EP1183327A1 - Metal chelating filters and metal chelate filters - Google Patents

Metal chelating filters and metal chelate filters

Info

Publication number
EP1183327A1
EP1183327A1 EP00926556A EP00926556A EP1183327A1 EP 1183327 A1 EP1183327 A1 EP 1183327A1 EP 00926556 A EP00926556 A EP 00926556A EP 00926556 A EP00926556 A EP 00926556A EP 1183327 A1 EP1183327 A1 EP 1183327A1
Authority
EP
European Patent Office
Prior art keywords
filter
metal
linker
species
groups
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Withdrawn
Application number
EP00926556A
Other languages
German (de)
French (fr)
Inventor
Edward Hanna Kachab
Graeme Ross Barnett
Martin Smith
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Abbott Rapid Diagnostics Pty Ltd
Whatman International Ltd
Original Assignee
Panbio Pty Ltd
Whatman International Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Panbio Pty Ltd, Whatman International Ltd filed Critical Panbio Pty Ltd
Publication of EP1183327A1 publication Critical patent/EP1183327A1/en
Withdrawn legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D67/00Processes specially adapted for manufacturing semi-permeable membranes for separation processes or apparatus
    • B01D67/0081After-treatment of organic or inorganic membranes
    • B01D67/0093Chemical modification
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D69/00Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
    • B01D69/14Dynamic membranes
    • B01D69/141Heterogeneous membranes, e.g. containing dispersed material; Mixed matrix membranes
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J45/00Ion-exchange in which a complex or a chelate is formed; Use of material as complex or chelate forming ion-exchangers; Treatment of material for improving the complex or chelate forming ion-exchange properties

Definitions

  • the present invention relates generally to the separation and analysis of molecules.
  • the invention relates to the isolation of these molecules from a mixture in a fluid phase on a porous membrane comprising a metal chelating filter or metal chelate filter
  • porous membrane is in a microplate format, tube, vial
  • bioaffinity molecules may then be analysed using a wide variety of methodologies including the employment of specific bioaffinity molecules, specific
  • the molecules may be released
  • Microporous membranes as support matrices have also
  • Ligand immobilised membranes provide a compact
  • Ligands have been immobilised on support materials in the
  • membranes have been initially coated with a water-insoluble protein such as Zein,
  • Porous membrane materials used for non-covalent ligand immobilisation in affinity chromatography have included materials such
  • PVDF polyvinylidene fluoride
  • Non-covalent binding results in random orientation of the ligand and can
  • peptides and the oligonucleotides are not only covalently bound to the
  • peptides may be coupled to a solid support via
  • biomolecules as ligands onto activated membranes are:-
  • N ⁇ 2+ and Zn 2+ are the most widely.
  • Suitable donor ligands include ammo acids histidine, cysteine and tryptophan Since natural proteins rarely contain suitably arranged donor
  • ligands recombinant proteins are engineered with a metal chelate
  • binding tag at either the C- or N- terminal ends of the protein for
  • microporous filter materials such as Sepharose (IDA-sepharose, Pharmacia), magnetic beads (Ni-NTA Magnetic Agarose Beads, Qiagen) and microtitre plates (Ni-NTA HisSorb, Qiagen).
  • Iminodiacetic acid (IDA) has also been covalently attached to a stable IDA
  • MPS microporous plastic sheet
  • the MPS matrix is an inert polymeric microporous sheet that contains
  • silica that can either be fu ⁇ ctionalised with ion exchange groups or affinity ligands solely for the purpose of protein purification.
  • metal chelate filter or metal chelating species filter when processed in accordance with the invention to provide a metal chelate filter or metal chelating species filter may provide a number of
  • the invention provides a ligand immobilisation
  • the invention provides for the capture and
  • the invention has particularity in the diagnostics, high-throughput screening, and biotechnology industries.
  • the invention has particularity in the diagnostics, high-throughput screening, and biotechnology industries.
  • the invention has particularity in the diagnostics, high-throughput screening, and biotechnology industries.
  • the invention has particularity in the diagnostics, high-throughput screening, and biotechnology industries.
  • the invention has particularity in the diagnostics, high-throughput screening, and biotechnology industries.
  • the process of the invention includes the following variants:-
  • the invention includes within its scope products produced
  • filter means a porous material
  • filter media having an average pore size in the region of 0.01 to 1000 microns and more preferably 0.1-5 microns.
  • the filter may be formed from either fully or partly from
  • accessible functional groups such as -Si-OH groups or which may be treated with a reagent to provide accessible functional groups including -OH, -Si-OH, -NH 2 and other amine
  • groups including alkylamino, thiols, cyanobromides, aldehydes, carboxylates, sulfonylchlorides, ketones, halogens,
  • haloacetyl inclusive of chloroacetyl, iodoacetyl or bromoacetyl and
  • epoxy groups may be attached directly to the filter or by an appropriate spacer arm or linker.
  • porous filter materials comprising
  • polyamides inclusive of nylon, cellulose acetate, nitrocellulose,
  • polyvinylidene fluoride or other fluoropolymers, polysulfone, paper, or
  • linkers and/or a metal chelating species or a metal chelate may also be suitable media for the attachment of linkers and/or a metal chelating species or a metal chelate.
  • linker as used herein means any spacer group
  • the linker prior to use has an appropriate functional group as
  • linker can be utilised which may include substituted or
  • unsubstituted alkyl groups having from one to twenty, or more preferably one to six carbons, and wherein the alkyl groups may be linear or
  • branched Linkers may also comprise substituted or unsubstituted aryl or aryl alkyl groups
  • the linking group may be variable comprising a single methylene or a plurality of methylene groups
  • linking group may also comprise peptides or branched peptides inclusive
  • linkers include, for example, both linear,
  • polyamides polyethyleneimines, polyarylene sulfides, polysiloxanes,
  • polyimides polyacetates, dend ⁇ mers and dendrime ⁇ c-like molecules or
  • linker as used
  • cross-linking species or reagents used to couple the metal chelate or metal chelating species to accessible functional
  • cross-linking species either on the filter or which have been produced by de ⁇ vatisation
  • Such cross-linking species are referred to by way of example to the
  • microfibre In a preferred embodiment of the invention, microfibre
  • glass filters made from silica are especially adapted for use in the
  • Such filters have silanol (Si-OH) functional groups as part of
  • the filter matrix may be derivatised using a suitable reagent to
  • such reagents may have an in-built linker or the linker may be pre-attached to the metal
  • the metal chelating species may be any metal chelating species.
  • the metal chelating species includes a functional group capable of reacting with Si-OH groups such as triethoxysilane or trimethoxysilane.
  • silanisation reagents which may be used for the
  • filters comprise accessible amine groups on the surface of the filter.
  • linker or metal chelating species with linker attached may
  • peptides as linkers.
  • filters may be treated with a reagent such as ethylenediamine which may be
  • a short linker in a suitable solvent such as acetonitrile and usually in the presence of a catalyst such as triethylamine.
