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Небесная энциклопедия

Космические корабли и станции, автоматические КА и методы их проектирования, бортовые комплексы управления, системы и средства жизнеобеспечения, особенности технологии производства ракетно-космических систем

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Мониторинг СМИ

Мониторинг СМИ и социальных сетей. Сканирование интернета, новостных сайтов, специализированных контентных площадок на базе мессенджеров. Гибкие настройки фильтров и первоначальных источников.

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Поддерживает ввод нескольких поисковых фраз (по одной на строку). При поиске обеспечивает поддержку морфологии русского и английского языка
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Применить Всего найдено 10469. Отображено 100.
09-02-2012 дата публикации

Method for removing vinyl monomers from a gas stream

Номер: US20120035295A1
Принадлежит: Individual

A method for removing vinyl monomers from a gas stream comprises steps of: irradiating a photoactive-inorganic medium by a light emitting unit to activate the photoactive-inorganic medium; and pumping a gas stream including vinyl monomers to contact with the activated photoactive-inorganic medium to make the vinyl monomers in the gas stream to polymerize on the photoactive-inorganic medium to jointly form a polymeric nano-composite.

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30-08-2012 дата публикации

Method of coating catalyst on a substrate

Номер: US20120220450A1
Принадлежит: Corning Inc

A method of coating a substrate with a catalytically active material using a polymer latex is disclosed. A slurry of catalytically active material and water is prepared, the catalytically active material containing activated carbon, and a binder is prepared that contains a polymer latex having a glass transition temperature of 10 C to 30 C. The slurry is combined with the binder to form a mixture, which can then be applied to the substrate to achieve a mixture loading of 20 to 30 weight percent on the substrate. The latex polymer binders can bind a catalytically active platinum on activated carbon powder to a cordierite honeycomb while not interfering with its catalytic activity, such as for hydrogenation.

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04-10-2012 дата публикации

Methods For Coating Ceramic Catalyst Supports With Base Coatings And Ceramic Catalyst Supports Having Base Coatings

Номер: US20120252664A1
Принадлежит: Corning Inc

The disclosure relates to methods for coating ceramic catalyst supports with a base coating, said method comprising, in part, providing an aqueous mixture comprising at least one polyvinyl alcohol homopolymer and at least one blocked isocyanate crosslinker, and to ceramic catalyst supports having a base coating comprising at least one polyvinyl alcohol homopolymer and at least one blocked isocyanate crosslinker.

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10-01-2013 дата публикации

Gas deacidizing method using an absorbent solution with cos removal through hydrolysis

Номер: US20130009101A1
Автор: Jeremy Gazarian
Принадлежит: IFP Energies Nouvelles IFPEN

The method deacidifies a gas including H 2 S and CO 2 . The gas is subjected to an absorption to collect the CO 2 and the H 2 S in an absorber, then to conversion through hydrolysis of the COS to H 2 S and CO 2 in a reactor, and to a second absorption to collect the H 2 S and the CO 2 formed in the reactor. The absorbent solution is regenerated in regenerator. The regenerated absorbent solution is separated into two which are: a main stream supplying the absorber, and a remaining stream supplying the second absorption

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18-04-2013 дата публикации

TUNGSTEN OXIDE PHOTOCATALYST AND METHOD FOR PRODUCING THE SAME

Номер: US20130095998A1
Принадлежит: SHOWA DENKO K.K.

The present invention relates to a method for producing a tungsten oxide photocatalyst having titanium oxide and copper ion supported thereon, comprising dissolving urea in a solution in which copper-ion supporting tungsten oxide particles are uniformly dispersed in a titanium oxide sol, thermally decomposing the urea to thereby allow the titanium oxide to precipitate on the surface of copper ion-supporting tungsten oxide and to be supported thereon; and a tungsten oxide photocatalyst modified by both titanium oxide and copper ion obtained by the method, wherein the rate of change of diffuse reflectivity (at wavelength of 700 nm) is less than 3% before and after the irradiation of ultraviolet and the titanium oxide is supported on the tungsten oxide in an island shape of 1 to 100 nm in size. 1. A method for producing a tungsten oxide photocatalyst having titanium oxide and copper ion supported thereon , comprising dissolving urea in a solution in which copper-ion supporting tungsten oxide particles are uniformly dispersed in a titanium oxide sol , thermally decomposing the urea to thereby allow the titanium oxide to precipitate on the surface of copper ion-supporting tungsten oxide and to be supported thereon.2. The method for producing a tungsten oxide photocatalyst having titanium oxide and copper ion supported thereon as claimed in claim 1 , wherein the thermal decomposition of urea is performed at 60 to 95° C.3. The method for producing a tungsten oxide photocatalyst having titanium oxide and copper ion supported thereon as claimed in claim 1 , wherein urea is added in an amount of 5 to 20 parts by mass to 100 parts by mass of the copper ion-supporting tungsten oxide particles.4. The method for producing a tungsten oxide photocatalyst having titanium oxide and copper ion supported thereon as described in claim 1 , wherein the titanium oxide sol is a water dispersed titanium oxide sol produced by mixing an aqueous solution of titanium tetrachloride and hot water ...

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25-04-2013 дата публикации

Nano Mixed Metal Oxide Thin Film Photocatalyst Consisting Of Titanium, Indium and Tin

Номер: US20130102953A1
Принадлежит: HCL TECHNOLOGIES LTD.

The present invention relates to a novel photocatalyst comprising Nano mixed metal oxides of titanium, Indium and tin as a thin film with nano sized grains, method of its preparation and applications. The photocatalyst disclosed herein can be used in oxygenation of human/mammalian blood along with all other applications of photocatalysts. A photocatalytic oxygenator for the oxygenation derives oxygen from the water content of mammalian blood. The photocatalyst disclosed herein can also be used for effluent treatments along with all other applications associated with photocatalysts. 1. A photocatalyst comprising mixed metal oxides of titanium , Indium and tin as a thin film with nano sized grains.214-. (canceled)15. The photocatalyst as claimed in claim 1 , wherein the atomic percentage of constituents are about 3.58-4.80 Indium claim 1 , about 0.29-0.32 Tin claim 1 , and about 0.62-0.72 Titanium claim 1 , as measured by EDX measurements on the thin films claim 1 , along with oxygen.16. The photocatalyst as claimed in claim 1 , wherein the photocatalyst consists of tin doped indium oxide (ITO) and titanium dioxide (TiO)17. The photocatalyst as claimed in claim 1 , wherein the photo energy required is any single or a range of wavelengths in the spectrum of 255 nm-1100 nm.18. A method making a photocatalyst consisting of a Titanium claim 1 , Indium and Tin mixed metal oxide thin film with nano sized grains comprising depositing the metal oxides by DC magnetron sputtering on a substrate followed by annealing.19. The method as claimed in claim 18 , wherein the substrate is quartz claim 18 , synthetic silicon dioxide claim 18 , soda lime glass claim 18 , poly-carbonates claim 18 , poly imides or a polymer.20. The method as claimed in claim 19 , wherein the substrate is quartz or synthetic silicon dioxide.21. The method as claimed in claim 18 , wherein the depositing of the metal oxides is performed at a temperature in the range of 300K to 400 K.22. The method as claimed ...

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16-05-2013 дата публикации

SOLAR-ACTIVATED PHOTOCHEMICAL PURIFICATION OF FLUIDS

Номер: US20130118995A1
Принадлежит: UVCleaning Systems, Inc.

Disclosed herein are embodiments of a solar-activated photochemical fluid treatment system, some of which comprise a fluid vessel, a porous enclosure positioned inside of the fluid vessel, a porous enclosure positioned inside of the fluid vessel, a fiber substrate contained within the enclosure, and a semiconductor photocatalyst coupled to the fiber substrate. The fluid vessel can be configured to contain a fluid in contact with the photocatalyst such that the fluid treatment system, responsive to solar radiation applied to the photocatalyst and to the fluid in the vessel, induces photochemical modification of contaminants and living organisms in the fluid. Related methods are also disclosed. 1. A solar-activated photochemical fluid treatment system comprising:a fluid vessel having at least one opening and comprising an at least partially sunlight transmissive portion;at least one enclosure positioned inside of the fluid vessel, the enclosure comprising material that allows fluid and sunlight to pass into the enclosure;an at least partially sunlight-transmissive fiber substrate contained within the at least one enclosure; anda semiconductor photocatalyst coupled to the fiber substrate;wherein the fluid vessel is configured to contain a fluid such that, responsive to solar radiation passing through the at least partially sunlight transmissive portion of the fluid vessel and into the at least one enclosure and to the semiconductor photocatalyst, photochemical modification of contaminants and living organisms in the fluid occurs.2. The system of claim 1 , wherein the at least one enclosure comprises a porous bag that contains the fiber substrate and the photocatalyst and allows the fluid and solar radiation to pass into the porous bag.3. (canceled)4. (canceled)5. (canceled)6. (canceled)7. (canceled)8. (canceled)9. (canceled)10. (canceled)11. (canceled)12. (canceled)13. (canceled)14. (canceled)15. The system of claim 1 , wherein the at least one enclosure is not ...

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23-05-2013 дата публикации

SUSTAINED RELEASE MICROPARTICLES AND SUSTAINED RELEASE MICROPARTICLE-CONTAINING PREPARATIONS

Номер: US20130130910A1
Принадлежит:

[Problem] 121-. (canceled)22. Sustained release microparticles comprising a supported substance , microgranular form having a hollow structure and coating agent which is at least one member selected from the group consisting of thermosetting resins , characterized in that the microgranular form has an average particle size within a range from 20 to 300 μm.23. Sustained release microparticles according to claim 22 , which contain claim 22 , based on the weight of the sustained release microparticles claim 22 , from 0.1 to 95 wt % of the supported substance claim 22 , from 0.1 to 90 wt % of the microgranular form claim 22 , and from 0.1 to 60 wt % of the coating agent.24. Sustained release microparticles according to claim 22 , in which the microgranular form has a floating ratio on water of from 20 to 95% and water absorption of from 10 to 170%.25. Sustained release microparticles according to claim 22 , in which the microgranular form is of hollow glass microspheres.26. Sustained release microparticles according to claim 22 , in which the microgranular form is at least one member selected from the group consisting of foamed pearlite claim 22 , foamed glass claim 22 , fly ash and hollow microballoon.27. Sustained release microparticles according to claim 22 , in which the microgranular form has an average particle size within a range from 20 to 150 μm.28. Sustained release microparticles according to claim 22 , in which the microgranular form has an average particle size within a range from 20 to 80 μm.29. Sustained release microparticles according to claim 22 , in which the supported substance is at least one member selected from the group consisting of agrochemically active component claim 22 , coloring matter claim 22 , flavor and fragrance claim 22 , functional substance claim 22 , medicament claim 22 , fertilizer component claim 22 , enzyme and physiologically active substance.30. Sustained release microparticles according to claim 29 , in which the supported ...

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27-06-2013 дата публикации

AMMONIA OXIDATION CATALYSTS

Номер: US20130164494A1
Принадлежит: SUED-CHEMIE CATALYSTS ITALIA S.R.L.

Ammonia oxidation catalyst units comprising a pair of honeycomb-type blocks having interplaced between them a layer of a gas permeable material performing the function of radially mixing the gas flow, said blocks comprising an ammonia oxidation catalysts, and having height of less than 15 cm and the interplaced layer height of 3 to 0.5 cm. 1. A catalyst for ammonia oxidation formed of one or more catalytic units each of which formed of a pair of blocks having a honeycomb structure containing tubular passages not interconnected through bores , comprising an ammonia oxidation catalyst , each of said blocks having height of less than 15 cm and more than 2 cm and interplaced between them a foamed layer having a height of not more than 3 cm and at least of 0.5 cm , formed of foamed material having open , randomly connected cells.2. The catalyst according to claim 1 , wherein the interplaced foamed layer has a height of 0.5-2 cm.3. The catalyst according to claim 1 , wherein the height of each of the blocks is from 2 to 6 cm.4. The catalyst according to claim 1 , wherein the density of the cells of the foamed layer ranges from 3 to 10 cells/cm.5. The catalyst according to claim 1 , wherein the blocks are formed of ceramic or metallic material.6. The catalyst according to claim 1 , wherein the blocks have a number of cells per cm claim 1 , which can be the same or different claim 1 , from 3 to 10 and wherein the number of pores per cm of the foamed layer is 4 to 20.7. The catalyst according to claim 1 , wherein the foamed layer is formed of foamed alumina. This application is a continuation of U.S. patent application Ser. No. 12/640,266, filed Dec. 17, 2009, the entire content and disclosure of which is incorporated herein by reference.The present invention relates to an ammonia oxidation catalyst unit formed of a pair of honeycomb-type blocks comprising an ammonia oxidation catalyst and having interplaced between them a layer of foamed material.For many years, the ...

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18-07-2013 дата публикации

PHOTOCATALYST WITH ENHANCED STABILITY FOR HYDROGEN PRODUCTION AND OXIDATIVE REACTIONS

Номер: US20130180861A1
Принадлежит: NORTHEASTERN UNIVERSITY

A Ti0-based photocatalyst is fabricated as a composite of titania with adhered nanostructures which contain a non-noble metal in galvanic contact with a noble metal. The catalyst effectively overcome aging and/or deactivation effects observed in a system free of the non-noble metal. The composite material showed a corrosion protective effect on the photoactivity of fresh catalyst for over 180-240 days, and it enhanced the rate of the water reduction reaction relative to bare Ti0. Variations in porosity and non-noble metal content of the alloy portion of the nanostructures influenced the performance of the catalyst composite. The protective effect of the non-noble metal is through a cathodic corrosion protection mechanism. 1. A photocatalyst comprising a TiOmaterial in surface contact with a plurality of nanostructures , the nanostructures comprising a noble metal in galvanic contact with a non-noble metal , wherein the noble metal is in galvanic contact with said TiOmaterial and acts as an electron trap during a photocatalytic redox reaction , and wherein the non-noble metal maintains the noble metal in a reduced state.2. The photocatalyst of claim 1 , wherein the noble metal is selected from the group consisting of Au claim 1 , Ag claim 1 , Pt claim 1 , and mixtures thereof.3. The photocatalyst of claim 1 , wherein the non-noble metal is selected from the group consisting of Fe claim 1 , Co claim 1 , and mixtures thereof.4. The photocatalyst of claim 1 , wherein the noble metal is Au and the non-noble metal is Fe.5. The photocatalyst of claim 1 , wherein the nanostructures are in the form of nanowires claim 1 , nanoparticles claim 1 , nanoclusters claim 1 , or nanocrystals.6. The photocatalyst of claim 1 , wherein the TiOmaterial comprises TiOin the crystalline anatase or rutile form.7. The photocatalyst of claim 1 , wherein the TiOmaterial comprises TiOparticles deposited onto a substrate claim 1 , the substrate comprising indium tin oxide or stainless steel.8. ...

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26-09-2013 дата публикации

DEVICE AND METHOD FOR PROCESSING CEMENT KILN COMBUSTION EXHAUST GAS

Номер: US20130251599A1
Принадлежит:

A combustion exhaust gas processing device comprises: a dust collector collecting dust in a cement kiln combustion exhaust gas; a wet dust collector as a catalyst-poisoning-substance stripper removing a catalyst-poisoning substance from a combustion exhaust gas which passed the dust collector, preheaters heating beforehand a combustion exhaust gas which passed the wet dust collector; and a catalyst device from which NOx, a persistent organic pollutant, etc. in the preheated combustion exhaust gas, are removed. A titanium-vanadium catalyst etc. as an oxide catalyst is used upstream of the catalyst device, and a platinum catalyst etc. as a noble-metal catalyst downstream of the catalyst device. The temperature of the combustion exhaust gas after the catalyst-poisoning substance is removed is increased up to 140° C. or more with the preheaters to prevent decline in denitration efficiency of and the decomposition efficiency of a volatile organic compound. 1. A device for processing cement kiln combustion exhaust gas comprising:a dust collector configured to collect dust in cement kiln combustion exhaust gas;a catalyst-poisoning-substance stripper configured to remove a catalyst-poisoning substance and mercury from the cement kiln combustion exhaust gas that passed said dust collector by adding sodium hypochlorite to said cement kiln combustion exhaust gas;a preheater configured to heat beforehand the cement kiln combustion exhaust gas that passed said catalyst-poisoning-substance stripper;a catalyst device configured to remove at least one member selected from the group consisting of a volatile organic compound, carbon monoxide, a persistent organic pollutant, hydrocarbon and an offensive odor substance in the cement kiln combustion exhaust gas preheated by said preheater; anda mercury adsorbing tower which adsorbs mercury in fluid exhausted from the catalyst-poisoning substance stripper, the mercury adsorbing tower producing wastewater, wherein a portion of the ...

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10-10-2013 дата публикации

CATALYST CERAMIC SUPPORT HAVING A CONTROLLED MICROSTRUCTURE

Номер: US20130266802A1
Принадлежит:

The invention relates to a catalyst support made of a ceramic, the support comprising an arrangement of crystallites having the same size, the same isodiametric morphology and the same chemical composition or substantially the same size, the same isodiametric morphology and the same chemical composition, in which each crystallite makes point contact or almost point contact with the surrounding crystallites. 114-. (canceled)15. A ceramic catalyst support comprising an arrangement of crystallites of equal size , equal isodiametric morphology , and equal chemical composition , or of substantially equal size , equal isodiametric morphology and equal chemical composition , in which each crystallite is in point or quasi-point contact with surrounding crystallites.16. The ceramic catalyst support of claim 15 , wherein the arrangement of crystallites is a face-centered cubic or hexagonal close-packed stack in which each crystallite is in point or quasi-point contact with not more than 12 other crystallites in a 3-dimensional space.17. The ceramic catalyst support of claim 15 , wherein said arrangement is in spinel phase.18. The ceramic catalyst support of claim 15 , wherein the crystallites are substantially spherical in shape.19. The ceramic catalyst support of claim 18 , wherein the crystallites have a mean equivalent diameter of between 5 and 15 nm claim 18 , preferably between 11 and 14 nm.20. The ceramic catalyst support of claim 15 , wherein said support comprises a substrate and a film on the surface of said substrate comprising said arrangement of crystallites.21. The ceramic catalyst support of claim 15 , wherein said support comprises granules comprising said arrangement of crystallites.22. The ceramic catalyst support of claim 21 , wherein the granules are substantially spherical in shape.23. The method for synthesizing a ceramic catalyst support of claim 20 , comprising the following steps:a) preparing a sol comprising magnesium nitrate and aluminum nitrate ...

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31-10-2013 дата публикации

THREE-WAY CATALYST HAVING AN UPSTREAM SINGLE-LAYER CATALYST

Номер: US20130287660A1
Принадлежит: UMICORE AG & CO. KG

Disclosed herein is a layered three-way catalytic system being separated in a front and a rear portion having the capability of simultaneously catalyzing the oxidation of hydrocarbons and carbon monoxide and the reduction of nitrogen oxides. Provided is a catalyst composite comprising a single front catalytic layer and two rear catalytic layers in conjunction with a substrate, where the single font layer and the rear bottom layer comprise a Pd component, the rear top layer comprises a Rh component, and the rear bottom layer is substantially free of an oxygen storage component (OSC). 1. A catalyst composite for the purification of exhaust gases of a combustion engine substantially running under stoichiometric conditions comprising in sequence and in order:a front single catalytic layer on a substrate; and{'sup': st', 'nd, 'a rear double layer on a substrate having a 1(lower) catalytic layer and a 2(upper) catalytic layer;'}{'sup': 'nd', 'wherein the 2catalytic layer comprises rhodium as a platinum group metal; and'}{'sup': 'st', 'wherein the front single catalytic layer and the 1catalytic layer comprise palladium as a platinum group metal compound;'}{'sup': 'st', 'wherein the 1catalytic layer is substantially free of an oxygen storage component (OSC); and'}wherein the front single catalytic layer forms a front zone and the rear double layer forms a rear zone where the catalyst composite is a single-brick system or the front single catalytic layer is located in a front brick and the rear double layer is located in a rear brick where the catalyst composite is a multi-brick system.2. The catalyst composite according to claim 1 , wherein the 1catalytic layer comprises less than 1% of an oxygen storage component (OSC) by weight of the layer.3. The catalyst composite according to claim 1 , wherein the PGM content of the layers are as follows:front single catalytic layer—0.01-12.0% by weight of the layer;{'sup': 'st', '1catalytic layer—0.05-6.0% by weight of the layer; and ...

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28-11-2013 дата публикации

SILICON CARBIDE MATERIAL, HONEYCOMB STRUCTURE, AND ELECTRIC HEATING TYPE CATALYST CARRIER

Номер: US20130316129A1
Принадлежит: NGK Insulators, Ltd.

A silicon carbide material according to the present invention includes a substrate containing, as a main component, silicon carbide or containing, as main components, silicon carbide and metallic silicon, and a film covering at least a portion of the surface of the substrate. The film contains, as a main component, a phase including at least four elements: lithium (Li), aluminum (Al), silicon (Si), and oxygen (O). One example of such a silicon carbide material includes a substrate having a structure in which silicon carbide particles are bonded by metallic silicon, and a lithium aluminosilicate film covering at least a portion of the surface of the silicon carbide particles. Such a silicon carbide material can be used for a DPF, an electric heating type catalytic converter, or the like. 1. A silicon carbide material , including:a substrate containing, as a main component, silicon carbide or containing, as main components, silicon carbide and metallic silicon, anda film covering at least a portion of the surface of the substrate,wherein the film contains, as a main component, a phase including at least four elements: lithium (Li), aluminum (Al), silicon (Si), and oxygen (O).2. The silicon carbide material according to claim 1 , wherein the film does not contain potassium.3. The silicon carbide material according to claim 1 , wherein the film contains a lithium aluminosilicate.4. The silicon carbide material according to claim 3 , wherein the lithium aluminosilicate is spodumene.5. The silicon carbide material according to claim 1 , wherein the substrate has a structure in which silicon carbide particles are bonded by metallic silicon.6. The silicon carbide material according to claim 1 , wherein the substrate has a porosity of 20% to 70%.7. The silicon carbide material according to claim 1 , wherein the film has the maximum thickness of 2 to 102 μm.8. The silicon carbide material according to claim 1 , wherein the film has the film weight ratio of 4.1% to 58.3% by ...

