JP2002147733A - Incineration method and apparatus for combustible waste - Google Patents

Incineration method and apparatus for combustible waste

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Publication number
JP2002147733A
JP2002147733A JP2000382913A JP2000382913A JP2002147733A JP 2002147733 A JP2002147733 A JP 2002147733A JP 2000382913 A JP2000382913 A JP 2000382913A JP 2000382913 A JP2000382913 A JP 2000382913A JP 2002147733 A JP2002147733 A JP 2002147733A
Authority
JP
Japan
Prior art keywords
emulsion fuel
combustible waste
incineration
waste
incinerator
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.)
Pending
Application number
JP2000382913A
Other languages
Japanese (ja)
Inventor
Katsumitsu Uehara
勝満 上原
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.)
Individual
Original Assignee
Individual
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Filing date
Publication date
Application filed by Individual filed Critical Individual
Priority to JP2000382913A priority Critical patent/JP2002147733A/en
Publication of JP2002147733A publication Critical patent/JP2002147733A/en
Pending legal-status Critical Current

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  • Feeding And Controlling Fuel (AREA)
  • Chimneys And Flues (AREA)
  • Incineration Of Waste (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide an incineration method and apparatus for waste wherein production of harmful matter such as dioxins is greatly and sharply suppressed without requiring conspicuous high temperature calcination and addition of a neutralizing material. SOLUTION: When combustible waste containing or producing harmful matter is converted to an emulsion fuel or an emulsion fuel is auxiliarily added and is incinerated, string electric field enough to ionize and disperse the emulsion fuel is added to the emulsion fuel, and the combustible waste is preheated with incineration heat of itself and completely combust while bringing waste smoke by incineration into contact with a heat storage structure and catalytic metal.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】この発明はPCBやダイオキ
シンなどの有害物を含有ないし生成する可燃性廃棄物
を、その有害物が無くなるように焼却する方法及び装置
に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method and an apparatus for incinerating combustible waste containing or producing harmful substances such as PCB and dioxin so as to eliminate the harmful substances.

【0002】[0002]

【従来の技術】いわゆる可燃性廃棄物のなかには、それ
自体にPCBなどの有害物を含むものもあれば、燃焼し
てダイオキシンなどの有害物を生成するものもある。こ
れらは一般に焼却処置を施すことによって無害化を図っ
ているが、そのためにはできるだけ完全燃焼化させるた
めに油性燃料をエマルジョン化するなどのさまざまな工
夫がなされている。しかしながら特に上記のような塩素
系の有害物に関しては、未だ技術的に困難な問題点を抱
えているのが現状である。
2. Description of the Related Art Some of the so-called combustible wastes themselves contain harmful substances such as PCBs, and others generate harmful substances such as dioxins by burning. These are generally made harmless by performing incineration treatments. For this purpose, various measures such as emulsifying an oily fuel to make combustion as complete as possible have been made. However, in particular, chlorine-based harmful substances as described above still have technically difficult problems at present.

【0003】PCBについてはこれを焼却することによ
ってダイオキシンを生成し、そのダイオキシンは甚だ高
温にしない限り分解・消失しない。従って比較的低温で
その生成を抑止する方法として、PCB混入オイルに水
と界面活性剤を加えてエマルジョン化するとともに水酸
化物を混合し、燃焼時にPCBに含まれる塩素と水酸化
物の塩基とを中和反応させる手段などが提案されてい
る。
[0003] PCBs produce dioxin by incineration, and the dioxins do not decompose or disappear unless the temperature is extremely high. Therefore, as a method of suppressing the formation at a relatively low temperature, water and a surfactant are added to the oil mixed with the PCB to emulsify the mixture, and the hydroxide is mixed with the oil. For example, means for neutralizing the acid have been proposed.

