JP2021003661A - Treatment apparatus and treatment method for incineration bottom ash - Google Patents

Treatment apparatus and treatment method for incineration bottom ash Download PDF

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JP2021003661A
JP2021003661A JP2019117151A JP2019117151A JP2021003661A JP 2021003661 A JP2021003661 A JP 2021003661A JP 2019117151 A JP2019117151 A JP 2019117151A JP 2019117151 A JP2019117151 A JP 2019117151A JP 2021003661 A JP2021003661 A JP 2021003661A
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main ash
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JP7143255B2 (en
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洸 瀧澤
Akira Takizawa
洸 瀧澤
智典 竹本
Tomonori Takemoto
智典 竹本
恭宗 武藤
Yasumune Muto
恭宗 武藤
泰之 石田
Yasuyuki Ishida
泰之 石田
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Taiheiyo Cement Corp
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Abstract

To effectively utilize an incineration bottom ash as a cement raw material and a raw material for refining while reducing treatment cost.SOLUTION: A treatment apparatus 1 for an incineration bottom ash includes: a magnetic separator 4 for separating incineration bottom ash into a magnetized material B and a non-magnetized material B; and a blowing separator 6 for separating the magnetized material B discharged from the magnetic separator 4 into a light product and a heavy product. The magnetic separator 4 may be a drum type magnetic separator having a magnet with a magnetic flux density of 1,500 gauss or more, and the blowing separator 6 can be a vertical type zigzag blowing separator. A drier 5 for drying the magnetized material B separated by the magnetic separator 4 is provided between the magnetic separator 4 and the blowing separator 6, and the blowing separator 6 can separate the magnetized material (dried material) dried by the drier 5 into a light product and a heavy product. A suspension type magnetic separator 2 having a magnet with a magnetic flux density of 1,000 gauss or more and 2,000 gauss or less is provided in front of the magnetic separator 4, and the magnetic separator 4 can separate the non-magnetized material A separated by the suspension type magnetic separator 2 into the magnetized material B and the non-magnetized material B.SELECTED DRAWING: Figure 1

Description

本発明は、都市ごみ焼却炉等で発生した焼却主灰をセメント原料及び精錬用原料として有効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 effectively utilizing incinerator ash generated in an urban waste incinerator or the like as a raw material for cement and a raw material for refining.

都市ごみなどの廃棄物は焼却処理され、焼却によって生ずる焼却灰は、従来埋立処分場で埋立処分されている。しかし、近年では、埋立処分場の枯渇のおそれに鑑み、焼却灰を有効利用する試みがなされている。特に、天然原料の代替としてセメント原料へ有効利用する試みが積極的になされている。 Waste such as municipal waste is incinerated, and the incinerated ash generated by incineration is conventionally landfilled at a landfill site. However, in recent years, in view of the risk of depletion of landfill sites, attempts have been made to effectively use incineration ash. In particular, attempts are being made to effectively use it as a cement raw material as a substitute for natural raw materials.

一方、都市ごみ焼却灰にはクロム(Cr)などの忌避成分や銅(Cu)などのセメント製造に不要な重金属も含まれる。特に焼却主灰のクロム濃度が高い場合には、セメント原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、焼却主灰のセメント原料としての利用が事実上制限されていた。そこで、安定して焼却主灰をセメント資源化するためには、クロムなどの忌避成分及びその他不要成分を前処理により低減することが好ましい。 On the other hand, municipal waste incineration ash also contains repellent components such as chromium (Cr) and heavy metals such as copper (Cu) that are unnecessary for cement production. In particular, when the chromium concentration of the incineration main ash is high, the amount of the incineration main ash used as a cement raw material may have to be reduced, and the use of the incineration main ash as a cement raw material has been practically restricted. Therefore, in order to stably convert the incinerated main ash into a cement resource, it is preferable to reduce repellent components such as chromium and other unnecessary components by pretreatment.

都市ごみ主灰からの重金属の分離技術として、例えば特許文献1には、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 separating heavy metals from municipal waste main ash, for example, in Patent Document 1, incineration main ash is separated into magnetic and non-magnetic deposits by magnetic force sorting, and the separated non-magnetic deposit is used as a cement firing device. It is described that it is used as a cement raw material with a reduced chromium content.

