JP2008264641A - Treatment apparatus of harmful substance, such as organic halogen compound - Google Patents

Treatment apparatus of harmful substance, such as organic halogen compound Download PDF

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JP2008264641A
JP2008264641A JP2007108830A JP2007108830A JP2008264641A JP 2008264641 A JP2008264641 A JP 2008264641A JP 2007108830 A JP2007108830 A JP 2007108830A JP 2007108830 A JP2007108830 A JP 2007108830A JP 2008264641 A JP2008264641 A JP 2008264641A
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harmful substances
organic halogen
halogen compounds
adsorbed
solid
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JP4494432B2 (en
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Michio Tatsumi
道雄 辰巳
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Nihon Spindle Manufacturing Co Ltd
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Nihon Spindle Manufacturing Co Ltd
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a treatment apparatus of harmful substances such as an organic halogen compound and the like which efficiently agitates solid to which harmful substances are attached and adsorbed by an agitation mechanism to enhance the treatment efficiency. <P>SOLUTION: The treatment apparatus of harmful substances is provided with an enclosure 1 to introduce the solid to which the harmful substances such as an organic compound and the like are attached and adsorbed, a micro-wave irradiation mechanism 2 to radiate microwave to the solid which the harmful substances introduced to the enclosure 1 are attached and adsorbed and the agitation mechanism 6 having a rotation blade 61A, 61B arranged multistagedly to the up and down direction for agitating the solid to which the harmful substances introduced into the disclosure 1 are attached and adsorbed. <P>COPYRIGHT: (C)2009,JPO&INPIT

Description

本発明は、有機ハロゲン化合物等の有害物質の処理装置に関し、特に、有機ハロゲン化合物等の有害物質が付着・吸着した固体にマイクロ波を照射することによって有機ハロゲン化合物等の有害物質を分解するようにした有機ハロゲン化合物等の有害物質の処理装置に関するものである。   The present invention relates to a processing apparatus for harmful substances such as organic halogen compounds, and in particular, to decompose harmful substances such as organic halogen compounds by irradiating microwaves on solids to which harmful substances such as organic halogen compounds are attached and adsorbed. The present invention relates to an apparatus for treating harmful substances such as organic halogen compounds.

都市ごみ焼却炉や電気炉等から排出され、集塵機によって回収される集塵灰には、ダイオキシン類を始めとする有機ハロゲン化合物等の有害物質が含有されており、この集塵灰を、灰固化装置等によって固形化して有機ハロゲン化合物等の有害物質の溶出を防止した後に埋め立て等の処理を行っていた。   Dust collection ash discharged from municipal waste incinerators, electric furnaces, etc. and collected by dust collectors contains harmful substances such as dioxins and other organic halogen compounds. After being solidified by an apparatus or the like to prevent the elution of harmful substances such as organic halogen compounds, a treatment such as landfilling was performed.

これに対して、ダイオキシン類の人体への悪影響を最小限に抑制する目的で、「廃棄物焼却炉に係るばいじん等に含まれるダイオキシン類の量の基準及び測定の方法に関する省令」により、平成14年12月1日以降、集塵灰中に含有されるダイオキシン類の含有濃度を集塵灰1グラムにつき3ナノグラム以下にすることについての規制がなされ、集塵灰に対してもダイオキシン類を除去する措置を施す必要が生じることとなった。   On the other hand, for the purpose of minimizing the adverse effects of dioxins on the human body, according to the “Ministerial Ordinance on the Standards and Measurement Methods for the Amount of Dioxins Contained in Soot and Dust in Waste Incinerators” Since December 1st, the regulation on the concentration of dioxins contained in dust collection ash to be 3 nanograms or less per gram of dust collection ash has been made, and dioxins are also removed from dust collection ash It became necessary to take measures to do.

そして、この規制に適合すべく、集塵灰を酸素欠乏状態で、350℃以上、好ましくは、400℃以上で30分以上加熱し、さらに再合成を防ぐために加熱後急速に200℃以下に冷却する方法や、集塵灰にマイクロ波を照射することによってダイオキシン類を分解することが提案され、実用化されている(例えば、特許文献1〜3参照)。   In order to comply with this regulation, the dust ash is heated in oxygen-deficient state at 350 ° C or higher, preferably 400 ° C or higher for 30 minutes or longer, and further rapidly cooled to 200 ° C or lower after heating to prevent resynthesis. And a method of decomposing dioxins by irradiating microwaves to dust collection ash, which has been put to practical use (see, for example, Patent Documents 1 to 3).

ところで、集塵灰にマイクロ波を照射する際に使用される集塵灰を導入する筐体には、筐体内に導入した有害物質が付着・吸着した固体を攪拌する回転羽根を有する攪拌機構が配設されているが、この攪拌機構は、回転羽根を回転軸に対して放射方向に延びるように取り付けた平面的なものであるため、有害物質が付着・吸着した固体の攪拌が行われにくく、処理効率が低いという問題があった。
特開2000−334062号公報 特開2001−19646号公報 特開2005−169291号公報
By the way, the casing for introducing the dust collection ash used when irradiating the dust collection ash with microwaves has a stirring mechanism having a rotating blade for stirring the solid adhering to and adsorbing the harmful substances introduced into the casing. Although it is arranged, this stirring mechanism is a flat one in which the rotating blades are attached so as to extend in the radial direction with respect to the rotation axis, so that it is difficult to stir solids with adhering or adsorbing harmful substances. There was a problem that processing efficiency was low.
JP 2000-334062 A JP 2001-19646 A JP 2005-169291 A

本発明は、上記マイクロ波を使用する処理装置が有する問題点に鑑み、攪拌機構による有害物質が付着・吸着した固体の攪拌を効率的に行い、処理効率を向上することができるようにした有機ハロゲン化合物等の有害物質の処理装置を提供することを目的とする。   In view of the problems of the processing apparatus using the microwave, the present invention efficiently stirs a solid to which harmful substances are adhered and adsorbed by a stirring mechanism, thereby improving the processing efficiency. It aims at providing the processing apparatus of harmful substances, such as a halogen compound.

