JP2008196710A - Compact waste mixing, melting and solidifying device for asbestos, medical waste, general waste and the like - Google Patents

Compact waste mixing, melting and solidifying device for asbestos, medical waste, general waste and the like Download PDF

Info

Publication number
JP2008196710A
JP2008196710A JP2006154011A JP2006154011A JP2008196710A JP 2008196710 A JP2008196710 A JP 2008196710A JP 2006154011 A JP2006154011 A JP 2006154011A JP 2006154011 A JP2006154011 A JP 2006154011A JP 2008196710 A JP2008196710 A JP 2008196710A
Authority
JP
Japan
Prior art keywords
combustion
waste
furnace
heat
air
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.)
Pending
Application number
JP2006154011A
Other languages
Japanese (ja)
Inventor
Shinichiro Kojima
信一郎 小嶋
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP2006154011A priority Critical patent/JP2008196710A/en
Publication of JP2008196710A publication Critical patent/JP2008196710A/en
Pending legal-status Critical Current

Links

Images

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
    • Y02E20/00Combustion technologies with mitigation potential
    • Y02E20/12Heat utilisation in combustion or incineration of waste
    • 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

  • Incineration Of Waste (AREA)
  • Chimneys And Flues (AREA)
  • Processing Of Solid Wastes (AREA)

Abstract

<P>PROBLEM TO BE SOLVED: To provide a furnace of a compact and simplified structure, which performs at a high speed combustion melting processing of wastes such as asbestos, medical water and general waste. <P>SOLUTION: The secondary air is spirally introduced into a furnace from a furnace wall, radiation heat is collected to a central portion simultaneously with generation of vortex inside, and a combustion promotor (nitro series) is charged or inserted to the central portion to form a combustion melting atmosphere at the central portion. A heat-resisting tray is disposed just under the combustion melting atmosphere. A burner for main combustion is disposed on a part of a clearance between the heat-resisting tray and a main body. Oxygen is taken into the central portion of the spiral portion by atmospheric air, the waste is slowly stirred with the combustion additive, and a spot temperature rise part is formed by synergetic effect of oxygen and the additive, so that an organic substance is burned and melted, and an inorganic substance is melted in the area. Depending on the wastes, the waste may be heated up to its melting point by activating calory generated by the burner for main combustion. The molten matter is taken out from a discharge pipe and processed as a solid material. <P>COPYRIGHT: (C)2008,JPO&INPIT

