JPH0519045B2 - - Google Patents
Info
- Publication number
- JPH0519045B2 JPH0519045B2 JP62079641A JP7964187A JPH0519045B2 JP H0519045 B2 JPH0519045 B2 JP H0519045B2 JP 62079641 A JP62079641 A JP 62079641A JP 7964187 A JP7964187 A JP 7964187A JP H0519045 B2 JPH0519045 B2 JP H0519045B2
- Authority
- JP
- Japan
- Prior art keywords
- ash
- melting
- incinerated ash
- temperature
- incinerated
- 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
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Landscapes
- Incineration Of Waste (AREA)
- Gasification And Melting Of Waste (AREA)
Description
【発明の詳細な説明】
[産業上の利用分野]
この発明は都市ゴミ等の焼却灰を溶融処理する
灰溶融炉の燃焼及溶融制御装置に関する。DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to a combustion and melting control device for an ash melting furnace for melting incinerated ash of municipal waste and the like.
[従来の技術]
都市ゴミ(都市から排出されたゴミ)の焼却灰
を溶融させてスラグを付る装置として従来にあつ
ては焼却灰を加熱して溶融処理する灰溶融炉が知
られている。[Prior Art] An ash melting furnace that heats and melts incinerated ash is conventionally known as a device for melting incinerated ash of municipal waste (garbage discharged from cities) to form slag. .
ところが、この種の灰溶融炉にあつては、焼却
灰の溶融源に油や電気を使用するために灰溶融炉
のランニングコストが増加し、経済的なものでな
かつた。 However, in this type of ash melting furnace, the running cost of the ash melting furnace increases due to the use of oil or electricity as a source for melting the incinerated ash, making it uneconomical.
そこで、近来にあつては焼却炉の排出口より下
方の炉体に、その排出口から投下された焼却灰を
下流へ移送する通路を形成し、その通路の上流に
通路に開口させて焼却灰中に空気を供給し、その
焼却灰中の残留カーボン(焼却灰の重量に対して
10〜15%)と空気とを混合させて燃焼発熱反応を
生じさせる空気供給手段を設け、この反応により
残留カーボンを燃焼させ、この反応熱(焼却熱)
を焼却灰の溶融熱として利用する灰溶融炉が開発
されている。 Therefore, in recent years, a passage has been formed in the furnace body below the incinerator outlet to transport the incinerated ash dropped from the outlet to the downstream, and a passage is opened upstream of the incinerator to transport the incinerated ash. The residual carbon in the incinerated ash (relative to the weight of the incinerated ash) is
An air supply means is provided to mix 10 to 15%) with air to produce a combustion exothermic reaction, and this reaction burns residual carbon and releases the reaction heat (heat of incineration).
An ash melting furnace has been developed that uses this as heat for melting incinerated ash.
[発明が解決しようとする問題点]
ところが、燃焼発熱反応により溶融炉内の焼却
灰が高温になり溶融温度を超えると、空気供給手
段の開口端が溶融された溶湯によつて閉塞される
不具合か発生する。開口端の閉塞は即ち、焼却灰
の再焼却を不能にする。また、逆に、低温になり
すぎると溶融された溶湯が凝固して固着し、炉内
閉塞を招き、運転不能に陥るため解決すべき問題
点に挙げられている。[Problems to be Solved by the Invention] However, when the incinerated ash in the melting furnace becomes high in temperature due to the combustion exothermic reaction and exceeds the melting temperature, the open end of the air supply means is blocked by the molten metal. or occur. Blocking the open end thus makes it impossible to re-incinerate the incinerated ash. On the other hand, if the temperature is too low, the molten metal will solidify and solidify, causing blockage in the furnace and rendering it inoperable, which is a problem that needs to be solved.
[問題点を解決するための手段]
この発明は上記問題点を解決することを目的と
し、主燃焼炉より灰溶融炉内に投下された焼却灰
中の残留カーボンに燃焼発熱反応を励起させ、そ
の燃焼発生熱を溶融熱源として焼却灰を溶融すべ
く、灰溶融炉内上流部に焼却灰に空気を供給する
ための開口を有する空気供給手段を設けた灰溶融
炉の焼却及び溶融制御装置において、上記灰溶融
炉内上流部に焼却灰を下流に移送するプツシヤー
を出没自在に設けると共に、その上流部もしくは
下流部雰囲気温度または溶融排ガス温度を連続し
て検出する温度検出手段を設け、この温度検出手
段により焼却灰の初期溶融温度が所定時間持続し
て検出されたとき、焼却灰を下流側へ移送すべく
上記プツシヤーを作動するコントローラを設けた
ものである。[Means for Solving the Problems] The present invention aims to solve the above problems by exciting a combustion exothermic reaction in the residual carbon in the incinerated ash thrown into the ash melting furnace from the main combustion furnace, In an incineration and melting control device for an ash melting furnace, which is provided with an air supply means having an opening for supplying air to the incinerated ash in the upstream part of the ash melting furnace, in order to melt the incinerated ash using the combustion generated heat as a melting heat source. A pusher for transporting the incinerated ash downstream is removably provided in the upstream part of the ash melting furnace, and a temperature detection means for continuously detecting the atmospheric temperature or the molten exhaust gas temperature in the upstream or downstream part is provided, and the temperature A controller is provided that operates the pusher to transfer the incinerated ash to the downstream side when the initial melting temperature of the incinerated ash is detected by the detection means for a predetermined period of time.
