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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 3872. Отображено 100.
02-08-2012 дата публикации

Method for producing ddr zeolite

Номер: US20120196739A1
Принадлежит: NGK Insulators Ltd

Disclosed is a method for producing a DDR zeolite, which can be carried out using materials that are less harmful to the environment. The method for producing a DDR zeolite has a short hydrothermal synthesis time and does not require continuous agitation of the raw material solution. Specifically disclosed is a method for producing a DDR zeolite, which comprises: a raw material solution preparation step in which a raw material solution that contains 1-adamantaneamine, silica (SiO 2 ) and water at a molar ratio 1-adamantaneamine/SiO 2 of 0.002-0.5 and a molar ratio water/SiO 2 of 10-500 but does not contain ethylenediamine is prepared; and a crystal growth step in which hydrothermal synthesis is carried out while having the raw material solution and a DDR zeolite powder in contact with each other, so that crystals of DDR zeolite are grown using the DDR zeolite powder as a seed crystal.

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02-05-2013 дата публикации

Support for protein immobilization, immobilized protein, and methods for producing the same

Номер: US20130109072A1

A support for enzyme immobilization is described, which is for immobilizing enzymes of various molecular sizes and also for, due to the modification of the surface silanol groups of porous silica particles, for immobilizing various kinds of enzymes, and enables the design of an immobilized enzyme, which exhibits an activity equivalent to that of the corresponding non-immobilized enzyme and withstands repeated use. A method for producing the support is also described. The support includes porous silica particles having an interparticle void structure therein, characterized in that the porous silica particles have a specific average particle size, a specific surface area, a specific pore volume, a specific pore size distribution and a specific porosity and have a substituent containing an organic group or an amino group on the surface thereof. An immobilized protein obtained by immobilizing a protein on the above support is also described.

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09-05-2013 дата публикации

Ordered mesoporous titanosilicate and the process for the preparation thereof

Номер: US20130116453A1

The invention discloses three-dimensional, ordered, mesoporous titanosilicates wherein the Ti is in a tetrahedral geometry and exclusively substituted for Si in the silica framework. Such titanosilicates find use as catalysts for epoxidation, hydroxylation, C—H bond oxidation, oxidation of sulfides, aminolysis of epoxide and amoximation, with approx. 100% selectivity towards the products.

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06-06-2013 дата публикации

Stabilized microporous crystalline material, the method of making the same, and the use for selective catalytic reduction of nox

Номер: US20130142727A1
Принадлежит: PQ Corp

There is disclosed a microporous crystalline material having pore opening ranging from 3 to 5 Angstroms, where the material comprises a first metal chosen from alkali earth group, rare earth group, alkali group, or mixtures thereof, and a second metal chosen from iron, copper or mixtures thereof; and has a molar silica to alumina ratio (SAR) from 3 to 10. The microporous crystalline material disclosed herein may comprise a crystal structure having building units of double-6-rings (d6r) and pore opening of 8-rings as exemplified with framework types defined by the Structure Commission of the International Zeolite Association having structural codes of CHA, LEV, AEI, AFT, AFX, EAB, ERI, KFI, SAT, TSC, and SAV. There is also disclosed a method of selective catalytic reduction of nitrogen oxides in exhaust gas, comprising at least partially contacting the exhaust gases with an article comprising the disclosed microporous crystalline material.

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05-12-2013 дата публикации

Hydrocarbon Conversion Process Using a High Throughpout Process for Manufacturing Molecular Sieves

Номер: US20130324760A1
Принадлежит: ExxonMobil Chemical Patents Inc

A method of crystallizing a crystalline molecular sieve having a pore size in the range of from about 2 to about 19 Å, said method comprising the steps of (a) providing a mixture comprising at least one source of ions of tetravalent element (Y), at least one hydroxide source (OH − ), and water, said mixture having a solid-content in the range of from about 15 wt. % to about 50 wt. %; and (b) treating said mixture to form the desired crystalline molecular sieve with stirring at crystallization conditions sufficient to obtain a weight hourly throughput from about 0.005 to about 1 hr −1 , wherein said crystallization conditions comprise a temperature in the range of from about 200° C. to about 500° C. and a crystallization time less than 100 hr.

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19-12-2013 дата публикации

Titano-silico-alumino-phosphate

Номер: US20130334460A1
Принадлежит: Clariant Produkte Deutschland GmbH

A titano-silico-aluminophosphate which contains tetrahedrally coordinated titanium in the framework structure, which has a free coordination site for CO which can be detected by means of a characteristic IR band at 2192±5 cm −1 . The titano-silico-aluminophosphate has extremely high hydrothermal stability and has a good adsorption capacity even at higher temperatures. Also, a hydrothermal method to obtain a titano-silico-aluminophosphate starting from a synthetic gel mixture of an aluminium, phosphorus, silicon and a titanium source, as well as corresponding templates.

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02-01-2014 дата публикации

Metallophosphate molecular sieves, methods of preparation and use

Номер: US20140004024A1
Принадлежит: UOP LLC

A new family of crystalline microporous metallophosphates designated AlPO-57 has been synthesized. These metallophosphates are represented by the empirical formula R + r M m n+ EP x Si y O z where R is an organoammonium cation such as the DEDMA + , M is a divalent framework metal such as an alkaline earth or transition metal, and E is a framework element such as aluminum or gallium. The microporous AlPO-57 compositions are characterized by a new unique ABC-6 net structure and have catalytic properties for carrying out various hydrocarbon conversion processes and separation properties for separating at least one component.

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30-01-2014 дата публикации

MANUFACTURE OF CRYSTALLITE PARTICLES

Номер: US20140030180A1
Автор: Björk Emma, Odén Magnus
Принадлежит: NANOLITH SVERIGE AB

A method for the manufacture of crystallite particles, said method comprising the steps of: a) reacting a reaction solution comprising a silicate, a micelle forming agent, an alkane, a salt under stirring at pH 2 or lower, wherein the reaction solution comprises HCI in a concentration of at least 1.5 M, wherein the stirring is performed not more than 10 minutes, and b) treating the obtained material to remove the micelle forming agent with one method selected from i) heat treating the material above 300° C., ii) treating the material with at least one selected from HO, and HSO, iii) treating the material with microwaves to digest the micelle forming agent. An advantage is that the time for the synthesis is shortened considerably compared to the prior art. 1. A method for the manufacture of crystallite particles , said method comprising the steps of:a) reacting a reaction solution comprising a silicate, a micelle forming agent, an alkane, and a salt with HCl under stirring at pH 2 or lower, wherein the reaction solution comprises the HCl in a concentration of at least 1.4 M, and wherein the stirring is performed for not more than 10 minutes; and i) heat treating the reaction solution above 300° C.,', {'sub': 2', '2', '2', '4, 'ii) treating the reaction solution with at least one compound selected from the group consisting of HOand HSO, and'}, 'iii) treating the reaction solution with microwaves to digest the micelle forming agent; and, 'b) treating the reaction solution obtained in step a to remove the micelle forming agent with a method selected from the group consisting of'}wherein the manufactured crystallite particles are separate from each other.2. The method according to claim 1 , wherein the reaction solution comprises the HCl in a concentration of at least 2.0 M.3. The method according to claim 1 , wherein the stirring is performed for not more than 5 minutes.4. The method according to claim 1 , wherein the silicate is at least one silicate selected from the ...

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07-01-2021 дата публикации

Method for Producing Silicoaluminophosphate Sorbent

Номер: US20210001308A1
Принадлежит:

The invention relates to a method for synthesizing silicoaluminophosphate sorbents such as SAPO-56 and SAPO-47 comprising the use of a specific structure directing agent (SDA) comprising a mixture of different types of amines The structure providing agent (SDA) comprises N,N,N′,N′-tetramethyl-1,6-hexanediamine (TMHD) and a co-structure providing agent (co-SDA) selected among primary, secondary and tertiary amines comprising up to 15 carbon atoms and mixtures thereof. A preferred SDA comprises isopropylamine, dibutylamine and tripropylamine The sorbents are particularly suitable for up-grading biogas such as separating carbon dioxide from methane. 1. A method for preparing a silicoaluminophosphate sorbent comprising:providing a reaction mixture, said mixture comprising: a silicon-containing composition, an aluminum-containing composition, a phosphorous-containing composition, and a structure directing agent (SDA);crystallization of the reaction mixture thereby providing crystallized silicoalum inophosphate;recovering crystalline silicoaluminophosphate from the mixture;wherein the structure providing agent (SDA) comprises N,N,N′,N′-tetramethyl-1,6-hexanediamine (TMHD) and a co-structure providing agent (co-SDA) selected among primary, secondary and tertiary amines comprising up to 15 carbon atoms and mixtures thereof.2. The method according to claim 1 , wherein the co-SDA is selected among primary amines comprising a saturated hydrocarbon comprising up to 6 carbon atoms.3. The method according to claim 1 , wherein the silicoaluminophosphate sorbent is selected among SAPO-47 and SAPO-56.4. The method according to claim 1 , wherein the silicoaluminophosphate sorbent is SAPO-56.5. The method according to claim 1 , wherein the SDA comprises up to about 75% wt of the co-SDA.6. The method according to claim 1 , wherein the primary claim 1 , secondary and tertiary amines comprise saturated hydrocarbons.7. The method according to claim 6 , wherein the saturated hydrocarbons ...

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04-01-2018 дата публикации

DDR-TYPE ZEOLITE SEED CRYSTAL AND METHOD FOR MANUFACTURING DDR-TYPE ZEOLITE MEMBRANE

Номер: US20180001276A1
Принадлежит: NGK Insulators, Ltd.

A DDR-type zeolite seed crystal has an average particle diameter of less than or equal to 0.2 μm, and an average aspect ratio of less than or equal to 1.3. 1. A DDR-type zeolite seed crystal having an average particle diameter of less than or equal to 0.2 μm , and an average aspect ratio of less than or equal to 1.3.2. The DDR-type zeolite seed crystal according to claim 1 , wherein a crystallinity index is greater than or equal to 60.3. A method for manufacturing a DDR-type zeolite membrane comprising the steps of:coating a slurry containing DDR-type zeolite seed crystals onto a surface of a support, the DDR-type zeolite seed crystals having an average particle diameter of less than or equal to 0.2 μm and an average aspect ratio of less than or equal to 1.3, andcausing crystal growth of the DDR-type zeolite seed crystals.4. The method for manufacturing a DDR-type zeolite membrane according to claim 3 , comprising the step of forming the DDR-type zeolite seed crystal by heating a starting material solution containing a nucleus that includes DDR-type zeolite seed crystal for greater than or equal to 24 hours.5. The method for manufacturing a DDR-type zeolite membrane according to claim 4 , wherein a concentration of the nucleus in the starting material solution is greater than or equal to 0.5 mass %.6. The method for manufacturing a DDR-type zeolite membrane according to claim 4 , wherein the starting material solution is heated to greater than or equal to 110 degrees C. and less than or equal to 150 degrees C.7. The method for manufacturing a DDR-type zeolite membrane according to claim 5 , wherein the starting material solution is heated to greater than or equal to 110 degrees C. and less than or equal to 150 degrees C. The present invention relates to a DDR-type zeolite seed crystal and to a method for manufacturing a DDR-type zeolite membrane.A method is known of forming a DDR-type zeolite membrane on a surface of a support by use of a DDR-type zeolite seed ...

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05-01-2017 дата публикации

ZEOLITIC MATERIALS AND METHODS FOR THEIR PREPARATION USING ALKENYLTRIALKYLAMMONIUM COMPOUNDS

Номер: US20170001874A1
Принадлежит: BASF SE

The present invention relates to a process for the preparation of a zeolitic material comprising the steps of: 1. A process for the preparation of a zeolitic material comprising:{'sub': '2', 'claim-text': [{'sup': 1', '2', '3', '4', '+, 'more alkenyltrialkylammonium cation RRRRN-containing compounds'}, 'as structure directing agent; and, '(1) providing a mixture comprising one or more sources for YOand one or'}(2) crystallizing the mixture obtained in (1) to obtain a zeolitic material;wherein Y is a tetravalent element, and{'sup': 1', '2', '3, 'wherein R, R, and Rare each independently an alkyl group; and'}{'sup': '4', 'Ris an alkenyl group.'}2. The process of claim 1 , wherein R claim 1 , R claim 1 , and Rare each independently (C-C)alkyl claim 1 , and{'sup': '4', 'sub': 2', '6, 'wherein Ris (C-C)alkenyl.'}3. The process of claim 2 , wherein the structure directing agent provided in (1) comprises one or more compounds selected from the group consisting of N—(C-C)alkenyl-tri-(C-C)alkylammonium hydroxides.4. The process of claim 1 , wherein the mixture provided in (1) comprises two or more RRRRN-containing compounds claim 1 , wherein Rof the two or more compounds are different from one another and are (C-C)alkenyl groups.5. The process of claim 4 , wherein the mixture provided in (1) comprises two RRRRN-containing compounds claim 4 , wherein Rof the first compound (A) contains an end-chain —CH═CHmoiety claim 4 , and Rof the second compound (B) contains an end-chain moiety —CH claim 4 , andwherein a molar ratio A:B in the mixture is from 25:75 to 99:1.6. The process of claim 5 , wherein the compounds A and B are constitutional isomers with respect to the position of the double bond in R.7. The process of claim 1 , wherein Y is at least one selected from the group consisting of Si claim 1 , Sn claim 1 , Ti claim 1 , Zr and Ge.8. 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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08-01-2015 дата публикации

METHOD OF SYNTHESIS OF CMK-3-TYPE CARBON REPLICA

Номер: US20150010459A1
Принадлежит: UNIWERSYTET JAGIELLONSKI

The method of obtaining the CMK-3-type carbon replica, consisting of the introduction of SBA-15-type molecular sieve to a mixture of furfuryl alcohol and a solvent, the subsequent polycondensation of furfuryl alcohol, carbonization of the prepared, composite and removal of the hard template, according to the invention, is characterised in that the reaction of furfuryl alcohol polycondensation is carried out by the precipitation method in a slurry containing SBA-15 silica sieve, water, furfuryl alcohol and concentrated solution of hydrochloric acid in mass ratios, respectively, in the range from 1.00:32.33:1.00:6.65 to 1.00:30.83:2.50:16.64, whereas the ratio of the total mass of furfuryl alcohol and water to the mass of SBA-15 as well as the mass ratio of the concentrated HCl solution to the mass of furfuryl alcohol are kept at the constant value every time. 1. The method of obtaining the CMK-3-type carbon replica , consisting of the introduction of SBA-15-type molecular sieve to a mixture of furfuryl alcohol and a solvent , the subsequent polycondensation of furfuryl alcohol , carbonization of the prepared composite and removal of the hard template , characterized in that the reaction of furfuryl alcohol polycondensation is carried out by the precipitation method in a slurry containing SBA-15 silica sieve , water , furfuryl alcohol and concentrated solution of hydrochloric acid in mass ratios , respectively , in the range from 1.00:32.33:1.00:6.65 to 1.00:30.83:2.50:16.64 , whereas the ratio of the total mass of furfuryl alcohol and water to the mass of SBA-15 as well as the mass ratio of the concentrated HCl solution to the mass of furfuryl alcohol are kept at the constant value every time.2. The method according to claim 1 , wherein said the polycondensation process is carried out at a temperature from the range of 30-100° C.3. The method according to claim 1 , wherein said polycondensation process is carried out for a time not less than 1 hour. The subject of ...

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08-01-2015 дата публикации

Process for preparing organic-inorganic hybrid silicates and metal-silicates with an ordered structure and new hybrid silicates and metal-silicates

Номер: US20150011787A1
Принадлежит: Eni Spa

The present invention relates to a process for the preparation of organic-inorganic hybrid silicates and metal-silicates of the ECS type which uses as starting material the corresponding disilanes: said process is characterized by the presence of boric acid in the reagent mixture. With the process of the invention, ECS silicates and metal-silicates are obtained, characterized by an X-Ray diffractogram with reflections exclusively at angular values higher than 4.0° of 2Θ, and characterized by an ordered structure which contains: —structural units having formula (a), wherein R is an organic group: —boron—one or more elements T, different from boron, selected from groups IIIB, NB, VB, and transition metals, with a molar ratio Si/(Si+T) in said structure greater than 0.3 and lower than 1, wherein Si is the silicon contained in the structural unit having formula (a). The silicates and metal-silicates so obtained, containing both boron and at least one element T, are new. The process also allows new crystalline phases called ECS-13 and ECS-14 to be prepared.

