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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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Применить Всего найдено 2474. Отображено 197.
27-04-2016 дата публикации

КАТАЛИТИЧЕСКАЯ СИСТЕМА НА ОСНОВЕ АЗОТИРОВАННОГО СМЕШАННОГО ОКСИДА И СПОСОБ ПОЛУЧЕНИЯ ЭТИЛЕН-НЕНАСЫЩЕННЫХ КАРБОНОВЫХ КИСЛОТ ИЛИ СЛОЖНЫХ ЭФИРОВ

Номер: RU2582996C2

Изобретение относится к способу получения α, β этилен-ненасыщенных карбоновых кислот или сложных эфиров, содержащему этапы, где вызывают контакт формальдегида или его подходящего источника с карбоновой кислотой или сложным эфиром формулы R-CH-COOR, где Rобозначает водород или алкильную группу, a Rобозначает водород, алкильную или арильную группу, в присутствии катализатора и возможно в присутствии спирта, где данный катализатор содержит азотированный оксид металла, имеющий, по меньшей мере, два типа катионов металлов Ми М, где Мвыбирают из металлов или металлоидов группы 3, 4, 13 (также называемой IIIA) или 14 (также называемой IVA) Периодической таблицы, и Мвыбирают из металлов металлоидов или фосфора группы 5 или 15 (также называемой VA) Периодической таблицы. Изобретение также относится к каталитической системе для реакции формальдегида или его подходящего источника с карбоновой кислотой или сложным эфиром формулы R-CH-COOR, где Rобозначает водород или алкильную группу, a Rобозначает ...

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22-09-2021 дата публикации

КАТАЛИЗАТОР КАТАЛИТИЧЕСКОГО КРЕКИНГА И ЕГО ПОЛУЧЕНИЕ

Номер: RU2755891C2

Раскрыты катализатор каталитического крекинга и его получение. Катализатор содержит от 20% до 40% по массе, в пересчете на сухое вещество, модифицированного редкоземельными элементами молекулярного сита типа Y, от 2% до 20% по массе, в пересчете на сухое вещество, содержащего добавку оксида алюминия и от 30% до 50% по массе, в пересчете на сухое вещество, глины; причем содержащий добавку оксид алюминия содержит, в пересчете на сухое вещество и в пересчете на массу содержащего добавку оксида алюминия, от 60% до 95% по массе оксида алюминия и от 5% до 40% по массе добавки, которая представляет собой одно или несколько соединений, выбранных из группы, которую составляют соединения, содержащие щелочноземельный металл и/или фосфор. Модифицированное редкоземельными элементами молекулярное сито типа Y имеет содержание оксидов редкоземельных элементов, составляющее от 4% до 12% по массе, содержание фосфора, составляющее от 0% до 10% по массе в пересчете на Р2О5, содержание оксида натрия, составляющее ...

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18-04-2023 дата публикации

СПОСОБ ПОЛУЧЕНИЯ СРЕДНИХ ДИСТИЛЛЯТОВ ИЗ ЛЕГКИХ АЛКАНОВ

Номер: RU2794439C1

Изобретение относится к получению углеводородов из углеводородов с меньшим числом атомов углерода в молекуле. Изобретение касается способа получения средних дистиллятов из легких алканов, содержащего этапы, на которых подвергают каталитическому преобразованию легкие алканы в каталитической установке. С помощью первого каталитического реактора на первом этапе подвергают смесь из метана, этана, пропана, бутана, пентана каталитической дегидроароматизации при температурах 350-500°С в присутствии нано- и микропористых цинк- и индийсодержащих алюмосиликатов с получением смеси производных бензола и полиароматических соединений нафталинового ряда, причем парциальное давление метана составляет от 1 до 3 атмосфер; выделяют из смеси производных бензола и полиароматических соединений нафталинового ряда фракции С8+ смеси, водород- и метансодержащие фракции смеси. С помощью второго каталитического реактора на втором этапе подвергают выделенные фракцию С8+ смеси, водород- и метансодержащие фракции смеси ...

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13-09-2024 дата публикации

Катализатор риформинга бензиновых фракций и способ его получения

Номер: RU2826623C1

Изобретение относится к производству катализатора риформинга бензиновых фракций и может быть использовано в нефтеперерабатывающей промышленности. Катализатор риформинга бензиновых фракций содержит следующие компоненты, масс. %: платина 0,2-0,4, рений 0,2-0,4, бинарное соединение индия и циркония, имеющее мольное отношение In:Zr=1,0:0,6-3,0, 0,07-0,35, хлор 0,8-1,3, алюмооксидный носитель - остальное. Для получения катализатора готовят алюмооксидный носитель из формовочной пасты, полученной последовательным смешиванием при перемешивании псевдобемита, бинарного соединения индия и циркония, имеющего мольное отношение In:Zr=1,0.(0,6-3,0), водного раствора азотной кислоты и воды, перемешиванием с растиранием в течение 8-10 мин, добавлением водного раствора метилцеллюлозы и перемешиванием в течение 30-35 мин, формованием пасты в гранулы, сушкой и прокаливанием в токе воздуха. Полученный алюмооксидный носитель предварительно промывают слабым раствором уксусной кислоты в течение 20-30 мин, затем ...

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27-04-2008 дата публикации

КАТАЛИТИЧЕСКАЯ КОМПОЗИЦИЯ ДЛЯ СЕЛЕКТИВНОГО ПРЕВРАЩЕНИЯ АЛКАНОВ В НЕНАСЫЩЕННЫЕ КАРБОНОВЫЕ КИСЛОТЫ, СПОСОБ ПОЛУЧЕНИЯ КОМПОЗИЦИИ И СПОСОБ ПРИМЕНЕНИЯ КОМПОЗИЦИИ

Номер: RU2006137281A
Принадлежит:

... 1. Каталитическая композиция для получения ненасыщенной карбоновой кислоты из алкана, содержащая соединение формулы Mo1VaSbbNbcMdOx, в которой Мо представляет собой молибден, V означает ванадий, Sb означает сурьму, Nb означает ниобий, М представляет собой галлий, висмут, серебро или золото, а составляет от 0,01 до 1, b составляет от 0,01 до 1, с составляет от 0,01 до 1, d составляет от 0,01 до 1 и х определяется требованиями валентности других присутствующих элементов. 2. Каталитическая композиция по п.1, которая имеет формулу Mo1VaSbbNbc MdM'eOx, в которой М' представляет собой тантал, титан, алюминий, цирконий, хром, марганец, железо, рутений, кобальт, родий, никель, платину, бор, мышьяк, литий, натрий, калий, рубидий, кальций, бериллий, магний, церий, стронций, гафний, фосфор, европий, гадолиний, диспрозий, гольмий, эрбий, тулий, тербий, иттербий, лютеций, лантан, скандий, палладий, празеодим, неодим, иттрий, торий, вольфрам, цезий, цинк, олово, германий, кремний, свинец, барий и таллий ...

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27-11-2009 дата публикации

СПОСОБ ПРИГОТОВЛЕНИЯ КАТАЛИЗАТОРА ГИДРООЧИСТКИ НЕФТЕПРОДУКТОВ

Номер: RU2008120436A
Принадлежит:

... 1. Способ приготовления катализатора с повышенной гидрообессеривающей активностью, включающий пропитку предварительно прокаленного носителя растворами активных компонентов с последующей термообработкой, путем сушки и прокалки, отличающийся тем, что пропитку носителя осуществляют в один этап пропиточным раствором, полученным смешением растворов фосфорномолибденовой кислоты, нитрата кобальта с добавлением растворов кремневольфрамовой кислоты, нитрата никеля, борной кислоты. ! 2. Способ по п.1, отличающийся тем, что полученный катализатор имеет следующий состав, мас.%: ! MoO39,5-20,0P2O50,3-0,9СоО3,0-6,0WO30-9,5SiO20-0,2B2O30-4,0NiO0-2,0носительостальное ...

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10-08-2014 дата публикации

КАТАЛИЗАТОР НА ОСНОВЕ СМЕШАННЫХ ОКСИДОВ И СПОСОБ ПОЛУЧЕНИЯ КАРБОНОВЫХ КИСЛОТ ИЛИ СЛОЖНЫХ ЭФИРОВ С ЭТИЛЕНОВОЙ НЕНАСЫЩЕННОСТЬЮ

Номер: RU2013104203A
Принадлежит:

... 1. Катализатор для взаимодействия формальдегида или его подходящего источника с карбоновой кислотой или сложным эфиром для получения карбоновой кислоты или сложного эфира с этиленовой ненасыщенностью, предпочтительно карбоновых кислот или сложного эфира с этиленовой ненасыщенностью в α, β-положении, где катализатор включает оксид металла, имеющий, по меньшей мере, два типа катионов металла, Ми М, где Мпредставляет собой, по меньшей мере, один металл, выбранный из группы 3 или 4 в 4-6 периодах Периодической таблицы, группы 13 в 3-5 периодах Периодической таблицы, или остающихся элементов в лантаноидной группе (а именно, скандия, иттрия, лантаноидных элементов, титана, циркония, гафния, алюминия, галлия, индия), и Мпредставляет собой, по меньшей мере, один металл, выбранный из группы 5 в 5 или 6 периодах Периодической таблицы или группы 15 в 4 или 5 периодах Периодической таблицы (а именно, ниобия, тантала, мышьяка и сурьмы),в котором отношение М:Mнаходится в диапазоне от 10:1 до 1:10,и в ...

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27-01-2009 дата публикации

КАТАЛИТИЧЕСКАЯ СИСТЕМА И СПОСОБ ВОССТАНОВЛЕНИЯ NOx

Номер: RU2007128028A
Принадлежит:

... 1. Каталитическая система для восстановления NOx,содержащая: катализатор, содержащий металлооксидный носитель, каталитический оксид металла, содержащий, по меньшей мере, один из оксидов: оксид галлия или оксид серебра, и, по меньшей мере, один активирующий металл, выбранный из группы, состоящей из серебра, кобальта, молибдена, вольфрама, индия и их смесей; и газовый поток, содержащий органический восстановитель, содержащий кислород. 2. Каталитическая система по п. 1, в которой указанный металлооксидный носитель включает в себя, по меньшей мере, одного представителя, выбранного из группы, состоящей из оксида алюминия, диоксида титана, диоксида циркония, диоксида серия, карбида кремния и их смесей. 3. Каталитическая система по п. 1, в которой указанный каталитический оксид металла включает окись галлия в диапазоне примерно от 5 мол.% до примерно 31 мол.%. 4. Каталитическая система по п. 1, в которой указанный каталитический оксид металла включает в себя окись галлия в диапазоне примерно от ...

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30-08-1991 дата публикации

Каталитическая композиция для дегидроциклодимеризации С @ -С @ -алифатических углеводородов и способ их дегидроциклодимеризации

Номер: SU1674686A3
Принадлежит: ЮОП ИНК (ФИРМА)

Изобретение относится к каталитической композиции для дегидроциклодимеризации C2- C4алифатических углеводородов и способу их дегидроциклодимеризации. С целью повышения стойкости к закоксовыванию каталитической композиции, она включает следующее соотношение компонентов, мас.%: галлий 0,6 - 1,2 компонент, содержащий оксид алюминия 44,0 - 51,8 цеолит ZSM-типа остальное (с отношением диоксида кремния к оксиду алюминия 32,2 - 71,2. В качестве компонента композиция включает фосфорсодержащий оксид алюминия при массовом отношении фосфора к алюминию 0,21 - 1,0. Получение ароматических углеводородов с 2 - 4 атомами углерода дегидроциклодимеризацией C2- C4-алифатических углеводородов ведут путем контактирования углеводородов при 532 - 545°С, давлении 103 - 517 кПа и часовой объемной скорости 0,8 - 2 ч-1с катализатором указанного состава. 1 табл.

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13-12-2007 дата публикации

Katalysatorsystem und Verfahren zum Reduzieren von NO x

Номер: DE112005003017T5
Принадлежит: GEN ELECTRIC, GENERAL ELECTRIC COMPANY

Katalysatorsystem zum Reduzieren von NOx, umfassend: einen Katalysator mit einem Metalloxid-Katalysatorträger, einem katalytischen Metalloxid mit mindestens einem von Galliumoxid oder Silberoxid und einem fördernden Metall, ausgewählt aus der Gruppe bestehend aus Silber, Cobalt, Molybdän, Wolfram, Indium, Wismut und Mischungen davon; einen Gasstrom mit einem organischen Reduktionsmittel und einer schwefelhaltigen Verbindung.

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22-06-1978 дата публикации

VERFAHREN ZUR HERSTELLUNG VON AROMATISCHEN KOHLENWASSERSTOFFEN

Номер: DE0002755900A1
Принадлежит:

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15-10-1980 дата публикации

Indium catalysts

Номер: GB0002044121A
Автор: Connor, Henry
Принадлежит:

Catalysts comprise indium dispersed within a porous carbonaceous support in such manner that the indium, when molten is substantially retained within the pores of the support. Preferably the catalyst contains up to 7.5 wt% of indium and the carbonaceous support material comprises either a carbon molecular sieve material or charcoal. The catalysts are useful in the dehydrogenation of alcohols to aldehydes and ketones.

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07-09-1983 дата публикации

DEHYDROGENATION CATALYSTS

Номер: GB0002044121B
Автор:

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15-01-1986 дата публикации

METHANE CONVERSION

Номер: GB0008529906D0
Автор:
Принадлежит:

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30-12-1977 дата публикации

DEHYDROCYCLODIMERISING C4 HYDROCARBONS

Номер: GB0001496379A
Автор:
Принадлежит:

... 1496379 Dehydrocyclodimerizing C 4 hydrocarbons BRITISH PETROLEUM CO Ltd 13 Oct 1976 [20 Nov 1975] 47830/75 Heading C5E Aromatic hydrocarbons, particularly benzene, toluene and xylenes, are produced by dehydrocyclodimerizing a C 4 hydrocarbon feed in the presence of a catalyst comprising Ge, In or Sn, in metal or compound form, deposited on a support. The reaction may be carried out in the presence of H 2 or under an atmosphere of N 2 . The support may be Al 2 O 3 , SiO 2 , activated carbon or refractory Ga 2 O 3 . Surface hydroxyl groups on hydrated SiO 2 or hydrated Al 2 O 3 may be exchanged with ions of the catalytic metals and optionally also with ions of Ga, Al or Fe. Preferably the catalytic metals are present as oxides.

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15-09-1986 дата публикации

VERFAHREN ZUR ISOMERISIERUNG DER DOPPELBINDUNG VON N-BUTEN

Номер: ATA192583A
Автор:
Принадлежит:

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15-09-1994 дата публикации

PROCEDURE FOR THE PRODUCTION OF A ALKOXYLIERUNGSADDUKTS.

Номер: AT0000110297T
Принадлежит:

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26-07-2012 дата публикации

Method of forming a catalyst with inhibited mobility of nano-active material

Номер: AU2010337188A1
Принадлежит:

A method of forming a catalyst, comprising: providing a plurality of support particles and a plurality of mobility-inhibiting particles, wherein each support particle in the plurality of support particles is bonded with its own catalytic particle; and bonding the plurality of mobility-inhibiting particles to the plurality of support particles, wherein each support particle is separated from every other support particle in the plurality of support particles by at least one of the mobility-inhibiting particles, and wherein the mobility-inhibiting particles are configured to prevent the catalytic particles from moving from one support particle to another support particle.

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26-03-1992 дата публикации

PROCESSES FOR THE PREPARATION OF CYCLIC ETHERS

Номер: AU0008463891A
Принадлежит:

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27-06-2013 дата публикации

Production of aromatics from renewable resources

Номер: AU2011348031A1
Принадлежит:

Renewable oils are converted to aromatics, by contact with a catalytically-active form of gallium, for use in the petrochemical industry and/or for fuel blending components or additives. The renewable oil(s) feature high oxygen content, high H/C mole ratios, and high fatty acid or fatty acid ester content prior to heating and contact with the catalyst. The catalyst may be, for example, a gallium-doped version of one or more zeolite- alumina matrix catalysts with pore sizes having 10 oxygen atoms in the pore mouth, such as ZSM-5, ZSM-11, ZSM-23, MCM-70, SSZ-44, SSZ-58, SSZ-35, and ZSM-22. Aromatics -production from the renewable oils is enhanced at higher gallium-cation levels, with the preferred level being about 1.0 Ga/framework-Al. While various renewable oils, or "bio-oils," may be used, algae oil has exhibited very high BTEX yields over the gallium cation catalyst, under conditions at or near 1 atm and approximately 400 degrees C.

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23-01-1986 дата публикации

CATALYST COMPOSITION FOR CONVERSION OF SYNTHESIS GAS TO HYDROCARBONS

Номер: AU0000549390B2
Принадлежит: BP PLC

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21-06-1979 дата публикации

PRODUCING AROMATIC HYDROCARBONS

Номер: AU0003156377A
Принадлежит:

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12-12-1978 дата публикации

AROMATISATION PROCESS

Номер: CA0001044259A1
Принадлежит:

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22-02-2001 дата публикации

QUASI-CRYSTALLINE BOEHMITES CONTAINING ADDITIVES

Номер: CA0002381410A1
Принадлежит:

The present invention pertains to a quasi-crystalline boehmite containing additive in a homogeneously dispersed state. Suitable additives are compounds containing elements selected from the group of alkaline earth metals, alkaline metals, transition metals, actinides, silicon, gallium, boron, titanium and phosphorus. Said QCBs according to the invention may be prepared in several ways. In general, a quasi-crystalline boehmite precursor and an additive are converted to a quasi-crystalline boehmite containing the additive in a homogeneously dispersed state. The application is also directed to shaped particles and catalysts comprising the quasi-crystalline boehmite to transition aluminas obtainable from these quasi-crystalline boehmites and to catalyst compositions comprising such transition alumina.

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29-04-2004 дата публикации

A STABILIZED TRANSITION ALUMINA CATALYST SUPPORT FROM BOEHMITE AND CATALYSTS MADE THEREFROM

Номер: CA0002500553A1
Принадлежит:

This invention relates to methods for making a stabilized transition alumina of enhanced hydrothermal stability, which include the introduction of at least one structural stabilizer; a steaming step before or after the introduction step, wherein steaming is effective in transforming a transition alumina at least partially to boehmite and/or pseudoboehmite; and a calcining step to create a stabilized transition alumina. The combination of the structural stabilizer and the steaming step is believed to impart high hydrothermal stability to the alumina crystal lattice. Particularly preferred structural stabilizers include boron, cobalt, and zirconium. The stabilized transition alumina is useful as a catalyst support for high water partial pressure environments, and is particularly useful for making a catalyst having improved hydrothermal stability. The invention more specifically discloses Fischer- Tropsch catalysts and processes for the production of hydrocarbons from synthesis gas.

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21-11-1978 дата публикации

PROCESS FOR MANUFACTURING A CARRIER OF TITANIUM DIOXIDE

Номер: CA0001042867A1
Автор: URWIN DONALD
Принадлежит:

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05-10-1982 дата публикации

HEAVY METAL-MANGANESE OXIDATION CATALYSTS AND PROCESS OF PRODUCING

Номер: CA0001132965A1
Принадлежит:

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02-07-2020 дата публикации

METHODS FOR PRODUCING C2 TO C5 PARAFFINS USING A HYBRID CATALYST COMPRISING GALLIUM METAL OXIDE

Номер: CA3125128A1
Принадлежит:

A method for preparing C2 to C5 paraffins includes introducing a feed stream including hydrogen gas and a carbon-containing gas selected from carbon monoxide, carbon dioxide, and mixtures thereof into a reaction zone of a reactor. Converting the feed stream into a product stream including C2 to C5 paraffins in the presence of a hybrid catalyst. The hybrid catalyst includes a microporous catalyst component; and a metal oxide catalyst component selected from (A) a bulk material consisting of gallium oxide, (B) gallium oxide present on a titanium dioxide support material, and (C) a mixture of gallium oxide and at least one promoter present on a support material selected from Group 4 of the IUPAC periodic table of elements.

