JP3725485B2 - How to remove dioxins - Google Patents

How to remove dioxins Download PDF

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Publication number
JP3725485B2
JP3725485B2 JP2002055446A JP2002055446A JP3725485B2 JP 3725485 B2 JP3725485 B2 JP 3725485B2 JP 2002055446 A JP2002055446 A JP 2002055446A JP 2002055446 A JP2002055446 A JP 2002055446A JP 3725485 B2 JP3725485 B2 JP 3725485B2
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JP
Japan
Prior art keywords
dioxins
fly ash
ultraviolet rays
microwaves
reaction accelerator
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.)
Expired - Fee Related
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JP2002055446A
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Japanese (ja)
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JP2003251302A (en
Inventor
澄生 辻井
良夫 飯尾
敬昌 木嶋
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Nihon Spindle Manufacturing Co Ltd
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Nihon Spindle Manufacturing Co Ltd
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Filing date
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Priority to JP2002055446A priority Critical patent/JP3725485B2/en
Publication of JP2003251302A publication Critical patent/JP2003251302A/en
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  • Processing Of Solid Wastes (AREA)
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Description

【0001】
【発明の属する技術分野】
本発明は、ダイオキシン類の除去方法に関し、特に気体による搬送中の飛灰からダイオキシン類を除去する方法に関する。
【0002】
【従来の技術】
従来、焼却設備等から排出される含塵空気は流入口11を介して集塵機(図例ではバク式集塵機10)の含塵空気室3に導入され、多数のバグフィルタ14により濾過され、浄化空気室15を経て排出口12より外部へ排出される。
【0003】
この際、含塵空気に含まれる飛灰はダイオキシン類を含む有害物質であり、バグフィルタ14により浄化空気室15への流入は阻止され、バクフィルタ14に付着する。
【0004】
バクフィルタ14に付着した有害物質を含む飛灰は、浄化空気室15側に設けた空気噴出手段(図示省略)等によりバグフィルタ14にパルスを与えることにより含塵空気室13の下部に落とされる。
【0005】
含塵空気室13の下部に落とされた飛灰はロータリーバルブ16を介し中継ホッパー17に一旦貯留され、開放弁18を介しトランスポータ19に移される。
【0006】
その後、周知の空気搬送方法によって灰バンカ21に搬送され、溶融により処理するか若しくは、無酸素下で加熱分解を行う等して灰バンカに貯まった飛灰を処理していた。
【0007】
【発明が解決しようとする課題】
しかし、この従来の方法の場合、溶融により処理するときは大量のエネルギーを消費し、ランニングコストが割高となる問題があり、また無酸素下で加熱分解を行い処理するときは設備の規模が大きくなり装置そのものが高価となりイニシャルコストが割高となる等の欠点がある。
本発明はかかる点に鑑み、イニシャル・ランニング両コストを低減し、簡便な設備でダイオキシン類を除去できる方法を提供することを目的とする。
【0008】
【課題を解決するための手段】
上記目的を達成するため、本発明のダイオキシン類の除去方法は、配管内を気体により輸送せしめる飛灰の輸送に際し、輸送配管適所でマイクロ波又は紫外線を照射しダイオキシン類を分解除去するダイオキシン類の除去方法において、輸送配管を、反応促進剤の通過を許容するとともに、紫外線又はマイクロウェーブが飛灰に十分照射される多孔配管で構成するようにしたことを特徴とする。
【0009】
上記の構成からなる本発明は、ダイオキシン類を含む飛灰を空気輸送する際にダイオキシン類の除去をすることができる。
【0010】
この場合において、反応促進剤は、オゾン又は過酸化水素とすることができる。
【0011】
反応促進剤として、オゾンや過酸化水素を使うときは、共に強力な酸化剤であり、また分解後は酸素や水になるので二次廃棄物が発生することなくダイオキシン類の分解除去効率を確実に高めることができる。
【0012】
【発明の実施の形態】
以下、本発明のダイオキシン類の除去方法の実施の形態を図面に基づいて説明する。
【0013】
図1は、本発明によるダイオキシン類の除去方法を説明する全体図を示す。
従来例と同様の構成については同様の符号を付し説明を省略する。
【0014】
ダイオキシン類を含む飛灰は、トランスポータ19に蓄えられ従来と同様に周知の空気搬送方法によって輸送配管20内を通り灰バンカ21に送られる。
【0015】
この際、輸送配管20の適所に紫外線又はマイクロウェーブ又はその両方を選択的に照射することができる照射装置1を設置する。
図例では1台の設置の例を示すが2台若しくはそれ以上設置してもよい。
【0016】
照射装置1は、輸送配管20を覆う用に設置し、適所に紫外線又はマイクロウェーブ又はその両方を選択的に照射する照射機構2を備え、内面を紫外線やマイクロウェーブが反射する反射板3とした円柱又は立方体の形状とする。
【0017】
5は、照射装置1に設けた反応促進物質供給管を示す。反応促進剤Hは、オゾン又は過酸化水素の他、アルカリ物質から水酸基(OH−)が分離し、脱塩素化つまり還元反応を促進せしめるような物質であればよい。
なお、反応促進物質供給管5は図3に示す参考例の如く照射装置1に設けることなく照射装置1の上流側の輸送配管20に設けてもよい。
【0018】
照射装置1内の輸送配管20は図2に示す如く多孔配管4とし反応促進剤Hの通過を許容するとともに、紫外線やマイクロウェーブが飛灰に十分照射されるように構成する。
【0019】
また、照射装置1内の輸送配管20は図3に示す参考例の如くガラス配管7とし更に照射装置1内部を蛇行して配設せしめて紫外線やマイクロウェーブの照射時間を十分に確保する様に構成することもできる。
この際、上述した多孔配管4を蛇行して配設することもできる。
【0020】
照射機構2は、図3に示す如く照射装置1の外部に1台以上設置するようにしてもよい。
【0021】
上記構成において、トランスポータ19より輸送配管20を通って送られてくる飛灰中の有害ダストDは照射装置1に至ると反応促進剤Hが混ざるとともに、照射機構2から照射されるマイクロウェーブにより無害ダストCとなる。
これは、マイクロウェーブを例に取るとマイクロウェーブの物体表面を局所的に高温加熱する作用によってダイオキシン類が分解されることによる。
【0022】
ダイオキシン類は飛灰表面に付着しているものであり、飛灰中心部は常温であっても表面を高温加熱することによりダイオキシン類は十分に分解される。
【0023】
照射機構2から紫外線を照射する場合は、反応促進剤Hとして、酸化剤を供給する。
酸化剤としては、OH(OHラジカル)、O(オゾン)、H(過酸化水素)、HClO等が挙げられ、紫外線は触媒の働きをする。
【0024】
酸化剤に紫外線が照射されることによりOHラジカルなどの活性酸素を発生させることができる。
【0025】
この、活性酸素によって有機物であるダイオキシン類を分解除去するもので、一般に水によるDXN分解処理法として利用されている促進酸化法と同様の効果によるものである。
【0026】
以上、本発明のダイオキシン類の除去方法について、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。
【0027】
【発明の効果】
以上の如く本発明のダイオキシン類の除去方法によるときは、輸送配管適所でマイクロ波又は紫外線を照射しダイオキシン類を除去するようにしたから、その方法は簡便でありイニシャル・ランニング両コストを従来に比して大幅に低減することができる。
