JP2608853B2 - Carbonization furnace - Google Patents

Carbonization furnace

Info

Publication number
JP2608853B2
JP2608853B2 JP5179836A JP17983693A JP2608853B2 JP 2608853 B2 JP2608853 B2 JP 2608853B2 JP 5179836 A JP5179836 A JP 5179836A JP 17983693 A JP17983693 A JP 17983693A JP 2608853 B2 JP2608853 B2 JP 2608853B2
Authority
JP
Japan
Prior art keywords
furnace
carbonization
gas
inner furnace
water
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
JP5179836A
Other languages
Japanese (ja)
Other versions
JPH0711255A (en
Inventor
俊雄 前里
Original Assignee
俊雄 前里
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Filing date
Publication date
Application filed by 俊雄 前里 filed Critical 俊雄 前里
Priority to JP5179836A priority Critical patent/JP2608853B2/en
Publication of JPH0711255A publication Critical patent/JPH0711255A/en
Application granted granted Critical
Publication of JP2608853B2 publication Critical patent/JP2608853B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/10Biofuels, e.g. bio-diesel
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/141Feedstock
    • Y02P20/143Feedstock the feedstock being recycled material, e.g. plastics

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は、木材や古タイヤ等の廃
材などを炭化処理する炭化炉に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a carbonizing furnace for carbonizing waste materials such as wood and old tires.

【0002】[0002]

【従来の技術】従来より木材や古タイヤ等の廃材などを
乾留炉内で乾留して炭化する装置が知られている(特公
昭63−36630号など)。
2. Description of the Related Art Conventionally, there has been known a device for carbonizing waste materials such as wood and old tires by carbonizing in a carbonization furnace (Japanese Patent Publication No. 63-36630).

【0003】[0003]

【発明が解決しようとする課題】従来知られている炭化
炉は、乾留炉の底部または側部を加熱するようにしてい
るので、乾留炉全体に熱が行き渡らず、そのため処理量
が少ないという問題があった。本発明は、効率的に加熱
することができる炭化炉を提供することを課題とする。
The known carbonization furnace heats the bottom or the side of the carbonization furnace, so that the heat is not distributed to the entire carbonization furnace, and therefore the amount of treatment is small. was there. An object of the present invention is to provide a carbonization furnace that can be efficiently heated.

【0004】[0004]

【課題を解決するための手段】上記課題を解決するため
に、本発明においては、外炉の中に乾留炉である内炉を
間隙を設けて配置し、前記間隙を燃焼室にするように構
成した。
In order to solve the above problems, in the present invention, an inner furnace, which is a carbonization furnace, is arranged in the outer furnace with a gap, and the gap serves as a combustion chamber. Configured.

【0005】[0005]

【実施例】以下本発明の一実施例を図を参照して説明す
る。図1は本発明による炭化炉の一実施例を使用した炭
化装置の全体構成図である。本実施例の炭化装置は、木
材や廃材等を加熱し乾留する横長の炭化炉Aと、乾留ガ
スから水分を除去する気水分離器Bと、気水分離された
ガスから油分を分離する油分離器Cと、油分離されたガ
スを浄化するガス清浄器Dと、ガス清浄されたガスの一
部を炭化炉Aの燃料として還流させる還流装置Eとによ
って構成されている。以下、各構成部分について順に説
明する。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS One embodiment of the present invention will be described below with reference to the drawings. FIG. 1 is an overall configuration diagram of a carbonization apparatus using an embodiment of a carbonization furnace according to the present invention. The carbonization apparatus of the present embodiment includes a horizontally long carbonization furnace A that heats and dry-distills wood and waste materials, a steam separator B that removes water from dry-distilled gas, and an oil that separates oil from the steam-separated gas It comprises a separator C, a gas purifier D for purifying oil-separated gas, and a recirculation device E for recirculating a part of the gas-purified gas as fuel for the carbonization furnace A. Hereinafter, each component will be described in order.

