JP7101637B2 - Combustible waste treatment equipment and treatment method - Google Patents

Combustible waste treatment equipment and treatment method Download PDF

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JP7101637B2
JP7101637B2 JP2019114415A JP2019114415A JP7101637B2 JP 7101637 B2 JP7101637 B2 JP 7101637B2 JP 2019114415 A JP2019114415 A JP 2019114415A JP 2019114415 A JP2019114415 A JP 2019114415A JP 7101637 B2 JP7101637 B2 JP 7101637B2
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智典 竹本
洸 瀧澤
恭宗 武藤
泰之 石田
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Taiheiyo Cement Corp
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Description

本発明は、可燃性廃棄物の処理装置及び処理方法に関し、特に、シュレッダーダスト、廃プラスチック、建設廃棄物等の可燃性廃棄物を有効利用する技術に関する。 The present invention relates to a combustible waste treatment apparatus and a treatment method, and more particularly to a technique for effectively utilizing combustible waste such as shredder dust, waste plastic, and construction waste.

シュレッダーダストをリサイクル処理するため、特許文献1には、シュレッダーダストを250~450℃の温度で加熱処理して脆化させ、脆化シュレッダーダストを破砕した後磁着物を除去し、磁着物を除去した脆化シュレッダーダストから、エアテーブルにより重産物として貴金属等を回収することで、シュレッダーダストから有価金属を回収し、残渣をセメント焼成用燃料等として利用する技術が記載されている。 In order to recycle the shredder dust, Patent Document 1 states that the shredder dust is heat-treated at a temperature of 250 to 450 ° C. to make it embrittled, the embrittled shredder dust is crushed, and then the magnetic deposit is removed to remove the magnetic deposit. A technique is described in which precious metals and the like are recovered as heavy products from the embrittled shredder dust by an air table, valuable metals are recovered from the shredder dust, and the residue is used as a fuel for cement firing.

また、特許文献2には、シュレッダーダスト等の可燃性廃棄物を加熱した後破砕し、その後エアテーブルに供給することで、可燃性廃棄物の選別精度を向上させた上で、有価金属や燃料として利用できる樹脂等を回収する技術が記載されている。 Further, in Patent Document 2, combustible waste such as shredder dust is heated and then crushed, and then supplied to an air table to improve the sorting accuracy of combustible waste, and then to use valuable metals and fuels. A technique for recovering a resin or the like that can be used as a fuel is described.

一方、シュレッダーダスト等の可燃性廃棄物には、クロム(Cr)等の忌避成分が含まれ、クロム濃度が高い場合には、セメントの品質に影響を与えるため、セメント燃料としての使用量を低下させざるを得ない場合があるなど、セメント燃料としての利用が事実上制限されていた。そこで、安定してシュレッダーダスト等をセメント資源化するためには、クロム等の忌避成分を低減することが好ましい。 On the other hand, combustible waste such as shredder dust contains repellent components such as chromium (Cr), and if the chromium concentration is high, it affects the quality of cement, so the amount used as cement fuel is reduced. The use as cement fuel was practically restricted, as in some cases it had to be forced to do so. Therefore, in order to stably convert shredder dust and the like into cement resources, it is preferable to reduce the repellent components such as chromium.

廃棄物からのクロム除去に関する技術として、例えば特許文献3には、都市ごみ焼却主灰からクロム等の重金属を分離するため、焼却主灰を磁力選別により磁着物と非磁着物とに分離し、分離して得られた非磁着物をセメント焼成装置においてクロム分を低減させたセメント原料として用いることが記載されている。 As a technique for removing chromium from waste, for example, in Patent Document 3, in order to separate heavy metals such as chromium from the main ash for incinerating municipal waste, the main ash for incineration is separated into magnetic and non-magnetic materials by magnetic sorting. It is described that the non-magnetized material obtained by separation is used as a cement raw material having a reduced chromium content in a cement firing apparatus.

