WO2008026248A1 - Équipement de décomposition thermique à champ magnétique - Google Patents

Équipement de décomposition thermique à champ magnétique Download PDF

Info

Publication number
WO2008026248A1
WO2008026248A1 PCT/JP2006/316938 JP2006316938W WO2008026248A1 WO 2008026248 A1 WO2008026248 A1 WO 2008026248A1 JP 2006316938 W JP2006316938 W JP 2006316938W WO 2008026248 A1 WO2008026248 A1 WO 2008026248A1
Authority
WO
WIPO (PCT)
Prior art keywords
magnetic field
external
ring
waste
outside air
Prior art date
Application number
PCT/JP2006/316938
Other languages
English (en)
Japanese (ja)
Inventor
Hatsuo Maeda
Original Assignee
Shiny World Co., Ltd.
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Shiny World Co., Ltd. filed Critical Shiny World Co., Ltd.
Priority to PCT/JP2006/316938 priority Critical patent/WO2008026248A1/fr
Publication of WO2008026248A1 publication Critical patent/WO2008026248A1/fr

Links

Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23L—SUPPLYING AIR OR NON-COMBUSTIBLE LIQUIDS OR GASES TO COMBUSTION APPARATUS IN GENERAL ; VALVES OR DAMPERS SPECIALLY ADAPTED FOR CONTROLLING AIR SUPPLY OR DRAUGHT IN COMBUSTION APPARATUS; INDUCING DRAUGHT IN COMBUSTION APPARATUS; TOPS FOR CHIMNEYS OR VENTILATING SHAFTS; TERMINALS FOR FLUES
    • F23L1/00—Passages or apertures for delivering primary air for combustion 
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
    • F23G5/24—Incineration of waste; Incinerator constructions; Details, accessories or control therefor having a vertical, substantially cylindrical, combustion chamber
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
    • B09B—DISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
    • B09B3/00—Destroying solid waste or transforming solid waste into something useful or harmless
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
    • B09B—DISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
    • B09B3/00—Destroying solid waste or transforming solid waste into something useful or harmless
    • B09B3/40—Destroying solid waste or transforming solid waste into something useful or harmless involving thermal treatment, e.g. evaporation
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B19/00—Heating of coke ovens by electrical means
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B47/00—Destructive distillation of solid carbonaceous materials with indirect heating, e.g. by external combustion
    • C10B47/02—Destructive distillation of solid carbonaceous materials with indirect heating, e.g. by external combustion with stationary charge
    • C10B47/12—Destructive distillation of solid carbonaceous materials with indirect heating, e.g. by external combustion with stationary charge in which the charge is subjected to mechanical pressures during coking
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B49/00—Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated
    • C10B49/02—Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated with hot gases or vapours, e.g. hot gases obtained by partial combustion of the charge
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B51/00—Destructive distillation of solid carbonaceous materials by combined direct and indirect heating
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B53/00—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23L—SUPPLYING AIR OR NON-COMBUSTIBLE LIQUIDS OR GASES TO COMBUSTION APPARATUS IN GENERAL ; VALVES OR DAMPERS SPECIALLY ADAPTED FOR CONTROLLING AIR SUPPLY OR DRAUGHT IN COMBUSTION APPARATUS; INDUCING DRAUGHT IN COMBUSTION APPARATUS; TOPS FOR CHIMNEYS OR VENTILATING SHAFTS; TERMINALS FOR FLUES
    • F23L2900/00—Special arrangements for supplying or treating air or oxidant for combustion; Injecting inert gas, water or steam into the combustion chamber
    • F23L2900/00001—Treating oxidant before combustion, e.g. by adding a catalyst

