JPH11236572A - Apparatus for carbonization of solid organic material - Google Patents

Apparatus for carbonization of solid organic material

Info

Publication number
JPH11236572A
JPH11236572A JP10038591A JP3859198A JPH11236572A JP H11236572 A JPH11236572 A JP H11236572A JP 10038591 A JP10038591 A JP 10038591A JP 3859198 A JP3859198 A JP 3859198A JP H11236572 A JPH11236572 A JP H11236572A
Authority
JP
Japan
Prior art keywords
furnace
carbonization
container
solid organic
waste
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP10038591A
Other languages
Japanese (ja)
Other versions
JP2951632B2 (en
Inventor
Yoshikazu Kobayashi
由和 小林
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Miike Tekkosho KK
Original Assignee
Miike Tekkosho KK
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Miike Tekkosho KK filed Critical Miike Tekkosho KK
Priority to JP10038591A priority Critical patent/JP2951632B2/en
Publication of JPH11236572A publication Critical patent/JPH11236572A/en
Application granted granted Critical
Publication of JP2951632B2 publication Critical patent/JP2951632B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

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

Landscapes

  • Processing Of Solid Wastes (AREA)
  • Coke Industry (AREA)
  • Solid Fuels And Fuel-Associated Substances (AREA)

Abstract

PROBLEM TO BE SOLVED: To obtain an apparatus which efficiently produces charcoal with a wide variety of applications from solid organic material, has relatively a compact structure with no extra space, can be flexibly adjustable in size according to the amount of waste, and can readily cope with prevention of the generation of dioxin. SOLUTION: An apparatus, in which a transferable container 10 which is so formed of side walls 11 being gas-permeable as to accommodate solid organic matter in a laminated state and the interior of a furnace having a cross-sectional shape almost corresponding to the external shape of a container are made of a refractory material, comprises a carbonization furnace 20A composed of an opening portion 21 which is selectively opened, an ignition portion 25 on upper side and an exhaust path 24 in a bottom portion on the opposite side of the ignition portion 25; a combustion furnace 40 comprised of an inlet portion 40 provided with a burner 47 which burns a combustible gas introduced from the carbonization furnace through the exhaust path 24, a gas flow detour wall 42 and an exhaust outlet portion 43 for letting exhaust gas out; and a flatcar 15 of a small height which can move along a rail R1 provided inside the furnace of the carbonization furnace by way of the opening portion 41 and mount the container.

Description

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

【0001】[0001]

【発明の属する技術分野】この発明は、事業所やオフィ
ス、家庭等から廃棄される各種の廃棄木材や竹、廃棄タ
イヤ等の固形有機質系廃棄物や、各種のプラスチック屑
や紙屑を含む軽量有機質系廃棄物、糞尿汚泥等の粘ちょ
う性有機質系廃棄物を混練、圧密化して得られた固形再
生燃料等の有機質系廃棄物を炭や活性炭に転換して無公
害裏に処理する炭化装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to solid organic waste such as various kinds of waste wood, bamboo, waste tires, and the like, which are discarded from offices, offices, and households, and lightweight organic waste including various types of plastic waste and paper waste. Device that kneads and consolidates viscous organic waste such as bio-waste, manure sludge, etc., and converts the organic waste such as solid regenerated fuel obtained into charcoal or activated carbon into a non-polluting treatment .

【0002】[0002]

【従来の技術】従来より、一般の可燃廃棄物は、大部分
多くの自治体の焼却場で焼却処理されるか、埋立処理さ
れていた。しかし、近年廃棄物の処理に関する状況も変
わって来ており、資源再利用の観点からも、1995年
6月には「容器包装に係わる分別収集及び再商品化の促
進等に関する法律(容器包装リサイクル法)」が制定、
公布された。
2. Description of the Related Art Conventionally, most combustible wastes have been incinerated or landfilled at most local government incineration plants. However, in recent years, the situation regarding waste disposal has changed, and from the viewpoint of resource reuse, in June 1995, the law on the promotion of separate collection and recycling of containers and packaging (container packaging recycling Law) is enacted,
It was promulgated.

【0003】これに伴い、従来安定型とされていた廃棄
物も管理型に変更されて安易に埋立ができなくなって来
た。これと同時に、廃棄プラスチックも分別収集されて
再利用し易くなって来ており、この傾向に沿って、再生
繊維の他、プラスチックを含む廃棄物が高い発熱量を有
していることを考慮したリサイクル方法が研究されるよ
うに成ってきた。また森林破壊を防止して地表の砂漠化
を防いだり、石油枯渇に対策する上で、有機質系廃棄物
を燃料として再生する技術も開発されて来た。
[0003] Along with this, waste which has been conventionally of a stable type has been changed to a management type, and it has become impossible to landfill easily. At the same time, waste plastics have been separated and collected, making it easier to reuse them.In line with this trend, we have considered that wastes including plastics, in addition to recycled fibers, have a high calorific value. Recycling methods have been studied. In addition, technologies to regenerate organic waste as fuel have been developed in order to prevent deforestation and prevent desertification on the surface and countermeasures against oil depletion.

【0004】[0004]

【発明が解決しようとする課題】そのようなプラスチッ
クを含む廃棄物のリサイクルとしては、本願出願人も既
に幾つか提案したように固形燃料の原料として活用する
ことが多かった。このプラスチックからの再生固形燃料
は、染色や晒しの工場やクリーニング所、銭湯やヘルス
センター等のボイラーの燃料として、また石灰やセメン
ト工場、製鉄所等の燃料として広く利用されて好評を博
している。
As the recycling of such waste containing plastic, the applicant of the present invention has often utilized it as a raw material for solid fuel, as already proposed by the present applicant. Recycled solid fuel from plastic is widely used as a fuel for boilers such as dyeing and bleaching factories and cleaning plants, public baths and health centers, and as a fuel for lime, cement factories and steelworks. I have.

【0005】しかし、広く利用されている塩化ビニル等
の塩化物は、必ず廃棄プラスチックに含まれており、従
って再生固形燃料にも含まれている為に燃焼条件いかん
ではダイオキシンが発生する。また可燃廃棄物として、
時には建築廃棄木材、間伐材、竹が大量に出されること
がある。
[0005] However, chlorides such as vinyl chloride, which are widely used, are always contained in waste plastics and are therefore also contained in regenerated solid fuel, so that dioxins are generated depending on combustion conditions. As combustible waste,
Occasionally, large amounts of construction waste wood, thinned wood and bamboo are produced.

【0006】本発明は、上記に鑑み案出されたものであ
って、土壌改良や、河川水浄化や、脱臭等多方面に広い
用途があり、炭酸ガス発生の抑制に寄与できる炭を固形
有機質系廃棄物から効率的に産出できるもので、蒸し焼
きで使用酸素量が少なく、余分な空間が無く正味被処理
物を収容できる比較的コンパクトな構造を有し、廃棄物
の排出量に対して規模を柔軟に対応させることができ、
更にダイオキシンの発生防止等の無公害化について容易
に対策のできる固形有機物の炭化装置を提供することを
目的にしている。
The present invention has been devised in view of the above, and has a wide variety of uses such as soil improvement, river water purification, and deodorization. It can be efficiently produced from system waste, uses less oxygen by steaming, has a relatively compact structure that can accommodate the net processed material without extra space, and is a scale for the amount of waste discharged. Can respond flexibly,
It is another object of the present invention to provide a carbonization apparatus for solid organic matter that can easily take measures against pollution, such as prevention of generation of dioxin.

【0007】[0007]

【課題を解決するための手段】上記目的を達成する本発
明の請求項1記載の固形有機物の炭化装置は、木片や竹
片の固形有機物片を積層状態で収容するようにガス通過
可能な側壁で形成された搬送可能容器と、該容器の外形
にほぼ一致した横断面形状でやや大きい炉内部が耐火材
で形成され、上記容器の出し入れ用の開閉可能な開口部
と、上方部の着火手段と、該着火手段の反対側に設けら
れた下方部の排気通路とを備えた炭化炉と、該炭化炉の
炉内部に上記開口部を経て敷設されたレール上で移動可
能で且つ上記容器の搭載可能な低い台車とから構成され
ており、上記台車上に搭載された上記搬送可能容器に木
片や竹片の固形有機物片を積層状態で入れ、上記炭化炉
の炉内部に余分な空間が生じない状態で上記台車ごと入
れて開口部を密閉し、上記上方部の着火手段によって上
記容器内の固形有機物片の上部に着火させ、その上部か
ら下部にかけて酸欠状態で蒸し焼きしながら下部まで炭
化を進行させて炭化物を得ることを特徴としている。
According to a first aspect of the present invention, there is provided a carbonization apparatus for solid organic matter, wherein the solid organic matter pieces such as wood pieces and bamboo pieces are gas-passed so as to be accommodated in a stacked state. The inside of the furnace, which is formed of a refractory material, has a cross-sectional shape substantially conforming to the outer shape of the container, is formed of a refractory material, and is openable and closable for opening and closing the container; And a carbonization furnace provided with a lower exhaust passage provided on the opposite side of the ignition means, and a movable member on a rail laid through the opening inside the furnace of the carbonization furnace, and It is composed of a low carriage that can be mounted, and solid organic matter pieces such as wood pieces and bamboo pieces are put in a stacked state in the transportable container mounted on the carriage, and extra space is generated inside the furnace of the carbonization furnace. Insert the whole trolley above and close the opening It is characterized by obtaining a is ignited at the top of the solid organic matter pieces, and allowed to proceed carbide to the bottom while braising with oxygen deficiency toward lower from the top carbides in the container by igniting means of the upper portion.

【0008】従って、上記の構成を有した請求項1記載
の固形有機物の炭化装置では、木片や竹片の固形有機物
片を積層状態で入れた搬送可能容器は、台車に搭載され
て炭化炉内にその開閉可能な開口部から導入され、開口
部は密閉される。その後、上方部の着火手段によって容
器内部の固形有機物片は上部から着火されて、着火手段
の反対側に設けられた下方部の排気通路から排気されな
がら下方部へ燃えて行くが、炉内部に余分な空間が生じ
ない状態で搬送可能容器は台車ごと入れられている為に
酸欠状態で蒸し焼きにされて炭に転換される。従って、
炭化には空気使用量が少なく、温度も低く、窒素酸化物
の発生量も少ない。
Therefore, in the carbonizing apparatus for solid organic matter according to claim 1 having the above structure, the transportable container in which the solid organic matter pieces such as wood pieces and bamboo pieces are put in a stacked state is mounted on a trolley and placed in the carbonizing furnace. Is introduced from the opening which can be opened and closed, and the opening is sealed. Thereafter, the solid organic matter pieces inside the container are ignited from above by the ignition means in the upper part and burn down to the lower part while being exhausted from the lower exhaust passage provided on the opposite side of the ignition means, but into the furnace. Since the transportable container is put in the carriage without any extra space, it is converted into charcoal by being steamed in an oxygen-deficient state. Therefore,
For carbonization, the amount of air used is small, the temperature is low, and the amount of generated nitrogen oxides is small.

