EP2630086A1 - Photocatalytic material - Google Patents
Photocatalytic materialInfo
- Publication number
- EP2630086A1 EP2630086A1 EP11833926.6A EP11833926A EP2630086A1 EP 2630086 A1 EP2630086 A1 EP 2630086A1 EP 11833926 A EP11833926 A EP 11833926A EP 2630086 A1 EP2630086 A1 EP 2630086A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- nanofibers
- metal
- photocatalyst material
- work function
- high work
- 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- Withdrawn
Links
Classifications
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61L—METHODS 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
- A61L2/00—Disinfection or sterilisation of materials or objects, in general; Accessories therefor
- A61L2/16—Disinfection or sterilisation of materials or objects, in general; Accessories therefor using chemical substances
- A61L2/23—Solid materials, e.g. granules, powders, blocks or tablets
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/40—Catalysts, in general, characterised by their form or physical properties characterised by dimensions, e.g. grain size
- B01J35/45—Nanoparticles
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61L—METHODS 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
- A61L9/00—Disinfection, sterilisation or deodorisation of air
- A61L9/16—Disinfection, sterilisation or deodorisation of air using physical phenomena
- A61L9/18—Radiation
- A61L9/20—Ultraviolet radiation
- A61L9/205—Ultraviolet radiation using a photocatalyst or photosensitiser
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J21/00—Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
- B01J21/06—Silicon, titanium, zirconium or hafnium; Oxides or hydroxides thereof
- B01J21/063—Titanium; Oxides or hydroxides thereof
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/38—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
- B01J23/40—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals of the platinum group metals
- B01J23/42—Platinum
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/38—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
- B01J23/40—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals of the platinum group metals
- B01J23/44—Palladium
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/30—Catalysts, in general, characterised by their form or physical properties characterised by their physical properties
- B01J35/39—Photocatalytic properties
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/50—Catalysts, in general, characterised by their form or physical properties characterised by their shape or configuration
- B01J35/58—Fabrics or filaments
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/50—Catalysts, in general, characterised by their form or physical properties characterised by their shape or configuration
- B01J35/58—Fabrics or filaments
- B01J35/59—Membranes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/02—Impregnation, coating or precipitation
- B01J37/0215—Coating
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/06—Washing
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/30—Ion-exchange
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen; Reversible storage of hydrogen
- C01B3/02—Production of hydrogen; Production of gaseous mixtures containing hydrogen
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen; Reversible storage of hydrogen
- C01B3/02—Production of hydrogen; Production of gaseous mixtures containing hydrogen
- C01B3/04—Production of hydrogen; Production of gaseous mixtures containing hydrogen by decomposition of inorganic compounds
- C01B3/042—Decomposition of water
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01G—COMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSES C01D OR C01F
- C01G23/00—Compounds of titanium
- C01G23/04—Oxides; Hydroxides
- C01G23/047—Titanium dioxide
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
- C01P2002/00—Crystal-structural characteristics
- C01P2002/50—Solid solutions
- C01P2002/52—Solid solutions containing elements as dopants
-
- 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
- Y02E60/36—Hydrogen production from non-carbon containing sources, e.g. by water electrolysis
Definitions
- the present invention relates to a photocatalyst material comprising N-doped Ti0 2 nanofibers.
- the present invention also relates to a method for producing said photocatalyst material and methods for using said material.
- Photocatalytic processes can be used to address several aspects of modern renewable energy production, organic contaminant removal from air and industrial waste water as well as anti-microbial surface treatment - just to mention a few.
- titanium dioxide Ti0 2
- Ti0 2 is probably the most promising photocata- lyst being environmentally friendly, with low cost, good photocatalytic activity and excellent photostability as has been demonstrated in electrochemical photolysis of water to produce hydrogen, to oxidize organic compounds, or to destroy cancer cells.
- Ti0 2 is a wide-band-gap semiconducting material with three kinds of natural crystalline phases such as rutile, brookite and anatase, from which the latter one is exhibiting the best photocatalytic activity.
- nanofibers can perform much better activity than the corresponding nano- particles.
- electrical devices applying nanoparticles e.g. for interconnects, electrodes, field-effect transistor channels, gas sensing layers
- it is vital to have a per- colated electrical network of the particles which is much easier to achieve with elongated 1 -dimensional particles than with ordinary 0-dimensional nanoparticles.
- bundling of nanofibers can also contribute to some mechanical robustness of tangled networks and also results in better entanglement with other nanofibers when forming macroscopic films.
- Wu et al. (Synthesis and electrochemical study of novel Pt-decorated Ti nano- wires, Electrochemistry Communications 1 1 (2009), 736-739) disclose the preparation of free-standing Ti nanowires and Pt-decorated Ti nanowires via a one-step environment-friendly and template-free process.
- SEM Scanning electron microscopy
- TEM transmission electron microscopy
- XRD X-ray diffraction
- EDX energy dispersive X-ray
- Lin et al. study the effect of calcination temperature on the structure of a Pt/Ti0 2 (B) nanofiber and its photocatalytic activity in ge- nerating H 2 .
- Platinized Ti0 2 (B) nanofiber was prepared and the activity thereof in generating H 2 gas from neat ethanol in photocatalytic dehydrogenation reaction was investigated.
- the present invention provides a photocatalyst material comprising N-doped Ti0 2 nanofibers decorated with nanoparticles of high work function material or p-type semiconductors.
- the present invention also provides a method for producing said photocatalyst material, said method comprising
- the present invention also provides a photocatalytic material obtained with said method.
- the invention points to applications in which the catalyst materials are used as prepared or applied in the form of composites with polymers (both synthetic and biopolymers) or inorganic materials.
- the present invention also provides methods for removing contaminants from surfaces, air or water, and methods for disinfecting thereof. Further, the present invention provides methods for generating H 2 fuel gas from water or alcohol/water mixture.
- the present invention is characterized in the claims.
- the obtained materials are efficient photocatalytic materials.
- the materials have enhanced visible-light activity.
- the materials are easy to produce even in industrial quantities with the methods of the invention. High ammonium concentrations during the preparation are avoided.
- a specific advantage of applying nanofiber-based catalysts is the versatility of post processing such materials because with the elongated nanoparticles it is simple to form large area films, coatings, and porous membranes as well as composites with polymers, all which are practical in several chemical processes due to easily accessible catalytic surfaces even when the photocatalyst is applied in a porous host of a composite matrix.
- Figure 1 shows EFTEM images of Pt and Pd nanoparticles supported on Ti0 2 nanoparticles (reference samples).
- the average particle sizes are 1 .8 ⁇ 0.3 nm and 3.5 ⁇ 1 .2 nm, respectively.
- Figure 2 shows (a) 25 mg Pd-Ti0 2 NFs and 25 mg cellulose immobilized on a filter paper by drop casting from aqueous suspension followed by drying. The diameter of the catalyst papers is -12 cm. (b) Two catalyst films wrapped around a plastic frame and (c) placed in the tube reactor. The 6 light sources are outside of the reactor volume, (d) Concentration of evolved H 2 gas under UV-B exposure (in 400 ml/min N 2 carrier flow).
