JP7137532B2 - Metal-containing waste treatment apparatus and treatment method - Google Patents

Metal-containing waste treatment apparatus and treatment method Download PDF

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JP7137532B2
JP7137532B2 JP2019114406A JP2019114406A JP7137532B2 JP 7137532 B2 JP7137532 B2 JP 7137532B2 JP 2019114406 A JP2019114406 A JP 2019114406A JP 2019114406 A JP2019114406 A JP 2019114406A JP 7137532 B2 JP7137532 B2 JP 7137532B2
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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、金属含有廃棄物の処理装置及び処理方法に関し、特に、焼却灰やシュレッダーダスト等から主に貴金属を回収する技術に関する。 TECHNICAL FIELD The present invention relates to a treatment apparatus and treatment method for metal-containing waste, and more particularly to a technique for mainly recovering precious metals from incineration ash, shredder dust, and the like.

焼却灰等の廃棄物から貴金属等の有価金属を回収するため、特許文献1には、焼却灰等を予備処理した後、竪型ローラーミルの操業条件を調整し、貴金属をミル排石側へ移行させて回収する技術が記載されている。 In order to recover valuable metals such as precious metals from waste such as incineration ash, Patent Document 1 discloses that after pretreatment of incineration ash, etc., the operating conditions of a vertical roller mill are adjusted, and precious metals are transferred to the stone discharge side of the mill. Techniques for migration and recovery are described.

一方、シュレッダーダスト等から貴金属等を回収するため、特許文献2には、シュレッダーダストの加熱物を選別処理し、エアテーブルで分離した重産物に貴金属等を濃縮させて回収する技術が記載されている。 On the other hand, in order to recover precious metals and the like from shredder dust and the like, Patent Document 2 describes a technique for sorting heated shredder dust and concentrating precious metals and the like in heavy products separated by an air table and recovering them. there is

特許第6375205号公報Japanese Patent No. 6375205 特開2018-164872号公報JP 2018-164872 A

上記特許文献1及び2に記載の発明において、貴金属等を濃縮させたミル排石や重産物には、アルミニウム(純Al、Al合金)や、ガラス等の密度3t/m3以下の粒子が混入していたり、粒子表面に灰やガラスが付着することがある。例えば、特許文献1のミル排石には20%以上のアルミニウムが含まれ、特許文献2の重産物には数%のアルミニウムが含まれている。そのため、ミル排石や重産物の貴金属の品位が低下するおそれがあった。 In the inventions described in Patent Documents 1 and 2 above, mill effluent and heavy products in which precious metals and the like are concentrated contain particles of aluminum (pure Al, Al alloy) and glass with a density of 3 t/m 3 or less. ash or glass may adhere to the surface of the particles. For example, the mill scum of Patent Document 1 contains 20% or more of aluminum, and the heavy product of Patent Document 2 contains several percent of aluminum. As a result, there is a possibility that the grade of precious metals in the mill waste and heavy products may be degraded.

そこで、上記重産物等をさらに軽産物と重産物に比重選別すると、軽産物に移行する貴金属の存在によって結果的に貴金属の回収率が低下することがある。例えば、比重選別でアルミニウムやガラスの混入を防止し、重産物の貴金属品位向上を図ると、重産物の回収量が少なくなり、結果的に回収率が低下するという問題がある。 Therefore, if the heavy products and the like are further sorted into light products and heavy products by specific gravity, the presence of the precious metals that migrate to the light products may result in a decrease in the recovery rate of the precious metals. For example, when the contamination of aluminum and glass is prevented by specific gravity sorting to improve the grade of precious metals in heavy products, the recovery amount of heavy products decreases, resulting in a problem of lower recovery rate.

また、渦電流選別で貴金属を多く含む導電産物を回収しようとした場合には、ガラスは非導電産物として除去できるが、アルミニウムは貴金属等と共に導電産物として回収されてしまう。特に、貴金属等に灰が付着している場合には、渦電流選別の効果は限定的となる。 Further, when trying to recover conductive products containing a large amount of precious metals by eddy current sorting, glass can be removed as non-conductive products, but aluminum is recovered as conductive products together with precious metals and the like. In particular, when ash adheres to precious metals, the effect of eddy current sorting is limited.

そこで、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、金属含有廃棄物から主に貴金属を効率よく回収することを目的とする。 SUMMARY OF THE INVENTION Accordingly, the present invention has been made in view of the above-described problems in the prior art, and an object of the present invention is to efficiently recover mainly precious metals from metal-containing waste.

