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JP3390767B2 - Waste treatment method and equipment - Google Patents
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JP3390767B2 - Waste treatment method and equipment - Google Patents

Waste treatment method and equipment

Info

Publication number
JP3390767B2
JP3390767B2 JP2000142724A JP2000142724A JP3390767B2 JP 3390767 B2 JP3390767 B2 JP 3390767B2 JP 2000142724 A JP2000142724 A JP 2000142724A JP 2000142724 A JP2000142724 A JP 2000142724A JP 3390767 B2 JP3390767 B2 JP 3390767B2
Authority
JP
Japan
Prior art keywords
waste
crushed
dried
treatment agent
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.)
Expired - Fee Related
Application number
JP2000142724A
Other languages
Japanese (ja)
Other versions
JP2001321744A (en
Inventor
弘憲 尾崎
登志夫 道本
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.)
Kawasaki Motors Ltd
Original Assignee
Kawasaki Jukogyo KK
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 Kawasaki Jukogyo KK filed Critical Kawasaki Jukogyo KK
Priority to JP2000142724A priority Critical patent/JP3390767B2/en
Publication of JP2001321744A publication Critical patent/JP2001321744A/en
Application granted granted Critical
Publication of JP3390767B2 publication Critical patent/JP3390767B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related 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
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/30Fuel from waste, e.g. synthetic alcohol or diesel

Landscapes

  • Processing Of Solid Wastes (AREA)
  • Solid Fuels And Fuel-Associated Substances (AREA)

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、廃棄物の乾燥過程
で発生する排ガス中の有害な塩化水素(HCl)ガスを
除去して、ダイオキシン類の生成を抑制する廃棄物処理
方法及び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 treatment method and apparatus for removing harmful hydrogen chloride (HCl) gas in exhaust gas generated during the drying process of waste to suppress the production of dioxins. Is.

【0002】[0002]

【従来の技術】都市ごみ等の廃棄物を破砕し乾燥させて
固形燃料として利用する技術は、既に知られている。上
記の廃棄物中には塩素系プラスチックが含まれており、
乾燥時に塩化水素(HCl)ガスが発生する。廃棄物の
乾燥時に生ずるHClを除去する方法として、特開平7
−316572号公報には、廃棄物を乾燥機に送り酸素
濃度14%以下で350℃以下の熱風を導入し、廃棄物
を250℃以上に加熱して乾燥させ、乾燥時に発生した
HClは後段の塩化水素除去装置で石灰に吸収させて処
理する方法が開示されている。
2. Description of the Related Art Techniques for crushing waste such as municipal solid waste and drying it for use as solid fuel are already known. Chlorine plastic is contained in the above waste,
Hydrogen chloride (HCl) gas is generated during drying. As a method for removing the HCl generated when the waste is dried, Japanese Patent Laid-Open No. Hei 7-1999
In Japanese Patent No. 316572, the waste is sent to a drier, hot air having an oxygen concentration of 14% or less and 350 ° C. or less is introduced, the waste is heated to 250 ° C. or more and dried, and HCl generated during the drying is generated in the latter stage. Disclosed is a method in which lime is absorbed in a hydrogen chloride removing device and treated.

【0003】[0003]

【発明が解決しようとする課題】この公報記載の方法で
は、廃棄物が局部的に250℃以上の熱風にさらされる
ため、廃棄物中に含まれる塩素系プラスチックが分解し
有害なHClが発生し、乾燥機内で廃棄物中の有機物と
反応してダイオキシン類が発生する。したがって、後段
の塩化水素除去装置ではダイオキシン類が除去できない
という問題があった。
In the method described in this publication, since the waste is locally exposed to hot air of 250 ° C. or higher, the chlorine-based plastic contained in the waste is decomposed and harmful HCl is generated. , Dioxins are generated in the dryer by reacting with organic substances in the waste. Therefore, there is a problem that dioxins cannot be removed by the hydrogen chloride removing device in the latter stage.

