JP2013215721A - Facility and method for recovering metal in slag - Google Patents

Facility and method for recovering metal in slag Download PDF

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JP2013215721A
JP2013215721A JP2013049814A JP2013049814A JP2013215721A JP 2013215721 A JP2013215721 A JP 2013215721A JP 2013049814 A JP2013049814 A JP 2013049814A JP 2013049814 A JP2013049814 A JP 2013049814A JP 2013215721 A JP2013215721 A JP 2013215721A
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slag
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metal particles
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JP5983473B2 (en
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Daisuke Imanishi
大輔 今西
Yoshiaki Nishina
慶晃 西名
Seiji Enoeda
成治 榎枝
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JFE Steel Corp
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Abstract

PROBLEM TO BE SOLVED: To provide a facility and method for recovering metal in slag, capable of high accurately separating/recovering metal in slag (i.e., iron particles in ironmaking slag) in a short time.SOLUTION: A facility 10 for recovering metal in slag includes a slag charging chute 1 for charging slag 8 (metal particles 8b and slag 8a having a silica compound as a main constituent are fixed with each other), a rotary crushing device (a pin setting base 2 and a crushing pin 3) for crushing the slag 8 by making a rotor collide with the charged slag 8, a fixed sieve 5 for performing separation into a material smaller in size than the sieve mesh and a material larger in size than the sieve mesh with the rotary crushing device, a metal particle recovering device (a shutter 6, a recovery duct 7) for recovering the material scattered in the rotary direction of the crushing pin 3 as metal particles 8b, a crushing chamber 4, and a base part 9.

Description

本発明は、広くはスラグ中に混入した金属粒を分離回収するスラグ中金属回収設備および回収方法に関するものであり、特に、金属粒が混入したスラグに対して回転体(例えば、ハンマーやピン)で衝撃力を与えた場合の金属粒とスラグの靭性差(粉砕強度差)を利用して金属粒を分離回収するスラグ中金属回収設備および回収方法に関するものである。   The present invention relates generally to a metal recovery facility and recovery method for separating and recovering metal particles mixed in slag, and in particular, a rotating body (for example, a hammer or a pin) for slag mixed with metal particles. The present invention relates to a slag metal recovery facility and a recovery method for separating and recovering metal particles using a difference in toughness (pulverization strength difference) between metal particles and slag when an impact force is applied.

例えば、製鉄プラントにおいては、大量の製鉄スラグが発生している。一般的に、鉄は鉄鉱石中の酸化鉄を、石炭を用いて還元し作製する。この際に発生した副産物が製鉄スラグであるが、これら製鉄スラグの中にも鉄分(鉄粒)が混入している。この鉄粒は単体として存在している場合よりも、スラグに鉄粒が取り囲まれるように凝着した状態であることが多い。従来、製鉄スラグ中の鉄粒を回収する手段として、様々な手法が提案されている。   For example, in a steel plant, a large amount of steel slag is generated. Generally, iron is produced by reducing iron oxide in iron ore using coal. The by-product generated at this time is iron slag, and iron (iron particles) is also mixed in these iron slag. The iron particles are often in a state of being adhered so that the iron particles are surrounded by the slag, rather than the case where the iron particles exist as a single body. Conventionally, various methods have been proposed as means for collecting iron particles in iron slag.

製鉄スラグから鉄粒を回収する方法としては、磁力選別、比重選別、分級選別が広く用いられている。   As methods for recovering iron particles from iron slag, magnetic sorting, specific gravity sorting, and classification sorting are widely used.

ここで、磁力選別は、強磁性体である鉄粒と弱磁性体および非磁性体を主成分とするスラグとの磁性差を利用して、鉄粒の分離回収を行う手法である。   Here, magnetic separation is a technique for separating and recovering iron particles by utilizing the magnetic difference between iron particles, which are ferromagnetic materials, and slag, which is mainly composed of weak magnetic materials and non-magnetic materials.

また、比重選別は、鉄粒とスラグとの比重差を利用して、鉄粒の分離回収を行う手法である。   Specific gravity sorting is a technique for separating and collecting iron particles by utilizing the specific gravity difference between the iron particles and slag.

また、分級選別は、鉄粒とその他スラグ分との延性、粉砕性の差を利用し、粉砕後の鉄粒とスラグ分の粒径差で分離する手法である。   In addition, classification and sorting is a method of separating by the difference in particle size between the iron particles after pulverization and the slag by utilizing the difference in ductility and pulverization between the iron particles and other slag components.

分級選別としては、例えば、鉄粒を含んだスラグをボールミルで破砕・圧延処理し、破砕処理によってスラグ成分を粉状に、圧延処理によって鉄粒を薄片に加工することで、スラグと鉄粒の形状(粒径)が異なるようにし、篩によって鉄粒の分離回収を行う方法が行われている(例えば、特許文献1)。   As classification classification, for example, slag containing iron particles is crushed and rolled with a ball mill, slag components are pulverized by crushing, and iron particles are processed into thin pieces by rolling, so that slag and iron particles A method of separating and recovering iron particles with a sieve so as to have different shapes (particle diameters) has been performed (for example, Patent Document 1).

同じく、分級選別として、篩に突起状の部材を設け、落下時のスラグと突起部の衝突によって、スラグを解砕し、篩で分級することにより鉄粒を分離回収する方法が行われている(例えば、特許文献2)。   Similarly, as a classification selection, a method is provided in which a projection-like member is provided on the sieve, and the iron particles are separated and recovered by crushing the slag by the collision of the slag and the projection when falling, and classifying with the sieve. (For example, patent document 2).

特開平10−216545号公報JP-A-10-216545 特開2003−334496号公報Japanese Patent Laid-Open No. 2003-33496

しかし、上述したような、製鉄スラグから鉄粒を回収する方法には、以下のような問題点がある。   However, the method for recovering iron particles from iron slag as described above has the following problems.

