JP6261518B2 - Waste fuel conversion apparatus and method including waste plastic - Google Patents
Waste fuel conversion apparatus and method including waste plastic Download PDFInfo
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- JP6261518B2 JP6261518B2 JP2014557351A JP2014557351A JP6261518B2 JP 6261518 B2 JP6261518 B2 JP 6261518B2 JP 2014557351 A JP2014557351 A JP 2014557351A JP 2014557351 A JP2014557351 A JP 2014557351A JP 6261518 B2 JP6261518 B2 JP 6261518B2
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- 239000002699 waste material Substances 0.000 title claims description 67
- 239000004033 plastic Substances 0.000 title claims description 38
- 229920003023 plastic Polymers 0.000 title claims description 38
- 239000000446 fuel Substances 0.000 title claims description 21
- 238000000034 method Methods 0.000 title claims description 8
- 238000006243 chemical reaction Methods 0.000 title claims description 4
- 239000000463 material Substances 0.000 claims description 39
- 239000004568 cement Substances 0.000 claims description 29
- 239000002245 particle Substances 0.000 claims description 25
- 238000010304 firing Methods 0.000 claims description 10
- 238000005096 rolling process Methods 0.000 claims description 10
- 230000006835 compression Effects 0.000 claims description 9
- 238000007906 compression Methods 0.000 claims description 9
- 238000010438 heat treatment Methods 0.000 claims description 9
- 238000007873 sieving Methods 0.000 claims description 9
- 238000000926 separation method Methods 0.000 claims description 8
- 239000000428 dust Substances 0.000 claims description 5
- 238000002485 combustion reaction Methods 0.000 description 14
- 239000010408 film Substances 0.000 description 6
- 230000002411 adverse Effects 0.000 description 4
- 239000010849 combustible waste Substances 0.000 description 3
- 239000002994 raw material Substances 0.000 description 3
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 238000007664 blowing Methods 0.000 description 2
- 238000001354 calcination Methods 0.000 description 2
- 229920001971 elastomer Polymers 0.000 description 2
- 239000002957 persistent organic pollutant Substances 0.000 description 2
- 239000005060 rubber Substances 0.000 description 2
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 230000006698 induction Effects 0.000 description 1
- 239000002440 industrial waste Substances 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- JTJMJGYZQZDUJJ-UHFFFAOYSA-N phencyclidine Chemical class C1CCCCN1C1(C=2C=CC=CC=2)CCCCC1 JTJMJGYZQZDUJJ-UHFFFAOYSA-N 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 238000006722 reduction reaction Methods 0.000 description 1
- 238000012216 screening Methods 0.000 description 1
- 239000010409 thin film Substances 0.000 description 1
Classifications
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L5/00—Solid fuels
- C10L5/40—Solid fuels essentially based on materials of non-mineral origin
- C10L5/406—Solid fuels essentially based on materials of non-mineral origin on plastic
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09B—DISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
- B09B3/00—Destroying solid waste or transforming solid waste into something useful or harmless
- B09B3/20—Agglomeration, binding or encapsulation of solid waste
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B7/00—Hydraulic cements
- C04B7/36—Manufacture of hydraulic cements in general
- C04B7/43—Heat treatment, e.g. precalcining, burning, melting; Cooling
- C04B7/44—Burning; Melting
- C04B7/4407—Treatment 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
- C04B7/4423—Waste or refuse used as fuel
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L5/00—Solid fuels
- C10L5/40—Solid fuels essentially based on materials of non-mineral origin
- C10L5/46—Solid fuels essentially based on materials of non-mineral origin on sewage, house, or town refuse
-
- 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
-
- 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
-
- 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
- Y02P40/00—Technologies relating to the processing of minerals
- Y02P40/10—Production of cement, e.g. improving or optimising the production methods; Cement grinding
- Y02P40/125—Fuels from renewable energy sources, e.g. waste or biomass
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Ceramic Engineering (AREA)
- Structural Engineering (AREA)
- Physics & Mathematics (AREA)
- Materials Engineering (AREA)
- Thermal Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- Processing Of Solid Wastes (AREA)
- Solid Fuels And Fuel-Associated Substances (AREA)
- Combined Means For Separation Of Solids (AREA)
- Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)
- Curing Cements, Concrete, And Artificial Stone (AREA)
Description
本発明は、ASR(自動車シュレッダーダスト)等の廃プラスチックを含む廃棄物を、セメント焼成装置において燃料として利用するための装置及び方法に関する。 The present invention relates to an apparatus and a method for using waste containing waste plastic such as ASR (automobile shredder dust) as a fuel in a cement baking apparatus.