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03-02-2022 дата публикации

METAL ORGANIC FRAMEWORKS AND METHODS OF PREPARATION THEREOF

Номер: US20220033425A1
Принадлежит:

A method of preparing a Metal Organic Framework (MOF) with an acoustically-driven microfluidic platform, the method comprising: depositing a liquid comprising MOF precursors on a piezoelectric substrate of an acoustic microfluidic platform, the MOF precursors comprising a metal ion and an organic ligand, applying acoustic irradiation to the liquid to induce azimuthal liquid recirculation, which causes formation of the MOF within the liquid, and isolating the MOF. 1. A method of preparing a Metal Organic Framework (MOF) with an acoustically-driven microfluidic platform , the method comprising:depositing a liquid comprising MOF precursors on a piezoelectric substrate of an acoustic microfluidic platform, the MOF precursors comprising a metal ion and an organic ligand,applying acoustic irradiation to the liquid to induce azimuthal liquid recirculation, which causes formation of the MOF within the liquid, andisolating the MOF.2. A method according to wherein the MOF is at least a partially activated MOF.3. A method according to wherein the MOF is an activated MOF.4. A method according to wherein the MOF has a high degree of orientation.5. A method according to wherein the acoustic irradiation comprises surface acoustic waves claim 1 , bulk acoustic waves or hybrid acoustic waves comprising both surface and bulk acoustic waves.6. A method according to wherein the surface acoustic waves are Rayleigh surface acoustic waves or shear-horizontal surface acoustic waves.7. A method according to wherein the acoustic irradiation comprises travelling or standing acoustic waves.8. A method according to wherein the azimuthal liquid recirculation is induced by off-centre acoustic waves.9. A method according to wherein the acoustic platform comprises at least one interdigitated transducer (IDT) positioned off-centred relative to the liquid comprising MOF precursors to generate off-centre acoustic waves.10. A method according to wherein the acoustic platform comprises two opposing off- ...

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18-01-2018 дата публикации

Method for the Pervaporation and Vapor-Permeation Separation of Gas-Liquid Mixtures and Liquid Mixtures by SAPO-34 Molecular Sieve Membrane

Номер: US20180015420A1
Принадлежит:

The present invention discloses a method for the pervaporation and vapor-permeation separation of a gas-liquid mixture or a liquid mixture by a SAPO-34 molecular sieve membrane, which comprises: 1) mixing an Al source, tetraethyl ammonium hydroxide, water, a Si source and a P source, and subjecting the resultant to hydrothermal crystallization, then centrifuging, washing and drying to get SAPO-34 molecular sieve seeds; 2) coating the SAPO-34 molecular sieve seeds onto the inner surface of a porous support tube; 3) synthesis of a SAPO-34 molecular sieve membrane tube; 4) calcining the obtained SAPO-34 molecular sieve membrane tube to obtain a SAPO-34 molecular sieve membrane; 5) using the SAPO-34 molecular sieve membrane obtained from step 4) to perform separation of a gas-liquid mixture or a liquid mixture via a process of pervaporation separation or vapor-permeation separation. The invention has the advantages of very high methanol selectivity and permeation flux, and provides an efficient and energy-saving separation way via pervaporation or vapor-permeation separation. 1. A method for pervaporation separation of a gas-liquid mixture or a liquid mixture by preparing and using a SAPO-34 molecular sieve membrane , characterized in that the method comprises:1) mixing and dissolving an Al source, tetraethyl ammonium hydroxide TEAOH, water, a Si source and a P source to make a reaction liquor for seeds, which is then subjected to crystallization for 4-7 h by heating at 170-210° C., then centrifuging, washing and drying to get SAPO-34 molecular sieve seeds;{'sub': 2', '3', '2', '5', '2', '2, 'wherein the molar ratio of the Al source, P source, Si source, tetraethylammonium hydroxide and all water in the reaction liquor for seeds is 1 AlO: 1-2 PO: 0.3-0.6 SiO: 1-3 TEAOH: 55-150 HO.'}2) coating the SAPO-34 molecular sieve seeds onto the internal surface of a porous support tube to get a porous support tube coated with SAPO-34 molecular sieve seeds;3) synthesizing a SAPO- ...

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24-01-2019 дата публикации

HIERARCHICAL SILICEOUS MESOSILICALITE NANOCARRIER

Номер: US20190022007A1
Принадлежит: Imam Abdulrahman Bin Faisal University

A mesosilicalite nanocarrier having a hierarchical silicalite characterized by a molar ratio of aluminum to silica in a range of 1:3000 to 1:1000. The hierarchical silicalite includes mesopores of a hexagonal structure, and micropores of silicalite structure with a microporous volume in the range of 0.05 cc/g to 0.1 cc/g. The nanocarrier has a mesophase content in the range of 30 wt % to 70 wt %, a microphase content in the range of 30 wt % to 70 wt %, and a mean pore diameter in the range of 1.5 nm to 5.5 nm. A method of preparing the stable mesosilicalite nanocarrier with hierarchical micro/mesopores to load an antioxidant or drug for targeted drug delivery is also described. 16-. (canceled)7. A method of preparing a mesosilicalite nanocarrier , comprising: a mesophase with mesopores of a hexagonal structure; and', 'a microphase with micropores of a microporous volume in the range of 0.05 cc/g to 0.1 cc/g;', 'wherein the mesophase content is in the range of 30% to 70% relative to a total weight of the nanocarrier, and the microphase content is in the range of 30% to 70% relative to the total weight of the nanocarrier; and', 'wherein a mean pore diameter of the mesosilicalite nanocarrier is in the range of 1.5 nm to 5.5 nm,, 'a hierarchical silicalite having a silica to aluminum molar ratio in a range of 1000:1 to 3000:1, comprisingthe method comprising:mixing a silica source with a template to form a first mixture,hydrothermally aging the first mixture at a temperature of 150° C.-200° C. for 24 hours to 86 hours to produce an aged first mixture;drying the aged first mixture to form a silicalite;treating the silicalite with an alkaline solution and a surfactant to form a second mixture;hydrothermally aging the second mixture at a temperature of 60° C.-120° C. for 12 hours to 36 hours at a rate of 3° C./min to 6° C./min to form an aged second mixture;neutralizing a pH of the aged second mixture;hydrothermally aging the aged second mixture at a temperature of 60° C.- ...

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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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01-02-2018 дата публикации

METALLO-SILICATE CATALYST (MSC) COMPOSITIONS, METHODS OF PREPARATION AND METHODS OF USE IN PARTIAL UPGRADING OF HYDROCARBON FEEDSTOCKS

Номер: US20180029022A1
Принадлежит:

The invention relates to the preparation of novel bi- or tri metallic silicate micro-porous and/or meso-porous materials based on cerium, nickel, copper and/or zinc on a porous silicate framework matrix to use its molecular sieve effect to target preferentially the acidic organic molecules present in hydrocarbon feedstocks like crude oil, bitumen, VGO and the like. The chosen metals are selected based on their ability to activate steam and transfer oxygen for completing the oxidation of carboxylic compounds or decarboxylating them. These composite materials can be prepared under hydrothermal synthesis conditions in order to produce suitable porous solids where the metals are well dispersed and preferentially distributed inside the channels of the silicate framework where they can interact only with the molecules that can go inside the channels. According to the invention, the metallo-silicate materials are prepared under hydrothermal synthesis conditions Modification of the physical-chemical properties of the porous silicate materials can be accomplished by partial replacement of the silicon atoms by cerium, nickel, copper and/or zinc atoms in the material by isomorphous substitutions of these elements in a synthesis gel or by post-synthesis modifications like ion-exchange or impregnation/deposition. The materials can be used as prepared catalysts for the steam catalytic reduction of the total acid number (TAN) in acidic crude oil feedstocks and in the presence of steam and/or COas oxidizing agent to complete decarboxylation and to keep the metal oxide active sites from reducing and deactivating as well as other partial upgrading reactions. 168-. (canceled)69. A porous metallo-silicate composition (MSC) having a molar composition:{'br': None, 'sub': 2', '2, 'i': :m', ':n, 'SiOCeOXO'}wherein X is a divalent element selected from the group consisting of nickel, copper, zinc and combinations thereof; m is between about 0.001 and 0.5; n is between about 0.001 and 0.5; ...

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31-01-2019 дата публикации

Crystalline metallophosphates, their method of preparation, and use

Номер: US20190030511A1
Принадлежит: UOP LLC

A new family of crystalline microporous metallophosphates designated AlPO-78 has been synthesized. These metallophosphates are represented by the empirical formula R + r M m 2+ EP x Si y O z where R is an organoammonium cation, M is a framework metal alkaline earth or transition metal of valence +2, and E is a trivalent framework element such as aluminum or gallium. The AlPO-78 compositions are characterized by a new unique ABC-6 net structure, and have catalytic properties suitable for carrying out various hydrocarbon conversion processes, as well as characteristics suitable for the efficient adsorption of water vapor in a variety of applications, such as adsorption heat pumps.

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17-02-2022 дата публикации

Methods of Synthesizing and Recycling Metal-Organic Framework Systems

Номер: US20220048929A1
Принадлежит: ExxonMobil Research and Engineering Co

Provided herein are methods of novel methods of synthesizing a metal-organic framework system by vapor-phase appending of a plurality of ligands appended to a metal-organic framework. Also, provided are methods of recycling metal-organic framework systems by detaching the ligand and re-appending the same ligand or appending a different ligand to the metal-organic framework to provide a recycled or repurposed metal-organic framework system.

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31-01-2019 дата публикации

EMM-23 MATERIALS AND PROCESSES AND USES THEREOF

Номер: US20190031519A1
Принадлежит:

The disclosure is related to various modified EMM-23 materials, processes, and uses of the same. 1. A process of preparing a modified EMM-23 material comprising a composition of Formula II:{'br': None, 'sub': 2', '3', '2, 'XO:(m)YO\u2003\u2003(Formula II),'} {'br': None, 'sub': 2', '3', '2, 'XO:(t)YO\u2003\u2003(Formula III),'}, 'comprising combining a composition of Formula (III)with an agent comprising X to generate a material of Formula II;wherein m is less than 150, t is greater than or equal to 150, X is a trivalent element, and Y is a tetravalent element.2. The process of further comprises adjusting the pH of the combination of the composition of Formula III and the agent comprising X to within the range of 2.4 to 2.6.3. The process of claim 1 , wherein the agent comprises Al(NO) claim 1 , Al(SO) claim 1 , AlCl claim 1 , Fe(NO) claim 1 , or a mixture thereof.4. The process of further comprises combining additional amount of the agent comprising X to the pH adjusted combination of the composition of Formula III claim 1 , and adjusting the pH of the combination having additional amount of the agent comprising X to within the range of 2.4 to 2.6.5. The process of claim 4 , wherein the process of combining additional amount of the agent comprising X and adjusting the pH of the combination to within the range of 2.4 to 2.6 is repeated until the pH does not change when additional amount of the agent comprising X is added.6. The process of claim 4 , wherein the adjusting of the pH comprises adding a base or an acid to the combination of the composition of Formula III and the agent comprising X.7. The process of claim 6 , wherein the adjusting of the pH comprises adding a base.8. The process of claim 7 , wherein the base comprises an organic amine base.9. The process of claim 7 , wherein the base comprises ammonium hydroxide.10. The process of further comprises heating the pH adjusted combination of the composition of Formula III and the agent comprising X at a ...

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31-01-2019 дата публикации

Crystalline metallophosphates, their method of preparation, and use

Номер: US20190031520A1
Принадлежит: UOP LLC

A new family of crystalline microporous metallophosphates designated AlPO-77 has been synthesized. These metallophosphates are represented by the empirical formula H x M m 2+ EP x Si y O z where M is a framework metal alkaline earth or transition metal of valence +2, and E is a trivalent framework element such as aluminum or gallium. The AlPO-77 compositions are characterized by a new unique ABC-6 net structure, and have catalytic properties suitable for carrying out various hydrocarbon conversion processes, as well as characteristics suitable for adsorption applications.

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04-02-2021 дата публикации

FUNCTIONALISED BIMODAL PERIODIC MESOPOROUS ORGANOSILICATES (PMOS) AND METHOD FOR PRODUCING SAME USING PSEUDOMORPHIC TRANSFORMATION

Номер: US20210032157A1

The invention relates to a method for producing functionalised bimodal periodic mesoporous organosilicates (PMOs) by means of pseudomorphic transformation, to functionalised bimodal periodic mesoporous organosilicates (PMOs) that comprise at least one organosilicate and at least one functional component, and to the use of the PMO as a filter material, adsorption means, sensor material or carrier material for pharmaceutical products, insecticides or pesticides. 1. A method for producing functionalised bimodal periodic mesoporous organosilicates (PMOs) by means of pseudomorphic transformation , comprising the following steps:a) providing a monomodal mesoporous or macroporous glass,b) adding at least one multiply silylated organosilane and a solvent,c) drying and cross-linking the at least one multiply silylated organosilane on the surface of the monomodal mesoporous or macroporous glass,d) adding at least one structure-directing agent and pseudomorphic transformation,e) extracting the structure-directing agent,wherein at least one functional component is added after step a) and/or after step e), wherein the macroscopic shape of the mesoporous or macroporous glass remains unchanged during steps b) to e).2. The method according to claim 1 , wherein the at least one functional component is selected from a functional group claim 1 , a dye claim 1 , an enzyme claim 1 , a protein claim 1 , an antibody claim 1 , a nucleic acid claim 1 , a virus or a noble metal cluster.3. The method according to claim 1 , wherein at least one functional group is added after step a) or after step e) claim 1 , and the functional group is covalently bonded with at least one other functional component.4. The method according to claim 1 , wherein the structure-directing agent is selected from ionic surfactants or non-ionic surfactants.5. The method according to claim 1 , wherein endcapping is carried out after steps a) to e).6. Functionalised bimodal periodic mesoporous organosilicates (PMOs) ...

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09-02-2017 дата публикации

General method to incorporate metal nanoparticles in zeolites and zeotypes

Номер: US20170036197A1
Принадлежит: Danmarks Tekniskie Universitet

Disclosed herein is a method for producing a zeolite, zeolite-like or zeotype structure with selective formation of metal, metal oxide or metal sulphide nanoparticles and/or clusters inside the zeolite, zeolite-like or zeotype structure.

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30-01-2020 дата публикации

SOUND ABSORBING MATERIAL AND SPEAKER BOX USING SAME

Номер: US20200037063A1
Принадлежит:

The present disclosure provides a sound absorbing material. The sound absorbing material comprises MFI-structural-type zeolite. The MFI-structural-type zeolite comprises a framework, and the framework comprises SiOand AlO, and the mass ratio of Si to Al in the framework is less than 200 and not less than 50. The present disclosure also provides a speaker box applying the sound absorbing material. The sound absorbing material provided by the present disclosure and the speaker box using the sound absorbing material can further improve the performance of the speaker box, reduce the failure of zeolite and improve the performance stability of the speaker box. 1. A sound absorbing material , comprising: MFI-structural-type zeolite which comprises a framework , the framework comprises SiOand AlO , and a mass ratio of Si to Al in the framework of the MFI-structural-type zeolite is less than 200 and not less than 50.2. The sound absorbing material as described in claim 1 , wherein the mass ratio of Si to Al in the framework of the MFI-structural-type zeolite is less than 200 and not less than 80.3. The sound absorbing material as described in claim 2 , wherein the mass ratio of Si to Al in the framework of the MFI-structural-type zeolite is less than 200 and not less than 120.4. The sound absorbing material as described in claim 3 , wherein the mass ratio of Si to Al in the framework of the MFI-structural-type zeolite is less than 200 and not less than 140.5. The sound absorbing material as described in claim 1 , wherein the framework further comprises a trivalent and/or tetravalent metal ion oxide more than AlO.6. The sound absorbing material as described in claim 5 , wherein the framework further comprises at least one Oxide of B claim 5 , Fe claim 5 , Ga claim 5 , Cr claim 5 , Ti claim 5 , Zr claim 5 , and Ge.7. The sound absorbing material as described in claim 1 , wherein the particle size of MFI structure zeolite is between 10 nm and 10 μm.8. The sound absorbing ...

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24-02-2022 дата публикации

METAL-ORGANIC FRAMEWORKS FOR GAS ADSORPTION

Номер: US20220056064A1
Принадлежит:

Disclosed are metal organic frameworks (MOFs) for adsorbing guest species, methods for the separation of gases using the MOFs, and systems comprising the MOFs. The MOFs comprise a plurality of secondary building units (SBUs), each SBU comprising a repeating unit of one metal cation connected to another metal cation via a first moiety of an organic linker; a layer of connected adjacent SBUs in which a second moiety of the linker in a first SBU is connected to a metal cation of an adjacent SBU, and wherein adjacent layers are connected to each other via linker-to-linker bonding interactions 1. A method for the separation of a first species from a mixture , comprising contacting the mixture with a sorbent comprising a metal organic framework (MOF) , wherein the MOF comprises:a plurality of secondary building units (SBUs), each SBU comprising a repeating unit of one metal cation connected to another metal cation via a first moiety of an organic linker;a layer of connected adjacent SBUs in which a second moiety of the linker in a first SBU is connected to a metal cation of an adjacent SBU, andwherein adjacent layers are connected to each other via linker-to-linker bonding interactions;and wherein the first species is selected from carbon dioxide, carbon disulfide, nitrous oxide, water, hydrogen sulfide, hydrogen cyanide, functionalised C1-3 hydrocarbons, and a combination thereof.4. The method of any one of the preceding claims , wherein the SBU has a formula of [ML] , wherein M is the metal cation ,L is the organic linker and n is an integer greater than 0.5. The method of any one of the preceding claims , wherein the metal is selected from Li , Na , K , Rb , Cs , Be , Mg , Ca , Sr , Ba , Sc , Sc , Sc , Y , Y , Y , Ti , Ti , Ti , Zr , Zr , Zr , Hf , Hf , V , V , V , V , Nb , Nb , Nb , Nb , Ta , Ta , Ta , Ta , Cr , Cr , Cr , Cr , Cr , Cr , Cr , Mo , Mo , Mo , Mo , Mo , Mo , Mo , W , W , W , W , W , W , W , Mn , Mn , Mn , Mn , Mn , Mn , Mn , Re , Re , Re , Re , Re , Re , ...

