Abstract: A compact efficient air flotation dryer with a built-in afterburner for combustion of solvent-laden air within a dryer-enclosed combustion chamber. An internal exhaust fan propels internal solvent-laden air across a burner where it combusts, causing a heat rise. Heated, combusted air is routed to a recirculating supply air fan which provides for pressurized heated air for air bars for drying a web. Heated air in excess of that required to dry the web is vented externally and helps to maintain desired solvent concentration levels Variable parameters such as fan speed, burner temperatures, air box pressures, exhaust air rate, solvent concentration, supply air flow, supply air temperature and damper vane position are monitored, and the components are actuated to effect a high level of clean up efficiency.

Abstract: The present invention relates to an apparatus treating waste comprising introducing a glass or mineral fiber substrate (7) contaminated with organic materials into a chamber (1) of a furnace by means of a conveyor belt (4), subjecting it to a gas consisting of a neutral gas and between 0 and 10% by volume of oxygen, heated to a temperature below the melting temperature of the waste substrate in order to pyrolyze the organic materials, and recovering the waste substrate. This apparatus has particular application to the recovery of the vitreous material forming the waste substrate, in order to recycle it for use in a glass melting furnace.

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: Oxidizable components in an exhaust air or gas flow are burnt by a burner in a combustion chamber enclosed in a housing. For this purpose the exhaust air is distributed into inlet ends of heat exchanger pipes which have outlet ends near the burner. The arrangement is such that the exhaust air carrying oxidizable components flows through the heat exchanger pipes while the exhaust air freed of oxidizable components flows around the heat exchanger pipes. In order to permit effective heat expansions and contractions of the heat exchanger pipes, these pipes have an L-configuration with radially inwardly extending legs having inlet ends connected into perforations in a jacket forming an exhaust air distribution chamber, and with substantially axially extending legs having outlet ends leading close to the burner. An air inlet leads centrally into the distribution chamber and a cleaned air outlet leads out of the housing.

Abstract: A reflow system for heating solders temporarily attaching electronic components to a circuit board, includes an elongated heating chamber in which a conveyor extending from an inlet to an outlet of the heating chamber, at least one first heating unit, a fan unit and an organic substance decomposition unit are disposed. The conveyor, first heater unit and fan unit are arranged to circulate gas in the heating chamber along a circulation path such that the gas is first heated by the first heater unit, then forced by the fan against the conveyor, and thereafter heated again by the first heater unit. The organic substance decomposition unit is disposed in the circulation path. The solders are heated by hot air. It is possible to heat the solder with hot nitrogen gas in which instance a nitrogen gas supply unit disposed outside the heating chamber is used to fill the heating chamber with nitrogen gas.

Abstract: Both aluminum scrap covered with a volatile coating and a heated airstream having a low oxygen content pass through a kiln where the airstream causes the coating to volatilize. The temperature of the airstream, where it enters the kiln, is maintained essentially constant, slightly below the melting temperature of the aluminum, and likewise the temperature of the airstream is maintained essentially constant where the airstream leaves the kiln, this being achieved by varying the mass flow of the airstream to compensate for variances in the nature and mass of the aluminum scrap within the kiln. Beyond the kiln the airstream enters an afterburner where it is heated in the presence of sufficient oxygen to effect combustion of the volatile components of the coating. The airstream then passes through a heat exchanger and back to the kiln. The mass flow within the kiln is controlled by diverting some of the airstream from the heat exchanger or by varying the speed of the fan which creates the airstream.

Abstract: An apparatus is disclosed which is capable of efficiently decontaminating soil, and which has several common components with a conventional asphalt production plant. This feature permits a conventional asphalt plant to be retrofitted by the addition of a relatively small number of additional components, so as to permit the apparatus to selectively produce asphalt, or to decontaminate soil. When operated in the configuration for decontainating soil, the soil is initially heated to a temperature above the vaporization temperature but below the autoignition temperature of the contaminants, so as to volatilize the contaminants. The volatilized contaminants are then delivered to an incinerator, wherein the volatilized contaminants are heated to a temperature sufficient to be converted to non-toxic products, such as carbon dioxide and water.

