JP2001059607A - Method and system for heating matter to be treated - Google Patents

Method and system for heating matter to be treated

Info

Publication number
JP2001059607A
JP2001059607A JP11234952A JP23495299A JP2001059607A JP 2001059607 A JP2001059607 A JP 2001059607A JP 11234952 A JP11234952 A JP 11234952A JP 23495299 A JP23495299 A JP 23495299A JP 2001059607 A JP2001059607 A JP 2001059607A
Authority
JP
Japan
Prior art keywords
furnace
pressure
heat treatment
gas
decomposition gas
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
JP11234952A
Other languages
Japanese (ja)
Inventor
Yoshiyuki Kashiwagi
佳行 柏木
Nobuyuki Yoshioka
信行 吉岡
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.)
Meidensha Corp
Meidensha Electric Manufacturing Co Ltd
Original Assignee
Meidensha Corp
Meidensha Electric Manufacturing Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Meidensha Corp, Meidensha Electric Manufacturing Co Ltd filed Critical Meidensha Corp
Priority to JP11234952A priority Critical patent/JP2001059607A/en
Publication of JP2001059607A publication Critical patent/JP2001059607A/en
Pending legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To keep a positive pressure in a decomposition gas combustion furnace by making the pressure in a heating furnace negative with respect to the atmospheric pressure and keeping the pressure in a decomposition gas combustion furnace positive with respect to the atmospheric pressure thereby preventing leakage of decomposition gas from the heating furnace. SOLUTION: Pressure in a rotary heating furnace has a trend to become negative with respect to atmospheric pressure because the heating furnace is normally sucked by means of a blower 39 having a bug filter 38 but it has a trend to become positive upon generation of decomposition gas through heating operation. Decomposition gas in the rotary heating furnace is sucked by means of the blower 53 in a decomposition gas introducing means 50 and the pressure in the rotary heating furnace can be made negative with respect to the atmospheric pressure. The negative pressure can be regulated easily by controlling rotation of blower preferably in the range of -5 to -10 mmH2O. Pressure in a decomposition gas combustion furnace 34 is preferably kept positive (0 to +10 mmH2O) in view point of combustion conditions by introducing air and decomposition gas.

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】本発明は、各種の廃棄物等の
被処理物を加熱処理する加熱処理方法および装置に関
し、特に、加熱処理中に発生する分解ガスの処理に関す
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method and an apparatus for heat-treating an object to be treated such as various kinds of wastes, and more particularly to a method for treating a decomposition gas generated during the heat treatment.

【0002】[0002]

【従来の技術】被処理物である各種廃棄物(産業廃棄
物、一般廃棄物等)は、ハロゲン物質(塩素など)等の
有機性物質を含有しており、加熱処理により各種有害物
質(例えば塩化水素、ダイオキシン類)が析出・生成し
て排ガス中に含まれていることが知られており、大気中
に排出する以前の段階で排ガスの浄化処理を行う事(排
出の抑制)が一般的に行われている。
2. Description of the Related Art Various wastes (industrial wastes, general wastes, etc.) to be treated contain organic substances such as halogen substances (chlorine, etc.), and various harmful substances (for example, It is known that hydrogen chloride and dioxins) are precipitated and generated and are contained in exhaust gas, and it is common practice to purify exhaust gas before it is released into the atmosphere (emission control). It has been done.

【0003】加熱処理により多量に発生した塩化水素
は、苛性ソーダなどで中和するか、塩酸にして回収する
ことが一般的に行われている。
[0003] Generally, hydrogen chloride generated in a large amount by heat treatment is neutralized with caustic soda or the like and recovered with hydrochloric acid.

【0004】また、排ガスの浄化処理装置として一般的
な装置として、特開平8−108026号などに示され
ているバグフィルタ装置がある。これらの装置は、排ガ
スの浄化剤として消石灰を使用して排ガス中の塩化水
素、ダイオキシン類の除去を行うようにしている。ま
た、同様な効果を得るために、最近各種の浄化剤が数多
く提案されている。
As a general exhaust gas purifying apparatus, there is a bag filter apparatus disclosed in Japanese Patent Application Laid-Open No. 8-108026. These apparatuses use slaked lime as a purifying agent for exhaust gas to remove hydrogen chloride and dioxins in the exhaust gas. In addition, in order to obtain the same effect, various purifying agents have recently been proposed.

【0005】しかし、排ガス処理のためのバグフィルタ
で使用した消石灰粉末、排ガス中の飛灰、焼却残渣(焼
却灰など)などの、排ガス以外の物にも塩素系ガス成分
は付着・吸着されて、猛毒のダイオキシン類を生成して
しまうことが知られている。
[0005] However, chlorine-based gas components are also adhered and adsorbed to substances other than exhaust gas, such as slaked lime powder used in a bag filter for exhaust gas treatment, fly ash in the exhaust gas, and incineration residue (eg, incinerated ash). It is known to produce highly toxic dioxins.

【0006】一方、発明者らは、有機性物質(塩素など
のハロゲン物質)である有機塩素化合物(塩化水素)が
従来の「排出の抑制」でなく、「発生の抑制」を行うこ
とで、塩化水素などの有害物質の発生を抑制し、排ガス
の無害化、残渣の無害化、塩素による処理装置の損害の
低減化を行うことを提案している。
On the other hand, the present inventors have proposed that organic chlorine compounds (hydrogen chloride), which is an organic substance (halogen substance such as chlorine), perform "suppression of generation" instead of conventional "suppression of emission". It has been proposed to suppress the generation of harmful substances such as hydrogen chloride, to make the exhaust gas harmless, to make the residue harmless, and to reduce the damage to the treatment equipment due to chlorine.

