Classifications

• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01D—SEPARATION
  • B01D67/00—Processes specially adapted for manufacturing semi-permeable membranes for separation processes or apparatus
  • B01D67/0002—Organic membrane manufacture
  • B01D67/0006—Organic membrane manufacture by chemical reactions
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01D—SEPARATION
  • B01D67/00—Processes specially adapted for manufacturing semi-permeable membranes for separation processes or apparatus
  • B01D67/0002—Organic membrane manufacture
  • B01D67/0023—Organic membrane manufacture by inducing porosity into non porous precursor membranes
  • B01D67/003—Organic membrane manufacture by inducing porosity into non porous precursor membranes by selective elimination of components, e.g. by leaching
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01D—SEPARATION
  • B01D67/00—Processes specially adapted for manufacturing semi-permeable membranes for separation processes or apparatus
  • B01D67/0002—Organic membrane manufacture
  • B01D67/0023—Organic membrane manufacture by inducing porosity into non porous precursor membranes
  • B01D67/0032—Organic membrane manufacture by inducing porosity into non porous precursor membranes by elimination of segments of the precursor, e.g. nucleation-track membranes, lithography or laser methods
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01D—SEPARATION
  • B01D67/00—Processes specially adapted for manufacturing semi-permeable membranes for separation processes or apparatus
  • B01D67/0002—Organic membrane manufacture
  • B01D67/0023—Organic membrane manufacture by inducing porosity into non porous precursor membranes
  • B01D67/0032—Organic membrane manufacture by inducing porosity into non porous precursor membranes by elimination of segments of the precursor, e.g. nucleation-track membranes, lithography or laser methods
  • B01D67/0034—Organic membrane manufacture by inducing porosity into non porous precursor membranes by elimination of segments of the precursor, e.g. nucleation-track membranes, lithography or laser methods by micromachining techniques, e.g. using masking and etching steps, photolithography
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01D—SEPARATION
  • B01D67/00—Processes specially adapted for manufacturing semi-permeable membranes for separation processes or apparatus
  • B01D67/0081—After-treatment of organic or inorganic membranes
  • B01D67/0093—Chemical modification
  • B01D67/00933—Chemical modification by addition of a layer chemically bonded to the membrane
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01D—SEPARATION
  • B01D69/00—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
  • B01D69/02—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor characterised by their properties
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01D—SEPARATION
  • B01D69/00—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
  • B01D69/12—Composite membranes; Ultra-thin membranes
  • B01D69/125—In situ manufacturing by polymerisation, polycondensation, cross-linking or chemical reaction
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01D—SEPARATION
  • B01D69/00—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
  • B01D69/12—Composite membranes; Ultra-thin membranes
  • B01D69/125—In situ manufacturing by polymerisation, polycondensation, cross-linking or chemical reaction
  • B01D69/127—In situ manufacturing by polymerisation, polycondensation, cross-linking or chemical reaction using electrical discharge or plasma-polymerisation
• • H—ELECTRICITY
  • H01—ELECTRIC ELEMENTS
  • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
  • H01M8/00—Fuel cells; Manufacture thereof
  • H01M8/10—Fuel cells with solid electrolytes
  • H01M8/1016—Fuel cells with solid electrolytes characterised by the electrolyte material
  • H01M8/1018—Polymeric electrolyte materials
  • H01M8/102—Polymeric electrolyte materials characterised by the chemical structure of the main chain of the ion-conducting polymer
  • H01M8/1023—Polymeric electrolyte materials characterised by the chemical structure of the main chain of the ion-conducting polymer having only carbon, e.g. polyarylenes, polystyrenes or polybutadiene-styrenes
• • H—ELECTRICITY
  • H01—ELECTRIC ELEMENTS
  • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
  • H01M8/00—Fuel cells; Manufacture thereof
  • H01M8/10—Fuel cells with solid electrolytes
  • H01M8/1016—Fuel cells with solid electrolytes characterised by the electrolyte material
  • H01M8/1018—Polymeric electrolyte materials
  • H01M8/1041—Polymer electrolyte composites, mixtures or blends
  • H01M8/1053—Polymer electrolyte composites, mixtures or blends consisting of layers of polymers with at least one layer being ionically conductive
• • H—ELECTRICITY
  • H01—ELECTRIC ELEMENTS
  • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
  • H01M8/00—Fuel cells; Manufacture thereof
  • H01M8/10—Fuel cells with solid electrolytes
  • H01M8/1016—Fuel cells with solid electrolytes characterised by the electrolyte material
  • H01M8/1018—Polymeric electrolyte materials