Abstract: Waste products, particularly scrap metal, adulterated by organic components, is pyroprocessed by: (1) shredding the adulterated scrap metal into particles having a maximum size of 5 cm.; (2) in a pyrolysis stage operating at a temperature of approximately 550.degree. C. to 600.degree. C. converting the particles into solids and pyrolysis gas; (3) in a mechanical processing stage separating the solids into unadulterated metal and pyrolysis coke; and (4) in a high-temperature gasification stage into which an oxidizing agent and, optionally, metallurgical coke is introduced converting the pyrolysis coke together with pyrolysis gas stemming from the pyrolysis stage into a heating gas free of organic substances.

Abstract: In a method and apparatus for cleaning a gas flow that carries oxidizable pollutants in varying concentrations, the temperature within the combustion apparatus is maintained substantially constant by admixing controllable proportions of the gas to be cleaned and/or fresh air to the combustion flow. However, admixing prior to introducing the gas to be cleaned into the combustion flow is avoided by performing the admixing at a location near the exit end of a flue gas mixing pipe. This mixing location permits maintaining the combustion chamber temperature constant or at its rated level while simultaneously keeping the temperature of the flow control device at acceptable levels. The flue gas mixing pipe is arranged downstream and coaxially with a burner so that the admixing takes place after the combustion or carrier flow has already passed the burner at the entrance to the combustion chamber.

Abstract: A device at a heat treatment oven of the type using a combination of radiation heat and convection heat, and where in connection to the oven chamber are provided means (4, 19) arranged to circulate the oven atmosphere through the oven chamber and a channel (20, 21) situated outside the oven chamber and back to the oven chamber, whereby the device incorporates a gas burner (7) arranged at combustion to emit its flame in a direction, which at least partly touches or coincides with the circulation channel (20, 21) for the oven atmosphere, and where the gas burner (7) is arranged to direct its flame into a vessel (22), provided in the circulation channel (20, 21) for the circulating atmosphere.

Abstract: An apparatus for burning pollutants in a carrier gas flow such as exhaust gases, is constructed as a compact unit. For this purpose a radial blower for the supply of the carrier gas which carries the pollutants is arranged directly in an inlet chamber of the gas cleaning apparatus. The inlet port of the inlet chamber is connected through a duct to the suction inlet of the radial blower. The compression outlet of the radial blower leads into a ring gap which in turn opens radially into the inlet chamber. For this purpose, the radial blower is enclosed by a blower housing which is arranged concentrically at one end of the housing opposite the burner arranged at the other end of the housing. The drive motor for the radial blower is mounted directly on the outside to an end wall of the housing of the apparatus.

Abstract: An improved industrial furnace employing a new and unique heat transfer arrangement is disclosed. The furnace is a closed end cylindrical chamber with a circular, concentrically positioned plate dividing one side of the furnace into a fan chamber containing a fan and the other side of the furnace into a heat treat chamber containing the work. The plate has a central under-pressure opening and its outer circular edge is spaced from the cylindrical wall to define an annular space which is non-orificing. Fan rotation in the fan chamber produces an annulus of wind mass swirling at high circumferential speed which axially travels through the non-orificing space towards the closed end of the heat treat chamber at slow speed. Heating elements extend through the non-orificing space into the heat transfer chamber and are constantly impinged by the swirling annulus wind mass to effect good heat transfer therewith.

Abstract: A compact efficient air flotation dryer with a built-in afterburner for combustion of solvent-laden air within a dryer-enclosed combustion chamber. An internal exhaust fan propels internal solvent-laden air across a burner where it combusts, causing a heat rise. Heated, combusted air is routed to a recirculating supply air fan which provides for pressurized heated air for air bars for drying a web. Heated air in excess of that required to dry the web is vented externally and helps to maintain desired solvent concentration levels. Variable parameters such as fan speed, burner temperatures, air box pressures, exhaust air rate, solvent concentration, supply air flow, supply air temperature and damper vane position are monitored, and the components are actuated to effect a high level of clean up efficiency.

Abstract: A combustion furnace having a cylindrical filter arranged to pass gases between a combustion cylinder and a gas analyzer attached to an output port on the furnace. The gases to be analyzed are generated from a sample burned in the combustion cylinder and removed through the filter. A cleaning gas supply port and supply line for supplying a cleaning gas to the inside of the furnace are provided. The cleaning gas is under pressure and may be oscillated to assist in the removal of dust stuck to the filter and the interior of the furnace. The improved dust removal provides for a much cleaner furnace and a more accurate analysis of the sample.

