WO2002094463A1 - Intermittent flowing type thermal decomposer - Google Patents
Intermittent flowing type thermal decomposer Download PDFInfo
- Publication number
- WO2002094463A1 WO2002094463A1 PCT/JP2001/004278 JP0104278W WO02094463A1 WO 2002094463 A1 WO2002094463 A1 WO 2002094463A1 JP 0104278 W JP0104278 W JP 0104278W WO 02094463 A1 WO02094463 A1 WO 02094463A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- crucible
- gas
- intermittent flow
- frame
- heating
- Prior art date
- Legal status (The legal status 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 status listed.)
- Ceased
Links
Classifications
-
- 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
- C10B53/07—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form of solid raw materials consisting of synthetic polymeric materials, e.g. tyres
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- 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
- C10B47/00—Destructive distillation of solid carbonaceous materials with indirect heating, e.g. by external combustion
- C10B47/28—Other processes
- C10B47/30—Other processes in rotary ovens or retorts
-
- 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
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/02—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment
- F23G5/027—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment pyrolising or gasifying stage
- F23G5/0276—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment pyrolising or gasifying stage using direct heating
-
- 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
- F23G5/20—Incineration of waste; Incinerator constructions; Details, accessories or control therefor having rotating or oscillating drums
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2203/00—Furnace arrangements
- F23G2203/20—Rotary drum furnace
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2203/00—Furnace arrangements
- F23G2203/20—Rotary drum furnace
- F23G2203/209—Rotary drum furnace with variable inclination of rotation axis
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/141—Feedstock
- Y02P20/143—Feedstock the feedstock being recycled material, e.g. plastics
Definitions
- the present invention relates to a pyrolysis apparatus for decomposing incinerated ash, sewage sludge, and waste discharged from a facility of a company, etc., discharged from an incinerator, and particularly to a rubber that generates toxic gas when incinerated.
- the present invention relates to a thermal decomposition apparatus capable of decomposing industrial wastes such as products and plastic products.
- waste discharged from households and corporate facilities is combustible waste that can be incinerated, non-burnable waste that cannot be incinerated because it generates toxic gas when burned, such as rubber and plastic products. It is mainly classified into recyclable waste such as paper, glass, and aluminum products that can be used, and industrial waste such as waste oil and concrete and metallic structures discharged from factories and facilities. Corresponding disposal is being performed.
- combustible waste is incinerated and non-burnable waste is buried in landfills. Recyclable waste is separated according to paper, glass, and aluminum materials, crushed and dissolved, and reused. In addition, industrial waste is specially processed and specially treated for each type.
- incinerated ash incombustible refuse that cannot be incinerated, and industrial waste are buried in landfills, so it is necessary to secure landfill sites, and they are included in odors and waste generated by waste. Heavy metals have adversely affected the environment around the landfill.
- the applicant has developed a device for placing an object to be processed in a sealed crucible, heating the crucible in a vacuum state, and thermally decomposing the object to be processed. _______________________________________________________________ No. 4-904, Patent No. 20382814).
- a crucible containing an object to be incinerated is supported in a furnace main body so as to have a gap between the crucible and an outer wall of the crucible other than the support portion, and a crucible is provided in a gap between an inner wall in the furnace main body and an outer wall of the crucible.
- a heating device is provided for heating the crucible, the opening of the crucible is located inside the opening of the furnace body, and an opening / closing lid is provided to simultaneously close these openings, and the gas generated when incinerating the workpiece is crucible.
- a suction pipe leading out from the inside is provided, and a suction device connected to the suction pipe and a gas separation and extraction device connected to the suction device are provided.
- the inside of the crucible is closed by opening and closing the lid to create a vacuum state, the object to be processed inside the crucible is heated by the heating device in the vacuum state, and the gas generated from the object to be processed is taken out of the crucible by the suction device, and the gas is separated and extracted by the gas separation and extraction device. Extract the gas.
- the present invention provides a pyrolysis apparatus capable of continuously performing a thermal decomposition process on a large amount of objects to be processed, thereby improving work efficiency.
- the invention according to claim 1 is an apparatus for thermally decomposing a workpiece by placing the workpiece in a crucible and heating the workpiece in the crucible in a state where the interior of the crucible is evacuated.
- the crucible has a cylindrical shape having inlets and outlets at both ends and a spiral groove formed on an inner wall, a frame, a rotatable furnace held on the frame, and the crucible being rotated by the rotary furnace.
