RU2012150425A - ZEOLITE COMPOSITION UZM-35, METHOD FOR PRODUCING AND METHODS OF APPLICATION - Google Patents
ZEOLITE COMPOSITION UZM-35, METHOD FOR PRODUCING AND METHODS OF APPLICATION Download PDFInfo
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- B01J29/00—Catalysts comprising molecular sieves
- B01J29/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
- B01J29/06—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
- B01J29/80—Mixtures of different zeolites
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- B01J29/00—Catalysts comprising molecular sieves
- B01J29/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
- B01J29/06—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
- B01J29/70—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of types characterised by their specific structure not provided for in groups B01J29/08 - B01J29/65
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- C01B39/00—Compounds having molecular sieve and base-exchange properties, e.g. crystalline zeolites; Their preparation; After-treatment, e.g. ion-exchange or dealumination
- C01B39/02—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof; Direct preparation thereof; Preparation thereof starting from a reaction mixture containing a crystalline zeolite of another type, or from preformed reactants; After-treatment thereof
- C01B39/36—Pentasil type, e.g. types ZSM-5, ZSM-8 or ZSM-11
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- C01B39/00—Compounds having molecular sieve and base-exchange properties, e.g. crystalline zeolites; Their preparation; After-treatment, e.g. ion-exchange or dealumination
- C01B39/02—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof; Direct preparation thereof; Preparation thereof starting from a reaction mixture containing a crystalline zeolite of another type, or from preformed reactants; After-treatment thereof
- C01B39/46—Other types characterised by their X-ray diffraction pattern and their defined composition
- C01B39/48—Other types characterised by their X-ray diffraction pattern and their defined composition using at least one organic template directing agent
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- C07C2/00—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms
- C07C2/54—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by addition of unsaturated hydrocarbons to saturated hydrocarbons or to hydrocarbons containing a six-membered aromatic ring with no unsaturation outside the aromatic ring
- C07C2/56—Addition to acyclic hydrocarbons
- C07C2/58—Catalytic processes
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- C07C2/00—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms
- C07C2/54—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by addition of unsaturated hydrocarbons to saturated hydrocarbons or to hydrocarbons containing a six-membered aromatic ring with no unsaturation outside the aromatic ring
- C07C2/64—Addition to a carbon atom of a six-membered aromatic ring
- C07C2/66—Catalytic processes
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- C07C6/00—Preparation of hydrocarbons from hydrocarbons containing a different number of carbon atoms by redistribution reactions
- C07C6/08—Preparation of hydrocarbons from hydrocarbons containing a different number of carbon atoms by redistribution reactions by conversion at a saturated carbon-to-carbon bond
- C07C6/12—Preparation of hydrocarbons from hydrocarbons containing a different number of carbon atoms by redistribution reactions by conversion at a saturated carbon-to-carbon bond of exclusively hydrocarbons containing a six-membered aromatic ring
- C07C6/123—Preparation of hydrocarbons from hydrocarbons containing a different number of carbon atoms by redistribution reactions by conversion at a saturated carbon-to-carbon bond of exclusively hydrocarbons containing a six-membered aromatic ring of only one hydrocarbon
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- C07—ORGANIC CHEMISTRY
