstrated below in Example 2, oy chromatography experiments using a number of feedstocks.
- immunoglobulin ss used herein to describe intact immunoglobulins themselves, including IgG, IgA, IgM and IgE, and also analogues that have the functional or structural characteristics of immunoglobulins, e.g in terms of affinity to a given compound described herein
- the anaiyte may be a protein that is a functional fragment of an immunoglobulin, or a structural analogue having one, more or all of the same binding sites, or a fusion protein
- the optional Nnker may comprise any means of attaching lsgands of the invention to support matrices and providing a means of spacing the ligand from the surface of the support matrix
- the support matrix may comprise any material, soluble or insoluble, particulate or non-particulate, including fibres and membranes, porous or non-porous. It provides a convenient means of separating lsgands of the invention from solutes in a contacting solution.
- support matrix and optional linker A examples include carbohydrate matrices such as agarose, cellulose, dextran, starch, alginate or carrageenan, synthetic polymer matrices such as polystyrene, styrene-dtvmySbenzene copolymers, polymethacrylates, (e g, poly(hydroxyethylmethacfylate), polyvinyl alcohol, poiyamides or perfluorocarbons, inorganic matrices such as glass, silica or metai oxsdes;and composite materials
- carbohydrate matrices such as agarose, cellulose, dextran, starch, alginate or carrageenan
- synthetic polymer matrices such as polystyrene, styrene-dtvmySbenzene copolymers
- polymethacrylates e g, poly(hydroxyethylmethacfylate), polyvinyl alcohol, poiyamides
- the gel was washed with 50% DMF (5 x 100 mL), RO water (5 x 100 mL), 0 1 M HCt (5 x 100 mL), 30% IPA/0.2 M NaOH (5 x 100 mL), RO water (10 x 100 mL), and 20% aqueous ethanoi (3 x 100 mL) before storage in the coid room in 20% aqueous ethanoi Example 2 - Chromatography
- the adsorbent was initially equilibrated wrth 10 CV of phosphate buffered saline (PBS), pH 7 4, and then loaded wrth pure IgG, IgG feedstock 1 (1 g/L IgG, 1 g/L Plur ⁇ mc F-68, and other proteins to mimic eel culture supernatant) or 2 (1 g/L !gG, 1 g/L Pluronsc F-8 ⁇ wrth 5% foetal calf serum), or murine IgGi feedstock up to a concentration of 30 g/L of adsorbent
- the adsorbent was then washed with 10 CV of PBS, pH 7 4, before the IgG was eiuted wrth 5 CV of 50 my citric acid, pH 3.5.
- the adsorbent then underwent a ciean in place (CiP) with 5 CV of 0 5 M sodsum hydroxide followed by re-equsl ⁇ brat ⁇ on of the adsorbent with 7 CV of PBS, pH 7 4
- IgG feed contained 1 g/L of polyclonal IgG sn PBS, pH 7 4 m the presence or absence of 1 g/L Pluro ⁇ ic F-68
- Mock feedstock 1 contained 1 g/L polyclonal IgG, 1 g/L horse skeletal myoglobin, 5 g/L human serum albumin and 1 g/L Pluro ⁇ ic F-68 in CHO cell culture medsum.
- Mock feedstock 2 contained 1 g/L polyclonal IgG, 5% foetal bovine serum and 1 g/L Pluronic F-68 in GHO ceil cu ⁇ ture medium Table 1
- ESution buffer 50 mM citric acid, pH 3.5 with 30% ethylene glycol and 2 M NaCi.
- adsorbent Xl The chromatographic performance of adsorbent Xl was further investigated, to assess the purification capability of the materia!. Experiments were completed using a 1 cm diameter column with a bed height of 2 5 cm and column volume (CV) of 2 0 mL and a linear flow rate of 50 cm/h (3 minute residence time) The adsorbent was initially equilibrated with 10 CV of phosphate buffered saline (PBS), pH 74. 60 mL o!
