SEPARATION OF PROTEIN MONOMERS FROM AGGREGATES BY USE OF ION-EXCHANGE CHROMATOGRAPHY

Abstract: A method is disclosed for separating a polypeptide monomer from a mixture comprising dimers and/or multimers. The method comprises applying the mixture to either a cation-exchange chromatography resin or an anion-exchange chromatography resin and eluting the mixture at a gradient of about 0-1 M of an elution salt, wherein the monomer is separated from the dimers and/or multimers present in the mixture.

Description: SEPARATION OF PROTEIN MONOMERS FROM AGGREGATES BY USE OF ION-EXCHANGE CHROMATOGRAPHY Field of the Invention This invention relates to a process for separating polypeptide monomers from dimers and/or other multimers using ion-exchange chromatography Description of Background and Related Art Attempts to purify authentic, properly folded protein from recombinant hosts have been frustrated due to the tertiary structure of the molecule In this regard, purification of the recombinantly produced molecule often yields a heterogeneous mixture that consists largely of inactive, misfolded, insoluble, and/or soluble dimers, multimers, and disulfϊde-linked aggregates Other aberrant molecules, such as fragments, nicked, oxidized, and glycosylated forms, may also be present Thus, purification is difficult and yields of the authentic monomer are often low See, e g , Elliott et al . J Protein Chem . 9 95-104 (1990) Different techniques have been used to correct these problems For example. Chang and Swartz, Protein Folding in vivo and in vitro (American Chemical Society, 1993), pp 178-188 describe a method for solubihzing aggregated IGF-I produced in E coli, using low concentrations of urea and dithiothreitol (DTT) in an alkaline buffer U S Pat No 5,231,178 descπbes a method for the purification of correctly folded, monomeπc IGF-I from P pastoris using a combination of cation exchange, hydrophobic interaction, and gel filtration chromatography WO 96/40776 describes a method for producing authentic properly folded IGF from yeast using a first cation exchange chromatography with the yeast cell medium, denaturing and chromatography, and performing reverse phase high performance liquid chromatography Separation of protein and peptide monomers from their dimers, tetramers, and multimers presents a serious challenge to the separations scientist Size-exclusion chromatography (SEC) and Tangential-How Filtration (IFF) (U S Pat Nos 5,256,294 and 5,490,937) have been used for separating monomers from aggregates but have limitations SEC can separate monomers from multimers and in some cases monomers from dimers The main limitations of SEC are 1) limited load volumes (typically 5% of the bed volume) requiring large columns or multiple cycles 2) and load protein concentration (low concentration feed stocks require pre-concentration or multiple cycles on the column Higher protein concentrations can be more viscous, thereby reducing the efficiency of the separation) Historically TFF can separate protein multimers that are tenfold larger than the monomer U S Pat No 5,256,294 U S Pat Nos 4,228.154 and 5,250,663 disclose separations of albumin from mixtures U S Pat No 4,228,154 describes use of both cation-exchange and anion-exchange chromatography steps for the purification, without separation of monomer from multimers There is a need for separating monomers from dimers and multimers that is satisfactory, requires the use of only one ion-exchange step, and does not have the limitations of SEC or TFF Summary of the Invention Accordingly, this invention provides a method for separating a polypeptide monomer from a mixture comprising dimers and or multimers. wherein the method comprises applying the mixture to either a cation- exchange or an anion-exchange chromatography resm in a buffer, wherein if the resin is cation-exchange, the pH of the buffer is about 4-7, and wherein if the resin is anion-exchange, the pH of the buffer is about 6-9, and eluting the mixture at a gradient of about 0-1 M of an elution salt wherein the monomer is separated from the dimers and/or multimers present in the mixture In this study it is demonstrated that ion-exchange