【0009】炭は、炭素の塊として固定されており、燃
料として、また土壌改良や、河川水浄化や、脱臭等多方
面に広い用途の有る活性炭として利用される。木片や竹
片の固形有機物片は、塩素分を含んでおらず、ダイオキ
シンの発生を心配せずに炭化できる。この炭化装置は、
廃棄物の排出量が多くなれば、長手方向に長く構成した
り、複数並設して炭化処理能力を柔軟に対応させること
ができる。得られた炭は、活性炭にして脱臭や河川水の
浄化や廃ガス処理に利用され、またボイラーやキルンの
燃料として、コンポストに混入したり単独で土壌改良
に、またゴルフ場や農地、道路の融雪材等として利用さ
れる。
[0009] Charcoal is fixed as a lump of carbon, and is used as a fuel and as activated carbon having a wide variety of uses such as soil improvement, river water purification and deodorization. Solid organic matter pieces such as wood pieces and bamboo pieces do not contain chlorine, and can be carbonized without worrying about the generation of dioxins. This carbonization device
If the amount of discharged waste increases, it can be configured to be long in the longitudinal direction or can be arranged in parallel to flexibly cope with the carbonization capacity. The charcoal obtained is converted into activated carbon and used for deodorization, purification of river water and waste gas treatment, and as fuel for boilers and kilns, it is mixed with compost or used alone for soil improvement, and is also used for golf courses, farmland and roads. Used as snow melting material.

【0010】請求項2に記載のように、上記排気通路は
切換弁を介して消煙バーナ部と煙突に接続されており、
該煙突は排気から木酢液やタールを凝縮する凝縮器を備
えることができ、点火時に多量に発生する煙を消煙バー
ナ部に切換弁によって導き、消煙燃焼させ、煙の発生が
少なくなると切換弁によって煙突に導き、野菜の害虫駆
除や消毒に利用可能な防虫、殺菌剤やハム、ソーセージ
の防腐剤や消臭剤として利用可能な木酢液と、燃料とし
て利用可能なタールとが凝縮器から得られる。
According to a second aspect of the present invention, the exhaust passage is connected to a smoke elimination burner and a chimney via a switching valve.
The chimney can be equipped with a condenser that condenses wood vinegar and tar from the exhaust gas. A large amount of smoke generated at the time of ignition is guided to a smoke-suppressing burner by a switching valve, and the smoke is combusted. A valve leads to the chimney, and wood vinegar liquid, which can be used as a disinfectant, fungicide, ham and sausage preservative and deodorant, and tar that can be used as fuel for insect pest control and disinfection of vegetables from the condenser. can get.

【0011】更に、上記目的を達成する本発明の請求項
3記載の固形有機物の炭化装置は、廃棄木材片や廃棄タ
イヤ等の固形有機質系廃棄物片や、各種のプラスチック
屑や紙屑を含む有機質系廃棄物やシュレッダーダストや
糞尿汚泥等の粘ちょう性有機質系廃棄物を混練、圧密化
して得られた固形再生燃料とかシュレッダーダスト成形
固化物等の有機質系廃棄物片を積層状態で収容するよう
にガス通過可能な側壁で形成された搬送可能容器と、該
容器の外形にほぼ一致した横断面形状でやや大きい炉内
部が耐火材で形成され、上記容器の出し入れ用の開閉可
能な開口部と、上方部の着火手段と、該着火手段の反対
側に設けられた下方部の排気通路とを備えた炭化炉と、
上記排気通路に接続されて上記炭化炉から導入した可燃
ガスを燃焼させるバーナを入口部に備え、炉内にガス流
迂回壁を備えると共に、排気を出口部から大気中に排出
する燃焼炉と、上記炭化炉の炉内部に上記開口部を経て
敷設されたレール上で移動可能で且つ上記容器の搭載可
能な低い台車とから構成されており、上記台車上に搭載
された上記搬送可能容器に木片や竹片の固形有機物片を
積層状態で入れ、上記炭化炉の炉内部に余分な空間が生
じない状態で上記台車ごと入れて開口部を密閉し、上記
上方部の着火手段によって上記容器内の固形有機物片の
上部に着火させ、その上部から下部にかけて酸欠状態で
蒸し焼きしながら下部まで炭化を進行させて炭化物を得
ると共に、その間にガス化した可燃ガスを上記燃焼炉内
に導入して800℃以上で完全燃焼させて排気ガス1m
3 中のダイオキシン含有量を0.1ナノグラム未満とす
ることを特徴としている。
Further, the solid carbonizing apparatus according to the third aspect of the present invention, which achieves the above object, comprises a solid organic waste piece such as a waste wood piece and a waste tire, and an organic material containing various types of plastic waste and paper waste. Mix and consolidate viscous organic wastes such as system waste, shredder dust, and manure sludge, and store organic waste pieces such as solid regenerated fuel obtained by compacting and solidified shredder dust molded products in a stacked state. A transportable container formed by a gas-permeable side wall, and a somewhat large furnace interior having a cross-sectional shape substantially matching the outer shape of the container, formed of a refractory material, and an openable and closable opening for taking in and out of the container. A carbonization furnace having an upper ignition section and a lower exhaust passage provided on the opposite side of the ignition section,
A burner connected to the exhaust passage and configured to burn a combustible gas introduced from the carbonization furnace at an inlet portion, a gas flow bypass wall is provided in the furnace, and a combustion furnace that discharges exhaust gas from an outlet portion to the atmosphere. A low truck movable on a rail laid through the opening inside the furnace of the carbonization furnace and capable of mounting the container, wherein the transportable container mounted on the truck has a piece of wood. And the solid organic matter pieces of bamboo pieces are put in a stacked state, and the bogie is put in a state where no extra space is generated inside the furnace of the carbonization furnace and the opening is sealed, and the opening portion is sealed by the ignition means of the upper part. The upper portion of the solid organic matter is ignited, carbonization proceeds from the upper portion to the lower portion while being roasted in an oxygen-deficient state, and carbonized to the lower portion to obtain carbides. Exhaust gas 1m by complete combustion at higher
3 , characterized in that the dioxin content is less than 0.1 nanogram.

【0012】従って、上記の構成を有した請求項3記載
の固形有機物の炭化装置では、固形有機物片から炭を得
る過程及び作用は、上記請求項1記載の炭化装置と同等
であり、特にダイオキシンの発生の心配の無い木片や竹
片の固形有機物片を炭の原料とする場合は、燃焼炉を使
用せずに炭化炉のみを使用して上記請求項1記載の炭化
装置と同等に使用できる。
Accordingly, in the solid organic matter carbonizing apparatus according to the third aspect having the above-described structure, the process and action of obtaining charcoal from the solid organic matter pieces are the same as those of the carbonizing apparatus according to the first aspect, and in particular, dioxin. When a solid organic material piece such as a wood piece or a bamboo piece is used as a raw material for charcoal, which can be used as a carbonization apparatus without using a combustion furnace, only a carbonization furnace can be used. .

【0013】ダイオキシンの発生の原因になるプラスチ
ックを含む固形再生燃料やシュレッダーダスト成形固化
物を炭の原料とする場合は、炭化炉で蒸し焼き中に発生
する可燃ガスを炭化炉の排気通路から燃焼炉内に導入
し、炉内のガス流迂回壁で迂回させている間に入口部の
バーナによって、また自己燃焼によって800℃以上で
完全燃焼させ、排気ガス1m3 中のダイオキシン含有量
を0.1ナノグラム未満とすることができる。その場
合、炭化時に発生するガス量は、燃焼と違って大量の空
気を必要としない為に、たとえ炭化中にダイオキシンが
発生しても処理ガス量が少なく、コンパクトな燃焼炉で
も上記完全燃焼でダイオキシンの発生を効果的に抑制す
ることができ、また酸化窒素の発生も大幅に削減でき
る。
When a solid regenerated fuel containing plastics or a solidified shredder dust that causes the generation of dioxin is used as a raw material for charcoal, combustible gas generated during steaming in a carbonization furnace is passed through the exhaust passage of the carbonization furnace to the combustion furnace. Into the furnace and burned completely at 800 ° C. or higher by a burner at the inlet while being diverted by a gas flow diverting wall in the furnace, and reduced the dioxin content in 1 m 3 of exhaust gas to 0.1% by self-combustion. It can be less than nanograms. In that case, the amount of gas generated during carbonization does not require a large amount of air unlike combustion, so even if dioxin is generated during carbonization, the amount of gas to be processed is small, and even in a compact combustion furnace, the above-mentioned complete combustion can be used. The generation of dioxin can be effectively suppressed, and the generation of nitric oxide can be significantly reduced.

【0014】請求項4に記載のように、燃焼炉の排気出
口部は、炭化炉の着火手段に開閉手段を介して接続され
ており、燃焼炉での完全燃焼によって酸素量の少なくな
った高温排気ガスを炭化炉に供給して蒸し焼きを促進さ
せることができる。
According to a fourth aspect of the present invention, the exhaust outlet of the combustion furnace is connected to the ignition means of the carbonization furnace via an opening / closing means, and the high-temperature high-temperature gas whose oxygen content has been reduced by the complete combustion in the combustion furnace. Exhaust gas can be supplied to the carbonization furnace to promote roasting.

【0015】請求項5に記載のように、炭化炉の排気出
口部と燃焼炉の入口部との間には、炭化炉の可燃ガスを
誘引して燃焼炉に供給する誘引ブロワーが設けられ、誘
引ブロワーの回転速度を制御することで炭化炉内での固
形有機物の炭化速度を制御することができる。
According to a fifth aspect of the present invention, an induction blower is provided between the exhaust outlet of the carbonization furnace and the entrance of the combustion furnace to attract the combustible gas of the carbonization furnace and supply the combustible gas to the combustion furnace. By controlling the rotation speed of the induction blower, the carbonization speed of solid organic matter in the carbonization furnace can be controlled.

【0016】請求項6に記載のように、炭化炉は、内部
にレールが敷設された消火炉と開閉可能な開口部同士を
向かい合わせて配置され、それら炭化炉と消火炉との間
にはそれらと直交する方向に移動可能で上記両炉に渡っ
て橋渡しする折り畳みレールを備えた容器配給台車が設
けられ、廃棄物の排出量に対応して複数炭化炉を消火炉
と向かい合わせて並設することができ、炭化炉と消火炉
の間で直交する方向に移動可能な容器配給台車によって
アイドリングの無いように固形有機物片の分配ができ
る。
According to a sixth aspect of the present invention, the carbonizing furnace is disposed with the openable and closable opening facing the fire extinguishing furnace in which the rail is laid therein, and between the carbonizing furnace and the fire extinguishing furnace. A container delivery trolley equipped with folding rails that can move in the direction perpendicular to them and that bridges both furnaces is provided, and multiple carbonization furnaces are arranged in parallel with the fire extinguisher in accordance with the amount of waste discharged The solid organic matter can be distributed without idling by a container delivery truck movable in a direction perpendicular to the direction between the carbonization furnace and the fire extinguishing furnace.

【0017】請求項7に記載のように、炭化炉は、側壁
に開閉可能な精錬燃焼空気供給孔を備え、炭化終了時に
空気供給孔を開放して精錬も炭化炉内で行うことがで
き、炭の品質を高めることができる。また、別の精錬炉
の設置を省くことができる。
According to a seventh aspect of the present invention, the carbonization furnace is provided with a refining combustion air supply hole which can be opened and closed on a side wall, and at the end of carbonization, the air supply hole can be opened to perform refining in the carbonization furnace. The quality of charcoal can be improved. Also, the installation of another smelting furnace can be omitted.