【0006】図2は炭化炉Aの横断面図であり、この炭
化炉Aは、木材または廃材等を乾留するための円筒状の
内炉1と、内炉1の周囲を囲むように配置された外炉3
とを備えている。外炉3は台5上に固定され、外炉3の
中に内炉受け7が置かれ、この内炉受け7の上に内炉1
が截置されている。内炉1と外炉3との間は空間であっ
て、この空間が燃焼室9となっている。外炉3の外側に
は、2つの水溜缶11が外炉3を取巻くように取り付け
られている。
FIG. 2 is a cross-sectional view of the carbonizing furnace A. The carbonizing furnace A is arranged so as to surround a cylindrical inner furnace 1 for carbonizing wood or waste material and the like and a periphery of the inner furnace 1. Outer furnace 3
It has and. The outer furnace 3 is fixed on a table 5, an inner furnace receiver 7 is placed in the outer furnace 3, and the inner furnace 1 is placed on the inner furnace receiver 7.
Is installed. There is a space between the inner furnace 1 and the outer furnace 3, and this space serves as a combustion chamber 9. Two water reservoirs 11 are attached to the outside of the outer furnace 3 so as to surround the outer furnace 3.

【0007】内炉1は、耐熱性のある金属(たとえば
鉄、ステンレスなど)やセラミックなどから成る。図3
に示すように、内炉1の一端は開閉自在の蓋2になって
おり、蓋2を閉めると内炉1内を密閉できる。蓋2は内
炉1本体から完全に取り外せるようにしてもよいが、蝶
番などを使って内炉1本体に取り付けるようにしてもよ
い。また蓋2を内炉1本体にロックする方法は、特に限
定されないが、たとえば金具を使って止めてもよい。あ
るいは蓋2の内側にピンを突出させておき、内炉1本体
側にはピンと係合するL字形の溝を形成し、蓋2を内炉
1本体に嵌合させて回せば蓋2がロックされるようにし
てもよい。内炉1の底部には廃材を置くための廃材截置
板(図示せず)が配置され、この網の上に廃材を並積す
る。廃材截置板は、たとえばステンレス等の金網、耐火
れんが、セラミックなどを使用する。熱分解は廃材の上
部から始まるので図1に示すように内炉1の底部にガス
排出口23が設けられ、そこから導管25によってガス
が気水分離気Bへ導かれる。またガス排出口は必要に応
じて他にも設けてよく、他の排出口は導管27(図1)
に接続され、導管25と合流する。
The inner furnace 1 is made of a heat-resistant metal (for example, iron or stainless steel) or ceramic. Figure 3
As shown in (1), one end of the inner furnace 1 is a lid 2 that can be opened and closed, and the inside of the inner furnace 1 can be sealed by closing the lid 2. The lid 2 may be completely detachable from the inner furnace 1 main body, or may be attached to the inner furnace 1 main body using a hinge or the like. Further, the method of locking the lid 2 to the inner furnace 1 body is not particularly limited, but may be stopped by using, for example, metal fittings. Alternatively, a pin may be protruded from the inside of the lid 2 and an L-shaped groove may be formed on the inner furnace 1 main body side to engage with the pin. The lid 2 is locked by fitting the lid 2 into the inner furnace 1 main body and turning the same. May be performed. A waste material storage plate (not shown) for placing the waste material is arranged at the bottom of the inner furnace 1, and the waste materials are stacked in parallel on this net. As the waste material cutting plate, for example, a wire mesh such as stainless steel, refractory brick, ceramic, or the like is used. Since the thermal decomposition starts from the upper part of the waste material, a gas outlet 23 is provided at the bottom of the inner furnace 1 as shown in FIG. In addition, another gas outlet may be provided if necessary, and the other outlet is a conduit 27 (FIG. 1).
And merges with the conduit 25.

