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Небесная энциклопедия

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

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Мониторинг СМИ

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

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Поддерживает ввод нескольких поисковых фраз (по одной на строку). При поиске обеспечивает поддержку морфологии русского и английского языка
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Применить Всего найдено 10068. Отображено 100.
05-01-2012 дата публикации

Process for producing alkylated aromatic compounds and process for producing phenols

Номер: US20120004471A1
Принадлежит: Mitsui Chemicals Inc

According to a process of the invention, a ketone, an aromatic compound and hydrogen as starting materials are reacted together in a single reaction step to produce an alkylaromatic compound in high yield. A process for producing phenols in the invention includes a step of performing the above alkylation process and does not increase the number of steps compared to the conventional cumene process. The process for producing alkylated aromatic compounds includes reacting an aromatic compound such as benzene, a ketone such as acetone and hydrogen in the presence of a solid acid substance, preferably a zeolite, and a silver-containing catalyst.

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12-01-2012 дата публикации

Olefin production process

Номер: US20120010453A1
Принадлежит: Mitsui Chemicals Inc

A novel olefin production process is provided which can be established as an industrial and practical process capable of producing olefins by directly reacting a ketone and hydrogen in a single reaction step. In particular, a novel olefin production process is provided in which propylene is obtained with high selectivity by directly reacting acetone and hydrogen. The olefin production process according to the present invention includes reacting a ketone and hydrogen in the presence of at least one dehydration catalyst and a silver-containing catalyst, and the at least one dehydration catalyst is selected from metal oxide catalysts containing a Group 6 element, zeolites, aluminas and heteropoly acid salts in which part or all the protons in heteropoly acids are exchanged with metal cations.

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26-01-2012 дата публикации

Process for preparing aromatics from methane

Номер: US20120022310A1
Принадлежит: BASF SE

The present invention relates to a process for carrying out endothermic, heterogeneously catalyzed reactions in which the reaction of the starting materials is carried out in the presence of a mixture of inert heat transfer particles and catalyst particles, where the catalyst particles are regenerated in a nonoxidative atmosphere at regular intervals and the heat of reaction required is introduced by separating off the inert heat transfer particles, heating the heat transfer particles in a heating zone and recirculating the heated heat transfer particles to the reaction zone. The process of the invention is particularly suitable for the nonoxidative dehydroaromatization of C 1 -C 4 -aliphatics in the presence of zeolite-comprising catalysts.

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01-03-2012 дата публикации

Process for selectively making olefins from energy dense alcohols

Номер: US20120053384A1
Принадлежит: US Department of Army

A process to perform selective catalytic oxidation of four-carbon alcohols to produce four-carbon olefins with yields greater than 90%. The process includes providing a supply of oxygen gas and a butanol fuel, atomizing and evaporating the fuel to produce a vapor, mixing the vapor with the oxygen to form a fuel mixture, reacting the fuel mixture in the presence of a heated solid Rh/Al 2 O 3 or Al 2 O 3 catalysts.

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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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03-05-2012 дата публикации

Process for preparing a phenylcyclohexane

Номер: US20120108874A1
Принадлежит: BASF SE

The present invention relates to an improved process for preparing a substituted or unsubstituted phenylcyclohexane by catalytic hydrogenation of a substituted or unsubstituted biphenyl.

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10-05-2012 дата публикации

Multiple zeolite catalyst

Номер: US20120116139A1

The multiple zeolite catalyst is a catalytic composition used to convert C 9+ alkylaromatic hydrocarbons to BTX, particularly commercially valuable xylenes. The catalyst is formed by mixing at least two zeolites selected from mordenite, beta zeolite, ZSM-5, ZSM-11, ZSM-12, ZSM-22, ZSM-23, MFI topology zeolite, NES topology zeolite, EU-1, MAPO-36, SAPO-5, SAPO-11, SAPO-34, and SAPO-41, and adding at least one metal component selected from Group VIB and Group VIII of the Periodic Table of the Elements. The two zeolites should have different physical and chemical characteristics, such as pore size and acidity. An exemplary catalyst includes mordenite, ZSM-5, and 3 wt. % molybdenum. The transalkylation reaction may be conducted in one or more reactors with a fixed bed, moving bed, or radial flow reactor at 200-540° C., a pressure of 1.0-5.0 MPa, and liquid hourly space velocity of 1.0-5.0 per hour.

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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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31-05-2012 дата публикации

Methods for producing fuels and solvents

Номер: US20120136185A1
Автор: David Bressler
Принадлежит: University of Alberta

Described herein are methods for producing fuels and solvents from fatty acid resources. Also disclosed herein are fuels and solvents produced by the methods described herein.

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21-06-2012 дата публикации

Methods for removing unsaturated aliphatic hydrocarbons from a hydrocarbon stream using an acidic molecular sieve

Номер: US20120157739A1
Принадлежит: UOP LLC

Disclosed is a method for removing unsaturated aliphatic compounds from a hydrocarbon feed stream by contacting the hydrocarbon feed stream with an acidic molecular sieve to produce a hydrocarbon effluent stream having a lower unsaturated aliphatic content relative to the hydrocarbon feed stream. The hydrocarbon feed stream comprises an aromatic compound, a nitrogen compound, and an unsaturated aliphatic compound.

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12-07-2012 дата публикации

Process For Producing Cyclohexylbenzene

Номер: US20120178969A1
Принадлежит: ExxonMobil Chemical Patents Inc

In a process for producing cyclohexylbenzene, benzene and hydrogen are contacted under hydroalkylation conditions with a catalyst system comprising a MCM-22 family molecular sieve and at least one hydrogenation metal. The conditions comprise a temperature of about 140° C. to about 175° C., a pressure of about 135 psig to about 175 psig (931 kPag to 1207 kPag), a hydrogen to benzene molar ratio of about 0.30 to about 0.65 and a weight hourly space velocity of benzene of about 0.26 to about 1.05 hr −1 .

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27-09-2012 дата публикации

Process for the conversion of mixed lower alkanes to aromatic hydrocarbons

Номер: US20120240467A1
Принадлежит: Individual

A process for the conversion of mixed lower alkanes into aromatics which comprises first reacting a mixed lower alkane feed comprising at least propane and ethane in the presence of an aromatization catalyst under reaction conditions which maximize the conversion of propane into first stage aromatic reaction products, separating ethane from the first stage aromatic reaction products, reacting ethane in the presence of an aromatization catalyst under reaction conditions which maximize the conversion of ethane into second stage aromatic reaction products, and optionally separating ethane from the second stage aromatic reaction products.

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11-10-2012 дата публикации

Production of lower olefins from synthesis gas

Номер: US20120259026A1

Disclosed is a process for the production of lower olefins by the conversion of a feed stream comprising carbon monoxide and hydrogen, and catalysts as used therein, such as a Fischer-Tropsch process. By virtue of the invention, lower olefins can be formed from synthesis gas, with high selectivity, and low production of methane. The catalysts used herein comprise an α-alumina support, and a catalytically active component that comprises iron-containing particles dispersed onto the support in at least 1 wt. %. The majority of the iron-containing particles is in direct contact with the α-alumina and is well-distributed thereon. Preferably, the iron-containing particles have an average particle size below 30 nm, and most preferably below 10 nm. The supported catalysts not only show a high selectivity, but also a high catalyst activity and chemical and mechanical stability.

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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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01-11-2012 дата публикации

Process for the regeneration of hydrocarbon conversion catalysts

Номер: US20120277089A1
Принадлежит: Individual

The present invention provides a process for hydrocarbon conversion, especially for producing aromatic hydrocarbons, which comprises: (a) alternately contacting a hydrocarbon feed, especially a lower alkane feed, with a hydrocarbon conversion catalyst, especially an aromatization catalyst, under hydrocarbon conversion, especially aromatization reaction conditions, in a reactor for a short period of time, preferably 30 minutes or less, to produce reaction products and then contacting the catalyst with hydrogen-containing gas at elevated temperature for a short period of time, preferably 10 minutes or less, (b) repeating the cycle of step (a) at least one time, (c) regenerating the catalyst by contacting it with an oxygen-containing gas at elevated temperature and (d) repeating steps (a) through (c) at least one time.

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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

Catalyst and process for hydrogenating aromatics

Номер: US20120296111A1
Принадлежит: BASF SE

The present invention relates to an eggshell catalyst comprising an active metal selected from the group consisting of ruthenium, rhodium, palladium, platinum and mixtures thereof, applied to a support material comprising silicon dioxide, wherein the pore volume of the support material is 0.6 to 1.0 ml/g, determined by Hg porosimetry, the BET surface area is 280 to 500 m 2 /g, and at least 90% of the pores present have a diameter of 6 to 12 nm, to a process for preparing this eggshell catalyst, to a process for hydrogenating an organic compound which comprises at least one hydrogenatable group using the eggshell catalyst, and to the use of the eggshell catalyst for hydrogenating an organic compound.

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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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29-11-2012 дата публикации

Process for preparing an alkene

Номер: US20120302810A1
Принадлежит: Individual

A process for the preparation of an alkene from an oxygenate comprising contacting a reactant feedstream comprising at least one oxygenate reactant and water with a supported heteropolyacid catalyst at a temperature of at least 170° C., wherein the process is initiated using a start-up procedure comprising the following steps: (i) heating the supported heteropolyacid catalyst to a temperature of at least 220° C.; (ii) maintaining the heat-treated supported heteropolyacid catalyst of step (i) at a temperature of at least 220° C. for a time sufficient to remove bound water from the heteropolyacid component of the supported heteropolyacid catalyst; and (iii) whilst maintaining the supported heteropolyacid catalyst of step (ii) at a temperature of at least 220° C., contacting the supported heteropolyacid catalyst with the reactant feedstream having a temperature of at least 220° C.

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21-02-2013 дата публикации

Process for the Production of Light Olefins from Synthesis Gas

Номер: US20130046033A1
Автор: Cristina Ferrini
Принадлежит: Casale Chemicals SA

A new process for light-olefins production is disclosed. The process comprises the step of contacting syngas with a iron-based catalyst at a temperature in the range from 250° C. to 350° C. and at a pressure in the range from 10 bar to 40 bar. By so doing a production of light olefins with a selectivity of at least 80% is obtained.

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14-03-2013 дата публикации

Hydroisomerization and selective hydrogenation of feedstock in ionic liquid-catalyzed alkylation

Номер: US20130066121A1
Принадлежит: Chevron USA Inc

A process for producing alkylate comprising contacting a first hydrocarbon stream comprising at least one olefin having from 2 to 6 carbon atoms which contains 1,3-butadiene and 1-butene with a hydroisomerization catalyst in the presence of hydrogen under conditions favoring the simultaneous selective hydrogenation of 1,3-butadiene to butenes and the isomerization of 1-butene to 2-butene and contacting the resulting stream and a second hydrocarbon stream comprising at least one isoparaffin having from 3 to 6 carbon atoms with an acidic ionic liquid catalyst under alkylation conditions to produce an alkylate is disclosed.

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18-04-2013 дата публикации

Heavy alkylbenzene transalkylation operating cost reduction

Номер: US20130096357A1
Принадлежит: UOP LLC

A process for increasing the production of monoalkylbenzenes is presented. The process includes utilizing a transalkylation process to convert dialkylbenzenes to monoalkylbenzenes. The transalkylation process recycles a portion of the effluent stream from the transalkylation reactor back to the feed of the transalkylation reactor. The recycled dialkylbenzenes and a portion of the recycled benzene are converted to monoalkylbenzenes.

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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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23-05-2013 дата публикации

Production of renewable aromatic compounds

Номер: US20130130345A1
Принадлежит: JNF BIOCHEMICALS LLC

The invention provides a process for producing a variety renewable aromatic compounds such as benzene, toluene, xylenes, and cumene, as well as compounds derived from these including, for example, aniline, benzoic acid, cresol, cyclohexane, cyclohexanone, phenol and bisphenol A, toluene di-isocyanate, isophthalic acid, phthalic anhydride, terephthalic acid and dimethyl terephthalate. The invention also provides for renewable forms of these aromatic compounds.

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04-07-2013 дата публикации

"process for producing cycloalkylaromatic compounds"

Номер: US20130172514A1
Автор: Teng Xu, Wenyih F. Lai
Принадлежит: ExxonMobil Chemical Patents Inc

In a process for producing a cycloalkylaromatic compound, an aromatic compound, hydrogen and at least one diluent are supplied to a hydroalkylation reaction zone, such that the weight ratio of the diluent to the aromatic compound supplied to the hydroalkylation reaction zone is at least 1:100. The aromatic compound, hydrogen and the at least one diluent are then contacted under hydroalkylation conditions with a hydroalkylation catalyst in the hydroalkylation reaction zone to produce an effluent comprising a cycloalkylaromatic compound.