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12-12-2013 дата публикации

METHOD FOR PRODUCING MICRO-NANO COMBINED ACTIVE SYSTEMS

Номер: US20130331257A1
Принадлежит: LASER ZENTRUM HANNOVER E.V.

The invention relates to a method for producing micro-nano combined active systems in which nanoparticles of a first component are bonded to microparticles of a second component, comprising the following steps: (a) producing a low-ligand colloidal suspension containing nanoparticles of the first component, (b) adding microparticles to the colloidal suspension containing the nanoparticles or adding the colloidal suspension containing the nanoparticles to a dispersion containing the microparticles and intensively mixing so that the nanoparticles adsorb onto the microparticles, (c) separating the microparticles and the nanoparticles bonded thereto from the liquid and drying the microparticles and the nanoparticles bonded thereto. 1. Method for producing micro-nano combined active systems in which nanoparticles of a first component are bonded to microparticles of a second component , comprising the following steps:a. Producing a low-ligand colloidal suspension containing nanoparticles of the first componentb. Adding microparticles to the colloidal suspension containing the nanoparticles or adding the colloidal suspension containing the nanoparticles to a dispersion containing the microparticles and intensively mixing, so that the nanoparticles adsorb onto the microparticlesc. Separating the microparticles and the nanoparticles bonded thereto from the liquid and drying the microparticles and the nanoparticles bonded thereto.2. Method according to claim 1 , wherein for production of the colloidal suspension claim 1 , containing low-ligand nanoparticles claim 1 , a substrate claim 1 , containing the first component claim 1 , is ablated by absorption of a laser beam claim 1 , whereby the substrate claim 1 , containing the first component claim 1 , is positioned in a liquid in a way claim 1 , that the vaporized substrate immediately solidifies in the liquid claim 1 , forming a colloidal suspension of nanoparticles.3. Method according to claim 2 , wherein the laser is an ...

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02-01-2014 дата публикации

Nanonet-Based Hematite Hetero-Nanostructures for Solar Energy Conversions and Methods of Fabricating Same

Номер: US20140000697A1
Принадлежит: The Trustees of Boston College

Nanonet-based hematite hetero-nanostructures () for solar energy conversions and methods of fabricating same are disclosed. In an embodiment, a hetero-nanostructure () includes a plurality of connected and spaced-apart nanobeams () linked together at an about 90° angle, the plurality of nanobeams () including a conductive silicide core having an n-type photo-active hematite shell. In an embodiment, a device () for splitting water to generate hydrogen and oxygen includes a first compartment () having a two-dimensional hetero-nanostructure (), the hetero-nanostructure having a plurality of connected and spaced-apart nanobeams, each nanobeam substantially perpendicular to another nanobeam, the plurality of nanobeams including an n-type photoactive hematite shell having a conductive core; and a second compartment () having a p-type material (), wherein the first compartment () and the second compartment () are separated by a semi-permeable membrane. 1. A hetero-nanostructure comprising a plurality of connected and spaced-apart nanobeams linked together at an about 90° angle , the plurality of nanobeams including a conductive silicide core having an n-type photoactive hematite shell.2. The hetero-nanostructure of wherein the conductive silicide core is a titanium silicide core.3. The hetero-nanostructure of wherein the n-type photoactive hematite shell includes a dopant to absorb visible light.4. The hetero-nanostructure of wherein the plurality of nanobeams are two-dimensional.5. The hetero-nanostructure of wherein the hetero-nanostructure is used as a photoelectrochemical cell.6. The hetero-nanostructure of wherein the hetero-nanostructure is used as a solar cell.7. The hetero-nanostructure of for use in producing hydrogen.8. The hetero-nanostructure of wherein a thickness of the n-type photoactive hematite shell ranges from about 7 nm to about 40 nm.9. The hetero-nanostructure of wherein a thickness of the n-type photoactive hematite shell ranges from about 25 nm to ...

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13-02-2014 дата публикации

Hydrocarbon trap having improved adsorption capacity

Номер: US20140044625A1
Принадлежит: FORD GLOBAL TECHNOLOGIES LLC

A hydrocarbon trap is provided for reducing cold-start hydrocarbon emissions. The trap is formed by extruding from about 60 to 80% by weight zeolite and from about 20 to 40% by weight of a binder to form an extruded zeolite monolith. A three-way catalyst and an oxygen storage capacity material may also be included in the trap. The hydrocarbon trap contains from about 5.0 to 8.0 g/in. 3 zeolite, which provides increased hydrocarbon retention. The hydrocarbon trap may be positioned in the exhaust gas passage of a vehicle such that hydrocarbons are adsorbed on the trap and stored until the monolith reaches a sufficient temperature for catalyst activation.

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27-03-2014 дата публикации

HONEYCOMB CATALYST BODY

Номер: US20140086805A1
Принадлежит: NGK Insulators, Ltd.

The honeycomb catalyst body includes a honeycomb structure having porous partition walls, outflow side plugged portions, inflow side plugged portions, and catalyst layers formed on the surfaces of the partition walls on the side of the outflow cells, the cells are formed so that an open area of each outflow cell is larger than an open area of each inflow cell, a porosity of the partition walls of the honeycomb structure is from 25 to 55%, and in a cross section parallel to the extending direction of the cells, a total area of the catalyst layers formed on the surfaces of the pores in the partition walls is 5% or less of a total area of the pores in the partition walls. 1. A honeycomb catalyst body comprising:a honeycomb structure having porous partition walls with which a plurality of cells extending from an inflow side end surface to an outflow side end surface are defined and formed to become through channels of an exhaust gas;outflow side plugged portions arranged in open frontal areas of the predetermined cells in the outflow side end surface, to form the inflow cells which are open in the inflow side end surface and are closed in the outflow side end surface;inflow side plugged portions arranged in open frontal areas of the remaining cells in the inflow side end surface, to form the outflow cells which are open in the outflow side end surface and are closed in the inflow side end surface; andporous catalyst layers formed on the surfaces of the partition walls on the side of the outflow cells, and having a catalyst to purify the exhaust gas,wherein in the honeycomb structure, the inflow cells and the outflow cells are alternately arranged via the partition walls, and the plurality of cells are formed so that an open area of each of the outflow cells in a cross section of the outflow cell which is vertical to an extending direction of the cells is larger than an open area of each of the inflow cells in a cross section of the inflow cell which is vertical to the ...

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27-03-2014 дата публикации

PHOTOCATALYST MEMBER

Номер: US20140087179A1
Принадлежит: TOTO LTD.

Disclosed is a photocatalyst member including a glaze layer and a photoctalyst layer provided on the glaze layer, the photocatalyst layer is good in layer strength, water resistance, or abrasion resistance. More specifically, the photocatalyst member includes a base having a glaze layer and a photocatalyst layer that is provided on the glaze layer and contains titanium oxide and zirconium titanate, wherein the content of zirconium titanate in the photocatalyst layer is 15 to 75% by mass based on the total content of titanium oxide and zirconium titanate, and the content of zirconium titanate in an area from around an interface between the photocatalyst layer and the base to an median line in the thickness of the photocatalyst layer is larger than the content of zirconium titanate in an area near the external surface of the photocatalyst layer. 1. A photocatalyst member comprising a base , a glaze layer provided on the base , and a photocatalyst layer which is provided on the glaze layer and contains titanium oxide and zirconium titanate , whereinthe content of zirconium titanate in the photocatalyst layer is 15 to 75% by mass based on the total content of titanium oxide and zirconium titanate; andthe content of zirconium titanate in an area from around an interface between the photocatalyst layer and the base to an median line in the thickness of the photocatalyst layer is larger than the content of zirconium titanate in an area near the external surface of the photocatalyst layer.2. The photocatalyst member according to claim 1 , wherein zirconium titanate is not observed on the external surface of the photocatalyst layer.3. The photocatalyst member according to claim 1 , wherein the content of zirconium titanate in the photocatalyst layer is 35 to 65% by mass.4. The photocatalyst member according to claim 1 , wherein the thickness of the photocatalyst layer is 50 nm to 200 nm.5. The photocatalyst member according to claims 1 , which is a sanitary ware.6. A process ...

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10-04-2014 дата публикации

CATALYTIC CONVERTER APPARATUS

Номер: US20140099246A1
Принадлежит: VIDA HOLDINGS LTD.

A catalytic converter apparatus for use in an exhaust system of an internal combustion engine includes a housing having a gas inlet and a gas outlet, and at least one catalytic substrate element disposed in the housing. The at least one substrate element is divided into a plurality of zones or sections, the zones at least partially separated from one another to inhibit heat flow. The zones can be at least partially separated with walls. The walls can include insulating material for reducing the mobility of heat radially outwardly. Each of the zones defines a generally separate flow passage connecting the inlet and outlet in fluid communication. The apparatus can heat more rapidly from a cold start compared with conventional catalytic converters. 2. The apparatus of claim 1 , wherein the at least one wall comprises cementitious insulating material.3. The apparatus of claim 2 , wherein thickness of the insulating material between the zones is varied.4. The apparatus of claim 1 , wherein the insulating material has a thickness between the zones of less than 10 mm.5. The apparatus of claim 1 , wherein the insulating material comprises ceramic material.6. The apparatus of claim 1 , wherein the at least one wall separates the zones along substantially an entire length of the zones in a direction extending from the inlet to the outlet.7. The apparatus of claim 1 , wherein the zones comprise a central zone and at least one radial zone.8. The apparatus of claim 7 , wherein the at least one wall separating the central substrate zone from the at least one radial zone comprises at least one connecting portion.9. The apparatus of claim 1 , wherein the at least one substrate element substantially fills the housing in a radial dimension perpendicular to a direction of gas flow extending from the inlet to the outlet.10. The apparatus of claim 1 , wherein the zones are arranged generally in parallel in a direction of gas flow extending from the inlet to the outlet.11. The apparatus ...

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07-01-2021 дата публикации

EXHAUST GAS PURIFICATION DEVICE

Номер: US20210001315A1
Принадлежит:

A substrate () includes an inflow-side cell (), an outflow-side cell (), and a porous, gas-permeable partition wall () that separates the inflow-side cell () and the outflow-side cell () from each other, and also includes a first catalyst portion () that is provided on a side of the partition wall () that faces the inflow-side cell () at least at a portion in upstream side in an exhaust gas flow direction, and a second catalyst portion () that is provided on a side of the partition wall that faces the outflow-side cell at least at a portion in downstream side. With respect to a pore volume of pores with a pore size of 10 to 18 μm, when a measured value of the pore volume in the first catalyst portion () and the partition wall () within a region where the first catalyst portion () is provided is defined as a first pore volume, and a measured value of the pore volume in the second catalyst portion () and the partition wall () within a region where the second catalyst portion () is provided is defined as a second pore volume, the first pore volume is greater than the second pore volume. A catalytically active component contained in the first catalyst portion () and a catalytically active component contained in the second catalyst portion () are of different types. 1. An exhaust gas purification catalyst comprising:a substrate; anda catalyst portion provided in the substrate, an inflow-side cell including a space whose inflow-side in an exhaust gas flow direction is open and whose outflow-side is closed;', 'an outflow-side cell including a space whose inflow-side in the exhaust gas flow direction is closed and whose outflow-side is open; and', 'a porous partition wall that separates the inflow-side cell and the outflow-side cell from each other, and, 'the substrate including a first catalyst portion that is provided at least on a portion of a side of the partition wall that faces the inflow-side cell, the portion being located on an upstream side in the flow direction; ...

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07-01-2016 дата публикации

PROCESS FOR THE PREPARATION OF Ni-CeMgAl2O4 CATALYST FOR DRY REFORMING OF METHANE WITH CARBON DIOXIDE

Номер: US20160001269A1
Принадлежит:

The present invention provides a process and catalyst system for the production of synthesis gas (a mixture of CO and H) from greenhouse gases like methane and carbon di oxide. The process provide a single step selective reforming of methane with carbon dioxide to produce synthesis gas over Ce—Ni—MgAlOcatalyst prepared by using combination of two methods evaporation induced self-assembly and organic matrix combustion method. These suitably combined methods generate a unique catalyst system with very fine Ni nano clusters evenly dispersed in high surface area support. The process provides both Methane and carbon di oxide conversion more than 90% without any noticeable deactivation till 100 hours between temperature range of 500-800° C. at atmospheric pressure. 1. A process for the preparation of Ni—CeMgAlOcatalyst wherein the said process comprising the steps of;i. dissolving Aluminium isopropoxide in a mixture of ethanol and concentrated nitric acid;ii. preparing a second solution by dissolving Poly (ethylene glycol)-block-poly (propylene glycol)-block-poly (ethylene glycol) (P123) in mole ration ranging between 0.003-0.004 in ethanol;iii. adding salt of Magnesium and Cerium into the second solution;{'sub': 2', '4, 'iv. mixing solution as prepared in step (i) and step (iii) and stirring for 8-10 hrs at room temp 25° C. for homogenation and kept for drying at 60-80° C. for 48-72 h and calcing at a range 700-900° C. for 6-8 hr and subsequently depositing nickel particles onto it to and further calcining at temperature 400-600° C. 6-8 h to obtain Ni—CeMgAlOcatalyst.'}2. A process as claimed in claim 1 , wherein the wt % of Ni to Ce—MgAl2O4 of the catalyst is varied in the range 1-10% (Ni:Ce—MgAl2O4).3. A process as claimed in claim 1 , wherein the wt % of MgO to Al2O3 of the catalyst is varied in the range of 1-5% (MgO:Al2O3).4. A process as claimed in claim 1 , wherein the wt % of Ce to Al2O3 is in the range of 0.1-5% Ce:Al2O3).5. A process as claimed in claim 1 , ...

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07-01-2016 дата публикации

Process for Limiting Self Heating of Activated Catalysts

Номер: US20160001279A1
Принадлежит:

The invention provides a process for limiting self heating of activated particle catalysts wherein the catalyst particles are placed in motion inside a hot gas flow that passes through them and a liquid composition containing one or several film forming polymer(s) is pulverized onto the particles in motion until a protective layer is obtained on the surface of said particles containing said film forming polymer and having an average thickness of less than or equal to 20 μm. The invention also provides the use of this process to reduce the quantities of toxic gases that may be emitted by the activated catalysts, as well as an activated catalyst for the hydroconversion of hydrocarbons covered with a continuous protective layer that are obtained by this process. 1. A process for limiting self heating of activated particle catalysts , in which the catalyst particles are placed in motion within a hot gas flow passing through them , and a liquid composition containing one or more film forming polymer(s) is pulverized onto the moving particles until on the surface of said particles a protective layer containing said film forming polymer is obtained , that has an average thickness lower than or equal to 20 μm.2. The process according to claim 1 , characterized in that the liquid composition is a solution or a dispersion of the film forming polymer(s) in a solvent claim 1 , and contains preferably from 0.1 to 50% by weight of film forming polymer claim 1 , more preferably from 0.5 to 25% by weight claim 1 , and even more preferably from 1 to 10% by weight of film forming polymer claim 1 , with respect to the total weight of the composition.3. The process according to claim 1 , characterized in that it is implemented in a perforated drum in which the catalyst particles are put in motion claim 1 , with a hot gas flow passing continuously through said perforated drum.4. The process according to claim 1 , characterized in that it is implemented by placing catalyst particles in a ...

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05-01-2017 дата публикации

Catalyst for ammonia oxidation

Номер: US20170001177A1
Принадлежит: Danmarks Tekniskie Universitet

The present invention relates to a bimetallic catalyst for ammonia oxidation, a method for producing a bimetallic catalyst for ammonia oxidation and a method for tuning the catalytic activity of a transition metal. By depositing an overlayer of less catalytic active metal onto a more catalytic active metal, the total catalytic activity is enhanced.

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02-01-2020 дата публикации

VISIBLE LIGHT-ACTIVATED PHOTOCATALYTIC COATING COMPOSITION AND AIR PURIFICATION FILTER

Номер: US20200001275A1
Принадлежит:

Disclosed is a visible light-activated photocatalytic coating composition comprising a visible light active photocatalytic material and an aqueous solvent. 1. An air purification filter comprising:a porous substrate comprising activated carbon; anda photocatalytic coating layer formed from a visible light-activated photocatalytic coating composition on the porous substrate comprising activated carbon,wherein an amount of the activated carbon ranges from 20% to 80% by weight based on an amount of the porous substrate comprising activated carbon, and the visible light-activated photocatalytic coating composition comprises a visible light active photocatalytic material,wherein the visible light active photocatalytic material comprises a porous first metal oxide; and a second metal particle supported on the porous first metal oxide, a second metal oxide particle, or both,{'sub': '3', 'wherein the first metal oxide is a tungsten oxide (WO) and a second metal of the second metal particle and the second metal oxide particle is platinum (Pt),'}the visible light active photocatalytic material is formed into particles,the visible light-activated photocatalytic coating composition does not comprise an alcohol and a binder material, andthe porous substrate comprising activated carbon is formed by attaching the activated carbon to or impregnating the activated carbon into a material comprising a woven or nonwoven fabric made of an organic fiber or inorganic fiber.2. The air purification filter of claim 1 , wherein the photocatalytic coating layer is coated on the porous substrate and the activated carbon by immersing the porous substrate and the activated carbon in the visible light-activated photocatalytic coating composition.3. The air purification filter of claim 1 , wherein an amount of the visible light active photocatalytic material ranges from 4% to 10% by weight based on an amount of the visible light-activated photocatalytic coating composition.4. The air purification ...

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05-01-2017 дата публикации

IN-SITU PRODUCED Y-FAUJASITE FROM KAOLIN-DERIVED, PRE-SHAPED PARTICLES AND THE METHOD OF PREPARATION AND THE USE THEREOF

Номер: US20170001179A1
Принадлежит:

A zeolite-containing fixed bed catalyst is formed by pre-shaping a mixture of a reactive aluminum-containing component and a matrix component into pre-shaped particles, and contacting the pre-shaped particles with a reactive liquid containing a silicate for a sufficient time and temperature to form an in-situ zeolite within the pre-shaped particles. The contacting of the pre-shaped particles and the liquid is achieved such that there is relative movement between the pre-shaped particles and the liquid. 1. A fixed bed catalyst comprising:a pre-shaped particle having been formed from a mixture of a reactive aluminum-containing component and one or more matrix-forming components, wherein the pre-shaped particle is shaped in a form of an extrudate, pellet, or sphere; andzeolite Y crystallized on the pre-shaped particle, the zeolite Y having been crystallized by contacting the pre-shaped particle with a liquid containing a reactive silicate component for a time and at a temperature sufficient to crystalize the zeolite Y.2. The fixed bed catalyst of claim 1 , wherein the reactive aluminum-containing component comprises metakaolin.3. The fixed bed catalyst of claim 2 , wherein the pre-shaped particle comprises hydrous kaolin claim 2 , and wherein the pre-shaped particle is calcined to convert the hydrous kaolin to metakaolin.4. The fixed bed catalyst of claim 1 , wherein the one or more matrix-forming components comprise at least one of kaolin calcined through exotherm of the kaolin to spinel claim 1 , mullite claim 1 , or alumina.5. The fixed bed catalyst of claim 1 , wherein the liquid is contacted with the pre-shaped particle by circulating the liquid through a stationary bed containing the pre-shaped particle.6. The fixed bed catalyst of claim 1 , wherein the liquid is contacted with the pre-shaped particle by forming a second mixture of the pre-shaped particle in the liquid claim 1 , and providing movement to the second mixture.7. The fixed bed catalyst of claim 1 , ...

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05-01-2017 дата публикации

CATALYST FOR PURIFYING COMBUSTION EXHAUST GAS, AND METHOD FOR PURIFYING COMBUSTION EXHAUST GAS

Номер: US20170001181A1
Принадлежит:

To provide a catalyst for purifying a combustion exhaust gas and a method for purifying a combustion exhaust gas. The denitration catalyst used in a method for purifying a combustion exhaust gas of removing a nitrogen oxide in the exhaust gas by making the catalyst into contact with the combustion exhaust gas having an alcohol as a reducing agent added thereto, contains zeolite as a support having supported thereon a catalyst metal, in a powder X-ray diffraction (XRD) measurement of the denitration catalyst a ratio (relative peak intensity ratio) r=I/J of a height I of a diffraction peak at a diffraction angle (2θ) of from 7.8 to 10.0° and a height J of a diffraction peak at a diffraction angle (2θ) of from 28.0 to 31.0° being in a range of from 3.0 to 5.0. 1. A denitration catalyst used in a method for purifying a combustion exhaust gas of removing a nitrogen oxide in the exhaust gas by making the catalyst into contact with the combustion exhaust gas having an alcohol as a reducing agent added thereto , the denitration catalyst comprising zeolite as a support having supported thereon cobalt (Co) as a catalyst metal , in a powder X-ray diffraction measurement of the denitration catalyst a ratio r=I/J of a height I of a diffraction peak at a diffraction angle (2θ) of from 7.8 to 10.0° and a height J of a diffraction peak at a diffraction angle (2θ) of from 28.0 to 31.0° being in a range of from 3.0 to 5.0.2. The catalyst for purifying a combustion exhaust gas according to claim 1 , wherein the zeolite as a support contains zeolite that has been baked in an inert gas atmosphere in advance.3. (canceled)4. (canceled)5. The catalyst for purifying a combustion exhaust gas according to claim 1 , wherein the alcohol as a reducing agent is methanol or ethanol.6. A method for purifying a combustion exhaust gas claim 1 , comprising making a combustion exhaust gas having an alcohol as a reducing agent added thereto claim 1 , into contact with a denitration catalyst containing a ...

