ES2155538T3 - Isomerizacion de xileno en doble lecho. - Google Patents
Isomerizacion de xileno en doble lecho.Info
- Publication number
- ES2155538T3 ES2155538T3 ES95941529T ES95941529T ES2155538T3 ES 2155538 T3 ES2155538 T3 ES 2155538T3 ES 95941529 T ES95941529 T ES 95941529T ES 95941529 T ES95941529 T ES 95941529T ES 2155538 T3 ES2155538 T3 ES 2155538T3
- Authority
- ES
- Spain
- Prior art keywords
- catalyst
- ethylbenzene
- isomerization
- zeolite
- xomene
- 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
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C15/00—Cyclic hydrocarbons containing only six-membered aromatic rings as cyclic parts
- C07C15/02—Monocyclic hydrocarbons
- C07C15/067—C8H10 hydrocarbons
- C07C15/08—Xylenes
-
- 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
- B01J29/42—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 iron group metals, noble metals or copper
- B01J29/44—Noble metals
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C15/00—Cyclic hydrocarbons containing only six-membered aromatic rings as cyclic parts
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C15/00—Cyclic hydrocarbons containing only six-membered aromatic rings as cyclic parts
- C07C15/02—Monocyclic hydrocarbons
- C07C15/067—C8H10 hydrocarbons
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C4/00—Preparation of hydrocarbons from hydrocarbons containing a larger number of carbon atoms
- C07C4/08—Preparation of hydrocarbons from hydrocarbons containing a larger number of carbon atoms by splitting-off an aliphatic or cycloaliphatic part from the molecule
- C07C4/12—Preparation of hydrocarbons from hydrocarbons containing a larger number of carbon atoms by splitting-off an aliphatic or cycloaliphatic part from the molecule from hydrocarbons containing a six-membered aromatic ring, e.g. propyltoluene to vinyltoluene
- C07C4/14—Preparation of hydrocarbons from hydrocarbons containing a larger number of carbon atoms by splitting-off an aliphatic or cycloaliphatic part from the molecule from hydrocarbons containing a six-membered aromatic ring, e.g. propyltoluene to vinyltoluene splitting taking place at an aromatic-aliphatic bond
- C07C4/18—Catalytic processes
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C5/00—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms
- C07C5/22—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by isomerisation
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C5/00—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms
- C07C5/22—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by isomerisation
- C07C5/27—Rearrangement of carbon atoms in the hydrocarbon skeleton
- C07C5/2702—Catalytic processes not covered by C07C5/2732 - C07C5/31; Catalytic processes covered by both C07C5/2732 and C07C5/277 simultaneously
- C07C5/2708—Catalytic processes not covered by C07C5/2732 - C07C5/31; Catalytic processes covered by both C07C5/2732 and C07C5/277 simultaneously with 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
- B01J2229/00—Aspects of molecular sieve catalysts not covered by B01J29/00
- B01J2229/10—After treatment, characterised by the effect to be obtained
- B01J2229/12—After treatment, characterised by the effect to be obtained to alter the outside of the crystallites, e.g. selectivation
-
- 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
-
- 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
-
- 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
- C07C2529/40—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the pentasil type, e.g. types ZSM-5, ZSM-8 or ZSM-11
-
- 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
- C07C2529/65—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the ferrierite type, e.g. types ZSM-21, ZSM-35 or ZSM-38
-
- 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
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/52—Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Crystallography & Structural Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Materials Engineering (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Catalysts (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
Abstract
UNA MEZCLA DE HIDROCARBUROS AROMATICOS, QUE COMPRENDE ETILBENCENO Y AL MENOS UN XILENO, ES ISOMERIZADA MEDIANTE UN SISTEMA CATALIZADOR DE DOS COMPONENTES PARA CONVERTIR EL ETILBENCENO EN COMPUESTOS QUE PUEDEN SER ELIMINADOS DE LA CORRIENTE DE HIDROCARBURO AROMATICO Y PRODUCIR UNA CORRIENTE DE PRODUCTO EN DONDE LA CONCENTRACION DE PARA-XILENO ES APROXIMADAMENTE IGUAL A LA PROPORCION DE EQUILIBRIO DEL PARAISOMERO. EL PRIMER CATALIZADOR COMPRENDE UNA ZEOLITA CON TAMAÑO DE PORO INTERMEDIO QUE ES EFICAZ PARA CONVERSION DE ETILBENCENO. EL PRIMER CATALIZADOR ES PREFERIBLEMENTE SILICE LIGADO. EL SEGUNDO CATALIZADOR COMPRENDE UNA ZEOLITA CON TAMAÑO DE PORO INTERMEDIO, QUE ADEMAS TIENE UN TAMAÑO DE CRISTAL PEQUEÑO Y QUE ES EFICAZ PARA CATALIZAR ISOMERIZACION DE XILENO. CADA UNO DE LOS CATALIZADORES DE ESTA INVENCION PUEDE CONTENER UNO O MAS COMPONENTES DE HIDROGENACION/DESHIDROGENACION.
