JPH0576360B2 - - Google Patents
Info
- Publication number
- JPH0576360B2 JPH0576360B2 JP61057553A JP5755386A JPH0576360B2 JP H0576360 B2 JPH0576360 B2 JP H0576360B2 JP 61057553 A JP61057553 A JP 61057553A JP 5755386 A JP5755386 A JP 5755386A JP H0576360 B2 JPH0576360 B2 JP H0576360B2
- Authority
- JP
- Japan
- Prior art keywords
- slag
- furnace
- waste
- melting
- molten
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
- 239000002893 slag Substances 0.000 claims description 85
- 239000002699 waste material Substances 0.000 claims description 26
- 238000002844 melting Methods 0.000 claims description 25
- 230000008018 melting Effects 0.000 claims description 25
- 239000000463 material Substances 0.000 claims description 11
- 238000007790 scraping Methods 0.000 claims description 11
- 238000004140 cleaning Methods 0.000 claims description 10
- 239000012768 molten material Substances 0.000 description 15
- 239000011449 brick Substances 0.000 description 8
- 238000010438 heat treatment Methods 0.000 description 7
- 239000000126 substance Substances 0.000 description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- 239000003999 initiator Substances 0.000 description 4
- 238000010309 melting process Methods 0.000 description 4
- 229910052751 metal Inorganic materials 0.000 description 4
- 239000002184 metal Substances 0.000 description 4
- 238000001514 detection method Methods 0.000 description 3
- 238000000605 extraction Methods 0.000 description 3
- 239000011819 refractory material Substances 0.000 description 3
- 229910001021 Ferroalloy Inorganic materials 0.000 description 2
- CPLXHLVBOLITMK-UHFFFAOYSA-N Magnesium oxide Chemical compound [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 description 2
- 239000000155 melt Substances 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000010802 sludge Substances 0.000 description 2
- 238000004056 waste incineration Methods 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- 229910000805 Pig iron Inorganic materials 0.000 description 1
- 229910004298 SiO 2 Inorganic materials 0.000 description 1
- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical compound [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 description 1
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 230000009970 fire resistant effect Effects 0.000 description 1
- 238000005187 foaming Methods 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 238000005469 granulation Methods 0.000 description 1
- 230000003179 granulation Effects 0.000 description 1
- 231100001261 hazardous Toxicity 0.000 description 1
- 229910001385 heavy metal Inorganic materials 0.000 description 1
- 238000010169 landfilling Methods 0.000 description 1
- 239000010985 leather Substances 0.000 description 1
- 239000000395 magnesium oxide Substances 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 230000003287 optical effect Effects 0.000 description 1
- 238000010298 pulverizing process Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 238000010079 rubber tapping Methods 0.000 description 1
- 239000004576 sand Substances 0.000 description 1
- 239000010801 sewage sludge Substances 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 229910052718 tin Inorganic materials 0.000 description 1
- 239000011135 tin Substances 0.000 description 1
- 229910052725 zinc Inorganic materials 0.000 description 1
- 239000011701 zinc Substances 0.000 description 1
Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/50—Fuel cells
Landscapes
- Processing Of Solid Wastes (AREA)
Description
【発明の詳細な説明】
[産業上の利用分野]
本発明は廃棄物溶融処理炉に関する。さらに詳
しくは、都市ゴミ焼却灰のような廃棄物の溶融処
理において溶融物の出滓をより円滑にするための
出滓樋自浄機構を備えた廃棄物溶融処理炉に係わ
るものである。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a waste melting furnace. More specifically, the present invention relates to a waste melting furnace equipped with a slag gutter self-cleaning mechanism for smoother sludge discharge in the melting process of waste such as municipal garbage incineration ash.
