JPH02238209A - Combustion treatment device for waste refuse with synthetic resin attached apparatus for incinerating synthetic resin-including waste - Google Patents
Combustion treatment device for waste refuse with synthetic resin attached apparatus for incinerating synthetic resin-including wasteInfo
- Publication number
- JPH02238209A JPH02238209A JP5922689A JP5922689A JPH02238209A JP H02238209 A JPH02238209 A JP H02238209A JP 5922689 A JP5922689 A JP 5922689A JP 5922689 A JP5922689 A JP 5922689A JP H02238209 A JPH02238209 A JP H02238209A
- Authority
- JP
- Japan
- Prior art keywords
- incinerator
- chamber
- synthetic resin
- incineration
- waste
- 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.)
- Granted
Links
- 238000002485 combustion reaction Methods 0.000 title claims abstract description 36
- 229920003002 synthetic resin Polymers 0.000 title claims abstract description 13
- 239000000057 synthetic resin Substances 0.000 title claims abstract description 13
- 239000002699 waste material Substances 0.000 title claims abstract description 12
- 239000002184 metal Substances 0.000 claims abstract description 14
- 229910052751 metal Inorganic materials 0.000 claims abstract description 14
- 238000004140 cleaning Methods 0.000 claims description 47
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 42
- 239000000498 cooling water Substances 0.000 claims description 16
- 230000005855 radiation Effects 0.000 claims description 15
- 238000005192 partition Methods 0.000 claims description 9
- 238000001816 cooling Methods 0.000 claims description 6
- 239000002440 industrial waste Substances 0.000 claims description 5
- 238000005338 heat storage Methods 0.000 claims 1
- 239000007789 gas Substances 0.000 abstract description 47
- 239000000567 combustion gas Substances 0.000 abstract description 14
- 238000011084 recovery Methods 0.000 abstract description 4
- 239000011819 refractory material Substances 0.000 abstract description 2
- 238000005406 washing Methods 0.000 description 15
- 239000000428 dust Substances 0.000 description 11
- 239000000463 material Substances 0.000 description 11
- 238000000034 method Methods 0.000 description 10
- 239000010802 sludge Substances 0.000 description 8
- 238000002347 injection Methods 0.000 description 7
- 239000007924 injection Substances 0.000 description 7
- 239000007921 spray Substances 0.000 description 6
- 230000017525 heat dissipation Effects 0.000 description 5
- 238000003860 storage Methods 0.000 description 5
- 239000004020 conductor Substances 0.000 description 4
- 239000007787 solid Substances 0.000 description 4
- 239000002023 wood Substances 0.000 description 3
- 238000004891 communication Methods 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 230000005070 ripening Effects 0.000 description 2
- 229910000975 Carbon steel Inorganic materials 0.000 description 1
- 229910001018 Cast iron Inorganic materials 0.000 description 1
- KZBUYRJDOAKODT-UHFFFAOYSA-N Chlorine Chemical compound ClCl KZBUYRJDOAKODT-UHFFFAOYSA-N 0.000 description 1
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical group [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- 208000010201 Exanthema Diseases 0.000 description 1
- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical compound [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 description 1
- 230000001174 ascending effect Effects 0.000 description 1
- 238000009933 burial Methods 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000010962 carbon steel Substances 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 238000010612 desalination reaction Methods 0.000 description 1
- 238000006477 desulfuration reaction Methods 0.000 description 1
- 230000023556 desulfurization Effects 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 201000005884 exanthem Diseases 0.000 description 1
- 230000009970 fire resistant effect Effects 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 239000003779 heat-resistant material Substances 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000007769 metal material Substances 0.000 description 1
- 239000010814 metallic waste Substances 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 206010037844 rash Diseases 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 239000006228 supernatant Substances 0.000 description 1
- 239000008400 supply water Substances 0.000 description 1
- 238000004056 waste incineration Methods 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
Landscapes
- Incineration Of Waste (AREA)
- Gasification And Melting Of Waste (AREA)
Abstract
Description
【発明の詳細な説明】
産業上の利用分野:
本発明は主として金属物品に合成樹脂が付着した廃棄物
の焼却処理装置に関するものであり、特に合成樹脂被覆
電線屑などの焼却処理に伴う排ガスを、効果的に処理で
きるように改良した装置である.
従来の技術:
1.C来、各種電線の不用品(電線製造工場などから送
り出される電線の切れ端、不合格電線など)あるいは電
気工事に際して生じる古電線、廃棄処分される各種機器
に付着した電線などの産業廃棄物は,これを集めて焼却
処理し、銅線その池金属部分を回収する方法が、最も能
率のよい処理手段として採用されている.しかしながら
、電線被覆材として塩1ヒビニル樹脂が最も多く使用さ
れており、したがって焼却にともなって塩素ガス等の有
害ガスを発生するので、これによる排ガス処理・炉壁の
損傷による焼却炉の耐久性の低下等各種の問題点がある
.このような問題点を解決するために,既に多くの解決
手段が組み込まれた,合成樹脂付着の廃棄物を焼却処理
する装置が提案され,実川に洪されている.
解決しようとする課題:
このような産業廃棄物の力゛L却処理装置においては,
大型の塵埃焼却炉と異なって比較的小型の装置に纏める
必要上(主に専用の焼却怨埋シ1置として設置している
)、過大な構造にすることが困ffliで、また有害ガ
スの発生を低減させるために、焼却炉内温度を高めると
炉壁の損耗が激しくなり、どうしても局部的に損出する
ことになり易・く、さらに燃焼後の排ガス中に含まれる
有害ガス成分の処理についても、その処理装置が7’2
雑1ヒし,さらに処理水を多量に必要とした.
