JPH0389953A - Dry grinding method - Google Patents

Dry grinding method

Info

Publication number
JPH0389953A
JPH0389953A JP22623189A JP22623189A JPH0389953A JP H0389953 A JPH0389953 A JP H0389953A JP 22623189 A JP22623189 A JP 22623189A JP 22623189 A JP22623189 A JP 22623189A JP H0389953 A JPH0389953 A JP H0389953A
Authority
JP
Japan
Prior art keywords
tank
grinding
gas
media
stirring
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.)
Pending
Application number
JP22623189A
Other languages
Japanese (ja)
Inventor
Takeshi Ishikawa
剛 石川
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Mitsui Miike Engineering Corp
Original Assignee
Mitsui Miike Engineering Corp
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Mitsui Miike Engineering Corp filed Critical Mitsui Miike Engineering Corp
Priority to JP22623189A priority Critical patent/JPH0389953A/en
Publication of JPH0389953A publication Critical patent/JPH0389953A/en
Pending legal-status Critical Current

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  • Crushing And Grinding (AREA)

Abstract

PURPOSE:To enhance grinding efficiency by connecting a gas generation source having pressure higher than atmospheric pressure to a grinding tank and supplying the gas from the gas generation source into the grinding tank at the time of stirring due to a stirring member. CONSTITUTION:A material 25 to be ground and media 26 are charged in a grinding tank 4 and stirred by the stirring member 13 rotated by a drive source 9 and the material 25 to be ground are struck and ground between the media 26 to be finely pulverized. At this time, a gas generation source 17 having pressure higher than atmospheric pressure is connected to the grinding tank 4 and the gas from the gas generation source 17 is supplied into the grinding tank 4 at the time of the stirring due to the stirring member 13. As a result, the flow characteristic of the material 25 to be ground is enhanced and the stagnation thereof in the grinding tank 4 is prevented to perform uniform grinding and grinding efficiency can be enhanced.

Description

【発明の詳細な説明】 〔産業上の利用分野] この発明は、乾式粉砕方法に関し、特に、砕料をメディ
アとともに撹拌して微細化するための乾式粉砕方法に関
するものである。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to a dry pulverization method, and particularly to a dry pulverization method for stirring pulverized material together with media to make it fine.

〔従来技術および解決しようとする課題]一般に、粉砕
タンク内に砕料とメディア(たとえば、鋼球)とを投入
し、撹拌部材によって撹拌してメディア間で砕料を粉砕
して微細化を行う乾式粉砕方法にあっては、メディア間
で砕料を挟撃して摩砕しつつ粉砕して徐々に微細化する
ようになっている。
[Prior art and problems to be solved] Generally, crushed materials and media (for example, steel balls) are put into a crushing tank, and the materials are agitated by a stirring member and the crushed materials are crushed between the media to achieve fineness. In the dry pulverization method, the pulverized material is pinched between media and pulverized while grinding and gradually pulverized.

しかしながら、上記のようにして微細化する際に、砕料
が微細になると、付着力が強くなり、粉砕タンクの内周
壁やメディア等に付着し、砕料が塊状になるとともに、
滞留してしまい、これによって粉砕が阻害されてしまう
という問題点を有していた。
However, when the crushed material becomes fine as described above, its adhesion becomes strong and adheres to the inner peripheral wall of the crushing tank, the media, etc., and the crushed material becomes lumpy.
There was a problem in that the particles would stagnate, thereby hindering the grinding.

この発明は、前記のような従来の問題点を解決して砕料
の流動特性を高めて粉砕タンク内での滞留を防止して均
一な粉砕を行えて粉砕効率を高めることができる乾式粉
砕方法を提供することを目的とする。
This invention solves the above-mentioned conventional problems and provides a dry pulverization method that improves the fluidity of the pulverized material, prevents it from stagnation in the pulverization tank, enables uniform pulverization, and increases the pulverization efficiency. The purpose is to provide

〔課題を解決するための手段〕[Means to solve the problem]

上記の目的を達成するために、この発明は、粉砕タンク
の内部に砕料とメディアとを投入し、これらを駆動源で
回転される撹拌部材で攪拌し、前記メディア間で砕料を
挟撃して粉砕して微細化する乾式粉砕方法であって、前
記粉砕タンクに大気圧よりも大きい圧力を有するガス発
生源を接続し、前記撹拌部材による攪拌時に、前記ガス
発生源からのガスを前記粉砕タンク内に供給する手段を
採用した。
In order to achieve the above object, the present invention introduces crushed material and media into a crushing tank, stirs them with a stirring member rotated by a drive source, and pinches the crushed materials between the media. A dry pulverization method in which a gas generation source having a pressure higher than atmospheric pressure is connected to the pulverization tank, and the gas from the gas generation source is pulverized during stirring by the stirring member. A method of supplying it into a tank was adopted.

