Abstract: A method of operating a regenerative glass furnace for melting glass for the manufacture of shaped glass articles so as to minimize emission of NOx in waste gases leaving the furnace, the furnace having sealed regenerators which act as heat exchangers, the method including supplying fuel in excess of that required for stoichiometric combustion to ensure that glass of the required quality at the required production rate is obtained, and that the waste gases leaving the furnace through the regenerators contain combustible material, and reacting the combustible material with sufficient air to ensure that the waste gases exiting to atmosphere contain permissible levels of combustible material and contain permissible levels of NOx. Alternatively, the furnace may be operated at substantially stoichiometric conditions and fuel is supplied to waste gases as they leave the melting chamber. The invention also relates to a regenerator glass furnace for use in the method.

Abstract: A method of operating a cross-fired regenerative glass furnace for melting flat glass so as to minimize emission of NOx in waste gases leaving the furnace, the furnace having sealed regenerators which act as heat exchangers, the method including supplying fuel in excess of that required for stoichiometric combustion to ensure that glass of the required quality at the required production rate is obtained, and that the waste gases leaving the furnace through the regenerators contain combustible material, and reacting the combustible material with sufficient air to ensure that the waste gases exiting to atmosphere contain permissible levels of combustible material and permissible levels of NOx. Alternatively, the furnace may be operated at substantially stoichiometric conditions and fuel is supplied to the waste gases as they leave the melting chamber. The invention also relates to a cross-fired regenerator glass furnace for use in the method.

Abstract: A method of operating a cross-fired regenerative glass furnace for melting flat glass so as to minimize emission of NOx in waste gases leaving the furnace, the furnace having sealed regenerators which act as heat exchangers, the method including supplying fuel in excess of that required for stoichiometric combustion to ensure that glass of the required quality at the required production rate is obtained, and that the waste gases leaving the furnace through the regenerators contain combustible material, and reacting the combustible material with sufficient air to ensure that the waste gases exiting to atmosphere contain permissible levels of combustible material and permissible levels of NOx. Alternatively, the furnace may be operated at substantially stoichiometric conditions and fuel is supplied to the waste gases as they leave the melting chamber. The invention also relates to a cross-fired regenerator glass furnace for use in the method.

Abstract: A recycling system processes used oil filters on a continuous basis by shredding the oil filters and then incinerating the shreds in a rotary kiln. The shreds are fed into the upper end of an inclined rotating drum kiln. The shreds of combustible material and any oil are burnt to produce exhaust gases and ash particles. The remaining metal shreds are discharged at the lower end of the rotating drum through a first port. The exhaust gases and ash particles flow from the kiln through a first cyclone which separates out any heavy unburnable pieces. The remaining exhaust gases and ash particles then pass through an afterburner to further ensure complete combustion and minimize air pollution. A second cyclone separates the ash particles from the exhaust gases. An exhauster can be used to induce the flow of exhaust gases and ash particles from the kiln through the afterburner and cyclones. This system automatically separates metal shreds and incinerates the combustible materials and oil in the oil filters.

Abstract: A system of this invention reduces the emission of NO.sub.x and fuel pollutants from a furnace. The system includes a furnace with a chamber for combusting air, oxygen and fuel flows in an approximately stoichiometric proportion. A reburn unit, that can be a port, is coupled to communicate with and receive the combustion exhaust from the chamber. The reburn unit is also coupled to receive a second fuel flow that is added to the exhaust flow at a stoichiometric ratio and temperature at which a reaction occurs to lower the amount of NO.sub.x in the exhaust flow. The reburn unit is coupled to a burnout unit that can be a regenerator or a recuperator, that is coupled to receive an oxidant flow with air and/or oxygen. The oxidant flow combusts fuel in the exhaust flow to prevent emission of this fuel into the atmosphere.