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15-08-2013 дата публикации

Fischer-tropsch catalyst regeneration

Номер: US20130210939A1
Принадлежит: GTL F1 AG

A process for the regeneration of deactivated catalyst from a Fischer-Tropsch synthesis reactor, the catalyst being a supported cobalt catalyst. The process comprises the following steps: a withdrawal step, in which a portion of deactivated catalyst together with liquid hydrocarbon is withdrawn from the reactor; a concentration step, in which the concentration of the catalyst in the liquid hydrocarbon is increased; a calcination step, in which the deactivated catalyst composition is subjected to an oxidising gas to oxidise carbonaceous material contained in the deactivated catalyst in to gaseous oxides of the components of the carbonaceous material; and a reactivation step, in which the deactivated catalyst composition is reactivated to produced a regenerated catalyst.

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19-09-2013 дата публикации

Production of propylene via simultaneous dehydration and skeletal isomerisation of isobutanol on acid catalysts followed by metathesis

Номер: US20130245348A1
Принадлежит: Total Research and Technology Feluy SA

The present invention relates to a process for the production of propylene in which in a first step isobutanol is subjected to a simultaneous dehydration and skeletal isomerisation to make substantially corresponding olefins, having the same number of carbons and consisting essentially of a mixture of n-butenes and iso-butene and in a second step n-butenes are subjected to methathesis, said process comprising: a) introducing in a reactor a stream (A) comprising isobutanol, optionally water, optionally an inert component, b) contacting said stream with a catalyst in said reactor at conditions effective to dehydrate and skeletal isomerase at least a portion of the isobutanol to make a mixture of n-butenes and iso-butene, c) recovering from said reactor a stream (B), removing water, the inert component if any and unconverted isobutanol if any to get a mixture of n-butenes and iso-butene, d) fractionating said mixture to produce a n-butenes stream (N) and to remove the essential part of isobutene optionally recycled with stream (A) to the dehydration/isomerization reactor of step b), e) sending the stream (N) to a methathesis reactor and contacting stream (N) with a catalyst in said methathesis reactor, optionally in the presence of ethylene, at conditions effective to produce propylene, f) recovering from said methathesis reactor a stream (P) comprising essentially propylene, unreacted n-butenes, heavies, optionally unreacted ethylene, g) fractionating stream (P) to recover propylene and optionally recycling unreacted n-butenes and unreacted ethylene to the methathesis reactor.

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31-10-2013 дата публикации

Method of carrying out cc-coupling reactions

Номер: US20130289321A1
Принадлежит: Universite Catholique de Louvain UCL

The present invention is directed to a method of carrying out Suzuki-Miyaura CC-coupling reactions, including reacting an aryl halide with an aryl boronic acid in an organic solvent in the presence of a carbon supported palladium catalyst and a base, wherein the reactions are carried out at constant pH. The invention is also directed to a palladium on carbon catalyst suitable for catalyzing Suzuki-Miyaura CC-coupling reactions.

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14-11-2013 дата публикации

Catalyst for the hydrogenation of unsaturated hydrocarbons and process for its preparation

Номер: US20130303812A1
Принадлежит: Shell Oil Co

The present invention relates to a catalyst for the hydrogenation of unsaturated hydrocarbons, in particular aromatics with a broad molecular weight range, a process for the production thereof and a process for hydrogenating unsaturated hydrocarbons.

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28-11-2013 дата публикации

Nickel-M-Alumina Xerogel Catalyst, Method for Preparing the Same, and Method for Preparing Methane Using the Catalyst

Номер: US20130317127A1
Принадлежит: Posco Co Ltd

A nickel-M-alumina hybrid xerogel catalyst for preparing methane, wherein the metal M is at least one element selected from the group consisting of Fe, Co, Ni, Ce, La, Mo, Cs, Y, and Mg, a method for preparing the catalyst and a method for preparing methane using the catalyst are provided. The catalyst has strong resistance against a high-temperature sintering reaction and deposition of carbon species, and can effectively improve a conversion ratio of carbon monoxide and selectivity to methane.

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28-11-2013 дата публикации

Process for non-oxidative dehydrogenation of alkane

Номер: US20130317273A1
Принадлежит: Saudi Basic Industries Corp

The invention relates to a process for producing an alkene by non-oxidative dehydrogenation of an alkane, comprising contacting a feed stream comprising the alkane with a catalyst composition comprising an unsupported catalyst comprising ZrV 2 O 7 at a temperature of 400 to 600° C.

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02-01-2014 дата публикации

Process for making isooctenes from aqueous isobutanol

Номер: US20140005443A1
Принадлежит: EI Du Pont de Nemours and Co

The present invention relates to a catalytic process for making isooctenes using a reactant comprising isobutanol and water. The isooctenes so produced are useful for the production of fuel additives.

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13-02-2014 дата публикации

Isomerization of light alpha-olefins to light internal olefins

Номер: US20140046110A1
Принадлежит: BASF SE

The present invention relates to a process for isomerizing linear alpha-olefins having from 4 to 8 carbon atoms over a heterogeneous catalyst, wherein the catalyst comprises a hydrogenation metal and a selectivity promoter selected from among selenium and tellurium on a support, and also a process for preparing 1-olefins by a metathesis reaction of 2-olefins with ethene, wherein the 2-olefins are prepared by the above mentioned isomerization process.

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27-02-2014 дата публикации

3,3',4,4'-tetraalkyl cyclohexylbenzene and method for producing same

Номер: US20140058143A1
Принадлежит: UBE Industries Ltd

The present invention relates to a 3,3′,4,4′-tetraalkyl cyclohexylbenzene represented by the general formula (1): wherein R represents an alkyl group having 1 to 4 carbon atoms, which may be easily converted into a 3,3′,4,4′-biphenyltetracarboxylic acid and a 3,3′,4,4′-biphenyltetracarboxylic dianhydride thereof, which are a starting material for a polyimide, via a 3,3′,4,4′-tetraalkylbiphenyl; and a method for producing the same.

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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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20-03-2014 дата публикации

Even carbon number paraffin composition and method of manufacturing same

Номер: US20140081057A1
Принадлежит: Syntroleum Corp

Paraffin compositions including mainly even carbon number paraffins, and a method for manufacturing the same, is disclosed herein. In one embodiment, the method involves contacting naturally occurring fatty acid/glycerides with hydrogen in a slurry bubble column reactor containing bimetallic catalysts with equivalent particle diameters from about 10 to about 400 micron. The even carbon number compositions are particularly useful as phase change material.

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07-01-2016 дата публикации

ALUMINA MATERIALS WITH INCREASED SURFACE ACIDITY, METHODS FOR MAKING, AND METHODS FOR USING THE SAME

Номер: US20160001265A1
Принадлежит:

Aluminas with increased surface acidity, methods of making the same, and methods for using the same are provided. In an exemplary embodiment, a method for increasing the surface acidity of an alumina material includes providing an alumina starting material, and processing the alumina starting material under hydrothermal conditions in the presence of one or more organic acids to generate a hydrothermally treated alumina. In this embodiment, the one or more organic acids includes a polyprotic organic acid with a pKa value of about 0 to about 10, and the resulting hydrothermally treated alumina has increased surface acidity relative to the alumina starting material. 1. A method for increasing surface acidity of an alumina material , the method comprising the steps of:providing an alumina starting material; andprocessing the alumina starting material under hydrothermal conditions in the presence of an organic acid to generate a hydrothermally treated alumina,wherein the organic acid comprises a polyprotic organic acid with a pKa value of about 0 to about 10, and the hydrothermally treated alumina has increased surface acidity relative to the alumina starting material.2. The method of claim 1 , wherein the organic acids comprises tartaric acid claim 1 , malic acid claim 1 , citric acid claim 1 , or a mixture thereof.3. The method of claim 1 , wherein the alumina starting material comprises a gamma alumina.4. The method of claim 1 , wherein the hydrothermally treated alumina comprises a boehmite alumina.5. The method of claim 4 , further comprising calcining the hydrothermally treated alumina to convert at least a portion of the boehmite alumina in the hydrothermally treated alumina into a gamma alumina.6. The method of claim 5 , wherein the gamma alumina has a Brunauer claim 5 , Emmett and Teller (BET) surface area that is ±25% of the alumina starting material.7. The method of claim 4 , wherein substantially all of the hydrothermally treated alumina is a boehmite alumina ...

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07-01-2016 дата публикации

Process for Making Alkylated Aromatic Compound

Номер: US20160001276A1
Принадлежит: ExxonMobil Chemical Patents Inc

A process for producing an alkylated aromatic compound comprises contacting an aromatic starting material and hydrogen with a plurality of catalyst particles under hydroalkylation conditions to produce an effluent comprising the alkylated aromatic compound, the catalyst comprising a composite of a solid acid, an inorganic oxide different from the solid acid and a hydrogenation metal, wherein the distribution of the hydrogenation metal in at least 60 wt % of the catalyst particles is such that the average concentration of the hydrogenation metal in the rim portion of a given catalyst particle is Crim, the average concentration of the hydrogenation metal in the center portion of the given catalyst particle is Ccenter, where 0.2≦Crim/Ccenter<2.0. Also disclosed are hydroalkylation catalyst and process for making phenol and/or cyclohexanone using the catalyst.

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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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02-01-2020 дата публикации

PROCESS FOR THE OLIGOMERIZATION OF ETHYLENE WITH STIRRED GAS/LIQUID REACTOR AND PLUG-FLOW REACTOR SEQUENCE

Номер: US20200001266A1
Принадлежит: IFP ENERGIES NOUVELLES

Reaction device which makes possible the oligomerization of olefins to give linear olefins and preferably linear α-olefins, comprising a gas/liquid reactor and a reactor of plug-flow type. The reaction device is also employed in an oligomerization process. 1. Device comprising:{'b': '1', 'a gas/liquid reactor (), of elongated shape along the vertical axis, comprising a liquid phase and a gas phase located above the said liquid phase,'}{'b': '3', 'a means for introduction of the olefin () into the gas/liquid reactor employing a means for injection of the olefin within the said liquid phase of the gas/liquid reactor,'}{'b': '14', 'a means for introduction of the catalytic system () into the gas/liquid reactor,'}{'b': 13', '1, 'a recirculation loop () comprising withdrawal means in the gas/liquid reactor for the withdrawal and the dispatch of a fraction of withdrawn liquid to a heat exchanger capable of cooling the said liquid fraction, and means for introduction of the said cooled liquid, exiting from the heat exchanger, into the upper part of the gas/liquid reactor (),'}{'b': '11', 'a reactor of plug-flow type () comprising withdrawal means in the gas/liquid reactor for the withdrawal and the dispatch of a fraction of withdrawn liquid to the reactor of plug-flow type and means for recovery of a reaction effluent, at the outlet of the reactor of plug-flow type.'}2. Device according to claim 1 , in which the reactor of plug-flow type is located outside the gas/liquid reactor.3. Device according to claim 1 , in which the reactor of plug-flow type comprises a heat exchanger.4. Olefin oligomerization process employing the device according to claim 1 , at a pressure between 1.0 and 10.0 MPa and at a temperature between 0° C. and 200° C. claim 1 , comprising the following stages:{'b': '1', 'a) a catalytic oligomerization system comprising at least one metal precursor and at least one activating agent is introduced into a gas/liquid reactor () comprising a liquid phase and a ...

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05-01-2017 дата публикации

Method For Producing Hydrocarbon Dehydrogenation Catalyst Using Sponge-Type Support

Номер: US20170001174A1
Принадлежит:

Disclosed are a catalyst for dehydrogenating a paraffinic hydrocarbon and a method of preparing the same, wherein the catalyst is configured such that a sponge-type alumina support having 3D meso/macro pores is directly impregnated with an active metal, thus decreasing the diffusion resistance of a material, realizing structural stability, and maximizing the distribution of the active metal in the support, thereby significantly increasing olefin conversion and selectivity. 1. A method of preparing a catalyst for dehydrogenating paraffin , comprising:providing a sponge-type alumina support having meso/macro pore sizes;thermally treating the support at 800 to 1200° C. for 2 to 10 hr in an air atmosphere;dispersing an active metal precursor in the support so as to be loaded into the support;drying the support having the loaded active metal at 80 to 150° C.; andfiring the dried catalyst at 500 to 900° C. for 2 to 10 hr in an air atmosphere.2. The method of claim 1 , further comprising reducing the fired catalyst at 400 to 700° C. in a hydrogen atmosphere claim 1 , after the firing the dried catalyst.3. The method of claim 1 , wherein the active metal comprises platinum claim 1 , tin claim 1 , or an alkali metal or alkaline earth metal.4. The method of claim 1 , wherein the sponge-type alumina support comprises two kinds of pores having a meso pore size and a macro pore size.5. The method of claim 1 , wherein the sponge-type alumina support is selected from the group consisting of alpha alumina claim 1 , theta alumina claim 1 , silicon carbide claim 1 , and mixtures thereof.6. The method of claim 1 , wherein the sponge-type alumina support has a specific surface area of 50 to 100 m/g claim 1 , a total pore volume of 0.1 to 0.7 cm/g claim 1 , and a pore size of 10 to 100 nm.7. A catalyst for dehydrogenating paraffin claim 1 , prepared by the method of any one of to .8. A method of producing an olefin claim 7 , comprising dehydrogenating a gas mixture comprising paraffin ...