- PBS phosphate buffered saline
- IgGi in a CHO (Chinese Hamster Ovary) cell culture supernatant was loaded onto the column to a concentration of 54 g/L of adsorbent
- the adsorbent was then washed with 10 CV of PBS, pH 74, before the IgG was eluted with 5 CV of 50 mM sodium crtrate at pH 3 0
- the adsorbent then underwent a clean in place (CfP) with 5 CV of 0 5 M sodium hydroxide followed by re- equilibration of the adsorbent with 7 CV of PBS 5 pH 7 4
- Fractions (2 mL) were collected throughout the chromatography and analysed for IgG content (Protein A HPLC) DNA content (Picogreen analysis) and total protein (Bradford total protein assay)
- the breakthrough profile of IgG 1 for adsorbent Xl shows the binding capacity to be 21 8 g/L and the elut ⁇ on capacity to be 20
- Pepsin is a non-specific ⁇ ndopeptidase that is only active at acid pH and is irreversibly denatured at neutral or alkaline pH
- Pepsin digestion results in the generation of one F(ab') 2 fragment and severai small peptides of the Fc fragment Fragments o! human, ovsne and bovine polyclonal antibodies (mixed population of antibodies) were prepared by contacting the IgG with pepsin for 1 hour at 37 0 C at pH 40 The digestion was halted by adjusting the pH above 7 0, and the F(ab') 2 fragments were separated by ge! filtration
- adsorbent Xl The chromatographic performance of adsorbent Xl was investigated to assess the purification capability of the materia! for antibody fragments
- Experiments were completed using a 1 cm diameter column with a bed height of 2 5 cm and column volume (CV) of 2.0 mL with a linear flow rate of 50 cm/h (3 minute residence tsme)
- the adsorbent was initially equilibrated with 10 CV of phosphate buffered saline (PBS), pH 7 4. Approximately 20 mg of F(ab') 2 fragments were loaded per mL of adsorbent.
- PBS phosphate buffered saline
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Analytical Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Peptides Or Proteins (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
Abstract
Description
Claims
Priority Applications (9)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
BRPI0708451-0A BRPI0708451A2 (en) | 2006-03-02 | 2007-03-02 | adsorbents for protein purification |
CA2645675A CA2645675C (en) | 2006-03-02 | 2007-03-02 | Adsorbents for protein purification |
EP07712978.1A EP1989189B1 (en) | 2006-03-02 | 2007-03-02 | Adsorbents for protein purification |
DK07712978.1T DK1989189T3 (en) | 2006-03-02 | 2007-03-02 | Adsorbents for protein purification |
CN2007800118656A CN101415692B (en) | 2006-03-02 | 2007-03-02 | Adsorbents for protein purification |
AU2007220260A AU2007220260B2 (en) | 2006-03-02 | 2007-03-02 | Adsorbents for protein purification |
JP2008556860A JP5192398B2 (en) | 2006-03-02 | 2007-03-02 | Adsorbent for protein purification |
US12/281,346 US8076477B2 (en) | 2006-03-02 | 2007-03-02 | Adsorbents for protein purification |
ES07712978T ES2430556T3 (en) | 2006-03-02 | 2007-03-02 | Adsorbents for protein purification |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB0604236.0 | 2006-03-02 | ||
GBGB0604236.0A GB0604236D0 (en) | 2006-03-02 | 2006-03-02 | Adsorbents for protein purification |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2007099374A1 true WO2007099374A1 (en) | 2007-09-07 |
Family
ID=36219022
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/GB2007/050095 WO2007099374A1 (en) | 2006-03-02 | 2007-03-02 | Adsorbents for protein purification |
Country Status (12)
Country | Link |
---|---|
US (1) | US8076477B2 (en) |
EP (1) | EP1989189B1 (en) |
JP (1) | JP5192398B2 (en) |
CN (1) | CN101415692B (en) |
AU (1) | AU2007220260B2 (en) |
BR (1) | BRPI0708451A2 (en) |
CA (1) | CA2645675C (en) |
DK (1) | DK1989189T3 (en) |
ES (1) | ES2430556T3 (en) |
GB (1) | GB0604236D0 (en) |
PT (1) | PT1989189E (en) |
WO (1) | WO2007099374A1 (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2009138714A1 (en) * | 2008-05-16 | 2009-11-19 | Avecia Biologics Limited | Purification process for antibody fragments using derivatized triazines as affinity ligands |
US20120149873A1 (en) * | 2009-05-07 | 2012-06-14 | Novozymes Biopharma Dk A/S | Method for purifying albumin |
US8293738B2 (en) | 2010-05-12 | 2012-10-23 | Abbott Laboratories | Indazole inhibitors of kinase |