Abstract: A method of operating a regenerative glass furnace for melting glass for the manufacture of shaped glass articles so as to minimize emission of NOx in waste gases leaving the furnace, the furnace having sealed regenerators which act as heat exchangers, the method includes supplying fuel in excess of that required for stoichiometric combustion to ensure that glass of the required quality at the required production rate is obtained, and that the waste gases leaving the furnace through the regenerators contain combustible material, and reacting the combustible material with sufficient air to ensure that the waste gases exiting to atmosphere contain permissible levels of combustible material and contain permissible levels of NOx. Alternatively, the furnace may be operated at substantially stoichiometric conditions and fuel is supplied to waste gases as they leave the melting chamber. The invention also relates to a regenerator glass furnace for use in the method.

Abstract: A regenerative thermal oxidizer unit comprising two heat regenerator units in which a gas to be purified from VOCs passes through the units in an essentially horizontal direction.

Abstract: A method and apparatus for minimizing disturbances caused by depositions on a feeding apparatus for a combustion or gasification plant. Secondary air is fed via perforated tubes 13 which by affecting the emission levels of the process with longer or shorter time intervals are inserted and withdrawn from the chamber, while being cleaned from slag, dust and other deposits outside the chamber by wire brushes 21. The combustion process may continue by using the remaining tubes while one or more are being cleaned.

Abstract: A mobile incinerator suitable for burning explosive material, has armored walls capable of withstanding internal explosions, a primary combustion chamber within which initial burning of the material to be incinerated takes place, a secondary combustion chamber to burn exhaust from the primary combustion chamber a second time to reduce pollution and safety hazards, and a trailer for providing transportation. The armored walls may include steel plates reinforced by steel channel beams. The mobile incinerator includes: vents for allowing air and exhaust to pass into; between and out of the combustion chambers, assisted by a draft induction fan, with flammable fluid delivered to and ignited within the combustion chambers; pressure release hatches; a loading cart mounted on telescoping rails by which material to be incinerated can be inserted through an opening; refractory material lining the primary combustion chamber; an exterior shell of aluminum sheeting; and a control system powered by a generator.

Abstract: A Stirling engine has an external combustion chamber for burning a kerosene and transferring a high temperature therein to working fluid in heater tubes. In the case of the present invention, the external combustion chamber is connected to a furnace for burning industrial waste materials such as plastic materials or rubber materials so that the high temperature above 900.degree. C. is able to be supplied to the combustion chamber. This serves in raising an output power of the Stirling engine. A conduit for connecting the furnace with the combustion chamber is proveded with a dumper capable of interrupting a flow of the high temperature combustion gases toward the combustion chamber of the Stirling engine.

Abstract: A biomass-fueled furnace for residential or institutional space and hot water heating. Wood chips, the preferred fuel, are purchased "green and/or wet" and are stored in a dryer/storage assembly which uses waste clean exhaust gases produced by the furnace to dry them. Wood chips are fed via gravity to the primary combustion chamber where, via pyrolysis, they are burned. A thimble combustor eliminates radiant heat loss from the primary pyrolysis zone, allowing stable pyrolysis at low burning rates. A second combustion chamber fed with pre-heated air completely oxidizes pyrolysis gases. This furnace is capable of operating continuously at extremely low fuel consumption rates so that heat release can be regulated by thermostat in the same manner as conventional gas and oil fired furnaces. A combination of fuel drying plus secondary air preheating by the secondary flame allows stable operation at extremely low or "idle" fuel rates.

Abstract: An incinerator comprises a feeding plate, a first combustion chamber, a second combustion chamber, a curved duct, an air exhausting device, a water screen device, and a water tank. The feeding plate is provided on the underside thereof with a vibrating device for causing the feeding plate to vibrate so as to move trash gradually into the first combustion chamber in which trash is incinerated to produce ash and exhaust fume which is then burned completely in the second combustion chamber. When the exhaust fume is passed through the water screen located in the curved duct, ash contained in the exhaust fume is washed away and deposited in the water tank which is provided therein with a device for removing ash that is deposited in the water tank.

