JPH11226542A - Waste treatment apparatus - Google Patents

Waste treatment apparatus

Info

Publication number
JPH11226542A
JPH11226542A JP10036915A JP3691598A JPH11226542A JP H11226542 A JPH11226542 A JP H11226542A JP 10036915 A JP10036915 A JP 10036915A JP 3691598 A JP3691598 A JP 3691598A JP H11226542 A JPH11226542 A JP H11226542A
Authority
JP
Japan
Prior art keywords
waste
treatment apparatus
kiln body
induction heating
waste treatment
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.)
Withdrawn
Application number
JP10036915A
Other languages
Japanese (ja)
Inventor
Kiyonori Kida
清則 喜田
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.)
Fuji Electric Co Ltd
Original Assignee
Fuji Electric 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 Fuji Electric Co Ltd filed Critical Fuji Electric Co Ltd
Priority to JP10036915A priority Critical patent/JPH11226542A/en
Publication of JPH11226542A publication Critical patent/JPH11226542A/en
Withdrawn legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To respond to the variation of a treatment quantity and the variation of pyrolysis energy varying by the change of a treatment material in a short time by improving the heat response of a rotary kiln apparatus and to improve heat efficiency by downscalling a heating zone. SOLUTION: A waste treatment apparatus is constituted from a kiln main body 1 which is constituted from a hollow cylindrical body which supports the lower part of a tire 1a rotatably by a roller and closed by apparatuses arranged in the front and rear stages, transports waste raw materials including chlorine compounds carried from the front stage while heating them at a prescribed temperature in the inside, and produces pyrolysis gas and a non-volatile residue, a waste raw material charging device 9 having a screw feeder 6 for transporting the waste to the kiln main body 1, induction heating coils 4a, 4b, 4c for induction-heating the kiln main body 1 from the outside, and a residue recovery chamber 13 which is arranged in the rear stage of the kiln main body 1, recovers the non-volatile residue, collects pyrolysis gas, and discharges the gas to a gas treatment apparatus in the rear stage.

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、塩化ビニール、
ポリエチレン等の塩素化合物を含む廃棄物をダイオキシ
ンが発生しないようにして処理する廃棄物処理装置に関
する。
[0001] The present invention relates to vinyl chloride,
The present invention relates to a waste treatment apparatus for treating waste containing a chlorine compound such as polyethylene so as not to generate dioxin.

【0002】[0002]

【従来の技術】塩化ビニール、ポリエチレン等の塩素化
合物を含む廃棄物を加熱処理して熱分解ガスと不揮発性
残渣とを生成するこの種の廃物処理装置については、特
開平9−217910号公報が知られている。この公報
によれば、廃棄物はスクリューフィーダーにより中空の
円筒回転体内に搬入され、前記円筒体の前後に配備され
た加熱空気室から、円筒体内に複数の加熱管を挿通し
て、例えば円筒体の長手方向の略中央で円筒体の外周側
に、前記加熱空気室からの加熱空気が排出されるように
前記加熱管を配管して、該加熱管に加熱空気室から加熱
空気を供給して、前記円筒体内に供給された廃棄物を加
熱して熱分解ガスと不揮発性残渣とを生成している。そ
の際に加熱空気の流入方向は、円筒体の上流側から中央
へと、および下流端から中央へと通風するようにして、
上流部での加熱管の温度が投入される廃棄物により過度
に冷却されて、廃棄物中の比較的低温(100℃以下)
で溶融するポリエチレン、ポリプロピレン等が加熱管に
溶融付着して、その後投入される廃棄物の加熱を阻害す
るのを防止するように工夫している。また、円筒体の下
流には加熱空気室があり、さらにその下流には加熱され
た廃棄物を熱分解ガスと不揮発性残渣とに分離して排出
する排出装置が設けられている。
2. Description of the Related Art Japanese Unexamined Patent Publication (Kokai) No. 9-217910 discloses a waste disposal apparatus of this type for producing waste by heating a waste containing a chlorine compound such as vinyl chloride and polyethylene to generate a pyrolysis gas and a non-volatile residue. Are known. According to this publication, waste is carried into a hollow cylindrical rotating body by a screw feeder, and a plurality of heating tubes are inserted into the cylindrical body from a heated air chamber provided before and after the cylindrical body, for example, the cylindrical body. At approximately the center in the longitudinal direction, on the outer peripheral side of the cylindrical body, the heating pipe is piped such that the heating air from the heating air chamber is discharged, and heating air is supplied from the heating air chamber to the heating pipe. Further, the waste supplied into the cylindrical body is heated to generate a pyrolysis gas and a non-volatile residue. At that time, the inflow direction of the heated air flows from the upstream side to the center of the cylindrical body, and from the downstream end to the center,
The temperature of the heating pipe in the upstream part is excessively cooled by the input waste, and the temperature in the waste is relatively low (100 ° C. or less)
It is devised so as to prevent polyethylene, polypropylene, etc., which melts in the above, from melting and adhering to the heating tube and hindering the heating of the waste to be charged thereafter. Further, a heating air chamber is provided downstream of the cylindrical body, and further downstream there is provided a discharge device for separating heated waste into a pyrolysis gas and a non-volatile residue and discharging the same.

