Albemarle Netherlands B.v.

Exxonmobil Research and Engineering Company

Eelko Brevoord

Stephan Janbroers

Stuart Leon Soled

Paul O'Connor

Sabato Miseo

Kenneth L Riley

Sonja Eijsbouts

Frans Lodewijk Plantenga

Robertus Gerardus Leliveld

Marinus Bruce Cerfontain

Edwin Mark Berends

Mark Hendrikus Harte

Francisco René Mas Cabre

Martinus Johannes Maria Baas

Paul O'connor

Martinus Johannes Baas

Paul O'CONNOR

A method for the hydrodeoxygenation of an oxygenate feedstock comprising contacting the feedstock with a sulphided catalyst composition under hydrodeoxygenation conditions, wherein the catalyst composition comprises: i) a porous carrier substantially comprised of alumina, the carrier comprising between about 0.001 and about 1 wt. % phosphorous and between about 0.001 and about 1 wt. % silicon (both calculated as oxides) and having a mean pore diameter in the range from about 5 nm to about 40 nm; and, ii) from about 1 to about 20 wt. % of an active metal component (calculated as oxides based on the weight of the composition) borne on said porous carrier and which comprises at least one Group VIB metal and at least one Group VIII metal.

Catalytic hydrodeoxygenation of an oxygenate feedstock

A process for the production of a ketone having a carbon number between about 20 and about 40 comprising contacting fatty acids containing from about 10 to about 21 carbons atoms with a hydrotalcite catalyst under conditions effective to decarboxylate said acids. More particularly said decarboxylation conditions comprise: a temperature in the range between about 300&#xb0; C. and about 400&#xb0; C.; a pressure in the range between about 0.01 and about 5 bar; and a weight hourly space velocity (WHSV) of from about 0.1 to about 10 hr.

Process for the decarboxylation of fatty acids

The present invention pertains to A cyclic process for testing FCC catalysts with resid feedstock on a small scale wherein in a first cycle:

Process for small-scale testing of FCC catalysts

A method for upgrading a naphtha feed to a naphtha product containing less than about 10 wppm of nitrogen and less than about 15 wppm sulfur, the method comprising contacting said naphtha feed with hydrogen in the presence of a bulk multimetallic catalyst under effective reactor conditions to hydrodesulfurize and hydrodenitrogenize said naphtha feed to produce said naphtha product, wherein said bulk multimetallic catalyst comprises at least one Group VIII non-noble metal and at least two Group VIB metals.

Process for upgrading naphtha

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Hoevelaken, Netherlands

Eelko Brevoord