JP3318893B2 - Metal contamination prevention high-speed stirrer - Google Patents

Metal contamination prevention high-speed stirrer

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Publication number
JP3318893B2
JP3318893B2 JP2000122971A JP2000122971A JP3318893B2 JP 3318893 B2 JP3318893 B2 JP 3318893B2 JP 2000122971 A JP2000122971 A JP 2000122971A JP 2000122971 A JP2000122971 A JP 2000122971A JP 3318893 B2 JP3318893 B2 JP 3318893B2
Authority
JP
Japan
Prior art keywords
stirrer
tank
stirring
stirring tank
drive shaft
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
JP2000122971A
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Japanese (ja)
Other versions
JP2001300281A (en
Inventor
彪 麻
Original Assignee
特殊機化工業株式会社
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Publication date
Application filed by 特殊機化工業株式会社 filed Critical 特殊機化工業株式会社
Priority to JP2000122971A priority Critical patent/JP3318893B2/en
Publication of JP2001300281A publication Critical patent/JP2001300281A/en
Application granted granted Critical
Publication of JP3318893B2 publication Critical patent/JP3318893B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Mixers Of The Rotary Stirring Type (AREA)

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、研磨材の粗い原料
粒子から微粒の研磨材を得るために、原料粒子と水を混
合したものを高速撹拌して粒子を微粒化する装置にあっ
て、撹拌時に研磨材中に金属成分が混入しないようにし
た撹拌装置、又は金属汚染を嫌う物質を微粒化するため
の撹拌装置に関する。研磨材を微粒化する撹拌装置で微
粒にされた研磨材は、シリコンウェーハのごとき半導体
のディスクや他の非金属材料をケミカルメカニカルポリ
シング(CMP)などによって平滑に研磨する際に使用
されるもので、前記原料粒子は、例えば平均直径が約5
0μmのシリカSiO2 又はアルミナAl2 3 であ
り、高速撹拌されて微粒になった研磨材は、平均直径が
0.1〜0.2μmである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an apparatus for atomizing particles by mixing a mixture of raw material particles and water at a high speed in order to obtain fine abrasive from raw material particles having a coarse abrasive. The present invention relates to a stirrer for preventing a metal component from being mixed into an abrasive during stirring or a stirrer for atomizing a substance which dislikes metal contamination. Abrasives that have been atomized by a stirrer that atomizes abrasives are used when a semiconductor disk such as a silicon wafer or other nonmetallic material is smoothly polished by chemical mechanical polishing (CMP) or the like. The raw material particles have, for example, an average diameter of about 5
The abrasive, which is 0 μm silica SiO 2 or alumina Al 2 O 3 and is agitated at high speed into fine particles, has an average diameter of 0.1 to 0.2 μm.

【0002】[0002]

【従来の技術】半導体を研磨する研磨材に金属成分が混
入していると、その量が僅かであっても、研磨された半
導体は、金属で汚染されて電気的特性が害される。一
方、原料粒子を微粒化するために使用する装置の撹拌槽
と撹拌具は、原料粒子の研磨作用で摩滅し易く、撹拌具
として、例えば金属羽根に硬質合成樹脂をコートしたも
のを用いると、短時間でコートが摩滅し、金属羽根の成
分が削られて原料粒子に混入するので、撹拌具を頻繁に
取り替える必要がある。これを防止するために、撹拌槽
と撹拌具を非金属の硬質合成樹脂で作り、原料粒子と水
の混合液中で撹拌具を高速回転させたところ、撹拌槽の
伝熱性が金属より低く冷却しにくいため、混合液と撹拌
具の摩擦熱によって液温が上昇し、これにより撹拌具の
温度も上昇して強度が低下し、撹拌具において力が集中
するボス部近傍で破損しやすかった。
2. Description of the Related Art If a metal component is mixed in a polishing material for polishing a semiconductor, even if the amount is small, the polished semiconductor is contaminated with metal and its electrical characteristics are impaired. On the other hand, the stirrer and stirrer of the device used to atomize the raw material particles are easily worn by the polishing action of the raw material particles, and, for example, when a metal blade coated with a hard synthetic resin is used as the stirrer, Since the coat is worn away in a short time and the components of the metal blades are shaved and mixed into the raw material particles, it is necessary to frequently replace the stirrer. To prevent this, the stirrer and stirrer were made of non-metallic hard synthetic resin, and the stirrer was rotated at high speed in a mixture of raw material particles and water. Since the liquid temperature rises due to the frictional heat between the mixed liquid and the stirrer, the temperature of the stirrer also rises to lower the strength, and the stirrer is liable to breakage in the vicinity of the boss where the force is concentrated.

