BR9912567A - Processo para a produção de ácido tereftálico e/ou tereftalato de dimetila - Google Patents
Processo para a produção de ácido tereftálico e/ou tereftalato de dimetilaInfo
- Publication number
- BR9912567A BR9912567A BR9912567-6A BR9912567A BR9912567A BR 9912567 A BR9912567 A BR 9912567A BR 9912567 A BR9912567 A BR 9912567A BR 9912567 A BR9912567 A BR 9912567A
- Authority
- BR
- Brazil
- Prior art keywords
- production
- terephthalic acid
- xylene
- dimethyl
- catalyst
- Prior art date
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C51/00—Preparation of carboxylic acids or their salts, halides or anhydrides
- C07C51/16—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation
- C07C51/21—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen
- C07C51/255—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen of compounds containing six-membered aromatic rings without ring-splitting
- C07C51/265—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen of compounds containing six-membered aromatic rings without ring-splitting having alkyl side chains which are oxidised to carboxyl groups
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C6/00—Preparation of hydrocarbons from hydrocarbons containing a different number of carbon atoms by redistribution reactions
- C07C6/08—Preparation of hydrocarbons from hydrocarbons containing a different number of carbon atoms by redistribution reactions by conversion at a saturated carbon-to-carbon bond
- C07C6/12—Preparation of hydrocarbons from hydrocarbons containing a different number of carbon atoms by redistribution reactions by conversion at a saturated carbon-to-carbon bond of exclusively hydrocarbons containing a six-membered aromatic ring
- C07C6/123—Preparation of hydrocarbons from hydrocarbons containing a different number of carbon atoms by redistribution reactions by conversion at a saturated carbon-to-carbon bond of exclusively hydrocarbons containing a six-membered aromatic ring of only one hydrocarbon
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C67/00—Preparation of carboxylic acid esters
- C07C67/39—Preparation of carboxylic acid esters by oxidation of groups which are precursors for the acid moiety of the ester
-
- 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)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
- Catalysts (AREA)
Abstract
Patente de Invenção: <B>"PROCESSO PARA A PRODUçãO DE áCIDO TEREFTáLICO E/OU TEREFTALATO DE DIMETILA"<D>. Um processo para a produção de ácido tereftálico e/ou tereftalato de dimetila inclui o contato de uma corrente de reação contendo tolueno com um primeiro catalisador sob condições de desproporção de tolueno para produzir uma corrente de produto intermediário de para-xileno com ortoxileno insignificante. O primeiro catalisador inclui uma peneira molecular cristalina que tem uma taxa de difusão de orto-xileno de pelo menos 50 minutos. O primeiro catalisador pode ser modificado através de seleção com um composto silício ou composto carbono. A corrente de produto intermediário, sem necessidade de purificação do para-xileno, é oxidada para ácido tereftálico de dimetila.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US09/123,281 US6133470A (en) | 1998-07-28 | 1998-07-28 | Integration of p-xylene production and subsequent conversion process |
PCT/US1999/016491 WO2000006530A1 (en) | 1998-07-28 | 1999-07-20 | A process for producing terephthalic acid and/or dimethyl terephthalate |
Publications (1)
Publication Number | Publication Date |
---|---|
BR9912567A true BR9912567A (pt) | 2001-05-02 |
Family
ID=22407751
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
BR9912567-6A BR9912567A (pt) | 1998-07-28 | 1999-07-20 | Processo para a produção de ácido tereftálico e/ou tereftalato de dimetila |
Country Status (14)
Country | Link |
---|---|
US (1) | US6133470A (pt) |