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15-02-2018 дата публикации

METALLO-SILICATE CATALYST (MSC) COMPOSITIONS, METHODS OF PREPARATION AND METHODS OF USE IN PARTIAL UPGRADING OF HYDROCARBON FEEDSTOCKS

Номер: US20180043341A1
Принадлежит:

The invention relates to the preparation of novel bi- or tri metallic silicate micro-porous and/or meso-porous materials based on cerium, nickel, copper and/or zinc on a porous silicate framework matrix to use its molecular sieve effect to target preferentially the acidic organic molecules present in hydrocarbon feedstocks like crude oil, bitumen, VGO and the like. The chosen metals are selected based on their ability to activate steam and transfer oxygen for completing the oxidation of carboxylic compounds or decarboxylating them. These composite materials can be prepared under hydrothermal synthesis conditions in order to produce suitable porous solids where the metals are well dispersed and preferentially distributed inside the channels of the silicate framework where they can interact only with the molecules that can go inside the channels. According to the invention, the metallo-silicate materials are prepared under hydrothermal synthesis conditions Modification of the physical-chemical properties of the porous silicate materials can be accomplished by partial replacement of the silicon atoms by cerium, nickel, copper and/or zinc atoms in the material by isomorphous substitutions of these elements in a synthesis gel or by post-synthesis modifications like ion-exchange or impregnation/deposition. The materials can be used as prepared catalysts for the steam catalytic reduction of the total acid number (TAN) in acidic crude oil feedstocks and in the presence of steam and/or COas oxidizing agent to complete decarboxylation and to keep the metal oxide active sites from reducing and deactivating as well as other partial upgrading reactions. 1. A method for partially upgrading a feedstock of produced hydrocarbons , the method comprising the step of:exposing the produced hydrocarbons to a micro-porous or meso-porous catalyst structure having an embedded catalytic phase, which partially upgrades the produced hydrocarbons under conditions to promote partial upgrading.2. ...

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03-03-2022 дата публикации

SOLIDOTHERMAL SYNTHESIS OF A BORON-CONTAINING ZEOLITE WITH AN MWW FRAMEWORK STRUCTURE

Номер: US20220064011A1
Принадлежит:

The present invention relates to a process for the production of a zeolitic material having an MWW framework structure comprising YOand BO, wherein Y stands for a tetravalent element, said process comprising

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14-02-2019 дата публикации

HIERARCHICAL ALUMINOPHOSPHATES AS CATALYSTS FOR THE BECKMANN REARRANGEMENT

Номер: US20190046963A1
Принадлежит:

Methods for producing lactams from oximes by performing a Beckmann rearrangement using a hierarchical porous aluminophosphate catalyst having interconnected microporous and mesoporous networks are provided. Exemplary catalysts include a plurality of weak Brønsted acid active sites, including silicon-containing aluminophosphates having the IZA framework code AFI, such as SAPO-5, CHA, such as SAPO-34, and FAU, such as SAPO-37. 1. A method of making a catalyst for a Beckmann rearrangement reaction , wherein the catalyst is a hierarchical porous catalyst with an aluminophosphate framework , a plurality of interconnected micropores , and a plurality of mesopores interconnected with the micropores , the method comprising:combining an organosilane surfactant, at least one structure directing agent, a metal precursor, a silicon source, phosphoric acid, and water to form a mixture;heating the mixture to form a solid; andcalcining the solid to form the catalyst.2. The method of claim 1 , wherein the organosilane surfactant includes:a carbon chain of 5 to 30 carbons; anda silicon-containing head group.3. The method of claim 2 , wherein the organosilane surfactant includes dimethyloctadecyl[3-(trimethoxysilyl)propyl]ammonium chloride.4. The method of claim 1 , wherein combining the organosilane surfactant claim 1 , the at least one structure directing agent claim 1 , the metal precursor claim 1 , the silicon source claim 1 , the phosphoric acid claim 1 , and the water to form the mixture includes:mixing the metal precursor and the phosphoric acid together with a portion of the water to form a homogeneous solution;adding the organosilane surfactant, the at least one structure directing agent and the remaining portion of the water to the homogeneous solution to form a thicker solution; andadding the silicon source to the thicker solution to form the mixture.5. The method of claim 4 , wherein the at least one structure directing agent includes triethylamine.6. The method of claim ...

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25-02-2021 дата публикации

PROCESS FOR PREPARING A ZEOLITIC MATERIAL COMPRISING TI AND HAVING FRAMEWORK TYPE CHA

Номер: US20210053041A1
Принадлежит: BASF SE

A process for preparing a zeolitic material comprising Ti, having framework type CHA and having a framework structure which comprises Si and O, said process comprising (i) preparing a pre-synthesis mixture comprising water, a CHA framework structure directing agent, and a zeolitic material comprising Ti, having framework type MFI and having a framework structure which comprises Si and O; (ii) removing water from the pre-synthesis mixture obtained from (i) by heating the pre-synthesis mixture to a temperature of less than 100° C. at a pressure of less than 1 bar (abs); (iii) hydrothermally crystallizing the zeolitic material comprising Ti, having framework type CHA and having a framework structure which comprises Si and O. 1. A process for preparing a zeolitic material comprising Ti , having framework type CHA and having a framework structure which comprises Si and O , said process comprising:{'sub': 2', '2', '2', '2', '2, '(i) preparing a pre-synthesis mixture comprising water, a CHA framework structure directing agent, and a zeolitic material comprising Ti, having framework type MFI and having a framework structure which comprises Si and O, wherein a molar ratio of the CHA framework structure directing agent relative to Si, comprised in the zeolitic material having framework type MFI and calculated as SiO, said molar ratio being defined as SDA:SiO, is at least 0.4:1, and wherein a molar ratio of water relative to Si, comprised in the zeolitic material having framework type MFI and calculated as SiO, said molar ratio being defined as HO:SiO, is at least 30:1;'}{'sub': 2', '2', '2, '(ii) removing water from the pre-synthesis mixture by heating the pre-synthesis mixture to a temperature of less than 100° C. at a pressure of less than 1 bar(abs) and keeping the temperature of the pre-synthesis mixture in this range and the pressure of the pre-synthesis mixture in this range, obtaining a synthesis mixture comprising water, the CHA framework structure directing agent, ...

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22-02-2018 дата публикации

Ion Sieve Material, and Methods of Preparing and Using the Same

Номер: US20180050918A1
Принадлежит:

The present invention relates to an ion sieve material, comprising, based on the weight of the ion sieve material, 15-55% by weight (wt %) of SiO, 5-50 wt % of an auxiliary material, and 15-48 wt % of at least one functional metal oxide, wherein the metal in the functional metal oxide is a monovalent and/or divalent metal. A method for preparing the ion sieve material and a method of using the same are further provided. 1. An ion sieve material , comprising , based on the weight of the ion sieve material , 15-55% by weight (wt %) of SiO , 5-50 wt % of an auxiliary material , and 15-48 wt % of at least one one functional metal oxide , wherein the metal in the functional metal oxide is a monovalent and/or divalent metal.2. The ion sieve material according to claim 1 , wherein the content of SiOis 30-50 wt % claim 1 , the auxiliary material forms a polar covalent bond and an ionic bond with SiO claim 1 , and the auxiliary material is at least one selected from the group consisting of phosphorous oxide claim 1 , boron oxide claim 1 , alumina claim 1 , zirconia claim 1 , chromium oxide claim 1 , iron oxide claim 1 , zinc oxide claim 1 , bismuth oxide claim 1 , cobalt oxide or titania.3. The ion sieve material according to claim 1 , wherein the content of the functional metal oxide is 18-36 wt % claim 1 , and the functional metal oxide is at least one monovalent metal oxide claim 1 , at least one divalent metal oxide or a mixture of at least one monovalent metal oxide and at least one divalent metal oxide.4. The ion sieve material according to claim 3 , wherein the monovalent metal oxide is derived from a raw material selected from a carbonate claim 3 , a silicate claim 3 , a fluoride claim 3 , a sulfate claim 3 , a nitrate claim 3 , a phosphate claim 3 , a hydroxide claim 3 , an oxide claim 3 , a chloride or a mixture thereof claim 3 , and the content of the monovalent metal oxide in the ion sieve material is 0-40 wt %.5. The ion sieve material according to claim 3 , ...

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28-02-2019 дата публикации

Small crystal zsm-5, its synthesis and use

Номер: US20190062171A1
Принадлежит: ExxonMobil Research and Engineering Co

A molecular sieve having the framework structure of ZSM-5 is described comprising crystals having an external surface area in excess of 100 m2/g (as determined by the t-plot method for nitrogen physisorption) and a unique X-ray diffraction pattern.

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07-03-2019 дата публикации

COMPOSITION FOR MODULATING CELL FATE

Номер: US20190071314A1
Принадлежит:

A composition includes porous silica particles to carry a cell fate modulating factor therein. A method for modulating cell fate includes treating various cells with the composition. The cell fate modulating factor is delivered to a stable target receptor, toxicity to subject cells for delivery may be reduced, a fate of the subject cells can be controlled through sustained release of at least 99 wt. % of the cell fate modulating factor. 1: A composition for modulating cell fate , comprising:porous silica particles which carry a cell fate modulating factor on a surface of the particle or inside pores of the particle, and have t of 20 or more, at which a ratio of absorbance in Mathematical Equation 1 below reaches 1/2, {'br': None, 'i': A', '/A, 'sub': t', '0, '[Mathematical Equation 1]'}, 'wherein the surface of the particle or the inside the pores of the particle has been chemically modified,'}{'sub': '0', 'wherein Ais an absorbance of the porous silica particles measured when 5 ml of suspension containing 1 mg/ml of porous silica particles is fed to a tubular permeable membrane having 50 kDa pores;'}15 ml of a solvent substantially the same as the suspension is placed outside the permeable membrane while contacting the same;the inside/outside of the permeable membrane are under horizontal agitation with 60 rpm at 37° C.; and{'sub': t', '0, 'Ais another absorbance of the porous silica particle measured t time after the measurement of A.'}2: The composition according to claim 1 , wherein the particle has a siloxane group on the surface of the particle or inside the pores of the particle.3: The composition according to claim 1 , wherein the cell fate modulating factor is a gene encoding: at least one selected from the group consisting of 3-isobutyl-1-methylxanthine claim 1 , CHIR claim 1 , KY02111 claim 1 , DZNep claim 1 , tranylcypromine claim 1 , LDN claim 1 , digoxin claim 1 , nicotinamide claim 1 , IWP2 claim 1 , IWP4 claim 1 , XAV939 claim 1 , TTNPB claim 1 , ...

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24-03-2022 дата публикации

Solid-State Synthesis Of Precursors Of Metal-Organic Frameworks

Номер: US20220089618A1
Принадлежит:

Metal-organic frameworks (MOFs) are highly porous entities comprising a multidentate ligand coordinated to multiple metal atoms, typically as a coordination polymer. MOFs are usually produced from a solvent in powder form under hydrothermal or solvothermal synthesis conditions. Alternately, powder-form precursors of MOFs may be formed by milling or mulling a substantially solid mixture of a metal salt and a multidentate organic ligand, optionally in the presence of a small amount of a solvent. The powder-form precursors may then undergo heating, typically in the absence of applied shear, to produce the corresponding MOF. Mulling may be differentiated from milling at least in that mulling applies to the substantially solid mixture at a non-constant pressure and milling applies a constant pressure while forming the powder-form precursor. In some cases, mulling may promote more effective formation of the powder-form precursor compared to milling. 1. A method comprising:providing a substantially solid mixture comprising a metal salt and a multidentate organic ligand; andmulling or milling the substantially solid mixture for a sufficient length of time to produce a powder-form precursor of a metal-organic framework, the powder-form precursor being substantially free of the metal-organic framework and comprising a reaction product of the metal salt and the multidentate organic ligand.2. The method of claim 1 , wherein the substantially solid mixture is milled and milling takes place at a constant pressure applied upon the substantially solid mixture by a mill.3. The method of claim 1 , wherein the substantially solid mixture is mulled and mulling takes place at a non-constant pressure applied upon the substantially solid mixture by a muller.4. The method of claim 1 , wherein the substantially solid mixture further comprises a solvent.5. The method of claim 4 , wherein an amount of the solvent in the substantially solid mixture is about 20 μL or above per gram of a ...

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05-03-2020 дата публикации

Extrudable composition comprising a titanium-containing zeolitic material having framework type mww

Номер: US20200070134A1
Принадлежит: BASF SE

A process for preparing an extrudable composition comprising a titanium-containing zeo-litic material having framework type MWW, the process comprising providing a titanium-containing zeolitic material having framework type MWW, having a water absorption ca-pacity of at least 11 weight-%, subjecting the titanium-containing zeolitic material having framework type MWW an acid treatment, optionally incorporating zinc in the acid-treated titanium-containing zeolitic material having framework type MWW; preparing a composi-tion comprising the titanium-containing zeolitic material having framework type MWW obtained from (ii) or (iii), a precursor of a silica binder, water, and a kneading agent, wherein the composition does not comprise a polyethylene oxide.

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05-03-2020 дата публикации

Methods for Synthesizing Mesoporous Zeolite ETS-10 Containing Metal Without a Templating Agent

Номер: US20200071174A1
Принадлежит: Petrochina Co Ltd

The invention provides a method for synthesizing a mesoporous zeolite ETS-10 containing a metal without a templating agent. The method according to the invention comprises the steps of: mixing a silicon source with a NaOH solution to obtain a mixed solution so that the content of Na 2 O in the mixed solution is 10.0% to 20.0% by weight; adding a KOH or KF solution so that the content of K 2 O is 10.0% to 25.0% by weight and stirring it well; adding a titanium source solution and stirring it well; adding a precursor compound containing metal Ni and/or Co and stirring it well; and subjecting it to a crystallization reaction to obtain the mesoporous zeolite ETS-10. The mesoporous zeolite ETS-10 obtained by the invention has a specific surface area of 320 to 420 m 2 /g, a mesoporous volume of 0.11 to 0.21 cm 3 /g, and thus can be used as a catalyst and a support thereof in synthesis industry for macromolecular fine chemicals.

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18-03-2021 дата публикации

METHOD FOR TRANSFORMING ARSENIC SULFIDE SLAG AND CURING AND STABILIZING RESULTING COMPOUND BY MEANS OF MICROENCAPSULATION

Номер: US20210078056A1

The present disclosure provides a method for transforming an arsenic sulfide slag and curing and stabilizing the resulting compound by means of microencapsulation, comprising the following steps: (1) preparing arsenic trioxide from the arsenic sulfide slag as a raw material; (2) preparing 4-hydroxy-3-nitrophenylarsonic acid from the arsenic trioxide as a raw material; (3) preparing an iron-manganese dinuclear cluster metal arsenate compound having a porous structure; (4) subjecting the iron-manganese dinuclear cluster metal arsenate compound having a porous structure to surface coating with silicon; (5) synthesizing an Fe(0)/Al-SBA-15 mesoporous composite stabilizer by a hydrothermal reaction; and (6) subjecting the silicon coated iron-manganese dinuclear cluster metal arsenate compound to curing and stabilizing treatment by means of microencapsulation. The present disclosure involves transforming the arsenic sulfide slag into 4-hydroxy-3-nitrophenylarsonic acid and finally into a metal arsenate compound having a porous structure, which has the characteristics of good stability and low toxicity in comparison to conventional arsenic compounds. Thus, the toxicity associated with arsenic compounds can be greatly reduced. 1. A method for transforming an arsenic sulfide slag and curing and stabilizing the resulting compound by means of microencapsulation , comprising the following steps:(1) preparing arsenic trioxide from the arsenic sulfide slag as a raw material;(2) preparing 4-hydroxy-3-nitrophenylarsonic acid from the arsenic trioxide as a raw material;(3) induce-preparing an iron-manganese dinuclear cluster metal arsenate compound having a porous structure by using the 4-hydroxy-3-nitrophenylarsonic acid through transformation and solvent evaporation;(4) subjecting the iron-manganese dinuclear cluster metal arsenate compound having a porous structure to surface coating with silicon;(5) synthesizing an Fe(0)/Al-SBA-15 mesoporous composite stabilizer by a hydrothermal ...

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12-06-2014 дата публикации

Selectivation of adsorbents for gas separation

Номер: US20140157984A1
Принадлежит: ExxonMobil Research and Engineering Co

Systems and methods are provided for improving separation of gas phase streams using an adsorbent, such as 8-member ring zeolite adsorbents or DDR type zeolite adsorbents. Suitable gas phase streams can include at least one hydrocarbon, such as methane or a hydrocarbon containing at least one saturated carbon-carbon bond, and at least one additional component, such as CO 2 or N 2 . The selectivity of the adsorbent is improved by selectivating the adsorbent with one or more barrier compounds. The presence of the barrier compounds is believed to alter the relative ability of potential adsorbates to enter into and/or move within the pores of the adsorbent.

