JPH11293254A - Apparatus and process for reductive pyrolytic carbonization of combustible waste - Google Patents
Apparatus and process for reductive pyrolytic carbonization of combustible wasteInfo
- Publication number
- JPH11293254A JPH11293254A JP10130945A JP13094598A JPH11293254A JP H11293254 A JPH11293254 A JP H11293254A JP 10130945 A JP10130945 A JP 10130945A JP 13094598 A JP13094598 A JP 13094598A JP H11293254 A JPH11293254 A JP H11293254A
- Authority
- JP
- Japan
- Prior art keywords
- carbonization
- waste
- reduction
- chamber
- reduction chamber
- 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
Links
Abstract
Description
【0001】[0001]
【発明の属する技術分野】この発明は可燃性廃棄物の熱
分解炭化処理に関する方法である。The present invention relates to a method for pyrolytic carbonization of combustible waste.
【0002】[0002]
【従来の技術】近年、可燃性廃棄物の処理に関してはダ
イオキシンや有害物質を排出する焼却処理の本題点が多
く指摘されている。2. Description of the Related Art In recent years, regarding the treatment of combustible waste, many of the main points of incineration for discharging dioxins and harmful substances have been pointed out.
【0003】焼却処理は排気ガスで大気を汚染し雨水に
より大地や河川をも汚しています。焼却後の残灰は埋め
立て処分をしているが、その管理に問題が多く指摘され
ています。[0003] The incineration process pollutes the atmosphere with exhaust gas and pollutes the earth and rivers with rainwater. The incinerated ash is disposed of in landfills, but many problems have been pointed out in its management.
【0004】そこで、可燃性廃棄物の焼却処理以外の方
法について関心が高まっています、[0004] Therefore, there is increasing interest in methods other than incineration of combustible waste.
【0005】しかし、未だ完全な処理方法が確立してい
ません、固形燃料化でできた燃料はは、その燃料の燃焼
装置が開発されず一般的な普及には時間がかかるようで
す。[0005] However, a complete treatment method has not yet been established. For fuel made from solid fuel, it seems that it will take time to spread the fuel because a combustion device for the fuel has not been developed.
【0006】また、固形化燃料を焼却をすれば残灰は生
じます。[0006] If the solidified fuel is incinerated, residual ash is generated.
【0007】そこで、焼却処理以外の処理方法が求めら
れています。Therefore, there is a demand for a treatment method other than the incineration treatment.
【0008】[0008]
【発明が解決しようとする課題】可燃性廃棄物の処理に
関して焼却処理以外の方法を確立し、環境の汚染をしな
い廃棄物処理を行わなければならない。A method other than incineration must be established for the treatment of combustible waste, and the waste must be treated without causing environmental pollution.
【0009】[0009]
【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、本発明の還元方式の可燃性廃棄物炭化処理装置
は、可燃性廃棄物を燃焼せずに炭化できます。Means for Solving the Problems In order to achieve the above object, the reduction type combustible waste carbonization apparatus of the present invention can carbonize combustible waste without burning it.
【0010】この装置は、廃棄物を定量にして、装置の
入口に設けた還元室に廃棄物を入れて、外部より持ち込
まれた酸素(空気)を還元室にて窒素を充填し無酸素状
態にして炭化処理装置に送ります。In this apparatus, waste is quantified, the waste is put into a reduction chamber provided at the entrance of the apparatus, and oxygen (air) brought in from the outside is filled with nitrogen in the reduction chamber, and the oxygen-free state is obtained. And send it to the carbonization unit.
【0011】炭化処理装置は、予め石油・ガス等の燃焼
や窒素充填等で還元域にしています。[0011] The carbonization equipment is set in the reduction zone in advance by burning oil and gas, filling with nitrogen, etc.
【0012】炭化処理装置には、気化された廃棄物内容
成分を排気するダクトが設けてあります。[0012] The carbonization equipment is provided with a duct for exhausting the vaporized waste content components.
