A METHOD FOR TREATING WASTE MATERIAL WHICH INCLUDES METAL AND/OR METAL OXIDE, ORGANIC MATERIAL AND POSSIBLY ALSO WATER; AND APPARATUS FOR CARRYING OUT THE METHOD

Abstract: There is disclosed a method for treating waste material containing metal and/or metal oxide, organic material and option­ ally also water, for the purpose of separating the organic material and any water present in vapour form. The waste material is heated indirectly while continuously advancing the waste mate­ rial through a screw housing (12, 13) by means of a screw, the heat being supplied in a quantity such that the volatile con­ stituents of the waste material are converted to gas and/or vapour form. The resultant gases and vapours are used as fuel for heating the waste material in the screw housing. The screw housing (12, 13) is only partially filled with material being treated, so as to form a vacant space in which the generated gases and/or vapours collect. The generated gases and/or vapours are dis­ charged from the screw housing without contacting the material being treated and/or the material to be treated, and are supplied, optionally after partial condensation of gas and/or vapour originating from the organic material, to a combustion chamber (48) for generating combustion gases, which are used to indi­ rectly heat the material in the screw housing.

Description: A METHOD FOR TREATING WASTE MATERIAL WHICH INCLUDES METAL AND/OR METAL OXIDE, ORGANIC MATERIAL AND POSSIBLY ALSO WATER; AND APPARATUS FOR CARRYING OUT THE METHOD The present invention relates to a method for treating waste material containing metal and/or metal oxide, organic material and possibly also water, in order to separate the organic material and any water present in vapour form, the waste material while being continously advanced through at least one screw housing by means of a screw being heated indirectly, and heat being supplied in such quantities as to gasify and/or vapourize the volatile constituents of the waste material, the gases and vapours generated being used as fuel for heating the waste material in the screw housing. Such methods form part of the state of the art (cf. DE-A-18 14 471 and SE-B-7907037-1). The waste material in question may comprise metal scrap, such as grindings etc., containing oil and water. The prime object of the method is to recover the valuable metals and/or metal oxides contained in the waste material, and to recover these metals and/or oxides in a form in which they are suitable for use in, for example, alloying plants. The aforementioned Swedish Patent Specification describes a method which is carried out in a vessel, in the lower part of which heat is indirectly supplied to the waste material in an amount sufficient to vapour ize the volatile constituents of the waste material, said material being advanced by means of a screw, and the vapours and/or gases generated drive the liquid present in a superimposed layer of waste material to the surface of said layer, where the liquid is allowed to run-off via an overflow means. Combustible gases obtained when heating the waste material can be recycled and used for the heating process. One disadvantage with this known method is that it is technically complicated to generate the mass of gases and/or vapours required to drive the liquid in the superimposed layer of waste material to the surface of said layer. The resultant gases and/or vapours are practically always obnoxious and, if released to atmosphere, can cause serious environmental problems. These and other disadvantages can be eliminated, or substantially reduced, if the heating process is carried into effect under conditions in which the gases and/or vapours generated by the volatile constituents of the waste material are collected in a space not filled with solid material and located in the close vicinity of the heating zone. The gases and/or vapours can be passed from the-space to a cooling means, and there caused to condense to liquid form which, if combustible, can be used as a fuel for the heating process required to convert the volatile material to vapour and/ or gas form. Gases and/or vapours which do not condense can be recycled and used for the same heating process. By immediately separating from the material being treated those vapours and/or gases generated during the heating process, it is possible to obtain in a more advantageous manner than previously a closed process which, in addition to being more favourable to the environment is also simpler to put into effect from a technical aspect. On the basis of the above, the method described in the introduction is characterized in that the screw housing or housings in which heating takes place is