JPS63205190A - Melt treatment of waste - Google Patents
Melt treatment of wasteInfo
- Publication number
- JPS63205190A JPS63205190A JP62036434A JP3643487A JPS63205190A JP S63205190 A JPS63205190 A JP S63205190A JP 62036434 A JP62036434 A JP 62036434A JP 3643487 A JP3643487 A JP 3643487A JP S63205190 A JPS63205190 A JP S63205190A
- Authority
- JP
- Japan
- Prior art keywords
- slag
- furnace
- flue
- duct
- molten slag
- 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
- 239000002699 waste material Substances 0.000 title claims description 16
- 239000002893 slag Substances 0.000 claims abstract description 64
- 238000002844 melting Methods 0.000 claims abstract description 29
- 230000008018 melting Effects 0.000 claims abstract description 29
- 238000000034 method Methods 0.000 claims abstract description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 17
- 239000000126 substance Substances 0.000 abstract description 7
- 239000000428 dust Substances 0.000 abstract description 3
- 238000007599 discharging Methods 0.000 abstract 1
- 230000001105 regulatory effect Effects 0.000 abstract 1
- 238000002347 injection Methods 0.000 description 3
- 239000007924 injection Substances 0.000 description 3
- 230000000694 effects Effects 0.000 description 2
- 238000010828 elution Methods 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 229910052745 lead Inorganic materials 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 238000012545 processing Methods 0.000 description 2
- 239000010801 sewage sludge Substances 0.000 description 2
- 238000012360 testing method Methods 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000009530 blood pressure measurement Methods 0.000 description 1
- 229910052793 cadmium Inorganic materials 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000001784 detoxification Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 229910001385 heavy metal Inorganic materials 0.000 description 1
- 238000011835 investigation Methods 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 238000009877 rendering Methods 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 229910052725 zinc Inorganic materials 0.000 description 1
Abstract
Description
【発明の詳細な説明】
[産業上の利用分野コ
本発明は都市ゴミ焼却灰や下水汚泥焼却灰等の廃棄物を
アーク炉等の溶融炉を用いて融解処理する方法に関する
もので、さらに詳しくほこれによって生成された溶融ス
ラグが凝固することなく出滓口から常にスムースに排出
されろようにするものである。[Detailed Description of the Invention] [Field of Industrial Application] The present invention relates to a method for melting waste such as municipal garbage incineration ash and sewage sludge incineration ash using a melting furnace such as an arc furnace. This ensures that the molten slag produced is always smoothly discharged from the slag outlet without solidifying.
[従来の技術とその問題点]
都市ゴミ焼却灰や下水汚泥焼却灰等の廃棄物中には20
.Pb、Cd等の重金層成いは有害物質が含まれている
のでこれをそのまま埋立に使用するとそれら有害物質が
地中に流出し二次公害を起こすおそれがある。そこで従
来からアーク式或いは直接通電式等の溶融炉中にこれら
廃棄物を投入し高温度にて融解して溶融スラグを生成さ
せこのi?5融スラスラグ中れらの有害物質を固溶させ
ることにより無害化し、これを埋立或いは土木用骨材等
に再利用することが行なわれている。[Conventional technology and its problems] Wastes such as municipal garbage incineration ash and sewage sludge incineration ash contain 20
.. Heavy metal layers such as Pb and Cd contain harmful substances, so if they are used as is for landfill, these harmful substances may flow into the ground and cause secondary pollution. Therefore, conventionally, these wastes are put into a melting furnace of an arc type or a direct current type, and melted at high temperature to produce molten slag. These harmful substances are dissolved in the 5-melt sludge slag to render it harmless, and this is then reused in landfills or as aggregates for civil engineering.