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- C07C6/00—Preparation of hydrocarbons from hydrocarbons containing a different number of carbon atoms by redistribution reactions
- C07C6/08—Preparation of hydrocarbons from hydrocarbons containing a different number of carbon atoms by redistribution reactions by conversion at a saturated carbon-to-carbon bond
- C07C6/12—Preparation of hydrocarbons from hydrocarbons containing a different number of carbon atoms by redistribution reactions by conversion at a saturated carbon-to-carbon bond of exclusively hydrocarbons containing a six-membered aromatic ring
- C07C6/126—Preparation of hydrocarbons from hydrocarbons containing a different number of carbon atoms by redistribution reactions by conversion at a saturated carbon-to-carbon bond of exclusively hydrocarbons containing a six-membered aromatic ring of more than one hydrocarbon
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G29/00—Refining of hydrocarbon oils, in the absence of hydrogen, with other chemicals
- C10G29/20—Organic compounds not containing metal atoms
- C10G29/205—Organic compounds not containing metal atoms by reaction with hydrocarbons added to the hydrocarbon oil
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G47/00—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions
- C10G47/02—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions characterised by the catalyst used
- C10G47/10—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions characterised by the catalyst used with catalysts deposited on a carrier
- C10G47/12—Inorganic carriers
- C10G47/16—Crystalline alumino-silicate carriers
- C10G47/20—Crystalline alumino-silicate carriers the catalyst containing other metals or compounds thereof
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G50/00—Production of liquid hydrocarbon mixtures from lower carbon number hydrocarbons, e.g. by oligomerisation
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J29/00—Catalysts comprising molecular sieves
- B01J29/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
- B01J29/06—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
- B01J29/40—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the pentasil type, e.g. types ZSM-5, ZSM-8 or ZSM-11, as exemplified by patent documents US3702886, GB1334243 and US3709979, respectively
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J29/00—Catalysts comprising molecular sieves
- B01J29/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
- B01J29/06—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
- B01J29/50—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the erionite or offretite type, e.g. zeolite T, as exemplified by patent document US2950952
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2529/00—Catalysts comprising molecular sieves
- C07C2529/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites, pillared clays
- C07C2529/06—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
- C07C2529/70—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of types characterised by their specific structure not provided for in groups C07C2529/08 - C07C2529/65
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2400/00—Products obtained by processes covered by groups C10G9/00 - C10G69/14
- C10G2400/02—Gasoline
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- Crystallography & Structural Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Silicates, Zeolites, And Molecular Sieves (AREA)
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Abstract