EP (1) | EP1100765B1 (pt) |
JP (1) | JP2002521467A (pt) |
KR (1) | KR20010071053A (pt) |
CN (1) | CN1319084A (pt) |
AR (1) | AR020637A1 (pt) |
AT (1) | ATE284859T1 (pt) |
AU (1) | AU5005599A (pt) |
BR (1) | BR9912567A (pt) |
CA (1) | CA2338656A1 (pt) |
DE (1) | DE69922660D1 (pt) |
TW (1) | TW491836B (pt) |
WO (1) | WO2000006530A1 (pt) |
ZA (1) | ZA200100764B (pt) |
Families Citing this family (25)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6037513A (en) * | 1998-07-09 | 2000-03-14 | Mobil Oil Corporation | Hydroalkylation of aromatic hydrocarbons |
US7683210B2 (en) | 2004-09-02 | 2010-03-23 | Eastman Chemical Company | Optimized liquid-phase oxidation |
US7692036B2 (en) | 2004-11-29 | 2010-04-06 | Eastman Chemical Company | Optimized liquid-phase oxidation |
US7572936B2 (en) | 2004-09-02 | 2009-08-11 | Eastman Chemical Company | Optimized liquid-phase oxidation |
US7568361B2 (en) | 2004-09-02 | 2009-08-04 | Eastman Chemical Company | Optimized liquid-phase oxidation |
US7692037B2 (en) | 2004-09-02 | 2010-04-06 | Eastman Chemical Company | Optimized liquid-phase oxidation |
US7589231B2 (en) | 2004-09-02 | 2009-09-15 | Eastman Chemical Company | Optimized liquid-phase oxidation |
US7741515B2 (en) | 2004-09-02 | 2010-06-22 | Eastman Chemical Company | Optimized liquid-phase oxidation |
US7381836B2 (en) | 2004-09-02 | 2008-06-03 | Eastman Chemical Company | Optimized liquid-phase oxidation |
US7504535B2 (en) | 2004-09-02 | 2009-03-17 | Eastman Chemical Company | Optimized liquid-phase oxidation |
US7910769B2 (en) | 2004-09-02 | 2011-03-22 | Eastman Chemical Company | Optimized liquid-phase oxidation |
US7582793B2 (en) | 2004-09-02 | 2009-09-01 | Eastman Chemical Company | Optimized liquid-phase oxidation |
US7507857B2 (en) | 2004-09-02 | 2009-03-24 | Eastman Chemical Company | Optimized liquid-phase oxidation |
US7249469B2 (en) * | 2004-11-18 | 2007-07-31 | Exxonmobil Chemical Patents Inc. | Method for separating a multicomponent stream |
US7884232B2 (en) | 2005-06-16 | 2011-02-08 | Eastman Chemical Company | Optimized liquid-phase oxidation |
CN101998942B (zh) | 2008-04-14 | 2016-02-03 | 埃克森美孚化学专利公司 | 制备环己基苯的工艺 |
WO2009134516A1 (en) * | 2008-05-01 | 2009-11-05 | Exxonmobil Chemical Patents Inc. | Process for producing cyclohexylbenzene |
CN102105397B (zh) * | 2008-07-28 | 2014-02-05 | 埃克森美孚化学专利公司 | 使用emm-13制备烷基芳族化合物的方法 |
CN102216215B (zh) * | 2008-07-28 | 2014-03-26 | 埃克森美孚化学专利公司 | 使用emm-12制备烷基芳族化合物的方法 |
CN102333747A (zh) | 2009-02-26 | 2012-01-25 | 埃克森美孚化学专利公司 | 生产环己基苯的方法 |
US9545622B2 (en) | 2010-10-11 | 2017-01-17 | Exxonmobil Chemical Patents Inc. | Activation and use of hydroalkylation catalysts |
US9233887B2 (en) | 2010-12-21 | 2016-01-12 | Exxonmobil Chemical Patents Inc. | Process for producing a monocycloalkyl-substituted aromatic compound |
US9108893B2 (en) | 2011-10-17 | 2015-08-18 | Exxonmobil Chemical Patents Inc. | Process for producing cyclohexylbenzene |
US10661258B2 (en) * | 2013-06-13 | 2020-05-26 | Exxonmobil Chemical Patents Inc. | In-situ trim coke selectivation of toluene disproportionation catalyst |
WO2024030751A1 (en) * | 2022-08-03 | 2024-02-08 | Eastman Chemical Company | Recycled content dimethyl terephthalate and related chemical components from waste plastic |
Family Cites Families (31)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US31782A (en) * | 1861-03-26 | Reerigeratob | ||
GB727989A (en) * | 1951-04-13 | 1955-04-13 | Imhausen & Co Ges Mit Beschrae | Improvements in or relating to the production of benzene polycarboxylic acids or derivatives thereof |
US2833816A (en) * | 1954-05-03 | 1958-05-06 | Mid Century Corp | Preparation of aromatic polycarboxylic acids |
NL120513C (pt) * | 1959-05-09 | |||
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 |
USRE31782E (en) | 1978-06-09 | 1984-12-25 | Mobil Oil Corporation | Xylene isomerization |
