EP2726204A2 - Production of a catalytically active, metalized reactive foam material and use thereof - Google Patents

Production of a catalytically active, metalized reactive foam material and use thereof

Info

Publication number
EP2726204A2
EP2726204A2 EP12729903.0A EP12729903A EP2726204A2 EP 2726204 A2 EP2726204 A2 EP 2726204A2 EP 12729903 A EP12729903 A EP 12729903A EP 2726204 A2 EP2726204 A2 EP 2726204A2
Authority
EP
European Patent Office
Prior art keywords
metal
layer
ventilation device
foam
optofluidic
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Withdrawn
Application number
EP12729903.0A
Other languages
German (de)
French (fr)
Inventor
Wolfgang Kollmann
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Publication of EP2726204A2 publication Critical patent/EP2726204A2/en
Withdrawn legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25DPROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D5/00Electroplating characterised by the process; Pretreatment or after-treatment of workpieces
    • C25D5/627Electroplating characterised by the visual appearance of the layers, e.g. colour, brightness or mat appearance
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61LMETHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
    • A61L2/00Methods or apparatus for disinfecting or sterilising materials or objects other than foodstuffs or contact lenses; Accessories therefor
    • A61L2/02Methods or apparatus for disinfecting or sterilising materials or objects other than foodstuffs or contact lenses; Accessories therefor using physical phenomena
    • A61L2/08Radiation
    • A61L2/088Radiation using a photocatalyst or photosensitiser
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61LMETHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
    • A61L9/00Disinfection, sterilisation or deodorisation of air
    • A61L9/16Disinfection, sterilisation or deodorisation of air using physical phenomena
    • A61L9/18Radiation
    • A61L9/20Ultraviolet radiation
    • A61L9/205Ultraviolet radiation using a photocatalyst or photosensitiser
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J21/00Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
    • B01J21/06Silicon, titanium, zirconium or hafnium; Oxides or hydroxides thereof
    • B01J21/063Titanium; Oxides or hydroxides thereof
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/38Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/70Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/70Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
    • B01J23/72Copper
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/70Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
    • B01J23/89Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with noble metals
    • B01J23/8926Copper and noble metals
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/70Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
    • B01J23/89Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with noble metals
    • B01J23/8933Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with noble metals also combined with metals, or metal oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
    • B01J23/8993Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with noble metals also combined with metals, or metal oxides or hydroxides provided for in groups B01J23/02 - B01J23/36 with chromium, molybdenum or tungsten
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J27/00Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
    • B01J27/14Phosphorus; Compounds thereof
    • B01J27/185Phosphorus; Compounds thereof with iron group metals or platinum group metals
    • B01J27/1853Phosphorus; Compounds thereof with iron group metals or platinum group metals with iron, cobalt or nickel
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J31/00Catalysts comprising hydrides, coordination complexes or organic compounds
    • B01J31/02Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides
    • B01J31/06Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides containing polymers
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J31/00Catalysts comprising hydrides, coordination complexes or organic compounds
    • B01J31/26Catalysts comprising hydrides, coordination complexes or organic compounds containing in addition, inorganic metal compounds not provided for in groups B01J31/02 - B01J31/24
    • B01J31/38Catalysts comprising hydrides, coordination complexes or organic compounds containing in addition, inorganic metal compounds not provided for in groups B01J31/02 - B01J31/24 of titanium, zirconium or hafnium
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J35/00Catalysts, in general, characterised by their form or physical properties
    • B01J35/30Catalysts, in general, characterised by their form or physical properties characterised by their physical properties
    • B01J35/39Photocatalytic properties
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J37/00Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/02Impregnation, coating or precipitation
    • B01J37/024Multiple impregnation or coating
    • B01J37/0244Coatings comprising several layers
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J37/00Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/02Impregnation, coating or precipitation
    • B01J37/03Precipitation; Co-precipitation
    • B01J37/036Precipitation; Co-precipitation to form a gel or a cogel
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J37/00Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/34Irradiation by, or application of, electric, magnetic or wave energy, e.g. ultrasonic waves ; Ionic sputtering; Flame or plasma spraying; Particle radiation
    • B01J37/348Electrochemical processes, e.g. electrochemical deposition or anodisation
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B15/00Layered products comprising a layer of metal
    • B32B15/04Layered products comprising a layer of metal comprising metal as the main or only constituent of a layer, which is next to another layer of the same or of a different material
    • B32B15/046Layered products comprising a layer of metal comprising metal as the main or only constituent of a layer, which is next to another layer of the same or of a different material of foam
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/30Treatment of water, waste water, or sewage by irradiation
    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23CCOATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C18/00Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating
    • C23C18/02Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating by thermal decomposition
    • C23C18/12Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating by thermal decomposition characterised by the deposition of inorganic material other than metallic material
    • C23C18/1204Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating by thermal decomposition characterised by the deposition of inorganic material other than metallic material inorganic material, e.g. non-oxide and non-metallic such as sulfides, nitrides based compounds
    • C23C18/1208Oxides, e.g. ceramics
    • C23C18/1216Metal oxides
    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23CCOATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C18/00Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating
    • C23C18/02Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating by thermal decomposition
    • C23C18/12Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating by thermal decomposition characterised by the deposition of inorganic material other than metallic material
    • C23C18/1229Composition of the substrate
    • C23C18/1241Metallic substrates
    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23CCOATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C18/00Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating
    • C23C18/02Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating by thermal decomposition
    • C23C18/12Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating by thermal decomposition characterised by the deposition of inorganic material other than metallic material
    • C23C18/125Process of deposition of the inorganic material
    • C23C18/1254Sol or sol-gel processing
    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23CCOATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C28/00Coating for obtaining at least two superposed coatings either by methods not provided for in a single one of groups C23C2/00 - C23C26/00 or by combinations of methods provided for in subclasses C23C and C25C or C25D
    • C23C28/30Coatings combining at least one metallic layer and at least one inorganic non-metallic layer
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25DPROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D5/00Electroplating characterised by the process; Pretreatment or after-treatment of workpieces
    • C25D5/10Electroplating with more than one layer of the same or of different metals
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25DPROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D5/00Electroplating characterised by the process; Pretreatment or after-treatment of workpieces
    • C25D5/10Electroplating with more than one layer of the same or of different metals
    • C25D5/12Electroplating with more than one layer of the same or of different metals at least one layer being of nickel or chromium
    • EFIXED CONSTRUCTIONS
    • E04BUILDING
    • E04CSTRUCTURAL ELEMENTS; BUILDING MATERIALS
    • E04C2/00Building elements of relatively thin form for the construction of parts of buildings, e.g. sheet materials, slabs, or panels
    • E04C2/02Building elements of relatively thin form for the construction of parts of buildings, e.g. sheet materials, slabs, or panels characterised by specified materials
    • E04C2/26Building elements of relatively thin form for the construction of parts of buildings, e.g. sheet materials, slabs, or panels characterised by specified materials composed of materials covered by two or more of groups E04C2/04, E04C2/08, E04C2/10 or of materials covered by one of these groups with a material not specified in one of the groups
    • E04C2/284Building elements of relatively thin form for the construction of parts of buildings, e.g. sheet materials, slabs, or panels characterised by specified materials composed of materials covered by two or more of groups E04C2/04, E04C2/08, E04C2/10 or of materials covered by one of these groups with a material not specified in one of the groups at least one of the materials being insulating
    • E04C2/292Building elements of relatively thin form for the construction of parts of buildings, e.g. sheet materials, slabs, or panels characterised by specified materials composed of materials covered by two or more of groups E04C2/04, E04C2/08, E04C2/10 or of materials covered by one of these groups with a material not specified in one of the groups at least one of the materials being insulating composed of insulating material and sheet metal
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61LMETHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
    • A61L2209/00Aspects relating to disinfection, sterilisation or deodorisation of air
    • A61L2209/10Apparatus features
    • A61L2209/14Filtering means
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/70Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
    • B01J23/76Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
    • B01J23/835Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36 with germanium, tin or lead
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J27/00Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
    • B01J27/14Phosphorus; Compounds thereof
    • B01J27/186Phosphorus; Compounds thereof with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
    • B01J27/188Phosphorus; Compounds thereof with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium with chromium, molybdenum, tungsten or polonium
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J37/00Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/02Impregnation, coating or precipitation
    • B01J37/0215Coating
    • B01J37/0225Coating of metal substrates
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J37/00Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/02Impregnation, coating or precipitation
    • B01J37/0238Impregnation, coating or precipitation via the gaseous phase-sublimation
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2303/00Specific treatment goals
    • C02F2303/04Disinfection
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2305/00Use of specific compounds during water treatment
    • C02F2305/10Photocatalysts

