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JP2008106221A - Carbonization apparatus - Google Patents

Carbonization apparatus Download PDF

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JP2008106221A
JP2008106221A JP2007094238A JP2007094238A JP2008106221A JP 2008106221 A JP2008106221 A JP 2008106221A JP 2007094238 A JP2007094238 A JP 2007094238A JP 2007094238 A JP2007094238 A JP 2007094238A JP 2008106221 A JP2008106221 A JP 2008106221A
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carbonization
carbonized
carburized
conveying
carbide
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Hiroe Muramatsu
弘恵 村松
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Shinten Kogyo KK
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Shinten Kogyo KK
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Priority to JP2007094238A priority Critical patent/JP2008106221A/en
Priority to KR1020070066384A priority patent/KR20080030466A/en
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    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B32/00Carbon; Compounds thereof
    • C01B32/90Carbides
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J6/00Heat treatments such as Calcining; Fusing ; Pyrolysis
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10BDESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B53/00Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form
    • C10B53/02Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form of cellulose-containing material
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
    • C10L5/00Solid fuels
    • C10L5/40Solid fuels essentially based on materials of non-mineral origin
    • C10L5/44Solid fuels essentially based on materials of non-mineral origin on vegetable substances
    • 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
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/30Fuel from waste, e.g. synthetic alcohol or diesel

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Inorganic Chemistry (AREA)
  • Processing Of Solid Wastes (AREA)
  • Coke Industry (AREA)

Abstract

<P>PROBLEM TO BE SOLVED: To provide a new carbonization apparatus which exhibits unprecedented workings. <P>SOLUTION: The carbonization apparatus heats and carbonizes materials to be carbonized 1 and is provided with material transportation and carbonization part 3 of a specific length in which the materials to be carbonized 1 are carbonized while they are being transported. The material transport and carbonization part 3 has material-dropping means 4 which drops the materials to be carbonized 1 during the process of the carbonization and material guide means 5 which guides the lighter materials to be carbonized 1 out of the materials to be carbonized 1 fallen by the material-dropping means 4 or in the process of falling for a longer distance in the direction of transport than the heavier materials to be carbonized 1 and discharges them from the material transport and carbonization part 3. <P>COPYRIGHT: (C)2008,JPO&INPIT

Description

本発明は、被炭化物を加熱して炭化する炭化装置に関するものである。   The present invention relates to a carbonization apparatus for heating and carbonizing an object to be carbonized.

例えば廃棄物を加熱させて炭とする炭化装置として、例えば特開平10−17311号や特開2006−104284号に開示される炭化装置(以下、従来例という。)が提案されている。   For example, carbonization apparatuses (hereinafter referred to as conventional examples) disclosed in, for example, JP-A-10-17311 and JP-A-2006-104284 have been proposed as carbonization apparatuses that heat waste to make charcoal.

この従来例は、低酸素雰囲気に保った炭化管を炭化炉内に略水平に設置し、スクリューコンベヤで搬送する被炭化物を炭化管の外部から加熱して乾留することで炭を得る構造である。   This conventional example is a structure in which a carbonized tube maintained in a low oxygen atmosphere is installed substantially horizontally in a carbonization furnace, and the carbonized material conveyed by the screw conveyor is heated from the outside of the carbonized tube and dry-distilled to obtain charcoal. .

この従来例であれば、被炭化物に直接火炎を接触させることなく炭化作業が行なわれる為、被炭化物が灰になってしまうのを可及的に防止して良質な炭を作出することができるとされる。このようにして作出された炭は、燃料としての利用に限らず、土壌改良材など様々な分野において有効利用される。   In the case of this conventional example, since the carbonization work is performed without bringing the carbonized material into direct contact with the flame, it is possible to prevent the carbonized material from becoming ash as much as possible and to produce good quality charcoal. It is said. The charcoal produced in this way is not limited to use as a fuel, but is effectively used in various fields such as soil improvement materials.

特開平10−17311号公報JP-A-10-17311 特開2006−104284号公報JP 2006-104284 A

ところで、被炭化物を炭化する場合、その種類(素材、大きさ、水分含有量などの様々な条件)によって炭化するまでの加熱時間は異なることになるが、これに対し、前述した従来例は、被炭化物の種類に応じてスクリューコンベヤの搬送速度を可変させて加熱時間を変化させることで対応している。   By the way, when carbonizing the object to be carbonized, the heating time until carbonization depends on the type (various conditions such as material, size, moisture content, etc.). This is done by changing the heating time by changing the conveying speed of the screw conveyor according to the type of carbide.

しかし、従来例は、種類の異なる被炭化物が混じっていた場合には良好な処理が行えない。即ち、例えば水分含有量の異なる複数種類の被炭化物を処理する場合、仮に水分含有量の多い被炭化物に合わせた設定により処理する場合には、スクリューコンベヤの搬送速度を遅くして加熱時間を長めにすることになり、水分含有量の少ない被炭化物は灰となって排出部から排出されることになり、反対に、水分含有量の少ない被炭化物に合わせた設定により処理する場合には、スクリューコンベヤの搬送速度を早くして加熱時間を短めにすることになり、水分含有量の多い被炭化物は半焼け(半生状態)のまま排出部から排出されることになる。   However, the conventional example cannot perform good treatment when different types of carbides are mixed. That is, for example, when processing a plurality of types of carbides having different moisture contents, if processing is performed according to settings corresponding to the carbides having a high moisture content, the heating time is increased by slowing the screw conveyor conveyance speed. If the material to be carbonized with a low water content becomes ash, it will be discharged from the discharge part. The conveying speed of the conveyor is increased to shorten the heating time, and the carbonized material having a high water content is discharged from the discharge portion while being semi-burned (semi-lived state).

従って、従来例は、同じ種類の被炭化物しか処理できないという問題点があり、仮に同じ種類の被炭化物であっても大きさの違いや水分含有量の違いなど条件が異なる場合は多々あり、良質な炭が安定的に得られないという問題点がある。   Therefore, the conventional example has a problem that only the same type of carbide can be processed, and even if the same type of carbide, there are many cases where the conditions such as the difference in size and moisture content are different, and the quality is high. There is a problem that stable charcoal cannot be obtained stably.

本発明は、上述した問題点に鑑み、従来にない作用効果を発揮する画期的な炭化装置を提供するものである。   In view of the above-described problems, the present invention provides an epoch-making carbonization device that exhibits unprecedented effects.

添付図面を参照して本発明の要旨を説明する。   The gist of the present invention will be described with reference to the accompanying drawings.

