Deutsche Solvay-werke Gmbh

Solvay Fluor Und Derivate Gmbh

Beiersdorf Ag

Werner Siemanowski

Gerald Jakobson

Karl-Heinz Uhlig

Florian Wolf

Helmut Dillenburg

Karlheinz Uhlig

Gunther Schneider

Bernd Traupe

Manfred Klier

Manfred Rockl

Winfried Klein

Ilona Voss

Deodorant active-substance combinations made from wool-grease acids and

Cosmetic deodorant preparation containing di- or triglycerin esters

A process for producing diglycerin having a low content of cyclic components by reacting glycerin with epichlorohydrin by a continuous process in which the epichlorohydrin required for the reaction is introduced into at least one flow reactor at several separate spots or reaction zones mutually separated in space in the direction of flow; the reacted reaction mixture is substantially freed of excess glycerin in at least one evaporator; the remaining chlorohydrin/ether mixture is hydrolyzed in at least one first step with a 5 to 40 mole % excess alkali carbonate solution, calculated with respect to organically bound chlorine in the chlorohydrin ether, at a pH of 6.5 to 9.5, and hydrolysis is at least substantially completed in a second step with an alkali hydroxide at a pH above 10; the resulting hydrolyzed crude product solution is adjusted to a pH of 5.5 to 8 with a mineral acid, preferably hydrochloric acid; and the resulting solution is condensed, precipitating salts are removed, and the diglycerin solution containing less than 8% by weight residual inorganic salts is freed of cyclic diglycerin and residual glycerin in a flash evaporator. Apparatus for carrying out the foregoing method is also disclosed.

Process and apparatus for producing diglycerin

Polyglycerol fatty acid ester mixtures of mono- di- and polyesters of polyglycerols having a degree of polymerization of 2 to 8 and at least one saturated and/or unsaturated fatty acid, the mixtures having an HLB of greater than 8 and containing 0 to less than 5 wt-% diglycerol fatty acid esters, 20 to 65 wt-% triglycerol fatty acid esters, 20 to 50 wt-% tetraglycerol fatty acid esters and 5 to 40 wt-% higher polyglycerol fatty acid esters, in which the fatty acid component consists of one or more fatty acids selected from the saturated and/or unsaturated, branched and/or unbranched C.sub.6 - to C.sub.14 -fatty acids containing less than 10 wt-% fatty acids having more than 14 carbon atoms; bath additive preparations containing such polyglycerol fatty acid ester mixtures; methods of using such polyglycerol fatty acid ester mixtures, and a process for preparing such mixtures.

Polyglycerol fatty acid ester mixture

A process for preparing polyglycerol fatty acid ester mixtures in which a polyglycerol mixture of 0.1 to 20 wt % monoglycerol, 20 to 35 wt % diglycerol, 30 to 40 wt % triglycerol and 49.9 to 5 wt % tetra- and higher polyglycerols is reacted with one or more fatty acids, selected from the saturated C.sub.8 - to C.sub.18 -fatty acids (containing 0 to 15 wt % unsaturated fatty acids), in a molar ratio of the polyglycerol to the fatty acid component of 0.3:1.5 to 1.5:0.5 in the presence of at least one catalyst and at reduced pressure, by initially heating the reaction mixture to at least 140.degree. C. and reducing the pressure to at least 600 mbar and then heating the reaction mixture at a temperature from 140.degree. to 220.degree. C. and reducing the pressure from 600 to 10 mbar. After completion of the reaction, the resulting polyglycerol fatty acid ester mixture is cooled and optionally worked up and/or purified. Also disclosed are polyglycerol fatty acid ester mixtures prepared by the process, a liquid thickening agent, an oil/water emulsifier, and the use of the polyglycerol fatty acid ester mixture in pharmaceutical, cosmetic and other chemical preparations.

