Lined Hazardous waste incinerator

Abstract: A hazardous waste incinerator (100, 200, 300, 400) is provided herein. The incinerator includes an inner incineration chamber (151, 212, 312, 411) and a separate outer combustion chamber (162, 232, 332, 432). The inner incineration chamber (151, 212, 312, 411) is either formed from, or is lined with, a non-porous, impervious, corrosion-resistant material (153, 216, 323, 417). The inner incineration chamber (151, 212, 312, 411) includes a means (128, 222, 322, 422) for supporting hazardous waste (130) to be incinerated, and a recirculating blower (156, 220, 320, 420). The outer combustion chamber (162, 232, 332, 432) is an insulated chamber and is provided in sealed, spaced-apart relationship to the inner incineration chamber (151, 212, 312, 411). The heat produced in the outer combustion chamber (162, 232, 332, 432) induces incineration of hazardous waste in the inner incineration chamber (151, 212, 312, 411). The outer combustion chamber (162, 232, 332, 432) is in sealed relationship, and does not communicate with, the inner incineration chamber (151, 212, 312, 411). The products of incineration of the hazardous waste from the inner incineration chamber (151, 212, 312, 411) are removed as a stream (158) which is separate and distinct from, and does not mix with, the products of combustion (170) in the combustion chamber.

Description: Technical Field to Which the Invention Relates This invention relates to a hazardous waste incinerator comprising an inner incineration chamber including means for supporting hazardous waste to be incinerated and product of incineration outlet means and an outer combustion chamber in spaced-apart relationship to the inner incinerator. Relevant Background Art, The prior art hazardous waste incinerators with which the present invention is concerned generally include an inner incineration chamber including means for supporting hazardous waste to be incinerated and product of incineration outlet means and an interconnected outer combustion chamber in spaced-apart relationship to the inner incineration chamber. Many patents are directed to such hazardous waste incinerators which included a fuel chamber and a combustion chamber. However, US-A-3 648,629 is considered to represent the most relevant state of the art. This patent discloses a waste incinerator comprising an inner incineration chamber including means for supporting hazardous waste to be incinereated and product of incineration outlet means and an outer combustions chamber in spaced-apart relationship to the inner incineration chamber and including combustion air inlet means and products of combustion outlet means. While many waste disposal problems have been solved by the teachings of the above-identified background art, there are still many improvements which are desirable. In the above patents which taught combustion chambers of the direct-fired type, large volumes of contaminated flue gases were produced which must be processed in a secondary combustion chamber. In the background art waste combustion chambers which could be vented to the atmosphere or to secondary treatment chambers, a high concentration of undesirable toxic pyrolysis products, e.g., dioxins and furans were produced, which had to be further treated. In the background art waste combustion chambers, the problem of non-uniformity of temperature in the incinerator chamber resulted in lack of uniformity of incineration products. Disclosure of the Invention as Claimed The invention as claimed is intended to provide a remedy to the above problems. The invention solves the problems of providing an improved hazardous waste combustion chamber in which the volume of contaminated gases which must be processed in a secondary combustion chamber is greatly reduced; of providing an improved hazardous waste combustion chamber in which the concentration of undesirable toxic pyrolysis products, e.g., dioxins and furans is greatly minimized; and of providing improved hazardous waste combustion chamber in which the temperature within the incineration chamber is uniformly controllable. The invention solves the above problems by means of an inner incineration chamber which is either formed from, or is lined with, a non-porous, impervious, corrosion-resistant material, and is provided with a recirculating blower; and by means of an outer combustion chamber which is in sealed relationship and does not communicate with, the inner incineration chamber. In one embodiment, the hazardous waste incinerator is provided comprising: (i) a base capable of horizontal movement on a transfer car and of vertical movement through the action of an elevator mechanism and including an insulated inverted domed floor which is either made from, or which is lined with, a non-porous, impervious, corrosion-resistant material, and a work support pad; (ii) a stationary, elevated, inner incineration chamber, which is either made from, or which is lined with, a non-porous, impervious, corrosion-resistant liner, the inner incineration chamber including a domed roof, incineration-supporting air inlet means, products of incineration outlet means, and a recirculating blower mounted in the domed roof, the inner, incineration chamber being disposed around the work support pad and the recirculating blower, the inner incineration chamber being in sealable relationship to the base; and (iii) an insulated outer combustion chamber disposed around, and spaced apart from, the inner incineration chamber and being in permanently-sealed relationship to the inner incineration chamber to provide a combustion zone therebetween, the outer combustion chamber being provided with fuel inlet means, combustion air inlet means and products of combustion outlet means; the outer combustion chamber being in sealed relationship and non-communicating with, the inner incineration chamber. By another embodiment of this invention, the hazardous waste incinerator includes: (i) a base supported on a pedestal; (ii) a pad support, incineration-supporting air inlet means, and products of incineration outlet means, and a recirculating blower mounted on the base; (iii) an inner incineration chamber which is either formed from, or which is lined with, a non-porous, impervious, corrosion-resistant material, the inner incineration chamber enclosing and being disposed around the pad support, the incineration-supporting air inlet means, the products of incineration outlet means, and the recirculating blower, the inner incineration chamber being in sealed relationship to the base; and (iv) an insulated outer combustion chamber disposed around the inner incineration chamber, and being in sealed relationship to the base, the outer combustion chamber being provided with fuel inlet means, combustion air inlet means and products of combustion outlet means; the outer combustion chamber being in sealed relationship, and non-communicating with, the inner incineration chamber. By yet another embodiment of this invention, the hazardous waste incinerator includes: (i) an open-topped shell in