Method and plant for producing secondary solid fuel

Abstract

A method and a plant for producing secondary solid fuel (SSF) provide for removing fine and heavy waste from a flow of treated waste and further subdividing the remaining waste into intermediate waste and light waste. Only the fraction of intermediate waste is subjected to removal of chlorinated plastics (PVC). Advantageously, thanks to the fact that only a small fraction of the treated waste is subjected to removal of the chlorinated plastics, high efficiency in the treatment of waste and in the production of SSF is obtained. Preferably, the intermediate waste fraction is also subjected to removal of ferrous metals and non-ferrous metals, such as aluminum.

Claims

1. A method for producing secondary solid fuel (SSF) starting from waste, the method comprising: receiving the waste; mechanically pretreating the waste; biologically treating the waste; and refining the waste; wherein refining the waste comprises: separating and removing fine waste; carrying out a first gravimetric separation for separating and removing heavy waste; carrying out a second gravimetric separation for separating the remaining waste into an intermediate waste fraction and a light waste fraction; separating chlorinated plastic materials from the intermediate waste fraction only; after having separated chlorinated plastic materials, mixing the intermediate waste fraction with the light waste fraction.

2. The method according to claim 1, wherein refining the waste further comprises, after having mixed the intermediate waste fraction with the light waste fraction, grinding and screening the resulting fraction of mixed intermediate and the light waste fractions.

3. The method according to claim 1, wherein refining the waste further comprises removing non-ferrous metals.

4. The method according to claim 3, wherein only the intermediate waste fraction is subjected to removal of non-ferrous metals.

5. The method according to claim 1, wherein refining the waste further comprises removing ferrous metals.

6. A plant for producing secondary solid fuel (SSF) starting from waste, the plant comprising: a station for receiving the waste; a station for mechanically pretreating the waste; a station for biologically treating the waste; and a station for refining the waste; wherein the refining station comprises: a rotating screen for separating fine waste; a first gravimetric separation device for separating and removing heavy waste; a second gravimetric separation device for separating the remaining waste into an intermediate waste fraction and a light waste fraction; a device for separating chlorinated plastic materials, which is provided downstream of the second gravimetric separation device and arranged so as to receive at its inlet the intermediate waste fraction only; a mixing device, arranged downstream of the device for separating chlorinated plastic materials, for mixing the intermediate waste fraction with the light waste fraction.

7. The plant according to claim 6, wherein the refining station further comprises, downstream of the mixing device for mixing the intermediate waste fraction with the light waste fraction, a grinder and a screen.

8. The plant according to claim 6, wherein the refining station further comprises a device for removing non-ferrous metals.

9. The plant according to claim 8, wherein the device for removing non-ferrous metals is provided downstream of the second gravimetric separation device and arranged so as to receive at its inlet the intermediate waste fraction only.

10. The plant according to claim 6, wherein the refining station further comprises one or more magnetic separators for removing ferrous metals.

11. The plant according to claim 6, wherein the first and second gravimetric separation devices are aeraulic separators.

12. The plant according to claim 6, wherein the device for separating chlorinated plastic materials is a NIR optical separator.

13. The plant according to claim 8, wherein the device for removing non-ferrous metals is an eddy current separator (235).

Description

BRIEF DESCRIPTION OF THE DRAWINGS

(1) Further features and advantages will become clearer from the detailed description of some preferred embodiments of the invention, given by way of non-limiting example with reference to the attached drawings, in which:

(2) FIG. 1a is a flow chart schematically showing the main steps of the method according to the invention;

(3) FIG. 1b is a flow chart schematically showing the main steps of the refining step of the method according to the invention;

(4) FIG. 2a is a block diagram schematically showing the main stations of the plant according to the invention;

(5) FIG. 2b is a block diagram schematically showing the main components of the refining station of the plant according to the invention.

DETAILED DESCRIPTION OF SOME PREFERRED EMBODIMENTS OF THE INVENTION

(6) FIG. 1a is a flow chart schematically showing the main steps of the method according to the invention.

(7) A first step 100 consists of a waste—in particular non-hazardous municipal solid waste—receiving step.

(8) In this step, it is possible to provide for an inspecting sub-step, aimed at eliminating any hazardous waste erroneously received, as well as waste that is excessively bulky or otherwise unacceptable. Such unacceptable waste is collected and disposed of appropriately. In a second step 110, the waste is subjected to a mechanical pre-treatment step, which substantially comprises a sub-step of mechanically opening the bags and a sub-step of coarse screening, with a screen of 100-300 mm, preferably of about 200 mm.

(9) Said mechanical pre-treatment step 110 allows to separate the waste having a size larger than the coarse screen size from those having a size smaller than said coarse screen size.

