Basf Se Corporation

Linde Aktiengesellschaft

Basf Aktiengesellschaft

Roche Diagnostics Operations, Inc.

Thyssenkrupp Industrial Solutions Ag

Roche Diagnostics Gmbh

F. Hoffmann-la Roche Ag

Linde Gmbh

Christian Schneider

Otto Machhammer

Grigorios Kolios

Andreas Bode

Matthias Kern

Dirk Klingler

Wolfgang Alois Hormuth

Thomas Heidemann

Marcus Guzmann

Sebastian Ahrens

Joana Coelho Tsou

Dieter Stuetzer

Volker Goeke

Hans-Juergen Maass

Ekkehard Schwab

Bilge Yilmaz

Robert Bayer

Martin Karches

Lothar Seidemann

Rene Koenig

Lucia Koenigsmann

Michael Hesse

Annebart Engbert Wentink

Lucia Königsmann

Jens Bernnat

Albena Kostova

Thomas Grassler

Volker Göke

Karsten Büker

Michael Schlei

Celine Liekens

Sebastian Kranz

Philipp Brueggemann

Frank Kiesslich

Achim Gritsch

Leo Denissen

Karsten Bueker

Andreas Heussler

Dieter Stützer

Nikolaus Zafred

Jutta Bickelhaupt

Philipp Brüggemann

Dirk Theis

Hans-Jurgen Mass

Frank Kießlich

Rene KÖNIG

Hans-Jürgen Maa

Hans-Jürgen Mass

Rene Konig

Philipp Bruggemann

Hans-Jurgen Maas

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 producing a particulate, Si-bonded fluidized-bed catalyst having improved abrasion resistance, which comprises the steps

Process for producing an Si-bonded fluidized-bed catalyst

Process for producing an si-bonded fluidized-bed catalyst

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

The invention relates to a process for preparing aromatic amines by catalytically hydrogenating the corresponding aromatic nitro compound, which comprises using a copper catalyst with a support comprising SiO, the SiOhaving been prepared by wet grinding and subsequent spray drying.

Method for producing aromatic amines

The present invention relates to a process for nonoxidatively dehydroaromatizing a reactant stream comprising C-C-aliphatics, comprising the steps of

Process for preparing benzene from methane

The present invention relates to a process for nonoxidatively dehydroaromatizing a reactant stream comprising C-C-aliphatics by converting the reactant stream in the presence of a catalyst in a reaction zoneto a product stream P comprising aromatic hydrocarbons, and regenerating the catalyst whose activity has been reduced by deposited coke with a hydrogen-comprising mixture H in a reaction zone, wherein at least a portion of the deposited coke is converted to methane and at least a portion of the methane formed is fed to reaction zone

Process for obtaining benzene, toluene (and naphthalene) from C1-C4-alkanes with co-dosage of hydrogen at a separate location

What is proposed is a process for preparation and distillative workup of diphenylmethane diisocyanate (MDI), proceeding from a benzene-comprising feedstream, in which, in

Process for preparation and preferably distillative workup of diphenylmethane diisocyanate (MDI)

Disclosed is a composition including IL-6, an isoform or a fragment thereof, a compound of the formula C-C-alkyl trimethylammonium halogenide (I), wherein the compound is saturated or unsaturated and/or substituted or unsubstituted, or a salt thereof, wherein the concentration of the compound in the composition is about 0.15 to about 0.4%, and a serum. Also disclosed is a kit including a composition or a lyophilisate and instructions for use. A further embodiment of the present invention is method of stabilizing IL-6, an isoform or a fragment thereof, including the steps of mixing IL-6, an isoform or a fragment thereof, a compound of the formula C-C-alkyl trimethylammonium halogenide (I), wherein the compound is saturated or unsaturated and/or substituted or unsubstituted, or a salt thereof, wherein the concentration of the compound in the composition is about 0.15 to about 0.4%, and a serum.

Stabilization of interleukin 6 in serum based solutions

A process for preparing aromatic amines by catalytic hydrogenation of the corresponding nitro compound in a fluidized-bed reactor, in which a gaseous reaction mixture comprising the nitro compound and hydrogen flows from the bottom upward through a heterogeneous particulate catalyst forming a fluidized bed, wherein the fluidized bed is provided with internals which divide the fluidized bed into a plurality of cells arranged horizontally in the fluidized-bed reactor and a plurality of cells arranged vertically in the fluidized-bed reactor, with the cells having cell walls which are permeable to gas and have openings which ensure an exchange number of the heterogeneous, particulate catalyst in the vertical direction in the range from 1 to 100 liters/hour per liter of reactor volume, is proposed.

Process for preparing aromatic amines in a fluidized-bed reactor

A fluidized-bed reactor for carrying out a gas-phase reaction, in which a gaseous reaction mixture flows from the bottom upward through a heterogeneous particulate catalyst forming a fluidized bed and internals are arranged in the fluidized bed, wherein the internals divide the fluidized bed into a plurality of cells arranged horizontally in the fluidized-bed reactor and a plurality of cells arranged vertically in the fluidized-bed reactor, with the cells having cell walls which are permeable to gas and have openings which ensure an exchange number of the heterogeneous particulate catalyst in the vertical direction in the range from 1 to 100 liters/hour per liter of reactor volume, is proposed.

Fluidized-bed reactor for carrying out a gas-phase reaction

Growing community of inventors

Mannheim, Germany

Christian Schneider