Abstract: An apparatus and method for burning fuel in a combustion chamber having an exhaust port. The invention includes a combustion device having a burner head for burning fuel to produce a volitilization zone of high heat. The burner head is positioned in the combustion chamber directly beneath the exhaust port to assure a substantially vertical flame. The upright flame produces a zone of volatilization that continuously contacts the fuel on the burner to vaporize or volatilize a higher percentage of the fuel than in previous combustion apparatuses.

Abstract: The present invention relates to a high speed burning furnace and incinerator, particularly to a high speed burning furnace and incinerator capable of completely burning pulverized coal in the burning furnace, separating the ash produced by the combustion, injecting the said flame into the incinerator, and then completely burning the waste products. The main feature of this invention resides in that a heavy oil or a pulverized coal can be mixed with a primary air flow and injected into the burning furnace so as to introduce a rapidly revolving secondary air flow from tangential air flow inlets on an inner pipe to help combustion and thus a complete combustion can be effected and the flame can be intensified. This intense flame is introduced into the incinerator to completely burn the waste products sent into the incinerator by a conveyer through a preheating chamber.

Abstract: An ash handling system includes a conveyor and crusher extending from an ash collection trough beneath an underfeed stoker retort to a hopper from which ash is discharged into an ash receiving zone of a container. A suction nozzle is used to extract ash from the zone for disposal.

Abstract: A vibratory fluidized bed reactor vibrates a solid particle bed to fluidize the bed, and air or other gaseous stream is injected into the bed. The reactor can employ a rotationally-vibrated bowl or a linearly-vibrated pan. The vibratory motion keeps the particles evenly distributed and prevents blowholes from developing, leading to improved reaction. The vibratory motion also marches particles up a spiral groove in the circumferential wall of the bowl, e.g., to facilitate ash removal from the fuel bed, to recycle reactants or catalysts, to sequence reactants to subsequent stages, etc. In the case of the pan, vibratory motion marches the particles up an inclined plate.

Abstract: An auxiliary apparatus with a trough or tank, to which the incineration residues are supplied by means of a drop shaft, a movable piston for moving the incineration residues from the trough to a discharge chute and at least one opening for inspecting and maintaining the trough arranged in a side wall at the latter and provided with a door. A plate, which can be inserted through the opening in the trough, is positioned in front of the front face of the piston. The plate is held on the chute walls by locking devices and is supported on the piston by adjusting mechanisms. The front face of the plate assembled from two parts is, for the same width, twice as high as the front face of the piston. The adjusting mechanisms are constructed as an adjustable arrangement of push rods or as pneumatic or hydraulic lift cylinders.

Abstract: A sewage screenings disposal system where raw screenings are fed to a dewatering press (7) for reducing the moisture content of the screenings, slugs of pressed screenings are conveyed from the dewatering press (7) to a multi-compartment storage carousel (17), loader ram means (16) charge the slugs into empty carousel compartments (21) and feeder ram means (26) located remote from the loader arm ram means (16) push the slugs from the full carousel compartments (21) into an incinerator (29). The carousel drive means are connected through a compartment indexing mechanism and carousel locking means (22) whereby during loading or feeding the carousel is locked against rotation.

Abstract: A blowdown pot is provided with an inlet pressure control valve through which the pot receives unwanted residue e.g., ash from a high pressure chemical reactor, and this reactor residue can thereby be continuously or semi-continuously blown out from the high pressure, high temperature chemical reactor into the relatively low pressure blowdown pot which includes means maintaining a liquid level therein minimizing steam flashing and vessel wear. At the same time the reactor residue is removed from the pot with a liquid overflow.

Abstract: The cremator disclosed is of the kind in which reduction burning takes place in a coffin chamber, followed by oxidation burning in an afterburner chamber. It is also of the kind in which partly cremated embers can be moved to an ember-reducing location to make room for another coffin to be admitted to the coffin chamber. The disclosure shows the ash removal port in the side of the cremator, which allows the afterburner chamber to occupy space behind and underneath the coffin chamber; an arrangement which makes for a very compact, fuel efficient, easy-to-construct unit. The hearth includes an ash-trough for ember reduction. The hearth can be thin because it is supported on the central wall that divides the ducts of the afterburner chamber, which makes for good heat transfer, and quick warm-up.