【0007】即ち、被処理物にアルカリ物質を添加混合
して所定の温度で加熱することで塩化水素を分解析出さ
せると同時に添加混合しているアルカリ物質と接触反応
させて無害な塩化物に置換生成する技術を見出し既に出
願し、(例えば、特開平9−155326号、特開平1
0−43713号、特開平10−235186号、特開
平10−235187号など)その後も研究開発を行っ
ている。
That is, an alkaline substance is added to and mixed with an object to be treated and heated at a predetermined temperature to decompose and precipitate hydrogen chloride, and at the same time, contact and react with the alkaline substance added and mixed to form harmless chloride. A technique for generating a replacement has been found and an application has been filed (for example, see JP-A-9-155326,
0-43713, JP-A-10-235186, JP-A-10-235187, etc.).

【0008】更に、脱塩素剤を多孔質化して接触反応す
る面積を増加させて反応効果を高めた脱塩素剤も提案し
ている(特開平10−193844号)。
[0008] Further, a dechlorinating agent has been proposed in which the dechlorinating agent is made porous to increase the area for the contact reaction to enhance the reaction effect (Japanese Patent Application Laid-Open No. 10-193844).

【0009】これらの処理剤を使用し被処理物を加熱処
理して炭化物の残渣を得、この炭化物は多孔質である特
性から、土壌改良剤、水質浄化剤、融雪剤、保温剤に使
用され、また、燃料としても利用できるなど、幅広い分
野でリサイクル品としての利用を可能としている。
Using these treating agents, the material to be treated is heat-treated to obtain a residue of carbide, which is used as a soil improver, a water purifier, a snow melting agent, and a heat insulator due to its porous nature. It can also be used as a recycled product in a wide range of fields, such as being used as fuel.

【0010】[0010]

【発明が解決しようとする課題】被処理物を外部加熱手
段により加熱処理炉で加熱して乾留処理などの加熱分解
処理した場合には、分解ガス(乾留ガス)が発生し、こ
のような発生ガスは850℃で2秒以上燃焼させて排出
することが規則で定められている。
When an object to be treated is heated by an external heating means in a heat treatment furnace and subjected to a thermal decomposition treatment such as a dry distillation treatment, a decomposition gas (a dry distillation gas) is generated. The regulations stipulate that the gas be burned at 850 ° C. for 2 seconds or more and discharged.

【0011】発生ガスは排ガス系統として後段にあるブ
ロアで全体が誘吸引されており、内部は大気圧に対して
負圧傾向にある。ただ、加熱処理内で分解ガスが発生し
た場合は、大気圧に対して正圧となる傾向にある。
The generated gas is entirely attracted and sucked by a blower located at a later stage as an exhaust gas system, and the inside has a negative pressure tendency with respect to the atmospheric pressure. However, when a decomposition gas is generated during the heat treatment, the pressure tends to be positive with respect to the atmospheric pressure.

【0012】加熱処理炉内が正圧になった場合に問題と
なるのは、炉を構成するシール部からのガス漏れであ
る。特に、回転シールを備えているロータリーキルン
(回転形)の場合には、シール部分から分解ガスが漏れ
るおそれがある。この場合、常時状態を監視し、正圧傾
向になった場合には、ブロワの吸引力を強化すればよい
が、監視と制御が煩雑となる。
When a positive pressure is applied to the inside of the heat treatment furnace, a problem is a gas leak from a seal portion constituting the furnace. In particular, in the case of a rotary kiln (rotary type) provided with a rotary seal, the decomposition gas may leak from the seal portion. In this case, the condition is constantly monitored, and if the pressure becomes positive, the suction force of the blower may be increased, but the monitoring and control become complicated.

【0013】また、ブロアで強力に吸引すると分解ガス
燃焼炉内が負圧になり、燃焼状態が変化することにな
る。つまり、850℃、2秒の燃焼が困難になる恐れが
ある。従って、(a)加熱処理炉内圧の負圧維持手段、
(b)分解ガス燃焼炉内での燃焼条件の変化(低下)防
止をいかに行うかが重要な課題となっている。
[0013] When the air is strongly sucked by the blower, the pressure inside the cracked gas combustion furnace becomes negative, and the combustion state changes. That is, combustion at 850 ° C. for 2 seconds may be difficult. Therefore, (a) means for maintaining a negative pressure in the heat treatment furnace,
(B) How to prevent a change (decrease) in combustion conditions in a cracked gas combustion furnace is an important issue.

【0014】本発明は、このような課題に鑑みなされた
もので、加熱処理炉からの分解ガスの漏れを防止すると
ともに、分解ガス燃焼炉の内圧を正圧に維持して分解ガ
スの燃焼を効果的に行うことを目的とする。
SUMMARY OF THE INVENTION The present invention has been made in view of the above problems, and prevents the decomposition gas from leaking from the heat treatment furnace, and maintains the internal pressure of the decomposition gas combustion furnace at a positive pressure to burn the decomposition gas. It aims to be effective.

【0015】[0015]

【課題を解決するための手段】上記の課題を解決するた
め本発明は、加熱処理炉で発生した分解ガス(排ガス、
乾留ガスともいう)を、分解ガス燃焼炉内に導入する
際、加熱処理炉内の圧力を大気圧に対して負圧になるよ
うに誘引して分解ガス燃焼炉内に導入し、且つ、分解ガ
ス燃焼炉内の圧力を大気圧に対して正圧に維持すること
により、加熱処理炉からの分解ガスの漏れを防止し、且
つ、分解ガス燃焼炉内の燃焼条件を850℃、2秒の燃
焼を維持できるようにするものである。
SUMMARY OF THE INVENTION In order to solve the above-mentioned problems, the present invention relates to a decomposition gas (exhaust gas,
When the carbonization gas is introduced into the decomposition gas combustion furnace, the pressure in the heat treatment furnace is induced to be negative with respect to the atmospheric pressure to be introduced into the decomposition gas combustion furnace. By maintaining the pressure in the gas combustion furnace at a positive pressure with respect to the atmospheric pressure, it is possible to prevent the decomposition gas from leaking from the heat treatment furnace, and to set the combustion conditions in the decomposition gas combustion furnace at 850 ° C. for 2 seconds. It allows the combustion to be maintained.