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22-03-2018 дата публикации

Synthesis of ZSM-5

Номер: US20180078928A1
Автор: Burton Allen W.
Принадлежит:

A molecular sieve having the framework structure of ZSM-5 is produced using one or more of 1,4-bis(N-pentylpyrrolidinium)butane dications, 1,5-bis(N-pentylpyrrolidinium)pentane dications, and 1,6-bis(N-pentylpyrrolidinium)hexane dications as a structure directing agent. 19.-. (canceled)12. The molecular sieve of claim 11 , wherein X includes aluminum claim 11 , and Y includes silicon and/or germanium.14. (canceled) The present application claims priority to and the benefit of U.S. Provisional Application No. 61/740,917 filed on 21 Dec. 2012, which is hereby incorporated by reference in its entirety.This invention relates to the synthesis of ZSM-5, and to the use of the resultant ZSM-5 as an adsorbent and a catalyst for organic conversion reactions.Crystalline ZS M-5, and its conventional preparation using tetrapropylammonium cations as a structure directing agent, are taught by U.S. Pat. No. 3,702,886 and U.S. Pat. No. Re. 29,948, the entire disclosures of which are incorporated herein by reference. Conventional ZSM-5 has a distinctive X-ray diffraction pattern which distinguishes it from organic conversion reactions.In addition to tetrapropylammonium cations, a large number of other organic nitrogen compounds, including certain diquaternary ammonium compounds, have been shown to direct the synthesis of ZSM-5. For example, U.S. Pat. No. 4,585,638 discloses that the synthesis of ZSM-5 can be directed by the diquaternary cation (alkyl)N(CH)N(alkyl), where the alkyl group is propyl or butyl.According to the present invention, it has now been found that ZSM-5 can be synthesized using certain novel bis(N-pentylpyrrolidinium)-diquat-n cations, where n=4, 5 or 6, as a structure directing agent. The ZSM-5 can be made across a wide range of Si/Al ratios (infinity to 12) and, in some cases, it has been found that novel ultra-small forms of ZSM-5 can be produced.In one aspect, the invention resides in a process for producing a molecular sieve having the framework structure of ...

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05-05-2022 дата публикации

BODY COMPRISING A FUNCTIONAL LAYER INCLUDING METAL ORGANIC FRAMEWORKS AND METHOD OF MAKING THE BODY

Номер: US20220134308A1
Принадлежит:

A body can comprise a substrate and a functional layer overlying at least a portion of a surface of the substrate. The functional layer can comprise metal organic frameworks (MOFs) and a binder, the binder including an organic polymer, and an adhesion loss factor (ALF) of the functional layer to the substrate can be not greater than 7%.

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19-06-2014 дата публикации

Micropowder and molding containing a zeolitic material containing ti and zn

Номер: US20140171667A1
Принадлежит: BASF SE

The present invention relates to a micropowder, wherein the particles of the micropowder have a Dv10 value of at least 2 micrometer and the micropowder comprises mesopores which have an average pore diameter in the range of from 2 to 50 nm and comprise, based on the weight of the micropowder, at least 95 weight-% of a microporous aluminum-free zeolitic material of structure type MWW containing titanium and zinc.

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19-06-2014 дата публикации

Nano sapo-35 and method of making

Номер: US20140171713A1
Принадлежит: UOP LLC

A porous crystalline nano metallo-alumino-phosphate molecular sieve is described. The molecular sieve has a framework composition on an anhydrous and calcined basis expressed by an empirical formula (El x Al y P z )O 2 wherein El is silicon, magnesium, zinc, iron, cobalt, nickel, manganese, chromium, or combinations thereof, where x is the mole fraction of El and has a value from 0.001 to about 0.5, y is the mole fraction of Al and has a value of at least 0.01, z is the mole fraction of P has a value of at least 0.01, and x+y+z=1, where the molecular sieve is characterized as having a LEV framework and nano octahedral crystals with an average crystal size of less than 700 nm. Methods of making the molecular sieves, and methods of using the molecular sieves are also described.

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28-03-2019 дата публикации

HIGH CHARGE DENSITY METALLOALUMINOPHOSPHOSILICATE MOLECULAR SIEVES MeAPSO-82

Номер: US20190091672A1
Автор: Gregory J. Lewis
Принадлежит: UOP LLC

A new family of crystalline microporous metalloalumino(gallo)phosphosilicates designated MeAPSO-82 has been synthesized. These metalloalumino(gallo)phosphosilicates are represented by the empirical formula of: R p+ r A + m M 2+ w E x PSi y O z where A is an alkali metal such as potassium, R is an quaternary ammonium cation such as ethyltrimethylammonium, M is a divalent metal such as Zn and E is a trivalent framework element such as aluminum or gallium. This family of metalloalumino(gallo)phosphosilicate materials are stabilized by combinations of alkali and quaternary ammonium cations, enabling unique, high charge density compositions. The MeAPSO-82 family of materials have the CGS topology and have catalytic properties for carrying out various hydrocarbon conversion processes and separation properties for separating at least one component.

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12-05-2022 дата публикации

Functionalised bimodal periodic mesoporous organosilicates (pmos) and method for producing same using pseudomorphic transformation

Номер: US20220144692A1

The invention relates to a method for producing functionalised bimodal periodic mesoporous organosilicates (PMOs) by means of pseudomorphic transformation, to functionalised bimodal periodic mesoporous organosilicates (PMOs) that comprise at least one organosilicate and at least one functional component, and to the use of the PMO as a filter material, adsorption means, sensor material or carrier material for pharmaceutical products, insecticides or pesticides.

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28-03-2019 дата публикации

Inorganic porous frameworklayered double hydroxide coreshell materials

Номер: US20190092644A1
Принадлежит: SCG Chemicals PCL

Core @ layered double hydroxide shell materials of the invention have the formula: T p @{[M z+ (1−x) M′ x y+ (OH) 2 ] a+ (X n− ) a/n ·bH 2 O·c(AMO-solvent)} q wherein T is a solid, porous, inorganic oxide-containing framework material, M z+ is a metal cation of charge z or a mixture of two or more metal cations each independently having the charge z; M′ y+ is a metal cation of charge y or a mixture of two or more metal cations each independently having the charge y; z=1 or 2; y=3 or 4; 0<x<0.9; b is 0 to 10; c is 0.01 to 10; p>0; q>0; X n− is an anion; with n>0; a=z(1−x)+xy−2; and AMO-solvent is an organic solvent which is completely miscible with water. Also disclosed are the products obtained by calcining the core @ layered double hydroxide shell materials which calcination products are core @ mixed metal oxide materials having the formula T p @[{M z+ 1−x M′ y+ x O w ] p Ÿ] wherein T is a solid, porous, inorganic oxide-containing framework material, M z+ 1−x M′ y+ x O w is a mixed metal oxide, or mixture of mixed metal oxides, which may be crystalline or non-crystalline, wherein M z+ and M′ y+ are different charged metal cations; M z+ is a metal cation of charge z or a mixture of two or more metal cations each independently having the charge z; M′ y+ is a metal cation of charge y or a mixture of two or more metal cations each independently having the charge y; z is 1 or 2; y is 3 or 4; 0<x<0.9; w>0; p>0 and q>0; Ÿ is the residue of an X n− anion in which n>0.

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23-04-2015 дата публикации

Process for the direct synthesis of cu-sapo-34

Номер: US20150110711A1
Принадлежит: Haldor Topsoe AS

Process for the direct synthesis of Cu-SAPO-34 comprising at least the following steps: preparation of a mixture containing water, at least one silicon source, at least one Al source, at least one P source, at least one Cu source, at least one OSDA1 (where OSDA1 is any polyamine), and at least one OSDA2 (where OSDA2 is any organic molecule capable of directing the synthesis of the SAPO-34); and where the final synthesis mixture has the next molar composition: a Si:0.5 Al:b P:c Cu:d OSDA1:e OSDA2:f H20 wherein a is in the range from 0.01 to 0.3; wherein b is in the range from 0.2 to 0.49; wherein c is in the range from 0.001 to 0.6; wherein d is in the range from 0.001 to 0.6; wherein e is in the range from 0.001 to 2; wherein f is in the range from 1 to 200; hydrothermal treatment of the mixture at 80-200° C. until formation of the crystalline material, and recovery of the crystal-line material.

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30-04-2015 дата публикации

Full-Si Molecular Sieve and its Synthesis Process

Номер: US20150119569A1

The present invention relates to a full-Si molecular sieve, wherein the full-Si molecular sieve has a Q 4 /Q 3 of (10-90):1.

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13-05-2021 дата публикации

Benzalkonium-Embedded Mesostructured Silica Compositions and Uses of Same

Номер: US20210137855A1
Принадлежит: Rutgers State University of New Jersey

The present invention relates in one aspect to the discovery of novel mesoporous silica nanoparticles (MSNs) templated around and comprising benzalkonium chloride (BAC). In certain embodiments, the BAC-SiO2 mesoporous nanoparticles are capable of sustained release of BAC under acidic conditions, thereby acting as a long release antimicrobial agent. In other embodiments, the BAC-SiO2 mesoporous nanoparticles can be incorporated into a variety of consumer products as an antimicrobial agent additive, including for example, but not limited to, surgical dressings, bandages, deodorants, soaps, facial cleansers and industrial cleaners.

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10-05-2018 дата публикации

METHOD OF PREPARING MOLECULAR SIEVE SSZ-85

Номер: US20180127281A1
Автор: Zones Stacey Ian
Принадлежит:

A method is disclosed for preparing molecular sieve SSZ-85 in the absence of a source of fluoride ions. 1. A method of preparing molecular sieve SSZ-85 comprising contacting under crystallization conditions a reaction mixture comprising a source of cobalt , a source of aluminum , a source of phosphorus , and an ionic liquid comprising a 1 ,3-diisopropylimidazolium cation; wherein the reaction mixture is substantially free of fluoride ions.4. The method of claim 1 , wherein the crystallizations conditions include a temperature of from 100° C. to 135° C.5. A cobalt aluminophosphate molecular sieve having the structure of SSZ-85 and claim 1 , in its as-synthesized form claim 1 , being substantially free of fluoride ions.7. The molecular sieve of claim 6 , wherein 0.01≤x≤0.5; 0.25≤y≤0.7; and 0.25≤z≤0.7. This application claims the benefit of U.S. Provisional Application Ser. No. 62/419,571, filed on Nov. 9, 2016, the disclosure of which is incorporated by reference in its entirety.This disclosure is directed to a method of preparing molecular sieve SSZ-85 in the absence of a source of fluoride ions.Because of their unique sieving characteristics as well as their catalytic properties, crystalline molecular sieves and zeolites are especially useful in applications such as hydrocarbon conversion, gas drying and separation.Cobalt aluminophosphate molecular sieve SSZ-85 and its synthesis are disclosed in U.S. Pat. No. 9,359,217. However, the reaction mixtures described in U.S. Pat. No. 9,359,217 require the presence of fluoride ions, which in commercial operations is disadvantageous in that they may lead to extra safety and cost considerations.The present disclosure provides a method of preparing molecular sieve SSZ-85 in the absence of a source of fluoride ions.In one aspect, there is provided a method of preparing a molecular sieve SSZ-85, the method comprising contacting under crystallization conditions a reaction mixture comprising a source of cobalt; a source of ...

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11-05-2017 дата публикации

CRYSTALLINE MICROPOROUS MATERIAL MEDIATED CONVERSION OF C1-3 OXYGENATE COMPOUNDS TO C4 OXYGENATE COMPOUNDS

Номер: US20170129913A1
Принадлежит: Haldor Topsoe A/S

A process for the preparation of Coxygenate compounds such as threose, erythrose or erythrulose starting from a composition comprising Coxygenate compounds such as formaldehyde, glycolaldehyde, glyoxal, pyruvaldehyde or acetol, wherein the process is carried out in the presence of a crystalline microporous material having a ring pore structure selected from an eight-membered ring pore structure or a ten-membered ring pore structure. 1. A process for the preparation of one or more Coxygenate compounds from a composition comprising Coxygenate compounds , wherein the process is carried out in the presence of a crystalline microporous material comprising a ring pore structure selected from one or more of the group consisting of an eight-membered ring pore structure and a ten-membered ring pore structure.2. A process according to claim 1 , wherein the Coxygenate compounds are compounds selected from one or more of the group consisting of threose claim 1 , erythrose and erythrulose.3. A process according to claim 1 , wherein the composition comprising Coxygenate compounds comprises one or more compounds selected from the group consisting of formaldehyde claim 1 , glycolaldehyde claim 1 , glyoxal claim 1 , pyruvaldehyde and acetol.4. A process according to claim 1 , wherein the composition comprising Coxygenate compounds is obtainable from the pyrolysis of biomass or one or more oxygenate compounds selected from the group consisting of fructose claim 1 , glucose claim 1 , sucrose claim 1 , xylose or isomers thereof.5. A process according to claim 1 , wherein the composition comprising Coxygenate comprises a solvent selected from one or more of the groups consisting of water claim 1 , alcohol and a water and alcohol mixture.6. A process according to claim 1 , wherein the alcohol is selected from one or more of the group consisting of methanol and ethanol.7. A process according to claim 1 , wherein the crystalline microporous material comprising a small or medium pore ...

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24-05-2018 дата публикации

COLLOIDAL COMPOSITIONS AND METHODS OF PREPARING SAME

Номер: US20180141822A1
Принадлежит: ECOLAB USA INC.

Colloidal compositions and methods of preparing same are provided. The colloidal compositions include a silicate and a metal dispersed therein. The colloidal compositions can further include a stabilizer, such as a quaternary amine, to enhance the and dispersion of the metal loading within the silicate. The colloidal compositions can be made such that the metal is dispersed within the silicate in a controlled manner. 1. A method of producing a silica colloid , comprising:providing an alkaline solution having a stabilizing component,adding a silicic acid solution to the alkaline solution, andforming a colloid of silica particles, wherein the stabilizing component is dispersed throughout each silica particle.2. The method of claim 1 , wherein the alkaline solution comprises a cationic metal component.3. The method of claim 2 , wherein the metal component is dispersed within one or more of the silica particles.4. The method of claim 3 , wherein the stabilizing component and/or the metal component is dispersed in a homogenous manner.5. The method of claim 1 , wherein the stabilizer is a quaternary compound.6. The method of claim 5 , wherein the stabilizer is a quaternary amine.7. The method of claim 6 , wherein the quaternary amine is quaternary ammonium hydroxide.8. A method of preparing a metal-containing silica colloid claim 6 , comprising:reacting a silicic acid solution with a cationic metal component,forming a metal-silicate solution,adding the metal-silicate solution to an alkaline solution,forming a colloid of metal silicate particles.9. The method of claim 8 , further comprising forming a metal-silicate monomer by reacting the silicic acid solution with the metal component.10. The method of claim 9 , further comprising polymerizing the metal-silicate monomer.11. The method of claim 10 , further comprising forming a homogenous metal-silicate lattice microstructure throughout a solid phase of the colloid.12. The method of claim 8 , wherein the colloid is further ...

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16-06-2016 дата публикации

Organosilica materials and uses thereof

Номер: US20160168333A1
Принадлежит: ExxonMobil Research and Engineering Co

Methods of preparing organosilica materials, which are a polymer comprising of at least one independent cyclic polyurea monomer of Formula wherein each R 1 is a Z 1 OZ 2 Z 3 SiZ 4 group, wherein each Z 1 represents a hydrogen atom, a C 1 -C 4 alkyl group, or a bond to a silicon atom of another monomer unit; each Z 2 and Z 3 independently represent a hydroxyl group, a C 1 -C 4 alkyl group, a C 1 -C 4 alkoxy group or an oxygen atom bonded to a silicon atom of another monomer unit; and each Z 4 represents a C 1 -C 8 alkylene group bonded to a nitrogen atom of the cyclic polyurea are provided herein. Methods of preparing and processes of using the organosilica materials, e.g., for gas separation, color removal, etc., are also provided herein.

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30-05-2019 дата публикации

Method for producing separation membrane using mfi-type zeolite (silicalite)

Номер: US20190160437A1
Принадлежит: Hitachi Zosen Corp

Provided is a method for producing a separation membrane including a silicalite membrane without using NaOH or the like that causes an increase in cost with respect to equipment, facilities, and process time. The method for producing a separation membrane is a method for producing a separation membrane including a porous support and a silicalite membrane that is formed on the support and has an MFI-type zeolite crystal structure, and is characterized in that the method includes a step of producing a seed crystal, a step of attaching the seed crystal onto the porous support, a step of producing a membrane synthesis raw material composition containing SiO2, an organic template, and H2O, and a step of immersing the porous support having the seed crystal attached thereto in the membrane synthesis raw material composition and performing hydrothermal synthesis, and the composition ratio of the membrane synthesis raw material composition is as follows: SiO2:organic template:H2O=1:(0.05 to 0.15):(50 to 120).

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06-06-2019 дата публикации

Synthetic Zeolite Comprising A Catalytic Metal

Номер: US20190168197A1
Принадлежит: ExxonMobil Chemical Co

A small pore size synthetic zeolite having a degree of crystallinity of at least 80% and comprising at least 0.01 wt % based on the weight of the zeolite of at least one catalytic metal selected from the group consisting of Ru, Rh, Pd, Ag, Os, Ir, Pt, Au, Mo, W, Re, Co, Ni, Zn, Cr, Mn, Ce, Ga and combinations thereof, wherein at least 80% of the catalytic metal is encapsulated in the zeolite, wherein if the zeolite is an aluminosilicate it has a SiO 2 :Al 2 O 3 molar ratio of greater than 6:1.

