JP3935742B2 - High quality fuel production apparatus and production method from organic waste - Google Patents

Description

[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a high-quality fuel production apparatus and production method from organic waste.
[0002]
[Prior art]
In a treatment method in which pyrolysis gas is obtained by pyrolyzing organic waste and burned, only the cracked gas is burned. For this reason, there is an advantage that high-temperature combustion is possible in an atmosphere where there are few metals and soot and there is little production of dioxins.
[0003]
On the other hand, in the carbide obtained by pyrolyzing organic waste, metals, salts and ash in the raw material remain, so when using this as fuel, volatilization of salts, Problems that affect the environment, such as the generation of soot and the production of dioxins, are more likely to occur. Therefore, in order to prevent such a problem from occurring, it is necessary to limit the combustion temperature and to make advanced exhaust gas detoxification equipment, and there is no economic rationality for using carbide as a fuel. For this reason, the use of the obtained carbide is limited to a fuel adsorbent and the like, and most of the carbide must be disposed of in landfills.
[0004]
[Problems to be solved by the invention]
This invention is made in view of the said problem, and provides the manufacturing apparatus and manufacturing method for manufacturing a high quality fuel or alkali mixed coal from the carbide | carbonized_material obtained by thermally decomposing organic waste. With the goal.
[0005]
[Means for Solving the Problems]
In order to achieve the above-mentioned object, the high-quality fuel production apparatus from organic waste according to the present invention comprises a stirring means for stirring organic waste, and the stirred organic waste is heated from the outside to become carbide. A heating circulation system zone having an external heating means, in which the oxygen concentration is limited, and a carbon component that becomes high-quality fuel and an ash component by electrostatic induction of the carbide extracted from the circulation system zone. And an electric separation means. The electrostatic separation means electrostatically induces the carbide extracted from the flow system zone by an electrode, and thereby carbon is a high-quality fuel attracted by a load having a polarity opposite to that of the electrode, and is dielectrically induced by the electrode. It is suitable to divide into difficult ash.
[0006]
The high-quality fuel production apparatus from the organic waste according to the present invention includes, as another aspect, a stirring means for stirring the organic waste, and an external heating means for heating the stirred organic waste from the outside to form a carbide. And a heating flow system zone in which the oxygen concentration is limited, and a specific gravity difference separating means for dividing the carbide extracted from the flow system zone into a carbon component that serves as a high-quality fuel and an ash component. The specific gravity difference separating means uses the wind of the wind given to the carbide as the carbide extracted from the circulation system zone, based on the difference in terminal measure determined by the difference in specific gravity and the difference in resistance to the wind. It is preferable to divide into carbon and ash which are high quality fuels.
[0007]
The high-quality fuel production apparatus from the organic waste according to the present invention includes, as another aspect, a stirring means for stirring the organic waste, and an external heating means for heating the stirred organic waste from the outside to form a carbide. And a heating flow system zone in which the oxygen concentration is limited, a specific gravity difference separating means for separating the carbide extracted from the flow system zone into carbon and high-quality fuel and ash, and from the specific gravity separating means By electrostatically inducing the extracted carbide, it includes electrostatic separation means that separates into carbon and high-quality fuel and ash.
The apparatus for producing high-quality fuel from organic waste according to the present invention is provided between the heating circulation system zone and the electrostatic separation means, and pulverizes the carbon extracted from the heating circulation system zone. A grinding means can be further included.
[0008]
The apparatus for producing high-quality fuel from organic waste according to the present invention is provided between the heating and circulation system zone and the specific gravity difference separation means, and pulverizes the carbon extracted from the heating and circulation system zone. A grinding means can be further included. In the pulverizing means, it is preferable to add an alkaline solid to the carbide. In addition, as an example of alkaline solid, quick lime, slaked lime, etc. are preferable, and 100 weight part-400 weight part of calcium in alkaline solid are preferable with respect to 100 weight part of chlorine content in carbide | carbonized_material.