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US08/342,322 US5516956A (en) | 1994-11-18 | 1994-11-18 | Dual bed xylene isomerization |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| ES2155538T3 true ES2155538T3 (es) | 2001-05-16 |
Family
ID=23341323
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| ES95941529T Expired - Lifetime ES2155538T3 (es) | 1994-11-18 | 1995-11-16 | Isomerizacion de xileno en doble lecho. |
Country Status (8)
| Country | Link |
|---|---|
| US (1) | US5516956A (es) |
| EP (1) | EP0792251B1 (es) |
| JP (1) | JP3857311B2 (es) |
| KR (1) | KR100369429B1 (es) |
| CA (1) | CA2203365C (es) |
| DE (1) | DE69520592T2 (es) |
| ES (1) | ES2155538T3 (es) |
| WO (1) | WO1996016005A1 (es) |
Families Citing this family (47)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5476823A (en) * | 1993-05-28 | 1995-12-19 | Mobil Oil Corp. | Method of preparation of ex situ selectivated zeolite catalysts for enhanced shape selective applications and method to increase the activity thereof |
| US5698756A (en) * | 1993-05-28 | 1997-12-16 | Mobil Oil Corporation | Toluene alkylation with ethylene to produce para-ethyloluene |
| US5659098A (en) * | 1993-05-28 | 1997-08-19 | Beck; Jeffrey S. | High conversion touluene disproportionation with ex situ selectivated zeolite catalysts |
| US5689027A (en) * | 1994-11-18 | 1997-11-18 | Mobil Oil Corporation | Selective ethylbenzene conversion |
| US5705726A (en) * | 1994-11-18 | 1998-01-06 | Mobil Oil Corporation | Xylene isomerization on separate reactors |
| US5625104A (en) * | 1995-06-06 | 1997-04-29 | Mobil Oil Corporation | Alkali metal ion exchanged selectivated zeolite catalyst |
| IN192640B (es) * | 1995-03-06 | 2004-05-08 | Toray Industries | |
| US5849968A (en) * | 1995-06-06 | 1998-12-15 | Mobil Oil Corporation | Hydrocarbon conversion process with alkaline earth metal ion exchanged selectivated zeolite catalyst |
| AU714275B2 (en) * | 1996-01-25 | 1999-12-23 | Exxon Research And Engineering Company | Separation process in which a membrane is used |
| ID18446A (id) * | 1996-05-29 | 1998-04-09 | Exxon Chemical Patents Inc | Proses untuk isomerisasi hidrokarbon-hidrokarbon alkilaromatik |
| DE69729797T2 (de) * | 1996-05-29 | 2004-12-02 | Exxonmobil Chemical Patents Inc., Baytown | Zeolitischer katalysator und seine verwendung bei der kohlenwasserstoffumsetzung |
| US5877379A (en) * | 1996-08-19 | 1999-03-02 | Phillips Petroleum Company | Olefin conversion process involving coke suppressor impregnated catalyst |
| US5968343A (en) * | 1997-05-05 | 1999-10-19 | Phillips Petroleum Company | Hydrocarbon conversion catalyst composition and processes therefor and therewith |
| US5905051A (en) * | 1997-06-04 | 1999-05-18 | Wu; An-Hsiang | Hydrotreating catalyst composition and processes therefor and therewith |
| US6207871B1 (en) | 1997-12-19 | 2001-03-27 | Mobil Oil Corporation | High-purity meta-xylene production process |
| US6028238A (en) * | 1998-04-14 | 2000-02-22 | Mobil Oil Corporation | Xylene isomerization |
| US5998688A (en) * | 1998-08-25 | 1999-12-07 | Mobil Oil Corporation | Xylene isomerization process using toluene co-feed |
| US5977420A (en) * | 1998-08-25 | 1999-11-02 | Mobil Oil Corporation | Dual-loop xylene isomerization process |
| US6709570B1 (en) * | 1999-09-27 | 2004-03-23 | Shell Oil Company | Method for preparing a catalyst |
| US7271305B2 (en) * | 2003-05-01 | 2007-09-18 | Bp Corporation North America Inc. | Method of obtaining para-xylene |
| US7122496B2 (en) * | 2003-05-01 | 2006-10-17 | Bp Corporation North America Inc. | Para-xylene selective adsorbent compositions and methods |
