JPH05256431A - Waste incinerating and melting device - Google Patents
Waste incinerating and melting deviceInfo
- Publication number
- JPH05256431A JPH05256431A JP5594692A JP5594692A JPH05256431A JP H05256431 A JPH05256431 A JP H05256431A JP 5594692 A JP5594692 A JP 5594692A JP 5594692 A JP5594692 A JP 5594692A JP H05256431 A JPH05256431 A JP H05256431A
- Authority
- JP
- Japan
- Prior art keywords
- incinerator
- ash
- ashes
- irons
- combustion
- 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
Landscapes
- Gasification And Melting Of Waste (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、例えば都市ごみ等を焼
却してその焼却灰を溶融する際に用いられるごみ焼却溶
融装置の改良に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an improvement of a refuse incineration / melting apparatus used when incinerating municipal solid waste and melting the incinerated ash.
【0002】[0002]
【従来の技術】最近は、都市ごみ及び産業廃棄物の排出
量が急増し、都市ごみに於ては、平成元年度で約500
0万トン/年、産業廃棄物に於ては、約3億7500万
トン/年と云われて居り、都市ごみは、大都市で毎年7
%の増加率を示す。一方、焼却灰等の埋立地は、都市ご
み於ては、約4年、産業廃棄物於ては、約1年とされ、
埋立地の逼迫が危機的状態にある。都市ごみは、焼却に
依りその容積が10%以下となるが、最近の状況から更
に減容化が要求されると同時に、焼却灰中の重金属、ダ
イオキシン等の無害化が要求される様になり、焼却灰の
溶融化が進んでいる。即ち、焼却灰を溶融する事に依り
元のごみの3%以下に減容され、ダイオキシン類が分解
され、且つ重金属類の大部分が昇華され、溶融炉の後に
設けたバグフィルタで濃縮されて捕集される。残りの焼
却灰は、スラグとなってガラス化されるので、残った重
金属が封じ込められ、水や酸に溶出しない状態になる。
従って、これを埋立てに使っても、骨材等に再利用して
も支障がない。焼却灰を溶融する溶融炉としては、電気
炉と表面溶融炉がある。電気炉は、焼却灰中の鉄類(鉄
等の磁性物、以下単に鉄類という)も溶融するが、電気
のコストが高い。表面溶融炉は、油バーナに依り焼却灰
の表面を加熱して溶融するが、事前に鉄類を除去して置
かないと、溶鉄の固形物ができ、スラグの排出時には冷
却して硬い大きな固化物となり、コンベア等に障害を与
える。従って、焼却炉から溶融炉へ入る間に除去する必
要があり、その除去率が高いほど円滑な運転ができる。
溶融炉の配置としては、焼却炉と全く切り離して設ける
独立型と、焼却炉の後に直結する直結型とがある。独立
型の場合は、焼却灰の破砕機、磁選機、篩機等を夫々独
立して設け、コンベアで連結する方式が採られるが、大
きなスペースを必要とし、建屋の容積も大きく、コスト
アップになる。又、配置上、コンベアが上下に行き交
い、システムが複雑となる。直結型の場合は、焼却炉の
焼却灰排出部と溶融炉の焼却灰供給部との間で、焼却灰
中のクリンカと鉄類の処理を行なう必要があり、工夫を
要し、できるだけ、密閉状態でコンパクトに纏める必要
がある。コスト的には、独立型より安く、且つ、高温状
態にある焼却灰を溶融するので、エネルギ的にも有利で
ある。従来、表面溶融炉を用いた直結型のごみ焼却溶融
装置としては、例えば特開平1−196412号に記載
されたものが知られている。これは、基本的には、ごみ
を焼却する焼却炉と、焼却炉からの焼却灰中のクリンカ
を除去する除去機と、焼却炉からの焼却灰中の鉄類を除
去する磁選機と、除去機と磁選機を経た焼却灰を溶融す
る溶融炉と、から構成されている。而して、ごみ焼却炉
からの焼却灰を、除去機と磁選機に依りクリンカと鉄類
を除去した後に、溶融炉で溶融する様になっている。と
ころが、この様なものは、除去されたクリンカの中に
は、鉄類を抱え込んでいる事が多く、クリンカを再処理
する必要があり、鉄類の回収率が芳しくなかった。2. Description of the Related Art Recently, the amount of municipal waste and industrial wastes has increased rapidly, and the amount of municipal waste is about 500 in 1989.
