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  • B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
  • B01J20/281—Sorbents specially adapted for preparative, analytical or investigative chromatography
  • B01J20/286—Phases chemically bonded to a substrate, e.g. to silica or to polymers
• • B—PERFORMING OPERATIONS; TRANSPORTING
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  • B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
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  • B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
  • B01J20/30—Processes for preparing, regenerating, or reactivating
  • B01J20/32—Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating
  • B01J20/3202—Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating characterised by the carrier, support or substrate used for impregnation or coating
  • B01J20/3206—Organic carriers, supports or substrates
  • B01J20/3208—Polymeric carriers, supports or substrates
  • B01J20/321—Polymeric carriers, supports or substrates consisting of a polymer obtained by reactions involving only carbon to carbon unsaturated bonds
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  • B01J20/32—Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating
  • B01J20/3214—Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating characterised by the method for obtaining this coating or impregnating
  • B01J20/3217—Resulting in a chemical bond between the coating or impregnating layer and the carrier, support or substrate, e.g. a covalent bond
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  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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  • B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
  • B01J20/30—Processes for preparing, regenerating, or reactivating
  • B01J20/32—Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating
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  • B01J20/3217—Resulting in a chemical bond between the coating or impregnating layer and the carrier, support or substrate, e.g. a covalent bond
  • B01J20/3219—Resulting in a chemical bond between the coating or impregnating layer and the carrier, support or substrate, e.g. a covalent bond involving a particular spacer or linking group, e.g. for attaching an active group
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  • B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
  • B01J20/30—Processes for preparing, regenerating, or reactivating
  • B01J20/32—Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating
  • B01J20/3231—Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating characterised by the coating or impregnating layer
  • B01J20/3242—Layers with a functional group, e.g. an affinity material, a ligand, a reactant or a complexing group
  • B01J20/3244—Non-macromolecular compounds
  • B01J20/3246—Non-macromolecular compounds having a well defined chemical structure
  • B01J20/3248—Non-macromolecular compounds having a well defined chemical structure the functional group or the linking, spacer or anchoring group as a whole comprising at least one type of heteroatom selected from a nitrogen, oxygen or sulfur, these atoms not being part of the carrier as such
  • B01J20/3251—Non-macromolecular compounds having a well defined chemical structure the functional group or the linking, spacer or anchoring group as a whole comprising at least one type of heteroatom selected from a nitrogen, oxygen or sulfur, these atoms not being part of the carrier as such comprising at least two different types of heteroatoms selected from nitrogen, oxygen or sulphur
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
  • B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
  • B01J20/30—Processes for preparing, regenerating, or reactivating
  • B01J20/32—Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating
  • B01J20/3231—Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating characterised by the coating or impregnating layer
  • B01J20/3242—Layers with a functional group, e.g. an affinity material, a ligand, a reactant or a complexing group
  • B01J20/3244—Non-macromolecular compounds
  • B01J20/3246—Non-macromolecular compounds having a well defined chemical structure
  • B01J20/3248—Non-macromolecular compounds having a well defined chemical structure the functional group or the linking, spacer or anchoring group as a whole comprising at least one type of heteroatom selected from a nitrogen, oxygen or sulfur, these atoms not being part of the carrier as such
  • B01J20/3255—Non-macromolecular compounds having a well defined chemical structure the functional group or the linking, spacer or anchoring group as a whole comprising at least one type of heteroatom selected from a nitrogen, oxygen or sulfur, these atoms not being part of the carrier as such comprising a cyclic structure containing at least one of the heteroatoms nitrogen, oxygen or sulfur, e.g. heterocyclic or heteroaromatic structures
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  • B01J20/30—Processes for preparing, regenerating, or reactivating
  • B01J20/32—Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating
