WO2002032591A2 - Matiere utile pour la separation de composes organiques, procedes pour sa preparation et utilisation de cette matiere - Google Patents

Matiere utile pour la separation de composes organiques, procedes pour sa preparation et utilisation de cette matiere Download PDF

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Publication number
WO2002032591A2
WO2002032591A2 PCT/DK2001/000689 DK0100689W WO0232591A2 WO 2002032591 A2 WO2002032591 A2 WO 2002032591A2 DK 0100689 W DK0100689 W DK 0100689W WO 0232591 A2 WO0232591 A2 WO 0232591A2
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WO
WIPO (PCT)
Prior art keywords
substrate
coating
gradient
monomers
polymer
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PCT/DK2001/000689
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English (en)
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WO2002032591A8 (fr
WO2002032591A3 (fr
Inventor
Bjørn WINTER-JENSEN
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Picosep A/S
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Priority to AU2002210397A priority Critical patent/AU2002210397A1/en
Publication of WO2002032591A2 publication Critical patent/WO2002032591A2/fr
Publication of WO2002032591A3 publication Critical patent/WO2002032591A3/fr
Publication of WO2002032591A8 publication Critical patent/WO2002032591A8/fr

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Classifications

    • G—PHYSICS
    • G01—MEASURING; TESTING
    • G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
    • G01N27/00—Investigating or analysing materials by the use of electric, electrochemical, or magnetic means
    • G01N27/26—Investigating or analysing materials by the use of electric, electrochemical, or magnetic means by investigating electrochemical variables; by using electrolysis or electrophoresis
    • G01N27/416—Systems
    • G01N27/447—Systems using electrophoresis
    • G01N27/44704—Details; Accessories
    • G01N27/44747—Composition of gel or of carrier mixture
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05D—PROCESSES FOR APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05D1/00—Processes for applying liquids or other fluent materials
    • B05D1/62—Plasma-deposition of organic layers
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05D—PROCESSES FOR APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05D2201/00—Polymeric substrate or laminate
    • B05D2201/02—Polymeric substrate
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05D—PROCESSES FOR APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05D2252/00—Sheets
    • B05D2252/02—Sheets of indefinite length
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05D—PROCESSES FOR APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05D2490/00—Intermixed layers
    • B05D2490/60—Intermixed layers compositions varying with a gradient parallel to the surface

Definitions

  • the present invention relates to a material, e.g. a material useful for the separation of organic compounds, such as proteins and biomolecules.
  • the invention also relates to a method of producing said material as well as a use of said material for the separation of organic compounds, in particular proteins.
  • the objective of the present invention is to provide a new method as well as the material for performing the method, and a method of producing said material, by use of which method it is possible to perform separation of one or more organic compounds from a mixture of compounds with a high resolution, and which method further is easy and relatively fast to perform.
  • the invention is based on the idea of separating organic compounds on a substrate comprising a chemically variation of compounds resulting in a composition gradient.
  • the term surface composition gradient thus means that the surface has a variation in chemical composition varying along the surface in a graduating pattern, preferably so that the composition in the form of a mixture of two or more compounds is varied with respect to the amount of the respective compounds stepwise or continuously along the surface of the substrate, preferably in one or more defined directions.
  • the surface preferably has an attractive force variation along the surface in a stepwise or continuously graduating pattern, where an attractive force variation means a variation in the surfaces attractive force property relative to organic compounds, such as a variation in pH value or a variation in hydrophobicity/hydrophilicity.
  • the figure illustrates a plasma reaction chamber 1 , which is useful in the process according to the invention.
  • the reaction chamber 1 also designated a vacuum chamber, comprise a winding system 2 in the form of two reels onto which a sheet-like substrate in the form of a tape or similar can be wounded during the application of a coating.
  • the system comprises a number of supply units 4 comprising the monomers e.g. as indicated in the form of acid, basic, and neutral components.
  • Each supply unit comprises a flow control 3 for controlling the respective amount of monomer added to the reaction chamber.
  • the reaction chamber 1 comprises two electrodes, 6, 7 which may be of stainless steel. In the shown reaction chamber one of the electrodes 6 is constituted by the outer wall and the other electrode is constituted by grid placed in a distance from the wall.
  • An isolating material 5 e.g. of PE is placed around the electrode wall 6.
  • a substrate 8 is wounded from one of he reels to the other during the coating.
  • the plasma 9 is generated in the reaction chamber, and monomer as well as inert gasses such as Ar is added as indicated by the arrows 10, 11.
  • the material according to the invention comprises a sheet-like substrate.
  • the term sheetlike substrate means any substrate having a 3-dimentional shape, wherein the substrate in at least one of its dimensions, designated the length, and measured at its longest point is more than, preferably more than 10 times, more preferably more than 100 times its shortest dimension, designated its thickness, and measured in its shortest point.
  • the substrate in its dimension designated its thickness, and measured in its shortest point is less than 0.5 times its other 2 dimensions measured in their longest points, preferably less than 0.1 times its other 2 dimensions.
  • the sheet-like substrate preferably includes tapes, bands, strips, felts, sheets, non-woven structures, woven structures, membranes, films, plates, etc. having regular or irregular dimensions.
  • the sheet-like substrate is a tape roll, which can have a length of up to several meters.
  • the sheet-like substrate may also include a hollow pipe with an inner surface and an outer surface.
