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JP3110784U - Dry distillation furnace - Google Patents

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JP3110784U
JP3110784U JP2005001754U JP2005001754U JP3110784U JP 3110784 U JP3110784 U JP 3110784U JP 2005001754 U JP2005001754 U JP 2005001754U JP 2005001754 U JP2005001754 U JP 2005001754U JP 3110784 U JP3110784 U JP 3110784U
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furnace
heating means
heat
heating device
space
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正明 中川
昌之 竹島
二郎 増田
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SHOEI MFG. CO., LTD.
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Abstract

【課題】ゴム組成物等の被熱処理物を間接的に加熱して良質の炭化物や生成ガスを回収でき、しかも被熱処理物を効率よく且つ均一に加熱できるようにする。
【解決手段】炉壁(2)の内面に沿って第1加熱装置(15)を配置する。炉壁(2)よりも内側に筒状の第2加熱装置(18)を配置する。両加熱装置(15・18)に高温ガスを循環する。第2加熱装置(18)と炉壁(2)との間に、被熱処理物(8)を収容する収容空間(20)を形成する。第2加熱装置(18)の内側に炉内の熱気が流通する流通空間(21)を形成する。第2加熱装置(18)の上方に覆い部(22)を配置して流通空間(21)への被熱処理物(8)の投入を防止する。第2加熱装置(18)の上端と覆い部(22)との間に、収容空間(20)と流通空間(21)とを互いに連通する第1連通部(26)を形成する。第2加熱装置(18)の下端と底壁部(10)との間に収容空間(20)と流通空間(21)とを互いに連通する第2連通部(28)を形成する。
【選択図】 図1
An object of the present invention is to indirectly heat a material to be heat treated such as a rubber composition so as to collect good quality carbides and generated gas, and to heat the material to be heat treated efficiently and uniformly.
A first heating device (15) is disposed along an inner surface of a furnace wall (2). A cylindrical second heating device (18) is arranged inside the furnace wall (2). Circulate hot gas through both heating devices (15, 18). Between the second heating device (18) and the furnace wall (2), an accommodation space (20) for accommodating the object to be heat treated (8) is formed. A circulation space (21) through which hot air in the furnace flows is formed inside the second heating device (18). A covering part (22) is arranged above the second heating device (18) to prevent the material to be heat treated (8) from being introduced into the circulation space (21). A first communication part (26) is formed between the upper end of the second heating device (18) and the cover part (22) to communicate the accommodation space (20) and the circulation space (21) with each other. A second communication portion (28) is formed between the lower end of the second heating device (18) and the bottom wall portion (10) to communicate the accommodation space (20) and the flow space (21) with each other.
[Selection] Figure 1

Description

本考案は被熱処理物を加熱する乾留炉に関し、さらに詳しくは、ゴム組成物等の被熱処理物を間接的に加熱して良質の炭化物や生成ガスを回収できるものでありながら、しかも被熱処理物を効率よく且つ均一に加熱できる、乾留炉に関する。   The present invention relates to a carbonization furnace for heating an object to be heat-treated. More specifically, the heat-treated object such as a rubber composition can be indirectly heated to recover high-quality carbides and product gas, and the object to be heat-treated. It is related with the dry distillation furnace which can heat | fever efficiently and uniformly.

廃タイヤ等のゴム製品廃棄物の発生量は年々急激に増加しており、これらは焼却すると黒煙や有毒ガス、悪臭等を発生し環境汚染を引き起こす虞がある。
近年、環境汚染を引き起こすこと無くこれらの廃棄物を再資源化する処理方法が多く研究されており、そのひとつに、これらの廃棄物を炉内に充填して、炉内の空気を理論燃焼量以下(無酸素雰囲気下)に保ちながら加熱して有機固形物を分解させ、炭化物(以下、乾留チャーと称する)とガス(以下、生成ガスと称する)とを生成する、乾留方式が開発されている。
The amount of rubber product waste such as waste tires is increasing rapidly year by year, and when they are incinerated, black smoke, toxic gas, bad odor and the like may be generated, causing environmental pollution.
In recent years, many research methods have been researched to recycle these wastes without causing environmental pollution, and one of them is the filling of these wastes into the furnace, and the theoretical amount of combustion in the furnace air. A dry distillation method has been developed in which organic solids are decomposed by heating while maintaining the following (in an oxygen-free atmosphere) to generate carbides (hereinafter referred to as dry distillation char) and gas (hereinafter referred to as product gas). Yes.