  • H01M8/1069—Polymeric electrolyte materials characterised by the manufacturing processes
  • H01M8/1072—Polymeric electrolyte materials characterised by the manufacturing processes by chemical reactions, e.g. in situ polymerisation or in situ crosslinking
• • H—ELECTRICITY
  • H01—ELECTRIC ELEMENTS
  • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
  • H01M8/00—Fuel cells; Manufacture thereof
  • H01M8/10—Fuel cells with solid electrolytes
  • H01M8/1016—Fuel cells with solid electrolytes characterised by the electrolyte material
  • H01M8/1018—Polymeric electrolyte materials
  • H01M8/1069—Polymeric electrolyte materials characterised by the manufacturing processes
  • H01M8/1081—Polymeric electrolyte materials characterised by the manufacturing processes starting from solutions, dispersions or slurries exclusively of polymers
• • H—ELECTRICITY
  • H01—ELECTRIC ELEMENTS
  • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
  • H01M8/00—Fuel cells; Manufacture thereof
  • H01M8/10—Fuel cells with solid electrolytes
  • H01M8/1016—Fuel cells with solid electrolytes characterised by the electrolyte material
  • H01M8/1018—Polymeric electrolyte materials
  • H01M8/1069—Polymeric electrolyte materials characterised by the manufacturing processes
  • H01M8/1086—After-treatment of the membrane other than by polymerisation
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01D—SEPARATION
  • B01D2323/00—Details relating to membrane preparation
  • B01D2323/30—Cross-linking
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01D—SEPARATION
  • B01D2323/00—Details relating to membrane preparation
  • B01D2323/34—Use of radiation
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01D—SEPARATION
  • B01D2323/00—Details relating to membrane preparation
  • B01D2323/34—Use of radiation
  • B01D2323/345—UV-treatment
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01D—SEPARATION
  • B01D2325/00—Details relating to properties of membranes
  • B01D2325/02—Details relating to pores or porosity of the membranes
  • B01D2325/028—Microfluidic pore structures
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01D—SEPARATION
  • B01D2325/00—Details relating to properties of membranes
  • B01D2325/04—Characteristic thickness
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01D—SEPARATION
  • B01D2325/00—Details relating to properties of membranes
  • B01D2325/22—Thermal or heat-resistance properties
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01D—SEPARATION
  • B01D2325/00—Details relating to properties of membranes
  • B01D2325/24—Mechanical properties, e.g. strength
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01D—SEPARATION
  • B01D2325/00—Details relating to properties of membranes
  • B01D2325/30—Chemical resistance
• • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
  • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
  • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
  • Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
  • Y02E60/30—Hydrogen technology
  • Y02E60/50—Fuel cells
• • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
  • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
  • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
  • Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
  • Y02P70/50—Manufacturing or production processes characterised by the final manufactured product
• • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
  • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
  • Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
  • Y10T428/00—Stock material or miscellaneous articles
  • Y10T428/24—Structurally defined web or sheet [e.g., overall dimension, etc.]
  • Y10T428/24273—Structurally defined web or sheet [e.g., overall dimension, etc.] including aperture
• • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
  • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
  • Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
  • Y10T428/00—Stock material or miscellaneous articles
  • Y10T428/24—Structurally defined web or sheet [e.g., overall dimension, etc.]
  • Y10T428/24273—Structurally defined web or sheet [e.g., overall dimension, etc.] including aperture
  • Y10T428/24322—Composite web or sheet

Definitions

• the present invention relates to a membrane which comprises at least one molecular monolayer composed of low molecular weight aromatics and crosslinked in a lateral direction, the membrane having a thickness in the range from 1 to 200 nm and a perforation in the form of openings with a diameter in the Range of 0.1 nm to 1 micron, a process for their preparation and their use.
• membranes are understood to mean semipermeable sheets. Such membranes have pores or openings extending from one major surface to the other major surface of the membrane.
• Conventional membranes are made of polymers such as polyethersulfones, cellulose acetates, polyvinylidene fluorides, polypropenes, polyethenes, polytetrafluoroethenes, and polyamides, and usually have a thickness in the range of 5 to 500 microns.
• semipermeable membranes are used as membrane filters or as adsorption membranes.
