JP2006297332A - Collected ash heating device for waste gasifying/melting equipment - Google Patents

Collected ash heating device for waste gasifying/melting equipment

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JP2006297332A
JP2006297332A JP2005125822A JP2005125822A JP2006297332A JP 2006297332 A JP2006297332 A JP 2006297332A JP 2005125822 A JP2005125822 A JP 2005125822A JP 2005125822 A JP2005125822 A JP 2005125822A JP 2006297332 A JP2006297332 A JP 2006297332A
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ash
heating
dust
waste
dust ash
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JP4663389B2 (en
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Mitsumasa Todaka
光正 戸高
Mitsuharu Hirano
満春 平野
Toru Kinukawa
徹 絹川
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Nippon Steel Engineering Co Ltd
Nippon Steel Plant Designing Corp
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Nittetsu Plant Designing Corp
Nippon Steel Engineering Co Ltd
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a collected ash heating device for waste gasifying/melting equipment capable of uniformly heating collected ash in the waste gasifying/melting equipment for gasifying and melting waste at a prescribed temperature. <P>SOLUTION: The collected ash heating device heats the collected ash in the waste gasifying/melting equipment for gasifying and melting the waste, and an ash discharging device provided with a rotary scraper 4 is disposed in a combustion chamber for heating the collected ash. <P>COPYRIGHT: (C)2007,JPO&INPIT

Description

本発明は、廃棄物ガス化溶融処理設備における集じん灰からダイオキシンを除去する集じん灰加熱装置に関する。   The present invention relates to a dust ash heating apparatus that removes dioxins from dust ash in a waste gasification and melting treatment facility.

廃棄物ガス化溶融処理設備における集じん灰加熱装置に関しては従来から種々の提案がなされている。
例えば、特開2002−147739号公報では、ガス化溶融炉から発生した灰を含む可燃ガスを燃焼室に送って燃焼させ、燃焼室で底部に落下した灰は灰出しコンベアで排出する方法が提案されている。
しかし、特開2002−147739号公報に記載された方法では、集じん灰中のダイオキシンは、燃焼ガス中に揮散し分解されるので、特別な分解装置は不要であるが、灰出しコンベアの上の灰は燃焼ガスにより表層のみが加熱され一様な加熱が困難であり、かつ、加熱温度のコントロールが困難なので灰の加熱不足や、過熱による溶融が発生する恐れがあった。
Various proposals have been made regarding dust ash heating devices in waste gasification and melting treatment facilities.
For example, Japanese Patent Laid-Open No. 2002-147739 proposes a method in which combustible gas containing ash generated from a gasification melting furnace is sent to a combustion chamber for combustion, and the ash that has fallen to the bottom in the combustion chamber is discharged by an ash removal conveyor. Has been.
However, in the method described in Japanese Patent Application Laid-Open No. 2002-147739, the dioxins in the dust collection ash are volatilized and decomposed in the combustion gas. In the ash, only the surface layer is heated by the combustion gas and uniform heating is difficult, and since it is difficult to control the heating temperature, there is a possibility that the ash is insufficiently heated or melted due to overheating.

また、特開2003−221111号公報には、スクリューコンベヤを電磁誘導加熱することによって飛灰等に含まれるダイオキシンを連続処理によって効率的で均一に揮発分離する装置が提案されている。
しかし、特開2003−221111号公報に記載された装置は誘導加熱による局所的な加熱方式であるため、スクリューコンベヤ内の灰は表層のみが加熱され一様な加熱が困難であり、かつ、加熱温度のコントロールが困難なので灰の加熱不足や、過熱による溶融が発生する恐れがあった。
特開2002−147739号公報 特開2003−221111号公報
Japanese Patent Laid-Open No. 2003-221111 proposes an apparatus that efficiently and uniformly volatilizes and separates dioxins contained in fly ash and the like by continuous treatment by electromagnetic induction heating of a screw conveyor.
However, since the apparatus described in Japanese Patent Application Laid-Open No. 2003-221111 is a local heating method by induction heating, only the surface layer of the ash in the screw conveyor is heated, and uniform heating is difficult. Since it was difficult to control the temperature, there was a risk that the ash was insufficiently heated or melted due to overheating.
JP 2002-147739 A JP 2003-221111 A

