WO2007099374A1 - Adsorbents for protein purification - Google Patents

Adsorbents for protein purification Download PDF

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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
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WIPO (PCT)
Prior art keywords
use according
adsorbent
formula
aryl
halogen
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PCT/GB2007/050095
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French (fr)
Inventor
Jason Richard Betley
Helen Tatton
Kelly Le Riche
Matthew Webb
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Prometic Biosciences Ltd
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Application filed by Prometic Biosciences Ltd filed Critical Prometic Biosciences Ltd
Priority to BRPI0708451-0A priority Critical patent/BRPI0708451A2/en
Priority to CA2645675A priority patent/CA2645675C/en
Priority to EP07712978.1A priority patent/EP1989189B1/en
Priority to DK07712978.1T priority patent/DK1989189T3/en
Priority to CN2007800118656A priority patent/CN101415692B/en
Priority to AU2007220260A priority patent/AU2007220260B2/en
Priority to JP2008556860A priority patent/JP5192398B2/en
Priority to US12/281,346 priority patent/US8076477B2/en
Priority to ES07712978T priority patent/ES2430556T3/en
Publication of WO2007099374A1 publication Critical patent/WO2007099374A1/en

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    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07DHETEROCYCLIC COMPOUNDS
    • C07D251/00Heterocyclic compounds containing 1,3,5-triazine rings
    • C07D251/02Heterocyclic compounds containing 1,3,5-triazine rings not condensed with other rings
    • C07D251/12Heterocyclic 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
    • C07D251/26Heterocyclic 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
    • C07D251/40Nitrogen atoms
    • C07D251/48Two nitrogen atoms
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D15/00Separating processes involving the treatment of liquids with solid sorbents; Apparatus therefor
    • B01D15/08Selective adsorption, e.g. chromatography
    • B01D15/26Selective adsorption, e.g. chromatography characterised by the separation mechanism
    • B01D15/38Selective adsorption, e.g. chromatography characterised by the separation mechanism involving specific interaction not covered by one or more of groups B01D15/265 - B01D15/36
    • B01D15/3804Affinity 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
    • 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
    • B01J20/32Impregnating 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
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10TTECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T436/00Chemistry: analytical and immunological testing
    • Y10T436/25Chemistry: analytical and immunological testing including sample preparation
    • Y10T436/25375Liberation or purification of sample or separation of material from a sample [e.g., filtering, centrifuging, etc.]
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10TTECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T436/00Chemistry: analytical and immunological testing
    • Y10T436/25Chemistry: analytical and immunological testing including sample preparation
    • Y10T436/25375Liberation or purification of sample or separation of material from a sample [e.g., filtering, centrifuging, etc.]
    • Y10T436/255Liberation 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

Use of an affinity adsorbent for the separation, removal, isolation, purification, characterisation, identification or quantification of a proteinaceous material, wherein the affinity adsorbent is a compound of formula (III). wherein R1 is H, alkyl, aryl, hydroxyalkyl, cyciohexyl, amino or a heterocyclic group which is optionally substituted with one or more of alkyl, aryl, alkoxy, aryloxy, acyloxy, acylamino, amino, OH, CO2H, sulphonyl, carbamoyl, sulphamoyl, alkylsuiphonyl and halogen; one X is N and the other is N, C-CI or C-CN; Y is O, S or NR2; Z is O, S or NR3; R2 and R3 are each H, alkyl, hydroxyalkyl, benzyl or β-phenylethyl; Q is benzene, naphthalene, benzthiazole, benzoxazole, 1-phenylpyrazole, indazoie or benzimidazoie; R4, R5 and R6 are each H, OH, alkyl, aryl, heterocyclic, alkoxy, aryloxy, amino, acyloxy, acylamino, CO2H, sulphonic acid, carbamoyl, suiphamoyl, atkylsulphonyl or halogen, or two or more of R4, R5 and R6 are linked to form a cyclic structure; U and V are the same or different C1-10 straight-chain alkylene groups optionally substituted by one or more of hydroxyl, alkyl, aryl, hydroxyl, alkyl, β-phenylethyl and halogen; and A is a support matrix optionally linked to the X-containing ring by a spacer.

