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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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Форма поиска

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 4061. Отображено 100.
29-03-2012 дата публикации

Removal of Hydrogen From Dehydrogenation Processes

Номер: US20120078024A1
Принадлежит: Fina Technology Inc

A process and system for dehydrogenating certain hydrocarbons is disclosed. The process includes contacting a dehydrogenatable hydrocarbon with steam in the presence of a dehydrogenation catalyst to form hydrogen and a dehydrogenated hydrocarbon. Some of the hydrogen is then removed and some of the remaining dehydrogenatable hydrocarbon is dehydrogenated.

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17-05-2012 дата публикации

Methane aromatization catalyst, method of making and method of using the catalyst

Номер: US20120123176A1
Принадлежит: Shell Oil Co

A catalyst for converting methane to aromatic hydrocarbons is described herein. The catalyst comprises an active metal or a compound thereof, and an inorganic oxide support wherein the active metal is added to the support in the form of metal oxalate. The metal oxalate-derived catalyst exhibits superior performance in the conversion of methane-rich feed to aromatics products relative to catalysts prepared from non-oxalate metal precursors. A method of making the catalyst and a method of using the catalyst are also described.

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25-10-2012 дата публикации

Process for the dehydration of aqueous bio-derived terminal alcohols to terminal alkenes

Номер: US20120271089A1
Автор: Michael E. Wright
Принадлежит: US Department of Navy

A method and apparatus for dehydrating bio-1-alcohols to bio-l-alkenes with high selectivity. The bio-1-alkenes are useful in preparing high flashpoint diesel and jet biofuels which are useful to civilian and military applications. Furthermore, the bio-1-alkenes may be converted to biolubricants useful in the transporation sector and other areas requiring high purity/thermally stable lubricants.

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08-11-2012 дата публикации

Dehydrogenation Process

Номер: US20120283494A1
Принадлежит: ExxonMobil Chemical Patents Inc

In a dehydrogenation process a hydrocarbon stream comprising at least one non-aromatic six-membered ring compound and at least one five-membered ring compound is contacted with a first catalyst comprising at least one metal component and at least one support and a second catalyst. The first catalyst is utilized to convert at least a portion of the at least one non-aromatic six-membered ring compound in the hydrocarbon stream to at least one aromatic compound and the second catalyst is utilized to convert at least a portion of the at least one five-membered ring compound in the hydrocarbon stream to at least one paraffin.

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22-11-2012 дата публикации

Process for alkylation of toluene to form styrene and ethylbenzene

Номер: US20120296136A1
Автор: Sivadinarayana Chinta
Принадлежит: Fina Technology Inc

A process is disclosed for making styrene and/or ethylbenzene by reacting toluene with a C 1 source over a catalyst in at least one radial reactor to form a product stream comprising styrene and/or ethylbenzene.

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02-05-2013 дата публикации

Process for reprocessing spent catalysts

Номер: US20130109560A1
Принадлежит: BASF SE

The invention relates to a process for reprocessing spent catalysts comprising rare earth metals, and to a process for producing a new styrene catalyst from a spent styrene catalyst.

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06-03-2014 дата публикации

Catalyst for metathesis of ethylene and 2-butene and/or double bond isomerization

Номер: US20140066681A1
Принадлежит: Lummus Technology Inc

A process for the double-bond isomerization of olefins is disclosed. The process may include contacting a fluid stream comprising olefins with a fixed bed comprising an activated basic metal oxide isomerization catalyst to convert at least a portion of the olefin to its isomer. The isomerization catalysts disclosed herein may have a reduced cycle to cycle deactivation as compared to conventional catalysts, thus maintaining higher activity over the complete catalyst life cycle.

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02-01-2020 дата публикации

Catalytic oxidation method and method for producing conjugated diene

Номер: US20200001262A1
Принадлежит: Mitsubishi Chemical Corp

An object of the present invention is to suppress performance deterioration of a molybdenum composite oxide-based catalyst at the time of performing gas-phase catalytic partial oxidation with molecular oxygen by using a tubular reactor. The present invention relates to a catalytic oxidation method using a tubular reactor in which a Mo compound layer containing a Mo compound and a composite oxide catalyst layer containing a Mo composite oxide catalyst are arranged in this order from a reaction raw material supply port side and under a flow of a mixed gas containing 75 vol % of air and 25 vol % of water vapor at 440° C., a Mo sublimation amount of the Mo compound is larger than a Mo sublimation amount of the Mo composite oxide catalyst under the same conditions.

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07-01-2021 дата публикации

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

Номер: US20210002184A1
Принадлежит:

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

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02-01-2020 дата публикации

METHOD FOR PRODUCING UNSATURATED HYDROCARBON

Номер: US20200002249A1
Принадлежит:

A method for producing an unsaturated hydrocarbon, comprising: a step of contacting a raw material gas containing an alkane with a dehydrogenation catalyst to obtain a product gas containing at least one unsaturated hydrocarbon selected from a group consisting of olefins and conjugated dienes, wherein the dehydrogenation catalyst contains at least one additive element selected from the group consisting of Na, K, and Ca, Al, Mg, a group 14 metal element, and Pt, and a content of the additive element is 0.05% by mass or more and 0.70% by mass or less based on a total mass of the dehydrogenation catalyst. 1. A method for producing an unsaturated hydrocarbon , comprising:a step of contacting a raw material gas containing an alkane with a dehydrogenation catalyst to obtain a product gas containing at least one unsaturated hydrocarbon selected from a group consisting of olefins and conjugated dienes, whereinthe dehydrogenation catalyst contains at least one additive element selected from a group consisting of Na, K, and Ca, Al, Mg, a group 14 metal element, and Pt, anda content of the additive element is 0.05% by mass or more and 0.70% by mass or less based on a total mass of the dehydrogenation catalyst.2. The method according to claim 1 , wherein the content of the additive element is 0.08% by mass or more and 0.35% by mass or less claim 1 , based on the total mass of the dehydrogenation catalyst.3. The method according to claim 1 , wherein a molar ratio of the Mg to the Al is 0.30 or more and 0.60 or less.4. The method according to claim 1 , wherein a molar ratio of the group 14 metal element to the Pt is 10 or less.5. The method according to claim 1 , wherein the group 14 metal element includes Sn.6. The method according to claim 1 , wherein the alkane is an alkane having 4 to 10 carbon atoms.7. The method according to claim 1 , wherein the alkane is butane claim 1 , the olefin is butene claim 1 , and the conjugated diene is butadiene. The present invention relates to ...

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02-01-2020 дата публикации

GAS CLEAN-UP FOR ALKANE OXIDATIVE DEHYDROGENATION EFFLUENT

Номер: US20200002251A1
Принадлежит:

The invention relates to a process for the production of an alkene by alkane oxidative dehydrogenation, comprising: (a) subjecting a stream comprising an alkane to oxidative dehydrogenation conditions, comprising contacting the alkane with oxygen in the presence of a catalyst comprising a mixed metal oxide, resulting in a stream comprising alkene, unconverted alkane, water, carbon dioxide, unconverted oxygen, carbon monoxide and optionally an alkyne; (b) removing water from at least part of the stream comprising alkene, unconverted alkane, water, carbon dioxide, unconverted oxygen, carbon monoxide and optionally an alkyne resulting from step (a), resulting in a stream comprising alkene, unconverted alkane, carbon dioxide, unconverted oxygen, carbon monoxide and optionally alkyne; (c) removing unconverted oxygen, carbon monoxide and optionally alkyne from at least part of the stream comprising alkene, unconverted alkane, carbon dioxide, unconverted oxygen, carbon monoxide and optionally alkyne resulting from step (b), wherein carbon monoxide and optionally alkyne are oxidized into carbon dioxide, resulting in a stream comprising alkene, unconverted alkane and carbon dioxide; (d) optionally removing carbon dioxide from at least part of the stream comprising alkene, unconverted alkane in and carbon dioxide resulting from step (c), resulting in a stream comprising alkene and unconverted alkane; (e) optionally separating at least part of the stream comprising alkene and unconverted alkane resulting from step (d), into a stream comprising alkene and a stream comprising unconverted alkane; (f) optionally recycling unconverted alkane from at least part of the stream comprising unconverted alkane resulting from step (e), to step (a). 1. A process for the production of an alkene by alkane oxidative dehydrogenation , comprising:(a) subjecting a stream comprising an alkane to oxidative dehydrogenation conditions, comprising contacting the alkane with oxygen in the presence of a ...

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03-01-2019 дата публикации

CATALYST AND HYDROCARBON CONVERSION PROCESS UTILIZING THE CATALYST

Номер: US20190002372A1
Принадлежит: SMH Co., Ltd

The present invention relates to a hydrocarbon conversion catalyst comprising i) a catalyst, in oxidic form, metals M1, M2, M3 and M4, wherein: M1 is selected from Si, Al, Zr, and mixtures thereof; M2 is selected from Pt, Cr, and mixtures thereof; M3 is selected from W, Mo, Re and mixtures thereof; M4 is selected from Sn, K, Y, Yb and mixtures thereof; and ii) a hydrogen scavenger selected from at least one alkali and/or alkaline earth metal derivative, preferably in metallic, hydride, salt, complex or alloy form; as well as a hydrocarbon conversion process utilizing this catalyst. 1. Hydrocarbon conversion catalyst comprising , M1 is selected from Si, Al, Zr, and mixtures thereof;', 'M2 is selected from Pt, Cr, and mixtures thereof;', 'M3 is selected from W, Mo, Re and mixtures thereof;', 'M4 is selected from Sn, K, Y, Yb, and mixtures thereof; wherein', 'the mass fraction of M1 is in the range of 0.1 to 0.8;', 'the mass fraction of M2 is in the range of 0.001 to 0.2;', 'the mass fraction of M3 is in the range of 0.001 to 0.2;', 'the mass fraction of M4 is in the range of 0.0001 to 0.2; and', 'the mass fraction of oxygen is in the range of 0.1 to 0.8;', 'and, 'i) a catalyst in oxidic form, comprising metals M1, M2, M3 and M4, whereinii) a hydrogen scavenger selected from at least one alkali and/or alkaline earth metal derivative.2. Hydrocarbon conversion catalyst according to claim 1 , wherein the at least one alkali and/or alkaline earth metal is selected from Li claim 1 , Na claim 1 , K claim 1 , Mg claim 1 , Ca claim 1 , and mixtures thereof.3. Hydrocarbon conversion catalyst according to claim 1 , wherein weight ratio of catalyst i) and hydrogen scavenger ii) is from 1-99 to 99-1.4. Hydrocarbon conversion catalyst according to claim 1 , wherein M2 is Pt and M3 is W.5. Process for conversion of a hydrocarbon feed comprising saturated hydrocarbon compounds to olefin products comprising contacting a hydrocarbon feed stream with the hydrocarbon conversion catalyst ...

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01-01-2015 дата публикации

Hydroalkylation Process

Номер: US20150005531A1
Принадлежит: ExxonMobil Chemical Patents Inc.

In a process for producing phenol, benzene is hydroalkylated with hydrogen in the presence of a catalyst under conditions effective to produce a hydroalkylation reaction product comprising cyclohexylbenzene and cyclohexane. At least a portion of the cyclohexane from said hydroalkylation reaction product is then dehydrogenated to produce a dehydrogenation effluent comprising benzene, toluene and hydrogen. At least a portion of the dehydrogenation effluent is washed with a benzene-containing stream to transfer at least a portion of the toluene from the dehydrogenation effluent to the benzene-containing stream. 1. A hydroalkylation process comprising:(a) hydroalkylating benzene with hydrogen in the presence of a catalyst under conditions effective to produce a hydroalkylation reaction product comprising cyclohexylbenzene and cyclohexane;(b) contacting at least a portion of the hydroalkylation reaction product with a dehydrogenation catalyst to produce a dehydrogenation effluent having at least a portion of the cyclohexane converted to benzene and hydrogen, wherein the dehydrogenation effluent further comprises toluene; and(c) washing at least a portion of the dehydrogenation effluent with a benzene-containing stream to produce a toluene-depleted dehydrogenation effluent and a wash stream containing at least a portion of the toluene from the dehydrogenation effluent, wherein the at least a portion of the dehydrogenation effluent is in the vapor phase and the benzene-containing stream is in the liquid phase.2. The process of claim 1 , wherein the at least a portion of the dehydrogenation effluent contains at least 50 wt % hydrogen claim 1 , the wt % based upon the weight of the at least a portion of the dehydrogenation effluent.3. The process of claim 1 , wherein at least a portion of the toluene in the dehydrogenation effluent is formed from the decomposition of the cyclohexylbenzene.4. The process of claim 1 , wherein the wash stream contains at least 80 wt % of the ...

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01-01-2015 дата публикации

PROCESS FOR THE PRODUCTION OF 1,3-BUTADIENE

Номер: US20150005532A1
Принадлежит: Versalis S.p.A.

The present invention relates to a process for the production of 1,3-butadiene which comprises the following phases: a) extracting, by means of extractive distillation, in an extraction section, an end-product containing 1,3-butadiene and a raffinate product, starting from mixtures of saturated and unsaturated compounds having from 2 to 10 carbon atoms in the chain; b) sending the raffinate product to a dehydrogenation section; c) dehydrogenating the raffinate product in the dehydrogenation section in the presence of a dehydrogenation catalyst and an inert product so as to form a reaction effluent containing 1,3-butadiene; d) recirculating the reaction effluent containing 1,3-butadiene directly to the extraction section after separating the incondensable compounds. 1. A process for the production of 1 ,3-butadiene , the process comprising:a) extracting, by a method of extractive distillation, in an extraction section, an end-product comprising 1,3-butadiene and a raffinate product, starting from mixtures of saturated and unsaturated compounds having from 2 to 10 carbon atoms in the chain;b) sending the raffinate product to a dehydrogenation section;c) dehydrogenating the raffinate product in the dehydrogenation section in the presence of a dehydrogenation catalyst and an inert product to form a reaction effluent containing 1,3-butadiene;d) recirculating the reaction effluent comprising 1,3-butadiene directly to the extraction section after separating the incondensable compounds.2. The process of claim 1 , wherein claim 1 , after separating the incondensable compounds claim 1 , the reaction effluent is separated into a stream enriched in 1 claim 1 ,3-butadiene and a stream which comprises the non-reacted saturated and unsaturated compounds having from 2 to 10 carbon atoms in the chain.3. The process of claim 2 , wherein the stream enriched in 1 claim 2 ,3-butadiene is recirculated to the extraction section.4. The process of claim 2 , wherein the stream comprising the ...

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09-01-2020 дата публикации

MATERIALS AND METHODS FOR OXIDATIVE DEHYDROGENATION OF ALKYL AROMATIC COMPOUNDS INVOLVING LATTICE OXYGEN OF TRANSITION METAL OXIDES

Номер: US20200009539A1
Принадлежит:

In one aspect, the disclosure relates to a process for dehydrogenating a first dehydrogenation reactant into its unsaturated counterparts. The disclosed process comprises introducing a dehydrogenation reactant to a metal oxide catalyst having dehydrogenation activity, and dehydrogenating the dehydrogenation reactant to provide its unsaturated counterpart and hydrogen; selectively combusting the hydrogen released during dehydrogenation using a lattice oxygen from the metal oxide catalyst, resulting in a reduced metal oxide catalyst and steam; re-oxidizing the reduced metal oxide catalyst by introducing a gaseous oxidant to the reduced metal oxide catalyst; and optionally re-using the re-oxidized metal oxide catalyst for catalytic conversion and combustion. This abstract is intended as a scanning tool for purposes of searching in the particular art and is not intended to be limiting of the present disclosure. 1. A process for oxidative dehydrogenation , comprising:a. introducing one or more dehydrogenation reactants to a metal oxide catalyst having dehydrogenation activity, and dehydrogenating the one or more dehydrogenation reactants to provide a dehydrogenated reaction product and hydrogen;b. selectively combusting the hydrogen released during dehydrogenation using a lattice oxygen from the metal oxide catalyst, resulting in a reduced metal oxide catalyst and steam;c. re-oxidizing the reduced metal oxide catalyst by introducing a gaseous oxidant to the reduced metal oxide catalyst; and optionallyd. re-using the re-oxidized metal oxide catalyst for a subsequent dehydrogenation and/or selective combustion.2. The process of claim 1 , wherein the dehydrogenation reactants comprise an alkyl aromatic hydrocarbon or a substituted alkyl aromatic hydrocarbon and the dehydrogenated reaction product comprises an alkene aromatic hydrocarbon or substituted alkene aromatic hydrocarbon claim 1 , respectively.3. The process of claim 1 , wherein the dehydrogenation reactants ...

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08-01-2015 дата публикации

PROCESS FOR PREPARING A PARAFFIN PRODUCT

Номер: US20150011663A1
Принадлежит:

The invention relates to a process for preparing a paraffin product from a carbonaceous feedstock comprising (a) partial oxidation of the carbonaceous feedstock to obtain a mixture comprising hydrogen and carbon monoxide, (b) performing a Fischer-Tropsch reaction using the mixture as obtained in step (a) and recovering an off-gas from the Fischer-Tropsch reaction and a paraffin product, (c) hydrogenating at least a part of the off-gas from the Fischer-Tropsch reaction using a steam/off-gas mol ratio in the range of between 0.5 and 1.5 and a catalyst comprising copper and zinc, followed by a conversion step (d) using a nickel based catalyst, and (e) preparing a hydrogen comprising gas from at least a part of the off-gas from the Fischer-Tropsch reaction. 18-. (canceled)9. A method for preparing a paraffin product from a carbonaceous feedstock comprising the following steps:(a) partial oxidation of the carbonaceous feedstock to obtain a mixture comprising hydrogen and carbon monoxide;(b) performing a Fischer-Tropsch reaction using the mixture as obtained in step (a) and recovering an off-gas from the Fischer-Tropsch reaction and a paraffin product;(c) subjecting at least a part of the off-gas from the Fischer-Tropsch reaction to hydrogenation using a steam/off-gas mol ratio in the range of between 0.5 and 1.5, and a catalyst comprising copper and zinc;(d) subjecting at least a part of the gas resulting from step (c) to conversion using a nickel based catalyst comprising at most 0.2 wt % cobalt, at most 0.2 wt % iron and at most 0.2 wt % ruthenium, calculated on the total weight of the catalyst; and,(e) preparing a hydrogen comprising gas from at least a part of the gas resulting from step (d) using a reforming process.10. The method of claim 9 , wherein the steam/off-gas mol ratio in step (c) is in the range of between 0.7 and 1.5.11. The method of claim 9 , wherein the steam/off-gas mol ratio in step (c) is in the range of between 0.8 and 1.2.12. The method of claim ...