(10) Waste having a size larger than the coarse screen size usually consists of biologically inactive waste (non-recyclable plastics, wood, cardboard, textiles).

(11) Said waste is therefore subjected to a primary grinding sub-step 112 and directly sent to subsequent refining without being subjected to any biological treatment step.

(12) On the other hand, in a third step 120, waste having a size smaller than said coarse screen size is subjected to a biological treatment step.

(13) Said biological treatment step 120 is preferably a bio-drying step, during which the waste is stabilized and dried (for example up to a homogeneous water content of about 20-25%).

(14) This biological treatment step can be carried out, for example, according to the teachings of European patent application EP 1431262 A1 in the name of the Applicant.

(15) In a preferred embodiment of the invention, a further step of receiving commercial and industrial waste (C&I waste) 100′ is also provided.

(16) Said waste of commercial and industrial origin is mainly composed of non-recyclable rubber and plastic materials and is substantially biologically inactive. Therefore it is not subjected to any biological treatment and it is subjected to a primary grinding phase 112′ and then directly addressed to subsequent refining.

(17) In a fourth step 130 of the method according to the invention, the waste coming from the biological treatment step 120 (together with the biologically inactive ground waste and the commercial and industrial waste) is subjected to a refining step.

(18) Said refining step 130 will be described in detail below. It aims to remove materials that do not have good calorific value, and in particular metals. It also has the purpose of removing materials containing chlorine, and in particular chlorinated plastics, since their combustion would generate dioxins.

(19) At the end of this refining step 130, a secondary solid fuel (SSF) is obtained (step 140), which fuel can be pressed and packaged for storage and subsequent use.

(20) FIG. 1b shows in detail the refining step 130 of the method according to the invention, in the form of a flow chart showing the main sub-steps of said refining step.

(21) At first, said refining step 130 provides for a screening sub-step 131 for separating fine waste, i.e. the waste which can be separated by a screen with holes of 30 mm or less.

(22) Such fine waste is removed from the flow of treated waste and sent to a landfill.

(23) The remaining waste is subjected to a first gravimetric separation sub-step 132 for separating heavy waste, i.e. waste having a density>40 t/m.sup.3 (typically wood, bricks, stones, clumps of soil, metals, shoes, and the like).

(24) This heavy waste, too, is removed from the flow of treated waste and sent to a landfill.

(25) Preferably, before being sent to the landfill, said heavy waste is subjected to a sub-step of removing ferrous metals 136a, for example by magnetic means.

(26) Advantageously, according to the invention, the remaining waste is further separated by a second gravimetric separation sub-step 133, which allows to separate waste into light waste, i.e. waste having a density<35 t/m.sup.3 and typically a two-dimensional shape (typically plastic films, dry leaves, paper sheets, cardboard, two-dimensional light cartons) and intermediate waste, which does not fall in the categories of heavy and light waste (such as, plastic pipes, three-dimensional plastic items, heavy cartons, three-dimensional light cartons).

(27) The provision of said second gravimetric separation sub-step 133 allows to considerably increase the efficiency of the method for producing SSF.

(28) In fact, chlorinated plastics (for example PVC), which are undesirable due to the formation of dioxins in the event of combustion and which, therefore, must be removed, are predominantly present in the intermediate waste fraction, while they are substantially absent in the light waste fraction.

(29) Accordingly, in a subsequent sub-step 134 of the method according to the invention, only the fraction of the intermediate waste is advantageously subjected to a treatment for separating chlorinated plastics.

(30) Said sub-step of separating chlorinated plastics 134 is preferably carried out by using the NIR (Near Infra-Red) technology. This technology is known per se and therefore it will not be illustrated in detail herein.

(31) It will be evident to the person skilled in the art that, on the one hand, NIR optical separators are able to handle only limited flow rates (of the order of 7 t/h), and that, on the other hand, such limitation is thoroughly compensated by the fact that only a limited fraction of the treated waste is sent to the NIR optical separator.

(32) In a preferred embodiment of the method according to the invention, a sub-step of separating non-ferrous metals 135, in particular aluminum, is also provided.

(33) The provision of this sub-step is advantageous due to the fact that aluminum is a high quality recyclable waste, and it is therefore advisable to separate it so that it can be treated separately.

(34) Aluminum, too, is substantially present in the intermediate waste fraction only while it is substantially absent in the light waste fraction.

(35) Therefore, only the fraction of the intermediate waste is advantageously subjected to the sub-step of removing non-ferrous metals 135.

(36) Said sub-step of removing non-ferrous metals 135 can be carried out, for example, by means of the eddy currents technology. This technology is known per se and therefore it will not be illustrated in detail herein.

