JP2008256283A - Vertical reduction melting furnace - Google Patents

Vertical reduction melting furnace Download PDF

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JP2008256283A
JP2008256283A JP2007099578A JP2007099578A JP2008256283A JP 2008256283 A JP2008256283 A JP 2008256283A JP 2007099578 A JP2007099578 A JP 2007099578A JP 2007099578 A JP2007099578 A JP 2007099578A JP 2008256283 A JP2008256283 A JP 2008256283A
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furnace
recovery pipe
gas
gas recovery
upper connecting
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Shoichi Kume
正一 久米
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Kangen Yoyu Gijutsu Kenkyusho KK
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Kangen Yoyu Gijutsu Kenkyusho KK
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<P>PROBLEM TO BE SOLVED: To provide a vertical reduction melting furnace capable of effectively preventing damage of an inner surface furnace material constituting a connection part of a gas recovery pipe recovering high temperature gas at a temperature of 800°C or more by optimizing an upper connection part of the gas recovery pipe disposed on a side part of a furnace lower part side of a furnace body. <P>SOLUTION: The vertical reduction melting furnace is provided with the furnace body 2 and the gas recovery pipe 3, wherein the gas recovery pipe 3 is extended upward so that an angle of the upper connecting part 10 formed by an upper inner wall surface 8 and an upper inner wall surface 9 of a furnace body side part 2a is a small angle α smaller than 90° when viewed on the cross section including both of a longitudinal center axis of the furnace body 2 and an extension direction center axis of the gas recovery pipe, and chamfering with a prescribed radius of curvature R is applied to the upper connecting part 10, and a thickness of an end of the upper connection part 10 is thick enough to withstand thermal impact in the furnace. <P>COPYRIGHT: (C)2009,JPO&INPIT

Description

本発明は、一般廃棄物や産業廃棄物等の被処理物を投入し、投入した前記被処理物を溶融するための円筒状の炉体と、該炉体内に投入された前記被処理物が堆積する堆積物の表面位置よりも下部であってかつ炉底側に設けた羽口よりも高い炉体側部に設けた円筒状のガス排出孔に連結され、前記被処理物の溶融時に発生する燃焼ガスや排ガス等の炉内ガスを800℃以上の高温ガスとして回収するためのガス回収管とを有する縦型還元溶融炉に関するものである。   The present invention includes a cylindrical furnace body for charging a processed object such as general waste or industrial waste, and melting the input processed object, and the processed object input into the furnace body. It is connected to a cylindrical gas discharge hole provided on the side of the furnace body lower than the surface position of the deposit to be deposited and higher than the tuyere provided on the furnace bottom side, and is generated when the workpiece is melted. The present invention relates to a vertical reduction melting furnace having a gas recovery pipe for recovering in-furnace gas such as combustion gas and exhaust gas as a high-temperature gas at 800 ° C. or higher.

近年、いわゆる都市ごみと呼ばれる一般廃棄物や、産業廃棄物等(以下、単に「廃棄物」という。)の排出量が増大し、この廃棄物の殆どが焼却処理により減量化され焼却灰もしくは不燃物として最終処分場に埋め立てられている。しかし、前記廃棄物の排出量の増加は、廃棄物の焼却残渣等の最終処分場不足の問題に発展している。   In recent years, so-called municipal waste, general waste, industrial waste, etc. (hereinafter simply referred to as “waste”) has increased in volume, and most of this waste has been reduced by incineration, resulting in incineration ash or incombustibility. It is landfilled at the final disposal site. However, the increase in the amount of waste discharged has developed into a problem of shortage of final disposal sites such as waste incineration residues.

この問題に有効に対処する手段を開発したものとしては、例えば出願人が提案した特許文献1記載の還元溶融炉が挙げられる。
特開2004−132655号公報
An example of a means for effectively dealing with this problem is a reduction melting furnace described in Patent Document 1 proposed by the applicant.
JP 2004-132655 A