[0009]
Another aspect of the present invention is a method for producing high-quality fuel from organic waste, and the high-quality production method is a heating flow system in which organic waste is limited to an oxygen concentration of 5% or less and heated from the outside. A supply step for supplying to the zone, a heating step for heating the inside of the heating and circulation system zone from outside the heating and circulation system zone while maintaining a temperature of 300 to 800 ° C., and the carbide extracted from the circulation system zone The electrostatic separation step of separating the carbon content and the ash content into high quality fuel by electrostatically inducing the ash. In the electrostatic separation step, the carbide extracted from the flow system zone is electrostatically induced by an electrode, so that a carbon component serving as a high-quality fuel attracted by a load having a polarity opposite to that of the electrode is induced by the electrode. The step is preferably divided into difficult ash.
[0010]
According to another aspect of the method for producing high-quality fuel from organic waste according to the present invention, the organic waste is limited to an oxygen concentration of 5% or less, and is supplied to a heating circulation system zone heated from outside, A heating step of heating from outside the heating circulation system zone while maintaining the inside of the heating circulation system zone at a temperature of 300 ° C. to 800 ° C., and the carbon extracted from the circulation system zone as a carbon component serving as a high-quality fuel. And a specific gravity difference separating step for dividing into ash. The specific gravity difference separating means uses the wind of the wind given to the carbide as the carbide extracted from the circulation system zone, based on the difference in terminal measure determined by the difference in specific gravity and the difference in resistance to the wind. It is preferable to divide into carbon and ash which are high quality fuels.
[0011]
According to another aspect of the method for producing high-quality fuel from organic waste according to the present invention, the organic waste is limited to an oxygen concentration of 5% or less, and is supplied to a heating circulation system zone heated from outside, A heating step of heating from outside the heating circulation system zone while maintaining the inside of the heating circulation system zone at a temperature of 300 ° C. to 800 ° C., and the carbon extracted from the circulation system zone as a carbon component serving as a high-quality fuel. And a specific gravity difference separating step for dividing into ash, and an electrostatic separating step for separating into carbon and high-quality fuel and ash by electrostatic induction of the carbide extracted from the specific gravity separating means. Including.
[0012]
In the method for producing high-quality fuel from the organic waste according to the present invention, the carbon component provided between the heating circulation system zone and the electrostatic separation means is pulverized. It is desirable to further include a grinding step. A crushing unit that is provided between the heating flow system zone and the specific gravity difference separation unit and that crushes the carbon extracted from the heating flow system zone may be further included. In the pulverizing means, it is preferable to add an alkaline solid to the carbide. In addition, as an example of alkaline solid, quick lime, slaked lime, etc. are preferable, and 100 weight part-400 weight part of calcium in alkaline solid are preferable with respect to 100 weight part of chlorine content in carbide | carbonized_material.
[0013]
DETAILED DESCRIPTION OF THE INVENTION
Next, embodiments of the present invention will be described by way of example with reference to the drawings. However, the dimensions, shapes, materials, relative arrangements, and the like of the products described in the present embodiment are not intended to limit the scope of the present invention unless otherwise specified, but are merely illustrative examples. Absent.
[0014]
[Embodiment 1: Dry grinding + carbon separator]
FIG. 1 is a process flow diagram showing an embodiment of an apparatus for producing high-quality fuel from organic waste according to the present invention. In FIG. 1, a high-quality fuel production apparatus 10 from organic waste includes a carbonization furnace 11, a heating jacket 12, a separation / extraction means 13, a quenching means 14, a cyclone 15, and an exhaust gas treatment apparatus 17. By these, the carbides described later are generated. Furthermore, the high-quality fuel production apparatus from organic waste includes a sieve 19, a pulverizer 20, and a carbon separator 21. By these, as will be described later, a high-quality fuel is produced from the generated carbide.
[0015]
Next, the operation of the high-quality fuel production apparatus 10 from organic waste according to the present embodiment will be described. By explaining this action, an embodiment of the method for producing a high quality fuel from the organic waste of the present invention will also be explained.
Organic waste is continuously supplied by a supply means (not shown) to the carbonization furnace 11 which is a heating flow system zone limited to an oxygen concentration of 5% or less. This supply means can be constituted by a crusher and a screw feeder. The carbonization furnace 11 is preferably an external heat kiln.
[0016]
In the carbonization furnace 11 which is a heating and circulation system zone, oxygen is limited, and thermal decomposition mainly including chemical bond breakage which occurs under mild conditions is a dominant reaction rather than oxidative combustion accompanied by heat generation. And the carbonization furnace 11 in which the thermal decomposition reaction is performed should always be a heating and circulation system zone which can supply the raw material system which is organic waste, and can produce | generate and take out high quality fuel. In the carbonization furnace 11, it is necessary to supply heat necessary for thermal decomposition, which is an endothermic reaction, from the outside.