【0003】[0003]

【発明が解決しようとする課題】本発明は、原料粒子を
微粒化するために必要な高密度のエネルギの投与と、そ
のために不可避的に起きる金属摩耗の防止を両立させて
実行できるように、耐摩耗性の樹脂を撹拌槽のライナー
として着脱容易に装着し、また撹拌具の耐熱性を増大し
て高温で撹拌具が破損するのを抑制し、且つ金属汚染が
生じない微粒子を生産できるようにした撹拌機を得るこ
とを課題とする。
SUMMARY OF THE INVENTION The present invention is intended to achieve both the application of high-density energy necessary for atomizing raw material particles and the prevention of metal wear which is inevitable to occur. Abrasion-resistant resin can be easily attached and detached as a liner for the stirring tank, and the heat resistance of the stirring tool is increased to prevent breakage of the stirring tool at high temperatures, and to produce fine particles free of metal contamination. It is an object of the present invention to obtain a stirrer having a reduced size.

【0004】[0004]

【課題を解決するための手段】前記課題を解決するため
の手段の一つは、請求項1に記載したとおり、円筒形の
撹拌槽内に駆動軸を同心に配置し、該撹拌槽の内径より
僅かに小径の撹拌具を駆動軸に取り付け、撹拌槽に少量
の被処理液を供給して撹拌具を駆動軸で高速回転し、被
処理液を撹拌槽内面に沿って薄い円筒状に立ち上がらせ
ながら撹拌する高速撹拌装置において、前記撹拌槽は、
冷却水室を備える金属製の外槽と、耐摩耗性と電気絶縁
性が高い硬質合成樹脂で作られ前記外槽の内面に密に嵌
合する内槽と、該内槽と同材質で内槽上端に設けたリン
グ状の堰板を備え、前記撹拌具は、耐摩耗性が高い硬質
合成樹脂で一体に作った撹拌部材と、駆動軸に着脱自在
の金属製のボス部材からなり、前記撹拌部材12は、内
槽より僅かに小径の外径をもち放射方向に無数の小穴を
貫通して設けた円筒部分と、該円筒部分から内側へ伸び
るアーム部分からなり、該アーム部に前記金属製のボス
部を固着していることを特徴とする。
According to one aspect of the present invention, a drive shaft is arranged concentrically in a cylindrical stirring tank, and the inner diameter of the stirring tank is set to a predetermined value. Attach a slightly smaller diameter stirrer to the drive shaft, supply a small amount of liquid to be stirred into the stirring tank, rotate the stirrer at high speed with the drive shaft, and turn the liquid to be processed into a thin cylindrical shape along the inner surface of the stirring tank. In a high-speed stirring device for stirring while standing up, the stirring tank,
A metal outer tub having a cooling water chamber, an inner tub made of a hard synthetic resin having high wear resistance and electrical insulation and closely fitted to the inner surface of the outer tub, and an inner tub made of the same material as the inner tub. A stirrer provided with a ring-shaped dam plate provided at the upper end of the tank, the stirrer includes a stirrer integrally formed of a hard synthetic resin having high wear resistance, and a metal boss member detachably attached to a drive shaft, The stirring member 12 has a cylindrical portion having an outer diameter slightly smaller than that of the inner tank and provided through an infinite number of small holes in the radial direction, and an arm portion extending inward from the cylindrical portion. A boss portion made of a metal is fixed.

【0005】この手段によれば、撹拌具の撹拌部材の部
分と内槽が硬質合成樹脂であるため、これらの部分が研
磨材などの被処理材料で削られても金属は露出せず、金
属成分は混入しない。また撹拌具のボスを金属にしたこ
とにより、ボスの耐熱強度が増し、撹拌の摩擦熱によっ
て撹拌具がかなり高温になっても撹拌を続けることがで
き、撹拌具を高速回転させて粗い原料粒子を短時間で微
粒子にすることができる。
According to this means, since the portion of the stirring member of the stirrer and the inner tank are made of a hard synthetic resin, the metal is not exposed even if these portions are shaved with a material to be processed such as an abrasive. No components are mixed. In addition, since the boss of the stirrer is made of metal, the heat resistance of the boss increases, and the stirring can be continued even if the stirrer becomes considerably high temperature due to frictional heat of the stirrer. Can be made into fine particles in a short time.

