Настройки

Укажите год
-

Небесная энциклопедия

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

Подробнее
-

Мониторинг СМИ

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

Подробнее

Форма поиска

Поддерживает ввод нескольких поисковых фраз (по одной на строку). При поиске обеспечивает поддержку морфологии русского и английского языка
Ведите корректный номера.
Ведите корректный номера.
Ведите корректный номера.
Ведите корректный номера.
Укажите год
Укажите год

Применить Всего найдено 1394. Отображено 100.
27-12-2012 дата публикации

Catalyst composition for direct conversion of ethanol to propylene

Номер: US20120330080A1
Принадлежит: Dow Global Technologies LLC

A process to prepare propylene showing desirably increased selectivity comprises contacting, at an elevated temperature, ethanol and a rhenium oxide-modified ZSM-5 zeolite catalyst, under conditions suitable to form propylene. The rhenium oxide-modified ZSM-5 zeolite catalyst may be prepared by impregnating, in an aqueous or organic medium, a ZSM-5 zeolite with a rhenium source, under conditions suitable to form a catalyst precursor, and calcining the catalyst precursor under conditions suitable to form a rhenium oxide-modified ZSM-5 zeolite catalyst.

Подробнее
25-07-2013 дата публикации

NOx REDUCTION CATALYST FOR EXHAUST GAS AND METHOD FOR PRODUCING SAME

Номер: US20130190166A1
Принадлежит: BABCOCK-HITACHI KABUSHIKI KAISHA

To provide a catalyst having excellent performance and durability by improving a NOx reduction ratio at 350° C. or higher without deteriorating excellent durability of a Ti—V—Mo—P catalyst in view of problems of conventional art. A NOx reduction catalyst for exhaust gas, which is composed of a catalyst composition that comprises titanium (Ti), an oxide of phosphorous, molybdenum (Mo) and/or tungsten (W), oxide of vanadium (V), and high-silica zeolite that has an SiO/AlOratio of not less than 20 is obtained by kneading in the presence of water, drying and calcining (1) titanium oxide, and phosphoric acid or an ammonium salt of phosphoric acid in an amount of more than 1% by weight and not more than 15% by weight relative to the titanium oxide in terms of HPO, (2) an oxo acid or oxo acid salt of molybdenum (Mo) and/or tungsten (W) and an oxo acid salt of vanadium (V) or vanadyl salt respectively in an amount of more than 0% by atom and not more than 8% by atom relative to the titanium oxide and (3) high-silica zeolite in an amount of more than 0% by weight and not more than 20% by weight relative to the titanium oxide. 1. (canceled)2. (canceled)3. (canceled)4. A NOx reduction catalyst for exhaust gas , in which the catalyst is composed ofa calcination product comprising titanium (Ti), an oxide of phosphorous (P), molybdenum (Mo) and/or tungsten (W), oxide of vanadium (V), and high-silica zeolite.5. The reduction catalyst according to claim 4 , in whichthe titanium is derived from titanium oxide, the oxide of phosphorous is derived from phosphoric acid or an ammonium salt of phosphoric acid in the amount of more than 1% by weight and not more than 15% by weight relative to the titanium oxide in terms of H3PO4,the molybdenum (Mo) and/or tungsten (W) are/is derived from an oxo acid or oxo acid salt of molybdenum (Mo) and/or tungsten (W) in the amount of more than 0% by atom and not more than 8% by atom relative to the titanium oxide,the oxide of vanadium (V) is derived ...

Подробнее
15-08-2013 дата публикации

HYDROCRACKING CATALYST FOR PREPARING VALUABLE LIGHT AROMATIC HYDROCARBONS FROM POLYCYCLIC AROMATIC HYDROCARBONS

Номер: US20130210611A1
Принадлежит: SK INNOVATION CO., LTD.

This invention relates to a hydrocracking catalyst for preparing valuable light aromatic hydrocarbons from polycyclic aromatic hydrocarbons derived from oil, which includes (i) beta-zeolite, (ii) pseudo-boehmite, and (iii) one or more metals selected from among metals of Groups VIII and VIB, and which further includes a cocatalyst component, thereby producing a maximum amount of BTX (Benzene, Toluene, Xylene) from LCO (Light Cycle Oil). 1. A hydrocracking catalyst for preparing light aromatic hydrocarbons from polycyclic aromatic hydrocarbons , comprising:(i) beta-zeolite;(ii) pseudo-boehmite;(iii) one or more metals selected from the group consisting of the metals of Groups VIII and VIB.2. The hydrocracking catalyst of claim 1 , wherein the metal of Group VIII is cobalt.3. The hydrocracking catalyst of claim 1 , wherein the metal of Group VIB is molybdenum.4. The hydrocracking catalyst of claim 1 , wherein the metal of Group VIII or VIB is in the form of a sulfide.5. The hydrocracking catalyst of claim 1 , further comprising a cocatalyst.6. The hydrocracking catalyst of claim 5 , wherein the cocatalyst is one or more selected from the group consisting of tin (Sn) claim 5 , phosphorus (P) claim 5 , boron (B) claim 5 , silicon (Si) claim 5 , bismuth (Bi) claim 5 , and lead (Pb).7. The hydrocracking catalyst of claim 6 , wherein the cocatalyst is tin (Sn).8. The hydrocracking catalyst of claim 1 , wherein a total Si/Al atom ratio of the beta-zeolite is in a range of 5-200.9. The hydrocracking catalyst of claim 8 , wherein the total Si/Al atom ratio of the beta-zeolite is in the range of 10-150.10. The hydrocracking catalyst of claim 1 , wherein an amount of the beta-zeolite is 10-95 wt % based on a total weight of the catalyst.11. The hydrocracking catalyst of claim 10 , wherein the amount of the beta-zeolite is 30-90 wt % based on the total weight of the catalyst.12. The hydrocracking catalyst of claim 2 , wherein an amount of cobalt is 0.1-20 wt % based on a total ...

Подробнее
22-08-2013 дата публикации

PROCESS FOR PRODUCING LIGHT OLEFINS BY USING A ZSM - 5 - BASED CATALYST

Номер: US20130217939A1
Автор: Mammadov Aghaddin Kh.
Принадлежит: SAUDI BASIC INDUSTRIES CORPORATION

The present invention relates to a catalyst composition useful in a process for producing lower olefins from a oxygenate feedstream, a process for producing said catalyst composition and a process for producing lower olefins comprising contacting a oxygenate feedstream with the catalyst composition M-M-P/ZSM-5 with an oxygenate-comprising feedstream, wherein Mis one or more basic species, Mis one or more redox elements selected from Groups 6-8 of the Periodic Table of Elements and Sn and P is phosphorus, wherein said basic species is a molecular entity forming a weak Lewis base and/or a weak Bronsted base in the catalyst composition. In addition thereto, the present invention relates to an integrated process for producing lower olefins from a feedstream comprising hydrocarbons. 2. The process according to claim 1 , wherein the basic species is selected from the group consisting of alkaline earth metals claim 1 , rare earth elements and elements forming amphoteric oxide or hydroxide.3. The process according to claim 1 , wherein the basic species is an element selected from the group consisting of Mg claim 1 , Ca claim 1 , Sr claim 1 , La and Zr; or an amphoteric oxide or hydroxide of Mn.4. The process according to claim 1 , wherein the redox element is selected from the group consisting of Fe claim 1 , Cr claim 1 , W and Sn or Mn not forming an amphoteric oxide or hydroxide.5. The process according to claim 1 , further comprising a binder claim 1 , preferably silica (SiO).6. The process according to claim 1 , wherein the basic element is Ca and the redox element is Mn; or wherein the basic element is Mg and the redox element is Cr.7. The process according to claim 1 , wherein the oxygenate is selected from the group consisting of dimethyl ether (DME) claim 1 , diethyl ether claim 1 , methanol (MeOH) and ethanol (EtOH).8. The process according to claim 1 , wherein the oxygenate-comprising feedstream is produced by a process comprising:{'sub': 2', '2, '(i) a syngas ...

Подробнее
12-09-2013 дата публикации

ZEOLITE SCR CATALYSTS WITH IRON OR COPPER

Номер: US20130236382A1
Принадлежит: TECHNICAL UNIVERSITY OF DENMARK

Cu/mordenite catalysts were found to be highly active for the SCR of NO with NHand exhibited high resistance to alkali poisoning. Redox and acidic properties of Cu/mordenite were well preserved after poisoning with potassium unlike that of vanadium catalysts. Fe-mordenite catalysts also revealed much higher alkali resistivity than that of commercial VO/WO—TiO(VWT) SCR catalyst which is currently used for NOabatement in stationary installations. Unique support properties like high surface area and surface acidity, which are not available in the commercial VWT catalyst, seem to be essential requirements for the high alkali resistance. Mordenite-type zeolite based catalysts could therefore be attractive alternatives to conventional SCR catalysts for biomass fired power plant flue gas treatment. 112.-. (canceled)14. The method according to claim 13 , wherein the Cu precursor is copper nitrate.15. The method according to claim 13 , wherein the zeolite support is HMORDENITE (400 m/g).16. The method according to claim 13 , wherein the zeolite support is HMORDENITE (400 m/g) obtained by protonation of the ammonia form CBV21A zeolite support from Zeolyst International.17. A zeolite catalyst obtainable by a method according to .18. A catalyst according to claim 17 , which comprises 4% w/w Cu.19. A catalyst according to claim 17 , wherein the catalyst is shaped as a monolith claim 17 , extrudate claim 17 , bead claim 17 , plate claim 17 , sheet or fibrous cloth.20. A method of selectively removing nitrogen oxides with ammonia from gases resulting from the burning of biomass claim 17 , combined biomass-fossil fuel claim 17 , or emerging from waste incineration units at a temperature from 320 to 550° C. comprising providing a zeolite catalyst according to .21. The method according to claim 20 , wherein said gases contain between 200-1000 mg KCl/Nm.22. The method according to claim 20 , wherein said gases contain between 10-15% H0.23. The method according to claim 20 , wherein ...

Подробнее
16-01-2014 дата публикации

A HIGH-SELECTIVITY CATALYST FOR PRODUCTION OF HIGH-QUALITY GASOLINE FRACTIONS FROM SYNGAS AND ITS PREPARATION METHOD

Номер: US20140018232A1
Принадлежит:

The invention relates to a catalyst for selective synthesis of high-quality gasoline fractions from syngas and the preparation method of the catalyst. This catalyst consists of cobalt, a promoter and molecular sieve, wherein cobalt is presented in an amount of 1-30%, the promoter is represented in an amount of 0.01-5% and the balance is molecular sieve based on the weight of the catalyst. This catalyst provides superior selectivity for C-Cisoparaffins and relatively lower selectivity for wax-type hydrocarbons with more than 20 carbon atoms. Thereof, this catalyst can be used for the synthesis of high-quality gasoline and is good at preventing catalyst coking. Besides, the invention provides a preparation method of the catalyst. 114-. (canceled)15. A high-selectivity catalyst for production of high-quality gasoline fractions from syngas , consisting of cobalt , a promoter and molecular sieve , wherein cobalt is presented in an amount of 1-30% , the promoter is presented in an amount of 0.01-5% and the balance is the molecular sieve based on the weight of the catalyst.16. The catalyst according to claim 15 , wherein cobalt is represented in an amount of 8-15% and the promoter is represented in an amount of 0.05-2% based on the weight of the catalyst.17. The catalyst according to claim 16 , wherein the molecular sieve is one or more selected from Beta claim 16 , ZSM-5 claim 16 , MOR claim 16 , Y and MCM-22; preferably claim 16 , a Si/Al ratio of the molecular sieve is 5-300; further preferably claim 16 , the molecular sieve is Beta and/or ZSM-5 with the Si/Al ratio of 20-100.18. The catalyst according to claim 17 , wherein the acidity of the molecular sieve is denoted by an amount of NHadsorbed claim 17 , and the adsorbing capability of the molecular sieve is 0.16-0.50 mmol NH/g; the molecular sieve has micropore-mesopore structure claim 17 , wherein the micropore has a diameter of 0.4-0.9 nm claim 17 , and the mesopore has a diameter of 2-30 nm claim 17 , the specific ...

Подробнее
13-03-2014 дата публикации

SINC-CONTAINING METHANE AROMATIZATION CATALYST, METHOD OF MAKING A METHOD OF USING THE CATALYST

Номер: US20140073828A1
Принадлежит:

A catalyst for converting methane to aromatic hydrocarbons is described herein. The catalyst comprises an active metal or a compound thereof, zinc or a compound thereof and an inorganic oxide support wherein the active metal is added to the support as a metal oxalate. A method of making the catalyst and a method of using the catalyst are also described. 1. A methane aromatization catalyst comprising an active metal or a compound thereof , zinc or a compound thereof and an inorganic oxide support wherein the active metal is added to the support as a metal oxalate and the active metal is not zinc.2. A catalyst as claimed in wherein the active metal comprises molybdenum.3. A catalyst as claimed in wherein an additional promoter compound is added to the support.4. A catalyst as claimed in wherein the inorganic oxide support is a zeolite or zeolite-containing support.5. A catalyst as claimed in wherein the zeolite is a ZSM-5 type zeolite.6. A catalyst as claimed in wherein the molybdenum concentration in the catalyst is in the range of from 4 to 15% wt.7. A catalyst as claimed in wherein the molybdenum concentration in the catalyst is in the range of from 6 to 10% wt.8. A catalyst as claimed in wherein the zinc is added as a zinc oxalate.9. A catalyst as claimed in wherein the zinc is present in an amount of from 0.5 to 5.0% wt.10. A catalyst as claimed in wherein the zinc is present in an amount of from 0.7 to 2.0% wt.11. A process for preparing a methane aromatization catalyst comprising: contacting an active metal oxalate with an inorganic oxide support to form a mixture claim 1 , contacting zinc or a compound thereof with the mixture to form a catalyst precursor and calcining the precursor wherein the active metal oxalate does not comprise zinc.12. A process as claimed in wherein the active metal oxalate is in the form of a solution that is used to impregnate the inorganic support.13. A process as claimed in wherein the active metal compound comprises molybdenum.14. ...

Подробнее
05-01-2017 дата публикации

CATALYST COMPOSITION FOR ISOMERIZATION OF PARAFFINS

Номер: US20170001180A1
Принадлежит:

A catalyst composition for isomerization of paraffins includes at least one metal, at least one heteropoly acid and a support material. Further provided are a process for preparation of the catalyst composition and a process for isomerization of paraffins using the catalytic composition. 1. A catalyst composition comprising:at least one metal in an amount in the range of 0.1% to 10% w/w of the total weight of the composition;at least one heteropoly acid in an amount in the range of 14% to 50% w/w of the total weight of the composition; anda support material in an amount in the range of 60% to 85% w/w of the total weight of the composition.2. The catalyst composition as claimed in claim 1 , wherein the at least one metal in an amount in the range of 0.1% to 6% w/w of the total weight of the composition.3. The catalyst composition as claimed in claim 1 , wherein the at least one metal in an amount in the range of 1.5% to 6% w/w of the total weight of the composition.4. The catalyst composition as claimed in claim 1 , wherein the at least one metal is selected from the group consisting of alkali metal claim 1 , alkaline earth metal claim 1 , transitional metal claim 1 , lanthanides claim 1 , and combinations thereof.5. The catalyst composition as claimed in claim 1 , wherein the at least one metal is a alkali metal selected from the group consisting of Na claim 1 , K claim 1 , Rb claim 1 , Cs claim 1 , and combinations thereof.6. The catalyst composition as claimed in claim 1 , wherein the at least one metal is a transitional metal selected from the group consisting of Pt claim 1 , Ni claim 1 , Pd claim 1 , Re claim 1 , Ir claim 1 , Rh claim 1 , and combinations thereof.7. The catalyst composition as claimed in claim 1 , wherein the at least one metal is nickel in an amount in the range of 1.5% to 6% w/w of the total weight of the composition.8. The catalyst composition as claimed in claim 1 , wherein the at least one heteropoly acid in an amount in the range of 18% to ...

Подробнее
12-01-2017 дата публикации

PROCESS FOR PRODUCING AN SI-BONDED FLUIDIZED-BED CATALYST

Номер: US20170007989A1
Принадлежит: BASF SE

The invention relates to a process for producing a particulate, Si-bonded fluidized-bed catalyst having improved abrasion resistance, which comprises the steps 1. (canceled)2. A particulate fluidized-bed catalyst , obtained by a process comprising:(I) forming an aqueous suspension comprising zeolite particles;(II) adding a silicone resin mixture comprising a hydrolyzable silicone resin precondensate to the aqueous suspension and mixing the aqueous suspension and the silicone resin mixture, to obtain an intermediate mixture;(III) homogenizing the intermediate mixture and then spray draying the intermediate mixture, to obtain a spray-dried fluidized-bed catalyst; and(IV) calcinating the spray-dried fluidized-bed catalyst, to obtain a calcinated fluidized-bed catalyst.3. The particulate fluidized-bed catalyst according to claim 2 , comprising claim 2 , based on a total weight of the fluidized-bed catalyst:from 5 to 40% by weight of silicon dioxide; andfrom 60 to 95% by weight of zeolite.4. The particulate fluidized-bed catalyst according to claim 2 , comprising a zeolite having at least one structure selected from the group consisting of a pentasil structure and a MWW structure.5. The particulate fluidized-bed catalyst according to claim 2 , comprising:from 0.1 to 20% by weight of an active metal selected from the group consisting of Mo, W, Re, Ir, Ru, Rh, Pt, Pd and mixtures thereof, based on the total weight of the particulate fluidized-bed catalyst.6. The particulate fluidized-bed catalyst according to claim 5 , further comprising:at least one metal selected from the group consisting of W, Cu, Ni, Fe, Co, Mn, Cr, Nb, Ta, Zr, V, Zn and Ga.7. A process for dehydroaromatizing a C-C-aliphatic claim 5 , the process comprising:{'sub': 1', '4, 'claim-ref': {'@idref': 'CLM-00005', 'claim 5'}, 'reacting a feedstream comprising a C-C-aliphatic and less than 5% by weight of oxidants, based on a total weight of the feedstream, in the presence of a fluidized-bed catalyst ...

Подробнее
01-02-2018 дата публикации

Novel catalysts and process for liquid hydrocarbon fuel production

Номер: US20180029024A1
Автор: Liu Shetian, White Mark G.
Принадлежит:

The present invention provides a novel process and system in which a mixture of carbon monoxide and hydrogen synthesis gas, or syngas, is converted into hydrocarbon mixtures composed of high quality gasoline components, aromatic compounds, and lower molecular weight gaseous olefins in one reactor or step. The invention utilizes a novel molybdenum-zeolite catalyst in high pressure hydrogen for conversion, as well as a novel rhenium-zeolite catalyst in place of the molybdenum-zeolite catalyst, and provides for use of the novel catalysts in the process and system of the invention. 1. A process for the production of hydrocarbon fuel products having an aromatic content of about 90% or greater from synthesis gas comprising:providing a synthesis gas; andproviding an alcohol-forming catalyst;providing a single reaction system and steam reformer in which the chemical reactions occur over the alcohol-forming catalyst found in the same matrix as a gasoline-forming catalyst, with the synthesis gas contacted in a Fischer-Tropsch reaction with the alcohol-forming catalyst in high pressure hydrogen;wherein the alcohol-forming catalyst is a zeolite-encaged, molybdenum-based catalyst active for deoxy-aromatization of alcohols and synthesis gas to mixed alcohols, isomerization of alkanes, and aromatization; andwherein the alcohol-forming catalyst produces high quality alcohols from the synthesis gas.2. The process of claim 1 , wherein the catalyst is a cluster comprising a molybdenum oxide represented by MoCOencaged in a zeolite and wherein the cluster comprises the active phase.3. The process of claim 2 , wherein the cluster comprises a molybdenum sulfide.4. The process of claim 3 , wherein the cluster further comprises at least one metal modifier selected from the group consisting of the elements of Groups 1A and 2A of the Periodic Table and mixtures of the aforementioned elements.5. The process of claim 3 , wherein the zeolite comprises a support claim 3 , and comprises one or ...