Abstract: A water-fillable trough receives the incineration residues from the drop shaft of a furnace. A partially water-fillable discharge chute slopes upwards from the trough and is provided at its upper end with an overflow edge. A reciprocatible piston conveys the incineration residue from the trough to a circulating device arranged in the discharge chute. The circulating device is in the form of a conveyor belt or a scraper chain and conveys the incineration residues through the discharge chute to the overflow edge. A shutting-off device for separating the chute from the trough is arranged above the transition point between the trough and the chute. The shutting-off device can be in the form of a slide provided with a hoist drive which passes through the upper wall of the chute, or a flap freely suspended by means of joints on the upper chute wall, or as a rubber apron freely suspended from the upper chute wall.

Abstract: A slag tap combustion apparatus which is characterized by comprising a slag tap combustion furnace, a slag granulation chamber for granulating a slag discharged from the slag tap combustion furnace, a slag grain accumulation tower which is filled with slag grains discharged from the slag granulation chamber, a secondary reactor provided with an inlet and an outlet for a waste gas from the slag tap combustion furnace and provided with means for introducing finely powdered lime, a duct for connecting the waste gas outlet of the secondary reactor to the slag grain accumulation tower, and another duct for allowing the waste gas to discharge from the slag accumulation tower.

Abstract: A rotary kiln has a sealable separating gap between the kiln outlet head and an inlet shaft leading to a cooler. In order that the shortest possible drop height for the fired material falling out of the discharge end of the rotating cylinder may be maintained despite the separating gap, interengaging steps and side openings defined thereby are formed in the side walls of the kiln outlet head and the inlet shaft, and sections of the separating gap which run at different heights open into the side openings and the horizontal distance between any two steps lying opposite one another corresponds approximately to the maximum displacement path of the kiln outlet head.

Abstract: An ash disposal system for a furnace (10) including a pair of submerged scraper conveyors (24, 26) mounted within a common water-filled tank (16) with a water seal (18, 28) between the tank and furnace. The tank is mounted on wheels (32) and has a divider wall (30) between the two conveyors so that the tank can be positioned such that one or the other, or both conveyors together, can be operated to remove ash from the tank. A door or gate (34) in one of the side walls of the tank permits the tank to be completely removed from beneath the furnace when desired.

Abstract: An incineration unit is provided with an open ended rotary incineration chamber having a main portion and a neck portion supported between two opposite stationary end chambers. Feed means are mounted adjacent first stationary end chamber and a burner for directing flame into the incineration chamber is mounted on the second stationary end chamber. A secondary combustion chamber extends axially above the incineration chamber and includes an afterburner for completely incinerating the combustion gases and by-products. A conduit is formed in first stationary end chamber for transferring hot incineration gases to the secondary combustion chamber. The burner directs the flow of hot incineration gases towards the raw waste material thereby to initiate drying thereof. A grate cleaning member is also provided at the discharge end of the chamber to assist in the separation of waste material.

Abstract: Wet ash removal equipment in which a trough is filled with quenching water. An immersion member attached to the ash funnel is immersed into the quenching water. A side wall of the trough is sealed by a plate. The plate is supported upon a height-adjustable rod linkage and is guided in its movement on the side of the trough arrangements of rollers.

Abstract: A device to force out the incineration ash in which the main shaft that turns in the positive and inverse directions at a fixed angle by means of a driving mechanism is installed horizontally in the main body case provided with an ash receiving chamber in which water is filled for extinguishing of burning, an inlet opening for the incineration ash discharged out of a refuse incinerator and an outlet opening for the incineration ash after extinguishing of burning; and a pusher to force out the incineration ash settled down on the bottom of the ash receiving chamber and a pressing plate to force down matter floating on the water surface in the ash receiving chamber are fitted on the main shaft that turns in the positive and inverse directions at a fixed angle so as to move the pusher forwards and backwards and the pressing plate upwards and downwards.