【0016】その具体的手段は、被処理物を加熱処理炉
に投入して加熱分解処理し、且つ発生した分解ガスを分
解ガス燃焼炉で燃焼処理した後排出する被処理物の加熱
処理方法であって、前記加熱処理炉内の圧力を大気圧に
対して負圧とし、分解ガス燃焼炉内の圧力は大気圧に対
して正圧としたことを特徴とする。
The specific means is a method of heating the object to be treated, which is put into a heat treatment furnace for thermal decomposition treatment, and the generated decomposition gas is burned in a decomposition gas combustion furnace and then discharged. The pressure in the heat treatment furnace is negative with respect to the atmospheric pressure, and the pressure in the cracked gas combustion furnace is positive with respect to the atmospheric pressure.

【0017】上記の加熱処理炉内の大気圧に対する負圧
は−5〜−10mmH2Oとし、分解ガス燃焼炉内の大
気圧に対する正圧は、0〜+10mmH2Oとすること
が望ましい。
[0017] The negative pressure relative to atmospheric pressure of the heat treatment furnace and -5 to-10 mm H 2 O, positive pressure relative to atmospheric pressure of the decomposition gas combustion furnace, it is desirable to 0~ + 10mmH 2 O.

【0018】また、加熱処理炉の炉内温度は、200℃
以上、分解ガス燃焼炉の炉内温度は800℃以上とする
ことが望ましい。
The temperature inside the heat treatment furnace is 200 ° C.
As described above, the internal temperature of the cracked gas combustion furnace is desirably 800 ° C. or higher.

【0019】また、加熱処理炉、分解ガス燃焼炉の燃料
として、LPG又はLNGを用いることが望ましい。
It is desirable to use LPG or LNG as fuel for the heat treatment furnace and the cracked gas combustion furnace.

【0020】上記の方法を実施するための装置は、被処
理物を加熱処理炉に投入して加熱分解処理し、且つ発生
した分解ガスを、分解ガス燃焼炉で燃焼した後排出する
ようにした被処理物の加熱処理装置において、前記分解
ガスを分解ガス燃焼炉に導入する分解ガス導入手段は、
加圧の駆動気体をノズルから噴出させ、その噴流の吸引
・搬送力によって分解ガスを導入するように構成する。
In the apparatus for carrying out the above method, an object to be processed is charged into a heat treatment furnace to be thermally decomposed, and the generated decomposition gas is discharged after burning in a decomposition gas combustion furnace. In the heat treatment apparatus for the object to be processed, the decomposition gas introduction means for introducing the decomposition gas into the decomposition gas combustion furnace,
A configuration is adopted in which a pressurized driving gas is ejected from a nozzle, and a decomposition gas is introduced by suction / transport force of the jet.

【0021】上記の分解ガス導入手段は、空気エゼクタ
を用い、駆動気体の噴流の調整により加熱処理炉内の圧
力を大気圧に対して負圧に、分解ガス燃焼炉内の圧力を
大気圧に対して正圧に維持するようにすることが望まし
い。
The above-mentioned decomposition gas introducing means uses an air ejector, and adjusts the pressure in the heat treatment furnace to a negative pressure with respect to the atmospheric pressure and the pressure in the decomposition gas combustion furnace to the atmospheric pressure by adjusting the jet of the driving gas. It is desirable to maintain a positive pressure.

【0022】[0022]

【発明の実施の形態】以下、本発明の実施の形態を図面
によって説明する。
Embodiments of the present invention will be described below with reference to the drawings.

【0023】図1は、本発明の被処理物の加熱処理装置
の概念図で、同じ構成の回転加熱処理炉を2基用い、第
1の回転加熱処理炉に、被処理物を乾燥し脱塩素処理の
機能を持たせ(以下、脱塩炉と称す)、第2の回転加熱
処理炉に、炭化又は灰化処理による減容化処理の機能を
持たせ(以下、減容炉と称す)た場合である。
FIG. 1 is a conceptual diagram of a heat treatment apparatus for an object to be treated according to the present invention. The two objects of the present invention are described below. The second rotary heating furnace is provided with a function of volume reduction by carbonization or incineration treatment (hereinafter, referred to as a volume reduction furnace). Is the case.

【0024】1はこの脱塩炉で、該脱塩炉1は、回転自
在の回転円筒体2と、この回転円筒体2の外周にガスダ
クトを形成して熱ガスを導入して回転円筒体2を外部か
ら加熱する外部加熱手段としての加熱ジャケット3と、
回転円筒体2を両端側で回転自在に支承する支持ローラ
4,4′と、回転円筒体2を回転駆動する回転駆動手段
5,5′とで構成され、また回転円筒体2には一端側に
被処理物を搬入する供給口6、他端側に被処理物を排出
する排出口7を有し、内部には図示を省略してあるが回
転円筒体の軸線に対して傾斜した送り羽根が径方向及び
軸方向に複数枚設けられ、回転円筒体2の回転により、
被処理物を供給口6側から排出口7側に撹拌しながら移
送する。
Reference numeral 1 denotes a desalination furnace. The desalination furnace 1 includes a rotatable rotary cylinder 2 and a gas duct formed on the outer periphery of the rotary cylinder 2 to introduce a hot gas to rotate the rotary cylinder 2. A heating jacket 3 as external heating means for externally heating
Support rollers 4, 4 'for rotatably supporting the rotating cylindrical body 2 at both ends, and rotation driving means 5, 5' for rotating the rotating cylindrical body 2 are provided. A supply port 6 for carrying the object to be processed, and a discharge port 7 for discharging the object to be processed at the other end, and a feed blade (not shown) that is inclined with respect to the axis of the rotating cylinder. Are provided in the radial direction and the axial direction, and by rotation of the rotating cylindrical body 2,
The workpiece is transferred from the supply port 6 side to the discharge port 7 while stirring.

