JP2006219597A - Carbonizing apparatus - Google Patents

Carbonizing apparatus Download PDF

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JP2006219597A
JP2006219597A JP2005034967A JP2005034967A JP2006219597A JP 2006219597 A JP2006219597 A JP 2006219597A JP 2005034967 A JP2005034967 A JP 2005034967A JP 2005034967 A JP2005034967 A JP 2005034967A JP 2006219597 A JP2006219597 A JP 2006219597A
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carbonization
cylinder
chamber
carbonizing
opening
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Masanori Nakayama
正則 中山
Yuzuru Horie
譲 堀江
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    • 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
    • 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
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/78Recycling of wood or furniture waste

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  • Processing Of Solid Wastes (AREA)
  • Treatment Of Sludge (AREA)

Abstract

<P>PROBLEM TO BE SOLVED: To carry out problem solving of safety such as diffusion of dry distillation gas from a hopper and improvement of heat efficiency in a carbonizing apparatus for converting waste material chips such as wood chip, bark, home garbage, papermaking sludge, sludge and vegetable waste and the other materials to carbonized products. <P>SOLUTION: The carbonizing apparatus is constituted so as to install a heating chamber and a carbonizing cylinder in a carbonizing furnace equipped with a charcoal material feed mechanism and a discharge gas discharging passage. In the carbonizing apparatus, the heating chamber is made to communicate through a communication passage with the carbonizing cylinder and a heating part is installed in the heating chamber and an agitating shaft having agitating blade and suspended in the carbonizing furnace is hung down into the carbonizing cylinder and the upper part of a wire passing through the interior of the agitating shaft is installed in winding means of the carbonizing furnace and an opening and closing tool is hung down in the lower part of the wire and an opening and closing port of the carbonizing cylinder is opened or closed by the opening and closing tool. <P>COPYRIGHT: (C)2006,JPO&NCIPI

Description

本発明は、木チップ、木皮、家庭用ゴミ・製紙スラッジ・汚泥・野菜クズ等の廃材チップ、その他の材料を炭化物に変換する炭化装置に関する。   The present invention relates to a carbonization apparatus for converting wood chips, bark, waste chips such as household waste, papermaking sludge, sludge, and vegetable scraps, and other materials into carbides.

従来の家庭用ゴミ・製紙スラッジ・汚泥・野菜クズ等の廃材の燃焼処理による方法おいては、この燃焼時に発生する二酸化炭素の量が年々増加の一途を辿っており、問題化している。この問題改良の一環として、この種の家庭用ゴミ・製紙スラッジ・汚泥・野菜クズ等の廃材を、脱水・固形化して廃材チップ(チップ形状)に変換し、この廃材チップを炭化処理により炭化物として有効利用する方法(炭化処理方式)が採用されつつある。所謂、廃材チップの炭化装置である。この炭化装置は、その後、種々の改良を行うことで、新たな問題となっている住宅廃材、間伐材、又は家庭用木質ゴミ等の木質廃材の炭化処理に採用されつつある。そして、この木質廃材を有効に炭化処理するには、前述の家庭用ゴミ等の廃材と同様にチップ化する方法が効率的であることが理解される状況となりつつある。   In the conventional method of burning waste materials such as household waste, papermaking sludge, sludge, vegetable waste, etc., the amount of carbon dioxide generated at the time of combustion has been increasing year by year and has become a problem. As part of this problem improvement, this kind of household waste, paper sludge, sludge, vegetable waste, and other waste materials are dewatered and solidified to convert into waste material chips (chip shape), and these waste chips are carbonized by carbonization. An effective utilization method (carbonization method) is being adopted. This is a so-called carbonization device for waste chips. Thereafter, the carbonization apparatus is being adopted for carbonization treatment of wood waste materials such as house waste materials, thinning materials, or household wood wastes, which are new problems, by making various improvements. In order to effectively carbonize this wooden waste material, it is becoming understood that the method of chipping is effective as in the case of the above-mentioned waste material such as household waste.

そして、従来の炭化処理方式では、バッチ炉が主体であって処理能率(処理能力)が悪く、また処理量の向上が望めないことと、この処理能率が処理対象となるゴミの種類によって不安定になり問題である。そして、ゴミの炭化物がスポンジ状になってその断熱作用により熱効率が悪く、ダイオキシンの発生が見られる等の問題点があった。一方炭化炉においては、この炉内温度が高温になると、炭素の存在化での金属炉材の浸炭腐食も問題となることが考えられる。この炭化処理方式の改良案として、連続炉方式といわれているロータリー炉が開発された。しかし、この連続炉方式は前述の問題点を改良するには適する反面、例えば、炉の大型化を招来すること、また設備が膨大となる等の設備面と、連続運転方式であって、かつ乾留ガスの処理能力・処理結果が十分でないこと等よりして、一部でダイオキシンを含むダストの飛散が問題となるケースが考えられる。   In the conventional carbonization treatment system, the batch furnace is mainly used, the processing efficiency (processing capacity) is poor, the improvement of the processing amount cannot be expected, and this processing efficiency is unstable depending on the kind of garbage to be processed. It becomes a problem. Further, there is a problem that the carbide of dust becomes sponge-like and the heat efficiency is poor due to its heat insulating action, and the generation of dioxins is observed. On the other hand, in the carbonization furnace, when the temperature in the furnace becomes high, carburizing corrosion of the metal furnace material due to the presence of carbon may be a problem. As an improvement plan for this carbonization method, a rotary furnace called a continuous furnace method has been developed. However, while this continuous furnace method is suitable for improving the above-mentioned problems, for example, it leads to an increase in the size of the furnace, and the equipment surface is enormous, and the continuous operation method, and There may be a case where scattering of dust containing dioxin becomes a problem due to the fact that the treatment capacity and treatment result of dry distillation gas are not sufficient.

そして、この種の連続炉は、社会が要求する処理能率を達成し、また所定の処理量が望めること等よりして有益であり、また連続炉に関する従来の文献(先行文献)を挙げられる。この文献は、特開2003−300049の「ゴミ処理方法および装置」である(文献(1)とする)。この文献(1)の内容は、縦型の加熱塔内にゴミを上部より投入し、この加熱塔内に充填したゴミを外部より加熱して順次に乾燥、炭化処理して生成した炭化物を、加熱塔の底部の排出口より連続的に排出する構成であり、前記加熱塔内の乾燥及び/又は炭化処理中におけるスポンジ状のゴミ炭化物を撹拌すること、加熱塔内の乾燥及び/又は炭化処理中のゴミから発生する乾留ガスを回収して加熱用の補助燃料として使用することを特徴とするものであって、各種のゴミを安定かつ能率良く処理すること、また熱効率が良くて安価なゴミ処理方法および装置を提供することにある。   And this kind of continuous furnace is useful because it achieves the processing efficiency demanded by society and a predetermined amount of treatment is desired, and the conventional literature (prior art) relating to the continuous furnace can be mentioned. This document is “garbage disposal method and apparatus” of Japanese Patent Laid-Open No. 2003-300049 (referred to as document (1)). The content of this document (1) is to introduce the carbide generated in the vertical heating tower by putting the garbage from the upper part, heating the garbage filled in the heating tower from the outside, and sequentially drying and carbonizing. It is the structure which discharges continuously from the discharge port at the bottom of the heating tower, stirring the sponge-like dust carbide during the drying and / or carbonization treatment in the heating tower, drying and / or carbonization treatment in the heating tower It is characterized by collecting the dry distillation gas generated from the waste inside and using it as a supplementary fuel for heating, and is capable of treating various types of waste stably and efficiently, and is efficient and inexpensive. It is to provide a processing method and apparatus.

