RU97114955A - METHOD FOR CONVERTING AROMATIC HYDROCARBONS - Google Patents

METHOD FOR CONVERTING AROMATIC HYDROCARBONS

Info

Publication number
RU97114955A
RU97114955A RU97114955/04A RU97114955A RU97114955A RU 97114955 A RU97114955 A RU 97114955A RU 97114955/04 A RU97114955/04 A RU 97114955/04A RU 97114955 A RU97114955 A RU 97114955A RU 97114955 A RU97114955 A RU 97114955A
Authority
RU
Russia
Prior art keywords
zeolite
catalytic composition
preceding paragraphs
treated
aromatic hydrocarbons
Prior art date
Application number
RU97114955/04A
Other languages
Russian (ru)
Other versions
RU2148573C1 (en
Inventor
Скотт Баканан Джон
Варрен Честер Артур
Лун Энтони Фунг Шиу
Фредерик Кинн Тимоти
Мизрахи Сади
Original Assignee
Мобил Ойл Корпорейшн
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Мобил Ойл Корпорейшн filed Critical Мобил Ойл Корпорейшн
Priority claimed from PCT/US1996/001818 external-priority patent/WO1996024568A1/en
Publication of RU97114955A publication Critical patent/RU97114955A/en
Application granted granted Critical
Publication of RU2148573C1 publication Critical patent/RU2148573C1/en

Links

Claims (14)

1. Способ конвертирования ароматических углеводородов С9+ в более легкие ароматические продукты, отличающийся тем, что включает стадию контактирования сырья, содержащего ароматические углеводороды С9+, бензол и/или толуол, с каталитической композицией, содержащей цеолит, имеющий показатель реакции связи от 0,5 до 3, и гидрирующий компонент, для получения продукта, содержащего ксилолы, в котором каталитическую композицию, имеющую гидрирующий компонент, обрабатывают для снижения его активности гидрирования ароматических соединений.1. A method of converting C9 + aromatic hydrocarbons into lighter aromatic products, characterized in that it comprises the step of contacting a feed containing C9 + aromatic hydrocarbons, benzene and / or toluene with a catalytic composition containing a zeolite having a bond reaction rate of from 0.5 to 3 and a hydrogenation component, to obtain a product containing xylenes, in which a catalytic composition having a hydrogenation component is processed to reduce its hydrogenation activity of aromatic compounds. 2. Способ по п.1, отличающийся тем, что каталитическую композицию обрабатывают острым паром. 2. The method according to claim 1, characterized in that the catalytic composition is treated with hot steam. 3. Способ по п.2, отличающийся тем, что стадию обработки острым паром осуществляют при условиях, включающих атмосферу от 5 до 100 5 пара и температуру 500 - 1200oF (260 - 665oC).3. The method according to claim 2, characterized in that the stage of treatment with hot steam is carried out under conditions including an atmosphere of 5 to 100 5 steam and a temperature of 500 - 1200 o F (260 - 665 o C). 4. Способ по п.1, отличающийся тем, что каталитическую композицию обрабатывают источником серы или азота. 4. The method according to claim 1, characterized in that the catalytic composition is treated with a source of sulfur or nitrogen. 5. Способ по п.1, отличающийся тем, что каталитическую композицию обрабатывают источником элемента Группы IВ. 5. The method according to claim 1, characterized in that the catalytic composition is treated with a source of an element of Group IB. 6. Способ по п.5, отличающийся тем, что элементом Группы IВ является медь. 6. The method according to claim 5, characterized in that the element of Group IB is copper. 7. Способ по любому из предшествующих пунктов, отличающийся тем, что стадию контактирования осуществляют при парциальном давлении водорода 100 - 3000 кПа. 7. The method according to any one of the preceding paragraphs, characterized in that the contacting step is carried out at a partial pressure of hydrogen of 100 to 3000 kPa. 8. Способ по любому из предшествующих пунктов, отличающийся тем, что цеолит выбирают из гриппы, включающей цеолит бета, ZSM-12 и МСМ-22. 8. The method according to any one of the preceding paragraphs, characterized in that the zeolite is selected from influenza, including zeolite beta, ZSM-12 and MSM-22. 9. Способ по любому из предшествующих пунктов, отличающийся тем, что гидрирующим компонентом является металл, выбранный из группы VIII Периодической таблицы элементов. 9. The method according to any one of the preceding paragraphs, characterized in that the hydrogenating component is a metal selected from group VIII of the Periodic table of elements. 10. Способ по п.9, отличающийся тем, что гидрирующим компонентом является благородный металл. 10. The method according to claim 9, characterized in that the hydrogenating component is a noble metal. 11. Способ по п.10, отличающийся тем, что благородным металлом является платина. 11. The method according to claim 10, characterized in that the noble metal is platinum. 12. Способ по п. 10, отличающийся тем, что цеолитом является ZSM-12 и благородным металлом является платина. 12. The method according to p. 10, characterized in that the zeolite is ZSM-12 and the noble metal is platinum. 13. Способ по п.9, отличающийся тем, что цеолитом является цеолит бета и гидрирующим компонентом является молибден. 13. The method according to claim 9, characterized in that the zeolite is zeolite beta and the hydrogenating component is molybdenum. 14. Способ по любому из предшествующих пунктов, отличающийся тем, что бензол и/или толуол составляют по крайней мере около 40 - 90% по объему общего перерабатываемого сырья. 14. The method according to any one of the preceding paragraphs, characterized in that the benzene and / or toluene comprise at least about 40 to 90% by volume of the total processed raw materials.
RU97114955/04A 1995-02-10 1996-02-09 Aromatic hydrocarbon conversion process RU2148573C1 (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
US38689295A 1995-02-10 1995-02-10
US08/386,892 1995-02-10
PCT/US1996/001818 WO1996024568A1 (en) 1995-02-10 1996-02-09 Heavy aromatics processing