【0006】他の手段は、請求項2に記載したとおり、
請求項1において、前記高速撹拌機の撹拌槽の前段に、
給水口をもつ撹拌槽と、該撹拌槽の底部を通る駆動軸で
駆動される撹拌具と、撹拌槽上面に設けた原料粒子のホ
ッパーとを備える固液接触機を配置したことを特徴とす
る。この手段によれば、固液接触機において、原料粒子
と水の固液接触が速やかになされ、高速撹拌機による処
理が簡単になる。
[0006] Another means is as described in claim 2.
In claim 1, before the stirring tank of the high-speed stirrer,
A solid-liquid contactor comprising a stirring tank having a water supply port, a stirring tool driven by a drive shaft passing through the bottom of the stirring tank, and a hopper for raw material particles provided on the top of the stirring tank is provided. . According to this means, in the solid-liquid contactor, the raw material particles and the water are brought into solid-liquid contact quickly, and the processing by the high-speed stirrer is simplified.

【0007】[0007]

【発明の実施の形態】以下、図面を参照して本発明の実
施の形態を説明する。図1は本発明の高速撹拌装置の縦
断面を示し、1は高速撹拌機、2はその撹拌槽、3は金
属製の外槽、4は硬質合成樹脂製の内槽であり、外槽
3、内槽4は有底の円筒形をなしている。外槽の外側は
水室カバー5で覆われて冷却水室5aが形成され、冷却
水の流入管6と流出管7が接続されている。撹拌槽2の
中心には駆動軸8が上方から挿入され、撹拌具9がスリ
ーブ10とナット11により固定されている。
Embodiments of the present invention will be described below with reference to the drawings. FIG. 1 shows a longitudinal section of a high-speed stirrer of the present invention, wherein 1 is a high-speed stirrer, 2 is its stirring tank, 3 is an outer tank made of metal, 4 is an inner tank made of hard synthetic resin, and 3 is an outer tank. The inner tank 4 has a bottomed cylindrical shape. The outside of the outer tub is covered with a water chamber cover 5 to form a cooling water chamber 5a, and an inflow pipe 6 and an outflow pipe 7 of the cooling water are connected. A drive shaft 8 is inserted into the center of the stirring tank 2 from above, and a stirring tool 9 is fixed by a sleeve 10 and a nut 11.

【0008】撹拌具9は、硬質合成樹脂製の撹拌部材1
2と金属製のボス13からなり、両部分はボルト14a
とナット14bで連結されている。前記撹拌部材12
は、図2に示され、円筒部分12aとアーム部分12b
からなる。円筒部分12aには無数の小穴15が放射方
向に開けられており、アーム部分12bには6個のボル
ト穴16と8個の連通穴17が開けられている。ボルト
穴16には、前記ボス13を固定するためのボルト14
aが挿入され、連通穴17には撹拌時に混合液が流通す
る。撹拌槽2の底部には、内槽4内に連通するパイプ1
8、19が接続され、混合液の供給排出に用いられる。
The stirrer 9 is a stirrer 1 made of a hard synthetic resin.
2 and a boss 13 made of metal, and both parts are bolts 14a.
And a nut 14b. The stirring member 12
Is shown in FIG. 2 and includes a cylindrical portion 12a and an arm portion 12b.
Consists of The cylindrical portion 12a is provided with an infinite number of small holes 15 in the radial direction, and the arm portion 12b is provided with six bolt holes 16 and eight communication holes 17. A bolt 14 for fixing the boss 13 is provided in the bolt hole 16.
a is inserted, and the mixture flows through the communication hole 17 at the time of stirring. A pipe 1 communicating with the inner tank 4 is provided at the bottom of the stirring tank 2.
8 and 19 are connected and used for supplying and discharging the mixed liquid.

