US7485747B2
(en)
*
|
2001-06-04 |
2009-02-03 |
Eastman Chemical Company |
Two stage oxidation process for the production of aromatic dicarboxylic acids
|
US7196215B2
(en)
|
2001-06-04 |
2007-03-27 |
Eastman Chemical Company |
Process for the production of purified terephthalic acid
|
US20040215036A1
(en)
*
|
2003-04-25 |
2004-10-28 |
Robert Lin |
Method for heating a crude carboxylic acid slurry in a post oxidation zone by the addition of steam
|
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
|
US7381386B2
(en)
*
|
2003-06-05 |
2008-06-03 |
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
|
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
|
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
|
US7105710B2
(en)
*
|
2003-09-26 |
2006-09-12 |
Shell Oil Company |
Process of preparing an alkylene glycol
|
KR100650536B1
(ko)
*
|
2003-12-19 |
2006-11-27 |
미쓰이 가가쿠 가부시키가이샤 |
테레프탈산의 제조 방법
|
JP4657674B2
(ja)
*
|
2003-12-19 |
2011-03-23 |
三井化学株式会社 |
テレフタル酸の製造方法
|
WO2006088470A2
(en)
*
|
2004-04-09 |
2006-08-24 |
Gtc Technology Inc. |
Purification of carboxylic acids by complexation with selective solvents
|
US20050283022A1
(en)
*
|
2004-06-18 |
2005-12-22 |
Sheppard Ronald B |
Filtrate preparation process for terephthalic acid filtrate treatment
|
IN2015DN00761A
(pt)
*
|
2004-09-02 |
2015-07-10 |
Grupo Petrotemex Sa De Cv |
|
JP2008511653A
(ja)
*
|
2004-09-02 |
2008-04-17 |
イーストマン ケミカル カンパニー |
芳香族ジカルボン酸の最適化製造
|
US7608733B2
(en)
*
|
2004-09-02 |
2009-10-27 |
Eastman Chemical Company |
Optimized liquid-phase oxidation
|
US7507857B2
(en)
|
2004-09-02 |
2009-03-24 |
Eastman Chemical Company |
Optimized liquid-phase oxidation
|
US20080161598A1
(en)
*
|
2004-09-02 |
2008-07-03 |
Eastman Chemical Company |
Optimized Production of Aromatic Dicarboxylic Acids
|
CN101768034A
(zh)
*
|
2004-09-02 |
2010-07-07 |
伊士曼化工公司 |
优化的液相氧化
|
US7888530B2
(en)
*
|
2004-09-02 |
2011-02-15 |
Eastman Chemical Company |
Optimized production of aromatic dicarboxylic acids
|
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
|
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
|
US7572936B2
(en)
|
2004-09-02 |
2009-08-11 |
Eastman Chemical Company |
Optimized liquid-phase oxidation
|
US7692036B2
(en)
*
|
2004-11-29 |
2010-04-06 |
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
|
US7582793B2
(en)
|
2004-09-02 |
2009-09-01 |
Eastman Chemical Company |
Optimized liquid-phase oxidation
|
US7568361B2
(en)
|
2004-09-02 |
2009-08-04 |
Eastman Chemical Company |
Optimized liquid-phase oxidation
|
US20070238899A9
(en)
*
|
2004-09-02 |
2007-10-11 |
Robert Lin |
Optimized production of aromatic dicarboxylic acids
|
US7273559B2
(en)
*
|
2004-10-28 |
2007-09-25 |
Eastman Chemical Company |
Process for removal of impurities from an oxidizer purge stream
|
US7291270B2
(en)
*
|
2004-10-28 |
2007-11-06 |
Eastman Chemical Company |
Process for removal of impurities from an oxidizer purge stream
|
ATE348093T1
(de)
*
|
2004-12-15 |
2007-01-15 |
Saudi Basic Ind Corp |
Verfahren zur herstellung gereinigter terephtalsäure
|
US7550627B2
(en)
*
|
2005-03-08 |
2009-06-23 |
Eastman Chemical Company |
Processes for producing aromatic dicarboxylic acids
|
US20060205974A1
(en)
*
|
2005-03-08 |
2006-09-14 |
Lavoie Gino G |
Processes for producing aromatic dicarboxylic acids
|
US20060264662A1
(en)
*
|
2005-05-19 |
2006-11-23 |
Gibson Philip E |
Esterification of an enriched composition