Definitions

  • the invention relates to an optofluidic reactor and thus a catalytic material for the elimination of bacteria, viruses or particulate matter and fungal spores and other pollutants.
  • photocatalytic substrates as opto-fluidic reactors.
  • a substrate is, for example, titanium dioxide (TiO 2 ) - preferably in the tetragonal, crystalline form of anatase.
  • TiO 2 titanium dioxide
  • the latter releases electrons when exposed to sunlight, breaking up contaminants or other pollutants into harmless substances.
  • the release of electrons from the oxide and the associated photocatalytic reaction is composed of a series of physical and chemical processes.
  • oxygen radicals are formed on the surface of the oxide by the free electrons, which are also referred to as active oxygen.
  • oxygen radicals include free radicals, such as the hyperoxide anion, the hydroxyl radical, the peroxyl radical or alkoxyl radical, and also stable molecular radicals, such as the known oxygen peroxide, hydroperoxide, ozone, or the hypochlorite anion.
  • These oxygen radicals decompose molecules and organic contaminants when they come in contact with the surface of the oxide.
  • the activated oxygen also builds odors and air pollutants, such. As nitrogen oxides, and organic particulate matter effectively. Furthermore, this oxygen kills bacteria and viruses - even aggressive pathogens such as SARS and H5N1 are effectively combated on contact with the oxide surface.
  • the object of the present invention is in particular to provide an Optofluidrik reactor, which shows a high efficiency.
  • this object is achieved by the provision of a coating in which a metal matrix with a catalytically active metal or metal oxide is formed on a surface.
  • a reticulated plastic foam of, for example, polyethersulfone (PES) or polypropylene (PP) or polyethylene (PE) or polyurethane (PU) or polyester or polyether is provided, which is reticulated as a base foam.
  • PES polyethersulfone
  • PP polypropylene
  • PE polyethylene
  • PU polyurethane
  • the thin intermediate walls between the individual foam cells are partially broken in such a way that the foam becomes fluid-permeable.
  • foam has an enormously large surface, which is contacted by the latter as it flows through a fluid.
  • the fluid may be air to be purified or water to be purified.
  • the optofluidic reactor is preferably used for room air or water treatment.
  • the optofluidic reactor can be embedded for its protection between UV-transparent layers, such as glass. This is then used in the flow gradient of a watercourse to be cleaned.
  • a prefilter for filtering coarse suspended matter may be upstream.
  • Such a reticulated foam suitable for the fluid flow advantageously has a pore number of up to 34 ppi (pores per inch).
  • the average number of pores is 9 ppi (fluctuation range of 8 to 10 ppi) or 10.5 ppi on average (fluctuation range of 8 to 13 ppi) or 14.5 ppi on average (fluctuation range of 12 to 17 ppi). or on average 19.5 ppi (range of variation from 16 to 23 ppi) or on average 25.5 (range of variation from 12 to 29 ppi) or on average 30.5 (range of variation from 27 to 34 ppi).
  • the reticulated base foam is then coated in a further process step with at least one first metal or metal alloy layer.
  • the foam undergoes solidification, so that the resulting solid composite z. B. in sheet form as a ceiling element in rooms or as partitions can be used herein.
  • This metal coating also embrittlement of the base material, ie the foam is prevented by light.
  • a coated foam by the appropriate choice of a metal or a metal alloy fulfills decorative claims.
  • the layer thickness of the metal is chosen so that the coated foam material acquires an Eigentragschreib. Also, this can cause sagging or sagging of the Composite material in that it is designed as a plate can be prevented. By choosing the layer thickness of the metal, the material is well controllable in terms of its strength.
  • a suitable layer thickness has at least one (number word) micrometer. While metal foaming by thin foaming ensures good results for thin foam boards, wet-chemical coating processes are advantageous for thicker foam boards because they allow the thicker foam to be well coated down to its center.
  • coating metals all physically, thermally or wet-chemically depositable metals or metal alloys are suitable.
  • the metallically coated foam composite material is now an ideal support for the catalytically active layer to be subsequently applied, ie the photocatalytic substrate.
  • a noble metal layer of silver, palladium or platinum or of alloys and compositions thereof is also suitable as the photocatalytic substrate.
  • an optofluidic reactor which, thanks to its strength, can be easily cleaned with water or the like by the at least one first metal layer without losing its effect.
  • the above combination according to the invention of photocatalysis and fluid flow show a tremendous improvement in the efficiency of the photocatalyst.
  • the channels produced in the foam, which branch out like branches in the foam, provide a high surface area to fluid volume ratio, thus achieving better purification of the optofluidic reactor of the present invention.
  • a preferred exemplary embodiment is described below:
  • a reticulated plastic foam having a preferred pore number of 12-17 ppi and a thickness of 10 mm is coated in a first coating step with a copper layer which is a few nanometers to one (1 ⁇ m) or several micrometers thick. which is applied by vapor deposition, sputtering or by electroplating on the foam.
  • This first metal layer is then reinforced by a further layer by means of metallization by galvanic means with copper, iron or aluminum with a layer thickness of more than 20 ⁇ .
  • a nickel, white bronze or cobalt-tin layer which can be combined with an anti-allergenic cobalt-tin metal layer is applied galvanically to this copper layer.
  • this layer or layer combination can also be a noble metal layer of z.
  • palladium platinum or silver or alloys thereof - including as an alloy with one of the above metals nickel, zinc, white bronze, cobalt or tin.
  • Layer thicknesses of at least 5 ⁇ m were found to be advantageous.
  • the metallized material obtained by the coating is subsequently coated with a titanium dioxide layer as a photocatalytic substrate by dipping or flooding the foam or spraying it on.
  • the coating is a sol or gel-based water or solvent based titanium dioxide solution. In addition to its photocatalytic action, this coating is also superhydrophilic, self-cleaning and highly antimicrobial.
  • interior ceiling panels or room divider can be made, which clean the room air.
  • design elements are advantageous, which can be set up indoors to clean the room air. In this case, the most varied forms of the material can be formed. In such embodiments, in addition to the air cleaning effect and the sound attenuation is remarkable.
  • the interior elements can be useful also used in open-plan offices for noise reduction.
  • the individual opto-fluidics elements for example plates
  • the individual opto-fluidics elements can be connected to one another, for example adhesively bonded. It should be ensured that sufficient UV light can penetrate into the center of the elements connected in this way and a flow is ensured.
  • a reactor made of elements between which a UV lamp is embedded proves to be advantageous. This radiates from the center of the reactor UV light to the outside. In addition to the emitted UV light, the integrated lamp can also emit light in the visible range, so that such a reactor then also serves as a luminaire. Such a connected lamp also leads by the resulting convection of the lamp by the resulting heat for forced flow through the Optofluidik reactor.
  • Also according to the invention comprises a ventilation device that has as an essential functional element an opto-fluidic reactor, as described above.
  • a ventilation device has a fan or the like to forcibly flow through the optofluidic reactor with air. This forced flow of the photocatalytic reactor increases the cleaning effect of the air many times.
  • the foam material according to the invention can be easily replaced as optofluidic reactor in such a ventilation device, d. H. dismantle, and also clean.
  • the optofluidic reactor according to the invention can also be used as a filter body for air suction hoods. These are in the art for kitchens, or for sucking vapors z. As solvents, welding fumes, or flue gases used.
  • the photocatalytic effect of the optofluidic reactor can be advantageously increased as already shown above, when it is irradiated with a UV-A lamp.
  • the attached Figures 1 and 2 are photographs of a reticulated base foam, as it can be used as starting material for the Optofluidik reactor.
  • FIG. 2 is an enlarged view of the foam of FIG. 1.
  • a new coating for the purpose of decontamination of bacteria, viruses and other general impurities is shown below.
  • additional coating applications without fluid flooding such as for door handles, sanitary fittings, or for all surfaces that touch experienced and thus exposed to contamination with bacteria and viruses. This concerns applications in the home, hospitals or public institutions.
  • the preferred particle size of the Ti0 2 is 0-3 ⁇ ; eg KRONOClean 7000 and KRONOClean 7050 It is also possible to use nanoscale TiO 2 particles with a size of about 20 nm, whereby the preparation of the suspension may be complicated due to conglomeration problems, but is feasible. For nanoscale particles, it helps to use dispersant chemicals.
  • the reticulated foam is coated in a first coating step with preferably a copper layer> 1 ⁇ by vapor deposition or by electroless process (chemical copper). 2.
  • This first metal layer is galvanically coated with copper, iron, or aluminum (preferably Cu) with a layer thickness of more than 10 ⁇ until the foam acquires its own rigidity.
  • NiP-Ti0 2 layer with a layer thickness> 1 ⁇ m is applied to this layer
  • a layer to the photocatalytic layer 4 e.g. Bright chrome, or a noble metal e.g. Au, Pd, Rt or Pt.
  • step 1 is omitted
  • Cationic Fluorosurfactant 0.2 g / 1 FT 248 (BASF)
  • BASF a rate of incorporation of up to 50% by weight is possible.
  • a wetting agent such as sodium dodecyl sulfate or standard wetting agents from galvanic chemicals supply companies to prevent pore formation.
  • the Ti0 2 particles are held in suspension by an electrolyte movement by means of mechanical stirring. A gentle air injection is advantageous.
  • Ti0 2 concentration depends on the desired incorporation rate of the oxide and the component geometry, as well as in general of the component (surface roughness, microgeometry, etc.).
  • the TiO 2 - metal matrix deposition is possible with a wide variety of electrolytes as matrix metal.
  • the matrix metals used as electroplated (by current) which are used are NiP, Ni, Co, Cu, W, Mn, Mo, Cr, Sn, Zn, (hard chromium), noble metals such as Pd, Pt, ruthenium, rhodium, and the like Alloys suitable.
  • sulfamate electrolytes or ionic liquids can be used.
  • the matrix metal is used with electroless processes such as chemical nickel-phosphorus and a variety of alloys, e.g. Ni-Co-P (hydrazine reducing agent), Co-P, Ni-Cu-P, Ni-W-P, Ni-Mo-P, and chemically copper.
  • Ni-Co-P hydrogen reducing agent
  • Co-P nickel-Cu-P
  • Ni-W-P nickel-W-P
  • Ni-Mo-P nickel-phosphorus
  • chemically copper such as chemical nickel-phosphorus and a variety of alloys, e.g. Ni-Co-P (hydrazine reducing agent), Co-P, Ni-Cu-P, Ni-W-P, Ni-Mo-P, and chemically copper.
  • Ti0 2 - intercalation layers The big advantage of these Ti0 2 - intercalation layers is that the catalytically active particles are fixed firmly in a very abrasion-resistant metal matrix and consequently a very long duration of action is to be expected.
  • TiO 2 particles are always exposed on the surface at any time, even with incoming wear of the coating, and thus continue to work until complete wear of the coating occurs.
  • these coatings of a metal matrix last incomparably longer and thus make them predestined for abrasion-stressed components and surfaces which are often damaged by, for example, , B. be claimed and contaminated, for example, especially in hospitals with different bacteria and viruses.
  • Ti0 2 metal matrix layers produced in this way have the great advantage that in combination with light, they continuously reduce viruses and bacteria in door clinics, gripping surfaces, etc., and thus ensure maximum safety against contagion and transmission of diseases through contact contamination outside of cleaning cycles ,