被炭化物1を加熱して炭化する炭化装置であって、前記被炭化物1を搬送しながら炭化する所定長の被炭化物搬送炭化部3を有し、この被炭化物搬送炭化部3は、炭化途時の前記被炭化物1を落下させる被炭化物落下手段4と、この被炭化物落下手段4により落下する落下途時若しくは落下した前記被炭化物1のうち、重量の軽い前記被炭化物1を重量の重い前記被炭化物1よりも長い距離だけ搬送方向に誘導して前記被炭化物搬送炭化部3から導出する被炭化物誘導手段5とを具備することを特徴とする炭化装置に係るものである。   A carbonization apparatus that heats and carbonizes the object to be carbonized 1, and has a carbonized object conveying carbonization part 3 having a predetermined length that carbonizes the object 1 while conveying the object 1, and The to-be-carburized object dropping means 4 for dropping the to-be-carburized object 1 and the to-be-carburized object 1 falling by the to-be-carburized object dropping means 4 or the falling to-be-carburized object 1 The present invention relates to a carbonization apparatus comprising: a carbide guiding means 5 that is guided in a conveying direction by a distance longer than that of the carbide 1 and is derived from the carbide conveying carbonization unit 3.

また、請求項1記載の炭化装置において、前記被炭化物落下手段4は、前記被炭化物1を所定高さ位置に上げた後に搬送方向若しくは逆搬送方向に斜め落下せしめるように構成されたものであることを特徴とする炭化装置に係るものである。   Further, in the carbonization apparatus according to claim 1, the carbide dropping means 4 is configured to drop the carbide 1 in a conveying direction or a reverse conveying direction after raising the carbide 1 to a predetermined height position. This relates to a carbonizing apparatus characterized by the above.

また、請求項1,2いずれか1項に記載の炭化装置において、前記被炭化物誘導手段5は、前記被炭化物搬送炭化部3内を搬送方向に流下する空気流であることを特徴とする炭化装置に係るものである。   The carbonization apparatus according to any one of claims 1 and 2, wherein the to-be-carburized guidance means 5 is an air flow that flows down in the to-be-carburized carrying carbonization section 3 in the carrying direction. It concerns the device.

また、請求項1〜3いずれか1項に記載の炭化装置において、前記被炭化物搬送炭化部3は、筒状の回転体25であることを特徴とする炭化装置に係るものである。   Moreover, the carbonization apparatus of any one of Claims 1-3 WHEREIN: The said to-be-carburized conveyance carbonization part 3 is the cylindrical rotary body 25, It concerns on the carbonization apparatus characterized by the above-mentioned.

また、請求項4記載の炭化装置において、前記被炭化物落下手段4は、前記回転体25の内面に設けられ、先端側ほど搬送方向且つ内方へ突出して傾斜する送り羽根体6と、この送り羽根体6の対向位置に設けられ該送り羽根体6と傾斜方向が反対となる戻し羽根体7とで構成されるものであることを特徴とする炭化装置に係るものである。   5. The carbonization apparatus according to claim 4, wherein the carbide dropping means 4 is provided on the inner surface of the rotating body 25, and the feed blade body 6 that protrudes inward in the transport direction and inclines toward the tip side, and the feed blade body 6. The carbonization apparatus is characterized by comprising a feed blade body 6 provided at a position opposed to the blade body 6 and a return blade body 7 whose inclination direction is opposite.

また、請求項1〜5いずれか1項に記載の炭化装置において、前記被炭化物搬送炭化部3は、前記被炭化物落下手段4及び前記被炭化物誘導手段5により前記被炭化物1を搬送しながら炭化して該被炭化物搬送炭化部3から導出するものであることを特徴とする炭化装置に係るものである。   Moreover, the carbonization apparatus of any one of Claims 1-5 WHEREIN: The said to-be-carburized conveyance carbonization part 3 is carbonized, conveying the said to-be-carburized 1 by the said to-be-carburized dropping means 4 and the said to-be-carbide to-be-carburized means 5. Thus, the carbonization apparatus is characterized in that it is derived from the carbonized article transport carbonization section 3.

また、請求項5,6いずれか1項に記載の炭化装置において、前記対向する送り羽根体6と戻し羽根体7は複数並設されていることを特徴とする炭化装置に係るものである。   Moreover, the carbonization apparatus of any one of Claims 5 and 6 concerns the carbonization apparatus characterized in that a plurality of the opposed feed blade bodies 6 and return blade bodies 7 are arranged in parallel.

また、請求項1〜7いずれか1項に記載の炭化装置において、前記被炭化物搬送炭化部3内にして前記被炭化物落下手段4が設けられる部位よりも下流側部位には、前記被炭化物1を強制搬送する強制搬送手段8が設けられていることを特徴とする炭化装置に係るものである。   Moreover, the carbonization apparatus of any one of Claims 1-7 WHEREIN: In the downstream part rather than the site | part in which the said to-be-carbide falling means 4 is provided in the to-be-carburized conveyance carbonization part 3, the said to-be-carbide 1 The carbonization apparatus is characterized by being provided with a forcible transport means 8 for forcibly transporting.

また、請求項8記載の炭化装置において、前記強制搬送手段8は、前記被炭化物1を低速で搬送する低速搬送領域8Aと、この低速搬送領域8Aよりも下流側に位置し、該低速領域8Aよりも前記被炭化物1を搬送する速度が速い高速搬送領域8Bとが設けられていることを特徴とする炭化装置に係るものである。   Further, in the carbonization apparatus according to claim 8, the forced conveying means 8 is located at a low speed conveyance area 8A for conveying the article 1 to be carbonized at a low speed, and downstream of the low speed conveyance area 8A, and the low speed area 8A. And a high-speed transfer region 8B having a higher speed for transferring the article 1 to be carbide is provided.

また、請求項9記載の炭化装置において、前記強制搬送手段8は、先端側ほど搬送方向且つ内方へ突出して傾斜する螺旋状の送り羽根体9A,9Bであり、前記低速搬送領域8Aと前記高速搬送領域8Bとにおいて、前記送り羽根体9A,9Bの傾斜度合は異なるように設定されていることを特徴とする炭化装置に係るものである。   Further, in the carbonization apparatus according to claim 9, the forced conveying means 8 is a spiral feed blade body 9A, 9B that protrudes inward and inclines toward the distal end side, and the low-speed conveying region 8A and the In the high-speed conveyance area 8B, the inclination degree of the feeding blade bodies 9A and 9B is set to be different from each other.

本発明は上述のように構成したから、極めて効率の良い炭化処理が行われ、高品位な炭が確実且つ安定的に得られることになるなど従来にない作用効果を発揮する画期的な炭化装置となる。   Since the present invention is configured as described above, an extremely efficient carbonization treatment is performed, and an innovative carbonization that exhibits unprecedented effects such as high-quality charcoal can be obtained reliably and stably. It becomes a device.