[作用]
主焼焼炉より投下された焼却灰は、上流部内に
開口された空気供給手段からの空気によつて焼却
灰中の残留カーボンが燃焼発熱反応を起こす。こ
れによつて焼却灰が溶融される。一方温度検出手
段は灰溶融炉内の上流部または下流部の雰囲気温
度を連続的に検出し、その検出温度をコントロー
ラに入力する。コントローラは温度検出手段によ
り焼却灰の初期溶融温度が所定時間持続して検出
されたとき、焼却灰を下流側へ移送すべく上記プ
ツシヤーを作動して上流部の焼却灰を下流部へ移
送する。これにより空気供給手段の開口端を溶湯
で閉塞させることなく、かつ、溶湯の冷却固着に
よる炉内閉塞に至らしめることなく、安定した溶
融運転が行なえる。[Function] The incinerated ash dropped from the main incinerator causes residual carbon in the incinerated ash to undergo a combustion exothermic reaction by air from the air supply means opened in the upstream section. This melts the incineration ash. On the other hand, the temperature detection means continuously detects the atmospheric temperature in the upstream or downstream part of the ash melting furnace, and inputs the detected temperature to the controller. When the initial melting temperature of the incinerated ash is detected by the temperature detection means for a predetermined period of time, the controller operates the pusher to transfer the incinerated ash to the downstream side, thereby transferring the incinerated ash in the upstream part to the downstream part. As a result, stable melting operation can be performed without clogging the open end of the air supply means with the molten metal and without clogging the furnace due to solidification of the molten metal upon cooling.
[実施例]
以下この発明の好適一実施例を添付図面に基づ
いて説明する。[Embodiment] A preferred embodiment of the present invention will be described below with reference to the accompanying drawings.
第1図には灰溶融炉のシステム図が示してあ
る。 FIG. 1 shows a system diagram of an ash melting furnace.
排出口6より下方の炉体1には、下方に傾斜さ
せて通路7が接続されており、この通路7の先端
部はさらに重力方向に屈曲されて図示しないスラ
グ生成室に接続される。主燃料室5より下方の炉
体1には、主燃料室5側と上記通路7側とに仕切
る開閉自在な開閉扉8が設けてあり、この実施例
にあつては開閉扉8は水平方向にスライドさせて
開閉できるように構成されている。 A downwardly inclined passage 7 is connected to the furnace body 1 below the discharge port 6, and the tip of this passage 7 is further bent in the direction of gravity and connected to a slag generation chamber (not shown). The furnace body 1 below the main fuel chamber 5 is provided with a door 8 that can be opened and closed to partition the main fuel chamber 5 side and the passage 7 side, and in this embodiment, the door 8 is oriented horizontally. It is configured so that it can be opened and closed by sliding it.
一方、通路7にはその上上流部7aに開閉扉8
の開時に主燃焼室から投下された一定量の焼却灰
を上流部7aから下流部7bへ移動させるプツシ
ヤー9が設けられる。プツシヤー9は実施例にあ
つては油圧または空圧の流体シリンダが採用さ
れ、その先端部9aが斜め下方に傾斜されて焼却
灰を移送しやすくなつている。通路7の炉床7c
内には、その通路方向に沿つて炉床7c及び通路
7内を加熱するヒータ10が順次配設され、上流
部7aのヒータは約800℃に、下流部7bのヒー
タ10は約1300℃に加熱される。即ち上流部7a
のヒータ10の温度は、焼却物の焼却温度に、下
流部7bの温度は焼却物の溶融温度に調整され
る。また通路7の上流部7aには、この上流部7
aの通路7内に開口されて通路7内に空気を噴出
する空気供給手段11が配設されており、この空
気供給手段11は通路方向に順次間隔をおいて複
数設けられている。下流部7bには、この下流部
7bの炉床7cを臨ませて火炎バーナ等のの加熱
手段12が配設されている。 On the other hand, in the passage 7, an opening/closing door 8 is provided at the upstream part 7a.