Abstract: The invention relates to an afterburner for various incinerators, said afterburner (3) including a housing portion provided with a smoke delivering pipe (2) for carrying the smokes coming from an incinerator firing chamber (1) into the afterburner chamber. The chamber (3) is provided with a burner (7), for example an oil burner or a gas burner. The chamber (3) is further fitted with a smoke dispensing box (9), whereby the particles not yet incinerated are recycled back into the fling chamber (1) and the flue gases are delivered into a flue gas scrubber (12). Between the afterburner (3) and the smoke dispensing box (9) is a wall (16) including a perforated section.

Abstract: An apparatus for purifying pollutant-containing waste or exhaust air from industrial plants by means of regenerative afterburning includes a heat exchanger in the form of a heat exchanger fill. The material for the heat exchanger fill is a sponge-like foamed ceramic material having open pores. In accordance with another embodiment, the material of the heat exchanger fill may be constituted by ceramic grate plates or grate bodies.

Abstract: An incinerator in which halogenated organic compounds are burned in the presence of oxygen or oxygen enriched air to produce combustion products. The combustion products potentially include unreacted oxygen and halogenated organic compounds which can react with oxygen to produce halogenated furans and dioxins. The formation of the halogenated furans and dioxins is minimized by firing a burner, burning a hydrogen containing fuel at a fuel-rich stoichiometry, into the combustion products so that the fuel will react with the unreacted oxygen. This will reduce formation of the halogenated furans and dioxins. Any of the halogenated furans and dioxins that are formed are substantially eliminated by the reaction of hydrogen supplied by the fuel with the halogenated furans and dioxins.

Abstract: A system for the abatement of industrial process emissions comprises a catalytic oxidizer and a selective catalytic reduction bank integrated into a single housing. The system utilizes at least two regenerative chambers in a controlled abatement process. The integrated system removes volatile organic compounds (VOCs), carbon monoxide (CO), and toxic oxides of nitrogen (NO.sub.x) from the process emissions. The singular housing of the present invention is efficient and eliminates the need for more than one supplementary heat source, while eliminating major pollutants from the emissions.

Abstract: A method of operating a regenerative glass furnace for melting glass for the manufacture of shaped glass articles so as to minimize emission of NOx in waste gases leaving the furnace, the furnace having sealed regenerators which act as heat exchangers, the method comprising supplying fuel in excess of that required for stoichiometric combustion to ensure that glass of the required quality at the required production rate is obtained, and that the waste gases leaving the furnace through the regenerators contain combustible material, and reacting the combustible material with sufficient air to ensure that the waste gases exiting to atmosphere contain permissible levels of combustible material and contain permissible levels of NOx. Alternatively, the furnace may be operated at substantially stoichiometric conditions and fuel is supplied to waste gases as they leave the melting chamber. The invention also relates to a regenerator glass furnace for use in the method.

Abstract: A system for removing airborne contaminants from the effluent air streams om spray paint booths and the like. The system includes a rectangular shaped underground pool having pool of water positioned below the work area. The underground pool has a plurality of suction pipes which are uniformly distributed throughout the pool at a distance of between one and two inches above the pool of water. The suction pipes terminate in a plenum located adjacent the underground pool. A gas turbine engine which is connected to the plenum is used to draw air including airborne contaminants into the plenum from the work area. Solid airborne contaminants such as droplets of water soluble paint, sand and the like will fall into the pool of water. Lighter airborne contaminants, such as gaseous toxins are drawn through the gas turbine type engine into a after-burning incinerator.

