|
IT1163145B
(it)
*
|
1983-03-11 |
1987-04-08 |
Friuli Chim Spa |
Preparazione di acido benzoico puro
|
|
US5567842A
(en)
*
|
1994-11-16 |
1996-10-22 |
Mitsubishi Chemical Corporation |
Process for producing terephthalic acid
|
|
US5502247A
(en)
*
|
1994-11-17 |
1996-03-26 |
Amoco Corporation |
Process for recovery of aromatic acid or ester and polyol from waste polyester resins
|
|
US6054610A
(en)
*
|
1995-06-07 |
2000-04-25 |
Hfm International, Inc. |
Method and apparatus for preparing purified terephthalic acid and isophthalic acid from mixed xylenes
|
|
US5929274A
(en)
*
|
1995-06-07 |
1999-07-27 |
Hfm International, Inc. |
Method to reduce carboxybenzaldehyde isomers in terephthalic acid or isophthalic acid
|
|
US5767311A
(en)
*
|
1995-06-07 |
1998-06-16 |
Glitsch International, Inc. |
Method and apparatus for preparing purified terephtalic acid
|
|
US5840968A
(en)
*
|
1995-06-07 |
1998-11-24 |
Hfm International, Inc. |
Method and apparatus for preparing purified terephthalic acid
|
|
US6013835A
(en)
*
|
1995-06-07 |
2000-01-11 |
Hfm International, Inc. |
Method and apparatus for preparing purified terephthalic acid
|
|
US7196215B2
(en)
*
|
2001-06-04 |
2007-03-27 |
Eastman Chemical Company |
Process for the production of purified terephthalic acid
|
|
US7485747B2
(en)
*
|
2001-06-04 |
2009-02-03 |
Eastman Chemical Company |
Two stage oxidation process for the production of aromatic dicarboxylic acids
|
|
US6689903B2
(en)
|
2001-06-04 |
2004-02-10 |
Eastman Chemical Company |
Crystallization method for production of purified aromatic dicarboxylic acids
|
|
US7276625B2
(en)
*
|
2002-10-15 |
2007-10-02 |
Eastman Chemical Company |
Process for production of a carboxylic acid/diol mixture suitable for use in polyester production
|
|
CN100453517C
(zh)
*
|
2003-01-10 |
2009-01-21 |
三菱化学株式会社 |
芳香羧酸的制备方法和对苯二甲酸的制备方法
|
|
US7193109B2
(en)
*
|
2003-03-06 |
2007-03-20 |
Eastman Chemical Company |
Process for production of a carboxylic acid/diol mixture suitable for use in polyester production
|
|
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
|
|
US7214760B2
(en)
*
|
2004-01-15 |
2007-05-08 |
Eastman Chemical Company |
Process for production of a carboxylic acid/diol mixture suitable for use in polyester production
|
|
US7546747B2
(en)
*
|
2004-01-15 |
2009-06-16 |
Eastman Chemical Company |
Process for production of a dried carboxylic acid cake suitable for use in polyester production
|
|
NZ549535A
(en)
|
2004-03-17 |
2010-11-26 |
Novartis Ag |
Use of aliskiren for treating renal and other disorders
|
|
US7390921B2
(en)
*
|
2004-09-02 |
2008-06-24 |
Eastman Chemical Company |
Optimized liquid-phase oxidation
|
|
US7563926B2
(en)
*
|
2004-09-02 |
2009-07-21 |
Eastman Chemical Company |
Optimized liquid-phase oxidation
|
|
US7361784B2
(en)
*
|
2004-09-02 |
2008-04-22 |
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
|
|
US7582793B2
(en)
|
2004-09-02 |
2009-09-01 |
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
|
|
US7371894B2
(en)
*
|
2004-09-02 |
2008-05-13 |
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
|
|
US7482482B2
(en)
*
|
2004-09-02 |
2009-01-27 |
Eastman Chemical Company |
Optimized liquid-phase oxidation
|
|
US20060047153A1
(en)
*
|
2004-09-02 |
2006-03-02 |
Wonders Alan G |
Optimized liquid-phase oxidation
|
|
US7572932B2
(en)
*
|
2004-09-02 |
2009-08-11 |
Eastman Chemical Company |
Optimized liquid-phase oxidation
|
|
US7589231B2
(en)
*
|
2004-09-02 |
2009-09-15 |
Eastman Chemical Company |
Optimized liquid-phase oxidation
|
|
US7586000B2
(en)
*
|
2004-09-02 |
2009-09-08 |
Eastman Chemical Company |
Optimized liquid-phase oxidation
|
|
US7507857B2
(en)
*
|
2004-09-02 |
2009-03-24 |
Eastman Chemical Company |
Optimized liquid-phase oxidation
|
|
US7504535B2
(en)
*
|
2004-09-02 |
2009-03-17 |
Eastman Chemical Company |
Optimized liquid-phase oxidation
|
|
US7683210B2
(en)
*
|
2004-09-02 |