- a discharge box that communicates with the exit of the crucible is provided on the frame, and the input box is provided with a blocking device that blocks communication between the outside and the crucible.
- the discharge box includes a blocking device that blocks communication between the outside and the crucible.
- a suction device that is connected to the discharge box, evacuates the crucible to a vacuum state, and suctions gas generated when the object to be processed is decomposed by the heating device from the crucible. In which was to so that.
- the invention according to claim 2 is the intermittent flow type pyrolysis apparatus according to claim 1, which is generated when a gas separation / extraction device is connected to the suction device and the object to be processed is decomposed by the gas selection / extraction device. This is to extract the gas that is generated.
- the gas separation and extraction apparatus in the intermittent fluid type pyrolysis apparatus according to the second aspect, is connected to a separate heating apparatus, and is generated when the gas separation and extraction apparatus decomposes an object to be processed. The unextracted gas is introduced into the separate heating device.
- the invention according to claim 4 is the intermittent flow type pyrolysis apparatus according to claim 1, wherein the position of the discharge port of the crucible is higher than the position of the input port.
- the frame is mounted on a base that can swing relative to each other, and the inclination angle of the frame relative to the base is freely changed. It is possible to do that.
- the invention of claim 6 is the intermittent flow type pyrolysis apparatus of claim 1, wherein the shutoff device for shutting off the inside and the outside of the crucible has a double shutoff structure.
- the invention according to claim 7 is the intermittent flow type pyrolysis apparatus according to claim 1, wherein the heating device is a far-infrared heating device capable of heating an object to be processed in the crucible to 1200 ° C. or more. You.
- the invention according to claim 8 is the intermittent flow type pyrolysis apparatus according to claim 1, wherein a ring-shaped conductor is provided on an outer wall of the rotary furnace, and the conductor is electrically connected to the heating device inside the rotary furnace.
- the frame is provided with a contact that is always in contact with the ring-shaped conductor during rotation of the rotary furnace.
- FIG. 1 is a front view of an apparatus according to an embodiment of the present invention
- FIG. 2 is a cross-sectional front view of a rotary furnace according to an embodiment of the present invention
- FIG. FIG. 4 is a cross-sectional view of the rotary furnace with the frame of the embodiment of the present invention removed
- FIG. 5 is a cross-sectional view of the crucible of the embodiment of the present invention
- FIG. 7 is a cross-sectional view of a rotary shirt according to an embodiment of the present invention.
- FIG. 7 is a plan view of a rotary shutter according to an embodiment of the present invention.
- FIG. 8 is a front view of an automatic shutter according to an embodiment of the present invention.
- FIG. 9 is a cross-sectional view of a pot showing another embodiment of the present invention. [Best Mode for Carrying Out the Invention]
- a frame 2 supported by a horizontal shaft 1a is provided on a base 1, and both ends of a cylindrical rotary furnace 3 are rotatably supported on the frame 2.
- the reason for supporting the frame 2 on the horizontal axis 1a at the center of the base 1 is to incline the rotary furnace 3 and to automatically discharge the crucible described later.
- Fixed disks 4, 4 are fixed to both ends of the frame 2, and these fixed disks 4, 4 are rotatable with the rotating disks 3a, 3a at both ends of the rotary furnace 3 via bearings 4a. Are facing each other.
- These fixed disks 4 and rotating disks 3a are mutually attracted by magnetic force.
- Each rotating disk 3a has a through hole 3b at the center, and each fixed disk 4 has a through hole 4b at the center.
- a plurality of ports 5, 5 that are in contact with the lower outer walls on both sides of the rotary furnace 3 are provided at lower portions on both sides of the frame 2, and these rollers 5 are driven and rotated by a driving device 5 a, The furnace 3 is rotated.
- One fixed disk 4 has a chamber-like input box 6 fixed thereto, and the other fixed disk 4 has a chamber-shaped discharge box 7 fixed thereto.
- a charging hopper 8 for charging an object to be processed is provided at an upper portion of the charging box 6, and a rotary shutter 9 as a first shutoff device is provided at a lower portion of the charging hopper 8 (an upper portion of the charging box 6).
- an automatic shutter 10 as a second shutoff device is provided in the input box 6.
- the discharge box 7 is also provided with an automatic shutter 11 as a first shut-off device.
- a rotary shutter 12 is provided as a second shut-off device in the lower part of the slot 7.