[0017]
Although some oxygen of 5% or less in the carbonization furnace 11 is involved in the oxidation reaction, the oxidation under such a low oxygen partial pressure does not proceed until combustion, and in terms of giving heat from the inside by an exothermic reaction. Although contributing, local high temperature conditions cannot be reached, leading to the formation of toxic organic halides. In addition, since organic halogenated substances such as dioxins are hardly decomposed once generated, it is also important to limit the overall temperature of the carbonization furnace 11 to 300 to 800 ° C. in order to increase the yield of carbides. Element.
[0018]
Furthermore, it is desirable that the organic waste is crushed before being supplied to the carbonization furnace 11. At the time of this pulverization, it is desirable that about 0.3% of organic waste sodium carbonate is added to the catalyst and continuously supplied to the carbonization furnace 11. Here, in addition to the sodium carbonate, it is desirable to supply the carbonization furnace 11 with at least one compound selected from water vapor or metal carbonate, oxide, sulfate, and hydroxide together with organic waste.
[0019]
The addition of water vapor reduces the oxygen partial pressure in the carbonization furnace 11 to suppress a violent oxidation reaction, and water reacts with carbon in the system to produce carbon monoxide and hydrogen, thereby reducing gas. It becomes an atmosphere, suppresses the production of toxic organic halogenated compounds, and contributes to fixing the carbon content in the raw material. In addition, metal carbonates, oxides, silicates, sulfates, and hydroxides have a catalytic action to promote carbon chain scission and an action to fix free halogen in the reaction system as an inorganic substance (metal salt). It can be seen that the method of the present invention is effective in rapidly proceeding at a low temperature. Examples of these compounds include sodium carbonate, iron oxide, calcium hydroxide and the like.
[0020]
Then, high temperature exhaust gas is circulated in the heating jacket 12 of the carbonization furnace 11 to heat the inside. During a sufficiently low temperature while the temperature is rising, the inside of the carbonization furnace 11 is flushed with nitrogen or water vapor to replace a part of the air inside and keep the oxygen concentration to 5% or less. The internal temperature of the carbonization furnace 11 is controlled to 300 to 800 ° C., and the carbide obtained from the tangible waste is led to the lower part of the separation / extraction means 13 at the end of the carbonization furnace 11 to obtain the carbide and incombustible material 18, and the pyrolysis gas Is taken out from the top and supplied to the cyclone 15. The separation / extraction means 13 is, for example, a cracked gas discharge pipe and a carbide discharge port connected to a solid-gas separation port provided in the vicinity of the terminal side outlet of the carbonization furnace 11. A screw conveyor for discharge may be attached to the carbide discharge port. The carbide 18 is extracted from the lower part of the separation / extraction means 13 at the end of the carbonization furnace 11 so that the kiln content in the carbonization furnace 11 is in a steady state in balance with the supply amount of the organic waste.
[0021]
It is preferable that a heat exchanger is provided as a quenching means 14 at the lower part of the separation / extraction means 13 at the end of the carbonization furnace 11. What is necessary is just to comprise in a heat exchanger so that the carbide | carbonized_material in the middle of extraction may contact and cool the heat-transfer surface of a heat exchanger. The other surface of the heat transfer surface is cooled with a low-temperature medium such as water to remove heat. From the viewpoint of cooling efficiency, the heat transfer area of the heat exchanger should be large in a limited space. Therefore, for example, the diameter of the pipe line can be enlarged to provide a cooling jacket surrounding the outside, a multi-tube heat exchanger inserted into the path, a finned tube, or the like. In the heat exchanger, it is desirable that the carbide mainly composed of carbon extracted from the carbonization furnace 11 which is a heating flow system zone is rapidly cooled to 250 ° C. or less and extracted. This is a means for preventing the conversion to a toxic halogenated compound such as dioxin when there is a residual halogenated substance transferred to the solid phase by the thermal decomposition. This operation is necessary in order to avoid contact with oxygen in the extracted air at high temperature.
