BR0107739A - Processos para a produção de ácido carboxìlico aromático, de recuperação de energia, e para a produção de ácido dicarboxìlico aromático, e, processo contìnuo para a produção de um ácido tricarboxìlico aromático - Google Patents
Processos para a produção de ácido carboxìlico aromático, de recuperação de energia, e para a produção de ácido dicarboxìlico aromático, e, processo contìnuo para a produção de um ácido tricarboxìlico aromáticoInfo
- Publication number
- BR0107739A BR0107739A BR0107739-2A BR0107739A BR0107739A BR 0107739 A BR0107739 A BR 0107739A BR 0107739 A BR0107739 A BR 0107739A BR 0107739 A BR0107739 A BR 0107739A
- Authority
- BR
- Brazil
- Prior art keywords
- acid
- production
- aromatic
- processes
- dicarboxylic acid
- 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
- C07C51/42—Separation; Purification; Stabilisation; Use of additives
- C07C51/43—Separation; Purification; Stabilisation; Use of additives by change of the physical state, e.g. crystallisation
-
- 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
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Crystallography & Structural Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
Abstract
"PROCESSOS PARA A PRODUçãO DE áCIDO CARBOXìLICO AROMáTICO, DE RECUPERAçãO DE ENERGIA, E PARA A PRODUçãO DE áCIDO DICARBOXìLICO AROMáTICO, E, PROCESSO CONTìNUO PARA A PRODUçãO DE UM áCIDO TRICARBOXìLICO AROMáTICO". São divulgados processos para produção de ácidos carboxílicos aromáticos. Os ácidos aromáticos são produzidos pela oxidação em fase líquida de um precursor de ácido em um meio de reação que compreende ácido benzóico. De acordo com uma forma de realização a oxidação é levada a efeito em condições de reação de fluxo tampão em um reator de fluxo tampão. As condições de fluxo tampão podem ser obtidas pelo uso de uma série de reatores tipo tanque agitados contínuos. Em outra forma de realização, a oxidação é levada a efeito em dois reatores tipo tanque agitados contínuos conectados de maneira fluida em série. Os produtos de oxidação preferidos são ácido tereftálico, ácido isoftálico, ácido trimelítico, ácido 2,6-naftaleno dicarboxílico, ácido 1,5-naftaleno dicarboxílico, ácido 2,7-naftaleno dicarboxílico e ácido ftálico.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US17742900P | 2000-01-21 | 2000-01-21 | |
PCT/US2001/001909 WO2001053246A1 (en) | 2000-01-21 | 2001-01-19 | Production of high purity aromatic carboxylic acid by oxidation in benzoic acid and water solvent |
Publications (1)
Publication Number | Publication Date |
---|---|
BR0107739A true BR0107739A (pt) | 2002-10-22 |
Family
ID=22648562
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
BR0107739-2A BR0107739A (pt) | 2000-01-21 | 2001-01-19 | Processos para a produção de ácido carboxìlico aromático, de recuperação de energia, e para a produção de ácido dicarboxìlico aromático, e, processo contìnuo para a produção de um ácido tricarboxìlico aromático |
Country Status (13)
Country | Link |
---|---|
US (1) | US6562997B2 (pt) |
EP (1) | EP1257520A1 (pt) |
JP (1) | JP2003520263A (pt) |
KR (1) | KR20020069261A (pt) |
CN (1) | CN1227208C (pt) |
AU (1) | AU2001232878A1 (pt) |
BR (1) | BR0107739A (pt) |
CA (1) | CA2396967A1 (pt) |
MX (1) | MXPA02007123A (pt) |
RU (1) | RU2259346C2 (pt) |
TR (1) | TR200201833T2 (pt) |
UA (1) | UA73971C2 (pt) |
WO (1) | WO2001053246A1 (pt) |
Families Citing this family (83)