Abstract: A method of operating a cross-fired regenerative glass furnace for melting flat glass so as to minimize emission of NOx in waste gases leaving the furnace, the furnace having sealed regenerators which act as heat exchangers, the method comprising supplying fuel in excess of that required for stoichiometric combustion to ensure that glass of the required quality at the required production rate is obtained, and that the waste gases leaving the furnace through the regenerators contain combustible material, and reacting the combustible material with sufficient air to ensure that the waste gases exiting to atmosphere contain permissible levels of combustible material and permissible levels of NOx. Alternatively, the furnace may be operated at substantially stoichiometric conditions and fuel is supplied to the waste gases as they leave the melting chamber. The invention also relates to a cross-fired regenerator glass furnace for use in the method.

Abstract: A single rotary valve is designed to control feed, purge and exit flow in a multiple bed regenerative fume incinerator system thereby replacing the large number of valves heretofore used to operate such a system. The housing of the rotary valve has ports for connection to at least one feed conduit, to at least one exit conduit, to at least 3 regenerator bed conduits and includes an annular opening on the valve axis for a purge gas conduit. The purge gas conduit extends through the annular opening and connects to an interior cavity of the valve rotor which has a peripheral opening registrable individually with the regenerator bed ports. The valve rotor divides the interior chamber of the valve housing into a feed subchamber and an exit subchamber and includes a sealing plenum preventing leakage from the feed subchamber to the exit subchamber.

Abstract: An apparatus for purifying a pollutant-containing outgoing air from the industrial installations has a heat exchanging bed, which has a predetermined thickness, consist of a suitable, preferably mineral, material, and is located in the interior of a shaft-like reactor housing. During the purifying operation, the pollutant-containing air flows through the heat exchanging bed into a combustion chamber, and heated purified air flows from the combustion chamber through the heat exchanging bed in opposite direction, giving up its heat to the heat exchanging bed and thereby being cooled down. The pollutants contained in the pollutant-containing air are burned in the heat exchanging bed and, if needed, in the combustion chamber.

Abstract: A method and an incinerator in which halogenated organic compounds are burned in the presence of oxygen or oxygen enriched air to produce combustion products. The combustion products potentially include unreacted oxygen and halogenated organic compounds which can react with oxygen to produce halogenated furans and dioxins. The formation of the halogenated furans and dioxins is minimized by firing a burner, burning a hydrogen containing fuel at a fuel-rich stoichiometry, into the combustion products so that the fuel will react with the unreacted oxygen. This will reduce formation of the halogenated furans and dioxins. Any of the halogenated furans and dioxins that are formed are substantially eliminated by the reaction of hydrogen supplied by the fuel with the halogenated furans and dioxins.

Abstract: A valve flushing system supplies a cleaning gas to a relatively large plenum, which in turn communicates with a restricted passage directing the flow along a face of the valve disk. In a main feature of this invention, a flushing gas flow moves through a restricted path along a face of a valve disk away from a valve disk contact area with a valve seat. In this way, the flushing gas prevents a potential leakage gas flow from approaching the valve/valve seat interface. In this way, leakage is reduced. Although the efficiency of the system may be reduced by a small amount, the resulting prevention of leakage more than justifies this potential small decrease in efficiency. The use of the relatively large plenum ensures that there will be complete and adequate coverage of the valve disk preventing any leakage across the valve disk. In an important feature of this invention, supply passages extend into the plenum along a direction which does not include a component moving in the direction of the valve disk.

Abstract: A waste heat recovery method can provide heat recovery from exhaust gases, full firing of exhaust gases, and auxiliary burning, either simultaneously or independently. Such method is carried out by installing a tube-nested (or heat-absorbing water tube furnace-inserted type) combustion chamber in a boiler of a cogeneration system or combined cycle system or the like which generates both heat and power. The boiler is provided with a combined full firing burner and auxiliary burner confronted by the exhaust gas entrance. This structure allows for elimination of a separate auxiliary chamber and thus has made it possible to provide a waste heat boiler of a simplified structure which is smaller in size and thus occupies less space, at a reduced price and with a greatly expanded heat-to-electricity ratio. Accordingly, the boiler of the invention has a greatly extended range of applications.