  • the hollow pipe corresponds to a folded sheet, and the hollow pipe may preferably have the dimensions mentioned in the following converted to such folded sheet.
  • the ratio between the "longest” dimension and the "shortest dimension” (of the three dimensions) is at least in the order of 10, in particular at least in the order 100.
  • the "shortest” dimension is typically referred to as the "thickness” and the “longest” dimension (usually perpendicular to the thickness) is typically referred to as the "length”.
  • the third dimension is often referred to as the "width”.
  • the length and the width are normally of about the same order of magnitude.
  • the thickness may be in the range of 50- 500 ⁇ m whereas the width may be in the range of 3-300 mm.
  • the substrate may in one embodiment be in the form of a cord.
  • the sheet like substrate is in the form of a three dimensional unit, wherein one dimension, designated the length is more than 2 times, preferably more than 5 times and even more preferably more than 10 times the longest of the other two dimension, preferably the length being at least 10 cm such as 25 or 50 cm more preferably at least 100 cm and even more preferably at least 200 cm.
  • the shortest dimension, designating thickness is between 1 ⁇ m and 1 mm, more preferably between 50 and 500 ⁇ m.
  • the dimension designating the width may preferably be between 1 and 1000 mm, more preferably between 3 and 300 mm.
  • the sheet-like substrate comprise a polymer gradient coating on at least a part of the surface of the substrate, said coating representing a surface composition gradient in at least one direction along the surface of the substrate or the material.
  • the surface composition gradient thus means that the surface has a variation in chemical composition varying along the surface in a graduating pattern, preferably so that the composition is varied in concentration of one or more components and/or in the form of a mixture of two or more compounds which is varied with respect to the amount of the respective compounds stepwise or continuously along the surface of the substrate.
  • the sheet like substrate should preferably comprise a surface area, such as an area of between 0.1 and 100 cm 2 , more preferably between 1 and 20 cm 2 , wherein said part of the substrate surface, which preferably may be substantially plane, is coated with the polymer gradient coating is or includes said substantially surface area.
  • the polymer gradient coating should preferably constitute or represent a surface composition gradient essentially parallel to the plane of the coated surface of the substrate.
  • the polymer gradient coating may preferably constitute a surface composition gradient in one direction essentially parallel to the plane of the surface of the substrate.
  • the polymer gradient coating may constitute a surface composition gradient in two or more directions essentially parallel to the plane of the surface of the substrate, e.g. the surface composition may constitute a surface composition gradient radially extending from a central area or a surface composition gradient extending in two opposite directions.
  • the polymer gradient coating constitute a surface composition gradient in one single direction essentially parallel to the plane of the surface of the substrate.
  • the substrate comprises a polymer gradient coating which constitute two or more surface composition gradients, such as gradients following each other along the same single direction or different gradients in different directions.
  • the two or more surface composition gradients may e.g. be pH gradients with different pH separation values.
  • the material according to the invention may e.g. comprise a substrate having one or more of the following gradients: One or more pH value gradients including gradients extending at least 0.5 pH units, preferably at least 2 pH units over the substrate surface and/or one or more hydrophilicity/hydrophobicity gradient measured as surface tension, wherein the gradient extending at least 1 dyne/cm, preferably at least 10 dynes/cm and more preferably at least 25 dynes/cm over the substrate surface, more preferably the gradient extension on the substrate is within 10-80 dynes/cm.
  • One or more pH value gradients including gradients extending at least 0.5 pH units, preferably at least 2 pH units over the substrate surface and/or one or more hydrophilicity/hydrophobicity gradient measured as surface tension, wherein the gradient extending at least 1 dyne/cm, preferably at least 10 dynes/cm and more preferably at least 25 dynes/cm over the substrate surface, more preferably the gradient
  • the coating is present on essentially the total surface of the substrate.
  • the sheet like substrate is in the form of a tape or strip having a thickness with a thickness surface, a first and a second side with, respectively, a first and a second surface
  • at least one of said thickness surface and first and second surfaces is partly or totally covered with the polymer gradient coating.
  • at least one of said first and second surfaces is partly or totally covered with the polymer gradient coating, even more it is preferred that essentially the whole of at least one of said first and second surfaces is covered with the polymer gradient coating.
  • At least an elongated surface area of the tape or strip is coated, and that the coating constitute or represent a surface composition gradient in one direction essentially parallel to the plane of the coated surface, where the direction preferably being essentially parallel to the longest line between boarder lines of the elongated surface area.
  • the elongated surface area may preferably be one of the major surfaces of the tape or strip.
  • the sheet-like substrate is in the form of a cord
  • said cord preferably having a round or angular cross-section, such a triangular or rectangular
  • the cord comprise a coating on its surface extending along the whole or part of the length of the cord and the coating preferably constitute a surface composition gradient in one direction essentially following the length of the cord.
  • the cord has a substantially circular cross-section, with a diameter of 1-10 mm, preferably between 2 and 4 mm.
  • the sheet-like substrate is in the form of a hollow pipe
  • the surface composition gradient is in one direction which preferably is a direction following the length direction of the sheet-like substrate, such as a direction substantially parallel to the longitudinal axis of the sheet-like substrate.
  • the material according to the invention may be constituted of the sheet-like substrate inclusive the polymer gradient coating and any pre- or top-coating.
  • the material according to the invention may, besides the sheet-like substrate inclusive the polymer gradient coating and any pre- or top-coating, comprise a supporting element for the substrate.