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10-01-2019 дата публикации

CATALYSTS FOR PETROCHEMICAL CATALYSIS

Номер: US20190010096A1
Принадлежит:

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

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03-02-2022 дата публикации

Catalyst for dehydration reaction of primary alcohols, method for preparing the same and method for preparing alpha-olefins using the same

Номер: US20220032272A1
Принадлежит: Korea Institute of Energy Research KIER

Provided are a catalyst for dehydration reaction of a primary alcohol, a method for preparing the same, and a method for preparing alpha-olefins using the same. According to the present invention, there is provided a catalyst for dehydration reaction of primary alcohols capable of adjusting the strength and distribution of Lewis acid sites (LASs) on a surface of an alumina catalyst to realize high selectivity to alpha-olefins as well as a high conversion rate in the dehydration reaction of primary alcohols. Therefore, high-purity alpha-olefins having a low isomeric yield fraction as well as a high conversion rate can be produced from the primary alcohols.

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19-01-2017 дата публикации

Silver Promoted Catalysts for Oxidative Coupling of Methane

Номер: US20170014807A1
Принадлежит:

An oxidative coupling of methane (OCM) catalyst composition comprising one or more oxides doped with Ag; wherein one or more oxides comprises a single metal oxide, mixtures of single metal oxides, a mixed metal oxide, mixtures of mixed metal oxides, or combinations thereof; and wherein one or more oxides is not LaOalone. A method of making an OCM catalyst composition comprising calcining one or more oxides and/or oxide precursors to form one or more calcined oxides, wherein the one or more oxides comprises a single metal oxide, mixtures of single metal oxides, a mixed metal oxide, mixtures of mixed metal oxides, or combinations thereof, wherein the one or more oxides is not LaOalone, and wherein the oxide precursors comprise oxides, nitrates, carbonates, hydroxides, or combinations thereof; doping the one or more calcined oxides with Ag to form the OCM catalyst composition; and thermally treating the OCM catalyst composition. 1. An oxidative coupling of methane (OCM) catalyst composition doped with silver (Ag).2. The OCM catalyst composition of claim 1 , wherein the OCM catalyst composition comprises one or more oxides doped with silver (Ag); wherein the one or more oxides comprises a single metal oxide claim 1 , mixtures of single metal oxides claim 1 , a mixed metal oxide claim 1 , mixtures of mixed metal oxides claim 1 , or combinations thereof; and wherein the one or more oxides is not LaOalone.3. The OCM catalyst composition of claim 2 , wherein the single metal oxide comprises one metal cation selected from the group consisting of alkali metal cations claim 2 , alkaline earth metal cations claim 2 , rare earth element cations claim 2 , and cations of elements that can form oxides with redox properties.4. The OCM catalyst composition of claim 2 , wherein the mixed metal oxide comprises two or more different metal cations claim 2 , wherein each metal cation can be independently selected from the group consisting of alkali metal cations claim 2 , alkaline earth ...

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18-01-2018 дата публикации

USE OF METAL-ACCUMULATING PLANTS FOR THE PREPARATION OF CATALYSTS THAT CAN BE USED IN CHEMICAL REACTIONS

Номер: US20180015317A1
Принадлежит:

A method of implementing organic synthesis reactions uses a composition containing a metal catalyst originating from a calcined plant. The plants can be from the Brassicaceae, Sapotaceae and Convolvulaceae family, and the metal catalyst contains metal in the M(II) form such as zinc, nickel, manganese, lead, cadmium, calcium, magnesium or copper. Examples of the organic synthesis reactions include halogenations, electrophilic reactions, cycloadditions, transesterification reactions and coupling reactions, among others. 1. A method for the implementation of an organic synthesis reaction , comprising: [{'sup': 2+', '2+', '3+', '+', '+, 'wherein said at least one metal in the M(II) form is selected from the group consisting of zinc (Zn), nickel (Ni), and manganese (Mn), said metal in the M(II) form having been accumulated by the plant during its growth in a soil containing said metal and at least one cationic species selected from the group consisting of MgCa, Fe, Na and K which have not been accumulated by said plant but are physiologically present in said plant and originate from the latter; and'}, 'bringing the composition into contact with at least one chemical compound capable of reacting with said composition., 'providing a composition comprising at least one metal catalyst containing a metal in the M(II) form, said metal originating from a calcined plant or calcined plant part, said composition having been acid treated,'}2. The method according to claim 1 , wherein the organic synthesis reaction is selected from halogenations claim 1 , electrophilic aromatic reactions in series claim 1 , synthesis of 3 claim 1 ,4-dihydropyrimidin-2(1H)-one or 3 claim 1 ,4-dihydropyrimidin-2(1H)-thione claim 1 , cycloaddition reactions claim 1 , transesterification reactions claim 1 , catalyst synthesis reactions for coupling or hydrogenation reactions after reduction of Ni(II) to Ni(0) claim 1 , synthesis of amino acid or oxime developers claim 1 , and hydrolysis of sulphur- ...

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18-01-2018 дата публикации

Method for producing conjugated diolefin

Номер: US20180016208A1
Принадлежит: Asahi Kasei Chemicals Corp

A method for producing a conjugated diolefin is configured as follows. A monoolefin having four or more carbon atoms is fed from a monoolefin feed nozzle(s) installed at n place(s) (n=1, 2, . . . , n). In addition, at least 50% or more of a total amount of an oxygen-containing gas is fed from an oxygen-containing gas feed nozzle located at a bottom of a fluidized bed reactor. Furthermore, the monoolefin feed nozzles at distances a1, a2, . . . , an from the oxygen-containing gas feed nozzle feed the monoolefin having four or more carbon atoms at ratios of b1, b2, . . . , bn (b1+b2+ . . . +bn=1), respectively, and an arithmetic mean value represented by the following formula and obtained from the above distances and the above ratios is 100 mm or more. arithmetic mean value= a 1* b 1+ a 2* b 2+ . . . + an*bn

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16-01-2020 дата публикации

CATALYSTS FOR NATURAL GAS PROCESSES

Номер: US20200016580A1
Принадлежит:

Catalysts, catalytic forms and formulations, and catalytic methods are provided. The catalysts and catalytic forms and formulations are useful in a variety of catalytic reactions, for example, the oxidative coupling of methane. Related methods for use and manufacture of the same are also disclosed. 138-. (canceled)39. A catalytic material comprising:(a) an OCM active catalyst; and {'br': None, 'sub': a', 'b', 'x', 'y, 'Ln1Ln2O(OH)'}, '(b) a second catalyst comprising the following formulawherein:Ln1 and Ln2 are each independently different lanthanide elements;O is oxygen;OH is hydroxy;a is a number greater than 0; andb, x and y are each independently numbers of 0 or greater, provided that at least one of x or y is greater than 0, andwherein the catalytic material comprises a methane conversion of greater than 20% and a C2 selectivity of greater than 50% when the catalytic material is employed as a heterogeneous catalyst in the oxidative coupling of methane at a temperatures ranging from about 550° C. to about 750° C.40. The catalytic material of claim 39 , wherein b and x are each independently numbers greater than 0 claim 39 , and y is 0.41. The catalytic material of claim 39 , wherein the OCM active catalyst is a bulk catalyst and the second catalyst is a nanostructured catalyst.42. The catalytic material of claim 39 , wherein the OCM active catalyst is a nanostructured catalyst.43. The catalytic material of claim 42 , wherein the OCM active catalyst is a nanowire catalyst.44. The catalytic material of claim 39 , wherein the second catalyst comprises a nanostructured catalyst comprising a lanthanum/neodymium oxide claim 39 , a lanthanum/cerium oxide claim 39 , a neodymium/cerium oxide claim 39 , a lanthanum/samarium oxide claim 39 , a neodymium/samarium oxide claim 39 , a europium/neodymium oxide claim 39 , a lanthanum/erbium oxide claim 39 , a neodymium/erbium oxide claim 39 , or a europium/lanthanum oxide.45. The catalytic material of claim 39 , wherein the ...

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21-01-2021 дата публикации

POROUS FORMED BODY AND PRODUCTION METHOD THEREOF, alpha-OLEFIN DIMERIZATION CATALYST AND PRODUCTION METHOD THEREOF, AND METHOD OF PRODUCING alpha-OLEFIN DIMER

Номер: US20210016248A1
Принадлежит:

A porous formed body (Y) including a porous formed body (X) that satisfies the following (x-1) to (x-3), and an alkali metal carbonate or an alkali metal bicarbonate, in which a content of the alkali metal carbonate or the alkali metal bicarbonate is in a range of from 1 part by mass to 230 parts by mass, with respect to 100 parts by mass of the porous formed body (X), and a production method thereof, an α-olefin dimerization catalyst and a production method thereof, and a method of producing an α-olefin dimer: 1. A porous formed body (Y) , comprising:a porous formed body (X) that satisfies the following requirements (x-1) to (x-3); andan alkali metal carbonate or an alkali metal bicarbonate,wherein a content of the alkali metal carbonate or the alkali metal bicarbonate is in a range of from 1 part by mass to 230 parts by mass, with respect to 100 parts by mass of the porous formed body (X):requirement (x-1): a volume of pores with a pore diameter in a range of from 0.01 μm to 100 μm is from 0.10 mL/g to 1.00 mL/g;requirement (x-2): a median pore diameter of pores with a pore diameter in a range of from 0.01 μm to 100 μm is from more than 0.01 μm to 10.0 μm; andrequirement (x-3): a crushing strength is from 0.7 kgf to 15.0 kgf.2. The porous formed body (Y) according to claim 1 , wherein the porous formed body (X) further satisfies the following requirement (x-4):requirement (x-4): the porous formed body (X) contains at least one compound selected from the group consisting of an oxide of a metal or a rare earth element and a complex oxide thereof, zeolite, activated carbon, and SiC.3. The porous formed body (Y) according to claim 1 , wherein the alkali metal carbonate or the alkali metal bicarbonate is at least one compound selected from the group consisting of NaCO claim 1 , NaHCO claim 1 , KCO claim 1 , and KHCO.4. The porous formed body (Y) according to claim 1 , wherein the porous formed body (Y) has a volume of pores with a pore diameter in a range of from 0.01 ...

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16-01-2020 дата публикации

MIXED OXIDE CATALYST FOR THE OXIDATIVE COUPLING OF METHANE

Номер: US20200017424A1
Принадлежит: SABIC Global Technologies, B.V.

A mixed oxide catalyst for the oxidative coupling of methane can include a catalyst with the formula ABCDO, wherein: element A is selected from alkaline earth metals; elements B and C are selected from rare earth metals, and wherein elements B and C are different rare earth metals; the oxide of at least one of A, B, C, and D has basic properties; the oxide of at least one of A, B, C, and D has redox properties; and elements A, B, C, and D are selected to create a synergistic effect whereby the catalytic material provides a methane conversion of greater than or equal to 15% and a C selectivity of greater than or equal to 70%. Systems and methods can include contacting the catalyst with methane and oxygen and purifying or collecting C products. 1. A catalytic material for oxidative coupling of methane comprising:{'sub': a', 'b', 'c', 'd', 'x, 'claim-text': element A is selected from alkaline earth metals;', 'elements B and C are selected from rare earth metals, and wherein elements B and C are different rare earth metals;', 'the oxide of at least one of A, B, C, and D has basic properties;', 'the oxide of at least one of A, B, C, and D has redox properties; and', {'sub': '2', 'sup': '−', 'elements A, B, C, and D are selected to create a synergistic effect whereby the catalytic material provides a methane conversion of greater than or equal to 15% and a C selectivity of greater than or equal to 70%.'}], 'a catalyst with the formula ABCDO, wherein2. The catalytic material according to claim 1 , wherein: =1.0; claim 1 , claim 1 , and are each in the range from about 0.01 to about 10; and is a number selected to balance the oxidation state of D.3. The catalytic material according to claim 1 , wherein element A is selected from the group consisting of magnesium claim 1 , calcium claim 1 , strontium claim 1 , and barium.4. The catalytic material according to claim 1 , wherein elements B and C are selected from the group consisting of cerium claim 1 , ytterbium claim 1 , ...

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16-01-2020 дата публикации

METHODS FOR MAKING LIGHT OLEFINS FROM DIFFERENT FEED STREAMS

Номер: US20200017427A1
Автор: Pretz Matthew T.
Принадлежит: Dow Global Technologies LLC

According to one or more embodiments of the present disclosure, chemical streams may be processed by a method which may comprise operating a first chemical process, stopping the first chemical process and removing the first catalyst from the reactor, and operating a second chemical process. The reaction of the first chemical process may be a dehydrogenation reaction, a cracking reaction, a dehydration reaction, or a methanol-to-olefin reaction. The reaction of the second chemical process may be a dehydrogenation reaction, a cracking reaction, a dehydration reaction, or a methanol-to-olefin reaction. The first reaction and the second reaction may be different types of reactions. 2. The method of claim 1 , wherein the first product stream and the second product stream comprise one or more of ethylene claim 1 , propylene claim 1 , or butene.3. The method of claim 1 , wherein the first reaction or the second reaction is a dehydrogenation reaction claim 1 , and the first catalyst or the second catalyst comprises gallium claim 1 , platinum claim 1 , or both.4. The method of claim 1 , wherein:the first reaction or the second reaction is a dehydrogenation reaction; andthe first feed stream or the second feed stream comprises one or more of ethane, propane, n-butane, and i-butane.5. The method of claim 1 , wherein the first reaction or the second reaction is a cracking reaction claim 1 , and the first catalyst or the second catalyst comprises one or more zeolites.6. The method of claim 1 , wherein:the first reaction or the second reaction is a cracking reaction; andthe first feed stream or the second feed stream comprises one or more of naphtha, n-butane, or i-butane.7. The method of claim 1 , wherein the first reaction or the second reaction is a dehydration reaction claim 1 , and the first catalyst or second catalyst comprises one or more acid catalysts.8. The method of claim 1 , wherein:the first reaction or the second reaction is a dehydration reaction;the first feed ...

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16-01-2020 дата публикации

PROCESS TO CONVERT SYNTHESIS GAS TO OLEFINS USING A BIFUNCTIONAL CHROMIUM/ZINC OXIDE-SAPO-34 CATALYST

Номер: US20200017774A1
Принадлежит: Dow Global Technologies LLC

A process for preparing Cto Colefins includes introducing a feed stream having a volumetric ratio of hydrogen to carbon monoxide from greater than 0.5:1 to less than 5:1 into a reactor, and contacting the feed stream with a bifunctional catalyst. The bifunctional catalyst includes a Cr/Zn oxide methanol synthesis component having a Cr to Zn molar ratio from greater than 1.0:1 to less than 2.15:1, and a SAPO-34 silicoaluminophosphate microporous crystalline material. The reactor operates at a temperature ranging from 350° C. to 450° C., and a pressure ranging from 10 bar (1.0 MPa) to 60 bar (6.0 MPa). The process has a cumulative productivity of Cto Colefins greater than 15 kg Cto Colefins/kg catalyst. 1. A process for preparing Cto Colefins , comprising:introducing a feed stream into a reactor, wherein the feed stream comprises hydrogen gas and carbon monoxide gas, such that a volumetric ratio of hydrogen to carbon monoxide ranges from greater than 0.5:1 to less than 5:1; andcontacting the feed stream with a bifunctional catalyst in the reactor, wherein the bifunctional catalyst comprises: (1) Cr/Zn oxide methanol synthesis component having a Cr to Zn molar ratio from greater than 1.0:1 to less than 2.15:1, and (2) a SAPO-34 silicoaluminophosphate microporous crystalline material, (a) a reactor temperature ranging from 350° C. to 450° C.; and', '(b) a pressure ranging from 10 bar (1.0 MPa) to 60 bar (6.0 MPa), and, 'wherein the reactor operates at reaction conditions comprising{'sub': 2', '3', '2', '3, 'wherein the process has a cumulative productivity of Cto Colefins greater than 15 kg Cto Colefins/kg catalyst.'}2. The process for preparing Cto Colefins according to claim 1 , wherein the Cr to Zn molar ratio is at least 1.1:1.3. The process for preparing Cto Colefins according to claim 1 , wherein the Cr to Zn molar ratio is at least 1.5:1.4. The process for preparing Cto Colefins according to claim 1 , wherein the reaction conditions comprises a pressure greater ...

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28-01-2016 дата публикации

OLEFIN CONVERSION PROCESS

Номер: US20160023964A1
Принадлежит: LUMMUS TECHNOLOGY INC.

A process for the production of Colefins, which may include: contacting a hydrocarbon mixture comprising alpha-pentenes with an isomerization catalyst to form an isomerization product comprising beta-pentenes; contacting ethylene and the beta-pentenes with a first metathesis catalyst to form a first metathesis product comprising butenes and propylene, as well as any unreacted ethylene and Colefins; and fractionating the first metathesis product to for an ethylene fraction, a propylene fraction, a butene fraction, and a Cfraction. 1. A system for the production of Colefins , the system comprising:an isomerization reaction zone for contacting a hydrocarbon mixture comprising alpha-pentenes with an isomerization catalyst to form an isomerization product comprising beta-pentenes;{'sub': '5', 'a first metathesis reaction zone for contacting ethylene and the beta-pentenes with a first metathesis catalyst to form a first metathesis product comprising butenes and propylene, as well as any unreacted ethylene and Colefins;'}{'sub': '5', 'a separation system for fractionating the first metathesis product to form an ethylene fraction, a propylene fraction, a butene fraction, and a Cfraction; and'}a second metathesis reaction zone for contacting the propylene with a second metathesis catalyst, which may be the same or different than the first metathesis catalyst, to convert at least a portion of the propylene to ethylene and 2-butene and form a second metathesis product.2. The system of claim 1 , further comprising a flow conduit for feeding the first metathesis product and the second metathesis product to a common fractionation system.3. The system of claim 2 , further comprising a flow conduit for withdrawing a propylene product stream.4. The system of claim 3 , further comprising a control system for adjusting a rate of withdrawing the propylene product stream to produce a selected ratio of butene to propylene product.5. The system of claim 1 , further comprising one or more ...