特許文献1記載の還元溶融炉は、廃棄物等の被処理物および副原料としてコークスおよび石灰石が装入口から装入され、装入された被処理物およびコークス等は炉内で堆積して充填層を形成し、上段羽口、中段羽口および下段羽口から空気が供給され廃棄物の可燃物およびコークスが還元燃焼する。この燃焼気体は溶融炉内を炉下部から上昇し、廃棄物を予熱、乾燥、熱分解する。このようにして装入口から投入された廃棄物および副原料、コークスおよび石灰石は投入ダンパー仕切弁を通り充填層、溶融滴下帯および溶融帯に至るまでに水分は水蒸気となり燃焼成分は熱分解され、また固形物は溶融される。熱分解残渣はスラグ排出孔より外部に取り出される。なお、前記被処理物の溶融時に発生する燃焼ガスや排ガス等の800℃以上の高温炉内ガスは、ガス回収管の内部を通って後処理工程に送られ、熱エネルギーやガス資源等として利用することができる。   In the reduction melting furnace described in Patent Document 1, coke and limestone are charged from the charging port as an object such as waste and auxiliary materials, and the charged object and coke are deposited and filled in the furnace. A layer is formed, and air is supplied from the upper tuyeres, the middle tuyeres and the lower tuyere, and the combustible waste and coke are reduced and burned. This combustion gas rises in the melting furnace from the lower part of the furnace and preheats, dries, and thermally decomposes the waste. In this way, the waste and auxiliary materials, coke, and limestone charged from the charging port pass through the charging damper gate valve, the moisture becomes steam, and the combustion components are pyrolyzed until reaching the packed bed, molten dripping zone and melting zone, The solid is melted. Thermal decomposition residue is taken out from the slag discharge hole. Note that high-temperature furnace gas of 800 ° C or higher, such as combustion gas and exhaust gas generated when the workpiece is melted, is sent to the post-treatment process through the inside of the gas recovery pipe and used as thermal energy, gas resources, etc. can do.

しかし、特許文献1記載の還元溶融炉は、800℃以上の高温ガスとして回収するため、炉体に対するガス回収管の連結位置が、従来の溶融炉のガス回収管の位置に比べて炉体の炉下部側にあり、具体的には、高温側下側被処理物が炉内に投入されて堆積した充填層の高位レベル(堆積物の表面位置レベル)よりも3m以上低い位置にあり、この連結位置の側壁内面は、直接高温(800〜2000℃程度)にさらされる。 However, since the reduction melting furnace described in Patent Document 1 collects as a high-temperature gas of 800 ° C. or higher, the connection position of the gas recovery pipe to the furnace body is higher than that of the gas recovery pipe of the conventional melting furnace. It is located on the lower part of the furnace. Specifically, it is at a position that is 3 m or more lower than the high level (the surface position level of the deposit) of the packed bed in which the high-temperature-side workpiece is put in the furnace and deposited. The inner surface of the side wall at the connection position is directly exposed to a high temperature (about 800 to 2000 ° C.).

しかも、特許文献1記載の溶融炉の前記ガス回収管は、炉内温度が高温である炉体の炉下部の側壁に連結され、かつ、炉内に投入した廃棄物等の投入物がガス回収管内に侵入し、処理できない廃棄物がガス回収管内に滞留するとともに、クリーンなガスが回収できなくなるのを回避する点で、上方に延びるように配置されるため、ガス回収管の上側内壁面と、炉体側部の上側内壁面とで形成される上側連結部が90°未満の鋭角部となって炉壁厚さが薄くなっており、このような場合には、炉壁厚さが薄くなった連結部の炉壁の内面と外面とに大きな温度差が生じ、これに伴って、ガス回収管の連結部を構成する内面炉材が熱衝撃によって損傷を受け脱落する場合があり、この場合、補修を頻繁に行わなければならないという問題があった。 In addition, the gas recovery pipe of the melting furnace described in Patent Document 1 is connected to the side wall of the furnace lower part of the furnace body having a high furnace temperature, and the input material such as waste that has been input into the furnace is gas recovered. In order to avoid waste that has entered the pipe and cannot be treated and stays in the gas recovery pipe and prevents the clean gas from being recovered, the upper inner wall surface of the gas recovery pipe The upper connecting portion formed by the upper inner wall surface of the furnace body side portion is an acute angle portion of less than 90 ° and the furnace wall thickness is reduced. In such a case, the furnace wall thickness is reduced. A large temperature difference occurs between the inner and outer surfaces of the furnace wall of the connected part, and along with this, the inner furnace material constituting the connecting part of the gas recovery pipe may be damaged by the thermal shock and fall off. There was a problem that repairs had to be performed frequently.

本発明の目的は、炉体の炉下部側の側部に設けたガス回収管の上側連結部の適正化を図ることにより、800℃以上の高温ガスの回収するガス回収管の連結部を構成する内面炉材の損傷を有効に防止した縦型還元溶融炉を提供する。 An object of the present invention is to configure a gas recovery pipe connecting part for recovering high-temperature gas of 800 ° C. or higher by optimizing the upper connecting part of the gas recovery pipe provided on the side of the furnace lower part of the furnace body. Provided is a vertical reduction melting furnace that effectively prevents damage to the inner surface furnace material.