上記目的を達成するため、本発明は、金属含有廃棄物の処理装置であって、金属含有廃棄物を選別処理して得られた貴金属濃縮物であって、Si(ケイ素)及びCa(カルシウム)の含有率の合計が5質量%以上30質量%以下、及びAl(アルミニウム)及びCu(銅)の含有率の合計が20質量%以上60質量%以下である貴金属濃縮物を磁力選別する磁力選別機と、該磁力選別機によって分離された非磁着物を破砕する破砕機と、該破砕機によって破砕された破砕物から微粒分を除去する選別機からなることを特徴とする。 In order to achieve the above object, the present invention provides a metal-containing waste treatment apparatus, which is a precious metal concentrate obtained by sorting metal-containing waste, comprising Si (silicon) and Ca (calcium) The total content of 5 mass% to 30 mass%, and the total content of Al (aluminum) and Cu (copper) is 20 mass% to 60 mass%. a crusher for crushing non-magnetic substances separated by the magnetic separator; and a separator for removing fine particles from the crushed material crushed by the crusher.

本発明によれば、貴金属濃縮物から、貴金属の品位を低下させる原因となるアルミニウム、ガラス、灰等の微粒分を除去することができるため、貴金属濃縮物の貴金属濃度を高めることができる。 According to the present invention, it is possible to remove fine particles such as aluminum, glass, and ash that cause deterioration of noble metal quality from the noble metal concentrate, so that the noble metal concentration of the noble metal concentrate can be increased.

上記金属含有廃棄物の処理装置に、前記選別機で分離された粗粒分を前記破砕機に戻す循環ルートを設け、粗粒分を再度破砕することで、回収する破砕物の貴金属濃度をさらに高めることができる。 The metal-containing waste treatment apparatus is provided with a circulation route that returns the coarse particles separated by the sorter to the crusher, and the coarse particles are crushed again to further increase the precious metal concentration of the crushed material to be recovered. can be enhanced.

また、本発明は、金属含有廃棄物の処理方法であって、金属含有廃棄物を選別処理して得られた貴金属濃縮物であって、Si及びCaの含有率の合計が5質量%以上30質量%以下、及びAl及びCuの含有率の合計が20質量%以上60質量%以下である貴金属濃縮物を磁力選別するステップと、該磁力選別によって得られた非磁着物を破砕するステップと、該破砕によって得られた破砕物から微粒分を除去するステップからなることを特徴とする。本発明によれば、貴金属濃縮物から、アルミニウム、ガラス、灰等の微粒分を除去することで、貴金属濃縮物の貴金属濃度を高めることができる。 The present invention also provides a method for treating metal-containing waste, which is a precious metal concentrate obtained by sorting metal-containing waste, wherein the total content of Si and Ca is 5% by mass or more and 30 a step of magnetically sorting a precious metal concentrate having a mass% or less and a total content of Al and Cu of 20 mass% or more and 60 mass% or less, and crushing a non-magnetic substance obtained by the magnetic sorting; It is characterized by comprising a step of removing fine particles from the crushed material obtained by the crushing. According to the present invention, the noble metal concentration of the noble metal concentrate can be increased by removing fine particles such as aluminum, glass, and ash from the noble metal concentrate.

上記金属含有廃棄物の処理方法において、前記微粒分を除去した後の粗粒分を再度破砕し、該破砕によって得られた破砕物から微粒分を除去することで、回収する破砕物の貴金属濃度をさらに高めることができる。 In the above method for treating metal-containing waste, the coarse particles after removing the fine particles are crushed again, and the fine particles are removed from the crushed material obtained by the crushing, so that the collected crushed material has a precious metal concentration. can be further increased.

以上のように、本発明によれば、金属含有廃棄物から主に貴金属を効率よく回収することができる。 As described above, according to the present invention, mainly noble metals can be efficiently recovered from metal-containing waste.

本発明に係る金属含有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。1 is a block diagram showing an embodiment of a metal-containing waste treatment apparatus according to the present invention; FIG.

次に、本発明に係る金属含有廃棄物の処理装置について図面を参照しながら詳細に説明する。 Next, the metal-containing waste treatment apparatus according to the present invention will be described in detail with reference to the drawings.

図1は、本発明に係る金属含有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、金属含有廃棄物を選別処理して得られた貴金属濃縮物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を破砕する破砕機3と、破砕機3によって破砕された破砕物から微粒分を除去する篩選別機4と、篩選別機4で分離された篩上物を破砕機3へ戻す循環ルート5とで構成される。 FIG. 1 shows an embodiment of a metal-containing waste treatment apparatus according to the present invention. This treatment apparatus 1 magnetically separates a precious metal concentrate obtained by sorting metal-containing waste. machine (hereinafter referred to as "magnetic separator") 2, a crusher 3 for crushing non-magnetic substances separated by the magnetic separator 2, and a sieve separator 4 for removing fine particles from the crushed material crushed by the crusher 3. and a circulation route 5 for returning the sieved material separated by the sieve sorter 4 to the crusher 3.