また前記従来技術及び/又は文献(1)等においても問題となる炭化物、材料(鋳物砂)排出用の排出口に関しは、この炭化物等の詰まり(ブリッジ)問題の解消が必須条件である。しかし、この条件を満足するには十分でない。そして、この必須条件を確保するための解消策として、次の文献が挙げられる。この文献は、特開2002−361404の「砂投入バケットと充填砂の充填方法」である(文献(2))。その内容は、従来の充填砂の排出方法の課題、即ち、円筒状保形金物を羽口れんが孔の孔縁に配置した状態で充填砂をノズル孔へ充填する際におけるその充填高さを制御し、かつそれぞれの操業条件に応じて充填高さを制御することで充填砂の焼結厚みを変化さ得ることと、焼結層のブリッジングによる不開孔を防止することであって、この文献(2)は、溶融金属容器のノズル孔の周縁部に保形筒を置くとともに、このノズル孔へ充填砂を充填する砂投入バケットであって、タンクは保持スタンドに上下方向に移動可能に設け、またこのタンクには投入口、排出口及び保形筒掴みを備え、さらにこの保持スタンドにはタンクの排出口を開閉するストッパーと保形筒掴みを開閉するための開閉部材を備え、タンクの上下方向の相対移動によって、排出口と保形筒掴みをそれぞれ開閉できることを特徴とするものであって、溶融金属容器に充填砂を充填する際に、充填砂を自動的に投入できる構造の砂投入バケット及びこれを利用した充填砂の充填方法を提供するにある。   Further, regarding the discharge port for discharging carbide and material (casting sand), which is also a problem in the prior art and / or document (1), it is essential to eliminate the clogging (bridge) problem of carbide and the like. However, it is not enough to satisfy this condition. And the following literature is mentioned as a solution for ensuring this essential condition. This document is "Sand throwing bucket and filling method of filled sand" disclosed in JP-A-2002-361404 (Reference (2)). The content is the problem of the conventional method of discharging the filled sand, that is, controlling the filling height when filling the nozzle hole with the filled sand with the cylindrical shaped metal fitting placed at the hole edge of the tuyere brick hole. In addition, by controlling the filling height according to each operating condition, it is possible to change the sintered thickness of the filled sand, and to prevent non-open holes due to bridging of the sintered layer, Document (2) is a sand charging bucket in which a shape-retaining cylinder is placed on the peripheral edge of the nozzle hole of the molten metal container, and the nozzle hole is filled with filled sand, and the tank can be moved vertically to a holding stand. The tank is provided with an inlet, an outlet, and a retaining cylinder grip, and the holding stand is provided with a stopper for opening and closing the tank outlet and an opening / closing member for opening and closing the retaining cylinder grip. By the relative movement of , Characterized by being able to open and close the discharge port and the shape retaining cylinder grip, respectively, and a sand charging bucket having a structure capable of automatically charging the filled sand when the molten metal container is filled with the sand It is in providing the filling method of the filled sand.

特開2003−300049JP2003-300049

特開2002−361404JP 2002-361404 A

前記文献(1)の発明は、連続式であるが、ゴミ投入装置(ホッパー)と加熱炉との境界及び/又は遮断が十分でなく、乾留ガスの逆流によるホッパーでの火災の危険性と、乾留ガスの拡散の危険性が指摘でき、安全性と燃焼効率の向上等の面において課題を抱えている。   The invention of the above-mentioned document (1) is a continuous type, but the boundary between the garbage throwing device (hopper) and the heating furnace and / or interruption is not sufficient, and there is a risk of fire in the hopper due to the backflow of dry distillation gas, The danger of diffusion of dry distillation gas can be pointed out, and there are problems in terms of improving safety and combustion efficiency.

次に文献(2)の発明は、タンクの下方に形成した漏斗状の排出口を、略逆台形のストッパーを介して開閉する構成であり、鋳物砂の充填及び/又は排出においてはさして問題となる構造とは考えられない。しかし、この構造では、炭化物の生成と、この炭化物を確実に排出し、また炭化筒内で発生するブリッジを確実に回避するためには、極めて困難と考えられる。   Next, the invention of the document (2) is configured to open and close a funnel-shaped discharge port formed below the tank through a substantially inverted trapezoidal stopper, and is problematic in filling and / or discharging sand. It is not considered to be a structure. However, with this structure, it is considered extremely difficult to generate carbides, reliably discharge the carbides, and reliably avoid the bridges generated in the carbonization cylinder.

請求項1の発明は、木チップ、木皮、家庭用ゴミ・製紙スラッジ・汚泥・野菜クズ等の廃材チップ、その他の材料(主としてチップ化された廃材、即ち、廃材チップ)等を間欠式で、連続的に炭化物に変換する炭化装置を提供することを主目的とし、この目的を達成するために、廃材チップを間欠式に供給し、この供給時に乾留ガスの逆流を防止し、廃材チップへの着火防止を図りつつ、この乾留ガスを加熱室にリターンし、熱効率を確保することと、また炭化筒に供給された廃材チップの確実な撹拌と、輻射熱との熱交換を介して炭化の促進と、高品質の炭化物を生成すること、そして、炭化筒で生成された炭化物を開口から炉外に排出すること等を意図する。   The invention of claim 1 is an intermittent type of wood chips, bark, waste material chips such as household garbage, papermaking sludge, sludge, vegetable scrap, and other materials (mainly chipped waste materials, ie, waste material chips), etc. The main purpose is to provide a carbonization device that continuously converts to carbide. To achieve this purpose, waste chips are supplied intermittently, and backflow of dry distillation gas is prevented at the time of supply. While preventing ignition, this dry distillation gas is returned to the heating chamber to ensure thermal efficiency, and the carbonization is promoted through reliable agitation of waste chips supplied to the carbonization cylinder and heat exchange with radiant heat. It is intended to produce high-quality carbide and to discharge the carbide produced in the carbonization cylinder out of the furnace through the opening.

また請求項1の発明は、炭化筒に供給された廃材チップを、この炭化筒に滞留させて炭化の促進と、高品質の炭化物を生成すること、また炭化筒内の廃材チップの撹拌を介して熱交換の促進を図ること等を意図する。   According to the invention of claim 1, the waste chip supplied to the carbonization cylinder is retained in the carbonization cylinder to promote carbonization, to produce high-quality carbide, and through the stirring of the waste chip in the carbonization cylinder. It is intended to promote heat exchange.

さらに請求項1の発明は、炭化筒で生成された乾留ガスを略100%加熱室に還流し、この加熱室で完全燃焼し、熱源の有効利用と、燃料消費量の効率化等を図ることを意図する。   Furthermore, the invention of claim 1 is to recirculate substantially 100% of the dry distillation gas generated in the carbonization cylinder to the heating chamber and burn it completely in the heating chamber, to effectively use the heat source, increase the efficiency of fuel consumption, and the like. Intended.

請求項1は、炭材供給機構を上方の一方側に、また排気ガス排出路を下方の接線方向にそれぞれ備えた炭化炉内に、加熱室と、この加熱室に囲繞されるように上下部を開放した炭化筒とを設けてなる構成であって、
前記加熱室と炭化筒とを連通路を介して連通し、また前記加熱室にバーナ等の加熱部を設け、前記炭化炉の上部より吊下した回転自在の撹拌軸を前記炭化筒に垂下し、この撹拌軸に間欠式に撹拌羽根を設け、またこの撹拌軸内を貫通するワイヤの上部を前記炭化炉の捲装手段に設けるとともに、その下部を炭化筒の下部に至らしめ、このワイヤの下部に開閉具を吊下し、この開閉具を介して前記炭化筒の下部に設けた開口を開閉し、この開口の下部に排出機構を設ける構成とした炭化装置である。
The first aspect of the present invention is a carbonization furnace provided with a carbonaceous material supply mechanism on one upper side and an exhaust gas discharge path in a lower tangential direction, and a heating chamber and upper and lower parts surrounded by the heating chamber. And a carbonized cylinder that is opened,
The heating chamber communicates with the carbonizing cylinder through a communication passage, and a heating unit such as a burner is provided in the heating chamber, and a rotatable stirring shaft suspended from the upper part of the carbonizing furnace is suspended from the carbonizing cylinder. The stirring shaft is intermittently provided on the stirring shaft, and the upper part of the wire penetrating the stirring shaft is provided in the outfitting means of the carbonization furnace, and the lower part thereof is led to the lower part of the carbonization cylinder. The carbonization apparatus has a configuration in which an opening / closing tool is suspended at a lower portion, an opening provided at a lower portion of the carbonization cylinder is opened / closed via the opening / closing tool, and a discharge mechanism is provided below the opening.