まず、磁力選別は、処理量が少ない場合は精度よく鉄とスラグ分を分離することが出来るが、処理量を増やすと鉄と磁石の間にスラグ分が巻き込まれ分離精度が落ちるので大量処理には向かないという問題がある。さらに、鉄粒の周りにスラグ分が付着している場合(特に、スラグと鉄粒が凝着している場合)などは、粉砕処理を行わなければ分離回収が不可能である。   First, magnetic separation can accurately separate iron and slag when the amount of processing is small, but if the amount of processing is increased, the amount of slag is caught between iron and the magnet, which reduces the separation accuracy, so it can be used for mass processing. There is a problem that is not suitable. Further, when slag is attached around the iron particles (particularly when slag and iron particles are adhered), separation and recovery are impossible unless pulverization is performed.

また、比重選別は、乾式で行う際は、分離物の比重差が大きくないと高精度分離が出来ないという問題を持つ。さらに、鉄粒の周りにスラグ分が付着している場合などは、粉砕処理を行わなければ分離回収が不可能である。また、湿式で行う場合は比重差が小さくても精度良く分離が出来るが、水処理を行わなければならないため、ランニングコストが多大になるという問題を持つ。   Further, when the specific gravity selection is performed by a dry method, there is a problem that high-precision separation cannot be performed unless the specific gravity difference of the separated material is large. Furthermore, when slag is adhered around the iron particles, separation and collection are impossible unless pulverization is performed. Further, in the case of wet processing, separation can be performed with high precision even if the specific gravity difference is small, but there is a problem that running cost becomes large because water treatment has to be performed.

また、特許文献1に記載の分級選別は、ボールミルを利用しており、粉砕物を連続で外部に排出することが出来ないため、連続破砕処理をすることが出来ない。また、ボールミルは破砕時間が他の破砕方法と比較して比較的長いため、時間当たりの処理量を増やすことが出来ないという問題点がある。   In addition, the classification and sorting described in Patent Document 1 uses a ball mill, and the pulverized product cannot be continuously discharged to the outside. Further, since the ball mill has a relatively long crushing time as compared with other crushing methods, there is a problem in that the amount of processing per hour cannot be increased.

また、特許文献2に記載の分級選別は、落下衝突のみでは、鉄粒に付着したスラグ分を完全に除去出来ないため、分離精度が悪いという問題点を持つ。また、落下したスラグが突起部に衝突しない可能性もあり、その際は全く分離回収が出来ない。   In addition, the classification and screening described in Patent Document 2 has a problem that the separation accuracy is poor because the slag adhering to the iron particles cannot be completely removed only by the drop collision. In addition, there is a possibility that the dropped slag does not collide with the protrusion, and in that case, separation and recovery cannot be performed at all.

本発明は、上記のような事情に鑑みてなされたものであり、スラグ中の金属分(例えば、製鉄スラグ中の鉄粒)を高精度で短時間に分離回収することができるスラグ中金属回収設備および回収方法を提供することを目的とするものである。   This invention is made | formed in view of the above situations, The metal content in slag which can isolate | separate and collect | recover the metal content in a slag (for example, iron particle in iron-making slag) with high precision in a short time. The object is to provide equipment and recovery methods.

上記課題を解決するために、本発明は以下の特徴を有する。   In order to solve the above problems, the present invention has the following features.

[1]スラグ中に存在する金属粒を分離回収するスラグ中金属回収設備であって、金属粒が存在するスラグを投入する粉砕室と、該粉砕室の内部で回転体を衝突させてスラグを粉砕する回転式粉砕装置と、前記粉砕室の下方に設けられ、篩目を通る大きさの物と篩目を通らない大きさの物とを分離する篩と、前記粉砕室の上方に設けられ、前記回転体の回転方向に飛ばされた物を金属粒として回収する金属粒回収装置とを備えていることを特徴とするスラグ中金属回収設備。   [1] A slag metal recovery facility for separating and recovering metal particles present in slag, wherein a pulverizing chamber into which slag containing metal particles is charged, and a rotating body collide with the slag to slag A rotary crusher for crushing, a sieve provided below the crushing chamber, separating a material having a size passing through a sieve and a material having a size not passing through a sieve, and provided above the crushing chamber An apparatus for recovering metal in slag, comprising: a metal particle recovery device that recovers a metal particle that has been blown in the rotating direction of the rotating body.

[2]前記金属粒回収装置が、金属粒を回収する回収ダクトと、該回収ダクトに前記篩の篩目を通る大きさの物が混入しないようにするためのシャッター装置とを備えていることを特徴とする前記[1]に記載のスラグ中金属回収設備。   [2] The metal particle recovery device includes a recovery duct for recovering metal particles, and a shutter device for preventing an object having a size passing through the mesh of the sieve from entering the recovery duct. The metal recovery facility for slag as described in [1] above.

[3]スラグ中に存在する金属粒を分離回収するスラグ中金属回収設備であって、金属粒が存在するスラグを投入する粉砕室と、該粉砕室の内部で回転体を衝突させてスラグを粉砕する回転式粉砕装置と、前記粉砕室の下方に設けられ、篩目を通る大きさの物と篩目を通らない大きさの物とを分離する篩と、前記粉砕室の下方に設けられ、前記回転体の回転方向に飛ばされた物を金属粒として回収する金属粒回収装置とを備えているとともに、前記金属粒回収装置が、金属粒を回収する回収ダクトと、該回収ダクトに前記篩の篩目を通る大きさの物が混入しないようにするためのシャッター装置とを備えていることを特徴とするスラグ中金属回収設備。   [3] A slag metal recovery facility for separating and recovering metal particles present in the slag, the pulverizing chamber into which the slag containing the metal particles is charged, and a rotating body colliding with the slag in the slag chamber. A rotary crusher for crushing, a sieve provided below the crushing chamber, separating a material having a size passing through a sieve and a material having a size not passing through a sieve, and provided below the crushing chamber And a metal particle recovery device that recovers the metal particles flying in the rotation direction of the rotating body as metal particles, and the metal particle recovery device includes a recovery duct for recovering metal particles, and A metal device for recovering metal in a slag, comprising a shutter device for preventing an object having a size passing through a sieve mesh from entering.