Abstract: A radiant wall oven with a heating chamber and hot air chamber separated by a radiant wall, an air heating chamber, supply and return ducts between the air heating chamber and hot air chamber and blower means for circulating hot air through the ducts is provided with a radiant wall temperature control comprising two cascaded closed loop controls. The first compares the radiant wall temperature with a first setpoint value to generate the difference as a second setpoint value for the second, which compares the temperature of the supply duct with the second setpoint value to control a heat source such as a burner. Under certain conditions, the air heating chamber is vented to atmosphere.

Abstract: A heat-treatment apparatus of the invention includes a collective exhaust unit for constantly performing gas exhaust from a clean room to keep the room in a clean atmosphere, a heat-treatment furnace for receiving a gas and/or a liquid for forming a desired film on a surface of an object to be treated in a heating atmosphere, an exhaust path, communicating with the collective exhaust unit and the heat-treatment furnace, for introducing a gas filling the heat-treatment furnace into the collective exhaust unit, an outer air intake unit for taking in outer air in the exhaust path to adjust an exhaust pressure of the exhaust path, and a trap unit, arranged below the exhaust path, for trapping a waste liquid collected in the exhaust path.

Abstract: A combustion process for nitrogen- or for sulphur- and nitrogen-bearing fuels wherein fuel combustion is divided, by staged oxygen (preferably in the form of air) injection, into at least two combustion zones. The first combustion zone involves providing fuel-rich stoichiometric conditions under which nitrogen chemically bound in the fuel (i.e. fuel-bound nitrogen) is substantially converted to molecular nitrogen. The second (final) combustion zone comprises at least two stages. In the first stage of the final combustion zone, combustion products from the first combustion zone are further conbusted under a condition of fuel-rich stoichiometry, preferably at an oxygen/fuel stoichiometric ratio of from about 0.08 to about 1.0 and at a temperature of less than about 2200 K. In the second stage of the final combustion zone, combustion products from the first stage are combusted at an oxygen/fuel stoichiometric ratio of greater than about 1.0 and at a temperature of less than about 1500 K.

Abstract: A reactor for the complete combustion of gases and fuels without emissions of polluting agents, with increased efficiency of combustion, and decreased condensation on the exchange surfaces, providing greater longevity of the firebox. Turbulence of the combustion gases is induced by a coupling ring, placed between a cone and a deflector, which cause the gases to take a trajectory parallel to the generator cover of the chamber, and causes the gases to inpinge against the heat exchange surfaces, thereafter causing a more even caloric heat distribution.

Abstract: The invention relates to a process and a device for indirectly heating a flow of gaseous fluid. According to the invention, the flow of fluid to be heated is first subjected to a first heat exchange with combustion products, in a heat exchanger (3), and is subsequently subjected to a second heat exchange with a heat-exchanging fluid circulating in a second heat-exchanger (5). The flow of fluid to be heated is then circulated in a third exchanger (7) where it is subjected to a heat exchange with the combustion products before the latter are used at the time of the first heat exchange. The third heat exchanger (7) can comprise radiating tubes (51) and convection surfaces for heating the flow of fluid in circulation, essentially by convection.

Abstract: Both aluminum scrap covered with a volatile coating and a heated airstream having a low oxygen content pass through a kiln where the airstream causes the coating to volatilize. The temperature of the airstream, where it enters the kiln, is maintained essentially constant, slightly below the melting temperature of the aluminum, and likewise the temperature of the airstream is maintained essentially constant where the airstream leaves the kiln, this being achieved by varying the mass flow of the airstream to compensate for variances in the nature and mass of the aluminum scrap within the kiln. Beyond the kiln the airstream enters an afterburner where it is heated in the presence of sufficient oxygen to effect combustion of the volatile components of the coating. The airstream then passes through a heat exchanger and back to the kiln. The mass flow within the kiln is controlled by diverting some of the airstream upstream from the heat exchanger or by varying the speed of the fan which creates the airstream.

Abstract: Apparatus includes a kiln (10) through the chamber (12) of which is passed a flow of scrap material, e.g. aluminium can scrap, for heat processing e.g. removal of lacquer and other contaminants, and gas circulation means having a heater (40) providing inflow of hot gases to the kiln, an outlet flue (32) leading off exhaust gases from the kiln with recirculation of at least part of the latter gases to the inflow, and a fan (36) or other flow inducing means for effecting circulation, preferably by suction with respect to the kiln, with flow through the latter in the opposite direction to the feed of material, and at least a temperature sensor (TI) at the material input end of the kiln for automatic regulation of the throughput of gases to regulate the kiln temperature.