【0013】炭化処理装置の装置内温度は400℃から
500℃に保たれるように還元気体を過熱する装置が有
ります。[0013] There is a device that superheats the reducing gas so that the temperature inside the carbonization device is maintained at 400 to 500 ° C.
【0014】炭化処理装置は、その形状がコンベア一方
式・ターンテーブル方式・バケット方式・連続加熱方式
の4つの方法を処理物の量や質又は、装置をは配置する
スペース等に応じて選択ができます。[0014] The carbonization apparatus can be selected from four methods, one of a conveyor type, a turntable type, a bucket type, and a continuous heating type, depending on the quantity and quality of the material to be processed or the space in which the device is to be arranged. I can do it.
【0015】廃棄物は、炭化処理装置内にて、約400
℃から500℃の温度を60分から200分間の間加熱
を受けて徐々に炭化をしていきます。[0015] The waste is reduced to about 400 in the carbonization equipment.
It is heated from ℃ to 500 ℃ for 60 to 200 minutes and carbonized gradually.
【0016】廃棄物の内容成分は加熱時間の中で気化
し、装置のダクトから排気されます。The components of the waste vaporize during the heating time and are exhausted from the duct of the device.
【0017】排気された内容成分は燃焼せずに吸着剤に
よる回収、又は、水洗され無害の気体になり外気に排出
されます。The exhausted components are not burnt, but are recovered by an adsorbent or washed with water to form harmless gas and discharged to the outside air.
【0018】炭化処理された廃棄物は炭になり装置の出
口の還元室を経由して排出されます[0018] The carbonized waste becomes charcoal and is discharged through the reduction chamber at the outlet of the device.
【0019】排出された炭は、土壌の改良や水の浄化に
利用ができます。The discharged charcoal can be used for soil improvement and water purification.
【0020】[0020]
【発明の実施の形態】以下本発明の実施の形態を説明す
る。まず、図1にて基本的な炭化装置の説明をする。一
般的に炭を作る場合、炉又は竈に木材を入れて点火し、
火力がついて炉又は竈の温度が、ある一定の温度に達し
たら炉又は、竈の入り口をふさぎ放置します。加熱され
た木材は、炉又は竈内の酸素が無くなり燃焼ができなく
なるが室内の温度を受けて気化成分を蒸発させ炭素分が
残ります。本発明の装置は、投入した可燃物に点火せず
1の還元室から 2の炭化処理装置3の還元室に処理
物を移動します。1と3の還元室には窒素を充填させ外
気からの酸素流入を防ぎます。2の炭化処理装置は、装
置内温度を400℃から500℃に保ち窒素充填や加熱
燃焼により還元域にしています。また、3の還元室は炭
化した炭が高温のまま外気に触れますと点火してしまい
ますので、冷却する部屋の役割をしています。Embodiments of the present invention will be described below. First, a basic carbonization device will be described with reference to FIG. In general, when making charcoal, put wood in a furnace or kettle and ignite,
When the temperature of the furnace or kiln reaches a certain temperature due to the heat, close the furnace or kiln entrance and leave it. Heated wood loses oxygen in the furnace or oven and cannot burn, but receives indoor temperature to evaporate vaporized components and leave carbon content. The apparatus of the present invention moves the processed material from the first reduction chamber to the second carbonization processing unit 3 without igniting the combustibles that have been input. The reduction chambers 1 and 3 are filled with nitrogen to prevent inflow of oxygen from outside air. The carbonization treatment unit 2 keeps the temperature in the unit from 400 ° C to 500 ° C and puts it in the reduction zone by filling with nitrogen and heating and burning. In addition, the reduction chamber of No. 3 is ignited when the carbonized charcoal is exposed to the outside air with high temperature, so it serves as a cooling room.