従来、セメント焼成装置では、ASR等の廃プラスチックを含む廃棄物をセメントキルンの燃焼用バーナーの代替燃料として利用している。例えば、特許文献1には、プラスチック類、スポンジ類、繊維類、ゴム類及び木質類からなる群より選択される一以上を主成分とする可燃性廃棄物を1次破砕機により粗砕する工程と、可燃性廃棄物に含まれる異物を除去する工程と、異物を除去した粗砕物を2次破砕機により破砕する工程と、破砕物をバーナーに吹き込む工程とを含み、粗砕物の水分を5質量%以下とした上で、2次破砕機の動力が一定になるように粗砕物を2次破砕機に供給する可燃性廃棄物の燃料化方法が記載されている。 Conventionally, in cement burning apparatuses, waste containing waste plastic such as ASR is used as an alternative fuel for a burner for cement kiln combustion. For example, Patent Document 1 discloses a step of roughly crushing combustible waste mainly composed of one or more selected from the group consisting of plastics, sponges, fibers, rubbers, and woods by a primary crusher. And a step of removing foreign matter contained in the combustible waste, a step of crushing the coarsely crushed product from which the foreign matter has been removed by a secondary crusher, and a step of blowing the crushed product into a burner. There is described a method for converting combustible waste into a fuel that supplies a coarsely crushed product to a secondary crusher so that the power of the secondary crusher is constant after setting the mass% or less.
しかし、廃棄物には様々な性状のものが含まれているため、廃棄物を単に破砕して得られる破砕物は、燃焼用バーナーによって完全に大気中で燃焼(空間燃焼)されない場合があり、そのような場合には、燃焼用バーナーに吹き込まれた廃棄物の一部がクリンカ上に着地して不完全燃焼を起こしたり、クリンカが還元反応を生じ、クリンカの品質や色相に影響を及ぼすという不具合があった。 However, since waste has various properties, the crushed material obtained by simply crushing the waste may not be completely burned in the atmosphere (spatial combustion) by the combustion burner. In such a case, some of the waste blown into the combustion burner will land on the clinker and cause incomplete combustion, or the clinker will undergo a reduction reaction, affecting the quality and hue of the clinker. There was a bug.
そこで、本発明は、上記問題点に鑑みてなされたものであり、クリンカの品質へ悪影響を及ぼすことなく、廃プラスチックを含む廃棄物全体をセメント焼成用燃料として有効利用することを目的とする。 Therefore, the present invention has been made in view of the above problems, and an object thereof is to effectively use the entire waste including waste plastic as a cement firing fuel without adversely affecting the quality of the clinker.
上記目的を達成するため、本発明は、廃プラスチックを含む廃棄物を破砕する破砕装置と、該破砕装置によって破砕した廃棄物を、所定の粒径範囲にある空間燃焼が困難な破砕物と、その他の破砕物とに分離する分離装置と、該分離装置によって分離された前記空間燃焼が困難な破砕物をフィルム状に薄片化する圧延装置と、該圧延装置によって薄片化された破砕物をセメント焼成装置に供給する供給装置とを備えることを特徴とする。ここで、空間燃焼が困難な破砕物とは、セメントキルンの燃焼用バーナーからキルン内に吹き込まれた場合に、クリンカ上に着地して不完全燃焼を起こすなどして、キルンの内部空間等において完全燃焼し難い破砕物をいう。 In order to achieve the above object, the present invention provides a crushing device for crushing waste containing waste plastic, a waste crushed by the crushing device, a crushed material that is difficult to spatially burn in a predetermined particle size range, Separation device for separating into other crushed materials, a rolling device for slicing the crushed materials separated by the separation device, which are difficult to burn in space, into a film, and a crushed material separated by the rolling device as cement And a supply device for supplying to the baking apparatus. Here, the crushed material that is difficult to burn in space means that when it is blown into the kiln from a burner for cement kiln, it will land on the clinker and cause incomplete combustion, etc. It refers to crushed material that is difficult to burn completely.
