JP2007516837A - C8アルキル芳香族化合物異性化のための方法及び触媒 - Google Patents
C8アルキル芳香族化合物異性化のための方法及び触媒 Download PDFInfo
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- B01J23/38—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
- B01J23/40—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals of the platinum group metals
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- 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
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- B01J21/12—Silica and alumina
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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
- B01J29/70—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of types characterised by their specific structure not provided for in groups B01J29/08 - B01J29/65
- B01J29/72—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of types characterised by their specific structure not provided for in groups B01J29/08 - B01J29/65 containing iron group metals, noble metals or copper
- B01J29/74—Noble metals
- B01J29/7469—MTW-type, e.g. ZSM-12, NU-13, TPZ-12 or Theta-3
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- C07C5/00—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms
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- 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
- C07C5/2767—Changing the number of side-chains
- C07C5/277—Catalytic processes
- C07C5/2775—Catalytic processes with crystalline alumino-silicates, e.g. molecular sieves
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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
- B01J2229/00—Aspects of molecular sieve catalysts not covered by B01J29/00
- B01J2229/10—After treatment, characterised by the effect to be obtained
- B01J2229/20—After treatment, characterised by the effect to be obtained to introduce other elements in the catalyst composition comprising the molecular sieve, but not specially in or on the molecular sieve itself
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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
- 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
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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
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/0009—Use of binding agents; Moulding; Pressing; Powdering; Granulating; Addition of materials ameliorating the mechanical properties of the product catalyst
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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
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/20—Sulfiding
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2521/00—Catalysts comprising the elements, oxides or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium or hafnium
- C07C2521/02—Boron or aluminium; Oxides or hydroxides thereof
- C07C2521/04—Alumina
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2521/00—Catalysts comprising the elements, oxides or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium or hafnium
- C07C2521/06—Silicon, titanium, zirconium or hafnium; Oxides or hydroxides thereof
- C07C2521/08—Silica
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2523/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00
- C07C2523/38—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of noble metals
- C07C2523/40—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of noble metals of the platinum group metals
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2523/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00
- C07C2523/38—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of noble metals
- C07C2523/40—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of noble metals of the platinum group metals
- C07C2523/42—Platinum