• a membrane filter is a membrane in which the separation of substances is determined by the pore size. Only those molecules can pass through the membrane whose diameter is smaller than the diameter of the pores of the membrane.
• the membrane material be mechanically stable as well as thermally and chemically resistant is.
• attempts are being made to produce increasingly thinner membranes and to bring them to use in various technical fields.
• reducing the thickness of membranes is generally associated with a deterioration in mechanical stability.
• molecular monolayers with a thickness in the range of a few nanometers have been described. However, these are not suitable as a membrane filter or adsorption membrane.
• the present invention is therefore based on the object to provide a membrane having a thickness in the nanometer range and thus thinner than conventional membranes, which is mechanically extremely stable and thermally and chemically resistant, and which is capable of membrane separation and / or adsorption membrane for separation ,
• This object is achieved by the embodiments characterized in the claims.
• a membrane which comprises at least one molecular monolayer composed of low molecular weight aromatics and cross-linked in a lateral direction, the membrane having a thickness in the range of 1 to 200 nm and a perforation in the form of openings in the range of 0.1 nm to 1 micron.
• a “molecular monolayer” is understood as meaning a layer which has only the thickness of a molecule. This monolayer is according to the invention of low molecular weight
• the molecular monolayer may have any suitable thickness.
• such a molecular monolayer has a layer thickness in the range of 0.1 nm to 10 nm, particularly preferably in the range of 0.3 nm to 3 nm, more preferably in the range of 1 to 2 nm.
• the membrane according to the invention has a thickness in the range from 1 to 200 nm. If the thickness is less than 1 nm, the membrane is difficult to handle and not sufficiently tear-resistant. On the other hand, if the thickness is more than 200 nm, the manufacturing process becomes too expensive and sufficient permeability is no longer given.
• the membrane according to the invention has a thickness in the range from 1 to 50 nm, more preferably a thickness in the range from 1 to 20 nm. More preferably, the membrane according to the invention has a thickness in the range from 1 to 2 nm. Since the membrane according to the invention has a thickness in the nanometer range, this is referred to below as a nanomembrane.
• the thickness of the monolayer or of the membrane according to the invention can be determined by methods known to the person skilled in the art, for example by means of atomic force microscopy (AFM).
• AFM atomic force microscopy
• the membrane according to the invention is therefore constructed from a stack of at least two molecular monolayers arranged one above the other.
• 2 to 100 monolayers are arranged one above the other, more preferably 2 to 50, more preferably 2 to 10 monolayers are arranged one above the other.
• the term “low molecular weight aromatics” means those aromatic compounds which are not present in oligomeric or polymeric form. This term further includes the possibility that the aromatics are crosslinked with each other after treatment with high-energy radiation.
• aromatics includes the term “heteroaromatics", ie the term “aromatics” is understood as meaning aromatic compounds which contain no heteroatom or one or more heteroatoms in at least one aromatic ring.
• the monolayer is composed of aromatics selected from the group consisting of phenyl, biphenyl, terphenyl, naphthalene, anthracene, bipyridine, terpyridine, thiophene, bithienyl, terthienyl, pyrrole, and combinations thereof.
• the monolayer is made of Biphenyl built up. This is particularly advantageous in terms of crosslinkability in the lateral direction.
• monolayers composed of biphenyl are extremely mechanically stable. But it is also possible that the monolayer contains at least two different aromatics. For example, one region of the monolayer may be composed of biphenyl while another region of the monolayer is composed of bipyridine.
• the monolayer according to the present invention is crosslinked in the lateral direction.
• the monolayer composed of the low molecular weight aromatics attains high mechanical and chemical stability.
• the monolayer is crosslinked by treatment with electron radiation, plasma radiation, X-radiation, .beta.-radiation, .gamma. Radiation, UV radiation or EUV radiation ("extreme UV", with a spectral range between about 1 nm and about 50 nm).
• the membrane according to the invention has a perforation.
• a perforation is understood to mean that the membrane has openings or pores which extend from one main surface to the other main surface of the membrane. These openings have a diameter in the range of 0.1 nm to 1 ⁇ m. In a preferred embodiment of the present invention, the openings have a diameter in the range of 0.1 nm to 100 nm. In another preferred embodiment, the openings have a diameter in the range of 100 nm to 1 ⁇ m.
• a suitable pore size or size of the openings can be selected here.
• the pore size can be determined by suitable imaging methods, such as. As transmission electron microscopy (TEM) or scanning electron microscopy (SEM) can be measured. The radius of circular pores can be determined as well as the shape and area of the opening in non-circular pores.