【0009】撹拌槽2の上部には、上部室20、シール
ケース21、軸受ケース22が気密に固定され、最上部
に駆動軸8を駆動する電動機が配置される。撹拌槽2の
上面と上部室20の下面の間には、硬質合成樹脂製のリ
ング状の厚い堰板23が挟持され、上部室20のの周壁
には、冷却水室5aと並列に冷却水管に連通された冷却
水室24と、混合液の出口25が設けられ、前記シール
ケース21内にはシール面26aをもつメカニカルシー
ル26が設置されている。出口25は、撹拌作業を連続
的に行なうときは解放され生産物を流出させるが、バッ
チ生産するときは閉じられ、生産物をパイプ18、19
の一方から流出させる。
An upper chamber 20, a seal case 21, and a bearing case 22 are hermetically fixed at an upper portion of the stirring tank 2, and an electric motor for driving the drive shaft 8 is disposed at an uppermost portion. A ring-shaped thick weir plate 23 made of a hard synthetic resin is sandwiched between the upper surface of the stirring tank 2 and the lower surface of the upper chamber 20, and a cooling water pipe is provided on the peripheral wall of the upper chamber 20 in parallel with the cooling water chamber 5a. A cooling water chamber 24 communicated with the cooling water chamber 24 and a mixed liquid outlet 25 are provided. A mechanical seal 26 having a sealing surface 26 a is provided in the seal case 21. The outlet 25 is opened to allow the product to flow out when the stirring operation is performed continuously, but closed when batch production is performed, and the product is supplied to the pipes 18 and 19.
Drain from one side.

【0010】前記内槽4、撹拌部材12、堰板23に用
いる硬質合成樹脂としては、超高分子量ポリエチレン、
硬質対摩耗型ナイロンなどが、耐摩耗性があって適して
いる。内槽4については、外槽3内面との間の伝熱性を
良好にするために、締まり嵌めで外槽3の内面に密着さ
せる必要があり、高い寸法精度が必要である。成形され
た内槽4の周壁外面と底壁外面は、切削加工して仕上げ
ることが望ましく、周壁内面も駆動軸8と同心性を保つ
ために切削加工するのが望ましい。内槽4の周壁の厚さ
は、熱伝導が良いようになるべく薄いのが好ましく、内
槽4の内径が80mmのものでは厚さtは2mm程度と
される。
As the hard synthetic resin used for the inner tank 4, the stirring member 12, and the weir plate 23, ultrahigh molecular weight polyethylene,
Hard versus abrasion nylon is suitable because of its abrasion resistance. The inner tank 4 needs to be tightly fitted to the inner surface of the outer tank 3 by interference fit in order to improve the heat transfer between the inner tank 4 and the inner surface of the outer tank 3, and high dimensional accuracy is required. The outer peripheral surface and the outer surface of the bottom wall of the formed inner tank 4 are desirably cut and finished, and the inner surface of the peripheral wall is desirably cut to maintain concentricity with the drive shaft 8. The thickness of the peripheral wall of the inner tank 4 is preferably as thin as possible so that heat conduction is good. When the inner diameter of the inner tank 4 is 80 mm, the thickness t is about 2 mm.

【0011】撹拌部材12については、回転のバランス
を保つために、円筒部分12aの内外周面を切削加工し
て正確な寸法に仕上げることが望ましい。ボス13、ボ
ルト14a、ナット14bの材質はステンレス鋼もしく
はチタンである。
As for the stirring member 12, it is desirable that the inner and outer peripheral surfaces of the cylindrical portion 12a be cut and finished to accurate dimensions in order to maintain the balance of rotation. The material of the boss 13, the bolt 14a and the nut 14b is stainless steel or titanium.

【0012】図1の装置において、撹拌槽2の内槽4内
に水とシリカの混合液即ちシリカスラリーLを供給して
駆動軸8を回転させ、撹拌具9を周速50〜70m/s
の高速で駆動すると、スラリーLは、撹拌具9で回転さ
せられ、瞬時に遠心力で内槽4の内面に密着して薄い円
筒状になりながら円周方向に撹拌される。そして円筒部
分12aの上下の端部から円筒部分の内側に回り、小穴
15から放射方向に流れることによっても撹拌され、短
時間で平均直径が50μmのシリカの粒子を0.1〜
0.2μm又はそれ以下の粒子に破砕することができ
る。
In the apparatus shown in FIG. 1, a mixed solution of water and silica, ie, a silica slurry L, is supplied into the inner tank 4 of the stirring tank 2 to rotate the drive shaft 8, and the stirring tool 9 is rotated at a peripheral speed of 50 to 70 m / s.
When the slurry L is driven at a high speed, the slurry L is rotated by the stirrer 9, and is instantaneously brought into close contact with the inner surface of the inner tank 4 by centrifugal force to be stirred in the circumferential direction while forming a thin cylindrical shape. Then, it is also stirred by flowing from the upper and lower ends of the cylindrical portion 12a to the inside of the cylindrical portion and flowing radially from the small hole 15, and in a short time, the silica particles having an average diameter of 50 μm are 0.1 to 0.1 μm.
It can be crushed to particles of 0.2 μm or less.