【0008】外炉3は、図2に示すように、金属板3a
の内側に複数の耐火れんが3bを敷き詰めて固定させた
もので、全体を4つの円弧片301,302,303,
304に分割して、それらを繋ぎ目30で繋ぎ合わせて
組み立てられる。すなわち、まず外炉の底片301を台
5の上に設置し、底片301の上に内炉受け7を配置
し、その上に内炉1を置く。内炉受け7は金属製でもよ
いが、耐火れんがやセラミックなどを使用してもよい。
次に外炉の側片302,304を底片301の両端に取
り付け、最後に上片303を側片302,304の上に
載せて外炉3が完成する。各円弧片は、たとえばボルト
や板金などを使って接続される。外炉3の端部は、図3
に示すように、蝶番によって蓋4が取り付けられ、蓋4
を閉めることによって外炉3は密閉される。外炉3が大
きくて蝶番では蓋4が支持できない場合は、外炉3のそ
ばに支柱を立て、この支柱に蓋4を開閉自在に取り付け
るようにすればよい。
As shown in FIG. 2, the outer furnace 3 has a metal plate 3a.
A plurality of refractory bricks 3b are spread all over the inside and fixed, and the whole is made up of four arc pieces 301, 302, 303,
It is divided into 304, and they are joined together at the joint 30 to be assembled. That is, first, the bottom piece 301 of the outer furnace is set on the table 5, the inner furnace receiver 7 is arranged on the bottom piece 301, and the inner furnace 1 is placed thereon. The inner furnace receiver 7 may be made of metal, but may be made of refractory brick or ceramic.
Next, the side pieces 302 and 304 of the outer furnace are attached to both ends of the bottom piece 301, and finally the upper piece 303 is placed on the side pieces 302 and 304 to complete the outer furnace 3. Each arc piece is connected using, for example, a bolt or a sheet metal. The end of the outer furnace 3 is shown in FIG.
The lid 4 is attached by a hinge as shown in FIG.
By closing the outer furnace 3, the outer furnace 3 is sealed. If the outer furnace 3 is large and the lid 4 cannot be supported by the hinge, a column may be set up near the outer furnace 3 and the lid 4 may be attached to the column so as to be freely opened and closed.

【0009】外炉3の底片301には、図1に示すよう
に、外炉の長さ方向に間隔をあけて加熱口が3個形成さ
れている。各加熱口301aの下方には燃焼バーナー1
3がそれぞれ配置され、各燃焼バーナー13には管15
によって燃料タンク17から燃料が送られる。燃焼バー
ナー13の燃焼ガスは排気筒18から外へ排出される。
燃焼バーナー13の数は炭化炉Aの長さに適宜決めると
よい。燃焼バーナー13の配置位置も内炉1の大きさに
応じて変えてよく、外炉3の下部に限らず外炉3の側部
または上部に、火口を内側に向けて設けるようにしても
よい。
As shown in FIG. 1, three heating ports are formed in the bottom piece 301 of the outer furnace 3 at intervals in the longitudinal direction of the outer furnace. A combustion burner 1 is provided below each heating port 301a.
3 are arranged, and each combustion burner 13 has a tube 15.
As a result, fuel is sent from the fuel tank 17. The combustion gas of the combustion burner 13 is discharged from the exhaust stack 18 to the outside.
The number of the combustion burners 13 may be appropriately determined according to the length of the carbonization furnace A. The arrangement position of the combustion burner 13 may be changed according to the size of the inner furnace 1, and may be provided not only at the lower part of the outer furnace 3 but also at the side or upper part of the outer furnace 3 with the crater facing inward. .