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05-01-2017 дата публикации

Visible-Light-Activated Multilayered Photocatalyst And The Method Of Its Preparation

Номер: US20170001183A1
Принадлежит:

Visible-light-active and photostable, multilayered materials and their preparation method based on surface-modified titanium(IV) oxide have been invented. 1. Preparation method of a visible-light-activated multilayered photocatalyst characterized in that:a) modifies the surface of titanium(IV) oxide in the form of powder or coating by impregnation with a modifier solution, where the modifier is an aromatic organic compound with at least two —OH or —COOH groups or a hexachloroplatinate(IV) ion,b) the protective layer of titanium(IV) oxide is applied on the modified material, where the known ALD or “spin-coating” techniques are used.2. Method according to claim 1 , characterized in that it uses crystalline titanium(IV) oxide with a structure of anatase or being a mixture of anatase and rutile structure.3. Method according to claim 1 , characterized in that stage a) is carried out in water or alcohol solution of the modifier of the 10mol/dmminimal concentration and the product of the modification is dried.5. Method according to claim 1 , characterized in that the organic is a compound selected from the group consisting of phthalic acid claim 1 , 4-sulfophthalic acid claim 1 , 4-amino-2-hydroxybenzoic acid claim 1 , 3-hydroxy-2-naphthoic acid claim 1 , salicylic acid claim 1 , 6-hydroxysalicylic acid claim 1 , 5-hydroxysalicylic acid claim 1 , 5-sulfosalicylic acid claim 1 , 3 claim 1 ,5-dinitrosalicylic acid claim 1 , 2 claim 1 ,5-dihydroxyterephthalic acid claim 1 , aurintricarboxylic acid claim 1 , disodium salt of 1 claim 1 ,4-dihydroxy-1 claim 1 ,3-benzenodisulfonic acid claim 1 , gallic acid claim 1 , pyrogallol claim 1 , 2 claim 1 ,3-naphthalenediol claim 1 , 4-methylcatechol claim 1 ,3-5-di-tert-butyl-catechol claim 1 , p-nitrocatechol claim 1 , 3 claim 1 ,4-dihydroxy-1-phenylalanine (DOPA) claim 1 , catechol (Table 2) claim 1 , rutin and ascorbic acid.6. Method according to claim 1 , characterized in that stage b) uses alcoholates claim 1 , preferably titanium( ...

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05-01-2017 дата публикации

ZINC-BASED NANOHYBRIDS, DEVICES AND METHODS THEREOF

Номер: US20170001186A1
Принадлежит: UMM AL-QURA UNIVERSITY

A zinc-based nanohybrid was prepared using a facile wet chemistry process. This nanohybrid has zinc oxide nanostructures connected to zinc phthalocyanine molecules via biologically important ligands. In addition, this nanohybrid has photocatalytic properties and photodegrades water pollutants, such as methyl orange. 1: A zinc-based nanohybrid , comprising:a zinc oxide nanostructure;a zinc phthalocyanine molecule; anda bridging ligand connecting the zinc oxide nanostructure and the zinc phthalocyanine molecule.2: The zinc-based nanohybrid of claim 1 , wherein the zinc oxide nanostructure has at least one morphology selected from the group consisting of a nanoparticle claim 1 , and a nontubular nanorod.3: The zinc oxide nanostructure of claim 2 , wherein the zinc oxide nanostructure is a nontubular nanorod with an average largest diameter of 50-100 nm and a length of 0.3-5 μm.4: The zinc oxide nanostructure of claim 2 , wherein the zinc oxide nanostructure is a nanoparticle with an average diameter of 10-50 nm.6: The zinc-based nanohybrid of claim 1 , wherein the zinc phthalocyanine molecule is of Formula (I) claim 1 , wherein R-Rare each hydrogen.7: The zinc-based nanohybrid of claim 1 , wherein the bridging ligand has two terminal carboxylate groups claim 1 , and through the two carboxylate end groups claim 1 , the bridging ligand forms a first Zn—O linkage with zinc in the zinc oxide nanostructure and a second Zn—O linkage with zinc in the zinc phthalocyanine molecule.9: The zinc-based nanohybrid of claim 1 , wherein the bridging ligand is selected from the group consisting of citrate claim 1 , tartrate claim 1 , an amino acid claim 1 , which is serine claim 1 , cysteine claim 1 , aspartate claim 1 , glutamate or tyrosine claim 1 , and enantiomers thereof.10: A substrate comprising:at least one plate; and{'claim-ref': {'@idref': 'CLM-00001', 'claim 1'}, 'the zinc-based nanohybrid of , wherein the zinc-based nanohybrid is coated on a surface of the plate to form a ...

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04-01-2018 дата публикации

PHOTOCATALYST FILTER, PHOTOCATALYST FILTER LAMINATE, EXHAUST UNIT, AND IMAGE FORMING APPARATUS

Номер: US20180001312A1
Принадлежит:

The present disclosure provides a photocatalyst filter that can efficiently decompose and eliminate ozone gas or VOC and has a low ventilation resistance. The photocatalyst filter includes a sheet-like filter substrate and a photocatalyst layer supported by the filter substrate. The photocatalyst layer exhibits a photocatalytic action by receiving light having a wavelength of 400 nm or more. The photocatalyst filter has an aperture ratio of 35% or more and 80% or less. 1. A photocatalyst filter comprising:a sheet-like filter substrate; anda photocatalyst layer supported by the filter substrate, whereinthe photocatalyst layer exhibits a photocatalytic action by receiving light having a wavelength of 400 nm or more; andthe photocatalyst filter has an aperture ratio of 35% or more and 80% or less.2. The photocatalyst filter according to claim 1 , wherein the filter substrate has a curved shape.3. A photocatalyst filter laminate comprising:{'claim-ref': {'@idref': 'CLM-00001', 'claim 1'}, 'a plurality of photocatalyst filters according to , wherein'}the photocatalyst filters are stacked; andthe photocatalyst filter laminate has a thickness of 1 mm or more and 10 mm or less.4. An exhaust unit comprising:{'claim-ref': {'@idref': 'CLM-00003', 'claim 3'}, 'a photocatalyst filter laminate according to ;'}a first light source section for irradiating the photocatalyst filter laminate with light having a wavelength of 400 nm or more; andan exhaust fan for discharging gas from an exhaust port, whereinthe photocatalyst filter laminate is disposed in the exhaust port.5. The exhaust unit according to claim 4 , whereinthe photocatalyst filter laminate has a curved shape; andthe first light source section irradiates light to a concave surface of the photocatalyst filter laminate.6. The exhaust unit according to claim 5 , whereinthe photocatalyst filter laminate includes a first photocatalyst filter disposed at the surface receiving light from the first light source section and a ...

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03-01-2019 дата публикации

IMAGING APPARATUS AND VEHICLE

Номер: US20190001932A1
Автор: ITO Mitsuru
Принадлежит:

An imaging apparatus includes an optical member, a housing, and a light source. The optical member contains a photocatalyst film on an object-side surface. The housing contains an accommodation section in which the optical member is accommodated. The light source is located in an internal space of the housing and emits light to activate the photocatalyst film. The light from the light source passes through the optical member and irradiates the photocatalyst film. 1. An imaging apparatus comprising:an optical member containing a photocatalyst film on an object-side surface;a housing containing an accommodation section in which the optical member is accommodated; anda light source that is located in an internal space of the housing and emits light to activate the photocatalyst film,wherein light from the light source passes through the optical member and irradiates the photocatalyst film.2. The imaging apparatus according to claim 1 ,wherein the housing includes one or more through holes extending from the internal space of the housing to the accommodation section, andlight from the light source passes through the one or more through holes and is incident upon the optical member.3. The imaging apparatus according to claim 2 ,wherein the light from the light source passes through the one or more through holes and is incident upon the optical member from at least one of an outer side surface or an object-side surface of the optical member.4. The imaging apparatus according to claim 2 ,wherein at least a part of the light which passes through the one or more through holes and is incident upon the optical member is reflected internally in the optical member.5. The imaging apparatus according to claim 2 ,wherein the one or more through holes include a plurality of through holes formed located around the optical member.6. The imaging apparatus according to claim 1 ,wherein the housing includes, on at least a part of an inner wall defining the internal space, a reflecting ...

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03-01-2019 дата публикации

Synthesis of fibrous nano-silica spheres with controlled particle size, fibre density, and various textural properties

Номер: US20190002297A1
Принадлежит: TATA INSTITUTE OF FUNDAMENTAL RESEARCH

The present disclosure provides a method for synthesizing fibrous silica nanospheres, the method can include, in sequence, the steps of: a) providing a reaction mixture comprising a silica precursor, a hydrolyzing agent, a template molecule, a cosurfactant and one or more solvents; b) maintaining the reaction mixture under stirring for a length of time; c) heating the reaction mixture to a temperature for a length of time; d) cooling the reaction mixture to obtain a solid, and (e) calcinating the solid to pro duce fibrous silica nanospheres, wherein desirable product characteristics such as particle size, fiber density, surface area, pore volume and pore size can be obtained by controlling one or more parameters of the method. The present disclosure further provides a method for synthesizing fibrous silica nanospheres using conventional heating such as refluxing the reactants in an open reactor, thereby eliminating the need for microwave heating in a closed reactor or the need for any pressure reactors.

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04-01-2018 дата публикации

Exhaust Gas Cleaning Component For Cleaning The Exhaust Gases Of An Internal Combustion Engine

Номер: US20180003096A1
Автор: Bohne Frank, Nagel Thomas
Принадлежит:

An exhaust gas cleaning component, having a housing with an inflow port and an outflow port, a first honeycomb structure in the housing with a casing, the casing having an outer surface over which exhaust gas can flow, and also having an applicator device by which an exhaust gas cleaning additive can be applied to the outer surface of the casing. 19.-. (canceled)10. An exhaust gas cleaning component , comprising:a housing with an inflow port and an outflow port;a first honeycomb body arranged in the housing;a shell of the first honeycomb body having an outer surface over which exhaust gas can flow within the housing; anda feed device configured to feed an exhaust gas cleaning additive onto the outer surface of the shell.11. The exhaust gas cleaning component as claimed in claim 10 , further comprising:at least one bypass duct formed between the outer surface of the shell and the housing through which duct a partial exhaust gas flow of an exhaust gas flow flowing from the inflow port to the outflow port can bypass the first honeycomb body,wherein the feed device is arranged at the at least one bypass duct and configured so that the exhaust gas cleaning additive is fed into the at least one bypass duct.12. The exhaust gas cleaning component as claimed in claim 11 , further comprising:a second honeycomb body, through which the partial exhaust gas flow flowing through the at least one bypass duct flows, is arranged in the at least one bypass duct upstream of the feed device in an exhaust gas flow direction.13. The exhaust gas cleaning component as claimed in claim 11 , further comprising:a heater arranged in the at least one bypass duct upstream of the feed device in an exhaust gas flow direction and configured to heat the partial exhaust gas flow flowing through the at least one bypass duct.14. The exhaust gas cleaning component as claimed in claim 11 , further comprising:a surface heating system arranged at an impact region of the outer surface of the shell at which ...

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01-01-2015 дата публикации

HONEYCOMB STRUCTURAL BODY

Номер: US20150004353A1
Принадлежит:

In a cross section, perpendicular to an axial direction of a honeycomb structural body having partition walls and cells, a plurality of sections having a different cell density is formed from a central area toward an outer peripheral area, and a partition wall is formed between the sections adjacent to each other. The boundary section has boundary partition walls and plural boundary cells having a polygonal shape different in shape from the cells in the sections formed adjacent to the boundary section. The partition walls in the sections adjacent to the boundary section are connected by the boundary partition walls. A part of the boundary cell is surrounded by at least the boundary partition walls. A relationship of φ1/φ2≧1.25 is satisfied, where φ1 indicates an average hydraulic diameter of the boundary cells and φ2 indicates an average hydraulic diameter of the cells. 1. A honeycomb structural body formed as a monolithic mold comprising partition walls arranged in a lattice shape and a plurality of cells surrounded by the partition walls , whereinthe honeycomb structural body comprises a plurality of cell density sections having a different cell density formed in a radial direction from a central side to an outer peripheral side,{'b': '2', 'a boundary section is formed between the cell density sections () which are immediately adjacent,'}the boundary section comprises boundary partition walls and a plurality of boundary cells having a polygonal shape,the boundary partition walls connect the partition walls in the cell density sections formed adjacent to the boundary section,the boundary cells having a polygonal shape are different in shape from the cells,at least a part of the boundary cell is surrounded by the boundary partition walls, and {'br': None, 'φ1/φ2≧1.25,'}, 'the honeycomb structural body satisfies a relationship of'}where φ1 indicates an average hydraulic diameter of the boundary cells formed in the boundary section, and φ2 indicates an average ...

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13-01-2022 дата публикации

Device for reducing airborne contaminants

Номер: US20220008608A1
Автор: Randy A. Mount
Принадлежит: Individual

A photocatalytic system for reducing airborne contaminants using an ultraviolet (UV) emitter and photocatalytic cells, the system comprises a housing comprising a front side having an opening therethrough, and a rear side opposite the front side, the rear side also having an opening therethrough. A first photocatalytic cell is located in the housing adjacent to the front side. Likewise, a second photocatalytic cell located in the housing adjacent to the rear side. A unitary removable structure slidably positionable within the housing between the first photocatalytic cell and the second photocatalytic cell.

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13-01-2022 дата публикации

CATALYST BED COMPRISING SILVER CATALYST BODIES AND PROCESS FOR THE OXIDATIVE DEHYDROGENATION OF OLEFINICALLY UNSATURATED ALCOHOLS

Номер: US20220008884A1
Принадлежит:

The present invention relates to a catalyst bed comprising silver catalyst bodies and a reactor comprising such a catalyst bed. Further, the invention relates to the use of the catalyst bed and the reactor for gas phase reactions, in particular for the oxidative dehydrogenation of organic compounds under exothermic conditions. In a preferred embodiment, the present invention relates to the preparation of olefinically unsaturated carbonyl compounds from olefinically unsaturated alcohols by oxidative dehydrogenation utilizing a catalyst bed comprising metallic silver catalyst bodies. 118.-. (canceled)19. A process for the preparation of an olefinically unsaturated carbonyl compound in a tubular reactor comprising a plurality of reactor tubes , comprising reacting an olefinically unsaturated alcohol with oxygen in the presence of a catalyst bed , comprising full-metallic silver catalyst bodies , wherein the catalyst bed has a packing density of the full-metallic silver catalyst bodies in the range of 3.0 g/cmto 10.0 g/cm.20. The process according to claim 19 , wherein the catalyst bed has a packing density of the full-metallic silver catalyst bodies in the range of 5.5 g/cmto 10.0 g/cm.21. The process according to claim 19 , wherein the catalyst bed has a void space ratio in the range of 5% to 70% claim 19 , based on the volume of the catalyst bed not occupied by the catalyst bodies per volume of the catalyst bed.22. The process according to claim 19 , wherein the full-metallic silver catalyst bodies have a mean particle size of 0.5 mm to 5.0 mm.23. The process according to claim 19 , wherein the full-metallic silver bodies have a cylindrical shape or spherical shape or sphere-like shape or combinations thereof.24. The process according to claim 19 , wherein the full-metallic silver bodies have a geometric surface area in the range of 100 mm/g to 600 mm/g.25. The process according to claim 19 , wherein the catalyst bed is located in a tube reactor.26. The process ...

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13-01-2022 дата публикации

HONEYCOMB BODIES HAVING AN ARRAY OF THROUGH CHANNELS WITH A RANGE OF HYDRAULIC DIAMETERS

Номер: US20220008907A1
Принадлежит:

A ceramic honeycomb body, suitable for use in exhaust gas processing, includes a honeycomb structure having a plurality of through-channels, a first portion of the plurality of through-channels have a first hydraulic diameter dh, a second portion of the plurality of through-channels have a second hydraulic diameter that is smaller than the first hydraulic diameter dh, the first hydraulic diameter dh is equal to or greater than 1.1 mm, and the first and second portions of through-channels, taken together, have a geometric surface area GSA greater than 2.9 mm. Diesel oxidation catalysts and methods of soot removal are also provided, as are other aspects. 1. A honeycomb body , comprising: {'sup': '−1', 'a plurality of channels disposed in parallel to each other in an axial direction, wherein a first portion of the plurality of channels have a dh≥1.1 mm, a second portion of the plurality of channels have a dh<1.1 mm, and the plurality of channels comprise GSA≥2.9 mm, wherein dh is hydraulic diameter and GSA is a geometric surface area.'}, 'a honeycomb structure comprising a plurality of unit channel structures disposed in a repeating pattern, each unit channel structure comprising2. The honeycomb body of claim 1 , wherein the plurality of channels extend from an inlet face to an outlet face.3. The honeycomb body of claim 1 , wherein every channel of the plurality of channels is a flow-through channel.4. The honeycomb body of claim 1 , wherein every channel of the plurality of channels is devoid of plugging.5. The honeycomb body of claim 1 , wherein at least a portion of the plurality of channels have a catalytic coating disposed thereon.6. The honeycomb body of claim 1 , wherein the honeycomb body comprises:{'sup': '2', 'CD≥62.0 cm(400 cpsi);'}{'sup': 2', '2, 'the first portion of the plurality of channels comprise 6.2 channels/ cm(40 cpsi)≤CD≤46.5 channels/ cm(300 cpsi); and'}3%≤CR≤40% wherein CR is a channel ratio of a total cross-sectional area of the first portion ...

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04-01-2018 дата публикации

PLASMONIC METAL NITRIDE AND TRANSPARENT CONDUCTIVE OXIDE NANOSTRUCTURES FOR PLASMON ASSISTED CATALYSIS

Номер: US20180003865A1
Принадлежит: PURDUE RESEARCH FOUNDATION

A nanostructured material system for efficient collection of photo-excited carriers is provided. They system comprises a plurality of plasmonic metal nitride core material elements coupled to a plurality of semiconductor material elements. The plasmonic nanostructured elements form ohmic junctions at the surface of the semiconductor material or at close proximity with the semiconductor material elements. A nanostructured material system for efficient collection of photo-excited carriers is also provided, comprising a plurality of plasmonic transparent conducting oxide core material elements coupled to a plurality of semiconductor material elements. The field enhancement, local temperature increase and energized hot carriers produced by nanostructures of these plasmonic material systems play enabling roles in various chemical processes. They induce, enhance, or mediate catalytic activities in the neighborhood when excited near the resonance frequencies. 1. A nanostructured material system for efficient collection of photo-excited carriers , comprising:a plurality of plasmonic metal nitride core material elements coupled to a corresponding plurality of semiconductor material elements.2. The system of claim 1 , wherein the plasmonic nanostructured elements form ohmic junctions at the surface of the semiconductor material elements or at close proximity with the semiconductor material elements.3. The system of claim 1 , wherein the plasmonic metal nitride core material is titanium nitride (TiN).4. The system of claim 3 , wherein the semiconductor is titanium dioxide (TiO) or TiON claim 3 , where 01.7. The system of claim 6 , wherein the semiconductor material elements comprise tantalum pentoxide (TaO).8. The system of claim 5 , ...

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20-01-2022 дата публикации

FUNCTIONAL STRUCTURE PRECURSOR AND FUNCTIONAL STRUCTURE

Номер: US20220016607A1
Принадлежит:

A functional structure which can prevent metal fine particles from aggregating, can suppress bonding of an active metal species and a support, and can easily undergo catalyst activation before being used for reactions. The functional structure includes supports each having a porous structure and including a zeolite-type compound, and at least one functional material precursor present in the supports and including a metal element (M), in which each of the supports has channels communicating with one another, the functional material precursor is present at least in the channel of each of the supports, and the metal element (M) having constituted the functional material precursor is partially substituted with an element having constituted the supports. 1. A functional structure precursor comprising:supports each having a porous structure and including a zeolite-type compound; andat least one functional material precursor present in the supports and including a metal element (M), whereineach of the supports has channels communicating with one another,the functional material precursor is present at least in the channel of each of the supports, andthe metal element (M) having constituted the functional material precursor is partially substituted with an element having constituted the supports.2. The functional structure precursor according to claim 1 , wherein the metal element (M) exists as a central atom of two types of coordination structures in the functional material claim 1 , a first type being a coordination structure of four-coordination number and a second type being a coordination structure of six-coordination number.3. The functional structure precursor according to claim wherein a ratio of the number of the metal element (M) in the coordination structure of four-coordination number to the total number of the metal element (M) in the coordination structure of four-coordination number and the coordination structure of six-coordination number is 0.75 or less ...

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20-01-2022 дата публикации

CATALYST STRUCTURE AND METHOD FOR PRODUCING SAME, AND METHOD FOR PRODUCING HYDROCARBON BY USE OF CATALYST STRUCTURE

Номер: US20220016608A1
Принадлежит: FURUKAWA ELECTRIC CO., LTD.