the form of an insulated outer combustion chamber provided with fuel inlet means, combustion air inlet means, and combustion products outlet means; (ii) a pedestal supporting the outer combustion chamber; (iii) an upper support resting atop the open-topped vessel, thereby closing-off the open-topped shell, the upper support supporting a suspended inner incineration chamber which is either made from, or which is lined with, a non-porous, impervious, corrosion-resistant material, and having a floor, the floor being provided with an incineration-supporting air inlet means, products of incineration outlet means and a recirculating blower; and (iv) a roof for the suspended inner incinerator chamber, the roof supporting a suspended pad support, and an upper rim resting atop and in sealed relationship with the upper support; the outer combustion chamber being in sealed relationship and non-communicating with, the inner incineration chamber. By still another embodiment of this invention, the hazardous waste incinerator includes: (i) an insulated rectangular parallelepiped shell having a vertically-movable front door, and providing an outer combustion chamber, the outer combustion chamber being provided with fuel inlet means, combustion air inlet means and products of combustion outlet means; (ii) an inner incineration chamber which is either formed from, or which is lined with, a non-porous, impervious, corrosion-resistant material, the inner incineration chamber also being provided with ambient air incineration-supporting air inlet means, products of incineration outlet means and a recirculating blower; and (iii) a false wall disposed interiorly of the inner incineration chamber resting on a pad support, the false wall being provided with a plurality of apertures; the outer combustion chamber being in sealed relationship and non-communicating with, the inner incineration chamber. In these embodiments, the seals at the base preferably comprise "O"-ring seals provided with recirculation coolant means. The incineration-supporting air preferably passes through the gap formed between the inner combustion chamber and the base and is bounded on its outer periphery by the "O"-ring seal. The products of incineration outlet means passes through the walls of the incineration chamber and the walls of the outer combustion chamber and is concentric with the products of combustion outlet means. The products of combustion outlet means passes through the wall of the outer combustion chamber. The base preferably is vertically movable from the inner incineration chamber to reveal the work support pad. The base preferably is horizontally movable from below the inner incineration chamber to provide ready access to the work support pad. The outer combustion chamber preferably is vertically-movable from the base to reveal the inner incineration chamber, the inner incinerator chamber being vertically-movable to expose the pad support. The roof of the inner incineration chamber preferably is domed and is insulated behind the impervious corrosion-resistant liner. The roof of the inner incineration chamber is preferably vertically-movable to expose the suspended pad. It is preferred that the false wall rest on a plurality of "T"-shaped pad supports, and/or that the false wall conceal electrical heaters. By another embodiment of this invention, a method is provided for incinerating hazardous waste including the steps of providing of an outer, heat-producing zone, providing an inner incineration zone in which a charge of hazardous waste is fed only to the inner incineration zone, and heating the inner incineration zone by means of heat from the outer heat-producing zone, and including the essential steps of: providing the exposed surfaces of the inner incineration zone as a non-porous, impervious, corrosion-resistant, surface; providing the inner incineration zone in sealed, spaced-apart and heat-conducting relation to the outer, heat-producing zone; withdrawing products of combustion from the outer heat-producing zone; and withdrawing products of incineration from the inner incineration zone; the products of incineration which are being separate and distinct from, and is not being mixed with, the products of combustion from the outer heat-producing zone. In general terms, one specific embodiment of the hazardous waste incinerator includes, as a first essential part, a base which is capable of horizontal movement, e.g. on a transfer car having wheels rolling on a track. The base is also capable of vertical movement through the action of some type of elevator mechanism. The base is provided with an insulated, impervious non-porous, corrosion-resistant inverted domed floor, or an insulated, inverted domed floor which is lined with a non-porous, impervious corrosion-resistant liner. The base also includes a work support pad. A second essential part of such hazardous waste incinerator includes a stationary, elevated, impervious non-porous, corrosion-resistant inner incineration chamber or a stationary, elevated, incineration-chamber which is lined with an impervious, non-porous, corrosion-resistant liner. The elevated incineration-chamber is provided with a domed roof. It also includes an incineration-supporting air inlet and products of incineration outlet. A recirculating blower mounted in the domed roof is capable of generating a highly turbulent motion of gases in the inner incineration chamber, a controlled inlet port to permit flow of makeup incineration-supporting air into the inner incineration chamber at a rate which will maintain the desired oxygen concentration in the effluent gas, a products of incineration gas outlet port and sealed ducting to a secondary stage of incineration, a water-cooled seal around the periphery of the inner incineration chamber, and a pad for support of the transformer fragments. A third essential part of such incinerator includes a stationary, elevated, insulated, outer combustion chamber enclosing the inner incinerator chamber. Burners or electric heating elements are associated with the outer combustion chamber, designed for rapid heat release in the annulus formed between the incinerator chamber and the combustion chamber. This heat is then transferred, by radiation and convection, to the circulating gases in the incineration chamber and, ultimately, to the transformer fragments. All fuel, air and combustion gases emerging from the annulus are separately ducted away from the unit and precluded from mixing with the gases in the inner incineration chamber. An inducted draft is induced in the inner incineration chamber to ensure operation at a controlled, negative pressure, thereby substantially preventing the escape of hazardous, or otherwise noxious, gaseous chemical constituents. The necessary mechanisms, cables, rails, pulleys, gears and motors to permit access to and guided movement of the elements of the system are also provided. When in operative association, the inner incineration chamber is disposed around the work support rod and the recirculating blower, with the inner incineration