EP2918641A1 (en) | 2014-03-13 | 2015-09-16 | Basf Se | Method for purification of antibodies, antibody fragments or engineered variants thereof using specific anthraquinone dye-ligand structures |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2012018135A (en) * | 2010-07-09 | 2012-01-26 | Mitsubishi Chemicals Corp | Separating agent |
JP6038774B2 (en) * | 2011-03-24 | 2016-12-07 | 株式会社カネカ | Proteinaceous substance binding low molecular weight compound |
CN106925212A (en) * | 2015-12-31 | 2017-07-07 | 中国石油天然气股份有限公司 | A kind of adsorbent and method for removing oxazole from acrylonitrile |
CN108246273B (en) * | 2018-02-08 | 2021-01-22 | 天津大学 | Sulfonated sodium alginate grafted agarose gel chromatographic medium, preparation method and application |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1997010887A1 (en) * | 1995-09-20 | 1997-03-27 | Novo Nordisk A/S | Novel affinity ligands and their use |
WO2004035199A1 (en) * | 2002-10-21 | 2004-04-29 | Cambridge University Technical Services Limited | Affinity adsorbents for immunoglobulins |
Family Cites Families (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5338659A (en) * | 1991-04-02 | 1994-08-16 | Terrapin Technologies, Inc. | Method for determining analyte concentration by cross-reactivity profiling |
US6117996A (en) * | 1995-09-20 | 2000-09-12 | Novo Nordisk A/S | Triazine based ligands and use thereof |
GB9910807D0 (en) * | 1999-05-10 | 1999-07-07 | Prometic Biosciences Limited | Novel detoxification agents and their use |
WO2003050237A2 (en) * | 2001-12-12 | 2003-06-19 | New York University | Triazine library with linkers |
-
2006
- 2006-03-02 GB GBGB0604236.0A patent/GB0604236D0/en not_active Ceased
-
2007
- 2007-03-02 BR BRPI0708451-0A patent/BRPI0708451A2/en not_active Application Discontinuation
- 2007-03-02 WO PCT/GB2007/050095 patent/WO2007099374A1/en active Application Filing
- 2007-03-02 US US12/281,346 patent/US8076477B2/en not_active Expired - Fee Related
- 2007-03-02 DK DK07712978.1T patent/DK1989189T3/en active
- 2007-03-02 CA CA2645675A patent/CA2645675C/en active Active
- 2007-03-02 PT PT77129781T patent/PT1989189E/en unknown
- 2007-03-02 AU AU2007220260A patent/AU2007220260B2/en active Active
- 2007-03-02 ES ES07712978T patent/ES2430556T3/en active Active
- 2007-03-02 CN CN2007800118656A patent/CN101415692B/en active Active
- 2007-03-02 EP EP07712978.1A patent/EP1989189B1/en not_active Not-in-force
- 2007-03-02 JP JP2008556860A patent/JP5192398B2/en not_active Expired - Fee Related
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1997010887A1 (en) * | 1995-09-20 | 1997-03-27 | Novo Nordisk A/S | Novel affinity ligands and their use |
WO2004035199A1 (en) * | 2002-10-21 | 2004-04-29 | Cambridge University Technical Services Limited | Affinity adsorbents for immunoglobulins |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2009138714A1 (en) * | 2008-05-16 | 2009-11-19 | Avecia Biologics Limited | Purification process for antibody fragments using derivatized triazines as affinity ligands |
US20120149873A1 (en) * | 2009-05-07 | 2012-06-14 | Novozymes Biopharma Dk A/S | Method for purifying albumin |
US9403898B2 (en) * | 2009-05-07 | 2016-08-02 | Novozymes Biopharma Dk A/S | Method for purifying albumin |
US8293738B2 (en) | 2010-05-12 | 2012-10-23 | Abbott Laboratories | Indazole inhibitors of kinase |
EP2918641A1 (en) | 2014-03-13 | 2015-09-16 | Basf Se | Method for purification of antibodies, antibody fragments or engineered variants thereof using specific anthraquinone dye-ligand structures |
Also Published As
Publication number | Publication date |
---|---|
DK1989189T3 (en) | 2013-10-21 |
ES2430556T3 (en) | 2013-11-21 |
CA2645675C (en) | 2015-11-03 |
PT1989189E (en) | 2013-10-14 |
CN101415692A (en) | 2009-04-22 |
BRPI0708451A2 (en) | 2011-06-07 |
JP2009531653A (en) | 2009-09-03 |
JP5192398B2 (en) | 2013-05-08 |
US20090221801A1 (en) | 2009-09-03 |
US8076477B2 (en) | 2011-12-13 |
AU2007220260B2 (en) | 2011-06-09 |
CA2645675A1 (en) | 2007-09-07 |
EP1989189B1 (en) | 2013-07-10 |
EP1989189A1 (en) | 2008-11-12 |
CN101415692B (en) | 2013-10-02 |
AU2007220260A1 (en) | 2007-09-07 |
GB0604236D0 (en) | 2006-04-12 |
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