【0021】図2の還元室は、横方向の使用と縦方向の
使用の方法があります。4の入口と5の出口に扉を設け
ています、4の扉は廃棄物の投入時に開きます、4の扉
が開いている場合は、5の扉は閉じています。廃棄物の
投入が終わり、4の扉を閉じて還元室内に窒素を充填し
ます。室内の酸素濃度が概ね5%以下になったら、5の
扉を開き廃棄物は炭化処理装置に入ります。二重扉にす
ることにより、外気を炭化処理装置に流入させません。
二重扉は縦方向のスライド式や横方向のスライド式又は
跳ね上げ扉を使用できます。The reduction chamber shown in FIG. 2 can be used horizontally or vertically. Doors are provided at the entrance 4 and the exit 5 and the door 4 opens when waste is put in. When the door 4 is open, the door 5 is closed. After the waste has been charged, close the door of 4 and fill the reduction chamber with nitrogen. When the oxygen concentration in the room becomes less than about 5%, open door 5 and waste enters the carbonization equipment. The double door prevents external air from flowing into the carbonization equipment.
Double doors can use a vertical sliding type, a horizontal sliding type or a flip-up door.
【0022】炭化処理装置のタイプ(形)は、廃棄物の
連続炭化処理を目的としていますから、図3のコンベア
ー方式・図4のターンテーブル方式・図5のバケット方
式・図6の連続過熱方式の4タイプが利用できます。Since the type (shape) of the carbonization apparatus is intended for continuous carbonization of waste, the conveyor system shown in FIG. 3, the turntable system shown in FIG. 4, the bucket system shown in FIG. 5, and the continuous heating shown in FIG. Four types of methods are available.
【0023】各タイプとも炭化処理装置の基本的機能は
同一ですが、廃棄物の性質や形状にに合わせて各タイプ
が選択できます。また、廃棄物の処理温度設定や処理時
間がその性質で異なるために各タイプの炭化処理装置が
必要になります。Although the basic functions of the carbonization equipment are the same for each type, each type can be selected according to the nature and shape of the waste. In addition, each type of carbonization equipment is required because the temperature setting and the processing time of the waste differ depending on the nature.
【0024】[0024]
【発明の効果】本発明により、可燃性廃棄物が公害を発
生させる焼却処理に依存せず、安全な炭化処理が可能に
なると同時に、本発明の装置より排出(製造)される炭
は燃料や土壌の改良また水の浄化に利用できる。According to the present invention, flammable waste can be safely carbonized without relying on incineration that generates pollution, and at the same time, the coal discharged (produced) from the apparatus of the present invention can be used as fuel or fuel. It can be used for soil improvement and water purification.
【図1】本発明の基本概念説明図である。FIG. 1 is a diagram illustrating the basic concept of the present invention.
【図2】炭化処理装置の前後の還元室の説明図である。FIG. 2 is an explanatory diagram of a reduction chamber before and after a carbonization device.
【図3】炭化処理装置のタイプ(形)別説明図である。FIG. 3 is an explanatory view of each type (shape) of a carbonization apparatus.
─────────────────────────────────────────────────────
────────────────────────────────────────────────── ───
【手続補正書】[Procedure amendment]
【提出日】平成10年7月27日[Submission date] July 27, 1998
【手続補正1】[Procedure amendment 1]
【補正対象書類名】明細書[Document name to be amended] Statement
【補正対象項目名】図面の簡単な説明[Correction target item name] Brief description of drawings
【補正方法】変更[Correction method] Change
【補正内容】[Correction contents]
【図面の簡単な説明】[Brief description of the drawings]
【図1】本発明の基本概念説明図である。FIG. 1 is a diagram illustrating the basic concept of the present invention.
【図2】炭化処理装置の前後の還元室の説明図である。FIG. 2 is an explanatory diagram of a reduction chamber before and after a carbonization device.
【図3】コンベアー方式の炭化処理装置の説明図であ
る。FIG. 3 is an explanatory view of a conveyor type carbonization apparatus.
【図4】ターンテーブル方式の炭化処理装置の説明図で
ある。FIG. 4 is an explanatory view of a turntable type carbonization apparatus.
【図5】バケット方式の炭化処理装置の説明図である。FIG. 5 is an explanatory diagram of a bucket type carbonization apparatus.
