JP3893200B2 - Method for preventing closure of slag outlet in combustion melting furnace of waste treatment equipment - Google Patents

Method for preventing closure of slag outlet in combustion melting furnace of waste treatment equipment Download PDF

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JP3893200B2
JP3893200B2 JP25308997A JP25308997A JP3893200B2 JP 3893200 B2 JP3893200 B2 JP 3893200B2 JP 25308997 A JP25308997 A JP 25308997A JP 25308997 A JP25308997 A JP 25308997A JP 3893200 B2 JP3893200 B2 JP 3893200B2
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melting furnace
combustion melting
combustion
discharge port
furnace
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JP25308997A
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JPH1194226A (en
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裕昭 原田
豊 大久保
孝 大野
俊美 塚田
幸利 横田
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Mitsui Engineering and Shipbuilding Co Ltd
Mitsui E&S Holdings Co Ltd
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Mitsui Engineering and Shipbuilding Co Ltd
Mitsui E&S Holdings Co Ltd
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Description

【0001】
【発明の属する技術分野】
本発明は、廃棄物処理装置の燃焼溶融炉におけるスラグ排出口の閉鎖防止方法に関するものである。
【0002】
【従来の技術】
従来、家庭やオフィスなどから出される都市ごみ等の一般廃棄物、または廃プラスチック、カーシュレッダー・ダスト、廃オフィス機器、電子機器、化成品等の産業廃棄物等、いわゆる可燃物を含有する廃棄物処理装置としては、種々の方式が提案、実施されているが、近年、環境問題、特にダイオキシン発生の問題から、燃焼溶融炉を有する廃棄物処理装置が注目されている。
【0003】
この燃焼溶融炉を有する廃棄物処理装置は、たとえば特公平6−56253号公報、EP0340537号等に示されるように、廃棄物を加熱して熱分解し、熱分解ガスと主として不揮発性成分からなる熱分解残留物とを生成し、前記熱分解ガスと、前記熱分解残留物から分離された燃焼性成分と、燃焼用空気とを燃焼溶融炉に供給して燃焼させ、この燃焼により生じた燃焼性成分中に含まれる灰分を溶融して溶融スラグとなし、この溶融スラグを燃焼溶融炉の内壁に付着させて流下させ、下部の排出口から排出して冷却固化させるとともに、高温の燃焼ガスを冷却して排ガスとなし、この排ガスの一部を燃焼溶融炉内に供給して温度制御するようにした廃棄物処理装置の燃焼溶融炉が知られている。
【0004】
【発明が解決しようとする課題】
ところで前記したような廃棄物処理装置の燃焼溶融炉において、この燃焼溶融炉の保守、点検等を行う場合、運転を停止する必要があるが、この場合、溶融スラグがスラグ排出口近傍において固化し、スラグ排出口が閉鎖する恐れがあった。すなわち、この燃焼溶融炉の運転を停止する場合、まず燃焼溶融炉および熱分解ガスの供給を停止した後、燃焼用空気の供給を停止することとなる。このことにより、燃焼溶融炉内の温度は自然冷却により低下することとなるが、この温度低下は外気に通じるスラグ排出口近傍において著しい。そのため、燃焼溶融炉の内壁に付着して流下してくる溶融スラグは、スラグ排出口近傍に達して冷却固化されることとなり、結果としてこのスラグ排出口を閉鎖することとなるのである。
【0005】
このようなスラグ排出口の閉鎖が生じると、再運転時には、この固化スラグを除去する必要があり、その結果、運転効率を低下させるばかりでなく、燃焼溶融炉に損傷を与える恐れがある等の問題があった。