また、特許文献4には、可燃性廃棄物からオーステナイト系ステンレス等のクロムを含む金属を回収するにあたって、廃棄物を破砕した後磁力選別することが記載されている。 Further, Patent Document 4 describes that when recovering a metal containing chromium such as austenitic stainless steel from combustible waste, the waste is crushed and then magnetically sorted.

特開2018-34143号公報Japanese Unexamined Patent Publication No. 2018-34143 特開2018-164872号公報Japanese Unexamined Patent Publication No. 2018-164872 特開2017-137224号公報Japanese Unexamined Patent Publication No. 2017-137224 特開平8-224498号公報Japanese Unexamined Patent Publication No. 8-224498

上記特許文献1及び2に記載の発明は、シュレッダーダスト等を加熱処理した後、破砕処理や物理選別処理を行うことで、貴金属を回収することを主眼とするものである。貴金属回収の途中の工程で磁着物を回収するが、その目的は磁着物が貴金属に混入しないようにするためであって、クロム等の忌避成分の低減を目的とするものではない。 The inventions described in Patent Documents 1 and 2 are intended to recover precious metals by heat-treating shredder dust and the like and then performing crushing treatment and physical sorting treatment. The magnetic deposit is recovered in the process of recovering the noble metal, but the purpose is to prevent the magnetic deposit from being mixed with the noble metal, and not to reduce the repellent component such as chromium.

また、特許文献3及び4に記載の発明のように、磁力選別、又は破砕後の磁力選別だけでは、クロム等の忌避成分の低減効果が充分ではない。 Further, as in the inventions described in Patent Documents 3 and 4, the effect of reducing the repellent component such as chromium is not sufficient only by the magnetic force sorting or the magnetic force sorting after crushing.

本発明は、上記従来の技術における問題点に鑑みてなされたものであって、シュレッダーダスト等の可燃性廃棄物からクロムを効果的に除去して有効利用することを目的とする。 The present invention has been made in view of the above-mentioned problems in the prior art, and an object of the present invention is to effectively remove chromium from combustible waste such as shredder dust and effectively utilize it.

上記目的を達成するため、本発明は、可燃性廃棄物の処理装置であって、可燃性廃棄物を磁着物と非磁着物とに分離する磁力選別機と、該磁力選別機から排出される磁着物を加熱する加熱装置と、該加熱装置から排出される加熱物を破砕する破砕機と、該破砕機から排出される破砕物を重産物と軽産物とに分離する風力選別機又は/及び比重選別機とを備えることを特徴とする可燃性廃棄物の処理装置。 In order to achieve the above object, the present invention is a combustible waste treatment apparatus, which is a magnetic force sorter that separates combustible waste into magnetic and non-magnetic waste, and is discharged from the magnetic force sorter. A heating device that heats the magnetic material, a crusher that crushes the heated material discharged from the heating device, and a wind sorter or / and a wind sorter that separates the crushed material discharged from the crusher into heavy products and light products. A combustible waste treatment device characterized by being equipped with a specific gravity sorter.

本発明によれば、可燃性廃棄物を磁力選別して得られた磁着物を加熱装置で加熱した後破砕するため、磁着物に含まれる金属と可燃分等を効率よく分離することができ、可燃性廃棄物からクロムを効果的に除去することができる。 According to the present invention, since the magnetic material obtained by magnetically sorting combustible waste is heated by a heating device and then crushed, the metal contained in the magnetic material and the combustible component can be efficiently separated. Chromium can be effectively removed from combustible waste.