【0018】請求項8に記載のように、台車は被炭化物
を積み込むコンテナーを備えることができ、コンテナー
の積み降ろしを省いた台車ごとの輸送管理を行うことが
できる。
[0018] As described in claim 8, the truck can be provided with a container for loading the material to be carbonized, and transport management for each truck can be performed without loading and unloading the container.

【0019】[0019]

【発明の実施の形態と実施例】図1は本発明に係る第一
実施例の固形有機物の炭化装置の縦断面図、図2は同装
置に搭載されている木酢液とタールの回収用凝縮器の縦
断面図、図3は大量廃棄物処理の為に複数配列された炭
化装置を示す平面図、図4は本発明に係る第二実施例の
固形有機物の炭化装置の側面図、図5は同炭化装置の正
面図、図6は有機廃棄物から固形燃料を造る固形化装置
の断面図、図11は同固形化装置の水平断面図である。
DESCRIPTION OF THE PREFERRED EMBODIMENTS FIG. 1 is a longitudinal sectional view of a solid organic matter carbonizing apparatus according to a first embodiment of the present invention, and FIG. 2 is a wooden vinegar solution and a condensate for collecting tars mounted on the apparatus. FIG. 3 is a plan view showing a plurality of carbonizers arranged for treating a large amount of waste, FIG. 4 is a side view of a solid organic matter carbonizer of a second embodiment according to the present invention, and FIG. Is a front view of the carbonization apparatus, FIG. 6 is a cross-sectional view of a solidification apparatus for producing solid fuel from organic waste, and FIG. 11 is a horizontal cross-sectional view of the solidification apparatus.

【0020】図1から図3において、本発明に係る第一
実施例の固形有機物の炭化装置1Aは、廃棄木材片や廃
棄タイヤ等の固形有機質系廃棄物片や、各種のプラスチ
ック屑や紙屑を含む有機質系廃棄物やシュレッダーダス
トや糞尿汚泥等の粘ちょう性有機質系廃棄物を混練、圧
密化して得られた固形再生燃料とかシュレッダーダスト
成形固化物等の有機質系廃棄物片を積層状態で満載する
ようにガス通過可能な周囲壁11で形成された搬送可能
容器10と、容器10の外形にほぼ一致した横断面形状
でやや大きい炉内部が耐火材で形成された炭化炉20A
と、この炭化炉内部に開口部21を経て敷設されたレー
ルR1上で移動可能で且つ容器10を、例えば3個搭載
可能な低い台車15と、炭化炉20Aから炭化中に発生
するガスを選択的に供給を受けて燃焼する燃焼炉40と
から構成されている。
Referring to FIGS. 1 to 3, a solid organic matter carbonizing apparatus 1A according to a first embodiment of the present invention removes solid organic waste pieces such as waste wood pieces and waste tires, various types of plastic waste and paper waste. Organic waste including organic waste and viscous organic waste such as shredder dust and manure sludge are kneaded and compacted, and solid waste fuel such as solid regenerated fuel and solidified shredder dust are loaded in layers. A transferable container 10 formed by a peripheral wall 11 through which gas can pass, and a carbonization furnace 20A having a cross-sectional shape substantially conforming to the outer shape of the container 10 and a somewhat large inside of the furnace formed of a refractory material
And a low trolley 15 movable on a rail R1 laid through an opening 21 inside the carbonization furnace and capable of mounting three containers 10, for example, and a gas generated during carbonization from the carbonization furnace 20A. And a combustion furnace 40 that receives the supply and burns.

【0021】搬送可能容器10は、ガスを通すように周
囲壁11をパンチングメタルや金網で形成した略直方体
形状を成しており、低い台車15の耐火材製の台16上
に互いに若干隙間をおいて載置される。底は、平板でも
よいが、火の回りを良くする為に火格子にしてもよい。
容器10は、後述の固形化装置からの固形有機物の投入
や、製造された炭の空け渡しにバッチ管理できるように
クレーンやフォークリフトで搬送可能となっている。台
車15は、車輪の軸受部を熱から保護する為に、炭化炉
20Aの内部床にレールR1に並行して設けられた溝
(図示は省略)の砂に下端が入ったスカートを台16か
ら垂れ下げることができる。
The transportable container 10 has a substantially rectangular parallelepiped shape in which the peripheral wall 11 is formed of a perforated metal or a wire mesh so as to allow gas to pass therethrough. Is placed. The bottom may be a flat plate, but may be a grate to improve the circumference of the fire.
The container 10 can be transported by a crane or a forklift so that batch management can be performed for charging solid organic matter from a solidifying device to be described later and emptying of manufactured coal. In order to protect the bearings of the wheels from heat, the carriage 15 is formed by attaching a skirt having a lower end into the sand of a groove (not shown) provided in parallel with the rail R1 on the inner floor of the carbonization furnace 20A from the platform 16. Can hang down.

【0022】炭化炉20Aは、容器10の出し入れ用の
開口部21に耐火材を内張した扉22Aを上下に開閉可
能に搭載している。扉22Aは、炭化作業中はジャッキ
等で炭化炉本体23Aに密閉される構造であり、灯油バ
ーナ26を備えた上部着火部25を有している。バーナ
26からの着火用火炎と高温ガスは、着火部25の火口
から天井に沿って炉内の容器10の固形有機物片の上部
に着火の為に供給される。天井に数条の火炎案内溝Gが
形成されている。
In the carbonizing furnace 20A, a door 22A lined with a refractory material is mounted in an opening 21 for taking in and out of the container 10 so as to be openable and closable up and down. The door 22A has a structure that is closed by a jack or the like to the carbonization furnace main body 23A during the carbonization operation, and has an upper ignition portion 25 provided with a kerosene burner 26. The ignition flame and the high-temperature gas from the burner 26 are supplied from the crater of the ignition part 25 along the ceiling to the upper part of the solid organic matter pieces of the container 10 in the furnace for ignition. Several flame guide grooves G are formed in the ceiling.

【0023】着火部25の反対側の奥の端壁W1の下部
には、炭化中に発生するガスを排出する排気通路24が
形成されている。また両側壁W2、W3には、炭化具合
を点検したり最終的に精錬燃焼させる際に空ける上、
中、下の小さい窓29が形成されており、開閉蓋で被わ
れている。
An exhaust passage 24 for discharging gas generated during carbonization is formed below the end wall W1 on the opposite side of the ignition portion 25. In addition, on both side walls W2 and W3, when checking the degree of carbonization and finally smelting and burning,
Small windows 29 are formed at the middle and bottom, and are covered with an opening / closing lid.

【0024】排気通路24には煙突30が接続されてお
り、煙突30の基部には差込み板式開閉弁V1(消煙切
換弁を兼用)が、また中間部には図2に示すような木酢
液とタールの回収用凝縮器32がそれぞれ設けられてい
る。この凝縮器32は、建築廃棄木材、間伐材、竹から
固形有機物片が作られている場合に、燃焼炉40(消煙
用燃焼炉を兼用)を休止させた状態で、炭化炉20Aか
らの排気ガスから野菜の害虫駆除や消毒に利用可能な防
虫、殺菌剤やハム、ソーセージの防腐剤や消臭剤として
利用できる木酢液と、燃料として利用可能なタールとを
凝縮回収するもので、傘付き通路34を複数上方に突設
した回収溜め部33と、複数のガス通路管36を囲んだ
冷却水ジャケット35とから構成されている。
A chimney 30 is connected to the exhaust passage 24. A plug-in type on-off valve V1 (also used as a smoke elimination switching valve) is provided at the base of the chimney 30, and a wood vinegar liquid as shown in FIG. And a condenser 32 for collecting tar. When a solid organic matter piece is made from building waste wood, thinned wood, and bamboo, the condenser 32 is supplied from the carbonization furnace 20A while the combustion furnace 40 (also used as a smoke-elimination combustion furnace) is stopped. It condenses and collects from the exhaust gas the insecticide that can be used for insect pest control and disinfection of vegetables, the wood vinegar liquid that can be used as a preservative and deodorant for ham and sausage, and the tar that can be used as fuel. A collection reservoir 33 is provided with a plurality of passages 34 projecting upward, and a cooling water jacket 35 surrounding a plurality of gas passage pipes 36.

【0025】溜め部33には溜った木酢液やタールを抜
く蛇口が、また冷却水ジャケット35には冷却水の出入
り口がそれぞれ設けられている。燃焼炉40を消煙用に
兼用せずに煙突30に消煙切換弁を設けて、初期の煙を
消煙専用バーナ部へ導くようにしてもよい。
The reservoir 33 is provided with a faucet for removing the collected wood vinegar and tar, and the cooling water jacket 35 is provided with an inlet / outlet for cooling water. Instead of using the combustion furnace 40 for smoke suppression, a smoke suppression switching valve may be provided in the chimney 30 to guide the initial smoke to the smoke burner section.

【0026】また炭化炉20の排気通路24は、燃焼炉
40の入口部41に誘引ブロワー45及びその配管46
を介して接続されている。誘引ブロワー45は、可変速
インバータモータで回転駆動され、回転速度を制御して
炭化炉20Aからの可燃ガスの誘引量を制御することで
炭化速度を制御するようになっている。配管46には開
閉弁V2が設けられている。
The exhaust passage 24 of the carbonization furnace 20 is connected to the inlet 41 of the combustion furnace 40 by an induction blower 45 and its piping 46.
Connected through. The induction blower 45 is rotatably driven by a variable speed inverter motor, and controls the rotation speed to control the amount of combustible gas from the carbonization furnace 20A to control the carbonization speed. The pipe 46 is provided with an on-off valve V2.

【0027】燃焼炉40の炉内部も耐火材で形成されて
おり、その入口部41にはガスに点火する灯油バーナ4
7(消煙バーナを兼用)が搭載されている。また、炉内
部の天井中間部からはガス流迂回壁42が垂下されてお
り、誘引した可燃ガスを3〜4秒に渡って迂回させてい
る間に800℃以上で完全燃焼させて排気ガス1m3
のダイオキシン含有量を0.1ナノグラム未満とするよ
うにしている。ガス流迂回壁42の垂下長さは、耐火材
の追加や除去で調節可能になっている。ガス流迂回壁4
2の後ろには排気出口部43を成す煙突が設けられてい
る。
The interior of the combustion furnace 40 is also made of refractory material, and its inlet 41 has a kerosene burner 4 for igniting gas.
7 (also used as a smoke suppression burner). In addition, a gas flow bypass wall 42 is hung down from the middle part of the ceiling inside the furnace, and while the attracted combustible gas is diverted for 3 to 4 seconds, it is completely burned at 800 ° C. or more and exhaust gas 1 m The dioxin content in 3 is less than 0.1 nanogram. The hanging length of the gas flow bypass wall 42 can be adjusted by adding or removing a refractory material. Gas flow bypass wall 4
Behind 2 is provided a chimney forming an exhaust outlet 43.

【0028】また、燃焼炉40の煙突43は、その分岐
部44から配管48と開閉弁V3を介して炭化炉20の
着火部25に接続されており、燃焼炉40での完全燃焼
によって酸素量の少なくなった高温排気ガスを炭化炉2
0Aに供給して蒸し焼きを促進させるようになってい
る。煙突43の分岐部44の上には、高温排気ガスの戻
しを制御する差込み板式開閉弁V4が設けられている。
The chimney 43 of the combustion furnace 40 is connected to the ignition part 25 of the carbonization furnace 20 from a branch part 44 thereof through a pipe 48 and an on-off valve V3. High temperature exhaust gas with reduced carbonization
0A is supplied to promote steaming. Above the branch portion 44 of the chimney 43, a plug-in plate on-off valve V4 for controlling the return of the high-temperature exhaust gas is provided.

