US2012041217A1
|
|
Two-stage calcination for catalyst production
|
TW200920478A
|
|
Chemical process optimization method that considers chemical process plant safety
|
CA2687234A1
|
|
Start-up of high selectivity catalysts in olefin oxide plants
|
US2009277305A1
|
|
Recovery of rhenium
|
US2009227820A1
|
|
Geometrically sized solid shaped carrier for olefin epoxidation catalyst
|
US2009099393A1
|
|
Solid catalyst useful for converting an alkylene oxide to an alkylene glycol
|
US2009082584A1
|
|
Process for initiating a highly selective ethylene oxide catalyst
|
US2009069583A1
|
|
Ethylene oxide production using fixed moderator concentration
|
US2009062556A1
|
|
Carrier for olefin oxide catalyst
|
US2009062557A1
|
|
Process for production of an olefin oxide
|
US2008300431A1
|
|
Process for preparing an alkylene glycol
|
US2008081920A1
|
|
Catalyst with bimodal pore size distribution and the use thereof
|
KR20080039486A
|
|
Process for preparation of catalyst carrier and its use in catalyst preperation
|
CN101237927A
|
|
Process for preparation of a catalyst carrier
|
US2007249848A1
|
|
Yield improvement in the production of maleic anhydride
|
US2007240974A1
|
|
Method of corrosion prevention
|
US2007225511A1
|
|
Activation of high selectivity ethylene oxide catalyst
|
US2006252643A1
|
|
Nanometer scale restructuring of alumina carrier surface and catalysts for the production of alkene oxides
|
US2006183927A1
|
|
Ethylene oxide plant operation
|
US7294317B2
|
|
Exothermic reaction system
|