JP4551747B2 - Production method of fine powder - Google Patents
Production method of fine powder Download PDFInfo
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- JP4551747B2 JP4551747B2 JP2004339879A JP2004339879A JP4551747B2 JP 4551747 B2 JP4551747 B2 JP 4551747B2 JP 2004339879 A JP2004339879 A JP 2004339879A JP 2004339879 A JP2004339879 A JP 2004339879A JP 4551747 B2 JP4551747 B2 JP 4551747B2
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- fine powder
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- zirconium oxide
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- Disintegrating Or Milling (AREA)
Description
本発明は微粉、特に医薬品、農薬、電子部品材料、セラミック、金属、金属酸化物、機能性顔料、食品等多くの産業分野において、対象となる原料を微粉化するための製造方法に関する。 The present invention relates to a production method for pulverizing a raw material which is a subject in many industrial fields such as fine powder, particularly pharmaceuticals, agricultural chemicals, electronic component materials, ceramics, metals, metal oxides, functional pigments, foods and the like.
従来より、上記した多くの産業分野において、原料を粉化、特に微粉化するについて、種々の粉砕機の存在が知られている。この粉砕の促進、即ち、より細かくし、その処理量を増やし、付着を防止することを目的として、機械的、気流式(ジェットミルを除く)、湿式(溶液化して粉砕)にあってはメディアを介在させることが知られている。このメディアとしてはボールあるいはビーズ、時によってはロッド等が用いられている。 Conventionally, in many industrial fields described above, various pulverizers have been known for pulverizing, in particular, pulverizing raw materials. For the purpose of promoting this crushing, that is, making it finer, increasing its throughput, and preventing adhesion, media in mechanical, airflow (excluding jet mill) and wet (solution pulverization) media It is known to intervene. As this medium, a ball or a bead, and sometimes a rod or the like are used.
しかしながら、一般的にジェットミルと称される乾式気流式(施流式)粉砕機にあっては、粉砕室内にあって超高速の旋回気流に砕料をのせ、その粒子間自体の衝突によって粉砕作用を実行するものであるため、メディアを介在させると、そのメディア自体の破砕によるコンタミの発生、粉砕室の内壁を摩耗させてしまう虞が原理上考えられるため、従来はジェットミルにメディアを使用するということは行なわれることがなかった。
本発明の課題はジェットミルを用いての粉砕作用をより一層効率のよいものとし、粉砕室内面への付着を防止することであり、そのジェットミルを用いて、粗砕、中間粉砕のほか、特に微粉砕、超微粉砕の促進を図ることで、そのために、上記した虞が生ずることがないようにすることである。 The object of the present invention is to make the pulverizing action using a jet mill more efficient and prevent adhesion to the inner surface of the pulverizing chamber. Using the jet mill, in addition to coarse pulverization, intermediate pulverization, In particular, by promoting fine pulverization and ultra-fine pulverization, it is to prevent the above-described concern from occurring.
係る課題を解決するために、本発明に係る微粉の製造方法は乾式気流式粉砕機の内壁面を酸化ジルコニウムで構成もしくは被覆された粉砕室内で、対象原料に、酸化ジルコニウム製のビーズであるメディアを加え、そのメディアと対象原料を同時に環流気流にのせ攪拌させる微粉の製造方法において、前記したメディアは対象原料と予め混合状態として粉砕室内に投入されることを特徴としている。
In order to solve the problem, the fine powder manufacturing method according to the present invention is a medium in which a zirconium oxide bead is used as a target raw material in a pulverization chamber in which an inner wall surface of a dry airflow pulverizer is configured or coated with zirconium oxide. In the method for producing fine powder in which the medium and the target raw material are simultaneously stirred in a reflux airflow, the above-described medium is preliminarily mixed with the target raw material and charged into the grinding chamber.