Подробнее
17-02-2022 дата публикации

FUNCTIONAL STRUCTURE

Номер: US20220048014A1
Принадлежит:

A functional structure which can resist a decrease in the functions of the functional material caused by influences such as force and heat and thus have a long life. The functional structure includes supports each having a porous structure and including a zeolite-type compound, and at least one functional material present in the supports, in which each of the supports has channels communicating with one another, the functional material is present at least in the channel of each of the supports, the functional material present in the supports includes a metal element (M), and the content of the metal element (M) is more than 2.5 mass % with respect to the functional structure. 1. A functional structure comprising:supports each having a porous structure and including a zeolite-type compound; andat least one functional material present in the supports, whereineach of the supports has channels communicating with one another,the functional material is present at least in the channel of each of the supports,the functional material present in the supports comprises a metal element (M), andthe content of the metal element (M) is more than 2.5 mass % with respect to the functional structure.2. The functional structure according to claim 1 , wherein the functional material present in the supports comprises at least one of a metal and a metal oxide.3. The functional structure according to claim 1 , whereinthe channels have any one of a one-dimensional pore, a two-dimensional pore, and a three-dimensional pore of a framework structure of the zeolite-type compound, and have an enlarged pore portion different from the one-dimensional pore, the two-dimensional pore, and the three-dimensional pore, andthe functional material is present at least in the enlarged pore portion.4. The functional structure according to claim 3 , wherein the enlarged pore portion connects a plurality of pores constituting any one of the one-dimensional pore claim 3 , the two-dimensional pore claim 3 , and ...

Подробнее
19-02-2015 дата публикации

CATALYST FOR SELECTIVE OXIDATION OF SULPHUR COMPOUNDS

Номер: US20150050204A1
Принадлежит: REPSOL, S.A.

The present invention is related to a catalyst supported for the selective oxidation of sulphur compounds of the tail gas from the Claus process or streams with an equivalent composition to elemental sulphur or sulphur dioxide (SO). It is also the object of the present invention, a process for the preparation of a catalyst of this type, as well as the process of selective oxidation of sulphur compounds to elemental sulphur using the catalyst of the invention, as well as the process of catalytic incineration of the tail gas from the Claus process using the catalyst of the present invention. 2. Catalyst according to claim 1 , where the support material comprises an aluminium-silicon mixed oxide.3. Catalyst according to claim 2 , where the aluminium-silicon mixed oxide is a natural zeolite.4. Catalyst according to claim 3 , where the zeolite is clinoptilolite.5. Catalyst according to claim 1 , where the support material comprises an aluminium oxide.6. Catalyst according to claim 5 , where the alumina is theta alumina.7. Catalyst according to claim 1 , where the cobalt content in the catalyst is comprised from 0.05 to 5% expressed by weight of cobalt with respect to the total of the weight of the catalyst.8. Catalyst according to claim 1 , where the catalytically active material is a mixture of CoO and CoOin a ratio by weight of between 10:1 and 1:10.9. Process for the preparation of the catalyst defined in claim 1 , comprising the impregnation of a solution of a cobalt salt on the surface of a support material comprising an aluminium oxide claim 1 , a silicon oxide claim 1 , an aluminium-silicon mixed oxide or mixtures thereof claim 1 , followed by the drying and calcination of the catalyst.10. Process for the selective oxidation of compounds that contain sulphur claim 1 , comprising contacting a gas stream containing the sulphur compounds with a gas stream containing oxygen in the presence of a catalyst defined in ; and a gaseous effluent with a reduced content of HS ...

Подробнее
19-02-2015 дата публикации

METHOD FOR PRODUCING HYDROISOMERIZATION CATALYST AND METHOD FOR PRODUCING LUBRICANT BASE OIL

Номер: US20150051432A1
Принадлежит: JX NIPPON OIL & ENERGY CORPORATION

A method for producing a hydroisomerization catalyst according to the present invention includes: a first step of preparing a catalyst to be treated, which contains a support having a one-dimensional porous structure including a 10-membered ring and at least one metal selected from the group consisting of: group 8 to 10 metals of the periodic table, Mo, and W supported on the hydroisomerization catalyst; and a second step of producing a hydroisomerization catalyst having a carbon content of 0.4 to 2.5% by mass by subjecting the catalyst to be treated to a coking treatment by means of a carbon-containing compound. 1. A method for producing a hydroisomerization catalyst comprising:a first step of preparing a catalyst to be treated, which contains a support having a one-dimensional porous structure including a 10-membered ring and at least one metal selected from the group consisting of: group 8 to 10 metals of the periodic table, Mo, and W supported on the hydroisomerization catalyst; anda second step of producing a hydroisomerization catalyst having a carbon content of 0.4 to 2.5% by mass by subjecting the catalyst to be treated to a coking treatment by means of a carbon-containing compound.2. The method for producing a hydroisomerization catalyst according to claim 1 ,wherein in the second step, a hydroisomerization catalyst is produced, for which a volume of micropores per unit mass of the catalyst is 0.02 to 0.11 cc/g and a volume of micropores per unit mass of the zeolite contained in the catalyst is 0.04 to 0.12 cc/g.3. The method for producing a hydroisomerization catalyst according to claim 1 ,wherein the zeolite is at least one selected from the group consisting of: a ZSM-22 zeolite; a ZSM-23 zeolite; an SSZ-32 zeolite; and a ZSM-48 zeolite.4. A hydroisomerization catalyst produced by the method for producing a hydroisomerization catalyst according to .5. A method for producing lubricant base oil claim 1 ,{'claim-ref': {'@idref': 'CLM-00004', 'claim 4'}, ' ...

Подробнее
14-02-2019 дата публикации

METHOD FOR PREPARING MOLECULAR SIEVE-MULTIELEMENT OXIDE COMPOSITE INTEGRALLY EXTRUDED DENITRATION CATALYST

Номер: US20190046962A1
Принадлежит: VALIANT CO., LTD.

Disclosed is a preparation method for a molecular sieve-multiple oxide composite integral extrusion type denitration catalyst, belonging to the technical fields of atmosphere pollution control and environment-friendly catalytic materials. The preparation method comprises: constructing an organic structure coating on the surface of a metal ion-exchanged molecular sieves and synchronously adding multiple oxide components, thus obtaining an ion-exchanged molecular sieve-multiple oxide composite denitration catalyst active component; and then mixing, kneading into paste, staling, carrying out integral extrusion forming, drying, and calcining, thus obtaining the integral extrusion type denitration catalyst. The molecular sieve-multiple oxide composite integral extraction type denitration catalyst has a denitration efficiency more than 80% at the temperature ranging from 250° C. to 420° C. in the presence of 10% steam and 500 ppm sulfuric dioxide. According to the present invention, the application field of metal-loaded molecular sieve denitration catalysts is widened, and thus the metal-loaded molecular sieve denitration catalysts can be widely applied to the flue gas denitration of stationary sources. 1. A method for preparing a molecular sieve-multiple oxide composite integral extrusion type denitration catalyst , comprising the following steps:(1) mixing a metal salt solution of one or two of manganese, iron, cobalt, nickel, copper, or cerium with molecular sieves; and after an ion exchange reaction, adding a surfactant and simultaneously carrying out shear emulsification and dispersion treatment to obtain an ion-exchanged molecular sieve slurry;(2) preparing an acidic precursor solution from a mixture of a metal salt of one or two of manganese, iron, cobalt, nickel, copper, or cerium with one or more of an aluminum source, a titanium source, or a zirconium source; preparing an alkaline precursor solution from an alkaline silicon source; and mixing the acidic ...

Подробнее
28-02-2019 дата публикации

Low-Temperature Oxidation Catalyst With Particularly Marked Hydrophobic Properties For The Oxidation Of Organic Pollutants

Номер: US20190060832A1
Принадлежит: Clariant Produkte (Deutschland) GmbH

The present invention relates to a catalyst comprising a macroporous noble metal-containing zeolite material and a porous SiO-containing binder, wherein the catalyst has a proportion of micropores of more than 70%, based on the total pore volume of the catalyst. The invention is additionally directed to a process for preparing the catalyst and to the use of the catalyst as an oxidation catalyst. 19.-. (canceled)10. Method of producing a catalyst according to , comprising the following steps:a) introducing a noble metal precursor compound into a microporous zeolite material;b) calcining the zeolite material loaded with the noble metal precursor compound;{'sub': '2', 'c) mixing the zeolite material loaded with the noble metal compound with a porous SiO-containing binder and a solvent;'}d) drying and calcining the mixture comprising the zeolite material loaded with the noble metal compound and the binder.11. Method according to claim 10 , wherein the mixture obtained in step c) is applied to a support.12. (canceled) The present invention relates to a catalyst comprising a microporous noble metal-containing zeolite material and a porous SiO-containing binder, wherein the catalyst has a proportion of micropores of more than 70%, relative to the total pore volume of the catalyst. The invention is additionally directed to a method of producing the catalyst as well as to the use of the catalyst as oxidation catalyst.Purifying exhaust gases by means of catalysts has been known for some time. For example, the exhaust gases from combustion engines are purified with so-called three-way catalysts (TWC). The nitrogen oxides are reduced with reductive hydrocarbons (HC) and carbon monoxide (CO).Likewise, the exhaust gases from diesel engines are post-treated with catalysts. Here, carbon monoxide, unburnt hydrocarbons, nitrogen oxides and soot particles, for example, are removed from the exhaust gas. Unburnt hydrocarbons which are to be treated catalytically include paraffins, ...

Подробнее
27-02-2020 дата публикации

HIGH-CAPACITY, LOW-TEMPERATURE, PASSIVE NOx AND CD ADSORBERS AND METHODS FOR MAKING SAME

Номер: US20200061595A1
Принадлежит:

Disclosed are passive NOadsorbers and methods for synthesizing the same. Small-pore zeolitic materials with practical loadings of transition metals atomically dispersed in the micropores are described herein. Also demonstrated are simple and scalable synthesis routes to high loadings of atomically dispersed transition metals in the micropores of a small-pore zeolite. 1. A passive adsorber for pre-selected gasses , the passive adsorber comprising: a zeolite having a loading greater than 0.3 wt % of a dispersed transition metal.2. The passive adsorber of wherein the preselected gas is selected from a group consisting of NOx and CO.3. The passive adsorber of claim 1 , wherein the zeolite comprises SSZ-13.4. The passive adsorber of claim 1 , wherein the loading is greater than or equal to 0.5 wt %.5. The passive adsorber of claim 1 , wherein the loading is greater than or equal to 1 wt %.6. The passive adsorber of claim 1 , wherein the transition metal comprises Pt.7. The passive adsorber of claim 1 , wherein the transition metal comprises Pd.8. The passive adsorber of claim 7 , wherein the loading of the dispersed transition metal is atomically dispersed in pores of the zeolite.9. A method for forming a passive adsorber claim 7 , the method comprising the steps of:{'sub': 4', '4, 'exposing a NH-form of zeolite to a transition metal precursor comprising a counter ion whereby ions are exchanged between the zeolite and the transition metal precursor, to yield a NH-counter ion product; and'}{'sub': '4', 'decomposing the NH-counter ion product into a gaseous product.'}10. The method of claim 9 , wherein the zeolite comprises SSZ-13.11. The method of claim 9 , wherein the transition metal precursor comprises Pt.12. The method of claim 9 , wherein the transition metal precursor comprises Pd.13. The method of claim 9 , wherein the counter ion of the transition metal precursor comprises NO3.14. The method of claim 9 , wherein the NH-counter ion product decomposes at a ...

Подробнее
27-02-2020 дата публикации

METHOD FOR PREPARING LOW-GRADE UNSATURATED FATTY ACID ESTER

Номер: US20200062686A1

Provided is a method for preparing a lower unsaturated fatty acid ester, which comprises carrying out an aldol condensation reaction between dimethoxymethane (DMM) and a lower acid or ester with a molecular formula of R—CH—COO—Ron an acidic molecular sieve catalyst in an inert atmosphere to obtain a lower unsaturated fatty acid or ester(CH═C(R)—COO—R), wherein Rand Rare groups each independently selected from the group consisting of H- and C-Csaturated alkyl group. 1. A method for preparing a lower unsaturated fatty acid or ester , comprising carrying out an aldol condensation reaction between dimethoxymethane and an acid or ester with a molecular formula of R—CHCOORin a reactor loaded with an acidic molecular sieve catalyst to obtain the corresponding lower unsaturated fatty acid or ester , wherein Rand Rare each independently selected from H— , CH— , CHCH— , CH(CH)— and CH(CH)—.2. The method according to claim 1 , wherein the lower unsaturated fatty acid or ester is further hydrogenated to produce the corresponding saturated alcohols.3. The method according to claim 1 , wherein Rand Rare each selected from H— and CH—.4. The method according to claim 1 , wherein the acidic molecular sieve catalyst comprises any one selected from a silica-alumina molecular sieve and an aluminum phosphate molecular sieve or a combination thereof.5. The method according to claim 1 , wherein the topology of the acidic molecular sieve catalyst comprises any one selected from RHO claim 1 , CHA claim 1 , FER claim 1 , MFI claim 1 , MOR claim 1 , FAU and βeta or a combination thereof.6. The method according to claim 5 , wherein the acidic molecular sieve catalyst comprises any one selected from a SAPO-34 molecular sieve claim 5 , a DNL-6 molecular sieve claim 5 , a ZSM-35 molecular sieve claim 5 , a ZSM-5 molecular sieve claim 5 , a MOR molecular sieve claim 5 , a Y molecular sieve claim 5 , a βeta molecular sieve and a MCM-22 molecular sieve or a combination thereof.7. The method ...

Подробнее
07-03-2019 дата публикации

PRODUCTION OF AMINES UTILIZING ZEOLITE CATALYSTS

Номер: US20190071389A1
Принадлежит: Rhodia Operations

The present invention concerns a process for forming a primary or a secondary amine via amination reaction comprising: reacting an alcohol with an amine in the presence of a zeolite comprising a transition metal chosen in the group consisting of Group 8 to 12 elements of the Periodic Table and any combination thereof. 1. A process for forming a primary or a secondary amine , comprising reacting:A first reactant having 5-30 carbon atoms and one or two primary hydroxyl functionalities, with{'sub': '3', 'A second reactant being NHor a reactant having primary amine functionality,'}in the presence of at least one zeolite comprising a transition metal selected from the group consisting of Group 8 to 12 elements of the Periodic Table and any combination thereof.2. The process according to claim 1 , wherein the first reactant is a compound of formula (I):{'br': None, 'sup': '1', 'sub': 'x', 'R(—OH)\u2003\u2003(I)'} x is 1 or 2', {'sup': '1', 'sub': 5', '30, 'Ris a straight, branched or cyclic C-Chydrocarbon group.'}], 'Wherein3. The process according to claim 2 , wherein Ris selected from the group consisting of: C-Cstraight aliphatic hydrocarbon group claim 2 , benzyl claim 2 , furfuryl and tetrahydrofurfuryl.4. The process according to claim 3 , wherein the first reactant is selected from the group consisting of: 1-pentanol claim 3 , 1-hexanol claim 3 , 1-heptanol claim 3 , 1-octanol claim 3 , 1-nonanol claim 3 , 1-decanol claim 3 , furfuryl alcohol claim 3 , 2 claim 3 ,5 furandimethanol claim 3 , 2 claim 3 ,5-tetrahydrofuranedimethanol claim 3 , benzyl alcohol claim 3 , 1 claim 3 ,6-hexandiol and 1 claim 3 ,7-heptandiol.5. The process according to claim 1 , wherein the second reactant is a compound of formula (II):{'br': None, 'sup': '2', 'sub': '2', 'R—NH\u2003\u2003(II)'} {'sup': '2', 'Ris H or a straight, branched or cyclic hydrocarbon group.'}, 'Wherein6. The process according to claim 5 , wherein Ris H or C-Calkyl.7. The process according to claim 1 , wherein the ...

Подробнее
18-03-2021 дата публикации

Novel catalysts and process for liquid hydrocarbon fuel production

Номер: US20210077987A1
Автор: Liu Shetian, White Mark G.
Принадлежит:

The present invention provides a novel process and system in which a mixture of carbon monoxide and hydrogen synthesis gas, or syngas, is converted into hydrocarbon mixtures composed of high quality gasoline components, aromatic compounds, and lower molecular weight gaseous olefins in one reactor or step. The invention utilizes a novel molybdenum-zeolite catalyst in high pressure hydrogen for conversion, as well as a novel rhenium-zeolite catalyst in place of the molybdenum-zeolite catalyst, and provides for use of the novel catalysts in the process and system of the invention. 1. A process for the production of hydrocarbon fuel products having an aromatic content of about 90% or greater from synthesis gas comprising:providing a synthesis gas; andproviding an alcohol-forming catalyst;providing a single reaction system and steam reformer in which the chemical reactions occur over the alcohol-forming catalyst found in the same matrix as a gasoline-forming catalyst, with the synthesis gas contacted in a Fischer-Tropsch reaction with the alcohol-forming catalyst in high pressure hydrogen;wherein the alcohol-forming catalyst is a zeolite-encaged, molybdenum-based catalyst active for deoxy-aromatization of alcohols and synthesis gas to mixed alcohols, isomerization of alkanes, and aromatization; andwherein the alcohol-forming catalyst produces high quality alcohols from the synthesis gas.2. The process of claim 1 ,wherein the catalyst is a cluster comprising a molybdenum oxide represented by MoCOencaged in a zeolite and wherein the cluster comprises the active phase.3. The process of claim 2 , wherein the cluster comprises a molybdenum sulfide.4. The process of claim 3 , wherein the cluster further comprises at least one metal modifier selected from the group consisting of the elements of Groups 1A and 2A of the Periodic Table and mixtures of the aforementioned elements.5. The process of claim 3 , wherein the zeolite comprises a support claim 3 , and comprises one or more ...