  • B01J20/3231—Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating characterised by the coating or impregnating layer
  • B01J20/3242—Layers with a functional group, e.g. an affinity material, a ligand, a reactant or a complexing group
  • B01J20/3268—Macromolecular compounds
  • B01J20/3272—Polymers obtained by reactions otherwise than involving only carbon to carbon unsaturated bonds
  • B01J20/3274—Proteins, nucleic acids, polysaccharides, antibodies or antigens
• • C—CHEMISTRY; METALLURGY
  • C07—ORGANIC CHEMISTRY
  • C07K—PEPTIDES
  • C07K1/00—General methods for the preparation of peptides, i.e. processes for the organic chemical preparation of peptides or proteins of any length
  • C07K1/14—Extraction; Separation; Purification
  • C07K1/16—Extraction; Separation; Purification by chromatography
  • C07K1/22—Affinity chromatography or related techniques based upon selective absorption processes
• • C—CHEMISTRY; METALLURGY
  • C07—ORGANIC CHEMISTRY
  • C07K—PEPTIDES
  • C07K14/00—Peptides having more than 20 amino acids; Gastrins; Somatostatins; Melanotropins; Derivatives thereof
  • C07K14/81—Protease inhibitors
  • C07K14/8107—Endopeptidase (E.C. 3.4.21-99) inhibitors
  • C07K14/811—Serine protease (E.C. 3.4.21) inhibitors
  • C07K14/8121—Serpins
  • C07K14/8128—Antithrombin III
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08B—POLYSACCHARIDES; DERIVATIVES THEREOF
  • C08B37/00—Preparation of polysaccharides not provided for in groups C08B1/00 - C08B35/00; Derivatives thereof
  • C08B37/006—Heteroglycans, i.e. polysaccharides having more than one sugar residue in the main chain in either alternating or less regular sequence; Gellans; Succinoglycans; Arabinogalactans; Tragacanth or gum tragacanth or traganth from Astragalus; Gum Karaya from Sterculia urens; Gum Ghatti from Anogeissus latifolia; Derivatives thereof
  • C08B37/0063—Glycosaminoglycans or mucopolysaccharides, e.g. keratan sulfate; Derivatives thereof, e.g. fucoidan
  • C08B37/0075—Heparin; Heparan sulfate; Derivatives thereof, e.g. heparosan; Purification or extraction methods thereof
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  • B01J2220/00—Aspects relating to sorbent materials
  • B01J2220/50—Aspects relating to the use of sorbent or filter aid materials
  • B01J2220/54—Sorbents specially adapted for analytical or investigative chromatography

Definitions

• the present invention relates to polymers having hydrazide functional ligands on their surfaces and to heparin functional polymers prepared from such hydrazide functional polymers and methods of preparing and using both.
• Immobilized heparin is widely used as a ligand in affinity chromatography for purification, preparation, separation and investigation of substances with biological activity. Heparin is immobilized for chromatographic purposes by a variety of -known processes onto solid supports. See, for example "Application of Immobilized Heparins for Isolation of Human Antithrombin III" by G. Mitra, E. Hall and I. Mitra, Biotechnology and Bioengineering. Vol. XXVm, pp. 217-222 (1986).
• East German Patent No. 276,814A1 describes coupling of nonderivatized heparin to hydrazide-derivatized polyacrylamide particles in an aqueous buffer at a pH less than or no greater than 3.8.
• This patent attributes improved coupling efficiency, greater stability of the coupling linkage and greater mechanical strength of the support to its process.
• the matrices claimed still have relatively poor mechanical stability and would be minimally useful for large scale separation processes where multiple uses and high flow rates are desired.
• the acidic conditions used for the preparation of the supports would result in some desulfation and hydrolysis of the heparin molecule, thus decreasing its biological specificity and usefulness for affinity chromatography purposes.
• heparin functional affinity chromatography supports to purify antithrombin III is well known (see e.g. United States Patent No. 3,842,061), and it is the method of choice for providing antithrombin III for therapeutic use. Since antithrombin III is a very important but very expensive substance useful to treat cardiovascular disease, any significant improvement in processes for its isolation and purification is potentially very valuable. It is one of the objectives of the present invention to provide novel compositions and processes for the production of purified antithrombin III and other molecules with group specific affinity for heparin i.e., heparin-interactive molecules.
• the present invention provides improved heparin functional polymers and hydrazide functional polymers derived from azlactone functional polymers.
• the present invention provides improved heparin functional affinity chromatography supports.
• Such supports are based on hydrazide functional supports derived from azlactone functional supports.
• the supports of the invention provide a surprisingly high binding efficiency of target molecules to the heparin functional support, a stable coupling linkage, mild reaction conditions to minimize degradation of heparin and high stability of the support to bases used to remove nontarget molecules from the heparin support.
• This invention also provides hydrazide functional polymer supports derived from azlactone functional polymer supports.