Process for preparing polyglycerol fatty acid ester mixtures and use in

A process for the preparation of mono-fatty acid or hydroxymono-fatty acid esters of isopropylidene derivatives of a polyglycerol is disclosed. A C6-C22 fatty acid or -hydroxy fatty acid is reacted with isopropylideneglycerol glycidyl ether or diisopropylidenetriglycerol glycidyl ether in a molar ratio of 0.5:1 to 1:0.5 at temperatures of 373473 K. in the presence of a catalyst. The monoisopropylidenediglycerol mono-fatty acid ester or monoisopropylidenediglycerol hydroxy mono-fatty acid ester or diisopropylidenetetraglycerol mono-fatty acid ester or diisopropylidenetetraglycerol hydroxy mono-fatty acid ester obtained is optionally purified by distillation, fractional distillation and/or ion exchange.

Preparation of fatty acid esters of isopropylidene derivatives of

A bath additive composition, in particular an oil bath preparation, containing at least one surface-active component, preferably a water-soluble emulsifier, at least one oily or oil-containing component selected from the natural and synthetic, mineral, ethereal and fatty animal and vegetable oils, optionally a solvent or solvent mixture and also further auxiliaries and additives, the bath additive preparation containing 10 to 60 wt-% of a polyglycerol fatty acid ester mixture as the water-soluble emulsifier and/or solubilizer, 10 to 60 wt-% of an oil, oil mixture and/or oil component having cosmetic and/or therapeutic activity and 0 to 70 wt-% of water, the polyglycerol fatty acid ester mixture containing 0 to 5 parts by weight diglycerol fatty acid esters, 20 to 65 parts by weight triglycerol fatty acid esters, 20 to 50 parts by weight tetraglycerol fatty acid esters, and 5 to 40 parts by weight higher polyglycerol fatty acid esters, for a total of 100 parts by weight, and the fatty acid component consisting of one or more fatty acids selected from the saturated and/or unsaturated, branched and/or unbranched C.sub.6 - to C.sub.14 - fatty acids containing less than 10 wt-% fatty acids having more than 14 carbon atoms.

Bath additive composition containing polyglycerol fatty acid ester

A process for preparing a nonionic surfactant includes the steps of: cleaving at least one of the isopropylidene groups of an isopropylidene polyglycerol C.sub.6 -C.sub.22 -fatty acid or mono- or polyhydroxy fatty acid ester, by hydrolysis or ketal exchange, in the presence of acid, at a temperature in the range of about 20.degree. C. to about 100.degree. C., and at atmospheric, reduced or superatmospheric pressure, thereby regenerating hydroxyl groups on the polyglycerol; and recovering the resultant polyol ester nonionic surfactant. Such polyol ester surfactants are useful as emulsifiers, especially for preparing skin care or cosmetic formulations and paints and wood-preservation agents.

Process for preparing nonionic surfactants

The present invention relates to a fatty acid polyglycerol ester mixture containing a C.sub.8 to C.sub.24 fatty acid ester component comprising (A) about 20 to 80% by weight of fatty acid monoester of a polyglycerol containing more than about 40% of C.sub.10 and/or C.sub.8 in the ester component of the polyglycerol; (B) about 80 to 20% by weight of fatty acid diester of polyglycerol; and (C) about 15 to 0% by weight of tri- and higher esters of the polyglycerol containing than about 40% of C.sub.10 and/or C.sub.8 in the ester component of the polyglycerol; and further wherein the resultinq fatty aoid polyglycerol ester mixture comprises (A) about 20 to 45% by weight of fatty acid diglycerol ester; (B) about 30 to 45% by weight of fatty acid triglycerol ester; and (C) about 50 to 10% by weight of fatty acid tetra-and higher polyglycerol esters. A thickened composition, skincare composition and a cleansing agent containing the fatty acid polyglycerol ester mixture as a component thereof and a process for the preparation of the fatty acid polyglycerol ester mixture are disclosed.