上記目的を達成するため、この発明の要旨構成は以下の通りである。
(1)一般廃棄物や産業廃棄物等の被処理物を投入し、投入した前記被処理物を溶融するための円筒状の炉体と、該炉体内に投入された前記被処理物が堆積する堆積物の表面位置よりも下部であってかつ炉底側に設けた羽口よりも高い炉体側部に設けた円筒状のガス排出孔に連結され、前記被処理物の溶融時に発生する燃焼ガスや排ガス等の炉内ガスを800℃以上の高温ガスとして回収するためのガス回収管とを有し、前記炉体の長手方向中心軸線と前記ガス回収管の延在方向中心軸線の双方を含む断面で見て、前記ガス回収管は、その上側内壁面と、該上側内壁面と連結される炉体側部の上側内壁面とで形成される上側連結部のなす角度が90°未満の小さな角度となるように上方に向かって延び、かつ、上側連結部に、所定の曲率半径で丸くした面取りを施して、前記上側連結部の先端厚みを、炉内の熱衝撃に耐えうる厚さにすることを特徴とする縦型還元溶融炉。
In order to achieve the above object, the gist of the present invention is as follows.
(1) A cylindrical furnace body for throwing in an object to be processed such as general waste or industrial waste, and melting the input object to be processed, and the object to be processed put in the furnace body are accumulated. Combustion that occurs when the workpiece is melted by being connected to a cylindrical gas discharge hole provided on the side of the furnace body that is lower than the surface position of the deposit and that is higher than the tuyere provided on the furnace bottom side A gas recovery pipe for recovering a furnace gas such as gas or exhaust gas as a high-temperature gas of 800 ° C. or higher, and both a longitudinal central axis of the furnace body and an extending central axis of the gas recovery pipe The gas recovery pipe has a small angle of less than 90 ° formed by the upper connecting portion formed by the upper inner wall surface and the upper inner wall surface of the furnace body side portion connected to the upper inner wall surface. Extends upward so as to form an angle, and has a predetermined radius of curvature at the upper connecting portion. Subjected to rounded chamfered tip thickness of the upper connecting portion, the vertical reduction melting furnace, characterized in that the thickness to withstand thermal shock in the furnace.

(2)前記配設角度が67°以下である上記(1)記載の縦型還元溶融炉。 (2) The vertical reduction melting furnace according to the above (1), wherein the arrangement angle is 67 ° or less.

(3)前記上側連結部に施した面取りの曲率半径は、炉体壁厚の1/3以上である上記(1)または(2)記載の縦型還元溶融炉。 (3) The vertical reduction melting furnace according to (1) or (2), wherein a radius of curvature of chamfering applied to the upper connecting portion is 1/3 or more of a furnace wall thickness.

(4)前記上側連結部に冷却手段を設ける上記(1)、(2)または(3)記載の縦型還元溶融炉。 (4) The vertical reduction melting furnace according to (1), (2) or (3), wherein a cooling means is provided in the upper connecting portion.

(5)前記上側連結部の所定位置に高温耐火物を設ける上記(1)〜(4)のいずれか1項記載の縦型還元溶融炉。 (5) The vertical reduction melting furnace according to any one of (1) to (4), wherein a high-temperature refractory is provided at a predetermined position of the upper connection portion.

この発明のよれば、炉体の炉下部側の側部に設けたガス回収管の上側内壁面と、該上側内壁面と連結される炉体側部の上側内壁面とで形成される上側連結部のなす角度を90°未満の小さな角度となるように上方に向かって延び、かつ、上側連結部に、所定の曲率半径で丸くした面取りを施して、前記上側連結部の先端厚みを、炉内の熱衝撃に耐えうる厚さにすることにより、800℃以上の高温ガスの回収するガス回収管の連結部を構成する内面炉材の損傷を有効に防止した耐久性に優れた縦型還元溶融炉の提供が可能になった。 According to the present invention, the upper connecting portion formed by the upper inner wall surface of the gas recovery pipe provided on the side of the furnace lower portion of the furnace body and the upper inner wall surface of the furnace body side portion connected to the upper inner wall surface. The upper connecting portion is chamfered with a predetermined radius of curvature to extend upward so that the angle formed is a small angle of less than 90 °, and the tip thickness of the upper connecting portion is set in the furnace. By making it thick enough to withstand the thermal shock of steel, it is a highly efficient vertical reductive melting that effectively prevents damage to the internal furnace material that forms the connecting part of the gas recovery pipe that collects high-temperature gas at 800 ° C or higher. Furnace can now be provided.

以下、本発明について図面に従って詳細に説明する。
図1は、本発明に従う縦型還元溶融炉の外観図であり、図2は図1に示す溶融炉のガス回収管の上側内壁面と炉体側部の上側内壁面とで形成される上側連結部を含む要部の拡大図である。
Hereinafter, the present invention will be described in detail with reference to the drawings.
FIG. 1 is an external view of a vertical reduction melting furnace according to the present invention, and FIG. 2 is an upper connection formed by an upper inner wall surface of a gas recovery pipe of the melting furnace shown in FIG. It is an enlarged view of the principal part containing a part.

