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JP4058910B2 - How to dispose of combustible waste - Google Patents
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JP4058910B2 - How to dispose of combustible waste - Google Patents

How to dispose of combustible waste Download PDF

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Publication number
JP4058910B2
JP4058910B2 JP2001052597A JP2001052597A JP4058910B2 JP 4058910 B2 JP4058910 B2 JP 4058910B2 JP 2001052597 A JP2001052597 A JP 2001052597A JP 2001052597 A JP2001052597 A JP 2001052597A JP 4058910 B2 JP4058910 B2 JP 4058910B2
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Prior art keywords
combustible waste
bag
waste
crushed
kiln
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JP2002257310A (en
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良一 滝口
佳秋 小松
正康 山崎
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Mitsubishi Materials Corp
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Mitsubishi Materials Corp
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    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B7/00Hydraulic cements
    • C04B7/36Manufacture of hydraulic cements in general
    • C04B7/43Heat treatment, e.g. precalcining, burning, melting; Cooling
    • C04B7/44Burning; Melting
    • C04B7/4407Treatment or selection of the fuel therefor, e.g. use of hazardous waste as secondary fuel ; Use of particular energy sources, e.g. waste hot gases from other processes
    • C04B7/4423Waste or refuse used as fuel
    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B7/00Hydraulic cements
    • C04B7/36Manufacture of hydraulic cements in general
    • C04B7/43Heat treatment, e.g. precalcining, burning, melting; Cooling
    • C04B7/44Burning; Melting
    • C04B7/4407Treatment or selection of the fuel therefor, e.g. use of hazardous waste as secondary fuel ; Use of particular energy sources, e.g. waste hot gases from other processes
    • C04B7/4438Treatment or selection of the fuel therefor, e.g. use of hazardous waste as secondary fuel ; Use of particular energy sources, e.g. waste hot gases from other processes the fuel being introduced directly into the rotary kiln
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/30Fuel from waste, e.g. synthetic alcohol or diesel
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P40/00Technologies relating to the processing of minerals
    • Y02P40/10Production of cement, e.g. improving or optimising the production methods; Cement grinding