本発明は、前述のような従来技術の問題点を解決し、廃棄物をガス化溶融処理する廃棄物ガス化溶融処理設備における集じん灰を所定の温度で均一に加熱処理することができる廃棄物ガス化溶融処理設備の集じん灰加熱装置を提供することを課題とする。   DISCLOSURE OF THE INVENTION The present invention solves the problems of the prior art as described above, and is capable of uniformly heat-treating dust collection ash in a waste gasification and melting treatment facility for gasifying and melting waste at a predetermined temperature. It is an object of the present invention to provide a dust ash heating device for a product gasification and melting treatment facility.

本発明は、前述の課題を解決するため鋭意検討の結果なされたものであり、その要旨とするところは特許請求の範囲に記載した通りの下記内容である。
(1)廃棄物をガス化溶融処理する廃棄物ガス化溶融処理設備における集じん灰を加熱処理する集じん灰加熱装置であって、
前記集じん灰を加熱する燃焼室に、回転スクレーパーを有する灰出し装置を配設することを特徴とする廃棄物ガス化溶融処理設備の集じん灰加熱装置。
(2)前記燃焼室の側壁に、前記回転スクレーパーの回転により外周部に移動した集じん灰を中心側に移動させる側壁突起を有することを特徴とする(1)に記載の廃棄物ガス化溶融処理設備の集じん灰加熱装置。
(3)前記回転スクレーパーの直上に、耐火物からなるリング状突起を設けることにより、燃焼ガスからの直接輻射熱を避け、該耐火物からの固体輻射により集じん灰を加熱することを特徴とする(1)または(2)に記載の廃棄物ガス化溶融処理設備の集じん灰加熱装置。
(4)前記耐火物の炉内表面を冷却する冷却ガスの吹き込み口を有することを特徴とする(1)乃至(3)のいずれかに記載の廃棄物ガス化溶融処理設備の集じん灰加熱装置。
The present invention has been made as a result of intensive studies in order to solve the above-mentioned problems, and the gist of the present invention is the following contents as described in the claims.
(1) A dust ash heating apparatus for heating dust ash in a waste gasification and melting treatment facility for gasifying and melting waste,
A dust ash heating device for a waste gasification and melting treatment facility, wherein an ash removal device having a rotary scraper is disposed in a combustion chamber for heating the dust ash.
(2) The waste gasification and melting according to (1), wherein the combustion chamber has side wall protrusions that move dust collection ash that has moved to the outer peripheral portion by rotation of the rotary scraper to the center side on the side wall of the combustion chamber. Dust ash heating device for processing equipment.
(3) A ring-shaped protrusion made of a refractory material is provided immediately above the rotating scraper, so that direct radiant heat from the combustion gas is avoided and the dust ash is heated by solid radiation from the refractory material. The dust ash heating device of the waste gasification melting treatment facility according to (1) or (2).
(4) The dust ash heating of the waste gasification and melting treatment facility according to any one of (1) to (3), wherein the refractory material has a cooling gas blowing port for cooling a furnace inner surface. apparatus.

本発明によれば、廃棄物をガス化溶融処理する廃棄物ガス化溶融処理設備における集じん灰を所定の温度で均一に加熱処理することができる廃棄物ガス化溶融処理設備の集じん灰加熱装置を提供することがことができ、具体的には以下のような産業上有用な著しい効果を奏する。
1)集じん灰の燃焼室に回転スクレーパーおよび側壁突起を設けて加熱面積を広くし集じん灰を攪拌することにより均一な温度に効率良く加熱することができる。
2)集じん灰の加熱処理を燃焼室の灰出し部に設けたことにより、加熱源が不要で、かつ、熱処理により揮散したダイオキシンは燃焼室の高温ガスにより分解されるためダイオキシンの分解装置は不要である。
3)加熱方式を耐火物からの固体輻射方式としたことにより、加熱温度が著しく安定し、かつ、加熱体と灰との接触がないため灰の溶融付着の問題がない。
ADVANTAGE OF THE INVENTION According to this invention, the dust ash heating of the waste gasification melting processing equipment which can heat-process the dust ash in the waste gasification melting processing equipment which gasifies and melts waste at a predetermined temperature uniformly An apparatus can be provided, and specifically, the following industrially useful remarkable effects are produced.
1) A rotating scraper and side wall protrusions are provided in the dust ash combustion chamber to widen the heating area and agitate the dust ash to efficiently heat to a uniform temperature.
2) Since the heat treatment of dust collection ash is provided in the ash extraction part of the combustion chamber, a heating source is unnecessary, and dioxins volatilized by the heat treatment are decomposed by the high-temperature gas in the combustion chamber. It is unnecessary.
3) Since the heating method is a solid radiation method from a refractory, the heating temperature is remarkably stabilized, and there is no contact between the heating body and the ash, so there is no problem of ash melt adhesion.

