Thyssen Krupp Ag

Basf Se Corporation

Evonik Degussa Gmbh

Uhde Gmbh

Thyssenkrupp Industrial Solutions Ag

Thyssenkrupp Uhde Gmbh

Linde Gmbh

Karsten Büker

Otto Machhammer

Georg Markowz

Grigorios Kolios

Markus Oles

Andreas Bode

Heinz Posselt

Dirk Klingler

Olaf Von Morstein

Volker Göke

Frederik Scheiff

Hans-Jörg Zander

Wolfgang Alois Hormuth

Nicolai Antweiler

Andreas Geisselmann

Bernd Langanke

Ralph Kleinschmidt

Peter Schmöle

Jens Wagner

Reinhold Achatz

Hans-Juergen Maass

Volker Goeke

Martin Schmitz-Niederau

Denis Krotov

Elias Johannes Klemm

Reinhard Machnik

Hans-Jürgen Maass

Frank Becker

Klaus Thomas Schwarz

Steffen Schirmeister

Dieter Flick

Markus Weikl

Matthias Kern

Achim Wechsung

Philipp Brüggemann

Rene KÖNIG

Ralf Hausmann

The invention relates to a reactor comprising a moving bed of solid particles that move in the direction of gravitation, and to a method for heating a reactor that comprises a moving bed, for the purpose of pyrolysis reactions.

Directly electrical heated reactor

The invention relates to a process for producing hydrogen, carbon monoxide and a carbon-containing product in at least one reaction apparatus, wherein the at least one reaction apparatus comprises a bed of carbon-containing material and is characterized in that the bed of carbon-containing material in the at least one reaction apparatus is alternately heated to a temperature of >800° C. and, no later than upon reaching a temperature of 1800° C., cooled to a maximum of 800° C., wherein hydrogen and carbon monoxide are produced during the heating phase and carbon and hydrogen are produced during the cooling phase.

Process and device for producing hydrogen, carbon monoxide and a carbon-containing product

A method for producing synthesis gas may involve introducing a hydrocarbon-containing coke-oven gas and a carbon dioxide-containing converter gas into a first reaction zone where hydrogen present in the hydrocarbon-containing coke-oven gas reacts at least partly with carbon dioxide to form water, which reacts thermally with hydrocarbon to form synthesis gas containing carbon monoxide and hydrogen. The method may further involve introducing an oxygen-containing gas in a second reaction zone, and using the oxygen-containing gas and some hydrogen from the first reaction zone to produce thermal energy. Still further, the method may involve supplying the thermal energy produced in the second reaction zone to the first reaction zone.

Method for producing synthesis gas

The invention relates to a method for producing syngas in combined operation with a metallurgical plant which comprises at least one blast furnace for producing crude iron, a converter steel mill and a coke-oven plant. Part of the blast-furnace top gas that is produced in the production of crude iron and/or part of the converter gas that occurs in the converter steel mill and/or part of the coke-oven gas that is produced in the coke-oven plant are mixed. By choosing the gas streams that are brought together to form a mixed gas and/or by changing the mixing ratios of the gas streams that are brought together, at least two streams of useful gas are produced, differing with regard to their composition and respectively prepared to form streams of syngas.

Method for generating synthesis gas in conjunction with a smelting works

Supports having a catalytic coating comprising at least one porous and cavity-containing catalyst layer are described, cavities being irregular spaces having dimensions greater than 5 &#x3bc;m in at least two dimensions or having cross-sectional areas of at least 10 &#x3bc;m. The catalytic coatings are distinguished by a high adhesive strength and can preferably be used in microreactors.

Catalyst-coated support, method for producing the same, reactor comprising the same and use thereof

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Dortmund, Germany

Karsten Büker