    • Y02P40/125Fuels from renewable energy sources, e.g. waste or biomass

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Ceramic Engineering (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Materials Engineering (AREA)
  • Structural Engineering (AREA)
  • Organic Chemistry (AREA)
  • Curing Cements, Concrete, And Artificial Stone (AREA)
  • Incineration Of Waste (AREA)
  • Processing Of Solid Wastes (AREA)

Description

【0001】
【発明の属する技術分野】
本発明は、例えば、磁気テープ等のテープ類、シート状やフィルム状のプラスチック、あるいは、ラミネート古紙からパルプを回収した後のラミネートフィルム等の嵩張り度合いの大きな可燃性廃棄物を、燃焼炉まで輸送して投入しやすい形態に減容化するとともに、その減容化したものをセメント焼成工程にて有効利用しながら処分する方法に関する。
【0002】
【従来の技術】
産業廃棄物の発生量は年々増加の一途をたどっている。その処理方法としては埋め立て処理、焼却処理等が知られている。しかし、埋め立て処理場の確保が難しくなってきていることから、焼却処理が注目を浴びてきている。かかる産業廃棄物の中でも廃プラスチック等の可燃性廃棄物は、焼却によって十分な熱量を発生するため、その燃焼によって生じる熱量を有効に利用するべく、各種の燃焼炉の燃料として使用されつつある。
【0003】
例えば、廃プラスチック等の可燃性廃棄物を燃料として利用する方法として、特開平7−277788号公報等に開示されるように、セメント焼成設備のロータリーキルン内に投入して燃焼させることで、主燃料とし使用している微粉炭の使用量を削減する技術が以前より知られている。
【0004】
【発明が解決しようとする課題】
しかし、テープ、フィルム、シート等の形態で廃棄されるプラスチック廃材、あるいは、シュレッダーで破砕された事務用箋などの嵩張り度合いの非常に大きな可燃性廃棄物は、そのままの形態では、セメント製造用のロータリーキルンや仮焼炉に供給するに当たって種々の問題を発生する。即ち、これらの廃材は、貯蔵、輸送、計量等のハンドリング操作が極めて困難である。例えば、貯蔵する場合は、嵩比重が小さいために広大な貯蔵スペースが必要となる。また、車で輸送する場合は、嵩比重が小さいために1車当たりの輸送量が極端に少なく、輸送効率が著しく悪い上、飛散しやすいためにその対策が必要である。更に、ベルトコンベヤ等の輸送機械で輸送する場合においても、飛散やこぼれ、詰まりなどが発生し易い。また、燃焼炉に投入した際に、投入したものが舞い上がる等の問題もある。
【0005】
そこで、これらの可燃性廃棄物をバインダーの添加により加熱圧縮して減容固化する方法が考えられている。しかし、洗浄工程を経由して送られてくる可燃性廃棄物には水分が付着していることが多くあり、そのような場合、減容化のために加熱温度を上げていくと、水蒸気爆発の危険性が出てくる。そのため、無条件に従来の減容固化法を採用することができないという問題があった。また、従来の減容固化方法は、加熱圧縮のための設備が必要であり、コストがかかる上、工程が複雑化する問題もあった。
【0006】
本発明は、上記事情を考慮し、嵩張り度合いの大きな磁気テープ等の可燃性廃棄物をハンドリングしやすい形態に簡単且つ安全に減容化して処分する方法を提供することを目的とする。
【0007】
【課題を解決するための手段】
請求項1の発明の可燃性廃棄物の処分方法は、圧縮可能で嵩張り度合いの大きな可燃性廃棄物を、気密性を保持し得る袋に収容して、該袋内の空気を排気することで、圧縮してマット状に形成し、該マット状に形成した袋入りの可燃性廃棄物を、袋のまま破砕機にかけて破砕し、得られた破砕品を、それより硬質の可燃性廃棄物の破砕品と混合した上で、セメント焼成工程に補助燃料として投入することを特徴としている。
【0008】
このように、減圧により圧縮して袋ごとマット状に形成することで、貯蔵したり車で輸送したりする場合に、多数枚を積み重ねることができるようになる。従って、大量に貯蔵したり積載したりすることができ、貯蔵効率や輸送効率が向上する。また、袋に入っているので、計量等の際のハンドリング操作が極めて容易にできるようになると共に、飛散対策も必要なくなる。また、袋に入れた状態のまま燃焼炉に投入することもできるため、飛散やこぼれの心配や舞い上がりの心配もなくなる。さらに、家庭用掃除機や真空ポンプを利用して簡単に安全にコストをかけずに減容化することができるので、従来の加熱圧縮式の減容化方法と比べて実現が容易である。
【0013】
そして、セメント焼成工程にマット状に減容化した可燃性廃棄物を投入するに当たって、袋のまま破砕した上でセメント焼成工程に投入する方法を採用しているために、機械化処理しやすくなる。
また、嵩張り度合いの大きい可燃性廃棄物を、その嵩張る状態のまま破砕機にかけた場合には、硬質の可燃性廃棄物(硬質プラスチック等)を破砕する場合と比べて、破砕能力が1/3程度にダウンしてしまうが、真空吸引してマット状に圧縮減容化した状態で袋のまま破砕機にかけると、破砕能力の回復を図ることができる。例えば、家庭用掃除機で吸引した場合には、破砕能力のダウン量を2/3に軽減できるし、真空ポンプで吸引した場合には、硬質の可燃性廃棄物を破砕する場合と同等かそれ以上の破砕能力を確保することができる。つまり、圧縮のレベルに応じて破砕能力を高めることができる。
【0015】