処理対象である貴金属濃縮物とは、焼却灰やシュレッダーダスト等の金属含有廃棄物を選別処理して貴金属を濃縮させたものであって、ケイ素(Si)及びカルシウム(Ca)の含有率の合計が5質量%以上30質量%以下、好ましくは5質量%以上20質量%以下、Al及び銅(Cu)の含有率の合計が20質量%以上60質量%以下、好ましくは30質量%以上50質量%以下、及び平均粒径が10mm以下のものをいう。 Precious metal concentrates to be treated are wastes containing metals such as incineration ash and shredder dust that are sorted and processed to concentrate precious metals, and are the total content of silicon (Si) and calcium (Ca). is 5% by mass to 30% by mass, preferably 5% by mass to 20% by mass, and the total content of Al and copper (Cu) is 20% by mass to 60% by mass, preferably 30% by mass to 50% by mass. % or less, and mean particle size is 10 mm or less.

磁選機2は、貴金属濃縮物を磁着物と非磁着物に分離するために設けられ、好ましくは吊り下げ式であって、磁石の磁束密度が700ガウス以上5000ガウス以下のものを用いることができる。 The magnetic separator 2 is provided to separate the precious metal concentrate into magnetic substances and non-magnetic substances, preferably of a hanging type, and a magnetic flux density of 700 gauss or more and 5000 gauss or less can be used. .

破砕機3は、非磁着物の粒子表面からAl、Si及びCaの粒子を剥離させるために設けられ、破砕方式は特に限定されず、乾式、湿式を問わない。但し、装置が磨耗したり、篩選別機4で貴金属が微粒分側へ移行する上で適さないので、過粉砕となるものは避ける。尚、湿式の破砕機を用いたとしても、処理対象である非磁着物は金属、スラグ、ガラスが主体であり、溶出成分は少ないため、水処理の付加は大きくない。 The crusher 3 is provided to separate the particles of Al, Si and Ca from the surfaces of the non-magnetic particles, and the crushing method is not particularly limited, regardless of whether it is a dry method or a wet method. However, over-pulverization should be avoided because it wears out the equipment and is not suitable for shifting the noble metal to the fine particle side in the sieve separator 4 . Even if a wet crusher is used, the non-magnetic substances to be treated are mainly metal, slag, and glass, and the amount of eluted components is small, so the addition of water treatment is not large.

篩選別機4は、粒径が0.5mm程度以下の微粒分を除去するために設けられる。篩選別機4の代わりに、分級機や、風力選別機を用いてもよい。 The sieve separator 4 is provided to remove fine particles having a particle size of about 0.5 mm or less. Instead of the sieve sorter 4, a classifier or a wind sorter may 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 apparatus 1 having the above configuration will be described with reference to FIG.

受け入れた貴金属濃縮物に含まれる磁着物を磁選機2で除去し、磁選機2から排出される非磁着物を破砕機3で破砕する。破砕機3から排出され、Al、Si及びCaを多く含む微粒分を篩下物として篩選別機4で除去する。 Magnetic substances contained in the received precious metal concentrate are removed by a magnetic separator 2, and non-magnetic substances discharged from the magnetic separator 2 are crushed by a crusher 3. Fine particles discharged from the crusher 3 and containing a large amount of Al, Si and Ca are removed by the sieve separator 4 as under-sieved material.

循環ルートを介し、篩選別機4で分離された粗粒分を篩上物として破砕機3へ戻し、破砕機3による破砕と、篩選別機4による篩選別を繰り返し行う。 Through the circulation route, the coarse particles separated by the sieve separator 4 are returned to the crusher 3 as the sieved material, and the crushing by the crusher 3 and the sieve separation by the sieve separator 4 are repeated.

上述のようにして最終的に粗粒分を篩上物として回収することで、回収する篩上物の貴金属品位を高めることができる。 By finally recovering the coarse particles as the screened material as described above, it is possible to increase the precious metal quality of the collected screened material.

次に、本発明の試験例について説明する。 Next, test examples of the present invention will be described.