【0006】
【課題を解決するための手段】
本発明は前記したような従来の問題点を解決するためになされたものであって、廃棄物を加熱して熱分解し、熱分解ガスと主として不揮発性成分からなる熱分解残留物とを生成し、前記熱分解ガスと前記熱分解残留物から分離された燃焼性成分と燃焼用空気とを燃焼溶融炉に供給して燃焼させ、生じた灰分を燃焼溶融炉内で溶融してなる溶融スラグを内壁に付着させて流下させ、燃焼溶融炉下部のスラグ排出口から排出して冷却固化させるようにした廃棄物処理装置の燃焼溶融炉において、燃焼溶融炉の運転停止時に少なくとも燃焼溶融炉の炉内下部に、排ガスの一部または燃焼用空気の一部の少なくとも一方を供給して炉内下部を急冷して、流下する溶融スラグを燃焼溶融炉の内壁面上で固化させるようにしたことを特徴とする。
【0007】
そして燃焼溶融炉の下部に排ガスの一部又は燃焼用空気の一部の少なくとも一方を供給するよう構成し、この燃焼溶融炉の運転を停止したとき、この排ガスの一部又は燃焼用空気の一部を供給して、炉内下部を急冷する方法を採るのが好ましい。
【0008】
更に炉内下部に温度検出器を設けこの温度検出器からの信号に基づいて炉内下部への排ガスの一部又は燃焼用空気の一部の供給量を制御するのがよい。
【0009】
更に又燃焼溶融炉には内部の圧力検知器が配置され、この圧力検知器の信号により燃焼溶融炉の後流側に配置される吸引装置を制御し、燃焼溶融炉の内圧が所定値以下、例えば大気圧以下になるよう制御される。かかる方法によれば燃焼溶融炉の運転が停止したとき下部が急冷されるため内壁面に沿って流下している溶融スラグはこの内壁面上に固化して付着するためスラグ排出口近傍まで達することはない。したがって、スラグ排出口の閉鎖が防止できるのである。
【0010】
そして、この燃焼溶融炉の下部の急冷手段としては、燃焼溶融炉内の温度制御用として用いられている排ガスの一部を炉内の下部に供給し、又は通常燃焼溶融炉の下部に供給されている2次、3次の燃焼用空気を冷却媒体として利用することにより特別の冷却装置を設けることなく炉内下部を急冷することができる。
【0011】
この溶融スラグは通常1,300℃程度で燃焼溶融炉の内壁に付着して流下しているが、この溶融スラグは本発明者の知見によれば1,200℃程度で粘度が大となり、1,100℃程度になると固化して流下しなくなる。したがって、燃焼溶融炉の下部の急冷は、少なくともこの1,100℃近傍まで急速に低下させるのがよい。そのため、燃焼溶融炉内の下部温度を検出し冷却媒体としての排ガスの一部又は燃焼用空気の一部の供給量が制御される。そして、1,100℃程度の所定値まで温度が低下すると、排ガスの一部又は燃焼用空気の一部の供給を停止することとなる。
【0012】
一方、排ガスの一部又は燃焼用空気の一部を燃焼溶融炉下部へ供給することにより炉内圧力が上昇する。このような炉内圧力が上昇すると残留する燃焼ガス等がスラグ排出口等から大気中に放出されるため、燃焼溶融炉内の圧力を検出し、この圧力が大気圧以下になるように吸引装置を制御する。
【0013】
【発明の実施の形態】
以下、図1乃至3に基づき本発明による廃棄物処理装置の燃焼溶融炉におけるスラグ排出口の閉鎖防止方法の実施例を説明する。
【0014】
図1は、廃棄物処理装置1の系統図である。この廃棄物処理装置1は、主として熱分解反応器2と燃焼溶融炉3とで構成されている。詳述すれば廃棄物aは投入部4及び駆動装置5を有するスクリューフィーダ6により熱分解反応器2内に供給される。熱分解反応器3は例えば横型回転式ドラムで構成され、吸引装置としての誘引送風機7により内部は低酸素雰囲気が形成されるようになっている。そしてこの熱分解反応器2内には、燃焼溶融炉3の後側に配置された高温空気加熱器8により、加熱された加熱空気bがラインL1から供給され、間接加熱により供給された廃棄物を300℃〜600℃に、通常は450℃程度に加熱するようになっている。そしてこの廃棄物aは熱分解し熱分解ガスG1と熱分解残留物cとが生成し、この熱分解ガスG1と熱分解残留物cとは排出装置9により分離され、熱分解ガスG1はラインL2を経て燃焼溶融炉3のバーナ10に供給され、一方熱分解残留物cは冷却装置11により冷却された後分離装置12に供給され、ここでカーボンを主体とする燃焼性成分dとガレキ等の不燃焼性成分eとに分離される。そして分離された不燃焼性物eはコンテナ13に回収され、燃焼性成分dは粉砕機14に供給されて例えば1mm以下に粉砕された後制御バルブV1を有するラインL3を経て燃焼溶融炉3のバーナ10に供給され、ここでラインL2から供給された熱分解ガスG1と押込送風機15によりラインL4から供給される燃焼用空気fとにより約1,300°程度の高温域で燃焼される。燃焼用空気fのラインは制御バルブV2を有する一次空気ラインL41によりバーナ10へ供給されるとともにその一部は制御バルブV3を有する2次空気ラインL42を経て下部に設けられた2次空気用ノズル16にまた制御バルブV4を有する3次空気ラインL43を経て3次空気用ノズル17に夫々供給され、低NOxを図るため所謂多岐燃焼を行うようになっている。