上記発明は有効であるが、焼却主灰を磁力選別して得られた磁着物、特にドラム式や、ロール式磁選機で回収される細粒物には灰が付着しているため、この灰によって磁着物の品位が低下し、磁着物を精錬用原料として利用し難いという問題があった。 Although the above invention is effective, this ash is attached to the magnetic material obtained by magnetically separating the main ash to be incinerated, especially the fine particles collected by the drum type or roll type magnetic separator. As a result, the quality of the magnetic material deteriorates, and there is a problem that it is difficult to use the magnetic material as a raw material for refining.

一方、特許文献2には、不純物の含有量が少なく、鉄の含有量が多く、再資源化が可能な鉄資源を効率的に回収するため、焼却残渣から鉄くずを磁力選別し、磁力選別した鉄くずに高圧の水を噴射し、鉄くずに付着している不純物を除去する技術が記載されている。 On the other hand, in Patent Document 2, in order to efficiently recover iron resources having a low impurity content and a high iron content and which can be recycled, iron scrap is magnetically sorted from the incineration residue and magnetically sorted. A technique for injecting high-pressure water onto the scrap iron to remove impurities adhering to the scrap iron is described.

また、特許文献3には、高速旋回する多段方式の鎖の打撃によって被破砕物を破砕処理する縦型円筒状の破砕室を有し、この破砕室の下部に熱風又は空気を旋回流として供給する鎖打撃式破砕乾燥機を用い、磁選機で回収した磁着物を乾式洗浄する技術が開示されている。 Further, Patent Document 3 has a vertical cylindrical crushing chamber for crushing a material to be crushed by hitting a multi-stage chain that swirls at high speed, and hot air or air is supplied as a swirling flow to the lower part of the crushing chamber. Disclosed is a technique for dry-cleaning a magnetic material recovered by a magnetic separator using a chain striking crushing dryer.

特開2017−137224号公報JP-A-2017-137224 特開2008−1931号公報Japanese Unexamined Patent Publication No. 2008-1931 特開2008−178808号公報Japanese Unexamined Patent Publication No. 2008-178808

しかし、上記特許文献2に記載の発明は、高圧の水を用いて湿式洗浄を行うため、水処理設備が必要になり、特許文献3に記載の発明は、磁着物の破砕による破砕乾燥機の磨耗が激しく、定期的なメンテナンスが必要になるため、いずれも処理コストが高くなるという問題があった。 However, the invention described in Patent Document 2 requires a water treatment facility because wet cleaning is performed using high-pressure water, and the invention described in Patent Document 3 is a crushing dryer for crushing a magnetic material. There is a problem that the processing cost is high in each case because the wear is severe and regular maintenance is required.

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、処理コストを低く抑えながら、焼却主灰をセメント原料及び精錬用原料と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 utilize the incineration main ash as a raw material for cement and a raw material for refining while keeping the processing cost low.

上記目的を達成するため、本発明は、焼却主灰の処理装置であって、焼却主灰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軽産物と重産物とに分離する風力選別機とを備えることを特徴とする。 In order to achieve the above object, the present invention is an incineration main ash processing apparatus, which is a magnetic force sorter that separates the incineration main ash into a magnetic material and a non-magnetic material, and a magnetic material discharged from the magnetic force sorter. It is characterized by being equipped with a wind sorter that separates light products and heavy products.

本発明によれば、磁力選別機の後段の風力選別機により磁着物を軽産物と重産物とに分離するため、湿式洗浄機や破砕乾燥機を用いずに、処理コストを低く抑えながら、焼却主灰をセメント原料及び精錬用原料として有効利用することができる。 According to the present invention, since the magnetic cement is separated into light products and heavy products by the wind power sorter in the subsequent stage of the magnetic force sorter, incineration is performed while keeping the processing cost low without using a wet washing machine or a crushing dryer. The main ash can be effectively used as a raw material for cement and a raw material for refining.

