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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 1032. Отображено 100.
09-08-2012 дата публикации

Method for manufacturing catalyst

Номер: US20120203048A1
Принадлежит: Mitsubishi Chemical Corp

A method for manufacturing a catalyst, which comprises regenerating a catalyst comprising a zeolite as an active ingredient and having an ethylene conversion lowered through reaction of producing propylene by bringing into contact with ethylene in a vapor phase, by bringing the catalyst into contact with a gas which does not comprise oxygen and comprises hydrogen having a hydrogen partial pressure of 0.01 MPa or more as an absolute pressure thereof.

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23-05-2013 дата публикации

Process for Ion Exchange on Zeolites

Номер: US20130129612A1
Принадлежит: BASF SE

Aspects of the present invention relate to an improved process for exchanging alkali metal or alkaline earth metal ions in zeolites for ammonium ions. For this exchange, aqueous solutions of ammonium salts, for example ammonium sulfate, ammonium nitrate or ammonium chloride, are currently being used. The resulting “ammonium zeolites” are calcined to convert them, with release of ammonia, to the H form of the zeolites suitable as a catalyst. Certain methods provided herein use ammonium carbonate instead of the ammonium compounds mentioned. As excess ammonium carbonate, in contrast to the nitrates, sulfates or chlorides, can be recycled in the form of carbon dioxide and ammonia, the amount of salt which has to be discharged is lowered significantly.

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05-09-2013 дата публикации

Silica composite, method for producing the same, and method for producing propylene using the silica composite

Номер: US20130231515A1
Принадлежит: Asahi Kasei Chemicals Corp

The present invention provides a method for producing a silica composite by the steps of: preparing a raw material mixture containing silica and zeolite; drying the raw material mixture to obtain a dried product; and calcining the dried product, wherein the method comprising the step of allowing the raw material mixture to contain phosphoric acid and/or phosphate or bringing a solution of phosphoric acid and/or phosphate into contact with the zeolite and/or the dried product, or a combination thereof to thereby adjust a phosphorus content in the silica composite to 0.01 to 1.0% by mass based on the total mass of the silica composite.

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05-12-2013 дата публикации

CHA-type Zeolite Materials and Methods for Their Preparation Using Cycloalkyammonium Compounds

Номер: US20130323164A1
Принадлежит:

Aspects of the present invention relate to a process for the preparation of a zeolitic material having a CHA-type framework structure comprising YOand XO, wherein said process comprises the steps of: 1. A process for the preparation of a zeolitic material having a CHA-type framework structure comprising YOand XO , wherein said process comprises the steps of:{'sub': 2', '2', '3, 'sup': 1', '2', '3', '4', '+, '(1) providing a mixture comprising one or more sources for YO, one or more sources for XO, and one or more tetraalkylammonium cation RRRRN-containing compounds as structure directing agent;'}(2) crystallizing the mixture obtained in step (1) for obtaining a zeolitic material having a CHA-type framework structure;wherein Y is a tetravalent element and X is a trivalent element,{'sup': 1', '2', '3, 'wherein R, R, and Rindependently from one another stand for alkyl,'}{'sup': '4', 'wherein Rstands for cycloalkyl, and'}{'sub': 2', '5, 'wherein the mixture provided in step (1) does not contain any substantial amount of a source for ZO, wherein Z is P.'}2. The process of claim 1 , wherein R claim 1 , R claim 1 , and Rindependently from one another stand for optionally substituted and/or optionally branched (C-C)alkyl.3. The process of claim 1 , wherein Rstands for optionally heterocyclic and/or optionally substituted 5- to 8-membered cycloalkyl.4. The process of claim 1 , wherein the one or more tetraalkylammonium cation RRRRN-containing compounds comprise one or more N claim 1 ,N claim 1 ,N-tri(C-C)alkyl-(C-C)cycloalkylammonium compounds.5. The process of claim 1 , wherein the one or more tetraalkylammonium cation RRRRN-containing compounds are salts.6. The process of claim 1 , wherein Y is selected from the group consisting of Si claim 1 , Sn claim 1 , Ti claim 1 , Zr claim 1 , Ge claim 1 , and mixtures of two or more thereof.7. The process of claim 1 , wherein the one or more sources for YOcomprises one or more compounds selected from the group consisting of fumed ...

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03-01-2019 дата публикации

CLUSTER SUPPORTED CATALYST AND PRODUCTION METHOD THEREFOR

Номер: US20190001306A1
Принадлежит:

A method for producing a cluster-supporting catalyst, the cluster-supporting catalyst including porous carrier particles that has acid sites, and catalyst metal clusters supported within the pores of the porous carrier particles, includes the following steps: providing a dispersion liquid containing a dispersion medium and the porous carrier particles dispersed in the dispersion medium; and in the dispersion liquid, forming catalyst metal clusters having a positive charge, and supporting the catalyst metal clusters on the acid sites within the pores of the porous carrier particles through an electrostatic interaction. 1. A method for producing a cluster-supporting catalyst ,wherein the cluster-supporting catalyst comprises porous carrier particles having acid sites, and catalyst metal clusters supported within the pores of the porous carrier particles; andwherein the method comprises the followings steps:providing a dispersion liquid containing a dispersion medium and the porous carrier particles dispersed in the dispersion medium, andforming, in the dispersion liquid, catalyst metal clusters having a positive charge, and supporting the catalyst metal clusters on the acid sites within the pores of the porous carrier particles through an electrostatic interaction.2. The method according to claim 1 , wherein the dispersion liquid is provided by pulverizing the porous carrier particles claim 1 , and dispersing the pulverized porous carrier particles in the dispersion medium.3. The method according to claim 1 , wherein the clusters are formed in the dispersion liquid by any of the following methods:a method of laser ablation in liquid,a method of microwave ablation in liquid,a method of plasma ablation in liquid, anda positive-negative inversion method.4. The method according to claim 1 , wherein the clusters are formed in the dispersion liquid by a method of reduction in liquid.5. The method according to claim 4 , wherein the dispersion liquid is irradiated with plasma ...

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07-01-2021 дата публикации

CATALYST, AND METHOD FOR DIRECT CONVERSION OF SYNGAS TO PREPARE LIGHT OLEFINS

Номер: US20210002184A1
Принадлежит:

A process for direct synthesis of light olefins uses syngas as the feed raw material. This catalytic conversion process is conducted in a fixed bed or a moving bed using a composite catalyst containing components A and B (A+B). The active ingredient of catalyst A is metal oxide; and catalyst B is an oxide supported zeolite. A carrier is one or more of AlO, SiO, TiO, ZrO, CeO, MgO and GaOhaving hierarchical pores; the zeolite is one or more of CHA and AEI structures. The loading of the zeolite is 4%-45% wt. A weight ratio of the active ingredients in the catalyst A and the catalyst B is within a range of 0.1-20, and preferably 0.3-5. The total selectivity of the light olefins comprising ethylene, propylene and butylene can reach 50-90%, while the selectivity of a methane byproduct is less than 15%. 1. A catalyst , wherein the catalyst is a composite catalyst composed of A+B; the catalyst component A and the catalyst component B are compounded by mechanical mixing method; the active ingredients of the catalyst component A are active metal oxides; the catalyst component B are supported zeolites; the carrier is at least one of porous AlO , SiO , TiO , ZrO , CeO , MgO and GaO; the zeolite is at least one of CHA and AEI structures; the loading of the zeolite is 4%-45% wt; and the active metal oxide is at least one of MnO , MnCrO , MnAlO , MnZrO , ZnO , ZnCrO , ZnAlO , CoAlOand FeAlO.2. The catalyst according to claim 1 , wherein at least one of porous AlO claim 1 , SiO claim 1 , TiO claim 1 , ZrO claim 1 , CeO claim 1 , MgO and GaOin the catalyst component B is used as the carrier; specific surface area is 30-250 m/g; pore volume is 0.25-0.80 ml/g; through calculation according to the specific surface area claim 1 , mesoporous specific surface area occupies 30-75% and macroporous specific surface area occupies 25-70%; and the zeolite is used as an active component and dispersed on the carrier by in situ growth or physical mixing mode.3. The catalyst according to claim 1 , ...

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03-01-2019 дата публикации

PROCESS TO PREPARE PROPYLENE

Номер: US20190002767A1
Принадлежит: INOVACAT B.V.

The invention is directed to a process to prepare propylene from a hydrocarbon feedstock comprising olefin hydrocarbon compounds by contacting the feedstock with a mixture of a heterogeneous cracking catalyst and a heterogeneous dehydrogenation catalyst as present in one or more packed beds thereby obtaining propylene and other reaction products. 1. A process to prepare propylene(i) from a hydrocarbon feedstock comprising olefin hydrocarbon compounds by contacting the feedstock with a mixture of a heterogeneous cracking catalyst and a heterogeneous dehydrogenation catalyst as present in one or more packed beds thereby obtaining propylene and other reaction products, wherein the cracking catalyst and the dehydrogenation catalyst are present in one or more packed beds in an in-series configuration and wherein the hydrocarbon feedstock, formed propylene and other reaction products will flow from an up-flow region to a down-flow region following a flow path and wherein in the direction of the flow path the concentration of the dehydrogenation catalyst in the bed increases compared to the cracking catalyst and/or(ii) from a hydrocarbon feedstock comprising paraffinic hydrocarbon compounds by contacting the feedstock with a mixture of a heterogeneous cracking catalyst and a heterogeneous dehydrogenation catalyst as present in one or more packed beds thereby obtaining propylene and other reaction products, wherein the cracking catalyst and the dehydrogenation catalyst are present in one or more packed beds in an in-series configuration and wherein the hydrocarbon feedstock, formed propylene and other reaction products will flow from an up-flow region to a down-flow region following a flow path and wherein in the direction of the flow path the concentration of the dehydrogenation catalyst in the bed decreases compared to the cracking catalyst.2. The process according to claim 1 , wherein the content of olefins having 4 or more carbon atoms in the feedstock of process (i) is ...

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09-01-2020 дата публикации

METHODS FOR PREPARATION OF CHA ZEOLITE AT AMBIENT PRESSURE

Номер: US20200010332A1
Автор: Lang David Ari
Принадлежит:

The disclosure, in one aspect, relates to methods of preparing a CHA zeolite under ambient pressure conditions. In further aspects, the disclosure relates to methods such that a mother liquor can be isolated from a disclosed method, and recycled for use in a disclosed method for further preparation of a CHA zeolite. This abstract is intended as a scanning tool for purposes of searching in the particular art and is not intended to be limiting of the present disclosure. 1. A method for preparing a CHA zeolite , the method comprising:heating a zeolite precursor mixture at ambient pressure in a reflux reaction vessel of a reflux reactor system comprising the reflux reaction vessel and a reflux condenser;wherein the zeolite precursor mixture comprises water, a silicate solution, a zeolite, and a CHA templating agent;wherein heating comprises heating the reaction vessel such the zeolite precursor mixture in the reflux reaction vessel has a reaction temperature of from about 80° C. to about 120° C.;thereby forming a CHA zeolite and a mother liquor solution.2. The method of claim 1 , wherein the ambient pressure is about 700 torr to about 800 torr.3. The method of claim 1 , wherein the zeolite in the zeolite precursor mixture is selected from a USY zeolite claim 1 , a pre-treated Na-Y zeolite claim 1 , a Na-Y zeolite claim 1 , and combinations thereof.4. The method of claim 3 , wherein the zeolite in the zeolite precursor mixture is selected from a pre-treated Na-Y zeolite claim 3 , a Na-Y zeolite claim 3 , and combinations thereof.5. The method of claim 3 , wherein the zeolite in the zeolite precursor mixture is a USY zeolite.6. The method of claim 1 , wherein the silicate in the zeolite precursor mixture is a sodium silicate solution comprising SiO claim 1 , NaO claim 1 , and water.7. The method of claim 1 , wherein the CHA templating agent is selected from N claim 1 ,N claim 1 ,N-trimethyl-1-ammonium adamantine claim 1 , tetraethylenepentamine claim 1 , and a combination ...

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16-01-2020 дата публикации

SCR METHOD FOR REDUCING OXIDES OF NITROGEN AND METHOD FOR PRODUCING A CATALYST FOR SUCH METHOD

Номер: US20200018210A1
Принадлежит:

A method of reducing nitrogen oxides in exhaust gas of an internal combustion engine by selective catalytic reduction (SCR) comprises contacting the exhaust gas also containing ammonia and oxygen with a catalytic converter comprising a catalyst () comprising at least one crystalline small-pore molecular sieve catalytically active component (Z) having a maximum ring opening of eight tetrahedral basic building blocks, which crystalline small-pore molecular sieve catalytically active component (Z) comprising mesopores. 1. A method of reducing nitrogen oxides in exhaust gas of an internal combustion engine by selective catalytic reduction (SCR) , which method comprising contacting the exhaust gas also containing ammonia and oxygen with a catalytic converter comprising a catalyst comprising at least one crystalline small-pore molecular sieve catalytically active component (ZM ,I) having a maximum ring opening of eight tetrahedral basic building blocks , which crystalline small-pore molecular sieve catalytically active component (ZM ,I) comprising mesopores.2. The method according to claim 1 , wherein the at least one crystalline small-pore catalytically active component is an aluminosilicate zeolite claim 1 , a silicoaluminophosphate molecular sieve or an aluminophosphate molecular sieve (ZM claim 1 ,I).3. The method according to claim 1 , wherein the molecular sieve comprises a promoter metal.4. The method according to claim 3 , wherein the crystalline molecular sieve is ion-exchanged with the promoter metal.5. The method according to claim 3 , wherein the promoter metal is iron or copper.6. The method according to claim 1 , wherein the crystalline molecular sieve is one or more of the framework structures CHA claim 1 , AEI claim 1 , ERI or AFX.7. The method according to claim 1 , comprising an inorganic binder component (B claim 1 ,BA).8. The method according to claim 7 , in which the inorganic binder component (B claim 7 ,BA) comprises porous particles having a ...

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25-01-2018 дата публикации

EXHAUST SYSTEM FOR A COMPRESSION IGNITION ENGINE COMPRISING A WATER ADSORBENT MATERIAL

Номер: US20180023439A1
Принадлежит:

An exhaust system for a compression ignition engine comprising: a water adsorbent material; and a catalyst composition for treating an exhaust gas pollutant produced by the compression ignition engine; wherein the water adsorbent material is: (i) arranged to contact exhaust gas from the compression ignition engine before the catalyst composition; and (ii) in thermal communication with the catalyst composition. 120-. (canceled)21. A diesel engine exhaust system comprising an oxidation catalyst , wherein the oxidation catalyst comprises:a water adsorbent material;a catalyst composition for treating an exhaust gas pollutant produced by the diesel engine, wherein the catalyst composition comprises a platinum group metal (PGM) and a support material, wherein the platinum group metal (PGM) comprises platinum; anda substrate;wherein the catalyst composition and the water adsorbent material is each disposed on the substrate, wherein a first washcoat layer comprising the water adsorbent material is disposed on a second washcoat layer comprising the catalyst composition such that the water adsorbent material is arranged to contact exhaust gas from the diesel engine before the catalyst composition.22. A diesel engine exhaust system according to claim 21 , wherein the water adsorbent material comprises a zeolite.23. A diesel engine exhaust system according to claim 22 , wherein the zeolite has a silica to alumina ratio (SAR) of 100:1 to 8:1.24. A diesel engine exhaust system according to claim 22 , wherein the zeolite has a pore size of from 3 Å to 15 Å.25. A diesel engine exhaust system according to claim 22 , wherein the zeolite is be selected from the group consisting of faujasite claim 22 , clinoptilolite claim 22 , mordenite claim 22 , silicalite claim 22 , ferrierite claim 22 , zeolite X claim 22 , zeolite Y claim 22 , ultrastable zeolite Y claim 22 , beta zeolite claim 22 , AEI zeolite claim 22 , ZSM-5 zeolite claim 22 , ZSM-12 zeolite claim 22 , ZSM-20 zeolite claim 22 ...

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23-01-2020 дата публикации

NANO-SIZED ZEOLITE CATALYST HAVING A HIGH SILICA TO ALUMINA RATIO

Номер: US20200023342A1
Принадлежит: SABIC Global Technologies, B.V.

A catalyst includes a zeolite, wherein the zeolite has: a CHA framework; a particle size less than or equal to 100 nanometers; and a silica to alumina mole ratio in the range of about 50:1 to about 150:1. The catalyst can include a metal dopant. The catalyst can be used for purifying a product by flowing a reactant across the catalyst to form the product; and condensing or separating the product. The product can be an olefin or alkenes with an increased carbon chain. The catalyst can be used for selective catalytic reduction of nitrogen oxide or a gas to liquid reaction. A method of producing the catalyst can include selecting the concentration of a crystal growth inhibitor based on the ratio of the silica precursor and an alumina precursor such that the zeolite crystals have a mean particle size less than or equal to 100 nanometers. 1. A catalyst comprising: a CHA framework;', 'a particle size less than or equal to 100 nanometers; and', 'a silica to alumina mole ratio in the range of about 50:1 to about 150:1., 'a zeolite, wherein the zeolite has2. The catalyst according to claim 1 , wherein the zeolite has a particle size less than or equal to 50 nanometers.3. The catalyst according to claim 1 , wherein zeolite further comprises a metal dopant.4. The catalyst according to claim 3 , wherein the dopant is selected from copper (Cu) claim 3 , nickel (Ni) claim 3 , iron (Fe) claim 3 , zinc (Zn) claim 3 , manganese (Mn) claim 3 , and molybdenum (Mo).5. A method of producing a catalyst comprising:combining a silica precursor and an alumina precursor, wherein the ratio of the silica precursor to the alumina precursor is in the range of about 50:1 to about 150:1;adding a crystal growth inhibitor;adding a structure directing agent; andcrystallizing the zeolite, wherein the zeolite crystals have a CHA framework and a mean particle size less than or equal to 100 nanometers.6. The method according to claim 5 , wherein the crystal growth inhibitor is polyethyleneimine.7. The ...

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01-02-2018 дата публикации

METHODS TO PRODUCE MOLECULAR SIEVES WITH LTA TOPOLOGY AND COMPOSITIONS DERIVED THEREFROM

Номер: US20180029021A1
Принадлежит:

The present disclosure is directed to processing for preparing crystalline pure-silica and heteroatom-substituted LTA frameworks in fluoride media using a simple organic structure-directing agent (OSDA), having a structure of Formula (I): 1. A crystalline microporous silicate of LTA topology that is substantially free of an Organic Structure Directing Agent (OSDA).2. The crystalline microporous silicate of claim 1 , that is an aluminosilicate having a molar ratio of Si:Al in a range of from about 5 to about 50.3. The crystalline microporous aluminosilicate of claim 2 , having a molar ratio of Si:Al in a range of from about 12 to about 42.4. The crystalline microporous aluminosilicate of claim 2 , comprising pores containing Li claim 2 , Na claim 2 , K claim 2 , Rb claim 2 , Cs claim 2 , Be claim 2 , Mg claim 2 , Ca claim 2 , Sr claim 2 , Be claim 2 , Al claim 2 , Ga claim 2 , In claim 2 , Zn claim 2 , Ag claim 2 , Cd claim 2 , Ru claim 2 , Rh claim 2 , Pd claim 2 , Pt claim 2 , Au claim 2 , Hg claim 2 , La claim 2 , Ce claim 2 , Pr claim 2 , Nd claim 2 , Pm claim 2 , Sm claim 2 , Eu claim 2 , or RNHcations claim 2 , where R is alkyl claim 2 , and n=0-4.5. The crystalline microporous aluminosilicate of claim 2 , comprising pores containing NaCl or KCl.6. The crystalline microporous aluminosilicate of claim 2 , comprising pores containing scandium claim 2 , yttrium claim 2 , titanium claim 2 , zirconium claim 2 , vanadium claim 2 , manganese claim 2 , chromium claim 2 , molybdenum claim 2 , tungsten claim 2 , iron claim 2 , ruthenium claim 2 , osmium claim 2 , cobalt claim 2 , rhodium claim 2 , iridium claim 2 , nickel claim 2 , palladium claim 2 , platinum claim 2 , copper claim 2 , silver claim 2 , gold claim 2 , or a mixture thereof claim 2 , each as a metal claim 2 , oxide claim 2 , or salt.7. The crystalline microporous aluminosilicate of claim 2 , comprising pores containing copper as a metal claim 2 , oxide claim 2 , or salt.8. The crystalline microporous ...