【0003】[0003]

【発明が解決しようとする課題】ところで従来の構成で
は、廃棄物を加熱する加熱管の加熱は加熱空気によりな
されており、加熱空気と加熱管との熱伝達量は比較的少
ないので、投入された廃棄物が加熱管と接触する量が大
きく変動すると、廃棄物に奪われる熱量による加熱管の
温度変化を補償するのに時間がかかり、加熱管の温度が
所定値を下回っている際は、新たに投入される廃物の加
熱が遅れる問題があり、その分加熱ゾーンを長くする必
要がある。
By the way, in the conventional structure, the heating pipe for heating the waste is heated by the heated air, and the heat transfer between the heated air and the heating pipe is relatively small. If the amount of waste that comes into contact with the heating tube fluctuates greatly, it takes time to compensate for the temperature change of the heating tube due to the amount of heat taken by the waste, and when the temperature of the heating tube is below a predetermined value, There is a problem that the heating of newly input waste is delayed, and the heating zone needs to be lengthened accordingly.

【0004】この発明は上記課題を解決するためになさ
れたもので、その目的とするところは、加熱応答性を良
くして、処理量の変動、および処理物の変化により変動
する熱分解エネルギの変動に短時間で対応して加熱ゾー
ンを小型化して熱効率を向上させた廃棄物処理装置を提
供することにある。
SUMMARY OF THE INVENTION The present invention has been made to solve the above-mentioned problems. An object of the present invention is to improve the heat response and to improve the thermal decomposition energy of the thermal decomposition energy which fluctuates due to the variation of the throughput and the variation of the workpiece. An object of the present invention is to provide a waste treatment apparatus in which a heating zone is reduced in size in response to fluctuations in a short time and thermal efficiency is improved.

【0005】[0005]

【課題を解決するための手段】上記課題を解決するため
に請求項1記載の発明は、長手方向の両端部に配備した
円筒形のタイヤの下部を駆動装置のローラで回転可能に
支持し、前後段に配備する機器により内部を密閉するよ
うにした中空の円筒体から構成し、前段から搬入された
塩素化合物を含む廃棄物原料を内部で所定の温度に加熱
保持しながら搬送して熱分解ガスおよび不揮発性残渣を
生成するキルン本体と、該キルン本体の前段に配備し
て、前記廃棄物を前記キルン本体に搬送するスクリュー
フィーダーを有する廃棄物原料投入装置と、該キルン本
体を外周側から誘導加熱する誘導加熱コイルと、前記キ
ルン本体の後段に配備して不揮発性残渣を回収するとと
もに、熱分解ガスを収集して後段のガス処理装置へ排出
する残渣回収室とを備えたことを特徴とする。
According to a first aspect of the present invention, there is provided a cylindrical tire provided at both ends in a longitudinal direction, the lower part of which is rotatably supported by rollers of a driving device. It is composed of a hollow cylindrical body whose interior is sealed by equipment installed in the front and rear stages, and transports waste materials containing chlorine compounds brought in from the front stage while heating and holding them at a predetermined temperature inside and thermally decomposes A kiln body that produces gas and non-volatile residue, a waste material input device having a screw feeder disposed in front of the kiln body and transporting the waste to the kiln body, and the kiln body from the outer peripheral side An induction heating coil for induction heating, and a residue recovery chamber disposed at a subsequent stage of the kiln body to collect non-volatile residues and collect a pyrolysis gas and discharge the gas to a gas treatment device at a subsequent stage. And it said that there were pictures.

【0006】また、請求項2記載の発明のように、請求
項1記載の廃棄物処理装置において、キルン本体を誘導
加熱する誘導加熱コイルはキルンの軸方向に複数個に分
割して各誘導加熱コイルを個別に出力制御できるように
することができる。さらに、請求項3記載の発明のよう
に、請求項1または請求項2に記載の廃棄物処理装置に
おいて、前記複数個に分割した誘導加熱コイルはキルン
入り口側を後段の出力よりも高出力とすることができ
る。
According to a second aspect of the present invention, in the waste treatment apparatus according to the first aspect, the induction heating coil for induction heating the kiln body is divided into a plurality of pieces in the axial direction of the kiln and each of the induction heating coils is divided into a plurality. The output of the coils can be individually controlled. Further, as in the invention according to claim 3, in the waste treatment apparatus according to claim 1 or 2, the induction heating coil divided into a plurality has a kiln entrance side with a higher output than the output of the subsequent stage. can do.