請求項2の発明は、請求項1の目的を達成すること、この目的を達成するに最適な排気ガス排出路と二次燃焼室の構造を提供することを意図する。   The invention of claim 2 is intended to achieve the object of claim 1 and to provide an exhaust gas exhaust passage and a structure of a secondary combustion chamber that are optimal for achieving the object.

請求項2は、請求項1の排気ガス排出路に二次燃焼室を形成し、この二次燃焼室内に送風ユニット及び/又は燃焼エア供給管・吸引エア供給管等を付設する構成とした炭化装置である。   According to a second aspect of the present invention, a secondary combustion chamber is formed in the exhaust gas discharge passage according to the first aspect, and a carbonization unit is configured such that a blower unit and / or a combustion air supply pipe / suction air supply pipe are provided in the secondary combustion chamber. Device.

請求項3の発明は、請求項1の目的を達成すること、この目的を達成するに最適な撹拌軸を提供し、またこの撹拌軸の清掃の容易化と、交換の容易な撹拌軸を提供すること等を意図する。   The invention of claim 3 achieves the object of claim 1, provides an optimum stirring shaft for achieving the object, and provides an easy-to-replace stirring shaft that facilitates cleaning of the stirring shaft. It is intended to do.

請求項3は、請求項1の撹拌軸は、炭化炉に設けた耐熱手段を経由して延設し、この延設した上端に連結用フランジを設け、この連結用フランジは前記炭化炉に開閉自在に設けてなるタワーフレームに軸承した連結軸に連結可能とし、またこの連結軸に設けた歯車にチェーンを介して駆動部に連繋し、この駆動部を前記タワーフレームに設ける構成とした炭化装置である。   According to a third aspect of the present invention, the stirring shaft of the first aspect is extended through a heat-resistant means provided in the carbonization furnace, and a connecting flange is provided at the extended upper end, and the connection flange opens and closes to the carbonization furnace. A carbonizing apparatus that can be connected to a connecting shaft that is supported by a tower frame that is freely provided, and that is connected to a driving portion via a chain on a gear provided to the connecting shaft, and the driving portion is provided on the tower frame. It is.

請求項4の発明は、請求項1の目的を達成すること、この目的を達成するに最適な炭材供給機構を提供し、またこの炭材供給機構の提供を介して乾留ガスの逆流防止と、この逆流に基づくトラブル、例えば、廃材チップへの着火防止を図ること、そして、この加熱室における熱効率を確保するとともに、熱交換を介して炭化の促進と、高品質の炭化物を生成すること等を意図する。   The invention of claim 4 achieves the object of claim 1, provides a carbonaceous material supply mechanism that is optimal for achieving this object, and prevents the backflow of dry distillation gas through the provision of this carbonaceous material supply mechanism. , Troubles due to this back flow, for example, preventing ignition of waste chips, and ensuring thermal efficiency in this heating chamber, promoting carbonization through heat exchange, producing high-quality carbides, etc. Intended.

請求項4は、請求項1に記載の炭材供給機構(廃材チップ供給機構)は、ホッパーと、このホッパーの収歛口に設けたこの収歛口と相似形の中間チャンバーと、この中間チャンバーの駆動を司る第一のシリンダーと、またこの中間チャンバーの移動端に設けた当該中間チャンバーの開閉を司るシャッターと、このシャッターの下部に設けた当該シャッターに連通する連通口を供えた供給路と、この供給路内を移動するピストン形の摺動チャンバーと、この摺動チャンバーを可動する第三のシリンダーとで構成した炭化装置である。   In a fourth aspect of the present invention, the carbonaceous material supply mechanism (waste material chip supply mechanism) according to the first aspect includes a hopper, an intermediate chamber similar to the converging port provided at the converging port of the hopper, and driving of the intermediate chamber. A first cylinder for controlling the opening, a shutter for opening and closing the intermediate chamber provided at the moving end of the intermediate chamber, a supply path provided with a communication port communicating with the shutter provided at a lower portion of the shutter, This is a carbonization apparatus comprising a piston-type sliding chamber that moves in a supply path and a third cylinder that moves the sliding chamber.

請求項5の発明は、請求項1の目的を達成すること、この目的を達成するに最適な中間チャンバー及び/又は摺動チャンバーを提供すること等を意図する。   The invention of claim 5 is intended to achieve the object of claim 1 and to provide an intermediate chamber and / or a sliding chamber which are optimal for achieving this object.

請求項5は、請求項4に記載の中間チャンバーの容積に対して、摺動チャンバーの容積を大きくする構成とした炭化装置である。   According to a fifth aspect of the present invention, there is provided a carbonizing apparatus in which the volume of the sliding chamber is increased with respect to the volume of the intermediate chamber according to the fourth aspect.

請求項1の発明は、炭材供給機構を上方の一方側に、また排気ガス排出路を下方の接線方向にそれぞれ備えた炭化炉内に、加熱室と、加熱室に囲繞されるように上下部を開放した炭化筒とを設けてなる構成であって、
加熱室と炭化筒とを連通路を介して連通し、また加熱室にバーナ等の加熱部を設け、炭化炉の上部より吊下した回転自在の撹拌軸を前記炭化筒に垂下し、撹拌軸に間欠式に撹拌羽根を設け、また撹拌軸内を貫通するワイヤの上部を炭化炉の捲装手段に設けるとともに、その下部を炭化筒の下部に至らしめ、ワイヤの下部に開閉具を吊下し、開閉具を介して炭化筒の下部に設けた開口を開閉し、開口の下部に排出機構を設ける炭化装置である。
In the first aspect of the present invention, a heating chamber and a heating chamber are provided so as to be surrounded by the heating chamber and the heating chamber. A structure in which a carbonized cylinder with an open portion is provided,
The heating chamber and the carbonizing cylinder are communicated via a communication passage, and a heating unit such as a burner is provided in the heating chamber, and a rotatable stirring shaft suspended from the upper part of the carbonization furnace is suspended from the carbonizing cylinder, and the stirring shaft In addition, the stirring blades are intermittently provided, and the upper part of the wire penetrating the stirring shaft is provided in the equipment of the carbonization furnace, and the lower part is brought to the lower part of the carbonization cylinder, and the opening / closing tool is suspended below the wire. And a carbonizing device that opens and closes an opening provided at a lower portion of the carbonizing cylinder via an opening / closing tool and provides a discharge mechanism at a lower portion of the opening.

従って、請求項1は、木チップ、木皮、家庭用ゴミ・製紙スラッジ・汚泥・野菜クズ等の廃材チップ、その他の材料等を間欠式で、連続的に炭化物に変換する炭化装置を提供することを主目的とする。この目的を達成するために、廃材チップを間欠式に供給し、この供給時に乾留ガスの逆流を防止し、廃材チップへの着火防止を図りつつ、この乾留ガスを加熱室にリターンし、優れた熱効率が確保できることと、また炭化筒に供給された廃材チップの確実な撹拌と、輻射熱との熱交換を介して炭化の促進と、高品質の炭化物が生成できること、そして、炭化筒で生成された炭化物を開口から炉外に排出できること等の特徴がある。   Accordingly, claim 1 provides a carbonization device that continuously converts wood chips, bark, waste chips such as household garbage, papermaking sludge, sludge, vegetable scraps, and other materials into carbide continuously. The main purpose. In order to achieve this purpose, waste chips are supplied intermittently, and during this supply, the dry distillation gas is prevented from flowing back, and the waste chips are ignited and returned to the heating chamber. It is possible to ensure thermal efficiency, to ensure the agitation of waste chips supplied to the carbonization cylinder, to promote carbonization through heat exchange with radiant heat, to produce high-quality carbide, and to be produced in the carbonization cylinder There is a feature that the carbide can be discharged out of the furnace through the opening.

また請求項1は、炭化筒に供給された廃材チップを、この炭化筒に滞留させて炭化の促進と、高品質の炭化物が生成できること、また炭化筒内の廃材チップの撹拌を介して熱交換の促進が図れること等の特徴がある。   Further, according to the first aspect of the present invention, the waste material chips supplied to the carbonization cylinder can be retained in the carbonization cylinder to promote carbonization and high quality carbide can be generated, and heat exchange can be performed through agitation of the waste material chips in the carbonization cylinder. There is a feature such as being able to promote.

