JP2010155231A6 - Method and apparatus for low-temperature decomposition treatment of processed material - Google Patents

Abstract

An object of the present invention is to detoxify exhaust gas by ashing by subjecting a treated product to low-temperature decomposition treatment to drastically reduce ash emission.
According to the present invention, a processing object is introduced from the upper part of a processing apparatus, the lower part of the processing object is heated, and magnetized air that has passed a magnetic field of 0.25 Tesla to 1.0 Tesla is contained in the processing object. In order to carbonize and incinerate by sequentially decomposing the processed material from the lower part thereof, along with the natural exhaust from the exhaust pipe on the one side upper part of the processing apparatus, The magnetized air is allowed to naturally flow in, and with the progress of the process from the vicinity of the inflow of magnetized air, the weight of the undecomposed portion on the upper part of the treated object is added and the cavities are prevented from being hollowed out. The object was achieved by a low-temperature decomposition treatment method for a treated product characterized in that the treated product is continuously treated by sequentially adding new treated products as the treated product decreases.
[Selection] Figure 1

Description

  In the present invention, treated materials containing organic matter (industrial waste, household waste, all other waste) are passed through a strong magnetic field at a low temperature (250 ° C. to 400 ° C.), low oxygen (hereinafter “magnetization”). Ashes that are decomposed using 0.25 Tesla (2500 gauss) to 0.5 Tesla (5000 gauss), called “air”, and splatters other than metal, glass, stones, and concrete (hereinafter referred to as metal) The present invention relates to a method and an apparatus for low-temperature decomposition treatment of a processed product that can reduce the residue other than the metal or the like extremely (eg, 1/90000).

  Conventionally, there has been proposed a device for decomposing waste under a strong magnetic field to decompose the waste at a low temperature without generating dioxin, which has been put into practical use based on each feature. For the magnetization of the air, it is also known to use a permanent magnet of 0.4 Tesla (4000 Gauss) to 0.45 Tesla (4500 Gauss) and a heating temperature of 350 ° C. to 400 ° C.

Utility Model Registration No. 312682 JP 2006-289296 A JP 2006-150295 A JP 2004-33966 A

  Conventionally, a technique for drying, carbonizing, and then ashing waste by heat of low-temperature heating of ash (for example, 350 ° C.) and magnetized air (for example, magnetic force of 0.45 Tesla (4500 gauss)) is disclosed. (Patent Document 1), however, there is a problem that not only processing time is long (for example, processing time of 10 hours or more), but processing defects often occur. Also, depending on the material of the waste, there is a strong odor in the flue gas, and this has been deodorized by flooding etc., but there was still a point to be improved.

  In Patent Document 2, the waste introduced into the sealed container is irradiated with a minute amount of air that has been activated by passing through a magnetic field, whereby the waste is decomposed and reduced in volume without burning. A waste treatment furnace is disclosed.

  Further, an organic substance is accommodated in a reaction vessel formed of a ferromagnetic material, and a pair of magnets arranged so that the N pole and the S pole are opposed to each other with an external conduit communicating with the inside of the reaction vessel interposed therebetween. There is a proposal of a technique for causing a magnetic field vibration in an organic substance and decomposing it (Patent Document 3). According to Patent Document 3, the decomposition process of organic matter is described for the time being, and 100 kg of raw garbage, 100 kg of waste paper, 100 kg of gypsum board and 150 kg of wood waste are charged and processed at a peripheral wall temperature of 50 ° C. to 60 ° C. for 24 hours. It is stated that it became ash. It is unclear whether the temperature of the central part is several times or only a chemical change in the above, but it can be treated with a solid material such as a tire or plastic alone, or it must be mixed with other combustible materials This is completely unknown, and there is no new technology that can be used stably.

  Patent Document 4 is a treatment method in which waste is thermally decomposed in a gas atmosphere containing negative ions, and is opened to an incinerator, an intake passage communicating with the incinerator, and an upper portion of the incinerator. The method is carried out by a waste treatment apparatus including a magnet installed in an exhaust passage and the intake passage.

  In the present invention, during the treatment of the treatment product (waste), the treatment product accommodated in the lower part of the treatment chamber is agitated so that the thermal decomposition treatment in the part is rationalized and equalized, and the treatment time is reduced to 20 times. % To 40% (for example, 10 hours was changed to 8 to 6 hours), and a stable treatment was observed. The reason is considered to be that the magnetized air uniformly comes into contact with the treatment by agitation, and the supply of magnetized air is rationalized, and as a result, the overall processing capacity is improved. Stirring is 1 to 2 times in 2 to 4 hours, and 5 to 10 minutes is sufficient for one stirring time (for example, the rotating shaft rotates 5 to 10 times per minute).

As described above, in the decomposition process, stirring is required when processing a product that is likely to be crosslinked, but stirring is not required when processing a product that cannot be crosslinked. For example, when the decomposition product is crushed small in advance (for example, about 5 cm) and does not crosslink, a stirring device is unnecessary. Originally, the decomposition process proceeds sequentially from the lower part of the processing chamber, so even if crosslinking is possible, it seems that the supporting force is weak. Therefore, if the next processed materials are put together, the pressure is applied to the vicinity of the semi-processed material in the processing chamber due to the weight of the processed material, so that crosslinking cannot be performed. Therefore, it can be seen that stirring is not required except for a specific processed product. For example, since the processed materials to be put together are approximately 150 kg to 700 kg at 1 m ³ , if this is accommodated in the upper portion of the processing tank, the weight of 150 kg to 700 kg is applied to the upper portion of the untreated material in the processing tank. There will be no risk of occurrence.

  By the agitation, the lower end of the processed product and the red hot part of ash (for example, ceramic ash) are always in close proximity and facing each other, and the processed product is rapidly dried by the radiant heat of the ceramic ash and magnetized air. And carbonized, and then promote ashing.

Conventionally, the treatment of the processed product takes 10 hours or more and is unstable. However, according to the present invention, the treatment time is several hours (4 to 7 hours / 1 m ³ ), and the efficiency is improved by continuous operation. As a result, it was found that stable treatment was possible. Further, depending on the material of the treated material, the odor of the exhaust gas may increase. However, the present invention has succeeded in removing the odor and deodorizing and removing foreign matter by flooding and magnetization by introducing the exhaust gas into the treatment tank.

  In the above, what generates odor is, for example, in the case of treatment of a treated product containing a large amount of sulfur oxides or nitrogen oxides such as tires, etc., but there is little odor in the treatment of household waste. Is normal.

  Further, in view of the fact that the lower end of the processed material thrown into the processing chamber often forms a bridge, making it difficult to perform efficient treatment, the present invention sometimes breaks the cross-linking so that the processed material and the ceramic ash Combined treatment of thermal radiation of ceramic ash with ionized oxygen (ionization by passing through a strong magnetic field) and other activated air by optimizing the relationship and bringing in uniform contact with magnetized air with controlled air volume. Thus, the conventional problems are solved. The amount of oxygen in the above is less than the amount of oxygen necessary for combustion, but the proportion varies depending on the material of the waste. Therefore, the best value is determined experimentally.

  The magnetized air in the above is normally naturally flowed along with the exhaust, but a fan can be interposed in the magnetized air passage to control the inflow of magnetized air.

  Furthermore, the increase in ash can be reduced by carrying out steady treatment with the best treatment condition. As described above, there is a result that no increase in ash is observed by continuously operating in a good state.

  That is, according to the present invention, the processed material is charged from the upper part of the processing apparatus, the lower part of the processed material is heated, and the magnetization passes through a magnetic field of 0.3 Tesla (3000 Gauss) to 1.0 Tesla (10000 Gauss). Air is introduced into the processed material, and the processed material is sequentially decomposed from the lower portion thereof to carbonize and ash, and with the natural exhaust from the exhaust pipe on one side upper portion of the processing device, the processing is performed. Magnetized air naturally flows into the lower inner side of the apparatus, and the processed object gradually descends due to the weight of the undecomposed portion at the upper part of the processed object as the process proceeds from the vicinity of the inflow of the magnetized air. Is a low-temperature decomposition treatment method for a treated product, characterized by continuously treating a treated product by sequentially adding a new treated product as the treated product decreases, from the exhaust pipe of the processing device. With the natural exhaust of While allowing natural air to flow in and adjusting the amount of air flowing in, the magnetized air naturally flows out from a supply pipe projecting into the apparatus from the lower side wall of the processing apparatus to the center, and the magnetized air is processed. The inside of the peripheral part of the device is lowered, and the central part is raised to cause convection up and down.