図1に示す縦型還元溶融炉1は、炉体2とガス回収管3とで主に構成されている。
炉体2は、一般廃棄物や産業廃棄物等の被処理物および副原料としてコークスおよび石灰石を装入口4から投入され、投入した前記被処理物等を溶融処理するための溶融炉の部分であり、略円筒状をなしている。
A vertical reduction melting furnace 1 shown in FIG. 1 is mainly composed of a furnace body 2 and a gas recovery pipe 3.
The furnace body 2 is a part of a melting furnace for injecting coke and limestone as auxiliary materials such as general waste and industrial waste from the inlet 4 and melting the input to-be-processed object. There is a substantially cylindrical shape.

ガス回収管3は、炉体2内に投入された前記被処理物が堆積する堆積物の表面位置5よりも下部であってかつ炉底4側に設けた羽口5a、5b、5cよりも高い炉体2の側部2aに設けた円筒状のガス排出孔6に連結され、前記被処理物の溶融時に発生する燃焼ガスや排ガス等の炉内ガス7を800℃以上の高温ガスとして回収するための溶融炉の部分である。 また、ガス回収管3は、図2に示すように、前記炉体2の長手方向中心軸線と前記ガス回収管の延在方向中心軸線の双方を含む断面で見て、ガス回収管3の上側内壁面8と、この上側内壁面8と連結される炉体側部2aの上側内壁面9とで形成される上側連結部10のなす角度αが90°未満、好適には67°以下の小さな角度となるように上方に向かって延びるように配設されている。 The gas recovery pipe 3 is lower than the surface position 5 of the deposit on which the object to be processed put in the furnace body 2 is deposited and more than tuyere 5a, 5b, 5c provided on the furnace bottom 4 side. It is connected to a cylindrical gas discharge hole 6 provided on the side 2a of the high furnace body 2, and the in-furnace gas 7 such as combustion gas and exhaust gas generated when the object to be processed is melted is recovered as a high-temperature gas at 800 ° C or higher. It is a part of the melting furnace. Further, as shown in FIG. 2, the gas recovery pipe 3 is an upper side of the gas recovery pipe 3 when viewed in a cross section including both the longitudinal central axis of the furnace body 2 and the central axis of the gas recovery pipe in the extending direction. An angle α formed by the upper connecting portion 10 formed by the inner wall surface 8 and the upper inner wall surface 9 of the furnace body side portion 2a connected to the upper inner wall surface 8 is less than 90 °, preferably a small angle of 67 ° or less. So as to extend upward.

そして、この発明の構成上の主な特徴は、炉体2の炉下部11側の側部に設けたガス回収管3の上側連結部10の適正化を図ること、具体的には、前記炉体2の長手方向中心軸線と前記ガス回収管3の延在方向中心軸線の双方を含む断面で見て、前記ガス回収管3は、その上側内壁面8と、その上側内壁面8と連結される炉体側部2aの上側内壁面9とで形成される上側連結部10のなす角度が90°未満の小さな角度となるように上方に向かって延び、かつ、上側連結部10に、所定の曲率半径Rで丸くした面取りを施して、前記上側連結部10の先端厚みを、炉内の熱衝撃に耐えうる厚さにすることにあり、この構成を採用することにより、800℃以上の高温ガスの回収するガス回収管の連結部を構成する内面炉材の損傷を有効に防止することができる。 The main feature of the configuration of the present invention is to optimize the upper connecting part 10 of the gas recovery pipe 3 provided on the side of the furnace body 2 on the furnace lower part 11 side, specifically, the furnace The gas recovery pipe 3 is connected to the upper inner wall surface 8 and the upper inner wall surface 8 when viewed in a cross section including both the longitudinal central axis of the body 2 and the extending central axis of the gas recovery pipe 3. The upper connecting portion 10 formed with the upper inner wall surface 9 of the furnace body side portion 2a extends upward such that the angle formed by the upper connecting portion 10 is a small angle of less than 90 °, and the upper connecting portion 10 has a predetermined curvature. By chamfering with a radius R, the tip of the upper connecting part 10 is made thick enough to withstand thermal shock in the furnace. By adopting this configuration, a high-temperature gas of 800 ° C. or higher is used. Effectively prevent damage to the inner furnace material that forms the connecting part of the gas recovery pipe be able to.

図1に示す構造をもつ従来の溶融炉(例えば特許文献1の図1に示される溶融炉)のように、ガス回収管が、上側内壁面と炉体側部の上側内壁面とで形成される上側連結部のなす角度が鋭角となるように上方に向かって延びる場合には、上側連結部が、図2の破線で示すように、上側連結部の先端形状が、壁厚が薄くなる鋭角形状となるのが一般的であり、このように鋭角になった先端部分は、熱容量が小さいため炉内の熱で他の部分に比べて容易に高温になり熱破壊されやすくなって、補修頻度が高くなるという問題があった。 As in the conventional melting furnace having the structure shown in FIG. 1 (for example, the melting furnace shown in FIG. 1 of Patent Document 1), the gas recovery pipe is formed by the upper inner wall surface and the upper inner wall surface of the furnace body side portion. When the upper connecting portion extends upward so that the angle formed by the upper connecting portion is an acute angle, the upper connecting portion has an acute-angle shape in which the tip shape of the upper connecting portion is thin as shown by the broken line in FIG. The tip part with such an acute angle has a small heat capacity, so the heat in the furnace easily becomes higher than other parts due to the heat in the furnace, and is easily destroyed by heat. There was a problem of becoming higher.

