JP2008106209A - Small carbonization furnace with distributed power generation function - Google Patents
Small carbonization furnace with distributed power generation function Download PDFInfo
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- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/12—Heat utilisation in combustion or incineration of waste
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- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/10—Biofuels, e.g. bio-diesel
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- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
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- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
- Y02P20/129—Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines
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- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/78—Recycling of wood or furniture waste
Abstract
Description
本発明は、有機物の小型炭化装置に係るもので、特に山中やゴルフ場において間伐材や剪定枝或いは水分の多い芝などを運送することなく現地で減量且つ炭化することにより従来は廃棄物として処理されたものを炭化燃料として資源化することを可能とした、小型の炭化装置に関するものである。 The present invention relates to a small-sized carbonization device for organic matter, and is conventionally treated as waste by reducing and carbonizing locally in the mountains and golf courses without transporting thinned wood, pruned branches, or moisturey turf. The present invention relates to a small-sized carbonization apparatus that makes it possible to use the carbonized fuel as a carbonized fuel.
生ごみや汚泥等の有機物を、過熱水蒸気を利用して炭化することは既に公知である。
過熱水蒸気を使用するためには、先ず過熱水蒸気を作らなければならない。
過熱水蒸気の製造は、先ず水を沸騰させて飽和水蒸気を製造し、できた飽和水蒸気を加熱して過熱水蒸気とする必要がある。
特許文献1に開示されているように、従来の装置は、飽和水蒸気の製造装置と、水蒸気の過熱装置と、過熱水蒸気を吹き込む炭化炉が別々の構造であり、大量の電力又は長時間を必要とし装置が大型化し、設備費が極めて高くなる欠点がある。
炭化は廃棄物の減容化はもとより炭素の固定化により地球温暖化防止対策即ちCO2対策に極めて有効である。また併せて無害安全にそのまま土壌改良剤や、調湿剤として有効に利用できる利点もある。本件は特にゴルフ場などでは生成した炭化物を直接ゴルフ場へ散布することが可能となり、山林などでも現地で直接減容炭化し、その炭化物は直接現地で山林の土壌改良に利用することができ、且つ装置は無煙無臭で、減容炭化できるものである。It is already known to carbonize organic matter such as garbage and sludge using superheated steam.
In order to use superheated steam, it must first be made.
In order to produce superheated steam, it is necessary to first boil water to produce saturated steam, and to heat the resulting saturated steam to superheated steam.
As disclosed in Patent Document 1, a conventional apparatus has a structure in which a saturated steam production apparatus, a steam superheater, and a carbonization furnace for blowing superheated steam are separate structures, and requires a large amount of power or a long time. However, there is a drawback that the apparatus becomes large and the equipment cost becomes extremely high.
Carbonization is extremely effective for preventing global warming, that is, for CO2 by fixing carbon as well as reducing the volume of waste. In addition, there is also an advantage that it can be effectively used as a soil conditioner or a humidity control agent as it is without harm. In this case, especially in golf courses, the generated carbides can be sprayed directly to golf courses, and in the forests, etc., the volume can be reduced directly, and the carbides can be directly used for soil improvement of the forests. The apparatus is smokeless and odorless and can be reduced in volume.
本発明はかかる問題点に鑑みてなされたもので、その目的は、小型で持ちはこびでき、各ゴルフ場の芝刈現場、山林での伐採現場やホテルなどの勝手口に直接配置することができ、かつ排ガスが無煙・無臭で処理できる有機物の炭化装置を提供することである。 The present invention has been made in view of such problems, and its purpose is small and portable, and can be directly placed on the lawn mowing site of each golf course, a logging site in a forest, a hotel, etc. And it is providing the carbonization apparatus of the organic substance which can process exhaust gas by smokeless and odorless.
