JP2013180289A - Flotation machine - Google Patents

Flotation machine Download PDF

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JP2013180289A
JP2013180289A JP2012048163A JP2012048163A JP2013180289A JP 2013180289 A JP2013180289 A JP 2013180289A JP 2012048163 A JP2012048163 A JP 2012048163A JP 2012048163 A JP2012048163 A JP 2012048163A JP 2013180289 A JP2013180289 A JP 2013180289A
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slurry
flotation
coarse
supplied
coarse particles
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JP6404538B2 (en
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Yuji Aoki
悠二 青木
Soji Nakamura
壮志 中村
Osamu Momotani
修 桃谷
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Sumitomo Metal Mining Co Ltd
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Abstract

PROBLEM TO BE SOLVED: To provide a flotation machine which prevents trouble although coarse particles are supplied thereto.SOLUTION: A flotation machine includes a flotation tank 10 which is supplied with slurry containing minerals, an air supply means 20 which supplies air to the slurry, a stirring means 20 which stirs the slurry, and a coarse particle outlet 15 which is installed in the vicinity of the bottom of the flotation tank 10 and discharges the coarse mineral particles. The coarse particle outlet 15 is provided with a valve 16 which can control the discharge amount. The flotation machine 1 can be protected from trouble because the coarse particles can be discharged from the coarse particle outlet 15 although the coarse particles 15 are supplied thereto.

Description

本発明は、浮遊選鉱機に関する。さらに詳しくは、アジテア型浮遊選鉱機に関する。   The present invention relates to a floatation machine. More specifically, it relates to an agitaire type flotation machine.

銅鉱石から金属銅を製錬する製錬工程で産出される転炉カラミには、約6〜10%の銅が含まれている。この転炉カラミは、破砕機で破砕した後、水を加えてスラリー状として磨鉱し、浮遊選鉱工程へ供給される。浮遊選鉱工程では、スラリー状の転炉カラミに起泡剤や捕収剤、pH調整剤などを添加し、浮遊選鉱機に供給する。そして、転炉カラミ中の銅分がカラミ精鉱として回収され、銅鉱石とともに金属銅の原料として処理される。   The converter calami produced in the smelting process of smelting copper metal from copper ore contains about 6-10% copper. This converter calami is crushed by a crusher, then water is added to grind it as a slurry, and it is supplied to the flotation process. In the flotation process, a foaming agent, a collecting agent, a pH adjusting agent, etc. are added to the slurry converter calami and supplied to the flotation machine. And the copper content in a converter calami is collect | recovered as a calami concentrate, and is processed as a raw material of metallic copper with a copper ore.

浮遊選鉱機としてアジテア型浮遊選鉱機が知られている(例えば、特許文献1)。
アジテア型浮遊選鉱機では、転炉カラミ中の銅鉱物が捕収剤などにより表面改質され、気泡表面に付着し、気泡とともに浮鉱として回収される。また、気泡に付着しなかった転炉カラミは沈鉱として外部に排出される。
An agitaire type float separator is known as a float separator (for example, Patent Document 1).
In the agitaire-type flotation beneficiator, the copper mineral in the converter calami is surface-modified with a collector or the like, adheres to the bubble surface, and is recovered as a float with the bubbles. Further, converter calami that has not adhered to the bubbles is discharged to the outside as a deposit.

浮遊選鉱においては、供給される鉱物の粒度が重要であるため、浮遊選鉱機にはサイクロンなどの分級機により分級された後の転炉カラミが供給される。しかし、分級が不十分な場合など、粒度の粗い粗粒子が浮遊選鉱機に供給される場合がある。
アジテア型浮遊選鉱機に粗粒子が供給されると、粗粒子が浮選槽内に沈積し、不具合が生じるという問題がある。特に、転炉カラミは他の鉱物に比べて比重が重いので、粗粒子が浮選槽内に沈積しやすいという性質がある。
In flotation, since the particle size of the supplied mineral is important, the converter calami after being classified by a classifier such as a cyclone is supplied to the flotation machine. However, there are cases where coarse particles with coarse particle sizes are supplied to the flotation machine, such as when classification is insufficient.
When coarse particles are supplied to an agitaire type flotation machine, the coarse particles are deposited in the flotation tank, causing a problem. In particular, converter calami has a higher specific gravity than other minerals, so that coarse particles tend to settle in the flotation tank.