【0025】この回転駆動手段5,5′は、例えば、図
1に示すように、駆動モータ5a,5′a,駆動歯車5
b,5′bおよび回転円筒体2の外周に設けた従動歯車
2a,2′aから成り、駆動モータ5a,5′aは図示
を省略したモータ制御装置で制御される。
As shown in FIG. 1, for example, the rotary driving means 5 and 5 'include driving motors 5a and 5'a and a driving gear 5
b, 5'b and driven gears 2a, 2'a provided on the outer periphery of the rotary cylinder 2, and the drive motors 5a, 5'a are controlled by a motor control device (not shown).

【0026】なお、この回転駆動手段は、駆動モータか
らの動力の伝達手段として歯車を使用した場合について
説明したが、必ずしも歯車による必要はなく、ローラチ
ェーン用のスプロケットを設け、ローラチェーンで伝達
するようにしてもよい。8はメカニカルシールで、円筒
体2の外周に接する加熱ジャケット3との接触部をシー
ルしている。
Although the rotary drive means has been described using a gear as a means for transmitting power from a drive motor, it is not always necessary to use a gear, but a sprocket for a roller chain is provided, and the rotation is transmitted by the roller chain. You may do so. Reference numeral 8 denotes a mechanical seal, which seals a contact portion with the heating jacket 3 which is in contact with the outer periphery of the cylindrical body 2.

【0027】20は減容化処理機能を有する減容炉で、
該減容炉20は脱塩炉1と同じ構成をなす。従って脱塩
炉1と同じ部分には、20の1の桁に脱塩炉1と同じ符
号を付して詳細な説明を省略する。
Reference numeral 20 denotes a volume reduction furnace having a volume reduction processing function.
The volume reduction furnace 20 has the same configuration as the desalination furnace 1. Therefore, the same parts as in the desalination furnace 1 are given the same reference numerals as those of the desalination furnace 1 in the order of 20 and their detailed description is omitted.

【0028】脱塩炉1と減容炉20とは、上下方向で、
且つ減容炉20の供給口26側を脱塩炉1の排出口7側
にして配置する。そして、脱塩炉1の供給口6側に、被
処理物を回転円筒体2内に供給するための供給ダクト1
0を設ける。9はこの供給側ダクト10内に設けたロー
タリーバルブである。また脱塩炉1の排出口7と減容炉
20の供給口26側には、これら排出口7と供給口26
を覆って連通する連通ダクト11を設け、脱塩炉1で加
熱処理した被処理物(残渣)を減容炉20に導入する。
12はこの連通ダクト11の中間部に設けられたロータ
リーバルブである。
The desalination furnace 1 and the volume reduction furnace 20 are vertically
In addition, the supply port 26 side of the volume reduction furnace 20 is arranged on the discharge port 7 side of the desalination furnace 1. A supply duct 1 for supplying the object to be processed into the rotary cylindrical body 2 is provided on the supply port 6 side of the desalination furnace 1.
0 is provided. Reference numeral 9 denotes a rotary valve provided in the supply duct 10. The discharge port 7 and the supply port 26 of the desalination furnace 1 and the supply port 26
A communication duct 11 is provided so as to cover the object, and an object to be treated (residue) heated in the desalination furnace 1 is introduced into the volume reduction furnace 20.
Reference numeral 12 denotes a rotary valve provided at an intermediate portion of the communication duct 11.

【0029】30は熱ガス発生手段で、燃料タンク29
からLNG又はLPG等の燃料の供給を受けてこれを燃
焼して熱ガスを発生させる。発生した熱ガスは、減容炉
20の加熱ジャケット23に供給し、減容炉20の回転
円筒体22を加熱した後、連絡管31を介して脱塩炉1
の加熱ジャケット3内に供給される。このとき、温度調
整空気32を送り込み、熱ガスの温度を調整する。
Reference numeral 30 denotes a hot gas generating means,
And supplies the fuel such as LNG or LPG, and burns the fuel to generate hot gas. The generated hot gas is supplied to the heating jacket 23 of the volume reduction furnace 20 to heat the rotating cylindrical body 22 of the volume reduction furnace 20, and then the desalination furnace 1 is connected via the connecting pipe 31.
Is supplied into the heating jacket 3. At this time, the temperature adjusting air 32 is sent in to adjust the temperature of the hot gas.

【0030】33はホッパで、被処理物と脱塩素剤とを
混合した混合物、又は混合しながら供給側ダクト10を
介して脱塩炉1の回転円筒体2内に供給する。
Reference numeral 33 denotes a hopper, which feeds the mixture of the object to be treated and the dechlorinating agent, or the mixture into the rotary cylindrical body 2 of the desalination furnace 1 via the supply duct 10 while mixing.

【0031】なお、図示を省略してあるが、回転円筒体
2と回転接触する供給側ダクト10,連通ダクト11お
よび回転円筒体22と回転接触する連通ダクト11およ
び排出側ダクト13との接触部には、ガス漏れを防止す
るためのメカニカルシールが施されている。
Although not shown, the contact portion between the supply duct 10, the communication duct 11 and the communication duct 11 and the discharge duct 13 which are in rotational contact with the rotary cylinder 2 and the rotary cylinder 22, respectively. Is provided with a mechanical seal for preventing gas leakage.

【0032】34は分解ガス燃焼炉で、脱塩炉1および
減容炉20で加熱処理中に発生した分解ガス(排ガス)
を、ガス導管35,36から導入し、バーナ34aでタ
ール分等の可燃性分および残存有害物質を燃焼処理し、
排ガス冷却手段37で冷却した後、バグフィルタ38で
浄化して煙突40から排出する。この排ガス冷却手段3
7での冷却は、冷却空気又は冷却液を噴霧することで冷
却できる。39はバグフィルタに設けられたブロワで、
加熱処理炉内で発生したガスを吸引する。
Reference numeral 34 denotes a cracked gas combustion furnace, which is a cracked gas (exhaust gas) generated during the heat treatment in the desalination furnace 1 and the volume reduction furnace 20.
Is introduced through gas conduits 35 and 36, and combustible components such as tar components and residual harmful substances are burned by a burner 34a.
After being cooled by the exhaust gas cooling means 37, it is purified by the bag filter 38 and discharged from the chimney 40. This exhaust gas cooling means 3
The cooling in 7 can be performed by spraying cooling air or a cooling liquid. 39 is a blower provided in the bag filter,
The gas generated in the heat treatment furnace is sucked.