上記目的を達成するため、本発明の有機ハロゲン化合物等の有害物質の処理装置は、有機ハロゲン化合物等の有害物質が付着・吸着した固体を導入する筐体と、該筐体内に導入した有害物質が付着・吸着した固体にマイクロ波を照射するマイクロ波照射機構と、筐体内に導入した有害物質が付着・吸着した固体を攪拌する回転羽根を有する攪拌機構とを備えた有機ハロゲン化合物等の有害物質の処理装置において、前記攪拌機構の回転羽根を上下方向に多段に配設したことを特徴とする。   In order to achieve the above-described object, the processing apparatus for harmful substances such as organic halogen compounds according to the present invention includes a housing for introducing a solid to which harmful substances such as organic halogen compounds are attached and adsorbed, and a harmful substance introduced into the housing. Hazardous to organic halogen compounds, etc., equipped with a microwave irradiation mechanism that irradiates a solid to which a solid adheres and is adsorbed, and a stirring mechanism that has a rotating blade that stirs the solid that has adhered and adsorbed to a hazardous substance In the substance processing apparatus, the rotating blades of the stirring mechanism are arranged in multiple stages in the vertical direction.

この場合において、上段に配設した回転羽根の回転外周径を、下段に配設した回転羽根の回転外周径より小さく設定することができる。   In this case, the rotational outer peripheral diameter of the rotary blade disposed in the upper stage can be set smaller than the rotational outer peripheral diameter of the rotary blade disposed in the lower stage.

また、回転羽根を板状部材で構成し、該板状部材を、板状部材の下端が回転羽根の回転方向の前方側に位置するように、回転軸に対して放射方向に延びる回転支軸に傾斜して取り付けるようにするとともに、下段に配設した回転羽根の傾斜方向の略延長線上に、上段に配設した回転羽根が位置するようにすることができる。   Further, the rotary blade is constituted by a plate-like member, and the plate-like member is a rotation support shaft that extends in the radial direction with respect to the rotation axis so that the lower end of the plate-like member is located on the front side in the rotation direction of the rotary blade. In addition, the rotary blades disposed in the upper stage can be positioned on a substantially extended line in the tilt direction of the rotary blades disposed in the lower stage.

また、回転羽根を、上部に櫛歯を下部にスクレーパをそれぞれ形成した板状部材で構成し、かつ、櫛歯の間隙の寸法を照射するマイクロ波の波長の1/4の整数倍の近傍域を外して形成することができる。   Further, the rotating blade is composed of a plate-like member in which the comb teeth are formed on the upper portion and the scraper is formed on the lower portion, and in the vicinity of an integral multiple of 1/4 of the wavelength of the microwave that irradiates the size of the gap between the comb teeth. Can be removed.

本発明の有機ハロゲン化合物等の有害物質の処理装置は、有機ハロゲン化合物等の有害物質が付着・吸着した固体を導入する筐体と、該筐体内に導入した有害物質が付着・吸着した固体にマイクロ波を照射するマイクロ波照射機構と、筐体内に導入した有害物質が付着・吸着した固体を攪拌する回転羽根を有する攪拌機構とを備えた有機ハロゲン化合物等の有害物質の処理装置において、前記攪拌機構の回転羽根を上下方向に多段に配設することにより、攪拌機構による有害物質が付着・吸着した固体(本明細書において、「処理対象物」という場合がある。)の攪拌を効率的に行い、処理対象物にマイクロ波を均一に照射し、処理効率を向上することができる。   The apparatus for treating harmful substances such as organic halogen compounds according to the present invention includes a housing for introducing solids to which harmful substances such as organic halogen compounds are attached and adsorbed, and a solid to which harmful substances introduced into the case are attached and adsorbed. In an apparatus for treating harmful substances such as organic halogen compounds, comprising a microwave irradiation mechanism for irradiating microwaves, and a stirring mechanism having a rotating blade for stirring solids adhering to and adsorbing the harmful substances introduced into the housing, By arranging the rotating blades of the stirring mechanism in multiple stages in the vertical direction, it is possible to efficiently stir solids (sometimes referred to as “objects to be treated” in this specification) to which harmful substances are attached and adsorbed by the stirring mechanism. The processing efficiency can be improved by uniformly irradiating the object to be processed with microwaves.

また、上段に配設した回転羽根の回転外周径を、下段に配設した回転羽根の回転外周径より小さく設定することにより、処理対象物が処理装置の中心側と外周側との間で循環しやすくなり、処理対象物の攪拌を一層効率的に行うことができる。   Further, by setting the rotational outer peripheral diameter of the rotary blade disposed in the upper stage to be smaller than the rotational outer peripheral diameter of the rotary blade disposed in the lower stage, the processing object is circulated between the center side and the outer peripheral side of the processing apparatus. This makes it easier to stir the object to be processed.

また、回転羽根を板状部材で構成し、該板状部材を、板状部材の下端が回転羽根の回転方向の前方側に位置するように、回転軸に対して放射方向に延びる回転支軸に傾斜して取り付けるようにするとともに、下段に配設した回転羽根の傾斜方向の略延長線上に、上段に配設した回転羽根が位置するようにすることにより、下段に配設した回転羽根によって掬い上げられ、移動しやすくなった処理対象物を、上段に配設した回転羽根によって続けて掬い上げることによって、処理対象物の攪拌を一層効率的に行うことができる。   Further, the rotary blade is constituted by a plate-like member, and the plate-like member is a rotation support shaft that extends in the radial direction with respect to the rotation axis so that the lower end of the plate-like member is located on the front side in the rotation direction of the rotary blade. By attaching the rotating blades disposed in the upper stage to the lower blades, the rotating blades disposed in the upper stage are positioned on the substantially extended line in the inclination direction of the rotating blades disposed in the lower stage. By continuously scooping up the processing target that has been scooped up and easily moved by the rotary blades arranged in the upper stage, the processing target can be stirred more efficiently.