試料1として、焼却灰を選別処理した貴金属濃縮物を、試料2として、シュレッダーダストの加熱物を選別処理した貴金属濃縮物を用い、各試料100gについて磁力選別(磁束密度1000ガウス)を行ってワイヤー等の異物を除去した後、粉砕機(WARING社製、MX1200XTM(破砕容器CAC90B))で、固液比1:5で水洗・破砕した。10秒間破砕した後、0.5mmの篩目で篩い分けた。各篩上物を再度水洗・破砕し、再度篩分けた。これを3回繰り返した。反復処理が完了した後、篩上物を乾燥させて成分を分析した。試料1の処理前後の成分分析値を表1に、試料2の処理前後の成分分析値を表2に、各試料の処理後の貴金属等の濃縮率を表3に示す。 As sample 1, a precious metal concentrate obtained by sorting incinerated ash was used, and as sample 2, a precious metal concentrate obtained by sorting heated shredder dust was used. After removing such foreign matter, the mixture was washed with water and crushed with a crusher (MX1200XTM (crushing container CAC90B) manufactured by WARING) at a solid-liquid ratio of 1:5. After crushing for 10 seconds, it was sieved with a sieve mesh of 0.5 mm. Each sieved material was again washed with water, crushed, and sieved again. This was repeated 3 times. After the iterations were completed, the sieves were dried and analyzed for composition. Table 1 shows the component analysis values of sample 1 before and after treatment, Table 2 shows the component analysis values of sample 2 before and after treatment, and Table 3 shows the concentration ratio of precious metals and the like of each sample after treatment.

Figure 0007137532000001
Figure 0007137532000001

Figure 0007137532000002
Figure 0007137532000002

Figure 0007137532000003
Figure 0007137532000003

表1~表3に示す通り、貴金属であるAu(金)、Ag(銀)及びPd(パラジウム)や、Cuの濃縮率が130%程度と高く、その他の金属(Al、Si及びCa)の濃縮率が25~70%程度と低下し、貴金属等がさらに濃縮していることが判る。 As shown in Tables 1 to 3, the concentration rate of precious metals Au (gold), Ag (silver) and Pd (palladium) and Cu is as high as about 130%, and other metals (Al, Si and Ca) It can be seen that the concentration rate decreased to about 25 to 70%, and precious metals and the like were further concentrated.

尚、上記実施の形態においては、循環ルート5を設けることで回収する篩上物の貴金属品位を高めることができて好ましいが、必ずしも循環ルート5を設ける必要はなく、篩選別機4で分離された粗粒分をそのまま処理物とすることも可能である。 In the above-described embodiment, the circulation route 5 is preferably provided to improve the quality of the recovered sieved material, but it is not always necessary to provide the circulation route 5. It is also possible to use the coarse grain fraction as it is as a processed material.

1 金属含有廃棄物の処理装置
2 磁選機
3 破砕機
4 篩選別機
5 循環ルート
1 Metal-containing waste treatment device 2 Magnetic separator 3 Crusher 4 Sieve separator 5 Circulation route

Claims (4)

金属含有廃棄物を選別処理して得られた貴金属濃縮物であって、Si及びCaの含有率の合計が5質量%以上30質量%以下、及びAl及びCuの含有率の合計が20質量%以上60質量%以下である貴金属濃縮物を磁力選別する磁力選別機と、
該磁力選別機によって分離された非磁着物を破砕する破砕機と、
該破砕機によって破砕された破砕物から微粒分を除去する選別機からなることを特徴とする金属含有廃棄物の処理装置。
A precious metal concentrate obtained by sorting metal-containing waste, having a total Si and Ca content of 5% by mass or more and 30% by mass or less, and a total Al and Cu content of 20% by mass. A magnetic sorter for magnetically sorting precious metal concentrates of 60% by mass or more;
a crusher for crushing non-magnetic substances separated by the magnetic separator;
An apparatus for treating metal-containing waste, comprising a sorter for removing fine particles from crushed materials crushed by the crusher.
前記選別機で分離された粗粒分を前記破砕機に戻す循環ルートを備えることを特徴とする請求項1に記載の金属含有廃棄物の処理装置。 2. The apparatus for treating metal-containing waste according to claim 1, further comprising a circulation route for returning coarse particles separated by said sorter to said crusher. 金属含有廃棄物を選別処理して得られた貴金属濃縮物であって、Si及びCaの含有率の合計が5質量%以上30質量%以下、及びAl及びCuの含有率の合計が20質量%以上60質量%以下である貴金属濃縮物を磁力選別するステップと
該磁力選別によって得られた非磁着物を破砕するステップと
該破砕によって得られた破砕物から微粒分を除去するステップからなることを特徴とする金属含有廃棄物の処理方法。
A precious metal concentrate obtained by sorting metal-containing waste, having a total Si and Ca content of 5% by mass or more and 30% by mass or less, and a total Al and Cu content of 20% by mass. a step of magnetically sorting a precious metal concentrate having a concentration of 60% by mass or more;
crushing the non-magnetic substances obtained by the magnetic selection;
A method for treating metal-containing waste, comprising the step of removing fine particles from the crushed material obtained by the crushing.
前記微粒分を除去した後の粗粒分を再度破砕し、該破砕によって得られた破砕物から微粒分を除去することを特徴とする請求項3に記載の金属含有廃棄物の処理方法。 4. The method for treating metal-containing waste according to claim 3, wherein the coarse particles after removing the fine particles are crushed again, and the fine particles are removed from the crushed material obtained by the crushing.
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