【0010】水溜缶11は内部に冷却用の水Wを収容し
た容器であって、水Wは図1に示すように給水弁19を
介して供給され、排水弁21から排出される。水溜缶1
1は外炉3に着脱自在に取り付けられ、たとえば外炉3
を補修、改修するときは水溜缶11を取り外すことがで
きる。図に示していないが、水溜缶11の上部には複数
の蒸気口が設けられ、缶内の水Wが高温になったとき前
記蒸気口から水蒸気が排気されるようになっており、そ
れにより水Wの温度は80〜100℃に保たれる。水W
が減ってきたら給水弁19から補給される。この水溜缶
11は、本発明においては必須のものではないが、炭化
炉3からの放熱を防止し、炭化炉3の温度を一定に保つ
役割を果すものである。また水溜缶11により外炉3を
保護(防錆、耐火れんがの保護など)することができ
る。また缶内の水Wは高温になっているので、排水弁2
1から排出させて暖房、風呂、温水プールなど様々に使
用することができる。
The water reservoir 11 is a container containing cooling water W therein, and the water W is supplied through a water supply valve 19 and discharged through a drain valve 21 as shown in FIG. Puddle 1
1 is detachably attached to the outer furnace 3, for example, the outer furnace 3
When repairing or repairing the water tank, the water can 11 can be removed. Although not shown in the figure, a plurality of steam ports are provided in the upper part of the water can 11 so that when the temperature of the water W in the can becomes high, steam is exhausted from the steam port, whereby The temperature of the water W is maintained at 80 to 100C. Water W
When the water consumption decreases, the water is supplied from the water supply valve 19. The water can 11 is not essential in the present invention, but serves to prevent heat radiation from the carbonization furnace 3 and keep the temperature of the carbonization furnace 3 constant. Further, the water can 11 can protect the outer furnace 3 (anticorrosion, protection of refractory bricks, etc.). Since the water W in the can is hot, the drain valve 2
It can be discharged from 1 and used for various purposes such as heating, bath, heated pool, etc.

【0011】気水分離器B内には多数のセパレート板4
1(金属製)がガスの流れを妨げるように設置され、ガ
ス流は分離器Bの上部および下部を水平方向に流れる。
ガス中の水蒸気は、その途中で仕切板41に衝突して凝
結し、貯水タンク43に回収される。気水分離器Bの上
流側のガス管25は、気水分離器Bの上側に付けてある
が、下側に付けて、ガスを仕切板41の間をくぐらせる
ようにしてもよい。
In the steam separator B, a number of separate plates 4 are provided.
1 (made of metal) is installed so as to obstruct the gas flow, and the gas flow flows in the upper and lower parts of the separator B in the horizontal direction.
The water vapor in the gas collides with the partition plate 41 on the way and condenses, and is collected in the water storage tank 43. Although the gas pipe 25 on the upstream side of the steam separator B is attached to the upper side of the steam separator B, the gas pipe 25 may be attached to the lower side to allow the gas to pass between the partition plates 41.

【0012】油分離器C内には、ジャマ板45が取り付
けられ、ジャマ板45には、ガスの通り穴が形成されて
いるが、隣り合う穴同士の高さは異なり、ガスはジャマ
板45にぶつかって上下動しながら移動する。図示して
いなが、油分離器Cの外周は冷却水の入った冷却器で取
巻かれている。分離された油はタンク47に貯蔵され
る。
A baffle plate 45 is mounted in the oil separator C, and a hole for gas is formed in the baffle plate 45. The height of adjacent holes is different. It bumps into and moves up and down. Although not shown, the outer circumference of the oil separator C is surrounded by a cooler containing cooling water. The separated oil is stored in the tank 47.

【0013】ガス清浄器D内には、活性炭49が配置さ
れている。活性炭49の中心部はガス通道になってい
て、清浄および脱臭されたガスはガス通道51から次工
程へ排出される。52は余水貯タンクである。
Activated carbon 49 is disposed in the gas purifier D. The central part of the activated carbon 49 serves as a gas passage, and the cleaned and deodorized gas is discharged from the gas passage 51 to the next step. 52 is a spill storage tank.

【0014】還流装置Eは、第1ガス受タンク53と、
ブロア55と、第2ガス受タンク57とから構成されて
いる。ブロア55によって第1ガス受タンク53を真空
にして、そこにガスを導入する。そして第2ガス受57
においてガスを調製して管59を介して燃焼バーナー1
3へ送り完全燃焼させる。ガスは、還流装置Eへ送られ
ない場合は排気管61より外部へ排出される。
The recirculation device E includes a first gas receiving tank 53,
It is composed of a blower 55 and a second gas receiving tank 57. The first gas receiving tank 53 is evacuated by the blower 55 and gas is introduced therein. And the second gas receiver 57
Gas is prepared in the combustion burner 1 through a pipe 59
Send to 3 for complete combustion. When the gas is not sent to the recirculation device E, the gas is exhausted from the exhaust pipe 61 to the outside.

