WO2016125858A1 - 磁気分解装置、及び磁気分解方法 - Google Patents
磁気分解装置、及び磁気分解方法 Download PDFInfo
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- WO2016125858A1 WO2016125858A1 PCT/JP2016/053362 JP2016053362W WO2016125858A1 WO 2016125858 A1 WO2016125858 A1 WO 2016125858A1 JP 2016053362 W JP2016053362 W JP 2016053362W WO 2016125858 A1 WO2016125858 A1 WO 2016125858A1
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- Prior art keywords
- decomposition
- filter
- magnetic
- flue gas
- air
- Prior art date
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- 238000000354 decomposition reaction Methods 0.000 title claims abstract description 75
- 230000005291 magnetic effect Effects 0.000 title claims abstract description 50
- 238000000034 method Methods 0.000 title claims description 30
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims abstract description 37
- 239000003546 flue gas Substances 0.000 claims abstract description 37
- 238000000197 pyrolysis Methods 0.000 claims abstract description 17
- 230000008569 process Effects 0.000 claims description 23
- 238000005979 thermal decomposition reaction Methods 0.000 claims description 22
- 239000000779 smoke Substances 0.000 claims description 16
- 239000007789 gas Substances 0.000 claims description 7
- 238000004332 deodorization Methods 0.000 claims description 5
- 238000001914 filtration Methods 0.000 claims description 4
- 239000002699 waste material Substances 0.000 abstract description 24
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 14
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 abstract description 11
- 239000004744 fabric Substances 0.000 abstract description 7
- 229910021536 Zeolite Inorganic materials 0.000 abstract description 6
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 abstract description 6
- 239000010457 zeolite Substances 0.000 abstract description 6
- 238000007664 blowing Methods 0.000 abstract description 2
- 229910052799 carbon Inorganic materials 0.000 abstract 1
- 239000011269 tar Substances 0.000 description 18
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 6
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- 238000002485 combustion reaction Methods 0.000 description 4
- 235000019645 odor Nutrition 0.000 description 4
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 229910052742 iron Inorganic materials 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 229910001172 neodymium magnet Inorganic materials 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 239000005416 organic matter Substances 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- CPELXLSAUQHCOX-UHFFFAOYSA-M Bromide Chemical compound [Br-] CPELXLSAUQHCOX-UHFFFAOYSA-M 0.000 description 1
- 239000003570 air Substances 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000011111 cardboard Substances 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000001877 deodorizing effect Effects 0.000 description 1
- 239000010791 domestic waste Substances 0.000 description 1
- 239000003302 ferromagnetic material Substances 0.000 description 1
- 238000011049 filling Methods 0.000 description 1
- 230000004907 flux Effects 0.000 description 1
- 238000011068 loading method Methods 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000010893 paper waste Substances 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 229910000938 samarium–cobalt magnet Inorganic materials 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 230000000087 stabilizing effect Effects 0.000 description 1
- 239000004094 surface-active agent Substances 0.000 description 1
- 235000013311 vegetables Nutrition 0.000 description 1
- 125000000391 vinyl group Chemical group [H]C([*])=C([H])[H] 0.000 description 1
- 229920002554 vinyl polymer Polymers 0.000 description 1
Images
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Definitions
- the present invention relates to a magnetic decomposition apparatus and a magnetic decomposition method for thermally decomposing waste and the like using magnetically treated air.
- Patent Document 1 As an example of a magnetic decomposition apparatus for waste or the like, there is an organic substance decomposition treatment apparatus described in Patent Document 1, for example. This is because organic substances are put into a bowl-shaped decomposition pot and ignited by an ignition rod, and magnetized air is introduced from the air inlet of the magnetized air introduction pipe so that the fire does not extinguish, and the organic substances are burned at low temperature. By doing so, the combustion decomposition treatment is performed. Then, smoke containing tar and water vapor generated by the combustion decomposition treatment is raised, tar and water vapor are separated in the tar removal unit, and further, the smoke and moisture removed from the deodorization unit It is designed to be deodorized by exposure to a spraying atmosphere, and to be exhausted without being brominated.