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02-01-2020 дата публикации

Palladium Catalysts Supported on Carbon for Hydrogenation of Aromatic Hydrocarbons

Номер: US20200001274A1
Принадлежит:

Provided is a process for preparing partially or fully hydrogenated hydrocarbons through hydrogenation of aromatic hydrocarbons in the presence of a hydrogenation catalyst. The hydrogenation catalyst comprises palladium deposited on carbon with optional acid wash and calcination treatments and with optional additions of silver and/or alkali metals. 1. A chemical catalyst , comprising an acid-washed carbon base and palladium deposited on said carbon base.2. The chemical catalyst of claim 1 , wherein said carbon base is an activated carbon base.3. The chemical catalyst of claim 1 , wherein said carbon base is calcinated before said palladium is deposited thereon.4. The chemical catalyst of claim 1 , wherein said catalyst comprises from about 0.1 to about 5 weight percentage of palladium.5. The chemical catalyst of claim 1 , further comprising a metal additive deposited on said carbon base with said palladium.6. The chemical catalyst of claim 5 , wherein the molar ratio of said palladium to said metal additive is in a range of from 1:1 to 12:1.7. The chemical catalyst of claim 5 , wherein said metal additive comprises a metal selected from the group consisting of alkali metals and silver.8. A method of making a chemical catalyst claim 5 , comprising the steps of:(i) dissolving a first precursor in deionized water to form a solution;(ii) depositing said solution onto an acid-washed carbon base; and(iii) drying said carbon base in the presence of static air.9. The method of claim 8 , wherein step (ii) is conducted according to the incipient wetness method.10. The method of claim 8 , wherein said carbon base is an activated carbon base.11. The method of claim 8 , further comprising the step of calcining said carbon base prior to the performance of step (ii).12. The method of claim 11 , wherein no calcination treatment is applied to said carbon base following the performance of step (ii).13. The method of claim 11 , wherein said calcining step involves subjecting said ...

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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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07-01-2021 дата публикации

METHOD OF PRODUCING A FUEL ADDITIVE

Номер: US20210002185A1
Принадлежит:

A method of producing a fuel additive includes producing a first product stream comprising butadiene by passing a feed stream comprising C4 hydrocarbons through a steam cracker; transforming greater than or equal to 90 weight % of the butadiene in the first product stream into a second product stream by passing the first product stream through a first hydrogenation unit, wherein the second product stream comprises 1-butene, 2-butene, n-butane, isobutylene, isobutane, or a combination thereof; and converting the second product stream into the fuel additive by passing the second product stream through a fuel additive synthesis unit with an acid catalyst. 1. A method of producing a fuel additive , comprising:producing a first product stream comprising butadiene by passing a feed stream comprising C4 hydrocarbons through a steam cracker;transforming greater than or equal to 90 weight % of the butadiene in the first product stream into a second product stream by passing the first product stream through a first hydrogenation unit, wherein the second product stream comprises 1-butene, 2-butene, n-butane, isobutylene, isobutane, or a combination thereof; andconverting the second product stream into the fuel additive by passing the second product stream through a fuel additive synthesis unit with an acid catalyst.2. The method of claim 1 , wherein the feed stream comprises a portion of an effluent from a fluid catalytic cracking process.3. The method of claim 1 , wherein the feed stream comprises at least one of methyl acetylene claim 1 , propylene claim 1 , 1 claim 1 ,3-butadiene claim 1 , 1 claim 1 ,2-butadiene claim 1 , isobutylene claim 1 , cis-2-butene claim 1 , trans-2-butene claim 1 , 1-butene claim 1 , propene claim 1 , isobutane claim 1 , or n-butane.4. The method of claim 1 , wherein greater than or equal to 95 weight % of the butadiene in the first product stream is transformed into the second product stream.5. The method of claim 1 , wherein the acid catalyst ...

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05-01-2017 дата публикации

Catalyst composite and preparation thereof for isomerization of paraffins

Номер: US20170001924A1
Принадлежит: Hindustan Petroleum Corp Ltd

A catalyst composition is provided for isomerization of paraffins comprising of at least one heteropoly acid and reduced graphene oxide. Further provided are a process for preparation of the catalyst composition and a process for isomerization of paraffins using the catalytic composition.

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05-01-2017 дата публикации

PROPYLENE PRODUCTION USING A MESOPOROUS SILICA FOAM METATHESIS CATALYST

Номер: US20170001925A1
Принадлежит:

Embodiments of a metathesis process for producing propylene comprise providing a metathesis catalyst comprising an amorphous mesoporous silica foam impregnated with metal oxides, where the metathesis catalyst has a pore size distribution of at least 3 nm to 40 nm and a total pore volume of at least 0.700 cm/g. The process further involves producing a product stream comprising propylene by contacting a feed stream comprising butene with the metathesis catalyst. 1. A metathesis process for producing propylene comprising:{'sup': '3', 'providing a metathesis catalyst comprising an amorphous mesoporous silica foam impregnated with metal oxides, where the metathesis catalyst has a pore size distribution of at least 3 nm to 40 nm and a total pore volume of at least 0.700 cm/g; and'}producing a product stream comprising propylene by contacting a feed stream comprising butene with the metathesis catalyst.2. The process of further comprising tri-block copolymer structuring agent claim 1 , where the tri-block copolymer structuring agent is poly(ethylene glycol)-block-poly(propylene glycol)-block-poly(ethylene glycol) structure.3. The process of where the metathesis catalyst catalyzes isomerization of 2-butene to 1-butene followed by cross-metathesis of 2-butene and 1-butene into a metathesis product stream comprising propylene4. The process of where at least 90% of the 2-butene is converted to 1-butene via isomerization.5. The process of where the pore size distribution is from at least 4 nm to 10 nm and the total pore volume is from at least 0.800 cm/g to 1.5 cm/g.6. The process of where the metathesis catalyst has a total acidity from 0.125 mmol/g to 0.500 mmol/g claim 1 , and a surface area of 400 to 500 m/g.7. The process of where the metal oxide is an oxide of molybdenum claim 1 , rhenium claim 1 , tungsten claim 1 , or combinations thereof.8. The process of where the metal oxide is tungsten oxide.9. The process of where the metathesis catalyst has a molar ratio for ...

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05-01-2017 дата публикации

SYSTEMS AND METHODS FOR PRODUCING PROPYLENE

Номер: US20170001926A1
Принадлежит: Saudi Arabian Oil Company

According to one embodiment described in this disclosure, a process for producing propylene may comprise at least partially metathesizing a first stream comprising at least about 10 wt. % butene to form a metathesis-reaction product, at least partially cracking the metathesis-reaction product to form a cracking-reaction product comprising propylene, and at least partially separating propylene from the cracking-reaction product to form a product stream comprising at least about 80 wt. % propylene. 1. A process for producing propylene , the process comprising:{'sup': '3', 'at least partially metathesizing a first composition comprising at least 10 wt. % butene to form a metathesis-reaction product, where the first composition is metathesized with a metathesis catalyst comprising a mesoporous silica catalyst impregnated with metal oxide, where the mesoporous silica catalyst includes a pore size distribution of about 2.5 nm to about 40 nm and a total pore volume of at least about 0.600 cm/g;'}at least partially cracking the metathesis-reaction product to form a cracking-reaction product comprising propylene, where the metathesis-reaction product is cracked with a cracking catalyst comprising a mordenite framework inverted (MFI) structured silica catalyst, where the MFI structured silica catalyst includes total acidity of 0.001 mmol/g to 0.1 mmol/g; andat least partially separating propylene from the cracking-reaction product to form a product composition comprising at least 80 wt. % propylene.2. The process of claim 1 , where the MFI structured silica catalyst has a pore size distribution of at least 1.5 nm to 3 nm.3. The process of claim 1 , where the MFI structured silica catalyst is free of acidity modifiers selected from the group consisting of rare earth modifiers claim 1 , phosphorus modifiers claim 1 , potassium modifiers claim 1 , and combinations thereof.4. The process of claim 1 , where the metathesis catalyst is positioned generally upstream of the cracking ...

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05-01-2017 дата публикации

DUAL CATALYST SYSTEM FOR PROPYLENE PRODUCTION

Номер: US20170001927A1
Принадлежит:

Embodiments of processes for producing propylene utilize a dual catalyst system comprising a mesoporous silica catalyst impregnated with metal oxide and a mordenite framework inverted (MFI) structured silica catalyst downstream of the mesoporous silica catalyst, where the mesoporous silica catalyst includes a pore size distribution of at least 2.5 nm to 40 nm and a total pore volume of at least 0.600 cm/g, and the MFI structured silica catalyst has a total acidity of 0.001 mmol/g to 0.1 mmol/g. The propylene is produced from the butene stream via metathesis by contacting the mesoporous silica catalyst and subsequent cracking by contacting the MFI structured silica catalyst. 1. A process for production of propylene comprising: [{'sup': '3', 'a mesoporous silica catalyst impregnated with metal oxide, where the mesoporous silica catalyst includes a pore size distribution of about 2.5 nm to about 40 nm and a total pore volume of at least about 0.600 cm/g, and'}, 'a mordenite framework inverted (MFI) structured silica catalyst downstream of the mesoporous silica catalyst, where the MFI structured silica catalyst includes a total acidity of 0.001 mmol/g to 0.1 mmol/g,, 'providing a dual catalyst system comprisingproducing propylene from a stream comprising butene via metathesis and cracking by contacting the stream comprising butene with the dual catalyst system, where the stream comprising butene contacts the mesoporous silica catalyst before contacting the MFI structured silica catalyst.2. The process of where the MFI structured silica catalyst has a pore size distribution of at least 1.5 nm to 3 nm.3. The process of where the MFI structured silica catalyst is free of acidity modifiers selected from the group consisting of rare earth modifiers claim 1 , phosphorus modifiers claim 1 , potassium modifiers claim 1 , and combinations thereof.4. The process of where the mesoporous silica catalyst catalyzes isomerization of 2-butene to 1-butene followed by cross-metathesis of ...

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05-01-2017 дата публикации

Systems and methods for producing propylene

Номер: US20170001928A1
Принадлежит: Saudi Arabian Oil Co

According to one or more embodiments described herein, a process for producing propylene, the process comprising at least partially metathesizing a first portion of a first stream to form a first metathesis-reaction product, at least partially cracking the first metathesis-reaction product to form a cracking-reaction product, the cracking reaction product comprising propylene and ethylene, at least partially separating ethylene from at least the cracking reaction product to form a first recycle stream, combining the first recycle stream with a second portion of the first stream to a form a mixed stream, and at least partially metathesizing the mixed stream to from a second metathesis-reaction product. In embodiments, the second metathesis-reaction product may comprise propylene, the first stream may comprise butene, and the first recycle stream may comprise ethylene.

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04-01-2018 дата публикации

PROCESS FOR THE DEHYDRATION OF OXYGENATED COMPOUNDS

Номер: US20180002249A1
Принадлежит: Versalis S.p.A.

The present invention relates to a process for the dehydration of at least one oxygenated compound, preferably selected from saturated alcohols, unsaturated alcohols, diols, ethers, in the presence of at least one dehydration catalyst selected from cerium oxide (CeO), aluminium oxide (γ-AlO), aluminium silicate, silica-aluminas (SiO-AlO), aluminas, zeolites, sulfonated resins, ion-exchange resins, metal oxides (for example, lanthanum oxide, zirconium oxide, tungsten oxide, thallium oxide, magnesium oxide, zinc oxide); of at least one basic agent selected from ammonia (NH), or from inorganic or organic compounds containing nitrogen capable of developing ammonia (NH) during said dehydration process; and, optionally, of silica (SiO), or of at least one catalyst for the dissociation of ammonia (NH) selected from catalysts comprising silica (SiO), preferably of silica (SiO). 1. A process comprising dehydrating at least one oxygenated compound in the presence of{'sub': 2', '2', '3', '2', '2', '3, '(i) at least one dehydration catalyst selected from the group consisting of cerium oxide (CeO), aluminum oxide (γ-AlO), aluminum silicate, silica-alumina (SiOAlO) alumina, a zeolite, a sulfonate resin, an ion exchange resin, and a metal oxide;'}{'sub': 3', '3, '(ii) at least one basic agent selected from the group consisting of ammonia (NH) and an inorganic or organic compound comprising nitrogen capable of developing ammonia (NH) during the dehydration; and'}{'sub': '2', '(iii) optionally silica (SiO).'}2. A process comprising dehydrating at least one oxygenated compound by feeding to a reactor a mixture comprising the oxygenated compound and at least one basic agent selected from the group consisting of ammonia (NH) and an inorganic or organic compound comprising nitrogen capable of developing ammonia (NH) during the dehydration , wherein the mixture is fed to the reactor so as to pass first through a first catalytic bed and subsequently through a second catalytic bed in the ...

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04-01-2018 дата публикации

PROCESS FOR THE PRODUCTION OF DIENES

Номер: US20180002250A1
Принадлежит: Versalis S.p.A.