It is said that the amount of industrial waste is about 375 million tons / year, and the amount of municipal solid waste is 7
The percentage increase is shown. On the other hand, the landfill of incinerated ash is about 4 years for municipal waste and about 1 year for industrial waste.
The tight landfill is in danger. The volume of municipal solid waste becomes 10% or less due to incineration, but the recent situation calls for further volume reduction and at the same time, detoxification of heavy metals, dioxins, etc. in the incinerated ash is required. The incineration ash is becoming more molten. That is, by melting the incinerated ash, the volume is reduced to 3% or less of the original refuse, dioxins are decomposed, and most of the heavy metals are sublimed and concentrated by a bag filter installed after the melting furnace. To be collected. Since the remaining incinerated ash is vitrified into slag, the remaining heavy metals are contained, and the ash does not elute into water or acid.
Therefore, it can be used for landfill or reused as aggregate or the like without any problem. As a melting furnace for melting the incineration ash, there are an electric furnace and a surface melting furnace. The electric furnace also melts iron (a magnetic substance such as iron, hereinafter simply referred to as iron) in the incinerated ash, but the cost of electricity is high. The surface melting furnace heats and melts the surface of the incineration ash by using an oil burner, but if iron is not removed in advance, molten iron solids will be formed, and when slag is discharged, it will be cooled and hardened to a large solidification. It becomes a thing and gives an obstacle to the conveyor etc. Therefore, it is necessary to remove it while entering the melting furnace from the incinerator, and the higher the removal rate, the smoother the operation.
There are two types of arrangements for the melting furnace: a stand-alone type that is completely separated from the incinerator, and a direct type that is directly connected after the incinerator. In the case of a stand-alone type, a method of separately installing an incinerator ash crusher, a magnetic separator, a sifter, etc. and connecting with a conveyor is adopted, but it requires a large space, the building volume is large, and the cost is increased. Become. In addition, because of the arrangement, the conveyors move up and down, which complicates the system. In the case of the direct connection type, it is necessary to treat the clinker and iron in the incinerator ash between the incinerator ash discharge part of the incinerator and the incinerator ash supply part of the melting furnace. It is necessary to put it together in a compact state. In terms of cost, it is cheaper than the stand-alone type, and since incinerator ash in a high temperature state is melted, it is also advantageous in terms of energy. Conventionally, as a direct coupling type refuse incineration and melting apparatus using a surface melting furnace, for example, one described in Japanese Patent Laid-Open No. 1-196412 is known. This is basically an incinerator that incinerates waste, a removal machine that removes clinker in the incinerator ash from the incinerator, a magnetic separator that removes iron in the incinerator ash from the incinerator, and the removal. And a melting furnace that melts incinerated ash that has passed through a magnetic separator. Thus, the incineration ash from the refuse incinerator is melted in the melting furnace after removing the clinker and irons by the removing machine and the magnetic separator. However, in such clinker, irons are often held in the removed clinker, and the clinker needs to be reprocessed, and the recovery rate of irons is not good.
【0003】[0003]
【発明が解決しようとする課題】本発明は、叙上の問題
点に鑑み、これを解決する為に創案されたもので、その
目的とする処は、クリンカを再処理する必要がないと共
に、鉄類の回収率を向上できるごみ焼却溶融装置を提供
するにある。SUMMARY OF THE INVENTION The present invention was devised to solve the above problems in view of the above problems, and the object of the present invention is to eliminate the need for reprocessing the clinker, and It is to provide a refuse incinerator / melting device that can improve the recovery rate of irons.
【0004】[0004]
【課題を解決するための手段】本発明のごみ焼却溶融装
置は、基本的には、ごみを焼却する焼却炉と、焼却炉か
らの焼却灰中のクリンカを破砕する破砕機と、破砕機か
らの焼却灰中の鉄類を除去する磁選機と、磁選機からの
焼却灰を溶融する溶融炉と、から構成した事に特徴が存
する。The refuse incinerator / melting apparatus of the present invention basically comprises an incinerator for incinerating refuse, a crusher for crushing clinker in incinerator ash from the incinerator, and a crusher. It is characterized in that it is composed of a magnetic separator that removes irons from the incinerated ash and a melting furnace that melts the incinerated ash from the magnetic separator.
