Abstract:
Adsorption agent cartridge includes a vacuum tight cover having an adsorption agent filler consisting of a substance which can adsorb operating medium steam. The adsorption agent cartridge further includes an inlet opening for the inflow of the operating medium steam and an exhaust opening, which preferably connects to an exhaust device, for expelling air and nonadsorbed gases from the adsorption agent filler. The adsorption agent filler is designed to adsorb the operating medium steam and not to adsorb air components. The exhaust opening and the inlet opening are so arranged with respect to the adsorption agent filler such that the non-adsorbed gases are expelled from the regions of the adsorption agent filler without the concurrent removal of the inflowing operating medium steam.
Abstract:
A leakage free bushing for placement through a surface of a fitting body. The leakage free bushing has flexible bellows, a moveable sealing element and a stationary sealing seat. The flexible bellows have one end connected to the fitting body in a leakage free manner while its other end is capable of an angular tilt movement with respect to the vertical axis of the flexible bellows. The moveable end of the flexible bellows are covered in order to prevent leakage. The flexible bellows have an actuating knob connected to its outer area which, when rotated, permits mechanical deflection of the bellows. In the inner area of the fitting body at the left of the bellows axis, a transmission assembly is located which transmits the mechanical deflection caused by the actuating knob to the inner space of the fitting body.
Abstract:
Steam power plant, including a steam turbine having a high pressure section with an exhaust steam outlet, a steam generator having a live steam side connected upstream of the high pressure section of the steam turbine, the steam generator having a combustion chamber and a convection space formed therein, an intermediate superheater heating surface having an outlet and having an inlet being connected to the exhaust steam outlet of the high pressure section of the steam turbine, a device for applying combustion air to the combustion chamber of the steam generator, and a device disposed at the outlet of the intermediate superheater heating surface for regulating steam temperature thereat, the regulating device including a nozzle terminating in the convection space of the steam generator between the combustion chamber and the intermediate superheater heating surface.
Abstract:
A steam generator configuration, in particular of a low temperature carbonization-combustion plant, includes a supporting structure. A flue gas channel is disposed in the supporting structure and has a first vertical segment, a second at least approximately horizontal segment, and a third vertical segment being connected through the second segment to the first segment to form a structural unit. Supporting members suspend the first segment in the supporting structure in order to avoid restrictions to expansion and deformation of the flue gas channel as a result of thermal expansion. The supporting members are in an oblique or slanted position relative to the vertical in a cold condition. The oblique position essentially corresponds to a thermal expansion of the second horizontal segment in a hot condition. The supporting elements are parallel to the vertical in the hot condition. Thus, regardless of the operating state, the flue gas channel remains a structural unit that allows free thermal expansion in the vertical and horizontal directions.
Abstract:
A cooling system with a vacuum tight operating system manifold line contains at least two connecting locations on which at least an operating medium evaporator and at least a sorption agent container having sorption medium therein are coupled in an airtight manner to the operating system manifold. The sorption medium container is capable of absorbing and deabsorbing operating medium vapor.
Abstract:
Reheating flue gas behind a wet flue gas desulfurization plant, in which the desulfurized flue gas is admixed with fresh air which had been warmed up first together with the fresh air intended for the combustion, in a heat exchanger by a third medium, then by the flue gas air preheater, by the flue gas flowing into the flue gas desulfurization plant without the temperature falling below the dew point temperature of the flue gas before it enters into the flue gas desulfurization plant.
Abstract:
A method for heating a low temperature carbonization drum includes generating a low temperature carbonization gas in the drum; combusting a partial flow of the low temperature carbonization gas for generating a heating gas; conducting the heating gas in a heating gas circuit; preheating the cooled heating gas flowing out of the drum; and then returning a controllable partial flow of the cooled heating gas to the drum while re-admixing the controllable partial flow with the heating gas. A device for heating the low temperature carbonization drum includes a heating gas circuit having an inflow line and an outflow line connected to the drum generating low temperature carbonization gas; the heating gas circuit having a combustion chamber for receiving a partial flow of the low temperature carbonization gas from the drum and generating a heating gas to be delivered to the drum; and the heating gas circuit having a heat exchanger connected upstream of the combustion chamber for preheating the heating gas being cooled in the drum. A low temperature carbonization/combustion plant includes a combustion chamber of a combustion system receiving a remaining flow of the low temperature carbonization gas generated in the drum. The combustion system produces steam to be supplied to the heat exchanger.
Abstract:
A plant for thermal waste disposal includes a pyrolysis reactor having a first heating device for indirectly heating the waste and a second heating device for directly heating the waste within the pyrolysis reactor. The pyrolysis reactor converts the waste into low-temperature carbonization gas and solid pyrolysis residue. The low-temperature carbonization gas and the solid pyrolysis residue, possibly after passing through a treatment device, are fed to a high-temperature reactor for combustion. The first heating device ensures a basal heating of the waste in the pyrolysis reactor. A separate fuel or waste heat from the flue gas of the high-temperature reactor can serve the purpose of ensuring the basal heating. Supplementary heating is provided as required with the aid of the second heating device by providing an air feed into the interior of the pyrolysis reactor. A process is also provided for operating the plant for thermal waste disposal.
Abstract:
Adsorbent bed coating for use on a metallic surface includes a powder-like solid adsorbent bed with a grain diameter between 1 and 50 .mu.m bonded by a finely dispersed binder agent with a mass component of less than 50% with respect to the powder component. The thickness of the adsorbent bed coating on the metallic surface is less than 4 mm such that the adsorption speed of water vapor at a steam pressure of less than 20 mbar results in a weight increase of at least 5% (with respect to the adsorbent bed) within 30 minutes.
Abstract:
Device for preventing flashing to steam in an economizer of a flow-through steam generator wherein the economizer has heating surfaces disposed downstream of an evaporator and superheater surfaces in direction of a flue-gas path, including at least one partition separating the cross section of the flue-gas path in vicinity of the economizer into at least two joint areas separated from one another, the economizer having tubes disposed only in one of the thus formed joint areas, and further including shut-off devices for the flue-gas disposed upstream of the tubes of the economizer as viewed in the direction of the flue-gas path.