Abstract: An apparatus and process using a pulse combustor to atomize a liquid or slurry is provided. The apparatus includes a pulse combustor for generating a stream of atomization fluid and an oscillating flow field and introduction apparatus for introducing to the influence of the oscillating stream of atomization fluid a liquid or slurry to be atomized. Furthermore, an improved pulse combustion atomizer employing a T-shaped burner is provided.

Abstract: An improved process and apparatus for the gas phase reaction of a feed gas mixture in a regenerative incinerator comprising a combustion zone in fluid communication with at least three separately-housed chambers. Each chamber contains a layer of solid heat exchange material, and is in selective fluid communication with an inlet manifold and an exhaust manifold such that each chamber is selectively operable in an intake mode and an exhaust mode. A layer of catalyst is disposed in each chamber such that catalytic reaction of the feed gas mixture occurs and the operating temperature of the combustion zone may be reduced.

Abstract: An improved apparatus and process for removal of particulates entrained in a gas stream are provided. The removal process employs a pulse combustor to provide an acoustic pressure wave to acoustically enhance agglomeration of particulates which may be collected and removed using a conventional separation apparatus. The apparatus may be employed as a direct fired system for improved operation of gas-operated equipment such as a gas turbine, or may, alternatively, be employed as an add-on subsystem for combustion exhaust clean-up. Additionally, added particulates may include a sorbent for effecting sorption of other contaminants such as sulfur. Various other particulates for contaminant removal may also be introduced into the system as exemplified by alkali-gettering agents.

Abstract: A livestock incinerator is provided, and includes a compartment or incineration chamber defined by opposite sidewalls, opposite end walls, a bottom wall, and an open top which is selectively closed by a plurality of lids pivotally connected to the walls of the incinerator. The interior of the incinerator is lined with firebricks, including all the walls and the lids. The firebricks are secured in place by a plurality of T-shaped brackets which define channels for receiving the edges of the firebricks. A primary burner is operatively connected to the incinerator for heating the chamber such that the carcasses burn to ashes. An exhaust stack is connected to one of the lids, and includes an afterburner for further combusting the products of combustion from the chamber so as to prevent atmospheric pollution. The primary burner and afterburner are operatively connected in series so that if one burner fails to operate, the other burner will automatically cease operation.

Abstract: A furnace for burning rubber tires. The furnace has a unique divided and apertured fire box to delay burning so that more complete combustion is complete. Forced air, and afterburner and a converter section also combine to provide for near smokeless discharge from the exhaust of the furnace.

Abstract: An incinerator for combustible or thermally-decomposable gases includes a device which insures that gas continues to flow through the incinerator in the event of failure of the scrubber fan connected to the outlet of the incinerator. When the scrubber fan fails, a solenoid-operated valve opens, and compressed gas from a tank flows through the valve into the main conduit of the incinerator. The compressed gas enters the main conduit through an air flow amplifier installed within the main conduit. The air flow amplifier magnifies the effect of the compressed gas, and creates a region of negative pressure which assures that toxic or hazardous gases do not remain in the incinerator, but instead continue to flow toward the scrubber fan, even after the fan has failed.

Abstract: A method and apparatus for gasifying tires comprises a housing divided into a tire hopper and vaporization chamber into which air and combustible fluid are inserted through intake manifolds to initially combust and thereafter oxidize tires placed in the housing. Oxidation results in volatile gases and solid residue. The latter is removed through a hatch in the vaporization chamber and the former is shunted to a mixing chamber which comprises an outer compartment, a middle compartment, and an inner compartment. The middle compartment receives the volatile gases which are then mixed with air in the outer and inner compartments. The mixture is combusted with the aid of a combustible fluid mixed in and thereafter shunted to a combustion chamber which further mixes the combustible fluid by means of baffles to thoroughly combust the mixture.