このため、本発明では、上側連結部の先端部が鋭角になるのを防止するため、上側連結部10に、所定の曲率半径Rで丸くした面取りを施して、前記上側連結部10の先端厚みを、炉内の熱衝撃に耐えうる厚さにしたものである。 For this reason, in the present invention, in order to prevent the distal end portion of the upper coupling portion from becoming an acute angle, the upper coupling portion 10 is chamfered with a predetermined radius of curvature R to obtain the thickness of the distal end of the upper coupling portion 10. Is made to a thickness that can withstand thermal shock in the furnace.

前記上側連結部に施した面取りの曲率半径Rは、炉体の壁厚t1の1/3以上とすることが好ましい。前記曲率半径Rが炉体の壁厚t1の1/3未満だと、前記上側連結部の先端厚さが十分に厚くできないため、前記上側連結部の先端部が熱衝撃によって早期に損傷しやすくなる傾向があるからである。 It is preferable that the radius of curvature R of the chamfering applied to the upper connection portion is 1/3 or more of the wall thickness t1 of the furnace body. If the radius of curvature R is less than 1/3 of the wall thickness t1 of the furnace body, the tip of the upper connecting part cannot be made sufficiently thick, so that the tip of the upper connecting part is easily damaged by thermal shock at an early stage. Because there is a tendency to become.

また、図3は、温度抑制効果を利用した他の実施形態を示す図であり、この実施形態では、上側連結部10と下側連結部12に円環状に冷却手段である冷却管13が埋め込まれ、この冷却管13に水や不燃性油などの液体、あるいは空気、窒素などの冷却媒体を導入し、冷却管出口から排出された媒体を冷却機で冷却した後、再び入口から循環させる構成をさらに有している。冷却媒体により炉壁部分が例えば1200℃に保持される。図示の例では冷却管13は上側連結部に埋設して設置する場合を示したが、上側連結部の外壁に設置することも可能である。この場合、冷却効率を上げるため、冷却管13はガス回収管3の連結位置に近い外壁に設置することが望ましい。冷却管13はガス回収管3を取り巻くように設置しても、ガス回収管3の上側連結部10のみを冷却するようにしてもよい。ガス回収管3の延在形状については、連結部分を除いて、任意の方向に延在させることができる。 FIG. 3 is a diagram showing another embodiment using the temperature suppression effect. In this embodiment, a cooling pipe 13 as a cooling means is embedded in an annular shape in the upper connecting portion 10 and the lower connecting portion 12. A configuration in which a liquid such as water or non-combustible oil, or a cooling medium such as air or nitrogen is introduced into the cooling pipe 13, the medium discharged from the cooling pipe outlet is cooled by a cooler, and then circulated from the inlet again. It has further. The furnace wall portion is maintained at 1200 ° C., for example, by the cooling medium. In the illustrated example, the cooling pipe 13 is embedded in the upper connecting portion and installed, but it can be installed on the outer wall of the upper connecting portion. In this case, it is desirable to install the cooling pipe 13 on the outer wall close to the connection position of the gas recovery pipe 3 in order to increase the cooling efficiency. The cooling pipe 13 may be installed so as to surround the gas recovery pipe 3, or only the upper connecting portion 10 of the gas recovery pipe 3 may be cooled. About the extended shape of the gas recovery pipe | tube 3, it can be made to extend in arbitrary directions except a connection part.

図4は、耐火物による保護効果を利用した他の実施形態を示す図である。これらは、例えば、ステンレス、耐熱鋳鉄、アルミナ、窒化珪素、炭化ケイ素、ジルコニアなどの超高耐熱材料からなる焼結片14で連結部10の内面を被覆して、炉体内部の火力から保護する構成を有している。
すなわち図4においては、炉内火力の影響を受けやすい上側連結部の形状に合わせて前記材料の一つで作った焼結片14を炉材に取り付けた場合の例である。
FIG. 4 is a diagram showing another embodiment using a protective effect by a refractory. For example, the inner surface of the connecting portion 10 is covered with a sintered piece 14 made of an ultra-high heat-resistant material such as stainless steel, heat-resistant cast iron, alumina, silicon nitride, silicon carbide, zirconia, and the like to protect from the thermal power inside the furnace body. It has a configuration.
That is, FIG. 4 shows an example of a case where a sintered piece 14 made of one of the above materials is attached to the furnace material in accordance with the shape of the upper connecting portion that is easily affected by the heating power in the furnace.