さらに請求項1は、炭化筒で生成された乾留ガスを略100%加熱室に還流し、この加熱室で完全燃焼し、熱源の有効利用と、燃料消費量の効率化等が図れること等の特徴がある。   Further, according to claim 1, the dry distillation gas generated in the carbonization cylinder is recirculated to the heating chamber approximately 100% and completely combusted in the heating chamber, so that the heat source can be effectively used and the fuel consumption can be improved. There are features.

請求項2発明は、請求項1の排気ガス排出路に二次燃焼室を形成し、二次燃焼室内に送風ユニット及び/又は燃焼エア供給管・吸引エア供給管等を付設する炭化装置である。   A second aspect of the present invention is a carbonization device in which a secondary combustion chamber is formed in the exhaust gas discharge passage of claim 1, and a blower unit and / or a combustion air supply pipe, a suction air supply pipe and the like are provided in the secondary combustion chamber. .

従って、請求項2は、請求項1の目的を達成できること、この目的を達成するに最適な排気ガス排出路と二次燃焼室の構造を提供できること等の特徴がある。   Therefore, the second aspect is characterized in that the object of the first aspect can be achieved, and the structure of the exhaust gas discharge passage and the secondary combustion chamber that are optimal for achieving the object can be provided.

請求項3の発明は、請求項1の撹拌軸は、炭化炉に設けた耐熱手段を経由して延設し、この延設した上端に連結用フランジを設け、この連結用フランジは前記炭化炉に開閉自在に設けてなるタワーフレームに軸承した連結軸に連結可能とし、またこの連結軸に設けた歯車にチェーンを介して駆動部に連繋し、この駆動部を前記タワーフレームに設ける構成とした炭化装置である。   According to a third aspect of the present invention, the stirring shaft of the first aspect is extended through a heat-resistant means provided in the carbonization furnace, and a connecting flange is provided at the extended upper end. It can be connected to a connecting shaft that is supported by a tower frame that can be freely opened and closed, and is connected to a driving portion via a chain on a gear provided on the connecting shaft, and this driving portion is provided on the tower frame. It is a carbonization device.

従って、請求項3は、請求項1の目的を達成できること、この目的を達成するに最適な撹拌軸を提供し、またこの撹拌軸の清掃の容易化と、交換の容易な撹拌軸を提供できる等の特徴がある。   Accordingly, the third aspect of the present invention can achieve the object of the first aspect, provides an optimum stirring shaft for achieving the object, and can facilitate the cleaning of the stirring shaft and provide a stirring shaft that can be easily replaced. There are features such as.

請求項4の発明は、請求項1に記載の炭材供給機構は、ホッパーと、ホッパーの収歛口に設けた収歛口と相似形の中間チャンバーと、中間チャンバーの駆動を司る第一のシリンダーと、また中間チャンバーの移動端に設けた中間チャンバーの開閉を司るシャッターと、シャッターの下部に設けたシャッターに連通する連通口を供えた供給路と、供給路内を移動するピストン形の摺動チャンバーと、摺動チャンバーを可動する第三のシリンダーとでなる炭化装置である。   According to a fourth aspect of the present invention, there is provided a carbonaceous material supply mechanism according to the first aspect of the present invention, comprising a hopper, an intermediate chamber similar to a converging port provided at the converging port of the hopper, and a first cylinder that controls the driving of the intermediate chamber. In addition, a shutter for opening and closing the intermediate chamber provided at the moving end of the intermediate chamber, a supply path provided with a communication port communicating with the shutter provided at the lower part of the shutter, and a piston-type sliding chamber that moves in the supply path And a carbonization device comprising a third cylinder that moves the sliding chamber.

従って、請求項4は、請求項1の目的を達成できること、この目的を達成するに最適な炭材供給機構を提供し、またこの炭材供給機構の提供を介して乾留ガスの逆流防止と、この逆流に基づくトラブル、例えば、廃材チップへの着火防止が図れること、そして、この加熱室における熱効率を確保するとともに、熱交換を介して炭化の促進と、高品質の炭化物を生成できること等の特徴がある。   Accordingly, claim 4 can achieve the object of claim 1, provides a carbon material supply mechanism that is optimal for achieving this object, and prevents the backflow of dry distillation gas through the provision of this carbon material supply mechanism. Troubles based on this reverse flow, for example, prevention of ignition of waste chips, and ensuring thermal efficiency in this heating chamber, promotion of carbonization through heat exchange, and generation of high quality carbides, etc. There is.

請求項5の発明は、請求項4に記載の中間チャンバーの容積に対して、摺動チャンバーの容積を大きくする炭化装置である。   A fifth aspect of the present invention is a carbonization apparatus that increases the volume of the sliding chamber with respect to the volume of the intermediate chamber according to the fourth aspect.

従って、請求項5は、請求項1の目的を達成できること、この目的を達成するに最適な中間チャンバー及び/又は摺動チャンバーを提供できること等の特徴がある。   Therefore, claim 5 is characterized in that the object of claim 1 can be achieved, and that an intermediate chamber and / or a sliding chamber optimal for achieving the object can be provided.

以下、本発明の実施の態様(形態)を説明する。   Hereinafter, embodiments (forms) of the present invention will be described.

先ず図面の説明をすると、図1は炭化装置に付設されたフレーム、屋根、柵(図示せず)等の必要機材を含めて示した全体正面図、図2は図1の要部の断面図、図3は図1の要部の平面図、図4は図1に示した加熱室、炭化筒、撹拌軸等の要部を示した断面図、図5は図1の全体側面図、図6は図4に示した炭化筒、撹拌軸等の要部を示した拡大断面図、図7は図4に示した炭化筒、撹拌軸の要部を示した拡大断面図、図8は炭材供給機構の全体を示した拡大正面図、図9は図8の背面図、図10は図8の平面図、図11は図8の左側面図、図12は図8の右側面図、図13は炭化炉の上方に設けたタワーフレームと連結軸、駆動部、ワイヤ等を示した一部欠截の拡大断面図、図14は図13に示したタワーフレームと連結軸、駆動部、ワイヤ等を示した拡大平面図、図15は図13に示したタワーフレームと連結軸、駆動部、ワイヤ等を示した拡大左側面図、図16は図13に示したタワーフレームと連結軸、駆動部、ワイヤ等を示した拡大右側面図である。   First, the drawings will be explained. FIG. 1 is an overall front view including necessary equipment such as a frame, a roof, a fence (not shown) attached to the carbonization apparatus, and FIG. 2 is a cross-sectional view of the main part of FIG. 3 is a plan view of the main part of FIG. 1, FIG. 4 is a sectional view showing the main part of the heating chamber, carbonization cylinder, stirring shaft and the like shown in FIG. 1, and FIG. 5 is an overall side view of FIG. 6 is an enlarged cross-sectional view showing the main parts of the carbonization cylinder and the stirring shaft shown in FIG. 4, FIG. 7 is an enlarged cross-sectional view showing the main part of the carbonization cylinder and the stirring shaft shown in FIG. 4, and FIG. FIG. 9 is a back view of FIG. 8, FIG. 10 is a plan view of FIG. 8, FIG. 11 is a left side view of FIG. 8, and FIG. 12 is a right side view of FIG. FIG. 13 is an enlarged cross-sectional view of a partial cutout showing a tower frame provided above the carbonization furnace, a connecting shaft, a drive unit, and a wire, and FIG. 14 shows a tower frame, a connecting shaft, a drive unit, and the like shown in FIG. Wai FIG. 15 is an enlarged left side view showing the tower frame and connecting shaft, drive unit, wires, etc. shown in FIG. 13, and FIG. 16 is a tower frame, connecting shaft and drive shown in FIG. It is the expansion right view which showed a part, a wire, etc.

本発明は、フレームAに設けた耐熱及び/又は耐火構造の炭化炉Cと、この炭化炉Cの上方の一方側に設けた炭材供給機構B(廃材チップ供給機構)と、またこの炭化炉Cの下方の接線方向に設けた排気ガス排出路D(乾留ガス排出路)と、この排気ガス排出路Dに連設した耐熱及び/又は耐火構造の排気ガス二次燃焼室E(乾留ガス二次燃焼室)と、前記炭化炉Cの上方に設けたタワーフレームFとを主構成要素とする。以下、個別に説明する。   The present invention includes a carbonization furnace C having a heat-resistant and / or refractory structure provided in a frame A, a carbon material supply mechanism B (waste material chip supply mechanism) provided on one side above the carbonization furnace C, and the carbonization furnace. Exhaust gas discharge passage D (dry distillation gas discharge passage) provided in the tangential direction below C, and a heat-resistant and / or refractory exhaust gas secondary combustion chamber E (dry distillation gas second passage) connected to the exhaust gas discharge passage D The main combustion chamber) and the tower frame F provided above the carbonization furnace C are main components. Hereinafter, it demonstrates individually.