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04-02-2021 дата публикации

A FAST BATCH PROCESS FOR PREPARING A ZEOLITIC MATERIAL HAVING FRAMEWORK TYPE CHA

Номер: US20210031175A1
Принадлежит:

A batch process for preparing a zeolitic material having framework type CHA and a framework structure comprising Si, Al, O, and H, comprising (i) providing a seeding material comprising a zeolitic material having framework type CHA and a framework structure comprising Si, Al, O, and H; (ii) preparing a mixture comprising a source of Si, a source of Al, a seeding material provided in (i), a CHA framework structure directing agent comprising a cycloalkylammonium compound, and water, wherein the cycloalkylammonium compound is a compound comprising a cation RRRRN wherein R, R, Rare, independently from one another, an alkyl residue having from 1 to 6 carbon atoms, and Ris a 5- to 8-membered cycloalkyl residue, wherein in mixture, the molar ratio of water relative to Si comprised in the source of Si and in the seeding material, calculated as SiO, is in the range of from 5:1 to 15:1, wherein the mixture, the molar ratio of sodium, calculated as NaO, relative to Si comprised in the source of Si and in the seeding material, calculated as SiO, is in the range of from 0:1 to 0.1:1; (iii) heating the mixture prepared in (ii) in its liquid state to a temperature of the mixture in the range of from 50 to 90° C. and keeping the liquid mixture at a temperature in this range for 5 to 100 h; (iv) heating the heated mixture of (iii) to a temperature of the mixture in the range of from 190 to 230° C. in a crystallization vessel and keeping the mixture at a temperature in this range under autogenous pressure in the crystallization vessel for 0.5 to 10 h, obtaining a solid material comprising a zeolitic material having framework type CHA and a framework structure comprising Si, Al, O, and H, suspended in its mother liquor. 1. A process for preparing a zeolitic material having a framework type CHA and a framework structure comprising Si , Al , O , and H , the process comprising:providing a seeding material comprising a zeolitic material having a framework type CHA and a framework ...

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06-02-2020 дата публикации

PRODUCTION OF HYDROTHERMALLY STABLE CHA ZEOLITES

Номер: US20200038849A1
Принадлежит: PQ CORPORATION

A method of producing hydrothermally stable chabazite (CHA) zeolites is disclosed. The disclosed method is based on the use of reaction mixtures that (1) are essentially void of alkali metal cations and (2) contain the N,N,N-trimethyl-1-adamantyl ammonium (TMAda+) organic as the sole OSDA. The disclosed method results in a higher crystalline CHA zeolite that exhibits hydrothermal stability. There is also disclosed a zeolite material having a CHA-type framework structure made by the disclosed method. A method of selective catalytic reduction of NOx in exhaust gas using the material described herein is also disclosed. 1. A method of making a microporous crystalline material from reaction mixtures that (1) are essentially void of alkali metal cations and (2) contain the N ,N ,N-trimethyl-1-adamantyl ammonium (TMAda+) organic as the sole OSDA , the method comprising:mixing sources of alumina, silica, water, TMAdaOH and optionally a chabazite seed material to form a gel;heating the gel in a vessel at a temperature ranging from 80° C. to 200° C. to form a crystalline chabazite product; andcalcining the product to produce an aluminosilicate zeolite having a CHA structure, and a silica-to-alumina ratio (SAR) ranging from 20 to 100.2. The method of claim 1 , wherein the reaction mixtures with (A) molar composition 1 SiO:w AlO:x TMAdaOH:y HO claim 1 , where w=0.010-0.050 claim 1 , x=0.04-0.20 claim 1 , y=1-25 and (B) trace concentrations of alkali cations.3. The method of claim 2 , wherein w ranges from 0.014-0.050.4. The method of claim 2 , wherein x ranges from 0.05-0.15.5. The method of claim 2 , wherein y ranges from 5-20.6. The method of claim 1 , wherein the aluminosilicate zeolite has a silica-to-alumina ratio (SAR) ranging from 20-70.7. The method of claim 1 , further comprising adding to the microporous crystalline material at least one metal chosen from copper claim 1 , iron or combinations thereof to form a metal containing chabazite.8. The method of claim 7 , ...

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02-03-2017 дата публикации

SSZ-13 AS A CATALYST FOR CONVERSION OF CHLOROMETHANE TO OLEFINS

Номер: US20170057886A1
Автор: FICKEL Dustin
Принадлежит:

Disclosed are methods and systems for converting chloromethane to olefins. A method includes contacting an aluminosilicate catalyst having a chabazite zeolite structure with a feed that includes an alkyl halide and is substantially free of oxygenates under reaction conditions sufficient to produce an olefin hydrocarbon product comprising C-Colefins. 1. A method for converting an alkyl halide to an olefin , the method comprising contacting an aluminosilicate catalyst having a chabazite zeolite structure with a feed comprising an alkyl halide under reaction conditions sufficient to produce an olefin hydrocarbon product comprising C-Colefins , wherein the feed is substantially free of oxygenates.2. The method of claim 1 , wherein the feed comprises at least 50 wt. % claim 1 , at least 75 wt. % claim 1 , at least 80 wt. % claim 1 , or at least 90 wt. % alkyl halide.3. The method of claim 1 , wherein the aluminosilicate catalyst has a silica (SiO) to alumina (AlO) ratio (SAR) of less than 100:1.4. The method of claim 3 , wherein the SAR is 30:1 to 50:1 or about 40:1.5. The method of claim 3 , wherein the SAR ratio is 65:1 to 85:1 or about 76:1.6. The method of claim 1 , wherein the aluminosilicate catalyst is SSZ-13.7. The method of claim 1 , wherein the feed stream includes less than 5 wt. % claim 1 , preferably less than 1 wt. % claim 1 , or preferably is alcohol free.8. The method of claim 7 , wherein the alcohol is methanol or ethanol.9. The method of claim 1 , wherein the feed stream includes less than 5 wt. % oxygenates claim 1 , preferably less than 1 wt. % oxygenates claim 1 , or is oxygenate free.10. The method of claim 1 , wherein the alkyl halide is a methyl halide.11. The method of claim 10 , wherein the methyl halide is methyl chloride claim 10 , methyl bromide claim 10 , methyl fluoride claim 10 , or methyl iodide claim 10 , or any combination thereof.12. The method of claim 11 , wherein the methyl halide is methyl chloride.13. The method of claim 1 , ...

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05-03-2015 дата публикации

Honeycomb catalyst and exhaust gas purifying apparatus

Номер: US20150065334A1
Принадлежит: Ibiden Co Ltd

A honeycomb catalyst includes a honeycomb unit. The honeycomb unit has a plurality of through holes that are arranged in parallel in a longitudinal direction and partitions that are provided between the plurality of through holes. The honeycomb unit includes a zeolite, inorganic particles, and an inorganic binder. The zeolite includes a CHA-structured aluminosilicate having a Si/Al ratio of about 15 to about 50. The inorganic particles includes an oxide that has a positive coefficient of thermal expansion. A volume ratio of the zeolite to the inorganic particles is about 50:about 50 to about 90:about 10.

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27-02-2020 дата публикации

Low-silica chabazite zeolites with high acidity

Номер: US20200061594A1
Принадлежит: PQ Corp

A microporous crystalline material having a molar silica to alumina ratio (SAR) ranging from 10 to 15 and a fraction of Al in the zeolite framework of 0.63 or greater is disclosed. A method of selective catalytic reduction of nitrogen oxides in exhaust gas that comprises contacting exhaust gases, typically in the presence of ammonia, urea, an ammonia generating compound, or a hydrocarbon compound, with an article comprising the disclosed microporous crystalline is also disclosed. Further, a method of making the disclosed microporous crystalline material is disclosed.

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08-03-2018 дата публикации

DIESEL OXIDATION CATALYST AND EXHAUST SYSTEM

Номер: US20180065084A1
Принадлежит:

An oxidation catalyst for treating an exhaust gas from a diesel engine and an exhaust system comprising the oxidation catalyst are described. The oxidation catalyst comprises: a first washcoat region for oxidising carbon monoxide (CO) and hydrocarbons (HCs), wherein the first washcoat region comprises a first platinum group metal (PGM) and a first support material; a second washcoat region for oxidising nitric oxide (NO), wherein the second washcoat region comprises platinum (Pt), manganese (Mn) and a second support material; and a substrate having an inlet end and an outlet end; wherein the second washcoat region is arranged to contact the exhaust gas at the outlet end of the substrate and after contact of the exhaust gas with the first washcoat region. 1. An exhaust system for a diesel engine , which comprises an oxidation catalyst for treating an exhaust gas from the diesel engine and an emissions control device , wherein the oxidation catalyst comprises:a first washcoat zone for oxidising carbon monoxide (CO) and hydrocarbons (HCs), wherein the first washcoat region comprises a first platinum group metal (PGM) and a first support material;a second washcoat zone for oxidising nitric oxide (NO), wherein the second washcoat zone comprises platinum (Pt) and manganese (Mn) disposed or supported on a second support material, wherein the second support material comprises a refractory metal oxide; anda substrate, andwherein the second washcoat zone is disposed at an outlet end of the substrate, and the first washcoat zone disposed at an inlet end of the substrate.2. An exhaust system according to claim 1 , wherein the second washcoat zone comprises platinum (Pt) as the only platinum group metal.3. An exhaust system according to claim 1 , wherein the second support material comprises a refractory metal oxide selected from the group consisting of alumina claim 1 , silica claim 1 , titania claim 1 , zirconia claim 1 , ceria and a mixed or composite oxide of two or more ...

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08-03-2018 дата публикации

DIESEL OXIDATION CATALYST AND EXHAUST SYSTEM

Номер: US20180065085A1
Принадлежит:

An oxidation catalyst for treating an exhaust gas from a diesel engine and an exhaust system comprising the oxidation catalyst are described. The oxidation catalyst comprises: a first washcoat region for oxidising carbon monoxide (CO) and hydrocarbons (HCs), wherein the first washcoat region comprises a first platinum group metal (PGM) and a first support material; a second washcoat region for oxidising nitric oxide (NO), wherein the second washcoat region comprises platinum (Pt), manganese (Mn) and a second support material; and a substrate having an inlet end and an outlet end; wherein the second washcoat region is arranged to contact the exhaust gas at the outlet end of the substrate and after contact of the exhaust gas with the first washcoat region. 1. An oxidation catalyst for treating an exhaust gas from a diesel engine , which comprises:a first washcoat layer for oxidising carbon monoxide (CO) and hydrocarbons (HCs), wherein the first washcoat layer comprises a first platinum group metal (PGM) and a first support material;a second washcoat layer for oxidising nitric oxide (NO), wherein the second washcoat layer comprises platinum (Pt) and manganese (Mn) disposed or supported on a second support material, wherein the second support material comprises a refractory metal oxide; anda substrate having an inlet end and an outlet end, andwherein the second washcoat layer is disposed on the first washcoat layer.2. An oxidation catalyst according to claim 1 , wherein the second washcoat layer comprises platinum (Pt) as the only platinum group metal.3. An oxidation catalyst according to claim 1 , wherein the second support material comprises a refractory metal oxide selected from the group consisting of alumina claim 1 , silica claim 1 , titania claim 1 , zirconia claim 1 , ceria and a mixed or composite oxide of two or more thereof.4. An oxidation catalyst according to claim 3 , wherein the second support material comprises alumina doped with silica.5. An oxidation ...

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15-03-2018 дата публикации

Zeolitic Materials And Methods Of Manufacture

Номер: US20180072579A1
Принадлежит: BASF CORPORATION

Zeolites, improved methods for their synthesis, and catalysts, systems, and methods of using these zeolites as catalysts are described. The method of synthesis of the zeolites includes forming a mixture including a zeolitic precursor material and a structure directing agent and subjecting the mixture to high shear processing conditions. 1. A method of producing a zeolitic material , the method comprising the steps of:mixing at least one first zeolitic precursor material to form a synthesis gel;{'sup': '″1', 'processing the synthesis gel at a fluid shear rate exceeding 25,000 sto provide a high shear processed gel; and'}hydrothermally treating the high shear processed gel to provide the zeolitic material.2. The method of claim 1 , wherein the at least one first zeolitic precursor material is selected from the group consisting of a silica precursor claim 1 , an alumina precursor claim 1 , a phosphorus precursor claim 1 , a gallium (Ga) precursor claim 1 , a boron (B) precursor claim 1 , an iron (Fe) precursor claim 1 , a germanium (Ge) precursor claim 1 , a titanium (Ti) precursor claim 1 , a structure directing agent claim 1 , an alkali source claim 1 , seeds claim 1 , and combinations thereof.3. The method of claim 1 , further comprising mixing the high shear processed gel with at least one second zeolitic precursor material.4. The method of claim 3 , wherein the at least one second zeolitic precursor material is selected from the group consisting of a silica precursor claim 3 , an alumina precursor claim 3 , a phosphorus precursor claim 3 , a gallium (Ga) precursor claim 3 , a boron (B) precursor claim 3 , an iron (Fe) precursor claim 3 , a germanium (Ge) precursor claim 3 , a titanium (Ti) precursor claim 3 , a structure directing agent claim 3 , an alkali source claim 3 , seeds claim 3 , and combinations thereof.5. The method of claim 2 , wherein the at least one first zeolitic precursor material comprises a structure directing agent and silica precursor claim 2 ...

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22-03-2018 дата публикации

SYNTHESIS OF ZEOLITE WITH THE CHA CRYSTAL STRUCTURE, SYNTHESIS PROCESS AND USE THEREOF FOR CATALYTIC APPLICATIONS

Номер: US20180079650A1
Принадлежит:

The present invention relates to a new synthesis process of a crystalline material with the CHA structure, which comprises the following steps: i) Preparation of a mixture that comprises one source of water, one source of a tetravalent element Y, one source of an alkaline or alkaline earth cation (A), one source of a trivalent element X, and one organic molecule (OSDA1) with the structure [RRRRN]Q, being the molar composition: n XO:YO:a A:m OSDA1:z HO, ii) crystallisation of the mixture obtained in i) in a reactor, iii) recovery of the crystalline material obtained in ii). 2. Process according to claim 1 , wherein the source of the tetravalent element Y is selected from silicon claim 1 , tin claim 1 , titanium claim 1 , germanium claim 1 , and combinations thereof.3. Process according to claim 2 , wherein the source of the tetravalent element Y is a source of silicon selected from silicon oxide claim 2 , silicon halide claim 2 , colloidal silica claim 2 , fumed silica claim 2 , tetraalkyl orthosilicate claim 2 , silicate claim 2 , silicic acid claim 2 , a previously synthesised crystalline material claim 2 , a previously synthesised amorphous material claim 2 , and combinations thereof.4. Process according to claim 3 , wherein the source of silicon is selected from a previously synthesised crystalline material claim 3 , a previously synthesised amorphous material and combinations thereof.5. Process according to claim 4 , wherein the previously synthesised materials contain other heteroatoms in their structure.6. Process according to claim 1 , wherein the source of the trivalent element X is selected from aluminium claim 1 , boron claim 1 , iron claim 1 , indium claim 1 , gallium claim 1 , and combinations thereof.7. Process according to claim 6 , wherein the source of the trivalent element X is aluminium.8. Process according to claim 1 , wherein the OSDA1 is selected from tetraethylammonium claim 1 , methyl triethylammonium claim 1 , propyl triethylammonium claim 1 ...

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22-03-2018 дата публикации

SCR DIESEL PARTICLE FILTER WITH OXIDATION CATALYST AND OXYGEN STORAGE CATALYST LOADINGS, AND EXHAUST SYSTEM INCLUDING THE SAME

Номер: US20180080359A1
Принадлежит: UMICORE AG & CO. KG

A particle filter for treating exhaust gases includes an SCR catalyst that, when in the presence of a reductant such as ammonia, promotes selective catalytic reduction of NO; an active oxidation catalyst that promotes oxidation of hydrocarbons and carbon monoxide; and an oxygen storage catalyst that alternately stores and releases oxygen, enhances soot oxidation, and stores NOx at temperatures below optimal SCR functioning. The particle filter may be included in a system having an oxidation catalytic device (OCD) upstream of the particle filter, and optionally includes one or more SCR converters upstream and/or downstream of the particle filter, and/or an ammonia slip catalyst downstream of the particle filter. The system may further be adapted for operation under a high frequency injection fuel control with an OCD having substantial NOx storage material content, or an NSC for improving the efficiency tradeoffs between soot oxidation during filter regeneration and NOreduction. 1. A particle filter comprising:a selective catalytic reduction (SCR) catalyst that, when in the presence of a reducing agent, promotes selective catalytic reduction of nitrogen oxides;an oxidation catalyst (OC) component that promotes oxidation of hydrocarbons and carbon monoxide; andan oxygen storage catalyst (OSC) component that alternates between adsorbing and storing oxygen and desorbing and releasing oxygen when exposed to oscillating rich and lean exhaust conditions,wherein the OSC component comprises a material that lowers the oxidation temperature for soot that comes in contact with said material.2. The particle filter of claim 1 , whereinthe SCR catalyst comprises at least one material selected from: MOR; USY; ZSM-5; ZSM-20; beta-zeolite; CHA; LEV; FER; SAPO; ALPO; vanadium; vanadium oxide; titanium oxide; tungsten oxide; molybdenum oxide; cerium oxide; zirconium oxide; niobium oxide; iron; iron oxide; manganese oxide; copper; molybdenum; tungsten; and mixtures thereof.3. The ...

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19-06-2014 дата публикации

PLATINUM GROUP METAL (PGM) CATALYST FOR TREATING EXHAUST GAS

Номер: US20140170045A1
Принадлежит: JOHNSON MATTHEY PUBLIC LIMITED COMPANY

Provided are catalysts comprising a small pore molecular sieve embedded with platinum group metal (PGM) and methods for treating lean burn exhaust gas using the same. 1. A catalyst comprising:a. a small pore aluminosilicate molecular sieve material comprising a plurality of crystals having a surface and a porous network; andb. at least one Platinum Group Metal (PGM),wherein a majority amount of said PGM is embedded in said porous network relative to PGM disposed on said surface.2. The catalyst of claim 1 , wherein said aluminosilicate molecular sieve has a silica-to-alumina ratio of about 8 to about 150 and an alkali content of no more than about 5 weight percent based on the total weight of the aluminosilicate molecular sieve.3. The catalyst of claim 2 , wherein said catalyst comprises about 0.01 to about 10 weight percent PGM relative to weight of the molecular sieve.4. The catalyst of claim 2 , wherein said catalyst comprises about 0.1 to about 1 weight percent PGM relative to weight of the molecular sieve.5. The catalyst of claim 2 , wherein the small pore molecular sieve material comprises a plurality of crystals having a mean crystalline size of about 0.01 to about 10 microns.6. The catalyst of claim 2 , wherein the small pore molecular sieve material comprises a plurality of crystals having a mean crystalline size of about 0.5 to about 5 microns.7. The catalyst of claim 5 , wherein the small pore molecular sieve material has a framework selected from ACO claim 5 , AEI claim 5 , AEN claim 5 , AFN claim 5 , AFT claim 5 , AFX claim 5 , ANA claim 5 , APC claim 5 , APD claim 5 , ATT claim 5 , CDO claim 5 , CHA claim 5 , DDR claim 5 , DFT claim 5 , EAB claim 5 , EDI claim 5 , EPI claim 5 , ERI claim 5 , GIS claim 5 , GOO claim 5 , IHW claim 5 , ITE claim 5 , ITW claim 5 , LEV claim 5 , KFI claim 5 , MER claim 5 , MON claim 5 , NSI claim 5 , OWE claim 5 , PAU claim 5 , PHI claim 5 , RHO claim 5 , RTH claim 5 , SAT claim 5 , SAV claim 5 , SIV claim 5 , THO claim 5 , ...