図5(a),(b)は、防御壁15を用いた他の実施形態を示す図である。炉体2の内壁9に設けられた図5(a)に示す防御壁15は、例えば、ステンレス、耐熱鋳鉄、アルミナ、窒化珪素、炭化ケイ素、ジルコニアなどの超高耐熱材料ガス回収管3のガス排出孔6から所定の距離W、好適には0.2〜0.5mだけ離隔させるとともに、上側連結部の面取り面から防御壁の先端位置までの距離L2を、ガス排出孔6の径L1との関係で適正距離、好適には(1〜2)L1の範囲になるように配設され、前記ガス排出孔6の全体を包む形となっており、炉内ガスは、防御壁15の上部からガス回収管3に流れ込むように構成されている。前記所定の距離Wが0.2mよりも短いと、炉内の高温ガスがガス回収管に回収されるガス量が十分煮えられなくなる傾向があるからであり、前記所定の距離Wが0.5mよりも長いと、上側連結部10の温度上昇を緩和する効果が十分には得られなくなる傾向があるからである。また、前記距離L2は、2L1よりも長いと、図6に示すように、炉内ガスがガス回収管内に上昇しにくくなる傾向があり、また、L1よりも短いと、上側連結部10の温度上昇を十分に抑制できなくなるからである。防御壁15を、ガス回収管3のガス排出孔6から所定の位置関係で設けることにより、防御壁15の下部には開口はなく表面が滑らかになっているので、炉内の熱気流はスムーズに流れ、温度上昇は緩和される。上側連結部10は直接熱気流にさらされることがなくなるため、熱破損の確率はより一層小さくなる。   FIGS. 5A and 5B are diagrams showing another embodiment using the defense wall 15. The protective wall 15 shown in FIG. 5 (a) provided on the inner wall 9 of the furnace body 2 is, for example, a gas of the super high heat resistant material gas recovery pipe 3 such as stainless steel, heat resistant cast iron, alumina, silicon nitride, silicon carbide, zirconia. While being separated from the discharge hole 6 by a predetermined distance W, preferably 0.2 to 0.5 m, the distance L2 from the chamfered surface of the upper connecting portion to the tip position of the defense wall is set to the diameter L1 of the gas discharge hole 6. Therefore, it is arranged so as to be within an appropriate distance, preferably (1 to 2) L1, and encloses the entire gas discharge hole 6. To flow into the gas recovery pipe 3. This is because if the predetermined distance W is shorter than 0.2 m, the amount of high-temperature gas in the furnace that is recovered in the gas recovery pipe tends not to be cooked sufficiently, and the predetermined distance W is 0.5 m. This is because the effect of alleviating the temperature rise of the upper connecting portion 10 tends not to be sufficiently obtained if the length is longer than that. Further, if the distance L2 is longer than 2L1, the furnace gas tends to hardly rise into the gas recovery pipe as shown in FIG. 6, and if the distance L2 is shorter than L1, the temperature of the upper connecting portion 10 tends to increase. This is because the rise cannot be sufficiently suppressed. By providing the protective wall 15 in a predetermined positional relationship from the gas discharge hole 6 of the gas recovery pipe 3, since there is no opening at the lower part of the protective wall 15 and the surface is smooth, the hot air flow in the furnace is smooth. The temperature rise is mitigated. Since the upper connecting part 10 is not directly exposed to the hot air flow, the probability of thermal damage is further reduced.

なお、図3〜図5は、それぞれ冷却管13、焼結片14および防御壁15を個別に設けた場合を示しているが、本発明では、これらを組み合わせて構成することも可能である。   3 to 5 show cases where the cooling pipe 13, the sintered piece 14, and the protective wall 15 are individually provided, but in the present invention, they may be combined.

本発明に従う溶融炉の例を示すと、炉体の、全長は3〜30m、内壁面の直径は0.5〜10m、炉体の壁厚t1は0.1〜0.5m、ガス回収管は、外径が0.3〜3.0m、内径が0.1〜2.8m、ガス回収管の壁厚t2が0.05〜0.5m、上側連結部のなす角度αは5〜80°である。 An example of a melting furnace according to the present invention is as follows. The length of the furnace body is 3 to 30 m, the diameter of the inner wall surface is 0.5 to 10 m, the wall thickness t1 of the furnace body is 0.1 to 0.5 m, and the gas recovery pipe The outer diameter is 0.3 to 3.0 m, the inner diameter is 0.1 to 2.8 m, the wall thickness t2 of the gas recovery pipe is 0.05 to 0.5 m, and the angle α formed by the upper connecting portion is 5 to 80 °.

次に、本発明に従う溶融炉を用い、廃棄物処理を行ったので以下で説明する。   Next, since the waste processing was performed using the melting furnace according to the present invention, it will be described below.