  • the supporting element may in principle be any type of supporting element, which does not destroy or totally mask the polymer gradient coating. It is preferred that the supporting element is shaped so that the total material preferably is essentially sheet-like, wherein the term sheet-like material means a material having a shape as a sheet-like substrate as defined above.
  • the supporting element is in the form of a supporting sheet selected from the group consisting of polymers, such as polyolefins including polyethylene (PE) and polypropylene (PP); polytetrafluoroethylene (PTFE); tetra-fluoroethylene- hexafluoropropylen-copolymers (FEP); polyvinyl-difluoride (PVDF); polyamides; polyvinylchloride (PVC); rubbers such as silicon rubbers; glass; paper; carbon fibres; ceramics; metals or mixtures or combinations thereof.
  • polymers such as polyolefins including polyethylene (PE) and polypropylene (PP); polytetrafluoroethylene (PTFE); tetra-fluoroethylene- hexafluoropropylen-copolymers (FEP); polyvinyl-difluoride (PVDF); polyamides; polyvinylchloride (PVC); rubbers such as silicon rubbers; glass; paper;
  • the sheet-like substrate may have any chemical composition such as polymers, e.g. polyolefins, such as polyethylene (PE) and polypropylene (PP), or other thermoplastics, such as polytetrafluoroethylene (PTFE), tetra-fluoroethylene-hexafluoropropylen- copolymers (FEP), polyvinyl-difluoride (PVDF), polyamides (e.g. nylon-6.6 and nylon-11), and polyvinylchloride (PVC), rubbers e.g. silicon rubbers, glass, paper, carbon fibres, ceramics, metals, mixtures thereof etc.
  • the material may further be made from or include any type of fibers and fiber enforced materials.
  • the sheet like substrate comprising the polymer gradient coating may preferably be porous, optionally with a porosity of at least 5 %, preferably at least 10 % by volume.
  • the density of the material should preferably be below 0.9 g/cm 3 , more preferably below 0.5 g/cm 3 , in dry and non-compressed state.
  • the substrate may e.g. be made from or include fibers or foam.
  • the substrate comprise pores or openings, which provides the substrate with a capillary effect to water.
  • Such materials may be in any suitable form, preferably representing a high surface area.
  • the currently most interesting examples are polyethylene or polypropylene felts, paper, non-woven glass fibres, etc. It is envisaged that particularly interesting sheet-like substrates are polyethylene (EP), polypropylene (PP) or PE/PP felts.
  • the material may include any type of fibers and fiber enforced materials.
  • the sheet-like substrate will in the preferred embodiment constitute all or the main part of the material or sheet-like material.
  • the mechanical properties (e.g. flexibility, strength, etc.) of the material will to a great extent be determined by the selection of the sheet-like substrate.
  • the substrate may be pre-coated in order to modify the properties thereof, e.g. the ability of the surface to adhere to polymer gradient layer or the hydrophobic properties of the substrate as such.
  • the pre-coating may preferably be in the form of a substantially uniform layer or it may alternatively be applied in a pattern such as a pattern providing a gradient as described in the following.
  • the pre-coating is in the form of a substantially homogenous layer of a polymer onto the native surface of the substrate.
  • the pre-coating may e.g. be performed in order to moderate the effect of the composition gradient. Thereby it may be possible to obtain an even higher resolution when separating organic compounds.
  • the polymer gradient coating may in principle have any thickness, but as it will be clear to the skilled person a too thin layer or a too thick layer may give a poor resolution and/or a prolonged separation time.
  • the thickness of the polymer gradient layer is at least 5 nm, preferably in the range of up to about 100 ⁇ m, more preferably in the range of 10-1000 nm.
  • the polymer gradient coating has a thickness of at the most 5000 nm.
  • the thickness of the layer as such may of course vary over the coated part of the surface of the substrate in accordance with the requirement for a composition gradient.
  • is a substantially uniform layer thickness such as a thickness of the polymer gradient coating which is essentially the same though out the coating area.
  • the polymer gradient coating varies in thickness continuously or step wise along its direction or directions of surface composition gradient.
  • the polymer gradient coating preferably varies in thickness essentially continuously along its direction or directions of surface composition gradient.
  • the polymer coating gradient may be in the form of a polymer coating which varies in chemical composition so that it varies along the surface of the substrate in a graduating pattern, preferably so that the composition is varied in concentration of one or more components and/or in the form of a mixture of two or more compounds which is varied with respect to the amount of the respective compounds stepwise or continuously along the surface of the substrate.
  • the coating discussed above represents the composition gradient, which is a characteristic feature of the present invention.
  • the coating provides a layer in the form of a polymer or polymeric composition as further described below, which does not have the same composition or concentration over the complete coated surface.
  • composition gradient or "surface composition gradient” is intended to mean a variation of chemical composition over a surface in a more or less gliding manner.
  • the variation can be expressed as the variation in density of one or more chemical groups.
  • the variance may be steep or flat, or may even be step-wise so as to express a virtual gradient.
  • the polymer gradient coating comprises one or more chemical components also designated monomers.
  • monomers mean components for the polymeric composition to provide the polymer gradient coating.
  • monomers should in the present invention include any polymerisable component but it may also include components, which is not polymerisable.
  • the coating may include monomers, which is not polymerised but is bound e.g. by an adhesive component.
  • the polymer gradient coating should preferably comprise or be made from at least 10 % by weight, more preferably at least 25 % by weight of polymerisable monomers. In one embodiment the polymer gradient coating consist essentially of polymerised monomers or is made from polymerisable monomers.