(37) In a preferred embodiment of the invention, the intermediate waste fraction is further subjected to a sub-step of removing ferrous metals 136b, for example by magnetic means. Also in this case, only the fraction of the intermediate waste is subjected to the sub-step of removing ferrous metals 136b, since said ferrous metals are substantially absent in the light waste fraction.

(38) In a subsequent sub-step 137 of the method according to the invention, the intermediate waste thus freed from the undesired components (chlorinated plastics and ferrous and non-ferrous metals) are mixed back with the light waste.

(39) The flow of waste thus obtained is subjected to a secondary grinding sub-step 138 and final screening 139, at the end of which the desired SSF is obtained.

(40) Turning now to FIGS. 2a and 2b, a plant according to the invention is schematically shown, which plant is capable of implementing the method described above.

(41) With reference initially to FIG. 2a, the plant according to the invention comprises a station for receiving waste 200—in particular non-hazardous municipal solid waste.

(42) Said station 200 may comprise means for inspecting the received waste in order to identify any hazardous waste erroneously received, as well as waste that is excessively bulky or otherwise unacceptable, and means for picking such unacceptable waste, such as for example a bridge crane.

(43) The plant according to the invention further comprises a station for mechanical pre-treatment 210, which may comprise means for mechanically opening the bags and a screen having a size of 100-300 mm, preferably of about 200 mm.

(44) Waste having a size larger than the screen size usually consists of biologically inactive waste. Said waste bypasses the following station of biological treatment and is sent to a primary grinder 212 and then directly to the refining station.

(45) On the other hand, waste having a size smaller than the coarse screen size is sent to a station for biologically treatment 220, preferably a bio-drying station.

(46) Said station for biological treatment 220 may be made, for example, according to the teachings of the European patent application EP 1431262 A1 in the name of the Applicant. In a preferred embodiment of the invention, the plant provides for a further receiving station 200′ for receiving commercial and industrial waste (C&I waste).

(47) Said waste of commercial and industrial origin is mainly composed of non-recyclable rubber and plastic materials and it is substantially biologically inactive. Therefore, it is not subjected to any biological treatment; on the contrary, it is sent to the primary grinder 212 (or to a primary grinder dedicated thereto) and, from there, directly sent to the refining station.

(48) The refining station 230 therefore receives the waste coming from the biological treatment station 220 and the biologically inactive waste coming from the primary grinder 212.

(49) Said refining station 230 is shown in greater detail in FIG. 2b.

(50) Firstly, said refining station 230 comprises a drum screen 231 for separating fine waste.

(51) Such fine waste is removed from the flow of treated waste and sent to a landfill.

(52) The remaining waste is sent to a first gravimetric separation device 232, in particular a first aeraulic separator, which is designed for separating heavy waste.

(53) This heavy waste, too, is removed from the flow of treated waste and sent to a landfill.

(54) Preferably, before being sent to the landfill, said heavy waste is passed through a magnetic separator 236a, such as for example a magnetic conveyor belt for removing ferrous metals. Advantageously, the plant according to the invention further comprises a second gravimetric separation device 233, in particular a second aeraulic separator, which allows to further separate the remaining waste into intermediate waste and light waste.

(55) Downstream of said second gravimetric separation device 233, a device for separating chlorinated plastics (for example PVC) 234 is provided, which device is arranged so as to receive at its inlet said fraction of intermediate waste only.

(56) Said device for separating chlorinated plastics can be, for example, a optical separator NIR 234. This separator is known per se and therefore it will not be illustrated in detail herein.

(57) In a preferred embodiment of the invention, the plant also comprises a non-ferrous metal removal device 235, designed in particular to separate aluminum.

(58) Preferably, also said non-ferrous metal removing device 235 is arranged so as to receive at its inlet the fraction of intermediate waste only.

(59) Said non-ferrous metal removing device may be, for example, a parasitic current separator 235. This separator is known per se and therefore it will not be shown in detail herein.

(60) In a preferred embodiment of the invention, the plant further comprises a magnetic separator 236b, which is also arranged so as to receive at its inlet the fraction of the intermediate waste only and is intended to separate the ferrous metals.

(61) The plant according to the invention further comprises means 237 for mixing back the intermediate waste (freed from the undesired components) with the light waste.

(62) The waste flow thus obtained is sent to a secondary grinder 238 and from there to a disc screen 239, at the output of which the desired SSF is obtained.

(63) It will be evident to the person skilled in the art from the above that the method and the plant according to the invention allow to achieve the objects set forth above, since they allow to optimize the treatment of waste for obtaining a secondary solid fuel having the desired characteristics.

(64) It will also be evident that the embodiment described above has been provided purely by way of non-limiting example and that numerous variations and modifications are possible without departing from the scope of protection as defined by the appended claims.