Abstract: A method and a unit for the thermal destruction of industrial fluid wastes in which first and second heating phases are performed by mixing the combustion gases with the fluid wastes into combustion chambers, maintaining the mixture under high turbulence conditions to bring it to a thermodestruction temperature at which the mixed fluid waste is destroyed by heat; the gaseous mixture is maintained in adiabatic conditions at the thermodestroying temperature for a predetermined period of time along a path extending along most of a primary combustion chamber of the destroyer unit. The thermodestroyer unit has a monolithic structure which develops vertically, comprising a primary combustion chamber and an annular stay chamber, which surrounds the primary combustion chamber in which the burning mixture is maintained in a substantially adiabatic condition; the apparatus may be provided with a heat exchanger arranged at the outlet of the stay chamber.

Abstract: An incinerating furnace, such as a cremation furnace or other batchwise chargeable furnace, is arranged with a main combustion chamber (1), from which the fumes are adapted to be led away through a following chamber arrangement (6-17) connected with a flue.

Abstract: A waste disposal system (10) which provides for the destruction of solid and liquid waste materials, through a controlled and monitored flow, from the loading of the material to be processed to the expulsion of clean nontoxic and sterile air and inert solid residue. The system includes; a waste loading module (30), a shredding module (33), an injection module (34), a first combustion chamber (40), a second combustion chamber (50), a first cooling module (60), an electrostatic module (701), a reducing catalyst module (70), an oxidizing catalyst module (80), a liquid filtering module (90), a neutralization module (100) and a second cooling module (101).

Abstract: A volatile organic compound (VOC) abatement system is provided which incorporates a carbon or zeolite type concentrating adsorption device, with VOCs collected upon the adsorption surfaces. A heat source is required heat gases flowing to the adsorption device in order to remove the concentrated VOCs. Also, heat is required to oxidize the VOCs into a safe form prior to their release into the atmosphere. The present invention employs a regenerative thermal oxidizer for efficiently combusting the VOCs prior their release into the atmosphere. The present system also employs a bypass valve for introducing a portion of the VOCs directly into a combustion chamber without regenerative preheating. The resulting lowering of thermal efficiency of the regenerative thermal oxidizer allows the exhaust from the regenerative thermal oxidizer to carry more thermal energy. The thermal energy from the exhaust is then transferred to a heat exchanger to heat gasses flowing into the adsorption device.

Abstract: A catalytic incinerator system for oxidation/combustion of volatile organic compounds (VOCs). The system is relatively compact, is designed to accommodate the thermal stresses within the system without adversely affecting the system components, and to provide substantially uniform temperature distribution in the VOCs and combustion air. The system includes a dual shell housing having an inner shell and an outer shell, wherein the inner shell is capable of thermal expansion and movement relative to the outer shell. Also included is a multi-pass tube-type heat exchanger suspended or otherwise mounted within a heat exchange chamber. The heat exchanger is mounted within the heat exchange chamber so that one end is unfixed and thus the heat exchanger can freely expand and contract due to temperature fluctuations within the heat exchange chamber.

Abstract: An incinerator system is built up of an air-permeable base (2), an outer wall (3) extending uprightly therefrom and a front or first furnace (4) and a rear or second furnace (5) set up thereon. The first and second furnaces are each in a vertically extending, cylindrical form and are connected with each other through first, second, third and fourth fume guide pipes (6) to (9), arranged from below, thereby assuring that refuse or trash can be incinerated and maintaining the outer wall at a temperature safe enough to allow access to it.

Abstract: A system for the controlled safe shutdown of a hazardous waste incinerator upon loss of power. The system includes a primary combustion chamber and a secondary combustion chamber, a gas treatment system, and two standby power sources. One standby power source is available immediately for elements that cannot be shut down even for a second. The other standby power source is a heavy duty generator that takes a short time to get up to speed but is used to power elements that can be allowed to coast for a short time without causing damage to the equipment or the environment. The system includes an uninterruptable power source connected to continue supplying heat and air to the secondary combustion chamber and prevent opening an emergency vent stack cap and thereby prevent the unwanted discharge of gas from the system.

