WO1995005240A1 - Composite biological-molecule-accretion material - Google Patents
Composite biological-molecule-accretion material Download PDFInfo
- Publication number
- WO1995005240A1 WO1995005240A1 PCT/US1994/009187 US9409187W WO9505240A1 WO 1995005240 A1 WO1995005240 A1 WO 1995005240A1 US 9409187 W US9409187 W US 9409187W WO 9505240 A1 WO9505240 A1 WO 9505240A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- binding
- filter
- aqueous solution
- molecules
- component
- Prior art date
Links
Classifications
-
- 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
- B01J20/02—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
- B01J20/20—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising free carbon; comprising carbon obtained by carbonising processes
-
- 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
- B01J20/22—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising organic material
- B01J20/26—Synthetic macromolecular compounds
- B01J20/261—Synthetic macromolecular compounds obtained by reactions only involving carbon to carbon unsaturated bonds
-
- 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
- B01J20/22—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising organic material
- B01J20/26—Synthetic macromolecular compounds
- B01J20/262—Synthetic macromolecular compounds obtained otherwise than by reactions only involving carbon to carbon unsaturated bonds, e.g. obtained by polycondensation
-
- 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
- B01J20/3202—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
- B01J20/3204—Inorganic carriers, supports or substrates
-
- 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
- B01J20/3268—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
-
- 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
- B01J20/3291—Characterised by the shape of the carrier, the coating or the obtained coated product
- B01J20/3295—Coatings made of particles, nanoparticles, fibers, nanofibers
-
- 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
- B01J2220/00—Aspects relating to sorbent materials
- B01J2220/40—Aspects relating to the composition of sorbent or filter aid materials
- B01J2220/46—Materials comprising a mixture of inorganic and organic materials
-
- 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
- B01J2220/00—Aspects relating to sorbent materials
- B01J2220/40—Aspects relating to the composition of sorbent or filter aid materials
- B01J2220/48—Sorbents characterised by the starting material used for their preparation
- B01J2220/4812—Sorbents characterised by the starting material used for their preparation the starting material being of organic character
- B01J2220/4825—Polysaccharides or cellulose materials, e.g. starch, chitin, sawdust, wood, straw, cotton
-
- 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
- B01J2220/00—Aspects relating to sorbent materials
- B01J2220/50—Aspects relating to the use of sorbent or filter aid materials
- B01J2220/56—Use in the form of a bed
Definitions
- the present invention relates generally to filters and other devices for removing undesired chemicals from solution, and more particularly to a composite biological-molecule-accretion material for extracting desired target biological molecules from aqueous solution and substantially permanently binding to those molecules.
- a composite biological-molecule-accretion material for extracting desired target biological molecules from aqueous solution and substantially permanently binding to those molecules.
- SUBSTITUTE SHEET (ROLE 26 chemically labeled target molecule from aqueous solution and substantially permanently binding to it.
- Another object is to provide such a material that provides for such removal and binding to a relatively wide variety of molecules such as the target molecules listed above.
- Yet another object is to provide such a material that has a relatively long working life.
- Another important object of the invention is to provide such a material that can be readily and easily disposed of after its working life is over. It is also an object of the invention to provide such a material that can be easily and cost-effectively manufactured.
- one aspect of the invention includes a composite biological-molecule-accretion material for extracting (or removing) desired target biological molecules from aqueous solution and substantially permanently binding to those molecules.
- the material includes a first component designed with a binding affinity for proteins and peptides in such solution, and a second component designed with a binding affinity for nucleic acids in such solution.
- the material is capable of being formed in a body for passing such solution through it, and such passing has the effect of removing the proteins, peptides and nucleic acids from such solution and binding them to the body. That binding is substantially permanent so that subsequent passage of additional aqueous solution will not unbind substantially the accreted proteins, peptides and nucleic acids from the body.
- the first component consists essentially of dextran-coated activated charcoal particles
- the second component consists essentially of an anion-exchange resin and a cation-exchange resin.
- the preferred relative volumes of both components are 1:1, and the relative volumes of the two ion-exchange resins is 1:1.
- relative volumes for the composition of the preferred version of the material is 2 parts dextran-coated charcoal particles to 1 part anion- exchange resin to 1 part cation-exchange resin.