従来、上記の乾留方式に用いる乾留炉としては、炉内に配置した加熱手段に高温ガスを循環させ、炉内に収容した被熱処理物を間接的に加熱する乾留炉がある(例えば、特許文献1参照)。
即ち、この従来技術は、炉壁の内面に沿って筒状の第1加熱手段を配置するとともに、この第1加熱手段よりも内側に筒状の第2加熱手段を配置してある。被熱処理物は細かくチップ状に裁断され、炉内に投入されて両加熱手段の間と第2加熱手段の内側に収容される。そして両加熱手段に高温ガスを循環させることにより、被熱処理物が間接的に加熱される。この加熱により被熱処理物から発生した生成ガスは、炉内の上部空間から排出用配管を介して取り出され、冷却してガス成分とオイル成分に分離されて回収される。一方、炉内には乾留チャーが残り、炉底部の取出口が開口されて、下方に配置された回収容器に回収されたのち、賦活炉へ搬送されて賦活処理される。
Conventionally, as a carbonization furnace used in the above-mentioned carbonization method, there is a carbonization furnace in which a high-temperature gas is circulated through a heating means arranged in the furnace and a heat-treated material accommodated in the furnace is indirectly heated (for example, patent literature). 1).
That is, in this prior art, a cylindrical first heating means is arranged along the inner surface of the furnace wall, and a cylindrical second heating means is arranged inside the first heating means. The object to be heat treated is finely cut into chips, put into a furnace and accommodated between both heating means and inside the second heating means. And a to-be-processed object is heated indirectly by circulating high temperature gas to both the heating means. The generated gas generated from the object to be heat-treated by this heating is taken out from the upper space in the furnace through the discharge pipe, cooled, separated into a gas component and an oil component, and recovered. On the other hand, the carbonization char remains in the furnace, the outlet at the bottom of the furnace is opened, and after being collected in a recovery container disposed below, it is transported to the activation furnace for activation treatment.

この従来技術は、炉内に筒状の第2加熱手段を配置してあるので、炉内の被熱処理物は加熱手段との距離が短く、良好に加熱される。しかも、被熱処理物は炉内の両加熱手段により間接的に加熱されるので、加熱のための燃焼ガスが被熱処理物と混合することがなく、良質の乾留チャーや生成ガスを回収することができる。   In this prior art, since the cylindrical second heating means is arranged in the furnace, the object to be heat-treated in the furnace has a short distance from the heating means and is heated well. In addition, since the object to be heat-treated is indirectly heated by both heating means in the furnace, the combustion gas for heating is not mixed with the object to be heat-treated, and high-quality dry distillation char and product gas can be recovered. it can.

特開2003−213033号公報JP 2003-213033 A

上記の従来技術では、炉内に被熱処理物を多く収容すると炉内の加熱された空気や生成ガスなどの熱気が流通し難くなり、炉内での温度分布に偏りを生じて被熱処理物への熱伝達効率が低下するうえ、炉内の上部と下部で加熱が不均一になる問題がある。このように熱伝達効率が低下し、加熱が不均一になると、被熱処理物に未処理部分が残り、また、処理後に炉内から炭化物を取り出す際、この未処理物がブリッジ現象を生じて、炭化物の取出しが困難になる問題を生じる。このため、充分な加熱処理に長時間を要するうえ、炉内に収容する被熱処理物の収容量を、例えば炉内空間の65%程度以上に多くすることができず、処理効率を向上することが容易でない問題があった。   In the above prior art, if a large number of materials to be heat-treated are contained in the furnace, it becomes difficult for hot air such as heated air and product gas in the furnace to circulate, and the temperature distribution in the furnace is biased to the materials to be heat-treated. There are problems that the heat transfer efficiency is reduced and the heating is not uniform in the upper and lower parts of the furnace. Thus, when the heat transfer efficiency is reduced and the heating becomes uneven, an untreated part remains in the object to be heat treated, and when the carbide is taken out from the furnace after the treatment, this untreated object causes a bridge phenomenon, This causes a problem that it is difficult to take out the carbide. For this reason, it takes a long time for sufficient heat treatment, and the amount of heat-treated material accommodated in the furnace cannot be increased to, for example, about 65% or more of the space in the furnace, thereby improving the processing efficiency. There was a problem that was not easy.

本考案の技術的課題は上記の問題点を解消し、ゴム組成物等の被熱処理物を間接的に加熱して良質の炭化物や生成ガスを回収できるものでありながら、しかも被熱処理物を効率よく且つ均一に加熱できる、乾留炉を提供することにある。   The technical problem of the present invention is to solve the above-mentioned problems, and indirectly heat the object to be heat treated such as a rubber composition to recover high-quality carbides and generated gas, while also making the object to be heat treated efficient. An object of the present invention is to provide a dry distillation furnace that can be heated well and uniformly.

本考案は上記の課題を解決するために、例えば、本考案の実施の形態を示す図1と図2に基づいて説明すると、次のように構成したものである。
即ち、本考案は乾留炉に関し、炉壁(2)の内面に沿って第1加熱手段(15)を配置するとともに、上記の炉壁(2)よりも内側に筒状の第2加熱手段(18)を配置し、この両加熱手段(15・18)にそれぞれ高温ガスを循環させて、炉内に収容した被熱処理物(8)を間接的に加熱する乾留炉であって、上記の第2加熱手段(18)と上記の炉壁(2)との間に、上記の被熱処理物(8)を収容する収容空間(20)を形成し、上記の第2加熱手段(18)の内側に、炉内の熱気が流通する流通空間(21)を形成するとともに、この流通空間(21)への被熱処理物(8)の投入を防止する覆い部(22)を上記の第2加熱手段(18)の上方に配置し、上記の第2加熱手段(18)の上部とその上側の少なくともいずれかに、上記の収容空間(20)と流通空間(21)とを互いに連通する第1連通部(26)を形成したことを特徴とする。
In order to solve the above problems, the present invention is configured as follows, for example, based on FIGS. 1 and 2 showing an embodiment of the present invention.
That is, the present invention relates to a carbonization furnace, wherein the first heating means (15) is disposed along the inner surface of the furnace wall (2), and the cylindrical second heating means (inside the furnace wall (2) ( 18), a high temperature gas is circulated through both the heating means (15, 18), and the heat treatment object (8) accommodated in the furnace is indirectly heated. An accommodation space (20) for accommodating the object to be heat treated (8) is formed between the two heating means (18) and the furnace wall (2), and the inside of the second heating means (18) is formed. In addition, a cover portion (22) that forms a circulation space (21) through which hot air in the furnace flows and prevents the material (8) to be heat-treated from flowing into the circulation space (21) is provided with the second heating means. (18) arranged above the first heating means (18) and at least one of the upper side of the second heating means (18) to communicate the accommodation space (20) and the circulation space (21) with each other. Part (26) formed And