Description

本発明は、現状アスベストなる有害危険物質を過去数十年前より建築物、構造物等の耐火被覆材として広く活用されてきましたが、現状極めて人体に有害であるということが特定でき、除去、廃棄することが非常に高価につき完全な決め手が現状ではありません。そこで今回発明した小型溶融固形化方式は先ず円筒状の処理室を形成し、(円筒状とは輻射熱を円筒状の中心部に全て集中するために行う形状であり、それに使われる材質は反射効率の良い物を使用し、又遠赤外線を出すような処理も行う場合もある)その処理室の周囲より円周上に対して空気で静圧をかけ円周上周囲に設けた吹き出し口より壁面に沿って回転方向に噴射することで、空気層を作り中心部の高温燃焼部より壁面を保護するとともに壁面に吹き込んだ空気の中で酸素は被酸化物と化合して水又は二酸化炭素、空気は上記の如く燃焼部分の高温帯から耐火物或いは耐熱金属等を酸化から保護するとともに外気を連続的に圧入することでこの現象は連続的に起き、内部に充満しすぎた空気は上記同様、排気口下部には水プールを設け、その水プールには静圧、送風管から分岐した空気を穴あきパイプ及びそれに付随する方法により、水プール底部よりエアーブローする場合がある。マイクロミクロンダストの大気中への飛散を防止し、そこから排煙燃焼室に流れ込み、それを経て排気口より排出される構造、排気口の中央部にハニカム状に設置した耐熱耐蝕鋼管、又はステンレス系耐熱耐蝕鋼管及びセラミック管等を設置し、その隙間を排気熱が通過することで熱交換用パイプ形状のパイプを加熱し、加熱した中に主燃焼用に必要な外気(大気)をブロアー、ターボブロアー、シロッコファン、多段式静圧ファン、軸流ファン等を使用し、それを内部に設けた主燃焼室に燃焼状況に合わせインバータ等を活用し、風量静圧の調整を自動的に行い、内部主燃焼室を溶融温度(つまりアスベストの溶融温度)まで上げそこに燃焼促進剤を適量挿入し、燃焼促進剤により中心部の燃焼各外炎部分を急激に温度上昇させることでアスベストを溶融瞬時に固形化するものである。又固形化したアスベストの溶融石は炉内主燃焼室下部に設けた耐火トレイの上に溶融石として堆積させ下部耐火トレイを定期的に排出勾配を持った状態で外部に安全な溶融石として排出される。耐熱トレイと内部空気回転層との中間位置に主燃焼用バーナー、石油系ガス系のものを設置し、耐火トレイと炉床部分との間に位置する排気口の一部に回転気流に合わせた方向に燃焼フレームが伸びるようバーナーをセットし、バーナーの先端部には主燃焼バーナーが燃焼中は上蓋は自動的にスライドし、バーナーを保護するような構造を有し、バーナー停止時はスライドし、耐熱耐蝕鋼又は主々の耐酸化鋼及び超耐火煉瓦、セラミック等を用いて停止時のバーナーを保護する構造を有し、バーナーに対する炉内静圧の逆流も同時に防止する構造とし、主燃焼バーナー停止時においても炉壁から円周方向に送風される空気の導入によりバーナー無しで炉内に可燃焼物を挿入することで炉の温度は一定条件まで上げることができる。このとき酸化を急激に促進し、スポット的に温度を上昇させるため燃焼促進剤を上部投入口又は予め設けた複数、単数の促進剤を自動挿入口より連続挿入及び間欠挿入し、炉内の主燃焼溶融エリア部分周辺の温度を高温に上げ、本発明でいうアスベストの溶融は1350度以上と溶融時間の問題があるので促進剤、主燃焼用バーナー、燃焼助材(木片、燃焼可能な廃ゴミ等も共用燃焼可能)の様なことをすることにより、より強固で安全な溶融物にすることができる。又燃焼促進剤を主燃部に投与、連続、断続、間欠何れかの方法で行うことにより溶融前の状態である石綿状の状態から瞬時に固形状態に促進されるため、外部に排ガスと一緒に飛散することが無い。これらの条件下で連続処理又はバッチ処理が可能なように炉壁には冷却余熱を兼ねた空気を多段式ターボファン、シロッコファン、セミシロッコファン、ターボファン等の送風機何れかを付け、炉の外壁と燃焼室の中間に過給帯等の空洞を設け、その空洞に上記に記載した様々な送風機を選択し適切な物を使用する。炉の内壁側に空気の気流方向が一定になり回転するよう空洞部の静圧を保ちながら、炉内に挿入できるよう角度をつけた穴を内壁に均等に開け、主処理室周囲の温度上昇を抑え、尚かつ渦巻き状に挿入することにより可燃物つまり(酸化されるもの)を内部に挿入口より投入することにより可燃物は中心部渦巻き帯に巻き込まれ、そこに燃焼促進剤等を挿入することで急激な温度上昇を起こし、殆どの可燃物がセラミック状になる溶融炉であり、本発明は燃焼促進剤を使用し、渦巻き現象で主燃焼部分、渦巻きの中心部の温度を上げられることが大きな発明であり、これにより今まで燃焼溶融出来なかった物までが出来るようになったことで医療用廃棄物など高温瞬間燃焼の必要な廃棄物が処理できるようになった。上記で排熱の熱交換を表記致していますが同じような方法で水等を媒体として通過させることで排熱利用が可能になる。その一端には燃焼促進剤、ニトロ系物質を協用するため炉の制作が安価で炉を保護するために全ての高熱部分に炉内で必要な空気の挿入を行うがため、必要部分以外の温度上昇が少なく排熱温度は高くなるが故、その排熱を活用し、円筒状渦巻き二次空気層の部分に様々な送風機の中でもそれらに有効な静圧の取れる送風機を選択し、静圧送風ダクト又は単数、複数の熱交換用耐熱耐蝕パイプの中を通し、本原理の円筒状炉壁面内部にある空洞化静圧体に加圧して送り込み、炉内部二次空気渦巻き状流域に熱空気層として回収加熱補助することもある。熱エネルギーや回転エネルギーに変えることが小型でも可能になり、本発明の装置に直接取り付けるか、本発明の装置から取り出した高圧蒸気又は温水等を使って発電用タービンを直接駆動するか低温媒体を加温し間接的に駆動することもある。何れにしても本発明は小型簡易溶融省エネ装置として使用はもちろん医療廃棄物などの高温溶融処理を必要とする物も処理物の中に入り、高温燃焼処理より二次公害等を出さないということも必態の事項である。The present invention has been widely used as a fireproof covering material for buildings, structures, etc. from the past several decades. There is currently no complete deciding factor because it is very expensive to dispose of. Therefore, the small melt solidification system invented this time first forms a cylindrical processing chamber (the cylindrical shape is a shape that is used to concentrate all of the radiant heat at the center of the cylindrical shape, and the material used for it is reflective efficiency) (In some cases, a process that emits far-infrared rays is also used.) Applying static pressure to the circumference from the circumference of the treatment chamber with air, the wall surface from the blowout port provided around the circumference The air is formed in the direction of rotation to protect the wall from the high-temperature combustion part in the center and oxygen combines with the oxide in the air blown into the wall to form water, carbon dioxide, air Protects refractories or refractory metals from oxidation from the high temperature zone of the combustion part as described above, and this phenomenon occurs continuously by continuously injecting the outside air, and the air that is excessively filled inside is similar to the above. A water pool is installed at the bottom of the exhaust port. , And its water pool static pressure, by a method accompanied the branched air perforated pipe and then the blower tube, sometimes air blow than water pool bottom. A structure that prevents micromicron dust from scattering into the atmosphere and flows from there to the flue gas combustion chamber, through which it is discharged from the exhaust port, a heat-resistant and corrosion-resistant steel pipe installed in the form of a honeycomb in the center of the exhaust port, or stainless steel System heat-resistant and corrosion-resistant steel pipes and ceramic pipes, etc., and the exhaust heat passes through the gaps to heat the pipes for heat exchange, and the outside air (atmosphere) required for main combustion is blowered while being heated, Uses a turbo blower, sirocco fan, multistage static pressure fan, axial fan, etc., and automatically adjusts the air flow static pressure by using an inverter etc. according to the combustion situation in the main combustion chamber installed inside it , Raise the internal main combustion chamber to the melting temperature (that is, the melting temperature of asbestos), insert an appropriate amount of combustion accelerator there, and suddenly raise the temperature of each external flame part in the center with the combustion accelerator. Best of is intended to solidify the molten instantly. The solidified asbestos molten stone is deposited as molten stone on the refractory tray provided at the lower part of the main combustion chamber in the furnace, and the lower refractory tray is discharged outside as a safe molten stone with a regular discharge gradient. Is done. A main combustion burner and a petroleum-based gas system were installed at an intermediate position between the heat-resistant tray and the internal air rotating layer, and a part of the exhaust port located between the fire-proof tray and the hearth was adjusted to the rotating airflow. The burner is set so that the combustion frame extends in the direction, and the top cover automatically slides at the tip of the burner while the main combustion burner is burning to protect the burner, and slides when the burner is stopped. It has a structure that protects the burner at the time of shutdown using heat-resistant and corrosion-resistant steel or main oxidation-resistant steel and super refractory bricks, ceramics, etc., and also prevents reverse flow of static pressure in the furnace against the burner at the same time, and main combustion Even when the burner is stopped, the temperature of the furnace can be raised to a certain condition by inserting combustible material into the furnace without a burner by introducing air blown in the circumferential direction from the furnace wall. At this time, in order to rapidly promote oxidation and increase the temperature in a spot manner, a combustion accelerator is inserted continuously or intermittently through an upper insertion port or a plurality or one of the previously provided accelerators from an automatic insertion port. The temperature around the combustion melting area is raised to a high temperature, and asbestos melting in the present invention has a problem of melting time of 1350 ° C. or more, so an accelerator, a main combustion burner, a combustion aid (wood pieces, combustible waste garbage) Etc. can be made into a stronger and safer melt. In addition, the combustion accelerator is administered to the main combustion part by any of the continuous, intermittent, and intermittent methods, and the solid state is instantly promoted from the asbestos-like state before melting. Will not be scattered. In order to enable continuous processing or batch processing under these conditions, air that also serves as cooling residual heat is attached to the furnace wall with a blower such as a multistage turbofan, sirocco fan, semi-sirocco fan, or turbofan. A cavity such as a supercharging zone is provided between the outer wall and the combustion chamber, and various blowers described above are selected in the cavity to use an appropriate one. While maintaining the static pressure of the cavity so that the air flow direction is constant and rotates on the inner wall side of the furnace, holes that are angled so that they can be inserted into the furnace are evenly formed on the inner wall, and the temperature around the main processing chamber rises By inserting a combustible material, that is, (oxidized) into the inside through the insertion port, the combustible material is caught in the central spiral band, and a combustion accelerator or the like is inserted there. This is a melting furnace in which most of the combustibles become ceramic-like, causing a rapid temperature rise, and the present invention uses a combustion accelerator and can raise the temperature of the main combustion part and the center of the swirl by the swirl phenomenon This is a big invention, and it has become possible to process even those that could not be burned and melted so far, and it has become possible to treat waste that requires high-temperature instantaneous combustion, such as medical waste. Although the heat exchange of waste heat is described above, waste heat can be used by passing water as a medium in the same way. At one end, combustion accelerators and nitro-based substances are used together, making the furnace cheap, and in order to protect the furnace, all the hot parts are inserted with the necessary air inside the furnace. Since the exhaust heat temperature rises with little temperature rise, the exhaust heat is utilized, and a blower that can take effective static pressure is selected for various parts of the cylindrical spiral secondary air layer, and the static pressure feed Passes through a wind duct or one or more heat-resistant and corrosion-resistant pipes for heat exchange, pressurizes and feeds into the hollow static pressure body inside the cylindrical furnace wall of this principle, and hot air enters the secondary air spiral flow area inside the furnace The layer may be recovered and heated as a support. It is possible to change to heat energy and rotational energy even in a small size, and it can be directly attached to the apparatus of the present invention, or the turbine for power generation can be directly driven using high-pressure steam or hot water extracted from the apparatus of the present invention, or a low-temperature medium can be used. It may be heated and indirectly driven. In any case, the present invention can be used as a small and simple melting energy-saving device, as well as medical waste and other items that require high-temperature melting treatment also enter the treated material and do not cause secondary pollution from high-temperature combustion treatment. Is an indispensable matter.

