Abstract: A process for polymerization of a diene is provided. The process comprises: a) reacting the diene with hydrogen peroxide in a hydrophilic organic solvent in the presence of water to obtain a polymerization reaction mixture; b) contacting the polymerization reaction mixture with water having a temperature of from 20 to 80° C. to form a mixture having an organic phase and an aqueous phase; c) removing unreacted gaseous diene from the water mixture obtained in b); d) separating the aqueous phase comprising the hydrophilic solvent from the organic phase of the water mixture; and e) distilling volatile materials from the separated organic phase from d) to obtain the polymerization product; wherein a temperature of the reaction a) is from 50-150° C.

Abstract: The present invention relates to a preparation comprising at least one encapsulation material and at least one bioactive natural substance, which bioactive natural substance can be released from the preparation in a controlled manner, wherein the encapsulation material comprises at least one glyceride with a melting point of at least 35° C. and additionally at least one polymer with polyester units, which has a melting temperature of at least 30° C. and a viscosity in the range from 50 mPa*s to 250 Pa*s, measured by means of rotational viscometry at 110° C. The present invention further describes processes for producing the preparation of the invention, as well as preferred uses.

Abstract: A halogen lamp is described that is intended in particular for at least one mode of operation at a lamp voltage substantially below the nominal voltage or a lamp power substantially below the nominal power or that is intended for switching between a first such mode of operation and a second, normal mode of operation in which the lamp is operated substantially at its nominal voltage or power. To prevent, in the first mode of operation, any increased mass transport of molybdenum and, as a result of this, possible blackening of the envelope of the lamp or growth of whiskers in the region of the legs of the incandescent filament or of the first turns of the incandescent filament, use is made of a bromine-free filling gas that has chlorine. Lamps of this kind are used for example in the headlights of motor vehicles for what is termed daylight running (DRL=daylight running light).

Abstract: A mixture of propyleneglycolmethylether and propyleneglycolether which is added in a ratio of 60:40 and 90:10 to the last rinsing bath in which metal parts are cleaned, in order to achieve intermediate corrosion resistance.

Abstract: The reflector lamp unit has an electric lamp (10) mounted in a reflector body (1) having a neck (4). A metal sleeve (20) is present around the neck. The sleeve has outward projections (21) to provide grip to retention means of a lamp holder, and inward projections (22) which engage grooves (6) present in the neck. The free-end portion (5) of the neck (4) extends beyond the sleeve (20). The unit is of a simple construction, which nevertheless provides for a rigid coupling of the sleeve (20) to the reflector body (1) even with large tolerances as to the size of the neck (4). The unit, moreover, obviates the risk of short-circuiting the contact elements of a lampholder by the metal sleeve.

Abstract: A cleaning agent composition and method, especially for cleaning electronic components, optical parts, and circuit boards. The liquid agent is completely CFC-free and biologically harmless. The composition includes a dipropylene glycol monoether and one or more of the following: N-alkyl-lactam; dihydro-2(3H)-furanone; a polypropylene glycol ether; R.sub.4 --CH(--OH)--CH.sub.2 --NH.sub.2 ; N(R.sub.5).sub.3 ; R.sub.6 --N[(CH.sub.2 CH.sub.2 O).sub.n H] wherein R.sub.4 is a chain of 1-6 carbons, R.sub.5 is a chain of 2-18 carbons, R.sub.6 is a chain of 8-18 carbons and n is a number between 2 and 25.

Abstract: A process isolates, in a closed circulation, the soluble fluid carried over into a rinsing bath from said rinsing bath and to return the fluid into the upstream bath. To this end, enrichment by separating the soluble fluid from the rinsing bath is provided, the enriched fluid, which has been carried over, is returned into the upstream bath together with solvent, where the solvent is separated out with the use of a membrane.