また、既設の設備においてもわずかな改造を工事を施すことによって、本発明のダイオキシン類の除去方法を適用することができる。
【図面の簡単な説明】
【図1】 本発明によるダイオキシン類の除去方法を説明する全体図を示す。
【図2】 照射装置の一部断面図を示す。
【図3】 照射装置の参考例の一部断面図を示す。
【図4】 従来例の説明図を示す。
【符号の説明】
20 輸送配管
H 反応促進剤
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a method for removing dioxins, and more particularly, to a method for removing dioxins from fly ash being transported by gas.
[0002]
[Prior art]
Conventionally, dust-containing air discharged from an incineration facility or the like is introduced into a dust-containing air chamber 3 of a dust collector (back-type dust collector 10 in the illustrated example) through an inflow port 11, filtered by a number of bag filters 14, and purified air. It is discharged to the outside through the discharge port 12 through the chamber 15.
[0003]
At this time, fly ash contained in the dust-containing air is a harmful substance including dioxins, and the bag filter 14 prevents the inflow into the purified air chamber 15 and adheres to the back filter 14.
[0004]
Fly ash containing harmful substances adhering to the back filter 14 is dropped to the lower part of the dust-containing air chamber 13 by applying a pulse to the bag filter 14 by air blowing means (not shown) provided on the purified air chamber 15 side. .
[0005]
Fly ash dropped in the lower part of the dust-containing air chamber 13 is temporarily stored in the relay hopper 17 through the rotary valve 16 and transferred to the transporter 19 through the release valve 18.
[0006]
Thereafter, the fly ash stored in the ash bunker was processed by being transported to the ash bunker 21 by a well-known air transport method and processed by melting or by thermal decomposition in the absence of oxygen.
[0007]
[Problems to be solved by the invention]
However, in the case of this conventional method, there is a problem that a large amount of energy is consumed when processing by melting, and the running cost is high, and the scale of equipment is large when performing the thermal decomposition in the absence of oxygen. There is a disadvantage that the device itself is expensive and the initial cost is high.
In view of the above, an object of the present invention is to provide a method capable of reducing both initial and running costs and removing dioxins with simple equipment.
[0008]
[Means for Solving the Problems]
To achieve the above object, the method for removing dioxins of the present invention, upon transport of fly ash in the pipe allowed to transport the gas in the transportation pipeline place microwave irradiation or ultraviolet dioxins decomposing and removing dioxins The removing method is characterized in that the transport pipe is constituted by a porous pipe that allows passage of the reaction accelerator and is sufficiently irradiated with ultraviolet rays or microwaves on the fly ash .
[0009]
The present invention having the above-described configuration can remove dioxins when pneumatically transporting fly ash containing dioxins.
[0010]
In this case, the reaction accelerator can be ozone or hydrogen peroxide.
[0011]
When ozone or hydrogen peroxide is used as a reaction accelerator, they are both strong oxidizers, and after decomposition they become oxygen and water, ensuring the efficiency of dioxin decomposition and removal without generating secondary waste. Can be increased.
[0012]
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, embodiments of a dioxin removal method of the present invention will be described with reference to the drawings.
[0013]
FIG. 1 is an overall view illustrating a method for removing dioxins according to the present invention.
Constituent elements similar to those of the conventional example are denoted by the same reference numerals and description thereof is omitted.
[0014]
The fly ash containing dioxins is stored in the transporter 19 and sent to the ash bunker 21 through the transport pipe 20 by a well-known air transport method in the same manner as before.
[0015]
At this time, the irradiation device 1 capable of selectively irradiating ultraviolet rays and / or microwaves at appropriate positions of the transport pipe 20 is installed.
Although the example of installation shows the example of installation of 1 unit | set, you may install 2 units | sets or more.