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Health & Medical Sciences (AREA)
  • Physics & Mathematics (AREA)
  • Electrochemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Mechanical Engineering (AREA)
  • General Chemical & Material Sciences (AREA)
  • Thermal Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Dispersion Chemistry (AREA)
  • Epidemiology (AREA)
  • Veterinary Medicine (AREA)
  • Public Health (AREA)
  • General Health & Medical Sciences (AREA)
  • Animal Behavior & Ethology (AREA)
  • Toxicology (AREA)
  • Plasma & Fusion (AREA)
  • Architecture (AREA)
  • Ceramic Engineering (AREA)
  • Structural Engineering (AREA)
  • Civil Engineering (AREA)
  • Hydrology & Water Resources (AREA)
  • Water Supply & Treatment (AREA)
  • Environmental & Geological Engineering (AREA)
  • Catalysts (AREA)
  • Treatment Of Water By Oxidation Or Reduction (AREA)
  • Physical Water Treatments (AREA)
  • Apparatus For Disinfection Or Sterilisation (AREA)
  • Disinfection, Sterilisation Or Deodorisation Of Air (AREA)
  • Exhaust Gas Treatment By Means Of Catalyst (AREA)

Abstract

The invention relates to a catalytic material which is used as an optofluidic reactor, and also a method for production thereof. In this case, first a reticulated plastic foam can be fabricated which then is coated with at least one first metal or metal alloy layer. Subsequently, a photocatalytic substrate is then applied to the metal or metal alloy layer. The photocatalytic substrate eliminates bacteria, viruses and other harmful substances, as well as fine dust or fungal spores, when the optofluidic reactor is used.