上記可燃性廃棄物の処理装置において、前記可燃性廃棄物を磁着物と非磁着物とに分離する磁力選別機は、吊り下げ式磁力選別機と、該吊り下げ式磁力選別機の後段に該吊り下げ式磁力選別機が分離した非磁着物を磁着物と非磁着物とに分離するドラム式又はプーリー式磁力選別機であって、前記加熱装置は、該ドラム式又はプーリー式磁力選別機から排出される磁着物を加熱するように構成することで、吊り下げ式磁力選別機で異物を混入させないで純度の高い磁着物を回収し、ドラム式又はプーリー式磁力選別機で異物の混入に関わらず磁着物を回収し、クロムを効果的に除去することができる。 In the combustible waste treatment apparatus, the magnetic force sorter for separating the combustible waste into a magnetic substance and a non-magnetic material is a suspension type magnetic force sorter and a post-stage of the suspension type magnetic force sorter. A drum-type or pulley-type magnetic force sorter that separates a non-magnetic material separated by a suspension-type magnetic force sorter into a magnetic material and a non-magnetic material, and the heating device is from the drum-type or pulley-type magnetic force sorter. By configuring the discharged magnetic material to be heated, a suspended magnetic force sorter can collect high-purity magnetic material without mixing foreign matter, and a drum-type or pulley-type magnetic force sorter can be used to collect foreign matter. The magnetic material can be recovered and the chromium can be effectively removed.

上記可燃性廃棄物の処理装置において、前記吊り下げ式磁力選別機の前段に、前記可燃性廃棄物を2粒群又は3粒群以上に分離する篩選別手段を備え、前記吊り下げ式磁力選別機は、前記2粒群又は3粒群以上の各々の可燃性廃棄物を磁着物と非磁着物とに分離し、前記ドラム式又はプーリー式磁力選別機は、前記吊り下げ式磁力選別機から排出される2粒群又は3粒群以上の非磁着物の各々を磁着物と非磁着物とに分離し、前記加熱装置は、前記ドラム式又はプーリー式磁力選別機から排出される2粒群又は3粒群以上の磁着物を一緒に加熱するように構成することで、篩選別機の後段の磁力選別機や渦電流選別機の処理効率を向上させることができる。 In the combustible waste treatment apparatus, the suspension-type magnetic force sorting machine is provided with a sieve sorting means for separating the combustible waste into two-grain group or three-grain group or more in front of the suspension-type magnetic force sorting machine. The machine separates each combustible waste of the two-grain group or three-grain group or more into magnetic and non-magnetic particles, and the drum-type or pulley-type magnetic force sorter is derived from the suspension-type magnetic force sorter. Each of the two or three or more non-magnetic particles to be discharged is separated into a magnetic and non-magnetic particles, and the heating device is a two-grain group discharged from the drum type or pulley type magnetic force sorter. Alternatively, by configuring the magnetic material of three or more grains to be heated together, the processing efficiency of the magnetic force sorter and the eddy current sorter at the subsequent stage of the sieve sorter can be improved.

上記可燃性廃棄物の処理装置において、前記ドラム式又はプーリー式磁力選別機の後段に、該磁力選別機から排出される2粒群又は3粒群以上の非磁着物の各々を導電産物と非導電産物とに分離する渦電流選別機を備えることで、オーステナイト系ステンレス等のクロムを含む金属を導電産物として除去することができ、可燃性廃棄物に含まれるクロムをさらに効率よく除去することができる。尚、導電産物にはステンレス以外にアルミニウム、銅、真鍮等の金属も含まれるため、ステンレスのみを回収する場合には、導電産物をメタルソーターで処理するとよい。 In the combustible waste treatment device, each of the two-grain group or three-grain group or more non-magnetic particles discharged from the magnetic force sorter is not regarded as a conductive product in the subsequent stage of the drum-type or pulley-type magnetic force sorter. By providing an eddy current sorter that separates from the conductive product, it is possible to remove chromium-containing metals such as austenite-based stainless steel as the conductive product, and it is possible to remove chromium contained in combustible waste more efficiently. can. Since the conductive product contains metals such as aluminum, copper, and brass in addition to stainless steel, it is advisable to treat the conductive product with a metal sorter when collecting only stainless steel.

さらに、本発明は、可燃性廃棄物の処理方法であって、可燃性廃棄物を第1の磁力選別によって磁着物と非磁着物とに分離し、該第1の磁力選別によって分離された磁着物を加熱し、該加熱物を破砕し、該破砕物を第2の磁力選別によって磁着物と非磁着物とに分離することを特徴とする。 Further, the present invention is a method for treating combustible waste, in which the combustible waste is separated into a magnetically-coated substance and a non-magnetically-coated matter by a first magnetic force sorting, and the magnetism separated by the first magnetic force sorting. It is characterized in that the kimono is heated, the heated material is crushed, and the crushed material is separated into a magnetic material and a non-magnetic material by a second magnetic force selection.

