WO1995031279A1 - Chromatography adsorbents utilizing mercapto heterocyclic ligands - Google Patents

Chromatography adsorbents utilizing mercapto heterocyclic ligands Download PDF

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Publication number
WO1995031279A1
WO1995031279A1 PCT/US1995/006014 US9506014W WO9531279A1 WO 1995031279 A1 WO1995031279 A1 WO 1995031279A1 US 9506014 W US9506014 W US 9506014W WO 9531279 A1 WO9531279 A1 WO 9531279A1
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Prior art keywords
ligand
group
solid support
support material
chromatography adsorbent
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PCT/US1995/006014
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French (fr)
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Alexander Schwarz
Meir Wilchek
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Biosepra Inc.
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Application filed by Biosepra Inc. filed Critical Biosepra Inc.
Priority to EP95919182A priority Critical patent/EP0764048B1/en
Priority to DE69531826T priority patent/DE69531826T2/en
Priority to CA002190379A priority patent/CA2190379C/en
Priority to AU25143/95A priority patent/AU681035B2/en
Priority to JP52981295A priority patent/JP3844496B2/en
Priority to AT95919182T priority patent/ATE250457T1/en
Publication of WO1995031279A1 publication Critical patent/WO1995031279A1/en

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    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/30Processes for preparing, regenerating, or reactivating
    • B01J20/32Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating
    • B01J20/3202Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating characterised by the carrier, support or substrate used for impregnation or coating
    • B01J20/3204Inorganic carriers, supports or substrates
    • BPERFORMING OPERATIONS; TRANSPORTING
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    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/28Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
    • B01J20/28002Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their physical properties
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    • B01J20/28014Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their form
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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    • 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
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    • B01J20/30Processes for preparing, regenerating, or reactivating
    • B01J20/3092Packing of a container, e.g. packing a cartridge or column
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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    • B01J20/30Processes for preparing, regenerating, or reactivating
    • B01J20/32Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating
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    • B01J20/3206Organic carriers, supports or substrates
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    • B01J20/30Processes for preparing, regenerating, or reactivating
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    • B01J20/3206Organic carriers, supports or substrates
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    • B01J20/3212Polymeric carriers, supports or substrates consisting of a polymer obtained by reactions otherwise than involving only carbon to carbon unsaturated bonds
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    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/30Processes for preparing, regenerating, or reactivating
    • B01J20/32Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating
    • B01J20/3214Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating characterised by the method for obtaining this coating or impregnating
    • B01J20/3217Resulting in a chemical bond between the coating or impregnating layer and the carrier, support or substrate, e.g. a covalent bond
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/30Processes for preparing, regenerating, or reactivating
    • B01J20/32Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating
    • B01J20/3214Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating characterised by the method for obtaining this coating or impregnating
    • B01J20/3217Resulting in a chemical bond between the coating or impregnating layer and the carrier, support or substrate, e.g. a covalent bond
    • B01J20/3219Resulting in a chemical bond between the coating or impregnating layer and the carrier, support or substrate, e.g. a covalent bond involving a particular spacer or linking group, e.g. for attaching an active group
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/30Processes for preparing, regenerating, or reactivating
    • B01J20/32Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating
    • B01J20/3231Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating characterised by the coating or impregnating layer
    • B01J20/3242Layers with a functional group, e.g. an affinity material, a ligand, a reactant or a complexing group
    • B01J20/3244Non-macromolecular compounds
    • B01J20/3246Non-macromolecular compounds having a well defined chemical structure
    • B01J20/3248Non-macromolecular compounds having a well defined chemical structure the functional group or the linking, spacer or anchoring group as a whole comprising at least one type of heteroatom selected from a nitrogen, oxygen or sulfur, these atoms not being part of the carrier as such
    • 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
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07KPEPTIDES
    • C07K1/00General methods for the preparation of peptides, i.e. processes for the organic chemical preparation of peptides or proteins of any length
    • C07K1/14Extraction; Separation; Purification
    • C07K1/16Extraction; Separation; Purification by chromatography
    • C07K1/22Affinity chromatography or related techniques based upon selective absorption processes
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07KPEPTIDES
    • C07K16/00Immunoglobulins [IGs], e.g. monoclonal or polyclonal antibodies
    • C07K16/06Immunoglobulins [IGs], e.g. monoclonal or polyclonal antibodies from serum
    • C07K16/065Purification, fragmentation
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2220/00Aspects relating to sorbent materials
    • B01J2220/40Aspects relating to the composition of sorbent or filter aid materials
    • B01J2220/46Materials comprising a mixture of inorganic and organic materials
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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    • B01J2220/00Aspects relating to sorbent materials
    • B01J2220/50Aspects relating to the use of sorbent or filter aid materials
    • B01J2220/54Sorbents specially adapted for analytical or investigative chromatography
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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    • B01J2220/00Aspects relating to sorbent materials
    • B01J2220/50Aspects relating to the use of sorbent or filter aid materials
    • B01J2220/58Use in a single column

Definitions

  • the present invention relates generally to affinity chromatography and more particularly to pseudobioaffinity chromatography.
  • liquid chromatography adsorbents such as ion exchangers, hydrophobic supports, hydroxy apatite and gel filtration media.
  • Affinity chromatography which relies on specific interactions between an immobilized ligand and a particular molecule sought to be purified, is another well- known, existing technique used to purify antibodies from solution.
  • Protein A which is derived from the bacterium Staphylococcus aureus, has a strong and specific affinity for the Fc fragment of IgG antibodies and has been used for approximately one decade as an affinity ligand for purifying IgG antibodies.
  • Protein A can be immobilized on a large variety of solid support materials, such as chromatographic beads and membranes, and can be used to obtain high purity antibodies in high
  • Protein A suffers from a number of limitations as an affinity
  • proteases that are commonly present in the same biological fluids (e.g., sera, ascitic fluids, milk, hybridoma cell culture supernatants, and the like) in which the antibodies being sought to be purified by affinity chromatography are also present.
  • This sensitivity of Protein A to such proteases often leads to one or both of the following effects: (1) The recognition of Protein A towards the Fc fragments of IgG is progressively reduced; and (2) Fragments of Protein A generated by protease action contaminate otherwise pure antibody preparations.
  • Protein A is possible for Protein A to be released intact from its associated solid support material, thereby contaminating antibody preparations brought into contact therewith. The contamination of therapeutic antibody preparations with traces of Protein A or Protein A fragments
  • Protein A is very serious not only because Protein A and/or Protein A fragments are capable of provoking an antigenic response in humans but also because Protein A is known as a potent mitogen.
  • Protein A is not the only protein which has been used as an affinity ligand for the purification of a class of antibodies.
  • Protein G has similarly been used as an affinity ligand. See Bjorck et al., J. Immunol., 133:969 (1984). Protein G also interacts with the Fc fragment of immunoglobulins and is particularly effective in isolating mouse IgG antibodies of class 1 (as contrasted with Protein A which is not very effective in isolating these antibodies). Protein G, however, suffers from the same types of limitations discussed above in connection with Protein A.
  • Protein L from Peptostreptococcus magnus. Protein L, as contrasted with Protein A and Protein G, interacts specifically with the light chains of IgG antibodies without interfering with their antigen binding sites.
  • Protein L This specificity permits Protein L to complex not only with antibodies of the IgG class but also with antibodies of the IgA and IgM classes. Despite its broad affinity, Protein L suffers from the same limitations described above in connection with Proteins A and G.
  • Proteins A, G and L are all sensitive to a number of chemical and physical agents (e.g., extreme pH, detergents, chaotropics, high temperature) which are frequently used to clean affinity chromatography columns between runs. Consequently, some people have chosen to minimize the number of cleaning cycles applied to the above-described columns so as to correspondingly minimize degradation thereto.
  • chemical and physical agents e.g., extreme pH, detergents, chaotropics, high temperature
  • Anti-antibodies represent still another type of affinity ligand used for gamma globulin purification. Anti-antibodies, however, are limited in use due to their high cost and very limited stability.
  • Thiophilic compounds represent another class of pseudobioaffinity ligands.
  • An adsorbent utilizing one type of thiophilic compound is disclosed by Porath et al. in FEBS Lett, 185:306 (1985), which is incorporated herein by reference. This type of adsorbent is produced by reacting either a hydroxyl- or thiol-containing support first with divinyl sulfone and then with mercaptoethanol.
  • the aforementioned adsorbent utilizes a salt-promoted approach to adsorb immunoglobulins. Elution of adsorbed immunoglobulins is effected by decreasing salt concentration and/or by modifying pH.
  • pseudobioaffinity adsorbent capable of adsorbing antibodies utilizes mercaptopyridine as its ligand. See Oscarsson et al., "Protein Chromatography with Pyridine- and Alkyl-Thioether-Based Agarose Adsorbents," Journal of Chromatography, 499:235-247 (1990), which is incorporated herein by reference.
  • This type of adsorbent is generated, for example, by reacting mercaptopyridine with a properly activated solid support. The adsorbent thus formed is capable of adsorbing antibodies under high salt conditions.
  • thiophilic adsorbents provide a generally satisfactory means for purifying antibodies; however, in those cases in which the initial biological liquid is a protein rich solution, such as a serum or ascites, the non ⁇ specific binding by such adsorbents of a number of proteins other than the desired antibodies can be a problem. This problem of non-specific binding is the primary limitation of these thiophilic adsorbents.