さらに、硬質の可燃性廃棄物(例えばブロック状や厚物状のプラスチック廃材)の破砕品と混合した上で、セメント焼成工程に投入することにより、燃焼分布のバランスを良くすることが可能になる。
【0016】
請求項2の発明の可燃性廃棄物の処分方法は、請求項1において、袋のまま破砕機にかけて破砕した破砕品と、それより硬質の可燃性廃棄物の破砕品との混合物を、セメント焼成工程のロータリーキルンの窯前部から窯尻部方向へ向かって空気流に乗せてロータリーキルン内に吹き込むことを特徴としている。
【0017】
このようにロータリーキルンの窯前部から空気流に乗せて混合物を吹き込む場合、破砕品の嵩比重がばらけるので、ロータリーキルンの焼成領域の広い範囲に可燃性廃棄物を分散させながら到達させることができ、燃焼バランスを良くすることができる。
【0018】
請求項3の発明の可燃性廃棄物の処分方法は、請求項2において、袋のまま破砕機にかけて破砕した破砕品と、それより硬質の可燃性廃棄物の破砕品との混合物を、その混合比率を調整した上で、ロータリーキルンの窯前部から空気流に乗せて吹き込むことを特徴としている。
【0019】
このように2種の破砕品の混合比率を調整することで、燃焼分布の調整や到達距離の分散度合いを調整することができる。なお、嵩張り度合いの大きい可燃性廃棄物については、マット状に減容化した状態のまま破砕するので、計量精度が上がり、硬質の可燃性廃棄物と混合する場合の混合比率調整を精度良く行うことができるようになる。
【0020】
【発明の実施の形態】
以下、本発明の実施形態を図面に基づいて説明する。
図1は可燃性廃棄物の減容化から車への積載までの手順を示している。
本実施形態の減容化方法を実施する場合は、まず、ハンドリングしやすい大きさの気密の袋1を用意する。袋1は、三辺が封止され、一辺が開口した樹脂製の四角形のものが望ましく、開口部1aに気密チャックのついた市販品を利用することができる。
【0021】
図1(a)に示すように、この袋1の中に、磁気テープ等のテープ類、シート状やフィルム状のプラスチック、ラミネート古紙からパルプを回収した後のラミネートフィルム等の嵩張り度合いの大きな可燃性廃棄物2を大量に押し込む。そして、袋1に収容したら、(b)に示すように、袋1の開口部1aを絞りながらブロア3のパイプを隙間から入れて、内部の空気をブロア3で排気する。ここでブロア3としては、真空ポンプを使用するのが理想的だが、家庭用掃除機等を使用してもよい。このように真空吸引することにより、(c)に示すように、内部の可燃性廃棄物2が袋1ごと圧縮されて、マット状の可燃性廃棄物2Aが出来上がる。この段階で、厚さ10〜20cm程度のマット状になるようにするのが後工程において有利である。
【0022】
このように圧縮してマット状に形成した可燃性廃棄物2Aは、マット形態であるから多数枚を積み重ねることができ、(d)に示すように、1台の車5に多数枚を大量に積載することができる。従って、輸送効率が大幅に向上する。また、貯蔵する場合にも多数枚を積み重ねることができるから、貯蔵効率が大幅に向上する。また、袋に入っているので、計量等の際のハンドリング操作が極めて容易にできるようになると共に、飛散対策も必要なくなる。更に、袋に入った状態のまま燃焼炉に投入することもできるため、飛散やこぼれの心配や舞い上がる心配もなくなる。
【0023】
また、この場合の減容化方法は、袋1とブロア3を使用して減圧により圧縮するだけであり、加熱圧縮による減容固化法と違って加熱を要しないから、洗浄工程等において水分の付着した可燃性廃棄物2であっても、安全に減容化することができるし、大がかりな減容固化装置を使用せずにすむ。
【0024】
図2は、上記のように形成したマット状の可燃性廃棄物2Aを、セメント焼成工程に投入するまでの手順を示している。図において、10はセメント焼成工程のロータリーキルンであり、10Aは窯前部、10Bは窯尻部を示す。セメント原料G1は、窯尻部1Bからロータリーキルン10内に投入され、ロータリーキルン10内を移動する間に焼成されて、窯前部10Aのクーラー11からセメントクリンカG2として排出される。
【0025】
ロータリーキルン10の下流端である窯前部10Aには、石炭粉や重油等の主燃料ノズル12と、可燃性廃棄物の投入ノズル13とが設置されており、それぞれのノズル12、13から、主燃料と可燃性廃棄物の破砕品とがロータリーキルン10内に投入されるようになっている。ここで、可燃性廃棄物の破砕品は、窯前部10Aから窯尻部10B方向へ向かって空気流に乗せてロータリーキルン10内に吹き込まれることで、セメントクリンカ焼成用の補助燃料として利用される。
【0026】
この設備を用いてセメントクリンカを製造するに当たり、前記マット状に形成した可燃性廃棄物2Aを補助燃料としてロータリーキルン10内に投入する。その場合、投入するに当たっては、マット形状そのままの形態で投入する方法(A)や、マット状に形成した袋入りの可燃性廃棄物2Aを、袋のまま破砕機7にかけて破砕した上で投入する方法(B)のどちらか、あるいは、両方を採用することができる。
【0027】
(B)の方法で投入する場合は、破砕品2Cを、ロータリーキルン10の窯前部10Aのノズル13から空気流(エア)に載せてロータリーキルン10内に吹き込むことができるので、機械化処理しやすくなる。
【0028】
このようにマット状に減容化した可燃性廃棄物2Aを袋のまま補助燃料としてセメント焼成工程に投入することにより、ハンドリングの容易化を図りながら、廃棄物の有効利用を図ることができて、微粉炭等の主燃料を節約することができる。
【0029】
また、図3に示すように、マット状に形成した可燃性廃棄物2Aの破砕品2Cと、それよりも硬質のブロック状や厚物状などの硬質プラスチック(硬質の可燃性廃棄物)22Aの破砕品22Cとを混合した上で、ロータリーキルン10の窯前部10Aのノズル13から空気流に乗せてロータリーキルン10内に吹き込むようにしてもよい。