chromatography — either anion or catιon~ιs an effective means to separate protein or polypeptide monomers from their dimers and/or multimers Separations are performed using either step or linear gradient elution Ion exchange has several advantages over the SEC and TFF methods described above First, separation is independent of polypeptide concentration in the load and therefore no pre-concentration is required Second resins can be loaded to greater than 30 mg polypeptide/mL resin and still achieve excellent separations Third ion-exchange resins are inexpensive and easy to use Typical separations achieve enrichment of monomer to greater than 99 5% purity and yields in excess of 90% Brief Description of the Drawings Figures 1A and IB show separation of U266 IgE monomer from dimers and multimers on a RESOURCE Q™ anion-exchange column The column was equilibrated in 25 mM Tπs/pH 8, and eluted with a gradient from 0 to 0 5 M sodium chloride over 10 column volumes Fig 1 A is full-scale, Fig IB is a close-up view to show the dimers and multimers Figures 2A1 2A2, 2B, and 2C show separation of anti-IgE monoclonal antibody monomer from dimers and multimers Figs 2A1 and 2A2 were run on a RESOURCE Q™ anion-exchange column Fig 2A1 is full-scale Fig 2A2 is a close-up view to show the dimers and multimers Fig 2B is a run on Q-SEPHAROSE FAST-FLOW™ resin Fig 2C is a plot of monomer and dimer/multimer observed in fractions, where the open dots are monomer and the solid dots are dimer The monomer and dimer/multimer were determined using a SUPERDEX 200 HR™ 10/30 analytical size-exclusion column (Pharmacia Biotech) In all cases the columns were equilibrated in 25 mM Tπs/pH 8 The gradient used in the Fig 2A panels was 0 to 0 5 M sodium chloπde over 40 column volumes The gradient used for Fig 2B (Q-SEPHAROSE FAST-FLOW™) was 0 05 to 02 M NaCl over 10 column volumes Figures 3A-C show separation of BSA monomer and dimer on a RESOURCE Q™ anion-exchange column at pH 8 The column was equilibrated in 25 mM Tπs/pH 8 and eluted with a gradient from 0 125 to 0 275 M sodium chloride over 40 column volumes Fig 3A is purified monomer Fig 3B is purified dimer, and Fig 3C is a commercial preparation of BSA (Bayer) that contains both monomer and dimer Figures 4A-C show separation of BSA monomer and dimer on a RESOURCE Q™ anion-exchange column at pH 6 The column was equilibrated in 20 mM sodium phosphate/pH 6, and eluted with a linear gradient from 0 to 0 5 M sodium chloride over 10 column volumes Fig 4A is purified monomer Fig 4B is purified dimer, and Fig 4C is a commercial preparation of BSA (Bayer) that contains both monomer and dimer Figures 5A and 5B show separation of anti-IgE monoclonal antibody monomer from dimers and multimers on a RESOURCE S™ cation-exchange column at pH 6 The column was equilibrated in 20 mM sodium phosphate/pH 6, and eluted with a linear gradient from 0 to 005 M sodium chloride over 30 column volumes Fig 5A is the chromatogram from the separation, and Fig 5B is a plot of monomer and dimer/mul timer observed in fractions using the same method described in Figure 2, where the open dots are monomer and the solid dots are dimer Figures 6A and 6B show separation of BSA monomer and dimer on a RESOURCE S M cation- exchange column at pH 4 3 The column was equilibrated in 20 mM sodium acetate/pH 4 3, then eluted with a gradient from 0 to 1 M sodium chloride over 20 column volumes Fig 6A is puπfied monomer, and Fig 6B is puπfied dimer Detailed Description of the Preferred Embodiments Definitions As used herein, "polypeptide" refers generally to peptides and proteins having more than about ten ammo acids Preferably, the polypeptides are "exogenous," meaning that they are "heterologous," t e . foreign to the host cell being utilized, such as a human protein produced by E colt However, they may also be deπved from a native source in which they are present naturally Examples of mammalian polypeptides include molecules such as, e g , renin, a growth hormone, including human growth hormone, bovine growth hormone, growth hormone releasing factor, parathyroid hormone, thyroid stimulating hormone, hpoproteins, 1-antιtrypsιn, insulin