JPH09170738A - Waste supplying device in waste treating device - Google Patents

Waste supplying device in waste treating device

Info

Publication number
JPH09170738A
JPH09170738A JP7330294A JP33029495A JPH09170738A JP H09170738 A JPH09170738 A JP H09170738A JP 7330294 A JP7330294 A JP 7330294A JP 33029495 A JP33029495 A JP 33029495A JP H09170738 A JPH09170738 A JP H09170738A
Authority
JP
Japan
Prior art keywords
waste
cylindrical body
supplied
sliding member
supply
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
JP7330294A
Other languages
Japanese (ja)
Inventor
Hiroaki Harada
裕昭 原田
Takashi Ono
孝 大野
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.)
Mitsui Engineering and Shipbuilding Co Ltd
Original Assignee
Mitsui Engineering and Shipbuilding 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 Mitsui Engineering and Shipbuilding Co Ltd filed Critical Mitsui Engineering and Shipbuilding Co Ltd
Priority to JP7330294A priority Critical patent/JPH09170738A/en
Publication of JPH09170738A publication Critical patent/JPH09170738A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E20/00Combustion technologies with mitigation potential
    • Y02E20/12Heat utilisation in combustion or incineration of waste
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/30Fuel from waste, e.g. synthetic alcohol or diesel

Landscapes

  • Gasification And Melting Of Waste (AREA)
  • Processing Of Solid Wastes (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a device capable of retaining the sealing property of a waste supplying unit for a pyrolytic reactor. SOLUTION: This device is constituted so that waste is supplied into a pyrolytic reactor 1 through a supplying device 7 to produce distillated gas and pyrolytic residue, consisting principally of a non-volatile constituent, through thermal decomposition by heating the waste under an atmospheric pressure, then, the distillated gas is separated from the pyrolytic residue and the pyrolytic residue is supplied to a separating device to separate it into combustible constituent and non-combustible constituent while the combustible constituent and the distillated gas are supplied into a melting furnace. In this case, the supplying device 7 is constituted of a cylindrical body 24, having a discharging port 22, whose one end is opened in the pyrolytic reactor 1 and the other end is provided with a waste supplying port 23, a sliding member 25, sliding in the cylindrical body 24, and a driving device 26 while the waste, supplied from the supplying port 23 to the cylindrical body 24, is pushed and shifted toward the discharging port 22 side of the cylindrical body 24.

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、廃棄物処理装置に
おける廃棄物供給装置、より詳しくは廃棄物を熱分解し
て得た熱分解生成物を溶融炉で燃焼するようにした廃棄
物処理装置における廃棄物供給装置に関するものであ
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a waste supply device in a waste treatment device, and more particularly to a waste treatment device in which a pyrolysis product obtained by thermally decomposing waste is burned in a melting furnace. Related to the waste supply device.

【0002】[0002]

【従来の技術】都市ごみなどの一般廃棄物や廃プラスチ
ックなどの可燃物を含む産業廃棄物の処理装置の一つと
して、廃棄物を供給装置により熱分解反応器に供給
し、大気圧下の低酸素雰囲気において加熱し、乾留ガス
と主として不揮発性分からなる熱分解残留物とを生成
し、この熱分解残留物を冷却したのち分離装置に導
き、この分離装置において燃焼成分及び灰分と例えば金
属や陶器、砂利、コンクリート片等のガレキよりなる不
燃焼成分とに分離し燃焼成分を粉砕し、この粉砕され
た燃焼成分と前記乾留ガスとを燃焼器である溶融炉に導
き、この溶融炉で燃焼させ、生じた燃焼灰を溶融スラグ
となし、この溶融スラグを排出して冷却固化させるよう
にした廃棄物処理装置が、例えば特開平1−9816号
公報で知られている。
2. Description of the Related Art As one of the treatment devices for general waste such as municipal solid waste and industrial waste including combustible substances such as waste plastic, the waste is supplied to a pyrolysis reactor by a supply device and is kept under atmospheric pressure. It is heated in a low oxygen atmosphere to generate a dry distillation gas and a thermal decomposition residue mainly consisting of non-volatile components, and after cooling this thermal decomposition residue, it is introduced into a separation device, in which the combustion component and ash content, such as metal and Separated into non-combustible components composed of debris such as earthenware, gravel, and concrete pieces, pulverize the combusted components, guide the pulverized combusted components and the dry distillation gas to a melting furnace that is a combustor, and burn in the melting furnace. For example, Japanese Patent Laid-Open No. 1-9816 discloses a waste treatment apparatus in which the generated combustion ash is formed into a molten slag, and the molten slag is discharged to be cooled and solidified.