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06-06-2019 дата публикации

METHOD FOR SYNTHESIZING NANO SAPO-34 MOLECULAR SIEVE, AND SAPO-34 MOLECULAR SIEVE CATALYST AND APPLICATION THEREOF

Номер: US20190169035A1

A method for synthesizing a nano SAPO-34 molecular sieve, and an SAPO-34 molecular sieve catalyst and application thereof. A nano SAPO-34 molecular sieve is synthesized by adding a microporous templating agent and a templating agent having a functionalized organic silane to hydrothermal synthesis. The nano SAPO-34 molecular sieve is calcined to obtain a nano SAPO-34 molecular sieve catalyst. The catalyst can be used in a reaction for preparing low-carbon olefin from an oxygen-containing compound. The nano SAPO-34 molecular sieve obtained by this method has a pure CHA crystal phase. Moreover, the nano SAPO-34 molecular sieve catalyst obtained by this method has good catalytic performance in a MTO reaction, the service life of the catalyst is significantly prolonged, and the selectivity of the low-carbon olefin is improved. 110-. (canceled)12. The method according to claim 11 , wherein in the Formula I claim 11 , n is an integer ranging from 3 to 8; Rand Rare each independently selected from Calkyl group; Ris selected from piperazinyl claim 11 , pyridyl or morpholinyl group.13. The method according to claim 11 , wherein the method comprises the following steps:a) dissolving the functionalized organosilane in water, and then adding sequentially an aluminum source, a phosphorus source, an organic amine and an additional silicon source to obtain a mixture with the following molar ratio:{'sub': 2', '2', '5', '2', '3', '2, 'SiO:PO:AlO:organic amine:HO=0.2˜1.2:0.5˜1.5:0.6˜1.4:1.5˜5.5:50˜200;'}b) crystallizing the mixture obtained from step a) for a crystallization time in a range from 0.4 to 10 days at a crystallization temperature in a range from 150 to 220° C.;c) after the crystallization of step b), separating the solid product, and washing and drying it to obtain the nano SAPO-34 molecular sieve.14. The method according to claim 13 , wherein the molar ratio of the functionalized organosilane to the additional silicon source in the mixture obtained from step a) is 1˜55: ...

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02-07-2015 дата публикации

Synthesis of zsm-58 crystals with improved diffusivity for use in gas separations

Номер: US20150182947A1
Принадлежит: ExxonMobil Research and Engineering Co

Methods are provided for synthesizing ZSM-58 crystals with an improved morphology and/or an improved size distribution. By controlling the conditions during synthesis of the ZSM-58 crystals, crystals of a useful size with a narrow size distribution can be generated. Additionally, by controlling the ratio of water content to silica content in the synthesis mixture, it has unexpectedly been found that ZSM-58 crystals can be formed with an improved morphology. The improved morphology can result in ZSM-58 crystals with a more uniform size across the various dimensions of the crystal, which allows for more uniform diffusion within the crystal. This is in contrast to conventionally synthesized crystals, where the size of the crystal can vary along different axes of the crystals.

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28-06-2018 дата публикации

Hydrogel Derived Carbon For Energy Storage Devices

Номер: US20180182564A1
Автор: David Mitlin, Jia DING
Принадлежит: David Mitlin, Jia DING

An energy storage device, such as a sodium ion capacitor, including an anode and a cathode, at least one of the anode and the cathode including a nitrogen and oxygen functionalized carbon (NOFC). The NOFC has a nitrogen content greater than 4 wt %, such as 13 wt %, an oxygen content greater than 8 wt %, such as 11 wt %, and a surface area greater than 800 m 2 g −1 , such as 945 m 2 g −1 . The energy storage device has favorable reversible and rate capability, such as 437 mAhg −1 at 100 mAg −1 , and 185 mAhg −1 at 1600 mA g −1 .

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20-06-2019 дата публикации

Production of zeolite-based composite materials with hierarchichal porosity

Номер: US20190185330A1

A method is provided for generating a composite material with a support structure and a coating on the surface of the support structure, the coating comprising, as active component, crystals of a zeolite material or of a zeolite-like material, with intercrystalline mesopores and/or macropores being formed in the coating, characterized in that the method comprises the following steps: a) providing a suspension which comprises nanoscale starting crystals of a zeolite material or of a zeolite-like material, and also precursor compounds of the zeolite material or zeolite-like material, b) applying the suspension provided in step a) to the surface of the support structure, c) compacting the suspension applied in step b) by at least partially removing the solvent that forms the liquid phase of the suspension, to yield a coating which comprises the starting crystals and the precursor compounds, d) keeping the coating obtained in step c) on the surface of the support structure in a vapor-containing atmosphere at an elevated temperature, so that the precursor compounds present are converted into a zeolite material or a zeolite-like material and, together with the starting crystals, form the coating which comprises crystals of a zeolite material or of a zeolite-like material.

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22-07-2021 дата публикации

ZEOLITE SEPARATION MEMBRANE AND PRODUCTION METHOD THEREFOR

Номер: US20210220779A1
Принадлежит:

Provided are an all-silica zeolite separation membrane for separating carbon dioxide, etc., and not causing a decrease in the processing amount due to adsorption of water molecules, and a production method therefor. One aspect of the present invention is a zeolite separation membrane, in which the framework of a zeolite crystal structure formed on a porous support is all silica, characterized in that the zeolite crystal structure formed on the porous support is fluorine free. Another aspect of the present invention is a method for producing a zeolite separation membrane having a zeolite crystal structure on a porous support, characterized in that the method includes a step of producing a seed crystal, a step of applying the seed crystal onto the porous support, a step of producing a membrane synthesis raw material composition, and a step of immersing the porous support having the seed crystal applied thereon in the membrane synthesis raw material composition and performing hydrothermal synthesis, and the membrane synthesis raw material composition contains a silica source and an organic template and does not contain a fluorine compound. 1. A method for producing a zeolite separation membrane having an all-silica CHA-type zeolite crystal structure on a porous support , characterized in that the method comprises:a step of producing a seed crystal of all-silica CHA-type zeolite;a step of applying the seed crystal onto the porous support;a step of producing a membrane synthesis raw material composition; anda step of immersing the porous support having the seed crystal applied thereon in the membrane synthesis raw material composition, and performing hydrothermal synthesis;wherein the membrane synthesis raw material composition contains a silica source and an organic template and does not contain a fluorine compound.2. The method for producing a zeolite separation membrane according to claim 1 , characterized in that the membrane synthesis raw material composition is ...

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12-07-2018 дата публикации

SYNTHESIS OF ZEOLITE SSZ-31

Номер: US20180194638A1
Автор: Xie Dan
Принадлежит:

A method is provided for synthesizing zeolite SSZ-31 using 2-ethyl-N,N,N-trimethylbutan-1-aminium cations as a structure directing agent. 1. A method of synthesizing a zeolite having the structure of SSZ-31 , the method comprising: (1) a source of silicon oxide;', '(2) optionally, a source of aluminum oxide;', '(3) a structure directing agent (Q) comprising 2-ethyl-N,N,N-trimethylbutan-1-aminium cations;', '(4) hydroxide ions; and', '(5) water; and, '(a) preparing a reaction mixture comprising(b) subjecting the reaction mixture to crystallization conditions sufficient to form crystals of the zeolite.4. The method of claim 1 , wherein the crystallization conditions include a temperature of from 125° C. to 200° C.5. A zeolite having the structure of SSZ-31 and comprising 2-ethyl-N claim 1 ,N claim 1 ,N-trimethylbutan-1-aminium cations in its pores. This application claims priority to U.S. Provisional Application Ser. No. 62/444,909, filed on Jan. 11, 2017, the disclosure of which is fully incorporated herein by reference.This disclosure relates to a method of synthesizing zeolite SSZ-31.Molecular sieve materials, both natural and synthetic, have been demonstrated in the past to be useful as adsorbents and to have catalytic properties for various types of hydrocarbon conversion reactions. Certain molecular sieves, such as zeolites, aluminosphosphates, and mesoporous materials, are ordered, porous crystalline materials having a definite crystalline structure as determined by X-ray diffraction (XRD). Within the crystalline molecular sieve material there are a large number of cavities which may be interconnected by a number of channels or pores. These cavities and pores are uniform in size within a specific molecular sieve material. Because the dimensions of these pores are such as to accept for adsorption molecules of certain dimensions while rejecting those of larger dimensions, these materials have come to be known as “molecular sieves” and are utilized in a variety of ...

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18-06-2020 дата публикации

MOLECULAR SIEVE SCM-15, SYNTHESIS METHOD THEREFOR AND USE THEREOF

Номер: US20200188891A1
Принадлежит:

The invention relates to a molecular sieve SCM-15, a preparation process and use thereof. The molecular sieve comprises a schematic chemical composition of a formula of “SiO.GeO”, wherein the molar ratio of silicon and germanium satisfies SiO/GeO≥1. The molecular sieve has unique XRD diffraction data and can be used as an adsorbent or a catalyst. 3. The molecular sieve SCM-15 according to claim 1 , characterized in that the molecular sieve has a schematic chemical composition of formula “SiO.GeO” claim 1 , wherein the molar ratio of silicon to germanium satisfies SiO/GeO≥1 claim 1 , preferably 1≤SiO/GeO≤15 claim 1 , more preferably 2≤SiO/GeO≤10 claim 1 , or more preferably 2.5≤SiO/GeO≤5.4. The molecular sieve SCM-15 according to claim 3 , characterized in that not more than 10% of the Ge atoms in the molecular sieve are substituted by atoms of at least one element other than silicon and germanium.5. The molecular sieve SCM-15 according to claim 4 , characterized in that the element other than silicon and germanium is at least one selected from the group consisting of boron claim 4 , aluminum claim 4 , tin claim 4 , zirconium and titanium.7. The process of preparing molecular sieve SCM-15 according to claim 6 , characterized in that the silicon source is at least one selected from the group consisting of silicic acid claim 6 , silica gel claim 6 , silica sol claim 6 , tetraalkyl orthosilicate and water glass; the germanium source is at least one selected from the group consisting of germanium oxide claim 6 , germanium nitrate and tetraalkoxygermanium;{'sub': 2', '2, 'and the molar ratio of the silicon source (calculated by SiO), the germanium source (calculated by GeO), the fluorine source (calculated by F), the organic template agent and water is 1:(0-1):(0.1-2.0): (0.1-2.0):(3-30); preferably 1:( 1/15-1.5):(0.2-1.5):(0.2-1.5):(4-25); more preferably 1:(0.1-0.5):(0.4-1.2):(0.4-1.2):(5-20); more preferably 1:(0.2-0.4):(0.6-1.0):(0.6-1.0):(5-15).'}8. The process of ...

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18-06-2020 дата публикации

MOLECULAR SIEVE SCM-14, A PREPARATION PROCESS AND USE THEREOF

Номер: US20200188892A1
Принадлежит:

The invention relates to a molecular sieve SCM-14, a preparation process and use thereof. The molecular sieve has a schematic chemical composition of a formula of “SiO.1/nGeO” or a formula of “kF.mQ.SiO.1/nGeO.pHO”, wherein the molar ratio of silicon to germanium, n, satisfies n≤30, and other values and symbols are defined in the specification. The molecular sieve has unique XRD diffraction data and can be used as an adsorbent or a catalyst. 3. The molecular sieve SCM-14 according to claim 1 , characterized in that the molecular sieve in the calcined form has a schematic chemical composition of formula “SiO.1/nGeO” claim 1 , wherein the molar ratio of silicon to germanium claim 1 , n claim 1 , satisfies n≤30 claim 1 , preferably 0.5≤n≤20 claim 1 , more preferably 1≤n≤10 claim 1 , or more preferably 1≤n≤5.5. The molecular sieve SCM-14 according to claim 1 , characterized in that not more than 10% of the Ge atoms in the molecular sieve are replaced by atoms of at least one element other than silicon and germanium.6. The molecular sieve SCM-14 according to claim 5 , characterized in that the element other than silicon and germanium is at least one selected from the group consisting of boron claim 5 , aluminum claim 5 , tin claim 5 , zirconium and titanium claim 5 , preferably at least one selected from the group consisting of boron and titanium.8. The process of preparing molecular sieve SCM-14 according to claim 7 , characterized in that the silicon source is at least one selected from the group consisting of silicic acid claim 7 , silica gel claim 7 , silica sol claim 7 , tetraalkyl orthosilicate and water glass; the germanium source is at least one selected from the group consisting of germanium oxide claim 7 , germanium nitrate and tetraalkoxygermanium;{'sub': 2', '2, 'the molar ratio of the silicon source (calculated as SiO), the germanium source (calculated as GeO), the fluorine source (calculated as F), the organic template agent and water is 1:(1/30 to ∞):(0.1 ...

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12-08-2021 дата публикации

NANOREACTORS FOR THE SYNTHESIS OF POROUS CRYSTALLINE MATERIALS

Номер: US20210246148A1
Принадлежит:

The present invention relates to the field porous crystalline materials, more particularly to metal organic frameworks (MOFs) and covalent organic frameworks (COFs). According to this invention, micelles are used as nanoreactors for the synthesis and stabilisation of porous crystalline materials in aqueous dispersions. Disclosed are dispersions comprising such porous crystalline materials, the synthesis and use of such dispersions. Further disclosed are novel porous crystalline materials, the synthesis and use of such crystalline materials. Further disclosed are novel inks comprising the dispersions and non-solvent, the synthesis and use of such inks for direct printing, 2D printing and 3D printing. 2. The dispersion of characterized in thatsaid dispersion having a micellar size between 15-200 nm; and/orsaid continuous phase comprises at least 90 wt % water; and/orsaid surfactants are selected from the group consisting of cationic surfactants, anionic surfactants and non-ionic surfactants; and/orsaid additives, if present, are selected from the group consisting of pH modifiers, ionic strength modifiers, viscosity modifiers, and catalysts; and/orsaid micelles are monodisperse in size; wherein monodisperse relates to the micelles having a narrow size distribution with a polydispersity index (PDI) between 0.05 and 0.5 determined according to dynamic light scattering (DLS) measurements; and/or 0.01-4 wt % of PCMs,', 'about 80-99 wt % of water,', 'about 0.01-4 wt % of surfactant,', 'about 0.01-4 wt % of co-surfactant; and', 'about 0.001-10 wt % of additive., 'wherein the colloidal dispersion comprises'}3. The colloidal dispersion according to ; wherein the surfactants are a combination of cetyl trimethylammonium bromide (CTAB) and sodium dodecyl sulfate (SDS).4. The colloidal dispersion according to ; wherein the porous crystalline materials (PCMs) are covalent organic frameworks (COFs).5. The colloidal dispersion according to ; wherein the metal organic frameworks (MOFs ...

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20-08-2015 дата публикации

SAPO-34 molecular sieve and method for preparing the same

Номер: US20150231616A1

A SAPO-34 molecular sieve and method for preparing the same, whose chemical composition in the anhydrous state is expressed as: mSDA.(Si x Al y P z )O 2 , wherein m is 0.08-0.3, x is 0.01-0.60, y is 0.2-0.60, z is 0.2-0.60, and x+y+z=1. The template agent SDA is in micropores of the molecular sieve. SDA is an organic amine with the structural formula (CH 3 ) 2 NRN(CH 3 ) 2 , wherein R is a saturated straight-chain or branched-chain alkylene group with having from 2-5 carbon atoms. There is a slight Si enrichment phenomenon on the crystal surface of the molecular sieve crystal, and the ratio of the surface Si content to the bulk Si content of the crystal ranges from 1.50-1.01. Said SAPO-34 molecular sieve, after being calcined at a temperature range from 400-700° C. in air, can be used as a gas adsorbent and catalyst for an acid-catalyzed reaction or oxygenate to olefin reaction.

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11-08-2016 дата публикации

Organosilica materials and uses thereof

Номер: US20160229959A1
Принадлежит: ExxonMobil Research and Engineering Co

Organosilica materials, which are a polymer of at least one independent monomer of Formula [Z 1 OZ 2 OSiCH 2 ] 3 (I), wherein each Z 1 and Z 2 independently represent a hydrogen atom, a C 1 -C 4 alkyl group or a bond to a silicon atom of another monomer and at least one other trivalent metal oxide monomer are provided herein. Methods of preparing and processes of using the organosilica materials, e.g., for catalysis etc., are also provided herein.

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09-08-2018 дата публикации

HIGHLY AMINATED SELF-ASSEMBLING FUNCTIONALIZED MESOPOROUS SILICA NANOPARTICLES AND METHOD OF SYNTHESIS

Номер: US20180222754A1
Принадлежит:

A method for self-assembling a mesoporous silica nanoparticle. The method comprises the step of condensing a silica precursor, a surfactant and a condensation agent in a solvent. Then, the addition of an organotriethoxysilane is performed. Finally, there is the step of removing the surfactant. The method is remarkable in that the portion of the organotriethoxysilane to the silica precursor is comprised between 5% and 15%. Additionally, a self-assembled mesoporous silica nanoparticle comprising at least one silica precursor and an organotriethoxysilane. 122-. (canceled)24. The method according to claim 23 , wherein the portion is 10%.25. The method according to claim 23 , wherein one of the silica precursor is tetraethyl orthosilicate claim 23 , the surfactant is cetyltrimethylammonium chloride claim 23 , the condensation agent is triethanolamine and the organotriethoxysilane is (3-aminoproplyl)triethoxysilane.26. The method according to claim 23 , whererin the number of equivalents of the condensation agent relative to one equivalent of the silica precursor is comprised between 1.6 and 2.4.27. The method according to claim 23 , wherein the number of equivalents of the condensation agent relative to one equivalent of the silica precursor is 2.0.28. The method according to claim 23 , wherein the number of equivalents of the surfactant relative to one equivalent of the silica precursor is comprised between 0.22 and 0.30.29. The method according to claim 23 , wherein the number of equivalents of the surfactant relative to one equivalent of the silica precursor is 0.26.30. The method according to claim 23 , wherein the organotriethoxysilane is added between 10 minutes and 30 minutes.31. The method according to claims 23 , wherein the step of removing the surfactant is a combination of a dialysis process and an extraction in hydrochloric acid.32. The method according to claim 31 , wherein the dialysis process is repeated five times.33. The method according to claim 23 , ...