【0004】本発明はこれらの問題を解決するためにな
されたもので、本発明の目的は、HClと反応するアル
カリ化合物を廃棄物と混合し、熱風による廃棄物の局部
加熱のために発生するHCl等の有害ガスを処理剤(ア
ルカリ化合物)と反応させてアルカリ塩化物とすること
により、乾燥機内でのダイオキシン類生成をなくし、さ
らには、反応処理剤を選別機で廃棄物より除去し、乾燥
排ガス中の処理剤を集塵機で捕集し排ガスと分離するよ
うにした廃棄物処理方法及び装置を提供することにあ
る。
The present invention has been made to solve these problems, and an object of the present invention is to mix an alkali compound which reacts with HCl with waste and generate local heating of the waste by hot air. By reacting a harmful gas such as HCl with a treatment agent (alkali compound) to form an alkali chloride, the generation of dioxins in the dryer is eliminated, and further, the reaction treatment agent is removed from the waste by a sorting machine, It is an object of the present invention to provide a waste treatment method and apparatus in which a treatment agent in dry exhaust gas is collected by a dust collector and separated from the exhaust gas.

【0005】[0005]

【課題を解決するための手段】上記の目的を達成するた
めに、本発明の廃棄物処理方法は、廃棄物とアルカリ化
合物からなる処理剤又はアルカリ化合物を含む処理剤と
を混合した後、この混合物を熱風を被乾燥物に直接接触
させて乾燥させる乾燥機に導入して乾燥させるととも
に、乾燥過程で発生する塩化水素ガスをアルカリ塩化物
として固定化、除去してダイオキシン類の生成を抑制す
るように構成されている(図1、図2参照)。この方法
において、廃棄物を破砕した後、破砕廃棄物とアルカリ
化合物からなる処理剤又はアルカリ化合物を含む処理剤
とを混合することが好ましい(図1、図2参照)。な
お、廃棄物を破砕する前に処理剤を添加混合してもよ
く、廃棄物破砕工程の前後の両方に処理剤を添加混合し
てもよい。
In order to achieve the above object, the waste treatment method of the present invention comprises the steps of mixing waste with a treatment agent containing an alkali compound or a treatment agent containing an alkali compound, and Directly contact the dried material with hot air from the mixture
It is configured such that it is introduced into a drier for drying and is dried, and at the same time, hydrogen chloride gas generated in the drying process is fixed and removed as an alkali chloride to suppress the generation of dioxins (FIG. 1, See FIG. 2). In this method, it is preferable to crush the waste and then mix the crushed waste with a treatment agent containing an alkali compound or a treatment agent containing an alkali compound (see FIGS. 1 and 2). The treating agent may be added and mixed before crushing the waste, or the treating agent may be added and mixed before and after the waste crushing step.

【0006】これらの方法において、乾燥機から排出さ
れる乾燥物と反応済処理剤との混合物を選別機に導入し
て、乾燥物と反応済処理剤(粗粒)とに分離することが
好ましい(図1、図2参照)。また、乾燥機から排出さ
れる乾燥排ガスと反応済処理剤との混合物を集塵機に導
入して、乾燥排ガスと反応済処理剤(細粒)とに分離す
ることが好ましい(図1、図2参照)。さらに、選別機
で分離された乾燥物を破砕した後、不燃物を分離し、不
燃物が分離された破砕物に石灰等の腐敗防止用の添加剤
を添加混合して成形する場合がある(図2参照)。これ
らの方法において、アルカリ化合物としては、Ca(O
H)2 、CaO、CaCO3 、Mg(OH)2 、Mg
O、MgCO3 及びCaMg(CO3 2 の少なくとも
いずれかの粉状体又は粒状体が用いられる。
In these methods, it is preferable to introduce a mixture of the dried product discharged from the dryer and the reacted treating agent into a sorter to separate the dried product and the reacted treating agent (coarse particles). (See FIGS. 1 and 2). Further, it is preferable to introduce a mixture of the dry exhaust gas discharged from the dryer and the reacted treatment agent into the dust collector to separate the dry exhaust gas and the reacted treatment agent (fine particles) (see FIGS. 1 and 2). ). Furthermore, after crushing the dried material separated by a sorter, the incombustible material may be separated, and the crushed material in which the incombustible material is separated may be mixed with an additive for preventing decay such as lime to be molded ( See FIG. 2). In these methods, the alkaline compound is Ca (O
H) 2 , CaO, CaCO 3 , Mg (OH) 2 , Mg
At least one of O, MgCO 3 and CaMg (CO 3 ) 2 powder or particles is used.