また、被処理廃棄物を焼却処理した場合、IjC来は、
その焼却済み金属部を取り出すのに、焼却作業終了後に
炉内から取り出す処理を行っている関係上,連続的に処
理するのが困難で、大型の′OJi処FW物や多量の披
処理物を取り扱うには不都合であつた.
課題を解決するための手段:
本発明では、焼却炉を二段に配して、被処理物は耐熱性
を有した受け入れ容2コを備えた台車に載せて,一次焼
却炉内でけ着合成樹脂の焼却を行うようにし、二次焼却
炉では炉内でガスを滞留させないようにして二次燃焼さ
せ、その後この燃焼ガスの温度を低下させて,ガス洗浄
部に送り,合理的に洗浄して有害成分の除去処理ができ
るようにし,一次焼却炉内で焼却済みの残留金属部は、
所要時間経過後に炉外に送り出して、洗浄水の一部を利
用して水洗冷却処理し、処理水を口】鎖サイクルで使用
すると共に、金萬材を有効回収でき、炉内の耐久性も低
下させることなく運転できるように構成した焼却処理装
置を提供することにある.すなわち、本発明は,合成樹
脂が付着した金属物からなる産業廃棄物の焼却処理装置
において:焼却炉は、1・ンネル炉型の一次焼却炉と、
円筒状の炉体を上下二室にtk tjJって、下室が前
記一次焼却炉と接続される二次燃焼室で、下室が放熱室
に形成した二次焼却炉とで構成され:該二次焼却炉の放
熱室ガス出口に、サイクロンを介して、シャワーリング
室および充填層を上下に組み合わせてなる塔形スクラツ
バーと、洗浄水循環機横と、からなる排ガス洗浄装置を
接続して.らり;披処}l1j物は台車に搭載した耐熟
性容2″:iに投入して前記一・次焼却炉に送り込むよ
うにし、焼却炉内からINり出した前記容器に対して、
排ガス洗浄装置の循環洗浄水の一部を用いて冷却処理す
る機措分、一次焼却炉の出口外に配設した;構成である
ことを特徴とする.
本発明における焼却炉は、1・ンネル炉型の一次焼却炉
と、円筒状の炉木を上下二室に区画して、その上室が二
次燃焼室で、下室が放熱室に形成した二次焼却炉とで構
成してあり;該二次焼却炉は、上部の二次燃焼室に対し
て一次焼却炉からのガス導入口が接線方向に設けてあり
、そのガス導入口近mにバーナを配設し、該二次燃焼室
中心に」一部で開口する導通筒を放熱室に連通ずるよう
に立股してあり、放熱室内には、同心円上で腹列に多数
の耐火ブロック体を断続的に設けてある.また、二次焼
却炉における二次燃焼室と放熱室とを仕切る佳切り壁は
、その内部に冷却水の通路を全面に配設した楢成とし、
該a−切り壁の耐久性を高めるようにした。DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application: The present invention mainly relates to an apparatus for incinerating waste in which synthetic resin has adhered to metal articles, and in particular to an apparatus for incinerating waste such as synthetic resin-coated wire scraps. This is a device that has been improved so that it can be processed effectively. Conventional technology: 1. Since then, industrial waste such as various types of unnecessary electric wires (cut ends of electric wires sent from electric wire manufacturing factories, rejected electric wires, etc.), old electric wires generated during electrical work, and electric wires attached to various types of equipment to be disposed of are The most efficient method of disposal is to collect this, incinerate it, and recover the copper wire and metal parts. However, salt-1 hibinyl resin is most commonly used as a wire coating material, and as a result, it generates harmful gases such as chlorine gas when incinerated, which reduces the durability of the incinerator due to exhaust gas treatment and damage to the furnace walls. There are various problems such as decline. In order to solve these problems, a device that incinerates waste with synthetic resin adhering to it has already been proposed and is being used in the river. Problems to be solved: In such industrial waste power treatment equipment,
Unlike large dust incinerators, it is necessary to combine them into a relatively small device (mainly installed as a dedicated incinerator and burial chamber), so it is difficult to build an excessively large structure, and it is difficult to produce harmful gases. In order to reduce emissions, increasing the temperature inside the incinerator will cause severe wear and tear on the incinerator walls, which tends to cause localized losses.In addition, it is necessary to treat harmful gas components contained in the exhaust gas after combustion. Also, the processing equipment is 7'2
It caused a lot of damage and required a large amount of treated water. In addition, if the waste to be treated is incinerated, IJC will
In order to take out the incinerated metal parts, it is difficult to process them continuously because the process is to take them out of the furnace after the incineration process is finished, and it is difficult to process them continuously. It was inconvenient to handle. Means for Solving the Problems: In the present invention, the incinerator is arranged in two stages, and the materials to be treated are placed on a trolley equipped with two heat-resistant receiving spaces, and the materials are dumped in the primary incinerator. Synthetic resin is incinerated, and the secondary incinerator burns the gas to prevent it from stagnation in the furnace.Then, the temperature of this combustion gas is lowered and sent to the gas cleaning section where it can be cleaned rationally. The remaining metal parts that have been incinerated in the primary incinerator are
After the required time has elapsed, it is sent outside the furnace, and a part of the cleaning water is used for washing and cooling treatment, and the treated water is used in a chain cycle, which allows for effective recovery of metal materials and reduces the durability of the inside of the furnace. The purpose of the present invention is to provide an incineration treatment device configured so that it can be operated without any problems. That is, the present invention provides an apparatus for incinerating industrial waste made of metal objects to which synthetic resin is attached: The incinerator includes: 1. a tunnel furnace type primary incinerator;
The cylindrical furnace body has two upper and lower chambers, the lower chamber is a secondary combustion chamber connected to the primary incinerator, and the lower chamber is a secondary incinerator formed into a heat radiation chamber. An exhaust gas cleaning device consisting of a tower-shaped scrubber consisting of a showering chamber and a packed bed combined above and below, and a washing water circulator next to it, is connected to the gas outlet of the heat radiation chamber of the secondary incinerator via a cyclone. The material is put into a ripening-resistant container 2'':i mounted on a trolley and sent to the primary incinerator, and the container taken out from the incinerator is
The system is characterized by a configuration in which the cooling process is performed using part of the circulating cleaning water of the exhaust gas cleaning system, and is located outside the outlet of the primary incinerator. The incinerator in the present invention has a tunnel furnace type primary incinerator and a cylindrical furnace wood divided into two upper and lower chambers, with the upper chamber serving as a secondary combustion chamber and the lower chamber serving as a heat dissipation chamber. The secondary incinerator has a gas inlet from the primary incinerator tangentially connected to the upper secondary combustion chamber, and the gas inlet is located near the gas inlet. A burner is arranged, and in the center of the secondary combustion chamber, there is a partially open conduction cylinder that stands upright so as to communicate with the heat radiation chamber, and inside the heat radiation chamber, there are many refractory blocks arranged in diagonal rows on a concentric circle. The body is provided intermittently. In addition, the partition wall that partitions the secondary combustion chamber and the heat dissipation chamber in the secondary incinerator is made of a partition wall with cooling water passages all over the inside.