A catalyst structure that allows prevention of aggregation of fine particles of a functional substance, suppresses decrease of catalyst activity, and thus enables extension of the lifetime of the catalyst structure. A catalyst structure has a carrier that is formed from a zeolite-type compound and has a porous structure. The functional substance includes a first element that is at least one metallic element selected from the group consisting of cobalt (Co), nickel (Ni), iron (Fe), and ruthenium (Ru), and at least one second element selected from the group consisting of metallic elements in group , group , group , group , and group on the periodic table. The carrier has paths connected to each other. The functional substance is present in at least the paths of the carrier. 1. A catalyst structure comprising:a support that has a porous structure and comprises a zeolite-type compound; andat least one functional material present in the support,at least one functional material comprising:at least one first metal element selected from the group consisting of cobalt (Co), nickel (Ni), iron (Fe), and ruthenium (Ru); andat least one second metal element selected from the group consisting of metal elements belonging to Groups 1, 2, 4, 7, and 12 of periodic table, whereinthe support has channels communicating with one another, andthe functional material is present at least in the channels of the support.2. The catalyst structure according to claim 1 , wherein the second element is at least one metal element selected from the group consisting of potassium (K) claim 1 , magnesium (Mg) claim 1 , titanium (Ti) claim 1 , zirconium (Zr) claim 1 , manganese (Mn) claim 1 , and zinc (Zn).3. The catalyst structure according to claim 1 , wherein a mass ratio of a content of the second element to a content of the first element is from 0.01 to 2.00.4. The catalyst structure according to claim 1 , wherein a total content of the first element is 0.5% by mass or more with respect to the mass ...

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12-01-2017 дата публикации

Multicatalyst Polyelectrolyte Membranes and Materials and Methods Utilizing the Same

Номер: US20170007871A1
Принадлежит:

A multi-catalytic material that includes a polyelectrolyte membrane and methods of preparing the same are provided herein. 1. A multi-catalytic material , comprising:a. a polyelectrolyte membrane (PEM);b. a polyoxometalate (POM); andc. a metal oxide (MO).2. The material of claim 1 , comprising a polyelectrolyte coating.3. The material of claim 2 , wherein the polyelectrolyte coating comprises a positively charged polyelectrolyte.4. The material of claim 1 , wherein the polyelectrolyte membrane comprises a block co-polymer comprising covalently bonded hydrophobic and hydrophilic units.5. The material of claim 4 , wherein at least one of the hydrophobic and hydrophilic units comprises a linear morphology claim 4 , a branched morphology claim 4 , or a combination thereof.6. The material of claim 1 , wherein the polyelectrolyte membrane comprises an ion exchanging functional group.7. The material of claim 6 , wherein the ion exchanging functional group comprises a sulfite claim 6 , a sulfate claim 6 , or a combination thereof.8. The material of claim 1 , wherein the polyelectrolyte membrane comprises sulfonated tetrafluoroethylene based fluoropolymer-copolymer claim 1 , sulfonated styrene-ethane/butadiene-styrene (sSEBS) claim 1 , or a combination thereof.9. The material of claim 1 , wherein the polyelectrolyte membrane comprises a cation selected from the group consisting of a monovalent cation claim 1 , a bivalent cation claim 1 , a trivalent cation claim 1 , a tetravalent cation claim 1 , a pentavalent cation claim 1 , a hexavalent cation claim 1 , and combinations thereof.10. The material of claim 9 , wherein the cation comprises Na claim 9 , Mg claim 9 , Ca claim 9 , Zn claim 9 , Ni claim 9 , Co claim 9 , Co claim 9 , Fe claim 9 , Fe claim 9 , Al claim 9 , Al claim 9 , Mn claim 9 , W claim 9 , Cr claim 9 , Cr claim 9 , Zr claim 9 , Y claim 9 , Nb claim 9 , Mo claim 9 , Mo claim 9 , Mo claim 9 , Mo claim 9 , Mo claim 9 , Mo claim 9 , or a combination thereof.11. The ...

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12-01-2017 дата публикации

CATALYTIC CONVERTER

Номер: US20170007985A1
Принадлежит:

In order to specify a catalytic converter, especially SCR catalytic converter, with maximum catalytic activity, this catalytic converter has at least one catalytically active component and additionally at least one porous inorganic filler component having meso- or macroporosity. The organic porous filler component has a proportion of about 5 to 50% by weight. More particularly, a diatomaceous earth or a pillared clay material is used as the porous inorganic filler component. 1. A catalytic converter comprising: (a) a base component comprising at least one catalytically active component , a binder component and optionally fibres that provide mechanical stability; and (b) at least one porous inorganic filler component , wherein the inorganic filler component has at least mesoporosity.2. The catalytic converter according to claim 1 , wherein at least one catalytically active component is an SCR catalyst.3. The catalytic converter according to claim 1 , wherein:the at least one catalytically active component, the binder component, and the fibers, if present, are present in a defined ratio of proportions by weight relative to one another, andthe catalytic converter has at least a same catalytic activity as a comparative catalytic converter without a filler component and with the same catalytically active component, the binder component, and the fibers, if present, having same defined ratio of proportions relative to one another.4. The catalytic converter according to claim 1 , wherein the inorganic porous filler component is present within the range from 5 to 50% by weight relative to the total weight of the catalytic converter.5. The catalytic converter according to claim 4 , wherein the inorganic porous filler component is present within the range from 10 to 25% by weight claim 4 , relative to the weight of the catalytic converter.6. The catalytic converter according to claim 1 , wherein the at least one porous filler component comprises a clay material.7. The ...

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14-01-2016 дата публикации

PHOTOCATALYTIC DEGRADATION OF SUGAR

Номер: US20160008783A1
Автор: Roundhill David Max
Принадлежит:

Systems having at least one photonic antenna molecule and at least one catalyst for degrading a sugar to degradation products using light energy are disclosed. Also disclosed are the devices and methods that use the systems for photocatalytically degrading a sugar into degradation products. 1. A system for photocatalytically degrading a sugar , the system comprising:at least one photonic antenna molecule; andat least one catalyst;wherein the photonic antenna molecule is capable of collecting a light energy and transferring the light energy to the catalyst; andwherein the catalyst is capable of degrading the sugar to produce at least one degradation product.2. The system of claim 1 , wherein the photonic antenna molecule is selected from the group consisting of 5-hydroxytryptamine claim 1 , an acridine claim 1 , an Alexa Fluor® dye claim 1 , an ATTO dye claim 1 , a BODIPY® dye claim 1 , Coumarin 6 claim 1 , a CY dye claim 1 , DAPI claim 1 , an ethidium compound claim 1 , a Hoechst dye claim 1 , Oregon Green claim 1 , rhodamine claim 1 , a compound comprising Ru(bpy) claim 1 , a compound comprising (Pt(pop)) claim 1 , a YOYO dye claim 1 , and a SeTau dye.3. The system of claim 1 , wherein the photonic antenna molecule is fluorescein.4. The system of claim 1 , wherein the catalyst is a metal nanoparticle.5. The system of claim 4 , wherein the metal nanoparticle comprises a metal selected from the group consisting of ruthenium claim 4 , palladium claim 4 , gold claim 4 , silver claim 4 , nickel claim 4 , tungsten claim 4 , molybdenum claim 4 , gallium claim 4 , iridium claim 4 , rhodium claim 4 , osmium claim 4 , copper claim 4 , cobalt claim 4 , iron claim 4 , and platinum claim 4 , or a mixture thereof.6. The system of claim 4 , wherein the metal nanoparticle comprises a lanthanide.7. The system of claim 4 , wherein the metal nanoparticle comprises a metal selected from the group consisting of platinum claim 4 , nickel claim 4 , and europium.8. The system of claim 5 , ...

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11-01-2018 дата публикации

ELECTRO-CATALYTIC HONEYCOMB FOR EXHAUST EMISSIONS CONTROL AND MANUFACTURING METHOD THEREOF

Номер: US20180008931A1
Принадлежит:

An electro-catalytic honeycomb for exhaust emissions control and manufacturing method thereof firstly provides a honeycomb structural body comprising a backbone, a solid-oxide layer, a cathode layer and an inner annular layer. The backbone is provided with an anode and gas channels. The anode is provided with an outer surface and an inner surface inside the gas channels. The solid-oxide layer is formed on the inner surface. The cathode layer is formed on the solid-oxide layer. The inner annular layer is allowed for encapsulating an annular end edge of the outer surface. Subsequently, a sealing body is provided over the inner annular layer. Then, the anode is reduced to a reducing environment. Finally, an encapsulation is provided over the honeycomb structural body to seal the outer surface and a sealing membrane of the sealing body is removed for passing a lean-burn exhaust through the gas channels. 1. A manufacturing method of an electro-catalytic honeycomb for exhaust emissions control , comprising the steps of:step 1: providing a honeycomb structural body, the honeycomb structural body including a backbone, a solid-oxide layer, a cathode layer and an inner annular layer, the backbone having an anode and a plurality of gas channels running through the anode, the anode being made of a first porous material, as well as the anode having an outer surface and an inner surface situated inside the gas channels, the solid-oxide layer being formed of a first dense structure and formed on the inner surface, as well as having a tube wall facing the gas channels, the cathode layer being made of a second porous material and adhered to the tube wall, the inner annular layer being formed of a second dense structure and encapsulating an annular end edge of the outer surface;step 2: covering the inner annular layer by a sealing body in such a way that the gas channels of the honeycomb structural body are formed as an enclosed chamber, the sealing body including a hollow outer ring ...

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11-01-2018 дата публикации

COMPOSITE WITH SYNERGISTIC EFFECT OF ADSORPTION AND VISIBLE LIGHT CATALYTIC DEGRADATION AND PREPARATION METHOD AND APPLICATION THEREOF

Номер: US20180008953A1
Принадлежит:

The invention discloses a composite with an adsorption-visible light catalytic degradation synergistic effect and a preparation method and application thereof. The preparation method includes the specific steps that firstly, a bismuth oxyiodide/bismuth oxychloride composite nano-particle loaded activated carbon fiber composite ACF@BiOIClis synthesized; then, the fiber surface is grafted with polyethyleneimine, and the end composite PEI-g-ACF@BiOIClis obtained. The composite can rapidly adsorb pollutants in water, and meanwhile the pollutants are efficiently degraded with a photocatalyst loaded on the surface of the composite; besides, the purpose of recycling and reusing the photocatalyst is achieved, the comprehensive treatment capability of the composite is improved, the service life of the composite is prolonged, and the use cost is lowered. 1. A preparation method of a composite with synergistic effect of adsorption and visible light catalytic degradation , which comprises the steps as below:1) preparation of activated carbon fibers with bismuth oxyiodide/bismuth oxychloride composite nanoparticles immobilized on:dissolving bismuth nitrate pentahydrate and activated carbon fiber in solvent to obtain solution A; dissolving potassium iodide and potassium chloride in solvent to obtain solution B; adding solution B to solution A under stirring, mixing evenly, then moving the reaction mixture to a hydrothermal reactor and reacting for 10 to 16 hours at 120 to 180° C., after the completion of the reaction, the reaction vessel is taken out, cooled and opened, and the fibrous product is collected by filtration, washed and dried to obtain bismuth oxyiodide/bismuth oxychloride composite nanoparticles immobilized activated carbon fiber composite;wherein,the molar ratio of bismuth nitrate pentahydrate, potassium iodide and potassium chloride is 1:x:(1−x), and 0 Подробнее

11-01-2018 дата публикации

MULTI-ZONED CATALYST SYSTEM FOR OXIDATION OF O-XYLENE AND/OR NAPHTHALENE TO PHTHALIC ANHYDRIDE

Номер: US20180008962A1
Принадлежит:

The present invention relates to a catalyst system for oxidation of o-xylene and/or naphthalene to phthalic anhydride (PA) comprising at least four catalyst zones arranged in succession in the reaction tube and filled with catalysts of different chemical composition wherein the active material of the catalysts comprise vanadium and titanium dioxide and the active material of the catalyst in the last catalyst zone towards the reactor outlet has an antimony content (calculated as antimony trioxide) between 0.7 to 3.0 wt. %. The present invention further relates to a process for gas phase oxidation in which a gas stream comprising at least one hydrocarbon and molecular oxygen is passed through a catalyst system which comprises at least four catalyst zones arranged in succession in the reaction tube and filled with catalysts of different chemical composition wherein the active materials of the catalysts comprise vanadium and titanium dioxide and the active material of the catalyst in the last catalyst zone towards the reactor outlet has an antimony content (calculated as antimony trioxide) between 0.7 to 3.0 wt. %. 114.-. (canceled)15. A catalyst system for oxidation of o-xylene and/or naphthalene to phthalic anhydride comprising at least four catalyst zones arranged in succession in the reaction tube and filled with catalysts of different chemical composition wherein the catalytically active material of the catalyst is applied to an inert catalyst carrier and comprises vanadium and titanium dioxide and the active material of the catalyst in the last catalyst zone towards the reactor outlet has an antimony content (calculated as antimony trioxide) between 0.7 to 3.0 wt. %.16. The catalyst system according to claim 15 , wherein the active materials of the catalysts in the last two catalyst zones towards the reactor outlet have a lower average antimony content than the active materials of the catalysts in the remaining catalyst zones towards the reactor inlet.17. The ...

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11-01-2018 дата публикации

CATALYZED CERAMIC CANDLE FILTER AND METHOD OF CLEANING PROCESS OFF- OR EXHAUST GASES

Номер: US20180008965A1
Принадлежит: Haldor Topsoe A/S

Ceramic candle filter and use of the filter in the removal of particulate matter in form of soot, ash, metals and metal compounds, together with hydrocarbons and optionally nitrogen oxides being present in process off-gas or engine exhaust gas, wherein a noble metal comprising catalyst is arranged on the permeation side of the filter and/or on the dispersion side of the filter and/or within wall of the filter, said noble metal comprising catalyst contains a noble metal in an amount of between 20 and 1000 ppm/weight of the filter. 1. A ceramic candle filter , wherein a noble metal comprising catalyst is arranged on the permeation side of the filter and/or on the dispersion side of the filter and/or within wall of the filter , said noble metal comprising catalyst contains a noble metal in a total amount of between 20 and 1000 ppm/weight of the filter.2. The ceramic candle filter of claim 1 , wherein the noble metal is palladium and/or platinum.3. The ceramic candle filter of claim 1 , wherein the noble metal comprising catalyst further comprises a vanadium oxide and titania.4. The ceramic candle filter according to claim 1 , wherein the ceramic material of the filter is selected from the group of silica-aluminate claim 1 , calcium-magnesium-silicates claim 1 , calcium-silicates fibers claim 1 , or a mixture thereof.5. The ceramic candle filter according to claim 4 , wherein the ceramic material of the filter consists of bio-soluble fibres selected from the group of calcium-magnesium-silicates.6. A method for the removal of particulate matter in form of soot claim 4 , ash claim 4 , metals and metal compounds claim 4 , together with hydrocarbons and carbon monoxide being present in process off-gas or engine exhaust gas claim 4 , comprising the steps ofpassing the off-gas or the exhaust gas through a ceramic candle filter and capturing the particulate matter;reducing amounts of soot in the particulate matter captured on dispersion side of the filter and reducing amounts ...

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11-01-2018 дата публикации

FERRITE PARTICLES PROVIDED WITH OUTER SHELL STRUCTURE FOR CATALYST SUPPORTING MEDIUM

Номер: US20180008966A1
Автор: AGA Koji, Sugiura Takao
Принадлежит: POWDERTECH CO., LTD.

An object of the present invention is to provide ferrite particles for supporting a catalyst having a small apparent density, various properties are maintained in a controllable state and a specified volume is filled with a small weight, and a catalyst using the ferrite particles for supporting a catalyst. To achieve the object, ferrite particles for supporting a catalyst provided with an outer shell structure containing Ti oxide, a catalyst using the ferrite particles for supporting a catalyst are employed. 1. Ferrite particles for supporting a catalyst characterized in provided with an outer shell structure containing Ti oxide.2. The ferrite particles for supporting a catalyst according to claim 1 , wherein the thickness of the outer shell structure is 0.5 to 10 μm.3. The ferrite particles for supporting a catalyst according to claim 1 , wherein the density of the internal part is lower than that of the outer shell structure.4. The ferrite particles for supporting a catalyst according to claim 1 , wherein the volume average particle diameter of the ferrite particles is 10 to 100 μm.5. A catalyst characterized in using the ferrite particles for supporting a catalyst according to as a catalyst supporting medium.6. The catalyst according to characterized in that a catalytically active component is at least one colloidal particle of a metal selected from gold claim 5 , silver claim 5 , copper claim 5 , platinum claim 5 , rhodium claim 5 , ruthenium claim 5 , palladium claim 5 , nickel claim 5 , and cobalt. The present invention relates to ferrite particles, and more particularly to ferrite particles for supporting a catalyst which is suitably used as a catalyst supporting medium and a catalyst using the ferrite particles as a catalyst supporting medium.Ferrite particles are used in various applications. For example, Patent Document 1 (Japanese Patent Laid-Open No. 6-313176) discloses a fluid catalytic cracking catalyst composed of zeolite as active component and a ...

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11-01-2018 дата публикации

HYBRID NANOSTRUCTURED PHOTOCATALYSTS AND PREPARATION METHOD THEREOF

Номер: US20180008967A1
Принадлежит:

The present invention relates to a hybrid nanostructured photocatalyst, comprising a first nanoparticle comprising silver halide (AgX); a second nanoparticle, which is formed on an outer surface of the first nanoparticle and comprises Ag; and a polymer formed on any one outer surface of the first nanoparticle and the second nanoparticle, and a preparation method thereof. Specifically, the present invention provides a hybrid nanostructured photocatalyst having a high photocatalytic activity in a visible light region and a preparation method thereof. 1. A hybrid nanostructured photocatalyst , comprising:a first nanoparticle comprising silver halide (AgX), wherein X is any of Cl, Br, and I;multiple second nanoparticles in a dendritic form on an outer surface of the first nanoparticle and comprising Ag; anda polymer formed on any one outer surface of the first nanoparticle and the multiple second nanoparticles.2. The hybrid nanostructured photocatalyst of claim 1 , wherein the first nanoparticle has at least one shape selected from the group consisting of a semi-sphere claim 1 , a sphere claim 1 , a truncated-cube claim 1 , and a cube.3. The hybrid nanostructured photocatalyst of claim 1 , wherein the second nanoparticle is formed on the outer surface of the first nanoparticle claim 1 , and the shape of the hybrid nanostructured photocatalyst is formed to correspond to the shape of the first nanoparticle.4. The hybrid nanostructured photocatalyst of claim 1 , wherein at least a part of the first nanoparticle and the second nanoparticle has a crystal structure.5. The hybrid nanostructured photocatalyst of claim 1 , wherein at least a part of the first nanoparticle and the second nanoparticle has a face-centered cubic structure.6. The hybrid nanostructured photocatalyst of claim 1 , wherein the photocatalyst has a band gap energy of 2.0 eV to 3.0 eV and a photocatalytic activity in a visible light region.7. (canceled)8. The hybrid nanostructured photocatalyst of claim 1 , ...

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27-01-2022 дата публикации

Honeycomb bodies having an array of channels with different hydraulic diameters and methods of making the same

Номер: US20220023792A1
Принадлежит: Corning Inc

A honeycomb body comprises a matrix of intersecting porous walls forming channels. Plugs are disposed in a percentage of the channels having the second hydraulic diameter, wherein the percentage of the channels of the second diameter having a plug is less than or equal to 15%. In some embodiments, some of the channels have a first hydraulic diameter and others have a second hydraulic diameter that is smaller than the first hydraulic diameter, and may be unplugged for plugged. The porous walls can further comprise a transverse thickness of the walls Tw less than or equal to 0.20 mm, a channel density CD greater than or equal to 62 channels per cm2, an average bulk porosity % P greater than or equal to 50%, and a median pore diameter d50 ranging from between 4.0 μm and 30.0 μm.

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14-01-2021 дата публикации

CATALYZED SCR FILTER AND EMISSION TREATMENT SYSTEM

Номер: US20210008531A1
Принадлежит:

Provided is a catalyst article for simultaneously remediating the nitrogen oxides (NOx), particulate matter, and gaseous hydrocarbons present in diesel engine exhaust streams. The catalyst article has a soot filter coated with a material effective in the Selective Catalytic Reduction (SCR) of NOx by a reductant, e.g., ammonia. 1. A catalyst article consisting essentially of a wall flow monolith and a catalytic material , wherein the wall flow monolith has a plurality of longitudinally extending passages fatined by longitudinally extending walls bounding and defining said passages , wherein the passages comprise inlet passages having an open inlet end and a closed outlet end , and outlet passages having a closed inlet end and an open outlet end , the wall flow monolith has a porosity of from 50% to 60% and an average pore size of from 10 to 25 microns , and the wall flow monolith contains the catalytic material;{'sup': '3', 'wherein the catalytic material comprises an SCR catalyst composition including a slurry-loaded washcoat of a zeolite and base metal selected from one or more of a copper and iron component, the washcoat permeating the walls at a loading up to 2.4 g/in, the wall flow monolith having integrated, NOx and particulate removal efficiency in which presence of the catalytic material in the wall flow monolith catalyzes the oxidation of soot.'}2. The catalyst article of claim 1 , wherein the SCR catalyst composition permeates the walls of the monolith at a concentration of at least 1.3 g/in.3. The catalyst article of claim 2 , wherein there is from 1.6 to 2.4 g/inof SCR catalyst composition disposed on the wall flow monolith.4. The catalyst article of claim 1 , wherein the SCR catalyst composition is effective to catalyze the reduction of NOx at a temperature below about 600° C. and is able to aid in regeneration of the wall flow monolith by lowering the temperature at which soot captured by the wall flow monolith is combusted.5. The catalyst article of ...

