JPH07185502A - Device for treating combustible waste - Google Patents

Device for treating combustible waste

Info

Publication number
JPH07185502A
JPH07185502A JP5348667A JP34866793A JPH07185502A JP H07185502 A JPH07185502 A JP H07185502A JP 5348667 A JP5348667 A JP 5348667A JP 34866793 A JP34866793 A JP 34866793A JP H07185502 A JPH07185502 A JP H07185502A
Authority
JP
Japan
Prior art keywords
container
filter
suction
heat
wastes
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
JP5348667A
Other languages
Japanese (ja)
Inventor
Kenro Motoda
田 謙 郎 元
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.)
G M KK
Motoda Electronics Co Ltd
MIC Co Ltd
Original Assignee
G M KK
Motoda Electronics Co Ltd
MIC 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 G M KK, Motoda Electronics Co Ltd, MIC Co Ltd filed Critical G M KK
Priority to JP5348667A priority Critical patent/JPH07185502A/en
Publication of JPH07185502A publication Critical patent/JPH07185502A/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
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/10Process efficiency
    • Y02P20/129Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines

Landscapes

  • Treating Waste Gases (AREA)
  • Processing Of Solid Wastes (AREA)
  • Carbon And Carbon Compounds (AREA)

Abstract

PURPOSE:To facilitate the conversion of wastes to useful active carbon or graphite by heating combustible wastes housed in a closed vessel in a non- oxygen state to a required temp. to generate steam and other gases and subjecting the formed noxious gas to neutralization and adsorption through a suction filter. CONSTITUTION:Wastes F including various kinds of formed parts and compositions of vinyl chloride are thrown in an inside vessel 1a from its throw-in hole 2, and after closing it, the closed vessel 1a is evacuated. Next, waste heat of a thermal power plant, etc., are introduced as an external heat source into a space layer 1b from the heat introducing pass of a heat feeding part 5 to evaporate volatile components, such as moisture and solvent contained in the wastes F. Gaseous Cl generated from compositions of vinyl chloride contained in the wastes F is led to a set of filter vessels 7A, 7B from an exhaust pipe 6 and treated by neutralization, adsorption, etc., to make it harmless. After that, it is discharged to the outside by suction force of an evacuating apparatus 8. Next, the heat feeding part 5 is controlled to perform heating of next stage, and non-decomposed components in the residual wastes F are thermally decomposed to accelerate carbonization.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、燃焼乃至は焼却可能な
廃棄物を含んだ廃棄物を、燃焼乃至は焼却することなく
炭化させることにより、減容,無害化、及び、無臭化す
ることができる処理装置に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention is to reduce the volume, detoxify and deodorize a waste material containing a combustible or incinerable waste material by carbonizing it without burning or incinerating it. The present invention relates to a processing device capable of

【0002】[0002]

【従来の技術】従来、各種の産業廃棄物、生ゴミ等の都
市型廃棄物は、燃焼乃至焼却処理するもの、そのまま埋
立て等に使用するもの、或は、金属や油分の回収をする
ための処理するものなどに分別し、それぞれの分別され
た廃棄物に対する処理方法によって処理されている。
2. Description of the Related Art Conventionally, various industrial wastes, municipal wastes such as kitchen wastes are burned or incinerated, used for landfill as they are, or used to recover metal or oil. The waste is separated into the ones to be treated and the waste is treated according to the treatment method.

【0003】しかし、従来の処理方法において、廃棄物
を燃焼乃至は焼却(以下、焼却という)によって処理す
る方法は、そのために多量のエネルギを不可欠とするほ
か、焼却に伴い塩素ガスやダイオキシン等の有害ガスが
生じるのみならず、燃焼に伴いCO2が多量に発生するこ
とが知られている。
However, in the conventional treatment method, the method of treating waste by combustion or incineration (hereinafter referred to as incineration) requires a large amount of energy for that purpose, and chlorine gas, dioxin, etc. are accompanied by the incineration. It is known that not only toxic gas is generated, but also a large amount of CO 2 is generated with combustion.

【0004】これまで、上記焼却に伴い発生する各種ガ
スのうち有害ガスについてはその除去の方策がとられつ
つあるものの、上記CO2は、廃棄物の焼却の際、そのま
ま大気中に放出されていた。しかし、近年、いわゆる地
球規模での公害問題、特に、地球温暖化の原因の一つと
して、大気中に放出されている前記CO2があることが指
摘されるに至った。
Up to now, although measures have been taken to remove harmful gases out of various gases generated by the above incineration, the above CO 2 is released into the atmosphere as it is when the waste is incinerated. It was However, in recent years, it has been pointed out that the CO 2 released into the atmosphere is one of the causes of so-called global pollution problems, particularly global warming.