chamber being in sealed relationship to the base. An insulated outer combustion chamber is disposed around and in a spaced-apart relationship from the inner incineration chamber to provide a combustion zone therebetween. The insulated outer combustion chamber is in permanently sealed relationship to the inner chamber. The outer combustion chamber is provided with a fuel inlet, with a combustion air inlet and with a product of combustion outlet. The base and the inner incineration chamber are each constructed of, or are lined with, a material which is impervious to the gases which are formed during the incineration, which is capable of withstanding temperatures of at least 1100°C, and which is resistant to high-temperature corrosive attack by acid gases, in particular HCl. Materials of construction include, but are not limited to HAYNES ALLOY HR160 (Registered Trade-mark), or a solid ceramic, e.g. silicon carbide, or a ceramic-coated, high-temperature-alloy steel. A second embodiment of the hazardous waste incinerator includes an internally-insulated, outer, bell-shaped chamber, open at the bottom and free of obstructions. An inner, bell-shaped incineration chamber, also open on the bottom is also provided, which is capable of forming a seal around the periphery of the opening. It is constructed of a material which is impervious to the gases which are formed during the incineration, which is capable of withstanding temperatures of at least 1100°C, and which is resistant, at least on its inner surface, to high-temperature, corrosive attack by acid gases, in particular HCl. Materials of construction may include, but are not limited to, HAYNES ALLOY HR160 (Registered Trade-mark), or a solid ceramic, e.g., silicon carbide, or a ceramic-coated, high-temperature alloy steel. The inner bell may be a separate element or may be integrally-mounted to the outer, heating chamber. A pedestal-type platform is also provided which is equipped with a recirculating blower capable of generating a highly turbulent motion of gases in the inner incineration chamber, a controlled inlet port to permit flow of incineration-supporting makeup air into the incineration chamber at a rate which will maintain the desired oxygen concentration in the effluent gas, a products of incineration gas outlet port and sealed ducting to a secondary stage of incineration, a water-cooled seal around the periphery of the inner incineration chamber, and a pad for support of the transformer fragments. Burners or electric heating elements are associated with the outer chamber, designed for rapid heat release in the annulus formed between the incineration chamber and the combustion chamber. This heat is then transferred, by radiation and convection, to the circulating gases in the incineration chamber and, ultimately, to the transformer fragments. All fuel, air and combustion gases emerging from the annulus are separately ducted away from the unit and precluded from mixing with the gases in the inner incineration chamber. An inducted draft is induced in the inner incineration chamber to ensure operation at a controlled, negative pressure, thereby substantially preventing the escape of hazardous, or otherwise noxious, gaseous chemical constituents. The necessary mechanisms, cables, rails, pulleys, gears and motors to permit access to and guided movement of the elements of the system are also provided. A third embodiment of the hazardous waste incinerator is similar to the second embodiment described above, except that the bells are inverted and are integrally-mounted to form a single unit comprising a central incineration chamber cavity and an annular heating chamber. The double bell unit is held stationary while the transformer fragment support pad is suspended below a movable lid which, when lowered into engagement with the double bell unit, forms a seal for the incineration chamber. All ducts, heating elements and air intakes are associated with the stationary components. A fourth embodiment of the hazardous waste incinerator, consists of an insulated chamber, totally enclosed except for one end wall which is completely open and free of obstructions. An inner, impervious lining, which may be either a metal (e.g., HAYNES ALLOY HR160) or ceramic-coated alloy steel or a ceramic (e.g., silicon carbide), which is sealed at all joints to preclude the escape of any vapours, and which is sufficiently resistant to chemical attack at high temperature to endure exposure to the inner incineration chamber environment encountered during operation. An insulated door is provided as the third element, which is lined on the inner surface, which fully covers the end wall opening, which is equipped with the necessary seals and pressuring mechanisms to create an air-tight seal at the periphery of the inner incineration chamber opening and which is provided with the cables, rails, gears, pulleys and motors to permit guided vertical or horizontal movement away from the opening. A recirculating blower is provided as the fourth element, to ensure highly turbulent movement of the gases in the incineration chamber, thereby ensuring a high heat transfer rate between the heating elements and the load under treatment, as well as satisfactory mixing of incineration-supporting air and combustible organics evolved from the load. A number of electric or fire tube heating elements are provided which extend into the outer combustion chamber. In the latter instance, all of the fuel, air and combustion gases present in the fire tubes are separately ducted away from the unit, and are precluded from mixing with the gases in the inner incineration chamber. The heating elements may be integral with the wall or may be freely suspended. Moreover they may be horizontally- or vertically-oriented. Appropriate baffles, deflectors and false walls and ceiling are provided to control the path of the circulating gases in the incineration chamber, thereby ensuring a uniform chamber temperature and enhanced heat transfer between the heating elements and the load under treatment. The lower section of the deflector mechanism also provides protection of the lining against physical damage during loading and unloading of the incinerator. Means are included for providing an induced draft in the incineration chamber to ensure operation at a controlled negative pressure, thereby preventing the escape of hazardous, or otherwise noxious, gaseous chemical constituents. Control louvres are provided to permit flow of makeup air into the incineration chamber at a rate which will maintain the desired oxygen concentration in the effluent gases. Finally, sealed heat traced ducting is provided to transport the gases from the incineration chamber to a high temperature, secondary combustion chamber which will ensure the complete destruction of residual hazardous contaminants. Advantageous Effects of the Invention There are many advantages offered by the present invention. The present invention in its broad aspect provides a sealed incineration chamber having an impervious, high-temperature, corrosion-resistant