JPH0754006A - Production of coated semifine particle - Google Patents

Production of coated semifine particle

Info

Publication number
JPH0754006A
JPH0754006A JP5219269A JP21926993A JPH0754006A JP H0754006 A JPH0754006 A JP H0754006A JP 5219269 A JP5219269 A JP 5219269A JP 21926993 A JP21926993 A JP 21926993A JP H0754006 A JPH0754006 A JP H0754006A
Authority
JP
Japan
Prior art keywords
particles
particle
dispersion
particle powder
quasi
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.)
Granted
Application number
JP5219269A
Other languages
Japanese (ja)
Other versions
JP3545784B2 (en
Inventor
Yukiyoshi Yamada
幸良 山田
Tadashi Fuyuki
正 冬木
Satoshi Akiyama
聡 秋山
Yoshiaki Hamada
美明 濱田
Eisuke Kuroda
英輔 黒田
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.)
Nisshin Seifun Group Inc
Original Assignee
Nisshin Seifun Group Inc
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 Nisshin Seifun Group Inc filed Critical Nisshin Seifun Group Inc
Priority to JP21926993A priority Critical patent/JP3545784B2/en
Publication of JPH0754006A publication Critical patent/JPH0754006A/en
Application granted granted Critical
Publication of JP3545784B2 publication Critical patent/JP3545784B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Abstract

PURPOSE:To form highly controlled uniform coats on particles. CONSTITUTION:When core particles are put in a coating space and brought into contact with a coat forming material formed through a vapor phase or having the state of a vapor phase to produce coated semifine particles, core particles having Xmum average particle diameter DM and particle size distribution represented by ([DM/5, 5DM], >=90%) as frequency distribution on volume basis are dispersed Y% dispersity and brought into contact with the coat forming material. The combination of Xmum with Y% (X, Y) is (10-20, 80), (20-50, 90), (50-300, 95), (300-800, 97) or (>800, 99).

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、被覆準微粒子の製造方
法とそのための装置に関する。より詳細には、準微粒子
芯粒子粉体の粒子又は主に準微粒子からなる芯粒子粉体
の粒子に、被覆形成物質を被覆する被覆準微粒子の製造
方法とそのための装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing coated quasi-fine particles and an apparatus therefor. More specifically, the present invention relates to a method for producing coated quasi-fine particles in which particles of a quasi-fine particle core particle powder or particles of a core particle powder mainly composed of quasi-fine particles are coated with a coating forming substance, and an apparatus therefor.

【0002】[0002]

【従来の技術】気相法により、粉体粒子表面に無機材料
や金属材料等の被覆形成物質を、膜を始めとする種々の
形態で被覆する方法は、原理的に、(1)雰囲気の制御
が容易である、(2)基本的に被覆形成物質の選択に制
限がなく、活性金属を始めとする金属単体物質、合金、
窒化物、炭化物、硼化物、酸化物などの種々の種類の物
質を粉体粒子表面に被覆できる、(3)高純度の物質を
被覆できる、(4)被覆形成物質の被覆量を任意に制御
できるなど、他の被覆法では成し得ない大きな特徴があ
る。
2. Description of the Related Art In principle, the method of coating the surface of a powder particle with a coating forming substance such as an inorganic material or a metal material in various forms such as a film by a gas phase method is (1) Easy to control, (2) Basically, there is no limitation on the selection of the coating forming substance, and simple substance substances such as active metals, alloys,
Various types of substances such as nitrides, carbides, borides and oxides can be coated on the powder particle surface, (3) high purity substance can be coated, (4) coating amount of coating forming substance can be controlled arbitrarily There are major features such as being impossible to achieve with other coating methods.

【0003】そしてこの気相法による、例えば10μm
を越える粒子径の準微粒子の芯粒子粉体の粒子又は主に
準微粒子からなる芯粒子粉体の粒子への、高度に制御さ
れた均一な被覆、即ち個々の粒子の表面の、大きな領域
にわたって未被覆部分が残らない均一な被覆で、且つこ
の均一な被覆が全ての粒子に漏れがなく成される被覆が
要求されている。しかも、この高度に制御された均一な
被覆は、その粒子径が大きいものについては、より一層
未被覆部分が少ない均一な被覆が求められている。
Then, by this vapor phase method, for example, 10 μm
Highly controlled and uniform coating of particles of quasi-fine particle core particles having a particle size of more than or equal to or mainly of quasi-fine particles on the surface of individual particles over a large area There is a demand for a uniform coating in which no uncoated portion remains, and a coating in which this uniform coating does not leak to all particles. In addition, this highly controlled and uniform coating is required to have a smaller particle size and a uniform coating with less uncoated portions.

【0004】しかし、公知の技術として提案されている
種々の被覆装置や被覆方法では前記高度に制御された均
一な被覆はいまだ達成されていない。
However, the highly controlled and uniform coating has not yet been achieved by various coating apparatuses and coating methods proposed as known techniques.

【0005】例えば、特開昭58−31076号公報に
開示されている装置・方法によれば、PVD装置内に設
置された容器の中に芯粒子粉体の粒子を入れ、容器を電
磁気的な方法により振動させ、前記容器内の芯粒子を転
動させながらPVD法により被覆される。また、特開昭
61−30663号公報に開示されている装置によれ
ば、PVD装置内に設置された容器の中に芯粒子粉体の
粒子を入れ、容器を機械的な方法により振動させ、前記
容器内の芯粒子を転動させながらPVD法により被覆す
ることができるとされている。しかし、これらの容器の
振動により芯粒子粉体の粒子を転動させながら被覆する
装置或いは方法では、実際には、準微粒子芯粒子粉体の
粒子又は主に準微粒子からなる芯粒子粉体の粒子は何層
にも重なった状態で摺動するのみで単一粒子状態で被覆
できなかった。
For example, according to the apparatus and method disclosed in Japanese Patent Application Laid-Open No. 58-31076, particles of core particle powder are put in a container installed in a PVD apparatus and the container is electromagnetically charged. The core particles in the container are vibrated by the method to roll the particles, and the core particles are coated by the PVD method. Further, according to the device disclosed in JP-A-61-30663, particles of core particle powder are put into a container installed in a PVD device, and the container is vibrated by a mechanical method. It is said that the core particles in the container can be coated by the PVD method while rolling. However, in an apparatus or method for coating while rolling the particles of the core particle powder by the vibration of these containers, in practice, the particles of the quasi-fine particle core particle powder or the core particle powder mainly composed of quasi-fine particles are The particles were slid only in the state of stacking many layers, and could not be coated in a single particle state.

【0006】特開平3−153864号公報に開示され
ている装置及び方法は、内面に障壁及び/又は凹凸を備
えた回転容器内に粒子を入れ、回転容器を回転しながら
蒸着法により芯粒子表面に被覆を行なうことを目的とす
るものであるが、このような装置或いは方法において、
準微粒子芯粒子粉体の粒子又は主に準微粒子からなる芯
粒子粉体の粒子は、何層にも重なった状態で多くの粒子
が接触したまま軽く撹拌されるだけで、単一粒子状態で
被覆できなかった。
The apparatus and method disclosed in Japanese Patent Laid-Open No. 153864/1993 discloses a method of depositing particles in a rotating container having a barrier and / or unevenness on the inner surface, and rotating the rotating container to form a core particle surface by vapor deposition. The purpose is to perform coating on the
The particles of the quasi-fine particle core particle powder or the particles of the core particle powder mainly composed of quasi-fine particles are in a single particle state simply by agitating lightly while many particles are in contact with each other in many layers. It could not be covered.

【0007】特開昭58−141375号公報には、反
応ガス雰囲気中に置かれた粉体を反応ガスの流れと重力
の作用とによって浮遊させて、反応ガスの化学反応によ
り生成される析出物質によって粉体の表面を被覆する装
置が開示されている。又、特開平2−43377号公報
には、粒子を減圧下において流動化させながら、熱化学
反応処理を行い被覆を行なう方法が開示されている。
又、特開昭64−80437号公報には、低・高周波合
成音波により芯粒子粉体の凝集体を崩して流動化させ被
覆する方法が開示されている。しかし、これらの気流や
振動により準微粒子芯粒子粉体の粒子又は主に準微粒子
からなる芯粒子粉体の粒子の流動層利用する方法又は装
置では、全ての芯粒子を同じ様に単一粒子状態で独立に
流動、浮遊させることは事実上不可能であり、粒子同士
が陰になってできる各粒子の被覆むらをなくすことがで
きなかった。
[0007] Japanese Patent Laid-Open No. Sho 58-141375 discloses a deposit material produced by a chemical reaction of a reaction gas by suspending a powder placed in a reaction gas atmosphere by the flow of the reaction gas and the action of gravity. Discloses a device for coating the surface of powder. Further, Japanese Patent Application Laid-Open No. 2-43377 discloses a method of performing coating by performing thermochemical reaction treatment while fluidizing particles under reduced pressure.
Further, JP-A-64-80437 discloses a method in which agglomerates of core particle powder are broken down and fluidized by low and high frequency synthetic sound waves to cover the particles. However, in the method or apparatus utilizing the fluidized bed of the particles of the quasi-fine particle core particle powder or the particles of the core particle powder mainly consisting of the quasi-fine particles by these air flows and vibrations, all the core particles are the same as a single particle. It is virtually impossible to independently flow and float in a state, and it was not possible to eliminate the uneven coating of each particle due to the shadow of the particles.

【0008】特開昭54−153789号公報には、金
属の蒸気を発生させた真空容器内を粉末材料を落下させ
金属を被覆する装置が開示されている。又、特開昭60
−47004号公報には真空槽中の高周波プラズマ領域
にモノマーガスと粉体粒子を導入し、プラズマ重合によ
り有機物の被覆膜を形成させる方法が開示されている。
これらの装置或いは方法の如く、導入するたけでは準微
粒子芯粒子粉体の粒子又は主に準微粒子からなる芯粒子
粉体の粒子は、単一粒子状態でない凝集体を形成して落
下するだけで、粒子の陰ができて被覆むらができたり、
凝集体の内部の粒子は全く被覆されなかったり、或いは
単一粒子に被覆されたものにくらべ被覆量の違いが生じ
てしまった。
Japanese Unexamined Patent Publication No. 54-153789 discloses an apparatus for coating a metal by dropping a powder material in a vacuum container in which vapor of metal is generated. In addition, JP-A-60
-47004 discloses a method of introducing a monomer gas and powder particles into a high-frequency plasma region in a vacuum chamber and forming a coating film of an organic substance by plasma polymerization.
As with these devices or methods, the particles of the quasi-fine particle core particle powder or the particles of the core particle powder mainly composed of quasi-fine particles can be simply formed by forming aggregates which are not in a single particle state and falling by introducing them. , The shade of the particles creates uneven coating,
The particles inside the agglomerates were not coated at all, or there was a difference in the coating amount compared to the coating of single particles.

【0009】特開昭62−250172号公報には、前
処理として、ジェットミル処理した粉体を、減圧加熱処
理室で滞留せしめ、ここで加熱処理を施した後、粉体フ
ィーダーでスパッタリング室に自然落下により導入せし
め、ターゲットを垂直に設けた円筒状のスパッタリング
室に自然落下させ被覆させる装置及び方法が開示されて
いる。又、特開平2−153068号公報には、前処理
として、ジェットミル処理した粉体を、減圧加熱処理室
で滞留させ、ここで加熱処理を施した後、粉体フィーダ
ーでスパッタリング室のスパッタリング源を納めた回転
容器に(単一粒子でない)粉体状で導入し、容器を回転
させた状態でスパッタリングする装置及び方法が開示さ
れている。これら装置及び方法では、被覆前の加熱工程
で、ジェットミル処理した芯粒子粉体を滞留させる工程
があり、加熱工程でのこの粉体の滞留のため再び単一粒
子状態でない凝集体を形成し、結局被覆工程ではこの凝
集体は単一粒子状態にはならない。
In JP-A-62-250172, as a pretreatment, powder subjected to jet mill treatment is retained in a reduced-pressure heat treatment chamber, and after heat treatment is performed therein, the powder is fed into a sputtering chamber with a powder feeder. An apparatus and a method are disclosed in which the target is introduced by natural fall and the target is naturally dropped and coated in a cylindrical sputtering chamber provided vertically. Further, in Japanese Patent Application Laid-Open No. 2-153068, as a pretreatment, powder subjected to jet mill treatment is retained in a reduced pressure heat treatment chamber, where after heat treatment is performed, a powder feeder is used to sputter the sputtering source in the sputtering chamber. There is disclosed an apparatus and a method for introducing powder in the form of powder (not single particles) into a rotating container containing therein and sputtering the container while rotating the container. In these devices and methods, there is a step of retaining the jet milled core particle powder in the heating step before coating, and due to the retention of this powder in the heating step, aggregates that are not in the single particle state are formed again. After all, in the coating process, this aggregate does not become a single particle state.