【0005】[0005]

【発明が解決しようとする課題】本発明は、上記のよう
な廃棄物の焼却処理に伴う有害ガスの発生,放出やCO2
放出の問題に鑑み、可燃性の廃棄物であっても、これを
焼却することなく、減容,無害化し、しかも、有用な活
性炭や黒鉛を生成させることができる処理装置を提供す
ることを課題としてなされたものである。
SUMMARY OF THE INVENTION The present invention is directed to the generation and release of harmful gases and CO 2 emissions associated with the incineration of waste materials as described above.
In view of the problem of emission, it is an object of the present invention to provide a processing device capable of reducing the volume and harmlessness of combustible waste without incinerating it and generating useful activated carbon and graphite. It was made as.

【0006】[0006]

【課題を解決するための手段】上記課題を解決すること
を目的としてなされた本発明処理装置の構成は、廃棄物
を収容し脱酸素又は空気遮断状態下で所要温度まで加熱
してその温度を所要時間保持できるようにした密閉加熱
容器と、上部に空間を残して中和剤などの液状濾過体を
収容すると共に、前記密閉加熱容器に接続されるガス導
入パイプが前記濾過体中に位置付けられ、かつ、前記上
部空間に外部から吸引力を作用させるようにした複数の
容器であって、これらの容器を少なくとも2群に分けて
切換可能に前記密閉加熱容器に接続した吸引式フィルタ
容器と、前記各フィルタ容器の上部空間に吸引力を作用
させる吸引装置と、該吸引装置の排気側に接続され、前
記吸引装置から排出される排気ガスを加熱,燃焼部を通
過させて脱臭する脱臭部とから成ることを特徴とするも
のである。
The structure of the treatment apparatus of the present invention made for the purpose of solving the above-mentioned problems is such that the waste is accommodated and heated to a required temperature under deoxygenated or air-shielded conditions and the temperature thereof is adjusted. A closed heating container capable of holding for a required time and a liquid filter body such as a neutralizer containing an empty space in the upper part are accommodated, and a gas introduction pipe connected to the closed heating container is positioned in the filter body. A plurality of containers adapted to exert a suction force on the upper space from the outside, the suction type filter container being connected to the closed heating container so as to be switchable by dividing these containers into at least two groups; A suction device that applies a suction force to the upper space of each filter container, and exhaust gas that is connected to the exhaust side of the suction device and that is discharged from the suction device is heated and passes through a combustion unit to deodorize. It is characterized in that comprising a smell section.

【0007】[0007]

【作用】無酸素状態の密閉容器に収容した可燃性廃棄物
を所要温度に加熱し、所要時間その加熱温度を保持する
ことにより、水蒸気、その他のガスを経時的に発生さ
せ、この間に生成される有害ガスは吸引式フィルタを通
して中和,吸着等により除去し無害化する。この間にお
いて当該廃棄物は前記密閉容器内で炭化するまで加熱さ
れるので、廃棄物の処理においてCO2は全く発生しな
い。吸引式フィルタは、2群以上を切換え可能に並列に
接続してガスが通過させられている液状濾過体のpHを
測定し、そのpH値により他の群の吸引式フィルタと切
換えて使用するようにしたから、連続運転ができ、処理
効率を高めることができる。
[Function] By heating the combustible waste contained in the oxygen-free airtight container to the required temperature and maintaining the heating temperature for the required time, steam and other gases are generated over time, and are generated during this period. The harmful gas is removed by neutralization and adsorption through a suction filter to render it harmless. During this period, the waste is heated in the closed container until it is carbonized, so no CO 2 is generated during the treatment of the waste. The suction type filter connects two or more groups in parallel in a switchable manner, measures the pH of the liquid filter medium through which gas is passed, and switches the suction type filter to the suction type filter of another group depending on the pH value. Therefore, continuous operation can be performed and processing efficiency can be improved.

【0008】[0008]

【実施例】次に、本発明処理装置の実施例を図により説
明する。図1は本発明処理装置の一例の概要を示すシス
テムブロック図、図2は吸引式フィルタの構成例を示す
断面図である。
DESCRIPTION OF THE PREFERRED EMBODIMENTS Next, an embodiment of the processing apparatus of the present invention will be described with reference to the drawings. FIG. 1 is a system block diagram showing an outline of an example of the processing apparatus of the present invention, and FIG. 2 is a sectional view showing a configuration example of a suction type filter.