従来、アスベストについては安全で使いやすい物とされ、難燃性に優れ、それらの特徴を生かし、火災などの発生時被害を最小限度に食い止めるため使用されていたが、現在ではガンなどの発病の根源の一つであることが実証され、その使用も出来なくなったのが必然的な物であり又それらの製造等に従事する人たちにとっても健康を害することが判明し、使用と製造が法律で規制され、今まで大量に構築物や建築物に生かされてきた物の撤去と廃棄が社会問題となっている。これらの廃棄に当たってはまだこれといった方法が見つけられていない。中間的な方法としてはプラスチック容器に封じ込め土中に埋設するぐらいの方法が有力候補として考えられているが問題点が多すぎて許可されていない。医療廃棄物についても高温の溶融炉のあるところ又は電炉、高炉等で補助的に処理されているのが現状で人が物に詰めて移動するには限界があり、もし万が一、中間で汚染されたら大変なことになるのが現状である。Conventionally, asbestos has been considered safe and easy to use, has excellent flame retardancy, and has been used to minimize damage at the time of occurrence such as fire, taking advantage of these characteristics. It has been proved that it is one of the roots, it is inevitable that its use can no longer be used, and it has been found that it is harmful to the health of those who are engaged in the manufacture of such products. The removal and disposal of objects that have been regulated in Japan and have been used in large numbers of structures and buildings until now has become a social issue. No such method has yet been found for disposal. As an intermediate method, a method of embedding in a plastic container and being buried in soil is considered as a promising candidate, but there are too many problems to allow. As for medical waste, there is a limit to how humans can pack and move in places where high temperature melting furnaces or electric furnaces, blast furnaces, etc. are supplementary, and in the unlikely event that they are contaminated in the middle. The current situation will be tough.