  • Monomers which is not polymerised or polymerisable should preferably be fixed in or to the coating to avoid unintended migration of these components.
  • the components in the polymer gradient coating may be any type of component, wherein preferably at least one of the components in the coating should have an effect of the migration of at least one of the organic compounds in a mixture that is to be separated, such as proteins.
  • the variance in composition may for example represent a pH gradient, a hydrophobicity gradient, a polarity gradient, a surface tension gradient, a biocompatibility gradient, a binding affinity gradient, etc.
  • a pH gradient is particularly relevant where the material is utilised in a method for the separation of proteins.
  • the composition gradient is generally in a direction substantially parallel to the plane of the material or sheet-like substrate.
  • the "plane of the material or sheet-like substrate” refers to the macroscopic plane of the sheet, film, tape, etc.
  • the composition gradient may as mentioned preferably be in a direction substantially parallel to the longitudinal axis of the material.
  • the polymer gradient coating varies in composition continuously or step wise along its direction or directions of surface composition gradient, and the polymer gradient coating varies in composition essentially continuously along its direction or directions of surface composition gradient, it is preferred that the is composed from two or more monomers with varying amounts of the respective monomers in the polymer gradient composition along the direction or directions of surface composition gradient.
  • the polymer gradient coating comprise acidic groups.
  • the polymer gradient coating being made from monomers including monomers selected from the group consisting of acrylic acid, methacrylic acid and vinylacetic acid.
  • the polymer gradient coating comprise alkaline groups.
  • the polymer gradient coating being made from monomers including monomers selected from the group consisting of cyanoacrylate, cyanomethacrylate, ethylene diamine and allylamine.
  • the polymer gradient coating comprise neutral groups, such as pH neutral groups.
  • the polymer gradient coating being made from monomers including monomers selected from the group consisting of propylene, ethylene, styrene, methyl vinyl ether, hexene, ethyleneglycolvinylether, diethyleneglycolvinylether and vinylpyrolidone.
  • the composition gradient is a pH gradient
  • the polymer gradient coating is made from monomers including at least mixtures of acrylic acid and cyanoacrylate, mixtures of acrylic acid and ethylene diamine, mixtures of acrylic acid and allylamine, or mixtures of vinylacetic acid and allylamine.
  • the composition gradient is a hydrophobicity gradient
  • the polymer gradient coating is made from monomers comprise a mixture of a monomer being relatively hydrophobic preferably selected from the group consisting of perfluorohexene, perfluoromethylpentene, hexene, pentene, cyclohexene, acetylene, styrene, vinylbornene, and mixtures thereof, and a monomer being relatively hydrophilic preferably selected from the group consisting of vinylacetate, vinylpyrolidone, ethyleneglycolvinylether, diethyleneglycolvinylether, methacrylate, methylmethacrylate, allylalcohol and mixtures thereof.
  • the substrate may further comprise a top-coating, which e.g. may be a polymeric coating, such as a top-coating in the form of a polymer layer with a thickness of below 20 nm, preferably below 5 nm, and more preferably between 0,5 and 3 nm.
  • This coating may be provided to protect the polymer gradient coating e.g. from CO 2 , O 2 or any other gases that unintentionally may react or block the components in the polymer gradient coating, or the top-coating may modified or moderated the composition gradient of the material.
  • the functional groups of e.g. a pH gradient i.e. acidic and basic groups, may not bind so strongly to the molecules intended for separation.
  • the material according to the invention is particularly useful for the separation of a mixture of organic compounds, in particular proteins.
  • the present invention also provides a novel process for the manufacture of the materials having on the surface thereof a composition gradient as defined in the claims.
  • the process according to the invention comprise the steps of:
  • the monomers being applied onto the surface so that the layer or the composition of monomers varies continuously or stepwise in at least one direction along the surface of the substrate to thereby provide a surface composition gradient.
  • the step iv of bringing the monomers to polymerises means that a least some of the monomers is broad to reaction or polymerisation, e.g. such at as least 10 %, preferably at least 20 % and more preferably at least 40 % by weight of the monomers. Basically it is preferred that the polymerisation is sufficient to provide a solid layer which is not soluble in an aqueous solvent having a pH value between 4 and 10.
  • the monomers may be applied and polymerised using any method. The skilled person will be able so find a method which is adequate for the given monomer composition. It should be understood that the selection of monomers the thickness of coating layer(s), the selection of substrate and material and e.t.c. are as described above for the material according to the invention.
  • the monomers may be applied onto the surface and broad to polymerises using any conventional methods e.g. by using a coating process including applying the monomer with a catalyst and initiating a free radical polymerisation.
  • a coating process including applying the monomer with a catalyst and initiating a free radical polymerisation.
  • Another preferred method is the plasma process which will be described in detail below:
  • the coating process includes vaporisation coating wherein coating process, the steps iii and iv of applying the monomers onto the surface of the substrate; and bringing the monomers to polymerises; being carried out by evaporation of the monomers, deposition of the monomers and optionally a catalyst onto the substrate to provide a gradient, and bringing the monomers to polymerises by free radical polymerisation of the monomers to form the polymer coating in such a manner that the composition gradient is prepared.
  • the monomer should basically be vaporisable for this process.
  • the catalyst may in principle be any type of catalyst useful for providing a sufficiently polymerisation.
  • the catalyst may be applied in a separate step or simultaneously with the other components.