- Figure 3 shows (a) XRD patterns of sodium hydrogen titanate nanofibers cal- cined in air at 400, 550, 600, 700 and 850 Q C for 2 hours (heating rate of 5 Q C/min). (b) Sodium hydrogen titanate nanofibers calcined for 2 h (heating rate of 5 Q C/min) and for 12 h (heating rates of 1 and 5 Q C/min).
- Figure 4 shows TEM images of (a) Ti0 2 nanofibers containing sodium impuri- ties (Ti0 2 -NFs), (b) 1 .0 wt% Pt-decorated, and (c) 1 .0 wt% Pd-decorated Ti0 2 - NFs. Insets in panels (b) and (c) show the corresponding Pt and Pd metal nano- particle size distributions, respectively.
- Figure 5 shows XRD patterns of the Ti0 2 -NFs and metal decorated Ti0 2 -NFs catalyst samples.
- Figure 6 shows (a) a linearized kinetic plot for the degradation of methyl orange using different types of Ti0 2 -based catalyst materials, (b) an UV-Vis absorbance spectra of methyl orange (initial concentration of 10.0 mg/l) as a function of illumi- nation time when applying Pd-Ti0 2 -NF catalyst (10.0 mg dispersed in 10 ml solution).
- Figure 7 shows the mechanism for photocatalytic generation of hydrogen from ethanol aqueous solution over Pt/Ti0 2 and Pd/Ti0 2 catalyst as a consequence of optical electron-hole pair generation, and efficient charge separation by the Schottky interface between metal nanoparticles of large work function and n-type semiconducting Ti0 2 . Protons forming by the reaction between holes and water as well as organic compounds are reduced by electrons injected previously to the metal nanoparticles.
- Figure 8 shows photographs of Ti0 2 -based catalyst/cellulose composite films showing the degradation of an organic dye deposited on the surface from a color ink.
- Each membrane (diameter of -38 mm) is filtered from an aqueous dispersion of 70 mg cellulose and 60 mg Ti0 2 NPs or Ti0 2 -NFs based catalyst (Pd or Pt content is 0.6 mg).
- Figure 9 shows scanning electron micrographs of cellulose fiber surfaces in (a) cellulose/Pt-Ti0 2 NPs and (b) cellulose/Pt-Ti0 2 NFs catalyst composite. Insets show lower magnification electron micrographs of the composite films, (c) Photograph taken from a bent catalyst membrane.
- Figure 10 shows (a) hydrogen formation over parent and metal loaded (1 w%) catalyst materials (0.2 g each) using ethanol: water (molar ratio 1 :3) mixture with UV-B irradiation (6 lamps), and (b) the effect of illumination power on hydrogen formation (using 0, 2, 4, 6, 4, 2, and 0 lamps) for Pt/Ti0 2 -NF and Pd/Ti0 2 -NF catalysts.
- Figure 1 1 shows TEM images of (a) pristine Ti0 2 NF, (b) N-Ti0 2 (A) NF, and (c) N-Ti0 2 (B) NF. Panels in the bottom right corners show high-magnification images of the lattice with the corresponding fast Fourier transformed pattern of each sample.
- Figure 12 shows TEM images of (a) N-Ti0 2 (A)-Pd NF, (b) N-Ti0 2 (A)-Pt NF, (c) N-Ti0 2 (B)-Pd NF, and (d) N-TiC1 ⁇ 2(B)-Pt NF.
- metal loading is -1 .0 wt %.
- Insets show histograms of the corresponding metal nanoparticle size distributions.
- Figure 13 shows hydrogen evolution from ethanol/water mixture (molar ratio 1 :3) over parent and noble metal loaded (1 .0 wt %) catalyst materials (100 mg each) under (a) UV-A (total UV power on the reactor ⁇ 1 .54 W, A(lmax) -365 nm) and (b) UV-B (total UV power on the reactor -1 .46 W, A(lmax) -312 nm) irradiation. N 2 gas was bubbled through the reactor at a flow rate of 400 mL/min, serving also as a purging gas for the evolving gaseous products.
- Figure 14 shows normalized absorption spectra of the Ti0 2 based materials used in the photocatalytic experiments.
- a photocatalyst (or photocatalytic) material comprising N- doped Ti0 2 nanofibers is decorated or coated with nanoparticles of high work function material or with nanoparticles of semiconductor material having less n- type semiconducting (i.e. more electron acceptor or more hole donor) character.
- decoration refers to non-continuous coating i.e. the nanoparticles may be at a certain distance from each other on the nanofibers "deco- rating" the fiber.
- coating may be understood to refer to similar coverage, as full 100% coverage is not required in the applications provided herein. Both terms may be used interchangeably, as well as the sometimes used term "deposited”.
- the amount of metal or semiconducting nanoparticles decorating the nanowires is typically relatively low, such as between 0.5-5 w%.
- the average par- tide sizes are typically between 0.5-20 nanometers.
- the Ti0 2 nanofibers contain alkali metal impurities.
- one method of making Ti0 2 nanofibers is a three-step process: 1 ) hydrothermal synthesis of sodium-titanate nanofibers from Ti0 2 nanoparticles, 2) washing of sodium-titanate nanofibers with HCI to replace sodium ions with protons and get hydrogen-titanate nanofibers, and 3) annealing of the hydrogen-titanate nanofibers at elevated temperatures to transform those to Ti0 2 nanofibers. If step 2 is not made long enough, there are still some sodium ions left in the titanate lattice i.e. in step two there may be sodium-hydrogen titanate.
- the alkali metal impurities are not limited to sodium, but also other alkali metals may be present, depending on the alkaline used in the first step, such as lithium or potassium.
- the presence of Na + or other alkali metal ions on the surface may influence water molecule adsorp- tion and lead to pH change at the catalyst/aqueous solution interface, thus changing electrochemical potentials in water splitting reactions, and can also be an additional source of charge carriers enhancing or inhibiting photochemical excitation effect.
- the Ti0 2 nanofibers are N-doped.
- N-doping refers to partial substitution (typically between 0.1 -2.0 atom-% or about 1 N per 100-200 O) of lattice oxygen with nitrogen (Ti0 2 - x N x ).
- the doping introduces visible-light activity from UV to the Ti0 2 and such doped material generally absorbs the light at less than 500 nm, such as at the range of 390-600 nm.
- One effect of the N-doping is intro- duction of visible-light activity to the photocatalytic material.
- Another effect is the enhancement in UV-A light activity in addition to UV-B light activity.
- the N-doping enhances the overall catalytic activity of the material.
- the high work function material refers to any suitable material having the electron work function of 4 eV or more.
- the high work function material is a platinum group metal, such as platinum or palladium.