Abstract: A process and apparatus for the combustion of carbon-containing fuel in a reaction zone, with the products of combustion being removed from the top of the reaction zone and the slag from the bottom of the reaction zone. The reaction zone is separated from the bottom of the reactor by a partition wall having a central opening through which the slag is removed. The central opening is maintained open by a cylindrical member that is mounted below the partition wall and moved upwardly to clear the opening.

Abstract: A wet ash remover which has a trough arranged underneath the ash funnel of a boiler and is filled with quenching water. A quenching water feed and an overflow are also provided. Ash conveying equipment passes through the wet ash remover. A cooling device with quenching water circulating through it continuously, is located between the overflow and the quenching water feed. One or more sets of parallel oblique plates are located inside the trough in front of the overflow. The set or sets of plates may extend throughout the entire length side of the wet ash remover. The plates may be inclined 50 to 60 degrees from the horizontal, and the planes may be planar. One of the sidewalls of the displaceable trough is connected detachably to the remainder of the trough and rigidly to stationary supports; the sidewall is at least as long as the immersion piece of the ash funnel protruding into the trough. The sidewall may accommodate the overflow and the set or sets of plates.

Abstract: A method for restoring slagging conditions in a substoichiometric slagging combustor first requires the establishment of a threshold condition below which an unacceptable risk of slag outlet pluggage exists. Upon observation of current slagging conditions below the threshold conditions, substantially pure oxygen is injected into the combustion reaction zone to increase both zone temperature and reaction rate, leading to improved slagging conditions within the slagging combustor.

Abstract: Apparatus for discharging solids from a shaft furnace comprises a lock chamber structure, the interior of which is connected to the shaft furnace by a conveyor duct, and a rotor, which is rotatably mounted in the interior of the lock chamber structure and adapted to be driven and arranged to receive solids from the furnace and seals the inlet of the lock chamber from the outlet of the lock chamber. To permit a continuous discharge of solids from the furnace without an escape of gas from the furnace, the rotor consists of a cellular wheel, which has cell-defining walls in a star-shaped configuration. The conveyor duct is connected to a source of a compressed blocking gas. An exhaust gas duct communicates with the interior of the lock chamber structure adjacent to the conveying portion of the cellular wheel between the inlet and the outlet of the cellular wheel.

Abstract: According to the present invention, a sealing chamber is provided into which a noncombustible residue from an incinerator, furnace or the like is moved. The residue may be sprayed with a liquid upon entering the sealing chamber to effect cooling and compaction of the residue. The sealing chamber is provided with a vibratory discharge mechanism which serves to convey the residue out of the chamber and to compact the residue accumulated in a vertical column in the chamber to provide an effective seal against the diffusion and entry of air into the combustion area of the incinerator. Controls are provided in the sealing chamber to maintain the seal and to actuate the vibratory mechanisms for moving the residue. By the time the residue reaches the discharge of the chamber, the liquid in the residue is evaporated by the residual heat in the residue particles.

Abstract: A filter member (98) is mounted on the inside of a sidewall (16) of a receptacle (10), in a position covering an opening (76) in the sidewall (16). A vacuum cleaner suction hose attachment (122) is provided on the opposite side of such opening (76). The receptacle (10) is a closed container when used, except for a sidewall inlet (38) in the sidewall (14) which is opposite the filter carrying wall (16). Ashes (134) are introduced into the inlet opening (38) and dumped into an ash pan (52) contained within the lower portion of the receptacle (10). The vacuum cleaner (130) draws the fine dust to the filter member (98). The fine ash dust is collected by the filter member (98) or is drawn into the vacuum cleaner (130). When the ash pan (52) needs to be emptied, the top (22) of the receptacle (10) is swung open.