A-chain, insulin B-chain, proinsuhn. thrombopoietin, follicle stimulating hormone, calcitonin, luteimzing hormone, glucagon, clotting factors such as factor VIIIC. factor IX, tissue factor, and von Willebrands factor, anti-clotting factors such as Protein C, atπal natuπetic factor, lung surfactant, a plasminogen activator, such as urokinase or human uπne or tissue-type plasminogen activator (t-PA), bombesin, thrombin. hemopoietic growth factor, tumor necrosis factor-alpha and -beta, enkephahnase, a serum albumin such as human serum albumin, mulleπan-inhibiting substance, relax A- chain, relaxin B-chain, prorelaxin, mouse gonadotropin-associated peptide, a microbial protein, such as beta- lactamase, DNase, mhibin; activin, vascular endothehal growth factor (VEGF), receptors for hormones or growth factors, lntegπn, protein A or D, rheumatoid factors, a neurotrophic factor such as brain-derived neurotrophic factor (BDNF), neurotrophm-3, -4, -5, or -6 (NT-3, NT-4, NT-5, or NT-6), or a nerve growth factor such as NGF, cardiotrophins (cardiac hypertrophy factor) such as cardiotrophin- 1 (CT-1), platelet- derived growth factor (PDGF), fibroblast growth factor such as aFGF and bFGF, epidermal growth factor (EGF), transforming growth factor (TGF) such as TGF-alpha and TGF-beta, including TGF- 1, TGF- 2, TGF- 3, TGF- 4 or TGF- 5, insulin-like growth factor-I and -II (IGF-I and IGF-II), des(l-3)-IGF-I (brain IGF-I), insulin-like growth factor binding proteins, CD proteins such as CD-3, CD-4, CD-8, and CD- 19, erythropoietin. osteoinductive factors, immunotoxins, a bone morphogenetic protein (BMP), an interferon such as mterferon- alpha, -beta, and -gamma, serum albumin, such as human serum albumin (HSA) or bovine serum albumin (BSA), colony stimulating factors (CSFs), e g , M-CSF, GM-CSF, and G-CSF, interleukins (ILs), e g . IL-1 to IL-10, antι-HER-2 antibody, superoxide dismutase, T-cell receptors, surface membrane proteins, decay accelerating factor, viral antigen such as, for example, a portion of the AIDS envelope, transport proteins, homing receptors, address s, regulatory proteins, antibodies, and fragments of any of the above-listed polypeptides The preferred polypeptides of interest are mammalian polypeptides Examples of such mammalian polypeptides include enzymes, hormones, cytokines, albumins, chemokines, immunotoxins, viral components, antibodies, neurotrophins, and antigens Suitable such polypeptides encompass polypeptides such as HSA, BSA, anti-IgE, antι-CD20, anti-IgG, t-PA, gpl20, anti-CDl la, antι-CD18, anti-VEGF, VEGF, TGF-beta, activin, inhibin, antι-HER-2, DNase, IGF-I, IGF-II. brain IGF-I, growth hormone, relaxm chains, growth hormone releasing factor, insulin chains or pro-msuhn, NGF, NT-3, BDNF, and urokinase Particularly preferred mammalian polypeptides include, e g , t-PA, gpl20 (Illb), antι-HER-2, anti-CDl la, antι-CD18, anti- VEGF, VEGF, BSA, HSA, antι-CD20, anti-IgE, anti-IgG, DNase, IGF-I, IGF-II, TGF-beta, IGFBP-3 IGFBP- 2, IGFBP-1 , growth hormone, NGF, NT-3, NT-4, NT-5. and NT-6 The polypeptide is more preferably an antibody or a serum albumin, more preferably. anti-IgE, anti-IgG, antι-Her-2. anti-CDl la. antι-CD18, anti- CD20, anti-VEGF, BSA, or HSA For purposes herein, the "mixture"' contains monomers and either dimers or multimers or both dimers and multimers Typically, the mixture is a biological fluid, which denotes any fluid derived from or containing cells, cell components, or cell products Biological fluids include, but are not limited to. fermentation broth, cell culture supernatants, cell lysates, cleared cell lysates. cell extracts, tissue extracts, blood, plasma, serum, sputum, semen, mucus, milk, and fractions thereof This definition includes cell-conditioned culture medium, which denotes a nutrient medium in which cells have been cultured and which contains cell products For purposes herein, "ion-exchange chromatography resin" refers to chromatography medium for anion- or cation-exchange separation As used herein, "elution salt" refers to an alkaline earth, alkali metal or ammonium salt, 1 e , a salt having a cation from the alkaline earth or alkali metal elements or an ammonium cation