ゴム組成物等の被熱処理物は、加熱手段により間接的に加熱され、加熱のための燃焼ガスが混入することがない。このため、乾留チャーに多量の酸化物が混入したり、生成ガスに多量の低発熱量成分が混入したりすることが防止され、良質の炭化物や生成ガスが回収される。 A material to be heat treated such as a rubber composition is indirectly heated by a heating means, and combustion gas for heating is not mixed. For this reason, it is prevented that a large amount of oxides are mixed in the dry distillation char and a large amount of low calorific value components are mixed in the product gas, and good quality carbides and product gas are recovered.

上記の流通空間は覆い部により被熱処理物の投入が防止されるので、空洞の状態が維持される。このため、流通空間内の熱気は第1連通部から収容空間の上部へ良好に流通し手順間し、炉内の隅々にまで行き渡る。この結果、上記の被熱処理物は、加熱手段からの輻射熱や伝導熱に加え、この熱気により効率よく加熱される。   Since the above-mentioned circulation space prevents the material to be heat-treated from being put in by the cover portion, a hollow state is maintained. For this reason, the hot air in the circulation space is well circulated from the first communication portion to the upper portion of the accommodation space, and spreads to every corner in the furnace during the procedure. As a result, the object to be heat-treated is efficiently heated by this hot air in addition to the radiant heat and conduction heat from the heating means.

上記の流通空間は被熱処理物が投入されず、空洞状態となっているが、この流通空間は炉壁よりも内側に配置された筒状の第2加熱手段の内方に形成されるので、上記の収容空間に比べて占有体積がかなり少なく、例えば、炉内空間の10%程度以下に設定される。
一方、上記の収容空間内には、上記の流通空間から熱気が良好に循環されるので、被熱処理物の収容量を多くしても良好に且つ均一に加熱される。この結果炉内全体としては、例えば炉内空間の70%以上など、前記の従来技術に比べて多量の被熱処理物が収容される。
The above-mentioned circulation space is in a hollow state without being subjected to heat treatment, but this circulation space is formed inside the cylindrical second heating means disposed inside the furnace wall. The occupied volume is considerably smaller than the above accommodation space, and is set to about 10% or less of the space in the furnace, for example.
On the other hand, since hot air is circulated well from the circulation space in the accommodation space, it is heated evenly and uniformly even if the amount of the object to be heat-treated is increased. As a result, as a whole in the furnace, a large amount of heat-treated material is accommodated as compared with the above-described prior art, such as 70% or more of the space in the furnace.

上記の第1連通部は、第2加熱手段の上部に透設してもよく、あるいはその上側に配置された上記の覆い部に透設してもよい。しかし、上記の第2加熱手段と覆い部との間に上部間隙を形成して、この上部間隙により上記の第1連通部を構成すると、第2加熱手段の上方に隙間をあけて覆い部を配置するだけで簡単に形成できるので、より好ましい。   Said 1st communicating part may be transparently provided in the upper part of a 2nd heating means, or may be transparently provided in said cover part arrange | positioned above it. However, if an upper gap is formed between the second heating means and the cover, and the first communication part is constituted by the upper gap, the cover is formed with a gap above the second heating means. It is more preferable because it can be easily formed simply by arranging.

上記の第2加熱手段の下部とその下側の少なくともいずれかに、上記の収容空間と流通空間とを連通する第2連通部を形成すると、収容空間の下部の熱気が流通空間を経て収容空間の上部へ良好に循環するので、より好ましい。
この場合、上記の第2加熱手段と底壁部との間に下部間隙を形成して、この下部間隙により上記の第2連通部を構成すると、第2加熱手段を底壁部から少し持ち上げるだけで簡単に形成することができ、好ましい。
When a second communication portion that communicates the accommodation space and the circulation space is formed in at least one of the lower portion and the lower side of the second heating means, the hot air in the lower portion of the accommodation space passes through the circulation space and is accommodated in the accommodation space. It is more preferable because it circulates well to the top of the.
In this case, if a lower gap is formed between the second heating means and the bottom wall portion, and the second communication portion is constituted by the lower gap, the second heating means is lifted slightly from the bottom wall portion. And can be easily formed.

上記の覆い部は、上記の流通空間に被熱処理物が投入されないように、この流通空間を覆うものであればよく、特定の形状や構造に限定されない。但し、この覆い部の上面を周辺に向かって下る傾斜面に形成すると、この覆い部の上面に落下した被熱処理物が、この上面を滑り落ちて上記の収容空間内へ円滑に案内されるので、好ましい。   The covering portion is not limited to a specific shape or structure as long as it covers the distribution space so that the material to be heat-treated is not put into the distribution space. However, if the upper surface of the cover portion is formed as an inclined surface that goes down toward the periphery, the heat-treated material that has dropped on the upper surface of the cover portion will slide down the upper surface and be smoothly guided into the accommodation space. ,preferable.