Подробнее
23-03-2017 дата публикации

Method and Catalyst System for Improving Benzene Purity in a Xylenes Isomerization Process

Номер: US20170081259A1
Принадлежит:

A process and catalyst system is disclosed for producing para-xylene from a Chydrocarbon mixture comprising ethylbenzene and at least one xylene isomer other than para-xylene. The process modifies the conventional process by operating with a higher weight hourly space velocity, lower pressure and lower hydrogen partial pressure, which allows production of on-specification benzene product without penalty with respect to ethylbenzene conversion, para-xylene approach to equilibrium or xylene losses. The catalyst system comprises a first catalyst bed comprising a first zeolite having a constraint index from 1 to 12 and an average crystal size from 0.1 to 1 micron and a platinum hydrogenation component, and a second catalyst bed comprising a second zeolite having a constraint index ranging from 1 to 12 and an average crystal size of less than 0.1 micron and a rhenium hydrogenation component. 1. A catalyst system for producing para-xylene from a Chydrocarbon mixture comprising ethylbenzene and at least one xylene isomer other than para-xylene , the catalyst system comprising a first catalyst bed (1) and a second catalyst bed (2) , wherein:the first catalyst bed (1) comprises a first catalyst comprising a first zeolite and a hydrogenation component comprising platinum, wherein the first zeolite has a constraint index ranging from 1 to 12 and an average crystal size of at least 1 micron; andthe second catalyst bed (2) comprises a second catalyst comprising a second zeolite and a hydrogenation component comprising rhenium, wherein the second zeolite has a constraint to index ranging from 1 to 12 and an average crystal size of about 0.02-0.05 microns.2. The catalyst system of claim 1 , wherein the hydrogenation component of the first catalyst consists essentially of platinum.3. The catalyst system of claim 1 , wherein the hydrogenation component of the second catalyst consists essentially of rhenium.4. The catalyst system of claim 1 , wherein the first zeolite comprises ZSM-5 ...

Подробнее
12-03-2020 дата публикации

CATALYST COMPOSITION

Номер: US20200078777A1
Принадлежит:

A catalyst composition comprising (a) carrier comprising (i) 5 to 95 wt % mordenite type zeolite having a mean crystallite length parallel to the direction of the 12-ring channels of 60 nm or less and a mesopore volume of at least 0.10 cc/gram, (ii) 5 to 95 wt % ZSM-5 type zeolite; and (iii) 10 to 60 wt % inorganic binder; and (b) 0.001 to 10 wt % of one or more catalytically active metals, wherein the inorganic binder comprises titania, its preparation and its use in alkylaromatic conversion. 1. A catalyst composition comprising(a) a carrier comprising (i) mordenite type zeolite having a mean crystallite length parallel to the direction of the 12-ring channels of 60 nm or less and a mesopore volume of at least 0.10 cc/gram in an amount in the range of from 5 to 95 wt %, based on total weight of carrier, (ii) ZSM-5 type zeolite in an amount of from 5 to 95 wt %, based on total weight of carrier; and (iii) an inorganic binder in an amount in the range of from 10 to 60 wt %, based on total weight of carrier; and(b) of from 0.001 to 10 wt % of one or more catalytically active metals, wherein the inorganic binder comprises titania.2. The catalyst composition according to claim 1 , in which the carrier comprises mordenite type zeolite in an amount in the range of from 20 to 90 wt % claim 1 , based on total weight of carrier.3. The catalyst composition according to claim 1 , in which the carrier comprises ZSM-5 type zeolite in an amount of from 10 to 70 wt % claim 1 , based on total weight of carrier.4. The catalyst composition according to claim 1 , wherein the ZSM-5 type zeolite has a silica to alumina molar ratio in the range of from 15 to 40.5. The catalyst composition according to claim 1 , wherein the ZSM-5 type zeolite has a number average crystal size in the range of from 25 to 200 nm claim 1 , as determined by X-ray diffraction.6. The catalyst composition according to claim 1 , wherein the ZSM-5 type zeolite has a number average.7. A crystal size in the range of ...

Подробнее
19-03-2020 дата публикации

PROCESS FOR THE CONVERSION OF ETHYLENE OXIDE TO MONOETHANOLAMINE AND ETHYLENEDIAMINE EMPLOYING A ZEOLITE

Номер: US20200087246A1
Принадлежит:

The present invention relates to a process for the conversion of ethylene oxide to 2-aminoethanol and/or ethane-1,2-diamme and/or linear polyethylenimines of the formula HN—(CHCHNH)—CHCH—NHwherein n≥1 comprising (i) providing a catalyst comprising a zeolitic material comprising YOand XO, wherein Y is a tetravalent element and X is a trivalent element; (ii) providing a gas stream comprising ethylene oxide and ammonia; (iii) contacting the catalyst provided in (i) with the gas stream provided in (ii) for converting ethylene oxide to 2-aminoethanol and/or ethane-1,2-diamine and/or linear polyethylenimines. 114-. (canceled)15. A process for the conversion of ethylene oxide to 2-aminoethanol and ethane-1 ,2-diamine comprising{'sub': 2', '2', '3, '(i) providing a catalyst comprising a zeolitic material comprising YOand XO, wherein Y is a tetravalent element and X is a trivalent element;'}(ii) providing a gas stream comprising ethylene oxide and ammonia;(iii) contacting the catalyst provided in (i) with the gas stream provided in (ii) for converting ethylene oxide to 2-aminoethanol and ethane-1,2-diamine, wherein in (i) the zeolitic material has the MOR framework structure.16. The process of claim 15 , wherein the gas stream provided in (ii) and contacted with the catalyst in (iii) contains ethylene oxide in an amount in the range of from 0.05 to 10 vol.-%.17. The process of claim 15 , wherein the gas stream provided in (ii) and contacted with the catalyst in (iii) contains ammonia in an amount in the range of from 5 to 90 vol.-%.18. The process of claim 15 , wherein the gas stream provided in (ii) and contacted with the catalyst in (iii) further contains hydrogen in an amount in the range of from 0.1 to 70 vol.-%.19. The process of claim 15 , wherein the gas stream provided in (ii) and contacted with the catalyst in (iii) contains 1 vol.-% or less of hydrogen.20. The process of claim 15 , wherein the gas stream provided in (ii) is heated to a temperature in the range of ...

Подробнее
07-04-2016 дата публикации

Production of Aromatics from Methane

Номер: US20160096168A1
Принадлежит:

A catalyst for the conversion of methane to higher hydrocarbons including aromatic hydrocarbons comprises molybdenum or a compound thereof dispersed on an aluminosilicate zeolite, wherein the amount of aluminum present as aluminum molybdate in the catalyst is less than 2700 ppm by weight. 1. A process for converting methane to higher hydrocarbons including aromatic hydrocarbons , the process comprising contacting a feed comprising methane with a regenerated catalyst in a reaction zone under conditions effective to convert said methane to aromatic hydrocarbons ,wherein said regenerated catalyst comprises molybdenum or a compound thereof dispersed on an aluminosilicate zeolite, wherein said zeolite is selected from a group consisting of ZSM-5, ZSM-11, ZSM-12, ZSM-22, ZSM-23, ZSM-35, ZSM-57 and MCM-22, wherein the amount of aluminum present as aluminum molybdate in said catalyst is less than 2700 ppm by weight; said catalyst characterized by the formation of aluminium molybdate during dehydrocyclization of methane to benzene, wherein the catalyst has been regenerated and prior to regeneration aluminum molybdate was present in the catalyst, andwherein said catalyst's exposure during dehydrocyclization and regeneration has been limited to not more than 100 wt ppm molecular oxygen and/or ozone at a temperature not in excess of 650° C. for a cumulative time not greater than 10 hours.2. The process of claim 1 , wherein the regenerated catalyst claim 1 , as supplied to the reaction zone claim 1 , contains less than 270 ppm by weight aluminum present as aluminum molybdate.3. The process of claim 1 , wherein the process is operated so as to maintain the amount of aluminum present as aluminum molybdate in said catalyst at less than 2700 ppm by weight.4. The process of claim 1 , wherein the amount of molybdenum or said compound thereof in the catalyst is between about 0.1 and about 20% by weight of the catalyst claim 1 , based on elemental molybdenum claim 1 , and wherein the ...

Подробнее
26-06-2014 дата публикации

ISOMERISATION CATALYST PREPARATION PROCESS

Номер: US20140179969A1
Принадлежит:

A process for preparing an alkylaromatics isomerisation catalyst comprising at least 0.01% wt of platinum on a carrier comprising of from 1 to 9 wt % of ZSM-12 and inorganic binder, which process comprises treating the carrier with an impregnation solution comprising a cationic platinum compound and having a pH of more than 9, and subsequently drying and calcining the impregnated carrier at a temperature of from 200 to 420° C.; and a process for the isomerisation of alkylaromatics with the help of catalyst thus obtained. 1. A process for preparing an alkylaromatics isomerisation catalyst , the process comprising at least 0.01% wt of platinum on a carrier comprising of from 1 to 9 wt % of ZSM-12 and inorganic binder , which process comprises treating the carrier with an impregnation solution comprising a cationic platinum compound and having a pH of more than 9 , and subsequently drying and calcining the impregnated carrier at a temperature of from 200 to 420° C.2. A process as claimed in in which the impregnated carrier is calcined at a temperature in the range of from 250 to 400 ° C.3. A process as claimed in in which the impregnation solution further comprises ammonium hydroxide.4. A process as claimed in in which the impregnation solution has a pH of at least 11.5. A process as claimed in in which the ZSM-12 zeolite has a silica to alumina molar ratio (SAR) in the range of from 60 to 200.6. A process as claimed in in which the catalyst comprises at least 50 wt % of an acidic inorganic binder.7. A process as claimed in in which the cationic platinum compound is a platinum hydroxide compound.8. A process for the isomerisation of alkylaromatics which process comprises contacting a hydrocarbon feed comprising alkylaromatics with a catalyst obtained in a process as claimed in . This invention relates to a zeolite-based catalyst for the isomerisation of alkylaromatics, more specifically ethylbenzene.Following fractionation or distillation of crude petroleum oil, a ...

Подробнее
03-07-2014 дата публикации

Low-temperature oxidation catalyst with particularly marked hydrophobic properties for the oxidation of organic pullutants

Номер: US20140186251A1
Принадлежит: Clariant Produkte Deutschland GmbH

The present invention relates to a catalyst comprising a macroporous noble metal-containing zeolite material and a porous SiO 2 -containing binder, wherein the catalyst has a proportion of micropores of more than 70%, based on the total pore volume of the catalyst. The invention is additionally directed to a process for preparing the catalyst and to the use of the catalyst as an oxidation catalyst.

Подробнее
29-04-2021 дата публикации

Catalyst for removal of sulphur oxides from flue gases of power plants

Номер: US20210121858A1

The present invention relates to the catalytic processes for rendering harmless the flue gases of the power stations or more precisely to the catalysts for sulfur oxides reduction to elemental sulfur. The novel catalyst presents the binary polycations of copper and zinc or copper and manganese incorporated into the low silica faujasite X (LSX) having transition metals ratio Cu:Zn or Cu:Mn in the range of 2:1 to 4:1.

Подробнее
03-06-2021 дата публикации

LIGHT HYDROCARBON PARTIAL OXIDATION CATALYST AND CARBON MONOXIDE PRODUCTION METHOD USING SAME

Номер: US20210163300A1
Принадлежит:

The present disclosure relates to a partial oxidation catalyst that causes a light hydrocarbon partial oxidation reaction to proceed readily with high activity and high selectivity and a high-yield carbon monoxide production method using the same. The present disclosure further relates to a light hydrocarbon partial oxidation catalyst containing a zeolite supporting cobalt and rhodium. 1. A partial oxidation catalyst for a light hydrocarbon , comprising cobalt and rhodium-supported zeolite.2. The partial oxidation catalyst according to claim 1 , wherein an amount of the rhodium which is supported is 0.001% by weight or more and 0.01% by weight or less with respect to 100% by weight of the zeolite; and', 'a ratio of the amount of the cobalt to the amount of the rhodium is 1 or more and 6000 or less., 'an amount of the cobalt which is supported is 0.01% by weight or more and 6.0% by weight or less with respect to 100% by weight of the zeolite;'}3. The partial oxidation catalyst according to claim 1 , wherein the zeolite is one or a mixture of two or more selected from the group consisting of mordenite zeolite claim 1 , WI zeolite claim 1 , and beta zeolite.4. The partial oxidation catalyst according to claim 1 , wherein the light hydrocarbon is methane or a mixture mainly comprising methane.5. A method for producing carbon monoxide claim 1 , comprising bringing a light hydrocarbon and oxygen into contact with each other in the presence of the partial oxidation catalyst according to to generate carbon monoxide and hydrogen by partial oxidation.6. The method for producing carbon monoxide according to claim 5 , wherein the light hydrocarbon and the oxygen are brought into contact with each other in a temperature range of 300° C. or more and 1000° C. or less. The present invention relates to a partial oxidation catalyst for a light hydrocarbon and, more specifically, relates to a partial oxidation catalyst comprising cobalt and rhodium-supported zeolite, which enables ...

Подробнее
17-05-2018 дата публикации

Catalyst Compositions and Their Use in Transalkylation of Heavy Aromatics to Xylenes

Номер: US20180134637A1
Принадлежит:

Disclosed are catalyst compositions and their use in a process for the conversion of a feedstock containing C+ aromatic hydrocarbons to produce light aromatic products, comprising benzene, toluene and xylene. The catalyst composition comprises a zeolite which comprises a MOR framework structure and a MFI and/or MEL framework structure, (b) at least one first metal of Group 10 of the IUPAC Periodic Table, and (c) optionally at least one second metal of Group 11 to 15 of the IUPAC Periodic Table. In one or more embodiments, the MOR framework structure comprises mordenite, preferably a mordenite zeolite having small particle size. The MFI framework structure preferably comprises ZSM-5, and the MEL framework structure preferably comprises ZSM-11. 1. A process for conversion of a feedstock comprising C aromatic hydrocarbons to lighter aromatic products , the process comprising the steps of contacting said feedstock and optionally hydrogen in the presence of a catalyst under suitable conversion conditions to produce said lighter aromatic products comprising benzene , toluene and xylene , wherein said catalyst composition comprises:(a) a zeolite comprising a MOR framework structure and a minor phase of MFI and/or MEL framework structure,(b) at least one first metal of Group 10 of the IUPAC Periodic Table, and(c) optionally at least one second metal of Group 11 to 15 of the IUPAC Periodic Table.2. The process of claim 1 , wherein said MOR framework structure comprises an x-ray diffraction pattern having a maximum peak at interplanar d-spacing of 9.10±0.1 Angstroms (9.72±0.30 degrees two-theta) and secondary peaks at interplanar d-spacings of 4.0±0.05 Angstroms (22.3±0.30 degrees two-theta) and 3.47±0.4 Angstroms (25.68±0.30 degrees two-theta).3. The process of claim 2 , wherein said MFI and/or MEL framework structure comprises an x-ray diffraction pattern having a peak at interplanar d-spacing of 3.85±0.07 Angstrom (23.08±0.30 degrees two-theta) and/or a peak at interplanar ...

Подробнее
15-09-2022 дата публикации

CARBONYLATION-DEHYDRATION DUAL-FUNCTIONAL CATALYST PRECURSOR, PREPARATION METHOD THEEOF, CARBONYLATION-DEHYDRATION DUAL-FUNCTIONAL CATALYST AND USE THEREOF

Номер: US20220289661A1
Принадлежит:

A carbonylation-dehydration dual-functional catalyst precursor, a preparation method thereof, a carbonylation-dehydration dual-functional catalyst and use thereof are provided. The carbonylation-dehydration dual-functional catalyst precursor includes a modified silica-aluminum molecular sieve having an 8-member ring channel structure; a modified metal oxie loaded on the modified silica-aluminum molecular sieve having an 8-member ring channel structure by coupling, the coupling being performed using a silane coupling agent, wherein a modified component in the modified silica-aluminum molecular sieve having an 8-member ring channel structure includes at least one selected from the group consisting of copper oxide, zing oxide and iron oxide, and has a loading amount of 0.5-5 wt %, based on a metal mass of the modified component; and the modified metal oxie is prepared by modifying a composite metal oxide with an acid solution or an alkali solution, wherein the composite metal oxide is prepared based on a co-precipitation-calcination method. 1. A carbonylation-dehydration dual-functional catalyst precursor , comprisinga modified silica-aluminum molecular sieve having an 8-member ring channel structure; anda modified metal oxide loaded on the modified silica-aluminum molecular sieve having an 8-member ring channel structure by coupling, the coupling being performed using a silane coupling agent, whereina modified component in the modified silica-aluminum molecular sieve having an 8-member ring channel structure comprises at least one selected from the group consisting of copper oxide, zinc oxide and iron oxide, and has a loading amount of 0.5-5 wt %, based on a metal mass of the modified component; and{'sub': a', '1-a', 'y', 'b', '1-b', 'y', 'm', 'n', '1-m-n', 'y, 'the modified metal oxide is prepared by modifying a composite metal oxide with an acid solution or an alkali solution, wherein the composite metal oxide is prepared based on a co-precipitation-calcination ...

Подробнее
17-06-2021 дата публикации

Catalyst for Converting Alkylaromatic Hydrocarbon and Preparation Method Thereof

Номер: US20210178372A1
Принадлежит:

Disclosed are a bifunctional catalyst and a preparation method therefor, the bifunctional catalyst being suitable to produce high-value aromatic hydrocarbons by subjecting alkylaromatic hydrocarbons to a disproportionation/transalkylation/dealkylation reaction while suppressing aromatic loss or subjecting C8 aromatic hydrocarbons to an isomerization reaction while suppressing xylene loss. 1. A method for preparing a catalyst for converting aromatic hydrocarbons , the method comprising:a) supporting a precursor of a first metal having hydrogenation activity on a refractory inorganic oxide binder to prepare a first metal precursor-supported binder;b) combining a first zeolite and/or a second zeolite with the first metal precursor-supported binder to prepare a shaped body; andc) calcining the shaped body to form a catalyst, in which the first metal is supported on a mixed support containing the first zeolite and/or the second zeolite and the binder,wherein the first zeolite has a silica-alumina ratio (SAR) of 5 to 300 and a 10-membered ring pore structure, and the second zeolite has a silica-alumina ratio (SAR) of 5 to 300 and a 12-membered ring pore structure with a pore diameter of 6 to 9 Å, andwherein the first metal is selectively supported on the refractory inorganic oxide binder in the mixed support, the amount of the first metal supported being in the range of 0.01 to 5 wt % on the basis of the weight of the mixed support.2. The method of claim 1 , wherein the refractory inorganic oxide is at least one selected from the group consisting of alumina claim 1 , silica claim 1 , aluminum phosphate claim 1 , titania claim 1 , zirconia claim 1 , bentonite claim 1 , kaolin claim 1 , clinoptilolite claim 1 , and montmorillonite.3. The method of claim 1 , wherein the first zeolite is at least one selected from the group consisting of ZSM-5 claim 1 , ZSM-11 claim 1 , ZSM-23 claim 1 , ZSM-48 claim 1 , ZSM-57 claim 1 , EU-2 claim 1 , TNU-9 claim 1 , and MCM-22.4. The method ...

Подробнее
17-06-2021 дата публикации

Process for producing lpg and btx from mixed hydrocarbons feed

Номер: US20210179951A1
Принадлежит: SABIC Global Technologies BV

The present invention relates to a process for producing LPG and BTX from a mixed feedstream comprising C5-C12 hydrocarbons by contacting said feedstream in the presence of hydrogen with a first hydrocracking catalyst and contacting the thus obtained first hydrocracked product in the presence of hydrogen with a second hydrocracking catalyst to produce a second hydrocracked product stream comprising LPG and BTX.

