Basf Aktiengesellschaft

Basf Se Corporation

Uwe Diehlmann

Ulrich Mueller

Michael Hesse

Markus Schubert

Jochem Henkelmann

Ulrich Müller

Boris Breitscheidel

Alois Kindler

Gerhard Cox

Thomas Ruhl

Andreas Brodhagen

Arnd B&ouml;ttcher

Sabine Weiguny

Stefan Marx

Frank Poplow

Lena Arnold

Juergen Stephan

Jürgen Stephan

Stefanie Clade

Volker Boehm

Martina Sinner-Lang

Jochen Pfeifer

Volker Böhm

A continuous process for preparing a zeolitic material comprising (i) preparing a mixture comprising a source of YO, optionally a source of XO, and a liquid solvent system; (ii) continuously feeding the mixture prepared in (i) into a continuous flow reactor at a liquid hourly space velocity in the range of from 0.3 to 20 h1 for a duration of at least 1 h; and (iii) crystallizing the zeolitic material from the mixture in the continuous flow reactor, wherein the mixture is heated to a temperature in the range of from 100 to 300&#xb0; C.; wherein the volume of the continuous flow reactor is in the range of from 150 cmto 75 m, as well as to zeolitic materials which may be obtained according to the inventive process and to their use.

Process for a continuous synthesis of zeolitic materials

The present invention relates to a method for producing a porous metal-organic framework material comprising the step reacting a reaction mixture in the liquid phase of at least one copper compound having at least one at least bidentate, organic compound which can bind by coordination to the copper in the presence of a nonaqueous solvent, the at least one at least bidentate, organic compound being derived from a polycarboxylic acid having at least three carboxyl groups, and the reaction proceeding at atmospheric pressure above 80&#xb0; C.

Process for preparing porous metal-organic framework materials

The present invention relates to a method for producing a porous metal-organic framework material comprising the step

The present invention provides a process for preparing a supported catalyst (catalyst C) having a support (support S) selected from among oxides, phosphates, silicates, carbides, borides and nitrides of main group elements and elements of transition groups VI and II and mixtures of the abovementioned compounds and an active component (activator A) comprising one or more compounds containing one or more elements of transition groups V, VI and VII customary for the catalysis of metathesis reactions.

Activated metathesis catalysts

In a process for reacting an organic compound in the presence of a catalyst comprising, as active metal, at least one metal of transition group VIII of the Periodic Table, either alone or together with at least one metal of transition group I or VII of the Periodic Table, in an amount of from 0.01 to 30% by weight, based on the total weight of the catalyst, applied to a support containing macropores, the support comprises, as a support component, boron(III) oxide in an amount of from 10 to 100% by weight, based on the total weight of the support.

Reaction of organic compounds over macroporous supported catalysts comprising boron oxide

An activated fixed-bed Raney metal catalyst which is free of metal powder, has macropores and is based on an alloy of aluminum and at least one metal of subgroup VIII of the Periodic Table, contains more than 80% by volume, based on the total pores, of macropores and is used for the hydrogenation of low molecular weight and polymeric organic compounds.

Fixed-bed Raney metal catalyst, its preparation and the hydrogenation of

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Hassloch, Germany

Uwe Diehlmann