- the high work function material may be for example a various form of carbon, such as a carbon nanotube, graphene, amorphous carbon or fullerene, or conductive polymer such as poly-thiophene, poly-acetylene, poly-pyrrole, or metal such as Ag, Au, Pt, Pd, Rh, or Ir, or other conductor forming Schottky junctions with TiO 2 or with N-doped TiO 2 .
- Semiconducting materials can be for example Co 3 O 4 , CuO, NiO, Cr 2 O 3 , Cu 2 S/CdS, Cu 2 O, ll-VI semiconductors (ZnO, ZnS, ZnSe, CdS, CdSe, CdTe, HgS, HgSe, HgTe) as well as Si, Ge or other compound semiconductors which make p-n junctions with TiO 2 and with N-doped TiO 2 .
- ll-VI semiconductors ZnO, ZnS, ZnSe, CdS, CdSe, CdTe, HgS, HgSe, HgTe
- the photocatalyst material is a composite with synthetic polymer, biopolymer or inorganic material.
- the synthetic polymer may be a step- growth polymer such as polyamide, polyacetate, polyester, nylon, bakelite, or a chain-growth polymer such as polyethylene, polypropylene, polyvinyl chloride, polystyrene, neoprene or synthetic rubber.
- the biopolymer may be a polysaccharide such as celluloses and derivatives thereof, hemicellulose, starch, glycogen or chi- tin, or polypeptide, such as wool, silk, or other polymer such as lignin or polyiso- prene.
- the inorganic material may be selected from ceramic-type materials, clays, cements, silicates, and alumino-silicates balanced with several type of alkali, earth and transition metal cations, transition and earth metal oxides, boron oxides and alloys thereof, mica, feldspar, carbides and nitrides of silicon and boron, various forms of alumina and hetero-atomic polymers.
- the cement may be hydraulic ce- ment, such as Portland cement or Portland-based cement, pozzolana cement, gypsum cement, high alumina cement, slag cement, silica cement, kiln dust or mixtures thereof.
- Hetero-atomic polymers may be selected from polyborazylenes; polysiloxanes, polysilazanes, polyphosphazenes, polythiazyls and polysulfides or perfluorated, chlorinated polymers with or without oxygen containing functional groups.
- the photocatalytic material of the invention may be for example in the form of a dispersion, a membrane, a film or a coating.
- the Ti0 2 nanofiber is a particle having at least one dimension less than 100 nm, such as a nanofiber having the length in the range of 0.2-5 ⁇ and diameter in the range of 10-100 nm. In one embodiment the Ti0 2 nanofiber is a particle having the length of about 1 ⁇ and the diameter of about 50 nm. In one embodiment the Ti0 2 is in the form of anatase.
- the present invention also provides a method for producing a photocatalyst material comprising N-doped Ti0 2 nanofibers coated with nanoparticles of high work function material or with p-type semiconductor as described above, said method comprising
- titanium dioxide nanofibers (4) impregnating said titanium dioxide nanofibers with inorganic or organic precursor of high work function material, or with inorganic or organic precursor of p-type semiconductor followed by decomposition of the metal/semiconductor-compounds (precursors) to metal/semiconductor.
- This may be done at elevated temperatures (such as about 300 Q C) followed by reduction in H 2 to pure metal/semiconductor (such as PdO and/or at about 500 Q C).
- the impregnation may be wet impregnation.
- the decomposition of the metal precursor may be carried out in air.
- the nanofibers may contain alkali metal impurities.
- the method is carried out at the substantial absence of separate catalyst metal.
- the required amount of ammonia or other nitrogen-containing base is very low, generally less than 5%, such as about 2. In one embodiment the amount of am- monia or other nitrogen-containing base is in the range of 1 -50%, preferably 1 - 10%, e.g. 1 -5%.
- the high work function material or p-type semiconducting material may be any of the materials described herein.
- the titanate nanofibers are synthesized in alkaline solutions at 120-175 Q C.
- the inorganic or organic precursor of high work function material may be nitrate, chloride, acetylacetonate, acetate or hydrochloroacidic form of the mentioned metals.
- Precursors of the semiconducting materials may be organic complexes, hydrides. In case of oxide and sulfide semiconductors, the precursors can be metal salts/complexes that are reacted in oxidative environment or in the presence of sulfides.
- step (3) the hydrogen titanates and/or alkali metal hydrogen titanate are annealed in air to obtain titanium dioxide (Ti0 2 , anatase) nanofibers.
- step (3) the hydrogen titanates are annealed in air to obtain titanium dioxide (Ti0 2 , anatase) nanofibers prior annealing in ammonia to obtain nitrogen-doped titanium oxide (N-Ti0 2 ).
- the photocatalytic material of the invention is obtained by any of the methods described herein.
- the N-doped titanium dioxide nanofibers are further dispersed with liquids or cellulose fibers in liquids, the dispersion is applied to a surface and dried to obtain a photocatalyst material membrane, film or coating for instance by painting, lamination, spraying, spinning.
- the photocatalytic materials described herein may be used in applications wherein organic or inorganic molecules are photodegraded.
- Such molecules can be considered as contaminants and may include for example organic contaminants such as polychlorinated biphenyls (PCBs), microorganisms, and pesticides, fungicides, and insecticides.
- PCBs polychlorinated biphenyls
- microorganisms microorganisms
- pesticides fungicides
- insecticides insecticides
- organic contaminants include non-aromatic chlorinated hydrocarbons (chloromethane; tetrachloroethylene; dichloromethane; dich- loroethane; trichloromethane; 1 ,1 -dibromoethane; carbon tetrachloride; 1 ,2- dibromoethane; dibromomethane; ethylene dibromide; tribromomethane; monoch- loroacetic acid; trichloroethylene; and dichloroacetic acid); aromatic chlorinated hydrocarbons (PCBs; 1 ,2,4-trichlorobenzene; dioxins; 3,3-dichlorobiphenyl; chlo- robenzene; 2,4,5-trichlorophenoxyacetic acid; and 4,4'-DDT); aromatic and non- aromatic hydrocarbons (benzene; alkanes; toluene; alkenes; xylene; alkynes; and
- One embodiment of the present invention provides a method for removing organic contaminant from surfaces, air or water comprising contacting said surface, air or water with the photocatalyst material of the invention to degrade the contaminants.
- the organic compounds may be for example grease, oil, toxic moieties, typically on the surfaces, volatile organic compounds in the air or alcohols, phenolic compounds, hydrocarbons or fatty-acids, esters in water.
- the water may be any suitable water or aqueous liquid, such as waste water, industrial water, domestic water, or the like. "Removing" refers to any degree of reducing the amount of said contaminants by degrading the contaminant molecules. Generally the degradation is photodegradation.
- Another embodiment of the present invention provides a method for disinfecting surfaces, air or water comprising contacting the air or the water with the photocatalyst material of the invention to kill microorganisms present on the surface, such as bacteria, yeast, fungi, viruses and the like.
