Kraftwerk Union Aktiengesellschaft

Siemens Aktiengesellschaft

Konrad Kunstle

Christian Koch

Gerd Brunner

Kurt Reiter

Rainer Hoffmann

Herbert Tratz

Wolfgang Kohler

Wolfgang Kastner

Hermann Finckh

Herbert Gottschlich

Till Dehrmann

Rainer Dorn

Jurgen Hoffmann

Steam is generated by conducting a medium through a line which is exposed to solar irradiation. The line has a starting point where a medium supply line issues into the line. The heated medium is conducted away from the at least one line through a drain line. The medium, prior to feeding in at the starting point, is prepared in a power plant component and the medium is supplied at a pressure which is higher than the prevailing pressure in the at least one line, and at an enthalpy which is greater than an enthalpy of saturated water in the line. The medium is fed in as water or water and steam.

Method and device for solar steam generation

A process and system for low-temperature carbonization of oil shale, oil sands and similar oil-bearing solids includes low-temperature carbonization of oil-bearing solids in a high-pressure fluidized bed reactor in the presence of a substance selected from the group consisting of hydrogen and steam at temperatures substantially between 400.degree.and 600.degree. C. for producing low-temperature carbonization gas. The low-temperature carbonization gas is condensed in at least two stages for producing relatively higher boiling and relatively lower boiling oil fractions. The oil-bearing solids are peripherally mashed with the higher boiling oil fraction of the low-temperature carbonization gas, before introducing the oil-bearing solids into the high-pressure fluidized bed reactor. The oil-bearing solids mashed with the higher boiling oil fraction are returned to the high-pressure fluidized bed reactor.

Process and system for low-temperature carbonization of oil shale, oil

Method of extracting liquid hydrocarbons from oil-containing stone or sand, wherein the oil-containing stone or the oil-containing sand undergoes hydrogenating, low temperature carbonization in a reactor at temperatures of 450.degree. to 520.degree. C. and a pressure of approximately 50 bar through the action of carbon monoxide, hydrogen and steam, and wherein the hydrocarbons are separated from the resulting gaseous, low temperature carbonization mixture. The low temperature carbonization mixture from the reactor is cooled in a first separation stage to a temperature of approximately 350.degree. C. to condense the less volatile hydrocarbons. The separated, liquid phase is fed to a solids separator and placed in contact with a circulating gas of carbon dioxide and a C.sub.6 /C.sub.7 hydrocarbon fraction. The low temperature carbonization mixture containing uncondensed gases and more volatile hydrocarbons are washed in a second separation stage with water and cooled to approximately 250.degree. C. Gas containing hydrogen separated from the volatile hydrocarbons is fed at least partly to the reactor again. Carbon monoxide is obtained from the solids through the action of carbon dioxide, contained in hot, combustion gases. This carbon monoxide together with carbon dioxide of the combustion gases is fed to the reactor.

Method of extracting hydrocarbons from oil-containing rock or sand

A process for extracting hydrocarbons from oil shale comprising the steps of subjecting oil shale under superatmospheric pressure in the presence of hydrogen and steam, to low temperature hydrogenating distillation; separating the resulting fluid distillation mixture into liquid and gaseous products; and returning water and hydrogen separated from the fluid distillation mixture to the low temperature distillation; in which:

Process and apparatus for extracting hydrocarbons from oil shale

Installation for generating superheated steam from raw water containing salt using preheaters for heating the raw water. The last preheater, as seen in the flow direction of the raw water, is followed via a control valve by a decompression cylinder. Part of the raw water evaporates and the vapor is withdrawn from the dome of the decomposition cylinder by a compressor which compresses and heats it and discharges it as superheated steam.

Installation for generating superheated process steam from

Steam generator for a solar power plant, with an evaporator heating surface having a front side exposable to focused sun rays and a rear side adjacent a chamber, and burner means for supplying at least part of the heat required by the steam generator, the burner including a sintered-block slab operating as a reformed-gas generator, a burner plate disposed downstream of the sintered-block slab in flow direction of the gas, the burner plate being disposed immediately adjacent the rear side of the evaporator heating surface, and an air-permeable further heating surface for the steam generator disposed between the sintered-block slab and the burner plate.

Steam generator for a solar power plant

System for recovering oil products from oil sands in which superheated steam from a nuclear reactor is mixed with water in a chamber under high superatmospheric pressure to obtain hot water at a temperature near the boiling point at the prevailing pressure. The hot water enters a reaction tube which has an input screw conveyor for feeding oil sands into the reaction tube in contact with the hot water to effect release of the oil from the sands. The outlet of the reaction tube opens into a hydrocyclone into which the reaction products of oil and sand and water are discharged. A screw conveyor at the bottom of the hydrocyclone discharges separated sand and some water which passes into a settling tank to settle the sand and the clarified water is filtered and returned to the pressure chamber. The separated oil together with some water from the hydrocyclone flows to an oil separator where the oil separates from the water, which latter is also returned to the pressure chamber. The oil may be separated into fractions in a fractionating column and the column bottoms may be hydrogenated and returned to the fractionating column. Better oil recovery from the oil sand can be achieved and more efficient operation attained.

Device for recovering oil products from oil sands

Refining of crude petroleum by fractionally distilling the crude into lighter cuts and distillate bottoms constituting more than 50% of the crude. Hydrogenating the distillate bottoms at a temperature above 700.degree. C. in a tubular reactor to produce saturated hydrocarbons, some gas and a solid carbonaceous material. Separating the solid material in a cyclone and returning the hydrogenated oil to the fractionating column. Passing the solid carbonaceous material by an extruder to a second tubular reactor in contact with a mixture at a temperature above 750.degree. C. of steam, 1 and 2 carbon atom gases, and combustion products containing O.sub.2 from a third cyclone. Discharging the reaction products containing unreacted carbonaceous material together with substantially no O.sub.2, production of H.sub.2 and increased amounts of CO and CO.sub.2 into a second cyclone. Separating the gaseous products from the solid, recovering H.sub.2 and passing it to the first reactor tube. Extracting heat from the gaseous reaction products to superheat the steam entering the second tubular reactor and to preheat the distillate bottoms prior to entrance in the first tubular reactor. Passing the remaining solid carbonaceous material by an extruder together with excess O.sub.2 into a third tubular reactor to effect substantially complete combustion. Discharging the unburned solid residue and combustion gases into a third cyclone from which the combustion gases are sent to the second tubular reactor and the residue containing ash is discharged from the system.

Process for hydrogenized reconditioning of crude oil or residues derived

Coal gasification apparatus having a hydrogenation gasifier chamber for gasifying a portion of coal charge and a steam gasifier vessel for gasifying unconverted coal from the hydrogenation chamber with the chamber disposed above the vessel and a pressure lock interposed between the outlet of the chamber and the inlet of the vessel to permit unconverted coal to flow into the vessel and prevent gas generated therein from passing into the chamber. An oxygen inlet is provided at the lower end of the vessel for residual-oxidation of remaining coal. A heat exchanger is provided for heat exchange between hot gas leaving vessel and incoming steam. The chamber may be preceded by a steam-heated heating tank for preheating the coal under pressure and then suddenly decompressing the coal.

Growing community of inventors

Rottenbach, Germany

Konrad Kunstle