本発明によれば、圧延装置によって、廃棄物に含まれる所定の粒径範囲にある空間燃焼が困難な破砕物をフィルム状に薄片化することで、燃焼用バーナーからセメントキルン等に吹き込んでも完全に空間燃焼させることができるため、クリンカの品質へ悪影響を及ぼすことなく、セメント焼成用燃料として有効利用することができる。 According to the present invention, the crushed material that is difficult to spatially burn within the predetermined particle size range included in the waste is thinned into a film shape by a rolling device, so that even if it is blown from a combustion burner into a cement kiln, etc. Therefore, it can be effectively used as a cement firing fuel without adversely affecting the quality of the clinker.
前記供給装置によって、前記その他の破砕物を、前記圧延装置によって薄片化された破砕物と共にセメント焼成装置に供給することができる。これにより、廃プラスチックを含む廃棄物全体をセメント焼成用燃料として有効利用することができる。 By the supply device, the other crushed material can be supplied to the cement firing device together with the crushed material thinned by the rolling device. Thereby, the whole waste containing waste plastic can be effectively used as a cement firing fuel.
上記廃棄物の燃料化装置において、前記廃プラスチックを含む廃棄物を自動車シュレッダーダストとし、前記破砕装置は、口径がXmmのスクリーンを備え、前記分離装置は、前記破砕装置の下流側に位置し、前記破砕装置によって破砕した廃棄物を篩い分ける篩分装置であって、前記空間燃焼が困難な破砕物は、前記篩分装置によって分離されたX/3mm以上4X/5mm以下の範囲にあるものとすることができる。これによって、自動車シュレッダーダストの有効利用を促進することができる。また、不完全燃焼に起因する様々な汚染物質の量を減少させ、それと共に残留性有機汚染物質(POPs:Persistent Organic Pollutants)類の排出量も低減することができる。 In the waste fueling device, waste containing the waste plastic is automobile shredder dust, the crushing device is provided with a screen having a diameter of X mm, and the separation device is located downstream of the crushing device, The sieving device for sieving the waste crushed by the crushing device, wherein the crushed material that is difficult to burn spatially is in the range of X / 3 mm to 4X / 5 mm separated by the sieving device . can do. Thereby, the effective utilization of the automobile shredder dust can be promoted. Moreover, the amount of various pollutants resulting from incomplete combustion can be reduced, and at the same time, the discharge amount of persistent organic pollutants (POPs) can be reduced.
また、前記スクリーンの口径Xを5mm以上100mm以下とすることができ、口径の小さいスクリーンで得られた破砕物を主にセメントキルンの燃焼用バーナーに吹き込むことができ、口径の大きいスクリーンで得られた破砕物をセメントキルンの窯尻に投入して燃料として使用することができる。 Further, the diameter X of the screen can be 5 mm or more and 100 mm or less, and the crushed material obtained by the screen having a small diameter can be mainly blown into the combustion burner of the cement kiln, which is obtained by the screen having a large diameter. The crushed material can be put into the kiln bottom of a cement kiln and used as fuel.
上記廃棄物の燃料化装置において、前記圧延装置を、前記空間燃焼が困難な破砕物を加熱しながら圧縮する加熱式の圧縮ロールとすることができる。 In the waste fueling apparatus, the rolling device may be a heating type compression roll that compresses the crushed material that is difficult to burn in space while heating.