炭化炉に関する上記問題点は、下記構成の本発明炭化炉によって解決することができる。
すなわち、本発明炭化炉の構造は、
上部に開閉扉を有する密閉された炉体キャビティーを上下別々の部屋に区画し、炭化目的の処理物が投入される最初の部屋は、炭化の前段処理機能としての有機物の乾燥部屋であり、最下部の加熱室からの廃熱投入により処理物の乾燥を行い、同区画下部側には一定時間で開閉する仕切り盤がついた炭化室への処理物の移行ゲートがあり、同移行ゲートが開くと処理物は区画された下方の炭化部屋に移動し、炭化部屋は過熱水蒸気の吹き込みにより還元雰囲気状態となり乾燥後の処理物の炭化が促進される構造であって、該開閉扉から投入され乾燥処理された有機質廃棄物は仕切り盤を通過後、過熱蒸気により炭化する炭化炉であって、炭化の際の熱分解ガスは炭化炉壁面に排出する排気装置が取り付けられ炭化炉の排気装置取り付け口には熱分解ガスを無害化する触媒装置が取り付けられ、乾燥並び炭化の両炉内中心部には排熱や過熱蒸気が行き渡りやすいように縦軸を中心として回転する複数枚の円盤がとりつけてあり、且つその円盤が逆転すれば炉内で処理された炭化物が炉外へ排出されるように、炭化炉最下部には円盤に直結した排出口が設けられており、該2室の炉体底面部には、セパレート型で加熱装置室が附設してあり、該加熱装置室内部には飽和蒸気発生機能並びに過熱蒸気発生装置並びに、温度差で発電する発電機能付きスターリングエンジンが取り付けられており、過熱蒸気で廃棄物を炭化すると同時に発電ができることを特徴とする小型炭化装置。The above-mentioned problems related to the carbonization furnace can be solved by the carbonization furnace of the present invention having the following configuration.
That is, the structure of the carbonization furnace of the present invention is
A closed furnace body cavity having an open / close door at the top is divided into upper and lower separate rooms, and the first room into which the treatment object for carbonization is charged is an organic matter drying room as a pretreatment function of carbonization, Processed material is dried by inputting waste heat from the lowermost heating chamber, and there is a transition gate for the processed material to the carbonization chamber with a partition plate that opens and closes for a certain time on the lower side of the section. When opened, the treated material moves to the lower carbonized compartment, and the carbonized chamber is in a reducing atmosphere state by blowing superheated steam to promote carbonization of the treated material after drying. The organic waste that has been dried is a carbonization furnace that carbonizes with superheated steam after passing through the partition board, and an exhaust device that discharges the pyrolysis gas during carbonization to the wall surface of the carbonization furnace is attached, and the exhaust device is attached to the carbonization furnace In the mouth A catalytic device for detoxifying the cracked gas is attached, and a plurality of disks rotating around the vertical axis are attached to the center of both dry and carbonized furnaces so that exhaust heat and superheated steam are easily distributed, and A discharge port directly connected to the disk is provided at the bottom of the carbonization furnace so that the carbide treated in the furnace is discharged out of the furnace if the disk is reversed, and the bottom of the furnace body of the two chambers is provided. Is a separate type and has a heating device chamber, and in the heating device chamber, a saturated steam generating function and a superheated steam generator, and a Stirling engine with a power generation function for generating power at a temperature difference are attached. A small carbonization device that can generate electricity at the same time as carbonizing waste.
乾燥機能並びに炭化炉と飽和蒸気生成装置、過熱水蒸気生成装置並びに発電装置が一体になった小型で持ちはこびが出来、無煙無臭であるため山林の剪定枝やゴルフ場の芝など各種廃棄物を発生現場で直接減容、炭化処理が可能となるばかりか、特に電気の届かない地域でも周辺の有機性廃棄物さえあればそれらを熱源として発電が可能となり、電気の届かない地域特に離島や山間地でも容易に現地での分散型発電が可能となる。Small size, durable, and odorless with a drying function, carbonization furnace, saturated steam generator, superheated steam generator, and power generator, producing various wastes such as pruned branches in forests and grass on golf courses. Not only can the volume be reduced and carbonized directly at the site, but even in areas where electricity cannot reach, it is possible to generate electricity using those nearby organic wastes as heat sources, especially in remote islands and mountainous areas where electricity does not reach However, distributed power generation can be easily performed locally.