Definitions

  • the present invention allows natural air to flow magnetized air into a pyrolysis chamber.
  • the present invention also relates to a magnetic field pyrolysis apparatus capable of decomposing various types of waste in a pyrolysis chamber at a relatively low temperature without generating dioxin or the like.
  • a conventional magnetic field pyrolysis apparatus is provided with a number of external airflow inlets at the lower portion of a side wall of a heat-resistant container formed of a heat-resistant member forming a thermal decomposition treatment chamber, and the external airflow inlets are led out from the respective ends.
  • a pair of permanent magnets for example, N pole magnets and S poles, sandwiching the outer pipe to magnetize the outside air flowing into the outer pipes.
  • Patent Document 1 Japanese Patent Application Laid-Open No. 2001-304520
  • Patent Document 2 JP 2006-150295 A
  • Patent Documents 1 and 2 a permanent magnet is provided outside the outer pipe, for example, held in a case made of resin, and magnetizes the outside air by these permanent magnets.
  • a permanent magnet is provided outside the outer pipe, for example, held in a case made of resin, and magnetizes the outside air by these permanent magnets.
  • the present invention has been made paying attention to such problems, and by stably magnetizing the outside air flowing into the thermal decomposition chamber, it is possible to obtain a stable thermal decomposition operation state.
  • An object of the present invention is to provide a magnetic field pyrolysis apparatus that can do this.
  • a magnetic field pyrolysis apparatus provides: A thermal decomposition chamber is formed and a heat-resistant container made of a heat-resistant member, a plurality of external airflow inlets provided on the side wall of the heat-resistant container, and each external airflow inlet is led out, and external air can be taken in from the end An external pipe line, a permanent magnet provided on the external pipe line, and an exhaust path communicating with an upper position of the pyrolysis chamber, and the outside magnetized by the permanent magnet
  • the permanent magnet is a ring-shaped magnet, and the ring It is characterized in that a magnet is inserted into the outer pipe.
  • the outside air passing through the outer conduit passes through the ring-shaped magnet in a state of being in contact with or very close to the conventional one.
  • the outside air can be magnetized well, and thus stable thermal decomposition operation status can be achieved. Obtainable.
  • a magnetic field pyrolysis apparatus according to claim 2 of the present invention is the magnetic field pyrolysis apparatus according to claim 1,
  • the ring-shaped magnet is a ring-shaped magnet having N and S poles in the thickness direction, and the plurality of ring-shaped magnets are inserted into the outer pipe line so that opposing faces thereof are different poles. It is characterized by that.
  • the outside air passes through the ring of the ring-shaped magnet, so that a large magnetic field change is applied to the outside air.
  • a larger magnetic field vibration can be applied to the outside air, and adjacent ring magnets are inserted so that the opposite faces have different poles, so that magnetic flux also exists between these adjacent ring magnets.
  • the magnetizing process is performed, so that it is possible to apply a large magnetic field vibration by the magnetizing process without filling the outside air efficiently. Furthermore, it is possible to obtain a defined operating state of thermal decomposition.
  • the magnetic field pyrolysis apparatus according to claim 3 of the present invention is the magnetic field pyrolysis apparatus according to claim 1 or 2, A predetermined number of end portions of the external pipe line are connected to each other, and a chamber portion having an outside air intake port having a predetermined size is provided.
  • the amount of outside air that flows in by using the individual valves arranged on each of these external pipes is reduced by, for example, discarding the inside of the thermal decomposition treatment chamber due to inflow of excessive outside air. It is necessary to make adjustments so that objects do not ignite and external air necessary for thermal decomposition flows in. These adjustments are very complicated and require skill.
  • the total amount of outside air flowing into the thermal decomposition treatment chamber through multiple external pipes can be controlled to exceed the predetermined upper limit, so thermal decomposition can be performed.
  • the outside air flowing into the chamber section varies depending on the thermal decomposition state near the outside air flow inlet where each external pipe is led out. Heat distributed to the external pipe Since flows into the processing chamber, as in the prior art, the amount of outside air flowing in from the outside line, there is no need to adjust individually sequentially by valves or the like.
  • a magnetic field pyrolysis apparatus is the magnetic field pyrolysis apparatus according to any one of claims:! To 3,
  • It has a vent hole for cracked gas generated in the pyrolysis chamber, and comprises a partition plate that partitions the pyrolysis chamber into upper and lower spaces, and an elevating means that moves the partition plate up and down. .
  • the magnetic field pyrolysis apparatus according to claim 5 of the present invention is the magnetic field pyrolysis apparatus according to claim 4,
  • the ring-shaped magnet is inserted into the vent hole. According to this feature, the cracked gas that passes through the vent is magnetized, so that the harmful substance force S contained in the cracked gas is heated in the upper space of the pyrolysis chamber separated by the partition plate. Since it is decomposed, the concentration of harmful substances contained in the exhausted cracked gas can be further reduced.
  • a magnetic field pyrolysis apparatus is the magnetic field pyrolysis apparatus according to any one of claims 1 to 5,
  • An internal input port having an internal opening / closing door for charging waste into the pyrolysis chamber, and an external input port having an external opening / closing door for charging waste from the outside. It is characterized by comprising an input part formed so as to cover the internal input port so that the space facing the door becomes a closed input chamber.
  • the internal input port is opened with the external door closed, so that the waste in the input chamber can be input into the pyrolysis chamber. Therefore, when these wastes are introduced into the pyrolysis chamber from the internal inlet, it is possible to prevent a large amount of outside air from flowing from the internal inlet into the pyrolysis chamber. As a result, it is possible to prevent ignition of the waste during the pyrolysis process due to the inflow of outside air and to continuously introduce new waste without greatly affecting the state of pyrolysis. Ability to obtain stable operating conditions over the long term.
  • a magnetic field pyrolysis apparatus is the magnetic field pyrolysis apparatus according to any one of claims 1 to 6,