Process for the production of a diene, preferably a conjugated diene, more preferably 1,3-butadiene, comprising the dehydration of at least one alkenol in the presence of at least one catalytic material comprising at least one acid catalyst based on silica (SiO) and alumina (AIO), preferably a silica-alumina (SiO-AIO), said catalyst having a content of alumina (AIO) lower than or equal to 12% by weight, preferably ranging from 0.1% by weight to 10% by weight, with respect to the total weight of the catalyst. Preferably, said alkenol can be obtained directly from biosynthesis processes, or through the catalytic dehydration of at least one diol, preferably a butanediol, more preferably 1,3-butanediol, even more preferably bio-1,3-butanediol, deriving from biosynthesis processes. Preferably, said 1,3-butadiene is bio-1,3-butadiene. 1. A process for manufacturing a diene , the process comprising dehydrating at least one alkenol in the presence of at least one catalytic material comprising at least one silica (SiO) and alumina (AlO) based acid catalyst , said catalyst having a content of alumina lower than or equal to 12% by weight , relative to a total weight of the catalyst.2. The process according to claim 1 , wherein the alkenol is selected from the group consisting of 3-buten-2-ol (methyl vinyl carbinol) claim 1 , 3-buten-1-ol (allyl carbinol) claim 1 , 2-buten-1-ol (crotyl alcohol) claim 1 , and mixtures thereof.3. The process Process according to claim 1 , wherein the alkenol is directly obtained from a biosynthetic process claim 1 , or by a catalytic dehydration processes of at least one diol claim 1 , deriving from a biosynthetic process.4. The process according to claim 1 , wherein the alkenol derives from catalytic dehydration of at least one diol deriving from the fermentation of sugars.5. The process according to claim 4 , wherein the diol is a bio-1 claim 4 ,3-butanediol deriving from fermentation of sugars obtained from guayule or thistle claim 4 , ...

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04-01-2018 дата публикации

CATALYTIC PROCESS FOR DIENE DIMERIZATION

Номер: US20180002251A1
Принадлежит:

The disclosure relates to a selective head-to-head dimerization of conjugated diene compounds by a catalytic process in a reaction medium without solvent or with solvent comprising hydrocarbons, in the presence of a specific additive of the phenol type. 1. A process for the head-to-head dimerization of conjugated diene compounds comprising contacting , in a reaction medium the conjugated diene compounds with a catalyst in the presence of a phenol compound.2. The process according to claim 1 , wherein the reaction medium comprises a solvent comprising hydrocarbons.3. The process according to claim 1 , wherein the reaction medium is solvent free.4. The process according to claim 1 , wherein the conjugated diene compounds are terminal conjugated diene compounds.5. The process according to claim 1 , wherein the conjugated diene compounds are asymmetric conjugated diene compounds.8. The process according to claim 1 , wherein the conjugated diene compounds are selected from myrcene or farnesene.9. The process according to claim 1 , wherein the catalyst is a homogeneous catalyst.10. The process according to claim 1 , wherein the catalyst is a heterogeneous catalyst.11. The process according to claim 2 , wherein the solvent comprises at least 50% by weight of hydrocarbons.12. The process according to claim 2 , wherein the hydrocarbons comprised in the solvent are chosen from pentane claim 2 , heptane claim 2 , hexane claim 2 , cyclohexane claim 2 , toluene and xylene.13. The process according to claim 1 , wherein the phenol compound is selected from phenol claim 1 , dimethylphenol claim 1 , diethylphenol claim 1 , mesitylphenol claim 1 , 2 claim 1 ,4 claim 1 ,6-trimethylphenol claim 1 , 2 claim 1 ,6-di-tert-butyl-4-methylphenol claim 1 , dichlorophenol claim 1 , 2-hydroxybenzotrifluoride claim 1 , o-methoxyphenol claim 1 , diphenylphenol claim 1 , o-cresol claim 1 , hydroquinone claim 1 , diisopropylphenol claim 1 , or diterbutylphenol.14. The process according to claim 1 , ...

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02-01-2020 дата публикации

Process for Converting Butanol into Propylene

Номер: US20200002244A1
Принадлежит:

Process for selective the conversion of primary C4 alcohol into propylene comprising: contacting a stream () containing essentially a primary C4 alcohol with at least one catalyst at a temperature ranging from 150° C. to 500° C. and at pressure ranging from 0.01 MPa to 10 MPa conditions effective to transform said primary C4 alcohol into an effluent stream () containing essentially propylene, carbon monoxide and di-hydrogen, said transformation of primary C4 alcohol comprising at least a reaction of decarbonylation and optionally a decarboxylation reaction, said at least one catalyst comprising a support being a non-acidic i.e. having a TPD NH3 of less than 50 preferably less than 40 μmol/g and optionally a non-basic catalyst i.e. having a TPD CO2 of less than 100 preferably less than 50 μmol/g. 115.-. (canceled)16. A process for the conversion of primary C4 alcohol into propylene comprising:{'b': 1', '2', '5, 'contacting a stream () containing a primary C4 alcohol with at least one catalyst at a temperature ranging from 150° C. to 500° C. and at pressure ranging from 0.01 MPa to 10 MPa to transform the primary C4 alcohol into an effluent stream (, ) containing propylene, carbon monoxide and di-hydrogen, the transformation of primary C4 alcohol comprising at least a reaction of decarbonylation and optionally a decarboxylation reaction, the at least one catalyst comprising support which is non-acidic, having a TPD NH3 of less than 50 μmol/g and which is also a non-basic, having a TPD CO2 of less than 100 μmol/g.'}17125. The process according to wherein stream () is contacted with the at least one catalyst to produce an effluent stream ( claim 16 , ) wherein at least 1 wt % of primary C4 alcohol is converted into propylene claim 16 , carbon monoxide and di-hydrogen.181121. The process according to claim 16 , wherein the step of contacting the primary C4 alcohol stream () with the at least one catalyst is performed in a single reaction zone (A) and the at least one ...

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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

Photocatalytic Conversion of Carbon Dioxide and Water Into Substituted or Unsubstituted Hydrocarbon(s)

Номер: US20190002364A1
Принадлежит:

A method for the production of hydrocarbon(s), such as methane, substituted hydrocarbons, such as methanol, or the production of hydrogen, the method comprising the steps of contacting a first catalyst with water in order to photocatalyse the splitting of at least some of the water into hydrogen and oxygen; and contacting a second catalyst with a gas stream comprising carbon dioxide and at least some of the hydrogen produced from step (a) in order to photocatalyse the reaction between the hydrogen and carbon dioxide to produce hydrocarbon(s), such as methane, and/or substituted hydrocarbons, such as methanol. In an embodiment, the catalyst comprises gold and or ruthenium nanoclusters supported on a substrate. 1. A method for the production of hydrocarbon(s) , such as methane , or substituted hydrocarbons , such as methanol , the method comprising the steps of:contacting a catalyst with water and carbon dioxide in the presence of light in order to photocatalyse:(i) the splitting of at least some of the water into hydrogen and oxygen; and(ii) the reaction between hydrogen and carbon dioxide to produce at least one of a hydrocarbon and/or substituted hydrocarbons;wherein the catalyst comprises at least gold and ruthenium, in the form of at least one nanocluster supported by a substrate.2. The method according to claim 1 , wherein support substrate is selected from the group comprising graphene claim 1 , graphite claim 1 , carbon black claim 1 , nanotubes claim 1 , fullerenes claim 1 , zeolites claim 1 , carbon nitrides claim 1 , metal nitrides and or oxides including zinc oxide or titanium oxide.3. The method according to claim 1 , wherein the gold and ruthenium nanocluster has at least one Au—Ru bond having a distance in the range of from about 2.5 to 3.0 Å.4. The method according to claim 1 , wherein the gold and ruthenium nanocluster comprise an average cluster size less than about 2 nm.5. A method for the production of hydrocarbon(s) claim 1 , such as methane claim ...

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03-01-2019 дата публикации

Systems and Methods for Producing Naphthalenes and Methylnaphthalenes

Номер: US20190002367A1
Принадлежит:

A process for producing naphthalene or methylnaphthalenes from an alkane-containing stream. In an embodiment, the produce includes providing an alkane-containing feed stream to a reactor, and contacting the ethane-containing stream with an aromatization catalyst within the reactor. The aromatization catalyst comprises molecular sieve, and a dehydrogenation component. In addition, the process includes producing a reactor effluent stream from the reactor, and separating a product stream from the reactor effluent stream. The product stream comprises at least one or both of naphthalene and methylnaphthalene. 1. A process , comprising:(a) providing an alkane-containing feed stream to a reactor;(b) contacting the alkane-containing stream with an aromatization catalyst within the reactor, wherein the aromatization catalyst comprises molecular sieve, and a dehydrogenation component;(c) producing a reactor effluent stream from the reactor; and(d) separating a product stream from the reactor effluent stream, wherein the product stream comprises at least one or both of naphthalene and methylnaphthalene.2. The process of claim 1 , wherein the alkane-containing feed comprises a majority fraction of ethane.3. The process of claim 2 , wherein the molecular sieve of the aromatization catalyst comprises ZSM-5.4. The process of claim 3 , wherein the dehydrogenation component comprises gallium.5. The process of claim 4 , further comprising:(e) removing a majority of one or both of sulfur or nitrogen in the feed stream before providing the feed stream to the reactor in (a).6. The process of claim 5 , wherein the reactor effluent stream contains one or both of:less than 5 ppm sulfur; andless than 5 ppm of nitrogen.7. The process of claim 6 , wherein the contacting in (b) is carried out with a temperature of about 500° C. to about 625° C. claim 6 , a pressure of about 207 kPaa (30 psia) to about 522 kPaa (80 psia) claim 6 , and a WHSV of about 0.1 hrto about 10 hr.8. The process of claim ...

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03-01-2019 дата публикации

NATURAL GAS LIQUID UPGRADING BY IONIC LIQUID CATALYZED ALKYLATION

Номер: US20190002368A1
Принадлежит:

We provide a process, comprising: 1. A process for making one or more middle distillate alkylate products , comprising:a. dehydrogenating a natural gas feedstock comprising saturated hydrocarbons in a dehydrogenation reactor to produce a mixture comprising one or more olefins and one or more unconverted paraffins;b. without further purification or modification other than mixing with an isoparaffin, sending the mixture to a single alkylation reactor that is not thermally coupled with the dehydrogenation reactor;c. alkylating the one or more olefins with the isoparaffin in the single alkylation reactor, using an ionic liquid catalyst, to produce the one or more alkylate products; andd. distilling the one or more alkylate products and collecting a bottoms distillation fraction that is a middle distillate blending component having a sulfur level of 50 wppm or less and a Bromine number less than 1.2. The process of claim 1 , wherein the natural gas feedstock comprises paraffins in the range of from C2 to C6 paraffins.3. The process of claim 1 , wherein the natural gas feedstock is one of a C2 claim 1 , a C3 claim 1 , a C4 claim 1 , a C5 claim 1 , or a C6 paraffin.4. The process of claim 1 , wherein the mixture comprises from 30 to 80 wt % of the one or more unconverted paraffins.5. The process of claim 1 , wherein the one or more alkylate products are selected from the group consisting of an alkylate gasoline claim 1 , an alkylate jet fuel claim 1 , an alkylate diesel fuel claim 1 , and mixtures thereof.6. The process of claim 1 , wherein the isoparaffin is isobutane claim 1 , isopentane claim 1 , an isohexane claim 1 , or a combination thereof.7. The process of claim 1 , wherein a molar ratio of the isoparaffin to the one or more olefins in the single alkylation reactor is from 4:1 to 12:1.8. The process of claim 1 , wherein a molar ratio of the isoparaffin to the one or more olefins in the single alkylation reactor is adjusted to change a boiling range of the one or ...

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03-01-2019 дата публикации

PROCESS TO PREPARE PROPYLENE

Номер: US20190002369A1
Принадлежит: INOVACAT B.V.

The invention is directed to a process to prepare propylene from a mixture of hydrocarbons by performing the following steps. (a) extracting aromatics from the mixture of hydrocarbons thereby obtaining a mixture of hydrocarbons poor in aromatics, (b) contacting the mixture obtained in step (a) with a heterogeneous cracking catalyst as present in a fixed bed thereby obtaining a cracked effluent, (c) separating propylene from the cracked effluent thereby also obtaining a higher boiling fraction, (d) recycling part of the higher boiling fraction to step (b) and at least 5 wt % of the higher boiling fraction to step (a). () 1. A process to prepare propylene from a mixture of hydrocarbons by performing the following steps:a. extracting aromatics from the mixture of hydrocarbons thereby obtaining a mixture of hydrocarbons poor in aromatics,b. contacting the mixture obtained in step (a) with a heterogeneous cracking catalyst as present in a fixed bed thereby obtaining a cracked effluent,c. separating propylene from the cracked effluent thereby also obtaining a higher boiling fraction,d. recycling part of the higher boiling fraction to step (b) and at least 5 wt % of the higher boiling fraction to step (a).2. The process according to claim 1 , wherein in step (d) between 10 and 30 wt % of the higher boiling fraction is recycled to step (a).3. The process according to claim 1 , wherein the mixture of hydrocarbons comprises any one of:(a) between 1 and 70 wt % olefins having 4 or more carbon atoms; or(b) between 1 and 20 wt % olefins having 4 or more carbon; or(c) a mixture of paraffins, olefins, naphthenic and aromatic compounds boiling for more than 90 wt % between 35 and 250° C.4. (canceled)5. (canceled)6. The process according to claim 3 , wherein the mixture of hydrocarbons comprises any one or more of: a light straight run naphtha claim 3 , a fraction as isolated from the effluent selected from of any one or more of the following processes: Fluid Catalytic Cracking ...

