Basf Se Corporation

Linde Aktiengesellschaft

Thyssenkrupp Industrial Solutions Ag

Philip Morris Products S.a.

Rene Koenig

Grigorios Kolios

Matthias Kern

Jens Bernnat

Andreas Bode

Dirk Klingler

Ulrich Mueller

Otto Machhammer

Stefan Maurer

Christian Schneider

Benedikt Kalo

Bernd Zoels

Thomas Geiger

Wolfgang Alois Hormuth

Volker Goeke

Hans-Juergen Maass

Friedrich Glenk

Philipp Brueggemann

Marcus Guzmann

Stephan Andreas Schunk

Jae Hyung Hwang

Ingo Muenster

Volker Klock

Guido Wasserschaff

Eike Hupe

Robert Prunchak

Karsten Bueker

Moritz Ehrenstein

Jose A Jimenez

Ralf Liebscher

Christoffer Kieburg

Joachim Nilges

Achim Wechsung

Sabine Schmidt

Hayder Schneider

Rastko Joksimovic

Guido Norbert Freund

Faizan Islam

A computer-implemented method for controlling and/or monitoring a production plant () is proposed. The production plant () comprises at least one process chain () comprising at least one batch process (). The method comprises the following steps: a) at least one step of determining of input data (), wherein the input data comprises at least one quality criterion and production plant layout data, wherein the step comprises retrieving the production plant layout data and receiving information relating to the quality criterion via at least one communication interface (); b) at least one prediction step (), wherein in the prediction step operating conditions for operating the production plant () are determined by applying at least one trained model () on the input data, wherein the trained model () is at least partially data-driven by being trained on sensor data from historical production runs; c) at least one control and/or monitoring step (), wherein the operating conditions are provided.

Method for controlling and/or monitoring a chemical production plant

The invention is related to a soft-magnetic powder comprising coated particles, the coated particles comprising a core and a shell, the core having an average particle size Din a range from 0.1 μm to 100 μm and comprising iron, wherein the shell has a thickness of not more than 20 nm and comprises at least two solid oxides and wherein the shell comprises at least three layers and the shell comprises more than one layers of a first solid oxide and at least one layer of a second solid oxide, wherein the more than one layers of the first solid oxide and the at least one layer of the second solid oxide are arranged in an alternating manner. The invention is further related to a process for the production of the soft-magnetic powder, a use of the soft-magnetic powder and an electronic component comprising the soft-magnetic powder.

Soft-magnetic powder comprising coated particles

A soft-magnetic powder coated with a silicon-based coating, wherein the silicon-based coating comprises at least one fluorine containing composition of formula (I), SiMOF(I), wherein c is in the range of 0.01 to 0.5, d is in the range of 0.04 to 2, and M is B or Al.

Temperature-stable soft-magnetic powder

The present invention relates to a process for conducting endothermic gas phase or gas-solid reactions, wherein the endothermic reaction is conducted in a production phase in a first reactor zone, the production zone, which is at least partly filled with solid particles, where the solid particles are in the form of a fixed bed, of a moving bed and in sections/or in the form of a fluidized bed, and the product-containing gas stream is drawn off from the production zone in the region of the highest temperature level plus/minus 200 K and the product-containing gas stream is guided through a second reactor zone, the heat recycling zone, which at least partly comprises a fixed bed, where the heat from the product-containing gas stream is stored in the fixed bed, and, in the subsequent purge step, a purge gas is guided through the production zone and the heat recycling zone in the same flow direction, and, in a heating zone disposed between the production zone and the heat recycling zone, the heat required for the endothermic reaction is introduced into the product-containing gas stream and into the purge stream or into the purge stream, and then, in a regeneration phase, a gas is passed through the two reactor zones in the reverse flow direction and the production zone is heated up; the present invention further relates to a structured reactor comprising three zones, a production zone containing solid particles, a heating zone and a heat recycling zone containing a fixed bed, wherein the solid particles and the fixed bed consist of different materials.

Method and device for carrying out endothermic gas phase-solid or gas-solid reactions

The present invention relates to a process for the calcination of a zeolitic material, wherein said process comprises the steps of

Process for the flash calcination of a zeolitic material

A process for the calcination of a zeolitic material, wherein the process contains the steps of (i) providing a zeolitic material containing YOand optionally further containing XOin its framework structure in the form of a powder and/or of a suspension of the zeolitic material in a liquid, wherein Y stands for a tetravalent element and X stands for a trivalent element; (ii) atomization of the powder and/or of the suspension of the zeolitic material provided in (i) in a gas stream for obtaining an aerosol; and (iii) calcination of the aerosol obtained in (ii) for obtaining a calcined powder, a zeolitic material obtained by the above process, and its use as a molecular sieve, as an adsorbent, for ion-exchange, as a catalyst, and/or as a catalyst support.

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 the parallel preparation of hydrogen, carbon monoxide and a carbon-comprising product, wherein one or more hydrocarbons are thermally decomposed and at least part of the pyrolysis gas formed is taken off from the reaction zone of the decomposition reactor at a temperature of from 800 to 1400&#xb0; C. and reacted with carbon dioxide to form a gas mixture comprising carbon monoxide and hydrogen (synthesis gas).

Parallel preparation of hydrogen, carbon monoxide and a carbon-comprising product

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Neustadt, Germany

Rene Koenig