本発明炭化炉の構造とその作用機能を図面で説明する。
第1図は、本発明構造の説明図である。
上部に開閉扉7を有する密閉された炉体キャビティーを上下別々の部屋に区画し、処理物が投入される最初の部屋は、炭化の前段処理機能としての有機物の乾燥部屋であり、最下部加熱室からの廃熱投入により処理物の乾燥を行い、同乾燥室下部の炭化部屋側との間には一定時間で開閉する仕切り盤がついた炭化室移行ゲート10があり、同仕切盤の移行ゲート10が開くと乾燥した処理物は区画された下方の炭化部屋に移動し、下方の炭化室は過熱水蒸気の吹き込みにより還元雰囲気状態となり炭化が促進される構造であって、該最上部開閉扉7から投入された処理物は上段区画室で乾燥処理された後、炉内かくはん機3の逆転により仕切り盤の移行ゲート10を通過し、かくはん機の逆転が停止すると移行ゲートが閉まり、下段の炭化室に搬送された処理物は、炭化室に吹き込まれた過熱蒸気により、炭化炉内は還元雰囲気状態が醸成されると同時に、投入された有機質廃棄物に高温の過熱蒸気が直接噴射されることにより、処理物の炭化が同時進行する炭化炉であって、該2室の炉体底面部には、飽和蒸気を生成するボイラー機能6並びに過熱蒸気5を生成する加熱室が附設されており、該加熱室には高温廃熱で発電する発電機能付きスターリングエンジン11が附設されたことを特徴とする小型炭化炉。The structure of the carbonization furnace of the present invention and its function will be described with reference to the drawings.
FIG. 1 is an explanatory diagram of the structure of the present invention.
A closed furnace cavity having an open / close door 7 at the top is divided into upper and lower separate chambers, and the first chamber into which the processed material is introduced is an organic matter drying chamber as a pre-treatment function for carbonization, There is a carbonization chamber transition gate 10 with a partition plate that opens and closes in a certain time between the carbonization chamber side at the bottom of the drying chamber, and the treated product is dried by inputting waste heat from the heating chamber. When the transition gate 10 is opened, the dried product is moved to a partitioned lower carbonization chamber, and the lower carbonization chamber is in a reducing atmosphere state by blowing superheated steam to promote carbonization. The processed material introduced from the door 7 is dried in the upper compartment and then passes through the transition gate 10 of the partition board by the reverse rotation of the in-furnace stirrer 3. When the reverse rotation of the agitator stops, the transition gate is closed and the lower step Carbonization chamber The treated material transported by the superheated steam blown into the carbonization chamber fosters a reducing atmosphere in the carbonization furnace, and at the same time, high-temperature superheated steam is directly injected into the input organic waste, A carbonization furnace in which the carbonization of the processed material proceeds at the same time, and a boiler function 6 for generating saturated steam and a heating chamber for generating superheated steam 5 are attached to the bottom of the furnace body of the two chambers. A small carbonization furnace characterized in that a Stirling engine 11 with a power generation function for generating power with high-temperature waste heat is attached to the chamber.