  • the external charging port has a height position below the heat-resistant container, the internal charging port has an upper position of the heat-resistant container, and waste charged from the external charging port is used as the internal charging port. It is characterized by having a lifting means for lifting.
  • a magnetic field pyrolysis apparatus is according to any one of claims 1 to 7.
  • the heat-resistant container has a cylindrical shape.
  • the outside air can be supplied almost uniformly into the pyrolysis chamber.
  • the pyrolysis chamber like the conventional square box-like pyrolysis chamber, Since it is possible to avoid the undecomposed waste locally remaining in the corners, it is possible to improve the efficiency of the thermal decomposition process.
  • FIG. 1 is a front view showing an overall image of a magnetic field pyrolysis apparatus in an embodiment of the present invention.
  • FIG. 2 is an AA sectional view of a magnetic field pyrolysis apparatus in an example of the present invention.
  • FIG. 3 is a BB cross-sectional view of the magnetic field pyrolysis apparatus in the example of the present invention.
  • FIG. 4 is a view showing a tray and a partition plate 12 in an embodiment of the present invention.
  • FIG. 5 is a C-C cross-sectional view of a magnetic field pyrolysis apparatus in an example of the present invention.
  • FIG. 6 is a diagram showing external pipes 20a to 20p according to an embodiment of the present invention.
  • FIG. 7 (a) is a diagram showing a state of generation of turbulent flow in the external pipelines 20a to 20p according to the embodiment of the present invention, and (b) is an external pipeline 20a to 20p according to the embodiment of the present invention. It is explanatory drawing which shows the condition of the magnetic flux in.
  • FIG. 8 is a block diagram showing a connection state between a control device and each part in the magnetic field pyrolysis apparatus of the embodiment of the present invention.
  • FIG. 9 is a view showing another form of magnet.
  • FIG. 1 is a perspective view showing an overall image of a magnetic field pyrolysis apparatus 1 in an embodiment of the present invention.
  • the magnetic field pyrolysis apparatus 1 of the present embodiment has a heat-resistant container 2 that has a vertically long cylindrical shape, and a mode that protrudes from the side surface of the heat-resistant container 2 on the front surface of the heat-resistant container 2. It consists mainly of an input part 3 for inputting waste.
  • the heat formed in the inside of the heat-resistant container 2 is formed on the lower outer periphery of the heat-resistant container 2 of the present embodiment, as shown in Fig. 5 (C-C cross section).
  • External pipe lines 20a-p led out from a plurality of outside air inlets 17a-p formed in the side wall of the heat-resistant container 2 so as to communicate the decomposition treatment chamber 30 and the outside of the heat-resistant container 2, and
  • An outside air intake section having two chambers 15 and 18 is provided, and an ash discharge port 32 for taking out magnetized ash deposited at the lowermost part of the thermal decomposition treatment chamber 30 is provided.
  • the ash outlet 32 can be opened and closed.
  • the ash outlet door 32 ′ is closed except when the magnetized ash is taken out.
  • an iron circular top plate 5 is welded to the heat-resistant container 2 at the upper end of the cylindrical heat-resistant container 2, and the inside of the heat-resistant container 2 is in a substantially hermetically sealed state. 30.
  • the heat-resistant container 2 used in this example is a double-layered hollow having a hollow portion 2c between the outer steel plate 2a and the inner steel plate 2b.
  • the thermal decomposition chamber 30 is thermally insulated from the outside by introducing the magnetized ash taken out from the ash discharge port 32 into the hollow portion 2c as a heat insulating material. It is configured so that the internal heat is difficult to escape to the outside.
  • the heat-resistant container 2 has a cylindrical shape. This is because, in a conventional magnetic field pyrolysis apparatus having a square box-shaped pyrolysis chamber, a corner in the pyrolysis chamber is provided. In order to decompose the remaining undecomposed waste locally, unexposed waste remains locally in the corners of the thermal decomposition chamber. In addition, it is necessary to move the undecomposed waste at the corner to the center of the thermal decomposition chamber, which is cumbersome and takes time to process the undecomposed waste at the corner. Therefore, it is preferable that the efficiency of the thermal decomposition treatment can be reduced, but the present invention is not limited to this.
  • the shape of the heat-resistant container 2 is subjected to the decomposition treatment. Select appropriately according to the amount and type of waste to be treated. Just do it.
  • a cylindrical pyrolysis is performed so that the interior of the pyrolysis chamber 30 is divided into upper and lower spaces.
  • a through-hole 5 ′ is provided through which a partition plate shaft 10 fixed at the center of a circular partition plate 12 having a size substantially inscribed in the processing chamber 30 is movably moved up and down.
  • a connection shaft 8 connected in a T-shape is connected to the upper end portion of the partition plate shaft 10 so as to be orthogonal to the partition plate shaft 10, and both of the connection shafts 8 are connected.
  • the end is connected to the cylinder shafts 6a and 6b of the two hydraulic cylinders 4a and 4b provided at opposite positions on the outer peripheral surface of the heat-resistant container 2, and controls the hydraulic pressure supplied to the hydraulic cylinders 4a and 4b.
  • the partition plate 12 can be moved up and down, and waste to be treated in the pyrolysis chamber 30 can be pressurized by the lower surface of the partition plate 12. ing.
  • two exhaust ports 28 are formed at opposing positions on the outer peripheral surface near the upper end of the heat-resistant container 2, and the rear surface position of the outer peripheral surface of the heat-resistant container 2 (the input portion 3 is disposed).
  • a water treatment device 7 for treating the exhaust water is fixedly installed at a position opposite to the upper side of the heat-resistant container 2 along the outer peripheral surface near the upper end of the heat-resistant container 2.
  • the decomposition gas (dry distillation gas) discharged from the exhaust port 28 flows into the water treatment device 7 and the water After being treated in a treatment water tank formed inside the treatment device 7, the water is exhausted from an exhaust chimney 9 erected on the upper surface of the water treatment device 7.
  • the input unit 3 used in the present embodiment will be described with reference to FIG. 3.
  • the input unit 3 includes a vertical passage 42 through which waste is pumped, and the transported waste is horizontal.
  • a transverse passage 35 that is moved in the direction, and the transverse passage 35 is connected to an internal charging port 31 formed on the outer peripheral surface of the upper part of the heat-resistant container 2.
  • the vertical passage 42 and the horizontal passage 35 are formed as a closed space by the box-shaped housing 3 ′.