第3図に従来の本冷却式の廃棄物溶融処理装置の一例を
示し、図中、1は密閉型の溶融炉、2はその天井壁から
垂下した電極棒である。3は天井壁に設けられた煙道、
4は該溶融炉の一側に設けられた出滓L1.5は溶融炉
l内に廃棄物6を投入するためその天井壁に設けら、扛
だシュートである。FIG. 3 shows an example of a conventional main cooling type waste melting processing apparatus. In the figure, 1 is a closed type melting furnace, and 2 is an electrode rod hanging from the ceiling wall thereof. 3 is a flue installed in the ceiling wall,
4 is a slag chute provided on one side of the melting furnace L1.5 is a slag chute provided on the ceiling wall of the melting furnace 1 for charging waste 6 into the melting furnace 1.
出滓[14は垂直なダクト7によって密閉状に被われて
おり、該ダク1−7の上端は溶融炉1内と連通し、下端
は水槽8の水面下に浸漬して水封されている。9は出滓
口4に設けられた補助電極棒である。ダクト7の下方寄
りには本噴射ノズル10が設けられている。11は水槽
8底に設けられた掬上用コンベヤ、12はその排出口で
ある。The slag [14] is hermetically covered by a vertical duct 7, the upper end of the duct 1-7 communicates with the inside of the melting furnace 1, and the lower end is immersed under the water surface of a water tank 8 and sealed with water. . Reference numeral 9 denotes an auxiliary electrode rod provided at the slag outlet 4. A main injection nozzle 10 is provided near the bottom of the duct 7. 11 is a scooping conveyor provided at the bottom of the water tank 8, and 12 is its discharge port.
この装置では、シュート5から投入された廃棄物を電極
棒2のアーク加熱により融解し炉底に溶融スラグ13を
生成させる。この溶融スラグ13は一側の出滓口4から
ダクト7中を流下しその途中でノズル10により水が噴
射され急冷することによって該溶融スラグは粒子状に破
砕され水槽8中に沈んで冷却される。そして水槽8中に
沈んだ破砕粒子は掬上用コンベヤ11によって水面上に
搬送され排出口12に至る。なお補助電極棒9は始動時
に出滓口4上に固化しているスラグをアーク加熱により
溶解するために使用される。In this device, waste material introduced from a chute 5 is melted by arc heating of an electrode rod 2 to generate molten slag 13 at the bottom of the furnace. The molten slag 13 flows through the duct 7 from the slag outlet 4 on one side, and on the way there, water is sprayed by the nozzle 10 to rapidly cool the molten slag, and the molten slag is crushed into particles and sinks into the water tank 8 to be cooled. Ru. The crushed particles submerged in the water tank 8 are conveyed onto the water surface by a scooping conveyor 11 and reach a discharge port 12. The auxiliary electrode rod 9 is used to melt the slag solidified on the slag outlet 4 by arc heating during startup.
しかしてこの装置では溶融炉l内にて発生した高温度の
ガスは専ら溶融炉1の天井壁に開l]する煙道3を通っ
て炉外に排出されるが、その際ノズル10の木の噴射に
よって生じた水蒸気が出滓口4を通って溶融炉1に侵入
し煙道3に排出される。However, in this lever device, the high-temperature gas generated in the melting furnace 1 is exclusively discharged outside the furnace through the flue 3 that opens on the ceiling wall of the melting furnace 1. Steam generated by the injection enters the melting furnace 1 through the slag outlet 4 and is discharged into the flue 3.
このため出滓口4の溶融スラグは常にこの水蒸気或いは
ダクト7を通って来る冷気にさらされその溶融スラグの
熱をうばって固化させ該出滓1]4を閉塞させるおそ汎
があった。For this reason, the molten slag in the slag outlet 4 is constantly exposed to this water vapor or the cold air coming through the duct 7, and there is a possibility that the heat of the molten slag will be absorbed and it will solidify, thereby clogging the slag 1]4.