また、回転羽根を、上部に櫛歯を下部にスクレーパをそれぞれ形成した板状部材で構成し、かつ、櫛歯の間隙の寸法を照射するマイクロ波の波長の1/4の整数倍の近傍域を外して形成することにより、回転羽根に櫛歯状のものを使用した場合における回転羽根の近傍域でのマイクロ波の共振による異常現象の発生を抑制することができるとともに、処理対象物を筐体の底部から掻き上げるようにして確実に攪拌することができる。   Further, the rotating blade is composed of a plate-like member in which the comb teeth are formed on the upper portion and the scraper is formed on the lower portion, and in the vicinity of an integral multiple of 1/4 of the wavelength of the microwave that irradiates the size of the gap between the comb teeth. In this case, it is possible to suppress the occurrence of an abnormal phenomenon due to the resonance of the microwave in the vicinity of the rotating blade when a comb-shaped rotating blade is used. Stirring can be ensured by scraping from the bottom of the body.

以下、本発明の有機ハロゲン化合物等の有害物質の処理装置の実施の形態を図面に基づいて説明する。   Embodiments of a processing apparatus for harmful substances such as organic halogen compounds according to the present invention will be described below with reference to the drawings.

図1〜図4に、本発明の有機ハロゲン化合物等の有害物質の処理装置の一実施例を示す。   1 to 4 show an embodiment of a processing apparatus for harmful substances such as organic halogen compounds of the present invention.

この有機ハロゲン化合物等の有害物質の処理装置は、有機ハロゲン化合物等の有害物質が付着・吸着した固体(例えば、集塵灰等の粉体)を導入する密閉容器として構成した筐体1と、この筐体1内に導入した有害物質が付着・吸着した固体にマイクロ波を照射するマイクロ波照射機構2と、筐体1内に導入した有害物質が付着・吸着した固体を攪拌する回転羽根61A、61Bを有する攪拌機構6(本実施例において、攪拌機構6は、処理済みの固体を導出部5aに導く排出機構を兼ねるようにしている。)とを備えるようにしている。   The processing apparatus for harmful substances such as organic halogen compounds includes a housing 1 configured as a sealed container for introducing a solid (for example, powder such as dust collection ash) to which harmful substances such as organic halogen compounds are attached and adsorbed; A microwave irradiation mechanism 2 that irradiates a solid to which a harmful substance introduced into and adsorbed in the casing 1 is irradiated with microwaves, and a rotating blade 61A that stirs the solid to which the harmful substance introduced into the casing 1 is adhered and adsorbed , 61B (in this embodiment, the stirring mechanism 6 serves as a discharge mechanism that guides the treated solid to the outlet portion 5a).

この場合において、筐体1は、筐体1内に導入した有害物質が付着・吸着した固体の上方においてマイクロ波の照射空間を構成する筐体1の上半部の周壁1Aの平面断面形状を5角形以上の多角形(特に限定されるものではないが、本実施例においては、略正8角形)に形成するようにしている。
ここで、「平面断面形状を5角形以上の多角形により形成する」とは、具体的には、筐体1の上半部の周壁1Aを、5角形以上の多角筒形状や角錐又は角錐台形状に形成することを意味する。
これにより、筐体1の上半部の周壁1Aの内壁面で反射したマイクロ波が特定箇所に集中することがなく、処理対象物である有機ハロゲン化合物等の有害物質が付着・吸着した固体にマイクロ波を均一に照射することができる。
なお、多角形の辺の個数は、5個以上であれば特に限定されるものではないが、20個を越えると、円形に近づいて、筐体1の上半部の周壁1Aの内壁面で反射したマイクロ波が筐体1の中心軸に集中する傾向が生じ、好ましくない。
一方、4個以下の場合は、角部等にマイクロ波が照射されにくい箇所が生じ、好ましくない。
In this case, the housing 1 has a planar cross-sectional shape of the peripheral wall 1A of the upper half of the housing 1 constituting the microwave irradiation space above the solid to which the harmful substance introduced into the housing 1 adheres and is adsorbed. The polygon is formed to be a pentagon or more (not particularly limited, but in the present embodiment, a substantially regular octagon).
Here, “the planar cross-sectional shape is formed by a polygon having a pentagon or more” specifically, the peripheral wall 1A of the upper half of the casing 1 is formed by a polygonal cylinder shape or a pyramid or a pyramid of a pentagon or more. It means forming into a shape.
As a result, the microwave reflected by the inner wall surface of the peripheral wall 1A of the upper half of the housing 1 does not concentrate on a specific location, and the solid object to which a harmful substance such as an organic halogen compound as a processing target adheres or is adsorbed. Microwaves can be irradiated uniformly.
The number of sides of the polygon is not particularly limited as long as it is 5 or more. However, when it exceeds 20, the shape approaches a circle, and the inner wall surface of the peripheral wall 1A of the upper half of the housing 1 The reflected microwave tends to concentrate on the central axis of the housing 1, which is not preferable.
On the other hand, when the number is four or less, a corner is difficult to be irradiated with microwaves, which is not preferable.

また、平面断面形状の多角形は、略正多角形にすることが好ましい。
これにより、処理対象物にマイクロ波を偏りなく、均一に照射することができる。
Moreover, it is preferable that the polygon of a planar cross-sectional shape is a substantially regular polygon.
Thereby, it is possible to uniformly irradiate the processing object with the microwave without bias.

また、平面断面形状の多角形は、奇数個の辺を有する多角形にすることが好ましい。 これにより、偶数個の辺を有する多角形の場合のようにマイクロ波が対向する筐体1の上半部の周壁1Aの内壁面間で反射することがなく、筐体1の上半部の周壁1Aの内壁面で反射したマイクロ波が分散されやすく、処理対象物にマイクロ波を一層均一に照射することができる。   Moreover, it is preferable that the polygon of a planar cross-sectional shape is a polygon having an odd number of sides. Thus, the microwave does not reflect between the inner wall surfaces of the peripheral wall 1A of the upper half of the casing 1 facing each other as in the case of a polygon having an even number of sides, and the upper half of the casing 1 is not reflected. The microwaves reflected by the inner wall surface of the peripheral wall 1A are easily dispersed, and the processing object can be more uniformly irradiated with the microwaves.