炭化炉Cは、下方本体部C1と収斂された上方筒部C2とで構成し、この下方本体部C1には加熱室1と、この加熱室1に囲繞された炭化筒2とを設け、またこの下方本体部C1にはバーナ3と炭化筒2用の開口部4、並びに排気ガス排出路4とを設ける。そして、この炭化筒2の開口200と前記加熱室1とは、開口部4及び/又は連通路201を介して連通されており、炭化筒2からの乾留ガスの略全部を加熱室1に送り、バーナ3を介して再燃焼して熱風に変換し、この熱風との熱交換で炭化筒2に投入された廃材チップW1を炭化する。この乾留ガスの再燃焼で、燃料の節約と、二酸化炭素の発生回避及び/又は量の削減化等を図る。またこの炭化筒2には筒状の撹拌軸5が吊下(垂下)されており、この撹拌軸5には間欠式に撹拌羽根500が設けられている。この撹拌羽根500は、廃材チップW1及び/又は炭化物Wの撹拌と流下とを図り、この廃材チップW1及び/又は炭化物Wを炭化筒2の壁面への移動を介して熱交換の促進が図れる可能があり有益である。また撹拌羽根500を間欠式に設けることで、炭化筒2内に存在する廃材チップW1及び/又は炭化物Wの滞留時間の確保と、炭化の効率化等が図れる。尚、この撹拌軸5は炭化筒2の上方に延設されており、その上部は筒外に至り、その上部端には連結用フランジ501が設けられている。またこの炭化筒2の開口部202と炭化炉Cの閉口部C3との間にはホッパー形状の排出口6を着脱自在に設ける。そして、この排出口6(炭化筒2の下部に設けた開口)には円錐形状のダンパー7(開閉具)を設け、このダンパー7の降下で閉塞し、その上昇で開放する構造となっている。そして、このダンパー7の降下・上昇はワイヤ8(チェーン等の懸架手段であれば採用できる)で操作する。従って、このワイヤ8の一端はダンパー7に固止されている。またこのワイヤ8は撹拌軸5内を貫通し、他端がタワーフレームFに設けた捲装手段9(巻取り装置)に捲装されていることから、この捲装手段9の操作で、弛緩(巻戻し)又は緊張(巻取り)される。このワイヤ8の弛緩又は緊張で、ダンパー7が降下・上昇する構造である。尚、炭化炉Cは、下方本体部C1から収斂部を介して上方筒部C2を形成する構成とすることで、炭化筒2からの乾留ガスの上方筒部C2への容易な排気と、所望する乾留ガスを加熱室1に流下できる利点がある。図中600は排出口6を受ける台座である。   The carbonization furnace C is composed of a lower main body C1 and a converged upper cylinder C2. The lower main body C1 is provided with a heating chamber 1 and a carbonization cylinder 2 surrounded by the heating chamber 1, and The lower body C1 is provided with a burner 3, an opening 4 for the carbonizing cylinder 2, and an exhaust gas discharge passage 4. The opening 200 of the carbonization cylinder 2 and the heating chamber 1 are communicated with each other via the opening 4 and / or the communication path 201, and substantially all of the dry distillation gas from the carbonization cylinder 2 is sent to the heating chamber 1. Then, it is recombusted through the burner 3 and converted into hot air, and the waste chip W1 put into the carbonizing cylinder 2 is carbonized by heat exchange with the hot air. By reburning the dry distillation gas, fuel is saved, carbon dioxide is avoided and / or the amount is reduced. Further, a cylindrical stirring shaft 5 is suspended (hanging down) on the carbonization cylinder 2, and the stirring blade 500 is provided on the stirring shaft 5 intermittently. The stirring blade 500 can stir and flow down the waste material chip W1 and / or the carbide W, and can promote heat exchange through the movement of the waste material chip W1 and / or the carbide W to the wall surface of the carbonization cylinder 2. Is beneficial. Further, by providing the stirring blades 500 intermittently, it is possible to secure the residence time of the waste material chips W1 and / or the carbides W existing in the carbonizing cylinder 2, and to increase the efficiency of carbonization. The agitation shaft 5 extends above the carbonization cylinder 2, the upper part thereof reaches the outside of the cylinder, and a connecting flange 501 is provided at the upper end thereof. A hopper-shaped discharge port 6 is detachably provided between the opening 202 of the carbonization cylinder 2 and the closing portion C3 of the carbonization furnace C. A conical damper 7 (opening / closing tool) is provided at the discharge port 6 (opening provided in the lower portion of the carbonizing cylinder 2), and is closed when the damper 7 is lowered and opened when the damper 7 is raised. . The lowering / raising of the damper 7 is operated by a wire 8 (which can be adopted by a suspension means such as a chain). Therefore, one end of the wire 8 is fixed to the damper 7. Further, since the wire 8 passes through the stirring shaft 5 and the other end is mounted on the mounting means 9 (winding device) provided on the tower frame F, the wire 8 is loosened by the operation of the mounting means 9. (Rewinding) or tension (winding). This is a structure in which the damper 7 is lowered and raised by the relaxation or tension of the wire 8. The carbonization furnace C has a configuration in which the upper cylinder part C2 is formed from the lower body part C1 through the converging part, so that it is possible to easily exhaust the dry distillation gas from the carbonization cylinder 2 to the upper cylinder part C2, There is an advantage that the dry distillation gas can flow down into the heating chamber 1. In the figure, reference numeral 600 denotes a pedestal for receiving the outlet 6.

尚、この炭化炉Cの開口部C3には、炭化物冷却室G(水冷式が簡便でよいが、空冷式等も有り得る)と搬送用コンベヤHが設けられている。図中G1は炭化物冷却室Gの開閉蓋を示す。この炭化物冷却室Gで連脚した炭化物Wは、搬送用コンベヤHで所定のヤード及び/又は容器等に送られる。   The opening C3 of the carbonization furnace C is provided with a carbide cooling chamber G (a water-cooling type may be simple, but an air-cooling type or the like is also possible) and a transfer conveyor H. In the figure, G1 indicates an open / close lid of the carbide cooling chamber G. The carbide W that is connected in the carbide cooling chamber G is sent to a predetermined yard and / or container by the conveyor H for conveyance.

この炭化炉Cの接線方向に設けた排気ガス排出路D(乾留ガス排出路)には排気ガス二次燃焼室Eが連通されていることから、前述の如く、加熱室1に至った乾留ガスを複数のバーナ3で熱風とし、この熱風で熱交換し、働き終えた排気ガスは、排気ガス排出路D(炭化炉Cの接線方向に設けた排気ガス排出路D)より排気ガス二次燃焼室Eに導かれ、導入した空気中の雰囲気下で二次燃焼される。この二次燃焼した略無臭及び/又は略無色・無害状態となった最終の排気ガスは、煙突10を介して空気中に拡散される。従って、乾留ガスの有効利用と、公害の回避が図れる。また前記働き終えた排気ガスを、接線方向に設けた排気ガス排出路Dに確実、スムーズに送風できる。   Since the exhaust gas secondary combustion chamber E communicates with the exhaust gas discharge passage D (dry distillation gas discharge passage) provided in the tangential direction of the carbonization furnace C, the dry distillation gas reaching the heating chamber 1 as described above. The exhaust gas is heated by a plurality of burners 3 and exchanged with the hot air, and exhaust gas that has finished working is subjected to secondary combustion of exhaust gas from an exhaust gas discharge path D (exhaust gas discharge path D provided in the tangential direction of the carbonization furnace C). It is led to the chamber E and subjected to secondary combustion under the atmosphere in the introduced air. The final exhaust gas that has become substantially odorless and / or substantially colorless and harmless after the secondary combustion is diffused into the air through the chimney 10. Therefore, effective utilization of dry distillation gas and avoidance of pollution can be achieved. In addition, the exhaust gas that has finished working can be reliably and smoothly blown into the exhaust gas discharge passage D provided in the tangential direction.