• perforation includes on the one hand an undirected perforation, on the other hand a directed perforation.
• Undirected perforation is understood as a formation of pores, which occurs in the context of the production of the membrane and for which no special measures are to be taken.
• a certain number of pores may be formed in the conventional manufacturing process of a membrane, resulting in an undirected perforation to some extent.
• a directed or targeted perforation according to the invention a perforation understood, for a targeted action is necessary to form the pores in the membrane. This can be done for example by chemical or physical methods.
• the membrane may have any suitable number of openings. The larger the number of openings, the greater the permeability of the membrane.
• the membrane has at least 10 3 openings per mm 2 of the surface of the membrane as a perforation. If the membrane comprises less than 10 3 openings, sufficient flow is not ensured, which makes substance separation using the membrane according to the invention more difficult.
• the membrane 10 has 3 to 10 12 openings per mm 2 of the surface of the membrane as a perforation. Further preferably, the membrane has at least 10 8 openings per mm 2 of the surface of the membrane as a perforation.
• the openings in the individual monolayers together form the openings or pores of the entire membrane.
• the pores, ie the openings make up at least 5% of the surface of the membrane. More preferably, at least 10%, more preferably at least 20%, of the surface area of the membrane is apertures. Preferably, not more than 80% of the surface of the membrane is made up of openings. If this value is exceeded, a sufficient mechanical stability of the membrane is no longer guaranteed.
• one of the two surfaces is at least one molecular monolayer modified by functional groups.
• the functional groups are each bound to the aromatics.
• the functional groups may be all functional groups which are not cleaved by the irradiation and which are suitable for further reaction, for example in order to reversibly or irreversibly attach further molecules to the monolayer.
• the functional groups are selected from amino groups, nitro groups, carboxy groups, cyano groups, thiol groups, hydroxy groups, and combinations thereof.
• one of the two surfaces of at least one molecular monolayer is modified by amino groups as functional groups.
• the functional groups are special ligands which are suitable for binding specific target molecules.
• ligands may be bonded to the molecular monolayer by modification of the aforementioned amino groups, nitro groups, carboxy groups, cyano groups, thiol groups or hydroxy groups.
• ligands are ion exchangers, chelating agents, amino acids, coenzymes, cofactors and their analogs, endocrine and exocrine substances, such as hormones, enzyme substrates, enzyme inhibitors, nucleic acids, such as DNA and RNA, viruses, and polypeptides, such as proteins, in particular Antibodies and enzymes.
• the surface of the monolayer is preferably substantially completely modified by functional group, ie, substantially all aromatics of the monolayer carry a functional group.
• the surface may have a pattern of functional groups.
• a pattern of functional groups is a chemical structuring of the surface, the functional groups representing this chemical structuring, forming the desired pattern on the surface of the monolayer. This pattern is obtained by partial functionalization of the surface with functional groups.
• a monolayer with a targeted pattern of functional groups can be obtained in this way.
• the use of a membrane modified by functional groups is particularly advantageous when the membrane is to be used as adsorption membrane for the separation of certain substances.
• Such substances may, for example, be substances which are to be obtained from a medium in enriched or pure form. These may be, for example, recombinant proteins. But it is also possible that the substances to be absorbed are contaminants that are to be removed from a medium. These may be, for example, viruses, proteins, amino acids, nucleic acids or endotoxins.
• the functional group should be chosen such that it is suitable for reversibly or irreversibly binding the substance to be absorbed. If a substance is to be isolated from a medium, it is advantageous if the binding of this substance to the functional group is reversible. Even if the molecules to be separated are not adsorbed on the functional groups, these functional groups may nevertheless influence the diffusion of these molecules.
• the membrane of the invention consists of more than one molecular monolayer, one or more of the molecular monolayers may be modified by functional groups.
• all molecular monolayers in a membrane according to the invention, which is composed of more than one molecular monolayer, are modified by functional groups. This allows a high concentration of functional groups on or in the membrane, which is advantageous, for example, in terms of absorption capacity when used as an absorption membrane.
• the membrane of the invention may further comprise an additional coating.
• this coating should not completely close the openings, so that further permeability of the membrane is given.
• the coating may be, for example, a metal coating.
• the coating is a coating of gold.
• the coating can be any have appropriate thickness.
• the coating preferably has a thickness in the range from 1 nm to 10 nm, particularly preferably in the range from 2 nm to 5 nm.