発明が解決しょうとする課題Problems to be solved by the invention

本発明が今社会問題になっているアスベストの簡易的完全溶融処理(半セラミック的物質、無機無公害)物質に安価で持ち運び等も可能な溶融処理装置である故に本原理は基本構造としては一般的に炉全体の蓄熱量により、カロリーの投入量により決まってくるが、この場合コストが非常に高い物になり使用可能な温度に上昇するまで時間がかかりすぎて燃料の投入量が多い割に高い温度を形成するのが不可能であった。又医療廃棄物等パッキングして搬送するという大変危険な行為を社会的に行っているのが現状で発生場所で直ちに処理できる方法がない。これらの点から考慮すると簡易的な溶融炉が無いのが現状である。又簡易的に行うことが溶融という状況下から非常に高温が要求され、溶融が難しい。又大電力を必要とし、結果的には二酸化炭素の排出量を増加するのが現状でありこの現状を如何にして解消するかが課題になっている。又エネルギー問題で高温燃焼を行った際に排出される排熱の利用方法等が問題になっている。これらを有効的に活用するにはどうすればよいかも課題となる。今までの焼却炉方式では灰分が多く、物によっては重金属等の混じった灰分となっている。特にアスベストのように無機物質で針状の微細粒子についてはその処理の方法如何では大変多くの二次的汚染を招く恐れがありこれらを処理の場所と処理の方法によって解消しようとしている物であり、それに加えて一般雑廃棄物についても混合処理等を含む処理を可能にするため、それらの課題を捕らえたものである。This principle is generally used as a basic structure because it is a low-priced and easy-to-carry melt processing device for asbestos, which is a simple social melting problem (semi-ceramic material, inorganic pollution-free). In general, the amount of calorie input depends on the amount of heat stored in the entire furnace, but in this case the cost is very high and it takes too much time to rise to a usable temperature, so the amount of fuel input is large. It was impossible to form a high temperature. In addition, there is no method that can be immediately processed at the place where it is socially performing a very dangerous act of packing and transporting medical waste. Considering these points, there is no simple melting furnace at present. Also, it is difficult to melt easily because a very high temperature is required from the situation of melting. In addition, a large amount of electric power is required, and as a result, the amount of carbon dioxide emission is increased, and there is a problem of how to solve this situation. In addition, there is a problem of how to use exhaust heat discharged when high-temperature combustion is performed due to energy problems. How to use these effectively is also an issue. The conventional incinerator system has a lot of ash, and depending on the object, it is ash with a mixture of heavy metals. Especially for fine particles of needle-like inorganic substances such as asbestos, there is a risk of causing a great deal of secondary contamination depending on the treatment method. In addition, in order to make it possible for general wastes to be processed including mixing, etc., these problems are captured.