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26-01-2017 дата публикации

Ethanol Production via Dimethylether Recycle

Номер: US20170022129A1
Принадлежит: ExxonMobil Chemical Patents Inc

This invention relates to a process for producing ethanol comprises supplying a feed comprising carbon monoxide, hydrogen and dimethyl ether to a reaction zone operated under conditions such that (i) part of the carbon monoxide in the feed reacts with part of the hydrogen in the feed to produce methanol; (ii) part of the carbon monoxide in the feed reacts with at least part of the dimethyl ether in the feed to produce methyl acetate; and (iii) part of the hydrogen in the feed reacts with at least part of the methyl acetate produced in (ii) to produce an effluent comprising methanol and ethanol. At least part of the ethanol is recovered from the effluent and at least part of the methanol is dehydrated to produce dimethyl ether, which is recycled to the reaction zone.

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24-01-2019 дата публикации

HETEROGENEOUS CATALYSTS

Номер: US20190022626A1
Принадлежит:

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

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23-01-2020 дата публикации

CATALYTIC FORMS AND FORMULATIONS

Номер: US20200024214A1
Принадлежит:

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

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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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17-02-2022 дата публикации

METHODS, SYSTEMS, AND CATALYSTS FOR THE DIRECT CONVERSION OF SYNGAS TO HIGH-OCTANE HYDROCARBONS

Номер: US20220048834A1
Принадлежит:

The present disclosure relates to a method that includes converting a gas stream that contains hydrogen (H) and carbon monoxide (CO) to a second mixture that contains a hydrocarbon, for example, a hydrocarbon having between 3 and 15 carbon atoms, where the converting is performed using a first catalyst configured to convert Hand CO to methanol, a second catalyst configured to convert methanol to dimethyl ether (DME), and a third catalyst configured to convert DME to the hydrocarbon. 1. A method comprising:{'sub': '2', 'converting a gas stream comprising hydrogen (H) and carbon monoxide (CO) to a second mixture comprising a hydrocarbon having between 3 and 15 carbon atoms, wherein{'sub': '2', 'the converting is performed using a first catalyst configured to convert Hand CO to methanol,'}a second catalyst configured to convert methanol to dimethyl ether (DME), anda third catalyst configured to convert DME to the hydrocarbon.2. The method of claim 1 , wherein the first catalyst comprises copper and a zinc oxide.3. The method of claim 2 , wherein the first catalyst further comprises at least one of silica claim 2 , alumina claim 2 , zirconia claim 2 , or ceria.4. The method of claim 1 , wherein the second catalyst comprises at least one of an alumina or silica.5. The method of claim 1 , wherein the third catalyst comprises at least one of copper or a zeolite.6. The method of claim 5 , wherein the zeolite comprises a beta zeolite having a silica to alumina ratio between about 20:1 and about 300:1.7. The method of claim 6 , wherein the copper in the third catalyst is present at a concentration between about 1 wt % and about 20 wt % claim 6 , relative to the total weight of the third catalyst.8. The method of claim 1 , wherein the first catalyst and the second catalyst are present at a ratio between about 1:1 and about 8:1.9. The method of claim 8 , wherein the second catalyst and the third catalyst are present at a ratio between about 0.1:1 and about 5:2.10. The method of ...

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30-01-2020 дата публикации

FUNCTIONALIZED BORON NITRIDE CATALYSTS FOR THE PRODUCTION OF LIGHT OLEFINS FROM ALKANE FEEDS VIA OXIDATIVE DEHYDROGENATION

Номер: US20200030781A1
Принадлежит:

Disclosed is a catalyst comprising: a composition having a formula BNMOwherein B represents boron, N represents nitrogen, M comprises a metal or metalloid, and O represents oxygen, x ranges from 0 to 1, y ranges from 0.01 to 5.5; and z ranges from 0 to 16.5. The catalyst may be suitable for converting alkanes to olefins. 1. A catalyst comprising: {'br': None, 'sub': x', 'y', 'z, 'BNMO'}, 'a composition having a formula'} B represents boron, N represents nitrogen, M is platinum, silver, lanthanum, tin, cerium, zirconium, titanium, tin, strontium, magnesium, tungsten, copper, gallium, lithium, sodium, cesium, calcium, manganese, zinc, lead, barium, gallium, yttrium, ytterbium, silicon, cesium, germanium, niobium, vanadium, chromium, molybdenum, rhenium, or a combination thereof, and O represents oxygen,', 'x ranges from 0 to 1,', 'y ranges from 0.01 to 5.5; and', 'z ranges from 0 to 16.5., 'wherein'}2. The catalyst of claim 1 , wherein x ranges from 0.01 to 1.3. The catalyst of claim 1 , wherein x ranges from 0.9 to 1.4. The catalyst of claim 3 , wherein y and z range from 0.01 to 0.06.5. The catalyst of claim 4 , wherein y and z are 0.06.6. The catalyst of claim 5 , wherein x is equal to 1 and boron is present as a component of boron nitride.7. The catalyst of claim 3 , wherein y and z are equal.8. The catalyst of claim 3 , wherein M and O is speciated as magnesium oxide.9. The catalyst of claim 3 , wherein M is strontium and M and O is speciated as strontium oxide.10. The catalyst of claim 6 , wherein boron nitride is present as hexagonal boron nitride.11. The catalyst of claim 6 , wherein boron nitride is present as cubic claim 6 , wurtzitic claim 6 , or amorphous boron nitride.12. The catalyst of claim 3 , further comprising a support.13. The catalyst of claim 12 , wherein the catalyst is suitable for converting an alkane to an olefin and wherein the olefin comprises ethylene claim 12 , propylene claim 12 , butylene claim 12 , isobutene claim 12 , or a combination ...

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31-01-2019 дата публикации

Catalyst and method for synthesis of aromatic hydrocarbons through direct conversion of synthesis gas

Номер: US20190031575A1

Synthesis of aromatic hydrocarbons from synthesis gas in a fixed bed or a moving bed reactor loaded with a composite catalyst comprising Catalyst Component A and Catalyst Component B mixed via a mechanical mixing mode, wherein the active ingredient of the Catalyst Component A is active metal oxides; and the Catalyst Component B is one or both of ZSM-5 zeolite and metal modified ZSM-5; the pressure of the synthesis gas is 0.1-6 MPa; the reaction temperature is 300-600° C.; and the space velocity is 500-8000 h−1. The reaction process has a high product yield and selectivity, with the selectivity of aromatics reaching 50-85%, while the selectivity of the methane byproduct is less than 15%.

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31-01-2019 дата публикации

A Process for Preparing Perhydrofluorene or Alkyl-Substituted Perhydrofluorene

Номер: US20190031576A1
Принадлежит: TIANJIN UNIVERSITY

The present invention discloses a process for preparing perhydrofluorene or alkyl-substituted perhydrofluorene, comprising the steps of: (1) reacting a phenolic compound or an aromatic hydrocarbon compound or an aromatic ketone compound or an aromatic ether compound with a benzyl compound to carry out an alkylation reaction in the presence of a first catalyst, thereby to produce substituted or unsubstituted diphenyl methane, wherein the first catalyst is an acidic catalyst; and (2) reacting the substituted or unsubstituted diphenyl methane with hydrogen gas to carry out an hydrogenation reaction or a hydrodeoxygenation reaction, thereby to produce perhydrofluorene or alkyl-substituted perhydrofluorene, wherein the second catalyst is a physical mixture of a metal catalyst and an acidic catalyst or a metal catalyst loaded on an acidic catalyst.

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11-02-2016 дата публикации

METHOD FOR PRODUCING METHACRYLIC ACID ESTER

Номер: US20160039738A1
Принадлежит: Sumitomo Chemical Company, Limited

Production of methacrylic acid ester comprising a step of having acetone undergo a dehydration reaction in the presence of a dehydration reaction catalyst to obtain a reaction mixture; a step of separating a mixture containing propyne and propadiene as main components from the obtained reaction mixture; a step of separating the separated mixture containing propyne and propadiene as main components into a liquid, gas, or gas-liquid mixture containing propyne as a main component, and a liquid, gas, or gas-liquid mixture containing propadiene as a main component; and a step of bringing the obtained liquid, gas, or gas-liquid mixture containing propyne as a main component into contact with carbon monoxide and an alcohol having 1 to 3 carbon atoms in the presence of a catalyst containing at least one selected from the group consisting of Group 8 metal elements, Group 9 metal elements, and Group 10 metal elements. 1. A method for producing a methacrylic acid ester , which comprises the following steps:a dehydration reaction step: a step of having acetone undergo a dehydration reaction in the presence of a dehydration reaction catalyst to obtain a reaction mixture containing propyne, propadiene, and water;a propyne/propadiene separation step: a step of separating a mixture containing propyne and propadiene as main components from the reaction mixture obtained in the dehydration reaction step;a propyne purification step: a step of separating the mixture containing propyne and propadiene as main components separated in the propyne/propadiene separation step into a liquid, gas, or gas-liquid mixture containing propyne as a main component, and a liquid, gas, or gas-liquid mixture containing propadiene as a main component; anda carbonylation reaction step: a step of bringing the liquid, gas, or gas-liquid mixture containing propyne as a main component obtained in the propyne purification step into contact with carbon monoxide and an alcohol having 1 to 3 carbon atoms in the ...

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24-02-2022 дата публикации

METHOD OF METHYL CYCLOPENTENE PRODUCTION FROM CYCLOHEXENE OVER ZEOLITE-BASED CATALYST STRUCTURE

Номер: US20220055971A1
Автор: Li Zhaofei, Song Hua, Xu Hao
Принадлежит:

Selective conversion from cyclohexene to methylcyclopentene can occur via skeletal isomerization reaction under mild temperature and near atmospheric pressure with the existence of a catalyst structure as described herein. The catalyst structure includes a porous zeolite as the support and one or more loaded metals to further modify its acidity and pore structures. Industrially available cyclohexene feedstock can be effectively converted to a high value-added product methylcyclopentene with over 90 wt % conversion and 95 wt % selectivity, which is highly profitable for potential application in the fine chemical industry. 1. A method for producing methylcyclopentene from cyclohexene via skeletal isomerization , the method comprising:reacting cyclohexene within a reactor in the presence of a gas atmosphere and a catalyst structure, wherein the catalyst structure comprises a porous support structure and one or more metals loaded in the porous support structure, the porous support structure comprises an aluminosilicate material, and the one or more metals loaded in the porous support structure is selected from the group consisting of Na, K, Co, Mo, Ag, Ga and Ce.2. The method of claim 1 , wherein the porous support structure includes Co and/or Mo.3. The method of claim 1 , wherein the gas atmosphere comprises a pure gas or a mixture of two or more gases selected from the group consisting of nitrogen claim 1 , helium claim 1 , methane claim 1 , and argon.4. The method of claim 1 , wherein the aluminosilicate material is selected from the group consisting of HZSM-5 type zeolite claim 1 , L-type zeolite claim 1 , HX type zeolite claim 1 , and HY type zeolite.5. The method of claim 1 , wherein each metal loaded in the porous support structure is present in an amount from 0.1 wt % to 20 wt % by weight of the catalyst support structure.6. The method of claim 5 , wherein the one or more metal components is loaded in the porous support structure as one or more salts selected ...

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18-02-2016 дата публикации

PROCESS FOR PREPARATION OF N-PROPYL BENZENE

Номер: US20160046543A1
Принадлежит:

Disclosed is a process for preparation of n-propyl benzene. The process gives high selectivity and yield of n-propyl benzene by single step catalytic alkylation that involves contacting a mixture of aromatic hydrocarbon having an active hydrogen on a saturated α-carbon, such as toluene, and an alkene, such as ethylene, in presence of a metal catalyst, a solid support, and an initiator. Following the alkylation, aqueous and organic phases are separated from a reaction mixture. The aqueous phase is separated for recovery of the catalyst, the solid support, and un-reacted aromatic hydrocarbon (e.g., toluene); and the organic phase is separated for obtaining n-propyl benzene and byproduct. Thus, the catalyst phase can be recovered and recycled in the next alkylation reaction. Also, the process facilitates recovery and recycling of the byproduct for the better selectivity. 1. A process for the preparation of n-propyl benzene , the process comprising the steps of:(a) adding an aromatic hydrocarbon that has an active hydrogen on a saturated α-carbon, and a solid support, to a first reactor to form a mixture;(b) adding an alkali metal catalyst and oleic acid to the mixture to form a reaction mass, and closing and agitating the first reactor for a time period of about 30 minutes to about 1 hour;(c) flushing nitrogen gas into the first reactor, and heating the reaction mass at a temperature to a range of about 185° C. to about 190° C. for about 15 minutes;(d) adding an aromatic hydrocarbon and an initiator to a second reactor, flushing the second reactor with nitrogen gas, and stirring for a time period of about 15 minutes to about 30 minutes, after which the second reactor is connected to the first reactor;(e) adding alkene to the first reactor to form a reaction mixture;(f) adding periodically an amount of initiator to the first reactor, and maintaining the reaction mixture at temperature in a range of about 180° C. to about 220° C. for at least 1 hour to 5 hours while ...

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15-02-2018 дата публикации

Catalytic composition and process for the dehydrogenation of butenes or mixtures of butanes and butenes to give 1,3-butadiene

Номер: US20180043338A1
Принадлежит: Versalis Spa

The present invention relates to a dehydrogenation process starting from reagents selected from single butenes, or mixtures thereof, or mixtures of butenes with butanes, to give 1-3 butadiene using catalytic composition of microspheroidal alumina and an active component containing a mixture comprising Gallium and/or Gallium oxides, Tin and/or Tin oxides, a quantity ranging from 1 ppm to 500 ppm with respect to the total weight of the catalytic composition of platinum and/or platinum oxides, and oxides of alkaline and/or alkaline earth metals.

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19-02-2015 дата публикации

Method of Forming a Catalyst with an Ion-Modified Binder

Номер: US20150051063A1
Принадлежит: Fina Technology Inc

An alkylation catalyst having a zeolite catalyst component and a binder component providing mechanical support for the zeolite catalyst component is disclosed. The binder component is an ion-modified binder that can include metal ions selected from the group consisting of Co, Mn, Ti, Zr, V, Nb, K, Cs, Ga, B, P, Rb, Ag, Na, Cu, Mg, Fe, Mo, Ce, and combinations thereof The metal ions reduce the number of acid sites on the zeolite catalyst component. The metal ions can range from 0.1 to 50 wt % based on the total weight of the ion-modified binder. Optionally, the ion-modified binder is present in amounts ranging from 1 to 80 wt % based on the total weight of the catalyst.

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03-03-2022 дата публикации

AROMATIZATION OF LIGHT HYDROCARBONS USING METAL-DOPED ZEOLITE CATALYSTS WITH ENHANCED MESOPOROSITY

Номер: US20220064082A1
Принадлежит:

According to embodiments, a process for aromatizing hydrocarbons may include contacting the hydrocarbons with a zinc- or gallium-doped ZSM-5 catalyst having a mesopore volume of greater than 0.09 cm/g. Contacting the hydrocarbons with the catalyst causes a least a portion of the hydrocarbons to undergo chemical reactions to form aromatic hydrocarbons.

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13-02-2020 дата публикации

STABLE CATALYSTS FOR OXIDATIVE COUPLING OF METHANE

Номер: US20200048164A1
Принадлежит:

A method of selecting a stable mixed metal oxide catalyst for an oxidative coupling of methane (OCM) reaction is disclosed. The method may include, obtaining a mixed metal oxide material having catalytically active metal oxides for the OCM reaction and identifying the Tammann temperature (TTam) of at least one of the catalytically active metals oxides of the mixed metal oxide material. The method further includes selecting the mixed metal oxide material for use as a catalyst in the OCM reaction if the at least one catalytically active metal oxides present in the mixed metal oxide material has a TTam greater than a predetermined temperature. 1. A method of selecting a stable mixed metal oxide catalyst for an oxidative coupling of methane (OCM) reaction , the method comprising:(a) obtaining a mixed metal oxide material having catalytically active metal oxides for the OCM reaction;{'sub': 'Tam', '(b) identifying the Tammann temperature (T) of at least one of the catalytically active metals oxides of the mixed metal oxide material; and'}{'sub': 'Tam', '(c) selecting the mixed metal oxide material for use as a catalyst in the OCM reaction if the at least one catalytically active metal oxides present in the mixed metal oxide material has a Tgreater than 750° C.'}2. The method of claim 1 , wherein the Tfor the at least one catalytically active metal oxide is greater than 850° C. claim 1 , preferably greater than 950° C. claim 1 , or more preferably greater than 1000° C. claim 1 , or 750° C. to 1700° C.3. The method of claim 1 , wherein each of the metal oxides in the mixed metal oxide material has a Tgreater than 750° C.4. The method of claim 1 , wherein the Tof the mixed metal oxide material is above 750° C.5. The method of claim 1 , wherein the mixed metal oxide material has two catalytically active metal oxides having a metal selected from the group consisting of thorium (Th) claim 1 , magnesium (Mg) claim 1 , strontium (Sr) claim 1 , cerium (Ce) claim 1 , ytterbium (Yb ...

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22-02-2018 дата публикации

Diene production method

Номер: US20180050970A1
Принадлежит: JXTG Nippon Oil and Energy Corp

A method for producing diene comprises a step 1 of obtaining a straight chain internal olefin by removing a branched olefin from a raw material including at least the branched olefin and a straight chain olefin; and a step 2 of producing diene from the internal olefin by oxidative dehydrogenation using a first catalyst and a second catalyst, and the first catalyst has a complex oxide including bismuth, molybdenum and oxygen, and the second catalyst includes at least one selected from the group consisting of silica and alumina.