特公昭47−17129号公報Japanese Patent Publication No. 47-17129

本発明は上記事情に鑑み、粗粒子が供給されても不具合を防止できる浮遊選鉱機を提供することを目的とする。   In view of the above circumstances, an object of the present invention is to provide a flotation machine capable of preventing problems even when coarse particles are supplied.

第1発明の浮遊選鉱機は、鉱物を含有するスラリーが供給される浮選槽と、前記スラリーに空気を供給する空気供給手段と、前記スラリーを撹拌する撹拌手段と、前記浮選槽の底部近傍に設けられた、前記鉱物の粗粒子を排出する粗粒子排出口と、を備えることを特徴とする。
第2発明の浮遊選鉱機は、第1発明において、前記粗粒子排出口には、排出量を調整可能な弁が設けられていることを特徴とする。
第3発明の浮遊選鉱機は、第1または第2発明において、前記粗粒子排出口は、前記浮選槽において前記スラリーの供給位置から遠い位置に設けられていることを特徴とする。
The flotation machine of the first invention includes a flotation tank to which a slurry containing mineral is supplied, an air supply means for supplying air to the slurry, a stirring means for stirring the slurry, and a bottom of the flotation tank And a coarse particle outlet provided in the vicinity for discharging coarse particles of the mineral.
According to a second aspect of the present invention, in the first aspect of the present invention, the coarse particle discharge port is provided with a valve capable of adjusting a discharge amount.
According to a third aspect of the present invention, in the first or second aspect, the coarse particle discharge port is provided in a position far from the slurry supply position in the flotation tank.

第1発明によれば、粗粒子が供給されても粗粒子排出口から排出できるので、浮遊選鉱機の不具合を防止できる。
第2発明によれば、粗粒子とともに排出されるスラリーの量を調整できる。
第3発明によれば、浮選槽におけるスラリーの滞留時間を長時間確保できる。
According to the first aspect of the invention, even if coarse particles are supplied, they can be discharged from the coarse particle discharge port, so that it is possible to prevent the flotation machine from malfunctioning.
According to the second invention, the amount of the slurry discharged together with the coarse particles can be adjusted.
According to the 3rd invention, the residence time of the slurry in a flotation tank is securable for a long time.

本発明の一実施形態に係る浮遊選鉱機の縦断面図である。It is a longitudinal cross-sectional view of the flotation machine based on one Embodiment of this invention. 図1におけるII-II線矢視断面図である。It is the II-II arrow directional cross-sectional view in FIG.

つぎに、本発明の実施形態を図面に基づき説明する。
本発明の一実施形態に係る浮遊選鉱機1は、銅鉱石から金属銅を製錬する製錬工程で産出される転炉カラミから銅分を回収するために用いられる浮遊選鉱機である。
図1に示すように、浮遊選鉱機1は、アジテア型浮遊選鉱機であり、転炉カラミを含有するスラリーが供給される浮選槽10と、浮選槽10内のスラリーに空気を導入し撹拌する撹拌機20とを備えている。
Next, an embodiment of the present invention will be described with reference to the drawings.
A flotation machine 1 according to an embodiment of the present invention is a flotation machine used to recover copper from converter calami produced in a smelting process of smelting metallic copper from copper ore.
As shown in FIG. 1, the flotation machine 1 is an agitaire type flotation machine, and introduces air into the flotation tank 10 to which slurry containing converter calami is supplied and the slurry in the flotation tank 10. And a stirrer 20 for stirring.

浮選槽10の一端には、垂直な筒状のスラリー供給口11が設けられており、スラリー供給口11からスラリーが供給されるようになっている。なお、スラリー供給口11から供給されるスラリーは、転炉カラミを破砕機で破砕した後、水を加えてスラリー状として磨鉱し、浮選に必要な起泡剤や捕収剤、pH調整剤などを添加して得られたものである。   A vertical cylindrical slurry supply port 11 is provided at one end of the flotation tank 10 so that the slurry is supplied from the slurry supply port 11. The slurry supplied from the slurry supply port 11 is obtained by crushing the converter calami with a crusher, adding water to polish it into a slurry, and adding a foaming agent, a collection agent, and pH adjustment necessary for flotation. It was obtained by adding an agent or the like.