- Another aspect of the present invention includes a method of filtering target biological molecules out of water.
- the method includes the step of forming a filter bed by soaking a mixture of dextran-coated, activated charcoal in water for a preselected time period, adding to the mixture an ion-exchange resin with a preselected charge-sensitivity, drying the mixture, and rehydrating the mixture.
- the method also includes the step of placing the filter bed into a water- filtration apparatus with an input and an output, and passing water containing the target biological molecules through the filtration apparatus to capture substantially the target biological molecules in the filter bed.
- Fig. 1 is an isometric view of the accretion material of the present invention after being formed in a body (or filter bed) and being placed into conventional water-filtration apparatus.
- Fig. 2 is a side-sectional view through line 2-2 of Fig. 1 with the accretion material being formed in a body, and with solid lines indicating an unswelled condition of the material, and dashed lines indicating a swelled condition of the same.
- Fig. 3 is a fragmentary, greatly enlarged, schematic view of the unswelled body of accretion material shown in Fig. 2.
- Fig. 4 is a fragmentary, greatly enlarged, schematic view of the swelled body of accretion material shown in Fig. 2.
- Fig. 5 is a greatly enlarged view of unswelled charcoal particles forming part of the accretion material.
- Fig. 6 shows the charcoal particles of Fig. 5 after swelling.
- Fig. 7 shows the charcoal particles of Fig. 6 after being coated with dextran substance.
- Fig. 8 shows the charcoal particles of Fig. 7 being mixed with anion- and cation-exchange resins, with the resins being indicated schematically by encircled + 's and -'s.
- Fig. 9 shows the charcoal particles of Fig. 8 after being mixed with the resins.
- Fig. 10 is like Fig. 2 only that it shows the swelled condition of the body of accretion material in solid lines, and shows introduction into the conventional water-filtration apparatus of aqueous solution containing desired target biological molecules, with the solution passing through the body.
- Material 10 is formed in a body 12, with body 12 being placed in a conventional water-filtration apparatus 14. In its place in apparatus 14, body 12 will allow a to-be-described aqueous solution to pass through it, with such passing having the effect of removing certain target molecules such as proteins, peptides and nucleic acids from such solution and binding them to body 12.
- the binding is substantially permanent in that subsequent passage of additional aqueous solution will not unbind substantially the accreted proteins, peptides and nucleic acids from the body.
- material 10 does not unbind substantially from the accreted proteins, peptides and nucleic acids even when subsequent passage of additional aqueous solution includes relatively harsh components such as detergents.
- conventional water-filtration apparatus 14 is constructed with an input 16 and an output 18, and includes a receptacle 20 for receiving effluent from output 18.
- Receptacle 20 is formed with a suitable port 22, which may be an aspiration port, for dispensing effluent from the receptacle.
- the port may be fitted with the usual control valve (undepicted).
- a suitable support screen (undepicted) may be provided within apparatus 14 and around body 12 to hold material 10 in place so that the to-be-described aqueous solution must pass through body 12 after being poured through input 16.
- the invention may include an arrangement of two or more apparatuses, like apparatus 14, with each such apparatus having a body of material, an input, and output, each like those described above.
- such arrangement would include a vertical stacking of such apparatuses, with the bottom apparatus being placed over a receptacle like receptacle 20.
- a one-stage filtration system is one like that depicted in Fig. 1.
- a two- stage filtration system is one that has a vertical stack of two apparatuses, like apparatus 14, with the bottom apparatus being placed over a receptacle like receptacle 20.
- suitable support structure for stabilizing the stack.
- body 12 is shown in an unswelled condition with solid lines between bracketed area A, and in a swelled condition up to a dashed line between bracketed area B. The significance of the unswelled/swelled condition will be described.
- the unswelled condition of body 12 is also shown in a greatly enlarged, schematic view in Fig. 4.
- Fig. 5 shows the swelled condition in a greatly enlarged, schematic view.
- material 10 includes a first component 10a (Fig. 7) designed with a binding affinity for proteins and peptides in aqueous solution such as solution 24 shown in to-be-described Fig. 10.
- material 10 also includes a second component 10b (Figs. 8-9) designed with a binding affinity for nucleic acids in such solution.