本発明炭化炉は、炉体キャビティーの周囲と底面を断熱材で囲まれた構造からなり、上部の開閉扉を開けて炭化する有機質廃棄物を投入する。有機質廃棄物は、そのままの現状投入、大型なら破砕処理後の投入、粉末などはボックスによる分散投入、オムツなどは炭化室内にスライド式の棚などを複数段設けその棚ごと投入するなど、扱いやすく且つ投入物によっては過熱蒸気の浸透がしやすいようにして投入する。
投入する有機物廃棄物は、廃木材、剪定枝、ゴルフ場の芝、生ごみ、残飯、おから、、野菜屑、食品残渣等、日常生活で排出される有機質のごみ類、およびその他必要に応じてほとんどの有機質廃棄物を投入して乾燥炭化することができる。又特別管理物である医療廃棄物についても殺菌、滅菌はもとより無煙無臭で無害化し減容炭化することができる。The carbonization furnace of the present invention has a structure in which the periphery and bottom surface of the furnace body cavity are surrounded by a heat insulating material, and an organic waste to be carbonized is opened by opening an upper opening / closing door. Organic waste can be handled as it is, such as loading the current state, throwing it after crushing treatment for large-sized products, dispersing powder using powder in boxes, and placing diapers in the carbonization chamber with multiple slide shelves. In addition, depending on the input, it is introduced so that superheated steam can easily penetrate.
Organic waste to be input includes waste wood, pruned branches, golf course turf, food waste, leftover food, okara, vegetable waste, food residue, etc., organic waste discharged in daily life, and other as required Most of the organic waste can be put into dry carbonization. In addition, medical waste that is specially managed can be sterilized and sterilized, as well as smokeless and odorless, detoxified and reduced in volume.
有機性廃棄物を投入後、開閉扉を閉めて、前段乾燥後、炉体キャビティーに過熱水蒸気を吹き込む。過熱水蒸気は、炉体の底部に設けられた加熱装置の炉壁部分のボイラー機能6で、先ず飽和水蒸気を作り、次に加熱装置天井部に設けられた過熱蒸気発生装置5で飽和水蒸気を過熱して過熱水蒸気とする。飽和水蒸気を作るための水は、炉体の外に設けた水タンク又は直結した水道から供給する。 After throwing in the organic waste, the door is closed, and after drying in the previous stage, superheated steam is blown into the furnace cavity. The superheated steam is first produced by the boiler function 6 in the furnace wall portion of the heating device provided at the bottom of the furnace body, and then superheated by the superheated steam generator 5 provided at the ceiling of the heating device. To superheated steam. Water for producing saturated steam is supplied from a water tank provided outside the furnace body or directly connected water.
炉体キャビティーの中は、廃熱利用による乾燥室並びに、吹き込んだ過熱水蒸気と底面の加熱部分、及び炉体キャビティーを保温する為に外周に設けられた加熱保温装置からの廃熱を分離した排気ガスを利用した保温装置により炭化炉内は高温に維持され、炉内は概ね330〜550℃程度の温度に加熱される。The inside of the furnace cavity separates the waste heat from the drying chamber using waste heat, the heated superheated steam and the heated part of the bottom, and the heat insulation device provided on the outer periphery to keep the furnace cavity warm. The inside of the carbonization furnace is maintained at a high temperature by the heat insulation device using the exhaust gas thus heated, and the inside of the furnace is heated to a temperature of about 330 to 550 ° C.
加熱装置部の熱源は330℃以上の過熱蒸気が生成できる熱源なら、重油や灯油バーナー、ガスバーナー、電気ヒーター、或いは薪焚きなどによるバイオマス燃料などいずれでも良いが出来れば550℃程度の過熱蒸気が短時間に生成できる熱源がより好ましい。If the heat source of the heating unit is a heat source that can generate superheated steam of 330 ° C or higher, it can be any fuel oil such as heavy oil, kerosene burner, gas burner, electric heater, or firewood. A heat source that can be generated in a short time is more preferable.