【0033】41は溶解槽で、減容炉20で減容化した
被処理物と、脱塩炉1内で脱塩素剤と反応して生成され
た塩化物等を排出側ダクト13、二重ダンパ14から排
出されるのを受け、これを水洗いして塩化物等を除去し
た後、脱水手段42で脱水し、乾燥手段43で乾燥して
炭化物等を取り出す。
Reference numeral 41 denotes a dissolving tank, which discharges the material to be treated reduced in the volume reducing furnace 20 and the chloride and the like generated by reacting with the dechlorinating agent in the desalination furnace 1 to the discharge side duct 13, After being discharged from the damper 14, it is washed with water to remove chlorides and the like, then dehydrated by the dehydrating means 42 and dried by the drying means 43 to take out carbides and the like.

【0034】44は排水処理手段で、溶解槽41からの
水、および脱水時に発生する水分を無害化処理した後、
排水する。
Reference numeral 44 denotes wastewater treatment means for detoxifying water from the dissolving tank 41 and water generated during dehydration.
Drain.

【0035】なお、ロータリーバルブ9,12は、開閉
自在で間欠的に被処理物を送り出す間欠送り出し手段で
構成してもよい。
Incidentally, the rotary valves 9 and 12 may be constituted by intermittent sending means for opening and closing and intermittently sending the object to be processed.

【0036】乾燥手段43には、熱源として、脱塩炉1
を加熱した後の熱ガスを排気管45からガス管46を介
して導入して加熱する。
The drying means 43 includes a desalination furnace 1 as a heat source.
The hot gas after heating is introduced from the exhaust pipe 45 through the gas pipe 46 and heated.

【0037】図2は図1の分解ガス燃焼炉34部分を拡
大した模式図で、50は分解ガス導入手段を示し、空気
エゼクタにより構成した場合を示している。該分解ガス
導入手段50は外筒51、該外筒51内に設けられたノ
ズル部材52およびこのノズル部材52に加圧の駆動気
体を送出するブロワ53とからなり、外筒51の一端は
分解ガス燃焼炉34内に開口し、他端側はガス導入管3
5,36と連通している。ノズル部材52は先端側が細
く絞られて外筒51の開口部の部分で開口し、他端側は
ブロワ53に接続されている。このブロワ53からの空
気をノズル部材52の先端から噴出させ、その噴流の吸
引・搬送力によって、分解ガスは分解ガス燃焼炉34内
に誘引され、燃焼される。
FIG. 2 is an enlarged schematic view of the cracked gas combustion furnace 34 shown in FIG. 1. Numeral 50 indicates a cracked gas introducing means, which is constituted by an air ejector. The decomposed gas introducing means 50 includes an outer cylinder 51, a nozzle member 52 provided in the outer cylinder 51, and a blower 53 for sending a pressurized driving gas to the nozzle member 52. One end of the outer cylinder 51 is disassembled. It is opened in the gas combustion furnace 34, and the other end side is a gas introduction pipe 3
It communicates with 5,36. The tip end of the nozzle member 52 is narrowed narrowly and is opened at the opening of the outer cylinder 51, and the other end is connected to the blower 53. The air from the blower 53 is ejected from the tip of the nozzle member 52, and the decomposed gas is attracted into the decomposed gas combustion furnace 34 and burned by the suction / conveyance of the jet.

【0038】回転加熱処理炉内の圧力は、通常はバグフ
ィルタ38に有するブロワ39で吸引されているので、
大気圧に対して負圧傾向にあるが、加熱処理により分解
ガスが発生すると正圧になる傾向にある。しかし、分解
ガス導入手段50のブロワ53からの送風量(流速)に
よって回転加熱処理内の分解ガスは誘引され、大気圧に
対して負圧とすることができる。この負圧値はブロワの
回転を制御することによって容易に調整でき、−5〜−
10mmH2Oとすることが望ましい。
Since the pressure in the rotary heating furnace is normally sucked by the blower 39 provided in the bag filter 38,
The pressure tends to be negative with respect to the atmospheric pressure, but tends to be positive when the decomposition gas is generated by the heat treatment. However, the decomposed gas in the rotary heating process is attracted by the air flow rate (flow rate) from the blower 53 of the decomposed gas introduction means 50, and can be made negative pressure with respect to the atmospheric pressure. This negative pressure value can be easily adjusted by controlling the rotation of the blower.
It is desirable to set it to 10 mmH 2 O.

【0039】また、分解ガス燃焼炉34内の圧力は、燃
焼条件から正圧が望ましく、空気と分解ガスの導入によ
り正圧(0〜+10mmH2O)を維持する。
The pressure in the cracked gas combustion furnace 34 is desirably a positive pressure in view of combustion conditions, and is maintained at a positive pressure (0 to +10 mmH 2 O) by introducing air and a cracked gas.

【0040】次に、被処理物の一連の処理方法について
説明する。まず、熱ガス発生手段30でLNG等の燃料
を燃焼して熱ガスを発生させ、減容炉20の加熱ジャケ
ット23に供給して回転円筒体22を加熱した後、連絡
管31を介して脱塩炉1の加熱ジャケット3に送り込
み、回転円筒体2を加熱する。
Next, a series of processing methods for the object to be processed will be described. First, the hot gas generating means 30 burns fuel such as LNG to generate a hot gas, and supplies the hot gas to the heating jacket 23 of the volume reduction furnace 20 to heat the rotary cylindrical body 22. It is fed into the heating jacket 3 of the salt furnace 1 to heat the rotating cylinder 2.

【0041】次に、ハロゲン物質等の有害成分を含有す
る被処理物を破砕して細かくしたもの(または混合しな
がら破砕)と脱塩素剤とを混合したもの、又は混合しな
がらホッパ33から供給側ダクト10を介して脱塩炉1
の回転円筒体2内に供給する。
Next, a material containing a harmful component such as a halogen substance is crushed into fine pieces (or crushed while mixing) and a mixture of a dechlorinating agent or supplied from a hopper 33 while mixing. Desalting furnace 1 through side duct 10
Is supplied into the rotating cylindrical body 2.