【0005】[0005]
【作用】ごみは、焼却炉に送られて焼却される。焼却炉
からの焼却灰は、破砕機に送られてこの中のクリンカが
破砕される。破砕機からの焼却灰は、磁選機に送られて
この中の鉄類が除去される。磁選機からの焼却灰は、溶
融炉に送られて溶融される。クリンカを破砕機に依り破
砕してこの中に含まれている鉄類を磁選機に依り除去し
ているので、鉄類の回収率が向上する。[Operation] Waste is sent to an incinerator and incinerated. The incineration ash from the incinerator is sent to a crusher to crush the clinker in it. The incinerated ash from the crusher is sent to the magnetic separator to remove iron contained therein. The incineration ash from the magnetic separator is sent to the melting furnace and melted. Since the clinker is crushed by the crusher and the iron contained therein is removed by the magnetic separator, the iron recovery rate is improved.
【0006】[0006]
【実施例】以下、本発明の実施例を、図面に基づいて説
明する。図1は、本発明の実施例に係るごみ焼却溶融装
置を示す縦断側面図。図2は、図1の要部を拡大して示
す縦断側面図である。ごみ焼却溶融装置1は、焼却炉
2、破砕機3、磁選機4、溶融炉5とからその主要部が
構成されている。焼却炉2は、ごみAを焼却するもの
で、この例では、ごみホッパ6と乾燥ストーカ7と焼却
ストーカ8と後燃焼ストーカ9とを備えている。後燃焼
ストーカ9は、駆動機構10に依り往復運動される様に
なっている。破砕機3は、焼却炉2からの焼却灰B中の
クリンカCを破砕するもので、この例では、固定格子1
1と、これに対して揺動可能な可動格子12と、これを
揺動させる油圧シリンダ等の駆動機構13とを備えて居
り、剪断式にしている。破砕機3は、その剪断動作が焼
却炉2の後燃焼ストーカ9の往復運動と連動させてあ
る。つまり、後燃焼ストーカ9が往復運動して焼却灰B
が固定格子11上に供給される都度、可動格子12が揺
動されてクリンカCが剪断される様になっている。磁選
機4は、破砕機3からの焼却灰B中の鉄類Dを除去する
もので、この例では、破砕機3からの焼却灰B中の鉄類
Dを除去するドラム式の一次磁選機14と、これからの
焼却灰B中の鉄類Dを更に除去する同じくドラム式の二
次磁選機15と、これらからの鉄類Dを密封しながら排
出する二重ダンパ16と、これからの鉄類Dを外部に排
出する鉄類排出コンベア17とを備えている。破砕機3
と磁選機4との間には、ダンパ18が設けられている。
これは、緊急用バイパスダンパであり、常時には図1の
実線位置にされて破砕機3からの焼却灰Bが磁選機4に
導かれると共に、溶融炉5の点検や補修時には図1の鎖
線位置にされて破砕機3からの焼却灰Bがこの下方に設
けられた二重ダンパ16を経て鉄類排出コンベア17か
ら外部に排出される様になっている。溶融炉5は、磁選
機4からの焼却灰Bを溶融するもので、この例では、磁
選機4からの焼却灰Bを一旦貯留する灰バンカ19と、
ここの焼却灰Bを定量づつ炉床20に押し出す定量供給
フィーダ21と、炉床20に押し出された焼却灰Bの表
面を加熱して溶融するバーナ22と、焼却灰Bが溶融さ
れてできたスラグEを外部に排出する水封コンベア23
とを備えている。灰バンカ19には、焼却灰Bの層レベ
ルを三段階に亘って検出する灰レベル計24,25,2
6が配設されて居り、これらに依る検出レベルに基づい
て制御器27に依り後燃焼ストーカ9の駆動機構10と
破砕機3の駆動機構13と定量供給フィーダ21の駆動
機構(図示せず)が制御される様になっている。次に、
この様な構成に基づいて作用を述解する。焼却炉2のご
みホッパ6に投入されたごみAは、乾燥ストーカ7、燃
焼ストーカ8、後燃焼ストーカ9を経て焼却灰Bとな
り、破砕機3に入る。普通の大きさの焼却灰Bや鉄缶等
の鉄類Bは、固定格子11の隙間を通って落下するが、
クリンカCは、固定格子11の上に乗って残る。このク
リンカCは、駆動機構13で揺動される可動格子12に
依り剪断され、バラバラとなって、固定格子11の隙間
から落下する。この可動格子12は、焼却炉2の後燃焼
ストーカ9と連動して居り、後燃焼ストーカ9が往復運
動すると、焼却灰Bが落下して来るので、後燃焼ストー
カ9を一旦停止し、その後で可動格子12が一回揺動
し、この動作を繰返す。破砕機3からの焼却灰Bは、図
1の実線位置にあるダンパ18の上を滑落して磁選機4
に依り磁選される。先ず、一次磁選機14に依りこの中
の鉄類Dが分離される。更に、一次磁選機14を経た焼
却灰Bは、二次磁選機15に依りこの中の鉄類Dが分離
され、磁選効率が完全にされる。鉄類Dは、二重ダンパ
16を通過して鉄類排出コンベア17に依り外部に排出
される。一方、磁選機4を経た焼却灰Bは、溶融炉5の
灰バンカ19内に一旦貯蔵され、定量供給フィーダ21
に依り炉床20上に押出され、上部天井からのバーナ2
2の加熱に依り表面が溶融され、水封コンベア23内に
スラグEとなって落下され、外部に排出される。焼却炉
2の後燃焼ストーカ9は、焼却灰Bの貯蔵も兼ねて居
り、灰バンカ19内の上、中、下の灰レベル計24,2
5,26からの信号に基づいて制御器27に依り後燃焼
ストーカ9が往復運動され、これと連動して破砕機3が
駆動される。この様なごみ焼却溶融装置1に依れば、焼
却炉2と溶融炉5が直結され、然も、焼却灰Bと鉄類D
との分離が確実に行なわれるので、円滑な運転ができ、
