Abstract: A configuration, which may be part of a heavy-duty dynamoelectric machine, in particular a stator, being impregnated with a filler such as a cured epoxy resin, includes a ferromagnetic and electrically conductive carrier body having grooves formed therein defining groove walls, and winding elements disposed in the grooves. Each of the winding elements has an electrically highly conductive basic unit, an impregnatable insulating sleeve surrounding the basic unit, and an electrically weakly conductive, impregnatable protective layer enveloping the insulating sleeve. Impregnatable separating layers are each disposed between a respective one of the winding elements and at least one of the groove walls of a respective one of the grooves. The separating layers are substantially formed of laminated mica sheets resting flat between the winding element and the groove wall.

Abstract: A water-soluble metallocene-complex composition which can be used as a cytostatic is described, which can be obtained by mixing a metallocene complex, a polyol, water and optionally additives, whereby glycols, sugar alcohols and carbohydrates are primarily used as the polyols.

Abstract: A process is described for the preparation of aqueous solutions of betaines of the formula ##STR1## in which: R.sup.1 is an alkyl radical having 6 to 22 carbon atoms or is a radical of the formula R'CONH(CH.sub.2).sub.z --, in which R' has the meaning of R.sup.1 and z is 2, 3 or 4, R.sup.2 is an alkyl radical having 1 to 4 carbon atoms or is a radical of the formula --(CH.sub.2).sub.m --OH, in which m is 1, 2 or 3, R.sup.3 is an alkyl radical having 1 to 4 carbon atoms or is a radical of said formula --(CH.sub.2).sub.m --OH and y is 1, 2 or 3. The aqueous betaine solutions are prepared by quaternization of the corresponding tertiary amines with an .omega.-halocarboxylic acid and with an alkali metal hydroxide in the aqueous phase. The quaternization is carried out continuously in two or three stirred tanks arranged in a cascade, defined process characteristics being maintained in each tank. Using the novel process, aqueous betaine solutions are obtained in high yield and purity in a simple manner.

Abstract: A process for producing carbamazepine ##STR1## by (i) optionally purifying a solution of CCDA ##STR2## in an anhydrous, aromatic solvent; (ii) if required distilling off water in the solution; (iii) diluting the water-free solution with an additional amount of the anhydrous, aromatic solvent; (iv) in a reactor aminating the diluted solution at from about 70.degree. C. to about 105.degree. C.

Abstract: The invention is directed to a process for the synthesis of 5-chlorocarbonyl-5H-dibenz[b,f]azepine, which is the precursor for the industrial scale synthesis of 5-carbamoyl-5H-dibenz[b,f]azepine. The latter substance is used as pharmaceutical compound. In the process phosgene is passed into a suspension of iminostilbene in an inert solvent at 20.degree. C.-60.degree. C. until the iminostilbene reacted to form an almost equimolar mixture of 5-chlorocarbonyl-5H-dibenz[b,f]azepine and iminostilbene hydrochloride, and then iminostilbene is released from the iminostilbene hydrochloride by the addition of an aqueous base. The iminostilbene so released is also made available for a complete phosgenation while an acidic reaction environment is maintained. After the iminostilbene reacted completely, the reaction mixture is heated slowly to 20.degree. C.-90.degree. C. with stirring and is detoxified by the hydrochloric acid that is formed.

Abstract: A process for the preparation of sulfated alkanol oxethylates or alkylphenol oxethylates is described. After completion of the reaction with SO.sub.3, 0.1 to 0.5% by weight, relative to the alkanol oxethylates or alkylphenol oxethylates employed, of at least one of the following compounds: water, ethanol, 1-propanol, 2-propanol or n-heptane are admixed to the reaction mixture and liquid and gas are subsequently separated at a temperature of 20.degree. to 60.degree. C. The liquid is then neutralized with aqueous alkali as customary and leads to ether sulfate/water mixtures with considerably reduced contents of 1,4-dioxane which can either be used without further aftertreatment or with a considerably reduced outlay in terms of aftertreatment as personal hygiene agents and for various other purposes.

Abstract: To extend the temperature range of composite materials the composite material is made up of more than two hard layers which are joined with thin intermediate layers of viscoelastic material where one intermediate layer differs from another intermediate layer in that its softening range lies in a different temperature range so that the damping ranges of the intermediate layers also are different.

Abstract: Medium-load power generating station with an integrated coal gasification plant, a gas turbine power generating station part connected to the coal gasification plant, a steam power generating station part connected to the raw gas heat exchanger plant of the coal gasification plant, a methanol synthesis plant having a plurality of modules connected in parallel to each other, and a purified gas distribution system which connects the methanol synthesis plant to the gas turbine power generating station part and which includes a purified gas continuous flow interim storage plant and is connected on the gas side to the raw gas heat exchanger plant. The methanol synthesis plant is associated, for hydrogen enrichment, to a "cooler-saturator loop" which is connected to the raw gas heat exchanger plant and consists of the saturator, a converting plant, cooler and following gas purification plant.

Abstract: Power generating station with a high-temperature reactor, a steam power generating station connected to the high-temperature reactor, a plant for generating hydrogen from carbon-containing material, with a coal gasifier for the hydrogenating coal gasification, a gas purification plant connected to the gas stream of the coal gasifier, a low-temperature gas separation plant following the gas purification and a tube cracking furnace which is connected to the methane line of this gas decomposition plant heated by the heat transporting medium of the high-temperature reactor for cracking a methane/steam mixture, and with a gas processing plant which is connected to the exhaust gas line of the tube cracking furnace and consists of at least one heat exchanger, a converting plant and a carbon dioxide scrubber.