[従来の技術]
都市ゴミ焼却灰、下水汚泥焼却灰、皮革処理汚
泥焼却灰等は各種廃棄物は、従来、埋立などによ
り処理されてきた。しかし、埋立用地の確保が困
難であること、含有される有害重金属類が土中に
溶出し、埋立用地周辺を汚染して二次公害を引き
起す恐れがあることなどから最近では、前記廃棄
物を溶融処理炉で溶融処理し、無害化減容する方
法が提案され、上記問題の解決がはかられてい
る。溶融処理炉の一つとして、アーク式溶融炉が
知られており、その代表例として、サブマージド
アーク溶融炉がある。[Prior Art] Various wastes such as municipal garbage incineration ash, sewage sludge incineration ash, leather processing sludge incineration ash, etc. have conventionally been treated by landfilling or the like. However, due to the difficulty of securing land for landfill, and the risk that the hazardous heavy metals contained in the waste may be leached into the soil and contaminate the area surrounding the landfill site, causing secondary pollution, the waste A method has been proposed in which the above-mentioned problems are solved by melting the material in a melting furnace to render it harmless and reduce its volume. An arc type melting furnace is known as one type of melting processing furnace, and a typical example thereof is a submerged arc melting furnace.
この溶融炉は、溶融物の出滓口を備えた耐火構
造の炉本体と、廃棄物投入口、複数の主電極、ガ
ス排出ダクト等を備えた炉蓋とからなつており、
これには、出滓口から排出された溶融物を受け入
れて、冷却し固化破砕する水砕槽が付設されてい
る。また前記出滓口の手前溶融物の流路には、排
出中の溶融物が、そこで冷却固化して出滓を妨げ
られることがないように、加熱用の補助電極が配
置され、溶融開始材投入口が開口している。さら
に、出滓口最先端にはU字型の切欠溝を備えた出
滓口堰レンガが交換可能にはめこまれている。 This melting furnace consists of a furnace body with a fireproof structure equipped with a molten slag outlet, and a furnace lid equipped with a waste inlet, multiple main electrodes, a gas exhaust duct, etc.
This is equipped with a water crushing tank that receives the molten material discharged from the slag outlet, cools it, solidifies it, and crushes it. In addition, an auxiliary electrode for heating is arranged in the flow path of the molten material before the slag outlet, so that the molten material being discharged will not cool and solidify there and prevent the slag from being disposed of. The input port is open. Furthermore, a slag mouth weir brick with a U-shaped notch groove is replaceably fitted at the leading edge of the slag mouth.
そして、電極はその下端乃至全長の約半分が廃
棄物投入口から炉本体内に投入された廃棄物によ
つて、埋没され、電極に通電することによつて、
アーク熱が発生し、投入された廃棄物は遂次溶融
して、前記出滓口堰レンガのU字型切欠溝から炉
外に排出され、水砕槽にて冷却されて細砂状に破
砕固化される。 Then, the lower end or about half of the entire length of the electrode is buried in the waste thrown into the furnace main body from the waste inlet, and by energizing the electrode,
Arc heat is generated, and the input waste is sequentially melted and discharged from the furnace through the U-shaped notch groove of the slag weir brick, cooled in a water crushing tank, and crushed into fine sand. solidified.
[発明が解決しようとする問題点]
サブマージドアーク溶融炉による溶融処理は、
前記の通り、電極の下端乃至全長の約半分が処理
されるべき廃棄物に埋没して行なわれるが、廃棄
物の加熱溶融が進むにつれて、炉内における溶融
物の溶融面レベルが上昇し、出滓口に設けられて
いる出滓堰レンガのU字型切欠溝から炉外にオー
バーフローし、連続して自重により出滓される。[Problems to be solved by the invention] The melting process using the submerged arc melting furnace is
As mentioned above, the lower end of the electrode or about half of its total length is buried in the waste to be processed, but as the waste is heated and melted, the level of the melting surface of the molten material in the furnace rises, causing The slag overflows to the outside of the furnace through the U-shaped notch groove of the slag weir brick provided at the slag opening, and is continuously drained by its own weight.
ところが、前記出滓口の炉本体と出滓堰レンガ
との接続部である出滓樋には溶融処理中に未溶融
物が渋滞し、円滑な出滓が行い得ないことがしば
しば起る。 However, the slag gutter, which is the connection between the furnace main body of the slag outlet and the slag weir brick, is often clogged with unmelted materials during the melting process, making it impossible to smoothly discharge the slag.