さらに、前記廃プラスチックを含む廃棄物を、硬質プラスチックと軟質プラスチックとを含むものとし、前記分離装置を、前記破砕装置の下流側に位置する風力選別機とすることができる。 Further, the waste containing the waste plastic may include hard plastic and soft plastic, and the separation device may be a wind power sorter located on the downstream side of the crushing device.
また、本発明は、廃プラスチックを含む廃棄物の燃料化方法であって、廃プラスチックを含む廃棄物を破砕し、該破砕した廃棄物を、所定の粒径範囲にある空間燃焼が困難な破砕物と、その他の破砕物とに分離し、該分離した空間燃焼が困難な破砕物をフィルム状に薄片化し、該薄片化した破砕物をセメント焼成装置に供給することを特徴とする。本発明によれば、上記発明と同様に、クリンカの品質へ悪影響を及ぼすことなく、空間燃焼が困難な破砕物をセメント焼成用燃料として有効利用することができる。 The present invention also relates to a method for fuelizing waste containing waste plastic, wherein the waste containing waste plastic is crushed, and the crushed waste is crushed in a predetermined particle size range and difficult to burn in space. The crushed material that is difficult to burn in space is cut into a thin film, and the crushed crushed material is supplied to a cement firing device. According to the present invention, as in the case of the above-described invention, a crushed material that is difficult to spatially burn can be effectively used as a cement firing fuel without adversely affecting the quality of the clinker.
以上のように、本発明によれば、クリンカの品質への悪影響を回避しながら、廃プラスチックを含む廃棄物全体をセメント焼成用燃料として有効利用することができる。 As described above, according to the present invention, the entire waste including waste plastic can be effectively used as a cement firing fuel while avoiding adverse effects on the quality of the clinker.
次に、本発明を実施するための形態について図面を参照しながら詳細に説明する。尚、以下の説明においては、本発明を自動車シュレッダーダスト(以下「ASR」という)の燃料化に適用した場合を例にとって説明する。尚、ASRとは、廃棄された自動車のエンジン等を取り除いた後の廃車ガラを工業用シュレッダーで粉々に粉砕して鉄等を回収した後、産業廃棄物として廃棄されるプラスチック、ガラス、ゴムなどの破片をいう。 Next, embodiments for carrying out the present invention will be described in detail with reference to the drawings. In the following description, the case where the present invention is applied to fuel conversion of automobile shredder dust (hereinafter referred to as “ASR”) will be described as an example. ASR refers to plastic, glass, rubber, etc. that are discarded as industrial waste after the scraped car waste after removing the discarded automobile engine, etc. is shattered with an industrial shredder to recover iron, etc. A debris.
本発明に係る廃プラスチックを含む廃棄物の燃料化装置(以下「燃料化装置」という)1は、図1に示すように、ASRを破砕する破砕装置10と、破砕物Cを篩い分ける篩分装置20と、篩い分けられた中間粒子群を薄片化する加熱式圧縮ローラ30とを備えている。尚、図1中の記号Aは粒度、及び記号Dはスクリーンの口径を各々示す。 As shown in FIG. 1, a waste fuelizing apparatus (hereinafter referred to as “fuelizing apparatus”) 1 including waste plastic according to the present invention includes a crushing apparatus 10 for crushing ASR and a sieving unit for screening crushed material C. The apparatus 20 and the heating-type compression roller 30 which thins the screened intermediate particle group are provided. In FIG. 1, symbol A indicates the particle size, and symbol D indicates the aperture of the screen.
破砕装置10は、例えば、一軸破砕機であって、回転刃等を収容した箱状の本体10aと、本体10aの上方に位置し、ASRを投入するために開口したホッパー10bと、本体10aの下方に配置され、スクリーンを収容する排出部10c等を備える。ここで、スクリーンの口径DをXmmとする。 The crushing device 10 is, for example, a uniaxial crusher, a box-shaped main body 10a that accommodates a rotary blade, a hopper 10b that is positioned above the main body 10a and that is opened to feed ASR, and a main body 10a. A discharge portion 10c or the like that is disposed below and accommodates the screen is provided. Here, the aperture D of the screen is Xmm.
