AR010997A1 - Un proceso para la produccion selectiva de para-xileno y un metodo para producir un catalizador para ser usado en dicho proceso. - Google Patents

Un proceso para la produccion selectiva de para-xileno y un metodo para producir un catalizador para ser usado en dicho proceso.

Info

Publication number
AR010997A1
AR010997A1 ARP970104502A ARP970104502A AR010997A1 AR 010997 A1 AR010997 A1 AR 010997A1 AR P970104502 A ARP970104502 A AR P970104502A AR P970104502 A ARP970104502 A AR P970104502A AR 010997 A1 AR010997 A1 AR 010997A1
Authority
AR
Argentina
Prior art keywords
para
xylene
catalyst
crystalline material
porous crystalline
Prior art date
Application number
ARP970104502A
Other languages
English (en)
Original Assignee
Mobil Oil Corp
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 Mobil Oil Corp filed Critical Mobil Oil Corp
Publication of AR010997A1 publication Critical patent/AR010997A1/es

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C1/00—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon
    • C07C1/20—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon starting from organic compounds containing only oxygen atoms as heteroatoms
    • 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
    • B01J29/005—Mixtures of molecular sieves comprising at least one molecular sieve which is not an aluminosilicate zeolite, e.g. from groups B01J29/03 - B01J29/049 or B01J29/82 - B01J29/89
    • 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
    • B01J29/061—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof containing metallic elements added to the zeolite
    • 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
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2/00—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms
    • C07C2/86—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by condensation between a hydrocarbon and a non-hydrocarbon
    • C07C2/862—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by condensation between a hydrocarbon and a non-hydrocarbon the non-hydrocarbon contains only oxygen as hetero-atoms
    • C07C2/864—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by condensation between a hydrocarbon and a non-hydrocarbon the non-hydrocarbon contains only oxygen as hetero-atoms the non-hydrocarbon is an alcohol
    • 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
    • B01J2229/40—Special temperature treatment, i.e. other than just for template removal
    • 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
    • B01J29/82—Phosphates
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2527/00—Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
    • C07C2527/14—Phosphorus; Compounds thereof
    • C07C2527/16—Phosphorus; Compounds thereof containing oxygen
    • 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
    • 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)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Catalysts (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)

Abstract

Se provee un proceso para la produccion selectiva de para-xileno que comprende hacer reaccionar tolueno con metanol en presencia de un catalizadorque comprende un material cristalino poroso que tiene un parámetro de difusion para 2,2dimetilb utano de alrededor de 0,1-15 (1/seg) cuando se lo mide a unatemperatura de 120°C y una presion de 2,2 dimetilbutano de 60 torr (8 kPa). El material cristalino poroso es preferiblemente una zeolita de poros medianos,particularmente ZSM-5que ha sido tratada severamente con vapor a una temperatura de por lo menos 950°C. El material cristalino poroso espreferiblemente combinado con por lo menos un modificador de oxido, que preferiblemente combinado con por lo menosun modificador de oxido, quepreferiblemente incluye fosforo para controlar la reduccion del volumen microcorporal del material durante el tratamiento con vapor.
ARP970104502A 1996-10-02 1997-09-30 Un proceso para la produccion selectiva de para-xileno y un metodo para producir un catalizador para ser usado en dicho proceso. AR010997A1 (es)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US72527796A 1996-10-02 1996-10-02

Publications (1)

Publication Number Publication Date
AR010997A1 true AR010997A1 (es) 2000-08-02

Family

ID=24913880

Family Applications (1)

Application Number Title Priority Date Filing Date
ARP970104502A AR010997A1 (es) 1996-10-02 1997-09-30 Un proceso para la produccion selectiva de para-xileno y un metodo para producir un catalizador para ser usado en dicho proceso.