【0004】[0004]

【発明が解決しようとする課題】上記のような方法もP
CBオイルという限定された廃棄物以外には適用させる
ことができず、また二次的に塩化物から成る焼却灰を生
じる問題点もある。本発明はかかる現状から、PCBや
塩化ビニールなどをはじめとする広範な可燃性廃棄物
を、比較的低温で有害物の生成を著しく抑止するように
焼却する手段を提供することを課題とする。
The above-mentioned method is also a P method.
It cannot be applied to other than the limited waste of CB oil, and there is also a problem that secondary incineration ash composed of chloride is generated. In view of the above, an object of the present invention is to provide a means for incinerating a wide range of combustible waste such as PCB and vinyl chloride at a relatively low temperature so as to significantly suppress the generation of harmful substances.

【0005】[0005]

【課題を解決するための手段】有害物を含有ないし生成
する可燃性廃棄物をエマルジョン燃料化するか或いはエ
マルジョン燃料を補助的に加えてこれを焼却する際に、
そのエマルジョン燃料にこれをイオン化させ分散化させ
るに足る強電界を与えるとともに、該可燃性廃棄物を自
らの焼却熱により予熱し、焼却による排気煙を蓄熱体及
び触媒金属に触れるようにしつつ完全燃焼させるように
する。
SUMMARY OF THE INVENTION When flammable waste containing or producing harmful substances is converted into an emulsion fuel or incinerated with an auxiliary emulsion fuel,
A strong electric field sufficient to ionize and disperse the emulsion fuel is given, and the combustible waste is preheated by its own incineration heat, and the exhaust smoke from the incineration is completely burned while touching the heat storage material and the catalytic metal. Let it do.

【0006】ここでいう可燃性廃棄物は、廃油、汚泥、
硫酸ピッチ、或いはPCBオイル等のような液状物と、
塩ビその他固体の粉砕物とに大別されるが、水や界面活
性剤を加えてエマルジョン化するのは前者である。但し
この場合も後者と同様に、重油や灯油などの化石燃料を
水と界面活性剤でエマルジョン燃料にしたものを補助的
に用いてもよいことは勿論である。いずれにしても本発
明においては、エマルジョン燃料に相当するものがその
燃焼・焼却において関与する。
[0006] The flammable waste mentioned here includes waste oil, sludge,
Liquids such as sulfuric acid pitch or PCB oil,
The former is roughly divided into PVC and other solid pulverized products, and the former is the case of emulsifying by adding water or a surfactant. However, in this case, as in the latter case, a fossil fuel such as heavy oil or kerosene converted into an emulsion fuel with water and a surfactant may be used as a supplement. In any case, in the present invention, the one corresponding to the emulsion fuel is involved in the combustion and incineration.

【0007】可燃性廃棄物を自らの焼却熱で予め加熱す
る度合いは、液状物にあってはそれを乾燥(水分)或い
は気化させる程度であり、粉砕物でもこれに匹敵する程
度が望ましい。
The degree to which the combustible waste is preheated by its own incineration heat is such that the liquid is dried (moisture) or vaporized, and the pulverized waste is desirably comparable.

【0008】これを具現する装置を図面とともに説明す
れば以下の通りである。すなわち可燃性廃棄物をエマル
ジョン化したエマルジョン燃料或いは補助的に加えるエ
マルジョン燃料の供給部6(バーナー等)に設置してこ
れに高電圧を付加する電極5Aと加熱体5Bを備えたエ
マルジョンの改質装置5と、該可燃性廃棄物を通過・放
出させる筒状体2を内に収めて、筒状体2の周りに充分
な焼却熱が予め当たるようにした焼却炉1と、、焼却炉
1に連通する消煙炉3においてその内部に触媒金属を有
する蓄熱体4を設置した消煙炉3とを、一連の焼却装置
(設備)における主要部として含ませるようにするもの
である。
The following is a description of an apparatus embodying this, with reference to the drawings. That is, the reforming of an emulsion provided with an electrode 5A for applying a high voltage to a supply unit 6 (a burner or the like) of an emulsion fuel in which combustible waste is emulsified or an emulsion fuel to be supplementarily added thereto and a heating element 5B is provided. An incinerator 1 in which a device 5 and a tubular body 2 for passing and discharging the combustible waste are housed so that sufficient incineration heat is applied beforehand around the tubular body 2; And a smoke removing furnace 3 in which a heat storage unit 4 having a catalytic metal is installed in the inside of the smoke removing furnace 3 communicating with the incinerator 3 is included as a main part in a series of incinerators (equipment).