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09-07-2013 дата публикации

TITANIUM OXIDE AND ALUMINA ALKALI METAL COMPOSITIONS

Номер: CA0002580930C

... ²²²The invention relates to Group 1 metal/porous metal oxide compositions ²comprising porous metal oxide selected from porous titanium oxide and porous ²alumina and an alkali metal or an alkali metal alloy. The compositions of the ²inventions are described as Stage 0 and I materials. These materials differ in ²their preparation and chemical reactivity. Each successive stage may be ²prepared directly using the methods described below or from an earlier stage ²material. Stage 0 materials may, for example, be prepared using liquid alloys ²of Na and K which are rapidly absorbed by porous metal oxide under isothermal ²conditions, preferably at or just above room temperature, to form loose black ²powders that retain much of the reducing ability of the parent metals. When ²the low melting Group 1 metals are absorbed into the porous metal oxide at ²about 150~C, an exothermic reaction produces Stage I material, loose black ²powders that are stable in dry air. Further heating forms higher stage ²materials ...

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05-04-1988 дата публикации

METHANE CONVERSION

Номер: CA0001234843A1
Принадлежит:

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05-01-2012 дата публикации

A MIXED OXIDE CATALYST AND A PROCESS FOR THE PRODUCTION OF ETHYLENICALLY UNSATURATED CARBOXYLIC ACIDS OR ESTERS

Номер: CA0002801279A1
Принадлежит:

The invention relates to a catalyst for the reaction of formaldehyde or a suitable source thereof with a carboxylic acid or ester to produce an ethylenically unsaturated carboxylic acid or ester. The catalyst comprises a metal oxide having at least two types of metal cations, M1 and M2. M1 is at least one metal selected from group 3 or 4 in the 4th to 6th periods of the periodic table, group 13 in the 3rd to 5th periods of the periodic table, or the remaining elements in the lanthanide series and M2 is at least one metal selected from group 5 in the 5th or 6th periods of the periodic table or group 15 in the 4th or 5th periods of the periodic table. The invention extends to a process to produce an ethylenically unsaturated carboxylic acid or ester.

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02-06-2020 дата публикации

A MIXED OXIDE CATALYST AND A PROCESS FOR THE PRODUCTION OF ETHYLENICALLY UNSATURATED CARBOXYLIC ACIDS OR ESTERS

Номер: CA0002801279C

The invention relates to a catalyst for the reaction of formaldehyde or a suitable source thereof with a carboxylic acid or ester to produce an ethylenically unsaturated carboxylic acid or ester. The catalyst comprises a metal oxide having at least two types of metal cations, M1 and M2. M1 is at least one metal selected from group 3 or 4 in the 4th to 6th periods of the periodic table, group 13 in the 3rd to 5th periods of the periodic table, or the remaining elements in the lanthanide series and M2 is at least one metal selected from group 5 in the 5th or 6th periods of the periodic table or group 15 in the 4th or 5th periods of the periodic table. The invention extends to a process to produce an ethylenically unsaturated carboxylic acid or ester.

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18-02-1993 дата публикации

Selective Epoxidation of Diolefins and Aryl Olefins

Номер: CA0002114138A1
Принадлежит:

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31-10-1979 дата публикации

Номер: CH0000613921A5
Принадлежит: BRITISH TITAN LTD, BRITISH TITAN LTD.

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27-10-2006 дата публикации

КАТАЛИЗАТОР С БИМОДАЛЬНЫМ РАСПРЕДЕЛЕНИЕМ РАДИУСОВ ПОР

Номер: EA0000007454B1

Описывается катализатор с бимодальным распределением радиусов, состоящий в основном из а) от 30 до 99,8 вес.% диоксида циркония, который на 50-100 вес. % имеется в моноклинной модификации, б) от 0,1 до 60 вес.% оксида алюминия, диоксида кремния и/или диоксида титана и в) от 0,1 до 10 вес.% по меньшей мере одного элемента, выбранного из первой или второй главных групп, третьей или восьмой побочной группы Периодической системы элементов и олова, при условии, что сумма весовых процентов составляет 100. Катализатор получают за счет того, что к сырой катализаторной массе добавляют от 2 до 30 вес.% полиаминов, полиакрилатов, полиспиртов, полисилоксанов, углеводов или их смесей, в частности поливинилприрролидон, и ее кальцинируют при температуре выше 550°С. Катализатор можно применять для дегидрирования C2-C16-углеводородов.

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15-07-2009 дата публикации

КАТАЛИТИЧЕСКАЯ КОМПОЗИЦИЯ ДЛЯ ДЕГИДРИРОВАНИЯ АЛКИЛАРОМАТИЧЕСКИХ УГЛЕВОДОРОДОВ (ВАРИАНТЫ), СПОСОБЫ ЕЕ ПРИГОТОВЛЕНИЯ И СПОСОБ КАТАЛИТИЧЕСКОГО ДЕГИДРИРОВАНИЯ АЛКИЛАРОМАТИЧЕСКИХ УГЛЕВОДОРОДОВ

Номер: KZ0000017348B

Заявлены каталитические композиции, включающие носитель из оксида алюминия, модифицированного оксидом кремния, и пропитанные совместно или по отдельности активными металлами (галлий и марганец), при этом отдельно пропитанные части носителя механически смешаны, а также способы их приготовления и дегидрирования ими алкилароматических углеводородов. Предложенный катализатор не только активен в каталитическом окислении метана, но также имеет срок действия, сравнимый со сроком действия других металлических катализаторов, активных в каталитическом дегидрировании.

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28-02-2011 дата публикации

Катализатор для гидрокрекинга высокосернистого нефтяного сырья

Номер: UZ0000004295C

Использование: нефтеперерабатывающая промышленность. Задача: повышение крекирующей активности катализатора и снижение температуры процесса гидрокрекинга на нем. Сущность изобретения: катализатор для гидрокрекинга высокосернистого нефтяного сырья включает оксид никеля, оксид молибдена, оксид галлия, оксид кальция и оксид алюминия, дополнительно содержит оксид бора при следующем соотношении компонентов, мас %: оксид никеля - 7,6; оксид молибдена - 7,4; оксид галлия - 0,2; оксид кальция - 1,0; оксид бора - 15,0-25,0; оксид алюминия - остальное. 1н.п. ф-лы, 3 прим., 1 табл., 1 ил.

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28-04-2006 дата публикации

Катализатор для гидрокрекинга нефтяного сырья

Номер: UZ0000003003C

Использование: в нефтеперерабатывающей промышленности, в частности в разработке катализатора для гидрокрекинга нефтяного сырья. Задача: повышение крекирующей активности катализатора для гидрокрекинга нефтяного сырья. Сущность изобретения: катализатор для гидрокрекинга нефтяного сырья включает оксиды никеля, молибдена, галлия, алюминия. Дополнительно содержит оксид кальция при следующем соотношении компонентов, мас.%: оксид никеля - 7,6; оксид молибдена - 7,4; оксид галлия 0,1-0,3; оксид кальция - 0,5-1,5; оксид алюминия - остальное. 1 н.п.ф-лы., 3 прим., 1 табл.

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28-04-2006 дата публикации

Катализатор для гидрокрекинга нефтяного сырья

Номер: UZ0000003003 C

Использование: в нефтеперерабатывающей промышленности, в частности в разработке катализатора для гидрокрекинга нефтяного сырья. Задача: повышение крекирующей активности катализатора для гидрокрекинга нефтяного сырья. Сущность изобретения: катализатор для гидрокрекинга нефтяного сырья включает оксиды никеля, молибдена, галлия, алюминия. Дополнительно содержит оксид кальция при следующем соотношении компонентов, мас.%: оксид никеля - 7,6; оксид молибдена - 7,4; оксид галлия 0,1-0,3; оксид кальция - 0,5-1,5; оксид алюминия - остальное. 1 н.п.ф-лы., 3 прим., 1 табл.

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05-10-1988 дата публикации

Production of aromatic hydrocarbons

Номер: CN0088101443A
Автор: HENRI DIAZ
Принадлежит:

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03-11-2020 дата публикации

Catalytic dehydrogenation process

Номер: CN0111875468A
Автор:
Принадлежит:

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16-11-2016 дата публикации

Visible light responding photocatalyst LiInSi3O8 and preparation method thereof

Номер: CN0106111111A
Автор: YE CUNJUN, DUAN LIAN, SU HEPING
Принадлежит:

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15-12-2020 дата публикации

Номер: CN0112076770A
Автор:
Принадлежит:

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09-09-2009 дата публикации

Method for degrading perfluorinated compounds

Номер: CN0101524583A
Принадлежит:

The invention discloses a method for degrading perfluorinated compounds, comprising the following steps: under the oxygen-free condition, belta-Ga2O3 is adopted as a photocatalyst. Ultraviolet with the wavelength of 185-254nm is used for irradiating the perfluorinated compounds to be degraded. The method for degrading the perfluorinated compounds has the advantages that: the technique has a simple structure and can be implemented under normal temperature and normal pressure without complex equipment; the initial concentration of the perfluorinated compounds is not required, and the perfluorinated compounds with any concentration and any pH value can be processed by the method of the invention; the toxicity of degraded products is lowered, and the products can be further processed by other methods.

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13-09-2019 дата публикации

Preparation method of carboxylic acid

Номер: CN0106431890B

本发明公开了一种羧酸的制备方法,所述制备方法中对活性氧化铝的金属负载改性,引入一种或多种金属离子调节载体表面活性中心的活性,以使催化剂能够高效、高选择性地用于羧酸的制备,因此可以连续高效地制备羧酸,并且根据本发明的制备方法制备工艺简单,易于控制和操作,有效降低成本,根据本发明的制备方法对羧酸的选择性高,适宜于大规模工业化生产。

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20-01-1978 дата публикации

'HYDROCARBURES MONO-OLEFINIQUES

Номер: FR0002355790A
Принадлежит:

La présente invention concerne un procédé de production d'hydrocarbures non saturés. Le procédé selon l'invention est caractérisé en ce qu'on soumet une mono-oléfine en C3 à C8 à une oligomérisation en présence d'une composition catalytique constituée par un composé de gallium déposé sur un support. Ce procédé est destiné à l'oligomérisation de monooléfines en C3 à C8 , en vue d'obtenir des hydrocarbures non saturés.

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25-06-1982 дата публикации

Aromatisation of olefins - by contact with a gallium catalyst

Номер: FR0002318134B1
Автор:
Принадлежит:

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27-12-1985 дата публикации

PROCEDE POUR LA PREPARATION D'ESTERS DES ACIDES ACRYLIQUE ET METHACRYLIQUE PAR TRANS-ESTERIFICATION

Номер: FR0002566393A
Принадлежит:

L'INVENTION CONCERNE UN PROCEDE POUR LA PREPARATION D'ESTERS DE L'ACIDE ACRYLIQUE OU METHACRYLIQUE ET D'ALCOOLS PAR TRANS-ESTERIFICATION DES ESTERS D'ACIDE ACRYLIQUE OU METHACRYLIQUE ET D'ALCOOLS EN C A C AVEC DES ALCOOLS QUI DIFFERENT DE CEUX-CI A L'EXCLUSION DE POLYALCOOLS, PROCEDE D'APRES LEQUEL ON EFFECTUE LA REACTION DE TRANS-ESTERIFICATION EN PRESENCE D'UN SYSTEME CATALYSEUR KS FORME DE LA COMBINAISON DES COMPOSES A B: A REPRESENTANT LE COMPOSE LI Y, DANS LEQUEL Y EST MIS POUR UN HALOGENURE OU CHLORATE, POUR LE CARBONATE OU LE SEL D'UN ACIDE CARBOXYLIQUE A 1-6 ATOMES DE CARBONE, POUR UN ALCOXYDE A 1-4 ATOMES DE CARBONE, UN HYDROXYDE OU POUR L'OXYGENE ET N ETANT MIS POUR 1 OU 2; ET B REPRESENTANT LE COMPOSE CAX, DANS LEQUEL X EST MIS POUR UN ATOME D'OXYGENE OU UN CHLORURE ET Q EST MIS POUR 1 OU 2, AVEC CETTE CONDITION QUE L'UN AU MOINS DES DEUX CONSTITUANTS ANIONIQUES X ET Y CONTIENNE DE L'OXYGENE.

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11-02-1977 дата публикации

Aromatisation of olefins - by contact with a gallium catalyst

Номер: FR0002318134A1
Принадлежит: BP PLC

The prodn. of aromatic hydrocarbons from >=6C unsatd. hydrocarbons is carried out using a catalyst comprising Ga or a Ga cpd. on a support. The catalyst are capable of dehydrogenating 3-8C alkanes to 3-8C monoolefins, dimerising the latter, and aromatising the resulting 6-18C olefins, all in the same process step (or in separate steps). Aromatisation is pref. effected at 400-750 degrees C and 1-20 atm. Combined dehydrogenation, dimerisation and aromatisation can be effected at 400-700 degrees C and 1-20 atm. Suitable catalyst can be prepd. by impregnating alumina or silica with Ga(NO3) and calcining the product to form Ga2O3, or by subjecting hydrated alumina or silica to ion exchange with Ga ions. The support can be modified by ion exchange with Al,Fe or Ni. The Ga content of the catalyst should be 0.01-10 (esp. 0.1-6) wt %.

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16-12-1997 дата публикации

Номер: KR0100133049B1
Автор:
Принадлежит:

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09-02-1987 дата публикации

OLEFFIN BOND ISOMERISATION PROCESS

Номер: KR19870000055B1
Принадлежит:

Gamma-alumina catalyst used in the isomerisation of olefins is of the formula a Al2O3. b SiO2. c MexOy(I)(in which MexOy is the oxide of 2- or 3-valent metal(S) of gp. mb+B. B is over 0.01. b is 0-0.300(0.020- 0.250). (b+c)/a is 0.01-9.0. m is 0.7-0.1). Pref. isomerisation is carried out at 350-550 deg. C., 0.1-10 (0.5-3) bar and an olefin through put of 2-20 hr. If MexOy is CaO, c is min. 0.500b+0.020; if MexOy is La and a mixt. of lanthanide oxides, c is min. 0.257b+0.014; and if MexOy is Fe2O3, c is min. 0.290b+ 0.018. In all cases, b=0.020-0.250. Copyright 1997 KIPO ...

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19-10-2017 дата публикации

METHOD FOR CONTINUOUSLY PRODUCING ACETIC ACID WITH METHANE AND CARBON DIOXIDE USING FIXED-BED CATALYTIC REACTOR

Номер: KR1020170116466A
Принадлежит:

The present invention relates to a method for continuously producing acetic acid with methane and carbon dioxide using a fixed-bed catalytic reactor. More specifically, the present invention relates to a method for continuously producing acetic acid using a fixed-bed catalytic reactor, comprising the following steps: a first step for injecting metal-supported solid catalyst into the fixed-bed catalytic reactor; a second step for reducing the catalyst; a third step for continuously supplying methane and carbon dioxide at the same time into the fixed-bed catalytic reactor; and a fourth step for producing acetic acid via a single reaction by conducting heat treatment of methane and carbon dioxide in the reactor. COPYRIGHT KIPO 2017 ...

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23-05-2002 дата публикации

CATALYST FOR ESTERIFICATION AND PROCESS FOR PRODUCING CARBOXYLIC ACID ESTERS USING THE SAME

Номер: KR20020037913A
Автор: MATSUOKA KAZUYUKI
Принадлежит:

PURPOSE: A method for economically preparing carboxylic acid ester to a high yield from olefin and carboxylic acid, and an esterification catalyst for the method are provided. CONSTITUTION: The esterification catalyst for forming carboxylic acid ester from olefin and carboxylic acid comprises crystalline gallium silicate, wherein the esterification catalyst is used for reacting olefin with carboxylic acid in the gas phase, a mole ratio of silicon to gallium is 10/1 to 500/1, the crystalline gallium silicate additionally comprises one or more elements selected from Al, Cr and B, wherein one or more elements selected from Al, Cr, B and Si composing the silicate are at least partially replaced with Ga, the crystalline gallium silicate is one or more silicates selected from the group consisting of aluminosilicate, borosilicate and chromosilicate, one or more elements selected from Al, Cr, B and Si composing the silicate are at least partially replaced with Ga, and a mole ratio of silicon to ...

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16-08-2012 дата публикации

Modified zirconia catalyst and manufacturing methods thereof

Номер: TW0201233438A
Принадлежит:

The present invention provides a modified zirconia catalyst including zirconia, sulfate anion, first metal ingredient and second metal ingredient, wherein the first metal ingredient can comprise of aluminum, or gallium, and the second metal ingredient can comprise of platinum or palladinum. The weight percentage of sulfur atoms of the sulfate anion based on the weight of the modified zirconia catalyst is less than 1.0 wt%. Decreasing the sulfate content of the modified zirconia catalyst during impregnation can remarkably enhanced the iso-C7 selectivity and adding alumina into the modified zirconia catalyst can maintain the catalytic activity thereof. The present invention also provides a manufacturing method of the modified zirconia catalyst that described above.

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28-09-2017 дата публикации

CATALYST COMPOSITION FOR INTERNAL COMBUSTION ENGINE

Номер: WO2017164637A3
Принадлежит:

The present invention relates to a catalyst composition for an internal combustion engine, comprising 2-ethylhexyl acetate as an ignition improver, a polyalkylene glycol, a metal nitrate compound, and a polyvinyl alcohol, and thus the present invention improves fuel ignitability so as to enhance fuel efficiency, thereby reducing exhaust gas fumes.

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20-01-2005 дата публикации

CATALYSTS AND METHODS FOR MAKING SAME

Номер: WO2005005033A3
Принадлежит:

Catalysts have a catalytic substrate impregnated with a catalytically active metal, and are prepared by adjusting the pH of a solution of catalytic metal ions to precipitate a layer of catalytic metal on the support.

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13-04-2017 дата публикации

CORE-SHELL AND YOLK-SHELL CATALYSTS AND MAKING THEREOF

Номер: WO2017062226A1
Принадлежит:

A supported catalyst having a core-shell or a yolk-shell structure is disclosed. The supported catalyst includes a catalytic metal-containing nano- or microstructure and an etched perforated metal oxide support shell encompassing the catalytic metal-containing nano- or microstructure, wherein the shell comprises silica (Si02), alumina (A1203), or both, and includes apertures where silica (Si02), alumina (A1203), or both, have been etched away from the shell, and wherein the apertures are configured to allow reactants to transverse from outside the shell to the surface of the catalytic metal-containing nano- or microstructure.