1. Композиция UZM-35, содержащая цеолит MFI, цеолит ERI, и цеолит MSE, которая обладает трехмерным каркасом, состоящим, по меньшей мере, из тетраэдров AlOи SiOи имеет эмпирический состав свежесинтезированной безводной основы, выражаемый эмпирической формулой:M RAlESiOгде М представляет собой сочетание ионообменных катионов калия и натрия, «m» является мольным отношением М к (Al+Е) и изменяется от около 0,05 до примерно 3, R представляет собой однозарядный катион диметилдипропиламмония, «r» является мольным отношением R к (Al+E) и имеет значение от около 0,25 до примерно 2,0; Е представляет собой элемент, выбранный из группы, состоящей из галлия, железа, бора и их смесей, «х» является мольной долей Е и имеет значение от 0 до примерно 1,0; «y» представляет собой мольное отношение Si к (Al+Е) и изменяется от больше 2 до примерно 12 и «z» является мольным отношением О к (Al+Е) и имеет значение, определяемое уравнением:z=(m+r+3+4·y)/2,отличающаяся тем, что она характеризуется рентгеновской дифрактограммой, включающей, по меньшей мере, d-расстояния и интенсивности, приведенные в таблице А:и является термически стабильной до температуры, равной, по меньшей мере, 400°С.2. Композиция по п.1, в которой «х» равен нулю.3. Композиция по п.1, в которой количество цеолита MSE изменяется от около 55% масс. до примерно 90% масс. в расчете на массу смеси, количество цеолита MFI изменяется от около 10% масс. до примерно 35% масс. в расчете на массу смеси и количество цеолита ERI изменяется от около 3% масс. до примерно 10% масс. в расчете на массу смеси.4. Способ получения композиции UZM-35, содержащей цеолит MFI, цеолит ERI и цеолит MSE, которая обладает трехмерным каркасом, по меньшей мере, из тетраэдров AlOи SiO�1. The composition UZM-35, containing zeolite MFI, zeolite ERI, and zeolite MSE, which has a three-dimensional skeleton, consisting of at least tetrahedra AlO and SiO and has the empirical composition of a freshly synthesized anhydrous base, expressed by the empirical formula: M RAlESiO where M is a combination ion exchange cations of potassium and sodium, “m” is the molar ratio of M to (Al + E) and varies from about 0.05 to about 3, R is the singly charged dimethyldipropylammonium cation, “r” is the molar ratio of R to (Al + E) and has a value of from about 0.25 to at measured 2.0; E is an element selected from the group consisting of gallium, iron, boron and mixtures thereof, “x” is the mole fraction of E and has a value from 0 to about 1.0; “Y” is the molar ratio of Si to (Al + E) and varies from more than 2 to about 12 and “z” is the molar ratio of O to (Al + E) and has the value defined by the equation: z = (m + r + 3 + 4 · y) / 2, characterized in that it is characterized by an X-ray diffraction pattern including at least the d-distances and intensities shown in Table A: and is thermally stable to a temperature of at least 400 ° C.2. The composition of claim 1, wherein “x” is zero. 3. The composition according to claim 1, in which the amount of zeolite MSE varies from about 55% of the mass. up to about 90% of the mass. based on the weight of the mixture, the amount of zeolite MFI varies from about 10% of the mass. up to about 35% of the mass. based on the weight of the mixture and the amount of zeolite ERI varies from about 3% of the mass. up to about 10% of the mass. based on the weight of the mixture. 4. A method of obtaining a UZM-35 composition containing MFI zeolite, ERI zeolite and MSE zeolite, which has a three-dimensional skeleton of at least AlO and SiO� tetrahedra
Claims (9)
Applications Claiming Priority (1)
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PCT/US2010/039380 WO2011162741A1 (en) | 2010-06-21 | 2010-06-21 | Uzm-35 zeolitic composition, method of preparation and processes |
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RU2012150425A true RU2012150425A (en) | 2014-06-10 |
RU2525417C2 RU2525417C2 (en) | 2014-08-10 |
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RU2012150425/05A RU2525417C2 (en) | 2010-06-21 | 2010-06-21 | Uzm-35 zeolite composition, method of production and methods of use |
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EP (1) | EP2582626A4 (en) |
JP (1) | JP2013534896A (en) |
CN (1) | CN102947224A (en) |
RU (1) | RU2525417C2 (en) |
WO (1) | WO2011162741A1 (en) |
Families Citing this family (13)
Publication number | Priority date | Publication date | Assignee | Title |
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US8993821B2 (en) * | 2012-12-18 | 2015-03-31 | Uop Llc | Hydrocarbon processes using UZM-43 an EUO-NES-NON zeolite |
US9193600B1 (en) * | 2014-06-04 | 2015-11-24 | Chevron U. S. A. Inc. | Method for making molecular sieve SSZ-99 |