〔作用〕[Effect]

この発明は上記の手段を採用したことにより、撹拌部材
による砕料およびメディアの撹拌時に、つねに大気圧以
上の圧力が作用しているので、粉砕された砕料間に充分
にガスが供給され、すなわち、個々の砕料の周囲がガス
と接触することにより砕料間の付着が阻止されて砕料の
滞留が防止できることになる。
By employing the above-mentioned means, this invention always applies a pressure higher than atmospheric pressure when stirring the crushed material and media by the stirring member, so that a sufficient amount of gas is supplied between the crushed materials. That is, the periphery of each granule comes into contact with the gas, thereby preventing adhesion between the granules and preventing the stagnation of the granules.

〔実施例〕〔Example〕

第1図にはこの発明の乾式粉砕方法を実施するための乾
式粉砕装置が示されている。
FIG. 1 shows a dry grinding apparatus for carrying out the dry grinding method of the present invention.

この乾式粉砕装置は、上面が開口した円筒状をなす本体
1の周壁にジャケット板2を配設して前記本体Iおよび
ジャケット板2の上下面間を閉塞し、本体lの周壁とジ
ャケット板2との間で流路であるジャケント3が形成さ
れている粉砕タンク4を有している。
This dry crushing device has a jacket plate 2 disposed on the peripheral wall of a cylindrical main body 1 with an open upper surface to close the upper and lower surfaces of the main body I and the jacket plate 2. It has a crushing tank 4 between which a Jaquent 3, which is a flow path, is formed.

さらに、前記粉砕タンク4の上面に、粉砕タンク4の本
体1の内部を開閉可能なタンクカッ\5が取付けられて
いて、このタンクカバー5は、前記粉砕タンク4の周面
に設けた固定部6との間をボルト・ナンド7.8で固定
可能となっていて、前記粉砕タンク4の内部を密閉でき
るようになっている。
Further, a tank cover 5 that can be opened and closed inside the main body 1 of the grinding tank 4 is attached to the top surface of the grinding tank 4, and this tank cover 5 is connected to a fixing part 6 provided on the circumferential surface of the grinding tank 4. The crushing tank 4 can be fixed with bolts 7.8, and the inside of the crushing tank 4 can be hermetically sealed.

一方、前記タンクカバー5の中央部には、駆動源9によ
って回転されるとともに、垂直方向を向いた回転軸10
が、シールU’ 11を介して回転可能に配設され、こ
の回転軸10の前記粉砕タンク4の内部に位置する部分
には水平方向に複数の撹拌アーム12が放射状に突設さ
れており、前記回転軸10と撹拌アーム12とで撹拌部
材13を形成している。
On the other hand, in the center of the tank cover 5, there is a rotating shaft 10 which is rotated by a driving source 9 and is oriented in the vertical direction.
is rotatably arranged via a seal U' 11, and a plurality of stirring arms 12 are provided radially protruding horizontally from a portion of the rotating shaft 10 located inside the grinding tank 4, The rotating shaft 10 and the stirring arm 12 form a stirring member 13.

さらに、前記タンクカバー5には、配管14を介して前
記粉砕タンク4の内圧を測定するための圧力計15が設
けられ、また、前記配管14に設けた供給ノズル16に
は、外部に配置したガス供給源17がバルブ18.19
を介して接続されている。
Further, the tank cover 5 is provided with a pressure gauge 15 for measuring the internal pressure of the crushing tank 4 via a pipe 14, and a supply nozzle 16 provided on the pipe 14 is provided with a pressure gauge 15 arranged externally. Gas supply source 17 is connected to valve 18.19
connected via.

なお、20は前記流路の流入1コ、21は流路の流出口
、22は粉砕タンク4とタンクカバー5との間のシール
材、23は圧力計である。
Note that 20 is an inlet of the flow path, 21 is an outlet of the flow path, 22 is a sealing material between the crushing tank 4 and the tank cover 5, and 23 is a pressure gauge.

つぎに前記のものの作用について説明する。Next, the operation of the above will be explained.

まず、砕料25とメディア26とを前記粉砕タンク4の
本体1の内部に投入し、こののちにタンクカバー5を用
いて前記粉砕タンク4の上面を閉塞し、ボルト・ナツト
7.8で固定して、前記粉砕タンク4の内部を密閉する
First, the crushed material 25 and media 26 are put into the main body 1 of the crushing tank 4, and then the top surface of the crushing tank 4 is closed using the tank cover 5, and fixed with bolts and nuts 7.8. Then, the inside of the grinding tank 4 is sealed.