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US6426431B1 (en) * | 1999-08-30 | 2002-07-30 | Mossi & Ghisolfi Overseas S.A. | Method for increasing the yield of 2,6 -NDA |
US6852879B2 (en) * | 2001-10-05 | 2005-02-08 | Bp Corporation North America Inc. | Method of removing iron oxide deposits from the surface of titanium components |
US6657068B2 (en) | 2002-03-22 | 2003-12-02 | General Electric Company | Liquid phase oxidation of halogenated ortho-xylenes |
US6657067B2 (en) | 2002-03-22 | 2003-12-02 | General Electric Company | Method for the manufacture of chlorophthalic anhydride |
US6649773B2 (en) | 2002-03-22 | 2003-11-18 | General Electric Company | Method for the manufacture of halophthalic acids and anhydrides |
US7135596B2 (en) * | 2002-04-23 | 2006-11-14 | Bp Corporation North America Inc. | Method of removing iron contaminants from liquid streams during the manufacture and/or purification of aromatic acids |
US7494641B2 (en) * | 2003-06-05 | 2009-02-24 | Eastman Chemical Company | Extraction process for removal of impurities from an oxidizer purge stream in the synthesis of carboxylic acid |
US7452522B2 (en) * | 2003-06-05 | 2008-11-18 | Eastman Chemical Company | Extraction process for removal of impurities from an oxidizer purge stream in the synthesis of carboxylic acid |
US7410632B2 (en) * | 2003-06-05 | 2008-08-12 | Eastman Chemical Company | Extraction process for removal of impurities from mother liquor in the synthesis of carboxylic acid |
US7351396B2 (en) * | 2003-06-05 | 2008-04-01 | Eastman Chemical Company | Extraction process for removal of impurities from an aqueous mixture |
US7282151B2 (en) * | 2003-06-05 | 2007-10-16 | Eastman Chemical Company | Process for removal of impurities from mother liquor in the synthesis of carboxylic acid using pressure filtration |
US7378544B2 (en) * | 2003-12-18 | 2008-05-27 | Bp Corporation North America Inc. | Anthracene and other polycyclic aromatics as activators in the oxidation of aromatic hydrocarbons |
US20050256335A1 (en) * | 2004-05-12 | 2005-11-17 | Ovidiu Marin | Providing gases to aromatic carboxylic acid manufacturing processes |
US7888530B2 (en) * | 2004-09-02 | 2011-02-15 | Eastman Chemical Company | Optimized production of aromatic dicarboxylic acids |
US7482482B2 (en) * | 2004-09-02 | 2009-01-27 | Eastman Chemical Company | Optimized liquid-phase oxidation |
US7589231B2 (en) * | 2004-09-02 | 2009-09-15 | Eastman Chemical Company | Optimized liquid-phase oxidation |
US7608733B2 (en) * | 2004-09-02 | 2009-10-27 | Eastman Chemical Company | Optimized liquid-phase oxidation |
US7568361B2 (en) * | 2004-09-02 | 2009-08-04 | Eastman Chemical Company | Optimized liquid-phase oxidation |
US7504535B2 (en) | 2004-09-02 | 2009-03-17 | Eastman Chemical Company | Optimized liquid-phase oxidation |
US20070238899A9 (en) * | 2004-09-02 | 2007-10-11 | Robert Lin | Optimized production of aromatic dicarboxylic acids |
US7608732B2 (en) * | 2005-03-08 | 2009-10-27 | Eastman Chemical Company | Optimized liquid-phase oxidation |
US7692037B2 (en) * | 2004-09-02 | 2010-04-06 | Eastman Chemical Company | Optimized liquid-phase oxidation |
US7692036B2 (en) * | 2004-11-29 | 2010-04-06 | Eastman Chemical Company | Optimized liquid-phase oxidation |
US7399882B2 (en) * | 2004-09-02 | 2008-07-15 | Eastman Chemical Company | Optimized liquid-phase oxidation |