US9409786B2 (en) * | 2014-07-03 | 2016-08-09 | Chevron U.S.A. Inc. | Molecular sieve SSZ-98 |
US10010878B2 (en) * | 2015-03-03 | 2018-07-03 | Uop Llc | High meso-surface area, low Si/Al ratio pentasil zeolite |
KR101795404B1 (en) * | 2016-05-18 | 2017-11-08 | 현대자동차 주식회사 | Catalyst and manufacturing method of catalyst |
JP6966087B2 (en) * | 2016-09-29 | 2021-11-10 | 国立大学法人横浜国立大学 | Zeolites and their manufacturing methods |
US10272420B2 (en) * | 2016-10-06 | 2019-04-30 | Uop Llc | Composition of matter and structure of zeolite UZM-55 |
CN110740973B (en) * | 2017-06-15 | 2023-05-30 | 三菱化学株式会社 | Method for separating ammonia and zeolite |
SG11201911569RA (en) * | 2017-07-27 | 2020-02-27 | Exxonmobil Res & Eng Co | Emm-23 materials and processes and uses thereof |
CA3086339A1 (en) * | 2017-12-21 | 2019-06-27 | Exxonmobil Research And Engineering Company | Emm-31 materials and processes and uses thereof |
WO2020038222A1 (en) | 2018-08-24 | 2020-02-27 | Rhodia Operations | A microporous aluminotitanosilicate crystalline zeolite, method of preparation and applications thereof |
CA3118464A1 (en) * | 2018-11-01 | 2020-05-07 | Exxonmobil Research And Engineering Company | Highly siliceous form of zeolite rho |
CN112973475A (en) * | 2019-12-14 | 2021-06-18 | 中国科学院大连化学物理研究所 | Method for preparing UZM series zeolite molecular sieve membrane by seed crystal method and application |
Family Cites Families (13)
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DE3136684A1 (en) * | 1981-09-16 | 1983-04-21 | Hoechst Ag, 6230 Frankfurt | "GALLIUM- AND / OR INDIUM-CONTAINING ZEOLITES AND METHOD FOR THE PRODUCTION THEREOF AND THEIR USE" |
US6049018A (en) * | 1999-01-21 | 2000-04-11 | Mobil Corporation | Synthetic porous crystalline MCM-68, its synthesis and use |
US6419895B1 (en) * | 2000-11-03 | 2002-07-16 | Uop Llc | Crystalline aluminosilicate zeolitic composition: UZM-4 |
US6890511B2 (en) * | 2003-03-21 | 2005-05-10 | Uop Llc | Crystalline aluminosilicate zeolitic composition: UZM-15 |
JP4733641B2 (en) * | 2003-09-23 | 2011-07-27 | ユーオーピー エルエルシー | Crystalline aluminosilicates: UZM-13, UZM-17, UZM-19 and UZM-25 |
WO2005042149A1 (en) * | 2003-10-31 | 2005-05-12 | Uop Llc | A process for preparing crystalline aluminosilicate compositions using charge density matching |
EP1742737A1 (en) * | 2004-04-20 | 2007-01-17 | Uop Llc | Catalyst for selective opening of cyclic paraffins and process for using the catalyst |
EP1756004B1 (en) * | 2004-04-23 | 2010-08-18 | Uop Llc | High silica zeolites uzm-5hs |
US7344694B2 (en) * | 2004-10-06 | 2008-03-18 | Uop Llc | UZM-12 and UZM-12HS: crystalline aluminosilicate zeolitic compositions and processes for preparing and using the compositions |
US7744850B2 (en) * | 2006-08-03 | 2010-06-29 | Uop Llc | UZM-22 aluminosilicate zeolite, method of preparation and processes using UZM-22 |
JP4954854B2 (en) * | 2007-11-22 | 2012-06-20 | ユーオーピー エルエルシー | Method for preparing layered molecular sieve composition |
US7922997B2 (en) * | 2008-09-30 | 2011-04-12 | Uop Llc | UZM-35 aluminosilicate zeolite, method of preparation and processes using UZM-35 |
US7575737B1 (en) * | 2008-12-18 | 2009-08-18 | Uop Llc | UZM-27 family of crystalline aluminosilicate compositions and a method of preparing the compositions |
-
2010
- 2010-06-21 WO PCT/US2010/039380 patent/WO2011162741A1/en active Application Filing
- 2010-06-21 RU RU2012150425/05A patent/RU2525417C2/en not_active IP Right Cessation
- 2010-06-21 JP JP2013516550A patent/JP2013534896A/en active Pending
- 2010-06-21 EP EP10853784.6A patent/EP2582626A4/en not_active Withdrawn
- 2010-06-21 CN CN2010800673919A patent/CN102947224A/en active Pending
Also Published As
Publication number | Publication date |
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WO2011162741A1 (en) | 2011-12-29 |
RU2525417C2 (en) | 2014-08-10 |
CN102947224A (en) | 2013-02-27 |
EP2582626A4 (en) | 2016-04-06 |
JP2013534896A (en) | 2013-09-09 |
EP2582626A1 (en) | 2013-04-24 |
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