- Still another embodiment of the present invention provides a method for generat- ing H 2 fuel gas from starting material, such as water, alcohol, alcohol/water mixture, or other organic compounds such as hydrocarbons or oxygen containing organic molecules, comprising contacting said starting material with the photocatalyst material of the invention to degrade said starting material to release H 2 gas.
- starting material such as water, alcohol, alcohol/water mixture, or other organic compounds such as hydrocarbons or oxygen containing organic molecules
- any hydrogen-containing molecule may be a potential source.
- UV light is applied in the catalytic reactions described herein, such as visible or UV light i.e. the methods described herein are carried out in the presence of light.
- UV light is used, for example at the wavelength in the range of 300-400 nm, such as UV-A or UV-B light (about 365 nm and 312 nm respective- ly). Examples
- anatase nanofibers (TiO 2 -NFs) are synthesized from acid treated sodium titanate nanofibers by calcination at 600 Q C and then used as support for Pt and Pd nanoparticles deposited by wet impregnation.
- Enhanced photocatalytic activity of the metal decorated TiO 2 nanofibers with or without alkali metal impurities has been demonstrated by (i) decomposing organic dyes in water, (ii) degrading organic stains on the surface of flexible freestanding composite catalyst films and by (iii) generating hydrogen from ethanol.
- the presented results are compared to corresponding catalyst materials based on commercial TiO 2 nanopar- ticle powders.
- examples of nitrogen-doped TiO 2 nanofibers for generating hydrogen from ethanol are demonstrated.
- Hydrogen titanate nanofibers and/or sodium hydrogen titanate nanofibers were prepared by suspending 20-30 g anatase in 1000 ml of 10-15 M NaOH aqueous solution followed by thermal treatment in a Teflon-lined autoclave at 120-175 Q C for 24-72 h applying 10-60 rpm revolving around its short axis. The product was then filtered and washed with deionized water and 0.1 M HCI aqueous solution then washed again with deionized water to reach pH ⁇ 7 and the absence of chloride, and finally dried in air at 70 Q C.
- TiO 2 anatase nanofibers TiO 2 - NFs
- the hydrogen titanate nanofibers were calcined at 600 Q C at a heating rate of 1 Q C/min for 12 h.
- Anchoring of Pt and Pd nanoparticles on TiO 2 -NFs was carried out by wet impregnation.
- Pt-TiC1 ⁇ 2- NFs and Pd-TiO 2 -NFs with ⁇ 1 w% metal load were made (Fig. 1 ) using the same routine as applied for the nanofibers. Nitrogen doping
- N-doped TiO 2 nanofibers were synthesized using different calcination methods of the titanate nanowires.
- One example is a direct doping by annealing in ammonia gas (e.g. at 600 Q C in N 2 buffer).
- Another route is, when the titanate is first annealed to obtain titania and then subsequently annealed in ammonia gas (e.g. at 600 Q C in N 2 buffer). Annealing in the presence of amines or other nitrogen- containing bases may be also applied for N-doping.
- Photocatalytic hydrogen generation tests were carried out using 1 :3 molar ratio mixture of ethanol and water (1 I) in which 0.2 g of Ti0 2 -based catalyst was sus- pended before each experiments. The temperature of the mixture was kept near the room temperature.
- 6 pieces of UVB lamps (Sankyo Denki, G15T8E, /max at ⁇ -313 nm, Puv ⁇ 3 W) were placed in a hexagonal arrangement around the reactor. In order to avoid sedimentation of the catalyst powders the reaction liquid was circulated by pumping. In addition, N 2 gas was bubbled through the reactor with 400 ml/min flow rate, serving also as a purging gas for the evolving gaseous products.
- the outlet of the reactor was connected to cold traps and to a molecular sieve (for condensing and removal the vapours of water and ethanol), and then to a hydrogen analyzer (General Electric, XMTC-6C-1 1 ).
- the illumination time was 60 minutes in each experiment.
- hydrogen production rates over Pt and Pd decorated Ti0 2 -NFs catalysts were tested with different irradiation powers.
- immobilized catalyst were also implemented.
- Each catalyst powder (25 mg) was mixed with 25 mg cellulose, then suspended in water and finally deposited on the surface of a filter 5 paper ( ⁇ 12 cm in diameter) by drop casting.
- the dried catalyst coated paper sheets were then folded to cylinders and fixed in the tube reactor to perform similar experiments as described above (Fig. 2).
- microstructure of composite films and diameter/structure of individual nanofi- bers and the decorating metal nanoparticles were studied by field-emission scanning electron microscopy (FESEM, Jeol JSM-6300F), by transmission electron microscopy combined with electron diffraction (EFTEM, LEO 912 OMEGA, 120 kV) as well as by X-ray diffraction (XRD, Siemens D5000 and Philips PW 1380, both using Cu Ka radiation).
- FESEM field-emission scanning electron microscopy
- EFTEM electron diffraction
- XRD X-ray diffraction
- the as-made anatase nanofibers with sodium impurities are having length of up to a few micrometers and diameter of -50 nm (Figure 4).
- Decoration of anatase Ti0 2 nanofibers were obtained by wet impregnation with metal-acetylacetonates followed by decomposition in air at 300 Q C and reduction in hydrogen at 500 Q C.
- the weak and broadened XRD reflections found at 2 ⁇ ⁇ 40 Q for both Pt and Pd-based catalyst are assigned to metallic Pd(1 1 1 ) and Pt(1 1 1 ) and suggest very small size nanoparticles (Figure 5).
- the Pt and Pd nanoparticles are homogeneously distributed on the surface of Ti0 2 nanofibers and show uniform size distribution with average particle diameters of 2.3 ⁇ 0.5 nm and 3.8 ⁇ 1 .1 nm, respectively.
- the photocatalytic activities of the synthesized Ti0 2 -based materials were tested by UV light-induced photodegradation of methyl orange in aqueous solutions.
- metals such as Au, Pt and Pd attached on Ti0 2 nanoparticles have been confirmed to help achieving better activity for the catalyst due to the rectifying Schottky barrier forming at the interface between metal nanoparticles and Ti0 2 .
- the barrier heights are 1 .8 eV and 1 .2 eV, respectively. Photogeneration of electrons and holes takes place by the absorption of high energy photons followed by charge separation.
- a letter "A” is written on each cellulose- catalyst composite film, then the membranes were exposed to UV light (Philips, HPR 125 W) for 48 hours.
- the composite membranes consisting of only cellulose and Ti0 2 or Ti0 2 -NFs show only minor change in the intensity of the color pattern, whereas, the other films in which also Pd and Pt nanoparticles are present degrade the deposited ink considerably.
- the original stain hardly can be seen, i.e. fading of the dye is practically complete.
- the cellulose microfibers are uniformly coated with the catalyst materials as shown in Figure 9.
- the composites are flexible and can be folded until a curvature radius of ⁇ 5 mm (when the membrane buckles and then breaks).
- the composites with Ti0 2 nanoparticles are significantly softer than those made of the nanofibers.