都市ゴミ焼却灰のうち、特に、ピン類が主体の
分別ゴミ(燃焼不適物のゴミ)焼却灰を溶融処理
したとき生成する溶融スラグは粘性が高く、ま
た、ガス発泡性があり、溶融レベルが連続溶融処
理連続出滓の途中に、変動しやすい。そして、分
別ゴミ焼却灰を連続処理するとき、皮膜状の未溶
融物が溶融処理炉の出滓樋内に生じ出滓が渋滞し
て炉内の溶融スラグレベルが増加する。そのほ
か、出滓樋を構成するスタンプ材(耐火物)が剥
がれてそのtに混在する場合もある。これら渋滞
物は補助加熱電極を稼働させても用意には溶解し
ない。そして現象的には、出滓樋内で5〜10mm程
度の厚みを有する固化スラグからなる未溶融物の
皮膜を生成し、溶融スラグの円滑な出滓を阻止し
てしまう。 Among municipal waste incineration ash, the molten slag produced when incineration ash of separated waste (unsuitable for combustion), which mainly consists of pins, is melted has a high viscosity and gas foaming property, and the melting level is low. It is easy to fluctuate during continuous melting process and continuous slag extraction. When the separated waste incineration ash is continuously processed, a film of unmelted material is formed in the slag drain of the melting furnace, causing congestion of the slag and increasing the level of molten slag in the furnace. In addition, the stamp material (refractory material) constituting the slag trough may be peeled off and mixed in the t. These jammed substances do not dissolve easily even if the auxiliary heating electrode is operated. As a phenomenon, a film of unmelted material made of solidified slag with a thickness of about 5 to 10 mm is formed in the slag drain, which prevents the molten slag from flowing smoothly.
[問題を解決するための手段]
本発明は、上記問題を解消するべく種々検討の
結果達成されたもので、出滓樋に生成する上記ス
ラグ固化皮膜はその生成の都度外部から僅かの機
械力を与えるだけで簡単に破砕することができ、
それにより、溶融スラグの出滓を円滑にすること
ができるとの知見に基くものである。即ち、本発
明は、廃棄物溶融処理炉の出滓口手前出滓樋上
に、非溶融物が渋滞して排出を妨害していること
を検出する感知器と、該非溶融物を除去するため
に出滓樋内に出没する掻き出し棒とを備えた出滓
樋の自浄機構を設置してなることを特徴とする廃
棄物溶融処理炉を要旨とするものである。[Means for Solving the Problems] The present invention was achieved as a result of various studies to solve the above problems. It can be easily crushed by simply giving
This is based on the knowledge that this allows the molten slag to flow out smoothly. That is, the present invention provides a sensor for detecting that unmelted substances are jammed and obstructing discharge on the slag gutter in front of the slag outlet of a waste melting processing furnace, and a sensor for removing the unmelted substances. The gist of the present invention is a waste melting processing furnace, characterized in that it is equipped with a self-cleaning mechanism for the slag gutter, which is equipped with a scraping rod that appears and retracts within the slag gutter.
[作用]
未溶融物が出滓樋が渋滞し、溶融物の炉外への
排出が進展しないときは、それを検出した感知器
の信号の基いで、掻き出し棒が作動して出滓樋の
自浄を行う。これによつて、固化スラグの渋滞を
解消し、円滑な連続出滓が行われる。[Operation] When the slag drain is clogged with unmelted material and the molten material is not being discharged outside the furnace, the scraping rod is activated based on the signal from the sensor that detects this and clears the slag drain. Perform self-purification. This eliminates the congestion of solidified slag and allows smooth continuous slag extraction.