好適と考える本発明の実施形態を、図面に基づいて本発明の作用を示して簡単に説明する。   An embodiment of the present invention which is considered to be suitable will be briefly described with reference to the drawings showing the operation of the present invention.

被炭化物1は被炭化物搬送炭化部3で搬送されながら炭化し炭となる。   The to-be-carburized object 1 is carbonized and becomes charcoal while being conveyed by the to-be-carburized object conveying carbonization unit 3.

ところで、本発明の被炭化物搬送炭化部3は、炭化途時の被炭化物1を落下させる被炭化物落下手段4と、この被炭化物落下手段4により落下する落下途時若しくは落下した被炭化物1のうち、重量の軽い被炭化物1を重量の重い被炭化物1よりも長い距離だけ搬送方向に誘導して該被炭化物搬送炭化部3から導出する被炭化物誘導手段5を具備しており、この構成から画期的な作用効果を呈することになる。   By the way, the to-be-carburized conveyance carbonization part 3 of the present invention includes a to-be-carburized dropping means 4 for dropping the to-be-carburized 1 at the time of carbonization, and a to-be-fallen or dropped to-be-falling to-be-carbide 1 by the to-be-carburized dropping means 4. And a carbide guiding means 5 for guiding the light-weight to-be-carbide 1 in the conveying direction by a longer distance than the heavy-to-be-carburized 1 and deriving from the to-be-carburized conveying carbonized portion 3. It will exhibit a periodical effect.

具体的には、前述したように従来例は種類(水分含有量)の異なる被炭化物1を処理しようとした際、この種類の異なる被炭化物1同士が同時に搬送されることになる為に問題点が生じていたが、この点、本発明は、被炭化物搬送炭化部3に前述した被炭化物落下手段4及び被炭化物誘導手段5を具備せしめたから、例えば水分含有量が多くて重量の重い被炭化物1はじっくり加熱され、一方、水分含有量が少なくて重量の軽い被炭化物1は早めに加熱されながら早く搬送される。つまり、被炭化物1のうち軽いものから被炭化物搬送炭化部3の下流側へ搬送される。   Specifically, as described above, in the conventional example, when the carbides 1 having different types (moisture contents) are to be processed, the different types of carbides 1 are simultaneously conveyed. However, since the present invention includes the above-described carbide dropping means 4 and the carbide guiding means 5 in the carbide conveying carbonization section 3, for example, the carbide to be carbide having a high water content and a heavy weight. 1 is carefully heated, while the light-weight to-be-carburized object 1 with a low water content is conveyed early while being heated early. That is, it is conveyed from the light thing among the to-be-carburized objects 1 to the downstream side of the to-be-carburized object conveying carbonization part 3.

従って、常に被炭化物1の種類に対応した加熱が行なわれることになり極めて効率の良い炭化処理が行われ、高品位な炭が確実且つ安定的に得られることになる。   Therefore, heating corresponding to the type of the object to be carbide 1 is always performed, and an extremely efficient carbonization process is performed, so that high-quality charcoal can be obtained reliably and stably.

本発明の具体的な実施例について図面に基づいて説明する。   Specific embodiments of the present invention will be described with reference to the drawings.

本実施例は、被炭化物1を加熱して炭化する炭化装置であって、前記被炭化物1を搬送しながら炭化する所定長の被炭化物搬送炭化部3を有し、この被炭化物搬送炭化部3は、炭化途時の前記被炭化物1を落下させる被炭化物落下手段4と、この被炭化物落下手段4により落下する落下途時若しくは落下した前記被炭化物1のうち、重量の軽い前記被炭化物1を重量の重い前記被炭化物1よりも長い距離だけ搬送方向に誘導して前記被炭化物搬送炭化部3から導出する被炭化物誘導手段5とを具備するものである。   The present embodiment is a carbonization apparatus that heats and carbonizes the object to be carbonized 1, and has a carbonized object conveying carbonization part 3 of a predetermined length that carbonizes while conveying the object 1, and this object conveying carbonization part 3. Is a carbide dropping means 4 for dropping the carbide 1 during carbonization, and the carbide 1 having a light weight among the carbides 1 dropped or dropped by the carbide dropping means 4. And a to-be-carburized material guiding means 5 for guiding from the to-be-carburized material-conveying carbonized portion 3 by guiding the material in the conveying direction by a distance longer than that of the heavy material-to-be-carburized 1.

具体的には、加熱室2は、図1に図示したように適宜な金属製の部材で形成された箱状基体10の内空間であり、基体10の所定位置に設けたバーナー装置11で後述する被炭化物搬送炭化部3を加熱するように構成されている。尚、本実施例は、加熱室2を密閉空間とすることで低酸素雰囲気中で炭化処理を行うバッジ式炭化装置として構成されている。   Specifically, the heating chamber 2 is an inner space of a box-like base 10 formed of an appropriate metal member as shown in FIG. 1 and is described later with a burner device 11 provided at a predetermined position of the base 10. It is comprised so that the to-be-carburized object conveyance carbonization part 3 to be heated may be heated. In addition, a present Example is comprised as a badge type carbonization apparatus which carbonizes in a low-oxygen atmosphere by making the heating chamber 2 into a sealed space.

また、加熱室2には被炭化物1を搬送する被炭化物搬送炭化部3が設けられている。   In addition, the heating chamber 2 is provided with a to-be-carburized transport carbonization unit 3 that transports the to-be-carburized 1.

この被炭化物搬送炭化部3は、図1に図示したように駆動装置12の駆動により回転して被炭化物1を内部において搬送し且つ加熱室2内の熱により炭化せしめる構成である。   As shown in FIG. 1, the to-be-carburized material conveying carbonization unit 3 is configured to rotate by driving the driving device 12 to convey the to-be-carburized material 1 inside and carbonize it by the heat in the heating chamber 2.

具体的には、図1に図示したように基体10の左右側壁10a,10b間に水平状態で架設され加熱室2内に配される金属管状の回転体25を設け、この回転体25の基端部に駆動装置12から延設されるチェーン15が巻回されるスプロケット16が設けられており、この駆動装置12の駆動により回転体25は回転自在に設けられている。   Specifically, as shown in FIG. 1, a metal tubular rotator 25 is provided between the left and right side walls 10 a and 10 b of the base 10 in a horizontal state and arranged in the heating chamber 2. A sprocket 16 around which a chain 15 extending from the driving device 12 is wound is provided at the end, and the rotating body 25 is rotatably provided by the driving of the driving device 12.