- the difference in stiffness is unexpected since the typical dimensions of the cellulose fibers (length hundreds of micrometers and diameter between 10 and 25 ⁇ ) are about 3 orders of magnitude larger than those for the Ti0 2 -based nanofibers (length of a few micrometers, and diameter between 20 and 60 nm), which rules out a conventional mechanical tangling.
- the presence of Ti0 2 with the different shapes in the different types of catalyst materials can influence mechanical friction and sticking of adjacent cellulose fibers coated with the nanoparticles, thus affecting flexibility.
- Ti0 2 nanofibers decorated either with Pt or Pd nanoparticles show excellent pho- tocatalytic behavior as demonstrated in decomposing organic dyes in water, degrading organic stains on the surface of flexible freestanding cellulose/catalyst composite films and in generating hydrogen from ethanol using both suspended and immobilized catalysts.
- the performance of the nanofiber-based catalyst materials competes with - and in some cases outperforms - their conventional nano- particle-based counterparts.
- Pd decorated Ti0 2 nanoparticles and nanofibers proved to be more efficient than their Pt-based counterparts making the Pd-based catalysts industrially relevant especially if we consider the lower cost of Pd metal (approximately 20-25% of Pt metal).
- non-doped nanofibers may also be applied to any nitrogen-doped nanofibers described herein.
- Wu et al. disclose the synthesis of the present nitrogen-doped Ti0 2 nanofibers (N-Ti0 2 NFs) and their metal (Pt and Pd) decorated derivatives, and demonstrate ultra-efficient H 2 generation from water- ethanol mixtures under UV-A and UV-B irradiation.
- Sodium titanate (Na 2 Ti y 0 2 y + i) nanofibers were synthesized through the hydrother- mal synthesis route from anatase Ti0 2 in aqueous NaOH solution (10 M) at 175 Q C for 24 h using a rotating autoclave applying 120 rpm revolving around its short axis. Washing of Na 2 Ti y 0 2y+ i in 0.1 M HCI was applied to exchange Na + ions to protons in the nanofibers. Finally, the product was washed with deionized water to reach pH ⁇ 7 and finally filtered and dried in air at 70 Q C.
- N-Ti0 2 (A) NF Two kinds of nitrogen-doped Ti0 2 nanofibers, referred as N-Ti0 2 (A) NF and N- Ti0 2 (B) NF, were synthesized using different calcination methods.
- N-Ti0 2 (A) NF was synthesized by the calcination of H 2- xNa x Ti y 0 2 y + i nanofibers at 600 Q C in ammonia gas flow (50 ml/min, 2% NH 3 in N 2 buffer) for 15 h.
- N-Ti0 2 (B) NF was synthesized also from H 2- xNa x Ti y 0 2 y + i nanofibers but in two subsequent calcination steps: first calcined in air at 600 Q C for 12 h to form Ti0 2 anatase nanofibers, followed by a second calcination step in ammonia gas (50 ml/min, 2% NH 3 in N 2 buf- fer) at the same temperature for 3 h.
- the Na/Ti atomic ratios of the two products were -30.4% in N-Ti0 2 (A) NF and -25.5% in N-Ti0 2 (B) NF.
- N-Ti0 2 (A) NF and N-Ti0 2 (B) NF were used as support for Pt and Pd nanoparticles deposited by wet impregnation.
- 20.4 mg of pla- tinum(ll) acetyl aceton ate (Aldrich, 99.99%) or 29.2 mg of palladium(ll) acetylace- tonate (Aldrich, 99%) was dissolved in 100 ml of acetone and mixed with 1 .0 g of N-Ti0 2 NF by ultrasonic agitation for 3 h and stirring for 6 h.
- the microstructure of diameter/structure of individual nanofibers (N-Ti0 2 (A) NF and N-Ti0 2 (B) NF) and the decorating metal nanoparticles (N-Ti0 2 (A)-Pd NF, N- Ti0 2 (A)-Pt NF, N-Ti0 2 (B)-Pd NF, and N-Ti0 2 (B)-Pt NF) were studied by transmis- sion electron microscopy (EFTEM, LEO 912 OMEGA, 120 kV) as well as by X-ray diffraction (XRD, Siemens D5000 and Philips PW 1380, both using Cu KR radiation).
- EFTEM transmis- sion electron microscopy
- XRD X-ray diffraction
- the ⁇ -potential of the catalysts was determined from their electrophoretic mobility using a ⁇ -potential analyzer, 90Plus/BI-MAS (Brookhaven Instruments Corporation). The velocity of the particles was measured by laser Doppler velocimetry. The analysis of chemical composition and oxidation state was carried out by X-ray photoelectron spectroscopy (XPS, Kratos Axis Ultra DLD, mono Al KR source, analysis area of 0.3x0.7 mm 2 , applying charge neutralizer).
- XPS X-ray photoelectron spectroscopy
- Photocatalytic H 2 generation tests were carried out using 1 :3 molar ratio mixture of ethanol and water (1 I) in which 100 mg of TiO 2 -based catalyst was suspended before each experiments. The temperature of the mixture was kept near the room temperature.
- UV-A lamps Philips Actinic BL 15W/10 SLV, the wavelength of maximum emission of UV-A lamp was at ⁇ 365 nm and the power in the UV range was ⁇ 3.15 W
- six pieces of UV-B lamps (Sankyo Denki G15T8E UV-B lamps, the wavelength of maximum emission of UV-B lamp was -312 nm, and the power in UV range was 3.0 W) were placed in a hexagonal arrangement around the reactor.
- N-Ti0 2 (A) NF Two kinds of nitrogen-doped Ti0 2 nanofibers, referred as N-Ti0 2 (A) NF and N- Ti0 2 (B) NF, were synthesized using different calcination methods.
- N-Ti0 2 (A) NF is synthesized by the calcination of H 2- xNa x Ti y 0 2 y + i nanofibers at 600 Q C in ammonia gas flow (50 ml/min, 2% NH 3 in N 2 buffer) for 15 hours.
- N-Ti0 2 (B) NF is synthesized also from H 2- xNa x Ti y 0 2 y + i nanofibers but in two subsequent calcination steps: first, calcined in air at 600 Q C for 12 hours to form Ti0 2 anatase nanofibers, followed by a second calcination step in ammonia gas (50 ml/min, 2% NH 3 in N 2 buf- fer) at the same temperature for 3 hours.
- the two different high-temperature treatments in NH 3 result in nitrogen doping of the raw materials as calculated from N 1 s XPS spectra (see Table 1 in Wu et al. 201 1 ).
- the N 1 s component at 397.8 eV of N-Ti0 2 (A) NF can be assigned to interstitial nitrogen atoms (N/Ti ratio of 0.01 1 1 ), while the peak at 396.3 eV of N-Ti0 2 (B) NF is due to substitutional nitrogen (formed Ti-N bond, N/Ti ratio of 0.0021 ).
- the other components with higher binding energies (>399.0 eV) detected for each sample correspond to decomposition products of NH 3 molecules and/or other surface contamination.