【0010】以上のように、従来公知の技術では、いず
れも準微粒子芯粒子粉体の粒子又は主に準微粒子からな
る芯粒子粉体の粒子に被覆する装置或いは方法としての
問題解決はなされておらず、準微粒子の芯粒子粉体の粒
子又は主に準微粒子からなる芯粒子粉体の粒子は、現実
には接触したままの凝集体の状態で被覆処理に供され、
そのために各粒子への高度に制御された均一な被覆がな
されることはなかった。すなわち高度に制御された均一
な被覆がなされる被覆準微粒子の製造方法もそのための
製造装置もなかった。それが為、事実上、上記問題が解
消出来なかった。
As described above, all of the conventionally known techniques have solved problems as an apparatus or method for coating particles of quasi-fine particle core particle powder or particles of core particle powder mainly composed of quasi-fine particles. Not present, particles of core particles powder of quasi-fine particles or particles of core particles powder mainly consisting of quasi-fine particles are actually subjected to coating treatment in the state of agglomerates in contact with each other,
This did not result in a highly controlled and uniform coating on each particle. That is, there has been neither a method for producing coated quasi-fine particles capable of performing highly controlled and uniform coating nor a production apparatus therefor. As a result, the above problems could not be practically resolved.

【0011】[0011]

【発明が解決しようとする課題】従って、現実に、例え
ば準微粒子が10μmを越える粒子である準微粒子の芯
粒子粉体の粒子又は主に準微粒子からなる芯粒子粉体の
粒子への、高度に制御された均一な被覆、即ち個々の粒
子の表面の大きな領域にわたって未被覆部分が残らない
均一な被覆で、且つこの均一な被覆が全ての粒子に漏れ
がなく成される被覆が要求されている。しかも、その粒
子径が大きいものについては、より一層未被覆部分が少
ない均一な被覆ができる被覆準微粒子の製造方法とその
ための装置が強く求められている。
Therefore, in reality, for example, the particles of the quasi-fine particles of which the quasi-fine particles are particles having a size of more than 10 μm or the particles of the core-particle powder mainly composed of quasi-fine particles are highly advanced. Controlled uniform coating, i.e. a uniform coating with no uncoated portion over a large area of the surface of the individual particles, and this uniform coating is required for all particles to be leak-tight. There is. In addition, for those having a large particle diameter, there is a strong demand for a method for producing coated quasi-fine particles and an apparatus therefor capable of uniform coating with a smaller number of uncoated portions.

【0012】本発明は、準微粒子芯粒子粉体の粒子又は
主に準微粒子からなる芯粒子粉体の粒子への、高度に制
御された均一な被覆、即ち個々の粒子の表面の大きな領
域にわたって未被覆部分が残らない均一な被覆で、且つ
この均一な被覆が全ての粒子に漏れがなく成される被覆
で、しかもその粒子径が大きいものについては、より一
層未被覆部分が少ない均一な被覆ができる被覆準微粒子
の製造方法とそのための装置を提供することを目的とす
る。
The present invention is directed to a highly controlled and uniform coating of particles of quasi-fine core particle powder or particles of core particle powder consisting essentially of quasi-fine particles over a large area of the surface of individual particles. A uniform coating in which no uncoated portion remains, and this uniform coating is a coating in which all particles do not leak, and for particles with a large particle size, a uniform coating with less uncoated portion It is an object of the present invention to provide a method for producing coated quasi-fine particles and an apparatus therefor.

【0013】[0013]

【課題を解決するための手段】前記課題を解決するため
に、本発明者が鋭意研究を重ねた結果、準微粒子芯粒子
粉体の粒子又は主に準微粒子からなる芯粒子粉体の粒子
への、高度に制御された均一な被覆、即ち個々の粒子の
表面の大きな領域にわたって未被覆部分が残らない均一
な被覆で、且つ均一な被覆が全ての粒子に漏れがなく成
される被覆で、しかも、その粒子径が大きいものについ
ては、より一層未被覆部分が少ない均一な被覆を成すた
めには、(1)体積基準頻度分布で平均粒子径が10μ
mを越え、20μm以下の芯粒子粉体の粒子が主に単一
粒子状態で気中に存在する高分散芯粒子粉体の粒子・気
体混合物中の芯粒子粉体の粒子を、分散度βが80%以
上である高い分散状態の被覆空間の被覆開始領域でか、
又は(2)体積基準頻度分布で平均粒子径が20μmを
越え、50μm以下の芯粒子粉体の粒子が主に単一粒子
状態で気中に存在する高分散芯粒子粉体の粒子・気体混
合物中の芯粒子粉体の粒子を、分散度βが90%以上で
ある高い分散状態の被覆空間の被覆開始領域でか、又は
(3)体積基準頻度分布で平均粒子径が50μmを越
え、300μm以下の芯粒子粉体の粒子が主に単一粒子
状態で気中に存在する高分散芯粒子粉体の粒子・気体混
合物中の芯粒子粉体の粒子を、分散度βが95%以上で
ある高い分散状態の被覆空間の被覆開始領域でか、又は
(4)体積基準頻度分布で平均粒子径が300μmを越
え、800μm以下の芯粒子粉体の粒子が主に単一粒子
状態で気中に存在する高分散芯粒子粉体の粒子・気体混
合物中の芯粒子粉体の粒子を、分散度βが97%以上で
ある高い分散状態の被覆空間の被覆開始領域でか、又は
(5)体積基準頻度分布で平均粒子径が800μmを越
える芯粒子粉体の粒子が主に単一粒子状態で気中に存在
する高分散芯粒子粉体の粒子・気体混合物中の芯粒子粉
体の粒子を、分散度βが99%以上である高い分散状態
の被覆空間の被覆開始領域で被覆を開始しなければなら
ないことを見い出した。
[Means for Solving the Problems] In order to solve the above-mentioned problems, as a result of intensive studies by the present inventors, particles of a quasi-fine particle core particle powder or particles of a core particle powder mainly composed of quasi-fine particles are obtained. A highly controlled and uniform coating, i.e. a uniform coating with no uncoated portion remaining over a large area of the surface of the individual particles, and a uniform coating in which all particles are made leak-proof, Moreover, for those having a large particle diameter, in order to form a uniform coating with less uncoated portions, (1) the average particle diameter is 10 μm in the volume standard frequency distribution.
Particles of core particle powder having a particle diameter of more than 20 μm and not more than 20 μm are mainly present in the air in a single particle state. In the coating start region of the coating space in a highly dispersed state where
Or (2) a particle / gas mixture of highly dispersed core particle powder in which particles of the core particle powder having an average particle diameter of more than 20 μm and 50 μm or less in the volume-based frequency distribution mainly exist in the air in a single particle state. The particles of the core particle powder are 300 μm in the coating start region of the coating space in a highly dispersed state where the dispersity β is 90% or more, or (3) the average particle size exceeds 50 μm and 300 μm in the volume standard frequency distribution. The following core particle powder particles are mainly present in the air in the form of a single particle. Highly dispersed core particle powder particles ・ The core particle powder particles in the gas mixture have a dispersity β of 95% or more. In the coating start region of the coating space in a certain high dispersion state, or (4) in the volume standard frequency distribution, the average particle size exceeds 300 μm and the particles of the core particle powder of 800 μm or less are mainly in the single particle state in the air. Particles of highly dispersed core particles in the air / particles of core particles in a gas mixture Is mainly in the coating start region of the coating space in a highly dispersed state where the dispersity β is 97% or more, or (5) particles of the core particle powder having an average particle diameter of more than 800 μm in the volume standard frequency distribution. In the coating start region of the coating space in a highly dispersed state where the dispersity β is 99% or more, the particles of the highly dispersed core particle powder present in the air in a single particle state / the particles of the core particle powder in the gas mixture are It was found that the coating had to be started.

【0014】より詳しくは、(I)芯粒子粉体の粒子が
主に単一粒子状態で気中に存在する高分散芯粒子粉体の
粒子・気体混合物の状態の芯粒子粉体の粒子は、滞留さ
せなくとも、時間の経過と共に主に乱流凝集等により再
凝集する傾向にあり、一旦再凝集すると、前記分散処理
前の凝集体と同じく特別に高い分散性能を有する分散処
理手段により分散させなければこの再凝集の状態を崩し
て高度に分散、即ち一個一個の単位の単一粒子状態へ再
分散させることが困難であり、このため、(1)体積基
準頻度分布で平均粒子径が10μmを越え、20μm以
下の芯粒子粉体の粒子が主に単一粒子状態で気中に存在
する高分散芯粒子粉体の粒子・気体混合物中の芯粒子粉
体の粒子を、分散度βが80%以上である高い分散状態
でか、又は(2)体積基準頻度分布で平均粒子径が20
μmを越え、50μm以下の芯粒子粉体の粒子が主に単
一粒子状態で気中に存在する高分散芯粒子粉体の粒子・
気体混合物中の芯粒子粉体の粒子を、分散度βが90%
以上である高い分散状態でか、又は(3)体積基準頻度
分布で平均粒子径が50μmを越え、300μm以下の
芯粒子粉体の粒子が主に単一粒子状態で気中に存在する
高分散芯粒子粉体の粒子・気体混合物中の芯粒子粉体の
粒子を、分散度βで95%以上である高い分散状態で
か、又は(4)体積基準頻度分布で平均粒子径が300
μmを越え、800μm以下の芯粒子粉体の粒子が主に
単一粒子状態で気中に存在する高分散芯粒子粉体の粒子
・気体混合物中の芯粒子粉体の粒子を、分散度βが97
%以上である高い分散状態の被覆空間の被覆開始領域で
か、又は(5)体積基準頻度分布で平均粒子径が800
μmを越える芯粒子粉体の粒子が主に単一粒子状態で気
中に存在する高分散芯粒子粉体の粒子・気体混合物中の
芯粒子粉体の粒子を、分散度βが99%以上である高い
分散状態で被覆空間の被覆開始領域に導く必要があるこ
と、またそのためには、(II)この芯粒子粉体からなる
凝集体を崩し、且つ粒子径に応じた非常に高い分散度で
気中に分散せしめる、一以上からなる特別に高い分散性
能を有する分散処理手段群が必要であることを見い出し
て本発明に至った。
More specifically, (I) the particles of the core particle powder are mainly in the form of a single particle in the air. The particles of the highly dispersed core particle powder and the particles of the core particle powder in the gas mixture state are as follows: However, even if it does not stay, it tends to reaggregate mainly due to turbulent agglomeration with the passage of time, and once reaggregated, it is dispersed by a dispersion treatment means having a particularly high dispersibility like the aggregate before the dispersion treatment. If this is not done, it is difficult to break this re-aggregation state and disperse it to a high degree, that is, to re-disperse it into a single particle state of each unit. Therefore, (1) in the volume standard frequency distribution, the average particle diameter The particles of the core particle powder having a particle diameter of more than 10 μm and 20 μm or less are mainly present in the air in a single particle state. In a highly dispersed state where the ratio is 80% or more, or (2) body The average particle diameter of the reference frequency distribution 20
Particles of highly dispersed core particle powder in which particles of core particle powder having a size of more than 50 μm and less than 50 μm mainly exist in the air in a single particle state.
The degree of dispersion β of the core particles in the gas mixture is 90%.
In the high dispersion state as described above, or (3) the high dispersion in which particles of the core particle powder having an average particle size of more than 50 μm and 300 μm or less in the volume standard frequency distribution are mainly present in the air in a single particle state. The particles of the core particle powder in the gas / particle mixture of the core particle powder are in a highly dispersed state with a dispersity β of 95% or more, or (4) the volume-based frequency distribution has an average particle diameter of 300.
Particles of the core particle powder having a particle size of more than 800 μm and more than 800 μm mainly exist in the air in the form of a single particle. Is 97
% Or more in the coating start region of the coating space in a highly dispersed state, or (5) the volume-based frequency distribution has an average particle size of 800
Particles of core particle powder exceeding μm mainly exist in the air in a single particle state. Particles of highly dispersed core particle powder / particles of core particle powder in a gas mixture with a dispersity β of 99% or more. It is necessary to lead to the coating start region of the coating space in a highly dispersed state, and for that purpose, (II) the agglomerates composed of the core particle powder are destroyed and the degree of dispersion is very high according to the particle diameter. The present invention was found by the need for a dispersion treatment means group having one or more particularly high dispersion performances, which can be dispersed in the air.