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29-04-2004 дата публикации

A STABILIZED TRANSITION ALUMINA CATALYST SUPPORT FROM BOEHMITE AND CATALYSTS MADE THEREFROM

Номер: WO2004035196A2
Принадлежит:

This invention relates to methods for making a stabilized transition alumina of enhanced hydrothermal stability, which include the introduction of at least one structural stabilizer; a steaming step before or after the introduction step, wherein steaming is effective in transforming a transition alumina at least partially to boehmite and/or pseudoboehmite; and a calcining step to create a stabilized transition alumina. The combination of the structural stabilizer and the steaming step is believed to impart high hydrothermal stability to the alumina crystal lattice. Particularly preferred structural stabilizers include boron, cobalt, and zirconium. The stabilized transition alumina is useful as a catalyst support for high water partial pressure environments, and is particularly useful for making a catalyst having improved hydrothermal stability. The invention more specifically discloses Fischer-Tropsch catalysts and processes for the production of hydrocarbons from synthesis gas.

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04-02-1986 дата публикации

Preparative process for methane conversion agents

Номер: US0004568785A1
Автор: Jaecker; John A.
Принадлежит: Atlantic Richfield Company

An improved support for a contact agent, useful for converting methane to higher hydrocarbon products by contacting a gas comprising methane with a contact agent at a selected temperature, is formed by sintering the surface of the support.

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05-08-2003 дата публикации

Nanotechnology for inks and dopants

Номер: US0006602595B2

Novel inks and dopant materials and their applications are discussed. More specifically, the specifications teach the use of nanotechnology and nanostructured materials for developing novel ink and dopant-based products.

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07-09-1982 дата публикации

Cracking process and catalyst for same

Номер: US4348304A
Автор:
Принадлежит:

A novel cracking catalyst, a method of preparing same, and an improved hydrocarbon cracking process are provided wherein the adverse effects of metals such as nickel, vanadium, iron, copper, and cobalt on the cracking catalys are reduced by contacting the cracking catalyst with a sufficient amount of at least one indium modifier selected from the group consisting of elemental indium and indium compounds free of the element antimony.

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19-02-1980 дата публикации

Intermetallic catalysts

Номер: US4189405A
Автор:
Принадлежит:

A catalyst comprising a substrate having deposited thereon a first coating containing a refractory metal oxide and having deposited upon the said oxide one or more intermetallic compounds of the general formula AxBy where A is selected from the group consisting of Ru, Rh, Pd, Ir and Pt, and B is selected from the group consisting of Al, Sc, Y, the lanthanides, Ti, Zr, Hf, V, Nb, and Ta, and where x and y are integral and may have values of 1 or more.

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22-05-2018 дата публикации

Photocatalyst for water splitting comprising gallium selenide and photoelectrode for water splitting comprising the same

Номер: US0009975115B2

Provided are a photocatalyst having higher activity for hydrogen production through water splitting and a photoelectrode comprising the photocatalyst. The photocatalyst for water splitting of the present invention comprises a Ga selenide, an Ag—Ga selenide, or both thereof.

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25-09-2019 дата публикации

PROCESS FOR PRODUCTION OF AROMATIC COMPOUNDS COMPRISING AT LEAST TWO AMINE FUNCTIONS

Номер: EP3541791A1
Принадлежит:

Подробнее
26-01-1983 дата публикации

Catalyst composition for conversion of synthesis gas to hydrocarbons

Номер: EP0000070690A1
Принадлежит:

The present invention relates to a process for conversion of synthesis gas hydrocarbons in general and to aromatics rich gasoline in particular by contacting the gas with a catalyst composition comprising gallium oxide and/or indium oxide and at least one additional oxide of a metal from Group IB-VIIB or VIII of the Periodic Table. Verium, thorium and uranium are the preferred additional metals. The catalyst composition may optionally contain a further component e.g. zeolite which in some cases can also act as a support. The present process (i) results in a low make of C1 to C2 hydrocarbons, (ii) is capable of using synthesis gas which has a low H2:CO ratio, and (iii) gives a higher conversion of CO than achieved hitherto under similar conditions.

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09-06-1999 дата публикации

Use of compounds having hydrotalcite structure for the preparation of beta-hydroxy and/or alpha-beta unsaturated carbonyl compounds

Номер: EP0000921110A1
Принадлежит:

A new method for the preparation of beta-hydroxy- and/or alpha,beta-unsaturated organic compounds from aldehydes or ketones The use of a compound with a hydrotalcite structure in aldol condensation reactions, particularly for the conversion of acetone to diacetone alcohol. The use of compounds of the general formula (I) as heterogeneous catalysts in the synthesis of ß-hydroxy and/or ¿/ß-unsaturated carbonylated compounds. (M(II)1-xM(III)x(OH)2+x).mH2O (I) M(II) = Ni, Zn, Co, Mg, or a mixture of two or more; M(III) = Al, Ga, Fe or Cr (compound I, in which M(II) = Mg and M(III) = Al, is excluded); x = 0.20 - 0.33; m = at most 1; ...

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18-12-1996 дата публикации

Catalyst composition for the dehydrogenation of C2-C5 paraffins

Номер: EP0000560437B1
Принадлежит: SNAMPROGETTI S.p.A., ENIRICERCHE S.p.A.

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23-02-2006 дата публикации

NITROGEN OXIDE REMOVAL CATALYST AND NITROGEN OXIDE REMOVAL METHOD USING IT

Номер: JP2006051448A
Автор: INOUE MASASHI, KAGAWA KOJI
Принадлежит:

PROBLEM TO BE SOLVED: To provide a nitrogen oxide removal catalyst capable of efficiently decomposing and removing nitrogen oxide by using hydrocarbon as a reducing agent and particularly showing excellent catalytic activity even in the presence of steam. SOLUTION: The catalyst is a catalyst to be used for a reaction of converting nitrogen oxide into nitrogen and water by reaction of the nitrogen oxide with hydrocarbon as a reducing agent and the catalyst is (1) a Ga-Al type crystalline oxide obtained by heating a raw material containing Ga and Al in an organic solvent at a temperature equal to or higher than the boiling point of the organic solvent and (2) the organic solvent has 3 to 6 non-covalent electron pairs. COPYRIGHT: (C)2006,JPO&NCIPI ...

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16-07-2008 дата публикации

Номер: JP0004119980B2
Автор:
Принадлежит:

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28-02-2020 дата публикации

КАТАЛИЗАТОР ГИДРООЧИСТКИ, СОДЕРЖАЩИЙ МЕТАЛЛООРГАНИЧЕСКИЕ СУЛЬФИДЫ НА ЛЕГИРОВАННЫХ НОСИТЕЛЯХ

Номер: RU2715424C2

Изобретение относится к катализатору для гидроочистки углеводородного сырья, способу его получения и к способу гидроочистки углеводородного сырья в присутствии указанного катализатора. Катализатор содержит: носитель катализатора; по меньшей мере один металлический компонент группы VIB; по меньшей мере один металлический компонент группы VIII; по меньшей мере одну меркаптокарбоновую кислоту. Носитель катализатора содержит легирующую примесь, содержащую бор, а также, необязательно, кремний и/или фосфор в интервале от 1 до 13 мас.%, в расчете на оксид и в расчете на общую массу катализатора для каждой добавленной легирующей примеси. Общее количество легирующей примеси, добавленной к материалу носителя, находится в интервале 1-26 мас.%. Содержание бора в катализаторе находится в интервале 2-13 мас.%, в расчете на оксид (BO) и в расчете на общую массу катализатора. Количество по меньшей мере одной меркаптокарбоновой кислоты находится в интервале от 0,4 до 3 эквивалентов по отношению к количеству ...

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27-12-2007 дата публикации

КАТАЛИЗАТОР И СПОСОБ ПОЛУЧЕНИЯ БЕНЗИНА-АЛКИЛАТА

Номер: RU2313391C2

Изобретение относится к химии гетерогенного катализа, в частности к процессам получения высокооктанового компонента бензина при алкилировании изобутана бутан-бутиленовой фракцией на гетерогенных катализаторах. Твердый гетерогенный катализатор представляет собой твердую пористую сверхкислоту на основе металлосиликатов циркония, гафния или их смесей, промотированных солями двух- или трехзарядных катионов металлов с двухзарядными анионами, и имеет общую формулу (ЭО2·а SiO2)·b(McXd), где Э=Zr, Hf или их смеси, а=17-34, b=0,5 при с=1 и d=1, M=Ni2+, Zn2+ и ZrO2+, X=SO42-, ZrF62-; b=0,1666 при с=2 и d=3, M=Sc3+, Y3+ Ga3+, X=SO42-, причем коэффициенты а и b могут отклоняться относительно указанных значений в большую или в меньшую сторону на 20% для коэффициента а и на 5% для коэффициента b. Заявлен также способ получения высокооктанового компонента автомобильного топлива бензина-алкилата путем алкилирования изобутана промышленной бутан-бутеновой фракцией в присутствии указанного катализатора при ...

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27-06-2012 дата публикации

КАТАЛИЗАТОР ОКИСЛЕНИЯ УГАРНОГО ГАЗА

Номер: RU2454276C2

Изобретение относится к катализаторам окисления оксида углерода (II), перспективным для очистки от него отходящих газов. Описано применение фосфида индия, легированного сульфидом кадмия, в качестве катализатора окисления оксида углерода. Технический эффект - повышение активности и селективности катализатора по отношению к реакции окисления оксида углерода. 1 табл.

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10-07-2007 дата публикации

КАТАЛИЗАТОР АРОМАТИЗАЦИИ ЛЕГКИХ УГЛЕВОДОРОДОВ, СПОСОБ ЕГО ПРИГОТОВЛЕНИЯ И СПОСОБ ПОЛУЧЕНИЯ АРОМАТИЧЕСКИХ УГЛЕВОДОРОДОВ

Номер: RU2302291C1

Изобретение относится к способам переработки углеводородного сырья в ароматические углеводороды, а именно к катализаторам ароматизации легких углеводородов, к способам приготовления катализатора и способу получения ароматических углеводородов. Описан комплексный катализатор ароматизации легких углеводородов, содержащий микропористый компонент, обладающий кислыми свойствами и размерами пор не менее 5 Å, и оксидный компонент, обладающий дегидрирующими свойствами, причем в качестве оксидного компонента катализатор содержит гидроксид и/или оксид алюминия с размером транспортных пор не менее 20 нм, обработанный соединениями промотирующих элементов. Описан способ приготовления этого катализатора и способ получения ароматических углеводородов в присутствии описанного выше катализатора. Технический результат - повышение активности и селективности в отношении образования ароматических углеводородов и улучшение стабильности действия приготовленного комплексного катализатора 3 н. и 8 з.п. ф-лы, 1 ...

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20-04-1998 дата публикации

СПОСОБ АКТИВАЦИИ КАТАЛИТИЧЕСКОЙ КОМПОЗИЦИИ НА ОСНОВЕ СОЕДИНЕНИЯ ГАЛЛИЯ И ОКСИДА АЛЮМИНИЯ И КАТАЛИТИЧЕСКАЯ КОМПОЗИЦИЯ ДЛЯ ДЕГИДРИРОВАНИЯ С2 - С5-ПАРАФИНОВ

Номер: RU2108861C1

Способ активации каталитической композиции дегидрирования парафинов, содержащей галлий, окись алюминия, двуокись кремния (необязательно) и/или один или более из щелочных или щелочноземельных металлов, включает термическую активацию на воздухе с последующей пост-активацией, осуществляемой на следующих стадиях: окисления воздухом и/или кислородом, или смесью, содержащей кислород и инертный газ; продувки инертным газом; восстановления водородом или смесью водорода и инертного или восстанавливающего газа. Каталитическая композиция, активированная в соответствии с указанным способом, содержит галлий, окись алюминия, двуокись кремния и необязательно один или более из щелочных или щелочноземельных металлов, причем окись алюминия существует в виде δ- или θ- фазы, или в виде смеси δ+θ или δ+θ+α. 2 с. и 4 з.п. ф-лы, 4 ил., 5 табл.

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27-01-2009 дата публикации

КАТАЛИТИЧЕСКАЯ СИСТЕМА И СПОСОБ ВОССТАНОВЛЕНИЯ NOx

Номер: RU2007128066A
Принадлежит:

... 1. Каталитическая система для восстановления NOx, содержащая: катализатор, содержащий металлоксидную подложку катализатора, каталитический оксид металла, содержащий, по крайней мере, один из оксида галлия или серебра, и инициирующий металл, выбранный из группы, состоящей из серебра, кобальта, молибдена, вольфрама, индия, висмута и их смеси; газовый поток, содержащий органический восстановитель; и соединение, содержащее серу. 2. Каталитическая система по п.1, где указанная металлоксидная подложка катализатора содержит, по крайней мере, один член, выбранный из группы, включающей оксид алюминия, диоксид титана, диоксид циркония, диоксид церия, карбида кремния, или их смесей. 3. Каталитическая система по п.1, где указанный каталитический оксид металла содержит в диапазоне примерно от 5 до 31 мольного % оксида галлия. 4. Каталитическая система по п.1, где указанный каталитический оксид металла содержит в диапазоне примерно от 0,5 до 31 мольного % оксида серебра. 5. Каталитическая система по ...

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27-11-2013 дата публикации

КАТАЛИЗАТОР ОБЕЗВРЕЖИВАНИЯ ДИОКСИДА АЗОТА

Номер: RU2012121356A
Принадлежит:

Предложен теллурид кадмия, легированный антимонидом индия, в качестве катализатора восстановления оксида азота (IV).

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27-01-2014 дата публикации

СПОСОБ ФОРМИРОВАНИЯ КАТАЛИЗАТОРА С ИНГИБИРОВАННОЙ ПОДВИЖНОСТЬЮ НАНОАКТИВНОГО МАТЕРИАЛА

Номер: RU2012129984A
Принадлежит:

... 1. Способ формирования катализатора, включающий:создание большого числа частиц подложки и большого числа частиц, ингибирующих мобильность, причем каждая частица из большого числа частиц подложки, связана со своей каталитической частицей, исвязывание большого числа частиц, ингибирующих мобильность, с большим числом частиц подложки,в котором каждая частица подложки отделена от всех других частиц подложки из большого числа частиц подложки, по меньшей мере, одной из частиц, ингибирующих мобильность,в котором частицы, ингибирующие мобильность, предназначены для предотвращения перемещения каталитических частиц от одной частицы подложки к другой частице подложки.2. Способ по п.1, в котором создание большого числа частиц подложки включает:получение наноразмерного предшественника порошка подложки со средним размером зерна 1 мкм или более;получение нано-размерного предшественника каталитического порошка со средним размером зерна 1 мкм или более,связывание наноразмерного каталитического порошка с ...

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14-01-2025 дата публикации

Трехкомпонентный фотокатализатор для разложения органических загрязнителей под действием видимого света и способ его получения

Номер: RU2833051C1

Изобретение относится к химической технологии получения катализаторов, а именно трехкомпонентного фотокатализатора на основе нитрида углерода, сульфида цинка индия и углеродных точек. Трехкомпонентный фотокатализатор для разложения органических загрязнителей под действием видимого света представляет собой водную суспензию порошка, состоящего из связанных между собой фаз графитоподобного нитрида углерода g-C3N4 и сульфида цинка индия ZnIn2S4 с включениями углеродных точек, при концентрации сульфида цинка индия в фотокатализаторе 60-92% масс. и массовом соотношении графитоподобного нитрида углерода g-C3N4 и углеродных точек (5-50):1 соответственно. Способ получения предлагаемого катализатора включает следующие этапы: сначала получают водную дисперсию графитоподобного нитрида углерода g-C3N4 и углеродных точек, взятых в массовом соотношении от 5:1 до 50:1, путем ультразвукового перемешивания, затем в полученную дисперсию добавляют источники цинка, индия и серы в количестве, обеспечивающем ...

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17-11-1988 дата публикации

METHANE CONVERSION

Номер: DE0003474545D1

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28-04-1988 дата публикации

A PROCESS FOR PRODUCING FORMALDEHYDE

Номер: DE0003470031D1

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19-03-1992 дата публикации

Номер: DE0002831465C2
Принадлежит: STAMICARBON B.V., GELEEN, NL

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08-02-2001 дата публикации

Katalysator mit bimodaler Porenradienverteilung

Номер: DE0019937107A1
Принадлежит:

Katalysatoren mit bimodaler Porenradienverteilung, die DOLLAR A a) 10 bis 99,9 Gew.-% Zirkondioxid und DOLLAR A b) 0 bis 60 Gew.-% Aluminiumoxid, Siliciumdioxid und/oder Titandioxid und DOLLAR A c) 0,1 bis 10 Gew.-% mindestens eines Elementes der ersten oder zweiten Hauptgruppe, eines Elementes der dritten Nebengruppe, eines Elementes der achten Nebengruppe des Periodensystems der Elemente, Lanthan oder Zinn DOLLAR A enthalten, mit der Maßgabe, daß die Summe der Gewichtsprozente 100 ergibt.

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24-04-1985 дата публикации

METHANE CONVERSION

Номер: GB0008506988D0
Автор:
Принадлежит:

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02-01-2020 дата публикации

EXHAUST GAS PURIFICATION SYSTEM

Номер: US20200001236A1
Принадлежит: Hitachi Automotive Systems, Ltd.

An object of the present invention is to provide an exhaust gas purification system which exhibits high exhaust gas purification performance. The present invention provides an exhaust gas purification system including: a carrier containing aluminum oxide; an exhaust gas purification device including a catalyst provided on the carrier and containing gallium, and connected to an internal combustion engine; and a system connected to the exhaust gas purification device for increasing an oxygen concentration. The system for increasing an oxygen concentration provides an oxygen concentration higher than that of a post combusted gas of the internal combustion engine. 1. An exhaust gas purification system comprising: a carrier containing aluminum oxide; an exhaust gas purification device including a catalyst provided on the carrier and containing gallium , and connected to an internal combustion engine; and a system for increasing an oxygen concentration , the system being connected to the exhaust gas purification device ,wherein the system for increasing an oxygen concentration provides an oxygen concentration higher than that of a post combusted gas of the internal combustion engine.2. The exhaust gas purification system according to claim 1 , wherein the catalyst further contains rhodium.3. The exhaust gas purification system according to claim 1 , wherein the system for increasing an oxygen concentration sets an oxygen concentration of a gas flowing into the catalyst to 0.5% or more.4. The exhaust gas purification system according to claim 1 , wherein the system for increasing an oxygen concentration supplies a gas containing oxygen to the catalyst separately from an exhaust gas discharged from the internal combustion engine.5. The exhaust gas purification system according to claim 4 , wherein the system for increasing an oxygen concentration includes a supercharger.6. The exhaust gas purification system according to claim 1 , wherein the internal combustion engine ...

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12-01-2017 дата публикации

Improved glycol acylation process with water-tolerant metal triflates

Номер: US20170008902A1
Принадлежит: Archer Daniels Midland Co

A method for acid-catalyzed acylation of an isohexide is described. The method can enable direct alcohol acylation with carboxylic acids. In particular, the method involves reacting an isohexide and an excess of carboxylic acid, in the presence of a water-tolerant Lewis acid catalyst. Water-tolerant Lewis acid catalysts can furnish relatively high diester yields (e.g., ≧55%-60%) at lower catalyst loads. This feature, among others, is highly desirable for cost savings, and can improve process economics.

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03-03-2022 дата публикации

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

Номер: US20220064082A1
Принадлежит:

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

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03-03-2022 дата публикации

ORGANIC SOLID BIOMASS CONVERSION FOR LIQUID FUELS/CHEMICALS PRODUCTION IN THE PRESENCE OF METHANE CONTAINING GAS ENVIRONMENT AND CATALYST STRUCTURE

Номер: US20220064538A1
Автор: Song Hua
Принадлежит:

A method provides for valorization of naturally abundant organic solid biomass under a specified gas atmosphere with the existence of a catalyst structure. The method effectively converts the organic solid feedstock while producing valuable liquid hydrocarbon products, as well as utilizing methane rich resources, providing an economical and environmental benefit in the oil & gas industry.