A pusher 9 is provided to move a certain amount of incinerated ash dropped from the main combustion chamber when the main combustion chamber is opened from the upstream section 7a to the downstream section 7b. In the embodiment, the pusher 9 is a hydraulic or pneumatic fluid cylinder, and its tip 9a is inclined diagonally downward to facilitate the transfer of the incinerated ash. Hearth 7c of passage 7
Inside, heaters 10 for heating the hearth 7c and the inside of the passage 7 are sequentially arranged along the passage direction, and the heater 10 in the upstream part 7a heats up to about 800°C, and the heater 10 in the downstream part 7b heats up to about 1300°C. heated. That is, the upstream part 7a
The temperature of the heater 10 is adjusted to the incineration temperature of the incinerated material, and the temperature of the downstream section 7b is adjusted to the melting temperature of the incinerated material. In addition, the upstream portion 7a of the passage 7 has a
Air supply means 11 which is opened in the passage 7 of a and blows air into the passage 7 is disposed, and a plurality of air supply means 11 are provided at sequential intervals in the passage direction. A heating means 12 such as a flame burner is disposed in the downstream portion 7b, facing the hearth 7c of the downstream portion 7b.
一方、開閉扉8より下方で且つ上流部7aの炉
床7cより上方の炉体1内には、上流部内雰囲気
温度を連続して計測する温度検出手段13が配設
されており、この温度検出手段13はコントロー
ラ14に接続される。コントローラ14は例えば
第2図に示されるように、検出温度、即ち燃焼ガ
ス温度(上流部内雰囲気温度)が所定時間焼却灰
の初期溶融温度に至つたときに(例えば950℃〜
1100℃)、上記プツシヤー9に出力して上流部7
aの焼却灰を下流部7bへ移送するように構成さ
れる。コントローラ14としては具体的にCPU、
PID等が採用される。 On the other hand, in the furnace body 1 below the opening/closing door 8 and above the hearth 7c of the upstream section 7a, a temperature detection means 13 for continuously measuring the atmospheric temperature in the upstream section is disposed. The means 13 are connected to a controller 14 . For example, as shown in FIG. 2, the controller 14 operates when the detected temperature, that is, the combustion gas temperature (atmosphere temperature in the upstream section) reaches the initial melting temperature of the incinerated ash for a predetermined period of time (for example, from 950°C to
1100℃), output to the pusher 9 and send it to the upstream section 7.
It is configured to transport the incinerated ash of a to the downstream part 7b. Specifically, the controller 14 includes a CPU,
PID etc. are adopted.
次に作用を説明する。 Next, the action will be explained.
通路7の上流部7aに投下された焼却灰はこの
上流部7aにて加熱され空気供給手段11からの
空気を供給されて燃焼発熱反応を起し、焼却灰中
の残留カーボンが焼却される。これと同時に、こ
のとき発生した燃焼熱は下流部7bの燃焼後の焼
却灰の溶融を促進する。温度検出手段13により
計測された上流部7aの燃料ガス熱が所定時間焼
却灰の初期溶融温度に達すると、コントローラ1
4はプツシヤー9を作動して上流部7aの焼却灰
を下流部7bに移送する。移送された焼却灰は下
流部7bで溶融される。ここで下流部で溶融され
た焼却灰は落下し、スラグ生成室で固化される。
即ち無公害で減容化したスラグが得られる。 The incinerated ash dropped into the upstream section 7a of the passage 7 is heated in this upstream section 7a, and air is supplied from the air supply means 11 to cause a combustion exothermic reaction, whereby residual carbon in the incinerated ash is incinerated. At the same time, the combustion heat generated at this time promotes the melting of the incinerated ash after combustion in the downstream section 7b. When the fuel gas heat in the upstream section 7a measured by the temperature detection means 13 reaches the initial melting temperature of the incinerated ash for a predetermined period of time, the controller 1
4 operates the pusher 9 to transfer the incinerated ash from the upstream section 7a to the downstream section 7b. The transferred incineration ash is melted in the downstream section 7b. Here, the incineration ash melted downstream falls and solidifies in the slag generation chamber.
That is, a pollution-free and reduced volume slag can be obtained.
[発明の効果]
以上説明したことがら明らかなようにこの発明
によれば次のごとき優れた効果を発揮する。[Effects of the Invention] As is clear from the above explanation, the present invention exhibits the following excellent effects.