maintained incompletely filled with the material being treated, so that the resultant gases and/or vapours are collected in the vacant space left in the screw housing; in that the gases and/or vapours generated are led away from the screw housing without coming into contact with the material to be treated and/or the material being treated; and in that the gases and/or vapours originating from the organic material are passed, optionally after being partially condensed, to a combustion chamber for generating combustion gases, which are used to indirectly heat the material in the screw housing or housings. The DE-A-18 14 471 also describes a method similar to the present method, in which waste material comprising a mixture of finely-divided metal and, in particular, cutting oil, is heated in a screw housing while being continuously fed therethrough, in order to vapourize the volatile constituents of said waste material. In this method, the vapours originating from the heating process are caused to pass through a layer of waste material, thereby creating disadvantages with respect to the handling of said waste material, in addition to environmental disadvantages. The published specification gives no indication of the use of the gases and/or vapours generated ed during the heating process as fuel for said heating process in a closed system. Thus, the teachings of said specification cannot be considered to render the present invention for which patent is claimed obvious to one of normal skill in this art. The invention also relates to apparatus for treating waste material containing metal and/or metal oxide, organic material and possibly also water, in order to separate the organic material and any water present in vapour form, the waste material while being continuously advanced through at least one screw housing, in which a conveyor screw is arranged to rotate and to convey the material in the screw housing from a supply location for the waste material to be treated to an discharge location for the material treated in the screw housing, being heated indirectly by means of heat being supplied in such quantities as to cause the volatile constituents of the waste material to convert to gas and/or vapour form, the gases and vapours generated being used as fuel for heating the waste material in the screw housing. In accordance with the invention, the apparatus is characterized in that each conveyor screw has a reduced conveying capacity in the vicinity of said supply location so as to form a space in the screw housing which is held only partially filled with material; and in that means are provided for conducting away the generated gases and/or vapours collected in the vacant space of the screw housing, out of contact with the material to be treated and/ or being treated, and from there, optionally via a condensor, to a combustion chamber for generating combustion gases, which are used for indirectly heating the material in the screw housing Other-fe-atures¯¯o¯f the invention are set- fO-rth in the following claims and will be apparent from the following description of the method and an apparatus for carrying out said method. The invention will now be described in more detail with reference to the accompanying drawings, in which Figure 1 illustrates schematically a plant for treating waste material containing metal and/or metal oxides, Figure 2 is a schematic side view of the unit in the plant in which actual treatment of the waste material takes place, and Figure 3 is a sectional view taken on the line A-A in Figure 2. Hereinafter there is described with reference to Figures 1 and 3 a process, together with variations thereof, with which the intention is to treat a waste material comprising a mixture of particulate metal or metal oxide obtained by chip removing or other machining operations on workpieces comprising high allow metallic materials, organic material in the form of oil used to facilitate said machining operations (cutting oil), and also water. Examples of such metal particles include grindings, e.g. grindings from centerless-grinding operations, and scale. In accordance with the process illustrated in Figure 1, the waste material is transported from a store (not shown) by means of an inclined first belt conveyor 10, to a screw conveyor 11 which extends transversely to the conveying direction of said conveyor 10, and from there to the actual plant for treating said waste material. The plant comprises two elongate screw housings arranged side by side, of which one is referenced 12 and the other 13 in the drawings. The material to be treated is advanced by means of the conveyor screw 14 of the conveyor 11, up to two openings in the bottom