【0030】
その場合、可燃性廃棄物の投入系統に計量器6、26、破砕機7、27、混合機28を用意しておき、それぞれの可燃性廃棄物2A、22Aの混合比率を調整しながら混合した物を吹き込むようにする。
【0031】
このように硬質プラスチックの破砕品22Cと混合した上でマット状の可燃性廃棄物の破砕品2Cを、ロータリーキルン10内に吹き込むことにより、ロータリーキルン10の焼成領域の広い範囲に可燃性廃棄物を適度に分散させながら到達させることができ、燃焼分布のバランスを良くすることが可能になる。また、2種の破砕品2C、22Cの混合比率を調整することにより、燃焼分布の調整や到達距離の分散度合いを調整することができる。なお、硬質の可燃性廃棄物としてプラスチックを例示したが、特にそれに限定されるものではない。
【0032】
【発明の効果】
以上説明したように、請求項1の発明によれば、嵩張り度合いの大きな可燃性廃棄物を気密性を有する袋に入れて、いわゆる真空パック方式でマット状に圧縮減容化するので、貯蔵したり車で輸送したりする場合に、多数枚を積み重ねることができ、貯蔵効率や輸送効率の向上が図れる。また、袋に入っているので、計量等の際のハンドリング操作が極めて容易にできるようになり、飛散対策が必要なくなる。また、袋に入れた状態のまま燃焼炉に投入することができるため、飛散やこぼれの心配や舞い上がりの心配もなくなる。
【0035】
また、袋のまま破砕機にかけて破砕した破砕品を、それより硬質の可燃性廃棄物の破砕品と混合した上で、セメント焼成工程に補助燃料として投入するようにしているので、燃焼分布のバランスを良くすることが可能になる。
【0036】
請求項2の発明によれば、請求項1における2種の破砕品の混合物をロータリーキルンの窯前部から窯尻部方向へ向かって吹き込むようにしているので、ロータリーキルンの焼成領域の広い範囲に可燃性廃棄物を分散させながら到達させることができ、燃焼バランスを良くすることができる。
【0037】
請求項3の発明によれば、2種の破砕品の混合物をロータリーキルン内に吹き込むに当たり、混合比率を調整した上で吹き込むようにしたので、燃焼分布の調整や到達距離の分散度合いを、その混合比率に応じて調整することができる。
【図面の簡単な説明】
【図1】本発明の実施形態の減容化の手順を示す説明図である。
【図2】本発明の実施形態のマット状に減容化した可燃性廃棄物をセメント焼成工程に投入するまでの手順を示す説明図である。
【図3】本発明の他の実施形態の説明図である。
【符号の説明】
1 袋
2 可燃性廃棄物
2A マット状の可燃性廃棄物
2C 破砕品
7,27 破砕機
10 ロータリーキルン
10A 窯尻部
10B 窯前部
22A 硬質プラスチック(硬質の可燃性廃棄物)
22C 破砕品
[0001]
BACKGROUND OF THE INVENTION
The present invention is applicable to, for example, a combustible waste having a large degree of bulk such as a tape such as a magnetic tape, a sheet-like or film-like plastic, or a laminated film after recovering pulp from a laminated waste paper, to a combustion furnace. while volume reduction to transport to put easily form, it relates to a method for the those that reduced iodide dispose while effectively utilized in cement burning process.
[0002]
[Prior art]
The amount of industrial waste generated has been increasing year by year. As the processing method, landfill processing, incineration processing and the like are known. However, incineration treatment has attracted attention because it has become difficult to secure a landfill site. Among such industrial wastes, combustible wastes such as waste plastic generate a sufficient amount of heat by incineration, and are therefore being used as fuel for various combustion furnaces in order to effectively use the amount of heat generated by the combustion.
[0003]
For example, as a method of using combustible waste such as waste plastic as a fuel, as disclosed in Japanese Patent Application Laid-Open No. 7-277788, etc., the main fuel is injected into a rotary kiln of a cement firing facility and burned. A technique for reducing the amount of pulverized coal used has been known for some time.