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13-02-2020 дата публикации

PROCESS FOR METHANOL SYNTHESIS USING AN INDIUM OXIDE BASED CATALYST

Номер: US20200048173A1
Принадлежит:

The invention relates to a process for methanol synthesis comprising the steps of providing a syngas feed stream comprising hydrogen and a mixture of carbon dioxide and carbon monoxide, wherein carbon dioxide represents from 1 to 50 mol % of the total molar content of the feed stream, carbon monoxide is contained from 0.1 to 85 mol % of the total molar content, and His comprised from 5 to 95 mol % of the total molar content of the feed stream; providing an indium oxide catalyst selected from a bulk catalyst and a supported catalyst comprising indium oxide (InO) as the main active phase; putting in contact said stream with said catalyst at a reaction temperature of at least 373 K (99.85° C.) and under a pressure ranging of at least 1 MPa; and recovering the methanol effluents. The invention also relates to an indium oxide based catalyst. 1. A process for methanol synthesis comprising:{'sub': '2', 'providing a syngas feed stream comprising hydrogen and a mixture of carbon dioxide and carbon monoxide, wherein carbon dioxide represents from 1 to 50 mol % of the total molar content of the feed stream, carbon monoxide is contained from 0.1 to 85 mol % of the total molar content of the feed stream, and His comprised from 5 to 95 mol % of the total molar content of the feed stream;'}{'sub': 2', '3, 'providing an indium oxide catalyst selected from the group consisting of a bulk catalyst consisting in indium oxide and a catalyst comprising indium oxide (InO) deposited on a support;'}putting in contact said stream with said catalyst at a reaction temperature of at least 373 K (99.85° C.) and under a pressure of at least 1 MPa; andrecovering the methanol effluents.2. The process according to wherein the reaction temperature is at least 463 K (189.85° C.).3. The process according to claim 1 , wherein the pressure is at least 2 MPa.4. The process according to claim 1 , wherein the molar ratio of carbon monoxide to carbon dioxide in the syngas feed stream is at least 1:10.5. The ...

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17-03-2022 дата публикации

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

Номер: US20220080392A1
Принадлежит: Dow Global Technologies LLC

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

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08-03-2018 дата публикации

NANOSTRUCTURED METAL OXIDE COMPOSITIONS FOR APPLIED PHOTOCATALYSIS

Номер: US20180065856A1
Принадлежит:

A nanostructured metal oxide composition comprising hydroxides or oxygen vacancies or both hydroxides and oxygen vacancies on its surface is described. A process for preparing the nanostructured metal oxide composition comprising hydroxides or oxygen vacancies or both hydroxides and oxygen vacancies on its surface, which hydroxides and oxygen vacancies can participate in chemical reactions, which composition is prepared by a method selected from the group of methods comprising: i) controlled thermally induced dehydroxylation of nanostructured metal hydroxide precursors; ii) thermochemical reaction of said nanostructured metal oxide with hydrogen gas; iii) vacuum thermal treatment of said nanostructured metal oxide; and iv) aliovalent doping with a lower oxidation state metal. A photocatalyst comprising a nanostructured metal oxide composition comprising an optimal loading of hydroxides or oxygen vacancies or both hydroxides and oxygen vacancies on its surface, which hydroxides and/or oxygen vacancies can participate in chemical or physical reactions. 1. A nanostructured metal oxide composition comprising both hydroxide groups and oxygen vacancies on its surface.2. The composition according to claim 1 , wherein said nanostructured metal oxide composition has an average particle size of from about 1000 nm to about 1 nm.3. The nanostructured metal oxide composition as claimed in claim 1 , wherein the metal is selected from the group of metals consisting of a main group claim 1 , a transition group and a rare earth group metal.4. The composition according to claim 1 , wherein said nanostructured metal oxide composition adsorbs carbon dioxide physically or chemically or both physically and chemically.5. The composition according to claim 4 , wherein said nanostructured metal oxide composition has an electronic configuration that provides long-lived photo-generated electron and hole-pairs claim 4 , increasing the opportunity for charge transfer between the composition and ...

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17-03-2016 дата публикации

NANOSTRUCTURED SOLAR SELECTIVE CATALYTIC SUPPORTS

Номер: US20160074833A1
Принадлежит:

A combined catalyst and catalyst support comprising: a nanostructured solar selective support to which at least one catalyst is affixed; the catalyst comprising at least one material that activates chemical reactions that produce fuels; the nanostructured solar selective support comprising material that is highly absorbing over a portion of the solar spectrum and exhibits low emissivity toward thermal radiation and/or has a surface textured to lower emissivity; the combined catalyst and catalyst support exhibiting at least one of a photochemical effect and a photothermal effect; wherein these effects cause the chemical reaction rates to increase with exposure to an increasing number of incident photons within the solar spectrum. 1. A combined catalyst and catalyst support comprising:a nanostructured solar selective support to which at least one catalyst is affixed;the catalyst comprising at least one material that activates chemical reactions that produce fuels;the nanostructured solar selective support comprising material that is highly absorbing over a portion of the solar spectrum and exhibits low emissivity toward thermal radiation and/or has a surface textured to lower emissivity; andthe combined catalyst and catalyst support exhibiting at least one of a photochemical effect and a photothermal effect;wherein these effects cause the chemical reaction rates to increase with exposure to an increasing number of incident photons within the solar spectrum.2. The combined catalyst and catalyst support according to claim 1 , wherein the chemical reaction is selected from the group consisting of Sabatier reaction claim 1 , methanol synthesis claim 1 , reverse water gas shift claim 1 , methane synthesis claim 1 , carbon dioxide splitting claim 1 , water gas shift claim 1 , Fischer-Tropsch synthesis claim 1 , water splitting claim 1 , reverse Boudard reaction claim 1 , dry reforming of methane claim 1 , bi-reforming of methane and the Carnol process.3. The combined ...

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23-04-2015 дата публикации

REFRACTORY MIXED-METAL OXIDES AND SPINEL COMPOSITIONS FOR THERMO-CATALYTIC CONVERSION OF BIOMASS

Номер: US20150111723A1
Принадлежит:

A process for biomass catalytic cracking is disclosed herein. More specifically, the process is in presence of is a mixed metal oxide catalyst represented by the formula (XO).(XO).(XYO) wherein X, Xand Xare alkaline earth elements selected from the group of Mg, Ca, Be, Ba, and mixture thereof, and Y is a metal selected from the group of Al, Mn, Fe, Co, Ni, Cr, Ga, B, La, P and mixture thereof, wherein the catalyst is formed by calcining at least one compound comprising at least one alkaline earth element and a metal element. 1. A method of forming a catalyst system , the method comprising:(a) combining one or more compounds comprising an element selected from the group including alkaline earth element X and a metal element Y, wherein X is selected from the group consisting of Mg, Ca, Be, Ba, and combinations thereof, and Y is selected from the group consisting of Al, Mn, Fe, Co, Ni, Cr, Ga, B, La, P, Ti, Zn and combinations thereof,(b) mixing the one or more compounds to form a mixture; and(c) calcining the mixture thereby forming a catalyst system,{'sub': 1', '2', 'a', '3', 'b', '4', '1', '2', '3, 'wherein the catalyst system comprises a composition represented by the formula (XO).(XO).(XYO), wherein X, Xand Xare alkaline earth elements selected from the group consisting of Mg, Ca, Be, Ba, and mixture thereof, and wherein a is 0 or 1 and b is 0, 1 or 2.'}2. A method of forming a catalyst system , the method comprising:(a) combining one or more compounds comprising an element selected from the group including alkaline earth element X and a metal element Y, wherein X is selected from the group consisting of Mg, Ca, Be, Ba, and combinations thereof, and Y is selected from the group consisting of Al, Mn, Fe, Co, Ni, Cr, Ga, B, La, P, Ti, Zn and combinations thereof, and{'sub': 1', '2', 'a', '3', 'b', '4', '1', '2', '3, '(b) precipitating the one or more compounds, thereby forming a catalyst system, wherein the catalyst system comprises a composition represented by the ...

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02-05-2019 дата публикации

DEHYDROGENATION CATALYSTS

Номер: US20190126242A1
Принадлежит:

This disclosure relates to catalyst compositions including gallium and a zirconium-based mixed oxide support, to methods for making such catalysts, and to methods for dehydrogenating hydrocarbons with such catalysts. For example, in one embodiment, a catalyst composition includes a mixed oxide support comprising at least about 50 wt. % of zirconium oxide, the mixed oxide support being present in the composition in an amount within the range of about 40 wt. % to about 99.9 wt. %; and disposed on the support, gallium, present in the composition in an amount within the range of about 0.1 wt. % to about 30 wt. %, calculated as GaOon a calcined basis. 1. A calcined dehydrogenation catalyst composition comprising a mixed oxide support comprising at least about 50 wt. % of zirconium oxide , the mixed oxide support being present in the composition in an amount within the range of about 40 wt. % to about 99.9 wt. %; and disposed on the support , gallium , present in the composition in an amount within the range of about 0.1 wt. % to about 30 wt% , calculated as GaOon a calcined basis.2. The catalyst composition of claim 1 , wherein gallium is present in an amount within the range of about 3 wt. % to about 15 wt. % claim 1 , calculated as GaOon a calcined basis.3. The catalyst composition of claim 1 , further comprising claim 1 , disposed on the support claim 1 , one or more primary promoters selected from platinum claim 1 , iridium claim 1 , lanthanum claim 1 , zinc claim 1 , iron claim 1 , rhodium claim 1 , palladium claim 1 , and ruthenium claim 1 , present in the composition in an amount within the range of about 0.01 wt. % to about 5 wt. % claim 1 , calculated as oxide on a calcined basis.4. The catalyst composition of claim 1 , wherein a platinum promoter is disposed on the support in an amount within the range of about 0.01 wt. % to about 1 wt. % claim 1 , calculated as PtOon a calcined basis.5. The catalyst composition of claim 1 , further comprising claim 1 , ...

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03-06-2021 дата публикации

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

Номер: US20210162373A1
Принадлежит: PURDUE RESEARCH FOUNDATION

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

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10-06-2021 дата публикации

METHOD FOR CO-PRODUCING 2,3,3,3-TETRAFLUOROPROPENE AND TRANS-1,3,3,3-TETRAFLUOROPROPENE

Номер: US20210171424A1
Принадлежит: Zhejiang Quhua Fluor-Chemistry Co Ltd

Disclosed is a method for co-producing 2,3,3,3-tetrafluoropropene and trans-1,3,3,3-tetrafluoropropene, comprising the following steps: preheating a mixture of 1,1,1,2,2-pentachloropropane and 1,1,1,3,3-pentachloropropane together with anhydrous hydrogen fluoride and simultaneously introducing into a first reactor to react in the presence of a catalyst LaO—CrOto obtain a first reactor product; directly introducing the first reactor product into a second reactor without separation, and carrying out a catalytic fluorination reaction in the presence of a catalyst GaO—YO—CrOto obtain a second reactor product; and separating the second reactor product to obtain the products of 2,3,3,3-tetrafluoropropene and trans-1,3,3,3-tetrafluoropropene. The invention has such advantages that the process is simple and less equipment investment is required; used catalysts have good activity, high selectivity and long total life; and the ratio of the two products can be flexibly adjusted according to market demands. 1. A method for co-producing 2 ,3 ,3 ,3-tetrafluoropropene and trans-1 ,3 ,3 ,3-tetrafluoropropene , comprising following steps of:{'sub': 2', '3', '2', '3, '(1) preheating a mixture of 1,1,1,2,2-pentachloropropane and 1,1,1,3,3-pentachloropropane together with anhydrous hydrogen fluoride and simultaneously introducing into a first reactor to react in the presence of a catalyst LaO—CrOat a reaction temperature of 200-350° C., with a contact time of 1-20 s to obtain a first reactor product, wherein a molar ratio of the anhydrous hydrogen fluoride to the mixture of 1,1,1,2,2-pentachloropropane and 1,1,1,3,3-pentachloropropane is 6-18:1;'}{'sub': 2', '3', '2', '3', '2', '3, '(2) directly introducing the first reactor product obtained in the step (1) into a second reactor without separation, and carrying out a catalytic fluorination reaction in the presence of a catalyst GaO—YO—CrOat a reaction temperature of 250-400° C., with a contact time of 1-35 s to obtain a second reactor ...

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24-06-2021 дата публикации

Catalyst compositions for aromatizing hydrocarbons and processes for producing aromatic compounds using the catalyst compositions

Номер: US20210187487A1

Processes for aromatizing hydrocarbons include contacting the hydrocarbons with a catalyst composition comprising a metal oxide dispersed on a surface of a zeolite support, where contacting the hydrocarbons with the catalyst composition causes at least a portion of the hydrocarbons to undergo a chemical reaction to form aromatic hydrocarbons. The catalyst composition is prepared by a synthesis process that includes combining the zeolite support with a hydrocarbon solvent to form a zeolite mixture, where the hydrocarbon solvent pre-wets the pores of the zeolite support. The synthesis process further includes combining a polar solvent comprising a metal salt with the zeolite mixture to form an impregnated zeolite support. The synthesis process also includes drying the impregnated zeolite support and calcining the impregnated zeolite support to convert the metal salt to the metal oxide, thereby forming the catalyst composition.

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24-06-2021 дата публикации

METHOD FOR DEGRADATING THERMOSETTING RESIN, CATALYST COMPOSITION USED THEREIN AND RESIN COMPOSITION OBTAINED THEREBY

Номер: US20210189057A1

A degradation method of thermosetting resin is provided. The method includes the following steps, for example, a first resin composition is provided. The resin in the first resin composition includes a carbon-nitrogen bond, an ether bond, an ester bond or a combination thereof. The first resin composition and a catalyst composition are mixed to perform a degradation reaction to form a second resin composition. The catalyst composition includes a transition metal compound and a group IIIA metal compound. The second resin composition includes a resin monomer or an oligomer thereof having functional groups. The functional group includes an amine group, a hydroxyl group, an ester group, an acid group or a combination thereof. A catalyst composition used in the degradation method and a resin composition obtained by the degradation method are also provided. 1. A method for degradating thermosetting resin , comprising:providing a first resin composition having a resin, wherein the resin in the first resin composition comprises a carbon-nitrogen bond, an ether bond, an ester bond or a combination thereof; andmixing the first resin composition and a catalyst composition to proceed to a degradation reaction to form a second resin composition, wherein the catalyst composition comprises a transition metal compound having a metal and a group IIIA metal compound having a metal, the second resin composition comprises a resin monomer having functional groups or an oligomer thereof, and the functional group comprises an amine group, a hydroxyl group, an ester group, an acid group or a combination thereof.2. The method for degradating thermosetting resin as claimed in claim 1 , wherein the first resin composition comprises a thermosetting resin.3. The method for degradating thermosetting resin as claimed in claim 1 , wherein the metal of the transition metal compound comprises cobalt claim 1 , nickel claim 1 , vanadium claim 1 , zinc claim 1 , scandium claim 1 , titanium claim 1 , ...

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18-06-2020 дата публикации

METHOD AND APPARATUS FOR PORTABLE ON-DEMAND HYDROGEN GENERATION

Номер: US20200189911A1
Принадлежит:

The present invention discloses hydrogen generation systems and methods of using the same. More particularly, hydrogen is generated on demand by injecting liquid feedstock onto a solid aluminum alloy containing a catalyst. The hydrogen may then be stored or used as fuel for various types of energy conversion, such as internal combustion engines or fuel cells. The hydrogen generation reaction oxidizes the alloy to alumina, which can recycled back into the original alloy using conventional smelting methods. 1. An apparatus for generating hydrogen on demand , comprising:a vessel for liquid feedstock, the vessel including an inlet for compressed air, and an outlet for liquid feedstock; andat least one reactor, the at least one reactor including an inlet in communication with the outlet for liquid feedstock and an outlet for hydrogen gas, the at least one reactor containing a solid alloy of aluminum and catalyst.2. The apparatus of claim 1 , wherein the liquid feedstock is water.3. The apparatus of claim 1 , wherein the catalyst includes gallium.4. The apparatus of claim 3 , wherein the catalyst includes galinstan.5. The apparatus of claim 1 , wherein the solid alloy is composed of about 90% aluminum and about 10% catalyst.6. The apparatus of claim 1 , wherein the solid alloy is composed of at least 90% aluminum and more than 0% claim 1 , but not more than 10% claim 1 , catalyst.7. The apparatus of claim 1 , further including a vented enclosure claim 1 , wherein the vessel and the at least one reactor are contained within the vented enclosure.8. The apparatus of wherein the enclosure includes a lid panel securable in a closed position by one or more compression lever locks.9. The apparatus of wherein the lid carries one or more compressible bumpers.10. The apparatus of wherein the at least one reactor is carried within the enclosure abutting a reactor saddle.11. The apparatus of claim 1 , wherein the vessel for liquid feedstock includes a pickup tube extending within the ...

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28-07-2016 дата публикации

WATER SPLITTING ACTIVITY OF LAYERED OXIDES

Номер: US20160214084A1
Принадлежит:

An efficient and economical process for Hevolution by water splitting, catalyzed by layered oxides that function in UV and visible light. 1. A photocatalytic water splitting process for Hgeneration catalyzed by InA(ZnO)m in the visible and UV light range , wherein A is selected from an oxide of Fe or Ga and m=1-5 , comprising:a) dispersing InA(ZnO)m powder in a reactant solution comprising water and methanol in ratio of 4:1 in a gas closed irradiation system;b) irradiating the reactant mixture as obtained in step (a) to obtain hydrogen.2. The photocatalytic water splitting process according to claim 1 , wherein the catalyst are selected from the group consisting of InFeO3(ZnO)m and InGaO3(ZnO)m claim 1 , wherein m=1-5.3. The photocatalytic water splitting process according to claim 1 , wherein the irradiation process is carried out in UV or visible light region.4. The photocatalytic water splitting process according to claim 1 , wherein the said process is carried for a period of 1-12 hours.5. The photocatalytic water splitting process according to claim 1 , wherein optionally the process is carried out in the presence of a metal co-catalyst selected from the group consisting of NiO claim 1 , CuO and Pt.6. The photocatalytic water splitting process according to claim 5 , wherein NiO is loaded onto InGaO3(ZnO)m claim 5 , where m=1-5.7. The photocatalytic water splitting process according to claim 5 , wherein CuO is loaded onto InGaO3(ZnO)m claim 5 , where m=1-5.8. The photocatalytic water splitting process according to claim 5 , wherein Pt is loaded onto InFeO3(ZnO)m claim 5 , where m=1-5.9. The photocatalytic water splitting process according to claim 2 , wherein the hydrogen evolution rate is in the range of 7 to 11 milli mol/g/h and 0.8 to 3.58 milli mol/g/h in the presence of catalyst InFeO3(ZnO)m and InGaO3(ZnO)m respectively.10. A photocatalyst composition InA(ZnO)m claim 2 , wherein A is selected from an oxide of Fe or Ga and m=1-5 for use as catalyst in water ...