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01-03-2018 дата публикации

REACTIVATING PROPANE DEHYDROGENATION CATALYST

Номер: US20180057422A1
Принадлежит:

Increase propane dehydrogenation activity of a partially deactivated dehydrogenation catalyst by heating the partially deactivated catalyst to a temperature of at least 660° C., conditioning the heated catalyst in an oxygen-containing atmosphere and, optionally, stripping molecular oxygen from the conditioned catalyst. 1. A process for dehydrogenating an alkane , the process comprising:a. placing an alkane in operative contact with a heated alkane dehydrogenation catalyst in a reactor, the alkane dehydrogenation catalyst comprising a Group VIII noble metal and a Group IIIA metal;b. removing from the reactor a partially deactivated catalyst, wherein at least a portion of the partially deactivated catalyst has coke deposited thereon; (1) heating at least a portion of the partially deactivated catalyst in a regenerator to a temperature of at least 660 degrees Celsius using heat at least partially generated by combusting a fuel source, wherein the fuel source is not the coke, said heating yielding a heated, further deactivated dehydrogenation catalyst which has an alkane dehydrogenation activity that is less than that of the partially deactivated catalyst; and', '(2) subjecting at least a portion of the heated, further deactivated catalyst to a conditioning step which comprises maintaining at least a portion of the heated, further deactivated dehydrogenation catalyst at a temperature of at least 660 degrees Celsius while exposing at least a portion of the heated, further deactivated dehydrogenation catalyst to a flow of an oxygen-containing gas for a period of time greater than two minutes to yield an oxygen-containing reactivated dehydrogenation catalyst that has an activity for dehydrogenating alkane that is greater than that of either the partially deactivated catalyst or the heated, further deactivated catalyst., 'c. rejuvenating at least a portion of the partially deactivated catalyst, yielding a rejuvenated dehydrogenation catalyst, by2. The process of claim 1 , ...

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04-03-2021 дата публикации

Catalyst for oxidative dehydrogenation reaction, and method for producing same

Номер: US20210060537A1
Принадлежит: LG Chem Ltd

Provided is a catalyst for an oxidative dehydrogenation reaction that comprises: a porous support; a core portion supported on the porous support and containing a first zinc ferrite-based catalyst; and a shell portion supported on the core portion and containing a second zinc ferrite-based catalyst, in which the first zinc ferrite-based catalyst and the second zinc ferrite-based catalyst are different from each other.

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02-03-2017 дата публикации

SEPARATION OF CATALYST AND INERT HEAT PARTICLE AFTER AROMATIZATION OF A METHANE CONTAINING GAS STREAM

Номер: US20170057887A1
Принадлежит:

Implementations of the disclosed subject matter provide a process for the aromatization of a methane-containing gas stream may include contacting the methane-containing gas stream in a reaction zone comprising an aromatization catalyst particulate and an inert heat carrier particulate under methane-containing gas aromatization reaction conditions to produce a product stream comprising aromatics in the reaction zone. The inert heat carrier particulate may be separated from the aromatization catalyst particulate in a separation zone under separation conditions. The aromatization catalyst particulate may have a first minimum fluidization velocity and the inert heat carrier particulate may have a second minimum fluidization velocity which may be greater than the first minimum fluidization velocity. The ratio of the second minimum fluidization velocity to the first minimum fluidization velocity may be less than 200 and may be more than 15. 1. A process for the aromatization of a methane-containing gas stream comprising:contacting the methane-containing gas stream in a reaction zone comprising an aromatization catalyst particulate and an inert heat carrier particulate under methane-containing gas aromatization reaction conditions to produce a product stream comprising aromatics in the reaction zone;separating the inert heat carrier particulate from the aromatization catalyst particulate in a separation zone under separation conditions;wherein the aromatization catalyst particulate has a first minimum fluidization velocity and the inert heat carrier particulate has a second minimum fluidization velocity, wherein the second minimum fluidization velocity is greater than the first minimum fluidization velocity, and wherein the ratio of the second minimum fluidization velocity to the first minimum fluidization velocity is less than 200 and the ratio of the second minimum fluidization velocity to the first minimum fluidization velocity is more than 15.2. The process of claim 1 ...

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04-03-2021 дата публикации

CONTINUOUS FLOW PROCESSES FOR MAKING BICYCLIC COMPOUNDS

Номер: US20210061730A1
Принадлежит:

Processes for making bicyclic compounds and precursors thereof, and particularly for making [1.1.1]propellane and bicyclo[1.1.1]pentane and derivatives thereof, utilize continuous flow reaction methods and conditions. A continuous process for making [1.1.1]propellane can be conducted under reaction conditions that advantageously minimize clogging of a continuous flow reactor. A continuous flow process can be used to make precursors of [1.1.1]propellane. 1. A continuous flow process for making a bicyclic compound , comprising mixing 1 ,1-dibromo-2 ,2-bis(chloromethyl)cyclopropane with an organometallic reagent in a continuous flow reactor under first reaction conditions selected to (a) react the 1 ,1-dibromo-2 ,2-bis(chloromethyl)cyclopropane with the organometallic reagent to produce [1.1.1]propellane and a salt; and (b) minimize clogging of the continuous flow reactor by the salt.2. The process of claim 1 , wherein the organometallic reagent is selected from the group consisting of n-butyllithium claim 1 , methyllithium claim 1 , methyllithium lithium bromide complex claim 1 , and phenyllithium.3. The process of or claim 1 , wherein the salt comprises LiCl claim 1 , LiBr claim 1 , or both.4. The process of claim 1 , wherein the first reaction conditions comprise mixing a solvent with the 1 claim 1 ,1-dibromo-2 claim 1 ,2-bis(chloromethyl)cyclopropane and the organometallic reagent in the continuous flow reactor claim 1 , wherein the solvent is selected from the group consisting of diethylether claim 1 , diethoxymethane claim 1 , dibutylether claim 1 , methyl tert-butyl ether tetrahydrofuran claim 1 , 2-methyltetrahydrofuran and mixtures thereof.5. The process of claim 1 , wherein the continuous flow reactor comprises a static mixer and wherein the mixing of the 1 claim 1 ,1-dibromo-2 claim 1 ,2-bis(chloromethyl)cyclopropane with an organometallic reagent is conducted with the static mixer at a mixing rate that is effective to minimize clogging of the continuous ...

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04-03-2021 дата публикации

METHOD FOR PRODUCING CARBODIIMIDE COMPOUND

Номер: US20210061756A1
Принадлежит: NISSHINBO CHEMICAL INC.

A method for producing a carbodiimide compound, comprising a carbodiimide production step of reacting an aliphatic tertiary isocyanate compound (A) in the presence of an inorganic alkali metal compound (B) and at least one of a phase transfer catalyst (C), a compound (D-1) represented by general formula (2-1), and a compound (D-2) represented by general formula (2-2). 2. The method for producing a carbodiimide compound according to claim 1 , wherein the aliphatic tertiary isocyanate compound (A) is reacted in the presence of the inorganic alkali metal compound (B) and the phase transfer catalyst (C) in the carbodiimide production step.3. The method for producing a carbodiimide compound according to claim 1 , wherein the method comprises an end-capping step of end-capping a portion of an isocyanate group in the aliphatic tertiary isocyanate compound (A) with an end-capping agent at at least one time point among three time points claim 1 , before the carbodiimide production step claim 1 , during the production step claim 1 , and after the production step claim 1 , and the end-capping agent is the compound (D-1) represented by the general formula (2-1).4. The method for producing a carbodiimide compound according to claim 1 , wherein the method comprises a chain extension step of reacting a portion of an isocyanate group in a carbodiimide obtained by carbodiimidization of the aliphatic tertiary isocyanate compound (A) with a chain extender claim 1 , at at least one time point among three time points claim 1 , before the carbodiimide production step claim 1 , during the production step claim 1 , and after the production step claim 1 , and the chain extender is the compound (D-2) represented by the general formula (2-2).5. The method for producing a carbodiimide compound according to claim 1 , wherein the inorganic alkali metal compound (B) is at least one of MOH claim 1 , MCO claim 1 , MHCO claim 1 , MNO claim 1 , MSO claim 1 , MSHO claim 1 , MF claim 1 , MCl claim 1 , ...

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17-03-2022 дата публикации

Mixed Metal Oxide Catalyst useful for Paraffin Dehydrogenation

Номер: US20220080390A1
Принадлежит:

A catalyst, methods of making, and process of dehydrogenating paraffins utilizing the catalyst. The catalyst includes at least 20 mass % Zn, a catalyst support and a catalyst stabilizer. The catalyst is further characterizable by physical properties such as activity parameter measured under specified conditions. The catalyst may also be disposed on a porous support in an attrition-resistant form and used in a fluidized bed reactor. 1. A mixed metal oxide catalyst suitable for the dehydrogenation of paraffins having 2-8 carbon atoms , comprising a catalyst composition of the general formula (AC) (CS) (ST) whereina) AC (Active Catalyst) represents oxides of zinc (Zn) wherein the catalyst comprises at least 20 mass % Zn,b) CS (Catalyst Support) represents oxides of aluminum (Al), silicon (Si), and titanium (Ti) or mixtures thereof,c) ST (Support Stabilizer) represents oxides of metals selected from the group of cerium (Ce), dysprosium (Dy), erbium (Er), europium (Eu), gadolinium (Gd), lanthanum (La), neodymium (Nd), praseodymium (Pr), samarium (Sm), terbium (Tb), ytterbium (Yb), yttrium (Y), tungsten (W), zirconium (Zr), or mixtures thereof, andcharacterizable by a Activity Parameter >90,000, Selectivity Parameter <0.5 and a stability parameter <0.005 using a test where the mixed metal oxide catalyst is loaded in a fixed-bed reactor such that the 50>dT/dP>10 (diameter of tube to diameter of catalyst particles) and 200>L/dP>50 (length of catalyst bed to diameter of catalyst particles) and 2>dP>0.5 mm exposed to a feed stream of propane at a temperature of 650oC, atmospheric pressure and a feed rate of 10 hr−1 weight hourly space velocity.2. The catalyst composition according to wherein the catalyst is characterizable by an activity parameter of between 90 claim 1 ,000 and about 125 claim 1 ,000 using a test where the mixed metal oxide catalyst is loaded in a fixed-bed reactor such that the 50>dT/dP>10 (diameter of tube to diameter of catalyst particles) and 200>L/dP>50 ...

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17-03-2022 дата публикации

CATALYSTS COMPRISING A ZIRCONIA AND GALLIUM OXIDE COMPONENT FOR PRODUCTION OF C2 TO C4 OLEFINS

Номер: US20220080392A1
Принадлежит: Dow Global Technologies LLC

A process for preparing Cto Colefins includes introducing a feed stream comprising hydrogen gas and a carbon-containing gas selected from carbon monoxide, carbon dioxide, and mixtures thereof into a reaction zone of a reactor. The feed stream is converted into a product stream including Cto Colefins in the reaction zone in the presence of the hybrid catalyst. The hybrid catalyst includes a metal oxide catalyst component comprising gallium oxide and phase pure zirconia, and a microporous catalyst component. 1. A process for preparing Cto Colefins comprising:introducing a feed stream comprising hydrogen gas and a carbon-containing gas selected from the group consisting of carbon monoxide, carbon dioxide, and mixtures thereof into a reaction zone of a reactor; and{'sub': 2', '4, 'claim-text': a metal oxide catalyst component comprising gallium oxide and phase pure zirconia; and', 'a microporous catalyst component., 'converting the feed stream into a product stream comprising Cto Colefins in the reaction zone in the presence of a hybrid catalyst, the hybrid catalyst comprising2. The process of claim 1 , wherein the phase pure zirconia comprises crystalline phase pure zirconia.3. The process of claim 1 , wherein the phase pure zirconia comprises monoclinic phase pure zirconia.4. The process of claim 1 , wherein the phase pure zirconia has a BET surface area that is greater than or equal to 40 m/g.5. The process of claim 1 , wherein the phase pure zirconia has a BET surface area that is greater than or equal to 100 m/g.6. The process of claim 1 , wherein the metal oxide catalyst component comprises from greater than 0.0 g gallium per 100 g phase pure zirconia to 30.0 g gallium per 100 g of phase pure zirconia.7. The process of claim 1 , wherein the metal oxide catalyst component comprises from greater than 0.0 g gallium per 100 g phase pure zirconia to 15.0 g gallium per 100 g of phase pure zirconia.8. The process of claim 1 , wherein microporous catalyst component ...

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27-02-2020 дата публикации

METHOD AND DEVICE FOR CARRYING OUT ENDOTHERMIC GAS PHASE-SOLID OR GAS-SOLID REACTIONS

Номер: US20200061565A1
Принадлежит: BASF SE

The present invention relates to a process for conducting endothermic gas phase or gas-solid reactions, wherein the endothermic reaction is conducted in a production phase in a first reactor zone, the production zone, which is at least partly filled with solid particles, where the solid particles are in the form of a fixed bed, of a moving bed and in sections/or in the form of a fluidized bed, and the product-containing gas stream is drawn off from the production zone in the region of the highest temperature level plus/minus 200 K and the product-containing gas stream is guided through a second reactor zone, the heat recycling zone, which at least partly comprises a fixed bed, where the heat from the product-containing gas stream is stored in the fixed bed, and, in the subsequent purge step, a purge gas is guided through the production zone and the heat recycling zone in the same flow direction, and, in a heating zone disposed between the production zone and the heat recycling zone, the heat required for the endothermic reaction is introduced into the product-containing gas stream and into the purge stream or into the purge stream, and then, in a regeneration phase, a gas is passed through the two reactor zones in the reverse flow direction and the production zone is heated up; the present invention further relates to a structured reactor comprising three zones, a production zone containing solid particles, a heating zone and a heat recycling zone containing a fixed bed, wherein the solid particles and the fixed bed consist of different materials. 1: A process for conducting endothermic gas phase or gas-solid reactions , the process comprising:conducting an endothermic reaction in a production step in a first reactor zone, a production zone, which is at least partly filled with solid particles, where the solid particles are in the form of a fixed bed, of a moving bed and in sections or in the form of a fluidized bed, anddrawing off a product-containing gas stream ...

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27-02-2020 дата публикации

ENHANCED OXYGEN TRANSFER AGENT SYSTEMS FOR OXIDATIVE DEHYDROGENATION OF HYDROCARBONS

Номер: US20200062677A1
Принадлежит: EcoCatalytic Inc.

Aspects of the invention relate to enhanced oxygen transfer agent systems and methods of use thereof. According to one aspect, a method for producing olefins from a hydrocarbon feed includes the step of contacting a hydrocarbon feed comprised of one or more alkanes with an oxygen transfer agent at a temperature of 350° C. to 1000° C. The oxygen transfer agent comprising an oxygen-donating chalcogen agent comprised of at least one of S, Se, or Te and a reducible metal oxide. The chalcogen having an oxidation state greater than +2. According to another aspect, a method for producing one or more olefins by partial combustion of a hydrocarbon feed includes partially combusting a hydrocarbon feed comprised of one or more alkanes by contacting the hydrocarbon feed with an oxygen transfer agent comprising CaS0at a temperature of 350° C. to 1000° C. to produce one or more olefins comprising ethylene and coproducing water. 1. A method for producing one or more olefins from a hydrocarbon feed comprised of one or more alkanes , the method comprising:a step of contacting a hydrocarbon feed comprised of one or more alkanes with an oxygen transfer agent at a temperature of 350° C. to 1000° C., wherein the oxygen transfer agent comprises i) an oxygen-donating chalcogen agent comprised of at least one of S, Se, or Te, and wherein the chalcogen has an oxidation state greater than +2, and ii) a reducible metal oxide.2. The method of claim 1 , wherein the hydrocarbon feed comprises at least one of methane or ethane claim 1 , and the produced one or more olefins comprises ethylene.3. The method of claim 1 , wherein water is produced as a co-product.4. The method of claim 3 , wherein the co-product water is formed from oxygen donated by the oxygen transfer agent.5. The method of claim 1 , wherein the oxygen transfer agent comprises MgMnOand at least one promoter selected from the group consisting of Sm claim 1 , Ga claim 1 , Ti claim 1 , W claim 1 , Mo claim 1 , V claim 1 , Nb claim 1 , ...

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11-03-2021 дата публикации

METHODS TO PRODUCE ZEOLITES WITH THE GME TOPOLOGY AND COMPOSITIONS DERIVED THEREFROM

Номер: US20210069682A1
Принадлежит:

The present disclosure is directed to microporous crystalline aluminosilicate structures with GME topologies having pores containing organic structure directing agents (OSDAs) comprising at least one piperidinium cation, the compositions useful for making these structures, and methods of using these structures. In some embodiments, the crystalline zeolite structures have a molar ratio of Si:Al that is greater than 3.5. 2. The crystalline microporous aluminosilicate composition of claim 1 , having a molar ratio of Si:Al that is greater than 3.5 to about 100.3. The crystalline microporous aluminosilicate composition of claim 1 , that exhibits one or more of:{'figref': [{'@idref': 'DRAWINGS', 'FIG. 3'}, {'@idref': 'DRAWINGS', 'FIG. 6'}, {'@idref': 'DRAWINGS', 'FIG. 7'}, {'@idref': 'DRAWINGS', 'FIG. 13'}], '(a) an XRD diffraction pattern that is the same as or consistent with any one of those shown in , , , or ;'}{'sup': '29', '(b) an Si MAS spectrum having a plurality of chemical shifts of about −99.1, −104.9 and −110.5 ppm, downfield of a peak corresponding to an external standard of tetramethylsilane;'}{'sup': '29', 'figref': {'@idref': 'DRAWINGS', 'FIG. 13'}, '(c) an Si MAS spectrum that is the same as or consistent with the one shown in ;'}{'sup': '27', 'figref': {'@idref': 'DRAWINGS', 'FIG. 11'}, '(d) an Al MAS NMR spectrum that is the same as or consistent with the one shown in , or'}{'figref': {'@idref': 'DRAWINGS', 'FIG. 4'}, '(e) a thermogravimetric analysis curve that is the same as or consistent with the one shown in ; or'}{'sup': '13', 'figref': {'@idref': 'DRAWINGS', 'FIG. 5'}, '(f) a C CP MAS NMR spectrum that is the same as or consistent with the one shown in .'}6. The crystalline microporous aluminosilicate composition of claim 1 , wherein the at least one isomer of the quaternary piperidinium cation of Formula (I) comprises cis-N claim 1 ,N-dimethyl-3 claim 1 ,5-lupetidinium cation claim 1 , trans-N claim 1 ,N-dimethyl-3 claim 1 ,5-lupetidinium cation ...