• this invention also describes a method of providing a heparin functional surface comprising derivatizing an azlactone functional polymer surface by reacting with hydrazine, providing a hydrazide, and further derivatizing by reacting with heparin.
• the invention also describes a method of effecting interaction of a heparin-interactive molecule with a heparin functional surface comprising providing a surface which is an azlactone functional polymer which is derivatized by reaction with hydrazine to provide a hydrazide which is further derivatized by reaction with heparin and exposing the surface to the heparin-interactive molecule.
• surface as used above is defined broadly as the outer or topmost boundary of a material.
• heparin is used generally throughout this application and includes natural heparin, derivatized heparin, heparin salts, low molecular weight heparin, various chemically modified heparins which will react with hydrazide functional groups and synthetic heparin-like molecules. It will be understood by those skilled in the art that both carbonyl functional heparin and carbonyl functional heparin-like molecules will provide some or all of the advantages of the invention.
• the heparin used in most of the Examples of the invention is an aldehyde functional sodium heparin available commercially from Diosynth Laboratories Inc., (Chicago, IL). Other suitable commercially available heparins are available from Sigma Chemical Co., Calbiochem, and Scientific Protein Laboratories.
• This invention provides improved processes for separating and purifying biologically active target molecules. More particularly, a su ⁇ risingly improved process for the purification of antithrombin III is described. Detailed Description
• European Patent Application No. 0392,735 A2 based on U.S. Serial No. 07/335,835 which was filed in the United States on October 4, 1989 describes the use of azlactone-functional polymer supports useful for a variety of purposes including providing biologically active supports.
• Useful reactive polymers, e.g., polymeric supports, of the invention which are hydrazide functional may be prepared by reaction of known azlactone-functional polymers, e.g., polymer supports, such as those described in European Patent Application No. 0392,735A2, with hydrazine. The reaction is carried out under su ⁇ risingly mild conditions, i.e. at ambient temperature (about 25 ⁇ C) and is rapidly completed (e.g. 1 to 24 hours, preferably 1 to 3 hours under laboratory conditions).
• a preferred azlactone-functional polymer support for use in the present invention is commercially available as Emphaze ® Biosupport Medium AB 1 from 3M, St. Paul, MN.
• the biosupport medium is prepared from commercially available methylene bis(acrylamide) monomer and 2-vinyl-4,4- dimethylazlactone as generally described in the European application cited above.
• the reaction is carried out in water (preferably) and/or a nonreactive solvent. An excess of hydrazine is conveniently used. Gentle warming can be used if it is desired to accelerate the reaction, but external warming is generally not needed.
• the reaction is generally carried out with azlactone functional beads, the azlactone functional polymer need not be in a bead form but can also be in any of the alternative forms such as films, matrices, membranes, coated membranes, other coated structures including organic and inorganic substrates and the like.
• Azlactone functional membranes and matrices are disclosed in United States Patent Application Serial Number 07/776,601 filed October 11, 1991, United States Patent Application Serial Number 07/896,107 filed June 9, 1992, and PCT Publication WO 93/06925.
• the azlactone-functional polymer supports used herein may also be prepared in situ and then reacted with hydrazine.
• the hydrazide functional polymers are particularly useful for reaction of heparin as described herein, the hydrazide groups can also be advantageously reacted with other molecules containing aldehyde groups and with molecules containing ketone groups.
• the hydrazide functional polymers of the invention can be made according to known procedures (see e.g. European Patent Application 0392,735A2 and United States Patent Applications 07/776,601 and 07/896,107) into supports and other useful forms e.g. , beads, films, matrices, membranes, or coatings on organic or inorganic substrates.
• hydrazide-functional reactive supports derived from azlactone-functional polymer supports can be carried out with reactive supports based on any of the known azlactone-functional supports which comprise an azlactone functional group of the Formula I
• R 1 and R 2 each independently are an alkyl group having 1 to 14 carbon atoms, a cycloalkyl group having 3 to 14 carbon atoms, an aryl group having 5 to 12 ring atoms, an arenyl group having 6 to 26 carbon and 0 to 3 S, N, and nonperoxidic O heteroatoms, or R 1 and R 2 taken together with the carbon to which they are joined form a carbocyclic ring containing 4 to 12 ring atoms, n is an integer 0 or 1 and Su represents the support.
• R 1 , R 2 , and n are described in Formula I above.
