ES2097863T3 - Aditivo de octano para una zeolita mejorada. - Google Patents
Aditivo de octano para una zeolita mejorada.Info
- Publication number
- ES2097863T3 ES2097863T3 ES92250316T ES92250316T ES2097863T3 ES 2097863 T3 ES2097863 T3 ES 2097863T3 ES 92250316 T ES92250316 T ES 92250316T ES 92250316 T ES92250316 T ES 92250316T ES 2097863 T3 ES2097863 T3 ES 2097863T3
- Authority
- ES
- Spain
- Prior art keywords
- zeolite
- gasoline
- group
- additive
- loss
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
- 239000000654 additive Substances 0.000 title abstract 4
- 230000000996 additive effect Effects 0.000 title abstract 3
- TVMXDCGIABBOFY-UHFFFAOYSA-N octane Chemical compound CCCCCCCC TVMXDCGIABBOFY-UHFFFAOYSA-N 0.000 title abstract 3
- 229910021536 Zeolite Inorganic materials 0.000 title abstract 2
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 title abstract 2
- 239000010457 zeolite Substances 0.000 title abstract 2
- 239000003054 catalyst Substances 0.000 abstract 2
- 239000011148 porous material Substances 0.000 abstract 2
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 abstract 1
- 150000001768 cations Chemical class 0.000 abstract 1
- 239000000463 material Substances 0.000 abstract 1
- 239000011159 matrix material Substances 0.000 abstract 1
- 230000000737 periodic effect Effects 0.000 abstract 1
Classifications
-
- 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
- C10G11/00—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
- C10G11/02—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils characterised by the catalyst used
- C10G11/04—Oxides
- C10G11/05—Crystalline alumino-silicates, e.g. molecular sieves
-
- 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
-
- 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
- B01J29/405—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 containing rare earth elements, titanium, zirconium, hafnium, zinc, cadmium, mercury, gallium, indium, thallium, tin or lead
-
- 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
- B01J29/80—Mixtures of different zeolites
-
- 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
- B01J2229/00—Aspects of molecular sieve catalysts not covered by B01J29/00
- B01J2229/10—After treatment, characterised by the effect to be obtained
- B01J2229/26—After treatment, characterised by the effect to be obtained to stabilize the total catalyst structure
-
- 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
- B01J2229/00—Aspects of molecular sieve catalysts not covered by B01J29/00
- B01J2229/30—After treatment, characterised by the means used
- B01J2229/36—Steaming
-
- 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
- B01J2229/00—Aspects of molecular sieve catalysts not covered by B01J29/00
- B01J2229/30—After treatment, characterised by the means used
- B01J2229/42—Addition of matrix or binder particles
-
- 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
- B01J29/65—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the ferrierite type, e.g. types ZSM-21, ZSM-35 or ZSM-38, as exemplified by patent documents US4046859, US4016245 and US4046859, respectively
-
- 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
- B01J29/70—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of types characterised by their specific structure not provided for in groups B01J29/08 - B01J29/65
Landscapes
- Chemical & Material Sciences (AREA)
- Crystallography & Structural Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Materials Engineering (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- General Chemical & Material Sciences (AREA)
- Catalysts (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
CUANDO SE AÑADE UNA COMPOSICION ADITIVA DE ZEOLITA DE UNA ZEOLITA DE PORO MEDIANO CON UN INDICE DE LIGADURA ENTRE 1 Y 12 APROXIMADAMENTE Y UNA RELACION MOLAR DE SILICE A ALUMINA MAYOR DE 12 A UNA CATALIZADOR DE CRACKING CONVENCIONAL DISPERSO EN UNA MATRIZ INORGANICA, EL OCTANO MEJORARA, PERO HABRA UNA PERDIDA EN LA CANTIDAD DE GASOLINA PRODUCIDA. UNA MEJORA EN ESE SISTEMA CATALIZADOR SE OBTIENE A BASE DE INTERCAMBIAR EL ADITIVO DE ZEOLITA DE PORO MEDIANO CON CATIONES DE UNO O MAS ELEMENTOS DEL GRUPO IA, DEL GRUPO IIA O DEL GRUPO IIIA DE LA TABLA PERIODICA. EL NUMERO DE OCTANO DEL PRODUCTO DENTRO DE LA GAMA DE LA GASOLINA DE UN PROCESO FCC SE SIGUE MEJORANDO MIENTRAS QUE LA CANTIDAD DE PERDIDA EN LA PRODUCCION DE GASOLINA TIPICAMENTE OBSERVADO PARA TALES ADITIVOS AUMENTADORES DEL OCTANO SE REDUCE.