US7495125B2 (en) * | 2004-09-02 | 2009-02-24 | Eastman Chemical Company | Optimized liquid-phase oxidation |
US7572936B2 (en) * | 2004-09-02 | 2009-08-11 | Eastman Chemical Company | Optimized liquid-phase oxidation |
US7361784B2 (en) * | 2004-09-02 | 2008-04-22 | Eastman Chemical Company | Optimized liquid-phase oxidation |
US7371894B2 (en) * | 2004-09-02 | 2008-05-13 | Eastman Chemical Company | Optimized liquid-phase oxidation |
US7586000B2 (en) * | 2004-09-02 | 2009-09-08 | Eastman Chemical Company | Optimized liquid-phase oxidation |
US7582793B2 (en) | 2004-09-02 | 2009-09-01 | Eastman Chemical Company | Optimized liquid-phase oxidation |
CN101023046B (zh) * | 2004-09-02 | 2019-01-18 | 奇派特石化有限公司 | 优化的液相氧化 |
CN102701940A (zh) * | 2004-09-02 | 2012-10-03 | 奇派特石化有限公司 | 优化的液相氧化 |
US7741515B2 (en) | 2004-09-02 | 2010-06-22 | Eastman Chemical Company | Optimized liquid-phase oxidation |
US7910769B2 (en) * | 2004-09-02 | 2011-03-22 | Eastman Chemical Company | Optimized liquid-phase oxidation |
US7683210B2 (en) * | 2004-09-02 | 2010-03-23 | Eastman Chemical Company | Optimized liquid-phase oxidation |
US7615663B2 (en) * | 2004-09-02 | 2009-11-10 | Eastman Chemical Company | Optimized production of aromatic dicarboxylic acids |
US7507857B2 (en) * | 2004-09-02 | 2009-03-24 | Eastman Chemical Company | Optimized liquid-phase oxidation |
US7390921B2 (en) * | 2004-09-02 | 2008-06-24 | Eastman Chemical Company | Optimized liquid-phase oxidation |
US7381836B2 (en) * | 2004-09-02 | 2008-06-03 | Eastman Chemical Company | Optimized liquid-phase oxidation |
US20080161598A1 (en) * | 2004-09-02 | 2008-07-03 | Eastman Chemical Company | Optimized Production of Aromatic Dicarboxylic Acids |
US7572932B2 (en) * | 2004-09-02 | 2009-08-11 | Eastman Chemical Company | Optimized liquid-phase oxidation |
US20060047153A1 (en) * | 2004-09-02 | 2006-03-02 | Wonders Alan G | Optimized liquid-phase oxidation |
BRPI0609328B1 (pt) * | 2005-03-21 | 2016-04-12 | Bp Corp North America Inc | processos de produção de ácidos carboxílicos aromáticos e equipamentos de separação dos componentes de gás |
US7884232B2 (en) * | 2005-06-16 | 2011-02-08 | Eastman Chemical Company | Optimized liquid-phase oxidation |
US7402694B2 (en) * | 2005-08-11 | 2008-07-22 | Eastman Chemical Company | Process for removal of benzoic acid from an oxidizer purge stream |
US7569722B2 (en) * | 2005-08-11 | 2009-08-04 | Eastman Chemical Company | Process for removal of benzoic acid from an oxidizer purge stream |
KR100744754B1 (ko) * | 2005-12-13 | 2007-08-01 | 삼성석유화학(주) | 방향족 카르복실산의 제조방법 |
US20070155987A1 (en) * | 2006-01-04 | 2007-07-05 | O'meadhra Ruairi S | Oxidative digestion with optimized agitation |
US7358389B2 (en) * | 2006-01-04 | 2008-04-15 | Eastman Chemical Company | Oxidation system employing internal structure for enhanced hydrodynamics |
US7355068B2 (en) | 2006-01-04 | 2008-04-08 | Eastman Chemical Company | Oxidation system with internal secondary reactor |
US20070203359A1 (en) * | 2006-03-01 | 2007-08-30 | Philip Edward Gibson | Versatile oxidation byproduct purge process |
US7772424B2 (en) * | 2006-03-01 | 2010-08-10 | Eastman Chemical Company | Polycarboxylic acid production system employing enhanced evaporative concentration downstream of oxidative digestion |
US7326807B2 (en) * | 2006-03-01 | 2008-02-05 | Eastman Chemical Company | Polycarboxylic acid production system with enhanced heating for oxidative digestion |