  • the space facing the internal insertion port 31 is the horizontal passage 35 and the vertical passage 42 closed by the box-shaped housing 3 ', and the horizontal passage 35 and the vertical passage 42 are used in the present invention.
  • An input room is formed.
  • an external inlet 13 having an external opening / closing door 14 is provided, and at the lower end position of the vertical passage 42.
  • the lifting device 39 having the lifting table 38 is installed so that the height position force of the lifting table 38 in the most contracted state of the lifting device 39 is substantially the same height as the lower end position of the external input port 13. The operator can input the waste from the external input port 13 onto the lifting table 38, and the input waste is transferred into the vertical passage 42 by the lifting device 39. Is transported to the level of the side passage 35.
  • the transfer device having the transfer plate 36 at the end position of the lateral passage 35 on the side opposite to the internal charging port 31 is the same as the above-described transfer device 39. 37 is provided, and the waste transported by the transporting device 39 is transferred to the internal input port 31 side by the transfer plate 36 and input into the thermal decomposition treatment chamber 30.
  • an internal opening / closing door 33 for opening and closing the internal charging port 31 is provided at a position immediately before the internal charging port 31 of the lateral passage 35 so as to be slidable in the vertical direction.
  • an exhaust valve 40 capable of discharging the air inside the side passage 35 to the outside without flowing outside air into the side passage 35. It is provided at the upper position of 35.
  • the partition plate 12 used in the present embodiment is provided with a plurality of vent holes 25 concentrically penetrating in the thickness direction of the partition plate 12, as shown in FIG.
  • the cracked gas generated in the thermal decomposition treatment chamber 30 below the partition plate 12 is discharged through the vent holes 25 to the decomposition gas treatment space 30 ′ formed above the partition plate 12.
  • Each of these vent holes 25 is provided with a ring-shaped magnet 26 which is a ring-shaped permanent magnet, and a cracked gas treatment space 30 for harmful substances contained in the cracked gas passing through these vent holes 25. Resolving power at 'is promoted by the magnetizing treatment by these ring magnets 26.
  • these partition plates 12 are made of heat-resistant steel from the viewpoint of heat resistance and strength.
  • the present invention is not limited to this. Any material that has sufficient heat resistance and mechanical strength can be used.
  • the provision of the ring-shaped magnet 26 in the vent hole 25 is that most of the cracked gas generated in the thermal decomposition treatment chamber 30 is passed through the vent hole 25 through the cracked gas treatment space 30 ′. Since most of the decomposed gas can be magnetized, the ring-shaped magnet 26 is used as a magnet for the magnetizing process, so that the decomposed gas and the magnet Therefore, it is possible to effectively magnetize the cracked gas passing therethrough.
  • the ring-shaped magnets 26 magnets having N poles and S poles in the thickness direction are used.
  • other magnets for example, semicircular magnets corresponding to the semicircular portion of the ring as shown in FIG. Compared to the case where a ring-shaped magnet is formed using two magnets, sufficient magnetization processing can be performed without using a magnet with a large magnetic force.
  • outside air intake part of the magnetic field pyrolysis apparatus 1 of this embodiment will be described with reference to FIG. 5.
  • the outside air flow inlets 17a to 17p are located at positions below the outer peripheral side surface of the heat-resistant container 2 of this embodiment. However, they are drilled at approximately equal intervals in the outer circumferential direction at substantially the same height position. Then, external pipe lines 20a to 20p are connected to the external air flow inlets 17a to 17p, respectively.
  • the length of the external pipe connected to the external air flow inlet near the chambers 15 and 18, for example, the external pipes 20a, i is short, and the external pipe connected to the external air inlet far from the chambers 15 and 18 is connected.
  • the length of external pipes such as external pipes 20m, e will be longer.
  • the outer pipe line having a short path length is formed concentrically with the outer peripheral surface at a position close to the outer peripheral surface of the heat resistant container 2.
  • the lower surfaces of the chambers 15 and 18 are larger in diameter than the outer pipes 20a to 20p, and have a predetermined size based on the maximum amount of outside air flowing into the pyrolysis chamber 30.
  • the outside air inlets 16 and 19 are formed, and the outside air that has flowed into the chambers 15 and 18 from the outside air inlets 16 and 19 is supplied to the outside air inlets 17a to 17p through the external pipes 20a to 20p.
  • a ring-shaped magnet 50 which is a ring-shaped permanent magnet, is inserted in each of the external pipes 20a to 20p.
  • the ring-shaped magnet 50 is arranged so as to be within one line with respect to a predetermined road length, and the short lengths 20a, 20b, 20h, 20i, 20j, 20p, 1 ring magnet 50 force inserted, then 20m, 20g, 20k, 20o f, 2 path lengths, 20d, 20f, 201
  • 20 ⁇ three ring magnets 50 are inserted, and in the case of 20m, 20e with the longest path length, four ring magnets 50 are inserted.
  • These ring-shaped magnets 50 have an outer diameter that is substantially the same as the outer diameter of the main pipe 51 that forms the outer pipes 20a to 20p, and the inner diameter is larger than the inner diameter of the main pipe 51. Small diameter It is said that.
  • these ring-shaped magnets 50 are arranged between two main pipes 51 having a predetermined length inside a joint pipe 52 having an inner diameter slightly larger than the outer diameter of the main pipe 51.
  • the outer pipes 20a-p in which the ring-shaped magnets 50 are inserted are formed by adhering the inner circumferential surface of the joint pipe 52 and the outer circumferential surface of the main pipe 51 while maintaining the clamping state.
  • the material of the main pipe 51 and the joint pipe 52 resin pipe materials that are relatively excellent in workability and are not magnetized by the ring-shaped magnet 50 can be suitably used. Since the joint pipe 52 is exposed to the outside and is not significantly affected by the heat of the heat-resistant container 2, a pipe made of salty vinyl resin is used in this embodiment.
  • the ring-shaped magnet 50 having an inner diameter smaller than the inner diameter of the main pipe 51 is used, and this is done as shown in FIG. 7 (a).
  • turbulent flow is generated in the passing outside air, which is preferable because large magnetic vibration can be imparted to the passing outside air.
  • the present invention is not limited to this, and the inner diameter of the ring-shaped magnet 50 and the inner diameter of the main pipe 51 may be set to substantially the same diameter.