  In the above, the temperature of ash is maintained by the heat of decomposition. Since the decomposition heat is used for drying heat of the heat-treated product of the exhaust, the balance between generation and consumption is maintained, and there is no possibility of increasing to 400 ° C. or higher. Even if the ash is not initially heated, the ash is heated with the progress of decomposition. However, since it takes a long time for the first time, it is preferable to start by heating the ash.

  In another aspect of the invention, the exhaust from the exhaust pipe is smoked and deodorized in a deodorizing and deodorizing treatment tank to be deodorized and deodorized. In this case, an intermittent charging method is employed in which a new treated material is introduced when a void is generated in the material, and the treated material is industrial waste, household waste, or other waste containing organic matter. To prevent cavitation, the vicinity of the lower part of the processed material is periodically stirred, or the weight of the new processed material is eliminated, and the inside of the upper part of the processing device is actually decompressed so that the internal gas is removed when the lid is opened. It prevents it from being discharged.

  Next, according to the present invention, a processing object is introduced from the upper part of the processing apparatus, the central lower part of the processing object is heated to generate an updraft, and a downward airflow is generated on the inner wall portion of the processing apparatus to move the magnetized air up and down. By conducting convection and guiding magnetized air that has passed through a magnetic field of 0.25 Tesla (2500 Gauss) to 1.0 Tesla (10000 Gauss) into the treatment object, the treatment object is sequentially decomposed from the lower part thereof, The treated material is carbonized and then incinerated, and magnetized air is naturally introduced into the lower inside of the processing device along with exhaust from the exhaust pipe on one side of the processing device, and the processing of the processed material proceeds. Accordingly, the processed material is gradually lowered by adding the weight of the undecomposed portion at the upper part thereof to prevent its hollowing, and as the processed material decreases, a new processed material is sequentially added to the processed material. Automatic continuous processing A method for low-temperature decomposition treatment of a treated product, characterized in that magnetized air is automatically introduced and the amount of inflow air can be adjusted with exhaust from an exhaust pipe of a processing apparatus. 1 is a method for low-temperature decomposition treatment of a treated product.

  In addition, a heating chamber is provided in the lower part of the bottomed cylindrical processing apparatus, a processing object is accommodated in the upper part of the heating chamber, magnetized air is supplied, and a double-walled processing chamber for processing is continuously provided. In the lower part of the heating chamber and the processing chamber, a plurality of air supply pipes of magnetized air are installed in a plurality of horizontal directions vertically from the side wall toward the center, and the air supply pipes are connected to a magnetizing cylinder for magnetizing the inflowing air. A processing material inlet is provided at the upper part of the processing chamber, an exhaust pipe is continuously provided, an opening / closing lid is covered with the input port, a processing tank is connected to the exhaust pipe, and a vertical convection in the processing chamber is provided. For this purpose, vents are provided in the upper and lower parts of the double wall, a stirring device for the processed material that can be operated from outside the processing apparatus is installed in the lower part of the processing chamber, and a residue outlet is provided in the lower part of the side wall of the heating chamber. , A low-temperature decomposition treatment apparatus for the treated product, characterized in that the residue outlet is covered with an open / close lid, Smoke and deodorize with water. Inside the magnetized cylinder, one end of the magnetized air supply pipe is connected, the other end is opened to the outside, and a permanent magnet for high magnetization is inserted in the center. The agitator is equipped with a ventilation pipe, and the agitation device is constructed by horizontally laying one or a plurality of rotating shafts with a plurality of stirring rods projecting from the lower part of the processing chamber, and one end of the rotating shaft is connected to the processing device. It protrudes out of the wall to form a protrusion, and a handle is attached to the protrusion.

  Further, when the stirring device is provided, the number of rotation shafts is three, two rotation shafts are installed in parallel on the upper part, and the other one rotation shaft is connected to the lower part of the middle of the two rotation shafts. One end of the exhaust hose is connected to the upper part of the opening / closing lid or the processing chamber, the other end of the exhaust hose is connected to the exhaust pump, and the discharge side of the exhaust pump is connected to the processing tank. The treatment tank for smoking and deodorizing is connected vertically to the inside of the cylindrical tank by a plurality of partition plates to form a vertically bent channel, and the upper part of the cylindrical tank. A water pipe is installed in the pipe and piped so that it can be watered in the upper part of the flow path.

  The treated materials mentioned above are industrial waste, household waste, and other treated materials containing organic matter, and all other unnecessary materials such as stone, glass, concrete, and ceramics are included.

  The ceramic ash in the present invention is residual ash (inorganic), mud or stone powder left after processing the processed product, but also includes ash obtained by processing a normal processed product. It can be attached at the time of processing equipment sale. When the processing apparatus is used for the first time, 5 kg to 10 kg of ceramic ash is accommodated in the processing chamber, the ceramic ash is heated to 350 ° C. to 400 ° C. with a gas burner or the like, and then the processed material is charged (or The ceramic ash may be heated after adding the treated product), and the treated product can be decomposed continuously after the soaking. When the processing is stopped, the ceramic ash is buried and its function is preserved for 100 to 120 hours. It was recognized that if the processed material was introduced during this period, the processing was started again immediately. Therefore, at the end of work in the evening in a production plant, etc., even if all the processed material for the day is put into the processing equipment and only the ceramic ash remains the next morning, if the processed material for the evening of that day is input, the next morning It can also be used by repeating the process of becoming ceramic ash and interruption. In the above description, the ceramic ash is heated in the first use. However, instead of the gas burner, a slight amount of combustible material such as paper (for example, 1 kg) is burned to create an upward flow, and magnetized air may be introduced. .

  In the above, the ceramic ash maintains a constant amount (amount initially supplied, for example, 10 kg to 30 kg) and does not increase even if the decomposition process is continued. Further, since the maximum temperature is 400 ° C., the outer wall of the processing apparatus is 60 ° C. or less, and there is almost no possibility of causing burns even if it is touched with bare hands. In addition, since the outer wall of the processing chamber is doubled, there is no possibility of igniting or damaging other objects. Furthermore, if a heat exchanger is installed in the processing chamber, hot water can be obtained by heat exchange with the gas in the processing chamber.

In the above experiment, ranch waste (rice husk, straw, cow dung, etc.) was put into 1 m ³ every 8 hours in an experimental processing apparatus with a capacity of 1 m ³ in the processing chamber and continuously treated for 200 hours or more. ) Was stabilized at a slight increase (20% to 30% increase), and no increase was observed after the eyelid.

In the present invention, the continuous supply of the processed material is performed when the processing of the previously input processed material has progressed and the volume has been reduced by half. For example, if a space of 1 m ³ is formed after ^{3 to} 4 hours have passed after the initial treatment product of 2.0 m ^{3 is} added to the processing chamber capacity of 2.0 m ³ , 1 m ³ of treatment material is replenished, If an additional 1 m ³ of processed material is added every 4 hours, this processing apparatus can be used most efficiently.

  In the above, the stirring device is used for about 5 minutes every 1 to 2 hours. If the stirring device automates the rotation of the stirring shaft using an electric circuit with a timer, the periodic stirring can be fully automated. In an area where there is no power transmission / distribution facility, a power source necessary for the automation can be obtained by, for example, a combination of power generation using sunlight and a battery.

Although the introduction of the processed material in the above-described manner involves human power, the automatic operation of the introduction of the processed material can be achieved by connecting an automatic input device to the input port of the decomposition processing device. For example, in the case of an apparatus that inputs 1 m ³ of processed material every 4 hours, the input amount per day is 6 m ³ , so that a lower portion of a hopper that can store the processed material 6 m ³ is connected to the upper part of the processing apparatus. If a fixed amount charging device is attached to the lower part of the hopper and this charging device is automated, the processing object can be fully automatically charged. Therefore, if the worker supplies a processed product of 6 m ³ once a day to the hopper, the processed product for one day is processed fully automatically thereafter.