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25-06-2020 дата публикации

SEMICONDUCTOR NANOCRYSTALS

Номер: US20200203472A1
Принадлежит:

Present subject matter provides a semiconductor nanocrystal comprises a core and a shell. The core is fabricated from a first semiconductor. The shell is fabricated from a second semiconductor. The optical cross section of the semiconductor nanocrystal is in a range of 10cm-10cmin a 2-3 eV region. The core is less than 2 nanometers from an outer surface of the shell in at least one region of the semiconductor nanocrystal. Present subject matter also provides method for preparation of the semiconductor nanocrystals and method for photosynthesis of organic compounds. 1. A semiconductor nanocrystal comprising:a core fabricated from a first semiconductor; and{'sup': −17', '2', '−12', '2, 'a shell fabricated from a second semiconductor, wherein the optical cross section of the semiconductor nanocrystal is in a range of 10cm-10cmin a 2-3 eV region, and wherein the core is less than 2 nanometers from an outer surface of the shell in at least one region of the semiconductor nanocrystal.'}2. The semiconductor nanocrystal as claimed in claim 1 , wherein the shell encloses the core non-uniformly.3. The semiconductor nanocrystal as claimed in claim 1 , wherein a core band offset is staggered compared to a shell band offset.4. The semiconductor nanocrystal as claimed in claim 1 , wherein a longest dimension of the semiconductor nanocrystal is in a range of 3 nanometers to 25 nanometers.5. The semiconductor nanocrystal as claimed in claim 1 , wherein a mean aspect ratio of the semiconductor nanocrystal is in a range of 1:1-1:10.6. The semiconductor nanocrystal as claimed in claim 1 , wherein the first semiconductor is selected from the group consisting of CuAlS claim 1 , CdSe claim 1 , CuGaS claim 1 , CuInS claim 1 , ZnTe claim 1 , ZnSe claim 1 , GaN claim 1 , AlN claim 1 , GaP claim 1 , InP claim 1 , InN claim 1 , AlP claim 1 , AlAs claim 1 , Copper doped ZnS claim 1 , Copper doped ZnSe claim 1 , AgAlS claim 1 , CuAlSe claim 1 , CuAlTe claim 1 , CuGaSe claim 1 , CuGaTe claim 1 , ...

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03-08-2017 дата публикации

ELECTROLYTE MEMBRANE, FUEL CELL INCLUDING SAME, BATTERY MODULE INCLUDING FUEL CELL, AND METHOD FOR MANUFACTURING ELECTROLYTE MEMBRANE

Номер: US20170222229A1
Принадлежит: LG CHEM, LTD.

The present specification relates to an electrolyte membrane, a fuel cell including the same, a battery module including the fuel cell, and a method for manufacturing the electrolyte membrane. 116-. (canceled)17. An electrolyte membrane which comprises a lanthanum-gallium-based composite metal oxide , and has a color region of 0.39≦x≦0.40 and 0.35≦y≦0.36 based on the CIE (Commission Internationale de l′Eclairage) x , y chromaticity distribution table ,wherein the electrolyte membrane manufactured by a method comprising:preparing a mixture comprising a precursor of a lanthanum-gallium-based composite metal oxide;warming the mixture to a temperature less than 950° C.;synthesizing the precursor in the mixture into lanthanum-gallium-based composite metal oxide particles; andforming the electrolyte membrane by using a slurry comprising the lanthanum-gallium-based composite metal oxide particles,the synthesized composite metal oxide particles comprise lanthanum-gallium-based composite metal oxide particles which are represented by the following Chemical Formula 1, and secondary phase particles,a content of the secondary phase particles is 5 wt % or more and 30 wt % or less based on the total weight of the synthesized composite metal oxide particles, {'br': None, 'sub': 1-x', 'x', '1-y', 'y', '3-δ, 'LaQGaZO\u2003\u2003[Chemical Formula 1]'}, 'wherein the lanthanum-gallium-based composite metal oxide of the electrolyte membrane is represented by the following Chemical Formula 1in Chemical Formula 1,Q is strontium, Z is magnesium, and 0 Подробнее

21-10-2021 дата публикации

NOBLE METAL PROMOTED SUPPORTED INDIUM OXIDE CATALYST FOR THE HYDROGENATION OF CO2 TO METHANOL AND PROCESS USING SAID CATALYST

Номер: US20210322957A1
Принадлежит:

Supported catalyst for use in a process for the synthesis of methanol, characterized in that the supported catalyst comprises indium oxide in the form of InOand at least one noble metal being palladium, Pd, wherein both indium oxide and at least one noble metal are deposited on a support remarkable in that the supported catalyst is a calcined supported catalyst comprising from 0.01 to 10.0 wt. % of palladium and zirconium dioxide (ZrO) in an amount of at least 50 wt. % on the total weight of said supported catalyst. 113-. (canceled)14. Supported catalyst for use in a process for the synthesis of methanol , characterized in that the supported catalyst comprises indium oxide in the form of InOand at least one noble metal being palladium , Pd , wherein both indium oxide and at least one noble metal are deposited on a support characterized in that the supported catalyst is a calcined supported catalyst comprising:from 0.01 to 10.0 wt. % of palladium and{'sub': '2', 'zirconium dioxide (ZrO) in an amount of at least 50 wt. %'}on the total weight of said supported catalyst.15. The supported catalyst according to claim 14 , characterized in that the supported catalyst comprises from 0.5 wt. % to 2.0 wt. %. of palladium based on the total weight of said supported catalyst.16. The supported catalyst according to claim 14 , characterized in that the support comprises zirconium dioxide (ZrO) in an amount of at least 80 wt. % claim 14 , based on the total weight of said supported catalyst.17. The supported catalyst according to claim 14 , characterized in that the support comprises zirconium dioxide (ZrO) in an amount of at least 90 wt. % based on the total weight of said supported catalyst.18. The supported catalyst according to claim 14 , characterized in that the supported catalyst is a calcined supported catalyst and in that the indium oxide content in the form of InOranges from 1 to 20% by weight based on the total weight of said supported catalyst.19. The supported ...

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11-11-2021 дата публикации

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

Номер: US20210347710A1
Принадлежит:

A supported catalyst for preparing light olefin using direct conversion of syngas is a composite catalyst and formed by compounding component I and component II in a mechanical mixing mode. The active ingredient of component I is a metal oxide; and the component II is a supported zeolite. A carrier is one or more than one of hierarchical pores AlO, SiO, TiO, ZrO, CeO, MgO and GaO; the zeolite is one or more than one of CHA and AEI structures; and the load of the zeolite is 4%-45% wt. A weight ratio of the active ingredients in the component I to the component II is 0.1-20. The reaction process has an extremely high light olefin selectivity; the sum of the selectivity of the light olefin comprising ethylene, propylene and butylene can reach 50-90%, while the selectivity of a methane side product is less than 7%. 1. A catalyst , comprising component I and component II , which are compounded in a mechanical mixing mode; wherein , an active ingredient of the component I is a metal oxide; the component II is a supported zeolite;{'sub': x', 'a', '(1-a)', 'x', 'a', '(1-a)', 'x', 'a', '(1-a)', 'x', 'a', '(1-a)', 'x', 'x', 'a', '(1-a)', 'x', 'a', '(1-a)', 'x', 'a', '(1-a)', 'x', 'x', 'a', '(1-a)', 'x', 'a', '(1-a)', 'x', 'x', 'x', 'x', 'a', 'b', '(1-a-b)', 'x', 'a', 'b', '(1-a-b)', 'x, 'the metal oxide is at least one of MnO, MnCrO, MnAlO, MnZrO, MnInO, ZnO, ZnCrO, ZnAlO, ZnGaO, CeO, COAlO, FeAlOaO, BiO, InO, InAlMnO, and InGaMnO,'}{'sub': x', 'x', 'x', 'x', 'x', 'x, 'sup': '2', 'a specific surface area of MnO, ZnO, CeO, GaO, BiO, and InOis 1-100 m/g;'}{'sub': a', '(1-a)', 'x', 'a', '(1-a)', 'x', 'a', '(1-a)', 'x', 'a', '(1-a)', 'x', 'a', '(1-a)', 'x', 'a', '(1-a)', 'x', 'a', '(1-a)', 'x', 'a', '(1-a)', 'x', 'a', '(1-a)', 'x', 'a', '(1-a)', 'x', 'a', 'b', '(1-a-b)', 'x', 'a', 'b', '(1-a-b)', 'x, 'sup': '2', 'a specific surface area of MnCrO, MnAlO, MnZrO, MnInO, ZnCrO, ZnAlO, ZnGaO, ZnInO, CoAlO, FeAlO, InAlMnO, and InGaMnOis 5-150 m/g.'}a value range of x is 0.7-3.7, and a ...

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06-10-2016 дата публикации

HETEROGENEOUS ALKANE DEHYDROGENATION CATALYST

Номер: US20160288093A1
Принадлежит:

A heterogeneous catalyst suitable for use in alkane dehydrogenation has an active layer that includes alumina and gallia. The active layer is dispersed on a support such as alumina or silica-modified alumina. 1. A heterogeneous alkane dehydrogenation catalyst consisting of a combination of a) both aluminum oxide and gallium oxide dispersed as an active layer on b) an alumina support or a silica-modified alumina support.2. The catalyst of claim 1 , wherein the aluminum and the gallium in the active layer are present in a molar ratio of gallium to aluminum that is within a range of from greater than 0.5:1 to less than 15:1.3. The catalyst of claim 2 , wherein the molar ratio is within a range of from 1:1 to 10:1.4. The catalyst of claim 1 , wherein the aluminum oxide in the active layer is present in an amount within a range of from 0.05 percent by weight to 14 percent by weight and the gallium oxide in the active layer is present in an amount within a range of from greater than 0 percent by weight to less than fourteen by weight claim 1 , each weight percent being based upon total catalyst weight.5. The catalyst of claim 4 , wherein the amount of aluminum oxide is within a range of from 0.05 percent by weight to 5 percent by weight and the gallium oxide is present in an amount within a range of from greater than 0 percent by weight to less than seven percent by weight claim 4 , each weight percent being based upon total catalyst weight. The present application claims the benefit of U.S. Provisional Application No. 61/916,393, filed on Dec. 16, 2013.This invention relates generally to a heterogeneous alkane dehydrogenation catalyst, particularly a heterogeneous alkane dehydrogenation catalyst wherein at least two metal oxides are dispersed on a catalyst support, more particularly a heterogeneous alkane dehydrogenation catalyst wherein two metal oxides are dispersed on a metal oxide catalyst support and one of the metals in the dispersed metal oxides is the same as the ...

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12-10-2017 дата публикации

PROCESS FOR MAKING A NiO-DOPED ALUMINOGALLATE NANOCOMPOSITE

Номер: US20170291165A1

The present disclosure relates to a process for producing a finely divided metal-doped aluminogallate nanocomposite comprising mixing a carrier solvent with a bulk metal-doped aluminogallate nanocomposite to form a bulk metal-doped aluminogallate slurry and atomizing the bulk metal-doped aluminogallate slurry using a low temperature collision to produce a finely divided metal-doped aluminogallate nanocomposite, the composition of a nickel-doped aluminogallate nanocomposite (GAN), and a method of NO decomposition using the nickel-doped aluminogallate nanocomposite. 1. A process for producing a finely divided NiO-doped aluminogallate nanocomposite having a spinel structure comprising:mixing a carrier solvent with a bulk metal-doped aluminogallate nanocomposite synthesized by a process selected from the group consisting of co-precipitation, sol-gel, and hydrothermal to form a bulk metal-doped aluminogallate slurry, wherein the bulk metal-doped aluminogallate nanocomposite comprises:{'sub': 2', '3, 'GaO;'}{'sub': 2', '3, 'AlO; and'}nickel oxide dopant; andatomizing the bulk metal-doped aluminogallate slurry using a collision to produce the finely divided NiO-doped aluminogallate nanocomposite;wherein the carrier solvent is at least one selected from the group consisting of deionized water, ethanol, butanol, isopropyl alcohol, diacetone alcohol, diglycol, triglycol, acetone, methyl ethyl ketone, ethyl acetate, butyl acetate, toluene, and xylene.2. The process of claim 1 , wherein the bulk divided NiO-doped aluminogallate is synthesized by a hydrothermal process comprising:adding a precipitating agent to an aqueous solution comprising a gallium salt, an aluminum salt, and a nickel dopant salt to form a nickel-doped aluminogallate suspension with a pH of 8-12; andheating the nickel-doped aluminogallate suspension to a hydrothermal reaction temperature in a range of 100° C.-350° C., for a reaction time range of 24-100 hrs to form the bulk metal-doped aluminogallate ...

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12-11-2015 дата публикации

Nanostructured metal oxide compositions for applied photocatalysis

Номер: US20150321174A1

A nanostructured metal oxide composition comprising hydroxides or oxygen vacancies or both hydroxides and oxygen vacancies on its surface is described. A process for preparing the nanostructured metal oxide composition comprising hydroxides or oxygen vacancies or both hydroxides and oxygen vacancies on its surface, which hydroxides and oxygen vacancies can participate in chemical reactions, which composition is prepared by a method selected from the group of methods comprising: i) controlled thermally induced dehydroxylation of nanostructured metal hydroxide precursors; ii) thermochemical reaction of said nanostructured metal oxide with hydrogen gas; iii) vacuum thermal treatment of said nanostructured metal oxide; and iv) aliovalent doping with a lower oxidation state metal. A photocatalyst comprising a nanostructured metal oxide composition comprising an optimal loading of hydroxides or oxygen vacancies or both hydroxides and oxygen vacancies on its surface, which hydroxides and/or oxygen vacancies can participate in chemical or physical reactions.

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01-11-2018 дата публикации

DEHYDROGENATION OF ALKANES

Номер: US20180311630A1
Принадлежит: Haldor Topsoe A/S

A reactor system for dehydrogenation of alkanes in a given temperature range upon bringing a reactant stream including alkanes into contact with a catalytic mixture. The reactor system includes a reactor unit arranged to accommodate the catalytic mixture, where the catalytic mixture includes catalyst particles and a ferromagnetic material. The catalyst particles are arranged to catalyze the dehydrogenation of alkanes. The ferromagnetic material is ferromagnetic at least at temperatures up to an upper limit of the given temperature range. The reactor system moreover includes an induction coil arranged to be powered by a power source supplying alternating current and being positioned so as to generate an alternating magnetic field within the reactor unit upon energization by the power source, whereby the catalytic mixture is heated to a temperature within the temperature range by means of the alternating magnetic field. Also, a catalytic mixture and a method of dehydrogenating alkanes. 1. A reactor system for dehydrogenation of alkanes in a given temperature range T upon bringing a reactant stream comprising alkanes into contact with a catalytic mixture , said reactor system comprising:a reactor unit arranged to accommodate said catalytic mixture, said catalytic mixture comprising catalyst particles in intimate contact with a ferromagnetic material, where said catalyst particles are arranged to catalyze the dehydrogenation of alkanes and said ferromagnetic material is ferromagnetic at least at temperatures up to an upper limit of the given temperature range T,an induction coil arranged to be powered by a power source supplying alternating current and being positioned so as to generate an alternating magnetic field within the reactor unit upon energization by the power source, whereby the catalytic mixture is heated to a temperature within said temperature range T by means of said alternating magnetic field.2. A reactor system according to claim 1 , wherein the given ...

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12-11-2020 дата публикации

Heterojunction composite material consisting of one-dimensional in2o3 hollow nanotube and two-dimensional znfe2o4 nanosheet, and application thereof in water pollutant removal

Номер: US20200354235A1
Автор: Jianmei Lu, Najun Li
Принадлежит: SUZHOU UNIVERSITY

A heterojunction composite material consisting of one-dimensional In2O3 hollow nanotube and two-dimensional ZnFe2O4 nanosheets and its application are disclosed. When using this material for catalytic reactions, the hollow cavity and two-dimensional nanosheets of hollow nanomaterials can not only reduce the migration distance to accelerate the electron-hole separation, but also provide a large surface area and rich active sites to promote pollution adsorption and surface catalysis. At the same time, multiple light scattering or reflection in the hollow cavity of the hollow nanomaterials can increase light absorption and utilization. In addition, the heterojunction photocatalyst constructed by growing two-dimensional semiconductor nanosheets on a tubular substrate can promote the effective separation of photogenerated electrons and photogenerated holes, thereby improving the catalytic efficiency. In terms of catalytic performance, In2O3 @ ZnFe2O4 shows effective degradation of tetracycline, and due to its ferromagnetism, it shows convenient and good separation effect and has good recycling performance.

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03-02-1983 дата публикации

Catalyst composition for conversion of synthesis gas to hydrocarbons

Номер: WO1983000326A1
Принадлежит: Heyward, Malcolm, Philip, Young, Dennis

Process for conversion of synthesis gas to hydrocarbons in general and to aromatics rich gasoline in particular by contacting the gas with a catalyst composition comprising gallium oxide and/or indium oxide and at least one additional oxide of a metal from Group IB-VIIB or VIII of the Periodic Table. Cerium, thorium and uranium are the preferred additional metals. The catalyst composition may optionally contain a further component eg a zeolite which in some cases can also act as a support. The present process (i) results in a low make of C1 to C2 hydrocarbons, (ii) is capable of using synthesis gas which has a low H2:CO ratio, and (iii) givs a higher conversion of CO than achieved hitherto under similar conditions.

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09-10-2003 дата публикации

Synthesis gas conversion and novel catalysts for same

Номер: US20030191200A1
Автор: James Kimble, Jianhua Yao
Принадлежит: Phillips Petroleum Co

A catalyst including a metal material and alumina, and a method of preparing such catalyst composition, are disclosed. A catalyst including a metal material, alumina, and thallium, and a method of preparing such catalyst composition are also disclosed. Each of these thus-obtained catalysts can be used for the conversion of synthesis gas into olefins.

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20-03-1985 дата публикации

A process for converting synthesis gas to hydrocarbons

Номер: EP0070690B1
Принадлежит: BP PLC

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13-09-2022 дата публикации

Catalyst compositions for aromatizing hydrocarbons and processes for producing aromatic compounds using the catalyst compositions

Номер: US11439991B2

Processes for aromatizing hydrocarbons include contacting the hydrocarbons with a catalyst composition comprising a metal oxide dispersed on a surface of a zeolite support, where contacting the hydrocarbons with the catalyst composition causes at least a portion of the hydrocarbons to undergo a chemical reaction to form aromatic hydrocarbons. The catalyst composition is prepared by a synthesis process that includes combining the zeolite support with a hydrocarbon solvent to form a zeolite mixture, where the hydrocarbon solvent pre-wets the pores of the zeolite support. The synthesis process further includes combining a polar solvent comprising a metal salt with the zeolite mixture to form an impregnated zeolite support. The synthesis process also includes drying the impregnated zeolite support and calcining the impregnated zeolite support to convert the metal salt to the metal oxide, thereby forming the catalyst composition.

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08-03-1985 дата публикации

触媒の処理法

Номер: JPS6044041A
Принадлежит: Mobil Oil Corp

(57)【要約】本公報は電子出願前の出願データであるた め要約のデータは記録されません。

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01-06-1983 дата публикации

Process for preparing a catalyst based on gamma-alumina

Номер: PT76765A
Принадлежит: Snam Progetti

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01-09-1999 дата публикации

Cerium oxide containing composition, the preparation thereof and the uses thereof

Номер: KR100219259B1
Принадлежит: 로디아 쉬미, 크리스도프 앙드랄

본 발명은 열 안정성 비표면을 지닌 세륨 산화물 기재 조성물 및 이 조성물의 제조방법에 관한 것이다. The present invention relates to a cerium oxide based composition having a thermally stable specific surface and a process for preparing the composition. 이 제2세륨 산화물 기재 조성물은 마그네슘, 스칸듐, 갈륨 및 붕소로 구성된 군으로부터 선택한 금속 원소 A의 산화물 1종 이상 및 제2세륨 산화물을 함유한다. This second cerium oxide based composition contains at least one oxide of the metal element A selected from the group consisting of magnesium, scandium, gallium and boron and a second cerium oxide.