【0007】上記請求項1から3の構成により廃棄物を
加熱する円筒体は誘導加熱により直接円筒体が発熱する
ので加熱応答性を良くすることが可能になり、また、廃
棄物加熱に最適な加熱パターンを選択することが可能に
なり、全体として小型化になるとともに、熱効率を向上
させることが可能になる。また、請求項4記載の発明
は、請求項1ないし請求項3のいずれかに記載の廃棄物
処理装置において、廃棄物原料投入装置のスクリューフ
ィーダーは、円筒部分と円錐部分とから構成されて、両
部分に連続してスクリュー刃を突設し円筒部分を廃棄物
原料を一時保持するホッパー内の下部に配して、円錐部
分の先端をキルン本体側に向けて、前記ホッパーから円
錐部分の先端までのスクリュウ刃の外径側に前記外径よ
り若干大きい内径の金属製の管で覆って該金属製の管の
先端にそこからキルン本体側に向かう直管を接続して構
成するとともに、前記直管を外側から冷却する冷却器を
設けたことを特徴とする。
According to the first to third aspects of the present invention, the cylindrical body for heating the waste can directly improve the heat response due to the direct heating of the cylindrical body by the induction heating, and is optimal for the heating of the waste. It becomes possible to select a heating pattern, and it is possible to reduce the size as a whole and to improve the thermal efficiency. According to a fourth aspect of the present invention, in the waste treatment apparatus according to any one of the first to third aspects, the screw feeder of the waste material input device includes a cylindrical portion and a conical portion, A screw blade is protruded continuously from both parts, the cylindrical part is disposed at the lower part in the hopper that temporarily holds the waste material, the tip of the conical part is directed toward the kiln body side, and the tip of the conical part from the hopper The outer diameter side of the screw blade is covered with a metal pipe having an inner diameter slightly larger than the outer diameter, and a straight pipe heading toward the kiln body side is connected to the tip of the metal pipe, and A cooler for cooling the straight pipe from outside is provided.

【0008】上記構成により、冷却器を装備した部分に
スクリューフィーダーから押し込まれる廃棄物原料を充
満することにより、キルン本体からの熱分解ガスの逆流
を防止する逆止弁の働きをさせることが可能になる。ま
た、請求項5記載の発明は、請求項1ないし請求項4の
いずれかに記載の廃棄物処理装置において、スクリュー
フィーダーの先端に接続した、冷却器を有する直管の後
段に、断熱材を介してキルン本体までを繋ぐ直管を接続
し、該直管を外部から誘導加熱して、スクリューフィー
ダーから押し込まれる廃棄物原料を加熱減容する誘導加
熱コイルを設けたことを特徴とする。
[0008] With the above configuration, the portion equipped with the cooler is filled with the waste material pushed from the screw feeder, so that it can function as a check valve for preventing the backflow of the pyrolysis gas from the kiln body. become. According to a fifth aspect of the present invention, in the waste disposal apparatus according to any one of the first to fourth aspects, a heat insulating material is provided downstream of a straight pipe having a cooler connected to a tip of the screw feeder. A straight pipe is connected to the kiln body via the main pipe, and an induction heating coil is provided for inductively heating the straight pipe from the outside and heating and reducing the volume of the waste material pushed in from the screw feeder.

【0009】また、請求項6記載の発明は、請求項1な
いし請求項5のいずれかに記載の廃棄物処理装置におい
て、各誘導加熱コイルの直下の被加熱ゾーンにその部分
の温度を検出するセンサを設けて、各ゾーンの温度制御
を行うとともに、各ゾーン共所定温度を越えないように
制御することを特徴とする。上記構成により、廃棄物は
直管内で、直管に密接した状態で加熱されるので、廃棄
物への熱伝達が良く、その部分で減容化されて、後続の
減容化された廃棄物に押し出されて円筒体に搬入された
時点では1/10〜1/20に減容化された炭化物にな
っている。そのために後続の回転式円筒体では若干の加
熱と、分解ガス発生のために減容化された廃棄物の温度
を保つだけで良く円筒体の長さおよび容積を、廃棄物を
プレヒートしないで円筒体内に搬入する場合と比較し
て、小型化できて、そのための外表面積の減少に起因す
る放熱損の減少により、単位処理量当たりの総熱量が減
少して、熱効率を向上させることが可能になる。
According to a sixth aspect of the present invention, in the waste disposal apparatus according to any one of the first to fifth aspects, the temperature of the heated zone immediately below each induction heating coil is detected. A sensor is provided to control the temperature of each zone, and to control not to exceed a predetermined temperature in each zone. According to the above configuration, the waste is heated inside the straight pipe in a state close to the straight pipe, so that the heat transfer to the waste is good, and the volume is reduced at that portion, and the subsequent reduced waste is discharged. When it is extruded into a cylindrical body, it is a carbide whose volume is reduced to 1/10 to 1/20. For this reason, the subsequent rotating cylinder only needs to maintain a certain amount of heating and the temperature of the waste reduced in volume due to the generation of cracked gas, and the length and volume of the cylinder can be reduced without preheating the waste. Compared to the case of carrying into the body, it can be downsized and the heat loss due to the reduction of the outer surface area due to the reduction of the outer surface area reduces the total amount of heat per unit processing amount, making it possible to improve the thermal efficiency Become.