  • Suitable reactive groups may need to be
  • Such hydroxyl groups can be directly used for the attachment of a filter
  • hydroxyl groups may be further derivatised with silanisation reagents
  • Such reagents for example may include cyanogen bromide, tosyl chloride, N-hydroxy succinamide, diamines, hydrazine and its
  • dialdehydes such as glutaraldehyde, carbodiimides, and
  • MCS metal chelating species
  • metal chelating species include iminodiacetic acid, nitrilotriacetic acid, diethylenetriamine
  • metal chelate means the metal chelating species having a metal coordinated thereto. Chelation type associations make use of metal ions such as but not limited to, the
  • metal chelate filters of the invention which include the
  • metal can be used for immobilisation of ligands that coordinate with the
  • species may be attached to the filter by a covalent bond, charge
  • metal chelating species may be attached to the filter via a linker by either of the
  • the linker may be pre-attached to the metal chelating species followed by attachment of
  • suitable protecting groups include Fmoc, Boc, trityl groups and any other protecting groups.
  • branched species such as lysine or branched polymeric species such as dendrimers may increase
  • FIG. 1 shows a derivatised glass fibre filter
  • imidodiacetic acid metal chelate attached to the filter with a linker.
  • FIG. 2 shows a polyacrylamide gel with a low range
  • dendrimer-HRP conjugate at about 73 kDa is readily apparent in the
  • FIG. 3 shows results of an experiment using Zn 2+ immobilised on the filter in which HRP, HRP-antibody conjugate and HRP-dendrimer conjugate were passed through metal chelate filter discs
  • FIG. 4 shows free HRP, HRP-antibody and E5 dendrimer-
  • metal chelate glass fibre filters (Whatman GF/B, GF/C and GF/F).
  • metal ion used was Zn 2+ .
  • FIG. 5 shows results of an experiment in which E5-
  • dendrimer conjugate, diluent only, E5 dend ⁇ mer only and E5 dendrimer- antibody conjugate were passed through Zn 2+ metal chelate filter discs
  • FIG 6 of a polyacrylamide gel shows that metal chelate filter discs efficiently capture a 6 x histidine tagged protein from a
  • the concentration of the tagged protein was found to be approximately five times higher in material eluted from the discs than material that flowed through the discs
  • TNBS trmitrobenzynesulfonic acid
  • HBTU Benzotriazole-N,N,N',N',-Tetramethyl-Uronium-Hexafluorophosphate
  • HOBt N-Hydroxybenzothazole
  • DIPEA diisopropylethylamine
  • the Fmoc group was then tested with a TNBS test.
  • the deprotected filters were treated with nitrilotriacetic acid
  • Nitrilotriacetic acid derivatised filter discs were each placed on a sintered glass funnel connected to a vacuum pump. The discs were
  • FIG. 1 shows an example of a molecular structure showing the derivatised filter, linker(s) and the metal chelate.
  • FIG. 2 shows examples of different molar ratios of E5 dendrimer-HRP conjugations.
  • FIG. 3 shows results of an experiment using Zn 2+
  • HRP-dendrimer conjugate were passed through metal chelate filter discs
  • FIG. 4 shows free HRP, HRP-antibody and E5 dendrimer-
  • metal chelate glass fibre filters (Whatman GF/B, GF/C and GF/F).
  • E5-dendrimer conjugate, diluent only, E5 dendrimer only and E5 dendrimer-antibody conjugate were passed through Zn 2+ metal
  • TMB substrate was applied and washed as described above.
  • FIG. 5 shows the results. It can be seen that the presence
  • FIG 6 of a polyacrylamide gel shows that metal chelate filter discs efficiently captured a hexahistidme tagged protein from a
  • MC and MCS filters may be incorporated into an immunoassay filter plate, column, syringe filter housing or tube for a wide
  • the MC and MCS filters may also be embodied with a second type filter such as an FTATM Gene Guard
  • the MC and MCS filters may further embodied with a second filter such as to restrict
  • the bound genetic material such as human genomic DNA can be ultimately removed by use of reagents such as restriction endonucleases
  • the fragments of the restriction digest can be incubated in the presence of a MC filter harbouring
  • probes could be derivatised at their 5' or 3' ends with a metal chelate tail such as a hexahistidme tag or dendrimer e g PAMAM
  • genomic DNA E g traditional methodology (other than FTA) of purification yields genomic DNA as a soluble fraction After restriction digest, or in vitro
  • template nucleic acid can be produced that is in a position to be captured by such
  • oligonucleotide probes may be mixed with the genomic DNA whereby the
  • DNA/probe hybrids formed can be captured on MC
  • a second probe conjugated to a detector label e g
  • Oligonucleotides, mRNA and cDNA coupled to dendrimers or other species capable of acting as a ligand, for example a hexahistidine tag, can be
  • dendrimers or a hexahistidine may be added directly to a MC filter sheet to form a microarray suitable for analysis without the need for a multi-well plate format.
  • proteins including a hexahistidine tail may be immobilised on a metal chelate filter. This will
  • Unstable recombinant protein may be immobilized on MC filters quickly and at room temperature
  • incorporating an MC filter would enable the user to rapidly immobilize potential drugs or target
  • the method could also be combined with a FTA filter for simultaneous
  • MCF-captured proteins may then be tested for function in bioassays.
  • An indicator of cellular events is the change in kinase activity. Interaction at the cell surface is
  • a synthetic kinase substrate is incubated with the kinase sample of
  • the substrate was engineered to contain a 6xHis
  • a MC filter will have greater specificity than Promega's streptavidin filter that is commonly used together with biotin tagged peptides.
  • the isolated library compound may then be further interrogated to
  • target molecule may be conjugated to a dendrimer or hexahistidine tag either of which
  • dendrimer or hexahistidine may then be further
  • Overlapping peptide sequences may be tagged with a hexahistidme tail or dendrimers and immobilised onto metal chelate filters for subsequent screening
  • metal chelate filter bottoms could be used to capture hexahistidine or dendrimer tagged or target molecules
  • product may be engineered to bear a hexahistidme sequence This product may then readily be captured onto a metal chelate filter
  • a deep well multiwell plate encapsulating a MC filter at the bottom of each well may be constructed
  • each well may be carried out mammalian, yeast or bacterial culture without fluid dripping through the filter bottoms Protein
  • FTA and MC filter materials within the same device may be constructed.
  • the cells will lyse, the cells
  • episomal and/or genomic DNA will bind to the FTA, and the recombinant protein containing an
  • the recombinant protein can be harvested and assayed. If the protein collected is of interest
  • Metalloproteases are implicated with the onset of
  • metastasis being part of the mechanism utilised by
  • Recombinant proteins and enzymes expressing a tag such as a hexahistidine tail may be assayed directly from culture to determine a) levels of
  • each tube, column or well will amplify the capacity
  • microorganisms or parts of microorganisms such as antigens or nucleic acids

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Inorganic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Organic Chemistry (AREA)
  • Dispersion Chemistry (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)
  • Treatment Of Liquids With Adsorbents In General (AREA)

Abstract

A method of making a metal chelate filter or metal chelating species filter including the following step of: treating a filter having a pore size of 0.01 to 1000 microns and accessible functional groups with a metal chelate or metal chelating species to provide the metal chelate filter or metal chelating filter species.

Description

TITLE
"METAL CHELATING FILTERS AND METAL CHELATE FILTERS"
BACKGROUND OF THE INVENTION
Field of the invention
The present invention relates generally to the separation and analysis of molecules. In particular, the invention relates to the isolation of these molecules from a mixture in a fluid phase on a porous membrane comprising a metal chelating filter or metal chelate filter
whereby the porous membrane is in a microplate format, tube, vial,
syringe filter housing, column or similar arrangement. The captured
molecules may then be analysed using a wide variety of methodologies including the employment of specific bioaffinity molecules, specific
chemical reactions, specific hybridisation probes, or interrogation using
lasers, UV light, IR, etc. Alternatively, the molecules may be released
from the porous membrane and collected for analysis.