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15-04-2011 дата публикации

Method for decomposing lean nitrogen oxides with mixed metal oxide catalyst

Номер: KR101029680B1
Принадлежит: 상명대학교 산학협력단

PURPOSE: A decomposing treatment method of lean nitrogen oxides is provided to improve the degradability of N2O and NOx by separate absorbing the nitrogen oxides from oxygen before detaching. CONSTITUTION: A decomposing treatment method of lean nitrogen oxides comprises the following steps: offering a catalyst layer containing a mixed metal oxide catalyst formed by a hydrotalcite or brucite type compound precursor marked with chemical formula 1; passing waste gas with the oxygen concentration greater than 0.01% through the catalyst layer for selectively absorbing the nitrogen oxides from the waste gas; passing a reducing agent through the catalyst layer with the nitrogen oxides; and detaching the nitrogen oxides from the catalyst layer using the reducing agent.

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24-01-1984 дата публикации

Activation of inorganic oxides

Номер: US4427791A
Принадлежит: Mobil Oil Corp

A method for enhancing the activity of inorganic oxide materials is disclosed which involves treating same with a fluoride reagent of ammonium fluoride or boron fluoride, contacting the fluoride reagent contacted material with an ammonium exchange solution and then calcining the final product.

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09-02-1987 дата публикации

Olefin bond isomerisation process

Номер: KR870000055B1

Gamma-alumina catalyst used in the isomerisation of olefins is of the formula a Al2O3. b SiO2. c MexOy(I)(in which MexOy is the oxide of 2- or 3-valent metal(S) of gp. mb+B. B is over 0.01. b is 0-0.300(0.020- 0.250). (b+c)/a is 0.01-9.0. m is 0.7-0.1). Pref. isomerisation is carried out at 350-550 deg. C., 0.1-10 (0.5-3) bar and an olefin through put of 2-20 hr. If MexOy is CaO, c is min. 0.500b+0.020; if MexOy is La and a mixt. of lanthanide oxides, c is min. 0.257b+0.014; and if MexOy is Fe2O3, c is min. 0.290b+ 0.018. In all cases, b=0.020-0.250.

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08-09-2011 дата публикации

Method for preparing gamma butyrolactone from 1,4-butanediol

Номер: KR101063772B1

본 발명은 하기 화학식 1 또는 화학식 2의 촉매를 이용하여 1,4-부탄디올을 감마부티로락톤으로 제조하는 방법에 관한 것이다. The present invention relates to a method for preparing 1,4-butanediol as gamma butyrolactone using a catalyst of formula (1) or (2). [화학식 1] [Formula 1] 상기 화학식 1 에서, M은 Cu와 Ga을 제외한 금속원소 또는 준금속원소로부터 선택되는 1종 이상이며, 원소비로 a : b : c 는 1 : 0.01~15 : 0~10 이고, x는 각 성분의 원자가 및 조성비에 따른 화학양론적 값이다. In Formula 1, M is at least one selected from metal elements or quasi-metal elements except Cu and Ga, a: b: c is from 1: 0.01 to 15: 0 to 10, x is each component The stoichiometric value of depends on the valence and composition ratio. 좀 더 상세하게는 상기 화학식 1 의 촉매 존재 하에서 150~300℃의 반응온도 및 0~10 kg/㎠ G의 반응압력으로 1,4-부탄디올을 기상 탈수소 반응시켜 감마부티로락톤을 제조하는 방법에 관한 것이다.  More specifically, in the method of preparing gamma butyrolactone by gas phase dehydrogenation of 1,4-butanediol at a reaction temperature of 150 to 300 ° C. and a reaction pressure of 0 to 10 kg / cm 2 G in the presence of the catalyst of Formula 1 It is about. 1,4-부탄디올, 감마부티로락톤, 구리, 갈륨, 촉매, 금속 또는 준금속 1,4-butanediol, gamma butyrolactone, copper, gallium, catalysts, metals or metalloids

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17-01-2003 дата публикации

The use of gallium salts in presence of sulfonyl anhydrides or sulfonate anions, as Lewis acid catalysts for sulfonylation reactions, e.g. aromatic mesylation

Номер: FR2827194A1
Принадлежит: Rhodia Chimie SAS

The use as catalysts of gallium(III) salts with a catalytic action of the Lewis acid type, in presence of sulfonyl groups in the form of (a) symmetrical or mixed anhydrides with a sulfonyl radical or (b) sulfonate anions. An Independent claim is also included for a composition for use in sulfonylation, comprising (for successive or simultaneous addition) (A) a source which is capable of providing an electrophilic cation in presence of Lewis acids, preferably an acid anhydride or more particularly an acid halide, especially a sulfonic acid halide, more especially a symmetrical or asymmetrical anhydride with a sulfonyl group as at least one of the substituents on the oxygen, and (B) gallium salt(s) as above.

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24-07-2020 дата публикации

用于银催化剂的α-氧化铝载体及其制备方法与应用

Номер: CN107413389B

本发明涉及一种用于银催化剂的α‑氧化铝载体及其制备方法。其制备方法为:将三水氧化铝、拟薄水铝石、含镓化合物、含硅化合物、含氟化合物和碱土金属化合物混合均匀得到固体粉状物,再加入粘结剂和水得到混合物,将该混合物进行捏合、成型、干燥、焙烧,最终得到α‑氧化铝载体。本发明还涉及由该α‑氧化铝载体制成的银催化剂及其在烯烃环氧化生产环氧化合物中的应用。

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16-03-2004 дата публикации

Metal/metal oxide doped oxide catalysts having high deNOx selectivity for lean NOx exhaust aftertreatment systems

Номер: US6706660B2
Автор: Paul W. Park
Принадлежит: Caterpillar Inc

A lean NOx catalyst and method of preparing the same is disclosed. The lean NOx catalyst includes a ceramic substrate, an oxide support material, preferably γ-alumina, deposited on the substrate and a metal promoter or dopant introduced into the oxide support material. The metal promoters or dopants are selected from the group consisting of indium, gallium, tin, silver, germanium, gold, nickel, cobalt, copper, iron, manganese, molybdenum, chromium, cerium, vanadium, oxides thereof, and combinations thereof. The γ-alumina preferably has a pore volume of from about 0.5 to about 2.0 cc/g; a surface area of between about 80 to 350 m 2 /g; an average pore size diameter of between about 3 to 30 nm; and an impurity level of less than or equal to 0.2 weight percent. In a preferred embodiment the γ-alumina is prepared by a sol-gel method, with the metal doping of the γ-alumina preferably accomplished using an incipient wetness impregnation technique.

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05-04-2006 дата публикации

A stabilized transition alumina catalyst support from boehmite and catalysts made therefrom

Номер: EP1551785A4
Принадлежит: ConocoPhillips Co

This invention relates to methods for making a stabilized transition alumina of enhanced hydrothermal stability, which include the introduction of at least one structural stabilizer; a steaming step before or after the introduction step, wherein steaming is effective in transforming a transition alumina at least partially to boehmite and/or pseudoboehmite; and a calcining step to create a stabilized transition alumina. The combination of the structural stabilizer and the steaming step is believed to impart high hydrothermal stability to the alumina crystal lattice. Particularly preferred structural stabilizers include boron, cobalt, and zirconium. The stabilized transition alumina is useful as a catalyst support for high water partial pressure environments, and is particularly useful for making a catalyst having improved hydrothermal stability. The invention more specifically discloses Fischer-Tropsch catalysts and processes for the production of hydrocarbons from synthesis gas.

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05-03-2019 дата публикации

A kind of metal oxide solid solution catalyst and preparation and application

Номер: CN109420484A

本发明涉及一类用于二氧化碳加氢合成甲醇的金属氧化物固溶体催化剂M a O x ‑M b O y ,其中M a O x 为溶质,M b O y 为溶剂。所述的固溶体是指M b O y 晶体中一定量的M b 离子被M a 离子所置换但不改变整个晶体的结构及对称性。所述的固溶体中M a O x 包括ZnO、CdO、Ga 2 O 3 或In 2 O 3 ;M b O y 包括ZrO 2 或TiO 2 。所述的金属氧化物固溶体催化剂应用于二氧化碳加氢制甲醇反应,在2MPa,300℃,24000h –1 条件下可使甲醇选择性最高达85%。

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19-10-2017 дата публикации

Continuous manufacturing methods of acetic acid from CH4 and CO2 using fixed-bed reactor

Номер: KR20170116466A
Принадлежит: 인하대학교 산학협력단

본 발명은 고정층 촉매 반응기를 이용한 메탄 및 이산화탄소로부터 아세트산의 연속식 제조방법에 관한 것으로, 상세하게는 고정층 촉매 반응기에 금속이 담지된 고체 촉매를 주입하는 단계(단계 1); 상기 촉매를 환원시키는 단계(단계 2); 상기 고정층 촉매 반응기에 메탄 및 이산화탄소를 동시에 연속적으로 공급하는 단계(단계 3);및 상기 메탄 및 이산화탄소를 상기 반응기 내에서 열처리하여 단일반응으로 아세트산을 제조하는 단계(단계 4);를 포함하는 고정층 촉매 반응기를 이용한 아세트산 연속식 제조방법에 관한 것이다.

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09-03-2004 дата публикации

Method of preparing doped oxide catalysts for lean NOx exhaust

Номер: US6703343B2
Автор: Paul W. Park
Принадлежит: Caterpillar Inc

The lean NOx catalyst includes a substrate, an oxide support material, preferably γ-alumina deposited on the substrate and a metal or metal oxide promoter or dopant introduced into the oxide support material. The metal promoters or dopants are selected from the group consisting of indium, gallium, tin, silver, germanium, gold, nickel, cobalt, copper, iron, manganese, molybdenum, chromium cerium, and vanadium, and oxides thereof, and any combinations thereof. The γ-alumina preferably has a pore volume of from about 0.5 to about 2.0 cc/g; a surface area of between 80 and 350 m 2 /g; an average pore size diameter of between about 3 to 30 nm; and an impurity level of less than or equal to about 0.2 weight percent. In a preferred embodiment the γ-alumina is prepared by a sol-gel method, with the metal doping of the γ-alumina preferably accomplished using an incipient wetness impregnation technique.

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13-06-1988 дата публикации

CATALYST AND PROCEDURE FOR PREPARING THIS.

Номер: NO158485B
Принадлежит: Snam Progetti

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15-06-2016 дата публикации

Preparation method of hexagonal-tube-shaped indium oxide with complex as precursor

Номер: CN105668612A
Принадлежит: University of Jinan

本发明涉及六方管状氧化铟及其制备方法,属于无机氧化物半导体材料制备技术领域。本发明以铟(III)-对苯二甲酸配合物为前驱体制备氧化铟并对其形貌尺寸进行控制。具体步骤如下:首先将硝酸铟和对苯二甲酸混合于N,N’-二甲基甲酰胺(DMF)溶液中进行加热搅拌得到铟(III)-对苯二甲酸配合物。进一步将离心分离、洗涤、干燥后得到铟(III)-对苯二甲酸配合物进行热解即可制得所述氧化铟材料。本发明的优点是制备过程简单易行,可以有效的控制所得氧化铟的形貌结构,所得产品对4-氯苯酚具有良好的降解能力,在污水处理等领域具有良好的应用前景。

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19-10-2021 дата публикации

Method for preparing butylene and butadiene through catalytic dehydrogenation of butane

Номер: CN109608301B
Принадлежит: SUZHOU UNIVERSITY

本发明提供一种丁烷催化脱氢制备丁烯和丁二烯的方法,使用包含锆和镓的双活性组分复合催化剂,丁烷进行高效脱氢,产物中丁二烯的选择性达到17%,总丁烯的选择性达到81.5%,而且催化剂在高温下表现出良好的稳定性和再生性。

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10-04-2009 дата публикации

Porous oxidation-promoting materials for saving fuel

Номер: KR100892175B1
Автор: 정영훈
Принадлежит: 이창엽, 정영훈

Porous oxidation-promoting materials are provided to reduce fuel by promoting an oxidation reaction in combustion of the fuel and activating an analysis of the fuel at the same time. A manufacturing method of porous oxidation-promoting materials for fuel reduction includes the following steps of: manufacturing a mixture by mixing milled powders after pulverizing aluminium carbide, tridymite, tantalum, zirconium oxide yttrium oxide lineage ceramics, calcium oxide, lithium, potassium feldspar and palladium to 300~350 mesh; plasticizing the mixture in temperature of 800~1200°C; molding the kneaded mixture after kneading the milled mixture with water; and obtaining a porosity oxidation reaction promoter by plasticizing the molding in 1600~2000°C.

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17-01-2023 дата публикации

Indium oxyhydroxide/modified attapulgite photocatalytic composite material and preparation method and application thereof

Номер: CN113877556B
Принадлежит: CHANGZHOU UNIVERSITY

本发明属于光催化领域,涉及羟基氧化铟/酸改性凹凸棒石(InOOH/H‑ATP)光催化复合材料及其制备方法和应用。制备方法包括:将酸化后的凹凸棒石与硝酸铟超声溶于蒸馏水和N,N‑二甲基甲酰胺混合溶液中;然后转移到微波反应釜中,微波溶剂热反应一定的时间;待冷却至室温后,离心收集反应产物,并水洗和醇洗、真空干燥、研磨;最后,转移至管式炉中煅烧得InOOH/H‑ATP光催化复合材料。本发明制备的InOOH/H‑ATP光催化复合材料负载均匀,分散性好,具有丰富的活性位点,比表面积大,富含氧空位,达到了可见光响应,有效地抑制了光生载流子的复合,增强了光催化剂的性能,对光催化还原二氧化碳制甲醇效果优异。

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18-02-2022 дата публикации

Catalyst for coproduction of oxamide and methyl carbamate and preparation method thereof

Номер: CN112915993B

本发明公开了一种联产草酰胺和氨基甲酸甲酯的催化剂及制备方法。所述催化剂的化学式表示为:Zn a In b Zr (1‑a‑b) O‑M;催化剂的活性组分包括Zn、In、Zr的氧化物或复合氧化物,所述a的取值范围是0.01~0.7;b的取值范围是0.01~0.5;为提升催化剂的整体性能,催化剂中还添加了Mo、Al、Ce等助剂。该催化剂的特点是表面同时含有强酸性中心和强碱性中心。这两种具有相反性质的活性中心在特殊的催化剂结构下可以稳定存在,并且协同加速了氨基和酯基的交换速率,使反应可以在较低的温度下发生,从而平衡了尿素醇解和草酸二甲酯氨解两个反应的热力学区间,可提高草酸酯和氨基甲酸甲酯的收率,降低甲醇、氨气和碳酸酯等副产物的生成量。

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27-11-2016 дата публикации

Catalyst for oxidative aromatisation of lower alkanes

Номер: RU2603774C1

Изобретение относится к катализаторам процесса получения ароматических углеводородов из углеводородного сырья. Катализатор окислительной ароматизации низших алканов содержит в мас.%: оксид цинка (в пересчете на металл) 3,00-7,00, оксид галлия (III) (в пересчете на металл) 0,5-3,00, оксид германия (IV) (в пересчете на металл) 0,01-0,10; γ-оксид алюминия 10,00-30,00, цеолит типа пентасила в водородной форме - остальное, до 100. Технический результат заключается в повышении активности катализатора по отношению к выходу целевых ароматических углеводородов, его селективности, конверсии. 1 пр. РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (51) МПК B01J 29/40 B01J 21/04 B01J 23/06 B01J 23/08 B01J 23/14 C07C 15/02 (13) 2 603 774 C1 (2006.01) (2006.01) (2006.01) (2006.01) (2006.01) (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ОПИСАНИЕ (21)(22) Заявка: ИЗОБРЕТЕНИЯ К ПАТЕНТУ 2015144091/04, 14.10.2015 (24) Дата начала отсчета срока действия патента: 14.10.2015 (73) Патентообладатель(и): Публичное акционерное общество "Газпром" (RU) (45) Опубликовано: 27.11.2016 Бюл. № 33 2 6 0 3 7 7 4 R U (54) КАТАЛИЗАТОР ПРОЦЕССА ОКИСЛИТЕЛЬНОЙ АРОМАТИЗАЦИИ НИЗШИХ АЛКАНОВ (57) Реферат: Изобретение относится к катализаторам γ-оксид алюминия 10,00-30,00, цеолит типа процесса получения ароматических пентасила в водородной форме - остальное, до углеводородов из углеводородного сырья. 100. Технический результат заключается в Катализатор окислительной ароматизации повышении активности катализатора по низших алканов содержит в мас.%: оксид цинка отношению к выходу целевых ароматических (в пересчете на металл) 3,00-7,00, оксид галлия углеводородов, его селективности, конверсии. 1 (III) (в пересчете на металл) 0,5-3,00, оксид пр. германия (IV) (в пересчете на металл) 0,01-0,10; Стр.: 1 C 1 C 1 Адрес для переписки: 117997, Москва, ГСП-7, ул. Наметкина, 16, ПАО "Газпром", начальнику Департамента О.Е. Аксютину 2 6 0 3 7 7 4 (56) Список документов, цитированных в отчете о поиске: RU 2523801 C1, ...

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23-11-1988 дата публикации

Catalyst for isomerizing butene-2 into butene-1

Номер: SU1440330A3

Изобретение касаетс  каталитической химии, в частности катализатора дл  изомеризации бутена-2 в бу- тен-1, используемых в производстве полимеров. Состав катализатора, мас.%: оксид металла 2,5-10; диоксид кремни  1,5-8; до 100; обща  ф-ла a(Al20 3) bCSiO) -с(.,) , где оксид металла - лантана, кальци , бари , стронци  или железа; а, Ь, с - число молей указанных оксидов металла, причем (b+B) при В 0,014-0,03; b 0,025-0,14; m ,666; (b+c)/a 0,01059- 0,4409. Катализатор обеспечивает высокую конверсию (до 100%) и селективность (до 99,9%) по бутену-1. 5 табл.