[0004]
[Problems to be solved by the invention]
However, plastic waste materials discarded in the form of tapes, films, sheets, etc., or flammable waste with a very large degree of bulk such as office papers crushed with a shredder are not suitable for cement production. Various problems occur when supplying to rotary kilns and calcining furnaces. That is, these waste materials are extremely difficult to handle, such as storage, transportation, and weighing. For example, when storing, a vast storage space is required because the bulk specific gravity is small. Further, when transporting by car, since the bulk specific gravity is small, the transport amount per car is extremely small, the transport efficiency is remarkably bad, and it is easy to scatter. Furthermore, even when transported by a transport machine such as a belt conveyor, scattering, spillage, clogging, etc. are likely to occur. In addition, there is a problem that, when it is put into a combustion furnace, the thrown-up thing soars.
[0005]
In view of this, a method has been considered in which these combustible wastes are heat-compressed by addition of a binder to solidify the volume. However, flammable waste sent through the cleaning process often has moisture attached. In such a case, if the heating temperature is increased for volume reduction, a steam explosion occurs. The danger comes out. Therefore, there is a problem that the conventional volume reduction solidification method cannot be adopted unconditionally. In addition, the conventional volume reduction and solidification method requires equipment for heat compression, which is costly and complicates the process.
[0006]
The present invention is, in consideration of the above circumstances, and an object thereof is to provide a method for disposal by simple and safe volume reduction of combustible wastes such as large magnetic tape handling form easy degree bulky.
[0007]
[Means for Solving the Problems]
In the method for disposing combustible waste according to the first aspect of the present invention, compressible and bulky combustible waste is accommodated in a bag capable of maintaining airtightness, and the air in the bag is exhausted. Then, it is compressed to form a mat, and the flammable waste in a bag formed into the mat is crushed by a crusher as it is, and the resulting crushed product is harder than that. It is characterized by being added as auxiliary fuel to the cement firing process after being mixed with the crushed product .