篩分装置20は、上下方向に2段にわたって配置された2つの振動篩20A、20Bからなり、振動篩20Aの口径は、4/5・Xmm、振動篩20Bの口径は、1/3・Xmmに設定される。 The sieving device 20 includes two vibrating sieves 20A and 20B arranged in two stages in the vertical direction. The diameter of the vibrating sieve 20A is 4/5 · Xmm, and the diameter of the vibrating sieve 20B is 1/3 · Xmm. Set to
圧延装置としての加熱式圧縮ローラ30は、所定温度に設定された一対の発熱回転ローラ30aと、発熱回転ローラ30aを保持する一対のハウジング30b等で構成される。発熱回転ローラ30aには、外部高周波誘導発熱ロールや外部取付型高周波ヒートロール等を用いることができる。 The heating compression roller 30 serving as a rolling device includes a pair of heat generating rotating rollers 30a set to a predetermined temperature, a pair of housings 30b holding the heat generating rotating rollers 30a, and the like. As the heat generating rotating roller 30a, an external high frequency induction heat generating roll, an external mounting type high frequency heat roll or the like can be used.
図示を省略するが、燃料化装置1によって燃料化されたASRを燃料として用いるセメント焼成装置は、セメント原料を予熱するためサイクロンを多段に重ねたプレヒータと、セメント原料を仮焼する仮焼炉と、バーナー等を備えてセメント原料を焼成するセメントキルン(ロータリーキルン)と、セメントキルンから排出されたセメントクリンカを冷却するクリンカクーラ等で構成される。 Although not shown in the drawings, a cement baking apparatus using ASR fueled by the fueling apparatus 1 as fuel includes a preheater in which cyclones are stacked in multiple stages to preheat the cement raw material, and a calcining furnace for calcining the cement raw material. And a cement kiln (rotary kiln) that burns cement raw material with a burner and the like, and a clinker cooler that cools the cement clinker discharged from the cement kiln.
次に、上記構成を有する燃料化装置1によるASRの燃料化方法について説明する。 Next, a fueling method for ASR by the fueling apparatus 1 having the above configuration will be described.
受け入れたASRを破砕装置10に投入して破砕する。ここで、破砕装置10のスクリーンの口径Xmmを所望の値に設定することにより、可燃物は回転刃により破砕されて所定の粒度になって排出部10cから破砕物Cとして排出される。スクリーンの口径Xmmは、10mm〜15mmに設定するのが好ましいが、5mm〜100mm程度に設定することができ、口径の小さいスクリーンで得られた燃料を主にセメントキルンの燃焼用バーナーに吹き込んで使用し、口径の大きいスクリーンで得られた燃料をセメントキルンの窯尻に投入して使用することができる。 The received ASR is put into the crushing apparatus 10 and crushed. Here, by setting the aperture Xmm of the screen of the crushing apparatus 10 to a desired value, the combustible material is crushed by the rotary blade, becomes a predetermined particle size, and is discharged as the crushed material C from the discharge portion 10c. The diameter of the screen Xmm is preferably set to 10 mm to 15 mm, but can be set to about 5 mm to 100 mm, and the fuel obtained from the screen with a small diameter is mainly used by blowing it into a burner for cement kiln combustion. However, the fuel obtained from the large-diameter screen can be used by putting it in the kiln bottom of the cement kiln.