また、筐体1の上半部の周壁1Aは、角錐又は角錐台形状(特に限定されるものではないが、本実施例においては、略正8角錐台形状)に形成することが好ましい。
これにより、筐体の上半部の周壁1Aの内壁面で反射したマイクロ波を下向きに指向させることができ、処理対象物にマイクロ波を効率よく照射することができる。
この場合、筐体1の上半部の周壁1Aの鉛直面に対する角度θは、数度〜20度程度(特に限定されるものではないが、本実施例においては、約5度)に設定することが好ましい。
Further, the peripheral wall 1A of the upper half of the housing 1 is preferably formed in a pyramid shape or a truncated pyramid shape (not particularly limited, but in the present embodiment, a substantially regular octagonal truncated pyramid shape).
Thereby, the microwave reflected on the inner wall surface of the peripheral wall 1A of the upper half of the casing can be directed downward, and the object to be processed can be efficiently irradiated with the microwave.
In this case, the angle θ of the upper half of the casing 1 with respect to the vertical surface of the peripheral wall 1A is set to several degrees to 20 degrees (although it is not particularly limited, it is about 5 degrees in this embodiment). It is preferable.

一方、筐体1の下半部の周壁1Bは、筐体1内に導入した有害物質が付着・吸着した固体を攪拌するとともに、処理済みの固体を導出部5aに導くための攪拌機構6を配設する関係上、円筒形状に形成するようにしている。
そして、本実施例においては、筐体1の上半部の周壁1Aと下半部の周壁1Bとを、なだらかな中間部の周壁1Cにより接続するようにし、電磁波に対してアンテナとなる突起物が少ない構造とするようにしている。
On the other hand, the peripheral wall 1B in the lower half of the housing 1 stirs the solid adhered to and adsorbed by the harmful substances introduced into the housing 1, and has a stirring mechanism 6 for guiding the treated solid to the outlet portion 5a. In view of the arrangement, it is formed in a cylindrical shape.
In this embodiment, the peripheral wall 1A of the upper half of the casing 1 and the peripheral wall 1B of the lower half are connected to each other by the gentle peripheral wall 1C so that the projection serves as an antenna against electromagnetic waves. The structure is small.

筐体1は、ステンレススチール、アルミニウム、アルミニウム合金等の電磁波吸収性の低い材料で構成するようにすることが好ましいが、鉄系材料で構成することもできる。   The housing 1 is preferably made of a material having low electromagnetic wave absorption such as stainless steel, aluminum, aluminum alloy or the like, but can also be made of an iron-based material.

そして、筐体1の上面及び/又は上半部の周面に複数台のマイクロ波照射機構2を、また、上面に筐体1内で発生した排ガスを濾過するフィルタ濾過機構3及び有機ハロゲン化合物等の有害物質が付着・吸着した固体の導入部4を、下面に排出機構を兼ねた攪拌機構6に加え、処理済みの固体の導出部5a、ドレンの導出部5b及び処理中の固体の温度を測定する熱電対7を、それぞれ配設するようにしている。   A plurality of microwave irradiation mechanisms 2 are provided on the upper surface and / or the upper half of the casing 1, and a filter filtering mechanism 3 for filtering exhaust gas generated in the casing 1 on the upper surface and an organic halogen compound. The solid introduction part 4 to which harmful substances such as adhering and adhering are added to the stirring mechanism 6 also serving as a discharge mechanism on the lower surface, the treated solid lead-out part 5a, the drain lead-out part 5b, and the temperature of the solid being treated The thermocouples 7 for measuring are respectively arranged.

有機ハロゲン化合物等の有害物質が付着・吸着した固体には、必要に応じて、水添加機構、アルカリ物質添加機構、電磁波吸収物質添加機構、還元剤添加機構等(図示省略)から、有害物質を分解処理するために必要な水分、アルカリ物質(酸化カルシウムCaOや水酸化ナトリウムNaOH等)、電磁波吸収物質(活性炭や酸化鉄等)、還元剤等を添加できるようにするが、これらの水添加機構、アルカリ物質添加機構、電磁波吸収物質添加機構、還元剤添加機構等は、筐体1に備えるようにするほか、この処理装置による処理工
程の前工程に配設し、有機ハロゲン化合物等の有害物質が付着・吸着した固体に水分、アルカリ物質、電磁波吸収物質、還元剤等を添加した状態で筐体1に供給するようにすることもできる。
なお、添加物質としては、このほか、酸化反応量の調整を主目的として、空気や窒素を筐体1内部に供給することも可能である。
If necessary, remove the harmful substances such as organic halogen compounds from the water addition mechanism, alkali substance addition mechanism, electromagnetic wave absorbing substance addition mechanism, reducing agent addition mechanism, etc. (not shown). It is possible to add water, alkali substances (calcium oxide CaO, sodium hydroxide NaOH, etc.), electromagnetic wave absorbing substances (activated carbon, iron oxide, etc.), reducing agents, etc. necessary for the decomposition treatment. In addition to the alkali substance addition mechanism, electromagnetic wave absorbing substance addition mechanism, reducing agent addition mechanism, etc. provided in the housing 1, they are disposed in the previous process of the treatment process by this treatment apparatus, and are toxic substances such as organic halogen compounds. It is also possible to supply to the housing 1 in a state where moisture, an alkaline substance, an electromagnetic wave absorbing substance, a reducing agent, etc. are added to the solid adhered and adsorbed.
In addition, as an additive substance, it is also possible to supply air or nitrogen into the housing 1 mainly for the purpose of adjusting the amount of oxidation reaction.

マイクロ波照射機構2は、マイクロ波照射機構2に各々マイクロ波発振器を備えるとともに、マイクロ波発振器の取付方向を隣接するマイクロ波照射機構2間で90°向きを変えて配設するようにしている。
これにより、隣接するマイクロ波照射機構2のマイクロ波発振器から照射されるマイクロ波の干渉を低く抑えることができ、発振効率を向上することができる。
The microwave irradiation mechanism 2 includes a microwave oscillator in each of the microwave irradiation mechanisms 2, and is arranged so that the mounting direction of the microwave oscillator is changed by 90 ° between the adjacent microwave irradiation mechanisms 2. .
Thereby, the interference of the microwave irradiated from the microwave oscillator of the adjacent microwave irradiation mechanism 2 can be suppressed low, and the oscillation efficiency can be improved.