[0022]
Since the pyrolysis gas discharged from the carbonization furnace 11 contains scattered particles, the dust is removed by the cyclone 15 or the bag filter and then burned in the high-temperature combustion furnace 16. The high-temperature combustion furnace 16 is characterized in that the pyrolysis gas extracted from the carbonization furnace 11 is subjected to high-temperature combustion at 850 to 1100 ° C. The high temperature combustion furnace 16 includes, for example, a pipe for introducing a pyrolysis gas extracted from the carbonization furnace 11 and an air or oxygen-enriched air feed pipe, and a burner for burning the pyrolysis gas at a high temperature. A combustion furnace 16 having a discharge outlet. For example, depending on the use of high-temperature combustion exhaust gas or for the purpose of preventing burner blockage, a dust remover is provided in the inlet path of the combustion furnace 16 to remove solid particles accompanying cracked gas and then supplied to the high-temperature combustion furnace 16. It is also possible to do.
[0023]
This combustible (pyrolytic) gas still has a halogen source and thus contains causative agents that produce potentially toxic organic halogenated compounds, so these compounds are not produced, even if they are produced. Even if it is, it is burned in a high temperature range where it decomposes. Thereby, since the halogen contained in the system becomes hydrogen halide, it can be easily and inexpensively removed by neutralization with an alkaline substance or the like in the exhaust path. The obtained high-temperature exhaust gas can be effectively used as a heat source for heating the carbonization furnace 11 from the outside. Combustion air in the high-temperature incinerator 16 or oxygen-added air is introduced into the exhaust gas treatment device 17 through another route.
[0024]
A part of the high-temperature exhaust gas obtained in the high-temperature combustion furnace 16 is led to the lower part (heating jacket 12) of the carbonization furnace (external heating kiln) 11 and used for supplying heat necessary for decomposition, and from the outlet of the heating jacket 12 The gas after the heat supply, which is still high in temperature discharged, can be combined with a part of the high-temperature gas discharged from the high-temperature combustion furnace 16 to be used as a gas for heating the exhaust gas treatment device 17 (for example, a boiler).
[0025]
When the exhaust gas treatment device 17 is a boiler, the high-temperature boiler heating gas is guided to the boiler, where it is used as a heat source for generating steam, and the generated steam drives a steam turbine generator and is condensed by a condenser. It is also possible to return the recovered water to the boiler and circulate it again. The boiler heating gas exchanges heat in the boiler to become exhaust gas from the boiler, and can be discharged from the chimney after dust removal by the bag filter. Organic waste is treated by suppressing the production of toxic organic halogenated compounds, carbon that is the main source of carbon, which can be effectively used as resources, is acquired, and the boiler is operated by the generated heat source to operate the turbine generator The energy can be recovered effectively.
[0026]
Further, carbide and non-combustible material 18 produced in the carbonization furnace 11 or recovered by the cyclone 15 are supplied to the sieve 19. In the sieve 19, the metals remaining on the sieve 19 are collected. The carbide falling below the sieve 19 is sent to the grinder 20. The sieve 19 may be a sieve having a mesh width of 10 mm to 30 mm.
[0027]
The pulverizer 20 pulverizes the carbide (dry pulverization). Grinding the carbide has the effect of reducing the particle size of the carbide and making it easier to separate the carbide and ash that will be separated later. Examples of the pulverizer 20 include an impact pulverizer using a high-speed rotating body, a vibration mill using a medium, a tube mill, and the like.
Carbide is supplied from the pulverizer 20 to the carbon separator 21. The carbon separation device 21 sorts the carbon content (carbon-rich (rich) particles) and the ash content (ash-rich particles) based on the difference in properties. The selected carbon-rich particles become high-quality fuel. Here, the high-quality fuel is a fuel from which salts and heavy metals have been removed, and is rich in carbon, so that it is a modified carbide having a combustion calorie per weight of about 3,000 kcal / kg to 7,000 kcal / g. Means that. The feature of the shape of the carbon-rich fuel obtained in the first embodiment has a particle size (diameter) of 10 μm to 1000 μm.
Examples of the carbon separator 21 include an electrostatic separator (30, 40, 50) and a specific gravity difference separator (60, 70).