【0015】即ち、本発明は芯粒子粉体を被覆空間に投
入し、気相を経て生成する被覆形成物質前駆体及び/又
は気相状態の被覆形成物質前駆体を、芯粒子粉体の粒子
に接触及び/又は衝突させて、芯粒子粉体の粒子の表面
を被覆形成物質で被覆する被覆準微粒子の製造装置にお
いて、 (A) 準微粒子高分散処理手段群の最終処理手段が、
(a) この芯粒子粉体の粒子を気中に分散させる分散
手段、及び(b) 芯粒子粉体の粒子を気中に分散させ
た芯粒子粉体の粒子と気体の混合物において低分散芯粒
子粉体部分を分離し、芯粒子粉体の粒子が主に単一粒子
状態で気中に存在する高分散芯粒子粉体の粒子・気体混
合物を選択する高分散芯粒子粉体の粒子・気体混合物選
択手段とこの高分散芯粒子粉体の粒子・気体混合物選択
手段により分離された低分散芯粒子粉体部分を準微粒子
高分散処理手段群中の分散手段の内の最終分散手段及び
/又は最終分散手段以前の処理手段に搬送するフィード
バック手段とを備えた高分散芯粒子粉体の粒子・気体混
合物選択手段、から選ばれる準微粒子高分散処理手段群
により、体積基準頻度分布で平均粒子径が10μmを越
える準微粒子芯粒子粉体の粒子又は主に準微粒子からな
る芯粒子粉体の粒子を、気中に分散させて高分散芯粒子
粉体の粒子・気体混合物とする分散工程、 (B) この分散工程で分散させた芯粒子粉体の粒子
を、その平均粒子径が10μmを越え20μm以下のと
きには分散度βが80%以上、20μmを越え50μm
以下のときには分散度βが90%以上、50μmを越え
300μm以下のときには分散度βが95%以上、30
0μmを越え800μm以下のときは分散度βが97%
以上、そして800μmを越えるときは分散度βが99
%以上の分散状態で、被覆空間の被覆開始領域において
被覆形成物質前駆体と接触及び/又は衝突させて被覆を
開始する被覆工程、を設けたことを特徴とする、被覆準
微粒子の製造方法を提供するものである。
That is, according to the present invention, the core particle powder is charged into the coating space, and the coating forming substance precursor and / or the gas phase state coating forming substance precursor produced through the gas phase are converted into particles of the core particle powder. In the apparatus for producing coated quasi-fine particles, which comprises contacting and / or colliding with a core particle powder, the surface of the particles of the core particle powder is coated with the coating-forming substance.
(A) Dispersing means for dispersing particles of the core particle powder in air, and (b) Low dispersion core in a mixture of particles of core particle powder and gas in which particles of the core particle powder are dispersed in air. Particles of high-dispersion core particle powder that separates the particle powder portion and particles of the core particle powder are mainly present in the air in a single particle state The low-dispersion core particle powder portion separated by the gas mixture selection means and the particle / gas mixture selection means of the high-dispersion core particle powder is the final dispersion means of the dispersion means in the quasi-fine particle high-dispersion processing means group and / or Alternatively, by means of a quasi-fine particle high dispersion treatment means group selected from a highly dispersed core particle powder particle / gas mixture selection means provided with a feedback means for conveying to a treatment means before the final dispersion means, average particles in a volume-based frequency distribution Quasi-fine core particle powder with a diameter exceeding 10 μm A dispersion step of dispersing body particles or particles of core particle powder mainly composed of quasi-fine particles in the air to form a particle / gas mixture of highly dispersed core particle powder, (B) dispersed in this dispersion step When the average particle size of the core particle powder is more than 10 μm and less than 20 μm, the dispersity β is 80% or more, and more than 20 μm and 50 μm.
When the dispersity β is 90% or more, and when the dispersity β exceeds 50 μm and is 300 μm or less, the dispersity β is 95% or more and 30
When it exceeds 0 μm and 800 μm or less, the dispersity β is 97%.
Above, and when it exceeds 800 μm, the dispersion degree β is 99
%, The coating step of contacting and / or colliding with the coating forming material precursor in the coating starting region of the coating space to start coating, is provided. It is provided.

【0016】更に本発明は前記した被覆準微粒子の製造
方法において体積基準頻度分布で平均粒径が10μmを
越え、20μm以下の芯粒子粉体を準微粒子高分散処理
手段群の最終処理により気中に分散させて高分散芯粒子
粉体の粒子・気体混合物とし、その芯粒子粉体の粒子の
分散度βを80%以上とするか、又は体積基準頻度分布
で平均粒径が20μmを越え、50μm以下の芯粒子粉
体を準微粒子高分散処理手段群の最終処理により気中に
分散させて高分散芯粒子粉体の粒子・気体混合物としそ
の芯粒子粉体の粒子の分散度βを90%以上とするか、
又は体積基準頻度分布で平均粒径が50μmを越え、3
00μm以下の芯粒子粉体を準微粒子高分散処理手段群
の最終処理により気中に分散させて高分散芯粒子粉体の
粒子・気体混合物としその芯粒子粉体の粒子の分散度β
を95%以上とするか、又は体積基準頻度分布で平均粒
子径が300μmを越え800μm以下の芯粒子粉体
を、準微粒子高分散処理手段群の最終処理により気中に
分散させて高分散芯粒子粉体の粒子・気体混合物とし、
その芯粒子粉体の粒子の分散度βを97%以上とする
か、又は体積基準頻度分布で平均粒子径が800μmを
越える芯粒子粉体を、準微粒子高分散処理手段群の最終
処理により気中に分散させて高分散芯粒子粉体の粒子・
気体混合物とし、その芯粒子粉体の粒子の分散度βを9
9%以上とする分散性能を有する準微粒子高分散処理手
段群による分散工程を設け、準微粒子高分散処理手段群
による高分散芯粒子粉体の粒子・気体混合物を被覆工程
に直接放出するか、又は分散工程と被覆工程の間に、準
微粒子高分散処理手段群の高分散芯粒子粉体の粒子・気
体混合物を放出する放出部から、直接放出するか、又は
搬送に不可避の、中空部材、中空を形成せしめる部材か
らなる中間部材、及びパイプから選択される一種類又は
それ以上の部材を介して搬送するか、及び/又は、前記
分散性能で気中に分散させた高分散芯粒子粉体の粒子・
気体混合物中の粒子の気中分散状態を維持する気中分散
維持手段、前記分散性能で気中に分散させた高分散芯粒
子粉体の粒子・気体混合物中の粒子の気中分散状態を高
める気中分散促進手段、芯粒子粉体の粒子と気体との混
合物の内の、低分散芯粒子粉体部分を分離し、芯粒子粉
体の粒子が主に単一粒子状態で気中に存在する高分散芯
粒子粉体の粒子・気体混合物を選択する高分散芯粒子粉
体の粒子・気体混合物選択手段の一種又はそれ以上を介
して搬送する、搬送工程を設けることを特徴とする被覆
準微粒子の製造方法にも関する。
Further, according to the present invention, in the above-mentioned method for producing coated quasi-fine particles, a core particle powder having an average particle size of more than 10 μm and 20 μm or less in a volume-based frequency distribution is subjected to the final treatment in the quasi-fine particle high dispersion treatment means group in the air. To form a particle / gas mixture of highly dispersed core particle powder, and the degree of dispersion β of the particles of the core particle powder is 80% or more, or the average particle diameter exceeds 20 μm in the volume standard frequency distribution, The core particle powder having a particle size of 50 μm or less is dispersed in the air by the final treatment of the quasi-fine particle high dispersion treatment means group to obtain a particle / gas mixture of the highly dispersed core particle powder, and the degree of dispersion β of the particles of the core particle powder is 90. % Or more,
Or, the volume-based frequency distribution has an average particle size exceeding 50 μm and 3
The core particle powder having a particle diameter of 00 μm or less is dispersed in the air by the final treatment of the quasi-fine particle high dispersion treatment means group to obtain a particle / gas mixture of the highly dispersed core particle powder, and the degree of dispersion β of the particles of the core particle powder.
Of 95% or more, or a core particle powder having an average particle diameter of more than 300 μm and 800 μm or less in a volume-based frequency distribution is dispersed in the air by the final treatment of the quasi-fine particle high-dispersion treatment means group to obtain a highly dispersed core. As a particle-gas mixture of particle powder,
A core particle powder having a particle dispersity β of 97% or more in the core particle powder or an average particle diameter of more than 800 μm in a volume-based frequency distribution is treated by a final treatment with a group of quasi-fine particle high dispersion treatment means. Particles of highly dispersed core particles powder dispersed in
As a gas mixture, the degree of particle dispersion β of the core particle powder is 9
Whether a dispersion process is performed by a group of quasi-fine particle high dispersion treatment means having a dispersion performance of 9% or more, and the particle / gas mixture of the highly dispersed core particle powder is directly discharged to the coating step by the quasi-fine particle high dispersion treatment means group. Or, between the dispersion step and the coating step, directly from the discharge part that discharges the particle / gas mixture of the highly dispersed core particle powder of the quasi-fine particle high dispersion treatment means group, or directly unavoidable for transportation, a hollow member, Highly dispersed core particle powder which is conveyed through one or more members selected from an intermediate member made of a member forming a hollow and a pipe and / or dispersed in the air with the above-mentioned dispersion performance. Particles of
In-air dispersion maintaining means for maintaining the air-dispersed state of particles in a gas mixture, the particles of highly dispersed core particle powder dispersed in air with the above-mentioned dispersion performance, and enhancing the air-dispersed state of particles in a gas mixture Air dispersion promoting means, separating low-dispersion core particle powder portion of a mixture of core particle powder particles and gas, and the core particle powder particles mainly exist in the air in a single particle state. A coating step for transporting the particles / gas mixture of highly dispersed core particle powder through one or more means for selecting particles / gas mixture of highly dispersed core particle powder It also relates to a method for producing fine particles.

【0017】更に本発明は、前記した被覆準微粒子の製
造方法において、体積基準頻度分布で平均粒子径が10
μmを越え、20μm以下の芯粒子粉体を、準微粒子高
分散処理手段群の最終処理により気中に分散させて高分
散芯粒子粉体の粒子・気体混合物とし、その芯粒子粉体
の粒子の分散度βを80%以上とするか、又は体積基準
頻度分布で平均粒子径が20μmを越え、50μm以下
の芯粒子粉体を、準微粒子高分散処理手段群の最終処理
により気中に分散させて高分散芯粒子粉体の粒子・気体
混合物とし、その芯粒子粉体の粒子の分散度βを90%
以上とするか、又は体積基準頻度分布で平均粒子径が5
0μmを越え、300μm以下の芯粒子粉体を準微粒子
高分散処理手段群の最終処理により気中に分散させて高
分散芯粒子粉体の粒子・気体混合物とし、その芯粒子粉
体の粒子の分散度βを95%以上とするか、又は体積基
準頻度分布で平均粒子径が300μmを越え800μm
以下の芯粒子粉体を、準微粒子高分散処理手段群の最終
処理により気中に分散させて高分散芯粒子粉体の粒子・
気体混合物とし、その芯粒子粉体の粒子の分散度βを9
7%以上とする分散性能を有する準微粒子高分散処理手
段群、又は体積基準頻度分布で平均粒子径が800μm
を越える芯粒子粉体を、準微粒子高分散処理手段群の最
終処理により気中に分散させて高分散芯粒子粉体の粒子
・気体混合物とし、その芯粒子粉体の粒子の分散度βを
99%以上とする分散性能を有する準微粒子高分散処理
手段群による分散工程の一部以上と前記被覆工程の一部
以上とを、空間を一部以上共有して行うことを特徴とす
る被覆準微粒子の製造方法にも関する。
Further, the present invention provides the above-mentioned method for producing coated quasi-fine particles, wherein the average particle size is 10 in volume-based frequency distribution.
A core particle powder having a particle size of more than 20 μm and more than 20 μm is dispersed in the air by the final treatment of the quasi-fine particle high dispersion treatment means group to form a particle / gas mixture of the highly dispersed core particle powder. With a degree of dispersion β of 80% or more, or a core particle powder having an average particle size of more than 20 μm and 50 μm or less in a volume-based frequency distribution, is dispersed in the air by the final treatment of the quasi-fine particle high dispersion treatment means group. To obtain a particle / gas mixture of highly dispersed core particle powder, and the degree of particle dispersion β of the core particle powder is 90%.
Or the average particle size is 5 in the volume-based frequency distribution.
A core particle powder having a particle diameter of more than 0 μm and not more than 300 μm is dispersed in the air by the final treatment of the quasi-fine particle high dispersion treatment means group to obtain a particle / gas mixture of the highly dispersed core particle powder. Dispersity β is 95% or more, or volume-based frequency distribution has an average particle size exceeding 300 μm and 800 μm
The following core particle powder is dispersed in the air by the final treatment of the quasi-fine particle high-dispersion treatment means group, and the particles of the high-dispersion core particle powder
As a gas mixture, the degree of particle dispersion β of the core particle powder is 9
A group of quasi-fine particles high-dispersion treatment means having a dispersion performance of 7% or more, or a volume-based frequency distribution having an average particle diameter of 800 μm.
The core particle powder exceeding the above is dispersed in the air by the final treatment of the quasi-fine particle high dispersion treatment means group to form a particle / gas mixture of the highly dispersed core particle powder, and the degree of dispersion β of the particles of the core particle powder is A coating method characterized in that a part or more of the dispersion step and a part or more of the coating step by the quasi-fine particle high-dispersion processing means group having a dispersion performance of 99% or more are performed by sharing a part or more of the space. It also relates to a method for producing fine particles.