Publications (2)

Publication Number Publication Date
RU97114955A true RU97114955A (en) 1999-06-27
RU2148573C1 RU2148573C1 (en) 2000-05-10

Family

ID=23527506

Family Applications (1)

Application Number Title Priority Date Filing Date
RU97114955/04A RU2148573C1 (en) 1995-02-10 1996-02-09 Aromatic hydrocarbon conversion process

Country Status (15)

Country Link
US (1) US5763720A (en)
EP (1) EP0808299B1 (en)
JP (1) JP3773530B2 (en)
KR (1) KR100404990B1 (en)
CN (1) CN1080248C (en)
AR (1) AR001083A1 (en)
AU (1) AU710073B2 (en)
BR (1) BR9607590A (en)
DE (1) DE69612279T2 (en)
ES (1) ES2155185T3 (en)
PT (1) PT808299E (en)
RU (1) RU2148573C1 (en)
TW (1) TW504501B (en)
WO (1) WO1996024568A1 (en)
ZA (1) ZA961124B (en)

Families Citing this family (76)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP3554804B2 (en) * 1995-05-25 2004-08-18 新日本石油株式会社 Catalyst for conversion of aromatic hydrocarbon compound and conversion method
US5942651A (en) * 1997-06-13 1999-08-24 Mobile Oil Corporation Process for converting C9 + aromatic hydrocarbons to lighter aromatic products by transalkylation in the prescence of two zeolite-containing catalysts
US6972347B1 (en) 1999-06-16 2005-12-06 Toray Industries, Inc. Method for converting aromatic hydrocarbons
US6750446B2 (en) * 2001-01-17 2004-06-15 Fuji Photo Film Co., Ltd. Ultrasonic-welding apparatus, optical sensor and rotation sensor for the ultrasonic-welding apparatus
US6815570B1 (en) * 2002-05-07 2004-11-09 Uop Llc Shaped catalysts for transalkylation of aromatics for enhanced xylenes production
US7148391B1 (en) * 2002-11-14 2006-12-12 Exxonmobil Chemical Patents Inc. Heavy aromatics processing
US6740788B1 (en) 2002-12-19 2004-05-25 Uop Llc Integrated process for aromatics production
JP2004238317A (en) * 2003-02-05 2004-08-26 Toray Ind Inc Method for producing xylenes from heavy oil
US6958425B1 (en) 2003-06-13 2005-10-25 Uop Llc Aromatics transalkylation to ethylbenzene and xylenes
US6855854B1 (en) 2003-06-13 2005-02-15 Uop Llc Process and apparatus for ethylbenzene production and transalkylation to xylene
US6872866B1 (en) * 2003-12-15 2005-03-29 Uop Llc Liquid phase process for C8 alkylaromatic isomerization
US20050197518A1 (en) * 2004-03-04 2005-09-08 Miller Jeffrey T. Method of converting C9 aromatics-comprising mixtures to xylene isomers
US6972348B2 (en) 2004-03-24 2005-12-06 Uop Llc Catalytic conversion of polycyclic aromatics into xylenes
ITMI20040798A1 (en) * 2004-04-23 2004-07-23 Eni Spa PROCESS AND CATALYSTS FOR THE OPENING OF NAFTENIC RINGS
US7273828B1 (en) 2004-05-27 2007-09-25 Uop Llc Catalyst treatment useful for aromatics conversion process
US7220885B2 (en) * 2004-05-27 2007-05-22 Uop Llc Catalyst treatment useful for aromatics conversion process
US7179434B1 (en) 2004-09-08 2007-02-20 Uop Llc Integrated apparatus for aromatics production
US7169368B1 (en) 2004-09-08 2007-01-30 Uop Llc Integrated apparatus for aromatics production
US7154014B1 (en) * 2004-09-22 2006-12-26 Uop Llc Alumina guard bed for aromatics transalkylation process
US7271303B1 (en) 2004-09-22 2007-09-18 Uop Llc Multi-zone process for the production of diesel and aromatic compounds
EP1846348A1 (en) * 2005-02-11 2007-10-24 Uop Llc Process for ethylbenzene production and transalkylation to xylene
US20070049780A1 (en) * 2005-08-30 2007-03-01 Schwartz Hilary E Methods of making xylene isomers
JP5292699B2 (en) * 2006-03-29 2013-09-18 東レ株式会社 Method for converting ethylbenzene and method for producing paraxylene