【0009】図1において、1は、主として可燃性の廃
棄物Fを無酸素下で密閉収容し、外部から加える熱によ
り、その廃棄物Fを加熱分解して炭化処理するための処
理容器で、ここでは内側容器1aと、間に空間層1bを保持
して前記容器1を断熱的に覆う外側容器1cとにより形成
されている。内側容器1aは、外部からの受熱或は内部へ
の放熱の効率を上げるため、表面を凹凸面に形成したも
のが望ましい。
In FIG. 1, reference numeral 1 denotes a processing container for hermetically containing a combustible waste material F in an oxygen-free state and thermally decomposing the waste material F by heat applied from the outside to carbonize the waste material F. Here, it is formed by an inner container 1a and an outer container 1c which holds the space layer 1b between them to cover the container 1 in an adiabatic manner. The inner container 1a preferably has an uneven surface in order to increase the efficiency of receiving heat from the outside or radiating heat to the inside.

【0010】上記処理容器1には、内,外側容器1a,1c
を貫通して廃棄物Fの投入口2、処理残渣物の取出口3
が設けられていると共に、内側容器1a内の温度を測定す
るための温度センサ1dが配設されている。なお、これら
両口2,3は、一つの開口部によって兼用させるように
してもよい。4a,4bは内,外側容器1a,1cの開口部に設
けた蓋である。
The processing container 1 includes inner and outer containers 1a and 1c.
2 through which the waste F is put in and the treatment residue is taken out 3
And a temperature sensor 1d for measuring the temperature inside the inner container 1a. It should be noted that these openings 2 and 3 may be combined by a single opening. Reference numerals 4a and 4b are lids provided at the openings of the inner and outer containers 1a and 1c.

【0011】また、前記処理容器1における空間層1bに
は、この実施例では外部熱源からの熱を制御し乍ら導入
するための熱供給部5が、ここでは2系統接続されてい
る。この熱供給部5における供給熱量の制御は、前記温
度センサ1dの測定温度と別設したタイマ(図示せず)に
よる計時デ−タとに基づいて、供給熱量のコントロ−ル
を行う。図において、5aは熱導入路、5bは熱量コントロ
−ルバルブ、5cは排熱路、5dはその開閉バルブである。
なお、熱源としては、内側容器1aを空間層1bに配したガ
スバ−ナや電気ヒ−タ等の加熱手段を用いこれにより加
熱してもよい。
In this embodiment, the space layer 1b of the processing container 1 is connected to two heat supply units 5 for controlling and introducing heat from an external heat source. The amount of heat supplied by the heat supply unit 5 is controlled based on the temperature measured by the temperature sensor 1d and the timing data provided by a timer (not shown) provided separately. In the figure, 5a is a heat introduction path, 5b is a heat quantity control valve, 5c is a heat exhaust path, and 5d is its opening / closing valve.
As the heat source, a heating means such as a gas burner in which the inner container 1a is arranged in the space layer 1b or an electric heater may be used for heating.

【0012】6は外側容器1cを貫通して内側容器1aに連
通接続した排気管で、途中に接続用排気管61,62を介し
て所定のガス成分を中和するためのフィルタ容器71や他
のガス成分を吸着,結合等により除去するためのフィル
タ容器72から成るフィルタ容器群7A,7Bに接続され、接
続用排気管63,64と切換弁74を介して吸引ファンによる
排気装置8の吸気側に接続されている。
Reference numeral 6 denotes an exhaust pipe penetrating the outer container 1c and communicating with the inner container 1a, and a filter container 71 for neutralizing a predetermined gas component via connecting exhaust pipes 61 and 62, and the like. Is connected to filter container groups 7A and 7B formed of filter containers 72 for removing the gas components of the exhaust gas by adsorption, bonding, and the like, and intake air of the exhaust device 8 is obtained by a suction fan via connection exhaust pipes 63 and 64 and a switching valve 74. Connected to the side.

【0013】ここで、上記の各フィルタ容器71,72はそ
れぞれ接続用排気管61,62により直列した2個を1組と
する2組のフィルタ容器群7A,7Bに形成され、各フィル
タ容器群7A,7Bにおける先頭側のフィルタ容器71と72
は、切換弁73を介在させた排気管6により上記の内側容
器1aに接続されている。なお、図示しないが、本発明で
は前記排気管6の中間をU字状に曲げ、このベント部分
を冷却して油分を凝集し、ドレンから当該油分を取出す
ようにしてもよい。
The filter containers 71 and 72 are formed into two sets of filter container groups 7A and 7B, each of which is a series of two exhaust pipes 61 and 62 for connection. Front side filter vessels 71 and 72 in 7A and 7B
Is connected to the inner container 1a by an exhaust pipe 6 with a switching valve 73 interposed. Although not shown, in the present invention, the middle portion of the exhaust pipe 6 may be bent in a U shape, and the vent portion may be cooled to agglomerate the oil component, and the oil component may be taken out from the drain.