Since the maximum temperature of decomposition heat of the processed product is 400 ° C. (usually 250 ° C. to 350 ° C.), even if the processing capacity decreases or is interrupted due to any failure, there is a thermal hazard to the outside. There is no fear of reaching. However, if the processing material inlet of the processing apparatus is left open, the processing object may burn at normal temperature due to the supply of oxygen, but because of the structure of the processing apparatus, there is no risk that the lid will automatically open. It is safe without fear. Even if there is a case where it is unintentional that the operator forgets to close the lid, the operator should notice that the white smoke is suddenly raised by the lid and combustion starts. Even if it may not be noticed, according to the above example, if the processed material of 2 m ³ is combusted, the combustion is completed, so there is no risk of other harm. Further, if the processing device is closed, intake is performed by the amount of exhaust (strictly speaking, the amount of intake is small by the amount of water vapor), so there is no risk of explosion due to an increase in atmospheric pressure. If the exhaust port is closed, the intake air is lost and the processing of the processed material is automatically interrupted.

  The inflow of magnetized air in the invention is determined by the exhaust amount. Therefore, if the moisture of the processed product evaporates due to the heating of the ceramic ash, the amount of suction of magnetized air temporarily decreases as the amount of evaporation increases. Moreover, further comparison tests are required for the amount of magnetized air inhaled and the efficiency of the treatment of the treated material. However, in the treatment of current waste with 20% to 80% moisture, automatic inflow (magnetized air) due to natural exhaust is not possible. Although it is recognized as good, a manual valve is provided on the suction side, and the amount of magnetized air sucked can be controlled by the processed material. In addition, various conditions (water content of waste, material, shape of equipment, dimensions, and magnetic strength) affect the efficient heating with ceramic ash and the setting of inflow of magnetized air corresponding to this, so the best conditions In order to obtain, you have to go through many experiments.

  Although the magnetization of the air is not theoretically clarified, it is said that the organic matter is decomposed using the magnetized air in the known example (for example, JP-A-2006-150295). In addition, several years of experimentation and research have been repeated to complete this invention. For example, it has been proved that 1.0 Tesla (10000 Gauss) has higher decomposition efficiency and can be equally decomposed than 0.3 Tesla (3000 Gauss) even in terms of magnetic strength. Although it has been confirmed that the amount of intake air is related to this case, the best magnetic strength must be awaited for future research due to the material and humidity of the treated material. Although magnetized air is used for the above circumstances, it is considered that air is activated by a strong magnetic field and promotes decomposition of organic matter. There is also a theory that the cylindrical device is a ferromagnetic material, so that the decomposition is accelerated. In addition, although the magnetic strength exceeded 0.4 Tesla (4000 Gauss) and experimented to 1.0 Tesla (10000 Gauss), the treatment state is more stable at 0.5 Tesla (5000 Gauss) or more. ing.

  As the apparatus of the present invention, since the air supply pipe of the magnetized air protrudes from the heating chamber to the lower part of the processing chamber in multiple stages, it becomes possible to supply the magnetized air to the inside of the processing object to be processed, The processing conditions were made uniform, the processing state was improved, the processing time was shortened, and continuous processing was possible in the best processing state regardless of the material of the processed material.

  In addition, since at least the side wall of the processing chamber is a double wall and vent holes are provided above and below to circulate and flow the magnetized air, the magnetized air generates up-down convection. That is, an upward flow is generated by the temperature of the heated ash (250 ° C. to 400 ° C.) in the heating chamber at the bottom. Accordingly, the magnetized air becomes an upward flow inside, becomes a downward flow at the peripheral wall portion (double wall), partially becomes exhaust, and new magnetized air is sucked in by the exhaust amount.

  As described above, the heat of decomposition is used for decomposition, and the remainder gathers in the ash, warms and raises the magnetized air, and radiates infrared rays to the lower side of the processed material to accelerate its drying and decomposition. . Due to the presence of the heated ash, it was possible to confirm the decomposition efficiency and the stability and certainty of the decomposition.

  According to the invention, one end of the exhaust hose is connected to the opening / closing lid or the upper part of the processing chamber, and the other end of the exhaust hose is connected (directly or indirectly) to the exhaust pump. The top of is depressurized. Therefore, it is possible to prevent the gas (odor and exhaust) in the processing chamber from coming out.

  Moreover, if a stirring apparatus is provided in the lower part of a process chamber and a process thing is stirred manually or automatically, the bridge | crosslinking of the process object accompanying a progress of a process will lose | eliminate, and an equal process will be performed. Accordingly, the processing time can be greatly shortened, and a rapid homogeneous process can be performed regardless of the material of the processed material. In the above, since no cross-linking is made depending on the size of the treated product, stirring is unnecessary.

  According to the present invention, a processed product is heated and dried by ceramic ash heated to 250 ° C. to 400 ° C. and magnetized air that has passed a magnetic field of 0.3 Tesla (3000 Gauss) to 1.0 Tesla (10000 Gauss). Since it is carbonized and then ashed, it has the effect of automatically and continuously decomposing and detoxifying it without depending on combustion or other external heat.

  In particular, since the air supply pipe is provided laterally toward the central portion of the heating chamber and the processing chamber and the air is supplied, there is an effect that the magnetized air can be evenly supplied into the processing object.

  Further, when a stirring device is provided in the upper part of the heating chamber and the lower part of the processing chamber, it is possible to prevent the cross-linking during the decomposition treatment of the processed material, to facilitate the uniform processing, and to shorten the processing time.

  Furthermore, since residual ash can be treated to prevent an increase in residual ash, there is no amount of residual ash taken out during continuous processing of processed products, or a small amount of residual ash is prevented from filling the combustion chamber in advance. There is a possible effect. Furthermore, there is an effect that the decomposition process can be rationalized by adjusting the amount of magnetized air.

(A) The block diagram of the Example of this invention, (b) The block diagram of the Example of the purified water in exhaust processing similarly. The front view of the Example of the apparatus which implements the method of this invention. The rear view which abbreviate | omitted a part similarly. The side view which abbreviate | omitted a part similarly. The top view which abbreviate | omitted a part similarly. Sectional drawing which abbreviate | omitted one part. Similarly, a longitudinal side view with a part omitted (cross-sectional line omitted). The cross-sectional top view which abbreviate | omitted a part similarly. The longitudinal cross-sectional view which abbreviate | omitted a part which shows piping of vaporized air similarly. The longitudinal cross-sectional view which abbreviate | omitted a part of the processing tank of smoke removal / deodorization similarly. The front view of the Example of another apparatus similarly. Similarly rear view. Similarly right side view. Similarly left side view. FIG. (A) The cross-sectional enlarged view which abbreviate | omitted one part, (b) The same partially enlarged cross-sectional view. The cross-sectional enlarged view which abbreviate | omitted one part. The cross-sectional enlarged plan view which abbreviate | omitted a part similarly. Similarly the enlarged plan view of a magnetization case. Sectional drawing which abbreviate | omitted a part of Example of the other apparatus similarly. (A) Sectional drawing which abbreviate | omitted a part of other Example similarly, (b) Explanatory drawing which shows the operation state of the steering wheel operation in (a). (A) The longitudinal cross-sectional view which abbreviate | omitted a part of other Example of the deodorizing processing tank similarly. (B) The cross-sectional view which abbreviate | omitted one part. (A) The partial sectional view which abbreviate | omitted a part of the Example which similarly attached the heat exchanger. (B) The top view which abbreviate | omitted partially. (C) The partially enlarged view which shows the example of the power of a partition lid similarly. The conceptual diagram of the Example which similarly shows an example of the automatic injection apparatus of a processed material.

According to the present invention, an appropriate amount of ceramic ash (for example, 30 kg if the capacity of the heating chamber capacity is 0.3 m ³ ) is accommodated in the heating chamber of the processing apparatus and heated to 250 ° C. to 350 ° C. (or initially heated). even without ash is heated automatically by the decomposition heat of the workpiece), the processing chamber (e.g., volume 2m ³⁾ to the processing of the processing device (industrial waste, such as a mixture of food residue and plastic containers) 2m ³ And seal the cover at the cover. An exhaust pipe is connected to the upper portion of the processing apparatus, and the exhaust pipe is connected to an exhaust treatment tank.

  Under the above conditions, the treated product is dried by radiant heat and magnetized air of the ceramic ash, then carbonized and further ashed, but a large amount of water vapor is generated and flows out of the exhaust pipe during drying. Therefore, when the inside of the processing apparatus is in a depressurized state, air to be magnetized flows from one end of the magnetized cylinder installed at the lower part of the processing apparatus, so that the processed product is moved to the lower part by the red heat radiation of the ceramic ash and the magnetized air. Then, the dry decomposition process proceeds, followed by carbonization and ashing.