炭材供給機構Bは、上部筒部C2に突出した導入管C20に連通するフレームA1に偏倚して設けた供給路11と、この供給路11内を略密着状態で移動(摺動移動)する摺動チャンバー12と、この摺動チャンバー12を可動する第三のシリンダー13と、前記フレームA1に移動可能に設けた中間チャンバー14と、この中間チャンバー14の開放底部140を一定の箇所で隠蔽するフレームA1に設けた底板15と、前記中間チャンバー14の開口140を開閉するシャッター16と、前記シャッター16を可動する第二のシリンダー17と、また前記中間チャンバー14を可動する第一のシリンダー18と、さらにこの中間チャンバー14に廃材チップW1を供給するホッパー19とで構成されている。従って、ホッパー19に供給された廃材チップW1はホッパー19の一部を兼用する中間チャンバー14に導入される。この中間チャンバー14の開放底部140は、ホッパー19と連通し、ホッパー14の一部となる位置関係(フレームA1の中心位置「図10の破線で示した位置」)においては、底板15により閉塞されている。従って、この中間チャンバー14には、ホッパー14内の廃材チップW1が収容(充填)されている。この廃材チップW1の充填状態で、第一のシリンダー18を可動し、当該中間チャンバー14が移動端に達した段階で、前記底板15に設けた開口150に位置することから、この中間チャンバー14の開放底部140は開放状態となり、廃材チップW1は摺動チャンバー12に落込まれる(フレームA1の左端位置「図12の破線で示した位置」)。そして、中間チャンバー14の容積に対して、摺動チャンバー12の容積を大きくし、廃材チップW1をこの摺動チャンバー12に山なりに落込む構造となっている。尚、この炭材供給機構Bは、上方筒部C2に存在する乾留ガスの逆流を防止するために、摺動チャンバー12を供給路11に略密着状態に収容するとともに、シャッター16及び/又は中間チャンバー14を介して防止する構造である。尚、この逆流防止は、乾留ガスの効率的な利用が図れること、乾留ガスの温度低下等を回避できること等の特徴がある。また摺動チャンバー12が上方筒部C2に至り、収容する廃材チップW1を炭化筒2に落込む状態では、中間チャンバー14は、ホッパー19の直下にあり(フレームA1の中心位置)、この供給路11及び/又は開口150とは離間されるとともに、この炭化筒2とは完全に離間されている。従って、ホッパー19内の廃材チップW1への着火は全くなく安全である。また爆発等の危険性を回避できる特徴がある。尚、この炭材供給機構Bは、一例であり、簡易な構造では図示しないがスクリューコンベア方式、落下方式、バケット供給方式等の採用も可能である。   The carbonaceous material supply mechanism B moves (slidably moves) in a substantially tight state in the supply path 11 provided in a biased manner in the frame A1 communicating with the introduction pipe C20 protruding from the upper cylindrical portion C2. The sliding chamber 12, the third cylinder 13 that moves the sliding chamber 12, the intermediate chamber 14 that is movably provided on the frame A1, and the open bottom 140 of the intermediate chamber 14 are concealed at a certain location. A bottom plate 15 provided on the frame A1, a shutter 16 for opening and closing the opening 140 of the intermediate chamber 14, a second cylinder 17 for moving the shutter 16, and a first cylinder 18 for moving the intermediate chamber 14. Further, the intermediate chamber 14 includes a hopper 19 for supplying the waste chip W1. Accordingly, the waste chip W1 supplied to the hopper 19 is introduced into the intermediate chamber 14 that also serves as a part of the hopper 19. The open bottom portion 140 of the intermediate chamber 14 communicates with the hopper 19 and is closed by the bottom plate 15 in a positional relationship (a center position of the frame A1 “position indicated by a broken line in FIG. 10”) that becomes a part of the hopper 14. ing. Therefore, the waste material chip W <b> 1 in the hopper 14 is accommodated (filled) in the intermediate chamber 14. The first cylinder 18 is moved in the state where the waste chip W1 is filled, and the intermediate chamber 14 is positioned at the opening 150 provided in the bottom plate 15 when the intermediate chamber 14 reaches the moving end. The open bottom 140 is opened, and the waste chip W1 is dropped into the sliding chamber 12 (the left end position of the frame A1 “position indicated by the broken line in FIG. 12”). Then, the volume of the sliding chamber 12 is made larger than the volume of the intermediate chamber 14, and the waste chip W1 is dropped into the sliding chamber 12 in a mountain shape. The carbonaceous material supply mechanism B accommodates the sliding chamber 12 in a substantially tight contact state with the supply path 11 and prevents the shutter 16 and / or intermediate in order to prevent backflow of the dry distillation gas existing in the upper cylindrical portion C2. This is a structure to prevent through the chamber 14. In addition, this backflow prevention has the characteristics that an efficient utilization of dry distillation gas can be aimed at, the temperature fall of dry distillation gas, etc. can be avoided. Further, when the sliding chamber 12 reaches the upper cylinder portion C2 and the waste chip W1 to be accommodated falls into the carbonization cylinder 2, the intermediate chamber 14 is directly below the hopper 19 (center position of the frame A1), and this supply path 11 and / or the opening 150 and completely separated from the carbonization cylinder 2. Therefore, there is no ignition to the waste material chip W1 in the hopper 19 and it is safe. In addition, there is a feature that can avoid danger such as explosion. The carbonaceous material supply mechanism B is an example, and although a simple structure is not shown, a screw conveyor method, a drop method, a bucket supply method, or the like can be employed.

タワーフレームFは、炭化炉Cの上方に取付け、取外し自在又は可動自在に設け、前記撹拌軸5の取付け、取外しの際に、この炭化炉Cから一時的に離間できる構成となっている。このタワーフレームFには、数段の区画板F1〜Fn等を介して第一のスペース21〜第三のスペース21nに区画する。そして、この第一のスペース21〜第三のスペース21nには、回転自在の連結軸22を垂設する。この連結軸22の垂設は、区画板F1、F2に設けた各軸受け23〜23nを介して確保する。そして、この連結軸22に設けたスプロケット24は懸架したチェーン25及び/又はモータ26を介して回転される。尚、連結軸22の下端に設けた被連結用フランジ220には、前述の撹拌軸5に設けた連結用フランジ501が合体され、かつ緊締具(図示せず)により固止される。これにより、撹拌軸5は連結軸22と同時に回転する。そして、この連結軸22にはダンパー7を吊下するワイヤ8が貫設されている。このワイヤ8はタワーフレームFに設けた滑車27を経由して捲装手段9に捲装されている。この構成により、捲装手段9の操作(駆動)で、ワイヤ8を弛緩又は緊張し、ダンパー7の降下・上昇を図るとともに、排出口6を開閉する。尚、前記撹拌軸5及び/又は撹拌はね500の修理又は交換等の際において、この撹拌軸5を取外す場合には、連結用フランジ501と被連結用フランジ220との合体を開放し、タワーフレームFを炭化炉Cより取外して離間する。このタワーフレームFの離間で、この炭化炉Cの上方筒部C2が開放されるので、この撹拌軸5を炭化炉Cより引抜いた後において、修理及び/又は交換を図ることが可能となる。尚、図中28は断熱手段の一例である石綿ケース、29は同様に一例である断熱ファイバーを示す。   The tower frame F is provided above the carbonization furnace C so as to be detachable or movable. The tower frame F can be temporarily separated from the carbonization furnace C when the stirring shaft 5 is attached or removed. The tower frame F is partitioned into a first space 21 to a third space 21n through several stages of partition plates F1 to Fn. A rotatable connecting shaft 22 is suspended from the first space 21 to the third space 21n. The suspending of the connecting shaft 22 is ensured through the bearings 23 to 23n provided on the partition plates F1 and F2. The sprocket 24 provided on the connecting shaft 22 is rotated via a suspended chain 25 and / or a motor 26. The connecting flange 220 provided at the lower end of the connecting shaft 22 is combined with the connecting flange 501 provided on the agitation shaft 5 and fixed by a fastening tool (not shown). Thereby, the stirring shaft 5 rotates simultaneously with the connecting shaft 22. The connecting shaft 22 is provided with a wire 8 that suspends the damper 7. The wire 8 is mounted on the mounting means 9 via a pulley 27 provided on the tower frame F. With this configuration, the operation (drive) of the rigging means 9 relaxes or tensions the wire 8 to lower and raise the damper 7 and open / close the discharge port 6. When the agitation shaft 5 and / or the agitation splash 500 is repaired or replaced, when the agitation shaft 5 is removed, the coupling of the connecting flange 501 and the connected flange 220 is opened, and the tower The frame F is removed from the carbonization furnace C and separated. Since the upper cylindrical portion C2 of the carbonization furnace C is opened by the separation of the tower frame F, after the stirring shaft 5 is pulled out from the carbonization furnace C, repair and / or replacement can be achieved. In the figure, 28 indicates an asbestos case which is an example of a heat insulating means, and 29 similarly indicates a heat insulating fiber which is an example.