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10-08-2017 дата публикации

SOLIDOTHERMAL SYNTHESIS OF ZEOLITIC MATERIALS AND ZEOLITES OBTAINED THEREFROM

Номер: US20170225959A1
Принадлежит: BASF SE

The present invention relates to a process for the preparation of a zeolitic material comprising YOin its framework structure, wherein Y stands for a tetravalent element, wherein said process comprises the steps of: 114.-. (canceled)15. A process for the preparation of a zeolitic material comprising YOin its framework structure , wherein Y is a tetravalent element , wherein said process comprises the steps of:{'sub': '2', '(1) providing a mixture comprising one or more sources for YO, one or more fluoride containing compounds, and one or more structure directing agents;'}{'sub': '2', '(2) crystallizing the mixture obtained in step (1) for obtaining a zeolitic material comprising YOin its framework structure;'}{'sub': 2', '2, 'wherein the mixture provided in step (1) and crystallized in step (2) contains 35 wt.-% or less of HO based on 100 wt.-% of YOcontained in the mixture provided in step (1) and crystallized in step (2).'}16. The process of claim 15 , wherein Y is selected from the group consisting of Si claim 15 , Sn claim 15 , Ti claim 15 , Zr claim 15 , Ge claim 15 , and mixtures thereof.17. The process of claim 15 , wherein the one or more fluoride containing compounds comprise one or more fluoride salts and/or hydrogen fluoride.18. The process of claim 15 , wherein the one or more structure directing agents provided in step (1) comprise one or more organic compounds.19. The process of claim 15 , wherein the molar ratio of the one or more structure directing agents: YOin the mixture provided in step (1) and crystallized in step (2) ranges from 0.01:1 to 2:1.20. The process of claim 15 , wherein the molar ratio of fluoride: YOin the mixture provided in step (1) and crystallized in step (2) is in the range of from 0.01:1 to 5:1.21. The process of claim 15 , wherein seed crystals are further provided in step (1).22. The process of claim 15 , wherein one or more sources of XOare further provided in step (1) claim 15 , wherein X is a trivalent element.23. The ...

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18-07-2019 дата публикации

GERMANIUM-68 SOURCE MATERIAL AND CALIBRATION DEVICES THAT INCLUDE SUCH SOURCE MATERIAL

Номер: US20190218105A1
Принадлежит:

Calibration devices including germanium-68 source material are disclosed. The source material may be a matrix material (e.g., zeolite) in which germanium-68 is isomorphously substituted for central atoms in tetrahedra within the matrix material. Methods for preparing such calibration devices are also disclosed. 1. A solid-state germanium-68 source material comprising: [{'sub': '4', 'a first tetrahedra comprising a central atom, T, and oxygen, the central atom being selected from the group consisting of silicon, aluminum, zirconium and stable germanium, the first tetrahedra having a formula TO; and'}, {'sup': '68', 'sub': '4', 'a second tetrahedra, the second tetrahedra being a germanium-68 tetrahedra comprising germanium-68 and oxygen and having a formula GeO, the first tetrahedra and germanium-68 tetrahedra being part of a three-dimensional polyhedral crystal structure.'}], 'a matrix material having a three-dimensional polyhedral crystal structure, the matrix material comprising2. The solid-state germanium-68 source material as set forth in wherein the first tetrahedra is a silicon tetrahedra having a formula SiO claim 1 , germanium-68 being isomorphously substituted for silicon as the central atom of a plurality of tetrahedra in the matrix material.3. The solid-state germanium-68 source material as set forth in wherein the matrix material further comprises a third tetrahedra claim 1 , the third tetrahedra comprising a central atom selected from the group consisting of silicon claim 1 , aluminum claim 1 , zirconium and stable germanium.4. The solid-state germanium-68 source material as set forth in wherein the third tetrahedra is an aluminum tetrahedra claim 3 , the aluminum tetrahedra comprising aluminum and oxygen and having a formula AlO.5. The solid-state germanium-68 source material as set forth in wherein the third tetrahedra is a stable germanium tetrahedra claim 3 , the stable germanium tetrahedra comprising stable germanium and oxygen and having a formula ...

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18-08-2016 дата публикации

Oxidation catalyst for treating a natural gas emission

Номер: US20160236147A1
Принадлежит: JOHNSON MATTHEY PLC

A catalytic material for treating an exhaust gas produced by a natural gas engine, which catalytic material comprises a molecular sieve and a platinum group metal (PGM) supported on the molecular sieve, wherein the molecular sieve has a framework comprising silicon, oxygen and optionally germanium, and has a content of heteroatom T-atoms is ≦about 0.20 mol %.

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25-07-2019 дата публикации

ZEOLITE SEPARATION MEMBRANE AND PRODUCTION METHOD THEREFOR

Номер: US20190224630A1
Принадлежит:

Provided are an all-silica zeolite separation membrane for separating carbon dioxide, etc., and not causing a decrease in the processing amount due to adsorption of water molecules, and a production method therefor. One aspect of the present invention is a zeolite separation membrane, in which the framework of a zeolite crystal structure formed on a porous support is all silica, characterized in that the zeolite crystal structure formed on the porous support is fluorine free. Another aspect of the present invention is a method for producing a zeolite separation membrane having a zeolite crystal structure on a porous support, characterized in that the method includes a step of producing a seed crystal, a step of applying the seed crystal onto the porous support, a step of producing a membrane synthesis raw material composition, and a step of immersing the porous support having the seed crystal applied thereon in the membrane synthesis raw material composition and performing hydrothermal synthesis, and the membrane synthesis raw material composition contains a silica source and an organic template and does not contain a fluorine compound. 1. A zeolite separation membrane , in which the framework of a zeolitecrystal structure formed on a porous support is all silica, characterized in that the zeolite crystal structure formed on the porous support is fluorine free.2. The zeolite separation membrane according to claim 1 , characterized in that the zeolite crystal structure is an STT type or a CHA type.3. A raw material composition for producing the zeolite separation membrane according to claim 1 , characterized in thatthe raw material composition contains a silica source and an organic template and does not contain a fluorine compound.4. A method for producing a zeolite separation membrane having a zeolite crystal structure on a porous support claim 1 , characterized in that a step of producing a seed crystal;', 'a step of applying the seed crystal onto the porous ...

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25-07-2019 дата публикации

Process for production of high silica content zeolite from fly ash

Номер: US20190225499A1
Принадлежит: University of the Western Cape

The present invention provides for a process for the production of an aluminosilicate zeolite from fly ash, and in particular but not exclusively, to a process for producing a high silica content zeolite from fly ash without the addition of an external silica source, such as sodium silicate.

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13-11-2014 дата публикации

Catalytic dehydration of alcohols using phase pure, calcined single- and multi-site heterogeneous catalysts

Номер: US20140335013A1
Принадлежит: Signa Chemistry Inc

The disclosure describes a new class of isomorphously metal-substituted aluminophosphate materials with high phase purity that are capable of performing selective Brönsted acid catalyzed chemical transformations, such as transforming alcohols to olefins, with high conversions and selectivities using mild conditions. Isomorphous substitutions of functional metal ions for both the aluminum ions and the phosphorous ions were successful in various AlPO structures, along with multiple metal substitutions into a single aluminum site and/or a phosphorous site. This invention can be used towards the catalytic conversion of hydroxylated compounds of linear and/or branched moiety with the possibility of being substituted to their respective hydrocarbon products, preferably light olefins containing 2 to 10 carbon atoms, among other chemistries.

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09-09-2021 дата публикации

METAL-ORGANIC FRAMEWORK CATALYSTS, AND USES THEREOF

Номер: US20210277028A1
Принадлежит:

Provided herein are metal-organic frameworks having a repeating core structure that generally includes a linker coordinated to a secondary building unit through O-metal-O bonds. The linkers create a framework with a plurality of pores, where a cobalt carbonyl moiety occupies at least a portion of the plurality of pores. Provided are also methods of making such metal-organic frameworks via a solvothermal reaction. The metal-organic frameworks are suitable for use in carbonylation reactions, such as carbonylation of epoxides. The metal-organic frameworks may be used for producing acrylic acid from ethylene oxide and carbon monoxide on an industrial scale. The production may involve various unit operations, including for example a beta-propiolactone production system configured to produce beta-propiolactone from ethylene oxide and carbon monoxide; a polypropiolactone production system configured to produce polypropiolactone from beta-propiolactone; and an acrylic acid production system configured to produce acrylic acid with a high purity by thermolysis of polypropiolactone. 1. A method to produce a metal-organic framework , comprising:solvothermally reacting a porphyrin linker with a metal salt in an amine-based solvent to produce a metal-organic framework, wherein{'sup': '2', 'the metal-organic framework comprises repeating cores, wherein the cores comprise the porphyrin linker coordinated to a secondary building unit through O-M-O bonds; and'}soaking the metal-organic framework in a cobalt solution to incorporate a cobalt carbonyl moiety in at least a portion of the pores in the metal-organic framework.2. The method of claim 1 , wherein solvothermally reacting the porphyrin linker with the metal salt in the amine-based solvent to produce the metal-organic framework claim 1 , comprises:mixing the porphyrin linker with the metal salt in the amine-based solvent to produce a reaction mixture; andheating the reaction mixture to a temperature between 80° C. and 140° C. to ...

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07-09-2017 дата публикации

Molecular sieve material, its synthesis and use

Номер: US20170252730A1
Принадлежит: ExxonMobil Research and Engineering Co

A molecular sieve material, EMM-25, having in its calcined form an X-ray diffraction pattern including the following peaks: d-spacing (Å) Relative Intensity [100 × I/I(o)]% 11.74-11.34  60-100 9.50-9.10 30-80 8.68-8.28 10-40 5.64-5.44 20-60 4.52-4.42 10-50 4.28-4.18 10-40 3.96-3.86 40-80 3.69-3.59 30-70

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07-09-2017 дата публикации

PROCESS FOR HYDROXYLATION OF AROMATIC COMPOUNDS, HYDROXYLATION CATALYST AND PROCESS FOR PREPARING SAME

Номер: US20170253547A1
Принадлежит:

The present invention relates to a process for hydroxylation of a compound of formula (I) by reacting the compound of formula (I) with an oxidizing agent, in the presence of a titanium silicalite zeolite prepared by crystallization preceded by a maturing step. The present invention also relates to a titanium silicalite zeolite and to the process for preparing same. 111.-. (canceled)12. A matured TS-1 or TS-2 titano-silicalite zeolite having:an apparent mean particle size of from 35 to 75 nm,{'sup': 2', '2, 'an outer surface area of from 60 m/g to 150 m/g, and'}an inter-grain distance of from 10 to 30 nm.1314.-. (canceled)15. The matured TS-1 or TS-2 titano-silicalite zeolite according to further having a specific surface area of between 350 and 600 m/g.16. The matured TS-1 or TS-2 titano-silicalite zeolite according to further having a specific surface area of between 400 and 500 m/g.17. The matured TS-1 or TS-2 titano-silicalite zeolite according to further having micropores of between 0.40 and 0.50 nm.18. The matured TS-1 or TS-2 titano-silicalite zeolite according to further having micropores of between 0.44 and 0.46 nm.19. The matured TS-1 or TS-2 titano-silicalite zeolite according to further having a mole ratio Ti/(Ti+Si) of from 0.0001 to 0.10.20. A process for preparing a TS-1 or TS-2 titano-silicalite zeolite claim 12 , comprising the following steps:a) preparation of a zeolite precursor from at least one source of silicon, at least one source of titanium, at least one mineralizing agent and at least one structuring agent;b) maturation of the zeolite precursor for obtaining a matured precursor;c) crystallization of the matured precursor for obtaining a matured crystalline precursor, and optionallyd) calcination of the matured crystalline precursor,wherein said maturation step consists in a step of thermal heating of said zeolite precursor, before crystallization, at a temperature of from 70 to 100° C.21. The process according to claim 20 , wherein said ...

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15-09-2016 дата публикации

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

Номер: US20160263562A1
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): 4. The process of claim 1 , wherein the aqueous composition further comprises:(b) a source of an aluminum oxide;(c) a source of a germanium oxide;(d) a source of a titanium oxide; or(e) a combination of (b)-(d).5. The process of claim 4 , wherein the hydrothermal treatment provides a crystalline microporous pure-silica claim 4 , aluminosilicate solid claim 4 , germanosilicate claim 4 , or titanosilicate of LTA topology.6. The process of claim 1 , wherein:(a) the source of silicon oxide comprises an alkoxide, a silicate, silica hydrogel, silicic acid, fumed silica, colloidal silica, tetra-alkyl orthosilicate, a silica hydroxide, a silicon alkoxide, or combination thereof;(b) the source of aluminum oxide, when present, comprises an alkoxide, hydroxide, or oxide of aluminum, a sodium aluminate, or combination thereof;{'sub': 4', '4', '4', '3', '2', '4', '8', '3', '4, 'sup': 4−', '−', '2−', '3−, '(c) the source of germanium oxide, when present, comprises a alkali metal orthogermanate, MGeO, containing discrete GeOions, GeO(OH), GeO2(OH), [(Ge(OH))(OH)]or neutral solutions of germanium dioxide containing Ge(OH), or an alkoxide or carboxylate derivative thereof;'}(d) the source of titanium oxide, when present, comprises a titanium alkoxide, oxide, or hydroxy oxide; and(e) the source of boron oxide, gallium oxide, hafnium oxide, iron oxide, tin oxide, titanium oxide, indium oxide, vanadium oxide, zinc oxide, zirconium oxide, when present, comprises a titanium alkoxide, oxide, or hydrated oxide (oxyhydroxide).7. The process of claim 1 , wherein the mineralizing agent comprises an aqueous alkali metal or alkaline earth metal hydroxide.8. The process of claim 1 , wherein the mineralizing agent comprises hydrofluoric acid (HF).9. The process ...

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13-08-2020 дата публикации

METHOD FOR SYNTHESISING MICROPARTICLES

Номер: US20200255297A1
Принадлежит:

A method for synthesizing mesoporous silica microparticles comprising the steps of: preparing a sol from an ammonium catalyzed hydrolysis and condensation reaction of a pre-sol solution comprising a silica precursor and a structure directing agent dissolved in a mixed solvent system comprising an alcohol and water to produce mesoporous particles of silica with an average diameter of up to about 50 μm; hydrothermally treating the particles to increase the pore size; treating the particles to remove residual structure directing agent; and further increasing the pore size using controlled dissolution. 2. The method of claim 1 , wherein the porous particles are hydrothermally treated at a temperature of between 70° C. and 150° C.3. The method of claim 1 , wherein the amine to water ratio is between 1 v/v % and 10 v/v %.4. The method of claim 1 , wherein the amine is N claim 1 ,N-dimethyldecylamine claim 1 , trioctylamine claim 1 , trimethylamine claim 1 , tridodecylamine claim 1 , trimethylamine claim 1 , or combinations thereof.5. The method of claim 1 , wherein the structure directing agent is cetyltrimethylammonium bromide (CTAB).6. The method of claim 1 , wherein in the etching process:(i) the base catalyst is present in a concentration of between 0.01 M and 1 M;(ii) the particles are etched for up to 12 hours or for between 1 day to 5 days;(iii) the particles are etched at a temperature of 50° C.;(iv) the etching process comprises a silica chelating or complexing agent;(v) the base catalyst is ammonium hydroxide;(vi) or combinations thereof.7. The method of claim 1 , wherein:(i) the particles are treated for 1 hour to 24 hours to remove residual structure directing agent;(ii) the particles are treated in the presence of an alcohol to remove residual structure directing agent; or(iii) a combination of (i) and (ii).8. The method of claim 1 , wherein the silica precursor is 1 claim 1 ,2-Bis(triethoxysilyl)ethane.9. The method of claim 1 , wherein(i) the mole ratio of ...

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22-08-2019 дата публикации

Hydrogel derived carbon for energy storage devices

Номер: US20190259544A1
Автор: David Mitlin, Jia DING
Принадлежит: Sparkle Power LLC

An energy storage device, such as a sodium ion capacitor, including an anode and a cathode, at least one of the anode and the cathode including a nitrogen and oxygen functionalized carbon (NOFC). The NOFC has a nitrogen content greater than 4 wt %, such as 13 wt %, an oxygen content greater than 8 wt %, such as 11 wt %, and a surface area greater than 800 m 2 g −1 , such as 945 m 2 g −1 . The energy storage device has favorable reversible and rate capability, such as 437 mAhg −1 at 100 mAg −1 , and 185 mAhg −1 at 1600 mA g −1 .