[4]スラグを投入後の一定時間、前記シャッター装置を閉めて、前記篩の篩目を通る大きさの物が前記回収ダクトへ混入するのを防止することを特徴とする前記[2]または[3]に記載のスラグ中金属回収設備。   [4] The above-mentioned [2], wherein the shutter device is closed for a certain period of time after the slag is thrown to prevent an object having a size passing through the sieve mesh from entering the recovery duct. [3] The metal recovery facility for slag according to [3].

[5]前記回転式粉砕装置は、1以上のハンマーまたはピンを回転させ、回転するハンマーまたはピンとスラグとの衝突力によりスラグを粉砕することを特徴とする前記[1]〜[4]のいずれかに記載のスラグ中金属回収設備。   [5] Any of the above [1] to [4], wherein the rotary crushing device rotates one or more hammers or pins and crushes the slag by a collision force between the rotating hammer or pins and the slag. Metal recovery equipment for slag as described in Crab.

[6]前記回収ダクトの長さは、当該回収ダクト内に飛ばされてきた物のうち、金属粒は飛翔して通過できる長さであり、かつ、金属粒でないスラグ分は飛翔できずに途中で当該回収ダクト内に落下する長さであることを特徴とする前記[1]〜[5]のいずれかに記載のスラグ中金属回収設備。   [6] The length of the recovery duct is a length that allows the metal particles to fly and pass among the items that have been blown into the recovery duct, and the slag that is not the metal particles cannot fly in the middle. The metal recovery equipment for slag according to any one of [1] to [5], wherein the metal recovery equipment has a length falling into the recovery duct.

[7]前記回収ダクトにファンが設置されていて、該ファンからの送風によって、金属粒でないスラグ分の飛翔できる長さを抑えることを特徴とする前記[6]に記載のスラグ中金属回収設備。   [7] A facility for recovering metal in slag as described in [6], wherein a fan is installed in the recovery duct, and the length by which the slag that is not metal particles can fly by air blown from the fan is suppressed. .

[8]スラグ中に存在する金属粒を分離回収するスラグ中金属回収方法であって、金属粒が存在するスラグに回転体を衝突させてスラグを粉砕する粉砕工程と、該粉砕工程での被粉砕物を篩によって大きさで分離する篩工程と、前記回転体の回転方向に飛ばされた物を金属粒として回収する金属粒回収工程とを備えていることを特徴とするスラグ中金属回収方法。   [8] A method for recovering metal in a slag that separates and recovers metal particles present in the slag, wherein the slag is smashed by colliding a rotating body with the slag in which the metal particles are present; A method for recovering a metal in slag, comprising: a sieving step for separating the pulverized product by size with a sieve; and a metal particle recovery step for recovering as a metal particle a product that has been blown in the rotational direction of the rotating body. .

[9]前記金属粒回収工程において、前記篩の篩目を通る大きさの物が金属粒に混入して回収されないようにするために、スラグを投入後の一定時間、金属粒の回収を停止することを特徴とする前記[8]に記載のスラグ中金属回収方法。   [9] In the metal particle recovery step, the collection of metal particles is stopped for a certain period of time after the slag is added in order to prevent an object having a size passing through the sieve of the sieve from being mixed into the metal particles and recovered. The method for recovering metal in slag as described in [8] above.

[10]金属粒回収工程において前記回転体の回転方向に飛ばされた物を金属粒として回収するための回収ダクトを設置し、その回収ダクトの長さは、当該回収ダクト内に飛ばされてきた物のうち、金属粒は飛翔して通過できる長さであり、かつ、金属粒でないスラグ分は飛翔できずに途中で当該回収ダクト内に落下する長さであることを特徴とする前記[8]または[9]に記載のスラグ中金属回収方法。   [10] A recovery duct for recovering as a metal particle the object that has been blown in the rotating direction of the rotating body in the metal particle recovery step is installed, and the length of the recovery duct has been skipped in the recovery duct Among the objects, the metal particles have such a length that they can fly and pass through, and the slag that is not metal particles cannot fly and has a length that falls in the recovery duct on the way [8] ] Or the metal recovery method in slag as described in [9].

[11]前記回収ダクトにファンを設置し、該ファンからの送風によって、金属粒でないスラグ分の飛翔できる長さを抑えることを特徴とする前記[10]に記載のスラグ中金属回収方法。   [11] The method for recovering metal in slag as described in [10], wherein a fan is installed in the recovery duct, and a length by which the slag that is not metal particles can fly is suppressed by blowing air from the fan.

本発明においては、スラグ中の金属分(例えば、製鉄スラグ中の鉄粒)を高精度で短時間に分離回収することができる。   In the present invention, a metal component in slag (for example, iron particles in iron slag) can be separated and recovered with high accuracy in a short time.

本発明の実施形態1を示す側面図である。It is a side view which shows Embodiment 1 of this invention. 本発明の実施形態2を示す側面図である。It is a side view which shows Embodiment 2 of this invention. 本発明の実施形態2を示す正面図である。It is a front view which shows Embodiment 2 of this invention. 本発明の実施形態3を示す側面図である。It is a side view which shows Embodiment 3 of this invention.

本発明は、スラグ分と金属粒で破砕のされやすさが異なり、スラグ分は細かくなるまで粉砕されるのに対し、金属粒は細かくならないことを利用して、それらを分離回収するものである。   In the present invention, the slag content and the metal particles are easily crushed, and the slag content is pulverized until it becomes fine, whereas the metal particles do not become fine, so that they are separated and recovered. .

本発明の実施形態を図面に基づいて説明する。   Embodiments of the present invention will be described with reference to the drawings.