【0018】更に本発明はまた、前記した被覆準微粒子
の製造方法において、体積基準頻度分布で平均粒子径が
10μmを越え20μm以下の芯粒子粉体を、準微粒子
高分散処理手段群の最終処理により気中に分散させて高
分散芯粒子粉体の粒子・気体混合物とし、その芯粒子粉
体の粒子の分散度βを80%以上とする空間領域、体積
基準頻度分布で平均粒子径が20μmを越え50μm以
下の芯粒子粉体を、準微粒子高分散処理手段群の最終処
理により気中に分散させて高分散芯粒子粉体の粒子・気
体混合物とし、その芯粒子粉体の粒子の分散度βを90
%以上とする空間領域、体積基準頻度分布で平均粒子径
が50μmを越え300μm以下の芯粒子粉体を、準微
粒子高分散処理手段群の最終処理により気中に分散させ
て高分散芯粒子粉体の粒子・気体混合物とし、その芯粒
子粉体の粒子の分散度βを95%以上とする空間領域、
体積基準頻度分布で平均粒子径が、300μmを越え8
00μm以下の芯粒子粉体を、準微粒子高分散処理手段
群の最終処理により気中に分散させて高分散芯粒子粉体
の粒子・気体混合物とし、その芯粒子粉体の粒子の分散
度βを97%以上とする空間領域、体積基準頻度分布で
平均粒子径が、800μmを越える芯粒子粉体を、準微
粒子高分散処理手段群の最終処理により気中に分散させ
て高分散芯粒子粉体の粒子・気体混合物とし、その芯粒
子粉体の粒子の分散度βを99%以上とする空間領域の
内の高分散芯粒子粉体の粒子・気体混合物中の芯粒子粉
体の粒子の全ての粒子が通過する面を含む空間領域に、
被覆空間の被覆開始領域を位置せしめるか、又は体積基
準頻度分布で平均粒子径が10μmを越え20μm以下
の芯粒子粉体を、準微粒子高分散処理手段群の最終処理
により気中に分散させて高分散芯粒子粉体の粒子・気体
混合物とし、その芯粒子粉体の粒子の分散度βを80%
以上とする空間領域、体積基準頻度分布で平均粒子径が
20μmを越え50μm以下の芯粒子粉体を、準微粒子
高分散処理手段群の最終処理により気中に分散させて高
分散芯粒子粉体の粒子・気体混合物とし、その芯粒子粉
体の粒子の分散度βを90%以上とする空間領域、体積
基準頻度分布で平均粒子径が50μmを越え300μm
以下の芯粒子粉体を、準微粒子高分散処理手段群の最終
処理により気中に分散させて高分散芯粒子粉体の粒子・
気体混合物とし、その芯粒子粉体の粒子の分散度βを9
5%以上とする空間領域、体積基準頻度分布で平均粒子
径が、300μmを越え800μm以下の芯粒子粉体
を、準微粒子高分散処理手段群の最終処理により気中に
分散させて高分散芯粒子粉体の粒子・気体混合物とし、
その芯粒子粉体の粒子の分散度βを97%以上とする空
間領域、体積基準頻度分布で平均粒子径が、800μm
を越える芯粒子粉体を、準微粒子高分散処理手段群の最
終処理により気中に分散させて高分散芯粒子粉体の粒子
・気体混合物とし、その芯粒子粉体の粒子の分散度βを
99%以上とする空間領域の内の、回収手段の回収部に
回収する全ての粒子が通過する面を含む空間領域に、被
覆空間の被覆開始領域を位置せしめることを特徴とする
被覆準微粒子の製造方法にも関する。
Further, in the present invention, in the above-mentioned method for producing coated quasi-fine particles, a core particle powder having a volume-based frequency distribution and an average particle diameter of more than 10 μm and 20 μm or less is subjected to the final treatment of the quasi-fine particle high dispersion treatment means group. To form a particle / gas mixture of highly dispersed core particle powder by dispersing in the air by means of a spatial region in which the degree of dispersion β of particles of the core particle powder is 80% or more, and the average particle diameter is 20 μm in the volume standard frequency distribution. The core particle powder having a particle diameter of more than 50 μm and not more than 50 μm is dispersed in the air by the final treatment of the quasi-fine particle high dispersion treatment means group to obtain a particle / gas mixture of the highly dispersed core particle powder, and the dispersion of the particles of the core particle powder. 90 degrees β
% Of the core particle powder having an average particle diameter of more than 50 μm and 300 μm or less in the spatial frequency distribution of volume standard frequency distribution in the air by the final treatment of the quasi-fine particle high dispersion treatment means group. A space region in which a particle / gas mixture of the body is used, and the degree of dispersion β of the core particle powder is 95% or more,
Volume-based frequency distribution with average particle size exceeding 300 μm 8
The core particle powder having a particle size of 00 μm or less is dispersed in the air by the final treatment of the quasi-fine particle high dispersion treatment means group to form a particle / gas mixture of the highly dispersed core particle powder, and the degree of dispersion β of the particles of the core particle powder Of core particles having an average particle size of more than 800 μm in the spatial region and volume-based frequency distribution of 97% or more are dispersed in the air by the final treatment of the quasi-fine particle high-dispersion processing means group to obtain high-dispersion core particle powder. The particle / gas mixture of the body, and the degree of dispersion β of the particle of the core particle powder is 99% or more of the highly dispersed core particle powder in the space region / the particle of the core particle powder in the gas mixture. In the space area including the surface through which all particles pass,
The coating start region of the coating space is located, or the core particle powder having an average particle size of more than 10 μm and 20 μm or less in the volume standard frequency distribution is dispersed in the air by the final treatment of the quasi-fine particle high dispersion treatment means group. A high-dispersion core particle powder is used as a particle / gas mixture, and the degree of dispersion β of the core particle powder is 80%.
Core particle powder having an average particle size of more than 20 μm and 50 μm or less in the above spatial region and volume standard frequency distribution is dispersed in the air by the final treatment of the quasi-fine particle high-dispersion processing means group to obtain highly dispersed core particle powder. The particle size of the core particle powder is 90% or more, and the average particle size is over 50 μm and 300 μm in the volume standard frequency distribution.
The following core particle powder is dispersed in the air by the final treatment of the quasi-fine particle high-dispersion treatment means group, and the particles of the high-dispersion core particle powder
As a gas mixture, the degree of particle dispersion β of the core particle powder is 9
A core particle powder having a spatial region of 5% or more and a volume-based frequency distribution and an average particle diameter of more than 300 μm and 800 μm or less is dispersed in the air by the final treatment of the quasi-fine particle high-dispersion treatment means group to obtain a highly dispersed core. As a particle-gas mixture of particle powder,
The average particle size is 800 μm in the spatial region and volume standard frequency distribution in which the dispersity β of the particles of the core particle powder is 97% or more.
The core particle powder exceeding the above is dispersed in the air by the final treatment of the quasi-fine particle high dispersion treatment means group to form a particle / gas mixture of the highly dispersed core particle powder, and the degree of dispersion β of the particles of the core particle powder is Of the coated quasi-fine particles, the coating start region of the coating space is located in a space region including a surface through which all particles to be collected by the collection unit of the collection unit out of the space region of 99% or more. It also relates to the manufacturing method.

【0019】更に本発明はまた、芯粒子粉体の粒子の粒
度分布が、平均粒子径をDMとしたとき、体積基準頻度
分布で(〔DM/5,5DM〕,≧90%)であることを
特徴とする被覆準微粒子の製造方法にも関する。
Further, according to the present invention, the particle size distribution of the particles of the core particle powder is a volume standard frequency distribution ([D M / 5,5D M ], ≧ 90%) when the average particle size is D M. Also relates to a method for producing coated quasi-fine particles.

【0020】また本発明は上記した被覆粒子の製造方法
を実施するための装置、すなわち芯粒子粉体を被覆空間
に投入し、気相を経て生成する被覆形成物質前駆体及び
/又は気相状態の被覆形成物質前駆体を、芯粒子粉体の
粒子に接触及び/又は衝突させて、芯粒子粉体の粒子の
表面を被覆形成物質で被覆する被覆準微粒子の製造装置
において、 (A) 準微粒子高分散処理手段群の最終処理手段が、
(a) この芯粒子粉体の粒子を気中に分散させる分散
手段、および(b) 芯粒子粉体の粒子を気中に分散さ
せた芯粒子粉体の粒子と気体の混合物において低分散芯
粒子粉体部分を分離し、芯粒子粉体の粒子が主に単一粒
子状態で気中に存在する高分散芯粒子粉体の粒子・気体
混合物を選択する高分散芯粒子粉体の粒子・気体混合物
選択手段とこの高分散芯粒子粉体の粒子・気体混合物選
択手段により分離された低分散芯粒子粉体部分を準微粒
子高分散処理手段群中の分散手段の内の最終分散手段及
び/又は最終分散手段以前の処理手段に搬送するフィー
ドバック手段とを備えた高分散芯粒子粉体の粒子・気体
混合物選択手段、から選ばれる準微粒子高分散処理手段
群により、体積基準頻度分布で平均粒子径が10μmを
越え、300μm以下の準微粒子芯粒子粉体の粒子又は
主に準微粒子からなる芯粒子粉体の粒子を、気中に分散
させて高分散芯粒子粉体の粒子・気体混合物とする分散
処理手段、 (B) この分散処理手段で分散した芯粒子粉体の粒子
を、その平均粒子径が10μmを越え20μm以下のと
きには分散度βが80%以上、20μmを越え50μm
以下のときには分散度βが90%以上、50μmを越え
300μm以下のときには分散度βが95%以上、30
0μmを越え800μm以下のときは分散度βが97%
以上、そして800μmを越えるときは分散度βが99
%以上の分散状態で、被覆空間の被覆開始領域において
被覆形成物質前駆体と接触及び/又は衝突させて被覆を
開始する被覆室、を設けたことを特徴とする、被覆準微
粒子の製造装置を提供するものである。
Further, the present invention is an apparatus for carrying out the above-mentioned method for producing coated particles, that is, a core-particle powder is charged into a coating space, and a coating-forming substance precursor and / or gas-phase state produced through a gas phase is produced. In the apparatus for producing coated quasi-fine particles, which comprises contacting and / or colliding the coating-forming substance precursor of 1 with the particles of the core particle powder to coat the surface of the particles of the core particle powder with the coating-forming substance, The final treatment means of the fine particle high dispersion treatment means group is
(A) a dispersing means for dispersing the particles of the core particle powder in the air; and (b) a low dispersion core in a mixture of the particles of the core particle powder and the gas in which the particles of the core particle powder are dispersed in the air. Particles of highly dispersed core particle powder that separates the particle powder portion and particles of the core particle powder are mainly present in the air in a single particle state. Particles of highly dispersed core particle powder that selects a gas mixture. The low dispersion core particle powder portion separated by the gas mixture selection means and the particle / gas mixture selection means of the high dispersion core particle powder is the final dispersion means of the dispersion means in the quasi-fine particle high dispersion treatment means group and / or Alternatively, by means of a group of quasi-fine particle high dispersion treatment means selected from highly dispersed core particles powder particle / gas mixture selection means provided with a feedback means for conveying to the treatment means before the final dispersion means, average particles in a volume-based frequency distribution Diameter exceeds 10 μm and 300 μm or less Dispersion processing means for dispersing particles of the quasi-fine particle core particle powder or particles of the core particle powder mainly consisting of quasi-fine particles in the air to form a particle / gas mixture of the highly dispersed core particle powder, (B) When the average particle size of the core particle powder dispersed by the dispersion treatment means is 10 μm or more and 20 μm or less, the dispersity β is 80% or more, and 20 μm or more and 50 μm.
When the dispersity β is 90% or more, and when the dispersity β exceeds 50 μm and is 300 μm or less, the dispersity β is 95% or more and 30
When it exceeds 0 μm and 800 μm or less, the dispersity β is 97%.
Above, and when it exceeds 800 μm, the dispersion degree β is 99
%, A coating chamber for contacting and / or colliding with the coating forming material precursor in the coating starting region of the coating space to start coating is provided. It is provided.

