Abstract: The invention relates to a method and an arrangement for torrefaction of a biomass. Said method and arrangements allows for precise control of torrefaction temperature, which is crucial for accurate control of the quality and properties of the torrefied material.

Abstract: A controlled kiln and manufacturing system for biochar production includes control systems and subsystems. An example controlled kiln (100) includes a drum (200), a lid (120) and a floor (250) together forming a combustion chamber configured to contain feedstock for conversion into biochar. A catalytic converter (700) may be operatively coupled with an outlet of the kiln (100). A monitor and control subsystem may be operative to issue notifications or automatically end biochar conversion. A ventilation and exhaust system including independently controllable air inlet ports (240), a chimney (300) and smoke inlet pipes (330) enables regulation of smoke flow from a combustion chamber of the kiln while a heat exchanger (1000) enables providing exhaust heat to one or more secondary applications.

Abstract: [Problem] To provide a waste gasification and melting furnace that promotes the drying and pyrolytic decomposition of waste in the shaft section, making it possible to limit the conveyance of moisture and volatile components to the bottom of the blast furnace and to reduce the consumption of extra coke.

Abstract: Pyrolytic gas generator for generating clean useful gas from biomass, particularly wood, oil seeds or the like, where a gasification channel in multi-chambered construction is provided, which gasification channel is provided with an assist burner which can supply heat from the outside to the gasification channel during gasification of the biomass, a pre-pyrolyzing pipe is connected upstream of the gasification channel and an ash discharge downstream of the gasification channel, wherein the generated gases are re-gasified in the gasification channel while the material to be gasified is mechanically transported from a material container to the ash discharge.

Abstract: The present invention provides a system and a process for preparing activated carbon from fly ash. The system of the present invention comprises a flotation system and a carbonization system. The present invention has the following advantages. Firstly, since a fuel gas-flue gas loop structure is arranged, the combustible fuel gas produced in carbonization process enters the combustion means for combustion via this loop structure, and also via this loop structure, the high temperature flue gas generated by the combustion enters the carbonization furnace to heat up and carbonize the charcoal powder raw material within the carbonization furnace. Such a solution not only saves energy, but also prevents a substantial amount of combustible gas from being emitted to the atmosphere, thereby reducing environmental pollution. Secondly, since two cylinders are arranged in the carbonization furnace, the charcoal powder raw material in the inner cylinder enters the outer cylinder and then exits from the outer cylinder.

Abstract: Vascular treatment and methods include a plurality of self-expanding bulbs and a hypotube including interspersed patterns of longitudinally spaced rows of kerfs. Joints between woven structures and hypotubes include solder. Woven structures include patterns of radiopaque filaments measurable under x-ray. Structures are heat treated to include at least shapes at different temperatures. A catheter includes a hypotube including interspersed patterns of longitudinally spaced rows of kerfs. Heat treating systems include a detachable flange. Laser cutting systems include a fluid flow system.

Abstract: A method and system for the conversion of waste into energy in a sealed system where combustion does not take place and the operating pressure prior to the inlet of the steam or power generating equipment is maintained below atmospheric pressure. Destruction of the RDF (refuse derived fuel) is accomplished by subjecting the RDF to a high temperature environment under controlled conditions in a purpose designed and built reactor. The high temperature environment, <5000° C., is achieved through the use of one or more non-transferred plasma torches for generation of plasma gas. The plasma gas exiting the torch and provides the thermal energy for the continual gasification of metallurgic coke configured as a carbon bed in the lower part of the reactor, which acts as a thermal catalyst and this provides the thermal energy for the gasification process.

Abstract: A method and system of processing animal waste is disclosed. In a particular embodiment, the method includes transferring animal waste to a gasifier to burn the animal waste, circulating water through a heat exchanger in a flue stack of the gasifier to generate heated water, and pumping the heated water to either an organic Rankine cycle system to generate electricity, a radiant heater, or any combination thereof. In addition, the method includes circulating the heated water through an evaporator of the organic Rankine cycle system to vaporize a refrigerant, and circulating the vaporized refrigerant from the evaporator, through a turbine to generate the electricity. Also, the method includes using a manure spreader to feed the animal waste to the gasifier at a varying feed rate that is based on contemporaneously calculating a British thermal units (BTU) of the animal waste being fed to the gasifier.