  Therefore, when treated for 1 to 2 hours, the lower part of the treated product may form a bridge and the distance from the ceramic ash may increase. In this case, the stirring shaft is rotated and the bridge is broken by stirring. Then, the processed material falls onto the ceramic ash, is heated under magnetized air and carbonized, and then ashed. Although depending on the material and shape of the processed material, if the weight of the processed material that has not been decomposed is added to the processed material being decomposed, the crosslinking is naturally eliminated.

When a sufficient gap is formed in the upper part of the processing apparatus in this way, the lid is opened and a necessary amount of processed material is replenished. For example, when the initially filled processed material 2m ³ becomes 1m ³ , the processed material 1m ³ is newly added. If the shortage is added in this way, a processed product of 1 m ³ or more always remains in the processing apparatus and the pressure is lowered by its own weight, and the processed product is continuously processed in the same state. Depending on the material of the workpiece, treated product was 2m ³ accommodated, because it is 1 m ³ at 4 to 5 hours, add-on is carried out every 4 to 5 hours.

  If a hopper for inputting a processed material is connected to the upper portion of the processing apparatus and the processed material for one day is accommodated in the hopper, the processed material is successively lowered by its own weight, and automatic continuous charging processing is performed. If it does in this way, if a processed material is thrown into a hopper once a day, automatic continuous processing can be performed.

An embodiment of the present invention will be described with reference to FIG. 1A. Separately produced ceramic ash is accommodated in a heating chamber of a processing apparatus. For example, if the capacity of the heating chamber is 0.3 m ³ , 30 kg of ceramic ash is accommodated therein, and 2 m ^{3 of} processed material is charged into the processing chamber above the heating chamber (the processing chamber has a volume of 2 m ³ ). When the ash is heated to 350 ° C., the lower part of the treated product is dried by the radiant heat of the ceramic ash, and the treated product is sequentially decomposed in combination with the active oxygen, hydrogen and the radiant heat generated by the sucked magnetized air. It is carbonized and then incinerated by low-temperature decomposition treatment.

As described above, when the processed product is ashed, the volume rapidly decreases. Therefore, the input processed product is successively lowered by its own weight, and halved in 3 to 4 hours. Therefore, the opening / closing lid of the charging port of the processing apparatus is opened, and 1 m ³ of the processed material is charged. That is, the processed material initially charged at 2 m ³ is halved in 3 to 4 hours. The treated material in the above refers to miscellaneous waste including, for example, industrial waste (wood, plastic product waste, expired food, factory waste), household waste, and other organic matter.

  Next, an embodiment of the present invention will be described with reference to FIG. 1 (b). The exhaust of the processing apparatus is guided to a processing tank, deodorized and deodorized by flooding, and the gas is released to the outside, or the magnetic treatment is deodorized. To the outside world. In this case, the presence or absence of the magnetization process is performed by switching the valve. For example, if there is a risk of residual odor due to the material of the processed material (for example, when it contains sulfide such as rubber processed material), the exhaust gas is applied with a magnetic field of 0.25 Tesla (2500 Gauss) to 0.4 Tesla (4000 Gauss). In this case, since the exhaust temperature is relatively low (for example, 150 ° C. or less), there is no risk of thermal degradation of the magnet, and the same deodorizing performance can be maintained over a long period of time.

  Next, the water in the treatment tank is purified by a ceramic ball layer or other filtration layer, and solids are separated and fed to the pump chamber, and again watered by the pump. That is, since the brine is circulated and used after the water purification treatment, the deodorization and deodorization treatment can be reliably performed with a relatively small amount of water. Therefore, if only natural reduction of circulating water due to flooding is supplemented, continuous operation can be performed for a long time. The airless solid in the above is discharged as purified soil, so there is no risk of environmental pollution.

As described above, if the processed material is charged to 1 m ³ every predetermined time (for example, 4 hours), the processed material can be continuously processed using the processing apparatus. In this way, in the experimental processing apparatus of the example, a processed product of about 6 m ³ per day (24 hours) could be processed.

The above is the case where the processed product is processed by packing it in a cardboard box as it is in principle, but when the generated processed product is crushed (average size is about 5 cm), the decomposition efficiency is improved by 50% or more. did. According to the result of the experiment, the treatment of 6 m ³ per day was improved to about 10 m ³ per day. By crushing Moreover, when you size having an average 2 cm, the decomposition efficiency is further improved, resulting ^{12m 3 ~15m} 3 experiments. As is clear from the above, if the surface area of the processed material is increased, the decomposition efficiency can be increased. Therefore, if a relatively small processing device and a crushing device are used in combination, a small high-performance decomposition device can be used. It can be.

  The exhaust generated by the low-temperature treatment may have a bad odor depending on the type of treated material (for example, synthetic resin waste or old tires), so it is put into a deodorizing / deodorizing tank (processing tank) and deodorized with water, and then magnetized. And release it to the outside world. As described above, since the chamber is depressurized by exhaust, magnetized air automatically sucks an amount commensurate with the amount of exhaust (effectively commensurate with the sum of the amount of generated water vapor and magnetized air) and supplies it to the heating chamber and the processing chamber. I care. This air supply amount can be adjusted by the degree of restriction of a valve provided in the suction portion. When the amount of air to be supplied (that is, the amount of oxygen) is large, the ashing process cannot be performed by the intended low-temperature decomposition because of normal oxidation combustion. Although the experimental treatment apparatus of the above example was continuously burned for 240 hours, it was confirmed that the lamix ash exceeded the initially supplied ceramic ash of 30 kg and increased slightly (about 35 kg).

  As described above, since 60 m3 of the processed product was processed in 240 hours, the ash should be 90 kg to 100 kg due to an increase of 60 kg or more of the inorganic substance. However, 35 kg of ash is initially 30 kg of ash, 55 kg to 65 kg. Ashes have disappeared. The reason for this is unknown, but it is thought that ash was also vaporized and discharged.

  The above-mentioned decomposition is considered as follows for a carbohydrate which is one of organic substances.

(1) C ₁₂ H ₂₂ O11 = 12C + 11H ₂ + 5.5O ₂
(2) C ₁₂ H ₂₂ O11 = C + 11CO + 11H _{2
(3) C 12 H 22 O11} = 12C + 11H 2 O
The result of the experiment also showed an increase in moisture (a larger amount of drainage than the amount of water added for draining and deodorizing treatment was observed).

  An embodiment of the present invention will be described with reference to FIGS. 2, 3, 4, 5, 6, and 7. A heating chamber 3 having an inverted trapezoidal cross section is provided on the bottom plate 2 of the apparatus body 1 having a square cylindrical shape. A processing chamber 4 is connected to the upper part of the heating chamber 3, a top plate 6 having an inlet 5 is provided on the upper part of the apparatus main body 1, and an opening / closing lid 7 is crowned on the inlet 5 of the top plate 6. 10 (FIGS. 6 and 7).

  A horizontal shaft 40 is fixed to the base end of the opening / closing lid 7 (FIG. 2), and the horizontal shaft 40 is rotatably attached to the top plate 6 of the processing apparatus 10 by retaining rings 41, 41. The support rod 42 parallel to the horizontal shaft 40 is fixed, the housings 43 and 43 are fixed to both ends of the horizontal shaft 40 and the support rod 42, and the opening / closing lid 7 is matched to the horizontal shaft side ends of the housings 43 and 43. Weight weights 44, 44 are fixed. In the drawing, 45 and 45 are latching pieces of the opening / closing lid 7, 46 is an exhaust pipe, 47 is an opening / closing lid for a residue outlet, and 48 is a handle of the opening / closing lid 47 (FIG. 2).

  In the heating chamber 3 of the apparatus main body 1 and the lower portion of the processing chamber 4 (FIG. 6), supply pipes 8 and 8 are provided in multiple stages in the horizontal direction from the left and right side walls 4a and 4b (slanted wall side). The air supply pipes 8 and 8 are longer in the center of the lower stage and project shorter in the upper stage, and the base ends of the air supply pipes 8 and 8 of each row are connected to the air supply pipes 9 and 9 for each row, respectively. The base ends (lower parts) of the pipes 9 and 9 are connected to connecting pipes 15 connected to the ventilation pipes 13 in the magnetizing cylinder 11 (FIG. 9). It is installed. Therefore, one end of the vent pipe 13 of the magnetizing cylinder 11 is opened to the outside of the apparatus main body 1 so that air can be freely sucked. A valve (not shown) is provided in the vent pipe 13, and the opening degree is adjusted by the valve so that the amount of air supplied can be controlled. In FIG. 5, 14 is a valve handle for adjusting the amount of magnetized air.