  • the ring-shaped magnet 50 has N and S poles in the thickness direction of the ring-shaped magnet 50, as in the case of the ring-shaped magnet 26.
  • the density of magnetic lines of force at the inner diameter of the ring-shaped magnet 50 through which the outside air passes can be increased, so that a ring-shaped magnet using two semicircular magnets as shown in FIG. Compared to the above, sufficient magnetization processing can be performed without using a magnet having a large magnetic force.
  • the ring-shaped magnet 50 having the N-pole and the S-pole in the thickness direction is placed so that the opposing surfaces of the ring-shaped magnet 50 in contact with the P are different poles, so that these ring-shaped magnets Since the magnetic field lines are interposed between the adjacent ring-shaped magnets 50 and between the adjacent magnets 50, the magnetizing process further proceeds.
  • the normal magnetic field pyrolysis apparatus does not require power for operating the blower motor or the like because the outside air is taken into the pyrolysis chamber 30 by natural intake air, but the magnetic field of this embodiment is not necessary.
  • the field pyrolysis apparatus 1 includes the hydraulic pump 62 for supplying hydraulic pressure to the hydraulic cylinders 4a and 4b for raising and lowering the partition plate 12, and the hydraulic pump 62 for supplying hydraulic pressure to the hydraulic cylinders 4a and 4b.
  • the hydraulic control valve device 65 that releases the hydraulic pressure supplied from the hydraulic cylinders 4a and 4b, the above-described lifting device 39, and the control computer that controls the operation of each part are connected to the transfer device 37.
  • An internal control device 60 is provided, and the control device 60 performs operation control according to the operation of various operation switches provided on the operation panel 61.
  • the operation status of the magnetic field pyrolysis apparatus 1 of the present embodiment will be described below.
  • a prescribed amount of water is poured into the water treatment apparatus 7 in advance.
  • the magnetized ash recovered from the other magnetic field pyrolysis apparatus 1 is thrown into the entire bottom surface of the pyrolysis chamber 30 so as to be deposited with a thickness of about 50 mm. Heat with a heater. It should be noted that these magnetized ash can be charged and heated with the ash outlet 32 opened.
  • easy-to-treat waste such as dried ogattaz, rice husks, or dead leaves. It should be noted that such easy-to-treat waste may be input with the ash outlet 32 open.
  • waste such as plastic having a relatively low water content is put into the upper part. Specifically, waste such as plastic with a relatively low moisture content is thrown from the external door 14 onto the lifting table 38 in the vertical passage 42, and then the external door 14 is closed. Operate the input button switch provided on panel 61.
  • control device 60 operates the lifting device 39 to raise the lifting table 38 to the lower surface position of the lateral passage 35, and then operates the transfer device 37 to move the lateral direction.
  • the waste pumped in the passage 35 is transferred to the internal inlet 31 side.
  • control device 60 operates the hydraulic pump 62 and controls the hydraulic control valve device 65 to supply hydraulic pressure to the hydraulic cylinders 4a and 4b.
  • the plate 12 is raised and the internal door 33 is slid upward.
  • the transfer device 37 is operated again to move the transfer plate 36, so that the waste having a relatively low water content is compressed into the internal inlet. It is thrown into the pyrolysis chamber 30 from 31.
  • the control device 60 controls the hydraulic control valve device 65 to release the hydraulic pressure applied to the hydraulic cylinders 4a and 4b, thereby simultaneously lowering the partition plate 12.
  • the partition plate 12 that has been lowered causes the waste having a relatively low water content that has been thrown into the pyrolysis chamber 30 to move downward in the pyrolysis chamber 30. It is deposited to be pushed.
  • the amount of the magnetized outside air flowing into the pyrolysis chamber 30 from the outside air flow inlets 17a to 17p is individually controlled by a valve or the like.
  • the total force of the magnetized outside air flowing into the pyrolysis chamber 30 from the outside air inlets 17a-p into the outside air intake port 16 The amount of outside air restricted by the size of 19 is appropriately distributed to each external pipe 20a-p according to the state of thermal decomposition in the vicinity of each outside air flow inlet 17a-p.
  • the amount of magnetization-treated outside air flowing from each of the outside air flow inlets 17a to 17p is automatically adjusted.
  • the amount of magnetized outside air flowing in from the air flow inlets 17a to 17p need not be sequentially adjusted by a valve or the like, and the troublesome adjustment by these valves or the like can be eliminated.
  • the partition plate 12 also falls in the thermal decomposition treatment chamber 30 when the re-absorbed waste is released from the compression at the time of introduction from the internal charging port 31. Then, by compressing the newly introduced waste from above, it is exhausted to the cracked gas treatment space 30 ′ through the vent hole 25, and the newly introduced waste and the already introduced waste are already introduced. By reducing the size of the gap between the waste and the waste, and the presence of outside air containing oxygen in these gaps, the pyrolyzed waste already in the pyrolysis chamber 30 is ignited. It is possible to suppress the occurrence of problems and to obtain a stable driving situation.
  • the pyrolysis temperature in these pyrolysis chambers 30 is significantly lower than the combustion temperature at which dioxin or the like is generated, plastics containing chlorine in the waste, etc., as in the conventional magnetic field pyrolysis apparatus 1
  • the cracked gas containing these harmful substances is provided in the vent hole 25.
  • the cracked gas treatment space 30 ′ which is the upper space of the partition plate 12 of the thermal decomposition treatment chamber 30 after being magnetized by the ring-shaped magnet 26
  • harmful substances in the cracked gas are further thermally decomposed, and the water treatment device Since the water is treated at 7 and exhausted from the exhaust stack 9, the exhaust from the magnetic field pyrolysis apparatus 1 can be made even cleaner.
  • the pyrolyzed waste is reduced in volume to 1/200. It becomes magnetized ash, is taken out from the ash outlet 32, and is used as a heat insulating material for other magnetic field pyrolysis apparatus 1.
  • the ring-shaped magnet 50 which is a feature of the magnetic field pyrolysis apparatus 1 of the present embodiment, is inserted, and a pair of magnets having substantially the same magnetic force as those of the ring-shaped magnet 50.
  • the following is a comparison of the processing time or the processing amount per unit time when the ring-shaped magnet 50 is disposed outside the external conduits 20a to 20p.