[実施形態1]
図1は、本発明の実施形態1に係るスラグ中金属回収設備21を示す側面図である。
[Embodiment 1]
FIG. 1 is a side view showing an in-slag metal recovery facility 21 according to Embodiment 1 of the present invention.

この実施形態1に係るスラグ中金属回収設備21は、回転体(ピン)を回転させて金属粒を含むスラグを粉砕し、その粉砕物を篩で分離するものであり、金属粒以外のスラグ分はこの粉砕により篩の篩目より小さくなるまで粉砕された後、篩下に分離され、金属粒は粉砕されないため篩の篩目より小さくならず、回転による風圧あるいはピンとの衝突によりピンの回転方向に飛ばされ、回収ダクトより金属粒として乾式で回収するピンミル型スラグ中金属回収設備であり、図1に示すように、スラグ8(金属粒8bとシリカ化合物を主成分とするスラグ分8aとが固着)を投入するスラグ投入シュート1と、投入されたスラグ8に回転体を衝突させてスラグ8を粉砕する回転式粉砕装置(ピン設置土台2、粉砕用ピン3)と、回転式粉砕装置で粉砕された物をその大きさで分離する固定篩5と、粉砕用ピン3の回転方向に飛ばされた物を金属粒8bとして回収する金属粒回収装置(シャッター6、回収ダクト7)と、粉砕室4と、土台部9とを備えている。   The metal recovery equipment 21 in the slag according to the first embodiment pulverizes slag containing metal particles by rotating a rotating body (pin), and separates the pulverized product with a sieve. Is pulverized until it becomes smaller than the sieve mesh of the sieve by this pulverization, and separated under the sieve, and the metal particles are not crushed, so it does not become smaller than the sieve mesh of the sieve, and the rotation direction of the pin due to wind pressure by rotation or collision with the pin 1 is a metal recovery facility in a pin mill type slag that is recovered in a dry manner as metal particles from a recovery duct. As shown in FIG. 1, slag 8 (metal particles 8b and a slag component 8a mainly composed of a silica compound are included. Slag charging chute 1 for charging), a rotary pulverizing device (pin installation base 2, pulverizing pin 3) for pulverizing the slag 8 by causing a rotating body to collide with the slag 8 charged, and a rotary pulverizing device. A fixed sieve 5 that separates the pulverized material by its size, a metal particle recovery device (shutter 6 and recovery duct 7) that recovers the material blown in the rotational direction of the pulverizing pin 3 as metal particles 8b, and pulverization The chamber 4 and the base part 9 are provided.

ここで、ピン設置土台2には、粉砕用ピン3が多数取り付けられており、ピン設置土台2が回転することにより、同時に粉砕用ピン3を回転させることが出来る。   Here, many pin 3 for grinding | pulverization is attached to the pin installation base 2, and when the pin installation base 2 rotates, the pin 3 for grinding | pulverization can be rotated simultaneously.

このようなスラグ中金属回収設備21においては、スラグ投入シュート1よりスラグ8(スラグ分8a、金属粒8b)を投入すると、スラグ8は粉砕室4内で落下する間に、回転する破砕用ピン3と何度も衝突し、あるいは衝突後に粉砕室4と衝突し、その衝撃でスラグ分8aが粉砕される。その際に、粉砕用ピン3の衝撃力とせん断力により金属粒8b(細かくなるまで粉砕されない)からスラグ分8a(細かくなるまで粉砕される)が分離し、さらにスラグ分8a(粉砕物)は破砕用ピン3とのさらなる衝突により細粒に粉砕される。そして、粉砕物であるスラグ分8aは篩5の篩下として回収される。一方、スラグ分に比べて粉砕されにくい金属粒8bは、粉砕室に投入した時の大きさをほぼ保持しているため、篩5の篩上となり、粉砕室4内を粉砕用ピン3の回転方向に循環して、粉砕室4の内壁に回収口を備えた回収ダクト7より回収される。回収した金属粒を再利用する際の作業性や金属粒の回収効率を考えると、通常、粒の大きさが1mm以上〜3mm以上の金属粒を回収するのが好ましい。また、スラグ分は、回転体にて粉砕を行なうことにより、1mm未満〜3mm未満の大きさまで粉砕することができるので、通常、篩目が1mm〜3mmの篩を用いる。   In such a slag metal recovery facility 21, when slag 8 (slag portion 8 a, metal particles 8 b) is charged from the slag charging chute 1, the crushing pin that rotates while the slag 8 falls in the crushing chamber 4. 3 collided with the crushing chamber 4 many times or after colliding with the crushing chamber 4, and the slag portion 8a is crushed by the impact. At that time, the slag portion 8a (pulverized until it becomes fine) is separated from the metal particles 8b (not pulverized until it becomes fine) by the impact force and shear force of the pulverizing pin 3, and the slag portion 8a (pulverized product) is further separated. By further collision with the crushing pin 3, it is crushed into fine particles. And the slag part 8a which is a ground material is collect | recovered as the sieving under the sieve 5. FIG. On the other hand, the metal particles 8b that are hard to be pulverized compared to the slag content are almost kept in size when they are put into the pulverization chamber, and therefore are on the screen of the sieve 5, and the inside of the pulverization chamber 4 rotates the pulverization pin 3 It circulates in the direction and is recovered from a recovery duct 7 provided with a recovery port on the inner wall of the crushing chamber 4. Considering the workability at the time of reusing the recovered metal particles and the recovery efficiency of the metal particles, it is usually preferable to recover the metal particles having a particle size of 1 mm to 3 mm. Moreover, since a slag part can be grind | pulverized to the magnitude | size of less than 1 mm-less than 3 mm by grind | pulverizing with a rotary body, a sieve with a mesh size of 1 mm-3 mm is normally used.