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14-01-2021 дата публикации

Improved Methods and Systems for Photo-Activated Hydrogen Generation

Номер: US20210008532A1
Принадлежит:

Systems and methods for providing alternative fuel, in particular hydrogen photocatalytically generated by a system comprising photoactive nanoparticles and a nitrogenase cofactor are provided. In one aspect, the system includes a water soluble cadmium selenide nanoparticle (CdSe) surface capped with mercaptosuccinate (CdSe-MSA) and a NafY.FeMo-co complex comprising a NafY protein and an iron-molybdenum cofactor (FeMo-co), wherein the CdSe-MSA and NafY.FeMo-co complex are present in about 1:2 to 1:10 molar ratio. 1. A system for photocatalytically producing hydrogen gas , comprising:a water soluble cadmium selenide nanoparticle (CdSe) surface capped with mercaptosuccinate (CdSe-MSA); anda NafY.FeMo-co complex comprising a NafY protein and an iron-molybdenum cofactor (FeMo-co);wherein the CdSe-MSA and NafY.FeMo-co complex are present in about 1:2 to 1:10 molar ratio.2. The system of claim 1 , wherein the CdSe-MSA and the NafY.FeMo-co complex are present in about 1:2 claim 1 , 1:3 claim 1 , 1:4 or 1:5 molar ratio.3. The system of claim 1 , further comprising sodium dithionite for providing protons and electrons.4. The system of claim 3 , wherein the dithionite salt is provided at a concentration of about 2 mM to 1 M claim 3 , or about 2-100 mM claim 3 , or about 2-10 mM.5. The system of claim 3 , further comprising an additional proton source such as ascorbic acid claim 3 , acetic acid claim 3 , citric acid claim 3 , and carbon dioxide.6. The system of claim 1 , wherein the system is capable of photocatalytically producing hydrogen gas for an extended period of about 5-90 days claim 1 , 10-72 days or 39-72 days.7. The system of claim 1 , wherein the system is kept under anaerobic conditions.8Azotobacter vinelandii.. The system of claim 1 , wherein the NafY protein is derived from9. The system of claim 1 , wherein the FeMo-co is derived from a molybdenum-iron (MoFe) protein.10Azotobacter vinelandii.. The system of claim 9 , wherein the MoFe protein is derived from11. A ...

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09-01-2020 дата публикации

SILVER CATALYST SYSTEM HAVING A REDUCED PRESSURE DROP FOR THE OXIDATIVE DEHYDROGENATION OF ALCOHOLS

Номер: US20200009535A1
Принадлежит:

The invention relates to a silver-comprising catalyst system for the preparation of aldehydes and/or ketones by oxidative dehydrogenation of alcohols, in particular the oxidative dehydrogenation of methanol to form formaldehyde, comprising a first catalyst layer and a second catalyst layer, wherein the first catalyst layer consists of a silver-comprising material in the form of balls of wire, gauzes or knitteds having a weight per unit area of from 0.3 to 10 kg/mand a wire diameter of from 30 to 200 μm and the second catalyst layer consists of a silver-comprising material in the form of granular material having an average particle size of from 0.5 to 5 mm and the two catalyst layers are in direct contact with one another. The invention further relates to a corresponding process for the preparation of aldehydes and/or ketones, in particular of formaldehyde, by oxidative dehydrogenation of corresponding alcohols over a silver-comprising catalyst system. 112.-. (canceled)14. The silver-comprising catalyst system according to claim 13 , wherein the silver-comprising material of the catalyst layer A has a weight per unit area in the range from 0.3 to 3 kg/mfor the entire catalyst layer A.15. The silver-comprising catalyst system according to claim 13 , wherein the silver-comprising material of the catalyst layer A has a wire diameter in the range from 30 μm to 150 μm.16. The silver-comprising catalyst system according to claim 13 , wherein the balls of wire claim 13 , gauzes and knitteds of the catalyst layer A consist of wires which are silver-comprising fibers or threads having an essentially circular cross section.17. The silver-comprising catalyst system according to claim 13 , wherein the silver-comprising material of the catalyst layer B has an average particle size in the range from 0.75 mm to 4 mm.18. The silver-comprising catalyst system according to claim 13 , wherein the silver-comprising material of the catalyst layer A has a silver content of >98% by weight. ...

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09-01-2020 дата публикации

PRECURSOR OF CATALYST FOR HYDROGENATION OF CARBON DIOXIDE AND MANUFACTURING METHOD THEREFOR, AND HYDROGENATION CATALYST OF CARBON DIOXIDE AND MANUFACTURING METHOD THEREFOR

Номер: US20200009537A1
Автор: CHOI Yohan, Lee Jae Sung
Принадлежит:

The present invention relates to a precursor of a hydrogenation catalyst of carbon dioxide, a method for preparing thereof, a hydrogenation catalyst of carbon dioxide, and a method for preparing thereof. An embodiment of the present invention provides a precursor of a hydrogenation catalyst of carbon dioxide comprising CuFeO. 1. A precursor of the hydrogenation catalyst of carbon dioxide comprising CuFeOhaving a particle diameter is 800 nm or less.2. The precursor of the hydrogenation catalyst of carbon dioxide of claim 1 , whereinthe precursor comprises a trigonal form.3. A method for preparing a precursor of the hydrogenation catalyst of carbon dioxide comprising:preparing an iron raw material and a copper raw material;adding the iron and copper raw materials into a solvent to prepare a solution;adding a reduction agent into the solution; andhydrothermal-synthesizing the solution in which the reduction agent is added to prepare a catalyst precursor;{'sub': '2', 'wherein the iron raw material is FeCl.'}4. The method for preparing a precursor of the hydrogenation catalyst of carbon dioxide of claim 3 , whereinthe solution is hydrothermally synthesized in the temperature range of 150 to 200° C. by the step of hydrothermal-synthesizing the solution in which the reduction agent is added to prepare a catalyst precursor.5. The method for preparing a precursor of the hydrogenation catalyst of carbon dioxide of claim 4 , whereinthe solution is hydrothermally synthesized for 30 minutes to 5 hours by the step of hydrothermal-synthesizing the solution in which the reduction agent is added to prepare a catalyst precursor.6. The method for preparing a precursor of the hydrogenation catalyst of carbon dioxide of claim 3 , wherein{'sub': 3', '2, 'the copper raw material is Cu(NO), CuCl or a combination thereof, in the step of preparing an iron raw material and a copper raw material.'}7. The method for preparing a precursor of the hydrogenation catalyst of carbon dioxide of claim ...

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09-01-2020 дата публикации

FIBROUS ZEOLITE CATALYST FOR HYDROCRACKING

Номер: US20200009542A1
Принадлежит:

A hydrocracking catalyst for petroleum hydrocracking is provided, the hydrocracking catalyst provided in a form of at least one fiber, and the at least one fiber comprising at least one zeolite and at least one metal oxide. Methods are also provided to form the hydrocracking catalyst in the form of at least one fiber, particularly electrospinning. 1. A hydrocracking catalyst for petroleum hydrocracking , comprising:the hydrocracking catalyst provided in a form of at least one fiber; andthe at least one fiber comprising at least one zeolite and at least one metal oxide.2. The catalyst of claim 1 , wherein:the at least one zeolite is a Y-zeolite.3. The catalyst of claim 2 , wherein:{'sub': 2', '2', '3, 'the Y-zeolite has a SiO/AlOmole ratio of at least 3 to 1.'}4. The catalyst of claim 1 , wherein:the at least one metal oxide is one of nickel oxide and tungsten trioxide.5. The catalyst of claim 1 , wherein:the at least one metal oxide further comprises at least a first metal oxide and a second metal oxide.6. The catalyst of claim 5 , wherein:the first metal oxide is nickel oxide; andthe second metal oxide is tungsten trioxide.7. The catalyst of claim 1 , wherein:81-87% by weight of the at least one fiber comprises the at least one zeolite; and1-19% by weight of the at least one fiber comprises the at least one metal oxide.8. The catalyst of claim 1 , wherein:the at least one fiber has a length in a range of 0.1-500 microns; andthe at least one fiber has a diameter in a range of 50-800 nanometers.9. The catalyst of claim 1 , wherein:the at least one fiber has a length-to-diameter aspect ratio in a range of 50:1 to 1,000:1.10. The catalyst of claim 1 , wherein:the hydrocracking catalyst is binder free.11. The catalyst of claim 1 , wherein:the at least one fiber comprises a plurality of fibers.12. The catalyst of claim 11 , wherein:the plurality of fibers form a fiber mat.13. A method of making a hydrocracking catalyst for petroleum hydrocracking claim 11 , comprising: ...

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14-01-2021 дата публикации

PARTIAL OXIDATION OF HYDROCARBONS

Номер: US20210009413A1
Автор: XU Bang-Cheng
Принадлежит:

A process of catalytic partial oxidation of hydrocarbons, particularly methane and/or natural gas to form a product containing hydrogen and carbon monoxide where the first catalyst comprises Co—Ni—Cr—W alloy. 1. A catalytic partial oxidation process comprising:passing a feed stream comprising a hydrocarbon feedstock and oxygen or an oxygen containing mixture through a reactor having at least a first reaction zone and a subsequent second reaction zone; andproducing an effluent stream comprising carbon monoxide and hydrogen, the first reaction zone comprises a first catalyst having a first surface area and a first thermal conductivity, the first catalyst comprising a Co—Ni—Cr—W alloy;', 'the second reaction zone comprises a second catalyst having a second surface area and a second thermal conductivity, the second catalyst comprising a second metal supported on a carrier;', 'the first surface area of the first catalyst is lower than the second surface area of the second catalyst; and', 'a pressure in said reactor is between about 600 kPa and about 7,500 kPa., 'wherein2. The catalytic partial oxidation process of claim 1 , wherein the Co—Ni—Cr—W alloy comprises 9.0-11.0 wt % Ni claim 1 , 19.0-21.0 wt % Cr claim 1 , 14.0-16.0 wt % W and balance Co.3. The catalytic partial oxidation process of claim 1 , wherein:{'sup': '2', 'the first thermal conductivity of the first catalyst is at least 0.05 cal/cm/cm/second/° C. at operating temperatures; and'}the first thermal conductivity of the first catalyst is higher than the second thermal conductivity of the second catalyst.4. The catalytic partial oxidation process of claim 1 , wherein the first thermal conductivity of the first catalyst is at least 0.10 cal/cm/cm/second/° C.5. The catalytic partial oxidation process of claim 1 , wherein the second metal is selected from the group consisting of iron claim 1 , cobalt claim 1 , nickel claim 1 , ruthenium claim 1 , rhodium claim 1 , palladium claim 1 , osmium claim 1 , iridium ...

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10-01-2019 дата публикации

CATALYSTS FOR PETROCHEMICAL CATALYSIS

Номер: US20190010096A1
Принадлежит:

Metal oxide catalysts comprising various dopants are provided. The catalysts are useful as heterogeneous catalysts in a variety of catalytic reactions, for example, the oxidative coupling of methane to C2 hydrocarbons such as ethane and ethylene. Related methods for use and manufacture of the same are also disclosed. 185-. (canceled)86. A method for the oxidative coupling of methane , the method comprising contacting methane with a catalyst at temperatures ranging from about 550° C. to about 750° C. , wherein the method comprises a methane conversion of greater than 20% and a C2 selectivity of greater than 50% , and wherein the catalyst comprises the following formula:{'br': None, 'sub': x', 'y', 'z, 'ABO;'} A is an element from the lanthanides or group 2, 3, 4, 6 or 13;', 'B is an element from groups 4, 12 or 13 of the periodic table or Ce, Pr, Nd, Sm, Eu, Gd, Tb or Ho;', 'O is an oxygen anion; and', 'x, y and z are each independently numbers greater than 0,, 'whereinthe catalyst further comprising one or more dopants from any one of groups 2, 3 or the lanthanides, and provided that A and B are not the same.87. The method of claim 86 , wherein A is Ba claim 86 , Zr claim 86 , Sr claim 86 , Sm claim 86 , Hf claim 86 , Gd claim 86 , Er claim 86 , Y claim 86 , Ca claim 86 , La claim 86 , Mg claim 86 , W claim 86 , B claim 86 , Tb or Ce.88. The method of claim 86 , wherein B is Zn claim 86 , Hf claim 86 , Zr claim 86 , Al claim 86 , Ti claim 86 , Pr claim 86 , Nd claim 86 , Ce claim 86 , Sm claim 86 , Eu claim 86 , Gd claim 86 , Tb or Ho.89. The method of claim 86 , wherein A is from group 2 claim 86 , and B is from group 4.90. The method of claim 86 , wherein A is Ba claim 86 , Sr or Ca.91. The method of claim 86 , wherein B is Ti claim 86 , Zr or Hf.92. The method of claim 86 , wherein the catalyst has the formula ABO.93. The method of claim 86 , wherein the catalyst comprises one or more dopant from group 2.94. The method of claim 86 , wherein the catalyst comprises ...

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03-02-2022 дата публикации

RADIAL OR AXIAL-RADIAL CHEMICAL REACTOR WITH A FINE CATALYST

Номер: US20220032251A1
Принадлежит:

Reactor for catalytic chemical reactions comprising a catalyst bed with an annular-cylindrical form crossed by a radial flow or mixed axial-radial flow, wherein the bed is delimited by cylindrical walls made gas-permeable by means of slits and the catalyst bed is formed by particles of catalyst with a nominal minimum size such that: the ratio between a transverse dimension of the slits and the nominal minimum size of the particles of catalyst is smaller than or equal to 0.6; the catalyst bed contains no more than 3% by weight of particles with an actual size smaller than said nominal size. 111-. (canceled)12. A reactor for catalytic chemical reactions , the reactor comprising:a catalyst bed with an annular-cylindrical form and a radial or mixed axial-radial crossing flow;at least a first cylindrical wall and a second cylindrical wall that delimit the catalyst bed being in direct with the catalyst, the second cylindrical wall being coaxial and internal relative to the first wall;wherein the first wall and the second wall include passages to make the first and second walls gas-permeable;wherein the passages are slits having an elongated form in a longitudinal direction of the slit and a respective transverse dimension in a transverse direction that is perpendicular to the longitudinal direction;wherein the catalyst bed is formed by particles of catalyst that have a nominal minimum size such that:a) a ratio between the transverse dimension of the slits and the nominal minimum size of the particles of catalyst is less than or equal to 0.6; 'wherein a minimum size of the catalyst is defined as a square root of a maximum square free flow area of a sieve that retains the catalyst, the sieving of the catalyst being performed according to the standard test method of ASTM D4513-11.', 'b) the catalyst bed contains no more than 3% by weight of particles with a size smaller than the nominal size,'}13. The reactor according to claim 12 , wherein the nominal minimum size of the ...

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03-02-2022 дата публикации

APPARATUS FOR PRODUCING LOWER OLEFIN-CONTAINING GAS AND METHOD FOR PRODUCING LOWER OLEFIN-CONTAINING GAS

Номер: US20220032252A1
Принадлежит: FURUKAWA ELECTRIC CO., LTD.

An apparatus and method for producing a lower olefin-containing gas including propylene from CHand COvia CO and Hwith high activity and high selectivity. The apparatus is provided with: a synthetic gas production unit to which a gas containing CHand COis supplied from a first supply unit, and which generates a synthetic gas containing CO and Hwhile heating a first catalytic structure; a gas production unit to which the synthetic gas is supplied and which generates a lower olefin-containing gas including propylene while heating a second catalytic structure; and a detection unit which detects propylene discharged from the gas production unit, in which the first catalytic structure includes first supports having a porous structure and a first metal fine particle in the first supports, the first supports have a first channels, the first metal fine particle is present in the first channels, the second catalyst structure includes second supports having a porous structure and a second metal fine particle in the second supports, the second supports have a second channels, and a portion of the second channels have an average inner diameter of 0.95 nm or less. 1. An apparatus for producing a lower olefin-containing gas containing propylene , the apparatus comprising:a first supply unit that supplies a raw material gas comprising methane and carbon dioxide;a synthesis gas production unit that comprises a first catalyst structure, receives supply of the raw material gas from the first supply unit, and produces a synthesis gas comprising carbon monoxide and hydrogen from methane and carbon dioxide in the raw material gas while heating the first catalyst structure;a second supply unit that supplies the synthesis gas discharged from the synthesis gas production unit;a lower olefin-containing gas production unit that comprises a second catalyst structure, receives supply of the synthesis gas from the second supply unit, and produces, from carbon monoxide and hydrogen in the ...

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03-02-2022 дата публикации

FUNCTIONAL STRUCTURE

Номер: US20220032276A1
Принадлежит:

A functional structure which can resist a decrease in the function of the functional material and thus have a long life, can be free from the need for complicated replacement operation, can contribute to resource-saving, and can exhibit high catalytic activity when used, for example, as a catalyst. The functional structure includes supports each having porous structure and including a zeolite-type compound, and at least one functional substance present in the supports, in which each of the supports has channels communicating with one another, the functional material is present at least in the channel of each of the supports, and the supports have an average external size of 20 μm or less. 1. A functional structure comprising:supports each having a porous structure and including a zeolite-type compound; andat least one functional material present in the supports, whereineach of the supports has channels communicating with one another,the functional material is present at least in the channel of each of the supports, andthe supports have an average external size of 20 μm or less.2. The functional structure according to claim 1 , whereinthe channels have any one of a one-dimensional pore, a two-dimensional pore, and a three-dimensional pore defined by framework structure of the zeolite-type compound, and have an enlarged pore portion different from the one-dimensional pore, the two-dimensional pore, and the three-dimensional pore, andthe functional material is present at least in the enlarged pore portion.3. The functional structure according to claim 2 , wherein the enlarged pore portion connects a plurality of pores constituting any one of the one-dimensional pore claim 2 , the two-dimensional pore claim 2 , and the three-dimensional pore.4. The functional structure according to claim 2 , wherein the functional material has an average particle size larger than an average inner diameter of the channels and equal to or smaller than an inner diameter of the enlarged ...

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19-01-2017 дата публикации

Apparatus and method for gaseous emissions treatment using front end induction heating

Номер: US20170014765A1
Принадлежит:

An assembly for treating gaseous emissions includes a substrate body having a front and a rear and cells for the passage of emissions gas. Inductance heating metal is located in the substrate body and an induction heating coil is mounted adjacent the substrate body for generating a varying electromagnetic field for inductively heating the metal and thereby heating the substrate body. A greater concentration of the metal is located near the front of the substrate body than near the rear. 1. An assembly for treating gaseous emissions comprising a substrate body having a front end , a rear end , a plurality of cells for the passage of emissions gas , inductance heating metal located in the substrate body , and an induction heating coil mounted adjacent the substrate body for generating a varying electromagnetic field , thereby inductively to heat the metal and thereby to heat the substrate body , wherein a greater concentration of the metal is located near the front end of the substrate body than near the rear end of the substrate body.2. The assembly of claim 1 , wherein the inductance heating metal is respective lengths of metal wire located in each of a first set of the plurality of cells3. The assembly of claim 1 , wherein claim 1 , the inductance heating metal is confined to a front part of the substrate body and the induction heating coil is mounted adjacent only a front part of the substrate body.4. The assembly of claim 2 , wherein at least some of the lengths of metal wire are wire segments shorter than the full length of the substrate body.5. The assembly of claim 2 , wherein end portions of the lengths of wire project from a front face of the substrate body at the front end.6. The assembly of claim 5 , wherein the induction heating coil extends beyond said front face so that a part thereof is mounted adjacent the projecting wire end portions.7. The assembly of claim 5 , wherein the projecting wire end portions taper towards the ends of the wires.8. The ...

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19-01-2017 дата публикации

Preparation method of fluorine-doped lamellar black titanium dioxide nano material

Номер: US20170014811A1
Принадлежит: NORTH CHINA ELECTRIC POWER UNIVERSITY

The method for preparing fluorine-doped lamellar black TiO 2 nanomaterials includes mixing a solution of tetra-n-butyl titanate, n-propanol and hydrofluoric acid together, and then stir the solutions for a period of time. The solution is transferred into an autoclave and reacts at a certain temperature for a period of time. The sample obtained by the reaction is washed and dried. Then, the sample is heated in a protective atmosphere for a period of time so as to produce the fluorine-doped lamellar black TiO 2 nanomaterials. This fluorine-doped lamellar black TiO 2 owns superior optical absorption and electron transport performances.

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19-01-2017 дата публикации

METHOD FOR IMPROVING SOLAR ENERGY CONVERSION EFFICIENCY USING METAL OXIDE PHOTOCATALYSTS HAVING ENERGY BAND OF CORE-SHELL FOR ULTRAVIOLET RAY AND VISIBLE LIGHT ABSORPTION AND PHOTOCATALYSTS THEREOF

Номер: US20170014813A1
Принадлежит:

The present invention discloses a method for improving solar energy conversion efficiency using metal oxide photocatalysts having an energy band of core-shell structure for ultraviolet (UV) ray and visible light absorption, comprising a first process of forming a nanoparticle thin film layer; a second process of preparing a core-shell metal oxide on metal oxide nanoparticles by a plasma reaction under a hydrogen and nitrogen gas atmosphere, and a third process of depositing a transition metal on surfaces of core-shell metal oxide nanoparticles to produce a photocatalyst for energy conversion. A great amount of oxygen vacancies is formed in a shell region by the core-shell metal oxide to achieve effects of improving transfer ability of electron-hole pairs excited by light, and extending a wavelength range of absorbable light to a visible light region by changing a band-gap structure. 1. A method for improving solar energy conversion efficiency using a metal oxide photocatalyst which has a core-shell energy band structure for absorption of ultraviolet (UV) ray and visible light , comprising:a first process of performing heat treatment on a metal oxide semiconductor having a band-gap to form a nanoparticle thin film layer;a second process of contacting a plasma ball including mixed gas in a substitutional NH or NHx radical state by a plasma reaction under a hydrogen and nitrogen gas atmosphere with a surface of a metal oxide particle to simultaneously generate a NH functional group and oxygen vacancies formed by hydrogenation, so as to prepare a core-shell metal oxide capable of absorbing UV ray and visible light; anda third process of further depositing a transition metal on surfaces of core-shell metal oxide nanoparticles to produce a photocatalyst of metal oxide-transition metal having a HN-core-shell structure for energy conversion.2. The method according to claim 1 , wherein the metal oxide and the transition metal include at least one element selected from Ti ...