【0013】撹拌槽1内で撹拌される最大液量は、堰板
23で制限された厚さTをもつ液量で、これを超える液
量が供給されると、上部室20に流出する。装置を連続
運転する場合は、所定の粒子径になったものが上部室2
0に流れるように供給量を制御し、バッチ運転の場合
は、厚さがT以下になる液量を供給する。いずれの場合
も駆動軸8やボス13の金属部分は、起動の瞬間を除い
てシリカのスラリーLと接触しないから、シリカから研
磨作用を受けることはなく、金属成分がスラリーLに混
合することはあり得ない。
The maximum amount of liquid stirred in the stirring tank 1 is the amount of liquid having a thickness T limited by the weir plate 23. If the amount of liquid exceeding this is supplied, the liquid flows out to the upper chamber 20. When the apparatus is operated continuously, the one having a predetermined particle size is the upper chamber 2
The supply amount is controlled so as to flow to 0, and in the case of batch operation, the liquid amount whose thickness becomes T or less is supplied. In any case, the metal parts of the drive shaft 8 and the boss 13 do not come into contact with the silica slurry L except for the moment of starting, so that they do not receive a polishing action from the silica, and the metal component does not mix with the slurry L. impossible.

【0014】図3は原料粒子と水を固液接触させて混合
液とする工程と、この混合液を高速撹拌して高分散させ
る工程を備える微粒化装置である。図3において、1は
前記図1に示した高速撹拌機であり、30はその前工程
に用いる固液接触機である。この固液接触機30は、撹
拌槽31と、駆動軸33を底部から挿入した撹拌具32
と、撹拌槽31の上部に設けた投入ホッパー34を備え
る。撹拌槽31の内面には、高速撹拌機1の内槽4と同
じ硬質合成樹脂を使用し、撹拌具32にも撹拌具9と同
じ材質のものを使用するのが望ましい。
FIG. 3 shows an atomizing apparatus including a step of bringing raw material particles and water into solid-liquid contact to form a liquid mixture, and a step of stirring this liquid mixture at high speed to highly disperse the liquid. In FIG. 3, reference numeral 1 denotes the high-speed stirrer shown in FIG. 1, and reference numeral 30 denotes a solid-liquid contactor used in the preceding step. The solid-liquid contactor 30 includes a stirring tank 31 and a stirring tool 32 having a drive shaft 33 inserted from the bottom.
And a charging hopper 34 provided above the stirring tank 31. It is desirable that the same hard synthetic resin as the inner tank 4 of the high-speed stirrer 1 be used for the inner surface of the stirring tank 31, and that the stirring tool 32 be made of the same material as the stirring tool 9.

【0015】投入ホッパー34の上部には、ホッパー3
6、粉体フィーダ37、ロードセル38を備える計量ホ
ッパー35が設置され、ロードセル38で計測した所定
量の原料粒子を固液接触機30に供給するようになって
おり、撹拌槽31の底部には給水口39aに水を供給す
るための送液ポンプ39が接続されている。撹拌槽31
に水を入れ、撹拌具32を周速10〜30m/sで駆動
しながら原料粒子を粉体フィーダ37から供給すると、
固液接触が十分になされる。
A hopper 3 is provided above the input hopper 34.
6. A weighing hopper 35 having a powder feeder 37 and a load cell 38 is provided to supply a predetermined amount of raw material particles measured by the load cell 38 to the solid-liquid contactor 30. A liquid feed pump 39 for supplying water to the water supply port 39a is connected. Stirring tank 31
When the raw material particles are supplied from the powder feeder 37 while the stirring tool 32 is driven at a peripheral speed of 10 to 30 m / s,
Solid-liquid contact is made sufficiently.