コストも安く、鉄類Dのリサイクル率も向上する。Embodiments of the present invention will be described below with reference to the drawings. FIG. 1 is a vertical sectional side view showing a refuse incinerator / melting apparatus according to an embodiment of the present invention. FIG. 2 is a vertical cross-sectional side view showing an enlarged main part of FIG. The refuse incineration / melting apparatus 1 is mainly composed of an incinerator 2, a crusher 3, a magnetic separator 4, and a melting furnace 5. The incinerator 2 incinerates the waste A, and in this example, includes a waste hopper 6, a drying stoker 7, an incinerator stoker 8, and a post-combustion stoker 9. The post-combustion stoker 9 is configured to reciprocate by the drive mechanism 10. The crusher 3 crushes the clinker C in the incineration ash B from the incinerator 2, and in this example, the fixed grid 1
1, a movable lattice 12 which can be swung with respect thereto, and a drive mechanism 13 such as a hydraulic cylinder for swinging the movable lattice 12, which are of a shear type. The shearing operation of the crusher 3 is linked with the reciprocating motion of the post combustion stoker 9 of the incinerator 2. That is, the post-combustion stoker 9 reciprocates to incinerate ash B.
The movable clincher 12 is swung and the clinker C is sheared each time the clinker C is supplied onto the fixed lattice 11. The magnetic separator 4 removes the irons D in the incineration ash B from the crusher 3, and in this example, the drum-type primary magnetic separator that removes the irons D in the incineration ash B from the crusher 3. 14, a secondary magnetic separator 15 of the same drum type for further removing irons D in the incinerated ash B, a double damper 16 for discharging the irons D from these while sealing them, and irons in the future It is provided with an iron discharging conveyor 17 for discharging D to the outside. Crusher 3
A damper 18 is provided between the magnetic separator 4 and the magnetic separator 4.
This is an emergency bypass damper, and the incinerator ash B from the crusher 3 is always guided to the magnetic separator 4 while being set to the solid line position in FIG. 1, and the chain line position in FIG. The incinerated ash B from the crusher 3 is discharged to the outside from the iron discharging conveyor 17 via the double damper 16 provided below this. The melting furnace 5 melts the incinerated ash B from the magnetic separator 4, and in this example, an ash bunker 19 that temporarily stores the incinerated ash B from the magnetic separator 4.
The incineration ash B here was quantitatively extruded into the hearth 20 in a fixed amount, the burner 22 that heats and melts the surface of the incineration ash B extruded into the hearth 20, and the incineration ash B is melted. Water-sealed conveyor 23 for discharging slag E to the outside
It has and. An ash leveler 24, 25, 2 for detecting the layer level of the incinerated ash B over three steps is provided in the ash bunker 19.