of the screw housing, of which openings one, 15, passes to the interior of the screw housing 12 via a short duct 16, while the other opening, 17, leads to the interior of the screw housing 13, via a similar duct 16. Any input waste material, which passes over the two openings 15, 17 in the bottom of the screw housing while being conveyed by the conveyor 11 and fails to fall through openings 15, 17, is discharged via a further opening 18 in the bottom of the screw housing at the end of the housing, onto a further belt conveyor 19, from which material not fed into the two screw housings 12, 13 is transferred onto the belt conveyor 10 and again passed to the transverse screw conveyor 11. By recycling material which is not fed into the the screw housings 12, 13, there is obtained a uniform supply of waste material, without requiring undue control with regard to the material fed to the belt conveyor 10. Each screw housing 12, 13 is divided into two screwhousing chambers 20 and 21, of which one chamber, 20, is always intended for expelling the volatile constituents of the waste material, i.e. oil and water, by means of indirect heating. The other chamber 21 may alternatively be intended for calcining the material treated in the chamber 20 at a temperature higher than the treatment temperature in the chamber 20. The two chambers 20, 21 are connected to one another by means of a passage 22 having a smaller cross-sectional area than the remainder of the screw housing. The screw housings 12, 13 accomodate a conveying screw 23, which is journalled in bearings 24, 25 at the ends thereof, and which is rotated by means of an electric motor 26, the drive shaft of which is connected to the shaft of the conveying screw 23 by means of a coupling 27. The screw housing 12 has an external shell or jacket member 28 which also embraces the adjacent screw housing 13. The shell 28 defines a space into which combustion gases from an individual hot-gas unit provided with a combustion chamber and associated with said plant are introduced. The combustion bases serve as heating gas for indirectly heating the waste material fed by the conveying screw 23 of the two screw housings 12 and 13. As it is advanced, the material is supplied with heat in a quantity sufficient to expel the volatile constituents of the waste material. Arranged between the screw 23 and the upper part of the screw housing 12 is a space which is not filled with material during operation. This free space forms a collecting chamber for the gases andjor vapours departing from the material undergoing treatment, these gases and/or vapours being prevented from contacting the material to be treated and/or the material being treated. In this respect, the gases and/or vapours can be immediately conducted away from the screw housing through a line 29, and passed to a cooling means 30, in which they are caused to condense to form a liquid (oil) which runs down through cooling tubes 31 and collects at the bottom of the cooling means 30, in a bottom sump arranged therein, from where the liquid runs to a storage vessel 33 through a line 32. For the purpose of further cooling the liquid formed, the liquid can be recycled through line 34, via a pump 35 and heat exchanger 36, and passed back to the cooling means 30, where it is collected on a bottom plate 37 in the upper part thereof. The bottom plate 37 is provided with openings through which cooling tubes 31 pass, said tubes extending above said plate such that the upper opening of respective tubes forms an overflow means. By returning cooled liquid to the cooling means 30, there is obtained an effective direct cooling of the mixture of gases and vapours arriving from the screw housings 12, 13. The cooling effect, however, is also obtained indirectly, by supplying air from the surroundings with the aid of fan 38, which air, subsequent to having passed the cooling tubes 31, leaves the cooling means 30 and passes through line 39 to consumer locations, such as local heating plants, burners etc. Any excess is passed to chimney 40. The heat exchanger 36 is cooled with water, which is supplied through a line 41 via valve 42. In order to form the space in which the cooling tubes 31 are cooled with cooling air, introduced by means of fan 38, there is provided a lower bottom plate 43 having openings in which the cooling tubes 31 are mounted. The storage vessel 33 is provided in a conventional manner with an overflow line 44 and a valve 45, to prevent the occurrence of an overpressure. In order to obtain the combustible gases required to heat the material in the two screw housings 12, 13, there can be used either the combustible liquid collected in the storage vessel 33, this