そして、このような燃焼により生じた燃焼灰や燃焼性成分中に含まれる灰分は溶融スラグgとなって燃焼溶融炉3の内壁に付着して流下し下部のスラグ排出口18から図示しない水槽中に排出され冷却固化され、一方燃焼ガスG2は高温空気加熱器8により熱回収された後ラインL5を経て廃熱ボイラ19で更に熱回収され、集塵装置20及びガス洗浄装置21で除塵かつ洗浄され比較的低温の排ガスG3となり、一部は煙突22から大気へ放出されるとともに他の一部は押込送風機23によりラインL6を経て冷却装置11ヘイナートガスとして供給される。更に排ガスG3の他の一部は押込送風機24によりラインL7を経て燃焼溶融炉3に供給され、燃焼溶融炉3の温度制御がなされるようになっている符号25は、電熱伝対の如き温度検出器であり符号26は圧力検出器であって、この温度検出器25と圧力検出器26とは燃焼溶融炉3の下部に設けられるとともにその信号S1、S2は夫々制御装置27に入力される。制御装置27は記憶装置28と比較器29と演算装置30と信号作成装置31とにより構成されている。符号32は廃熱ボイラ19で発生した蒸気Xにより発電される発電装置である。
【0015】
かかる構成の廃棄物処理装置1における燃焼溶融炉3において通常運転実施例においては、図示しない制御装置により制御バルブV1〜V4や押込送風機24が制御され、燃焼溶融炉3内の温度が約1,300℃になるように燃焼性成分dや熱分解ガスG1の又は排ガスG3の一部等の供給が制御されている。
【0016】
そして、このような通常運転時において熱分解残留物3の運転を停止する場合、先ず制御バルブV1を制御して燃焼性成分dの供給を停止するとともにライン2から供給される熱分解ガスG1を図示しないラインから排出することにより燃焼溶融炉3への供給を停止する。そして温度検出器25の信号S1が制御装置27の比較器29に入力され、ここで記憶装置28に予め入力されている所定値、例えば、1,100℃近傍の温度の信号S3と比較され変差の信号S4が演算装置30に入力される。そしてこの変差による比例信号S5が信号作成装置31に入力され、ここで制御信号S6が押込送風機15及び制御バルブV2〜V4に与えられる。具体的にはこの制御信号S6により押込送風機15が作動するとともに少なくとも制御バルブV3、V4が開放され、燃焼溶融炉3の下部へ燃焼用空気の一部である二次空気及び三次空気が冷却媒体として供給され、勿論この場合必要に応じて制御バルブV2を開放し一次空気を冷却媒体として利用してもよい。このとき燃焼溶融炉3内の圧力が圧力検査器26により検出され、その信号S2が比較器29に入力され前記と同様にして記憶装置28に予め入力されている所定値、例えば大気圧と比較された後、演算器30及び信号作成装置31を経て制御信号S7が吸引装置としての誘引送風機7に与えられ、少なくとも燃焼溶融炉3の圧力が大気圧以下になるよう制御される。
【0017】
図2は他の実施例を示すものであって、この図において図1と同一符号は同一名称を示す。この実施例においては排ガスG3の一部を燃焼溶融炉3に供給するラインL7には分岐のラインL71が設けられ、このラインL71の他端は燃焼溶融炉3の下部に連結されている。そして制御装置27からの制御信号S6を押込送風機24、制御バルブV5、V6に与えることによって少なくとも燃焼溶融炉3の下部にこの排ガスG3の一部を冷却媒体として供給することにより例えば急冷速度が50〜500℃/minとなるよう急冷することができるのである。本発明者の知見によれば図3に示すように溶融スラグgの流下速度は温度が1,300℃においては、1〜5m/minであるが、その速度は温度の低下とともに減速する。そしてその温度が1,100℃近傍においては固化して流下しなくなることが判明した。そして通常燃焼溶融炉3内の温度が自然冷却によりこの1,100℃程度まで低下するのには約0.1〜0.5H程度を必要とするため、燃焼溶融炉3の下部に存在する溶融スラグgは殆どスラグ排出18近傍まで達し冷却固化されるが、前記したように溶融スラグgが固化する温度まで急速に冷却することにより、燃焼溶融炉3の内壁上にこの溶融スラグgを固化して付着させることができ、結果としてスラグ排出口18の閉鎖を防止することができる。
【0018】
前記実施例においては燃焼用空気の一部とを夫々燃焼溶融炉3の下部に別々に供給する場合について説明したが、これらは併せて供給するようにしてもよい。
【0019】
【発明の効果】
以上の説明から明らかなように、本発明による廃棄物処理装置の燃焼溶融炉におけるスラグ排出口の閉鎖防止方法によれば、燃焼溶融炉の運転停止時においてこの燃焼溶融炉の下部を急冷することにより内壁面上に付着して流下している溶融スラグを冷却固化させることとなり、結果としてスラグ排出口の閉鎖を防止することができる。
【0020】