Abstract: A biomass gasification system for efficiently extracting heat energy from biomass material. The biomass gasification system includes a primary combustion chamber, a rotating grate within the primary combustion chamber for supporting the biomass during gasification, a feeder unit in communication with the primary combustion chamber for delivering biomass, a secondary combustion chamber fluidly connected to the primary combustion chamber, an oxygen mixer positioned between the primary combustion chamber and the secondary combustion chamber, a heat exchanger and an exhaust stack.

Abstract: A method and apparatus for incinerating different types of combustible waste in a cement manufacturing process. Two combustion chambers for incinerating waste are arranged in series, with first combustion chamber being a down draft chamber in which there is a downward flow of combustion gas and waste fuel to a waste and gas outlet. The second chamber is adaptable to support waste on a supporting surface incorporated in the compartment, wherein the waste is transported through the compartment from a waste inlet to a waste outlet along a circular path.

Abstract: A waste treatment technique includes: blowing a fluidizing gas from around a mixture discharge port to form a first fluidization region having a degree of fluidization of the fluidizable particles which is set to an extent allowing waste to be accumulated on fluidizable particles, while blowing a fluidizing gas between the first fluidization region and an opposite-side wall at a higher flow velocity to form a second fluid region having a degree of fluidization of fluidizable particles greater than that in the first fluidization region, whereby the fluidizable particles are mixed with the waste to gasify the waste; and supplying waste from a supply-side sidewall portion onto the fluidized bed to cause the waste to be accumulated on the first fluidization region while causing the accumulated waste to be moved into the second fluidization region step-by-step.

Abstract: The invention has its object to arbitrarily adjust an amount of particles to be circulated without changing a flow rate of a gasification agent to thereby enhance gasification efficiency in a fluidized bed gasification furnace. The fluidized bed gasification furnace 107 comprises first and second chambers 113 and 114 in communication with each other in a fluidized bed 105. The hot particles 102 separated in the separator 104 and raw material M are introduced into the first chamber 113. The particles 102 introduced from the first chamber 113 through interior in the fluidized bed 105 to the second chamber 114 are supplied in an overflow manner to the fluidized bed combustion furnace 100.

Abstract: A relatively level fuel grate surface angle cooperates with multiple feed screws that press solid fuel material into and across the grate surface to continually clear off the grate. Air spaces between each pair of adjacent grate elements for under fire air each have a ninety degree deflector flange at the top of the air space extending from one grate element across the air space and up and over an adjacent grate element to deflect under fire airflow across the adjacent grate element to act as a grate sweeper. The smooth curved surface of the deflector flange between grate elements facilitates movement of the fuel and ash material and prevents from one grate element to the next and prevents clogging of the airflow space.

Abstract: The present invention provides a process for burning coal instead of oil comprising the stages of coal gasification, gas combustion and optionally gas purification, utilization of residual heat of flue gas and flue gas discharge. The present invention further provides an apparatus for burning coal instead of oil. By present invention, the fuel cost for an oil-burning apparatus can be reduced by about four-fifths, so the resources of oil and natural gas can be saved either. Furthermore, the present invention has the advantages such as good reliability, high heat efficiency, high level of automation, high return on investment and good environmental benefits.

Abstract: The present invention provides a burner which uses solid fuels, especially waste plastic fuels. Burner size is minimized by having multiple combustion chambers concentrically located around a rotating screw conveyor. Heat efficiency is improved by having air passages disposed around the combustion chambers, thus preheating air for the combustion prior to its delivery to the combustion chambers, while simultaneously thermally insulating the combustion chambers against the environment. Waste plastic is transported from a fuel hopper to the combustion chambers by a rotating screw conveyor having the spiraling auger blades. Speed of screw conveyor rotation controls the consumption of waste plastic and, thus, the amount of thermal energy generated in the burner.