liquid comprising a hydrocarbon mixture of high calorific value, or the noncondensible gases obtained from the cooling means, or both. If the material volatilized in the screw housings 12, 13 contains water, as is normally the case when the treated material consists of turnings or grindings, since an aqueous emulsion containing a hydrocarbon mixture will have been used to facilitate the cutting work, the resultant water vapour will accompany the material volatilized in the screw housings. By suitably adjusting the cooling effect obtained in the cooling means 30, it is possible to restrict condensation to solely the hydrocarbon mixture, while the water vapour can be conducted away, oprionally together with other non-condensed gases. Non-condensed material taken from the cooling means 30 is passed from said means through line 46, which incorporates fan 47, and further to a hot-gas unit generally referenced 48. Oil which, subsequent to condensation, has collected in the storage vessel 33, is conveyed, by means of pump 49, to the hot-gas unit 48 through line 50, which incorporates a valve 51 by means of which the amount of liquid fuel charged to the hot-gas unit 48 can be regulated. Part of the hot air from the cooling means 30 can be branched from line 39 to a further line 53 and conveyed therefrom as air of combustion to the hotgas unit through fan 54. In principle, the hot-gas unit 48 comprises a casing 52 into which fuel-supply nozzles extend. The combustible liquid (oil) conveyed from the storage vessel 33 with the aid of pump 49 is introduced into a first nozzle 55'in the hot-gas unit 48, and mixed in said nozzle with pre-heated combustion air which is conveyed through line 53 with the aid of fan 54 and which has been pre-heated by being fed past the tubes 31 in the cooling means 30. The nozzle 55 is encircled by a chamber 56, to which a mixture of non-condensed combustible gases and water vapour is supplied through a line 46, with the aid of fan 47. When the fuels and combustion air come into contact with each other combustion takes place and the resultant combustion gases are introduced into the combustion chamber 57 of the hotgas unit 48, where a more complete combustion takes place. Prior to entering the combustion chamber 57, the fuel mixture from nozzle 55 is caused to pass through two further nozzles 58 and 59, each of which is encircled by a respective chamber 60 and 61, which are supplied with secondary combustion air or combustion gas from the screw-nousing chamber 21 in the screw housings 12, 13 under certain operating conditions of the plant, as will be described hereinafter. The hot-gas unit 48 includes a fourth nozzle 62 located in the actual combustion zone, this nozzle being encircled by an annular chamber 63. This latter chamber is supplied with combustion gases which have been used to heat the material in the screwhousing chambers 20 and optionally 21 in the screw housings 12, 13. These combustion gases are conveyed through line 64 with the aid of fan 65. The combustion gases generated in the hot-gas unit 48 as a result of the combustion process are collected in a space in the end of the unit, and led therefrom through an exhaust line 66 to various parts of the heating jacket 28 of the screw housings 12, 13. For the purpose of distributing the combustion gases discharged from the hot-gas unit through line 66 under different operational conditions, there is arranged a system of pipes with associated valves for controlling the flow of combustion gas in a given manner desirable with respect to prevailing operational conditions. As before indicated, the plant can be operated in different ways. In a first operational mode the waste material is solely treated to remove volatile constituents, by expelling said constituents in the screw housing chamber 20. In this case, the hot-gas flow from the hot-gas unit 48 is caused to pass through the exhaust line 66, the line 67 and the line 74 incorporating valve 72, which is then open, and through the line 70 to the heating jacket 28. In this case the valve 71 in line 68 is kept closed. Subsequent to the flow of combustion gas passing the jacket 28 of the screwhousing chamber 20, the flow of combustion gas is fed out through the line 64 from said jacket with the aid of fan 65, and recycled to the annular chamber 63 of the hot-gas unit 48. Part of the gas flow is led to the chimney 40 through line 75, while another part of said flow is passed parallel with the hot-gas.unit 48, via valve 73, to line 66 for controlling the temperature of the gas arriving from the hot-gas unit. The amount of gas discharged to the surroundings through the chimney 40 is regulated by means of the valve 76 and