- a ring body 13 composed of a plurality of conductors for supplying power is provided at the center of the outer wall of the rotary furnace 3, and a plurality of ring bodies 14 for temperature measurement are provided at both ends of the outer wall. .
- these ring bodies 14 are supported by a plurality of supports 14 a provided at appropriate intervals on the outer wall of the rotary furnace 3, and float from the outer wall of the rotary furnace 3.
- the ring body 13 is supported in the same manner as the ring body 14. Also, even when the rotary furnace 3 rotates, the contacts 15, 16 that always contact the ring bodies 13, 14, respectively, are attached to the upper part of the frame 2 by hanging.
- a cylindrical crucible 17 made of a material having high thermal conductivity that generates far-infrared rays is provided in the internal space of the cylindrical rotary furnace 3, and the crucible 17 is shared with the rotary furnace 3. Rotated.
- the center axis of the cylindrical crucible 17 is aligned with the center axis of the rotary furnace 3.
- the cylindrical crucible 17 has a hollow portion 17a for accommodating the object to be processed, and inlets 17b, which are openings at both ends, and an outlet 17c.
- a spiral groove 17 d is formed on the inner wall of 17 a. Both ends of the crucible 17 are supported by the rotating disk 3a.
- the inlet 17b of the hollow part 17a communicates with the input box 6 through the through hole 3b of the rotating disk 3a and the through hole 4b of the fixed disk 4, and the outlet 17 of the hollow part 17a c communicates with the discharge box 7 through the through hole 3b of the rotating disk 3a and the through hole 4b of the fixed disk 4.
- the discharge box 7 is provided with a suction pipe 18.
- Suction device 32 is connected.
- the suction device 32 is connected to a gas separation and extraction device 33 for separating and extracting gas generated during decomposition of the object to be treated.
- the gas selection and extraction device 33 further includes a gas separation and extraction device 33
- a heat treatment device 34 for heating the gas that could not be selected and extracted in the process is connected.
- the rotary furnace 3 is provided with a heating device 19 for heating an object to be processed introduced into the crucible 17.
- the temperature of the heating device 19 is from room temperature to 1200. This is a far-infrared heating device capable of heating up to C or more, as shown in FIGS. 2 and 4, with a gap provided between the outer wall of the crucible 17 and the It is provided over the entire length.
- the heating device 19 supplies power from the ring body 13. taking it.
- FIG. 6 is a sectional view showing the structure of the rotating shirt 9 of the charging box 6, and FIG. 7 is a plan view thereof.
- the rotary shutter 9 is provided with a large number of through holes 21 concentrically in a circular shielding plate 20 above the input box 6, and a rotatable shutter 23 around the shaft 23 is provided on the shielding plate 20.
- This is a stack of rotating plates 22 having holes 24.
- the through hole 24 intermittently overlaps with one of the through holes 22 so that the object to be processed can pass through.
- the rotary shaft 12 of the discharge box 7 has the same configuration as the rotary shaft 19.
- FIG. 8 shows the configuration of the automatic shutter 10 in the charging box 6.
- the auto shutter 10 is provided with an upper shutter 26 at the upper part in a passage 25 having a rectangular cross section in the vertical direction and a lower shirt 27 at the lower part.
- the upper shutter 26 is rotatably supported at its upper end by a hinge 28 provided on the inner wall of the passage 25. When the free end opposite to the hinge 28 is raised, the passage 25 is closed, and the free end is closed. Lowering opens the passage 25.
- the lower shutter 27 is rotatably supported at its lower end by a hinge 29 provided on the inner wall of the passage 25, and when its free end is lowered, the free end of the upper shutter 26 is raised.
- the passage 25 is closed by the upper chassis 26, and the passage 25 is also closed by itself.
- the lower part of the upper shirt 26 lowers under its own weight and overlaps the inside of the lower shutter 27.
- the lower shirt 27 is connected to the piston 31 of the cylinder 30 provided outside the passage 25, and is linked to the movement of the biston 31.
- the automatic shirt 11 of the discharge box 7 also has the same configuration as the automatic shutter 110.
- the workpiece When the workpiece is loaded into the loading hopper 8, the workpiece is intermittently transferred to the loading box 6 by the rotary shutter 9.
- the automatic shutter 10 opens and enters the hollow portion 17a of the crucible 17 at the center of the rotary furnace 3. Then, close the rotary shutter 9 and the auto shutter 10 to close the suction Activate the device 32 to evacuate the crucible 17.