また、本発明は、可燃性廃棄物の処理方法であって、可燃性廃棄物を磁力選別によって磁着物と非磁着物とに分離し、該磁力選別によって分離された磁着物を加熱し、該加熱物を破砕し、該破砕物を風力選別又は/及び比重選別によって重産物と軽産物とに分離することを特徴とする。 Further, the present invention is a method for treating combustible waste, in which combustible waste is separated into a magnetic substance and a non-magnetic material by magnetic force sorting, and the magnetic substance separated by the magnetic force selection is heated. It is characterized in that a heated product is crushed and the crushed product is separated into a heavy product and a light product by wind sorting and / and specific gravity sorting.

上記両発明によれば、可燃性廃棄物を磁力選別して得られた磁着物を加熱した後破砕するため、磁着物に含まれる金属と可燃分等を効率よく分離することができ、可燃性廃棄物からクロムを効果的に除去することができる。 According to both of the above inventions, since the magnetic material obtained by magnetically sorting combustible waste is heated and then crushed, the metal contained in the magnetic material and the combustible component can be efficiently separated, and the combustible material is combustible. Chromium can be effectively removed from waste.

以上のように、本発明によれば、シュレッダーダスト等の可燃性廃棄物からクロムを効果的に除去して有効利用することができる。 As described above, according to the present invention, chromium can be effectively removed from combustible waste such as shredder dust and effectively used.

本発明に係る可燃性廃棄物の処理装置の一実施の形態を示すブロック図である。It is a block diagram which shows one Embodiment of the combustible waste processing apparatus which concerns on this invention.

次に、本発明の一実施の形態について図面を参照しながら詳細に説明する。尚、以下の説明では、可燃性廃棄物としてシュレッダーダストを処理する場合を例示する。 Next, an embodiment of the present invention will be described in detail with reference to the drawings. In the following description, a case where shredder dust is treated as combustible waste will be illustrated.

図1は、本発明に係る可燃性廃棄物の処理装置の一実施の形態を示し、この処理装置1は、シュレッダーダストを篩選別する篩選別機2と、篩選別機2によって分離された篩下物を磁力選別する磁力選別機(以下「磁選機」という。)3と、篩上物を磁力選別する磁選機4と、磁選機3によって分離された非磁着物Aを再度磁力選別する磁選機5と、磁選機4によって分離された非磁着物Bを再度磁力選別する磁選機6と、磁選機5によって分離された非磁着物Cを渦電流選別する渦電流選別機7と、磁選機6によって分離された非磁着物Dを渦電流選別する渦電流選別機8と、磁選機5、6によって分離された磁着物C、Dを加熱する加熱装置9と、加熱装置9から排出される加熱物を破砕する破砕機10と、破砕機10から排出される破砕物を重産物と軽産物とに分離する風力選別機11とを備える。 FIG. 1 shows an embodiment of a combustible waste treatment device according to the present invention, in which the treatment device 1 is a sieve sorting machine 2 for sieving shredder dust and a sieve separated by a sieving sorting machine 2. A magnetic sorter (hereinafter referred to as a "magnetic sorter") 3 that sorts underneaths by magnetic force, a magnetic sorter 4 that sorts magnetically on a sieve, and a magnetic sorter that sorts non-magnetic material A separated by the magnetic sorter 3 again. The machine 5, a magnetic separator 6 that re-selects the non-magnetic material B separated by the magnetic separator 4, a vortex current sorter 7 that sorts the vortex current of the non-magnetic material C separated by the magnetic separator 5, and a magnetic separator. The vortex current sorter 8 that sorts the non-magnetic material D separated by 6 and the heating device 9 that heats the magnetic particles C and D separated by the magnetic separators 5 and 6 are discharged from the heating device 9. The crusher 10 for crushing the heated material and the wind sorter 11 for separating the crushed material discharged from the crusher 10 into heavy products and light products are provided.