上記の第1加熱手段と第2加熱手段は、炉内の被熱処理物を間接的に加熱できるものであればよく、配管等で構成してもよいが、これをパネル状に形成すると被熱処理物を均一に加熱できるうえ、加熱手段の表面が複雑な形状にならないので、乾留後に乾留チャーを収容空間から容易に取り出すことができ、好ましい。   The first heating means and the second heating means are not limited as long as they can indirectly heat the object to be heat-treated in the furnace, and may be constituted by piping or the like. The object can be heated uniformly, and the surface of the heating means does not have a complicated shape. Therefore, the dry distillation char can be easily taken out from the storage space after the dry distillation, which is preferable.

本考案は上記のように構成され作用することから、次の効果を奏する。   Since the present invention is configured and operates as described above, the following effects can be obtained.

(1) 収容空間に被熱処理物が多量に収容されていても、炉内の熱気が流通空間から収容空間の上部へ良好に流通して循環し、炉内の隅々にまで行き渡ることから、この熱気を介して加熱手段からの熱を被熱処理物へ良好に伝えることができ、しかも、炉内の上下で熱のかかり方を均等にすることができる。この結果、ゴム組成物等の被熱処理物を間接的に加熱して良質の炭化物や生成ガスを回収できるものでありながら、被熱処理物を効率よく且つ均一に加熱することができる。   (1) Even if a large amount of material to be heat-treated is stored in the storage space, the hot air in the furnace circulates and circulates well from the distribution space to the top of the storage space, and reaches every corner of the furnace. Through this hot air, the heat from the heating means can be transmitted well to the object to be heat treated, and furthermore, the heat application can be made uniform in the upper and lower parts in the furnace. As a result, the object to be heat treated such as a rubber composition can be heated indirectly and efficiently while being able to recover good quality carbides and product gas.

(2) 上記の流通空間は収容空間に比べて占有体積がかなり少なく、一方、上記の収容空間には被熱処理物を多量に収容しても良好に加熱できることから、上記の流通空間を空洞の状態に維持しても、炉内全体としては、前記の従来技術に比べて被熱処理物の収容量を多くでき、熱処理効率を高めることができる。   (2) The circulation space has a considerably smaller volume than the accommodation space. On the other hand, the accommodation space can be heated satisfactorily even if a large amount of the heat-treated material is accommodated. Even if it maintains in a state, as the whole furnace inside, the accommodation amount of to-be-processed material can be increased compared with the said prior art, and heat processing efficiency can be improved.

以下、本考案の実施の形態を図面に基づき説明する。
図1と図2は本考案の実施形態を示し、図1は乾留炉の概略構成を示す断面図、図2は覆い部近傍の一部破断斜視図である。
Hereinafter, embodiments of the present invention will be described with reference to the drawings.
1 and 2 show an embodiment of the present invention, FIG. 1 is a cross-sectional view showing a schematic configuration of a dry distillation furnace, and FIG. 2 is a partially broken perspective view in the vicinity of a cover portion.

図1に示すように、この乾留炉(1)の炉壁(2)は、略円筒状の胴壁部(3)と伏椀状の上壁部(4)と平板状の炉底部(5)とからなる。上壁部(4)は胴壁部(3)の上端縁に保密状に固定してあり、平面視で中央に投入口(6)が開口され、この投入口(6)が開閉可能な蓋部(7)で保密状に蓋してある。廃タイヤ等のゴム組成物からなる被熱処理物(8)は、この蓋部(7)を開いて投入口(6)から乾留炉(1)内に投入される。また、上記の上壁部(4)の肩部にはガス回収配管(9)が透設してある。このガス回収配管(9)は図外の冷却装置や気液分離装置に連結してあり、乾留により炉内の被熱処理物(8)から発生した生成ガスは、このガス回収配管(9)から回収される。   As shown in FIG. 1, the furnace wall (2) of the carbonization furnace (1) has a substantially cylindrical trunk wall (3), a prone upper wall (4), and a flat furnace bottom (5). ). The upper wall portion (4) is tightly fixed to the upper end edge of the body wall portion (3), and a loading port (6) is opened in the center in a plan view, and the loading port (6) can be opened and closed. The part (7) is covered tightly. An object to be heat-treated (8) made of a rubber composition such as a waste tire is introduced into the dry distillation furnace (1) through the inlet (6) with the lid (7) opened. Further, a gas recovery pipe (9) is provided through the shoulder of the upper wall (4). This gas recovery pipe (9) is connected to a cooling device and a gas-liquid separation device (not shown), and the generated gas generated from the heat-treated material (8) in the furnace by dry distillation is discharged from this gas recovery pipe (9). Collected.