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US07/787,170 US5302567A (en) | 1991-11-04 | 1991-11-04 | Zeolite octane additive |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| ES2097863T3 true ES2097863T3 (es) | 1997-04-16 |
Family
ID=25140625
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| ES92250316T Expired - Lifetime ES2097863T3 (es) | 1991-11-04 | 1992-11-02 | Aditivo de octano para una zeolita mejorada. |
Country Status (5)
| Country | Link |
|---|---|
| US (2) | US5302567A (es) |
| EP (1) | EP0541191B1 (es) |
| JP (1) | JPH05214347A (es) |
| DE (1) | DE69217610T2 (es) |
| ES (1) | ES2097863T3 (es) |
Families Citing this family (23)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5308475A (en) * | 1992-11-23 | 1994-05-03 | Mobil Oil Corporation | Use of ZSM-12 in catalytic cracking for gasoline octane improvement and co-production of light olefins |
| CN1102634C (zh) * | 1997-10-15 | 2003-03-05 | 中国石油化工集团公司 | 催化热裂解制取低碳烯烃催化剂 |
| NO318036B1 (no) | 1997-10-15 | 2005-01-24 | Res Inst Petroleum Processing | Katalysator for katalytisk pyrolyseprosess for fremstilling av lette olefiner og fremgangsmate for fremstilling derav |
| US6852214B1 (en) * | 1998-08-31 | 2005-02-08 | Mobil Oil Corporation | Gasoline sulfur reduction in fluid catalytic cracking |
| AU1727800A (en) * | 1998-11-24 | 2000-06-13 | Mobil Oil Corporation | Catalytic cracking for olefin production |
| US7803267B2 (en) * | 1998-12-28 | 2010-09-28 | W. R. Grace & Co.-Conn. | Gasoline sulfur reduction in fluid catalytic cracking |
| US6726834B2 (en) * | 1999-10-22 | 2004-04-27 | Intevep, S.A. | Process for catalytic cracking of a hydrocarbon feed with a MFI aluminisilcate composition |
| US6740236B2 (en) | 2001-09-25 | 2004-05-25 | Kuss Corporation | Fuel filter assembly having a conductive spring |
| KR100599251B1 (ko) * | 2003-09-20 | 2006-07-13 | 에스케이 주식회사 | 디메틸에테르 합성용 촉매와 촉매의 제조방법 |
| US20050227853A1 (en) * | 2004-04-02 | 2005-10-13 | Ranjit Kumar | Catalyst compositions comprising metal phosphate bound zeolite and methods of using same to catalytically crack hydrocarbons |
| US20100010279A1 (en) * | 2004-04-02 | 2010-01-14 | Ranjit Kumar | Catalyst Compositions Comprising Metal Phosphate Bound Zeolite and Methods of Using Same to Catalytically Crack Hydrocarbons |
| EP1609840A1 (en) * | 2004-06-25 | 2005-12-28 | Indian Oil Corporation Limited | Process for conversion of hydrocarbons to saturated lpg and high octane gasoline |
| CN1322928C (zh) * | 2004-08-13 | 2007-06-27 | 中国石油化工股份有限公司 | 一种降低催化裂化汽油烯烃含量的裂化催化剂 |
| CN100344374C (zh) * | 2004-08-13 | 2007-10-24 | 中国石油化工股份有限公司 | 一种稀土y分子筛及其制备方法 |
| TWI379711B (en) * | 2004-11-05 | 2012-12-21 | Grace W R & Co | Catalyst for light olefins and lpg in fluidized catalytic cracking units |
| ES2730002T3 (es) * | 2005-06-29 | 2019-11-07 | Grace W R & Co | Catalizador de pentasil para olefinas ligeras en unidades catalíticas fluidizadas |
| BRPI0705179B1 (pt) | 2007-10-10 | 2016-10-11 | Petróleo Brasileiro S A Petrobras | aditivo para maximizar olefinas leves em fcc e processo para preparação do mesmo |