internal surface, either as a separate structural element or as a liner within the inner incineration chamber. This represents a major improvement over the existing technology, since it precludes the commonly experienced diffusion of the high boiling, hazardous constituents, e.g., PCB's, dioxins and furans, into and through conventional ceramic linings. The escape of these materials has, in several instances, resulted in severe contamination of the surrounding environment. The invention provides separate, non-interconnected inner incineration and outer indirect heating zones. Whereas incineration normally implies direct firing of the fuel within the same chamber as the contaminated charge, indirect firing, (referred to as roasting), is peculiar to systems employed in vaporization and pyrolysis. By this invention, however, several significant benefits are provided, including: a substantial reduction in the volume of contaminated gases, when compared with the direct fired system, which must be processed in the secondary combustion chamber; a reduction in the number and concentration of undesirable, toxic pyrolysis products, e.g., dioxins and furans, when compared with a roaster; improved uniformity of temperature in the incineration chamber when compared with either of the traditional approaches; fuel, air and combustion gases emerging from the annulus are separately ducted away from the unit and precluded from mixing with the gases in the incineration chamber; and inducted draft is induced in the incineration chamber to ensure operation at a controlled, negative pressure, thereby substantially preventing the escape of hazardous, or other noxious, gaseous chemical constituents. Thus, the present invention provides a method and apparatus for the containment and incineration of hazardous organic solids and liquids. One specific adaptation of the invention applies to the decontamination of ASKAREL- and PCB-contaminated electrical transformers and capacitors. Brief Description of the Figures of the Drawings Several ways of carrying out the invention are described in detail below with reference to drawings which illustrate several specific embodiments, in which: Figure 1 is a central longitudinal cross-section through one embodiment of the hazardous waste incinerator of this invention; Figure 2 is a central longitudinal cross-section through a second embodiment of the hazardous waste incinerator of this invention; Figure 3 is a central longitudinal cross-section through a third embodiment of the hazardous waste incinerator of the apparatus aspect of this invention; Figure 4 is a front isometric view of a fourth embodiment of the hazardous waste incinerator of the apparatus aspect of this invention; Figure 5 is a core segment thermal response data graph showing temperature in degrees C as ordinate and time elapsed in minutes as abscissa; Figure 6 is a core segment thermal response simulation graph showing temperatures in degrees C as ordinate and time elapsed in minutes as abscissa; and Figure 7 is a time to temperature vs. centre distance graph showing the correlation between time to temperature in hours as ordinate and centre distance in inches as abscissa. Description Of At Least One Way of Carrying Out the Invention As seen in Figure 1, mounted within a generally rectangular parallelpiped open framework 110 is a hazardous waste incinerator 100 of a first preferred embodiment of this invention which includes a lower base section 120 and an upper combustion section 150. The lower base section 120 includes an open topped chamber 122 including an outer floor 124 having an inverted dome-shaped insulation 126 thereon, the upper exposed surface of such insulation being covered with an impervious, non-porous and corrosion resistant liner 127. The lower base section 120 is mounted on a transfer car 112 having wheels 114 rolling on rails 116. The transfer car 112 is engageable by an elevator 118, vertically moveably-mounted on the vertical posts 111 of the open framework 110. The open-topped chamber 122 is provided with a work support pad 128 to support a load 130 to be incinerated. The exposed peripheral or perimetral upper surfaces on rim 132 of the open-topped chamber 122 includes a liquid-cooled "O"-ring seal 134 fed with liquid coolant circulating therethrough via inlet line 136 and outlet line 138. The upper combustion section 150 is stationary and is elevated. The inner incinerator chamber 151 of this upper combustion section 150 has an exposed inner surface 153 which is either formed from, or is line with an impervious, non-porous and corrosion-resistant material. The inner incineration chamber 151 is provided with a domed roof 152. Descending through a sealed aperture 154 in the domed roof 152 is a recirculating blower 156 which inducts the incineration products upwardly in the central core, as shown by the "up" arrows, and discharges them downwardly along the sidewalls as shown by the "down" arrows. The products of incineration from within the inner incineration chamber 151 are vented or expelled through flue or outlet 158. The inner incineration chamber 151 is surrounded by a heat-insulated outer combustion chamber 160 formed of steel lined with a refractory material. The outer combustion chamber 160 is provided in permanently sealed relationship to the inner incineration chamber 151 to provide a combustion zone 162 therebetween. The outer combustion chamber 160 is provided with suitable burners 164, which are arrayed around the outer combustion chamber, and which may be either fuel oil burners fed with fuel oil through fuel oil inlet lines 166, or gas burners fed with gas through gas inlet line 166. The fuel is mixed with combustion air at the burners 164. The relatively clean products of combustion produced in combustion zone 162 are expelled through combustion chamber flue 170 which is concentric with incinerator chamber flue 158. The lower peripheral rim 172 of the upper chamber is provided with a liquid coolent for the "O"-ring seals 134 which is fed with liquid-coolent circulating therethrough, via inlet line 176 and outlet line 178. In its operative position, the rims 132 and 172 are in sealing contact with one another through "O"-ring seal 134 and form a gap through which the incineration air enters the incineration chamber 151. As seen in Figure 2, the hazardous waste incinerator 200 is supported on a circular base platform 202 which is situated atop a hollow cylindrical pedestal 204 supported on the ground 206. Supported in sealing engagement with an inner, liquid cooled "O"-ring seal 208 is the annular rim 210 of an inner incineration chamber 212, which is formed of and/or may be lined with non-porous, impervious, corrosion-resistant material 214 as previously described in the general description of the invention. The inner incineration chamber 212 is provided with a domed roof 216 and is surmounted by an eye 218 in order to be able to raise and lower (as shown by the double arrow) the inner incineration chamber 212 by means (not shown) which are well-known to those