6 are provided, and the drive mechanism 10 of the post-combustion stoker 9, the drive mechanism 13 of the crusher 3 and the drive mechanism of the constant quantity supply feeder 21 (not shown) are controlled by the controller 27 based on the detection levels based on these. Is controlled. next,
The operation will be described based on such a configuration. The waste A thrown into the waste hopper 6 of the incinerator 2 becomes the incineration ash B through the dry stoker 7, the combustion stoker 8, and the post-combustion stoker 9, and enters the shredder 3. Although the incinerated ash B of a normal size and the iron B such as the iron can fall through the gaps of the fixed grid 11,
The clinker C remains on the fixed lattice 11. The clinker C is sheared by the movable lattice 12 that is swung by the drive mechanism 13 and becomes disjointed, and falls from the gap of the fixed lattice 11. The movable grid 12 is interlocked with the post-combustion stoker 9 of the incinerator 2, and when the post-combustion stoker 9 reciprocates, the incineration ash B falls, so the post-combustion stoker 9 is temporarily stopped, and thereafter The movable grid 12 swings once, and this operation is repeated. The incinerated ash B from the crusher 3 slides down on the damper 18 at the solid line position in FIG.
Is selected according to. First, the primary magnetic separator 14 separates the irons D therein. Further, in the incineration ash B that has passed through the primary magnetic separator 14, irons D therein are separated by the secondary magnetic separator 15, and the magnetic separation efficiency is perfected. The irons D pass through the double damper 16 and are discharged to the outside by the irons discharge conveyor 17. On the other hand, the incinerated ash B that has passed through the magnetic separator 4 is once stored in the ash bunker 19 of the melting furnace 5, and the fixed amount supply feeder 21
Is pushed onto the hearth 20 by the burner 2 from the upper ceiling.
The surface is melted by the heating of 2, and is dropped into slag E in the water-sealed conveyor 23 and discharged to the outside. The post-combustion stoker 9 of the incinerator 2 also serves to store the incinerated ash B, and the upper, middle, and lower ash level meters 24, 2 in the ash bunker 19
The post-combustion stoker 9 reciprocates by the controller 27 based on the signals from 5, 26, and the crusher 3 is driven in conjunction with this. According to such a refuse incineration and melting apparatus 1, the incinerator 2 and the melting furnace 5 are directly connected to each other, and the incineration ash B and the iron D
Since it is reliably separated from the
The cost is low and the recycling rate of iron D is improved.
【0007】尚、磁選機4は、先の実施例では、二段に
設けたが、これに限らず、例えば一段でも、三段以上で
も良い。Although the magnetic separator 4 is provided in two stages in the above embodiment, the present invention is not limited to this and may be one stage or three or more stages.
【0008】[0008]
【発明の効果】以上、既述した如く、本発明に依れば、
次の様な優れた効果を奏する事ができる。 (1) 焼却炉、破砕機、磁選機、溶融炉とで構成し、
とりわけ、焼却炉と溶融炉との間に、焼却炉からの焼却
灰中のクリンカを破砕する破砕機とここからの焼却灰中
の鉄類を除去する磁選機を設ける様にしたので、クリン
カを再処理する必要がないと共に、鉄類の回収率を向上
できる。 (2) 焼却灰中の鉄類のみを除去して溶融する様にし
たので、焼却灰の溶融率が向上し、ごみの減容率を高め
る事ができる。As described above, according to the present invention,
The following excellent effects can be achieved. (1) Consists of an incinerator, a crusher, a magnetic separator, and a melting furnace,
Above all, between the incinerator and the melting furnace, a crusher for crushing the clinker in the incinerator ash from the incinerator and a magnetic separator for removing iron in the incinerator ash from here were installed. It is not necessary to reprocess, and the recovery rate of irons can be improved. (2) Since only the irons in the incineration ash are removed and melted, the melting rate of the incineration ash is improved and the volume reduction rate of dust can be increased.
【図1】本発明の実施例に係るごみ焼却溶融装置を示す
縦断側面図。FIG. 1 is a vertical sectional side view showing a refuse incineration / melting apparatus according to an embodiment of the present invention.
【図2】図1の要部を拡大して示す縦断側面図。FIG. 2 is a vertical cross-sectional side view showing an enlarged main part of FIG.