また、回転体25の基端部は、炭化処理により生じた蒸気を蒸気抜きパイプ20に逃がすための蒸気抜き部に設定され、回転体25の先端部は、加熱されて炭化処理済みの炭を排出し且つ一次燃焼ガス(Coを含んだ可燃性ガス)をガス抜きパイプ19へ排出する排出部に設定されている。   Further, the base end of the rotating body 25 is set as a steam vent for releasing the steam generated by the carbonization treatment to the steam vent pipe 20, and the tip of the rotating body 25 is heated and carbonized. It is set in a discharge section that discharges and discharges the primary combustion gas (a combustible gas containing Co) to the degassing pipe 19.

また、回転体25の基端側には、該回転体25の回転を伴い被炭化物1を所定高さ位置に上げた後に搬送方向若しくは逆搬送方向に斜め落下せしめる被炭化物落下手段4が設けられている。   Further, on the base end side of the rotating body 25, there is provided a carbide dropping means 4 for causing the carbide 1 to be raised to a predetermined height position with the rotation of the rotating body 25 and then obliquely dropping in the conveying direction or the reverse conveying direction. ing.

この被炭化物落下手段4は、回転体25の内面に設けられ、先端側ほど搬送方向且つ内方へ突出して傾斜する送り羽根体6と、この送り羽根体6の対向位置に設けられ該送り羽根体6と傾斜方向が反対となる戻し羽根体7とが複数並設された構成である。   The carbide dropping means 4 is provided on the inner surface of the rotating body 25, and is provided at a position opposite to the feed blade body 6 and the feed blade body 6 that protrudes inward in the transport direction and inclines toward the tip side. It is the structure by which the body 6 and the return blade body 7 from which an inclination direction is opposite were arranged in multiple numbers.

送り羽根体6は、図2に図示したように適宜な金属製の板材をC字状に形成したものであり、この送り羽根体6の断面形状は湾曲形状に形成されている。   As shown in FIG. 2, the feed blade body 6 is formed by forming an appropriate metal plate material in a C shape, and the cross section of the feed blade body 6 is formed in a curved shape.

また、送り羽根体6の基端部6a(径大部の縁)は、回転体25の内面所定位置に溶接されており、また、送り羽根体6の先端部は、この回転体25の内面に対して約40°となるよう先端側ほど搬送方向且つ内方へ突出して傾斜する状態に設けられている。   The base end portion 6 a (the edge of the large diameter portion) of the feed blade body 6 is welded to a predetermined position on the inner surface of the rotating body 25, and the distal end portion of the feed blade body 6 is the inner surface of the rotating body 25. In contrast, the tip end side is provided in an inclined state so as to project inward and inward so as to be about 40 °.

戻し羽根体7は、図2に図示したように適宜な金属製の板材を逆C字状に形成したものであり、この戻し羽根体7の断面形状は湾曲形状に形成されている。   As shown in FIG. 2, the return blade body 7 is formed by forming an appropriate metal plate material in an inverted C shape, and the return blade body 7 has a curved cross-sectional shape.

また、戻し羽根体7の基端部7a(径大部の縁)は、回転体25の内面所定位置に溶接されており、また、戻し羽根体7の先端部は、この回転体25の内面に対して約40°となるよう先端側ほど逆搬送方向且つ内方へ突出して傾斜する状態に設けられている。   Further, the base end portion 7 a (the edge of the large diameter portion) of the return blade body 7 is welded to a predetermined position on the inner surface of the rotating body 25, and the distal end portion of the return blade body 7 is the inner surface of the rotating body 25. In contrast, the tip end side is provided so as to be inclined in the reverse conveying direction and inward so as to be about 40 °.

送り羽根体6及び戻り羽根体7の切欠部6d,7dは、上下が逆転した位置となっている。尚、図3中の実線部分が送り羽根体6であり、二点鎖線部分が戻し羽根体7である。   The cutout portions 6d and 7d of the feed blade body 6 and the return blade body 7 are positions where the top and bottom are reversed. The solid line portion in FIG. 3 is the feed blade body 6, and the two-dot chain line portion is the return blade body 7.

以上の構成から、被炭化物落下手段4は、送り羽根体6と戻し羽根体7とで回転体25の回転に伴い被炭化物1を所定高さ位置に上げた後に搬送方向若しくは逆搬送方向に斜め落下せしめることになる。   From the above configuration, the to-be-carburized dropping means 4 is inclined in the transport direction or the reverse transport direction after raising the to-be-carburized 1 to a predetermined height position with the rotation of the rotating body 25 by the feed blade body 6 and the return blade body 7. It will fall.

具体的には、回転体25の回転により図4−Aに図示したように送り羽根体6で受けた被炭化物1は上方へ持ち上げられた後、戻り羽根体7の切欠部7dを通過して搬送方向へ斜め落下し、続いて、図4−Bに図示したように戻し羽根体7で受けた被炭化物1は上方へ上げられた後、送り羽根体6の切欠部6dを通過して逆搬送方向へ斜め落下する。この送り羽根体6及び戻し羽根体7で被炭化物1が斜め落下する際、水分含有量の少ない重量の軽い被炭化物1は後述する被炭化物誘導手段5としての空気流により搬送方向に送られ、水分含有量の多い重量の重い被炭化物1は真下へ落ちるか若しくは送り羽根体6及び戻し羽根体7が傾斜する方向(搬送方向若しくは逆搬送方向)に短い距離で斜め落下することになる。尚、送り羽根体6及び戻り羽根体7により被炭化物1が所定高さ位置まで上げられるのは、被炭化物1が水分を有して送り羽根体6及び戻り羽根体7に付着した状態となるからである。この被炭化物1の付着力を向上することを考慮し、送り羽根体6及び戻り羽根体7の摩擦抵抗を増すために表面に粗面処理を施しても良い。   Specifically, as shown in FIG. 4-A, the to-be-carburized object 1 received by the feed blade body 6 is lifted upward by the rotation of the rotating body 25, and then passes through the cutout portion 7d of the return blade body 7. As shown in FIG. 4B, the carbide 1 received by the return blade body 7 is lifted upward, and then passes through the notch 6d of the feed blade body 6 to be reversed. Drop diagonally in the transport direction. When the article to be carbide 1 falls obliquely by the feed blade body 6 and the return blade body 7, the light article 1 having a low moisture content and light weight is sent in the conveying direction by an air flow as the article-to-be-carburized guiding means 5 described later. The heavy to-be-carburized object 1 with a high water content falls directly below or falls obliquely at a short distance in the direction in which the feed blade body 6 and the return blade body 7 are inclined (conveying direction or reverse conveying direction). In addition, the to-be-carburized object 1 is raised to a predetermined height position by the feed blade body 6 and the return blade body 7 is in a state where the to-be-carburized object 1 has moisture and adheres to the feed blade body 6 and the return blade body 7. Because. In consideration of improving the adhesion of the carbide 1, the surface may be roughened to increase the frictional resistance of the feed blade body 6 and the return blade body 7.