[0028]
Examples of the electrostatic separator include a rotary drum electrostatic separator 30 (FIG. 3), a conveyor belt electrostatic separator 40 (FIG. 4), and an inclined plate electrostatic separator 50 (FIG. 5). As shown in FIGS. 3 to 5, the carbide extracted from the circulation system zone is electrostatically induced by the high-voltage electrodes (31, 41, 51), so that a load having a polarity opposite to that of the high-voltage electrodes (31, 41, 51) is obtained. Is an electrostatic separation means that divides the carbon (34, 44, 54), which is a high quality fuel attracted by, and the ash that is difficult to dielectric by the high voltage electrode (31, 41, 51).
[0029]
In general, electrostatic separation is performed by utilizing a difference in chargeability due to a difference in conductivity of particles. The surfaces of the carbon-rich particles (34, 44, 54), which are conductive particles, are opposite in polarity to the high voltage electrodes (31, 41, 51) by electrostatic induction, or electrodes (32, 42) in contact with the particles. , 52) is induced, and the particles are ejected from the electrodes (32, 42, 52) in contact with the electrostatic repulsive force. On the other hand, in the ash-rich particles (33, 43, 53) that are insulating particles, since a very long time is required until dielectric charges are induced, a large electrostatic force does not act on the particles, so the particles are in contact with each other. It is difficult to jump out of the electrodes (32, 42, 52).
[0030]
In order to make a difference in charge amount by utilizing the difference in conductivity between particles, it is necessary to pass carbide particles and ash particles to be sorted through the same electric field at a constant speed. The configuration of the apparatus for passing these particles through the electric field with a constant measure includes a rotating drum (32) that conveys particles by rotating them, and a belt-conveying installation belt (42) that conveys particles by rotating them. There is a charging unit such as an inclined flat plate type ground plate (52) which is conveyed by gravity applied to the particles. Particles passing over these charging parts (32, 42, 52) are affected by the electric field of the high-voltage electrodes (31, 41, 51), which are charging electrodes, and the difference in charge amount depending on the properties of the particles. Thus, the drop positions of the particles on the partition plates (35, 45, 55) are different and sorted. The particles fall on the partition plates (35, 45, 55) are different in that the carbon-rich particles (34, 44, 54) that are conductor particles are ash particles (33, 43) that are insulator particles. 53), it is more likely to be electrostatically dielectric, so it is easy to jump out of the grounded electrodes (32, 42, 52), and the fall position is farther away from the grounded electrodes (32, 42, 52).
[0031]
The specific gravity difference separation device (60, 70) uses the wind force of the wind that gives the carbide extracted from the distribution system zone to the carbide, and has an end measure determined by the difference in specific gravity and the difference in resistance to the wind. It is a specific gravity difference separation means that divides into carbon and ash, which are high-quality fuel, due to the difference. Examples of the specific gravity difference separation device include an air table sorter 60 (FIG. 6) and a wind sorter 70 (FIG. 7). In the air table sorter 60 shown in FIG. 6, when particles having different specific gravity are put on a vibrating inclined sieve, carbon-rich particles (light product 61), which are particles having a small specific gravity, are caused by the air flowing from the lower part. The ash-rich particles (heavy product 62), which are particles having a large specific gravity that are lifted and transported downward, are separated by being transported upward by a weir 64 that is engraved in a sieve in accordance with vibration. The wind power sorter 70, which is an example of a specific gravity difference separation apparatus, is soared by air that is inserted from the raw material inlet 71 into the carbide and blown from the air inlet 72 to the air outlet 77. The carbon-rich particles that are light particles rise and enter the fine particles 76. Further, the ash-rich particles that are heavy particles descend and are separated by being stored in the coarse particle chamber 73.
[0032]
In addition, in the carbon separation apparatus 21, only an electrostatic separation apparatus or a specific gravity difference separation apparatus may be sufficient, and a specific gravity difference separation apparatus and an electrostatic separation apparatus may be combined. Here, when combining both the specific gravity difference separation device and the electrostatic separation device, the specific gravity difference separation device is preferably upstream of the electrostatic separation device.
The high-quality fuel production apparatus 10 from organic waste according to the present embodiment has an advantage that no wastewater treatment facility is required and the cost for wastewater treatment is not required.
[0033]
[Embodiment 2: Addition of alkaline solid]
Next, another embodiment 2 of the high-quality fuel production apparatus from organic waste according to the present invention will be described using the high-quality fuel production apparatus 25 from organic waste shown in FIG.