Abstract: Process for solid waste treatment, and particularly municipal solid waste, with recovery of the thermal energy, which is based on the general pyrolysis process modified in order to improve, on the one hand, the energy yield and, on the other, to reduce the quantity of unusable solid residues to be sent to the waste disposal, the unusable solid waste being limited to 10-15% of the total weight of the initial residue. The process and relative plant include a boosted treatment of the incoming waste, with a preliminary separation into three solid fractions, the first one of which is separately subjected to a preliminary drying step and the third one undergoes further shredding. The process and relative plant also include a section for recovering energy from the pyrolysis coke, wherein the latter is subjected to a thermochemical treatment with the production of a further quantity of synthesis gas.

Abstract: A partition divides an enclosure into an upper space and a lower space, the partition having a hole which provides essentially the only passage for gas to flow from the lower space to the upper space. A reactor tube having open ends is supported by the partition over the hole, and a grate spaced below the hole. A primary air inlet arrangement feeds air into the lower space for gasification of solid fuel on the grate, and a secondary air inlet directs a jet of air toward the inlet end of combustion tube communicating with the upper space and having an open exhaust end outside the enclosure. Product gas formed by gasification of solid fuel on the grate and passing through the reactor tube into the upper space will be drawn into the combustion tube to create a sub-atmospheric pressure in the upper space.

Abstract: A combustor apparatus and method for the combustion of viscous fuels are provided. The combustor apparatus can include a precombustion chamber particularly adapted to heat and at least partially combust a heavy primary fuel, and a main combustion chamber adapted to combust the primary fuel uniformly through the main combustion chamber (in flameless mode). The precombustion chamber can include at least one air injection inlet port positioned to induce a first stage vortex in the main body portion of the housing of the precombustion chamber. Further, the precombustion chamber can be interfaced with a main combustion chamber to induce a second stage vortex within the main combustion chamber. The main combustion chamber can have an extended axial length in order to accommodate heavier fuels that require additional time to sufficiently combust (oxidize) within the combustion chamber.

Abstract: Apparatus for batch processing source material into charcoal in a battery of kilns, each of which use forced convection of process gases through the source material to shorten the process cycle time, and all of which use an external combustor to burn the process waste gases from each kiln to provide the primary source of applied energy for the process.

Abstract: A pyrolysis device has a pyrolyzer (retort) and a thermal oxidizer, each with its own burner, but coupled so that the burner of the pyrolyzer can be down-regulated as heat from the thermal oxidizer is used to hear the pyrolyzer. One or more automatic controllers preferably adjust a burn rate of the extrinsic gas by the first burner as a function of a rate at which heat is transferred from the thermal oxidizer to the pyrolyzer. In preferred embodiments, the burn rate of the extrinsic gas can be adjusted to ?50%, ?30% or even lower relative to a base rate that would be required to pyrolyze the waste without the heat thermal oxidizer.

Abstract: A versatile oven for converting carbon based natural resources and waste material to hydrocarbon vapor and carbon char utilizing rapid thermal processing and having the capability of utilizing a portion of the relatively inexpensive carbon based material being processed as the fuel to provide at least some of the process heat and also including a means for reducing NOx emissions in the gases exhausted from a furnace used to burn the converted hydrocarbon vapor for application of the heat energy and also a means for delivering the converted hydrocarbon vapor to a condensing system if it is desired to liquefy at least some portion of the thermally converted hydrocarbon vapor.

Abstract: A waste carbonizing and energy utilizing system comprises a carbonizer, a gasifying fusion furnace, and a power generation plant for utilizing heat energy. The carbonizer 20 carbonizes waste to generate charcoal. The gasifying fusion furnace incinerates the charcoal, and then the heat generated by the incineration of the charcoal is used for operation of the power generation plant. Exhaust heat from the power generation plant is recycled to the carbonizer.