【0009】ここにおける焼却炉1の内壁炉材には、炉
の耐久性を向上させるための酸化防止材をコーティング
施工しておくことが望ましい。
It is desirable that the inner wall furnace material of the incinerator 1 is coated with an antioxidant to improve the durability of the furnace.

【0010】液状(油性)の廃棄物をエマルジョン燃料
化する手段は、水と界面活性剤を加えてミキシングする
などの公知の方法によればよい。また補助燃料としての
化石燃料を材料とするエマルジョン燃料についても同様
である。
The means for converting the liquid (oily) waste into an emulsion fuel may be a known method such as mixing by adding water and a surfactant. The same applies to an emulsion fuel using a fossil fuel as an auxiliary fuel.

【0011】消煙炉3の内部に設置する築熱体4は、略
円柱形でその周囲にらせん段を設けたような形状が、炉
内に旋回流を起こして対流速度を遅延させるためにも望
ましい。またその材質はセラミック蓄熱材にチタン、バ
ナジウム、タングステン等の触媒金属を混合させたもの
でよい。
The heat-generating body 4 installed inside the smoke-removing furnace 3 has a substantially cylindrical shape with a spiral step provided therearound. Is also desirable. The material may be a mixture of a ceramic heat storage material and a catalytic metal such as titanium, vanadium, and tungsten.

【0012】なお消煙炉3の先に、排気温度を基準値以
下にするための冷却装置7(冷却式サイクロン)や、そ
こから出る排気ガスを吸引する集塵装置8などが一般的
に設けられるが、これらは公知手段でも賄うことができ
る。
In general, a cooling device 7 (cooling type cyclone) for lowering the exhaust gas temperature to a reference value or less and a dust collecting device 8 for sucking the exhaust gas flowing therefrom are provided in front of the smoke removing furnace 3. However, these can be covered by known means.

【0013】本発明に使用されるエマルジョン燃料に対
する改質装置5の電極5Aは、後述のような三極電極に
してこれを高周波発振器5Cに繋ぎ、加熱体5Bは、そ
の先のエマルジョン燃料の通路において(触媒付)蓄熱
チャンバー5B1やインダクション加熱ゾーン5B2等
のような形態で実施することが望ましい。
The electrode 5A of the reformer 5 for the emulsion fuel used in the present invention is a three-electrode as described later, which is connected to a high-frequency oscillator 5C. In this case, it is desirable to carry out in the form of a heat storage chamber (with a catalyst) 5B1, an induction heating zone 5B2, or the like.

【0014】[0014]

【作用】本発明において燃焼・焼却に関与するエマルジ
ョン燃料は、改質装置5の電極5Aより強力な電荷を与
えられてコロナ放電又はこれに近い状態を得ることによ
り、分子レベルで陰イオン化されたものとなるため、ノ
ズルより放出して燃焼する際に、その気体分子は互いの
反発力により甚だ良好な均一分散性を発揮し、また加熱
体5Bにより予熱しておくと、その安定性が著しく向上
する。
In the present invention, the emulsion fuel involved in combustion and incineration is anionized at the molecular level by being given a stronger electric charge than the electrode 5A of the reformer 5 to obtain a corona discharge or a state close to the corona discharge. Therefore, when the gas molecules are discharged from the nozzle and burned, the gas molecules exhibit extremely good uniform dispersibility due to the repulsive force of each other, and if the gas molecules are preheated by the heating element 5B, the stability is remarkably increased. improves.

【0015】更に前述のように、焼却炉1に入る前にも
廃棄物が自らの焼却熱で予熱されて充分に乾燥ないし気
化状態になっているから、それらの相乗効果によって炉
内にはきわめて分散性の良い理想的な燃焼環境が現出す
る。
Further, as described above, even before entering the incinerator 1, the waste is preheated by its own incineration heat and is sufficiently dried or vaporized. An ideal combustion environment with good dispersibility appears.