Abstract: A method and system for flue gas recirculation is disclosed which will minimize NOx production from hydrocarbon combustion. In the present invention a furnace having an oxygen-bearing primary source of combustion air, a mixing chamber, a combustion chamber in downstream communication with the mixing chamber and an exhaust section downstream of the combustion chamber is provided with a flue gas recirculation line. The recirculation line establishes communication between the exhaust section and the mixing chamber for the return of combustion products as a secondary source of combustion air which is relatively lean in oxygen and is combined with the primary source of combustion air in the mixing chamber. The ratio of flow rates for the primary and secondary sources of combustion air is controlled by a signal generated by a sensor which senses the oxygen concentration in the mixing chamber.

Abstract: The present invention provides an oven comprising an elongate chamber with an inlet orifice at one end and an outlet orifice at the other end, via which a filament can pass through the chamber. Primary nozzles for use in introducing hot gas into the chamber are arranged, together with a gas outlet port, adjacent to the said one end of the chamber. Preferably the outlet port is nearer to the said one end than the primary nozzles. Secondary nozzles also for introducing hot gas into the chamber are arranged adjacent to the other end of the chamber. In use, hot gas is fed under pressure into the chamber via the primary and secondary nozzles against the direction of filament travel. Whilst the hot gas is fed under high pressure through the primary nozzles, the hot gas is fed at a relatively low pressure but high volume through the secondary nozzles. In this way the filament is heated all along its length in the chamber.

Abstract: A pyrolyzer-kiln system for generating combustible fume from waste material and supplementing the fuel used to provide heat energy to a clinker kiln. The system includes a pyrolyzer for generating a combustible pyrolytic fume, a kiln for burning the fume as part of a cement-forming process, a conduit for conveying the fume from the pyrolyzer to the kiln, and a closed-loop feedback component for monitoring the heating value of the fume and varying the operational parameters of the pyrolyzer to maintain the heating value of the fume generated within a predetermined range. The closed-loop feedback component includes a calorimeter which continuously samples and burns fume from the conduit. The heating value of the fume is determined by measuring the amount of auxiliary fuel and air required to be mixed with the fume to maintain a predetermined temperature when the combustion is burned within the calorimeter.

Abstract: An inorganic reinforcement component, such as fiberglass, is reclaimed from a scrap material including a vaporizable organic resin, such as epoxy, by heating the scrap material in an elongated, rotary furnace to a temperature above the vaporization point of the organic resin and below a point where the structural integrity of the reinforcement material is degraded. A purge gas flowing through the furnace countercurrently to the moving bed of scrap material sweeps away volatized gases, the organic reinforcement component is withdrawn from the outlet end of the furnace and a stream of combined gases including the purge gas and the volatized organic material is withdrawn from the inlet end of the furnace.

Abstract: An oven for drying and curing a film of paint, ink, or the like on a continuous strip of metal has a non-rectangular, and preferably oval, elongated oven chamber without sharp internal corners. By avoiding sharp corners in the oven, air flow is more uniform and deposits of condensed fumes are minimized. In some embodiments no internal bracing structure required. The absence of internal structure is permitted by the oven's walls, oval shaped in transverse cross section, which result a naturally self supporting structure. Cleaning nozzles may be provided for washing the inside of the oven without need for people to enter the oven.

Abstract: A method and system for flue gas recirculation is disclosed which will minimize NOx production from hydrocarbon combustion. In the present invention a furnace having an oxygen-bearing primary source of combustion air, a mixing chamber, a combustion chamber in downstream communication with the mixing chamber and an exhaust section downstream of the combustion chamber is provided with a flue gas recirculation line. The recirculation line establishes communication between the exhaust section and the mixing chamber for the return of combustion products as a secondary source of combustion air which is relatively lean in oxygen and is combined with the primary source of combustion air in the mixing chamber. The ratio of flow rates for the primary and secondary sources of combustion air is controlled by a signal generated by a sensor which senses the oxygen concentration in the mixing chamber.

Abstract: A continuous process aggregate drying and mixing plant for producing a hot asphaltic material, such as is used for paving highways or the like, includes a combination of a drum drier and a pugmill. Both the drum drier and the pugmill are supported by a common trailer frame. The pugmill is coextensively mounted at the discharge end of the drum drier towards the rear of the frame. The drum drier discharges dried and heated virgin aggregate material through a feed and transfer chute directly into a first, pre-mix region of the pugmill. The feed and transfer chute also provides for the addition of recycled pavement to the heated and dried aggregate and for the side discharge of such heated and dried aggregate. A second region of the pugmill within which liquid asphalt is added to the mixed aggregate is substantially separated from the first, pre-mix region. The space above the second region of the pugmill is substantially enclosed and coupled directly to a secondary air supply of a burner for the drum drier.

