Abstract: A method of binding sulfur compounds, which result as react products during the combustion of sulfur-containing fuels in firing equipment, by the addition of additives. A mixture of alkali carbonate and an alkaline earth oxide, for example a mixture of sodium carbonate and magnesium oxide, are used as the additive. Such a mixture may include approximately one part by weight sodium carbonate and approximately two parts by weight magnesium oxide.

Abstract: A tank containing a water separator composed of bundles of laminations for drying wet vapor, and a superheater for subsequent superheating of the dried vapor. The water separator is coaxially disposed ahead of the superheater in the horizontal-cylindrical tank, which has at least one vapor inlet and one vapor outlet. The superheater includes tube bundles which are uniformly disposed about the central axis of the tank, and can vary in number and type of construction. In the direction of the central axis of the tank, the water separator has the shape of a truncated pyramid or cone. The vapor discharge surfaces of the bundles of laminations, within the water separator, are disposed symmetrically, vertically, and in tiers relative to the central axis of the tank, and are disposed at an angle of between 10.degree. and 170.degree. thereto.

Abstract: A pressure vessel including a cylindrical vessel shell body, a bottom, and a cover, which are composed of cast elements and are clamped together or restrained by axial prestressing tendons located in channels which are distributed over the periphery of the cylindrical shell body, have axes which are parallel to the axis of the vessel, and by tangential prestressing cables located in annular channels on the outer surface of the vessel. The pressure tank also includes a steel liner which is anchored by means of a special gun welded or bolt connection directly to the inner side of the tank shell body. This tank shell body includes at least two cylindrical shells which are formed of cast elements and are successively arranged when viewed in the radial direction.

Abstract: A method of regulating the amount of reducing agent added, especially NH.sub.3 in the case of the catalytic reduction of NO.sub.x of flue gases which originate from a combustion installation which is fired with fossil fuels. The adjustment value for the quantity to be added is determined in response to a prescribed reducing agent/NO.sub.x stoichiometry factor from the quantity of combustion air supplied to the combustion installation or from the exiting quantity of flue gas, and from the NO.sub.x concentration downstream ahead of the catalyzer. Regulation is effected by influencing the stoichiometry factor. The NO.sub.x concentration downstream after the catalyzer is returned to the regulation process as the primary correction value, and the reducing agent concentration downstream after the catalyzer, and the flue gas temperature ahead of the catalyzer, are returned to the regulation process as the secondary correction values.

Abstract: A waste-heat tank which is constructed as a pressure tank, is charged with coolant, and is connected after a pressure gasification. The waste-heat tank has a cooled feed device or tubular-fin-tubular construction which includes an ash container. The waste-heat tank also has a gas/liquid heat exchanger which includes equally long tubular elements which serve as heat transfer surfaces and are integrated into tubular or planar wall units. Each element of the tubular elements is formed of a tube having an axis which is located extending generally parallel to the container axis of the waste-heat tank. Each element itself is guided in a winding manner. Each tube opens via a feed tube into the finger-like end portion of the feed device. The finger-like end portion is coated with refractory material. Each tube is arranged in an individual tubular or channel-like chamber about a polygonal, preferably hexagonal, tubular or channel-like inner space arrangement.

Abstract: A burner for combustion of nitrogen-containing fuels. The burner includes a core-air tube with centrally arranged oil atomizing lance, a dust tube surrounding the core-air tube, a mantle-air tube which surrounds the dust tube and is provided with an axially shiftable twist-blade ring arranged at the air inlet, as well as a burner opening which expands conically toward the combustion chamber. The core-air tube and the mantle-air tube are supplied from a main air conduit. Air jets or nozzles are provided in a concentric arrangement around the burner opening. These air nozzles are connected with the main air passage by conduits, and the air stream discharging from the air nozzles is regulated by a flap.