撹拌機20は、中空の軸部21と、軸部21の下端に設けられた円板22と、円板22の外周に沿って下垂して設けられた複数の羽根23とから構成されている。また、浮選槽10の底面には、羽根23の周囲を囲むように放射状に複数の邪魔板24が立設されている。   The stirrer 20 includes a hollow shaft portion 21, a disc 22 provided at the lower end of the shaft portion 21, and a plurality of blades 23 provided so as to hang down along the outer periphery of the disc 22. . In addition, a plurality of baffle plates 24 are erected on the bottom surface of the flotation tank 10 so as to surround the periphery of the blades 23.

撹拌機20は、軸部21の上端が図示しないモータに接続されており、そのモータの駆動により回転し、羽根23によりスラリーを撹拌できるようになっている。また、軸部21の内部には空気が圧送されており、軸部21の下端からスラリーに空気を供給できるようになっている。
なお、撹拌機20は、特許請求の範囲に記載の撹拌手段および空気供給手段に相当する。
The stirrer 20 is connected to a motor (not shown) at the upper end of the shaft portion 21, and is rotated by driving the motor so that the slurry can be stirred by the blades 23. Air is pumped into the shaft portion 21 so that air can be supplied to the slurry from the lower end of the shaft portion 21.
The stirrer 20 corresponds to the stirring means and the air supply means described in the claims.

撹拌機20が空気を供給しながら回転することにより、供給された空気が羽根23で分割され、スラリー中に気泡が発生する。また、邪魔板24によりスラリーの無駄な旋回を防ぎ、撹拌を強くしている。これにより、転炉カラミ中の銅分が発生した気泡に付着してスラリー液面に上昇し浮鉱となる。そして、図2に示すように、浮選槽10の側壁12からオーバーフローした浮鉱は浮鉱樋31に受け止められ回収される。   When the agitator 20 rotates while supplying air, the supplied air is divided by the blades 23 and bubbles are generated in the slurry. Further, the baffle plate 24 prevents the slurry from being swirled and strengthens the stirring. As a result, the copper content in the converter calami adheres to the generated bubbles and rises to the slurry liquid surface to become floating ore. Then, as shown in FIG. 2, the floating ore overflowing from the side wall 12 of the flotation tank 10 is received and collected by the flotation pit 31.

浮選槽10には、撹拌機20を挟んでスラリー供給口11と対向する端部に、スラリー界面調整ゲート13が設けられている。スラリー界面調整ゲート13は、図示しないハンドルにより上下位置が調整可能となっている。気泡に付着しなかった転炉カラミは沈鉱としてスラリー界面調整ゲート13の上縁をオーバーフローして沈鉱樋32に排出される。
なお、撹拌機20とスラリー界面調整ゲート13との間には、隔壁14が設けられており、浮鉱がスラリー界面調整ゲート13に流れないようにスラリー液面付近をせき止めている。
In the flotation tank 10, a slurry interface adjustment gate 13 is provided at an end facing the slurry supply port 11 with the stirrer 20 interposed therebetween. The slurry interface adjustment gate 13 can be adjusted in the vertical position by a handle (not shown). The converter calami that has not adhered to the bubbles overflows the upper edge of the slurry interface adjusting gate 13 as sedimentation and is discharged to the sedimentation pit 32.
A partition wall 14 is provided between the stirrer 20 and the slurry interface adjustment gate 13 to block the vicinity of the slurry liquid level so that floating ore does not flow to the slurry interface adjustment gate 13.