【0007】本発明の廃棄物処理装置は、廃棄物を破砕
するための破砕機と、破砕された廃棄物を乾燥させるた
めの熱風を被乾燥物に直接接触させて乾燥させる乾燥機
と、乾燥排ガスを除塵処理するための集塵機とを備えた
廃棄物処理装置において、破砕機の出口側の破砕廃棄物
搬送手段又は/及び破砕機の入口側の廃棄物搬送手段
に、アルカリ化合物からなる処理剤又はアルカリ化合物
を含む処理剤を添加するための処理剤添加手段を接続し
たことを特徴としている(図1、図2参照)。
The waste treatment apparatus of the present invention comprises a crusher for crushing the waste, a dryer for directly contacting the material to be dried with hot air for drying the crushed waste, and a dryer. In a waste treatment device provided with a dust collector for dedusting exhaust gas, in the crushed waste transport means on the outlet side of the crusher or / and the waste transport means on the inlet side of the crusher, a treatment agent comprising an alkali compound Alternatively, it is characterized in that a treatment agent adding means for adding a treatment agent containing an alkaline compound is connected (see FIGS. 1 and 2).

【0008】この装置において、乾燥機からの乾燥物と
反応済処理剤との混合物を乾燥物と反応済処理剤とに分
離するための選別機をさらに備えた構成とすることが好
ましい(図1、図2参照)。さらに、選別機からの乾燥
物を破砕するための破砕機と、破砕機からの破砕物から
不燃物を分離するための選別機と、選別機からの不燃物
が分離された破砕物に腐敗防止用の添加剤を添加するた
めの添加剤添加手段と、添加剤が添加された破砕物を成
形するための成形機とをさらに備えた構成とする場合も
ある(図2参照)。
It is preferable that this apparatus further comprises a selector for separating the mixture of the dried product from the dryer and the reacted treating agent into the dried product and the reacted treating agent (FIG. 1). , See FIG. 2). In addition, a crusher for crushing the dried material from the sorter, a separator for separating incombustibles from the crushed material from the crusher, and a crushed material from which the incombustibles from the separator have been separated are prevented from decaying. In some cases, the constitution may further include an additive adding means for adding an additive for use with a molding machine, and a molding machine for molding a crushed product to which the additive has been added (see FIG. 2).

【0009】[0009]

【発明の実施の形態】以下、本発明の実施の形態につい
て説明するが、本発明は下記の実施の形態に何ら限定さ
れるものではなく、適宜変更して実施することができる
ものである。図1は本発明の実施の第1形態による廃棄
物処理装置を示している。塩素系プラスチックを含む都
市ごみ等の廃棄物を破砕機10で乾燥に適する粒度まで
破砕し、この破砕物にアルカリ化合物からなる処理剤又
はアルカリ化合物を含む処理剤を添加混合したものを乾
燥機12に投入し、熱風炉14からの熱風と直接的に接
触させることにより、廃棄物中の水分を蒸発させる。熱
風の温度は250〜600℃である。
BEST MODE FOR CARRYING OUT THE INVENTION Hereinafter, embodiments of the present invention will be described. However, the present invention is not limited to the following embodiments, and can be appropriately modified and implemented. FIG. 1 shows a waste treatment device according to a first embodiment of the present invention. Waste such as municipal waste containing chlorine-based plastics is crushed by a crusher 10 to a particle size suitable for drying, and the crushed material is mixed with a treatment agent containing an alkaline compound or a treatment agent containing an alkaline compound, and the resulting mixture is dried by a dryer 12. Then, the water in the waste is evaporated by directly contacting it with the hot air from the hot air oven 14. The temperature of the hot air is 250 to 600 ° C.