| US7067052B2 (en) * | 2003-07-01 | 2006-06-27 | Exxonmobil Chemical Patents Inc. | Process for the production of reformate having reduced ethylbenzene content |
| US7247762B2 (en) * | 2003-09-12 | 2007-07-24 | Exxonmobil Chemical Patents Inc. | Process for xylene isomerization and ethylbenzene conversion |
| US7271118B2 (en) * | 2004-07-29 | 2007-09-18 | Exxonmobil Chemical Patents Inc. | Xylenes isomerization catalyst system and use thereof |
| EP2027917A1 (en) * | 2007-07-31 | 2009-02-25 | Shell Internationale Researchmaatschappij B.V. | Catalyst composition, its preparation and use |
| US20100004493A1 (en) * | 2008-07-02 | 2010-01-07 | Porter John R | Integrated Process |
| US8575055B2 (en) * | 2010-03-30 | 2013-11-05 | Uop Llc | Surface-modified zeolites and methods for preparing the same |
| US9604204B2 (en) * | 2010-04-19 | 2017-03-28 | Shell Oil Company | Process for the preparation of a catalyst support |
| KR20130056357A (ko) * | 2010-10-29 | 2013-05-29 | 엑손모빌 케미칼 패턴츠 인코포레이티드 | 파라자일렌의 제조 방법 |
| WO2013032630A2 (en) | 2011-08-31 | 2013-03-07 | Exxonmobil Chemical Patents Inc. | Production of paraxylene |
| US9260360B2 (en) | 2012-12-05 | 2016-02-16 | Exxonmobil Chemical Patents Inc. | Manufacturing process |
| US10661258B2 (en) * | 2013-06-13 | 2020-05-26 | Exxonmobil Chemical Patents Inc. | In-situ trim coke selectivation of toluene disproportionation catalyst |
| WO2016003612A1 (en) | 2014-06-30 | 2016-01-07 | Exxonmobil Chemical Patents Inc. | Processes for the production of para-xylene |
| WO2016003613A2 (en) | 2014-06-30 | 2016-01-07 | Exxonmobil Chemical Patents Inc. | Process for the production of xylenes |
| US9302953B2 (en) | 2014-06-30 | 2016-04-05 | Exxonmobil Chemicals Patents Inc. | Process for the production of xylenes |
| US9469579B2 (en) | 2014-06-30 | 2016-10-18 | Exxonmobil Chemical Patents Inc. | Process for the production of xylenes |
| CN110790625B (zh) * | 2014-08-15 | 2022-09-06 | 埃克森美孚化学专利公司 | 芳族烃的生产方法 |
| US9708233B2 (en) | 2014-08-15 | 2017-07-18 | Exxonmobil Chemical Patents Inc. | Aromatics production process |
| EP3368501B1 (en) * | 2015-10-28 | 2021-04-28 | Ineos Us Chemicals Company | Improved catalyst for ethylbenzene conversion in a xylene isomerization process |
| US9809509B2 (en) | 2015-12-15 | 2017-11-07 | Exxonmobil Chemical Patents Inc. | Process for xylenes isomerization |
| WO2017105617A1 (en) | 2015-12-15 | 2017-06-22 | Exxonmobil Chemical Patents Inc. | Process for xylenes isomerization |
| US10710060B2 (en) | 2016-07-13 | 2020-07-14 | Shell Oil Company | Catalyst composition comprising con-type zeolite and zsm-5-type zeolite, preparation and process using such composition |
| CN109790082B (zh) * | 2016-10-06 | 2022-02-25 | 国际壳牌研究有限公司 | 烷基芳烃转化催化剂 |
| WO2021048693A1 (en) * | 2019-09-10 | 2021-03-18 | Sabic Global Technologies B.V. | Aromatization catalyst with improved isomerization, reactor configurations and use thereof |
| US10927057B1 (en) * | 2020-01-06 | 2021-02-23 | Uop Llc | Two bed liquid phase isomerization process |
| CN117358297B (zh) * | 2022-07-01 | 2026-03-24 | 中国石油化工股份有限公司 | 一种芳烃转化催化剂及制备方法 |
| CN118847227B (zh) * | 2024-07-08 | 2025-03-07 | 北京化工大学 | 一种用于低浓度co2还原的光催化剂的制备方法及应用 |
Family Cites Families (21)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4090981A (en) * | 1976-09-23 | 1978-05-23 | Mobile Oil Corporation | Catalyst for selective production of para dialkyl substituted benzenes |
| US4117026A (en) * | 1976-05-12 | 1978-09-26 | Mobil Oil Corporation | Selective production of para dialkyl substituted benzenes |
| US4163028A (en) * | 1977-07-22 | 1979-07-31 | Mobil Oil Corporation | Xylene isomerization |
| USRE31782E (en) * | 1978-06-09 | 1984-12-25 | Mobil Oil Corporation | Xylene isomerization |