更に、排ガスの一部又は燃焼用空気の一部を冷却媒体として使用することにより、特別の装置を設ける必要もなくスラグ排出口の閉鎖を防止することができるという効果がある。
【図面の簡単な説明】
【図1】本発明による廃棄物処理装置の燃焼溶融炉におけるスラグ排出口の閉鎖防止方法を実施するための系統図である。
【図2】本発明による廃棄物処理装置の燃焼溶融炉におけるスラグ排出口の閉鎖防止方法の他の実施形態を示す系統図である。
【図3】溶融スラグの流下速度と温度との関係図である。
【符号の説明】
1 廃棄物処理装置
2 熱分解反応器
3 燃焼溶融炉
4 投入部
5 起動装置
6 スクリューフィーダ
7 誘引送風機
8 高温空気加熱器
9 排出装置
10 バーナ
11 冷却装置
12 分離装置
13 コンテナ
14 粉砕機
15,23,24 押込送風機
16 2次空気ノズル
17 3次空気ノズル
18 スラグ排出口
19 廃熱ボイラ
20 集塵装置
21 ガス洗浄装置
22 煙突
25 温度検出器
26 圧力検出器
27 制御装置
28 記憶装置
29 比較器
30 演算装置
31 信号作成装置
32 発電装置
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a method for preventing closure of a slag discharge port in a combustion melting furnace of a waste treatment apparatus.
[0002]
[Prior art]
Conventional waste such as municipal waste from households and offices, or waste containing so-called combustibles, such as industrial waste such as waste plastic, car shredder dust, waste office equipment, electronic equipment, and chemical products Various types of treatment apparatus have been proposed and implemented, but in recent years, a waste treatment apparatus having a combustion melting furnace has attracted attention due to environmental problems, particularly the problem of dioxin generation.
[0003]
As shown in, for example, Japanese Patent Publication No. 6-56253, EP0340537, etc., the waste treatment apparatus having this combustion melting furnace is composed of pyrolysis gas and mainly non-volatile components. The pyrolysis residue is generated, and the pyrolysis gas, the combustible component separated from the pyrolysis residue, and the combustion air are supplied to the combustion melting furnace and burnt, and the combustion generated by this combustion The molten slag is melted to form molten slag, and this molten slag adheres to the inner wall of the combustion melting furnace and flows down, is discharged from the lower discharge port, is cooled and solidified, and high-temperature combustion gas is 2. Description of the Related Art A combustion melting furnace for a waste treatment apparatus is known that is cooled to form exhaust gas, and a part of the exhaust gas is supplied into the combustion melting furnace to control the temperature.