[0008]
Thus, by compressing by decompression and forming the whole bag in a mat shape, a large number of sheets can be stacked when stored or transported by car. Therefore, it can be stored and loaded in large quantities, and storage efficiency and transportation efficiency are improved. In addition, since it is in a bag, handling operation during weighing and the like can be performed very easily, and it is not necessary to take measures against scattering. Moreover, since it can be put into the combustion furnace as it is in the bag, there is no need to worry about scattering or spilling or soaring. Furthermore, since the volume can be reduced simply and safely without cost by using a household vacuum cleaner or a vacuum pump, it is easy to realize compared with the conventional heat compression type volume reduction method.
[0013]
In addition, when the flammable waste reduced to a mat shape is introduced into the cement firing process, a method is adopted in which the bag is crushed and then introduced into the cement firing process, which facilitates mechanization.
In addition, when a flammable waste with a large degree of bulk is applied to a crusher in its bulky state, the crushing ability is 1 / compared to the case of crushing a hard flammable waste (hard plastic, etc.). Although it will be reduced to about 3, it can be recovered by crushing it with a bag while it is vacuum-sucked and compressed into a mat to reduce the volume. For example, when sucked with a household vacuum cleaner, the amount of crushing ability can be reduced to 2/3, and when sucked with a vacuum pump, it is equivalent to that when crushing hard flammable waste. The above crushing capacity can be ensured. That is, the crushing capacity can be increased according to the level of compression.
[0015]
Furthermore, it becomes possible to improve the balance of the combustion distribution by mixing it with a crushed product of hard flammable waste (for example, block-like or thick plastic waste) and then putting it into the cement firing process. .
[0016]
The method for disposing combustible waste according to the invention of claim 2 is the method according to claim 1, wherein a mixture of a crushed product crushed by a crusher with a bag and a crushed product of a harder combustible waste is burned with cement. It is characterized in that it is blown into the rotary kiln by putting it in an air flow from the front part of the rotary kiln of the process toward the bottom of the kiln.
[0017]
In this way, when the mixture is blown in the air flow from the front of the kiln of the rotary kiln, the bulk specific gravity of the crushed product is dispersed, so that it is possible to reach the wide range of the firing area of the rotary kiln while dispersing the combustible waste. The combustion balance can be improved.
[0018]
The method for disposing combustible waste according to the invention of claim 3 is the mixing method of the mixture of a crushed product crushed by a crusher with a bag and a crushed product of harder flammable waste in claim 2 After adjusting the ratio, it is characterized by blowing in an air stream from the front of the kiln of the rotary kiln.
[0019]
In this way, by adjusting the mixing ratio of the two types of crushed products, it is possible to adjust the combustion distribution and the degree of dispersion of the reach distance. In addition, combustible waste with a large degree of bulk is crushed in a mat-like volume-reduced state, so the weighing accuracy is improved and the mixing ratio adjustment when mixing with hard combustible waste is accurate. Will be able to do.
[0020]
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, embodiments of the present invention will be described with reference to the drawings.
FIG. 1 shows a procedure from volume reduction of combustible waste to loading into a car.
When implementing the volume reduction method of this embodiment, the airtight bag 1 of the magnitude | size which is easy to handle first is prepared. The bag 1 is desirably a resin-made rectangular shape that is sealed on three sides and opened on one side, and a commercially available product with an airtight chuck attached to the opening 1a can be used.
[0021]
As shown in FIG. 1 (a), the bag 1 has a large degree of bulk such as a tape such as a magnetic tape, a sheet-like or film-like plastic, and a laminated film after the pulp is recovered from waste laminated paper. Push a large amount of combustible waste 2. And if it accommodates in the bag 1, as shown to (b), the pipe | tube of the blower 3 will be inserted from a clearance gap, narrowing the opening part 1a of the bag 1, and internal air will be exhausted with the blower 3. FIG. Here, as the blower 3, it is ideal to use a vacuum pump, but a household vacuum cleaner or the like may be used. By vacuum suction in this way, as shown in (c), the combustible waste 2 inside is compressed together with the bag 1, and a mat-like combustible waste 2A is completed. At this stage, it is advantageous in a post-process to form a mat having a thickness of about 10 to 20 cm.