• the preferred support group is obtained by reaction of an azlactone of Formula I in which R 1 and R 2 are methyl and n is zero with hydrazine to provide the hydrazide functional reactive support shown below.
• the reaction of the above described hydrazide-functional reactive support is carried out with heparin to bond the heparin covalently to the hydrazide group under very mild conditions, for example under ambient conditions (e.g. 25 °C) in a buffered solution.
• Suitable buffers provide a pH range of about 5 to 10 and are e.g., sodium acetate, sodium phosphate and sodium carbonate in the presence or absence of salts, e.g. sodium sulfate.
• the reaction is relatively rapid and is usually essentially complete in less than 100 hours although small amounts of reaction continue for many hours e.g. up to 144 hours. Preferably the reaction time is 24 to 72 hours or less. The reaction may be accelerated by heating if desired.
• the heparin used to provide the heparin functional affinity chromatography supports of the present invention contains reactive carbonyl groups such as aldehyde groups.
• Heparin preparations containing aldehyde groups are commercially available and certain of these may be used without further treatment to react with hydrazide functional reactive supports.
• the number of carbonyl groups in commercially available naturally occurring heparin can be enhanced by simple oxidation of the heparin as described in the art, e.g. with a periodate salt.
• Some of the heparin preparations available commercially are chemically modified to enhance the number of aldehyde groups present. Reaction of a hydrazide functional support with heparin yields a heparin-functional support of the formula below wherein Hep is a heparin residue.
• heparin functional polymers prepared by the process of the present invention may be used in any convenient form such as films, membranes, coated membranes, beads or matrices or coated onto any desired support such as organic or inorganic supports, but are most conveniently used as beads in affinity chromatographic columns.
• Such heparin functional beads are slurry packed into typical glass, metal or plastic chromatographic columns and equilibrated with buffer, e.g. commercially available 0.05 M tris(hydroxymethyl)aminomethane (TRIS) buffer, generally with added sodium chloride, e.g. at 0.1 to 0.5 M sodium chloride, preferably at about 0.15 M sodium chloride at or near neutral pH e.g. at pH 7.4.
• buffer e.g. commercially available 0.05 M tris(hydroxymethyl)aminomethane (TRIS) buffer
• sodium chloride e.g. at 0.1 to 0.5 M sodium chloride, preferably at about 0.15 M sodium chloride at or near neutral pH e.g. at pH 7.4.
• the column of beads is then subjected to a salt rinse by rinsing first with a volume of 0.05 M TRIS buffer containing 0.15 M sodium chloride (loading buffer), followed by an equal volume of 4.0 M sodium chloride in 0.05 M TRIS and finally using an equal volume of the loading buffer.
• Purified antithrombin III obtained from the American Red Cross, was used to quantitate the capacity of the columns to hold this substance.
• antithrombin III capacities as high as 11.10 mg/mL are observed when compared to commercial columns providing a capacity of 3.86 under the same conditions.
• the use of the heparin functional affinity chromatography supports of the present invention is advantageously carried out on a large scale for the production of commercially useful amounts of AT III in large columns.
• heparin functional affinity chromatography columns of the invention have also been found to be useful in purification of human growth factors.
• Heparin functional chromatographic supports are known to be gradually contaminated by molecules, e.g. proteins, other than the target molecules. Such nontarget molecules are said to undergo nonspecific binding which gradually blocks the heparin binding sites.
• the supports of the invention have been found to be significantly less susceptible to nonspecific binding than certain commercially available supports i.e. the supports of the invention have low nonspecific binding.
• Cleaning of nonspecific molecules from heparin supports is usually carried out with organic or inorganic bases. Inorganic bases are preferred because they are easier to remove from target molecules.
• the supports of the present invention have been found to demonstrate su ⁇ risingly good stability when washed with inorganic bases such as aqueous sodium hydroxide, retaining over 90% of their binding capacity when washed with 0.1 N aqueous sodium hydroxide and greater than 80% when washed with 1.0 N aqueous sodium hydroxide.
