Symyx Technologies, Inc.

Honda Giken Kogyo Kabushiki Kaisha

Archer Daniels Midland Company

Sued-Chemie IP Gmbh & Co. Kg

Clariant Produkte (Deutschland) Gmbh

Sud-Chemie Ag

Rennovia Inc.

Honda Giken Koygo Kabushiki Kaisha

Other

Bayer Aktiengesellschaft

Celanese Gmbh

Celanese Chemicals Europe Gmbh

Symyx Solutions, Inc.

Exxonmobil Research and Engineering Company

Clariant International Ltd

Alfred Gerhard Hagemeyer

Eric L Dias

Gerhard Mestl

Karin Yaccato

Christopher James Brooks

Raymond E Carhart

James A W Shoemaker

Valery Sokolovskii

Guang Zhu

Peter Scheck

Vincent J Murphy

Cory Bernard Phillips

Hong Jiang

Gary Michael Diamond

James M Longmire

Claus G Lugmair

Silvia Neumann

Michael Herrmann

Robert K Grasselli

David M Lowe

Peter Strasser

Lynn Van Erden

Yumin Liu

Anthony F Volpe

Hans-Jörg Wölk

Damodara M Poojary

Carolin Fischer

Uwe Dingerdissen

Mayya Lavrenko

Chuansheng Bai

Daniel Mark Giaquinta

Christian Rasp

Ulrich Notheis

Jason Wu

Frank Grossmann

Xiao Ping Zhou

Jun Han

El-Mekki El-Malki

Mingyong Sun

Andreas Lesik

Normen Szesni

Jozsef Margitfalvi

Oliver Wegner

Roman Bobka

Elif Ispir Gürbüz

Alice Kyriopoulos

Lajos Istvan Vegvari

Andras Tompos

James Aw Shoemaker

Pallassana S Venkataraman

Johannes Heitz

Joshua Terrian

Peter W Jacobs

Harald Werner

Ralph Armbrust

Klaus K&uuml;hlein

Prasenjeet Ghosh

Richard Fischer

Jeff Elks

Claus Lugmair

Jennifer Boyer

Hongyi C Hou

Andrew J Ingram

Ramesh Borade

Karl-Heinz Hable

Hans-Joerg Woelk

Frank Groβmann

Sybille Ungar

Zhigou Hou

Dieter B&auml;uerle

Ernst Haberkorn

Stephan Weidlich

Andrea Rutsch

Gerhardt Geiss

Günter Dambeck

Klaus Kühlein

Rudolf Kerscher

George Fredrick Salem

Frank Großmann

David Michael Lowe

Michael Urbancic

James AW Shoemaker

Elif Ispir GÜRBÜZ

Dan Giaquinta

Jon M Mcconnachie

Shaped porous carbon products and processes for preparing these products are provided. The shaped porous carbon products can be used, for example, as catalyst supports and adsorbents. Catalyst compositions including these shaped porous carbon products, processes of preparing the catalyst compositions, and various processes of using the shaped porous carbon products and catalyst compositions are also provided.

Shaped porous carbon products

The present invention provides a porous metal-containing carbon-based material that is stable at high temperatures under aqueous conditions. The porous metal-containing carbon-based materials are particularly useful in catalytic applications. Also provided, are methods for making and using porous shaped metal-carbon products prepared from these materials.

Porous shaped metal-carbon products

The present invention relates to a porous catalyst support, consisting of a material comprising a natural sheet silicate, containing ZrOdispersed throughout the material. The present invention also relates to a method for the production of the catalyst support according to the invention and to a shell catalyst containing the catalyst support according to the invention and also the use of the catalyst according to the invention in particular for the production of vinyl acetate monomer (VAM).

Zirconium oxide-doped catalyst support, method for producing the same and catalyst containing a zirconium oxide-doped catalyst support

Industrial scale conversions of 5-hydroxymethylfurfural to commodity chemicals such as 1,2,6-hexanetriol and 1,6-hexanediol by chemocatalytic conversions using hydrogen and a heterogeneous reduction catalyst are provided. The reactions are suitable for use in continuous flow reactors. Methods of carrying out the conversions are provided, as are product and catalyst compositions.

Process for production of hexanetriol from 5-hydroxymethylfurfural

The invention relates to a method for producing a shell catalyst that is suitable for producing vinyl acetate monomer (VAM). The invention further relates to a shell catalyst that is obtainable by the method according to the invention and to the use of the shell catalyst according to the invention for producing VAM.

Post-gilding of PD-AU-coated shell catalysts

A method for producing a shell catalyst which comprises, in the outer shell, one or more of the following metals: Pd, Pt, Ag and Au. Also the use of the shell catalyst produced using the method according to the invention for the production of vinyl acetate monomer, in the hydrogenation of hydrocarbons, in particular the selective hydrogenation of polyunsaturated hydrocarbon compounds, or in the oxidation of alcohols to ketones/aldehydes/carboxylic acids.

Method for producing a metal-containing shell catalyst without intermediate calcining

An open-pore catalyst support comprising a material that comprises a natural sheet silicate and ZrO. In order to provide a catalyst support, by means of which alkenyl acetate catalysts can be prepared which are characterized by a high level of alkenyl acetate activity over a relatively long period, the catalyst support comprises a material that comprises a natural sheet silicate and ZrOin the tetragonal modification.

Catalyst support, process for its preparation and use

The present invention relates to a method for producing a shell catalyst that is suitable for producing vinyl acetate monomer (VAM). The present invention also relates to a shell catalyst that can be obtained by the method according to the invention as well as the use of the shell catalyst according to the invention for producing VAM.

Pre-gold-plating Pd-Au-coated shell catalysts

Disclosed are catalysts comprised of platinum and rhodium on a support selected from the group of zirconia, stabilized (doped) zirconia, zirconia-metal oxide composites, and mixtures thereof, wherein the outer surfaces of the support are selected from the group of zirconia, stabilized zirconia, and mixtures thereof. More particularly, the supported catalysts comprise platinum and rhodium, wherein the molar ratio of platinum to rhodium is in the range of about 3:1 to about 1:2. The average pore diameter of the catalyst supports is in the range of about 5 nm to about 70 nm and the surface area is in the range of about 15 m/g to about 200 m/g. Also disclosed are methods for the hydrodeoxygenation of carboxylic acids, mono- and/or di-lactones thereof having at least one hydroxyl group on the backbone thereof to corresponding acids where the backbone hydroxyl group has been reduced in the presence of the catalyst.

Reduction catalysts

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Sunnyvale, CA, United States of America

Alfred Gerhard Hagemeyer