課題を解決するための手段Means for solving the problem

本発明は従来、難しかったアスベスト等の溶融及び医療用廃棄物、一般廃棄物の高密度、高温燃焼簡易方式を使った方法でその解決方法は先ず炉壁、炉内の均一燃焼方式から円筒渦巻き燃焼方式にすることにより、熱と空気から吸気した酸素を中心部の必要ポイントエリアに集中して加熱し、それに燃焼促進剤即ちニトロ系物質を安全範囲で相乗し、更に完全酸化と燃焼促進を図り内部に付着しやすいスス等の付着を抑制し、炉内クリーニングも兼ねたものであり、炉体本体と燃焼室壁面に隙間及び空洞を設け、それに対してブロアー、多段、単段、シロッコファン等で静圧過給し、円筒炉内で一方方向に空気を導く穴を開け、内部炉壁に対して冷却するような形をとり、燃焼炉内部で渦巻きを起こし、渦巻きの中心部に主バーナーを設置し、渦巻き内の雰囲気のみ部分的に高温にし、更にそれに対してニトロ系燃焼促進剤を挿入することにより、燃焼速度が速まり又熱が中心状に集中するため中心トレイの真上中心部を部分的に高温エリアとして作り出す。その部分に対して主燃焼バーナーを固定し、バーナー運転時にはバーナーダンパーが開くような構造にし、停止時にはバーナーダンパーが閉じるように構築することでバーナーに対しての逆火することを防止し、バーナーの損傷を防ぐべき構造とし、下部耐熱トレイは連続処理の場合、定期的に内部の燃焼溶融物を排出するような構造にし、断続処理の場合、内部の燃焼溶融物を上部の投入口より取り出す簡易構造とする。The present invention is a method using a high density, high-temperature combustion simple method of melting asbestos and the like, medical waste, general waste, which has been difficult in the past, and the solution is first from the furnace wall, the uniform combustion method in the furnace to the cylindrical swirl By adopting a combustion method, heat and oxygen drawn from air are concentrated and heated in the necessary point area in the center, and combustion accelerators, that is, nitro substances, are combined in a safe range, and further complete oxidation and combustion promotion are achieved. Suppresses adhesion of soot that tends to adhere to the inside of the plan, and also serves as cleaning in the furnace. A gap and a cavity are provided in the furnace body and combustion chamber wall, and a blower, multistage, single stage, sirocco fan Etc., form a hole that guides air in one direction in the cylindrical furnace, cools the inner furnace wall, creates a vortex inside the combustion furnace, Install a burner Only the atmosphere in the swirl is partially heated, and a nitro-based combustion accelerator is inserted into the swirl to increase the combustion speed and concentrate the heat centrally. Create as a high temperature area. The main combustion burner is fixed to the part, and the burner damper is opened when the burner is operated, and the burner damper is closed when the burner is stopped. The lower heat-resistant tray is structured to periodically discharge the internal combustion melt in the case of continuous processing, and the internal combustion melt is taken out from the upper inlet in the case of intermittent processing. A simple structure is adopted.