このような問題点を解決するものとして本発明者はすで
に実開昭58−46932号公報に開示された廃棄物溶
融処理装置を提案している。これは溶融炉内で発生した
ガスを全部出滓口側から炉外に排出するようにして出滓
口に位置する溶融スラグがその炉内発生ガスの熱で常に
保温できるようにしたものであった。しかるにそうする
と次のような新らたな問題点が生じる。即ち、未溶融の
廃棄物から舞い上がったダストがその炉内発生ガスと共
に出滓口に運ばれて溶融スラグ中にこれが混入するので
廃棄物中の有害物質が未滓化のまま炉外に排出されるこ
ととなり公害防止という本来の目的が達成されないおそ
れがあった。In order to solve these problems, the present inventor has already proposed a waste melting treatment apparatus disclosed in Japanese Utility Model Application Publication No. 58-46932. This is a system in which all the gas generated in the melting furnace is discharged from the slag outlet side to the outside of the furnace, so that the molten slag located at the slag outlet can always be kept warm by the heat of the gas generated in the furnace. Ta. However, if this is done, the following new problems will arise. In other words, the dust raised from the unmelted waste is carried to the slag outlet together with the gas generated in the furnace and mixed into the molten slag, so that harmful substances in the waste are discharged from the furnace without slag. As a result, there was a risk that the original purpose of preventing pollution would not be achieved.
[問題点を解決するための手段]
本発明は上記問題点を解決しようとするもので、廃棄物
を溶融炉に投入し融解することによって生成された溶融
スラグを該溶融炉の一側に設けられた出滓口から流出さ
せるものにおいて、溶融炉内で発生する全ガス量のうち
5〜10%を前記出滓口側から炉外へ排出し該出滓口の
溶融スラグを保温するようにしたことを特徴とする廃棄
物溶融処理方法である。[Means for Solving the Problems] The present invention attempts to solve the above problems, and includes a method in which molten slag produced by charging waste into a melting furnace and melting it is provided on one side of the melting furnace. 5 to 10% of the total amount of gas generated in the melting furnace is discharged from the slag outlet side to the outside of the furnace to keep the molten slag at the slag outlet warm. This is a waste melting treatment method characterized by the following.
[実施例1]
第1図に示した実施例1は第3図の従来例と同じく出滓
口4の下方に水槽8が設けられダクト7の途中には流下
する溶融スラグを砕化するための水を噴射するノズル1
0が設けられている。なお第1図中第3図と同一符号は
同一部分を示すのでその同一部分の詳しい説明は割愛す
る。しかしてこの実施例では、ダクト7途中のノズルI
Oの上方位置−側に副煙道14を開口させる。該副煙道
14は溶融炉lの天井壁に連通ずる前記煙道3と合流す
る。[Embodiment 1] In Embodiment 1 shown in Fig. 1, a water tank 8 is provided below the slag outlet 4 and a water tank 8 is provided in the middle of the duct 7 to crush the molten slag flowing down, as in the conventional example shown in Fig. 3. Nozzle 1 that sprays water of
0 is set. Note that the same reference numerals in FIG. 1 as in FIG. 3 indicate the same parts, so a detailed explanation of the same parts will be omitted. However, in this embodiment, the nozzle I in the middle of the duct 7
The sub-flue 14 is opened on the - side above the O. The auxiliary flue 14 merges with the flue 3 which communicates with the ceiling wall of the melting furnace I.
そしてその先に集塵装置(図示せず)が設けられ煙道3
および副煙道14を通してガスを吸引する。A dust collector (not shown) is installed at the end of the flue 3.
and sucks gas through the sub-flue 14.
15は煙道3に設けられたダンパー、1Gは副煙道14
に設けられたダンパーである。ダンパー15は煙道3に
炉内ガス圧をd1g定するため設けられた圧力計17か
ら得られた圧力測定信号に従い調節計18がその圧力を
設定値に自動制御する。また、19は煙道3のガス流敬
を測定する流量計、20は副煙道14のガス流量を測定
する流量計で、該各流量計の流准測定信号が調節計21
に入力され、該調節に+21はダンパー16の開度を調
節することにより炉内で発生した全ガスのうち5〜10
%が副煙道14を通って炉外へ排出されるようにする。15 is a damper installed in flue 3, 1G is sub-flue 14
This is a damper installed in the In the damper 15, a controller 18 automatically controls the pressure to a set value in accordance with a pressure measurement signal obtained from a pressure gauge 17 provided in the flue 3 to determine the furnace gas pressure d1g. Further, 19 is a flowmeter for measuring the gas flow rate in the flue 3, 20 is a flowmeter for measuring the gas flow rate in the sub-flue 14, and the flow rate measurement signal of each flowmeter is sent to the controller 21.