【0014】而して、各フィルタ容器71,72は、それぞ
れの内部に、上部に空間71b,72bを有して溶液タイプの
中和剤や濾過剤71a,72aが収容されており、各剤71a,7
2aに対しては、モ−タ71c,72cにより回転させられる混
合板71d,72dが配設されている。71e,72eはモ−タ71
c,72cと混合板71d,72dを結ぶ軸である。
Thus, each of the filter containers 71, 72 has a space 71b, 72b in the upper part and a solution type neutralizing agent or a filtering agent 71a, 72a is housed in each of the filter containers 71, 72. 71a, 7
For 2a, mixing plates 71d and 72d that are rotated by motors 71c and 72c are provided. 71e and 72e are motors 71
It is an axis connecting c, 72c and mixing plates 71d, 72d.

【0015】また、上記各剤71a,72aに対しては、pH
センサ71f,72fを接触させ、中和剤,濾過剤71a,72aの
pHを常時又は適宜のサンプリング周期で検出できるよ
うにされており、このセンサ71f,72fによりサンプリン
グしたpH度によって、ここでは2組のフィルタ群7A,
7Bにおける排気管6と同63,64に設けた切換弁73,74の
切換えを行うように形成されている。
For each of the agents 71a and 72a, the pH is
The sensors 71f and 72f are brought into contact with each other so that the pH of the neutralizing agent and the filtering agents 71a and 72a can be detected constantly or at an appropriate sampling cycle. Filter group 7A,
The switching valves 73 and 74 provided in the exhaust pipe 6 and 63 and 64 in 7B are formed to be switched.

【0016】前記排気装置8の排気管65の外周には、図
示しないがフィンやグリッド等により形成する受熱部9
を設け、該受熱部9を、一例としてガスバ−ナ等の熱源
9aにより800℃程度乃至はそれ以上に加熱することによ
り、この排気管65内を通り、外部に放出される気体の脱
臭を行うように形成されている。
On the outer circumference of the exhaust pipe 65 of the exhaust device 8, a heat receiving portion 9 formed of fins or grids (not shown)
And the heat receiving portion 9 is a heat source such as a gas burner as an example.
It is formed so as to deodorize the gas that passes through the exhaust pipe 65 and is released to the outside by heating at about 800 ° C. or higher by the 9a.

【0017】以上より、本発明処理装置の一例を形成す
るので、次にこの処理装置による廃棄物の処理態様の一
例について述べる。
As described above, an example of the processing apparatus of the present invention is formed. Next, an example of a waste processing mode by this processing apparatus will be described.

【0018】廃棄物Fは、塩ビ系(塩化ビニル系の略)
の各種成形品や組成品を含み、かつ、水分を始めとする
各種の液体に含浸乃至は湿潤された紙系,布系,フィル
ム系,固形物による混成可燃性廃棄物である。具体的に
は、農業用或は漁業用等の産業用塩ビ製品、一般家庭や
事務所,ホテル,レストラン等の各種事業所、或は、病
院,養老院等で排出される様々な可燃性の廃棄物であ
る。
Waste F is a vinyl chloride type (abbreviation of vinyl chloride type)
It is a mixed combustible waste consisting of paper-based, cloth-based, film-based, and solid matter that includes various molded products and compositions and is impregnated or moistened with various liquids such as water. Specifically, industrial PVC products for agriculture or fisheries, various establishments such as general households, offices, hotels, restaurants, etc., or various flammable wastes discharged from hospitals, nursing homes, etc. It is a thing.

【0019】この廃棄物Fの所要量が、内側容器1a内に
その投入口2から投入され容器1が密閉されて内側容器
1aの空気を排出する。なお、内側容器1aの内部には、こ
の容器1aの底から浮かせて支持した金網状の受皿Mが配
設され、収容された廃棄物に偏りなく熱が伝導されるよ
うに工夫されている。また、内側容器1aの内,外面はフ
ィン等による凹凸面に形成し外部からの吸熱、及び、内
部での放熱効率を高めるようにすることが望ましい。上
記受皿Mは、金網製の篭に代えることもある。
A required amount of this waste material F is put into the inner container 1a through its charging port 2 and the container 1 is hermetically sealed.
Exhaust the air of 1a. In addition, inside the inner container 1a, a wire-mesh-like tray M which is floated from the bottom of the container 1a and supported is arranged so that heat can be uniformly transferred to the stored waste. In addition, it is desirable that the inner and outer surfaces of the inner container 1a are formed as uneven surfaces by fins or the like so as to enhance heat absorption from the outside and heat dissipation efficiency inside. The saucer M may be replaced with a cage made of wire mesh.