1…ごみ焼却溶融装置、2…焼却炉、3…破砕機、4…
磁選機、5…溶融炉、6…ごみホッパ、7…乾燥ストー
カ、8…焼却ストーカ、9…後燃焼ストーカ、10…駆
動機構、11…固定格子、12…可動格子、13…駆動
機構、14…一次磁選機、15…二次磁選機、16…二
重ダンパ、17…鉄類排出コンベア、18…ダンパ、1
9…灰バンカ、20…炉床、21…定量供給フィーダ、
22…バーナ、24〜26…灰レベル計、27…制御
器、A…ごみ、B…焼却灰、C…クリンカ、D…鉄類、
E…スラグ。1 ... refuse incineration and melting device, 2 ... incinerator, 3 ... crusher, 4 ...
Magnetic separator, 5 ... Melting furnace, 6 ... Garbage hopper, 7 ... Drying stoker, 8 ... Incineration stoker, 9 ... Post-combustion stoker, 10 ... Driving mechanism, 11 ... Fixed lattice, 12 ... Movable lattice, 13 ... Driving mechanism, 14 ... primary magnetic separator, 15 ... secondary magnetic separator, 16 ... double damper, 17 ... iron discharge conveyor, 18 ... damper, 1
9 ... Ash bunker, 20 ... Hearth, 21 ... Fixed amount feeder,
22 ... Burner, 24-26 ... Ash level meter, 27 ... Controller, A ... Garbage, B ... Incinerated ash, C ... Clinker, D ... Irons,
E ... Slag.
Claims (2)
焼却灰中のクリンカを破砕する破砕機と、破砕機からの
焼却灰中の鉄類を除去する磁選機と、磁選機からの焼却
灰を溶融する溶融炉と、から構成した事を特徴とするご
み焼却溶融装置。1. An incinerator for incinerating refuse, a crusher for crushing clinker in incinerator ash from the incinerator, a magnetic separator for removing iron in the incinerator ash from the crusher, and a magnetic separator. A refuse incinerator / melting device characterized by comprising a melting furnace for melting incinerated ash.
可能な可動格子とを備えた剪断式にし、剪断動作と焼却
炉の後燃焼ストーカの往復運動とを連動させた請求項1
記載のごみ焼却溶融装置。2. The crusher is of a shear type having a fixed grid and a movable grid swingable with respect to the fixed grid, and the shearing operation and the reciprocating motion of the post combustion stoker of the incinerator are interlocked.
Waste incineration and melting device described.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP04055946A JP3113723B2 (en) | 1992-03-16 | 1992-03-16 | Waste incineration melting equipment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP04055946A JP3113723B2 (en) | 1992-03-16 | 1992-03-16 | Waste incineration melting equipment |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH05256431A true JPH05256431A (en) | 1993-10-05 |
JP3113723B2 JP3113723B2 (en) | 2000-12-04 |
Family
ID=13013246
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP04055946A Expired - Fee Related JP3113723B2 (en) | 1992-03-16 | 1992-03-16 | Waste incineration melting equipment |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP3113723B2 (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2000022348A1 (en) * | 1998-10-12 | 2000-04-20 | Nkk Corporation | Waste disposal device |
JP2000199620A (en) * | 1998-10-12 | 2000-07-18 | Nkk Corp | Incinerating heat treating furnace for refuse |
KR100647269B1 (en) * | 2006-05-04 | 2006-11-23 | 한국기계연구원 | Waste pyrolysis and smelting system able to incinerating process |
JP2013032876A (en) * | 2011-08-02 | 2013-02-14 | Yazaki Energy System Corp | Absorption type chiller and heater |
CN108333000A (en) * | 2018-04-28 | 2018-07-27 | 中国城市建设研究院有限公司 | The automatic sampling sample preparation integral system of domestic waste incineration deslagging |
-
1992
- 1992-03-16 JP JP04055946A patent/JP3113723B2/en not_active Expired - Fee Related
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2000022348A1 (en) * | 1998-10-12 | 2000-04-20 | Nkk Corporation | Waste disposal device |
JP2000199620A (en) * | 1998-10-12 | 2000-07-18 | Nkk Corp | Incinerating heat treating furnace for refuse |
KR100647269B1 (en) * | 2006-05-04 | 2006-11-23 | 한국기계연구원 | Waste pyrolysis and smelting system able to incinerating process |
JP2013032876A (en) * | 2011-08-02 | 2013-02-14 | Yazaki Energy System Corp | Absorption type chiller and heater |
CN108333000A (en) * | 2018-04-28 | 2018-07-27 | 中国城市建设研究院有限公司 | The automatic sampling sample preparation integral system of domestic waste incineration deslagging |
Also Published As
Publication number | Publication date |
---|---|
JP3113723B2 (en) | 2000-12-04 |
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