TWI432409B (en) * 2006-03-29 2014-04-01 Toray Industries Process for converting hydrocarbon and process for producing p-xylene
US7288687B1 (en) 2006-05-18 2007-10-30 Uop Llc Integrated process for aromatics production
US7268263B1 (en) 2006-05-18 2007-09-11 Uop Llc Integrated process for aromatics production
US7304193B1 (en) 2006-05-18 2007-12-04 Uop Llc Integrated process for aromatics production
US7566810B2 (en) * 2006-09-12 2009-07-28 Uop Llc Xylene production processes employing rhenium-containing catalysts
US7687674B2 (en) 2006-12-28 2010-03-30 Uop Llc Low temperature process for recovering and producing para-xylene and heat exchange network therefore
US7692052B2 (en) * 2006-12-29 2010-04-06 Uop Llc Multi-zone process for the production of xylene compounds
JP5351152B2 (en) * 2007-07-06 2013-11-27 ユーオーピー エルエルシー Method for producing xylene
WO2009008878A1 (en) * 2007-07-06 2009-01-15 Uop Llc Process for the production of diesel and aromatic compounds
PL391673A1 (en) * 2007-07-30 2010-12-06 Uop Llc Methods for xylene production and device with integrated processing of a raw material
US7776283B2 (en) * 2007-07-30 2010-08-17 Uop Llc Xylene production apparatus with integrated feedstock treatment
US7847137B2 (en) * 2007-07-30 2010-12-07 Uop Llc Xylene production processes with integrated feedstock treatment
US8653315B2 (en) 2008-07-30 2014-02-18 King Fahd University Of Petroleum And Minerals Multiple zeolite catalyst and method of using the same for toluene disproportionation
KR101443476B1 (en) 2010-02-03 2014-09-22 엑손모빌 케미칼 패턴츠 인코포레이티드 Transalkylation of heavy aromatic hydrocarbon feedstocks
US8242322B2 (en) * 2010-09-30 2012-08-14 Uop Llc Processes for transalkylating aromatic hydrocarbons
JP5759263B2 (en) * 2011-05-24 2015-08-05 Jx日鉱日石エネルギー株式会社 Monocyclic aromatic hydrocarbon production method
JP5759262B2 (en) * 2011-05-24 2015-08-05 Jx日鉱日石エネルギー株式会社 Method for producing xylene
US8835705B2 (en) 2011-08-31 2014-09-16 Exxonmobil Chemical Patents Inc. Production of paraxylene
WO2013095815A1 (en) 2011-12-22 2013-06-27 Uop Llc Enhanced aromatics production by low pressure end point reduction and selective hydrogenation and hydrodealkylation
US9000247B2 (en) 2012-04-19 2015-04-07 Saudi Arabian Oil Company Combined heavy reformate dealkylation-transalkylation process for maximizing xylenes production
FR2999955B1 (en) 2012-12-20 2015-11-13 IFP Energies Nouvelles MODIFIED CATALYST OF STRUCTURAL TYPE MTW, ITS PREPARATION METHOD AND ITS USE IN ISOMERIZATION PROCESS OF C8 AROMATIC CUTTING
US9725377B2 (en) * 2013-03-14 2017-08-08 Exxonmobil Chemical Patents Inc. Hydroalkylation catalyst and process for use thereof
US9522858B2 (en) 2013-05-31 2016-12-20 Exxonmobil Chemical Patents Inc. Transalkylation system
US9783462B2 (en) 2013-09-10 2017-10-10 Saudi Basic Industries Corporation Toluene methylation with transalkylation of heavy aromatics
CN104549471A (en) * 2013-10-28 2015-04-29 中国石油化工股份有限公司 Catalyst for converting C10<+> heavy aromatics into mononuclear aromatics and preparation method of catalyst
RU2665477C2 (en) * 2014-10-31 2018-08-30 Чайна Петролеум & Кемикал Корпорейшн Method for obtaining aromatic hydrocarbons
US10450243B2 (en) * 2014-12-19 2019-10-22 Exxonmobil Chemical Patents Inc. Sulfiding process for aromatic transalkylations
US10118165B2 (en) 2015-02-04 2018-11-06 Exxonmobil Chemical Patents Inc. Catalyst compositions and use in heavy aromatics conversion processes
US10053403B2 (en) 2015-02-04 2018-08-21 Exxonmobil Chemical Patents Inc. Catalyst compositions and their use in transalkylation of heavy aromatics to xylenes