本発明を実施するための最良の形態について、図1乃至図4をいて詳細に説明する。
図1は、燃焼室下部に設けられた本発明の灰加熱装置の縦断面図である。
図2は、図1に示すA−Aの水平断面図である。
図3は、図1に示すB−Bの水平断面図である。
図4は、図1に示す加熱室の詳細図である。
図1乃至図4において、1はバーナ、2は側壁、2´はリング状耐火物、3は断熱耐火物、4は回転スクレーパー、4´はかき羽根、5は回転駆動装置、6は加熱室、7は側壁突起、8は集じん灰供給コンベア、9は冷却ガス吹き込み口、10は排出口、11は温度計、14はコーン部を示す。
The best mode for carrying out the present invention will be described in detail with reference to FIGS.
FIG. 1 is a longitudinal sectional view of the ash heating apparatus of the present invention provided at the lower part of the combustion chamber.
FIG. 2 is a horizontal sectional view taken along line AA shown in FIG.
FIG. 3 is a horizontal sectional view taken along line BB shown in FIG.
FIG. 4 is a detailed view of the heating chamber shown in FIG.
1 to 4, 1 is a burner, 2 is a side wall, 2 'is a ring refractory material, 3 is a heat insulating refractory material, 4 is a rotating scraper, 4' is a shaving blade, 5 is a rotary drive device, and 6 is a heating chamber. , 7 are side wall protrusions, 8 is a dust collecting ash supply conveyor, 9 is a cooling gas blow-in port, 10 is a discharge port, 11 is a thermometer, and 14 is a cone part.

従来、廃棄物をガス化溶融処理する廃棄物ガス化溶融処理設備における集じん灰の灰出しコンベアとしてスクリューコンベア方式が一般的であり、この方式では加熱面が狭く、かつ、表層のみの加熱となり、一様に加熱ができないという問題点があった。
そこで、本発明においては、加熱面積が広くとれる回転スクレーパー方式とし、外壁の1ケ所から装入された集じん灰はほぼ一周回転する間に加熱され、底部の排出穴10より排出される。
すなわち、本発明は、廃棄物をガス化溶融処理する廃棄物ガス化溶融処理設備における集じん灰を加熱処理する集じん灰加熱装置であって、前記集じん灰を加熱する燃焼室6に、回転スクレーパー4を有する灰出し装置を配設することを特徴とする。
Conventionally, a screw conveyor system is generally used as a dust ash ash removal conveyor in waste gasification and melting processing equipment that gasifies and melts waste. In this method, the heating surface is narrow and only the surface layer is heated. There was a problem that heating could not be performed uniformly.
Therefore, in the present invention, a rotary scraper system is adopted that can take a wide heating area, and the dust ash charged from one place on the outer wall is heated while rotating almost once and discharged from the discharge hole 10 at the bottom.
That is, the present invention is a dust collection ash heating device for heat treating dust collection ash in a waste gasification melting treatment facility for gasifying and melting waste, and in the combustion chamber 6 for heating the dust collection ash, An ashing device having a rotating scraper 4 is provided.