スラリー界面調整ゲート13が設けられた浮選槽10の側壁には、底部近傍に粗粒子排出口15が設けられている。この粗粒子排出口15は、浮選槽10の内部と沈鉱樋32とを連通している。また、粗粒子排出口15の沈鉱樋32側の端部には、ゲートバルブ16が設けられている。このゲートバルブ16により、粗粒子排出口15の開閉および開閉量を調整できるようになっている。   On the side wall of the flotation tank 10 provided with the slurry interface adjusting gate 13, a coarse particle discharge port 15 is provided in the vicinity of the bottom. The coarse particle outlet 15 communicates the inside of the flotation tank 10 with the sedimentation pit 32. A gate valve 16 is provided at the end of the coarse particle outlet 15 on the side of the sedimentation pit 32. The gate valve 16 can adjust the opening / closing amount and opening / closing amount of the coarse particle discharge port 15.

浮遊選鉱機1に供給されるスラリーに粒度の粗い転炉カラミ(粗粒子)が含まれていると、その粗粒子は浮選槽10に沈積する。沈積した粗粒子はスラリーの撹拌の邪魔となったりして、浮選の不具合の原因となる。ここで、例えば、浮選に適した転炉カラミの粒度が数十から数百μmであるのに対して、粗粒子の粒度は数mmである。
そこで、浮選槽10に粗粒子が沈積した場合には、ゲートバルブ16を開き、粗粒子排出口15から沈鉱樋32へ粗粒子を排出する。ここで、粗粒子は、粗粒子排出口15から排出されるスラリーの流れに乗って排出される。
When the slurry supplied to the flotation machine 1 contains coarse converter grain (coarse particles), the coarse particles are deposited in the flotation tank 10. The deposited coarse particles obstruct the stirring of the slurry and cause flotation problems. Here, for example, the particle size of the converter calami suitable for flotation is several tens to several hundred μm, whereas the particle size of the coarse particles is several mm.
Therefore, when coarse particles are deposited in the flotation tank 10, the gate valve 16 is opened and the coarse particles are discharged from the coarse particle discharge port 15 to the sedimentation pit 32. Here, the coarse particles are discharged on the flow of the slurry discharged from the coarse particle discharge port 15.

このように、浮遊選鉱機1は、粗粒子が供給されても粗粒子排出口15から排出できるので、粗粒子の沈積を解消および防止できるので、不具合を防止できる。そのため、転炉カラミの浮選を安定して効率良く行える。   As described above, the flotation machine 1 can discharge the coarse particles from the coarse particle discharge port 15 even if the coarse particles are supplied. Therefore, the sedimentation of the coarse particles can be eliminated and prevented. Therefore, flotation of converter calami can be performed stably and efficiently.

また、ゲートバルブ16により、粗粒子排出口15からの排出量を調整できるので、粗粒子とともに排出されるスラリーの量を調整できる。そのため、浮選の効率の低下を抑制できる。   Moreover, since the discharge amount from the coarse particle discharge port 15 can be adjusted by the gate valve 16, the amount of the slurry discharged together with the coarse particles can be adjusted. Therefore, a decrease in flotation efficiency can be suppressed.

さらに、本実施形態では、浮選槽10においてスラリー供給口11(スラリーの供給位置)から最も遠い位置に粗粒子排出口15が設けられている。このように配置することで、浮選槽10におけるスラリーの滞留時間を長時間確保できる。そのため、浮選の効率の低下を抑制できる。   Furthermore, in this embodiment, the coarse particle discharge port 15 is provided in the position farthest from the slurry supply port 11 (slurry supply position) in the flotation tank 10. By arrange | positioning in this way, the residence time of the slurry in the flotation tank 10 is securable for a long time. Therefore, a decrease in flotation efficiency can be suppressed.

(その他の実施形態)
上記実施形態では、粗粒子排出口15を沈鉱樋32に連通させ、粗粒子を沈鉱樋32に排出するように構成したが、これに代えて、粗粒子排出口15を別の樋に連通させ、粗粒子と沈降とを分離して排出するようにしてもよい。
このようにすれば、排出した沈降と粗粒子とを別系統で処理することができる。例えば、粗粒子をミルなどの破砕機で破砕して浮選に適した粒度にした後、再度浮遊選鉱機に供給してもよい。
(Other embodiments)
In the above embodiment, the coarse particle discharge port 15 is configured to communicate with the sedimentation slag 32 and the coarse particles are discharged to the sedimentation sediment 32. Instead, the coarse particle discharge port 15 is communicated with another slag, The particles and the sediment may be separated and discharged.
If it does in this way, the discharged sediment and coarse particles can be processed by another system. For example, coarse particles may be crushed with a crusher such as a mill to obtain a particle size suitable for flotation, and then supplied again to the flotation beneficiator.