Description of the background art
Molecular separation based on affinity interaction has
proven to be a valuable tool for the purification of biological or related
molecules (Affinity Chromatography: a practical approach, P. D. G. Dean, W. S. Johnson, and F. A. Middle (eds.). IRL Press, Oxford, 1986. Affinity
Separations: a practical approach, P. Matejtschuk (ed.) IRL Press,
Oxford, 1997). The principle of affinity separation relies on the selective
recognition and interaction of the desired biological or related substance,
present in a fluid phase, with its complementary ligand immobilised on a solid support as it passes over the support in a column. The desired material is retained on the column whilst most impurities are flushed through. The binding is reversible allowing for the recovery of the desired
molecules by applying an appropriate eluting solution to the column
which disrupts the ligand-binding interaction, by either changing the ionic
strength, the pH, or adding a competing reagent, thereby releasing the desired molecules from the column. The types of ligands which may be
used in affinity separation is very broad and include antibodies, antigens, enzymes, peptides, oligonucleotides, isolated receptors, carbohydrates,
and recombinant proteins. There is now a wide range of support matrices that have been used in affinity chromatography, e.g. Agarose (Sepharose
(Pharmacia)), cross-linked dextran (sephadex (Pharmacia)), cross-linked
cellulose (Matrex Cellufine (Amicon)), controlled pore glass (CPG
(Pierce)), and silica (Hypersil WP 300 (Shandon)) beads.
Microporous membranes as support matrices have also
been used in the art. Ligand immobilised membranes provide a compact,
easy to manipulate system allowing for the capture of the desired
molecule and the removal of unwanted components in a fluid phase at
higher throughput and faster processing times than possible with column chromatography. This is due to the fast diffusion rates possible on
membranes. Ligands have been immobilised on support materials in the
form of microporous membranes used in affinity chromatography. This
has occurred either through simple adsorption or through a chemical
reaction between complementary reactive groups present on the membrane and on the ligand resulting in the formation of a covalent bond
between the ligand and membrane In some instances, membranes have been initially coated with a water-insoluble protein such as Zein,
collagen, fibnnogen, etc , followed by the immobilisation of the ligand of interest (e g U S Pat No 4407943)
Porous membrane materials used for non-covalent ligand immobilisation in affinity chromatography have included materials such
as nylon, nitrocellulose, and hydrophobic polyvinylidene fluoride (PVDF)
Non-covalent binding results in random orientation of the ligand and can
also be a problem with small molecules such as peptides,
oligonucleotides or oligosacchaπdes or where competing ions may wash
away the adsorbed ligand To circumvent this problem, peptides and oligonucleotides have been synthesised directly onto membranes as a
means of generating the desired membrane affinity supports in which the
peptides and the oligonucleotides are not only covalently bound to the
support but are also placed in the correct orientation (e g U S Pat No 4923901 ) This method is limited, as individual membranes would need
to be generated, every time, for different peptide and ohgonucleotide
sequences More often, peptides may be coupled to a solid support via
the C- or N-terminal ends of the peptide which may also result in random
coupling via reactive groups on the side chains of the peptide A number of methods and reagents have been developed to also allow the direct
coupling of oligonucleotides onto solid supports (e g J M Coull et al ,
Tetrahedron Lett 27 3991 , B A Conolly, 1987, Nucleic Acids Res , 15 3131 ; B. A. Conolly and P. Rider, 1985, Nucleic Acids Res., 12 4485).
UV cross-linking of DNA (Church et al., 1984, PNAS, 81 1991 ) and RNA
(Khandjian, et al., 1986, Anal. Biochem., 159 227) to nylon membranes
have also been reported.
Many chemical methods have been developed for the immobilisation of proteins as ligands on microporous membranes. For example, activated paper (TransBind.TM., Schleicher & Schuell Ltd., Keene, N.H.) carbodimidazole-activated hydrogel-coated PVDF
membrane (Immobilin-IAV ™, Millipore Corp., Bedford, Mass.), activated
nylon (BioDyne. TM., Pall Corp., (Glen Cove, N.Y.), DVS- and cyanogen bromide-activated nitrocellulose. Membranes bound with specific ligands
are also known such as the SAM2TM Biotin Capture Membrane (Promega) which binds biotinylated molecules based on their affinity to
streptavidin or MAC affinity membrane system (protein A/G) (Amicon).
Some of the disadvantages of covalent attachment of
biomolecules as ligands onto activated membranes are:-
(a) Most of the chemistries used for covalent ligand attachment couple the ligand randomly through amino residues on the protein which often results in
partial or complete loss of binding capacity due to the reduced efficiency of ligand-product binding.
This is mostly due to multi-site attachment of the
ligand when the activated support contains an
excess of activating groups, making the binding site on the ligand inaccessible due to steric hindrance
(Spitznagel, T. M. and Clark, D. S., 1993,
Biotechniques, 11 825).
(b) Ligand immobilisation is often slow requiring 20-180 minutes for reaction completion.
(c) High ligand concentration is needed for fast ligand immobilisation.
(d) Constant agitation is needed during the
immobilisation process that may result in further ligand denaturation and deactivation.
(e) Unsuitable for the immobilisation of unstable recombinant proteins due to immobilisation
chemistry, mechanical agitation, and the long
incubation times needed at room temperature.
(f) Once the immobilisation process is complete, often a blocking (capping) step is required to remove
residual covalent binding capacity.
(g) Covalently bound ligands can not be retrieved from
the membrane.
The technique of immobilised metal affinity
chromatography (IMAC) has found the widest application in affinity purification of recombinant proteins (e.g. J. Porath, Prot. Express. And
Purif., 1992, 3 263; Vosters et al., 1992, Protein Expr. Purif., 3 18;
Alnemri et al., 1993, Proc. Natl Acad. Sci., 90 6839; C. Tang, and H. L. Henry, 1993, J Biol Chem , 268 5069) In this technique, a metal chelate
possessing suitable co-ordination sites is immobilised on a solid support
(e g Iminodiacetic acid immobilised on sepharose beads (IDA-
Sepharose , Pharmacia) or nitπlotπacetic acid immobilised on sepharose (NTA-Sepharose)) Only those proteins with two or three suitable donor ligands in a conformationally favourable arrangement will bind and form
a stable complex (E Sulkowski, 1989, BioEssays, 10, 170, K J Petty,
1996, Metal-chelate affinity chromatography In Current protocols in
molecular biology, F M Ausubel (ed ), vol 2, John Wiley and Sons, New
York) In theory, a wide variety of metal ions with high affinity for electron
donor groups can be utilised Of these, Nι2+ and Zn2+ are the most widely
used Suitable donor ligands include ammo acids histidine, cysteine and tryptophan Since natural proteins rarely contain suitably arranged donor
ligands, recombinant proteins are engineered with a metal chelate
binding tag at either the C- or N- terminal ends of the protein for
purification purposes via IMAC (e g Sharma et al , 1992, In Methods A
companion to Methods in enzymology, F Arnold (ed ) 457-67, Academic
Press, New York) The most popular tag is the hexahistidine tag although
many other tags utilising a combination of histidine and other ammo
acids such as aspartic acid or tryptophan residues have been used (e g
Kasher ef a/ , 1993, Bio/Techniques, 14630)
Metal chelating ligands have been immobilised on solid
supports exclusive of microporous filter materials, such as Sepharose (IDA-sepharose, Pharmacia), magnetic beads (Ni-NTA Magnetic Agarose Beads, Qiagen) and microtitre plates (Ni-NTA HisSorb, Qiagen).