  • the volume of waste thrown into the pyrolysis chamber 30 is a maximum of 1 cubic meter, and the amount of waste reduced by pyrolysis for a predetermined time is thrown in after the predetermined time.
  • the results of comparison based on the amount of input (volume) are shown below.
  • the ring-shaped magnet 50 is internally placed in the external conduits 20a to 20p so that the external conduit 20a to The outside air that passes through p passes through the ring-shaped magnet 50 while being in contact with or very close to the ring-shaped magnet 50, and the inner diameter of the ring-shaped magnet 50 is made smaller than the inner diameter of the external pipes 20a to 20p.
  • the magnetite 50 it can generate turbulent flow in the outside air.
  • the outside air can be magnetized well, and thus the ability to obtain a stable thermal decomposition operating condition. S can.
  • the magnetic field pyrolysis apparatus 1 of the present embodiment when the ring-shaped magnet 50 having the N pole and the S pole in the thickness direction is used, a magnet as shown in FIG. 9 is used.
  • the magnetic flux density inside the ring-shaped magnet 50 can be improved, and the outside air passes through the ring having the high magnetic flux density, so that a large change in the magnetic field is applied to the outside air, resulting in a larger magnetic field vibration.
  • Motion can be applied to the outside air, and the adjacent ring-shaped magnets 50 are inserted so that the opposing surfaces have different poles, so that magnetic flux also exists between these adjacent ring-shaped magnets 50.
  • magnetization processing is performed, so that it is possible to apply large magnetic field vibrations by magnetization processing efficiently without filling the outside air. Get the driving status of Can.
  • the size of the voids generated by the thermal decomposition or new input of waste between the waste input into the thermal decomposition treatment chamber 30 is described above.
  • the partition plate 12 By lowering the partition plate 12, it is possible to reduce the gas, and the gas existing in the gap can be exhausted to the cracked gas treatment space 30 ′, which is the upper space of the partition plate 12, through the air holes 25.
  • the outside air (oxygen) present in the gaps caused by the introduction of new waste and the This makes it possible to suppress the occurrence of ignition etc. from the pyrolyzed waste present in the plant, and a stable operating situation can be obtained.
  • the cracked gas passing through the vent hole 25 is magnetized by the ring-shaped magnet 26, so that harmful substances contained in the cracked gas are removed. Since it is thermally decomposed in the cracked gas treatment space 30 ′, which is the upper space of the pyrolysis chamber 30 divided by the partition plate 12, the concentration of harmful substances contained in the exhausted cracked gas is This can be further reduced.
  • the magnetic field pyrolysis apparatus 1 of the present embodiment after the waste is introduced into the vertical passage 42 (lateral passage 35) serving as the input chamber from the external input port 13, the external door 14 is closed. In this state, the internal input port 31 is opened so that the waste in the lateral passage 35 serving as the input chamber can be input into the thermal decomposition treatment chamber 30. Since it is possible to prevent a large amount of outside air from flowing into the thermal decomposition treatment chamber 30 from the internal charging port 31 when it is introduced into the inside 30, the large amount of outside air flowing in during the thermal decomposition treatment In addition to preventing the ignition of waste, new waste can be continuously input without significantly affecting the thermal decomposition status, so that stable operation status can be obtained over a long period of time. Can do.
  • the magnetic field pyrolysis apparatus 1 of the present embodiment by putting waste into the external charging port 13 provided at a height position below the heat-resistant container 2, the thrown waste Is transferred to the internal charging port 31 provided at the upper position of the heat-resistant container 2 and then injected, so that the work efficiency in the operation of charging these wastes can be improved.
  • the magnetic field pyrolysis apparatus 1 of the present embodiment by making the heat-resistant container 2 cylindrical, outside air can be supplied almost uniformly into the pyrolysis chamber 30, for example, a conventional square box Since the undecomposed waste can be prevented from locally remaining in the corners of the pyrolysis chamber as in the case of the thermal crack chamber, the efficiency of the pyrolysis process can be improved.
  • the ring-shaped magnet 50 is easily inserted in the external pipes 20a to 20p, so that the ring-shaped magnet 50 is inserted into the joint pipe 52.
  • the ring-shaped magnet 50 which is not limited, may be inserted into the main pipe 51.
  • the force for providing 16 external air flow inlets 17a to 17p is not limited to this. It may be determined appropriately depending on the size of 30 and the pipe diameter of the external airflow inlet 17a-p to be used.
  • all the external air flow inlets 17a to 17p are formed at substantially the same height position, but the present invention is not limited to this, for example, the external air flow inlets 17a to 17a.
  • An external air flow inlet and an external pipe line are provided at a position higher than the height of p and at a position substantially in the middle of each of the external air flow inlets 17a to 17p. It may be formed in multiple stages.
  • the force using two chambers 15 and 18 is not limited to this, and the number of these chambers may be three or four.
  • the force by which the internal opening / closing door 33 opens and closes the slide in conjunction with the partition plate 12 by the engagement piece 34 is not limited to this.
  • An opening / closing mechanism for opening / closing the opening / closing door 33 may be provided independently.
  • the waste to be input is compressed in the lateral passage 35 and the air contained in the waste is exhausted from the exhaust valve 40.
  • the present invention is not limited to this. It is not specified, and these compression processes are not performed, and the configuration is also good.
  • vent holes 25 are arranged concentrically, but the present invention is not limited to this.
  • the number and arrangement of the vent holes 25 are not limited thereto. Etc. may be selected as appropriate.
  • the internal charging port 31 is provided on the outer peripheral surface of the upper portion of the heat-resistant container 2, and this is because the partition plate for compressing the input waste as in this embodiment is used.
  • the partition plate 12 is also provided with an opening / closing portion so that the internal insertion port 31 is provided. Circle It may be provided on the top plate 5.
  • the outer pipes 20a-p are formed by pipes having a circular cross-sectional shape, but the present invention is not limited to this, and the outer pipes 20a-p are not limited to this.
  • the cross-sectional shape may be an elliptical or square tube, and accordingly, it may be a ring-shaped magnet or an elliptical, square or polygonal ring-shaped magnet.