【0021】更に本発明は前記した被覆準微粒子の製造
装置において体積基準頻度分布で平均粒径が10μmを
越え20μm以下の芯粒子粉体を準微粒子高分散処理手
段群の最終処理により気中に分散させて高分散芯粒子粉
体の粒子・気体混合物とし、その芯粒子粉体の粒子の分
散度βを80%以上とするか、又は体積基準頻度分布で
平均粒径が20μmを越え50μm以下の芯粒子粉体を
準微粒子高分散処理手段群の最終処理により気中に分散
させて高分散芯粒子粉体の粒子・気体混合物としその芯
粒子粉体の粒子の分散度βを90%以上とするか、又は
体積基準頻度分布で平均粒径が50μmを越え300μ
m以下の芯粒子粉体を準微粒子高分散処理手段群の最終
処理により気中に分散させて高分散芯粒子粉体の粒子・
気体混合物としその芯粒子粉体の粒子の分散度βを95
%以上とするか、又は体積基準頻度分布で平均粒子径が
300μmを越え800μm以下の芯粒子粉体を、準微
粒子高分散処理手段群の最終処理により気中に分散させ
て高分散芯粒子粉体の粒子・気体混合物とし、その芯粒
子粉体の粒子の分散度βを97%以上とする分散性能を
有する準微粒子高分散処理手段群、又は体積基準頻度分
布で平均粒子径が800μmを越える芯粒子粉体を、準
微粒子高分散処理手段群の最終処理により気中に分散さ
せて高分散芯粒子粉体の粒子・気体混合物とし、その芯
粒子粉体の粒子の分散度βを99%以上とする分散性能
を有する準微粒子高分散処理手段群による処理手段を設
け、準微粒子高分散処理手段群の最終処理により生成さ
せた高分散芯粒子粉体の粒子・気体混合物を、準微粒子
高分散処理手段群から放出する、準微粒子高分散処理手
段群の放出部を、被覆準微粒子の製造装置の被覆空間を
有する被覆室に、直結させ又は搬送に不可避の、中空部
材、中空を形成せしめる部材からなる中間部材及びパイ
プから選択される一種類又はそれ以上の部材を介して接
続し、及び/又は、分散性能で気中に分散させた高分散
芯粒子粉体の粒子・気体混合物中の粒子の気中分散状態
を維持させる気中分散維持手段、分散性能で気中に分散
させた高分散芯粒子粉体の粒子・気体混合物中の粒子の
気中分散状態を高める気中分散促進手段、芯粒子粉体の
粒子と気体との混合物において、低分散芯粒子粉体部分
を分離し、芯粒子粉体の粒子が主に単一粒子状態で気中
に存在する高分散芯粒子粉体の粒子・気体混合物を選択
する高分散芯粒子粉体の粒子・気体混合物選択手段の内
の一種又はそれ以上を介して接続したことを特徴とする
被覆準微粒子の製造装置にも関する。
Further, according to the present invention, in the above-mentioned apparatus for producing coated quasi-fine particles, core particle powder having an average particle size of more than 10 μm and 20 μm or less in a volume-based frequency distribution is put into the air by the final treatment of the quasi-fine particle high dispersion treatment means group. Disperse it into a particle / gas mixture of highly dispersed core particle powder, and make the degree of dispersion β of the particles of the core particle powder 80% or more, or in the volume standard frequency distribution, the average particle size exceeds 20 μm and 50 μm or less. Is dispersed in the air by the final treatment of the quasi-fine particle high dispersion treatment means group to form a particle / gas mixture of the highly dispersed core particle powder, and the degree of dispersion β of the particles of the core particle powder is 90% or more. Or the volume-based frequency distribution has an average particle size of more than 50 μm and 300 μm
The core particle powder having a particle size of m or less is dispersed in the air by the final treatment of the quasi-fine particle high dispersion treatment means group to form a high-dispersion core particle powder particle.
As a gas mixture, the particle dispersity β of the core particles is 95
% Or a core particle powder having an average particle size of more than 300 μm and 800 μm or less in a volume-based frequency distribution is dispersed in the air by the final treatment of the quasi-fine particle high dispersion treatment means group to obtain a highly dispersed core particle powder. A particle / gas mixture of the body, a group of quasi-fine particle high-dispersion treatment means having a dispersibility of making the degree of particle dispersion β of the core particle powder 97% or more, or the average particle diameter exceeds 800 μm in the volume standard frequency distribution. The core particle powder is dispersed in the air by the final treatment of the quasi-fine particle high dispersion treatment means group to obtain a particle / gas mixture of the highly dispersed core particle powder, and the degree of dispersion β of the particles of the core particle powder is 99%. A processing means is provided by the quasi-fine particle high-dispersion processing means group having the above dispersion performance, and the particle / gas mixture of the highly-dispersed core particle powder generated by the final treatment of the quasi-fine particle high-dispersion processing means group From the group of distributed processing means An intermediate member consisting of a hollow member and a member for forming a hollow, which directly discharges or discharges the quasi-fine particle high-dispersion processing means group to the coating chamber having the coating space of the apparatus for producing coated quasi-fine particles. And high-dispersion core particles that are connected through one or more members selected from pipes and / or dispersed in the air with a dispersion performance-in-air dispersion of particles in a gas mixture. Air-dispersion maintaining means for maintaining the state, air-dispersion promoting means for increasing the air-dispersion state of particles in a high-dispersion core particle powder dispersed in air with dispersion performance, and core particle powder In the mixture of particles and gas, the low-dispersion core particle powder part is separated, and the particles of the core particle powder are mainly present in the air in a single particle state. High-dispersion core particle powder / particle gas mixture Also it relates to apparatus for producing a coated semi microparticles, characterized in that the one or connected through more of the selection means.

【0022】更に本発明は、前記した被覆準微粒子の製
造装置において、体積基準頻度分布で平均粒子径が10
μmを越え20μm以下の芯粒子粉体を、準微粒子高分
散処理手段群の最終処理により気中に分散させて高分散
芯粒子粉体の粒子・気体混合物とし、その芯粒子粉体の
粒子の分散度βを80%以上とするか、又は体積基準頻
度分布で平均粒子径が20μmを越え50μm以下の芯
粒子粉体を、準微粒子高分散処理手段群の最終処理によ
り気中に分散させて高分散芯粒子粉体の粒子・気体混合
物とし、その芯粒子粉体の粒子の分散度βを90%以上
とするか、又は体積基準頻度分布で平均粒子径が50μ
mを越え300μm以下の芯粒子粉体を準微粒子高分散
処理手段群の最終処理により気中に分散させて高分散芯
粒子粉体の粒子・気体混合物とし、その芯粒子粉体の粒
子の分散度βを95%以上とするか、又は体積基準頻度
分布で平均粒子径が300μmを越え800μm以下の
芯粒子粉体を、準微粒子高分散処理手段群の最終処理に
より高い分散させて芯粒子粉体の粒子・気体混合物と
し、その芯粒子粉体の粒子の分散度βを97%以上とす
るか、又は体積基準頻度分布で平均粒子径が800μm
を越える芯粒子粉体を、準微粒子高分散処理手段群の最
終処理により高分散させて芯粒子粉体の粒子・気体混合
物とし、その芯粒子粉体の粒子の分散度βを99%以上
とする分散性能を有する準微粒子高分散処理手段群を含
む分散処理手段の一部以上と、前記被覆室とを、それら
が占める空間を一部以上共有するようにして設けること
を特徴とする被覆準微粒子の製造装置にも関する。
Further, the present invention is the apparatus for producing coated quasi-fine particles as described above, wherein the volume-based frequency distribution has an average particle diameter of 10
A core particle powder having a particle size of more than 20 μm and more than 20 μm is dispersed in the air by the final treatment of the quasi-fine particle high dispersion treatment means group to obtain a particle / gas mixture of the highly dispersed core particle powder. The degree of dispersion β is set to 80% or more, or core particle powder having an average particle size of more than 20 μm and 50 μm or less in a volume-based frequency distribution is dispersed in the air by the final treatment of the quasi-fine particle high dispersion treatment means group. A high-dispersion core particle powder is used as a particle / gas mixture, and the degree of dispersion β of the particles of the core particle powder is 90% or more, or the average particle diameter is 50μ in a volume-based frequency distribution.
The core particle powder having a particle size of more than 300 m and not more than 300 μm is dispersed in the air by the final treatment of the quasi-fine particle high dispersion treatment means group to obtain a particle / gas mixture of the highly dispersed core particle powder, and the dispersion of the particles of the core particle powder. The core particle powder having a degree β of 95% or more, or a core particle powder having an average particle size of more than 300 μm and 800 μm or less in a volume-based frequency distribution is highly dispersed by the final treatment of the quasi-fine particle high dispersion treatment means group. A particle / gas mixture of the body, and the degree of particle dispersion β of the core particle powder is 97% or more, or the average particle diameter is 800 μm in the volume standard frequency distribution.
The core particle powder exceeding the above is highly dispersed by the final treatment of the quasi-fine particle high dispersion treatment means group to form a particle / gas mixture of the core particle powder, and the degree of dispersion β of the particles of the core particle powder is 99% or more. A coating process characterized in that at least a part of the dispersion treatment means including a group of quasi-fine particle high-dispersion treatment means having dispersion performance and the coating chamber are provided so as to share at least a part of the space occupied by them. It also relates to an apparatus for producing fine particles.

【0023】更に本発明はまた、前記した被覆準微粒子
の製造装置において、体積基準頻度分布で平均粒子径が
10μmを越え20μm以下の芯粒子粉体を、準微粒子
高分散処理手段群の最終処理により気中に分散させて高
分散芯粒子粉体の粒子・気体混合物とし、その芯粒子粉
体の粒子の分散度βを80%以上とする空間領域、体積
基準頻度分布で平均粒子径が20μmを越え50μm以
下の芯粒子粉体を、準微粒子高分散処理手段群の最終処
理により気中に分散させて高分散芯粒子粉体の粒子・気
体混合物とし、その芯粒子粉体の粒子の分散度βを90
%以上とする空間領域、体積基準頻度分布で平均粒子径
が50μmを越え300μm以下の芯粒子粉体を、準微
粒子高分散処理手段群の最終処理により気中に分散させ
て高分散芯粒子粉体の粒子・気体混合物とし、その芯粒
子粉体の粒子の分散度βを95%以上とする空間領域、
体積基準頻度分布で平均粒子径が、300μmを越え8
00μm以下の芯粒子粉体を、準微粒子高分散処理手段
群の最終処理により気中に分散させて高分散芯粒子粉体
の粒子・気体混合物とし、その芯粒子粉体の粒子の分散
度βを97%以上とする空間領域、体積基準頻度分布で
平均粒子径が、800μmを越える芯粒子粉体を、準微
粒子高分散処理手段群の最終処理により気中に分散させ
て高分散芯粒子粉体の粒子・気体混合物とし、その芯粒
子粉体の粒子の分散度βを99%以上とする空間領域の
内の高分散芯粒子粉体の粒子・気体混合物中の芯粒子粉
体の粒子の全ての粒子が通過する面を含む空間領域に、
被覆空間の被覆開始領域を位置せしめるか、又は体積基
準頻度分布で平均粒子径が10μmを越え20μm以下
の芯粒子粉体を、準微粒子高分散処理手段群の最終処理
により気中に分散させて高分散芯粒子粉体の粒子・気体
混合物とし、その芯粒子粉体の粒子の分散度βを80%
以上とする空間領域、体積基準頻度分布で平均粒子径が
20μmを越え50μm以下の芯粒子粉体を、準微粒子
高分散処理手段群の最終処理により気中に分散させて高
分散芯粒子粉体の粒子・気体混合物とし、その芯粒子粉
体の粒子の分散度βを90%以上とする空間領域、体積
基準頻度分布で平均粒子径が50μmを越え300μm
以下の芯粒子粉体を準微粒子高分散処理手段群の最終処
理により気中に分散させて高分散芯粒子粉体の粒子・気
体混合物とし、その芯粒子粉体の粒子の分散度βを95
%以上とする空間領域、体積基準頻度分布で平均粒子径
が、300μmを越え800μm以下の芯粒子粉体を、
準微粒子高分散処理手段群の最終処理により気中に分散
させて高分散芯粒子粉体の粒子・気体混合物とし、その
芯粒子粉体の粒子の分散度βを97%以上とする空間領
域、体積基準頻度分布で平均粒子径が、800μmを越
える芯粒子粉体を、準微粒子高分散処理手段群の最終処
理により気中に分散させて高分散芯粒子粉体の粒子・気
体混合物とし、その芯粒子粉体の粒子の分散度βを99
%以上とする空間領域の内の、回収手段の回収部に回収
する全ての粒子が通過する面を含む空間領域に、被覆空
間の被覆開始領域を位置せしめることを特徴とする被覆
準微粒子の製造装置にも関する。
Furthermore, in the present invention, in the above-mentioned apparatus for producing coated quasi-fine particles, a core particle powder having a volume-based frequency distribution and an average particle size of more than 10 μm and 20 μm or less is subjected to the final treatment of the quasi-fine particle high dispersion treatment means group. To form a particle / gas mixture of highly dispersed core particle powder by dispersing in the air by means of a spatial region in which the degree of dispersion β of the core particle powder is 80% or more, and the average particle diameter is 20 μm in volume standard frequency distribution. The core particle powder having a particle diameter of more than 50 μm and not more than 50 μm is dispersed in the air by the final treatment of the quasi-fine particle high dispersion treatment means group to obtain a particle / gas mixture of the highly dispersed core particle powder, and the dispersion of the particles of the core particle powder. 90 degrees β
% Of the core particle powder having an average particle diameter of more than 50 μm and 300 μm or less in the spatial frequency distribution of volume standard frequency distribution in the air by the final treatment of the quasi-fine particle high dispersion treatment means group. A space region in which a particle / gas mixture of the body is used, and the degree of dispersion β of the core particle powder is 95% or more,
Volume-based frequency distribution with average particle size exceeding 300 μm 8
The core particle powder having a particle size of 00 μm or less is dispersed in the air by the final treatment of the quasi-fine particle high dispersion treatment means group to form a particle / gas mixture of the highly dispersed core particle powder, and the degree of dispersion β of the particles of the core particle powder Of core particles having an average particle size of more than 800 μm in the spatial region and volume-based frequency distribution of 97% or more are dispersed in the air by the final treatment of the quasi-fine particle high-dispersion processing means group to obtain high-dispersion core particle powder. The particle / gas mixture of the body, and the degree of dispersion β of the particle of the core particle powder is 99% or more of the highly dispersed core particle powder in the space region / the particle of the core particle powder in the gas mixture. In the space area including the surface through which all particles pass,
The coating start region of the coating space is located, or the core particle powder having an average particle size of more than 10 μm and 20 μm or less in the volume standard frequency distribution is dispersed in the air by the final treatment of the quasi-fine particle high dispersion treatment means group. A high-dispersion core particle powder is used as a particle / gas mixture, and the degree of dispersion β of the core particle powder is 80%.
Core particle powder having an average particle size of more than 20 μm and 50 μm or less in the above spatial region and volume standard frequency distribution is dispersed in the air by the final treatment of the quasi-fine particle high-dispersion processing means group to obtain highly dispersed core particle powder. The particle size of the core particle powder is 90% or more, and the average particle size is over 50 μm and 300 μm in the volume standard frequency distribution.
The following core particle powder is dispersed in the air by the final treatment of the quasi-fine particle high dispersion treatment means group to obtain a particle / gas mixture of the highly dispersed core particle powder, and the degree of dispersion β of the particles of the core particle powder is 95.
% Core particles having an average particle size of more than 300 μm and 800 μm or less in a spatial region and volume standard frequency distribution,
A space region in which the particles / gas mixture of the highly dispersed core particle powder is dispersed in the air by the final treatment of the quasi-fine particle high dispersion treatment means group, and the degree of dispersion β of the particles of the core particle powder is 97% or more, A core particle powder having a volume-based frequency distribution and an average particle diameter of more than 800 μm is dispersed in the air by the final treatment of the quasi-fine particle high dispersion treatment means group to obtain a particle / gas mixture of the highly dispersed core particle powder, The particle dispersity β of the core particle powder is 99
Of coated quasi-fine particles, characterized in that the coating start region of the coating space is located in a space region including a surface through which all particles to be recovered by the recovery unit of the recovery means out of the space region of not less than 10%. It also relates to the device.