US7420082B2 (en) * | 2006-03-01 | 2008-09-02 | Eastman Chemical Company | Polycarboxylic acid production system employing hot liquor removal downstream of oxidative digestion |
US7863481B2 (en) * | 2006-03-01 | 2011-01-04 | Eastman Chemical Company | Versatile oxidation byproduct purge process |
US7897808B2 (en) * | 2006-03-01 | 2011-03-01 | Eastman Chemical Company | Versatile oxidation byproduct purge process |
US7880032B2 (en) * | 2006-03-01 | 2011-02-01 | Eastman Chemical Company | Versatile oxidation byproduct purge process |
US7462736B2 (en) * | 2006-03-01 | 2008-12-09 | Eastman Chemical Company | Methods and apparatus for isolating carboxylic acid |
US7393973B2 (en) * | 2006-03-01 | 2008-07-01 | Eastman Chemical Company | Polycarboxylic acid production system with enhanced residence time distribution for oxidative digestion |
US7501537B2 (en) * | 2006-03-01 | 2009-03-10 | Eastman Chemical Company | Polycarboxylic acid production system employing oxidative digestion with reduced or eliminated upstream liquor exchange |
US7847121B2 (en) * | 2006-03-01 | 2010-12-07 | Eastman Chemical Company | Carboxylic acid production process |
US7863483B2 (en) * | 2006-03-01 | 2011-01-04 | Eastman Chemical Company | Carboxylic acid production process |
US20070208194A1 (en) * | 2006-03-01 | 2007-09-06 | Woodruff Thomas E | Oxidation system with sidedraw secondary reactor |
US7326808B2 (en) * | 2006-03-01 | 2008-02-05 | Eastman Chemical Company | Polycarboxylic acid production system employing cooled mother liquor from oxidative digestion as feed to impurity purge system |
US8173835B2 (en) * | 2006-03-01 | 2012-05-08 | Grupo Petrotemex, S.A. De C.V. | Method and apparatus for drying carboxylic acid |
US7816556B2 (en) * | 2006-03-01 | 2010-10-19 | Eastman Chemical Company | Polycarboxylic acid production system employing enhanced multistage oxidative digestion |
US8697906B2 (en) * | 2006-03-01 | 2014-04-15 | Grupo Petrotemex, S.A. De C.V. | Methods and apparatus for producing a low-moisture carboxylic acid wet cake |
US20070208199A1 (en) * | 2006-03-01 | 2007-09-06 | Kenny Randolph Parker | Methods and apparatus for isolating carboxylic acid |
US7465824B2 (en) * | 2007-02-08 | 2008-12-16 | Bp Corporation North America Inc. | Process for the production of high purity aromatic carboxylic acids using a benzoic acid and water solvent for oxidation and purification |
US8455680B2 (en) * | 2008-01-15 | 2013-06-04 | Eastman Chemical Company | Carboxylic acid production process employing solvent from esterification of lignocellulosic material |
US8614350B2 (en) | 2008-01-15 | 2013-12-24 | Eastman Chemical Company | Carboxylic acid production process employing solvent from esterification of lignocellulosic material |
CN101531588B (zh) * | 2008-03-13 | 2016-02-24 | 周向进 | 一种新的精对苯二甲酸的制造方法 |
CN105732256B (zh) | 2008-03-18 | 2019-06-28 | Gtc技术有限公司 | 用于生产间苯二甲酸和对苯二甲酸的方法 |
CN101575284B (zh) * | 2008-05-05 | 2014-11-26 | 周向进 | 一种新的精间苯二甲酸的制造方法 |
CN101362687B (zh) * | 2008-10-08 | 2012-04-11 | 湖南大学 | 空气氧化对二甲苯制备对苯二甲酸的方法和设备 |
RU2523798C2 (ru) * | 2009-03-17 | 2014-07-27 | Тейджин Арамид Б.В. | Способ превращения ароматических альдегидов в ароматические ацилгалогениды |
CN102652122B (zh) * | 2009-12-16 | 2015-09-09 | 英威达技术有限公司 | 生产芳香羧酸的***和方法 |
US9024059B2 (en) | 2011-12-29 | 2015-05-05 | Uop Llc | Process for producing terephthalic acid |
KR20140102761A (ko) * | 2011-12-29 | 2014-08-22 | 유오피 엘엘씨 | 테레프탈산의 제조 방법 |