(実施例1)
実施例1の溶融炉は、図1および図2に示す形態を有し、炉体の、全長が10m、内壁面の直径が3m、炉体の壁厚t1が0.2m、ガス回収管は、外径が1.5m、内径が1.1m、ガス回収管の壁厚t2が0.2m、上側連結部のなす角度αが40°、上側連結部の面取りの曲率半径Rが0.15mである。
Example 1
The melting furnace of Example 1 has the form shown in FIG. 1 and FIG. 2, the length of the furnace body is 10 m, the diameter of the inner wall surface is 3 m, the wall thickness t1 of the furnace body is 0.2 m, and the gas recovery pipe is The outer diameter is 1.5 m, the inner diameter is 1.1 m, the wall thickness t2 of the gas recovery pipe is 0.2 m, the angle α formed by the upper connecting portion is 40 °, and the curvature radius R of the chamfering of the upper connecting portion is 0.15 m. It is.

(実施例2)
実施例2の溶融炉は、図1および図3に示す形態を有し、上側および下側連結部に水を循環させて冷却する冷却管を埋設したことを除いて実施例1の溶融炉と同様な構造する。
(Example 2)
The melting furnace of Example 2 has the form shown in FIGS. 1 and 3, and the melting furnace of Example 1 except that a cooling pipe for circulating and cooling water is embedded in the upper and lower connecting portions. Similar structure.

(実施例3)
実施例3の溶融炉は、図1および図4に示す形態を有し、上側連結部の面取りの外面にステンレス材料からなる焼結片で被覆したことを除いて実施例1の溶融炉と同様な構造を有する。
(Example 3)
The melting furnace of Example 3 has the form shown in FIGS. 1 and 4 and is similar to the melting furnace of Example 1 except that the chamfered outer surface of the upper connecting portion is covered with a sintered piece made of a stainless material. It has a simple structure.

(実施例4)
実施例4の溶融炉は、図1および図5(a)に示す形態を有し、上側連結部が高温になるのを防止するため、ステンレス材料からなる防御壁(W=0.3m)を設けたことを除いて実施例1の溶融炉と同様な構造を有する。
Example 4
The melting furnace of Example 4 has the form shown in FIG. 1 and FIG. 5A, and has a protective wall (W = 0.3 m) made of a stainless material in order to prevent the upper connecting portion from becoming high temperature. It has the same structure as the melting furnace of Example 1 except having provided.

(比較例)
比較例の溶融炉は、上側連結部に面取りを施さないことを除いて実施例1の溶融炉と同様な構造を有する。
(Comparative example)
The melting furnace of the comparative example has the same structure as the melting furnace of Example 1 except that the upper connecting portion is not chamfered.

上述した実施例および比較例の溶融炉を用い、15〜50トン/日の廃棄物を1年間にわたって処理し、上側連結部の外面位置10で測定した温度が、操業(廃棄物処理)開始時は80℃であったが、300℃以上になった場合に上側連結部の補修が必要であるものとし、各溶融炉の上側連結部を補修したときの回数を測定した。この測定結果を表1に示す。   Using the melting furnaces of the examples and comparative examples described above, 15 to 50 tons / day of waste was treated for one year, and the temperature measured at the outer surface position 10 of the upper connecting portion was at the start of operation (waste treatment). Was 80 ° C., but when the temperature became 300 ° C. or higher, it was assumed that the upper connecting portion needs to be repaired, and the number of times when the upper connecting portion of each melting furnace was repaired was measured. The measurement results are shown in Table 1.

Figure 2008256283
Figure 2008256283

表1に示す結果から、実施例1〜4の溶融炉はいずれも、上側連結部の補修回数が、比較例の溶融炉に比べて少ないことがわかる。   From the results shown in Table 1, it can be seen that all of the melting furnaces of Examples 1 to 4 have a smaller number of repairs of the upper connecting portion than the melting furnace of the comparative example.

本発明によれば前記するように種々の実施形態があるがいずれにおいても、本発明者が開示するまで前例のなかった炉体の側部にガス回収管を設けた還元溶融炉においてガス回収管のガス排出孔が溶融炉の高い温度に起因して熱損傷を受ける問題を解決して、より安全なガス回収管を実現することができる。これにより廃棄物処理においてより効果的な熱収支の改善およびダイオキシン等の有害ガスの排出をゼロにし、かつ固体排出物も無害化され資源として有効に再利用することが可能になった。   According to the present invention, as described above, there are various embodiments. In any case, the gas recovery pipe is used in a reduction melting furnace in which a gas recovery pipe is provided on the side of the furnace body, which has not been preceded by the present inventors. This solves the problem that the gas discharge holes are thermally damaged due to the high temperature of the melting furnace, thereby realizing a safer gas recovery pipe. This makes it possible to improve the heat balance more effectively in waste disposal and to eliminate the emission of harmful gases such as dioxins, and to make solid emissions harmless and effectively reuse them as resources.