【0016】これに加え、消煙炉3においても、蓄熱体
4によって炉内の温度を蓄熱し、また触媒作用も加わる
ことによって燃焼効率が著しく高められており、これら
の組合せによって、特に高温の燃焼環境にすることなく
甚だ高度の有害物抑止効果が実現し、従来は不可能であ
ったようなダイオキシンの生成防止も可能となった。
In addition, also in the smoke elimination furnace 3, the temperature inside the furnace is stored by the regenerator 4, and the combustion efficiency is remarkably increased by adding a catalytic action. A very high degree of harmful substance deterrent effect was realized without using a combustion environment, and it was possible to prevent the generation of dioxin, which was impossible in the past.

【0017】実際に本発明のテストプラントで実施した
排気ガス中の有害物を日立分析センター(茨城県日立
市)で分析したところ(報告書受付No.D9812
9)、ダイオキシン類についてはO=12%換算値に
おいて0.016ng−TEQ/mN以下であり、こ
れは大気汚染防止法改正令で定める猶予基準値の500
0分の1以下に相当する。またダストは同じく0.06
g/mN、窒素酸化物は56ppm、硫黄酸化物は5
ppm以下、塩化水素は0.9mg/mN、一酸化炭
素は10ppmであり、いずれも基準値を大幅に下回る
ものであった。
Analysis of harmful substances in the exhaust gas actually performed by the test plant of the present invention at Hitachi Analysis Center (Hitachi City, Ibaraki Prefecture) (Report No. D9812)
9) For dioxins, it is 0.016 ng-TEQ / m 3 N or less when converted to O 2 = 12%, which is 500 of the grace standard value specified by the Ordinance for Revision of the Air Pollution Control Law.
This corresponds to 1/0 or less. The dust is also 0.06
g / m 3 N, nitrogen oxides 56 ppm, sulfur oxides 5
ppm or less, hydrogen chloride was 0.9 mg / m 3 N, and carbon monoxide was 10 ppm, all of which were significantly below the reference values.

【0018】[0018]

【発明の実施の形態】PCBオイル等の液状可燃性廃棄
物と補助燃料の重油等をエマルジョン燃料化するため
に、それぞれに公知のエマルジョン生成装置9とその改
質装置5を設置し、特に補助燃料のものについては図3
のような形態のものにする。すなわち、エマルジョン生
成装置9から出たエマルジョン燃料は二連ポンプユニッ
ト10により変換装置11内に導かれ、そこには高周波
発振器5Cから高圧同軸ケーブル12を経た三極の電極
5Aがセットされる。さらにそれは流量調節弁13を経
て触媒付の蓄熱チャンバー5B1及びインダクション加
熱ゾーン5B2に導かれ、放電電極付のノズル14より
焼却炉1内に噴射される。
DESCRIPTION OF THE PREFERRED EMBODIMENTS In order to make liquid combustible waste such as PCB oil and auxiliary fuel heavy oil etc. into an emulsion fuel, a well-known emulsion generating device 9 and a reforming device 5 are installed in each of them. Fig. 3 for fuel
The form is as follows. That is, the emulsion fuel discharged from the emulsion generator 9 is guided into the converter 11 by the dual pump unit 10, where the triode electrode 5A is set via the high-frequency coaxial cable 12 from the high-frequency oscillator 5C. Further, it is guided to a heat storage chamber 5B1 with a catalyst and an induction heating zone 5B2 via a flow control valve 13, and is injected into the incinerator 1 from a nozzle 14 with a discharge electrode.