Abstract: The invention relates to vibrating hearth burners. Three problems exist in known such burners, these being uniformity of fuel combustion; ash discharge; and over-heating of the grate. To meet the first of these, the present invention provides a burner in which the grate (30) and the vibrating mechanism (10,16) cooperate to decelerate the movement of fuel along the grate (30) as it travels towards the discharge end. This results in a build-up of ash towards the discharge end providing a substantially uniform thickness of fuel/ash on the grate (30), and a substantially uniform pressure drop across the grate (30). The provision of an ignition grate (32) is also contemplated to ensure that the fuel is ignited at the delivery end of the grate (30). To meet the second, the invention contemplates the provision of an ash return chute (54) incorporated in the vibrating grate assembly (8).

Abstract: A hydro-pressurized fluidized bed combustor having an uptanding shell and an entry at its bottom for admission of feedstock. The feedstock passes through a conduit surrounded by a heat exchanger. Inside the shell an entry conduit is outwardly flared in the upward direction to furnish a controlled expansion entry feeding into the fluidized bed. The entry conduit has a plurality of tuyeres in its peripheral wall. An injector pump feeds the feedstock into the entry. A weir above the entry conduit keeps the height of the bed constant within the combustion during operation.

Abstract: This invention provides a system for breaking and removing cremated remains from a crematory furnace. The system includes means for breaking cremated remains into fragments for transmission through a vacuum line into a grinder which reduces the fragments into fine particles. A filter collects fine particles output from the vacuum line; and after completion of the grinding process, the output of the grinder and the particles collected in the filter are collected in a receptacle for removal from the system.

Abstract: Method and/or system for removing liquid slag from a pressurized gasifier. Hot liquid slag is quenched in a quenching medium such as water. The quenched and solidified slag is crushed to a maximum particle size. The crushed slag and quenching medium are alternatively connected to opposite ends of a floating piston while the other end is connected to an outlet for disposal of the slag. The crushed slag and quenching medium are subjected to the gasifier pressure so that the piston acts to forceably eject the mixture through the outlet.

Abstract: A melting apparatus has a low temperature melting portion (29), an exhaust gas cooling portion (26), and a dust collecting portion (B27) which are arranged, in succession, in an exhaust gas duct (54) of a melting furnace (B22). A low boiling point dust collected in the dust collecting portion (B27) is returned to the low temperature melting portion (29) for melting by retention heat of an exhaust gas flowing into the exhaust gas duct (54).

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: Outlet structure of a powdered coal gasification generator. The bottom of the generator has an outlet throat with cylindrical walls that extend beyond the base. And, the walls terminate in an oblique manner with a face shaped to promote flow of slag from the generator to a single point in order to minimize reentrainment of slag into the gasification products.

Abstract: A furnace having a primary heat exchange unit also providing a combustion chamber, a secondary heat exchange unit connected by an upper crossover conduit to the primary heat exchange unit, and a tertiary heat exchange unit connected by a lower V-shaped crossover conduit to the secondary heat exchange unit. A third crossover conduit connects the V-shaped crossover conduit with the primary heat exchange unit. A fly ash removal screw is located in the V-shaped crossover conduit to move fly ash therefrom through the third crossover conduit back into the primary heat exchange unit to an ash depository for removal therefrom. Vibrating means are provided between the secondary and tertiary heat exchange units to vibrate the walls thereof and dislodge clinging fly ash so that it falls into the V-shaped crossover conduit for removal by the screw conveyor. A burner assembly of the furnace includes a combustion air housing carrying a circular, stationary grate with an annular valley for carrying fuel during combustion.

Abstract: A method for incinerating material is disclosed wherein a vertical thermal reactor of the fluidized bed type is employed, the reactor being generally a rectangular shape in a horizontal section and having opposed side walls. Fluidizing medium is subjected to different mass flow at the center portion and the side portions so that relatively strong side fluidized beds are formed adjacent the side walls and a relatively weak fluidized bed is formed at the center sandwiched by the side fluidized beds free of any obstructions therebetween. The center fluidized bed tends to descend relative to the side fluidized beds which are deflected at the upper portions thereof, respectively toward the center so that the fluidized medium circulates from the lower part of the center fluidized bed to the lower parts of the side fluidized beds and from the upper parts of the side fluidized beds towards the upper part of the center fluidized bed.