• Su represents the polymeric support media (methylenebisacrylamide) which were prepared according to a variation (described hereinafter in
• Example 2 of the method of Example 4E of United States Application No. 335,835 and published as European Patent Application 0392,735A2 and commercially available as Emphaze ® Biosupport Medium AB 1 from 3M Company, St. Paul, MN, was weighed into a 50 mL centrifuge tube and 30 mL of 64% hydrazine in water was added. The mixture warmed slightly due to the initiation of reaction during addition and was stirred on a rotating mixer for two hours. The beads were then separated by filtration, washed repeatedly with distilled water until the wash water was neutral according to pH paper and stored in a refrigerator.
• Example 2 Alternative Preparation of Hydrazide Functional Beads An organic solution of 348 mL of heptane, 188 mL of toluene and 0.13 g of polymeric stabilizer as described in Example 4E of European Patent Application 0392,735A2 was heated with stirring to 35 °C. To this stirred solution under a nitrogen atmosphere was added 0.72 mL of 2-vinyl-4,4- dimethylazlactone monomer.
• aqueous solution was made from 13.33 g of methylenebis(acrylamide) available from Sigma Chemical Company, 90 mL of isopropyl alcohol, 60 mL of deionized water which was stirred at low heat until dissolved, then 0.55 g of sodium persulfate was added and the mixture was stirred until it dissolved.
• Example 3 Preparation of Hydrazide Functional Beads-Hydrazine Concentration Study Aliquots of Emphaze Biosupport Medium AB 1 beads (125 mg) were weighed into each of four separate Bio-Rad Poly-Prep ® polypropylene columns and reacted with 5 mL of hydrazine solution in deionized water for two hours while being agitated on a rotating mixer. The breakoff tip on each column was removed, the excess hydrazine solution drained off, and the derivatized beads were washed with deionized water until the eluate was neutral to pH paper. The hydrazide content of the beads was measured according to the protocol described by G.T. Hermanson, A.K.
• hydrazide functionalities can be obtained from azlactone-functional beads even when using concentrations of hydrazine as low as 0.2 M for derivatization.
• hydrazide functional supports can be prepared from other azlactone functional supports such as those described in Examples 5 of European Patent Application 0392,735A2.
• Example 2 To a stirred solution of 32 mL of anhydrous hydrazine in 968 mL of distilled water was added slowly over 2.5 minutes 63 g of the lot of azlactone-functional beads used in Example 1. The mixture was stirred for 2 hours and 20 minutes, then the beads were separated by filtration using a sintered glass funnel and washed with distilled water until the water wash was neutral to pH paper. The beads were slurried with distilled water, allowed to settle for thirty minutes and the supernatant was poured off to remove unwanted extra fine beads. The procedure was repeated. A third repeat produced a clear supernatant without fine beads. The measured hydrazide content was 22.4 micromoles per milliliter of beads. The desired hydrazide functional beads were stored in a refrigerator.
• Example 1 To 5 mL of buffered solution of 0.1 M aqueous sodium acetate (pH 5.0) and 5 mg/mL of sodium heparin (obtained from Diosynth, Chicago, IL as Batch No. 129) was added 1 mL of the hydrazide functional beads obtained in Example 1. After two hours of reaction the beads were isolated by filtration, washed with 5 mL of 0.1 M aqueous sodium acetate buffer, then washed with 10 mL of 1 M sodium chloride in 20 millimolar sodium phosphate (pH 7.0) then washed with distilled water.
• pH 7.0 millimolar sodium phosphate
• heparin adduct To assess the presence of heparin adduct a sample of the beads was mixed with 0.5 mL of an aqueous toluidine blue solution (1 % by weight). When the excess toluidine blue was removed by repeated washings with distilled water, the beads were reddish-pu ⁇ le in color, indicative of a characteristic heparin-toluidine blue reaction.
• heparin with hydrazide functional beads was repeated as described hereinabove except the proportion of reactants was 5 mL of buffered heparin and 2 mL of hydrazide functional beads.
• the heparin functional heads obtained were evaluated qualitatively and found to bind antithrombin HI.
• Example 6 Preparation of Heparin Functional Beads Hydrazide functional beads prepared as described in Example 4 from commercially available Emphaze ® Biosupport Medium AB 1 were reacted at three separate concentrations of heparin (25, 50 and 75 mg/mL) by adding the heparin solution in a volume equal to the volume of hydrazide-functional beads. The reaction was carried out by mixing at about 25 °C in sodium acetate buffer, pH 5.0. After 72 hours the supernatant solution was discarded, the beads were rinsed with 10 volumes of water, followed by 10 volumes of 2.0 M sodium chloride at neutral pH, followed by 2 additional rinses with 10 volumes of water.