The durability of the a-cut wall was increased.
さらに、本発明における排ガス洗浄装置の塔形スクラツ
バーは、最下層に洗浄空室を配し、その上側に充填層室
を、さらにその上側に充分広い洗浄室をそれぞれ配し、
該洗浄室では中心に配した洗浄木管から放射状に、かつ
多段で洗浄水が噴射される多1’<の噴霧ノズルが配さ
れた構成としたのである。Furthermore, the tower-shaped scrubber of the exhaust gas cleaning device according to the present invention has a cleaning chamber in the lowest layer, a packed bed chamber above it, and a sufficiently wide cleaning chamber above it,
The cleaning chamber is configured to have multiple spray nozzles that spray cleaning water radially and in multiple stages from a cleaning wood pipe placed in the center.
作 用 :
本発明の焼却処理装置は,耐火性を備えた上面開放型の
容器搭載台車に、被処理物を投入搭社して、■・ンネル
型一次焼却炉内に送り込んで焼却する.この一次焼却炉
内で発生した一次燃焼ガスは、二次焼却炉の二次燃焼室
に導入され、該燃焼室内で二次燃焼して一次側よりも高
い温度で有害ガス成分の分解を泥進させる.この燃焼室
内では、燃拉効果を高めるために導入した一次燃焼ガス
に旋回流を与え、その旋回流によってS;}留時間を長
くして、バーナによって一次燃焼ガスを再燃焼さCて完
全燃焼させるようにする.
この二次燃焼室内で燃焼して高温になったガスは,導通
崎上部開口部分からこれに連通ずる放熟室内に流下し、
該放熱室内に配置されているブロック間の通+1”+f
を移動する間に,そのブロックと接して熱交換し、ガス
出口からガス洗浄処理装置fullI\移行する。二次
焼却炉の放熱室出口から排出されたガスは、サイクロン
内に入ってダス1・が分漬され、次いで塔形スクラツバ
ーの洗浄空室内に3’tり込まれると,洗浄水と接触し
て次第に冷却・和されることになる.すなわち、充填層
の内部を上昇する間に流れ落ちる洗浄水と充填物の?4
面で接触して徐々に洗汀され、次いで洗浄室に移行する
と洗浄水と接触してダスI・は凝鳴し、充填層内を下降
して集められ、洗浄水の噴霧によって洗われたガスは、
同時に温度が低下して大気中に放出される.
また、この洗浄処理装置において使用されている洗浄水
は、循環使用されるので、次第にダストが収集し、アル
カリ濃度も低下するから、当然新しい洗浄水の補給が行
われる.しかし、収集されたダス1・は、泥状になって
その処理が困難であるが、本発明ではこの汚泥を沈降さ
せて廃棄することなく,汚泥濃度が高くなった水を取り
出して、一次焼却炉から引き出した焼却済みの台車搭載
容器に対して、前記のil7泥水を注水し、容器を冷却
するのに筺用する.このようにすれば、汚泥を含んだ水
が高温である容器とその内部に残った金属物を冷却する
際の熱交換で水分だけが蒸発し、ダス1・がそのまま乾
燥して収り残される.したがって,汚泥水の処理を別個
に行うことなしに、処理できることになり、併せて速や
かに焼却済みの金属残留物が回収処理できることになる
.これとは別に、二次焼却炉は上下二室に仕切られたそ
の陸切り壁内に、冷却水の通路を饅けて、運転中は常時
冷却水を通水することにより、炉内の温度が上昇しても
、この仕切り壁は蓄熱することがな< . li’e−
》て高錫に曝されても長期曲用に耐えることになる.
また,1・冫ネル型一次焼却炉においては、被処理容器
搭載台車が一方から他方へ,いわゆる通り抜けになるよ
うにして、所要時間ごとに出1」側から焼却済みの容器
’t?7栽台車を引き出し、二hに代わって入口側から
新たな被処理物投入の容:拐搭桟台車を送り込んで、炉
の火を落とすことな・く処jlできる.