篩選別機2は、シュレッダーダストを篩い分けて、粒群毎に処理を行うために設けられ、粒群毎に選別することで、後段の磁力選別や渦電流選別を効率的に処理することができる。篩い分けの粒群は、2粒群以上で篩い目は3~30mmとする。3粒群以上とする際は、篩い目の設定を5mm以上の差とする(例えば、5mmと10mm等)。 The sieve sorter 2 is provided to screen the shredder dust and process it for each grain group. By sorting each grain group, it is possible to efficiently process the magnetic force sorting and the eddy current sorting in the subsequent stage. can. The grain group for sieving is 2 or more grains, and the mesh size is 3 to 30 mm. When the number of grains is 3 or more, the difference in the mesh setting is 5 mm or more (for example, 5 mm and 10 mm, etc.).

磁選機3、4は、吊り下げ式が好ましく、異物を混入させないで純度の高い磁着物を回収するために設けられる。磁選機3、4の磁石の磁束密度は700~1500ガウスが好ましい。 The magnetic separators 3 and 4 are preferably of a hanging type, and are provided to recover a highly pure magnetic substance without mixing foreign matter. The magnetic flux density of the magnets of the magnetic separators 3 and 4 is preferably 700 to 1500 gauss.

2段目の磁選機5、6はドラム式又はプーリー式が好ましく、異物(可燃物)混入に関わらず磁着物C、Dを回収するために設けられる。磁選機5、6の磁石の磁束密度は1500ガウス以上が好ましい。 The second-stage magnetic separators 5 and 6 are preferably of a drum type or a pulley type, and are provided to recover the magnetic deposits C and D regardless of the inclusion of foreign matter (combustibles). The magnetic flux density of the magnets of the magnetic separators 5 and 6 is preferably 1500 gauss or more.

渦電流選別機7、8は、非磁着物C、Dから非磁性のステンレス由来のクロムやアルミニウム、銅、真鍮等の金属を除去するために設けられ、ローター回転数は、処理物の粒径が10mm以上の場合は1500rpm以上、10mm未満の場合は3000rpm以上とする。 The eddy current sorters 7 and 8 are provided to remove metals such as chromium, aluminum, copper, and brass derived from non-magnetic stainless steel from the non-magnetic particles C and D, and the rotor rotation speed is the particle size of the processed product. When is 10 mm or more, it is 1500 rpm or more, and when it is less than 10 mm, it is 3000 rpm or more.

加熱装置9は、磁着物C、Dを加熱して磁着物を分離回収し易くするために設けられ、図示例では、磁着物C、Dを一緒に加熱するが、磁着物C、Dを各々別々に加熱処理してもよい。加熱方式は特に指定はないが、処理能力を踏まえると外熱式ロータリーキルンが好ましい The heating device 9 is provided to heat the magnetic objects C and D to facilitate separation and recovery. In the illustrated example, the magnetic objects C and D are heated together, but the magnetic objects C and D are respectively. It may be heat-treated separately. The heating method is not specified, but considering the processing capacity, an external heat type rotary kiln is preferable.

破砕機10は、加熱装置9から排出された加熱物を金属と可燃分(温度が高い場合は灰)とに分離させるために設けられ、破砕機10としては、微粉砕の必要がないため、ジョークラッシャ、インパクトクラッシャ、ロールクラッシャ、ハンマークラッシャ等を用いることができる。 The crusher 10 is provided to separate the heated material discharged from the heating device 9 into a metal and a combustible component (ash when the temperature is high), and the crusher 10 does not need to be finely crushed. Joe crushers, impact crushers, roll crushers, hammer crushers and the like can be used.

風力選別機11は、破砕機10による破砕物を重産物と軽産物とに分離するために設けられ、吹上げ式、 吸引式、密閉式等種々の形式から選択することができる。 The wind power sorter 11 is provided to separate the crushed material by the crusher 10 into heavy products and light products, and can be selected from various types such as a blow-up type, a suction type, and a closed type.