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28-10-2009 дата публикации

Fuel-saving porous oxidation reaction catalysis material fuel and preparation method thereof

Номер: CN101564700A
Автор: 李昌烨, 郑煐勋
Принадлежит: Individual

本发明涉及一种节约燃料的多孔性氧化反应催化材料及其制备方法。具体地说,是一种当燃料燃烧时,在促进氧化反应的同时,还能够活化燃料分解,使燃料完全燃烧,从而节约燃料的多孔性氧化反应催化材料。依据本发明,当燃料燃烧时,通过促进化学反应即氧化反应,就可以节约燃料,它无需其它的节约燃料专用设备,获得了较好的经济效益。它与通过物理方式促进燃料完全燃烧的方法相比,其节约燃料的效率更高。

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19-08-2022 дата публикации

Spinel catalyst for preparing ethylene by ethane dehydrogenation under carbon dioxide atmosphere and preparation method thereof

Номер: CN111013563B
Принадлежит: FUDAN UNIVERSITY

本发明属于化工催化剂技术领域,具体为一种用于二氧化碳气氛下乙烷脱氢制乙烯的尖晶石催化剂及其制备方法。本发明催化剂为掺杂氧化镓的镁铝尖晶石,其通式为:MgGa x Al 2‑ x O 4 , x =0.5~2。制备时以可溶性无机盐为前驱体,尿素为沉淀剂,经过溶剂热共沉淀处理,再通过焙烧得到催化剂。本发明方法过程简单、原料易得。制备的催化剂稳定性好,失活慢,易再生;用于二氧化碳气氛下乙烷脱氢反应,乙烷的转化率高且乙烯的选择性较好。

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18-06-2018 дата публикации

Acid-resistant catalyst for decomposing perfluorinated compounds and use thereof

Номер: KR101867507B1
Принадлежит: 주식회사 에코프로

본 발명은 트리하이드록사이드(aluminum trihydroxide), 보에마이트(boehmite) 및 의보에마이트(pseudo-boehmite)로 구성된 군에서 선택된 원료와, 지르코니아(ZrO 2 ) 또는 지르코니아 졸을 물 함유 용매에서 혼합, 건조 및 소성하여 제조한, 알루미나 및 지르코니아 혼합 촉매 지지체를 포함하되, 바람직하게는 알루미나 및 지르코니아 혼합 촉매 지지체에 활성금속으로 아연(Zn)이 담지된 것이 특징인 과불화 화합물 분해용 촉매를 제공한다. 본 발명에 따른 과불화 화합물 분해용 촉매는 내산성 촉매로서, 과불화 화합물에 포함된 할로겐족 산성가스 또는 과불화합물이 분해하여 생성된 불소에 대해 내구성을 가지며, 반응활성도 증진시킬 수 있다. 따라서, 반도체 제조공정 및 디스플레이 제조공정에서 사용되는 과불화 화합물의 세정제 및 에칭제를 분해하는 목적으로 사용이 가능하고, 특히 F 2 , Cl 2 , Br 2 등과 같은 할로겐 산성가스를 사용하는 공정에서 배출되는 과불화 화합물을 분해하는 촉매로 유용하게 사용할 수 있다. The present invention relates to a process for the preparation of zirconia (ZrO 2 ) or zirconia sol from raw materials selected from the group consisting of aluminum trihydroxide, boehmite and pseudo-boehmite, (Zn) supported on an alumina and zirconia mixed catalyst support, comprising an alumina and zirconia mixed catalyst support prepared by drying and firing an alumina and zirconia mixed catalyst support. The catalyst for decomposing a perfluorinated compound according to the present invention is an acid-resistant catalyst having durability against fluorine generated by decomposition of a halogen acid gas or a perfluorinated compound contained in a perfluorinated compound, and can increase the reaction activity. Therefore, for the purpose of decomposition of the semiconductor manufacturing processes and cleaning agents and etchants in the perfluorinated compounds to be used in display manufacturing process used is possible, in particular, F 2, Cl 2, discharged from the process using a halogen acid gas, such as Br 2 Which can be used as a catalyst for decomposing perfluorinated compounds.

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21-09-2018 дата публикации

Interesterification catalyst and process

Номер: RU2667526C2

FIELD: technological processes. SUBSTANCE: invention relates to a process for the production of an ester product by interesterification from a first mixture comprising at least two different ester compounds to form a second ester mixture having a lower melting point than the melting point of said first ester mixture comprising the following steps of: a) mixing at least two different starting ester compounds to form a first ester mixture and b) contacting said first ester mixture with a catalyst comprising from 30 to 60 wt% of calcium oxide and at least one second metal oxide, wherein the second metal oxide is selected from the group consisting of a group 2A metal oxide other than calcium, a transition metal oxide, a lanthanum oxide, a silica, an alumina and a metal aluminate. Invention also relates to a catalyst intended for use in interesterification reaction. EFFECT: method for the production of an ester product is proposed. 14 cl, 38 ex, 3 tbl РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (51) МПК B01J 23/02 (2006.01) B01J 23/04 (2006.01) B01J 23/10 (2006.01) B01J 23/34 (2006.01) B01J 23/92 (2006.01) B01J 35/10 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА B01J 38/00 (2006.01) ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ C07C 67/03 (2006.01) C07C 69/24 (2006.01) C07C 69/533 (2006.01) (12) (13) 2 667 526 C2 C07C 69/58 (2006.01) C11C 3/10 (2006.01) ОПИСАНИЕ ИЗОБРЕТЕНИЯ К ПАТЕНТУ (52) СПК B01J 23/02 (2006.01); B01J 23/04 (2006.01); B01J 23/10 (2006.01); B01J 23/34 (2006.01); B01J 23/92 (2006.01); B01J 35/10 (2006.01); B01J 38/00 (2006.01); C07C 67/03 (2006.01); C07C 69/24 (2006.01); C07C 69/533 (2006.01); C07C 69/58 (2006.01); C11C 3/10 (2006.01) 2016110916, 15.08.2014 (24) Дата начала отсчета срока действия патента: 15.08.2014 (73) Патентообладатель(и): ДЖОНСОН МЭТТИ ПАБЛИК ЛИМИТЕД КОМПАНИ (GB) 21.09.2018 Приоритет(ы): (30) Конвенционный приоритет: (56) Список документов, цитированных в отчете о поиске: СN 102430400 A, 02.05.2012. WO 28.08.2013 GB 1315276.4 (43) Дата публикации заявки: 03.10.2017 Бюл. № ...

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17-12-2021 дата публикации

Metal oxide solid solution catalyst, preparation and application thereof

Номер: CN109420484B

本发明涉及一类用于二氧化碳加氢合成甲醇的金属氧化物固溶体催化剂M a O x ‑M b O y ,其中M a O x 为溶质,M b O y 为溶剂。所述的固溶体是指M b O y 晶体中一定量的M b 离子被M a 离子所置换但不改变整个晶体的结构及对称性。所述的固溶体中M a O x 包括ZnO、CdO、Ga 2 O 3 或In 2 O 3 ;M b O y 包括ZrO 2 或TiO 2 。所述的金属氧化物固溶体催化剂应用于二氧化碳加氢制甲醇反应,在2MPa,300℃,24000h –1 条件下可使甲醇选择性最高达85%。

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10-10-2005 дата публикации

METHOD FOR PRODUCING THE CARRIER FOR THE CATALYST FROM STABILIZED TRANSITION ALUMINUM OXIDE (OPTIONS), METHOD FOR PRODUCING THE FISCHER-TROPHES CATALYST AND METHOD FOR SYNTHESIS OF PARAFFIN CARBON CARBON CARBON

Номер: RU2005115063A

ÐÎÑÑÈÉÑÊÀß ÔÅÄÅÐÀÖÈß (19) RU (51) ÌÏÊ 7 (11) 2005 115 063 (13) A B 01 J 31/00 ÔÅÄÅÐÀËÜÍÀß ÑËÓÆÁÀ ÏÎ ÈÍÒÅËËÅÊÒÓÀËÜÍÎÉ ÑÎÁÑÒÂÅÍÍÎÑÒÈ, ÏÀÒÅÍÒÀÌ È ÒÎÂÀÐÍÛÌ ÇÍÀÊÀÌ (12) ÇÀßÂÊÀ ÍÀ ÈÇÎÁÐÅÒÅÍÈÅ (21), (22) Çà âêà: 2005115063/04, 16.10.2003 (71) Çà âèòåëü(è): ÊîíîêîÔèëëèïñ Êàìïýíè (US) (30) Ïðèîðèòåò: 16.10.2002 US 60/419,021 (43) Äàòà ïóáëèêàöèè çà âêè: 10.10.2005 Áþë. ¹ 28 (86) Çà âêà PCT: US 03/33460 (16.10.2003) (87) Ïóáëèêàöè PCT: WO 2004/035196 (29.04.2004) Àäðåñ äë ïåðåïèñêè: 127055, Ìîñêâà, à/ 11, ïàò.ïîâ. Í.Ê.Ïîïåëåíñêîìó R U ÏÅÐÅÕÎÄÍÎÃÎ ÎÊÑÈÄÀ ÀËÞÌÈÍÈß (ÂÀÐÈÀÍÒÛ), ÑÏÎÑÎÁ ÈÇÃÎÒÎÂËÅÍÈß ÊÀÒÀËÈÇÀÒÎÐÀ ÔÈØÅÐÀ-ÒÐÎÏØÀ È ÑÏÎÑÎÁ ÑÈÍÒÅÇÀ ÏÀÐÀÔÈÍÎÂÛÕ ÓÃËÅÂÎÄÎÐÎÄΠÈÇ ÑÈÍÒÅÇ-ÃÀÇÀ Ôîðìóëà èçîáðåòåíè 1. Ñïîñîá èçãîòîâëåíè íîñèòåë äë êàòàëèçàòîðà èç ñòàáèëèçèðîâàííîãî ïåðåõîäíîãî îêñèäà àëþìèíè , îòëè÷àþùèéñ òåì, ÷òî â ïåðåõîäíûé îêñèä àëþìèíè ââîä ò ïî êðàéíåé ìåðå îäèí ïðåäøåñòâåííèê ñòðóêòóðíîãî ñòàáèëèçàòîðà ñ îáðàçîâàíèåì îêñèäà àëþìèíè , ïðîïèòàííîãî ñòàáèëèçàòîðîì; ïî âûáîðó, âûñóøèâàþò ïðîïèòàííûé ñòàáèëèçàòîðîì îêñèä àëþìèíè ; îáðàáàòûâàþò åãî ïàðîì ïðè óñëîâè õ, äîñòàòî÷íûõ äë ïî êðàéíåé ìåðå ÷àñòè÷íîãî ïðåâðàùåíè ïðîïèòàííîãî ñòàáèëèçàòîðîì îêñèäà àëþìèíè â ïðîïèòàííûé ñòàáèëèçàòîðîì îêñèä àëþìèíè òèïà áåìèòà, è çàòåì ïðîêàëèâàþò ñîäåðæàùèé ñòàáèëèçàòîð îêñèä àëþìèíè òèïà áåìèòà. 2. Ñïîñîá ïî ï.1, îòëè÷àþùèéñ òåì, ÷òî ïåðåõîäíûé îêñèä àëþìèíè ñîäåðæèò ôàçó, âûáðàííóþ èç ãðóïïû, âêëþ÷àþùåé γ-Al2Î3, β -Al2Î3, θ-Al2Î3 è èõ ëþáûå êîìáèíàöèè. 3. Ñïîñîá ïî ï.1, îòëè÷àþùèéñ òåì, ÷òî ïåðåõîäíûé îêñèä àëþìèíè ñîäåðæèò ôàçó β -Al2O3. 4. Ñïîñîá ïî ï.1, îòëè÷àþùèéñ òåì, ÷òî ñòàáèëèçèðîâàííûé ïåðåõîäíûé îêñèä àëþìèíè ñîäåðæèò ôàçó, âûáðàííóþ èç ãðóïïû, âêëþ÷àþùåé γ-Al2Î3, β -Al2Î3, θ-Al2Î3 è èõ ëþáûå êîìáèíàöèè. 5. Ñïîñîá ïî ï.1, îòëè÷àþùèéñ òåì, ÷òî ñòàáèëèçèðîâàííûé ïåðåõîäíûé îêñèä àëþìèíè ñîäåðæèò ôàçó γ-Al2Î3. 6. Ñïîñîá ïî ï.1, îòëè÷àþùèéñ òåì, ÷òî ïî êðàéíåé ìåðå îäèí ïðåäøåñòâåííèê ñòðóêòóðíîãî ñòàáèëèçàòîðà ñîäåðæèò ïî êðàéíåé ìåðå îäèí ýëåìåíò, âûáðàííûé èç Ñòðàíèöà: 1 RU A ...

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17-12-1991 дата публикации

Catalyst comprising TiO2 dispersed phase on a monolayer of SiO2 on alumina support

Номер: US5073658A
Принадлежит: Exxon Chemical Patents Inc

The present invention provides for a non-nickel-containing catalyst which is effective for use in the production of dimer products and higher olefin products from a butene starting material at relatively high conversion, good selectivity towards octene production and good activity maintenance over prolonged polymerization times. The catalyst is prepared by impregnating an amorphous trivalent metal oxide support selected from the group consisting of aluminum oxide, gallium oxide and indium oxide with a silicon-containing precursor compound which, after calcination, yields a substantial mono layer of SiO 2 on the surface of the metal oxide support. A disperse layer of TiO 2 is then deposited on the surface of the SiO 2 monolayer by application of a solvent solution of a precursor compound containing titanium onto the SiO 2 monolayer, followed by calcination to reduce the precursor titanium compound to TiO 2 .

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20-12-1983 дата публикации

Olefin isomerization

Номер: JPS58219128A
Принадлежит: SnamProgetti SpA

(57)【要約】本公報は電子出願前の出願データであるた め要約のデータは記録されません。

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20-04-2010 дата публикации

CATALYST SYSTEM AND METHOD OF REDUCING NOx

Номер: RU2386475C2

FIELD: chemistry. SUBSTANCE: invention relates to a catalyst system and a method of reducing nitrogen oxide emissions. The described catalyst system for reducing NO x contains: a catalyst having a support which contains at least one compound selected from a group consisting of aluminium oxide, titanium dioxide, zirconium dioxide, cerium oxide, silicon carbide and mixtures thereof, a catalytic metal oxide containing at least one of gallium oxide or silver oxide and at least one activating metal selected from a group consisting of silver, cobalt, molybdenum, tungsten, indium or mixtures thereof; and a gas stream containing oxygen ranging from approximately 1 mol % to approximately 12 mol % and an organic reducing agent selected from a group consisting of alcohol, carbonate or combinations thereof, where the said organic reducing agent and the said NO x are present in molar ratio carbon: NO x ranging from approximately 0.5:1 to approximately 24:1. A catalyst system for reducing NO x which contains the following is described: a catalyst consisting of (i) metal oxide support which contains aluminium oxide, (ii) at least one of the following oxides: gallium oxide or silver oxide, present in amount ranging from approximately 5 mol % to approximately 31 mol %; and (iii) an activating metal or a combination of activating metals, present in amount ranging from approximately 1 mol % to approximately 22 mol % and selected from a group consisting of silver, cobalt, molybdenum, tungsten, indium and molybdenum, indium and cobalt, and indium and tungsten; and a gas stream containing (A) water in range from approximately 1 mol % to approximately 12 mol %; (B) oxygen in the range from approximately 1 mol % to approximately 15 mol %; and (C) an organic reducing agent containing oxygen and selected from a group consisting of methanol, ethanol, butyl alcohol, propyl alcohol, dimethyl carbonate or combinations thereof; where the said organic reducing agent and NO x are present in molar ...

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01-02-2012 дата публикации

Fuel-saving porous oxidation reaction catalysis material fuel and preparation method thereof

Номер: CN101564700B
Автор: 李昌烨, 郑煐勋
Принадлежит: Individual

本发明涉及一种节约燃料的多孔性氧化反应催化材料及其制备方法。具体地说,是一种当燃料燃烧时,在促进氧化反应的同时,还能够活化燃料分解,使燃料完全燃烧,从而节约燃料的多孔性氧化反应催化材料。依据本发明,当燃料燃烧时,通过促进化学反应即氧化反应,就可以节约燃料,它无需其它的节约燃料专用设备,获得了较好的经济效益。它与通过物理方式促进燃料完全燃烧的方法相比,其节约燃料的效率更高。

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11-12-1992 дата публикации

CERIC OXIDE COMPOSITION, PREPARATION THEREOF AND USES THEREOF.

Номер: FR2677347A1
Принадлежит: Rhone Poulenc Chimie SA

La présente invention cocnerne une composition à base d'oxyde de cérium à surface spécifique thermiquemeent stabilisée et des procédés de fabrication de cette composition. Cette composition à base d'oxyde cérique comprend un oxyde cérique et au moins un oxyde d'un élément métallique A choisi dans le groupe comprenant le magnésium, le scandium, le gallium et le bore. Utilisation comme catalyseur. The present invention relates to a composition based on cerium oxide with a thermally stabilized specific surface area and methods of making this composition. This composition based on ceric oxide comprises a ceric oxide and at least one oxide of a metallic element A chosen from the group comprising magnesium, scandium, gallium and boron. Use as a catalyst.

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02-12-1983 дата публикации

METHOD OF ISOMERIZING THE OLEFIN BOND

Номер: FR2527596A1
Принадлежит: SnamProgetti SpA

CE PROCEDE POUR L'ISOMERISATION DE LA LIAISON OLEFINIQUE EST EFFECTUE A L'AIDE D'UN CATALYSEUR A BASE D'ALUMINE GAMMA CONTENANT SIO ET D'OXYDES D'UN METAL CHOISIS PARMI CEUX DU GROUPE II A ETOU VIII ETOU IIIB ETOU LES LANTHANIDES, AVEC DES RAPPORTS MOLAIRES PARTICULIERS ENTRE LES DIVERS OXYDES. LE CATALYSEUR EST STABLE THERMIQUEMENT ET DANS LA CONVERSION DU BUTENE-2 EN BUTENE-1 IL PERMET D'OBTENIR LE BUTENE-1 AVEC UNE TENEUR EN ISOBUTENE INFERIEURE AUX LIMITES PERMISES POUR LE BUTENE-1 DESTINE A LA POLYMERISATION. THIS METHOD FOR ISOMERIZING THE OLEFIN BOND IS CARRIED OUT USING A CATALYST BASED ON SIO-CONTAINING ALUMINA GAMMA AND OXIDES OF A METAL CHOSEN FROM THOSE OF GROUP II TO ETOU VIII ETOU IIIB ETOU LANTHANIDES , WITH PARTICULAR MOLAR REPORTS BETWEEN THE VARIOUS OXIDES. THE CATALYST IS THERMALLY STABLE AND IN THE CONVERSION OF BUTENE-2 TO BUTENE-1 IT ALLOWS OBTAINING BUTENE-1 WITH AN ISOBUTENE CONTENT LESS THAN THE LIMITS PERMITTED FOR BUTENE-1 FOR POLYMERIZATION.

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13-07-1978 дата публикации

DEHYDROCYCLO-DIMERIZATION OF A CHARGE OF HYDROCARBONS IN C3 TO C8, FOR THE MANUFACTURE OF AROMATIC HYDROCARBONS, IN PARTICULAR OF XYLENES

Номер: FR2374284A1
Принадлежит: BP PLC

L'invention a trait au domaine de la fabrication d'hydrocarbures aromatiques à partir d'hydrocarbures linéaires en C3 à C8. Le procédé selon l'invention est essentiellement caractérisé en ce qu'on met en contact les hydrocarbures en C3 à C8 , à température élevée, avec un catalyseur comprenant du gallium sur un support de silice, cette dernière ayant une surface active supérieure à 500 m**2/gramme et un volume des pores inférieur à 0,8 cm**3/gramme. Application notamment à la fabrication des xylènes. The invention relates to the field of the manufacture of aromatic hydrocarbons from linear C3 to C8 hydrocarbons. The process according to the invention is essentially characterized in that the C3 to C8 hydrocarbons are brought into contact, at high temperature, with a catalyst comprising gallium on a silica support, the latter having an active surface greater than 500 m. ** 2 / gram and a pore volume of less than 0.8 cm ** 3 / gram. Application in particular to the manufacture of xylenes.

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10-09-1985 дата публикации

Catalyst based on gamma alumina, and its method of preparation

Номер: CA1193238A
Принадлежит: SnamProgetti SpA

CATALYST BASED ON GAMMA ALUMINA, AND ITS METHOD OF PREPARATION Abstract Or the Disclosure A catalyst based on gamma alumina, constituted by gamma alumina stabilised by silica containing oxides of bivalent or trivalent metals chosen from those of Group II A and/or VIII and/or III B and/or lanthanides. The catalyst is particularly active in isomerisation reactions.