実 施 例
以下本発明処理装置を一実施例について図面により説明
すれば、次の通りである。Function: In the incineration treatment equipment of the present invention, the materials to be treated are loaded onto a fire-resistant, open-topped container-mounted trolley, and then sent into a tunnel-type primary incinerator for incineration. The primary combustion gas generated in this primary incinerator is introduced into the secondary combustion chamber of the secondary incinerator, where it undergoes secondary combustion and decomposes harmful gas components at a higher temperature than the primary side. Let. In this combustion chamber, a swirling flow is given to the primary combustion gas introduced in order to enhance the combustion effect, and the swirling flow lengthens the residence time, and the primary combustion gas is re-burned by the burner, resulting in complete combustion. Let them do it. The high-temperature gas that burns in this secondary combustion chamber flows down from the upper opening of the conductor into the ripening chamber that communicates with it.
Communication between blocks placed in the heat dissipation chamber +1”+f
While moving, the gas exchanges heat with the block, and transfers from the gas outlet to the gas cleaning treatment device. The gas discharged from the outlet of the heat dissipation chamber of the secondary incinerator enters the cyclone, where the dust 1 is separated, and then enters the washing cavity of the column-shaped scrubber by 3', where it comes into contact with washing water. It will be gradually cooled and softened. i.e. the wash water and the filling that flows down while rising inside the packed bed? 4
The gas is gradually washed in contact with the surface, and then transferred to the washing chamber where it condenses on contact with washing water, descends in the packed bed, is collected, and is washed by the spray of washing water. teeth,
At the same time, the temperature drops and it is released into the atmosphere. Furthermore, since the cleaning water used in this cleaning treatment equipment is recycled, dust is gradually collected and the alkaline concentration decreases, so naturally new cleaning water must be replenished. However, the collected dust 1 becomes sludge and is difficult to dispose of, but in the present invention, the sludge does not settle and is disposed of, but the water with a high sludge concentration is taken out and subjected to primary incineration. The above-mentioned il7 slurry water is poured into the incinerated container mounted on the trolley pulled out from the furnace, and the container is used to cool the container. In this way, only the moisture evaporates through heat exchange when the sludge-containing water cools the high-temperature container and the metal objects left inside, and the dust 1 remains as it is, drying out. .. Therefore, sludge water can be treated without separate treatment, and at the same time, incinerated metal residues can be quickly recovered and treated. Separately, the secondary incinerator is divided into upper and lower chambers, and a cooling water passage is installed in the land partition wall, and cooling water is constantly passed through it during operation to maintain the temperature inside the furnace. Even if the temperature rises, this partition wall will not accumulate heat. li'e-
》It can withstand long-term use even if exposed to high levels of tin. In addition, in the 1/2 channel type primary incinerator, the trolley carrying the containers to be treated is passed from one side to the other in a so-called "passing" manner, and the incinerated containers are output from the 1" side every required time. 7.You can pull out the cultivar and send in the new material to be processed from the entrance side in place of the 2nd h. Embodiment Hereinafter, one embodiment of the processing apparatus of the present invention will be explained with reference to the drawings.
第1図に示すのは、本発明焼却処理装置の概要図であっ
て、10は1・ンネル型の一次焼却炉,2f〕は上下二
室に区画した円筒状の二次焼却炉で16ろ.30は排ガ
ス洗浄装置であって、サイクロン31と、排風機32と
、塔形スクラツバ−35と、洗浄7}C Q%給逅環a
横40とで構成゛されている.
一次焼却炉10は、その全長が少なくとも被処理物を投
入する容器搭載台車15を複数収容できる長さを有し、
入口側と出口側とに扉を備えたl・ンネル型炉になって
いる。Fig. 1 is a schematic diagram of the incineration processing apparatus of the present invention, in which 10 is a tunnel-type primary incinerator, 2f is a cylindrical secondary incinerator divided into two upper and lower chambers, and 16 is a tunnel-type primary incinerator. .. 30 is an exhaust gas cleaning device, which includes a cyclone 31, an exhaust fan 32, a tower-shaped scrubber 35, and a cleaning 7}CQ% feeding ring a.
It consists of 40 horizontal sections. The primary incinerator 10 has a total length that can accommodate at least a plurality of container-mounted carts 15 into which the materials to be treated are loaded,
It is a tunnel type furnace with doors on the inlet and outlet sides.
この一次焼却炉10に被処理物を送り込んで焼却するの
に、被処理物は耐熱性材科《たとえば炭素鋼板、鋳鉄》
で製作された容器16に入れ、この容器16を台車15
に搭載して焼却炉10の入口側から枚数、炉内に送り込
み、焼却された後は台車15を1白づつ出口側から引き
出すようにして処理する.なお、台車15の移動部分は
炉内床部を掘り下げて、直火に曝され難いようにしてお
けば、損fiが低減ずる.また、台車15に搭載する容
器16は、繰り返し使用することになるので、必要に応
じて耐火材を内張リしたものを使用することもできる.
二次焼却炉20は円崎状をした炉木の内部中間位置で、
上下二室に仕切られており、その上側の室が二次燃焼室
21に、下側の室が放熱室22になっている.上側の二
次燃焼室21は、中央に適宜直径の導通[24を仕切り
壁23から立設してあり、前記一次焼却炉10上部から
の煙道11が、接線方向に開口部を絞って繋がれている
.また、煙道11からの入口12から適宜離れた位置に
、バーナ26が配設してある.炉体内下側の放熱室22
は、前記導通簡2・1を通じて二次燃4;″t室21と
連通しており、内部に耐火煉瓦等の耐火物で形成したブ
ロック27を同心円で複数列、断続的に配設してあり、
二次燃焼したガスが該ブロック27間を通過する間に,
放熱してガス出口28に移動するようにしてある。When the material to be treated is sent to this primary incinerator 10 and incinerated, the material to be treated is made of heat-resistant material (for example, carbon steel plate, cast iron).