上記の炉底部(5)は、胴壁部(3)の下端縁に対し水平方向および垂直方向へ移動可能に構成してあり、胴壁部(3)の下端開口を保密状に封止する底壁部(10)と、この底壁部(10)から側方に延設した排出部(11)とから構成される。上記の底壁部(10)には、例えば、電熱線等から成る底部加熱装置(12)が付設してある。また、上記の排出部(11)には、例えば直径が胴壁部(3)の下端開口よりも大きい開口を備えた、漏斗状の排出路(13)が上下に透設してある。乾留炉(1)内で生成された乾留チャーは、この排出路(13)から下方に配置された回収容器(14)へ排出される。   The furnace bottom portion (5) is configured to be movable in the horizontal direction and the vertical direction with respect to the lower end edge of the trunk wall portion (3), and seals the lower end opening of the trunk wall portion (3) in a tight manner. The bottom wall portion (10) and a discharge portion (11) extending laterally from the bottom wall portion (10) are configured. For example, a bottom heating device (12) made of a heating wire or the like is attached to the bottom wall (10). The discharge part (11) is provided with a funnel-shaped discharge path (13) that has an opening that is larger in diameter than the lower end opening of the body wall part (3). The dry distillation char generated in the dry distillation furnace (1) is discharged from the discharge passage (13) to a recovery container (14) disposed below.

なお、上記の炉底部(5)を水平方向および垂直方向に移動させる構成は、特定の構造や装置に限定されないが、例えば台車やレール等から成る水平移動装置と、この水平移動装置を垂直方向に動作できる油圧シリンダ等から成る垂直移動装置とから構成することが考えられる。   The configuration for moving the furnace bottom portion (5) in the horizontal direction and the vertical direction is not limited to a specific structure or device. For example, a horizontal movement device including a carriage or a rail, and the horizontal movement device in the vertical direction. It is conceivable that the apparatus is composed of a vertical movement device composed of a hydraulic cylinder or the like that can be operated in a simple manner.

上記の炉壁(2)のうち胴壁部(3)の内面には、略円筒形に形成したパネル状の第1加熱装置(15)が付設してあり、胴壁部(3)に透設された供給配管(16)と排出配管(17)とがこの第1加熱装置(15)に接続してある。この供給配管(16)と排出配管(17)は、図外の燃焼装置を介して互いに連通連結してあり、この燃焼装置で所定温度に加熱された高温の燃焼ガスが、上記の供給配管(16)を介して第1加熱装置(15)へ供給され、排出配管(17)から燃焼装置へ再循環される。   A panel-shaped first heating device (15) formed in a substantially cylindrical shape is attached to the inner surface of the body wall (3) of the furnace wall (2), and the body wall (3) is transparent. A provided supply pipe (16) and a discharge pipe (17) are connected to the first heating device (15). The supply pipe (16) and the discharge pipe (17) are connected to each other via a combustion device (not shown), and the high-temperature combustion gas heated to a predetermined temperature by the combustion device is supplied to the supply pipe ( It is supplied to the first heating device (15) via 16) and recirculated from the discharge pipe (17) to the combustion device.

上記の第1加熱装置(15)よりも内側には、略円筒形に形成したパネル状の第2加熱装置(18)が配置してあり、この第2加熱装置(18)と上記の第1加熱装置(15)とは接続配管(19)を介して互いに連通連結してある。上記の供給配管(16)から第1加熱装置(15)に供給された高温の燃焼ガスの一部が、この接続配管(19)を介して第2加熱装置(18)内を流通する。
この第1加熱装置(15)と第2加熱装置(18)内を高温の燃焼ガスが流通することにより、乾留炉(1)内に投入された前記の被熱処理物(8)が間接的に加熱される。
Inside the first heating device (15), a panel-shaped second heating device (18) formed in a substantially cylindrical shape is arranged. The second heating device (18) and the first heating device (18) are arranged. The heating device (15) is connected to each other through a connection pipe (19). Part of the high-temperature combustion gas supplied from the supply pipe (16) to the first heating device (15) flows through the second heating device (18) through the connection pipe (19).
As the high-temperature combustion gas flows through the first heating device (15) and the second heating device (18), the heat-treated material (8) charged into the dry distillation furnace (1) is indirectly indirectly collected. Heated.

上記の第1加熱装置(15)と第2加熱装置(18)との間には、上記の被熱処理物(8)を収容する収容空間(20)が形成してある。また、第2加熱装置(18)の内側には、炉内の熱気が流通する流通空間(21)が形成してある。この第2加熱装置(18)の上方には、上面が周辺に向かって下る傾斜面となった、笠状の覆い部(22)が付設してあり、この覆い部(22)により、上記の流通空間(21)への被熱処理物(8)の投入が防止されるようにしてある。   Between the first heating device (15) and the second heating device (18), an accommodation space (20) for accommodating the object to be heat treated (8) is formed. A circulation space (21) through which hot air in the furnace flows is formed inside the second heating device (18). Above this second heating device (18), a shade-like cover (22) is attached with an inclined surface whose upper surface is lowered toward the periphery. The introduction of the material to be heat-treated (8) into the circulation space (21) is prevented.

図2に示すように、上記の覆い部(22)は筒籠状の支持台(23)上端に固定してあり、この支持台(23)は4つの支持部材(24)により、上記の第2加熱装置(18)の上端に取り付けてある。この第2加熱装置(18)の上端と上記の覆い部(22)の下端縁との間には上部間隙(25)が形成してある。乾留炉(1)内の上部では、上記の収容空間(20)と流通空間(21)とがこの上部間隙(25)からなる第1連通部(26)を介して互いに連通してあり、流通空間(21)内の熱気がこの第1連通部(26)から収容空間(20)へ流出するようにしてある。   As shown in FIG. 2, the cover (22) is fixed to the upper end of a cylindrical support base (23), and the support base (23) is formed by the four support members (24). 2 is attached to the upper end of the heating device (18). An upper gap (25) is formed between the upper end of the second heating device (18) and the lower end edge of the cover (22). In the upper part in the dry distillation furnace (1), the accommodation space (20) and the distribution space (21) are in communication with each other via a first communication part (26) comprising the upper gap (25). Hot air in the space (21) flows out from the first communication part (26) to the accommodation space (20).