Подробнее
21-05-2020 дата публикации

ALDEHYDE DECOMPOSITION CATALYST, AND EXHAUST GAS TREATMENT APPARATUS AND EXHAUST GAS TREATMENT METHOD

Номер: US20200156003A1
Принадлежит:

One object is to provide a useful aldehyde decomposition catalyst, and an exhaust gas treatment apparatus and an exhaust gas treatment method using the aldehyde decomposition catalyst that achieve low cost and sufficient aldehyde decomposition performance with a small amount of the catalyst. An aldehyde decomposition catalyst of the present invention is made of a zeolite in a cation form NHhaving a structure of CHA or MOR and carrying Cu. 1. A method for decomposing an aldehyde contained in a combustion exhaust gas , the method comprising a step of contacting the aldehyde with an aldehyde decomposition catalyst , characterized in that the aldehyde decomposition catalyst is made of a zeolite in a cation form NHhaving a structure of CHA or MOR and carrying Cu.2. An exhaust gas treating method in which a combustion exhaust gas is denitrated by contacting the combustion exhaust gas with a denitration catalyst claim 1 , wherein an alcohol is fed as a reducing agent for the denitration to the combustion exhaust gas claim 1 , and an aldehyde by-produced in the denitration is decomposed according to the method of .3. The exhaust gas treatment method according to claim 2 , in which the temperature range of the combustion exhaust gas is from 200 to 400° C.4. The method for decomposing an aldehyde contained in a combustion exhaust gas according to claim 1 , wherein the aldehyde contained in the combustion exhaust gas is formaldehyde.5. The exhaust gas treating method according to claim 2 , wherein the aldehyde contained in the combustion exhaust gas is formaldehyde.6. The exhaust gas treatment method according to claim 3 , wherein the aldehyde contained in the combustion exhaust gas is formaldehyde. The subject application is a Divisional Application of U.S. Ser. No. 15/526,626, filed May 12, 2017, which is the U.S. National Phase of PCT/JP2015/081556, filed Nov. 10, 2015, which in turn claims priority to Japanese Patent Application No. 2014-229692, filed Nov. 12, 2014. The ...

Подробнее
25-06-2015 дата публикации

METHODS AND APPARATUSES FOR ISOMERIZING HYDROCARBONS

Номер: US20150175506A1
Автор: Shakur Mohamed S.
Принадлежит: UOP LLC

Methods and apparatuses are provided for isomerizing a hydrocarbon stream. The method includes isomerizing a hydrocarbon stream in a reactor to produce an intermediate isomerized stream. The intermediate isomerized stream is fractionated to produce an off gas stream and a heavy isomerized stream, where the off gas stream includes an off gas recycle stream. The off gas recycle stream is dried in an off gas dryer to produce a hydrogen recycle stream, where the off gas drier includes an off gas dryer membrane separating the off gas recycle stream from an off gas purge stream. The off dryer membrane includes a perfluorosulfonated ionomer. The hydrogen recycle stream is then fed into the reactor. 1. A method of isomerizing hydrocarbons , the method comprising the steps of:isomerizing a hydrocarbon stream in a reactor to produce an intermediate isomerized stream;fractionating the intermediate isomerized stream to produce an off gas stream and a heavy isomerized stream, wherein the off gas stream comprises an off gas recycle stream;drying the off gas recycle stream in an off gas dryer to produce a hydrogen recycle stream, wherein the off gas dryer comprises an off gas dryer membrane separating the off gas recycle stream from an off gas purge stream, and wherein the off gas dryer membrane comprises a perfluorosulfonated ionomer; andfeeding the hydrogen recycle stream into the reactor.3. The method of wherein drying the off gas recycle stream further comprises drying the off gas recycle stream in the off gas dryer comprising the off gas dryer membrane claim 1 , wherein the off gas dryer membrane comprises a copolymer of tetrafluoroethylene and perfluoro-3 claim 1 ,6-dioxa-4-methyl-7-octene-sulfonic acid.4. The method of wherein drying the off gas recycle stream further comprises drying the off gas recycle stream in the off gas dryer comprising the off gas dryer membrane claim 3 , wherein the off gas dryer membrane comprises the copolymer of tetrafluoroethylene and perfluoro- ...

Подробнее
13-06-2019 дата публикации

NH3 ABATEMENT WITH GREATER SELECTIVITY TO N2

Номер: US20190176128A1
Принадлежит:

Catalysts having a first catalyst coating and a second catalyst coating, the first catalyst coating including a blend of 1) Pt on a support, and 2) a molecular sieve, and the second catalyst coating including an SCR catalyst. 1. A catalyst comprising a first catalyst coating and a second catalyst coating ,the first catalyst coating comprising a blend of 1) Pt on a support, and 2) a molecular sieve, andthe second catalyst coating comprising an SCR catalyst.2. The catalyst of claim 1 , wherein the SCR catalyst comprises a Cu-SCR catalyst comprising copper and a molecular sieve claim 1 , and/or an Fe-SCR catalyst comprising iron and a molecular sieve.3. The catalyst of claim 1 , wherein the support comprises silica claim 1 , titania claim 1 , and/or Me-doped alumina or titania where Me comprises a metal selected from W claim 1 , Mn claim 1 , Fe claim 1 , Bi claim 1 , Ba claim 1 , La claim 1 , Ce claim 1 , Zr claim 1 , or mixtures of two or more thereof.4. The catalyst of claim 1 , wherein the molecular sieve comprises FER claim 1 , BEA claim 1 , CHA claim 1 , AEI claim 1 , MOR claim 1 , MFI claim 1 , and mixtures and intergrowths thereof.5. The catalyst of claim 1 , wherein the Pt is present in an amount of about 1 g/ftto about 10 g/ftrelative to the weight of the first catalyst coating.6. The catalyst of claim 1 , wherein the molecular sieve is present in an amount of up to about 2 g/inrelative to the weight of the first catalyst coating.7. The catalyst of claim 1 , wherein the first and second catalyst coatings are configured such that exhaust gas contacts the second catalyst coating before contacting the first catalyst coating.8. The catalyst of claim 1 , wherein the second catalyst coating completely overlaps the first catalyst coating.9. The catalyst of claim 1 , wherein the second catalyst coating partially overlaps the first catalyst coating.10. The catalyst of claim 1 , wherein the first catalyst coating and the second catalyst coating do not overlap.11. The ...

Подробнее
11-06-2020 дата публикации

NANO-SIZED ZEOLITE SUPPORTED CATALYSTS AND METHODS FOR THEIR PRODUCTION

Номер: US20200179912A1
Принадлежит: Saudi Arabian Oil Company

According to one or more embodiments described, a zeolite supported catalyst may be synthesized by a process that includes combining a colloidal mixture with a metal oxide support material to form a support precursor material, processing the support precursor material to form a support material, and impregnating the support material with one or more metals to form the zeolite supported catalyst. The colloidal mixture may include nano-sized zeolite crystals, and the nano-sized zeolite crystals may have an average size of less than 100 nm. 2. The zeolite supported catalyst of claim 1 , where the zeolite supported catalyst has a pore volume of at least 0.45 mL/g3. The zeolite supported catalyst of claim 1 , where the zeolite supported catalyst has a pore size of at least 9.5 nm.4. The zeolite supported catalyst of claim 1 , where the metal catalyst material comprises one or more of WO claim 1 , MoO claim 1 , NiO claim 1 , and CoO.5. The zeolite supported catalyst of claim 1 , where the porous alumina comprises:a small pore size alumina having a pore volume of from 0.4 mL/g to 0.6 mL/g; anda large pore size alumina having a pore volume of from 0.8 mL/g to 1.2 mL/g.6. The zeolite supported catalyst of claim 5 , comprising:from 10 wt. % to 65 wt. % of the small pore size alumina; andfrom 15 wt. % to 25 wt. % of the large pore size alumina. This application is a divisional application of and claims priority to U.S. patent application Ser. No. 15/480,917, filed on Apr. 6, 2017, which claims priority to U.S. Provisional Application Ser. No. 62/320,938, filed Apr. 11, 2016, all of which are incorporated by reference.The present disclosure relates to catalysts for chemical conversion of petrochemical fuels. More specifically, the disclosure relates methods for preparing catalysts which may be utilized in hydroprocessing treatments.Hydrocracking is a versatile catalytic process that converts heavy oils to lighter products by aromatic saturation, cracking, and isomerization ...

Подробнее
30-07-2015 дата публикации

CATALYST COMPOSITION AND PROCESS FOR PRODUCING AROMATIC HYDROCARBON USING THE CATALYST COMPOSITION

Номер: US20150209768A1
Принадлежит:

It is an object of the present invention to provide a catalyst that is excellent in stability even at a high catalyst-regeneration temperature. It is another object of the present invention to provide a process for producing an aromatic hydrocarbon from a lower hydrocarbon by using the above catalyst. The catalyst composition comprises molybdenum, a second metal that is not molybdenum, and a crystalline metallosilicate, wherein the content of molybdenum is 1 to 20% by weight in terms of a molybdenum atom, and the content of the second metal is 2 to 20% by weight in terms of a metal atom. 1. A catalyst composition for producing an aromatic hydrocarbon by contacting at least one hydrocarbon with the catalyst composition , comprising molybdenum , a second metal that is not molybdenum , and a crystalline metallosilicate , wherein the content of molybdenum is 1 to 20% by weight in terms of a molybdenum atom and the content of the second metal is 2 to 20% by weight in terms of a metal atom.2. The catalyst composition according to claim 1 , wherein the second metal is at least one metal selected from the group consisting of Sc claim 1 , Y and lanthanoids (La claim 1 , Ce claim 1 , Pr claim 1 , Nd claim 1 , Pm claim 1 , Sm claim 1 , Gd claim 1 , Tb claim 1 , Dy claim 1 , Ho claim 1 , Er claim 1 , Tm claim 1 , Yb or Lu).3. The catalyst composition according to claim 1 , wherein a relative weight reduction ratio (C) defined by the following formula is 60% or less;{'br': None, 'i': C=', 'A/B;, '100'}wherein,A is a weight variation in terms of %, which is defined as a deviation in weight at a temperature of 900° C. based on a weight measured at a temperature of 650° C. wherein the measurement is conducted by heating the catalyst composition with a differential thermogravimetric analyzer at a temperature increase rate of 5° C. per minute from a room temperature to 900° C. in air atmosphere, wherein the weight of the catalyst composition is normalized such that the weight of the ...

Подробнее
04-08-2016 дата публикации

Catalyst Compositions and Use in Heavy Aromatics Conversion Processes

Номер: US20160220987A1
Принадлежит:

Disclosed is a catalyst composition and its use in a process for the conversion of a feedstock containing C+ aromatic hydrocarbons to produce light aromatic products, comprising benzene, toluene and xylene. The catalyst composition comprises a first zeolite having a constraint index of 3 to 12, a second zeolite comprising a mordenite zeolite synthesized from TEA or MTEA, at least one first metal of Group 10 of the IUPAC Periodic Table, and at least one second metal of Group 11 to 15 of the IUPAC Periodic Table, wherein said mordenite zeolite has a mesopore surface area of greater than 30 m/g and said mordenite zeolite comprises agglomerates composed of primary crystallites, wherein said primary crystallites have an average primary crystal size as measured by TEM of less than 80 nm and an aspect ratio of less than 2. 1. A catalyst composition for conversion of C aromatic hydrocarbons to lighter aromatic products , said catalyst composition comprising (i) a first zeolite having a constraint index of 3 to 12 , (ii) a second zeolite comprising a mordenite zeolite synthesized from TEA or MTEA , (iii) at least one first metal of Group 10 of the IUPAC Periodic Table , and (iv) at least one second metal of Group 11 to 15 of the IUPAC Periodic Table , wherein said mordenite zeolite has a mesopore surface area of greater than 30 m/g and said mordenite zeolite comprises agglomerates composed of primary crystallites , wherein said primary crystallites have an average primary crystal size as measured by TEM of less than 80 nm and an aspect ratio of less than 2.2. The catalyst composition of claim 1 , wherein said first zeolite having a constraint index of 3 to 12 is selected from the group consisting of ZSM-5 claim 1 , ZSM-11 claim 1 , ZSM-22 claim 1 , ZSM-23 claim 1 , ZSM-35 claim 1 , ZSM-48 claim 1 , ZSM-50 claim 1 , ZSM-57 claim 1 , ZSM-58 claim 1 , a MCM-22 family material and mixtures of two or more thereof.3. The catalyst composition of claim 2 , wherein said MCM-22 family ...

Подробнее
04-08-2016 дата публикации

Process for Preparing a Molecular Sieve

Номер: US20160221832A1
Принадлежит: ExxonMobil Chemical Patents Inc

The present invention provides a mordenite zeolite having a mesopore surface area of greater than 30 m 2 /g and an average primary crystal size as measured by TEM of less than 80 nm, and methods of making the mordenite zeolite.

Подробнее
04-08-2016 дата публикации

Catalyst Compositions and Use in Heavy Aromatics Conversion Processes

Номер: US20160221895A1
Принадлежит:

Disclosed is a catalyst composition and its use in a process for the conversion of a feedstock containing C+ aromatic hydrocarbons to produce light aromatic products, comprising benzene, toluene and xylene. The catalyst composition comprises a mordenite zeolite synthesized from TEA or MTEA, optionally at least one first metal of Group 10 of the IUPAC Periodic Table, and optionally at least one second metal of Group 11 to 15 of the IUPAC Periodic Table, wherein said mordenite zeolite has a mesopore surface area of greater than 30 m/g and said mordenite zeolite comprises agglomerates composed of primary crystallites, wherein said primary crystallites have an average primary crystal size as measured by TEM of less than 80 nm and an aspect ratio of less than 2. 1. A catalyst composition for conversion of Caromatic hydrocarbons to lighter aromatic products , said catalyst composition comprising (i) a mordenite zeolite synthesized from tetraethylammonium cation (TEA) or methyltriethylammonium cation (MTEA) , wherein said mordenite zeolite has a mesopore surface area of greater than 30 m/g and said mordenite zeolite comprises agglomerates composed of primary crystallites , wherein said primary crystallites have an average primary crystal size as measured by TEM of less than 80 nm and an aspect ratio of less than 2.2. The catalyst composition of claim 1 , said catalyst composition further comprising 0.005 to 5.0 wt. % of at least one first metal of Group 10 of the IUPAC Periodic Table claim 1 , based on the weight of said catalyst composition.3. The catalyst composition of claim 2 , said catalyst composition further comprising 0.01 to 5.0 wt. % of at least one second metal of Group 11 to 15 of the IUPAC Periodic Table claim 2 , based on the weight of said catalyst composition.4. The catalyst composition of claim 2 , wherein said at least first metal of Group 10 is selected from the group consisting of nickel claim 2 , platinum claim 2 , palladium and mixtures thereof.5. The ...

Подробнее
04-08-2016 дата публикации

Transalkylation of Heavy Aromatic Hydrocarbon Feedstocks

Номер: US20160221897A1
Принадлежит: ExxonMobil Chemical Patents Inc

A process for producing xylene comprises contacting a first feed comprising C 9+ aromatic hydrocarbons and hydrogen with a first catalyst composition comprising a first molecular sieve having a Constraint Index of 3 to 12 and at least one hydrogenation component. The first catalyst composition dealkylates at least part of the C 9+ aromatic hydrocarbons containing C 2+ alkyl groups and to saturate the resulting C 2+ olefins to produce a second feed. The second feed is then contacted with a second catalyst composition under conditions effective to transalkylate at least part of the C 9+ aromatic hydrocarbons in the second feed to produce a product comprising xylene. The second catalyst composition comprises a second molecular sieve having a Constraint Index less than 3 and a third molecular sieve having a Constraint Index of 3 to 12.

Подробнее
30-08-2018 дата публикации

METHOD FOR PREPARING ACETIC ACID BY CARBONYLATION OF METHANOL

Номер: US20180244599A1

The present invention provides a method for preparing acetic acid by carbonylation of methanol, which comprises: passing a raw material containing methanol, carbon monoxide and water through a reaction region loaded with a catalyst containing an acidic molecular sieve with an adsorbed organic amine, and carrying out a reaction under the following conditions to prepare acetic acid. The method in the present invention offers high acetic acid selectivity and good catalyst stability. The catalyst in the present invention does not contain noble metals such as rhodium or iridium, and does not need additional agent containing iodine, and thus does not generate a strong corrosive hydroiodic acid and the like. 1. A method for preparing acetic acid by carbonylation of methanol , which comprises: passing a raw material containing methanol , carbon monoxide and water through a reaction region loaded with a catalyst containing an acidic molecular sieve with an adsorbed organic amine , and carrying out a reaction under the following conditions to prepare acetic acid;wherein the acidic molecular sieve is one or two molecular sieves selected from the group consisting of molecular sieves with MOR framework and molecular sieves with FER framework;{'sub': '1-3', 'the organic amine is one or more organic amines selected from the group consisting of pyridine, phenylamine, cyclohexylamine, piperidine, substituted pyridines with one or more substituents, substituted phenylamines with one or more substituents, substituted cyclohexylamines with one or more substituents and substituted piperidines with one or more substituents; and the substituents are independently selected from halogen or Calkyl group;'}the reaction region is constituted by one or more reactors which are connected in series and/or in parallel;{'sup': −1', '−1, 'the reaction conditions are listed as follows: the reaction temperature is in a range from 150° C. to 350° C.; and the reaction pressure is in a range from 0.5 MPa ...

Подробнее
04-11-2021 дата публикации

METHODS OF HEAVY REFORMATE CONVERSION INTO AROMATIC COMPOUNDS

Номер: US20210340080A1
Принадлежит:

Method of making BTX compounds including benzene, toluene, and xylene, including feeding heavy reformate to a reactor containing a composite zeolite catalyst. The composite zeolite catalyst includes a mixture of layered mordenite (MOR-L) comprising a layered or rod-type morphology with a layer thickness less than 30 nm and ZSM-5. The MOR-L, the ZSM-5, or both include one or more impregnated metals. The method further includes producing the BTX compounds by simultaneously performing transalkylation and dealkylation of the heavy reformate in the reactor. The composite zeolite catalyst is able to simultaneously catalyze both the transalkylation and dealkylation reactions. 1. A composite zeolite catalyst ,the composite zeolite catalyst comprising a mixture of layered mordenite (MOR-L) and ZSM-5, where:the MOR-L or both the MOR-L and ZSM-5 comprise one or more impregnated metals,the MOR-L comprises a rod morphology with a smallest dimension less than 28 nm,{'sup': '2', 'the MOR-L without the impregnated metals comprises an external surface area greater than 120 m/g, and'}the MOR-L has a molar ratio of silicon to aluminum (Si/Al) from 4:1 to 8:1.2. The composite zeolite catalyst of claim 1 , where the one or more impregnated metals are selected from the group consisting of molybdenum claim 1 , chromium claim 1 , platinum claim 1 , nickel claim 1 , tungsten claim 1 , palladium claim 1 , ruthenium claim 1 , gold claim 1 , rhenium claim 1 , rhodium claim 1 , or combinations thereof and their respective oxides.3. The composite zeolite catalyst of claim 1 , where the one or more impregnated metals comprises rhenium.4. The composite zeolite catalyst of claim 1 , where the MOR-L claim 1 , the ZSM-5 claim 1 , or both the MOR-L and ZSM-5 comprise up to 20 wt. % of the one or more impregnated metals.5. The composite zeolite catalyst of claim 1 , where the MOR-L is impregnated with 0.25 to 0.5 wt. % rhenium.6. The composite zeolite catalyst of claim 1 , where the ZSM-5 is ...