- Figs. 5-7 show formation of first component 10a
- Figs. 8-9 show introduction and then mixing of second component 10b with first component 10a.
- the first component includes, and preferably consists essentially of, dextran-coated activated charcoal particles, which exhibit the requisite binding affinity for proteins and peptides.
- the second component includes, and preferably consists essentially of, an anion-exchange resin and a cation-exchange resin. Those resins exhibit the requisite binding affinity for nucleic acids.
- Material 10 is preferably formed of 1 part by volume of first component 10a and 1 part by volume of second component 10b.
- Second component 10b is preferably formed of 1 part by volume anion-exchange resin and 1 part by volume cation-exchange resin.
- the preferred formulation of material 10 is 2 parts first component 10a to 1 part anion-exchange resin and 1 part cation-exchange resin.
- the total volume of ion exchange resin (both anion- and cation-exchange resins) in the preferred embodiment is about one-third to one-half of the volume of the dextran-coated activated charcoal.
- suitable quantities of suitable filler material, such as course sand, may be added to increase flow rate through material 10.
- First component 10a may also be thought of as a filter-matrix component formed from first and second subcomponents.
- the first subcomponent is preferably activated charcoal particles
- the second component is a water-soluble, high-molecular-weight substance such as dextran.
- Second component 10b may also be thought of as a charge- carrier component distributed substantially in the filter-matrix component to provide a plurality of charged sites therein.
- the filter-matrix component (first component 10a) and the charge-carrier component (second component 10b) are usable in a desired thickness (as body 12) in a filter system (apparatus 14) to provide a filter that defines paths through its thickness for allowing the aqueous solution (e.g. solution 24 of Fig. 10) to pass, and removes substantially the target biological substances by binding them to the charged sites.
- aqueous solution e.g. solution 24 of Fig.
- Material 10 being formed as body 12 may also be characterized in yet another way as a filter bed for use in a filter system to remove target biological substances contained in an aqueous solution (e.g. solution 24 of Fig. 10).
- First component 10a may be characterized as means for forming a filter matrix that is porous substantially only to that portion of such solution that does not include the target biological substances.
- the filter-matrix-forming means includes first and second subcomponents, activated charcoal particles and a water- soluble, high-molecular-weight substance, respectively.
- the high-molecular-weight substance is preferably dextran, and it is mixed with the charcoal particles to coat them.
- Second component 10b may be characterized as a charge-carrier component distributed substantially in the filter-matrix-forming means to provide a plurality of charged sites therein.
- the filter-matrix-forming means and the charge-carrier component are usable in a desired thickness (i.e. body 12) in a filter system (i.e. apparatus 14) to provide a filter bed that defines paths through its thickness for allowing the aqueous solution (solution 24 of Fig. 10) to pass, and removes substantially the target biological substances by binding them to the charged sites.
- first component 10a being formed by soaking a mixture of activated charcoal lOa ⁇ and dextran 10a 2 in water (undepicted) for a preselected time period.
- Figs. 5-6 show the swelling of charcoal 10a ⁇ in water prior to addition of dextran 10a 2 .
- the presently preferred time period is about one hour.
- second component 10b taking the form of preselected anion- and cation-exchange resins (shown schematically as encircled + 's and -'s), is mixed with first component 10a.
- the resins forming second component 10b have a preselected charge-sensitivity, and preferred ones will be described below in connection with example formulations.
- the mixture is aspirated to remove residual water and allowed to dry, and then rehydrated with a suitable amount of water so that it swells. Applicant has found that such rehydration promotes formation of the above-described filter matrix within body 12, and lessens the possibility that some target molecules will be missed when the first amount of the aqueous solution (e.g. solution 24 of Fig. 10) is passed through body 12.
- the first amount of the aqueous solution e.g. solution 24 of Fig.
- Material 10 was prepared using 45% activated charcoal such as that marketed under the trademark "NORIT A”, 25% Whatman DE52 pre-swollen microgranular anion exchanger (diethylaminoethyl cellulose, catalog number 4057
- EXAMPLE II Material 10 was prepared as in example I and placed in a filter structure like apparatus 14. Solutions containing 24 ⁇ Ci of 32 P-CTP DNA probe in 0.1% sodium dodecyl sulfate solution were passed through material 10. Despite the harsh character of a detergent like the sodium dodecyl sulfate solution, only 2 ⁇ Ci of the 32 P-CTP DNA probe passed through the material, indicating a permanent binding efficiency of greater than 99%.