上記焼却主灰の処理装置において、前記磁力選別機として、磁束密度が1500ガウス以上5000ガウス以下の磁石を有するドラム式磁力選別機を用いることができる。また、前記風力選別機として、縦型のジグザグ風力選別機を用いることができる。 In the incineration main ash processing apparatus, a drum type magnetic force sorter having a magnet having a magnetic flux density of 1500 gauss or more and 5000 gauss or less can be used as the magnetic force sorter. Further, as the wind power sorter, a vertical zigzag wind power sorter can be used.

上記焼却主灰の処理装置において、前記磁力選別機と前記風力選別機の間に、前記磁力選別機で分離された磁着物を乾燥させる乾燥機を設け、前記風力選別機は、該乾燥機で乾燥された磁着物を軽産物と重産物とに分離することで、風力選別機の分離効率を高めることができる。 In the incineration main ash processing apparatus, a dryer for drying the magnetic deposits separated by the magnetic force sorter is provided between the magnetic force sorter and the wind power sorter, and the wind power sorter is the dryer. By separating the dried magnetic material into light products and heavy products, the separation efficiency of the wind power sorter can be improved.

上記焼却主灰の処理装置において、前記磁力選別機の前段に、1000ガウス以上2000ガウス以下の磁束密度の磁石を有する吊下げ式磁力選別機を設け、前記磁力選別機(吊下げ式磁力選別機ではない磁力選別機)は、該吊下げ式磁力選別機で分離された非磁着物を磁着物と非磁着物とに分離するように構成することで、比較的大きな磁着物を予め除去し、比較的大きな磁着物が存在することでその他の非磁着物が後段の磁力選別機で比較的大きな磁着物に巻き込まれる形で磁着物側に回収され難くなるおそれを回避し、磁着物の品位やクロムの分離効率を高めることができる。 In the incineration main ash processing apparatus, a hanging magnetic sorter having a magnet having a magnetic flux density of 1000 gauss or more and 2000 gauss or less is provided in front of the magnetic sorter, and the magnetic sorter (suspended magnetic sorter). The magnetic sorter (not a magnetic sorter) is configured to separate the non-magnetic deposits separated by the hanging magnetic sorter into a magnetic deposit and a non-magnetic deposit, thereby removing relatively large magnetic deposits in advance. The presence of a relatively large magnetic substance avoids the risk that other non-magnetic objects will be caught in the relatively large magnetic object by the magnetic sorter in the subsequent stage and will not be easily collected on the magnetic object side. The separation efficiency of chromium can be increased.

上記焼却主灰の処理装置において、前記吊下げ式磁力選別機の後段に、該吊下げ式磁力選別機で分離された非磁着物を篩上物と篩下物とに分離する篩選別機を設け、前記磁力選別機(吊下げ式磁力選別機ではない磁力選別機)は、該篩選別機で分離された篩下物を磁着物と非磁着物とに分離することで、磁力選別機の前段で比較的大きな物を予め回収し、磁着物の品位やクロムの分離効率をさらに高めることができる。 In the incineration main ash processing apparatus, a sieving machine that separates the non-magnetic material separated by the hanging magnetic force sorter into a sieving product and a sieving material is provided after the hanging type magnetic force sorting machine. The magnetic force sorter (a magnetic force sorter that is not a hanging type magnetic force sorter) is provided by separating the undersieved material separated by the sieve sorter into a magnetic material and a non-magnetic material. A relatively large object can be collected in advance in the previous stage to further improve the quality of the magnetic object and the separation efficiency of chromium.

また、本発明は、焼却主灰の処理方法であって、焼却主灰を磁着物と非磁着物とに磁力選別し、該磁力選別で得られた磁着物を軽産物と重産物とに風力選別し、該風力選別で得られた軽産物をセメント原料として用い、該風力選別で得られた重産物を精錬用原料として用いることを特徴とする。本発明によれば、湿式洗浄機や破砕乾燥機を用いずに、処理コストを低く抑えながら、焼却主灰をセメント原料及び精錬用原料として有効利用することができる。 Further, the present invention is a method for treating the main ash to be incinerated, in which the main ash to be incinerated is magnetically sorted into a magnetic material and a non-magnetic material, and the magnetic material obtained by the magnetic force selection is made into light products and heavy products by wind power. It is characterized in that light products obtained by sorting are used as a raw material for cement, and heavy products obtained by the wind sorting are used as a raw material for refining. According to the present invention, the main ash incinerated can be effectively used as a raw material for cement and a raw material for refining without using a wet washing machine or a crushing dryer while keeping the processing cost low.