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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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20-01-2022 дата публикации

DEHYDROGENATION CATALYSTS AND METHODS FOR USING THEM

Номер: US20220016604A1
Принадлежит:

The present disclosure relates to gallium-based dehydrogenation catalysts that further include additional metal components, and to methods for dehydrogenating hydrocarbons using such catalysts. One aspect of the disclosure provides a calcined dehydrogenation catalyst that includes a gallium species, a cerium species, a platinum promoter, and a silica-alumina support. Optionally, the composition can include a promoter selected from the alkali metals and alkaline earth metals. 1. A dehydrogenation catalyst composition comprisingGa, present in the composition in an amount within the range of 0.5 wt. % to 20 wt. %, calculated as elemental metal on a calcined basis;Ce, present in the composition in an amount within the range of 0.2 wt. % to 20 wt. %, calculated as elemental metal on a calcined basis;Pt, present in the composition in an amount within the range of 1 ppm to 500 ppm, calculated as elemental metal on a calcined basis;optionally, a promoter M2 selected from the alkali metals, the alkaline earth metals, and any mixture thereof, present in the composition in an amount of up to 20 wt. %, calculated as elemental metal on a calcined basis; and{'sub': '2', 'a silica-alumina support S1, present in the composition in an amount within the range of 50 wt. % to 99 wt. %, calculated as oxide on a calcined basis, silica being present in S1 in an amount within the range of 1 wt. % to 30 wt. %, calculated as SiOon a calcined basis.'}2. The catalyst composition of claim 1 , wherein Ga is present in the composition in an amount within the range of 1.5 wt. % to 10 wt. % claim 1 , e.g. claim 1 , 1.5 wt. % to 8.5 wt. % claim 1 , or 1.5 wt. % to 7 wt. % claim 1 , or 1.5 wt. % to 5 wt. % claim 1 , or 1.5 wt. % to 3 wt. % claim 1 , calculated as elemental metal on a calcined basis.3. The catalyst composition of claim 1 , wherein Ce is present in the composition in an amount of 0.5 wt. % to 20 wt. % claim 1 , e.g. claim 1 , 0.5 wt. % to 15 wt. % claim 1 , or 0.5 wt. % to 10 wt. % ...

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12-01-2017 дата публикации

PROCESS FOR MAKING STYRENE USING MICROCHANNEL PROCESS TECHNOLOGY

Номер: US20170007978A1
Принадлежит:

The disclosed invention relates to a process for converting ethylbenzene to styrene, comprising: flowing a feed composition comprising ethylbenzene in at least one process microchannel in contact with at least one catalyst to dehydrogenate the ethylbenzene and form a product comprising styrene; exchanging heat between the process microchannel and at least one heat exchange channel in thermal contact with the process microchannel; and removing product from the process microchannel. Also disclosed is an apparatus comprising a process microchannel, a heat exchange channel, and a heat transfer wall positioned between the process microchannel and heat exchange channel wherein the heat transfer wall comprises a thermal resistance layer. 1178-. (canceled)179. An apparatus , comprising:a process microchannel;a heat exchange channel; anda heat transfer wall positioned between the process microchannel and the heat exchange channel, the heat transfer wall comprising at least one thermal resistance layer.180. The apparatus of wherein the thermal resistance layer is positioned on the heat transfer wall and/or embedded within the heat transfer wall.181. The apparatus of wherein the thermal resistance layer comprises a vacuum claim 179 , a gaseous material claim 179 , a liquid and/or a solid material.182. The apparatus of wherein the thermal resistance layer comprises a solid material which contains void spaces claim 179 , openings and/or through holes.183. The apparatus of wherein the thermal resistance layer comprises one or more strips or shims which contain void spaces claim 179 , openings and/or through holes.184. The apparatus of wherein the thermal resistance layer comprises one or more strips with grooves formed in the strip.185. The apparatus of wherein the thermal resistance layer comprises one or more shims claim 179 , each of the shims having a first surface and a second surface claim 179 , and grooves formed in the first surface and/or the second surface.186. The ...

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12-01-2017 дата публикации

CATALYST AND METHOD FOR AROMATIZATION OF C3-C4 GASES, LIGHT HYDROCARBON FRACTIONS AND ALIPHATIC ALCOHOLS, AS WELL AS MIXTURES THEREOF

Номер: US20170007992A1
Принадлежит: NGT GLOBAL AG

The invention relates to hydrocarbon feedstock processing technology, in particular, to catalysts and technology for aromatization of C-Chydrocarbon gases, light low-octane hydrocarbon fractions and oxygen-containing compounds (C-Caliphatic alcohols), as well as mixtures thereof resulting in producing an aromatic hydrocarbon concentrate (AHCC). The catalyst comprises a mechanical mixture of 2 zeolites, one of which is characterized by the silica/alumina ratio SiO/AlO=20, pre-treated with an aqueous alkali solution and modified with oxides of rare-earth elements used in the amount from 0.5 to 2.0 wt % based on the weight of the first zeolite. The second zeolite is characterized by the silica/alumina ratio SiO/AlO═82, comprises sodium oxide residual amounts of 0.04 wt % based on the weight of the second zeolite, and is modified with magnesium oxide in the amount from 0.5 to 5.0 wt % based on the weight of the second zeolite. Furthermore, the zeolites are used in the weight ratio from 1.7:1 to 2.8:1, wherein a binder comprises at least silicon oxide and is used in the amount from 20 to 25 wt % based on the weight of the catalyst. The process is carried out using the proposed catalyst in an isothermal reactor without recirculation of gases from a separation stage, by contacting a fixed catalyst bed with a gaseous feedstock, which was evaporated and heated in a preheater. The technical result consists in achieving a higher aromatic hydrocarbon yield while ensuring almost complete conversion of the HC feedstock and oxygenates, an increased selectivity with respect to forming xylols as part of an AHCC, while simultaneously simplifying the technological setup of the process by virtue of using a reduced (inter alia, atmospheric) pressure. 14-. (canceled)5. A catalyst for the aromatization of mixtures of hydrocarbons and aliphatic alcohols , the catalyst comprising: a mixture of a first pentasil zeolite and a second pentasil zeolite; the first pentasil zeolite comprising a ...

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12-01-2017 дата публикации

FLUIDIZABLE CATALYSTS FOR OXIDATIVE DEHYDROGENATION OF HYDROCARBONS

Номер: US20170008821A1

Fluidizable catalysts for oxygen-free oxidative dehydrogenation of alkanes to corresponding olefins. The catalysts contain 10-20% (by weight per total catalyst weight) of one or more vanadium oxides as the catalytic material, which are mounted upon an alumina support that is modified with zirconia at alumina/zirconia ratios of 5:1 up to 1:2. Various methods of preparing and characterizing the fluidizable catalysts are also provided. 1: A fluidizable catalyst for oxidative dehydrogenation of an alkane comprising:a zirconia-modified alumina support material; and10-20% of one or more vanadium oxides by weight based on the total catalyst weight, the one or more vanadium oxides being adsorbed onto the support material;wherein the support material comprises an alumina/zirconia weight ratio of 1-5:1-3.2: The fluidizable catalyst of claim 1 , wherein the one or more vanadium oxides are selected from the group consisting of VO claim 1 , VOand VO.3: The fluidizable catalyst of claim 2 , comprising at least 50% of VObased on total weight of the one or more vanadium oxides.4: The fluidizable catalyst of claim 1 , wherein the alumina/zirconia weight ratio is 1-2:1.5: The fluidizable catalyst of claim 1 , wherein the one or more vanadium oxides form a crystalline phase on the surface of the zirconia-modified alumina support material.6: The fluidizable catalyst of claim 1 , having an average particle size of 40-120 μm.7: The fluidizable catalyst of claim 1 , wherein the fluidizable catalyst comprises a plurality of particles and more than 75% of the particles are in the 40-120 μm size range.8: The fluidizable catalyst of claim 1 , having an apparent particle density of 1.5-3.5 g/cm.9: The fluidizable catalyst of claim 1 , having Class B powder properties in accordance with Geldart particle classification.10: The fluidizable catalyst of claim 1 , having a BET surface area of 10-50 m/g.11: The fluidizable catalyst of claim 1 , wherein the zirconia present in the alumina/zirconia ...

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11-01-2018 дата публикации

METHOD FOR PREPARING HIGHLY NITROGEN-DOPED MESOPOROUS CARBON COMPOSITES

Номер: US20180008968A1
Принадлежит:

Some embodiments are directed to a new methodology aimed at preparing highly N-doped mesoporous carbon macroscopic composites, and their use as highly efficient heterogeneous metal-free catalysts in a number of industrially relevant catalytic transformations. 1. A method of preparing macroscopic composites made of a macroscopic support coated with a thin layer of highly nitrogen-doped mesoporous carbon phase (active phase) , said method comprising:{'sub': 4', '2', '3, '(a) providing an aqueous solution of (i) (NH)CO; (ii) a carbohydrate as carbon source, selected from aldose monosaccharides and glycosilated forms thereof, disaccharides and oligosaccharides or dextrine deriving from biomass conversion, and (iii) a carboxylic acid source selected from citric acid, and any other mono-, di-, tri-, and poly-carboxylic acid or their ammonium mono-, di-, tri- and poly-basic forms;'} [ (a1) providing an aqueous solution of citric acid and a carbohydrate as carbon source, selected from aldose monosaccharides and glycosilated forms thereof, disaccharides and oligosaccharides;', '(c1) prior to step (c), immerging/soaking or impregnating the macroscopic support of step (b) in the aqueous solution of step (a1) for a suitable amount of time;', '(d1) optionally removing the immerged macroscopic support from the aqueous solution of step (a1) if an excess aqueous solution is used in step (c1);', '(e1′) optionally subjecting the resulting macroscopic support to a gentle thermal treatment (drying) under air at low temperatures from 45 to 55° C., preferably 50° C.±3° C.;', '(e1) subjecting the resulting macroscopic support to a first thermal treatment (drying) under air at moderate temperatures from 110-150° C.±5° C., preferably 130° C.±5° C.; and', '(f1) subjecting the thermally treated (dried) macroscopic support to a second thermal treatment under inert atmosphere at higher temperatures from 600-800° C.±10° C., preferably 600° C.±5° C.; thereby generating a macroscopic composite ...

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14-01-2016 дата публикации

PROCESS FOR MAKING LINEAR LONG-CHAIN ALKANES FROM RENEWABLE FEEDSTOCKS USING CATALYSTS COMPRISING HETEROPOLYACIDS

Номер: US20160009610A1
Принадлежит:

A hydrodeoxygenation process for producing a linear alkane from a feedstock comprising a saturated or unsaturated Coxygenate that comprises an ester group, carboxylic acid group, carbonyl group and/or alcohol group is disclosed. This process comprises contacting the feedstock with (i) a catalyst comprising about 0.1% to about 10% by weight of a metal selected from Group IB, VIB, or VIII of the Periodic Table, and (ii) a heteropolyacid or heteropolyacid salt, at a temperature between about 150° C. to about 250° C. and a hydrogen gas pressure of at least about 300 psig. By contacting the feedstock with the catalyst and heteropolyacid or heteropolyacid salt under these temperature and pressure conditions, the Coxygenate is hydrodeoxygenated to a linear alkane that has the same carbon chain length as the Coxygenate. 1. A hydrodeoxygenation process for producing a linear alkane from a feedstock comprising a saturated or unsaturated Coxygenate comprising a moiety selected from the group consisting of an ester group , carboxylic acid group , carbonyl group , and alcohol group , wherein the process comprises:{'sub': 10-18', '10-18, 'a) contacting said feedstock with (i) a catalyst comprising about 0.1% to about 10% by weight of a metal selected from Group IB, VIB, or VIII of the Periodic Table, and (ii) a heteropolyacid or heteropolyacid salt, at a temperature between about 150° C. to about 250° C. and a hydrogen gas pressure of at least about 300 psig, wherein the Coxygenate is hydrodeoxygenated to a linear alkane, and wherein the linear alkane has the same carbon chain length as the Coxygenate; and'}b) optionally, recovering the linear alkane produced in step (a).2. The hydrodeoxygenation process of claim 1 , wherein said Coxygenate is a fatty acid or a triglyceride.3. The hydrodeoxygenation process of claim 1 , wherein said feedstock comprises a plant oil or a fatty acid distillate thereof.4. The hydrodeoxygenation process of claim 3 , wherein said feedstock comprises(i) ...