Подробнее
29-08-2019 дата публикации

Low-Temperature Oxidation Catalyst With Particularly Marked Hydrophobic Properties ForThe Oxidation Of Organic Pollutants

Номер: US20190262771A1
Принадлежит:

The present invention relates to a catalyst comprising a macroporous noble metal-containing zeolite material and a porous SiO-containing binder, wherein the catalyst has a proportion of micropores of more than 70%, based on the total pore volume of the catalyst. The invention is additionally directed to a process for preparing the catalyst and to the use of the catalyst as an oxidation catalyst. 112-. (canceled)13. A method of purifying exhaust , the method comprising:providing an exhaust gas containing an organic pollutant; a microporous noble metal-containing zeolite material, the zeolite material having less than 2 mol. % aluminium, the zeolite material being selected from zeolites of the types AFI, AEL, BEA, CHA, EUO, FAU, FER, KFI, LTL, MAZ, MOR, MEL, MTW, OFF, TON and MFI, the noble metal being selected from the group consisting of rhodium, iridium, palladium, platinum, ruthenium, osmium, gold and silver and combinations thereof; and', {'sub': '2', 'a porous SiO-containing binder having less than 0.04 wt % aluminium,'}, 'wherein the catalyst has a proportion of micropores having a diameter of less than 1 nm of more than 70% relative to the total pore volume of the catalyst., 'oxidizing the exhaust gas with a catalyst under conditions sufficient to oxidize the organic pollutant, the catalyst comprising'}14. The method according to claim 13 , wherein the exhaust gas is an exhaust gas from a combustion process.15. The method according to claim 13 , wherein the exhaust gas is an exhaust gas from a power plant.16. The method according to claim 13 , wherein the exhaust gas is an exhaust gas from an industrial process.17. The method according to claim 13 , wherein the oxidation is performed at a temperature below 300° C.18. The method according to claim 13 , wherein the organic pollutant is a solvent-type organic pollutant.19. The method according to claim 13 , wherein the organic pollutant is a paraffin claim 13 , an olefin claim 13 , an aldehyde or an aromatic.20. ...

Подробнее
05-10-2017 дата публикации

FORMING LIGHT HYDROCARBONS

Номер: US20170283708A1
Принадлежит: Dow Global Technologies LLC

Form liquid product stream that has a Cto Chydrocarbon content of less than 5.0 wt % based upon a total weight of the liquid product stream via a process that includes contacting synthesis gas with a sulfurized Zeolite Socony Mobil-5 catalyst. The sulfurized Zeolite Socony Mobil-5 catalyst can include ZSM-5, cobalt, an alkali metal, sulfur, and a reduction promoter. 1. A process for producing a liquid product stream that has a Cto Chydrocarbon content of less than 5.0 wt % based upon a total weight of the liquid product stream , the process comprising:{'sup': '−1', 'contacting synthesis gas with a sulfurized Zeolite Socony Mobil-5 catalyst, wherein the sulfurized Zeolite Socony Mobil-5 catalyst includes cobalt and a sulfur doped Zeolite Socony Mobil-5 support, with the sulfur being incorporated via sulfate ions, the cobalt being present in an amount within a range of from 1 to 25 wt % based upon a dry weight of the sulfurized Zeolite Socony Mobil-5 catalyst, the sulfur being present in an amount within a range of from 0.01 to 1.00 w t%, based upon a dry weight of the sulfurized Zeolite Socony Mobil-5 catalyst, the conditions consisting essentially of a temperature within a range of from 150 to 300° C., a pressure within a range of from 5 to 40 bar, and a gas hourly space velocity within a range of from 100 to 10000 h.'}2. The process of claim 1 , wherein the sulfurized Zeolite Socony Mobil-5 catalyst includes an alkali metal.3. The process of claim 2 , wherein the alkali metal is within a range of from 0.01 to 4.50 wt % based upon a dry weight of the sulfurized ZSM-5 catalyst.4. The process of claim 2 , wherein the alkali metal is sodium.5. The process of claim 1 , wherein the sulfurized Zeolite Socony Mobil-5 catalyst includes a reduction promoter.6. The process of claim 5 , wherein the reduction promoter is within a range of from 0.01 to 5.00% based upon a dry weight of the sulfurized ZSM-5 catalyst.7. The process of claim 6 , wherein the reduction promoter is ...

Подробнее
27-08-2020 дата публикации

HEAT SOURCE DEVICE AND METHOD FOR USING SILVER ZEOLITE

Номер: US20200269223A1
Принадлежит:

Provided is a new heat source device that utilizes the catalytic reaction heat as a heat source for industries. The heat source device utilizing the catalytic reaction heat of silver zeolite includes an accommodation container for accommodating the silver zeolite while ensuring air permeability, wherein the accommodation container is configured to be ventilated with a mixed gas G containing hydrogen, steam, and air. The mixed gas has a hydrogen concentration of 1 to 20% by volume, a steam concentration of 1 to 95% by volume, an air concentration of 1 to 95% by volume, and a temperature of 100° C. or higher. 1. A heat source device utilizing a catalytic reaction heat of silver zeolite , the heat source device comprisingan accommodation container for accommodating the silver zeolite while ensuring air permeability, whereinthe accommodation container is configured to be ventilated with a mixed gas containing hydrogen, steam, and air.2. The heat source device of claim 1 , whereinthe mixed gas has a hydrogen concentration of 1 to 20% by volume, a steam concentration of 1 to 95% by volume, an air concentration of 1 to 95% by volume, and a temperature of 100° C. or higher.3. The heat source device of claim 1 , whereina temperature of the silver zeolite accommodated in the accommodation container becomes 400° C. or higher after one minute has elapsed from the ventilation of the accommodation container with the mixed gas.4. The heat source device of claim 1 , whereinthe silver zeolite is at least one selected from the group consisting of zeolite AgX in which at least a part of ion exchange sites included in zeolite X is substituted with silver, zeolite AgA in which at least a part of ion exchange sites included in zeolite A is substituted with silver, zeolite AgY in which at least a part of ion exchange sites included in zeolite Y is substituted with silver, zeolite AgL in which at least a part of ion exchange sites included in zeolite L is substituted with silver, and ...

Подробнее
19-09-2019 дата публикации

METHODS OF PRODUCING COMPOSITE ZEOLITE CATALYSTS FOR HEAVY REFORMATE CONVERSION INTO XYLENES

Номер: US20190284057A1
Принадлежит:

A method of forming composite zeolite catalyst particles includes combining a silicon source, an aqueous organic structure directing agent having a polyquaternary ammonium compound, water and an aluminum source to form a catalyst gel. The method also includes heating the catalyst gel to form the composite zeolite catalyst particle having an intergrowth region with a mixture of both Mordenite crystals and ZSM-5 crystals. An associated method of making xylene includes feeding heavy reformate to a reactor, the reactor containing the composite zeolite catalyst particles, and producing xylene by simultaneously performing dealkylation and transalkylation of the heavy reformate in the reactor, where each composite zeolite catalyst particle is able to catalyze both the dealkylation and transalkylation reactions. 2. The method of where the silicon source comprises a silica gel claim 1 , silicon oxide claim 1 , silicon halide claim 1 , tetraalkyl orthosilicate claim 1 , silicic acid claim 1 , fumed silica claim 1 , sodium silicate claim 1 , colloidal silica claim 1 , or combinations thereof.3. The method of where the silicon source is a silica gel and the silica gel is a 20 to 60 wt. % suspension of silica in water.4. The method of where the polyquaternary ammonium compound is a diquaternary ammonium compound.5. The method of where claim 1 ,X is a halogen selected from Cl, Br, I, or combinations thereof,{'sub': '18-22', 'R1 is a substituted or an unsubstituted Calkyl group;'}{'sub': '6', 'R2 is a substituted or an unsubstituted Calkyl group; and'}{'sub': '6-8', 'R3 is a substituted or an unsubstituted Calkyl group or an alkenyl group.'}6. The method of where the aluminum source comprises NaAlO.7. The method of where the aluminum source claim 1 , the silicon source claim 1 , the organic structure directing agent claim 1 , and the water are further combined with NaOH to form the catalyst gel.8. The method of where the heating of the catalyst gel is conducted in a sealed vessel ...

Подробнее
19-09-2019 дата публикации

Methods of heavy reformate conversion into aromatic compounds

Номер: US20190284114A1

Method of making BTX compounds including benzene, toluene, and xylene, including feeding heavy reformate to a reactor containing a composite zeolite catalyst. The composite zeolite catalyst includes a mixture of layered mordenite (MOR-L) comprising a layered or rod-type morphology with a layer thickness less than 30 nm and ZSM-5. The MOR-L, the ZSM-5, or both include one or more impregnated metals. The method further includes producing the BTX compounds by simultaneously performing transalkylation and dealkylation of the heavy reformate in the reactor. The composite zeolite catalyst is able to simultaneously catalyze both the transalkylation and dealkylation reactions.

Подробнее
10-09-2020 дата публикации

METHOD FOR PRODUCING OLIGOSILANE

Номер: US20200283297A1
Принадлежит: SHOWA DENKO K.K.

A method for producing an oligosilane which includes a reaction step of producing an oligosilane by dehydrogenative coupling of hydrosilane. The reaction step is carried out in the presence of a catalyst containing at least one transition element selected from the group consisting of Periodic Table group 3 transition elements, group 4 transition elements, group 5 transition elements, group 6 transition elements, and group 7 transition elements. Also disclosed is a method for producing a catalyst for dehydrogenative coupling that produces an oligosilane by dehydrogenative coupling of hydrosilane. 1. A method for producing an oligosilane , comprising a reaction step of producing an oligosilane by dehydrogenative coupling of hydrosilane , whereinthe reaction step is carried out in the presence of a catalyst containing at least one transition element selected from the group consisting of Periodic Table group 3 transition elements, group 4 transition elements, group 5 transition elements, group 6 transition elements, and group 7 transition elements.2. The method for producing an oligosilane according to claim 1 , wherein the catalyst is a heterogeneous catalyst containing a support and contains the transition element on the surface and/or in the interior of the support.3. The method for producing an oligosilane according to claim 2 , wherein the support is at least one selected from the group consisting of silica claim 2 , alumina claim 2 , titania claim 2 , and zeolite.4. The method for producing an oligosilane according to claim 3 , wherein the zeolite has pores with a minor diameter of at least 0.43 nm and a major diameter of not more than 0.69 nm.5. The method for producing an oligosilane according to claim 3 , wherein the support is a spherical or cylindrical molding claim 3 , of an alumina-containing powder as a binder and a zeolite having pores with a minor diameter of at least 0.43 nm and a major diameter of not more than 0.69 nm claim 3 , and has an alumina ...

Подробнее
18-10-2018 дата публикации

Method of Forming a Catalyst with an Ion-Modified Binder

Номер: US20180297017A1
Принадлежит:

An alkylation catalyst having a zeolite catalyst component and a binder component providing mechanical support for the zeolite catalyst component is disclosed. The binder component is an ion-modified binder that can include metal ions selected from the group consisting of Co, Mn, Ti, Zr, V, Nb, K, Cs, Ga, B, P, Rb, Ag, Na, Cu, Mg, Fe, Mo, Ce, and combinations thereof. The metal ions reduce the number of acid sites on the zeolite catalyst component. The metal ions can range from 0.1 to 50 wt % based on the total weight of the ion-modified binder. Optionally, the ion-modified binder is present in amounts ranging from 1 to 80 wt % based on the total weight of the catalyst. 1. An alkylation catalyst , comprising:a catalyst component; anda binder component providing mechanical support for the catalyst component;wherein the binder component comprises an ion-modified binder comprising metal ions;wherein the metal ions are selected from the group consisting of Co, Mn, Ti, Zr, V, Nb, K, Cs, Ga, B, P, Rb, Ag, Na, Cu, Mg, Fe, Mo, Ce, and combinations thereof; andwherein the metal ions reduce the number of acid sites on the catalyst component.2. The catalyst of claim 1 , wherein the ion-modified binder comprises metal ions in amounts ranging from 0.1 to 50 wt % based on the total weight of the ion-modified binder.3. The process of claim 1 , wherein the ion-modified binder comprises metal ions in amounts ranging from 0.1 to 20 wt % based on the total weight of the ion-modified binder.4. The catalyst of claim 1 , wherein the ion-modified binder is present in amounts ranging from 1 to 80 wt % based on the total weight of the catalyst.5. The catalyst of claim 1 , wherein the ion-modified binder is present in amounts ranging from 5 to 60 wt % based on the total weight of the catalyst.6. The catalyst of claim 1 , wherein the metal ions on the ion-modified binder alters the spacial structure of the catalyst.7. The catalyst of claim 1 , wherein the binder comprises amorphous silica or ...

Подробнее
25-10-2018 дата публикации

PASSIVE NOx ADSORBER

Номер: US20180304244A1
Принадлежит: JOHNSON MATTHEY PLC

A NOx absorber catalyst for treating an exhaust gas from a diesel engine. The NOx absorber catalyst comprises a first region comprising a NOx absorber material comprising a molecular sieve catalyst, and a second region comprising a nitrogen dioxide reduction material; and a substrate having an inlet end and an outlet end.

Подробнее
10-10-2019 дата публикации

PROCESS FOR PREPARING A MOLYBDENUM-PLATINUM-BASED CATALYST FOR THE SYNTHESIS OF BENZENE BY TRANSALKYLATION

Номер: US20190308176A1
Принадлежит:

A process for preparing a catalyst composition comprising (a) preparing a carrier comprising (i) mordenite in an amount in the range of from 20 to 80 wt %, based on total weight of carrier, (ii) ZSM-5 type zeolite in an amount in the range of from 10 to 70 wt %, based on total weight of carrier; and (iii) an inorganic binder in an amount in the range of from 10 to 50 wt %, based on total weight of carrier; (b) incorporating in the carrier molybdenum in an amount in the range of from 1 to 10 wt %, as metal based on total weight of catalyst composition, and subjecting the thus treated carrier to a temperature of from 100 to at most 300° C. and (c) incorporating in the molybdenum containing carrier obtained in step (b) platinum in an amount of from 0.005 to 1 wt %, as metal based on total weight of catalyst composition, and subjecting the thus treated carrier to a temperature of from 200 to at most 600° C.; and a process for conversion of alkylaromatic hydrocarbons containing feedstock using a catalyst prepared by said process. Process using the prepared catalyst composition for alkylaromatic hydrocarbon conversion. 1. A process for preparing a catalyst composition comprising:(a) preparing a carrier comprising (i) mordenite in an amount in the range of from 20 to 80 wt %, based on total weight of carrier, (ii) ZSM-5 type zeolite in an amount in the range of from 10 to 70 wt %, based on total weight of carrier; and (iii) an inorganic binder in an amount in the range of from 10 to 50 wt %, based on total weight of carrier;(b) incorporating in the carrier molybdenum in an amount in the range of from 1 to 10 wt %, as metal based on total weight of catalyst composition, and subjecting the thus treated carrier to a temperature of from 100 to at most 300° C.; and(c) incorporating in the molybdenum containing carrier obtained in step (b) platinum in an amount of from 0.005 to 1 wt %, as metal based on total weight of catalyst composition, and subjecting the thus treated ...

Подробнее
01-10-2020 дата публикации

Processes for Producing Xylenes

Номер: US20200308087A1
Принадлежит: ExxonMobil Chemical Patents Inc

A process for making p-xylene comprising co-feeding toluene with C8 aromatics into a vapor phase isomerization unit can improve xylenes loss and benzene selectivity in ethylbenzene conversion

Подробнее
26-11-2015 дата публикации

CATALYST AND METHOD FOR PREPARATION THEREOF

Номер: US20150336088A1
Принадлежит:

A process for converting one or more C3-C12 oxygenates comprising: contacting a feed, which feed comprises one or more C3-C12 oxygenates, with hydrogen at a hydrogen partial pressure of more than 1.0 MegaPascal in the presence of a sulphided carbon-carbon coupling catalyst; wherein the carbon-carbon coupling catalyst comprises equal to or more than 60 wt % of a zeolite and in the range from equal to or more than 0.1% wt to equal to or less than 10 wt % of a hydrogenation metal, based on the total weight of the carbon-carbon coupling catalyst; and wherein the zeolite comprises 10-membered and/or 12-membered ring channels and a Silica to Alumina molar Ratio (SAR) in the range from equal to or more than 10 to equal to or less than 300. 1. A sulphided carbon-carbon coupling catalyst comprising equal to or more than 60 wt % of a zeolite and in the range from equal to or more than 0.1 wt % to equal to or less than 10 wt % of a hydrogenation metal , based on the total weight of the carbon-carbon coupling catalyst;wherein the zeolite comprises 10-membered and/or 12-membered ring channels and a Silica to Alumina molar Ratio (SAR) in the range from equal to or more than 10 to equal to or less than 300.2. The sulphided carbon-carbon coupling catalyst according to claim 1 , wherein the carbon-carbon coupling catalyst comprises in the range from equal to or more than 0.5 wt % to equal to or less than 5 wt % of a hydrogenation metal claim 1 , based on the total weight of the carbon-carbon coupling catalyst.3. The sulphided carbon-carbon coupling catalyst according to claim 1 , wherein the carbon-carbon coupling catalyst comprises one or more hydrogenation metals chosen from the group consisting of copper claim 1 , molybdenum claim 1 , tungsten claim 1 , cobalt and nickel.4. The sulphided carbon-carbon coupling catalyst according to claim 1 , wherein the carbon-carbon coupling catalyst only contains hydrogenation metals chosen from the group consisting of nickel claim 1 , cobalt ...

Подробнее
22-12-2016 дата публикации

PROCESS FOR THE AROMATIZATION OF A METHANE-CONTAINING GAS STREAM USING TITANIUM HYDROGEN ACCEPTOR PARTICLES

Номер: US20160368835A1
Принадлежит:

Implementations of the disclosed subject matter provide a process for the aromatization of a methane-containing gas stream that includes contacting the methane-containing gas stream in a reaction zone of an aromatization reactor comprising an aromatization catalyst and a titanium hydrogen acceptor under methane-containing gas aromatization conditions to produce a product stream comprising aromatics and hydrogen, wherein at least a portion of the produced hydrogen is bound by the titanium hydrogen acceptor in the reaction zone and removed from the product and the reaction zone as titanium hydride, and wherein the weight ratio of titanium hydrogen acceptor to the aromatization catalyst is at least 1:1. 1. A process for the aromatization of a methane-containing gas stream comprising:contacting the methane-containing gas stream in a reaction zone of an aromatization reactor comprising an aromatization catalyst and a titanium hydrogen acceptor under methane-containing gas aromatization conditions to produce a product stream comprising aromatics and hydrogen, wherein at least a portion of the produced hydrogen is bound by the titanium hydrogen acceptor in the reaction zone and removed from the product stream and the reaction zone, andwherein the weight ratio of titanium hydrogen acceptor to the aromatization catalyst is at least 1:1.2. The process of claim 1 , wherein the methane-containing gas stream conversion and corresponding benzene yield per pass are higher than the conversion and yield obtained with the same aromatization catalyst and under the same methane-containing gas aromatization conditions claim 1 , but in the absence of the weight ratio of titanium hydrogen acceptor to the aromatization catalyst in the reaction zone of the aromatization reactor.3. The process of claim 1 , wherein the weight ratio of titanium hydrogen acceptor to the aromatization catalyst is from 1:1 to 10:1.4. The process of claim 1 , wherein the weight ratio of titanium hydrogen acceptor ...