| US4312790A (en) * | 1980-04-14 | 1982-01-26 | Mobil Oil Corporation | Aromatics processing catalysts |
| US4560820A (en) * | 1981-04-13 | 1985-12-24 | Chevron Research Company | Alkylaromatic dealkylation |
| US4477583A (en) * | 1983-06-09 | 1984-10-16 | Mobil Oil Corporation | Silica-modified catalyst and use for selective production of para-dialkyl substituted benzenes |
| US4465886A (en) * | 1983-06-09 | 1984-08-14 | Mobil Oil Corporation | Silica-modified catalyst and use for selective production of para-dialkyl substituted benzenes |
| US4582815A (en) * | 1984-07-06 | 1986-04-15 | Mobil Oil Corporation | Extrusion of silica-rich solids |
| US4783568A (en) * | 1985-09-13 | 1988-11-08 | Uop Inc. | Xylene producing process having staged catalytic conversion of ethylbenzene |
| US4899011A (en) * | 1986-01-15 | 1990-02-06 | Mobil Oil Corporation | Xylene isomerization process to exhaustively convert ethylbenzene and non-aromatics |
| US5053374A (en) * | 1987-05-01 | 1991-10-01 | Mobil Oil Corporation | Method for preparing a zeolite catalyst bound with a refractory oxide of low acidity |
| US5004855A (en) * | 1987-08-25 | 1991-04-02 | Toray Industries, Inc. | Process for conversion of ethylbenzene in C8 aromatic hydrocarbon mixture |
| US4950835A (en) * | 1989-10-24 | 1990-08-21 | Taiwan Styrene Monomer Corporation | Novel silicon-modified catalyst Si/HZSM-5, it's preparation, and a process for synthesizing high purity p-dialkyl benzene from monoalkyl benzene by using said catalyst |
| US5321183A (en) * | 1992-03-12 | 1994-06-14 | Mobil Oil Corp. | Process for the regioselective conversion of aromatics to para-disubstituted benzenes |
| US5365003A (en) * | 1993-02-25 | 1994-11-15 | Mobil Oil Corp. | Shape selective conversion of hydrocarbons over extrusion-modified molecular sieve |
| US5371312A (en) * | 1993-04-05 | 1994-12-06 | Mobil Oil Corp. | Shape selective hydrocarbon conversions over modified catalyst |
| US5349114A (en) * | 1993-04-05 | 1994-09-20 | Mobil Oil Corp. | Shape selective hydrocarbon conversions over modified catalyst |
| US5382737A (en) * | 1993-05-28 | 1995-01-17 | Mobil Oil Corp. | Selective ethylbenzene disproportionation process (SEBDP) with ex situ selectivated zeolite catalysts |
| US5367099A (en) * | 1993-05-28 | 1994-11-22 | Mobil Oil Corp. | Selective toluene disproportionation process (STDP) with ex situ selectivated zeolite catalyst |
| US5365004A (en) * | 1993-05-28 | 1994-11-15 | Mobil Oil Corp. | Selective toluene disproportionation process (STDP) with ex situ selectivated zeolite catalysts |
-
1994
- 1994-11-18 US US08/342,322 patent/US5516956A/en not_active Expired - Lifetime
-
1995
- 1995-11-16 KR KR1019970703266A patent/KR100369429B1/ko not_active Expired - Lifetime
- 1995-11-16 WO PCT/US1995/016006 patent/WO1996016005A1/en not_active Ceased
- 1995-11-16 DE DE69520592T patent/DE69520592T2/de not_active Expired - Fee Related
- 1995-11-16 EP EP95941529A patent/EP0792251B1/en not_active Expired - Lifetime
- 1995-11-16 JP JP51711796A patent/JP3857311B2/ja not_active Expired - Lifetime
- 1995-11-16 ES ES95941529T patent/ES2155538T3/es not_active Expired - Lifetime
- 1995-11-16 CA CA002203365A patent/CA2203365C/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| WO1996016005A1 (en) | 1996-05-30 |
| US5516956A (en) | 1996-05-14 |
| KR100369429B1 (ko) | 2003-04-10 |
| JPH10509720A (ja) | 1998-09-22 |
| EP0792251A1 (en) | 1997-09-03 |
| DE69520592T2 (de) | 2001-07-12 |
| JP3857311B2 (ja) | 2006-12-13 |
| EP0792251B1 (en) | 2001-04-04 |
| CA2203365C (en) | 2007-06-26 |
| CA2203365A1 (en) | 1996-05-30 |
| EP0792251A4 (en) | 1997-11-19 |
| DE69520592D1 (de) | 2001-05-10 |
| KR970707062A (ko) | 1997-12-01 |
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