【0019】焼却炉1の内部に該可燃性廃棄物を通過・
放出させる筒状体2は図1のような形態にして炉内に下
方に向けて放出するようにし、焼却炉1は下方の一次焼
却炉の他に上方に二次焼却炉1Aを設けてそれが該筒状
体2を取り囲むようにする。なおこの図は粉砕可燃物の
場合であって、適宜の搬送装置15等が設けられる。
The combustible waste passes through the inside of the incinerator 1
The tubular body 2 to be discharged is configured as shown in FIG. 1 so as to be discharged downward into the furnace, and the incinerator 1 is provided with a secondary incinerator 1A above and a primary incinerator below. Surrounds the cylindrical body 2. This figure shows the case of crushed combustibles, and an appropriate transport device 15 and the like are provided.

【0020】その先の消煙炉等は図2のようであって、
消煙炉3の内部には前記のような触媒金属が混合するセ
ラミック製のスパイラル段付き蓄熱体4が設置される。
これに連通してサイクロン式の冷却装置7が設置される
が、これには給水管16を介して水が噴射状に供給さ
れ、その水分は下方に設けられたエマルジョン生成装置
9に供給されて、得られたエマルジョン燃料は消煙炉3
内に噴射される。従ってここにおいても前記の改質装置
5(図示せず)を取り付けるものとする。
FIG. 2 shows a smoke-removing furnace and the like ahead of the furnace.
Inside the smoke removing furnace 3 is provided a ceramic spiral stepped regenerator 4 in which the above-mentioned catalyst metal is mixed.
A cyclone-type cooling device 7 is installed in communication therewith. Water is supplied in a jet form through a water supply pipe 16 and the water is supplied to an emulsion generating device 9 provided below. , The obtained emulsion fuel is used in the smoke
Injected into. Therefore, the reforming apparatus 5 (not shown) is also attached here.

【0021】なおその先に公知の集塵装置8や煙突17
等を設置し、或いは必要に応じ排熱を利用した発電或い
は温水供給装置を付設して、極力自己完結型のものとす
る。
A known dust collector 8 and a chimney 17
Etc., or a power generation or hot water supply device using waste heat as needed to make it as self-contained as possible.

【0022】[0022]

【発明の効果】このように本発明によれば、甚だ困難な
問題点を抱えた高温焼成によることなく、ダイオキシン
等の有害物質の生成を著しく抑止して廃棄物の焼却処理
を行なうことができ、しかもその適用は広範にわたり、
余分な塩化物等の二次焼却灰も生じないなどの多大な効
果がある。
As described above, according to the present invention, the incineration of waste can be carried out by significantly suppressing the generation of harmful substances such as dioxins without using high-temperature sintering, which has extremely difficult problems. And its application is extensive,
There is a great effect that secondary incineration ash such as excess chloride does not occur.

【図面の簡単な説明】[Brief description of the drawings]

【図1】本発明の装置の前半部の例を示す側断面図FIG. 1 is a side sectional view showing an example of the first half of the device of the present invention.

【図2】本発明の装置の後半部の例を示す側面図FIG. 2 is a side view showing an example of the rear half of the device of the present invention.

【図3】エマルジョン燃料改質装置の例を示す概念的側
面図
FIG. 3 is a conceptual side view showing an example of an emulsion fuel reforming apparatus.

【符号の説明】[Explanation of symbols]

1……焼却炉 1A……二次焼却炉 2……
筒状体 3……消煙炉 4……蓄熱体 5……改質装
置 5A……電極 5B……加熱体 5B1……
蓄熱チャンバー 5B2……インダクション加熱ゾーン 5C……
高周波発振器 6……エマルジョン燃料の供給部 7……冷却装
置 8……集塵装置 9……エマルジョン生成装置 10……二連ポンプユニット 11……変換装
置 12……高圧同軸ケーブル 13……流量調節
弁 14……ノズル 15……搬送装置 16
……給水管 17……煙突
1 ... incinerator 1A ... secondary incinerator 2 ...
Cylindrical body 3 ... Smoke removal furnace 4 ... Regenerator 5 ... Reformer 5A ... Electrode 5B ... Heating body 5B1 ...
Thermal storage chamber 5B2… Induction heating zone 5C ……
High-frequency oscillator 6 Emulsion fuel supply unit 7 Cooling device 8 Dust collector 9 Emulsion generator 10 Dual pump unit 11 Converter 12 High-pressure coaxial cable 13 Flow rate control Valve 14 ... Nozzle 15 ... Transfer device 16
...... Water supply pipe 17 ... Chimney