Description

ADSORBENTS FOR PROTEIN PURIFICATION Field of the Invention
This invention relates to compounds and their use as affinity ligands for protein purification. Background of the Invention
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. There are five different types o! heavy chain (y, μ, α3 ε and δ) that distinguish the immunoglobulin classes (IgG, IgM, IgA, IgD and IgE, respectively). There are also two different types of light chain (A and K) resulting from different gene products.
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.
Monoclonal antibodies (herein termed Mabs) are antibodies that have identical specificity towards a single antigen and are generated from a cell line that has been produced from a single cloned cell. Mabs constitute the fastest growing sector in the biopharmaceutical industry where is it estimated that sales will reach $30 billion (US) by 2010. Antibody litres from mammalian cell cultures have continued to improve over the last 20 years and aiternative downstream processes and chromatography adsorbents are required to resolve the process bottlenecks in the processing of Mabs.
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. There are several types of antibody fragments that are either lgG! domains prepared by specific endopeptidase enzyme digestion or that have been genetically engineered in cell lines. These include monovalent fragments such as Fab', Fab and scFv; bivalent fragments such as F(ab!)2 diabodies and msntbodies; and multivalent fragments such as triabodies and fetrabodies.
Many antibody fragment products are in devefopment for use as therapeutics or in diagnostics. Recombinant antibody fragments are expected to have a significant share of the $6 billion (US) per year diagnostic market, from in vitro immunoassays to in vivo tumour and clot imaging applications (Hoiiiger, P., & Hudson P.J., Nat. Biotech 23 (9; 2005) 1126- Most antibody fragment products iack a protein A-bϊnding site and therefore, unlike full-chain antibodies, cannot be purified by protein A affinity chromatography. In most instances, conventional chromatography techniques are used to purify antibody fragments. Protein L5 a protein with a molecular weight of 35000 Daltons derived from a bacterial species of Peptostreptococcus magnυs, 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
Figure imgf000003_0001
wherein R1 is H, alky!, hydroxyalkyl, cyclohexyl, NH2, phenyl, naphthyl, 1-ρhenylpyrazole, indazoie, benzthiazole, benzoxazole or benzimidazote, any of which aromatic groups can be substituted with one or more of aikyl, alkoxy, acytoxy, acylamino, amino, NH2, OH, CO2H, 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 NR2;
Z is O, S or NR3;
R2 and R3 are each H1 alkyi, hydroxyaikyl, benzyl or β-phenylethyl;
Q is benzene, naphthalene, benzthiazole, benzoxazoie, 1 -phenylpyrazoie, indazoie or benzimidazole;
R4, R5 and R6 are each H, OH, alky!, alkoxy, amino, NH2, acyloxy, acylamino, CO2H, 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 of related structure are disclosed in WO00/67900 and WO03/097112. They have affinity for endotoxins. Certain trϊazine-based compounds disclosed in WG97/1Q887 have affinity for immunoglobulins. An example of a compound showing such affinity is a compound of structure !!
Figure imgf000004_0001
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.
Summary of the Invention
Surprisingly, it has been found that certain compounds, many of which are novel, are useful for affinity-based purification of immunoglobulins, including but not limited to monoclonal antibodies and antibody fragments, even in the presence of compounds such as Piuronic F-68. Compounds for use in the invention are of formula I!!:
/5
Figure imgf000004_0002
wherein 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, CO2H, 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 NR25
Z is O, S or NR3,
R2 and R3 are each H, aikyi, hydroxyalkyi, benzyl or β-phenylethyi; Q is benzene, naphthalene, benzthiazole, benzoxazole, 1-phenyIpyrazoie, indazole or benzimidazole,
R4, R5 and Rs are each H, OH, alkyi, aryi, heterocyclic alkoxy, aryloxy, amino, acyloxy, acySamsno, CO2H, sulphonic acsd, carbamoyl, suiphamoyi, alkylsuSpnonyi or halogen, or two or more of R4, R5 and R6 are linked to form a cyclic structure, U and V are the same or different C-i 10 straight-chain aϊkyiene groups optionally substituted by one or more of hydroxy!, alky!, aryl, hydroxyaikyl, β-phenylethyl and halogen such as CHOH, and
A is a support matrix optionally linked to the X-containing ring by a spacer
Further compounds of the invention include the corresponding ligands, in whsch A is replaced by a functional group, linked dfrectSy or indirectly to the tπazsne ring, which can be immobilised on a support matπx The terms isgand" and "adsorbent" may be used interchangeably, below Description of the Invention
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
In compounds for use m the invention, rt is preferred that R and/or QR4R5R6 is or includes a cyclic structure, erther or each cyclic structure preferably has a OH or SO3H substituenf Preferably, each X ss N Further it is preferred that U and/or V 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:
Figure imgf000006_0001
Figure imgf000007_0001
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.
The term "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 Thus, 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. Examples of support matrix and optional linker A 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 The following Examples illustrate the invention
Example 1 - Synthesis of Adsorbents
The synthesis of adsorbents of the type described is explained in WO97/10887, WO00/67900 and WG003/097112 The synthesis of Adsorbent Xf
Figure imgf000008_0001
described and is typical 6% cross-linked PuraBead agarose gel (650 g settled in RO water) was slurried with
RO water (650 mL), 10 M sodium hydroxide (NaOH) {88 ml), and epichSorohydnn (124 ml), The slurry was stirred over 19 hours Further 10 M sodium hydroxide (NaOH) (22 mL), and epichlorohydrsn (37 mL) was then added and the slurry stirred over 1.5 hours. After a sample was taken for analysis, the slurry was filtered then washed with RO water (12 x 1 L) Analysis for epoxy groups showed that the gel was deπvatised with 21 6 μmoi epoxy groups per g of settled gel
The gel was drained before RO water (780 mL) and 0.88 specific gravity ammonia solution (200 mL) were added The mixture was stirred and heated to 400C, then stirred at this temperature over 18 hours After a sample was taken for analysis, the slurry was filtered and then washed with 12 x 1 L RO water (12 x 1 L) TNBS analysis for amine groups showed that the ges was deπvatised with 20 8 μmol amine groups per g of settled gel Settled aminated gel (475 g) was slurried in 1 M potassium phosphate (475 ml_) and allowed to settle. 1 M potassium phosphate (140 mL) was then added, the mixture stirred vigorously, and acetone (70 mL) added. The mixture was cooled to O0C in an ice sail bath, before cyanuric chloride (11.9 g) in cold acetone (120 mL) was added in one portion The siurry was stirred over 1 hour at 0-40C, before being drained, then washed wrth 50% v/v aqueous acetone (5 x 500 mL), RO water (5 x 500 mL)3 with 50% v/v aqueous acetone (5 x 500 ml), and RO water (1O x 500 mL). Analysis revealed the attachment of 25 μmol dichlorotriazine groups per g of settled gei
The dichlorotπazinyl agarose (50 g) was slurried in RO water (55 mL) NorphenySephπne hydrochloride (1.99 g) was dissolved in RO water (15 mL), 10 M NaOH (0.95 mL) was added, and the mixture was cooled on see, prior Io addition to the dichlorotπaztnyi agarose. The mixture was reacted at 6θ'C over 19 hours. 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
Chromatography experiments were performed wrth each of the adsorbents tabulated in Table 1. For all experiments a 1 cm diameter column was used with a bed height of 5 5 cm and column volume (CV) of 4.3 mL with a linear flow rate of 300 cm/h. 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 Plurømc F-68, and other proteins to mimic eel culture supernatant) or 2 (1 g/L !gG, 1 g/L Pluronsc F-8Θ 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-equslιbratιon of the adsorbent with 7 CV of PBS, pH 7 4
Subsequent to the chromatography experiment, the IgG content of the ioad, post- load wash, elution and CIP fractions were assessed by nephelometry, A280, HPLC or GPC, to assess the binding and etuison capacities and SDS PAGE analysis to assess purity The biπdmg and elutson capacities are summarised in Table 1
Pure IgG feed contained 1 g/L of polyclonal IgG sn PBS, pH 7 4 m the presence or absence of 1 g/L Pluroπic 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 Pluroπic 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 cuϊture medium Table 1
Figure imgf000010_0001
ESution buffer 50 mM citric acid, pH 3.5 with 30% ethylene glycol and 2 M NaCi.
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! 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 PBS5 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 IgG1 for adsorbent Xl shows the binding capacity to be 21 8 g/L and the elutϊon capacity to be 20 9 g/L Using gel permeation chromatography, the pυπty of the eluted IgG was determined to be 92.8% and adsorbent Xl has a 2 log clearance of DNA
Chromatography experiments were completed with adsorbent XS using antibody fragments prepared by enzyme (pepsin) digestion Pepsin is a non-specific βndopeptidase 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 370C 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
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. The adsorbent was then washed with 10 CV of PBS, pH 7 4, before the fragments were eiuted with 5 CV of 50 mM sodium citrate at pH 3 0 The adsorbent then underwent a clean in place (CiP) with 5 CV of 0 5 M sodtunn hydroxide followed by re-equilibration of the adsorbent with 7 CV of PBS, pH 7 4 The controS for all experiments was Protein L adsorbent fusing the same experimental conditions as for adsorbent Xl) Each fraction from the chromatography column was collected and analysed ussng Western blot techniques This technique indicated that adsorbent Xl bound both hunan kappa and lambda iight chasn and ovine and bovsne F(ab')2 fragments, protein L b^nds only human kappa light chain and does not tand ovine and bovine fragments