【0029】この高温排気ガスの戻し循環を行っている
間に、循環ガス中の残存酸素量を計測して炭化炉側壁W
2の小さい窓29を開閉して適宜酸素量を制御するよう
にしている。一番下の小さい窓29から炭化作業の完了
が確認された後は、小さい窓29を開放したり、炭化炉
20Aから出して精錬燃焼させて揮発分を燃やす。この
燃焼炉40の排気ガスは、煙突43の基部のダイオキシ
ン計測器の計測値に応じて、適宜入口部41に導入して
再循環させることができる。
During the return circulation of the high-temperature exhaust gas, the amount of oxygen remaining in the circulating gas is measured to measure the carbonization furnace side wall W.
The two small windows 29 are opened and closed to appropriately control the amount of oxygen. After the completion of the carbonization operation is confirmed from the bottom small window 29, the small window 29 is opened or taken out of the carbonization furnace 20A to be smelted and burnt to burn volatiles. The exhaust gas from the combustion furnace 40 can be appropriately introduced into the inlet 41 and recirculated according to the measurement value of the dioxin measuring device at the base of the chimney 43.

【0030】炭化炉20Aは、コンパクトな構造のわり
には大量に廃棄物処理ができるが、これは嵩高い一般ゴ
ミを固形化して固形有機物片とするためである。廃棄物
の排出量に対応して上記炭化装置1を図3に示すように
消火炉50と向かい合わせて複数並設することができ
る。消火炉50は、炭化炉20Aの稼働率を高める為
に、出来上がった炭の火を消す為に使用され、扉51は
気密に閉鎖される。
Although the carbonization furnace 20A has a compact structure, it can process a large amount of waste, but this is because solid bulky garbage is solidified into solid organic matter pieces. According to the amount of waste discharged, a plurality of the above-mentioned carbonization devices 1 can be arranged in parallel with the fire extinguishing furnace 50 as shown in FIG. The fire extinguishing furnace 50 is used to extinguish the fire of the finished charcoal in order to increase the operation rate of the carbonization furnace 20A, and the door 51 is closed airtightly.

【0031】それら炭化炉20Aと消火炉50との間に
はそれらの長手軸線に直交する方向のピット61内にレ
ールR2上で移動可能で両炉20A、50に渡って橋渡
しする折り畳みレールR3を両端に備えた容器配給台車
65が設けられ、アイドリングの無いように固形有機物
片の分配や消火炉50への台車移動を制御するようにし
ている。勿論、容器配給台車65もレールR4を備えて
いる。容器(コンテナー)10は、台車15に固定され
るように構成され、台車15と一体として輸送制御を受
けることもできる。
Between the carbonizing furnace 20A and the fire extinguishing furnace 50, a folding rail R3 movable on a rail R2 and bridging over both furnaces 20A, 50 is provided in a pit 61 in a direction perpendicular to their longitudinal axes. Container delivery carts 65 provided at both ends are provided to control the distribution of the solid organic matter pieces and the movement of the carts to the fire extinguishing furnace 50 without idling. Of course, the container delivery cart 65 also includes the rail R4. The container (container) 10 is configured to be fixed to a cart 15, and can be subjected to transport control integrally with the cart 15.

【0032】上記第一実施例の固形有機物の炭化装置1
Aに代えて、図4と図5に示す第二実施例の固形有機物
の炭化装置1Bも使用される。その基本的な構想は、第
一実施例の固形有機物の炭化装置1Aと同じであり、同
じ作用と構造の構成要素は同じ符号が付けられている。
異なった構成について説明すると、炭化炉20Bは、灯
油バーナ26を備えた上部着火部25を一方の側壁W2
に設けており、また排気通路24を他方の側壁W3に形
成している。また燃焼炉40の設置向きが、変えられて
いる。炭化装置1A、1Bは、設置場所に応じて適宜選
択される。
The solid organic matter carbonizing apparatus 1 of the first embodiment.
Instead of A, the solid organic matter carbonizing device 1B of the second embodiment shown in FIGS. 4 and 5 is also used. The basic concept is the same as the solid organic matter carbonizing apparatus 1A of the first embodiment, and the components having the same operation and structure are denoted by the same reference numerals.
Describing a different configuration, the carbonization furnace 20B is configured such that the upper igniter 25 provided with the kerosene burner 26 has one side wall W2.
And an exhaust passage 24 is formed on the other side wall W3. Further, the installation direction of the combustion furnace 40 is changed. The carbonizing devices 1A and 1B are appropriately selected according to the installation location.

【0033】また、ダイオキシンの発生の心配の無い木
材や竹を原料にする場合は、燃焼炉や誘引ブロワーを止
めて運転したり、更には省いた構成とすることができ
る。更に上記灯油バーナ26、47は、ガスバーナに代
えることもできる。また、燃焼炉を省いた木片や竹片専
用の炭化装置の場合、点火時に多量に発生する煙を消煙
するために排気通路に切換弁を介して消煙バーナ部と煙
突を接続することになる。
In the case of using wood or bamboo as a raw material which does not cause generation of dioxin, the operation can be performed with the combustion furnace or the induction blower stopped or the configuration can be omitted. Further, the kerosene burners 26 and 47 can be replaced with gas burners. In addition, in the case of a carbonization device dedicated to wood chips and bamboo chips without a combustion furnace, in order to extinguish a large amount of smoke generated at the time of ignition, it is necessary to connect the smoke suppression burner section and the chimney to the exhaust passage via a switching valve. Become.

【0034】廃棄物を固形有機物片にする作業を概説す
ると、下水汚泥やし尿汚泥、糞尿汚泥は、遠心式脱水装
置で脱水後に破砕済み紙屑や、廃タイヤ等から生成され
た廃活性炭と混合後に生ごみと同様に乾燥装置を経て乾
燥生ごみ用サイロに搬送され、貯蔵される。廃タイヤ
は、そのまま又は破砕後に上記のような炭化装置で乾留
炭化されて、生ごみや下水汚泥や糞尿汚泥に混合され
る。
An outline of the operation of converting waste into solid organic matter pieces is as follows: sewage sludge, night soil sludge, and manure sludge are mixed with crushed paper waste and waste activated carbon generated from waste tires and the like after dehydration with a centrifugal dehydrator. Like the garbage, the garbage is conveyed to a dry garbage silo via a drying device and stored. The waste tire is subjected to dry distillation carbonization as it is or after crushing by the carbonization device as described above, and is mixed with garbage, sewage sludge, and manure sludge.

【0035】各廃プラスチック用サイロ、木屑チップ用
サイロ、乾燥生ごみ用サイロ、廃プラ・紙屑用定量供給
機付きサイロからそれぞれの定量供給機によってプラス
チック分が70〜30重量%、その他が30〜70重量
%となるように供給されて混合物MWが定量供給機付き
サイロ内に一時的に貯蔵される。そこから固形化装置に
消費量に合わせて定量供給機とコンベヤを介して混合物
は供給される。
From each silo for waste plastic, silo for wood chip chips, silo for dry garbage, silo with quantitative feeder for waste plastic and paper waste, the amount of plastic is 70 to 30% by weight, and the others are 30 to 30% by weight. The mixture MW supplied so as to be 70% by weight is temporarily stored in a silo equipped with a metering device. From there, the mixture is supplied to the solidification device via a metering feeder and a conveyor according to the consumption.

【0036】図6と図7に示すように、固形化装置80
では、後述するように螺旋体82A、Bによって混合物
WMに送りをかけて撹拌混合しながら圧縮して150℃
前後に加熱し、プラスチックを溶融して練り合わせて流
動可能状態にし、この流動状態の中間生成物から多孔板
85に通して押し出し成形して棒状や粒状の有機物から
成る固形物WSを形成する。プラスチック分が上記含有
量であれば、形崩れの起きない保形性の良い固形物WS
が得られる。
As shown in FIG. 6 and FIG.
Then, the mixture is fed to the mixture WM by the spiral bodies 82A and B and compressed while stirring and mixing at 150 ° C. as described later.
It is heated back and forth, the plastic is melted and kneaded into a flowable state, and the fluidized intermediate product is extruded through a perforated plate 85 to form a solid WS consisting of a rod-like or granular organic matter. If the plastic content is the above content, a solid material WS with good shape retention without shape collapse
Is obtained.

【0037】固形化装置80は、混合廃棄物WMは、螺
旋体82A、Bで破砕混練され、圧搾部83で圧縮粉砕
されて発熱し、溶融後に多孔板成形部85で固形物の燃
料WSとして押し出し形成される。これは、カロリーが
安定し、臭やカビの発生も無くボイラーの燃料としても
好適である。
In the solidifying device 80, the mixed waste WM is crushed and kneaded by the spirals 82A and 82B, compressed and pulverized by the pressing unit 83 to generate heat, and after being melted, extruded as solid fuel WS by the perforated plate forming unit 85. It is formed. This has a stable calorie, does not generate odor or mold, and is suitable as a fuel for a boiler.

【0038】より具体的に説明すると、固形燃料形成機
80は、一端部の投入口81Aから投入されたプラスチ
ックを含む混合廃棄物WMを他端部の取り出し口81B
に至る長手方向にかけて搬送しながら破砕、混練、圧縮
及び粉砕を行い、摩擦や圧縮の発熱で温度を上げ、プラ
スチックを溶融したりするもので、細長ケーシング81
内の長手方向に並設され対向方向に回転駆動される一対
の回転軸80S、80Sと、それらの各々に取り付けら
れた螺旋体82A、82B及び圧搾体83A、83B
と、これらに対して所定の隙間をとってケーシング81
内に取り外し可能に付設された耐摩耗性内張体81C
と、取り出し口81Bの固形化用ノズル付き多孔板85
とから構成されている。
More specifically, the solid fuel forming machine 80 is configured to remove the mixed waste WM containing the plastic injected from the input port 81A at one end, and to take out the mixed waste WM at the other end.
Crushing, kneading, compressing and pulverizing while transporting in the longitudinal direction up to, the temperature is raised by the heat of friction and compression, and the plastic is melted.
A pair of rotating shafts 80S, 80S arranged side by side in the longitudinal direction and driven to rotate in the opposite direction, and spiral bodies 82A, 82B and compressed bodies 83A, 83B attached to each of them.
The casing 81
Abrasion resistant lining 81C removably attached inside
And a perforated plate 85 with a nozzle for solidification at the outlet 81B
It is composed of

【0039】圧搾体は、特に粉砕と溶解を促進する臼状
圧搾部83を構成している。固形燃料成形機80で、発
熱量が大きくて塩素ガスが発生するおそれがある時、適
宜給水して温度上昇を抑制するように給水ラインを付設
することが出来る。
The squeezed body constitutes a mortar-shaped squeezed portion 83 for promoting crushing and melting. In the solid fuel molding machine 80, when the calorific value is large and there is a risk of generating chlorine gas, a water supply line can be provided so as to supply water appropriately to suppress a rise in temperature.