- the organic matter introduced into the decomposition treatment chamber is burned by magnetic combustion at a low temperature to raise the smoke containing tar and moisture, and the tar removal unit is almost tar
- the smoke is reduced and no bromide by exposing it to a sprinkling atmosphere in the deodorizing part, and exhausted to the atmosphere.
- Patent Documents 1 and 2 remove tar and odor, they are not necessarily sufficient, and as a result, flue gas containing tar and the like is emitted.
- the filter for removing tar and the like needs to be replaced or cleaned after a certain period of time, but the operation of the entire apparatus must be stopped at that time.
- the present invention pays attention to the above points, and its purpose is to perform the magnetic decomposition process by effectively utilizing the flue gas. Another object is to replace or clean the filter without stopping the operation of the entire apparatus.
- a magnetic decomposition apparatus of the present invention is a magnetic decomposition apparatus that decomposes an object by performing magnetic decomposition using air to which a magnetic field is applied, and performs the decomposition process of the object.
- a separation processing unit a filter unit that is separated from the decomposition processing unit and that performs a filter process on the flue gas generated by the decomposition process, and sends the flue gas of the decomposition processing unit to the filter unit, and the filter A pipe for sending flue gas after filtering by the section to the decomposition processing section, a magnet provided in the pipe for applying a magnetic field to the flue gas after filtering, and the flue gas, the decomposition processing section, Circulating means for circulating between the filter unit and the filter unit is provided.
- the decomposition processing unit starts the decomposition process using a hot air gun.
- the filter section is provided with means for lowering the temperature of the flue gas on the intake side of the circulation means.
- the filter section is provided with a tar removal and deodorization filter processing function.
- the present invention is characterized in that a swash plate flue is formed on the inner wall of the thermal decomposition treatment chamber constituting the decomposition treatment portion, the air suction portion being an upward swash plate along the air flow direction.
- the circulation means provided between the decomposition processing section and the filter section is provided with a bypass means for sucking a required amount of exhaust from the decomposition processing section into the decomposition processing section.
- a magnetic decomposition method of the present invention is a magnetic decomposition method in which an object is decomposed by performing magnetic decomposition with air to which a magnetic field is applied, with the lower shutter portion closed.
- the flue gas generated in the decomposition processing unit is sent to the filter unit, and after tar removal and deodorization processing by the filter unit, the magnetic field is applied by the magnet and returned to the decomposition processing unit for circulation. Therefore, the magnetic decomposition process can be performed by effectively utilizing the flue gas.
- the filter unit is separated from the disassembly processing unit, the filter can be replaced or cleaned without stopping the operation of the entire apparatus.
- FIG. 1 It is a top view which shows the magnetic decomposition apparatus which concerns on embodiment of this invention. It is a cross-sectional top view of the thermal decomposition process chamber of the magnetic decomposition apparatus shown in FIG. It is the side view seen from the A1 and A2 direction in FIG. It is the sectional side view seen from the A1 and A2 direction in FIG. It is a sectional side view of the thermal decomposition process chamber of the magnetic decomposition apparatus shown in FIG. It is the expansion
- the magnetic decomposing apparatus 10 includes a decomposition processing unit 100 and a filter unit 200. Both are connected by the exhaust duct 20 and the intake duct 30, and the smoke is circulated between the decomposition processing unit 100 and the filter unit 200.
- a hopper 120 for introducing waste is provided at the top of the thermal decomposition processing chamber 110 where the waste is decomposed.
- Various items such as household waste, waste paper, cardboard, waste plastic, wood waste, vegetable waste, rubber, vinyl, etc. can be targeted as the hopper 120.
- the upper shutter 122 is provided on the upper part of the hopper 120, and the lower shutter 124 is provided on the lower part. Further, a staircase 130 for transporting waste from the ground to the hopper 120 and a step (floor) 132 for loading are provided.