Abstract: A firebox has a liquid or gaseous burner and also a solid fuel grate assembly associated with a solid fuel inlet above the grate assembly for dropping solid fuel particles thereon. The grate assembly includes upper and lower bar type members and an intermediate member of expanded metal. A blower is mounted under the grate assembly and in combination with the latter provides an even pressurized draft for burning solid fuel particles. A sweeping bar on side runs is capable of sweeping clinkers and ashes from the grate assembly. A bottom auger receives the clinkers and ashes and carries them out of the firebox. A forced air inlet directs a flow of air down on the solid fuel inlet to prevent combustion gases from traveling reversely through the solid fuel inlet. A heat exchange chamber includes a plurality of reversely turned tubes arranged in a plurality of paths and connected by end housings capable of removal for inspection and cleaning.

Abstract: A wet-bottom, solid fuel gasifier has a slag tap through which a portion of the product gas is back-flowed through the slag tap to maintain the temperature of the slag hot enough to maintain continuous slagging. The reverse flow of the product gas portion is controlled by the negative pressure generated in the throat of the gasifier.

Abstract: A water-wall, coal-fired furnace has a Coutant transition section extending down from the lower end to the water wall to the surface of water impounded in the lower ash hopper. The surface of the water is provided with a reflecting material which will permit the passage of solid residue from the coal firing into the water while reflecting incident radiant heat back up into the generating section of the furnace.

Abstract: Apparatus and process for incinerating waste and reclaiming resources, particularly ferrous metals, galss, and aluminum, in separate output streams. The incinerator itself can use combustion draft air as a medium for separating lighter and heavier fractions of the burned material in the incinerator. The combustion zone of the incinerator is defined by a foraminated cylindrical wall which is rotated to distribute the incinerating materials and separate burned waste from the combustion zone.The incinerator can be cooled by a eutectic liquid metal coolant. The use of this coolant allows the heat exhange surfaces of the incinerator to be quite thin for greater economy, as such fluids, particularly a eutectic mixture of sodium and potassium, do not vaporize at atmospheric pressure over a wide working temperature also disclosed, as is improved means for separating aluminum rich and glass rich fractions from the heavier fraction of burned waste separated in the incinerator.

Abstract: A combustion apparatus for a granular solid fuel, comprising a plurality of horizontal cylindrical combustion chambers serially connected in their axial direction, partitions interposed between the combustion chambers, communication holes pierced through the partitions for passing the combustion gas. To the combustion chambers, air is delivered in directions to cause the gas to flow in a swirled state, allow the granular fuel to be burnt as agitated and fluidized within the upstream combustion chamber, and forward the gas in a swirled state from the upstream to the downstream combustion chamber. The combusted gas, on reaching the extreme downstream combustion chamber is drawn out by means of a gas delivery pipe having one end thereof communicating with the combustion chamber.

Abstract: A slag breaker of a pressure-type coal gasifier having a rotary grate with a plurality of grate segments, a generator bottom and an ash separator, has an inclined breaking plate arranged to be located immediately below the grate segment and prior to the ash separator and provided with a plurality of breaking projections, and a wear sheet arranged to be located on the generator bottom and provided with a plurality of breaking webs.

Abstract: In combination, a top-supported furnace (10) in which an ash-bearing fuel is burned, opening means (12) in the furnace bottom, a bottom supported tank (16) open at its upper end and containing water (18) positioned beneath the furnace opening means (12), into which the ash from the furnace (10) falls, means (20) for removing the ash from the tank (16), an intermediate transition piece (26) hydraulic drive means (30) carried by the tank (16) for moving the transition piece (26) between a first position spaced from the furnace bottom, and a second position in engagement with the furnace bottom, means (32, 34) for removably securing the transition piece (26) to the furnace bottom, seal means (36) which completely surround the furnace bottom for sealing the space between the transition piece (26) and the furnace bottom when the transition piece (26) is in its second position, stop means (38) for limiting the movement of the transition piece (26) towards the furnace bottom to prevent the seal means (36) from becom