【0042】この脱塩炉1での加熱処理は、被処理物か
ら塩素系ガスが析出する温度と時間を事前に調査して、
被処理物の性質を把握し、この調査結果を十分にカバー
できる温度(例えば、200℃〜350℃)と時間で処
理する。この温度の調整は、基本的には連絡管31に供
給する温度調整空気32の供給量によって行う。
In the heat treatment in the desalination furnace 1, the temperature and time at which the chlorine-based gas precipitates from the object to be treated are investigated in advance,
The properties of the object to be treated are grasped, and the treatment is performed at a temperature (for example, 200 ° C. to 350 ° C.) and time that can sufficiently cover the result of the investigation. This temperature adjustment is basically performed by the supply amount of the temperature adjustment air 32 supplied to the communication pipe 31.

【0043】この脱塩炉1での加熱は、燃焼、焼却では
なく、低酸素雰囲気中での蒸し焼き、熱分解での処理と
し、熱分解により析出したHCIガス等の有害成分と脱
塩素剤とを接触反応させる。
The heating in the desalination furnace 1 is not burning and incineration but steaming and pyrolysis in a low oxygen atmosphere, and harmful components such as HCI gas deposited by the pyrolysis and the dechlorinating agent are not used. Is subjected to a contact reaction.

【0044】被処理物と混合又は添加する脱塩素剤は、
少なくともHCI(塩化水素)と接触反応して無害な塩
化物を生成するアルカリ物質を使用する。例えば、本願
の出願人が先に出願した特開平9−155326号、特
開平10−43731号、特開平10−235186
号、特開平10−235187号、特開平10−193
844号に示すように、アルカリ土類金属、アルカリ土
類金属化合物、アルカリ金属、アルカリ金属化合物で、
具体的には、カルシウム、石灰、消石灰、炭酸カルシウ
ム、ドロマイト、珪酸塩(珪酸カルシウムなど)、炭酸
水素ナトリウム、炭酸ナトリウム、セスキ炭酸ナトリウ
ム、天然ソーダ、水酸化ナトリウム、水酸化カリウム、
炭酸水素カリウム、炭酸カリウムの中から1種類選択す
るか、数種類混合して使用する。使用量としては、被処
理物に対して5〜30重量%を混合又は添加する。
The dechlorinating agent to be mixed or added with the object to be treated is
An alkaline substance is used that at least reacts with HCI (hydrogen chloride) to form harmless chlorides. For example, Japanese Patent Application Laid-Open Nos. Hei 9-155326, Hei 10-43731 and Hei 10-235186 filed earlier by the applicant of the present application
JP-A-10-235187, JP-A-10-193
No. 844, an alkaline earth metal, an alkaline earth metal compound, an alkali metal, an alkali metal compound,
Specifically, calcium, lime, slaked lime, calcium carbonate, dolomite, silicate (such as calcium silicate), sodium hydrogen carbonate, sodium carbonate, sodium sesquicarbonate, natural soda, sodium hydroxide, potassium hydroxide,
One of potassium hydrogen carbonate and potassium carbonate is selected, or several types are mixed and used. As an amount to be used, 5 to 30% by weight based on the material to be treated is mixed or added.

【0045】例えば、上記の炭酸水素ナトリウム(Na
HCO3)を使用した場合、第1の加熱処理炉である脱
塩炉内においてHCl成分の分解ガスが発生するが、直
ちに炭酸水素ナトリウムと反応して(NaHCO3)+
(HCl)→(NaCl)+(H2O)+(CO2)とな
り、無害な塩化ナトリウム(NaCl)を生成し、分解
ガスから有害なHClが無くなる。このことによって、
分解ガス中のHCl成分の無害化と残渣の無害化が同時
に行われる。
For example, sodium bicarbonate (Na
When HCO 3 ) is used, a decomposition gas of the HCl component is generated in the desalination furnace, which is the first heat treatment furnace, but immediately reacts with sodium hydrogen carbonate to produce (NaHCO 3 ) +
(HCl) → (NaCl) + (H 2 O) + (CO 2 ), producing harmless sodium chloride (NaCl) and eliminating harmful HCl from the decomposition gas. This allows
The detoxification of the HCl component in the cracked gas and the detoxification of the residue are performed simultaneously.

【0046】この有害成分を析出し、無害化した後の被
処理物(残渣)は、連通ダクト11、ロータリーバルブ
12を介して第2の回転加熱処理炉である減容炉20の
回転円筒体22の供給口26に送り込まれ、ここで被処
理物が炭化する温度(紙類は350℃程度で炭化が始ま
る。)350℃〜700℃に加熱して炭化処理、又は8
00℃以上に加熱して灰化処理して減容化する。
The object (residue) after the harmful components are precipitated and detoxified is passed through a communication duct 11 and a rotary valve 12 to a rotary cylindrical body of a volume reduction furnace 20 as a second rotary heating furnace. The material is fed into the supply port 26 of 22 and is carbonized at a temperature at which the object is carbonized (paper begins to carbonize at about 350 ° C.).
The volume is reduced by heating to 00 ° C. or more by incineration.

【0047】この減容化した被処理物と、反応後の塩化
ナトリウムは、排出側ダクト13および二重ダンパ14
を介して溶解槽41に排出される。この溶解槽41内
で、減容化された被処理物、反応後の脱塩素剤(塩化ナ
トリウム)を水に溶解し、水に溶解した塩化ナトリウム
を排水処理手段44に排出し、残りの固形物は脱水手段
42で脱水してこれを乾燥手段43で乾燥し、炭化物等
の固形物を取り出す。取り出された固形物は、物性に応
じて分別して、再利用に供する。
The volume-reduced material to be treated and the sodium chloride after the reaction are discharged into the discharge duct 13 and the double damper 14.
Is discharged to the dissolving tank 41 through In this dissolving tank 41, the reduced volume of the object to be treated and the dechlorinating agent (sodium chloride) after the reaction are dissolved in water, and the sodium chloride dissolved in the water is discharged to a wastewater treatment means 44, and the remaining solids are discharged. The material is dehydrated by the dehydrating means 42 and dried by the drying means 43 to take out solid matter such as carbide. The solids taken out are separated according to their physical properties and are reused.