そして、前記駆動源9を起動して前記撹拌部材13を始
動して前記砕料25およびメディア26の撹拌を開始す
る。
Then, the driving source 9 is started to start the stirring member 13 and the stirring of the crushed material 25 and the media 26 is started.

すると、各砕料25が各メディア26間で挟持されつつ
打撃されて粉砕されて微小な砕料となり、その表面積が
大きくなって粉粒体間の隙間がだんだんと小さくなって
塊状になる。
Then, each crushed material 25 is held between each media 26 and is struck and crushed into fine crushed materials, whose surface area increases and the gaps between the particles gradually become smaller to form a lump.

この場合、従来の方法にあっては、塊状の内部へガスが
浸透しにくくなって流動化が損なわれ、撹拌アームの回
転力、遠心力によってさらに塊状となってしまい、粉砕
効率が低下してしまう。
In this case, in the conventional method, it becomes difficult for the gas to penetrate inside the lumps, impairing fluidization, and the rotational force and centrifugal force of the stirring arm cause them to become even more lumpy, reducing the grinding efficiency. Put it away.

これに対して、この発明にあっては、前記砕料タンク4
の内部へガス供給#+17からのガスがバルブ18.1
9および配管14を介して導入され、そして、粉砕タン
ク4の内圧は大気よりも高圧となっているので、前記撹
拌部材13およびメディア26によって微細化された塊
状の砕料の内部へガスが浸透する。
On the other hand, in this invention, the crushed material tank 4
Gas from gas supply #+17 to the inside of valve 18.1
9 and piping 14, and since the internal pressure of the crushing tank 4 is higher than the atmospheric pressure, the gas permeates into the inside of the lumpy crushed material that has been atomized by the stirring member 13 and the media 26. do.

すなわち、微細化された個々の砕料の周囲がガスと接触
することにより砕料間の付着が発生しにくくなって前記
砕料が流動し易くなり、したがって、滞留が発生せずに
粉砕効率が高められることとなる。
In other words, when the periphery of each finely divided granule comes into contact with gas, adhesion between the granules becomes less likely to occur, and the granules become more fluid, thereby increasing the pulverization efficiency without causing stagnation. It will be enhanced.

また、前記砕料を粉砕することによって、砕料の温度が
高くなった場合には、粉砕効率が低下するが、この時は
前記流入口20から冷却用の水を流入してジャケット3
内を流し、こののちに流出口21から流出させることに
より、粉砕タンク4の内部を冷却して粉砕効率を低下さ
せることなく砕料の粉砕を行うことができるものである
Furthermore, if the temperature of the crushed material becomes high due to the crushing of the crushed material, the crushing efficiency decreases, but in this case, water for cooling may be introduced from the inlet port 20 into the jacket 3.
By flushing the inside of the crushing tank 4 and then letting it flow out from the outlet 21, the crushed material can be crushed without cooling the inside of the crushing tank 4 and reducing the crushing efficiency.

したがって、この発明によれば、粉砕した砕料が微細に
なった際にも内部にガスが充分に浸透するので微細化し
た個々の砕料どうしが塊状になるのが防止され、これに
よって粉砕した砕料の流動性が高められて砕料の滞留が
阻止され、したがって、粉砕効率が著しく向上すること
となる。
Therefore, according to the present invention, even when the pulverized material becomes fine, the gas sufficiently penetrates into the inside, so that the individual pulverized materials are prevented from forming into clumps. The fluidity of the crushed material is increased and stagnation of the crushed material is prevented, and therefore the crushing efficiency is significantly improved.

〔発明の効果〕〔Effect of the invention〕

この発明は、粉砕タンクの内部に砕料とメディアとを投
入し、これらを駆動源で回転される撹拌部材で攪拌し、
前記メディア間で砕料を挟撃して粉砕して微細化する乾
式粉砕方法であって、前記粉砕タンクに大気圧よりも大
きい圧力を有するガス発生源を接続し、前記撹拌部材に
よる攪拌時に、前記ガス発生源からのガスを前記粉砕タ
ンク内に供給するようにしたので、撹拌部材で撹拌され
つつメディア間で微細化された砕料は、個々の砕料間に
前記ガス発生源からのガスが供給されるので砕料間の付
着が阻止されて粉砕タンク内で滞留することが防止でき
、これによって良好なる粉砕が行えて粉砕効率が著しく
高められるというずくれた効果を有するものである。
This invention introduces crushed material and media into a crushing tank, stirs them with a stirring member rotated by a drive source,
A dry pulverization method in which the pulverized material is pinched between the media and pulverized to make it fine, in which a gas generation source having a pressure higher than atmospheric pressure is connected to the pulverization tank, and during stirring by the stirring member, the Since the gas from the gas generation source is supplied into the crushing tank, the crushed material is agitated by the stirring member and pulverized between the media, and the gas from the gas generation source is between the individual crushed materials. Since the powder is supplied, it is possible to prevent adhesion between particles and prevent them from stagnation in the grinding tank, which has the unique effect of allowing good grinding to be carried out and significantly increasing the grinding efficiency.