- the difference in the N/Ti atomic ratios measured for the interstitial and substitutional nitrogen is reasonable considering the different synthesis condition. It is important to point out that a significant amount of sodium ions (Na atom concentration: 8.54 at %) was found in the samples probably due to limited ion exchange in the interior of the initial sodium titanate (Na x Ti y 0 2y+ i) nanofibers. The presence of Na + ions on the surface may influence water molecule adsorption and lead to pH change at the catalyst/aqueous solution interface, thus changing electrochemical potentials in water splitting reactions, and can also be an additional source of charge carriers enhancing or inhibiting photochemical excitation effect.
- the XPS results on the N content of the samples are consistent with the HR-TEM analysis because the considerable amount of interstitial N atoms may indeed contribute to the expansion of the lattice.
- the average ⁇ -potentials of original Ti0 2 NF, N-Ti0 2 (A) NF, and N-Ti0 2 (B) NF measured on powders dispersed in ethanol are -10.14, -18.02, and -16.32 mV, respectively.
- the somewhat lower potential values (calculated with the Henry equ- ation from the electrophoretic mobility) for the N-doped samples compared to the original Ti0 2 NFs suggests slight accumulation of additional negative charge on the surface as a consequence of nitrogen doping.
- the as-prepared N-doped Ti0 2 nanofibers were finally decorated with Pt and Pd nanoparticles (1 w% each sample) by wet impregnation with Pt- and Pd- acetyla- cetonate in acetone followed by drying, thermal decomposition in air at 300 Q C for 2 hours and reduction in H 2 flow at 500 Q C for 4 hours (for details see Supporting Information).
- the anatase crystalline structure is left intact during the metal nanopar- ticle deposition step as verified by X-ray diffraction.
- the weak and broadened reflections of the Pd (1 1 1 ) and Pt (1 1 1 ) at 2 ⁇ -40.0 5 and the Pt (200) at 2 ⁇ -46.5 5 indicate the presence of small metal particles in the samples.
- the average size of Pt nanoparticles is considerably smaller than that measured for Pd on both types of supporting surfaces (1 .4 ⁇ 0.3 nm on N- Ti0 2 (A) and 1 .9 ⁇ 0.3 nm N-Ti0 2 (B) for Pt; and 4.7 ⁇ 1 .4 nm on N-Ti0 2 (A) and 5.9 ⁇ 1 .2 nm on N-Ti0 2 (B) NF for Pd).
- the particle size is determined by several factors as decomposition of the noble metal source compounds, seed formation rates, and diffusion properties.
- the rates of H 2 evolution were found to be around 330 ⁇ / ⁇ for N- Ti0 2 (A)-Pd NF, 330 ⁇ /h for N-TiC1 ⁇ 2(A)-Pt NF, 250 ⁇ /h for N-Ti0 2 (B)-Pd NF, and 700 pmol/h for N-Ti0 2 (B)-Pt NF, while only 50 pmol/h for N-Ti0 2 (A) NF and 30 ⁇ /h for N-Ti0 2 (B) NF.
- the hydrogen production rate normalized to the total catalyst mass is 3300 ⁇ /gh for N- Ti0 2 (A)-Pd NF, 3300 pmol/gh for N-TiC1 ⁇ 2(A)-Pt NF, 2500 pmol/gh for N-Ti0 2 (B)-Pd NF, and 7000 pmol/gh for N-Ti0 2 (B)-Pt NF, while only 500 pmol/gh for N-Ti0 2 (A) NF and 300 ⁇ /gh for N-Ti0 2 (B) NF.
- N-Ti0 2 (A) NF performs better than N- Ti0 2 (B) NF.
- the metal-decorated samples seem to perform quite similarly except N-Ti0 2 (B)-Pt NF, which produces almost twice as much hydrogen as the other metal-decorated catalysts. This difference is not thoroughly understood; however, a direct electron transition from the p-states to any empty states of the Pt nanopar- ticle might give a reasonable explanation as such transitions should be more fa- vored energetically than the ones from the valence band and/or the p-states to the conduction band of the semiconductor followed by a subsequent transition to the metal.
- Pt-decorated samples have advantages over the Pd- decorated ones derived from the smaller particle size and accordingly higher dispersion value of the catalyst particles.
- the turnover frequency values were calculated (see Supporting Information of Wu et al. 201 1 ) and higher ones for Pt in three of the four cases were found.
- the product rate/amount of catalyst values for comparing different methods was used, and this value has the practical advantage to lead easily to product amount/cost of catalyst calculations.
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Materials Engineering (AREA)
- Health & Medical Sciences (AREA)
- Inorganic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- General Health & Medical Sciences (AREA)
- Veterinary Medicine (AREA)
- Animal Behavior & Ethology (AREA)
- Epidemiology (AREA)
- Public Health (AREA)
- Combustion & Propulsion (AREA)
- General Chemical & Material Sciences (AREA)
- Medicinal Chemistry (AREA)
- Environmental & Geological Engineering (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Geology (AREA)
- Catalysts (AREA)
Abstract
Description
Claims
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| FI20106086A FI20106086A0 (en) | 2010-10-21 | 2010-10-21 | PHOTOCATALYTICAL MATERIAL |
| PCT/FI2011/050925 WO2012052624A1 (en) | 2010-10-21 | 2011-10-21 | Photocatalytic material |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| EP2630086A1 true EP2630086A1 (en) | 2013-08-28 |
| EP2630086A4 EP2630086A4 (en) | 2014-09-17 |
Family
ID=43064244
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| EP11833926.6A Withdrawn EP2630086A4 (en) | 2010-10-21 | 2011-10-21 | PHOTO-CATALYTIC MATERIAL |
Country Status (3)
| Country | Link |
|---|---|
| EP (1) | EP2630086A4 (en) |
| FI (1) | FI20106086A0 (en) |
| WO (1) | WO2012052624A1 (en) |
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107159262A (en) * | 2017-06-23 | 2017-09-15 | 江汉大学 | Room temperature removes formaldehyde gas Pd/CuxThe preparation method of O@GO composite catalysts |
| CN109647511A (en) * | 2019-01-21 | 2019-04-19 | 南京融众环境工程研究院有限公司 | A method of catalysis light degradation sewage |
| CN109772410A (en) * | 2019-02-21 | 2019-05-21 | 西南大学 | A kind of high-efficiency iridium-based bifunctional catalyst for electrolysis of water and its preparation method and application |
| CN109939732A (en) * | 2019-03-26 | 2019-06-28 | 中国科学院化学研究所 | Application of the semiconductor composite of fullerene derivate modification in formaldehyde degradation by photocatalytic oxidation process |
| CN110354906A (en) * | 2019-08-27 | 2019-10-22 | 合肥学院 | A kind of Cu2O/ chitin composite membrane and preparation method thereof |