発明の効果The invention's effect

本発明は今大変社会問題となっているアスベスト処理又は今後大きな社会問題を起こすと見込まれる医療廃棄物及び雑廃棄物等の遠距離輸送一括処理に対して、廃棄物が見込まれる場所の近くに配置或いは車両搭載し、移動又は更に小型化し医療現場で直接使用が可能な大きさにすることが可能であり、特にアスベスト処理ではアスベストのミクロン針状ダストが飛散するということで今までこれといった処理方法が確立できなかったが、雰囲気でオブラードし、渦巻き状接触燃焼により飛散の防止を可能にした物であり同じように医療廃棄物若しくは雑廃棄物等を同時に溶融、酸化無機物にすることができ、炉本体の構造も極めて簡易的な構造で炉全体の温度上昇を活用せず、エリア燃焼、集中輻射、輻射熱等を一カ所に集中するため、熱効率が極めて高く、それに含めて燃焼助材(ニトロ系燃焼促進剤)の協用により今まで考えられなかった物まで急激に酸化、溶融を起こし、大気中に有害なダスト等を排出しないような複合処理等も同時に可能になり、排気筒手前に熱交換機を付けることで極めて効率の良い燃焼条件を兼ね備え、回収した熱はエネルギー源としてあらゆる用途に活用でき、二次公害の無い方法と言え、又あらゆる廃棄物を急速につまり瞬時に近く燃焼、溶融できることがクリーンな環境を作る上でとても重要なことである。又通常の回転燃焼と違い空気を強制的に送り込み、炉内で回転させながら中心部は円周率が低く、非処理材が渦巻きの中央部で静かに回転しながら燃焼溶融するため、排気が極めて清浄化されたもので、しかも燃焼促進剤をしようするため満遍なく攪拌され、中心部下部に溶融されたものは固形化して重量が増すため落下し、回収しやすくなる等の原理を作り得た物である。The present invention is close to a place where waste is expected for asbestos treatment, which is a very social problem, or for long-distance transportation batch processing such as medical waste and miscellaneous waste that is expected to cause a large social problem in the future. It can be placed or mounted on a vehicle, moved or further miniaturized to a size that can be used directly in the medical field. Especially in asbestos processing, asbestos micron needle dust is scattered, so far this processing Although the method could not be established, it was obraded in the atmosphere, and it was possible to prevent scattering by spiral contact combustion. Similarly, medical waste or miscellaneous waste can be simultaneously melted and made into an oxidized inorganic substance. The structure of the furnace body is very simple and does not use the temperature rise of the whole furnace, but concentrates area combustion, concentrated radiation, radiant heat, etc. in one place. The rate is extremely high, and in addition to this, the use of combustion aids (nitro-based combustion accelerators) causes sudden oxidation and melting of objects that could not be considered before, and does not emit harmful dust into the atmosphere. Combined processing is possible at the same time, and by attaching a heat exchanger in front of the exhaust stack, it has extremely efficient combustion conditions, and the recovered heat can be used as an energy source for all purposes, and it can be said that there is no secondary pollution, Also, it is very important to create a clean environment that any waste can be burned and melted quickly, that is, instantly. Also, unlike normal rotary combustion, air is forcibly sent and rotated in the furnace, the center part has a low circularity, and the non-treated material burns and melts while rotating gently in the center of the spiral, so the exhaust is It was extremely purified, and evenly stirred to use as a combustion accelerator, and melted at the lower part of the center solidified and increased its weight, so it could fall down and make it easier to recover. It is a thing.

本発明はまさに現在社会問題として問題となっているアスベストの処理が安全尚かつスムーズに出来るよう原理を構築した物でその一つにはアスベスト即ちボロベスト又は石綿ともいう人工的に作られた耐火断熱性の良い物ですが、現在医学的に発ガン性物質として又他の病気の誘因性を持つもので大変生命体にとっては大変危険な物と実証されてきました。これらの問題を解決するには、現在様々な試みをされていますが、皆十分と言えません。そこで本発明を使用することにおいて簡易的に場所を移動しながら本件の根源となる近くに設置し、処理を可能とした物でこの処理は高温瞬間溶融と一般廃棄物等を同時に処理できるよう、空気層の筒の中側で燃焼促進剤を協用し、範囲高温で完全に溶融し、固形物として安全な状態で処理後に廃棄でき、その廃棄の方法は多種多様であるが、例えばコンクリートの骨材等に使えるなど有効リサイクルが可能になるものである。医療廃棄物についてはこれには当てはまらないが、完全にセラミック化するため、最終処分と定めることが出来ることである。何れにしても殆どの物が溶融、グラスロック化できる。更に排出される熱エネルギーを有効に活用して省エネルギーを全体像で測ることも可能であり、焚き込みと立ち上がりが早く、万が一、化成品等が混じっていても有害なダイオキシン等の発生が無く、環境にも適している。The present invention is a construction of the principle so that the treatment of asbestos, which is currently a problem as a social problem, can be performed safely and smoothly, one of which is artificially made fireproof insulation called asbestos, ie borobest or asbestos. Although it is a good substance, it has been proven to be a very dangerous thing for living organisms because it is medically carcinogenic and has the potential to cause other diseases. Various attempts are currently being made to solve these problems, but not all are sufficient. Therefore, by using the present invention, it is installed close to the root of the case while moving the place easily, so that this treatment can be processed simultaneously with high temperature instantaneous melting and general waste, etc. Combustion promoters are used inside the cylinder of the air layer, melted completely at high temperatures, and can be disposed of in a safe state as solids. It can be effectively recycled, such as being used for aggregates. This is not the case for medical waste, but it can be defined as final disposal because it is completely ceramicized. In any case, almost everything can be melted and made into a glass lock. Furthermore, it is possible to measure the overall energy savings by effectively using the heat energy that is discharged, so that the start-up and start-up are fast, and there is no generation of harmful dioxins even if chemical products are mixed. Also suitable for the environment.