Abstract: A furnace for firing an enamelled wire comprising a principal chamber, an auxiliary unit for the aspiration of a first stream of air and solvent vapours from this principal chamber and combustion of the vapors themselves, and a duct assembly operable to introduce gaseous streams into the principal chamber for controlling the temperature within the principal chamber; the auxiliary unit comprises a heater constituted by a plurality of electrical resistances operable to heat this first stream at least up to a temperature sufficient to cause initiation of the combustion of the said vapors, and by a support structure for these resistances, housable in a duct of the auxiliary unit; the support structure and the walls of the duct are made in steel alloy which is highly resistant to high temperatures. (FIG. 1 and 2).

Abstract: A carbon desorption heater (10) for use in a system for removing volatile organic contaminants from a carbon filter is disclosed as having a housing (30) in which a recirculating heating circuit (36) is provided with a recirculation blower (44) that moves the air past a burner (50) for flow through a first flow path (60) of a heat exchanger (58) with a portion of the recirculated air exhausted during each cycle of flow through an exhaust stack outlet (52). A delivery blower (64) within the housing (30) moves air through a second flow path (62) of the heat exchanger (58) for heating prior to delivery to a supply outlet (34). The heater includes a plurality of modules (90) that are sufficiently small so as to be shippable and subsequently securable to each other at the factory site where the heater is to be used.

Abstract: A material heating oven for sterilizing items for use in a sterile environment or the like comprising a hot air supply device having a filter, a cool air supply device having a filter, an oven cavity separate from the hot air supply and cool air supply devices, and a dampering system for selectively drawing air from the hot air supply and cool air supply devices to regulate the temperature of the oven cavity. Both the hot air supply and cool air supply devices include independent air recirculation loops for maintaining substantially constant temperature airstreams from which selected quantities of air are exchanged with the oven cavity. The nearly constant temperature airstreams prevent the filters in the devices from being thermally stressed which may cause them to shed particles to the clean environment. An electrically controlled temperature control system is used to regulate the temperature of the airstream flowing through the hot air supply and cool air supply devices.

Abstract: A test oven wherein heated air having a predetermined temperature is supplied and the oxygen concentration in the supplied air is controlled. The test oven has a test oven body having an air supply port and an air discharge port, a blower connected to the air supply port for blowing air thereinto, an oxygen concentration detector connected to the test oven body, an oxygen concentration setting control unit connected to the oxygen concentration detecting detector and including an oxygen concentration setter for setting a desired level of oxygen, and an oxygen concentration controller constantly comparing a reference output level generated on the basis of a concentration level set in advance in the oxygen concentration setter with an output level outputted from the oxygen concentration detector and for controling the actual output level to a set level, and at least one oxygen concentration adjusting device.

Abstract: A flame arresting method, conduit section and apparatus for the safe disposal of combustible waste gases from a source such as a reactor. The invention involves providing a waste gas conduit section with a flame-detecting chamber and one or more upstream snuffing chambers divided by flame arresting grid members, and automatically introducing snuffing gases to the snuffing chamber(s) whenever a flame is detected in the flame-detecting chamber. The outlet from the waste gas conduit section opens to a combustion chamber, for incineration purposes, or to a scrubber.

Abstract: A multimode thermal treatment system includes a series of particle treatment zones. Perforate conveyer structure for supporting the particulate product to be thermally treated is disposed for movement through the series of treatment zones. Each treatment zone includes first (upper) distribution plenum structure disposed above the treatment zone and an array of nozzle tubes extending downwardly from the upper distribution plenum into the treatment zone to flow conditioned gas with substantial velocity into the treatment zone for thermal treatment of particulate material being transported by the conveyer structure through the treatment zone; and a second (lower) distribution plenum disposed below the treatment zone for pressurizing the region below the treatment zone and flowing conditioned gas upward through the conveyer structure and the particulate material on the conveyer.