【0016】固液接触機30の流出管45は、撹拌槽2
の底部のパイプ18、19の一方に接続されており、高
速撹拌機1の流出口25は、クッションタンク48に連
通され、液送ポンプ49とフィルタ50を経て取り出さ
れる。
The outflow pipe 45 of the solid-liquid contactor 30 is connected to the stirring tank 2
The outlet 25 of the high-speed stirrer 1 is connected to a cushion tank 48, and is taken out through a liquid feed pump 49 and a filter 50.

【0017】図3の装置の使用例を図4のデータを参照
して説明する。図4に記載したサンプル1〜3は、平均
粒径が46μmのシリカとアルミナを原料粒子とし、こ
れを原料袋41から取り出しながら処理する例を示し、
固液接触機30では、撹拌具32を周速28m/sで回
転し、各サンプルを60秒撹拌した後、高速撹拌機1に
送って撹拌処理している。
An example of use of the apparatus shown in FIG. 3 will be described with reference to data shown in FIG. Samples 1 to 3 described in FIG. 4 show an example in which silica and alumina having an average particle diameter of 46 μm are used as raw material particles and are processed while being taken out from the raw material bag 41.
In the solid-liquid contactor 30, the stirrer 32 is rotated at a peripheral speed of 28 m / s, each sample is stirred for 60 seconds, and then sent to the high-speed stirrer 1 to perform a stirring process.

【0018】サンプル1は、シリカの濃度が17%の混
合液で、未処理のときの金属イオンの濃度ppmは、N
i 0.9,Cr 1.5,Fe 1.51,Na
1.6と計測された。これを固液接触機30で撹拌した
後のそれぞれの濃度は、0.91,1.3,1.2,<
0.01ppmと計測され、更に、高速撹拌機1で60
m/sの周速で8秒ずつ5回撹拌することにより、それ
ぞれの濃度は、0.84,0.94,1.56,<0.
01ppmと計測された。
Sample 1 is a mixed solution having a silica concentration of 17%, and the untreated metal ion concentration ppm is N
i 0.9, Cr 1.5, Fe 1.51, Na
It was measured as 1.6. After being stirred by the solid-liquid contactor 30, the respective concentrations are 0.91, 1.3, 1.2, <
It was measured as 0.01 ppm.
By stirring 5 times for 8 seconds each at a peripheral speed of m / s, the respective concentrations were 0.84, 0.94, 1.56, <0.
It was measured as 01 ppm.

【0019】この数値において、未処理時より撹拌後の
濃度が減少するのは計測誤差によるものと解され、撹拌
中に金属イオンは増減していないと思われる。なお高速
撹拌機1で間欠的に撹拌するのは、摩擦熱で温度上昇し
た混合液が冷却水室5a側から冷却されるための時間を
与えるためである。
In these numerical values, it is understood that the concentration after stirring is lower than that in the untreated state due to a measurement error, and it is considered that the metal ions do not increase or decrease during the stirring. The reason why the high-speed stirrer 1 intermittently stirs is to allow time for the mixed liquid whose temperature has been increased by frictional heat to be cooled from the cooling water chamber 5a side.

【0020】サンプル2は、シリカの濃度が10.5%
の混合液で、未処理時の金属イオンの濃度は、Ni
0.72,Cr 0.7,Fe 0.83,Na <
0.01ppmと計測された。これを固液接触機30で
撹拌後、高速撹拌機1で60m/sの周速で7秒ずつ3
回撹拌した後の数値は、CrとFeが僅かに増加してい
るが、計測値が増減しているので、計測誤差の範囲であ
り、金属イオンの増減はないと思われる。
Sample 2 had a silica concentration of 10.5%.
, The untreated metal ion concentration is Ni
0.72, Cr 0.7, Fe 0.83, Na <
It was measured as 0.01 ppm. This was stirred by the solid-liquid contactor 30 and then by the high-speed stirrer 1 at a peripheral speed of 60 m / s for 7 seconds each.
The numerical values after the second stirring are slightly increased in Cr and Fe, but the measured values are increased and decreased, so it is within the range of measurement error, and it is considered that there is no increase or decrease in metal ions.