また、本発明に係る微粉の製造方法は前記したメディアである酸化ジルコニウムのビーズは直径が数十mm〜数ミクロンで真球に近い球状であることを特徴とし、前記したメディアの対象原料に対して混合される量は容積として数十%としたことを特徴としている。
A method of manufacturing a fine powder of the present invention is characterized by beads of zirconium oxide media described above is spherical close to a true sphere tens mm~ several microns in diameter, with respect to the target material of the media The amount to be mixed is characterized by a volume of several tens of percent.
上記した構成としたことによって、本発明によれば、従来懸念されているメディア自体の破砕によるコンタミの発生や粉砕室内の壁面を摩耗により損傷してしまうこともなく、より一層ジェットミルによって砕料の粉砕を促進することができ、即ち、より細かく、処理量を増やし、付着を防止し、しかも短時間での処理を可能とする。 By adopting the above-described configuration, according to the present invention, there is no generation of contamination due to the crushing of the media itself, which has been a concern in the past, and the wall surface in the crushing chamber is not damaged by wear, and the crushing material is further increased by the jet mill. Can be promoted, i.e., more finely, increasing the processing amount, preventing adhesion, and enabling processing in a short time.
また、本発明では使用するメディアとして酸化ジルコニウム(ジルコニア)を採用することを想定している。この酸化ジルコニウムは耐火材、るつぼあるいは特殊磁器の材料として使用されるもので、耐衝撃性、耐熱性に優れているもので、メディアとして自ら破砕する虞もなく、粉砕室の内壁面も摩耗や衝突等によって傷つけられてしまうこともなくなるのである。 In the present invention, it is assumed that zirconium oxide (zirconia) is employed as a medium to be used. Zirconium oxide is used as a material for refractory materials, crucibles or special porcelain, and is excellent in impact resistance and heat resistance. It will not be damaged by a collision or the like.
後述する実施例のように実行することとして実現した。 This was implemented as in the embodiment described later.
次に、本発明の好ましい実施の例を説明する。まず、本発明に係る微粉の製造方法を実施するにあたり、用意される乾式気流式粉砕機(ジェットミル)は既知のものでよく、格別に特殊な構造、機構、付設部材等を必要とするものではないが、但し、粉砕室の内壁面は酸化ジルコニウムにより構成あるいは被覆されていることが耐衝撃として好ましい。 Next, a preferred embodiment of the present invention will be described. First, in carrying out the method for producing fine powder according to the present invention, the dry-type airflow pulverizer (jet mill) to be prepared may be a known one and requires a special structure, mechanism, attached member, etc. However, it is preferable as an impact resistance that the inner wall surface of the crushing chamber is composed or covered with zirconium oxide.
前記した乾式気流式粉砕機の粉砕室内では対象原料(砕料)とともにメディアが超高速の旋回気流にのせられることとなり、その対象原料(砕料)の微粉化を促進させることとなる。 In the pulverization chamber of the above-described dry airflow pulverizer, the medium is put on the super-high-speed swirling air flow together with the target raw material (crushed material), and the pulverization of the target raw material (crushed material) is promoted.
ここで、本発明の実施に使用するメディアとしては特に酸化ジルコニウム(ジルコニア)製のビーズが良好である。また、この酸化ジルコニウム製のビーズとしては直径が数十mm〜数ミクロン、特に0.05mm程度であり、真球に近い球状であることが好ましく、真球に近いほどメディア間の衝突では芯で当たる率よりも球表面での滑接が多くなり、メディア自体の破砕や粉砕室の内壁との衝突による摩耗、損傷が避けられることとなるのであり、さらに、直径サイズは砕料の粉砕の程度と対応しやすくなることとなる。 Here, as a medium used for carrying out the present invention, beads made of zirconium oxide (zirconia) are particularly preferable. Further, the zirconium oxide beads have a diameter of several tens to several microns, particularly about 0.05 mm, and preferably have a spherical shape close to a true sphere. The sliding surface on the surface of the sphere increases more than the hit rate, and wear and damage due to crushing of the media itself and collision with the inner wall of the crushing chamber can be avoided, and the diameter size is the degree of crushing of the crushing material. It will be easier to deal with.