- the upper shutter 122 is opened with the lower shutter 124 closed, and waste is thrown into the hopper 120.
- the lower shutter 124 is opened with the upper shutter 122 closed, and the waste is disposed in the pyrolysis chamber 110. It is possible to satisfactorily prevent the outside air (air that has not been magnetically decomposed) from flowing into the thermal decomposition treatment chamber 110 by dropping it into the air.
- the hopper 120 is connected to the exhaust duct 20, and the exhaust gas filling the hopper 120 can be exhausted to the filter unit 200 by the above-described opening and closing operation, so that the exhaust gas can be prevented from flowing out to the outside.
- the upper shutter 122 and the lower shutter 124 may be electrically operated, hydraulic, or the like as necessary, or may be opened and closed in conjunction with each other.
- the upper shutter 122 operates a switch (not shown) to rotationally drive the ball screw 122E via the geared motor 122A, the sprocket 122B, the roller chain 122C, and the sprocket 122D, and the rotational motion is shuttered by the driving screw 122F.
- the drive rod 122G is converted into a linear motion and driven to open and close.
- the lower shutter 124 rotates a ball screw 124E via a geared motor 124A, a sprocket 124B, a roller chain 124C, and a sprocket 124D by operating a switch (not shown). It is driven to open and close by converting into a linear motion. Since the lower shutter 124 is a pair of left and right shutter plates, it is driven by a right and left target drive mechanism.
- the thermal decomposition chamber 110 is provided with an opening 112 on its side surface and is closed during the decomposition process.
- the opening 112 is used to send hot air into the processing chamber at the start of the decomposition process and to remove residues after the decomposition process.
- the inner wall of the thermal decomposition treatment chamber 110 mainly serves as a flue, and is formed using a material such as an iron plate that is a ferromagnetic material. Further, as shown in FIGS. 4 and 5, a swash plate flue 114 having an air suction portion facing upward is formed on the inner wall of the pyrolysis chamber 110. Regardless of the position of the waste thrown into the chamber 110, the flue gas generated by the thermal decomposition of the waste is guided upward by the swash plate flue 114 and efficiently discharged into the exhaust duct 20. It will be.
- the filter unit 200 includes a plurality of filter devices and a blower device for circulating the exhaust gas.
- Smoke introduced from the exhaust duct 20 described above passes through the filter unit 200 in the order of the shower 210, the swash plate filter 220, the blower 230, the water tank filter 240, the cloth filter 250, the zeolite filter 260, and the activated carbon filter 270, and takes in the intake air. It reaches the duct 30. Further, the blower 230 circulates smoke in the entire apparatus.
- the shower 210 is configured to apply a shower to the flue gas from the water spray pipe 212.
- the swash plate filter 220 is configured to emit smoke to a plurality of diagonally arranged plates 222.
- the shower 210 and the swash plate filter 220 are for reducing the temperature of the flue gas, removing tar, and reducing the burden on the subsequent blower 230.
- the aquarium filter 240 is mainly for removing tar by the smoke exhausted as bubbles in the water.
- the cloth filter 250 is for removing moisture in the flue gas by the cloth.
- the zeolite filter 260 mainly has a smoke eliminating effect and removes the color.
- the activated carbon filter 270 is mainly for removing odors in the flue gas.
- the flue gas from which tars and odors have been removed by these filters does not pose any problem even if it is released into the atmosphere, but in this embodiment, the flue gas passes through the intake duct 30 and passes through the iron pipe and is thermally decomposed. Return to the processing chamber 110. At this time, the flue gas is magnetically decomposed by the strong magnetic field generated by the magnet 32 provided in the intake duct 30. The magnet 32 is attached to the outside of the iron pipe protruding outside the pyrolysis chamber 110.
- a permanent magnet such as an Nd—Fe—B magnet (neodymium magnet) or an Sm—Co magnet (samarium-cobalt magnet) is a suitable example.
- a strong magnetic field can be obtained without the need for another energy source.
- oxygen and nitrogen in the air are separated.