Description

OPTOFLUIDIK-RE AKTOR  OPTOFLUIDIK-RE ACTOR
Die Erfindung betrifft einen Optofluidik-Reaktor und damit einen kataly- tischen Werkstoff zur Eliminierung von Bakterien, Viren oder Feinstaub und Pilzsporen und anderen Schadstoffen. The invention relates to an optofluidic reactor and thus a catalytic material for the elimination of bacteria, viruses or particulate matter and fungal spores and other pollutants.
Im Stand der Technik ist es bekannt, fotokatalytische Substrate als opto- fluidische Reaktoren einzusetzen. Ein solches Substrat ist beispielsweise Titandioxid (TiO2) - bevorzugt in der tetragonalen, kristallinen Form von Anatas. Letzteres setzt bei Sonnenlichtbestrahlung Elektronen frei, die Verschmutzungen oder andere Schadstoffe in harmlose Substanzen aufbrechen. Die Freisetzung an Elektronen des Oxids und die damit einhergehende fotokatalytische Reaktion setzt sich aus einer Reihe von physikalischen und chemischen Prozessen zusammen. Im Wesentlichen werden an der Oberfläche des Oxids durch die freien Elektronen Sauerstoffradikale gebildet, die auch als Aktivsauerstoff bezeichnet werden. Zu diesen Sauerstoffradikalen gehören freie Radikale, wie beispielsweise das Hyperoxid- Anion, das Hydroxyl-Radikal, das Peroxyl-Radikal oder Alkoxyl-Radikal und auch stabile molekulare Radikale, wie das bekannte Sauerstoffperoxid, dass Hydroperoxid, Ozon, oder das Hypochlorid-Anion. Diese Sauerstoffradikale zersetzen Moleküle und organische Schmutzpartikel, wenn sie mit der Oberfläche des Oxids in Berührung kommen. Der aktivierte Sauerstoff baut auch Geruchsstoffe und Luftschadstoffe, wie z. B. Stickoxide, und organischen Feinstaub wirksam ab. Ferner tötet dieser Sauerstoff Bakterien und Viren - sogar aggressive Erreger wie SARS und H5N1 werden bei Kontakt mit der Oxidoberfläche wirkungsvoll bekämpft. In the prior art, it is known to use photocatalytic substrates as opto-fluidic reactors. Such a substrate is, for example, titanium dioxide (TiO 2 ) - preferably in the tetragonal, crystalline form of anatase. The latter releases electrons when exposed to sunlight, breaking up contaminants or other pollutants into harmless substances. The release of electrons from the oxide and the associated photocatalytic reaction is composed of a series of physical and chemical processes. Essentially, oxygen radicals are formed on the surface of the oxide by the free electrons, which are also referred to as active oxygen. These oxygen radicals include free radicals, such as the hyperoxide anion, the hydroxyl radical, the peroxyl radical or alkoxyl radical, and also stable molecular radicals, such as the known oxygen peroxide, hydroperoxide, ozone, or the hypochlorite anion. These oxygen radicals decompose molecules and organic contaminants when they come in contact with the surface of the oxide. The activated oxygen also builds odors and air pollutants, such. As nitrogen oxides, and organic particulate matter effectively. Furthermore, this oxygen kills bacteria and viruses - even aggressive pathogens such as SARS and H5N1 are effectively combated on contact with the oxide surface.
Die Aufgabe der vorliegenden Erfindung liegt insbesondere darin, einen Optofluidrik-Reaktor bereitzustellen, der einen hohen Wirkungsgrad aufzeigt. The object of the present invention is in particular to provide an Optofluidrik reactor, which shows a high efficiency.
Diese Aufgabe wird This task will
a) zum Einen gelöst durch die Herstellung eines katalytischen Werkstoffs, in dem die Fotokatalyse und eine Fluid-Durchströmung kombi- niert sind.  a) solved by the production of a catalytic material in which the photocatalysis and a fluid flow are combined.
b) Zum Anderen wird diese Aufgabe gelöst durch das Vorsehen einer Beschichtung, bei der eine Metallmatrix mit einem katalytisch wirkenden Metall oder Metalloxid auf einer Oberfläche ausgebildet wird. Diese beiden Aspekte können dabei vorteilhaft miteinander kombiniert sein.  b) On the other hand, this object is achieved by the provision of a coating in which a metal matrix with a catalytically active metal or metal oxide is formed on a surface. These two aspects can be advantageously combined with each other.
Zu a) Zum Zwecke einer Fluiddurchströmung wird ein retikulierter Kunststoff-Schaum aus beispielsweise Polyethersulfon (PES) oder Polypropylen (PP) oder Polyethylen (PE) oder Polyurethan (PU) oder Polyester oder Polyether geschaffen, der als Basisschaum retikuliert wird.To a) For the purpose of fluid flow, a reticulated plastic foam of, for example, polyethersulfone (PES) or polypropylene (PP) or polyethylene (PE) or polyurethane (PU) or polyester or polyether is provided, which is reticulated as a base foam.
Beim Retikulieren werden die dünnen Zwischenwände zwischen den einzelnen Schaum-Zellen derart teilweise aufgebrochen, dass der Schaum fluiddurchlässig wird. Ein solcher Schaum weist eine enorm große Oberfläche auf, die beim Durchströmen eines Fluids von letzterem kontaktiert wird. Das Fluid kann zu reinigende Luft sein oder auch zu reinigendes Wasser. Insofern findet der Optofluidik-Reaktor bevorzugt einen Einsatz zur Raumluft- oder Wasseraufbereitung. Zur Wasseraufbereitung kann der Optofluidik-Reaktor zu seinem Schutz zwischen UV-Lichtdurchlässigen Schichten, wie beispielsweise Glas eingebettet sein. Dieser wird dann im Strömungsgefälle eines zu reinigenden Wasserlaufes eingesetzt. Ein Vorfilter zum Filtern von groben Schwebstoffen kann vorgeschaltet sein. During reticulation, the thin intermediate walls between the individual foam cells are partially broken in such a way that the foam becomes fluid-permeable. Such a foam has an enormously large surface, which is contacted by the latter as it flows through a fluid. The fluid may be air to be purified or water to be purified. In this respect, the optofluidic reactor is preferably used for room air or water treatment. For water treatment, the optofluidic reactor can be embedded for its protection between UV-transparent layers, such as glass. This is then used in the flow gradient of a watercourse to be cleaned. A prefilter for filtering coarse suspended matter may be upstream.
Vorteilhaft weist ein solcher für die Fluid-Durchströmung geeigneter retikulierter Schaum eine Porenanzahl von bis zu 34 ppi (pores per inch) auf. Als Beispiel beträgt die Porenanzahl im Mittel 9 ppi auf (Schwankungsbreite von 8 bis 10 ppi) oder von im Mittel 10,5 ppi (Schwankungsbreite von 8 bis 13 ppi) oder von im Mittel 14,5 ppi (Schwankungsbreite von 12 bis 17 ppi) oder von im Mittel 19,5 ppi (Schwankungsbreite von 16 bis 23 ppi) oder von im Mittel 25,5 (Schwankungsbreite von 12 bis 29 ppi) oder von im Mittel 30,5 (Schwankungsbreite von 27 bis 34 ppi). Such a reticulated foam suitable for the fluid flow advantageously has a pore number of up to 34 ppi (pores per inch). As an example, the average number of pores is 9 ppi (fluctuation range of 8 to 10 ppi) or 10.5 ppi on average (fluctuation range of 8 to 13 ppi) or 14.5 ppi on average (fluctuation range of 12 to 17 ppi). or on average 19.5 ppi (range of variation from 16 to 23 ppi) or on average 25.5 (range of variation from 12 to 29 ppi) or on average 30.5 (range of variation from 27 to 34 ppi).
Der retikulierte Basisschaum wird sodann in einem weiteren Verfahrensschritt mit mindestens einer ersten Metall- oder Metalllegierungsschicht beschichtet. Hierdurch erfährt der Schaum eine Verfestigung, so dass der daraus resultierende feste Verbundwerkstoff z. B. in Plattenform als Deckenelement in Räumen oder als Trennwände hierin eingesetzt werden kann. Durch diese Metallbeschichtung wird auch eine Versprödung des Basiswerkstoffes, d.h. des Schaums durch Licht verhindert. Ferner erfüllt ein derart beschichteter Schaum durch die geeignete Wahl eines Metalls oder einer Metalllegierung dekorative Ansprüche. Die Schichtdicke des Metalls ist dabei so gewählt, dass der beschichtete Schaumwerkstoff eine Eigentragfähigkeit erlangt. Auch kann dadurch ein Durchhängen oder Durchbiegen des Verbundwerkstoffes insofern er als Platte ausgebildet ist, verhindert werden. Durch die Wahl der Schichtdicke des Metalls ist der Werkstoff hinsichtlich seiner Festigkeit gut steuerbar. Auch können mehrere Metall-Schichten nacheinander aufgetragen werden. Eine geeignete Schichtdicke hat mindes- tens einen (Zahlwort) Mikrometer. Während bei dünnen Schaumplatten eine Metallbeschichtung mittels Bedampfens gute Ergebnisse gewährleistet, sind nasschemische Beschichtungsverfahren bei dickeren Schaumplatten von Vorteil, weil damit der dickere Schaum bis in sein Zentrum hinein gut beschichtet werden kann. The reticulated base foam is then coated in a further process step with at least one first metal or metal alloy layer. As a result, the foam undergoes solidification, so that the resulting solid composite z. B. in sheet form as a ceiling element in rooms or as partitions can be used herein. This metal coating also embrittlement of the base material, ie the foam is prevented by light. Furthermore, such a coated foam by the appropriate choice of a metal or a metal alloy fulfills decorative claims. The layer thickness of the metal is chosen so that the coated foam material acquires an Eigentragfähigkeit. Also, this can cause sagging or sagging of the Composite material in that it is designed as a plate can be prevented. By choosing the layer thickness of the metal, the material is well controllable in terms of its strength. Also, several metal layers can be applied one after the other. A suitable layer thickness has at least one (number word) micrometer. While metal foaming by thin foaming ensures good results for thin foam boards, wet-chemical coating processes are advantageous for thicker foam boards because they allow the thicker foam to be well coated down to its center.
Als Beschichtungsmetalle sind alle physikalisch, thermisch oder nasschemisch abscheidbaren Metalle oder Metalllegierungen geeignet. As coating metals, all physically, thermally or wet-chemically depositable metals or metal alloys are suitable.
Der metallisch beschichtete Schaum- Verbundwerkstoff ist nun ein idealer Träger der nachfolgend zu applizierenden kataly tisch wirksamen Schicht, d.h. des fotokatalytischen Substrats. Als geeignetes fotokatalytisches Substrat wird Titandioxid (Ti02) - bevorzugt in der tetragonalen, kristallinen Form von Anatas - herangezogen oder eine Metallschicht aus Kupfer, Nickel, Zink, Zinn, Kobalt oder Mangan, bzw. Legierungen oder Oxide, auch in Gemischen der einzelnen Oxide, hieraus. Als fotokatalytisches Substrat eignet sich auch eine Edelmetallschicht aus Silber, Palladium oder Platin oder aus Legierungen und Zusammensetzungen hieraus. The metallically coated foam composite material is now an ideal support for the catalytically active layer to be subsequently applied, ie the photocatalytic substrate. Titanium dioxide (TiO 2 ) - preferably in the tetragonal, crystalline form of anatase - or a metal layer of copper, nickel, zinc, tin, cobalt or manganese, or alloys or oxides, also in mixtures of the individual oxides, is used as a suitable photocatalytic substrate , from this. Also suitable as the photocatalytic substrate is a noble metal layer of silver, palladium or platinum or of alloys and compositions thereof.