続いて、図4−Cに図示したように十分に水分が蒸発した被炭化物1は、重量が軽くなる為、斜め落下の際、被炭化物誘導手段5に誘導されてそれまで受けていた戻し羽根体7を越えて搬送方向へ送られる。   Subsequently, as shown in FIG. 4-C, the to-be-carburized object 1 having sufficiently evaporated water is reduced in weight, and therefore, the return vane that has been received by being guided by the to-be-carburized object guiding means 5 at the time of the oblique fall. It is sent in the transport direction over the body 7.

尚、図示していないが回転体25の内面に付着した被炭化物1が上方位置まで上げられ、その位置から落下する場合もある。   Although not shown, the carbide 1 attached to the inner surface of the rotating body 25 may be raised to an upper position and dropped from that position.

この被炭化物落下手段4に係る送り羽根体6と戻し羽根体7とにより、含水率の高い被炭化物1は撹拌され(煽られ)ながら加熱されることで水分が十分に飛ばされることになる(乾燥燃焼作用が発揮される)。   By the feed blade body 6 and the return blade body 7 related to the carbonized material dropping means 4, the carbonized material 1 having a high moisture content is heated while being stirred (squeezed), so that moisture is sufficiently blown away ( Dry combustion effect is exerted).

また、被炭化物搬送炭化部3は、この被炭化物落下手段4により落下する落下途時若しくは落下した前記被炭化物1のうち、重量の軽い前記被炭化物1を重量の重い前記被炭化物1よりも長い距離だけ搬送方向に誘導する被炭化物誘導手段5を具備する。   Moreover, the to-be-carburized conveyance carbonization part 3 is longer than the said to-be-carburized object 1 with a heavy weight of the to-be-carburized object 1 with a light weight among the to-be-carburized objects 1 which fall by the to-be-carburized object fall means 4 Carbide material guiding means 5 for guiding the distance in the conveying direction is provided.

被炭化物誘導手段5は、後述する二次燃焼室22で一次燃焼ガス(加熱室2で燃焼した排ガス)を燃焼した際に、被炭化物搬送炭化部3内で自然に生ずる搬送方向への空気流(ドラフト作用)であり、この空気流により被炭化物1は搬送方向に誘導される。尚、被炭化物誘導手段5としては、例えばファンなどを設けて被炭化物搬送炭化部3内に空気を強制的に流下させる構成としても良い。また、本実施例で言う被炭化物誘導手段5としての空気とは、被炭化物搬送炭化部3で発生する一次燃焼ガスも含むものである。   The to-be-carburized guidance means 5 is a flow of air in the conveying direction that naturally occurs in the to-be-carburized conveying carbonization section 3 when the primary combustion gas (exhaust gas combusted in the heating chamber 2) is combusted in the secondary combustion chamber 22 described later. (Draft action), and this air flow induces the article to be carbide 1 in the conveying direction. In addition, as the to-be-carburized guidance means 5, it is good also as a structure which provides a fan etc. and forcibly flows down air in the to-be-carburized material conveyance carbonization part 3, for example. Moreover, the air as the to-be-carburized guidance means 5 said by a present Example also includes the primary combustion gas which generate | occur | produces in the to-be-carburized material conveyance carbonization part 3. FIG.

本実施例は、回転体25の回転速度を適宜調整し、更に、加熱室2及び二次燃焼室22での燃焼を適宜調整して空気流を所望の速度とし、これら適宜設定により良好な炭が得られるように構成されている。   In this embodiment, the rotational speed of the rotating body 25 is appropriately adjusted, and further, the combustion in the heating chamber 2 and the secondary combustion chamber 22 is appropriately adjusted to obtain a desired air flow. It is comprised so that can be obtained.

以上の構成から成る被炭化物落下手段4、即ち、複数の送り羽根体6及び戻り羽根体7並びに被炭化物誘導手段5により被炭化物1の重量別に適正な炭化搬送が行われ、良好に炭化した炭は被炭化物搬送炭化部3の先端側に設けられる強制搬送手段8へ搬送されることになる。   The carbonized material dropping means 4 having the above configuration, that is, the plurality of feed blade bodies 6 and the return blade body 7 and the carbonized material guiding means 5 perform proper carbonization conveyance according to the weight of the carbonized material 1, and the carbonized well. Is transported to the forced transport means 8 provided on the front end side of the carbonized material transport carbonization section 3.

本発明者は、この送り羽根体6及び戻り羽根体7による搬送方向若しくは逆搬送方向への落下及び空気流により良好な炭化が行われることを実験により確認している。   The inventor has confirmed by experiments that good carbonization is performed by the drop in the transport direction or the reverse transport direction by the feed blade body 6 and the return blade body 7 and the air flow.

強制搬送手段8は、前記被炭化物1を低速で搬送する低速搬送領域8Aと、この低速搬送領域8Aよりも下流側に位置し、該低速領域8Aよりも前記被炭化物1を搬送する速度が速い高速搬送領域8Bとを有するものである。   The forced conveying means 8 is located at a low speed conveying area 8A for conveying the carbide 1 at a low speed and downstream of the low speed conveying area 8A, and has a higher speed for conveying the carbide 1 than the low speed area 8A. And a high-speed conveyance area 8B.

この強制搬送手段8は、適宜な金属製の板材を螺旋状にした送り羽根体9A,9Bで構成され、送り羽根体9Aは、先端側ほど搬送方向且つ内方へ突出して傾斜する状態に設けられている。更に、この送り羽根体9Aの回転体25からの突出長さは前述した送り羽根体6の三分の二程度に設定されている。   This forced conveying means 8 is composed of feed blade bodies 9A and 9B in which an appropriate metal plate material is spirally formed, and the feed blade body 9A is provided in a state of projecting inward and inclining toward the tip side. It has been. Further, the protruding length of the feed blade body 9A from the rotating body 25 is set to about two thirds of the feed blade body 6 described above.

また、送り羽根体9Aは、その基端部9A’が回転体25の内面所定位置に溶接されており、この回転体25の内面に対して約35°となるように設けられている。   Further, the feed blade body 9A has a base end portion 9A 'welded to a predetermined position on the inner surface of the rotating body 25, and is provided so as to be approximately 35 ° with respect to the inner surface of the rotating body 25.

一方、送り羽根体9Bは、先端側ほど搬送方向且つ内方へ突出して傾斜する状態に設けられている。更に、この戻り羽根体9Bの回転体25からの突出長さは前述した送り羽根体9Aの半分程度に設定され、更に、螺旋のピッチも送り羽根体9Aに比して短く設定されている。   On the other hand, the feed blade body 9B is provided in a state in which it protrudes inward in the transport direction and inclines toward the tip side. Further, the protruding length of the return blade body 9B from the rotating body 25 is set to about half of the above-described feed blade body 9A, and the helical pitch is set to be shorter than that of the feed blade body 9A.