US4705909A (en) * | 1986-02-27 | 1987-11-10 | Mobil Oil Corporation | Process for the separation of para-xylene |
US5243117A (en) * | 1990-06-05 | 1993-09-07 | Mobil Oil Corp. | Catalyst and process for the selective production of para-dialkyl substituted benzenes |
US5498814A (en) * | 1992-03-12 | 1996-03-12 | Mobil Oil Corp. | Regioselective methylation of toluene to para-xylene |
US5475179A (en) * | 1992-03-12 | 1995-12-12 | Mobil Oil | Regioselective production of para-dialkyl benzenes |
US5571768A (en) * | 1992-03-12 | 1996-11-05 | Mobil Oil Corporation | Zeolite functionalized with organosiliceous groups |
US5321183A (en) * | 1992-03-12 | 1994-06-14 | Mobil Oil Corp. | Process for the regioselective conversion of aromatics to para-disubstituted benzenes |
US5516736A (en) * | 1992-03-12 | 1996-05-14 | Mobil Oil Corp. | Selectivating zeolites with organosiliceous agents |
US5365003A (en) * | 1993-02-25 | 1994-11-15 | Mobil Oil Corp. | Shape selective conversion of hydrocarbons over extrusion-modified molecular sieve |
US5349113A (en) * | 1993-02-25 | 1994-09-20 | Mobil Oil Corp. | Shape selective hydrocarbon conversion over pre-selectivated, activated catalyst |
US5349114A (en) * | 1993-04-05 | 1994-09-20 | Mobil Oil Corp. | Shape selective hydrocarbon conversions over modified catalyst |
US5371312A (en) * | 1993-04-05 | 1994-12-06 | Mobil Oil Corp. | Shape selective hydrocarbon conversions over modified catalyst |
US5659098A (en) * | 1993-05-28 | 1997-08-19 | Beck; Jeffrey S. | High conversion touluene disproportionation with ex situ selectivated zeolite catalysts |
US5406015A (en) * | 1993-05-28 | 1995-04-11 | Mobil Oil Corp. | Selective ethylbenzene disproportionation processes (SEBDP) with ex situ selectivated zeolite catalyst |
US5403800A (en) * | 1993-05-28 | 1995-04-04 | Mobil Oil Corp. | Multiple impregnation technique for the preparation of ex situ selectivated zeolite catalysts |
US5365004A (en) * | 1993-05-28 | 1994-11-15 | Mobil Oil Corp. | Selective toluene disproportionation process (STDP) with ex situ selectivated zeolite catalysts |
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 |
US5367099A (en) * | 1993-05-28 | 1994-11-22 | Mobil Oil Corp. | Selective toluene disproportionation process (STDP) with ex situ selectivated zeolite catalyst |
ES2139752T3 (es) * | 1993-10-18 | 2000-02-16 | Mobil Oil Corp | Material cristalino poroso sintetico, mcm-58, su sintesis y uso. |
US5488194A (en) * | 1994-05-16 | 1996-01-30 | Mobil Oil Corp. | Selective production of para-dialkyl substituted benzenes and catalyst therefor |
US5625104A (en) * | 1995-06-06 | 1997-04-29 | Mobil Oil Corporation | Alkali metal ion exchanged selectivated zeolite catalyst |
US5567666A (en) * | 1995-05-15 | 1996-10-22 | Mobil Oil Corporation | Selectivated zeolite catalyst treated with a dealuminizing agent |
US5625103A (en) * | 1995-05-15 | 1997-04-29 | Mobil Oil Corporation | Continuous toluene disproportionation process |
US5612270A (en) * | 1995-05-15 | 1997-03-18 | Mobil Oil Corporation | Ammonium treated selectivated zeolite catalyst |
US5602066A (en) * | 1995-06-29 | 1997-02-11 | Mobil Oil Corporation | Method of making a liquid washed selectivated zeolite catalyst |
-
1998
- 1998-07-28 US US09/123,281 patent/US6133470A/en not_active Expired - Fee Related
-
1999
- 1999-07-20 WO PCT/US1999/016491 patent/WO2000006530A1/en active IP Right Grant
- 1999-07-20 DE DE69922660T patent/DE69922660D1/de not_active Expired - Lifetime
- 1999-07-20 EP EP99934165A patent/EP1100765B1/en not_active Expired - Lifetime
- 1999-07-20 CA CA002338656A patent/CA2338656A1/en not_active Abandoned
- 1999-07-20 BR BR9912567-6A patent/BR9912567A/pt not_active IP Right Cessation
- 1999-07-20 AT AT99934165T patent/ATE284859T1/de not_active IP Right Cessation
- 1999-07-20 CN CN99810145A patent/CN1319084A/zh active Pending
- 1999-07-20 AU AU50055/99A patent/AU5005599A/en not_active Abandoned