  A 0.8 Tesla (8000 gauss) permanent magnet 16 is fitted and installed in the vent pipe 13 (FIG. 9). The permanent magnet 16 is provided with a yoke (not shown), and the relationship between the permanent magnet 16 and the yoke is to provide a magnetic flux that is reasonably concentrated by the yoke. The specific shape and installation structure are not specified, and a conventionally known magnetic flux collecting structure using a yoke can be used as it is or improved.

  Further, the exhaust pipe 17 of the processing apparatus 10 is connected to a smoke / deodorant treatment tank 18 (FIG. 7). The smoke / deodorant treatment tank 18 is vertically partitioned by a plurality of partition plates 19a, 19b, 19c, 19d, 19e, and the exhaust gas can be bent and flow by opening sequentially above or below the partition plates. At the same time, a soaking pipe 20 is provided at the top, and the flue gas is purified by soaking (FIG. 10). In the above description, the flue gas enters the smoke / deodorant treatment tank 18 as shown by an arrow 21 in FIG. 7, and solids are separated and dropped by the water particles discharged from the submerged pipes 20, 20, and the smoke is absorbed and cleaned. At the same time, particles are separated and dropped during bending flow as indicated by arrows 21, 22, 23, 24, 25, 26, 27, and 28 in FIG. Accordingly, the foreign matter adhering to the water droplets and the particles dropped during the bending flow are mixed in the waste water accumulated on the bottom of the tank and are discharged from the drain pipe 29 as indicated by an arrow 30. A smoke passage pipe 31 is interposed on the upper part of the partition plate 19b, and permanent magnets 33 and 33 are fixed together with the discharge pipe 32. Therefore, if solid matter is mixed in the exhaust gas passing through the passage pipe 31 and the drain pipe 32, this is magnetized (or ionized) to form agglomerate, which increases its own weight and falls or decomposes odor. The exhaust can be cleaned (FIG. 10).

  Therefore, the exhaust gas is almost completely cleaned by flooding, magnetization by the permanent magnet, and foreign matter. However, since the temperature of the exhaust gas is 150 ° C. or less at the highest, even if this treatment tank is used for many years, there is no possibility that the magnetization capacity of the permanent magnet will be lowered or that aging will occur. Therefore, the flue gas in the treatment of general waste becomes colorless (or only light water vapor) and is purified to such an extent that fine solids are hardly found. In the figure, 49 and 50 are water supply pumps, 51 is a water supply pipe for supplying water to a flooded pipe, and 52 is a water level.

  Stirring shafts 34, 34 are horizontally mounted at predetermined intervals on the upper portion of the heating chamber 3 of the processing apparatus (FIG. 6), and stirring is performed below the middle portion of the stirring shafts 34, 34 (almost at the intermediate height of the heating chamber). A shaft 35 is installed in parallel with the stirring shafts 34, 34, and a plurality of stirring rods 36, 36 project from the stirring shafts 34, 35. The stirring rods 36 of the stirring shafts 34 and 35 are for the purpose of preventing cross-linking of the input processed products, and there are no particular limitations on the number and position of the stirring rods (FIGS. 6 and 8). In the above description, the handle 37 is fixed to the stirring shaft 35, the gears (34a, 35a) are fixed to the stirring shafts 34, 35, and the gears are engaged with each other. , 35 can be rotated (FIGS. 6 and 8).

  The processed material 53 (FIG. 6) is dried from the lower surface side, carbonized, and incinerated, so that the processed material 53 is processed from the lower surface, but sometimes does not come into contact with the inner wall of the heating chamber 3 and fall. In some cases, a cavity 54 is formed in a bridged state (for example, a convex arc shape because processing proceeds only at the center lower surface and peripheral processing does not proceed) (FIG. 6). In such a case, the intensity of the radiation due to red heat of the ceramic ash with respect to the lower surface of the waste is increased, resulting in a slow processing speed, and there is a risk of processing delay as a whole. In such a case, by holding the handle 37 of the stirring shaft (FIG. 2) and rotating the stirring rod 36, it is possible to easily break the bridge and return to normal processing. In the above, the gear is fixed to the stirring shaft 35. For example, sprockets 34a and 34a are fixed to the stirring shafts 34 and 35 of the handle 37, respectively, and a chain is attached to the sprocket to rotate the stirring shafts 34 and 35 simultaneously. (FIG. 8).

  The rotation interval of the agitation shaft varies depending on the material of the processed material, but the object can be achieved by rotating about once every 1 to 2 hours and about 1 to 5 minutes (5 to 10 rotations per minute). ). For example, when replenishing the processed material once every four hours, it is considered that the object can be achieved by rotating once or twice between each replenishment.

  There is no specific number and structure for the number of the stirring shafts 34 and 35 and the installation position, but the number is 2 to 3 and the position is preferably in the vicinity of the heating chamber 3.

  Since the heating chamber 3 of the present invention is a low-temperature treatment, there is no need for special consideration on the side wall of the processing apparatus 10, etc. It is preferable to use a double wall (for example, an outer wall 1a and an inner wall 1b are provided with a space of 2 cm to 5 cm apart) (FIG. 6). Further, hot water can be generated by flowing water through a pipe connecting the water supply pipe 38 and the hot water supply pipe 39, and this hot water can be used for greenhouse heating or the like.

  In the above, when water is supplied directly to the double wall without connecting the water supply pipe 38 and the water supply pipe 39 with a pipe, it is necessary to divide the double wall into one for heat exchange and one for lowering the magnetized air. In other words, the double wall is also used for lowering the magnetized air while also serving as heat insulation.

  In some cases, a heat insulating plate is sandwiched between the double walls. For example, there is a case where it is necessary to take care not to let the heat generated inside during the cold district specification escape to the outside.

  In the above embodiment, the ash in the heating chamber 3 is heated to around 300 ° C. by the decomposition heat, so the inflowing air is heated to become an upward flow (indicated by arrows 90 and 91 in FIG. 6), part of which is indicated by the arrows. It descends through the double wall as shown by 92 and 93, enters the heating chamber 3 from the lower part as indicated by arrows 94 and 94, and circulates and flows. Accordingly, since the magnetized air passes through the processed object 53 through heating, the processed object 53 is uniformly heated, dried, decomposed and processed. In FIG. 6, the double wall and the air supply pipe 9 are overlapped with each other. However, since the air supply pipe is installed in the double wall, there is no problem in the circulation of the magnetized air.

  According to this apparatus, since the heating chamber 3 is in the lower part and the air in the vicinity is heated, vertical convection can be naturally generated without using any power. Therefore, the decomposition efficiency can be optimized without using power.

  Another embodiment of the present invention will be described with reference to FIGS. 11 to 18. A funnel-shaped heating chamber 63 is provided on a bottom plate 62 of a rectangular cylindrical apparatus body 61, and the upper portion of the heating chamber 63 is disposed in a processing chamber. 64 (FIG. 16), a top plate 66 having an insertion port 66a is fixed to the mouth of the apparatus main body 61, and an opening / closing lid 67 is crowned on the insertion port 66a so as to be freely opened and closed (FIGS. 13 and 16).

  The mouth of the apparatus main body 61 is opened obliquely with the front wall 61a side lowered (the left side in FIG. 13 is the front side), and the opening / closing lid 67 has an arrow 56 centered on the support shaft 55 at the rear edge. (FIG. 13).

  At the upper part of the heating chamber 63 of the apparatus main body 61 and the lower part of the processing chamber 64, air supply pipes 68, 68 are provided in the upper and lower multi-stages (FIG. 16) in the horizontal direction from the left and right side walls 64a, 64b. Are diagonally cut 68a downward. The air supply pipe 68 is provided to supply magnetized air. However, the air outlet 68 is inclined downward 68a as described above so as not to be blocked by the charged material, or the net 68b is covered. You can also.