【0024】更に本発明はまた、芯粒子粉体の粒子の粒
度分布が、平均粒子径をDMとしたとき、体積基準頻度
分布で(〔DM/5,5DM〕,≧90%)であることを
特徴とする被覆準微粒子の製造装置にも関する。
Further, according to the present invention, the particle size distribution of the particles of the core particle powder is a volume standard frequency distribution ([D M / 5,5D M ], ≧ 90%) when the average particle size is D M. Also relates to an apparatus for producing coated quasi-fine particles.

【0025】而して、本発明によれば、気中において、
被覆形成物質の原料から気相法により気相を経て生成す
る被覆形成物質前駆体と、準微粒子高分散処理手段群の
最終処理により気中に分散させた平均粒子径が10μm
を越える準微粒子からなる高分散芯粒子粉体の粒子・気
体混合物を、被覆空間の被覆開始領域で、高分散芯粒子
粉体の粒子・気体混合物中の芯粒子粉体の粒子の分散度
が粒子の平均粒径に応じてβ≧80%、β≧90%、β
≧95%、β≧97又はβ≧99%である高分散状態で
合流させ、接触及び/又は衝突させて芯粒子粉体の粒子
の表面を被覆形成物質で被覆するものである。この場
合、被覆形成物質前駆体は、原子、分子、イオン、クラ
スター、原子クラスター、分子クラスター、クラスター
イオン等からなる気相を経て生成したばかりのもので、
それ自体はいわば発生期で非常に活性な状態にあり、高
分散状態の芯粒子と接触及び/又は衝突を始めることに
より、単一粒子状態の個々の芯粒子の表面に被覆形成物
質は強固に結合し、その結果、芯粒子粉体の粒子の単一
粒子単位で状態が均一な被覆形成物質で且つ各粒子ごと
に量の均一な被覆形成物質で被覆してなる被覆粒子が製
造できる。
Therefore, according to the present invention, in the air,
The coating-forming substance precursor produced from the raw material of the coating-forming substance through the vapor phase by the vapor phase method, and the average particle size dispersed in the air by the final treatment of the quasi-fine particle high dispersion treatment means group is 10 μm.
In the coating start region of the coating space, the degree of dispersion of the particles of the core particle powder in the mixture of the highly dispersed core particle powder and the gas in the gas mixture of the highly dispersed core particle powder consisting of quasi-fine particles exceeding Β ≧ 80%, β ≧ 90%, β depending on the average particle size
The particles of the core particle powder are coated with the coating forming substance by merging in a highly dispersed state of ≧ 95%, β ≧ 97 or β ≧ 99%, and contacting and / or colliding them. In this case, the coating-forming substance precursor is one that has just been generated through a gas phase composed of atoms, molecules, ions, clusters, atomic clusters, molecular clusters, cluster ions, etc.
As such, it is in a very active state as it is during the nascent stage, and by initiating contact and / or collision with the highly dispersed core particles, the coating forming substance is firmly attached to the surface of each individual core particle in the single particle state. As a result, it is possible to produce coated particles in which the particles of the core particle powder are coated with a uniform coating forming substance in a single particle unit and the amount of each particle is coated with a uniform coating forming substance.

【0026】以下に本発明を詳細に説明する前に、本明
細書中に使用する用語をはじめに定義することとし、そ
して必要によってその用語の具体的内容を説明すること
にする。
Before describing the present invention in detail below, terms used in the present specification will be first defined, and if necessary, specific contents of the terms will be explained.

【0027】被覆粒子 被覆粒子とは、被覆が施された粒子をいう。例えば、具
体的には、前記被覆形成物質が、超微粒子状、島状、連
続質状、一様な膜状、突起物状等の内の一種以上からな
る形態で芯粒子に被覆された粒子をいう。
Coated Particles Coated particles are particles that have been coated. For example, specifically, particles in which the coating forming substance is coated on the core particles in a form of one or more of ultrafine particles, islands, continuous substances, uniform films, protrusions and the like. Say.

【0028】気相被覆法 気相被覆法とは、被覆形成物質の原料が、真空の分子
流、イオン流、プラズマ、ガス、蒸気、エアロゾルの一
種以上からなる気相状態を少なくとも一度は経て被覆す
る方法、又は気相状態の被覆形成物質の原料により被覆
する方法をいう。
Vapor-phase coating method The vapor-phase coating method is a method for coating a raw material of a coating-forming substance at least once in a vapor-phase state composed of one or more kinds of vacuum molecular flow, ion flow, plasma, gas, vapor and aerosol. Or a method of coating with a raw material of a coating forming substance in a gas phase.

【0029】芯粒子 芯粒子とは、被覆を施す対象物となる粒子をいう。これ
はまた、母材粒子、種粒子或は被覆される粒子ともい
う。この芯粒子は、基本的にはそれを構成する物質に制
限がなく、例えば無機材料、金属材料、有機材料などか
らなる公知の粉体粒子が芯粒子として使用可能である。
Core Particles Core particles are particles to be coated. This is also referred to as matrix particles, seed particles or coated particles. The core particles are basically not limited in the substance constituting them, and known powder particles made of, for example, an inorganic material, a metal material, an organic material or the like can be used as the core particles.

【0030】芯粒子粉体 芯粒子粉体とは、芯粒子からなる粉体をいう。芯粒子粉
体の粒子とは、芯粒子粉体を構成する粒子をいう。本発
明で被覆に供する準微粒子芯粒子粉体の粒子又は主に準
微粒子からなる芯粒子粉体の粒子は、平均粒子径が体積
基準頻度分布で10μmを越えるものである。好ましく
は、平均粒子径をDMとしたとき、DMが10μmを越え
て、粒度分布が体積基準頻度分布で(〔DM/5,5
M〕,≧90%)である。このような比較的分布幅の
狭い粉体では、平均粒子径で粉体の分散特性又は凝集特
性が特徴付けられ、DMの値に適した条件で微粒子高分
散処理手段群を作動させれば分散できる。平均粒子径が
10μmを越える芯粒子粉体の粒子の粒度分布が、幅広
い分布又は互いに離れた複数のピークを持つ分布の粉体
では、好適には適当な選択分離処理、例えば分級処理を
行ってそれぞれ分級された粉体ごとに、本発明の被覆処
理を施す。これにより、それぞれ分級された粉体ごとに
上記条件の下で、被覆空間の被覆開始領域で分散度が平
均粒子径に応じて分散度βで80%以上、90%以上、
95%以上、97%以上又は99%以上の状態で被覆が
開始され、芯粒子粉体の粒子一つ一つの粒子に被覆が可
能となる。
Core particle powder The core particle powder is a powder composed of core particles. The particles of the core particle powder refer to particles constituting the core particle powder. The particles of the quasi-fine particle core particle powder used for coating in the present invention or the particles of the core particle powder mainly consisting of quasi-fine particles have an average particle diameter of more than 10 μm in volume-based frequency distribution. Preferably, when the average particle size is D M , D M exceeds 10 μm, and the particle size distribution is a volume-based frequency distribution ([D M / 5,5
D M ], ≧ 90%). In such a powder having a relatively narrow distribution width, the dispersion property or agglomeration property of the powder is characterized by the average particle size, and if the fine particle high dispersion treatment means group is operated under the condition suitable for the value of D M. Can be dispersed. In the case of a powder having a core particle powder having an average particle diameter of more than 10 μm and having a particle size distribution of a wide distribution or a distribution having a plurality of peaks separated from each other, a suitable selective separation treatment, for example, classification treatment is preferably performed. The coating treatment of the present invention is applied to each classified powder. As a result, under the above conditions for each classified powder, the dispersity in the coating start region of the coating space is 80% or more, 90% or more in terms of the dispersity β according to the average particle size,
The coating is started in the state of 95% or more, 97% or more, or 99% or more, and it becomes possible to coat each particle of the core particle powder.

【0031】被覆形成物質 被覆形成物質とは、被覆を施す対象物に被覆を形成する
物質をいう。例えば、具体的には、超微粒子状、島状、
連続質状、一様な膜状、突起物状等の内の一種以上から
なる形態で被覆を形成する物質をいう。特に、被覆形成
物質の形態が超微粒子状の場合、超微粒子の粒子径は、
0.005μm〜0.5μmの範囲のものである。この被
覆形成物質は、得られる被覆粒子に対して希望される性
質及び機能に応じて、芯粒子とは同一であるか又は異な
った種々の無機材料、金属材料又は有機材料で構成さ
れ、例えば酸化物であるAl23、SiO2、ZrO2
23、CaO、MgO、MgAl24(スピネル)、
Al2SiO5(ムライト)など、窒化物であるSi
34、AlN、TiN、ZrN、Si22O、HfN、
xN(x=1〜3)、NbN、TaN、Ta2N、BN
など、炭化物であるWC、SiC、W2C、HfC、T
aC、Ta2C、NbC、Mo2Cなど、ほう素化物であ
るBP、TiB、TiB2、ZrB2、VB、V32、V
2、NbB、NbB2、TaB、TaB2、MoB、M
oB2、MoB4、Mo2B、WB、W2B、W25、La
6、B132など、単体金属、例えばSi、Al、N
i、Co、Cu、Fe、Ti、W、B、Nb、V、Z
r、Hf、Ta、Re、Cr、Mo、Y、Laなど、及
び金属間化合物および合金の種々のもの例えばTiA
l、Ti2Al、TiAl3、TiNi、NiAl、Ni
3Alなどの材料、並びにこれらの材料を複合したもの
など及びエポキシ樹脂、フェノール樹脂、ポリアクリル
アミド樹脂、ポリアミド樹脂、ウレタン樹脂、ポリエス
テル樹脂、ポリ塩化ビニル樹脂、アクリル樹脂、ポリエ
チレン等を用いることができる。
Coating-forming substance The coating-forming substance is a substance that forms a coating on an object to be coated. For example, specifically, ultrafine particles, islands,
A substance that forms a coating in the form of one or more of a continuous substance, a uniform film, and protrusions. In particular, when the form of the coating forming material is ultrafine particles, the particle size of the ultrafine particles is
It is in the range of 0.005 μm to 0.5 μm. This coating-forming substance is composed of various inorganic materials, metallic materials or organic materials which are the same as or different from the core particles, depending on the desired properties and functions of the resulting coated particles, such as oxidation. Al 2 O 3 , SiO 2 , ZrO 2 ,
Y 2 O 3 , CaO, MgO, MgAl 2 O 4 (spinel),
Si, which is a nitride such as Al 2 SiO 5 (mullite)
3 N 4 , AlN, TiN, ZrN, Si 2 N 2 O, HfN,
V x N (x = 1 to 3), NbN, TaN, Ta 2 N, BN
Etc., which are carbides such as WC, SiC, W 2 C, HfC, T
Boron BP, TiB, TiB 2 , ZrB 2 , VB, V 3 B 2 , V such as aC, Ta 2 C, NbC, Mo 2 C
B 2 , NbB, NbB 2 , TaB, TaB 2 , MoB, M
oB 2 , MoB 4 , Mo 2 B, WB, W 2 B, W 2 B 5 , La
B 6, etc. B 13 P 2, a single metal, for example Si, Al, N
i, Co, Cu, Fe, Ti, W, B, Nb, V, Z
r, Hf, Ta, Re, Cr, Mo, Y, La, etc., and various intermetallic compounds and alloys such as TiA
l, Ti 2 Al, TiAl 3 , TiNi, NiAl, Ni
3 Materials such as Al, composites of these materials, and epoxy resin, phenol resin, polyacrylamide resin, polyamide resin, urethane resin, polyester resin, polyvinyl chloride resin, acrylic resin, polyethylene, etc. can be used. .

【0032】均一な被覆 一様な膜状の被覆形成物質の場合には、単一粒子におい
て被覆膜の厚さがいたるところで均一であることをい
う。被覆形成物質が超微粒子状、島状又は突起物状の場
合には、超微粒子状、島状又は突起物状の被覆形成物質
が均一な分布で被覆することをいう。被覆形成物質の生
成過程で、避けられない不均一さは、均一の範疇に含ま
れるものである。
Uniform coating In the case of a uniform film-forming coating material, it means that the thickness of the coating film is uniform every single particle. When the coating forming substance is in the form of ultrafine particles, islands or protrusions, it means that the coating forming substance in the form of ultrafine particles, islands or protrusions is coated in a uniform distribution. Inevitable inhomogeneities in the process of producing coating-forming substances are included in the category of uniformity.