【0010】処理剤は、破砕機10の下流側に添加する
のが好ましいが、破砕機10の上流側に添加してもよ
く、又は破砕機10の上流側と下流側の両方に添加して
もよい。16は廃棄物搬送手段(例えばスクリューコン
ベア、ベルトコンベア等)、18は破砕廃棄物搬送手段
(例えばスクリューコンベア、ベルトコンベア等)、2
0、22は処理剤添加手段である。処理剤としては、例
えばCa(OH)2 、CaO、CaCO3 、Mg(O
H) 2 、MgO、MgCO3 、CaMg(CO3
2 (ドロマイト)等の粉状体(〜10μm )又は粒状体
(〜2mm)が用いられる。また、破砕機10としては、
一軸あるいは二軸せん断式等が用いられる。
The treating agent is added to the downstream side of the crusher 10.
However, it may be added upstream of the crusher 10.
Or add both upstream and downstream of the crusher 10.
Good. 16 is a waste transport means (for example, screw controller)
Bear, belt conveyor, etc.), 18 is a crushing waste conveying means
(Eg screw conveyor, belt conveyor, etc.), 2
0 and 22 are processing agent adding means. Examples of treatment agents
For example Ca (OH)2, CaO, CaCO3, Mg (O
H) 2, MgO, MgCO3, CaMg (CO3)
2(Dolomite) and other powders (~ 10 μm) or particles
(~ 2 mm) is used. Moreover, as the crusher 10,
A uniaxial or biaxial shearing method or the like is used.

【0011】乾燥過程では、熱風の導入により廃棄物が
局部的に高温となるため、廃棄物中に含まれるPVC等
の塩素系プラスチック又は他の有機塩素化合物が熱分解
してHClを発生し、このHClが廃棄物中の有機化合
物と反応することによりダイオキシン類が発生する。こ
こで、アルカリ化合物は、HClと反応しClを取り込
み安定なアルカリ塩化物になる。このようにアルカリ化
合物はHClと反応し、Clをアルカリ塩化物として固
定化できるため、ダイオキシン類の生成がなくなる。
In the drying process, the temperature of the waste locally rises due to the introduction of hot air, so chlorine-containing plastics such as PVC or other organic chlorine compounds contained in the waste are thermally decomposed to generate HCl, Dioxins are generated by the reaction of this HCl with the organic compounds in the waste. Here, the alkaline compound reacts with HCl and takes in Cl to become a stable alkaline chloride. In this way, the alkaline compound reacts with HCl and Cl can be fixed as an alkaline chloride, so that dioxins are not produced.

【0012】HClと反応した処理剤は、乾燥機12の
後流に設置された振動ふるい、風力式分級機等の選別機
24で乾燥物と処理剤の粗粒とに分離される。乾燥物は
燃料等として用いられる。一方、乾燥排ガスに同伴され
た処理剤の細粒は、サイクロン、ろ過集塵機(例えばバ
グフィルタ)等の集塵機26で分離、捕集される。28
は送風機である。
The treating agent that has reacted with HCl is separated into a dried product and coarse particles of the treating agent by a sorting machine 24 such as a vibrating sieve installed in the downstream of the dryer 12 or a wind-powered classifier. The dried product is used as fuel or the like. On the other hand, the fine particles of the treatment agent entrained in the dry exhaust gas are separated and collected by a dust collector 26 such as a cyclone or a filter dust collector (for example, a bag filter). 28
Is a blower.

【0013】図2は本発明の実施の第2形態による廃棄
物処理装置を示している。本実施形態は、ごみ固形化燃
料(RDF)製造に適用したもので、選別機24からの
乾燥物を破砕機30でさらに細かく破砕し、振動ふる
い、風力式分級機等の選別機32で不燃物等の異物を分
離除去した後、腐敗防止用に添加剤(例えば消石灰、生
石灰等)を混合し、成形機34でごみ固形化燃料(RD
F)とすることで、Cl又はアルカリ塩化物(例えばC
aCl2 )等の不燃性の反応生成物の含有量の少ないご
み固形化燃料(RDF)を製造するものである。36は
添加剤添加手段である。破砕機30としては、一軸せん
断式等が用いられ、成形機34としては、リング・ダイ
式等が用いられる。他の構成及び作用は、実施の第1形
態の場合と同様である。
FIG. 2 shows a waste treatment device according to a second embodiment of the present invention. The present embodiment is applied to the production of solid waste fuel (RDF), in which the dried product from the sorting machine 24 is further finely crushed by the crushing machine 30, and is incombustible by the sorting machine 32 such as a vibrating sieve or a wind-powered classifier. After separating and removing foreign substances such as things, additives (for example, slaked lime, quick lime, etc.) are mixed to prevent spoilage, and the waste solidified fuel (RD
F) means that Cl or an alkali chloride (for example, C
It is intended to produce refuse solidified fuel (RDF) having a low content of non-combustible reaction products such as aCl 2 ). 36 is an additive addition means. A uniaxial shearing type is used as the crusher 30, and a ring die type is used as the molding machine 34. Other configurations and operations are similar to those of the first embodiment.