【0010】また、直管無いで加熱された廃棄物は後続
の廃棄物で押されてキルン本体内に搬入され、キルン本
体内に搬入された時点では前記廃棄物は炭化物になって
いるのでキルン本体の壁面に付着することが無くなる。
さらに、廃棄物の処理量、および質の変化に対しても各
ゾーンの温度を検出して予め決められた温度に制御する
ことにより、誘導加熱の特長と相まって比較的迅速に応
答することが可能になり、過加熱によるダイオキシンな
どの有害ガスの発生を抑制したり、加熱不足による円筒
体内壁への廃棄物の付着を抑制することが可能になる。
[0010] Further, the waste heated without the straight pipe is pushed by the subsequent waste and carried into the kiln main body. At the time when the waste is carried into the kiln main body, the waste is carbonized. It does not adhere to the wall surface of the main body.
In addition, by detecting the temperature of each zone and controlling it to a predetermined temperature even for changes in waste treatment volume and quality, it is possible to respond relatively quickly in combination with the characteristics of induction heating Thus, it is possible to suppress generation of harmful gases such as dioxin due to overheating, and to suppress adhesion of waste to the inner wall of the cylinder due to insufficient heating.

【0011】また、請求項7記載の発明は、請求項1な
いし請求項6のいずれかに記載の廃棄物処理装置におい
て、キルン本体に不活性ガスを導入する不活性ガス導入
手段を設けたことを特徴とする。上記構成により、廃棄
物が加熱、保温されているゾーンでは酸素濃度を減少さ
せることができるので熱分解ガスに含まれる塩素ガスな
どから有害ガスを生成するのを未然に防止することが可
能になる。
According to a seventh aspect of the present invention, in the waste disposal apparatus according to any one of the first to sixth aspects, an inert gas introducing means for introducing an inert gas into the kiln body is provided. It is characterized by. With the above configuration, the oxygen concentration can be reduced in the zone where the waste is heated and kept warm, so that it is possible to prevent the generation of harmful gas from chlorine gas or the like contained in the pyrolysis gas beforehand. .

【0012】[0012]

【発明の実施の形態】図1はこの発明の実施の形態の主
要部の構成図を示す。この図1において、1は両端に径
の大きい円筒のタイヤ1aを備え、該タイヤをそれぞれ
少なくとも2個の車輪2aがタイヤ1aの円の中心を頂
点とする三角形を形成する接点で接触してタイヤ1aを
受けて回転可能に支持するタイヤ支持装置2により回転
可能に支持されたキルン本体であり、該キルン本体1の
外周にはキルン本体1からの放熱を抑制する断熱材3が
施工されている。さらにその外周側には前記断熱材3と
の間に間隔を開けて、キルン本体1と略同芯円の軸方向
に3分割された誘導加熱コイル4a,4b,4cが配備
されている。また、該キルン本体1の上流には、廃棄物
を投入するホッパー5と、該ホッパー5の下部に装着さ
れ円筒部およびその先端に固着された円錐体に連続して
刃をスパイラルに突設したスクリューフィーダー6と、
該スクリューフィーダー6からキルン本体1に向かう直
管7と、該直管7を外側から冷却する冷却器8とを備え
た廃棄物原料投入装置9が、その先端に断熱材10を介
して取り付けられ、キルン本体1とを繋ぐ直管11とそ
の外周に配備されて該直管11を誘導加熱する誘導加熱
コイル12とを具備して装備されている。そしてキルン
本体1の下流には、該キルン本体1内で、廃棄物が熱分
解ガスと不揮発性残渣とに生成された不揮発性残渣を回
収し、熱分解ガスを次工程の排ガス処理装置へ排出する
不揮発性残渣回収室13が配備されている。また、この
不揮発性残渣回収室13に回収された不揮発性残渣は排
出フィーダー13aにより先送りされて該不揮発性残渣
回収室13の先端下部の上側ダンパ13b上に運ばれ、
ダンパ13bを開放して下ダンパ13b上に送られ、上
側のダンパ13bを閉鎖してから下側のダンパ13bを
開放して外部に排出され。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS FIG. 1 shows a configuration diagram of a main part of an embodiment of the present invention. In FIG. 1, reference numeral 1 denotes a tire provided with a large-diameter cylindrical tire 1a at each end, and at least two wheels 2a contacting each other at a contact point forming a triangle having the center of a circle of the tire 1a as an apex. A kiln body rotatably supported by a tire support device 2 rotatably receiving and supporting 1a, and a heat insulating material 3 for suppressing heat radiation from the kiln body 1 is provided on an outer periphery of the kiln body 1. . Further, on the outer peripheral side, induction heating coils 4a, 4b, 4c which are divided into three in the axial direction of a substantially concentric circle with the kiln body 1 are arranged with a space between the heat insulating material 3 and the heat insulating material 3. Further, upstream of the kiln body 1, a hopper 5 into which waste is charged, and a blade continuously projecting from a cylindrical portion attached to a lower portion of the hopper 5 and a cone fixed to the tip thereof are spirally provided. A screw feeder 6,
A waste material input device 9 having a straight pipe 7 extending from the screw feeder 6 toward the kiln body 1 and a cooler 8 for cooling the straight pipe 7 from the outside is attached to the distal end thereof through a heat insulating material 10. And a straight tube 11 connected to the kiln body 1 and an induction heating coil 12 provided on the outer periphery thereof for induction heating the straight tube 11. Downstream of the kiln body 1, the waste collects the non-volatile residue generated in the pyrolysis gas and the non-volatile residue in the kiln body 1, and discharges the pyrolysis gas to an exhaust gas treatment device in the next step. A non-volatile residue recovery chamber 13 is provided. The non-volatile residue collected in the non-volatile residue collection chamber 13 is forwarded by the discharge feeder 13a and is carried on the upper damper 13b at the lower end of the non-volatile residue collection chamber 13,
The damper 13b is opened to be fed onto the lower damper 13b, the upper damper 13b is closed, and then the lower damper 13b is opened to be discharged to the outside.

