Basf Se Corporation

Vito Nv

Magneto B.v.

Jungheinrich Aktiengesellschaft

Florian Scharf

Christian Walsdorff

Bernard Hendrik Reesink

Carsten Schöttke

Jasper Lefevere

Bart Michielsen

Marco Oskar Kennema

Michael Schönauer

Fred Borninkhof

David Van Asten

Miguel Angel Romero Valle

Juergen Zuehlke

Reiner Giese

Egon Schmidt

Joachim Hege

Steven Alan Jacobs

Christoph Grossmann

Alexey Shilkin

Christian-Andreas Winkler

Markus Schwind

Stefan Haedicke

Juergen Paschold

Lian Zhang

Bernard Reesink

Marko Petteri Kajasvirta

Dirk Hensel

Frank Breithecker

Daniel RÖSCH

A three-dimensional porous catalyst, catalyst carrier or absorbent structure of stacked strands of catalyst, catalyst carrier or absorbent material, composed of layers of spaced-apart parallel strands, wherein parallel strands within a layer are arranged in groups of two or more closely spaced-apart, equidistant strands separated by a small distance, wherein the groups of equidistant strands are separated from adjacent strands or adjacent groups of strands by a larger distance.

Three-dimensional porous catalyst, catalyst carrier or absorbent structure of stacked strands

A three-dimensional porous catalyst, catalyst carrier or absorbent monolith of stacked strands of catalyst, catalyst carrier or absorbent material, composed of alternating layers of linear spaced-apart parallel strands, wherein the strands in alternating layers are oriented at an angle to one another, wherein the distance between inner spaced-apart parallel strands is larger than the distance between outer spaced-apart parallel strands in at least a part of the layers of the monolith.

Catalyst, catalyst carrier or absorbent monolith of stacked strands

A magnetocaloric lattice element formed by fibres of magnetocaloric material, wherein the fibres are arranged in respective parallel lattice planes, each fibre having a respective mass of magnetocaloric material, the fibres of given lattice plane do not contact each other but each fibre of a given lattice plane is attached to at least two fibres in a next neighbouring lattice place, and wherein the magnetocaloric lattice element exhibits exactly one predominant mass-weighted direction of longitudinal fibre extension.

Packed-screen type magnetocaloric element

The present invention concerns a method and a device for feeding at least one chemical substance into a main process stream. The method of the invention comprises the steps of providing a concentrated stream of said chemical substance, mixing said concentrated stream with a diluent stream to provided a diluted stream of said chemical substance, injecting said diluted stream of said chemical substance into said main process stream, wherein said mixing of said concentrated stream with said diluent stream is effected by injecting a jet of either one of said concentrated stream or said diluent stream into the respective other stream. The device of the invention comprises a first pipe segment () having a first inlet () for a first fluid and a first outlet () for a mixed fluid, a second pipe segment () having a second inlet () for a second fluid and a second outlet () connected to and leading into said first pipe segment () between said first inlet () and said first outlet (), and first connection means () for connecting said first outlet () of said first pipe section () to a main pipe () of said main process stream, wherein said second pipe segment () comprises at least one nozzle () for generating a jet () of said second fluid arranged upstream of said second outlet ().

Method and device for feeding at least one chemical substance into a main process stream

A magnetocaloric cascade contains a sequence of magnetocaloric material layers having different Curie temperatures T, wherein the magnetocaloric material layers include a cold-side outer layer, a hot-side outer layer and at least three inner layers between the cold-side outer layer and the hot-side outer layer, and each pair of next neighboring magnetocaloric layers of the magnetocaloric cascade has a respective Curie-temperature difference amount &#x394;Tbetween their respective Curie temperatures, wherein the hot-side outer layer or the cold-side outer layer or both the hot-side and cold-side outer layer exhibits a larger ratio m&#x394;S/&#x394;Tin comparison with any of the inner layers, m denoting the mass of the respective magnetocaloric material layer and &#x394;Sdenoting a maximum amount of isothermal magnetic entropy change achievable in a magnetic phase transition of the respective magnetocaloric material layer.

Magnetocaloric cascade and method for fabricating a magnetocaloric cascade

A valve for carrying out a mass-transfer process, in which a gas flows through liquid standing on a separating tray, when the gas supply is interrupted the liquid flows into a lock and, when the gas supply is restarted, the liquid flows out of the lock, wherein the valve contains a closing element which is designed in such a manner that, with the closing element in a first valve position, a first opening in a lower tray of the lock is closable, and the closing element is conducted in a first sleeve which is positioned between the upper tray bordering the lock and the lower tray in which sleeve, in the region of the lock, second openings are formed, and which projects over the upper tray and has a lift limiter for the closing element.

Method for carrying out a mass-transfer process in a column

Growing community of inventors

Frankfurt-am-Main, Germany

Florian Scharf