|
US4054561A
(en)
*
|
1975-01-27 |
1977-10-18 |
Owens-Corning Fiberglas Corporation |
Thermoplastic additives for molding compounds
|
|
US4096102A
(en)
*
|
1975-01-27 |
1978-06-20 |
Owens-Corning Fiberglas Corporation |
Moldable compositions comprising thermosetting polyester resin and thermoplastic resin
|
|
DE3047474C2
(de)
*
|
1980-12-17 |
1983-05-11 |
Didier Engineering Gmbh, 4300 Essen |
Verfahren und Vorrichtung zur kontinuierlichen Herstellung von Polyestern
|
|
EP1453883B1
(en)
*
|
2000-12-07 |
2012-11-21 |
Grupo Petrotemex, S.A. de C.V. |
Low cost polyester process using a pipe reactor
|
|
US6906164B2
(en)
*
|
2000-12-07 |
2005-06-14 |
Eastman Chemical Company |
Polyester process using a pipe reactor
|
|
US7074879B2
(en)
*
|
2003-06-06 |
2006-07-11 |
Eastman Chemical Company |
Polyester process using a pipe reactor
|
|
US7135541B2
(en)
|
2003-06-06 |
2006-11-14 |
Eastman Chemical Company |
Polyester process using a pipe reactor
|
|
US7332548B2
(en)
*
|
2004-03-04 |
2008-02-19 |
Eastman Chemical Company |
Process for production of a polyester product from alkylene oxide and carboxylic acid
|
|
US8557950B2
(en)
|
2005-06-16 |
2013-10-15 |
Grupo Petrotemex, S.A. De C.V. |
High intrinsic viscosity melt phase polyester polymers with acceptable acetaldehyde generation rates
|
|
US7655746B2
(en)
*
|
2005-09-16 |
2010-02-02 |
Eastman Chemical Company |
Phosphorus containing compounds for reducing acetaldehyde in polyesters polymers
|
|
US7838596B2
(en)
*
|
2005-09-16 |
2010-11-23 |
Eastman Chemical Company |
Late addition to effect compositional modifications in condensation polymers
|
|
US9267007B2
(en)
|
2005-09-16 |
2016-02-23 |
Grupo Petrotemex, S.A. De C.V. |
Method for addition of additives into a polymer melt
|
|
US7649109B2
(en)
*
|
2006-12-07 |
2010-01-19 |
Eastman Chemical Company |
Polyester production system employing recirculation of hot alcohol to esterification zone
|
|
US7943094B2
(en)
*
|
2006-12-07 |
2011-05-17 |
Grupo Petrotemex, S.A. De C.V. |
Polyester production system employing horizontally elongated esterification vessel
|
|
US20080139780A1
(en)
*
|
2006-12-07 |
2008-06-12 |
Debruin Bruce Roger |
Polyester production system employing short residence time esterification
|
|
US8901272B2
(en)
*
|
2007-02-02 |
2014-12-02 |
Grupo Petrotemex, S.A. De C.V. |
Polyester polymers with low acetaldehyde generation rates and high vinyl ends concentration
|
|
US7863477B2
(en)
*
|
2007-03-08 |
2011-01-04 |
Eastman Chemical Company |
Polyester production system employing hot paste to esterification zone
|
|
US7872090B2
(en)
*
|
2007-07-12 |
2011-01-18 |
Eastman Chemical Company |
Reactor system with optimized heating and phase separation
|
|
US7858730B2
(en)
*
|
2007-07-12 |
2010-12-28 |
Eastman Chemical Company |
Multi-level tubular reactor with dual headers
|
|
US7868129B2
(en)
*
|
2007-07-12 |
2011-01-11 |
Eastman Chemical Company |
Sloped tubular reactor with spaced sequential trays
|
|
US7829653B2
(en)
*
|
2007-07-12 |
2010-11-09 |
Eastman Chemical Company |
Horizontal trayed reactor
|
|
US7842777B2
(en)
*
|
2007-07-12 |
2010-11-30 |
Eastman Chemical Company |
Sloped tubular reactor with divided flow
|
|
US7847053B2
(en)
*
|
2007-07-12 |
2010-12-07 |
Eastman Chemical Company |
Multi-level tubular reactor with oppositely extending segments
|
|
US7872089B2
(en)
|
2007-07-12 |
2011-01-18 |
Eastman Chemical Company |
Multi-level tubular reactor with internal tray
|
|
US7868130B2
(en)
*
|
2007-07-12 |
2011-01-11 |
Eastman Chemical Company |
Multi-level tubular reactor with vertically spaced segments
|