尚、図中Iは屋根、Jは送風機ユニット、Kはエア供給管をそれぞれ示す。   In the figure, I represents a roof, J represents a blower unit, and K represents an air supply pipe.

次に本発明の炭化装置の作用を概述すると、ホッパー19に供給された廃材チップW1は、ホッパー19の収歛口を経由して中間チャンバー14(収斂口と相似形のチャンバー)に導入された後、この廃材チップW1が充填された中間チャンバー14は、第一のシリンダー18により、移動端に達した段階で、底板15に設けた開口150を介して摺動チャンバー12に山なりに落込む構造となっている。この落込まれた廃材チップW1は、当該摺動チャンバー12が第三のシリンダー13により押圧されることで、供給路11を前進し、その前進端に達した段階で、炭化炉Cの上方筒部C2に至る。この摺動チャンバー12の前面及び/又は先端底部より炭化筒2内に廃材チップW1を投入する。この炭化筒2内に投入された廃材チップW1は、撹拌羽根500で解されながら(団子状にならず)下方に向かって順次送込まれる。この送込まれる過程で炭化されるとともに、この廃材チップW1は炭化筒2の周壁部に導かれて、乾留ガス(熱風)との熱交換を介して効率よく、かつ高温(略700℃〜850℃)雰囲気の中で炭化される。従って、炭化物Wは、高品質で、火力が強く、また脱臭、吸着性が優れた物性を備えており、本来の炭と略同程度の物性を備えている。そして、本発明では、従来の炭化装置では不可能であった物性を備えた炭化物Wを製造できる。   Next, the operation of the carbonization apparatus of the present invention will be outlined. After the waste chip W1 supplied to the hopper 19 is introduced into the intermediate chamber 14 (chamber similar to the converging port) via the converging port of the hopper 19. The intermediate chamber 14 filled with the waste chip W1 is dropped into the sliding chamber 12 through the opening 150 provided in the bottom plate 15 when reaching the moving end by the first cylinder 18. It has become. The dropped waste material chip W1 is moved forward in the supply path 11 by the sliding chamber 12 being pressed by the third cylinder 13 and reaches the forward end thereof. It reaches C2. Waste material chips W1 are put into the carbonization cylinder 2 from the front surface and / or the bottom of the tip of the sliding chamber 12. The waste material chips W <b> 1 thrown into the carbonization cylinder 2 are sequentially fed downward while being unwound by the stirring blades 500 (not in a dumpling shape). While being carbonized in this process, the waste chip W1 is led to the peripheral wall portion of the carbonization cylinder 2, and efficiently and at a high temperature (approximately 700 ° C. to 850 ° C.) through heat exchange with the dry distillation gas (hot air). ° C) is carbonized in the atmosphere. Therefore, the carbide W has high quality, strong thermal power, physical properties excellent in deodorizing and adsorbing properties, and has substantially the same physical properties as the original charcoal. And in this invention, the carbide | carbonized_material W provided with the physical property which was impossible with the conventional carbonization apparatus can be manufactured.

尚、この炭化筒2で発生した乾留ガスは、連通路201を介して略全部を加熱室1に送り、バーナ3を介して再燃焼して熱風に変換し、前述の如く、この熱風との熱交換で炭化筒2に投入された廃材チップW1を炭化する。この炭化筒2で生成された炭化物Wは、炭化筒2の下方に至り、排出口6に達した後、この排出口6を閉塞するダンパー7の開放により落下し炭化物冷却室Gに送られる。その後、搬送用コンベヤHで所定の箇所に搬送、収容等する。尚、加熱室1で生成された熱風は、熱交換用として利用された後(働きを終えた乾留ガス)、排気ガス排出路Dより排気ガス二次燃焼室Eに導かれて、二次燃焼される。この二次燃焼された排気ガスは、煙突10を介して空気中に拡散される。以上で説明した廃材チップW1の供給と、炭化物Wの排出は間欠式に行われるが、炭化装置は連続式に稼働される。   The carbonized gas generated in the carbonization cylinder 2 is almost entirely sent to the heating chamber 1 through the communication path 201, recombusted through the burner 3 and converted into hot air, and as described above, The waste chip W1 charged into the carbonization cylinder 2 by heat exchange is carbonized. The carbide W generated in the carbonization cylinder 2 reaches the lower side of the carbonization cylinder 2 and reaches the discharge port 6. Then, the carbide W falls by opening the damper 7 that closes the discharge port 6 and is sent to the carbide cooling chamber G. Then, it conveys, accommodates, etc. in a predetermined location with the conveyor H for conveyance. The hot air generated in the heating chamber 1 is used for heat exchange (the dry distillation gas that has finished its work), and is then led from the exhaust gas discharge passage D to the exhaust gas secondary combustion chamber E to be subjected to secondary combustion. Is done. The secondary combustion exhaust gas is diffused into the air through the chimney 10. Although the supply of the waste chip W1 and the discharge of the carbide W described above are performed intermittently, the carbonization apparatus is operated continuously.

図1は炭化装置に付設されたフレーム、屋根等の必要機材を含めて示した全体正面図Fig. 1 is an overall front view showing necessary equipment such as frames and roofs attached to the carbonization equipment. 図2は図1の要部の断面図2 is a cross-sectional view of the main part of FIG. 図3は図1の要部の平面図3 is a plan view of the main part of FIG. 図4は図1に示した加熱室、炭化筒、撹拌軸等の要部を示した断面図4 is a cross-sectional view showing the main parts of the heating chamber, carbonization cylinder, stirring shaft, etc. shown in FIG. 図5は図1の全体側面図5 is an overall side view of FIG. 図6は図4に示した炭化筒、撹拌軸等の要部を示した拡大断面図6 is an enlarged cross-sectional view showing the main parts such as the carbonization cylinder and the stirring shaft shown in FIG. 図7は図4に示した炭化筒、撹拌軸の要部を示した拡大断面図FIG. 7 is an enlarged cross-sectional view showing the main parts of the carbonization cylinder and the stirring shaft shown in FIG. 図8は炭材供給機構の全体を示した拡大正面図FIG. 8 is an enlarged front view showing the entire carbonaceous material supply mechanism. 図9は図8の背面図9 is a rear view of FIG. 図10は図8の平面図10 is a plan view of FIG. 図11は図8の左側面図11 is a left side view of FIG. 図12は図8の右側面図12 is a right side view of FIG. 図13は炭化炉の上方に設けたタワーフレームと連結軸、駆動部、ワイヤ等を示した一部欠截の拡大断面図FIG. 13 is an enlarged cross-sectional view of a partially cutout showing a tower frame, a connecting shaft, a drive unit, wires, and the like provided above the carbonization furnace 図14は図13に示したタワーフレームと連結軸、駆動部、ワイヤ等を示した拡大平面図FIG. 14 is an enlarged plan view showing the tower frame, the connecting shaft, the drive unit, the wires, etc. shown in FIG. 図15は図13に示したタワーフレームと連結軸、駆動部、ワイヤ等を示した拡大左側面図FIG. 15 is an enlarged left side view showing the tower frame, the connecting shaft, the drive unit, the wires, etc. shown in FIG. 図16は図13に示したタワーフレームと連結軸、駆動部、ワイヤ等を示した拡大右側面図16 is an enlarged right side view showing the tower frame, the connecting shaft, the drive unit, the wires, etc. shown in FIG.

