Hte Gmbh the High Throughput Experimentation Company

Hte Aktiengesellschaft

Basf Se Corporation

Hte Aktiengesellschaf the High Throughput Experimentation Company

Hte Aktiengesellschaft the High Throughtput Experimentation Company

Markus Friess

Oliver Koechel

Alfred Haas

Kurt-Erich Finger

Wolfgang Strehlau

Armin Brenner

Torsten Zech

Michael Dejmek

Josef Find

Marius Kirchmann

Christoph Hauber

Luca Mazzoncini

Georg Vassiliadis

Edgar Jordan

Andreas Haas

The invention relates to an apparatus for analyzing heterogeneously catalyzed reactions comprising at least one reactor () through which a particulate catalyst flows and at least one reactant feed, wherein arranged downstream of each reactor () is a separation apparatus () for separating the particulate catalyst from a reaction product comprising condensable gases and arranged downstream of the separation apparatus () is a liquid separator () for separating liquid constituents from the reaction product, wherein the liquid separator () comprises a metallic tube () and a deflection body (), wherein the metallic tube () is closed at its ends and the deflection body () is accommodated in the metallic tube () and the metallic tube () comprises a side feed () at a first end () and a gas outlet () at a second end () and the gas outlet () is connected to at least one sample vessel (). The invention further relates to a process for analyzing heterogeneously catalyzed reactions in the apparatus.

Apparatus and method for examining heterogeneously catalyzed reactions

The invention relates to an apparatus for analyzing reactions, comprising at least one reactor () and at least two sample vessels (), wherein, in the case of an apparatus having one reactor (), the reactor () is connected to at least two sample vessels (), and, in the case of an apparatus having more than one reactor (), each reactor () is connected to at least one sample vessel (). The invention further relates to a method of analyzing reactions in such an apparatus.

Device and method for examining reactions

Disclosed herein is an apparatus and a method for catalytic conversion of chemical substances in the presence of pulverulent catalysts in a trickle bed reactor with residence times in the range of 0.1-10 seconds, wherein the apparatus includes a trickle bed reactor (), the inlet side of which is functionally connected to a catalyst reservoir vessel () and a reactant feed, and the outlet side of which is functionally connected to a separator (). The separator () has an exit conduit for leading off product stream, wherein the apparatus has the characteristic feature that the exit conduit disposed on the separator () for leading off product stream has a continuously acting valve connected via a controller to a pressure measurement sensor, wherein the continuously acting valve and the pressure measurement sensor form a pressure control circuit with a controller.

Device and method for catalytically converting chemical substances at dwell times in the range of 0.1-10 seconds

An apparatus and process for spraying liquids and producing very fine mist with the apparatus, the apparatus including: a needle injector that includes a capillary line () and an outer tube (); a liquid supply (); and a gas supply (), where: the capillary line () is arranged in the interior space of the outer tube (); the internal diameter of the capillary line in the needle injector is in the range of 2-1000 &#x3bc;m; the capillary line is in active communication with a gas supply (); and the outer tube () is in active communication with a liquid supply ().

Apparatus and process for spraying liquids and producing very fine mist

The present invention relates to a multi-zone furnace for heating and tempering reactors and pipes in devices. The multi-zone furnace according to the invention is modularly constructed, wherein it is e.g. possible to efficiently heat or cool the furnace or also individual zones of the furnace. Furthermore, exchangeable cassettes provide the advantage that the reactors and the components, which are connected to the reactors, are particularly well accessible, wherein reconverting work is facilitated.

Multi-zone furnace

A method and a device for the parallel study of chemical reactions in at least two spatially separated reaction spaces is provided. A device for the parallel study of chemical reactions includes at least the following components: (a) at least two spatially separated reaction spaces; (b) on the reaction space input side, at least one common educt feed for the reaction spaces according to (a); (d) on the reaction space output side, at least one connection per reaction space to at least one holding gas feed common to all the reaction spaces, or subsets of them; (e) on the reaction space output side, and downstream of the connection to the holding gas feed according to (d) in the product flow direction, at least one restrictor per reaction space.

Device and method for pressure and flow control in parallel reactors

The present invention relates to a method and a device for the parallel study of chemical reactions in at least two spatially separated reaction spaces. In particular, the invention is suitable for reactions which are not constant volume reactions and/or for reactions in which fluid flows through at least two spatially separated reaction spaces are intended to be controlled together for all the reaction spaces, or for related subsets of them, in the most straightforward way possible. According to one embodiment, the device according to the invention for the parallel study of chemical reactions comprises at least the following components: (a) at least two spatially separated reaction spaces; (b) on the reaction space input side, at least one common educt feed for the reaction spaces according to (a); (d) on the reaction space output side, at least one connection per reaction space to at least one holding gas feed common to all the reaction spaces, or subsets of them; (e) on the reaction space output side, and downstream of the connection to the holding gas feed according to (d) in the product flow direction, at least one restrictor per reaction space.

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Lindenberg, Germany

Markus Friess