マイクロ波照射機構2の照射口2aは、石英ガラスやフッ素樹脂等の電磁波透過性が高くかつ耐薬品性と耐熱性に優れた材料で構成することによりシールを行い、筐体1内で発生する高温腐食性ガスのマイクロ波照射機構2への侵入を防止するようにする。   The irradiation port 2a of the microwave irradiation mechanism 2 performs sealing by being made of a material having high electromagnetic wave permeability such as quartz glass or fluororesin and having excellent chemical resistance and heat resistance, and is generated in the housing 1. Intrusion of the hot corrosive gas into the microwave irradiation mechanism 2 is prevented.

フィルタ濾過機構3は、図4に示すように、筐体1内で発生した排ガスを濾過して外部に排出するためのもので、フィルタ濾過機構3のケーシング30の開口部30aを介して筐体1内に照射されたマイクロ波がフィルタ濾過機構3のフィルタ部31に照射されるように、フィルタ濾過機構3のケーシング30を筐体1に連通して取り付けるようにしている。
このように、フィルタ濾過機構3のケーシング30を筐体1に連通して取り付けるようにすることにより、フィルタ濾過機構3の取り付けが簡易となり、メンテナンス時の作業も容易となる。
As shown in FIG. 4, the filter filtration mechanism 3 is for filtering the exhaust gas generated in the casing 1 and discharging it to the outside. The filter filtration mechanism 3 is connected to the casing through the opening 30 a of the casing 30 of the filter filtration mechanism 3. The casing 30 of the filter filtration mechanism 3 is attached in communication with the housing 1 so that the microwave irradiated in the filter 1 is irradiated on the filter unit 31.
Thus, by attaching the casing 30 of the filter filtration mechanism 3 in communication with the housing 1, the filter filtration mechanism 3 can be easily attached and maintenance work can be facilitated.

フィルタ濾過機構3のフィルタ部31には、マイクロ波が照射されることによって直接的に、あるいは、マイクロ波の照射によって加熱されるフィルタ部31を介して間接的に活性化される、有機ハロゲン化合物等の有害物質を分解する酸化チタンや5酸化バナジウム等の触媒32を濾布の表面に塗布又は吹き付けによって層状に配する(プレコート処理)ようにする。
フィルタ部31を構成する濾布には、セラミックスフィルタ等の電磁波吸収特性が低く、耐熱性が高い材料を使用することにより、マイクロ波による加熱ロスが生じず、このため、熱損傷を受けることがなく、省エネルギとフィルタ部の耐久性の向上を図ることができる。
The organic halogen compound that is activated directly by the microwave irradiation to the filter unit 31 of the filter filtration mechanism 3 or indirectly through the filter unit 31 heated by the microwave irradiation A catalyst 32 such as titanium oxide or vanadium pentoxide that decomposes harmful substances such as these is applied or sprayed on the surface of the filter cloth (pre-coating treatment).
By using a material having low electromagnetic wave absorption characteristics, such as a ceramic filter, and high heat resistance, the filter cloth constituting the filter unit 31 does not cause heating loss due to microwaves, and thus may be damaged by heat. Therefore, energy saving and durability of the filter part can be improved.

そして、マイクロ波の照射による加熱では、筐体1内の気体温度が上昇しにくいことから、フィルタ部31にマイクロ波によって活性化される有機ハロゲン化合物等の有害物質を分解する触媒32を配したことと相俟って、図5に示すように、フィルタ濾過機構3において、比較的低温、より具体的には、フィルタ濾過機構3に導入する排ガスの温度が200℃未満となるようにしても、有機ハロゲン化合物等の有害物質を確実に分解し、フィルタ部31に捕集した粉塵粒子(汚染粒子)を浄化粒子とするとともに、排ガスを浄化ガスとすることができる。
このように、フィルタ濾過機構3において有機ハロゲン化合物等の有害物質を比較的低温で確実に分解できることから、低沸点有害物質の捕捉効率を高めることができるとともに、フィルタ部31の耐久性を向上し、さらに、ダイオキシン類が再合成されるおそれをなくすことができる。
Since the gas temperature in the housing 1 is unlikely to rise during heating by microwave irradiation, the filter 31 is provided with a catalyst 32 that decomposes harmful substances such as organic halogen compounds activated by the microwave. In combination with this, as shown in FIG. 5, in the filter filtration mechanism 3, the temperature of the exhaust gas introduced into the filter filtration mechanism 3 is relatively low temperature, more specifically, less than 200 ° C. Further, harmful substances such as organic halogen compounds can be reliably decomposed, dust particles (contaminated particles) collected in the filter unit 31 can be used as purified particles, and exhaust gas can be used as purified gas.
Thus, since harmful substances such as organic halogen compounds can be reliably decomposed at a relatively low temperature in the filter filtration mechanism 3, the trapping efficiency of low boiling point harmful substances can be increased and the durability of the filter unit 31 can be improved. Furthermore, the possibility that dioxins are re-synthesized can be eliminated.

また、フィルタ濾過機構3には、浄化ガスを外部に排出するための排気管33と、フィルタ部31に捕集した粉塵粒子をパルスジェット等の気流により払い落とすための逆洗機構34を、それぞれ配設するようにしている。
さらに、有用低沸点物質でフィルタ濾過機構3を通過したものについては、系外に凝縮装置(図示省略)を後置することによって目的物質を回収することができる。
また、フィルタ濾過機構3を通過した浄化ガスに対して中和処理を必要とする場合は、系外にアルカリ溶液タンク(図示省略)などを後置して処理を行ったり、フィルタ部31にアルカリ物質(水酸化カルシウムCa(OH))等のアルカリ物質をプレコート処理することによって対処することができる。
Further, the filter filtration mechanism 3 includes an exhaust pipe 33 for discharging the purified gas to the outside, and a backwash mechanism 34 for removing dust particles collected by the filter unit 31 by an air flow such as a pulse jet, respectively. It is arranged.
Further, for a useful low-boiling substance that has passed through the filter filtration mechanism 3, the target substance can be recovered by placing a condenser (not shown) outside the system.
Further, when the neutralizing process is required for the purified gas that has passed through the filter filtration mechanism 3, an alkaline solution tank (not shown) or the like is placed outside the system to perform the process, or the filter unit 31 can be treated with This can be dealt with by pre-coating an alkaline substance such as a substance (calcium hydroxide Ca (OH) 2 ).