  • the composition gradient may be provided by use of masking as described above under the plasma process.
  • the plasma process may preferably comprise the steps of:
  • Plasma chemical vapour deposition (CVD) methods for modification of surfaces are known in the art.
  • US 5,643,638 describes a method for producing a gradient layer in the direction of the layer growth. The technique was developed for modification of the mechanical properties of optical lenses.
  • US 5,217,749 describes a method of making polymer thin films for optical uses by utilising plasma polymerisation techniques. The method is particularly relevant for depositing layers having different refractive indices on optical lenses, optical wave guides or in optical integrated circuitry.
  • the sheet-like substrate can be of any format and size as described above, and the substrate may comprise a pre-coating e.g. in the form of a plasma-coating.
  • the layer of plasma polymerised coating is deposited on the sheet-like substrate in a manner so as to provide the composition gradient in thicknesses as described above.
  • the coating layer should as mentioned be present on at least a part of the surface of the substrate, typically on at least 20% of the surface area, such as at least 40% of the surface area. In many instances, such as those illustrated in the examples, the coating is present on essentially the total surface of the substrate. In the instances where only a fraction of the surface of the substrate should be covered, the plasma reaction chamber may include means for covering/masking the part of the surface where the coating is undesirable/unnecessary, or the substrate may be covered by a material (e.g. an adhesive tape) which subsequently can be detached from the substrate. Generally, both sides of a substrate is coated, but it is possible to avoid coating of the one side of the substrate by the means indicated above or by means easily derived by the person skilled in the art.
  • the direction of the gradient may preferably be determined by a movement of the substrate through the plasma reaction chamber during the application of polymer gradient coating.
  • the plasma reaction chamber can basically be of any conventional type, however it should be possible to adapt means for moving the substrate through the reaction chamber.
  • One example of a suitable reaction chamber is outlined in the figure.
  • An other possible reaction chamber is the one described by the applicant in the earlier WO 00/44207 or those utilising the electrode system described in EP 0 741 404 B1. These publications are hereby incorporated by reference.
  • the plasma generated should have a level of intensity which allows a substantial portion of the functional groups, e.g. acidic groups, basic groups, lipophilic group, etc. to be preserved. It is possible to utilise a 2 or 3 phase AC plasma which offers the possibility of using a sufficiently low energy, e.g. energy levels of less than 10 W/l such as less than 5 W/l or even less than 2 W/l. Alternatively, a pulsed RF plasma can be used, e.g. of 20-100 ms on-time per second.
  • the pressure in the reaction chamber should preferably be in the range of 10-1000 ⁇ bar, such as 50-200 ⁇ bar.
  • the pressure in the reaction chamber is controlled by a vacuum pump, and a supply of an inert gas and the coating gas.
  • the inert gas is suitably a noble gas such as helium, argon, neon, krypton or a mixture thereof.
  • the combination of energy level and pressure could be so that the pressure is about 50-200 ⁇ bar and the energy level should be less than 6 W/l for a situation where the coating gas comprises sensitive monomers.
  • the step of providing a plasma reaction chamber will be performed in accordance with the instructions given herein with possible modification obvious for the person skilled in the art.
  • the step of moving the part of the substrate on which the plasma polymerisation is intended relative to the reaction chamber is essential for the process according to the invention.
  • the substrate is typically moved in a direction substantially parallel to the plane of the substrate. More precisely, the substrate is moved in the direction corresponding to the direction of the desired gradient. It should be understood that the substrate may be moved in an angled direction with respect to the plane of the substrate (e.g. up to 30° off the parallel to the plane), however this will normally not provide any significant benefits.
  • the sheet-like substrate may be more or less stationary relative to the reaction chamber.
  • the sheet-like substrate may be masked so that only an only a part of the substrate is exposed to the coating gas (e.g. through a slot in the "mask”).
  • the "mask” may then be moved relative to the reaction chamber in order to provide the composition gradient.
  • the surface to be coated is being exposed to be coated in the reaction zone by moving the substrate through the reaction chamber or placing the substrate in the reaction chamber with its surface partly or totally masked, and moving the mask continuously or stepwise to expose the surface to be coated.
  • the movement of the mask may preferably be in a direction substantially parallel to the plane of the substrate; and the movement of the mask and the feeding of the coating gas providing conditions so that the coating gas is allowed to deposit and polymerise on the surface of the substrate; wherein the deposition and polymerisation conditions are varied in response to the position of the mask on the sheet-like substrate in the plasma reaction chamber so as to provide the composition gradient.
  • the feeding of the substrate may preferably be conducted in a continuous manner so as to provide a uniform gradient, however it is possible to vary the speed (see below) or to move the sheet-like substrate in a step-wise manner.
  • the sheet-like substrate can be moved through the reaction chamber using a conveyor belt to which the sheet-like substrate is clamped, or the sheet-like substrate may be attached to a tape.
  • the sheet-like substrate is provided in the form of a tape, which is spooled between two reels. In this way a relatively long and broad band is provided which can be cut into finer tapes or sheets.
  • the prepared material may subsequently be divided into two or more smaller pieces.
  • a coating gas is fed into the reaction chamber.
  • the coating gas may comprise one or more monomers participating in the plasma polymerisation process; preferably two or more monomer types are used. It is envisaged that the feeding can be conducted by using "conventional" means such as flow controllers, gas inlets, etc., however as will be apparent from following, the accurate control of the feeding process is often quite important for the overall process.