この際、回収ダクト7の回収口を粉砕室4の上方(回転体であるピン設置土台2の回転軸を通る水平線より上)に設けることにより、細粒に粉砕されたスラグ分が回収ダクト7に混入しにくくなるため、スラグ分の混入の少ない金属粒の回収が可能になる。   At this time, the recovery port of the recovery duct 7 is provided above the crushing chamber 4 (above the horizontal line passing through the rotation axis of the pin installation base 2 that is a rotating body), so that the slag component pulverized into fine particles can be recovered. Therefore, it becomes possible to collect metal particles with less slag content.

なお、スラグ分8aが粉砕されにくく、篩5の篩目以上の大きさのスラグ分8aが発生する場合(言い換えれば、金属粒8bとスラグ分8aが凝結した未粉砕のスラグ8が十分に粉砕・分離されていない場合)は、スラグ8を投入後の一定時間(予め操業実績等から定めておいた時間)、シャッター6を閉めて、篩5の篩目以上の大きさのスラグ分8aや未粉砕のスラグ8が回収ダクト7へ混入するのを防止しながら、スラグ8およびスラグ分8aの循環時間を増やすことで、未粉砕のスラグ8およびスラグ分8aが粉砕用ピン3の回転による風圧で再び巻き上げられ、粉砕用ピン3で破砕されて、スラグ分8a(篩目より小さくなるまで粉砕された物)と金属粒8b(篩目より小さくなるまで粉砕されない物)とに分離回収することが出来る。   When the slag portion 8a is difficult to be crushed and a slag portion 8a having a size larger than the mesh size of the sieve 5 is generated (in other words, the unground slag 8 in which the metal particles 8b and the slag portion 8a are condensed is sufficiently pulverized. If not separated), the slag portion 8a having a size larger than the mesh size of the sieve 5 is closed by closing the shutter 6 for a certain time after the slag 8 is charged (the time determined in advance from the operation results). By increasing the circulation time of the slag 8 and the slag portion 8a while preventing the unground slag 8 from mixing into the recovery duct 7, the wind pressure caused by the rotation of the pulverizing pin 3 causes the slag 8 and the slag portion 8a to rotate. And crushed with the crushing pin 3 and separated and recovered into the slag content 8a (the product pulverized until it becomes smaller than the sieve mesh) and the metal particles 8b (the product that is not pulverized until it becomes smaller than the sieve mesh). Can .

このようにして、この実施形態1においては、回転体(粉砕用ピン3)をスラグ8に衝突させてスラグ分8aを粉砕した後、粉砕物は篩下でスラグ分8aとして回収し、スラグ分8aが粉砕室からほとんどなくなるまでシャッター6を閉めて、その後、シャッター6を開けることにより、回転による風圧あるいは粉砕用ピン3との衝突により粉砕用ピン3の回転方向に飛ばされた、篩5の篩目より小さくなるまで粉砕されなかった物を回収ダクト7より金属粒8bとして回収することができる。この場合、回収ダクト7の回収口(金属粒の回収口)は、粉砕室4の上方(回転体であるピン設置土台2の回転軸を通る水平線より上)に設けても、粉砕室4の下方(回転体であるピン設置土台2の回転軸を通る水平線より下)に設けてもよい。   Thus, in the first embodiment, after the slag portion 8a is crushed by colliding the rotating body (pulverizing pin 3) with the slag 8, the pulverized material is recovered as the slag portion 8a under the sieve, and the slag portion The shutter 6 is closed until the 8a almost disappears from the crushing chamber, and then the shutter 6 is opened so that the screen 5 is blown in the rotation direction of the crushing pin 3 due to the wind pressure by the rotation or the collision with the crushing pin 3. A material that has not been crushed until it becomes smaller than the sieve mesh can be recovered from the recovery duct 7 as metal particles 8b. In this case, even if the recovery port (metal particle recovery port) of the recovery duct 7 is provided above the crushing chamber 4 (above the horizontal line passing through the rotation axis of the pin mounting base 2 which is a rotating body), You may provide below (below the horizontal line which passes along the rotating shaft of the pin installation base 2 which is a rotary body).

ちなみに、回収ダクト7の回収口(金属粒の回収口)を粉砕室4の下方(回転体であるピン設置土台2の回転軸を通る水平線より下)に設けた場合は、スラグ分8aが回収ダクト7に混入しやすくなるので、それを防止するために、回収ダクト7の回収口の前面にシャッター6を設けておき、粉砕室4からスラグ分8aがほとんどなくなるまでシャッター6を閉めて、その後、シャッター6を開けることが肝要である。   Incidentally, when the recovery port (metal particle recovery port) of the recovery duct 7 is provided below the crushing chamber 4 (below the horizontal line passing through the rotation axis of the pin installation base 2 which is a rotating body), the slag portion 8a is recovered. In order to prevent this, the shutter 6 is provided in front of the recovery port of the recovery duct 7, and the shutter 6 is closed until the slag portion 8 a from the pulverization chamber 4 almost disappears. It is important to open the shutter 6.

これによって、このスラグ中金属回収設備21は、以下のような効果を奏する。   Thereby, this metal recovery equipment 21 in slag has the following effects.

(a)スラグ8を乾式で回転式粉砕装置の上部から連続投入し、さらに連続分離・回収処理することが可能であるとともに、回転式粉砕装置はボールミルと比較して短時間でスラグ分8aの粉砕が可能なので、処理量を大きく向上させることができる。その上、粉砕工程(スラグ分8aの粉砕)と分離工程(スラグ分8aと金属粒8bとの分離)を同時に行うことが出来るので、磁力選別や比重選別のように粉砕工程を単独で行う必要がなく、効率的である。   (A) The slag 8 can be continuously fed from the top of the rotary pulverizer in a dry manner and further subjected to continuous separation / recovery processing. The rotary pulverizer can reduce the slag content 8a in a short time compared to a ball mill. Since pulverization is possible, the throughput can be greatly improved. In addition, since the pulverization step (pulverization of the slag portion 8a) and the separation step (separation of the slag portion 8a and the metal particles 8b) can be performed at the same time, it is necessary to perform the pulverization step independently such as magnetic force selection and specific gravity selection. There is no, it is efficient.