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01-04-2021 дата публикации

MULTI-FUNCTION CATALYST ARTICLE FOR TREATING BOTH CO AND NOx IN STATIONARY EMISSION SOURCE EXHAUST GAS

Номер: US20210094022A1

A multi-function catalyst article for treating both NO and carbon monoxide emissions in a flow of a combustion exhaust gas from a stationary emission source comprises a honeycomb monolith substrate comprising one or more channels which are open at both ends and extend along an axial length thereof and through which, in use, a combustion exhaust gas flows, which catalyst article comprising a catalyst composition comprising a combination of a first, vanadium-containing SCR catalyst component and a second component which is a compound of a transition metal comprising copper, manganese, cobalt, molybdenum, nickel or cerium or a mixture of any two or more thereof and optionally a third, crystalline molecular sieve component.

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05-04-2018 дата публикации

NOVEL ZEOLITE SYNTHESIS WITH A FLUORIDE SOURCE

Номер: US20180093255A1
Принадлежит:

Provided are a novel synthesis technique for producing pure phase aluminosilicate zeolite and a catalyst comprising the phase pure zeolite in combination with a metal, and methods of using the same. 1. A method for making an aluminosilicate zeolite comprising reacting a synthesis gel comprising at least one zeolite , a fluoride source , a structure directing agent (SDA) , and an optional additional silica source at a temperature of at least 100° C. until crystals of the desired zeolite form.2. The method of claim 1 , wherein the crystals are at least about 90% phase pure.3. The method of claim 1 , wherein the crystals have a silica-to-alumina rrtole ratio (SAR) of at least about 20.4. The method of claim 1 , wherein the at least one zeolite is selected from a group consisting of a small pore zeolite claim 1 , a medium pore zeolite claim 1 , and a large pore zeolite claim 1 , and(a) when the zeolite is a small pore zeolite, the desired zeolite has an AIX, AEI, CHA, LTA, ITW, RTH, LEV, STT, SFW, or IHW framework;(b) when the zeolite is a medium pore zeolite, the desiredzeolite has an MFI, STW, MWW, ITH, or MEL framework; and(c) when the zeolite is a large pore zeolite, the desiredzeolite has a BEA or ISV framework.5. The method of claim 4 , wherein the SDA comprises a cation and:(a) when the zeolite is a small pore zeolite; the cation comprises trimethyladamantammonium, N,N,N-dimethylethylcyclohexylammonium, pentamethylimidazolium, 1,2-dimethyl-3-(4-methylbenzypimidazolium, 1,2,3-trimethylimidazolium, 1,3-bis(1-adamantyl) imidazolium, 2,6-N,N-diethyl-cis 2,6-dimethylpiperidium, or a combination thereof;(b) when the zeolite is a medium pore zeolite, the cation comprises tetrapropylammonium, 2-ethyl-1,3,4-trimethylimidazolium, trimethyladamantammonium, hexamethyleneimine, hexamethonium, tetrabutyl ammonium, or a combination thereof;{'sup': '6,6', '(c) when the zeolite is a large pore zeolite, the cation comprises tetraethylammonium, 1,3,3-trimethyl-6-azoniumtricyclo [3. ...

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12-05-2022 дата публикации

Selective ammonia oxidation catalyst

Номер: US20220143579A1
Принадлежит: BASF Corp

The invention relates to a selective ammonia oxidation catalysts comprising a platinum group metal and a support comprising TiO2 doped with 0-10% by weight of SiO2, WO3, ZrO2, Y2O3, La2O3, or a mixture thereof. The invention further comprises methods for the manufacture of the selective ammonia oxidation catalysts, and integrated catalyst systems comprising the selective ammonia oxidation catalysts for treating an exhaust gas stream.

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14-04-2016 дата публикации

ORGANIC-FREE SYNTHESIS OF SMALL PORE ZEOLITE CATALYSTS

Номер: US20160101415A1
Принадлежит:

The present invention is directed to methods of enhancing the catalytic activities of 8-MR zeolites, the methods comprising treating a precursor 8-MR zeolite that has been prepared without the use of an organic structure directing agent and having an Si/Al ratio of less than 5, with high temperature steam for a period of time sufficient to extract at least a portion of the aluminum from the precursor zeolite framework to form a steam-treated zeolite having an Si/tetrahedral Al ratio of greater than 5, wherein the steam has a temperature in a range of from about 350° C. to about 850° C. The compositions produced by these methods and their use in catalytic reactions are also provided.

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08-04-2021 дата публикации

SDA-FREE SYNTHESIS OF CHABAZITE (CHA) ZEOLITE AND USES THEREOF

Номер: US20210101799A1
Принадлежит:

A method of making a chabazite (CHA) zeolite is disclosed. The method can include obtaining an aqueous gel comprising silicon dioxide (SiO), aluminum oxide (AlO), potassium oxide (KO), and a nucleating agent, and hydrothermally treating the aqueous gel to obtain the CHA zeolite. 1. A method of making a chabazite (CHA) zeolite , the method comprising:{'sub': 2', '2', '3', '2, '(a) obtaining an aqueous gel comprising silicon dioxide (SiO), aluminum oxide (AlO), potassium oxide (KO), and a nucleating agent; and'}(b) hydrothermally treating the aqueous gel to obtain the CHA zeolite.2. The method of claim 1 , wherein the aqueous gel in step (a) is maintained at room temperature for up to 24 hours claim 1 , preferably 6 to 24 hours claim 1 , 6 to 12 hours claim 1 , or 12 to 24 hours prior to the step (b) hydrothermal treatment.3. The method of any claim 1 , wherein the nucleating agent is a fluoride-containing nucleating agent.4. The method of claim 3 , wherein the fluoride-containing nucleating agent is ammonium fluoride (NHF).5. The method of claim 1 , wherein the gel has a molar composition of:{'sub': 2', '2', '3', '2', '4', '2', '2', '2, '1SiO: 0.2AlO: 0.391KO: 0.3NHF: xHO, where x is the molar ratio of HO/SiOand ranges from 10 to 20,'}{'sub': 2', '2', '3', '2', '4', '2, '1SiO: 0.2AlO: 0.39KO: yNHF: 15HO;'}{'sub': 2', '2', '3', '2', '4', '2, '1SiO: zAlO: 0.39KO: 0.3NHF: 15HO;'}{'sub': 2', '2', '3', '2', '4', '2, '1SiO: 0.2AlO: w KO: 0.3NHF: 15HO; or'}{'sub': 2', '2', '3', '2', '2', '4', '2, '1SiO: 0.2AlO: wKO: 0.04NaO: 0.3NHF: 15HO.'}6. The method of claim 1 , wherein hydrothermal treatment is performed at a temperature of 130° C. to 200° C.7. The method of claim 1 , further comprising:(c) washing the CHA zeolite, preferably with deionized water until a pH of around 7 is obtained; and(d) optionally performing an ion-exchange to protonate the CHA zeolite to produce an H-form of the CHA zeolite.8. The method of any claim 1 , wherein the CHA zeolite is calcined.9. The ...

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29-04-2021 дата публикации

CATALYST AND METHOD FOR PREPARING LIGHT OLEFIN USING DIRECT CONVERSION OF SYNGAS

Номер: US20210121859A1
Принадлежит:

A catalyst for preparing light olefin using direct conversion of syngas is a composite catalyst and formed by compounding component I and component II in a mechanical mixing mode. The active ingredient of component I is a metal oxide; and the component II is one or more than one of zeolite of CHA and AEI structures or metal modified CHA and/or AEI zeolite. A weight ratio of the active ingredients in the component Ito the component II is 0.1-20. The reaction process has high product yield and selectivity, wherein the sum of the selectivity of the propylene and butylene reaches 40-75%; and the sum of the selectivity of light olefin comprising ethylene, propylene and butylene can reach 50-90%. Meanwhile, the selectivity of a methane side product is less than 15%. 1. A catalyst , comprising a component I and a component II , which are compounded in a mechanical mixing mode; an active ingredient of the component I being a metal oxide; the component II being a zeolite of CHA or AEI topology; wherein ,{'sub': x', 'a', '(1-a)', 'x', 'a', '(1-a)', 'x', 'a', '(1-a)', 'x', 'a', '(1-a)', 'x', 'x', 'a', '(1-a)', 'x', 'a', '(1-a)', 'x', 'a', '(1-a)', 'x', 'a', '(1-a)', 'x', 'x', 'a', '(1-a)', 'x', 'a', '(1-a)', 'x', 'x', 'x', 'x', 'a', 'b', '(1-a-b)', 'x', 'a', 'b', '(1-a-b)', 'x, 'the metal oxide is at least one of MnO, MnCrO, MnAlO, MnZrO, MnInO, ZnO, ZnCrO, ZnAlO, ZnGaO, ZnInO, CeO, CoAlO, FeAlO, GaO, BiO, InO, InAlMnOand InGaMnO;'}{'sub': x', 'x', 'x', 'x', 'x', 'x, 'sup': '2', 'a specific surface area of MnO, ZnO, CeO, GaO, BiOand InOis 1-100 m/g;'}{'sub': a', '(1-a)', 'x', 'a', '(1-a)', 'x', 'a', '(1-a)', 'x', 'a', '(1-a)', 'x', 'a', '(1-a)', 'x', 'a', '(1-a)', 'x', 'a', '(1-a)', 'x', 'a', '(1-a)', 'x', 'a', '(1-a)', 'x', 'a', '(1-a)', 'x', 'a', 'b', '(1-a-b)', 'x', 'a', 'b', '(1-a-b)', 'x, 'sup': '2', 'a specific surface area of MnCrO, MnAlO, MnZrO, MnInO, ZnCrO, ZnAlO, ZnGaO, ZnInO, CoAlO, FeAlO, InAlMnO, and InGaMnOis 5-150 m/g;'}a value range of x is 0.7-3.7, and a ...

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20-04-2017 дата публикации

METHODS OF SYNTHESIZING CHABAZITE ZEOLITES WITH CONTROLLED ALUMINUM DISTRIBUTION AND STRUCTURES MADE THEREFROM

Номер: US20170107114A1
Принадлежит: PURDUE RESEARCH FOUNDATION

A method of synthesizing chabazite zeolites with controlled aluminum distribution. The method utilizes a source of an organic structure-directing agent, a source of an inorganic structure-directing agent, a source of aluminum and a source of silicon to form a synthesis gel which is subjected to a crystallization process to crystallize a chabazite zeolite with controlled aluminum distribution. A chabazite zeolite structure with controlled aluminum distribution. The structure contains zeolite crystal lattice framework containing silicon, aluminum, and oxygen; and extra-framework positions containing non-divalent chemical species such that each aluminum atom in the zeolite crystal lattice framework is in an isolated configuration. Another variant of this structure wherein a fraction of the aluminum atoms in the zeolite crystal lattice framework positions are not in an isolated configuration and hence oxygen atoms associated with aluminum atoms in the fraction can bind with the non-aluminum cations in the extra-framework positions. 1. A method of synthesizing chabazite zeolites with controlled aluminum distribution , the method comprising:adding a source of an organic structure-directing agent and a source of an inorganic structure-directing agent to water to form an aqueous solution and homogenizing the aqueous solution for a first time period;adding a source of aluminum to the homogenized aqueous solution to form an intermediate agent and homogenizing the intermediate agent for a second time period to form an aluminum-containing intermediate agent;adding a source of silicon to the aluminum-containing intermediate agent to form an aluminosilicate-containing intermediate agent and homogenizing the aluminosilicate-containing intermediate agent for a third time period to form a synthesis gel;subjecting the synthesis gel to a crystallization process to crystallize a chabazite zeolite with controlled aluminum distribution.2. The method of claim 1 , wherein the source of the ...

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11-04-2019 дата публикации

Metal-containing cha-type zeolite and method for producing the same

Номер: US20190105639A1
Принадлежит: Tosoh Corp

Provided is a metal-containing CHA-type zeolite in which a ratio of a maximum intensity of an absorption peak in a range of 3685 cm −1 or more and 3750 cm −1 or less to a maximum intensity of an absorption peak in a range of 1800 cm −1 or more and 1930 cm −1 or less is less than 1.5 in an IR spectrum. A method for producing the metal-containing CHA-type zeolite includes a metal incorporation step of mixing a metal source and a CHA-type zeolite in which a ratio of a maximum intensity of an absorption peak in a range of 3665 cm −1 or more and 3750 cm −1 or less to a maximum intensity of an absorption peak in a range of 1800 cm −1 or more and 1930 cm −1 or less is less than 1.5 in an IR spectrum.

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28-04-2016 дата публикации

Zeolite production method

Номер: US20160115039A1

Provided is a method for continuous production of zeolite in which a starting material is continuously supplied to a tubular reactor to produce an aluminophosphate zeolite that contains, in the framework structure, at least aluminum atoms and phosphorus atoms or an aluminosilicate zeolite having 5≦SiO 2 /Al 2 O 3 ≦2000. The tubular reactor is heated using a heat medium; a ratio (volume)/(lateral surface area) of the volume (inner capacity) to the lateral surface area of the tubular reactor is 0.75 cm or smaller; and seed crystals are added to the starting material. Through using a small-diameter tubular reactor and heating with a heat medium, it becomes possible to heat sufficiently the entirety of a starting material (zeolite precursor gel) in a short time, and to allow reaction to proceed at a high rate. The occurrence of irregular pressure fluctuations during continuous production of the zeolite can be prevented by adding seed crystals.

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30-04-2015 дата публикации

SEEDED SYNTHESIS OF ALUMINOSILICATE MOLECULAR SIEVES

Номер: US20150118151A1
Автор: Cao Guang, Shah Matu J.

A process for producing an aluminosilicate molecular sieve comprises crystallizing a reaction mixture comprising water, a source of silica and seeds of a silicoaluminophosphate and/or an aluminophosphate molecular sieve. The resultant aluminosilicate molecular sieve product can advantageously be substantially free of framework phosphorus. 1. A process for producing an aluminosilicate molecular sieve , wherein the process comprises:(a) crystallizing a reaction mixture comprising water, a source of silica and seeds of a silicoaluminophosphate and/or an aluminophosphate molecular sieve; and(b) recovering an aluminosilicate molecular sieve product substantially free of framework phosphorus.2. The process of claim 1 , wherein said reaction mixture comprises at least 500 wppm of said seeds.3. The process of claim 1 , wherein said reaction mixture comprises from about 1000 wppm to about 50000 wppm of said seeds.4. The process of claim 1 , wherein said synthesis mixture comprises from about 2000 wppm to about 25000 wppm of said seeds.5. The process of claim 1 , wherein said reaction mixture is substantially free of phosphorus claim 1 , apart from the phosphorus contained by said seeds.6. The process of claim 1 , wherein said reaction mixture also comprises a source of fluoride ions.7. The process of claim 1 , wherein said reaction mixture has a pH no more than 9.8. The process of claim 1 , wherein said reaction mixture has a pH from about 5 to about9. The process of claim 1 , wherein said reaction mixture further comprises an organic directing agent effective to direct the synthesis of said aluminosilicate molecular sieve product.10. The process of claim 1 , wherein said aluminosilicate molecular sieve product has a CHA framework claim 1 , and wherein said seeds comprise a silicoaluminophosphate and/or an aluminophosphate molecular sieve having double 6-membered rings as a structural building unit.11. The process of claim 10 , wherein said seeds comprise a ...

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07-05-2015 дата публикации

CARBON DIOXIDE GAS ADSORBENT INCLUDING CHABAZITE ZEOLITE, METHODS FOR PREPARING THE SAME, AND METHODS OF SEPARATING CARBON DIOXIDE USING THE SAME

Номер: US20150122124A1
Принадлежит: INHA-INDUSTRY PARTNERSHIP INSTITUTE

A carbon dioxide adsorbent may include a chabazite zeolite containing an alkali metal ion or alkaline earth metal ion. The chabazite zeolite may have a Si/Al mole ratio of about 1 to about 9.9 and mesopores. The carbon dioxide adsorbent may be included in a carbon dioxide capture module. The carbon dioxide adsorbent may also be used in a method of separating carbon dioxide. 1. A carbon dioxide adsorbent comprising:a chabazite zeolite containing an alkali metal ion or alkaline earth metal ion, the chabazite zeolite having a Si/Al mole ratio of about 1 to about 9.9, the chabazite zeolite having mesopores.2. The carbon dioxide adsorbent of claim 1 , wherein the Si/Al mole ratio is about 1 to about 5.3. The carbon dioxide adsorbent of claim 1 , wherein the alkali metal ion or alkaline earth metal ion comprises a lithium (Li) ion claim 1 , sodium (Na) ion claim 1 , potassium (K) ion claim 1 , barium (Ba) ion claim 1 , magnesium (Mg) ion claim 1 , calcium (Ca) ion claim 1 , or a combination thereof.4. The carbon dioxide adsorbent of claim 1 , wherein the chabazite zeolite has a chabazite structure resulting from structural transformation using a strong base.5. The carbon dioxide adsorbent of claim 1 , wherein the chabazite zeolite has an average pore size of about −1 nm to about 10 nm.6. The carbon dioxide adsorbent of claim 1 , wherein a volume of the mesopores in the chabazite zeolite is about 0.05 to about 0.50 cm/g as measured by the Barrett-Joyner-Halenda (BJH) method.7. The carbon dioxide adsorbent of claim 1 , wherein the chabazite zeolite has a BET surface area of greater than or equal to about 50 m/g.8. A process for preparing a carbon dioxide adsorbent including a chabazite zeolite containing an alkali metal ion or alkaline earth metal ion claim 1 , the chabazite zeolite having a Si/Al mole ratio of about 1 to about 9.9 claim 1 , the chabazite zeolite having mesopores claim 1 , the process comprising:obtaining a zeolite having a non-chabazite structure, the ...

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25-08-2022 дата публикации

CHABAZITE SYNTHESIS METHOD INCLUDING ORGANIC AND INORGANIC STRUCTURE DIRECTING AGENTS AND CHABAZITE ZEOLITE WITH FLAKE-LIKE MORPHOLOGY

Номер: US20220266228A1
Принадлежит:

The disclosure generally provides zeolites having the CHA crystalline framework and methods of preparing the same. Provided herein are CHA zeolites containing intergrowths, a controlled framework aluminum distribution, or both. Further provided are CHA zeolites wherein crystals of the zeolite material have a predominantly flake-like morphology as determined by scanning electron microscopy (SEM). Further provided are catalyst compositions, articles, and systems including CHA zeolites promoted with a metal. 1. A method of synthesizing a zeolite having a CHA crystalline framework , the method comprising:preparing a mixture of water, an aluminum source, a silica source, a source of an organic structure directing agent, and an inorganic structure-directing agent to form a synthesis gel, wherein the inorganic structure-directing agent is a source of potassium cations; andsubjecting the synthesis gel to a crystallization process to crystallize the zeolite having the CHA crystalline framework.2. The method of claim 1 , wherein the source of the potassium cations is potassium hydroxide.3. The method of claim 1 , wherein preparing comprises:a first mixing step comprising adding the source of the organic structure-directing agent, the source of the inorganic structure-directing agent, and the source of aluminum to the water to form an aluminum-containing aqueous solution;mixing the aqueous solution for a first time period; anda second mixing step comprising adding the source of silicon to the aluminum-containing aqueous solution and mixing for a second time period to form an aluminosilicate-containing solution.4. (canceled)5. (canceled)6. The method of claim 1 , wherein the crystallization process comprises mixing the synthesis gel at a temperature ranging from about 140° C. to about 200° C. for a time period of from about 24 hours to about 6 days.7. (canceled)8. The method of claim 1 , wherein the source of the organic structure-directing agent is N claim 1 ,N claim 1 ,N- ...

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14-05-2015 дата публикации

METHOD FOR PREPARING CHA-TYPE MOLECULAR SIEVES USING COLLOIDAL ALUMINOSILICATE AND A NOVEL OCTAHYDROINDOLIUM-BASED STRUCTURE DIRECTING AGENT

Номер: US20150132216A1
Автор: Elomari Saleh Ali
Принадлежит: Chevron U.S.A. INC.