破砕装置10から排出された破砕物Cは、振動篩20Aに供給され、4/5・Xmmを超える粒子群(大径粒子群LP)は、そのまま代替燃料として用いられる。4/5・Xmm以下の粒子群は、振動篩20Bに供給され、1/3・Xmm以下の粒子群(小径粒子群SP)もそのまま代替燃料として用いられる。一方、1/3・Xmmを超え、4/5・Xmm以下の粒子群(中間粒子群MP)は、加熱式圧縮ローラ30に導入される。 The crushed material C discharged from the crushing apparatus 10 is supplied to the vibrating sieve 20A, and the particle group (large particle group LP) exceeding 4/5 · X mm is used as it is as an alternative fuel. A particle group of 4/5 · X mm or less is supplied to the vibrating sieve 20B, and a particle group (small particle group SP) of 1/3 · X mm or less is also used as an alternative fuel as it is. On the other hand, a particle group (intermediate particle group MP) exceeding 1/3 · Xmm and 4/5 · Xmm or less is introduced into the heating compression roller 30.
加熱式圧縮ローラ30において、中間粒子群MPの破砕物が、所定温度に設定された一対の発熱回転ローラ30aによって圧延され、フィルム状に薄片化される。薄片化された破砕物は、大径粒子群LP及び小径粒子群SPの破砕物と共に、セメントキルンの燃焼用バーナーに燃料として吹き込むことができる。 In the heating-type compression roller 30, the crushed material of the intermediate particle group MP is rolled by a pair of heat-generating rotating rollers 30a set to a predetermined temperature and thinned into a film shape. The crushed crushed material can be injected as fuel into the combustion burner of the cement kiln together with the crushed material of the large particle group LP and the small particle group SP.
次に、本発明に係る燃料化装置及び燃料化方法の試験例について説明する。 Next, test examples of the fueling apparatus and the fueling method according to the present invention will be described.
スクリーンの口径Dを10mmに設定した破砕装置10にASRを投入し、破砕物Cを篩い分けすると、各粒度群(No.1〜5)において表1に示すような物が得られた。表1には、各粒度群における質量(%)、発熱量(cal/g)、熱量割合(%)、ig.loss(Ignition Loss:強熱減量)(%)及び内容物を示している。また、各粒度群における内容物の写真を図2に示す。 When ASR was put into the crushing apparatus 10 in which the aperture D of the screen was set to 10 mm and the crushed material C was sieved, products shown in Table 1 were obtained in each particle size group (No. 1 to 5). Table 1 shows the mass (%), calorific value (cal / g), calorie ratio (%), ig.loss (Ignition Loss) (%) and contents in each particle size group. Moreover, the photograph of the content in each particle size group is shown in FIG.
上記No.1〜5の破砕物について各々燃焼試験を行ったところ、No.1、2は燃焼し易く、質量が最も大きく、発熱量の高いNo.3が最も燃焼し難く、No.4、5については、綿状のため空中に浮遊して即座に空間燃焼することが判明した。 No. above. When a combustion test was performed on each of the crushed materials 1 to 5, No. 1 was obtained. Nos. 1 and 2 are easy to burn, have the largest mass, and have the highest calorific value. No. 3 is the most difficult to burn. It was found that Nos. 4 and 5 floated in the air due to the flocculent form and immediately burned in space.
そこで、本発明者は、上記No.3についても空間燃焼を可能とするため、加熱式圧縮ローラ30によりフィルム状に薄片化することとした。フィルム状に薄片化することで、比表面積が増大すると共に、燃焼用バーナー等を介してセメントキルン内に吹き込まれると、空中に漂って空間燃焼し易くなる。 Therefore, the present inventor has made the above-mentioned No. In order to make space combustion possible also for No. 3, it was decided to make it into a film shape with the heating compression roller 30. By making the film into thin pieces, the specific surface area is increased, and when it is blown into a cement kiln through a combustion burner or the like, it becomes easy to float in the air and burn in space.
尚、上記実施の形態及び試験例では、廃プラスチックを含む廃棄物がASRの場合について説明したが、廃プラスチックを含む廃棄物が硬軟質混合プラスチックの場合には、破砕後に風力選別により硬質プラスチックと軟質プラスチックとに分級し、硬質プラスチックは空間燃焼し難いため、加熱式圧縮ローラによりフィルム状に薄片化する。一方、軟質プラスチックは、空間燃焼し易いのでそのままの状態で燃料となる。 In the above embodiments and test examples, the case where the waste containing waste plastic is ASR has been described. However, when the waste containing waste plastic is a hard / soft mixed plastic, it is classified into a hard plastic by wind sorting after crushing. Since it is classified into soft plastic and hard plastic is difficult to burn in space, it is sliced into a film by a heating compression roller. On the other hand, soft plastics are easily burned in space and are used as fuel as they are.