[実施例]
以下、本発明の一実施例を図面に基いて説明す
る。第1図は、溶融物溶融処理炉の1つの挙げら
れるサブマージドアーク炉の概略側面図であり、
1はカーボン、マグネシア、アルミナ等の1種ま
たは複数を含有した耐火材料で構築された炉本体
である。炉本体1の上面は炉蓋2で蔽われてい
る。炉蓋2は複数の種電極3が貫通し、また、都
市ゴム焼却灰のような廃棄物の投入口4、排ガス
ダクト5が設けられる。炉本体1の下方には、出
滓口6が設けられている。該出滓口6には第1図
のA矢視方向からみた拡大概略正面図である第2
図に示すように、U字型の切欠構8を備えた耐火
性の出滓口堰レンガ7が設けられており炉本体1
内で形成された溶融物がここからオーバーフロー
して炉外へ出滓される。[Example] Hereinafter, an example of the present invention will be described based on the drawings. FIG. 1 is a schematic side view of a submerged arc furnace, which is one example of a molten material melting processing furnace;
1 is a furnace body constructed of a refractory material containing one or more of carbon, magnesia, alumina, and the like. The upper surface of the furnace body 1 is covered with a furnace lid 2. A plurality of seed electrodes 3 pass through the furnace lid 2, and an inlet 4 for waste such as municipal rubber incineration ash and an exhaust gas duct 5 are provided. A slag outlet 6 is provided below the furnace body 1. The slag outlet 6 has a second opening which is an enlarged schematic front view seen from the direction of arrow A in FIG.
As shown in the figure, a fire-resistant slag weir brick 7 with a U-shaped notch structure 8 is provided, and the furnace body 1
The melt formed inside overflows from here and is slaged out of the furnace.
炉本体1の底面全体には、耐火性材料(スタン
プ材)よりなるキヤスタブル1Aが内張りしてあ
り、該キヤスタブル1Aは、出滓口6近傍では溶
融物の排出が容易なように樋状に構築してある。
そして該出滓樋上には通常の出滓で溶融物が、こ
こで固化するのを防止するための補助加熱電極
9、溶融開始剤貯蔵ホツパー11から溶融開始剤
10を投入する溶融開始剤投入口12が設けられ
る。これら補助加熱電極9、溶融開始剤投入口1
2は、出滓口6を蔽う出滓口蓋13に配置され
る。 The entire bottom surface of the furnace body 1 is lined with a castable 1A made of a refractory material (stamp material), and the castable 1A is constructed in the form of a gutter near the slag outlet 6 to facilitate the discharge of the melt. It has been done.
On the slag drain, there is an auxiliary heating electrode 9 for preventing the molten material from solidifying in the normal slag, and a melting initiator inlet for charging the melting initiator 10 from the melting initiator storage hopper 11. 12 are provided. These auxiliary heating electrodes 9, melting initiator inlet 1
2 is placed on a slag outlet cover 13 that covers the slag outlet 6.
出滓口蓋13の縦方向、すなわち溶融物を流れ
方向において、炉本体1の反対側側壁には、出滓
口6を通り、前記出滓樋内に出没(矢印で示す)
して、そこに滞留するスラグ固化皮膜のような未
溶融物を引き出し、または破砕作動する自浄機構
14の掻き出し棒15出没口が設けられる。さら
に、その下方即ち、出滓堰レンガ7の下端に、出
滓口6からの溶融物の排出状況を検出する検知器
16が設けられ、これに対応するものとして、公
知の光高温計、ITV等が設けられる。 In the vertical direction of the slag outlet cover 13, that is, in the flow direction of the molten material, on the opposite side wall of the furnace body 1, there is a wall that passes through the slag outlet 6 and enters and retracts into the slag gutter (indicated by an arrow).
A scraping rod 15 of the self-cleaning mechanism 14 is provided with an inlet and an outlet for pulling out or crushing unmelted substances such as a solidified slag film remaining there. Furthermore, a detector 16 is provided below, that is, at the lower end of the slag weir brick 7, for detecting the state of discharge of the molten material from the slag outlet 6. etc. will be provided.
