Basf Se Corporation

Dow Global Technolgoies LLC

Basf Corporation

Basf Interservicios S.a. De C.v.

Basf Espanola S.l.

Basf Espagnola S.l.

Bianca Seelig

Andrei-Nicolae Parvulescu

Joaquim Henrique Teles

Ulrich Mueller

Markus Weber

Philip Kampe

Dominic Riedel

Daniel Urbanczyk

Meinolf Weidenbach

Werner J Witzl

Alexander Schroeder

Peter Resch

Ulrike Wegerle

Robert Bayer

Sebastian Ahrens

Gabriele Iffland

Mathias Feyen

Christian Bartosch

Bernd Bastian Schaack

Sunghee Son

Dirk Gerhard

Karsten Seidel

Holger Baer

Michael Hesse

Ulrich Müller

Peter Bassler

Christian Schade

Volker Wendel

Rainer Klopsch

Kai Gumlich

Veit Stegmann

Hans-Juergen Luetzel

Andreas Walch

Richard Jacubinas

Boris Gaspar

Hans-Martin Haake

Sandra Mack

Rolf Werner

Henning Althöfer

Henning Althoefer

Christoph Tonhauser

Andrea Tomlinson

Luis Angel Ibarra

Volker Bendig

Cristina Amela

Frank Stallmach

Peter Hoessel

Anne Kristin Pusch

Patricia Grund

Martin Hauke

Sylvia Jeck

David Graham

Jeremie Miller

Hans-Jürgen Lützel

Alexander SCHRÖDER

Björn SCHRÖDER

Holger BÄR

A polymer having the following monomers in polymerized form (in weight %): A) 49-60% of a first monomer which is selected from the group consisting of methyl acrylate, methyl methacrylate, ethyl acrylate, ethyl methacrylate, C3-alkyl acrylate, C3-alkyl methacrylate, C4-alkyl acrylate, C4-alkyl methacrylate and mixtures thereof, B) 30-40% methacrylic acid, C) 4-15% acrylic acid, and D) 0.02-0.30% of a crosslinking agent having at least two allyl moieties, wherein the sum of the amounts of monomers A to D is 100%. A hair styling composition containing the polymer and use of the polymer or of the hair styling composition for styling hair also are disclosed.

Polymer

The present invention relates to A process for the production of a molding, comprising (I) providing a zeolitic material; (II) mixing the zeolitic material provided in step (I) with one or more binders; (III) kneading of the mixture obtained in step (II); (IV) molding of the kneaded mixture obtained in step (III) to obtain one or more moldings; (V) drying of the one or more moldings obtained in step (IV); and (VI) calcining of the dried molding obtained in step (V); wherein the zeolitic material provided in step (I) displays a water adsorption ranging from 1 to 15 wt.-% when exposed to a relative humidity of 85%, as well as to a molding obtainable or obtained according to the inventive process in addition to a molding per se and to their respective use.

Molding for a hydrophobic zeolitic material and process for its production

A continuous process for preparing propylene oxide proceeds by (a) reacting propene with hydrogen peroxide in a reaction apparatus in the presence acetonitrile as solvent, obtaining a stream S0 containing propylene oxide, acetonitrile, water, at least one further component B; (b) separating propylene oxide from S0, obtaining stream S1 containing acetonitrile, water and B; (c) dividing S1 into streams S2 and S3; (d) subjects S3 to vapor-liquid fractionation in a first fractionation unit, obtaining vapor fraction stream S4a being depleted, relative to S3, of at least one of B and obtaining liquid bottoms stream S4b, and subjecting at least part of vapor fraction stream S4a to vapor-liquid fractionation in a second fractionation unit, obtaining vapor fraction stream S4c and liquid bottoms stream S4 being depleted, relative to S4a, of at least one of B; (e) recycling at least a portion of S4 to (a).