and having an inorganic or organic (hydrocarbon-based) anion Examples of such salts include sodium chloride, ammonium chloride. sodium citrate, potassium citrate, potassium chloride, magnesium chloride, calcium chloride, sodium phosphate, calcium phosphate, ammonium phosphate, magnesium phosphate, potassium phosphate, sodium sulfate, ammonium sulfate, potassium sulfate, magnesium sulfate, calcium sulfate, etc Preferred salts herein are chlorides or sulfates. The most preferred salt herein is sodium chloride As used herein, "multimers" refer to n-mers where n is 3-10, i.e , polymers that are not dimers out exclude aggregates In contrast to multimers, aggregates have a value for n of greater than 10, and/or a molecular weight of greater than 2 million daltons, and/or are species contained in the excluded volume of analytical size-exclusion chromatography columns such as SUPEROSE 6™ (Pharmacia) Modes for Carrying out the Invention This invention relates to a method of separating monomers of polypeptides from their dimers or multimers or both. The method involves placing the mixture of monomers and dimers and/or multimers, from whatever source, in an equilibration buffer at a pH in the range of about 4 and 9 depending on whether the resin used for chromatographic separation is a cation- or anion-exchange resin The resulting mixture is loaded onto either a cation-exchange or anion-exchange chromatography resin to capture all the n-mers (monomers, dimers, tπmers, tetramers, etc.) present in the mixture For ion-exchange column chromatography. ligands of general affinity can be used to achieve the desired selectivities and binding properties The loading takes place in a buffer at a pH of about 6-9 if the resm is anion-exchange and about 4-7 if the resin is cation-exchange The exact pH will depend, for example, on the lsoelectπc point of the polypeptide If the resin is a cation-exchange resin, pnor to loading the mixture, the matrix can be equilibrated using several column volumes of a dilute, weak acid (e.g., four column volumes of 20 mM acetic acid, pH 3, or of 20 mM phosphoric acid, pH about 2 8) Following equilibration, the mixture is added and the column can be washed one to several times, pnor to elution of the mixture, also using a weak acid solution such as a weak acetic acid or phosphoπc acid solution The buffer used for this purpose depends on, e.g , the polypeptide and the anionic or cationic nature of the resin. For anion-exchange, preferably the buffer is TRIS or phosphate buffer, for cation-exchange, the buffer is preferably acetate or phosphate buffer Ion-exchange chromatography is typically carried out at a temperature of about 18-25°C, preferably about 20°C (room temperature) The preferred column loading is about 1 ml resin per 20-30 mg total polypeptide Following adsorption of the n-mer molecules to the ion exchanger, the mixture is eluted by contacting the res with an elution salt having an appropπate ionic strength to displace the monomer from the matrix An elution salt gradient is used of about 0 to 1 M The gradient may be linear or stepwise Preferably the gradient is from about 0 to 500 mM elution salt, more preferably 50 to 200 mM elution salt, and most preferably, 0 to 50 mM elution salt Preferably the elution salt is a sodium salt, such as sodium chlonde, although other elution salts and concentration gradients, known to those of skill in the art, also find use herein The quantity of elution buffer can vary widely and will generally be in the range of about 2 to 40 column volumes preferably 10 to 40 column volumes Following elution, the eluate can be assayed for total monomeπc concentration Suitable cation-exchange resins herein include a wide variety of mateπals known in the art, including those capable of binding polypeptides over a wide pH range For example, carboxymethvlated, sulfonated, agarose-based, or polymeric polystyrene/divinyl benzene cation-exchange matrices are particularly preferred Other useful matrix materials include, but are not limited to, cellulose matrices, such as fibrous, microgranular, and beaded matrices, dextran, polyacrylate, polyvinyl, polystyrene, silica, and polyether