自浄機構14は前記掻き出し棒15、感知器1
6のほかに掻き出し棒15の出没作動を行わせる
油圧シリンダー17、電磁弁18の、感知器16
から検出信号をうけて油圧シリンダー17の掻き
出を作動し指令する制御器19よりなる。出滓口
6の直下には、出滓された溶融物を受け入れて、
これを急冷細粒固化させるための水19を満した
水砕槽20が配置される。 The self-cleaning mechanism 14 includes the scraping rod 15 and the sensor 1.
In addition to 6, a sensor 16 of a hydraulic cylinder 17 and a solenoid valve 18 that cause the scraping rod 15 to move in and out.
The controller 19 receives a detection signal from the controller 19 and operates and commands the hydraulic cylinder 17 to scrape out. Immediately below the slag outlet 6, there is a space for receiving the slag molten material,
A water pulverization tank 20 filled with water 19 for rapidly cooling and solidifying the water into fine particles is arranged.
以上のような溶融処理炉は、本来や、銑鉄、フ
エロアロイ、銅、亜鉛、錫等や精錬や、カーバイ
ド、隣、溶性隣肥等の化成品の製造に用いられる
ものを改良したもので、主電極3から電流を導入
し炉内に装入された廃棄物または溶融物との間に
(サブマージド)アークを発生させ、乍ら、運転
される。本発明ではこれを廃棄物特に塩基度
(CaO/SiO2)が0.1以下でガラス分の大きい都市
ゴム焼却灰を処理用として好適に応用できるもの
である。 The above-mentioned melting furnaces are improved versions of those originally used for pig iron, ferroalloys, copper, zinc, tin, etc., refining, and chemical products such as carbide, ferroalloys, and soluble ferrofertilizers. The furnace is operated while a current is introduced from the electrode 3 to generate a (submerged) arc between it and the waste or melt charged into the furnace. In the present invention, this can be suitably applied to the treatment of waste, particularly municipal rubber incineration ash, which has a basicity (CaO/SiO 2 ) of 0.1 or less and a large glass content.
上記炉の操作法においては、まず、廃棄物とし
ての焼却灰aを廃棄物投入口4より均一な厚みと
なるように順次投入して、これを溶融処理してい
く。この処理により、焼却灰aからはメタル分を
主体とする溶融金属層bと、無機質成分と主体と
する溶融スラグ層cと2層よりなる溶融物が形成
され、炉底に溶融金属層b、その上に、溶融スラ
グ層c、さらにその上に、未溶融の焼却灰aが積
層される。 In the method of operating the furnace described above, first, incinerated ash a as waste is sequentially charged into the waste inlet 4 so as to have a uniform thickness, and is melted. Through this treatment, a molten material consisting of two layers is formed from the incineration ash a, a molten metal layer b mainly composed of metal components, and a molten slag layer c mainly composed of inorganic components, and the molten metal layer b, On top of that, a molten slag layer c is layered, and further on top of that, unmelted incineration ash a is layered.
炉本体1内に形成された溶融物(溶融スラグc
と溶融金属b)は、1350〜1550℃の高温を維持す
るが、焼却灰aの継続装入により、その嵩が増加
すると、排出口6の出滓口堰レンガ7のU字型切
欠溝8からオーバーフローし、流下物dとして、
水砕槽20に落下し、水砕スラグeとなる。 The molten material (molten slag c) formed in the furnace body 1
The molten metal b) maintains a high temperature of 1,350 to 1,550°C, but when its volume increases due to continuous charging of incinerated ash a, the U-shaped notch groove 8 of the slag weir brick 7 of the discharge port 6 overflows from the flow, and as a downstream material d,
It falls into the granulated slag tank 20 and becomes granulated slag e.
本発明の廃棄物溶融処理炉の特徴は、溶融物を
炉外に出滓中に、出滓口6手前の出滓樋上に渋滞
して溶融物の円滑な出滓を妨げる未溶融物を取除
く出滓樋自浄機構を設けたことにある。 A feature of the waste melting processing furnace of the present invention is that, while the molten material is being slaged out of the furnace, unmelted material is removed from the slag that is jammed on the slag gutter in front of the slag outlet 6 and prevents the molten material from being slaged smoothly. This is because a self-cleaning mechanism has been installed to remove the slag.