一方、図1に示すように、上記の第2加熱装置(18)の下端縁は、前記の底壁部(10)から僅かに持ち上げてあり、底壁部(10)との間に下部間隙(27)が形成してある。炉内の下部では、上記の収容空間(20)と流通空間(21)とがこの下部間隙(27)からなる第2連通部(28)を介して互いに連通してあり、収容空間(20)の下部の熱気の一部がこの第2連通部(28)から流通空間(21)へ流入するようにしてある。   On the other hand, as shown in FIG. 1, the lower end edge of the second heating device (18) is slightly lifted from the bottom wall (10), and the lower gap is between the bottom wall (10). (27) is formed. In the lower part of the furnace, the accommodation space (20) and the distribution space (21) communicate with each other via a second communication part (28) comprising the lower gap (27), and the accommodation space (20) Part of the hot air in the lower part of the gas flows from the second communication part (28) into the circulation space (21).

次に、上記の乾留炉により被熱処理物を乾留する手順について説明する。
最初に、炉底部(5)の底壁部(10)を胴壁部(3)の下端に保密状に装着した状態で、前記の蓋部(7)を開いて投入口(6)から被熱処理物(8)を炉内に投入する。この投入口(6)から投入された被熱処理物(8)は、覆い部(22)の上面に案内されて前記の収容空間(20)内に収容され、流通空間(21)は空洞の状態に維持される。
Next, the procedure for carbonizing the object to be heat-treated in the carbonization furnace will be described.
First, in a state where the bottom wall portion (10) of the furnace bottom portion (5) is tightly attached to the lower end of the trunk wall portion (3), the lid portion (7) is opened and the cover (6) is covered. The heat-treated product (8) is put into the furnace. The object to be heat-treated (8) introduced from the inlet (6) is guided by the upper surface of the cover (22) and accommodated in the accommodating space (20), and the distribution space (21) is in a hollow state. Maintained.

なお、上記の被熱処理物(8)が例えば廃タイヤの場合には、その廃タイヤのビードワイヤを取り除いたのちチップ状に裁断したものが用いられる。これにより、炉内で各加熱装置(12・15・18)からの熱をチップ状のゴム組成物に対してのみ伝達して十分に乾留を行うことができ、また、粒径の大きい乾留チャーの形成を防止することができる。   In addition, when said heat-treated material (8) is a waste tire, for example, it removes the bead wire of the waste tire and cuts it into a chip shape. As a result, the heat from each heating device (12, 15, 18) can be transferred only to the chip-like rubber composition in the furnace to perform dry distillation sufficiently, and the dry distillation char Can be prevented.

次に、上記の投入口(6)を蓋部(7)で蓋したのち、図外の燃焼装置から供給配管(16)と接続配管(19)を介して上記の第1加熱装置(15)と第2加熱装置(18)に高温の燃焼ガスを供給し、収容空間(20)内の被熱処理物(8)を内外から間接的に加熱する。また、前記の底壁部(10)内の底部加熱装置(12)に通電して、上記の被熱処理物(8)を下方から加熱する。   Next, after the charging port (6) is covered with a lid (7), the first heating device (15) is supplied from a combustion device (not shown) through a supply pipe (16) and a connection pipe (19). And a high-temperature combustion gas is supplied to the 2nd heating apparatus (18), and the to-be-processed object (8) in a storage space (20) is indirectly heated from the inside and outside. Moreover, it supplies with electricity to the bottom part heating apparatus (12) in the said bottom wall part (10), and heats said to-be-processed object (8) from the downward direction.

これらの加熱により上記の被熱処理物(8)から発生した生成ガスや炉内の空気は、熱気となって炉内を上昇しようとする。収容空間(20)内には被熱処理物(8)が多量に収容してあるので、上記の熱気はこの収容空間(20)内を上昇するのが容易でない。しかし、上記の流通空間(21)は空洞状態に維持されているので、収容空間(20)の下部で高温となった熱気の一部は、前記の第2連通路(28)と流通空間(21)と第1連通路(26)を順に介して、収容空間(20)の上部へ流通して循環する。これにより、上記の熱気が乾留炉(1)内の隅々にまで行き渡り、収容空間(20)内の被熱処理物(8)が効率よく均等に加熱される。   The generated gas generated from the heat-treated object (8) and the air in the furnace as a result of the heating tend to rise in the furnace as hot air. Since a large amount of the object to be heat-treated (8) is accommodated in the accommodation space (20), it is not easy for the hot air to rise in the accommodation space (20). However, since the circulation space (21) is maintained in a hollow state, a part of the hot air that has become hot at the lower part of the housing space (20) is part of the second communication passage (28) and the circulation space ( 21) and the first communication path (26) are sequentially passed to the upper portion of the accommodation space (20) and circulate. Thereby, said hot air spreads to every corner in a dry distillation furnace (1), and the to-be-processed object (8) in a storage space (20) is heated efficiently and uniformly.