The container 16 is placed in a container 16 manufactured by
A number of sheets are loaded into the incinerator 10 from the entrance side and fed into the furnace, and after being incinerated, the cart 15 is pulled out one by one from the exit side for disposal. Incidentally, if the movable part of the cart 15 is dug into the floor of the furnace so that it is not easily exposed to direct flame, the loss fi will be reduced. Further, since the container 16 mounted on the trolley 15 will be used repeatedly, it may be lined with a fireproof material if necessary.
The secondary incinerator 20 is located at an intermediate position inside the furnace wood shaped like a circle.
It is divided into two upper and lower chambers, with the upper chamber serving as a secondary combustion chamber 21 and the lower chamber serving as a heat radiation chamber 22. The upper secondary combustion chamber 21 has a conductor [24] of an appropriate diameter erected from the partition wall 23 in the center, and the flue 11 from the upper part of the primary incinerator 10 is connected by narrowing the opening in the tangential direction. It is. Further, a burner 26 is arranged at a position appropriately away from the inlet 12 from the flue 11. Heat radiation chamber 22 at the bottom of the furnace body
is in communication with the secondary combustion chamber 21 through the conductive strip 2.1, and blocks 27 made of refractory material such as firebricks are disposed intermittently in a plurality of concentric rows inside. can be,
While the secondary combustion gas passes between the blocks 27,
It is designed to radiate heat and move to the gas outlet 28.
このような゜二次燃焼炉20の上下を区UJJるIt:
Ulり壁23は、その内部に冷却水が流れる通ノ1ク
クi’2:{aを,尋通筒24の開口部を除く全域にわ
たり埋設し、この通水管23aの冷却水人口231)か
ら冷却l{ζ11冒]23cに、冷却水が流動するよう
にしてある.また、放熱室22内のブロック27に対し
ても,その内部に冷却水を通すようにしておけば,熱交
換速度含高めることができる.
二次焼却炉20の放熱室22ガス出口28がら排出した
排ガスは、排ガス洗浄処理装置3oのサイク1コン31
にーダクト33を通じて送り込まれ、このサイクロン3
1内で排ガス中にかまれるダス1・が分離されるように
する.この排ガスは排風機32によってダク1・34を
通り、塔形スクラツバ−35の最下部洗浄空室36内に
送り込まれるようにする.塔形スクラツバ−35は、下
部から洗浄空室36、ラシヒリングを充填した充填層室
37、洗浄水を噴霧させて洗浄する洗浄室38、ワイヤ
ーデミスター39を配置してミス1・を同r’l’する
排気がらミス1・を補集するようにして処理する排気室
39゜の順に組立られており、頂部に排気@39”を備
えている.前記洗浄室38は、その中心部で、多段にか
つ放射状に噴霧ノズル38”付設した洗浄水噴射管38
゜が立設してあり、この洗浄水噴射管38′には塔外が
ら、洗浄水供給循環機横40の洗浄水(4+,給管41
により、周知のアルカリ性洗浄水を供給するようにして
あり,該洗浄室38で噴霧されてガス洗浄した洗浄水は
、そのままラシヒリング充填[37に、多孔板37゜の
各孔部から流れ落ちて、流入下降し、その充填層37内
ラシしリングの表面に濡れ面を形成して、上昇する排ガ
スとの接触を良くする.この充填層37を流下した洗浄
水は、そのまま洗浄空室36内に流れ落ち、該洗浄空室
36底部で集められて貯水槽42に戻されるようにして
ある.この貯水槽42の底部には洗浄によって落とされ
たダス1・が沈降分離できるようにし、泥状になった濃
度の高い汚泥水は別途ボンプ45によって一次焼却炉1
0の出口外の適所に設けた冷却水噴射管50(第2レ1
v照)に接続してある.・1・1は洗浄水詰環1ノ(給
田のボン1で,貯水槽42内の清澄4ζを吸引して、前
記冷却水噴射管38゛に配管し,給水するようにしてあ
る。It is divided between the upper and lower parts of the secondary combustion furnace 20 like this:
The vertical wall 23 has a passage through which cooling water flows through the entire area except for the opening of the passage pipe 24, and the cooling water flows from the water passage pipe 23a. Cooling water is allowed to flow through the cooling l{ζ11-extension} 23c. Furthermore, if cooling water is allowed to pass through the block 27 in the heat radiation chamber 22, the heat exchange rate can be increased. The exhaust gas discharged from the heat radiation chamber 22 gas outlet 28 of the secondary incinerator 20 is transferred to the cycle 1 controller 31 of the exhaust gas cleaning treatment device 3o.
This cyclone 3 is sent through the duct 33.
The dust trapped in the exhaust gas in the exhaust gas is separated. This exhaust gas is sent through the ducts 1 and 34 by the exhaust fan 32 into the lowest cleaning chamber 36 of the tower-shaped scrubber 35. The tower-shaped scrubber 35 has, from the bottom, a cleaning chamber 36, a packed bed chamber 37 filled with Raschig rings, a cleaning chamber 38 for cleaning by spraying cleaning water, and a wire demister 39 to eliminate mistakes. The cleaning chamber 38 is assembled in the order of exhaust chambers 39 to collect and process the exhaust gas mistakes 1. Cleaning water injection pipe 38 with spray nozzles 38” radially attached
゜ is installed upright, and this wash water injection pipe 38' is connected to the wash water (4+, supply pipe 41
The well-known alkaline cleaning water is supplied, and the cleaning water that has been sprayed and gas-cleaned in the cleaning chamber 38 flows down from each hole in the perforated plate 37 and flows into the Raschig ring filling [37]. As it descends, a wetted surface is formed on the surface of the rash ring within the filling layer 37 to improve contact with the ascending exhaust gas. The cleaning water that has flown down the packed bed 37 flows directly into the cleaning chamber 36, is collected at the bottom of the cleaning chamber 36, and is returned to the water storage tank 42. At the bottom of this water storage tank 42, the dust 1. dropped by washing is allowed to settle and separate, and the highly concentrated sludge water that has become muddy is sent separately to the primary incinerator 45 through a pump 45.