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19-01-2017 дата публикации

PHOTOCATALYTIC ELEMENT

Номер: US20170014815A1
Принадлежит:

In an embodiment, there is provided a photocatalyst element comprising: a porous resin base material that comprises interconnecting pores, and a three-dimensional network skeleton forming the pores; and a photocatalyst which is supported on a surface of the three-dimensional network skeleton of the porous resin base material and/or contained in the three-dimensional network skeleton of the porous resin base material. The photocatalyst element has excellent antimicrobial effects. 1. A photocatalytic element comprising:a porous resin base material that comprises interconnecting pores, and a three-dimensional network skeleton forming the pores; anda photocatalyst which is supported on a surface of the three-dimensional network skeleton of the porous resin base material and/or contained in the three-dimensional network skeleton of the porous resin base material.2. The photocatalytic element according to claim 1 , wherein the resin constituting the porous resin base material comprises at least one selected from the group consisting of a thermosetting resin claim 1 , a thermoplastic resin claim 1 , a ultraviolet curable resin claim 1 , and an electron beam curable resin.3. The photocatalytic element according to claim 2 , wherein the resin constituting the porous resin base material contains an epoxy resin.4. The photocatalytic element according to claim 1 , wherein the photocatalyst shows a visible light responsiveness.5. The photocatalytic element according to claim 1 , wherein a co-catalyst is further supported on the surface of the three-dimensional network skeleton of the porous resin base material and/or contained in the three-dimensional network skeleton of the porous resin base material.6. The photocatalytic element according to claim 1 , wherein a photocatalyst layer containing the photocatalyst claim 1 , or a photocatalyst layer containing the photocatalyst and the co-catalyst is formed on the surface of the three-dimensional network skeleton of the porous resin ...

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18-01-2018 дата публикации

NICKEL-BASED CATALYST FOR THE DECOMPOSITION OF AMMONIA

Номер: US20180015443A1
Принадлежит:

The invention relates to a catalyst for the thermal decomposition of ammonia. The catalyst comprises at least 25% by weight of nickel oxide and is present in powder form and/or comprises from 30% to 42% by weight of nickel oxide. Also disclosed is a process for the thermal decomposition of ammonia into hydrogen and nitrogen, which process comprises contacting ammonia with the catalyst of the invention. 115.-. (canceled)16. A catalyst for the thermal decomposition of ammonia , wherein the catalyst (i) comprises at least 25% by weight of nickel oxide and is present in powder form and/or (ii) comprises from 30% to 42% by weight of nickel oxide.17. The catalyst of claim 16 , wherein the catalyst is present in powder form.18. The catalyst of claim 17 , wherein at least 50% of all powder particles have a particle size of not more than 0.5 mm.19. The catalyst of claim 17 , wherein at least 90% of all powder particles have a particle size of not more than 0.25 mm.20. The catalyst of claim 17 , wherein at least 95% of all powder particles have a particle size of not more than 0.1 mm.21. The catalyst of claim 17 , wherein not more than 10% of all powder particles have a particle size of more than 1 mm.22. The catalyst of claim 17 , wherein not more than 5% of all powder particles have a particle size of more than 0.7 mm.23. The catalyst of claim 17 , wherein the catalyst comprises at least 30% by weight of nickel oxide.24. The catalyst of claim 23 , wherein the catalyst comprises at least 34% by weight of nickel oxide.25. The catalyst of claim 17 , wherein the catalyst comprises not more than 42% by weight of nickel oxide.26. The catalyst of claim 25 , wherein the catalyst comprises not more than 38% by weight of nickel oxide.27. The catalyst of claim 17 , wherein the catalyst further comprises inert material comprising at least one of alumina and calcium aluminate.28. The catalyst of claim 16 , wherein the catalyst is present in partially or completely reduced form.29. The ...

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21-01-2016 дата публикации

Cobalt-Containing Fischer-Tropsch Catalysts, Methods of Making, and Methods of Conducting Fischer-Tropsch Synthesis

Номер: US20160016154A1
Принадлежит:

Catalyst compositions, methods of making catalysts, and methods of conducting Fischer-Tropsch (FT) reactions are described. It has been discovered that a combination of large crystallite size and high porosity results in catalysts and FT catalyst systems with high stability and low methane selectivity.

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19-01-2017 дата публикации

FLUORINE-CONTAINING TITANIUM OXIDE - NANO-SILICA COMPOSITE PARTICLES AND METHOD FOR PRODUCING THE SAME

Номер: US20170015833A1
Принадлежит:

Fluorine-containing titanium oxide—nano-silica composite particles comprising a condensate of a fluorine-containing alcohol and an alkoxysilane, and titanium oxide and nano-silica particles, wherein the fluorine-containing alcohol is represented by the general formula: 1. Fluorine-containing titanium oxide—nano-silica composite particles comprising a condensate of a fluorine-containing alcohol and an alkoxysilane , and titanium oxide and nano-silica particles , wherein the fluorine-containing alcohol is represented by the general formula:{'br': None, 'sub': 'F', 'R—A—OH\u2003\u2003[I]'}{'sub': 'F', '(wherein Ris a perfluoroalkyl group having 6 or less carbon atoms, or a polyfluoroalkyl group, in which some of the fluorine atom or atoms of the perfluoroalkyl group are replaced by a hydrogen atom or atoms, and which contains a terminal perfluoroalkyl group having 6 or less carbon atoms and a perfluoroalkylene group having 6 or less carbon atoms; and A is an alkylene group having 1 to 6 carbon atoms).'}2. The fluorine-containing titanium oxide—nano-silica composite particles according to claim 1 , wherein the fluorine-containing alcohol represented by the general formula [I] is a polyfluoroalkyl alcohol represented by the general formula:{'br': None, 'sub': n', '2n+1', '2', 'j, 'CF(CH)OH\u2003\u2003[II]'}wherein n is an integer of 1 to 6 and j is an integer of 1 to 6.3. The fluorine-containing titanium oxide—nano-silica composite particles according to claim 1 , wherein the fluorine-containing alcohol represented by the general formula [I] is a polyfluoroalkyl alcohol represented by the general formula:{'br': None, 'sub': n', '2n+1', '2', '2', 'a', '2', '2', 'b', '2', '2', 'c, 'CF(CHCF)(CFCF)(CHCH)OH\u2003\u2003[III]'}wherein n is an integer of 1 to 6, a is an integer of 1 to 4, b is an integer of 0 to 2, and c is an integer of 1 to 3.4. The fluorine-containing titanium oxide—nano-silica composite particles according to claim 1 , wherein the alkoxysilane is a silane ...

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17-01-2019 дата публикации

CATALYST FOR METAL MERCURY OXIDATION REACTIONS AND NITROGEN OXIDE REDUCTION REACTIONS, AND EXHAUST GAS PURIFICATION METHOD

Номер: US20190015821A1
Принадлежит: Mitsubishi Hitachi Power Systems, Ltd.

A catalyst for oxidation reaction of metallic mercury and reduction reaction of nitrogen oxide, comprising an oxide of titanium, an oxide of molybdenum, an oxide of vanadium, an oxide of phosphorus and gypsum is obtained by kneading titanium dioxide, ammonium molybdate, ammonium metavanadate, phosphoric acid, gypsum dihydrate and water using a kneader to obtain a paste, applying the paste to a metal lath substrate, and then drying and calcining the resultant. 1. A catalyst for oxidation reaction of metallic mercury and reduction reaction of nitrogen oxide , comprising:an oxide of titanium,an oxide of molybdenum and/or tungsten,an oxide of vanadium,an oxide of phosphorus, andgypsum.2. The catalyst according to claim 1 , wherein a ratio of the dry-based mass of gypsum dihydrate to the mass of the oxide of titanium is 1/99 to 40/60.3. A method for exhaust gas purification claim 1 , comprising bringing an exhaust gas containing metallic mercury claim 1 , nitrogen oxide and sulfur dioxide in contact with a catalyst comprising an oxide of titanium claim 1 , an oxide of molybdenum and/or tungsten claim 1 , an oxide of vanadium claim 1 , an oxide of phosphorus and gypsum to oxidize the metallic mercury and reduce the nitrogen oxide. The present invention relates to a catalyst for oxidation reaction of metallic mercury and reduction reaction of nitrogen oxide, and a method for exhaust gas purification. More specifically, the present invention relates to a catalyst that is capable of accelerating gas phase oxidation reaction of metallic mercury and gas phase reduction reaction of nitrogen oxide, and is also capable of suppressing gas phase oxidation reaction of sulfur dioxide, as well as a method for purifying exhaust gas, which comprises oxidizing metallic mercury and reducing nitrogen oxide.There is concern that metallic mercury contained in flue gas discharged from power stations, factories, automobiles and the like affects the environment. Hence, removal of metallic ...

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17-01-2019 дата публикации

CATALYST, STRUCTURES, REACTORS, AND METHODS OF FORMING SAME

Номер: US20190015825A1
Принадлежит:

Structures, catalysts, and reactors suitable for use for a variety of applications, including gas-to-liquid and coal-to-liquid processes and methods of forming the structures, catalysts, and reactors are disclosed. The catalyst material can be deposited onto an inner wall of a microtubular reactor and/or onto porous support structures using atomic layer deposition techniques. 1. A catalyst structure comprising:a support structure having a surface comprising one or more crystalline regions; and{'sup': '2', 'a crystalline catalyst layer formed overlying the one or more crystalline regions, wherein the support structure has a surface area greater than or equal to 50 m.'}2. The catalyst support structure of claim 1 , wherein the crystalline catalyst layer is deposited onto the support structure using ALD.3. The catalyst support structure of claim 1 , wherein the support structure comprises an oxide.4. The catalyst support structure of claim 1 , wherein the support structure comprises heat-conductive material.5. The catalyst support structure of claim 1 , wherein the support structure comprises one or more of gamma alumina claim 1 , delta alumina claim 1 , theta alumina claim 1 , and alpha alumina.6. The catalyst support structure of claim 1 , wherein the support structure comprises ALD deposited material terminated with organic material.7. The catalyst support structure of claim 1 , wherein the support structure comprises a carbon-containing protective layer.8. A method of forming a catalyst claim 1 , the method comprising the steps of:forming an oxide support structure;heat treating the oxide support structure to form one or more crystalline regions; andforming a catalyst layer overlying the one or more crystalline regions, wherein the catalyst layer comprises crystalline planes.9. The method of claim 8 , wherein the support structure has a surface area greater than or equal to 50 m.10. The method of claim 8 , wherein the step of forming comprises ALD deposition.11. ...

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18-01-2018 дата публикации

CATALYTIC MEMBRANE REACTOR FOR DIMETHYL ETHER SYNTHESIS FROM CARBON DIOXIDE AND HYDROGEN

Номер: US20180016218A1
Принадлежит: GAS TECHNOLOGY INSTITUTE

Methods and systems or devices for synthesis of dimethyl ether (DME) from carbon dioxide and hydrogen are provided. A high surface area hollow fiber catalytic membrane reactor such as with hollow fibers coated with a water permeable membrane material is used. The reactor also contains a bi-functional methanol synthesis component and dehydration catalyst component such that the two-step reaction takes place on the catalyst surface. Produced water permeates through the membrane, exiting the reactor immediately after it is formed. Unreacted reactants and products flow to the reactor exit. 1. A system for synthesis of dimethyl ether from carbon dioxide and hydrogen , the system comprising:a catalytic membrane reactor including a plurality of channels and having an outer surface with a water permeable membrane coating, the reactor further containing a bi-functional catalyst material including a methanol synthesis catalyst component to catalyze reaction of carbon dioxide and hydrogen to form methanol and water and a dehydration catalyst component to catalyze dehydration of methanol to form dimethyl ether,wherein upon formation formed water permeates through the water permeable membrane coating and exits the reactor.2. The system of wherein the catalytic membrane reactor comprises at least one of: a) at least one reactor body including at least two of said channels and b) a plurality of hollow fibers claim 1 , each fiber forming at least one of said channels.3. The system of wherein the catalytic membrane reactor comprises at least one reactor body including at least two of said channels.4. The system of wherein each of the channels includes an inner surface claim 3 , wherein the bi-functional catalyst material is disposed on the inner surface of the channels claim 3 , and wherein formed water permeates through the reactor body and the water permeable membrane coating to a shell side of the reactor.5. The system of wherein the catalytic membrane reactor comprises a ...

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17-01-2019 дата публикации

CATALYTIC BODY COATED WITH METAL OXIDE, METHOD OF MANUFACTURING THE SAME, AND METHOD OF PREPARING 1,3-BUTADIENE USING THE SAME

Номер: US20190016649A1
Принадлежит:

According to an embodiment of the present invention, there are provided a catalytic body, a method of manufacturing the same, and a method of preparing 1,3-butadiene using the same. The catalytic body includes an inactive support; an intermediate layer disposed on a surface of the inactive support; and an active layer disposed on a surface of the intermediate layer, wherein the active layer includes catalyst powder and a binder. 1. A catalytic body comprising:an inactive support;an intermediate layer disposed on a surface of the inactive support; andan active layer disposed on a surface of the intermediate layer,wherein the active layer includes catalyst powder and a binder.2. The catalytic body of claim 1 , wherein the inactive support has a porosity of 70 vol % or less.3. The catalytic body of claim 2 , wherein the inactive support is of one shape selected from the group consisting of a spherical shape claim 2 , a cylindrical shape claim 2 , a ring shape claim 2 , a platy shape claim 2 , and a combination of two or more thereof.4. The catalytic body of claim 3 , wherein the inactive support is one selected from the group consisting of alumina claim 3 , silica claim 3 , zirconia claim 3 , silicon carbide claim 3 , cordierite claim 3 , and a combination of two or more thereof.5. The catalytic body of claim 1 , wherein the intermediate layer may consist of one selected from the group consisting of alumina claim 1 , silica claim 1 , kaolin claim 1 , TiO claim 1 , ZnO claim 1 , bentonite claim 1 , and a combination of two or more thereof.6. The catalytic body of claim 1 , wherein the intermediate layer has a weight of 3 to 15 g/L with respect to a volume of the inactive support.7. The catalytic body of claim 1 , wherein the catalyst powder is an oxide derived from one selected from the group consisting of iron claim 1 , magnesium claim 1 , manganese claim 1 , zinc claim 1 , bismuth claim 1 , molybdenum claim 1 , and a combination of two or more thereof.8. The catalytic ...

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21-01-2021 дата публикации

PHOTOCATALYST TRANSFER FILM AND PRODUCTION METHOD THEREOF

Номер: US20210016249A1
Принадлежит: SHIN-ETSU CHEMICAL CO., LTD.

Provided are a photocatalyst transfer film allowing a uniform and highly transparent photocatalyst layer to be transferred to the surfaces of various transfer base materials; and a production method thereof. The photocatalyst transfer film has, on a biaxially oriented polypropylene film, a photocatalyst layer containing a titanium oxide particle-containing photocatalyst, a silicon compound and a surfactant. The production method of the photocatalyst transfer film includes applying a photocatalyst coating liquid to a biaxially oriented polypropylene film; and performing drying. The photocatalyst coating liquid contains a titanium oxide particle-containing photocatalyst, a silicon compound, a surfactant and an aqueous dispersion medium. 1. A photocatalyst transfer film having , on a biaxially oriented polypropylene film , a photocatalyst layer containing a titanium oxide particle-containing photocatalyst , a silicon compound and a surfactant.2. The photocatalyst transfer film according to claim 1 , wherein the silicon compound is a hydrolysis condensate of a tetrafunctional silicon compound claim 1 , the hydrolysis condensate being obtained under the presence of an organic ammonium salt.3. The photocatalyst transfer film according to claim 1 , wherein the surfactant is an acetylene-based surfactant.4. The photocatalyst transfer film according to claim 1 , wherein the photocatalyst layer has a thickness of 20 to 300 nm.5. The photocatalyst transfer film according to claim 1 , wherein the biaxially oriented polypropylene film has a thickness of 12.5 to 100 μm.6. The photocatalyst transfer film according to claim 1 , wherein a protective layer containing a silicon compound is further laminated on the photocatalyst layer.7. A method for producing a photocatalyst transfer film claim 1 , comprising:applying a photocatalyst coating liquid to a biaxially oriented polypropylene film, the photocatalyst coating liquid containing a titanium oxide particle-containing photocatalyst ...

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16-01-2020 дата публикации

METHOD FOR APPLYING PHOTOCATALYTIC COATINGS WITHOUT USING BINDERS, AND USE OF A COATING

Номер: US20200016587A1
Принадлежит:

The invention relates to a method for applying titanium dioxide-based photocatalytic coatings to a carrier material without using binders. The invention also relates to the use of a coating. According to the invention, a titanium dioxide suspension together with a carrier liquid is sprayed onto a hot carrier in the form of a fine aerosol so that the carrier liquid flash evaporates and titanium dioxide particles of the titanium dioxide suspension are flash sintered onto the carrier material, water being used as the carrier liquid and the carrier material having a temperature of 150 to 250° C. during spraying. According to the invention, a porous and yet stable layer for a catalyst for an efficient and rapid degradation of pollutants is produced. 1. A method for binder-free application of titanium dioxide-based photocatalytic coatings to a support material , where a titanium dioxide suspension with a carrier liquid is sprayed in the form of a fine aerosol onto a hot support , so that the carrier liquid undergoes flash evaporation and titanium dioxide particles of the titanium dioxide suspension undergo flash sintering onto the support material , the carrier liquid used being water , during the sprayed application, the support material has a temperature of 150 to 250° C., thus forming a porous and yet stable layer for a catalyst for efficient and rapid pollutant degradation,', 'the heat is generated in the support material itself, and', 'the support material is traversed by an electrical current., 'characterized in that'}2. The method as claimed in claim 1 , characterized in that during the sprayed application claim 1 , the support material has a temperature which lies above the boiling temperature of the carrier liquid.3. The method as claimed in claim 1 , characterized in that the titanium dioxide suspension has a fraction of 5 to 20 mass % of titanium dioxide particles.4. The method as claimed in claim 1 , characterized in that the method is multiply repeated.5. ( ...

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21-01-2021 дата публикации

CERIUM MANGANESE CATALYST, PREPARATION METHOD THEREFOR AND USE THEREOF

Номер: US20210016255A1
Принадлежит:

A cerium manganese catalyst for ozone decomposition, which is mainly a composite oxide of MnOand CeOwith the chemical constitution of CeMnO, a being a natural number selected from 6 to 15. A method for preparing a catalyst comprises: mixing a solution containing a cerium source and a manganese source with excessive urea, reacting to obtain a precipitate, washing the precipitate to neutral, drying, and roasting to obtain the cerium manganese catalyst. 1. A cerium-manganese catalyst , wherein the cerium-manganese catalyst has a following chemical composition: CeMnO , a value of a in CeMnOis a natural number selected from 6 to 15 , and the cerium-manganese catalyst is mainly a composite oxide of MnOand CeO.2. The cerium-manganese catalyst according to claim 1 , wherein the cerium-manganese catalyst is in a form of particles.3. A method for preparing a cerium-manganese catalyst claim 1 , comprising: mixing a solution containing a cerium source and a manganese source with excess urea claim 1 , carrying out a reaction to obtain a precipitate claim 1 , washing the precipitate to a neutral pH claim 1 , drying claim 1 , and calcining to obtain the cerium-manganese catalyst.4. The preparation method according to claim 3 , wherein a molar ratio of cerium in the cerium source to manganese in the manganese source is 1:(6-15).5. The preparation method according to claim 3 , wherein a temperature of the reaction is 60° C. to 100° C.6. The preparation method according to claim 3 , wherein the cerium source is selected from one or a mixture of at least two of cerium nitrate claim 3 , cerium sulfate claim 3 , cerium acetate or cerium chloride.7. The preparation method according to claim 3 , wherein the manganese source is selected from one or a mixture of at least two of manganese nitrate claim 3 , manganese sulfate claim 3 , manganese acetate or manganese chloride.8. The preparation method according to claim 3 , wherein a period for the reaction is 8 to 24 hours.9. The preparation ...

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21-01-2021 дата публикации

CATALYTIC TEST PAPER PREPARED BY COMPOSITING METAL PARTICLE-EMBEDDED BACTERIAL CELLULOSE WITH PLANT FIBERS, AND METHOD THEREFOR

Номер: US20210016264A1
Принадлежит: SOUTH CHINA UNIVERSITY OF TECHNOLOGY

Disclosed is a catalytic test paper prepared by compositing metal particle-embedded bacterial cellulose with plant fibers, and a preparation method therefor. Hydroxyl groups of bacterial cellulose are bonded with a nitrogen-containing or phosphorus-containing organic small molecule compound. By means of a chelation between a nitrogen or phosphorus atom with a metal, transition metal ions are adsorbed to a nanoporous surface of bacterial cellulose, and the transition metal ions are reduced in situ to obtain bacterial cellulose embedded with metal nanoparticles. The bacterial cellulose is composited with the plant fiber, and the catalytic test paper is prepared by a papermaking method. The catalytic test paper has the advantages of convenient use and recovery, high reusability, simple design, low manufacturing cost, higher catalytic efficiency, a green degradable support material, etc. 1. A method for preparing a catalytic test paper by compositing metal particle-embedded bacterial cellulose with plant fibers , characterized in that , the method comprises the following steps:(1) chemically bonding a nitrogen-containing or phosphorus-containing organic small molecule compound with hydroxyl groups in a structure of bacterial cellulose to obtain a functionalized bacterial cellulose having a nitrogen or phosphorus-containing group;(2) preparing an aqueous solution of an inorganic salt of a transition metal, adding the aqueous solution into the functionalized bacterial cellulose prepared in the step (1), stirring and reacting according to a solubility of the inorganic salt of the transition metal until the nitrogen-containing or phosphorus-containing group adsorbs transition metal ions onto a nanoporous surface of the bacterial cellulose till saturation, separating and washing with water;(3) reducing the transition metal ions adsorbed on the surface of the bacterial cellulose in the step (2) in situ to obtain bacterial cellulose embedded with transition metal nanoparticles ...