Подробнее
05-11-2020 дата публикации

Organic base modified composite catalyst and method for producing ethylene by hydrogenation of carbon monoxide

Номер: US20200346992A1

An organic base modified composite catalyst for producing ethylene by hydrogenation of carbon monoxide is a composite catalyst and formed by compounding component I and component II in a mechanical mixing mode. The active ingredient of the component I is a metal oxide; the component II is an organic base modified zeolite of MOR topology; and a weight ratio of the active ingredients in the component I to the component II is 0.1-20, and preferably 0.3-8. The reaction process has an extremely high product yield and selectivity. The selectivity of C2-C3 olefins is as high as 78-87%; the selectivity of hydrocarbon products with more than 4 C atoms is less than 10%; the selectivity of a methane side product is extremely low (<9%); and meanwhile, the selectivity of the ethylene is 75-82%.

Подробнее
05-11-2020 дата публикации

CATALYST CONTAINING LF-TYPE B ACID AND METHOD FOR PREPARING ETHYLENE USING DIRECT CONVERSION OF SYNGAS

Номер: US20200346993A1
Принадлежит:

A catalyst containing LF-type B acid preparing ethylene using direct conversion of syngas is a composite catalyst and formed by compounding component A and component B in a mechanical mixing mode. The active ingredient of the component A is a metal oxide; the component B is a zeolite of MOR topology; and a weight ratio of the active ingredients in the component A to the component B is 0.1-20. The reaction process has an extremely high product yield and selectivity, with the selectivity for light olefin reaching 80-90%, wherein ethylene has high space time yield and can reach selectivity of 75-80%. Meanwhile, the selectivity for a methane side product is extremely low (<15%). 1. A catalyst , comprising a component I and a 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 zeolite of MOR topology;{'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, FeAlO, GaO, BiO, InO, InAlMnO, and InGaMnO,'}{'sub': x', 'x', 'x', 'x', 'x', 'x, 'sup': '2', 'a specific surface area of MnO, ZnO, CeO, GaO, BiOand InOis 1-100 m/g;'}{'sub': a', '(1-a)', 'x', 'a', '(1-a)', 'x', 'a', '(1-a)', 'x', 'a', '(1-a)', 'x', 'a', '(1-a)', 'x', 'a', '(1-a)', 'x', 'a', '(1-a)', 'x', 'a', '(1-a)', 'x', '(1-a)', 'x', 'a', '(1-a)', 'x', 'a', 'b', 'x', 'a', 'b', '(1-a-b)', 'x, 'sup': (1-a-b)', '2, 'a specific surface area of MnCrO, MnAlO, MnZrO, MnInO, ZnCrO, ZnAlO, ZnGaO, ZnInO, CoaAlO, FeAlO, InAlMnO, and InGaMnOis 5-150 m/g;'}a value range of x is 0.7-3.7, and a value range of a is 0-1; and a value range of a+b is 0-1;the MOR zeolite in the component B comprises LF-type B acid; and the content ...

Подробнее
29-12-2016 дата публикации

Catalyst for Direct Production of Isoparaffine-rich Synthetic Oil and Method for Preparing Catalyst

Номер: US20160375430A1
Принадлежит:

A catalyst for producing isoparaffins-rich synthetic oil is a granulated porous composite material comprising a three-dimensional heat-conducting structure of metal aluminum and Raney cobalt, and a binding component comprising an H-form zeolite. The particles of Raney cobalt and zeolite are in mutual direct contact. Fractions of macropores in an open porosity of the catalyst granules and of mesopores of the size of 70-500 Å in an open porosity of the catalyst granules are respectively 55-79% and 7-20%, a fraction of micropores being the rest. A method for preparing the catalyst comprises mixing binding component powders, peptizing the mixture with a nitric acid solution, mixing obtained homogeneous gel with powders of Raney cobalt and metal aluminum and a liquid phase to form a paste, extruding same into granules and calcinating the granules. The catalyst improves reagents mass transfer inside the granules and increases isoparaffine content in the produced oil. 1. A catalyst for producing isoparaffins-rich synthetic oil from CO and H , where said catalyst is a granulated porous composite material comprising:a three-dimensional heat-conducting structure of metal aluminum and Raney cobalt particles, anda binding component,wherein said binding component comprises H-form zeolite and wherein a fraction of macropores in an open porosity of the catalyst granules is 55-79% and a fraction of mesopores of the size of 70-500 Å in an open porosity of the catalyst granules is 7-20%, a fraction of micropores being the rest.2. (canceled)3. (canceled)4. The catalyst of claim 1 , wherein thermal conductivity of the catalyst granules is no less than 4 W/m·K.5. The catalyst of claim 1 , wherein said H-form zeolite comprises either of beta zeolite claim 1 , mordenite claim 1 , and ZSM-5 in H-form or any combination thereof.6. The catalyst of claim 1 , wherein content of said Raney cobalt is 10-50% of the catalyst weight.7. The catalyst of claim 1 , wherein content of said metal ...

Подробнее
20-12-2018 дата публикации

COMPOSITE HIERARCHICAL ZEOLITE CATALYST FOR HEAVY REFORMATE CONVERSION TO XYLENES

Номер: US20180361372A1
Принадлежит: Saudi Arabian Oil Company

A method of producing a hierarchical zeolite composite catalyst. The method including dissolving, in an alkaline solution and in the presence of a surfactant, a catalyst precursor comprising mesoporous zeolite to yield a dissolved zeolite solution, where the mesoporous zeolite comprises large pore mordenite and medium pore ZSM-5. The method also including condensing the dissolved zeolite solution to yield a solid zeolite composite from the dissolved zeolite solution and heating the solid zeolite composite to remove the surfactant. The method further including impregnating the solid zeolite composite with one or more active metals selected from the group consisting of molybdenum, platinum, rhenium, nickel, and combinations thereof to yield impregnated solid zeolite composite and calcining the impregnated solid zeolite composite to produce the hierarchical zeolite composite catalyst. The hierarchical zeolite composite catalyst has a mesostructure comprising at least one disordered mesophase and at least one ordered mesophase. 1. A method of producing a hierarchical zeolite composite catalyst comprising:dissolving, in an alkaline solution and in the presence of a surfactant, a catalyst precursor comprising mesoporous zeolite while heating, stirring, or both to yield a dissolved zeolite solution, where the mesoporous zeolite comprises large pore mordenite, medium pore ZSM-5, or both large pore mordenite and medium pore ZSM-5; adjusting a pH of the dissolved zeolite solution; and', 'aging the pH adjusted dissolved zeolite solution;, 'condensing the dissolved zeolite solution to yield a solid zeolite composite from the dissolved zeolite solution, where condensing the dissolved zeolite solution comprisesheating the solid zeolite composite to remove the surfactant;impregnating the solid zeolite composite with one or more active metals selected from the group consisting of molybdenum, platinum, rhenium, nickel, and combinations thereof to yield impregnated solid zeolite ...

Подробнее
27-12-2018 дата публикации

CATALYST COMPOSITION, ITS PREPARATION AND PROCESS USING SUCH COMPOSITION

Номер: US20180369795A1
Принадлежит:

Catalyst composition comprising a carrier and one or more Group 10 metal components, wherein the carrier comprises (i) 20 to 90 wt % mordenite having a silica to alumina molar ratio in the range of from 10 to 60; (ii) 10 to 70 wt % ZSM-5 type zeolite having a silica to alumina molar ratio in the range of from 5 to 50 and an average particle size in the range of from 5 to 50 nm; and (iii) 10 to 50 wt % of binder; a process for preparing the catalyst, and a process for the conversion of an aromatic hydrocabons-containing feedstock using the catalyst. 1. A catalyst composition which comprises a carrier and one or more metal components supported on the carrier , wherein the carrier comprises (i) mordenite in an amount in the range of from 20 to 90 wt % , based on total weight of carrier , the mordenite having a silica to alumina molar ratio in the range of from 10 to 60; (ii) ZSM-5 type zeolite in an amount of from 10 to 70 wt % , based on total weight of carrier , the ZSM-5 type zeolite having a silica to alumina molar ratio in the range of from 5 to 50 and an average particle size in the range of from 5 to 50 nm; and (iii) an inorganic binder in an amount in the range of from 10 to 50 wt % , based on total weight of carrier; and wherein the one or more metal components comprise a group 10 metal.2. The catalyst composition according to claim 1 , wherein the mordenite is present in an amount in the range of from 30 to 70 wt % claim 1 , based on total weight of carrier.3. The catalyst composition according to claim 1 , wherein the ZSM-5 type zeolite is present in an amount in the range of from 15 to 60 wt % claim 1 , based on total weight of carrier.4. The catalyst composition according to claim 1 , wherein the inorganic binder is present in an amount in the range of from 10 to 40 wt % claim 1 , based on total weight of carrier material.5. The catalyst composition according to claim 1 , wherein the ZSM-5 type zeolite has a number average particle size in the range of ...

Подробнее
12-12-2019 дата публикации

HYDROCRACKING PROCESS

Номер: US20190375696A1
Принадлежит:

A process for hydrocracking 2,4-dimethylpentane and/or 2,2,3-trimethylbutane can comprise: contacting a hydrocracking feed stream in the presence of hydrogen with a hydrocracking catalyst, wherein the hydrocracking feed stream comprises at least 0.5 wt % of 2,4-dimethylpentane and/or 2,2,3-trimethylbutane, based upon a total weight of the hydrocracking feed stream; and wherein the hydrocracking catalyst comprises a medium pore zeolite having a pore size of 5-6 A and a silica to alumina molar ratio of 20-75; preferably the hydrocracking catalyst comprises a medium pore zeolite having a pore size of 5-6 A and a silica to alumina molar ratio of 20-75 and a large pore zeolite having a pore size of 6-8 A and a silica to alumina molar ratio of 10-80, wherein the hydrogenation metal is deposited on the medium pore zeolite and the large pore zeolite. 1. A method of hydrocracking at least one of 2 ,4-dimethylpentane and 2 ,2 ,3-trimethylbutane , comprising:{'sup': '−1', 'contacting a hydrocracking feed stream in the presence of hydrogen with a hydrocracking catalyst under process conditions including a temperature of 425-580° C., a pressure of 300-5000 kPa gauge and a Weight Hourly Space Velocity of 0.1-30 hto produce a hydrocracking product stream comprising benzene;'}{'sub': 5', '12, 'wherein the hydrocracking feed stream comprising C-Chydrocarbons which includes at least 0.5 wt % of 2,4-dimethylpentane and/or 2,2,3-trimethylbutane, based upon a total weight of the hydrocracking feed stream; and'}wherein the hydrocracking catalyst comprises a hydrogenation metal in an amount of 0.010-0.30 wt % with respect to the total catalyst; andwherein the hydrocracking catalyst comprises a medium pore zeolite having a pore size of 5-6 Å and a silica to alumina molar ratio of 20-75.2. The process according to claim 1 , wherein the total amount of 2 claim 1 ,4-dimethylpentane and 2 claim 1 ,2 claim 1 ,3-trimethylbutane in the hydrocracking feed stream is at least 1.0 wt % with respect ...

Подробнее
26-12-2019 дата публикации

PROCESS FOR THE CONVERSION OF MONOETHANOLAMINE TO ETHYLENEDIAMINE EMPLOYING A COPPER-MODIFIED ZEOLITE OF THE MOR FRAMEWORK STRUCTUR

Номер: US20190389794A1
Принадлежит:

The present invention relates to a process for the conversion of 2-aminoethanol to ethane-1,2-diamine and/or linear polyethylenimines of the formula HN—[CHCHNH]—CHCHNHwherein n≥1 comprising: (i) providing a catalyst comprising a zeolitic material having the MOR framework structure comprising YOand XO, wherein Y is a tetravalent element and X is a trivalent element, said zeolitic material containing copper as extra-framework ions; (ii) providing a gas stream comprising 2-aminoethanol and ammonia; (iii) contacting the catalyst provided in (i) with the gas stream provided in (ii) for converting 2-aminoethanol to ethane-1,2-diamine and/or linear polyethylenimines. 1. A process for the conversion of 2-aminoethanol to ethane-1 ,2-diamine and/or linear polyethylenimines of the formula HN—[CHCHNH]—CHCHNHwherein n≥1 comprising{'sub': 2', '2', '3, '(i) providing a catalyst comprising a zeolitic material having the MOR framework structure comprising YOand XO, wherein Y is a tetravalent element and X is a trivalent element, said zeolitic material containing copper as extra-framework ions;'}(ii) providing a gas stream comprising 2-aminoethanol and ammonia;(iii) contacting the catalyst provided in (i) with the gas stream provided in (ii) for converting 2-aminoethanol to ethane-1,2-diamine and/or linear polyethylenimines.2. The process of claim 1 , wherein the gas stream provided in (ii) and contacted with the catalyst in (iii) contains 2-aminoethanol in an amount in the range of from 0.1 to 10 vol.-%.3. The process of claim 1 , wherein the gas stream provided in (ii) and contacted with the catalyst in (iii) contains ammonia in an amount in the range of from 5 to 90 vol.-%.4. The process of claim 1 , wherein the gas stream provided in (ii) and contacted with the catalyst in (iii) contains 1 vol.-% or less of hydrogen.5. The process of claim 1 , wherein the gas stream provided in (ii) and contacted with the catalyst in (iii) further contains hydrogen in an amount in the range of ...

Подробнее
22-06-2007 дата публикации

Preparation of a catalyst, useful in oligomerization of an olefinic charge, comprises introduction of a metal on a support containing protonated zeolite, treatment of the zeolite in the presence of a molecular compound and heat treatment

Номер: FR2894850A1
Автор: LAURENT Simon
Принадлежит: IFP Energies Nouvelles IFPEN

Preparation of a catalyst containing a modified zeolite that exhibits a maximum opening diameter of pores =7A[deg] before being modified, comprises introduction of a metal i.e. from metals of the groups VIB and VIII of the periodic classification of elements, on a support containing protonated zeolite, treatment of the zeolite in the presence of a molecular compound containing silicon and exhibiting a diameter higher than the maximum opening diameter of the zeolite pores and heat treatment.

Подробнее
27-08-2008 дата публикации

Catalytically activated diesel particulate filter with ammoniac blocking action

Номер: EP1961933A1
Принадлежит: Umicore AG and Co KG

The catalytic activated diesel particle filter has a filter body and an oxidation-active catalytic coating (2) and has a selective catalytic reduction (SCR) active coating (1) in the reaction, where an ammonia storage material is contained. An arrangement maintains the layers, so that the exhaust gas to be cleaned is passed in catalytically active coating in the SCR-reaction and after that the oxidation active catalytic coating is passed. The active coating in selective catalytic reduction reaction contains multiple hydrogen cations or transition metal cations exchanged zeolites.

Подробнее
25-04-1978 дата публикации

Conversion of synthesis gas to hydrocarbon mixtures

Номер: US4086262A
Принадлежит: Mobil Oil Corp

Contacting a mixture of carbon monoxide and hydrogen with an intimate mixture of a carbon monoxide reduction catalyst, such as a Fischer-Tropsch catalyst or a methanol synthesis catalyst, and an acidic crystalline aluminosilicate having a pore dimension greater than about 5 Angstroms to produce hydrocarbon mixtures useful in the manufacture of heating fuels, high octane gasoline, aromatic hydrocarbons, and chemicals intermediates.

Подробнее
30-01-2018 дата публикации

Catalyst for direct production of isoparaffins-rich synthetic oil and a method for preparing the catalyst

Номер: US9878314B2
Принадлежит: Infra Xtl Technology Ltd

A catalyst for producing isoparaffins-rich synthetic oil is a granulated porous composite material comprising a three-dimensional heat-conducting structure of metal aluminum and Raney cobalt, and a binding component comprising an H-form zeolite. The particles of Raney cobalt and zeolite are in mutual direct contact. Fractions of macropores in an open porosity of the catalyst granules and of mesopores of the size of 70-500 Å in an open porosity of the catalyst granules are respectively 55-79% and 7-20%, a fraction of micropores being the rest. A method for preparing the catalyst comprises mixing binding component powders, peptizing the mixture with a nitric acid solution, mixing obtained homogeneous gel with powders of Raney cobalt and metal aluminum and a liquid phase to form a paste, extruding same into granules and calcinating the granules. The catalyst improves reagents mass transfer inside the granules and increases isoparaffine content in the produced oil.

Подробнее
23-04-2009 дата публикации

Method of direct synthesis of light hydrocarbons from natural gas

Номер: WO2009051353A2

The present invention relates to a method of direct synthesis of light hydrocarbons from natural gas and carbon dioxide capable of improving production yield of light hydrocarbons and carbon utilization efficiency through a series of process of preparing synthesis gas with a predetermined molar ratio of carbon monoxide and hydrogen by a combined steam reforming of natural gas and carbon dioxide reforming of methane, performing Fischer-Tropsch reaction of the prepared synthesis gas in the presence of a specific catalyst, and recycling the byproducts of methane and carbon dioxide as the source material of the combined reforming.

Подробнее
23-06-2010 дата публикации

Method of direct synthesis of light hydrocarbons from natural gas

Номер: EP2197816A2

The present invention relates to a method of direct synthesis of light hydrocarbons from natural gas and carbon dioxide capable of improving production yield of light hydrocarbons and carbon utilization efficiency through a series of process of preparing synthesis gas with a predetermined molar ratio of carbon monoxide and hydrogen by a combined steam reforming of natural gas and carbon dioxide reforming of methane, performing Fischer-Tropsch reaction of the prepared synthesis gas in the presence of a specific catalyst, and recycling the byproducts of methane and carbon dioxide as the source material of the combined reforming.

Подробнее
06-06-2002 дата публикации

Process for producing aromatic hydrocarbon compounds and liquefied petroleum gas from hydrocarbon feedstock

Номер: WO2002044306A1
Принадлежит: Sk Corporation

Fisclosed are a process for producing aromatic hydrocarbon compounds and liquefied petroleum gas (LPG) from a hydrocarbon feedstock having boiling points of 30-250 °C and a catalyst useful therefor. In the presence of said catalyst, aromatic components in the hydrocarbon feedstock are converted to BTX-enriched components of liquid phase through hydrodealkylation and/or transalkylation, and non-aromatic components are converted to LPG-enriched gaseous materials through hydrocracking. The products of liquid phase may be separated as benzene, toluene, xylene, and C9 or higher aromatic compounds, respectively according to their different boiling points, while LPG is separated from the gaseous products, in a distillation tower.

Подробнее
30-12-2009 дата публикации

Novel transalkylation process

Номер: WO2009158244A2
Принадлежит: UOP LLC

This invention embodies a catalyst and a process for transalkylation of C 7 , C 9 , and C 10 aromatics to obtain a high yield of xylenes. The catalyst comprises a novel UZM-14 catalytic material comprising globular aggregates of crystallites having a MOR framework type with a mean crystallite length parallel to the direction of the 12 ring channels of 60 nm or less and a mesopore volume of at least 0.10 cc/gram. The UZM-14 catalyst is particularly active and stable in a transalkylation process.