1 浮遊選鉱機
10 浮選槽
11 スラリー供給口
12 側壁
13 スラリー界面調整ゲート
14 隔壁
15 粗粒子排出口
16 ゲートバルブ
20 撹拌機
21 軸部
22 円板
23 羽根
24 邪魔板
31 浮鉱樋
32 沈鉱樋
DESCRIPTION OF SYMBOLS 1 Flotation machine 10 Flotation tank 11 Slurry supply port 12 Side wall 13 Slurry interface adjustment gate 14 Partition 15 Coarse particle discharge port 16 Gate valve 20 Stirrer 21 Shaft part 22 Disc 23 Blade 24 Baffle plate 31 Flotation iron 32 Sedimentation iron

Claims (3)

鉱物を含有するスラリーが供給される浮選槽と、
前記スラリーに空気を供給する空気供給手段と、
前記スラリーを撹拌する撹拌手段と、
前記浮選槽の底部近傍に設けられた、前記鉱物の粗粒子を排出する粗粒子排出口と、を備える
ことを特徴とする浮遊選鉱機。
A flotation tank to which a slurry containing minerals is supplied;
Air supply means for supplying air to the slurry;
Stirring means for stirring the slurry;
And a coarse particle outlet provided near the bottom of the flotation tank for discharging coarse particles of the mineral.
前記粗粒子排出口には、排出量を調整可能な弁が設けられている
ことを特徴とする請求項1記載の浮遊選鉱機。
The float beneficiation machine according to claim 1, wherein a valve capable of adjusting a discharge amount is provided at the coarse particle discharge port.
前記粗粒子排出口は、前記浮選槽において前記スラリーの供給位置から遠い位置に設けられている
ことを特徴とする請求項1または2記載の浮遊選鉱機。
The flotation machine according to claim 1 or 2, wherein the coarse particle discharge port is provided at a position far from a supply position of the slurry in the flotation tank.
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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2015073987A (en) * 2013-10-04 2015-04-20 コリア インスティチュート オブ ジオサイエンス アンド ミネラル リソースズ Simplified valuable mineral sorting apparatus and method of sorting valuable mineral using the same

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JPS57182145A (en) * 1981-05-02 1982-11-09 Asama Kasei Kk Aminoacid fluorometry
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JPH02298371A (en) * 1989-05-10 1990-12-10 Babcock Hitachi Kk Deashing apparatus of slurry mixture of coal and water and deashing control method using the same
US5687609A (en) * 1995-10-05 1997-11-18 Cyprus Amax Minerals Company Method and apparatus for mineral flotation cell level detection
JP2008246305A (en) * 2007-03-29 2008-10-16 Taiheiyo Cement Corp Flotation machine and operation method of flotation machine
JP2012011303A (en) * 2010-06-30 2012-01-19 Taiheiyo Cement Corp Ore flotation method and system

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5444274A (en) * 1977-09-14 1979-04-07 Akira Katayanagi Device for separating floated mineral in flotator
JPS57182145A (en) * 1981-05-02 1982-11-09 Asama Kasei Kk Aminoacid fluorometry
JPS57182145U (en) * 1981-05-12 1982-11-18
JPH02298371A (en) * 1989-05-10 1990-12-10 Babcock Hitachi Kk Deashing apparatus of slurry mixture of coal and water and deashing control method using the same
US5687609A (en) * 1995-10-05 1997-11-18 Cyprus Amax Minerals Company Method and apparatus for mineral flotation cell level detection
JP2008246305A (en) * 2007-03-29 2008-10-16 Taiheiyo Cement Corp Flotation machine and operation method of flotation machine
JP2012011303A (en) * 2010-06-30 2012-01-19 Taiheiyo Cement Corp Ore flotation method and system

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2015073987A (en) * 2013-10-04 2015-04-20 コリア インスティチュート オブ ジオサイエンス アンド ミネラル リソースズ Simplified valuable mineral sorting apparatus and method of sorting valuable mineral using the same

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