The present invention is directed to a process for preparing CHA-type molecular sieves using a colloidal aluminosilicate in the presence of a octahydroindolium-based cationic structure directing agent. 1. A method of preparing a CHA-type molecular sieve , comprising:(a) preparing a reaction mixture containing: (1) a colloidal aluminosilicate; (2) cationic 1,1,2-trimethyloctahydroindolium as the structure directing agent; (3) at least one source of an element selected from Groups 1 and 2 of the Periodic Table; (4) hydroxide ions; and (5) water; and(b) subjecting the reaction mixture to crystallization conditions sufficient to form crystals of the CHA-type molecular sieve.10. The method of claim 1 , wherein the reaction mixture further comprises CHA seed crystals. The present invention is directed to a process for preparing CHA-type molecular sieves using a colloidal aluminosilicate composition and a 1,1,2-trimethyloctahydroindolium cation as the structure directing agent.Molecular sieves are a commercially important class of crystalline materials. They have distinct crystal structures with ordered pore structures which are demonstrated by distinct X-ray diffraction patterns. The crystal structure defines cavities and pores which are characteristic of the different species.Molecular sieves identified by the International Zeolite Associate (IZA) as having the structure code CHA are known. For example, the molecular sieve known as SSZ-13 is a known crystalline CHA material. It is disclosed in U.S. Pat. No. 4,544,538, issued Oct. 1, 1985 to Zones. In that patent, the SSZ-13 molecular sieve is prepared in the presence of a N-alkyl-3-quinuclidinol cation, a N,N,N-trialkyl-1-adamantammonium cation and/or, and N,N,N-trialkyl-2-exoaminonorbornane cation as the structure-directing agent (SDA).U.S. Publication No. 2007-0286798 to Cao et al., published Dec. 13, 2007, discloses the preparation of CHA-type molecular sieves using various SDAs, including a N,N,N-trimethyl-2- ...

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11-05-2017 дата публикации

HIGH EFFICIENCY AND DURABILITY SELECTIVE CATALYTIC REDUCTION CATALYST

Номер: US20170128883A1
Автор: Goffe Randal A.
Принадлежит: PACCAR INC

This disclosure features an exhaust aftertreatment system that includes a selective catalytic reduction catalyst that includes a metal oxide catalyst and a metal zeolite catalyst, a metal oxide catalyst that is other than a vanadium oxide catalyst and a vanadium oxide catalyst, or a metal oxide catalyst that is other than a vanadium oxide catalyst together with a metal zeolite catalyst and a vanadium oxide catalyst. When used in a selective catalytic reduction system in a diesel engine, the catalyst composition can increase a conversion efficiency of nitrogen oxides (NOx) to nitrogen and water by a minimum of 2 percent compared to the metal zeolite catalyst alone, the metal oxide catalyst alone, or the vanadium oxide catalyst alone, when present. 1. A selective catalytic reduction catalyst composition , comprising:a metal oxide catalyst; anda metal zeolite catalyst or a vanadium oxide catalyst,wherein the catalyst composition increases a conversion efficiency of nitrogen oxides to nitrogen and water by at least 2% compared to the metal oxide catalyst alone, the metal zeolite catalyst alone, or the vanadium oxide catalyst alone.2. The catalyst composition of claim 1 , wherein the metal oxide catalyst is selected from cerium oxide claim 1 , titanium oxide claim 1 , zirconium oxide claim 1 , aluminum oxide claim 1 , silicon oxide claim 1 , hafnium oxide claim 1 , vanadium oxide claim 1 , niobium oxide claim 1 , tantalum oxide claim 1 , chromium oxide claim 1 , molybdenum oxide claim 1 , tungsten oxide claim 1 , ruthenium oxide claim 1 , rhodium oxide claim 1 , iridium oxide claim 1 , nickel oxide claim 1 , barium oxide claim 1 , yttrium oxide claim 1 , scandium oxide claim 1 , calcium oxide claim 1 , manganese oxide claim 1 , chromium oxide claim 1 , lanthanum oxide claim 1 , strontium oxide claim 1 , cobalt oxide claim 1 , and any combination thereof.3. The catalyst composition of claim 1 , wherein the metal oxide catalyst is selected from the group consisting of ...

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09-05-2019 дата публикации

POROUS CERAMIC BODY TO REDUCE EMISSIONS

Номер: US20190134614A1
Принадлежит:

A porous ceramic honeycomb body including a substrate of intersecting porous walls forming axial channels extending from a first end face to a second end face. An active portion of the walls include a zeolite catalyst disposed inside pores thereof and/or is comprised of an extruded zeolite and a three way catalyst (TWC) is disposed on wall surfaces of at least a portion of the active portion. 1. A method of manufacturing a ceramic article , comprising:disposing zeolite catalyst inside pores in walls of a first portion of walls of a porous ceramic body; anddisposing three way catalyst (TWC) on wall surfaces of at least a portion of the first portion of the walls of the porous ceramic body.2. The method of claim 1 , wherein the TWC comprises at least one of hydrocarbon oxidation claim 1 , CO oxidation claim 1 , and NOx reduction catalysts.3. The method of claim 1 , wherein the walls of the porous ceramic body define axial channels extending from a first end face to a second end face of the porous ceramic body claim 1 , andthe first portion of the walls extends at least partially from the first end face to the second end face.4. The method of claim 1 , wherein the first portion of the walls is spaced apart from the first end face by a second portion of the walls.5. The method of claim 4 , wherein the second portion of the walls is substantially free of zeolite catalyst inside pores of the walls.6. The method of claim 4 , wherein the second portion of the walls has a lower density than the first portion of the walls.7. The method of claim 4 , wherein the first portion of the walls is spaced apart from the second end face by a third portion of the walls.8. The method of claim 7 , wherein the third portion of the walls is substantially free of zeolite catalyst inside pores of the walls.9. The method of claim 7 , wherein the second portion of the walls and the third portion of the walls are each substantially free of zeolite catalyst inside pores of the walls.10. A porous ...

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09-05-2019 дата публикации

ION-EXCHANGED MOLECULAR SIEVE CATALYSTS EXHIBITING REDUCED N2O EMISSIONS

Номер: US20190134617A1
Принадлежит:

The present disclosure generally provides catalysts, catalyst articles and catalyst systems including such catalyst articles. In particular, the catalyst composition includes a metal ion-exchanged molecular sieve ion-exchanged with at least one additional metal, which reduces the number of metal centers often present in metal promoted zeolite catalysts. Methods of making and using the catalyst composition are also provided, as well as emission treatment systems including a catalyst article coated with the catalyst composition. The catalyst article present in such emission treatment systems is useful to catalyze the reduction of nitrogen oxides in gas exhaust in the presence of a reductant while minimizing the amount of dinitrogen oxide emission. 1. A catalyst composition comprising:a metal ion-exchanged molecular sieve, comprising an ion-exchanged metal within at least a portion of the exchange sites of the molecular sieve, wherein the ion-exchanged metal is a rare-earth metal or a transition metal, and a combination thereof, and further comprising a promoter metal on or in the molecular sieve, wherein at least a portion of the promoter metal is located on a surface of the sieve or in an intra-pore site other than an exchange site, and wherein the ion-exchange metal and promoter metal are not the same metal.2. The catalyst composition of claim 1 , wherein the ion-exchanged metal is selected from the group consisting of Cu claim 1 , Co claim 1 , Ni claim 1 , La claim 1 , Mn claim 1 , Fe claim 1 , V claim 1 , Ag claim 1 , Ce claim 1 , Nd claim 1 , Pr claim 1 , Ti claim 1 , Cr claim 1 , Zn claim 1 , Nb claim 1 , Mo claim 1 , Hf claim 1 , Y claim 1 , and W.3. The catalyst composition of claim 1 , wherein the molecular sieve is a small pore molecular sieve comprising an 8-ring pore opening structure having a pore size of about 3 to about 5 Angstroms.4. The catalyst composition of claim 3 , wherein the molecular sieve has a structure type selected from AEI claim 3 , AFT ...

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10-06-2021 дата публикации

CHA ZEOLITE MATERIAL AND RELATED METHOD OF SYNTHESIS

Номер: US20210171357A1
Принадлежит:

The invention provides a method of synthesizing a zeolite having the CHA crystalline framework, the method including forming a reaction mixture comprising an alumina source comprising a zeolite having an FAU crystalline framework, a silica source, and an organic structure directing agent, the reaction mixture—having a combined molar ratio of M/Si+R/Si higher than the molar ratio OH/Si, wherein M is moles of alkali metal and R is moles of organic structure directing agent; and crystallizing the reaction mixture to form a product zeolite having the CHA crystalline framework, wherein the product zeolite has a mesopore surface area (MSA) of less than about 25 m/g. The invention also includes catalyst articles made using the product zeolite, exhaust gas treatment systems including the catalyst articles, and methods of treating exhaust gas using the catalyst articles. 1. A method of synthesizing a zeolite having the CHA crystalline framework , comprising:{'sup': '−', 'i) forming a reaction mixture comprising at least one alumina source comprising a zeolite, at least one silica source, and at least one organic structure directing agent, the reaction mixture having a combined molar ratio of M/Si+R/Si higher than the molar ratio OH/Si, wherein M is moles of alkali metal and R is moles of organic structure directing agent; and'}{'sup': '2', 'ii) crystallizing the reaction mixture to form a product zeolite having the CHA crystalline framework, wherein the product zeolite has a mesopore surface area (MSA) of less than about 25 m/g.'}2. The method of claim 1 , wherein the zeolite of the alumina source has an FAU crystalline framework.3. The method of claim 2 , wherein the zeolite having an FAU crystalline framework is zeolite Y.4. The method of claim 3 , wherein the zeolite Y is in the Na+ form and has a silica-to-alumina ratio (SAR) in the range of about 3 to about 6.5. The method of claim 1 , wherein M is sodium and the alkali metal silicate solution is sodium silicate.6. The ...

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25-05-2017 дата публикации

PROCESS FOR PRODUCING A CATALYST AND CATALYST AS SUCH

Номер: US20170144143A1
Принадлежит: JOHNSON MATTHEY PUBLIC LIMITED COMPANY

To be able to produce an SCR catalyst (), in particular one having a zeolite fraction (Z) as catalytically active fraction, in a reliable process and at the same time achieve good catalytic activity of the catalyst (), an inorganic binder fraction (B) which is catalytically inactive in the starting state and has been treated to develop catalytic activity is mixed into a catalyst composition (). The inorganic binder component for the binder fraction (B) is, in the starting state, preferably porous particles (), in particular diatomaceous earth, which display mesoporosity. To effect catalytic activation, the individual particles () are either coated with a catalytically active layer () or transformed into a catalytically active zeolite () with maintenance of the mesoporosity. 1. A process for producing an extruded catalyst , wherein a catalyst composition is extruded to produce a catalyst body , where , to set desired rheological properties of the catalyst composition , the latter comprises an inorganic binder fraction which is catalytically inactive in the starting state and is composed of at least one inorganic binder component consisting of individual particles and at least part of the inorganic binder fraction has been treated to develop catalytic activity.2. The process according to claim 1 , wherein a catalytically active component is mixed in addition to the binder fraction into the catalyst composition.3. The process according to claim 2 , wherein the catalytically active component is selected from among a zeolite and a molecular sieve.4. The process according to claim 2 , wherein the particles of the at least one inorganic binder component do not have a zeolitic framework structure in the catalytically inactive starting state.5. The process according to claim 2 , wherein the particles of the at least one inorganic binder component have a porous structure.6. The process according to claim 5 , wherein the particles have a greater pore width compared to a ...

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16-05-2019 дата публикации

CHA-TYPE ZEOLITE AND METHOD FOR PRODUCING THE SAME

Номер: US20190143309A1
Принадлежит: TOSOH CORPORATION

A CHA-type zeolite has a molar ratio of silica to alumina of 10.0 or more and less than 20.0 and a molar ratio of silanol groups to silicon of 0.15×10or more and 0.50×10or less, a molar ratio of silica to alumina of 20.0 or more and 35.0 or less and a molar ratio of silanol groups to silicon of 0.15×10or more and 1.10×10or less, a molar ratio of silica to alumina of more than 35.0 and 45.0 or less and a molar ratio of silanol groups to silicon of 0.15×10or more and 1.65×10or less, or a molar ratio of silica to alumina of more than 45.0 and 55.0 or less and a molar ratio of silanol groups to silicon of 0.15×10or more and 1.80×10or less. 1. A CHA-type zeolite having a molar ratio of silica to alumina of 10.0 or more and less than 20.0 and a molar ratio of silanol groups to silicon of 0.15×10or more and 0.50×10or less ,{'sup': −2', '−2, 'a molar ratio of silica to alumina of 20.0 or more and 35.0 or less and a molar ratio of silanol groups to silicon of 0.15×10or more and 1.10×10or less,'}{'sup': −2', '−2, 'a molar ratio of silica to alumina of more than 35.0 and 45.0 or less and a molar ratio of silanol groups to silicon of 0.15×10or more and 1.65×10or less, or'}{'sup': −2', '−2, 'a molar ratio of silica to alumina of more than 45.0 and 55.0 or less and a molar ratio of silanol groups to silicon of 0.15×10or more and 1.80×10or less.'}2. The CHA-type zeolite according to claim 1 , wherein a ratio of an intensity of a powder X-ray diffraction peak corresponding to a 20-1 reflection of the CHA-type zeolite subjected to heat treatment at 1000° C. for 5 hours in air to an intensity of a powder X-ray diffraction peak corresponding to a 20-1 reflection of the CHA-type zeolite subjected to heat treatment at 600° C. for 5 hours in air is 0.30 or more.3. The CHA-type zeolite according to claim 1 , comprising a crystal particle formed by chemical aggregation of primary particles.5. The production method according to claim 4 , wherein at least one of the N claim 4 ,N claim 4 ,N- ...

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16-05-2019 дата публикации

PROCESS FOR A CONTINUOUS SYNTHESIS OF ZEOLITIC MATERIALS

Номер: US20190144290A1
Принадлежит: BASF SE

The present invention relates to a continuous process for preparing a zeolitic material comprising (i) preparing a mixture comprising a source of YO, optionally a source of XO, and a liquid solvent system; (ii) continuously feeding the mixture prepared in (i) into a continuous flow reactor at a liquid hourly space velocity in the range of from 0.3 to 20 hfor a duration of at least 1 h; and (iii) crystallizing the zeolitic material from the mixture in the continuous flow reactor, wherein the mixture is heated to a temperature in the range of from 100 to 300° C.; wherein the volume of the continuous flow reactor is in the range of from 150 cmto 75 m, as well as to zeolitic materials which may be obtained according to the inventive process and to their use. 1. A continuous process for preparing a zeolitic material , comprising:{'sub': 2', '2', '3, 'preparing a mixture comprising a source of YO, optionally a source of XO, and a liquid solvent system;'}{'sup': '−1', '(ii) continuously feeding the mixture prepared in (i) into a continuous flow reactor at a liquid hourly space velocity in the range of from 0.3 to 20 hfor a duration of at least 1 h; and'}(iii) crystallizing the zeolitic material from the mixture in the continuous flow reactor,wherein the mixture is heated to a temperature in the range of from 100 to 300° C.;{'sup': 3', '3, 'wherein the volume of the continuous flow reactor is in the range of from 150 cmto 75 m.'}2. The process of claim 1 , wherein the continuous flow reactor is selected from the group consisting of a tubular reactor claim 1 , a ring reactor claim 1 , and a continuously oscillating reactor.3. The process of claim 1 , wherein the wall of the continuous flow reactor comprises a metallic material.4. The process of claim 1 , wherein the surface of the inner wall of the continuous flow reactor is lined with an organic polymer material.5. The process of claim 1 , wherein in (iii) the mixture is heated under autogenous pressure.6. The process of ...

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16-05-2019 дата публикации

ZEOLITE COMPOSITIONS AND METHODS FOR TAILORING ZEOLITE CRYSTAL HABITS WITH GROWTH MODIFIERS

Номер: US20190144291A1
Принадлежит: UNIVERSITY OF HOUSTON SYSTEM

Embodiments of the invention generally provide compositions of crystalline zeolite materials with tailored crystal habits and the methods for forming such crystalline zeolite materials. The methods for forming the crystalline zeolite materials include binding one or more zeolite growth modifiers (ZGMs) to the surface of a zeolite crystal, which results in the modification of crystal growth rates along different crystallographic directions, leading to the formation of zeolites having a tailored crystal habit. The improved properties enabled by the tailored crystal habit include a minimized crystal thickness, a shortened internal diffusion pathlength, and a greater step density as compared to a zeolite having the native crystal habit prepared by traditional processes. The tailored crystal habit provides the crystalline zeolite materials with an aspect ratio of about 4 or greater and crystal surfaces having a step density of about 25 steps/μmor greater. 1. A composition of a zeolite , comprising:a crystalline zeolite material comprised of a plurality of zeolite crystals, each zeolite crystal having a single cubic crystal structure;an upper surface of the zeolite crystal extending substantially parallel to a lower surface of the zeolite crystal;a length of the upper surface within a range from about 10 nm to about 1 μm;a width of the upper surface within a range from about 10 nm to about 1 μm;a plurality of side surfaces extending between the upper and lower surfaces;a thickness of the crystalline zeolite material extending substantially perpendicular between the upper and lower surfaces;an aspect ratio of about 4 or greater, wherein the aspect ratio is determined as a sum of one half of the length and one half of the width of the upper surface relative to the thickness of the crystalline zeolite material; anda plurality of vertical channels extending between the upper and lower surfaces, wherein each vertical channel independently has an exclusive diffusion pathway ...

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31-05-2018 дата публикации

LOW PHOSPHORUS CHABAZITES

Номер: US20180147569A1
Принадлежит: JOHNSON MATTHEY PUBLIC LIMITED COMPANY

A catalyst washcoat is provided having a molecular sieve with a CHA crystal structure; about 0.5 to about 5.0 mol % phosphorus; and SiOand AlOin a mole ratio of about 5 to about 40. The washcoat includes one or more promoters or stabilizers, and may be applied to a monolith substrate to produce a catalytically active article. 1. A method for reducing NOx in an exhaust gas comprising contacting the gas with a catalyst for a time and temperature sufficient to reduce the level of NOx compounds in the gas , wherein the catalyst is a catalyst comprising a composition comprising a molecular sieve material having a CHA framework , wherein the framework consists of periodic building units having 36 interlinked T-atoms selected from the group consisting of aluminum , silicon , and phosphorous , and wherein said molecular sieve material has a mean phosphorous concentration of about 0.5 to about 1.5 atoms per periodic building unit.2. The method of claim 1 , wherein said mean phosphorus concentration is about 1.0 to about 1.5 atoms per periodic building unit.3. The method of claim 1 , wherein said molecular sieve material has a silica-to-alumina ratio of at least about 10.4. The method of claim 1 , wherein said molecular sieve material has a silica-to-alumina ratio of at least about 10 and an Al:P ratio of greater than about 1.5. The method of claim 1 , wherein said molecular sieve material has a silica-to-alumina ratio of at least about 10 and an Al:P ratio of greater than about 10.6. The method of claim 1 , wherein said molecular sieve material has a silica-to-alumina ratio of at least about 10 and an Al:P ratio of greater than about 100.7. The method of claim 1 , wherein said phosphorus is connected to at least a portion of said aluminum via oxygen bridges.8. The method of claim 1 , wherein said molecular sieve material further comprises a non-aluminum base metal.9. The method of claim 8 , wherein said non-aluminum base metal is ion-exchanged.10. The method of claim 9 , ...

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07-06-2018 дата публикации

Polyaluminum salts and their uses in preparation of high-purity colloidal aluminum-silica composite particles and zeolites

Номер: US20180155203A1
Принадлежит: ECOLAB USA INC

Disclosed are novel aqueous aluminum complex compositions and methods of making and using them. The novel compositions comprise very low halide content, even when made from aluminum chlorohydrate. The compositions find use in the production of zeolites, coatings, abrasives, binders, and refractories; and in the treatment of wastewater for example. The methods of making the novel compositions include passing a first aqueous aluminum complex composition through an anion exchange column or otherwise contacting the first composition with the anion exchange resin to provide a second aqueous aluminum complex composition that is different from the first aqueous aluminum complex composition. Also disclosed are methods of making zeolites and aqueous silica-alumina compositions from the novel aqueous aluminum complex compositions.

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11-09-2014 дата публикации

CARBON DIOXIDE ADSORBENT INCLUDING ZEOLITE AND METHODS FOR PREPARING THE SAME

Номер: US20140251135A1
Принадлежит:

A carbon dioxide adsorbent may include a chabazite zeolite containing an alkali metal ion or an alkaline earth metal ion. The chabazite zeolite may have a Si/Al mole ratio of about 1 to about 9.9. The carbon dioxide adsorbent may be included in a carbon dioxide capture module. The carbon dioxide adsorbent may also be used in a method of separating carbon dioxide.

