Clariant Produkte (deutschland) Gmbh

Evonik Degussa Gmbh

Linde Aktiengesellschaft

Technische Universitat Munchen

Clariant Produkte Gmbh

Maria Cruz Sanchez-Sanchez

Johannes Lercher

Gerhard Mestl

Klaus Wanninger

Julia Tseglakova

Daniel Melzer

Guido Stochniol

Stephan Peitz

Andreas Meiswinkel

Florian Winkler

Karl-Heinz Hofmann

Hans-Jörg Zander

Christian Thaller

Daniela Hartmann

Andre Cornelis Van Veen

Andreas Ehrmaier

Ricardo Bermejo De Val

Yue Liu

A novel mixed oxide material is disclosed which comprises molybdenum, vanadium, tellurium and niobium and the use of the mixed oxide material as catalyst for the oxidative dehydrogenation of ethane to ethene or the oxidation of propane to acrylic acid and a process for producing the mixed oxide material.

Synthesis of a MoVNbTe catalyst having an increased specific surface and higher activity for the oxidative dehydrogenation of ethane to ethylene

A novel mixed oxide material is disclosed which contains molybdenum, vanadium, tellurium and niobium and the use of the molybdenum mixed oxide material as catalyst for the oxidative dehydrogenation of ethane to ethene or the oxidation of propane to acrylic acid and a process for producing the mixed oxide material.

Synthesis of a MoVNbTe catalyst having a reduced niobium and tellurium content and higher activity for the oxidative dehydrogenation of ethane

A novel catalyst and process for producing a mixed oxide material containing molybdenum, vanadium, tellurium and niobium is disclosed. The material can be used as a catalyst for the oxidative dehydrogenation of ethane to ethene or the oxidation of propane to acrylic acid.

Synthesis of a moVNbTe catalyst from low-cost metal oxides

The invention relates to a catalyst system for oligomerizing olefins over a catalyst comprising nickel, to the use of this catalyst and to a method for dimerizing olefins.

Selective oligomerization of olefins

A process for preparing a catalyst provided in the form of a metal oxide catalyst having at least one element selected from Mo, Te, Nb, V, Cr, Dy, Ga, Sb, Ni, Co, Pt and Ce. The catalyst is subjected to an aftertreatment to increase the proportion of the M1 phase, by contacting the catalyst with steam at a pressure below 100 bar or by contacting the catalyst with oxygen to obtain an aftertreated catalyst. The aftertreated catalyst may be used for oxidative dehydrogenation processes.

Process for preparing a catalyst, catalyst and process for the oxidative dehydrogenation of hydrocarbons

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Munich, Germany

Maria Cruz Sanchez-Sanchez