【0040】[0040]

【発明の効果】以上の説明から明らかなように、本発明
の請求項1記載の固形有機物の炭化装置によれば、木片
や竹片の固形有機物片を積層状態で入れた搬送可能容器
は、台車に搭載されて炭化炉内にその開閉可能な開口部
から導入され、開口部は密閉され、その後、上方部の着
火手段によって容器内部の固形有機物片は上部から着火
されて、着火手段の反対側に設けられた下方部の排気通
路から排気されながら下方部へ燃えて行くようにしてお
り、従って炉内部に余分な空間が生じない状態で搬送可
能容器は台車ごと入れられている為に酸欠状態で蒸し焼
きにされて炭に転換される。炭は、炭素の塊として固定
されており、燃料として、また土壌改良や、河川水浄化
や、脱臭等多方面に広い用途の有る活性炭として利用さ
れる。
As is clear from the above description, according to the solid organic matter carbonizing apparatus of the first aspect of the present invention, the transportable container in which the solid organic matter pieces such as the wood pieces and the bamboo pieces are put in a laminated state is provided. It is mounted on a trolley and introduced into the carbonization furnace through its openable and closable opening, the opening is sealed, and then the solid organic matter pieces inside the container are ignited from above by the igniting means in the upper part, and are opposed to the igniting means. It is designed to burn down while being exhausted from the lower exhaust passage provided on the side, so that the transportable containers are put together with the carts without any extra space inside the furnace, so the acid It is steamed in the missing state and converted to charcoal. Charcoal is fixed as a lump of carbon, and is used as a fuel and as activated carbon having a wide variety of uses such as soil improvement, river water purification, and deodorization.

【0041】木片や竹片の固形有機物片は、塩素分を含
んでおらず、ダイオキシンの発生を心配せずに炭化でき
る。この炭化装置は、廃棄物の排出量が多くなれば、長
手方向に長く構成したり、複数並設して炭化処理能力を
柔軟に対応させることができる。
The solid organic matter pieces such as wood pieces and bamboo pieces do not contain chlorine and can be carbonized without worrying about the generation of dioxins. If the amount of discharged waste increases, the carbonization apparatus can be configured to be long in the longitudinal direction or can be arranged in parallel to flexibly cope with the carbonization processing capacity.

【0042】請求項2記載の固形有機物の炭化装置によ
れば、煙突は排気から木酢液やタールを凝縮する凝縮器
を備えることができ、点火時に多量に発生する煙を消煙
バーナ部に切換弁によって導き、消煙燃焼させ、煙の発
生が少なくなると切換弁によって煙突に導き、野菜の害
虫駆除や消毒に利用可能な防虫、殺菌剤やハム、ソーセ
ージの防腐剤や消臭剤として利用可能な木酢液と、燃料
として利用可能なタールとが凝縮器から得られる。
According to the second aspect of the present invention, the chimney can be provided with a condenser for condensing wood vinegar and tar from the exhaust gas, and a large amount of smoke generated at the time of ignition is switched to a smoke eliminating burner. Guided by a valve, deodorized and burned, and when the generation of smoke is reduced, it is guided to a chimney by a switching valve, and it can be used as an insect repellent that can be used for pest control and disinfection of vegetables, fungicide, ham, sausage preservative and deodorant Natural wood vinegar and tar available as fuel are obtained from the condenser.

【0043】更に、本発明の請求項3記載の固形有機物
の炭化装置によれば、固形有機物片から炭を得る過程及
び作用は、上記請求項1記載の炭化装置と同等であり、
特にダイオキシンの発生の心配の無い木片や竹片の固形
有機物片を炭の原料とする場合は、燃焼炉を使用せずに
炭化炉のみを使用して上記請求項1記載の炭化装置と同
等に使用できる。
Further, according to the carbonizing apparatus for solid organic matter according to the third aspect of the present invention, the process and action of obtaining charcoal from the solid organic matter pieces are the same as those of the carbonizing apparatus according to the first aspect,
In particular, when using a solid organic material piece such as a wood piece or a bamboo piece having no concern about the generation of dioxin as a raw material for charcoal, using only a carbonization furnace without using a combustion furnace, the same as the carbonization apparatus according to claim 1 above. Can be used.

【0044】ダイオキシンの発生の原因になるプラスチ
ックを含む固形再生燃料やシュレッダーダスト成形固化
物を炭の原料とする場合は、炭化炉で蒸し焼き中に発生
する可燃ガスを炭化炉の排気通路から燃焼炉内に導入
し、炉内のガス流迂回壁で迂回させている間に入口部の
バーナによって、また自己燃焼によって800℃以上で
完全燃焼させ、排気ガス1m3 中のダイオキシン含有量
を0.1ナノグラム未満とすることができる。その場
合、炭化時に発生するガス量は、燃焼と違って大量の空
気を必要としない為に、たとえ炭化中にダイオキシンが
発生しても処理ガス量が少なく、コンパクトな燃焼炉で
上記完全燃焼を達成することができる。
In the case of using a solid regenerated fuel containing plastics or a solidified shredder dust which causes the generation of dioxin as a raw material for charcoal, the combustible gas generated during steaming in the carbonization furnace is passed through the exhaust passage of the carbonization furnace to the combustion furnace. Into the furnace and burned completely at 800 ° C. or higher by a burner at the inlet while being diverted by a gas flow diverting wall in the furnace, and reduced the dioxin content in 1 m 3 of exhaust gas to 0.1% by self-combustion. It can be less than nanograms. In that case, the amount of gas generated during carbonization does not require a large amount of air unlike combustion, so even if dioxin is generated during carbonization, the amount of processing gas is small, and the complete combustion described above can be performed with a compact combustion furnace. Can be achieved.

【0045】請求項4記載の固形有機物の炭化装置によ
れば、燃焼炉の排気出口部は、炭化炉の着火手段に開閉
手段を介して接続されており、燃焼炉での完全燃焼によ
って酸素量の少なくなった高温排気ガスを炭化炉に供給
して蒸し焼きを促進させることができる。
According to the fourth aspect of the present invention, the exhaust outlet of the combustion furnace is connected to the ignition means of the carbonization furnace via the opening / closing means, and the amount of oxygen is reduced by complete combustion in the combustion furnace. The high-temperature exhaust gas, which has been reduced, can be supplied to the carbonization furnace to promote steaming.

【0046】請求項5記載の固形有機物の炭化装置によ
れば、炭化炉の排気出口部と燃焼炉の入口部との間に
は、炭化炉の可燃ガスを誘引して燃焼炉に供給する誘引
ブロワーが設けられ、誘引ブロワーの回転速度を制御す
ることで炭化炉内での固形有機物の炭化速度を制御する
ことができる。
According to the apparatus for carbonizing solid organic matter according to the fifth aspect, between the exhaust outlet of the carbonizing furnace and the inlet of the combustion furnace, the flammable gas of the carbonizing furnace is attracted and supplied to the combustion furnace. A blower is provided, and by controlling the rotation speed of the induction blower, the carbonization rate of the solid organic matter in the carbonization furnace can be controlled.

【0047】請求項6記載の固形有機物の炭化装置によ
れば、炭化炉は、内部にレールが敷設された消火炉と開
閉可能な開口部同士を向かい合わせて配置され、それら
炭化炉と消火炉との間にはそれらと直交する方向に移動
可能で上記両炉に渡って橋渡しする折り畳みレールを備
えた容器配給台車が設けられ、廃棄物の排出量に対応し
て複数炭化炉を消火炉と向かい合わせて並設することが
でき、炭化炉と消火炉の間で直交する方向に移動可能な
容器配給台車によってアイドリングの無いように固形有
機物片の分配ができる。
According to the apparatus for carbonizing solid organic matter according to the present invention, the carbonization furnace is disposed so that the openable and closable opening faces the fire extinguishing furnace in which the rail is laid, and the carbonizing furnace and the fire extinguishing furnace In between, there is provided a container delivery cart having folding rails movable in a direction orthogonal to them and bridging over the two furnaces, and a plurality of carbonizing furnaces and a fire extinguishing furnace corresponding to the amount of waste discharged are provided. The solid organic matter pieces can be distributed without idling by a container delivery cart that can be juxtaposed and movable in an orthogonal direction between the carbonizing furnace and the fire extinguishing furnace.

【0048】請求項7記載の固形有機物の炭化装置によ
れば、炭化炉は、側壁に開閉可能な精錬燃焼空気供給孔
を備え、炭化終了時に空気供給孔を開放して精錬も炭化
炉内で行うことができ、炭の品質を高めることができ
る。また、別の精錬炉の設置を省くことができる。
According to the solid organic matter carbonizing apparatus of the present invention, the carbonizing furnace is provided with a refining combustion air supply hole which can be opened and closed on the side wall. Can be done and the quality of charcoal can be increased. Also, the installation of another smelting furnace can be omitted.

【0049】請求項8記載の固形有機物の炭化装置によ
れば、台車は被炭化物を積み込むコンテナーを備えるこ
とができ、コンテナーの積み降ろしを省いた台車ごとの
輸送管理を行うことができる。
According to the carbonization apparatus for solid organic matter according to the eighth aspect, the carriage can be provided with a container for loading the material to be carbonized, and the transportation of each carriage can be controlled without loading and unloading the container.

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

【図1】本発明に係る第一実施例の固形有機物の炭化装
置の縦断面図である。
FIG. 1 is a longitudinal sectional view of a solid organic matter carbonizing apparatus according to a first embodiment of the present invention.

【図2】同装置に搭載されている木酢液とタールの回収
用凝縮器の縦断面図である。
FIG. 2 is a longitudinal sectional view of a condenser for collecting wood vinegar and tar mounted on the apparatus.

【図3】大量廃棄物処理の為に複数配列された炭化装置
を示す平面図である。
FIG. 3 is a plan view showing a plurality of carbonizing apparatuses arranged for mass waste disposal.

【図4】本発明に係る第二実施例の固形有機物の炭化装
置の側面図である。
FIG. 4 is a side view of an apparatus for carbonizing solid organic matter according to a second embodiment of the present invention.

【図5】同炭化装置の正面図である。FIG. 5 is a front view of the carbonization device.

【図6】有機廃棄物から固形燃料を造る固形化装置の断
面図である。
FIG. 6 is a cross-sectional view of a solidification device for producing solid fuel from organic waste.

【図7】同固形化装置の水平断面図である。FIG. 7 is a horizontal sectional view of the solidifying device.