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

第1図はこの発明による乾式粉砕方法を実施するための
乾式粉砕装置を示す概略断面図である。 1・・・・・・本体 2・・・・・・ジャケット板 3・・・・・・ジャケット(流路) 4・・・・・・粉砕タンク 5・・・・・・タンクカバー 6・・・・・・固定部 7.8・・・・・・ボルト・す、ト ・・・・・駆動源 O・・・・・・回転軸 1.22・・・・・・シール拐 2・・・・・・撹拌アーム 3・・・・・・撹拌部材 4・・・・・・配管 5.23・・・・・・圧力計 6・・・・・・供給ノズル 7・・・・・・ガス供給源 8.19・・・・・・ハルツ 0・・・・・・流入口 1・・・・・・流出口 5・・・・・・砕料 6・・・・・・メディア
FIG. 1 is a schematic sectional view showing a dry crushing apparatus for carrying out the dry crushing method according to the present invention. 1...Body 2...Jacket plate 3...Jacket (channel) 4...Crushing tank 5...Tank cover 6... ...Fixing part 7.8...Bolt...Drive source O...Rotating shaft 1.22...Seal removal 2... ... Stirring arm 3 ... Stirring member 4 ... Piping 5.23 ... Pressure gauge 6 ... Supply nozzle 7 ... Gas supply source 8.19... Harz 0... Inlet 1... Outlet 5... Crushed material 6... Media

Claims (1)

【特許請求の範囲】[Claims] (1)粉砕タンクの内部に砕料とメディアとを投入し、
これらを駆動源で回転される撹拌部材で撹拌し、前記メ
ディア間で砕料を挟撃して粉砕して微細化する乾式粉砕
方法であって、前記粉砕タンクに大気圧よりも大きい圧
力を有するガス発生源を接続し、前記撹拌部材による攪
拌時に、前記ガス発生源からのガスを前記粉砕タンク内
に供給することを特徴とする乾式粉砕方法。
(1) Putting the crushed material and media into the crushing tank,
A dry pulverization method in which these are stirred by a stirring member rotated by a driving source, and the pulverized material is pinched between the media and pulverized into fine particles, and the pulverization tank is filled with a gas having a pressure higher than atmospheric pressure. A dry pulverization method, characterized in that a gas generation source is connected to the pulverization tank, and gas from the gas generation source is supplied into the pulverization tank during stirring by the stirring member.
JP22623189A 1989-08-31 1989-08-31 Dry grinding method Pending JPH0389953A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP22623189A JPH0389953A (en) 1989-08-31 1989-08-31 Dry grinding method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP22623189A JPH0389953A (en) 1989-08-31 1989-08-31 Dry grinding method

Publications (1)

Publication Number Publication Date
JPH0389953A true JPH0389953A (en) 1991-04-15

Family

ID=16841951

Family Applications (1)

Application Number Title Priority Date Filing Date
JP22623189A Pending JPH0389953A (en) 1989-08-31 1989-08-31 Dry grinding method

Country Status (1)

Country Link
JP (1) JPH0389953A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010517739A (en) * 2007-02-02 2010-05-27 マシーネンファブリーク・グスタフ・アイリッヒ・ゲゼルシャフト・ミット・ベシュレンクテル・ハフツング・ウント・コムパニー・コマンディットゲゼルシャフト Continuous dry pulverization operation method of vertical pulverizer and vertical pulverizer
CN103240150A (en) * 2013-05-15 2013-08-14 王瑛玮 Novel stirring mill

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010517739A (en) * 2007-02-02 2010-05-27 マシーネンファブリーク・グスタフ・アイリッヒ・ゲゼルシャフト・ミット・ベシュレンクテル・ハフツング・ウント・コムパニー・コマンディットゲゼルシャフト Continuous dry pulverization operation method of vertical pulverizer and vertical pulverizer
CN103240150A (en) * 2013-05-15 2013-08-14 王瑛玮 Novel stirring mill

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