【0020】熱供給部5の熱導入路からは、外部熱源、
例えば、火力発電所の排熱等による熱が、閉鎖容器1の
空間層1bに導入され、内側容器1aの内部温度の上昇が図
られる。前記内側容器1aの内部は、一例として、例え
ば、当初100℃〜200℃前後の温度に上昇させてその温度
を適宜時間保持し、廃棄物Fに含まれる水分や溶剤等揮
発成分の蒸発を図る。温度コントロ−ルは、例えば、
入,排熱路5a,5cのバルブ5b,5dの開閉度合の調節によ
って行う。
From the heat introduction path of the heat supply unit 5, an external heat source,
For example, heat generated by exhaust heat from a thermal power plant is introduced into the space layer 1b of the closed container 1 to increase the internal temperature of the inner container 1a. The inside of the inner container 1a is, for example, initially raised to a temperature of around 100 ° C. to 200 ° C. and held at that temperature for an appropriate period of time to evaporate volatile components such as water and solvent contained in the waste F. . The temperature control is, for example,
This is performed by adjusting the opening / closing degree of the valves 5b, 5d of the heat input / exhaust heat paths 5a, 5c.

【0021】上記加熱による水分等の蒸発に要する時間
は、廃棄物Fの量によって異なるが、水分等の蒸発によ
り廃棄物の重量は約70〜80%減量されることが、実験の
結果、判明している。水分等の蒸発過程が終了したら、
引きつづき、熱供給部5からの熱供給量を拡大し、内側
容器1aの内部温度を約280℃前後まで上昇させ、この温
度を所要時間保持する。
Although the time required for evaporation of water or the like due to the heating varies depending on the amount of waste F, the result of the experiment has revealed that the weight of the waste is reduced by about 70 to 80% by the evaporation of water or the like. is doing. When the evaporation process of water etc. is completed,
Subsequently, the amount of heat supplied from the heat supply unit 5 is increased, the internal temperature of the inner container 1a is raised to about 280 ° C., and this temperature is maintained for the required time.

【0022】上記280℃前後の温度に内側容器1aの内部
が保持されることより、水分等が飛んだ前記廃棄物Fに
含まれていた塩ビ系組成物からClガスが生成するが、こ
のClガスは、排気管6から一組のフィルタ容器群7A又は
7Bのフィルタ容器71又は72を通過して中和,吸着等によ
り処理され、Clガスを含まないガスが排気装置8の吸引
力によって排気管65側へ排出される。
Since the inside of the inner container 1a is kept at the temperature of about 280 ° C., Cl gas is generated from the vinyl chloride composition contained in the waste F from which water and the like have been blown. Gas is discharged from the exhaust pipe 6 into a set of filter container groups 7A or
Gas that does not contain Cl gas is discharged to the exhaust pipe 65 side by the suction force of the exhaust device 8 after passing through the 7B filter container 71 or 72 and processed by neutralization, adsorption and the like.

【0023】内側容器1aの内部から排気管6に流出する
Cl系ガスは、各フィルタ容器71又は72を経由することに
よって、ほぼ完全に、乃至は、少なくとも人畜等に安全
なレベルまで中和,除去され、排気管65から排気され
る。
Outflow from the inside of the inner container 1a to the exhaust pipe 6
The Cl gas is neutralized and removed almost completely or at least to a level safe for humans and animals by passing through each filter container 71 or 72, and is exhausted from the exhaust pipe 65.

【0024】このあと、熱供給部5を制御して、次の段
階の加熱温度として内側容器1aの内部を約500℃前後の
温度にまで加熱し、その加熱温度を所要時間保持する。
Thereafter, the heat supply unit 5 is controlled to heat the inside of the inner container 1a to a temperature of about 500 ° C. as the heating temperature for the next stage, and the heating temperature is maintained for the required time.

【0025】この加熱によって、前記温度の加熱完了時
点で残留した廃棄物Fの中の未分解成分の熱分解が進
み、廃棄物全体の炭化が促進される。この加熱や先に述
べた100〜200℃、或は、280℃前後の加熱において廃棄
物Fから生成される各種のガスは、所定のガス(有害ガ
スや不要ガス)がフィルタ容器71又は72において除去さ
れるが、各ガスに含まれる異臭,悪臭成分は、前記フィ
ルタ容器71又は72を通過して、排気装置8から外部へ放
出されるものがある。
By this heating, the thermal decomposition of the undecomposed components in the waste F remaining at the time when the heating at the above temperature is completed is promoted, and the carbonization of the entire waste is promoted. Of the various gases produced from the waste F by this heating and the above-mentioned heating at 100 to 200 ° C. or around 280 ° C., a predetermined gas (toxic gas or unnecessary gas) is generated in the filter container 71 or 72. Some of the offensive odors and malodorous components contained in the respective gases, which are removed, pass through the filter container 71 or 72 and are discharged from the exhaust device 8 to the outside.