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11-03-2021 дата публикации

Multistage Nanoreactor Catalyst and Preparation and Application Thereof

Номер: US20210070672A1
Принадлежит:

The present disclosure discloses a multistage nanoreactor catalyst and preparation and application thereof, belonging to the technical field of synthesis gas conversion. The catalyst consists of a core of an iron-based Fischer-Tropsch catalyst, a transition layer of a porous oxide or porous carbon material, and a shell layer of a molecular sieve having an aromatization function. The molecular sieve of the shell layer can be further modified by a metal element or a non-metal element, and the outer surface of the molecular sieve is further modified by a silicon-oxygen compound to adjust the acidic site on the outer surface and the aperture of the molecular sieve, thereby inhibiting the formation of heavy aromatic hydrocarbons. According to the disclosure, the shell layer molecular sieve with a transition layer and a shell layer containing or not containing auxiliaries, and with or without surface modification can be prepared by the iron-based Fischer-Tropsch catalyst through multiple steps. The catalyst can be used for direct preparation of aromatic compounds, especially light aromatic compounds, from synthesis gas; the selectivity of light aromatic hydrocarbons in hydrocarbons can be 75% or above, and the content in the liquid phase product is not less than 95%; and the catalyst has good stability and good industrial application prospect. 1. A multistage nanoreactor catalyst , comprising a structure of a core , a shell body and a core-shell transition layer; wherein the core layer is an iron-based catalyst having Fischer-Tropsch activity , weight of the core layer being 0.1% to 80% of total weight of the catalyst; wherein the shell body is a molecular sieve , the weight of the shell body being 0.1% to 80% of the total weight of the catalyst; and wherein the core-shell transition layer is a porous oxide or porous carbon material , the weight of the transition layer being 0.01% to 35% of the total weight of the catalyst.2. The multistage nanoreactor catalyst according ...

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12-03-2015 дата публикации

HIGH TEMPERATURE CCR PROCESS WITH INTEGRATED REACTOR BYPASSES

Номер: US20150073189A1
Принадлежит:

A process is presented for increasing the aromatics content in a reformate process stream. The process modifies existing processes to change the operation without changing the reactors or heating units. The process includes bypasses to utilize heating capacity of upstream heating units, and passes the excess capacity of the upstream heating units to downstream process streams. 1. A process for increasing the aromatic content of a hydrocarbon stream , comprising:passing the hydrocarbon stream through a series of reforming reactors and reactor feed heaters, wherein the reactors feed heaters generate a heated stream and at least one of the heated streams is split into a first portion and a second portion, with the first portion passed to a reforming reactor to generate a reforming reactor effluent stream; andwherein the second portion of the heated stream is combined with a downstream reforming reactor effluent stream and the combined stream is passed to a downstream reactor feed heater, to generate a reactor product stream with increased aromatic content.2. The process of wherein the first reactor is operated at a first temperature claim 1 , and the subsequent reactors are operated at a second temperature and the second temperature is greater than the first temperature.3. The process of further comprising:splitting at least one reactor effluent stream into a first portion and a second portion;passing the first portion of the effluent stream with the second portion of the heated stream to a reactor interheater; andcombining the second portion of the effluent stream with a downstream heated feedstream to a downstream reactor.4. The process of wherein the downstream reactor is the next reactor in the series of reactors.5. The process of wherein the downstream reactor is the reactor after the next reactor in the series of reactors.6. The process of wherein the first reaction temperature is between 400° C. and 500° C.7. The process of wherein there are at least two ...

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05-06-2014 дата публикации

Catalyst for use in production of saturated hydrocarbons from synthesis gas

Номер: US20140151265A1

A catalyst composition is provided for use in the conversion of carbon oxide(s) to saturated hydrocarbons. The catalyst composition comprises a carbon oxide(s) conversion catalyst; and a dehydration/hydrogenation catalyst comprising a silicoalumino phosphate (SAPO) molecular sieve and a metal M, for example Pd. In one embodiment, the target saturated hydrocarbons include LPG, the SAPO comprises SAPO-5 and/or SAPO-37.

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17-03-2016 дата публикации

SELECTIVE ALKANE ACTIVATION WITH SINGLE-SITE ATOMS ON AMORPHOUS SUPPORT

Номер: US20160074838A1
Принадлежит: UCHICAGO ARGONNE, LLC

The present invention relates generally to catalysts and methods for use in olefin production. More particularly, the present invention relates to novel amorphously supported single-center, Lewis acid metal ions and use of the same as catalysts. 1. A catalyst for use in olefin production comprising one or more single-atom Lewis acid metal ions on the surface of an amorphous support , wherein said catalyst selectively cleaves C—H bonds over C—C bonds in the conversion of alkenes to alkanes.2. The catalyst of claim 1 , wherein the Lewis acid metal is selected from the group consisting of Fe claim 1 , Co claim 1 , Zn claim 1 , Ni claim 1 , Ti claim 1 , Sc claim 1 , Zr claim 1 , Hf claim 1 , Ce claim 1 , Ta claim 1 , La claim 1 , Ga claim 1 , and the lanthanides.3. The catalyst of claim 2 , wherein the Lewis acid metal is selected from the group consisting of Fe claim 2 , Co claim 2 , Zn claim 2 , and Ga.4. The catalyst of claim 2 , wherein the amorphous support is a refractory oxide.5. The catalyst of claim 4 , wherein the refractory oxide is selected from the group consisting of TiO claim 4 , ZrO claim 4 , CeO claim 4 , AlzO claim 4 , MgO claim 4 , and mixtures of these.6. The catalyst of claim 5 , wherein the amorphous support is a silica support.7. The catalyst of claim 4 , wherein the lewis acid metal ion is tetrahedrally coordinated.8. The catalyst of claim 7 , wherein the catalyst is a heterogeneous claim 7 , single-site Zn(II) catalyst claim 7 , in which the tetrahedrally coordinated Zn(II) ion is bonded to the silica support at 3-membered ring siloxane sites.9. The catalyst of claim 1 , wherein the catalyst is not redox-active.10. The catalyst of claim 1 , wherein the catalyst has a selectivity of greater than 75% for C—H activation.11. The catalyst of claim 1 , wherein the catalyst has a selectivity of greater than 90% for C—H activation.12. The catalyst of claim 1 , wherein the catalyst has a selectivity of greater than 95% for C—H activation.13. The catalyst ...

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17-03-2016 дата публикации

CATALYSTS FOR NATURAL GAS PROCESSES

Номер: US20160074844A1
Принадлежит:

Catalysts, catalytic forms and formulations, and catalytic methods are provided. The catalysts and catalytic forms and formulations are useful in a variety of catalytic reactions, for example, the oxidative coupling of methane. Related methods for use and manufacture of the same are also disclosed. 3. The catalytic material of claim 2 , wherein B is Ba claim 2 , Sr or Ca.4. The catalytic material of claim 2 , wherein A is Ce claim 2 , Ti claim 2 , Zr or Hf.5. The catalytic material of claim 2 , wherein α is greater than 0.6. The catalytic material of claim 5 , wherein the perovskite has the following formula:{'br': None, 'sup': '1', 'sub': α', 'm', 'n', 'p, 'EABO.'}7. The catalytic material of claim 2 , wherein Eis an element from group 2 or group 3 of the periodic table.8. The catalytic material of claim 2 , wherein the perovskite has the formula ABO.9. The catalytic material of claim 1 , wherein the catalyst has the formula Ln1Ln2O(OH).10. The catalytic material of claim 1 , wherein x is greater than zero.11. The catalytic material of claim 9 , wherein b and y are both 0.12. The catalytic material of claim 1 , wherein the catalyst is a nanostructured catalyst.13. The catalytic material of claim 12 , wherein the catalyst is a nanowire catalyst.14. The catalytic material of claim 1 , wherein the catalyst further comprises a dopant selected from one or more elements from groups 2 claim 1 , 6 and the lanthanides.15. The catalytic material of claim 14 , wherein the catalyst further comprises a dopant from each of groups 2 claim 14 , 6 and the lanthanides.16. The catalytic material of claim 14 , wherein the catalyst further comprises a dopant from each of groups 2 and 6.17. A method for performing a catalytic reaction claim 14 , the method comprising contacting a composition comprising a molten salt and a catalyst with a reactant gas claim 14 , thereby converting the reactant gas to a product gas claim 14 , wherein the reaction is oxidative coupling of methane or ...

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24-03-2022 дата публикации

SUPPORTED CORE-SHELL STRUCTURED ZnO CATALYST, AND PREPARATION METHOD AND USE THEREOF

Номер: US20220088573A1
Принадлежит:

The present invention belongs to the technical field of supported catalysts, and discloses a supported core-shell structured ZnO catalyst, and a preparation method and use thereof. With AlOas a support and ZnO as active sites, the catalyst is characteristic of a NiZn@ZnO core-shell structure, which consists of a NiZn alloy core and a ZnO shell The preparation method comprises firstly dissolving Ni(NO).6HO and Zn(NO).6HO in deionized water; then impregnating AlOwith the solution described above, followed by uniform ultrasonic dispersion and complete drying; and finally the obtained solid is calcinated and reduced to obtain the target catalyst, which exhibits high activity, selectivity and stability. The catalyst can be used for the dehydrogenation of light alkanes to alkenes, especially in dehydrogenation of propane to propylene. 1. A supported core-shell structured ZnO catalyst , wherein the catalyst is composed of AlOas a support and ZnO as active sites; a NiZn@ZnO core-shell structure , which consists of a NiZn alloy core and a ZnO shell , is supported on the AlO , denoted as NixZny/AlO , wherein x:y=(1:1)-(1:4) , representing the molar ration of Ni/Zn.2. The supported core-shell structured ZnO catalyst according to claim 1 , wherein the catalyst contains 1%-3% of Ni based on the mass of the AlOsupport.3. The supported core-shell structured ZnO catalyst according to claim 2 , wherein the catalyst contains 0.5%-6% of Ni based on the mass of the AlOsupport.4. The supported core-shell structured ZnO catalyst according to claim 1 , wherein x:y=1:3.5. A method for preparing the supported core-shell structured ZnO catalyst according to claim 1 , wherein the method comprises the following steps:{'sub': ['3', '3', '2', '3', '2', '2'], '#text': '(1) dissolving Ni(NO).6HO and Zn(NO).6HO in deionized water;'}{'sub': ['2', '3'], '#text': '(2) impregnating AlOwith the solution obtained in step (1), followed by uniform ultrasonic dispersion and complete drying; and'}{'sub': ['2 ...

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05-03-2020 дата публикации

HYDROCARBON CONVERSION CATALYST SYSTEM

Номер: US20200070128A1
Принадлежит: SMH Co., Ltd

The present invention relates to a hydrocarbon conversion catalyst system comprising: a first composition comprising a dehydrogenation active metal on a solid support; and a second composition comprising a transition metal on an inorganic support and a hydrocarbon conversion process utilizing the hydrocarbon conversion catalyst system. 1. A hydrocarbon conversion catalyst system , comprising:a. a first composition comprising a dehydrogenation active metal on a solid support; andb. a second composition comprising a transition metal on an inorganic support.2. The hydrocarbon conversion catalyst system according to claim 1 , wherein the dehydrogenation active metal is selected from the group consisting of platinum claim 1 , palladium claim 1 , iridium claim 1 , chromium claim 1 , and mixtures thereof.3. The hydrocarbon conversion catalyst system according to claim 1 , wherein the dehydrogenation active metal is platinum.4. The hydrocarbon conversion catalyst system according to claim 1 , wherein the solid support is selected from aluminum oxide claim 1 , silicon dioxide claim 1 , zirconium dioxide claim 1 , titanium dioxide claim 1 , magnesium oxide claim 1 , calcium oxide claim 1 , and mixtures thereof.5. The hydrocarbon conversion catalyst system according to claim 4 , wherein the solid support is a mixed of at least two or more metal oxides selected from the group consisting of mixed magnesium-aluminum oxide claim 4 , mixed calcium-aluminum oxide claim 4 , and mixture thereof.6. The hydrocarbon conversion catalyst system according to claim 5 , wherein the mixed of at least two or more metal oxides is derived from a layered double hydroxide.7. The hydrocarbon conversion catalyst system according to claim 1 , wherein the first composition further comprises an additional active metal selected from the group consisting of potassium claim 1 , tin claim 1 , lanthanum claim 1 , indium claim 1 , yttrium claim 1 , ytterbium claim 1 , rhenium claim 1 , and mixtures thereof.8. ...

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05-03-2020 дата публикации

Polyoxometalates Comprising Noble Metals and Post-Transition Metals and Metal Clusters Thereof

Номер: US20200070131A1
Принадлежит: ExxonMobil Chemical Patents Inc

The invention relates to polyoxometalates represented by the formula (A n ) m+ [M′M 12 X 8 O y R z H q ] m− or solvates thereof, corresponding supported polyoxometalates, and processes for their preparation, as well as corresponding metal clusters, optionally in the form of a dispersion in a liquid carrier medium or immobilized on a solid support, and processes for their preparation, as well as their use in reductive conversion of organic substrate.

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05-03-2020 дата публикации

PRODUCTION OF ETHYLENE WITH NANOWIRE CATALYSTS

Номер: US20200070136A1
Принадлежит:

Nanowires useful as heterogeneous catalysts are provided. The nanowires catalysts are useful in a variety of catalytic reactions, for example, the oxidative coupling of methane to ethylene. Related methods for use and manufacture of the same are also disclosed. 1. A catalyst comprising an inorganic catalytic nanowire , the nanowire having a ratio of effective length to actual length of less than one and an aspect ratio of greater than ten as measured by TEM in bright field mode at 5 keV , wherein the nanowire comprises one or more elements from any of Groups 1 through 7 , lanthanides , actinides or combinations thereof , wherein the catalyst has a catalytic activity effective to catalyze the oxidative coupling of methane with a Cselectivity of greater than 30% at a temperature below 600° C.2. The catalyst of claim 1 , wherein the one or more elements are in the form of oxides claim 1 , hydroxides claim 1 , oxyhydroxides claim 1 , sulfates claim 1 , carbonates claim 1 , oxide carbonates claim 1 , oxalates claim 1 , phosphates claim 1 , hydrogenphosphates claim 1 , dihydrogenphosphates claim 1 , oxyhalides claim 1 , hydroxihalides claim 1 , oxysulfates or combinations thereof.3. The catalyst of claim 2 , wherein the one or more elements are in the form of oxides.4. The catalyst of claim 2 , wherein the one or more elements are in the form of hydroxides.5. The catalyst of claim 1 , wherein the nanowire comprises Mg claim 1 , Ca claim 1 , La claim 1 , W claim 1 , Mn claim 1 , Mo claim 1 , Nd claim 1 , Sm claim 1 , Eu claim 1 , Pr claim 1 , Zr or combinations thereof.6. The catalyst of claim 1 , wherein the nanowire comprises MgO claim 1 , CaO claim 1 , LaO claim 1 , NaWO claim 1 , MnO claim 1 , MnO claim 1 , NdO claim 1 , SmO claim 1 , EuO claim 1 , PrO claim 1 , MgMnO claim 1 , NaMnO claim 1 , Na/Mn/W/O claim 1 , MnWOor combinations thereof.7. The catalyst of claim 1 , wherein the nanowire further comprises one or more dopants comprising metal elements claim 1 , semi- ...

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18-03-2021 дата публикации

Catalyst for oxygen-free direct conversion of methane and method of converting methane using the same

Номер: US20210077982A1

The present invention relates to a catalyst for oxygen-free direct conversion of methane and a method of converting methane using the same, and more particularly to a catalyst for oxygen-free direct conversion of methane, in which the properties of the catalyst are optimized by adjusting the free space between catalyst particles packed in a reactor, thereby maximizing the catalytic reaction rate without precise control of reaction conditions for oxygen-free direct conversion of methane, minimizing coke formation and exhibiting stable catalytic performance even upon long-term operation, and to a method of converting methane using the same.

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24-03-2016 дата публикации

PROCESS FOR THE PRODUCTION OF 1,3-BUTADIENE

Номер: US20160082417A1
Принадлежит:

The invention relates to the use of a novel silica-supported trimetallic (La/Zr/Zn) catalyst in the production of 1,3-butadiene from ethanol. The presence of lanthanum in the catalyst further comprising zirconium and zinc increases the catalyst's yield and selectivity to 1,3-butadiene. 1. A process for the production of 1 ,3-butadiene , the process comprisingi) providing a supported catalyst comprising lanthanum, zirconium, and zinc, the support comprising silica; andii) contacting a feed comprising ethanol with the supported catalyst, to obtain a raw product comprising 1,3-butadiene.2. The process according to claim 1 , wherein contacting ii) takes place at a temperature in a range of 300 to 425° C.3. The process according to claim 1 , wherein contacting ii) takes place at a weight hourly space velocity of 0.2-7 h.4. The process according to claim 1 , wherein the feed additionally comprises acetaldehyde.5. The process according to claim 1 , wherein it further comprisesiii) separating the raw product into a first portion comprising 1,3-butadiene and a second portion comprising acetaldehyde.6. The process according to claim 5 , wherein at least part of the second portion is recycled into the feed.8. The process according to claim 7 , wherein the method further comprisesd) impregnating the calcined dried impregnated support of step c) with a salt of zirconium and a salt of zinc;e) drying the impregnated support of step d); andf) calcining the dried impregnated support of step e).9. The process according to claim 7 , wherein claim 7 , in said method claim 7 , the support is impregnated in step a) with a salt of lanthanum claim 7 , a salt of zirconium claim 7 , and a salt of zinc.10. Use of lanthanum in a catalyst for the production of 1 claim 7 ,3-butadiene from a feed comprising ethanol and optionally acetaldehyde claim 7 , to increase the selectivity of the catalytic reaction to 1 claim 7 ,3-butadiene claim 7 , the catalyst further comprising zirconium and zinc. The ...

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26-03-2015 дата публикации

Multimetallic mixed oxides, its preparation and use for the oxidative dehydrogenation of ethane for producing ethylene

Номер: US20150086471A1

A layered multimetallic oxide catalyst having the formula M1 M2 M3 O δ wherein: M1 is selected from the group of Ag, Au, Zn, Sn, Rh, Pd, Pt, Cu, Ni, Fe, Co, an alkaline metal, an alkaline earth metal, a rare earth metal, and mixtures thereof; M2 is selected from the group of Ti, Hf, Zr, Sn, Bi, Sb, V, Nb, Ta and P, and mixtures thereof; M3 is selected from the group of Mo, W and Cr, and mixtures thereof; and where said multilayered metallic oxide exhibits a major X-ray diffraction peak between 5<2θ<15, is prepared by a process of mixing metallic precursors of M 1 , M 2 and M 3 to form a precursor mixture, hydrothermal treatment of the resulting mixture to obtain a homogeneous solid mixture, and thermally treating the solid mixture to activate the solid mixture and obtain said catalyst.