| CN104981290A (zh) * | 2012-12-21 | 2015-10-14 | 阿尔比马尔欧洲有限公司 | 增加丙烯产量的改良y型沸石/zsm-5催化剂 |
| WO2016199164A1 (en) * | 2015-06-09 | 2016-12-15 | Hindustan Petroleum Corporation Ltd. | Catalyst composition for fluid catalytic cracking, and use thereof |
| EP3135373A1 (en) | 2015-08-24 | 2017-03-01 | INDIAN OIL CORPORATION Ltd. | Preparation and composition of a fluid catalytic cracking catalyst additive with lower phosphate content for enhanced lpg yield |
| US10413889B2 (en) | 2015-11-24 | 2019-09-17 | Indian Oil Corporation Limited | Composition and process for preparation of cracking catalyst suitable for enhancing yields of light olefins |
| US20220259505A1 (en) * | 2019-08-05 | 2022-08-18 | Sabic Global Technologies B.V. | A method for catalytic cracking of hydrocarbons to produce olefins and aromatics without steam as diluent |
| EP3800232A3 (en) | 2019-10-04 | 2021-06-30 | Indian Oil Corporation Limited | Fluid catalytic cracking additive composition for enhancing gasoline octane barrel and a process of preparation thereof |
Family Cites Families (28)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3140249A (en) * | 1960-07-12 | 1964-07-07 | Socony Mobil Oil Co Inc | Catalytic cracking of hydrocarbons with a crystalline zeolite catalyst composite |
| US3352796A (en) * | 1962-09-11 | 1967-11-14 | Exxon Research Engineering Co | Catalyst for hydrocarbon conversions |
| US3293192A (en) * | 1965-08-23 | 1966-12-20 | Grace W R & Co | Zeolite z-14us and method of preparation thereof |
| USRE28629E (en) * | 1966-12-19 | 1975-11-25 | Ion exchange of crystalline zeolites | |
| US3647718A (en) * | 1969-03-25 | 1972-03-07 | Engelhard Min & Chem | Microspherical zeolitic molecular sieve composite catalyst and preparation thereof |
| US3758403A (en) * | 1970-10-06 | 1973-09-11 | Mobil Oil | Olites catalytic cracking of hydrocarbons with mixture of zsm-5 and other ze |
| US3758402A (en) * | 1970-10-06 | 1973-09-11 | Mobil Oil Corp | Catalytic hydrocracking of hydrocarbons |
| US3894933A (en) * | 1974-04-02 | 1975-07-15 | Mobil Oil Corp | Method for producing light fuel oil |
| US3894931A (en) * | 1974-04-02 | 1975-07-15 | Mobil Oil Corp | Method for improving olefinic gasoline product of low conversion fluid catalytic cracking |
| US4061724A (en) * | 1975-09-22 | 1977-12-06 | Union Carbide Corporation | Crystalline silica |
| US4137152A (en) * | 1977-11-10 | 1979-01-30 | Mobil Oil Corporation | Selective high conversion cracking process |
| US4899007A (en) * | 1979-01-31 | 1990-02-06 | Mobil Oil Corporation | Aromatic conversion reactions with zeolitic catalyst composition of improved shape selectivity |
| US4289606A (en) * | 1979-05-31 | 1981-09-15 | Exxon Research & Engineering Co. | Hydrocarbon cracking with mixture of zeolites Y and ZSM-5 |
| US4309279A (en) * | 1979-06-21 | 1982-01-05 | Mobil Oil Corporation | Octane and total yield improvement in catalytic cracking |