• Example 7 Evaluation of Heparin Functional Beads for Antithrombin III Capacity
• Example 6 Separate columns were prepared to evaluate the beads prepared in Example 6 for antithrombin III capacity and to compare them to commercially available heparin-Sepharose ® CL-6B beads (available from Pharmacia Biotech, Piscataway, NJ).
• the heparin beads were slurry packed in glass columns (3 mm by 5 cm) and equilibrated and loaded using 0.15 M sodium chloride in 0.05 M TRIS buffer (available from Sigma Chemical Company, St. Louis, MO), pH 7.4. Each column of beads was subjected to rinsing in the FPLC ® liquid chromatography instrument (available from Pharmacia) by rinsing with the loading buffer (3.5 mL), followed by 3.5 mL of 4.0 M sodium chloride in 0.05 M TRIS, pH 7.4 and reequilibrated with 3.5 mL of the loading buffer. Purified antithrombin III from the American Red Cross was diluted to a concentration of 1.0 mg/mL in 0.15 M sodium chloride-0.05 M TRIS buffer.
• the measured antithrombin III (ATIII) capacities were:
• Heparin products of four descriptions were obtained from Scientific Protein Laboratories (Waunakee, WI). These heparin salts were dissolved at 100 mg/mL in 0.1 M acetate buffer, pH 5.0, and reacted with hydrazide functional beads from Example 4 at a 1:3 volume ratio of beads to heparin solution for 72 hours at about 25 * C, with mixing. Rinsing of these heparin functional bead preparations was performed according to Example 6.
• heparin functional beads were packed into 3 mm by 5 cm chromatographic columns and tested for ATHI capacity, as described in Example 7. Resultant ATIII capacities were as follows:
• Frozen human blood plasma (American Red Cross, Rockville, MD) was thawed at 4 * C, centrifuged to remove cryo-precipitated material, and filtered through 0.8 ⁇ m and 0.2 ⁇ m seive sizes to remove additional particulates.
• 10.0 mL of plasma (29 column volumes) were loaded onto the chromatographic column at 200 cm/hr, followed by 10.0 mL of loading buffer to rinse the column.
• Non-specifically bound proteins were removed with 7.0 mL (20 column volumes) of 0.30 M sodium chloride in 0.05 M TRIS buffer, pH 7.4.
• Elution of ATm was effected by a sodium chloride gradient step of 1.0 M sodium chloride with subsequent rinses of 2.0 M sodium chloride and 4.0 M sodium chloride to ensure complete removal of residual proteins. Fractions were collected during each step.
• Absorbance readings of the fractions of the 0.30 M sodium chloride fraction are indicative of non-specifically bound proteins.
• non-specifically bound proteins were reduced by about 35% on the heparin-Emphaze ® support. This is qualitatively apparent in the chromatographic tracings, as the heparin-Emphaze ® support returned more quickly to baseline absorbance after loading, and revealed a smaller peak of eluted proteins upon the 0.30 M sodium chloride rinse.
• Heparin was coupled to hydrazide-activated Emphaze ® Biosupport Medium AB 1 beads prepared according to Example 4 at three pH levels and in increasing molarities of aqueous sodium sulfate, using a heparin challenge of 100 mg/mL and a 48-hour coupling time.
• the buffers used were dependent on the desired pH, with coupling buffer of 0.1 M sodium acetate at pH 5.07, 0.1 M sodium phosphate at pH 7.0, and 0.1 M sodium carbonate at pH 10.0. The following results were obtained:
• the experiment demonstrates that the heparin coupling reaction was more efficient in terms of producing high ATm capacity at about pH 5 or about pH 7 than at about pH 10.
• the salt effect varied with pH.

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• 1994
  • 1994-08-12 CA CA 2168038 patent/CA2168038A1/en not_active Abandoned
  • 1994-08-12 JP JP7507090A patent/JPH09501719A/ja active Pending
  • 1994-08-12 CN CN 94193121 patent/CN1130386A/zh active Pending
  • 1994-08-12 WO PCT/US1994/009149 patent/WO1995005400A1/en not_active Application Discontinuation
  • 1994-08-12 EP EP94925859A patent/EP0714412A1/de not_active Withdrawn

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