  • Another group of low molecular weight ligands capable of selectively binding antibodies includes pentafluoropyridine and N-dimethylaminopyridine reacted with ethylene glycol, glycine or mercaptoethanol. See Ngo, J. Chromatogr., 510:281 (1990), which is incorporated herein by reference. Adsorbents utilizing these materials can be used to isolate immunoglobulins in either high salt or low salt buffers or to isolate other types of proteins under low salt conditions. Elution of
  • adsorbed proteins can be obtained by lowering pH. Still other low molecular weight pseudobioaffinity ligands have been
  • ligands are special dyes. Elution of the bound antibodies from the ligands is achieved by special dispiacers.
  • pseudobioaffinity ligands are very attractive in terms of their low cost and their chemical and physical stability. However, their level of non-specific binding and/or their toxicity (should they, for example, contaminate a therapeutic antibody preparation intended for administration to humans) are too high, and their capacity for antibodies is too low to counterbalance the attractiveness of adsorbents utilizing Proteins A, G or L as specific antibody ligands.
  • a pseudobioaffinity chromatography adsorbent adapted for use in selectively adsorbing immunoglobulins is hereinafter provided, the adsorbent comprising in a first embodiment: (a) a solid support material; and (b) a ligand
  • said ligand being a compound of the formula
  • each of X 1 f X 2 and X 3 is selected from the group consisting of S, SCH 3 + ,
  • Y 1 is selected from the group consisting of S, SCH 3 + , O, NH, NCH 3 , CH 2 and CR 1 R 2 wherein at least one of R and R 2 is not hydrogen; wherein each of Y 2 ,
  • Y 3 and Y 4 is selected from the group consisting of N, NCH 3 + , CH, and CR wherein
  • R is not hydrogen; and wherein at least two of Y.,, Y 2 , Y 3 and Y 4 are neither CH 2 ,
  • the present invention is also directed to methods of making the aforementioned adsorbents and to methods of using the aforementioned adsorbents to perform affinity separations.
  • the present invention is directed to novel pseudobioaffinity chromatography adsorbents useful in the selective adsorption of a wide of range of
  • the adsorbents of the present invention may also be used to selectively adsorb non-immunoglobulin proteins.
  • the pseudobioaffinity chromatography adsorbents comprise (a) a solid support material; and (b) a ligand immobilized on the surface of the solid support material, the ligand being a mercapto five-membered heterocyclic ring of the type hereinafter described.
  • said ligand has the structure represented below by compound I.
  • each of X 1 f X 2 and X 3 is selected from the group consisting of S, SCH 3 + , O, NH, NCH 3 , CH 2 and CR 1 R 2 wherein at least one of R 1 and R 2 is not hydrogen; wherein X 4 is selected from the group consisting of N, NCH 3 + , CH and CR wherein R is not hydrogen; and wherein at least two of X ⁇ X 2 , X 3 and X 4 are neither CH 2 , CH, CR nor CR.R.,.
  • R, R ⁇ and R 2 can be virtually any functional group.
  • R, R., and R 2 for illustrative purposes only, include substituted or unsubstituted alkyl, aryl, alkenyl, alkynyl, aralkyl, acyl, cycloalkyl, carboxyl, amino, aryloxy or alkoxy, halo, hydroxy, nitro, O, S, cyano or any of the functional groups disclosed in U.S. Patent Nos. 4,223,036, 4,835,161 and 4,699,904, all of which are incorporated herein by reference.
  • R 2 of compound I may be either the same or different for two or more of X 1 ( X 2 and X 3 .
  • R ⁇ and R 2 could be H and methyl, respectively, for
  • R ⁇ and R 2 could be, for example, ethyl and OH, respectively, for both X 1 and X 2 .
  • compound I examples include mercaptothiazoline (e.g., 2- mercaptothiazoline) and 2-mercapto-5-thiazolidone.
  • said ligand has the structure represented below by compound II.
  • Y 1 is selected from the group consisting of S, SCH 3 + , O, NH, NCH 3 , CH 2 and CR ⁇ wherein at least one of R, and R 2 is not hydrogen; wherein each of Y 2 , Y 3 and Y 4 is selected from the group consisting of N, NCH 3 + , CH, and CR wherein R is not hydrogen; and wherein at least two of Y 1 f Y 2 , Y 3 and Y 4 are neither CH 2 , CH, CR nor CR 1 R 2 .
  • R, R 1 and R 2 of compound II can be virtually any functional group. Examples
  • R, R ⁇ and R 2 for illustrative purposes only, include substituted or unsubstituted alkyl, aryl, alkenyl, alkynyl, aralkyl, acyl, cycloalkyl, carboxyl, amino, aryloxy or alkoxy, halo, hydroxy, nitro, O, S, cyano or any of the functional groups disclosed in U.S. Patent Nos. 4,223,036, 4,835,161 and 4,699,904, all of which are incorporated herein by reference.
  • CR of compound II may be either the same or different for two or more of Y 2 , Y 3 and Y 4 .
  • R could be methyl in the case of Y 2 and OH in the case of
  • R could be, for example, ethyl for both Y 2 and Y 3 .
  • compound II examples include mercaptoimidazole (e.g., 2- mercaptoimidazole), mercaptoimidazoline, mercaptothiazole (e.g., 2- mercaptothiazole), mercaptotriazole (e.g., 3-mercapto-1 ,2,4-triazole and 5-
  • mercapto-1 ,2,3-triazole mercaptotetrazole
  • mercaptotetrazole e.g., 5-mercapto-1 ,2,3,4-tetrazole
  • mercaptoth iad iazole e. g . , 2-mercapto- 1 , 3 ,4-th iad iazole
  • mercaptomethylimidazole e.g., N-methyl-2-mercaptoimidazole - a pharmaceutical known to be safe to humans.
  • the solid support material of the present adsorbents may be composed of polysaccharides, such as cellulose, starch, dextran, agar or agarose, or hydrophilic synthetic polymers, such as substituted or unsubstituted polyacrylamides, polymethacryiamides, polyacrylates, poiymethacryiates, polyvinyl hydrophilic polymers, polystyrene, polysulfone or the like.
  • suitable materials for use as the solid support material include porous mineral materials, such as silica, alumina, titania oxide, zirconia oxide and other ceramic structures.
  • composite materials may be used as the solid support material.
  • Such composite materials may be formed by the copolymerization of or by an interpenetrated network of two or more of the above mentioned entities.
  • suitable composite materials include polysaccharide-synthetic polymers and/or polysaccharide-mineral structures and/or synthetic polymer-mineral structures, such as are disclosed in U.S. Patent Nos. 5,268,097, 5,234,991 and 5,075,371 , all of which are incorporated herein by
  • the solid support material of the present invention may take the form of beads or irregular particles ranging in size from about 0.1 mm to 1000 mm in diameter, fibers (hollow or otherwise) of any size, membranes, flat surfaces ranging in thickness from about 0.1 mm to 1 mm thick and sponge-like materials with holes from a few /m to several mm in diameter.
  • the ligands described above are chemically immobilized on the solid support material via a covalent bond formed between the mercapto group of the ligand and a reactive group present on the solid support.
  • Reactive groups capable of reacting with the mercapto group of the present ligand include epoxy groups, tosylates, tresylates, halides and vinyl groups. Because many of the aforementioned solid support materials do not include one of the reactive groups recited above, bifunctional activating agents capable of both reacting with the solid support materials and providing the necessary reactive groups may be used.
  • activating agents include epichlorhydrin, epibromhydrin, dibromo- and dichloropropanol, dibromobutane, ethyleneglycol diglycidylether, butanediol diglycidylether, divinyl sulfone and the like.
  • concentration of the activating agent By varying the concentration of the activating agent, the amount of immobilized ligand of the present invention can vary anywhere between a fraction of a //mole and several hundred //moles per ml of solid matrix.
  • ligand per unit volume results in a low separation capacity for immunoglobulins whereas a large quantity of ligand per unit volume results in an increased sorption capacity for immunoglobulins (and can induce nonspecific binding of proteins other than immunoglobulins).
  • the activating agents listed above have different chain lengths. Accordingly, by selecting a particular activating agent, one can control the distance between the solid support material and the immobilized ligand. Due to steric constraints, this
  • Preparation of the adsorbents of the present invention may be effected in a manner similar to that by which conventional adsorbents have typically been prepared. More specifically, this may be done by reacting a solid support material of the type described above with an activating agent of the type described above under established conditions of concentration, temperature, pH, medium composition and time. Once activated, the support is then washed extensively in the established manner with solvents used to remove excess activating agent and/or activation byproducts therefrom. The washed, activated support is then contacted with ligands of the type described above under established conditions of concentration, pH, reaction temperature, reaction medium, time and agitation to produce an adsorbent which selectively adsorbs immunoglobulins from biological
  • the adsorbents of the present invention may be used in the same manner that conventional adsorbents have been used. This comprises introducing the adsorbent into a chromatographic column and then washing the column with an appropriate aqueous solution of salts at a given pH. A biological solution containing the immunoglobulins wished to be
  • salts e.g., Na 2 S0 4
  • the immunoglobulins present in the solution are captured by the adsorbent whereas the non-immunoglobulin proteins present in the solution and the remainder of the solution are recovered in the flowthrough.