キャビティーの中、特に炭化室は過熱蒸気の吹込みにより炉内酸素が追い出され、無酸素状態の還元雰囲気並びに過熱水蒸気雰囲気であるために、炉内に投入された有機物は、燃焼することなく、水分及び揮発性の非有機質成分、有機質成分は共に蒸発、一部の有機物は熱分解されてガスとなる。非熱分解成分は炭化されて、固形の炭化物となる。 In the cavity, especially in the carbonization chamber, oxygen in the furnace is expelled by blowing superheated steam, and since there is an oxygen-free reducing atmosphere and superheated steam atmosphere, the organic matter put into the furnace does not burn. Both water and volatile non-organic components and organic components evaporate, and some organic substances are thermally decomposed into gas. Non-pyrolytic components are carbonized to form solid carbide.
排ガスの成分は、これら水分、揮発性の非有機質成分、有機質成分及び有機物の熱分解ガスからなり、燃焼性ガスも含んでおり、加熱装置から排出される高温の排ガスと合流することにより、高温急速燃焼して臭いの成分も完全に加熱分解されて無煙無臭になる。
加熱装置から排出される排ガス温度は、600℃以上が良い。600℃未満では炉体キャビティーから排出される熱分解ガスとの混合の際、臭いの成分が完全に燃焼分解されず、臭気が残る。この際低温の為臭いなどが残る場合には、熱分解ガスの臭いなどの完全燃焼を促す為、排気混合部分に小さいバーナーを取り付けても良い。又は加熱室に取り付けたスターリングエンジンに発電機を付設して電気できる為、電気ヒーターを取り付けても良い。The components of the exhaust gas are composed of these moisture, volatile non-organic components, organic components, and pyrolysis gases of organic matter, and also include combustible gases. When combined with the high-temperature exhaust gas discharged from the heating device, It burns rapidly and the odorous components are completely decomposed by heating and become smokeless and odorless.
The exhaust gas temperature discharged from the heating device is preferably 600 ° C. or higher. When the temperature is lower than 600 ° C., the odor component is not completely burned and decomposed when mixed with the pyrolysis gas discharged from the furnace cavity, and the odor remains. At this time, if the odor remains because of the low temperature, a small burner may be attached to the exhaust gas mixing portion in order to promote complete combustion such as the odor of the pyrolysis gas. Alternatively, an electric heater may be attached because a generator can be attached to a Stirling engine attached to the heating chamber.
有機質廃棄物の内、木材系は投入後概ね60分で炭化が終わる。生ごみやオムツなど含水率が80%以上あるような廃棄物は120分を要する。
炭化物は炭化室内に残留するので、炉体キャビティー底部に設けた回転式円盤の逆転により炭化物排出口から自動的に排出される。又燃えない無機質、金属成分も炭化物と一緒に外に取り出すことが出来る。Of the organic wastes, the carbonization of the wood system ends in about 60 minutes after the addition. Wastes with a moisture content of 80% or more, such as kitchen waste and diapers, require 120 minutes.
Since the carbide remains in the carbonization chamber, it is automatically discharged from the carbide discharge port by reversing the rotary disk provided at the bottom of the furnace cavity. Also, non-burning inorganic and metal components can be taken out together with carbides.
実施例によって本発明を説明する。
炭化炉の構造:第1図の構造
炉体キャビティー部の乾燥室及び炭化室合計内容積 : 約0.55m3
炉体部寸法:幅1.5m×奥行き1.7m×高さ2.6m(車載処理可能)
炉内温度: 550℃
過熱蒸気温度:450℃
ごみの種類:剪定技、ゴルフ場芝
剪定枝を各30cm程度に裁断し、刈った芝と半々程度合計約60kgを直接上段の乾燥室に投入し、投入口を密閉後スイッチONし、約40分間廃熱を利用して乾燥した後、次に仕切り盤の炭化室移行ゲートを開け処理物を炭化室に移動した。最初に乾燥室に投入してから合計約1.5時間で炭化が完了。炭化終了後、炉内円盤を逆転し炭化物を取り出した。芝はほとんど原型が無くなり剪定枝のみが原型を留めまま炭化し、重量は約5kgであった。又その間加熱装置室に取り付けたスターリングエンジンによる発電も55kw能力があるものの加熱装置部の温度が低い為25kw程度の発電でしたが、電気の届かない山林でもごみ処理を兼ねながら十分電気を賄うことが出来、排ガスも無色、無臭であった。The examples illustrate the invention.