【符号の説明】[Explanation of symbols]

1A、1B 固形有機物の炭化装置 10 搬送可能容器 11 ガス通過可能な側壁 15 台車 20A、20B 炭化炉 21 開口部 24 排気通路 25 着火部 30 煙突 40 燃焼炉 41 入口部 42 ガス流迂回壁 43 凝縮器 45 誘引ブロワー 47 バーナ 50 消火炉 65 容器配給台車 1、R3 レール DESCRIPTION OF SYMBOLS 1A, 1B Solid organic matter carbonization device 10 Transportable container 11 Gas permeable side wall 15 Cart 20A, 20B Carbonization furnace 21 Opening 24 Exhaust passage 25 Ignition part 30 Chimney 40 Combustion furnace 41 Inlet part 42 Gas flow bypass wall 43 Condenser 45 Induction blower 47 Burner 50 Fire extinguishing furnace 65 Container distribution trolley 1, R3 rail

─────────────────────────────────────────────────────
────────────────────────────────────────────────── ───

【手続補正書】[Procedure amendment]

【提出日】平成11年3月23日[Submission date] March 23, 1999

【手続補正1】[Procedure amendment 1]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】特許請求の範囲[Correction target item name] Claims

【補正方法】変更[Correction method] Change

【補正内容】[Correction contents]

【特許請求の範囲】[Claims]

【手続補正2】[Procedure amendment 2]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】0006[Correction target item name] 0006

【補正方法】変更[Correction method] Change

【補正内容】[Correction contents]

【0006】本発明は、上記に鑑み案出されたものであ
って、土壌改良や、河川水浄化や、脱臭等多方面に広い
用途があり、炭酸ガス発生の抑制に寄与できる炭を固形
有機質系廃棄物から効率的に産出できるもので、蒸し焼
きで使用酸素量が少なく、余分な空間が無く正味被処理
物を収容できる比較的コンパクトな構造を有し、廃棄物
の排出量に対して規模を柔軟に対応させることができる
ものでありながら、点火時に多量に発生する煙を消煙バ
ーナ部に切換弁によって導き、消煙燃焼させ、煙の発生
が少なく成ると切換弁によって煙突に導き、野菜の害虫
駆除や消毒に利用可能な防虫、殺菌剤やハム、ソーセジ
の防腐剤や消臭剤として利用可能な木酢液と、燃料とし
て利用可能なタールとが凝縮器から得られ、更にダイオ
キシンの発生防止等の無公害化について容易に対策ので
きる固形有機物の炭化装置を提供することを目的として
いる。
The present invention has been devised in view of the above, and has a wide variety of uses such as soil improvement, river water purification, and deodorization. It can be efficiently produced from system waste, uses less oxygen by steaming, has a relatively compact structure that can accommodate the net processed material without extra space, and is a scale for the amount of waste discharged. Although it is possible to respond flexibly, the smoke generated in a large amount at the time of ignition is guided to the smoke suppression burner part by the switching valve, the smoke is combusted, and when the generation of smoke is reduced, the smoke is guided to the chimney by the switching valve, Insect repellents that can be used for insect pest control and disinfection of vegetables, wood vinegar liquid that can be used as a preservative and deodorant for fungicides and hams and sausages, and tar that can be used as fuel are obtained from the condenser. Prevention And its object is to provide a carbonization apparatus of solid organic matter that can easily measure the pollution-free of.

【手続補正3】[Procedure amendment 3]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】0007[Correction target item name] 0007

【補正方法】変更[Correction method] Change

【補正内容】[Correction contents]

【0007】[0007]

【課題を解決するための手段】上記目的を達成する本発
明の請求項1記載の固形有機物の炭化装置は、木片や竹
片の固形有機物片を積層状態で収容するようにガス通過
可能な側壁で形成された搬送可能容器と、該容器の外形
にほぼ一致した横断面形状でやや大きい炉内部が耐火材
で形成され、上記容器の出し入れ用の開閉可能な開口部
と、上方部の着火手段と、該着火手段の反対側に設けら
れた下方部の排気通路とを備えた炭化炉と、該炭化炉の
炉内部に上記開口部を経て敷設されたレール上で移動可
能で且つ上記容器の搭載可能な低い台車とから構成され
ており、上記台車上に搭載された上記搬送可能容器に木
片や竹片の固形有機物片を積層状態で入れ、上記炭化炉
の炉内部に余分な空間が生じない状態で上記台車ごと入
れて開口部を密閉し、上記上方部の着火手段によって上
記容器内の固形有機物片の上部に着火させ、その上部か
ら下部にかけて酸欠状態で蒸し焼きしながら下部まで炭
化を進行させて炭化物を得るものにおいて、上記排気通
路は、切換弁を介して消煙バーナ部と煙突に接続されて
おり、該煙突は排気から木酢液やタールを凝縮する凝縮
器を備えていることを特徴としている。
According to a first aspect of the present invention, there is provided a carbonization apparatus for solid organic matter, wherein the solid organic matter pieces such as wood pieces and bamboo pieces are gas-passed so as to be accommodated in a stacked state. The inside of the furnace, which is formed of a refractory material, has a cross-sectional shape substantially conforming to the outer shape of the container, is formed of a refractory material, and is openable and closable for opening and closing the container; And a carbonization furnace provided with a lower exhaust passage provided on the opposite side of the ignition means, and a movable member on a rail laid through the opening inside the furnace of the carbonization furnace, and It is composed of a low carriage that can be mounted, and solid organic matter pieces such as wood pieces and bamboo pieces are put in a stacked state in the transportable container mounted on the carriage, and extra space is generated inside the furnace of the carbonization furnace. Insert the whole trolley above and close the opening By igniting the upper part of the solid organic matter piece in the container by the ignition means of the upper part, to progress the carbonization from the upper part to the lower part while steaming in an oxygen-deficient state to the lower part to obtain a carbide, the exhaust passage is The switch is connected to a smoke-suppressing burner section and a chimney via a switching valve, and the chimney is characterized by having a condenser for condensing wood vinegar and tar from exhaust gas.

【手続補正4】[Procedure amendment 4]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】0008[Correction target item name] 0008

【補正方法】変更[Correction method] Change

【補正内容】[Correction contents]

【0008】従って、上記の構成を有した請求項1記載
の固形有機物の炭化装置では、木片や竹片の固形有機物
片を積層状態で満載した搬送可能容器は、台車に搭載さ
れて炭化炉内にその開閉可能な開口部から導入され、開
口部は密閉される。その後、上方部の着火手段によって
容器内部の固形有機物片は上部から着火されて、着火手
段の反対側に設けられた下方部の排気通路から排気され
ながら下方部へ燃えて行くが、炉内部に余分な空間が生
じない状態で搬送可能容器は台車ごと入れられている為
に酸欠状態で蒸し焼きにされて炭に転換される。従っ
て、炭化には空気使用量が少なく、温度も低く、窒素酸
化物の発生量も少ない。また、点火時に多量に発生する
煙を消煙バーナ部に切換弁によって導き、消煙燃焼さ
せ、煙の発生が少なく成ると切換弁によって煙突に導
き、野菜の害虫駆除や消毒に利用可能な防虫、殺菌剤や
ハム、ソーセジの防腐剤や消臭剤として利用可能な木酢
液と、燃料として利用可能なタールとが凝縮器から得ら
れる。
Therefore, in the carbonizing apparatus for solid organic matter according to the first aspect of the present invention, the transportable container loaded with the solid organic matter pieces such as wood pieces and bamboo pieces in a stacked state is mounted on a trolley and placed in the carbonization furnace. Is introduced from the opening which can be opened and closed, and the opening is sealed. Thereafter, the solid organic matter pieces inside the container are ignited from above by the ignition means in the upper part and burn down to the lower part while being exhausted from the lower exhaust passage provided on the opposite side of the ignition means, but into the furnace. Since the transportable container is put in the carriage without any extra space, it is converted into charcoal by being steamed in an oxygen-deficient state. Therefore, carbonization requires a small amount of air, a low temperature, and a small amount of nitrogen oxides. In addition, a large amount of smoke generated at the time of ignition is guided to a smoke-suppressing burner by a switching valve, and the smoke is combusted. When the generation of smoke is reduced, the switching valve is used to guide the smoke to a chimney, which can be used for extermination and disinfection of vegetables. A wood vinegar solution that can be used as a disinfectant, a preservative or deodorant for ham and sausage, and tar that can be used as fuel are obtained from the condenser.

【手続補正5】[Procedure amendment 5]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】0010[Correction target item name] 0010

【補正方法】削除[Correction method] Deleted

【手続補正6】[Procedure amendment 6]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】0011[Correction target item name] 0011

【補正方法】変更[Correction method] Change

【補正内容】[Correction contents]

【0011】更に、上記目的を達成する本発明の請求項
2記載の固形有機物の炭化装置は、廃棄木材片や廃棄タ
イヤ等の固形有機質系廃棄物片や、各種のプラスチック
屑や紙屑を含む有機質系廃棄物やシュレッダーダストや
糞尿汚泥等の粘ちょう性有機質系廃棄物を混練、圧密化
して得られた固形再生燃料とかシュレッダーダスト成形
固化物等の有機質系廃棄物片を積層状態で収容するよう
にガス通過可能な側壁で形成された搬送可能容器と、該
容器の外形にほぼ一致した横断面形状でやや大きい炉内
部が耐火材で形成され、上記容器の出し入れ用の開閉可
能な開口部と、上方部の着火手段と、該着火手段の反対
側に設けられた下方部の排気通路とを備えた炭化炉と、
上記排気通路に接続されて上記炭化炉から導入した可燃
ガスを燃焼させるバーナを入口部に備え、炉内にガス流
迂回壁を備えると共に、排気を出口部から大気中に排出
する燃焼炉と、上記炭化炉の炉内部に上記開口部を経て
敷設されたレール上で移動可能で且つ上記容器の搭載可
能な低い台車とから構成されており、上記台車上に搭載
された上記搬送可能容器に木片や竹片の固形有機物片を
積層状態で入れ、上記炭化炉の炉内部に余分な空間が生
じない状態で上記台車ごと入れて開口部を密閉し、上記
上方部の着火手段によって上記容器内の固形有機物片の
上部に着火させ、その上部から下部にかけて酸欠状態で
蒸し焼きしながら下部まで炭化を進行させて炭化物を得
ると共に、その間にガス化した可燃ガスを上記燃焼炉内
に導入して800℃以上で完全燃焼させて排気ガス1m
3中のダイオキシン含有量を0.1ナノグラム未満とす
ることを特徴としている。
Further, the solid organic matter carbonizing apparatus according to the second aspect of the present invention, which achieves the above object, comprises a solid organic waste piece such as a waste wood piece and a waste tire, and an organic material containing various types of plastic waste and paper waste. Mix and consolidate viscous organic wastes such as system wastes, shredder dust, and manure sludge, and store organic waste pieces such as solid regenerated fuel or shredder dust molded solids obtained in a stacked state. A transportable container formed by a gas-permeable side wall, and a somewhat large furnace interior having a cross-sectional shape substantially matching the outer shape of the container, formed of a refractory material, and an openable and closable opening for taking in and out of the container. A carbonization furnace having an upper ignition section and a lower exhaust passage provided on the opposite side of the ignition section,
A burner connected to the exhaust passage and configured to burn a combustible gas introduced from the carbonization furnace at an inlet portion, a gas flow bypass wall is provided in the furnace, and a combustion furnace that discharges exhaust gas from an outlet portion to the atmosphere. A low truck movable on a rail laid through the opening inside the furnace of the carbonization furnace and capable of mounting the container, wherein the transportable container mounted on the truck has a piece of wood. And the solid organic matter pieces of bamboo pieces are put in a stacked state, and the bogie is put in a state where no extra space is generated inside the furnace of the carbonization furnace and the opening is sealed, and the opening portion is sealed by the ignition means of the upper part. The upper portion of the solid organic matter is ignited, carbonization proceeds from the upper portion to the lower portion while being roasted in an oxygen-deficient state, and carbonized to the lower portion to obtain carbides. Exhaust gas 1m by complete combustion at higher
3 , characterized in that the dioxin content is less than 0.1 nanogram.