|
US7834208B2
(en)
*
|
2005-05-19 |
2010-11-16 |
Eastman Chemical Company |
Process to produce a post catalyst removal composition
|
US7919652B2
(en)
*
|
2005-05-19 |
2011-04-05 |
Eastman Chemical Company |
Process to produce an enriched composition through the use of a catalyst removal zone and an enrichment zone
|
US7432395B2
(en)
*
|
2005-05-19 |
2008-10-07 |
Eastman Chemical Company |
Enriched carboxylic acid composition
|
US7880031B2
(en)
|
2005-05-19 |
2011-02-01 |
Eastman Chemical Company |
Process to produce an enrichment feed
|
US7304178B2
(en)
|
2005-05-19 |
2007-12-04 |
Eastman Chemical Company |
Enriched isophthalic acid composition
|
US7741516B2
(en)
*
|
2005-05-19 |
2010-06-22 |
Eastman Chemical Company |
Process to enrich a carboxylic acid composition
|
US7557243B2
(en)
*
|
2005-05-19 |
2009-07-07 |
Eastman Chemical Company |
Enriched terephthalic acid composition
|
US7897809B2
(en)
*
|
2005-05-19 |
2011-03-01 |
Eastman Chemical Company |
Process to produce an enrichment feed
|
US7884231B2
(en)
*
|
2005-05-19 |
2011-02-08 |
Eastman Chemical Company |
Process to produce an enriched composition
|
US20060264664A1
(en)
*
|
2005-05-19 |
2006-11-23 |
Parker Kenny R |
Esterification of an exchange solvent enriched composition
|
US20060264656A1
(en)
*
|
2005-05-19 |
2006-11-23 |
Fujitsu Limited |
Enrichment process using compounds useful in a polyester process
|
US7884232B2
(en)
|
2005-06-16 |
2011-02-08 |
Eastman Chemical Company |
Optimized liquid-phase oxidation
|
US7569722B2
(en)
|
2005-08-11 |
2009-08-04 |
Eastman Chemical Company |
Process for removal of benzoic acid from an oxidizer purge stream
|
US7402694B2
(en)
*
|
2005-08-11 |
2008-07-22 |
Eastman Chemical Company |
Process for removal of benzoic acid from an oxidizer purge stream
|
US20070155987A1
(en)
*
|
2006-01-04 |
2007-07-05 |
O'meadhra Ruairi S |
Oxidative digestion with optimized agitation
|
US20070179312A1
(en)
*
|
2006-02-02 |
2007-08-02 |
O'meadhra Ruairi Seosamh |
Process for the purification of a crude carboxylic axid slurry
|
US7880032B2
(en)
|
2006-03-01 |
2011-02-01 |
Eastman Chemical Company |
Versatile oxidation byproduct purge process
|
US20070208194A1
(en)
*
|
2006-03-01 |
2007-09-06 |
Woodruff Thomas E |
Oxidation system with sidedraw secondary reactor
|
US7326807B2
(en)
*
|
2006-03-01 |
2008-02-05 |
Eastman Chemical Company |
Polycarboxylic acid production system with enhanced heating for oxidative digestion
|
US7897808B2
(en)
*
|
2006-03-01 |
2011-03-01 |
Eastman Chemical Company |
Versatile oxidation byproduct purge process
|
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
|
US20070208199A1
(en)
*
|
2006-03-01 |
2007-09-06 |
Kenny Randolph Parker |
Methods and apparatus for isolating carboxylic acid
|
US7863483B2
(en)
*
|
2006-03-01 |
2011-01-04 |
Eastman Chemical Company |
Carboxylic acid production process
|
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
|
US7393973B2
(en)
*
|
2006-03-01 |
2008-07-01 |
Eastman Chemical Company |
Polycarboxylic acid production system with enhanced residence time distribution for oxidative digestion
|
US8173836B2
(en)
*
|
2006-03-01 |
2012-05-08 |
Grupo Petrotemex, S.A. De C.V. |
Method and apparatus for drying carboxylic acid
|
US7863481B2
(en)
*
|
2006-03-01 |
2011-01-04 |
Eastman Chemical Company |
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
|
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