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09-12-2021 дата публикации

Modified Metal-Organic Framework (MOF) Compositions, Process of Making and Process of Use Thereof

Номер: US20210379559A1
Принадлежит: Numat Technologies Inc

This invention relates to modified MOF materials, methods of preparing them and processes using them. A modified MOF of the invention is modified by impregnating a MOF with an inorganic metal salt. The starting MOF contains at least one linker or ligand which contains an aryl amino group as part of its structure. These modified MOFs are able to adsorb either basic or acidic toxic industrial compounds (TIC). The modified MOFs can be used to remove TICs from various gaseous streams such as air.

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04-10-2018 дата публикации

HIERARCHICAL SILICEOUS MESOSILICALITE NANOCARRIER

Номер: US20180280303A1
Принадлежит: Imam Abdulrahman Bin Faisal University

A mesosilicalite nanocarrier having a hierarchical silicalite characterized by a molar ratio of aluminum to silica in a range of 1:3000 to 1:1000. The hierarchical silicalite includes mesopores of a hexagonal structure, and micropores of silicalite structure with a microporous volume in the range of 0.05 cc/g to 0.1 cc/g. The nanocarrier has a mesophase content in the range of 30 wt % to 70 wt %, a microphase content in the range of 30 wt % to 70 wt %, and a mean pore diameter in the range of 1.5 nm to 5.5 nm. A method of preparing the stable mesosilicalite nanocarrier with hierarchical micro/mesopores to load an antioxidant or drug for targeted drug delivery is also described. 1: A mesosilicalite nanocarrier comprising: a mesophase with mesopores of a hexagonal structure; and', 'a microphase with micropores of a microporous volume in the range of 0.05 cc/g to 0.1 cc/g;, 'a hierarchical silicalite having a silica to aluminum molar ratio in a range of 1000:1 to 3000:1, comprisingwherein the mesophase content is in the range of 30% to 70% relative to a total weight of the nanocarrier, and the microphase content is in the range of 30% to 70% relative to the total weight of the nanocarrier; andwherein a mean pore diameter of the mesosilicalite nanocarrier in the range of 1.5 nm to 5.5 nm.2: The mesosilicalite nanocarrier of claim 1 , wherein a volume of the mesopores is in the range of 0.11 cc/g to 1.5 cc/g.3: The mesosilicalite nanocarrier of claim 1 , wherein the mesopores are ordered.4: The mesosilicalite nanocarrier of claim 1 , further comprising an antioxidant loaded in the mesopores and the micropores of the nanocarrier.5: The mesosilicalite nanocarrier of claim 4 , wherein an adsorbed antioxidant weight is 10%-50% of a nanocarrier weight at an antioxidant loading rate in the range of 0.1 mmol/g of the nanocarrier to 16 mmol/g of the nanocarrier.6: The mesosilicalite nanocarrier of claim 4 , wherein a total recovery yield for the antioxidant is in the range of 95 ...

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12-09-2019 дата публикации

Synthesis of *mre framework type molecular sieves

Номер: US20190276323A1
Принадлежит: Chevron USA Inc

A molecular sieve of *MRE framework can be synthesized using one or more of (2-hydroxyethyl)trimethylammonium cations, (2-hydroxpropyl)trimethylammonium cations, propyltrimethylammonium cations, and benzyltrimethylammonium cations as a structure directing agent.

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26-09-2019 дата публикации

SEED CRYSTALS, METHOD OF PRODUCING SEED CRYSTALS, METHOD OF PRODUCING SEED CRYSTALS ATTACHMENT SUPPORT, AND METHOD OF PRODUCING ZEOLITE MEMBRANE COMPLEX

Номер: US20190292062A1
Принадлежит: NGK Insulators, Ltd.

Seed crystals are crystals of zeolite to be attached onto a support in production of a zeolite membrane complex including the support and a zeolite membrane formed on the support. The specific surface area of the seed crystals is not smaller than 10 m/g and not larger than 150 m/g. The strength obtained from a crystal component at a diffraction angle 2θ indicating a maximum peak in a range of diffraction angle 2θ from 12° to 25° in an X-ray diffraction pattern obtained by emitting X-ray to the seed crystals is not less than once and not more than 30 times that obtained from an amorphous component. It is thereby possible to improve adherence of the seed crystals to the support. 1. Seed crystals of zeolite to be attached onto a support in production of a zeolite membrane complex comprising said support and a zeolite membrane formed on said support , wherein{'sup': 2', '2, 'the specific surface area is not smaller than 10 m/g and not larger than 150 m/g, and'}the strength obtained from a crystal component at a diffraction angle 2θ indicating a maximum peak in a range of diffraction angle 2θ from 12° to 25° in an X-ray diffraction pattern obtained by emitting X-ray to said seed crystals is not less than once and not more than 30 times that obtained from an amorphous component.2. The seed crystals of zeolite according to claim 1 , containing:any two or more of silicon, aluminum, and phosphorus, or silicon.3. The seed crystals of zeolite according to claim 2 , containing:at least aluminum, phosphorus, and oxygen.4. The seed crystals of zeolite according to claim 1 , wherein{'sup': 3', '3, 'the tap density is not lower than 0.2 g/cmand not higher than 1.0 g/cm.'}5. The seed crystals of zeolite according to claim 1 , being attached onto a substantially vertical plane or a downward-facing plane in production of said zeolite membrane complex claim 1 , out of a surface of said support.6. The seed crystals of zeolite according to claim 1 , whereinsaid support is porous.7. The ...

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26-10-2017 дата публикации

CRYSTALLINE MOLECULAR SIEVES AND SYNTHESIS THEREOF

Номер: US20170305752A1
Автор: Zones Stacey Ian
Принадлежит:

Crystalline molecular sieves and their synthesis using quaternary N-methyl-diisoalkylammonium cations as organic structure directing agents are disclosed. The structure directing agent has the following structure (1): 1. A crystalline molecular sieve , wherein the molecular sieve has a framework type of SSZ-47 and a three-dimensional framework comprising oxides of silicon and aluminum , comprising within its pore structure N ,N-dimethyl-di-sec-butylammonium cations.2. A method of synthesizing the crystalline molecular sieve of claim 1 , the method comprising subjecting to crystallization conditions one or more sources of oxides silicon and aluminum in the presence of fluoride ions claim 1 , water claim 1 , and N claim 1 ,N-dimethyl-di-sec-butylammonium cations.5. The method of claim 2 , wherein the crystallization conditions include a temperature of from 135° C. to 200° C. This application is a divisional application of pending U.S. patent application Ser. No. 15/215,657, filed Jul. 21, 2016 which claims priority to and the benefit of U.S. patent application Ser. No. 62/195,826, filed Jul. 23, 2015, the disclosures of which are fully incorporated herein by reference in their entireties.This disclosure relates generally crystalline molecular sieves and their synthesis using quaternary N-methyl-diisoalkylammonium cations as organic structure directing agents.Zeolites and zeolite-like materials are porous crystalline materials made of tetrahedral or octahedral oxide building blocks, linked together through tetrahedral or octahedral corner oxygen atoms. There are many ways in which the tetrahedral or octahedral building blocks may link to form polynuclear complex structures, having different topologies. In some structures, the building blocks link to form infinite chains, forming fibrous needle-like crystals. In other structures, the building blocks are linked in layers or sheets. In yet other structures, the building blocks are linked in three dimensions with mutual ...

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24-09-2020 дата публикации

METHOD OF USING BIOPOLYMER TO SYNTHESIZE TITANIUM-CONTAINING SILICON OXIDE MATERIAL AND APPLICATIONS THEREOF

Номер: US20200298218A1
Принадлежит:

A method of using biopolymer to synthesize titanium-containing silicon oxide material and applications thereof are disclosed. The method comprises steps: mixing a titanium source, a silicon source, an acid source, a base source, a biopolymer and a solvent to form an aqueous solution, and letting the aqueous solution react to form a semi-product; performing aging, solid-liquid separation and drying of the semi-product to obtain a dried solid; and performing calcination or extraction of the dried solid to obtain a titanium-containing silicon oxide material with a high specific surface area. The present invention adopts a biopolymer as the templating agent, which makes the fabrication process of titanium-containing silicon oxide material more environment-friendly. After calcination or extraction, the product still has superior catalytic activity, able to catalyze epoxidation of olefins and favorable for the production of epoxide. 1. A method for fabricating titanium-containing silicon oxide material , comprising steps:mixing a titanium source, a silicon source, an acid source, a base source, a biopolymer, and a solvent to form an aqueous solution;letting said aqueous solution react to form a first resultant liquid, aging said first resultant liquid to form a second resultant liquid, performing a solid-liquid separation process on said second resultant liquid, and drying a solid obtained from said solid-liquid separation process to obtain a dried solid; andperforming a calcination process on said dried solid to obtain said titanium-containing silicon oxide material or performing an extraction process on said dried solid with an extracting agent to obtain said titanium-containing silicon oxide material, wherein said titanium-containing silicon oxide material meets following conditions:pores of said titanium-containing silicon oxide material have an average diameter of greater than 10 Å;more than 90% of total volume of said pores of said titanium-containing silicon oxide ...

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08-11-2018 дата публикации

AROMATIC HYDROGENATION CATALYSTS AND USES THEREOF

Номер: US20180318790A1
Принадлежит:

Hydrogenation catalysts for aromatic hydrogenation including an organosilica material support, which is a polymer comprising independent units of a monomer of Formula [ZOZOSiCH](I), wherein each Zand Zindependently represent a hydrogen atom, a C-Calkyl group or a bond to a silicon atom of another monomer; and at least one catalyst metal are provided herein. Methods of making the hydrogenation catalysts and processes of using, e.g., aromatic hydrogenation, the hydrogenation catalyst are also provided herein. 125.-. (canceled)26. A method of making a hydrogenation catalyst for aromatic hydrogenation , the method comprising:a) providing an aqueous mixture that contains essentially no structure directing agent and/or porogen,{'sup': 15', '16', '15', '16, 'sub': 2', '3', '1', '4', '1', '4', '1', '4, '(b) adding at least one compound of Formula [ZZSiCH](VII) into the aqueous mixture to form a solution, wherein each Zrepresents a C-Calkoxy group and each Zrepresents a C-Calkoxy group or a C-Calkyl group;'}(c) aging the solution to produce a pre-product;{'sup': 1', '2', '1', '2, 'sub': 2', '3', '1', '4, '(d) drying the pre-product to obtain an organosilica material support which is a polymer comprising independent units of a monomer of Formula [ZOZOSiCH](I), wherein each Zand Zindependently represent a hydrogen atom, a C-Calkyl group or a bond to a silicon atom of another monomer, wherein the organosilica material support has an X-ray diffraction pattern with one peak between 1 and 3 degrees 2θ and no peaks in the range of from 3 to 20 degrees 2θ; and'}(e) impregnating the organosilica material support with at least one catalyst metal selected from the group consisting of a Group 8 metal, a Group 9 metal, a Group 10 metal and a combination thereof.27. The method of claim 26 , wherein each Zrepresents a C-Calkoxy group.28. The method of claim 27 , wherein each Zrepresents a C-Calkoxy group.29. The method of claim 28 , wherein each Zrepresents a C-Calkoxy group.30. The method ...

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16-11-2017 дата публикации

Process for preparing a molecular sieve

Номер: US20170326535A1
Автор: Allen W. Burton
Принадлежит: ExxonMobil Research and Engineering Co

The present invention relates to the synthesis of molecular sieves of the STT and ITE framework types using, as structure directing agent Q, [L(DETA)2] 2+ cation or [L(TEPA)] 2+ cation, or a mixture thereof, where L is a divalent metal cation comprising at least one of Ni, Co and Mn and DETA is diethylene triamine and TEPA is tetraethylene pentamine.

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15-11-2018 дата публикации

DUAL CATALYST SYSTEM FOR PROPYLENE PRODUCTION

Номер: US20180326408A1
Принадлежит:

Embodiments of processes for producing propylene utilize a dual catalyst system comprising a mesoporous silica catalyst impregnated with metal oxide and a mordenite framework inverted (MFI) structured silica catalyst downstream of the mesoporous silica catalyst, where the mesoporous silica catalyst includes a pore size distribution of at least 2.5 nm to 40 nm and a total pore volume of at least 0.600 cm/g, and the MFI structured silica catalyst has a total acidity of 0.001 mmol/g to 0.1 mmol/g. The propylene is produced from the butene stream via metathesis by contacting the mesoporous silica catalyst and subsequent cracking by contacting the MFI structured silica catalyst. 1. A dual catalyst system for producing propylene from butene , the dual catalyst system comprising a metathesis catalyst zone and a cracking catalyst zone directly downstream of the metathesis catalyst zone where:the metathesis catalyst zone comprises mesoporous silica catalyst impregnated with metal oxide; andthe cracking catalyst zone comprises a mordenite framework inverted (MFI) structured silica catalyst.2. The dual catalyst system of where the metathesis catalyst zone and the cracking catalyst zone are disposed in one reactor.3. The dual catalyst system of in which at least a portion of the MFI structured silica catalyst is in contact with at least a portion of the mesoporous silica catalyst impregnated with metal oxide.4. The dual catalyst system of where the metathesis catalyst zone is disposed in a first reactor and the cracking catalyst zone is disposed in a second reactor directly downstream of the first reactor.5. The dual catalyst system of further comprising a conduit between the first reactor and the second reactor.6. The dual catalyst system of where the metal oxide of the mesoporous silica catalyst comprises one or more oxides of molybdenum claim 1 , rhenium claim 1 , tungsten claim 1 , or combinations thereof.7. The dual catalyst system of where the mesoporous silica catalyst ...

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22-11-2018 дата публикации

METHOD FOR THE PREPARATION OF DEFECT-FREE NANOSIZED SYNTHETIC ZEOLITE MATERIALS

Номер: US20180334389A1
Принадлежит:

Some embodiments are directed to a method for the preparation of defect-free nanosized synthetic zeolite materials, to the defect-free nanosized synthetic zeolite materials, to stable colloidal suspensions of the defect-free synthetic zeolite materials, and to the use of the defect-free nanosized synthetic zeolite materials and the stable colloidal suspensions in various applications. 1. A method for the preparation of a defect-free synthetic zeolite material in the form of monodisperse single nanocrystals having a size ranging from 10 to 400 nm , the defect-free synthetic zeolite material having a MFI- , BEA- or MEL-framework type and a silicon to metal M molar ratio Si/M ranging from 179 to 65440 , the metal M being selected from W , V , Mo , Sn and Zr , the method comprising: [{'br': None, 'i': x', ':y', 'z', 'u, 'sub': n', 'm', '2', '2', '2', '2, 'MO:25SiOTAAO:M′O:HO\u2003\u2003(I)'}, 0.01≤x≤1.5,', '2≤y≤9,', '0.01≤z≤4,', '300≤u≤3000,', 'n is an integer equal to 1 or 2, and', 'm is an integer and 2≤m≤5;, 'in which], '1) contacting at least one source of silicon, at least one source of alkali metal M′ selected from Na and K, at least one source of metal M selected from W, V, Mo, Sn and Zr, at least one tetraalkylammonium hydroxide structure-directing agent and water, so as to obtain a clear aqueous suspension having the following molar composition2) aging the resulting clear suspension of step 1) at a temperature ranging from 20° C. to 30° C.;3) heating the resulting clear suspension at a temperature ranging from 40° C. to 180° C. so as to form a dispersion of a solid comprising monodisperse single nanocrystals of the synthetic zeolite material in a liquid;4) separating and recovering the solid from the liquid; and5) calcining the solid so as to obtain the synthetic zeolite material in the form of monodisperse single nanocrystals.2. The method according to claim 1 , wherein the source of silicon is selected from silica hydrogel claim 1 , silicic acid claim 1 , ...

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17-12-2015 дата публикации

Microporous Zirconium Silicate for the Treatment of Hyperkalemia

Номер: US20150359821A1
Принадлежит: ZS Pharma Inc

The present invention relates to novel microporous zirconium silicate compositions that are formulated to remove toxins, e.g. potassium ions, from the gastrointestinal tract at an elevated rate without causing undesirable side effects. The preferred composition has at least 95% ZS-9. These compositions are particularly useful in the therapeutic treatment of hyperkalemia. These compositions are also useful in the treatment of chronic kidney disease, coronary vascular disease, diabetes mellitus, and transplant rejection.