【0014】[0014]

【発明の効果】本発明は上記のように構成されているの
で、つぎのような効果を奏する。 (1) 廃棄物の乾燥過程で発生する有害なHClを除
去して、ダイオキシン類の生成を抑制、低減することが
できる。 (2) 有害なHClやダイオキシン類を除去又は低減
するため、排ガス処理装置が不要となり、このため乾燥
工程が簡略化でき、コンパクト化及びコストダウンを図
ることができる。 (3) HCl等の有害ガスと反応した処理剤を分離す
ることにより、乾燥物又はごみ固形化燃料(RDF)中
に不燃性のアルカリ塩化物が残留しなくなる。
Since the present invention is configured as described above, it has the following effects. (1) The harmful HCl generated during the drying process of waste can be removed to suppress or reduce the production of dioxins. (2) Since harmful HCl and dioxins are removed or reduced, an exhaust gas treatment device is not required. Therefore, the drying process can be simplified, and the size and cost can be reduced. (3) By separating the treating agent that has reacted with a harmful gas such as HCl, nonflammable alkali chlorides do not remain in the dried product or the refuse solidified fuel (RDF).

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

【図1】本発明の実施の第1形態による廃棄物処理装置
の系統的概略構成図である。
FIG. 1 is a systematic schematic configuration diagram of a waste treatment device according to a first embodiment of the present invention.

【図2】本発明の実施の第2形態による廃棄物処理装置
の系統的概略構成図である。
FIG. 2 is a systematic schematic configuration diagram of a waste treatment device according to a second embodiment of the present invention.

【符号の説明】[Explanation of symbols]

10、30 破砕機 12 乾燥機 14 熱風炉 16 廃棄物搬送手段 18 破砕廃棄物搬送手段 20、22 処理剤添加手段 24、32 選別機 26 集塵機 28 送風機 34 成形機 36 添加剤添加手段 10, 30 crusher 12 dryer 14 hot stove 16 Waste transportation means 18 Crushed waste transportation means 20, 22 Treatment agent adding means 24, 32 sorter 26 dust collector 28 blower 34 molding machine 36 Means for adding additives

───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開2000−8056(JP,A) 特開 昭60−166397(JP,A) 特開 平11−106773(JP,A) 特開 平10−311677(JP,A) (58)調査した分野(Int.Cl.7,DB名) B09B 3/00 - 5/00 ─────────────────────────────────────────────────── --Continued from the front page (56) Reference JP 2000-8065 (JP, A) JP 60-166397 (JP, A) JP 11-106773 (JP, A) JP 10-311677 (JP, A) (58) Fields investigated (Int.Cl. 7 , DB name) B09B 3/00-5/00