|
US20070203359A1
(en)
|
2006-03-01 |
2007-08-30 |
Philip Edward Gibson |
Versatile oxidation byproduct purge process
|
US7888529B2
(en)
*
|
2006-03-01 |
2011-02-15 |
Eastman Chemical Company |
Process to produce a post catalyst removal composition
|
US7420082B2
(en)
*
|
2006-03-01 |
2008-09-02 |
Eastman Chemical Company |
Polycarboxylic acid production system employing hot liquor removal downstream of oxidative digestion
|
US7816556B2
(en)
*
|
2006-03-01 |
2010-10-19 |
Eastman Chemical Company |
Polycarboxylic acid production system employing enhanced multistage oxidative digestion
|
US9205388B2
(en)
*
|
2007-06-27 |
2015-12-08 |
H R D Corporation |
High shear system and method for the production of acids
|
KR100934163B1
(ko)
|
2007-10-01 |
2009-12-29 |
주식회사 효성 |
결정화 공정을 이용한 고순도 나프탈렌디카르복실산의분리정제 방법 및 장치
|
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
|
RU2527035C2
(ru)
*
|
2009-04-24 |
2014-08-27 |
Инвиста Текнолоджиз С.А.Р.Л. |
Способы, процессы и системы для обработки и очистки сырой терефталевой кислоты и ассоциированные потоки процесса
|
US8968686B2
(en)
*
|
2010-01-29 |
2015-03-03 |
Grupo Petrotemex, S.A. De C.V. |
Oxidation system with sidedraw secondary reactor
|
US8936767B2
(en)
*
|
2010-01-29 |
2015-01-20 |
Grupo Petrotemex. S.A. de C.V. |
Oxidation system with sidedraw secondary reactor
|
US8790601B2
(en)
*
|
2010-01-29 |
2014-07-29 |
Grupo Petrotemex, S.A. De C.V. |
Oxidation system with sidedraw secondary reactor
|
US8835678B2
(en)
|
2010-06-30 |
2014-09-16 |
Uop Llc |
Solid terephthalic acid composition
|
US8884055B2
(en)
*
|
2010-06-30 |
2014-11-11 |
Uop Llc |
Process for producing terephthalic acid
|
US8933265B2
(en)
|
2010-06-30 |
2015-01-13 |
Uop Llc |
Process for oxidizing alkyl aromatic compounds
|
US8933266B2
(en)
|
2010-06-30 |
2015-01-13 |
Uop Llc |
Process for producing terephthalic acid
|
US8754254B2
(en)
|
2010-06-30 |
2014-06-17 |
Uop Llc |
Process for purifying terephthalic acid
|
US8884054B2
(en)
|
2010-06-30 |
2014-11-11 |
Uop Llc |
Process for oxidizing alkyl aromatic compounds
|
US9045407B2
(en)
|
2010-06-30 |
2015-06-02 |
Uop Llc |
Mixtures used in oxidizing alkyl aromatic compounds
|
US9963413B2
(en)
|
2010-08-20 |
2018-05-08 |
Grupo Petrotemex, S.A. De C.V. |
Terephthalic acid purge filtration rate by controlling % water in filter feed slurry
|
US8167974B2
(en)
*
|
2010-08-20 |
2012-05-01 |
Grupo Petrotemex, S.A. De C.V. |
Terephthalic acid purge filtration rate by controlling % water in filter feed slurry
|
US8466312B2
(en)
*
|
2010-08-20 |
2013-06-18 |
Grupo Petrotemex, S.A. De C.V. |
Terephthalic acid purge filtration rate by controlling % water in filter feed slurry
|
EP2522426B1
(en)
|
2011-05-12 |
2014-02-12 |
King Saud University |
Method for preparing carboxylic acids
|
US9573120B2
(en)
|
2014-05-08 |
2017-02-21 |
Eastman Chemical Company |
Furan-2,5-dicarboxylic acid purge process
|
US8791278B2
(en)
|
2011-05-24 |
2014-07-29 |
Eastman Chemical Company |
Oxidation process to produce a crude and/or purified carboxylic acid product
|
US9199958B2
(en)
|
2011-05-24 |
2015-12-01 |
Eastman Chemical Company |
Oxidation process to produce a crude and/or purified carboxylic acid product
|
US8791277B2
(en)
|
2011-05-24 |
2014-07-29 |
Eastman Chemical Company |
Oxidation process to produce a crude and/or purified carboxylic acid product
|
US20120302768A1
(en)
|
2011-05-24 |
2012-11-29 |