Abstract: Power generating plant with an integratd coal gasification plant, with a heat exchanger and gas purification plant connected to the coal gasifier, with a gas turbine and steam power generating plant part connected to the heat exchanger and gas purification plant, and with a methanol synthesis plant. The methanol generated in the methanol synthesis plant as well as the synthesis exhaust gas of the methanol synthesis can be fed, at least partially, to a further subplant for a second chemical manufacturing process and the excess synthesis exhaust gas from the methanol synthesis and the exhaust from this further subplant, to the combustion chamber of the gas turbine power generating plant part.

Abstract: Power generating plant with an integrated coal gasification plant, with a heat exchanger and gas purification plant connected to the coal gasifier, with a gas turbine and steam power generating plant part connected to the heat exchanger and gas purification plant, and with a methanol synthesis plant. The methanol generated in the methanol synthesis plant as well as the synthesis exhaust gas of the methanol synthesis can be fed, at least partially, to a further subplant for a second chemical manufacturing process and the excess synthesis exhaust gas from the methanol synthesis and the exhaust from this further subplant, to the combustion chamber of the gas turbine power generating plant part.

Abstract: Gas turbine and steam power generating station with an integrated coal gasification plant which is supplied with oxygen via an air decomposition plant, with a methanol synthesis plant connected to the coal gasification plant, with a steam generating station part connected to the exhaust heat boiler of the gas turbine, as well as with a nitrogen line leading from an air decomposition plant to the combustion chamber of the gas turbine. The coal gasifier for the hydrogenating coal gasification is connected to a hydrogen supply line; the coal gasifier is followed, for utilizing the residual coke, by an iron bath gasifier, which is followed on the exhaust gas side by a converting plant and a carbon dioxide scrubbing plant connected to the hydrogen supply line. The exhaust gas line of the coal gasifier is connected via a gas purifier to a methanol synthesis plant and the exhaust gas line of the methanol synthesis plant is connected to the combustion chamber of the gas turbine.

Abstract: Medium-load power generating plant with an integrated coal gasification plant, with a gas-turbine power generating plant part connected to the coal gasification plant, with a steam generating plant part connected to the raw-gas heat exchanger installation of the coal gasification plant, and with a methanol synthesis plant. The methanol synthesis plant has parallel-connected modules and is connected to the gas-turbine power generating plant part via a central purified gas distribution system which includes a purified gas continuous-flow interim storage plant connected parallel to the pure gas supply line and is connected on the gas side to the raw-gas heat exchanger installation.

Abstract: The invention relates to synergistically active mixtures for the control of phytopathogenic fungi and bacteria comprising antimicrobially effective derivatives of a phenol of the general formula ##STR1## R.sub.1, R.sub.2, R.sub.5 and R.sub.6 represent hydrogen (for R.sub.5 and R.sub.6 only), bromine, chlorine or alkyl with up to 5 C-atoms, R.sub.3 represents hydrogen, sodium, potassium, calcium, barium or ammonium*, magnesium, bismuth, tin, zinc or copper, furthermore R.sub.1, R.sub.2 and R.sub.3 may be interchangeably positioned in the ortho position as well as in the para position, and using fungicides.Benzimidazole fungicides or dithiocarbamates are predominantly used preferably on potato tubers with carbendazim and thiabendazole as mixing components.

Abstract: Medium-load power generating station with an integrated coal gasification plant, a gas turbine power generating station part connected to the coal gasification plant, a steam power generating station part connected to the raw gas heat exchanger plant of the coal gasification plant, a methanol synthesis plant having a plurality of modules connected in parallel to each other, and a purified gas distribution system which connects the methanol synthesis plant to the gas turbine power generating station part and which includes a purified gas continuous flow interim storage plant and is connected on the gas side to the raw gas heat exchanger plant. The methanol synthesis plant is associated, for hydrogen enrichment, to a "cooler-saturator loop" which is connected to the raw gas heat exchanger plant and consists of the saturator, a converting plant, cooler and following gas purification plant.

Abstract: Power generating station with an integrated coal gasification plant, with an air separation plant, a coal gasifier and a heat exchanger and dust removal plant connected to the coal gasifier, as well as with a gas turbine and steam power generating part connected to the heat exchanger and dust removal plant part. An ammonia synthesis plant is connected to the coal gasification plant with the interposition of a gas purification plant and a gas decomposition plant. Part of the exhaust gas produced in the ammonia synthesis can be fed as so-called purge gas to the combustion chamber of the gas turbine together with the gases separated in the gas purification plant and in the gas separation plant, and part of the dust-free raw gas of the coal gasifier.

Abstract: A high frequency amplifier for a frequency range from 300 MHz to 3 GHz and having output power in the megawatt range. A beam generating device for generating a rotating electron beam includes an input resonator ring rotationally symmetric with respect to the amplifier axial axis and which presents a concentric input gap. A cathode ring disposed in front of the input gap generates the electron beam in response to an HF electrical field. The azimuthal angle width of that electron beam can be adjusted by means of a direct voltage between cathode ring and grid ring. An output resonator ring converts the kinetic energy of the beam electrons into HF power in dependence on the azimuthal angle width of the entering beam. The output resonator is rotationally symmetric with respect to the amplifier axis, axially spaced from and biassed with respect to the input resonator by a direct voltage.

Abstract: Combination method for the gasification of coal and the reduction of metal ores involving hydrogenation gasification of coal to produce hydrocarbons and a coke component. The coke is subjected to steam gasification and the gas therefrom used to reduce ores. Spent gas from the reduction is treated to convert CO in the gas to H.sub.2 and CO.sub.2. The CO.sub.2 is scrubbed out and the H.sub.2 is sent to the hydrogenation gasification to hydrogenate the coal.