Sodann ist ein Optofluidik-Reaktor geschaffen, der Dank seiner Festigkeit durch die mindestens eine erste Metallschicht leicht mit Wasser oder ähnlichem gereinigt werden kann, ohne seine Wirkung zu verlieren. Obige erfindungsgemäße Kombination aus Fotokatalyse und Fluid-Durch- strömung zeigen eine enorme Verbesserung der Effizienz des Fotokatalysators. Die in dem Schaum produzierten Kanäle, die sich wie Äste in dem Schaum verzweigen, sorgen für ein hohes Verhältnis von Oberfläche zu Fluid- Volumen, womit der erfindungsgemäße Optofluidik-Reaktor eine bessere Aufreinigung erzielt. Then, an optofluidic reactor is provided which, thanks to its strength, can be easily cleaned with water or the like by the at least one first metal layer without losing its effect. The above combination according to the invention of photocatalysis and fluid flow show a tremendous improvement in the efficiency of the photocatalyst. The channels produced in the foam, which branch out like branches in the foam, provide a high surface area to fluid volume ratio, thus achieving better purification of the optofluidic reactor of the present invention.
Im Folgenden wird ein bevorzugtes Ausführungsbeispiel beschrieben: Ein retikulierter Kunststoff-Schaum mit einer bevorzugten Porenanzahl von 12 - 17 ppi und einer Dicke von 10 mm wird in einem ersten Beschichtungsschritt mit einer wenige Nanometer bis ein (1 pm) oder mehreren Mikrometern dicken Kupferschicht beschichtet, die durch Aufdampfen, Sputtern oder auf galvanischem Weg auf den Schaum aufgetragen wird. Diese erste Metallschicht wird dann durch eine weitere Schicht mittels Metallisierung auf galvanischem Wege mit Kupfer, Eisen oder Aluminium mit einer Schichtdicke von mehr als 20 μιη verstärkt. Auf diese Kupferschicht wird als Korrosionsschutz eine Nickel, Weißbronze- oder Kobalt-Zinn-Schicht galvanisch aufgebracht, die mit einer antiallergenen Kobalt-Zinn-Metallschicht kombiniert sein kann. Anstelle dieser Schicht oder Schichtkombination kann auch eine Edelmetallschicht von z. B. Palladium, Platin oder Silber oder aus Legierungen hieraus aufgebracht sein - auch als Legierung mit einem der oben genannten Metalle Nickel, Zink, Weißbronze, Kobalt oder Zinn. Als vorteilhaft zeigten sich Schichtdicken von mindestens 5 μιη. Der durch die Beschichtung erhaltene metallisierte Werkstoff wird im Anschluss mit einer Titandioxid-Schicht als fotokatalytisches Substrat durch Tauchen oder Fluten des Schaums oder Aufsprühen auf diesen beschichtet. Die Beschichtung ist eine im Sol-Gel-Verfahren hergestellte Wasser- oder Lösungsmittel-basierte Titandioxid-Lösung. Diese Beschichtung ist zusätzlich zu ihrer fotokatalytischen Wirkung auch superhydrophil, selbstreinigend und stark antimikrobiell. A preferred exemplary embodiment is described below: A reticulated plastic foam having a preferred pore number of 12-17 ppi and a thickness of 10 mm is coated in a first coating step with a copper layer which is a few nanometers to one (1 μm) or several micrometers thick. which is applied by vapor deposition, sputtering or by electroplating on the foam. This first metal layer is then reinforced by a further layer by means of metallization by galvanic means with copper, iron or aluminum with a layer thickness of more than 20 μιη. As corrosion protection, a nickel, white bronze or cobalt-tin layer which can be combined with an anti-allergenic cobalt-tin metal layer is applied galvanically to this copper layer. Instead of this layer or layer combination can also be a noble metal layer of z. As palladium, platinum or silver or alloys thereof - including as an alloy with one of the above metals nickel, zinc, white bronze, cobalt or tin. Layer thicknesses of at least 5 μm were found to be advantageous. The metallized material obtained by the coating is subsequently coated with a titanium dioxide layer as a photocatalytic substrate by dipping or flooding the foam or spraying it on. The coating is a sol or gel-based water or solvent based titanium dioxide solution. In addition to its photocatalytic action, this coating is also superhydrophilic, self-cleaning and highly antimicrobial.
Aus einem Formkörper, der aus einem Werkstoff gemäß obiger Beschreibung gewonnen wird, lassen sich Innenraum-Deckenplatten oder Raumteiler fertigen, die so die Raumluft reinigen. Auch sind Designelemente vorteilhaft, die man in Innenräumen aufstellen kann, um die Raumluft zu säubern. Hierbei lassen sich unterschiedlichste Formen des Werkstoffs bilden. Bei solchen Ausführungsformen ist neben der die Raumluft reinigenden Wirkung auch die Schalldämpfung bemerkenswert. So sind die Innenraum-Elemente gerade in Großraumbüros nutzbringend auch zur Geräuschreduzierung einsetzbar. From a molded body, which is obtained from a material according to the above description, interior ceiling panels or room divider can be made, which clean the room air. Also, design elements are advantageous, which can be set up indoors to clean the room air. In this case, the most varied forms of the material can be formed. In such embodiments, in addition to the air cleaning effect and the sound attenuation is remarkable. Thus, the interior elements can be useful also used in open-plan offices for noise reduction.
Zum Zweck der Formgebung können die einzelnen Optofluidik-Elemente, beispielsweise Platten, miteinander verbunden, beispielsweise verklebt werden. Dabei sollte darauf geachtet werden, dass ausreichend UV-Licht bis in das Zentrum der so verbundenen Elemente dringen kann und eine Durchströmung gewährleistet ist. For the purpose of shaping, the individual opto-fluidics elements, for example plates, can be connected to one another, for example adhesively bonded. It should be ensured that sufficient UV light can penetrate into the center of the elements connected in this way and a flow is ensured.
Als vorteilhaft erweist sich ein Reaktor aus Elementen, zwischen denen eine UV-Lampe eingebettet ist. Diese strahlt vom Zentrum des Reaktors UV-Licht nach außen. Neben dem emittierten UV-Licht kann die eingebundene Lampe auch noch Licht im sichtbaren Bereich abstrahlen, sodass ein solcher Reaktor dann auch als Leuchte dient. Eine derart eingebundene Lampe führt ferner durch die damit erzielte Konvektion der Lampe durch die entstehende Wärme zur Zwangsdurchströmung des Optofluidik-Reaktors. A reactor made of elements between which a UV lamp is embedded proves to be advantageous. This radiates from the center of the reactor UV light to the outside. In addition to the emitted UV light, the integrated lamp can also emit light in the visible range, so that such a reactor then also serves as a luminaire. Such a connected lamp also leads by the resulting convection of the lamp by the resulting heat for forced flow through the Optofluidik reactor.
Auch ist erfindungsgemäß ein Lüftungsgerät umfasst, dass als wesentliches Funktionselement einen Optofluidik-Reaktor aufweist, wie er oben beschrieben ist. Ein solches Lüftungsgerät verfügt über einen Ventilator oder dergleichen, um den Optofluidik-Reaktor mit Luft zwangs zu durchströmen. Diese Zwangsdurchströmung des fotokatalytischen Reaktors erhöht die Reinigungswirkung der Luft um ein Vielfaches. In vorteilhafter Weise lässt sich der erfindungsgemäße Schaumwerkstoff als Optofluidik-Reaktor in einem solchen Lüftungsgerät leicht auswechseln, d. h. demontieren, und auch reinigen. Also according to the invention comprises a ventilation device that has as an essential functional element an opto-fluidic reactor, as described above. Such a ventilation device has a fan or the like to forcibly flow through the optofluidic reactor with air. This forced flow of the photocatalytic reactor increases the cleaning effect of the air many times. Advantageously, the foam material according to the invention can be easily replaced as optofluidic reactor in such a ventilation device, d. H. dismantle, and also clean.
In vorteilhafter Weise ist der erfindungsgemäße Optofluidik-Reaktor auch als Filterkörper für Luft- Absaughauben einsetzbar. Diese werden im Stand der Technik für Küchen, oder zum Absaugen von Dämpfen z. B. von Lösungsmitteln, Schweißrauch, oder Rauchgase verwendet. Advantageously, the optofluidic reactor according to the invention can also be used as a filter body for air suction hoods. These are in the art for kitchens, or for sucking vapors z. As solvents, welding fumes, or flue gases used.
Die fotokatalytische Wirkung des Optofluidik-Reaktors kann wie oben bereits dargestellt in vorteilhafter Weise erhöht werden, wenn dieser mit einer UV-A- Lampe bestrahlt wird. Insofern weist eine vorteilhafte Ausführungsform des Lüftungsgerätes, der Dunstabzugshaube oder des Innenraum-Formkörpers eine solche UV-A-Lampe auf, mit der dann der Optofluidik-Reaktor bei Bedarf angestrahlt werden kann. Insofern ist auch geeignet, einen Design- körper aus dem erfindungsgemäßen metallisierten Schaumwerkstoff zu bilden, der mit einer solchen UV-Lampe bestrahlt wird. Die beigefügten Figuren 1 und 2 sind Fotoaufnahmen eines retikulierten Basis-Schaums, wie er als Ausgangsstoff für den Optofluidik-Reaktor verwendet werden kann. Fig. 2 ist dabei eine vergrößerte Ansicht des Schaums aus Fig. 1. The photocatalytic effect of the optofluidic reactor can be advantageously increased as already shown above, when it is irradiated with a UV-A lamp. In this respect, an advantageous embodiment of the ventilation device, the extractor hood or the interior molded body on such a UV-A lamp, with which then the optofluidic reactor can be irradiated if necessary. In this respect, it is also suitable to form a design body from the metallized foam material according to the invention, which is irradiated with such a UV lamp. The attached Figures 1 and 2 are photographs of a reticulated base foam, as it can be used as starting material for the Optofluidik reactor. FIG. 2 is an enlarged view of the foam of FIG. 1. FIG.
Mit Bezug auf die Lösungsvariante b), gemäß der eine Metallmatrix auf einer Oberfläche ausgebildet wird, wird im Folgenden eine zum Zwecke der Dekontamination von Bakterien, Viren und anderen allgemeinen Verunreinigungen neue Beschichtung aufgezeigt. Es ergeben sich neben einer Beschichtung für einen retikulierten Basis-Schaum, wie er oben beschrieben und für verschiedenste Anwendungen erläutert ist, zusätzlich auch Beschich- tungsanwendungen ohne Fluid-Durchflutung, wie beispielsweise für Türgriffe, Sanitärarmaturen, bzw. für alle Flächen, die eine Berührung erfahren und somit einer Kontamination mit Bakterien und Viren ausgesetzt sind. Dies betrifft Anwendungen im Privathaushalt, Krankenhäusern oder öffentlichen Einrichtungen. With reference to the solution variant b), according to which a metal matrix is formed on a surface, a new coating for the purpose of decontamination of bacteria, viruses and other general impurities is shown below. In addition to a coating for a reticulated base foam, as described above and explained for a variety of applications, there are also additional coating applications without fluid flooding, such as for door handles, sanitary fittings, or for all surfaces that touch experienced and thus exposed to contamination with bacteria and viruses. This concerns applications in the home, hospitals or public institutions.