+21 is input to the adjustment to adjust the opening degree of the damper 16 so that 5 to 10 of the total gas generated in the furnace is
% is discharged out of the furnace through the auxiliary flue 14.
このため炉内で発生した高温度のガスのうちの5〜IO
+%が出滓口4」−を通過し該出滓[]4付近の溶融ス
ラグを保温できると共に、ノズルIOの本噴射によって
生じた水蒸気は専らこの副煙道14に導びかれで排出さ
4し炉内l\侵入することがない。For this reason, 5 to IO of the high temperature gas generated in the furnace
+% passes through the slag outlet 4''- and the molten slag near the slag []4 can be kept warm, and the water vapor generated by the main injection from the nozzle IO is exclusively led to this sub-flue 14 and discharged. 4. No intrusion into the furnace.
表1はこの実用化試験に供した廃棄物溶融処理設備の具
体的処理能力および稼動条件等を列設したものである。Table 1 lists the specific processing capacity and operating conditions of the waste melting treatment equipment used in this practical test.
表1
この結果溶融スラグが出滓口で固化するようなことなく
その稼動状況は非常にスムースであった。Table 1 As a result, the molten slag did not solidify at the slag outlet, and the operating conditions were very smooth.
[実施例2]
第2図に示した実施例2は実施例1のような水槽を備え
ず、出滓口4の下に設けられたコンベヤ30上に滓化物
31が直に受支されるようにしたもので、この場合コン
パv30の全体を被うチャンバ32がダクト7と連通状
に設けられている。そして副煙道1・1を該チャンバ3
2に連結し、炉内で発生した全ガス量のうちの5〜10
%を出滓口4.ダクト7゜チVンハ32を通して副煙道
14に導びくようにしている。[Example 2] Example 2 shown in FIG. 2 does not include a water tank like Example 1, and the slag 31 is directly supported on the conveyor 30 provided under the slag outlet 4. In this case, a chamber 32 that covers the entire comparator v30 is provided in communication with the duct 7. Then, connect the sub-flue 1 and 1 to the chamber 3.
2 and 5 to 10 of the total amount of gas generated in the furnace.
% to the slag outlet 4. The duct is led to the auxiliary flue 14 through a 7-inch V channel 32.
次に炉内発生ガスの全量を出滓口側から排出した場合と
本発明に従いその7%だけを出滓1コ側から排出した場
合について、その得られた滓化物の有害物質の溶出試験
を行なったので表2にその結果を示す。Next, an elution test of harmful substances in the obtained slag was conducted for the case where the entire amount of the gas generated in the furnace was discharged from the slag port side, and when only 7% of it was discharged from the slag side according to the present invention. The results are shown in Table 2.
表2
(mg/ l )
このように本発明によればZn、Pb等の溶出量が少な
(無害化の効果が確認された。Table 2 (mg/l) As described above, according to the present invention, the elution amount of Zn, Pb, etc. is small (the effect of detoxification was confirmed).
[究明の効果]
以上実施例について説明したように本発明によれば、出
滓!=1を保温してその閉塞を防ぎ溶融スラグのスムー
スな流出を維持できると共に、有害物質を可及的に確実
に溶融により無害化できる産業上有益な効果があるもの
である。[Effects of investigation] As described above in the embodiments, according to the present invention, slag! = 1 can be kept warm to prevent clogging and maintain smooth outflow of molten slag, and has the industrially beneficial effect of rendering harmful substances harmless by melting them as reliably as possible.