次に、上記構成を有する処理装置1の動作について図1を参照しながら説明する。 Next, the operation of the processing apparatus 1 having the above configuration will be described with reference to FIG.

受け入れたシュレッダーダストを篩選別機(篩選別手段)2で2粒群以上に篩い分ける。図示例では、2粒群に篩い分けている。 The received shredder dust is sieved into two or more grain groups by a sieve sorter (sieving sorting means) 2. In the illustrated example, it is sieved into two grain groups.

篩選別機2で分離した篩下物及び篩上物の各々を磁選機3、4で磁力選別し、異物が少なく純度の高い磁着物A、Bを回収する。磁着物A、Bの粒径は10mm以上のものが多く、強磁性のステンレス由来のクロムが含まれている。 Each of the sieving material and the sieving material separated by the sieving machine 2 is magnetically sorted by the magnetic separators 3 and 4, and the magnetic deposits A and B having a small amount of foreign matter and high purity are recovered. Most of the magnetic particles A and B have a particle size of 10 mm or more, and contain chromium derived from ferromagnetic stainless steel.

次に、磁選機3、4からの非磁着物A、Bを磁選機5、6で磁力選別し、異物の混入に関わらず磁着物C、Dを回収する。磁着物C、Dには可燃物が混入しているため、後段で加熱処理を行う。磁着物C、Dの粒径は10mm以下のものも多く、強磁性及び弱磁性のステンレス由来のクロムが含まれている。 Next, the non-magnetic particles A and B from the magnetic separators 3 and 4 are magnetically sorted by the magnetic separators 5 and 6, and the magnetic particles C and D are recovered regardless of the inclusion of foreign matter. Since flammable substances are mixed in the magnetic objects C and D, heat treatment is performed in the subsequent stage. Most of the magnetic particles C and D have a particle size of 10 mm or less, and contain chromium derived from ferromagnetic and weakly magnetic stainless steel.

さらに、磁選機5、6からの非磁着物C、Dを渦電流選別機7、8に導入し、渦電流選別機7、8によって渦電流選別を行い、導電産物A、Bに非磁性のステンレス由来のクロムを回収する。渦電流選別機7で分離された非導電産物Aは、粒径が小さいため、例えばセメントキルンの窯前、窯尻、仮焼炉から燃料として投入することができる。また、渦電流選別機8で分離された非導電産物Bは、粒径が大きいため、例えばセメントキルンの窯尻、仮焼炉から燃料として投入することができる。 Further, the non-magnetic deposits C and D from the magnetic separators 5 and 6 are introduced into the eddy current sorters 7 and 8, and the eddy currents are sorted by the eddy current sorters 7 and 8, and the conductive products A and B are non-magnetic. Recover chromium derived from stainless steel. Since the non-conductive product A separated by the eddy current sorter 7 has a small particle size, it can be charged as fuel from, for example, in front of the kiln of a cement kiln, at the end of the kiln, or in a calciner. Further, since the non-conductive product B separated by the eddy current sorter 8 has a large particle size, it can be charged as fuel from, for example, a kiln tail of a cement kiln or a calciner.

一方、磁選機5、6で分離した磁着物C、Dを加熱装置9で加熱して後段で磁着物を分離回収し易くする。加熱装置9によって磁着物C、Dを高温で炭化・灰化させてもよいが、可燃物の熱エネルギー利用を考慮すると250~450℃で加熱するのが好ましい。 On the other hand, the magnetic deposits C and D separated by the magnetic separators 5 and 6 are heated by the heating device 9 to facilitate separation and recovery of the magnetic deposits in the subsequent stage. The magnetic particles C and D may be carbonized and incinerated at a high temperature by the heating device 9, but it is preferable to heat them at 250 to 450 ° C. in consideration of the utilization of thermal energy of the combustible material.

次に、加熱装置9から排出された加熱物を破砕機10で破砕し、金属と可燃分又は灰とに分離する。破砕機10によって加熱物を目標粒径5~20mm以下になるまで破砕する。 Next, the heated material discharged from the heating device 9 is crushed by the crusher 10 and separated into a metal and a combustible component or ash. The heated material is crushed by the crusher 10 until the target particle size is 5 to 20 mm or less.

