Fraunhofer-Gesellschaft Zur Foerderung Der Angewandten Forschung E.V.

Forschungszentrum Karlsruhe Gmbh

Sea Marconi Technologies Di Wander Tumiatti S.a.s.

Ykk Corporation

Karlsruher Institut Fur Technologie

Wse Bioenergy Ug

Andreas Hornung

Andreas Apfelbacher

Herbert Vogel

Miloud Ouadi

Johannes Neumann

Samir Binder

Helmut Seifert

Wander Tumiatti

Thorsten Hornung

Michael Jakuttis

Carlo Maria Roggero

Peter Hense

Daniela Dommel

Clemens Schmetterer

Karl Appenzeller

Susanne Donner

Aliaksandr Balabanovich

Alberto Pedrazzini

Jonathan Aigner

Henning Bockhorn

Sonja Verena Herrmann

Alfons Drochner

Andreas Weddigen

Ulrich Wirtz

Katharina Reh

Martin Meiller

Martin Nieberl

Matthias Franke

Robert Daschner

A method for producing a pyrolysis oil is described. In said method, a feedstock to be treated is first pyrolyzed in a pyrolysis zone, in which the feedstock is heated to a temperature of 250 degrees Celsius to 700 degrees Celsius; and pyrolyzed solids and pyrolysis vapors are formed. The pyrolysis vapors are then reformed at a temperature of 450 degrees Celsius to 1,200 degrees Celsius in a post-conditioning zone, in which the pyrolysis vapors are brought into contact with a catalyst bed, wherein the pyrolysis oil is formed. In this case, the catalyst comprises a pyrolyzed solid, which can be obtained according to the pyrolysis, described above. Finally the pyrolysis oil is separated from the additional pyrolysis products, which are formed, in a separation unit.

Pyrolysis oil and method and system for the production thereof

A process for dehydrogenating organic molecules (OM) and a reaction vessel (RB) suitable for the process for dehydrogenating organic molecules by means of an inductive field (IF), wherein the reaction vessel comprises a device for generating an inductive field and a solid loose material (FLM), and wherein the reaction vessel and its contents are free of platinum, palladium, rhodium, gold, iridium, titanium, tantalum or ruthenium.

Method for the dehydrogenation of organic molecules

A reaction device is provided with a first wall that defines an interior in which a stirring mechanism is located. A heat exchanger is at least partly provided on the first outer wall surface facing away from the interior and/or on the stirring mechanism, wherein the heat exchanger has a grate structure, and at least two layers are provided which have a grate structure. Thus, it is possible to transfer heat in a precise and efficient manner primarily by means of thermal radiation in endothermic processes at different temperature levels, in particular pyrolysis, gassing, and reforming processes, and thereby use the exhaust heat for other processes.

Reaction device with heat exchanger and use thereof

A catalyst support may be provided that comprises: an inner core, which includes at least one phase change material; a coating layer around the inner core, which includes at least one metal oxide; a catalytically active layer, which is positioned in interstices of the coating layer and/or lying on the coating layer, wherein at least one catalytically active substance is included in the catalytically active layer; and a supporting layer which is positioned under the coating layer. A recycle reactor may be provided comprising a reservoir for accommodating a chemical hydrogen storage substance; the catalyst support; a screw conveyor for input and transport of the catalyst support; and a heating device with which the catalyst support can be heated. A method for releasing hydrogen from a chemical hydrogen storage substance may be provided.

Catalyst support, recycle reactor and method for releasing hydrogen

Systems and methods for thermocatalytic treatment of material are provided. The system can have a charging region to supply starting material, a preconditioning zone in which preconditioned material is formed from the starting material, a pyrolysis zone in which pyrolyzed material is formed from the preconditioned material, and a separation unit for separation of the pyrolyzed material. In the preconditioning zone and the pyrolysis zone, a heater can be provided for heating of the material. Also provided in the pyrolysis zone are recirculation means with which a solid portion of the pyrolyzed material can be recirculated directly into the region of the pyrolysis zone facing toward the preconditioning zone.

System and method for thermocatalytic treatment of material and pyrolysis oil produced therewith

In a method for the treatment of halogen containing waste materials wherein valuable materials and/or energy can be recuperated without the generation of additional halogenated waste materials, the halogen containing waste materials are mixed with a molten substituted or non-substituted polyolefin in an inert gas atmosphere, whereby, upon melting, hydrogen halogenides are formed and the hydrogen halogenides are separated from the mixture.

Method for treating waste materials containing halogen

The plant for the thermal treatment of material, in particular scrap material, comprises at least a reaction zone within a rotary kiln having the longitudinal axis inclined of an angle in the range 0&#xb0;&#xb1;45&#xb0; with regard to an horizontal plane and provided of first heating means and of at least a rotary screw having second heating means. The screw shaft is hollow and has, at least locally, apertures allowing the flow of gas from and/or into the reaction zone, a plurality of thermally conductive particles being movable within the reaction zone.

Plant for the thermal treatment of material and operation process thereof

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Karlsruhe, Germany

Andreas Hornung