  • the immunoglobulins are then desorbed by a pH shift and/or by changing the salt concentration.
  • the isolated immunoglobulins are then neutralized.
  • adsorbents of the present invention do not require that salt be added to the biological solution for the antibodies contained therein to adsorb to the ligand. This elimination of the need for salt is clearly advantageous in those instances in which the addition of salt is undesirable.
  • Those adsorbents of the present invention for which salt need not be added (and, in fact, cannot be added in order for the adsorbent to function properly) are those which employ ligands of compounds I and II in which nitrogen atoms constitute the two or more heteroatoms of the five-membered heterocyclic ring.
  • Examples of such ligands include 2-mercaptoimidazole, 3-mercapto- 1 ,2,4- triazole, 5-mercapto-1 ,2,3-triazole, 5-mercapto-1 ,2,3,4-tetrazole and N-methyl-2- mercapto-imidazole.
  • the adsorbents of the present invention can be used to isolate a variety of different types of antibodies, such as native antibodies, chemically modified antibodies, bioengineered antibodies, antibody fragments and antibody conjugates containing enzymes, as well as various toxins, haptens and the like.
  • the adsorbents of the present invention can be used to isolate antibodies from a variety of different biological liquids, such as hybridoma cell culture supernatants, plasma and plasma fractions, milk and milk fractions, ascitic fluids, fermentation broths and the like.
  • the adsorbents of the present invention represent a significant advancement in the art over adsorbents utilizing antibody-specific proteins, such as Protein A, Protein G, Protein L and the like. This is, in part, because the present adsorbents are stable against biological degradation, particularly degradation by hydrolytic enzymes. In addition, many of the ligands of the present adsorbents are commercially available chemicals of a current cost significantly lower than protein-
  • the present adsorbents can be treated with strong acidic and alkaline solutions which would otherwise be inappropriate with adsorbents utilizing protein ligands.
  • the present adsorbents can be treated with other cleaning agents, such as detergents, chaotropic salts and the like, without running the risk of adsorbent degradation or inactivation.
  • heat treatment can be applied to the adsorbents of the present invention without modifying their capture efficiency or specificity.
  • the present adsorbents are more specific and/or show higher sorption capacity for antibodies.
  • the following examples are illustrative only and should in no way limit the scope of the present invention:
  • Example 1 Immobilization of 2-mercaptoimidazole on an epoxy-activated HyperD TM support 20 grams of epoxy-activated HyperD TM silica oxide/polystyrene composite support with functionalized hydrogel filled pores (commercially available from BioSepra, Inc., Marlborough, MA and described in U.S. Patent No. ' 5,268,097) were
  • a chromatographic assay was then performed on the above-described adsorbent using 10 mM HEPES at pH 7.5. 1.5 ml of human serum was diluted three times with HEPES buffer and passed through a column of 1.2 ml gel volume. Elution was performed by changing the pH to 3.5 with citric acid buffer. Electrophoretic analysis of the elution fractions collected revealed that immunoglobulins constituted the major part of the adsorbed proteins, and the purity of the immunoglobulins was judged to be greater than 75%.
  • the dynamic capacity of the modified gel by frontal analysis was 9.2 mg/ml at c/10 (i.e., 10% breakthrough) and 14.4 mg/ml at c/2 (i.e., 50% breakthrough) for human immunoglobulins at a flow rate of 120 cm/hr.
  • Example 2 Immobilization of 2-aminoimidazole on an epoxy-activated HyperD TM support An adsorbent similar to that synthesized in Example 1 was prepared, the only difference being that 2-aminoimidazole was substituted for 2- mercaptoimidazole. An evaluation of the dynamic capacity of the adsorbent was
  • 2-aminoimidazole adsorbent had a dynamic capacity of 1.5 mg/ml at c/10 and 2.5 mg/ml at c/2 for human immunoglobulins at a flow rate of 120 cm/hr.
  • Example 3 Immobilization of 2-mercaptothiazole on an epoxy-activated HyperD TM support An adsorbent similar to that synthesized in Example 1 was prepared, the only difference being that 2-mercaptothiazole was substituted for 2- mercaptoimidazole. A chromatographic assay was performed using 10 mM HEPES and 500 mM sodium sulfate at pH 7.5. 1.5 ml of human serum was passed through a column of 4.6 ml gel volume, and elution was performed by changing the pH to 3.5 with citric acid buffer.
  • Electrophoretic analysis of the elution fractions collected revealed that immunoglobulins constituted the major part of the adsorbed proteins, and the purity of the immunoglobulins was judged to be greater than 85%.
  • the capacity of the modified gel by frontal analysis was determined to be 6.2 mg/ml at c/10 and 7.9 mg/ml at c/2 at a flow rate of 120 cm/hr.
  • Example 4 Immobilization of 2-mercaptothiazoline on an epoxy-activated HyperD TM support An adsorbent similar to that synthesized in Example 1 was prepared, the
  • modified gel by frontal analysis was determined to be 6.2 mg/ml at c/10 and 7.7 mg/ml at c/2 at a flow rate of 120 cm/hr.
  • Example 5 lmmobilizationof3-mercapto-1,2,4-triazole on an epoxy-activated HyperD TM support An adsorbent similar to that synthesized in Example 1 was prepared, the only difference being that 3-mercapto-1 ,2,4-triazole was substituted for 2-
  • Example 2 An adsorbent similar to that synthesized in Example 1 was prepared, the only difference being that 2-mercapto-1 ,3,4-thiadiazole was substituted for 2- mercaptoimidazole. Using the same sort of assay described above in Example 1 ,
  • the capacity of the modified gel for pure human antibodies was determined by frontal analysis to be 9.1 mg/ml at c/10 and 11.2 mg/ml at c/2 at a flow rate of 140 cm/hr in an adsorption buffer containing 10 mM HEPES and 750 mM sodium sulfate at pH 7.
  • Example 7 Immobilization of 2-mercapto-5- thiazolidone on an epoxy-activated HyperD TM support An adsorbent similar to that synthesized in Example 1 was prepared, the
  • the capacity of the modified gel for pure human antibodies was determined by frontal analysis to be 9 mg/ml at c/10 and 12.2 mg/ml at c/2 at a flow rate of 134 cm/hr in an adsorption buffer containing 10 mM HEPES and 750 mM sodium sulfate at pH 7.
  • Example 8 Immobilization of 2-mercaptothiazoline on a vinyl-activated HyperD TM support 15 grams of amino-HyperD TM (prepared by amination by reacting the epoxy- activated HyperD TM of Example 1 with ethylene diamine) were suspended in 80 ml of a mixture containing 35% 100 mM carbonate buffer, pH 9.5, and 65% ethanol. To this slurry was added 7 ml of divinyl sulfone, and the slurry was shaken for 20 hours at 45°C. The slurry was filtered, washed with ethanol and dried.
  • the beads were resuspended in 75 ml of a mixture of 35% 50 ml carbonate buffer, pH 8.6, and 65% ethanol containing 5 mM 2-mercaptothiazoline and then shaken for 24 hours at 45°C.
  • the slurry was then filtered onto a sinter glass filter, washed with ethanol and dried.
  • the modified HyperD TM support was then resuspended in 100 ml of a solution containing 1 M ethanolamine, pH 10.5, shaken for 2.5 hours at
  • the capacity of the modified gel was determined by frontal analysis to be 11.8 mg/ml at c/10 and 14.4 mg/ml at c/2 at a flow rate of 120 cm/hr.
  • bromo-activated HyperD TM support 5 grams of bromo-activated HyperD TM were suspended in 25 ml of a mixture of 35% 50 mM carbonate buffer, pH 8.6, and 65% ethanol containing 600 mg of 2- mercaptothiazole. The slurry was rotated, head over head, for 20 hours at room temperature and then filtered onto a sinter glass filter, washed and drained. The slurry was then resuspended in an aqueous solution of 1 M ethanolamine at pH
  • Example 10 I mmobi lization of 2- mercaptothiazole on Epoxy- Sepharose CL-6B support
  • Epoxy-Sepharose CL-6B support epoxy-activated agarose beads
  • Eupergit ® support 20 g of Eupergit ® support (a copolymer of methacrylamide, N,N- methylenebis(methacrylamide) and a component containing an active oxirane group; commercially available from Rohm Pharma, Darmstadt, Germany) are suspended in 50 ml of 50% 50 mM carbonate buffer, pH 8.6, and 50% ethanol.
  • Epoxy-Fractogel support epoxy-activated polymethacrylate support; commercially available from E. Merck, Wakefield, Rl
  • 50 ml of 50% of 50 mM carbonate buffer, pH 8.6, and 50% ethanol To this suspension are added 50 ml of ethanol containing 5 mM of 2-mercapto-1 ,3,4-thiadiazole, and the slurry is shaken for 16 hours. The slurry is then filtered, washed with 50 mM carbonate buffer at pH 8.6/ethanol (1 :1) and drained under vacuum.
  • the modified support is then saturated with ethanolamine as described in Example 1 and tested for its ability to separate antibodies from human plasma. Its sorption capacity is
  • Example 13 I m mobilization of 3- mercapto- 1 , 2, 4-triazole on
  • Example 14 P u r i f i c a t i o n o f immunog lobulins from bovine colostrum on 2- mercaptoimidazole
  • Bovine colostrum was diluted 1 :1 with adsorption buffer (10 mM HEPES, pH 7.3) and filtered. Adsorption was performed on a 5.9 ml column at a flow rate of 120 cm/hr. Elution was performed by 200 mM sodium dihydrogen phosphate, pH 4.25. Electrophoretic analysis revealed that the immunoglobulins eluted were greater than 80% pure.