筐体1内に導入した有害物質が付着・吸着した固体を攪拌する、排出機構を兼ねた攪拌機構6は、図2〜図3に示すように、上下方向に多段(本実施例においては、2段の例を示したが、3段以上とすることもできる。)に配設した回転羽根61A、61Bを備えるようにしている。
この攪拌機構6は、有害物質が付着・吸着した固体の攪拌を効率的に行って、処理対象物にマイクロ波が均一に照射されるようにして、処理効率を向上することができるようにしている。
As shown in FIGS. 2 to 3, the stirring mechanism 6 that also serves as a discharge mechanism for stirring the solid adhering / adsorbing the harmful substance introduced into the housing 1 has multiple stages in the vertical direction (in this embodiment, Although an example of two stages is shown, it is possible to provide three or more stages.
The stirring mechanism 6 efficiently stirs a solid to which harmful substances are adhered and adsorbed so that the processing object can be uniformly irradiated with microwaves so that the processing efficiency can be improved. Yes.

この場合において、上段に配設した回転羽根61Bの回転外周径を、下段に配設した回転羽根61Aの回転外周径より小さく設定(特に限定されるものではないが、本実施例においては、約85%に設定)するようにしている。
これにより、処理対象物が筐体1の中心側と外周側との間で循環しやすくなり、処理対象物の攪拌を一層効率的に行うことができる。
In this case, the rotational outer diameter of the rotary blade 61B disposed in the upper stage is set smaller than the rotational outer diameter of the rotary blade 61A disposed in the lower stage (although it is not particularly limited, Set to 85%).
Thereby, it becomes easy to circulate a process target object between the center side of the housing | casing 1, and the outer peripheral side, and stirring of a process target object can be performed still more efficiently.

また、回転羽根61A、61Bは、図3に詳示するように(図3(a)〜(d)には、回転羽根61Aを記載しているが、回転羽根61Bも同様である。)、それぞれ櫛歯状で、かつ、櫛歯61aの間隙の寸法W1を照射するマイクロ波の波長の1/4の整数倍の近傍域(マイクロ波の波長の1/4の±10〜20%程度)を外して形成するようにし、両方の回転羽根61A、61Bを回転駆動用モータ62によって回転するようにしている。
櫛歯61aの間隙の寸法W1は、具体的には、波長:12.2cm(周波数:2.45GHz)のマイクロ波を使用する場合で、1〜2.5、3.5〜5.5、6.5〜8.5、9.5〜11.5cm程度、より好ましくは、1〜2.5、3.5〜5.5cm程度に形成するようにする。
また、櫛歯61aの幅寸法W2及び高さ方向の寸法Hは、櫛歯61aの間隙の寸法W1と略同一寸法、具体的には、1〜2.5、3.5〜5.5、6.5〜8.5、9.5〜11.5cm程度、より好ましくは、1〜2.5、3.5〜5.5cm程度に形成するようにする。
これにより、回転羽根61A、61Bに櫛歯状のものを使用した場合における回転羽根61A、61Bの近傍域でのマイクロ波の共振による異常現象の発生を抑制することができる。
Further, as shown in FIG. 3 in detail, the rotary blades 61A and 61B are shown in FIGS. 3A to 3D, but the rotary blade 61B is also the same. Each region is comb-shaped, and is in the vicinity of an integral multiple of ¼ of the wavelength of the microwave that irradiates the gap dimension W1 of the comb-tooth 61a (about ± 10 to 20% of ¼ of the wavelength of the microwave) The rotary blades 61 </ b> A and 61 </ b> B are rotated by a rotation driving motor 62.
Specifically, the dimension W1 of the gap between the comb teeth 61a is 1 to 2.5, 3.5 to 5.5 when using a microwave having a wavelength of 12.2 cm (frequency: 2.45 GHz), It is formed to have a thickness of about 6.5 to 8.5 and 9.5 to 11.5 cm, and more preferably about 1 to 2.5 and 3.5 to 5.5 cm.
The width dimension W2 and the height dimension H of the comb teeth 61a are substantially the same as the gap dimension W1 of the comb teeth 61a, specifically, 1 to 2.5, 3.5 to 5.5, It is formed to have a thickness of about 6.5 to 8.5 and 9.5 to 11.5 cm, and more preferably about 1 to 2.5 and 3.5 to 5.5 cm.
Accordingly, it is possible to suppress the occurrence of an abnormal phenomenon due to the resonance of the microwaves in the vicinity of the rotary blades 61A and 61B when the combs are used as the rotary blades 61A and 61B.

また、回転羽根61A、61Bは、上部に櫛歯61aを、下部にスクレーパ61bをそれぞれ形成した板状部材で構成し、回転軸60に対して等間隔(特に限定されるものではないが、本実施例においては、60度間隔。なお、回転羽根61A、61Bの個数に応じて、角度は設定される。)に放射方向に延びる回転支軸60aに回転方向(図2(b)の矢印方向)の前方側に位置して傾斜して取り付けるようにする。
これにより、処理対象物を筐体1の底部から掻き上げるようにして確実に攪拌することができ、処理対象物にマイクロ波を均一に照射することができる。
Further, the rotary blades 61A and 61B are constituted by plate-like members each having a comb tooth 61a formed at the upper portion and a scraper 61b formed at the lower portion, and are equally spaced with respect to the rotary shaft 60 (although not particularly limited, In the embodiment, the interval is 60 degrees, and the angle is set according to the number of the rotating blades 61A and 61B.) The rotating support shaft 60a extends in the radial direction (in the direction of the arrow in FIG. 2B). ) It is located on the front side and is inclined and attached.
Thereby, it is possible to reliably stir the processing object from the bottom of the housing 1 and to uniformly irradiate the processing object with microwaves.