  • the feeding may be continuous or varied, or step-wise, e.g. in phase with the step-wise feed of the substrate, etc. The location of feed nozzles, etc. will determine where and how efficient the coating gas is deposited as will be appreciated by the person skilled in the art.
  • the plasma reaction chamber, the movement of the substrate, and the feeding of the coating gas may preferably in combination provide conditions so that the coating gas is allowed to deposit and polymerise on the surface of the substrate; wherein the deposition and polymerisation conditions are varied in response to the position of the sheet-like substrate in the plasma reaction chamber so as to provide the composition gradient.
  • the coating gas may comprise one or more monomers.
  • the coating gas comprises at least two monomers and preferably at least one functional group monomer.
  • the functionalities of the monomers may deliberately be chosen so that the functionality is transformed in the plasma polymerisation process, e.g. as described and illustrated below for the cyanoacrylate which transforms to acrylamide in the course of the plasma polymerisation process. Due to the fact that a substantial amount of the monomers should survive (or at least not loose the desired functional group) in the plasma until polymerisation on the substrate, it is preferred that monomers having relatively low molecular weights are utilised, e.g.
  • a pH gradient it is relevant to utilise at least one type of monomer providing an acidic group (e.g. acrylic acid, methacrylic acid, vinylacetic acid, etc.) and/or at least one type of monomer providing a basic group (e.g. cyanoacrylate, cyanomethacrylate, ethylene diamine, allylamine, etc.).
  • a monomer which only provides a substantially neutral group so at to moderate the density of the acidic and/or basic groups on the coating.
  • the term "providing” is use in order to express that the functional group may be "masked” in the monomer used as starting material (e.g. as for cyanoacrylate).
  • a coating gas for providing a pH gradient may comprise a mixture of a monomer providing an acidic group and a monomer providing a basic group, e.g. mixtures of acrylic acid and cyanoacrylate, mixtures of acrylic acid and ethylene diamine, mixtures of acrylic acid and allylamine, or mixtures of vinylacetic acid and allylamine.
  • mixtures may furthermore include monomers which only provides substantially neutral groups, e.g. propylene, ethylene, styrene, methyl vinyl ether, hexene, ethyleneglycolvinylether, diethyleneglycolvinylether, vinylpyrolidone, etc.
  • monomers which only provides substantially neutral groups e.g. propylene, ethylene, styrene, methyl vinyl ether, hexene, ethyleneglycolvinylether, diethyleneglycolvinylether, vinylpyrolidone, etc.
  • a coating gas for providing a hydrophobicity gradient, a polarity gradient, or a surface tension gradient may comprise a mixture of a monomer being relatively hydrophobic (e.g. perfluorohexene, perfluoromethylpentene, hexene, pentene, cyclohexene, acetylene, styrene, vinylbornene, etc.) and a monomer being relatively hydrophilic (e.g. vinylacetate, vinylpyrolidone, ethyleneglycolvinylether, diethyleneglycolvinylether, methacrylate, methylmethacrylate, allylalcohol, etc.).
  • a monomer being relatively hydrophobic e.g. perfluorohexene, perfluoromethylpentene, hexene, pentene, cyclohexene, acetylene, styrene, vinylbornene, etc.
  • a monomer being relatively hydrophilic
  • the deposition and polymerisation conditions are important for the preparation of the composition gradient.
  • the plasma polymerisation process can be changed to a smaller or larger degree in such a manner that the desired composition gradient is obtained.
  • the deposition and polymerisation conditions are varied by varying the composition of the coating gas (see the examples section).
  • the deposition and polymerisation conditions are varied by varying the speed at which the substrate is moved through the plasma reaction chamber.
  • the deposition and polymerisation conditions are varied by varying the partial pressure of the coating gas. In still another embodiments, the deposition and polymerisation conditions are varied by varying the pressure and/or voltage in the plasma reaction chamber or the pulse width and/or amplitude of the plasma voltage.
  • composition gradient of the material may be further modified or moderated by providing a thin coat of a further polymer on top of the gradient, e.g. by a plasma polymerisation process.
  • the functional groups of e.g. a pH gradient i.e. acidic and basic groups, may not bind so strongly to the molecules intended for separation.
  • a layer may be quite thin such as 0.5-20 nm.
  • the materials of the present invention are according to preliminary experiments particularly useful for the separation of mixtures of organic compounds, e.g. biomolecules such as proteins in application where electrophoresis gels normally are used.
  • the present invention also relates to the use of the sheet-formed material as described above for the separation of a mixture of organic compounds, in particular proteins.
  • Example 1 Manufacturing a pH-gradient for separation of proteins
  • the substrate for the pH-gradient was a polyethylene/polypropylene (PE/PP) felt from Freudenberg (VK1099, 60g/m2), which was available in 30 mm wide rolls.
  • PE/PP polyethylene/polypropylene
  • the substrate felt was spooled from one reel to another under the plasma polymerisation. Hereby the felt passed through the plasma reaction chamber; about 5 cm of the felt (in the length-wise direction) was exposed in the reaction chamber.
  • the plasma was generated by a 2-phase AC supply.
  • the plasma polymerisation of the acidic and basic monomers took place in the reaction chamber by simultaneously varying the mixture of acidic and basic monomers.
  • Acrylic acid was used as the monomer having an acidic group and allylamine was used as monomer having a basic group.
  • the acrylic acid was bubbled through with argon.