Country Status (20)

Country Link
EP (1) EP0935591B1 (es)
JP (1) JP4077518B2 (es)
KR (1) KR100569657B1 (es)
CN (1) CN1088694C (es)
AR (1) AR010997A1 (es)
AU (1) AU718083B2 (es)
BR (1) BR9712484A (es)
CA (1) CA2267915C (es)
DE (1) DE69734206T2 (es)
ES (1) ES2244994T3 (es)
ID (1) ID21235A (es)
IN (1) IN207438B (es)
MX (1) MX207687B (es)
MY (1) MY122348A (es)
NZ (1) NZ334123A (es)
RU (1) RU2179964C2 (es)
TR (1) TR199900717T2 (es)
TW (1) TW375602B (es)
WO (1) WO1998014415A1 (es)
ZA (1) ZA978671B (es)

Families Citing this family (39)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EA002376B1 (ru) * 1996-05-29 2002-04-25 Эксон Кемикэл Пейтентс Инк. Способ получения параксилола
US6048816A (en) * 1996-10-02 2000-04-11 Mobil Oil Corporation Catalyst and process for converting methanol to hydrocarbons
US6613708B1 (en) 1999-06-07 2003-09-02 Exxonmobil Chemical Patents Inc. Catalyst selectivation
US6388156B1 (en) * 1999-05-14 2002-05-14 Exxonmobil Chemical Patents Inc. Direct selective synthesis of para-xylene by reacting an aromatic compound with a methylating agent formed from CO, Co2 and H2
WO2004000974A1 (en) 2002-06-19 2003-12-31 Exxonmobil Chemical Patents Inc. Manufacture of xylenes from reformate
AU2003243674A1 (en) 2002-06-19 2004-01-06 Exxonmobil Chemical Patents Inc. Manufacture of xylenes from reformate
US7119239B2 (en) 2002-06-19 2006-10-10 Exxonmobil Chemical Patents Inc. Manufacture of xylenes using reformate
US20040097769A1 (en) * 2002-11-14 2004-05-20 Ou John D. Y. Para-xylene production process employing in-situ catalyst selectivation
GB0303659D0 (en) 2003-02-18 2003-03-19 Johnson Matthey Plc Process
US7238636B2 (en) 2003-07-23 2007-07-03 Exxonmobil Chemical Patents Inc. High temperature calcination of selectivated molecular sieve catalysts for activity and diffusional modification
US7326818B2 (en) 2003-08-15 2008-02-05 Exxonmobil Chemical Patents Inc. Selectivation of molecular sieve catalysts and use therof in hydrocarbon conversion
US7060864B2 (en) * 2003-09-30 2006-06-13 Saudi Basic Industries Corporation Toluene methylation process
US7453018B2 (en) 2003-12-31 2008-11-18 Exxonmobil Chemical Patents Inc. Process for aromatic alkylation
US7399727B2 (en) * 2004-04-23 2008-07-15 Saudi Basic Industries Corporation Zeolite catalyst and method
JP4965798B2 (ja) * 2004-07-30 2012-07-04 サウジ ベイシック インダストリーズ コーポレイション トルエンのメチル化法
CN101172252B (zh) * 2006-11-01 2010-05-12 中国石油化工股份有限公司 一种重整催化剂及其在高选择性制备对二甲苯中的应用
US8115041B2 (en) * 2008-04-02 2012-02-14 Saudi Basic Industries Corporation Pretreatment of a phosphorus-modified zeolite catalyst for an aromatic alkylation process
CN101306974B (zh) * 2008-06-12 2011-03-30 江苏工业学院 一种催化合成对二甲基苯的方法
US8252967B2 (en) * 2009-04-14 2012-08-28 Exxonmobil Chemical Patents Inc. Process for the purification of paraxylene
US8344197B2 (en) * 2009-10-21 2013-01-01 Exxonmobil Chemical Patents Inc. Production of para-xylene by the methylation of benzene and/or toluene
TWI495511B (zh) * 2011-07-27 2015-08-11 Exxonmobil Chem Patents Inc 具有分階擋板的流體床反應器
TWI623511B (zh) * 2011-12-08 2018-05-11 Ｇｔｃ科技美國有限責任公司 藉由將芳香族化合物甲基化以製造二甲苯的方法
EP2855406A4 (en) * 2012-05-31 2016-01-06 Exxonmobil Chem Patents Inc REMOVAL OF STYRENE IN A PROCESS FOR RECOVERING PARAXYLENE
CN103664488B (zh) * 2012-09-05 2015-09-09 中国石油化工股份有限公司 脱除含氧化合物杂质的芳烃甲醇烷基化方法
CN103113182B (zh) * 2013-01-22 2015-01-07 上海华谊（集团）公司 甲苯与甲醇择形烷基化合成对二甲苯的方法
WO2014120422A1 (en) * 2013-01-31 2014-08-07 Exxonmobile Chemical Patents, Inc. Production of para-xylene
CN104096589A (zh) * 2013-04-02 2014-10-15 上海华谊（集团）公司 甲苯与甲醇择形烷基化催化剂及其方法
CN103638963B (zh) * 2013-12-06 2017-01-18 陕西煤化工技术工程中心有限公司 甲苯甲醇烷基化制对二甲苯流化床催化剂及其制备方法
CN106458794B (zh) * 2014-06-30 2020-02-14 埃克森美孚化学专利公司 制备二甲苯的方法
US20150376087A1 (en) * 2014-06-30 2015-12-31 Exxonmobil Chemical Patents Inc. Process for the Production of Xylenes
EP3433223A4 (en) * 2016-03-25 2019-12-25 ExxonMobil Chemical Patents Inc. CATALYST AND PROCESS FOR PRODUCING PARAXYLENE
JP6743173B2 (ja) * 2016-03-25 2020-08-19 エクソンモービル・ケミカル・パテンツ・インク パラキシレンの製造用触媒およびプロセス
KR102235872B1 (ko) * 2016-10-06 2021-04-06 엑손모빌 케미칼 패턴츠 인코포레이티드 방향족 탄화수소의 메틸화 방법
BR112019006868A2 (pt) * 2016-10-06 2019-06-25 Exxonmobil Chemical Patents Inc processo para seletivar catalisador para produzir paraxileno por metilação de benzeno e/ou tolueno
CN106669818B (zh) * 2016-12-27 2019-08-30 西安元创化工科技股份有限公司 一种烷基化制备对甲基乙苯用催化剂的制备方法及其应用
CN108786904B (zh) * 2017-04-27 2020-08-11 中国科学院大连化学物理研究所 一种制低碳烯烃联产对二甲苯的催化剂的原位制备方法
CN108786906B (zh) * 2017-04-27 2020-08-07 中国科学院大连化学物理研究所 一种苯、甲醇制甲苯联产对二甲苯和低碳烯烃的催化剂的原位制备方法
CN117414865B (zh) * 2022-06-24 2026-03-03 中国石油化工股份有限公司 一种甲苯和甲醇烷基化催化剂及其制备方法和应用
KR20250005985A (ko) * 2022-11-24 2025-01-10 차이나 센화 골 투 리퀴드 앤드 케미칼 컴퍼니 리미티드 나프타와 메탄올을 결합하여 방향족 탄화수소들을 제조하기 위한 장치 및 방법