Abstract: The present invention provides an energy conserving process for calcining a clay and apparatus for carrying out the process. A dry pulverized clay powder (1) is fed to a calciner (20) to be calcined therein. The calcined clay product (3) is removed from the calciner (20) and preferably passed in heat exchange relationship with a cooling medium (71) whereby the calcined clay product (3) is cooled and the cooling medium is heated. The hot off-gas (7) discharged from the calciner (20) is passed through an electrostatic precipitator (30) to remove at least a substantial portion of calcined clay product dust (11) entrained in the exhaust gas from the calciner. The clean gas (13) leaving the electrostatic precipitator (30) is passed in heat exchange relationship with a cooling fluid (51) to further cool the gas, and preferably to evaporate at least a portion of the cooling portion to produce a heating vapor (53).

Abstract: A drier for a web of material in particular for a offset printing machine, consisting of an housing with an inlet slot and an outlet slot for the web of material. The housing is provided with air nozzles which are fed via one or more fans with the atmosphere in the housing. The housing also have at least one heating appliance provided with a combustion unit for treating the atmosphere inside the housing. The interior of the housing is divided by a partition into a heating section and an evaporating section. The heating appliance is provided with an incinerating portion and part of the combustion gases is via an opening discharged to the heating section, while the remaining combustion gases are discharged into the outside air, and the atmosphere of the evaporating section is used as combustion air for the burner of the combustion unit.

Abstract: A soldering apparatus of the reflow type contains a preheating chamber and a reflow chamber which are provided with a plurality of heaters for heating printed circuit boards with chips temporarily mounted thereon with solder pastes during conveyance by a conveyor. The heaters are provided with a screening member and/or a partition member so as to prevent direct radiation of radiant heat from the heaters into the chambers and onto the printed circuit boards and to provide a uniform air flow to be blown uniformly onto the printed circuit boards. The heaters are arranged so as to heat them in such a manner as to increase temperatures in the direction from an inlet to an outlet so as to become higher with a predetermined temperature differential from the previous heater, thus removing bubbles generated upon fusion of the solder pastes and minimizing heat shock to the chips as they are heated.

Abstract: A furnace for firing an enamel-insulated wire comprising a principal cham, an auxiliary unit for withdrawing a first stream of air and solvent vapors from this principal chamber for effecting combustion of the vapors themselves. A part of a second stream leaving the auxiliary unit is mixed with a volume of air at ambient temperature and passed to the principal chamber; another part is sent to a heat exchanger in which it gives up part of its thermal energy to a second volume of air at ambient temperature which is heated and introduced into the principal chamber.

Abstract: A contaminant elimination system is disclosed which eliminates (or dramatically reduces) the contaminating components in, for example, exhaust gas from a kiln by enclosing the kiln gas venting channel and processing the exhaust gas by the contaminant eliminator system. This system includes a heating element which is disposed adjacent to the gas venting channel. The heating element is controlled to heat the kiln exhaust gas to a temperature (e.g., 1800.degree.) at which many of the contaminating gases change to a less harmful state. The heated exhaust gas is directed along a winding cooling path where metallic particles in contaminated exhaust gas compounds are plated on relatively cold condensing plates. The cooled exhaust gas is then filtered to trap substantially all remaining airborne metallic or other contaminating particles.

Abstract: The invention relates to a tunnel kiln for fine ceramic products comprizing a heating section, a firing section, and a cooling section, where by means of gas conveying means (10) gases are taken in from the region of said cooling section (140, 176, 182) and are conveyed to said firing section (41, 78, 80, 126, 128), whereby at least one additional burner (132) is arranged in a transition region (130) between said firing section (128) and said cooling section (140).

Abstract: Corrosion and sulfuric acid formation in an integrated spray-drying and calcining operation is inhibited by operating the calciner at a temperature so that the exit gases from the calciner provides sufficient heat to the spray drier to keep the exit gases from the spray drier at a temperature above the dew point of the SO.sub.3 /H.sub.2 O vapors present in the spray drier exit gas.

Abstract: To provide for energy-efficient non-polluting heat treatment of workpieces (W) which, during heat treatment, emit oxidizable or combustible substances, hot gases are generated in a hot gas generating chamber (2) by a jet burner (5) emitting a flame jet. The hot gas generating chamber (2) is connected through a hot gas outlet (7) with a processing chamber retaining the workpieces, and a recirculating inlet (8) to receive the gases from the processing chamber, after they have been contaminated or received polluting combustible components. The hot gas generating chamber is, additionally, in communication through a duct or gap (4) with an after-burner chamber (3).