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Abstract

A pseudobioaffinity chromatography adsorbent adapted for use in selectively adsorbing immunoglobulins. In one embodiment, the adsorbent comprises: (a) a solid support material; and (b) a ligand immobilized on the surface of the solid support material, said ligand being a compound of formula (II) wherein Y1 is selected from the group consisting of S, SCH3+, O, NH, NCH¿3?, CH2 and CR1R2 wherein at least one of R1 and R2 is not hydrogen; wherein each of Y2, Y3 and Y4 is selected from the group consisting of N, NCH3?+¿, CH, and CR wherein R is not hydrogen; and wherein at least two of Y¿1?, Y2, Y3 and Y4 are neither CH2, CH, CR nor CR1R2.

Description

CHROMATOGRAPHY ADSORBENTS UTILIZING MERCAPTO HETEROCYCLIC LIGANDS
FIELD OF THE INVENTION
The present invention relates generally to affinity chromatography and more particularly to pseudobioaffinity chromatography.
BACKGROUND OF THE INVENTION
With the rapid development of and increasing need for monoclonal and polyclonal antibodies for both diagnostic and therapeutic purposes, research efforts
have recently been directed to devising new techniques for effectively isolating antibodies from antibody-containing solutions. Some well-known, existing
techniques include the use of classic liquid chromatography adsorbents, such as ion exchangers, hydrophobic supports, hydroxy apatite and gel filtration media.
Unfortunately, these techniques are time-consuming and tedious to perform and cannot be applied generally to the isolation of heterogenous populations of antibodies. As a result, such techniques need to be adjusted on a case-by-case basis depending upon the specific antibody sought to be isolated.
Affinity chromatography, which relies on specific interactions between an immobilized ligand and a particular molecule sought to be purified, is another well- known, existing technique used to purify antibodies from solution. Protein A, which is derived from the bacterium Staphylococcus aureus, has a strong and specific affinity for the Fc fragment of IgG antibodies and has been used for approximately one decade as an affinity ligand for purifying IgG antibodies. Protein A can be immobilized on a large variety of solid support materials, such as chromatographic beads and membranes, and can be used to obtain high purity antibodies in high
yield.
Unfortunately, Protein A suffers from a number of limitations as an affinity
ligand. One such limitation is the prohibitive cost of Protein A. Because of its high cost, the large scale utilization of Protein A as an affinity ligand is not often economically feasible. Another such limitation is the sensitivity of Protein A to
those proteases that are commonly present in the same biological fluids (e.g., sera, ascitic fluids, milk, hybridoma cell culture supernatants, and the like) in which the antibodies being sought to be purified by affinity chromatography are also present. This sensitivity of Protein A to such proteases often leads to one or both of the following effects: (1) The recognition of Protein A towards the Fc fragments of IgG is progressively reduced; and (2) Fragments of Protein A generated by protease action contaminate otherwise pure antibody preparations.
Still another limitation with Protein A is that it is possible for Protein A to be released intact from its associated solid support material, thereby contaminating antibody preparations brought into contact therewith. The contamination of therapeutic antibody preparations with traces of Protein A or Protein A fragments
is very serious not only because Protein A and/or Protein A fragments are capable of provoking an antigenic response in humans but also because Protein A is known as a potent mitogen.
Protein A is not the only protein which has been used as an affinity ligand for the purification of a class of antibodies. Protein G has similarly been used as an affinity ligand. See Bjorck et al., J. Immunol., 133:969 (1984). Protein G also interacts with the Fc fragment of immunoglobulins and is particularly effective in isolating mouse IgG antibodies of class 1 (as contrasted with Protein A which is not very effective in isolating these antibodies). Protein G, however, suffers from the same types of limitations discussed above in connection with Protein A.
Recently, a third protein has been identified as an effective affinity ligand for purifying antibodies. This protein is Protein L from Peptostreptococcus magnus. Protein L, as contrasted with Protein A and Protein G, interacts specifically with the light chains of IgG antibodies without interfering with their antigen binding sites.
This specificity permits Protein L to complex not only with antibodies of the IgG class but also with antibodies of the IgA and IgM classes. Despite its broad affinity, Protein L suffers from the same limitations described above in connection with Proteins A and G.
In addition to suffering from the aforementioned limitations, Proteins A, G and L are all sensitive to a number of chemical and physical agents (e.g., extreme pH, detergents, chaotropics, high temperature) which are frequently used to clean affinity chromatography columns between runs. Consequently, some people have chosen to minimize the number of cleaning cycles applied to the above-described columns so as to correspondingly minimize degradation thereto. One drawback to
this tactic, however, is that failure to clean the columns regularly prevents optimal antibody purification. Anti-antibodies represent still another type of affinity ligand used for gamma globulin purification. Anti-antibodies, however, are limited in use due to their high cost and very limited stability.
In addition to the above-described protein-based affinity ligands, there are
numerous lower molecular weight pseudobioaffinity (i.e., less specific) ligands which have been used for antibody purification. Histidine, pyridine and related
compounds represent one type of pseudobioaffinity ligand commonly used for
antibody purification. See e jL, Hu et al., "Histidine-ligand chromatography of proteins: Multiple modes of binding mechanism," Journal of Chromatography, 646:31-35 (1993); El-Kak et al., "Interaction of immunoglobulin G with immobilized
histidine: mechanistic and kinetic aspects," Journal of Chromatography, 604:29-37
(1992); Wu et al., "Separation of immunoglobulin G by high-performance pseudo¬ bioaffinity chromatography with immobilized histidine," Journal of Chromatography, 584:35-41 (1992); El-Kak et al., "Study of the separation of mouse monoclonal antibodies by pseudobioaffinity chromatography using matrix-linked histidine and histamine," Journal of Chromatography, 570:29-41 (1991), all of which are incorporated herein by reference. See generally U.S. Patent Nos. 5,185,313, 5,141 ,966, 4,701 ,500 and 4,381 ,239, all of which are incorporated herein by
reference. However, non-specific binding of proteins and low capacity are the major limitations to adsorbents employing the above-identified compounds.
Thiophilic compounds represent another class of pseudobioaffinity ligands. An adsorbent utilizing one type of thiophilic compound is disclosed by Porath et al. in FEBS Lett, 185:306 (1985), which is incorporated herein by reference. This type of adsorbent is produced by reacting either a hydroxyl- or thiol-containing support first with divinyl sulfone and then with mercaptoethanol. The aforementioned adsorbent utilizes a salt-promoted approach to adsorb immunoglobulins. Elution of adsorbed immunoglobulins is effected by decreasing salt concentration and/or by modifying pH. Another type of pseudobioaffinity adsorbent capable of adsorbing antibodies utilizes mercaptopyridine as its ligand. See Oscarsson et al., "Protein Chromatography with Pyridine- and Alkyl-Thioether-Based Agarose Adsorbents," Journal of Chromatography, 499:235-247 (1990), which is incorporated herein by reference. This type of adsorbent is generated, for example, by reacting mercaptopyridine with a properly activated solid support. The adsorbent thus formed is capable of adsorbing antibodies under high salt conditions.
Other pseudobioaffinity adsorbents utilizing thiophilic compounds are
described in the following patents and publications, all of which are incorporated herein by reference: U.S. Patent No. 4,897,467; published PCT Application No.
PCT/US89/02329; published European Patent Application No. 168,363; Oscarsson et al., "Thiophilic adsorbents for RIA and ELISA procedures," Journal of Immunological Methods, 143:143-149 (1991); and Porath et al., "A New King of Thiophilic' Electron-Donor-Acceptor Adsorbent," Makromol. Chem., Macromol. Symp., 17:359-371 (1988).
The above-described thiophilic adsorbents provide a generally satisfactory means for purifying antibodies; however, in those cases in which the initial biological liquid is a protein rich solution, such as a serum or ascites, the non¬ specific binding by such adsorbents of a number of proteins other than the desired antibodies can be a problem. This problem of non-specific binding is the primary limitation of these thiophilic adsorbents.
Another group of low molecular weight ligands capable of selectively binding antibodies includes pentafluoropyridine and N-dimethylaminopyridine reacted with ethylene glycol, glycine or mercaptoethanol. See Ngo, J. Chromatogr., 510:281 (1990), which is incorporated herein by reference. Adsorbents utilizing these materials can be used to isolate immunoglobulins in either high salt or low salt buffers or to isolate other types of proteins under low salt conditions. Elution of
adsorbed proteins can be obtained by lowering pH. Still other low molecular weight pseudobioaffinity ligands have been
identified as being capable of selectively binding antibodies from egg yolk and other
biological liquids. These ligands are special dyes. Elution of the bound antibodies from the ligands is achieved by special dispiacers.
All of the above-mentioned adsorbents utilizing low molecular weight
pseudobioaffinity ligands are very attractive in terms of their low cost and their chemical and physical stability. However, their level of non-specific binding and/or their toxicity (should they, for example, contaminate a therapeutic antibody preparation intended for administration to humans) are too high, and their capacity for antibodies is too low to counterbalance the attractiveness of adsorbents utilizing Proteins A, G or L as specific antibody ligands.