【0003】このこの種の廃棄物処理装置において熱分
解反応器に廃棄物を供給する場合にスクリューフィーダ
が使用されている。即ち、図4に示されるように熱分解
反応器1に、一端が開口する排出口2を有し、他端側に
供給口3を有するケーシング4内にスクリュー軸に取付
けられたスクリュー5を配置したスクリューフィーダ6
を配置し、供給口3からケーシング4内に供給された廃
棄物aはスクリュー5により圧密状態に押圧されながら
排出口2から熱分解反応器1内に供給するようになって
いる。このとき廃棄物aが圧密状態に押圧されているた
め熱分解反応器1とケーシング4との接続部におけるシ
ールが保持され、この熱分解反応器1内は大気圧下に保
たれるのである。
In this type of waste treatment apparatus, a screw feeder is used when supplying waste to the pyrolysis reactor. That is, as shown in FIG. 4, in the thermal decomposition reactor 1, a screw 5 attached to a screw shaft is arranged in a casing 4 having a discharge port 2 having one end opened and a supply port 3 on the other end side. Screw feeder 6
The waste a supplied from the supply port 3 into the casing 4 is supplied into the thermal decomposition reactor 1 from the discharge port 2 while being pressed in a compacted state by the screw 5. At this time, since the waste a is pressed in a compacted state, the seal at the connecting portion between the thermal decomposition reactor 1 and the casing 4 is maintained, and the inside of the thermal decomposition reactor 1 is kept under atmospheric pressure.

【0004】[0004]

【発明が解決しようとする課題】ところで前記構造の廃
棄物供給装置を有する廃棄物処理装置において、廃棄物
が多量となり、それに応じて装置が大型化してくると、
必然的にスクリューフィーダ6も大型化する。即ち、ケ
ーシング4も大径化するため、このケーシング4に対し
て回転する熱分解反応器1と前記ケーシング4との間に
配置されるシール機構が複雑化する。
By the way, in the waste treatment apparatus having the waste supply apparatus of the above structure, when the amount of waste becomes large and the apparatus becomes large accordingly,
Inevitably, the screw feeder 6 also becomes larger. That is, since the diameter of the casing 4 is also increased, the sealing mechanism arranged between the pyrolysis reactor 1 rotating with respect to the casing 4 and the casing 4 becomes complicated.

【0005】このようなシール機構上に問題点があるこ
とから、スクリューフィーダ6のケーシングを小径化し
てこの多量の廃棄物を供給しようとすると、回転数を増
大するか、又はスクリューのピッチを増大させることと
なるが、前者においてはスクリューの摩耗が大となり耐
久性が低下する。一方、後者においては廃棄物がスクリ
ュー5と一体となって回転する、所謂共廻り現象が生じ
やすくなり廃棄物を供給することができなくなる恐れが
生ずるという問題がある。
Due to such a problem in the sealing mechanism, if the casing of the screw feeder 6 is made smaller in diameter to supply this large amount of waste, the number of revolutions is increased or the pitch of the screws is increased. However, in the former case, the abrasion of the screw is large and the durability is reduced. On the other hand, in the latter case, there is a problem that the waste rotates together with the screw 5, that is, a so-called co-rotation phenomenon is likely to occur and the waste cannot be supplied.

【0006】[0006]

