Basf Aktiengesellschaft

Basf Se Corporation

Other

Basfaktiengesellschaft

Veba Oel Ag

Basf Aktiengesellschaft Ludwigshafen

Alwin Rehfinger

Peter Bassler

Rolf Hartmuth Fischer

Hermann Luyken

Guido Voit

Joaquim Henrique Teles

Johann-Peter Melder

Norbert Rieber

Martin Merger

Wolfgang Harder

Andreas Ansmann

Frank Ohlbach

Peter Rudolf

Anne Wenzel

Klaus Ebel

Tom Witzel

Werner Schnurr

Klemens Flick

Harald Rust

Ulrich M&uuml;ller

Ralf Boehling

Andreas Walch

G&uuml;nther Achhammer

Anne Berg

Ulrich Müller

Klaus Ditrich

Martin Ernst

Alois Kindler

Kai-Uwe Baldenius

Werner Hefner

Klaus Gottlieb

Ralf Böhling

Michael Schelper

Wilfried Sager

Ulrich Hoffmann

Marta Zajaczkowski-Fischer

Frank Mrzena

Wilfried Graf

Andrea Piatesi

Kuno Schadlich

Peter Ba&bgr;ler

Michael Hayer

Ralf Bohling

Martin Gann

Rudiger Schmitt

Robert Markl

Jorg Flato

Axel Schimpf

Kuno Schaedlich

Joerg Flato

Ralf BÖHLING

Rolf Fischer

A process for preparing sebacic acid by reacting in a first step (i) linoleic acid with water catalyzed by an oleate hydratase to form 10-hydroxy-12-octadecenoic acid, in a second step (ii) pyrolysing the 10-hydroxy-12-octadecenoic acid to 1-octene and 10-oxo-decanoic acid and in a third step (iii) oxidizing the 10-oxo-decanoic acid to sebacic acid.

Process for preparing sebacic acid

The invention relates to a process for preparing nitroalkanes by reaction of at least one alkane with at least one nitrating agent in the gas phase, wherein the nitration is carried out in a microstructured reaction zone having parallel channels having hydraulic diameters of less than 2.5 mm and a total specific internal surface area of more than 1600 m/mand the alkane and the nitrating agent are conveyed under a pressure of from 1 bar to 20 bar through the reaction zone and reacted at a temperature of from 150&#xb0; C. to 650&#xb0; C. and the reaction products are cooled downstream of the reaction zone and discharged and the at least one nitrating agent is introduced over from two to ten introduction points along the reaction zone.

Method for producing nitroalkanes in a microstructured reactor

A material useful as catalyst for the hydrogenation of alpha, omega-dinitriles comprises

Hydrogenation catalyst

An organic compound having at least one C&#x2014;C double bond is epoxidized by means of hydrogen peroxide in the presence of at least one catalytically active compound and at least one solvent, wherein a product mixture comprising &#x3b1;-hydroperoxyalcohols is reduced using at least one reducing agent. The process advantageously comprises at least the following steps:

Method for producing an epoxide

A process for the regeneration of a zeolite catalyst which comprises treating the catalyst thermally in the presence of a gas stream at temperatures above 120&#xb0; C., the weight-based residence time of the gas stream over the catalyst during the thermal treatment being greater than 2 hours.

Method for regenerating a zeolite catalyst

A process for preparing propylene oxide comprises at least the following steps:

Method for producing propylene oxide

A material useful as catalyst for the hydrogenation of alpha, omega-dinitriles comprises (a) iron or a compound based on iron or mixtures thereof, (b) from 0.001 to 0.3% by weight based on (a) of a promoter based on 2, 3, 4 or 5 elements selected from the group consisting of aluminum, silicon, zirconium, titanium and vanadium, (c) from 0 to 0.3% by weight based on (a) of a compound based on an alkali and/or alkaline earth metal, and also (d) from 0.001 to 1% by weight based on (a) of manganese.

A process for the preparation of propylene oxide in the presence of methanol, in which propylene oxide is separated from a mixture propylene oxide and methanol, and the resultant methanol containing mixture is worked up, including seperating methanol from a mixture comprising methanol and methyl formate during the work-up.

Method for the production of propylene oxide

A process for regenerating a zeolite catalyst comprises thermal treatment of the catalyst at above 120&deg; C. in the presence of a gas stream comprising hydrogen.

In a continuous process for reacting an organic compound with hydroperoxide in the presence of a catalyst, the reaction is carried out in a reactor assembly comprising at least two reactors connected in parallel.

Method for converting an organic compound with a hydroperoxide

A mixture (M1) comprising an alkene and oxygen is worked up by a process in which (i) oxygen is removed from the mixture (M1) by a nondistillative method to give a mixture (M2) and (ii) the alkene is separated off from the mixture (M2) by distillation.

Working up a mixture comprising alkene and oxygen

In a process for reacting an organic compound with a hydroperoxide using at least one heterogeneous catalyst, both the pH and the temperate of the reaction medium are changed during the reaction

Method for reacting an organic compound with a hydroperoxide

Method for simultaneous preparation of 6-aminocapronitrile and hexamethylene diamine

Method for producing hexamethylene diamine

Growing community of inventors

Mutterstadt, Germany

Alwin Rehfinger