[自浄機構の作用]
自浄機構14の作用につき第3図〜第5図の要
部を拡大して示す概略側面図に副つて説明する
と、溶融スラグcの出滓中、出滓口6手前の出滓
樋上で、外気と接触冷却されて表面に厚みが5〜
10mm程度の固化皮膜c1が生ずる。これが溶融スラ
グcの出滓樋上での流れを止め出滓をストツプさ
せてしまう(第3図参照)。この場合、出滓堰レ
ンガ7の下端を測定点とする感知器16が、通常
の連続出滓時には、溶融スラグcの温度1000℃〜
1500℃を検知していたのを、溶融スラグcの出滓
流が認められず出滓がストツプして、ある温度以
外例えば600℃以下の温度を示したときは、それ
が検出信号として、制御器19に伝達される。制
御器19には、ある温度以下(例えば600℃以下)
の上記検出信号を受けときは、補助加熱電極9の
揚降装置(図示せず)に対する電極下稼働指令、
電磁弁18作動指令がプログラムとして入力され
ており、これによつて、油圧シリンダ17の掻ぎ
出し棒が15が一定時間出滓口6を通して出滓樋
内に前進後退をくり返しその先端で、固化膜c1
を破砕する(第4図参照)。これにより内部の溶
融スラグは出滓流dとして水砕槽20に落下し、
出滓が再開される。表面の固化皮膜c1は前記の
ように5〜10mmと比較的薄いものであり、しかも
内部は溶融状のスラグであるためやすく破砕され
掻き出し棒15の機械力も5Kg/cm以下と極めて
軽度の応力ですむ。出滓が再開されれば、感知器
16は再い通常の感知温度を検知するので、この
信号により制御器19は、電磁弁18に対する掻
き出し棒15の作動停止と、補助加熱電極9の上
昇を指令し、通常の出滓に戻る(第5図参照)。
以上は感知器16に光高温計を適用し制御器19
を用いたシーケンスを組み込んだ場合についての
べたが、感知器16としてITVを用い、手動に
より掻き出し棒15を出没させる自浄機構を適用
できることは言うまでもない。[Operation of the self-cleaning mechanism] The operation of the self-cleaning mechanism 14 will be explained with reference to the schematic side views showing the main parts enlarged in FIGS. 3 to 5. The slag is cooled in contact with the outside air on the trough and the surface becomes 5~5 thick.
A solidified film c1 of about 10 mm is formed. This stops the flow of the molten slag c on the slag drain and stops the slag (see Figure 3). In this case, the sensor 16 whose measurement point is the lower end of the slag weir brick 7 detects that the temperature of the molten slag c ranges from 1000° C. during normal continuous slag tapping.
1500℃ was detected, but when the flow of molten slag C is not detected and the slag stops, and a temperature other than a certain temperature, for example 600℃ or less, is detected, this is used as a detection signal and the control is started. The signal is transmitted to the device 19. The controller 19 has a temperature below a certain level (for example, below 600°C).
When receiving the above detection signal, an electrode lower operation command is issued to the lifting device (not shown) of the auxiliary heating electrode 9
An operating command for the electromagnetic valve 18 is input as a program, whereby the scraping rod 15 of the hydraulic cylinder 17 repeatedly moves forward and backward into the slag gutter through the slag outlet 6 for a certain period of time, and solidifies at its tip. Membrane c1
Crush (see Figure 4). As a result, the molten slag inside falls into the granulation tank 20 as a slag flow d,
The slag is restarted. As mentioned above, the solidified film c1 on the surface is relatively thin at 5 to 10 mm, and since the inside is molten slag, it is easily crushed, and the mechanical force of the scraping rod 15 is less than 5 kg/cm, which is an extremely light stress. nothing. When the slag extraction is resumed, the sensor 16 detects the normal sensing temperature again, and this signal causes the controller 19 to stop the operation of the scraping rod 15 relative to the solenoid valve 18 and to raise the auxiliary heating electrode 9. command and return to normal slag (see Figure 5).