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26-03-2015 дата публикации

OXIDATIVE DEHYDROGENATION OF ETHANE TO ETHYLENE AND PREPARATION OF MULTIMETALLIC MIXED OXIDE CATALYST FOR SUCH PROCESS

Номер: US20150087505A1
Принадлежит:

Oxidative dehydrogenation of light paraffins, such as ethane at moderate temperatures (<500° C.) to produce ethylene without the formation of side products such as acetic acid and/or other oxygenated hydrocarbons is achieved using tellurium-free, multimetallic catalysts possessing orthorhombic M1 phase and other crystalline structures that have an important role for obtaining high performance catalysts for the oxidative dehydrogenation of ethane to ethylene. Such catalysts are prepared using thermal and hydrothermal methods. 1. A method for the formation of a multimetallic mixed oxide having the formula{'br': None, 'sub': h', 'i', 'x, 'MoVSbO'}wherein h and i, respectively, are each between 0.001 and 4.0, the ratio i/h is between 0.3 and 10.0, and x represents the number determined by and consistent with the valence requirements of the other elements present in the multimetallic mixed oxide, which comprises, forming a tellurium-free aqueous solution of metallic precursors consisting of molybdenum, vanadium and antimony and a structure-directing compound selected from the group consisting of primary amines, secondary amines, tertiary amines, ammonia, tetra-methyl ammonium and hydrazine, and subjecting said tellurium-free mixture to hydrothermal conditions to form a solid, washing and drying said solid, and thermally activating said dried solid to form a catalyst having one or more crystalline phases in addition to the M1 crystalline phase.2. The process of claim 1 , wherein structure-directing compound is selected from the group consisting of methylamine claim 1 , dimethyl amine claim 1 , tri-methyl amine claim 1 , diethyl amine claim 1 , or mixtures thereof.3. The process of claim 1 , wherein said hydrothermal treatment is conducted at a temperature between 100-200° C. for 6-150 hours and the resulting solids are washed and dried at 80-120° C. claim 1 , prior to activation.4. The process of claim 3 , wherein said hydrothermal treatment is at a temperature between ...

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26-03-2015 дата публикации

NANOWIRE CATALYSTS AND METHODS FOR THEIR USE AND PREPARATION

Номер: US20150087875A1
Принадлежит:

Nanowires useful as heterogeneous catalysts are provided. The nanowire catalysts are useful in a variety of catalytic reactions, for example, the oxidative coupling of methane to C2 hydrocarbons. Related methods for use and manufacture of the same are also disclosed. 1. A method for the preparation of ethane , ethylene or combinations thereof , the method comprising contacting a catalytic material with a gas comprising methane , wherein the catalytic material is in the form of a pressed pellet , extrudate or monolith and comprises:a) a plurality of catalytic nanowires, the catalytic nanowires comprising one or more doping elements; andb) a diluent or support selected from one or more alkaline earth metal compounds,and wherein the catalytic material has a C2+ yield above 5% when employed as catalytic material in the oxidative coupling of methane at an inlet temperature of 550° C. and an inlet pressure of about 2 atm in a fixed bed reactor with a gas-hour space velocity (GHSV) of at least about 20,000/hr.2. The method of claim 1 , wherein the catalytic materials is in the form of a pressure treated claim 1 , pressed pellet and comprises substantially no binder material.3. The method of claim 1 , wherein the catalytic material is in the form of a pressed pellet or extrudate and comprises pores greater than 20 nm in diameter.4. The method of claim 1 , wherein the alkaline earth metal compound is an alkaline earth metal oxide claim 1 , alkaline earth metal carbonate claim 1 , alkaline earth metal sulfate or alkaline earth metal phosphate.5. The method of claim 1 , wherein the alkaline earth metal compound is an alkaline earth metal carbonate claim 1 , alkaline earth metal sulfate or alkaline earth metal phosphate.6. The method of claim 1 , wherein the alkaline earth metal compound is MgO claim 1 , MgCO claim 1 , MgSO claim 1 , Mg(PO) claim 1 , MgAlO claim 1 , CaO claim 1 , CaCO claim 1 , CaSO claim 1 , Ca(PO) claim 1 , CaAlO claim 1 , SrO claim 1 , SrCO claim 1 , SrSO ...

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12-06-2014 дата публикации

Process for the Oxidative Dehydrogenation of N-Butenes to Butadiene

Номер: US20140163290A1
Принадлежит: BASF SE

The invention relates to a process for the oxidative dehydrogenation of n-butenes to butadiene, which comprises two or more production steps (i) and at least one regeneration step (ii), in which (i) in one production step, a starting gas mixture comprising n-butenes is mixed with an oxygen-comprising gas and brought into contact with a multimetal oxide catalyst which comprises at least molybdenum and a further metal and is arranged in a fixed catalyst bed in a fixed-bed reactor at a temperature of from 220 to 490° C., and, before the relative decrease in conversion at constant temperature is >25%, (ii) in a regeneration step, the multimetal oxide catalyst is regenerated by passing an oxygen-comprising regeneration gas mixture at a temperature of from 200 to 450° C. over the fixed catalyst bed and burning off the carbon deposited on the catalyst, where a regeneration step (ii) is carried out between two production steps (i), wherein from 2 to 50% by weight of the carbon deposited on the catalyst is burnt off per regeneration step (ii).

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12-03-2020 дата публикации

A METHOD FOR THE PRODUCTION OF HIGH PURITY BUTADIENE AND N-BUTENE FROM N-BUTANE USING AN OXIDATIVE DEHYDROGENATION PROCESS IN A CONTINUOUS-FLOW MULTI-LAYER-CATALYST FIXED-BED REACTOR

Номер: US20200079710A1
Принадлежит:

Systems and methods for the production of n-butene isomers and/or 1,3-butadiene are disclosed. The systems and method involve an oxidative dehydrogenation (ODH) process for the production of n-butene isomers and 1,3-butadiene light olefins using an adjustable, multi-purpose, and multi-layer-catalyst bed for a reactor. 1. A method of producing n-butene (CHCHCH═CH) and/or 1 ,3-butadiene (HC═CH—CH═CH) , the method comprising:{'sub': 4', '4', '10, 'flowing a feed stream comprising Chydrocarbons, including n-butane (CH), to a reactor, the reactor including a catalyst bed that comprises three separate catalytic layers arranged in series with respect to the flow of the feed stream, wherein a first inert layer of material is disposed between a first catalytic layer of the three separate catalytic layers and a second catalytic layer of the three separate catalytic layers, wherein a second inert layer of material is disposed between the second catalytic layer and a third catalytic layer of the three separate catalytic layers,'}contacting the n-butane with the first catalytic layer under reaction conditions sufficient to convert n-butane to n-butene and 1,3-butadiene, wherein the first catalytic layer is adapted to catalyze conversion of n-butane to n-butene and 1,3-butadiene; andflowing n-butene and/or 1,3-butadiene from the reactor.2. The method of claim 1 , wherein the feed stream comprises primarily n-butane.3. The method of claim 1 , wherein the feed stream comprises 85 to 99 wt. % n-butane claim 1 , 1 to 10 wt. % of n-butene claim 1 , and 0 to 5 wt. % of residual Ccompounds.4. The method of claim 1 , wherein each catalytic layer comprises different catalytic materials from the other catalytic layers.5. The method of claim 1 , further comprising:contacting a first portion of the n-butene with the second catalytic layer under reaction conditions sufficient to convert the first portion of the n-butene to 1,3-butadiene, wherein the second catalytic layer is adapted to ...

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25-03-2021 дата публикации

Method and Reactor for Oxidative Coupling of Methane

Номер: US20210087121A1
Принадлежит:

A method of autothermal oxidative coupling of methane (OCM) utilizes introducing a methane-containing feedstock and an oxygen-gas-containing feedstock into a reactor () as a flowing mixture () with a space time of 500 ms or less. The reactor () contains a catalyst bed () of an OCM catalyst that contacts the flowing mixture and wherein the catalyst bed () has a heat Peclet number (Pe) of from 5 or less, a mass Peclet number (Pe) of from 5 or more, and a transverse Peclet number (P) of from 1 or less while contacting the flowing mixture. The methane and oxygen of the feedstocks are allowed to react within the reactor () to form methane oxidative coupling reaction products. A reactor () for carrying out the OCM reaction is also disclosed. 1. A method of carrying out autothermal oxidative coupling of methane (OCM) comprising:{'sub': h', 'm, 'introducing a methane-containing feedstock and an oxygen-gas-containing feedstock into a reactor as a flowing mixture with a space time of 500 ms or less, the reactor containing a catalyst bed of an OCM catalyst that contacts the flowing mixture and wherein the catalyst bed has a heat Peclet number (Pe) of from 5 or less, a mass Peclet number (Pe) of from 5 or more, and a transverse Peclet number (P) of from 1 or less while contacting the flowing mixture; and'}allowing the methane and oxygen of the feedstocks to react within the reactor to form methane oxidative coupling reaction products.2. The method of claim 1 , wherein: a layer of OCM catalyst formed as catalyst particles having a particle size of from 0.1 mm to 3 mm;', 'at least one monolithic body of one of a ceramic or metal material having pores or channels with a pore or channel size from 0.1 to 5 mm, the monolithic body having an OCM catalyst material present on at least all or a portion of the surface of the monolithic body;', 'at least one monolithic body of one of a ceramic or metal material having pores or channels with a pore or channel size from 0.1 to 5 mm, and ...

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29-03-2018 дата публикации

Upgrading 5-nonanone

Номер: US20180086677A1
Принадлежит: Neste Oyj

Provided are fuel components, a method for producing fuel components, use of the fuel components and fuel containing the fuel components based on 5-nonanone.

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29-03-2018 дата публикации

Process for producing butadiene by oxidative dehydrogenation of butylene

Номер: US20180086679A1
Принадлежит: Wison Engineering Ltd

The present invention provides a process for producing butadiene by oxidative dehydrogenation of butylene, comprising: a reaction stage, wherein a multi-stage adiabatic fixed bed in series is used, wherein butylene, oxygen-comprising gas and water are reacted in the presence of a catalyst in each stage of the adiabatic fixed bed with the first stage of the adiabatic fixed bed being further separately fed a diluent, being nitrogen and/or carbon dioxide, and the molar ratio between this separately fed diluents and the oxygen of all the oxygen-comprising gases fed in the subsequent stage(s) of the adiabatic fixed bed being controlled, wherein the oxygen-comprising gas is air, oxygen-enriched air or oxygen, and at least one of all the oxygen-comprising gases fed in the subsequent stage(s) of the adiabatic fixed bed is oxygen-enriched air having a specific oxygen concentration or oxygen; and a post treatment stage, wherein the effluent from the last stage of the adiabatic fixed bed is treated to obtain a product butadiene. The present invention has an advantage that the whole process is with reduced total energy consumption.

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05-05-2022 дата публикации

DIRECT SYNTHESIS OF LIGHT OLEFINS FROM CARBON DIOXIDE USING YTTRIA-STABILIZED ZIRCONIA SUPPORT

Номер: US20220135495A1
Автор: KIM Sunkyu, Sasmaz Erdem
Принадлежит:

The present invention features a direct synthesis of light olefins through the hydrogenation of carbon dioxide. InOsupported on cubic phase yttria-stabilized zirconia is used as a catalyst and is mixed with a molecular sieve to perform the hydrogenation. The cubic crystal structure of the yttria-stabilized zirconium dioxide is an excellent support for indium oxide particles and prevents their deactivation during COhydrogenation. This direct synthesis route promotes a stable and efficient method for producing light olefins.

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05-04-2018 дата публикации

CATALYSTS FOR PETROCHEMICAL CATALYSIS

Номер: US20180093931A1
Принадлежит:

Metal oxide catalysts comprising various dopants are provided. The catalysts are useful as heterogenous catalysts in a variety of catalytic reactions, for example, the oxidative coupling of methane to C2 hydrocarbons such as ethane and ethylene. Related methods for use and manufacture of the same are also disclosed. 185-. (canceled)87. The catalyst of claim 86 , wherein A is from groups 2 claim 86 , 3 or 4.88. The catalyst of claim 86 , wherein A is Ce claim 86 , Pr claim 86 , Sr claim 86 , Ca claim 86 , Mg claim 86 , Y claim 86 , Zr or Ba.89. The catalyst of claim 86 , wherein B is from group 4.90. The catalyst of claim 86 , wherein B is Zr or Hf.91. The catalyst of claim 86 , wherein the dopant is Sr claim 86 , Mg or Ca.92. The catalyst of claim 86 , wherein the catalyst comprises one of the following formulas: Y/SrZrO claim 86 , SrHfO claim 86 , SrZrO claim 86 , Mg/SrHfO claim 86 , CaHfOor SrTbO.93. The catalyst of claim 86 , wherein the catalyst is a bulk catalyst.94. The catalyst of claim 86 , wherein the catalyst is a nanostructured catalyst.95. The catalyst of claim 94 , wherein the catalyst is a nanowire.96. A method for the oxidative coupling of methane claim 86 , the method comprising contacting methane with the catalyst of at temperatures ranging from about 550° C. to about 750° C. claim 86 , thereby converting the methane to C2 hydrocarbons at a methane conversion of greater than 20% and a C2 selectivity of greater than 50%.97. The method of claim 96 , wherein the method produces a product gas comprising less than 0.5% carbon monoxide. This invention is generally related to novel catalysts and, more specifically, to doped metal oxide catalysts useful as heterogeneous catalysts in a variety of catalytic reactions, such as the oxidative coupling of methane to C2 hydrocarbons.Catalysis is the process in which the rate of a chemical reaction is either increased or decreased by means of a catalyst. Positive catalysts increase the speed of a chemical reaction, ...

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05-04-2018 дата публикации

Catalyst and Process for Olefin Metathesis Reaction

Номер: US20180093933A1
Принадлежит: Borealis AG

The present invention relates to a magnesium oxide (MgO) catalyst for isomerisation of olefins with defined physical properties. The present invention further relates to a catalyst for conversion of olefins having a first catalyst component and a second catalyst component. The first catalyst component has a metathesis catalyst. The second catalyst component has the magnesium oxide catalyst. A process for obtaining an olefin is also disclosed.

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05-04-2018 дата публикации

PROCESS FOR THE PRODUCTION OF ETHYLENICALLY UNSATURATED CARBOXYLIC ACIDS OR ESTERS

Номер: US20180093937A1
Принадлежит:

The present invention relates to a process for the production of an ethylenically unsaturated carboxylic acid or ester, preferably α,β ethylenically unsaturated carboxylic acids or esters, by the liquid phase reaction of formaldehyde or a suitable source thereof with a non-cyclic carboxylic acid ester in the presence of a basic metal salt. 1. A process for production of an ethylenically unsaturated carboxylic acid or ester , unsaturated carboxylic by a liquid phase reaction of formaldehyde or a suitable source thereof with a non-cyclic carboxylic acid ester in the presence of a basic metal salt.2. The process according to claim 1 , wherein the basic metal salt is a group I or a group II metal salt.3. The process according to claim 1 , wherein the basic metal salt is selected from group I or group II metal oxides claim 1 , hydroxides claim 1 , carbonates claim 1 , hydrogen carbonates claim 1 , methyl carbonates claim 1 , alkoxides claim 1 , fluorides and phosphates.4. The process according to claim 1 , wherein the basic metal salt is selected from potassium oxide claim 1 , caesium oxide claim 1 , sodium oxide claim 1 , rubidium oxide claim 1 , barium oxide claim 1 , potassium hydroxide claim 1 , caesium hydroxide claim 1 , sodium hydroxide claim 1 , rubidium hydroxide claim 1 , barium hydroxide claim 1 , potassium phosphate claim 1 , caesium phosphate claim 1 , sodium phosphate claim 1 , rubidium phosphate claim 1 , barium phosphate claim 1 , sodium methoxide claim 1 , potassium methoxide claim 1 , rubidium methoxide claim 1 , sodium t-butoxide claim 1 , potassium t-butoxide claim 1 , rubidium t-butoxide claim 1 , caesium t-butoxide claim 1 , sodium fluoride claim 1 , potassium fluoride claim 1 , rubidium fluoride claim 1 , caesium fluoride claim 1 , potassium carbonate claim 1 , caesium carbonate claim 1 , sodium carbonate claim 1 , rubidium carbonate claim 1 , barium carbonate claim 1 , potassium hydrogen carbonate claim 1 , sodium hydrogen carbonate claim 1 , ...

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26-03-2020 дата публикации

Catalyst for the methanation of syngas and producer gas

Номер: US20200094227A1
Принадлежит: UNIVERSITY OF CALIFORNIA

Disclosed herein, inter alia, are novel nickel-ruthenium-magnesium oxide catalyst compositions and methods of making and using the same. The catalysts provide for improved methanation activity of syngas (CO+H2) and producer gas in, for example, a fixed-bed reactor. In this manner, the CO conversion and CH4 yield can be maximized in methanation reactions.

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26-03-2020 дата публикации

Method for producing fullerene derivative

Номер: US20200095209A1
Принадлежит: Showa Denko KK

(in formula (1), C* are each carbon atoms adjacent to each other for forming a fullerene skeleton, A is a linking group having 1-4 carbon atoms for forming a ring structure with two C*, in which a portion thereof may be a substituted or condensed group).