- the heating device 19 is operated to heat the crucible 17 to about 1200 ° C., and the roller 5 is driven by the driving device 5 a to rotate the rotary furnace 3.
- the object to be processed in the crucible 17 is heated and decomposed by the ultra-high heat energy of electromagnetic waves (far infrared radiation) in a vacuum state.
- the object to be treated in the crucible 17 is thermally decomposed, and along the spiral groove 17 d on the inner circumference of the rotating crucible 17, the outlet 17 from the inlet 17 b side of the crucible 17. Move to c side.
- the gas generated by the thermal decomposition of the object to be processed is led out of the crucible by the suction tube 18. Therefore, the inside of the crucible 17 is always in a vacuum state by suction by the suction tube 18.
- the gas sucked by the suction device 32 reaches the gas separation and extraction device 33, and the gas is extracted and sorted by type by the gas separation and extraction device 33, and is liquefied to be processed or reused.
- the gas not extracted by the gas separation and extraction device 33 is introduced into the heat treatment device 34, and a part of the introduced gas is decomposed by high temperature, and another part is converted into a harmless gas by a clean filter (not shown). Released to the outside.
- the object to be treated in the crucible 17 reaches the outlet 17c along the spiral groove 17d while being thermally decomposed, and the object to be treated is decomposed into ash by being heated for a certain time, and is discharged into the discharge box 7 Will be introduced.
- the ash introduced into the discharge box 7 is discharged from the discharge box 7 by opening the auto shirt 1-11, dropping the ash downward, closing one end, and then opening the rotating shirt 1 1 2 You. That is, the ash is discharged outside by opening and closing the double shut-off device of the discharge box 7.
- the discharged ash is cooled and solidified by another method, and can be reused as a product such as ceramic.
- the workpiece is thrown into the crucible 17 by the intermittent opening and closing of the auto shirt 10, and the workpiece is discharged from the discharge box 7 by the intermittent opening and closing of the auto shutter 11.
- the crucible 17 is temporarily opened by the auto shirt 10 in the input box 6 and the auto shirt 11 in the discharge box 7, except for that time.
- 11 is closed inside the crucible 17 and the crucible 17 is evacuated by the suction device 32.
- the time for which the object is in the crucible 17 is about 20 to 40 minutes. In some cases, 3 kg to 10 kg of an object to be treated can be processed in one minute.
- the material to be treated is intermittently put into the crucible 17, and the ash is intermittently discharged from the discharge box 7.
- the object to be processed is subjected to continuous thermal decomposition while being intermittent.
- FIG. 9 shows a state in which crucibles 17 (rotary furnace 3) are inclined.
- Fig. 9 shows the crucible 17 in which the outlet 17c is relatively higher than the inlet 17b (the inclination angle with respect to the horizontal plane is 0).
- the reverse may be applied.
- the thermally decomposed ash is automatically moved to a high position such as for drying. There is an advantage that can be lifted.
- the inside of the crucible in a vacuum state is heated to about 1200 ° C. to thermally decompose the object to be processed, so that dioxin and the like can be decomposed.
- the object to be processed that has entered the crucible is sequentially transferred from the inlet side to the outlet side of the crucible along the spiral groove of the crucible by the rotation of the rotary furnace, so that the object is intermittently passed through the crucible.
- the object can be thermally decomposed. Therefore, compared with the conventional method in which the object is put into and taken out of the crucible each time, a large amount of the object can be pyrolyzed continuously, and the working efficiency can be improved.
- the gas sucked from the crucible is extracted and sorted by the gas sorting and extracting device and collected. I do.
- the gas is introduced into the heat treatment device and thermally decomposed, so that no harmful gas or odor is discharged to the outside.
- the thermally decomposed ash can be automatically transferred to a high position for drying, A lift for lifting the pyrolyzed ash to a high position can be eliminated.
- the rotation speed of the crucible by the driving device it is possible to adjust the amount of decomposition of the object to be processed in the crucible. Ash produced by pyrolysis of the material to be treated can be solidified into solids and reused.
- the object to be treated since the object to be treated is thermally decomposed while rotating the rotary furnace, the object to be treated can be decomposed evenly.
- a pan-shaped ring is provided on the outer wall of the rotary furnace, and power can be supplied stably from the fixed frame during rotation of the rotary furnace to the inside of the rotary furnace.