第1図は本発明に係る実施例1を示した装置の縦断面図
、第2図は本発明に係る実施例2を示した装置の縦断面
図、第3図は従来の装置の縦断面図である。
1・・・・1容融炉、3・・・・煙道、4・・・・出滓
1コ、6・・・・廃棄物、7・・・・ダクト、8・・・
・水槽、 10・・・・ノズル、13・・・・溶融スラ
グ、■・1・・・・副W道、 15・・・・ダンパー、
lG・・・・ダンパー。
第 1 図FIG. 1 is a vertical sectional view of a device showing a first embodiment of the present invention, FIG. 2 is a vertical sectional view of a device showing a second embodiment of the present invention, and FIG. 3 is a vertical sectional view of a conventional device. It is a diagram. 1...1 melting furnace, 3...flue, 4...1 slag, 6...waste, 7...duct, 8...
・Water tank, 10... Nozzle, 13... Molten slag, ■ 1... Sub-W road, 15... Damper,
lG...Damper. Figure 1
Claims (1)
された溶融スラグを該溶融炉の一側に設けられた出滓口
から流出させるものにおいて、溶融炉内で発生する全ガ
ス量のうち5〜10%を前記出滓口側から炉外へ排出し
該出滓口の溶融スラグを保温するようにしたことを特徴
とする廃棄物溶融処理方法。 2、出滓口から水槽に流下する溶融スラグを被うように
ダクトを形成し、該ダクトの途中には出滓口より流下す
る溶融スラグに砕化用の水を噴射するノズルを設け、溶
融炉内で発生する全ガス量のうち5〜10%を前記出滓
口を経てダクト中に導びいて前記ノズルの上方から排出
するようにしたことを特徴とする特許請求の範囲第1項
に記載の廃棄物溶融処理方法。[Scope of Claims] 1. In a device in which molten slag generated by charging waste into a melting furnace and melting it flows out from a slag outlet provided on one side of the melting furnace, 5 to 10% of the total amount of gas generated in the process is discharged from the slag outlet to the outside of the furnace, and the molten slag at the slag outlet is kept warm. 2. A duct is formed to cover the molten slag flowing down from the slag outlet into the water tank, and a nozzle is installed in the middle of the duct to inject water for crushing into the molten slag flowing down from the slag outlet. Claim 1, characterized in that 5 to 10% of the total amount of gas generated in the furnace is guided into the duct through the slag outlet and discharged from above the nozzle. The described waste melting treatment method.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP62036434A JPS63205190A (en) | 1987-02-19 | 1987-02-19 | Melt treatment of waste |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP62036434A JPS63205190A (en) | 1987-02-19 | 1987-02-19 | Melt treatment of waste |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS63205190A true JPS63205190A (en) | 1988-08-24 |
Family
ID=12469706
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP62036434A Pending JPS63205190A (en) | 1987-02-19 | 1987-02-19 | Melt treatment of waste |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS63205190A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2001330234A (en) * | 2000-05-19 | 2001-11-30 | Tsukishima Kikai Co Ltd | Melting furnace and discharging method therefor |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS55102815A (en) * | 1979-02-01 | 1980-08-06 | Takuma Co Ltd | Melting slag take out and control device for vertical type waste melting and gasifying furnace |
JPS611912A (en) * | 1984-06-13 | 1986-01-07 | Central Res Inst Of Electric Power Ind | Method of discharging molten slag |
-
1987
- 1987-02-19 JP JP62036434A patent/JPS63205190A/en active Pending
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS55102815A (en) * | 1979-02-01 | 1980-08-06 | Takuma Co Ltd | Melting slag take out and control device for vertical type waste melting and gasifying furnace |
JPS611912A (en) * | 1984-06-13 | 1986-01-07 | Central Res Inst Of Electric Power Ind | Method of discharging molten slag |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2001330234A (en) * | 2000-05-19 | 2001-11-30 | Tsukishima Kikai Co Ltd | Melting furnace and discharging method therefor |
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