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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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- 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
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Crystallography & Structural Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
- Catalysts (AREA)
Abstract
【選択図】 なし
Description
トルエン 0.2
C8非芳香族化合物 8.3
エチルベンゼン 26.8
パラ−キシレン 0.9
メタ−キシレン 42.4
オルソ−キシレン 21.0
C9 +非芳香族化合物 0.4
触媒 A B
温度℃ 386 371
パラ−キシレン/キシレン 22.5 22.3
EB転化、重量% 31 38
ベンゼン収率、重量% 0.25 0.10
C8環ロス 2.5 2.5
C8非芳香族化合物 7
エチルベンゼン 16
パラ−キシレン <1
メタ−キシレン 52
オルソ−キシレン 25
触媒 C D E F
パラ−キシレン/キシレン 22.3 22.3 22.3 22.3
C8環ロス 2.6 3.3 3.6 5.4
従って、触媒Cは環ロスが最低で、触媒D〜Fはモルデナイト不純物レベルと共にモル%環ロスの増大を示した。そうした循環はコストが高くつくので、C8環ロスの低さはモルデナイト不純物をほとんど含まないMTWを用いた本発明の触媒の好ましい特徴である。
Claims (9)
- C8環ロスを最低に抑えつつエチルベンゼンをキシレンに安定的に異性化するための触媒であって、この触媒は元素ベースで計算して0.1〜2重量%のプラチナ族成分、基本的にモルデナイトを含まず、シリカ対アルミナのモル比が45以下である1〜90重量%のMTW型ゼオライト成分、及び無機酸化物結合材成分を含むことを特徴とする触媒。
- 元素ベースで計算して0.01〜5重量%のIVA族成分(IUPAC14)をさらに含んでいることを特徴とする請求項1記載の触媒。
- 上記IVA族成分(IUPAC14)が錫であることを特徴とする請求項2記載の触媒。
- さらに0.05〜1.0重量%の硫黄を含むことを特徴とする請求項1又は2記載の触媒。
- 上記MTW型ゼオライト成分の含有量が2〜20重量%であることを特徴とする請求項1又は2記載の触媒。
- 上記MTW型ゼオライト成分が20対40のシリカ対アルミナ比を有していることを特徴とする請求項1又は2記載の触媒。
- 上記無機酸化物結合材成分がアルミナとシリカの1種又は両方を含んでいることを特徴とする請求項1又は2記載の触媒。
- 上記MTW型ゼオライト成分が最大で20重量%のモルデナイトを含んでいることを特徴とする請求項1又は2記載の触媒。
- キシレンとエチルベンゼンを含む供給原料混合物を異性化するための方法において、異性化ゾーン内で水素の存在下、300℃から500℃の範囲の温度、1〜50気圧の圧力、0.5〜10毎時の液体時間空間速度、そして0.5:1〜25:1の範囲の水素対炭化水素モル比を含む異性化条件で、上記供給原料混合物を請求項1又は2記載の触媒と接触させて、供給原料混合物に対するC8環ロスを4モル%以下に抑えて、キシレンの割合が上記供給原料中の割合より多く含んでいる異性化生成物を得ることを特徴とする方法。
Applications Claiming Priority (5)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US10/749,156 US20050143614A1 (en) | 2003-12-30 | 2003-12-30 | Process and catalyst for C8 alkylaromatic isomerization |
US10/749,179 | 2003-12-30 | ||
US10/749,156 | 2003-12-30 | ||
US10/749,179 US20050143615A1 (en) | 2003-12-30 | 2003-12-30 | Process and bimetallic catalyst for C8 alkylaromatic isomerization |
PCT/US2004/043952 WO2005065380A2 (en) | 2003-12-30 | 2004-12-29 | Process and catalyst for c8 alkylaromatic isomerization |
Publications (3)
Publication Number | Publication Date |
---|---|
JP2007516837A true JP2007516837A (ja) | 2007-06-28 |
JP2007516837A5 JP2007516837A5 (ja) | 2008-01-31 |
JP4939947B2 JP4939947B2 (ja) | 2012-05-30 |
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ID=34753191
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Application Number | Title | Priority Date | Filing Date |
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JP2006547574A Expired - Fee Related JP4939947B2 (ja) | 2003-12-30 | 2004-12-29 | C8アルキル芳香族化合物異性化のための方法及び触媒 |
Country Status (6)
Country | Link |
---|---|
US (1) | US7525008B2 (ja) |
EP (1) | EP1699556A2 (ja) |
JP (1) | JP4939947B2 (ja) |
KR (1) | KR100991482B1 (ja) |
CN (1) | CN100512954C (ja) |
WO (1) | WO2005065380A2 (ja) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2009090285A (ja) * | 2007-10-08 | 2009-04-30 | Uop Llc | 芳香族異性化触媒 |
JP2013523632A (ja) * | 2010-03-31 | 2013-06-17 | ユーオーピー エルエルシー | Uzm−35を用いるキシレン及びエチルベンゼンの異性化方法 |
JP2014533269A (ja) * | 2011-11-14 | 2014-12-11 | ユーオーピー エルエルシー | デュアル触媒系を用いた芳香族異性体化 |
Families Citing this family (20)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US7297830B2 (en) * | 2005-09-14 | 2007-11-20 | Uop Llc | Process for isomerizing non-equilibrium xylene-containing feed streams |
WO2007114127A1 (ja) * | 2006-03-29 | 2007-10-11 | Toray Industries, Inc. | エチルベンゼンの転化方法およびパラキシレンの製造方法 |
FR2909906B1 (fr) | 2006-12-13 | 2009-02-06 | Inst Francais Du Petrole | Procede d'isomerisation des composes c8 aromatiques en presence d'un catalyseur comprenant une zeolithe euo modifiee |
FR2915113B1 (fr) | 2007-04-23 | 2009-06-26 | Inst Francais Du Petrole | Zeolithe eu-1 modifiee et son utilisation en isomerisation des composes c8 aromatiques. |
FR2915112B1 (fr) | 2007-04-23 | 2009-11-20 | Inst Francais Du Petrole | Procede d'isomerisation d'une coupe c8 aromatique en presence d'un catalyseur a base d'une zeolithe euo desaluminee. |
