Evonik Rohm Gmbh

Evonik Operations Gmbh

Evonik Roehm Gmbh

Roehm Gmbh

Rohm Gmbh

Boehringer Ingelheim Pharma Gmbh & Co Kg

Andreas Weber

Johannes Vorholz

Marcus Denger

Norbert Hoffmann

Steffen Krill

Christian Meier

Alpertunga Kueksal

Klaus Albrecht

Marcel Treskow

Andreas Klosendorf

Pamela Boehmann

Nikolaos Papadopoulos

Reiner Mueller

Marita Kaufmann

Mona Rueppel

Andrea Wittkowski

Kathrin Salwiczek

Ralf Richter

Alexander Richter

Dominic Stoerkle

Michael Schnabel

Wolfgang Luley

Matthias Schellhorn

Maren Kuhn

David Bailey

Lukas Friedrich Dössel

Berthold Buchholz

Melanie Jungkamp

Christine Weiß

Alpertunga Küksal

Pamela Böhmann

Reiner MÜLLER

Dominic STÖRKLE

Mona RÜPPEL

Isabelle Klein

Christine Weiss

Reiner Muller

Mona Ruppel

Dominic Storkle

Alpertunga Kuksal

Pamela Bohmann

A mixture contains at least one polyether block amide (PEBA) and at least one poly(meth)acrylate, selected from poly(meth)acrylimides, poly-alkyl(meth)acrylates, and mixtures thereof. The mass ratio of PEBA to poly(meth)acrylate is 95:5 to 60:40. The polyalkyl(meth)acrylate contains 80% by weight to 99% by weight of methyl methacrylate (MMA) units and 1% by weight to 20% by weight of C1-C10-alkyl acrylate units, based on the total weight of polyalkyl(meth)acrylate. The mixture can be processed to give foamed mouldings. The mouldings can be used in footwear soles, stud material, insulation or insulating material, damping components, lightweight components, or in a sandwich structure.

Polyether block amide-poly(meth)acrylate foams

The present invention relates to a process for preparing a poly(meth)acrylic acid, characterized in that a (meth)acrylic acid-containing process stream from (meth)acrolein synthesis is subjected to free-radical polymerization. The invention also relates to the esterification of the polymer obtained to give a homopolymer or copolymer ester, and to the use thereof as additive, flow improver and water reducer.

Concrete flow improvers and water reducers

The present invention relates to a continuous or semi-continuous freeze coagulation process for aqueous polymer dispersions, wherein said process comprises a freezing step and a solid-liquid separation step and is further characterized in that it comprises the further step of admixing water and/or water vapor between the freezing step and the solid-liquid separation step.

Continuous or semi-continuous freezing coagulation method for aqueous polymer dispersions

The invention relates to a process for preparing a (meth)acrylate copolymer containing tertiary amino groups by free-radical polymerization in solution from a monomer mixture selected from a) 30 to 70% by weight of a C-C-alkyl ester of acrylic acid or methacrylic acid and b) 70 to 30% by weight of an alkyl ester of acrylic acid or methacrylic acid with a tertiary amino group in the alkyl radical and c) 0 to 10% of further copolymerizable vinyl monomers, whereby one or more polymerization initiators, optionally one or more molecular weight regulators and one or more solvents or of a solvent mixture are added to the monomer mixture to give a polymerization mixture, which is polymerized at temperatures from 30 to 120&#xb0; C. over a period of 2 to 24 hours, where the polymerization mixture is finally polymerized to give a polymerization syrup with a conversion of the monomers to the copolymer of at least 99% by weight, where the polymerization syrup is subsequently degassed by distillation or by extrusion and the degassed polymerization syrup is further comminuted to a copolymer preparation in the form of a granulate or powder, where the copolymer preparation is characterized by a molecular weight (M) of 25.000 to 75.000 g/mol a polydispersity index of 2.1 to 2.9 and a residual solvent concentration of less than 1.000 ppm by weight.

Process for preparing a (meth)acrylate copolymer containing tertiary amino groups by free-radical polymerization in solution

The invention relates to a process for preparing a (meth)acrylate copolymer containing quaternary ammonium groups from a monomer mixture selected from: (a) 80 to 99% by weight of a C1-C4-alkyl ester of acrylic acid or methacrylic acid; and (b) 20 to 1% by weight of an alkyl ester of acrylic acid or methacrylic acid with a quaternary ammonium group in the alkyl radical; and (c) 0 to 10% of further copolymerizable vinyl monomers whereby one or more polymerization initiators, optionally one or more molecular weight regulators and one or more solvents or of a solvent mixture are added to the monomer mixture to give a polymerization mixture, which is polymerized at temperatures from 30 to 120 C over a period of 2 to 24 hours, where the polymerization mixture is polymerized to a polymerization syrup with a conversion of the monomers to the copolymer of at least 99% by weight, where the polymerization syrup is subsequently degassed by distillation or by extrusion and the degassed polymerization syrup is further comminuted to a copolymer preparation in the form of a granulate or powder and where the copolymer preparation is characterized by a molecular weight (Mw) of 25.000 to 50.000, a polydispersity index of 2.0 to 3.0 and a residual solvent concentration of less than 10.000 ppm by weight.

Process for preparing a (meth)acrylate copolymer containing quaternary ammonium groups by free-radical polymerization in solution

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Frankfurt-am-Main, Germany

Andreas Weber