溶融燃焼炉、横から見た断面図、本発明の原理、加圧式多段ブロアーで大気を本発明の二次空気、本図中に記載した静圧、加圧空洞層に加圧した、或いは静圧をかけた状態で、本図、加圧空気噴射口から炉内に二次空気(又は主燃焼空気)となりうる空気の吹き込みを炉内に効率よく、行うため設置したもので、この空気は炉内壁面が高温に耐えられるよう、吹き込み角度は円周方向、壁面に沿った方向に吹き込む事を図面3にその流れを標記したものであり、炉内に導かれる燃焼助剤噴射ノズル、及び酸素注入用ノズルを設け、渦巻き状の中央部を高温に上げ、溶融を目的とした原理を例として記載したものである。Melting combustion furnace, cross-sectional view from the side, principle of the present invention, pressurized multistage blower is used to pressurize the atmosphere into the secondary air of the present invention, static pressure described in the figure, pressurized cavity layer, or static In the state where pressure is applied, this figure is installed to efficiently blow air into the furnace from the pressurized air injection port into the furnace, which can become secondary air (or main combustion air). The flow angle in FIG. 3 indicates that the blowing angle is blown in the circumferential direction and the direction along the wall surface so that the inner wall surface can withstand high temperatures, and a combustion auxiliary agent injection nozzle guided into the furnace, and An oxygen injection nozzle is provided, and the spiral central portion is raised to a high temperature, and the principle for melting is described as an example. 本発明の原理を本体の例を記載した時点で、本体のあらましの構造、等が排気筒付近で分かるよう簡単に、主になる部分を後ろから見た図として標記、明細を記載したものである。At the time when the principle of the present invention is described as an example of the main body, the structure of the main body, etc. are easily described so that the main part can be seen in the vicinity of the exhaust stack, and the main part is shown as a view from the back, with the description and description is there. 本原理の燃焼室、及びその空気、或いはガス類の流れを分かりやすく、矢印で表記したもので加圧空気挿入口とは、図1の横から見た断面図に標記されているものであり、主燃焼バーナーの高温時の保護用ダンパーの位置などを明確に記載し、又、二次空気の静圧、加圧噴射方向などに対しても矢印で表したものである。The combustion chamber of this principle and its air or gas flow are easy to understand and are indicated by arrows, and the pressurized air insertion port is shown in the sectional view seen from the side of FIG. The position of the protection damper at high temperature of the main combustion burner is clearly described, and the static pressure of the secondary air, the pressurized injection direction, and the like are also indicated by arrows.

符号の説明Explanation of symbols

▲1▼.主燃焼バーナーブロアー及びバーナー
▲2▼.加圧多段ブロアー
▲3▼.高温熱交換機
▲4▼.助燃剤噴射ノズル
▲5▼.セラミック酸素注入用ノズル
▲6▼.加圧空気噴射口
▲7▼.加圧空気空洞層
(1). Main combustion burner blower and burner (2). Pressurized multistage blower (3). High temperature heat exchanger (4). Auxiliary combustion agent injection nozzle (5). Ceramic oxygen injection nozzle (6). Pressurized air injection port (7). Pressurized air cavity layer

Claims (6)