Abstract: The device relates to a device for leveling the coal filled in the retort of a coke oven, comprising a leveler bar (2) connected with a leveler bar drive (1) that can be moved into and out of the retort (4) through a leveling opening (3), and performs a leveling movement back and forth in the retort (4). According to the invention, the leveler bar (2) has a rake blade (5) on its front end with a width that can be adjusted by an operating device (6) arranged in the leveler bar (2).

Abstract: Process for incinerating refuse derived fuels to obtain fuel gas therefrom by thermal cracking, comprising the following steps: subjecting the material to deaeration; advancing a bed of material within a vacuum environment insulated from the outside (thermal cracking chamber) and in which a temperature of between 400 DEG C. and 600 DEG C. is maintained by the countercurrent flow of hot gases which lap the material; feeding the material which has passed through the thermal cracking chamber to a reactor in order to be subjected to a temperature of between 1200 DEG C. and 1800 DEG C.; in proximity ot the entry end of said thermal cracking chamber, drawing off the gases generated by the thermal cracking together with the gases which have lapped the bed of material, in order to maintain the thermal cracking chamber under vacuum; feeding the drawn-off gases to the discharge conduit for the gases generated in the reactor; purifying and filtering the gases obtained in this manner for their use as fuel gases.

Abstract: A furnace has a dual structure for carbonizing material. The furnace has a group of inner chambers and an outer chamber. Each of the inner chambers has a lid which can open and close to input the material for carbonizing. The outer chamber moves so that the group of inner chambers is housed in the outer chamber. Due to this, a combustion space is formed between the group of inner chambers and the outer chamber so as to heat each of the inner chambers to dry the material by distillation.

Abstract: The invention relates to an industrial and/or household waste treatment method and to an industrial and/or household waste treatment installation (1). According to the invention, the method is characterised in that it consists of, in particular, the loading of the waste into numerous pierced containers (20), thermolysis of the waste in the containers (20) being conveyed into a pyrolysis oven (12); emptying of the containers (20) into a separation tank (18) in order to separate the products formed by the thermolysis; and treatment of the separated products.

Abstract: A process for the pyrolysis of waste materials, particularly medical waste, is provided. In the pyrolysis process, waste material is placed in a sealed container. The sealed container is placed in a load chamber and the waste material is subjected to pyrolysis. The process generates pyrolysis gases containing volatile organic compounds which are fed to an oxidation chamber containing tangential and radial air inlet ports. The pyrolysis gases are combusted and hot gases are produced in the oxidation chamber. In the operation, at least a portion of the generated heat and hot gases is fed to the load chamber which holds the pyrolysis container.

Abstract: A gasification system that includes a gasification reactor chamber having perforated conduits or an inner lining that increases the exposed surface area of waste materials to gasification conditions, thereby decreasing gasification temperature, time, and cooling period between subsequent gasification procedures. After an aspirator withdraws and oxidizes fuel gas from the gasification reactor chamber, a flare assembly combusts the mixed fuel gas to provide power or heat to at least one heat recovery device. The at least one heat recovery device recaptures thermal energy entrained in the exhaust, thereby reducing exhaust temperature and eliminating the need for an exhaust stack. An absorber purifies the exhaust and an extractor removes carbon dioxide. A portion of the removed carbon dioxide may be used for industrial purposes or for supporting vegetation. At least a portion of the remaining exhaust is returned to the gasification reactor chamber as recycled process gas, thereby completing a closed-loop system.

Abstract: A reactor for gasifying and/or melting feed materials, the reactor including a charging section with a feed opening, through which the feed materials are charged to the reactor from above and a pyrolysis section which has an expanded cross section and is located below the charging section so that a discharge cone of the feed material can form. Gas supply devices, open into the pyrolysis section substantially at a level of the expanded cross section and through which hot gases can be fed to the discharge cone. A melting and superheating section is located below the pyrolysis section and has a narrowing cross section. Upper injection devices are arranged so that an energy-rich medium is supplyable to the melting and superheating section immediately below a level of the narrowing section. A reduction section is located below the melting and superheating section. The reduction section has gas exhaust devices through which excess gases are exhausted.