【課題を解決するための手段】本発明は前記従来技術の
問題点を解決するためになされたものであって、廃棄物
を供給装置により熱分解反応器に供給し、この熱分解反
応器内を大気圧下にして前記廃棄物を加熱して熱分解
し、乾留ガスと主として不揮発性分からなる熱分解残留
物とを生成し、前記乾留ガスと熱分解残留物とを分離
し、熱分解残留物を分離装置に供給して燃焼成分と不燃
焼線分とに分離し、燃焼成分と前記乾留ガスとを溶融炉
に供給をするようにした廃棄物処理装置において、前記
供給装置を一端が前記熱分解反応器内に開口する排出口
を有し他端に廃棄物供給口を設けた筒体と、この筒体内
を摺動する摺動部材と、この摺動部材を駆動する駆動装
置とよりなり、前記供給口から前記筒体内に供給された
廃棄物を前記筒体の排出口側へ押圧移送するようにした
廃棄物処理装置における廃棄物供給装置を提供するもの
である。
The present invention has been made to solve the above-mentioned problems of the prior art, in which waste is supplied to a thermal decomposition reactor by a supply device, and Under atmospheric pressure to thermally decompose the waste to generate a dry distillation gas and a thermal decomposition residue mainly consisting of non-volatile components, separate the dry distillation gas and the thermal decomposition residue, and decompose the thermal decomposition residue. In a waste treatment device in which a substance is supplied to a separation device to be separated into a combustion component and a non-combustion line segment, and a combustion component and the dry distillation gas are supplied to a melting furnace, one end of the supply device is A tubular body having a discharge port opened in the pyrolysis reactor and a waste supply port provided at the other end, a sliding member that slides in the tubular body, and a drive device that drives the sliding member. Therefore, the waste material supplied from the supply port into the cylinder is discharged from the cylinder. There is provided a waste feed device in the waste disposal apparatus designed to push transferred to the mouth side.

【0007】そして好ましくは、摺動部材はその先端が
筒体に設けられた供給口を開放可能な位置から筒体の排
出口より所定の間隔を置いた供給口側の位置間において
摺動可能であって、かつその先端が排出口側端部に達し
たとき前記供給口を閉鎖可能な如く構成される。前記の
ように構成された廃棄物処理装置における廃棄物供給装
置によれば、供給口から筒体内に供給された廃棄物は摺
動部材により押圧されて圧密状態となり排出口側へ移送
される。
[0007] Preferably, the sliding member is slidable between the position at which the tip of the sliding member can open the supply port provided in the cylindrical body and the position on the supply port side at a predetermined distance from the discharge port of the cylindrical body. In addition, the supply port can be closed when its tip reaches the end on the discharge port side. According to the waste supply device in the waste treatment device configured as described above, the waste supplied from the supply port into the cylindrical body is pressed by the sliding member to be in a consolidated state and transferred to the discharge port side.

【0008】そして排出口端部においてこの廃棄物は圧
密状態となってこの排出口を閉鎖しシール作用をなし熱
分解反応器内の大気圧下の状態を保持する。そして次に
摺動部材により移送されてくる廃棄物により押圧され排
出口から熱分解反応器内に供給されるのである。
At the end of the discharge port, the waste material is in a compacted state, and the discharge port is closed to perform a sealing action and maintain the state under atmospheric pressure in the thermal decomposition reactor. Then, it is pressed by the waste material transferred by the sliding member and is supplied from the discharge port into the thermal decomposition reactor.

【0009】[0009]

【発明の実施の形態】以下、図1ないし図3を参照して
本発明による廃棄物処理装置における廃棄物供給装置の
実施例を説明する。図1において7は廃棄物供給装置
で、この廃棄物供給装置により廃棄物aは熱分解反応器
1内に供給される。この熱分解反応器1は通常横型回転
式ドラムが用いられ、図示しないシール機構によりシー
ルされるとともに、煙突19の近傍に設けた誘引送風機8
により内部は誘引され大気圧下(負圧)となるようにな
っている。
BEST MODE FOR CARRYING OUT THE INVENTION Embodiments of a waste supply device in a waste treatment device according to the present invention will be described below with reference to FIGS. In FIG. 1, 7 is a waste supply device, and the waste a is supplied into the thermal decomposition reactor 1 by this waste supply device. A horizontal rotary drum is normally used for the thermal decomposition reactor 1, and the induction blower 8 provided near the chimney 19 is sealed by a sealing mechanism (not shown).
Due to this, the inside is attracted and becomes under atmospheric pressure (negative pressure).