Cooling water injection pipe 50 (second level 1
It is connected to the v-sho).・1.1 is a cleaning water filling ring 1 (a supply tank 1), which sucks the clarified 4ζ in the water storage tank 42, and connects it to the cooling water injection pipe 38' to supply water.
このように構成したことで、たとえば電線屑(古電線な
どら含む)を焼却処理用の容器1(Iに入れて白車l5
に搭載し、一次焼却炉10内に送り込む.この一次焼却
炉10内では、比較的低い温度(8oOC゜程度)で合
成樹脂部分を焼却する,燃焼ガスは煙道11を通って二
次焼却炉20の二次燃焼室21に流入する.この際.二
次燃焼室21の入口l2は、接線方向に、かつ開口部を
絞って構成してあるから、流入した一次燃焼ガスは、旋
回流となって、該二次燃焼室21で滞留することなく流
動し、この間に付設されているバーナ26により再燃焼
される.この際バーナ26の火焔は流入するガスと接触
するのに有効な方向に噴出され、流入ガスと速やかに反
応して燃焼速度を高め得る.この二次燃焼室21内では
燃焼ガスが約1200゜Cに高まり、周知のように有害
ガス成分を熱分解させる.この燃焼室21での燃焼ガス
は旋回しつつ上昇して、導通筒24上端開口部から該導
通簡24内を通り、下側の放熱室22に流入する.この
放悲室22においては、流入した燃焼ガスが室内で、同
心円にて複数列断続して設けてあるブロック27間を旋
回流動する間に、該ブロック27と接触して、熱交換し
て放熱し、ガス温度を低下させて出口28からダク1・
33に流出移動する。したがって、前記したようにブロ
ック27内に冷却71(を通すようにしておけば、ガス
温度を低下させるのに有効である.
なお、二次焼却炉20における仕切り壁23は、その内
部に冷却水を通して壁内部に蓄熱されるのを防止するよ
うにしてあるから、上下画室に温度差が生じていても、
冷却水によって温度勾配を制御することで破損や損耗を
阻止することができる.二次焼却炉20から送り出され
た排ガスは、それに含まれるダス1−が、まずサイクロ
ン31内で分離される.次いで排風機32により塔形ス
クラツバー35の下部洗浄空室36内に送られ、充填層
室37および洗浄室38を通って上部の排気筒かlチ外
部に放出される.
この塔形スクラッパ−35内では、洗浄室38において
,その中心に立設の洗浄水噴射管38゜に設けてある多
数の噴霧ノズル38゜゜がらの噴霧洗(TI水が充填層
37内のラシヒリング間を流下し、これに向流する排ガ
スが洗浄水と接触して、周知の手段で脱塩・脱硫処理さ
れることになる.洗浄室38内での洗浄水の噴霧中を通
って上昇するガスに同(1−シたミスl・は5該洗浄室
38の上側の室に配置したワイヤーデミスター39によ
って補葉され、洗浄済みのガスのみが大気中に排出され
る。117形スクラッパ−35内で洗浄された排ガス中
に含まれる固形物は、洗浄空室36底部の排水管36゛
を経て、貯!■ζ槽42に流入し、ここで沈降分離さ
れる.したがって循環して筺用する洗浄水は上澄水をボ
ン・プl1・1によって汲み出し得るように、該貯水槽
42内には仕切り壁を設けてある.この貯水槽42で分
離して沈降したダス1・等による汚泥水は、別途ボンブ
45によって一次焼却炉10出口外に配役の冷却水噴射
部に送り、焼却後一次焼却炉10出口から取り出した焼
却済みの容器16に注水して冷却するのに使用する.こ
の際汚泥を含む冷却水は水分が蒸発して、固形物のみが
容器や焼却物に付着して乾燥状態で残留する.し・たが
って、この焼却処理後の金属物の回収時に、排ガスに同
1′Pシた固形物も回収することができるから、その処
分は粉本状のものとして処理すればよい.もちろん、こ
の冷却水噴射部の周囲に集塵手段を配して、粉塵として
散逸しない手段をDIA Lでおくことが好ましい.発
明の効果:
本発明によれば、合成樹脂が付着した金属の廃棄物を焼
却処理するのに、これを焼却工程では二段階で処理して
金属部分の回収と燃焼ガスの排ガス処理とを容易にしな
のであり、二次焼却炉においては燃焼室とガス温度を低
下させる放熱室との佳QJり壁内に冷却水を通すように
して、この仕切り壁の損f’sをNj止し、炉体の耐久
性と高める装置とすることができた.また、排ガスの洗
浄工程において発生するダス1・等の汚泥水は、これを
焼却後の金属屑の冷却に使用することで、乾燥固体とし
て回収でき,洗浄水を閉鎖サイクルで曲川できるから,
洗浄排水のための処理設備を・ピ・要とぜず、合理化が
図れることになる.With this configuration, for example, electric wire scraps (including old electric wires, etc.) can be placed in the incineration container 1 (I) and placed in the white car 15.