【0033】被覆空間に投入の定義 被覆空間に投入とは、例えば、自由落下等の落下によっ
て芯粒子粉体を被覆空間に導入することをいう。搬送ガ
スにより投入する場合には、芯粒子粉体を芯粒子粉体の
粒子・気体混合物の流れの方向に乗せて導入したり、気
体に乗せて流れの方向へ、或いは気体に乗り方向が変え
られて導入することをいう。又は、搬送ガスの作用を受
けて導入することをもいう。例えば搬送ガスの波動現
象、具体的には非線系波動によって導入することをい
う。或いは、ガス中の音波、超音波、磁場、電子線等に
よって被覆空間に導入することをもいう。又、外場、例
えば電場、磁場、電子線等により導入することをもい
う。具体的には、電場、磁場、電子線等により粉体粒子
を帯電させ、又は帯磁させ引力又は斥力により被覆空間
に導入することをいう。又、ガスの背圧や減圧によって
吸い込まれ、導入することも含む。
Definition of charging into the coating space The charging into the coating space means, for example, introducing the core particle powder into the coating space by falling such as free fall. In the case of charging with carrier gas, the core particle powder is introduced by carrying it in the flow direction of the particle / gas mixture of the core particle powder, or by carrying it on the gas in the flow direction, or by changing the riding direction of the gas. It means being introduced. Alternatively, it also means to be introduced by receiving the action of a carrier gas. For example, it is introduced by a wave phenomenon of carrier gas, specifically, a non-linear wave. Alternatively, it also means introducing into the coating space by a sound wave in a gas, an ultrasonic wave, a magnetic field, an electron beam, or the like. It also means introduction by an external field such as an electric field, a magnetic field, or an electron beam. Specifically, it means that the powder particles are charged or magnetized by an electric field, a magnetic field, an electron beam or the like and introduced into the coating space by an attractive force or a repulsive force. It also includes the introduction and introduction of gas by back pressure or pressure reduction.

【0034】被覆空間 被覆空間とは、被覆形成物質の原料から気相を経て生成
する被覆形成物質前駆体及び/又は気相状態の被覆形成
物質前駆体と芯粒子粉体の粒子が接触及び/又は衝突す
る空間をいう。或いは、芯粒子粉体の粒子の表面を被覆
形成物質で被覆する空間領域をいう。
Coating Space The coating space is a precursor of a coating-forming substance which is produced from a raw material of a coating-forming substance through a gas phase and / or a coating-forming substance precursor in a gas phase and particles of core particle powder contact and / or Or, it means the space where it collides. Alternatively, it refers to a space region in which the surface of the particles of the core particle powder is coated with the coating forming substance.

【0035】被覆室 被覆室とは、被覆空間を一部以上共有する室をいう。よ
り具体的には、被覆室とは、被覆空間を含む仕切られ
た、又は略仕切られた(略閉じた、半閉じた)室であっ
て、被覆空間を一部以上含む室である。
Coating Chamber The coating chamber is a chamber which shares a part or more of the coating space. More specifically, the coating chamber is a partitioned or substantially partitioned (substantially closed or semi-closed) chamber including the coating space, and a chamber including a part or more of the coating space.

【0036】気中 気中とは、真空又は気相状態の空間内をいう。ここで、
本発明において、気相状態とは、分子流、イオン流、プ
ラズマ、ガス、蒸気、エアロゾルなどの状態をいう。真
空とは、技術的には、減圧状態をさす。どんな減圧下で
も、厳密にはガス、分子、原子、イオン等が含まれる。
In the air, the air refers to the inside of a vacuum or a gas phase space. here,
In the present invention, the gas phase state means a state such as molecular flow, ion flow, plasma, gas, vapor, and aerosol. The vacuum is technically a reduced pressure state. Strictly speaking, gas, molecule, atom, ion, etc. are contained under any reduced pressure.

【0037】被覆形成物質前駆体 被覆形成物質前駆体とは、被覆形成物質の前駆体であ
る。より詳しくは、気相状態の被覆形成物質の原料がそ
のまま、又は被覆形成物質の原料から気相を経て形成及
び/又は合成され、被覆を施す対象物となる粒子である
芯粒子に被覆を形成する直前の物質をいう。被覆形成物
質前駆体は、被覆形成物質の原料から、どこかで気相を
経て形成及び/又は合成する限り、状態の制限はない。
被覆形成物質の原料が気相の場合、原料が被覆形成物質
前駆体にもなりうる。被覆形成物質前駆体そのものが気
相であってもよい。又、反応前でも良く、反応中でもよ
く、反応後でもよい。被覆形成物質前駆体の具体例とし
ては、イオン、原子、分子、クラスター、原子クラスタ
ー、分子クラスター、クラスターイオン、超微粒子、ガ
ス、蒸気、エアロゾル等が挙げられる。
Coating Forming Substance Precursor A coating forming substance precursor is a precursor of a coating forming substance. More specifically, the raw material of the coating-forming substance in the vapor phase is formed as it is, or is formed and / or synthesized from the raw material of the coating-forming substance through the vapor phase to form the coating on the core particles which are the particles to be coated. The substance just before The coat-forming substance precursor is not limited in its state as long as it is formed and / or synthesized from the raw material of the coat-forming substance through the gas phase somewhere.
When the raw material of the coating forming substance is in the gas phase, the raw material can also be a coating forming substance precursor. The coating forming material precursor itself may be in the gas phase. It may be before the reaction, during the reaction, or after the reaction. Specific examples of the coating material precursor include ions, atoms, molecules, clusters, atomic clusters, molecular clusters, cluster ions, ultrafine particles, gas, vapor and aerosols.

【0038】被覆形成物質の原料 被覆形成物質の原料とは、気相を経て被覆を形成する物
質となる原料物質をいう。被覆形成物質の原料の形態の
具体例として、塊状の固体、粉体粒子、気体、液体等が
挙げられる。
Raw Material of Coating Forming Material The raw material of the coating forming material means a raw material which becomes a material which forms a coating through a gas phase. Specific examples of the form of the raw material of the coating forming substance include lumpy solids, powder particles, gas and liquid.

【0039】分散度β 分散度βとは、粉体分散装置の分散性能を評価する指数
として増田、後藤氏らが提案(化学工学、第22回、秋
季大会研究発表講演要旨集、P349(1989)参
照)したように、全粒子の重量に対する、見かけの一次
粒子状態の粒子の重量の割合と定義する。ここで、見か
けの一次粒子状態の粒子とは、任意の分散状態の粉体粒
子の質量基準の頻度分布fm2と完全分散されている粉体
粒子の質量基準の頻度分布fm1のオーバーラップしてい
る部分の割合を示し、次の式のβで表される。
Dispersity β Dispersity β is an index for evaluating the dispersion performance of a powder disperser, proposed by Masuda, Goto et al. )), The ratio of the weight of particles in the apparent primary particle state to the weight of all particles is defined. Here, the particles in the apparent primary particle state are the overlap of the mass-based frequency distribution f m2 of the powder particles in an arbitrary dispersed state and the mass-based frequency distribution f m1 of the completely dispersed powder particles. The ratio of the part that is shown is represented by β in the following equation.

【0040】[0040]

【数1】 上式において、粒子径の単位(μm)は規定されるもの
ではない。
[Equation 1] In the above equation, the unit of particle diameter (μm) is not specified.

【0041】上式は質量基準で表した粒度分布を基にし
て分散度を評価しているが、本来分散度は体積基準で表
した粒度分布を基にして評価されるべきものである。し
かし粉体粒子密度が同じである場合には質量基準で表し
た粒度分布と体積基準で表した粒度分布は同じになる。
そこで実用上測定が容易な質量基準の粒度分布を測定
し、それを体積基準の粒度分布として用いている。従っ
て本来の分散度βは次の式及び図1の斜線部分の面積で
表される。
In the above formula, the dispersity is evaluated based on the particle size distribution expressed on a mass basis, but the dispersity should be evaluated on the basis of the particle size distribution expressed on a volume basis. However, when the powder particle densities are the same, the particle size distribution expressed by mass and the particle size distribution expressed by volume are the same.
Therefore, the mass-based particle size distribution, which is practically easy to measure, is measured and used as the volume-based particle size distribution. Therefore, the original dispersion degree β is expressed by the following equation and the area of the shaded area in FIG.

【0042】[0042]

【数2】 上式において粒子径の単位(μm)は規定されるもので
はない。そして芯粒子粉体の分布及び平均粒子径は、特
に断らない限り基本的には体積基準を用いることとす
る。
[Equation 2] In the above equation, the unit of particle size (μm) is not specified. The distribution and average particle diameter of the core particle powder are basically based on volume unless otherwise specified.

【0043】体積基準頻度分布 体積基準頻度分布とは、粒子径の分布をある粒子径に含
まれる体積割合をもって表したものをいう。
Volume-Based Frequency Distribution The volume-based frequency distribution refers to the distribution of particle diameters expressed by the volume ratio contained in a certain particle diameter.

【0044】(〔D1,D2〕,≧90%)の定義 (〔D1,D2〕,≧90%)分布とは、D1、D2を粒子
径、但しD1<D2とするとき、D1以上でD2以下の粒子
が体積で90%以上含まれる分布を表し、図1(b)の
ように斜線の部分の割合が90%以上である粒子からな
る粉体を表す。
[0044] ([D 1, D 2], ≧ 90%) Definition of ([D 1, D 2], ≧ 90%) and the distribution, D 1, the particle diameter D 2, where D 1 <D 2 , A distribution in which 90% or more by volume of particles of D 1 or more and D 2 or less is contained, and a powder composed of particles having a shaded portion ratio of 90% or more as shown in FIG. Represent

【0045】体積基準頻度分布(〔DM/5,5DM〕,
≧90%)の定義 本発明で用いる、粒度分布が、体積基準頻度分布で
(〔DM/5,5DM〕,≧90%)分布とは、DMを体
積基準の平均粒子径とするとき、DMの1/5倍の粒子
径以上、DMの5倍の粒子径以下の粒子を体積で90%
以上含む分布を表す。例えば平均粒子径DMが20μm
で体積基準頻度分布が(〔DM/5,5DM〕,≧90
%)とは、体積基準の平均粒子径が20μmで、4μm
以上且つ100μm以下の粒子径の粒子が体積で90%
以上含まれるような分布を表す。ここで、体積基準の平
均粒子径DMは、
Volume-based frequency distribution ([D M / 5,5D M ],
Definition of ≧ 90%) The particle size distribution used in the present invention is a volume-based frequency distribution ((D M / 5,5D M ], ≧ 90%), and D M is the volume-based average particle size. when, 1/5 of the particle size or less on the D M, 90% by volume five times under particle size or less particles of D M
It represents the distribution including the above. For example, the average particle diameter D M is 20 μm
And the volume-based frequency distribution is ([D M / 5,5D M ], ≧ 90
%) Means that the volume-based average particle diameter is 20 μm and is 4 μm.
90% by volume of particles having a particle size of 100 μm or less
It represents a distribution that is included above. Here, the volume-based average particle diameter D M is

【数3】 又は技術的には、ある粒子径間隔をDi±△Di/2(△
iは区分の幅)内にある粒子群の体積をviとすると、 DM=Σ(vii)/Σvi と表される。
[Equation 3]Or technically, a certain particle size interval Di± △ Di/ 2 (△
DiIs the width of the partition)iThen, DM= Σ (viDi) / Σvi  Is expressed as

【0046】被覆開始領域 準微粒子高分散処理手段群の最終処理後、初めて被覆が
開始される領域を被覆開始領域という。従って、準微粒
子高分散処理手段群の最終処理以前では、初めて被覆が
開始される領域でも、本発明での被覆開始領域ではな
い。
Coating start region The region where coating is started for the first time after the final treatment of the quasi-fine particle high dispersion treatment means group is called the coating start region. Therefore, even before the final treatment of the quasi-fine particle high dispersion treatment means group, the region where the coating is first started is not the coating start region in the present invention.

【0047】被覆開始領域での分散度β 本発明では、(1)体積基準頻度分布で平均粒径が10
μmを越え20μm以下の芯粒子粉体を準微粒子高分散
処理手段群の最終処理により気中に分散させて高分散芯
粒子粉体の粒子・気体混合物とし、その芯粒子粉体の粒
子の分散度βを80%以上とするか、又は(2)体積基
準頻度分布で平均粒径が20μmを越え50μm以下の
芯粒子粉体を準微粒子高分散処理手段群の最終処理によ
り気中に分散させて高分散芯粒子粉体の粒子・気体混合
物とし、その芯粒子粉体の粒子の分散度βを90%以上
とするか、又は(3)体積基準頻度分布で平均粒径が5
0μmを越え300μm以下の芯粒子粉体を準微粒子高
分散処理手段群の最終処理により気中に分散させて高分
散芯粒子粉体の粒子・気体混合物とし、その芯粒子粉体
の粒子の分散度βを95%以上とするか、又は(4)体
積基準頻度分布で平均粒子径が300μmを越え800
μm以下の芯粒子粉体を準微粒子高分散処理手段群の最
終処理により気中に分散させて高分散芯粒子粉体の粒子
・気体混合物とし、その芯粒子粉体の粒子の分散度βを
97%以上とするか、又は(5)体積基準頻度分布で平
均粒子径が800μmを越える芯粒子粉体を、準微粒子
高分散処理手段群の最終処理により気中に分散させて高
分散芯粒子粉体の粒子・気体混合物とし、その芯粒子粉
体の粒子の分散度βを99%以上とした領域に被覆空間
の被覆開始領域を位置せしめた被覆室を設ける。
Dispersion degree β in coating start region In the present invention, (1) volume-based frequency distribution has an average particle size of 10
A core particle powder having a particle diameter of more than 20 μm and not more than 20 μm is dispersed in the air by the final treatment of the quasi-fine particle high dispersion treatment means group to obtain a particle / gas mixture of the highly dispersed core particle powder, and the dispersion of the particles of the core particle powder. The degree β is set to 80% or more, or (2) core particle powder having an average particle size of more than 20 μm and 50 μm or less in the volume standard frequency distribution is dispersed in the air by the final treatment of the quasi-fine particle high dispersion treatment means group. A high-dispersion core particle powder as a particle / gas mixture, and the degree of dispersion β of the particles of the core particle powder is 90% or more, or (3) the volume-based frequency distribution has an average particle diameter of 5
A core particle powder having a particle size of more than 0 μm and not more than 300 μm is dispersed in the air by the final treatment of the quasi-fine particle high dispersion treatment means group to form a particle / gas mixture of the highly dispersed core particle powder, and the dispersion of the particles of the core particle powder. The degree β is 95% or more, or (4) the volume-based frequency distribution has an average particle size exceeding 300 μm and 800
The core particle powder having a particle diameter of μm or less is dispersed in the air by the final treatment of the quasi-fine particle high dispersion treatment means group to obtain a particle / gas mixture of the highly dispersed core particle powder, and the degree of dispersion β of the particles of the core particle powder is Or 95% or more, or (5) core particle powder having an average particle size of more than 800 μm in the volume-based frequency distribution is dispersed in the air by the final treatment of the quasi-fine particle high-dispersion treatment means group to obtain highly dispersed core particles. A coating chamber in which the coating start region of the coating space is located in a region in which the degree of dispersion β of the particles of the core particle powder is 99% or more is provided as a powder particle / gas mixture.