また、回転羽根61A、61Bは、図3(e)に示すように、下段に配設した回転羽根61Aの傾斜方向の略延長線上に、上段に配設した回転羽根61Bが位置するように取り付けるようにする。
これにより、下段に配設した回転羽根61Aによって掬い上げられ、移動しやすくなった処理対象物を、上段に配設した回転羽根61Bによって続けて掬い上げることによって、処理対象物の攪拌を一層効率的に行うことができる。
Further, as shown in FIG. 3E, the rotating blades 61A and 61B are attached so that the rotating blade 61B disposed in the upper stage is positioned on a substantially extended line in the inclination direction of the rotating blade 61A disposed in the lower stage. Like that.
As a result, the processing object that has been scooped up by the rotating blade 61A disposed in the lower stage and easily moved is continuously scooped up by the rotating blade 61B disposed in the upper stage, thereby further stirring the processing object. Can be done automatically.

また、回転羽根61Aの外周側端部に、櫛歯61aよりも高さの高い(特に限定されるものではないが、1.5〜3倍程度に設定することが好ましい。)外周端スクレーパ61cを形成するようにする。
これにより、処理対象物が筐体1の下半部の周壁1Bの内壁面に沿って滞留することを防止し、処理対象物にマイクロ波を均一に照射することができる。
In addition, the outer peripheral end scraper 61c is higher at the outer peripheral end of the rotary blade 61A than the comb teeth 61a (although it is not particularly limited, it is preferably set to about 1.5 to 3 times). To form.
Thereby, it can prevent that a process target object stays along the inner wall face of the surrounding wall 1B of the lower half part of the housing | casing 1, and can irradiate a process target object with a microwave uniformly.

攪拌機構6の回転羽根61A、61Bは、ステンレススチール、アルミニウム、アルミニウム合金等の電磁波吸収性の低い材料で構成するようにする。
なお、回転羽根61A、61Bは、鉄系材料で構成することもできる。
The rotating blades 61A and 61B of the stirring mechanism 6 are made of a material having low electromagnetic wave absorption such as stainless steel, aluminum, and an aluminum alloy.
The rotary blades 61A and 61B can be made of an iron-based material.

また、攪拌機構6の回転羽根61A、61Bは、攪拌効率が高いため、回転駆動用モータ62によって、比較的低速、具体的には、数〜数十rpm程度、好ましくは、2〜60rpm程度、より好ましくは、5〜30rpm程度で回転駆動するようにすることができる。
これにより、エネルギコストを低廉にすることができる。
Further, since the rotating blades 61A and 61B of the stirring mechanism 6 have high stirring efficiency, they are relatively low speed, specifically about several to several tens of rpm, preferably about 2 to 60 rpm, by the rotation driving motor 62. More preferably, it can be rotationally driven at about 5 to 30 rpm.
Thereby, energy cost can be made low.

また、攪拌機構6の回転支軸60aの基部は、特に限定されるものではないが、回転軸60を含む径方向長さの1/5〜1/3程度が蓋付円筒体63で覆われている。
これにより、処理対象物が移動しにくくなる回転中心部分の発生を防止している。
Further, the base portion of the rotation support shaft 60 a of the stirring mechanism 6 is not particularly limited, but about 1/5 to 1/3 of the radial length including the rotation shaft 60 is covered with the cylindrical body 63 with a lid. ing.
Thereby, generation | occurrence | production of the rotation center part which becomes difficult to move a process target object is prevented.

熱電対7は、処理中の固体の温度を測定するためのもので、測定した温度に基づいて、マイクロ波照射出力制御機構(図示省略)によりマイクロ波照射機構2からのマイクロ波の照射出力を制御し、これにより、処理中の固体の加熱温度を常に適正に保持し、有機ハロゲン化合物の脱ハロゲン化反応等の有害物質の分解処理を優位に促進するようにしている。
なお、マイクロ波照射機構2からのマイクロ波の照射出力の制御は、熱電対7のほか、筐体1の上部に設置した放射温度計(図示省略)を併用して行うこともできる。
The thermocouple 7 is for measuring the temperature of the solid being processed. Based on the measured temperature, the microwave irradiation output control mechanism (not shown) outputs the microwave irradiation output from the microwave irradiation mechanism 2. In this way, the heating temperature of the solid during the treatment is always properly maintained, and the decomposition process of harmful substances such as the dehalogenation reaction of organic halogen compounds is promoted.
Note that the microwave irradiation output from the microwave irradiation mechanism 2 can be controlled by using a thermocouple 7 as well as a radiation thermometer (not shown) installed on the top of the housing 1.

以上、本発明の有機ハロゲン化合物等の有害物質の処理装置について、その実施例に基づいて説明したが、本発明は上記実施例に記載した構成に限定されるものではなく、その趣旨を逸脱しない範囲において適宜その構成を変更することができるものである。   As mentioned above, although the processing apparatus of harmful substances, such as the organic halogen compound of this invention, was demonstrated based on the Example, this invention is not limited to the structure described in the said Example, and does not deviate from the meaning. The configuration can be changed as appropriate within the range.

本発明の有機ハロゲン化合物等の有害物質の処理装置は、攪拌機構による有害物質が付着・吸着した固体の攪拌を効率的に行い、処理効率を向上することができるという特性を有していることから、ダイオキシン類を始めとする有機ハロゲン化合物等の有害物質が含有されている集塵灰の無害化処理の用途に好適に用いることができるほか、汚染土壌や川底の底質等の各種有害物質の無害化処理の用途にも用いることができる。   The apparatus for treating harmful substances such as organic halogen compounds according to the present invention has a characteristic that the solids adhered and adsorbed by the stirring mechanism can be efficiently stirred to improve the processing efficiency. Can be used for detoxification treatment of dust collection ash containing harmful substances such as dioxins and other organic halogen compounds, as well as various harmful substances such as polluted soil and riverbed sediment It can also be used for detoxification treatment.