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) // C10G 32/02 F23J 15/00 H ──────────────────────────────────────────────────続 き Continued on the front page (51) Int.Cl. 7 Identification symbol FI theme coat ゛ (reference) // C10G 32/02 F23J 15/00 H

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】可燃性廃棄物をエマルジョン燃料化するか
或いはエマルジョン燃料を補助的に加えてこれを焼却す
る際に、そのエマルジョン燃料にこれをイオン化させ分
散化させるに足る強電界を与えるとともに、該可燃性廃
棄物を自らの焼却熱により予熱し、焼却による排気煙を
蓄熱体及び触媒金属に触れるようにしつつ完全燃焼させ
ることを特徴とする可燃性廃棄物の焼却方法。
When the combustible waste is converted into an emulsion fuel or incinerated by supplementing the emulsion fuel, a strong electric field sufficient to ionize and disperse the emulsion fuel is provided, A method for incinerating combustible waste, characterized in that the combustible waste is preheated by its own incineration heat, and exhaust smoke from the incineration is completely burned while being brought into contact with a heat storage body and a catalytic metal.
【請求項2】可燃性廃棄物をエマルジョン化したエマル
ジョン燃料或いは補助的に加えるエマルジョン燃料に高
電圧を付加する電極と加熱体を備えたエマルジョン改質
装置と、該可燃性廃棄物を通過・放出させる筒状体を内
に収めてその筒状体の周りに充分な焼却熱が予め当たる
ようにした焼却炉と、これに連通する消煙炉においてそ
の内部に触媒金属を有する蓄熱体を設置した消煙炉と
を、主要部として含むことを特徴とする可燃性廃棄物の
焼却装置。
2. An emulsion reforming apparatus having an electrode and a heating element for applying a high voltage to an emulsion fuel obtained by emulsifying combustible waste or an emulsion fuel to be supplementarily added thereto, and passing and discharging the combustible waste. An incinerator in which sufficient heat of incineration was previously applied around the cylindrical body, and a heat storage unit having a catalytic metal therein was installed in a smoke eliminating furnace communicating with the incinerator. An incinerator for combustible waste, characterized by including a smoke-removing furnace as a main part.
JP2000382913A 2000-11-13 2000-11-13 Incineration method and apparatus for combustible waste Pending JP2002147733A (en)

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Country Link
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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005028303A (en) * 2003-07-07 2005-02-03 Dowa Mining Co Ltd Sulfate pitch treatment method
WO2008029898A1 (en) * 2006-09-01 2008-03-13 Nanomizer Inc. Method for production of emulsion fuel and apparatus for production of the fuel
JP2008081740A (en) * 2006-09-01 2008-04-10 Sg Engineering Kk Method for producing emulsion fuel by mixing water and combustible oil in fine particle state, device for producing emulsion fuel and emulsion fuel
WO2023065391A1 (en) * 2021-10-22 2023-04-27 歙县绿源环保设备有限公司 Small garbage incinerator additionally provided with bypass garbage preheating channel

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005028303A (en) * 2003-07-07 2005-02-03 Dowa Mining Co Ltd Sulfate pitch treatment method
JP4555982B2 (en) * 2003-07-07 2010-10-06 Dowaエコシステム株式会社 Treatment method of sulfuric acid pitch
WO2008029898A1 (en) * 2006-09-01 2008-03-13 Nanomizer Inc. Method for production of emulsion fuel and apparatus for production of the fuel
JP2008081740A (en) * 2006-09-01 2008-04-10 Sg Engineering Kk Method for producing emulsion fuel by mixing water and combustible oil in fine particle state, device for producing emulsion fuel and emulsion fuel
WO2023065391A1 (en) * 2021-10-22 2023-04-27 歙县绿源环保设备有限公司 Small garbage incinerator additionally provided with bypass garbage preheating channel

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