Abstract: A process for the pyrolysis of waste materials, particularly medical waste, is provided. In the pyrolysis process, waste material is placed in a sealed container. The sealed container is placed in a load chamber and the waste material is subjected to pyrolysis. The process generates pyrolysis gases containing volatile organic compounds which are fed to an oxidation chamber containing tangential and radial air inlet ports. The pyrolysis gases are combusted and hot gases are produced in the oxidation chamber. In the operation, at least a portion of the generated heat and hot gases is fed to the load chamber which holds the pyrolysis container.

Abstract: A process is described for gasifying solid fuels at a constant rate with a small regulated amount of primary air followed by combustion of the gas so formed with a larger regulated amount of secondary air to produce a clean hot combustion gas which is used for process heat, space heating or cooking.

Abstract: A waste incineration machine capable of rendering a waste gas occurring during the combustion of waste smokeless and odorless. A heat insulating wall to which a first far infrared ray radiator is fixed is provided so as to surround a combustion furnace and a combustion chamber, and a heat exchanger so as to surround the heat insulating wall. An inner flue is formed between the heat insulating wall and combustion furnace, and an outer flue serving as a waste gas convection chamber between the heat insulating wall and heat exchanger. An upper part of a communication portion between the inner and outer flues is covered with a heat insulating member constituting a second far infrared ray radiator so as to subject the waste gas to secondary heating using far infrared rays, and thereby to render the waste gas smokeless and odorless.

Abstract: A process for incinerating waste material to produce slag without the addition of fuel other than the waste material begins with carbonizing the waste material in a low temperature process in a generator to produce carbonized solid material with a high energy content and flammable gases which are extracted from the waste material. The carbonization and temperature in the generator are controlled by limiting the supply of air to the material in the generator, the temperature being less than 1000° C. The carbonized waste material and the carbonization gases are delivered together to a furnace which is supplied with excess air. The carbonized material and carbonization gases are incinerated at a high temperature, typically 1400° C., in the furnace, thereby substantially completely incinerating burnable products in the furnace and melting materials which will not burn. The result is a glassy slag which binds therein materials such as heavy metals which could otherwise be pollutants.

Abstract: Farm animal biomass, such as the waste and shredded carcasses of poultry and hogs, and/or animal bedding, is incinerated by being delivered to the inlet of a duct. During a processing period the biomass is heated uniformly to a temperature while advanced through the duct by a feed screw without sufficient oxygen to support combustion. The temperature and processing time are sufficient for partially carbonizing the biomass into combustible gas and partially carbonized char. The char is discharged to a first combustion chamber to be combusted and converted to ash. The combustible gas is discharged to a second combustion chamber to be combusted within hot porous cylindrical ceramic combustors. A portion of the duct passes through the second combustion chamber in order to supply heat for partially carbonizing the biomass. Additional heat is provided by passing hot air through the feed screw. That hot air is discharged from the feed screw and supplied to the combustion chambers to support combustion therein.

Abstract: Apparatus for processing and recycling CCA (copper, chrome, arsenic) treated wood chips that includes a vertical reaction chamber into which a continuous stream of wood chips is poured. Hot gases at about 400.degree. C. are introduced into the bottom of the column to heat the chips below their ignition point. The combustion gases flow upwardly through the chips to progressively cool the gases and allow them to condense in the column. The condensate is deposited upon the surface of the chips and the gases, which are now free of heavy metals, are evacuated from the column.

Abstract: A discharge apparatus includes a housing into which a discharge pipe of a carbonization drum opens. A residue discharge chute which starts from the housing opens into a conveying device ending at an outlet. A filling-level meter is disposed at the residue discharge chute. The conveying device has a profiled separating shelf with an end remote from the mouth of the residue discharge chute, at which a bar screen is formed. The bar screen covers a delivery opening for fine residue and ends at the outlet for coarse residue. A vibrator is associated with the conveying device.