• Such an additional coating enables, for example, better imaging of the surface of the membrane in the electron microscope.
• this additional coating can increase the mechanical stability of the membrane.
• the membrane of the invention can be prepared by any of the methods described below.
• the present invention relates to a process for producing a membrane which comprises at least one molecular monolayer composed of low molecular weight aromatics and cross-linked in a lateral direction, the membrane having a thickness in the range of 1 to 200 nm and a perforation in the form of Having openings with a diameter in the range of 0.1 nm to 1 ⁇ m, the method comprising the steps of:
• step (c) treating the substrate obtained in step (b) with high-energy radiation in such a way that the monolayer composed of low molecular weight aromatics is cross-linked in the lateral direction, and
• the method further comprising the step during or after any one of the above steps (a) to (d):
• the process described above describes a production process for the membrane according to the invention, in which the perforation is directed or targeted.
• This method therefore comprises the step (e) of perforating the membrane, whereby the pores are formed in a targeted manner.
• the method according to the invention comprises the step (e) of perforating the membrane, which is effected in such a way that openings having a diameter in the range from 0.1 nm to 1 ⁇ m are produced ,
• the perforation can be done by any suitable method.
• the perforation between steps (c) and (d) or after step (d) is carried out by irradiation with particle radiation selected from the group consisting of electron radiation and ion radiation.
• particle radiation selected from the group consisting of electron radiation and ion radiation. This method is also referred to below as the perforation method (1).
• an intact membrane is first prepared, which may either still bound to the substrate or after removal of the substrate in step (d) may be free.
• This membrane is then perforated by irradiation with particle radiation.
• particle radiation For this it is necessary that this radiation has an appropriate energy and dose to create openings in the membrane. If energy and dose are too high, the membrane can tear. If the energy is too low, it must be exposed too long.
• radiation from a range of 5V to 5OkV is used, since only small doses of radiation are sufficient to perforate thin membranes. This can be done, for example, by means of finely focused electron radiation or ion radiation.
• the focusing and the scanning of the beam over the areas to be structured can be done by electron-optical or ion-optical elements, such as in electron beam lithography with scanning electron microscopes or focused ion lithography (FIB).
• the generation of openings in the nanomembrane can also be carried out by means of local probe methods.
• the focusing of electrons or ions is ensured in these by the smallness of the electron or ion source (Nahsonde).
• the local probe is then guided over the regions to be structured at intervals of between 0.1 and 1000 nm.
• STM scanning tunneling microscopes
• AFM atomic force microscopes
• FAM atomically defined field emitter tips
• the openings by irradiation with particle radiation in conjunction with a shadow mask such that only spatially defined areas of the membrane are sieved, whereby the openings are produced at the irradiated sites.
• a large area illuminating electron source can be used in conjunction with a shadow mask, so that only the open areas are exposed to the electrons.
• the perforation is performed by incompletely crosslinking in step (c) to form a monolayer having crosslinked and uncrosslinked areas, thereby removing the uncrosslinked areas of the monolayer, thereby forming the perforation ,
• This can be done, for example, by one of the following perforation methods (2) to (5).
• the perforation of the nanomembrane already takes place during the crosslinking in step (c) of the method according to the invention.
• the entire monolayer is crosslinked by radiation, but only a certain area.
• the low molecular weight aromatics of the non-crosslinked regions have essentially no bonds to the crosslinked regions of the monolayer and can therefore be easily removed after removal of the substrate.
• Corresponding methods are known to the person skilled in the art. This can be done, for example, by simply washing out the non-crosslinked low molecular weight aromatics.
• the openings in the monolayer then form If the substrate is dissolved, for example, by wet-chemical etching, the molecules in the non-crosslinked regions lack the fixing backing. Since the molecules are not interlinked with each other, they go into solution when the substrate is etched and openings are formed.
• the dissolution of a gold substrate can be done, for example, by placing it in a KCN solution.
• the dissolution of a SiN substrate can be done for example by HF, the dissolution of Si can be done for example by KOH.
• the selective crosslinking can be carried out, for example, to form a structuring by means of finely focused ionizing electron, ion or photon radiation.
• the treatment with high-energy radiation is carried out using a lithographic method such that only spatially defined regions of the monolayer applied to the substrate surface are irradiated, whereby a structured surface is formed on the substrate.
• a lithographic method such that only spatially defined regions of the monolayer applied to the substrate surface are irradiated, whereby a structured surface is formed on the substrate.