助燃剤としてニトロ系燃焼促進剤を使用すると共に主燃焼バーナーを保護するためバーナー停止時、耐熱耐蝕ダンパー等を設置するなどの方法を用い、これらを効率的に行うため圧縮酸素と酸素分離器等から発せられる酸素を過剰に供給することもあること。In order to protect the main combustion burner while using a nitro-based combustion accelerator as a combustor, use a method such as installing a heat-resistant, corrosion-resistant damper, etc. when the burner is stopped. Oxygen emitted from the water may be supplied in excess. 排気熱及び炉外部壁熱を回収し、ボイラー暖房等の熱源、発電及び温水を得て、他に転嫁すること。Collect exhaust heat and furnace wall heat, obtain heat sources such as boiler heating, power generation and hot water, and pass on to others. 炉内に空気の渦巻きベルトを形成し、炉壁を保護すると共に炉内に渦巻きを起こし、燃焼物を攪拌すること。Form a swirl belt of air in the furnace to protect the furnace wall and create a swirl in the furnace to stir the combustion products. 送風機にインバーター等を使用し、炉内空気層ベルトの大きさと渦巻きの早さ、空気の量を調整すること。Use an inverter for the blower, and adjust the size of the air layer belt in the furnace, the speed of the spiral, and the amount of air. 本発明の装置にアスベスト又は医療廃棄物及び一般可燃ゴミなどの有害物質を混合燃焼し、溶融固形化すること。To burn and solidify asbestos or medical waste and harmful substances such as general combustible waste in the apparatus of the present invention. 底部排気ゲート下に水プールを設け、ダストの飛散を防止すると共にミクロンダスト回収用水プール及びウォータースクリーン等を形成し、その器には循環方式を使用し、排熱の回収をするよう構造を取り入れると共に更にその後に排ガスが収縮する際、発生する微小ダストについては静電集塵システム等を活用し、大気汚染を防ぐこと。A water pool is provided under the bottom exhaust gate to prevent dust scattering and to form a micron dust collection water pool and water screen, etc., using a circulation system in the vessel and incorporating a structure to collect waste heat. At the same time, when the exhaust gas shrinks, use an electrostatic dust collection system etc. to prevent air pollution for the generated fine dust.
JP2006154011A 2006-05-02 2006-05-02 Compact waste mixing, melting and solidifying device for asbestos, medical waste, general waste and the like Pending JP2008196710A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2006154011A JP2008196710A (en) 2006-05-02 2006-05-02 Compact waste mixing, melting and solidifying device for asbestos, medical waste, general waste and the like

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2006154011A JP2008196710A (en) 2006-05-02 2006-05-02 Compact waste mixing, melting and solidifying device for asbestos, medical waste, general waste and the like

Publications (1)

Publication Number Publication Date
JP2008196710A true JP2008196710A (en) 2008-08-28

Family

ID=39755822

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2006154011A Pending JP2008196710A (en) 2006-05-02 2006-05-02 Compact waste mixing, melting and solidifying device for asbestos, medical waste, general waste and the like

Country Status (1)

Country Link
JP (1) JP2008196710A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112775164A (en) * 2021-03-17 2021-05-11 广东烁鼎环境科技有限公司 Wide temperature range melting prediction control system and control method for waste incineration fly ash

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112775164A (en) * 2021-03-17 2021-05-11 广东烁鼎环境科技有限公司 Wide temperature range melting prediction control system and control method for waste incineration fly ash
CN112775164B (en) * 2021-03-17 2024-01-09 广东烁鼎环境科技有限公司 System and method for predicting and controlling wide-temperature-section melting of waste incineration fly ash

Similar Documents

Publication Publication Date Title
CN108730990A (en) Utilize the hybrid burner of the thermal decomposition of water and burning air
TW201702529A (en) Smokeless incinerator and system using the same
CN107543155A (en) A kind of auxiliary burner and standby firing system and control method
JP2008196710A (en) Compact waste mixing, melting and solidifying device for asbestos, medical waste, general waste and the like
EP3106529B1 (en) Method and plant of treating and smelting metals
KR100413188B1 (en) Burner for inflammable pulverized fuel
JP4822849B2 (en) Exhaust gas treatment equipment for ash melting furnace
JP3460605B2 (en) Waste incineration and heat treatment furnace
TW473605B (en) Waste treatment apparatus
CN207514928U (en) A kind of waste incinerator of calorific value wide adaptation range adjusts burner hearth radiation appliance
JP3844327B2 (en) Method and apparatus for processing radioactive graphite
JP2010139229A (en) Energy saving type spiral combustion furnace for medical waste and other waste using autonomous thermal energy, incinerator high temperature high heat shortened combustion ultimate disposal combustion furnace, and device for the same
JP2008275180A (en) Waste melting treatment method and equipment
US7678164B2 (en) Ash handling and treatment in solid fuel burners
JP2002089813A (en) Waste gas processing method for ash melting furnace and its apparatus
JP3460604B2 (en) Waste incineration melting furnace
JP2004077013A (en) Operation method of waste incinerator, and waste incinerator
JPH11351530A (en) Incinerator system
JP3154230U (en) Continuous heat treatment and clean combustion system for water-containing oil-contaminated soil incinerated ash.
JP3744401B2 (en) Heat treatment method and heat treatment apparatus
CN103939922B (en) Wet-type short flue high-pressure air inducing incinerator
JP2004163009A (en) Operation method of waste incineration system and waste incineration system
KR20230035537A (en) Movable and continuous all in one incineration system
JP2004181323A (en) Operation method for ash treatment system and ash treatment system
AU2002218878B2 (en) Ash handling and treatment in solid fuel burners