Abstract: An apparatus for removing and transporting ashes includes a scoop member having a hollow body, a forward end defining an ash receiving opening, and a scoop lid mounted to the body to rotate outwardly therefrom for alternating covering and uncovering the opening; and a container member defining an ash storage compartment and including a lid member defining mouth shaped to receive the forward end of the scoop member and a flap mounted to the lid member to rotate into the compartment for alternately covering and uncovering the mouth. The scoop lid includes a hook member and the flap includes a loop member so that the hook member may engage the loop member to form a rotatable link between the scoop lid and flap such that, when the forward end is inserted into the mouth of the container member, the scoop lid and flap rotate to an open position, thereby uncovering the opening mouth to allow ashes in the scoop member to fall into the storage compartment.

Abstract: The invention provides a conveyer for receiving bed drain material from a coal-burning fluid bed combuster and consists of a jacketed water cooled casing in which is a helical flight for conveying said material, the flight being mounted on an outer tube which is supported by a bearing at one end only in cantilever fashion with its other end within the closed end of the water cooled tube, an inner water cooling tube being located within the outer tube for water to circulate through the inner tube and back through the outer tube.

Abstract: An incineration system for processing solid, semi-solid waste material and sludge includes an incinerator unit which has a horizontally disposed rotary primary oxidation chamber and a generally vertically disposed secondary oxidation chamber which receives gaseous products of combustion from the primary chamber. Baffles within the secondary chamber provide a tortuous gas flow path through the secondary chamber. Gaseous emissions from the incinerator unit pass through a heat recovery boiler, a baghouse and a scrubber tower before being discharged to atmosphere. A control system controls rotation of the primary oxidation chamber and an auger/shredder which feeds waste material to be burned into the primary oxidation chamber. The control system may include a programmable computer for modifying the control functions in response to programmed data relating to the characteristics of material processed in the incineration system.

Abstract: A solid fuel furnace includes a vibratory bowl for its fuel bed. Structure in the furnace defines a fuel chamber over the central part of the bowl and a combustion chamber over the outward part of the bowl. Fuel is distributed outward by a central cone on the bowl. Primary air is fed beneath the rim of the cone into the fuel in the combustion chamber. The vibratory motion keeps the fuel particles evenly distributed and prevents blowholes from developing, leading to improved combustion. The vibratory motion also marches ash particles up a spiral groove in the circumferential wall of the bowl to facilitate ash removal from the fuel bed.

Abstract: Wood waste fuel is piled on a perforated grate within a combustion chamber. The fuel is burned by underfire air passing through the grate up through the pile. Ash forms at the bottom of the pile and is removed about a complete 360 degree perimeter where it falls into an ash pit and is subsequently removed from the burner. Fuel is fed to the burner through an elongated continuously expanding tube by a reciprocating ram feeder.

Abstract: An ignition burner and a pilot burner form part of an ignition system for a fluidized stream of finely-divided coal particles in a pressurized gasifier housing having a slag overflow pipe coupled to a discharge vessel. A fuel supply pipe delivers fuel for combustion by the ignition burner and the pilot burner. A sparkplug or hot wire is used to ignite the fuel delivered to the ignition burner. The flame produced by the ignition burner is widened by a baffle so that ignition by the pilot burner occurs to produce a flame which is monitored through a thermocouple. The parts forming the ignition system are carried by a pair of levers with pivots on the inner wall of a slag overflow pipe for movement between an operative position wherein the ignition burner is situated near the slag-receiving opening of the overflow pipe and an inoperative position wherein the ignition burner is protected from contact by slag and radiation heating.