【0010】そしてこの熱分解反応器1は、熱交換器9
からラインL1 を経て供給された加熱空気bにより30
0℃〜600℃に、通常は450℃程度に加熱され供給
された廃棄物aは熱分解され、乾留ガスG1 と主として
不揮発性の熱分解残留物cとが生成される。そしてこの
乾留ガスG1 と熱分解残留物cとは排出装置10により
分離され、乾留ガスG1 はラインL2 を経て燃焼器を構
成している溶融炉11のバーナ12に供給される。
The thermal decomposition reactor 1 is composed of a heat exchanger 9
The heated air b supplied via line L 1 from 30
The waste a supplied after being heated to 0 ° C. to 600 ° C., ordinarily about 450 ° C., is thermally decomposed, and a dry distillation gas G 1 and mainly non-volatile thermal decomposition residue c are generated. Then, the dry distillation gas G 1 and the thermal decomposition residue c are separated by the discharge device 10, and the dry distillation gas G 1 is supplied to the burner 12 of the melting furnace 11 constituting the combustor via the line L 2 .

【0011】一方、排出装置10より排出された熱分解
残留物cは、冷却装置を有する分離装置13に供給され
る。この分離装置13は、例えば5mm、2mm、1mm程度
の複数段の篩装置が配置されて構成され、熱分解残留物
c中に存在する主として粗大な不燃焼成分d、即ち、金
属やガレキなどが分離除去される。そしてこの分離装置
13で分離された比較的微細な粒子よりなる燃焼成分e
は粉砕機14により、好ましくは1mm以下の微粉よりな
る燃焼成分e′とされ、この燃焼成分e′はラインL3
を経由して直接に、又は図示しない貯蔵装置を経て前記
溶融炉11のバーナ12に供給される。
On the other hand, the thermal decomposition residue c discharged from the discharging device 10 is supplied to the separating device 13 having a cooling device. This separating device 13 is constituted by arranging a plurality of stages of sieving devices of, for example, 5 mm, 2 mm, and 1 mm, and mainly coarse non-combustible components d existing in the pyrolysis residue c, that is, metal and rubble, etc. Separated and removed. The combustion component e composed of relatively fine particles separated by the separator 13
The grinder 14 is preferably 'is a, the combustion component e' combustion component e which consists of the following fine 1mm the line L 3
Is directly supplied to the burner 12 of the melting furnace 11 via a storage device (not shown).

【0012】そしてラインL2 を経由して供給された乾
留ガスG1 と、ラインL3 を経由して供給された燃焼成
分e’と、送風機15とラインL4 を経由して供給され
た燃焼用空気fとは、バーナ12を通じて溶融炉11内
に混合して供給され、この溶融炉11内で約1,300
℃の高温で燃焼され、このとき生じた燃焼灰は溶融スラ
グhとなって水槽16中に落下して冷却固化する。な
お、この冷却固化されたスラグは舗装材等の建材として
利用される。
The dry distillation gas G 1 supplied via the line L 2 , the combustion component e'supplied via the line L 3 , and the combustion supplied via the blower 15 and the line L 4 The working air f is mixed and supplied into the melting furnace 11 through the burner 12, and in the melting furnace 11, about 1,300
Combustion is performed at a high temperature of ° C, and the combustion ash generated at this time becomes molten slag h and falls into the water tank 16 to be cooled and solidified. The cooled and solidified slag is used as a building material such as a pavement material.

【0013】前記溶融炉11内の燃焼ガスG3 はライン
5 を経由して熱交換器9、廃熱ボイラ17及び集塵装
置18a,18bにより熱回収及び除塵され、比較的低
温のクリーンな燃焼ガスG3 となって誘引送風機8によ
り誘引され、煙突19から大気中に放出される。集塵器
18bの吐出側に連結されたラインL6 は、燃焼ガスG
3 の一部を前記分離装置13、具体的には分離装置13
中に組込まれた冷却装置に供給するラインである。ま
た、溶融炉11の後段に配置されている廃熱ボイラ17
によって熱回収して発生した蒸気sによって蒸気タービ
ン21を作動し、これによって発電機20を駆動して廃
熱を電力として回収するようになっている。
The combustion gas G 3 in the melting furnace 11 is recovered and dust-removed by the heat exchanger 9, the waste heat boiler 17 and the dust collectors 18a and 18b via a line L 5 , and a relatively low temperature and clean. It becomes combustion gas G 3 and is attracted by the induced air blower 8 and discharged from the chimney 19 into the atmosphere. The line L 6 connected to the discharge side of the dust collector 18b is the combustion gas G
Part of 3 is the separating device 13, specifically, the separating device 13
It is a line that supplies the cooling device built in. In addition, the waste heat boiler 17 disposed in the latter stage of the melting furnace 11
The steam turbine 21 is operated by the steam s generated by recovering the heat, and thereby the generator 20 is driven to recover the waste heat as electric power.