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17-01-2019 дата публикации

PURIFICATION AND DECOLORIZATION OF POLYMERS

Номер: US20190016860A1
Принадлежит:

Methods according to the present invention decolorize a polymer by mixing a solution of the polymer with a photocatalyst and exposing the mixture to ultraviolet light; by way of non-limiting example, the polymer may be a star polymer and the photocatalyst may be titanium dioxide. Methods according to the present invention also utilize a metal scavenger, in some embodiments a solid-phase metal scavenger, to remove a metal catalyst from a polymer solution; by way of non-limiting example, the metal catalyst may be a tin catalyst. The decolorization methods and the catalyst removal methods of the present invention may be practiced separately, sequentially in any order, or simultaneously. 1. A method for decolorization of a polymer composition comprising a polymer and a solvent , comprising:(a) adding a photocatalyst to the polymer composition, and(b) exposing the polymer composition to ultraviolet (UV) light to remove color from the polymer composition.2. A method for preparing a polymer composition comprising a polymer and a solvent , comprising:(a) adding a metal scavenger to the polymer composition to form a complex with a metal contaminant in the polymer composition;(b) separating the metal scavenger and metal contaminant complex from the polymer;(c) adding a photocatalyst to the polymer composition;(d) exposing the polymer composition to ultraviolet (UV) light to remove color from the polymer composition; and(e) separating the photocatalyst from the polymer composition.3. A method for preparing a polymer composition comprising a polymer and a solvent , comprising:(a) adding a metal scavenger to the polymer composition to form a complex with a metal contaminant in the polymer composition; and(b) separating the metal scavenger and metal contaminant complex from the polymer,wherein the metal scavenger is a metal scavenger chelating agent.4. A method for preparing a pharmaceutical composition , comprising:(a) treating a polymer composition comprising a polymer and a ...

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16-01-2020 дата публикации

CATALYSTS AND METHODS FOR NATURAL GAS PROCESSES

Номер: US20200017423A1
Принадлежит:

Catalysts and catalytic methods are provided. The catalysts and methods are useful in a variety of catalytic reactions, for example, the oxidative coupling of methane. 1. A catalyst comprising the following formula (IA):{'br': None, 'sub': x', 'y', 'v', 'w', 'z, 'ABCDO\u2003\u2003 (IA)'}wherein:A is a lanthanide or group 4 element;B is a group 2 element;C is a group 13 element;D is a lanthanide element;O is oxygen;v and w are independently numbers greater than 0;{'sub': x', 'y', 'v', 'w', 'z, 'x, y and z are independently numbers greater than 0, and v, w, x, y and z are selected such that ABCDOhas an overall charge of 0.'}2. The catalyst of claim 1 , wherein A is a lanthanide.3. The catalyst of claim 2 , wherein A is lanthanum claim 2 , cerium claim 2 , praseodymium or neodymium.4. The catalyst of claim 1 , wherein A is a Group 4 element.5. The catalyst of claim 4 , wherein A is titanium claim 4 , zirconium or hafnium.6. The catalyst of claim 1 , wherein B is magnesium claim 1 , calcium claim 1 , strontium or barium.7. The catalyst of claim 1 , wherein A is lanthanum and B is strontium claim 1 , A is cerium and B is barium claim 1 , A is praseodymium and B is barium claim 1 , A is cerium and B is strontium claim 1 , A is titanium and B is barium claim 1 , A is titanium and B is strontium or A is titanium and B is calcium.8. The catalyst of claim 1 , wherein C is aluminum claim 1 , gallium claim 1 , indium or thallium.9. The catalyst of claim 1 , wherein D is lanthanum claim 1 , neodymium claim 1 , gadolinium or ytterbium.10. The catalyst of claim 1 , wherein:A is titanium, zirconium or cerium;B is calcium, strontium or barium;C is aluminum, gallium or indium; andD is lanthanum, neodymium; gadolinium or ytterbium.11. The catalyst of claim 1 , comprising one of the following formulas: CeBaInNdO; TiCaInLaO; TiCaInNdO; TiCaInGdO; TiCaInYbO; ZrCaInLaO; ZrCaInNdO; ZrCaInGdO; ZrCaInYbO; CeCaInLaO; ZrCaInNdO; ZrCaInGdO; ZrCaInYbO; TiSrInLaO; TiSrInNdO; TiSrInGdO; TiSrInYbO; ...

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26-01-2017 дата публикации

GLASS ARTICLE PROVIDED WITH PHOTOCATALYST FILM, PROCESS FOR PRODUCING GLASS ARTICLE, AND COATING LIQUID

Номер: US20170021335A1
Принадлежит:

The present invention provides a glass article including a photocatalyst film containing silicon oxide particles and titanium oxide particles and a glass sheet Assuming that the photocatalyst film has a film thickness T, 80% or more of the titanium oxide particles are localized in a region between a surface of the glass sheet and a position spaced from the surface by 0.6 T toward a surface of the photocatalyst film in a thickness direction of the photocatalyst film The glass article has an increased transmittance provided by enhancing the reflection-reducing function of the photocatalyst film while maintaining the film strength and photocatalytic function of the photocatalyst film 13-. (canceled)4. A glass article comprising a glass sheet and a photocatalyst film formed on a surface of the glass sheet , whereinthe photocatalyst film contains silicon oxide particles, titanium oxide particles, and a binder material whose main component is silicon oxide,the silicon oxide particles are contained in an amount of 72 to 79 mass %, the titanium oxide particles are contained in an amount of 13 to 18 mass %, and the binder material is contained in an amount of 8 to 12 mass %, with respect to a total amount of the silicon oxide particles, the titanium oxide particles, and the binder material,the silicon oxide particles have an average particle diameter of 50 nm to 150 nm, the titanium oxide particles have an average particle diameter of 5 nm to 20 nm, and the average particle diameter of the silicon oxide particles is five times or more of the average particle diameter of the titanium oxide particles, andassuming that the photocatalyst film has a film thickness T, 80% or more of the titanium oxide particles are present between the surface of the glass sheet and a position spaced from the surface of the glass sheet by 0.6 T toward a surface of the photocatalyst film in a thickness direction of the photocatalyst film.5. The glass article according to claim 4 , wherein the ...

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25-01-2018 дата публикации

CERIUM-ZIRCONIUM COMPOSITE OXIDE, PREPARATION METHOD THEREFOR, AND APPLICATION OF CATALYST

Номер: US20180021759A1
Принадлежит:

Provided are a cerium-zirconium composite oxide, a preparation method therefor and application of a catalyst. The cerium-zirconium composite oxide has a composite phase structure, and comprises a cerium oxide phase and a cerium-zirconium solid solution phase, or consists of two or more cerium-zirconium solid solution phases with different crystal structures and different chemical compositions, wherein the chemical formula of the cerium-zirconium solid solution phase is CeZrMO, where M is at least one selected from the group consisting of a rare earth element other than cerium, a transition metal element and an alkaline earth metal element, x is 15-85 mol %, and y is 0-20 mol %. 1. A cerium-zirconium composite oxide , wherein the cerium-zirconium composite oxide has a composite phase structure , and comprises a cerium oxide phase and a cerium-zirconium solid solution phase , wherein the chemical formula of the cerium-zirconium solid solution phase is CeZrMO , where M is at least one selected from the group consisting of a rare earth element other than cerium , a transition metal element and an alkaline earth metal element , x is 15˜85 mol % , and y is 0˜20 mol %.2. The cerium-zirconium composite oxide as claimed in claim 1 , wherein after the cerium-zirconium composite oxide is subjected to heat preservation at 1000° C. for 4 hours claim 1 , the cerium oxide phase has a proportion of 0.5˜30 vol % in the cerium-zirconium composite oxide claim 1 , preferably 3˜20 vol %.3. The cerium-zirconium composite oxide as claimed in claim 1 , wherein the cerium-zirconium composite oxide comprises cerium oxide needle-like particles and cerium-zirconium solid solution near-spherical particles claim 1 , and after being subjected to heat preservation at 1000° C. for 4 hours claim 1 , the cerium oxide needle-like particles have a diameter of 7˜20 nm and a length of 50˜300 nm claim 1 , the cerium-zirconium solid solution near-spherical particles have a diameter of 5˜30 nm claim 1 , and ...

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10-02-2022 дата публикации

SURFACE COATINGS FOR SELF-DECONTAMINATION

Номер: US20220040674A1
Автор: Young Roger K.
Принадлежит: Pure-Light Technologies, Inc.

An apparatus includes a substrate having a surface and a transparent photocatalyst coating secured on the surface of the substrate, wherein the transparent photocatalyst coating includes titanium oxide and a component selected from a fluorescent dye, ultra-fine glitter, indium tin oxide, aluminum zinc oxide, silver nitrate, and combinations thereof. The substrate is preferably selected from an appliance handle, doorknob, switch, keyboard, countertop, appliance handle, equipment button, touchscreen, handrail, light emitting device, and light cover. Such substrates are frequently touched by one or more users and may become contaminated. However, the transparent photocatalyst coating may be self-decontaminating. 1. An apparatus , comprising:a substrate having a surface; anda transparent photocatalyst coating secured on the surface of the substrate, wherein the transparent photocatalyst coating includes titanium oxide and a component selected from a fluorescent dye, ultra-fine glitter, indium tin oxide, aluminum zinc oxide, silver nitrate, and combinations thereof.2. The apparatus of claim 1 , wherein the substrate is selected from an appliance handle claim 1 , doorknob claim 1 , switch claim 1 , keyboard claim 1 , countertop claim 1 , appliance handle claim 1 , equipment button claim 1 , touchscreen claim 1 , handrail claim 1 , light emitting device claim 1 , and light cover.3. The apparatus of claim 1 , wherein the photocatalyst coating is transparent.4. The apparatus of claim 3 , wherein the photocatalyst coating is secured to the surface of the substrate by a layer of a binder disposed between the surface of the substrate and the photocatalyst coating claim 3 , wherein the binder layer is transparent.5. The apparatus of claim 1 , wherein the photocatalyst coating is formed from a mixture including a titanium oxide sol and an amorphous titanium peroxide sol claim 1 , wherein the mixture includes less than or equal to 30 weight percent (wt %) titanium oxide sol based ...

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10-02-2022 дата публикации

THREE-DIMENSIONALLY ORDERED MACROPOROUS OXYGEN-DEFICIENT CERIUM DIOXIDE CATALYST, AND PREPARATION METHOD AND APPLICATION THEREOF

Номер: US20220040675A1
Принадлежит: GUANGDONG UNIVERSITY OF TECHNOLOGY

The present application is related to a three-dimensionally ordered macroporous oxygen-deficient cerium dioxide catalyst, and a preparation method and an application thereof. The catalyst is prepared by using a polymethyl methacrylate (PMMA) colloidal crystal template method, calcining in a reducing/oxidizing atmosphere, and treating with water vapor, and the prepared catalyst shows an excellent activity and stability in photothermocatalytic purification of typical amospheric pollutants such as styrene, n-hexane, and cyclohexane. The method has the characteristics of cheap and easily available raw materials, simple preparation process, controllable oxygen vacancy, surface acid amount, and acid strength of the obtained material, and excellent photothermocatalytic performance. 1. A preparation method of a three-dimensionally ordered macroporous oxygen-deficient cerium dioxide catalyst , comprising following steps of:S1: adding cerium nitrate hexahydrate and citric acid monohydrate powder into an alcohol solution to obtain an even transparent solution A after ultrasonic treatment;S2: immersing polymethyl methacrylate microsphere powder in the solution A, carrying out ultrasonic homogenization, then removing excess liquid by suction filtration to obtain a solid B, and sequentially carrying out vacuum drying, calcination I, and calcination II on the solid B to obtain a solid C; andS3: transferring the solid C obtained in the step S2 into a fixed bed reactor, and then carrying out calcination III, water vapor treatment, and calcination IV to obtain the three-dimensionally ordered macroporous oxygen-deficient cerium dioxide catalyst;wherein the calcination III and the water vapor treatment in the step S3 are carried out at the same time, and comprise processes of: controlling a humidity in the reactor to be 10% to 90% by using a nitrogen bubbling device, and calcinating at 200° C. to 600° C. for 1 hour to 24 hours in a mixed gas atmosphere of hydrogen and nitrogen with a ...

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10-02-2022 дата публикации

Catalyst Compositions and Methods for Producing Long-Chain Hydrocarbon Molecules

Номер: US20220040679A1
Автор: WANG Cong

Provided is a nanostructure catalyst composition and a method for producing organic molecules having at least two carbon atoms chained together by the reaction of a hydrogen-containing source, a carbon-containing source and an optional nitrogen-containing source. Composition of the nanostructure catalyst affects the solar-to-chemical efficiency, active lifetime and reaction product of the artificial photosynthesis reaction. 1. A nanostructure catalyst composition , comprising:at least one plasmonic provider; andat least one catalytic property provider, whereinthe plasmonic provider and the catalytic property provider are in contact with each other or have a distance of less than 200 nm apart from each other, andthe plasmonic provider is about 0.1%-30% by mole of a total mole of the plasmonic provider and the catalytic property provider.2. The nanostructure catalyst composition of claim 1 , whereinthe plasmonic provider is about 0.1%-10% by mole of a total mole of the plasmonic provider and the catalytic property provider, about 4%-6% by mole.3. The nanostructure catalyst composition of claim 1 , whereinthe plasmonic provider is about 10%-30% by mole of a total mole of the plasmonic provider and the catalytic property provider, about 18%-20% by mole.4. The nanostructure catalyst composition of claim 1 , whereinthe plasmonic provider is selected from the group consisting of Co, Mn, Fe, Al, Ag, Au, Pt, Cu, Ni, Zn, Ti, C or any combination thereof.5. The nanostructure catalyst composition of claim 4 , whereinthe plasmonic provider comprises 10%-100% by mole, of Co, Mn, Fe, Al, Ag, Au, Pt, Cu, Ni and/or Zn, and less than 10% by mole of Ti and/or C, relative to a total mole of the plasmonic provider.6. The nanostructure catalyst composition of claim 1 , whereinthe catalytic property provider is selected from the group consisting of Co, Mn, Ag, Fe, Ru, Rh, Pd, Os, Ir, La, Ce, Cu, Ni, Ti, oxides thereof, hydroxides thereof, chlorides thereof, carbonates thereof, ...

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10-02-2022 дата публикации

LIGHT UPCONVERSION MICROCAPSULES

Номер: US20220040682A1
Принадлежит:

A composition, method, and article of manufacture are disclosed. The composition is a microcapsule that includes a transparent shell encapsulating a mixture comprising light upconversion molecules. The method is a method of forming a microcapsule, which includes obtaining light upconversion molecules, forming an emulsion of the light upconversion molecules and a shell formation solution, and encapsulating the light upconversion molecules in a transparent shell. The article of manufacture comprises the microcapsule. 1. A microcapsule , comprising:a transparent shell encapsulating a mixture, the mixture comprising light upconversion molecules.2. The microcapsule of claim 1 , wherein the light upconversion molecules comprise a molecular sensitizer and a molecular annihilator.3. The microcapsule of claim 1 , wherein the mixture further comprises a non-polar solvent.4. The microcapsule of claim 1 , wherein the transparent shell is a urea-formaldehyde shell.5. The microcapsule of claim 1 , wherein the light upconversion molecules comprise a molecular sensitizer selected from the group consisting of a transition metal complex of a porphyrin and a transition metal complex of a phthalocyanine.6. The microcapsule of claim 1 , wherein the light upconversion molecules comprise a molecular annihilator selected from the group consisting of a furanyldiketopyrrolopyrrole and a perylene.7. A method of forming a microcapsule claim 1 , comprising:obtaining light upconversion molecules;forming an emulsion that includes the light upconversion molecules and a shell formation solution; andencapsulating the light upconversion molecules in a transparent shell.8. The method of claim 7 , wherein the light upconversion molecules comprise a molecular sensitizer and a molecular annihilator.9. The method of claim 8 , further comprising:forming a reaction system that includes the microcapsule, a photocatalyst, and a substrate; andexposing the reaction system to light having sufficient energy to ...

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10-02-2022 дата публикации

SURFACE-MODIFIED LIGHT UPCONVERSION SILICA PARTICLES

Номер: US20220040683A1
Принадлежит:

A composition, method, and article of manufacture are disclosed. The composition includes a silica particle with light upconversion molecules bound to its surface. The method includes obtaining silica particles and light upconversion molecules having sidechains with reactive functional groups. The method further includes binding the light upconversion molecules to surfaces of the silica particles. The article of manufacture includes the composition. 1. A composition , comprising:a silica particle; andlight upconversion molecules bound to a surface of the silica particle.2. The composition of claim 1 , wherein the light upconversion molecules comprise molecular sensitizers.3. The composition of claim 1 , wherein the light upconversion molecules comprise molecular annihilators.4. The composition of claim 1 , wherein the light upconversion molecules comprise molecular annihilators and molecular sensitizers.5. The composition of claim 1 , wherein the surface of the silica particle includes a first face and a second face.6. The composition of claim 5 , wherein the light upconversion molecules comprise molecular sensitizers bound to the first face of the silica particle.7. The composition of claim 6 , wherein the light upconversion molecules comprise molecular annihilators bound to the second face of the silica particle.8. A method of forming surface-modified particles claim 6 , comprising:obtaining silica particles;obtaining light upconversion molecules having sidechains with reactive functional groups; andbinding the light upconversion molecules to surfaces of the silica particles.9. The method of claim 8 , wherein the reactive functional groups are silyl groups.10. The method of claim 8 , further comprising forming a reaction environment claim 8 , the reaction environment comprising:the surface-modified particles;a photocatalyst; anda substrate.11. The method of claim 8 , wherein the silica particles are Janus particles.12. The method of claim 8 , wherein the light ...

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26-01-2017 дата публикации

Apparatus and method for gaseous emissions treatment with enhanced catalyst distribution

Номер: US20170022868A1
Принадлежит:

An assembly for treating gaseous emissions includes a substrate body having cells for the passages of emissions gas. Lengths of metal wire are located in selected ones of the cells and an induction heating coil is mounted adjacent the substrate body for generating a varying electromagnetic field for inductive heating of the assembly including gaseous emissions passing along the cells. Within the cells, parts of the cell walls and parts of the wire surfaces are exposed to the passage of the gaseous emissions and both the cell wall parts and the wire surface parts have pollution treating catalyst at their surfaces. 1. An assembly for treating gaseous emissions comprises a substrate body having a plurality of cells for the passage of emissions gas , respective lengths of metal wire located in each of a first set of the plurality of cells , and an induction heating coil mounted adjacent the substrate body for generating a varying electromagnetic field , thereby inductively to heat the lengths of wire and thereby to heat the substrate body , at least one of the wires covering a part of interior walls of the cell in which the wire is contained and leaving another part of the walls of the cell exposed to passage of exhaust gas along the cell , a part of the at least one wire having at least part of a surface thereof exposed to passage of exhaust gas along the cell and having a pollution treating catalyst at the exposed surface part.2. The assembly as claimed in claim 1 , wherein such exposed wall part bears a layer of pollution treating catalyst.3. The assembly as claimed in claim 2 , the pollution treating catalyst at the exposed surface part being in an applied layer.4. The assembly as claimed in claim 2 , the pollution treating catalyst at the exposed surface part being a catalyst metal alloyed with the metal of the wire.5. The assembly as claimed in claim 1 , wherein the at least one metal wire has one of a hollow cross section and an open cross-sectional shape claim 1 ...

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10-02-2022 дата публикации

COATINGS THAT REDUCE OR PREVENT BARNACLE ATTACHMENT TO A MARINE STRUCTURE

Номер: US20220041258A1
Автор: Young Roger K.
Принадлежит:

An apparatus includes a marine component or structure having a surface to be exposed to a marine environment during use. A photocatalyst coating is secured to the surface of the marine structure, wherein the photocatalyst coating includes titanium oxide. The marine component or structure is preferably selected from a boat hull, dock post, dock piling, pier, and buoy. A method may be provided for reducing or preventing barnacle attachment to a marine component or structure, including forming a transparent photocatalyst coating on an external surface of the marine structure, wherein the transparent photocatalyst coating includes a titanium oxide, and placing the marine component or structure in service within a marine environment. 1. An apparatus , comprising:a marine component or structure having a surface to be exposed to a marine environment during use of the marine component or structure; anda photocatalyst coating secured to the surface of the marine structure, wherein the photocatalyst coating includes titanium oxide.2. The apparatus of claim 1 , wherein the marine component or structure is selected from a boat hull claim 1 , dock post claim 1 , dock piling claim 1 , pier claim 1 , and buoy.3. The apparatus of claim 1 , wherein the photocatalyst coating further includes a fluorescent dye and/or ultra-fine glitter.4. The apparatus of claim 1 , wherein the titanium oxide includes anatase titanium oxide.5. The apparatus of claim 1 , wherein the photocatalyst coating includes a further photocatalytic oxide including indium tin oxide and/or aluminum zinc oxide.6. The apparatus of claim 1 , wherein the marine structure includes a material selected from wood claim 1 , fiberglass claim 1 , plastic claim 1 , metal claim 1 , and glass.7. The apparatus of claim 1 , wherein the photocatalyst coating is secured to a layer of paint that has been applied to the surface of the marine structure.8. The apparatus of claim 1 , further comprising:a transparent binder layer secured ...