• electromagnetic radiation eg X-ray radiation, UV radiation, EUV radiation
• light sources available in the prior art are available in conjunction with masks suitable for the respective wavelength range or scanning by means of suitable light guides.
• the structuring is carried out by a large area illuminated electron source in conjunction with a shadow mask, so that only the open areas are exposed to the electrons.
• the crosslinking takes place by illuminating a surface by means of coherent EUV radiation, wherein two or more coherent EUV rays generate an interference pattern of standing waves on the surface of the monolayer, resulting in a selective exposure and thus in a Structuring leads.
• This EUV interference lithography can be performed at wavelengths in the range of 600 nm to 6 nm, preferably in the range of about 13 nm.
• Perforation method (3) results in perforation of the nanomembrane due to incomplete crosslinking, for example near defects in the molecular monolayer and / or the underlying substrate.
• a homogeneous and defect-free membrane is only achieved if already the surface of the substrate is atomically flat and homogeneous, i. for example, that it has no step dislocations or defects.
• a substrate having a non-homogeneous surface structure is used.
• a substrate with a rough surface can be used.
• the perforation is formed by a self-aggregation process on a prestructured substrate.
• This substrate has various regions on which the low molecular weight aromatics adsorb in different ways.
• the low molecular weight aromatics for example thiols
• adsorb in an orderly manner in another region which is not coated, no adsorption of the low molecular weight aromatics takes place.
• substrates with regions of different ordered surface morphology can be used. In the atomically smooth regions, ordered films form, while in the rough regions, no ordered adsorption occurs.
• step (c) of the method according to the invention only the ordered regions are crosslinked, while the other regions are not crosslinked.
• perforation method (2) described above can by Removing the non-crosslinked low molecular weight aromatics from the membrane to obtain a perforated membrane.
• the perforation is carried out by in step (b) of the method according to the invention a monolayer of crosslinkable low molecular weight aromatics and non-crosslinkable molecules is applied to the substrate.
• This process can also be referred to as "chemical perforation".
• At least two groups of molecules are used.
• the first group are cross-linkable molecules which later form the membrane.
• the other group are non-crosslinkable molecules, which later form the holes.
• step (c) of the process according to the invention only the crosslinkable low molecular weight aromatics are crosslinked.
• a perforated membrane can be obtained.
• non-crosslinkable molecule for example, hexadecanethiol can be used.
• a mixture of biphenylthiol as a crosslinkable aromatic (90%) and hexadecanethiol (10%) in step (b) of the method according to the invention can be used.
• Particularly preferred is the use of non-crosslinkable molecules that can form clusters of defined size by assembly. In this way it is possible to set a defined pore size controlled by the appropriate selection of non-crosslinkable molecules.
• the person skilled in the art is able to carry out the perforation methods (1) to (5) described above in such a way that openings with a diameter in the range from 0.1 nm to 1 ⁇ m are obtained.
• apertures having a diameter in the range of 0.1 nm to 100 nm are obtained. In another preferred embodiment, apertures having a diameter in the range of 100 nm to 1 ⁇ m are obtained.
• a suitable pore size or size of the openings can be selected here.
• the person skilled in the art is also able to carry out the above-described Perfoherungshabilit (1) to (5) such that a membrane with the desired number of openings is obtained.
• the perforation is performed such that the membrane has at least 10 openings per mm 2 of the surface of the membrane as a perforation.
• the membrane comprises less than 10 openings, sufficient flow is not ensured, which makes substance separation difficult by the membrane obtained by the process according to the invention.
• the membrane has 10 to 1,000 openings per mm 2 of the surface of the membrane as a perforation. Further preferably, the membrane has at least 100 openings per mm 2 of the surface of the membrane as a perforation. If the membrane according to the invention consists of more than one molecular monolayer, the openings in the individual monolayers together form the openings or pores of the entire membrane.
• the present invention further relates to a process for producing a membrane in which the perforation is carried out in an undirected manner.
• a certain number of pores may be formed in the conventional manufacturing process of a membrane, resulting in an undirected perforation to some extent.