skilled in the art. Within the inner incineration chamber 212 and resting on a hollow cylindrical vented support 220 is a pad support 222. Within the hollow cylindrical vented support 220 is a recirculatory blower (not seen), which draws up incineration-supporting air through inlet conduit 224 and expels products of incineration through exhaust conduit 225, for discharge to a secondary combustion chamber (not shown) of known construction which forms no part of the present invention. Supported in sealing engagement with an outer, liquid cooled "O"-ring seal 226 is the annular base 228 of an outer combustion chamber 230, which is spaced-apart from the inner incineration chamber by a surrounding combustion zone 232. The outer combustion chamber 230 is provided with heat insulation 234, as previously described in the general description of the invention. The outer combustion chamber 230 is provided with a domed roof 236 and is surmounted by an eye 238 in order to be able to raise and lower (as shown by the double arrow) the outer combustion chamber 230 by means (not shown) well-known to those skilled in the art. The outer combustion chamber 230 is provided with a burner 240, either a fuel oil burner fed with fuel oil through fuel inlet line 242, or a gas burner fed with gas through fuel inlet line 242. The burner is also fed with combustion air through air inlet line 244. The relatively clean products of combustion produced in the combustion zone 232 are expelled through flue gas outlet conduit 246. "O"-ring seals 208 and 226 are cooled with liquid coolant circulating through the platform 202 and inlet line 248 and outlet line 250. The outer combustion chamber 230 and the inner incineration chamber 212 may be combined into an integrated component by replacing the separate annular ring 210 of the incineration chamber 212 and the annular base 228 of the combustion chamber 230 with a single common ring mounted in permanent sealing engagement with both chambers. As seen in Figure 3, the hazardous waste incinerator 300 includes an outer combustion chamber 330 having a lower circular base platform 302 which is situated atop a hollow cylindrical pedestal 304 supported on the ground 306. The outer combustion chamber 330 is provided with a heat insulation 334, as previously described in the general description the invention. The outer combustion chamber 330 is also provided with a burner 340, either a fuel oil burner fed with fuel oil through fuel inlet line 342, or a gas burner fed with gas through fuel inlet line 342. The burner is also fed with combustion air through air inlet line 344. The relatively clean products of combustion produced in the combustion zone 332 is expelled through flue gas outlet conduit 346. An inner incineration chamber 312 is secured to, and suspended within, outer combustion chamber 330 by annular rim 310 fixed to the upper rim 327 of the outer combustion chamber 330. The inner incineration chamber 312 is heat-resistant and is either formed from or is provided with, a non-porous, impervious corrosion-resistant, liner 314. The zone surrounding the inner incinerator chamber 312, as far as the insulation 334 of the outer combustion chamber 330, provides a combustion zone 332. Supported in sealing engagement with a liquid cooled "O"-ring seal 326 on the annular rim 310 is the annular base 328 of the domed roof 316 of the inner incineration chamber 312. The domed roof 316 is provided with insulation 317 which is isolated from the inner incineration chamber atmosphere by the non-porous impervious, corrosion-resistant liner 319. The outer face of the domed roof 316 is surmounted by an eye 318 in order to raise and lower (as shown by double arrows) the roof 316. Resting on the base of the inner incineration chamber 312 is a vented support 320 within which is a recirculating blower (not seen) which draws up incineration-supporting air through inlet conduit 324, and expels the products of incineration through exhaust conduit 325 for discharge to a secondary combustion chamber (not shown) of known construction which forms no part of the present invention. A pad support 322 is suspended from the interior of the domed roof 316 by means of a plurality of suspension rods 323. "O"-ring seals 326 are cooled with liquid coolant circulating through the annular ring 310 via inlet line 348 and outlet line 350. As seen in Figure 4, the hazardous waste incinerator 400 is in the form of a generally rectangular parallelepiped 410 having an open front 411 provided with a vertically-sliding door 412 (shown by the double arrow), which is in sliding-sealed-engagement with vertical slots 413 in the open front, as previously described. The interior walls thereof are provided with heat insulation 434 to provide an outer combustion chamber 430. Suspended from the interior of the roof 416 of the parallelepiped 410 is an inner incineration chamber 414, which is either formed from or is provided with an non-porous, impervious combustion-resistant material 415. The inner incineration chamber 414 is separated from the outer combustion chamber 430 in order to provide a combustion zone 432 therebetween. To provide combustion, a plurality of burners 440 may be provided, which are fed with a fuel/ air mixture through inlet line 442. Alternatively, a plurality of vertically-arranged, electrically-heated fire tube exchangers 443 may be provided to form the combustion zone. The products of combustion are withdrawn by outlet line 446 to a flue stack. Within the inner incinerator chamber 414 is a false wall 417 provided with a plurality of apertures 419. The bottom 421 of the false wall rests on a pair of horizontally-oriented "T"-beams 423 to provide a pad support 422. A recirculating blower 420 is provided on the outer roof 416, the blower serving to circulate ambient air as incineration-supporting air, and vents products of incineration to a secondary combustion chamber through exhaust conduit 425. The batch transformer decontamination furnace has been subjected to preliminary, theoretical and/or experimental testing to provide evidence to confirm that the system will function reliably under the imposed operating conditions and will achieve the desired level of metal decontamination and reclamation in a cost effective manner. It has been found that the following are of particular concern, namely: an appropriate metal or internal lining material for the furnace should be selected which is impervious to diffusion of hazardous vapour emissions, capable of withstanding high temperature corrosive chemical attack and sufficiently durable to survive the levels of abuse normally encountered in service; an incinerator air recirculating system must be provided which will ensure efficient heat transfer between the externally-fired heat exchanger and the transformer components and which will provide the oxygen required for combustion of the various primary organic constituents and pyrolysis products emanating from the transformer carcass; the minimum time required to elevate the temperature of the most remote internal regions