また、戻り羽根体9Bは、その基端部9B’が回転体25の内面所定位置に溶接されており、この回転体25の内面に対して約20°となるように設けられている。   Further, the return blade body 9B has a base end portion 9B 'welded to a predetermined position on the inner surface of the rotating body 25, and is provided so as to be about 20 ° with respect to the inner surface of the rotating body 25.

低速搬送領域8Aは、被炭化物1を搬送する搬送速度が送り羽根体9Bによる搬送速度よりも遅くなるように設定されており、被炭化物落下部4を通過した被炭化物1を比較的時間を掛けて加熱する部分である(有機素材が持つ乾留ガスが燃焼する自然燃焼作用が発揮される)。   The low-speed conveyance region 8A is set so that the conveyance speed for conveying the carbide 1 is slower than the conveyance speed by the feed blade body 9B, and it takes a relatively long time for the carbide 1 that has passed through the carbide falling part 4 to pass. (The natural combustion effect of burning the dry distillation gas of organic materials is demonstrated).

高速搬送領域8Bは、被炭化物1を搬送する搬送速度が前述した低速搬送領域8Aでの搬送速度の約2倍となるように設定されており、送り羽根体9Aで加熱されて炭となった被炭化物1が灰とならないように早く搬送しつつ仕上げ加熱する部分である(調整燃焼作用が発揮される)。   The high-speed conveyance area 8B is set so that the conveyance speed for conveying the carbide 1 is about twice the conveyance speed in the low-speed conveyance area 8A described above, and is heated by the feed blade body 9A to become charcoal. It is a part which finishes heating while conveying quickly so that the to-be-carburized 1 may not become ash (adjustment combustion action is exhibited).

また、被炭化物搬送炭化部3は、その基端部に被炭化物1を該被炭化物搬送炭化部3に供給する被炭化物供給部17が設けられている。   Moreover, the to-be-carburized conveyance carbonization part 3 is provided with the to-be-carburized supply part 17 which supplies the to-be-carburized substance 1 to this to-be-carburized conveyance carbonization part 3 in the base end part.

この被炭化物供給部17は、図1に図示したように、内部に駆動装置17bにより回動する周面に螺旋羽根体17dが突設された回動軸17cを配して構成され、この被炭化物供給部17にはホッパー体17aが設けられている。   As shown in FIG. 1, the carbide supply unit 17 includes a rotating shaft 17c having a spiral blade 17d projecting on a peripheral surface rotated by a driving device 17b. The carbide supply part 17 is provided with a hopper body 17a.

また、被炭化物搬送炭化部3は、その先端部に炭化処理された処理済の炭を排出する炭排出部18が設けられている。   Moreover, the to-be-carburized material conveyance carbonization part 3 is provided with the charcoal discharge part 18 which discharges the processed charcoal carbonized at the front-end | tip part.

この炭排出部18は、図1に図示したように回転体25の先端部に接続される炭通過パイプ18a内に駆動装置18bにより回動する周面に螺旋羽根体18dが突設された回動軸18cを配して構成されている。   As shown in FIG. 1, the charcoal discharge unit 18 includes a spiral blade 18d projecting on a circumferential surface rotated by a driving device 18b in a charcoal passage pipe 18a connected to the tip of the rotary body 25. The moving shaft 18c is arranged.

また、被炭化物搬送炭化部3の基端部には、蒸気抜きパイプ20が連設され、更に、被炭化物搬送炭化部3の先端部には被炭化物1の炭化処理により発生した乾留ガスを排出するガス抜きパイプ19が連設されている。   Further, a steam vent pipe 20 is connected to the base end portion of the carbonized material transport carbonization unit 3, and further, the carbonized gas generated by the carbonization treatment of the material to be carbonized 1 is discharged to the distal end portion of the carbonized material transport carbonization unit 3. A degassing pipe 19 is continuously provided.

この蒸気抜きパイプ20及びガス抜きパイプ19は、夫々その先端部が基体10の上部中央に設けた排気部10cに連設されており、この排気部10cに設けたパイプ体21は二次燃焼室22に接続される。   The steam vent pipe 20 and the gas vent pipe 19 are respectively connected to an exhaust portion 10c provided at the top center of the base body 10, and the pipe body 21 provided on the exhaust portion 10c is a secondary combustion chamber. Connected to 22.

二次燃焼室22は、図1に図示したように適宜な金属製の部材で形成された箱状体23の内空間であり、排気部10cのバーナー装置24により点火され、一次燃焼ガスは完全に燃焼される。符号26は酸素供給部である。   The secondary combustion chamber 22 is an inner space of a box-like body 23 formed of an appropriate metal member as shown in FIG. 1, and is ignited by the burner device 24 of the exhaust part 10c, so that the primary combustion gas is completely Is burned. Reference numeral 26 denotes an oxygen supply unit.

従って、加熱室2での炭化処理により発生する乾留ガスは、二次燃焼室22で燃焼されることになる為、箱状体23の上部に設けた排気筒23aからはクリーンな排気が排出される。   Accordingly, the dry distillation gas generated by the carbonization process in the heating chamber 2 is combusted in the secondary combustion chamber 22, so that clean exhaust is discharged from the exhaust cylinder 23 a provided at the upper portion of the box-like body 23. The

本実施例は上述のように構成したから、被炭化物1は被炭化物搬送炭化部3で搬送されながら炭化し炭となる。   Since the present embodiment is configured as described above, the article to be carbide 1 is carbonized while being conveyed by the article-conveying carbonization unit 3 to be charcoal.

本実施例は、被炭化物搬送炭化部3に被炭化物落下手段4及び被炭化物誘導手段5を具備することで、例えば水分含有量が多くて重量の重い被炭化物1はじっくり加熱され、一方、水分含有量が少なくて重量の軽い被炭化物1は早めに加熱されながら早く下流側へ搬送される。   In the present embodiment, the to-be-carburized transporting carbonization unit 3 includes the to-be-carburized dropping means 4 and the to-be-carburized guiding means 5. The to-be-carburized material 1 having a small content and a light weight is conveyed early to the downstream side while being heated early.

また、本実施例に係る被炭化物供給部17に被炭化物1を投入するにあたり、水分含有量が多い被炭化物1に対しては予め水分含有率を50%以下に低減しておくことが望ましい。尚、この水分含有量の少ない素材の混合割合は適宜な計算により求められる。   In addition, it is desirable to reduce the moisture content to 50% or less in advance for the carbide 1 having a high moisture content when the carbide 1 is introduced into the carbide supply unit 17 according to the present embodiment. Note that the mixing ratio of the material having a low water content can be obtained by appropriate calculation.