• the present invention relates to a process for producing a membrane which comprises at least one molecular monolayer composed of low molecular weight aromatics and cross-linked in a lateral direction, the membrane having a thickness in the range from 1 to 200 nm and a perforation in the form of Having openings with a diameter in the range of 0.1 nm to 1 ⁇ m, the method comprising the steps of:
• step (b) applying a monolayer of low molecular weight aromatics with binding to at least one surface of the substrate, (c) treating the substrate obtained in step (b) with high-energy radiation in such a way that the monolayer composed of low molecular weight aromatics is cross-linked in the lateral direction, and
• step (c) wherein the perforation is formed during step (c) and / or step (d).
• the perforation which in this case is undirected, is formed in this process during step (c) and / or step (d).
• the perforation may occur at random during crosslinking of the monolayer.
• openings to form in the membrane during the removal of the substrate in step (d).
• steps (a) to (d) relate independently of one another to both methods described above.
• the substrate provided in step (a) of the method according to the invention has at least one surface and may consist of any suitable material.
• the substrate is selected from the group consisting of gold, silver, titanium, zirconium, vanadium, chromium, manganese, tungsten, molybdenum, platinum, aluminum, iron, steel, silicon, germanium, indium phosphide, gallium arsenide, silicon nitride, and oxides or alloys or Mixtures thereof, as well as indium tin oxide (ITO) and silicate or borate glasses.
• the substrate is particularly preferably gold-coated silicon, which still has a titanium primer between the silicon layer and the gold layer.
• the surface of the substrate is atomically flat and homogeneous, i. for example, that it has no step dislocations or defects. In this way it is possible to produce a membrane which is also homogeneous and defect-free.
• the substrate surface can be optionally modified beforehand.
• the modification may be, for example, a chemical modification and / or a purification include.
• the cleaning can be done by simply rinsing the surface with water or organic solvents such as ethanol, acetone or dimethylformamide or by treatment with an oxygen plasma generated by UV radiation. Particularly preferably, treatment with UV radiation first takes place, followed by rinsing with ethanol and subsequent drying in a nitrogen stream. If the monolayers with anchor groups such as phosphonic acid, carboxylic acid or hydroxamic acid groups are to be applied to oxidized metal surfaces, a prior controlled oxidation of the metal surface is advantageous.
• oxidizing agents such as hydrogen peroxide, Caro's acid or nitric acid.
• oxidizing agents such as hydrogen peroxide, Caro's acid or nitric acid.
• Another possibility for modifying a substrate surface is to apply a first organic monolayer with terminal reactive groups such as amino, hydroxyl, chlorine, bromine, carboxyl or isocyanate groups, to which in a second step the monolayer actually to be crosslinked by means of suitable chemically coupled to functional groups.
• a monolayer of low molecular weight aromatics is applied with bonding to at least one surface of the substrate.
• This binding may be by adsorption or by attachment via anchor groups.
• the monolayer is preferably applied to the surface of the substrate by covalent bonding via anchor groups.
• the application of the monolayer can be carried out, for example, by dipping, casting, spin-coating or by adsorption from solution. Such methods are known in the art.
• a monolayer of aromatics selected from the group consisting of phenyl, biphenyl, terphenyl, naphthalene, anthracene, bipyridine, terpyridine, thiophene, bithienyl, terthienyl, pyrrole and combinations thereof is applied.
• the aromatic is biphenyl, which is covalently bound to the substrate via a thiol group.
• step (c) of the method according to the invention the substrate obtained in step (b) is treated with high-energy radiation such that the low molecular weight aromatics monolayer is crosslinked in the lateral direction.
• the monolayer is crosslinked covalently in the lateral direction.
• the treatment is preferably carried out by electron radiation, plasma radiation, X-radiation, ⁇ radiation, ⁇ radiation, UV radiation or EUV radiation.
• a large area illuminating electron source for.
• the electron energies used can be adapted within a wide range, preferably 1 to 1000 eV, to the respective organic films and their substrates.
• electron beam radiation of 50 eV can be used to crosslink biphenyl-4-thiol to gold.
• step (b) instead of a monolayer of low molecular weight aromatics, for example, saturated molecules or units such as cyclohexyl, bicyclohexyl, tercyclohexyl, partially or fully hydrogenated naphthalenes or anthracenes or partially or completely hydrogenated heteroaromatics applied and covalently bonded by means of an anchor group on the substrate surface, so
• step (c) by means of treatment with high-energy radiation in step (c), in addition to cross-linking in the lateral direction, dehydrogenation to the corresponding aromatics or heteroaromatics can take place.
• step (d) of the method according to the invention the removal of the substrate is then carried out in order to obtain the membrane.