- the magnetic susceptibility of oxygen is 1000 times that of nitrogen, this acts on waste and undergoes thermal decomposition.
- a permanent magnet having a magnetic flux density of, for example, about 700 mT (7000 gauss) or higher is used as the magnet 32.
- the hot air gun 40 is used to start processing. Thereby, the decomposition process is started and continued without using any fire. Specifically, the opening 112 of the thermal decomposition treatment chamber 110 is opened, hot air is blown from here with the hot air gun 40, and the blower 230 is driven to magnetically decompose and circulate the smoke to continue the decomposition process. It is supposed to be done.
- the upper shutter 122 is opened with the lower shutter 124 closed, and waste is thrown into the hopper 120.
- the lower shutter 124 is opened with the upper shutter 122 closed, and the waste falls into the pyrolysis chamber 110.
- the blower 230 is driven to circulate air between the decomposition processing unit 100 and the filter unit 200 through the exhaust duct 20 and the intake duct 30. Thereby, the air is magnetically decomposed by the magnetic field of the magnet 32 provided in the intake duct 30, and the decomposed air is sent to the thermal decomposition treatment chamber 110.
- the intake / exhaust of the decomposition processing unit 110 exhausts the flue gas expanded by the thermal decomposition through the exhaust duct 20, but only the required amount is sent in by the bypass pipe 50 without forcibly sending in the intake air.
- the bypass pipe 50 by providing the bypass pipe 50, the gas in the intake duct 30 can be sucked into the pyrolysis chamber 110 by a necessary amount and the unnecessary amount can be diverted to the exhaust duct 20 via the bypass pipe 50.
- the opening 112 of the pyrolysis chamber 110 is opened, and hot air of about 500 ° C. is blown by the hot air gun 40, for example. Then, the waste is thermally decomposed in the thermal decomposition treatment chamber 110. Air blowing by the hot air gun 40 may be performed for about 3 minutes, and then thermal decomposition continues.
- the temperature in the pyrolysis chamber 110 is approximately 400 to 500 ° C., and no internal combustion occurs.
- Smoke generated by the thermal decomposition is sent to the filter unit 200 through the exhaust duct 20.
- the flue gas passes through the shower 210 and the swash plate filter 220 of the filter unit 200, so that the temperature decreases, tar is removed, and the exhaust gas passes through the blower 230.
- the flue gas further passes through the water tank filter 240 to further remove tar, and then the cloth filter 250 removes moisture.
- the flue gas is sent from the intake duct 30 to the thermal decomposition treatment chamber 110. At this time, a magnetic field of smoke is applied by the magnet 32 and used for the thermal decomposition process.
- the water tank of the shower 210 separates the water tank of the shower 210 and the water tank filter 240, and mix the surfactant in the water tank of the shower 210 in the range of 1% to 5%. Further, sodium hydroxide is mixed in the water tank of the water tank filter 240 in the range of 1% to 5% to adsorb carbon dioxide in the flue gas. As a result, the gas that passes through the intake duct 30 and returns to the thermal decomposition treatment chamber 110 is made cleaner.
- the present embodiment has the following effects. a. Smoke generated in the decomposition processing unit 100 is sent from the exhaust duct 20 to the filter unit 200, and after the tar removal and deodorization processing by the filter unit 200, the decomposition process is performed while applying the magnetic field by the magnet 32 provided in the intake duct 30. Since it was made to return and circulate to the part 100, a magnetic decomposition process can be performed using a flue gas effectively. b. Since the filter unit 200 is separated from the decomposition processing unit 100, if a plurality of filter units 200 are prepared and the connection between the exhaust duct 20 and the intake duct 30 is switched, the used filter unit 200 can be changed.
- this invention is not limited to embodiment mentioned above, A various change can be added in the range which does not deviate from the summary of this invention. For example, the following are also included.
- (1) The shapes and dimensions shown in the above embodiment are merely examples, and the design can be changed so as to achieve the same actions and effects.