Abstract: A single unit, shell and tube fume incinerator utilizes a vacuum baffle (34) structure proximate a combustion zone (24) to control the flow of combustion exhaust gas. The vacuum baffle (34) is located slightly above the hot ends of a plurality of heat exchange tubes (20) to deflect the hot exhaust gases from the combustion zone (24) away from the ends of the tubes (20), and back to the outside of the tubes (20), thereby controlling the "time at temperature" for contaminants in the impure gas feed. A vacuum effect is created just below the baffle (34) to draw cleansed exhaust below the baffle (34) back up into the combustion zone (24) to prevent the escape of impure gas.

Abstract: A process for disposing of a waste chemical stream containing materials which can produce objectionable combustion products, such as NO.sub.x, free bromine, carbon, particulates or ash, the process comprising the steps of passing the waste chemical stream to an oxidizing first zone where burning occurs in stoichiometric oxygen excess above about 2000.degree. F.; then to a reducing second zone where reaction occurs in stoichiometric reduction at a temperature of above about 2000.degree. F.; and then to an oxidizing third zone to oxidize the combustibles at temperatures of between about 1400.degree. F. and 2000.degree. F. The process provides high efficiency destruction of waste compounds, whether solid, liquid or gaseous, in a substantially NO.sub.x free manner. In the case of brominated compounds, the process generates HBr which is readily scrubbed.

Abstract: An automatic firebox provided with a fuel hopper that delivers fuel through a pivoting funnel to a grate burning area. The grate burning area is provided with at least one pivoting fuel grate which operates automatically in sequence with the fuel feed and hopper so as to provide automatic stoking. An automatic control operated by temperature and/or time is disclosed.

Abstract: A method and a unit for the thermal destruction of industrial fluid wastes in which first and second heating phases are performed by mixing the combustion gases with the fluid wastes into combustion chambers, maintaining the mixture under high turbulence conditions to bring it to a thermodestruction temperature at which the mixed fluid waste is destroyed by heat; the gaseous mixture is maintained in adiabatic conditions at the thermodestroying temperature for a predetermined period of time along a path extending along most of a primary combustion chamber of the destroyer unit. The thermodestroyer unit has a monolithic structure which develops vertically, comprising a primary combustion chamber and an annular stay chamber, which surrounds the primary combustion chamber in which the burning mixture is maintained in a substantially adiabatic condition; the apparatus may be provided with a heat exchanger arranged at the outlet of the stay chamber.

Abstract: A power plant with efficient emission control and high turbine inlet temperatures is disclosed. The power plant includes a combustor for the combustion of carbonaceous sulfur-bearing fuel. The combustion of this fuel produces a hot gas with SO.sub.x and NO.sub.x contaminants. This gas is conveyed to a refractory heat exchanger where some of the heat from the gas is transferred to a pressurized air stream. The gas is then conveyed to a fluidized bed reactor. The fluidized bed reactor includes a central chamber with a fluidized bed positioned at the base of the chamber. Heat exchangers are positioned within the fluidized bed. These heat exchangers preheat the pressurized air stream which is then conveyed to the refractory heat exchanger and later conveyed to a turbine assembly. The fluidized bed reactor also includes circulating particulate matter, such as CaO. Ammonia may also be injected into the fluidized bed reactor. When operating at a temperature of at least 1,500.degree. F.

Abstract: A smokestack addition to a conventional outdoor type of domestic grill is shown that provides a suction at the outlet from the cooking zone of the grill to pull the products of combustion arising from the operation of the grill which suction of the gasses is effective to minimize the circulation of carcinogens in such gasses from flowing over the food being cooked and directs the these effluent gasses over an afterburner associated with the stack that functions to initiate the oxidation of substantially all of the pollutants that flow away from the cooking zone and through the stack to be to be discharged into the atmosphere.