matrices, and composites These matrices include, for example, CM52 CELLULOSE™ (Whatman, Inc ), S-HYPERD™ and CM SPHERODEX™ (Secpracor), SP SEPHAROSE FF™, DEAE SEPHAROSE FF™, CM-SEPHAROSE™, and RESOURCE S™ (Amersham Pharmacia Biotech AB), and JT BAKER CSx™ (J T Baker, Inc ), as well as those containing the functional hgand R-S0 3 , preferably sulfopropyl resins, such as TOYOPEARL SP550C™ (Tosohaas) and FRACTOGEL EMD™ S0 3 -650 (m) (Merck) Other suitable materials for use in cation- exchange chromatography are within the knowledge of those skilled in the art Anion-exchange chromatography is carried out using media appropπate therefor as are known in the art Suitable media include, e g , polymeric polystyrene/divinyl benzene resins and agarose-based resins, as well as agarose beads, dextran beads, polystyrene beads, media that compnse an insoluble particulate support deπvatized with tertiary or quaternary ammo groups , and supports deπvatized with tπmethylaminoethyl groups Examples of suitable such media include DE92™ (diethylaminoethyl cellulose Whatman), DEAE- CELLULOSE™ (Sigma), BAKERBOND ABX 40 mu™ (J T Baker, Inc ), DEAE resins such as FRACTOGEL EMD DEAE-650™ (EM Separations), FRACTOGEL EMD TMAE-650 (S) ™ (EM Science, Gibbstown, NJ), TSK gel DEAE-SPW™ (Tosohaas), DEAE-SEPHAROSE CL-6B™ and chelating SEPHAROSE™ (Amersham Pharmacia Biotech AB), DEAE MERE SEP 1000™ (Milhpore), and DEAE SPHERODEX™ (Sepracor), RESOURCE Q™ and Q SEPHAROSE™ (QSFF) (Amersham Pharmacia Biotech AB), MACRO-PEP Q™ (Bio-Rad Laboratories, Hercules, CA), Q- HYPERD™ (BioSepra. Inc , Marlborough, Mass), and the like Other suitable anion-exchange chromatography mateπals, as well as the selection and use of these mateπals for the present application, are conventional in the art Purified fractions of monomer obtained from the ion-exchange chromatography may be further processed by subjecting them to any appropπate technique designed for downstream processing and purification This will depend largely on the type of polypeptide and its intended use Only one ion-exchange step is necessary to effect the desired separation of monomer from dimers and/or multimers in a mixture, although the invention does not exclude using more such steps if desired in the upstream or downstream processing of the polypeptide The invention will be more fully understood by reference to the following examples They should not, however, be construed as limiting the scope of the invention All literature and patent citations herein are incorporated by reference EXAMPLE I This example shows the separation of anti-IgE monomers and bovine serum albumin monomers from dimers and multimers MATERIALS AND METHODS: Resins: Pharmacia Q-SEPHAROSE FAST FLOW™ 4mL to 235L bed volumes evaluated Pharmacia RESOURCE S and RESOURCE Q™ lmL prepacked columns JT Baker CSx™, 046 X 5cm, 5μ particles Proteins: A Humanized anti-IgE monoclonal antibodies (IgGi) available from Genentech, Inc pi ~ 7 5, designated as E25 and E26 WO 93/04173 published March 4, 1993 describes humanized anti-IgE antibodies wherein a muπne antibody directed against human IgE (MaEl 1) was used to provide the CDR regions that were substituted into an IgGl lmmunoglobulin framework (rhuMaE25) See also Cacia et al . Biochemistry. 35 1897-1903 (1996) for studies and further descriptions of E-25 B Monoclonal anti-IgE antibody prepared from the culture supernatants of an immortalized human myeloma cell line U266B1 (ATCC TIB 196) using affinity chromatography purification on an isolated anti-IgE antibody (Genentech MAE1) Specifically, five BALB/c female mice, age six weeks, were immunized in their foot pads with 10 μg of purified IgE in Ribi's adjuvant Subsequent injections were done in the same manner at one and three weeks after the initial immunizations Three days after the final injection, the inguinal and popliteal lymph nodes were removed and pooled and a single cell suspension was made by passing the tissue through steel gauze The cells were fused at a 4 1 ratio with mouse myeloma P3X63-Ag8 653 (ATCC CRL 1580) in high glucose (DMEM) containing 50% w/v polyethylene glycol 4000 Alternatively, the immunizations were done in a similar