Polyglycerine and capric acid ester mixture

A process for the preparation of a composition containing diglycerol, in which process at least a stoichiometric amount of isopropylideneglycerol is reacted with .alpha.-monochlorohydrin in the presence of at least one alkaline compound at sufficient temperatures to yield an intermediate product composition containing monoisopropylidenediglycerol and a salt. Most of the salt and water formed is removed from the intermediate product composition, and any unreacted isopropylideneglycerol is removed by distillation. The remaining intermediate product composition containing monoisopropylidenediglycerol is subsequently reacted with water in the presence of at least one acidic catalyst at sufficient temperatures to yield a product composition containing diglycerol and acetone and substantially no cyclic glycerols.

Process for the preparation of diglycerol and/or polyglycerol

The present invention relates to a process for preparing ultrapure epichlorohydrin from epichlorohydrin containing technical impurities, by fractional distillation under particular conditions, preferably with continuous operation, that yield a product of very high purity and very low content of halogenated hydrocarbons. Epoxy resins made with such ultrapure epichlorohydrin are especially well suited for use in fabricating electrical components and microchips.

Process for preparing high purity epichlorohydrin

The present invention relates to a washing agent, cleansing agent and/or toiletry containing at least one ionic and/or amphoteric surfactant and at least one C.sub.8 to C.sub.18 fatty acid monoester of diglycerol and/or C.sub.8 to C.sub.18 fatty acid diester of tetraglycerol as a constituent of the mixture, 2 to 30% by weight, perferably 10 to 20% by weight, of at least one fatty acid monoester of diglycerol and/or fatty acid diester of tetraglycerol, relative to the total surfactant content (100% by weight), being present in the surfactant mixture. The agent is employed together with certain compositions, in particular with a solvent, additives and the like. The invention also relates to the preparation of the washing agent, cleansing agent and/or toiletry and to its use as a shower preparation, bubble bath preparation, liquid hand cleanser or hair shampoo.

Cleaning agent and process for its preparation

A method of making 2,2-dimethyl-4-(2',3'-epoxy)propoxymethyl-1,3-dioxolane is disclosed, wherein isopropylidene glycerol and epichlorohydrin are reacted in a molar ratio of 0.7:1.0 to 1.0:0.7, respectively, in the presence of at least one Lewis acid or at least one strong inorganic acid at temperatures 283.degree. K. to 373.degree. K., and the initially formed isopropylidene glycerol chlorohydrin ether is reacted with a strongly alkaline base in a molar ratio of chlorohydrin ether to the alkaline base of 1.0:1.0 to 1.0:1.1, respectively, to givbe the 2,2-dimethyl-4-(2',3'-epoxy)propoxymethyl-1,3-dioxolane. This compound is suitable for use as an intermediate for the production of nonionic and/or ionic surfactants, as a reactive diluent and as an auxiliary solvent and auxiliary stabilizer.

Method of preparing 2,2-dimethyl-4-(2',3'-epoxy)

The invention relates to a process for the preparation of polyglycerols (with more than 50% by weight of diglycerol) which are low in cyclic components, by reacting glycerol with chlorohydrins. In this reaction, glycerol is reacted with epichlorohydrin (instead of chlorohydrin) at temperatures from 20.degree. to 120.degree. C. and at certain mole ratios of glycerol to epichlorohydrin and in the presence of an acidic catalyst and the reaction mixture obtained, which has not been separated into its components, is reacted at a temperature from 50.degree. C. to 120.degree. C. according to the content of organically bound chlorine in the reaction mixture, with an alkaline-reacting, preferably aqueous solution. After the addition of water, the reaction mixture is desalinated via one or more cation and subsequent anion exchangers, dehydrated by distillation and the glycerol-polyglycerol mixture obtained is separated by fractional distillation into glycerol, diglycerol and higher polyglycerols.

Growing community of inventors

Rheinberg, Germany

Werner Siemanowski