以上のように、本発明によれば、処理コストを低く抑えながら、焼却主灰をセメント原料及び精錬用原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 incineration main ash can be effectively used as a cement raw material and a refining raw material while keeping the processing cost low.

本発明に係る焼却主灰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 incineration main ash 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。 Next, an embodiment of the present invention will be described in detail with reference to the drawings.

図1は、本発明に係る焼却主灰の処理装置の一実施の形態を示し、この処理装置1は、焼却主灰を磁力選別する磁力選別機(以下「磁選機」という。)2と、磁選機2によって分離された非磁着物Aを篩選別する篩選別機3と、篩選別機3によって分離された篩下物を磁力選別する磁選機4と、磁選機4によって分離された磁着物Bを乾燥させる乾燥機5と、乾燥機5から排出される乾燥物を軽産物と重産物とに分離する風力選別機6とを備える。 FIG. 1 shows an embodiment of an incinerator main ash processing device according to the present invention, in which the processing device 1 includes a magnetic force sorter (hereinafter referred to as “magnetic separator”) 2 for magnetically sorting incinerated main ash. A sieving machine 3 for sieving the non-magnetic material A separated by the magnetic separator 2, a magnetic separator 4 for magnetically sorting the sieving material separated by the sieving machine 3, and a magnetic material separated by the magnetic separator 4. A dryer 5 for drying B and a wind sorter 6 for separating the dried product discharged from the dryer 5 into light products and heavy products are provided.

磁選機2は、焼却主灰に含まれる比較的大きな磁着物Aを予め除去し、後段での磁力選別等を効果的に行うために設けられ、1000ガウス以上2000ガウス以下の磁束密度を有する磁石を備える吊下げ式磁力選別機等を用いることができる。 The magnetic separator 2 is provided to remove a relatively large magnetic deposit A contained in the incineration main ash in advance and effectively perform magnetic force selection in the subsequent stage, and is a magnet having a magnetic flux density of 1000 gauss or more and 2000 gauss or less. A hanging magnetic flux sorter or the like can be used.

篩選別機3も、磁選機2と同様に、焼却主灰に含まれる比較的大きな物を予め除去し、後段での磁力選別等を効果的に行うために設けられ、篩目が25mm以上のものを用いることができる。 Similar to the magnetic separator 2, the sieve sorter 3 is also provided to remove relatively large substances contained in the incinerator main ash in advance and effectively perform magnetic separation in the subsequent stage, and has a sieve mesh of 25 mm or more. Can be used.

磁選機4は、篩選別機3の篩下物から磁着物Bを回収するために設けられ、1500ガウス以上5000ガウス以下の磁束密度の磁石を有するドラム式磁力選別機を用いることができる。 The magnetic separator 4 is provided to recover the magnetic material B from the sieve material of the sieve sorter 3, and a drum type magnetic force sorter having a magnet having a magnetic flux density of 1500 gauss or more and 5000 gauss or less can be used.

乾燥機5は、磁選機4によって分離された磁着物Bを乾燥させて風力選別機6の分離効率を高めるために設けられ、ロータリードライヤ等を用いることができる。 The dryer 5 is provided to dry the magnetic material B separated by the magnetic separator 4 to improve the separation efficiency of the wind power sorter 6, and a rotary dryer or the like can be used.

風力選別機6は、乾燥機5による乾燥物を軽産物と重産物とに分離するために設けられ、選別精度の高い縦型のジグザグ風力選別機を用いることができる。 The wind power sorter 6 is provided to separate the dried product from the dryer 5 into light products and heavy products, and a vertical zigzag wind power sorter with high sorting accuracy can be used.

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 device 1 having the above configuration will be described with reference to FIG.