【0015】次に上記装置の動作について説明する。ま
ず廃材を内炉1に入れて内炉1、外炉3の蓋を閉じ燃焼
バーナー13に点火する。3時間ほどで水蒸気、水分を
含む白色煙(75〜80℃程度)が発生する。5時間
後、炭化が始まりガスは白色煙から淡褐色煙(120℃
程度)に変わる。この間、ガスは導管25,27から気
水分離器Bへ送られて水分を除去され、油分離器Cで油
分を除去され、ガス清浄器Dで清浄、脱臭され、還流装
置Eへ送られる。ガスは還流装置Eから燃焼バーナー1
3へ送られて完全燃焼する。開始後6時間でガスは白色
に黒色のまじった煙(120℃程度)に変わり、7時間
後うす紫色煙(150℃)になり、10時間後混じり紫
煙(150℃)となって終る。その後内炉1から炭化物
を取り出す。廃材を炭化するときに発生するガスを冷却
すれば多量の木酢が取れる。
Next, the operation of the above device will be described. First, the waste material is put into the inner furnace 1, the lids of the inner furnace 1 and the outer furnace 3 are closed, and the combustion burner 13 is ignited. White smoke (about 75 to 80 ° C.) containing water vapor and water is generated in about 3 hours. After 5 hours, carbonization begins and the gas turns from white smoke to light brown smoke (120 ° C).
Degree). During this time, the gas is sent from the conduits 25 and 27 to the steam separator B to remove the water content, the oil separator C removes the oil content, the gas purifier D cleans and deodorizes and is sent to the reflux device E. The gas is supplied from the recirculation device E to the combustion burner 1
It is sent to 3 and burns completely. At 6 hours after the start, the gas changes to white and black mixed smoke (about 120 ° C.), after 7 hours becomes light purple smoke (150 ° C.), and after 10 hours, it becomes mixed purple smoke (150 ° C.) and ends. After that, carbide is taken out from the inner furnace 1. A large amount of wood vinegar can be obtained by cooling the gas generated when carbonizing the waste material.

【0016】以上のように、上記装置を用いれば、内炉
1は燃焼室9に完全に囲まれているので、効率よく加熱
することができる。また上記装置は横に長くなっている
ので、長い材料でも簡単に横から出し入れできる。
As described above, by using the above-described apparatus, the inner furnace 1 is completely surrounded by the combustion chamber 9, so that the heating can be performed efficiently. Further, since the above device is elongated in the lateral direction, even a long material can be easily taken in and out from the lateral direction.