  The proximal ends of the air supply pipes 68, 68 are connected to header pipes 57, 57 installed on the bottom plate 62 of the apparatus main body 61 (FIGS. 16, 20). The header pipes 57, 57 are connected to the magnetizing case 71. The vent pipe 73a communicates with the vent pipe 74a of the magnetizing case 71, and a valve 74 is interposed between the vent pipe 73a and the vent quantity (magnetized air) can be adjusted by the handle of the valve 74 (FIGS. 18 and 19). The vent pipe 74a opens to the outside and can suck air freely. A permanent magnet body 75 of 0.4 Tesla (4000 Gauss) to 0.8 Tesla (8000 Gauss) is installed in the magnetized case 71, and the air flows through the gap 78 between the magnetic poles N, S76, 77. Magnetized (FIG. 19), the vent pipe 73a is connected to the vent pipe 73.

Therefore, when magnetized air is blown out from the supply pipes 68, 68 into the processing chamber 4, the magnetized air enters the heating chamber 63 and the processing chamber 64, acts on the ash and the processed material, dries the processed material, and carbonizes. And ash. During processing, gases such as CO, H ₂ O (vapor), H ₂ , O ₂ , NO _{2 and} other wastes are decomposed, and metals, ceramics (stones, glass) and other inorganic substances are present. Remains as metal and ash.

If the decomposition treatment is continued as described above, the ash is also slightly changed into a gas (for example, Ca, Si, etc.). For example, even if the processed material of 8 m ³ per day is processed continuously for 30 days, the amount of ash corresponding to the amount of processed material does not increase (for example, when the capacity of the processing chamber is 2 m ³ , the ash amount is only 30 kg to 40 kg. )

  The opening / closing lid 67 and the exhaust pipe 65 provided on the top plate 66 are connected by hoses 69 and 69 (FIG. 15), and the exhaust pipe 65 and the suction port of the exhaust pump 70 are connected by a pipe 72 to discharge the exhaust pump 70. The outlet and the deodorizing / smoke removing treatment tank 79 are connected by an exhaust pipe 80. Therefore, when the exhaust pump 70 is operated when the processing object is introduced using the open / close lid 67, the upper gas in the processing chamber 64 is sucked into the exhaust pipe 65 as indicated by an arrow 129 through the exhaust hose 69. The upper part of the processing chamber 64 immediately becomes negative pressure, and external air flows into the upper part of the processing chamber 64. That is, it is possible to prevent the exhaust in the processing chamber 64 from flowing out to the outside. During general processing, the pump 70 is normally stopped, so there is no risk that the exhaust from the processing chamber will flow forcibly.

  The exhaust gas that has entered the treatment tank 79 is subjected to a deodorizing action and a particle separating action by watering treatment (the description is omitted as in the second embodiment). The exhaust from the treatment tank 79 enters the centrifuge 82 through an exhaust pipe 81 connected to the upper part of the treatment tank 79, separates solid matter, and is discharged to the outside as indicated by an arrow 83 (FIG. 11). , 12, 15). When the centrifuge 82 is not entered, it is discharged as indicated by an arrow 83a.

  A rotating shaft 58 is installed horizontally to the center of the processing chamber 64 (approximately the same height as the highest air supply pipe), and a stirring plate 59 is provided on the rotating shaft 58 so as to project one end of the rotating shaft 58. And the handle 60 is fixed to the protruding portion. Therefore, when the handle 60 is rotated, the stirring plate 59 is rotated to stir the lower portion of the processing chamber 64, thereby preventing the cross-linking of the processed product (FIGS. 14 and 20).

  Although the manual handle 60 has been exemplified above, the rotation and the stirring action can be automatically given every set time if the rotation is rotated by a motor and a timer is provided in the motor circuit. In the figure, 84 is an opening / closing lid for the ash inspection port, 85 is an opening / closing lid for the inspection port at the bottom of the processing chamber, 86 is an opening / closing lid for the water level inspection port of the processing tank 79, and 87, 87 are opening / closing lids for the inspection port above the processing tank 79. It is.

  In the above embodiment, if the exhaust gas is treated with water, the odor will be almost zero. However, when this processing apparatus is installed in a ship or other sealed chamber, it is preferable not to generate a trace amount of odor. If it is used in combination with the agent coating, odorlessness can be achieved.

  In the processing apparatus of the present invention, when processing wood, oil may be mixed in water and flow down along the inner wall of the apparatus. In such a case, a liquid tray 156 is installed inside the lower part of the apparatus, and the liquid (mixed water and oil) is received in the liquid tray 156. In this case, since the liquid flows down along the inner side, the receiving tray 156 is connected to the inner wall 158 and the upper portion is covered with a lid 157 (to prevent ash and the like from entering). In this case, since the ambient temperature can be 150 ° C to 250 ° C, the water inevitably evaporates and the oil content is concentrated, so the oil content is extracted to the outside, and sawdust, paper, etc. are mixed and decomposed. For example, no special consideration is required for the oil generated inside.

  Next, an experimental example of the present invention (the amount of ceramic ash unchanged) will be described.

[Experimental Example 1]
1. Test items:
(1) Quantitative evaluation (a) Reduction of general waste (weight / volume)
(B) Disappearance of ceramic ash (2) Qualitative evaluation (a) Ceramics and disappearance of general waste 2. Implementation date October 24-December 9, 2007 3. place:
3. Nasu Kashiyama City, Tochigi Prefecture, etc. Implementation procedure (1) Processing capacity of cow dung, etc. During the 14-day test period, about 3 to 4 tons (4-5 m ³ ) of cow dung and litter are put into the processor every day, and no ash etc. are taken out.

  Confirm that ash and other residues do not increase despite the increased throughput.

(2) Industrial waste treatment capacity During the 14-day test period, 2 to 3 tons of industrial waste is put into the treatment equipment every day, and no metal or concrete pieces are taken out.

  Confirm that ash and other residues do not increase despite the increased throughput.

5). Test results (1) Wastes that maintain a certain level of quality, such as cow dung and bedding discharged from the ranch Despite the introduction of about 50 tons of cow dung, carbide (black) and ash (gray) in the processing machine In addition, there is no change in the visual amount of the ceramic ash (white), and there is no change in the overall processing speed.

  During this time, it is considered that ash and the like have not been removed at all and disappeared inside the processing machine.

(2) Disposal of industrial waste at industrial waste disposal sites During the period, an increase in the amount of residue (ash) in the processing machine was visually observed despite an estimated 35 tons of industrial waste being input. There wasn't.

In addition, miscellaneous things such as wood chips, waste plastics, various packaging containers, wastes from pets, papers, automobile tires, polyurethane bumpers, and the like were directly put into these wastes.

  During this time, the ash was not removed at all, except for the metal, gravel, and concrete pieces such as steel wires of the tire that came out at the bottom of the processor once a day. It is thought that it has disappeared inside.

  An embodiment of the input drying according to the present invention will be described with reference to FIG. An auxiliary cylinder 61 a having the same cross section is provided continuously on the upper portion of the apparatus main body 61 except for the top plate. Instead of the top plate, the support plates 95 and 95 of the input material are rotatably supported from the horizontal position to the vertical position by the support shafts 96 and 96 as indicated by arrows 88 and 88, and the processing chamber 64 and the drying chamber. Divided into 97. A drying air blow-off port 98 is provided at a lower part of one side of the drying chamber 97, and an exhaust port 99 is provided at an upper part of the other side. The exhaust port 99 is connected to a suction device 100 (blower) through a pipe 101. The suction device 100 is connected to the cooler 102, the cooler 102 is connected to the heater 103, one end of the hose 104 is connected to the air supply side of the heater 103, and the other end of the hose 104 is connected to the outlet 98. Concatenate with

  In the above description, when the aspirator 100 is driven to cause the air to flow as indicated by arrows 105, 106, 107, 108, and 109, the humid air sucked by the pipe 101 is cooled by the cooler 102 to form water droplets. As a result, the drain is discharged from the drain pipe 110 as indicated by an arrow 111, and thus becomes dry air. By the heater 103, the dry air is heated to 70 ° C. to 80 ° C. and passes through the hose 104 as indicated by an arrow 207. And enters the drying chamber 97 and passes through the input 112 while drying. According to the apparatus, since the humid air separates moisture by cooling and becomes dry air by heating, the humid air can be dried with high efficiency and the input is heated (for example, around 90 ° C.). The decomposition efficiency in the chamber 64 can be improved. In the seed decomposition, the decomposition efficiency is remarkably reduced for an input having a water content of 70% or more, but it has been confirmed that even an input having a water content of 90% can be efficiently dried to a water content of 60% or less. Therefore, although energy is consumed by the drying, the loss energy can be sufficiently repaired by improving the decomposition efficiency.