Iminodiacetic acid (IDA) has also been covalently attached to a stable
epoxy resin and incorporated into a microporous plastic sheet (MPS)
matrix (Acti-Disk, Whatman) and used for the selective purification of proteins (U.S. Patent Nos. 3862030, 4102746, 4169014 and 4689302).
The MPS matrix is an inert polymeric microporous sheet that contains
silica that can either be fuπctionalised with ion exchange groups or affinity ligands solely for the purpose of protein purification.
SUMMARY OF THE INVENTION
Unexpectedly, it has now been discovered that filter media
when processed in accordance with the invention to provide a metal chelate filter or metal chelating species filter may provide a number of
surprising advantages and applications as described hereinafter which
would not have been contemplated from the prior art discussed above.
Thus use of the filter media of the invention may now provide advantages
of faster processing of fluids as well as multiple processing of fluids.
Thus the invention provides a ligand immobilisation
procedure for peptides, oligonucleotides and recombinant proteins, which involves site specific attachment of the ligand onto the membrane via use
of a metal chelating species or metal chelate thus avoiding the use of harsh chemical reactions and long incubation times as was the case in
the prior art. In particular, the invention provides for the capture and
separation of these biomolecules from a mixture in a fluid or liquid phase
onto a microporous filter matrix. Such a filter matrix processed in accordance with the invention would have valuable and widespread
applications in the diagnostics, high-throughput screening, and biotechnology industries. In particular the invention has particular
application to fluid phase assay systems and methods described in
International Publications WO 9932884 and/or WO 9932885which are totally incorporated herein by reference.
The process of the invention includes the following variants:-
(i) reaction of a filter with a linker and metal chelating species to produce a metal chelating filter;
(ii) reaction of a filter with a linker and metal chelating species and a metal to produce a metal chelate
filter;
(iii) reaction of a filter with a metal chelating species to produce a metal chelating filter; and
(iv) reaction of a filter with a metal chelate to produce a
metal chelate filter. The invention includes within its scope products produced
by the above mentioned alternative variants (i) to (iv).
The term "filter" as used herein means a porous material or
filter media having an average pore size in the region of 0.01 to 1000 microns and more preferably 0.1-5 microns. Viral antigen immune
complexes would generally be retained by a pore size of 0.05-3 microns while a larger size may be more appropriate for bacterial antigen immune complexes. The filter may be formed from either fully or partly from
glass, silica or quartz including their beads, fibres or derivatives thereof,
having bound thereto accessible functional groups such as -Si-OH groups or which may be treated with a reagent to provide accessible functional groups including -OH, -Si-OH, -NH2 and other amine
containing groups, including alkylamino, thiols, cyanobromides, aldehydes, carboxylates, sulfonylchlorides, ketones, halogens,
maleimido, hydrazine, acetyl or other groups combining acetyl including
haloacetyl inclusive of chloroacetyl, iodoacetyl or bromoacetyl and
epoxy groups. It will also be appreciated that the functional groups may be attached directly to the filter or by an appropriate spacer arm or linker.
It will further be appreciated that porous filter materials comprising
polyamides inclusive of nylon, cellulose acetate, nitrocellulose,
polyvinylidene fluoride, or other fluoropolymers, polysulfone, paper, or
combinations thereof, may also be suitable media for the attachment of linkers and/or a metal chelating species or a metal chelate.
The term "linker" as used herein means any spacer group
which can be utilised to link the various entities described above. As
such, the linker, prior to use has an appropriate functional group as
described above at each end. One group is appropriate for the
attachment to the filter and the other group is appropriate for attachment
to the metal chelate or metal chelating species. Any suitable linking
group, as linker, can be utilised which may include substituted or
unsubstituted alkyl groups having from one to twenty, or more preferably one to six carbons, and wherein the alkyl groups may be linear or
branched Linkers may also comprise substituted or unsubstituted aryl or aryl alkyl groups Thus for example the linking group may be variable comprising a single methylene or a plurality of methylene groups The
linking group may also comprise peptides or branched peptides inclusive
of lysine Other examples of linkers include, for example, both linear,
cyclic, and branched polymers of polysacchandes, phospho pids and peptides having either alpha- beta-, or omega-ammo acids, heteropolymers, polyurethanes, polyesters, polycarbonates, polyureas,
polyamides, polyethyleneimines, polyarylene sulfides, polysiloxanes,
polyimides, polyacetates, dendπmers and dendrimeπc-like molecules or
other polymers as will be readily apparent to those skilled in the art
It will also be appreciated that the term linker as used
herein may also include cross-linking species or reagents used to couple the metal chelate or metal chelating species to accessible functional
groups either on the filter or which have been produced by deπvatisation Such cross-linking species are referred to by way of example to the
Pierce Chemical Company Product Catalog 1999-2000 which is totally
incorporated herein by reference
In a preferred embodiment of the invention, microfibre
glass filters made from silica are especially adapted for use in the
invention Such filters have silanol (Si-OH) functional groups as part of
the filter matrix These may be derivatised using a suitable reagent to
provide appropriate functional groups such as those described above for the attachment of the metal chelating species or metal chelate to the filter or by use of a linker.
In this regard it will be appreciate that such reagents may have an in-built linker or the linker may be pre-attached to the metal
chelating species prior to attachment to the functional groups on the
filter. It may further be appreciated that these reagents may also
comprise the various functional groups inclusive of amine, halogen, or
epoxy as described above. Alternatively the metal chelating species may
be reacted with the Si-OH groups on the filter if the metal chelating species includes a functional group capable of reacting with Si-OH groups such as triethoxysilane or trimethoxysilane. Such functional
groups may also be attached to the metal chelating species by a linker.
Examples of silanisation reagents which may be used for the
derivatisation of the glass fibre filters are: 3-aminopropyl triethoxysilane, 3-aminopropyltrimethoxysilane, 3-(2-aminoethylamino) propyltrimethoxysilane and 3-glycidoxypropyitrimethoxysilane.
In relation to nitrocelluose or cellulose paper such porous
filters comprise accessible amine groups on the surface of the filter. In
this case the linker or metal chelating species with linker attached may
be attached to the filter directly without the need for prior derivatisation using for example standard peptide and conjugation chemistries such as
those described in Frank, et al., 1991 , "Peptides", Giralt and Andrew Eds,
ESCOM Science Pub, pp 151-152, which is directed to facile and rapid
"spot synthesis" of large numbers of peptides as linkers on porous membrane filters. This reference is incorporated herein by reference.
Reference also may be made to Furka et al., 1991 , Int. J.
Peptide Protein Res. 37: 487-493, which is totally incorporated herein by
reference with regard to use of peptides as linkers. Usually such filters may be treated with a reagent such as ethylenediamine which may be
considered as a short linker in a suitable solvent such as acetonitrile and usually in the presence of a catalyst such as triethylamine.
In the case of fluoropolymers, there are no existing
functional groups suitable or otherwise for the attachment of a linker of a metal chelating species. Suitable reactive groups may need to be
introduced onto the filter by a process which is described in the following
publications each of which are incorporated herein by reference ie Vargo
et al., 1992, Langmuir 8:130; Vargo et al., 1992, J. Polym. Sci. Part A:
Poly. Chem. 29:555; and Hook et al., 1991 , Langmuir 7:142.