a fan 102. The heat contained by the flow of gas departing through line 75 can be recovered with the aid of a heat exchanger 77. According to an alternative operational mode, both the screw-housing chambers 20 and the screw-housing chambers 21 can be used to expel volatile constituents from the waste material advanced by the screws 23. In this case, the combustion gases originating from the hotgas unit 48 are led from said unit through line 66, through line 67, through line 68, with valve 71 open, to the part of the jacket 28 enclosing the chambers 21, through said jacket part and back from said jacket part through lines 69 and 70 to the jacket 28 of the screwhousing chambers 20. The return path for used combustion gases is the same as that of the first alternative operational mode. The valve 72 is kept closed in this case. In a third optional, operational mode the process carried out in the plant is modified so that the volatile constituents are expelled from the waste material in the screw-housing chambers 20 and the material treated in the screw-housing chambers 20 is calcined (oxidized) in the screw-housing chambers 21. In this case the flow of combustion gases is passed through exhaust lines 66, the line 67, the line 74 incorporating valve 72, through line 70 to the jacket 28 of the screw-housing chambers 20, whereby material advanced in said chambers is heated to expel volatile constituents which are collected and discharged through line 29 to the cooling means 30, for partial condensation. In this case, the valve 71 is closed. The expulsion process effected in the screwhousing chambers 20 is regulated so that not all volatile material is expelled, but that a part of the carbon or highly carbonaceous material is permitted to remain on the treated material. This treated material, which consists of a mixture of metal and/or metal oxides and carbon or carbonaceous material, is now subjected to a calcination process in the screw-housing chamber 21. To this end, there is opened a flap 79 on the upper part of the screw-housing chamber 21 (see Figure 3). Because of the high temperature of the carbon-laden metal material, the carbon, when coming into contact with the air, will ignite and burn, and the metal material will be oxidized. The gases generated during this oxidation process are discharged through a hood 80, shown in chain lines in Figures 1 and 2. The oxygen-containing waste gases from the hood 80 are passed through line 81, through valve 82 with the aid of fan 83, either to the chamber 60 through line 84, or to the chamber 61 through line 85 incorporating valve 86, or along both paths, as secondary combustion air in the hot-gas unit 48. One condition for enabling the two processes, i.e. expulsion and calcination, to take place in the two chambers 20 and 21 of the screw housing, is that the chambers can be kept separate from one another. This is achieved by providing a "sealing plug" in the narrowed passage portion 22, more specifically by adjusting the screw 23 relative the portion 22 so as to create a material build-up in said portion 22. Material which has been finally treated in the chambers 20, 21 of the screw housings 12, 13 is permitted to fall through openings 78 (Figure 1) and a chute 87 (Figure 2) down into a screw conveyor 88, where it is advanced by a screw which, under indirect cooling via a cooling jacket 89, feeds the material to an outlet through which the material is packed into suitable conveying vessels 90, which are advanced by a belt-type conveyor 91 which extends transversely of the screw conveyor 88 and which is optionally provided with a weighing station at the output end of the conveyor 88. The indirect cooling is achieved with the aid of a coolant, e.g. air or water, which is introduced through a valve 92 and through an inlet line 93, and which subsequent to passing the cooling jacket 89 is discharged through an outlet 94. For the purpose of equalizing the temperature of the conveying screws 23 in the screw housings 12, 13, each screw axle is preferably of hollow construction and is provided with a plurality of openings at either end, the openings at one end being referenced 95 and the openings at the other end being referenced 96. The portions of the axles which exhibit said openings are surrounded by housings, the housing associated with the openings 95 being referenced 97 while the housing associated with the openings 96 being referenced 98. Each housing 97, 98 sealingly abuts the axles of conveyor screws 23. A coolant is caused, with the aid of fan 99, to circulate into the housing 98, through the openings 96 in the hollow axle, through the part of said axle located in the screw housing 12 or 13, and