Abstract: An apparatus for manufacturing a rapidly cooled solidified slag, which comprises: at least one rotating cooling drum rotating around a horizontal center axis thereof, said cooling drum being cooled by a cooling medium, and having an outer peripheral surface comprising a plurality of jogs over the entire surface thereof; a slag sump arranged at a position where said peripheral surface of said cooling drum begins to rise, the depositing molten slag onto said peripheral surface of said cooling drum; a scraper proved at the lower part of said peripheral surface of said cooling drum; and a slag feeding means arranged above said cooling drum, for pouring said molten slag into said slag sump; whereby said molten slag poured into said slag sump is deposited onto said peripheral surface of said cooling drum, rapidly cooled through heat exchange with said cooling medium along with rotation of said cooling drum to become a solidified slag, and peeled off from said peripheral surface of said cooling drum by said scraper.

Abstract: Apparatus for handling ash and slag produced in the combustion of coal or other ash-bearing fuel in a top-supported furnace (10) of a steam generator, including a submerged scraper conveyor unit (14) beneath the furnace (10), and a water seal (24, 26) including a bottom-supported trough (26) positioned beneath the furnace (10), and plates (24) secured to the furnace bottom extending down into the trough (26). The submerged scraper conveyor unit (14) is bottom-supported independently of the trough (26), and there is an adjustable (34) seal member (29) between the two to prevent gas leakage therebetween.

Abstract: A method and apparatus for cooling hot bulk material, such as glowing coke, clinker, or sinter material, include a vertically oriented cooling tank into which the hot bulk material is introduced and in which the material flows downwardly under gravity and is discharged from an outlet. At least two partial currents of cooling gas are fed into the cooling tank at respective feeding points therein, the feeding point being respectively arranged one over the other so that the cooling gas fed into the tank flows upwardly around the bulk material as the latter flows downwardly to cool the same with the cooling gas being correspondingly heated.

Abstract: A high temperature solids gasification generator which employs finely divided solids, e.g. powdered coal, has a down flow and discharges into a plenum chamber below the generator. The plenum chamber has a restricted outlet at the bottom so that a pool of liquid slag will form, and there is a lateral outlet above the slag pool for effluent gas. The lateral outlet has its throat located offset farther from the axis of the plenum chamber than the inside radius of the chamber.

Abstract: A wet deasher arrangement in which a trough is filled with quenched water and is arranged underneath an ash hopper of a boiler. The trough is provided with a quench water feed as well as an overflow and ash conveying equipment. The quench water is permanently circulated through a cooling unit with the aid of a pump, and the cooling unit is arranged between the overflow and the quench water feed. Oblique parallel plates are arranged within the trough before the overflow. The cooling unit has heat exchanger tubes divided into sections which are swept successively by quench water. They are accommodated in a pump upstream tank which precedes the pump. The upstream tank is obliquely arranged and converges to an outlet opening. The sections of the cooling unit may be arranged above each other within the pump upstream tank.

Abstract: A pressure container forms a shaft gasifier for receiving coarse coal in the form of a coal bed. A burner extends through the pressure container into a chamber therein and produces at least one primary gas jet directed against the coal bed, thereby gasifying the coal and generating a product gas and forming liquid slag. The liquid slag collects in a slag bath tank having an overflow weir over which the collected slag flows and falls freely toward a cooling water bath beneath the chamber. A water jet nozzle directs at least one water jet against the liquid slag as it falls freely between the weir and the cooling water bath. This atomizes the liquid slag, thereby cooling the slag and generating steam. At least a part of the steam is supplied as process steam to the coarse coal.

Abstract: A continuous gasification furnace and method of operation. The charge is fed into the furnace chamber between two rolls at least one of which is driven. The furnace chamber can be sealed from the ambient atmosphere. The bed of the furnace contains three zones from top to bottom, these zones are; a volatilization zone, a char reaction zone and an ash zone. Additionally, there can be a drying zone above the volatilization zone. Fuel, air, and steam enter the lower portion of the furnace through strategically located inlet ports. Fuel is used to start up the burning bed while carefully controlled steam to air ratio is used during continuous operation of the furnace. Simultaneously controlled steam cooling effects and exothermic reactions occur in the char reaction zone whereby all or controlled amounts of the oxygen is consumed so that pyrolysis can occur in the volatilization zone without the danger of combustion in that zone or combustion of the fumes leaving the bed.