SUMMARY OF THE INVENTION
Therefore, it is an object of the present invention to provide a novel pseudobioaffinity chromatography adsorbent which overcomes at least some of the
limitations discussed above in connection with existing affinity and pseudobioaffinity chromatography adsorbents.
In furtherance of the above and other objects to be described or to become apparent below, a pseudobioaffinity chromatography adsorbent adapted for use in selectively adsorbing immunoglobulins is hereinafter provided, the adsorbent comprising in a first embodiment: (a) a solid support material; and (b) a ligand
immobilized on the surface of the solid support material, said ligand being a compound of the formula
Figure imgf000009_0001
wherein each of X1 f X2 and X3 is selected from the group consisting of S, SCH3 +,
O, NH, NCH3, CH2 and CR1R2 wherein at least one of R and R2 is not hydrogen; wherein X4 is selected from the group consisting of N, NCH3 +, CH and CR wherein R is not hydrogen; and wherein at least two of X1 f X2, X3 and X4 are neither CH2, CH, CR nor CR.R^ Alternatively, a pseudobioaffinity chromatography adsorbent adapted for use in selectively adsorbing immunoglobulins in accordance with a second embodiment of the invention comprises: (a) a solid support material; and (b) a ligand immobilized on the surface of the solid support material, said ligand being a compound of the formula
Figure imgf000010_0001
wherein Y1 is selected from the group consisting of S, SCH3 +, O, NH, NCH3, CH2 and CR1R2 wherein at least one of R and R2 is not hydrogen; wherein each of Y2,
Y3 and Y4 is selected from the group consisting of N, NCH3 +, CH, and CR wherein
R is not hydrogen; and wherein at least two of Y.,, Y2, Y3 and Y4 are neither CH2,
CH, CR nor CR.R;,.
The present invention is also directed to methods of making the aforementioned adsorbents and to methods of using the aforementioned adsorbents to perform affinity separations.
Additional objects, features and advantages of the present invention will be set forth in part in the description which follows, and in part will be obvious from the description or may be learned by practice of the invention. These embodiments will be described in sufficient detail to enable those skilled in the art to practice the invention, and it is to be understood that other embodiments may be utilized and that changes may be made without departing from the scope of the invention. The following detailed description is, therefore, not to be taken in a limiting sense, and the scope of the present invention is best defined by the appended claims.
DETAILED DESCRIPTION OF PREFERRED EMBODIMENTS
The present invention is directed to novel pseudobioaffinity chromatography adsorbents useful in the selective adsorption of a wide of range of
immunoglobulins. The adsorbents of the present invention may also be used to selectively adsorb non-immunoglobulin proteins.
In accordance with the teachings of the present invention, the pseudobioaffinity chromatography adsorbents comprise (a) a solid support material; and (b) a ligand immobilized on the surface of the solid support material, the ligand being a mercapto five-membered heterocyclic ring of the type hereinafter described.
In a first embodiment, said ligand has the structure represented below by compound I.
Figure imgf000011_0001
wherein each of X1 f X2 and X3 is selected from the group consisting of S, SCH3 +, O, NH, NCH3, CH2 and CR1R2 wherein at least one of R1 and R2 is not hydrogen; wherein X4 is selected from the group consisting of N, NCH3 +, CH and CR wherein R is not hydrogen; and wherein at least two of X^ X2, X3 and X4 are neither CH2, CH, CR nor CR.R.,. As indicated above, R, R^ and R2 can be virtually any functional group.
Examples of R, R., and R2, for illustrative purposes only, include substituted or unsubstituted alkyl, aryl, alkenyl, alkynyl, aralkyl, acyl, cycloalkyl, carboxyl, amino, aryloxy or alkoxy, halo, hydroxy, nitro, O, S, cyano or any of the functional groups disclosed in U.S. Patent Nos. 4,223,036, 4,835,161 and 4,699,904, all of which are incorporated herein by reference.
For purposes of the present specification and claims, the particulars of R^
and R2 in CR.,R2 of compound I may be either the same or different for two or more of X1 ( X2 and X3. For example, R^ and R2 could be H and methyl, respectively, for
X1 and H and OH, respectively, for X2. Alternatively, R^ and R2 could be, for example, ethyl and OH, respectively, for both X1 and X2.
Examples of compound I include mercaptothiazoline (e.g., 2- mercaptothiazoline) and 2-mercapto-5-thiazolidone. In a second embodiment of the present invention, said ligand has the structure represented below by compound II.
Figure imgf000012_0001
wherein Y1 is selected from the group consisting of S, SCH3 +, O, NH, NCH3, CH2 and CR^ wherein at least one of R, and R2 is not hydrogen; wherein each of Y2, Y3 and Y4 is selected from the group consisting of N, NCH3 +, CH, and CR wherein R is not hydrogen; and wherein at least two of Y1 f Y2, Y3 and Y4 are neither CH2, CH, CR nor CR1R2. R, R1 and R2 of compound II can be virtually any functional group. Examples
of R, Rϊ and R2, for illustrative purposes only, include substituted or unsubstituted alkyl, aryl, alkenyl, alkynyl, aralkyl, acyl, cycloalkyl, carboxyl, amino, aryloxy or alkoxy, halo, hydroxy, nitro, O, S, cyano or any of the functional groups disclosed in U.S. Patent Nos. 4,223,036, 4,835,161 and 4,699,904, all of which are incorporated herein by reference.
For purposes of the present specification and claims, the particulars of R in
CR of compound II may be either the same or different for two or more of Y2, Y3 and Y4. For example, R could be methyl in the case of Y2 and OH in the case of
Y3. Alternatively, R could be, for example, ethyl for both Y2 and Y3.
Examples of compound II include mercaptoimidazole (e.g., 2- mercaptoimidazole), mercaptoimidazoline, mercaptothiazole (e.g., 2- mercaptothiazole), mercaptotriazole (e.g., 3-mercapto-1 ,2,4-triazole and 5-
mercapto-1 ,2,3-triazole), mercaptotetrazole (e.g., 5-mercapto-1 ,2,3,4-tetrazole), mercaptoth iad iazole (e. g . , 2-mercapto- 1 , 3 ,4-th iad iazole) and mercaptomethylimidazole (e.g., N-methyl-2-mercaptoimidazole - a pharmaceutical known to be safe to humans).
The solid support material of the present adsorbents may be composed of polysaccharides, such as cellulose, starch, dextran, agar or agarose, or hydrophilic synthetic polymers, such as substituted or unsubstituted polyacrylamides, polymethacryiamides, polyacrylates, poiymethacryiates, polyvinyl hydrophilic polymers, polystyrene, polysulfone or the like. Other suitable materials for use as the solid support material include porous mineral materials, such as silica, alumina, titania oxide, zirconia oxide and other ceramic structures. Alternatively, composite materials may be used as the solid support material. Such composite materials may be formed by the copolymerization of or by an interpenetrated network of two or more of the above mentioned entities. Examples of suitable composite materials include polysaccharide-synthetic polymers and/or polysaccharide-mineral structures and/or synthetic polymer-mineral structures, such as are disclosed in U.S. Patent Nos. 5,268,097, 5,234,991 and 5,075,371 , all of which are incorporated herein by
reference.
The solid support material of the present invention may take the form of beads or irregular particles ranging in size from about 0.1 mm to 1000 mm in diameter, fibers (hollow or otherwise) of any size, membranes, flat surfaces ranging in thickness from about 0.1 mm to 1 mm thick and sponge-like materials with holes from a few /m to several mm in diameter.
Preferably, the ligands described above are chemically immobilized on the solid support material via a covalent bond formed between the mercapto group of the ligand and a reactive group present on the solid support. Reactive groups capable of reacting with the mercapto group of the present ligand include epoxy groups, tosylates, tresylates, halides and vinyl groups. Because many of the aforementioned solid support materials do not include one of the reactive groups recited above, bifunctional activating agents capable of both reacting with the solid support materials and providing the necessary reactive groups may be used. Examples of suitable activating agents include epichlorhydrin, epibromhydrin, dibromo- and dichloropropanol, dibromobutane, ethyleneglycol diglycidylether, butanediol diglycidylether, divinyl sulfone and the like. By varying the concentration of the activating agent, the amount of immobilized ligand of the present invention can vary anywhere between a fraction of a //mole and several hundred //moles per ml of solid matrix. Typically, a small quantity of ligand per unit volume results in a low separation capacity for immunoglobulins whereas a large quantity of ligand per unit volume results in an increased sorption capacity for immunoglobulins (and can induce nonspecific binding of proteins other than immunoglobulins).
The activating agents listed above have different chain lengths. Accordingly, by selecting a particular activating agent, one can control the distance between the solid support material and the immobilized ligand. Due to steric constraints, this
distance between the ligand and the solid matrix can affect the adsorption
characteristics of the final product both in terms of specificity and sorption capacity. Generally, more ligand can be immobilized on the solid support material in those instances in which the chain length is great than in those instances in which it is not.