out through the openings 95 into the housing 97, and from there through an outer line 100. In accordance with an embodiment illustrated in Figure 3, this embodiment being particularly favourable when treating material containing a high percentage of gasifiable and vapourizable constituents, there may be provided in the vacant or non-filled part of the screwhousing chambers 20 and optionally chambers 21 heating pipes 101 arranged to be through-passed by hot gas from the unit 48. The hot heating pipes 101 superheat the gases and/or vapours generated by said indirect heating process via the jacket 28, so as to prevent undesirable re-condensation of said gases and/or vapours on the material undergoing heat treatment. This greatly increases the capacity of the apparatus according to the invention. In order to prevent coatings from forming on the inner surfaces of the screw-housing chambers 20,21, which coatings would prevent effective heat transfer between the combustion gases flowing through the jacket 28 and the material being treated, means may be provided for scraping the walls of said chambers. For example, the screws 23 may be provided with scraper means in the form of a rod rigidly connected to peripheral parts of a respective screw, and extending along the whole length of said screw in a manner such that when the screw rotates, the rod moves across the cylindrical part of the screw-housing wall associated with said screw. Suitably, the rod may be caused to extend helically along the screw 23, the pitch of the rod helix advantageously being much greater than the pitch of the screw 23, and preferably in counter direction to the screw 23. When waste material containing water and oil is treated in accordance with the invention, condensation is effected in the condensor or cooling means 30 only to a limited extent, wuch that all water vapour arriving from the screw-housing chambers 20, 21 is maintained in vapour form. The water vapour is passed through line 46 to the hot-gas unit, together with other non-condensed and non-condensible parts of the gases and vapours generated during the dry-distillation process, these gases and vapours being used as fuel. The gases are fully combusted in the hot-gas unit 48 with an oxygen surplus and at high temperatures, above 8000C, whereby, subsequent to being used for indirectly heating the material being treated, the waste gases from said unit can be discharged to atmosphere without creating environmental problems. Similarly, water obtained by condensing water vapour from consumed gases, for example in the heat exchanger 77, can be discharged without being purified. Advantageously, the extent of condensation in the cooling means 30 can be adjusted in a manner such that, if the material to be treated contains at times, or constantly contains, more combustible material than what is required to effect the process, substantially only the surplus combustible vapours are condensed. To this end, only a minor amount of fuel is supplied via the line 50, so as to maintain a pilot flame in the burner zone 55, the purpose of this pilot flame being to facilitate starting-up of the unit 48 with fuel from the tank 33 when the gases and vapours arriving from the screwhousing chambers 20 and possibly 21 are-deficient of combustible constituents. In order to ensure that a substantially uniform product is obtained when treating the material supplied to the screw-housing chambers 20, irrespective of the amount of oil and/or water contained by said material, a substantially constant temperature can be maintained on both the gases supplied to the jacket 28 and those discharged from said jacket. When the amount of oil and/or water contained by the material in the screw-housing chamber 20 increases, when the temperature of the gases departing from the jacket 28 through line 64 tends to fall, it is possible to increase the amount of fuel supplied to the hot-gas unit 48, and the extent of the combustion therein, and to change the setting of the valves 73 and 76 so as to maintain a.desired pre-determined temperature of the combustion gases utilized for the dry destillation process in screw housings 11, 12, at the inlet and outlet of the jacket 28. In a corresponding manner, the amount of fuel and combustion air supplied is reduced and the valves 73, 76 re-set when the temperature of the gases discharged from the jacket 28 tend to increase, owing to a decrease in the amount of components which can be expelled from the materials supplied to the screw-housing chambers 20. The aforedescribed regulating steps, and also regulation of the process in general, is suitably effected with the aid of automatic process control devices (not shown).