of the core to the desired level, and the time and temperature required to ensure complete removal of the noxious organic materials from transformer components must be accurately determined. An experimental evaluation of the efficacy of this method, with the aid of a batch-type kiln, has demonstrated that the transformer core fragments can be adequately decontaminated, at acceptable temperature levels and in a reasonable period of time. The results of this evaluation and an experimentally-verified mathematical model of the response of the centre-core temperature, are now provided. A series of experiments were conducted with the aid of a Von Roll kiln at the plant site, operating in the stationary mode to simulate the proposed transformer decontamination facility, in order to determine the furnace temperature and treatment period required to achieve a residual PCB contaminant level of less than 2 ppm. (It should be noted that the specification is considerably below the 50 ppm concentration permitted in most political jurisdictions for landfilling of decontaminated transformers. However, since it is intended to recycle the recovered metals, it is essential that the residuals be considered acceptable by potential purchasers of the salvage). The experiments were also designed to establish a theoretically-based, empirical correlation between the properties and dimensions of the core and the time required to achieve the specified temperature at the most remote location within the core. This correlation must be structured in such a form as to permit the reliable estimation of the treatment time required for any core segment of known properties and dimensions. EXPERIMENTAL PROCEDURE A) With respect to the first objective, a number of transformer cores of various sizes were extracted from drained transformer casings, bisected, and treated in the kiln for periods of time ranging from 90 minutes to 180 minutes. Samples obtained from the cores, both before and after treatment, were subjected to a standard laboratory analysis to determine the PCB removal efficiency affected by the thermal treatment. The results obtained from those experiments which were concerned with the speed and extent of PCB removal are presented below in Table 1. These results suggest that: (i) For core segments, ranging in weight from 4 to 30 kg, exposure to a temperature of approximately 1000°C for a period exceeding 90 minutes is sufficient to affect a reduction in PCB concentration to prescribed levels, regardless of the initial concentration; and (ii) The residual contamination, following thermal treatment, appears to be more dependent upon the configuration of the core segment than on the initial PCB concentration. Thus, most probably as a consequence of its densely packed structure, segment No. 87-307B, which is among the smallest of the group treated, exhibits the highest residual PCB contamination. B) In order to secure the data required for the development of a dynamic thermal response model, a thermocouple, installed at the centre of a core segment, was used to measure the temperature transient when the segment, initially at a temperature of 27°C, was inserted into the preheated, stationary kiln and, thereby, subjected to a step change in ambient temperature to approximately 965°C. The rather unusual, bi-modal temperature response recorded at the centre of the thermocouple-equipped, core segment is depicted in Figure 5. The initial, steep temperature rise and first maximum are likely due to the rapid combustion of the paper laminations and associated organic liquids characterized by relatively low ignition temperatures. It might be expected that a considerable portion of the less strongly adsorbed PCB would be vaporized during this phase. The thermal response of the metallic bulk of the core segment is most accurately described by that region of the curve which extends to the right, beyond approximately 10 minutes of elapsed treatment time, and which might be extrapolated toward the origin, at the left, in a continuous downward fashion. Based on smoothed data derived from Figure 5, it is possible to develop an entirely empirical relationship which would be useful in predicting the response of similar core segments, provided that differences in size and configuration were small. A more satisfactory approach involves development of a predictive model, based on theoretical considerations, which can then be evaluated through comparison with the measured response. It is this latter strategy which has been chosen and which will now be described. If it assumed that surface resistance to heat transfer is small, the general differential equation for transient heat conduction, derived from the basic Fourier equation, when combined with a heat balance and applied to the core segment geometry, which may be adequately described as comprising an infinite slab (characterized by a very large ratio of heat transfer surface area to core thickness), may be solved to yield a rapidly converging infinite series of the form: where: t x = instantaneous temperature at the mid-point of the core segment. t f = final temperature at the mid-point (assumed to be 750°C on the basis of the extrapolated curve) ti = initial core segment temperature (27°C) ϑ = time since insertion of core segment into kiln α = thermal diffusivity of solid ( κ ρ Cp ) where: κ = thermal conductivity ρ = density Cp = specific heat x = distance from the heat transfer surfaces to the mid-point of the core (2.54 cm = one inch) If it is, reasonably, assumed that the resistance to heat transfer is primarily within the laminations between the copper coils and that the laminations consist primarily of flakes of charcoal after the initial combustion phase, the thermal diffusivity may be approximated on the basis of the following properties of charcoal: Thus, since : κ = 0.088 w/mK (0.051 BTU (ft)/hr (°F) ft²) and ρ = 240.27 kg/m³ (15 lbs/ft³) and Cp = 1.005 KJ/KgK (0.24 BTU/lb (°F)) the thermal diffusivity is : α = 3.613 x 10⁻⁷ m²/s (1.4 E-2 Ft²/hr) Following substitution of the known parameters, the foregoing equation may be reduced to the form: The indicated relationship between mid-point temperature and elapsed time is plotted on Figure 6, and demonstrates the remarkable correlation between the actual and theoretically predicted response over the time period of particular interest. Having confirmed the validity of the mathematical model, it is now desirable to rearrange the equation in the following form: where: F = the fraction of the total mid-point temperature rise attained at time ϑ = t x - ti t f - ti which permits calculation the time required to achieve any desired fraction of the total temperature rise at the midpoint of a core segment of thickness, 2x. For convenience, this relationship may be plotted, at selected fractional temperature rises, as illustrated in Figure 7. While it is unlikely that the thermal diffusivity of the complex core matrix is precisely that of powdered charcoal, it is surprising that there is this apparent accuracy. However, from a practical