[0016]
The irradiation device 1 is installed to cover the transportation pipe 20 and includes an irradiation mechanism 2 that selectively irradiates ultraviolet rays and / or microwaves at appropriate positions, and the inner surface is a reflector 3 that reflects ultraviolet rays and / or microwaves. The shape is a cylinder or a cube.
[0017]
Reference numeral 5 denotes a reaction promoting substance supply pipe provided in the irradiation apparatus 1. The reaction accelerator H may be any substance that promotes dechlorination, that is, a reduction reaction, by separating hydroxyl groups (OH-) from alkaline substances in addition to ozone or hydrogen peroxide.
The reaction promoting substance supply pipe 5 may be provided in the transport pipe 20 on the upstream side of the irradiation apparatus 1 without being provided in the irradiation apparatus 1 as in the reference example shown in FIG.
[0018]
As shown in FIG. 2, the transport pipe 20 in the irradiation apparatus 1 is a perforated pipe 4 that allows the reaction accelerator H to pass therethrough and is configured to sufficiently irradiate the fly ash with ultraviolet rays and microwaves.
[0019]
Further, as in the reference example shown in FIG. 3, the transport pipe 20 in the irradiation apparatus 1 is a glass pipe 7, and the irradiation apparatus 1 is meandered to ensure sufficient irradiation time of ultraviolet rays and microwaves. It can also be configured.
At this time, the above-described porous pipe 4 can be meandered.
[0020]
One or more irradiation mechanisms 2 may be installed outside the irradiation apparatus 1 as shown in FIG.
[0021]
In the above configuration, the harmful dust D in the fly ash sent from the transporter 19 through the transport pipe 20 is mixed with the reaction accelerator H when reaching the irradiation device 1, and by the microwave irradiated from the irradiation mechanism 2. It becomes harmless dust C.
This is due to the fact that dioxins are decomposed by the action of locally heating the surface of the microwave object at a high temperature, for example.
[0022]
Dioxins adhere to the fly ash surface, and even if the fly ash center is at room temperature, the dioxins are sufficiently decomposed by heating the surface at a high temperature.
[0023]
When irradiating ultraviolet rays from the irradiation mechanism 2, an oxidizing agent is supplied as the reaction accelerator H.
Examples of the oxidizing agent include OH (OH radical), O 3 (ozone), H 2 O 2 (hydrogen peroxide), HClO, and the like, and ultraviolet rays act as a catalyst.
[0024]
Active oxygen such as OH radicals can be generated by irradiating the oxidizing agent with ultraviolet rays.
[0025]
This is a method for decomposing and removing organic dioxins with active oxygen, and has the same effect as the accelerated oxidation method generally used as a DXN decomposition treatment method with water.
[0026]
As mentioned above, although the removal method of the dioxins of this invention was demonstrated based on the Example, this invention is not limited to the structure described in the said Example, The structure suitably in the range which does not deviate from the meaning. Can be changed.
[0027]
【The invention's effect】
As described above, when the dioxins removal method of the present invention is used, the dioxins are removed by irradiating microwaves or ultraviolet rays at an appropriate place in the transportation piping. Therefore, the method is simple, and both initial and running costs are conventionally required. As compared with this, it can be greatly reduced.
In addition, the dioxins removal method of the present invention can be applied by applying a slight modification to existing facilities.
[Brief description of the drawings]
FIG. 1 is an overall view illustrating a method for removing dioxins according to the present invention.
FIG. 2 is a partial cross-sectional view of an irradiation apparatus.
FIG. 3 is a partial cross-sectional view of a reference example of an irradiation apparatus.
FIG. 4 is an explanatory diagram of a conventional example.
[Explanation of symbols]
20 Transport piping H Reaction accelerator