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US4380685A (en) * 1980-05-19 1983-04-19 Mobil Oil Corporation Shape selective reactions with zeolite catalysts modified with iron and/or cobalt
US4491678A (en) * 1982-10-19 1985-01-01 Idemitsu Kosan Company Limited Process for the production of para-xylene

Also Published As

Publication number Publication date
TR199900717T2 (xx) 1999-07-21
IN207438B (es) 2007-06-29
BR9712484A (pt) 2000-01-11
KR20000048645A (ko) 2000-07-25
CA2267915C (en) 2008-04-01
ES2244994T3 (es) 2005-12-16
KR100569657B1 (ko) 2006-04-11
ID21235A (id) 1999-05-06
CA2267915A1 (en) 1998-04-09
RU2179964C2 (ru) 2002-02-27
DE69734206T2 (de) 2006-07-06
AU4895497A (en) 1998-04-24
WO1998014415A1 (en) 1998-04-09
NZ334123A (en) 1999-11-29
CN1231653A (zh) 1999-10-13
MX9902863A (en) 1999-08-31
TW375602B (en) 1999-12-01
MY122348A (en) 2006-04-29
DE69734206D1 (de) 2005-10-20
EP0935591A1 (en) 1999-08-18
CN1088694C (zh) 2002-08-07
JP2001524069A (ja) 2001-11-27
MX207687B (en) 2002-05-06
JP4077518B2 (ja) 2008-04-16
ZA978671B (en) 1999-03-26
EP0935591B1 (en) 2005-09-14
EP0935591A4 (en) 2001-04-18
AU718083B2 (en) 2000-04-06

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