Abstract: A combustion assembly catalytically oxidizes organic hydrocarbon gases and recovers the heat held by the heated oxidized exhaust generated by such oxidation. The assembly includes a preheater and a catalytic recuperative heat generator which contains a suitable oxidation catalyst. An outside air inlet provides communication between the outside air and the heat generator. The assembly also includes a recirculation duct coupled with a fan which form a loop for storing heated oxidized exhaust for later use, and for moderating temperature losses and gains. A return duct also provides heated oxidized exhaust to the preheater. Variable flow control devices are provided at various positions within the apparatus.

Abstract: A furnace for firing electrically conductive wires clad with an insulating lastics resin, comprising a principal chamber defining a first portion in which evaporation of solvents from the resin takes place and a second portion in which this resin is polymerized and cross linked, and a diffuser element provided with separator means operable to divide the gas stream into a plurality of partial streams and means for distribution and introduction of these partial streams into a peripheral zone of the first portion in a direction substantially parallel to the lateral surface of the first portion itself.

Abstract: Apparatus for the heat treatment of a length of continuously moving material in a plurality of treatment zones contains a fan to provide a stream of circulating air. The outer wall of the machine and fan housing is provided with an opening which can be closed by a closure device, through which the interior of the fan housing and the nozzle casing are accessible.

Abstract: A method of providing an air circulation and exhaust control system for an oven (20) includes an oven enclosure (24) having a conveyor (40) mounted therein for transporting food products through the oven. A plurality of ribbon burners (100) are mounted within the oven interior (32) adjacent the path of the conveyor to heat the interior of the oven. Heated gases generated by operation of the ribbon burners are received through inlet plenums (140) under operation of a circulation fan (146) and are discharged through discharge tubes (154) extending adjacent portions of the conveyor (40) remote from the locations of the ribbon burners (100). Exhaust gases are removed from the oven interior through discharge ports (180) by exhaust blower assemblies (184) which are operated to remove exhaust gases from the oven interior at a rate proportional to the flow rate of combustion air and gaseous fuel into the ribbon burners.

Abstract: The invention relates to a continuous material heating oven ideally suited for sterilizing and depyrogenating materials for introduction to a sterile environment. The oven includes a cool air supply means which is self-deprogenating eliminating the need for manual sterilization. A volumetric airflow control means is included with the cool air supply means for substantially linearly cooling materials to reduce breakage. Control means is provided by the system for maintaining the sterile environment at a greater positive pressure than its adjacent environments to protect the sterile environment from contamination.

Abstract: A system and method for conditioning and recycling inert gases which are used in a plasma furnace. The method comprises the steps of receiving the gas that is output from the plasma furnace and cooling the gas to a desired temperature. Substantially all the dust is removed from the gas and then the gas is compressed to the desired pressure using an oil-flooded screw compressor. Any oil which is introduced by the compressor is removed from the gas and an alarm is provided to signal a high oil level. Substantially all water vapor in the gas is removed and the gas is filtered to remove any remaining dust and small particulates. The amounts of water vapor and oxygen in the gas are monitored. The gas is then recycled to the plasma furnace.

Abstract: The present invention relates to method and apparatus for heating a strip of metallic material in a continuous annealing furnace and more particularly to an improvement relating to a method and apparatus for heating a strip of metallic material in a continuous annealing furnace in which annealing of the strip is continuously carried out in such a manner that a gas, serving to adjust temperature of the strip, is blown toward the strip through a plurality of gas jet nozzles which are arranged on one side or both sides of the strip, wherein the temperature and flow rate of the strip are properly determined to a required level in response to the changing of the operating conditions such as the heat cycle, line speed, thickness of strip, width of strip and the like.

Abstract: Apparatus, and a method for using the apparatus, for detoxifying material contaminated with at least one volatile organic compound (VOC). The apparatus is provided with a dryer having a heat source to heat the VOC-contaminated material to a first temperature, hot enough to volatilize the VOC, but below the cracking temperature of the VOC. The VOC in the dryer is volatilized to form VOC gases. A kiln heats the VOC gases with excess air to a second temperature, hot enough to destroy the organics in the VOC gases. Simultaneously the kiln is used to treat a kiln processable material to form a desired product. The kiln includes means for feeding the kiln processable material to the heating chamber, means for cooling and recovering the desired product, and means for providing heat for the VOC dryer. The apparatus also includes a conduit for conducting the gases containing VOC from the dryer to the kiln.