WO2017172066A1 (en) * 2016-03-28 2017-10-05 Exxonmobil Chemical Patents Inc. Liquid phase transalkylation process
CN107867968B (en) * 2016-09-23 2021-08-03 中国石油化工股份有限公司 Method for reducing side reaction of hydrogenation ring opening of benzene ring
KR102252012B1 (en) 2016-10-04 2021-05-17 엑손모빌 케미칼 패턴츠 인코포레이티드 Disproportionation and transalkylation of heavy aromatic hydrocarbons
JP7185625B2 (en) * 2016-10-10 2022-12-07 エクソンモービル ケミカル パテンツ インコーポレイテッド Process for converting heavy aromatics to BTX and catalyst composition used
US10173950B2 (en) 2017-01-04 2019-01-08 Saudi Arabian Oil Company Integrated process for the production of benzene and xylenes from heavy aromatics
US10464868B2 (en) 2017-05-26 2019-11-05 Saudi Arabian Oil Company Process for maximizing production of xylenes from heavy reformate without purge
US10252958B2 (en) 2017-05-26 2019-04-09 Saudi Arabian Oil Company Process for xylene production with energy optimization
US10035742B1 (en) 2017-05-26 2018-07-31 Saudi Arabian Oil Company Process for maximizing xylenes production from heavy aromatics for use therein
US10661260B2 (en) 2017-06-15 2020-05-26 King Fahd University Of Petroleum And Minerals Zeolite composite catalysts for conversion of heavy reformate to xylenes
CN110180581B (en) * 2018-02-22 2021-11-30 中国石油化工股份有限公司 Catalysts and their use in C11+Application in reaction for converting heavy aromatics into light aromatics
US10696609B2 (en) 2018-10-15 2020-06-30 Saudi Arabian Oil Company Integrated process for maximizing production of para-xylene from full reformate
US10894755B2 (en) 2018-10-15 2021-01-19 Saudi Arabian Oil Company Integrated process for optimum production of para-xylene
US10501389B1 (en) 2018-10-25 2019-12-10 Saudi Arabian Oil Company Process and system for the production of para-xylene and benzene from streams rich in C6 to C12+ aromatics
WO2021015900A1 (en) 2019-07-19 2021-01-28 Exxonmobil Chemical Patents Inc. Isomerization processes for converting aromatic hydrocarbons comprising alkyl-demethylation
WO2021015901A1 (en) 2019-07-19 2021-01-28 Exxonmobil Chemical Patents Inc. Transalkylation processes for converting aromatic hydrocarbons comprising alkyl-demethylation
WO2021015898A1 (en) 2019-07-19 2021-01-28 Exxonmobil Chemical Patents Inc. Processes for converting aromatic hydrocarbons via alkyl-demethylation
CN112570005B (en) * 2019-09-30 2023-08-04 中国石油化工股份有限公司 Method for regulating and controlling metal hydrogenation activity in reaction system and application thereof
US10981160B1 (en) 2019-12-19 2021-04-20 Saudi Arabian Oil Company Composite hierarchical zeolite catalyst for heavy reformate conversion to xylenes
CN111635780B (en) * 2020-06-04 2021-05-14 浙江大学 Method for producing BTX (benzene-toluene-xylene) from coal tar
US11827523B2 (en) 2022-04-13 2023-11-28 Saudi Arabian Oil Company Method for manufacture of zeolite beta in the presence of ODSO
US11905176B2 (en) 2022-04-13 2024-02-20 Saudi Arabian Oil Company Method for manufacture of low silica MFI framework zeolite in the presence of ODSO
US11970403B2 (en) 2022-06-27 2024-04-30 Saudi Arabian Oil Company Method of zeolite synthesis including pH-modified water-soluble oxidized disulfide oil composition
US11649405B1 (en) 2022-06-27 2023-05-16 Saudi Arabian Oil Company Methods of modifying pH of water-soluble oxidized disulfide oil
US11958751B2 (en) 2022-06-27 2024-04-16 Saudi Arabian Oil Company Method of synthesizing materials integrating supernatant recycle