【手続補正7】[Procedure amendment 7]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】0012[Correction target item name] 0012

【補正方法】変更[Correction method] Change

【補正内容】[Correction contents]

【0012】従って、上記の構成を有した請求項2記載
の固形有機物の炭化装置では、固形有機物片から炭を得
る過程及び作用は、上記請求項1記載の炭化装置と同等
であり、特にダイオキシンの発生の心配の無い木片や竹
片の固形有機物片を炭の原料とする場合は、燃焼炉を使
用せずに炭化炉のみを使用して上記請求項1記載の炭化
装置と同等に使用できる。
Therefore, in the carbonizing apparatus for solid organic matter according to the second aspect having the above structure, the process and action of obtaining charcoal from the solid organic matter pieces are the same as those of the carbonizing apparatus according to the first aspect, and in particular, dioxin. When a solid organic material piece such as a wood piece or a bamboo piece is used as a raw material for charcoal, which can be used as a carbonization apparatus without using a combustion furnace, only a carbonization furnace can be used. .

【手続補正8】[Procedure amendment 8]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】0014[Correction target item name] 0014

【補正方法】変更[Correction method] Change

【補正内容】[Correction contents]

【0014】請求項3に記載のように、燃焼炉の排気出
口部は、炭化炉の着火手段に開閉手段を介して接続され
ており、燃焼炉での完全燃焼によって酸素量の少なくな
った高温排気ガスを炭化炉に供給して蒸し焼きを促進さ
せることができる。
According to a third aspect of the present invention, the exhaust outlet of the combustion furnace is connected to the ignition means of the carbonization furnace through an opening / closing means, and the high temperature of which the amount of oxygen is reduced by the complete combustion in the combustion furnace is reduced. Exhaust gas can be supplied to the carbonization furnace to promote roasting.

【手続補正9】[Procedure amendment 9]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】0015[Correction target item name] 0015

【補正方法】変更[Correction method] Change

【補正内容】[Correction contents]

【0015】請求項4に記載のように、炭化炉の排気出
口部と燃焼炉の入口部との間には、炭化炉の可燃ガスを
誘引して燃焼炉に供給する誘引ブロワーが設けられ、誘
引ブロワーの回転速度を制御することで炭化炉内での固
形有機物の炭化速度を制御することができる。
According to a fourth aspect of the present invention, an induction blower is provided between the exhaust outlet of the carbonization furnace and the entrance of the combustion furnace, for inducing the combustible gas of the carbonization furnace and supplying the combustible gas to the combustion furnace. By controlling the rotation speed of the induction blower, the carbonization speed of solid organic matter in the carbonization furnace can be controlled.

【手続補正10】[Procedure amendment 10]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】0016[Correction target item name] 0016

【補正方法】変更[Correction method] Change

【補正内容】[Correction contents]

【0016】請求項5に記載のように、炭化炉は、内部
にレールが敷設された消火炉と開閉可能な開口部同士を
向かい合わせて配置され、それら炭化炉と消火炉との間
にはそれらと直交する方向に移動可能で上記両炉に渡っ
て橋渡しする折り畳みレールを備えた容器配給台車が設
けられ、廃棄物の排出量に対応して複数炭化炉を消火炉
と向かい合わせて並設することができ、炭化炉と消火炉
の間で直交する方向に移動可能な容器配給台車によって
アイドリングの無いように固形有機物片の分配ができ
る。
According to a fifth aspect of the present invention, the carbonizing furnace is disposed with the openable and closable opening facing the fire extinguishing furnace in which the rail is laid inside, and between the carbonizing furnace and the fire extinguishing furnace. A container delivery trolley equipped with folding rails that can move in the direction perpendicular to them and that bridges both furnaces is provided, and multiple carbonization furnaces are arranged in parallel with the fire extinguisher in accordance with the amount of waste discharged The solid organic matter can be distributed without idling by a container delivery truck movable in a direction perpendicular to the direction between the carbonization furnace and the fire extinguishing furnace.

【手続補正11】[Procedure amendment 11]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】0017[Correction target item name] 0017

【補正方法】変更[Correction method] Change

【補正内容】[Correction contents]

【0017】請求項6に記載のように、炭化炉は、側壁
に開閉可能な精錬燃焼空気供給孔を備え、炭化終了時に
空気供給孔を開放して精錬も炭化炉内で行うことがで
き、炭の品質を高めることができる。また、別の精錬炉
の設置を省くことができる。
According to a sixth aspect of the present invention, the carbonization furnace has a smelting combustion air supply hole which can be opened and closed on a side wall, and the air supply hole is opened at the end of carbonization so that smelting can be performed in the carbonization furnace. The quality of charcoal can be improved. Also, the installation of another smelting furnace can be omitted.

【手続補正12】[Procedure amendment 12]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】0018[Correction target item name] 0018

【補正方法】変更[Correction method] Change

【補正内容】[Correction contents]

【0018】請求項7に記載のように、台車は被炭化物
を積み込むコンテナーを備えることができ、コンテナー
の積み降ろしを省いた台車ごとの輸送管理を行うことが
できる。
[0018] As described in claim 7, the truck can be provided with a container for loading the material to be carbonized, and the transport management for each truck can be performed without loading and unloading the container.

【手続補正13】[Procedure amendment 13]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】0040[Correction target item name] 0040

【補正方法】変更[Correction method] Change

【補正内容】[Correction contents]

【0040】[0040]

【発明の効果】以上の説明から明らかのように、本発明
の請求項1記載の固形有機物の炭化装置によれば、木片
や竹片の固形有機物片を積層状態で入れた搬送可能容器
は、台車に搭載されて炭化炉内にその開閉可能な開口部
から導入され、開口部は密閉され、その後、上方部の着
火手段によって容器内部の固形有機物片は上部から着火
されて、着火手段の反対側に設けられた下方部の排気通
路から排気されながら下方部へ燃えて行くようにしてお
り、従って炉内部に余分な空間が生じない状態で搬送可
能容器は台車ごと入れられている為に酸欠状態で蒸し焼
きにされて炭に転換される。炭は、炭素の塊として固定
されており、燃料として、また土壌改良や、河川水浄化
や、脱臭等多方面に広い用途の有る活性炭として利用さ
れる。また、点火時に多量に発生する煙を消煙バーナ部
に切換弁によって導き、消煙燃焼させ、煙の発生が少な
く成ると切換弁によって煙突に導き、野菜の害虫駆除や
消毒に利用可能な防虫、殺菌剤やハム、ソーセジの防腐
剤や消臭剤として利用可能な木酢液と、燃料として利用
可能なタールとが凝縮器から得られる。
As is apparent from the above description, according to the solid organic matter carbonizing apparatus of the first aspect of the present invention, the transportable container in which the solid organic matter pieces such as the wood pieces and the bamboo pieces are put in a laminated state is: It is mounted on a trolley and introduced into the carbonization furnace through its openable and closable opening, the opening is sealed, and then the solid organic matter pieces inside the container are ignited from above by the igniting means in the upper part, and are opposed to the igniting means. It is designed to burn down while being exhausted from the lower exhaust passage provided on the side, so that the transportable containers are put together with the carts without any extra space inside the furnace, so the acid It is steamed in the missing state and converted to charcoal. Charcoal is fixed as a lump of carbon, and is used as a fuel and as activated carbon having a wide variety of uses such as soil improvement, river water purification, and deodorization. In addition, a large amount of smoke generated at the time of ignition is guided to a smoke-suppressing burner by a switching valve, and the smoke is combusted. When the generation of smoke is reduced, the switching valve is used to guide the smoke to a chimney, which can be used for extermination and disinfection of vegetables. A wood vinegar solution that can be used as a disinfectant, a preservative or deodorant for ham and sausage, and tar that can be used as fuel are obtained from the condenser.

【手続補正14】[Procedure amendment 14]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】0042[Correction target item name] 0042

【補正方法】削除[Correction method] Deleted

【手続補正15】[Procedure amendment 15]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】0043[Correction target item name] 0043

【補正方法】変更[Correction method] Change

【補正内容】[Correction contents]

【0043】更に、本発明の請求項2記載の固形有機物
の炭化装置によれば、固形有機物片から炭を得る過程及
び作用は、上記請求項1記載の炭化装置と同等であり、
特にダイオキシンの発生の心配の無い木片や竹片の固形
有機物片を炭の原料とする場合は、燃焼炉を使用せずに
炭化炉のみを使用して上記請求項1記載の炭化装置と同
等に使用できる。
Further, according to the carbonizing apparatus for solid organic matter according to the second aspect of the present invention, the process and action of obtaining charcoal from the solid organic matter pieces are the same as those of the carbonizing apparatus according to the first aspect,
In particular, when using a solid organic material piece such as a wood piece or a bamboo piece having no concern about the generation of dioxin as a raw material for charcoal, using only a carbonization furnace without using a combustion furnace, the same as the carbonization apparatus according to claim 1 above. Can be used.

【手続補正16】[Procedure amendment 16]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】0045[Correction target item name] 0045

【補正方法】変更[Correction method] Change

【補正内容】[Correction contents]

【0045】請求項3記載の固形有機物の炭化装置によ
れば、燃焼炉の排気出口部は、炭化炉の着火手段に開閉
手段を介して接続されており、燃焼炉での完全燃焼によ
って酸素量の少なくなった高温排気ガスを炭化炉に供給
して蒸し焼きを促進させることができる。
According to the third aspect of the present invention, the exhaust outlet of the combustion furnace is connected to the ignition means of the carbonization furnace through the opening / closing means. The high-temperature exhaust gas, which has been reduced, can be supplied to the carbonization furnace to promote steaming.

【手続補正17】[Procedure amendment 17]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】0046[Correction target item name] 0046

【補正方法】変更[Correction method] Change

【補正内容】[Correction contents]

【0046】請求項4記載の固形有機物の炭化装置によ
れば、炭化炉の排気出口部と燃焼炉の入口部との間に
は、炭化炉の可燃ガスを誘引して燃焼炉に供給する誘引
ブロワーが設けられ、誘引ブロワーの回転速度を制御す
ることで炭化炉内での固形有機物の炭化速度を制御する
ことができる。
According to the apparatus for carbonizing solid organic matter according to the fourth aspect, between the exhaust outlet of the carbonizing furnace and the inlet of the combustion furnace, the flammable gas of the carbonizing furnace is attracted and supplied to the combustion furnace. A blower is provided, and by controlling the rotation speed of the induction blower, the carbonization rate of the solid organic matter in the carbonization furnace can be controlled.

【手続補正18】[Procedure amendment 18]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】0047[Correction target item name] 0047

【補正方法】変更[Correction method] Change

【補正内容】[Correction contents]

【0047】請求項5記載の固形有機物の炭化装置によ
れば、炭化炉は、内部にレールが敷設された消火炉と開
閉可能な開口部同士を向かい合わせて配置され、それら
炭化炉と消火炉との間にはそれらと直交する方向に移動
可能で上記両炉に渡って橋渡しする折り畳みレールを備
えた容器配給台車が設けられ、廃棄物の排出量に対応し
て複数炭化炉を消火炉と向かい合わせて並設することが
でき、炭化炉と消火炉の間で直交する方向に移動可能な
容器配給台車によってアイドリングの無いように固形有
機物片の分配ができる。
According to the apparatus for carbonizing solid organic matter according to the fifth aspect, the carbonizing furnace is disposed with the openable and closable opening facing the fire extinguisher with the rail laid therein, and the carbonizing furnace and the fire extinguishing furnace In between, there is provided a container delivery cart having folding rails movable in a direction orthogonal to them and bridging over the two furnaces, and a plurality of carbonizing furnaces and a fire extinguishing furnace corresponding to the amount of waste discharged are provided. The solid organic matter pieces can be distributed without idling by a container delivery cart that can be juxtaposed and movable in an orthogonal direction between the carbonizing furnace and the fire extinguishing furnace.