Claims (9)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 廃棄物とアルカリ化合物からなる処理剤
又はアルカリ化合物を含む処理剤とを混合した後、この
混合物を熱風を被乾燥物に直接接触させて乾燥させる
燥機に導入して乾燥させるとともに、乾燥過程で発生す
る塩化水素ガスを除去してダイオキシン類の生成を抑制
することを特徴とする廃棄物処理方法。
1. A drier in which waste is mixed with a treating agent containing an alkaline compound or a treating agent containing an alkaline compound, and the mixture is dried by bringing hot air into direct contact with an object to be dried. A method for treating waste, which comprises introducing and drying, and at the same time, removing hydrogen chloride gas generated during the drying process to suppress the production of dioxins.
【請求項2】 廃棄物を破砕した後、破砕廃棄物とアル
カリ化合物からなる処理剤又はアルカリ化合物を含む処
理剤とを混合する請求項1記載の廃棄物処理方法。
2. The waste treatment method according to claim 1, wherein after the waste is crushed, the crushed waste is mixed with a treatment agent containing an alkali compound or a treatment agent containing an alkali compound.
【請求項3】 乾燥機から排出される乾燥物と反応済処
理剤との混合物を選別機に導入して、乾燥物と反応済処
理剤とに分離する請求項1又は2記載の廃棄物処理方
法。
3. The waste treatment according to claim 1 or 2, wherein a mixture of the dried product discharged from the dryer and the reacted treating agent is introduced into a sorting machine to separate the dried product and the reacted treating agent. Method.
【請求項4】 乾燥機から排出される乾燥排ガスと反応
済処理剤との混合物を集塵機に導入して、乾燥排ガスと
反応済処理剤とに分離する請求項1、2又は3記載の廃
棄物処理方法。
4. The waste according to claim 1, 2 or 3, wherein a mixture of the dry exhaust gas discharged from the dryer and the reacted treatment agent is introduced into a dust collector to separate the dry exhaust gas and the reacted treatment agent. Processing method.
【請求項5】 選別機で分離された乾燥物を破砕した
後、不燃物を分離し、不燃物が分離された破砕物に腐敗
防止用の添加剤を添加混合して成形する請求項3記載の
廃棄物処理方法。
5. The method according to claim 3, wherein after crushing the dried material separated by a sorting machine, the incombustible material is separated, and the crushed material from which the incombustible material has been separated is added and mixed with an additive for preventing decay. Waste disposal method.
【請求項6】 アルカリ化合物が、Ca(OH)2 、C
aO、CaCO3 、Mg(OH)2 、MgO、MgCO
3 及びCaMg(CO3 2 の少なくともいずれかの粉
状体又は粒状体である請求項1〜5のいずれかに記載の
廃棄物処理方法。
6. The alkaline compound is Ca (OH) 2 , C
aO, CaCO 3 , Mg (OH) 2 , MgO, MgCO
3 and CaMg (CO 3) 2 in waste treatment method according to claim 1 is at least one pulverulent body or granules.
【請求項7】 廃棄物を破砕するための破砕機と、破砕
された廃棄物を乾燥させるための熱風を被乾燥物に直接
接触させて乾燥させる乾燥機と、乾燥排ガスを除塵処理
するための集塵機とを備えた廃棄物処理装置において、
破砕機の出口側の破砕廃棄物搬送手段又は/及び破砕機
の入口側の廃棄物搬送手段に、アルカリ化合物からなる
処理剤又はアルカリ化合物を含む処理剤を添加するため
の処理剤添加手段を接続したことを特徴とする廃棄物処
理装置。
7. A crusher for crushing waste and hot air for drying the crushed waste are directly applied to the material to be dried.
In a waste treatment device provided with a dryer for contacting and drying, and a dust collector for dedusting dry exhaust gas,
A treatment agent addition means for adding a treatment agent comprising an alkali compound or a treatment agent containing an alkali compound is connected to the crushed waste transportation means on the outlet side of the crusher or / and the waste transportation means on the inlet side of the crusher. A waste treatment device characterized in that
【請求項8】 乾燥機からの乾燥物と反応済処理剤との
混合物を乾燥物と反応済処理剤とに分離するための選別
機をさらに備えた請求項7記載の廃棄物処理装置。
8. The waste treatment device according to claim 7, further comprising a separator for separating a mixture of the dried product from the dryer and the reacted treatment agent into the dried material and the reacted treatment agent.
【請求項9】 選別機からの乾燥物を破砕するための破
砕機と、破砕機からの破砕物から不燃物を分離するため
の選別機と、選別機からの不燃物が分離された破砕物に
腐敗防止用の添加剤を添加するための添加剤添加手段
と、添加剤が添加された破砕物を成形するための成形機
とをさらに備えた請求項8記載の廃棄物処理装置。
9. A crusher for crushing the dried product from the sorter, a separator for separating incombustibles from the crushed product from the crusher, and a crushed product from which the incombustibles have been separated from the sorter. 9. The waste treatment apparatus according to claim 8, further comprising: an additive adding means for adding an additive for preventing spoilage to the product, and a molding machine for molding a crushed product to which the additive is added.
JP2000142724A 2000-05-16 2000-05-16 Waste treatment method and equipment Expired - Fee Related JP3390767B2 (en)

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Application Number Priority Date Filing Date Title
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Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2000142724A JP3390767B2 (en) 2000-05-16 2000-05-16 Waste treatment method and equipment

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Publication Number Publication Date
JP2001321744A JP2001321744A (en) 2001-11-20
JP3390767B2 true JP3390767B2 (en) 2003-03-31

Family

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Application Number Title Priority Date Filing Date
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Country Link
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