[0004]
[Problems to be solved by the invention]
By the way, in the combustion melting furnace of the waste treatment apparatus as described above, when performing maintenance, inspection, etc. of this combustion melting furnace, it is necessary to stop the operation. In this case, the molten slag is solidified in the vicinity of the slag discharge port. The slag outlet could be closed. That is, when the operation of the combustion melting furnace is stopped, first, the supply of the combustion melting furnace and the pyrolysis gas is stopped, and then the supply of combustion air is stopped. As a result, the temperature in the combustion melting furnace decreases due to natural cooling, but this temperature decrease is significant in the vicinity of the slag discharge port leading to the outside air. Therefore, the molten slag that adheres to the inner wall of the combustion melting furnace and flows down reaches the vicinity of the slag discharge port and is cooled and solidified. As a result, the slag discharge port is closed.
[0005]
When such a slag discharge port is closed, it is necessary to remove the solidified slag at the time of re-operation. As a result, not only the operation efficiency is lowered but also the combustion melting furnace may be damaged. There was a problem.
[0006]
[Means for Solving the Problems]
The present invention has been made to solve the conventional problems as described above, and heats and decomposes waste to produce pyrolysis gas and pyrolysis residue mainly composed of nonvolatile components. The slag is obtained by supplying the combustible component separated from the pyrolysis gas, the pyrolysis residue, and the combustion air to the combustion melting furnace and burning it, and melting the generated ash in the combustion melting furnace. at least the combustion melting adhere to the furnace inner wall is flow down, in a combustion melting furnace of the combustion melting furnace bottom of the waste was Unishi by Ru cooled and solidified was discharged from the slag discharge port processor, during shutdown of the combustion melting furnace in the furnace bottom of the furnace, at least one of a portion of a part of the exhaust gas or combustion air quenching the furnace bottom by supplying the molten slag to lower the flow so as to solidify on the inner wall surface of the combustion melting furnace It is characterized by that.
[0007]
Then, at least one part of the exhaust gas or part of the combustion air is supplied to the lower part of the combustion melting furnace, and when the operation of the combustion melting furnace is stopped, a part of the exhaust gas or one of the combustion air is supplied. It is preferable to take a method of supplying the part and quenching the lower part in the furnace.
[0008]
Further, it is preferable to provide a temperature detector at the lower part of the furnace and control the supply amount of a part of the exhaust gas or a part of the combustion air to the lower part of the furnace based on a signal from the temperature detector.
[0009]
Furthermore, an internal pressure detector is arranged in the combustion melting furnace, and a suction device arranged on the downstream side of the combustion melting furnace is controlled by a signal of this pressure detector, and the internal pressure of the combustion melting furnace is below a predetermined value, For example, it is controlled to be equal to or lower than atmospheric pressure. According to such a method, when the operation of the combustion melting furnace is stopped, the lower part is rapidly cooled, so the molten slag flowing down along the inner wall surface solidifies and adheres to the inner wall surface and reaches the vicinity of the slag discharge port. There is no. Therefore, closing of the slag discharge port can be prevented.
[0010]
As a quenching means for the lower part of the combustion melting furnace, a part of the exhaust gas used for temperature control in the combustion melting furnace is supplied to the lower part of the furnace, or is usually supplied to the lower part of the combustion melting furnace. By using the secondary and tertiary combustion air as the cooling medium, the lower part in the furnace can be rapidly cooled without providing a special cooling device.
[0011]
The molten slag is usually attached to the inner wall of the combustion melting furnace at about 1,300 ° C. and flows down. According to the knowledge of the present inventor, the molten slag has a large viscosity at about 1,200 ° C. , Solidify at about 100 ° C and stop flowing. Therefore, the rapid cooling of the lower part of the combustion melting furnace should be rapidly lowered to at least about 1,100 ° C. Therefore, the lower temperature in the combustion melting furnace is detected, and the supply amount of a part of exhaust gas or a part of combustion air as a cooling medium is controlled. And when temperature falls to the predetermined value of about 1,100 degreeC, supply of a part of exhaust gas or a part of combustion air will be stopped.
[0012]
On the other hand, the pressure in the furnace rises by supplying a part of the exhaust gas or a part of the combustion air to the lower part of the combustion melting furnace. When the pressure in the furnace rises, the remaining combustion gas etc. is released into the atmosphere from the slag discharge port etc., so the pressure in the combustion melting furnace is detected and the suction device is set so that this pressure is below atmospheric pressure To control.
[0013]
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, an embodiment of a method for preventing closure of a slag discharge port in a combustion melting furnace of a waste treatment apparatus according to the present invention will be described with reference to FIGS.