【0014】廃棄物の供給装置7は、図2に示されるよ
うに一端が熱分解反応器1内に開口した排出口22を有
し、他端に廃棄物供給口23を設けた筒体24(シリン
ダー)と、この筒体24内に摺動部材25(押圧体ある
いはプランジャ)が矢印A−A′方向に摺動可能な如く
挿入され、駆動装置である空気圧又は油圧を利用した流
体シリンダー26により駆動されるようになっている。
As shown in FIG. 2, the waste supply device 7 has a cylindrical body 24 having a discharge port 22 having one end opened into the thermal decomposition reactor 1 and a waste supply port 23 provided at the other end. A (cylinder) and a sliding member 25 (pressing body or plunger) are inserted into the cylindrical body 24 so as to be slidable in the direction of the arrow AA ', and a fluid cylinder 26 that uses air pressure or hydraulic pressure as a drive device. It is designed to be driven by.

【0015】なお、前記筒体24は廃棄物aを押圧しな
がら移送する案内筒となるものであるから、円筒状か又
は角筒状の何れのものでも使用できるが、実際には円筒
状のものが良好である。摺動部材25の先端25aは、
筒体24に設けられた廃棄物供給口23を開放できる位
置Bから、排出口20より、排出口22の端部から所定
の間隔Lを有する位置Cとの間の移動距離Dの範囲で摺
動可能なように構成されている。
Since the cylindrical body 24 serves as a guide cylinder for transferring the waste a while pressing it, either a cylindrical shape or a rectangular cylindrical shape can be used, but in reality, it is a cylindrical shape. Things are good. The tip 25a of the sliding member 25 is
In the range of the moving distance D from the position B where the waste supply port 23 provided in the cylindrical body 24 can be opened to the position C having a predetermined distance L from the end of the discharge port 22 through the discharge port 20. It is configured to be movable.

【0016】そしてこの摺動部材25は筒体24と同一
の断面形状を有している。なお、27は筒体25の排出
口22側の所定の位置Cの近傍に設けられた放出管28
に取付けられた逆止弁であり、筒体24内が加圧状態に
なると放圧するようになっている。前記のように構成さ
れた廃棄物供給装置7において、図3(a)に示される
ように摺動部材25をあらかじめ廃棄物供給口23が完
全に開放するまで矢印A方向に摺動させた後、廃棄物a
を廃棄物供給口23から筒体24内に供給する。
The sliding member 25 has the same sectional shape as the cylindrical body 24. Incidentally, 27 is a discharge pipe 28 provided near the predetermined position C on the discharge port 22 side of the tubular body 25.
Is a check valve attached to the cylinder 24 and releases pressure when the inside of the cylindrical body 24 is in a pressurized state. In the waste supply device 7 configured as described above, after sliding the sliding member 25 in the direction of arrow A in advance until the waste supply port 23 is completely opened, as shown in FIG. , Waste a
Is supplied from the waste supply port 23 into the cylindrical body 24.

【0017】そして図3(b)に示すように流体シリン
ダー26を作動させて筒体24内に充填された廃棄物a
を押圧しながら、摺動部材25を矢印A′方向に摺動さ
せる。このとき廃棄物aはその圧密の程度が順次高めら
れる。そしてこの摺動部材25の先端25aが所定の位
置Cまで達すると、筒体24の排出口22は、この筒体
24内で圧縮された廃棄物a′が一種の詰め物となって
シールされる。なお、このとき摺動部材25の後端部2
5bは図3(b)に示すように廃棄物供給口23を同時
に閉鎖するようになっている。
Then, as shown in FIG. 3 (b), the fluid cylinder 26 is actuated so that the waste a filled in the cylinder 24 is discharged.
While pressing, the sliding member 25 is slid in the arrow A'direction. At this time, the degree of compaction of the waste a is gradually increased. When the tip 25a of the sliding member 25 reaches a predetermined position C, the discharge port 22 of the tubular body 24 is sealed with the waste a'compressed in the tubular body 24 as a kind of stuffing. . At this time, the rear end portion 2 of the sliding member 25
5b is adapted to simultaneously close the waste supply port 23 as shown in FIG. 3 (b).