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Materials Engineering (AREA)
  • Organic Chemistry (AREA)
  • Combustion & Propulsion (AREA)
  • General Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Environmental & Geological Engineering (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Processing Of Solid Wastes (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)

Abstract

Le problème à résoudre dans le cadre de la présente invention est d'obtenir une condition de fonctionnement stabilisée de décomposition thermique en magnétisant l'air extérieur de façon efficace. La solution proposée consiste en un équipement de décomposition thermique à champ magnétique (1) qui comprend un récipient résistant à la chaleur (2) qui est composé d'un élément résistant à la chaleur et forme une chambre de traitement de décomposition thermique (30), une pluralité d'entrées d'air extérieur (17a-p) prévues dans la paroi latérale du récipient résistant à la chaleur (2), des conduits externes (20a-p) qui commencent à partir des entrées d'air extérieur respectives (17a-p) et sont capables d'aspirer de l'air extérieur par l'intermédiaire de leurs parties d'extrémité, des aimants permanents (50) prévus au-dessus des conduits externes (20a-p), et un passage de sortie (28) qui communique avec la position supérieure de la chambre de traitement de décomposition thermique (30). L'air extérieur magnétisé par les aimants permanents (50) est distribué dans la chambre de traitement de décomposition thermique (30) par aspiration d'air naturelle et le gaspillage est soumis à une décomposition thermique. Dans un tel équipement de décomposition thermique à champ magnétique, les aimants permanents (50) sont des aimants annulaires (50) et les aimants annulaires sont insérés dans les conduits externes (20a-p).
PCT/JP2006/316938 2006-08-29 2006-08-29 Équipement de décomposition thermique à champ magnétique WO2008026248A1 (fr)

Priority Applications (1)

Application Number Priority Date Filing Date Title
PCT/JP2006/316938 WO2008026248A1 (fr) 2006-08-29 2006-08-29 Équipement de décomposition thermique à champ magnétique

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
PCT/JP2006/316938 WO2008026248A1 (fr) 2006-08-29 2006-08-29 Équipement de décomposition thermique à champ magnétique

Publications (1)

Publication Number Publication Date
WO2008026248A1 true WO2008026248A1 (fr) 2008-03-06