[0034]
In the high-quality fuel production apparatus 25 from the organic waste in FIG. 2, the same reference numerals as those in the high-quality fuel production apparatus 10 from the organic waste in FIG. Is omitted. A feature of the high-quality fuel production apparatus 25 from the organic waste according to the present embodiment is that an alkaline solid is added in the pulverizer 20. In addition, as an example of alkaline solid, quick lime, slaked lime, etc. are preferable, and 100 weight part-400 weight part of calcium in alkaline solid are preferable with respect to 100 weight part of chlorine content in carbide | carbonized_material.
[0035]
In the pulverizer 20, an alkaline solid such as quick lime is added to the carbide, and fine particles are formed by dry pulverization without adding water. And by a mechanochemical reaction by a physical contact action, not only an inorganic salt but also an organic chlorine, a chemical bond is cut | disconnected and a desalination reaction is caused. Here, in the mechanochemical reaction, mechanical energy of pulverization in the pulverizer 20 is converted into chemical energy that induces a change in the physicochemical properties of these substances.
[0036]
As a result, the organic chlorine remaining in the carbide without being dechlorinated in the carbonization furnace 11 can also be dechlorinated. Next, the carbides added with the alkaline solid and pulverized are sent to the carbon separator 21. Examples of the carbon separator 21 include the electrostatic separator and the specific gravity difference separator as described above. In the carbon separator 21, the carbide is separated from the incombustible material that is ash and the alkali salt generated by the desalting reaction. The separated carbides can be applied to a wider range of industrial applicability as a clean high quality fuel.
[0037]
Further, when it is desired to produce alkali mixed coal instead of clean high quality fuel, the carbon separation device 21 can be omitted in the high quality fuel production device 25 from organic waste. In the pulverizer 20, the alkaline solid is mixed and the pulverized carbide becomes an alkali mixed coal. Therefore, the carbide taken out from the pulverizer 20 as it is becomes an alkali mixed coal. Alkaline mixed coal can be used as an in-furnace desalting or soil conditioner when using fuel. The high-quality fuel production apparatus 25 from the organic waste according to the present embodiment has an advantage that no waste water treatment facility is required and the cost for waste water treatment is not required.
[0038]
【The invention's effect】
As is apparent from the above, high-quality fuel or alkali mixed coal from carbide obtained by pyrolyzing organic waste by the high-quality fuel production apparatus and production method from organic waste of the present invention. Can be manufactured.
[Brief description of the drawings]
FIG. 1 is a conceptual diagram illustrating an embodiment of a high-quality fuel production apparatus from organic waste according to the present invention.
FIG. 2 is a conceptual diagram illustrating another embodiment of an apparatus for producing high-quality fuel from organic waste according to the present invention.
FIG. 3 is a conceptual diagram illustrating an embodiment of an electrostatic separation unit according to an apparatus for producing high-quality fuel from organic waste according to the present invention.
FIG. 4 is a conceptual diagram illustrating an embodiment of an electrostatic separation unit according to an apparatus for producing high-quality fuel from organic waste according to the present invention.
FIG. 5 is a conceptual diagram illustrating an embodiment of an electrostatic separation unit according to an apparatus for producing high-quality fuel from organic waste according to the present invention.
FIG. 6 is a conceptual diagram for explaining an embodiment of a specific gravity difference separating means according to an apparatus for producing high-quality fuel from organic waste according to the present invention.