Подробнее
22-01-2004 дата публикации

Method and apparatus for reducing the content of NOx and N2O in gases

Номер: DE10226461A1
Принадлежит: UHDE GMBH

Das Verfahren umfasst das Leiten des N¶2¶O und NO¶x¶ enthaltenden Gases über eine Folge zweier Katalysatorbetten, enthaltend einen oder mehrere mit Eisen beladene Zeolithe, die Zugabe eines Reduktionsmittels für NO¶x¶ zwischen den Katalysatorbetten, das Einstellen einer Temperatur von weniger als 500 DEG C im ersten und zweiten Katalysatorbett, das Einstellen eines Gasdruckes von mindestens 2 bar in den beiden Katalysatorbetten, und die Auswahl einer solchen Raumgeschwindigkeit im ersten und zweiten Katalysatorbett, so dass im ersten Katalysatorbett ein Abbau des N¶2¶O-Gehalts des Gases um höchstens bis zu 90%, bezogen auf den N¶2¶O-Gehalt am Eingang des ersten Katalysatorbettes, erfolgt, und dass im zweiten Katalysatorbett ein weiterer Abbau des N¶2¶O-Gehalts des Gases um mindestens 30%, bezogen auf den N¶2¶O-Gehalt am Eingang des zweiten Katalysatorbettes, erfolgt. DOLLAR A Die erste Reaktionszone dient zum Abbau von N¶2¶O und in der zweiten Reaktionszone wird das NO¶x¶ reduziert und zumindest ein Teil des verbliebenen N¶2¶O wird zersetzt. DOLLAR A Die beschriebene Vorrichtung umfasst mindestens ein radial durchströmtes Katalysatorbett. The process comprises passing the gas containing N 2 O 2 and NO 3 x 10 over a series of two catalyst beds containing one or more iron-loaded zeolites, adding a reducing agent for NO 2+ between the catalyst beds, adjusting a temperature of less than 500 ° C in the first and second catalyst beds, setting a gas pressure of at least 2 bar in the two catalyst beds, and selecting such a space velocity in the first and second catalyst beds such that in the first catalyst bed there is a reduction in N 2 O 2 Content of the gas at most up to 90%, based on the N¶2¶O content at the entrance of the first catalyst bed, takes place, and that in the second catalyst bed, a further reduction of the N¶2¶O content of the gas by at least 30 %, based on the N¶2¶O content at the entrance of the second catalyst bed, takes place. DOLLAR A The first ...

Подробнее
29-10-2014 дата публикации

DIMETHYL CARBONILATION PROCESS

Номер: BRPI0810842A2
Принадлежит: Bp Chem Int Ltd

Подробнее
29-10-2014 дата публикации

DIMETHYL CARBONILATION PROCESS

Номер: BRPI0810817A2
Принадлежит: Bp Chem Int Ltd

Подробнее
09-05-1984 дата публикации

改良水素化脱ロウ触媒及びその方法

Номер: JPS5980334A
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。

Подробнее
07-09-2010 дата публикации

Process for preparing alkylated aromatic compound

Номер: US7790936B2
Принадлежит: Mitsui Chemicals Inc

The present invention provides a process in which a ketone is directly reacted with an aromatic compound in a single reaction step to obtain the corresponding alkylated aromatic compound in a higher yield. By reacting an aromatic compound with a ketone and hydrogen in the presence of a solid acid substance and a catalyst composition containing Cu and Zn in a ratio of Zn to Cu ranging from 0.70 to 1.60 (atomic ratio), the corresponding alkylated aromatic compound is prepared.

Подробнее
27-03-2013 дата публикации

烷基化芳香族化合物的制造方法

Номер: CN101589009B
Принадлежит: Mitsui Chemical Industry Co Ltd

本发明提供用单一反应工序使酮和芳香族化合物直接反应,以更高的收率获得对应的烷基化芳香族化合物的方法。在固体酸物质和以Zn相对于Cu为0.70~1.60(原子比)的比例含有Cu和Zn的催化剂组合物存在下,使芳香族化合物与酮和氢反应来制造对应的烷基化芳香族化合物。

Подробнее
27-04-2012 дата публикации

Catalytically activated filter to filtrate hard particles from spent gases of diesel engine having ammonia-retaining action

Номер: RU2449135C2
Принадлежит: Умикоре Аг Унд Ко. Кг

FIELD: engines and pumps. SUBSTANCE: catalytically activated filter designed to filtrate solid particles from spent gases (SG) of a diesel engine and having a filtering element and an oxidising-active catalytic coating, and also one more coating catalytically active in the reaction of selective catalytic reduction (SCR-reaction), containing a material that accumulates ammonia, besides, the specified coatings are arranged in the order, in which SG exposed to neutralisation or reduction of toxicity first go through a coating that is catalytically active in the SCR-reaction, and then through the oxidising-active catalytic coating. EFFECT: simplified and cheaper system of SG neutralisation or toxicity reduction designed to remove nitrogen oxides and solid particles from SG from engines operating at depleted fuel mixtures, and also minimised backpressure of SG. 20 cl, 9 dwg РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) 2 449 135 (13) C2 (51) МПК F01N 3/035 (2006.01) B01D 53/94 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ОПИСАНИЕ ИЗОБРЕТЕНИЯ К ПАТЕНТУ (21)(22) Заявка: 2009135272/06, 28.01.2008 (24) Дата начала отсчета срока действия патента: 28.01.2008 (43) Дата публикации заявки: 27.03.2011 Бюл. № 9 (56) Список документов, цитированных в отчете о поиске: DE 202005008146 U1, 28.07.2005. US 6732507 B1, 11.05.2004. WO 2005064130 A1, 14.07.2005. RU 2212929 C2, 27.09.2003. RU 2108140 C1, 10.04.1998. 2 4 4 9 1 3 5 R U (86) Заявка PCT: EP 2008/000631 (28.01.2008) C 2 C 2 (85) Дата начала рассмотрения заявки PCT на национальной фазе: 23.09.2009 (87) Публикация заявки РСТ: WO 2008/101585 (28.08.2008) Адрес для переписки: 101000, Москва, М. Златоустинский пер., 10, кв. 15, "ЕВРОМАРКПАТ", пат.пов. И.А. Веселицкой, рег. № 0011 (54) КАТАЛИТИЧЕСКИ АКТИВИРОВАННЫЙ ФИЛЬТР ДЛЯ ОТФИЛЬТРОВЫВАНИЯ ТВЕРДЫХ ЧАСТИЦ ИЗ ОТРАБОТАВШИХ ГАЗОВ ДИЗЕЛЬНОГО ДВИГАТЕЛЯ, ОБЛАДАЮЩИЙ ЗАДЕРЖИВАЮЩИМ АММИАК ДЕЙСТВИЕМ (57) Реферат: Изобретение относится к каталитически активированному фильтру для ...

Подробнее
02-08-1977 дата публикации

Hydrocarbon isomerization with increased temperature and lowered hydrogen/hydrocarbon ratio

Номер: US4039604A
Принадлежит: Phillips Petroleum Co

In a process for isomerizing light hydrocarbons with a catalyst system comprising a halogenated alumina or platinum alumina when hydrogen is utilized to sustain the catalyst activity, the ratio of hydrogen to hydrocarbon in the feed is decreased and the temperature increased after a substantial period of operation. This results in an improved conversion and selectivity which allows for increasing the total catalyst life.

Подробнее
11-06-2020 дата публикации

액체상 트랜스알킬화 방법

Номер: KR102121889B1

본 발명은 파라-크실렌 및/또는 다른 크실렌을 형성하기 위해 1-고리 (C 9+ ) 방향족 화합물의 트랜스알킬화, 예컨대 트랜스알킬화에 촉매 방법 및 상응 촉매를 제공한다. 적당한 촉매는 3-D 12원 고리 골격 구조를 갖는 분자체, 1-D 12원 고리 골격 구조를 갖는 분자체, 적어도 6.0 옹스트롬의 기공 채널 크기를 갖는 산성 마이크로다공성 물질, 및/또는 MWW 골격 구조를 갖는 분자체를 포함한다. 방법은 트랜스알킬화 공정에 대한 공급물의 적어도 일부가 액체상인 트랜스알킬화를 수행하는 것을 포함한다. 경우에 따라, 트랜스알킬화 조건은 연속 액체상이 반응 환경 내에 존재하는 조건에 상응할 수 있다. 일부 실시양태는 나프탈렌 함유 공급원료 스트림에 대한 액체상 트랜스알킬화 공정을 포함한다.

Подробнее
11-10-2018 дата публикации

액체상 트랜스알킬화 방법

Номер: KR20180112072A

본 발명은 파라-크실렌 및/또는 다른 크실렌을 형성하기 위해 1-고리 (C 9+ ) 방향족 화합물의 트랜스알킬화, 예컨대 트랜스알킬화에 촉매 방법 및 상응 촉매를 제공한다. 적당한 촉매는 3-D 12원 고리 골격 구조를 갖는 분자체, 1-D 12원 고리 골격 구조를 갖는 분자체, 적어도 6.0 옹스트롬의 기공 채널 크기를 갖는 산성 마이크로다공성 물질, 및/또는 MWW 골격 구조를 갖는 분자체를 포함한다. 방법은 트랜스알킬화 공정에 대한 공급물의 적어도 일부가 액체상인 트랜스알킬화를 수행하는 것을 포함한다. 경우에 따라, 트랜스알킬화 조건은 연속 액체상이 반응 환경 내에 존재하는 조건에 상응할 수 있다. 일부 실시양태는 나프탈렌 함유 공급원료 스트림에 대한 액체상 트랜스알킬화 공정을 포함한다.

Подробнее
25-11-2009 дата публикации

烷基化芳香族化合物的制造方法

Номер: CN101589009A
Принадлежит: Mitsui Chemical Industry Co Ltd

本发明提供用单一反应工序使酮和芳香族化合物直接反应,以更高的收率获得对应的烷基化芳香族化合物的方法。在固体酸物质和以Zn相对于Cu为0.70~1.60(原子比)的比例含有Cu和Zn的催化剂组合物存在下,使芳香族化合物与酮和氢反应来制造对应的烷基化芳香族化合物。

Подробнее
25-01-2019 дата публикации

Method for producing metal-exchanged microporous materials by solid-state ion exchange

Номер: RU2678303C2
Принадлежит: ХАЛЬДОР ТОПСЕЭ А/С

FIELD: separation.SUBSTANCE: invention relates to a method for producing metal-exchanged microporous materials selected from the group consisting of zeolite or zeotype materials having an MFI, BEA or CHA framework structure, or mixtures of said metal-exchanged crystalline microporous materials, and a method for removing nitrogen oxides from exhaust gas by selective catalytic reduction with a reducing agent in the presence of the obtained catalyst. Method for producing a crystalline microporous metal-exchanged material includes steps of providing a dry mixture containing a) one or more crystalline microporous materials that exhibit ion-exchange ability, and b) one or more metal compounds, wherein the metals in the metal compounds are selected from the group of Fe, Co and Cu; heating the mixture in a gaseous atmosphere containing ammonia and one or more nitrogen oxides, oxygen in an amount of 1 vol. % or less and water in an amount of 5 vol. % or less, to a temperature and for a time sufficient for the initiation and implementation of solid-phase ion exchange of the metal compound ions and the ions of the crystalline microporous material; and obtain a metal-exchanged crystalline microporous material. Production of metal-exchanged crystalline microporous materials is significantly improved when solid-state ion exchange is carried out with a physical mixture of oxide and / or metal salt and crystalline microporous material in an atmosphere containing NO and NH.EFFECT: advantage of the present invention is that metal-exchanged microporous material can be obtained at temperatures below 300 °C.13 cl, 7 tbl, 9 ex РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (13) 2 678 303 C2 (51) МПК B01J 37/30 (2006.01) B01J 29/064 (2006.01) B01J 29/85 (2006.01) B01J 29/42 (2006.01) B01D 53/94 (2006.01) B01D 53/56 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ОПИСАНИЕ ИЗОБРЕТЕНИЯ К ПАТЕНТУ (52) СПК B01J 37/30 (2018.08); B01J 29/064 (2018.08); B01J 29/85 (2018.08); B01J 29/42 ( ...

Подробнее
30-09-2016 дата публикации

Carbonylation process using bound silver and/or copper mordenite catalysts

Номер: KR101661781B1
Принадлежит: 비피 케미칼즈 리미티드

은 및/또는 구리가 담지된 모데나이트와 무기 산화물 결합제를 복합화함으로써 형성되는 촉매의 존재 하에, 메틸 아세테이트 및/또는 아세트산을 제조하기 위한, 디메틸 에테르 및/또는 메탄올과 일산화탄소의 카르보닐화 방법. A process for the carbonylation of dimethyl ether and / or methanol and carbon monoxide to produce methyl acetate and / or acetic acid in the presence of a catalyst formed by complexing silver and / or copper-doped mordenite with an inorganic oxide binder.

Подробнее
20-06-2013 дата публикации

Highly selective catalyst for producing high-quality gasoline fractions from synthesis gas and method for production thereof

Номер: RU2484897C1

FIELD: chemistry. SUBSTANCE: invention relates to a catalyst for selective synthesis of high-quality gasoline fractions from synthesis gas and a method for production thereof. Described is a highly selective catalyst for producing high-quality gasoline fractions from synthesis gas, which consists of cobalt, a promoter and a molecular sieve, wherein the weight content of cobalt is 1-30%, the weight content of the promoter is 0.01-5%, and the remaining part is a molecular sieve, with respect to the weight of the catalyst, wherein the molecular sieve is one or more molecular sieves selected from molecular sieves Beta, ZSM-5, MOR, Y and MCM-22, wherein acidity of the molecular sieve is expressed through the amount of adsorbed NH 3 , and the adsorption capacity of the molecular sieve ranges from 0.16 to 0.50 mmol NH 3 /g; the molecular sieve has a microporous-mesoporous structure, wherein the micropores have diameter of 0.4-0.9 nm, and the mesopores have diameter of 2-30 nm, the specific surface area of the molecular sieve is 100-900 m 2 /g and the volume of micropores and mesopores is 0.1-0.6 cm 3 /g, respectively. Described is a method of producing a highly selective catalyst used for synthesis of high-quality gasoline fractions from synthesis gas by Fischer-Tropsch synthesis, involving the following steps: (1) preparing a weighed portion of a cobalt salt according to content of components given above, mixing with a solvent which is deionised water, alcohol or a ketone, to obtain a solution which contains a cobalt salt with concentration of 0.5-20 wt %; (2) preparing a weighed portion of a promoter according to content of components established above, adding to the prepared solution a cobalt salt and stirring for 0.5-3 hours; (3) preparing a weighed portion of a molecular sieve according to content of components established above, adding the molecular sieve to the prepared solution of cobalt salt, stirring for 0.1-15 hours and holding for 0.1-24 hours; (4) evaporating ...

Подробнее
28-05-2021 дата публикации

合成气一步法生产低碳烯烃的方法

Номер: CN109305871B

本发明涉及合成气一步法生产低碳烯烃的方法,主要解决现有技术中存在的合成气一步法制低碳烯烃反应中CO转化率低和低碳烯烃选择性低的问题。本发明采用合成气一步法生产低碳烯烃的方法,包括以合成气为原料,原料与催化剂接触反应生成含C 2 ~C 4 的烯烃,所述催化剂以重量份数计包括以下组分:a)5~40份铁系元素或其氧化物;b)1~20份包括IVB族中的至少一种元素或其氧化物;c)20~70份α‑氧化铝;d)10~40份ZSM‑5型分子筛;其中,ZSM‑5型分子筛为稀土改性ZSM‑5分子筛的技术方案,较好地解决了该问题,可用于合成气一步法制低碳烯烃的工业生产。

Подробнее
27-07-2012 дата публикации

Method for carbonylation of dimethyl ether

Номер: RU2457030C2
Принадлежит: Бп Кемикэлз Лимитед

FIELD: chemistry. SUBSTANCE: invention relates to catalysts for producing methyl acetate and a method of producing methyl acetate. Described is a method of producing methyl acetate, involving carbonylation of dimethyl ether-based material with carbon monoxide with almost no water in the presence of a mordenite catalyst in which at least one of the following elements is introduced using an ion exchange or some other method: silver and copper, and in which platinum is also introduced into the mordenite via an ion exchange or some other method in amount of 0.05-10 mol % with respect to aluminium. Described is a catalyst for producing methyl acetate via carbonylation of dimethyl ether-based material with carbon monoxide in virtually anhydrous conditions, which is prepared via simultaneous ion exchange or saturation of the ammonium or hydrogen form of mordenite with platinum and at least one of the metals - silver and copper, drying and/or calcination of the mordenite which has been saturated or subjected to ion exchange, wherein the catalyst contains platinum in amount of 0.05-10 mol % with respect to aluminium and a catalyst prepared via ion exchange or saturation of the ammonium or hydrogen form of mordenite with at least one of the metals - silver and copper, drying and/or calcination of the mordenite which has been saturated or subjected to ion exchange to obtain copper- and/or silver-containing mordenite, followed by ion exchange or saturation of the copper- and/or silver-containing mordenite with platinum, wherein the catalyst contains platinum in amount of 0.05-10 mol % with respect to aluminium. EFFECT: high catalytic activity. 15 cl, 1 tbl, 2 dwg, 2 ex РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) 2 457 030 (13) C2 (51) МПК B01J B01J C07C C07C 29/22 (2006.01) 29/24 (2006.01) 69/14 (2006.01) 67/37 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ОПИСАНИЕ ИЗОБРЕТЕНИЯ К ПАТЕНТУ (21)(22) Заявка: 2009143553/04, 23.04.2008 (24) Дата начала отсчета срока ...

Подробнее
10-03-2008 дата публикации

Method and the device for reduction of the contents of nitrogen oxides in the gases

Номер: RU2318581C2
Принадлежит: Уде Гмбх

FIELD: chemical industry; other industries; methods and the devices for reduction of the nitrogen oxides content in the technological and effluent gases. SUBSTANCE: the invention is pertaining to the method of reduction of the nitrogen oxides content in the gases, in particular, to the technological and effluent gases and also to the device used for realization of this purpose. The method provides for gating of N 2 O - and NO x -containing gas through the row of two catalyst layers containing one type or some types of zeolites loaded with iron, addition of the reducing agent foe NO x between these layers of the catalyst, maintenance of the temperature less, than 500°C in first layer of the catalyst and in the second layer of the catalyst, maintenance of the gas pressure, at least of 2 bar in both layers of the catalysts, selection of a such volumetric speed flow in the first and second catalyst layers, that in first layer of the catalyst the decomposition of N 2 O till its content of no more then 90 % with the respect to the contents of N 2 O at the inlet of the first layer of the catalyst and set the content of N 2 O more, than 200 parts per million, and that in the second layer of the catalyst the further decomposing of N 2 O contained in the gas, at least, by 30 % with the respect to the contents of N 2 O at the inlet of the second catalyst layer. The device used for reduction of the contents of NO X and N 2 O in the gases, in particular, in the technological gases and the effluent gases includes: two catalyst layers disposed one after another and containing one type or some types of the iron loaded zeolites, through which the gas containing NO X and N 2 O passes. At that the device is disposed between catalyst layers for injection of the gaseous reducing agent in the stream containing NO X and N 2 O of the gas includes the mixer, through which the gas is gated after passing the first layer of the catalyst and including the pipe duct for the reducing agent, which ...