(1) 通路内に開口させて空気を噴出する流体供給
手段の開口の閉塞や固着スラグ(クリンカ)発
生による通路閉塞が防止され、通路の上流部で
の焼却灰の燃焼、通路の下流部での焼却灰の溶
融が確実になされ信頼性が大幅に向上する。(1) This prevents clogging of the opening of the fluid supply means that opens into the passage and blows out air, and prevents the passage from being blocked due to the generation of fixed slag (clinker), and prevents the combustion of incinerated ash in the upstream part of the passage and the downstream part of the passage. The incineration ash is reliably melted, greatly improving reliability.
(2) 炉のランニングコストを低下させることがで
きる。(2) Furnace running costs can be reduced.
第1図はこの発明の好適一実施例を示すシステ
ム図、第2図は制御パターンの一例を示す図であ
る。
図中、1は炉体、4は扉、5は主燃焼室、6は
排出口、7は通路、8は開閉扉、9はプツシヤ
ー、10はヒータ、11は空気供給手段、12は
加熱手段、13は温度検出手段、14はコントロ
ーラである。
FIG. 1 is a system diagram showing a preferred embodiment of the present invention, and FIG. 2 is a diagram showing an example of a control pattern. In the figure, 1 is a furnace body, 4 is a door, 5 is a main combustion chamber, 6 is an exhaust port, 7 is a passage, 8 is an opening/closing door, 9 is a pusher, 10 is a heater, 11 is an air supply means, and 12 is a heating means , 13 is a temperature detection means, and 14 is a controller.
Claims (1)
中の残留カーボンに燃焼発熱反応を励起させ、そ
の燃焼発生熱を溶融熱源として焼却灰を溶融すべ
く、灰溶融炉内上流部に焼却灰に空気を供給する
ための開口を有する空気供給手段を設けた灰溶融
炉の焼焼及び溶融制御装置において、上記灰溶融
炉内上流部に焼却灰を下流に移送するプツシヤー
を出没自在に設けると共に、その上流部もしくは
下流部雰囲気温度または溶融排ガス温度を連続し
て検出する温度検出手段を設け、該検出手段によ
り焼却灰の初期溶融温度が所定時間持続して検出
されたとき、焼却灰を下流側へ移送すべく上記プ
ツシヤーを作動するコントローラを設けたことを
特徴とする灰溶融炉の焼焼及び溶融制御装置。1 Excite a combustion exothermic reaction in the residual carbon in the incinerated ash thrown into the ash melting furnace from the main combustion furnace, and incinerate it in the upstream part of the ash melting furnace in order to melt the incinerated ash using the generated heat of combustion as a melting heat source. In the incineration and melting control device for an ash melting furnace, which is provided with an air supply means having an opening for supplying air to the ash, a pusher for transferring the incinerated ash to the downstream is provided in the upstream part of the ash melting furnace so that it can appear and disappear at will. At the same time, a temperature detection means for continuously detecting the atmospheric temperature or molten exhaust gas temperature at the upstream or downstream part is provided, and when the initial melting temperature of the incinerated ash is detected by the detection means for a predetermined period of time, the incinerated ash is An apparatus for controlling incineration and melting of an ash melting furnace, characterized in that a controller is provided to operate the pusher to transfer the ash to the downstream side.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP7964187A JPS63247519A (en) | 1987-04-02 | 1987-04-02 | Ash melting furnace combustion and melting control device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP7964187A JPS63247519A (en) | 1987-04-02 | 1987-04-02 | Ash melting furnace combustion and melting control device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS63247519A JPS63247519A (en) | 1988-10-14 |
| JPH0519045B2 true JPH0519045B2 (en) | 1993-03-15 |
Family
ID=13695728
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP7964187A Granted JPS63247519A (en) | 1987-04-02 | 1987-04-02 | Ash melting furnace combustion and melting control device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS63247519A (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2737861B2 (en) * | 1991-07-08 | 1998-04-08 | 三機工業株式会社 | Combustion control method for refuse incinerator |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5585813A (en) * | 1978-12-22 | 1980-06-28 | Kubota Ltd | Incinerator |
| JPS59180212A (en) * | 1983-03-30 | 1984-10-13 | Kawasaki Heavy Ind Ltd | Combustion controller in refuse incinerator |
| JPS6033418A (en) * | 1983-08-03 | 1985-02-20 | Ishikawajima Harima Heavy Ind Co Ltd | Disposal device for incinerating slag |
-
1987
- 1987-04-02 JP JP7964187A patent/JPS63247519A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS63247519A (en) | 1988-10-14 |
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|---|---|---|---|
| EXPY | Cancellation because of completion of term | ||
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