上記の加熱により被熱処理物(8)から発生した生成ガスは、ガス回収用配管(9)から取り出されて、図外の冷却装置と気液分離装置で処理され、ガス成分とオイル成分に分離される。なお、得られたガス成分やオイル成分は、上記の燃焼装置の燃料として使用することができる。   The generated gas generated from the object to be heat-treated (8) by the above heating is taken out from the gas recovery pipe (9) and processed by a cooling device and a gas-liquid separation device (not shown) to be separated into gas components and oil components Is done. In addition, the obtained gas component and oil component can be used as fuel of said combustion apparatus.

上記の加熱により生成ガスが発生しきると、乾留炉(1)内に乾留チャーが残留する。この乾留チャーは、所定時間放置して炉内を冷却したのち、炉底部(5)を底壁部(10)から排出部(11)に切り替えることで、前記の排出路(13)から取り出されて前記の回収容器(14)に収容される。このとき、胴壁部(3)の内面にはパネル状の第1加熱装置(15)が配置してあるので、この乾留チャーは炉壁(2)に付着することなく、乾留炉(1)内から容易に取り出される。この取り出された乾留チャーは、上記の回収容器と共に図外の賦活処理装置へ搬送され、賦活処理されて活性炭にされる。   When the generated gas is completely generated by the above heating, the dry distillation char remains in the dry distillation furnace (1). This dry distillation char is left for a predetermined time to cool the inside of the furnace, and then the furnace bottom part (5) is switched from the bottom wall part (10) to the discharge part (11) to be taken out from the discharge passage (13). And stored in the collection container (14). At this time, since the panel-shaped first heating device (15) is arranged on the inner surface of the trunk wall (3), the carbonization char does not adhere to the furnace wall (2), and the carbonization furnace (1) Easily removed from inside. The taken-out dry distillation char is transferred to an activation processing apparatus (not shown) together with the above-described recovery container, and is activated to be activated carbon.

なお、上記の実施形態で説明した乾留炉は、本考案の技術的思想を具体化するために例示したものであって、炉壁や各加熱装置、覆い部などの形状、構造等をこれらの実施形態のものに限定するものではなく、本考案の実用新案登録請求の範囲内において種々の変更を加え得るものであり、また、被熱処理物も廃タイヤなどのゴム組成物に限定されないことはいうまでもない。   Note that the carbonization furnace described in the above embodiment is illustrated in order to embody the technical idea of the present invention, and the shape, structure, etc. of the furnace wall, each heating device, the cover, etc. It is not limited to the embodiment, and various modifications can be made within the scope of the utility model registration request of the present invention, and the heat-treated material is not limited to a rubber composition such as a waste tire. Needless to say.

例えば、上記の実施形態では第1加熱装置をパネル状に形成して炉壁の内面に付設したが、本考案では第1加熱手段を配管で構成してもよく、炉壁内に付設してもよい。
上記の第2加熱手段は円筒状に限定されず、例えば角筒状であってもよい。
上記の実施形態では第1加熱装置と第2加熱装置とを接続配管を介して互いに連通連結したが、本考案では第2の供給配管と排出配管を炉壁や第1加熱手段に透設して、この第2供給配管と排出配管を第2加熱装置に接続してもよい。
上記の底部加熱装置は、電熱線以外の加熱手段を採用することができ、また、第1加熱手段と第2加熱手段により炉内の被熱処理物を十分に加熱できる場合は、この底部加熱装置を省略することも可能である。
For example, in the above embodiment, the first heating device is formed in a panel shape and attached to the inner surface of the furnace wall. However, in the present invention, the first heating means may be configured by piping, Also good.
Said 2nd heating means is not limited to a cylindrical shape, For example, a rectangular tube shape may be sufficient.
In the above embodiment, the first heating device and the second heating device are connected in communication with each other via a connection pipe. However, in the present invention, the second supply pipe and the discharge pipe are provided through the furnace wall and the first heating means. The second supply pipe and the discharge pipe may be connected to the second heating device.
The above bottom heating device can employ a heating means other than the heating wire, and if the heat treatment object in the furnace can be sufficiently heated by the first heating means and the second heating means, this bottom heating device Can be omitted.

上記の実施形態では、第2加熱装置の上・下端と覆い部や底壁部との間の間隙で第1連通路と第2連通路を構成したので、簡単に形成することができるが、本考案ではこれらの両連通路を第2加熱手段の上部と下部に透設してもよく、或いは、第1連通路を覆い部に透設してもよい。
また上記覆い部の形状は平板状など、笠状以外の形状であってもよい。この覆い部を第2加熱装置の上端に固定する支持構造は上記の支持台に限定されず、例えば覆い部の周縁に支持部材を固定してもよい。
In the above embodiment, since the first communication path and the second communication path are configured by the gap between the upper and lower ends of the second heating device and the cover part or the bottom wall part, it can be easily formed. In the present invention, these two communication passages may be provided through the upper and lower portions of the second heating means, or the first communication passage may be provided through the cover.
Further, the shape of the covering portion may be a shape other than a shade shape such as a flat plate shape. The support structure for fixing the cover portion to the upper end of the second heating device is not limited to the above-described support base, and for example, a support member may be fixed to the periphery of the cover portion.