Eastman Chemical Company |
Oxidation process to produce a crude and/or purified carboxylic acid product
|
US8846960B2
(en)
|
2011-05-24 |
2014-09-30 |
Eastman Chemical Company |
Oxidation process to produce a crude and/or purified carboxylic acid product
|
US8748479B2
(en)
*
|
2012-06-22 |
2014-06-10 |
Eastman Chemical Company |
Process for purifying crude furan 2,5-dicarboxylic acid using hydrogenation
|
US8969404B2
(en)
*
|
2012-06-22 |
2015-03-03 |
Eastman Chemical Company |
Purifying crude furan 2,5-dicarboxylic acid by hydrogenation
|
US9029580B2
(en)
|
2012-07-20 |
2015-05-12 |
Eastman Chemical Company |
Oxidation process to produce a purified carboxylic acid product via solvent displacement and post oxidation
|
US8809556B2
(en)
|
2012-07-20 |
2014-08-19 |
Eastman Chemical Company |
Oxidation process to produce a purified carboxylic acid product via solvent displacement and post oxidation
|
US8772513B2
(en)
|
2012-08-30 |
2014-07-08 |
Eastman Chemical Company |
Oxidation process to produce a crude dry carboxylic acid product
|
US9156805B2
(en)
|
2012-11-20 |
2015-10-13 |
Eastman Chemical Company |
Oxidative purification method for producing purified dry furan-2,5-dicarboxylic acid
|
US8916720B2
(en)
|
2012-11-20 |
2014-12-23 |
Eastman Chemical Company |
Process for producing dry purified furan-2,5-dicarboxylic acid with oxidation off-gas treatment
|
US8916719B2
(en)
|
2012-11-20 |
2014-12-23 |
Eastman Chemical Company |
Process for producing dry purified furan-2,5-dicarboxylic acid with oxidation off-gas treatment
|
US9943834B2
(en)
|
2014-05-08 |
2018-04-17 |
Eastman Chemical Company |
Furan-2,5-dicarboxylic acid purge process
|
EP3012244A1
(en)
*
|
2014-10-24 |
2016-04-27 |
Sulzer Chemtech AG |
Process and apparatus for purification of acrylic acid
|
US20160264511A1
(en)
*
|
2015-03-13 |
2016-09-15 |
Grupo Petrotemex, S.A. De C.V. |
Bubble column reactor based digester and method for its use
|
EP3277656A1
(en)
*
|
2015-03-31 |
2018-02-07 |
SABIC Global Technologies B.V. |
Method for purification of an aromatic diacid or the corresponding anhydride
|
WO2016157018A1
(en)
*
|
2015-03-31 |
2016-10-06 |
Sabic Global Technologies B.V. |
Method for purification of a aromatic diacid or the corresponding anhydrides
|
CN105085229A
(zh)
*
|
2015-09-02 |
2015-11-25 |
刘健 |
限定稀土材料的回收涤纶碱减量废渣中对苯二甲酸的方法
|
CN105130797A
(zh)
*
|
2015-09-02 |
2015-12-09 |
刘健 |
优化参数的回收涤纶碱减量废渣中对苯二甲酸的方法
|
CN105085230A
(zh)
*
|
2015-09-02 |
2015-11-25 |
刘健 |
一种用混合溶剂回收涤纶碱减量废渣中对苯二甲酸的方法
|
PT3397610T
(pt)
*
|
2015-12-31 |
2021-03-03 |
Bp Corp North America Inc |
Processo de recuperação de ácido acético de correntes aquosas
|
TW201823193A
(zh)
*
|
2016-12-29 |
2018-07-01 |
美商Bp公司北美股份有限公司 |
經純化的對苯二甲酸(pta)排氣孔乾燥器蒸氣流出物處理技術
|
US10000435B1
(en)
*
|
2017-02-28 |
2018-06-19 |
Grupo Petrotemex, S.A. De C.V. |
Energy and environmentally integrated method for production of aromatic dicarboxylic acids by oxidation
|
WO2019005532A1
(en)
*
|
2017-06-29 |
2019-01-03 |
Bp Corporation North America Inc. |
METHODS OF MAKING AROMATIC CARBOXYLIC ACIDS
|
CN110755873A
(zh)
*
|
2019-10-08 |
2020-02-07 |
杭州安永环保科技有限公司 |
一种液态物质连续结晶的生产工艺
|
CN111569788B
(zh)
*
|
2020-03-31 |
2023-04-11 |
南京延长反应技术研究院有限公司 |
对二甲苯制备对苯二甲酸的外置微界面氧化系统及方法
|
CN113731339B
(zh)
*
|
2021-11-08 |
2022-03-11 |
东营威联化学有限公司 |
一种对二甲苯氧化结晶装置
|
KR102658069B1
(ko)
*
|
2022-09-05 |
2024-04-17 |
에스케이케미칼 주식회사 |
테레프탈산의 제조 방법 및 이로부터 제조된 테레프탈산
|