【0017】図4は本発明の第2の実施例を示し、この
実施例においては、内炉を移動式にした。すなわち、台
5の中央部を移動台51として他の部分から切り離し、
キャスター52を付けて移動可能にし、移動台51上に
外炉1の底部305を固定する。内炉1は第1の実施例
と同様に内炉受け7を介して底部305上に截置され
る。炭化終了後は外炉3の蓋4を開けて、移動台51を
内炉1とともに引き出し、次に内炉1の蓋2を開けて中
の炭化物を取り出す。この実施例の炭化炉を使用すれ
ば、長くて大型の材料でも楽に処理できる。なお、移動
台51と台5本体との間にわずかの隙間ができるが、こ
の場合は、移動台51に横に伸びる板材を取り付けて、
この板材によって、前記隙間から火が漏れないように隙
間を覆うようにするのが望ましい。上記第2の実施例に
おいて、外炉3の蓋4の他に外炉3の後端に蓋を設ける
ようにしてもよい。そして、たとえば内炉を別にもう1
つ用意してその中に材料を入れて外炉の後方で待機させ
ておき、1つの内炉が終了して外炉の前蓋から前方へ取
り出されたら、外炉の後蓋を開けて待機していた別の内
炉を外炉内へ挿入する。このようにすれば、内炉の入替
えが即座にでき、連続的に炭化作業を行うことができて
効率が良い。たとえば24時間のうち2回も炭化ができ
るようになる。
FIG. 4 shows a second embodiment of the present invention, in which the inner furnace is movable. That is, the center of the table 5 is separated from other parts as the moving table 51,
The caster 52 is attached so as to be movable, and the bottom portion 305 of the outer furnace 1 is fixed on the moving table 51. The inner furnace 1 is cut on the bottom 305 via the inner furnace receiver 7 as in the first embodiment. After the carbonization is completed, the lid 4 of the outer furnace 3 is opened, the movable table 51 is pulled out together with the inner furnace 1, and then the lid 2 of the inner furnace 1 is opened to remove the carbide therein. Using the carbonization furnace of this embodiment, long and large materials can be easily processed. Note that a slight gap is formed between the moving table 51 and the table 5 main body. In this case, a horizontally extending plate material is attached to the moving table 51,
It is preferable that the plate material covers the gap so that fire does not leak from the gap. In the second embodiment, in addition to the lid 4 of the outer furnace 3, a lid may be provided at the rear end of the outer furnace 3. And, for example, another inner furnace
Prepare the material, put the material in it and wait at the back of the outer furnace. When one inner furnace is finished and taken out from the front lid of the outer furnace, open the rear lid of the outer furnace and wait Insert another inner furnace into the outer furnace. In this way, the inner furnace can be replaced immediately, and the carbonization work can be performed continuously, which is efficient. For example, carbonization can be performed twice in 24 hours.

【0018】図5は第3の実施例を示し、この実施例に
おいては、炭化炉を縦型にした。すなわち、この炭化炉
は、縦型の内炉71と、同じく縦型の外炉73とを備
え、外炉73の上部には支持棒75が設けられ、この支
持棒75に吊り棒77によって内炉71が吊り下げられ
ている。そして内炉71と外炉73との間に燃焼室79
が形成される。内炉71、外炉73の上部には、蓋8
1,83がそれぞれ取り付けられて開閉自在となってい
る。なお図5において第1の実施例と同様の部分には同
じ番号を付してある。この第3実施例の炭化炉は小さい
材料を炭化するのに適している。
FIG. 5 shows a third embodiment, in which the carbonization furnace is of a vertical type. That is, the carbonization furnace includes a vertical inner furnace 71 and a vertical outer furnace 73, and a support rod 75 is provided on the upper portion of the outer furnace 73. The furnace 71 is suspended. A combustion chamber 79 is provided between the inner furnace 71 and the outer furnace 73.
Is formed. A lid 8 is provided on top of the inner furnace 71 and the outer furnace 73.
1, 83 are attached respectively and can be opened and closed. In FIG. 5, the same parts as those in the first embodiment are denoted by the same reference numerals. The carbonization furnace of the third embodiment is suitable for carbonizing small materials.

【0019】[0019]

【発明の効果】以上説明したように、本発明によれば、
乾留炉である内炉の周囲すべてが加熱されるので、廃材
等を極めて効率的にかつ大量に炭化処理できるという効
果が得られる。
As described above, according to the present invention,
Since the entire circumference of the inner furnace, which is a dry distillation furnace, is heated, the effect that the waste material can be carbonized very efficiently and in large quantities can be obtained.

【図面の簡単な説明】[Brief description of the drawings]

【図1】本発明による炭化炉の一実施例を用いた炭化装
置の全体構成を示す概略図である。
FIG. 1 is a schematic diagram showing an overall configuration of a carbonization apparatus using an embodiment of a carbonization furnace according to the present invention.

【図2】図1の装置に用いる炭化炉の拡大横断面図であ
る。
FIG. 2 is an enlarged cross-sectional view of a carbonization furnace used in the apparatus of FIG.

【図3】炭化炉を一部切り欠いて示した斜視図である。FIG. 3 is a perspective view showing a carbonization furnace with a part cut away.

【図4】本発明の第2実施例を示す斜視図である。FIG. 4 is a perspective view showing a second embodiment of the present invention.