Briefly these processes are called radiofrequency glow
discharge (RFGD) plasma using hydrogen gas and methanol vapour
which facilitates the introduction of hydroxyl groups to the filter surface.
Such hydroxyl groups can be directly used for the attachment of a filter,
metal chelating species or a metal chelate using standard coupling
chemistries and protocols such as those described above. Alternatively
the hydroxyl groups may be further derivatised with silanisation reagents
as described above to introduce the more versatile amino group. This
can then be used for the attachment of the linker, metal chelating species
or metal chelate. It will be appreciated from standard texts such as a publication entitled "Affinity Membranes in Bioseparations" by E. Klein
which is part of "Membrane Processes in Separation and Purification"
1994, by Crespo and Boddeker Eds, published by Kluwer Academic Publishers which is totally incorporated herein by reference that there is
a full description of various microporous membranes which may be
utilised in the current invention and also reference to various reagents
and processes which may attach the above mentioned functional groups to the filter. Such reagents for example may include cyanogen bromide, tosyl chloride, N-hydroxy succinamide, diamines, hydrazine and its
derivatives, dialdehydes such as glutaraldehyde, carbodiimides, and
diepoxides. This reference also described the preparation of polyamide
filters having accessible functional groups.
The term "metal chelating species" (MCS) as used herein
can be any species with electron donating groups such as -NH2, -COOH,
-SH, -OH and heterocyclic moieties comprising nitrogen atoms, capable
of coordinating with metal ions. Examples of such metal chelating species include iminodiacetic acid, nitrilotriacetic acid, diethylenetriamine
- N,N,N',N" - pentoacetic acid and branched superstructures such as dendrimers or dendrimeric - like molecules or polymeric structures with
the appropriate donating groups, triethylenetetramine, ethylenediamine,
glycine, o-phenanthroline, 4,4-bipyridyl, 2,2-bipyridyl, pyridine and 6-
hydroxynicotinic acid
The term "metal chelate" (MC) as used herein means the metal chelating species having a metal coordinated thereto. Chelation type associations make use of metal ions such as but not limited to, the
metals Fe, Co, Ru, Rh, Rh, Pd, Os, Ir, Pt, Pb, Sn, Ge, Sc, Y, lanthanides and actinides, B, Al, Ga, In, Tl, Li, Na, K, Rb, Cs, Fr and Be, Mg, Ca, Sr, Ba, Ra, Cu, Ni, Zn and transition metals.
It will be appreciated that the above mentioned products of the invention which incorporate the metal chelating species can be utilised for immobilisation of metal containing ligands or metal ions. On
the other hand metal chelate filters of the invention which include the
metal can be used for immobilisation of ligands that coordinate with the
metal.
In the above it will be appreciated that the metal chelating
species may be attached to the filter by a covalent bond, charge
interaction or metal chelation. It will also be appreciated that the metal chelating species may be attached to the filter via a linker by either of the
following:-
(i) attaching the linker first to the filter followed by attachment of the metal chelating species followed
by addition of the metal; (ii) alternatively, the linker may be pre-attached to the metal chelating species followed by attachment of
the linker - metal chelate species moiety on to the
filter (Ji er a/., 1996, Analy. Biochem., 240 197);
(iii) pre-attachment of a linker moiety on the filter in which one of its reactive functional groups is protected by a suitable protecting group will allow
for unreacted functional groups on the filter to be
blocked. Examples of suitable protecting groups include Fmoc, Boc, trityl groups and any other
protecting groups as is known in the art. For example, attachment of an Fmoc group protected linker will allow for uncoupled amine groups on the
filter to be blocked by an acetic anhydride/pyridine/DMF blocking procedure. It will
also be appreciated that reaction of the linker with
branched species such as lysine or branched polymeric species such as dendrimers may increase
the number of functional groups on the filter. This
may then be reacted with a MCS thereby increasing
the metal chelating capacity of the filter. Examples of suitable protecting groups are disclosed in The
Peptides, Vol 3. (eds. Gross, E., and J. Meienhofter,
Academic Press, 1981 ).
BRIEF DESCRIPTION OF THE FIGURES
FIG. 1 shows a derivatised glass fibre filter with
imidodiacetic acid metal chelate attached to the filter with a linker.
FIG. 2 shows a polyacrylamide gel with a low range
molecular weight marker in lane 1 and various molar ratios of E5 dendπmer-horseradish peroxidase (HRP) conjugates in lanes 2 to 5. In
lanes 2 and 3 free HRP is detected at around 45 kDa. In lane 4 the
dendrimer-HRP conjugate at about 73 kDa is readily apparent in the
absence of free HRP. In lane 5 the concentration of the dendrimer-HRP conjugate at a 1 :1 ratio has reduced noticeably.
FIG. 3 shows results of an experiment using Zn2+ immobilised on the filter in which HRP, HRP-antibody conjugate and HRP-dendrimer conjugate were passed through metal chelate filter discs
at varying concentrations. At 1 :1600, only the dendrimer-HRP conjugate
was detectable. Traces of HRP-antibody conjugates were detectable at 1 :400 to 1 :1200 and free HRP was detectable at 1 :400 only. HRP was
detected by applying an HRP substrate (3,3',5,5'-Tetramethylbenzidine
(TMB), insoluble) for 2 minutes after which the discs were then removed,
washed with doubly deionised water and dried on filter paper.
FIG. 4 shows free HRP, HRP-antibody and E5 dendrimer-
HRP conjugates diluted 1 :100 and passed through different derivatised
metal chelate glass fibre filters (Whatman GF/B, GF/C and GF/F). The
metal ion used was Zn2+.
FIG. 5 shows results of an experiment in which E5-
dendrimer conjugate, diluent only, E5 dendπmer only and E5 dendrimer- antibody conjugate were passed through Zn2+ metal chelate filter discs
in duplicate. For one set of discs, phosphate buffered saline with Tween 20 only was used to wash the discs to remove unbound reagent. For the
other set of discs, 500 mM imidazole was added to the washing buffer. Then a 1 1000 dilution of anti-mouse immunoglobulin conjugated to HRP
was added to the discs and incubated for 30 minutes at 37JC After this the discs were washed as before and TMB substrate was applied and washed as described above
FIG 6 of a polyacrylamide gel shows that metal chelate filter discs efficiently capture a 6 x histidine tagged protein from a
solution The concentration of the tagged protein was found to be approximately five times higher in material eluted from the discs than material that flowed through the discs
E X P E R I M E N T A L
EXAMPLE 1 Functionalization of glass fibre membranes with
3-amin opropyltrieth oxysilane
Twenty sheets (10 5 cm x 14 7 cm) of GF/F glass microfibre filters, as obtained from Whatman, Maidstone, England, were
placed in a flat dish and covered with 300 mL of a 10% solution of 3-
aminopropyltπethoxysilane in ethanol (99 7-100% v/v) The reaction was
allowed to proceed for 48 hours with rocking The sheets were then
washed with ethanol and air dried before they were activated at 110DC
for 3 hours The presence of amine groups was confirmed with a 2, 4, 6-
trmitrobenzynesulfonic acid (TNBS) test A few drops of a 1 % TNBS solution in N,N-dιmethylformamιde (DMF) were added to a small piece
of filter membrane and the colour change recorded after I minute EXAMPLE 2 Coupling of linker (Fmoc α-aminocaproic acid).