[0022]
Since the combustible waste 2A thus compressed and formed into a mat shape is in a mat form, a large number of sheets can be stacked. As shown in FIG. Can be loaded. Therefore, the transportation efficiency is greatly improved. Moreover, since a large number of sheets can be stacked when storing, the storage efficiency is greatly improved. In addition, since it is in a bag, handling operation during weighing and the like can be performed very easily, and it is not necessary to take measures against scattering. Furthermore, since it can be put into the combustion furnace as it is in the bag, there is no need to worry about scattering or spilling or soaring.
[0023]
Further, the volume reduction method in this case is only compression by decompression using the bag 1 and the blower 3, and unlike the volume reduction solidification method by heat compression, heating is not required. Even the adhering combustible waste 2 can be safely reduced in volume, and it is not necessary to use a large volume reduction and solidification device.
[0024]
FIG. 2 shows a procedure until the mat-like combustible waste 2A formed as described above is put into a cement firing step. In the figure, 10 is a rotary kiln for a cement firing step, 10A is a kiln front part, and 10B is a kiln bottom part. The cement raw material G1 is charged into the rotary kiln 10 from the kiln bottom 1B, fired while moving in the rotary kiln 10, and discharged as a cement clinker G2 from the cooler 11 of the kiln front 10A.
[0025]
A kiln front portion 10A, which is the downstream end of the rotary kiln 10, is provided with a main fuel nozzle 12 such as coal powder or heavy oil, and an injection nozzle 13 for combustible waste. Fuel and combustible waste products are fed into the rotary kiln 10. Here, the pulverized combustible waste product is used as an auxiliary fuel for cement clinker firing by being blown into the rotary kiln 10 in an air flow from the kiln front part 10A toward the kiln bottom part 10B. .
[0026]
In manufacturing a cement clinker using this equipment, the flammable waste 2A formed in the mat shape is put into the rotary kiln 10 as an auxiliary fuel. In that case, when charging, the method (A) of charging in the form of the mat as it is, or the flammable waste 2A in the bag formed in the mat shape is crushed by the crusher 7 and then charged. Either or both of the methods (B) can be employed.
[0027]
In the case of charging by the method (B), the crushed product 2C can be blown into the rotary kiln 10 by being put on the air flow (air) from the nozzle 13 of the kiln front part 10A of the rotary kiln 10, so that it can be easily mechanized. .
[0028]
By introducing the flammable waste 2A, which has been reduced to a mat-like shape, into the cement firing process as an auxiliary fuel in the form of a bag, the waste can be effectively used while facilitating handling. Main fuel such as pulverized coal can be saved.
[0029]
Further, as shown in FIG. 3, a crushed product 2C of combustible waste 2A formed in a mat shape, and a hard plastic (hard combustible waste) 22A such as a hard block shape or a thick material shape. After mixing with the crushed product 22C, the air flow may be blown into the rotary kiln 10 from the nozzle 13 of the front kiln 10A of the rotary kiln 10.
[0030]
In that case, the measuring devices 6 and 26, the crushers 7 and 27, and the mixer 28 are prepared in the combustible waste input system, and mixed while adjusting the mixing ratio of the combustible wastes 2A and 22A. Try to blow things.
[0031]
In this way, by mixing the crushed combustible waste 2C into the rotary kiln 10 after mixing with the hard plastic crushed product 22C, the combustible waste can be appropriately distributed over a wide range of the firing area of the rotary kiln 10. It is possible to achieve a good balance of combustion distribution. Moreover, by adjusting the mixing ratio of the two types of crushed products 2C and 22C, it is possible to adjust the combustion distribution and the degree of dispersion of the reach distance. In addition, although the plastic was illustrated as a hard combustible waste, it is not specifically limited to it.