  • the reels for spooling were placed in boxes provided with a flow of argon (slight over pressure in relation to the polymerisation area) to prevent undesirable downstream polymerisation ("protection Ar").
  • the reaction chamber with reels was essentially constructed as outlined in the figure
  • the felt (4 metres) was placed on the winding-equipment (reels).
  • the vacuum chamber was closed and evacuated to a pressure of 10 ⁇ bar.
  • a flow of argon for bubbling the acrylic acid was adjusted to 20 seem (standard cubic centimetres per minute (ml/min)) with the use of a flow controller.
  • the flow of argon/acrylic acid was adjusted to 40 seem.
  • the flow of allylamine was adjusted to 3 seem.
  • the flow of "protection Ar" was adjusted to
  • the pressure was increased to 100 ⁇ bar and was kept constant at this level during the plasma polymerisation.
  • the plasma was turned on with an effect of 2 W/l and was kept constant at this level during the plasma polymerisation.
  • the spooling of the felt was started with a speed of 10 cm/min corresponding to a "residence time" in the plasma reaction chamber of 30 sec.
  • the reaction provided a felt having a pH gradient on the surface thereof.
  • the strips showed a pH-range from 4.5 to 7.5 which equals to 1 pH-unit per metre.
  • the thickness of the plasma polymerised layer of acidic and basic monomer was in the range of 30-40 nm.
  • the felt was cut into strips of 3 mm width, spooled and packed.
  • Example 2 Modification ofpH gradient
  • the felt provided with a pH gradient as described in Example 1 was modified in order to make the functional groups of the plasma polymerised coating less susceptible to reaction with the organic molecules to be separated on the surface. This was done by providing .a thin layer of a pH inert polymer on top of the polymers representing the pH gradient. This modification procedure followed the above process after the plasma was turned off (i.e. before the "All flows, except for that of "protection Ar", were interrupted") :
  • the thickness of the polymerised diethylenglycolvinylether was around 3-4 nm.
  • the strips showed a pH-range from 4.5 to 7.5 which equals to 1 pH-unit per metre.
  • the roll could be sliced into strips of 3 mm width for the protein separation.
  • Example 3 Manufacturing a membrane with varying hydrophilicity for the separation of biomolecules
  • PE membrane 200 ⁇ m thick, 10 ⁇ m pore size
  • hydrophilic monomer vinylpyrolidone bubbled with argon (argon/vinylpyrolidone) and as the hydrophobic monomer was used hexene.
  • the membrane was spooled from one reel to another during the plasma polymerisation. Hereby the felt passed through the plasma reaction chamber equipped as described in Example 1.
  • the plasma polymerisation of the hydrophilic and hydrophobic monomers took place by simultaneously varying the mixture of hydrophilic and hydrophobic monomers.
  • the vacuum chamber was closed and evacuated to a pressure of 10 ⁇ bar.
  • the flow of argon for bobbling the vinylpyrolidone was adjusted to 10 seem by a flow controller.
  • the flow of argon/vinylpyrolidone was adjusted to 50 seem.
  • the initial flow of hexene was set to 0 seem.
  • the flow of "protection Ar” was adjusted to 20 seem.
  • the pressure was allowed to increase to 100 ⁇ bar and was kept at this level during the polymerisation.
  • the plasma was turned on with an effect of 0.5 W/l and was kept constant at this level during the polymerisation.
  • the plasma was turned off and after one minute the spooling was stopped. All flows, except "protection Ar", were interrupted and the pressure was lowered to 40 ⁇ bar. After 1 min at this pressure, the flow of "protection Ar” was interrupted and the pressure was allowed to raise to atmospheric pressure and the vacuum chamber was opened.

Abstract

L'invention concerne une matière comportant un substrat s'apparentant à une feuille et une couche polymère à gradient sur au moins une partie de la surface du substrat, ladite couche représentant un gradient de composition de surface, tel qu'un gradient de pH ou un gradient d'hydrophilie/hydrophobie dans au moins une direction le long de la surface du substrat. L'invention concerne également un procédé de production de ladite matière et de son substrat comprenant les étapes suivantes : i. mettre à disposition le substrat s'apparentant à une feuille, ii. mettre à disposition les monomères pour la couche polymère à gradient, iii. appliquer les monomères sur la surface du substrat et iv. provoquer la polymérisation des monomères, ces derniers étant appliqués sur la surface de manière à ce que la couche ou la composition des monomères varie continuellement ou par étapes dans au moins une direction le long de la surface du substrat pour permettre l'obtention d'un gradient de composition de surface. Le procédé peut de préférence consister à appliquer la couche polymère à gradient au moyen d'un traitement au plasma.