- EXAMPLE III Material 10 was prepared as in example I and placed in a filter structure like apparatus 14. 49 ⁇ Ci of 32 P-labeled, 1450 base-pair DNA fragment in a 50% formamide solution was passed through the material. Analysis of the effluent from apparatus 14 revealed .3 ⁇ Ci of radio-isotope passed through the material, indicating a permanent binding efficiency of greater than 99%.
- EXAMPLE IV Material 10 was prepared as in example I and placed in a filter structure like apparatus 14. A mixed waste solution of HPLC waste (40% acetonitrile/60% water - by volume) containing radiolabeled peptide was passed through the material. Specifically, 300-mL of the solution containing approximately 4.5 ⁇ Ci 125 I- ?EP ( ?-endorphine) was passed through the material. Analysis of the effluent from apparatus 14 revealed less than 0.0004 ⁇ Ci of radio- isotope passed through the material, indicating a permanent binding efficiency of greater than 99.99%. Over a 48-hour time period, water was intermittently passed through the material, and analysis of the effluent after such time period indicated no change in the 99.99+ % permanent binding efficiency.
- a prolonged use of material 10 in a one-stage filtration system was ran over an 8-month period to remove 35 S radioactive nucleotides. Specifically, an amount of material 10 having a wet volume of 100 ml was formed in a body like body 12 and placed in a filter structure like apparatus 14. 58 units of aqueous solutions containing ⁇ S radioactive nucleotides were passed through the amount of material 10, and the average % of radioactive material absorbed by the amount of that material was 91.3%.
- Material 10 worked as described above with acidic or basic aqueous solutions. It has also indicated a relatively long working life, i.e. an amount of material 10 with a wet volume of 100 ml continues to exhibit the above binding efficiency of 98-99% after weekly use in a biological laboratory for approximately six months.
- buffer-like components may be added to material 10. It is presently proposed to use solid forms of acid- or base-leaching substances. For example, solid masses or nuggets of NaOH may be uniformly distributed in the material, using suitable mixing apparatus, to act as a buffer when acidic solutions are passed through material 10. Likewise, suitable weak acids may be used, in solid masses/nuggets, to act as a buffer when basic solutions are passed through material 10.
- a method may be practiced for extracting desired target biological molecules from aqueous solution and substantially permanently binding them to that solid.
- the method includes the step of forming a solid with a binding affinity for such molecules.
- the forming step is preferably practiced by making the above-described biological-molecule-accretion material 10.
- the method also includes the steps of shaping the solid into a body and placing the body into a water-filtration apparatus with an input and an output, and passing aqueous solution containing such molecules through the filtration apparatus to remove them substantially from such solution, and substantially permanently bind them to the solid.
- Use of material 10 also involves a method of filtering target biological molecules out of water. That method includes a step of forming a filter bed by the substeps of soaking a mixture of dextran and activated charcoal in water for a preselected time period, adding to the mixture an ion-exchange resin with a preselected charge-sensitivity, drying the mixture, and then rehydrating the mixture.
- the second step involves placing the filter bed into a water-filtration apparatus with an input and an output
- the third step involves passing water containing the target biological molecules through the filtration apparatus to capture substantially the target biological molecules in the filter bed.
- material 10 When material 10 has exceeded its working life, it is dried by aspiration, removed from water-filtration apparatus 14, and disposed of as solid radioactive waste. Any effluent from aspirating may be poured down a drain if sufficiently low radioactivity is detected. It is presently contemplated that state and federal regulations do, or may soon, require extremely low or no radioactivity for effluent poured down a drain to a public water supply. With those regulations in mind, multiple-stage filtration systems utilizing material 10 may be used until a sufficiently low radioactivity is detected.
- material 10 could be tailored to be selective to certain types of molecules as opposed to being designed for removal of the entire class of target molecules listed above. For example, if one wanted to remove only those molecules with negative charges in aqueous solution (such as D ⁇ A compounds), then only a cation-exchange resin would be used as second component 10b.