符号の説明Explanation of symbols

A フレーム
A1 フレーム
B 炭材供給機構
C 炭化炉
C1 下方本体部
C2 上方筒部
C3 開口部
C20 導入管
D 排気ガス排出路
E 排気ガス二次燃焼室
F タワーフレーム
F1〜Fn 区画板
G 炭化物冷却室
G1 開閉蓋
H 搬送用コンベヤ
I 屋根
J 送風ユニット
K エア供給管
W 炭化物
W1 廃材チップ
1 加熱室
2 炭化筒
200 開口
201 連通路
202 開口部
3 バーナ
4 開口部
5 撹拌軸
500 撹拌羽根
501 連結用フランジ
6 排出口
600 台座
7 ダンパー
8 ワイヤ
9 捲装手段
10 煙突
11 供給路
12 摺動チャンバー
13 第三のシリンダー
14 中間チャンバー
140 開放底部
15 底板
150 開口
16 シャッター
17 第二のシリンダー
18 第一のシリンダー
19 ホッパー
21〜21n 第一のスペース〜第三のスペース
22 連結軸
220 被連結用フランジ
23〜23n 軸受け
24 スプロケット
25 チェーン
26 モータ
27 滑車
28 石綿ケース
29 断熱ファイバー
A Frame A1 Frame B Carbonaceous material supply mechanism C Carbonization furnace C1 Lower body C2 Upper cylinder C3 Opening C20 Inlet pipe D Exhaust gas discharge path E Exhaust gas secondary combustion chamber F Tower frame F1 to Fn Partition plate G Carbide cooling chamber G1 Opening / closing lid H Conveyor I Roof J Air supply unit K Air supply pipe W Carbide W1 Waste material chip 1 Heating chamber 2 Carbonization cylinder 200 Opening 201 Communication path 202 Opening part 3 Burner 4 Opening part 5 Stirring shaft 500 Stirring blade 501 Connecting flange 6 Discharge port 600 Pedestal 7 Damper 8 Wire 9 Fitting means 10 Chimney 11 Supply path 12 Sliding chamber 13 Third cylinder 14 Intermediate chamber 140 Open bottom 15 Bottom plate 150 Opening 16 Shutter 17 Second cylinder 18 First cylinder 19 Hoppers 21 to 21n First space to third space 22 Connecting shaft 2 20 Connected flanges 23 to 23n Bearing 24 Sprocket 25 Chain 26 Motor 27 Pulley 28 Asbestos case 29 Insulating fiber

Claims (5)

炭材供給機構を上方の一方側に、また排気ガス排出路を下方の接線方向にそれぞれ備えた炭化炉内に、加熱室と、この加熱室に囲繞されるように上下部を開放した炭化筒とを設けてなる構成であって、
前記加熱室と炭化筒とを連通路を介して連通し、また前記加熱室にバーナ等の加熱部を設け、前記炭化炉の上部より吊下した回転自在の撹拌軸を前記炭化筒に垂下し、この撹拌軸に間欠式に撹拌羽根を設け、またこの撹拌軸内を貫通するワイヤの上部を前記炭化炉の捲装手段に設けるとともに、その下部を炭化筒の下部に至らしめ、このワイヤの下部に開閉具を吊下し、この開閉具を介して前記炭化筒の下部に設けた開口を開閉し、この開口の下部に排出機構を設ける構成とした炭化装置。
Inside a carbonization furnace equipped with a carbonaceous material supply mechanism on one upper side and an exhaust gas discharge path in the lower tangential direction, a heating chamber and a carbonization cylinder with upper and lower parts opened so as to be surrounded by the heating chamber It is the structure formed by providing
The heating chamber communicates with the carbonizing cylinder through a communication passage, and a heating unit such as a burner is provided in the heating chamber, and a rotatable stirring shaft suspended from the upper part of the carbonizing furnace is suspended from the carbonizing cylinder. The stirring shaft is intermittently provided on the stirring shaft, and the upper part of the wire penetrating the stirring shaft is provided in the outfitting means of the carbonization furnace, and the lower part thereof is led to the lower part of the carbonization cylinder. A carbonization apparatus having a configuration in which an opening / closing tool is suspended at a lower portion, an opening provided at a lower portion of the carbonization cylinder is opened / closed via the opening / closing tool, and a discharge mechanism is provided below the opening.
請求項1の排気ガス排出路に二次燃焼室を形成し、この二次燃焼室内に送風ユニット及び/又は燃焼エア供給管・吸引エア供給管等を付設する構成とした炭化装置。   A carbonization apparatus having a structure in which a secondary combustion chamber is formed in the exhaust gas discharge passage according to claim 1 and a blower unit and / or a combustion air supply pipe / suction air supply pipe are attached to the secondary combustion chamber. 請求項1の撹拌軸は、炭化炉に設けた耐熱手段を経由して延設し、この延設した上端に連結用フランジを設け、この連結用フランジは前記炭化炉に開閉自在に設けてなるタワーフレームに軸承した連結軸に連結可能とし、またこの連結軸に設けた歯車にチェーンを介して駆動部に連繋し、この駆動部を前記タワーフレームに設ける構成とした炭化装置。   The stirring shaft according to claim 1 is extended through a heat-resistant means provided in the carbonization furnace, and a connecting flange is provided at the extended upper end, and the connection flange is provided in the carbonization furnace so as to be openable and closable. A carbonization apparatus configured to be connectable to a connecting shaft supported by a tower frame, and to be connected to a driving unit via a chain on a gear provided on the connecting shaft, and to provide the driving unit on the tower frame. 請求項1に記載の炭材供給機構は、ホッパーと、このホッパーの収歛口に設けたこの収歛口と相似形の中間チャンバーと、この中間チャンバーの駆動を司る第一のシリンダーと、またこの中間チャンバーの移動端に設けた当該中間チャンバーの開閉を司るシャッターと、このシャッターの下部に設けた当該シャッターに連通する連通口を供えた供給路と、この供給路内を移動するピストン形の摺動チャンバーと、この摺動チャンバーを可動する第三のシリンダーとで構成した炭化装置。   The carbonaceous material supply mechanism according to claim 1 includes a hopper, an intermediate chamber similar to the converging port provided at the converging port of the hopper, a first cylinder that controls the driving of the intermediate chamber, and the intermediate A shutter for opening and closing the intermediate chamber provided at the moving end of the chamber, a supply path provided with a communication port communicating with the shutter provided at the lower part of the shutter, and a piston-type sliding moving in the supply path A carbonization device comprising a chamber and a third cylinder that moves the sliding chamber. 請求項4に記載の中間チャンバーの容積に対して、摺動チャンバーの容積を大きくする構成とした炭化装置。   A carbonization apparatus configured to increase the volume of the sliding chamber with respect to the volume of the intermediate chamber according to claim 4.
JP2005034967A 2005-02-10 2005-02-10 Carbonizing apparatus Pending JP2006219597A (en)

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109022001A (en) * 2018-08-16 2018-12-18 湖北师范大学 A kind of self weight spiral progressive biomass high-efficiency energy-saving pyrolysis furnace apparatus
CN110790273A (en) * 2019-12-03 2020-02-14 郑州铁路职业技术学院 Constant-temperature carbonization-based charcoal making process
JP7197958B1 (en) * 2022-04-27 2022-12-28 株式会社大木工藝 Waste fabric processing method and waste fabric processing apparatus

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109022001A (en) * 2018-08-16 2018-12-18 湖北师范大学 A kind of self weight spiral progressive biomass high-efficiency energy-saving pyrolysis furnace apparatus
CN109022001B (en) * 2018-08-16 2023-04-14 湖北师范大学 Dead weight spiral gradually-advancing type biomass high-efficiency energy-saving pyrolysis furnace device
CN110790273A (en) * 2019-12-03 2020-02-14 郑州铁路职业技术学院 Constant-temperature carbonization-based charcoal making process
CN110790273B (en) * 2019-12-03 2021-08-03 深圳市起源环保科技有限公司 Constant-temperature carbonization-based charcoal making process
JP7197958B1 (en) * 2022-04-27 2022-12-28 株式会社大木工藝 Waste fabric processing method and waste fabric processing apparatus

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