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02-06-2022 дата публикации

RECONSTITUTED DEHYDROGENATION CATALYST SHOWING SLOWED ACTIVITY LOSS WHEN COMPARED WITH FRESH CATALYST

Номер: US20220168709A1
Принадлежит: Dow Global Technologies LLC

A process for dehydrogenating alkane or alkylaromatic compounds comprising contacting the given compound and a dehydrogenation catalyst in a fluidized bed. The dehydrogenation catalyst is prepared from an at least partially deactivated platinum/gallium catalyst on an alumina-based support that is reconstituted by impregnating it with a platinum salt solution, then calcining it at a temperature from 400° C. to 1000° C., under conditions such that it has a platinum content ranging from 1 to 500 ppm, based on weight of catalyst; a gallium content ranging from 0.2 to 2.0 wt %; and a platinum to gallium ratio ranging from 1:20,000 to 1:4. It also has a Pt retention that is equal to or greater than that of a fresh catalyst being used in a same or similar catalytic process. 18-. (canceled)9. A process for dehydrogenating alkane or alkylaromatic compounds comprising: (a) obtaining a dehydrogenation catalyst comprising platinum and gallium on an alumina-based support, the dehydrogenation catalyst having been previously fresh but having become at least partially deactivated by the selective removal of platinum from the dehydrogenation catalyst, wherein the at least partially deactivated dehydrogenation catalyst has a ratio of platinum to gallium that is less than a ratio of platinum to gallium of the previously fresh dehydrogenation catalyst;', '(b) impregnating the at least partially deactivated dehydrogenation catalyst with a solution consisting of a platinum salt in water to form an impregnated dehydrogenation catalyst; and', '(c) calcining the impregnated dehydrogenation catalyst at a temperature ranging from 400° C. to 1000° C.;', '(b) and (c) being carried out under conditions suitable to form a reconstituted dehydrogenation catalyst having (i) a platinum content ranging from 1 part per million, based on weight of catalyst, to 500 parts per million, based on weight of catalyst; (ii) a gallium content ranging from 0.2 wt % to 2.0 wt %; and (iii) a ratio of platinum to ...

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08-04-2021 дата публикации

STABLE MIXED OXIDE CATALYSTS FOR DIRECT CONVERSION OF ETHANOL TO ISOBUTENE AND PROCESS FOR MAKING

Номер: US20210104442A1
Принадлежит:

ZnZrOmixed oxide catalysts having improved stability for the conversion of ethanol to isobutene are described, together with methods for making such catalysts. 1. A process for converting ethanol to products including isobutene , comprising:{'sub': x', 'y', 'z, 'sup': −1', '−1, 'contacting ethanol with a ZnZrOmixed oxide catalyst containing less than 0.14 percent by weight of sulfur, and wherein x:y is from 1:100 to 10:1 and z is a stoichiometric integer for the mixed oxide catalyst, at a temperature in the range of from about 350 to about 700 degrees Celsius and a WHSV in the range of from about 0.01 hrto 10 hr, to produce a product mixture including isobutene; and'}recovering isobutene from the product mixture.2. The process of claim 1 , wherein the catalyst contains less than 0.01 percent by weight of sulfur.3. The process of claim 2 , wherein the catalyst contains less than 0.001 percent by weight of sulfur. The present application is a divisional of U.S. application Ser. No. 15/860,815, filed Jan. 3, 2018, as a continuation of U.S. application Ser. No. 14/683,787, filed Apr. 10, 2015, which in turn was a national stage entry of International Application No. PCT/US2013/062784, filed Oct. 1, 2013, now published as WO 2014/070354, which directly claimed the benefit of U.S. Provisional Patent Application Ser. No. 61/720,433 filed Oct. 31, 2012.The present invention relates generally to renewable process alternatives for the production of isobutene. More particularly, the present invention relates to processes for the direct conversion of ethanol to isobutene and to the catalysts used therein, and still more particularly relates to the methods used for making such catalysts.As background, biomass is considered as a COneutral energy carrier, and is one of the most abundant and renewable of natural resources. In recent years, both as a result of market conditions as well as in response to a variety of governmental initiatives and mandates, biomass transformation to ...

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29-04-2021 дата публикации

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

Номер: US20210121859A1
Принадлежит:

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

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02-04-2020 дата публикации

CATALYST FOR THE OXIDATIVE COUPLING OF METHANE WITH LOW FEED TEMPERATURES

Номер: US20200101443A1
Принадлежит: SABIC Global Technologies, B.V.

A catalytic material for oxidative coupling of methane includes: a catalyst with the formula ABCO, wherein: A is selected from alkaline earth metals; B and C are selected from rare earth metals, and wherein B and C are different rare earth metals; and the oxide of at least A, B, and C has basic, redox, or both basic and redox properties, and wherein the elements A, B, and C are selected to create a synergistic effect whereby the catalytic material provides an oxygen conversion of greater than or equal to 50% and a C selectivity of greater than or equal to 70%, and wherein the catalyst provides the oxygen conversion and selectivity at a temperature of 797° F. (425° C.) or greater. The catalyst can be used in an oxidative coupling of methane reactor at lower feed temperatures compared to other catalysts. 1. A catalytic material for oxidative coupling of methane comprising:{'sub': a', 'b', 'c', 'x, 'claim-text': A is selected from alkaline earth metals;', 'B and C are selected from rare earth metals, and wherein', 'B and C are different rare earth metals; and', {'sub': '2', 'sup': '+', 'the oxide of at least A, B, and C has basic, redox, or both basic and redox properties, and wherein the elements A, B, and C are selected to create a synergistic effect whereby the catalytic material provides an oxygen conversion of greater than or equal to 50% and a C selectivity of greater than or equal to 70%, and wherein the catalyst provides the oxygen conversion and selectivity at a temperature of 797° F. (425° C.) or greater.'}], 'a catalyst with the formula ABCO, wherein2. The catalytic material according to claim 1 , wherein the catalyst is thermally stable at a temperature of 797° F. (425° C.) or greater.3. The catalytic material according to claim 1 , wherein the catalyst is thermally stable at a temperature in the range of about 797° F. (425° C.) to about 2 claim 1 ,372° F. (1 claim 1 ,300° C.).4. The catalytic material according to claim 1 , wherein the catalyst provides ...

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02-04-2020 дата публикации

Mixed Metal Oxide Catalyst useful for Paraffin Dehydrogenation

Номер: US20200101445A1
Принадлежит:

The invention relates to a catalyst composition suitable for the dehydrogenation of paraffins having 2-8 carbon atoms comprising zinc oxide and titanium dioxide, optionally further comprising oxides of cerium (Ce), dysprosium (Dy), erbium (Er), europium (Eu), gadolinium (Gd), lanthanum (La), neodymium (Nd), praseodymium (Pr), samarium (Sm), terbium (Tb), ytterbium (Yb), yttrium (Y), tungsten (W) and Zirconium (Zr) or mixtures thereof, wherein said catalyst composition is substantially free of chromium and platinum. The catalysts possess unique combinations of activity, selectivity, and stability. Methods for preparing improved dehydrogenation catalysts and a process for dehydrogenating paraffins having 2-8 carbon atoms, comprising contacting the mixed metal oxide catalyst with paraffins are also described. The catalyst may also be disposed on a porous support in an attrition-resistant form and used in a fluidized bed reactor. 133-. (canceled)34. A process for continuous dehydrogenating of paraffins having 2-8 carbon atoms , preferably propane or isobutane , comprising:{'sup': −1', '−1, 'contacting said paraffins with a catalyst composition at a reaction temperature of 500-800° C., a space velocity of 0.1-5 hror 0.1-1 hrand a pressure of 0.01-0.2 MPa for a reaction period in the range of 0.05 seconds to 10 minutes;'}regenerating the catalyst with an oxygen-containing gas wherein said catalyst regeneration is performed at a reaction temperature of 500-800° C., a pressure of 0.01-0.2 MPa and a regeneration period ranging from 0.05 seconds to 10 minutes;wherein the catalyst composition comprises:(a) zinc oxide with optional modifiers selected from the group of Copper, Manganese, and Niobium and a stabilized titania support, comprising: the stabilized titania support stabilized with a stabilizing element(s) comprising zirconium, tungsten, or a rare earth element or combinations thereof; and Zn; wherein the catalyst composition from 10 to 95 wt % titania, 0.1 to 25 wt % ...

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27-04-2017 дата публикации

PROCESS FOR PREPARING ALKANOLAMINES USEFUL IN REMOVAL OF ACID-GAS FROM A GASEOUS STREAM

Номер: US20170114001A1
Принадлежит:

The invention relates to a process for preparing alkanolamines, useful in the removal of COand/or HS from a COand/or HS containing gaseous stream, wherein the preparation of the alkanolamines is conducted using specifically selected ionic liquids under specifically selected reaction conditions. 2. A process according to claim 1 , wherein the molar ratio of glycerol to dimethylcarbonate in step i) is from 1:5 to 1:8.3. A process according to or claim 1 , wherein the reaction in step i) is conducted at a temperature of from 110° C. to 140° C.4. A process according to any of to claim 1 , wherein the reaction in step i) is conducted at a temperature of from 115° C. to 130° C.5. A process according to any of to claim 1 , wherein the reaction in step i) is conducted at a temperature of from 115° C. to 125° C.6. A process according to any of to claim 1 , wherein the amount of ionic liquid catalyst in step i) is at least 5 mol % based on glycerol.7. A process according to any of to claim 1 , wherein the glycidol formed in step i) is reacted with the amine of formula III in step ii) without prior separating from the reaction mixture.8. A process according to any of to claim 1 , wherein the glycidol formed in step i) is isolated from the reaction mixture before being reacted with the amine of formula III in step ii).9. A process according to claim 8 , wherein glycidol is isolated from the reaction mixture using liquid-liquid extraction and glycidol is preferentially extracted into an organic phase.10. A process according to claim 9 , wherein the liquid extraction is with ethyl acetate and glycidol is preferentially extracted into an ethyl acetate organic phase.11. A process according to claim 8 , wherein glycidol is isolated from the reaction mixture using azeotropic distillation.12. A process according to claim 11 , wherein azeotropic distillation is performed using cumene.13. A process according to claim 12 , wherein the glycidol-cumeme mixture obtained from azeoptropic ...

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13-05-2021 дата публикации

SYSTEMS AND METHODS FOR THE OXIDATIVE COUPLING OF METHANE

Номер: US20210139392A1
Принадлежит:

The present disclosure provides systems and methods for producing olefins via an oxidative coupling of methane (OCM) process. The systems and methods may comprise the use of a staged process comprising at least one non-adiabatic section that is in thermal communication with a heat transfer medium and at least one substantially adiabatic section. The systems and methods may also comprise the use of a diluent stream which may improve methane conversion in an OCM reactor and an ethylene/ethane ratio in a post-bed cracking unit. The methods and systems may further comprise injecting oxygen (O) and a paraffin into a gas stream containing a radical transfer agent to provide a reaction mixture. The reaction mixture may be held in a vessel for a time period greater than an auto-ignition delay time (AIDT), such that the reaction mixture may ignite to liberate heat and convert to a product mixture comprising olefins. 1. A method for producing an olefin , the method comprising:{'sub': 4', '2, '(a) producing a gas stream comprising methane (CH), oxygen (O), and a diluent; and'}{'sub': 4', '2+, '(b) passing the gas stream over an oxidative coupling of methane (OCM) catalyst at a pressure of at least 2 bar(g) to convert at least some of the CHinto hydrocarbon compounds having two or more carbon atoms (C compounds),'}wherein a ratio of diluent molecules to carbon atoms in the gas stream is at least 0.1:1.2. The method of claim 1 , wherein the diluent comprises water (HO).3. The method of claim 1 , wherein the diluent comprises carbon dioxide (CO).4. The method of claim 1 , wherein the diluent comprises HO and CO.5. The method of claim 1 , wherein the ratio of diluent molecules to carbon atoms in the gas stream is at least 0.5:1.6. The method of claim 1 , wherein the ratio of diluent molecules to carbon atoms in the gas stream is at most 20:1.7. The method of claim 1 , wherein the ratio of diluent molecules to carbon atoms in the gas stream is from 0.1:1 to 5:1.8. The method of ...

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09-04-2020 дата публикации

POLYMER TEMPLATED NANOWIRE CATALYSTS

Номер: US20200109094A1
Принадлежит:

Nanowires useful as heterogeneous catalysts are provided. The nanowire catalysts are prepared by polymer templated methods and are useful in a variety of catalytic reactions, for example, the oxidative coupling of methane to ethane and/or ethylene. Related methods for use and manufacture of the same are also disclosed. 133.-. (canceled)34. A process for the preparation of ethylene from methane comprising contacting a mixture comprising oxygen and methane with a catalytic material comprising nanowires comprising a plurality of metal oxides (MO) , metal oxy-hydroxides (MOOH) , metal oxycarbonates (MO(CO)) or metal carbonates (M(CO)) or combinations thereof , the nanowires prepared by a method comprising:a) providing a solution comprising a polymer template; and{'sub': m', 'n', 'p, '(b) introducing at least one metal ion and at least one anion to the solution under conditions and for a time sufficient to allow for nucleation and growth of nanowires comprising a plurality of metal salts (MXZ) on the polymer template,'}wherein:M is, at each occurrence, independently a metal element from any of Groups 1 through 7, lanthanides or actinides;X is, at each occurrence, independently hydroxide, carbonate, bicarbonate, phosphate, hydrogenphosphate, dihydrogenphosphate, sulfate, nitrate or oxalate;Z is O;n, m, x and y are each independently a number from 1 to 100; andp is a number from 0 to 100.35. The process of claim 34 , wherein the polymer template is functionalized with at least one of amine claim 34 , carboxylic acid claim 34 , sulfate claim 34 , alcohol or thiol groups.36. The process of claim 35 , wherein the polymer template comprises a hydrocarbon polymer.37. The process of claim 36 , wherein the polymer template comprises polystyrene.38. The process of claim 34 , wherein the method further comprises converting the nanowires comprising the plurality of metal salts (MXZ) to the nanowires comprising the plurality of metal oxides (MO) claim 34 , metal oxy-hydroxides (MOOH) ...

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03-05-2018 дата публикации

CATALYSTS FOR NATURAL GAS PROCESSES

Номер: US20180117570A1
Принадлежит:

Catalysts, catalytic forms and formulations, and catalytic methods are provided. The catalysts and catalytic forms and formulations are useful in a variety of catalytic reactions, for example, the oxidative coupling of methane. Related methods for use and manufacture of the same are also disclosed. 1189-. (canceled)192. The catalytic material of claim 191 , wherein B is Ba claim 191 , Sr or Ca.193. The catalytic material of claim 191 , wherein A is Ce claim 191 , Ti claim 191 , Zr or Hf.194. The catalytic material of claim 191 , wherein a is greater than 0.195. The catalytic material of claim 194 , wherein the perovskite has the following formula:{'br': None, 'sup': '1', 'sub': α', 'm', 'n', 'p, 'EABO.'}196. The catalytic material of claim 191 , wherein Eis an element from group 2 or group 3 of the periodic table.197. The catalytic material of claim 191 , wherein the perovskite has the formula ABO.198. The catalytic material of claim 190 , wherein x is greater than zero.199. The catalytic material of claim 190 , wherein b and y are both 0.200. The catalytic material of claim 190 , wherein the catalyst is a nanostructured catalyst.201. The catalytic material of claim 200 , wherein the catalyst is a nanowire catalyst.202. The catalytic material of claim 190 , wherein the catalyst further comprises a dopant selected from one or more elements from groups 2 claim 190 , 6 and the lanthanides.203. The catalytic material of claim 202 , wherein the catalyst further comprises a dopant from each of groups 2 claim 202 , 6 and the lanthanides.204. The catalytic material of claim 202 , wherein the catalyst further comprises a dopant from each of groups 2 and 6. This invention is generally related to catalysts and catalytic forms and formulations for use in natural gas processes, such as the oxidative coupling of methane.Catalysis is the process in which the rate of a chemical reaction is either increased or decreased by means of a catalyst. Positive catalysts lower the rate- ...

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03-05-2018 дата публикации

PRODUCTION OF ETHYLENE WITH NANOWIRE CATALYSTS

Номер: US20180117579A1
Принадлежит:

Nanowires useful as heterogeneous catalysts are provided. The nanowire catalysts are useful in a variety of catalytic reactions, for example, the oxidative coupling of methane to ethylene. Related methods for use and manufacture of the same are also disclosed. 1113-. (canceled)114. A method for the preparation of ethylene from methane , the method comprising contacting a mixture comprising oxygen and methane at a temperature below 600° C. with a catalytic nanowire , thereby producing C2 hydrocarbons at a selectivity of greater than 30% , wherein the catalytic nanowire comprises one or more elements from any of Groups 1 through 7 , lanthanides , actinides or combinations thereof in the form of oxides , hydroxides , oxyhydroxides , sulfates , carbonates , oxide carbonates , oxalates , phosphates , hydrogenphosphates , dihydrogenphosphates , oxyhalides , hydroxihalides , oxysulfates or combinations thereof.115. The method of claim 114 , wherein the one or more elements are in the form of oxides.116. The method of claim 114 , wherein the catalytic nanowire comprises Mg claim 114 , Ca claim 114 , La claim 114 , W claim 114 , Mn claim 114 , Mo claim 114 , Nd claim 114 , Sm claim 114 , Eu claim 114 , Pr claim 114 , Zr or combinations thereof.117. The method of claim 114 , wherein the catalytic nanowire comprises MgO claim 114 , CaO claim 114 , LaO claim 114 , NaWO claim 114 , MnO claim 114 , MnO claim 114 , NdO claim 114 , SmO claim 114 , EuO claim 114 , PrO claim 114 , MgMnO claim 114 , NaMnO claim 114 , Na/Mn/W/O claim 114 , MnWOor combinations thereof.118. The method of claim 114 , wherein the catalytic nanowire further comprises one or more dopants comprising metal elements claim 114 , semi-metal elements claim 114 , non-metal elements or combinations thereof.119. The method of claim 118 , wherein the dopant comprises Li claim 118 , Na claim 118 , K claim 118 , Mg claim 118 , Ca claim 118 , Ba claim 118 , Sr claim 118 , Eu claim 118 , Sm claim 118 , Co or Mn.120. The ...

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03-05-2018 дата публикации

NANOWIRE CATALYSTS AND METHODS FOR THEIR USE AND PREPARATION

Номер: US20180118637A1
Принадлежит:

Nanowires useful as heterogeneous catalysts are provided. The nanowire catalysts are useful in a variety of catalytic reactions, for example, the oxidative coupling of methane to C2 hydrocarbons. Related methods for use and manufacture of the same are also disclosed. 141-. (canceled)42. A method for the preparation of ethane , ethylene or combinations thereof , the method comprising contacting a catalytic material with a gas comprising methane , wherein the catalytic material comprises a plurality of catalytic nanowires and a diluent or support , the diluent or support comprising an alkaline earth metal compound.43. The method of claim 42 , wherein the catalytic material is in the form of a pressed pellet claim 42 , extrudate or monolith.44. The method of claim 42 , wherein the catalytic material is in the form of a pressed pellet.45. The method of claim 42 , wherein the catalytic material is in the form of an extrudate.46. The method of claim 42 , wherein the catalytic material is in the form of a monolith.47. The method of claim 42 , wherein the catalytic nanowires comprise one or more doping elements.48. The method of claim 42 , wherein the catalytic material is in the form of a pressure treated claim 42 , pressed pellet and comprises substantially no binder material.49. The method of claim 42 , wherein the catalytic material is in the form of a pressed pellet or extrudate and comprises pores greater than 20 nm in diameter.50. The method of claim 42 , wherein the alkaline earth metal compound is an alkaline earth metal oxide claim 42 , alkaline earth metal carbonate claim 42 , alkaline earth metal sulfate or alkaline earth metal phosphate.51. The method of claim 42 , wherein the alkaline earth metal compound is an alkaline earth metal carbonate claim 42 , alkaline earth metal sulfate or alkaline earth metal phosphate.52. The method of claim 42 , wherein the diluent or support comprises MgO claim 42 , MgCO claim 42 , MgSO claim 42 , Mg(PO) claim 42 , MgAlO claim ...