US7629283B2 (en) * | 2007-10-08 | 2009-12-08 | Uop Llc | Aromatic isomerization catalyst and isomerization process |
US20090143218A1 (en) * | 2007-12-03 | 2009-06-04 | Bogdan Paula L | Regeneration process for a c8 alkylaromatic isomerization catalyst |
CN102199066B (zh) * | 2010-03-25 | 2014-05-28 | 中国石油化工股份有限公司 | 一种烷基芳烃异构化方法 |
US8138385B2 (en) | 2010-03-31 | 2012-03-20 | Uop Llc | Process for xylene and ethylbenzene isomerization using UZM-35HS |
US8071831B1 (en) | 2010-06-21 | 2011-12-06 | Uop Llc | Process for xylene and ethylbenzene isomerization using UZM-35 |
FR2974801B1 (fr) * | 2011-05-04 | 2013-04-26 | IFP Energies Nouvelles | Procede d'isomerisation d'une coupe c8 aromatique en presence d'un catalyseur specifique constitue par un composite de type zeolithe/carbure de silicium et d'une fonction hydro-deshydrogenante |
US8889937B2 (en) | 2011-06-09 | 2014-11-18 | Uop Llc | Process for producing one or more alkylated aromatics |
FR2984308B1 (fr) * | 2011-12-20 | 2013-12-20 | IFP Energies Nouvelles | Procede d'isomerisation d'une coupe c8 aromatique en presence d'un catalyseur a base d'une zeolithe euo et d'un liant particulier |
US9018121B2 (en) | 2012-02-29 | 2015-04-28 | Exxonmobil Chemicals Patents Inc. | Bimetallic catalyst and use in xylene production |
CN103483137B (zh) * | 2012-06-11 | 2016-05-25 | 中国石油化工股份有限公司 | 一种乙苯转化为苯和对二甲苯的方法 |
FR3054454B1 (fr) | 2016-07-26 | 2020-04-10 | IFP Energies Nouvelles | Catalyseur comprenant une zeolithe izm-2 ayant un rapport molaire si/al optimise pour l'isomerisation de coupes c8 aromatiques |
FR3059325B1 (fr) | 2016-11-30 | 2019-01-25 | IFP Energies Nouvelles | Utilisation d'un catalyseur a base de zeolithe izm-2 et d'un catalyseur a base de zeolithe euo pour l'isomerisation de coupes c8 aromatiques |
FR3104458B1 (fr) | 2019-12-17 | 2022-01-07 | Ifp Energies Now | Catalyseur a base de zeolithe izm-2 ayant une teneur en alcalin faible et son utilisation pour l’isomerisation de la coupe c8 aromatique |
CN114433218B (zh) * | 2020-10-30 | 2024-03-15 | 中国石油化工股份有限公司 | 一种苯和合成气烷基化催化剂及其制备方法和应用 |
CN113880110B (zh) * | 2021-10-25 | 2023-01-03 | 南昌大学 | 一种纳米多级孔mor/mtw共晶分子筛及其制备方法和应用 |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS4928181B1 (ja) * | 1968-06-24 | 1974-07-24 | Universal Oil Prod Co | |
JPS55129232A (en) * | 1979-03-29 | 1980-10-06 | Teijin Yuka Kk | Isomerization of xylenes |
US4962259A (en) * | 1987-10-16 | 1990-10-09 | Uop | Catalyst for isomerizing alkylaromatics |
Family Cites Families (31)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
NL76445C (ja) | 1950-03-08 | |||
US3201491A (en) | 1962-09-05 | 1965-08-17 | Universal Oil Prod Co | Continuous sorption process with emphasis on product purity |
US3626020A (en) | 1969-03-12 | 1971-12-07 | Universal Oil Prod Co | Separation of paraxylene from mixture of c aromatic utilizing crystalline aluminosilicate adsorbent |
US3832449A (en) | 1971-03-18 | 1974-08-27 | Mobil Oil Corp | Crystalline zeolite zsm{14 12 |
US3696107A (en) | 1971-05-27 | 1972-10-03 | Richard W Neuzil | Improved hydrocarbon separation process |
US3856871A (en) | 1973-09-13 | 1974-12-24 | Mobil Oil Corp | Xylene isomerization |
US3856872A (en) | 1973-09-13 | 1974-12-24 | Mobil Oil Corp | Xylene isomerization |
US4016219A (en) | 1975-08-22 | 1977-04-05 | Mobil Oil Corporation | Disproportionation of toluene |
US4097543A (en) | 1976-05-12 | 1978-06-27 | Mobil Oil Corporation | Selective disproportionation of toluene |
US4039599A (en) | 1976-08-26 | 1977-08-02 | Uop Inc. | Xylene isomerization process |
US4268420A (en) | 1978-04-18 | 1981-05-19 | Standard Oil Company (Indiana) | Hydrocarbon-conversion catalyst and its method of preparation |
US4184943A (en) | 1978-12-21 | 1980-01-22 | Uop Inc. | Fractionation in an adsorptive hydrocarbon separation process |