Es ist bekannt, in galvanischen Elektrolyten unterschiedliche Stoffe, wie Diamantstaub, SiC, Al2O3, CBN, WC, TiC, PTFE oder Graphit zu dispergieren und mit dem jeweiligen Elektrolyten galvanisch (z.B. Sulfamatnickel, Watf s Sulfat Nickel o.ä.) oder außenstromlos (z.B. Chemisch Nickel) auf ein jeweiliges Bauteil mit abzuscheiden, um einen Abrieb zu mindern, eine Temperaturbeständigkeit zu erhöhen oder Gleiteigenschaften zu verbessern. Gemäß der vorliegenden Erfindung wird TiO2 - in bevorzugt der Anatasform - zur Verwendung als photokatalytisch aktive Dispersionsschicht als sog. TiO2-Metall Matrix-Schicht ausgebildet. Die bevorzugte Partikelgröße des Ti02 ist 0- 3μιη; z.B. KRONOClean 7000 und KRONOClean 7050 Es ist auch möglich, nanoskalige TiO2 Partikel mit einer Größe von ca. 20nm zu verwenden, wobei die Herstellung der Suspension aufgrund von Konglomerationsproblemen aufwendig sein kann, jedoch durchführbar ist. Bei den nanoskaligen Partikeln ist es hilfreich, Dispergierchemikalien zu Hilfe zu nehmen. It is known to disperse in galvanic electrolytes different substances, such as diamond dust, SiC, Al 2 O 3 , CBN, WC, TiC, PTFE or graphite and galvanically with the respective electrolyte (eg sulfamate nickel, Watf s sulfate nickel or similar). or electrolessly (eg, chemically nickel) on a respective component to be deposited in order to reduce abrasion, to increase temperature resistance or to improve sliding properties. According to the present invention is TiO 2 - preferably in the anatase form - adapted for use as a photocatalytically active dispersion layer as so-called TiO2-metal matrix layer.. The preferred particle size of the Ti0 2 is 0-3μιη; eg KRONOClean 7000 and KRONOClean 7050 It is also possible to use nanoscale TiO 2 particles with a size of about 20 nm, whereby the preparation of the suspension may be complicated due to conglomeration problems, but is feasible. For nanoscale particles, it helps to use dispersant chemicals.
Der grundlegende Verfahrensablauf für die Beschichtung mit z.B. TiO2 - ENiP (TiO2 mit Chemisch Nickel-Phosphor Metallschicht) oder Galvanisch NiP wird nachfolgend für den retikulierten Schaum für die Luft-, und Wasserreinigung, wie auch bei Kunststoffbauteilen beschrieben: The basic procedure for the coating with eg TiO 2 - ENiP (TiO 2 with chemical nickel-phosphorus metal layer) or Galvanic NiP is described below for the reticulated foam for air and water purification as well as for plastic components:
1. Der retikulierte Schaum wird in einem ersten Beschichtungsschritt mit bevorzugt einer Kupferschicht > 1 μιη durch Aufdampfen oder durch außenstromloses Verfahren (chemisch Kupfer) beschichtet. 2. Diese erste Metallschicht wird auf galvanischem Weg mit Kupfer, Eisen, oder Aluminium (bevorzugt Cu) mit einer Schichtdicke von mehr als 10 μιη beschichtet, bis der Schaum eine Eigensteifigkeit erlangt. 1. The reticulated foam is coated in a first coating step with preferably a copper layer> 1 μιη by vapor deposition or by electroless process (chemical copper). 2. This first metal layer is galvanically coated with copper, iron, or aluminum (preferably Cu) with a layer thickness of more than 10 μιη until the foam acquires its own rigidity.
3. Auf diese Schicht wird eine weitere Metall-, oder Metalllegierungsschicht z. B. Ni, Weißbronze, Gelbbronze, NiP, Cr, NiKo,ENiCoP, mit einer Schichtdicke > 5 μιη aufgebracht. 4. Auf diese Schicht wird die photokatalytische z.B. NiP-Ti02 Schicht mit einer Schichtdicke > 1 μιη aufgebracht 3. On this layer, another metal or metal alloy layer z. B. Ni, white bronze, yellow bronze, NiP, Cr, NiKo, ENiCoP, applied with a layer thickness> 5 μιη. 4. The photocatalytic, for example, NiP-Ti0 2 layer with a layer thickness> 1 μm is applied to this layer
Es ist auch möglich, eine Cu-Ti02 Schicht mit einer Schichtdicke > Ιμιη auf die nach Punkt 2 hergestellte erste Metallschicht aufzubringen. It is also possible to apply a Cu-Ti0 2 layer with a layer thickness> Ιμιη on the first metal layer produced according to point 2.
Gemäß einer Ausführungsform ist es möglich, die photokatalytische Schicht direkt ohne weitere Zwischenschicht auf die Kupferschicht 2 aufzubringen According to one embodiment, it is possible to apply the photocatalytic layer directly to the copper layer 2 without further intermediate layer
Gemäß einer Ausführungsform ist es auch möglich, auf die photokatalytische Schicht 4 eine Schicht aufzubringen, z.B. Glanzchrom, oder ein Edelmetall z.B. Au, Pd, Rt oder Pt. According to one embodiment, it is also possible to apply a layer to the photocatalytic layer 4, e.g. Bright chrome, or a noble metal e.g. Au, Pd, Rt or Pt.
Bei metallischen Werkstücken entfällt der Schritt 1  For metallic workpieces step 1 is omitted
Ausführungsbeispiel zur Herstellung eines Elektrolyten zur Bildung einer Metallmatrix mit einer T102- Ni Abscheidung nach Schritt 4: Exemplary embodiment for producing an electrolyte for forming a metal matrix with a T102-Ni deposition after step 4:
Watf scher (Sulfat) Nickelelektrolyt mit der Zusammensetzung Watf shear (sulfate) nickel electrolyte with the composition
NiS04.6H20 350 g/1 NiSO4.6H20 350 g / 1
NiC12.6H20 45 g/l  NiC12.6H20 45 g / l
H3B03 45 g/1  H3B03 45g / 1
pH 4 pH 4
T 55 °C  T 55 ° C
Ti02 20- 150 g/1 Partikelgröße 0-3 μιη  TiO 2 20-150 g / 1 particle size 0-3 μιη
Kathodische Stromdichte 5 A/dm2  Cathodic current density 5 A / dm2
Kationenaktives Fluortensid 0,2 g/1 FT 248 (Fa. BASF) Mit dieser Zusammensetzung ist eine Einbaurate von bis zu 50 Masse % möglich. Gemäß einer Ausführungsform ist es auch möglich, ein Netzmittel wie Natriumdodecylsulfat oder Standardnetzmittel von Galvanochemikalienlieferfirmen zur Verhinderung von Porenbildung zu verwenden. Cationic Fluorosurfactant 0.2 g / 1 FT 248 (BASF) With this composition, a rate of incorporation of up to 50% by weight is possible. According to one embodiment, it is also possible to use a wetting agent such as sodium dodecyl sulfate or standard wetting agents from galvanic chemicals supply companies to prevent pore formation.
Die Ti02 Partikel werden durch eine Elektrolytbewegung mittels mechanischer Rührung in Schwebe gehalten. Eine sanfte Lufteinblasung ist vorteilhaft. The Ti0 2 particles are held in suspension by an electrolyte movement by means of mechanical stirring. A gentle air injection is advantageous.
Die jeweilige exakte Ti02- Konzentration ist abhängig von der gewünschten Einbaurate des Oxides und der Bauteilgeometrie, sowie generell des Bauteils (Oberflächenrauhigkeit, Mikrogeometrie, etc.). The respective exact Ti0 2 concentration depends on the desired incorporation rate of the oxide and the component geometry, as well as in general of the component (surface roughness, microgeometry, etc.).
Einen wesentlichen Einfluss auf die Einbaurate haben auch die Rührgeschwindigkeit und die angewandte Stromdichte in Abhängigkeit der Bauteilgeometrie und der angeführten Mikrostruktur. The rate of stirring and the applied current density as a function of the component geometry and the stated microstructure also have a significant influence on the incorporation rate.
Wesentlich ist auch die genaue Einhaltung des pH-Wertes, da durch die Herstellung der einzulagernden TiO2- Teilchen noch Reste von z.B. Precursor Substanzen anhaften können (alkalisch und sauer). Die TiO2- Metall- Matrixabscheidung ist mit unterschiedlichsten Elektrolyten als Matrixmetall möglich. Als galvanisch (mit Strom) hergestellte Matrixmetalle, welche verwendet werden, sind NiP, Ni, Co, Cu, W, Mn, Mo, Cr, Sn, Zn, (Hartchrom), Edelmetalle wie Pd, Pt, Ruthenium, Rhodium und die unterschiedlichen Legierungen daraus geeignet. Auch können Sulfamatelektrolyte oder ionische Flüssigkeiten verwendet werden. It is also essential to strictly adhere to the pH, since residues of, for example, precursor substances can adhere to the TiO 2 particles to be stored (alkaline and acidic). The TiO 2 - metal matrix deposition is possible with a wide variety of electrolytes as matrix metal. The matrix metals used as electroplated (by current) which are used are NiP, Ni, Co, Cu, W, Mn, Mo, Cr, Sn, Zn, (hard chromium), noble metals such as Pd, Pt, ruthenium, rhodium, and the like Alloys suitable. Also, sulfamate electrolytes or ionic liquids can be used.
Auch ist das Matrixmetall mit außenstromlosen Verfahren wie Chemisch Nickel-Phosphor und den unterschiedlichsten Legierungen z.B. Ni-Co-P (Hydrazin Reduktionsmittel), Co-P, Ni-Cu-P, Ni-W-P, Ni-Mo-P und chemisch Kupfer geeignet. Also, the matrix metal is used with electroless processes such as chemical nickel-phosphorus and a variety of alloys, e.g. Ni-Co-P (hydrazine reducing agent), Co-P, Ni-Cu-P, Ni-W-P, Ni-Mo-P, and chemically copper.
Der große Vorteil dieser Ti02- Einlagerungsschichten ist, dass man die katalytisch aktiven Partikel fest in einer sehr abriebbeständigen Metall-Matrix fixiert hat und folglich mit einer sehr langen Wirkdauer zu rechnen ist. The big advantage of these Ti0 2 - intercalation layers is that the catalytically active particles are fixed firmly in a very abrasion-resistant metal matrix and consequently a very long duration of action is to be expected.
Zusätzlich liegen zu jedem Zeitpunkt auch bei einem eintretenden Verschleiß der Beschichtung immer wieder neue Ti02-Partikel an der Oberfläche frei und wirken damit solange, bis ein vollständiger Verschleiß der Beschichtung eintritt. Im Gegensatz zu im Sol-Gel-Verfahren, Lackierverfahren (Naß,- Pulverlack), oder Dünnschichtverfahren (Sputter, Aufdampfen etc.) aufgebrachten Beschichtungen halten diese Beschichtungen einer Metallmatrix unvergleichlich länger und machen sie somit prädestiniert für abriebbeanspruchte Bauteile und Oberflächen welche häufig durch z. B. Berührung beansprucht werden und z.B. besonders in Krankenhäusern mit unterschiedlichen Bakterien und Viren kontaminiert sind. Derartig hergestellte Ti02- Metall-Matrix Schichten haben den großen Vorteil, dass sie in Verbindung mit Licht kontinuierlich Viren und Bakterien an Türkliniken, Griffflächen etc. abbauen, und somit auch außerhalb von Reinigungszyklen größtmögliche Sicherheit gegen Ansteckung und Übertragung von Krankheiten durch Berührungskontamination gegeben ist. In addition, new TiO 2 particles are always exposed on the surface at any time, even with incoming wear of the coating, and thus continue to work until complete wear of the coating occurs. In contrast to coatings applied in the sol-gel process, painting process (wet, powder coating), or thin-film processes (sputtering, vapor deposition, etc.), these coatings of a metal matrix last incomparably longer and thus make them predestined for abrasion-stressed components and surfaces which are often damaged by, for example, , B. be claimed and contaminated, for example, especially in hospitals with different bacteria and viruses. Ti0 2 metal matrix layers produced in this way have the great advantage that in combination with light, they continuously reduce viruses and bacteria in door clinics, gripping surfaces, etc., and thus ensure maximum safety against contagion and transmission of diseases through contact contamination outside of cleaning cycles ,
Der Eintrag von Ti02- Partikeln in die Umwelt ist damit gegenüber weniger abriebbeständigen Lackschichten minimiert. The entry of Ti0 2 - particles in the environment is thus minimized compared to less abrasion resistant paint layers.
Mit dem beschriebenen Verfahrensweg ist es auch möglich, metallisierte, textile Grundwerkstoffe wie Vliese, Gewebe und ähnliches aus Kunststoff-, Glas-, oder Carbongrundwerkstoff zu beschichten. With the described method, it is also possible to coat metallized, textile base materials such as nonwovens, fabrics and the like of plastic, glass, or carbon base material.