【手続補正19】[Procedure amendment 19]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】0048[Correction target item name] 0048

【補正方法】変更[Correction method] Change

【補正内容】[Correction contents]

【0048】請求項6記載の固形有機物の炭化装置によ
れば、炭化炉は、側壁に開閉可能な精錬燃焼空気供給孔
を備え、炭化終了時に空気供給孔を開放して精錬も炭化
炉内で行うことができ、炭の品質を高めることができ
る。また、別の精錬炉の設置を省くことができる。
According to the apparatus for carbonizing solid organic matter according to the sixth aspect, the carbonization furnace has a refining combustion air supply hole which can be opened and closed on the side wall, and when the carbonization is completed, the air supply hole is opened to perform refining in the carbonization furnace. Can be done and the quality of charcoal can be increased. Also, the installation of another smelting furnace can be omitted.

【手続補正20】[Procedure amendment 20]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】0049[Correction target item name] 0049

【補正方法】変更[Correction method] Change

【補正内容】[Correction contents]

【0049】請求項7記載の固形有機物の炭化装置によ
れば、台車は被炭化物を積み込むコンテナーを備えるこ
とができ、コンテナーの積み降ろしを省いた台車ごとの
輸送管理を行うことができる。
According to the carbonizing device for solid organic matter according to the seventh aspect, the carriage can be provided with a container for loading the material to be carbonized, and the transportation of each carriage can be controlled without loading and unloading the container.

Claims (8)

【特許請求の範囲】[Claims] 【請求項1】 木片や竹片の固形有機物片を積層状態で
収容するようにガス通過可能な側壁で形成された搬送可
能容器と、 該容器の外形にほぼ一致した横断面形状でやや大きい炉
内部が耐火材で形成され、上記容器の出し入れ用の開閉
可能な開口部と、上方部の着火手段と、該着火手段の反
対側に設けられた下方部の排気通路とを備えた炭化炉
と、 該炭化炉の炉内部に上記開口部を経て敷設されたレール
上で移動可能で且つ上記容器の搭載可能な低い台車とか
ら構成されており、 上記台車上に搭載された上記搬送可能容器に木片や竹片
の固形有機物片を積層状態で入れ、上記炭化炉の炉内部
に余分な空間が生じない状態で上記台車ごと入れて開口
部を密閉し、上記上方部の着火手段によって上記容器内
の固形有機物片の上部に着火させ、その上部から下部に
かけて酸欠状態で蒸し焼きしながら下部まで炭化を進行
させて炭化物を得ることを特徴とする固形有機物の炭化
装置。
1. A transportable container formed of gas-permeable side walls for accommodating solid organic material pieces such as wood pieces and bamboo pieces in a laminated state, and a furnace having a slightly larger cross-sectional shape substantially matching the outer shape of the vessel. An inner portion formed of a refractory material, a carbonization furnace having an openable and closable opening for taking in and out of the container, an upper ignition section, and a lower exhaust passage provided on the opposite side of the ignition section. A low carriage movable on a rail laid through the opening inside the furnace of the carbonization furnace and capable of mounting the container, wherein the transportable container mounted on the carriage includes Solid organic matter pieces such as wood pieces and bamboo pieces are put in a stacked state, and the cart is put together with the carriage in a state where no extra space is created inside the furnace of the carbonization furnace, and the opening is sealed. Ignite the top of the piece of solid organic matter A carbonization apparatus for solid organic matter, characterized in that carbonization proceeds from the upper part to the lower part while being roasted in an oxygen-deficient state while carbonizing to the lower part to obtain a carbide.
【請求項2】 上記排気通路は切換弁を介して消煙バー
ナ部と煙突に接続されており、該煙突は排気から木酢液
やタールを凝縮する凝縮器を備えている請求項1記載の
炭化装置。
2. The carbonizing apparatus according to claim 1, wherein the exhaust passage is connected to a smoke-suppressing burner and a chimney via a switching valve, and the chimney includes a condenser for condensing wood vinegar and tar from exhaust gas. apparatus.
【請求項3】 廃棄木材片や廃棄タイヤ等の固形有機質
系廃棄物片や、各種のプラスチック屑や紙屑を含む有機
質系廃棄物やシュレッダーダストや糞尿汚泥等の粘ちょ
う性有機質系廃棄物を混練、圧密化して得られた固形再
生燃料とかシュレッダーダスト成形固化物等の有機質系
廃棄物片を積層状態で収容するようにガス通過可能な側
壁で形成された搬送可能容器と、 該容器の外形にほぼ一致した横断面形状でやや大きい炉
内部が耐火材で形成され、上記容器の出し入れ用の開閉
可能な開口部と、上方部の着火手段と、該着火手段の反
対側に設けられた下方部の排気通路とを備えた炭化炉
と、 上記排気通路に接続されて上記炭化炉から導入した可燃
ガスを燃焼させるバーナを入口部に備え、炉内にガス流
迂回壁を備えると共に、排気を出口部から大気中に排出
する燃焼炉と、 上記炭化炉の炉内部に上記開口部を経て敷設されたレー
ル上で移動可能で且つ上記容器の搭載可能な低い台車と
から構成されており、 上記台車上に搭載された上記搬送可能容器に木片や竹片
の固形有機物片を積層状態で入れ、上記炭化炉の炉内部
に余分な空間が生じない状態で上記台車ごと入れて開口
部を密閉し、上記上方部の着火手段によって上記容器内
の固形有機物片の上部に着火させ、その上部から下部に
かけて酸欠状態で蒸し焼きしながら下部まで炭化を進行
させて炭化物を得ると共に、その間にガス化した可燃ガ
スを上記燃焼炉内に導入して800℃以上で完全燃焼さ
せて排気ガス1m3 中のダイオキシン含有量を0.1ナ
ノグラム未満とすることを特徴とする固形有機物の炭化
装置。
3. Kneading solid organic waste pieces such as waste wood pieces and waste tires, organic waste containing various types of plastic waste and paper waste, and viscous organic waste such as shredder dust and manure sludge. A transportable container formed of gas-permeable side walls so as to accommodate a solid regenerated fuel obtained by consolidation or an organic waste piece such as a shredder dust solidified product in a stacked state; The inside of the furnace, which has a slightly larger cross-sectional shape and is somewhat large, is formed of a refractory material, an opening and closing opening for opening and closing the container, ignition means on the upper part, and a lower part provided on the opposite side of the ignition means. An exhaust passage, and a burner connected to the exhaust passage for burning combustible gas introduced from the carbonization furnace at an inlet portion, a gas flow bypass wall in the furnace, and an exhaust outlet. Department And a low carriage movable on a rail laid through the opening inside the furnace of the carbonization furnace and capable of mounting the container. The solid organic matter pieces such as wood pieces and bamboo pieces are put in a stacked state in the transportable container mounted on the above, and the cart is put together with the cart in a state where no extra space is generated inside the furnace of the carbonization furnace, and the opening is sealed, The upper part of the solid organic matter piece in the container is ignited by the upper part ignition means, carbonization proceeds to the lower part while steaming in an oxygen-deficient state from the upper part to the lower part to obtain a carbide, and the combustible gas gasified in the meantime Wherein the dioxin content in 1 m 3 of exhaust gas is reduced to less than 0.1 nanograms by introducing into the combustion furnace and burning completely at 800 ° C. or higher.
【請求項4】 上記燃焼炉の排気出口部は、上記炭化炉
の着火手段に開閉手段を介して接続されており、酸素量
の少なくなった高温排気ガスを上記炭化炉に供給して上
記蒸し焼きを促進させる請求項3記載の炭化装置。
4. An exhaust outlet of the combustion furnace is connected to an ignition means of the carbonization furnace via an opening / closing means, and supplies high-temperature exhaust gas having a reduced amount of oxygen to the carbonization furnace to provide the steaming. The carbonization device according to claim 3, wherein the carbonization is promoted.
【請求項5】 上記炭化炉の排気出口部と上記燃焼炉の
入口部との間には、上記炭化炉の可燃ガスを誘引して上
記燃焼炉に供給する誘引ブロワーが設けられている請求
項3記載の炭化装置。
5. An induction blower for attracting combustible gas from the carbonization furnace and supplying the combustible gas to the combustion furnace is provided between an exhaust outlet of the carbonization furnace and an inlet of the combustion furnace. 3. The carbonizing device according to 3.
【請求項6】 上記炭化炉は、内部にレールが敷設され
た消火炉と開閉可能な開口部同士を向かい合わせて配置
されており、それら炭化炉と消火炉との間にはそれらと
直交する方向に移動可能で上記両炉に渡って橋渡しする
折り畳みレールを備えた容器配給台車が設けられている
請求項1又は3記載の炭化装置。
6. The carbonization furnace is arranged with a fire extinguisher with a rail laid therein and openable and closable openings facing each other, and a space between the carbonization furnace and the fire extinguishing furnace is orthogonal to them. 4. The carbonization apparatus according to claim 1, further comprising a container delivery truck provided with a folding rail movable in a direction and bridging the two furnaces.
【請求項7】 上記炭化炉は、側壁に開閉可能な精錬燃
焼空気供給孔を備えている請求項1又は3記載の炭化装
置。
7. The carbonization apparatus according to claim 1, wherein the carbonization furnace has a smelting combustion air supply hole that can be opened and closed on a side wall.
【請求項8】 上記台車は、被炭化物を積み込むコンテ
ナーを備えている請求項1又は3記載の炭化装置。
8. The carbonizing apparatus according to claim 1, wherein the cart includes a container for loading the material to be carbonized.
JP10038591A 1998-02-20 1998-02-20 Solid organic carbonization equipment Expired - Fee Related JP2951632B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10038591A JP2951632B2 (en) 1998-02-20 1998-02-20 Solid organic carbonization equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10038591A JP2951632B2 (en) 1998-02-20 1998-02-20 Solid organic carbonization equipment

Publications (2)

Publication Number Publication Date
JPH11236572A true JPH11236572A (en) 1999-08-31
JP2951632B2 JP2951632B2 (en) 1999-09-20

Family

ID=12529553

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10038591A Expired - Fee Related JP2951632B2 (en) 1998-02-20 1998-02-20 Solid organic carbonization equipment

Country Status (1)

Country Link
JP (1) JP2951632B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001262579A (en) * 2000-03-17 2001-09-26 Nisshoku Corp Treating method for thinnings, extracted root, construction surplus soil and compressed block
JP2002241761A (en) * 2001-02-21 2002-08-28 Mhi Environment Engineering Co Ltd Method for treating lumber from thinning and pruned branch, and treating system

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001262579A (en) * 2000-03-17 2001-09-26 Nisshoku Corp Treating method for thinnings, extracted root, construction surplus soil and compressed block
JP2002241761A (en) * 2001-02-21 2002-08-28 Mhi Environment Engineering Co Ltd Method for treating lumber from thinning and pruned branch, and treating system

Also Published As

Publication number Publication date
JP2951632B2 (en) 1999-09-20

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