本考案の乾留炉は、被熱処理物を間接的に加熱して良質の炭化物や生成ガスを回収できるものでありながら、しかも被熱処理物を効率よく且つ均一に加熱できるので、廃タイヤなどのゴム組成物の乾留に特に好適であるが、他の被熱処理物の乾留にも好適に利用される。   The carbonization furnace of the present invention is capable of recovering high-quality carbides and product gas by indirectly heating the object to be heat-treated, and also efficiently and uniformly heating the object to be heat-treated, so that rubber such as waste tires can be used. Although it is particularly suitable for the dry distillation of the composition, it is also suitably used for the dry distillation of other heat-treated materials.

本考案の実施形態の、乾留炉の概略構成を示す断面図である。It is sectional drawing which shows schematic structure of the dry distillation furnace of embodiment of this invention. 本考案の実施形態の、覆い部近傍の一部破断斜視図である。It is a partially broken perspective view of a cover part vicinity of an embodiment of the present invention.

符号の説明Explanation of symbols

1…乾留炉
2…炉壁
8…被熱処理物
10…底壁部
15…第1加熱手段(第1加熱装置)
18…第2加熱手段(第2加熱装置)
20…収容空間
21…流通空間
22…覆い部
25…上部間隙
26…第1連通部
27…下部間隙
28…第2連通部
DESCRIPTION OF SYMBOLS 1 ... Carbonization furnace 2 ... Furnace wall 8 ... Material to be heat-treated
10… Bottom wall
15 ... 1st heating means (1st heating device)
18 ... second heating means (second heating device)
20 ... Containment space
21. Distribution space
22 ... cover
25… Top gap
26 ... 1st communication part
27 ... Bottom gap
28 ... Second communication part

Claims (6)

炉壁(2)の内面に沿って第1加熱手段(15)を配置するとともに、上記の炉壁(2)よりも内側に筒状の第2加熱手段(18)を配置し、この両加熱手段(15・18)にそれぞれ高温ガスを循環させて、炉内に収容した被熱処理物(8)を間接的に加熱する乾留炉であって、
上記の第2加熱手段(18)と上記の炉壁(2)との間に、上記の被熱処理物(8)を収容する収容空間(20)を形成し、
上記の第2加熱手段(18)の内側に、炉内の熱気が流通する流通空間(21)を形成するとともに、この流通空間(21)への被熱処理物(8)の投入を防止する覆い部(22)を上記の第2加熱手段(18)の上方に配置し、
上記の第2加熱手段(18)の上部とその上側の少なくともいずれかに、上記の収容空間(20)と流通空間(21)とを互いに連通する第1連通部(26)を形成したことを特徴とする、乾留炉。
The first heating means (15) is disposed along the inner surface of the furnace wall (2), and the cylindrical second heating means (18) is disposed on the inner side of the furnace wall (2). It is a dry distillation furnace for indirectly heating the material to be heat-treated (8) accommodated in the furnace by circulating high-temperature gas in each means (15, 18),
An accommodation space (20) for accommodating the object to be heat treated (8) is formed between the second heating means (18) and the furnace wall (2).
A flow space (21) through which hot air in the furnace flows is formed inside the second heating means (18), and a cover for preventing the material to be heat treated (8) from entering the flow space (21). The part (22) above the second heating means (18),
The first communication portion (26) that connects the accommodation space (20) and the circulation space (21) to each other is formed in at least one of the upper portion and the upper side of the second heating means (18). A carbonization furnace.
上記の第2加熱手段(18)と覆い部(22)との間に上部間隙(25)を形成して、この上部間隙(25)により上記の第1連通部(26)を構成した、請求項1に記載の乾留炉。   An upper gap (25) is formed between the second heating means (18) and the cover portion (22), and the first communication portion (26) is constituted by the upper gap (25). Item 2. The carbonization furnace according to Item 1. 上記の第2加熱手段(18)の下部とその下側の少なくともいずれかに、上記の収容空間(20)と流通空間(21)とを互いに連通する第2連通部(28)を形成した、請求項1に記載の乾留炉。   A second communication portion (28) for communicating the accommodation space (20) and the circulation space (21) with each other is formed at least on the lower side and the lower side of the second heating means (18). The carbonization furnace according to claim 1. 上記の第2加熱手段(18)と底壁部(10)との間に下部間隙(27)を形成して、この下部間隙(27)により上記の第2連通部(28)を構成した、請求項3に記載の乾留炉。   A lower gap (27) is formed between the second heating means (18) and the bottom wall portion (10), and the second communication portion (28) is constituted by the lower gap (27). The carbonization furnace according to claim 3. 上記の覆い部(22)の上面を、周辺に向かって下る傾斜面に形成した、請求項1に記載の乾留炉。   The dry distillation furnace according to claim 1, wherein the upper surface of the covering portion (22) is formed as an inclined surface that descends toward the periphery. 上記の第1加熱手段(15)と第2加熱手段(18)とをパネル状に形成した、請求項1から5のいずれか1項に記載の乾留炉。   The dry distillation furnace according to any one of claims 1 to 5, wherein the first heating means (15) and the second heating means (18) are formed in a panel shape.
JP2005001754U 2005-04-01 2005-04-01 Dry distillation furnace Expired - Fee Related JP3110784U (en)

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