【図5】本発明の第3の実施例を示す斜視図である。FIG. 5 is a perspective view showing a third embodiment of the present invention.

【符号の説明】[Explanation of symbols]

1 内炉 3 外炉 9 燃焼室 1 inner furnace 3 outer furnace 9 combustion chamber

Claims (4)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 外炉の中に乾留炉である内炉を間隙を設
けて配置し、前記間隙を燃焼室とし、前記外炉および内
炉を横長形状とし、前記外炉および内炉にその長さ方向
に材料を出し入れするための開閉部を設けた炭化炉にお
いて、前記外炉の一部を構成する移動台を設け、前記移
動台上に前記内炉を截置し、前記移動台を移動させるこ
とにより前記内炉を移動可能にしたことを特徴とする炭
化炉。
1. An inner furnace, which is a carbonization furnace, is arranged in the outer furnace with a gap, the gap serves as a combustion chamber, and the outer furnace and the inner furnace have a horizontally long shape. In a carbonization furnace provided with an opening / closing part for loading and unloading the material in the length direction, a moving table forming a part of the outer furnace is provided, and the inner furnace is placed on the moving table, and the moving table is A carbonization furnace, wherein the inner furnace is made movable by moving the inner furnace.
【請求項2】 前記移動台の移動により前記内炉を前記
外炉から取り出し可能にした請求項1に記載の炭化炉。
2. The carbonization furnace according to claim 1, wherein the inner furnace can be taken out of the outer furnace by moving the moving table.
【請求項3】 前記外炉の両端に開閉部を設けた請求項
2に記載の炭化炉。
3. The carbonization furnace according to claim 2, wherein opening and closing portions are provided at both ends of the outer furnace.
【請求項4】 前記外炉の外周に保温手段を設けた請求
項1ないし3のいずれか1項に記載の炭化炉。
4. The carbonization furnace according to claim 1, wherein a heat retaining means is provided on an outer periphery of said outer furnace.
JP5179836A 1993-06-25 1993-06-25 Carbonization furnace Expired - Fee Related JP2608853B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5179836A JP2608853B2 (en) 1993-06-25 1993-06-25 Carbonization furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5179836A JP2608853B2 (en) 1993-06-25 1993-06-25 Carbonization furnace

Publications (2)

Publication Number Publication Date
JPH0711255A JPH0711255A (en) 1995-01-13
JP2608853B2 true JP2608853B2 (en) 1997-05-14

Family

ID=16072751

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5179836A Expired - Fee Related JP2608853B2 (en) 1993-06-25 1993-06-25 Carbonization furnace

Country Status (1)

Country Link
JP (1) JP2608853B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102559222A (en) * 2012-02-17 2012-07-11 北京神雾环境能源科技集团股份有限公司 Low-temperature dry distillation furnace

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6395152B1 (en) * 1998-07-09 2002-05-28 Acm Research, Inc. Methods and apparatus for electropolishing metal interconnections on semiconductor devices
US6669822B1 (en) 1998-10-28 2003-12-30 Ebara Corporation Method for carbonizing wastes
KR100920741B1 (en) * 2007-12-17 2009-10-07 강원대학교산학협력단 Heat exchanging apparatus using waste energy of charcoal kiln

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5247922B2 (en) * 1975-02-17 1977-12-06
JPS5944351B2 (en) * 1981-11-16 1984-10-29 章 脇本 Treatment method for waste mainly consisting of organic matter
JPH01132688A (en) * 1987-11-18 1989-05-25 Yukio Miyazaki Gasification device for combustible solid
JPH01193391A (en) * 1988-01-28 1989-08-03 Mokuzai Tanka Seibun Tayouto Riyou Gijutsu Kenkyu Kumiai Assembling type carbonization furnace

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102559222A (en) * 2012-02-17 2012-07-11 北京神雾环境能源科技集团股份有限公司 Low-temperature dry distillation furnace

Also Published As

Publication number Publication date
JPH0711255A (en) 1995-01-13

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