Claims

1. Use of an affinity adsorbent for the separation, removal, isolation, purification, characterisation, identification or quantification of a proteinaceous material, wherein the affinity adsorbent is a com ound of formula III
Figure imgf000012_0001
wherein R1 is H, alky!, aryl, hydroxyalky!, cyclohexyi, amino or a heterocyclic group which is optionally substituted with one or more of alkyl, aryl, alkoxy, aryloxy, acyloxy, acylamino, amino, OH, GC^H, sulphonyl, carbamoyl, sulphamoyi, alkyisuSphonyl and halogen; one X is N and the other is N, C-C! or C-CN;
Y is O, S or NR2; Z is O, S or NR3;
R2 and R3 are each H, alkyl, hydroxyalkyl, benzyl or β-phenylethyl; Q is benzene, naphthalene, benzthiazole, benzoxazole, 1-phenyipyrazote, indazole or Denzimidazole;
R4, R5 and Re are each H, OH, aikyl, aryl, heterocyclic, alkoxy, aryloxy, amino, acyloxy, acylamino, CO2H, suiphonic acid, carbamoyl, sulphamoyi, alkylsulphonyi or halogen, or two or more of R4, R5 and R6 are linked to form a cyclic structure;
U and V are the same or different C1-I 0 straight-chain aikylene groups optionally substituted by one or more of hydroxy!, alky!, aryl, hydroxyalkyl, β-phenySethyl and halogen; and
A is a support matrix optionally linked to the X-containing ring by a spacer. 2. Use according to claim 1 , wherein R1 and/or QR4R5R6 is or includes a cyclic structure. 3. Use according to ciaim 2, wherein either or each cyclic structure has a OH or SO3H substituent.
4. Use according to any preceding ciasm, wherein either or each of U and V is CHOH.
5. Use according to any preceding ciaim, wherein each X is N,
6. Use according to ciaim 1 , wheresn the adsorbent is of formula 111 1. Use according to claim 1 , wherein the adsorbent ss of formula IV.
8. Use according to claim 1 , wherein the adsorbent is of formula V.
9. Use according to claim 1 , wherein the adsorbent is of formula V!.
10. Use according to claim 1, wherein the adsorbent is of formula VlI.
1 1. Use according to claim 1, wherein the adsorbent is of formula VHI. 12. Use according to claim 1, wherein the adsorbent is of formula IX.
13. Use according to ciaim 1 , wherein the adsorbent is of formula X.
14. Use according to claim 1, wherein the adsorbent is of formula XL
15. Use according to any preceding claim, wherein the proteinaceous material is an immunoglobulin, immunoglobulin fragment or protein. 16. Use according to claim 15, wherein the material is a monoclonal antibody.
17. Use according to claim 15, wherein the material is an immunoglobulin f ragmen! selected from Fab, Fab', F(ab')2, scFV, diabody, minibody, tribody and tetrabody fragments.
18. Use according to any preceding claim, wherein the proteinaceous material is in cell culture. 19. Use according to any preceding ciaim, wherein the proteinaceous materia! is in combination with an anti-foaming agent.
20. Use according to claim 19, wherein the anti-foaming agent is a block copolymer of polyoxyethylene and polyoxypropyiene.
21. A compound of formula II! as defined in any of claims 1 to 14, wherein U and/or V is substituted.
22. A compound according to ciaim 21 , wherein the substitueπt is OH1 aryi or halogen,
23. A compound according to claim 21 , wherein U and/or V is CHOH.
PCT/GB2007/050095 2006-03-02 2007-03-02 Adsorbents for protein purification WO2007099374A1 (en)

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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

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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
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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

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