Structure of carbonization furnace: structure of Fig. 1 Total volume of drying chamber and carbonization chamber in the furnace body cavity: about 0.55m 3
Furnace size: 1.5m width x 1.7m depth x 2.6m height (can be mounted on vehicle)
Furnace temperature: 550 ° C
Superheated steam temperature: 450 ° C
Garbage type: pruning technique, golf course turf Pruned branches are cut to about 30 cm each, about 60 kg of cut grass and half are put directly into the upper drying chamber, the inlet is sealed, the switch is turned on, and about 40 After drying using waste heat for a minute, the gate of the partitioning chamber was opened, and the treated product was moved to the chamber. Carbonization is completed in about 1.5 hours in total after first putting into the drying room. After the completion of carbonization, the inside of the furnace disk was reversed and the carbide was taken out. The turf almost disappeared and only the pruned branches were carbonized while retaining the original shape, and the weight was about 5 kg. During that time, power generation by the Stirling engine installed in the heating device room was 55 kW, but it was about 25 kW because the temperature of the heating device was low. The exhaust gas was also colorless and odorless.
以上詳記した様に、本発明小型炭化炉は、車載で簡単に持ち運び可能であるので有機機質廃棄物であれば、いかなるものでも、現地で簡単、簡便、迅速に、かつ悪臭を発生させることも無く、乾燥炭化、減容化でき、ごみ収集コスト、ごみ処理費用の低減が可能となることはもとより、電気の届かない地域でも廃棄物さえあれば発電も簡易に可能であり、分散型発電が廉価に且つ手軽に可能となり、従来廃棄物として扱われた廃棄物が、炭化物として燃料に生まれ変わることが出来、周辺住民に嫌われる大型のごみ処理施設の建設をも不用とするものであり、廃棄物処理分野で多大の貢献をなすものである。As described in detail above, the small carbonization furnace of the present invention can be easily carried on-board, so any organic waste can easily, conveniently, quickly and generate a bad odor on the spot. It is possible to reduce carbonization, volume reduction, waste collection costs and waste disposal costs, and even in areas where electricity does not reach, it is possible to easily generate electricity as long as there is waste. Power generation is cheap and easy, and waste that has been treated as waste can be converted into fuel as charcoal, making it unnecessary to construct a large waste disposal facility that is disliked by the surrounding residents. It makes a great contribution in the field of waste treatment.
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2012096186A (en) * | 2010-11-04 | 2012-05-24 | Yuichi So | Treatment method of infectious waste and treatment apparatus thereof |
JP2012120503A (en) * | 2010-12-10 | 2012-06-28 | Imura Satoru | Forest resource using system |
CN103173232A (en) * | 2012-11-30 | 2013-06-26 | 徐学冬 | Method for realizing intensive production and comprehensive utilization of forestry residues |
JP2013178164A (en) * | 2012-02-28 | 2013-09-09 | Nisshin Steel Co Ltd | Continuous volume reduction storage system vehicle for radioactive substance contaminated organic material |
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2006
- 2006-10-24 JP JP2006313561A patent/JP2008106209A/en active Pending
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2012096186A (en) * | 2010-11-04 | 2012-05-24 | Yuichi So | Treatment method of infectious waste and treatment apparatus thereof |
JP2012120503A (en) * | 2010-12-10 | 2012-06-28 | Imura Satoru | Forest resource using system |
JP2013178164A (en) * | 2012-02-28 | 2013-09-09 | Nisshin Steel Co Ltd | Continuous volume reduction storage system vehicle for radioactive substance contaminated organic material |
CN103173232A (en) * | 2012-11-30 | 2013-06-26 | 徐学冬 | Method for realizing intensive production and comprehensive utilization of forestry residues |
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