【0048】一方、脱塩炉1および減容炉20内で加熱
処理中に発生した分解ガス(排ガス、乾留ガス)は、分
解ガス導入手段50によってガス導出管35および36
から分解ガス燃焼炉34内に誘引され、ここで燃焼処理
される。
On the other hand, the decomposition gas (exhaust gas, dry distillation gas) generated during the heat treatment in the desalination furnace 1 and the volume reduction furnace 20 is supplied to the gas outlet pipes 35 and 36 by the decomposition gas introduction means 50.
From the furnace to the cracked gas combustion furnace 34, where it is burned.

【0049】この分解ガスには、塩化水素などの有害成
分は、脱塩炉1における反応処理によって基本的には除
去されるが、何等かの事由によって反応しきれず、排ガ
ス中に残存する可能性もある。また、タール等の可燃成
分も含まれているので、ガス燃焼手段34で燃焼処理し
た後、排ガス冷却手段37で、バグフィルタ38の耐熱
許容温度以下に下げて、バグフィルタ38で清浄して煙
突40から排出される。
In this decomposed gas, harmful components such as hydrogen chloride are basically removed by the reaction treatment in the desalination furnace 1, but they cannot be completely reacted for some reason and may remain in the exhaust gas. There is also. In addition, since combustible components such as tar are also contained, the gas is burned by the gas combustion means 34, then cooled by the exhaust gas cooling means 37 to a temperature lower than the allowable temperature limit of the bag filter 38, and cleaned by the bag filter 38 to form a chimney It is discharged from 40.

【0050】[0050]

【発明の効果】以上詳細に説明したように、本発明は廃
棄物の被処理物から塩素系ガス等の有害成分を分解析出
し、この析出した有害成分とアルカリ物質の脱塩素剤と
を接触反応させて無害な塩化物を形成し、発生する分解
ガスの大気中への放出と残渣の減容化までの一連の過程
における各工程を有益的に結合し、熱源の有効利用をは
かることなどによって被処理物の処理装置全体として高
効率で安全な施設が得られるとともに、分解ガス燃焼炉
に分解ガス導入手段を設けて、回転加熱処理炉内の圧力
を大気圧に対して負圧に、分解ガス燃焼炉内の圧力を大
気圧に対して正圧に維持するようにしたので、加熱処理
炉における回転円筒体と各ダクトとの接触部のメカニカ
ルシール部分からのガス漏れは生じない。また誘引され
る空気も非常に少ないので、安定した分解と反応環境を
確保・維持できる。
As described in detail above, the present invention decomposes and deposits harmful components such as chlorine-based gas from waste materials to be treated, and contacts the deposited harmful components with a dechlorinating agent for alkaline substances. Reacts to form harmless chlorides.Effectively combines each step in the series of processes from release of generated decomposition gas to the atmosphere and volume reduction of residues, and to use heat sources effectively. As a result, a high-efficiency and safe facility can be obtained as a whole of the processing apparatus for the object to be processed, and a cracking gas introducing means is provided in the cracking gas combustion furnace, and the pressure in the rotary heating furnace is reduced to a negative pressure with respect to the atmospheric pressure. Since the pressure in the cracked gas combustion furnace is maintained at a positive pressure with respect to the atmospheric pressure, gas leakage does not occur from the mechanical seal portion at the contact portion between the rotating cylinder and each duct in the heat treatment furnace. In addition, since the amount of induced air is very small, a stable decomposition and reaction environment can be secured and maintained.

【0051】また、分解ガス燃焼炉内の圧力は、大気圧
に対して正圧(0〜+10mmH2O)を維持でき、規
定されている850℃、2秒の燃焼を維持できる、等の
効果を奏する。
The pressure in the cracked gas combustion furnace can be maintained at a positive pressure (0 to +10 mmH 2 O) with respect to the atmospheric pressure, and the specified combustion at 850 ° C. for 2 seconds can be maintained. To play.

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

【図1】本発明の実施の形態の概念図。FIG. 1 is a conceptual diagram of an embodiment of the present invention.

【図2】本発明の分解ガス燃焼炉の説明図。FIG. 2 is an explanatory view of a cracked gas combustion furnace of the present invention.

【符号の説明】[Explanation of symbols]

1…脱塩炉 20…減容炉 2,22…回転円筒体 3,23…加熱ジャケット 4,24…支持ローラ 5,25…回転駆動手段 6,26…供給口 7,27…排出口 8…メカニカルシール 9…ロータリーバルブ 10…供給側ダクト 11…連通ダクト 12…ロータリーバルブ 13…排出側ダクト 14…二重ダンパ 29…燃料タンク 30…熱ガス発生手段 31…連絡管 32…温度調節空気 33…ホッパ 34…ガス燃焼炉 35,36…ガス導入管 37…排ガス冷却手段 38…バグフィルタ 39…ブロワ 40…煙突 41…熔解槽 42…脱水手段 43…乾燥手段 44…排水処理手段 45…排気管 46…ガス管 50…分解ガス導入手段 51…外筒 52…ノズル部材 53…ブロワ DESCRIPTION OF SYMBOLS 1 ... Demineralization furnace 20 ... Volume reduction furnace 2, 22 ... Rotating cylindrical body 3, 23 ... Heating jacket 4, 24 ... Support roller 5, 25 ... Rotation drive means 6, 26 ... Supply port 7, 27 ... Discharge port 8 ... Mechanical seal 9 Rotary valve 10 Supply duct 11 Communication duct 12 Rotary valve 13 Discharge duct 14 Double damper 29 Fuel tank 30 Hot gas generating means 31 Communication pipe 32 Temperature controlled air 33 Hopper 34 Gas combustion furnace 35 36 Gas introduction pipe 37 Exhaust gas cooling means 38 Bag filter 39 Blower 40 Chimney 41 Melting tank 42 Dewatering means 43 Drying means 44 Wastewater treatment means 45 Exhaust pipe 46 ... gas pipe 50 ... decomposition gas introduction means 51 ... outer cylinder 52 ... nozzle member 53 ... blower