Preparation of the adsorbents of the present invention may be effected in a manner similar to that by which conventional adsorbents have typically been prepared. More specifically, this may be done by reacting a solid support material of the type described above with an activating agent of the type described above under established conditions of concentration, temperature, pH, medium composition and time. Once activated, the support is then washed extensively in the established manner with solvents used to remove excess activating agent and/or activation byproducts therefrom. The washed, activated support is then contacted with ligands of the type described above under established conditions of concentration, pH, reaction temperature, reaction medium, time and agitation to produce an adsorbent which selectively adsorbs immunoglobulins from biological
liquids contacted therewith.
Save for the one exception noted below, the adsorbents of the present invention may be used in the same manner that conventional adsorbents have been used. This comprises introducing the adsorbent into a chromatographic column and then washing the column with an appropriate aqueous solution of salts at a given pH. A biological solution containing the immunoglobulins wished to be
isolated is then combined with salts (e.g., Na2S04) and directly loaded into the column. The immunoglobulins present in the solution are captured by the adsorbent whereas the non-immunoglobulin proteins present in the solution and the remainder of the solution are recovered in the flowthrough. After an appropriate
washing to eliminate non-specifically adsorbed macromolecules, the immunoglobulins are then desorbed by a pH shift and/or by changing the salt concentration. The isolated immunoglobulins are then neutralized.
The one exception alluded to above is that certain adsorbents of the present invention do not require that salt be added to the biological solution for the antibodies contained therein to adsorb to the ligand. This elimination of the need for salt is clearly advantageous in those instances in which the addition of salt is undesirable. Those adsorbents of the present invention for which salt need not be added (and, in fact, cannot be added in order for the adsorbent to function properly) are those which employ ligands of compounds I and II in which nitrogen atoms constitute the two or more heteroatoms of the five-membered heterocyclic ring. Examples of such ligands include 2-mercaptoimidazole, 3-mercapto- 1 ,2,4- triazole, 5-mercapto-1 ,2,3-triazole, 5-mercapto-1 ,2,3,4-tetrazole and N-methyl-2- mercapto-imidazole.
The adsorbents of the present invention can be used to isolate a variety of different types of antibodies, such as native antibodies, chemically modified antibodies, bioengineered antibodies, antibody fragments and antibody conjugates containing enzymes, as well as various toxins, haptens and the like. In addition, the adsorbents of the present invention can be used to isolate antibodies from a variety of different biological liquids, such as hybridoma cell culture supernatants, plasma and plasma fractions, milk and milk fractions, ascitic fluids, fermentation broths and the like.
The adsorbents of the present invention represent a significant advancement in the art over adsorbents utilizing antibody-specific proteins, such as Protein A, Protein G, Protein L and the like. This is, in part, because the present adsorbents are stable against biological degradation, particularly degradation by hydrolytic enzymes. In addition, many of the ligands of the present adsorbents are commercially available chemicals of a current cost significantly lower than protein-
based ligands. In addition, the present adsorbents can be treated with strong acidic and alkaline solutions which would otherwise be inappropriate with adsorbents utilizing protein ligands. Moreover, the present adsorbents can be treated with other cleaning agents, such as detergents, chaotropic salts and the like, without running the risk of adsorbent degradation or inactivation. Furthermore, heat treatment can be applied to the adsorbents of the present invention without modifying their capture efficiency or specificity.
As compared to existing pseudobioaffinity adsorbents, the present adsorbents are more specific and/or show higher sorption capacity for antibodies. The following examples are illustrative only and should in no way limit the scope of the present invention:
Example 1: Immobilization of 2-mercaptoimidazole on an epoxy-activated HyperD support 20 grams of epoxy-activated HyperD silica oxide/polystyrene composite support with functionalized hydrogel filled pores (commercially available from BioSepra, Inc., Marlborough, MA and described in U.S. Patent No.' 5,268,097) were
suspended in 100 ml of 35% 50 mM carbonate buffer, pH 8.6, and 65% ethanol, containing 5 mM 2-mercaptoimidazole and shaken for 16 hours. The slurry was filtered onto a sinter glass filter, washed with ethanol and drained. The modified HyperD adsorbent was resuspended in 1 M ethanolamine, pH 10.5, shaken for 2.5 hours at 45°C, filtered and then washed with water. The beads were then resuspended in 2 M sodium acetate, and 2 ml of acetic anhydride was added over a period of one hour during shaking. The mixture was then shaken for an additional hour, filtered onto a sinter glass filter and washed with water until neutrality.
A chromatographic assay was then performed on the above-described adsorbent using 10 mM HEPES at pH 7.5. 1.5 ml of human serum was diluted three times with HEPES buffer and passed through a column of 1.2 ml gel volume. Elution was performed by changing the pH to 3.5 with citric acid buffer. Electrophoretic analysis of the elution fractions collected revealed that immunoglobulins constituted the major part of the adsorbed proteins, and the purity of the immunoglobulins was judged to be greater than 75%. The dynamic capacity of the modified gel by frontal analysis was 9.2 mg/ml at c/10 (i.e., 10% breakthrough) and 14.4 mg/ml at c/2 (i.e., 50% breakthrough) for human immunoglobulins at a flow rate of 120 cm/hr.
Example 2: Immobilization of 2-aminoimidazole on an epoxy-activated HyperD support An adsorbent similar to that synthesized in Example 1 was prepared, the only difference being that 2-aminoimidazole was substituted for 2- mercaptoimidazole. An evaluation of the dynamic capacity of the adsorbent was
performed using frontal analysis and showed that the 2-aminoimidazole adsorbent had a dynamic capacity of 1.5 mg/ml at c/10 and 2.5 mg/ml at c/2 for human immunoglobulins at a flow rate of 120 cm/hr.
Comparing the results of Examples 1 and 2, it can be seen that, when a
sulfur group (mercaptoimidazole) is replaced by a nitrogen group (aminoimidazole), the sorption capacity and capture efficiency are dramatically decreased. Example 3: Immobilization of 2-mercaptothiazole on an epoxy-activated HyperD support An adsorbent similar to that synthesized in Example 1 was prepared, the only difference being that 2-mercaptothiazole was substituted for 2- mercaptoimidazole. A chromatographic assay was performed using 10 mM HEPES and 500 mM sodium sulfate at pH 7.5. 1.5 ml of human serum was passed through a column of 4.6 ml gel volume, and elution was performed by changing the pH to 3.5 with citric acid buffer.
Electrophoretic analysis of the elution fractions collected revealed that immunoglobulins constituted the major part of the adsorbed proteins, and the purity of the immunoglobulins was judged to be greater than 85%. The capacity of the modified gel by frontal analysis was determined to be 6.2 mg/ml at c/10 and 7.9 mg/ml at c/2 at a flow rate of 120 cm/hr.
Example 4: Immobilization of 2-mercaptothiazoline on an epoxy-activated HyperD support An adsorbent similar to that synthesized in Example 1 was prepared, the
only difference being that 2-mercaptothiazoline was substituted for 2- mercaptoimidazole. A chromatographic assay was performed using 10 mM HEPES and 500 mM sodium sulfate at pH 7.5. 1.5 ml of human serum was passed through a column of 4.6 ml gel volume, and elution was performed by changing the
pH to 3.5 with citric acid buffer.
Electrophoretic analysis of the elution fractions collected revealed that immunoglobulins constituted the major part of the adsorbed proteins, and the purity of the immunoglobulins was judged to be greater than 85%. The capacity of the
modified gel by frontal analysis was determined to be 6.2 mg/ml at c/10 and 7.7 mg/ml at c/2 at a flow rate of 120 cm/hr.
Example 5: lmmobilizationof3-mercapto-1,2,4-triazole on an epoxy-activated HyperD support An adsorbent similar to that synthesized in Example 1 was prepared, the only difference being that 3-mercapto-1 ,2,4-triazole was substituted for 2-
mercaptoimidazole. Using the same sort of assay described above in Example 1 , the capacity of the modified gel for pure human antibodies was determined by frontal analysis to be 1.5 mg/ml at c/10 and 8.1 mg/ml at c/2 at a flow rate of 146 cm/hr and an adsorption buffer containing 10 mM HEPES at pH 7. Example 6: Immobilization of 2-mercapto-1 ,3,4-
thiadiazole on an epoxy-activated HyperD support An adsorbent similar to that synthesized in Example 1 was prepared, the only difference being that 2-mercapto-1 ,3,4-thiadiazole was substituted for 2- mercaptoimidazole. Using the same sort of assay described above in Example 1 ,
the capacity of the modified gel for pure human antibodies was determined by frontal analysis to be 9.1 mg/ml at c/10 and 11.2 mg/ml at c/2 at a flow rate of 140 cm/hr in an adsorption buffer containing 10 mM HEPES and 750 mM sodium sulfate at pH 7.
Example 7: Immobilization of 2-mercapto-5- thiazolidone on an epoxy-activated HyperD support An adsorbent similar to that synthesized in Example 1 was prepared, the
only difference being that 2-mercapto-5-thiazolidone was substituted for 2- mercaptoimidazole. Using the same sort of assay described above in Example 1 , the capacity of the modified gel for pure human antibodies was determined by frontal analysis to be 9 mg/ml at c/10 and 12.2 mg/ml at c/2 at a flow rate of 134 cm/hr in an adsorption buffer containing 10 mM HEPES and 750 mM sodium sulfate at pH 7.