US4452769A (en) | 1979-03-21 | 1984-06-05 | Mobil Oil Corporation | Method of preparing crystalline zeolite |
US4537758A (en) | 1979-03-21 | 1985-08-27 | Mobil Oil Corporation | Process for preparing highly siliceous porous ZSM-12 type crystalline material |
ZA801627B (en) * | 1979-03-21 | 1981-03-25 | Mobil Oil Corp | Method of preparing zsm-12 |
US4341914A (en) | 1980-12-22 | 1982-07-27 | Uop Inc. | Transalkylation process with recycle of C10 hydrocarbons |
US4381419A (en) | 1981-04-22 | 1983-04-26 | Exxon Research & Engineering Co. | Adsorption-desorption separation process with integrated light and heavy desorbents |
US4402832A (en) | 1982-08-12 | 1983-09-06 | Uop Inc. | High efficiency continuous separation process |
US4899011A (en) | 1986-01-15 | 1990-02-06 | Mobil Oil Corporation | Xylene isomerization process to exhaustively convert ethylbenzene and non-aromatics |
US5081084A (en) * | 1987-10-16 | 1992-01-14 | Uop | Catalyst for isomerizing alkylaromatics |
US4943424A (en) | 1988-02-12 | 1990-07-24 | Chevron Research Company | Synthesis of a crystalline silicoaluminophosphate |
US5744673A (en) | 1988-03-30 | 1998-04-28 | Uop | Activated zeolite beta and its use for hydrocarbon conversion |
US4899012A (en) | 1988-10-17 | 1990-02-06 | Uop | Catalyst for the isomerization of aromatics |
US4962258A (en) | 1988-12-15 | 1990-10-09 | Amoco Corporation | Liquid-phase xylene isomerization |
CA2174045C (en) | 1995-04-24 | 2003-01-28 | John Ivor Hammerman | C8 aromatics isomerization using catalyst containing modified silicoaluminophosphate molecular sieve |
US6057486A (en) | 1997-12-22 | 2000-05-02 | Institut Francais Du Petrole | Catalyst containing a zeolite EUO and the use of the catalyst in a process for isomerizing aromatic compounds containing 8 carbon atoms per molecule |
FR2772751B1 (fr) | 1997-12-22 | 2000-04-14 | Inst Francais Du Petrole | Catalyseur a base de mordenite contenant au moins un metal du groupe viii et au moins un metal des groupes iii et iv et son utilisation en isomerisation d'une coupe c8 aromatique |
US6143941A (en) | 1999-03-03 | 2000-11-07 | Uop Llc | Selective xylenes isomerization and ethylbenzene conversion |
US6652832B2 (en) | 2001-02-05 | 2003-11-25 | Exxonmobil Oil Corporation | Synthesis of ZSM-12 |
US6797849B2 (en) | 2002-11-01 | 2004-09-28 | Exxonmobil Chemical Patents Inc. | Xylene isomerization |
US6872866B1 (en) | 2003-12-15 | 2005-03-29 | Uop Llc | Liquid phase process for C8 alkylaromatic isomerization |
-
2004
- 2004-12-29 EP EP04815941A patent/EP1699556A2/en not_active Withdrawn
- 2004-12-29 WO PCT/US2004/043952 patent/WO2005065380A2/en active Application Filing
- 2004-12-29 JP JP2006547574A patent/JP4939947B2/ja not_active Expired - Fee Related
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Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS4928181B1 (ja) * | 1968-06-24 | 1974-07-24 | Universal Oil Prod Co | |
JPS55129232A (en) * | 1979-03-29 | 1980-10-06 | Teijin Yuka Kk | Isomerization of xylenes |
US4962259A (en) * | 1987-10-16 | 1990-10-09 | Uop | Catalyst for isomerizing alkylaromatics |
Cited By (3)
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JP2009090285A (ja) * | 2007-10-08 | 2009-04-30 | Uop Llc | 芳香族異性化触媒 |
JP2013523632A (ja) * | 2010-03-31 | 2013-06-17 | ユーオーピー エルエルシー | Uzm−35を用いるキシレン及びエチルベンゼンの異性化方法 |
JP2014533269A (ja) * | 2011-11-14 | 2014-12-11 | ユーオーピー エルエルシー | デュアル触媒系を用いた芳香族異性体化 |
Also Published As
Publication number | Publication date |
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KR20070004603A (ko) | 2007-01-09 |
CN100512954C (zh) | 2009-07-15 |
KR100991482B1 (ko) | 2010-11-04 |
WO2005065380A3 (en) | 2005-11-24 |
EP1699556A2 (en) | 2006-09-13 |
JP4939947B2 (ja) | 2012-05-30 |
CN1901991A (zh) | 2007-01-24 |
US7525008B2 (en) | 2009-04-28 |
WO2005065380A2 (en) | 2005-07-21 |
US20050277796A1 (en) | 2005-12-15 |
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