1 廃プラスチックを含む廃棄物の燃料化装置(燃料化装置)
10 破砕装置
10a 本体
10b ホッパー
10c 排出部
20 篩分装置
20A、20B 振動篩
30 加熱式圧縮ローラ
30a 発熱回転ローラ
30b ハウジング
C 破砕物
LP 大径粒子群
MP 中間粒子群
SP 小径粒子群1 Waste fueling equipment including waste plastic (fuelizing equipment)
DESCRIPTION OF SYMBOLS 10 Crushing apparatus 10a Main body 10b Hopper 10c Discharge part 20 Sieving apparatus 20A, 20B Vibrating sieve 30 Heating compression roller 30a Heating rotation roller 30b Housing C Crushed material LP Large particle group MP Intermediate particle group SP Small particle group
Claims (7)
該破砕装置によって破砕した廃棄物を、所定の粒径範囲にある空間燃焼が困難な破砕物と、その他の破砕物とに分離する分離装置と、
該分離装置によって分離された前記空間燃焼が困難な破砕物をフィルム状に薄片化する圧延装置と、
該圧延装置によって薄片化された破砕物をセメント焼成装置に供給する供給装置とを備えることを特徴とする廃プラスチックを含む廃棄物の燃料化装置。A crushing device for crushing waste including waste plastic,
A separation device for separating the waste crushed by the crushing device into a crushed material that is difficult to burn in space within a predetermined particle size range and other crushed materials;
A rolling device for thinning the crushed material difficult to burn in space separated by the separation device into a film;
A waste fuelizing device including waste plastic, comprising: a supply device that supplies the crushed material thinned by the rolling device to a cement firing device.
前記破砕装置は、口径がXmmのスクリーンを備え、
前記分離装置は、前記破砕装置の下流側に位置し、前記破砕装置によって破砕した廃棄物を篩い分ける篩分装置であって、
前記空間燃焼が困難な破砕物は、前記篩分装置によって分離されたX/3mm以上4X/5mm以下の範囲にあることを特徴とする請求項1又は2に記載の廃プラスチックを含む廃棄物の燃料化装置。 The waste containing the waste plastic is automobile shredder dust,
The crushing device includes a screen having a diameter of X mm,
The separation device is located on the downstream side of the crushing device, and is a sieving device for sieving the waste crushed by the crushing device ,
The waste material containing waste plastic according to claim 1 or 2, wherein the crushed material that is difficult to spatially burn is in the range of X / 3mm to 4X / 5mm separated by the sieving device . Fueling device.
前記分離装置は、前記破砕装置の下流側に位置する風力選別機であることを特徴とする請求項1に記載の廃プラスチックを含む廃棄物の燃料化装置。The waste containing the waste plastic includes hard plastic and soft plastic,
The said separation apparatus is a wind power sorter located in the downstream of the said crushing apparatus, The fuelization apparatus of the waste containing waste plastics of Claim 1 characterized by the above-mentioned.
該破砕した廃棄物を、所定の粒径範囲にある空間燃焼が困難な破砕物と、その他の破砕物とに分離し、
該分離した空間燃焼が困難な破砕物をフィルム状に薄片化し、
該薄片化した破砕物をセメント焼成装置に供給することを特徴とする廃プラスチックを含む廃棄物の燃料化方法。Crushing waste including waste plastic,
The crushed waste is separated into a crushed material that is difficult to burn in space within a predetermined particle size range, and other crushed materials,
The separated crushed material difficult to burn in space is sliced into a film,
A method for fuelizing waste containing waste plastic, characterized in that the crushed crushed material is supplied to a cement firing device.
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