Example 8: Immobilization of 2-mercaptothiazoline on a vinyl-activated HyperD support 15 grams of amino-HyperD (prepared by amination by reacting the epoxy- activated HyperD of Example 1 with ethylene diamine) were suspended in 80 ml of a mixture containing 35% 100 mM carbonate buffer, pH 9.5, and 65% ethanol. To this slurry was added 7 ml of divinyl sulfone, and the slurry was shaken for 20 hours at 45°C. The slurry was filtered, washed with ethanol and dried. The beads were resuspended in 75 ml of a mixture of 35% 50 ml carbonate buffer, pH 8.6, and 65% ethanol containing 5 mM 2-mercaptothiazoline and then shaken for 24 hours at 45°C. The slurry was then filtered onto a sinter glass filter, washed with ethanol and dried. The modified HyperD support was then resuspended in 100 ml of a solution containing 1 M ethanolamine, pH 10.5, shaken for 2.5 hours at
45°C, filtered and washed with water. A chromatographic assay was performed using 10 mM HEPES and 500 mM sodium sulfate at pH 7.5. 1.5 ml of human serum was passed through a column of 4.6 ml gel volume, and elution was performed by changing the pH to 2.5 with citric acid buffer. Electrophoretic analysis of the elution fractions collected revealed that immunoglobulins constituted the major part of the adsorbed proteins, and the
purity of the immunoglobulins was judged to be greater than 85%. The capacity of the modified gel was determined by frontal analysis to be 11.8 mg/ml at c/10 and 14.4 mg/ml at c/2 at a flow rate of 120 cm/hr.
Example 9: Immobilization of 2-mercaptothiazole on a
bromo-activated HyperD support 5 grams of bromo-activated HyperD were suspended in 25 ml of a mixture of 35% 50 mM carbonate buffer, pH 8.6, and 65% ethanol containing 600 mg of 2- mercaptothiazole. The slurry was rotated, head over head, for 20 hours at room temperature and then filtered onto a sinter glass filter, washed and drained. The slurry was then resuspended in an aqueous solution of 1 M ethanolamine at pH
10.5 and rotated, head over head, for two hours at room temperature. The slurry was then filtered, washed with water until neutrality and then resuspended in 2 M sodium acetate. 1 ml of acetic anhydride was then added over the course of one hour. The slurry was then rotated for an additional hour and then filtered onto a sinter glass filter, washed to neutrality and drained. The modified gel was then evaluated with pure human IgG. Frontal analysis of the modified gel showed a dynamic capacity of 2.2 mg/ml at c/10 and 7.8 mg/ml at c/2 at a flow rate of 160 cm/hr using 10 mM HEPES and 500 mM Na2S04 at pH 7.0.
Example 10: I mmobi lization of 2- mercaptothiazole on Epoxy- Sepharose CL-6B support
2.5 ml of Epoxy-Sepharose CL-6B support (epoxy-activated agarose beads
with an epoxy content of 10-12 /M/ml of gel; commercially available from Pharmacia Biotech, Piscataway, NJ) were suspended in 15 ml of a mixture of 35% 50 mM carbonate buffer, pH 8.6, and 65% ethanol containing 600 mg of 2- mercaptothiazole. The slurry was rotated, head over head, for 20 hours and then filtered onto a glass filter, washed and drained. The agarose beads were then resuspended in an aqueous solution of 1 M ethanolamine at pH 10.5 and rotated, head over head, for two hours at room temperature. The slurry was then filtered and washed with water until neutrality and then resuspended in 2 M sodium
acetate. 1 ml of acetic anhydride was then added over the course of one hour. The slurry was then rotated for an additional hour, filtered onto a sinter glass filter, washed to neutrality and drained. The modified gel was evaluated with pure human IgG. Frontal analysis of the modified gel showed a dynamic capacity of 5.4 mg/ml at c/10 and 24.2 mg/ml
at c/2 at a flow rate of 75 cm/hr using 10 mM HEPES and 500 mM Na2S04 at pH 7.0. Example 11 : I m mob il ization of 2- mercapto-1 ,3,4-thiadiazoie
on Eupergit® support 20 g of Eupergit® support (a copolymer of methacrylamide, N,N- methylenebis(methacrylamide) and a component containing an active oxirane group; commercially available from Rohm Pharma, Darmstadt, Germany) are suspended in 50 ml of 50% 50 mM carbonate buffer, pH 8.6, and 50% ethanol. To
this suspension are added 50 ml of ethanol containing 5 mM of 2-mercapto-1 ,3,4- thiadiazole, and the slurry is shaken for 16 hours. The slurry is then filtered, washed with 50 mM carbonate buffer at pH 8.6/ethanol (1 :1) and drained under vacuum. The modified support is then saturated with ethanolamine as described in Example 1 and tested for its ability to separate antibodies from human plasma. Its sorption capacity is also checked by frontal analysis using pure human IgG and is expected to be within ±10% of that disclosed for the adsorbent in Example 6. Example 12: I mmobil ization of 2- mercapto-1 ,3,4-thiadiazole on Epoxy-Fractogel support
20 g of Epoxy-Fractogel support (epoxy-activated polymethacrylate support; commercially available from E. Merck, Wakefield, Rl) are suspended in 50 ml of 50% of 50 mM carbonate buffer, pH 8.6, and 50% ethanol. To this suspension are added 50 ml of ethanol containing 5 mM of 2-mercapto-1 ,3,4-thiadiazole, and the slurry is shaken for 16 hours. The slurry is then filtered, washed with 50 mM carbonate buffer at pH 8.6/ethanol (1 :1) and drained under vacuum. The modified support is then saturated with ethanolamine as described in Example 1 and tested for its ability to separate antibodies from human plasma. Its sorption capacity is
also checked by frontal analysis using pure human IgG and is expected to be within ±10% of that disclosed for the adsorbent in Example 6. Example 13: I m mobilization of 3- mercapto- 1 , 2, 4-triazole on
Spherodex® support
20 g of the commercially-available Spherodex® support (dextran-silica
composite support available from BioSepra, Inc., Marlborough, MA) are suspended in 70 ml of deionized water. Under agitation, 10 ml of ethyleneglycoldiglycidylether and 30 ml of 1 M sodium hydroxide containing 200 mg sodium borohydride are added. The mixture is shaken for 16 hours at room temperature and then rapidly washed with deionized water until neutrality. The epoxy-activated Spherodex® support is then reacted with 3-mercapto-1 ,2,4-triazole as described in Example 1
(without the last acetylation step) and tested for its ability to separate antibodies from human plasma. Its sorption capacity is also checked by frontal analysis using pure human IgG and is expected to be within ±10% of that disclosed for the adsorbent in Example 5.
Example 14: P u r i f i c a t i o n o f immunog lobulins from bovine colostrum on 2- mercaptoimidazole Bovine colostrum was diluted 1 :1 with adsorption buffer (10 mM HEPES, pH 7.3) and filtered. Adsorption was performed on a 5.9 ml column at a flow rate of 120 cm/hr. Elution was performed by 200 mM sodium dihydrogen phosphate, pH 4.25. Electrophoretic analysis revealed that the immunoglobulins eluted were greater than 80% pure.
The embodiments of the present invention recited herein are intended to be
merely exemplary and those skilled in the art will be able to make numerous variations and modifications to it without departing from the spirit of the present invention. All such variations and modifications are intended to be within the scope of the present invention as defined by the claims appended hereto.

Claims

WHAT IS CLAIMED IS:
1. A pseudobioaffinity chromatography adsorbent for use in selectively adsorbing immunoglobulins, said pseudobioaffinity chromatography adsorbent
comprising:
(a) a solid support material; and
(b) a ligand immobilized on the surface of the solid support material, said ligand being a compound of the formula
Figure imgf000027_0001
wherein each of X^ X2 and X3 is selected from the group consisting of S, SCH 3 '
O, NH, NCH3, CH2 and CR1R2 wherein at least one of R^ and R2 is not hydrogen; wherein X4 is selected from the group consisting of N, NCH3 +, CH and CR wherein R is not hydrogen; and wherein at least two of X1( X2, X3 and X4 are neither CH2, CH, CR nor CR.R2.
2. The pseudobioaffinity chromatography adsorbent as claimed in claim 1 wherein said ligand is selected from the group consisting of mercaptothiazoline and 2-mercapto-5-thiazolidone.
3. The pseudobioaffinity chromatography adsorbent as claimed in claim 1 wherein said ligand is 2-mercaptothiazoline.
4. The pseudobioaffinity chromatography adsorbent as claimed in claim 1 wherein said ligand is 2-mercapto-5-thiazolidone.
5. The pseudobioaffinity chromatography adsorbent as claimed in claim 1
wherein none of X.,, X2 and X3 are S, SCH3 + or O.
6. The pseudobioaffinity chromatography adsorbent as claimed in claim 1 wherein said solid support is selected from the group consisting of cellulose, starch,
dextran, agar, agarose, substituted or unsubstituted polyacrylamides, polymethacryiamides, polyacrylates, poiymethacryiates, polyvinyl hydrophilic polymers, polystyrene and polysulfone, silica, alumina, titania oxide, zirconia oxide, polysaccharide-synthetic polymers, polysaccharide-mineral structures and synthetic polymer-mineral structures.
7. The pseudobioaffinity chromatography adsorbent as claimed in claim 1 wherein said solid support material has a physical form selected from the group
consisting of beads, irregular particles, fibers, membranes, flat surfaces and sponge-like materials.