【0021】サンプル3は、アルミナの濃度が10.5
%の混合液で、未処理時の金属イオンの濃度は測定して
ないが、固液接触機で処理した後に計測した濃度、Ni
9.04,Cr 3.6,Fe 5.5,Na <
0.01ppmの数値と、高速撹拌機1で70m/sの
周速で9秒ずつ22回撹拌した後の数値は、Naが4.
22ppmと増加したこと以外は殆ど変化がない。この
Naは水に含まれていたものから検出されたと思われ
る。
Sample 3 had an alumina concentration of 10.5.
%, The untreated metal ion concentration was not measured, but the concentration measured after treatment with a solid-liquid contactor, Ni
9.04, Cr 3.6, Fe 5.5, Na <
The numerical value of 0.01 ppm and the numerical value after stirring 22 times for 9 seconds each at a peripheral speed of 70 m / s with the high-speed stirrer 1 are as follows.
There is almost no change except for the increase to 22 ppm. It is considered that this Na was detected from those contained in the water.

【0022】以上のとおり、前記高速撹拌機1によれ
ば、混合液と接触する内槽4と撹拌具9の撹拌部材12
の部分が無垢の硬質合成樹脂で作られているので、微粒
化された研磨材中に金属イオンが入り込むことがない。
As described above, according to the high-speed stirrer 1, the inner tank 4 in contact with the mixed liquid and the stirring member 12 of the stirrer 9 are used.
Is made of solid hard synthetic resin, so that metal ions do not enter into the atomized abrasive.

【0023】[0023]

【発明の効果】以上の説明から明らかなとおり、請求項
1の手段によれば、撹拌具の撹拌部材の部分と内槽を硬
質合成樹脂にしたことによって、金属成分による汚染を
防止でき、撹拌具のボスを金属にしたことにより、耐熱
強度が増して撹拌の摩擦熱によって撹拌具がかなり高温
になるまで撹拌を続けることができ、撹拌具を高速回転
させることによって、研磨材などの原料粒子を、短時間
で微粒の研磨材又は微粒材料にすることができる効果を
奏する。また請求項2の手段によれば、固液接触機にお
いて、原料粒子と水の固液接触が速やかになされる利点
がある。
As is apparent from the above description, according to the first aspect of the present invention, the use of a hard synthetic resin for the portion of the stirring member of the stirrer and the inner tank makes it possible to prevent contamination by metal components, The boss of the tool is made of metal, which increases the heat resistance and allows the stirring tool to continue stirring until the stirring tool becomes extremely hot due to the frictional heat of the stirring. Can be made into a fine abrasive or fine material in a short time. According to the second aspect of the present invention, there is an advantage that the solid-liquid contacting machine can quickly make solid-liquid contact between the raw material particles and water.

【図面の簡単な説明】[Brief description of the drawings]

【図1】 本発明の高速撹拌機の実施の形態を示す縦断
面図
FIG. 1 is a longitudinal sectional view showing an embodiment of a high-speed stirrer according to the present invention.

【図2】 撹拌部材を示し(a)は平面図、(b)は側
面図、(c)は断面図
FIG. 2 shows a stirring member, (a) is a plan view, (b) is a side view, and (c) is a cross-sectional view.

【図3】 高速撹拌機と固液接触機を用いた設備のフロ
ー図
FIG. 3 is a flow chart of equipment using a high-speed stirrer and a solid-liquid contactor.

【図4】 被処理物の金属イオン濃度を示す表FIG. 4 is a table showing the metal ion concentration of an object to be treated.

【符号の説明】[Explanation of symbols]

1 高速撹拌機 2、31 撹拌槽 4
内槽 5a 冷却水室 8、33 駆動軸 1
2 撹拌部材 12a 円筒部分 12b アーム部分
13 ボス 23 堰板 30 固液接触機
1 high-speed stirrer 2, 31 stirring tank 4
Inner tank 5a Cooling water chamber 8, 33 Drive shaft 1
2 Stirring member 12a Cylindrical part 12b Arm part
13 Boss 23 Weir plate 30 Solid-liquid contactor