point of view, the utility of the correlation is fortuitous. In view of the excellent correspondence of the shape of predicted and actual response curves, the form of the mathematical model appears appropriate and the thermal diffusivity, α, may be considered as purely an empirically-derived coefficient. Way in Which Invention Is Capable of Exploitation By Industry The use of the apparatus of this invention is as follows: In preparation for charging a transformer to the incinerator, the transformer is disassembled by removal of the core from the casing. A large core may be bisected or even further reduced in size to facilitate heat transfer and the escape and oxidation of the organic components, e.g., PCB's, mineral oils, and the paper laminations. The transformer casing and the various core fragments are then loaded on the pad and, depending on the incineration configurations adopted, either deposited on the work support pad, or on the pedestal platform or inserted into the rectangular incinerator by means of a fork lift truck, or other suitable transporting mechanism. The incineration chamber is then closed. With the elevator system (shown in Figure 1) this is accomplished by moving the base upwardly to achieve sealing engagement with the upper, stationary bell and combustion chamber section. With the bell-shaped system (shown in Figure 2), this is accomplished by placing the inner and outer bells into sealing engagement with the pedestal. With the inverted, bell-shaped, system (shown in Figure 3), this is accomplished by lowering the domed roof to achieve sealing engagement with the annular rim of the incineration chamber. The incineration chamber of the rectangular incineration (shown in Figure 4) is secured by closing and sealing the door. The heating elements are activated and the recirculating blower is set into motion. The temperature of the furnace is controlled through manipulation of the energy input to the heating elements and is maintained at a level below the melting temperature of the metallic components in the charge (i.e., less than 1000°C). The flow rate of combustion air through the incineration chamber is controlled to maintain the desired oxygen content in the effluent to the secondary combustion chamber. There should be very efficient circulation of such air to provide turbulent mixing. Suitable flow rates are between 2832 and 5664 L/minute (10,000 and 20,000 c.f./minute) for an incineration chamber of approximately 2.83 cubic meters volume (100 cubic feet volume). The oxygen content of the exhaust from the incineration chamber is desirably from 5 - 15% by volume. The transformer components are allowed to remain in the incinerator for a length of time which is sufficient to attain the centre-core temperature required to affect virtually complete destruction and/or removal of all organic constituents. While the time required will depend on the size and configuration of the core and the centre-core temperature desired, it will generally range from 90 minutes to 240 minutes.

Claims: A hazardous waste incinerator (110, 200, 300, 400) comprising an inner incineration chamber (151, 212, 312, 411) including means (128, 222, 322, 422) for supporting hazardous waste to be incinerated and product of incineration outlet means (158, 225, 325, 425), and an outer combustion chamber (162, 232, 332, 432) in spaced-apart relationship to said inner incineration chamber (151, 212, 312, 411) and including combustion air inlet means (154, 244, 344) and products of combustion outlet means (170, 246, 346, 446), characterized in that said inner incineration chamber (151, 212, 312, 411) is constituted by a chamber which is either formed from, or is lined with, a non-porous, impervious, corrosion-resistant material (153, 216, 323, 417) and is provided with a recirculating blower, and said outer combustion chamber (162, 232, 332, 432) is in sealed relationship to, and does not communicate with, said inner incineration chamber (151, 212, 312, 411). The hazardous waste incinerator of claim 1 characterized by : (i) a base (120) capable of horizontal movement on a transfer car (112) and of vertical movement through the action of an elevator mechanism (118) and including an insulated inverted domed floor (126) which is either made from, or which is lined with, a non-porous, impervious, corrosion-resistant material (127), and a work support pad (128); (ii) a stationary, elevated, inner incineration chamber (151), which is either made from, or which is lined with, a non-porous, impervious, corrosion-resistant liner (153), said inner incineration chamber including a domed roof (152), incineration-supporting air inlet means (gap at 134), products of incineration outlet means (158), and a recirculating blower (156) mounted in said domed roof (152), said inner, incineration chamber (151) being disposed around said work support pad (128) and said recirculating blower (156), said inner incineration chamber (151) being in sealable relationship (134) to said base (120); and (iii) an insulated outer combustion chamber (160) disposed around, and spaced apart from, said inner incineration chamber (151) and being in permanently-sealed relationship to said inner incineration chamber (151) to provide a combustion zone (162) therebetween, said outer combustion chamber (160) being provided with fuel inlet means (166), combustion air inlet means (164) and products of combustion outlet means (170); and said outer combustion chamber (160) is in sealed relationship to, and does not communicate with, said inner incineration chamber (151). The hazardous waste incinerator of claim 1 characterized by : (i) a base (202) supported on a pedestal (204); (ii) a pad support (222), incineration-supporting air inlet means (224), products of incineration outlet means (225), and a recirculating blower (in 220) mounted on said base (202); (iii) an inner incineration chamber (212) which is either formed from, or which is lined with, a non-porous, impervious, corrosion-resistant material (214), said inner incineration chamber (212) enclosing, and being disposed around, said pad support (222), said incineration-supporting air inlet means (224), said products of incineration outlet means (225), and said recirculating blower (in 220), said inner incineration chamber (212) being in sealed relationship to said base (210, 208); and (iv) an insulated outer combustion chamber (230) disposed around said inner incineration chamber (212), and being in sealed relationship to said base (202), said outer combustion chamber (230) being provided with fuel inlet means (242), combustion air inlet means (244) and products of combustion outlet means (246); and said outer combustion chamber (232) is in sealed relationship to, and does not communicate with, said inner incineration chamber (212). The hazardous waste incinerator of claim 1 characterized by: (i) an open-topped shell in the form of an insulated outer combustion chamber (330) provided with fuel inlet means (342), combustion air inlet means (344), and combustion products outlet means (346); (ii) a pedestal (304) supporting said outer combustion chamber (330); (iii) an upper support (310) resting atop said open-topped vessel, thereby closing-off said open-topped shell, said upper support (316) supporting a suspended inner incineration chamber (312) which is either made from, or which is lined with, a non-porous, impervious, corrosion-resistant material (314), and having a floor, said floor being provided with an incineration-supporting air inlet means (324), products of incineration outlet means (325) and a recirculating blower (in 320); and (iv) a roof (316) for said suspended inner incinerator chamber, said roof (316) supporting a suspended pad support (322), and an upper rim (328) resting atop and in sealed relationship with said upper support (310); and said outer combustion chamber (332) is in sealed relationship to, and does not communicate with, said inner incineration chamber (312). The hazardous waste incinerator of claim 1, characterized by: (i) an insulated rectangular parallelepiped shell (410) having a vertically-movable front door (412), and providing an outer combustion chamber (430), said outer combustion chamber (430) being provided with fuel inlet means (442), combustion air inlet means (442) and products of combustion outlet means (446); (ii) an inner incineration chamber (414) which is either formed from, or which is lined with, a non-porous, impervious, corrosion-resistant material (415), said inner incineration chamber (414) also being provided with ambient air incineration-supporting air inlet means, products of incineration outlet means (425) and a recirculating blower (420); and (iii) a false wall (417) disposed interiorly of said inner incineration chamber (414) resting on a pad support (422), said false wall (417) being provided with a plurality of apertures (419); and said outer combustion chamber (432) is in sealed relationship to, and does not communicate with, said inner incineration chamber (411). The hazardous waste incinerator of claims 2 to 4 inclusive, characterized in that said seals at said base (120, 202) includes "O"-ring seals (134, 208) provided with recirculation coolant means (176 and 178, 248 and 250). The hazardous waste incinerator of claims 2 to 4 inclusive, characterized in that said seals at said upper support (304) comprise "O"-ring seals (326) provided with recirculation coolant means (348 and 350). The hazardous waste incinerator of claims 2, 6 or 7 characterized in that said incineration-supporting air inlet passes through a gap formed between said inner chamber (151) and said base (120), and bordered on its outer periphery by an "O"-ring seal (134). The hazardous waste incinerator of claims 2, 6 or 7 characterized in that said incineration air inlet means passes through said pedestal (204, 304). The hazardous waste incinerator of claims 2, or 6 to 9 inclusive, characterized in that the products of incineration outlet means (158) passes through walls of said inner incineration chamber (151) and through the walls of the outer combustion chamber (160) and is concentric with the products of combustion outlet means (170). The hazardous waste incinerator of claims 2, or 6 to 9 inclusive, characterized in that said products of incineration outlet means (225, 325) passes through said base (202, 302). The hazardous waste incinerator of claims 2, or 6 to 11 inclusive, characterized in that the products of combustion outlet means (246, 346) passes through walls of said outer combustion chamber (234, 334) and forms an annular combustion gas duct (246, 346). The hazardous waste incinerator of claims 2 to 4 and 6 to 12 inclusive, characterized in that said inner incineration chamber (151, 212, 312) has a roof which is domed (152, 216, 319) and is insulated (317) behind a non-porous impervious, corrosion-resistant liner (319). The hazardous waste incinerator of claims 2 to 4 and 6 to 13 inclusive, characterized in that said inner incinerator chamber (212, 312) and said outer combustion chamber (234, 334) each have an upper domed roof (216 and 236, 319 and 316). The hazardous waste incinerator of claims 2 to 4 and 6 to 13 inclusive, characterized in that said inner incinerator chamber (151) is vertically-movable to expose said pad support (120) and said outer chamber (160) is vertically-movable from said base (120) to reveal said inner incineration chamber (151). The hazardous waste incinerator of claims 2 to 4 and 6 to 13 inclusive, characterized in that said inner incinerator chamber (212) has a roof (216) which is vertically-movable to expose pad support (222). The hazardous waste incinerator of claims 2 to 4 and 6 to 13 inclusive, characterized in that said inner incineration chamber (312) and said outer combustion chamber (334) are combined into an integrated component by replacing said separate annular ring of said incineration chamber and said annular base of said combustion chamber with a single common ring (326) mounted in permanent sealing engagement with both said chambers. The hazardous waste incinerator of claims 2 and 6 to 17 inclusive, characterized in that said base (120) is vertically movable from said inner incineration chamber (151) to reveal said work support pad (122). The hazardous waste incinerator of claims 2 and 6 to 17 inclusive, characterized in that said base (120) is horizontally movable from below the inner incinerator chamber (151) to provide ready access to the work support pad (122). The hazardous waste incinerator of claim 5, characterized in that said outer combustion chamber (430) is provided with electrical heaters (443) behind said false wall (417). The hazardous waste incinerator of claim 5, characterized in that said false wall (417) rests on a plurality of "T"-shaped pad supports (423). The hazardous waste incinerator of claim 5, characterized in that said outer combustion chamber (430) is provided with electrical heaters (443) behind said false wall (417), and said false wall (417) rests on a plurality of "T"-shaped pad supports (423). A method for incinerating hazardous waste in a hazardous waste incinerator having an outer, heat-producing zone, and an inner incineration zone in which a charge of hazardous waste is fed only to said inner incineration zone, the exposed surfaces of said inner incineration zone being a non-porous, impervious, corrosion-resistant surface, said inner incineration zone being in sealed, spaced-apart and heat-transfer relation to said outer, heat-producing zone, characterized by : (1) heating said inner incineration zone by means of transfer of heat from said outer heat-producing zone, (2) withdrawing products of combustion from said outer, heat-producing zone; and (3) withdrawing products of incineration from said inner incineration zone; said products of incineration being separate and distinct from, and not mixed with, the products of combustion from said outer heat-producing zone.

Inventors: RITTER ROBERT A, RITTER, ROBERT A.
Applicants: RITTER ROBERT A, RITTER, ROBERT A.
Application year: 1990
Main classification: F23G5
IPC codes: F23M5, F23G5, F23J15, F23G7