manner except that 30 μg of IgE per injection were used and IgE fragment 315-347 (Kabat) was assayed as a prefusion boost, or injections were given subcutaneously in two doses of 100 μg and a final booster of 50 μg, and spleen cells were used for the fusions The fused cells were then plated at a density of 2x105 per well in 96-well tissue culture plates After 24 hours HAT selective medium hypoxanthine/aminopteπn/thymidine, Sigma, #H0262) was added Of 1440 wells plated, 365 contained growing cells after HAT selection Fifteen days after the fusion, supernatants were tested for the presence of antibodies specific for human IgE using an enzyme-linked immunosorbent assay (ELISA) The ELISA was performed as follows, with all incubations done at room temperature Test plates (Nunc Immunoplate) were coated for 2 hours with rat anti- mouse IgG (Boehπnger Mannheim, #605-500) at 1 μg/ml in 50 mM sodium carbonate buffer, pH 9 6, then blocked with 05% bovine serum albumin in phosphate buffered saline (PBS) for 30 minutes, then washed four times with PBS containing 005% TWEEN 20™ (PBST) Test supernatants were added and incubated two hours with shaking, then washed four times with PBST Human IgE (puπfied from U266 cells as descπbed above) was added at 0 5 μg/ml and incubated for one hour with shaking, then washed four times in PBST Horseradish-peroxidase-conjugated goat anti-human IgE (Kirkegarrd & Perry Labs, #14-10-04, 0 5 mg/ml) was added at a 1 2500 dilution and incubated for one hour, then washed four times with PBST The plates were developed by adding 100 μl well of a solution containing 10 mg of o-phenylenediamine dihydrochloπde (Sigma, #P8287) and 10 μl of a 30% hydrogen peroxide solution in 25 ml phosphate citrate buffer, pH 5 0, and incubating for 15 minutes The reaction was stopped by adding 100 μl/well of 2 5 M sulfuπc acid Data were obtained by reading the plates in an automated ELISA plate reader at an absorbance of 490 nm For one antibody, 365 supernatants were tested and 100 were specific for human IgE Similar frequencies of IgE specificity were obtained when screening for the other antibodies C Bovine serum Albumin pi 4 7 and 4 9 (Radola. Biochim Biophvs Acta. 295 412-428 (1973)) •Bayer Corp P/N 81-024-2, "Bovine Albumin, Sulfhydryl Modified" (BSA Mix, blocked) •ICN Biomedical Inc P/N 810013, "Albumin Bovine" (BSA Mix, native) •BSA monomer and dimer prepared in house from Bayer BSA (BSA Monomer and BSA Dimer. respectively) Chromatography Systems: Hewlett-Packard 1090™ HPLC Pharmacia™ FPLC Detection at 215 or 280 nm Buffers: (see Table I for details) Purified water TπsΗCl Sodium acetate Sodium chloride Sodium phosphate Sodium citrate and citric acid Sample Preparation: Samples were diluted with the buffer used for equilibration (indicated in Table I below) to assure pH and conductivity matched starting column conditions All samples were 0 2-μm filtered prior to loading Chromatography: Samples were introduced to the column using either an automatic or manual injector All runs were performed at room temperature Fractions were collected manually or with a PHARMACIA FRAC 100 collector Chromatographic separation performance was evaluated by compaπng elution profiles of BSA stock reagent and puπfied BSA monomer and dimer, the same was done for IgE and the monoclonal antibodies (MAb) Separation of IgE and MAb from their dimers and multimers was further evaluated by analyzing elution fraction using analytical size-exclusion chromatography Plots of MAb MW forms vs Fraction number were created Recovery of IgE and MAb was determined spectrophotometπcally by measuring absorbance at 280nm RESULTS: The results are summarized in Table I below Table I MONOMER-DIMER/MULTIMER SEPARATIONS Separations were evaluated using polymeric polystyrene/divinyl benzene resins (RESOURCE Q and S™), a sihca-based resin (JT BAKER CSX™), and an agarose-based resin (Q-SEPHAROSE FAST FLOW™, QSFF) While separations were accomplished using any of these resins, separations worked especially well on Q-SEPHAROSE FAST FLOW™, RESOURCE Q™, and RESOURCE S™ The separation of BSA monomer and dimer from both suppliers looked very similar, suggesting the "Sulfhydryl