Five sheets (10 5 cm x 14 7 cm) of functionalised GF/F filters were treated with Fmoc α-aminocaproic acid (4.0 mmol), O-
Benzotriazole-N,N,N',N',-Tetramethyl-Uronium-Hexafluorophosphate (HBTU) (3.9 mmol), N-Hydroxybenzothazole (HOBt) (4.5 mmol), and
diisopropylethylamine (DIPEA) (5.0 mmol) in 40 mL of dry DMF overnight with rocking. The sheets were washed with methanol, dichloromethane
and then air-dried. The extent of coupling was measured with an Fmoc test and gave an Fmoc loading of 0.016 mmol/g of filter. Briefly, accurately weighed filter discs (16 mg) were treated with a 0.4 mL of a
50% solution of piperidine in dichloromethane for 10 minutes with
sonication. This volume was then made up to 2.4 mL with dichloromethane and the absorbance of the liberated Fmoc group
measured at 301 nm (extinction coefficient at 7,800).
EXAMPLE 3 Coupling of metal chelating species.
Eighty filter discs (5 mm diameter) were treated with a 20%
solution of piperidine in DMF for 5 min with sonication to effect the deprotection of the Fmoc group on the linker moiety. The filters were then
washed with methanol, dichloromethane and then air-dried. Removal of
the Fmoc group was then tested with a TNBS test.
The deprotected filters were treated with nitrilotriacetic acid
(1.0 mmol), HBTU (0.9 mmol), HOBt, (1.2 mol), and DIPEA (0.26 mmol) in 6 mL of dry DMF overnight with rocking. The filters were washed with
DMF, methanol, and dichloromethane and air-dried. TNBS test indicated
efficient coupling of the nitrilotriacetic acid. EXAMPLE 4 Immobilisation of Zn2+ on filter discs. Nitrilotriacetic acid derivatised filter discs were each placed on a sintered glass funnel connected to a vacuum pump. The discs were
each initially washed with 100 μL of doubly deionised water, 100 μL of
50 mM phosphate buffered saline, pH 7.5, containing 50 mM sodium
chloride, and followed by 100 μL of doubly deionised water. Fifty μL of
a θ.1 M solution of Zinc sulphate were then allowed to pass through each filter discs followed by washing with a 100 μL of doubly deionised water.
FIG. 1 shows an example of a molecular structure showing the derivatised filter, linker(s) and the metal chelate.
EXAMPLE 5 Preparation of enzyme dendrimer conjugates.
To a solution of HRP (4.3 mg) made up in 30 mM sodium
acetate buffer containing 150 mM sodium chloride, pH 4.5, was added 80
μL of a freshly prepared solution of sodium periodate (Nal04) and the reaction mixture allowed to incubate for 5 hours in the dark. The mixture
was then loaded onto a Sephadex G-25 PD-10 column equilibrated with
20 mM phosphate buffer, pH 6.0, and the activated enzyme eluted with
the same buffer. Thirteen μL of a 50 mg/ml solution of generation five dendrimer (E5) (Michigan Molecular Institute) was then incubated with
1.1 mg of the activated HRP enzyme in the presence of 0.70 mg of sodium cyanoborohydride (NaBH3CN) at 4°C for 16 hours. The reaction
mixture was then dialysed against 0.1 M NaCI and doubly deionised
water. Polyacrylamide gel electrophoresis (PAGE) on a linear gradient
gel (4-15%) under SDS reducing conditions revealed the main product
to be a 1 :1 conjugate of HRP to E5. FIG. 2 shows examples of different molar ratios of E5 dendrimer-HRP conjugations.
EXAMPLE 6 HRP-E5 conjugate capture on a glass microfibre metal chelate filter
Metal chelate glass microfibre disc filters prepared as in EXAMPLE 4 were used for the capture of HRP-E5 conjugates. The discs
were each washed with 100 μL of 50 mM phosphate buffered saline, pH 7.5, containing 500 mM NaCI and 500 mM imidazole. Fifty μL of either
diluted HRP, HRP-antibody conjugate, or HRP-E5 conjugate were then
allowed to pass through the filter followed by a washing step of 100 μL of the imidazole, buffer. The filter discs were then incubated in the
presence of an HRP substrate (3,3',5,5'-Tetramethylbenzidine (TMB)
insoluble) for 2 minutes after which the discs were then removed, washed
with doubly deionised water and dried on filter paper.
FIG. 3 shows results of an experiment using Zn2+
immobilised on the filter in which HRP, HRP-antibody conjugate and
HRP-dendrimer conjugate were passed through metal chelate filter discs
at varying concentrations. At 1 :1600, only the dendrimer-HRP conjugate
was detectable. Traces of HRP-antibody conjugates were detectable at
1 :400 to 1 :1200 and free HRP was detectable at 1 :400 only.
FIG. 4 shows free HRP, HRP-antibody and E5 dendrimer-
HRP conjugates diluted 1 :100 and passed through different derivatised
metal chelate glass fibre filters (Whatman GF/B, GF/C and GF/F). The
metal ion used was Zn2+. EXAMPLE 7 An immunoassay to detect the presence of
mouse antibody on a metal chelate filter
E5-dendrimer conjugate, diluent only, E5 dendrimer only and E5 dendrimer-antibody conjugate were passed through Zn2+ metal
chelate filter discs in duplicate. For one set of discs, phosphate buffered
saline with Tween 20 only was used to wash the discs to remove unbound reagent. For the other set of discs, 500 mM imidazole was added to the washing buffer. Then a 1 :1000 dilution of anti-mouse
immunoglobulin conjugated to HRP was added to the discs and incubated for 30 minutes at 37°C. After this the discs were washed as
before and TMB substrate was applied and washed as described above.
FIG. 5 shows the results. It can be seen that the presence
of 500 mM imidazole inhibited non-specific binding of HRP-conjugated
anti-mouse immunoglobulin from the metal chelate filters.
EXAMPLE 8 Recombinant 6 X histidine tagged protein capture on Zn2+ immobilised metal chelate filter
Two metal chelate filter discs (5 mm diameter) immobilised
with Zn2+ prepared as in EXAMPLE 4 were incubated with 30 μg of 6 X histidine tagged protein in 400 μL of phosphate buffer for 20 minutes.