US8927764B2 (en) | 2011-12-29 | 2015-01-06 | Uop Llc | Process for producing terephthalic acid |
US9085522B2 (en) | 2011-12-29 | 2015-07-21 | Uop Llc | Process for producing terephthalic acid |
US9156765B2 (en) | 2011-12-29 | 2015-10-13 | Uop Llc | Process for oxidizing alkyl-aromatic compounds |
CN108017532A (zh) * | 2016-10-28 | 2018-05-11 | 中国石油化工股份有限公司 | 一种间二甲苯液相氧化生成间苯二甲酸的方法 |
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US3484458A (en) | 1966-09-19 | 1969-12-16 | Standard Oil Co | Trimellitic acid production and recovery of intramolecular anhydride |
US4081464A (en) | 1976-07-26 | 1978-03-28 | Standard Oil Company | Iso- or terephthalic acid production in and recovery from benzoic acid-water solvent system |
US5292934A (en) * | 1992-06-18 | 1994-03-08 | Amoco Corporation | Method for preparing aromatic carboxylic acids |
US5612007A (en) * | 1994-10-14 | 1997-03-18 | Amoco Corporation | Apparatus for preparing aromatic carboxylic acids with efficient energy recovery |
US6307099B1 (en) * | 1997-02-27 | 2001-10-23 | E. I. Du Pont De Nemours And Company | Production of terephthalic acid |
US6034269A (en) | 1998-08-03 | 2000-03-07 | E. I. Du Pont De Nemours And Company | Process for producing pure carboxylic acids |
-
2001
- 2001-01-19 CN CNB018038433A patent/CN1227208C/zh not_active Expired - Fee Related
- 2001-01-19 AU AU2001232878A patent/AU2001232878A1/en not_active Abandoned
- 2001-01-19 BR BR0107739-2A patent/BR0107739A/pt not_active IP Right Cessation
- 2001-01-19 MX MXPA02007123A patent/MXPA02007123A/es unknown
- 2001-01-19 EP EP01904949A patent/EP1257520A1/en not_active Withdrawn
- 2001-01-19 TR TR2002/01833T patent/TR200201833T2/xx unknown
- 2001-01-19 UA UA2002086885A patent/UA73971C2/uk unknown
- 2001-01-19 RU RU2002121869/04A patent/RU2259346C2/ru not_active IP Right Cessation
- 2001-01-19 CA CA002396967A patent/CA2396967A1/en not_active Abandoned
- 2001-01-19 WO PCT/US2001/001909 patent/WO2001053246A1/en active Application Filing
- 2001-01-19 US US09/766,192 patent/US6562997B2/en not_active Expired - Fee Related
- 2001-01-19 JP JP2001553253A patent/JP2003520263A/ja active Pending
- 2001-01-19 KR KR1020027009334A patent/KR20020069261A/ko not_active Application Discontinuation
Also Published As
Publication number | Publication date |
---|---|
AU2001232878A1 (en) | 2001-07-31 |
CN1395554A (zh) | 2003-02-05 |
US6562997B2 (en) | 2003-05-13 |
EP1257520A1 (en) | 2002-11-20 |
JP2003520263A (ja) | 2003-07-02 |
RU2259346C2 (ru) | 2005-08-27 |
CA2396967A1 (en) | 2001-07-26 |
TR200201833T2 (tr) | 2002-12-23 |
UA73971C2 (en) | 2005-10-17 |
CN1227208C (zh) | 2005-11-16 |
WO2001053246A1 (en) | 2001-07-26 |
KR20020069261A (ko) | 2002-08-29 |
MXPA02007123A (es) | 2002-12-13 |
RU2002121869A (ru) | 2004-01-10 |
US20010041811A1 (en) | 2001-11-15 |
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Legal Events
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B25G | Requested change of headquarter approved |
Owner name: BP CORPORATION NORTH AMERICA INC. (US) Free format text: SEDE ALTERADA CONFORME SOLICITADO NA PETICAO NO 020060184537/RJ DE 12/12/2006. |
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B08F | Application fees: application dismissed [chapter 8.6 patent gazette] |
Free format text: REFERENTE A 8A, 9A E 10A ANUIDADE(S). |
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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 2116 DE 26/07/2011. |