PCT/DK2001/000689 2000-10-19 2001-10-18 Matiere utile pour la separation de composes organiques, procedes pour sa preparation et utilisation de cette matiere WO2002032591A2 (fr)

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WO2002071048A1 (fr) * 2001-03-07 2002-09-12 Picosep A/S Processus de separation de biocomposants sur une surface de substrat
WO2003082483A1 (fr) * 2002-03-28 2003-10-09 Plasso Technology Limited Preparation de revetements au moyen de la polymerisation par plasma
WO2004023131A1 (fr) * 2002-09-03 2004-03-18 Proteosys Ag Focalisation isoelectrique sur des gradients de ph immobilises
EP1448807A1 (fr) * 2001-10-30 2004-08-25 Massachusetts Institute Of Technology Copolymeres de fluorocarbone-organosilicium et revetements prepares par depot chimique en phase vapeur par filament chaud
WO2004111648A2 (fr) * 2003-06-12 2004-12-23 Plasso Technology Ltd Procedes
EP1540324A2 (fr) * 2002-06-07 2005-06-15 Picosep A/S Procede et systeme pour focalisation ipoeletrique en plusieures etapes
WO2008022682A1 (fr) * 2006-08-23 2008-02-28 Carl Freudenberg Kg Non-tissés avec un potentiel zêta positif
EP1930721A3 (fr) * 2002-06-07 2008-09-03 Picosep A/S Procédé et système pour focalisation isoélectrique en plusieures étapes
US8288118B2 (en) 2007-09-19 2012-10-16 Becton, Dickinson And Company Method of analyzing various surface chemistries for culturing a given cell line
WO2023185672A1 (fr) * 2022-03-29 2023-10-05 江苏菲沃泰纳米科技股份有限公司 Revêtement antibuée, son procédé de préparation, et produit

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EP0896035A2 (fr) * 1997-08-08 1999-02-10 Board of Regents, The University of Texas System Revêtements mouillables, résistants à l'encrassement
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WO1999028530A1 (fr) * 1997-12-04 1999-06-10 Korea Institute Of Science And Technology Amelioration par polymerisation au plasma de la surface d'un metal utilisable dans des applications de refrigeration ou de climatisation
EP0962549A2 (fr) * 1998-05-28 1999-12-08 John T. Felts Appareil de déposition à plasma à sources multiples
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GB1012745A (en) * 1962-11-07 1965-12-08 Radiation Res Corp Polymerizing method and apparatus
US4609445A (en) * 1983-12-29 1986-09-02 Mobil Oil Corporation Method of plasma treating a polymer film to change its properties
US6123821A (en) * 1997-06-24 2000-09-26 Large Scale Biology Corporation Automated system for two-dimensional electrophoresis
EP0896035A2 (fr) * 1997-08-08 1999-02-10 Board of Regents, The University of Texas System Revêtements mouillables, résistants à l'encrassement
WO1999010560A1 (fr) * 1997-08-29 1999-03-04 Minnesota Mining And Manufacturing Company Procede et appareil a jet de plasma pour deposer des revetements, et revetements resultants
WO1999028530A1 (fr) * 1997-12-04 1999-06-10 Korea Institute Of Science And Technology Amelioration par polymerisation au plasma de la surface d'un metal utilisable dans des applications de refrigeration ou de climatisation
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WO2002071048A1 (fr) * 2001-03-07 2002-09-12 Picosep A/S Processus de separation de biocomposants sur une surface de substrat
EP1448807A1 (fr) * 2001-10-30 2004-08-25 Massachusetts Institute Of Technology Copolymeres de fluorocarbone-organosilicium et revetements prepares par depot chimique en phase vapeur par filament chaud
EP1448807A4 (fr) * 2001-10-30 2005-07-13 Massachusetts Inst Technology Copolymeres de fluorocarbone-organosilicium et revetements prepares par depot chimique en phase vapeur par filament chaud
CN100400183C (zh) * 2002-03-28 2008-07-09 普拉索技术有限公司 通过等离子体聚合制备涂层
WO2003082483A1 (fr) * 2002-03-28 2003-10-09 Plasso Technology Limited Preparation de revetements au moyen de la polymerisation par plasma
AU2003216858B2 (en) * 2002-03-28 2008-04-10 Corning Incorporated Preparation of coatings through plasma polymerization
EP2177902A1 (fr) * 2002-06-07 2010-04-21 Picosep A/S Procédé et système pour focalisation isoélectrique en plusieures étapes
EP1540324A2 (fr) * 2002-06-07 2005-06-15 Picosep A/S Procede et systeme pour focalisation ipoeletrique en plusieures etapes
EP1930721A3 (fr) * 2002-06-07 2008-09-03 Picosep A/S Procédé et système pour focalisation isoélectrique en plusieures étapes
WO2004023131A1 (fr) * 2002-09-03 2004-03-18 Proteosys Ag Focalisation isoelectrique sur des gradients de ph immobilises
WO2004111648A2 (fr) * 2003-06-12 2004-12-23 Plasso Technology Ltd Procedes
WO2004111648A3 (fr) * 2003-06-12 2005-06-02 Plasso Technology Ltd Procedes
EP2282207A1 (fr) * 2003-06-12 2011-02-09 Becton, Dickinson and Company Procedes de polymerisation plasma pour deposer des gradients chimiques et surfaces contenant un gradient de biomolecules immobilisees
JP2012214815A (ja) * 2003-06-12 2012-11-08 Becton Dickinson & Co 方法
WO2008022682A1 (fr) * 2006-08-23 2008-02-28 Carl Freudenberg Kg Non-tissés avec un potentiel zêta positif
US8288118B2 (en) 2007-09-19 2012-10-16 Becton, Dickinson And Company Method of analyzing various surface chemistries for culturing a given cell line
US8501477B2 (en) 2007-09-19 2013-08-06 Corning Incorporated Kit including substrates with various surface chemistries
US8748120B2 (en) 2007-09-19 2014-06-10 Corning Incorporated Method of selecting a surface chemistry for culturing a given cell line
WO2023185672A1 (fr) * 2022-03-29 2023-10-05 江苏菲沃泰纳米科技股份有限公司 Revêtement antibuée, son procédé de préparation, et produit

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