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24-01-2019 дата публикации

CATALYTICALLY ACTIVE FILTER FOR USE IN HOT GAS FILTRATION, A PROCESS FOR PREPARING THE FILTER AND A METHOD FOR SIMULTANEOUS REMOVAL OF SOLID PARTICLES AND UNDESIRED CHEMICAL COMPOUNDS FROM GAS STREAMS

Номер: US20190022582A1
Автор: Navid Asad
Принадлежит:

A catalytically active filter for use in hot gas filtration to simultaneously remove solid particles and one or more undesirable compounds from a hot gas stream is partly or fully impregnated with a suitable catalyst. The compounds are selected from HCN, arsenic, organic sulfur compounds and carbonyls. The filter is prepared by making an impregnation liquid, which comprises a catalytically effective amount of at least one active metal and an oxide support, impregnating the filter substrate with the impregnation liquid by dipping it in the liquid or spraying it with the liquid to control the amount of liquid and drying and optionally calcining the impregnated filter. 1. A catalytically active filter for use in hot gas filtration to simultaneously remove solid particles and one or more compounds selected from hydrogen cyanide (HCN) , arsenic , organic sulfur compounds and carbonyls from a hot gas stream , said filter , which is partly or fully impregnated with a suitable catalyst , consists of two layers or zones , whereinthe outer layer or zone, facing the gas first, is inert and serves to remove the solid particles from the gas, andthe underlying layer or zone is impregnated with a catalyst-containing liquid and serves to remove one or more of said compounds from the gas.2. Catalytically active filter according to claim 1 , wherein the catalyst comprises cobalt claim 1 , molybdenum claim 1 , nickel and active alumina.3. A process for preparing a catalytically active filter for use in hot gas filtration according to claim 1 , said method comprising the steps ofproviding an appropriately shaped filter substrate having a gas inlet surface and a gas outlet surface,preparing an impregnation liquid, which comprises an effective amount of one or more catalyst metal precursors which, inherently or upon activation, are capable of catalytically removing one or more compounds selected from hydrogen cyanide (HCN), arsenic, organic sulfur compounds and carbonyls,impregnating the ...

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24-01-2019 дата публикации

HETEROGENEOUS CATALYSTS

Номер: US20190022626A1
Принадлежит:

Heterogeneous catalysts with optional dopants are provided. The catalysts are useful in a variety of catalytic reactions, for example, the oxidative coupling of methane to C hydrocarbons. Related methods for use and manufacture of the same are also disclosed. 1. A catalyst comprising a mixed oxide base material , the mixed oxide comprising erbium (Er) and at least one further lanthanide element.2. The catalyst of claim 1 , wherein the mixed oxide comprises a physical blend of Er claim 1 , or an oxidized form thereof claim 1 , and the further lanthanide element claim 1 , or an oxidized form thereof.3. The catalyst of claim 1 , wherein the mixed oxide has the following formula (I):{'br': None, 'sub': x', 'y', 'z, 'LnErO\u2003\u2003 (I)'} Ln is the lanthanide element;', 'Er is erbium;', 'O is oxygen; and', 'x, y and z are each independently numbers greater than 0., 'wherein4. The catalyst of claim 3 , wherein x claim 3 , y and z are selected such that the overall charge of the catalyst is about 0.5. The catalyst of claim 3 , wherein x claim 3 , y and z are selected such that z is from 150% to 200% of the sum of x and y.6. The catalyst of claim 3 , wherein the mixed oxide is LnErOor LnErO.727-. (canceled)28. A bulk catalyst comprising a base material comprising an oxide of one or more lanthanide elements and a dopant combination selected from Sr/Ce claim 3 , Sr/Tb claim 3 , Sr/B and Sr/Hf/K.29. The catalyst of claim 28 , wherein the oxide has the following formula (III):{'br': None, 'sub': a', 'b', 'd', 'e', 'f', 'c, 'Ln1Ln2Ln3Ln4Ln5O\u2003\u2003 (III)'} Ln1, Ln2, Ln3, Ln4 and Ln5 are independently different lanthanide elements;', 'O is oxygen; and', 'a and c are each independently numbers greater than 0; and', 'b, d, e, and f are independently 0 or a number greater than 0., 'wherein30. The catalyst of claim 28 , wherein the dopant combination consists essentially of Sr/Ce claim 28 , Sr/Tb claim 28 , Sr/B or Sr/Hf/K.31. The catalyst of claim 28 , wherein the dopant ...

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24-01-2019 дата публикации

Catalyst and method for fractionating lignocellulosic material

Номер: US20190022632A1
Принадлежит: Individual

Various embodiments disclosed relate to solid catalysts that convert lignocellulosic material to monomer sugars that are suitable for fermentation. The solid catalysts include a transition metal complex attached to a magnetic bead, and can be physically separated from a fermentation mixture and reused several times.

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25-01-2018 дата публикации

Electric Exhaust-Gas Catalytic Converter, Vehicle And Method For Operating An Electric Exhaust-Gas Catalytic Converter

Номер: US20180023442A1
Принадлежит: Continental Automotive GmbH

The disclosure relates to an electric exhaust-gas catalytic converter that has a heating device. The heading device includes a first heating element and a second heating element that are arranged separately from one another upstream and downstream of an active catalysis region of the electric exhaust-gas catalytic converter. The disclosure also relates to a vehicle which includes the electric exhaust-gas catalytic converter and to a method for operating the electric exhaust-gas catalytic converter.

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25-01-2018 дата публикации

CATALYTIC CONVERTERS HAVING NON-LINEAR FLOW CHANNELS

Номер: US20180023445A1
Автор: MASOUDI Mansour
Принадлежит:

Disclosed is a honeycomb catalyst substrate core having geometrically non-linear flow channels. In an embodiment, the honeycomb catalyst substrate core includes helical flow channels. In another embodiment, the honeycomb catalyst substrate core includes sinusoidal flow channels. In yet another embodiment, the honeycomb catalyst substrate core includes helical plus sinusoidal flow channels. The honeycomb catalyst substrate core comprises a plurality of parallel non-linear flow channels formed along a longitudinal axis of symmetry of the catalyst substrate core, each non-linear flow channel configured such that eddies occurs during engine exhaust gas flow. Also disclosed is a method for manufacturing a ceramic honeycomb having non-linear flow channels, comprising the steps extrusion soft ceramic material through a die whilst the die moves through six degrees of freedom along its axis of symmetry. Disclosure includes a method for manufacturing a ceramic honeycomb having non-linear flow channels using three-dimensional printing. 1. A honeycomb catalyst substrate core , the honeycomb catalyst substrate core comprising:(a) a plurality of flow channels formed along a longitudinal axis of symmetry of a catalyst substrate core of a catalyst substrate, each flow channel configured into a sinusoidal substrate core adapted to increase heat-transfer and/or mass-transfer performance through formation of stable vortical structures, exclusively operative under strictly non-turbulent flow conditions, which create secondary flow, lateral to longitudinal channel flow, and enhance interactions with channel walls;(b) a washcoat within which a catalyst is embedded, said washcoat being applied over said catalyst substrate;(c) a mat cover that forms a skin over a honeycomb formed by said plurality of flow channels; and(d) a housing that forms a protective outer shell over said honeycomb, said housing having an inlet and an outlet on opposite ends of said honeycomb, said inlet and said ...

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23-01-2020 дата публикации

Apparatus and Method for Making Spherical Catalyst Beads

Номер: US20200023326A1
Принадлежит:

Apparatuses and methods for making uniform spherical beads are disclosed. Specifically, the uniform spherical beads are made by dropping droplets on a droplet rolling part, creating beads by rolling the droplets on the droplet rolling part from one spot to another spot, and collecting the beads by a beads collector. 1. An apparatus for making spherical beads from a liquid suspension , comprising:a droplet generating device for generating droplets;a droplet rolling part comprising at least one omniphobic-coated plate; anda beads collector,wherein the droplets move from one spot of the droplet rolling part to another spot before reaching the beads collector.2. The apparatus according to claim 1 , wherein the droplet generating device comprises a fluid reservoir and a tip.3. The apparatus according to claim 1 , wherein the size of the droplets is adjustable by adjusting the volume of the liquid suspension in the droplet generating device.4. The apparatus according to claim 1 , wherein the at least one omniphobic-coated plate is inclined.5. The apparatus according to claim 4 , wherein the angle between the omniphobic-coated plate and the horizontal plane is between 0 and 90 degrees.6. The apparatus according to claim 1 , wherein the droplet rolling part further comprises at least one heating element.7. The apparatus according to claim 6 , wherein the droplet rolling part is heated to a temperature between about 80° C. and about 120° C.8. The apparatus according to claim 1 , wherein the at least one omniphobic-coated plate comprises a super-omniphobic coating layer on the surface.9. The apparatus according to claim 1 , wherein the at least one omniphobic-coated plate is superhydrophobic claim 1 , superoleophobic claim 1 , thermal stable and durable.10. The apparatus according to claim 1 , wherein the beads collector comprises a omniphobic-coated plate for collecting spherical beads.11. The apparatus according to claim 1 , wherein the beads collector further comprises at ...

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28-01-2021 дата публикации

MULTICOMPONENT PLASMONIC PHOTOCATALYSTS CONSISTING OF A PLASMONIC ANTENNA AND A REACTIVE CATALYTIC SURFACE: THE ANTENNA-REACTOR EFFECT

Номер: US20210023541A1
Принадлежит: William Marsh Rice University

A multicomponent photocatalyst includes a reactive component optically, electronically, or thermally coupled to a plasmonic material. A method of performing a catalytic reaction includes loading a multicomponent photocatalyst including a reactive component optically, electronically, or thermally coupled to a plasmonic material into a reaction chamber; introducing molecular reactants into the reaction chamber; and illuminating the reaction chamber with a light source. 1. (canceled)2. (canceled)3. (canceled)4. (canceled)5. (canceled)6. (canceled)7. (canceled)8. (canceled)9. (canceled)10. (canceled)11. (canceled)12. (canceled)13. (canceled)14. (canceled)15. (canceled)16. (canceled)17. (canceled)18. (canceled)19. (canceled)20. (canceled)21. (canceled)22. A multicomponent photocatalyst comprising:a reactive component optically, electronically, or thermally coupled to a plasmonic material, wherein the reactive component is alloyed at the surface of the plasmonic material.23. The multicomponent photocatalyst of claim 22 , wherein the plasmonic material is selected from gold (Au) claim 22 , silver (Ag) claim 22 , copper (Cu) claim 22 , aluminum (Al) claim 22 , alloys thereof claim 22 , TiN claim 22 , or doped semiconductors.24. The multicomponent photocatalyst of claim 22 , wherein the plasmonic material is a 2-dimensional material.25. The multicomponent photocatalyst of claim 22 , wherein a molar ratio of the plasmonic material to the reactive component may be between 1000:1 to 10:1.26. The multicomponent photocatalyst of claim 22 , wherein the plasmonic material has a plasmon resonance at a wavelength between 180 nm and 10 microns.27. The multicomponent photocatalyst of claim 22 , wherein the plasmonic material has a plasmon resonance at a wavelength between about 380 nm-760 nm of the electromagnetic spectrum.28. The multicomponent photocatalyst of claim 22 , wherein the plasmonic material has at least one dimension with a size between about 1 nm and 300 nm.29. The ...

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28-01-2021 дата публикации

Fenton-like Catalytic Material with Dual Reaction Centers and Preparation Method Thereof

Номер: US20210023545A1

A method for preparing a Fenton-like catalytic material with dual reaction centers includes the following steps: (1) placing a nitrogen-containing compound in a muffle furnace for calcination, then dissolving the product in deionized water to form a suspension solution; (2) dissolving aluminum nitrate nonahydrate, copper nitrate trihydrate and glucose in deionized water to form a solution; (3) adding the suspension solution in a dropwise manner to the solution, then performing a closed hydrothermal reaction, washing with water, centrifuging and drying to obtain a solid; and (4) placing the prepared solid in a muffle furnace for calcination to obtain the Fenton-like catalytic material. The catalytic material presents a complete ball-flower shaped mesoporous structure, has a large specific surface area, and can expose more catalytic active sites, so that H2O2 is reduced at the electron-rich center as much as possible to generate hydroxyl radicals during the reaction.

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23-01-2020 дата публикации

CATALYTIC FORMS AND FORMULATIONS

Номер: US20200024214A1
Принадлежит:

Catalytic forms and formulations are provided. The catalytic forms and formulations are useful in a variety of catalytic reactions, for example, the oxidative coupling of methane. Related methods for use and manufacture of the same are also disclosed. 152-. (canceled)53. A catalytic material comprising a first and second catalyst , wherein the first and second catalysts have a different catalytic activity in the oxidative coupling of methane (OCM) reaction under the same conditions , wherein the catalytic material comprises a C2 selectivity of greater than 50% and a methane conversion of greater than 20% when the catalyst is employed as a heterogeneous catalyst in the oxidative coupling of methane at a temperature of 750° C. or less.54. The catalytic material of claim 53 , wherein the first catalyst is a nanowire catalyst.55. The catalytic material of claim 53 , wherein the second catalyst is a bulk catalyst.56. The catalytic material of claim 53 , wherein each of the first and second catalysts are nanowire catalysts.57. The catalytic material of claim 53 , wherein each of the first and second catalyst are bulk catalysts.58. The catalytic material of claim 53 , wherein the second catalyst has a lower catalytic activity than the first catalyst under the same conditions.59. The catalytic material of claim 58 , wherein the catalytic activity of the second catalyst increases with increasing temperature.6070-. (canceled)71. The catalytic material of claim 53 , wherein the catalytic material comprises a void fraction volume of about 35% to about 70%.72. The catalytic material of claim 71 , wherein the catalytic material comprises a void fraction volume of about 45% to about 65%.73. The catalytic material of claim 53 , wherein the catalytic material comprises catalyst particles having a cross sectional dimension in at least one dimension between about 1 mm and about 20 mm.74. The catalytic material of claim 73 , wherein the cross sectional dimension is between about 2 mm ...

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24-01-2019 дата публикации

Method for Elemental Analysis

Номер: US20190025266A1
Автор: KÜPPERS Werner, MACKE Jan
Принадлежит: C. Gerhardt GmbH & Co. KG

The invention relates to a method for elemental analysis, in particular for determining carbon and nitrogen in a sample, an apparatus suitable for said method, and the use of a catalyst suitable for said method, the catalyst being a metal oxide catalyst comprising oxides of Ce, Cu and Mn. 1. A method for elemental analysis for determination of the amount of carbon and nitrogen in a sample , comprising:(a) feeding the sample to a first part of a combustion unit at a temperature of at least 500° C. and an atmosphere with a high oxygen content,(b) passing resultant gas from step (a) over a metal oxide catalyst in a second part of the combustion unit, wherein the metal oxide catalyst comprises oxides of Ce, Cu and Mn,(c) reducing nitrogen oxides obtained from step (b) to nitrogen,(d) measuring the amount of nitrogen in the sample obtained from step (c),{'sub': 2', '2, '(e)separating HO and COfrom the sample obtained from step (c), and'}{'sub': '2', '(f) measuring the amount of carbon in the sample by determining the COcontent.'}2. The method according to claim 1 , wherein the sample is introduced into the combustion unit via an automatic sampler.3. The method according to claim 2 , wherein the amount of Ce claim 2 , Mn and Cu in the metal oxide catalyst satisfies the mass ratio Ce Подробнее

02-02-2017 дата публикации

Unit for chlorine dioxide generation and chlorine dioxide generation device

Номер: US20170028371A1
Принадлежит: Taiko Pharmaceutical Co Ltd

The present invention provides a chlorine dioxide generation unit that can release practically sufficient amount of chlorine dioxide for an extended period of time while being compact. The present invention provides a chlorine dioxide generation unit, characterized in that said unit comprises an agent storage space portion and at least two light source portions, said light source portion is for generating light consisting of wavelengths substantially in the visible region, said agent storage space portion stores an agent comprising solid chlorite, and said agent storage space portion comprises one or more openings so that air could move in and out of said agent storage space portion, wherein chlorine dioxide gas is generated by irradiating said light generated from said light source portion onto said agent present inside said agent storage space portion.

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04-02-2016 дата публикации

MICROENCAPSULATED CATALYST-LIGAND SYSTEM

Номер: US20160030935A1
Принадлежит:

A microencapsulated catalyst-ligand system is provided comprising a catalyst and a ligand microencapsulated within a permeable polymer microcapsule shell, wherein the ligand is a polymeric ligand. Processes for the preparation of said microencapsulated catalyst-ligand system are also provided. 151-. (canceled)53. The process according to claim 52 , which comprises forming a microcapsule shell by interfacial polymerisation in the presence of a catalyst and a ligand.54. The process according to claim 53 , which comprises(a) dissolving or dispersing the catalyst and a ligand in a first phase;(b) dispersing the first phase in a continuous second phase to form an emulsion;(c) reacting one or more microcapsule wall-forming materials at interface between the dispersed first phase and the continuous second phase to form a microcapsule polymer shell encapsulating the dispersed first phase; and optionally(d) recovering the microcapsules from the continuous phase.55. The process according to claim 52 , which comprises forming a microcapsule shell by interfacial polymerisation in the presence of a catalyst and treating the microcapsule shell with a ligand.56. The process according to claim 55 , which comprises(a) dissolving or dispersing the catalyst in a first phase;(b) dispersing the first phase in a continuous second phase to form an emulsion;(c) reacting one or more microcapsule wall-forming materials at interface between the dispersed first phase and the continuous second phase to form a microcapsule polymer shell encapsulating the dispersed first phase; and(d) treating the microcapsules with a ligand.57. The process according to claim 52 , which comprises forming a microcapsule shell by interfacial polymerisation in the presence of a ligand and treating the microcapsule shell with a catalyst solution.58. The process according to claim 57 , which comprises(a) dissolving or dispersing the ligand in a first phase;(b) dispersing the first phase in a continuous second phase to ...

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04-02-2016 дата публикации

Removable Protective Coating For The Receipt Of A Dust Free Catalyst

Номер: US20160030937A1
Автор: GABRIEL Wolfgang
Принадлежит: CLARIANT INTERNATIONAL LTD.

The invention pertains to a stabilized catalyst mould comprising a catalyst body formed of a catalyst material, said catalyst material comprising a catalytically active material or a precursor material of the catalytically active material, characterized in that at least parts of the surface of the catalyst mould are provided with a protective coating comprising an organic binder. Further, the invention pertains to a method for obtaining a stabilized catalyst mould. 1. Stabilized catalyst mould comprising a catalyst body formed of a catalyst material , said catalyst material comprising a catalytically active material or a precursor material of the catalytically active material , characterized in that at least parts of the surface of the catalyst mould are provided with a protective coating comprising an organic binder.2. Catalyst mould according to claim 1 , wherein the organic binder has an average molecular weight of at least 100 g/mol.3. Catalyst mould according to claim 1 , wherein the organic binder comprises a copolymer of at least two monomers.4. Catalyst mould according to claim 1 , wherein the organic binder comprises a copolymer of vinyl acetate and a further monomer claim 1 , preferably claim 1 , ethylene claim 1 , propylene claim 1 , maleic anhydride and combinations.5. Catalyst mould according to claim 1 , wherein the organic binder is polyvinyl acetate.6. Catalyst mould according to claim 1 , wherein the amount of the organic binder comprised in the catalyst mould is at least 0.05 weight-%.7. Catalyst mould according to the catalyst mould is free-flowing.8. Catalyst mould according to claim 1 , wherein the catalyst mould has a maximum extension of 20 mm.9. Catalyst mould according to claim 1 , wherein the catalyst mould has at least one bore holes.10. Method for producing a stabilized catalyst mould claim 1 , comprising a catalyst material comprising a catalytically active material or a precursor material of the catalytically active material is provided ...

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23-01-2020 дата публикации

RADIOACTIVE CESIUM ADSORBENT AND METHOD OF REMOVING RADIOACTIVE CESIUM USING THE SAME

Номер: US20200027615A1
Принадлежит:

A radioactive cesium adsorbent includes photocatalyst particles and Prussian blue. The ferric ions of the Prussian blue are reduced to ferrous ions by activation of the photocatalyst particles. A method of removing radioactive cesium using the radioactive cesium adsorbent includes preparing a composition comprising photocatalyst particles and Prussian blue; preparing a precursor solution by mixing radioactive cesium and the composition prepared in the preparing of a composition; and reducing ferric ions of the Prussian blue to ferrous ions by activating the photocatalyst particles in the precursor solution prepared in the preparing of a precursor solution. 1. A radioactive cesium adsorbent comprising:photocatalyst particles; andPrussian blue,wherein ferric ions of the Prussian blue are reduced to ferrous ions by activation of the photocatalyst particles.2. The radioactive cesium adsorbent according to claim 1 , wherein the photocatalyst particles comprise one or more selected from the group consisting of TiO claim 1 , ZnO claim 1 , WO claim 1 , SnO claim 1 , CdS claim 1 , and FeO.3. The radioactive cesium adsorbent according to claim 1 , wherein activation of the photocatalyst particles is caused by UV light within a wavelength range within which the photocatalyst particles are activated.5. A method of removing radioactive cesium claim 1 , comprising:preparing a composition comprising photocatalyst particles and Prussian blue;preparing a precursor solution by mixing radioactive cesium and the composition prepared in the preparing of a composition; andreducing ferric ions of the Prussian blue to ferrous ions by activating the photocatalyst particles in the precursor solution prepared in the preparing of a precursor solution.6. The method according to claim 5 , wherein claim 5 , in the preparing of a precursor solution claim 5 , a total concentration of the photocatalyst particles and the Prussian blue contained in the precursor solution is 2 to 20 g/L.7. The method ...

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