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- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Thermal Sciences (AREA)
- Combustion & Propulsion (AREA)
- Physics & Mathematics (AREA)
- Processing Of Solid Wastes (AREA)
- Control Of Resistance Heating (AREA)
- Muffle Furnaces And Rotary Kilns (AREA)
- Pharmaceuticals Containing Other Organic And Inorganic Compounds (AREA)
Description
Claims
Priority Applications (7)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP35097899A JP3266591B2 (ja) | 1999-12-10 | 1999-12-10 | 断続流動式熱分解装置 |
| ES01932201T ES2269394T3 (es) | 1999-12-10 | 2001-05-22 | Descomponedor termico de tipo con flujo intermitente. |
| DE60121829T DE60121829D1 (de) | 1999-12-10 | 2001-05-22 | Thermischer zersetzer mit intermittierender strömung |
| PCT/JP2001/004278 WO2002094463A1 (en) | 1999-12-10 | 2001-05-22 | Intermittent flowing type thermal decomposer |
| AT01932201T ATE333955T1 (de) | 1999-12-10 | 2001-05-22 | Thermischer zersetzer mit intermittierender strömung |
| US10/474,835 US6877444B2 (en) | 1999-12-10 | 2001-05-22 | Intermittent flow type thermal decomposer |
| EP01932201A EP1396291B1 (en) | 1999-12-10 | 2001-05-22 | Intermittent flowing type thermal decomposer |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP35097899A JP3266591B2 (ja) | 1999-12-10 | 1999-12-10 | 断続流動式熱分解装置 |
| PCT/JP2001/004278 WO2002094463A1 (en) | 1999-12-10 | 2001-05-22 | Intermittent flowing type thermal decomposer |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| WO2002094463A1 true WO2002094463A1 (en) | 2002-11-28 |
Family
ID=26345084
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/JP2001/004278 Ceased WO2002094463A1 (en) | 1999-12-10 | 2001-05-22 | Intermittent flowing type thermal decomposer |
Country Status (7)
| Country | Link |
|---|---|
| US (1) | US6877444B2 (ja) |
| EP (1) | EP1396291B1 (ja) |
| JP (1) | JP3266591B2 (ja) |
| AT (1) | ATE333955T1 (ja) |
| DE (1) | DE60121829D1 (ja) |
| ES (1) | ES2269394T3 (ja) |
| WO (1) | WO2002094463A1 (ja) |
Families Citing this family (14)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP3266591B2 (ja) | 1999-12-10 | 2002-03-18 | アートセラミック株式会社 | 断続流動式熱分解装置 |
| US8029749B2 (en) | 2004-09-21 | 2011-10-04 | Technip France S.A.S. | Cracking furnace |
| US7749462B2 (en) | 2004-09-21 | 2010-07-06 | Technip France S.A.S. | Piping |
| GB0420971D0 (en) | 2004-09-21 | 2004-10-20 | Imp College Innovations Ltd | Piping |
| WO2007040381A1 (es) * | 2005-10-05 | 2007-04-12 | Agustin Javier Pretelin Nova | Sistema para reciclar neumáticos de desecho y derivados de hule |
| KR100799349B1 (ko) | 2006-11-20 | 2008-01-30 | (주)메덱스 | 열분해장치 및 이를 이용한 폐기물 처리시스템 |
| KR101522304B1 (ko) * | 2007-04-10 | 2015-05-28 | 판리 멩 | 노 |
| CA2734737C (en) * | 2008-08-20 | 2016-04-19 | P-Fuel Ltd | Disposal of electrical and electronic equipment |
| GB0817219D0 (en) | 2008-09-19 | 2008-10-29 | Heliswirl Petrochemicals Ltd | Cracking furnace |
| JP5519240B2 (ja) * | 2009-10-20 | 2014-06-11 | 株式会社イーデェス | 減圧無酸素熱分解処理機の連続処理方法及びその方法に使用するユニット式装置 |
| CN103421523A (zh) * | 2013-09-02 | 2013-12-04 | 潍坊金丝达环境工程股份有限公司 | 连续气化裂解炉用穿心加热炉体 |
| CN109332351B (zh) * | 2018-09-10 | 2020-10-30 | 邢台国运工贸有限公司 | 一种环保型废旧橡胶轮胎裂解装置 |