| WO2020177485A1 (en) * | 2019-03-05 | 2020-09-10 | 华南理工大学 | Nano silver particle/cellulosic fiber composite material and preparation method |
| CN107746041B (en) * | 2017-09-28 | 2021-01-29 | 合肥师范学院 | Ternary metal hybrid PtNiTe porous magnetic nanowire and preparation and application thereof |
| CN113247942A (en) * | 2021-05-13 | 2021-08-13 | 贵州理工学院 | Preparation method and application of nano copper oxide |
| CN121222467A (en) * | 2025-12-03 | 2025-12-30 | 内蒙古工业大学 | Titanium-doped biochar, its preparation method and application |
Families Citing this family (31)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103111276A (en) * | 2013-01-17 | 2013-05-22 | 河南科技大学 | Preparation Method of Porous Array ZnO/TiO2 Composite Photocatalyst |
| CN103316673B (en) * | 2013-06-27 | 2015-07-08 | 中国空间技术研究院 | Silver-carbon co-doped bicrystalline mesoporous titanium dioxide visible light photocatalyst and preparation method thereof |
| CN103331159B (en) * | 2013-07-10 | 2015-01-21 | 中南大学 | A kind of Cu2O-TiO2/reduced graphene ternary compound and its preparation method and application |
| GB201318846D0 (en) * | 2013-10-24 | 2013-12-11 | Univ London Queen Mary | Photocatalysts |
| CN104043470B (en) * | 2014-05-28 | 2016-04-13 | 华中科技大学 | A kind of preparation method of nano titanium dioxide photocatalyst of energy degrading high concentration benzene |
| CN104001535B (en) * | 2014-06-04 | 2015-04-01 | 齐鲁工业大学 | Preparation method of photocatalyst for recycling sewage sulfur |
| WO2016005855A1 (en) * | 2014-07-10 | 2016-01-14 | Sabic Global Technologies B.V. | Photocatalytic hydrogen production from water over mixed phase titanium dioxide nanoparticles |
| CN104174421B (en) * | 2014-08-08 | 2016-04-13 | 浙江大学 | A kind of heterogeneous catalyst for fragrant nitro compound selective hydrogenation and application thereof |
| US20170274364A1 (en) | 2014-08-29 | 2017-09-28 | Sabic Global Technologies B.V. | Photocatalytic hydrogen production from water over catalysts having p-n junctions and plasmonic materials |
| CN104888777A (en) * | 2015-04-09 | 2015-09-09 | 南京大学 | A preparation method of attapulgite clay-TiO2-Cu2O composite visible light catalyst |
| CN104923216B (en) * | 2015-06-25 | 2017-05-10 | 青岛科技大学 | Precious metal loaded TiO2 nanorod photocatalyst preparation method |
| KR101790291B1 (en) | 2016-04-26 | 2017-10-26 | 울산과학기술원 | Precursor of catalyst for hydrogenation reaction of co2, method for manufacturing the same, catalyst for hydrogenation reaction of co2, and method for manufacturing the same |
| CN106732737A (en) * | 2017-01-25 | 2017-05-31 | 邵阳学院 | P n junction type composite photo-catalysts and preparation method thereof |
| WO2018159869A1 (en) | 2017-02-28 | 2018-09-07 | 울산과학기술원 | Precursor of catalyst for hydrogenation of carbon dioxide and manufacturing method therefor, and hydrogenation catalyst of carbon dioxide and manufacturing method therefor |
| KR101912298B1 (en) * | 2017-02-28 | 2018-10-26 | 울산과학기술원 | Precursor of catalyst for hydrogenation reaction of co2, method for manufacturing the same, catalyst for hydrogenation reaction of co2, and method for manufacturing the same |
| WO2018223054A1 (en) | 2017-06-01 | 2018-12-06 | University Of Connecticut | Manganese-cobalt spinel oxide nanowire arrays |
| US11691123B2 (en) | 2017-06-02 | 2023-07-04 | University Of Connecticut | Low-temperature diesel oxidation catalysts using TiO2 nanowire arrays integrated on a monolithic substrate |
| US11465129B2 (en) | 2017-06-06 | 2022-10-11 | University Of Connecticut | Microwave assisted and low-temperature fabrication of nanowire arrays on scalable 2D and 3D substrates |
| CN107670495A (en) * | 2017-09-29 | 2018-02-09 | 常州市隆圣石墨烯科技有限公司 | A kind of graphene quantum energy material and preparation method thereof |
| CN108499575B (en) * | 2018-03-01 | 2020-07-14 | 中南大学 | A kind of preparation method of copper sulfide-titanium dioxide nanocomposite |
| CN108311132A (en) * | 2018-03-06 | 2018-07-24 | 绍兴文理学院 | A kind of preparation method of visible light ternary photochemical catalyst |
| CN108554416B (en) * | 2018-03-29 | 2021-03-19 | 上海化工研究院有限公司 | A kind of modified cobalt-based catalyst and its preparation method and application |
| US11577224B2 (en) * | 2018-05-01 | 2023-02-14 | Hamilton Sundstrand Corporation | Gas treatment method and materials |
| CN108906131A (en) * | 2018-06-29 | 2018-11-30 | 佛山腾鲤新能源科技有限公司 | A kind of preparation method of composite photocatalyst material |
| CN110560106A (en) * | 2019-09-27 | 2019-12-13 | 南京工业大学 | Preparation method of bismuth phosphate-cadmium sulfide nanorod composite visible-light-driven photocatalyst |
| CN111389365B (en) * | 2020-04-16 | 2022-11-25 | 郑州大学 | Carbon nanotube/titanium dioxide composite film and preparation method and application thereof |
| CN113578384B (en) * | 2021-08-19 | 2023-07-18 | 江苏大学 | Preparation method and application of a kind of ectopic reaction Cr6+ ion imprinted photocatalytic film |
| CN114029045A (en) * | 2021-11-30 | 2022-02-11 | 河海大学 | Photocatalyst prepared by doping titanium dioxide with nano material and preparation method thereof |
| CN115957749B (en) * | 2023-01-16 | 2024-08-02 | 福州大学 | Platinum-loaded titanium dioxide composite photocatalyst, preparation method thereof, and application in degradation of harmful pollutants |
| CN116429838A (en) * | 2023-03-16 | 2023-07-14 | 西安交通大学 | Composite gas-sensing material based on light-assisted sensitization and its preparation method and gas sensor |
| CN116554914B (en) * | 2023-05-04 | 2024-06-07 | 重庆工商大学 | Application of modified CdSe QDs/B-SiO2 in photocatalytic preparation of fuel precursor and syngas from lignin oil and carbon dioxide |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20110039690A1 (en) * | 2004-02-02 | 2011-02-17 | Nanosys, Inc. | Porous substrates, articles, systems and compositions comprising nanofibers and methods of their use and production |
| US20120125781A1 (en) * | 2008-12-10 | 2012-05-24 | Zhang jin zhong | Compositions and methods for synthesis of hydrogen fuel |
| US20100213046A1 (en) * | 2009-01-06 | 2010-08-26 | The Penn State Research Foundation | Titania nanotube arrays, methods of manufacture, and photocatalytic conversion of carbon dioxide using same |
-
2010
- 2010-10-21 FI FI20106086A patent/FI20106086A0/en not_active Application Discontinuation
-
2011