Abstract: Waste material is conveyed in an uncomminuted state on a grate (5) through a combustion chamber (12) of a stationary furnace (10) and at the same time mixed by a thrust and shearing action of the grate (5). A gaseous oxidizing agent is introduced, for example via gas lances, into the combustion chamber (12) from above the layer of waste material (11) lying on the grate (5). The oxidizing agent cooperates with the combustible volatile substances escaping from the waste to form flames. The layer of waste is heated by the thermal radiation of the flames such that degasification occurs. The combustible gases thus freed are partially burnt. The waste material freed from the volatile substances, that is to say refuse coke, and the unburnt volatile substances, that is to say combustible gases, can be used as fuels outside the plant or within the plant. The oxidizing agent does not come into contact with the thermally stressed parts of the plant.

Abstract: A closed tube extension or deadleg is included below the vertical tube of a hydrocarbon pyrolysis furnace. The deadleg passively collects spall coke particles to avoid plugging of the tube or its hydrocarbon inlet. Inspection or cleaning devices can be inserted through the deadleg into the tube and blocked tubes can be cleared. Pressurized steam and/or air can be injected through the deadleg to accelerate decoking of individual tubes.

Abstract: The invention provides methods, apparatuses, and rotary furnaces for continuously manufacturing charcoal having a carbon content by weight which is greater than 95% of the total weight of carbon and volatile matter. Fragments of vegetable material contained in a hopper are inserted into a rotary furnace, with the transit time of the fragment through the furnace lying in the range 45 minutes to 60 minutes. The temperature in the front zone of the furnace where carbonization takes place is maintained in the range 900.degree. C. to 1000.degree. C. The furnace is heated by an axial burner which burns both combustible gases due to pyrolysis of the vegetable matter fragments and a second fuel. The charcoal falls into a hopper, from which it passes through a cooling chamber where it is colled by sprayed jets of water, after which it is extracted by an endless screw extractor. One application of the invention is manufacturing charcoal for making activated charcoal free from inorganic impurities.

Abstract: Industrial, municipal, sanitary, marine, and infectious waste materials are thermally and chemically converted principally to steam, fuels and environmentally acceptable solids by dehydration, pyrolysis of the solid residue therefrom, and finally gasification of the pyrolysis char residue. In contrast to incineration processes, the products have significant market value and present no atmospheric pollution problems. Temperatures employed range up to about 3000.degree. F.

Abstract: A method for economically separating chemical contaminants such as volatile organic chemicals (VOC's) and polychlorinated biphenyls (PCB's), even if the contaminants are present at low concentrations, from inert materials such as soils or sludges, comprising subjecting inert materials contaminated with chemical compounds to a temperature effective to volatilize the contaminants but below incineration temperature, with continuous removal of evolved vapors, for a period of time sufficient to effect the desire degree of separation of contaminants. The evolved vapors may be subjected to catalytic oxidation to destroy the volatilized chemical compounds.

Abstract: There is provided a slagging combustion system for generating high purity working fluid suitable for driving gas turbines. The system consists of a precombustor for preheating oxidant tangentially fed to a primary slagging combustor where a solid carbonaceous material is combusted under substoichiometric slagging conditions. Slag is collected in the primary slagging combustor and products of combustion passed to a transition section where tertiary oxidant and sulfur-gettering agents are added, and then to a cyclonic secondary combustion chamber.

Abstract: A two zone pyrolysis unit having a first drying zone and a second pyrolysis zone is provided for detoxifying heavy metals contained in sludges, soils and similar materials. A condenser and an afterburner are in flow communication with the first and second zones respectively.