In the above, an optical pyrometer is applied to the sensor 16 and the controller 19
Although the case has been described above in which a sequence using the ITV is incorporated, it goes without saying that a self-cleaning mechanism can be applied in which the ITV is used as the sensor 16 and the scraping rod 15 is manually moved in and out.
[効果]
本発明は、以上のような構成よりなるので、廃
棄物特に、溶融物の溶融レベルが激しく変動し、
出滓口手前で固化スラグを生じて、出滓樋の詰り
を起し易い廃棄物、特に塩基分の小さい都市ゴミ
で焼却灰で、分別ゴミ焼却灰の処理炉として好適
である。[Effects] Since the present invention has the above-described configuration, the melting level of waste, especially molten material, fluctuates drastically,
It is suitable as a processing furnace for incinerated ash of separated garbage, which is waste that tends to solidify slag in front of the slag outlet and clog the slag gutter, especially urban garbage with a low base content and incinerated ash.
図面は本発明の一実施例を示すものであり、第
1図は概略側面図、第2図は第1図における矢視
方向からみた部分拡大概略正面図、第3図〜第5
図は、本発明溶融処理炉の作動状態を示す要部拡
大概略側面図を示す。
1……炉本体、2……炉蓋、3……主電極、4
……廃棄物投入口、6……出滓口、7……出滓
堰、8……切次き溝、9……補助加熱電極、14
……自浄機構、15……掻き出し棒、16……感
知器、17……油圧シリンダー、18……電磁
弁、19……制御器。
The drawings show one embodiment of the present invention, and FIG. 1 is a schematic side view, FIG. 2 is a partially enlarged schematic front view seen from the direction of the arrow in FIG. 1, and FIGS.
The figure shows an enlarged schematic side view of essential parts showing the operating state of the melting furnace of the present invention. 1... Furnace body, 2... Furnace lid, 3... Main electrode, 4
... Waste inlet, 6 ... Slag outlet, 7 ... Slag weir, 8 ... Cut groove, 9 ... Auxiliary heating electrode, 14
... Self-cleaning mechanism, 15 ... Scraping rod, 16 ... Sensor, 17 ... Hydraulic cylinder, 18 ... Solenoid valve, 19 ... Controller.
Claims (1)
非溶融物が渋滞して排出を妨害していることを検
出する感知器と、該非溶融物を除去するために出
滓樋内に出没する掻き出し棒とを備えた出滓樋の
自浄機構を設置してなることを特徴とする廃棄物
溶融処理炉。1 On the slag gutter in front of the slag outlet of the waste melting processing furnace,
A self-cleaning mechanism for the slag gutter is installed, which is equipped with a sensor that detects when unmelted materials are jamming and obstructing discharge, and a scraping rod that moves into the slag gutter to remove the unmelted materials. A waste melting processing furnace characterized by:
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP61057553A JPS62213889A (en) | 1986-03-14 | 1986-03-14 | Melt treatment furnace for waste |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP61057553A JPS62213889A (en) | 1986-03-14 | 1986-03-14 | Melt treatment furnace for waste |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS62213889A JPS62213889A (en) | 1987-09-19 |
JPH0576360B2 true JPH0576360B2 (en) | 1993-10-22 |
Family
ID=13058998
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP61057553A Granted JPS62213889A (en) | 1986-03-14 | 1986-03-14 | Melt treatment furnace for waste |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS62213889A (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0580576U (en) * | 1992-04-06 | 1993-11-02 | 日立造船エンジニアリング株式会社 | Electrode attachment structure for heating of melting furnace for industrial waste |
-
1986
- 1986-03-14 JP JP61057553A patent/JPS62213889A/en active Granted
Also Published As
Publication number | Publication date |
---|---|
JPS62213889A (en) | 1987-09-19 |
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