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 円筒形の撹拌槽内に駆動軸を同心に配置
し、該撹拌槽の内径より僅かに小径の撹拌具を駆動軸に
取り付け、撹拌槽に少量の被処理液を供給して撹拌具を
駆動軸で高速回転し、被処理液を撹拌槽内面に沿って薄
い円筒状に立ち上がらせながら撹拌する高速撹拌装置に
おいて、前記撹拌槽は、冷却水室を備える金属製の外槽
と、耐摩耗性と電気絶縁性が高い硬質合成樹脂で作られ
前記外槽の内面に密に嵌合する内槽と、該内槽と同材質
で内槽上端に設けたリング状の堰板を備え、前記撹拌具
は、耐摩耗性が高い硬質合成樹脂で一体に作った撹拌部
材と、駆動軸に着脱自在の金属製のボス部材からなり、
前記撹拌部材12は、内槽より僅かに小径の外径をもち
放射方向に無数の小穴を貫通して設けた円筒部分と、該
円筒部分から内側へ伸びるアーム部分からなり、該アー
ム部に前記金属製のボス部を固着していることを特徴と
する金属汚染防止高速撹拌装置。
1. A drive shaft is arranged concentrically in a cylindrical stirring tank, a stirrer having a diameter slightly smaller than the inner diameter of the stirring tank is attached to the drive shaft, and a small amount of the liquid to be treated is supplied to the stirring tank. In a high-speed stirrer that rotates the stirrer at a high speed with a drive shaft and stirs the liquid to be treated while rising in a thin cylindrical shape along the inner surface of the stirrer, the stirrer is a metal outer tank having a cooling water chamber. An inner tank made of a hard synthetic resin having high abrasion resistance and electrical insulation and closely fitted to the inner surface of the outer tank; and a ring-shaped weir plate provided at the upper end of the inner tank with the same material as the inner tank. The stirrer comprises a stirrer integrally formed of a hard synthetic resin having high wear resistance, and a metal boss member detachably attached to the drive shaft,
The stirring member 12 has a cylindrical portion having an outer diameter slightly smaller than the inner tank and penetrating through a myriad of small holes in the radial direction, and an arm portion extending inward from the cylindrical portion. A high-speed stirrer for preventing metal contamination, wherein a metal boss is fixed.
【請求項2】 請求項1において、前記高速撹拌機の撹
拌槽の前段に、給水口をもつ撹拌槽と、該撹拌槽の底部
を通る駆動軸で駆動される撹拌具と、撹拌槽上面に設け
た原料粒子のホッパーとを備える固液接触機を配置した
ことを特徴とする金属汚染防止高速撹拌装置。
2. The stirring tank according to claim 1, wherein a stirring tank having a water supply port, a stirring tool driven by a drive shaft passing through the bottom of the stirring tank, and a stirring tank are provided in front of the stirring tank of the high-speed stirrer. A high-speed stirrer for preventing metal contamination, comprising a solid-liquid contactor provided with a hopper of raw material particles provided.
JP2000122971A 2000-04-24 2000-04-24 Metal contamination prevention high-speed stirrer Expired - Fee Related JP3318893B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2000122971A JP3318893B2 (en) 2000-04-24 2000-04-24 Metal contamination prevention high-speed stirrer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2000122971A JP3318893B2 (en) 2000-04-24 2000-04-24 Metal contamination prevention high-speed stirrer

Publications (2)

Publication Number Publication Date
JP2001300281A JP2001300281A (en) 2001-10-30
JP3318893B2 true JP3318893B2 (en) 2002-08-26

Family

ID=18633379

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2000122971A Expired - Fee Related JP3318893B2 (en) 2000-04-24 2000-04-24 Metal contamination prevention high-speed stirrer

Country Status (1)

Country Link
JP (1) JP3318893B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109289603A (en) * 2018-09-30 2019-02-01 江门市金德丰塑业科技有限公司 A kind of multi-functional chemical engineering raw material mixed stirring device

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007125454A (en) * 2005-11-01 2007-05-24 Primix Copr High-speed stirring device
KR101364300B1 (en) * 2009-10-23 2014-02-18 도요타지도샤가부시키가이샤 Stirring device
CN105170293B (en) * 2015-09-29 2023-11-24 深圳市科力纳米工程设备有限公司 Forced dispersing device
CN105771753A (en) * 2016-04-23 2016-07-20 长葛市怡盛蜂业有限公司 Honey stirring device

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109289603A (en) * 2018-09-30 2019-02-01 江门市金德丰塑业科技有限公司 A kind of multi-functional chemical engineering raw material mixed stirring device

Also Published As

Publication number Publication date
JP2001300281A (en) 2001-10-30

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