本発明の有機ハロゲン化合物等の有害物質の処理装置の一実施例を示し、(a)は正面図、(b)は平面図である。One Example of the processing apparatus of harmful substances, such as an organic halogen compound of this invention, is shown, (a) is a front view, (b) is a top view. 同処理装置の攪拌機構を示し、(a)は正面図、(b)は平面図である。The stirring mechanism of the processing apparatus is shown, (a) is a front view, and (b) is a plan view. 同処理装置の攪拌機構を示し、(a)は正面拡大図、(b)は(a)のX−X断面図、(c)は(a)のY−Y断面図、(d)は(a)のZ−Z断面図、(e)は(b)に対応する上下段の回転羽根の断面図である。The stirring mechanism of the processing apparatus is shown, (a) is an enlarged front view, (b) is an XX sectional view of (a), (c) is a YY sectional view of (a), (d) is ( a) Z-Z sectional view of (a), (e) is a sectional view of upper and lower rotary blades corresponding to (b). 同処理装置のフィルタ濾過機構を示し、(a)は正面図、(b)は平面図(c)は側面図である。The filter filtration mechanism of the processing apparatus is shown, (a) is a front view, (b) is a plan view (c), and is a side view. 本発明の有機ハロゲン化合物等の有害物質の処理装置による有害物質の分解処理の概念図である。It is a conceptual diagram of the decomposition | disassembly process of a harmful substance by the processing apparatus of harmful substances, such as an organic halogen compound of this invention.

符号の説明Explanation of symbols

1 筐体
1A 上半部の周壁
1B 下半部の周壁
1C 中間部の周壁
2 マイクロ波照射機構
2a 照射口
3 フィルタ濾過機構
30 ケーシング
30a 開口部
31 フィルタ部
32 触媒
33 排気管
34 逆洗機構
4 導入部
5a 固体の導出部
5b ドレンの導出部
6 攪拌機構
60 回転軸
60a 回転支軸
61A 下段の回転羽根
61B 上段の回転羽根
61a 櫛歯
61b スクレーパ
61c 外周端スクレーパ
62 回転駆動用モータ
63 蓋付円筒体
7 熱電対
DESCRIPTION OF SYMBOLS 1 Case 1A Upper half peripheral wall 1B Lower half peripheral wall 1C Middle peripheral wall 2 Microwave irradiation mechanism 2a Irradiation port 3 Filter filtration mechanism 30 Casing 30a Opening part 31 Filter part 32 Catalyst 33 Exhaust pipe 34 Backwash mechanism 4 Introduction part 5a Solid lead-out part 5b Drain lead-out part 6 Stirring mechanism 60 Rotating shaft 60a Rotating support shaft 61A Lower rotating blade 61B Upper rotating blade 61a Comb tooth 61b Scraper 61c Outer end scraper 62 Rotation drive motor 63 Cylindrical cylinder with lid Body 7 Thermocouple

Claims (4)

有機ハロゲン化合物等の有害物質が付着・吸着した固体を導入する筐体と、該筐体内に導入した有害物質が付着・吸着した固体にマイクロ波を照射するマイクロ波照射機構と、筐体内に導入した有害物質が付着・吸着した固体を攪拌する回転羽根を有する攪拌機構とを備えた有機ハロゲン化合物等の有害物質の処理装置において、前記攪拌機構の回転羽根を上下方向に多段に配設したことを特徴とする有機ハロゲン化合物等の有害物質の処理装置。   A case that introduces solids with attached or adsorbed toxic substances such as organic halogen compounds, a microwave irradiation mechanism that irradiates the solids with attached or adsorbed toxic substances into the case, and a microwave irradiation mechanism. In a processing apparatus for harmful substances such as organic halogen compounds, equipped with a stirring mechanism having a rotating blade that stirs the solid adhering or adsorbing the harmful substance, the rotating blades of the stirring mechanism are arranged in multiple stages in the vertical direction. An apparatus for treating harmful substances such as organic halogen compounds. 上段に配設した回転羽根の回転外周径を、下段に配設した回転羽根の回転外周径より小さく設定したことを特徴とする請求項1記載の有機ハロゲン化合物等の有害物質の処理装置。   The apparatus for treating harmful substances such as organic halogen compounds according to claim 1, wherein the rotational outer peripheral diameter of the rotary blade disposed in the upper stage is set smaller than the rotational outer peripheral diameter of the rotary blade disposed in the lower stage. 回転羽根を板状部材で構成し、該板状部材を、板状部材の下端が回転羽根の回転方向の前方側に位置するように、回転軸に対して放射方向に延びる回転支軸に傾斜して取り付けるようにするとともに、下段に配設した回転羽根の傾斜方向の略延長線上に、上段に配設した回転羽根が位置するようにしたことを特徴とする請求項1又は2記載の有機ハロゲン化合物等の有害物質の処理装置。   The rotary blade is constituted by a plate-like member, and the plate-like member is inclined to a rotation support shaft that extends radially with respect to the rotation axis so that the lower end of the plate-like member is located on the front side in the rotation direction of the rotation blade. 3. The organic material according to claim 1, wherein the rotating blades disposed in the upper stage are positioned on a substantially extended line in the inclination direction of the rotating blades disposed in the lower stage. Equipment for treating harmful substances such as halogen compounds. 回転羽根を、上部に櫛歯を下部にスクレーパをそれぞれ形成した板状部材で構成し、かつ、櫛歯の間隙の寸法を照射するマイクロ波の波長の1/4の整数倍の近傍域を外して形成したことを特徴とする請求項1、2又は3記載の有機ハロゲン化合物等の有害物質の処理装置。   The rotating blade is composed of a plate-like member having a comb tooth at the upper part and a scraper at the lower part, and the area near the integral multiple of 1/4 of the wavelength of the microwave that irradiates the dimension of the gap of the comb tooth is removed. The processing apparatus for harmful substances such as organic halogen compounds according to claim 1, 2 or 3.
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Publication number Priority date Publication date Assignee Title
WO2013035435A1 (en) * 2011-09-09 2013-03-14 新東工業株式会社 Method for treating waste material in foundry, and system for treating toxic substance in molding sand

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CN106955591B (en) * 2017-04-27 2023-07-21 北京达盛环保工程有限公司 Catalytic plate and device for microwave catalytic cracking of dioxin by using same

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2013035435A1 (en) * 2011-09-09 2013-03-14 新東工業株式会社 Method for treating waste material in foundry, and system for treating toxic substance in molding sand
JP2013056358A (en) * 2011-09-09 2013-03-28 Sintokogio Ltd Method for treating waste material in foundry, and system for treating toxic substance in molding sand

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