- the present invention achieves the above objects by providing a composite biological-molecule-accretion material for extracting desired target biological molecules from aqueous solution and substantially permanently binding to those molecules. That material overcomes the drawbacks of prior-art materials, and provides for such extraction/removal and binding to a relatively wide variety of molecules such as the target molecules listed above.
- the invented material has presently shown to have a relatively long working life, and when its working life is over the material can be disposed of readily and easily. Based on its preferred embodiment, the material can also be easily and cost-effectively manufactured. Accordingly, while a preferred embodiment of the invention has been described herein, it is appreciated that modifications are possible that are within the scope of the invention.
Landscapes
- Chemical & Material Sciences (AREA)
- Analytical Chemistry (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Inorganic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Health & Medical Sciences (AREA)
- Biochemistry (AREA)
- General Health & Medical Sciences (AREA)
- Molecular Biology (AREA)
- Engineering & Computer Science (AREA)
- Nanotechnology (AREA)
- Treatment Of Liquids With Adsorbents In General (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
- Curing Cements, Concrete, And Artificial Stone (AREA)
Abstract
Description
Claims
Priority Applications (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP7507115A JPH09509920A (en) | 1993-08-13 | 1994-08-12 | Composite biological molecule attachment material |
AU75651/94A AU682391B2 (en) | 1993-08-13 | 1994-08-12 | Composite biological-molecule-accretion material |
EP94925877A EP0713423A4 (en) | 1993-08-13 | 1994-08-12 | Composite biological-molecule-accretion material |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US10641593A | 1993-08-13 | 1993-08-13 | |
US08/106,415 | 1993-08-13 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO1995005240A1 true WO1995005240A1 (en) | 1995-02-23 |
Family
ID=22311298
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/US1994/009187 WO1995005240A1 (en) | 1993-08-13 | 1994-08-12 | Composite biological-molecule-accretion material |
Country Status (5)
Country | Link |
---|---|
EP (1) | EP0713423A4 (en) |
JP (1) | JPH09509920A (en) |
AU (1) | AU682391B2 (en) |
CA (1) | CA2168767A1 (en) |
WO (1) | WO1995005240A1 (en) |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4135943A (en) * | 1973-05-31 | 1979-01-23 | Toyo Jozo Company, Ltd. | Novel selective adsorbents |
US4897467A (en) * | 1986-02-13 | 1990-01-30 | Gelinnovation H.B. | Nitrilophoric EDA-adsorbents |
US5232853A (en) * | 1989-12-28 | 1993-08-03 | Takeda Chemical Industries, Ltd. | Method for producing (2r,3s)-3-hydroxy-2-methylbutyrate by microbial reduction |
Family Cites Families (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3420709A (en) * | 1965-04-29 | 1969-01-07 | Diamond Shamrock Corp | Liquid purification by adsorption |
US3847889A (en) * | 1969-12-22 | 1974-11-12 | Exploaterings Ab Tbf | Protein separation by insoluble,amphoteric ion exchangers |
US3753655A (en) * | 1971-11-09 | 1973-08-21 | B Schreiber | Process for isolation and separation of thyroid hormones |
US4187120A (en) * | 1978-05-30 | 1980-02-05 | Ecodyne Corporation | Method for purification of polyhydric alcohols |
-
1994
- 1994-08-12 AU AU75651/94A patent/AU682391B2/en not_active Ceased
- 1994-08-12 CA CA 2168767 patent/CA2168767A1/en not_active Abandoned
- 1994-08-12 WO PCT/US1994/009187 patent/WO1995005240A1/en not_active Application Discontinuation
- 1994-08-12 JP JP7507115A patent/JPH09509920A/en active Pending
- 1994-08-12 EP EP94925877A patent/EP0713423A4/en not_active Withdrawn
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4135943A (en) * | 1973-05-31 | 1979-01-23 | Toyo Jozo Company, Ltd. | Novel selective adsorbents |
US4897467A (en) * | 1986-02-13 | 1990-01-30 | Gelinnovation H.B. | Nitrilophoric EDA-adsorbents |