  The fourth embodiment is a pre-drying of the processed product, but is disposed on the upper part of the apparatus main body 61. Therefore, the processing of the dried processed product is exactly the same as the third embodiment. That is, the apparatus main body 61 in FIG. 20 is exactly the same as the apparatus main body in FIG. 16, and is given the same reference numerals. Therefore, the description about the decomposition | disassembly process of a processed material is abbreviate | omitted.

A description will be given of another embodiment of the present invention (apparatus that does not discharge odor when the lid is opened / closed) with reference to FIG. An auxiliary cylinder 112 having an input volume (for example, 1 m ³ ) that can be processed at a time with the same cross-sectional area is connected to the upper portion of the apparatus main body 61, and the support plates 113 are opposed to the upper inner side of the apparatus main body 61. Then, the rotation shafts 114 and 114 are installed horizontally along the inner wall of the apparatus main body 61 so that the front ends of the support plates 113 and 113 can be airtightly overlapped.

  Inside the auxiliary cylinder 112, the guide plates 115, 115 are inclined and arranged in a funnel shape, and the lower end surfaces of the guide plates 115, 115 and the upper surfaces of the support plates 113, 113 are in airtight contact. preferable. In this way, the auxiliary cylinder 112 on the upper part of the apparatus main body 61 is double-tightened by the support plates 113 and 113 and the lid 116.

  In the above description, if the processed product at the lower part of the apparatus main body 61 is disassembled and the processed product at the upper part moves as indicated by an arrow 117 so that the support plates 113 and 113 can be returned to the horizontal position, the rotating shaft When the handles 118 and 118 of the 114 and 114 are rotated as indicated by arrows 119 and 119 to return the support plates 113 and 113 to the horizontal position and the handles 118 and 118 are locked, the upper portion of the apparatus main body 61 is sealed. be able to. Therefore, even if the lid 116 is opened as indicated by an arrow 121, there is no possibility that the exhaust in the apparatus main body 61 leaks to the outside.

  Then, after accommodating the processed material 122 on the support plates 113 and 113, the lid 116 is sealed, and the handles 118 and 118 are rotated as indicated by arrows 123 and 123, so that the support plates 113 and 113 are indicated by arrows 124, If it opens like 124, the processed material 122 will fall like an arrow 126 with dead weight. In this case, since the lid 116 is sealed, there is no possibility that the exhaust in the processing apparatus is discharged to the outside. As described above, exhaust leakage when replenishing the processed material 122 using the support plates 113 and 113 and the lid 116 can be prevented in advance.

  Another embodiment of the deodorizing process of the present invention will be described with reference to FIG. Although the deodorizing process has been described in the processing tank 18 (FIG. 10), the sixth embodiment is different from the second embodiment. That is, the inside of the processing tank 130 having a rectangular cross section is divided into a plurality of chambers (for example, eight chambers) by a plurality of partition plates 131a and 131b. The partition plate 131a is provided with a vent 132 at the lower end, and the partition plate 131b is provided with a water vent 133 at the lower end and a vent 134 at the upper end. Therefore, the smoke that has entered from the exhaust pipe 17 as indicated by arrow 136 flows as indicated by arrows 137, 138, 139, 140, 141, 142, 143, 144, and 145 and is discharged from the exhaust pipe 46 to the outside. .

  A water supply pipe 146 is installed inside the upper part of the treatment tank 130, and a plurality of flooding pipes 147 and 147 are connected to the water supply pipe 146. In addition, a pump chamber 148 is installed in the lower part of the processing tank 130, and a purification chamber 149 is connected to the pump chamber 148. Then, the water that has been flooded from the flooded pipe 147 as indicated by arrow 150 flows on the bottom of the treatment tank 130 as indicated by arrow 151, enters the purification chamber 149, passes through the filter layer 175 made of ceramic balls, Passes through the filter 152 and enters the pump chamber 148. Therefore, the submersible pump 153 in the pump chamber 148 supplies water from the water supply pipe 154 through the water supply pipe 146 to the flooded pipe 147 and then floods from the flooded pipe 147.

The ceramic balls are, for example, hard barley stones having a diameter of 5 mm to 20 mm made of SiO ₂ , Al ₂ O ₃ , Na ₂ O, K ₂ O, or SiO ₂ , Al ₂ O ₃ , Na ₂ O, TiO ₂ components. In the ceramic ball, the circulating water by the pump is purified by the ceramic ball. Ceramic balls generate far infrared rays and decompose organic substances in water, so that they have a so-called self-cleaning ability and can be used continuously for a long time. According to the trial operation, the self-cleaning ability did not deteriorate even after 6 months to 1 year of continuous use.

  It is also effective to use a mixture of zeolite and shell fossil as a filter layer in place of the ceramic balls, but further examination is required for the purification of waste water caused by the magnetic decomposition of organic matter as in the present invention.

  When solid matter (mainly sand 177) is deposited in the lower part of the purification chamber 149, it is discharged from the drain pipe 178 as indicated by an arrow 176. Since the solid 177 is purified by a ceramic ball, there is no odor even if it is taken out to the outside, and it can be abandoned freely without fear of environmental pollution.

  Further, when the circulating water in the pump chamber 148 decreases, the water can be freely supplied from the water supply pipe 178 as shown by the arrow, so there is no possibility of causing shortage of the circulating water. A magnetic deodorizer 135 may be installed in the exhaust pipe 46. The magnetic deodorizer 135 is provided with a strong magnetic field of 0.3 Tesla (3000 Gauss) to 0.4 Tesla (4000 Gauss), and can decompose the odor of the passing exhaust gas. For example, there is an effective deodorizing effect when a slight odor remains even after the deodorizing process, such as when a rubber material is processed.

  An embodiment of batch loading of processed materials according to the present invention will be described with reference to FIG. In the fifth embodiment, the charging device that does not leak odor when the lid is opened has been described. FIG. 23 is a charging device having the same concept as that of FIG. Therefore, it is preferable to appropriately select and use the apparatus and the apparatus of Example 7 according to the properties of the processed material. That is, the lower end portion of the hopper 162 is connected to the insertion port edge of the top plate 161 of the apparatus main body 160, and the partition lid 163 is covered with the input port 159 so as to be freely opened and closed. A palate 164 is crowned on the mouth of the hopper 162 so as to be freely opened and closed.

  Two grooves 155 are provided on the upper surface of the partition lid 163 in parallel with the opening / closing direction of the partition lid 163, and racks 165 and 165 are provided in the grooves 155, respectively, and pinions 166 are provided on the racks 165 and 165. The shaft 167 of the pinion 166 is connected to the shaft of the reduction motor 168. As described above, by providing the rack 165 in the groove, the partition lid 163 and its upper surface contact portion can be easily kept airtight.

  In the above, when the motor 168 is started and the pinion 166 is rotated in the direction of the arrow 169, the partition lid 163 moves in the direction of the arrow 170 and opens, and the pinion 166 is indicated by the arrow in the opposite direction. When rotating in the direction of 175, the partition lid 163 is closed. A heat exchanger 171 is installed on the inner wall of the apparatus main body 160. In the figure, 172 is a water supply pipe, and 173 is a hot water supply pipe. Since there is no restriction | limiting about the specific shape of the said heat exchanger 171, it is the same as that of the heat exchanger used for the heat exchange between the conventionally known steam. Therefore, either a multi-tube type or a thin plate type can be used. A rack 165 is provided in the groove 155 so that the upper end of the rack does not protrude from the groove 155.

  Since the heat exchanger 171 is installed from the inner central portion of the apparatus main body 160 to the upper side, the heat exchanger 171 has an effect of lowering the exhaust temperature and preventing the heat dissipation from the wall surface, but lowers the decomposition efficiency of the processed material. There is no fear. This is because even if the heat exchanger 171 is installed, there is no possibility that the temperature of the decomposed portion of the processed product will decrease.

  In the above-described embodiment, when the processed material 125 is charged, the partition lid 163 is closed, the mouth lid 164 is opened, and the processed material 125 is loaded into the hopper 162 as indicated by an arrow 127. Next, when the partition lid 163 is opened after closing the palate 164, the processed material falls into the apparatus main body 160 by its own weight as indicated by an arrow 128. Further, when there is not enough space in the apparatus main body 160 to drop all the processed material in the hopper, the processed material 125 remains in the hopper, but the palate 164 is closed, so that the exhaust leaks to the outside. It is not. That is, the leakage of the exhaust gas to the outside at the time of introducing the treatment object is prevented in advance.