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08-12-2016 дата публикации

TITANIUM-SILICALITE MOLECULAR SIEVE, METHOD FOR PREPARING THE SAME AND METHOD FOR PREPARING CYCLOHEXANONE OXIME USING THE MOLECULAR SIEVE

Номер: US20160355467A1
Принадлежит:

The present invention provides a titanium-silicalite molecular sieve and a method for preparing the same. The method includes the steps of preparing a mixture of a titanium source, a silicon source, a metal source selected from IIA to IVA elements and a template agent; heating the mixture to form a gel mixture; heating the gel mixture in a water bath; and calcining the gel mixture after the gel mixture in the water bath to form the titanium-silicalite molecular sieve. The present invention further provides a method for preparing cyclohexanone oxime by using the titanium-silicalite molecular sieve as the catalyst which results in high conversion rate, high selectivity and high usage efficiency of hydrogen peroxide. 115-. (canceled)16. A titanium-silicalite molecular sieve , comprising:a silicon oxide;a titanium oxide; anda metal oxide, wherein a metal of the metal oxide is at least one selected from IIA to IVA elements, a molar ratio of titanium to silicon is in a range of from 0.005 to 0.1, and a molar ratio of the metal to the silicon is in a range of from 0.00001 to 0.05.17. The titanium-silicalite molecular sieve of claim 16 , wherein the metal of the metal oxide is positioned inside or outside a skeleton of the titanium-silicalite molecular sieve.18. A method for preparing cyclohexanone oxime claim 16 , comprising the step of:{'claim-ref': {'@idref': 'CLM-00016', 'claim 16'}, 'performing a reaction of cyclohexanone, ammonia and hydrogen peroxide in the presence of a titanium-silicalite molecular sieve of as a catalyst and a solvent.'}19. The method of claim 18 , wherein a molar ratio of the ammonia to the cyclohexanone is in a range of from 1.1:1 to 2:1.20. The method of claim 18 , wherein a molar ratio of the hydrogen peroxide to the cyclohexanone is in a range of from 0.7:1 to 2.5:1.21. The method of claim 18 , wherein the solvent is one or more selected from the group consisting of an alcohol claim 18 , a ketone and water.22. The method of claim 21 , wherein ...

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06-12-2018 дата публикации

SYNTHESIS OF SFE FRAMEWORK TYPE MOLECULAR SIEVES

Номер: US20180346340A1
Автор: Xie Dan
Принадлежит:

A method is provided for synthesizing a molecular sieve of SFE framework type using a structure directed agent selected from one or more of 1,2,3,5-tetramethyl-1H-pyrazol-2-ium cations and 1,2,3,4-tetramethyl-1H-imidazol-3-ium cations. 1. A method of synthesizing a molecular sieve of SFE framework type , the method comprising: (1) a source of silicon oxide;', '(2) a source of an oxide of a trivalent element (X);', '(3) optionally, a source of a Group 1 or Group 2 metal (M);', '(4) a structure directing agent (Q) comprising one or more of 1,2,3,5-tetramethyl-1H-pyrazol-2-ium cations and 1,2,3,4-tetramethyl-1H-imidazol-3-ium cations;', '(5) hydroxide ions; and', '(6) water; and, '(a) preparing a reaction mixture comprising(b) subjecting the reaction mixture to crystallization conditions sufficient to form crystals of the molecular sieve.4. The method of claim 1 , wherein the trivalent element X is selected from one or more of boron claim 1 , aluminum claim 1 , gallium claim 1 , and iron.5. The method of claim 1 , wherein the trivalent element X comprises boron.6. The method of claim 1 , wherein the reaction mixture also contains seeds.7. The method of claim 6 , wherein the reaction mixture comprises from 0.01 to 10 claim 6 ,000 ppm by weight of seeds.8. The method of claim 6 , wherein the seeds comprise a crystalline material of SFE framework type.9. The method of claim 1 , wherein the crystallization conditions include a temperature of from 125° C. to 200° C.10. A molecular sieve of SFE framework type and claim 1 , in its as-synthesized form claim 1 , comprising one or more of 1 claim 1 ,2 claim 1 ,3 claim 1 ,5-tetramethyl-1H-pyrazol-2-ium cations and 1 claim 1 ,2 claim 1 ,3 claim 1 ,4-tetramethyl-1H-imidazol-3-ium cations in its pores.11. The molecular sieve of claim 10 , and having a SiO/XOmolar ratio of 20 to 300 claim 10 , wherein X is selected from one or more of boron claim 10 , aluminum claim 10 , gallium claim 10 , and iron.12. The molecular sieve of claim 11 ...

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29-10-2020 дата публикации

Catalyst for producing olefins from dehydrogenation of alkane and a method for producing olefins using said catalyst

Номер: US20200338535A1
Принадлежит: PTT Global Chemical Pcl

The present invention relates to a catalyst for producing olefins from dehydrogenation of alkane having 2 to 5 carbon atoms and a method for producing olefins using said catalyst, wherein said catalyst comprises a hierarchical zeolite nanosheet having a silica to alumina(SiO2/AI2O3) ratio more than 120 and group X metal(s) in a range of 0.3 to 5% by weight. The catalyst according to the conversion of precursor to yields and high olefins selectivity.

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15-12-2016 дата публикации

DDR ZEOLITE SEED CRYSTAL, METHOD FOR PRODUCING SAME, AND METHOD FOR PRODUCING DDR ZEOLITE MEMBRANE

Номер: US20160361691A1
Принадлежит: NGK Insulators, Ltd.

There are provided DDR type zeolite seed crystals capable of inhibiting generation of surplus DDR type zeolite crystals in the case of using the DDR type zeolite seed crystals as seed crystals upon forming a DDR type zeolite membrane on the surface of a porous support. The DDR type zeolite seed crystals have an average particle size of 0.05 to 1.5 μm; contain 90% or more of particles having an aspect ratio, which is obtained by dividing the maximum Feret's diameter by the minimum Feret's diameter, of 1 to 3; and have not more than 0.3 of a coefficient of variation of the square of the aspect ratio. 1. A method for manufacturing a DDR type zeolite seed crystal , comprising:a heating step of heating a raw material solution containing silica, and a nucleus containing a DDR type zeolite, at 130 to 180° C. for four hours or more to form a DDR type zeolite seed crystal; anda washing step of washing the formed DDR type zeolite seed crystal, by preparing a DDR type zeolite seed crystal dispersion liquid by dispersing the DDR type zeolite seed crystal in a dispersion medium to obtain a DDR type zeolite seed crystal-dispersed liquid having a pH of 7.5 or more,wherein the resulting DDR type zeolite seed crystal has an average particle size of 0.05 to 1.5 μm, contains 90% or more of particles having an aspect ratio, which is a value obtained by dividing the maximum Feret's diameter by the minimum Feret's diameter, of 1 to 3, and has not more than 0.3 of a coefficient of variation of the square of the aspect ratio.2. The method according to claim 1 , wherein a Y value calculated from the following formula (1) is not less than 60 claim 1 , while defining a diffraction intensity of a diffraction peak caused by (024) plane of the DDR type zeolite seed crystal as A claim 1 , a minimum value of a diffraction intensity between the peaks of the (024) plane and (116) plane claim 1 , which is influenced by an amorphous substance content claim 1 , as B claim 1 , and a minimum value of a ...

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29-10-2020 дата публикации

SOLIDOTHERMAL SYNTHESIS OF A BORON-CONTAINING ZEOLITE WITH AN MWW FRAMEWORK STRUCTURE

Номер: US20200339430A1
Принадлежит: BASF SE

Described herein is a process for producing a zeolitic material having an MWW framework structure containing YOand BO, in which Y stands for a tetravalent element. The process includes the steps of (i) preparing a mixture containing one or more sources for YO, one or more sources for BO, one or more organotemplates, and seed crystals, (ii) crystallizing the mixture obtained in (i) for obtaining a layered precursor of the MWW framework structure, and (iii) calcining the layered precursor obtained in (ii) for obtaining the zeolitic material having an MWW framework structure. Also disclosed herein are synthetic boron-containing zeolites obtain by the process and uses thereof. 1: A process for producing a zeolitic material having an MWW framework structure comprising YOand BO , wherein Y stands for a tetravalent element , the process comprising:{'sub': 2', '2', '3, '(i) mixing one or more sources for YO, one or more sources for BO, one or more organotemplates, and seed crystals, to obtain a mixture;'}(ii) crystallizing the mixture to obtain a layered precursor of the MWW framework structure; and(iii) calcining the layered precursor to obtain the zeolitic material having the MWW framework structure,wherein: {'br': None, 'sup': 1', '2', '3, 'RRRN\u2003\u2003(I);'}, 'the one or more organotemplates have the formula (I){'sup': '1', 'sub': 5', '8, 'Ris (C-C)cycloalkyl;'}{'sup': 2', '3, 'Rand Rare independently from each other H or alkyl; and'}{'sub': 2', '2, 'the mixture and the layered precursor comprise 35 wt.-% or less of HO based on 100 wt.-% of YOcontained in the mixture and the layered precursor.'}2: The process of claim 1 , wherein the mixture and the layered precursor comprise 5 wt.-% or less of fluoride calculated as the element and based on 100 wt.-% of YO.3: The process of claim 1 , wherein the mixture and the layered precursor comprise 5 wt.-% or less of P and/or Al calculated as the respective element and based on 100 wt.-% of YO.4: The process of claim 1 , ...

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29-10-2020 дата публикации

MOLECULAR SIEVE, ITS PREPARATION AND APPLICATION THEREOF

Номер: US20200339433A1
Принадлежит:

The present invention relates to a molecular sieve, particularly to an ultra-macroporous molecular sieve. The present invention also relates to a process for the preparation of the molecular sieve and to its application as an adsorbent, a catalyst, or the like. The molecular sieve has a unique X-ray diffraction pattern and a unique crystal particle morphology. The molecular sieve can be produced by using a compound represented by the following formula (I), 2. The method according to claim 1 , wherein the first oxide is silica or a combination of silica and germanium dioxide.3. The method according to claim 1 , wherein the second oxide is alumina.4. The method according to claim 1 , wherein the groups Rand Rare different from each other claim 1 , with one of them being selected from the group consisting of Clinear alkylene groups claim 1 , and the other being selected from the group consisting of Clinear alkylene groups and Clinear oxaalkylene groups.5. The method according to claim 1 , wherein the groups Rand Rare different from each other claim 1 , with one of them being selected from the group consisting of Clinear alkylene groups and the other being selected from the group consisting of Clinear alkylene groups and Clinear oxaalkylene groups.6. The method according to claim 5 , wherein the Clinear oxaalkylene group is represented by the formula —(CH)—O—(CH)— claim 5 , wherein each value m claim 5 , being identical or different from each other claim 5 , independently represents 2 or 3.7. The method according to claim 1 , wherein the plural groups R are identical or different from each other claim 1 , each independently selected from the group consisting of methyl and ethyl.8. The method according to claim 1 , wherein:the molar ratio of the first oxide source (calculated on the basis of the first oxide) to the second oxide source (calculated on the basis of the second oxide) is in a range from 5 to co;the molar ratio of water to the first oxide source (calculated on ...

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28-12-2017 дата публикации

Itq-49 material, method for the production thereof and use of same

Номер: US20170368537A1

The present invention refers to a microporous crystalline material, to the method for the production thereof and to the use of same, the material having a composition: x X 2 O 3 :z ZO 2 :y YO 2 in which: X is a trivalent element such as Al, B, Fe, In, Ga, Cr, or mixtures thereof, where (y+z)/x can have values of between 9 and infinity; Z corresponds to a tetravalent element selected from Si, Ge or mixtures thereof; and Y corresponds to a tetravalent element such as Ti, Sn, Zr, V or mixtures thereof, where z/y can have values of between 10 and infinity.

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28-12-2017 дата публикации

SILICOALUMINOPHOSPHATE CATALYST FOR CHLOROMETHANE CONVERSION

Номер: US20170368542A1
Принадлежит: Sabic Global Technologies B.V.

Disclosed is a catalyst capable of producing an olefin from an alkyl halide, the catalyst comprising a silicoaluminophosphate (SAPO) having a chabazite zeolite structure with the following chemical composition (SiAlP)O, where x, y, and z represent the mole fractions of silicon, aluminum, and phosphorus, respectively, present as tetrahedral oxides, x is 0.01 to 0.30 and the sum of x+y+z is 1, and where the catalyst comprises silicon tetrahedral oxides that are connected with three or less aluminum tetrahedral oxide as shown by Si magic angle spinning (MAS) nuclear magnetic resonance (NMR) spectroscopy peak(s) with peak(s) maxima between −93 ppm and −115 ppm. 1. A catalyst capable of producing an olefin from an alkyl halide , the catalyst comprising a silicoaluminophosphate (SAPO) having a chabazite zeolite structure with the following chemical composition:{'br': None, 'sub': x', 'y', 'z', '2, '(SiAlP)O'}where x, y, and z represent the mole fractions of silicon, aluminum, and phosphorus, respectively, present as tetrahedral oxides, x is 0.01 to 0.30 and the sum of x+y+z is 1, and{'sup': '29', 'where the catalyst comprises silicon tetrahedral oxides that are connected with three or less aluminum tetrahedral oxide as shown by Si magic angle spinning (MAS) nuclear magnetic resonance (NMR) spectroscopy peak(s) with peak(s) maxima between −93 ppm and −115 ppm, and'}wherein the catalyst includes 25% or less of silicon tetrahedral oxide shared by four aluminum tetrahedral oxides.2. The catalyst of claim 1 , where a majority of the silicon tetrahedral oxides in the crystal lattice are connected with three or less aluminum tetrahedral oxides.3. (canceled)4. The catalyst of claim 1 , where each silicon tetrahedral oxide is connected with three tetrahedral oxides.5. The catalyst of claim 1 , wherein the peak maxima is between −93 ppm and −97 ppm.6. The catalyst of claim 1 , wherein y is 0.40 to 0.60 and z is 0.25 to 0.49.7. The catalyst of claim 1 , wherein the catalyst is ...

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20-12-2018 дата публикации

A tin-containing zeolitic material having a bea framework structure

Номер: US20180362351A1
Принадлежит: BASF SE

A process for preparing a tin-containing zeolitic material having framework type BEA, comprising providing an aqueous synthesis mixture comprising a boron source, a silicon source, and a BEA structure directing agent; subjecting the synthesis mixture provided in to hydrothermal pre-crystallization conditions; adding the tin source to the obtained mixture; subjecting the obtained aqueous synthesis mixture to hydrothermal crystallization conditions, obtaining a tin-containing zeolitic material having framework type BEA comprised in its mother liquor.

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20-12-2018 дата публикации

PROCESS FOR PREPARING A BORON CONTAINING ZEOLITIC MATERIAL HAVING MWW FRAMEWORK STRUCTURE

Номер: US20180362352A1
Принадлежит: BASF SE

A process for preparing an aluminum-free boron containing zeolitic material comprising the framework structure MWW (BMWW), comprising (a) hydrothermally synthesizing the BMWW from a synthesis mixture containing water, a silicon source, a boron source, and an MWW template compound obtaining the BMWW in its mother liquor, the mother liquor having a pH above 9; (b) adjusting the pH of the mother liquor, obtained in (a) and containing the BMWW, to a value in the range of from 6 to 9; (c) separating the BMWW from the pH-adjusted mother liquor obtained in (b) by filtration in a filtration device. 1. An aluminum-free boron containing zeolitic material comprising the framework structure MWW (BMWW) , obtained by a process comprising(a) hydrothermally synthesizing a BMWW precursor from a synthesis mixture containing water, a silicon source, a boron source, and an MWW template compound obtaining the BMWW precursor in its mother liquor, the mother liquor having a pH above 9;(b) adjusting the pH of the mother liquor, obtained in (a) and containing the BMWW precursor, to a value in the range of from 6 to 9; {'sup': '2', 'and being contained in a spray powder wherein at least 99 weight-% of the spray powder consist of the BMWW, wherein the BMWW has boron content in the range of from 1.0 to 2.2 weight-%, calculated as elemental boron and based on the total weight of the BMWW, a silicon content of at least 37 weight-%, calculated as elemental silicon and based on the total weight of the BMWW, a degree of crystallinity of at least (80 ±5) %, as determined via XRD, and a BET specific surface area of at least 300 m/g, as determined according to DIN 66131.'}, '(c) separating the BMWW precursor from the pH-adjusted mother liquor obtained in (b) by filtration in a filtration device.'}2. The BMWW of claim 1 , wherein the BET specific surface area is in the range of from 300 to 500 m/g claim 1 , as determined according to DIN 66131.3. A catalyst claim 1 , a catalyst support claim 1 , or a ...

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05-12-2019 дата публикации

METHOD OF PRODUCING SEPARATION MEMBRANE

Номер: US20190366275A1
Принадлежит:

There is provided a method of producing a separation membrane in which a zeolite membrane is formed on an inorganic oxide porous substrate. The substrate has amorphous SiOas a main component of a zeolite formation portion of the substrate, the method includes: a first step of forming a zeolite seed crystal and an alkaline component including a structure directing agent on a surface of the substrate; and a second step of treating a formed product obtained in the first step under a heated steam atmosphere, and the zeolite membrane is formed on the surface of the substrate. 1. A method of producing a separation membrane in which a zeolite membrane is formed on an inorganic oxide porous substrate , wherein{'sub': '2', 'the substrate has amorphous SiOas a main component of a zeolite formation portion of the substrate,'}the method comprises:a first step of forming a zeolite seed crystal and an alkaline component including a structure directing agent on a surface of the substrate; anda second step of treating a formed product obtained in the first step under a heated steam atmosphere, andthe zeolite membrane is formed on the surface of the substrate.2. The method of producing a separation membrane according to claim 1 , whereinthe alkaline component is an aqueous solution including an organic ammonium hydroxide.3. The method of producing a separation membrane according to claim 1 , whereinthe alkaline component is an aqueous solution including an organic ammonium halogen salt and an alkali metal hydroxide.4. The method of producing a separation membrane according to claim 1 , further comprising:a third step of drying the alkaline component of the surface of the substrate, between the first step and the second step.5. The production method according to claim 1 , whereinin the first step, the zeolite seed crystal is formed on the surface of the substrate, and then the alkaline component is applied to the surface of the substrate.6. The production method according to claim 5 ...

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