回転スクレーパー4には、図2に示すように放射状に多数のかき羽根4´が設けられており、集じん灰は、かき羽根4´に押されて回転方向に移動するとともに回転により外周側にも移動する。外周に移動した集じん灰は、図4に示すように、周囲の外周壁に設けられる側壁突起7により中心側に押し戻される。これを回転中に繰り返すことにより灰の攪拌が行われ一様な加熱が可能となる。
また、加熱手段として温度変動の激しい高温の炉内ガスからの直接輻射でなく炉内ガスにより回転スクレーパー直上に設けたリング状耐火物突起2´を加熱し、この耐火物突起2´からの固体輻射により加熱する方式とすることにより、安定した加熱を実現することができる。
具体的には、図1に示すように、燃焼室6の下部に回転スクレーパー4を設け、これに多数のかき羽根4´を接続している。
燃焼室6の側面の一ヶ所より、集じん灰供給コンベア8から集じん灰を供給し、かき板4´により、灰は周方向に移動し、ほぼ1周回転した後、排出口10より炉外へ排出される。
As shown in FIG. 2, the rotary scraper 4 is provided with a large number of radial shaving blades 4 '. The dust collecting ash is pushed by the shaving blades 4' to move in the rotational direction and rotates to the outer peripheral side. Also move. As shown in FIG. 4, the dust ash that has moved to the outer periphery is pushed back toward the center by the side wall projection 7 provided on the outer peripheral wall. By repeating this during rotation, the ash is stirred and uniform heating becomes possible.
Further, as a heating means, the ring-shaped refractory protrusion 2 'provided immediately above the rotating scraper is heated by the furnace gas, not directly from the high-temperature furnace gas having a large temperature fluctuation, and the solid from the refractory protrusion 2' is heated. By adopting a method of heating by radiation, stable heating can be realized.
Specifically, as shown in FIG. 1, a rotary scraper 4 is provided at the lower part of the combustion chamber 6, and a large number of shaving blades 4 'are connected thereto.
Dust ash is supplied from a dust ash supply conveyor 8 from one side of the combustion chamber 6, and the ash is moved in the circumferential direction by the scraper 4 ′ and rotated almost once. It is discharged outside.

また、集じん灰は回転により周方向移動だけでなく、外周部への移動も伴うが、外周部に移動した灰は、4図の矢印で示すように側壁突起7により中心側に押し戻される。この動作を1回転中に繰り返すことにより灰の攪拌が行われ一様な加熱が可能となる。
一方、加熱方法に関しては、燃焼バーナー1からの燃焼ガスは約1000〜1100℃程度であり、燃焼室下部側壁2及びリング状耐火物突起2´をガス輻射および伝熱により加熱し、加熱室6を加熱する固体輻射源として作用する。
この場合、2,2´は輻射率が高く、かつ、熱伝導率の高い炭化珪素質の耐火物が好ましい。
また、加熱室6の温度を適正な温度(400〜500℃)に保つため、図3に示すように、燃焼室6の下部に炉内旋回流を形成し、耐火物表面を冷却する冷却ガスを冷却ガス吹き込み口9より流し、この風量を例えば図1に示すTICにより制御して側壁耐火物2、2´の温度を一定にすることで温度計11にて計測する加熱室6の温度を400〜500℃の間の適正な温度に維持することができる。
なお、燃焼室6の底部における集じん灰の層厚および加熱時間は回転駆動装置5の回転数を変化させることにより自由にコントロールすることができる。
The dust ash is not only moved in the circumferential direction by rotation but also moved to the outer peripheral portion, but the ash that has moved to the outer peripheral portion is pushed back to the center side by the side wall projection 7 as shown by the arrow in FIG. By repeating this operation during one rotation, the ash is stirred and uniform heating becomes possible.
On the other hand, regarding the heating method, the combustion gas from the combustion burner 1 is about 1000 to 1100 ° C., the combustion chamber lower side wall 2 and the ring-shaped refractory projection 2 ′ are heated by gas radiation and heat transfer, and the heating chamber 6 is heated. It acts as a solid radiation source for heating.
In this case, silicon carbide refractories having a high emissivity and a high thermal conductivity are preferable for 2,2 ′.
Further, in order to keep the temperature of the heating chamber 6 at an appropriate temperature (400 to 500 ° C.), as shown in FIG. 3, a cooling gas that forms a swirling flow in the furnace at the lower portion of the combustion chamber 6 and cools the refractory surface. Is supplied from the cooling gas inlet 9, and the temperature of the heating chamber 6 measured by the thermometer 11 is controlled by controlling the air volume by, for example, the TIC shown in FIG. It can be maintained at an appropriate temperature between 400-500 ° C.
Note that the layer thickness and heating time of the dust ash at the bottom of the combustion chamber 6 can be freely controlled by changing the rotational speed of the rotary drive device 5.