Abstract: Method and apparatus for burning fine grained material, particularly for the manufacture of cement clinker whereby the product quality is enhanced. At least a portion of the exhaust gases from the kiln at a temperature of about 1000.degree. to 1300.degree. C. are cooled by passing them through a steam generator to a temperature of about 200.degree. to 300.degree. C. At least a portion of the noxious substances such as alkali chlorides and sulfur are condensed out of the gas stream as well as possibly some mineral particles such as partially deacidified kiln dust. The materials condensed out of the gas are separated in the steam generator by means of periodic or continuous cleaning of the heating surfaces of the steam generator. The steam which is generated in the generator is conducted to at least one prime mover such as a steam turbine or a steam motor for the purpose of producing electrical or mechanical energy.

Abstract: A gas/liquid, parallel flow heat exchanger in a waste-heat tank which is constructed as a pressure tank, is charged with coolant, and is connected after a pressure gasification. The waste-heat tank includes conduit-like elements of equal length which serve as heat transfer surfaces and are installed in conduit-like components or wall units. The wall units divide the interior of the waste-heat tank into regions having upwardly and downwardly directed fluid flow. A central, coaxial, polygonal, preferably hexagonal, cylindrical displacement body is provided, with the number of surfaces of the displacement body depending upon the number of heat transfer surface elements. Also provided are wall units which project out of the wall of the container of the waste-heat tank into the interior thereof across from the corners of the polygonal displacement body. Cylindrical displacement bodies are located centrally between the corners of the polygonal displacement body on an imaginary circle.

Abstract: A method of igniting a pulverized-coal pilot-burner flame for a pulverized-coal annular burner flame having an internal back flow region, with the ignition energy being introduced centrally into the interior of the back flow region of the pulverized-coal annular burner flame. To ignite the pilot-burner flame during the process of the initial ignition, at constant primary and secondary air flow and an air coefficient .lambda.--1.1 to 0.4, once or more a powder-laden air/powder mixture is supplied to the pilot-burner at a powder-laden air/powder weight ratio of 1.0 to 0.2. After ignition has been effected, a specified coal flow is continuously added to the pilot-burner flame at the fixed air coefficient .lambda.--1.1 to 0.4.

Abstract: An arrangement for producing gaseous products from solid and liquid, ash-containing fuels and mixtures thereof in an air stream in a reactor. The fuels are introduced into the reactor parallel to the axis thereof. The solid and liquid ash constituents are extensively separated from the gaseous products of the fuel in a slag bath before further cooling-off. The gaseous products are reversed by 180.degree. after leaving the reactor, and subsequently flow into one or more consecutively or parallel connected annular chambers, which are provided with heat exchanger heating surfaces and concentrically surround the reactor. The gaseous products are cooled in these annular chambers.

Abstract: A method of treating process gases coming from a gasification reactor before entry of such process gases into a system of waste heat utilization. The process gases are cooled off to a temperature of at least 800.degree. C. before entry thereof into the waste heat system. Thereafter, the gases are extensively freed of solid matter in a cyclone separator system located ahead of the convective cooling system, and thereafter the gases are cooled off further to a temperature of at least 250.degree. C. in a convective cooling system.

Abstract: A substantially vertical apparatus for cooling process gases originating from a gasification process, along with simultaneous separation of solid matter contained in the process gases. The apparatus is a cylindrical container including several cylindrical container parts. A gas inlet is provided in the lower region of the container shell or mantle and substantially tangential thereto. The gas inlet opens into a cyclone. Cooling surfaces are provided above the cyclone, with those directly above the cyclone being embodied as platen heat transfer surfaces, and those further above being embodied as cylindrical heat transfer surfaces. The cylindrical heat transfer surfaces are suspended in the container via support elements in the manner of an immersion heater. The support elements, in conjunction with a tube and a regulating device arranged at the process gas outlet, regulate the volume or quantity of the process gases flowing or circulating around the upper cylindrical heat transfer surface.

Abstract: A method of treating final products from a flue gas desulfurization. The flue gas desulfurization is carried out by the absorption of sulfur oxide in a spray dryer with a suspension which contains lime, or in a reactor with a dry, fine-grained, absorbent which contains lime. Prior to desulfurization, the fly ash carried along by the flue gas which is to be desulfurized is separated entirely, partially, or not at all from the flue gas, and the final products from the flue gas desulfurization, prior to any further treatment thereof, amount to 1-99% by weight, preferably 1-70% by weight, of fly ash, and 1-99% by weight, preferably 30-99% by weight, of the sum of the desulfurization products, preferably calcium sulfite hemihydrate, and/or calcium sulfite, and/or calcium sulfate dyhydrate, and/or calcium sulfate hemihydrate, and/or calcium sulfate, as well as residue of the absorbent. The reduction of the amount of calcium sulfite is implemented by a dry oxidation with air.