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21-06-2018 дата публикации

FUEL UPGRADING BY REFORMING AND DEHYDROCRACKING

Номер: US20180169623A1
Принадлежит:

Zn-promoted and/or Ga-promoted cracking catalysts, such as cracking catalysts comprising an MSE framework zeolite or an MFI framework zeolite can provide unexpectedly superior conversion of branched paraffins when used as part of a catalyst during reforming of a hydrocarbon fuel stream. The conversion and reforming of the hydrocarbon fuel stream can occur, for example, in an internal combustion engine. The conversion and reforming can allow for formation of higher octane compounds from the branched paraffins. 1. A catalytic composition comprising:at least 5 wt % relative to a weight of the catalytic composition of a first catalyst comprising a support material and about 0.25 wt % to about 10 wt % Rh relative to the weight of the first catalyst;at least 10 wt % relative to a weight of the catalytic composition of a second catalyst comprising a zeolite having a largest ring size of an 8-member ring and about 0.25 wt % to about 10 wt % Rh relative to the weight of the second catalyst; andat least 20 wt % relative to a weight of the catalytic composition of a third catalyst comprising a MSE framework type zeolite, an MFI framework type zeolite, or a combination thereof, and further comprising about 0.2 wt % to about 3.0 wt % of Zn, Ga, or a combination thereof relative to a weight of the third catalyst.2. The catalytic composition of claim 1 , wherein the catalytic composition comprises a physical mixture of the first catalyst claim 1 , the second catalyst claim 1 , and the third catalyst.3. The catalytic composition of claim 1 , wherein the MSE framework type zeolite comprises MCM-68.4. The catalytic composition of claim 1 , wherein the MFI framework type zeolite comprises ZSM-5 claim 1 , the third catalyst further comprising about 0.1 wt % to about 5.0 wt % P relative to a weight of the third catalyst.5. The catalytic composition of claim 1 , wherein the third catalyst comprises about 0.7 wt % to about 2.5 wt % Ga claim 1 , wherein the third catalyst comprises about 0 ...

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08-07-2021 дата публикации

ZEOLITE HAVING IMPROVED HEAT RESISTANCE AND CATALYST COMPOSITE USING SAME

Номер: US20210205794A1
Принадлежит:

Proposed is a reformed zeolite and a catalyst composite using the reformed zeolite which have improved heat resistance and are used in a selective catalytic reduction (SCR) catalyst using ammonia or urea as a reducing agent, in a filter-type selective catalytic reduction (SDPF) catalyst in which a filter is coated with the SCR catalyst, or in a lean nitrogen oxide diesel oxidation catalyst (NA-DOC). In the reformed zeolite and the catalyst composite, alumina components, which are a zeolite coating material, improve heat-resistance of the zeolite and promote catalytic efficiency in a high-temperature condition. 1. A nitrogen oxide adsorbing type diesel oxidation catalyst article comprising zeolite placed on a carrier , wherein the zeolite is coated with alumina sol.2. A selective catalytic reduction catalyst article comprising zeolite placed on a carrier , wherein the zeolite is coated with alumina sol.3. A filter-type selective catalytic reduction catalyst article comprising a zeolite placed on a carrier , wherein the zeolite is coated with alumina sol.4. (canceled)5. The catalyst article according to claim 1 , wherein the zeolite is H-beta zeolite or CHA zeolite.6. An exhaust gas treatment system comprising the catalyst article according to . The present disclosure relates to a reformed zeolite and a catalyst composite using the same which have improved heat-resistance and are used in a selective catalytic reduction (SCR) catalyst using ammonia or urea as a reducing agent, or in a filter-type SCR catalyst in which a filter is coated with the SCR catalyst, or in a lean nitrogen oxide diesel oxidation catalyst. The reformed zeolite according to the present disclosure is manufactured by coating or mixing zeolite with alumina sol, and a catalyst including the reformed zeolite according to the present disclosure may be improved at nitrogen oxide (NO) lowering performance at a high-temperature region and may be improved at thermal durability even when being exposed to ...

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04-06-2020 дата публикации

Method

Номер: US20200172405A1
Принадлежит:

A method for modifying the surface of a molecular sieve, comprising reacting a molecular sieve with an aminosilane, wherein the reaction is carried out in an aqueous solvent. A modified molecular sieve obtained by the method is also described. 1. A method for preparing a modified molecular sieve , which method comprises reacting a crystalline small pore or large pore molecular sieve with an aminosilane , wherein the reaction is carried out in an aqueous solvent and wherein the aqueous solvent comprises water in an amount of at least 10% by volume.2. The method according to claim 1 , wherein the aqueous solvent comprises water in an amount of at least 25% by volume claim 1 , preferably at least 50% by volume claim 1 , more preferably at least 75% by volume.3. The method according to or claim 1 , wherein the crystalline molecular sieve has an aluminosilicate framework claim 1 , an aluminophosphate framework claim 1 , a silicoaluminophosphate framework claim 1 , a metal-substituted aluminosilicate framework claim 1 , a metal-loaded aluminophosphate framework claim 1 , or a metal-loaded silicoaluminophosphate framework.4. The method according to claim 3 , wherein the crystalline molecular sieve is a metal-loaded molecular sieve having an aluminosilicate framework and the loaded metal comprises copper claim 3 , palladium claim 3 , platinum claim 3 , or mixtures thereof.5. The method according to claim 1 , wherein the crystalline molecular sieve is a small pore molecular sieve and has a Framework Type selected from the group consisting of ACO claim 1 , AEI claim 1 , AEN claim 1 , AFN claim 1 , AFT claim 1 , AFX claim 1 , ANA claim 1 , APC claim 1 , APD claim 1 , ATT claim 1 , CDO claim 1 , CHA claim 1 , DDR claim 1 , DFT claim 1 , EAB claim 1 , EDI claim 1 , EPI claim 1 , ERI claim 1 , GIS claim 1 , GOO claim 1 , IHW claim 1 , ITE claim 1 , ITW claim 1 , LEV claim 1 , KFI claim 1 , MER claim 1 , MON claim 1 , NSI claim 1 , OWE claim 1 , PAU claim 1 , PHI claim 1 , RHO ...

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18-09-2014 дата публикации

Selective Catalytic Reduction Catalyst System

Номер: US20140274665A1
Принадлежит: BASF Corp

Described are SCR catalyst systems comprising a first SCR catalyst composition and a second SCR catalyst composition arranged in the system, the first SCR catalyst composition having a faster DeNOx response time when exposed to ammonia than the second catalyst composition and the second SCR catalyst composition has a higher steady state DeNOx performance than the first catalyst composition. The SCR catalyst systems are useful in methods and systems to catalyze the reduction of nitrogen oxides in the presence of a reductant.

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05-07-2018 дата публикации

CHA TYPE ZEOLITIC MATERIALS AND METHODS FOR THEIR PREPARATION USING COMBINATIONS OF CYCLOALKYL- AND TETRAALKYLAMMONIUM COMPOUNDS

Номер: US20180186648A1
Принадлежит:

The present invention relates to a process for the preparation of a zeolitic material having a CHA-type framework structure comprising YOand XO, wherein said process comprises the steps of: 115.-. (canceled)17. The process of claim 16 , wherein the crystallization in step (2) is conducted under solvothermal conditions.18. The process of claim 16 , wherein the mixture provided in step (1) does not contain any substantial amount of a trimethyl benzyl ammonium containing compound.19. The process of claim 16 , wherein the mixture provided in step (1) further comprises seed crystals.20. A synthetic zeolitic material having a CHA-type framework structure prepared by the process of .22. The zeolitic material of claim 21 , wherein the particle size D10 of the zeolitic material is comprised in the range of from 400 to 2500 nm.23. The zeolitic material of claim 21 , wherein the average particle size D50 of the zeolitic material is comprised in the range of from 600 to 3500 nm.24. The zeolitic material of claim 21 , wherein the particle size D90 of the zeolitic material is comprised in the range of from 1200 to 4 claim 21 ,500 nm.25. The zeolitic material of claim 21 , wherein the CHA-type framework contains 5 wt-% or less of the elements P and/or As based on 100 wt-% a of SiOcontained in the framework structure.27. The zeolitic material of claim 21 , wherein the SiO:AlOmolar ratio ranges from 4 to 200.29. The synthetic zeolitic material of claim 21 , wherein the material is an adsorbent material claim 21 , an ion-exchange material claim 21 , a catalyst or a catalyst support. The present invention relates to a process for the preparation of a zeolitic material as well as to a zeolitic material having the CHA-type framework structure as such and as obtainable from the inventive process. Furthermore, the present invention relates to the use of the inventive zeolitic materials in specific applications.Molecular sieves are classified by the Structure Commission of the ...

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20-06-2019 дата публикации

SCR-Active Material

Номер: US20190184338A1
Принадлежит:

The present invention relates to an SCR-active material, comprising a small-pore zeolite, aluminum oxide and copper, characterized in that it contains 5 to 25 wt-% of aluminum oxide in relation to the entire material and that the copper is present on the aluminum oxide in a first concentration and on the small-pore zeolite in a second concentration. 2. The SCR-active material according to claim 1 , wherein the total amount of copper calculated as CuO and based on the total SCR-active material is 1 to 15 wt-%.3. The SCR-active material according to claim 1 , wherein the first concentration is higher than the second concentration.4. The SCR-active material according to claim 1 , wherein the first concentration is at least 1.5 times higher than the second concentration.5. The SCR-active material according to claim 1 , wherein the atomic ratio of copper to backbone aluminum submerged in the zeolite is 0.25-0.6 in the zeolite.6. The SCR-active material according to claim 1 , wherein the small-pore zeolite is an aluminosilicate and belongs to the structure type AEI claim 1 , CHA (chabazite) claim 1 , ERI (erionite) claim 1 , LEV (levyne) claim 1 , AFX claim 1 , DDR claim 1 , or KFI.7. The SCR-active material according to claim 6 , wherein the small-pore zeolite has an SAR value of 5 to 50.8. The SCR-active material according to claim 1 , wherein the small-pore zeolite is a silicoaluminosilicate or aluminophosphate and belongs to the structure type AEI claim 1 , CHA (chabazite) claim 1 , ERI (erionite) claim 1 , LEV (levyne) claim 1 , AFX claim 1 , DDR claim 1 , or KFI.9. The SCR-active material according to claim 1 , wherein the average crystallite size (d50) of the small-pore zeolite is 0.1 to 20 μm.10. The SCR-active material according to claim 1 , wherein the small-pore zeolite forms a core and the aluminum oxide forms a shell encasing said core.11. The SCR-active material according to claim 1 , wherein it is present in powder form.12. The SCR-active material according ...

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23-07-2015 дата публикации

DIESEL OXIDATION CATALYST AND EXHAUST SYSTEM

Номер: US20150202611A1
Принадлежит:

An oxidation catalyst for treating an exhaust gas from a diesel engine, which oxidation catalyst comprises: a first washcoat region comprising platinum (Pt), manganese (Mn) and a first support material; a second washcoat region comprising a platinum group metal (PGM) and a second support material; and a substrate having an inlet end and an outlet end; wherein the second washcoat region is arranged to contact the exhaust gas at the outlet end of the substrate and after contact of the exhaust gas with the first washcoat region. 1. An oxidation catalyst for treating an exhaust gas from a diesel engine , which oxidation catalyst comprises:a first washcoat region comprising platinum (Pt), manganese (Mn) and a first support material;a second washcoat region comprising a platinum group metal (PGM) and a second support material; anda substrate having an inlet end and an outlet end;wherein the second washcoat region is arranged to contact the exhaust gas at the outlet end of the substrate and after contact of the exhaust gas with the first washcoat region.2. An oxidation catalyst according to claim 1 , wherein the second washcoat region is a second washcoat zone disposed at an outlet end of the substrate claim 1 , and the first washcoat region is a first washcoat zone disposed at an inlet end of the substrate.3. An oxidation catalyst according to claim 1 , wherein the first washcoat region is a first washcoat zone and the second washcoat region is a second washcoat zone claim 1 , wherein the first washcoat zone and the second washcoat zone are disposed on the substrate as a single layer.4. An oxidation catalyst according to claim 1 , wherein the first washcoat region is a first washcoat layer claim 1 , and wherein the second washcoat region is a second washcoat zone claim 1 , which is disposed on the first washcoat layer.5. An oxidation catalyst according to claim 1 , wherein the first washcoat region is a first washcoat layer and the second washcoat region is a second ...

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22-07-2021 дата публикации

PROCESS FOR THE FLASH CALCINATION OF A ZEOLITIC MATERIAL

Номер: US20210221695A1
Принадлежит:

The present invention relates to a process for the calcination of a zeolitic material, wherein said process comprises the steps of 1. A process for the calcination of a zeolitic material , comprising:{'sub': '2', '(i) providing a zeolitic material comprising YOin its framework structure in the form of at least one of a powder or a suspension of the zeolitic material in a liquid, wherein Y is a tetravalent element;'}(ii) atomizing the zeolitic material in a gas stream to obtain an aerosol;(iii) calcining the aerosol to obtain a calcined powder.2. The process of claim 1 , wherein the providing comprises:{'sub': '2', '(i.a) preparing a mixture comprising a source for YOand a solvent system; and'}(i.b) crystallizing the mixture to obtain a suspension of a zeolitic material in a mother liquor as the suspension of the zeolitic material in a liquid.3. The process of claim 2 , wherein the providing further comprises:(i.c) separating the zeolitic material from the mother liquor;(i.d) optionally washing the zeolitic material obtained in (i.b) and/or (i.c) with at least one solvent; and(i.e) optionally drying the zeolitic material obtained in at least one of (i.b), (i.c) or (i.d).4. The process of claim 2 , wherein for providing the zeolitic material in the zeolitic material in a mother liquor is spray-dried.5. The process of claim 3 , wherein the providing further comprises:(i.f) providing a solvent system; and(i.g) suspending the zeolitic material in the form of a powder as obtained according to (i.c), (i.d) or (i.e) in the solvent system.6. The process of claim 2 , wherein the mixture provided in (i.a) further comprises an organotemplate.7. The process of claim 2 , wherein the solvent system comprises at least one of water or one or more organic solvents.8. The process of claim 1 , wherein Y is selected from the group consisting of Si claim 1 , Sn claim 1 , Ti claim 1 , Zr claim 1 , Ge claim 1 , and mixtures of two or more thereof.9. (canceled)10. The process of claim 1 , ...

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18-06-2020 дата публикации

Chabazite zeolite catalysts having low silica to alumina ratios

Номер: US20200188894A1
Принадлежит: BASF Corp

Disclosed are zeolite catalysts having the CHA crystal structure with a low silica to alumina ratio, as well as articles and systems incorporating the catalysts and methods for their preparation and use. The catalysts can be used to reduce NOx from exhaust gas streams, particularly those emanating from gasoline or diesel engines.

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30-07-2015 дата публикации

METHOD FOR PRODUCING MAZ-TYPE ZEOLITE

Номер: US20150210556A1
Принадлежит:

Provided is a method for producing a MAZ-type zeolite, the method having an environmental impact which has been reduced as much as possible whilst not using a structure-directing agent as far as possible. In the method for producing a MAZ-type zeolite according to the present invention: (1) a silica source, an alumina source, an alkali source and water are mixed so as to form a reaction mixture that has a composition represented by a specific molar ratio; (2) a MAZ-type zeolite, which has a SiO/AlOratio of 5-10, has an average particle diameter of at least 0.1 μm and does not contain an organic compound, is added, as a seed crystal, into the reaction mixture in an amount of 0.1-30 weight % relative to the silica components in the reaction mixture; and (3) the reaction mixture, into which the seed crystal has been added, is heated at 80-200° C. in a closed system. 1. A production method for an MAZ-type zeolite , which comprises(1) mixing a silica source, an alumina source, an alkali source and water so as to be a reaction mixture having a composition represented by a molar ratio given below;{'sub': 2', '2', '3, 'SiO/AlO=24-60'}{'sub': 2', '2', '2, '(NaO+KO)/SiO=0.25-0.5'}{'sub': 2', '2', '2, 'KO/(NaO+KO)=0.1-0.5'}{'sub': 2', '2, 'HO/SiO=5-50'}{'sub': 2', '2', '3, '(2) using an MAZ-type zeolite having no organic matters which has an SiO/AlOratio of 5-10 and an average particle size of 0.1 μm or more, as a seed crystal, and adding the MAZ-type zeolite to the reaction mixture at a proportion of 0.1-30% by weight with respect to a silica component in the reaction mixture; and'}(3) airtightly heating the reaction mixture to which the seed crystal is added at 80-200° C.2. The production method according to claim 1 , wherein after the reaction mixture not containing the seed crystal is airtightly preheated at a temperature of 80-200° C. claim 1 , the seed crystal is added to the reaction mixture claim 1 , and the reaction mixture is further airtightly heated at a ...

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18-06-2020 дата публикации

Process

Номер: US20200190005A1
Принадлежит:

A process the dehydration of methanol to dimethyl ether in the presence of a solid Br∅nsted acid catalyst selected from aluminosilicate zeolites which have a maximum free sphere diameter of greater than 3.67 Angstroms and heteropolyacids and a promoter selected from methyl formate, dimethyl oxalate and dimethyl malonate and the molar ratio of promoter to methanol is maintained at less than 1. 1. A process comprising dehydrating methanol to dimethyl ether product in the presence of a catalyst and a promoter , wherein the catalyst is at least one solid Br∅nsted acid catalyst selected from aluminosilicate zeolites which have a maximum free sphere diameter of greater than 3.67 Angstroms and heteropolyacids and the promoter is selected from methyl formate , dimethyl oxalate and dimethyl malonate , wherein the molar ratio of promoter to methanol is maintained at less than 1.2. A process according to wherein the total amount of promoter relative to methanol is maintained in an amount of at least 10 ppm.3. A process according to wherein the molar ratio of promoter to methanol is maintained in the range 0.00001:1 to 0.2:14. A process according to wherein a promoter is added to the dehydration process.5. A process according to wherein a promoter is generated in-situ in the dehydration process.6. A process according to wherein methyl acetate is not a component of the feed to the process.7. A process according to wherein the Br∅nsted acid catalyst is a zeolite which zeolite is a H-form zeolite.8. A process according to wherein the Br∅nsted acid catalyst is a zeolite which zeolite is a medium or large pore zeolite.9. A process according to wherein the zeolite is a medium pore zeolite and is a zeolite selected from framework types FER claim 8 , MFI claim 8 , MWW claim 8 , MTT and TON.10. A process according to wherein the zeolite is selected from framework types CHA claim 1 , MOR claim 1 , FAU and BEA.11. A process according to wherein the zeolite is composited with a binder ...

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06-08-2015 дата публикации

Pgm catalyst for treating exhaust gas

Номер: US20150217282A1
Принадлежит: JOHNSON MATTHEY PLC

Provided are catalysts comprising a small pore molecular sieve embedded with PGM and methods for treating lean burn exhaust gas using the same.

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04-07-2019 дата публикации

Process for producing a catalyst and catalyst as such

Номер: US20190201885A1
Принадлежит: JOHNSON MATTHEY PLC

To be able to produce an SCR catalyst ( 2 ), in particular one having a zeolite fraction (Z) as catalytically active fraction, in a reliable process and at the same time achieve good catalytic activity of the catalyst ( 2 ), an inorganic binder fraction (B) which is catalytically inactive in the starting state and has been treated to develop catalytic activity is mixed into a catalyst composition ( 4 ). The inorganic binder component for the binder fraction (B) is, in the starting state, preferably porous particles ( 10 ), in particular diatomaceous earth, which display mesoporosity. To effect catalytic activation, the individual particles ( 10 ) are either coated with a catalytically active layer ( 12 ) or transformed into a catalytically active zeolite ( 14 ) with maintenance of the mesoporosity.

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05-08-2021 дата публикации

Novel zeolite synthesis with a fluoride source

Номер: US20210237043A1
Принадлежит: JOHNSON MATTHEY PLC

Provided are a novel synthesis technique for producing pure phase aluminosilicate zeolite and a catalyst comprising the phase pure zeolite in combination with a metal, and methods of using the same.