The protein solution was then removed and concentrated (flow through)
and the filters washed with 400 μL of phosphate buffer. Bound protein
was then eluted from the filter by incubation with 400 μL of 500 mM imidazole in phosphate buffer for 20 minutes (eluate). This fraction was
concentrated and along with the flow through fraction was subjected to PAGE under SDS denaturating conditions
FIG 6 of a polyacrylamide gel shows that metal chelate filter discs efficiently captured a hexahistidme tagged protein from a
solution and that the concentration of the tagged protein was
approximately five times higher in filter eluates than in the flow through
APPLICATIONS
MC and MCS filters may be incorporated into an immunoassay filter plate, column, syringe filter housing or tube for a wide
range of diagnostics, high-throughput screening, recombinant protein assays, and research applications The MC and MCS filters may also be embodied with a second type filter such as an FTA™ Gene Guard
System (Fitzco Inc, a member of the Whatman Group) filter which will
perform a complementary function to the MC or MCS filters The MC and MCS filters may further embodied with a second filter such as to restrict
the flow of fluids through the MC and MCS filters
Molecular and immunoassay diagnostics
(1 ) FTA coated filters are known to capture nucleic
acids after spontaneously lysmg cells introduced to it Once captured the genetic material is maintained
in a bound form for any length of time without damage The bound genetic material such as human genomic DNA can be ultimately removed by use of reagents such as restriction endonucleases
The fragments of the restriction digest, can be incubated in the presence of a MC filter harbouring
dendnmer-bound gene specific capture probes, to which genes of interest will bind and ultimately be detected
(2) Immobilisation of oligonucleotide probes for genomic
assays Such probes could be derivatised at their 5' or 3' ends with a metal chelate tail such as a hexahistidme tag or dendrimer e g PAMAM
dendrimers (Dendntech Inc, Midland, Michigan,
USA) or dendrimeπc-like structure for the
hybridization capture of genomic DNA E g traditional methodology (other than FTA) of purification yields genomic DNA as a soluble fraction After restriction digest, or in vitro
transcription, template nucleic acid can be produced that is in a position to be captured by such
oligonucleotide probes Alternatively, these probes may be mixed with the genomic DNA whereby the
DNA/probe hybrids formed can be captured on MC
filter through their metal chelate tail on an MC filter
A second probe conjugated to a detector label, e g
an enzyme can then be added
(3) Oligonucleotides, mRNA and cDNA coupled to dendrimers or other species capable of acting as a ligand, for example a hexahistidine tag, can be
immobilized onto a MC filter. Incorporation of metal
chelate filters into multi-well filterplates provides a
platform for microarray analysis. It will also be appreciated that nucleic acids tagged with
dendrimers or a hexahistidine may be added directly to a MC filter sheet to form a microarray suitable for analysis without the need for a multi-well plate format.
(4) Recombinant proteins may be directly immobilized
on a metal chelate without the need for a purification step. Proteins with a hexahistidine tag
will be captured on the filter while the culture
supernatant is washed away. Such proteins may then be detected or utilised in an immunoassay or
similar type of analysis.
(5) Site-directed immobilisation of recombinant proteins
for use in immunoassays. Recombinant fusion
proteins including a hexahistidine tail may be immobilised on a metal chelate filter. This will
ensure that the majority of the proteins have their
active site(s) available for ligand binding resulting in
more efficient antigen usage and more sensitive
immunoassays. (6) Unstable recombinant protein may be immobilized on MC filters quickly and at room temperature
without the need for covalent bond formation involving harsh chemical reactions which may damage the protein
High-throughput screening (HTS)
(1 ) Microplates and filterplates in a 96-well or greater
format are widely used in HTS A filterplate
incorporating an MC filter would enable the user to rapidly immobilize potential drugs or target
molecules labelled with a specific tag, e g hexahistidine
(2) "DELphi" (Cytos Biotechnology Ag, Zurich, Switzerland) is a virus-based expression and
screening system that allows reproduction of all
proteins from a chosen tissue or cell type using
cDNA libraries converted into alphaviral expression
libraries that are used to infect cell cultures expressing the original proteins in a "one-gene-per- cell" or "one-gene-per-plaque" format (WO
99/50432, WO 99/25876, C Blaser, et al , Genetic
Engineering News 2000,20(6) 32-35) If the cDNA were co-expressed with 6-hιs this would permit rapid
capture of the expressed protein The method could also be combined with a FTA filter for simultaneous
capture of the amplified viral DNA for sequencing
either after or without the need for RT-PCR. The
MCF-captured proteins may then be tested for function in bioassays.
(3) An indicator of cellular events is the change in kinase activity. Interaction at the cell surface is
translated to gene expression via a multitude of pathways consisting of discrete quinces. This process is known as signal transduction, and is the
mechanism by which a cell interacts with its
environment. Kinases are therefore regarded as useful drug targets as their (de)activation can alter
the behaviour of a cell. To this end many assay techniques to detect kinase activity exist. In the
microplate format, typically, a synthetic kinase substrate is incubated with the kinase sample of
interest and the level of phosphorylation of the substrate measured post incubation. Difficulty has
always arisen when attempting to isolate the substrate in a purified form to facilitate detection. If
the substrate was engineered to contain a 6xHis
tag, it could therefore be readily captured on a MC
filterplate that is incorporated within a multiwell device. A MC filter will have greater specificity than Promega's streptavidin filter that is commonly used together with biotin tagged peptides.
(4) Antibodies, enzymes and other molecules (targets)
required to be tested against solid phase or liquid phase combinatorial chemistry libraries may be tagged with hexahistadine or dendrimers. Following
an incubation, the reacted mixtures are passed
through a MC filter and washed. The hexahistidine or dendrimer tagged targets are retained by the MC
filter together with any combinatorial library
compound of "hit" compound. The isolated library compound may then be further interrogated to
determine its identity as is known in the art. As an
alternative the target molecule may be conjugated to a dendrimer or hexahistidine tag either of which
may be itself tagged with a dye, fluorescent
compound, enzyme, etc. Following an incubation, the "hit" library compounds either on a resin particle
or in free solution, are labeled by the tagged
dendrimer or hexahistidine and may then be further
interrogated.
(5) Peptide immobilisation for epitope mapping.
Overlapping peptide sequences may be tagged with a hexahistidme tail or dendrimers and immobilised onto metal chelate filters for subsequent screening
(6) Filterplates with 96, 384, 1536 or more wells with
metal chelate filter bottoms could be used to capture hexahistidine or dendrimer tagged or target molecules
(7) When searching for reporter genes, le those that
switch on or off in response to a drug, the gene
product may be engineered to bear a hexahistidme sequence This product may then readily be captured onto a metal chelate filter
Biotechnology applications
(1 ) A deep well multiwell plate encapsulating a MC filter at the bottom of each well may be constructed
with a hydrophobic filter layer placed directly
beneath the chelate filter to act as a liquid retention
barrier Within each well may be carried out mammalian, yeast or bacterial culture without fluid dripping through the filter bottoms Protein,
recombinant or otherwise, either secreted from the
cells in culture, obtained via peπplasmic harvesting
or lysis will bind to the metal chelate filter at the
bottom of the well if it has a hexahistidine tag
Application of vacuum to the well will remove cellular debris; leaving recombinant protein bound to the filter. After washing steps the captured protein may be released with an elution procedure as is known in the art.
(2) Simultaneous capture of library DNA and
recombinant protein. A device encapsulating both
FTA and MC filter materials within the same device (tube, column or multiwell) may be constructed.
Upon application of a cellular population containing
an expression library, the cells will lyse, the
episomal and/or genomic DNA will bind to the FTA, and the recombinant protein containing an
engineered hexahistidine tag will bind to the chelate
filter. With the addition of imidazole elution buffer, the recombinant protein can be harvested and assayed. If the protein collected is of interest
(desired level, activity, interaction, etc.), the exact
DNA that produced it can be collected using the
FTA techniques.
(3) Immobilization of metalloproteases.
Metalloproteases are implicated with the onset of
metastasis, being part of the mechanism utilised by
transformed cells during the break through of epithelial layers. The action of metalloprotease is currently of interest to the drug discovery community as they provide a good anti-cancer target. The ability to rapidly harvest and assay for
metalloproteases is advantageous. Such proteases
will specifically bind to MC or MCS filters.