【0013】キルン本体1の誘導コイル4a,4b,4
cに対応する箇所の代表温度は温度センサ14a,14
b,14cにより検出され、キルン本体1手前の直管1
1の温度は温度センサ15で検出されてそれぞれの目標
温度に制御される。また、キルン本体1内の酸素濃度を
低下させるために不活性ガスが不活性ガス導入手段15
から導入される。
The induction coils 4a, 4b, 4 of the kiln body 1
The representative temperature at the location corresponding to c is the temperature sensor 14a, 14
b, 14c, the straight pipe 1 in front of the kiln body 1
The temperature 1 is detected by the temperature sensor 15 and controlled to each target temperature. In order to reduce the oxygen concentration in the kiln body 1, an inert gas is supplied to the inert gas introducing means 15.
Introduced from.

【0014】上記の構成において、廃棄物原料投入装置
9のホッパー5に投入された、塩化ビニール、ポリプロ
ピレン等の塩素化合物を含む廃棄物はスクリューフィー
ダー6により冷却器8をその外周に備えた直管7内に充
満するように押し込まれる。この時、スクリューフィー
ダー6の内部摩擦熱により廃棄物が加熱されて温度上昇
するが、ここでは減容化するまで加熱しないように外側
から、冷却器8により冷却して直管7内に充満した状態
で後続の廃棄物で押されて前進するようにして、この部
分からホッパー5側に熱分解ガスが逆流しないようにし
ている。そして、さらに後続の廃棄物で押し進められ
て、断熱材10を介して前方に繋がれ外周を誘導加熱す
る誘導加熱コイル12を備えた直管11内に導かれてそ
こで加熱されて容積が1/10〜1/20に減容して一
部は熱分解ガスになり、このガス圧と後続の廃棄物とに
押されてキルン本体1内に搬入される。該キルン本体1
は両端に設けたキルン本体1より径の大きいタイヤ1a
と該タイヤ1aを回転可能に支持する車輪2aを有する
タイヤ支持装置2により回転可能に支持されており、図
示されていない駆動装置により回転駆動されている。直
管11内で加熱減容化され、該キルン本体1内に搬入さ
れた廃棄物はキルン本体1の回転に伴って回転力を与え
られながら、また、キルン本体1の外周に装着された断
熱材3との間に間隔を開けて配備した誘導加熱コイル4
a,4b,4cによりキルン本体1の温度をそれぞれの
箇所で目標値になるように、温度センサ14a,14
b,14cと図示されていない制御装置とにより制御さ
れて、加熱されたキルン本体1からの熱で加熱されて熱
分解ガスと不揮発性残渣とに生成されて前進して不揮発
性残渣回収室13に回収される。
In the above construction, the waste containing a chlorine compound such as vinyl chloride or polypropylene, which has been introduced into the hopper 5 of the waste material introduction device 9, is cooled by a screw feeder 6 into a straight pipe provided with a cooler 8 on its outer periphery. It is pushed so that it may fill in 7. At this time, the waste heats up due to the internal frictional heat of the screw feeder 6, and the temperature rises. Here, the waste is cooled by the cooler 8 from the outside so as not to be heated until the volume is reduced, and the straight pipe 7 is filled. In this state, the waste is pushed forward by the following waste, so that the pyrolysis gas does not flow backward from this portion to the hopper 5 side. Then, it is further pushed by the following waste, and is led into a straight pipe 11 having an induction heating coil 12 which is connected forward through an insulating material 10 and inductively heats the outer periphery. The volume is reduced to 10 to 1/20 and partly becomes pyrolysis gas. The pyrolysis gas is pushed into the kiln body 1 by the gas pressure and subsequent waste. The kiln body 1
Is a tire 1a having a larger diameter than the kiln body 1 provided at both ends.
The tire 1a is rotatably supported by a tire support device 2 having wheels 2a rotatably supporting the tire 1a, and is rotationally driven by a drive device (not shown). The waste volume reduced by heating in the straight pipe 11 and carried into the kiln body 1 is given a rotational force in accordance with the rotation of the kiln body 1, and is provided with heat insulation attached to the outer periphery of the kiln body 1. Induction heating coil 4 arranged at a distance from material 3
a, 4b, and 4c, the temperature sensors 14a, 14b are set so that the temperature of the kiln body 1 becomes a target value at each location.
b, 14c and a control device (not shown), heated by the heat from the heated kiln main body 1 to generate a pyrolysis gas and a non-volatile residue, advance and advance to the non-volatile residue recovery chamber 13 Will be collected.