受け入れた焼却主灰に含まれる比較的大きな磁着物Aを磁選機2で除去し、磁選機2によって選別された非磁着物Aを篩選別機3で篩い、比較的大きな物を篩上物として除去する。篩上物は、スクラップとして再資源化することができる。篩選別機3の篩下物を磁選機4に供給して磁着物Bと非磁着物Bとに分離し、非磁着物Bをセメント原料として利用する。 The relatively large magnetic material A contained in the received incineration main ash is removed by the magnetic separator 2, the non-magnetic material A sorted by the magnetic separator 2 is sieved by the sieve sorter 3, and the relatively large material is used as a sieve. Remove. The sieved material can be recycled as scrap. The sieve material of the sieving machine 3 is supplied to the magnetic separator 4 to separate the magnetic material B and the non-magnetic material B, and the non-magnetic material B is used as a cement raw material.

さらに、磁着物Bを乾燥機5に供給し、水分が15%以下程度になるまで乾燥させ、乾燥機による乾燥物を風力選別機6に供給し、軽産物及び重産物に分離し、重産物を精錬用原料として利用する。 Further, the magnetic substance B is supplied to the dryer 5, dried until the water content is about 15% or less, and the dried product by the dryer is supplied to the wind power sorter 6, separated into light products and heavy products, and the heavy products are separated. Is used as a raw material for refining.

上述のように、本実施の形態によれば、湿式洗浄機や破砕機を用いずに、磁着物Bをセメント原料と精錬用原料に効率よく分離して有効利用することができる。 As described above, according to the present embodiment, the magnetic deposit B can be efficiently separated into a cement raw material and a refining raw material and effectively used without using a wet washing machine or a crusher.

次に、本発明の実施例について説明する。 Next, examples of the present invention will be described.

都市ごみ焼却主灰(原灰)204kgを上記処理装置1で処理した。本実施例では磁選機2は1000ガウスの磁石密度を有する磁石を備える吊下げ式磁力選別機等を用いた。篩選別機3は、篩目を35mmに設定した。磁選機4は1500ガウスの磁石密度を有する磁石を備えるドラム式磁力選別機等を用いた。風力選別機6はジグザグ式風力選別機を用いた。焼却主灰及び各工程での分離物の重量割合、水分、クロム濃度(化学組成)、クロム含有量及び分配率を表1に示す。重量割合は原灰の重量を100としたときの各分離物の重量割合を示した。水分は105℃にて重量が恒量となるまで加熱した際の減少量から算出した。クロム濃度はマット融解処理を行った後100μm以下まで微粉砕した試料に対し、吸光光度法又はICP発光分光法によって定量した。クロム分配率は各分離物の重量割合とクロム濃度分析結果から推定した。 204 kg of municipal waste incineration main ash (raw ash) was treated by the above treatment device 1. In this embodiment, the magnetic separator 2 uses a hanging magnetic sorter or the like equipped with a magnet having a magnet density of 1000 gauss. The sieve sorter 3 set the sieve mesh to 35 mm. As the magnetic separator 4, a drum-type magnetic force sorter or the like equipped with a magnet having a magnet density of 1500 gauss was used. As the wind power sorter 6, a zigzag type wind power sorter was used. Table 1 shows the weight ratio, water content, chromium concentration (chemical composition), chromium content and distribution rate of the incinerated main ash and the separated product in each step. The weight ratio is the weight ratio of each separated product when the weight of the raw ash is 100. Moisture was calculated from the amount of decrease when heated at 105 ° C. until the weight became constant. The chromium concentration was quantified by absorptiometry or ICP emission spectroscopy on a sample that was finely pulverized to 100 μm or less after mat melting treatment. The chromium distribution ratio was estimated from the weight ratio of each isolate and the results of the chromium concentration analysis.

Figure 2021003661
Figure 2021003661

表1より、セメント原料として利用する非磁着物Bのクロム分配率は、57.7%であり、焼却主灰に含まれるクロムの1/2程度を除去でき、焼却主灰から効率的にクロムを除去できることが判る。 From Table 1, the chromium distribution ratio of the non-magnetic deposit B used as a cement raw material is 57.7%, and about 1/2 of the chromium contained in the incineration main ash can be removed, and chromium is efficiently removed from the incineration main ash. It turns out that can be removed.

また、磁着物Bを風力選別機6の風速を変えて風力選別した。風力選別機6の風力選別による重産物中の磁着物と灰(軽産物)の重量割合を表2に示す。 Further, the magnetic material B was wind-sorted by changing the wind speed of the wind power sorter 6. Table 2 shows the weight ratio of the magnetic substance and the ash (light product) in the heavy products obtained by the wind power sorting of the wind power sorter 6.

