Henkel Kommanditgesellschaft Auf Aktien

Gerd Gobel

Franz-Josef Carduck

Norbert Behr

Othmar Von Ettingshausen

Henk Van Der Mei

For continuous heterogeneous hydrogenation, fats, fatty acids and/or fatty acid derivatives are brought into contact with hydrogen in the presence of a heterogeneous catalyst dispersed in a liquid phase in a tubular packed reactor, of which the length-to-diameter ratio is .gtoreq.10:1, under pressure of from 0.5 to 300 bar and at temperatures of from 60.degree. to 260.degree. C. The reactor is packed with a geometrically regularly arranged elements of a material inert to the components under the reaction conditions, and the hydrogen is passed through the reactor in parallel current or countercurrent to the fatty acid substrate under a gas velocity of from 0.5 to 30 cm/sec., based on the overall cross-section of the reactor. Preferably the catalyst is fixed on an insoluble support and suspended in small quantities of the particular reaction product before being added to the substrate and entering the reactor.

Process for the continuous hydrogenation of fats, fatty acids and fatty

This invention relates to a process for concentrating aqueous solutions having temperature-sensitive components. More particularly, this invention relates to an improved process for concentrating aqueous solutions having temperature-sensitive components which comprises the steps of:

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Erkrath, Germany

Gerd Gobel