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03-08-2017 дата публикации

TRANSITION METAL-CONTAINING ALUMINOSILICATE ZEOLITE

Номер: US20170216826A1
Принадлежит:

A synthetic aluminosilicate zeolite catalyst containing at least one catalytically active transition metal selected from the group consisting of Cu, Fe, Hf, La, Au, In, V, lanthanides and Group VIII transition metals, which aluminosilicate zeolite is a small pore aluminosilicate zeolite having a maximum ring size of eight tetrahedral atoms, wherein the mean crystallite size of the aluminosilicate zeolite determined by scanning electron microscope is >0.50 micrometer. 1. A catalyst comprising at least one of catalytically active metal selected from copper (Cu) , iron (Fe) , or vanadium (V) on an aluminosilicate zeolite having a CHA framework and a mean crystallite size , determined by scanning electron microscope , of >0.50 microns.2. The catalyst of claim 1 , wherein the mean crystallite size determined by scanning electron microscope is >1.00 microns.3. The catalyst of claim 1 , wherein the catalytically active metal is copper.4. The catalyst of claim 3 , wherein a majority of the copper is present as copper oxide.5. The catalyst of claim 1 , wherein the catalytically active metal is iron.6. The catalyst of claim 1 , wherein the catalytically active metal is vanadium.7. The catalyst of claim 1 , wherein the catalytically active metal is present from about 0.1 to 10 weight percent based on the total weight of the zeolite.8. The catalyst of claim 1 , wherein the catalytically active metal is present from about 0.5 to 5 weight percent based on the total weight of the zeolite.9. The catalyst of claim 1 , wherein the zeolite has a silica-to-alumina ratio (SAR) of 10 to 28.10. The catalyst of claim 1 , wherein said catalyst is characterized as achieving a greater than 60% NOx conversion at temperature below 200 deg. C. after the catalyst has been hydrothermally aged at a temperature of at least 750 deg. C. for at least 24 hours in at least 10% water vapor.11. An exhaust system for an engine claim 1 , which system comprising a catalyst according to and a reductant ...

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09-08-2018 дата публикации

REACTIVE FILTER FOR MOTOR VEHICLE

Номер: US20180223711A1
Принадлежит:

Disclosed is a reactive filter, that is a selective catalytic reduction filter or an oxidative reaction filter, including a porous substrate including internal pores having their inner surface, totally or partially, directly coated with a catalytic zeolite material resulting from an in situ hydrothermal synthesis. Also disclosed is a process for preparing such a reactive filter and the use thereof in an engine exhaust depolluting system. 129-. (canceled)3051112. A reactive filter comprising a porous substrate () comprising internal pores () having their inner surface () , totally or partially , directly coated with a catalytic zeolite material resulting from an in situ hydrothermal synthesis.31. A reactive filter according to that is a selective catalytic reduction filter or an oxidative reaction filter.325. A reactive filter according to claim 30 , wherein the porous substrate () hasa porosity when coated comprised between 5 and 90% and a mean pore size comprised between 0.1 and 100 μm; and/oran intrinsic porosity comprised between 5 and 90% and an intrinsic mean pore size comprised between 0.1 and 100 μm.335. A reactive filter according to claim 30 , wherein the porous substrate () is selected from the group consisting ofceramic-like materials, ceramic materials,cordierite ceramic, α-alumina, silicon carbide, aluminium titanate, silicon nitride, zirconia, mullite, spodumene, alumina-silica-magnesia, zirconium silicate,one or more metal alloys, metal alloys, sintered metals, porous refractory metals,titanium oxide, aluminium, iron, steel, sintered carbon,stainless steel, iron alloys, nickel alloys, chromium alloys, aluminium alloys, titanium alloys.345. A reactive filter according to claim 30 , wherein the porous substrate () is in a form selected from trapezoidal forms claim 30 , rectangular forms claim 30 , square forms claim 30 , sinusoidal forms claim 30 , hexagonal forms claim 30 , oval forms claim 30 , a honeycomb structure claim 30 , a monolith structure ...

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25-07-2019 дата публикации

ALUMINUM GRADIENT ALUMINOSILICATE ZEOLITE COMPOSITIONS

Номер: US20190225500A1
Принадлежит:

Disclosed herein are compositions comprising an aluminosilicate zeolite crystals with an 8 ring pore size having a depth dependent silica to alumina molar ratio and processes of making aluminosilicate zeolite crystals with an 8 ring pore size having a depth dependent silica to alumina molar ratio. 1. A composition comprising:an aluminosilicate zeolite crystal with an 8 ring pore size, the aluminosilicate zeolite crystal having a surface silica to alumina molar ratio and an internal silica to alumina molar ratio, wherein the surface silica to alumina molar ratio is either higher or lower than the internal silica to alumina molar ratio.2. The composition of claim 1 , wherein the aluminosilicate zeolite crystal comprises structural codes selected from the group consisting of AEI claim 1 , AFX claim 1 , CHA claim 1 , LEV claim 1 , AFT claim 1 , EAB claim 1 , KFI claim 1 , SAT claim 1 , TSC claim 1 , SAV claim 1 , ERI claim 1 , and combinations thereof.3. The composition of claim 1 , wherein the aluminosilicate zeolite crystal comprises CHA.4. The composition of claim 1 , wherein the composition is about 80% or more crystalline on a molar basis.5. The composition of claim 4 , wherein the composition is about 80% to about 95% crystalline on a molar basis.6. The composition of claim 1 , wherein the composition has a zeolitic BET surface area of about 400 m/g or more.7. The composition of claim 1 , wherein the surface silica to alumina molar ratio is one or more of the following:at least about 50 times higher or lower than the maximum value of the internal silica to alumina molar ratio;at least about 30 times higher or lower than the maximum value of the internal silica to alumina molar ratio;at least about 10 times higher or lower than the maximum value of the internal silica to alumina molar ratio;at least about 5 times higher or lower than the maximum value of the internal silica to alumina molar ratio; orat least about 1.5 times higher or lower than the maximum value of ...

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16-07-2020 дата публикации

Method for producing zeolite having controlled aluminum content by adjusting composition of synthesis mixture

Номер: US20200223707A1

Provided is a method for producing zeolite having a controlled aluminum content, wherein the sodium hydroxide molar concentration of a zeolite synthesis mixture can be adjusted to adjust the aluminum content in synthesized CHA. The structure of the low aluminum-content CHA produced by the provided method does not collapse even after high-temperature hydrothermal treatment, and thus the catalytic activity of the CHA can be maintained. Moreover, by adjusting the aluminum content in the framework, the properties of the produced CHA significantly change, and thus the CHA can be applied to various fields.

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25-08-2016 дата публикации

PROCESSES FOR PREPARING ZINCOALUMINOSILICATES WITH AEI, CHA, AND GME TOPOLOGIES AND COMPOSITIONS DERIVED THEREFROM

Номер: US20160243531A1
Принадлежит:

The present disclosure is directed to methods of producing zincoaluminosilicate structures with AEI, CHA, and GME topologies using organic structure directing agents (OSDAs), and the compositions and structures resulting from these methods. 6. The process of claim 5 , wherein R claim 5 , R claim 5 , and Rare each methyl.7. The process of claim 1 , wherein the composition being hydrothermally treated comprises a source of silicon oxide claim 1 , a source of aluminum oxide claim 1 , and a source of zinc oxide.8. The process of claim 1 , wherein:(a) the source of silicon oxide is or comprises an aluminosilicate, a zincoaluminosilicate, zincosilicate a silicate, silica hydrogel, silicic acid, fumed silica, colloidal silica, tetra-alkyl orthosilicate, a silica hydroxide or combination thereof;(b) the source of aluminum oxide is or comprises an alkoxide, hydroxide, or oxide of aluminum, a sodium aluminate, an aluminum siloxide, an aluminosilicate, a zincoaluminosilicate, zincoaluminate or combination thereof;(c) the source of zinc oxide is or comprises a zinc(II) dicarboxylate, zinc(II) halide, zinc(II) hydroxide, zinc(II)oxide, zinc(II)nitrate, zincosilicate, zincoaluminate or zincoaluminosilicate.9. The process of claim 1 , wherein the source of silicon oxide comprises sodium silicate claim 1 , the source of Al comprises a FAU-zeolite claim 1 , and the source of zinc oxide comprises zinc acetate.10. The process of claim 1 , wherein the mineralizing agent comprises an aqueous alkali metal or alkaline earth metal hydroxide.11. The process of claim 1 , wherein:(a) the molar ratio of Al:Si is in a range of 0.005 to 0.2.(b) the molar ratio of OSDA:Si is in a range of 0.1 to 0.75;(c) the molar ratio of water:Si is in a range of 5 to 50.(d) the molar ratio of total hydroxide:Si is in a range of 0.1 to 1.25; and(e) the molar ratio of Zn:Si is in a range of 0.01 to 0.2.12. The process of claim 1 , wherein the conditions effective to crystallize a crystalline microporous ...

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23-08-2018 дата публикации

CHABAZITE-TYPE ZEOLITE AND METHOD OF MANUFACTURING CHABAZITE-TYPE ZEOLITE

Номер: US20180237307A1
Принадлежит: TOSOH CORPORATION

A process of manufacturing a chabazite-type zeolite is provided having high heat resistance without having a large crystal size. A catalyst is also provided that contains such a chabazite-type zeolite and exhibits high nitrogen oxide reduction properties, and in particular high nitrogen oxide reduction properties in low temperatures below 200° C., even after exposure to high temperature and high humidity. A chabazite-type zeolite is provided having a silica to alumina molar ratio of no less than 15, a silanol group to silicon molar ratio of no more than 1.6×10, an average crystal size of 0.5 μm to less than 1.5 μm, and a ratio of 50%-volume particle size to 10%-volume particle size of no more than 3.2. The chabazite-type zeolite preferably contains at least one of copper and iron. 1. A process for producing a chabazite-type zeolite having a silica-to-alumina molar ratio of no less than 15 , a silanol group to silicon molar ratio of no more than 1.6×10 , an average crystal size of 0.5 μm to less than 1.5 μm , and a 50%-volume particle size to 10%-volume particle size of no more than 3.2 , comprising crystallizing a composition that contains a silica source , aluminum source , alkali source , structure directing agent , and water , where the composition has a sodium to silica molar ratio greater than zero , a potassium to sodium molar ratio less than 1.0 , a structure directing agent to silica molar ratio less than 0.1 , a water to silica molar ratio less than 20 , and a silica to alumina molar ratio of 27.5 to less than 50.0.2. The process according to claim 1 , wherein the structure directing agent is at least one selected from among an N claim 1 ,N claim 1 ,N-trialkyladamantane ammonium cation claim 1 , an N claim 1 ,N claim 1 ,N-trimethylbenzyl ammonium cation claim 1 , an N-alkyl-3-quinuclidinol cation claim 1 , and an N claim 1 ,N claim 1 ,N-trialkyl exoaminonorbornane cation.3. The process according to claim 1 , wherein the structure directing agent to silica ...

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30-07-2020 дата публикации

SELECTIVE OXIDATION USING ENCAPSULATED CATALYTIC METAL

Номер: US20200239784A1
Принадлежит:

Systems and methods are provided for selective oxidation of CO and/or C hydrocarbonaceous compounds in a reaction environment including hydrocarbons and/or hydrocarbonaceous components. The selective oxidation can be performed by exposing the CO and/or C hydrocarbonaceous compounds to a catalytic metal that is encapsulated in a small pore zeolite. The small pore zeolite containing the encapsulated metal can have a sufficiently small pore size to reduce or minimize the types of hydrocarbons or hydrocarbonaceous compounds that can interact with the encapsulated metal. 1. A method for selective oxidation of CO and C hydrocarbonaceous compounds , comprising:{'sub': 3−', '3−, 'exposing a feed comprising a) CO, C hydrocarbonaceous compounds, or a combination thereof, and b) at least one additional hydrocarbon, hydrocarbonaceous compound, or combination thereof, to an oxidizing environment in the presence of a small pore zeolite-encapsulated metal catalyst comprising 0.01 wt % to 10 wt % of Ru, Rh, Pd, Os, Ir, Pt, Ni, Au, Ag, or combination thereof as a catalytic metal, to oxidize at least a portion of the CO, C hydrocarbons, or a combination thereof, at least 20 wt % of the catalytic metal being encapsulated in the zeolite.'}2. The method of claim 1 , wherein exposing the feed comprises exposing the feed to a catalyst mixture comprising 0.001 wt % to 10 wt % of the small pore zeolite-encapsulated metal catalyst claim 1 , relative to a weight of the catalyst mixture.3. The method of claim 1 , wherein the C hydrocarbonaceous compounds comprise C hydrocarbons.4. The method of claim 1 , wherein the feed comprises CO claim 1 , C-hydrocarbonaceous compounds claim 1 , or a combination thereof.5. The method of claim 1 , wherein the feed comprises CO claim 1 , C-hydrocarbons claim 1 , or a combination thereof.6. The method of claim 1 , wherein the small pore zeolite-encapsulated metal catalyst comprises a synthetic small pore zeolite.7. The method of claim 6 , wherein at least 80 ...

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15-08-2019 дата публикации

Synthesis of Zeolite with the CHA Crystal Structure, Synthesis Process and Use Thereof for Catalytic Applications

Номер: US20190248663A1
Принадлежит:

Disclosed is a synthesis process of a crystalline material with the CHA structure, which comprises the following steps: i) Preparation of a mixture that comprises one source of water, one source of a tetravalent element Y, one source of an alkaline or alkaline earth cation (A), one source of a trivalent element X, and one organic molecule (OSDA1) with the structure [RRRRN]Q, being the molar composition: n XO:YO:a A:m OSDA1:z HO, ii) crystallisation of the mixture obtained in i) in a reactor, iii) recovery of the crystalline material obtained in ii). 130-. (canceled)31. A process of synthesizing a crystalline material with the CHA zeolite structure comprising , at least , the following steps:{'sup': 1', '2', '3', '4', '+', '−, 'claim-text': wherein the tetravalent element Y is silicon, and', 'wherein the trivalent element X is aluminium, and', 'wherein the source of the tetravalent element Y and the trivalent element X comprises faujasite', {'sup': 1', '2', '3', '4', '1', '2', '3', '4', '−, 'wherein R, R, Rand Rare selected from linear alkyl groups, and wherein R, R, Rand Reach have between 1 and 4 carbon atoms, but at least two of them must have at least two carbon atoms, and wherein Q is an anion, and'}, {'br': None, 'i': n', ':a', 'm', 'z, 'sub': 2', '3', '2', '2, 'XO:YOA:OSDA1:HO'}, 'wherein the OSDA1 is selected from tetraethylammonium, methyl triethylammonium, propyl triethylammonium, diethyl dipropylammonium, diethyl dimethylammonium, and combinations thereof, the mixture being the molar composition, n ranges between 0.005 and 0.1;', 'a ranges between 0 and 2;', 'm ranges between 0.01 and 2;', 'z ranges between 1 and 200;, 'wherein'}], 'i) Preparation of a mixture that comprises at least one source of water, at least one source of a tetravalent element Y, at least one source of an alkaline or alkaline earth cation A, at least one source of a trivalent element X, and at least one organic molecule (OSDA1) with the structure [RRRRN]Q,'}ii) Crystallization of the ...

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15-08-2019 дата публикации

Synthesis of Zeolite with the CHA Crystal Structure, Synthesis Process and Use Thereof for Catalytic Applications

Номер: US20190248664A1
Принадлежит:

Disclosed is a synthesis process of a crystalline material with the CHA structure, which comprises the following steps: i) Preparation of a mixture that comprises one source of water, one source of a tetravalent element Y, one source of an alkaline or alkaline earth cation (A), one source of a trivalent element X, and one organic molecule (OSDA1) with the structure [RRRRN]Q, being the molar composition: n XO:YO:a A:m OSDA:z HO, ii) crystallisation of the mixture obtained in i) in a reactor, iii) recovery of the crystalline material obtained in ii). 130-.31. A mixture comprising at least one source of water , at least one source of a tetravalent element Y , at least one source of an alkaline or alkaline earth cation A , at least one source of a trivalent element X , and at least one organic molecule (OSDA1) with the structure [RRRRN]Q ,{'sup': 1', '2', '3', '4', '1', '2', '3', '4', '−, 'claim-text': {'br': None, 'i': n', ':a', 'm', 'z, 'sub': 2', '3', '2', '2, 'XO:YOA:OSDA1:HO'}, 'wherein R, R, Rand Rare selected from linear alkyl groups, and wherein R, R, Rand Reach have between 1 and 4 carbon atoms, but at least two of them must have at least two carbon atoms, and wherein Q is an anion, being the molar composition n ranges between 0 and 0.1;', 'a ranges between 0 and 2;', 'm ranges between 0.01 and 2;', 'z ranges between 1 and 200., 'wherein'}32. The mixture according to claim 31 , wherein the source of the tetravalent element Y is selected from silicon claim 31 , tin claim 31 , titanium claim 31 , germanium claim 31 , and combinations thereof.33. The mixture according to claim 32 , wherein the source of the tetravalent element Y is a source of silicon selected from silicon oxide claim 32 , silicon halide claim 32 , colloidal silica claim 32 , fumed silica claim 32 , tetraalkyl orthosilicate claim 32 , silicate claim 32 , silicic acid claim 32 , a previously synthesised crystalline material claim 32 , a previously synthesised amorphous material claim 32 , and ...

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15-08-2019 дата публикации

Synthesis of Zeolite with the CHA Crystal Structure, Synthesis Process and Use Thereof for Catalytic Applications

Номер: US20190248665A1
Принадлежит:

Disclosed is a synthesis process of a crystalline material with the CHA structure, which comprises the following steps: i) Preparation of a mixture that comprises one source of water, one source of a tetravalent element Y, one source of an alkaline or alkaline earth cation (A), one source of a trivalent element X, and one organic molecule (OSDA1) with the structure [RRRRN]Q, being the molar composition: n XO:YO:a A:m OSDA1:z HO, ii) crystallisation of the mixture obtained in i) in a reactor, iii) recovery of the crystalline material obtained in ii). 130-.31. A crystalline material with the CHA zeolite structure made by a process comprising , at least , the following steps:{'sup': 1', '2', '3', '4', '+', '−, 'claim-text': [{'sup': 1', '2', '3', '4', '1', '2', '3', '4', '−, 'claim-text': {'br': None, 'i': n', ':a', 'm', ':z, 'sub': 2', '3', '2', '2, 'XO:YOA:OSDA1HO'}, 'wherein R, R, Rand Rare selected from linear alkyl groups, and wherein R, R, Rand Reach have between 1 and 4 carbon atoms, but at least two of them must have at least two carbon atoms, and wherein Q is an anion, being the molar composition, n ranges between 0 and 0.1;', 'a ranges between 0 and 2;', 'm ranges between 0.01 and 2;', 'z ranges between 1 and 200;, 'wherein'}], 'i) Preparation of a mixture that comprises at least one source of water, at least one source of a tetravalent element Y, at least one source of an alkaline or alkaline earth cation A, at least one source of a trivalent element X, and at least one organic molecule (OSDA1) with the structure [RRRRN]Q,'}ii) Crystallization of the mixture obtained in i) in a reactor; andiii) Recovery of the crystalline material obtained in ii).32. The crystalline material according to claim 31 , wherein the source of the tetravalent element Y is selected from silicon claim 31 , tin claim 31 , titanium claim 31 , germanium claim 31 , and combinations thereof.33. The crystalline material according to claim 32 , wherein the source of the tetravalent element ...