Family

ID=39135540

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/JP2006/316938 WO2008026248A1 (fr) 2006-08-29 2006-08-29 Équipement de décomposition thermique à champ magnétique

Country Status (1)

Country Link
WO (1) WO2008026248A1 (fr)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2013181730A1 (fr) * 2012-06-08 2013-12-12 Oxys Ambiental Ltda. Équipement de combustion de matière organique solide
EP3234465A4 (fr) * 2016-02-24 2018-09-12 Amen Dhyllon Appareil four
CN111810959A (zh) * 2020-07-02 2020-10-23 浙江双屿实业有限公司 一种有机固废处理能量转换装置

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH11257632A (ja) * 1998-03-11 1999-09-21 Kawasaki Steel Corp 有害物質の生成を抑制した廃棄物の焼却処理方法
JP2001304520A (ja) * 2000-04-18 2001-10-31 Toshimi Hirozo 焼却炉および焼却方法
JP2002242769A (ja) * 2001-02-16 2002-08-28 Hisanari Tabata 燃焼性改善用磁気装置
JP2004033966A (ja) * 2002-07-05 2004-02-05 Sanyusha:Kk 廃棄物処理方法及び装置
JP2004091367A (ja) * 2002-08-30 2004-03-25 Katsuya Kihira 消臭殺菌剤
JP2006036859A (ja) * 2004-07-23 2006-02-09 Kanji Abe 炭化装置
JP2006086307A (ja) * 2004-09-15 2006-03-30 Masaru Nagasaki 磁粉体製造装置及び磁粉体製造方法

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH11257632A (ja) * 1998-03-11 1999-09-21 Kawasaki Steel Corp 有害物質の生成を抑制した廃棄物の焼却処理方法
JP2001304520A (ja) * 2000-04-18 2001-10-31 Toshimi Hirozo 焼却炉および焼却方法
JP2002242769A (ja) * 2001-02-16 2002-08-28 Hisanari Tabata 燃焼性改善用磁気装置
JP2004033966A (ja) * 2002-07-05 2004-02-05 Sanyusha:Kk 廃棄物処理方法及び装置
JP2004091367A (ja) * 2002-08-30 2004-03-25 Katsuya Kihira 消臭殺菌剤
JP2006036859A (ja) * 2004-07-23 2006-02-09 Kanji Abe 炭化装置
JP2006086307A (ja) * 2004-09-15 2006-03-30 Masaru Nagasaki 磁粉体製造装置及び磁粉体製造方法

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2013181730A1 (fr) * 2012-06-08 2013-12-12 Oxys Ambiental Ltda. Équipement de combustion de matière organique solide
EP3234465A4 (fr) * 2016-02-24 2018-09-12 Amen Dhyllon Appareil four
CN111810959A (zh) * 2020-07-02 2020-10-23 浙江双屿实业有限公司 一种有机固废处理能量转换装置

Similar Documents

Publication Publication Date Title
JP3948486B1 (ja) 揮発性有機化合物の処理方法、吸着・脱着装置及び揮発性有機化合物の処理システム
WO2013133194A1 (fr) Dispositif de traitement pour substance à traiter
US20080202395A1 (en) Vacuum Incineration Apparatus For Waste Disposal and Vacuum Preservation Method Thereof
WO2008026248A1 (fr) Équipement de décomposition thermique à champ magnétique
CZ20022979A3 (cs) Způsob sušení dřeva
KR101956786B1 (ko) 자기장 이온화 저온 열분해장치
JP2011067743A (ja) 排気処理装置
JP3122682U (ja) 低温熱処理炉
JP5997482B2 (ja) 有機物処理装置
JP6223720B2 (ja) 磁場熱分解炉
JP6905242B1 (ja) 有機物の無機物化装置
WO2023008560A1 (fr) Dispositif de décomposition à basse température de substance organique
TWI551825B (zh) 廢氣淨化裝置
JP2008008559A (ja) 熱分解炉
US5931663A (en) Purge system for regenerative thermal oxidizer
JP2008144131A (ja) 有機廃棄物の炭化処理方法および有機廃棄物炭化処理用連続加熱炉
JP6046906B2 (ja) 有機物処理装置
JP2007296465A (ja) 廃棄物処理器および廃棄物処理方法
KR100848494B1 (ko) 고형연료용 연소장치
JP5032691B1 (ja) 磁化空気を用いた分解装置
WO2023281703A1 (fr) Appareil de formation d'une substance inorganique à partir d'une substance organique
WO2008053571A1 (fr) Procédé de pyrolyse de déchets contenant de la matière organique, appareil correspondant et système de gaséification pyrolitique
JP2008064325A (ja) 廃棄物処理装置
KR200266999Y1 (ko) 원적외선 히터를 이용한 탄화장치
JP2013224872A (ja) 被処理物質の処理装置及び被処理物質の処理方法

Legal Events

Date Code Title Description
121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 06796918

Country of ref document: EP

Kind code of ref document: A1

NENP Non-entry into the national phase

Ref country code: DE

NENP Non-entry into the national phase

Ref country code: RU

122 Ep: pct application non-entry in european phase

Ref document number: 06796918

Country of ref document: EP

Kind code of ref document: A1

NENP Non-entry into the national phase

Ref country code: JP