Abstract:
An arrangement for separating coarse ash out of a flue gas stream, comprising a catalytic converter disposed in a widened flue gas channel portion and serving for reducing the NOx level in the flue gas stream. Also disposed in the widened channel portion is a separator sieve that extends essentially over the entire cross-section thereof. The separator sieve is provided with a plurality of openings for the passage of flue gas therethrough. Each opening has a cross-section that is smaller than a cross-section of coarse ash particles that are to be separated out.
Abstract:
Apparatus for the separation of undesirable constituents from a waste gas, with a first reaction stage (4) defining at least one reaction chamber (14), exhibiting on the head side feeding structure and on the bottom side funnel-shaped discharge structure for the feeding and discharging of a lumpy or granular adsorbent. The feeding structure is formed by a grid of several feed hoppers (18) arranged in side-by-side relationship and one behind the other. The discharge structure is formed by a further grid of discharge hoppers (20) arranged in side-by-side relationship and one behind the other. At least on one side as well as in the head zone of the reaction chamber (14), waste gas passages are provided.
Abstract:
An adsorption medium reactor has a plurality of removal hoppers for removing flowable adsorption medium from the reactor. Each one of the removal hoppers has at least one removal opening. A common collecting funnel is arranged below the removal openings of the removal hoppers. The common collecting funnel has a removal device for emptying the common collecting funnel. Each one of the removal openings of the removal hoppers is slot-shaped and has two parallel-extending limiting edges. A rotary gate with at least one gate chamber is arranged below each one of the removal openings. The rotary gate is limited by a substantially cylindrical circumferential wall. The cylindrical circumferential wall has a plurality of inlet/outlet openings adapted to a cross-section of the corresponding removal opening. The inlet/outlet openings are arranged in a row axially adjacent to one another parallel to an axis of rotation of the rotary gate. The rotary gate is arranged such and a size of the cylindrical circumferential wall is selected such that all of the inlet/outlet openings arranged in a row communicate in one rotary position with the corresponding removal opening and in at least one other rotary position allow for emptying of the bulk material from the gate chamber under the force of gravity. In at least one other position the removal opening is closed off by the circumferential wall forming a closure body.
Abstract:
In a method for purifying a carbon-containing adsorption medium used for treating flue gases within a flue gas scrubbing process the adsorption medium is introduced into an adsorption medium reactor where the adsorption medium adsorbs pollutants from the flue gas. The adsorption medium laden with pollutants is then removed from the adsorption medium reactor and conveyed into a thermal regeneration apparatus. At temperatures of 350.degree. to 650.degree. C. the pollutants are desorbed in the thermal regeneration apparatus, resulting in a desorption gas. In the desorbing step, pollutants in the form of heavy metals are vaporized and pollutants other than heavy metals are released from the adsorption medium and optionally decomposed. The desorption gas is then guided into an adsorption apparatus where the heavy metals are removed from the desorption gas by adsorption. The desorption gas substantially free of heavy metals is subjected to further treatment, preferably is reintroduced into the flue gas scrubbing process upstream of a flue gas scrubbing apparatus.
Abstract:
A device for metered removal of flowable solid material comprises at least one delivery opening for the flowable solid material and an essentially horizontal intermediate storage floor for receiving the flowable solid material, arranged below said delivery opening. A collecting space for the flowable solid material is defined between the intermediate storage floor and the delivery opening. A lateral opening is positioned in the intermediate storage floor adjacent to the delivery opening. At least one removal rake with at least one blade is inserted into the collecting space and movable relative to the intermediate storage floor transverse to a delivery direction of the delivery opening for pushing the flowable solid material collected under the delivery opening into the lateral opening. A pivoting parallelogram-shaped rod arrangement with upper pivoting axes that are arranged in a common horizontal plane is provided for pivotably supporting the removal rake.
Abstract:
The invention relates to a method for reducing a chimney draught in an upstream connected exhaust gas cleaning system consisting in immersing a chimney tube (1; 1′) provided with the open top part thereof in a bath in such a way that a liquid (condensate) collected therein forms a liquid barrier closing the exhaust gas input end of the chimney tube with respect to environment. In order to remove the exhaust gases from the upstream connected exhaust gas cleaning system, at least one part of the chimney tube cross section is exposed by lowering the liquid level under the edge thereof. Said lowering of the liquid level can be carried out by lowering the bath.
Abstract:
A fluid-permeable wall component of a sandwich-type construction has a slotted hole screen with substantially parallel extending vertical slot-limiting elements. A stabilizing grate is connected to the slot-limiting elements and includes connecting rods extending transverse to the slot-limiting elements and a louver-type construction with slats that extend transverse to the slot-limiting elements. The wall component is employed in an adsorption medium reactor of the fluidized bed type as a dividing wall for dividing the treatment chamber into compartments or an outer limiting wall. It retains particles of the adsorption medium within the divided compartments of the treatment chamber without obstructing the transverse fluid flow and allows separate removal of adsorption medium from either compartment.
Abstract:
Process for adsorbing undesirable constituents from a waste gas by feeding the waste gas through at least one reaction chamber filled with lumpy or granular adsorbent, and through at least one adsorption layer. The adsorbent is introduced into the reaction chamber and discharged therefrom through several separate feed and discharge hoppers in a grid-like distribution. The waste gas is guided in part from the side transversely to the adsorption layer and in part vertically through the reaction chamber by introducing the waste gas between the separate feed hoppers from above to flow downward through an exposed upper surface of the adsorbent in such a manner that the adsorbent in all zones of the reaction chamber participates practically uniformly in the adsorption.
Abstract:
A device for separating undesired exhaust gas components from a fluid comprises a reactor with a reaction chamber and having a top and a bottom. The top has a device for introducing a granular adsorption medium. The bottom comprises first and second oppositely slanted sidewalls arranged parallel to one another and forming between them a gutter open in an upward direction. Sections of the gutter form removal funnels with a funnel mouth for removing the granular adsorption medium. The bottom further has fluid inflow openings for admitting the fluid into the reaction chamber, whereby the funnel mouths and the fluid inflow openings are arranged alternatingly in the gutters. The funnel mouths are arranged to form a grid structure. The bottom also has distributing elements for covering the fluid inflow openings. The distributing elements have a pyramid, a cone, a pyramid sector, or a cone sector shape. The distributing elements have lower edges that are vertically spaced at least with portions thereof from the oppositely slanted sidewalls for forming the fluid inflow openings.
Abstract:
The invention relates in general to a reactor installation for countercurrent treatment of gases and bulk solids and, in particular, to a moving bed reactor installation with at least one reaction chamber which latter has at least one inlet and at least one outlet for passing therethrough a solid material present in bulk from the top toward the bottom countercurrently to a gas, at least one flow baffle by means of which the gas is conducted from the bottom toward the top into the bulk material present in the reaction chamber, at least one first sliding surface for the bulk material, arranged above the reaction chamber and terminating at its upper end into a feeding shaft or hopper and supplying the inlet of the reaction chamber with bulk material, and at least one second sliding surface for the bulk material, arranged below the outlet, wherein the sliding surfaces are inclined regarding the horizontal to such an extent that the bulk material is conveyed in the inclined direction solely under the action of gravity.