[0014]
FIG. 1 is a system diagram of the waste treatment apparatus 1. This waste treatment apparatus 1 is mainly composed of a pyrolysis reactor 2 and a combustion melting furnace 3. More specifically, the waste a is supplied into the pyrolysis reactor 2 by a screw feeder 6 having a charging unit 4 and a driving device 5. The pyrolysis reactor 3 is constituted by a horizontal rotary drum, for example, and a low oxygen atmosphere is formed inside by an induction blower 7 as a suction device. In the pyrolysis reactor 2, the heated air b heated by the high-temperature air heater 8 disposed on the rear side of the combustion melting furnace 3 is supplied from the line L 1 and discarded by indirect heating. The product is heated to 300 ° C. to 600 ° C., usually about 450 ° C. The waste a is pyrolyzed to produce pyrolysis gas G 1 and pyrolysis residue c. The pyrolysis gas G 1 and pyrolysis residue c are separated by the discharge device 9, and pyrolysis gas G 1 is supplied to the burner 10 of the combustion melting furnace 3 via the line L 2 , while the pyrolysis residue c is cooled by the cooling device 11 and then supplied to the separation device 12, where a combustible component mainly composed of carbon is used. It is separated into d and an incombustible component e such as rubble. The separated non combustible material e is recovered in the container 13, the combustion component d is a combustion melting furnace via a line L 3 having a control valve V 1 after being pulverized is supplied for example to 1mm or less in grinder 14 3 in the high temperature range of about 1,300 ° by the pyrolysis gas G 1 supplied from the line L 2 and the combustion air f supplied from the line L 4 by the forced blower 15. Burned. A line of combustion air f is supplied to the burner 10 by a primary air line L 41 having a control valve V 2, and a part thereof is provided at a lower portion through a secondary air line L 42 having a control valve V 3. The secondary air nozzle 16 is supplied to a tertiary air nozzle 17 via a tertiary air line L 43 having a control valve V 4, and so-called multi-combustion is performed in order to achieve low NOx. The combustion ash produced by such combustion and the ash contained in the combustible component become molten slag g and adhere to the inner wall of the combustion melting furnace 3 and flow down from the lower slag discharge port 18 into a water tank (not shown). On the other hand, the combustion gas G 2 is recovered by the high-temperature air heater 8 and then recovered by the waste heat boiler 19 through the line L 5 and is removed by the dust collector 20 and the gas cleaning device 21. And it is cleaned and becomes a relatively low temperature exhaust gas G 3 , a part is released from the chimney 22 to the atmosphere, and the other part is supplied by the forced blower 23 through the line L 6 as the cooling device 11 hanate gas. Further, another part of the exhaust gas G 3 is supplied to the combustion melting furnace 3 via the line L 7 by the forced air blower 24, and the temperature 25 of the combustion melting furnace 3 is controlled by an electric thermocouple. The temperature detector 25 is a pressure detector, and the temperature detector 25 and the pressure detector 26 are provided in the lower part of the combustion melting furnace 3, and their signals S 1 and S 2 are respectively controlled by a control device 27. Is input. The control device 27 includes a storage device 28, a comparator 29, an arithmetic device 30, and a signal creation device 31. Reference numeral 32 denotes a power generation device that generates electric power from the steam X generated in the waste heat boiler 19.
[0015]
In the embodiment of normal operation in the combustion melting furnace 3 in the waste treatment apparatus 1 having such a configuration, the control valves V 1 to V 4 and the pusher blower 24 are controlled by a control device (not shown), and the temperature in the combustion melting furnace 3 is about. The supply of the combustible component d, the pyrolysis gas G 1 or a part of the exhaust gas G 3 is controlled so as to be 1,300 ° C.