【0026】そこで、本発明装置では、吸引ファンによ
る排気装置8の排気管65に受熱部9を設け、この受熱部
9において排気ガスにガス火炎等の熱源を接触させるこ
とにより、前記排気成分中の臭気分を加熱,燃焼させて
無臭化するようにしている。
Therefore, in the device of the present invention, the heat receiving portion 9 is provided in the exhaust pipe 65 of the exhaust device 8 by the suction fan, and in this heat receiving portion 9, the exhaust gas is brought into contact with a heat source such as a gas flame, so that The odorous mood is heated and burned to make it odorless.

【0027】上述のように、廃棄物Fは無酸素状態の密
閉容器1の内部において、一例として約100℃〜約500℃
程度までの加熱温度によって段階的に順次加熱処理さ
れ、この間に、排気中に含まれる悪臭,異臭成分が再加
熱,燃焼されることによって、廃棄物自体は全く燃焼さ
れることなく無害化,無臭化される。
As described above, the waste material F is stored in the airtight closed container 1 in an amount of, for example, about 100 ° C to about 500 ° C.
Heat treatment is performed step by step depending on the heating temperature up to a certain degree, and during this time, the malodorous and offensive odor components contained in the exhaust gas are reheated and burned, so that the waste itself is rendered harmless and odorless without being burned at all. Be converted.

【0028】このようにして処理が進行する本発明装置
による廃棄物Fの燃焼を伴なわない加熱炭化を主体とす
る処理においては、2組のフィルタ容器群7Aと7Bを切換
え、密閉容器1の内側容器1aに加熱温度の高低によって
生じる異なるガスの効率のよい除去や、経時劣化する中
和剤,濾過剤71aや72aの再生や回復等を図ることができ
るようにした。
In the treatment mainly by heating and carbonization without combustion of the waste F by the apparatus of the present invention in which the treatment progresses in this way, two sets of filter vessel groups 7A and 7B are switched to close the closed vessel 1. It has been made possible to efficiently remove different gases generated in the inner container 1a depending on the heating temperature and to regenerate or recover the neutralizing agent and the filtering agents 71a and 72a that deteriorate over time.

【0029】このため、本発明装置では、例えば、各フ
ィルタ容器71,72の中和剤,濾過剤71a及び72aに、pH
検出手段としてのセンサ71f,72fを設け、中和剤,濾過
剤71a、又は、72aのpH度が、例えば、中和剤としての
機能を発揮できなくなる前に切換弁73,74を切換え、現
在、使用しているフィルタ容器群7A又は7Bを、使用して
いないフィルタ容器群7B又は7Aに切換え、それまで使用
していたフィルタ容器群7A又は7Bの中和剤,濾過剤71a
又は72aの再生や入替えを行う。
Therefore, in the apparatus of the present invention, for example, the pH of the neutralizing agent and the filtering agents 71a and 72a of the respective filter containers 71 and 72 is
Sensors 71f and 72f as detection means are provided to switch the switching valves 73 and 74 before the pH of the neutralizing agent, the filtering agent 71a, or 72a becomes unable to exhibit the function as the neutralizing agent. , The used filter container group 7A or 7B is switched to the unused filter container group 7B or 7A, the neutralizing agent of the filter container group 7A or 7B used until then, the filtering agent 71a
Alternatively, the 72a is reproduced or replaced.

【0030】また、本発明装置では、上記フィルタ容器
群7A,7Bの切換えを、加熱温度によって密閉容器1に生
成する異なるガスの種類に対応させて切換えるようにす
る。このため、フィルタ容器群7Aと7Bでは、中和剤,濾
過剤71a,72aに、それぞれ異なるガスの中和,吸着等の
機能をもつものを使用する。
Further, in the device of the present invention, the switching of the filter container groups 7A and 7B is switched according to the kind of different gas generated in the closed container 1 depending on the heating temperature. Therefore, in the filter container groups 7A and 7B, the neutralizing agent and the filtering agents 71a and 72a having different gas neutralizing and adsorbing functions are used.