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15-08-2019 дата публикации

Synthesis of Zeolite with the CHA Crystal Structure, Synthesis Process and Use Thereof for Catalytic Applications

Номер: US20190248666A1
Принадлежит:

Disclosed is a synthesis process of a crystalline material with the CHA structure, which comprises the following steps: i) Preparation of a mixture that comprises one source of water, one source of a tetravalent element Y, one source of an alkaline or alkaline earth cation (A), one source of a trivalent element X, and one organic molecule (OSDA1) with the structure [RRRRN]Q, being the molar composition: n XO:YO:a A:m OSDA1:z HO, ii) crystallisation of the mixture obtained in i) in a reactor, iii) recovery of the crystalline material obtained in ii). 130-. (canceled)31. A selective catalytic reduction catalyst comprising a crystalline material with the CHA zeolite structure , wherein the crystalline material is made by a process comprising , at least , the following steps:{'sup': 1', '2', '3', '4', '+', '−, 'claim-text': {'sup': 1', '2', '3', '4', '1', '2', '3', '4', '−, 'claim-text': {'br': None, 'i': n', ':z, 'sub': 2', '3', '2', '2, 'XO:YO: a A:m OSDA1HO'}, 'wherein R, R, Rand Rare selected from linear alkyl groups, and wherein R, R, Rand Reach have between 1 and 4 carbon atoms, but at least two of them must have at least two carbon atoms, and wherein Q is an anion, being the molar composition, 'i) Preparation of a mixture that comprises at least one source of water, at least one source of a tetravalent element Y, at least one source of an alkaline or alkaline earth cation A, at least one source of a trivalent element X, and at least one organic molecule (OSDA1) with the structure [RRRRN]Q,'} n ranges between 0 and 0.1;', 'a ranges between 0 and 2;', 'm ranges between 0.01 and 2;', 'z ranges between 1 and 200;, 'wherein'}ii) Crystallization of the mixture obtained in i) in a reactor, andiii) Recovery of the crystalline material obtained in ii).32. The selective catalytic reduction catalyst according to claim 31 , wherein the source of the tetravalent element Y is selected from silicon claim 31 , tin claim 31 , titanium claim 31 , germanium claim 31 , and ...

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14-09-2017 дата публикации

AEI TYPE ZEOLITE, METHOD FOR PRODUCING SAME, AND USES THEREOF

Номер: US20170259250A1
Принадлежит: MITSUBISHI CHEMICAL CORPORATION

Provided is a method for producing an inexpensive, high-performance AEI type zeolite and an AEI type zeolite having a Si/Al ratio of 6.5 or less by using neither an expensive Y type zeolite as a raw material nor dangerous hydrofluoric acid. The method for producing an AEI type zeolite having a Si/Al ratio of 50 or less includes: preparing a mixture including a silicon atom material, an aluminum atom material, an alkali metal atom material, an organic structure-directing agent, and water; and performing hydrothermal synthesis of the obtained mixture, in which a compound having a Si content of 20% by weight or less and containing aluminum is used as the aluminum atom material; and the mixture includes a zeolite having a framework density of 14 T/1000 Åor more in an amount of 0.1% by weight or more with respect to SiOassuming that all Si atoms in the mixture are formed in SiO. 1. A method for producing an AEI type zeolite having a Si/Al ratio of 50 or less , the method comprising: a step of preparing a mixture comprising a silicon atom material , an aluminum atom material , an alkali metal atom material , an organic structure-directing agent , and water; and a step of performing hydrothermal synthesis by using the mixture obtained in the step , whereinthe aluminum atom material is a compound having a Si content of 20% by weight or less and containing aluminum; and{'sup': '3', 'sub': 2', '2, 'the mixture comprises a zeolite having a framework density of 14 T/1000 Åor more in an amount of 0.1% by weight or more with respect to SiOassuming that all Si atoms in the mixture are formed in SiO.'}2. The method for producing an AEI type zeolite according to claim 1 , wherein 50 mol % or more of alkali metal atoms contained in the alkali metal atom material in the mixture is sodium; and a molar ratio of sodium to the organic structure-directing agent in the mixture is 0.1 or more and 2.5 or less.3. The method for producing an AEI type zeolite according to claim 1 , wherein less ...

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04-12-2014 дата публикации

FORMED CERAMIC SUBSTRATE COMPOSITION FOR CATALYST INTEGRATION

Номер: US20140357476A1
Принадлежит:

Disclosed herein are formed ceramic substrates comprising an oxide ceramic material, wherein the formed ceramic substrate comprises a low elemental alkali metal content, such as less than about 1000 ppm. Also disclosed are composite bodies comprising at least one catalyst and a formed ceramic substrate comprising an oxide ceramic material, wherein the composite body has a low elemental alkali metal content, such as less than about 1000 ppm, and methods for preparing the same. 1. A formed ceramic substrate comprising an oxide ceramic material , wherein said formed ceramic substrate comprises an elemental sodium content of less than about 1200 ppm , and has a porosity of at least about 55%.2. The formed ceramic substrate according to claim 1 , wherein the elemental sodium content is less than about 1000 ppm.3. The formed ceramic substrate according to claim 1 , wherein the elemental sodium content is less than about 750 ppm.4. The formed ceramic substrate according to claim 1 , wherein the elemental sodium content is less than about 500 ppm.5. The formed ceramic substrate according to claim 1 , wherein the porosity is at least about 58%.6. The formed ceramic substrate according to claim 1 , wherein the porosity is at least about 60%.7. The formed ceramic substrate according to claim 1 , wherein the porosity is at least about 65%.8. A composite body comprising:a formed ceramic substrate comprising at least one oxide ceramic material; andat least one catalyst,wherein the formed ceramic substrate has an elemental sodium content of less than about 1200 ppm.9. The composite body according to claim 8 , wherein the elemental sodium content is less than about 1000 ppm.10. The composite body according to claim 8 , wherein the elemental sodium content is less than about 750 ppm.11. The composite body according to claim 8 , wherein the elemental sodium content is less than about 500 ppm.12. The composite body according to claim 8 , wherein the at least one catalyst is in a ...

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22-08-2019 дата публикации

Synthesis of Zeolite with the CHA Crystal Structure, Synthesis Process and Use Thereof for Catalytic Applications

Номер: US20190256366A1
Принадлежит:

Disclosed is a synthesis process of a crystalline material with the CHA structure, which comprises the following steps: i) Preparation of a mixture that comprises one source of water, one source of a tetravalent element Y, one source of an alkaline or alkaline earth cation (A), one source of a trivalent element X, and one organic molecule (OSDA1) with the structure [RRRRN]Q, being the molar composition: n XO:YO:a A:m OSDA:z HO, ii) crystallisation of the mixture obtained in i) in a reactor, iii) recovery of the crystalline material obtained in ii). 130-. (canceled)32. The zeolite material with the CHA structure according to claim 31 , wherein the tetravalent element Y is selected from silicon claim 31 , tin claim 31 , titanium claim 31 , germanium claim 31 , and combinations thereof.33. The zeolite material with the CHA structure according to claim 31 , wherein the tetravalent element Y is silicon.34. The zeolite material with the CHA structure according to claim 31 , wherein the trivalent element X is selected from aluminium claim 31 , boron claim 31 , iron claim 31 , indium claim 31 , gallium claim 31 , and combinations thereof.35. The zeolite material with the CHA structure according to claim 31 , wherein the trivalent element X is aluminium.36. A material which is obtainable by eliminating the organic content retained inside zeolite material according to by means of a heat treatment at temperatures ranging between 100° C. and 1000° C. for a period of time ranging between 2 minutes and 25 hours.37. A material which comprises the zeolite material with the CHA structure according to having ion exchanged cations by conventional ion exchange techniques.38. The material according to claim 37 , wherein the ion exchanged cations are selected from metals claim 37 , protons claim 37 , proton precursors claim 37 , and mixtures thereof.39. The material according to claim 38 , wherein the ion exchanged cations are of a metal selected from rare earth metals claim 38 , metals ...

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29-09-2016 дата публикации

Tin-containing zeolitic material having a bea framework structure

Номер: US20160279621A1
Принадлежит: BASF SE

A process for preparing a tin-containing zeolitic material having a BEA framework structure comprising providing a zeolitic material having a BEA framework structure having vacant tetrahedral framework sites, providing a tin-ion source in solid form, incorporating tin into the zeolitic material via solid-state ion exchange, calcining the zeolitic material, and treating the calcined zeolitic material with an aqueous solution having a pH of at most 5.

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29-08-2019 дата публикации

DIESEL OXIDATION CATALYST AND EXHAUST SYSTEM

Номер: US20190262772A1
Принадлежит:

An oxidation catalyst for treating an exhaust gas from a diesel engine, which oxidation catalyst comprises: a first washcoat region comprising platinum (Pt), manganese (Mn) and a first support material; a second washcoat region comprising a platinum group metal (PGM) and a second support material; and a substrate having an inlet end and an outlet end; wherein the second washcoat region is arranged to contact the exhaust gas at the outlet end of the substrate and after contact of the exhaust gas with the first washcoat region. 1. An oxidation catalyst for treating an exhaust gas from a diesel engine , which oxidation catalyst comprises:a first washcoat region comprising platinum (Pt), manganese (Mn) and a first support material;a second washcoat region comprising a platinum group metal (PGM) and a second support material; anda substrate having an inlet end and an outlet end;wherein the second washcoat region is arranged to contact the exhaust gas at the outlet end of the substrate and after contact of the exhaust gas with the first washcoat region.2. An oxidation catalyst according to claim 1 , wherein the second washcoat region is a second washcoat zone disposed at an outlet end of the substrate claim 1 , and the first washcoat region is a first washcoat zone disposed at an inlet end of the substrate.3. An oxidation catalyst according to claim 1 , wherein the first washcoat region is a first washcoat zone and the second washcoat region is a second washcoat zone claim 1 , wherein the first washcoat zone and the second washcoat zone are disposed on the substrate as a single layer.4. An oxidation catalyst according to claim 1 , wherein the first washcoat region is a first washcoat layer claim 1 , and wherein the second washcoat region is a second washcoat zone claim 1 , which is disposed on the first washcoat layer.5. An oxidation catalyst according to claim 1 , wherein the first washcoat region is a first washcoat layer and the second washcoat region is a second ...

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05-09-2019 дата публикации

CATALYTIC CONVERTER

Номер: US20190270070A1
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 ,wherein the at least one porous filler component comprises a diatomaceous earth material.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 , ...

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05-10-2017 дата публикации

MULTIPLE ZEOLITE HYDROCARBON TRAPS

Номер: US20170282166A1
Принадлежит:

Hydrocarbon (HC) traps are disclosed. The HC trap may include a first zeolite material having an average pore diameter of at least 5.0 angstroms and configured to trap hydrocarbons from an exhaust stream and to release at least a portion of the trapped hydrocarbons at a temperature of at least 225° C. The HC trap may also include a second zeolite material having an average pore diameter of less than 5.0 angstroms or larger than 7.0 angstroms. One or both of the zeolite materials may include metal ions, such as transition, Group 1A, or platinum group metals. The HC trap may include two or more discrete layers of zeolite materials or the two or more zeolite materials may be mixed. The multiple zeolite HC trap may form coke molecules having a relatively low combustion temperature, such as below 500° C. 1. A hydrocarbon trap , comprising:a first zeolite material having an average pore diameter of at least 5.0 angstroms and configured to trap hydrocarbons from an exhaust stream and to release at least a portion of the trapped hydrocarbons at a temperature of at least 225° C.; anda second zeolite material having an average pore diameter of less than 5.0 angstroms or larger than 7.0 angstroms.2. The trap of claim 1 , wherein the second zeolite material is configured to react with the hydrocarbons that are released from the first zeolite material to form coke molecules.3. The trap of claim 2 , wherein the second zeolite material is configured to form coke molecules having a combustion temperature of less than 500° C.4. The trap of claim 1 , wherein the first zeolite material is a beta (BEA) claim 1 , mordenite (MOR) or ZSM-5 (MFI) type zeolite.5. The trap of claim 1 , wherein the second zeolite material is a chabazite (CHA) claim 1 , ferrierite (FER) claim 1 , or ultra-stable Y (FAU) type zeolite.6. The trap of claim 1 , wherein the first zeolite material has a Si/Alratio of 20-50.7. The trap of claim 1 , wherein the first zeolite material includes from 0.1 to 10 wt. % ...

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05-10-2017 дата публикации

Manufacturing method of honeycomb structure

Номер: US20170282168A1
Принадлежит: NGK Insulators Ltd

The manufacturing method includes a step of mixing a coarse particle zeolite, a fine particle zeolite, and a raw material of an inorganic bonding material to prepare a zeolite raw material; a step of forming the prepared zeolite raw material into a honeycomb shape to prepare a honeycomb formed body; and a step of firing the prepared honeycomb formed body to prepare the honeycomb structure. In the step of preparing the zeolite raw material, as the coarse particle zeolite, a chabazite type zeolite having a specific average particle diameter, the fine particle zeolite having a specific average particle diameter, the raw material of the inorganic bonding material which includes at least basic aluminum lactate is used.

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04-10-2018 дата публикации

SELECTIVE CATALYTIC REDUCTION CATALYST

Номер: US20180280947A1
Принадлежит:

A selective catalytic reduction catalyst composition for converting oxides of nitrogen (NO) in an exhaust gas using a nitrogenous reductant, which catalyst composition comprising a mixture of a first component and a second component, wherein the first component is the H-form of an aluminosilicate chabazite zeolite (CHA); or an admixture of the H-form of an aluminosilicate mordenite zeolite (MOR) and the H-form of an aluminosilicate chabazite zeolite (CHA); and the second component is a vanadium oxide supported on a metal oxide support, which is titania, silica-stabilized titania or a mixture of titania and silica-stabilized titania, wherein the weight ratio of the first component to the second component is 10:90 to 25:75. 1. A selective catalytic reduction catalyst composition for converting oxides of nitrogen (NO) in an exhaust gas using a nitrogenous reductant , which catalyst composition comprising a mixture of a first component and a second component , wherein the first component is the H-form of an aluminosilicate chabazite zeolite (CHA); or an admixture of the H-form of an aluminosilicate mordenite zeolite (MOR) and the H-form of an aluminosilicate chabazite zeolite (CHA); and the second component is a vanadium oxide supported on a metal oxide support , which is titania , silica-stabilized titania or a mixture of titania and silica-stabilized titania , wherein the weight ratio of the first component to the second component is 10:90 to 25:75.2. The catalyst composition according to claim 1 , wherein the weight ratio of the H-form of the aluminosilicate mordenite zeolite (MOR) to the H-form of an aluminosilicate chabazite zeolite (CHA) is from 5:3 to 3:5 claim 1 , preferably 1:1 to 3:5.3. The catalyst composition according to claim 1 , wherein the weight ratio of the first component to the second component is 15:85 to 20:80.4. The catalyst composition according to claim 1 , comprising one or more binder component claim 1 , wherein the weight ratio of the ...

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12-09-2019 дата публикации

Catalyst and method for direct conversion of syngas to light olefins

Номер: US20190275505A1

Direct conversion of syngas to light olefins is carried out in a fixed bed or a moving bed reactor with a composite catalyst A+B. The active ingredient of catalyst A is active metal oxide; and catalyst B is one or more than one of zeolite of CHA and AEI structures or metal modified CHA and/or AEI zeolite. A spacing between geometric centers of the active metal oxide of the catalyst A and the particle of the catalyst B is 5 μm-40 mm. A spacing between axes of the particles is preferably 100 μm-5 mm, and more preferably 200 μm-4 mm. A weight ratio of the active ingredients in the catalyst A and the catalyst B is within a range of 0.1-20 times, and preferably 0.3-5.

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19-10-2017 дата публикации

HONEYCOMB CATALYST

Номер: US20170297007A1
Принадлежит: IBIDEN CO., LTD.

Provided is a honeycomb catalyst in which a plurality of through holes are provided in proximity to each other in a row arrangement in the lengthwise direction, and are set apart by partitions. A honeycomb unit contains at least two types of inorganic particles and an inorganic binder. The inorganic particles contain zeolite having an SiO2/Al2O3 composition ratio of less than 15 and a CHA structure and an oxide other than zeolite, which has a positive thermal expansion coefficient. The ratio (X:Y) of the volume (X) of zeolite and the volume (Y) of oxide is 50:50 to 80:20. A displacement amount of absorbed water is reduced and cracking is controlled while maintaining high NOx purging performance. 1. A honeycomb catalyst including a honeycomb unit having a plurality of through holes provided in parallel in a longitudinal direction and separated from one another by partition walls ,wherein the honeycomb unit contains two types of inorganic particles and an inorganic binder,{'sub': 2', '2', '3, 'the inorganic particles contain: zeolite having a CHA structure, a composition ratio of SiO/AlObeing less than 15; and an oxide other than the zeolite, the oxide having a positive linear expansion coefficient, and'}a ratio (X:Y) of a volume (X) of the zeolite and a volume (Y) of the oxide is 50:50 to 90:10.2. The honeycomb catalyst according to claim 1 , wherein an average particle size of the zeolite is 0.1 to 1.0 μm claim 1 , and an average particle size of the oxide is 0.01 to 5.0 μm.3. The honeycomb catalyst according to claim 1 , wherein a ratio (B/A) of the average particle size (A) of the zeolite and the average particle size (B) of the oxide is 1/10 to 5.4. The honeycomb catalyst according to claim 1 , wherein Cu is carried on the zeolite claim 1 , and a carried amount of Cu is 3.5 to 6.0 wt % with respect to the zeolite.5. The honeycomb catalyst according to claim 1 , wherein the oxide is at least one selected from the group consisting of alumina claim 1 , titania and ...

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18-10-2018 дата публикации

Exhaust gas treatment catalyst

Номер: US20180297014A1
Принадлежит: BASF Corp

Described is a catalyst composition suitable for use as a selective catalytic reduction catalyst, including small-pore molecular sieve particles having a pore structure and a maximum ring size of eight tetrahedral atoms and impregnated with a promoter metal, and metal oxide particles dispersed within the small-pore molecular sieve particles and external to the pore structure of the small-pore molecular sieve particles, wherein the metal oxide particles include one or more oxides of a transition metal or lanthanide of Group 3 or Group 4 of the Periodic Table. A method for preparing the catalyst, a method for selectively reducing nitrogen oxides, and an exhaust gas treatment system are also described.

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18-10-2018 дата публикации

CATALYST BLENDS

Номер: US20180297016A1
Принадлежит:

Provided is a catalyst for the selective reduction of NOx comprising a two molecular sieve materials having a CHA structure, wherein the first molecular sieve has a mean crystal size of about 0.01 to 1 μm and the second molecular sieve has a mean crystal size of about 1-5 μm, and wherein the first molecular sieve contains a first extra-framework metal, the second molecular sieve contains a second extra-framework metal, and wherein said first and second extra-framework metals are independently selected from the group consisting of cesium, copper, nickel, zinc, iron, tin, tungsten, molybdenum, cobalt, bismuth, titanium, zirconium, antimony, manganese, chromium, vanadium, niobium, and combinations thereof. 1. A catalyst composition comprising a blend of two molecular sieve materials each having a CHA structure , wherein the first molecular sieve has a first silica-to-alumina ratio (SAR) of about 10-25 and contains a first extra-framework metal , the second molecular sieve has second SAR of about 20-35 and contains a second extra-framework metal , and wherein said first and second SAR are different and said first and second extra-framework metals are independently selected from the group consisting of cesium , copper , nickel , zinc , iron , tin , tungsten , molybdenum , cobalt , bismuth , titanium , zirconium , antimony , manganese , chromium , vanadium , niobium , and combinations thereof ,and wherein at least one of the first and second extra-framework metals comprises manganese.2. The catalyst of claim 1 , wherein the two molecular sieve materials are aluminosilicates.3. The catalyst of claim 1 , wherein said first and second extra-framework metals are independently selected from the group consisting of copper claim 1 , iron claim 1 , and manganese claim 1 , and wherein at least one of the first and second extra-framework metals comprises manganese.4. The catalyst of claim 1 , wherein at least one of the first molecular sieve and the second molecular sieve is an ...

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27-10-2016 дата публикации

Diesel particulate filter

Номер: US20160310935A1
Принадлежит: Individual

A method of making a filter for filtering particulate matter from exhaust gas emitted from a lean-burn internal combustion engine, which filter comprising a porous substrate having inlet surfaces and outlet surfaces, wherein the inlet surfaces are separated from the outlet surfaces by a porous structure containing pores of a first mean pore size, wherein the inlet surfaces comprise a bridge network comprising interconnected particles of refractory material over the pores of the porous structure, which method comprising the step of contacting inlet surfaces of the filter substrate with an aerosol comprising refractory material in dry powder form. The invention also relates to a filter obtainable by such method.