(b)また、回転体(粉砕用ピン3)の回転により金属粒8bに衝撃力とせん断力を何度も与えるので、全ての金属粒8bで固着したスラグ分8aを完全に除去することが出来ることから、金属粒8bとスラグ分8aとの高精度の分離回収が可能である。   (B) Further, since the impact force and the shearing force are repeatedly applied to the metal particles 8b by the rotation of the rotating body (grinding pin 3), the slag portion 8a fixed by all the metal particles 8b can be completely removed. As a result, the metal particles 8b and the slag portion 8a can be separated and recovered with high accuracy.

(c)さらに、スラグ分8aはほぼ全量篩下で回収されるため、磁気選別で見られるような巻込みは発生しない。また、乾式分離であるため、水処理コストも発生しない。   (C) Furthermore, since almost the entire amount of the slag 8a is collected under the sieve, no entanglement as seen in magnetic sorting occurs. Moreover, since it is dry separation, the water treatment cost does not occur.

なお、この実施形態では、ピンを回転させてスラグを粉砕しているが、ハンマーを回転させてスラグを粉砕してもよく、回転速度はスラグ分が粉砕される速度であればよく適宜選択することができる。   In this embodiment, the slag is pulverized by rotating the pin. However, the slag may be pulverized by rotating the hammer, and the rotation speed may be appropriately selected as long as the slag is pulverized. be able to.

[実施形態2]
図2、図3は、本発明の実施形態2に係るスラグ中金属回収設備22を示す側面図と正面図である。
[Embodiment 2]
2 and 3 are a side view and a front view showing the metal recovery facility 22 in the slag according to the second embodiment of the present invention.

図2、図3に示すように、この実施形態2に係るスラグ中金属回収設備22は、基本的には、上記の実施形態1に係るスラグ中金属回収設備21と同様の構成であるが、破砕用ピン3の構成が異なっている。   As shown in FIGS. 2 and 3, the slag metal recovery facility 22 according to the second embodiment has basically the same configuration as the slag metal recovery facility 21 according to the first embodiment. The configuration of the crushing pin 3 is different.

すなわち、スラグ中金属回収設備22では、破砕用ピン3として、粉砕室4に固定された多数の固定ピン3aと、ピン設置土台2に設置された多数の回転ピン3bを備えている。   That is, the slag metal recovery facility 22 includes a large number of fixed pins 3 a fixed to the crushing chamber 4 and a large number of rotating pins 3 b installed on the pin installation base 2 as the crushing pins 3.

これによって、モータ10によってピン設置土台2が回転することにより同時に回転ピン3bが回転し、回転ピン3bと固定ピン3aによるせん断と衝撃力により、スラグ8が破砕される。   As a result, the rotation of the pin mounting base 2 by the motor 10 causes the rotation pin 3b to rotate at the same time, and the slag 8 is crushed by the shearing and impact force of the rotation pin 3b and the fixed pin 3a.

また、このスラグ中金属回収設備22では、回収ダクト7の長さが、回収ダクト7内に飛ばされてきた物のうち、金属粒8bは飛翔して通過できる長さであり、かつ、スラグ分8aは飛翔できずに途中で回収ダクト7内に落下する長さである。   Moreover, in this metal recovery equipment 22 in the slag, the length of the recovery duct 7 is the length that allows the metal particles 8b to fly and pass among the items that have been blown into the recovery duct 7, and the slag component. 8a is the length which cannot fly and falls in the collection | recovery duct 7 on the way.

具体的には、図2に示すように、回収ダクト7が回収口から上方に向かった後、下方に向かう形状をしており、方向が上方から下方に変わる長さ位置(高さ位置)は、回収ダクト7内に飛ばされてきた物のうち、金属粒8bは飛翔して通過できる長さ位置(高さ位置)で、かつ、スラグ分8aは飛翔できずに途中で回収ダクト7内に落下する長さ位置(高さ位置)となっている。   Specifically, as shown in FIG. 2, after the recovery duct 7 is directed upward from the recovery port, the shape is directed downward, and the length position (height position) where the direction changes from the upper side to the lower side is Of the items that have been blown into the recovery duct 7, the metal particles 8b are in a length position (height position) where they can fly and pass, and the slag portion 8a cannot fly and enters the recovery duct 7 halfway. It is the falling position (height position).

すなわち、スラグ分8aは比重が金属粒(例えば、鉄粒)8bの比重の1/3程度であるとともに、破砕されやすいので細粒である場合が多く、鉄粒8bよりも空気抵抗によって減速しやすい。したがって、鉄粒8bとスラグ分8aが回収ダクト7内に飛ばされてくる速度(射出速度)と比重に基づいて、空気抵抗の影響下によるスラグ分8aと鉄粒8bのそれぞれの飛翔距離(飛翔高さ)を計算し、回収ダクト7の上方に向かう部分の長さ(最上高さ位置)を、スラグ分8aの飛翔距離(飛翔高さ)以上、鉄粒8bの飛翔距離(飛翔高さ)未満とすることにより、仮にスラグ分8aが鉄粒8bに混じって回収ダクト7内に射出されても、鉄粒8bは最上高さ位置を通過して回収され、スラグ分8aは回収ダクト7内で落下して、回収ダクト7から系外には出ないため、回収精度が向上する。   That is, the slag portion 8a has a specific gravity of about 1/3 of the specific gravity of the metal particles (for example, iron particles) 8b, and is easily crushed, so it is often a fine particle and is slowed down by air resistance than the iron particles 8b. Cheap. Therefore, based on the speed (injection speed) at which the iron particles 8b and the slag portion 8a are blown into the recovery duct 7 and the specific gravity, the respective flight distances (flights) of the slag portion 8a and the iron particles 8b due to the influence of air resistance. (Height) is calculated, and the length of the portion (uppermost height position) toward the upper side of the recovery duct 7 is equal to or greater than the flight distance (flight height) of the slag 8a, and the flight distance (flight height) of the iron particles 8b. Even if the slag portion 8a is mixed with the iron particles 8b and injected into the recovery duct 7, the iron particles 8b are recovered through the uppermost height position, and the slag portion 8a is stored in the recovery duct 7. , And it does not come out of the system from the recovery duct 7, so that the recovery accuracy is improved.