最後に、破砕機10による破砕物を風力選別機11で重産物と軽産物とに分離し、重産物に強磁性及び弱磁性のステンレス由来のクロムを含む比重の大きい金属を回収し、軽産物に磁着物C、Dに付着してきた可燃物を回収することができ、回収した可燃物を燃料として、例えばセメントキルンの窯前、窯尻、仮焼炉から燃料として投入することができる。尚、重産物中の弱磁性・強磁性のステンレスと他の金属、樹脂の塊を分けたい場合には、さらに磁力選別を行う。 Finally, the crushed material by the crusher 10 is separated into a heavy product and a light product by the wind sorter 11, and a metal having a high specific gravity including chromium derived from ferromagnetic and weak magnetic stainless steel is recovered in the heavy product, and the light product is obtained. The combustibles adhering to the magnetic deposits C and D can be recovered, and the recovered combustibles can be used as fuel, for example, as fuel from the front of the kiln of the cement kiln, the kiln butt, or the calcining furnace. If it is desired to separate weak magnetic / ferromagnetic stainless steel from heavy products and lumps of other metals and resins, further magnetic force sorting is performed.

尚、上記実施の形態においては、破砕機10による破砕物を重産物と軽産物とに分離するために風力選別機11を用いたが、風力選別機11に代えて、又は風力選別機11と共にエアテーブル等の比重選別機を用いることもできる。 In the above embodiment, the wind power sorter 11 is used to separate the crushed material by the crusher 10 into heavy products and light products, but instead of the wind power sorter 11 or together with the wind power sorter 11. A specific gravity sorter such as an air table can also be used.

また、シュレッダーダストを篩選別機2で篩下物と篩上物の2粒群に分離した後各々を別々に処理したが、さらに篩選別機を設け、シュレッダーダストを3粒群以上に分離して各々を別々に処理することも可能であり、分離処理により篩選別機2の後段の磁力選別機や渦電流選別機の処理効率を向上させることができる。 Further, the shredder dust was separated into two groups of sieving material and sieving material by the sieving machine 2, and then treated separately. However, a sieving machine was further provided to separate the shredder dust into three or more grain groups. It is also possible to process each of them separately, and the separation processing can improve the processing efficiency of the magnetic force sorter and the eddy current sorter in the subsequent stage of the sieve sorter 2.

一方、シュレッダーダストを篩選別機2で篩下物と篩上物とに分離せずに処理することも可能であり、シュレッダーダストをそのまま磁力選別し、磁着物を加熱し、破砕した後、風力選別又は/及び比重選別を行うこともできる。 On the other hand, it is also possible to process the shredder dust without separating it into the sieve undercoat and the sieve top product by the sieve sorter 2, and the shredder dust is magnetically sorted as it is, the magnetic material is heated and crushed, and then the wind power is applied. Sorting and / and specific gravity sorting can also be performed.

さらに、上記実施の形態においては、シュレッダーダストを処理する場合を例示したが、建設廃棄物等その他の可燃性廃棄物を処理することもできる。 Further, in the above embodiment, the case of treating shredder dust is exemplified, but other combustible waste such as construction waste can also be treated.

1 可燃性廃棄物の処理装置
2 篩選別機
3~6 磁選機
7、8 渦電流選別機
9 加熱装置
10 破砕機
11 風力選別機
1 Combustible waste treatment device 2 Sieving machine 3 to 6 Magnetic separator 7, 8 Eddy current sorter 9 Heating device 10 Crusher 11 Wind power sorter

Claims (5)