【0031】上記のような本発明装置におけるフィルタ
容器群7A,7Bの切換え使用は、上記のpHセンサ71f,7
2fの検出信号、或は、種々のガスを検出するガスセンサ
(図示せず)の検出信号に基づいて、切換弁73,74を自
動的に切換え作動させる。勿論、この切換えを人の判断
などに基づいて手動的に行うことは任意である。
The switching use of the filter container groups 7A and 7B in the apparatus of the present invention as described above is performed by the above-mentioned pH sensors 71f and 7B.
Based on the detection signal of 2f or the detection signal of a gas sensor (not shown) that detects various gases, the switching valves 73 and 74 are automatically switched and operated. Of course, it is arbitrary to perform this switching manually based on a person's judgment.

【0032】上記のような処理により、廃棄物Fは密閉
容器1の内部において、ほぼ完全に炭化された状態の残
渣物となる。この残渣炭化物は、無臭,無害ゆえに、そ
のまま埋立てなどに使用しても何ら問題ないことは勿
論、更に進んで活性炭、或は、黒鉛として利用すること
が出来る。特に、塩ビ系廃棄物の処理残渣は、きわめて
純度の高い炭素分として取出すことが出来るので、活性
炭として利用する上できわめて好適合である。
By the treatment as described above, the waste F becomes a residue in a state in which it is almost completely carbonized inside the closed container 1. Since the residual carbide is odorless and harmless, it can be used as it is for landfill without any problem, and it can be further used as activated carbon or graphite. In particular, the processing residue of the vinyl chloride waste can be taken out as a carbon component having an extremely high purity, which is extremely suitable for use as activated carbon.

【0033】[0033]

【発明の効果】本発明は以上の通りであって、従来、可
燃性ゴミとして焼却処分されたり、そのまま埋立てられ
ていた廃棄物を、密閉容器内で無酸素状態下で加熱処理
するため、CO2の発生を極力押えることができるので、
Cを固定する廃棄物の無燃焼処理装置としてきわめて有
用である。しかも、排気中の臭気を、排気時に加熱,燃
焼することにより脱臭できるから、悪臭が生じることも
ない。
EFFECTS OF THE INVENTION The present invention is as described above, and in order to heat-treat waste that has been conventionally incinerated as flammable garbage or landfilled as it is in an airtight state in an airtight container, Since the generation of CO 2 can be suppressed as much as possible,
It is extremely useful as a non-combustion treatment device for waste that fixes C. Moreover, since the odor in the exhaust gas can be deodorized by heating and burning during exhaust gas, no bad odor is generated.

【0034】また、本発明装置は、加熱処理中に複数の
フィルタ容器を切換えて使用するようにしたことによ
り、各フィルタの有害ガスの中和,吸着等のガス除去能
力が経時劣化することがあっても、その再生,回復,入
替え等をフィルタ容器群を単位として交互に行うことが
できるので、連続運転が可能であり、また、有害ガス等
の種類に応じて使用するフィルタ容器群を切換えること
ができるので、前記連続運転と相俟って、加熱温度の違
いによって生成する種々異なるガスを連続運転し乍ら逐
次除去することができ、従って、廃棄物を効率よく無害
化処理することが可能になる。
Further, in the apparatus of the present invention, a plurality of filter vessels are switched and used during the heat treatment, so that the gas removal ability of each filter such as neutralization and adsorption of harmful gas may deteriorate with time. Even if there is, the regeneration, recovery, replacement, etc. can be performed alternately for each filter container group, so continuous operation is possible, and the filter container group to be used is switched according to the type of harmful gas, etc. Therefore, in combination with the above continuous operation, various gases generated due to the difference in heating temperature can be successively removed during continuous operation, and therefore waste can be efficiently detoxified. It will be possible.

【0035】更に、残渣分として生じる炭化物は、無
害,無臭であるため、そのまま活性炭や黒鉛としても利
用することができるので、他の産業分野で有用される。
Further, since the carbide generated as a residue is harmless and odorless, it can be used as it is as activated carbon or graphite, so that it is useful in other industrial fields.

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

【図1】本発明処理装置の一例の概要を示すシステムブ
ロック図。
FIG. 1 is a system block diagram showing an outline of an example of a processing apparatus of the present invention.

【図2】吸引式フィルタの構成例を示す断面図。FIG. 2 is a cross-sectional view showing a configuration example of a suction filter.