and send it into the primary incinerator 10. In the primary incinerator 10, the synthetic resin portion is incinerated at a relatively low temperature (about 8 oC°). Combustion gas flows through the flue 11 into the secondary combustion chamber 21 of the secondary incinerator 20. On this occasion. Since the inlet l2 of the secondary combustion chamber 21 is configured in a tangential direction and with a narrowed opening, the primary combustion gas that has flowed into the secondary combustion chamber 21 becomes a swirling flow and does not stagnate in the secondary combustion chamber 21. The fuel flows and is re-burned by the burner 26 attached during this time. At this time, the flame of the burner 26 is ejected in an effective direction to come into contact with the inflowing gas, and can quickly react with the inflowing gas to increase the combustion rate. In this secondary combustion chamber 21, the combustion gas reaches a temperature of approximately 1200°C, and as is well known, harmful gas components are thermally decomposed. The combustion gas in the combustion chamber 21 rises while swirling, passes through the conductor tube 24 from the upper end opening of the conductor tube 24, and flows into the lower heat radiation chamber 22. In this radiation chamber 22, while the inflowing combustion gas swirls and flows between the blocks 27 provided intermittently in a plurality of concentric rows within the chamber, it comes into contact with the blocks 27, exchanges heat, and radiates the heat. Then, the gas temperature is lowered and the duct 1 is discharged from the outlet 28.
Move to 33. Therefore, if the cooling 71 is passed through the block 27 as described above, it is effective for lowering the gas temperature. This prevents heat from accumulating inside the walls through the walls, so even if there is a temperature difference between the upper and lower compartments,
Damage and wear can be prevented by controlling the temperature gradient using cooling water. The dust 1- contained in the exhaust gas sent out from the secondary incinerator 20 is first separated in the cyclone 31. The air is then sent into the lower cleaning chamber 36 of the tower-shaped scrubber 35 by the exhaust fan 32, passes through the packed bed chamber 37 and the cleaning chamber 38, and is discharged to the outside through the upper exhaust pipe. In this tower-shaped scrapper 35, in the cleaning chamber 38, a large number of spray nozzles 38° installed in the cleaning water injection pipe 38° installed in the center of the cleaning chamber 38 are spray-cleaned (TI water is applied to the Raschig rings in the packed bed 37). The exhaust gas flowing down through the cleaning chamber 38 and flowing countercurrent thereto comes into contact with the cleaning water and is subjected to desalination and desulfurization treatment by well-known means. The gas is supplemented by a wire demister 39 placed in the upper chamber of the cleaning chamber 38, and only the cleaned gas is discharged into the atmosphere. 117 type scrapper 35 The solids contained in the exhaust gas washed in the cleaning chamber 36 flow into the storage tank 42 through the drain pipe 36 at the bottom of the washing chamber 36, where they are sedimented and separated. A partition wall is provided in the water storage tank 42 so that the supernatant water can be pumped out using the Bonn Plu1. is separately sent to a cooling water injection part located outside the outlet of the primary incinerator 10 by a bomb 45, and is used to inject water into the incinerated container 16 taken out from the outlet of the primary incinerator 10 after incineration to cool it. The moisture in the cooling water containing sludge evaporates and only the solid matter remains in a dry state, adhering to containers and incinerated materials. Therefore, when collecting metal objects after this incineration process, the same amount of water is added to the exhaust gas. 'P solids can also be recovered, so they can be disposed of in the form of powder.Of course, dust collection means should be placed around this cooling water injection part to prevent it from dissipating as dust. It is preferable to use DIAL as the means. Effects of the invention: According to the present invention, when metal waste with synthetic resin attached is incinerated, the incineration process is performed in two stages to remove the metal parts. This is to facilitate the recovery and exhaust gas treatment of combustion gas, and in secondary incinerators, cooling water is passed through the QJ wall between the combustion chamber and the heat radiation chamber that lowers the gas temperature. We were able to create a device that reduces the loss of F's and increases the durability of the furnace body.Also, the sludge water such as Dust 1 generated in the exhaust gas cleaning process is used to collect metal scraps after incineration. By using it for cooling, it can be recovered as a dry solid, and the washing water can be recycled in a closed cycle.
This will allow for rationalization without the need for additional processing equipment for washing wastewater.