Claims (6)

【特許請求の範囲】[Claims] 【請求項1】 被処理物を加熱処理炉に投入して加熱分
解処理し、且つ発生した分解ガスを分解ガス燃焼炉で燃
焼処理した後排出する被処理物の加熱処理方法であっ
て、前記加熱処理炉内の圧力を大気圧に対して負圧と
し、分解ガス燃焼炉内の圧力は大気圧に対して正圧とし
たことを特徴とする被処理物の加熱処理方法。
1. A heat treatment method for an object to be treated, wherein the object to be treated is charged into a heat treatment furnace for thermal decomposition treatment, and the generated decomposition gas is burned in a decomposition gas combustion furnace and then discharged. A method for heat treating an object to be processed, wherein the pressure in the heat treatment furnace is set to a negative pressure with respect to the atmospheric pressure, and the pressure in the cracked gas combustion furnace is set to a positive pressure with respect to the atmospheric pressure.
【請求項2】 加熱処理炉内の大気圧に対する負圧は、
−5〜−10mmH2Oとし、分解ガス燃焼炉内の大気
圧に対する正圧は、0〜+10mmH2Oとしたことを
特徴とする請求項1記載の被処理物の加熱処理方法。
2. The negative pressure with respect to the atmospheric pressure in the heat treatment furnace is:
And -5 to-10 mm H 2 O, positive pressure relative to atmospheric pressure of the decomposition gas combustion furnace, the heat treatment method according to claim 1 the processed material, wherein it has a 0~ + 10mmH 2 O.
【請求項3】 加熱処理炉の炉内温度は200℃以上、
分解ガス燃焼炉の炉内温度は800℃以上としたことを
特徴とする請求項1又は2記載の被処理物の加熱処理方
法。
3. The furnace temperature of the heat treatment furnace is 200 ° C. or more,
3. The method according to claim 1, wherein the furnace temperature of the cracked gas combustion furnace is 800 ° C. or higher.
【請求項4】 加熱処理炉、分解ガス燃焼炉の燃料とし
て、LPG又はLNGを用いることを特徴とする請求項
1ないし3のいずれか1項に記載の被処理物の加熱処理
方法。
4. The heat treatment method for an object according to claim 1, wherein LPG or LNG is used as a fuel for the heat treatment furnace and the cracked gas combustion furnace.
【請求項5】 被処理物を加熱処理炉に投入して加熱分
解処理し、且つ発生した分解ガスを、分解ガス燃焼炉で
燃焼した後排出するようにした被処理物の加熱処理装置
において、前記分解ガスを分解ガス燃焼炉に導入する分
解ガス導入手段は、加圧の駆動気体をノズルから噴出さ
せ、その噴流の吸引・搬送力によって分解ガスを導入す
るようにしたことを特徴とする被処理物の加熱処理装
置。
5. A heat treatment apparatus for an object to be processed, wherein the object to be processed is charged into a heat treatment furnace to be thermally decomposed, and the generated decomposition gas is discharged after being burned in a decomposition gas combustion furnace. The cracked gas introducing means for introducing the cracked gas into the cracked gas combustion furnace ejects a pressurized driving gas from a nozzle, and introduces the cracked gas by suction / transport force of the jet. Heat treatment equipment for processed materials.
【請求項6】 分解ガス導入手段は、空気エゼクタを用
い、駆動気体の噴流の調整により、加熱処理炉内の圧力
を大気圧に対して負圧に、分解ガス燃焼炉内の圧力を大
気圧に対して正圧に維持するようにしたことを特徴とす
る請求項6記載の被処理物の加熱処理装置。
6. The decomposition gas introduction means uses an air ejector, and adjusts the pressure in the heat treatment furnace to a negative pressure with respect to the atmospheric pressure and the pressure in the decomposition gas combustion furnace to the atmospheric pressure by adjusting the jet of the driving gas. 7. The apparatus according to claim 6, wherein the apparatus is maintained at a positive pressure.
JP11234952A 1999-08-23 1999-08-23 Method and system for heating matter to be treated Pending JP2001059607A (en)

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Application Number Priority Date Filing Date Title
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Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01144623U (en) * 1988-03-17 1989-10-04
JPH03274311A (en) * 1990-03-22 1991-12-05 Nippon Jietsuto Kk Incinerating method for gasification of waste plastic and incinerator thereof
JPH109538A (en) * 1996-06-21 1998-01-16 Chiyoda Corp Method for incinerating municipal refuse
JPH10132239A (en) * 1996-10-30 1998-05-22 Ishikawajima Harima Heavy Ind Co Ltd Method and apparatus for disposing of thermal decomposition gas of waste thermal decomposition gasifying apparatus
JPH11153313A (en) * 1997-11-21 1999-06-08 Hitachi Chem Co Ltd Carbonizing apparatus

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01144623U (en) * 1988-03-17 1989-10-04
JPH03274311A (en) * 1990-03-22 1991-12-05 Nippon Jietsuto Kk Incinerating method for gasification of waste plastic and incinerator thereof
JPH109538A (en) * 1996-06-21 1998-01-16 Chiyoda Corp Method for incinerating municipal refuse
JPH10132239A (en) * 1996-10-30 1998-05-22 Ishikawajima Harima Heavy Ind Co Ltd Method and apparatus for disposing of thermal decomposition gas of waste thermal decomposition gasifying apparatus
JPH11153313A (en) * 1997-11-21 1999-06-08 Hitachi Chem Co Ltd Carbonizing apparatus

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