また、前記したメディアの砕料に対し、投入される量はその砕料や粉砕の程度によっても異なってくるが、およそ容積として数十%程度となる。 The amount of the medium crushed is different depending on the pulverized material and the degree of pulverization, but the volume is about several tens of percent.
さらに、このメディアの投入は予め砕料と混合させた状態で粉砕室に投入することも、砕料とは別途に投入すること、及びその投入の順序も砕料の種類や目的に応じ自在に選択することが可能であり、別途に投入する場合、その投入口も共通とするか、別途とするかは設計上自在に選択することができる。 In addition, the media can be added to the pulverization chamber in a state of being mixed with the pulverized material in advance, or separately from the pulverized material, and the order of the input can be freely selected according to the type and purpose of the pulverized material. It is possible to select, and when the charging is performed separately, whether the charging port is common or separate can be freely selected in terms of design.
本発明に係る微粉の製造方法は上述のように構成されるもので、従来より一層に乾式気流式粉砕機の効率を高めるものであるが、これに加えて、分級機構を付加して、粉砕の粒度ごとに粉砕生成物を仕分けすること等も可能となり、その際に必要となるシールエアの供給機構等も遂次付設していくことが設計上可能となる。勿論、粉砕品の回収(粉砕品とメディアの分離、回収)に各種分級装置を利用できることは当然である。
The method for producing fine powder according to the present invention is configured as described above, and further improves the efficiency of the dry airflow type pulverizer than before, but in addition to this, a classification mechanism is added and pulverized. It is also possible to sort the pulverized product for each particle size, and it is possible to design a seal air supply mechanism and the like that are necessary at that time. Of course, it is natural that various classifiers can be used for recovery of the pulverized product (separation and recovery of the pulverized product and media).
Claims (3)
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JP2004339879A JP4551747B2 (en) | 2004-11-25 | 2004-11-25 | Production method of fine powder |
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JP2004339879A JP4551747B2 (en) | 2004-11-25 | 2004-11-25 | Production method of fine powder |
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JP2006150150A JP2006150150A (en) | 2006-06-15 |
JP4551747B2 true JP4551747B2 (en) | 2010-09-29 |
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JP5154103B2 (en) * | 2007-03-08 | 2013-02-27 | キョーリンフード工業株式会社 | Jet mill and manufacturing method thereof |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5815079A (en) * | 1981-07-14 | 1983-01-28 | 日本化学陶業株式会社 | Crusher member comprising zirconia sintered body |
JPS62197164A (en) * | 1986-02-24 | 1987-08-31 | コトブキ技研工業株式会社 | Method for transferring recirculation media in wet stirring ball mill |
JPS63156550A (en) * | 1986-12-20 | 1988-06-29 | 川崎重工業株式会社 | Liquid drive type medium agitation type pulverizer |
JPH01317556A (en) * | 1988-06-17 | 1989-12-22 | Freunt Ind Co Ltd | Crushing and coating apparatus |
JPH04161257A (en) * | 1990-10-23 | 1992-06-04 | Kurimoto Ltd | Air jet grinding method using grinding medium |
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Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5815079A (en) * | 1981-07-14 | 1983-01-28 | 日本化学陶業株式会社 | Crusher member comprising zirconia sintered body |
JPS62197164A (en) * | 1986-02-24 | 1987-08-31 | コトブキ技研工業株式会社 | Method for transferring recirculation media in wet stirring ball mill |
JPS63156550A (en) * | 1986-12-20 | 1988-06-29 | 川崎重工業株式会社 | Liquid drive type medium agitation type pulverizer |
JPH01317556A (en) * | 1988-06-17 | 1989-12-22 | Freunt Ind Co Ltd | Crushing and coating apparatus |
JPH04161257A (en) * | 1990-10-23 | 1992-06-04 | Kurimoto Ltd | Air jet grinding method using grinding medium |
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