Modified" material from Bayer did not alter the protein such that the species were easier to separate It can be seen that phosphate buffer at pH 6 worked well, but no protein bound to the cation- or anion-exchange columns when 20 mM citrate buffer at pH 6 was used as equilibration buffer Citrate buffer would be expected to work for both anion- and cation- exchange at a lower concentration, e g , about 5 mM Recovery of monomeπc IgE and MAbs to IgE on anion-exchange resins was typically greater than 90% at greater than 99 5% purity Figures 1A and IB show anion-exchange (RESOURCE™ Q) chromatograms in the separation of IgE monomers from dimers and multimers Figures 2A1 and 2A2 show anion-exchange (RESOURCE™ Q) chromatograms in the separation of anti-IgE MAb monomers from dimers and multimers Fig 2B shows an anion-exchange (Q-SEPHAROSE FAST-FLOW™) chromatogram in the separation of anti-IgE MAb monomers from dimers and multimers SEC (SUPERDEX 200 HR 10/30™) was used as an analytical method to determine the amount of monomer and multimer in samples from the ion- exchange separation, and Figure 2C shows the SEC analysis of fractions from Figure 2B Separation of BSA monomer from dimer was readily achieved on anion-exchange resins at pH 8 and pH 6 See Figures 3A-C and 4A-C for chromatograms in the separation of BSA monomers from dimers and multimers by anion-exchange (RESOURCE™ Q) at pH 8 (Tns buffer) and at pH 6 (phosphate buffer), respectively Recovery and purity of MAb monomer from the cation-exchange resin was comparable to that of the anion-exchange resin Figures 5A-B show cation-exchange (RESOURCE™ S) chromatograms in the separation of anti-IgE MAb monomers from dimers and multimers at pH 6 (phosphate buffer) Separations of BSA on cation-exchange resins could be performed at pH 4 6 and 4 3, 4 3 being somewhat better Figures 6A- B show cation-exchange (RESOURCE™ S) chromatograms in the separation of BSA monomers from dimers and multimers at pH 4 3 (acetate buffer) In summary, mixtures of polypeptide mers were subjected to cation- or anion-exchange chromatography using a variety of resins and under a variety of pH and elution salt conditions, and successful separation was achieved Based on results from four proteins with basic and acidic isoelectric points (two IgG, MAbs, IgE and serum albumin), the method demonstrates general applicability to separation of polypeptide monomers from their dimers and multimers

Claims: WHAT IS CLAIMED IS 1 A method is disclosed for separating a polypeptide monomer from a mixture comprising dimers or multimers or both, wherein the method compπses applying the mixture to a cation-exchange or anion- exchange chromatography resin in a buffer, wherein if the resin is cation-exchange, the pH of the buffer is about 4-7, and wherein if the resm is anion-exchange, the pH of the buffer is about 6-9, and elutmg the mixture at a gradient of about 0-1 M of an elution salt, wherein the monomer is separated from the dimers or multimers or both present in the mixture 2 The method of claim 1 wherein the polypeptide is an antibody or a serum albumin 3 The method of claim 2 wherein the antibody is anti-IgE, anti-IgG, antι-Her-2, anti-CDl la, anti-CD 18 , antι-CD20, or anti- VEGF 4 The method of claim 2 wherein the serum albumin is bovine serum albumin 5 The method of claim 1 wherein the ion-exchange resin is a cation-exchange resin 6 The method of claim 1 wherein the ion-exchange resin is an anion-exchange resin 7 The method of claim 1 wherein the gradient is linear 8 The method of claim 1 wherein the gradient is stepwise 9 The method of claim 1 wherein the elution salt is a sodium salt 10 The method of claim 9 wherein the elution salt is sodium chloπde 11 The method of claim 1 wherein the gradient is from 0 to 500 mM elution salt 12 The method of claim 1 wherein the gradient is from 50 to 200 mM elution salt 13 The method of claim 1 wherein the gradient is from 0 to 50 mM elution salt

Inventors: ANSALDI DEBORAH, LESTER PHILIP, ANSALDI, DEBORAH, LESTER, PHILIP
Applicants: GENENTECH INC, GENENTECH, INC.
Application year: 1999
Main classification: C07K1
IPC codes: B01J20, C07K1, C07K14, C07K16, G01N30