【0015】そして、不揮発性残渣は排出フィーダー1
3aにより上側のダンパ13b上に送られ、この上側の
ダンパ13bを開放して下側のダンパ13b上に送り込
んだから上側のダンパ13bを閉鎖して、キルン本体1
内に外気が進入するのを防ぎ、かつキルン本体1からの
ガスの漏洩を防いでから下側のダンパ13bを開放して
外部に排出する。
The non-volatile residue is discharged from the discharge feeder 1.
3a, the upper damper 13b is sent to the upper damper 13b, and the upper damper 13b is opened and sent to the lower damper 13b.
After the outside air is prevented from entering the inside and the gas is prevented from leaking from the kiln body 1, the lower damper 13b is opened and discharged to the outside.

【0016】なお、該不揮発性残渣回収室13には熱分
解ガスを回収して次工程の排ガス処理装置へ熱分解ガス
を排出するように配管されている。また、上記の工程で
酸素濃度を低くして熱分解ガスが有害ガスにならないよ
うに不活性ガス導入手段15からキルン本体1内に不活
性ガスが導入されている。
The non-volatile residue recovery chamber 13 is provided with a pipe so as to collect the pyrolysis gas and discharge the pyrolysis gas to an exhaust gas treatment device in the next step. In addition, an inert gas is introduced into the kiln main body 1 from the inert gas introduction means 15 so that the oxygen concentration is reduced in the above process so that the pyrolysis gas does not become a harmful gas.

【0017】[0017]

【発明の効果】この発明によれば、キルン本体を軸方向
に分割した誘導コイルにより加熱制御しているので熱応
答性が良く、廃棄物の量、および質の変化によるキルン
本体壁面の温度変化に即応して、該温度変化を少なくす
るように制御できるので廃棄物の量、および質の変化に
よるキルン本体壁面の極度な温度降下に起因する廃棄物
の付着により後続の廃棄物が前記付着した廃棄物に重な
り、キルン本体壁面からの熱伝達が不足して後続の廃棄
物が加熱不足になるのを未然に防止でき、その分余分な
加熱面積を確保する必要が無くなるのでキルン本体を小
型化できる。
According to the present invention, since the heating of the kiln body is controlled by the induction coil divided in the axial direction, the thermal response is good, and the temperature change of the kiln body wall surface due to the change in the amount and quality of waste. In response to the temperature change, the temperature change can be controlled to be small, so that the amount of waste, and the waste attached due to the extreme temperature drop of the kiln body wall due to the change in quality, the subsequent waste adhered. It is possible to prevent the following waste from being underheated due to insufficient heat transfer from the kiln body wall due to overlapping with the waste, and the kiln body can be downsized because there is no need to secure an extra heating area. it can.

【0018】さらにキルン本体と廃棄物原料投入装置と
の間に配備した直管内で廃棄物原料を加熱減容化するこ
とによりキルン本体をさらに小型化して、小型化したこ
とによるキルン本体外壁の表面積の減少により、そこか
らの放熱損が減少して単位処理量当たりの消費熱量がそ
の分減少して熱効率が向上する効果がある。
Further, the size of the kiln body is further reduced by heating and reducing the volume of the waste material in a straight pipe provided between the kiln body and the waste material input device, and the surface area of the outer wall of the kiln body due to the miniaturization. As a result, the heat dissipation loss therefrom is reduced, the heat consumption per unit processing amount is reduced correspondingly, and the heat efficiency is improved.