具体的には、水分含有量が多い被炭化物1に水分含有量の少ない素材を混ぜることで被炭化物1の水分含有率を低減させる。この被炭化物1の水分含有率を低減するために混ぜる素材としては、吸水性を有し且つそれ自体が炭化され得る素材(例えば籾殻など)が望ましく、被炭化物1の水分含有率を低減させることで炭化処理速度は飛躍的に向上し、それだけコスト面(ランニングコスト等)においても秀れることになる(従来から行われているエネルギーを使用した機械的脱水方法に比しても有効と考えられる。)。   Specifically, the moisture content of the to-be-carburized object 1 is reduced by mixing the to-be-carburized object 1 having a high moisture content with a material having a low moisture content. As a material to be mixed in order to reduce the moisture content of the carbonized object 1, a material having water absorption and capable of being carbonized itself (for example, rice husk) is desirable, and the moisture content of the carbonized object 1 is reduced. Thus, the carbonization rate will be dramatically improved, and the cost (running cost, etc.) will be superior (effectively compared to the conventional mechanical dehydration method using energy). .)

よって、本実施例によれば、被炭化物1の種類(素材のばらつき)に対応した加熱が行なわれることになり極めて効率の良い炭化処理が行われ、高品位な炭が確実且つ安定的に得られることになる。   Therefore, according to the present embodiment, heating corresponding to the type (variation of materials) of the object to be carbide 1 is performed, and extremely efficient carbonization treatment is performed, and high-grade charcoal is obtained reliably and stably. Will be.

また、本実施例は、被炭化物搬送炭化部3に被炭化物1の重量(水分含有量)に合わせて加熱する被炭化物落下手段4として、この送り羽根体6の対向位置に該送り羽根体6と傾倒方向が反対となる戻し羽根体7とからなる構造を採用したから、簡易構造にして量産性に秀れるのは勿論、前述した従来例のような被炭化物1を単に下流側へ進めながら加熱する構造に比し、被炭化物搬送炭化部3の長さは短くても被炭化物1の水分含有量に合った十分な加熱をすることができ、よって、装置自体を小型軽量化することができることになり、ひいては、この小型軽量化により移動式とすることができ、前述した従来例のように設置されていたものと異なり、被炭化物1が生じる場所へ運んで炭化処理を行うことも可能となる。   Further, in this embodiment, as the carbonized article dropping means 4 that heats the carbonized article transporting carbonization section 3 in accordance with the weight (water content) of the article 1 to be carbonized, the feed blade body 6 is disposed at a position opposite to the feed blade body 6. Since the structure composed of the return blade body 7 whose tilt direction is opposite is employed, the simplified structure is excellent in mass productivity, and the carbide 1 as in the conventional example described above is simply advanced downstream. Compared with the structure to be heated, even if the length of the carbonized article transporting carbonization section 3 is short, sufficient heating can be performed in accordance with the moisture content of the article to be carbide 1, and thus the apparatus itself can be reduced in size and weight. As a result, it can be made mobile due to this small size and light weight, and unlike the conventional example described above, it can be carried to the place where the object to be carbonized 1 is generated and carbonized. It becomes.

また、本実施例は、被炭化物誘導手段5は、この種の装置で必須とされる二次燃焼室22で一次燃焼ガス(加熱室2で燃焼した排ガス)を燃焼した際に、被炭化物搬送炭化部3内で自然に生ずる搬送方向への空気流(ドラフト作用)を利用した構造であるから、空気を圧送するに何ら特別な装置は不要となるから極めて経済的である。   In the present embodiment, the carbide guiding means 5 conveys the carbide when the primary combustion gas (exhaust gas combusted in the heating chamber 2) is combusted in the secondary combustion chamber 22 which is essential in this type of apparatus. Since the structure utilizes the air flow (draft action) in the conveying direction that occurs naturally in the carbonizing section 3, no special device is required to pump the air, which is extremely economical.

尚、本発明は、本実施例に限られるものではなく、各構成要件の具体的構成は適宜設計し得るものである。   Note that the present invention is not limited to this embodiment, and the specific configuration of each component can be designed as appropriate.

本実施例の説明断面図である。It is explanatory sectional drawing of a present Example. 本実施例に係る要部の説明斜視図である。It is a description perspective view of the principal part concerning a present Example. 本実施例に係る要部の説明図である。It is explanatory drawing of the principal part which concerns on a present Example. 本実施例に係る要部の動作説明図である。It is operation | movement explanatory drawing of the principal part which concerns on a present Example. 本実施例に係る要部の説明斜視図である。It is a description perspective view of the principal part concerning a present Example. 本実施例に係る要部の動作説明図である。It is operation | movement explanatory drawing of the principal part which concerns on a present Example.

符号の説明Explanation of symbols

1 被炭化物
3 被炭化物搬送炭化部
4 被炭化物落下手段
5 被炭化物誘導手段
6 送り羽根体
7 戻し羽根体
8 強制搬送手段
8A 低速搬送領域
8B 梗塞搬送領域
9A 送り羽根体
9B 送り羽根体
25 回転体
DESCRIPTION OF SYMBOLS 1 Carbide 3 Carbide conveyance carbonization part 4 Carbide fall means 5 Carbide guidance means 6 Feed blade body 7 Return blade body 8 Forced conveyance means 8A Low speed conveyance area 8B Infarct conveyance area 9A Feed blade body 9B Feed blade body
25 Rotating body

Claims (10)