Claims (2)

配管内を気体により輸送せしめる飛灰の輸送に際し、輸送配管適所でマイクロ波又は紫外線を照射しダイオキシン類を分解除去するダイオキシン類の除去方法において、輸送配管を、反応促進剤の通過を許容するとともに、紫外線又はマイクロウェーブが飛灰に十分照射される多孔配管で構成するようにしたことを特徴とするダイオキシン類の除去方法。In the method of removing dioxins by decomposing and removing dioxins by irradiating microwaves or ultraviolet rays at appropriate places in the transportation piping when transporting fly ash that is transported by gas in the piping, the transportation piping is allowed to pass through the reaction accelerator. A method for removing dioxins, characterized by comprising a porous pipe that sufficiently irradiates fly ash with ultraviolet rays or microwaves . 反応促進剤は、オゾン又は過酸化水素としたことを特徴とする請求項1記載のダイオキシン類の除去方法。2. The method for removing dioxins according to claim 1 , wherein the reaction accelerator is ozone or hydrogen peroxide.
JP2002055446A 2002-03-01 2002-03-01 How to remove dioxins Expired - Fee Related JP3725485B2 (en)

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JP3725485B2 true JP3725485B2 (en) 2005-12-14

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Publication number Priority date Publication date Assignee Title
WO2009110071A1 (en) * 2008-03-05 2009-09-11 日本スピンドル製造株式会社 Treating apparatus for solid containing hazardous substance such as organohalogen compound
CN114602952B (en) * 2020-12-09 2024-01-19 陕西青朗万城环保科技有限公司 Harmless treatment method and control system for fly ash

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