• This can be done, for example, by dissolving the substrate by etching away, or by chemically dissolving the bond between monolayer and substrate via the anchor group.
• Corresponding methods for removing the substrate from the Monolayer are known in the art. When using a thiol group as an anchor group, this can be done for example by treatment with iodine (see, for example, W. Eck et al., Adv., Mater. 2005, 17, 2583-2587).
• the molecular monolayer is then in the form of a membrane.
• At least partially low molecular weight aromatics having at least one functional group are used, whereby a membrane is obtained in which one of the two surfaces of the molecular monolayer is modified by functional groups.
• the term "aromatics which have at least one functional group” is understood as meaning those aromatics which have at least one functional group.
• the functional group may be any functional group which is not cleaved by the subsequent irradiation and which is suitable for further reaction, for example to attach further molecules to the monolayer.
• the functional groups are selected from amino groups, nitro groups, carboxy groups, cyano groups, thiol groups, hydroxy groups, and combinations thereof.
• Particularly preferred as a functional group is the nitro group.
• the nitro groups are converted to amino groups. It is believed that this reduction initially precedes C-H bond cleavage in the aromatics, and that the liberated hydrogen atoms subsequently reduce the nitro groups to amino groups.
• the functional groups are special ligands which are suitable for binding specific target molecules.
• These ligands may be bonded to the molecular monolayer by modification of the aforementioned amino groups, nitro groups, carboxy groups, cyano groups, thiol groups or hydroxy groups. This modification is preferably done after the crosslinking of the Moriotik and the perforation is done.
• ligands examples include ion exchangers, chelating agents, amino acids, coenzymes, cofactors and their analogs, endocrine and exocrine substances, such as hormones, enzyme substrates, enzyme inhibitors, nucleic acids, such as DNA and RNA, viruses, and polypeptides, such as proteins, in particular Antibodies and enzymes.
• ion exchangers such as EDTA, EDTA, EDTA, EDTA, TRF33, TRF33, TRF33, TRF33, TRF33, TRF33, TRF33, TRF33, TRF33, TRF33, TRF33, TRF33, TRF33, TRF33, TRF33, TRF33, TRF33, TRF33, TRF33, TRF33, TRF33, TRF33, TRF33, TRF33, TRF33, TRF33, TRF33, TRF33, TRF33, TRF33, TRF33, TRF33, TRF33, TRF33, T
• the low molecular weight aromatics have the functional group in a terminal position such that the functional groups are on their surface after formation of the monolayer.
• At least two perforated molecular monolayers are stacked to form a stack.
• Monolayers arranged one above the other more preferably 2 to 50, more preferably 2 to 10 monolayers are arranged one above the other.
• a membrane having a thickness in the range of 1 to 200 nm can be obtained.
• the method according to the invention further comprises the final step of applying an additional coating to the membrane.
• the coating may be, for example, a metal coating.
• the coating is a coating of gold.
• the coating may have any suitable thickness.
• the coating preferably has a thickness in the range from 1 nm to 10 nm, particularly preferably in the range from 2 nm to 5 nm Coating may be applied by methods known in the art, for example by vapor deposition.
• the membrane according to the present invention is mechanically more stable than conventional membranes.
• the present invention further relates to the use of the membrane according to the invention as a membrane filter or adsorption membrane for the separation of
• Wastewater analysis for the purification of drinking water or wastewater, in medicine, for example in dialysis, in batteries or in fuel cells.
• the present invention furthermore relates to the use of the membrane obtainable by the processes according to the invention as a membrane filter or adsorption membrane for the separation of mixtures of substances.
• a membrane filter or adsorption membrane for the separation of mixtures of substances.
• Particularly preferred is the use in the filtration or separation of gases and liquids.
• Particularly preferred is the use in food, drinking water or wastewater analysis, for the purification of drinking water or wastewater, in medicine, for example in dialysis, in batteries or in fuel cells.
• the membrane according to the invention is used in sensor technology.
• the membrane obtainable by the processes according to the invention is used in sensor technology.
• the present invention will be further elucidated by the following non-limiting example.
• Example 1 Example 1 :
• a nitrobiphenylthiol monolayer was crosslinked by means of EUV-IL.
• circular openings were formed with diameters in the range of 300 nm to 30 nm, wherein the distances between the individual openings were 300 nm to 100 nm.
• the size and positions of the openings were determined by transmission electron microscopy.
• the obtained nanomembranes were coated with a gold film having a thickness in the range of 2 nm to 5 nm.

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