2010-03-23 |
Eastman Chemical Company |
Optimized liquid-phase oxidation
|
|
US7608732B2
(en)
*
|
2005-03-08 |
2009-10-27 |
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
|
|
US7608733B2
(en)
*
|
2004-09-02 |
2009-10-27 |
Eastman Chemical Company |
Optimized liquid-phase oxidation
|
|
US7381836B2
(en)
*
|
2004-09-02 |
2008-06-03 |
Eastman Chemical Company |
Optimized liquid-phase oxidation
|
|
US20060264664A1
(en)
*
|
2005-05-19 |
2006-11-23 |
Parker Kenny R |
Esterification of an exchange solvent enriched composition
|
|
US7897809B2
(en)
*
|
2005-05-19 |
2011-03-01 |
Eastman Chemical Company |
Process to produce an enrichment feed
|
|
US7741516B2
(en)
|
2005-05-19 |
2010-06-22 |
Eastman Chemical Company |
Process to enrich a carboxylic acid composition
|
|
US20060264656A1
(en)
*
|
2005-05-19 |
2006-11-23 |
Fujitsu Limited |
Enrichment process using compounds useful in a polyester process
|
|
US7304178B2
(en)
*
|
2005-05-19 |
2007-12-04 |
Eastman Chemical Company |
Enriched isophthalic acid composition
|
|
US7884231B2
(en)
|
2005-05-19 |
2011-02-08 |
Eastman Chemical Company |
Process to produce an enriched composition
|
|
US20060264662A1
(en)
*
|
2005-05-19 |
2006-11-23 |
Gibson Philip E |
Esterification of an enriched composition
|
|
US7880031B2
(en)
*
|
2005-05-19 |
2011-02-01 |
Eastman Chemical Company |
Process to produce an enrichment feed
|
|
US7432395B2
(en)
*
|
2005-05-19 |
2008-10-07 |
Eastman Chemical Company |
Enriched carboxylic acid 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
|
|
US7557243B2
(en)
|
2005-05-19 |
2009-07-07 |
Eastman Chemical Company |
Enriched terephthalic acid composition
|
|
US7884232B2
(en)
*
|
2005-06-16 |
2011-02-08 |
Eastman Chemical Company |
Optimized liquid-phase oxidation
|
|
US7358389B2
(en)
*
|
2006-01-04 |
2008-04-15 |
Eastman Chemical Company |
Oxidation system employing internal structure for enhanced hydrodynamics
|
|
US20070155987A1
(en)
*
|
2006-01-04 |
2007-07-05 |
O'meadhra Ruairi S |
Oxidative digestion with optimized agitation
|
|
US7355068B2
(en)
|
2006-01-04 |
2008-04-08 |
Eastman Chemical Company |
Oxidation system with internal secondary reactor
|
|
US20070179312A1
(en)
*
|
2006-02-02 |
2007-08-02 |
O'meadhra Ruairi Seosamh |
Process for the purification of a crude carboxylic axid slurry
|
|
US7888529B2
(en)
*
|
2006-03-01 |
2011-02-15 |
Eastman Chemical Company |
Process to produce a post catalyst removal composition
|
|
US7462736B2
(en)
*
|
2006-03-01 |
2008-12-09 |
Eastman Chemical Company |
Methods and apparatus for isolating carboxylic acid
|
|
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
|
|
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
|
|
US7772424B2
(en)
*
|
2006-03-01 |
2010-08-10 |
Eastman Chemical Company |
Polycarboxylic acid production system employing enhanced evaporative concentration downstream of oxidative digestion
|
|
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
|
|
US7393973B2
(en)
*
|
2006-03-01 |
2008-07-01 |
Eastman Chemical Company |
Polycarboxylic acid production system with enhanced residence time distribution for oxidative digestion
|
|
US7816556B2
(en)
*
|
2006-03-01 |
2010-10-19 |
Eastman Chemical Company |
Polycarboxylic acid production system employing enhanced multistage oxidative digestion
|
|
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
|
|
US9205388B2
(en)
*
|
2007-06-27 |
2015-12-08 |
H R D Corporation |
High shear system and method for the production of acids
|
|
US8614350B2
(en)
|
2008-01-15 |
2013-12-24 |
Eastman Chemical Company |
Carboxylic acid production process employing solvent from esterification of lignocellulosic material
|
|
US8455680B2
(en)
|
2008-01-15 |
2013-06-04 |
Eastman Chemical Company |
Carboxylic acid production process employing solvent from esterification of lignocellulosic material
|
|
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
|