[0032]
【The invention's effect】
As described above, according to the first aspect of the present invention, combustible waste having a large bulkiness is put in an airtight bag and compressed and reduced into a mat shape by a so-called vacuum pack method. When transporting by car or by car, a large number of sheets can be stacked, and storage efficiency and transport efficiency can be improved. In addition, since it is in a bag, handling operation during weighing and the like can be performed very easily, and no scattering measures are required. Moreover, since it can be put into the combustion furnace as it is in the bag, there is no need to worry about scattering or spilling or soaring.
[0035]
In addition, the crushed product that has been crushed with a crusher in the form of a bag is mixed with the crushed product of harder flammable waste and then injected into the cement firing process as an auxiliary fuel. Can be improved.
[0036]
According to the invention of claim 2 , since the mixture of the two kinds of crushed products in claim 1 is blown from the front part of the kiln of the rotary kiln toward the kiln bottom part, it is combustible in a wide range of the firing area of the rotary kiln. It is possible to reach the volatile waste while dispersing it, and to improve the combustion balance.
[0037]
According to the invention of claim 3 , since the mixture of the two kinds of crushed products is blown into the rotary kiln after the mixing ratio is adjusted, the combustion distribution is adjusted and the dispersion degree of the reach distance is adjusted by mixing the mixture. It can be adjusted according to the ratio.
[Brief description of the drawings]
FIG. 1 is an explanatory diagram showing a procedure for volume reduction according to an embodiment of the present invention.
FIG. 2 is an explanatory diagram showing a procedure until the combustible waste reduced to a mat shape according to the embodiment of the present invention is put into a cement firing step.
FIG. 3 is an explanatory diagram of another embodiment of the present invention.
[Explanation of symbols]
1 bag 2 flammable waste 2A mat-like flammable waste 2C shredded product 7,27 shredder 10 rotary kiln 10A kiln bottom 10B kiln front 22A hard plastic (hard combustible waste)
22C crushed product

Claims (3)

圧縮可能で嵩張り度合いの大きな可燃性廃棄物を、気密性を保持し得る袋に収容して、該袋内の空気を排気することで、圧縮してマット状に形成し、該マット状に形成した袋入りの可燃性廃棄物を、袋のまま破砕機にかけて破砕し、得られた破砕品を、それより硬質の可燃性廃棄物の破砕品と混合した上で、セメント焼成工程に補助燃料として投入することを特徴とする可燃性廃棄物の処分方法。 Compressible and bulky flammable waste is contained in a bag that can maintain airtightness, and the air in the bag is exhausted to form a mat that is compressed. The formed combustible waste in the bag is crushed with a crusher as it is in the bag, and the obtained crushed product is mixed with the crushed product of harder combustible waste. Disposal method of combustible waste, characterized by being introduced as 前記袋のまま破砕機にかけて破砕した破砕品と、それより硬質の可燃性廃棄物の破砕品との混合物を、セメント焼成工程のロータリーキルンの窯前部から窯尻部方向へ向かって空気流に乗せてロータリーキルン内に吹き込むことを特徴とする請求項1記載の可燃性廃棄物の処分方法。 The mixture of the crushed product crushed by the crusher with the bag and the crushed product of harder combustible waste is put on the air flow from the front of the kiln of the rotary kiln in the cement firing process toward the bottom of the kiln. The method for disposing of combustible waste according to claim 1, wherein the combustible waste is blown into a rotary kiln . 前記袋のまま破砕機にかけて破砕した破砕品と、それより硬質の可燃性廃棄物の破砕品との混合物を、その混合比率を調整した上で、ロータリーキルンの窯前部から空気流に乗せて吹き込むことを特徴とする請求項2記載の可燃性廃棄物の処分方法。 The mixture of the crushed product crushed by the crusher with the bag and the crushed product of harder combustible waste is blown in the air flow from the front of the kiln of the rotary kiln after adjusting the mixing ratio. The disposal method of the combustible waste of Claim 2 characterized by the above-mentioned.
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