Abstract: A method of treating reaction products which result from the combustion of fuels containing contaminants such as sulfur, chlorine, and fluorine compounds, and ash. Additives are reacted in the combustion chamber with gaseous contaminants of the reaction products of the combustion. Subsequently, the remaining reactive additives, the reactive ash constituents, and possibly supplementary additives are reacted externally of the combustion chamber with the still uncombined gaseous contaminants of the reaction products.

Abstract: A method of ignition of a coal dust annular burner flame having an internal back flow region. The ignition energy is introduced centrally into the internal back flow region of the coal dust annular burner flame, and is delivered entirely or at least partially by a dust-ignition flame. The dust air-dust weight ratio for the dust-ignition flame is smaller than that of the main burner flame, being either 0.5 to 1.0, or 0.2 to 0.5, compared with a ratio of 1.5 to 2.0 for the main burner flame.

Abstract: An apparatus for dry removal of hot residues resulting from a gasification of coal or carbon-containing solid materials in the lower region or a shaft-like fluid flow gasification reactor which is operated under pressure in downward flow. A wall-heating surface, having upward flow therethrough and having a tube-fin-tube construction, is disposed parallel to and on the inner side of the insulation of the pressure tank wall. This wall-heating surface tapers in the manner of a funnel from a large cylindrical diameter to a small cylindrical diameter. The wall-heating surface has a constricted throat, and thereafter passes over from the cylindrical cross section to the cross section of a four-cornered chamber. Inlet openings are located directly ahead of and at the narrowest point of the constricted throat for cold, clean product gas which is used as fluidizing and cooling gas.

Abstract: A method of treating reaction products which result from the flame combustion of fuels containing contaminants such as sulfur, chlorine, and fluorine compounds, and ash. Additives are added to the combustion chamber by means of a gaseous and/or liquid carrier flow accompanied by the formation of a veil which surrounds the burner flame. Subsequently, the remaining reactive additives, the reactive ash constituents, and possibly supplementary additives are reacted externally of the combustion chamber with the still uncombined gaseous contaminants of the reaction products.

Abstract: A flue-stream reactor for gasifying fossil fuels which contain ballast. The reactor comprises two cylindrical, cooled, and insulated reaction chambers which are disposed one after the other in the axial direction. The first reaction chamber is provided with an axial inlet for accommodating a gasification burner. The second reaction chamber is provided with an opening for the addition of gasification material. A cooled, coaxial channel provides communication between the two reaction chambers. The reactor further includes a radial discharge and a device for removing liquid and solid ash and slag.

Abstract: A method and apparatus including a connection element for transfer of knock- or impact-beating energy from a mechanically, hydraulically or pneumatically driven knock- or impact-beating device upon heating or cooling surfaces to be cleaned intermittently. The heating or cooling surfaces are installed in a container or vessel driven and operated on the gas side at an elevated pressure compared with respect to the atmospheric environmental pressure. The heating or cooling surfaces have external flow of hot, dust-laden gases thereagainst. The knock- or impact-beating device is fastened externally of the pressure container.

Abstract: A method of continuously introducing additive, which is conveyed by gaseous and/or liquid carriers, into a turbulent reaction gas flow in the combustion chamber of a steam generator having dry ash withdrawal for selective removal, in a dry manner, of environmentally harmful gaseous noxious materials, such as sulfur, chlorine, and chlorine compounds, which are contained in a hot reaction gas flow which results after a complete or incomplete flame combustion of solid, liquid, or gaseous fuels. Depending upon the additive introduced, heat is stored and/or used for decomposition reactions. The additive, is first introduced at one or more input locations, due to locally different pressure conditions in the combustion chamber, into one or more recirculation flows which are within the system and are closed. The additive is subsequently withdrawn from these recirculation flows and is introduced into the reaction gas flow.