Linde Aktiengesellschaft

Basf Se Corporation

Basf Aktiengesellschaft

Thyssenkrupp Industrial Solutions Ag

Linde Gmbh

Wolfgang Alois Hormuth

Otto Machhammer

Grigorios Kolios

Andreas Bode

Christian Schneider

Matthias Kern

Dirk Klingler

Marcus Guzmann

Hans-Juergen Maass

Volker Goeke

Rene Koenig

Jens Bernnat

Philipp Brueggemann

Onno Graalmann

Peter Claassen

Volker Göke

Karsten Büker

Karsten Bueker

Marinus Visseren

Philipp Brüggemann

Hans-Jurgen Mass

Hans-Jurgen Maas

Philipp Bruggemann

Rene Konig

Rene KÖNIG

Hans-Jürgen Mass

Hans-Jürgen Maa

The invention relates to a method of carrying out heat-consuming processes, wherein the total energy required averaged over a year for the heat-consuming process originates from at least two different energy sources, where one of the energy sources is an electric energy source whose power varies in the range from 0 to 100% of the total power required, and three different energy modes can individually provide the total power required for the heat-consuming process: (i) exclusively electric energy, (ii) a mixture of electric energy and at least one further nonelectric energy source or (iii) exclusively nonelectric energy, where the changeover time in which the change from one energy mode to another energy mode is completed is not more than 30 minutes.

Method for performing endothermic processes

The invention relates to a process for utilizing a hydrocarbon-comprising and/or carbon dioxide-comprising coproduct gas, accompanying gas and/or biogas, wherein hydrocarbon-comprising and/or carbon dioxide-comprising coproduct gas, accompanying gas and/or biogas is introduced into a reaction space and the multicomponent mixture comprised in the coproduct gas, accompanying gas and/or biogas is converted in a high-temperature zone at temperatures of more than 1000&#xb0; C. and in the presence of a carrier into a product gas mixture which comprises more than 95% by volume of CO, CO, H, HO, CHand Nand optionally into a carbon-comprising solid which is deposited to an extent of at least 75% by weight, based on the total mass of the carbon-comprising solid, on the carrier where the flow velocity of the gas mixture of coproduct gas, accompanying gas and/or biogas in the reaction zone is less than 20 m/s.

Process for utilizing blast furnace gases, associated gases and/or biogases

The invention relates to a process for parallel preparation of hydrogen and one or more carbonaceous products, in which hydrocarbons are introduced into a reaction space (R) and decomposed thermally to carbon and hydrogen in the presence of carbon-rich pellets (W). It is a feature of the invention that at least a portion of the thermal energy required for the hydrocarbon decomposition is introduced into the reaction space (R) by means of a gaseous heat carrier.

Method for the parallel production of hydrogen and carbon-containing products

Process for the production of synthesis gas (), in which methane and carbon dioxide () are introduced into a reaction space (R) and reacted in the presence of a solid (W) at elevated temperatures to give hydrogen and carbon monoxide. Methane and carbon dioxide are passed through a carbon-containing granular material (W) and reacted in a high-temperature zone (H).

Process for production of synthesis gas

An aqueous polymer dispersion is prepared by free radical aqueous emulsion polymerization of a mixture of monomers having at least one ethylenically unsaturated group, which comprises at least 30% by weight of monomers having two conjugated ethylenically unsaturated double bonds, by a process in which the polymerization temperature is varied in the course of the free radical aqueous emulsion polymerization.

Preparation of an aqueous polymer dispersion

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St. Martin, Germany

Wolfgang Alois Hormuth