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16-04-2020 дата публикации

CATALYST SYSTEMS THAT INCLUDE METAL OXIDE CO-CATALYSTS FOR THE PRODUCTION OF PROPYLENE

Номер: US20200115299A1
Принадлежит:

Embodiments of methods of synthesizing a metathesis catalyst system, which include impregnating tungsten oxide on silica support in the presence of a precursor to produce a base catalyst; calcining the base catalyst; impregnating a metal oxide co-catalyst comprising a metal oxide onto the surface of the base catalyst to produce a doped catalyst; and calcining the doped catalyst to produce a metathesis catalyst system. Further embodiments of processes for the production of propylene, which include contacting a hydrocarbon feedstock comprising a mixture of 1-butene and 2-butene with embodiments of the metathesis catalyst system to produce, via metathesis conversion, a product stream comprising propylene. 1. A method of synthesizing a metathesis catalyst system comprising:impregnating a metal oxide onto a large pore silica support in the presence of a precursor to produce a base catalyst;calcining the base catalyst;impregnating a metal oxide co-catalyst onto the surface of the base catalyst to produce a doped catalyst; andcalcining the doped catalyst to produce a metathesis catalyst system.2. The method of claim 1 , wherein the large pore silica support comprises an amorphous silica.3. The method of claim 1 , wherein the metal oxide co-catalyst comprises one or more transition metals.4. The method of claim 1 , wherein the metal oxide co-catalyst comprises one or more metals selected from Cu claim 1 , Co claim 1 , Ce claim 1 , Ni claim 1 , Ga claim 1 , Al claim 1 , and Mo.5. The method of claim 1 , wherein the metathesis catalyst system comprises at least 0.5 weight percent (wt. %) metal oxide co-catalyst.6. The method of claim 1 , wherein the metathesis catalyst system comprises from about 0.5 wt. % to about 2.5 wt. % metal oxide co-catalyst.7. The method of claim 1 , wherein the base catalyst comprises from about 8 wt. % to about 12 wt. % tungsten oxide.8. The method of claim 1 , wherein the precursor comprises ammonium metatungstate hexahydrate.9. The method of claim ...

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31-07-2014 дата публикации

Artificial Photosynthetic System Using Photocatalyst

Номер: US20140209478A1
Автор: Daniel Landry
Принадлежит: SUNPOWER TECHNOLOGIES LLC

A photosynthetic system for splitting water to produce hydrogen and using the produced hydrogen for the reduction of carbon dioxide into methane is disclosed. The disclosed photosynthetic system employs photoactive materials that include photocatalytic capped colloidal nanocrystals within their composition, in order to harvest sunlight and obtain the energy necessary for water splitting and subsequent carbon dioxide reduction processes. The photosynthetic system may also include elements necessary to transfer water produced in the carbon dioxide reduction process, for subsequent use in water splitting process. The systems may also include elements necessary to store oxygen and collect and transfer methane, for subsequent transformation of methane into energy.

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10-05-2018 дата публикации

METHODS TO PRODUCE ZEOLITES WITH THE GME TOPOLOGY AND COMPOSITIONS DERIVED THEREFROM

Номер: US20180126364A1
Принадлежит:

The present disclosure is directed to producing zeolite structures with GME topologies using organic structure directing agents (OSDAs) comprising a piperidinium cation, and the compositions and structures resulting from these methods. In some embodiments, the crystalline products have a molar ratio of a molar ratio of Si:Al that is greater than 3.5. 1. A crystalline microporous aluminosilicate composition of GME topology comprising:(a) an oxide of silicon, and optionally an oxide of germanium;(b) an oxide of aluminum, and optionally one or more oxides boron, gallium, hafnium, iron, tin, titanium, indium, vanadium, or zirconium, wherein the molar ratio of the metals of (a) to the metals of (b) is greater than 3.5 to about 100; and which crystalline microporous aluminosilicate composition of GME topology exhibits a powder XRD pattern having at least five peaks having 2-theta values at 7.5±0.1°, 11.6±0.1°, 14.9±0.1°, 17.9±0.2°, 19.9±0.1°, 21.75±0.15°, 28.1±0.2°, or 30.1±0.1°.2. The crystalline microporous aluminosilicate composition of claim 1 , having a molar ratio of Si:Al that is greater than 3.5 to about 100.3. The crystalline microporous aluminosilicate composition of claim 1 , that exhibits one or more of:{'figref': [{'@idref': 'DRAWINGS', 'FIG. 3'}, {'@idref': 'DRAWINGS', 'FIG. 6'}, {'@idref': 'DRAWINGS', 'FIG. 7'}, {'@idref': 'DRAWINGS', 'FIG. 13'}], '(a) an XRD diffraction pattern the same as or consistent with any one of those shown in , , , or ;'}{'sup': '29', '(b) an Si MAS spectrum having a plurality of chemical shifts of about −99.1, −104.9 and −110.5 ppm downfield of a peak corresponding to and external standard of tetramethylsilane;'}{'sup': '29', 'figref': {'@idref': 'DRAWINGS', 'FIG. 13'}, '(c) an Si MAS spectrum the same as or consistent with the one shown in ;'}{'sub': '2', 'figref': {'@idref': 'DRAWINGS', 'FIG. 10'}, '(d) a physisorption isotherm with N-gas or with argon the same as or consistent with any one of those shown in ;'}{'sup': '27', ' ...

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01-09-2022 дата публикации

SELECTIVE PRODUCTION OF ETHYLENE FROM METHANE

Номер: US20220274094A1
Автор: HAIDER Muhammad H.
Принадлежит:

Disclosed are processes for producing ethylene. The processes can include contacting a first stream containing methane with an oxidant and oxidizing at least a portion of the methane under conditions suitable to produce a second stream containing carbon monoxide (CO) and hydrogen (H), contacting the second stream with a CO hydrogenation catalyst under conditions suitable to produce a third stream containing methanol and ethanol, obtaining a fourth stream containing the ethanol and a fifth stream containing the methanol from the third stream, and contacting the fourth stream with an ethanol dehydration catalyst under conditions suitable to dehydrate at least a portion of the ethanol and produce a products stream containing ethylene. 1. A process for producing ethylene , the process comprising:{'sub': '2', '(a) contacting a first stream comprising methane with an oxidant and oxidizing at least a portion of the methane under conditions suitable to produce a second stream comprising carbon monoxide (CO) and hydrogen (H);'}(b) contacting the second stream with a CO hydrogenation catalyst under conditions suitable to produce a third stream comprising methanol and ethanol;(c) obtaining a fourth stream comprising the ethanol, and a fifth stream comprising methanol from the third stream; and(d) contacting the fourth stream with an ethanol dehydration catalyst under conditions suitable to dehydrate at least a portion of the ethanol and produce a products stream comprising ethylene.2. The process of claim 1 , wherein the third stream further comprises C2-C7 paraffins and carbon dioxide (CO) and the process further comprises:{'sub': '2', '(i) separating the third stream to obtain a first intermediate stream containing the methanol and ethanol and a second intermediate stream containing the C2-C7 paraffins and CO; and'}(ii) separating the first intermediate stream to obtain the fourth stream and the fifth stream.3. The process of claim 1 , wherein the CO hydrogenation catalyst ...

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02-05-2019 дата публикации

CATALYST AND PROCESS FOR THE SELECTIVE CONVERSION OF HYDROCARBONS

Номер: US20190126250A1
Принадлежит:

A catalyst for a selective conversion of hydrocarbons. The catalyst includes a first component selected from the group consisting of Group VIII noble metals and mixtures thereof, a second component selected from the group consisting of alkali metals or alkaline-earth metals and mixtures thereof, and a third component selected from the group consisting of tin, germanium, lead, indium, gallium, thallium and mixtures thereof. The catalyst is a support formed as a spherical catalyst particle with an average pore diameter between 200 to 350 Angstroms, a porosity of at least 75% and an apparent bulk density between 0.60 and 0.3 g/cc. Also, a process of using such a catalyst for a selective hydrocarbon conversion reaction and a process for regenerating such a catalyst by removing coke from same. 1. A catalyst for a selective conversion of hydrocarbons , the catalyst comprising:a first component selected from the group consisting of Group VIII noble metals and mixtures thereof, a second component selected from the group consisting of alkali metals or alkaline-earth metals and mixtures thereof, and a third component selected from the group consisting of tin, germanium, lead, indium, gallium, thallium and mixtures thereof; anda support forming a catalyst particle comprising a plurality of pores, wherein at least 15% of the pores have an average pore diameter between 200 to 350 Angstroms, and wherein the catalyst particle has an apparent bulk density between 0.60 and 0.3 g/cc.2. The catalyst of wherein the apparent bulk density is between 0.60 and 0.5 g/cc.3. The catalyst of wherein the apparent bulk density is between 0.57 to 0.52 g/cc.4. The catalyst of wherein the wherein the apparent bulk density is 0.57 g/cc.5. The catalyst of wherein the at least 15% of the pores having an average pore diameter between 200 to 350 Angstroms have an average pore diameter between 240 to 280 Angstroms.6. The catalyst of wherein the catalyst has mono-modal porous distribution.7. The catalyst ...

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02-05-2019 дата публикации

Processes for regenerating a catalyst for the selective conversion of hydrocarbons

Номер: US20190126251A1
Принадлежит: UOP LLC

A catalyst for a selective conversion of hydrocarbons. The catalyst includes a first component selected from the group consisting of Group VIII noble metals and mixtures thereof, a second component selected from the group consisting of alkali metals or alkaline-earth metals and mixtures thereof, and a third component selected from the group consisting of tin, germanium, lead, indium, gallium, thallium and mixtures thereof. The catalyst is a support formed as a spherical catalyst particle with an average pore diameter between 200 to 350 Angstroms, a porosity of at least 75% and an apparent bulk density between 0.60 and 0.3 g/cc. Also, a process of using such a catalyst for a selective hydrocarbon conversion reaction and a process for regenerating such a catalyst by removing coke from same.

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23-04-2020 дата публикации

METHOD FOR PREPARING DEHYDROGENATION CATALYST FOR LINEAR CHAIN LIGHT HYDROCARBONS WITH HIGH REGENERATION EFFICIENCY

Номер: US20200122125A1
Принадлежит:

The present invention relates to a catalyst used in a dehydrogenation reaction of a linear hydrocarbon gas in a range of C3 to C4, and provides a dehydrogenation catalyst which is deposited on a carrier obtained by changing the phase of platinum, an auxiliary metal and an alkali metal, wherein the platinum and the auxiliary metal are present as a single complex within a certain thickness from the outer edges of the catalyst in an alloy form. 1. A dehydrogenation catalyst for use in dehydrogenation of straight-chain hydrocarbon gas in a range of C3 to C4 , the dehydrogenation catalyst comprising:platinum, an auxiliary metal, and an alkali metal which are carried in a phase-changed carrier,wherein the platinum and the auxiliary metal form a single complex and are present in an alloy form within a predetermined thickness from an outer periphery of the catalyst.2. The dehydrogenation catalyst of claim 1 , wherein the predetermined thickness is realized by a rapid heat-treatment process and a rapid drying process of the single complex using an organic acid and an inorganic acid.3. The dehydrogenation catalyst of claim 1 , wherein the catalyst is obtained using a process further including a calcination step and a reduction step claim 1 , and the reduction step is realized by a high-temperature rapid reduction process.4. The dehydrogenation catalyst of claim 1 , wherein the predetermined thickness is 300 to 500 μm thick from the outer periphery of the catalyst.5. The dehydrogenation catalyst of claim 2 , wherein the inorganic acid is a hydrochloric acid claim 2 , a nitric acid claim 2 , or a sulfuric acid.6. The dehydrogenation catalyst of claim 2 , wherein the organic acid further includes one among a formic acid claim 2 , an acetic acid claim 2 , a glycolic acid claim 2 , a glyoxylic acid claim 2 , an oxalic acid claim 2 , a propionic acid claim 2 , and a butyric acid claim 2 , or a mixture including two thereof.7. The dehydrogenation catalyst of claim 1 , wherein the ...

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01-09-2022 дата публикации

Selective production of propylene and butylene from methane

Номер: US20220274902A1
Автор: Muhammad H. HAIDER
Принадлежит: SABIC Global Technologies BV

Disclosed are processes for producing propylene and butylene. The processes can include contacting a first stream containing methane with an oxidant and oxidizing at least a portion of the methane under conditions suitable to produce a second stream containing carbon monoxide (CO) and hydrogen (H2), contacting the second stream with a CO hydrogenation catalyst under conditions suitable to produce a third stream containing propanol and butanol, and contacting the third stream with an dehydration catalyst under conditions suitable to dehydrate at least a portion of the propanol and butanol and produce a products stream containing propylene and butylene.

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23-04-2020 дата публикации

Process for oligomerizing olefins with streams having a reduced olefin content

Номер: US20200123080A1
Принадлежит: EVONIK OPERATIONS GMBH

A process is used for oligomerizing C2- to C8-olefins in several reaction stages in which the starting mixture and the respective outputs from the reaction stages are separated and are fed to different reaction stages. 1. A process for oligomerizing C2- to C8-olefins in at least three reaction stages connected in series , each reaction stage comprising at least one reactor and at least one distillation column , wherein the process comprises:(a) providing a starting mixture comprising C2- to C8-olefins, and dividing the starting mixture into first feed stream and second feed stream, wherein the first feed stream is fed as feed stream to the first reaction stage and the second feed stream is added to the feed stream to at least one of the downstream reaction stages, in which the olefin content is less than 50% by weight;(b) a first reaction stage: oligomerizing, using an oligomerization catalyst, the olefins in the feed stream to the first reaction stage in at least one reactor and separating oligomers formed as bottom product in a downstream distillation column, wherein an overhead product formed in the distillation column is at least partially fed as feed stream to the second reaction stage;(c) a second reaction stage: oligomerizing, using an oligomerization catalyst, the olefins in the feed stream to the second reaction stage in at least one reactor and separating oligomers formed as bottom product in a distillation column, wherein an overhead product formed in the distillation column is at least partially fed as feed stream to the third reaction stage; and(d) a third reaction stage: oligomerizing, using an oligomerization catalyst, the olefins in the feed stream to the third reaction stage in at least one reactor and separating oligomers formed in this case as bottom product in a distillation column;wherein the at least one reactor in the last reaction stage is operated adiabatically, but the reactors in the preceding reaction stages are cooled using a cooling ...

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03-06-2021 дата публикации

Zinc(II) and Gallium(III) Catalysts for Olefin Reactions

Номер: US20210162373A1
Принадлежит: PURDUE RESEARCH FOUNDATION

Oligomerization catalyst and method for oligomerization using the catalyst. The catalyst comprises a single Zn(II) or Ga(III) metal ion center directly bonded to a support through a shared oxygen atom, the catalyst having at least one M-O bond which forms an active site for oligomerization. The method includes reacting one or more C2 to C12 olefins with the oligomerization catalyst at a temperature of about 200° C. or higher to provide an oligomer product comprising C4 to C26 olefins. 1. An oligomerization catalyst , comprising a single Zn(II) metal ion center directly bonded to a support through a shared oxygen atom , the catalyst having at least one Zn—O bond which forms an active site for oligomerization.2. The catalyst of claim 1 , wherein the zinc metal ion has a +2 oxidation state at a temperature of at least 200° C.3. The catalyst of claim 1 , wherein zinc is present in an amount ranging from about 0.1 wt % to about 20 wt % claim 1 , based on the total weight of the catalyst.4. The catalyst of claim 1 , wherein the support has a surface area of about 30 m/g to about 600 m/g.5. The catalyst of claim 1 , wherein the support has a pore size of about 5 Å to about 500 Å.6. The catalyst of claim 1 , wherein the support is silica oxide claim 1 , aluminum oxide or silica-aluminum oxide claim 1 , zeolite claim 1 , aluminum phosphate molecular sieve claim 1 , silicon-aluminum phosphate molecular sieve claim 1 , mesoporous molecular sieve.7. A method for making light hydrocarbon oligomers claim 1 , comprising:reacting one or more C2 to C12 olefins with a supported zinc catalyst at a temperature of about 200° C. or higher to provide an oligomer product comprising C4 to C26 olefins, wherein the supported zinc catalyst comprises a single Zn(II) metal ion center directly bonded to a support through a shared oxygen atom, the zinc is present in an amount ranging from about 0.1 wt % to about 20 wt %, based on the total weight of the catalyst.8. The method of claim 7 , wherein ...

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08-09-2022 дата публикации

Processes for Upgrading Alkanes and Alkyl Aromatic Hydrocarbons

Номер: US20220281783A1
Принадлежит: ExxonMobil Chemical Patents Inc

Processes for upgrading a hydrocarbon. The process can include introducing, contacting, and halting introduction of a hydrocarbon-containing feed into a reaction zone. The feed can be contacted with a catalyst within the reaction zone to effect dehydrogenation, dehydroaromatization, and/or dehydrocyclization of the feed to produce a coked catalyst and an effluent. The process can include introducing, contacting, and halting introduction of an oxidant into the reaction zone. The oxidant can be contacted with the coked catalyst to effect combustion of the coke to produce a regenerated catalyst. The process can include introducing, contacting, and halting introduction of a reducing gas into the reaction zone. The reduction gas can be contacted with the regenerated catalyst to produce a regenerated and reduced catalyst. The process can include introducing and contacting an additional quantity of the feed with the regenerated and reduced catalyst to produce a re-coked catalyst and additional first effluent.

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