本発明に従う縦型還元溶融炉の概略正面図である。1 is a schematic front view of a vertical reduction melting furnace according to the present invention. 本発明の一の実施態様を示す図である。It is a figure which shows one embodiment of this invention. 本発明の他の実施態様を示す図である。It is a figure which shows the other embodiment of this invention. 本発明の他の実施態様を示す図である。It is a figure which shows the other embodiment of this invention. 本発明の他の実施態様を示す図である。It is a figure which shows the other embodiment of this invention. 上側連結部の面取り面から防御壁の先端位置までの距離L2と、ガス排出孔6の径L1との関係を示す図である。It is a figure which shows the relationship between the distance L2 from the chamfering surface of an upper connection part to the front-end | tip position of a defense wall, and the diameter L1 of the gas exhaust hole 6. FIG.

符号の説明Explanation of symbols

1 縦型還元溶融炉
2 炉体
3 ガス回収管
4 装入口
5a、5b、5c 羽口
6 ガス排出孔
7 炉内ガス
8 ガス回収管の上側内壁面
9 炉体側部の上側内壁面
10 上側連結部
11 炉体の炉下部
12 下側連結部
13 冷却管
14 焼結片
15 防御壁
1 Vertical Reduction Melting Furnace 2 Furnace 3 Gas Recovery Pipe 4 Charger
5a, 5b, 5c Tuyere 6 Gas exhaust hole 7 Furnace gas 8 Upper inner wall surface of gas recovery pipe 9 Upper inner wall surface of furnace body side
10 Upper connection
11 Furnace lower part
12 Lower connection
13 Cooling pipe
14 Sintered pieces
15 Defense wall

Claims (5)

一般廃棄物や産業廃棄物等の被処理物を投入し、投入した前記被処理物を溶融するための円筒状の炉体と、該炉体内に投入された前記被処理物が堆積する堆積物の表面位置よりも下部であってかつ炉底側に設けた羽口よりも高い炉体側部に設けた円筒状のガス排出孔に連結され、前記被処理物の溶融時に発生する燃焼ガスや排ガス等の炉内ガスを800℃以上の高温ガスとして回収するためのガス回収管とを有し、前記炉体の長手方向中心軸線と前記ガス回収管の延在方向中心軸線の双方を含む断面で見て、前記ガス回収管は、その上側内壁面と、該上側内壁面と連結される炉体側部の上側内壁面とで形成される上側連結部のなす角度が90°未満の小さな角度となるように上方に向かって延び、かつ、上側連結部に、所定の曲率半径で丸くした面取りを施して、前記上側連結部の先端厚みを、炉内の熱衝撃に耐えうる厚さにすることを特徴とする縦型還元溶融炉。   Cylindrical furnace body for throwing in treated objects such as general waste and industrial waste, and melting the inputted treated objects, and deposits on which the treated objects thrown into the furnace body are deposited Combustion gas and exhaust gas generated when the object to be processed is melted, connected to a cylindrical gas discharge hole provided in the furnace body side part lower than the surface position of the furnace and higher than the tuyere provided on the furnace bottom side And a gas recovery pipe for recovering the gas in the furnace as a high-temperature gas of 800 ° C. or higher, and includes both a longitudinal central axis of the furnace body and a central axis of the gas recovery pipe in the extending direction. The gas recovery pipe has a small angle of less than 90 ° formed by the upper connecting portion formed by the upper inner wall surface and the upper inner wall surface of the furnace body side portion connected to the upper inner wall surface. So as to extend upward and round the upper connecting portion with a predetermined radius of curvature. And chamfered, the tip thickness of the upper connecting portion, the vertical reduction melting furnace, characterized in that the thickness to withstand thermal shock in the furnace. 前記配設角度が67°以下である請求項1記載の縦型還元溶融炉。 The vertical reduction melting furnace according to claim 1, wherein the arrangement angle is 67 ° or less. 前記上側連結部に施した面取りの曲率半径は、炉体壁厚の1/3以上である請求項1または2記載の縦型還元溶融炉。 The vertical reduction melting furnace according to claim 1 or 2, wherein a radius of curvature of chamfering applied to the upper connecting portion is 1/3 or more of a furnace wall thickness. 前記上側連結部に冷却手段を設ける請求項1、2または3記載の縦型還元溶融炉。   The vertical reduction melting furnace according to claim 1, 2 or 3, wherein a cooling means is provided at the upper connecting portion. 前記上側連結部の所定位置に高温耐火物を設ける請求項1〜4のいずれか1項記載の縦型還元溶融炉。   The vertical reduction melting furnace according to claim 1, wherein a high-temperature refractory is provided at a predetermined position of the upper connection part.
JP2007099578A 2007-04-05 2007-04-05 Vertical reduction melting furnace Pending JP2008256283A (en)

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