【0018】然る後、再度摺動部材25を矢印A方向に
引いて廃棄物供給口23から筒体24内に廃棄物aを供
給し、そして摺動部材25を図3(c)に示すように、
矢印A′方向に摺動させ、これにより形成された圧密状
態の廃棄物a″により先に圧密状態になっている廃棄物
a′を熱分解反応器1内に供給するのである。つまり、
廃棄物aはブロック状の廃棄物a’となって筒体24の
端部の排出口22の近傍を閉止し、次のブロック状の廃
棄物a″を利用して前の廃棄物a’を送り出して熱分解
反応器1内に供給するのである。
After that, the sliding member 25 is again pulled in the direction of arrow A to supply the waste a into the cylindrical body 24 through the waste supply port 23, and the sliding member 25 is shown in FIG. 3 (c). like,
The sludge is slid in the direction of the arrow A ', and the waste a'consolidated by the compact waste a'formed thereby is fed into the thermal decomposition reactor 1 in the following manner.
The waste a becomes a block-shaped waste a ′ and closes the vicinity of the discharge port 22 at the end of the cylindrical body 24, and the next block-shaped waste a ″ is used to remove the previous waste a ′. It is sent out and supplied into the thermal decomposition reactor 1.

【0019】なお、このとき始めに圧密状態にした廃棄
物a′と次に移送され、シール部材となる廃棄物a″と
の間の空気は圧縮されるが、この圧力が所定以上になる
と図3(a)に示した逆止弁27が自動的に開放され、
放出管28からこの圧縮空気は大気へ放出されるのであ
る。
At this time, the air between the waste a'compressed first and the waste a'which is transferred next and becomes the sealing member is compressed, but when this pressure exceeds a predetermined value, The check valve 27 shown in 3 (a) is automatically opened,
This compressed air is discharged from the discharge pipe 28 to the atmosphere.

【0020】[0020]

【発明の効果】以上の説明から明らかなように、本発明
による廃棄物処理装置における廃棄物供給装置によれ
ば、筒体24内に供給された廃棄物aを、この筒体24
内を摺動する摺動部材25の先端部で押圧して熱分解反
応器1内に供給するように構成しているため、摩耗の少
ない、かつ確実に廃棄物aを熱分解反応器1内に供給す
ることができる装置であり、特に大型で多量の廃棄物a
を供給する場合にその効果は特に大となる。
As is apparent from the above description, according to the waste material supply device in the waste material treatment apparatus of the present invention, the waste material a supplied into the cylindrical body 24 is transferred to the cylindrical body 24.
Since the tip of the sliding member 25 that slides inside is pressed and supplied into the thermal decomposition reactor 1, the waste a is less worn and the waste a is reliably stored inside the thermal decomposition reactor 1. It is a device that can supply a large amount of waste a.
The effect is particularly large when the above is supplied.

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

【図1】本発明の実施の形態を示す廃棄物供給装置を装
備した廃棄物処理装置の系統図である。
FIG. 1 is a system diagram of a waste treatment device equipped with a waste supply device showing an embodiment of the present invention.

【図2】本発明による廃棄物供給装置の側面図である。FIG. 2 is a side view of the waste supply device according to the present invention.

【図3】(a)〜(c)は本発明による廃棄物供給装置
の作用説明図である。
3 (a) to 3 (c) are explanatory views of the operation of the waste material supply device according to the present invention.

【図4】従来の廃棄物供給装置の側面図である。FIG. 4 is a side view of a conventional waste supply device.

【符号の説明】[Explanation of symbols]

1 熱分解反応器 2,22 排
出口 3 供給口 4 ケ
ーシング 5 スクリュー 6 ス
クリューフィーダ 7 廃棄物供給装置 8 誘
引送風機 9 熱交換器 10 排
出装置 11 溶融炉 12 バ
ーナ 13 分離装置 14 粉
砕機 15 送風機 16 水
槽 17 排熱ボイラ 18a,18b
集塵器 19 煙突 20 発
電機 21 スチームタービン 23 廃
棄物供給口 24 筒体 25 摺
動部材 26 流体シリンダー 27 逆
止弁 28 放出管
1 Thermal Decomposition Reactor 2,22 Discharge Port 3 Supply Port 4 Casing 5 Screw 6 Screw Feeder 7 Waste Feeding Device 8 Induction Blower 9 Heat Exchanger 10 Discharging Device 11 Melting Furnace 12 Burner 13 Separator 15 Blower 16 Water Tank 17 Exhaust heat boiler 18a, 18b
Dust collector 19 Chimney 20 Generator 21 Steam turbine 23 Waste supply port 24 Cylindrical body 25 Sliding member 26 Fluid cylinder 27 Check valve 28 Discharge pipe