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17-09-2020 дата публикации

PROCESS FOR THE FLASH CALCINATION OF A ZEOLITIC MATERIAL

Номер: US20200290884A1
Принадлежит: BASF SE

A process for the calcination of a zeolitic material, wherein the process contains the steps of (i) providing a zeolitic material containing YOand optionally further containing XOin its framework structure in the form of a powder and/or of a suspension of the zeolitic material in a liquid, wherein Y stands for a tetravalent element and X stands for a trivalent element; (ii) atomization of the powder and/or of the suspension of the zeolitic material provided in (i) in a gas stream for obtaining an aerosol; and (iii) calcination of the aerosol obtained in (ii) for obtaining a calcined powder, a zeolitic material obtained by the above process, and its use as a molecular sieve, as an adsorbent for ion-exchange, as a catalyst, and/or as a catalyst support.

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25-10-2018 дата публикации

CARBONYLATION CATALYST AND PROCESS

Номер: US20180304245A1
Автор: Sunley John Glenn
Принадлежит:

A catalyst and process for the production of methyl acetate by contacting dimethyl ether and carbon monoxide in the presence of a catalyst which is a zeolite of micropore volume of 0.01 ml/g or less. 1. A catalyst for the carbonylation of dimethyl ether with carbon monoxide to produce methyl acetate wherein the catalyst comprises a zeolite of micropore volume of 0.01 ml/g or less and which zeolite contains at least one channel which is defined by an 8-member ring.2. The catalyst according to wherein the 8-member ring is interconnected with at least one channel defined by a ring with 10 or 12 members.3. The catalyst according to wherein the zeolite is selected from zeolites of framework type MOR claim 1 , FER claim 1 , CHA claim 1 , OFF claim 1 , MFS and GME.4. The catalyst according to wherein the zeolite is in an ion-exchanged form.5. The catalyst according to wherein the ion-exchanged form is an ammonium or hydrogen form.6. The catalyst according to wherein the zeolite has the framework type MOR and is a mordenite.7. The catalyst according to wherein the mordenite is in an ammonium form.8. The catalyst according to wherein the mordenite has the framework elements claim 6 , silicon claim 6 , aluminium and at least one of gallium claim 6 , boron and iron.9. The catalyst according to wherein the framework elements are silicon claim 8 , aluminium and gallium.10. The catalyst according to wherein the zeolite micropore volume is from 0.00 ml/g to 0.01 ml/g.11. The catalyst according to wherein the zeolite contains 4% or greater by weight of carbon.12. The catalyst according to wherein the zeolite contains 4% to 5% by weight of carbon.13. The catalyst according to in which the zeolite is an uncalcined zeolite.14. The catalyst according to wherein the zeolite is composited with a binder material.15. The catalyst according to wherein the zeolite is prepared from a synthesis mixture comprising a source of silica claim 1 , a source of alumina claim 1 , a source of alkali or ...

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03-10-2019 дата публикации

Process for the production of a zeolitic material via solvent-free interzeolitic conversion

Номер: US20190300375A1
Принадлежит: BASF SE

A process for preparing a zeolitic material containing YO2 and X2O3, where Y and X represent a tetravalent element and a trivalent element, respectively, is described. The process includes (1) a step of preparing a mixture containing one or more structure directing agents, seed crystals, and a first zeolitic material containing YO2 and X2O3 and having FAU-, GIS-, MOR-, and/or LTA-type framework structures; and (2) a step of heating the mixture for obtaining a second zeolitic material containing YO2 and X2O3 and having a different framework structure than the first zeolitic material. The mixture prepared in (1) and heated in (2) contains 1000 wt % or less of H2O based on 100 wt % of YO2 in the framework structure of the first zeolitic material. A zeolitic material obtainable and/or obtained by the process and its use are also described.

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08-10-2020 дата публикации

Intra-crystalline binary catalysts and uses thereof

Номер: US20200316571A1
Автор: Randal A. Goffe
Принадлежит: PACCAR INC

The present disclosure describes, inter alia, binary catalyst compositions including a (metal) zeolite having a crystal lattice that incorporates a metal oxide, wherein the metal oxide is covalently bound to elements within the crystal lattice. The metal oxide forms an integral part of the (metal) zeolite crystal lattice, forming covalent bonds with at least the Si or Al atoms within the crystal lattice of the (metal) zeolite, and is dispersed throughout the (metal) zeolite crystal lattice. The metal oxide can substitute atoms within the crystal lattice of the (metal) zeolite.

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08-10-2020 дата публикации

Ammonia facilitated cation loading of zeolite catalysts

Номер: US20200316573A1
Автор: Randal A. Goffe
Принадлежит: PACCAR INC

The present disclosure features a high metal cation content zeolite-based binary catalyst (e.g., a high copper and/or iron content zeolite-based binary catalyst, where the zeolite can be a chabazite) for NO x reduction, having relatively low N 2 O make, and having low corresponding metal oxide content; where the metal in the metal oxide corresponds to the metal of the metal cation. The present disclosure also describes the synthesis of the zeolite-based binary catalyst having high metal cation content.

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03-12-2015 дата публикации

Molecular sieve precursors and synthesis of molecular sieves

Номер: US20150343375A1
Принадлежит: BASF Corp

Molecular sieves, improved methods for their synthesis, and catalysts, systems and methods of using these molecular sieves as catalysts in a variety of processes such as abating pollutants in exhaust gases and conversion processes are described. The molecular sieves are made using a tailored colloid including an alumina source, a silica source and a structure directing agent.

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24-10-2019 дата публикации

AEI TYPE ZEOLITE, METHOD FOR PRODUCING SAME, AND USES THEREOF

Номер: US20190321810A1
Принадлежит: MITSUBISHI CHEMICAL CORPORATION

Provided is a method for producing an inexpensive, high-performance AEI type zeolite and an AEI type zeolite having a Si/Al ratio of 6.5 or less by using neither an expensive Y type zeolite as a raw material nor dangerous hydrofluoric acid. The method for producing an AEI type zeolite having a Si/Al ratio of 50 or less includes: preparing a mixture including a silicon atom material, an aluminum atom material, an alkali metal atom material, an organic structure-directing agent, and water; and performing hydrothermal synthesis of the obtained mixture, in which a compound having a Si content of 20% by weight or less and containing aluminum is used as the aluminum atom material; and the mixture includes a zeolite having a framework density of 14 T/1000 Åor more in an amount of 0.1% by weight or more with respect to SiOassuming that all Si atoms in the mixture are formed in SiO. 1. An AEI type zeolite having an acidity of 1.2 mmol/g or more and 3.0 mmol/g or less and a Si/Al ratio of 6.5 or less.2. An AEI type zeolite , wherein a ratio of a Si/Al ratio of a calcined zeolite determined by Si-NMR to a Si/Al ratio {Si-NMR (Si/Al ratio)/XRF (Si/Al ratio)} is 90% or more and 200% or less; and the XRF (Si/Al ratio) is 20 or less.3. The AEI type zeolite according to claim 1 , wherein the AEI type zeolite comprises potassium and/or cesium at a molar ratio of 0.001 or more and 1.0 or less with respect to aluminum.4. The AEI type zeolite according to claim 2 , wherein the AEI type zeolite comprises potassium and/or cesium at a molar ratio of 0.001 or more and 1.0 or less with respect to aluminum.5. The AEI type zeolite according to claim 1 , wherein the AEI type zeolite has an average primary particle diameter of 0.01 μm or more and 3 μm or less.6. The AEI type zeolite according to claim 2 , wherein the AEI type zeolite has an average primary particle diameter of 0.01 μm or more and 3 μm or less.7. An AEI type zeolite from which an organic structure-directing agent has been ...

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17-12-2015 дата публикации

TRANSITION METAL-CONTAINING ALUMINOSILICATE ZEOLITE

Номер: US20150360212A1
Принадлежит: JOHNSON MATTHEY PUBLIC LIMITED COMPANY

A synthetic aluminosilicate zeolite catalyst containing at least one catalytically active transition metal selected from the group consisting of Cu, Fe, Hf, La, Au, In, V, lanthanides and Group VIII transition metals, which aluminosilicate zeolite is a small pore aluminosilicate zeolite having a maximum ring size of eight tetrahedral atoms, wherein the mean crystallite size of the aluminosilicate zeolite determined by scanning electron microscope is >0.50 micrometer. 1. A catalyst comprising at least one of catalytically active metal selected from copper (Cu) , iron (Fe) , or vanadium (V) on an aluminosilicate zeolite having a CHA framework and a mean crystallite size , determined by scanning electron microscope , of >0.50 microns.2. The catalyst of claim 1 , wherein the mean crystallite size determined by scanning electron microscope is >1.00 microns.3. The catalyst of claim 1 , wherein the catalytically active metal is copper.4. The catalyst of claim 3 , wherein a majority of the copper is present as copper oxide.5. The catalyst of claim 1 , wherein the catalytically active metal is iron.6. The catalyst of claim 1 , wherein the catalytically active metal is vanadium.7. The catalyst of claim 1 , wherein the catalytically active metal is present from about 0.1 to 10 weight percent based on the total weight of the zeolite.8. The catalyst of claim 1 , wherein the catalytically active metal is present from about 0.5 to 5 weight percent based on the total weight of the zeolite.9. The catalyst of claim 1 , wherein the zeolite has a silica-to-alumina ratio (SAR) of 10 to 28.10. The catalyst of claim 1 , wherein said catalyst is characterized as achieving a greater than 60% NOx conversion at temperature below 200 deg. C. after the catalyst has been hydrothermally aged at a temperature of at least 750 deg. C. for at least 24 hours in at least 10% water vapor.11. An exhaust system for an engine claim 1 , which system comprising a catalyst according to and a reductant ...

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07-11-2019 дата публикации

CORE-SHELL HYBRID CHABAZITE MATERIAL WITH A WIDE SILICON TO ALUMINUM RATIO (SAR) ACTIVITY WINDOW

Номер: US20190336954A1
Принадлежит:

A crystalline, core-shell hybrid Chabazite (CHA) material for use as a catalyst has a core with a silicon to aluminum ratio (SAR) that is less than 25 and a shell that at least partially encapsulates the core, the shell having an SAR of about 25 or greater. The crystalline, core-shell hybrid Chabazite is prepared by forming a first chabazite (CHA) material having a silicon to aluminum ratio (SAR) that is less than 25, placing the first CHA material into an aqueous reaction mixture comprising one or more precursors capable of forming a second chabazite (CHA) material having an SAR that is 25 or greater, growing the second CHA material on the surface of the first CHA material, and collecting the core-shell hybrid CHA material. 1. A crystalline , core-shell hybrid Chabazite (CHA) material for use as a catalyst , the core-shell hybrid CHA material comprising:a core having a silicon to aluminum ratio (SAR) that is less than 25; anda shell that at least partially encapsulates the core, the shell having an SAR of about 25 or greater.2. The core-shell hybrid CHA material according to claim 1 , wherein the SAR of the core is between about 10 to 15 and the SAR of the shell is about 25 to 50.3. The core-shell hybrid CHA material according to claim 2 , wherein the SAR of the core is between 12 to 14 and the SAR of the shell is about 25 to 30.4. The core-shell hybrid CHA material according to claim 3 , wherein the SAR of the core is about 13 and the SAR of the shell is about 25.5. The core-shell hybrid CHA material according to claim 1 , wherein the core is equivalent to an SSZ-13 zeolite phase and the shell is equivalent to an SSZ-25 zeolite phase.62. The core-shell hybrid CHA material according to claim 1 , wherein the material exhibits peaks in an x-ray diffraction pattern with a theta degree at as shown in claim 1 , when the material is freshly prepared.72. The core-shell hybrid CHA material according to claim 6 , wherein after hydrothermal aging at 800° C. for 6 hours claim ...

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13-12-2018 дата публикации

DIESEL OXIDATION CATALYST AND EXHAUST SYSTEM

Номер: US20180353902A1
Принадлежит:

An exhaust system for a diesel engine comprises an oxidation catalyst for treating an exhaust gas from the diesel engine and an emissions control device, wherein the oxidation catalyst comprises: a first washcoat zone for oxidizing carbon monoxide (CO) and hydrocarbons (HCs), wherein the first washcoat zone comprises a first platinum group metal (PGM), which is a combination of platinum and palladium, a first support material and a hydrocarbon adsorbent material, which is a zeolite, and wherein the first washcoat zone does not comprise rhodium and is substantially free of manganese or an oxide thereof; a second washcoat zone for oxidizing nitric oxide (NO), wherein the second washcoat zone comprises platinum (Pt) and manganese (Mn) disposed or supported on a second support material, wherein the second support material comprises a refractory metal oxide, wherein the refractory metal oxide is silica-alumina or an alumina doped with silica in a total amount of 0.5 to 45% by weight of the alumina, and wherein the second washcoat zone does not comprise a hydrocarbon adsorbent material, which is a zeolite; and a substrate having and inlet end and an outlet end, and wherein the second washcoat zone is disposed at an outlet end of the substrate, and the first washcoat zone disposed at an inlet end of the substrate; and wherein the emissions control device is a selective catalytic reduction (SCR) catalyst, a selective catalytic reduction filter catalyst, a diesel particulate filter (DPF), or a catalyzed soot filter (CSF). 1. An exhaust system for a diesel engine , which comprises an oxidation catalyst for treating an exhaust gas from the diesel engine and an emissions control device , wherein the oxidation catalyst comprises: a first washcoat zone for oxidizing carbon monoxide (CO) and hydrocarbons (HCs) , wherein the first washcoat zone comprises a first platinum group metal (PGM) , which is a combination of platinum and palladium , a first support material and a ...

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13-12-2018 дата публикации

DIESEL OXIDATION CATALYST AND EXHAUST SYSTEM

Номер: US20180353903A1
Принадлежит:

An oxidation catalyst for treating an exhaust gas from a diesel engine comprises: a first washcoat region for oxidising carbon monoxide (CO) and hydrocarbons (HCs), wherein the first washcoat region comprises a first platinum group metal (PGM) and a first support material, and wherein the first washcoat region does not comprise manganese or an oxide thereof; a second washcoat region for oxidising nitric oxide (NO), wherein the second washcoat region comprises platinum (Pt), manganese (Mn) and a second support material comprising a refractory metal oxide, which is silica-alumina or alumina doped with silica in a total amount of 0.5 to 45% by weight of the alumina, wherein the platinum (Pt) is disposed or supported on the second support material and the manganese (Mn) is disposed or supported on the second support material; and a substrate having an inlet end and an outlet end, and wherein the first washcoat region is a first washcoat layer and the second washcoat region is a second washcoat layer, and the second washcoat layer is disposed on the first washcoat layer; and wherein when the oxidation catalyst comprises a hydrocarbon adsorbent, which is a zeolite, then the first washcoat region further comprises the hydrocarbon adsorbent 1. An oxidation catalyst for treating an exhaust gas from a diesel engine , which oxidation catalyst comprises:a first washcoat region for oxidising carbon monoxide (CO) and hydrocarbons (HCs), wherein the first washcoat region comprises a first platinum group metal (PGM) and a first support material, and wherein the first washcoat region does not comprise manganese or an oxide thereof;a second washcoat region for oxidising nitric oxide (NO), wherein the second washcoat region comprises platinum (Pt), manganese (Mn) and a second support material comprising a refractory metal oxide, which is silica-alumina or alumina doped with silica in a total amount of 0.5 to 45% by weight of the alumina, wherein the platinum (Pt) is disposed or ...

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29-12-2016 дата публикации

CATALYTIC WALL-FLOW FILTER HAVING A MEMBRANE

Номер: US20160375429A1
Принадлежит:

The present invention relates to a catalytic wall-flow monolith for use in an emission treatment system, the monolith comprising a porous substrate and having a first face and a second face defining a longitudinal direction therebetween and first and second pluralities of channels extending in the longitudinal direction, 1. A catalytic wall-flow monolith for use in an emission treatment system , the monolith comprising a porous substrate and having a first face and a second face defining a longitudinal direction therebetween and first and second pluralities of channels extending in the longitudinal direction ,wherein the first plurality of channels provides a first plurality of inner surfaces and is open at the first face and closed at the second face, and wherein the second plurality of channels is open at the second face and closed at the first face,wherein a first catalytic material is distributed within the porous substrate,wherein a microporous membrane is provided in the first plurality of channels on a first portion, extending in the longitudinal direction, of the first plurality of inner surfaces, andwherein the first portion extends from the first face for 75 to 95% of a length of the first plurality of channels.2. The catalytic wall-flow monolith according to claim 1 , wherein the first portion extends 80 to 90% of a length of the first plurality of channels.3. The catalytic wall-flow monolith according to claim 1 , wherein the microporous membrane has a thickness which decreases along the longitudinal direction claim 1 , such that the thickness is greatest in a region adjacent the first face.4. The catalytic wall-flow monolith according to claim 1 , wherein the porous substrate has a first section extending in the longitudinal direction from the first face and a second section extending in the longitudinal direction from the second face and extending to the first section claim 1 , and wherein the first catalytic material is distributed throughout the ...

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12-11-2020 дата публикации

NOVEL ZEOLITE SYNTHESIS WITH A FLUORIDE SOURCE

Номер: US20200353453A1
Принадлежит: JOHNSON MATTHEY PUBLIC LIMITED COMPANY

Provided are a novel synthesis technique for producing pure phase aluminosilicate zeolite and a catalyst comprising the phase pure zeolite in combination with a metal, and methods of using the same. 1. An aluminosilicate zeolite comprising at least about 90% phase pure CHA framework and the aluminosilicate zeolite has an FT-IR spectrum according to .2. An aluminosilicate zeolite comprising at least about 90% phase pure CHA framework , wherein the aluminosilicate zeolite , according to its FT-IR spectrum , has an intensity ratio of less than about 5 between frequencies of about 3730 cmand about 1870 cm.3. The aluminosilicate zeolite of claim 2 , wherein the aluminosilicate zeolite has the intensity ratio ranges of about 1:10 to about 5:1 between frequencies of about 3730 cmand about 1870 cm.4. The aluminosilicate zeolite of claim 2 , wherein the aluminosilicate zeolite has a mean crystal size of less than about 3 μm.5. The aluminosilicate zeolite of claim 2 , wherein the aluminosilicate zeolite has an SAR of about 20 to about 500.6. The aluminosilicate zeolite of claim 2 , wherein the aluminosilicate zeolite is substantially free of alkaline metal.7. A method for storing NOcomprising contacting an exhaust gas stream containing NOwith an aluminosilicate zeolite of .8. A method for selectively reducing NOcomprising contacting an exhaust gas stream containing NOx with an aluminosilicate zeolite of .9. A method for oxidizing a component of an exhaust gas comprising contacting an exhaust gas stream containing the component with an aluminosilicate zeolite of claim 2 , wherein the component is selected from CO claim 2 , hydrocarbon claim 2 , and NH. This application is a continuation of U.S. application Ser. No. 15/718,002, filed Sep. 28, 2017, which claims priority benefit to U.S. Provisional Application No. 62/402,698, filed Sep. 30, 2016, the entire contents of each of which are incorporated herein by reference.The present invention relates to a method for synthesizing a ...

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20-12-2018 дата публикации

Cha type zeolitic materials and methods for their preparation using combinations of cycloalkyl and ethyltrimethylammonium compounds

Номер: US20180362357A1
Принадлежит: BASF Corp

The present invention relates to a process for the preparation of a zeolitic material having a CHA-type framework structure comprising YO 2 and X 2 O 3 , wherein said process comprises the steps of: (1) providing a mixture comprising one or more sources for YO 2 , one or more sources for X 2 O 3 , one or more optionally substituted ethyltrimethylammonium cation-containing compounds, and one or more tetraalkylammonium cation R 1 R 2 R 3 R 4 N + -containing compounds as structure directing agent; (2) crystallizing the mixture obtained in step (1) for obtaining a zeolitic material having a CHA-type framework structure; wherein Y is a tetravalent element and X is a trivalent element, wherein R 1 , R 2 , and R 3 independently from one another stand for alkyl, wherein R 4 stands for cycloalkyl, and wherein the YO 2 :X 2 O 3 molar ratio of the mixture in (1) ranges from 2 to 1,000, as well as to zeolitic materials which may be obtained according to the inventive process and to their use.

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