Abstract: This invention relates to a plant and arrangement and method for the low temperature carbonization of waste material with low-temperature carbonization device and a secondary incineration chamber. The heating system of the low-temperature carbonization device is substantially corrosion-free and gases hazardous to the environment are transformed into gases with a lower level of hazardous matter in a simple manner by directing the heating gas of the low-temperature carbonization device into a closed loop cycle through a low temperature carbonization device and into a heat exchanger of a secondary incineration device. The heat exchanger is equipped with a lining which insures a temperature of the burner gases in the heat exchanger of 1200.degree. C. or more for a period of dwell of 1 to 5 sec.

Abstract: An installation for the low temperature carbonization of waste under the exclusion of air with a low temperature carbonization cylinder, in particular device for after-burning of residual materials for the low-temperature carbonization installation, has an improved energy balance by carrying out a low-temperature carbonization so as to increase the ratio of internal energy requirement to energy release in favor of energy release. The carbon containing residual materials from the low-temperature carbonization cylinder are exposed to a complete after-burning on an inclined step grate and also a subsequent after-burning in a chamber. The burning gases for the burning devices of the step-grate are low temperature carbonization gasses obtained from the low-temperature carbonization installation. Gases from a waste heat boiler arranged after the after-burn chamber are utilized as heating gases for a low-temperature carbonization installation cylinder.

Abstract: In the operation of a slagging combustor, including an apertured baffle defining part of a cylindrical combustion chamber having a head end which includes a nozzle for injection of sulfur-containing particulate carbonaceous material to be combusted in a whirling oxidant flow field, there is injected a particulate sulfur sorbent at the aperture of the baffle towards the nozzle to react with released sulfur. The sulfur sorbent is injected into the combustion zone from a location near the exit end thereof. Fuel is injected near the center of the head end. A relatively fuel-rich recirculation zone is established and maintained along the longitudinal axis of the combustion chamber surrounded by a relatively oxygen-rich annular region.

Abstract: The invention is a system for detecting the level of slag in a solid fuels gasification reactor. In this invention a pokerod is extended into the quench chamber of the reactor, and pulled back to a retract position, in a timed sequence. The timed sequence is initiated by an electronic controller unit, in combination with an air pressure regulator, a solenoid valve, a double chamber air cylinder, and two sensor switches. The end of the pokerod that moves into the quench chamber is designed to contact the solid slag without penetrating the material itself. If the pokerod makes contact with the slag material, the controller sets off an alarm to warn the operator of slag build up in the reactor.

Abstract: Method and apparatus for incinerating low density organic materials using a pair of side by side multiple hearth furnaces are disclosed. The first furnace of the pair operates in a temperature-controlled reducing atmosphere to achieve complete volatilization of non-fixed carbon contained in the fuel feed stock. The second furnace operates in a temperature-controlled oxidizing atmosphere to achieve complete oxidation of all fixed-carbon contained in the char output of the first furnace. The gaseous products of both furnaces are combined and burned in a low - Btu gas burner, thus providing the heat input to a power boiler or other process suited to the heat quality produced.

Abstract: An apparatus and method for continuously treating material for performing such functions as burning, roasting, smelting, coking, melting, high temperature chemical reactions and the like in a combustion chamber wherein the chamber or an extension thereof, is tuned to permit combustion gases therein to resonate and to thereby effect maximum combustion efficiency. In particular, the invention concerns controllably varying the geometry of the combustion chamber, such as the length of a pipe or tubed section thereof in accordance with the variables of combustion occuring therein, so as to optimize efficiency of combustion and the reaction which takes place between the burning material and the material being treated or reacted on. In addition to effecting such reactions, the apparatus is also operable to effect the transfer of the heat of combustion to a heat transfer medium, such as water for generating steam or other form of heat transfer medium to maximize the utilization of the energy generated.

Abstract: Slugs (4) of products dehydrated by compression are thrust into the tube (11) up to the hearth (15). The hot gases from the hearth passing round the tube (11) heat it up in order to release the gases and carbonize the solids which burn in the form of coke in the bottom (16) of the hearth. Household refuse may thus be eliminated not only without expense but with recovery of energy from it.