Claims

Λ Α. Ansprüche: Λ Α. Claims:
1. Verfahren zur Herstellung eines kataly tischen Werkstoffs zur Eliminierung von Schadstoffen, aufweisend 1. A process for the preparation of a catalytic material for the elimination of pollutants, comprising
- die Fertigung eines retikulierten Kunststoff-Schaumes als Platte mit einer Dicke von mindestens 10 mm;  - The production of a reticulated plastic foam as a plate with a thickness of at least 10 mm;
- Auftragen mindestens einer ersten Metall- oder Metalllegierungs- Schicht auf die Oberfläche der retikulierten Schaumplatte;  - Applying at least one first metal or metal alloy layer on the surface of the reticulated foam sheet;
- Auftragen eines photokatalytischen Substrates auf die Metall- oder Metalllegierungs-Schicht als eine im Sol-Gel-Verfahren hergestellte Lösung durch Tauchen oder Fluten auf die Metall- oder Metalllegierungs-Schicht.  - Applying a photocatalytic substrate on the metal or metal alloy layer as a solution prepared by sol-gel method by dipping or flooding on the metal or metal alloy layer.
2. Verfahren nach Anspruch 1, 2. The method according to claim 1,
dadurch gekennzeichnet, dass das photokataly tische Substrat characterized in that the photocatalytic substrate
- Titandioxid TiO2 ist oder Titanium Dioxide TiO 2 is or
- eine Metallschicht aus Kupfer, Nickel, Zink, Zinn, Kobalt oder Mangan aufweist, oder aus Legierungen oder Oxiden hieraus, a metal layer of copper, nickel, zinc, tin, cobalt or manganese, or of alloys or oxides thereof,
- oder eine Edelmetallschicht aus Silber, Palladium, Platin ist oder aus Legierungen hieraus or a noble metal layer of silver, palladium, platinum or alloys thereof
- oder eine Legierung aus mindestens zwei Metallen der Gruppe Kupfer, Nickel, Zink, Zinn, Kobalt, Mangan, Silber, Palladium, Platin. or an alloy of at least two metals of the group copper, nickel, zinc, tin, cobalt, manganese, silver, palladium, platinum.
3. Verfahren nach einem der vorangehenden Ansprüche, 3. The method according to any one of the preceding claims,
dadurch gekennzeichnet, dass nachfolgend der mindestens einen ersten Metallschicht und vor dem Auftrag des photokatalytischen Substrats eine weitere Metallschicht aus characterized in that following the at least one first metal layer and before the application of the photocatalytic substrate, a further metal layer
- Kupfer, Aluminium, Nickel, Zinn, Zink, Silber, Palladium, Platin oder aus Legierungen hieraus aufgetragen wird.  - Copper, aluminum, nickel, tin, zinc, silver, palladium, platinum or alloys thereof is applied therefrom.
4. Verfahren nach einem der vorangehenden Ansprüche, 4. The method according to any one of the preceding claims,
dadurch gekennzeichnet, dass der retikulierte Schaum aus Polyethersulfon (PES) oder Polypropylen (PP) oder Polyethylen (PE) oder Polyurethan (PU) oder Polyester oder Polyether ist. characterized in that the reticulated foam is of polyethersulfone (PES) or polypropylene (PP) or polyethylene (PE) or polyurethane (PU) or polyester or polyether.
5. Verfahren nach einem der vorangehenden Ansprüche, 5. The method according to any one of the preceding claims,
dadurch gekennzeichnet, dass der retikulierte Schaum eine Porenanzahl bis 34 ppi (pores per inch) hat. characterized in that the reticulated foam has a pore number up to 34 ppi (pores per inch).
6. Verfahren zur Herstellung eines katalytischen Werkstoffs oder einer Beschichtung zur Eliminierung von Schadstoffen, bei welchem Verfahren eine photokatalytisch aktive Dispersionsschicht als Metall-Matrix-Schicht auf einer Oberfläche ausgebildet wird.. 6. A process for the preparation of a catalytic material or a coating for the elimination of pollutants, in which process a photocatalytically active dispersion layer is formed as a metal-matrix layer on a surface.
7. Innenraumelement aus einem Herstellungsverfahren eines optofluidischen Katalysator-Werkstoffes nach einem der Ansprüche 1 bis 6. 7. Interior element of a manufacturing method of an optofluidic catalyst material according to one of claims 1 to 6.
8. Lüftungsgerät mit einem Element aus einem Herstellungsverfahren eines optofluidischen Katalysator-Werkstoffes nach einem der Ansprüche 1 bis 6. 8. Ventilation device with an element from a production process of an optofluidic catalyst material according to one of claims 1 to 6.
9. Lüftungsgerät nach Anspruch 8, 9. Ventilation device according to claim 8,
dadurch gekennzeichnet, dass das Lüftungsgerät eine UV-Lampe aufweist. characterized in that the ventilation device comprises a UV lamp.
10. Lüftungsgerät nach Anspruch 8 oder 9, 10. Ventilation device according to claim 8 or 9,
dadurch gekennzeichnet, dass das Element aus optofluidischem Katalysator- Werkstoff als Filtereinsatz des Lüftungsgerätes ausgebildet ist. characterized in that the element of optofluidic catalyst material is designed as a filter insert of the ventilation device.
EP12729903.0A 2011-05-31 2012-05-25 Production of a catalytically active, metalized reactive foam material and use thereof Withdrawn EP2726204A2 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE102011050758A DE102011050758A1 (en) 2011-05-31 2011-05-31 Optofluidics reactor
PCT/EP2012/059897 WO2012163853A2 (en) 2011-05-31 2012-05-25 Production of a catalytically active, metalized reactive foam material and use thereof

Publications (1)

Publication Number Publication Date
EP2726204A2 true EP2726204A2 (en) 2014-05-07

Family

ID=46384324

Family Applications (1)

Application Number Title Priority Date Filing Date
EP12729903.0A Withdrawn EP2726204A2 (en) 2011-05-31 2012-05-25 Production of a catalytically active, metalized reactive foam material and use thereof

Country Status (7)

Country Link
US (1) US9346041B2 (en)
EP (1) EP2726204A2 (en)
JP (2) JP6223327B2 (en)
CN (2) CN103635259B (en)
DE (1) DE102011050758A1 (en)
HK (2) HK1195027A1 (en)
WO (1) WO2012163853A2 (en)

Families Citing this family (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP6078336B2 (en) * 2012-12-27 2017-02-08 日本ピラー工業株式会社 Photocatalyst carrier and method for producing the same
CN106794450B (en) * 2014-08-29 2020-12-25 日东电工株式会社 Photocatalytic coating and preparation method thereof
US10471170B2 (en) * 2015-06-29 2019-11-12 Puresys Co., Ltd. Air purifying sterilizer module with improved catalytic performance and air purifying sterilizer including the same
DE102016209952A1 (en) 2016-06-07 2017-12-07 Robert Bosch Gmbh filter means
JP7130198B2 (en) 2017-06-29 2022-09-05 日本光電工業株式会社 Method for producing layered cell sheet, and layered cell sheet produced thereby
IL309140A (en) * 2021-06-08 2024-02-01 Photio Spa A high-efficient decontaminant additive comprising metal oxide nanoparticles in a metallic or semi-metallic nanoparticle matrix, useful to be added in paints, formulations or the like for protecting, coating or decorating, soft or hard, surfaces
CN115814746A (en) * 2021-09-16 2023-03-21 中国科学院大连化学物理研究所 Integral adsorption inactivation material and preparation method and application thereof
DE102022113128A1 (en) 2022-05-24 2023-11-30 Zahnen Technik Gmbh Water treatment system for destroying organic pollutants in water and use of a water treatment system