- 1999-07-20 JP JP2000562337A patent/JP2002521467A/ja not_active Withdrawn
- 1999-07-20 KR KR1020017001218A patent/KR20010071053A/ko not_active Application Discontinuation
- 1999-07-27 AR ARP990103687A patent/AR020637A1/es unknown
- 1999-07-28 TW TW088112787A patent/TW491836B/zh not_active IP Right Cessation
-
2001
- 2001-01-26 ZA ZA200100764A patent/ZA200100764B/en unknown
Also Published As
Publication number | Publication date |
---|---|
CN1319084A (zh) | 2001-10-24 |
AR020637A1 (es) | 2002-05-22 |
TW491836B (en) | 2002-06-21 |
ZA200100764B (en) | 2001-10-22 |
AU5005599A (en) | 2000-02-21 |
CA2338656A1 (en) | 2000-02-10 |
WO2000006530A1 (en) | 2000-02-10 |
US6133470A (en) | 2000-10-17 |
EP1100765B1 (en) | 2004-12-15 |
ATE284859T1 (de) | 2005-01-15 |
EP1100765A1 (en) | 2001-05-23 |
DE69922660D1 (de) | 2005-01-20 |
JP2002521467A (ja) | 2002-07-16 |
KR20010071053A (ko) | 2001-07-28 |
EP1100765A4 (en) | 2002-07-17 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
BR9912567A (pt) | Processo para a produção de ácido tereftálico e/ou tereftalato de dimetila | |
BR0010565A (pt) | Sìntese seletiva direta de para-xileno | |
CA2208984A1 (fr) | Procede de separation de paraxylene comportant au moins deux etages de cristallisation a haute temperature | |
KR880003891A (ko) | 방향족 카르복시산의 제조방법 | |
KR840006961A (ko) | 직접 중합에 적합한 테레프탈산의 제조방법 | |
BR9307822A (pt) | Processo para a purificação de um ácido tereftálico bruto de um ácido isoftálico bruto ou de um ácido naftaleno dicarbocílico bruto e composição catalítica | |
MY162520A (en) | Oxidation system with sidedraw secondary reactor | |
ATE380169T1 (de) | Verfahren zur selektiven herstellung von meta- diisopropylbenzol | |
BR9713703A (pt) | Processo para preparação de aminas aromáticas por hidrogenação em fase gasosa | |
BR9910817A (pt) | Processo para purificar ácido tereftálico bruto | |
DE69802863D1 (de) | Verfahren zur Alkylierung in der Gasphase und zur Transalkylierung in der Flüssigphase | |
ATE368021T1 (de) | Verfahren zur alkylierung in der gasphase - zur transalkylierung in der flüssigen phase | |
BR9815986A (pt) | Processo de produção de um ácido carboxìlico puro, processo de produção de ácido tereftálico puro e composição de matéria | |
BR0011679A (pt) | Seletivação de catalisador | |
BR9912725A (pt) | Processo para a purificação de um fluxo de gás, sistema para realizar o processo e uso de uma sonda lambda | |
EP0676400A3 (en) | Method for production of pyromellitic anhydride | |
KR900700177A (ko) | 일산화탄소 및/또는 수소가 함유된 기류로부터 불순물을 제거하는 방법 | |
BRPI0407115A (pt) | Métodos para purificação de uma corrente de produto de fenol, e para fabricação de um produto de fenol de alta pureza, e, composição de fenol de alta prioridade | |
BR9916866A (pt) | Processo para a produção de cristais de ácidocarboxìlico aromático altamente puros a partirde um produto de ácido sólido impuro | |
NO20023045D0 (no) | Fremgangsmåte for fremstilling av olefiner | |
BR9809222A (pt) | Método para preparação de ácido formilfosfÈnico | |
BR9813560A (pt) | Catalisador à base de paládio, cádmio, metal alcalino e lantanóides e processo para preparação de acetato de vinila | |
BR9901225A (pt) | Processo para a preparação de polìmeros com unidades succinila repetitivas com aplicação de catalisadores. | |
DE69422754D1 (de) | Verfahren zur Herstellung von Polypropylen | |
BR0008034A (pt) | Oxidação de hidrocarbonetos em ácido na presença de fluorocomposto |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
B08F | Application dismissed because of non-payment of annual fees [chapter 8.6 patent gazette] |
Free format text: REFERENTE A 5A, 6A, 7A E 8A ANUIDADES |
|
B08K | Patent lapsed as no evidence of payment of the annual fee has been furnished to inpi [chapter 8.11 patent gazette] |
Free format text: REFERENTE AO DESPACHO 8.6 PUBLICADO NA RPI 1911 DE 21/08/2007. |