第1図は本発明Uε棄物の焼却処理装置の全体概要図、
第2図は一次焼却炉の朴{断而レ1、第3レ1は二次焼
却炉の二次燃焼室の平断面図、第41・4は二次燃焼炉
の放熱室の平断面図、第5[2lは佳切り壁の一部拡大
断面図、第()図は塔形スクラッパーの洗浄室部分を示
す図である。
10・・・一次焼却炉 11・・・煙 道12
・・・燃焼ガスの入口
15・・・被処理物焼却処理用の台車
16・・・被処理物焼却処理用の容器
20・・・二次焼却炉 21・・・二次燃焼室2
2・・・放 熱 室 23・・・仕切り壁23a
・・・冷却水の通水管
26・・・バーナ
28・・・ガス出口
31・・・サイクロン
33.3=1・・・ダ ク 1・36・・・洗
浄空室
38・・・洗 浄 室
38″・・・噴霧ノズル
41〕・・・洗浄水循環供給機構
41・・・洗浄水供給管
44.45・・・ポ ン プFIG. 1 is an overall schematic diagram of the Uε waste incineration processing apparatus of the present invention;
Figure 2 is a plan view of the primary incinerator, Figure 1 is a plan cross-sectional view of the secondary combustion chamber of the secondary incinerator, and Figures 41 and 4 are plan cross-sectional views of the heat radiation chamber of the secondary combustion furnace. , No. 5 [2l is a partially enlarged cross-sectional view of the cut wall, and FIG. 10... Primary incinerator 11... Flue duct 12
...Combustion gas inlet 15...Dolly 16 for incineration of objects to be processed...Container 20 for incineration of objects to be processed...Secondary incinerator 21...Secondary combustion chamber 2
2... Heat dissipation chamber 23... Partition wall 23a
... Cooling water pipe 26 ... Burner 28 ... Gas outlet 31 ... Cyclone 33.3 = 1 ... Dak 1.36 ... Washing chamber 38 ... Washing chamber 38″...Spray nozzle 41]...Washing water circulation supply mechanism 41...Washing water supply pipe 44.45...Pump
Claims (1)
却処理装置において: 焼却炉は、トンネル炉型の一次焼却炉と、円筒状の炉体
を上下二室に仕切って、上室が前記一次焼却炉と接続さ
れる二次燃焼室で、下室が放熱室に形成した二次焼却炉
とで構成され;該二次焼却炉の放熱室ガス出口に、サイ
クロンを介して、シャワーリング室および充填層を上下
に組み合わせてなる塔形スクラツバーと、洗浄水循環機
構と、からなる排ガス洗浄装置を接続してあり; 被処理物は台車に搭載した耐熱性容器に投入して前記一
次焼却炉に送り込むようにし、焼却炉内から取り出した
前記容器に対して、排ガス洗浄装置の循環洗浄水の一部
を用いて冷却処理する機構を、一次焼却炉の出口外に配
設した;ことを特徴とする合成樹脂付着廃棄物の焼却処
理装置。 2 合成樹脂が付着した金属物からなる産業廃棄物の焼
却処理装置において: 焼却炉は、トンネル炉型の一次焼却炉と、円筒状の炉体
を上下二室に区画して、その上室が二次燃焼室で、下室
が放熱室に形成した二次焼却炉とで構成してあり; 該二次焼却炉は、上部の二次燃焼室に対して、一次焼却
炉からのガス導入口が接線方向に設けてあり、そのガス
導入口近傍にバーナを配設し、該二次燃焼室中心に上部
で開口する導通筒を蓄熱室に連通するように立設してあ
り、放熱室内には、同心円上で複列に多数の耐火ブロッ
ク体を断続的に設けてある; ことを特徴とする合成樹脂付着廃棄物の焼却処理装置。 3 二次燃焼室と放熱室との仕切り壁は、その内部に冷
却水の通路を設けて、冷却するようにしてある、請求項
2に記載の合成樹脂付着廃棄物の焼却処理装置。[Claims] 1. In an apparatus for incinerating industrial waste made of metal objects to which synthetic resin has adhered: The incinerator comprises a tunnel furnace-type primary incinerator and a cylindrical furnace body divided into two upper and lower chambers. , a secondary combustion chamber whose upper chamber is connected to the primary incinerator, and a secondary incinerator whose lower chamber is formed into a heat radiation chamber; An exhaust gas cleaning device consisting of a tower-shaped scrubber consisting of a showering chamber and a packed bed arranged above and below, and a cleaning water circulation mechanism is connected to the exhaust gas cleaning system; A mechanism is arranged outside the outlet of the primary incinerator to send the container to the primary incinerator, and to cool the container taken out from the incinerator using part of the circulating cleaning water of the exhaust gas cleaning device. ; An apparatus for incineration of waste adhering to synthetic resin. 2. In incineration equipment for industrial waste made of metal objects with synthetic resin attached: The incinerator consists of a tunnel-type primary incinerator, a cylindrical furnace body divided into two upper and lower chambers, and an upper chamber with a It consists of a secondary combustion chamber and a secondary incinerator whose lower chamber is formed as a heat radiation chamber; the secondary incinerator has a gas inlet from the primary incinerator connected to the upper secondary combustion chamber. is provided in the tangential direction, a burner is arranged near the gas inlet, and a conduction cylinder opening at the upper part is erected in the center of the secondary combustion chamber so as to communicate with the heat storage chamber. An apparatus for incineration of synthetic resin-adhered waste, characterized in that a large number of refractory blocks are disposed intermittently in double rows on concentric circles; 3. The incineration treatment apparatus for synthetic resin-adhered waste according to claim 2, wherein the partition wall between the secondary combustion chamber and the heat radiation chamber is provided with a cooling water passage therein for cooling.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP5922689A JPH0692812B2 (en) | 1989-03-10 | 1989-03-10 | Incineration treatment equipment for synthetic resin-adhered waste |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP5922689A JPH0692812B2 (en) | 1989-03-10 | 1989-03-10 | Incineration treatment equipment for synthetic resin-adhered waste |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH02238209A true JPH02238209A (en) | 1990-09-20 |
JPH0692812B2 JPH0692812B2 (en) | 1994-11-16 |
Family
ID=13107249
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP5922689A Expired - Lifetime JPH0692812B2 (en) | 1989-03-10 | 1989-03-10 | Incineration treatment equipment for synthetic resin-adhered waste |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0692812B2 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100383799B1 (en) * | 2000-03-21 | 2003-05-12 | 주식회사 삼성엔지니어링 | Device of reducing dust and dioxide from an incinerator |
-
1989
- 1989-03-10 JP JP5922689A patent/JPH0692812B2/en not_active Expired - Lifetime
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100383799B1 (en) * | 2000-03-21 | 2003-05-12 | 주식회사 삼성엔지니어링 | Device of reducing dust and dioxide from an incinerator |
Also Published As
Publication number | Publication date |
---|---|
JPH0692812B2 (en) | 1994-11-16 |
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