US5232853A (en) * | 1989-12-28 | 1993-08-03 | Takeda Chemical Industries, Ltd. | Method for producing (2r,3s)-3-hydroxy-2-methylbutyrate by microbial reduction |
Non-Patent Citations (1)
Title |
---|
See also references of EP0713423A4 * |
Also Published As
Publication number | Publication date |
---|---|
JPH09509920A (en) | 1997-10-07 |
AU7565194A (en) | 1995-03-14 |
AU682391B2 (en) | 1997-10-02 |
EP0713423A1 (en) | 1996-05-29 |
EP0713423A4 (en) | 1996-09-11 |
CA2168767A1 (en) | 1995-02-23 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
KR20050088164A (en) | Isolation of nucleic acids | |
Chase | Affinity separations utilising immobilised monoclonal antibodies—a new tool for the biochemical engineer | |
Eveleigh et al. | Immunochemical characteristics and preparative application of agarose-based immunosorbents | |
US4594135A (en) | Process and apparatus for electrically desorbing components selectively sorbed on granules | |
JP2564335B2 (en) | Method for isolating and purifying nucleic acids from biological samples | |
US7052609B2 (en) | Method for regeneration of adsorbent matrices | |
US20110117596A1 (en) | Composite sorbent material, its preparation and its use | |
KR20070057266A (en) | Composite filtration article | |
JPH102891A (en) | Selective recognition of solute in chromatographic medium by artificial affinity | |
JP2004501054A5 (en) | ||
JPH10500615A (en) | Chromatographic sorbents using mercapto heterocyclic ligands | |
Baran et al. | Efficient adsorption of hemoglobin from aqueous solutions by hybrid monolithic cryogel column | |
WO2001061355A1 (en) | Molecular impriniting compositions and methods for binding and analyzing macromolecules | |
AU682391B2 (en) | Composite biological-molecule-accretion material | |
SK283578B6 (en) | Magnetic particles, method for the preparation thereof and their use in purification of solutions | |
US4969995A (en) | Removal of metal ions from aqueous solution | |
EP1599286B1 (en) | A method of preparing multi-modal anion-exchange ligands | |
Schwartz et al. | Desalting of proteins, peptides, and amino acids on polyacrylamide gel | |
JPH0337976B2 (en) | ||
Hearn et al. | High-performance liquid chromatography of amino acids, peptides and proteins: CXI. Retention behaviour of proteins with macroporous tentacle-type anion exchangers | |
WO1996006134A9 (en) | Responsive gels for selective removal of a target from an environment and methods therefor | |
WO2005069310A1 (en) | Method for cleaning radioactive aqueous solutions | |
Burton | Affinity chromatography | |
Sakata et al. | Chromatographic removal of host cell DNA from cellular products using columns packed with cationic copolymer beads | |
Hashimoto | Macroporous synthetic hydrophilic resin-based packings for the separation of biopolymers |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
AK | Designated states |
Kind code of ref document: A1 Designated state(s): AT AU BB BG BR BY CA CH CN CZ DE DK ES FI GB HU JP KP KR KZ LK LU LV MG MN MW NL NO NZ PL PT RO RU SD SE SK UA US UZ VN |
|
AL | Designated countries for regional patents |
Kind code of ref document: A1 Designated state(s): AT BE CH DE DK ES FR GB GR IE IT LU MC NL PT SE BF BJ CF CG CI CM GA GN ML MR NE SN TD TG |
|
DFPE | Request for preliminary examination filed prior to expiration of 19th month from priority date (pct application filed before 20040101) | ||
121 | Ep: the epo has been informed by wipo that ep was designated in this application | ||
WWE | Wipo information: entry into national phase |
Ref document number: 2168767 Country of ref document: CA |
|
WWE | Wipo information: entry into national phase |
Ref document number: 1994925877 Country of ref document: EP |
|
WWP | Wipo information: published in national office |
Ref document number: 1994925877 Country of ref document: EP |
|
REG | Reference to national code |
Ref country code: DE Ref legal event code: 8642 |
|
ENP | Entry into the national phase |
Ref document number: 1998 24935 Country of ref document: US Date of ref document: 19980217 Kind code of ref document: A |
|
WWW | Wipo information: withdrawn in national office |
Ref document number: 1994925877 Country of ref document: EP |