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14-01-2016 дата публикации

Process for Making Alkylated Aromatic Compound

Номер: US20160009613A1
Принадлежит:

A process for producing an alkylated aromatic compound comprises contacting an aromatic starting material and hydrogen with a plurality of catalyst particles under hydroalkylation conditions to produce an effluent comprising the alkylated aromatic compound, the catalyst comprising a composite of a solid acid, an inorganic oxide different from the solid acid and a hydrogenation metal, wherein the distribution of the hydrogenation metal in at least 60 wt % of the catalyst particles is such that the average concentration of the hydrogenation metal in the rim portion of a given catalyst particle is Crim, the average concentration of the hydrogenation metal in the outer portion of a given catalyst particle is Couter, the average concentration of the hydrogenation metal in the center portion of the given catalyst particle is Ccenter, where Crim/Ccenter≧2.0 and/or Couter/Ccenter2.0. Also disclosed are rimmed catalyst and process for making phenol and/or cyclohexanone using the catalyst. 1. A process for producing an alkylated aromatic compound , the process comprising contacting an aromatic starting material and hydrogen with a plurality of catalyst particles under hydroalkylation conditions to produce an effluent comprising the alkylated aromatic compound , the catalyst comprising a composite of a solid acid , an inorganic oxide different from the solid acid and a hydrogenation metal , wherein the distribution of the hydrogenation metal in at least 60 wt % of the catalyst particles is such that:the average concentration of the hydrogenation metal in the rim portion of a given catalyst particle is Crim;the average concentration of the hydrogenation metal in the outer portion of a given catalyst particle is Couter; andthe average concentration of the hydrogenation metal in the center portion of the given catalyst particle is Ccenter; andat least one of the following conditions is met:(i) Crim/Ccenter≧2.0; and(ii) Couter/Ccenter≧2.0.2. The process of claim 1 , wherein the ...

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14-01-2021 дата публикации

A SUPPORTED COBALT-CONTAINING FISCHER-TROPSCH CATALYST, PROCESS FOR PREPARING THE SAME AND USES THEREOF

Номер: US20210008527A1
Принадлежит:

The present invention relates to a process for preparing a cobalt-containing Fischer-Tropsch synthesis catalyst with good physical properties and high cobalt loading. In one aspect, the present invention provides a process for preparing a supported cobalt-containing Fischer-Tropsch synthesis catalyst, said process comprising the steps of: (a) impregnating a support material with cobalt haydroxide nitrate, or a hydrate thereof, of formula (I) below to form an impregnated support material, [Co(OH)(NO).yHO] (I) where: 0 Подробнее

11-01-2018 дата публикации

PROCESS FOR DEHYDRATION OF OXYGENATES WITH HETEROPOLYACID CATALYSTS HAVING MIXED OXIDE SUPPORTS AND USE OF THE SAME

Номер: US20180009725A1
Принадлежит: TECHNIP E&C LIMITED

The present invention relates to a process for producing ethene by the vapour phase dehydration of ethanol using a supported heteropolyacid catalyst. In particular, the present invention involves the use of a supported heteropolyacid catalyst, wherein the supported heteropolyacid catalyst is: i) a mixed oxide support comprising silica and a transition metal oxide, wherein silica is present in an amount of at least 50 wt. %, based on the weight of the mixed oxide support; or ii) a mixed oxide support comprising zirconia and a different transition metal oxide, wherein zirconia is present in an amount of at least 50 wt. %, based on the weight of the mixed oxide support. When used in a process for the preparation of ethene by vapour phase dehydration, and after attaining steady-state performance of the catalyst, the process may be operated continuously with the same supported heteropolyacid catalyst for at least 150 hours without any regeneration of the catalyst. 1. A process for the vapour phase chemical dehydration of ethanol in a reactor in the presence of a supported heteropolyacid catalyst , wherein the support of the supported heteropolyacid catalyst is: i) a mixed oxide support comprising silica and a transition metal oxide , wherein silica is present in an amount of at least 50 wt. % , based on the weight of the mixed oxide support; or ii) a mixed oxide support comprising zirconia and a different transition metal oxide , wherein zirconia is present in an amount of at least 50 wt. % , based on the weight of the mixed oxide support; and wherein , after attaining steady-state performance of the catalyst , said process is operated continuously with the same supported heteropolyacid catalyst for at least 150 hours , without any regeneration of the catalyst.2. A process according to claim 1 , wherein claim 1 , after attaining steady-state performance of the catalyst claim 1 , the process is operated continuously with the same supported heteropolyacid catalyst for at ...

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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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14-01-2021 дата публикации

Linear Alpha Olefin Processes

Номер: US20210009486A1
Принадлежит:

The present disclosure provides assemblies for producing linear alpha olefins and methods for producing linear alpha olefins. In at least one embodiment, a method for producing a linear alpha olefin includes oligomerizing an olefin in the presence of a catalyst and a process solvent in at least one reactor, quenching the reactor effluent, and subjecting the quenched effluent to separation steps to obtain a stream enriched in one or more linear alpha olefins. 1. A method for forming one or more linear alpha olefins , the method comprising the steps of:(a) providing a feed comprising an olefin, a catalyst, and a process solvent to a reaction zone including at least one reactor under oligomerization conditions to obtain a reactor effluent produced in the at least one reactor;(b) contacting at least a portion of the reactor effluent with a quench agent to obtain a quenched effluent;(c) separating at least a portion of the quenched effluent to obtain a vapor effluent and a liquid effluent;(d) separating at least a portion of the liquid effluent to obtain at least one aqueous phase enriched in catalyst and quench agent and an organic phase depleted in catalyst and quench agent;(e) separating at least a portion of the organic phase to obtain a stream enriched in one or more linear alpha olefins.2. The process of claim 1 , wherein the feed comprises <25 ppb water by weight.3. The method of claim 1 , wherein step (a) comprises:providing the feed to a first tubular reactor under oligomerization conditions to obtain a first effluent; andtransferring the first effluent to a second tubular reactor under oligomerization conditions to obtain the reactor effluent.4. The method of claim 3 , further comprising providing steam to a first steam jacket disposed around the first tubular reactor and providing steam to a second team jacket disposed around the second tubular reactor claim 3 ,optionally further comprising controlling the pressure of steam in the first steam jacket pressure ...

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08-01-2015 дата публикации

Production Method for 1-Chloro-3,3,3-Trifluoropropene

Номер: US20150011806A1
Принадлежит: CENTRAL GLASS COMPANY, LIMITED

A production method of 1-chloro-3,3,3-trifluoropropene according to the present invention includes reaction of 1,1,1,3,3-pentachloropropane with hydrogen fluoride, characterized in that the concentrations of respective catalytic components in the 1,1,1,3,3-pentachloropropane as the raw material is controlled to a predetermined level or less. By controlling the concentrations of the respective catalytic components in the 1,1,1,3,3-pentachloropropane to the predetermined level or less, it is possible to improve the problems of shortening of catalyst life, retardation of reaction and scaling or corrosion of equipment in the production of the 1-chloro-3,3,3-trifluoropropene. In addition, the 1,1,1,3,3-pentachloropropane can be obtained selectively with high yield by telomerization reaction of carbon tetrachloride and vinyl chloride. The present invention is thus useful as the method for industrially advantageous, high-yield production of the 1-chloro-3,3,3-trifluoropropene. 1. A method for producing 1-chloro-3 ,3 ,3-trifluoropropene , comprising reacting 1 ,1 ,1 ,3 ,3-pentachloropropane with hydrogen fluoride in a reaction system ,wherein the method comprises a concentration control step of controlling the concentrations of a metal solubilizer and/or a hydrochloride thereof and an iron complex in the 1,1,1,3,3-pentachloropropane supplied to the reaction system to be 100 ppm or less.2. The method according to claim 1 , wherein the metal solubilizer is at least one kind selected from the group consisting of N claim 1 ,N-dimethylacetamide claim 1 , acetonitrile claim 1 , 2-aminoacetonitrile claim 1 , N claim 1 ,N-dimethylformamide and hexamethylphosphoric amide.3. The method according to claim 1 , wherein the iron complex is a complex of N claim 1 ,N-dimethylacetamide claim 1 , iron (II) chloride and iron (III) chloride (FeCl.2FeCl.6DMAC).4. The method according to claim 1 , wherein the concentration control step includes claim 1 , before supplying the 1 claim 1 ,1 claim 1 ...

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08-01-2015 дата публикации

High Density Cyclic Fuels Derived From Linear Sesquiterpenes

Номер: US20150011810A1
Автор: Benjamin G Harvey
Принадлежит: US Department of Navy

A method to generate cyclic hydrocarbons from farnesene to increase both the density and net heat of combustion of the product fuels. The high density hydrocarbons produced by this method have applications for missile, UAV, jet, and diesel propulsion.

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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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09-01-2020 дата публикации

Conversion of mixtures of c2-c8 olefins to jet fuel and/or diesel fuel in high yield from bio-based alcohols

Номер: US20200010767A1
Принадлежит: Gevo Inc

The present disclosure provides methods and materials for oligomerization of lower olefins (e.g., C 2 -C 8 ) to transportations fuels including diesel and/or jet fuel. The oligomerization employs, in certain embodiments, tungstated zirconium catalysts. Surprisingly, the oligomerizations proceed smoothly in high yields and exhibit little to no sensitivity to the presence of significant amounts of oxygenates (e.g., water, lower alcohols such as C 2 -C 8 alcohols) in the feed stream. Accordingly, the present disclosure is uniquely suited to the production of fuels derived from bio-based alcohols, wherein olefins produced from such bio-based alcohols typically contain high levels of oxygenates.

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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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17-01-2019 дата публикации

METHOD OF TREATING BUTENE TO FORM PROPYLENE/ETHYLENE MIXTURE

Номер: US20190015822A1

A method of producing propylene and ethylene from a butene-containing hydrocarbon stream by cracking olefin compounds in the butene-containing hydrocarbon stream in the presence of a core-shell ZSM catalyst, wherein the core-shell ZSM catalyst comprises a ZSM-5 core and a silica shell disposed thereon. Various embodiments of the method of producing propylene and ethylene, and the method of making the core-shell ZSM catalyst are also provided. 1. A method of treating butene to form a mixture of propylene and ethylene , comprising:contacting a butene-containing hydrocarbon stream with a core-shell ZSM catalyst in a fixed-bed reactor to form a product stream comprising propylene and ethylene, wherein the core-shell ZSM catalyst is present in the fixed bed reactor as particles having a diameter of 0.5-1.0 mm packed in the fixed bed reactor,wherein at least 50 wt % of the butene-containing hydrocarbon stream is butene, andwherein the core-shell ZSM catalyst comprises:a ZSM-5 core, anda silica shell having a thickness in the range of 0.5 to 50 μm, which covers at least a portion of a surface of the ZSM-5 core.25-. (canceled)6. The method of claim 1 , wherein at least 50 wt % of the product stream is propylene and ethylene.7. The method of claim 1 , wherein a propylene-to-ethylene weight ratio of the product stream is within the range of 0.2 to 4.8. The method of claim 1 , further comprising:treating the core-shell ZSM catalyst with nitrogen at a temperature in the range of 400 to 700° C. prior to the contacting.9. The method of . further comprising:mixing the butene-containing hydrocarbon stream with nitrogen to form a gaseous mixture prior to the contacting, wherein a partial pressure of the butene-containing hydrocarbon stream in the gaseous mixture is within the range of 5 to 50 psi.10. The method of claim 1 , wherein the butene-containing hydrocarbon stream is contacted with the core-shell ZSM catalyst at a temperature in the range of 400 to 700° C. claim 1 , and a ...

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17-01-2019 дата публикации

METHOD FOR MAKING A CATALYST AND CRACKING A HYDROCARBON STREAM TO FORM PROPYLENE/ETHYLENE

Номер: US20190015823A1

A method of producing propylene and ethylene from a butene-containing hydrocarbon stream by cracking olefin compounds in the butene-containing hydrocarbon stream in the presence of a core-shell ZSM catalyst, wherein the core-shell ZSM catalyst comprises a ZSM-5 core and a silica shell disposed thereon. Various embodiments of the method of producing propylene and ethylene, and the method of making the core-shell ZSM catalyst are also provided. 1. A method for making a catalyst and cracking a hydrocarbon stream to form propylene and ethylene , comprising:mixing a ZSM silicalite with a silicalite gel to form a silicalite mixture, hydrothermally treating the silicalite mixture then calcining to form a core-shell ZSM catalyst.contacting a butene-containing hydrocarbon stream with the core-shell ZSM catalyst in a fixed-bed reactor to form a product stream comprising propylene and ethylene,wherein at least 50 wt % of the butene-containing hydrocarbon stream is butene, and a ZSM-5 core, and', 'a silica shell having a thickness in the range of 0.5 to 50 μm, which covers at least a portion of a surface of the ZSM-5 core., 'wherein the core-shell ZSM catalyst comprises2. The method of claim 1 , wherein the silica shell has a thickness in the range of 0.5 to 30 μm.3. The method of claim 1 , wherein the core-shell ZSM catalyst is dispersed in a silica and/or an alumina binder.4. The method of claim 1 , wherein a weight percent of the silica shell in the core-shell ZSM catalyst is within the range of 4 to 75 wt % claim 1 , with the weight percent being relative to the total weight of the core-shell ZSM catalyst.5. The method of claim 1 , wherein the core-shell ZSM catalyst has an acidity of less than 0.1 mmol/g.6. The method of claim 1 , wherein at least 50 wt % of the product stream is propylene and ethylene.7. The method of claim 1 , wherein a propylene-to-ethylene weight ratio of the product stream is within the range of 0.2 to 4.8. The method of claim 1 , further comprising: ...