(4) Recombinant proteins and enzymes expressing a tag such as a hexahistidine tail, may be assayed directly from culture to determine a) levels of
expression, b) enzyme activity, c) the best construct,
d) best culture medium to use thereby eliminating tedious column chromatography work for simple assay determinations.
(5) Immobilisation of metalloproteins for purification and
quantitation.
(6) Western blot and dot blot applications.
(7) Immunoassays where it is desirable to capture, for example, dendrimer or hexahistidine tagged
peptides, proteins, nucleic acids or other
substances onto a MC or MCS filter.
Other applications
(1 ) Multi-layer MC or MCS filterplates, tubes or
columns. Several layers of MC or MCS filter within
each tube, column or well will amplify the capacity
to isolate and harvest compounds tagged with dendrimers or hexahistidine or other suitable substances
(2) Environmental samples incubated with specific dendrimer or hexahistidme conjugated reagents
may be passed through columns containing large rolled up sheets of MC or MCS filters This
approach allows for large volumes processing of
fluids such as water supplies Captured pollutants
and microorganisms or parts of microorganisms such as antigens or nucleic acids may then be
assayed using methods well known in the art
(3) The inclusion of a flow restriction filter beneath the MC or MCS filter may be used to control flow
through of fluids
(4) Large and small scale filter devices for heavy metal
removal systems using the MC or MCS filter

Claims

1. A method of making a metal chelate filter or metal chelating species filter including the following step of:
treating a filter having a pore size of 0.01 to 1000 microns and
accessible functional groups with a metal chelate or metal chelating
species to provide the metal chelate filter or metal chelating filter species.
2. A process is claimed in claim 1 wherein the accessible functional groups are bound directly to the filter.
3. A process as claimed in claim 1 wherein the accessible functional
groups are attached to a linker which is bound to the filter.
4. A process as claimed in claim 3 wherein the metal chelate is
attached to the linker.
5. A process as claimed in claim 1 wherein the filter is derivatised or
treated with a reagent to provide the accessible functional groups
on its surface.
6. A process as claimed in claim 3 wherein the linker is treated with a reagent to provide the linker with accessible functional groups.
7. A process as claimed in claim 3 wherein the linker is pre-attached
to the metal chelating species to form a linker - metal chelating species moiety followed by attachment of the moiety to the filter.
8. A process as claimed in claim 1 wherein a linker is pre-attached to
the filter in the form of a linker moiety in which at least one of the
reactive functional groups of the linker is protected by a suitable protecting group to allow for unreacted functional groups to be blocked.
9. A process as claimed in any preceding claim wherein the metal
chelating species is selected from the group consisting of:
iminodiacetic acid, nitrilotriacetic acid, diethylenet amine -
N,N,N',N" - pentoacetic acid, branched superstructures or polymers, triethylenetetramine, ethylenediamine, glycine, o- phenanthroline, 4,4-bipyridyl, 2,2-bipyridyl, pyridine and 6-
hydroxynicotinic acid.
10. A process as claimed in claim 8 wherein the branched superstructures or polymers are selected from the group consisting of: dendrimers, dendrimeric - like molecules or polymeric structures
with appropriate election donating groups capable of coordinating
with metal ions.
11. A process as claimed in claim 9 wherein the electron donating
groups are selected from the group consisting of: -NH2, -COOH, -SH, -OH and heterocyclic moieties comprising nitrogen atoms.
12. A process as claimed in claim 1 wherein the metal chelate is a
metal chelating species having a metal coordinated thereto which
is selected from the group consisting of: Fe, Co, Ru, Rh, Rh, Pd, Os, Ir, Pt, Pb, Sn, Ge, Sc, Y, lanthanides and actinides, B, Al, Ga,
In, Tl, Li, Na, K, Rb, Cs, Fr and Be, Mg, Ca, Sr, Ba, Ra, Cu, Ni, Zn
and transition metals.
13. A process as claimed in claim 1 wherein the functional groups are selected from the group consisting of -OH, -Si-OH, -NH2,
canobromides, hydrazides and other amine containing groups, thiols, aldehydes, carboxylates, sulfonyl chlorides, ketones,
halogens, acetyl, epoxy groups, maleimido, hydrazzme, groups containing acetyl and epoxy
A process as claimed in claim 1 wherein the linker is selected from the group consisting of substituted or unsubstituted alkyl groups,
substituted or unsubstituted aryl groups, substituted or
unsubstituted arylalkyl groups, peptides and branched peptides, linear, cyclic, and branched polymers of polysacchandes,
phospholipids and peptides having either alpha-, beta-, or omega-
ammo acids, heteropolymers, polyurethanes, polyesters,
polycarbonates, polyureas, polyamides, polyethyleneimines,
polyarylene sulfides, polysiloxanes, polyimides, polyacetates,
dendrimers and dendπmeπc-like molecules A process as claimed in claim 14 wherein the substituted or
unsubstituted alkyl groups have 1 to 6 carbons A process as claimed in claim 15 wherein the alkyl group comprises
a single methylene or plurality of methylene groups A process as claimed in claim 1 wherein the filter is filter media
formed either fully or partly from glass, silica or quartz, including
their fibre or derivatives thereof A process as claimed in claim 1 wherein the filter comprises a porous material selected from polyvinyhdene fluoride and other fluoropolymer, polyamide, cellulose acetate, nitrocellulose, polyv yl chloride, polysulfone, polyamide, paper or combinations thereof
A process as claimed in claim 1 wherein the metal chelate filter incorporates a metal which is selected from Fe, Co, Ru, Rh, Rh,
Pd, Os, Ir, Pt, Pb, Sn, Ge, Sc, Y, lanthanides and actinides, B, Al, Ga, In, Tl, Li, Na, K, Rb, Cs, Fr and Be, Mg, Ca, Sr, Ba, Ra, Cu, Ni, Zn and transition metals
A process as claimed in claim 1 wherein the metal chelating species is attached to the filter by a covalent bond, charge interaction or metal chelation
A process is claimed in claim 1 wherein the linker is reacted with a branched species inclusive of lysme or a branched polymeric
species inclusive of dendrimers and dendπmer-like species to
increase the number of functional groups on the filter
A process as claimed in claim 20 wherein the reacted linker is
treated with a metal chelating species to increase the metal
chelating capacity of the filter A process as claimed in claim 1 wherein the filter is glass or glass
fibre A metal chelate filter or metal chelating species filter when prepared
by a process as claimed in any preceding claim A metal chelate filter or metal chelating species filter comprising a filter incorporating a metal chelating species bound thereto by accessible functional groups located on the filter.
26. A filter incorporating a metal chelate bound thereto by accessible functional groups located on the filter.
27. A filter having a linker bound thereto by accessible functional groups located on the filter and a metal chelating species attached
to the linker.
28. A filter having a linker bound thereto by accessible functional groups located on the filter and a metal chelate attached to the
linker.
29. A filter as claimed in claim 24, 25, 27, 27 or 28 which is a porous
membrane in the form of a filterplate, microplate, tube, vial, syringe
filter housing, column or similar arrangement.
EP00926556A 1999-05-14 2000-05-15 Metal chelating filters and metal chelate filters Withdrawn EP1183327A1 (en)

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AUPQ034399 1999-05-14
AUPQ0343A AUPQ034399A0 (en) 1999-05-14 1999-05-14 Metal chelating filters and metal chelate filters
PCT/AU2000/000477 WO2000070012A1 (en) 1999-05-14 2000-05-15 Metal chelating filters and metal chelate filters

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