Подробнее
29-04-2022 дата публикации

一种Cs修饰的铁酸钴分子筛多功能型催化剂及其制备方法和应用

Номер: CN114405537A
Автор: 刘爽, 王金果, 秦克叶, 门勇

本发明涉及一种Cs修饰的铁酸钴分子筛多功能型催化剂及其制备方法和应用,催化剂的组成为xCs‑Co y Fe z /H‑ZSM‑5(n),其中x为质量分数,y,z为钴和铁的摩尔量,n为两活性部分的质量比,x=0‑10,y:z=1:(1‑10),n=0‑4。本催化剂通过简单的共沉淀法、浸渍法及物理混合的组合方式制得多功能型催化剂。将本催化剂用于二氧化碳加氢制油品的反应中,CO 2 转化率高达62.1%,CO选择性低于3%,C 2+ 碳氢化合物的选性大于90%,其中C 5+ 选择性大于54%,且有稳定性好、生产周期短、成本低等特点,解决了CO 2 加氢制油品中转化率低和一氧化碳选择性高的问题。

Подробнее
11-06-2021 дата публикации

Organic base-modified composite catalyst and method for synthesis of ethylene by hydrogenation of carbon monoxide

Номер: RU2749513C1

FIELD: chemistry. SUBSTANCE: invention relates to a catalyst for producing ethylene using a synthesis gas reaction, wherein the catalyst contains a component I and a component II; the component I and the component II are combined by means of mechanical stirring; the active component of the component I is a metal oxide with a high specific surface area; the component II constitutes a molecular sieve with a MOR topological structure; in the component II, said molecular sieve with a MOR topological structure is modified with a fatty amine, wherein the modification constitutes dispersing the fatty amines at acid sites B in channels formed by 12-membered rings in said molecular sieve with a MOR topological structure. The invention also relates to a method for highly selective production of ethylene using a synthesis gas reaction. EFFECT: synthesis of low-carbon olefins and achieved selectivity in relation to C 2 -C 3 -olefins - 78 to 87%, ethylene as a separate product - 75 to 82%, methane - less than 9%, alkanes C4 or higher - less than 10%. 9 cl, 5 tbl РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (13) 2 749 513 C1 (51) МПК B01J 29/18 (2006.01) B01J 29/26 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ОПИСАНИЕ ИЗОБРЕТЕНИЯ К ПАТЕНТУ (52) СПК B01J 29/18 (2021.02); B01J 29/26 (2021.02) (21)(22) Заявка: 2020121777, 28.01.2019 (24) Дата начала отсчета срока действия патента: Дата регистрации: Приоритет(ы): (30) Конвенционный приоритет: 26.01.2018 CN 201810079670.5 (56) Список документов, цитированных в отчете о поиске: CN 106345514 А, 25.01.2017. CN 101722034 A, 09.06.2010. CN 105688872 А, 22.06.2016. CN 106311317 A, 11.01.2017. EA 7872 B1, 27.02.2007. (45) Опубликовано: 11.06.2021 Бюл. № 17 (85) Дата начала рассмотрения заявки PCT на национальной фазе: 02.07.2020 (86) Заявка PCT: 2 7 4 9 5 1 3 R U (87) Публикация заявки PCT: WO 2019/144953 (01.08.2019) C 1 C 1 CN 2019/073387 (28.01.2019) 2 7 4 9 5 1 3 (73) Патентообладатель(и): ДАЛЯНЬ ИНСТИТЬЮТ ОФ КЕМИКАЛ ФИЗИКС, ...

Подробнее
04-10-2018 дата публикации

Hydrocracking catalysts for the production of light alkyl-aromatic hydrocarbons, preparation method thereof and method for producing light alkyl-aromatic hydrocarbons using the same

Номер: KR101895497B1

본 발명은 다환 방향족 탄화수소로부터 BTX 함량이 증가된 C 6 -C 9 범위의 경방향족 탄화수소를 제조하는 수소화 분해 반응용 촉매, 이의 제조방법 및 이를 이용한 BTX 함량이 증가된 C 6 -C 9 범위의 경방향족 탄화수소의 제조방법에 관한 것으로, 보다 상세하게는 제올라이트 베타 및 제올라이트 ZSM-5의 복합 제올라이트 담체에 VIII족에서 선택되는 하나 이상의 금속, 및 VIB족에서 선택되는 하나 이상의 금속이 담지된 촉매를 사용함으로써, 나프탈렌, 알킬-나프탈렌 등과 같은 다환 방향족 탄화수소가 포함되어 있는 정유 및 석유화학 공정의 부산물로부터 BTX 함량이 증가된 C 6 -C 9 범위의 경방향족 탄화수소를 높은 수율로 얻는 효과를 달성할 수 있다. The present invention relates to a catalyst for hydrocracking reaction for producing a C 6 -C 9 range light aromatic hydrocarbon having an increased BTX content from polycyclic aromatic hydrocarbons, a process for preparing the same, and a process for producing a C 6 -C 9 range More particularly, the present invention relates to a process for producing aromatic hydrocarbons, and more particularly, to a process for producing aromatic hydrocarbons by using a catalyst in which at least one metal selected from Group VIII and at least one metal selected from Group VIB are supported on a composite zeolite carrier of zeolite beta and zeolite ZSM- , Naphthalene, alkyl-naphthalene, and the like can be obtained in high yield from a by-product of refinery and petrochemical processes containing polycyclic aromatic hydrocarbons, such as naphthalene, alkyl-naphthalene and the like, in the C 6 -C 9 range in which the BTX content is increased.

Подробнее
10-12-2012 дата публикации

Method for carbonylation of dimethyl ether

Номер: RU2469018C2
Принадлежит: Бп Кемикэлз Лимитед

FIELD: chemistry. SUBSTANCE: invention relates to an improved method of increasing catalytic activity when producing methyl acetate, involving carbonylation of dimethyl ether-based material with carbon monoxide in the presence of hydrogen in virtually anhydrous conditions at temperature ranging from more than 250°C to 350°C, in the presence of a zeolite catalyst which is efficient in said carbonylation, wherein concentration of dimethyl ether is at least 1 mol % with respect to the total amount of material. EFFECT: improved method of increasing catalytic activity when producing methyl acetate. 13 cl, 4 ex, 3 tbl, 4 dwg РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) 2 469 018 (13) C2 (51) МПК C07C C07C C07C C07C 67/37 51/09 53/08 69/14 (2006.01) (2006.01) (2006.01) (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ОПИСАНИЕ ИЗОБРЕТЕНИЯ К ПАТЕНТУ (21)(22) Заявка: 2009143549/04, 23.04.2008 (24) Дата начала отсчета срока действия патента: 23.04.2008 (72) Автор(ы): ДИТЦЕЛЬ Эверт Ян (GB), ЛО Дейвид Джон (GB) (73) Патентообладатель(и): БП КЕМИКЭЛЗ ЛИМИТЕД (GB) R U Приоритет(ы): (30) Конвенционный приоритет: 26.04.2007 EP 07251759.2 (43) Дата публикации заявки: 10.06.2011 Бюл. № 16 (56) Список документов, цитированных в отчете о поиске: US 20060287551 А, 21.12.2006. US 20060252959 A1, 09.11.2006. WO 2005/105720 A1, 10.11.2005. US 6387842 B1, 14.05.2002. US 4612387 A, 16.09.1986. RU 2183619 C2, 20.06.2002. CHEUNG, PATRICIA et al. Selective carbonylation of dimethyl ether to methyl acetate catalyzed by acidic zeolites // ANGEWANDTE CHEMIE, INTERNATIONAL EDITION. - 45(10), 1617-1620, 2006. C 2 C 2 2 4 6 9 0 1 8 (45) Опубликовано: 10.12.2012 Бюл. № 34 R U 2 4 6 9 0 1 8 (85) Дата начала рассмотрения заявки PCT на национальной фазе: 26.11.2009 (86) Заявка PCT: GB 2008/001447 (23.04.2008) (87) Публикация заявки РСТ: WO 2008/132450 (06.11.2008) Адрес для переписки: 105082, Москва, Спартаковский пер., д. 2, стр. 1, секция 1, этаж 3, "Евромаркпат", И.А.Веселицкой, рег.№ 11 (54) ...

Подробнее
14-04-2020 дата публикации

负载钯铜合金纳米颗粒的介孔沸石及其制备方法及应用

Номер: CN111001433A
Автор: 路建美, 陈冬赟
Принадлежит: SUZHOU UNIVERSITY

本发明公开了一种新型负载钯铜合金纳米颗粒的介孔沸石(PdCu/MZ)及其制备方法与应用,将介孔沸石前驱体煅烧,得到介孔沸石;所述介孔沸石前驱体由铵盐、铝钠氧化物、碳粉与硅酸盐为原料制备得到;将所述介孔沸石与含有钯盐、铜盐的溶液混合后干燥、煅烧、还原,得到负载钯铜合金纳米颗粒的介孔沸石。本发明通过改变沸石的孔道结构,同时负载金属纳米颗粒,有助于提高其纳米复合材料的催化性能,并且本发明沸石在转化甲苯中还展现出极高的抗失活性。

Подробнее
12-09-2019 дата публикации

Method of producing molecular sieve

Номер: RU2700052C2

FIELD: chemistry. SUBSTANCE: invention relates to synthesis of zeolites. Disclosed is a zeolite mordenite containing a pore inside a pore for forming a structure selected from a group comprising tetraethylammonium (TEA), methyltriethylammonium (MTEA) and mixtures thereof, having a mesopore surface area of more than 30 m 2 /g and up to 62 m 2 /g, and the mesopore surface area to total zeolite surface area ratio of more than 0.05 and up to 0.11. Zeolite contains agglomerates consisting of primary crystallites. Crystallites have a mean primary crystal size determined by transmission electron microscopy of less than 80 nm. Also disclosed is a method of producing zeolite. EFFECT: invention enables to obtain mordenite having fine crystals and a large surface of mesopores. 10 cl, 12 dwg, 1 tbl РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (13) 2 700 052 C2 (51) МПК C01B 39/26 (2006.01) B01J 20/18 (2006.01) B01J 29/04 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ОПИСАНИЕ ИЗОБРЕТЕНИЯ К ПАТЕНТУ (52) СПК C01B 39/26 (2019.02); B01J 20/18 (2019.02); B01J 29/04 (2019.02) (21)(22) Заявка: 2017125266, 21.01.2016 (24) Дата начала отсчета срока действия патента: Дата регистрации: (73) Патентообладатель(и): ЭКСОНМОБИЛ КЕМИКЭЛ ПЕЙТЕНТС ИНК. (US) 12.09.2019 04.02.2015 US 62/111,730; 23.03.2015 EP 15160258.8 (43) Дата публикации заявки: 17.01.2019 Бюл. № 2 (56) Список документов, цитированных в отчете о поиске: WO 00/06492 A1, 10.02.2000. WO 2014/135662 A1, 12.09.2014. RU 2515729 C2, 20.05.2014. RU 2160228 C1, 10.12.2002. (45) Опубликовано: 12.09.2019 Бюл. № 26 (86) Заявка PCT: C 2 C 2 (85) Дата начала рассмотрения заявки PCT на национальной фазе: 14.07.2017 US 2016/014264 (21.01.2016) (87) Публикация заявки PCT: 2 7 0 0 0 5 2 WO 2016/126431 (11.08.2016) R U 2 7 0 0 0 5 2 Приоритет(ы): (30) Конвенционный приоритет: R U 21.01.2016 (72) Автор(ы): ЛАЙ Вэньи Ф. (US), РОЛЛМЕН Николас С. (US), КАО Гуан (US) Адрес для переписки: 105082, Москва, Спартаковский пер., 2, стр. 1, секция 1 ...

Подробнее
22-06-2021 дата публикации

用于合成气生产低碳烯烃的催化剂

Номер: CN109304217B

本发明涉及用于合成气生产低碳烯烃的催化剂,主要解决现有技术中存在的合成气生产低碳烯烃反应中CO转化率低和低碳烯烃选择性低的问题。本发明采用用于合成气生产低碳烯烃的催化剂,以重量份数计包括以下组分:a)20~50份铁元素或其氧化物;b)5~30份包括选自IIB族中的至少一种元素或其氧化物;c)5~30份包括选自VB族中的至少一种元素或其氧化物;d)5~15份包括选自IA族元素中的至少一种元素或其氧化物;e)10~65份包括选自ZSM‑5型分子筛的技术方案,较好地解决了该问题,可用于合成气生产低碳烯烃的工业生产。

Подробнее
21-10-2021 дата публикации

Method for obtaining catalyst based on molybdenum and platinum for benzene synthesis by transalkylation

Номер: RU2757851C2

FIELD: chemistry. SUBSTANCE: invention relates to a method for obtaining a catalyst composition and a method for converting alkylaromatic hydrocarbons, including producing a catalyst composition by the specified method and bringing the mentioned feedstock into contact with the specified catalyst composition The method for obtaining the catalyst composition includes: (a) obtaining a carrier containing (i) mordenite in amount ranging from 30 to 70% by wt. per the total weight of the carrier, (ii) zeolite of ZSM-5 type in amount ranging from 15 to 60% by wt. per the total weight of the carrier; and (iii) an inorganic binder in amount ranging from 10 to 40% by wt. per the total weight of the carrier; (b) introducing molybdenum into the carrier in amount ranging from 2 to 9% by wt. in the form of metal per the total weight of the catalyst composition and affecting the carrier treated in this way with a temperature from 100 to a maximum of 300°C ; and (c) introducing platinum in amount from 0.005 to 0.5% by wt. into the molybdenum-containing carrier obtained at stage (b) per metal relatively to the total weight of the catalyst composition, and affecting the carrier treated in this way with a temperature from 300 to a maximum of 600°C. EFFECT: high degree of purity of benzene, high yield of benzene and high product selectivity at commercially profitable reaction temperatures. 10 cl, 2 tbl, 2 ex РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (13) 2 757 851 C2 (51) МПК B01J 29/80 (2006.01) B01J 29/26 (2006.01) B01J 29/48 (2006.01) B01J 37/02 (2006.01) C07C 6/12 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ОПИСАНИЕ ИЗОБРЕТЕНИЯ К ПАТЕНТУ (52) СПК B01J 29/80 (2021.05); B01J 29/26 (2021.05); B01J 29/48 (2021.05); B01J 29/22 (2021.05); B01J 29/44 (2021.05); B01J 37/0205 (2021.05); C07C 6/12 (2021.05); C07C 2529/00 (2021.05) (21)(22) Заявка: 2019117379, 06.12.2017 06.12.2017 Дата регистрации: Приоритет(ы): (30) Конвенционный приоритет: 08.12.2016 EP 16203011.8 (43) Дата ...

Подробнее
05-10-2017 дата публикации

Catalyst for thermo-catalytic processing of heavy and residual hydrocarbon feedstock

Номер: RU2632467C1

FIELD: oil and gas industry. SUBSTANCE: invention relates to production of heterogeneous catalysts for processing of oil wastes and heavy oil residues (mazut, tar, resin and asphaltene fraction of oil, bitumen, heavy oil) containing zeolite and can be successfully sold to petrochemical and petroleum industries for increasing of oil processing depth and obtaining high-quality liquid and gaseous fuel products. A catalytic converter for thermal and catalytic processing of heavy and residual hydrocarbon feedstocks includes HZSM-5 zeolite and bentonite clay. According to the invention, the catalyst is obtained by mixing components at the following component ratio, wt %: zeolite HZSM-5 30-40; bentonite clay 40-50; calcium carbonate 18-22; metal chloride of iron subgroup 1.8-2.2, followed by annealing the resulting mixture. In addition, nickel chloride, or iron, or cobalt chloride is used as the metal chloride of the iron subgroup. EFFECT: increase of activity and stability of the catalyst and selectivity of the process in the processing of heavy and residual hydrocarbon feedstocks, possibility of regeneration and reduction of catalyst losses during production, storage and use. 2 cl, 2 tbl, 24 ex РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (13) 2 632 467 C1 (51) МПК B01J 29/42 (2006.01) B01J 23/10 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ОПИСАНИЕ ИЗОБРЕТЕНИЯ К ПАТЕНТУ (21)(22) Заявка: 2016143653, 07.11.2016 (24) Дата начала отсчета срока действия патента: 07.11.2016 Дата регистрации: Приоритет(ы): (22) Дата подачи заявки: 07.11.2016 (45) Опубликовано: 05.10.2017 Бюл. № 28 (56) Список документов, цитированных в отчете о поиске: RU 2283177 C2, 10.09.2006. WO 2 6 3 2 4 6 7 R U (54) Катализатор термокаталитической переработки тяжелого и остаточного углеводородного сырья (57) Реферат: Изобретение относится к нефтехимической компонентов, мас.%: промышленности, а именно к области цеолит HZSM-5 30-40 производства гетерогенных катализаторов бентонитовая глина 40-50 ...

Подробнее
10-06-2016 дата публикации

Катализатор селективного окисления соединений серы

Номер: RU2014147010A
Принадлежит: Репсоль С.А.

1. Катализатор селективного окисления соединений, содержащих серу, включающий:- материал носителя, включающий оксид алюминия, диоксид кремния, смешанный оксид алюминия и кремния или их смеси; и- каталитически активный материал, состоящий из оксида кобальта, который нанесен на вышеупомянутый материал носителя;где катализатор имеет следующие свойства:- удельная поверхность, измеряемая азотной порометрией и с использованием метода BET, составляет от 10 до 150 м/г;- пористость, измеряемая методом ртутной порометрии, составляет от 0,05 до 10 см/г;- средний диаметр пор, измеряемый методом ртутной порометрии, составляет от 2 до 50 нм; и- прочность на раздавливание составляет более чем 3 кп (28,43 Н).2. Катализатор по п. 1, где материал носителя включает смешанный оксид алюминия и кремния.3. Катализатор по п. 2, где смешанный оксид алюминия и кремния представляет собой природный цеолит.4. Катализатор по п. 3, где цеолит представляет собой клиноптилолит.5. Катализатор по п. 1, где материал носителя включает оксид алюминия.6. Катализатор по п. 5, где оксид алюминия представляет собой тета-оксид алюминия.7. Катализатор п. 1, где содержание кобальта в катализаторе составляет от 0,05 до 5% и выражено как масса кобальта по отношению к суммарной массе катализатора.8. Катализатор по п. 1, где каталитически активный материал представляет собой смесь CoO и CoOв массовом соотношении, составляющем от 10:1 до 1:10.9. Способ изготовления катализатора по любому из пп. 1-8, включающий пропитывание раствором соли кобальта поверхности материала носителя, включающего оксид алюминия, оксид кремния,смешанный оксид алюминия-кремния или их смеси, а также последующее высушивание и прокаливание катализатора.10. Способ селективного окисления соед РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (51) МПК B01J 21/04 B01J 21/08 B01J 23/75 B01J 29/89 B01J 37/02 C01B 17/04 ФЕДЕРАЛЬНАЯ СЛУЖБА B01D 53/52 ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ B01D 53/86 (12) ЗАЯВКА НА ИЗОБРЕТЕНИЕ (21)(22) Заявка: 2014147010, 23.04.2012 (13) ...

Подробнее