| US4614578A (en) * | 1979-06-21 | 1986-09-30 | Mobil Oil Corporation | Octane and total yield improvement in catalytic cracking |
| US4368114A (en) * | 1979-12-05 | 1983-01-11 | Mobil Oil Corporation | Octane and total yield improvement in catalytic cracking |
| US4309280A (en) * | 1980-07-18 | 1982-01-05 | Mobil Oil Corporation | Promotion of cracking catalyst octane yield performance |
| US4340465A (en) * | 1980-09-29 | 1982-07-20 | Chevron Research Company | Dual component crystalline silicate cracking catalyst |
| NZ205859A (en) * | 1982-10-15 | 1986-04-11 | Mobil Oil Corp | Organic conversion using zeolite catalyst |
| US4493902A (en) * | 1983-02-25 | 1985-01-15 | Engelhard Corporation | Fluid catalytic cracking catalyst comprising microspheres containing more than about 40 percent by weight Y-faujasite and methods for making |
| US4581341A (en) * | 1983-11-23 | 1986-04-08 | Engelhard Corporation | Method for producing cracking catalyst |
| US4522705A (en) * | 1984-06-13 | 1985-06-11 | Mobil Oil Corporation | Octane enhancement and total liquid product yield improvements in catalytic cracking using in-situ crystallized ZSM-5 clay aggregates |
| US4740292A (en) * | 1985-09-12 | 1988-04-26 | Mobil Oil Corporation | Catalytic cracking with a mixture of faujasite-type zeolite and zeolite beta |
| US4752375A (en) * | 1986-09-03 | 1988-06-21 | Mobil Oil Corporation | Single riser fluidized catalytic cracking process utilizing a C3-4 paraffin-rich co-feed and mixed catalyst system |
| US4818738A (en) * | 1987-12-09 | 1989-04-04 | Mobil Oil Corp. | High equilibrium activity additive catalyst for catalytic cracking |
| US4929337A (en) * | 1988-12-30 | 1990-05-29 | Mobil Oil Corporation | Process for catalytic cracking of heavy hydrocarbon feed to lighter products |
| GB9012725D0 (en) * | 1990-06-07 | 1990-08-01 | Exxon Chemical Patents Inc | Process for catalytic conversion of olefins |
| US5318696A (en) * | 1992-12-11 | 1994-06-07 | Mobil Oil Corporation | Catalytic conversion with improved catalyst catalytic cracking with a catalyst comprising a large-pore molecular sieve component and a ZSM-5 component |
-
1991
- 1991-11-04 US US07/787,170 patent/US5302567A/en not_active Expired - Lifetime
-
1992
- 1992-10-28 JP JP4311091A patent/JPH05214347A/ja active Pending
- 1992-11-02 DE DE69217610T patent/DE69217610T2/de not_active Expired - Fee Related
- 1992-11-02 EP EP92250316A patent/EP0541191B1/en not_active Expired - Lifetime
- 1992-11-02 ES ES92250316T patent/ES2097863T3/es not_active Expired - Lifetime
-
1993
- 1993-12-16 US US08/167,307 patent/US5382351A/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| EP0541191A2 (en) | 1993-05-12 |
| US5382351A (en) | 1995-01-17 |
| EP0541191A3 (en) | 1993-06-30 |
| DE69217610T2 (de) | 1997-07-17 |
| JPH05214347A (ja) | 1993-08-24 |
| US5302567A (en) | 1994-04-12 |
| DE69217610D1 (de) | 1997-04-03 |
| EP0541191B1 (en) | 1997-02-26 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| FG2A | Definitive protection |
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