燃焼室下部に設けられた本発明の灰加熱装置の縦断面図である。It is a longitudinal cross-sectional view of the ash heating apparatus of this invention provided in the combustion chamber lower part. 図1に示すA−Aの水平断面図である。It is a horizontal sectional view of AA shown in FIG. 図1に示すB−Bの水平断面図である。It is a horizontal sectional view of BB shown in FIG. 図1に示す加熱室の詳細図である。It is detail drawing of the heating chamber shown in FIG.

符号の説明Explanation of symbols

1 バーナ
2 側壁
2´リング状耐火物
3 断熱耐火物
4 回転スクレーパー
4´かき羽根
5 回転駆動装置
6 加熱室
7 側壁突起
8 集じん灰供給コンベア
9 冷却ガス吹き込み口
10 排出口
11 温度計
14 コーン部
DESCRIPTION OF SYMBOLS 1 Burner 2 Side wall 2 'ring-shaped refractory material 3 Thermal insulation refractory material 4 Rotating scraper 4' Shaving blade 5 Rotating drive device 6 Heating chamber 7 Side wall protrusion 8 Dust collection ash supply conveyor 9 Cooling gas inlet 10 Exhaust port 11 Thermometer 14 Cone Part

Claims (4)

廃棄物をガス化溶融処理する廃棄物ガス化溶融処理設備における集じん灰を加熱処理する集じん灰加熱装置であって、
前記集じん灰を加熱する燃焼室に、回転スクレーパーを有する灰出し装置を配設することを特徴とする廃棄物ガス化溶融処理設備の集じん灰加熱装置。
A dust ash heating device for heat treating dust ash in a waste gasification and melting treatment facility for gasifying and melting waste,
A dust ash heating device for a waste gasification and melting treatment facility, wherein an ash removal device having a rotary scraper is disposed in a combustion chamber for heating the dust ash.
前記燃焼室の側壁に、前記回転スクレーパーの回転により外周部に移動した集じん灰を中心側に移動させる側壁突起を有することを特徴とする請求項1に記載の廃棄物ガス化溶融処理設備の集じん灰加熱装置。   2. The waste gasification and melting treatment facility according to claim 1, wherein the combustion chamber has a side wall protrusion that moves dust collection ash that has moved to the outer peripheral portion due to rotation of the rotary scraper to the center side on the side wall of the combustion chamber. Dust ash heating device. 前記回転スクレーパーの直上に、耐火物からなるリング状突起を設けることにより、燃焼ガスからの直接輻射熱を避け、該耐火物からの固体輻射により集じん灰を加熱することを特徴とする請求項1または請求項2に記載の廃棄物ガス化溶融処理設備の集じん灰加熱装置。   2. A ring-shaped protrusion made of a refractory material is provided immediately above the rotary scraper to avoid direct radiant heat from the combustion gas, and the dust ash is heated by solid radiation from the refractory material. Or the dust ash heating apparatus of the waste gasification fusion processing equipment of Claim 2. 前記耐火物の炉内表面を冷却する冷却ガスの吹き込み口を有することを特徴とする請求項1乃至請求項3のいずれかに記載の廃棄物ガス化溶融処理設備の集じん灰加熱装置。
The dust ash heating apparatus for a waste gasification and melting treatment facility according to any one of claims 1 to 3, further comprising a cooling gas blowing port for cooling a furnace inner surface of the refractory.
JP2005125822A 2005-04-25 2005-04-25 Waste ash heating system for waste gasification and melting equipment Expired - Fee Related JP4663389B2 (en)

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CN111219715A (en) * 2020-03-10 2020-06-02 张付良 Municipal refuse pyrolysis gasification treatment equipment

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CN108679619A (en) * 2018-06-13 2018-10-19 黄林 A kind of deslagging processing unit of environment-protecting garbage incinerating stove
CN111219715A (en) * 2020-03-10 2020-06-02 张付良 Municipal refuse pyrolysis gasification treatment equipment

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