可燃性廃棄物を磁着物と非磁着物とに分離する磁力選別機と、
該磁力選別機から排出される磁着物を加熱する加熱装置と、
該加熱装置から排出される加熱物を破砕する破砕機と、
該破砕機から排出される破砕物を重産物と軽産物とに分離する風力選別機又は/及び比重選別機とを備えることを特徴とする可燃性廃棄物の処理装置。
A magnetic sorter that separates combustible waste into magnetic and non-magnetic materials,
A heating device that heats the magnetic material discharged from the magnetic force sorter,
A crusher that crushes the heated material discharged from the heating device, and
A combustible waste treatment apparatus comprising a wind power sorter and / or a specific gravity sorter that separates crushed matter discharged from the crusher into heavy products and light products.
前記可燃性廃棄物を磁着物と非磁着物とに分離する磁力選別機は、吊り下げ式磁力選別機と、該吊り下げ式磁力選別機の後段に該吊り下げ式磁力選別機が分離した非磁着物を磁着物と非磁着物とに分離するドラム式又はプーリー式磁力選別機であって、
前記加熱装置は、該ドラム式又はプーリー式磁力選別機から排出される磁着物を加熱することを特徴とする請求項1に記載の可燃性廃棄物の処理装置。
The magnetic force sorter for separating the combustible waste into a magnetic substance and a non-magnetic material is a suspension type magnetic force sorter and a non-suspension type magnetic force sorter separated after the suspension type magnetic force sorter. A drum-type or pulley-type magnetic force sorter that separates a magnetic material into a magnetic material and a non-magnetic material.
The combustible waste treatment device according to claim 1, wherein the heating device heats a magnetic material discharged from the drum type or pulley type magnetic force sorter.
前記吊り下げ式磁力選別機の前段に、前記可燃性廃棄物を2粒群又は3粒群以上に分離する篩選別手段を備え、
前記吊り下げ式磁力選別機は、前記2粒群又は3粒群以上の各々の可燃性廃棄物を磁着物と非磁着物とに分離し、
前記ドラム式又はプーリー式磁力選別機は、前記吊り下げ式磁力選別機から排出される2粒群又は3粒群以上の非磁着物の各々を磁着物と非磁着物とに分離し、
前記加熱装置は、前記ドラム式又はプーリー式磁力選別機から排出される2粒群又は3粒群以上の磁着物を一緒に加熱することを特徴とする請求項2に記載の可燃性廃棄物の処理装置。
A sieve sorting means for separating the combustible waste into a group of 2 grains or a group of 3 grains or more is provided in front of the suspension type magnetic force sorter.
The suspension-type magnetic force sorter separates each combustible waste of the two-grain group or the three-grain group or more into a magnetic substance and a non-magnetic substance.
The drum-type or pulley-type magnetic force sorter separates each of the two-grain group or three-grain group or more non-magnetic material discharged from the suspension-type magnetic force sorter into a magnetic material and a non-magnetic material.
The combustible waste according to claim 2, wherein the heating device heats together two or three or more magnetic particles discharged from the drum-type or pulley-type magnetic force sorter. Processing equipment.
前記ドラム式又はプーリー式磁力選別機の後段に、該磁力選別機から排出される2粒群又は3粒群以上の非磁着物の各々を導電産物と非導電産物とに分離する渦電流選別機を備えることを特徴とする請求項3に記載の可燃性廃棄物の処理装置。 An eddy current sorter that separates each of the two-grain group or three-grain group or more non-magnetic particles discharged from the magnetic force sorter into a conductive product and a non-conductive product after the drum-type or pulley-type magnetic force sorter. The combustible waste treatment apparatus according to claim 3, further comprising: 可燃性廃棄物を磁力選別によって磁着物と非磁着物とに分離し、
該磁力選別によって分離された磁着物を加熱し、
該加熱物を破砕し、
該破砕物を風力選別又は/及び比重選別によって重産物と軽産物とに分離することを特徴とする可燃性廃棄物の処理方法。
Combustible waste is separated into magnetic and non-magnetic materials by magnetic sorting.
The magnetic material separated by the magnetic force sorting is heated to heat it.
The heated material is crushed and
A method for treating combustible waste, which comprises separating the crushed material into heavy products and light products by wind power sorting and / or specific gravity sorting.
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JP2018034143A (en) 2016-08-29 2018-03-08 太平洋セメント株式会社 Shredder dust recycling method
JP2018164882A (en) 2017-03-28 2018-10-25 太平洋セメント株式会社 Valuable metal recovery method
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