FIG. 7 is a conceptual diagram illustrating an embodiment of a specific gravity difference separating means according to a high quality fuel production apparatus from organic waste according to the present invention.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 10 High-quality fuel production apparatus from organic waste 11 Carbonization furnace 12 Heating jacket 13 Separation extraction apparatus 14 Quenching 15 Cyclone 16 Combustion furnace 17 Exhaust gas treatment apparatus 18 Carbide, incombustible material 19 Sieve 20 Crusher 21 Carbon separation apparatus (electrostatic Separation device, specific gravity difference separation device)
30 Rotating drum electrostatic separator 31 High voltage electrode 32 Ground rotating drum 33 Insulator particle 34 Conductor particle 35 Partition plate 40 Transport belt electrostatic separator 41 High voltage electrode 42 Ground belt 43 Insulator particle 44 Conductor particle 45 Partition plate 50 Inclined plate Electrostatic separator 51 High voltage electrode 52 Ground plate 53 Insulator particle 54 Conductor particle 55 Partition plate 60 Air table sorter 61 Light product 62 Heavy product 63 Input port 70 Wind sorter 71 Raw material inlet 72 Air inlet 73 Coarse grain chamber 74 Classification Tube 75 Cyclone 76 Fine granule 77 Air outlet

Claims (8)

A heating circulation system zone having a stirring means for stirring the organic waste, and an external heating means for heating the stirred organic waste from the outside to form a carbide, and limiting the oxygen concentration;
The Most sieve to recover metals from in the carbide withdrawn from the flow passage system zone,
Pulverizing means for dry pulverizing the carbide that has passed through the sieve;
An apparatus for producing high-quality fuel from organic waste, comprising: a carbon component that becomes a high-quality fuel and an electrostatic separation unit that separates the ash into a carbon component that is pulverized by the pulverization device. A heating circulation system zone having a stirring means for stirring the organic waste, and an external heating means for heating the stirred organic waste from the outside to form a carbide, and limiting the oxygen concentration;
A sieve for recovering metals from the carbide extracted from the distribution system zone ;
Pulverizing means for dry pulverizing the carbide that has passed through the sieve;
An apparatus for producing high-quality fuel from organic waste, comprising: a specific gravity difference separation means for separating the carbonized material pulverized by the pulverizing means into high-quality fuel carbon and ash. A heating distribution system zone having a stirring means for stirring the organic waste, and an external heating means for heating the stirred organic waste from the outside to form a carbide, the oxygen concentration being limited;
A sieve for recovering metals from the carbide extracted from the distribution system zone ;
Pulverizing means for dry pulverizing the carbide that has passed through the sieve;
Specific gravity difference separating means for dividing the carbide pulverized by the pulverizing means into carbon and high-quality fuel, and ash,
An apparatus for producing high-quality fuel from organic waste, comprising: electrostatic separation means for separating the carbon extracted from the specific gravity separation means into carbon and high-grade fuel and ash by electrostatic induction. The apparatus for producing high-quality fuel from organic waste according to any one of claims 1 to 3 , wherein an alkaline solid is added to the carbide in the pulverizing means. A supply step of supplying organic waste to a heating distribution system zone in which oxygen concentration is limited to 5% or less and heated from the outside;
A heating step of heating from the outside of the heating and circulation system zone while maintaining the inside of the heating and circulation system zone at a temperature of 300 ° C to 800 ° C;
And recovering at sieve metals carbide withdrawn from the flow passage system zone,
Dry pulverizing the carbide that has passed through the sieve;
A method for producing a high-quality fuel from organic waste, comprising: a step of electrostatically separating the carbonized pulverized carbide in the pulverizing step into a carbon component that becomes a high-quality fuel and an electrostatic separation step that separates the ash into an ash component. A supply step of supplying organic waste to a heating distribution system zone in which oxygen concentration is limited to 5% or less and heated from the outside;
A heating step of heating from the outside of the heating and circulation system zone while maintaining the inside of the heating and circulation system zone at a temperature of 300 ° C to 800 ° C;
Recovering the metals in the carbide extracted from the flow zone by sieving;
Dry pulverizing the carbide that has passed through the sieve;
A method for producing high-quality fuel from organic waste, comprising: a step of separating a specific gravity difference separating the carbonized material pulverized in the pulverizing step into carbon and high-quality fuel. A supply step of supplying organic waste to a heating distribution system zone in which oxygen concentration is limited to 5% or less and heated from the outside;
A heating step of heating from the outside of the heating and circulation system zone while maintaining the inside of the heating and circulation system zone at a temperature of 300 ° C to 800 ° C;
Recovering the metals in the carbide extracted from the flow zone by sieving;
Dry pulverizing the carbide that has passed through the sieve;
A specific gravity difference separation step of dividing the carbide pulverized in the pulverization step into a carbon component that becomes a high-quality fuel and an ash component;
A method for producing a high-quality fuel from organic waste, comprising: an electrostatic separation step in which the carbide extracted in the specific gravity separation step is electrostatically induced to divide it into a carbon component that becomes a high-quality fuel and an ash component. In the said grinding | pulverization step , alkaline solid is added to the said carbide | carbonized_material, The high quality fuel manufacturing method from the organic waste in any one of Claims 5-7 characterized by the above-mentioned.

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