【図6】連続過熱方式の炭化処理装置の説明図である。FIG. 6 is an explanatory diagram of a continuous superheating type carbonization apparatus.
【符号の説明】 図1より 1〜還元室 入口 2〜炭化処理装置 3〜還元室 出口 図2より 4〜扉 5〜扉[Description of References] From FIG. 1 1-Reduction chamber inlet 2-Carbonization treatment device 3-Reduction chamber outlet From Fig. 2 4-Door 5-Door
Claims (5)
を送り込む入口と排出する出口に、二重扉を持つ還元室
を設ける。還元室の二重扉は、入口扉と出口が同時に解
放しない構造にして、還元室内に窒素を充填し無酸素室
とし炭化処理装置に外気が流入することを防ぐ装置1. A reduction chamber having a double door is provided at an inlet for sending waste to an apparatus for carbonizing flammable waste and an outlet for discharging waste. The double door of the reduction chamber has a structure in which the inlet door and the outlet do not open at the same time, and the reduction chamber is filled with nitrogen to make it an oxygen-free chamber to prevent outside air from flowing into the carbonization equipment.
された無酸素空気又は窒素充填した還元域の部屋になっ
ている、その装置内温度は400℃から500℃程度に
保たれ、投入された廃棄物は連続して入口から出口に移
動をして炭化処理される。その廃棄物の移動方法一つ
が、コンベア一方式であります。炭化処理装置をダクト
状又は、パイプ状にしてエンドレスチェーンを通し、請
求項1の無酸素室内の容量が収納できる容積を1スパン
としたプレート設けたスクレパータイプのコンベアー方
式であります。2. The combustible waste carbonization apparatus is a room in a reduction zone filled with heated oxygen-free air or nitrogen. The temperature inside the apparatus is maintained at about 400 ° C. to about 500 ° C. The wastes are continuously moved from the inlet to the outlet and carbonized. One method of transferring waste is a conveyor system. This is a scraper type conveyor system with a plate that has a 1-span capacity that can store the capacity of the anoxic chamber according to claim 1 by passing the carbonization processing unit through a duct or a pipe and passing through an endless chain.
て、廃棄物は請求項1の還元室の容量が収納できる、炭
化処理装置の円周を6から8当分した装置内の箱に投入
して、円筒形の炭化処理装置の底部が回転するターンテ
ーブルにて移動し炭化するターンテーブル方式。3. The carbonization treatment apparatus is formed in a columnar shape, and the waste is put into a box in the apparatus in which the circumference of the carbonization treatment apparatus can be accommodated by 6 to 8 in which the capacity of the reduction chamber according to claim 1 can be stored. In addition, a turntable system in which the bottom of a cylindrical carbonization device moves and carbonizes on a rotating turntable.
廃棄物を予めバケットに入れてバケットごと装置内を移
動して炭化するバケット方式4. The shape of the carbonization device is made rectangular,
Bucket method in which waste is put in a bucket in advance and carbonized by moving the entire bucket inside the device
連続的に配置し各部室ごとに加温して炭化する連続加熱
方式、(この場合廃棄物はバケットにて移動するが温度
降下が遅い廃棄物に利用できる)5. A continuous heating system in which a carbonization treatment device is provided by continuously arranging the reduction chambers of claim 1 and heating and carbonizing each of the chambers (in this case, the waste moves in a bucket, but the temperature drops. (Available for late waste)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10130945A JPH11293254A (en) | 1998-04-06 | 1998-04-06 | Apparatus and process for reductive pyrolytic carbonization of combustible waste |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10130945A JPH11293254A (en) | 1998-04-06 | 1998-04-06 | Apparatus and process for reductive pyrolytic carbonization of combustible waste |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH11293254A true JPH11293254A (en) | 1999-10-26 |
Family
ID=15046348
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP10130945A Pending JPH11293254A (en) | 1998-04-06 | 1998-04-06 | Apparatus and process for reductive pyrolytic carbonization of combustible waste |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH11293254A (en) |
-
1998
- 1998-04-06 JP JP10130945A patent/JPH11293254A/en active Pending
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