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07-06-1974 дата публикации

Patent FR2206298A1

Номер: FR2206298A1
Автор: [UNK]
Принадлежит: BASF SE

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16-09-1959 дата публикации

Advanced catalytic process for the oxidation of aliphatic compounds

Номер: FR1187762A
Автор:
Принадлежит: Imperial Chemical Industries Ltd

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15-02-2017 дата публикации

Preparation method and application of carbon nanofiber-bimetal composite catalyst

Номер: CN106391029A
Принадлежит: SOUTHEAST UNIVERSITY

本发明公开了一种纳米碳纤维‑双金属复合催化剂的制备方法及应用,具体涉及将碱土金属盐混入纺丝液中进行纺丝,再将原丝混合硝酸,过渡金属盐进行浸渍。所得双金属复合原纤维经预氧化、碳化后即得纳米碳纤维/双金属复合催化剂。本发明利用纺丝过程中嵌在纤维上的碱土金属与过渡金属高温时的相互作用固定活性组分,保证了载体表面活性组分的高度分散及高温抗烧结性,同时利用碱土金属在CH 4 /CO 2 重整过程中吸附活化CO 2 的特性保证了800℃95%左右的转化率。

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11-04-2015 дата публикации

New compound semiconductors and their application

Номер: TWI480226B
Принадлежит: Lg Chemical Ltd

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25-09-2018 дата публикации

Catalyst for hydroisomerization of hydrocarbon fractions and method of its application

Номер: RU2667920C1

FIELD: oil and gas industry.SUBSTANCE: invention relates to the field of oil refining, in particular to a hydroisomerization catalyst for hydrocarbon fractions and a method for using it. Hydroisomerization catalyst of the hydrocarbon fractions contains 0.05–8.0 % by weight at least one metal or metal compound selected from the series: platinum, palladium, rhenium, nickel, cobalt, chromium, manganese, molybdenum, tin, lead, zirconium, lanthanum, 5–75 % by weight crystalline ferroaluminosilicate or ferrogallium aluminosilicate with ZSM-5 or ZSM-11 zeolite structure and aluminium oxide is the rest. When the catalyst is used in the hydroisomerization of hydrocarbon fractions, the process is carried out at a temperature of 260–360 °C, a pressure of 0.1–5.0 MPa, volume feed rate of liquid feed 0.5–10 h, molar ratio of hydrogen to hydrocarbons 1–12.EFFECT: technical result consists in lower temperature of the complete burning out of the catalyst coke at the stage of catalyst regeneration.6 cl, 3 dwg, 2 tbl, 18 ex РОССИЙСКАЯ ФЕДЕРАЦИЯ ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) (19) RU (11) (13) 2 667 920 C1 (51) МПК B01J 29/88 (2006.01) B01J 23/38 (2006.01) B01J 23/16 (2006.01) C10G 45/64 (2006.01) C07C 5/27 (2006.01) B01J 23/08 (2006.01) B01J 23/10 (2006.01) ОПИСАНИЕ ИЗОБРЕТЕНИЯ К ПАТЕНТУ (52) СПК B01J 29/88 (2006.01); B01J 23/38 (2006.01); B01J 23/16 (2006.01); B01J 23/08 (2006.01); B01J 23/10 (2006.01); C07C 5/27 (2006.01); C10G 45/64 (2006.01) (21)(22) Заявка: 2018128108, 30.07.2018 30.07.2018 Дата регистрации: Приоритет(ы): (22) Дата подачи заявки: 30.07.2018 (56) Список документов, цитированных в отчете о поиске: RU 2658018 С1, 19.06.2018. CN (45) Опубликовано: 25.09.2018 Бюл. № 27 (54) Катализатор для гидроизомеризации углеводородных фракций и способ его применения (57) Реферат: Изобретение относится к области цеолита ZSM-5 или ZSM-11 и оксид алюминия нефтепереработки, в частности к катализатору остальное. При применении катализатора в ...

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07-03-1986 дата публикации

Method of converting lower paraffinic hydrocarbon into aromatic hydrocarbon

Номер: JPS6147423A
Автор: Satoyuki Inui, 智行 乾
Принадлежит: Individual

(57)【要約】本公報は電子出願前の出願データであるた め要約のデータは記録されません。

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28-09-2017 дата публикации

Catalyst composition for internal combustion engine

Номер: WO2017164637A2
Автор: 김칠곤, 손복수, 유명도
Принадлежит: 유명도

The present invention relates to a catalyst composition for an internal combustion engine, comprising 2-ethylhexyl acetate as an ignition improver, a polyalkylene glycol, a metal nitrate compound, and a polyvinyl alcohol, and thus the present invention improves fuel ignitability so as to enhance fuel efficiency, thereby reducing exhaust gas fumes.

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10-04-2016 дата публикации

Mixed oxide based catalyst and method of producing ethylenically unsaturated carboxylic acids or esters

Номер: RU2579516C2

FIELD: chemistry. SUBSTANCE: invention relates to a catalyst for the reaction of formaldehyde or a suitable source thereof with a carboxylic acid or ester to produce an ethylenically unsaturated carboxylic acid or ester, preferably an α,β-position ethylenically unsaturated carboxylic acid or ester, where the catalyst includes a metal oxide having at least two types of metal cations, M 1 and M 2 , where M 1 is at least one metal selected from group 3 or 4 in the 4th to 6th periods of the periodic table, group 13 in the 3rd to 5th periods of the periodic table, or the remaining elements in the lanthanide series, namely scandium, yttrium, lanthanide elements, titanium, zirconium, hafnium, aluminium, gallium, indium, and M 2 is at least one metal selected from group 5 in the 5th or 6th periods of the periodic table or group 15 in the 4th or 5th periods of the periodic table, namely niobium, tantalum, arsenic and antimony, wherein the ratio of M 1 :M 2 is in the range of 5:1 to 1:5 and wherein the metal oxide based catalyst compound according to the invention does not include other types of metals above the 0.1 mol% level, different from M 1 , M 2 and, optionally, M 3 and/or M 4 . The present invention also relates to the method of producing an ethylenically unsaturated carboxylic acid or ester and to the use of the catalyst (versions). EFFECT: obtaining the catalyst which provides high catalytic activity in the reaction of formaldehyde or a suitable source thereof with a carboxylic acid or ester to obtain ethylenically unsaturated carboxylic acids or esters. 33 cl, 13 ex, 6 tbl РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (13) 2 579 516 C2 (51) МПК B01J 23/08 (2006.01) B01J 23/10 (2006.01) B01J 23/18 (2006.01) B01J 23/20 (2006.01) B01J 37/03 (2006.01) C07C 51/353 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА C07C 67/343 (2006.01) ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ C07C 57/04 (2006.01) C07C 69/54 (2006.01) (12) ОПИСАНИЕ (21)(22) Заявка: ИЗОБРЕТЕНИЯ К ПАТЕНТУ 2013104203/04, 24.06.2011 (24) Дата ...

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31-03-2023 дата публикации

ZnO/In (OH) with different shapes 3 Preparation method of composite photocatalyst

Номер: CN111013562B

本发明公开了一种不同形貌ZnO/In(OH) 3 复合光催化材料的制备方法,属于纳米材料以及光催化材料制备领域。该方法采用如下步骤:1)配置一定浓度的In源溶液;2)将Zn源溶液与In源溶液混合搅拌,用氨水调节pH为9左右,搅拌至均匀得到白色混合溶液:3)将混合溶液转移至高压反应釜,以一定温度在一定时间下进行水热反应;4)将产物冷却到室温离心并用去离子水、乙醇洗涤;5)将产物置于干燥箱中干燥处理。本发明采用的合成方法流程简单,操作简便,无二次污染。合成的光催化材料具有形貌均一、性能优异等特点。

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26-01-1988 дата публикации

Methane conversion

Номер: US4721828A
Автор: Howard P. Withers
Принадлежит: Atlantic Richfield Co

A method for synthesizing hydrocarbons from a methane source which comprises contacting methane with a reducible oxide of Fe. The iron oxide is preferably combined with an amount of alkali and/or alkaline earth metal which is sufficient to improve the selectively to higher hydrocarbon products. The oxide is reduced by the contact which is carried at about 500° to 1000° C. Reducible oxides of Fe are regenerated by oxidizing the reduced composition with oxygen. The oxide Fe 3 O 4 is particularly effective in the process. Bulk iron oxides promoted by sodium and/or compounds thereof are particularly preferred contact solids.

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17-04-2020 дата публикации

ZnO/in (OH) with different shapes3Preparation method of composite photocatalyst

Номер: CN111013562A

本发明公开了一种不同形貌ZnO/In(OH) 3 复合光催化材料的制备方法,属于纳米材料以及光催化材料制备领域。该方法采用如下步骤:1)配置一定浓度的In源溶液;2)将Zn源溶液与In源溶液混合搅拌,用氨水调节pH为9左右,搅拌至均匀得到白色混合溶液:3)将混合溶液转移至高压反应釜,以一定温度在一定时间下进行水热反应;4)将产物冷却到室温离心并用去离子水、乙醇洗涤;5)将产物置于干燥箱中干燥处理。本发明采用的合成方法流程简单,操作简便,无二次污染。合成的光催化材料具有形貌均一、性能优异等特点。

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07-11-2015 дата публикации

Nanostructured metal oxide compositions for applied photocatalysis

Номер: CA2890789A1
Принадлежит: Individual

A nanostructured metal oxide composition comprising hydroxides or oxygen vacancies or both hydroxides and oxygen vacancies on its surface is described. A process for preparing the nanostructured metal oxide composition comprising hydroxides or oxygen vacancies or both hydroxides and oxygen vacancies on its surface, which hydroxides and oxygen vacancies can participate in chemical reactions, which composition is prepared by a method selected from the group of methods comprising: i) controlled thermally induced dehydroxylation of nanostructured metal hydroxide precursors; ii) thermochemical reaction of said nanostructured metal oxide with hydrogen gas; iii) vacuum thermal treatment of said nanostructured metal oxide; and iv) aliovalent doping with a lower oxidation state metal. A photocatalyst comprising a nanostructured metal oxide composition comprising an optimal loading of hydroxides or oxygen vacancies or both hydroxides and oxygen vacancies on its surface, which hydroxides and/or oxygen vacancies can participate in chemical or physical reactions.

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23-03-2021 дата публикации

Black indium oxide ultrathin nanosheet and preparation method and photo-thermal catalysis application thereof

Номер: CN109647373B
Принадлежит: TIANJIN UNIVERSITY

本发明公开了一种黑色氧化铟超薄纳米片及其制备方法和光热催化应用,通过光热还原的手段在纳米氧化铟晶体的形成过程中引入大量氧空位活性位点,相比传统的宽带隙的淡黄色氧化铟,引入的氧空位不仅扩展了材料对光的吸收范围,也提高了材料的光热转化效率。并且由于黑色氧化铟纳米片特殊的二维层状结构,导致在其周围的二氧化碳分子可以被片层表面高浓度的氧空位活性位点高效吸附并活化,在汇聚太阳光照射的条件下,催化CO 2 和H 2 反应,合成工业费托反应的原料CO。该方法绿色环保,简单可行,产品纯净无其他杂质,使得本发明制备的黑色氧化铟纳米片在电子、光电、和环境能源领域具有广泛的应用前景。

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02-07-2018 дата публикации

A mixed oxide catalyst and a process for the production of ethylenically unsaturated carboxylic acids or esters

Номер: KR101873036B1

본 발명은 에틸렌성 불포화 카르복시산 또는 에스테르를 제조하기 위한, 포름알데하이드 또는 그의 적절한 공급원과 카르복시산 또는 에스테르의 반응용 촉매에 관한 것이다. 상기 촉매는 2가지 유형 이상의 금속 양이온 M 1 및 M 2 를 가진 금속 산화물을 포함하며, 이때 M 1 은 주기율표의 4 주기 내지 6 주기에 속한 3족 또는 4족, 주기율표의 3 주기 내지 5 주기에 속한 13족, 또는 란탄계열의 나머지 원소들 중에서 선택된 1종 이상의 금속이고, M 2 는 주기율표의 5 주기 또는 6 주기에 속한 5족, 또는 주기율표의 4 주기 또는 5 주기에 속한 15족 중에서 선택된 1종 이상의 금속이다. 본 발명은 또한 에틸렌성 불포화 카르복시산 또는 에스테르의 제조 방법에 관한 것이다. The present invention relates to a catalyst for the reaction of a carboxylic acid or ester with formaldehyde or a suitable source thereof for preparing an ethylenically unsaturated carboxylic acid or ester. Wherein the catalyst comprises a metal oxide having two or more types of metal cations M 1 and M 2 , wherein M 1 is a Group 3 or 4 group belonging to 4 to 6 cycles of the periodic table, 13 or a group of the remaining elements of the lanthanide series, M 2 is at least one element selected from the group consisting of 5 elements belonging to 5 or 6 elements of the periodic table, or 15 elements selected from 15 elements belonging to 4 or 5 periods of the periodic table, It is metal. The present invention also relates to a process for the preparation of ethylenically unsaturated carboxylic acids or esters.

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17-09-2003 дата публикации

Catalyst having two-peak hole radius distribution

Номер: CN1121268C
Принадлежит: BASF SE

具有双峰孔半径分布的催化剂,含有a)10-99.9%重量的二氧化锆,和b)0-60%重量的氧化铝、二氧化硅和/或二氧化钛,和c)0.1-10%重量的元素周期表中IA族或IIA族的至少一种元素,过渡族III的一种元素,过渡族VIII的一种元素,镧和/或锡,条件是重量百分比的总和为100。

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25-06-2015 дата публикации

An improved glycol acylation process

Номер: CA2932349A1
Принадлежит: Archer Daniels Midland Co

A method for acid-catalyzed acylation of an isohexide is described. The method can enable direct alcohol acylation with carboxylic acids. In particular, the method involves reacting an isohexide and an excess of carboxylic acid, in the presence of a water-tolerant Lewis acid catalyst. Water-tolerant Lewis aid catalysts can furnish relatively high diester yields (e.g., = 55%-60%) at lower catalyst loads. This feature, among others, is highly desirable for cost savings, and can improve process economics.

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03-04-2002 дата публикации

Crystalline Gallium Silicate Catalysts and their use in the preparation of Est ers

Номер: GB2367292A
Автор: Kazuyuki Matsuoka
Принадлежит: Daicel Chemical Industries Ltd

A catalyst used in the production of a carboxylic acid ester from an olefin and a carboxylic acid comprises a crystalline gallium silicate. The ratio of silicon to gallium is about 10/1 to 500/1 (molar ratio). The olefin may for example be a chain C<SB>2-20</SB> olefin or a cyclic C<SB>3-12</SB> olefin. The carboxylic acid may for example be a C<SB>1-18</SB> aliphatic carboxylic acid, a C<SB>4-8</SB> alicyclic carboxylic acid, or an aromatic carboxylic acid. The esterification catalyst is not corrosive, with the aid of which an olefin can react with a carboxylic acid even under a relatively low pressure to produce the corresponding carboxylic acid ester.

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18-08-2010 дата публикации

A catalyst and a process for the production of ethylenically unsaturated carboxylic acids or esters

Номер: GB201011091D0
Автор: [UNK]
Принадлежит: Lucite International UK Ltd

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31-08-1990 дата публикации

Process for obtaining a catalyst on the base of gamma-alumina, for izomerization reactions

Номер: YU44435B
Принадлежит: Snam Progetti

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09-12-1983 дата публикации

ALUMINA GAMMA CATALYST AND PROCESS FOR PREPARING THE SAME

Номер: FR2527941A1
Принадлежит: SnamProgetti SpA

CE CATALYSEUR A BASE D'ALUMINE GAMMA EST CONSTITUE PAR DE L'ALUMINE GAMMA STABILISEE PAR DE LA SILICE CONTENANT DES OXYDES DE METAUX BIVALENTS OU TRIVALENTS CHOISIS PARMI CEUX DES GROUPES IIA ETOU VIII ETOU IIIB ETOU DES LANTHANIDES. UTILISATION DE CES CATALYSEURS DANS LES REACTIONS D'ISOMERISATION.

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30-04-1991 дата публикации

Alkoxylation catalyst

Номер: US5012012A
Принадлежит: Lion Corp

An alkoxylation catalyst for causing an alkylene oxide to react with an organic compound having one or more active hydrogen, comprising magnesium oxide modified by the addition of at least one metal ion selected from the group consisting of Al 3+ , Ga 3+ , In 3+ , Tl 3+ , Co 3+ , Sc 3+ , La 3+ , and Mn 2+ . In the presence of the catalyst, an addition polymerization reaction between the alkylene oxide and the organic compound having one or more active hydrogen such as an alcohol or phenol can be performed with only small amounts of unreacted material and byproducts, and the alkylene oxide adduct having a very narrow alkylene oxide adduct distribution can be obtained.

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20-04-1989 дата публикации

Process for the preparation of an aromatic hydrocarbon mixture

Номер: AU583013B2
Автор: Eduard Philip Kieffer

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07-03-1984 дата публикации

OLEFINIC LINK ISOMERIZATION PROCESS

Номер: LU84823A1
Принадлежит: Snam Progetti

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13-02-1985 дата публикации

Olefin bond isomerisation process

Номер: MW2283A1
Автор: [UNK]
Принадлежит: Snam Progetti

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29-11-2016 дата публикации

CRYSTAL ORGANIC-INORGANIC MATERIAL BASED ON CATIONS OF GROUP XIII OF THE PERIODIC TABLE, PREPARATION AND USE PROCEDURE

Номер: ES2561352B1

Material órgano-inorgánico cristalino basado en cationes del grupo XIII de la tabla periódica, procedimiento de preparación y uso.#La presente invención se refiere a una familia de materiales órgano-inorgánicos cristalinos conteniendo cationes del grupo XIII (Al, Ga e In) y la combinación química de éstos, y ácidos policarboxílicos, su procedimiento de preparación y su uso como catalizadores heterogéneos reutilizables para reacciones en química orgánica. Crystalline organ-inorganic material based on cations of group XIII of the periodic table, preparation and use procedure. # The present invention relates to a family of crystalline organ-inorganic materials containing cations of group XIII (Al, Ga and In) and the chemical combination of these, and polycarboxylic acids, their preparation process and their use as reusable heterogeneous catalysts for reactions in organic chemistry.

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20-01-1978 дата публикации

PROCESS FOR THE PRODUCTION OF UNSATURATED HYDROCARBONS BY OLIGOMERIZATION OF MONO-OLEFINIC HYDROCARBONS

Номер: FR2355790A1
Принадлежит: BP PLC

La présente invention concerne un procédé de production d'hydrocarbures non saturés. Le procédé selon l'invention est caractérisé en ce qu'on soumet une mono-oléfine en C3 à C8 à une oligomérisation en présence d'une composition catalytique constituée par un composé de gallium déposé sur un support. Ce procédé est destiné à l'oligomérisation de monooléfines en C3 à C8 , en vue d'obtenir des hydrocarbures non saturés. The present invention relates to a process for producing unsaturated hydrocarbons. The process according to the invention is characterized in that a C3 to C8 monoolefin is subjected to oligomerization in the presence of a catalytic composition consisting of a gallium compound deposited on a support. This process is intended for the oligomerization of C3 to C8 monoolefins, with a view to obtaining unsaturated hydrocarbons.

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10-06-2009 дата публикации

GLASS BROWNING LIGHTING FOR PASSENGER TRANSPORT

Номер: DE602004020940D1
Принадлежит: Otis Elevator Co

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