| RU204240U1 (ru) * | 2020-08-03 | 2021-05-17 | Федеральное государственное бюджетное учреждение науки Институт проблем химической физики Российской Академии наук (ФГБУН ИПХФ РАН) | Устройство для синтеза полупроводниковых пленок |
| CN114073393B (zh) * | 2020-08-19 | 2023-06-02 | 佛山市顺德区美的电热电器制造有限公司 | 烹饪器具及其保鲜控制方法、计算机可读存储介质 |
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| DE3049250C2 (de) * | 1980-12-27 | 1985-10-24 | Kernforschungsanlage Jülich GmbH, 5170 Jülich | Einrichtung mit Schweldrehtrommel und Schachtofen |
| US4667609A (en) * | 1986-09-08 | 1987-05-26 | Robert Hardison | Apparatus and method for treatment of soil contaminated with hydrocarbons |
| DE3633212A1 (de) * | 1986-09-30 | 1988-04-14 | Kwu Umwelttechnik Gmbh | Pyrolyseanlage |
| AU674007B2 (en) * | 1992-06-09 | 1996-12-05 | Waste Gas Technology Limited | Generation of electricity from waste material |
| FI95746C (fi) * | 1994-04-20 | 1996-03-11 | Matti Pappinen | Laitteisto kostean polttoaineen polttamiseksi |
| DE4429908A1 (de) * | 1994-08-23 | 1996-02-29 | Siemens Ag | Mit Heizrohren ausgestattete Heizkammer für Festgut |
| AUPN585795A0 (en) * | 1995-10-06 | 1995-11-02 | Tox Free Systems Inc. | Volatile materials treatment system |
| AU3469497A (en) * | 1996-06-25 | 1998-01-14 | Swedish Bioburner System Aktiebolag | Rotary burner for solid fuel |
| CA2194805C (en) * | 1997-01-10 | 2004-04-27 | Richard Bouziane | Batch process for recycling hydrocarbon containing used material |
| US6084149A (en) * | 1998-08-24 | 2000-07-04 | Akae; Yukoh | Method and apparatus for decomposing hazardous substances using high frequency waves to provide environmentally safe fixation ashes in an incinerator |
-
1999
- 1999-12-10 JP JP35097899A patent/JP3266591B2/ja not_active Expired - Fee Related
-
2001
- 2001-05-22 EP EP01932201A patent/EP1396291B1/en not_active Expired - Lifetime
- 2001-05-22 US US10/474,835 patent/US6877444B2/en not_active Expired - Fee Related
- 2001-05-22 AT AT01932201T patent/ATE333955T1/de not_active IP Right Cessation
- 2001-05-22 WO PCT/JP2001/004278 patent/WO2002094463A1/ja not_active Ceased
- 2001-05-22 ES ES01932201T patent/ES2269394T3/es not_active Expired - Lifetime
- 2001-05-22 DE DE60121829T patent/DE60121829D1/de not_active Expired - Lifetime
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS4915693A (ja) * | 1972-06-03 | 1974-02-12 | ||
| JPH06218353A (ja) * | 1993-01-28 | 1994-08-09 | Art Ceramic Kk | 遠赤外線分解装置 |
| JPH07155731A (ja) * | 1993-12-09 | 1995-06-20 | Mitsui Eng & Shipbuild Co Ltd | 集じん灰の加熱脱塩素化処理方法 |
| JPH1085703A (ja) * | 1996-09-19 | 1998-04-07 | Mitsui Eng & Shipbuild Co Ltd | 熱分解反応器 |
| JPH11263977A (ja) * | 1998-03-19 | 1999-09-28 | Meidensha Corp | 被処理物の加熱処理装置 |
| JP2001162256A (ja) * | 1999-12-10 | 2001-06-19 | Art Ceramic Kk | 断続流動式熱分解装置 |
Also Published As
| Publication number | Publication date |
|---|---|
| ATE333955T1 (de) | 2006-08-15 |
| EP1396291A4 (en) | 2004-08-25 |
| JP2001162256A (ja) | 2001-06-19 |
| ES2269394T3 (es) | 2007-04-01 |
| US20040118327A1 (en) | 2004-06-24 |
| EP1396291A1 (en) | 2004-03-10 |
| JP3266591B2 (ja) | 2002-03-18 |
| EP1396291B1 (en) | 2006-07-26 |
| DE60121829D1 (de) | 2006-09-07 |
| US6877444B2 (en) | 2005-04-12 |
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