Another embodiment of the present invention (automatic supply of the processed material) will be described with reference to FIG. 24. A hopper 182 is continuously provided on the falling top 79 of the upper top plate 181 of the apparatus main body 180, and the mouth portion of the hopper 182 is provided. An open / close lid 183 is installed to be openable and closable. The hopper 182 can accommodate a processing amount of one day (24 hours) by the apparatus main body 180 (for example, 6 m ³ if the capacity can be processed in 1 m ³ 4 hours). A partition lid 174 is provided at the dropping port 179 so as to be freely opened and closed. The partition lid 174 can be opened or closed by sliding automatically or manually as indicated by an arrow 159.

  In the above embodiment, the open / close lid 183 is closed by protruding the rod 185 of the air cylinder 184 in the direction of the arrow 186 and opened by retracting in the direction of the arrow 187. In the figure, reference numerals 188 and 189 denote supply and exhaust pipes. The supply air is supplied from a compressor (not shown) and is adjusted by a valve (not shown) interposed in each of the supply and exhaust pipes 188 and 189. That is, when pressurized air is supplied to the supply / exhaust pipe 188, a piston (not shown) fixed to the rod 185 moves in the direction of the arrow 187, so the rod also moves in the same direction, and the opening / closing lid 183 Since it rotates in the direction of the arrow 191 around the support shaft 190, the lid is opened.

  Next, when pressurized air is supplied to the air supply / exhaust pipe 189, the piston fixed to the rod 185 moves in the direction of the arrow 186, so that the opening / closing lid 183 is centered on the support shaft 190 in the direction of the arrow 192. Since it rotates, the open / close lid 183 is closed.

    Since the above is the operation of the opening / closing lid 183 using the air cylinder 184, the detailed description is omitted. In the figure, 193 is an exhaust pipe, and 194 is a belt conveyor used when a processed material is introduced.

DESCRIPTION OF SYMBOLS 1 Apparatus main body 2 Bottom plate 3 Heating chamber 4 Processing chamber 5 Input port 6 Top plate 7 Opening and closing lid 8 Air supply pipe 9 Air supply pipe 10 Processing apparatus 11 Magnetizing cylinder 12 Valve 13 Vent pipe 14 Valve handle 15 Connection pipe 16 Permanent magnet 17 Exhaust pipe 18 Smoke / deodorant treatment tank 19 Partition plate 20 Flooded pipe 29 Drain pipe 31 Passing pipe 32 Discharge pipe 33 Permanent magnet 55 Support shaft 57 Header pipe 58 Rotating shaft 59 Stirring plate 60 Handle 61 Apparatus body 63 Heating chamber 64 Processing chamber 65 Exhaust cylinder 67 Opening / closing lid 68 Air supply pipe 69 Exhaust hose 70 Exhaust pump 71 Magnetizing case 73 Vent pipe 79 Treatment tank 80 Disposal pipe 81 Exhaust pipe 82 Centrifuge 97 Drying chamber 100 Suction device 102 Cooler 103 Superheater 130 Treatment tank 131a Partition plate 131b Partition plate 148 Pump chamber 149 Water purification chamber 160 Device body 163 Setsufuta 164 palate 171 heat exchanger 174 the partition cover 180 device body

Claims (13)

  A processing object is introduced from the upper part of the processing apparatus, the lower central part of the processing object is heated to generate an ascending air current, a descending air current is generated on the inner wall of the processing apparatus, and magnetized air is vertically convected. The magnetized air that has passed through a magnetic field of 25 Tesla to 1.0 Tesla is guided into the treatment object, and the treatment object is sequentially decomposed from the lower part thereof to carbonize the treatment object, and then ash it. With the exhaust from the exhaust pipe on the upper side of the apparatus, magnetized air is allowed to flow into the lower inner side of the processing apparatus, and as the processing of the processed object proceeds, the processed object has its own undecomposed portion weight. Is added to prevent the hollowing out of the processed material, and with the decrease in the processed material, the processed material is automatically continuously decomposed by intermittently introducing a new processed material. Decomposition method.   2. The method for low-temperature decomposition of a processed product according to claim 1, wherein magnetized air is automatically flowed in along with the exhaust from the processing apparatus, and the amount of the flow-in air can be adjusted.   2. The method for low-temperature decomposition of a processed product according to claim 1, wherein the magnetized air is caused to flow out from a supply pipe projecting and installed in a plurality of upper and lower stages into the apparatus from the lower side wall of the processing apparatus toward the center.   The method for low-temperature decomposition treatment of a treated product according to claim 1, wherein a heat exchanger is installed on the inner wall of the treatment apparatus to exchange heat between the internal gas and water to generate hot water.   2. The method for low-temperature decomposition treatment of a treated product according to claim 1, wherein the exhaust from the exhaust pipe is subjected to a soaking treatment with circulating water in the smoke-eliminating / deodorizing treatment tank and smoke-deodorizing treatment is performed.   2. The low temperature of the processed product according to claim 1, wherein an intermittent charging method is employed in which a new processed product is input without discharging exhaust gas when processing of the processed product proceeds and a gap is generated in the upper portion of the processing apparatus. Decomposition method.   2. The method of low-temperature decomposition treatment of a treated product according to claim 1, wherein the prevention of cavitation is performed by periodically or irregularly stirring the vicinity of the lower part of the middle of the input treated product, or preventing crosslinking by the weight of the treated product. .   A processing material input hopper is provided inside the upper part of the processing apparatus, a partition plate is provided at the lower part of the input hopper, an opening / closing lid is provided at the upper part, and the partition plate and the opening / closing lid are alternately opened and closed to input the processing object. The low-temperature decomposition processing method of the processed material of Claim 1 characterized by the above-mentioned.   A heating chamber is provided in the lower part of the bottomed cylindrical processing apparatus, a processing object is accommodated in the upper part of the heating chamber, magnetized air is supplied, and a double-walled processing chamber for processing is continuously provided, In the lower part of the heating chamber and the processing chamber, magnetized air supply pipes are installed in a plurality of horizontal directions in multiple upper and lower stages from the side wall toward the central part, and the air supply pipes are connected to a magnetized cylinder for magnetizing the inflow air, Provided with a processing material inlet at the top of the processing chamber, and connected to an exhaust pipe, covered with an opening / closing lid, connected to the exhaust pipe, a processing tank, and a submerged pipe in the processing tank A water circulation device is provided, vents are provided above and below the double wall for vertical convection in the processing chamber, and a residue outlet with an open / close lid is provided at the bottom of the side wall of the heating chamber. Low-temperature decomposition processing equipment for processed products.   A heating chamber is provided in the lower part of the bottomed cylindrical processing apparatus, a processing object is accommodated in the upper part of the heating chamber, magnetized air is supplied, and a double-walled processing chamber for processing is continuously provided, In the lower part of the heating chamber and the processing chamber, magnetized air supply pipes are installed in a plurality of horizontal directions in multiple upper and lower stages from the side wall toward the central part, and the air supply pipes are connected to a magnetized cylinder for magnetizing the inflow air, Provided with a processing material inlet at the upper part of the processing chamber, connected to an exhaust pipe, covered with an opening / closing lid, connected to a processing tank to the exhaust pipe, for vertical convection in the processing chamber A low-temperature decomposition treatment apparatus for a treated product, wherein a vent is provided in the upper and lower portions of the double wall, and a heat exchanger is installed on the inner wall of the treatment chamber.   The processing tank low-temperature decomposition treatment apparatus according to claim 9 or 10, characterized in that the treatment tank is vertically partitioned by a plurality of partition plates, and is provided with a vertically bent flow path for exhaust gas, and smoke is removed and deodorized by flooding. .   The magnetized cylinder is provided with a magnetized air supply pipe connected to one end, the other end opened to the outside, and a vent pipe interposing a permanent magnet for high magnetization at the center. The low-temperature decomposition processing apparatus of the processed material of 9 or 10.   The low-temperature decomposition treatment apparatus for processed products according to claim 9 or 10, wherein the brine in the treatment tank is obtained by a circulating fluidizer through a filtration layer.

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