[0016]
When the operation of the pyrolysis residue 3 is stopped during such normal operation, the control valve V 1 is first controlled to stop the supply of the combustible component d and the pyrolysis gas G supplied from the line 2. By discharging 1 from a line (not shown), the supply to the combustion melting furnace 3 is stopped. Then, the signal S 1 of the temperature detector 25 is input to the comparator 29 of the control device 27, where it is compared with a predetermined value previously input to the storage device 28, for example, a signal S 3 having a temperature in the vicinity of 1,100 ° C. Then, the difference signal S 4 is input to the arithmetic unit 30. The proportional signal S 5 by the variable difference is input to the signal generating apparatus 31, where the control signal S 6 is applied to the forced draft fan 15 and the control valve V 2 ~V 4. More specifically, the control blower 15 is actuated by the control signal S 6 and at least the control valves V 3 and V 4 are opened, and the secondary air and the tertiary air that are part of the combustion air are provided below the combustion melting furnace 3. There is provided as a cooling medium, of course the case open primary air control valve V 2 optionally may be used as a cooling medium. In this case the detected pressure in the combustion melting furnace 3 by the pressure tester 26, a predetermined value is input in advance to the signal S 2 is comparator 29 is input to the same to and stored device 28, for example, the atmospheric pressure after being compared, the control signal S 7 via the operation unit 30 and the signal generating apparatus 31 is provided to attract the blower 7 as a suction device, is controlled so that at least a combustion pressure in the melting furnace 3 is less than atmospheric pressure.
[0017]
FIG. 2 shows another embodiment, in which the same reference numerals as those in FIG. 1 denote the same names. Line L 71 branch line L 7 are fed to the combustion melting furnace 3 a portion of the exhaust gas G 3 is provided in this embodiment, the other end of the line L 71 is connected to the lower portion of the combustion melting furnace 3 ing. Then, by supplying a control signal S 6 from the control device 27 to the pusher fan 24 and the control valves V 5 and V 6 , at least a part of the exhaust gas G 3 is supplied as a cooling medium to the lower part of the combustion melting furnace 3. The rapid cooling can be performed so that the rapid cooling rate is 50 to 500 ° C./min. According to the knowledge of the present inventor, as shown in FIG. 3, the flow rate of the molten slag g is 1 to 5 m / min when the temperature is 1,300 ° C., but the velocity decreases as the temperature decreases. It was found that when the temperature was around 1,100 ° C., it solidified and did not flow down. In order to reduce the temperature in the combustion melting furnace 3 to about 1,100 ° C. by natural cooling, about 0.1 to 0.5 H is required. The slag g almost reaches the vicinity of the slag discharge 18 and is cooled and solidified. As described above, the molten slag g is solidified on the inner wall of the combustion melting furnace 3 by rapidly cooling to the temperature at which the molten slag g solidifies. As a result, it is possible to prevent the slag discharge port 18 from being closed.
[0018]
In the above embodiment, a case where a part of the combustion air is separately supplied to the lower part of the combustion melting furnace 3 has been described. However, these may be supplied together.
[0019]
【The invention's effect】
As is clear from the above description, according to the method for preventing closure of the slag discharge port in the combustion melting furnace of the waste treatment apparatus according to the present invention, the lower part of the combustion melting furnace is rapidly cooled when the combustion melting furnace is stopped. As a result, the molten slag adhering to the inner wall surface and flowing down is cooled and solidified, and as a result, the slag discharge port can be prevented from closing.
[0020]
Furthermore, by using a part of the exhaust gas or a part of the combustion air as the cooling medium, there is an effect that it is possible to prevent the slag discharge port from being closed without providing a special device.
[Brief description of the drawings]
FIG. 1 is a system diagram for implementing a method for preventing closure of a slag discharge port in a combustion melting furnace of a waste treatment apparatus according to the present invention.
FIG. 2 is a system diagram showing another embodiment of a method for preventing closure of a slag discharge port in a combustion melting furnace of a waste treatment apparatus according to the present invention.