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

【図1】この発明の実施の形態の主要部分の構成図FIG. 1 is a configuration diagram of a main part of an embodiment of the present invention.

【符号の説明】[Explanation of symbols]

1 キルン本体 1a タイヤ 2 タイヤ支持装置 2a 車輪 3 断熱材 4a,4b,4c、12 誘導加熱コイル 5 ホッパー 6 スクリュウフィーダー 7、11 直管 8 冷却器 9 廃棄物原料投入装置 10 断熱材 13 不揮発性残渣回収室 14a,14b,14c 温度センサ 15 不活性ガス導入手段 DESCRIPTION OF SYMBOLS 1 Kiln main body 1a Tire 2 Tire support device 2a Wheel 3 Heat insulating material 4a, 4b, 4c, 12 Induction heating coil 5 Hopper 6 Screw feeder 7, 11 Straight pipe 8 Cooler 9 Waste material input device 10 Heat insulating material 13 Non-volatile residue Collection chamber 14a, 14b, 14c Temperature sensor 15 Inert gas introduction means

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 FI F27B 7/32 B09B 3/00 ZAB ──────────────────────────────────────────────────続 き Continued on the front page (51) Int.Cl. 6 Identification code FI F27B 7/32 B09B 3/00 ZAB

Claims (7)

【特許請求の範囲】[Claims] 【請求項1】長手方向の両端部に配備した円筒形のタイ
ヤの下部を駆動装置のローラで回転可能に支持し、前後
段に配備する機器により内部を密閉するようにした中空
の円筒体から構成し、前段から搬入された塩素化合物を
含む廃棄物原料を内部で所定の温度に加熱保持しながら
搬送して熱分解ガスおよび不揮発性残渣を生成するキル
ン本体と、該キルン本体の前段に配備して、前記廃棄物
を前記キルン本体に搬送するスクリューフィーダーを有
する廃棄物原料投入装置と、該キルン本体を外周側から
誘導加熱する誘導加熱コイルと、前記キルン本体の後段
に配備して不揮発性残渣を回収するとともに、熱分解ガ
スを収集して後段のガス処理装置へ排出する残渣回収室
とを備えたことを特徴とする廃棄物処理装置。
1. A hollow cylindrical body in which a lower portion of a cylindrical tire provided at both ends in a longitudinal direction is rotatably supported by rollers of a driving device, and the inside thereof is hermetically sealed by devices provided at front and rear stages. A kiln body configured to transport a waste material containing a chlorine compound carried in from the preceding stage while heating and holding the waste material therein at a predetermined temperature to generate a pyrolysis gas and a non-volatile residue; and disposed at a preceding stage of the kiln body. A waste material input device having a screw feeder for transferring the waste to the kiln body, an induction heating coil for induction heating the kiln body from the outer peripheral side, and a non-volatile A waste treatment apparatus comprising: a residue collection chamber that collects the residue, collects the pyrolysis gas, and discharges the pyrolysis gas to a downstream gas treatment apparatus.
【請求項2】請求項1記載の廃棄物処理装置において、
キルン本体を誘導加熱する誘導加熱コイルはキルンの軸
方向に複数個に分割して各誘導加熱コイルを個別に出力
制御できるようにしたことを特徴とする廃棄物処理装
置。
2. The waste disposal apparatus according to claim 1,
A waste treatment apparatus, wherein an induction heating coil for induction heating a kiln body is divided into a plurality of pieces in an axial direction of the kiln so that output of each induction heating coil can be individually controlled.
【請求項3】請求項1または請求項2に記載の廃棄物処
理装置において、前記複数個に分割した誘導加熱コイル
はキルン入り口側を後段の出力よりも高出力としたこと
を特徴とする廃棄物処理装置。
3. The waste treatment apparatus according to claim 1, wherein the induction heating coil divided into a plurality of units has a kiln entrance side with a higher output than a subsequent stage output. Object processing equipment.
【請求項4】請求項1ないし請求項3のいずれかに記載
の廃棄物処理装置において、廃棄物原料投入装置のスク
リューフィーダーは、円筒部分と円錐部分とから構成さ
れて、両部分に連続してスクリュー刃を突設し円筒部分
を廃棄物原料を一時保持するホッパー内の下部に配し
て、円錐部分の先端をキルン本体側に向けて、前記ホッ
パーから円錐部分の先端までのスクリュウ刃の外径側に
前記外径より若干大きい内径の金属製の管で覆って該金
属製の管の先端にそこからキルン本体側に向かう直管を
接続して構成するとともに、前記直管を外側から冷却す
る冷却器を設けたことを特徴とする廃棄物処理装置。
4. The waste treatment apparatus according to claim 1, wherein the screw feeder of the waste material input device is composed of a cylindrical portion and a conical portion, and is continuous with both portions. The screw blade is protruded and the cylindrical part is disposed in the lower part of the hopper that temporarily holds the waste material.The tip of the conical part is directed toward the kiln body, and the screw blade from the hopper to the tip of the conical part is screwed. The outer diameter side is covered with a metal pipe having an inner diameter slightly larger than the outer diameter, and a straight pipe heading toward the kiln body side is connected to the tip of the metal pipe. A waste treatment device comprising a cooler for cooling.
【請求項5】請求項1ないし請求項4のいずれかに記載
の廃棄物処理装置において、スクリューフィーダーの先
端に接続した、冷却器を有する直管の後段に、断熱材を
介してキルン本体までを繋ぐ直管を接続し、該直管を外
部から誘導加熱して、スクリューフィーダーから押し込
まれる廃棄物原料を加熱減容する誘導加熱コイルを設け
たことを特徴とする廃棄物処理装置。
5. A waste treatment apparatus according to claim 1, wherein the kiln body is connected to the tip of the screw feeder through a heat insulating material at a stage subsequent to a straight pipe having a cooler. A waste treatment apparatus comprising: an induction heating coil for connecting a straight pipe connecting the pipes, inductively heating the straight pipe from the outside, and heating and reducing the volume of the waste material pushed in from the screw feeder.
【請求項6】請求項1ないし請求項5のいずれかに記載
の廃棄物処理装置において、各誘導加熱コイルの直下の
被加熱ゾーンにその部分の温度を検出するセンサを設け
て、各ゾーンの温度制御を行うとともに、各ゾーン共所
定温度を越えないように制御することを特徴とする廃棄
物処理装置。
6. A waste treatment apparatus according to claim 1, wherein a sensor for detecting the temperature of the heated zone immediately below each induction heating coil is provided, and a sensor is provided for each zone. A waste treatment apparatus which performs temperature control and controls so that each zone does not exceed a predetermined temperature.
【請求項7】請求項1ないし請求項6のいずれかに記載
の廃棄物処理装置において、キルン本体に不活性ガスを
導入する不活性ガス導入手段を設けたことを特徴とする
廃棄物処理装置。
7. The waste treatment apparatus according to claim 1, further comprising an inert gas introduction means for introducing an inert gas into the kiln body. .
JP10036915A 1998-02-19 1998-02-19 Waste treatment apparatus Withdrawn JPH11226542A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10036915A JPH11226542A (en) 1998-02-19 1998-02-19 Waste treatment apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10036915A JPH11226542A (en) 1998-02-19 1998-02-19 Waste treatment apparatus