被炭化物を加熱して炭化する炭化装置であって、前記被炭化物を搬送しながら炭化する所定長の被炭化物搬送炭化部を有し、この被炭化物搬送炭化部は、炭化途時の前記被炭化物を落下させる被炭化物落下手段と、この被炭化物落下手段により落下する落下途時若しくは落下した前記被炭化物のうち、重量の軽い前記被炭化物を重量の重い前記被炭化物よりも長い距離だけ搬送方向に誘導して前記被炭化物搬送炭化部から導出する被炭化物誘導手段とを具備することを特徴とする炭化装置。   A carbonization apparatus that heats and carbonizes a material to be carbonized, and has a carbonized material conveying carbonization portion having a predetermined length that carbonizes while conveying the material to be carbonized, and the carbonized material conveying carbonization portion is the carbonized material during carbonization. Of the carbonized material dropping means for dropping the carbonized material, and the falling of the carbonized material falling by the carbonized material dropping means in the conveying direction by a distance longer than the heavy weight of the carbonized material. A carbonization apparatus, comprising: a carbonized material guiding means for guiding and deriving from the carbonized material transport carbonization unit. 請求項1記載の炭化装置において、前記被炭化物落下手段は、前記被炭化物を所定高さ位置に上げた後に搬送方向若しくは逆搬送方向に斜め落下せしめるように構成されたものであることを特徴とする炭化装置。   The carbonization apparatus according to claim 1, wherein the carbide dropping means is configured to drop the carbide to be obliquely dropped in a conveyance direction or a reverse conveyance direction after being raised to a predetermined height position. Carbonization equipment. 請求項1,2いずれか1項に記載の炭化装置において、前記被炭化物誘導手段は、前記被炭化物搬送炭化部内を搬送方向に流下する空気流であることを特徴とする炭化装置。   The carbonization apparatus according to claim 1, wherein the carbide guiding means is an air flow that flows down in the conveyance direction within the carbonization carbonization unit. 請求項1〜3いずれか1項に記載の炭化装置において、前記被炭化物搬送炭化部は、筒状の回転体であることを特徴とする炭化装置。   The carbonization apparatus of any one of Claims 1-3 WHEREIN: The said to-be-carburized conveyance carbonization part is a cylindrical rotary body, The carbonization apparatus characterized by the above-mentioned. 請求項4記載の炭化装置において、前記被炭化物落下手段は、前記回転体の内面に設けられ、先端側ほど搬送方向且つ内方へ突出して傾斜する送り羽根体と、この送り羽根体の対向位置に設けられ該送り羽根体と傾斜方向が反対となる戻し羽根体とで構成されるものであることを特徴とする炭化装置。   5. The carbonization apparatus according to claim 4, wherein the carbide dropping means is provided on an inner surface of the rotating body, and a feed blade body that protrudes inward in the transport direction and inclines toward the tip side, and a position opposite to the feed blade body. A carbonization apparatus comprising: a feeding blade body and a return blade body whose inclination direction is opposite to each other. 請求項1〜5いずれか1項に記載の炭化装置において、前記被炭化物搬送炭化部は、前記被炭化物落下手段及び前記被炭化物誘導手段により前記被炭化物を搬送しながら炭化して該被炭化物搬送炭化部から導出するものであることを特徴とする炭化装置。   6. The carbonization apparatus according to claim 1, wherein the to-be-carburized conveying carbonization unit carbonizes the to-be-carburized object by conveying the to-be-carburized object by the to-be-carburized dropping unit and the to-be-carburized guiding unit. A carbonization apparatus derived from a carbonization section. 請求項5,6いずれか1項に記載の炭化装置において、前記対向する送り羽根体と戻し羽根体は複数並設されていることを特徴とする炭化装置。   7. The carbonization apparatus according to claim 5, wherein a plurality of the opposed feed blade bodies and the return blade bodies are arranged in parallel. 請求項1〜7いずれか1項に記載の炭化装置において、前記被炭化物搬送炭化部内にして前記被炭化物落下手段が設けられる部位よりも下流側部位には、前記被炭化物を強制搬送する強制搬送手段が設けられていることを特徴とする炭化装置。   The carbonization apparatus of any one of Claims 1-7 WHEREIN: The forced conveyance which forcibly conveys the said to-be-carburized object in the downstream part rather than the site | part in which the said to-be-carbide falling means is provided in the said to-be-carburized object conveyance carbonization part. A carbonization device characterized in that means are provided. 請求項8記載の炭化装置において、前記強制搬送手段は、前記被炭化物を低速で搬送する低速搬送領域と、この低速搬送領域よりも下流側に位置し、該低速領域よりも前記被炭化物を搬送する速度が速い高速搬送領域とが設けられていることを特徴とする炭化装置。   9. The carbonization apparatus according to claim 8, wherein the forced conveying means is located at a low speed conveyance area for conveying the carbonized object at a low speed, and is located downstream of the low speed conveyance area, and conveys the carbonized object from the low speed area. And a high-speed transfer area having a high speed. 請求項9記載の炭化装置において、前記強制搬送手段は、先端側ほど搬送方向且つ内方へ突出して傾斜する螺旋状の送り羽根体であり、前記低速搬送領域と前記高速搬送領域とにおいて、前記送り羽根体の傾斜度合は異なるように設定されていることを特徴とする炭化装置。   The carbonization apparatus according to claim 9, wherein the forced conveying means is a spiral feed blade body that protrudes inward and inclines toward the leading end side, and in the low-speed conveyance region and the high-speed conveyance region, A carbonization apparatus, wherein the inclination degree of the feed blade body is set to be different.
JP2007094238A 2006-09-29 2007-03-30 Carbonization apparatus Pending JP2008106221A (en)

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WO2010047283A1 (en) * 2008-10-20 2010-04-29 合資会社Liberty Net INTERNATIONAL Apparatus for carbonization and method of carbonization
JP2011116618A (en) * 2009-08-31 2011-06-16 Shinten Kogyo Kk Method for manufacturing hydrophilic member, hydrophilic member, chaff carbonization method, chaff carbonizing apparatus, and method for preserving hydrophilic member
WO2011096444A1 (en) * 2010-02-02 2011-08-11 株式会社ガイア環境技術研究所 Method for producing oil or gas adsorbent, and oil or gas adsorbent
CN106118697A (en) * 2016-08-12 2016-11-16 田东昊润新材料科技有限公司 The brown coal continuous way coker of heat energy recycling
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Cited By (9)

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Publication number Priority date Publication date Assignee Title
WO2010047283A1 (en) * 2008-10-20 2010-04-29 合資会社Liberty Net INTERNATIONAL Apparatus for carbonization and method of carbonization
JP2013177620A (en) * 2008-10-20 2013-09-09 Gaia Kankyo Gijutsu Kenkyusho:Kk Apparatus for carbonization and method for carbonization
JP5480814B2 (en) * 2008-10-20 2014-04-23 株式会社ガイア環境技術研究所 Carbonization apparatus and carbonization method
JP2011116618A (en) * 2009-08-31 2011-06-16 Shinten Kogyo Kk Method for manufacturing hydrophilic member, hydrophilic member, chaff carbonization method, chaff carbonizing apparatus, and method for preserving hydrophilic member
WO2011096444A1 (en) * 2010-02-02 2011-08-11 株式会社ガイア環境技術研究所 Method for producing oil or gas adsorbent, and oil or gas adsorbent
JP2016093811A (en) * 2010-02-02 2016-05-26 株式会社ガイア環境技術研究所 Method for producing oil and gas adsorbent, and oil and gas adsorbent
JP6002877B2 (en) * 2010-02-02 2016-10-05 株式会社ガイア環境技術研究所 Method for producing oil or gas adsorbent and oil or gas adsorbent
CN106118697A (en) * 2016-08-12 2016-11-16 田东昊润新材料科技有限公司 The brown coal continuous way coker of heat energy recycling
KR102450826B1 (en) * 2022-04-05 2022-10-06 김일 Biochar manufacturing system using waste heat produced in heatstick manufacturing system

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