8. The pseudobioaffinity chromatography adsorbent as claimed in claim 1 wherein said ligand is immobilized on the surface of said solid support material via a bifunctional activating agent having a group reactive with the mercapto group of said ligand.
9. The pseudobioaffinity chromatography adsorbent as claimed in claim 8 wherein said bifunctional activating agent is selected from the group consisting of
epichlorhydrin, epibromhydrin, dibromo- and dichloropropanol, dibromobutane, ethyleneglycol diglycidylether, butanediol diglycidylether, and divinyl sulfone.
10. A pseudobioaffinity chromatography adsorbent for use in selectively adsorbing immunoglobulins, said pseudobioaffinity chromatography adsorbent
comprising:
(a) a solid support material; and (b) a ligand immobilized on the surface of the solid support material, said ligand being a compound of the formula
Figure imgf000029_0001
wherein Y, is selected from the group consisting of S, SCH3 +, O, NH, NCH3, CH2 and CR1R2 wherein at least one of R, and R2 is not hydrogen; wherein each of Y2,
Y3 and Y4 is selected from the group consisting of N, NCH3 +, CH, and CR wherein
R is not hydrogen; and wherein at least two of Y1? Y2, Y3 and Y4 are neither CH2, CH, CR nor CR.R.,.
11. The pseudobioaffinity chromatography adsorbent as claimed in claim 10 wherein said ligand is selected from the group consisting of mercaptoimidazole, mercaptoimidazoline, mercaptothiazole, mercaptotriazole, mercaptotetrazole, mercaptothiadiazole and mercaptomethylimidazole.
12. The pseudobioaffinity chromatography adsorbent as claimed in claim 10 wherein said ligand is selected from the group consisting of N-methyl-2- mercaptoimidazole, 2-mercaptoimidazole, 2-mercaptothiazole, 3-mercapto-1 ,2,4- triazole, 5-mercapto-1 ,2,3-triazole, 5-mercapto-1 ,2,3,4-tetrazole, 2-mercapto-1 ,3,4- thiadiazole.
13. The pseudobioaffinity chromatography adsorbent as claimed in claim 10 wherein said ligand is N-methyl-2-mercaptoimidazole.
14. The pseudobioaffinity chromatography adsorbent as claimed in claim 10
wherein said ligand is 2-mercaptothiazole.
15. The pseudobioaffinity chromatography adsorbent as claimed in claim 10
wherein said ligand is 2-mercapto-1 ,3,4-thiadiazole.
16. The pseudobioaffinity chromatography adsorbent as claimed in claim 10
wherein Y1 is neither S, SCH3 + nor O.
17. The pseudobioaffinity chromatography adsorbent as claimed in claim 10
wherein said solid support is selected from the group consisting of cellulose, starch, dextran, agar, agarose, substituted or unsubstituted polyacrylamides, polymethacryiamides, polyacrylates, poiymethacryiates, polyvinyl hydrophilic polymers, polystyrene and polysulfone, silica, alumina, titania oxide, zirconia oxide, polysaccharide-synthetic polymers, polysaccharide-mineral structures and synthetic polymer-mineral structures.
18. The pseudobioaffinity chromatography adsorbent as claimed in claim 10 wherein said solid support material has a physical form selected from the group consisting of beads, irregular particles, fibers, membranes, flat surfaces and sponge-like materials.
19. The pseudobioaffinity chromatography adsorbent as claimed in claim 10 wherein said ligand is immobilized on the surface of said solid support material via a bifunctional activating agent having a group reactive with the mercapto group of said ligand.
20. The pseudobioaffinity chromatography adsorbent as claimed in claim 19 wherein said bifunctional activating agent is selected from the group consisting of epichlorhydrin, epibromhydrin, dibromo- and dichloropropanol, dibromobutane, ethyleneglycol diglycidylether, butanediol diglycidylether, and divinyl sulfone.
21. A method of making a pseudobioaffinity chromatography adsorbent for use in binding a target protein during affinity separations of the target protein from a mixture of compounds, said method comprising the steps of:
(a) providing a solid support material;
(b) immobilizing a ligand on the surface of said solid support material, said ligand being a compound of the formula
Figure imgf000031_0001
wherein each of X X2 and X3 is selected from the group consisting of S, SCH3 +, O, NH, NCH3, CH2 and CR^ wherein at least one of R1 and R2 is not hydrogen; wherein X4 is selected from the group consisting of N, NCH3 +, CH and CR wherein R is not hydrogen; and wherein at least two of X1 ( X2, X3 and X4 are neither CH2, CH, CR nor CR.,R2.
22. The method as claimed in claim 21 wherein said immobilizing step comprises activating said solid support material with a bifunctional activating agent having a group reactive with the mercapto group of said ligand and contacting said ligand with said activated solid support material.
23. The method as claimed in claim 22 wherein said bifunctional activating agent is selected from the group consisting of epichlorhydrin, epibromhydrin, dibromo- and dichloropropanol, dibromobutane, ethyleneglycol diglycidylether, butanediol diglycidylether, and divinyl sulfone.
24. A method of making a pseudobioaffinity chromatography adsorbent for use in binding a target protein during affinity separations of the target protein from a mixture of compounds, said method comprising the steps of:
(a) providing a solid support material;
(b) immobilizing a ligand on the surface of said solid support
material, said ligand being a compound of the formula
Figure imgf000032_0001
wherein Y. is selected from the group consisting of S, SCH3 +, O, NH, NCH3, CH2 and CR.R2 wherein at least one of R., and R2 is not hydrogen; wherein each of Y2, Y3 and Y4 is selected from the group consisting of N, NCH3 +, CH, and CR wherein R is not hydrogen; and wherein at least two of Y1 ( Y2, Y3 and Y4 are neither CH2, CH, CR nor CR^.
25. The method as claimed in claim 24 wherein said immobilizing step comprises activating said solid support material with a bifunctional activating agent having a group reactive with the mercapto group of said ligand and contacting said ligand with said activated solid support material.
26. The method as claimed in claim 25 wherein said bifunctional activating agent is selected from the group consisting of epichlorhydrin, epibromhydrin, dibromo- and dichloropropanol, dibromobutane, ethyleneglycol diglycidylether, butanediol diglycidylether, and divinyl sulfone.
27. A method of performing affinity separations of a target protein to be
separated from a mixture of compounds, said method comprising the steps of: (a) providing a pseudobioaffinity chromatography adsorbent comprising:
(i) a solid support material; and
(ii) a ligand immobilized on the surface of the solid support material, said ligand being a compound of the formula
Figure imgf000033_0001
wherein each of X2 and X3 is selected from the group consisting of S, SCH3 +,
O, NH, NCH3, CH2 and CR1R2 wherein at least one of R., and R2 is not hydrogen; wherein X4 is selected from the group consisting of N, NCH3 +, CH and CR wherein R is not hydrogen; and wherein at least two of X^ X2, X3 and X4 are neither CH2, CH, CR nor CR.,R2;
(b) contacting the mixture of compounds containing the target protein with said pseudobioaffinity chromatography adsorbent, said mixture of compounds having added thereto an appropriate amount of salt to permit the target protein to bind to said ligand; and
(c) maintaining contact between the mixture and said pseudobioaffinity chromatography adsorbent for a time sufficient to selectively and reversibly bind the target protein to the immobilized ligand, thereby separating the target protein from the mixture.
28. The method as claimed in claim 27 wherein said target protein is an immunoglobulin.
29. The method as claimed in claim 28 wherein none of X2 and X3 are S, SCH3 + or O and wherein said appropriate amount of salt is zero.
30. A method of performing affinity separations of a target protein to be
separated from a mixture of compounds, said method comprising the steps of: (a) providing a pseudobioaffinity chromatography adsorbent
comprising:
(i) a solid support material; and
(ii) a ligand immobilized on the surface of the solid support material, said ligand being a compound of the formula
Figure imgf000034_0001
wherein Y1 is selected from the group consisting of S, SCH3 +, O, NH, NCH3, CH2 and CR1R2 wherein at least one of R and R2 is not hydrogen; wherein each of Y2, Y3 and Y4 is selected from the group consisting of N, NCH3 +, CH, and CR wherein
R is not hydrogen; and wherein at least two of Y Y2, Y3 and Y4 are neither CH2, CH, CR nor CR1R2;
(b) contacting the mixture of compounds containing the target protein with said pseudobioaffinity chromatography adsorbent, said mixture of compounds having added thereto an appropriate amount of salt to permit the target protein to bind to said ligand; and
(c) maintaining contact between the mixture and said pseudobioaffinity chromatography adsorbent for a time sufficient to selectively and reversibly bind the target protein to the immobilized ligand, thereby separating the target protein from the mixture.
31. The method as claimed in claim 30 wherein said target protein is an
immunoglobulin.
32. The method as claimed in claim 32 wherein Y, is neither S, SCH3 + nor
O and wherein said appropriate amount of salt is zero.
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DE69531826D1 (en) 2003-10-30
US5719269A (en) 1998-02-17
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US5502022A (en) 1996-03-26
EP0764048A4 (en) 1998-03-18
DE69531826T2 (en) 2004-07-08
AU681035B2 (en) 1997-08-14
JP3844496B2 (en) 2006-11-15
ATE250457T1 (en) 2003-10-15
US6610630B2 (en) 2003-08-26

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