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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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21-01-2016 дата публикации

METHODS AND SYSTEMS FOR ENERGY CONVERSION AND GENERATION

Номер: US20160017800A1
Автор: Simpson Robert
Принадлежит:

The invention relates to methods and systems of converting electrical energy to chemical energy and optionally reconverting it to produce electricity as required. In preferred embodiments the source of electrical energy is at least partially from renewable source. The present invention allows for convenient energy conversion and generation without the atmospheric release of CO2. One method for producing methane comprises electrolysis of water to form hydrogen and oxygen, and using the hydrogen to hydrogenate carbon dioxide to form methane. It preferred to use the heat produced in the hydrogenation reaction to heat the water prior to electrolysis. The preferred electrical energy source for the electrolysis is a renewable energy source such as solar, wind, tidal, wave, hydro or geothermal energy. The method allows to store the energy gained at times of low demand in the form of methane which can be stored and used to generate more energy during times of high energy demand. A system comprising an electrolysis apparatus and a hydrogenation apparatus, and a pipeline for the transportation of two fluids, is also described.

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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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21-01-2021 дата публикации

Olefin aromatization catalyst, preparation method and use thereof, and low-carbon olefin aromatization process

Номер: US20210016261A1

The present discloses an aromatization catalyst, preparation process and application thereof and a low-carbon olefin aromatization process. The aromatization catalyst comprises a microporous material, a binder and a modifier; the microporous material is a zeolite molecular sieve, the binder is alumina, the modifier is phosphorus, and the molar ratio of the aluminum element in the binder to the phosphorus element is more than or equal to 1 and less than 5; the ratio of the acidity of the strongly acidic sites to the acidity of the weakly acidic sites of the olefin aromatization catalyst is less than 1.

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21-01-2021 дата публикации

Processes for Converting Aromatic Hydrocarbons via Alkyl-Demethylation

Номер: US20210017102A1
Принадлежит:

Alkyl-demethylation of C2+-hydrocarbyl substituted aromatic hydrocarbons can be utilized to treat one or more of a heavy naphtha reformate stream, a hydrotreated SCN stream, a C8 aromatic hydrocarbon isomerization feed stream, a C9+ aromatic hydrocarbon transalkylation feed stream, and similar hydrocarbon streams to produce additional quantity of xylene products. 1. A process for making xylenes , the process comprising:(I) providing a C6+ aromatic hydrocarbon-containing stream comprising a C2+-hydrocarbyl-substituted aromatic hydrocarbon, wherein the C2+-hydrocarbyl-substituted aromatic hydrocarbon has (i) a C2+ alkyl substitute attached to an aromatic ring therein and/or (ii) an aliphatic ring annelated to an aromatic ring therein;(II) optionally contacting the C6+ aromatic hydrocarbon-containing stream with a first alkyl-demethylation catalyst in a first alkyl-demethylation zone under a first set of alkyl-demethylation conditions to convert at least a portion of the C2+-hydrocarbyl-substituted aromatic hydrocarbon to an alkyl-demethylated aromatic hydrocarbon to obtain an optional first alkyl-demethylated effluent exiting the first alkyl-demethylation zone;(III) separating at least a portion of the C6+ aromatic hydrocarbon-containing stream and/or the first alkyl-demethylated effluent in a first separation apparatus to obtain a C6-C7 hydrocarbons-rich stream and a first C8+ aromatic hydrocarbons-rich stream;(IV) optionally contacting the first C8+ aromatic hydrocarbons-rich stream with a second alkyl-demethylation catalyst in a second alkyl-demethylation zone under a second set of alkyl-demethylation conditions to convert at least a portion of the C2+-hydrocarbyl-substituted aromatic hydrocarbon, if any, contained in the first C8+ aromatic hydrocarbons-rich stream to an alkyl-demethylated aromatic hydrocarbon to obtain an optional second alkyl-demethylated effluent exiting the second alkyl-demethylation zone;(V) separating at least a portion of the first C8+ ...

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21-01-2021 дата публикации

Transalkylation Processes for Converting Aromatic Hydrocarbons Comprising Alkyl-Demethylation

Номер: US20210017103A1
Принадлежит: ExxonMobil Chemical Patents Inc

Alkyl-demethylation of C2+-hydrocarbyl substituted aromatic hydrocarbons can be utilized to treat one or more of a heavy naphtha reformate stream, a hydrotreated SCN stream, a C8 aromatic hydrocarbon isomerization feed stream, a C9+ aromatic hydrocarbon transalkylation feed stream, and similar hydrocarbon streams to produce additional quantity of xylene products.

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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

CONVERSION OF OLIGOMERIC STARCH, CELLULOSE, HYDROLYSATES OR SUGARS TO HYDROCARBONS

Номер: US20170022122A1
Принадлежит:

Embodiments of the present invention are directed to the conversion of a source material (e.g., a depolymerized oligosaccharide mixture, a monomeric sugar, a hydrolysate, or a mixture of monomeric sugars) to intermediate molecules containing 7 to 26 contiguous carbon atoms. These intermediates may also be converted to saturated hydrocarbons. Such saturated hydrocarbons are useful as, for example, fuels. 1. A process of preparing a saturated hydrocarbon comprising:combining a source material with a dicarbonyl under conditions suitable to form an intermediate mixture, the source material comprising a depolymerized oligosaccharide mixture, a monomeric sugar, a hydrolysate, or a mixture of monomeric sugars; andadding hydrogen and a hydrogenation catalyst to the intermediate mixture under conditions suitable to form the saturated hydrocarbon.2. The process of claim 1 , wherein the dicarbonyl is methyl acetoacetate claim 1 , ethyl acetoacetate claim 1 , i-propyl acetoacetate claim 1 , 2 claim 1 ,4-pentanedione claim 1 , n-propyl acetoacetate claim 1 , malonate esters claim 1 , cyanoacetates claim 1 , or a mixture thereof.3. The process of claim 2 , wherein the dicarbonyl is 2 claim 2 ,4-pentanedione.4. The process of claim 1 , wherein the saturated hydrocarbon is 3-ethylnonane.5. The process of claim 1 , wherein the hydrogenation catalyst is palladium/carbon or nickel.6. The process of claim 1 , wherein the source material comprises a depolymerized oligosaccharide mixture claim 1 , and the depolymerized oligosaccharide mixture is prepared by heating an oligosaccharide for a time sufficient to form the depolymerized oligosaccharide mixture.7. The process of claim 6 , wherein the heating is achieved using microwave radiation.8. The process of claim 6 , wherein the heating of the oligosaccharide to form the depolymerized oligosaccharide mixture is under acidic conditions.9. The process of claim 8 , wherein the acidic conditions are achieved using hydrochloric acid claim 8 , ...

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26-01-2017 дата публикации

MANUFACTURE OF ETHYLENE FROM ETHANOL

Номер: US20170022123A1
Автор: STAUFFER John E.
Принадлежит:

Ethylene is produced from ethanol in a one-step process by reacting ethanol with hydrogen chloride over a silica alumina catalyst. 13-. (canceled)4. A process for the manufacture of ethylene from ethanol comprising the steps of:reacting ethanol with hydrogen chloride over a solid catalyst chosen from the group consisting of activated charcoal and zinc chloride in a temperate range of about 325° C. to 375° C. to dehydrate the ethanol and render ethylene and water; andseparating the ethylene from the water.5. The process defined in carried out at a pressure of between 1 and 10 atmospheres.6. A process as defined in wherein the reactions{'sub': 2', '5', '2', '5', '2, 'CHOH+HCl→CHCl+HO'}{'sub': 2', '5', '2', '4, 'CHCl→CH+HCl'}are carried out simultaneously to yield{'sub': 2', '5', '2', '4', '2, 'CHOH→CH+HO.'} The present invention relates to a process for manufacturing ethylene from ethanol. The process is conducted in one step by reacting ethanol with hydrogen chloride over a solid catalyst, thereby dehydrating the ethanol to render ethylene and water.There is growing interest in the manufacture of ethylene from renewable sources. This trend is motivated by concerns about global warming and the uncertainty about prices of petroleum feedstock. As a result, leading manufacturers of ethylene are turning to ethanol as a raw material. The ethanol may be supplied by the fermentation of sugar from either sugar cane or corn syrup. The chemistry for producing ethylene from ethanol is well known. It is straightforward in concept, having been the subject of much academic research. Ethylene is formed by the dehydration of ethanol in the vapor phase reaction when the alcohol is passed over a catalyst of gamma aluminum oxide at a temperature in the range of 348° to 428° C.The commercial application of this technology, however, presents certain problems. The catalyst life is limited. Byproducts are formed, including such impurities as heavy residues, as well as light ends. ...

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26-01-2017 дата публикации

METHOD FOR DEHYDRATING A MIXTURE CONTAINING ETHANOL AND ISOPROPANOL

Номер: US20170022124A1
Принадлежит:

Production of a mixture of ethylene and propylene from a mixture containing ethanol and isopropanol and having a water content between 30 and 75 wt. % is obtained by a process comprising: 2. Process according to claim 1 , in which the mixture contains between 1 and 75% by weight of ethanol and between 99 and 25% by weight of isopropanol with respect to the total weight of ethanol and isopropanol.3. Process according to claim 1 , in which the aluminas (A) and (B) are gamma aluminas.4. Process according to claim 1 , in which the alumina (A) has a mean mesopore diameter comprised between 6 and 12 nm and preferably comprised between 7 and 11 nm.5. Process according to claim 1 , in which the alumina (B) has a BET specific surface area measured according to the standard ASTM D 3663-03 comprised between 150 and 180 m/g.6. Process according to claim 1 , in which the alumina (B) has a mean mesopore diameter comprised between 15 and 20 nm.7. Process according to claim 1 , in which when the mixture also comprises butanol claim 1 , said mixture is treated in order to separate the butanol before dehydration stage a).8. Process according to claim 7 , in which a separation of the butanol is carried out by distillation.930305343735. Process according to claim 1 , in which before stage a) the mixture is brought into contact with an aromatic cut comprising a mixture of aromatic compounds having 7 to 10 carbon atoms claim 1 , in a separation unit comprising a liquid-liquid extraction column () claim 1 , so as to separate from said extraction column () an aqueous fraction () and an organic fraction containing the aromatic cut claim 1 , ethanol and isopropanol claim 1 , and said organic fraction is sent into a distillation column () configured in order to extract an effluent () containing the aromatic cut and a mixture () containing ethanol and isopropanol claim 1 , and said mixture is sent into the dehydration unit.10. Process according to claim 9 , in which the aromatic cut is a ...

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26-01-2017 дата публикации

Processes for producing polymer grade light olefins from mixed alcohols

Номер: US20170022125A1
Автор: Geoffrey W. Fichtl
Принадлежит: UOP LLC

Processes for providing a high purity olefin product are described. The processes involve dehydrating a feedstream comprising a mixture of alcohols having 3 to 8 carbon atoms and forming a mixed olefin stream and a water stream, the mixed olefin stream comprising a mixture of olefins having 3 to 8 carbon atoms. The mixed olefin stream is separated into at least a C 3 olefin stream comprising olefins having 3 carbon atoms and a C 4-8 olefin stream comprising olefins having 4 to 8 carbon atoms. The C 4-8 olefin stream is separated into a C 4 olefin stream comprising olefins having 4 carbon atoms and a C 5-8 olefin stream comprising olefins having 5 to 8 carbon atoms. At least one of the C 3 olefin stream and the C 4 olefin stream is purified.

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10-02-2022 дата публикации

MULTIMETALLIC CATALYSTS FOR METHANATION OF CARBON DIOXIDE AND DRY REFORMING OF METHANE

Номер: US20220040677A1
Принадлежит: UCHICAGO ARGONNE, LLC

Processes for forming multimetallic catalysts by grafting nickel precusors to metal oxide supports. Dry reforming reaction catalysts having nickel and promotors grafted to metal oxides supports. Methanation reaction catalysts having nickel and promotors grafted to metal oxides supports. 1. A method of forming a multimetallic catalyst comprising:{'sub': 2', '3', '2', '2', '2, 'grafting an organometallic promotor comprising a metal selected from the group consisting of B, Cu, Co, Fe, Mn, Sn, Mg, V, and Zn and an organic ligand, onto a metal oxide support selected from the group consisting of AlO, CeO, MgO, SiO, and TiO, forming a promotor-support material;'}calcine the organometallic promotor in air to form a calcined promotor-support material;grafting an organonickel precursor grafted onto the calcined promotor-support material; andreducing the organonickel grafted promotor-support material to form an active multimetallic catalyst.2. The method of claim 1 , wherein reducing comprises reduction with 5-20% hydrogen at 200-600° C. for 2 hours and the active multimetallic catalyst is a methanation reaction catalyst.3. The method of claim 2 , wherein reducing comprises reduction with 10% hydrogen at 500° C. for 2 hours.4. The method of claim 2 , wherein the metal oxide support comprises CeO.5. The method of claim 4 , wherein the metal is selected from the group consisting of B claim 4 , Co claim 4 , Mn claim 4 , Sn claim 4 , and V.6. The method of claim 1 , wherein the wherein the oxide support comprises AlO.7. The method of claim 4 , wherein the metal is selected from the group consisting of Mg and V.8. The method of claim 1 , wherein reducing comprises reduction with 5-20% hydrogen at 700-850° C. for 2 hours and the active multimetallic catalyst is a dry reforming reaction catalyst.9. The method of claim 1 , wherein reducing comprises reduction with 10% hydrogen at 800° C. for 2 hrs.10. The method of claim 8 , wherein the wherein oxide support is selected from the group ...