Part-stream distillation

The present invention relates to a process for the preparation of a zeolitic material comprising the steps of:

Zeolitic materials and methods for their preparation using alkenyltrialkylammonium compounds

The present invention relates to a process for the regeneration of a catalyst comprising a titanium-containing zeolite, said catalyst having been used in a process for the preparation of an olefin oxide and having phosphate deposited thereon, said process for the regeneration comprising the steps: (a) separating the reaction mixture from the catalyst, (b) washing the catalyst obtained from (a) with liquid aqueous system; (c) optionally drying the catalyst obtained from (b) in a gas stream comprising an inert gas at a temperature of less than 300&#xb0; C.; (d) calcining the catalyst obtained from (c) in a gas stream comprising oxygen at a temperature of at least 300&#xb0; C.

Regeneration of a titanium containing zeolite

A continuous process for the preparation of propylene oxide, comprising (a) reacting propene, optionally admixed with propane, with hydrogen peroxide in a reaction apparatus in the presence of acetonitrile as solvent, obtaining a stream Scontaining propylene oxide, acetonitrile, water, at least one further component B, optionally propene and optionally propane, wherein the normal boiling point of the at least one component B is higher than the normal boiling point of acetonitrile and wherein the decadic logarithm of the octanol-water partition coefficient (log K) of the at least one component B is greater than zero; (b) separating propylene oxide from S, obtaining a stream Scontaining acetonitrile, water and the at least one further component B; (c) dividing Sinto two streams Sand S; (d) subjecting Sto a vapor-liquid fractionation in a fractionation unit, obtaining a vapor fraction stream Sbeing depleted of the at least one component B; (e) recycling at least a portion of S, optionally after work-up, to (a).

A continuous process for the preparation of propylene oxide, comprising (i) providing a liquid feed stream comprising propene, hydrogen peroxide, acetonitrile, water, optionally propane, and at least one dissolved potassium salt of a phosphorus oxyacid wherein the molar ratio of potassium relative to phosphorus in the at least one potassium salt of a phosphorus oxyacid is in the range of from 0.6 to 1.4; (ii) passing the liquid feed stream provided in (i) into an epoxidation reactor comprising a catalyst comprising a titanium zeolite of structure type MWW comprising zinc, and subjecting the liquid feed stream to epoxidation reaction conditions in the epoxidation reactor, obtaining a reaction mixture comprising propylene oxide, acetonitrile, water, the at least one dissolved potassium salt of a phosphorus oxyacid, optionally propene, and optionally propane; (iii) removing an effluent stream from the epoxidation reactor, the effluent stream comprising propylene oxide, acetonitrile, water, at least a portion of the at least one dissolved potassium salt of a phosphorus oxyacid, optionally propene, and optionally propane.

Process for preparing propylene oxide

A continuous process for the preparation of propylene oxide, comprising (i) providing a liquid feed stream comprising propene, hydrogen peroxide, acetonitrile, water, dissolved potassium dihydrogen phosphate, and optionally propane; (ii) passing the liquid feed stream provided in (i) into an epoxidation reactor comprising a catalyst comprising a titanium zeolite of structure type MWW, and subjecting the liquid feed stream to epoxidation reaction conditions; (iii) removing an effluent stream from the epoxidation reactor; wherein the concentration of the dissolved potassium dihydrogen phosphate in the liquid feed stream is at least 10% of the solubility limit of the potassium dihydrogen phosphate in the liquid feed stream.

Process for the preparation of propylene oxide

The present invention relates to a micropowder, wherein the particles of the micropowder have a Dv10 value of at least 2 micrometer and the micropowder comprises mesopores which have an average pore diameter in the range of from 2 to 50 nm and comprise, based on the weight of the micropowder, at least 95 weight-% of a microporous aluminum-free zeolitic material of structure type MWW containing titanium and zinc.

Micropowder and molding containing a zeolitic material containing Ti and Zn

Process for preparing epoxides of the formula I  

Process for preparing epoxycarboxylic esters

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Cologne, Germany

Bianca Seelig