また、回収ダクト7の長さ(高さ)を十分に確保できず、そのままではスラグ分8aが回収ダクト7内で落下しない場合には、図2に示すように、回収ダクト7にファン11を設置し、ファン11からの送風によって、スラグ分8aの飛翔距離(飛翔高さ)を抑えて、鉄粒8bは最上高さ位置を通過して回収され、スラグ分8aは回収ダクト7内で落下するようにすればよい。   Further, if the length (height) of the recovery duct 7 cannot be sufficiently secured and the slag portion 8a does not fall in the recovery duct 7 as it is, a fan 11 is attached to the recovery duct 7 as shown in FIG. It is installed and the flying distance (flying height) of the slag portion 8a is suppressed by blowing air from the fan 11, and the iron particles 8b are recovered through the highest height position, and the slag portion 8a falls in the recovery duct 7. You just have to do it.

[実施形態3]
図4は、本発明の実施形態3に係るスラグ中金属回収設備23を示す側面図である。
[Embodiment 3]
FIG. 4 is a side view showing the slag metal recovery facility 23 according to Embodiment 3 of the present invention.

図4に示すように、この実施形態3に係るスラグ中金属回収設備23は、基本的には、上記の実施形態2に係るスラグ中金属回収設備22と同様の構成であるが、破砕用ピン3に替えて、ハンマー13がハンマー設置土台12に取り付けられている点が異なっている。   As shown in FIG. 4, the slag metal recovery facility 23 according to the third embodiment is basically configured in the same manner as the slag metal recovery facility 22 according to the second embodiment described above. 3 is different in that the hammer 13 is attached to the hammer installation base 12.

これによって、ハンマー設置土台12が回転することにより同時にハンマー13が回転するとともに、ハンマー13はハンマー設置土台12との取り付け部を中心にして円弧状に回転する。そのため、ハンマー13先端の周速をハンマー設置土台12の回転速度以上にすることができる。このハンマー13とスラグ8との衝突時の衝撃力により、スラグ8が破砕される。   Accordingly, the hammer 13 rotates simultaneously with the rotation of the hammer installation base 12, and the hammer 13 rotates in an arc shape around the attachment portion with the hammer installation base 12. Therefore, the peripheral speed at the tip of the hammer 13 can be made higher than the rotational speed of the hammer installation base 12. The slag 8 is crushed by the impact force when the hammer 13 and the slag 8 collide.

なお、図4では、シャッター6が設置されていないが、スラグ中金属回収設備21、22と同様に、シャッター6を設置してもよい。   In FIG. 4, the shutter 6 is not installed, but the shutter 6 may be installed similarly to the metal recovery facilities 21 and 22 in the slag.

1 スラグ投入シュート
2 ピン設置土台
3 粉砕用ピン
3a 固定ピン
3b 回転ピン
4 粉砕室
5 固定篩
6 シャッター
7 回収ダクト
8 スラグ
8a スラグ分
8b 金属粒
9 土台部
10 モータ
11 ファン
12 ハンマー設置土台
13 ハンマー
21 スラグ中金属回収設備
22 スラグ中金属回収設備
23 スラグ中金属回収設備
DESCRIPTION OF SYMBOLS 1 Slag throwing chute 2 Pin installation base 3 Crushing pin 3a Fixed pin 3b Rotating pin 4 Crushing chamber 5 Fixed sieve 6 Shutter 7 Collection duct 8 Slag 8a Slag 8b Metal particle 9 Base part 10 Motor 11 Fan 12 Hammer installation base 13 Hammer 21 Metal recovery facility for slag 22 Metal recovery facility for slag 23 Metal recovery facility for slag

Claims (11)