Figure 2021003661
Figure 2021003661

表2より、風速2m/s以上の条件で風力選別を行うことにより、磁着物中に10%程度付着していた灰を5%以下まで低減できることが分かる。また、風速が高い程、灰の除去率が高まることが分かる。 From Table 2, it can be seen that the ash adhering to about 10% in the magnetic material can be reduced to 5% or less by performing wind sorting under the condition of a wind speed of 2 m / s or more. It can also be seen that the higher the wind speed, the higher the ash removal rate.

以上のように、本実施の形態によれば、クロム含有率の低い非磁着物Bをセメント原料として有効利用することができ、クリンカのクロム含有率を低く維持することができる。また、磁着物含有率の高い重産物を精錬用原料として有効利用することができる。 As described above, according to the present embodiment, the non-magnetic deposit B having a low chromium content can be effectively used as a cement raw material, and the chromium content of clinker can be kept low. In addition, heavy products having a high content of magnetic deposits can be effectively used as raw materials for refining.

尚、上記実施の形態では、焼却主灰に含まれる比較的大きな磁着物等を除去するため、磁選機2及び篩選別機3を設けたが、受け入れた焼却主灰の性状等によっては、これらを省略したり、いずれか一方のみを用いることができる。 また、磁選機2及び篩選別機3の種類、磁石の磁束密度、篩目の大きさについても、上記のものに限定されない。 In the above embodiment, a magnetic separator 2 and a sieve sorter 3 are provided in order to remove relatively large magnetic deposits and the like contained in the incinerator main ash. However, depending on the properties of the received incinerator main ash and the like, these are provided. Can be omitted or only one of them can be used. Further, the types of the magnetic separator 2 and the sieve sorter 3, the magnetic flux density of the magnet, and the size of the mesh are not limited to the above.

さらに、磁選機4の種類、磁石の磁束密度についても上記のものに限定されない。また、乾燥機5を設けることで後段の風力選別機6の分離効率を高めることができて好ましいが、磁着物Bの水分が既に15%以下程度の場合には、これを省略することもできる。 Further, the type of the magnetic separator 4 and the magnetic flux density of the magnet are not limited to the above. Further, it is preferable to provide the dryer 5 because the separation efficiency of the wind power sorter 6 in the subsequent stage can be improved, but this can be omitted when the water content of the magnetic substance B is already about 15% or less. ..

1 焼却主灰の処理装置
2 磁選機
3 篩選別機
4 磁選機
5 乾燥機
6 風力選別機
1 Incinerator main ash processing device 2 Magnetic separator 3 Sieving separator 4 Magnetic separator 5 Dryer 6 Wind separator

Claims (7)