Claims: CLAIMS 1. A method for treating waste material containing metal and/or metal oxide, organic material and possibly also water, in order to separate the organic material and any water present in vapour form, the waste material while being-continously advanced through at least one screw housing (12, 13) being heated indirectly and heat being supplied in such quantities as to gasify and/or vapourize the volatile constituents of the waste material, the gases and vapours generated being used as fuel for heating the waste material in the screw housing, characterized in that the screw housing (12, 13) is maintained incompletely filled with the material being treated, so that the resultant gases and/or vapours are collected in the vacant space left in the screw housing; in that the gases and/or vapours generated are led away from the screw housing without coming into contact with the material to be treated and/or the material being treated; and in that the gases and/or vapours originating from the organic material are passed, optionally after being partially condensed, to a combustion chamber (48) for generating combustion gases which are used to indirectly heat the material in the screw housing. 2. A method according to Claim 1, characterized by maintaining the combustion chamber (48) at a temperature of about 8000C or thereabove. 3. A method according to Claim 1 or Claim 2, characterized by using the material obtained subsequent to said condensation process as fuel for the combustion chamber (48). 4. A method according to Claims 1-3, characterized by heating the material in the screw housing (12, 13) under such conditions that a residue of carbon or highly carbonaceous material is formed by organic material contained in said waste material, this residue being optionally used as a reductant when smelting the metal-contain ing product obtained subsequent to treating the waste material in said screw housing. 5. A method according to Claims 1-4, characterized by calcining the material treated in the screw housing (12, 13) in a separate treatment zone (21) which is connected to said screw housing and which suitably has the form of a second screw housing, said second screw housing being separated from the first mentioned screw housing by means of a narrowed bridging portion (22). 6. A method according to any one of Claims 1-5, characterized by condensing from the gases and/or vapours discharged from the screw housing (12, 13) substantially only surplus combustible gas and/or vapour not required for generating said combustion gases. 7. A method according to Claims 1-6, characterized by subjecting the air used for the combustion process in the combustion chamber (48) to a heat exchange with the gases and/or the vapours obtained when treating waste material in the screw housing (12, 13) prior to introducing said air into the combustion chamber. 8. A method according to Claims 1-7, characterized by circulating gases through an axial passage in the con ¯veyor screws or screws (23) used for advancing waste material being treated, in order to equalize the temperature in said screw or screws. 9. A method according to Claims 1-8, characterized by heating material located in the screw housing or housings (12, 13) with the aid of a jacket means (28) arranged around the screw housing or housings and to which heating gases are supplied from the combustion chamber (48). 10. A method according to Claim 9, characterized by returning part of the heating gases arriving from the jacket means (28) to the gases arriving from the combustion chamber (48) for an exchange of heat therebetween. 11. A method according to Claim 9 or Claim 10, characterized by maintaining the heating gases supplied to or discharged from the jacket means (28) at a substantially constant temperature. 12. Apparatus for treating waste material containing metal and/or metal oxide. organic material and optionally also water, in order to separate the organic material and any water present in vapour form, the waste material while being continuously advanced through at least one screw housing (12, 13), in which a conveyor screw (23) is arranged to rotate, therewith to convey the material in the screw housing from a supply location (16) for the waste material to be treated to a discharge location (78, 87) for the material treated in the screw housing, being heated indirectly and heat being supplied in such quantities as to gasify and/or vapourize the volatile constituents of the waste material, and the gases and vapours generated being used as fuel for heating the waste material in the screw housing, characterized in that each conveyor screw (23) has a reduced conveying capacity adjacent said supply location (16) so that the screw housing (12, 13) is maintained only partially filled with material so as to provide a vacant space in said screw housing, and in that means (29, 46 47) are provided for passing the generated gases and/or vapours collecting in said vacant space in said screw housing, out of contact with the material to be treated and/or the material being treated, away from the screw housing and, optionally via a condensor (30), passing said gases and/or vapours to a combustion chamber (48) for generating combustion gases, which are used for indirectly heating the material in the screw housing. 13. An apparatus according to Claim 12, characterized by a further screw housing (21) which is connected to the first mentioned screw housing (12, 13) and in which the material treated in said first mentioned screw housing is adapted to be calcined. 14. An apparatus according to Claim 13, characterized in that the first-mentioned screw housing (12, 13) and the further screw housing (21) are separated from one another by means of a constricted portion (22), and in that the axis of the conveyor screw (23) is common to both screw housings. 15. An apparatus according to Claims 12-14, characterized in that the conveyor screw (23) has a hollow axle, and in that said axle is provided with a supply location (96) and a discharge location (95) for gas, which can be cycled through the axle in order to equalize screw temperature. 16. An apparatus according to any one of Claims 12-15, characterized in that said apparatus includes line means for passing part of the heating gases already used for said indirect heating process back to the gases arriving from the combustion chamber (48), for controlling the temperature of these gases.

Inventors: FRIDH, BENGT, JOHANSSON, JAN
Applicants: INDUSTRI-TEKNIK BENGT FRIDH AB
Application year: 1982
Main classification: C22B1
IPC codes: C22B1, F23G5