【符号の説明】[Explanation of symbols]

1 処理容器 1a 内側容器 1b 空間層 1c 外側容器 1d 温度センサ 2 投入口 3 取出口 5 熱供給部 5a 熱導入路 5b 熱量コントロ−ル 5c 排熱路 5d 開閉バルブ 6,61〜65 排気管 71,72 フィルタ容器 7A,7B フィルタ容器群 71a,72a 中和剤,濾過剤 71b,72b 空間 71c,72c モ−タ 71d,72d 混合板 71e,72e 軸 71f,72f pHセンサ 8 吸引ファン式の排気装置 9 受熱部 F 廃棄物 1 Processing container 1a Inner container 1b Space layer 1c Outer container 1d Temperature sensor 2 Input port 3 Outlet 5 Heat supply part 5a Heat introduction path 5b Heat quantity control 5c Exhaust heat path 5d Open / close valve 6,61-65 Exhaust pipe 71, 72 Filter container 7A, 7B Filter container group 71a, 72a Neutralizing agent, filter agent 71b, 72b Space 71c, 72c Motor 71d, 72d Mixing plate 71e, 72e Shaft 71f, 72f pH sensor 8 Suction fan type exhaust device 9 Heat receiving part F Waste

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 B01D 53/38 53/81 53/74 C01B 31/02 101 Z B01D 53/34 116 J 116 H B09B 3/00 ZAB ─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 6 Identification code Internal reference number FI Technical display location B01D 53/38 53/81 53/74 C01B 31/02 101 Z B01D 53/34 116 J 116 H B09B 3/00 ZAB

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 廃棄物を収容し脱酸素又は空気遮断状態
下で所要温度まで加熱してその温度を所要時間保持でき
るようにした密閉加熱容器と、上部に空間を残して中和
剤などの液状濾過体を収容すると共に、前記密閉加熱容
器に接続されるガス導入パイプが前記濾過体中に位置付
けられ、かつ、前記上部空間に外部から吸引力を作用さ
せるようにした複数の容器であって、これらの容器を少
なくとも2群に分けて切換可能に前記密閉加熱容器に接
続した吸引式フィルタ容器と、前記各フィルタ容器の上
部空間に吸引力を作用させる吸引装置と、該吸引装置の
排気側に接続され、前記吸引装置から排出される排気ガ
スを加熱,燃焼部を通過させて脱臭する脱臭部とから成
ることを特徴とする廃棄物の処理装置。
1. A closed heating container which accommodates waste and is heated to a required temperature under a deoxygenated or air-shielded condition so as to maintain the temperature for a required time, and a space such as a neutralizer for leaving a space above the container. A plurality of containers, each containing a liquid filter body, wherein a gas introduction pipe connected to the closed heating container is positioned in the filter body, and a suction force is applied to the upper space from the outside. A suction type filter container in which these containers are divided into at least two groups and switchably connected to the closed heating container, a suction device for exerting a suction force on the upper space of each filter container, and an exhaust side of the suction device. And a deodorizing unit that is connected to the degassing unit for heating and exhausting the exhaust gas discharged from the suction device to deodorize the exhaust gas.
【請求項2】 複数の吸引式フィルタ容器は、少なくと
も2個を直列接続した2組以上のフィルタ容器群により
形成し、各群のフィルタ容器における先頭に位置した吸
引式フィルタ容器をガス導入パイプの始端側に切換弁を
介して密閉加熱容器に並列に接続する一方、各群の最後
に位置した吸引式フィルタ容器の上部空間に吸引装置の
吸引側を接続した請求項1の廃棄物の処理装置。
2. The plurality of suction type filter containers are formed by two or more sets of filter container groups in which at least two are connected in series, and the suction type filter container positioned at the head of the filter containers of each group is connected to a gas introducing pipe. The waste treatment device according to claim 1, wherein the suction end of the suction device is connected to the upper space of the suction type filter container located at the end of each group while being connected in parallel to the closed heating container via the switching valve at the start end side. .
【請求項3】 各群の吸引式フィルタ容器の切換えは、
各フィルタ容器内の液状濾過体のpH値により切換える
ようにした請求項2の廃棄物の処理装置。
3. Switching of the suction type filter container of each group,
3. The waste treatment device according to claim 2, wherein the switching is performed according to the pH value of the liquid filter in each filter container.
JP5348667A 1993-12-27 1993-12-27 Device for treating combustible waste Pending JPH07185502A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5348667A JPH07185502A (en) 1993-12-27 1993-12-27 Device for treating combustible waste

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5348667A JPH07185502A (en) 1993-12-27 1993-12-27 Device for treating combustible waste

Publications (1)

Publication Number Publication Date
JPH07185502A true JPH07185502A (en) 1995-07-25

Family

ID=18398551

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5348667A Pending JPH07185502A (en) 1993-12-27 1993-12-27 Device for treating combustible waste

Country Status (1)

Country Link
JP (1) JPH07185502A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6875317B1 (en) 1999-03-03 2005-04-05 Jiro Toyoda Waste treating method

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6875317B1 (en) 1999-03-03 2005-04-05 Jiro Toyoda Waste treating method

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