Family Cites Families (33)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3729409A (en) * 1970-12-24 1973-04-24 Mobil Oil Corp Hydrocarbon conversion
US3832449A (en) * 1971-03-18 1974-08-27 Mobil Oil Corp Crystalline zeolite zsm{14 12
US3767568A (en) * 1971-03-19 1973-10-23 Mobil Oil Corp Hydrocarbon conversion
US3948758A (en) * 1974-06-17 1976-04-06 Mobil Oil Corporation Production of alkyl aromatic hydrocarbons
US3957621A (en) * 1974-06-17 1976-05-18 Mobil Oil Corporation Production of alkyl aromatic hydrocarbons
US3965208A (en) * 1975-01-06 1976-06-22 Mobil Oil Corporation Methylation of toluene
US4100215A (en) * 1974-09-25 1978-07-11 Mobil Oil Corporation Selective production of para-xylene
US4001346A (en) * 1975-01-06 1977-01-04 Mobil Oil Corporation Selective production of para-xylene
US3965209A (en) * 1975-01-06 1976-06-22 Mobil Oil Corporation Selective production of para-xylene
US4052476A (en) * 1975-04-24 1977-10-04 Mobil Oil Corporation Toluene disproportionation over zeolite catalyst
US4016218A (en) * 1975-05-29 1977-04-05 Mobil Oil Corporation Alkylation in presence of thermally modified crystalline aluminosilicate catalyst
US4016219A (en) * 1975-08-22 1977-04-05 Mobil Oil Corporation Disproportionation of toluene
US4007231A (en) * 1975-11-24 1977-02-08 Mobil Oil Corporation Selective production of para-xylene
US4029716A (en) * 1975-12-08 1977-06-14 Mobil Oil Corporation Selective production of para-xylene
US4011276A (en) * 1976-04-28 1977-03-08 Mobil Oil Corporation Disproportionation of toluene
US4117026A (en) * 1976-05-12 1978-09-26 Mobil Oil Corporation Selective production of para dialkyl substituted benzenes
US4150062A (en) * 1976-12-20 1979-04-17 Mobil Oil Corporation Light olefin processing
US4127471A (en) * 1977-07-28 1978-11-28 Texaco Inc. Hydrocracking alkylaromatic-containing hydrocarbons at mild cracking conditions and then subjecting the alkylaromatic hydrocarbon to alkyl transfer
US4172813A (en) * 1977-11-08 1979-10-30 Standard Oil Company (Indiana) Process for selectively hydrodealkylating/transalkylating heavy reformate
US4152364A (en) * 1978-01-19 1979-05-01 Mobil Oil Corporation Selective production of para-xylene
US4418235A (en) * 1980-02-14 1983-11-29 Mobil Oil Corporation Hydrocarbon conversion with zeolite having enhanced catalytic activity
US4380685A (en) * 1980-05-19 1983-04-19 Mobil Oil Corporation Shape selective reactions with zeolite catalysts modified with iron and/or cobalt
US4341914A (en) * 1980-12-22 1982-07-27 Uop Inc. Transalkylation process with recycle of C10 hydrocarbons
US4370508A (en) * 1981-06-26 1983-01-25 Mobil Oil Corporation Para-selective zeolite catalysts treated with nitrogen compounds
US4365104A (en) * 1981-06-26 1982-12-21 Mobil Oil Corporation Para-selective zeolite catalysts treated with sulfur compounds
US4367359A (en) * 1981-06-26 1983-01-04 Mobil Oil Corporation Para-selective zeolite catalysts treated with carbon dioxide
ZA861382B (en) * 1986-02-24 1987-10-28 Mobil Oil Corp Process for improving the octane number of cracked gasolines
US4983274A (en) * 1986-12-04 1991-01-08 Mobil Oil Corp. Shape selective crystalline silicate zeolite containing intermetallic component and use as catalyst in hydrocarbon conversions
US4812223A (en) * 1987-05-01 1989-03-14 Mobil Oil Corporation Hydrocracking naphthas using mildly steamed, noble metal-containing zeolite beta
US4857666A (en) * 1987-09-11 1989-08-15 Uop Alkylation/transalkylation process
US4891458A (en) * 1987-12-17 1990-01-02 Innes Robert A Liquid phase alkylation or transalkylation process using zeolite beta
US5030787A (en) * 1990-01-24 1991-07-09 Mobil Oil Corp. Catalytic disproportionation/transalkylation utilizing a C9+ aromatics feed
US5406016A (en) * 1993-06-07 1995-04-11 Exxon Research And Engineering Company Transalkylation of benzene with heavy catalytic naphtha