スラグ中に存在する金属粒を分離回収するスラグ中金属回収設備であって、金属粒が存在するスラグを投入する粉砕室と、該粉砕室の内部で回転体を衝突させてスラグを粉砕する回転式粉砕装置と、前記粉砕室の下方に設けられ、篩目を通る大きさの物と篩目を通らない大きさの物とを分離する篩と、前記粉砕室の上方に設けられ、前記回転体の回転方向に飛ばされた物を金属粒として回収する金属粒回収装置とを備えていることを特徴とするスラグ中金属回収設備。   A slag metal recovery facility that separates and recovers metal particles present in the slag, and a pulverization chamber into which the slag containing the metal particles is charged, and a rotation in which the slag is pulverized by colliding a rotating body inside the pulverization chamber. Type crusher, a sieve provided below the crushing chamber, separating a size passing through a sieve and a size not passing through a sieve, and provided above the crushing chamber and rotating An apparatus for recovering metal in slag, comprising: a metal particle recovery device that recovers metal particles that have been blown in the direction of rotation of the body as metal particles. 前記金属粒回収装置が、金属粒を回収する回収ダクトと、該回収ダクトに前記篩の篩目を通る大きさの物が混入しないようにするためのシャッター装置とを備えていることを特徴とする請求項1に記載のスラグ中金属回収設備。   The metal particle recovery device includes a recovery duct for recovering metal particles, and a shutter device for preventing an object having a size passing through the mesh of the sieve from entering the recovery duct. The metal collection | recovery equipment in slag of Claim 1 to do. スラグ中に存在する金属粒を分離回収するスラグ中金属回収設備であって、金属粒が存在するスラグを投入する粉砕室と、該粉砕室の内部で回転体を衝突させてスラグを粉砕する回転式粉砕装置と、前記粉砕室の下方に設けられ、篩目を通る大きさの物と篩目を通らない大きさの物とを分離する篩と、前記粉砕室の下方に設けられ、前記回転体の回転方向に飛ばされた物を金属粒として回収する金属粒回収装置とを備えているとともに、前記金属粒回収装置が、金属粒を回収する回収ダクトと、該回収ダクトに前記篩の篩目を通る大きさの物が混入しないようにするためのシャッター装置とを備えていることを特徴とするスラグ中金属回収設備。   A slag metal recovery facility that separates and recovers metal particles present in the slag, and a pulverization chamber into which the slag containing the metal particles is charged, and a rotation in which the slag is pulverized by colliding a rotating body inside the pulverization chamber. Type crusher, a sieve provided below the crushing chamber and separating an article having a size passing through a sieve and an article having a size not passing through a sieve, and provided below the crushing chamber and rotating A metal particle recovery device that recovers metal particles that have been blown in the direction of rotation of the body as metal particles, the metal particle recovery device recovers the metal particles, and a sieve sieve for the recovery duct. A metal device for recovering metal in slag, comprising a shutter device for preventing an object having a size passing through the eye from entering. スラグを投入後の一定時間、前記シャッター装置を閉めて、前記篩の篩目を通る大きさの物が前記回収ダクトへ混入するのを防止することを特徴とする請求項2または3に記載のスラグ中金属回収設備。   The said shutter apparatus is closed for a fixed time after throwing in slag, The thing of the magnitude | size which passes along the sieve mesh of the said sieve is prevented from mixing in the said collection | recovery duct. Metal recovery equipment for slag. 前記回転式粉砕装置は、1以上のハンマーまたはピンを回転させ、回転するハンマーまたはピンとスラグとの衝突力によりスラグを粉砕することを特徴とする請求項1〜4のいずれかに記載のスラグ中金属回収設備。   5. The slag according to claim 1, wherein the rotary crusher rotates one or more hammers or pins and crushes the slag by a collision force between the rotating hammers or pins and the slag. Metal recovery equipment. 前記回収ダクトの長さは、当該回収ダクト内に飛ばされてきた物のうち、金属粒は飛翔して通過できる長さであり、かつ、金属粒でないスラグ分は飛翔できずに途中で当該回収ダクト内に落下する長さであることを特徴とする請求項1〜5のいずれかに記載のスラグ中金属回収設備。   The length of the recovery duct is the length that allows the metal particles to fly and pass among the items that have been blown into the recovery duct, and the slag that is not metal particles cannot fly and is recovered in the middle. The metal recovery facility for slag according to any one of claims 1 to 5, wherein the metal recovery facility has a length falling into the duct. 前記回収ダクトにファンが設置されていて、該ファンからの送風によって、金属粒でないスラグ分の飛翔できる長さを抑えることを特徴とする請求項6に記載のスラグ中金属回収設備。   The metal recovery equipment for slag according to claim 6, wherein a fan is installed in the recovery duct, and a length capable of flying a slag that is not metal particles is suppressed by blowing air from the fan. スラグ中に存在する金属粒を分離回収するスラグ中金属回収方法であって、金属粒が存在するスラグに回転体を衝突させてスラグを粉砕する粉砕工程と、該粉砕工程での被粉砕物を篩によって大きさで分離する篩工程と、前記回転体の回転方向に飛ばされた物を金属粒として回収する金属粒回収工程とを備えていることを特徴とするスラグ中金属回収方法。   A method for recovering metal in slag by separating and recovering metal particles present in slag, comprising a pulverizing step of colliding a rotating body with slag in which metal particles are present and pulverizing slag, and an object to be crushed in the pulverizing step. A method for recovering a metal in slag, comprising: a sieving step of separating by size with a sieve; and a metal particle recovery step of recovering as a metal particle an object that has been blown in the rotating direction of the rotating body. 前記金属粒回収工程において、前記篩の篩目を通る大きさの物が金属粒に混入して回収されないようにするために、スラグを投入後の一定時間、金属粒の回収を停止することを特徴とする請求項8に記載のスラグ中金属回収方法。   In the metal particle recovery step, the collection of the metal particles is stopped for a certain period of time after the slag is added in order to prevent an object having a size passing through the sieve of the sieve from being mixed into the metal particles and recovered. The method for recovering a metal in a slag according to claim 8, wherein the metal is recovered. 金属粒回収工程において前記回転体の回転方向に飛ばされた物を金属粒として回収するための回収ダクトを設置し、その回収ダクトの長さは、当該回収ダクト内に飛ばされてきた物のうち、金属粒は飛翔して通過できる長さであり、かつ、金属粒でないスラグ分は飛翔できずに途中で当該回収ダクト内に落下する長さであることを特徴とする請求項8または9に記載のスラグ中金属回収方法。   In the metal particle recovery process, a recovery duct is provided for recovering as a metal particle an object that has been blown in the rotating direction of the rotating body, and the length of the recovery duct is the length of the object that has been skipped in the recovery duct. The metal particles have such a length that they can fly and pass through, and the slag that is not metal particles has a length that does not fly and falls into the recovery duct on the way. The metal recovery method in slag as described. 前記回収ダクトにファンを設置し、該ファンからの送風によって、金属粒でないスラグ分の飛翔できる長さを抑えることを特徴とする請求項10に記載のスラグ中金属回収方法。   The method for recovering metal in slag according to claim 10, wherein a fan is installed in the recovery duct, and a length by which the slag that is not metal particles can fly is suppressed by blowing air from the fan.
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CN117548339A (en) * 2024-01-12 2024-02-13 四川省宜宾威力化工有限责任公司 Powder raw material screening device based on civil explosion production usefulness
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CN117861988A (en) * 2024-03-12 2024-04-12 哈尔滨荣实基业工程建设有限公司 High-efficient environmental protection construction waste treater

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