- 2011-10-21 WO PCT/FI2011/050925 patent/WO2012052624A1/en not_active Ceased
- 2011-10-21 EP EP11833926.6A patent/EP2630086A4/en not_active Withdrawn
Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107159262A (en) * | 2017-06-23 | 2017-09-15 | 江汉大学 | Room temperature removes formaldehyde gas Pd/CuxThe preparation method of O@GO composite catalysts |
| CN107746041B (en) * | 2017-09-28 | 2021-01-29 | 合肥师范学院 | Ternary metal hybrid PtNiTe porous magnetic nanowire and preparation and application thereof |
| CN109647511A (en) * | 2019-01-21 | 2019-04-19 | 南京融众环境工程研究院有限公司 | A method of catalysis light degradation sewage |
| CN109772410A (en) * | 2019-02-21 | 2019-05-21 | 西南大学 | A kind of high-efficiency iridium-based bifunctional catalyst for electrolysis of water and its preparation method and application |
| CN109772410B (en) * | 2019-02-21 | 2021-11-09 | 西南大学 | High-efficiency iridium-based electrolytic water bifunctional catalyst and preparation method and application thereof |
| WO2020177485A1 (en) * | 2019-03-05 | 2020-09-10 | 华南理工大学 | Nano silver particle/cellulosic fiber composite material and preparation method |
| CN109939732A (en) * | 2019-03-26 | 2019-06-28 | 中国科学院化学研究所 | Application of the semiconductor composite of fullerene derivate modification in formaldehyde degradation by photocatalytic oxidation process |
| CN110354906A (en) * | 2019-08-27 | 2019-10-22 | 合肥学院 | A kind of Cu2O/ chitin composite membrane and preparation method thereof |
| CN113247942A (en) * | 2021-05-13 | 2021-08-13 | 贵州理工学院 | Preparation method and application of nano copper oxide |
| CN113247942B (en) * | 2021-05-13 | 2022-04-26 | 贵州理工学院 | Preparation method and application of nano copper oxide |
| CN121222467A (en) * | 2025-12-03 | 2025-12-30 | 内蒙古工业大学 | Titanium-doped biochar, its preparation method and application |
Also Published As
| Publication number | Publication date |
|---|---|
| EP2630086A4 (en) | 2014-09-17 |
| WO2012052624A1 (en) | 2012-04-26 |
| FI20106086A0 (en) | 2010-10-21 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| WO2012052624A1 (en) | Photocatalytic material | |
| Wu et al. | Nitrogen-doped anatase nanofibers decorated with noble metal nanoparticles for photocatalytic production of hydrogen | |
| Chen et al. | Enhanced visible-light photoactivity of CuWO4 through a surface-deposited CuO | |
| Xing et al. | Novel ternary MoS2/C-ZnO composite with efficient performance in photocatalytic NH3 synthesis under simulated sunlight | |
| Etacheri et al. | Highly visible light active TiO2− x N x heterojunction photocatalysts | |
| Kandiel et al. | Direct synthesis of photocatalytically active rutile TiO2 nanorods partly decorated with anatase nanoparticles | |
| Wei et al. | Mesoporous TiO2/g-C3N4 microspheres with enhanced visible-light photocatalytic activity | |
| Kumar et al. | Perovskite-structured CaTiO3 coupled with g-C3N4 as a heterojunction photocatalyst for organic pollutant degradation | |
| Zhou et al. | Heterojunction of g-C3N4/BiOI immobilized on flexible electrospun polyacrylonitrile nanofibers: facile preparation and enhanced visible photocatalytic activity for floating photocatalysis | |
| Sheng et al. | Generation of H2O2 and OH radicals on Bi2WO6 for phenol degradation under visible light | |
| Van Tuan et al. | In-situ hydrothermal fabrication and photocatalytic behavior of ZnO/reduced graphene oxide nanocomposites with varying graphene oxide concentrations | |
| Yu et al. | Synthesis of natural cellulose-templated TiO2/Ag nanosponge composites and photocatalytic properties | |
| Shanmugam et al. | Synthesis and characterization of TiO2@ C core− shell composite nanoparticles and evaluation of their photocatalytic activities | |
| Zhang et al. | Hybrid 0D–2D nanoheterostructures: in situ growth of amorphous silver silicates dots on g-C3N4 nanosheets for full-spectrum photocatalysis | |
| Tan et al. | Noble metal modified reduced graphene oxide/TiO2 ternary nanostructures for efficient visible-light-driven photoreduction of carbon dioxide into methane | |
| Li et al. | Photocatalytic degradation of rhodamine B over Pb3Nb4O13/fumed SiO2 composite under visible light irradiation | |
| Li et al. | High-efficient degradation of dyes by Zn x Cd1− x S solid solutions under visible light irradiation | |
| Zhang et al. | Dramatic visible photocatalytic degradation performances due to synergetic effect of TiO2 with PANI | |
| Hollmann et al. | Structure–activity relationships in bulk polymeric and sol–gel-derived carbon nitrides during photocatalytic hydrogen production | |
| Chang et al. | Novel mesoporous graphite carbon nitride/BiOI heterojunction for enhancing photocatalytic performance under visible-light irradiation | |
| Slamet et al. | Photocatalytic hydrogen production from glycerol–water mixture over Pt‐N‐TiO2 nanotube photocatalyst | |
| Wu et al. | Enhanced photocatalytic activity of TiO2 nanofibers and their flexible composite films: Decomposition of organic dyes and efficient H2 generation from ethanol-water mixtures | |
| Paramanik et al. | Stupendous photocatalytic activity of p-BiOI/n-PbTiO3 heterojunction: the significant role of oxygen vacancies and interface coupling | |
| Liu et al. | Construction of a novel Z-scheme heterojunction with molecular grafted carbon nitride nanosheets and V2O5 for highly efficient photocatalysis | |
| Dou et al. | Core–shell gC 3 N 4/Pt/TiO 2 nanowires for simultaneous photocatalytic H 2 evolution and RhB degradation under visible light irradiation |
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: 20130424 |
|
| AK | Designated contracting states |
Kind code of ref document: A1 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) | ||
| A4 | Supplementary search report drawn up and despatched |
Effective date: 20140820 |
|
| RIC1 | Information provided on ipc code assigned before grant |
Ipc: A61L 2/08 20060101ALI20140813BHEP Ipc: C01B 3/02 20060101ALI20140813BHEP Ipc: B01J 35/06 20060101ALI20140813BHEP Ipc: C01G 23/047 20060101AFI20140813BHEP |
|
| STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: EXAMINATION IS IN PROGRESS |
|
| 17Q | First examination report despatched |
Effective date: 20180309 |
|
| STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: THE APPLICATION IS DEEMED TO BE WITHDRAWN |
|
| 18D | Application deemed to be withdrawn |
Effective date: 20180523 |