Family Cites Families (34)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE3522287A1 (en) 1985-06-21 1987-01-02 Moc Danner Gmbh Open-pored body for filtering and/or catalytic treatment of gases or liquids and process for the production thereof
DE3916713A1 (en) 1989-05-23 1990-11-29 Hoechst Ag THREE-DIMENSIONALLY MOLDED, METALLIZED NETWORK, METHOD FOR PRODUCING IT AND ITS USE
DE3920428A1 (en) 1989-06-22 1991-01-03 Gutec Gmbh CARRIER CATALYST FOR THE DECOMPOSITION OF OZONE
JP2630575B2 (en) * 1995-02-17 1997-07-16 株式会社鈴寅 Sheet-shaped deodorizing photocatalyst
US6830785B1 (en) * 1995-03-20 2004-12-14 Toto Ltd. Method for photocatalytically rendering a surface of a substrate superhydrophilic, a substrate with a superhydrophilic photocatalytic surface, and method of making thereof
US6468428B1 (en) 1996-02-28 2002-10-22 Hoya Corporation Glass material for carrying a photocatalyst, filter device using the same and light irradiating method
JP3781065B2 (en) * 1996-08-29 2006-05-31 株式会社ブリヂストン Photocatalyst
JPH1072664A (en) * 1996-08-29 1998-03-17 Bridgestone Corp Photocatalyst coated body
US6051117A (en) * 1996-12-12 2000-04-18 Eltech Systems, Corp. Reticulated metal article combining small pores with large apertures
JP3275032B2 (en) 1997-03-03 2002-04-15 独立行政法人産業技術総合研究所 Environmental purification material and method for producing the same
JPH10329261A (en) * 1997-06-03 1998-12-15 Asahi Chem Ind Co Ltd Polymer material inorganic thin film laminate
EP0911078A1 (en) * 1997-10-20 1999-04-28 Hitachi Metals, Ltd. Photocatalyst-supporting body and photocatalytic apparatus
JPH11158694A (en) * 1997-11-27 1999-06-15 Toto Ltd Article with hydrophilic coating, and coating method
US6154311A (en) * 1998-04-20 2000-11-28 Simtek Hardcoatings, Inc. UV reflective photocatalytic dielectric combiner having indices of refraction greater than 2.0
JP3018034B2 (en) * 1998-05-28 2000-03-13 ライザー工業株式会社 Ultraviolet sterilization and purification method and device
JP2000084415A (en) * 1998-09-11 2000-03-28 Nobuyuki Koura Composite material having photocatalytic function and its production
JP2000192368A (en) * 1998-12-24 2000-07-11 Toray Ind Inc Fiber structure
JP2000210534A (en) 1999-01-25 2000-08-02 Mitsubishi Paper Mills Ltd Photocatalyst deodorizing filter
US6537379B1 (en) * 2000-01-13 2003-03-25 Hrl Laboratories, Llc Photocatalytic coating and method for cleaning spacecraft surfaces
DE10013237A1 (en) 2000-03-10 2002-04-25 Dieter Meissner Production of foam from a solution used in disinfecting processes, photo-induced syntheses or decontamination processes comprises introducing a photo-reactive substance into the foam
US6815052B2 (en) * 2000-12-01 2004-11-09 P1 Diamond, Inc. Filled diamond foam material and method for forming same
JP3945255B2 (en) * 2001-01-29 2007-07-18 住友チタニウム株式会社 Photocatalyst composite and method for producing the same
JP3791901B2 (en) * 2001-07-16 2006-06-28 株式会社ノリタケカンパニーリミテド Photocatalyst holder and method for producing the same
DE10210465A1 (en) 2002-03-04 2003-10-09 Fraunhofer Ges Forschung Photocatalytic element for decomposing hydrogen-containing compounds, especially for supplying hydrogen to fuel cells, comprises a thin photocatalytic layer on a support with an open pore structure
AU2003287691A1 (en) * 2002-11-12 2004-06-03 University Of Virginia Patent Foundation Extremely strain tolerant thermal protection coating and related method and apparatus thereof
US7354624B2 (en) * 2004-05-28 2008-04-08 Ppg Industries Ohio, Inc. Multi-layer coatings and related methods
US7354650B2 (en) * 2004-05-28 2008-04-08 Ppg Industries Ohio, Inc. Multi-layer coatings with an inorganic oxide network containing layer and methods for their application
JP2007275292A (en) * 2006-04-06 2007-10-25 Bridgestone Corp Deodorization filter and deodorizing device
US20090117371A1 (en) 2006-04-07 2009-05-07 Interpane Entwicklungs-Und Beratungsgesellschaft Mbh & Co. Kg Weather-resistant layer system
US8017247B2 (en) * 2007-03-30 2011-09-13 Alcoa Inc. Self cleaning aluminum alloy substrates
JP5565602B2 (en) * 2008-07-02 2014-08-06 住友電気工業株式会社 Porous photocatalytic element
US9095636B2 (en) 2008-09-29 2015-08-04 Carrier Corporation Catalytic substrates and methods for creating catalytic coatings for indoor air quality applications
US8372477B2 (en) * 2009-06-11 2013-02-12 Basf Corporation Polymeric trap with adsorbent
US8673157B2 (en) 2009-09-15 2014-03-18 Basf Se Photoreactor

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
None *
See also references of WO2012163853A2 *

Also Published As

Publication number Publication date
JP6223327B2 (en) 2017-11-01
HK1195027A1 (en) 2014-10-31
US20140179513A1 (en) 2014-06-26
WO2012163853A2 (en) 2012-12-06
US9346041B2 (en) 2016-05-24
CN105749989A (en) 2016-07-13
WO2012163853A3 (en) 2013-01-24
CN103635259A (en) 2014-03-12
HK1227353A1 (en) 2017-10-20
JP2017127873A (en) 2017-07-27
DE102011050758A1 (en) 2012-12-06
JP2014523335A (en) 2014-09-11
CN103635259B (en) 2016-03-16

Similar Documents

Publication Publication Date Title
WO2012163853A2 (en) Production of a catalytically active, metalized reactive foam material and use thereof
Goei et al. Ag-decorated TiO2 photocatalytic membrane with hierarchical architecture: Photocatalytic and anti-bacterial activities
EP2758171A1 (en) Method for the photocatalytically active coating of surfaces
EP1509083A1 (en) Antimicrobial polymeric coating composition
KR102323781B1 (en) Multi-layer structure and method of manufacturing multi-layer structure
DE102007061965A1 (en) Reduction of microbial contamination in cooling towers
EP1984675A1 (en) Filter element for extractor hood
EP2352377B1 (en) Use of a component with an antimicrobial surface
DE102010020427A1 (en) Product with an antimicrobial surface layer and process for its preparation
DE4416501C2 (en) Germ protection for house water filter sieve inserts
DE102010021554A1 (en) Component with a catalytic surface, process for its preparation and use of this component
WO2010057800A1 (en) Component having a catalytic surface, method for the production thereof, and use of said component
DE102010021555A1 (en) Fan for a room extractor, room extractor with such a fan and method of making such a fan
KR20070039199A (en) Method for treating the surface of aluminium material and aluminium material manufactured by the same
DE102008060800A1 (en) Coating composition, useful to produce layer with hierarchical micro- and nano-structured surface, comprises mixture of nanocrystalline metal oxide particles, titanium dioxide sol and compounds from glass-forming elements
DE102015116547B4 (en) Photocatalytic filter for mixing gas breakdown and manufacturing process therefor
EP1835051A2 (en) Self-cleaning surface
JPH11158694A (en) Article with hydrophilic coating, and coating method
DE102006029544B4 (en) Backwashable water filter
EP2669004B1 (en) Ozone-decomposing catalyst system and process for production
US11964739B2 (en) Coatings that reduce or prevent barnacle attachment to a marine structure
DE102012209262A1 (en) Preparing supported catalyst useful for decomposition of substances e.g. ozone, comprises providing carrier comprising polymer, dissolving carrier surface using solvent, applying catalyst to dissolved carrier surface, and removing solvent
EP1911513A2 (en) Ozone catalytic converter
KR20220125762A (en) Method for manufacturing photocatalyst-substrate composite and photocatalyst-substrate composite manufactured therefrom
WO2022008520A1 (en) Device for depleting active microorganisms in fluids

Legal Events

Date Code Title Description
PUAI Public reference made under article 153(3) epc to a published international application that has entered the european phase

Free format text: ORIGINAL CODE: 0009012

17P Request for examination filed

Effective date: 20131223

AK Designated contracting states

Kind code of ref document: A2

Designated state(s): AL AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO PL PT RO RS SE SI SK SM TR

DAX Request for extension of the european patent (deleted)
17Q First examination report despatched

Effective date: 20180124

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: THE APPLICATION HAS BEEN WITHDRAWN

18W Application withdrawn

Effective date: 20180530