Publications (1)

Publication Number Publication Date
JPH11226542A true JPH11226542A (en) 1999-08-24

Family

ID=12483077

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10036915A Withdrawn JPH11226542A (en) 1998-02-19 1998-02-19 Waste treatment apparatus

Country Status (1)

Country Link
JP (1) JPH11226542A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1280382A2 (en) * 2001-07-23 2003-01-29 Ken Kansa High-frequency induction heating device and device and method for pyrolyzing organic compounds using said heating device
JP2007132552A (en) * 2005-11-08 2007-05-31 Kyudenko Corp Heating device for waste gypsum
JP2008128492A (en) * 2006-11-16 2008-06-05 Takasago Ind Co Ltd External heating-type rotary kiln and screw feeder
JP2013103998A (en) * 2011-11-14 2013-05-30 Tossmic Kk Waste plastic catalytic cracking liquefaction apparatus and catalytic cracking liquefaction method
KR101277756B1 (en) * 2012-02-15 2013-06-24 전한수 Plant for resource recovery from macromolecule waste

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1280382A2 (en) * 2001-07-23 2003-01-29 Ken Kansa High-frequency induction heating device and device and method for pyrolyzing organic compounds using said heating device
US6787742B2 (en) * 2001-07-23 2004-09-07 Ken Kansa High-frequency induction heating device
EP1280382A3 (en) * 2001-07-23 2006-04-05 Ken Kansa High-frequency induction heating device and device and method for pyrolyzing organic compounds using said heating device
JP2007132552A (en) * 2005-11-08 2007-05-31 Kyudenko Corp Heating device for waste gypsum
JP2008128492A (en) * 2006-11-16 2008-06-05 Takasago Ind Co Ltd External heating-type rotary kiln and screw feeder
JP2013103998A (en) * 2011-11-14 2013-05-30 Tossmic Kk Waste plastic catalytic cracking liquefaction apparatus and catalytic cracking liquefaction method
KR101277756B1 (en) * 2012-02-15 2013-06-24 전한수 Plant for resource recovery from macromolecule waste

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