Abstract: A process and system for low NO.sub.x cogeneration to produce electricity and useful heat. Fuel and oxygen are provided to an internal combustion engine connected to drive an electric generator, to thereby generate electricity. An exhaust stream is recovered from the engine at a temperature of about 500.degree. to 1000.degree. F. which includes from about 6 to 15 percent oxygen. Fuel is added to the exhaust stream to create a fuel-rich mixture, the quantity of fuel being sufficient to react with oxygen and reduce the NO.sub.x in said exhaust stream. The fuel-enriched stream is provided to an afterburner, and the fuel, NO.sub.x and available oxygen are reacted to provide a heated oxygen-depleted stream. The oxygen-depleted stream is cooled in a first heat exchanger. Conversion oxygen is admixed with the cooled stream which is then passed over a catalyst bed under overall reducing conditions. NO is converted to NO.sub.2 at the forward end of the bed, and the NO.sub.

Abstract: An incinerator having a first combustion chamber capable of receiving material to be incinerated, a second combustion chamber capable of receiving the flue gas, and a particulate extraction and containment system connecting the two is provided. Also provided is a method for incineration which involves combusting a material using a substoichiometric amount of oxygen so as to produce a flue gas, collecting the flue gas, cooling the flue gas, and combusting the flue gas using at least a stoichiometric amount of oxygen. The incinerator and method allow for the removal of toxins and toxin precursors prior to exposure to stoichiometric or greater levels of oxygen and to temperatures greater than 1000.degree. F. Moreover, the incinerator and method provide for the recycling of materials and a reduction of waste volume to a level below that which is currently obtainable.

Abstract: A refuse-burning apparatus having a main combustion-housing with an interior in which refuse is placed and burned, which main combustion-housing has a plurality of substantially-upright walls, a top wall, and a lower meshed screen. One side wall has an entrance through which refuse may enter into the interior of the housing, which entrance is selectively opened and closed. A loader for loading refuse into the interior of the housing is operatively associated with the entrance, so that refuse may be inserted into the interior when the entrance is opened up. A ventilator supplies air to the interior. An after-burner is mounted to the top wall of the main housing for achieving secondary burning of the refuse, which after-burner has a main frame, at least one burner mounted to the main frame, and exhaust for directing the products of combustion from the main frame to the ambient surroundings. In the preferred embodiment, the bottom meshed screen is periodically vibrated to loosen any ash lodged therein.

Abstract: An apparatus and process using a pulse combustor to atomize a liquid or slurry is provided. The apparatus includes a pulse combustor for generating a stream of atomization fluid and an oscillating flow field and introduction apparatus for introducing to the influence of the oscillating stream of atomization fluid a liquid or slurry to be atomized.

Abstract: A waste disposal system (10) which provides for the destruction of solid and liquid waste materials, through a controlled and monitored flow, from the loading of the material to be processed to the expulsion of clean nontoxic and sterile air and inert solid residue. The system includes; a waste loading module (30), a shredding module (33), an injection module (34), a first combustion chamber (40), a second combustion chamber (50), a first cooling module (60), an electrostatic module (701), a reducing catalyst module (70), an oxidizing catalyst module (80), a liquid filtering module (90), a neutralization module (100) and a second cooling module (101).

Abstract: An improved apparatus and process for removal of particulates entrained in a gas stream are provided. The removal process employs a pulse combustor to provide an acoustic pressure wave to acoustically enhance bimodal agglomeration of particulates which may be collected and removed using a conventional separation apparatus. A particulate having a size different from the size of the particulate in the gas stream to be cleaned is introduced into the system to effectuate the bimodal process. The apparatus may be employed as a direct fired system for improved operation of gas-operated equipment such as a gas turbine, or may, alternatively, be employed as an add-on subsystem for combustion exhaust clean-up. Additionally, the added particulate may be a sorbent for effecting sorption of other contaminants such as sulfur. Various other particulates for contaminant removal may also be introduced into the system as exemplified by alkali-gettering agents.