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10-02-2022 дата публикации

Catalyst Compositions and Methods for Producing Long-Chain Hydrocarbon Molecules

Номер: US20220040679A1
Автор: WANG Cong

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

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25-01-2018 дата публикации

OLIGOMERIZATION OF ETHYLENE TO LIQUID TRANSPORTATION FUELS WITH POST SYNTHESIS TREATED ZSM-5 CATALYST

Номер: US20180022664A1
Принадлежит: Phillips 66 Company

A process for post synthesis treatment of ZSM-5 catalyst for converting ethylene to liquid fuel products providing substantially improved catalyst life. The treatment comprises either a base treatment, an acid treatment or a two-step treatment where one is with an acid and the other is with a base. The base treatment is provided by a weak sodium hydroxide such as less than 1 Molar concentration. The acid treatment is stronger acid where, for example, a hydrogen chloride solution at greater than 2 Molar concentration is used. 1. Oligomerizing ethylene to transportation fuel products in a reactor with a fixed bed of ZSM-5 catalyst that is essentially free of catalyst metals other than silica and alumina wherein the ZSM-5 catalyst has been provided with post synthesis two step treatment of an acid wash and a base wash to resist coke formation in the zeolite crystallites and extend catalyst life wherein the oligomerizing is conducted at a pressure between 0 psig and 800 psig , a temperature of between 260° C. and 420° C. , and a gas hourly space velocity of between 1000 and 5000 inverse hours and wherein at least 85% of the ethylene is converted.2. The process according to wherein the post synthesis treatment of the catalyst comprises catalyst a base treatment with sodium hydroxide and an acid treatment of hydrogen chloride.3. The process according to wherein the base treatment of sodium hydroxide is at between about 0.001 and about 0.5 Molar concentration.4. The process according to wherein the base treatment of sodium hydroxide is at between about 0.005 and about 0.25 Molar concentration.5. The process according to wherein the base treatment of sodium hydroxide is at between about 0.0075 and about 0.15 Molar concentration.6. The process according to wherein the acid treatment of hydrogen chloride is at between about 1 and 10 Molar concentration.7. The process according to wherein the acid treatment of hydrogen chloride is at between about 2 and 7 Molar concentration.8 ...

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25-01-2018 дата публикации

OLIGOMERIZATION OF ETHYLENE TO LIQUID TRANSPORTATION FUELS WITH POST SYNTHESIS TREATED ZSM-5 CATALYST

Номер: US20180022665A1
Принадлежит: Phillips 66 Company

A process for post synthesis treatment of ZSM-5 catalyst for converting ethylene to liquid fuel products providing substantially improved catalyst life. The treatment comprises either a base treatment, an acid treatment or a two-step treatment where one is with an acid and the other is with a base. The base treatment is provided by a weak sodium hydroxide such as less than 1 Molar concentration. The acid treatment is stronger acid where, for example, a hydrogen chloride solution at greater than 2 Molar concentration is used. 1. Oligomerizing ethylene to transportation fuel products in a reactor with a fixed bed of ZSM-5 catalyst that is essentially free of catalyst metals other than silica and alumina wherein the ZSM-5 catalyst has been provided with post synthesis acid treatment to resist coke formation in the zeolite crystallites and extend catalyst life wherein the oligomerizing is conducted at a pressure between 0 psig and 800 psig , a temperature of between 260° C. and 420° C. , and a gas hourly space velocity of between 1000 and 5000 inverse hours wherein at least 85% of the ethylene is converted.2. The process according to wherein the post synthesis treatment of the catalyst comprises catalyst an acid treatment with hydrogen chloride.3. The process according to wherein the acid treatment is a hydrogen chloride solution at between about 1 and 10 Molar concentration.4. The process according to wherein the acid treatment is between about 2 and 7 Molar concentration.5. The process according to wherein the acid treatment is between about 3 and 5 Molar concentration.6. The process according to wherein the post synthesis treatment of the catalyst further comprises the steps of drying catalyst and calcining the catalyst after the acid treatment.7. The process according to wherein the post synthesis treatment of the catalyst further comprises the steps of drying catalyst at a temperature above 105° C. and calcining the catalyst after the acid treatment at a ...

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25-01-2018 дата публикации

OLIGOMERIZATION OF ETHYLENE TO LIQUID TRANSPORTATION FUELS WITH POST SYNTHESIS TREATED ZSM-5 CATALYST

Номер: US20180022666A1
Принадлежит: Phillips 66 Company

A process for post synthesis treatment of ZSM-5 catalyst for converting ethylene to liquid fuel products providing substantially improved catalyst life. The treatment comprises either a base treatment, an acid treatment or a two-step treatment where one is with an acid and the other is with a base. The base treatment is provided by a weak sodium hydroxide such as less than 1 Molar concentration. The acid treatment is stronger acid where, for example, a hydrogen chloride solution at greater than 2 Molar concentration is used. 1. Oligomerizing ethylene to transportation fuel products in a reactor with a fixed bed of ZSM-5 catalyst that is essentially free of catalyst metals other than silica and alumina wherein the ZSM-5 catalyst has been provided with post synthesis treatment of a base wash to resist coke formation in the zeolite crystallites and extend catalyst life wherein the oligomerizing is conducted at a pressure between 0 psig and 800 psig , a temperature of between 260° C. and 420° C. , and a gas hourly space velocity of between 1000 and 5000 inverse hours and wherein at least 85% of the ethylene is converted.2. The process according to wherein the post synthesis treatment of the catalyst comprises catalyst a base treatment with sodium hydroxide.3. The process according to wherein the base treatment is with a solution of sodium hydroxide at between about 0.001 and about 0.5 Molar concentration.4. The process according to wherein the base treatment is with a solution of sodium hydroxide at between about 0.005 and about 0.25 Molar concentration.5. The process according to wherein the base treatment is with a solution of sodium hydroxide at between about 0.0075 and about 0.15 Molar concentration.6. The process according to wherein the post synthesis treatment of the catalyst further comprises the steps of drying catalyst and calcining the catalyst after the base-acid treatment.7. The process according to wherein the post synthesis treatment of the catalyst ...

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24-01-2019 дата публикации

HETEROGENEOUS CATALYSTS

Номер: US20190022626A1
Принадлежит:

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

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24-01-2019 дата публикации

METHOD OF MAKING AND SEPARATING A PROPYLENE/ETHYLENE MIXTURE FROM BUTENE

Номер: US20190022633A1

A method of producing propylene and ethylene from a butene-containing hydrocarbon stream by cracking olefin compounds in the butene-containing hydrocarbon stream in the presence of a core-shell ZSM catalyst, wherein the core-shell ZSM catalyst comprises a ZSM-5 core and a silica shell disposed thereon. Various embodiments of the method of producing propylene and ethylene, and the method of making the core-shell ZSM catalyst are also provided. 1: A fluidized-bed method of cracking butene to form propylene and ethylene , comprising:contacting a butene-containing hydrocarbon stream with a core-shell ZSM catalyst in a fluidized-bed reactor to form a product stream comprising propylene and ethylene, thenseparating the propylene and ethylene from the product stream with a stripping column,wherein at least 50 wt % of the butene-containing hydrocarbon stream is butene, andwherein the core-shell ZSM catalyst comprises:a ZSM-5 core, anda silica shell having a thickness in the range of 0.5 to 50 μm, which covers at least a portion of a surface of the ZSM-5 core.24-. (canceled)5: The method of claim 1 , wherein the core-shell ZSM catalyst has an acidity of less than 0.1 mmol/g.6: The method of claim 1 , wherein at least 50 wt % of the product stream is propylene and ethylene.7: The method of claim 1 , wherein a propylene-to-ethylene weight ratio of the product stream is within the range of 0.2 to 4.8: The method of claim 1 , further comprising:treating the core-shell ZSM catalyst with nitrogen at a temperature in the range of 400 to 700° C. prior to the contacting.9: The method of claim 1 , further comprising:mixing the butene-containing hydrocarbon stream with nitrogen to form a gaseous mixture prior to the contacting, wherein a partial pressure of the butene-containing hydrocarbon stream in the gaseous mixture is within the range of 5 to 50 psi.10: The method of claim 1 , wherein the butene-containing hydrocarbon stream is contacted with the core-shell ZSM catalyst at a ...

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28-01-2021 дата публикации

SUPPORTED BIMETALLIC CORE-SHELL STRUCTURE CATALYST AND ITS PREPARATION METHOD

Номер: US20210023536A1

The purpose of the invention is to provide a supported bimetallic core-shell structure catalyst and its preparation method. Supporter, metal salt and reducing agent solution are mixed to synthesize the catalyst M@PdM/ZT by using a one-step synthesis method, wherein the active metal particle M@PdM as core-shell structure, M Is the core representing one of the Ag, Pt, Au and Ir. ZT is the supporter, representing one of hydrotalcite (MgAl-LDH), alumina (AlO) and silica (SiO). By changing the temperature and the reaction time to control the kinetic behavior of the reduction of two kinds of metal ions to realize the construction of core-shell structure. Active metal particle composition and shell thickness are regulated by controlling metal ion concentration. The bimetallic core-shell catalyst prepared by this method showed excellent selectivity and stability in acetylene selective hydrogenation and anthraquinone hydrogenation. 1. A preparation method of supported bimetallic core-shell catalyst comprising:{'sub': 3', '6', '5', '7', '2', '2', '2', '6', '2', '5', '7', '2', '3', '4', '2', '2', '3', '2', '5', '7', '2', '2', '3', '2', '2', '3', '2, 'adding M salt and Pd salt to a reducing solution to obtain a mixed salt solution after ultrasonic irradiation for 4-5 min; wherein a total concentration of M and Pd ions is 0.01-20 mmol/L, a molar ratio of M:Pd ions is 0.1 to 10; M is one of Ag, Pt, Au and Ir; M salt is one of AgNO, HPtCl, Pt(CHO), HIrCl.6HO, Ir(CHO)and HAuCl.4HO; Pd salt is one of the PdCl, Pd(NO), Pd(CHO), Pd(CHCOO); the reducing solution is a mixture of reducing agent and deionized water, wherein, a mass ratio of the deionized water is 0-20%; the reducing agent is one of ethylene glycol, isopropanol, N, n-dimethyl acetamide, N, n-dimethyl formamide and glyceraldehyde; stirring and heating the mixed salt solution for 10-30 min under 40-50° C., adding a supporter and continuing to stir for 10-20min; raising temperature to 100-160° C. and keeping the temperature ...

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28-01-2021 дата публикации

METHOD OF PREPARING SILICA SUPPORTED CoMoS HYDRODESULFURIZATION CATALYSTS

Номер: US20210024435A1

A method of preparing hydrodesulfurization catalysts having cobalt and molybdenum sulfide deposited on a support material containing mesoporous silica. The method utilizes a sulfur-containing silane that dually functions as a silica source and a sulfur precursor. The method involves an one-pot strategy for hydrothermal treatment and a single-step calcination and sulfidation procedure. The application of the hydrodesulfurization catalysts in treating a hydrocarbon feedstock containing sulfur compounds to produce a desulfurized hydrocarbon stream is also specified. 1: A method of preparing a CoMoS hydrodesulfurization catalyst , the method comprising:mixing a molybdenum precursor, a cobalt precursor, a mercaptoalkyltrialkoxysilane, a structural directing surfactant, an acid, and a solvent to form a reaction mixture;hydrothermally treating the reaction mixture to form a dried mass; andcalcining the dried mass in an activation gas thereby forming the CoMoS hydrodesulfurization catalyst,wherein:the activation gas is at least one selected from the group consisting of air, argon, nitrogen, helium, hydrogen, and carbon monoxide; andthe CoMoS hydrodesulfurization catalyst comprises cobalt and molybdenum sulfide disposed on a support material comprising a mesoporous silica.2: The method of claim 1 , wherein the CoMoS hydrodesulfurization catalyst is not subjected to a sulfidation with a sulfidation reagent.3: The method of claim 1 , wherein the mercaptoalkyltrialkoxysilane is at least one selected from the group consisting of (mercaptomethyl)trimethoxysilane claim 1 , (mercaptomethyl)triethoxysilane claim 1 , (mercaptomethyl)tripropoxysilane claim 1 , (2-mercaptoethyl)trimethoxysilane claim 1 , (2-mercaptoethyl)triethoxysilane claim 1 , (2-mercaptoethyl)tripropoxysilane claim 1 , (3-mercaptopropyl)trimethoxysilane claim 1 , (3-mercaptopropyl)triethoxysilane claim 1 , and (3-mercaptopropyl)tripropoxysilane.4: The method of claim 3 , wherein the mercaptoalkyltrialkoxysilane is ...

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