Similar Documents

Publication Publication Date Title
RU97114955A (en) METHOD FOR CONVERTING AROMATIC HYDROCARBONS
JP4021943B2 (en) Treatment of heavy aromatic compounds
JP3773530B2 (en) Treatment of heavy aromatic compounds
JP4074667B2 (en) Multi-stage hydroprocessing method in a single reactor
MY140891A (en) Heavy aromatics processing
CN106573855B (en) Process for producing aromatic hydrocarbons
JP4074668B2 (en) Multi-stage hydroprocessing method with multi-stage stripping in a single stripper tank
US4713167A (en) Multiple single-stage hydrocracking process
JP5568625B2 (en) Olefin production process
JPS5911635B2 (en) Catalytic dewaxing method for gas oil
EP1051457B1 (en) Decreasing bi-reactive contaminants in aromatic streams
HU217791B (en) Hydrocracking and hydrodewaxing process and preparated product
EP3870674A1 (en) Method for co-production of aviation fuel and diesel
AU1476799A (en) Production of olefins
RU2000100988A (en) METHOD FOR PROCESSING HEAVY AROMATIC HYDROCARBONS
CS213304B2 (en) Method of making the hydrocarbon fraction of predetermined end of the distillation interval
JP2013518715A (en) Transalkylation of heavy aromatic hydrocarbon feedstocks
JPH0756035B2 (en) Hydrocracking method
RU96108801A (en) METHOD OF CRACKING AND DEPAFFINIFICATION IN A HYDROGEN ENVIRONMENT
KR960037626A (en) Isomerization of C8 aromatics using catalysts containing modified silicoaluminophosphate molecular sieves
JP2023545175A (en) Method and system for processing hydrocarbon-containing mixtures
EP0032621B1 (en) Improvement in selective cracking reactions by cofeeding organic amine or ammonia
KR920701087A (en) Catalytic Conversion of C_9 ^ + Aromatics
TW200502207A (en) Benzene and C9 and above arene transalkylation method
CA2209658A1 (en) Heavy aromatics processing