- the shower 210 and the swash plate filter 220 are provided in the front stage (intake side) of the blower 230, and the water tank filter 240, the cloth filter 250, the zeolite filter 260, and the activated carbon filter 270 are provided in the rear stage of the blower 230 ( Although provided on the exhaust side), which filter is provided at which position may be appropriately set as necessary.
- the filter unit is separated from the decomposition processing unit, and the magnetic field is applied between them to circulate the smoke, which is suitable for the decomposition processing of various wastes.
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Abstract
Description
排煙は、フィルタ部200のシャワー210及び斜板フィルタ220を通過することで、温度が低下するとともに、タールが除去されて、ブロワ230を通過する。排煙は、更に水槽フィルタ240を通過することで更にタールが除去され、次に布フィルタ250で水分の除去が行われる。その後、排煙は、ゼオライトフィルタ260及び活性炭フィルタ270によって臭いが除去された後、吸気ダクト30から熱分解処理室110に送られる。このとき、磁石32によって排煙の磁場印加が行われ、熱分解処理に利用される。
a.分解処理部100で生じた排煙を、排気ダクト20からフィルタ部200に送り、フィルタ部200によるタール除去や消臭処理の後、吸気ダクト30に設けた磁石32による磁場を印加しつつ分解処理部100に戻して循環させるようにしたので、排煙を有効に活用して磁気分解処理を行うことができる。
b.フィルタ部200を分解処理部100と分離することとしたので、フィルタ部200を複数台用意して、排気ダクト20と吸気ダクト30の接続切り替えを行うようにすれば、使用済みのフィルタ部200のメンテナンスを行いつつ、新しいフィルタ部200による分解処理を行うことができ、装置全体の稼働停止を伴うことなく、分解処理を継続することができる。
c.ホットエアガンを用いて熱分解の開始を行うこととしたので、火を全く使用せず、安全に廃棄物を処理することができる。
d.排煙を循環させるブロワの前段に、排煙の温度を下げるフィルタ、タールを除去するフィルタを設けることとしたので、ブロワの負担が低減される。
(1)前記実施の形態で示した形状や寸法は一例であり、同様の作用・効果を奏するように設計変更可能である。
(2.)前記実施の形態では、シャワー210及び斜板フィルタ220をブロワ230の前段(吸気側)に設け、水槽フィルタ240、布フィルタ250、ゼオライトフィルタ260、活性炭フィルタ270をブロワ230の後段(排気側)に設けたが、どの位置にどのフィルタを設けるかは、必要に応じて適宜設定してよい。
20 排気ダクト
30 吸気ダクト
32 磁石
40 ホットエアガン
50 バイパス配管
100 分解処理部
110 熱分解処理室
112 開口
114 斜板煙道
120 ホッパー
122 上部シャッター
122A ギヤドモータ (ギヤーモータ)
122B スプロケット
122C ローラーチェーン
122D スプロケット
122E ボールねじ
122F 駆動ねじ
122G シャッター駆動棒
124 下部シャッター
124A ギヤドモータ (ギヤーモータ)
124B スプロケット
124C ローラーチェーン
124D スプロケット
124E ボールねじ
124F 駆動ねじ
124G シャター駆動棒
130 階段
132 投入用ステップ
200 フィルタ部
210 シャワー
212 散水管
220 斜板フィルタ
230 ブロワ
240 水槽フィルタ
250 布フィルタ
260 ゼオライトフィルタ
270 活性炭フィルタ
Claims (7)
- 磁場が印加された空気による磁気分解を行って対象物を分解処理する磁気分解装置であって、
前記対象物の分解処理を行う分解処理部と、
該分解処理部と分離しており、分解処理によって生じた排煙に対してフィルタ処理を施すフィルタ部と、
前記分解処理部の排煙を前記フィルタ部に送るとともに、前記フィルタ部によるフィルタ処理後の排煙を前記分解処理部に送る配管と、
前記配管に設けられており、フィルタ処理後の排煙に磁場を印加する磁石と、
前記排煙を、前記分解処理部とフィルタ部との間で循環させるための循環手段と
を備えたことを特徴とする磁気分解装置。 - 前記分解処理部は、ホットエアガンを利用して分解処理を開始することを特徴とする請求項1記載の磁気分解装置。
- 前記フィルタ部は、前記循環手段の吸気側に、排煙の温度を低下させる手段を備えていることを特徴とする請求項1記載の磁気分解装置。