FIG. 3 is a graph showing the relationship between the flow rate of molten slag and the temperature.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 Waste disposal apparatus 2 Pyrolysis reactor 3 Combustion melting furnace 4 Input part 5 Start-up apparatus 6 Screw feeder 7 Induction fan 8 High temperature air heater 9 Discharge apparatus 10 Burner 11 Cooling apparatus 12 Separation apparatus 13 Container 14 Crushers 15, 23 24 Air blower 16 Secondary air nozzle 17 Tertiary air nozzle 18 Slag outlet 19 Waste heat boiler 20 Dust collector 21 Gas scrubber 22 Chimney 25 Temperature detector 26 Pressure detector 27 Controller 28 Storage device 29 Comparator 30 Arithmetic unit 31 Signal generator 32 Power generator

Claims (5)

廃棄物を加熱して熱分解し、熱分解ガスと主として不揮発性成分からなる熱分解残留物とを生成し、前記熱分解ガスと前記熱分解残留物から分離された燃焼性成分と燃焼用空気とを燃焼溶融炉に供給して燃焼させ、生じた灰分を燃焼溶融炉内で溶融してなる溶融スラグを内壁に付着させて流下させ、燃焼溶融炉下部のスラグ排出口から排出して冷却固化させるようにした廃棄物処理装置の燃焼溶融炉において、燃焼溶融炉の運転停止時に少なくとも燃焼溶融炉の炉内下部に、排ガスの一部または燃焼用空気の一部の少なくとも一方を供給して炉内下部を急冷して、流下する溶融スラグを燃焼溶融炉の内壁面上で固化させるようにしたことを特徴とする廃棄物処理装置の燃焼溶融炉におけるスラグ排出口の閉鎖防止方法。Waste is heated and pyrolyzed to produce pyrolysis gas and pyrolysis residue mainly composed of non-volatile components. Combustion components and combustion air separated from the pyrolysis gas and pyrolysis residue preparative burned by supplying the combustion melting furnace, resulting ash was flow down the molten slag by melt adhered to the furnace inner wall in the combustion melting furnace, cooled and discharged from the combustion melting furnace bottom of the slag discharge port supply in a combustion melting furnace by Ru solidified was Unishi waste treatment apparatus, in the furnace bottom of at least the combustion melting furnace during operation stop of the combustion melting furnace, a portion of at least one of a portion of the exhaust gas or combustion air by quenching the lower furnace and waste disposal closure method for preventing slag discharge port in the combustion melting furnace of the apparatus, characterized in that the molten slag to lower flow and to solidify on an inner wall surface of the combustion melting furnace . 燃焼溶融炉の下部に温度検出器を配置するとともに制御装置を設け該温度検出器の信号を前記制御装置に入力し、該制御装置により作成された制御信号により排ガスの一部または燃焼用空気の一部の供給量を制御するようにしてなる請求項1に記載の廃棄物処理装置の燃焼溶融炉におけるスラグ排出口の閉鎖防止方法。A temperature detector is arranged at the bottom of the combustion melting furnace and a control device is provided, and a signal from the temperature detector is input to the control device, and a part of the exhaust gas or combustion air is detected by the control signal generated by the control device. The method for preventing closure of a slag discharge port in a combustion melting furnace of a waste disposal apparatus according to claim 1, wherein a part of the supply amount is controlled. 燃焼溶融炉の後流側に排ガスの吸引装置を設けるとともに該燃焼溶融炉内に圧力検知器を設け該圧力検知器の信号を制御装置に入力し、該制御装置により作成された制御信号により前記吸引装置を制御して、燃焼溶融炉内の圧力を所定値以下に保持することを特徴とする請求項1に記載の廃棄物処理装置の燃焼溶融炉におけるスラグ排出口の閉鎖防止方法。An exhaust gas suction device is provided on the downstream side of the combustion melting furnace, a pressure detector is provided in the combustion melting furnace, a signal of the pressure detector is input to the control device, and the control signal generated by the control device by controlling the suction device, the closing method for preventing slag discharge port in the combustion melting furnace waste disposal apparatus according to claim 1 you wherein the Turkey to retain the pressure in the combustion melting furnace to a predetermined value or less . 燃焼溶融炉の下部温度が1,100℃以下となるよう急冷するようにした請求項1乃至のいずれかに記載の廃棄物処理装置の燃焼溶融炉におけるスラグ排出口の閉鎖防止方法。The method for preventing closure of a slag discharge port in a combustion melting furnace of a waste treatment apparatus according to any one of claims 1 to 3 , wherein the lower temperature of the combustion melting furnace is rapidly cooled so as to be 1,100 ° C or lower. 急冷速度が50〜500℃/minとなるよう急冷するようにした請求項1または4に記載の廃棄物処理装置の燃焼溶融炉におけるスラグ排出口の閉鎖防止方法。The method for preventing closure of a slag discharge port in a combustion melting furnace of a waste treatment apparatus according to claim 1 or 4 , wherein the rapid cooling is performed so that the rapid cooling rate is 50 to 500 ° C / min.
JP25308997A 1997-09-18 1997-09-18 Method for preventing closure of slag outlet in combustion melting furnace of waste treatment equipment Expired - Fee Related JP3893200B2 (en)

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