焼却主灰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軽産物と重産物とに分離する風力選別機とを備えることを特徴とする焼却主灰の処理装置。
A magnetic sorter that separates the main ash from incineration into magnetic and non-magnetic materials,
An incinerator main ash processing apparatus comprising a wind power sorter for separating magnetic deposits discharged from the magnetic force sorter into light products and heavy products.
前記磁力選別機は、磁束密度が1500ガウス以上5000ガウス以下の磁石を有するドラム式磁力選別機であることを特徴とする請求項1に記載の焼却主灰の処理装置。 The incinerator main ash processing apparatus according to claim 1, wherein the magnetic force sorter is a drum type magnetic force sorter having a magnet having a magnetic flux density of 1500 gauss or more and 5000 gauss or less. 前記風力選別機は、縦型のジグザグ風力選別機であることを特徴とする請求項1又は2に記載の焼却主灰の処理装置。 The incinerator main ash processing device according to claim 1 or 2, wherein the wind power sorter is a vertical zigzag wind power sorter. 前記磁力選別機と前記風力選別機の間に、前記磁力選別機で分離された磁着物を乾燥させる乾燥機を備え、
前記風力選別機は、該乾燥機で乾燥された磁着物を軽産物と重産物とに分離することを特徴とする請求項1、2又は3に記載の焼却主灰の処理装置。
A dryer for drying the magnetic material separated by the magnetic force sorter is provided between the magnetic force sorter and the wind power sorter.
The incinerator main ash processing apparatus according to claim 1, 2 or 3, wherein the wind power sorter separates a magnetic substance dried by the dryer into a light product and a heavy product.
前記磁力選別機の前段に、1000ガウス以上2000ガウス以下の磁束密度の磁石を有する吊下げ式磁力選別機を備え、
前記磁力選別機(吊下げ式磁力選別機ではない磁力選別機)は、該吊下げ式磁力選別機で分離された非磁着物を磁着物と非磁着物とに分離することを特徴とする請求項1乃至4のいずれかに記載の焼却主灰の処理装置。
A hanging magnetic force sorter having a magnet having a magnetic flux density of 1000 gauss or more and 2000 gauss or less is provided in front of the magnetic force sorter.
The magnetic force sorter (a magnetic force sorter that is not a hanging type magnetic force sorter) is characterized in that the non-magnetic material separated by the hanging type magnetic force sorter is separated into a magnetic material and a non-magnetic material. Item 4. The incineration main ash processing apparatus according to any one of Items 1 to 4.
前記吊下げ式磁力選別機の後段に、該吊下げ式磁力選別機で分離された非磁着物を篩上物と篩下物とに分離する篩選別機を備え、
前記磁力選別機(吊下げ式磁力選別機ではない磁力選別機)は、該篩選別機で分離された篩下物を磁着物と非磁着物とに分離することを特徴とする請求項5に記載の焼却主灰の処理装置。
A sieving sorter for separating the non-magnetic material separated by the hanging magnetic sorter into a sieving object and a sieving object is provided after the suspension type magnetic force sorting machine.
The fifth aspect of the invention is characterized in that the magnetic force sorter (a magnetic force sorter that is not a hanging type magnetic force sorter) separates the undersieved material separated by the sieve sorter into a magnetic material and a non-magnetic material. The described incineration main ash processing apparatus.
焼却主灰を磁着物と非磁着物とに磁力選別し、
該磁力選別で得られた磁着物を軽産物と重産物とに風力選別し、
該風力選別で得られた軽産物をセメント原料として用い、
該風力選別で得られた重産物を精錬用原料として用いることを特徴とする焼却主灰の処理方法。
The main ash to be incinerated is magnetically sorted into magnetic and non-magnetic materials.
The magnetic deposits obtained by the magnetic force sorting are wind-sorted into light products and heavy products.
Using the light products obtained by the wind power sorting as a cement raw material,
A method for treating incineration main ash, which comprises using the heavy products obtained by the wind power sorting as a raw material for refining.
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Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH09236224A (en) * 1995-12-28 1997-09-09 Mitsui Eng & Shipbuild Co Ltd Method for treating big refuse
JP2003120921A (en) * 2001-10-10 2003-04-23 Kubota Corp Iron recovery system
JP2003236837A (en) * 2002-02-18 2003-08-26 Jfe Engineering Kk Method for recycling shredder dust of scrapped automobile and installation therefor
JP2008178808A (en) * 2007-01-25 2008-08-07 Shin Nihonkai Jukogyo Kk Dry washing method for iron component with incineration ash
JP2016089196A (en) * 2014-10-30 2016-05-23 太平洋セメント株式会社 Valuable metal recovery method and valuable metal recovery system
JP2017137224A (en) * 2016-02-05 2017-08-10 太平洋セメント株式会社 Method for treating incineration main ash

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH09236224A (en) * 1995-12-28 1997-09-09 Mitsui Eng & Shipbuild Co Ltd Method for treating big refuse
JP2003120921A (en) * 2001-10-10 2003-04-23 Kubota Corp Iron recovery system
JP2003236837A (en) * 2002-02-18 2003-08-26 Jfe Engineering Kk Method for recycling shredder dust of scrapped automobile and installation therefor
JP2008178808A (en) * 2007-01-25 2008-08-07 Shin Nihonkai Jukogyo Kk Dry washing method for iron component with incineration ash
JP2016089196A (en) * 2014-10-30 2016-05-23 太平洋セメント株式会社 Valuable metal recovery method and valuable metal recovery system
JP2017137224A (en) * 2016-02-05 2017-08-10 太平洋セメント株式会社 Method for treating incineration main ash

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