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 廃棄物を供給装置により熱分解反応器に
供給し、この熱分解反応器内を大気圧下にして前記廃棄
物を加熱して熱分解し、乾留ガスと主として不揮発性分
からなる熱分解残留物とを生成し、前記乾留ガスと熱分
解残留物とを分離し、熱分解残留物を分離装置に供給し
て燃焼成分と不燃焼線分とに分離し、燃焼成分と前記乾
留ガスとを溶融炉に供給するようにした廃棄物処理装置
において、 前記供給装置を一端に前記熱分解反応器内に開口する排
出口と、他端に廃棄物供給口を設けた筒体と、この筒体
内を摺動する摺動部材と、この摺動部材を駆動する駆動
装置とよりなり、前記供給口から前記筒体内に供給され
た廃棄物を前記筒体の排出口側へ押圧移送するようにし
た廃棄物処理装置における廃棄物供給装置。
1. Waste is supplied to a thermal decomposition reactor by a supply device, and the inside of this thermal decomposition reactor is heated to atmospheric pressure to heat and decompose the waste, which is composed of dry distillation gas and mainly non-volatile components. Pyrolysis residue is generated, the carbonization gas and the pyrolysis residue are separated, the pyrolysis residue is supplied to a separation device to separate into a combustion component and a non-combustion line segment, and the combustion component and the carbonization residue are separated. In a waste treatment device adapted to supply gas to a melting furnace, an outlet opening into the pyrolysis reactor at one end of the supply device, and a cylinder provided with a waste supply port at the other end, It is composed of a sliding member that slides in the cylindrical body and a drive device that drives the sliding member, and presses and transfers the waste supplied from the supply port into the cylindrical body to the discharge port side of the cylindrical body. Waste supply device in the waste treatment device.
【請求項2】 供給装置の摺動部材を駆動する装置は、
空気圧又は油圧よりなる流体圧を作用させるシリンダー
機構よりなる請求項1記載の駆動装置。
2. The device for driving the sliding member of the supply device comprises:
2. The drive device according to claim 1, comprising a cylinder mechanism that exerts a fluid pressure of pneumatic pressure or hydraulic pressure.
【請求項3】 摺動部材は、その先端が筒体に設けられ
た供給口を開放可能な位置から筒体の排出口より所定の
間隔を置いた供給口側の位置間において摺動可能であっ
て、かつその先端が排出口側端部に達したとき前記供給
口を閉鎖可能な如く構成された請求項1記載の廃棄物処
理装置における廃棄物供給装置。
3. The sliding member is slidable between a position at which a tip of the sliding member can open a supply port provided in the cylindrical body and a position on the supply port side which is spaced a predetermined distance from the discharge port of the cylindrical body. The waste supply device for a waste treatment device according to claim 1, wherein the supply port is configured to be closed when the tip thereof reaches the end portion on the discharge port side.
JP7330294A 1995-12-19 1995-12-19 Waste supplying device in waste treating device Pending JPH09170738A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7330294A JPH09170738A (en) 1995-12-19 1995-12-19 Waste supplying device in waste treating device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7330294A JPH09170738A (en) 1995-12-19 1995-12-19 Waste supplying device in waste treating device

Publications (1)

Publication Number Publication Date
JPH09170738A true JPH09170738A (en) 1997-06-30

Family

ID=18231048

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7330294A Pending JPH09170738A (en) 1995-12-19 1995-12-19 Waste supplying device in waste treating device

Country Status (1)

Country Link
JP (1) JPH09170738A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107603647A (en) * 2017-10-20 2018-01-19 王雄鹰 A kind of horizontal biomass reacting furnace

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107603647A (en) * 2017-10-20 2018-01-19 王雄鹰 A kind of horizontal biomass reacting furnace

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