- 前記フィルタ部は、タール除去及び消臭のフィルタ処理機能を備えたことを特徴とする請求項1記載の磁気分解装置。
- 前記分解処理部を構成する熱分解処理室の内壁に、空気吸入部が空気の流れ方向に沿って上向きの斜板である斜板煙道が形成されている請求項1記載の磁気分解装置。
- 前記分解処理部と前記フィルタ部との間に設けられる前記循環手段に、前記分解処理部からの排気の一部の必要量を分解処理部に吸気するためのバイパス手段を設けた請求項1記載の磁気分解装置。
- 磁場が印加された空気による磁気分解を行って対象物を分解処理する磁気分解方法であって、
下部シャッター部を閉じた状態で、上部シャッター部を開けて対象物をホッパーに投入する工程と、
前記対象物を前記ホッパーに投入した後に、前記上部シャッター部を閉める工程と、
前記上部シャッター部を閉めた後に、前記下部シャッター部を開けて、前記対象物を熱分解処理室に投入する工程と、
ブロアを駆動して、少なくとも前記熱分解処理室、排気ダクト、及び吸気ダクトにおいて空気を循環する工程と、
を備えたことを特徴とする磁気分解方法。
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CN201680008737.5A CN107206440A (zh) | 2015-02-06 | 2016-02-04 | 磁分解装置及磁分解方法 |
MYPI2017702847A MY182480A (en) | 2015-02-06 | 2016-02-04 | Magnetic decomposition device |
US15/549,105 US20180021721A1 (en) | 2015-02-06 | 2016-02-04 | Magnetic decomposition device, and magnetic decomposition method |
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Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2006214712A (ja) * | 2005-01-07 | 2006-08-17 | Mitsubishi Heavy Ind Ltd | 加圧高温ガス冷却器 |
JP2010058103A (ja) * | 2008-09-01 | 2010-03-18 | Eco Clean Eiko:Kk | 磁気空気作用による有機物熱分解装置 |
JP2010075823A (ja) * | 2008-09-25 | 2010-04-08 | Jiro Terasawa | 有機物分解処理装置 |
JP2011005457A (ja) * | 2009-06-29 | 2011-01-13 | Akira Uzawa | 有機物分解処理装置 |
JP2014128781A (ja) * | 2012-12-27 | 2014-07-10 | Sekiji Aoki | 磁場空気流による不用有機物熱分解継続装置 |
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Publication number | Priority date | Publication date | Assignee | Title |
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CN101307154B (zh) * | 2007-05-15 | 2011-06-22 | 蔡松桦 | 复合式物质热裂解整合系统 |
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BRPI0908589A2 (pt) * | 2008-03-17 | 2019-09-24 | Cornerstone Tech Partners Inc | sistema e método de decomposição de resíduo orgânico |
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Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2006214712A (ja) * | 2005-01-07 | 2006-08-17 | Mitsubishi Heavy Ind Ltd | 加圧高温ガス冷却器 |
JP2010058103A (ja) * | 2008-09-01 | 2010-03-18 | Eco Clean Eiko:Kk | 磁気空気作用による有機物熱分解装置 |
JP2010075823A (ja) * | 2008-09-25 | 2010-04-08 | Jiro Terasawa | 有機物分解処理装置 |
JP2011005457A (ja) * | 2009-06-29 | 2011-01-13 | Akira Uzawa | 有機物分解処理装置 |
JP2014128781A (ja) * | 2012-12-27 | 2014-07-10 | Sekiji Aoki | 磁場空気流による不用有機物熱分解継続装置 |
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