【0048】上記した被覆空間の被覆開始領域における
分散度であれば、芯粒子粉体の粒子が、体積基準頻度分
布で平均粒子径が10μmを越える準微粒子芯粒子粉体
の粒子又は主に準微粒子からなる芯粒子粉体の粒子を、
実質的に気中に単一粒子状態に分散でき、被覆空間の被
覆開始領域を通過する全ての芯粒子粉体の粒子の表面
に、被覆形成物質前駆体が均等に接触及び/又は衝突す
るため、単一粒子に均一な量の被覆形成物質を付けるこ
とができる。平均粒子径が10μmを越える準微粒子に
おいて、上記分散度βは、芯粒子粉体の平均粒子径と共
に連続的に変化するが、表現困難なため便宜的に段階的
な表現とした。
As far as the dispersity is in the coating start region of the above-mentioned coating space, the particles of the core particle powder are quasi-fine particles having an average particle size of more than 10 μm in the volume-based frequency distribution, or mainly quasi-fine particles. Core particles consisting of fine particles
The coating material precursor can evenly contact and / or collide with the surface of all particles of the core particle powder that can be dispersed in the air into a single particle state and pass through the coating start region of the coating space. , A uniform amount of coating-forming material can be applied to a single particle. In the quasi-fine particles having an average particle size of more than 10 μm, the dispersity β changes continuously with the average particle size of the core particle powder, but since it is difficult to express, it is expressed stepwise for convenience.

【0049】好適には、(1)体積基準頻度分布で平均
粒径が10μmを越え20μm以下の芯粒子粉体を準微
粒子高分散処理手段群の最終処理により気中に分散させ
て高分散芯粒子粉体の粒子・気体混合物とし、その芯粒
子粉体の粒子の分散度βを90%以上とするか、又は
(2)体積基準頻度分布で平均粒径が20μmを越え5
0μmの芯粒子粉体を準微粒子高分散処理手段群の最終
処理により気中に分散させて高分散芯粒子粉体の粒子・
気体混合物とし、その芯粒子粉体の粒子の分散度βを9
5%以上とするか、又は(3)体積基準頻度分布で平均
粒子径が50μmを越え300μm以下の芯粒子粉体を
準微粒子高分散処理手段群の最終処理により気中に分散
させて高分散芯粒子粉体の粒子・気体混合物とし、その
芯粒子粉体の粒子の分散度βを97%以上とするか、又
は(4)体積基準頻度分布で平均粒子径が300μmを
越える芯粒子粉体を準微粒子高分散処理手段群の最終処
理により気中に分散させて高分散芯粒子粉体の粒子・気
体混合物とし、その芯粒子粉体の粒子の分散度βを99
%以上とした空間領域に被覆空間の被覆開始領域を位置
せしめた被覆室を設けることである。被覆空間の被覆開
始領域をこのように位置せしめた被覆室であれば、芯粒
子粉体の粒子が、体積基準頻度分布で平均粒子径が10
μmを越える準微粒子芯粒子粉体の粒子又は主に準微粒
子からなる芯粒子粉体の粒子に対して、単一粒子単位で
被覆形成物質をより均一に被覆でき、且つ各芯粒子ごと
に被覆量のより均一な被覆ができる。
Preferably, (1) a core particle powder having an average particle size of more than 10 μm and 20 μm or less in a volume standard frequency distribution is dispersed in the air by the final treatment of the quasi-fine particle high dispersion treatment means group to obtain a highly dispersed core. A particle / gas mixture of particle powder, and the degree of particle dispersion β of the core particle powder is 90% or more, or (2) the volume-based frequency distribution has an average particle size of more than 20 μm and 5
0 μm core particle powder is dispersed in the air by the final treatment of the quasi-fine particle high-dispersion treatment means group to form particles of high-dispersion core particle powder.
As a gas mixture, the degree of particle dispersion β of the core particle powder is 9
5% or more, or (3) core particle powder having an average particle size of more than 50 μm and 300 μm or less in the volume standard frequency distribution is dispersed in the air by the final treatment of the quasi-fine particle high dispersion treatment means group to achieve high dispersion. A particle / gas mixture of the core particle powder, and the degree of dispersion β of the particles of the core particle powder is 97% or more, or (4) the core particle powder having an average particle diameter of more than 300 μm in a volume standard frequency distribution. Is dispersed in the air by the final treatment of the quasi-fine particle high dispersion treatment means group to form a particle / gas mixture of the highly dispersed core particle powder, and the degree of dispersion β of the particles of the core particle powder is 99.
It is to provide a coating chamber in which the coating start region of the coating space is located in the space region of not less than%. In the coating chamber in which the coating start region of the coating space is positioned as described above, the particles of the core particle powder have an average particle diameter of 10 in volume-based frequency distribution.
Particles of quasi-fine particle core particles having a particle size of more than μm or particles of core particle powder mainly consisting of quasi-fine particles can be more uniformly coated with a coating forming substance in a single particle unit, and each core particle can be coated. A more uniform amount of coating is possible.

【0050】体積基準頻度分布で平均粒子径が10μm
を越える準微粒子芯粒子粉体の粒子又は主に準微粒子か
らなる芯粒子粉体の粒子は、気中に於いては凝集作用が
働き、粒子同士で接触及び/又は衝突しあい高分散芯粒
子粉体の粒子・気体混合物中の芯粒子粉体の粒子の分布
が不均一になる。しかし、上記、芯粒子粉体の粒子の粒
径に応じた分散度のごとき分散状態で被覆を開始すれ
ば、準微粒子芯粒子粉体の粒子又は主に準微粒子からな
る芯粒子粉体の粒子単一粒子単位により均一に被覆形成
物質を被覆でき、且つ各粒子ごとにより均一な量に被覆
形成物質を被覆できる。
Volume-based frequency distribution with an average particle size of 10 μm
Particles of quasi-fine particle core particles having a particle size of more than 50% or particles of core particle powder mainly composed of quasi-fine particles have an aggregating action in the air, and the particles are in contact with each other and / or collide with each other to obtain highly dispersed core particle powder. Non-uniform distribution of particles in the core particle powder in the body particle / gas mixture. However, if the coating is started in a dispersed state such as the degree of dispersion according to the particle size of the core particle powder, the particles of the quasi-fine particle core particle powder or the particles of the core particle powder mainly composed of quasi-fine particles The single particle unit can coat the coating forming material uniformly, and each particle can coat the coating forming material in a more uniform amount.

【0051】準微粒子高分散処理手段群 本発明に於いて、準微粒子高分散処理手段群とは、 (A) 少なくとも分散手段を1以上有し、 (B) 最終の処理手段として、(a)芯粒子粉体の粒
子を気中に分散させる分散手段、又は、(b)芯粒子粉
体の粒子を気中に分散させた芯粒子粉体の粒子と気体と
の混合物において低分散芯粒子粉体部分を分離し、芯粒
子粉体の粒子が主に単一粒子状態で気中に存在する高分
散芯粒子粉体の粒子・気体混合物を選択する高分散芯粒
子粉体の粒子・気体混合物選択手段とこの高分散芯粒子
粉体の粒子・気体混合物選択手段により分離された低分
散芯粒子粉体部分をこの準微粒子高分散処理手段群中の
分散手段の内の最終分散手段及び/又は最終分散手段以
前の処理手段に搬送するフィードバック手段とを備えた
高分散芯粒子粉体の粒子・気体混合物選択手段を有する
ものである。
Semi-fine particle high dispersion treatment means group In the present invention, the semi-fine particle high dispersion treatment means group includes (A) at least one dispersion means, and (B) a final treatment means (a) Dispersing means for dispersing particles of the core particle powder in the air, or (b) a low dispersion core particle powder in a mixture of particles of the core particle powder in which the particles of the core particle powder are dispersed in the air and gas. A particle / gas mixture of highly dispersed core particle powder that separates the body part and selects the particle / gas mixture of highly dispersed core particle powder in which the particles of the core particle powder mainly exist in the air in a single particle state. The low-dispersion core particle powder portion separated by the selection means and the particle / gas mixture selection means of the high-dispersion core particle powder is the final dispersion means and / or the final dispersion means of the dispersion means in the quasi-fine particle high-dispersion processing means group. Feedback means to convey to the processing means before the final dispersion means And has a particle-gas mixture selection means e was highly dispersed core particles powder.

【0052】好適には、(1)体積基準頻度分布で平均
粒径が10μmを越え20μm以下の芯粒子粉体を準微
粒子高分散処理手段群の最終処理により気中に分散させ
て高分散芯粒子粉体の粒子・気体混合物とし、その芯粒
子粉体の粒子の分散度βを80%以上とするか、又は
(2)体積基準頻度分布で平均粒径が20μmを越え5
0μm以下の芯粒子粉体を準微粒子高分散処理手段群の
最終処理により気中に分散させて高分散芯粒子粉体の粒
子・気体混合物とし、その芯粒子粉体の粒子の分散度β
を90%以上とするか、又は(3)体積基準頻度分布で
平均粒径が50μmを越え300μm以下の芯粒子粉体
を準微粒子高分散処理手段群の最終処理により気中に分
散させて高分散芯粒子粉体の粒子・気体混合物とし、そ
の芯粒子粉体の粒子の分散度βを95%以上とするか、
又は(4)体積基準頻度分布で平均粒子径が300μm
を越え800μm以下の芯粒子粉体を準微粒子高分散処
理手段群の最終処理により気中に分散させて高分散芯粒
子粉体の粒子・気体混合物とし、その芯粒子粉体の粒子
の分散度βを97%以上とするか、又は(5)体積基準
頻度分布で平均粒子径が800μmを越える芯粒子粉体
を、準微粒子高分散処理手段群の最終処理により気中に
分散させて高分散芯粒子粉体の粒子・気体混合物とし、
その芯粒子粉体の粒子の分散度βを99%以上とする分
散性能を有するものである。前記被覆開始領域における
種々の分散度に対応してそれらと同等以上の分散性能の
準微粒子高分散処理手段群を設けることにより、被覆開
始領域において、各分散度に応じた高品位な被覆を施す
ことができる。
Preferably, (1) a core particle powder having an average particle size of more than 10 μm and not more than 20 μm in a volume-based frequency distribution is dispersed in the air by the final treatment of the quasi-fine particle high-dispersion treatment means group to obtain a highly dispersed core. The particle / gas mixture of the particle powder is used, and the dispersity β of the particles of the core particle powder is 80% or more, or (2) the volume-based frequency distribution has an average particle size of more than 20 μm and 5
The core particle powder having a particle size of 0 μm or less is dispersed in the air by the final treatment of the quasi-fine particle high dispersion treatment means group to form a particle / gas mixture of the highly dispersed core particle powder, and the degree of dispersion β of the particles of the core particle powder
Is 90% or more, or (3) core particle powder having an average particle size of more than 50 μm and 300 μm or less in the volume standard frequency distribution is dispersed in the air by the final treatment of the quasi-fine particle high dispersion treatment means group to obtain a high A particle / gas mixture of dispersed core particle powder, and the degree of dispersion β of the core particle powder is 95% or more,
Or (4) volume-based frequency distribution with an average particle size of 300 μm
The core particle powder having a diameter of more than 800 μm and not more than 800 μm is dispersed in the air by the final treatment of the quasi-fine particle high dispersion treatment means group to form a particle / gas mixture of the highly dispersed core particle powder, and the degree of dispersion of the particles of the core particle powder. β is set to 97% or more, or (5) core particle powder having an average particle size of more than 800 μm in the volume-based frequency distribution is dispersed in the air by the final treatment of the quasi-fine particle high dispersion treatment means group to achieve high dispersion. As a particle / gas mixture of core particle powder,
The core particle powder has a dispersibility in which the dispersity β of the particles is 99% or more. Corresponding to various dispersities in the coating start region, by providing a group of quasi-fine particle high dispersion treatment means having a dispersion performance equivalent to or higher than those of the dispersion start regions, a high-quality coating corresponding to each dispersity is performed in the coating start region. be able to.

【0053】最終処理手段 準微粒子高分散処理手段群の最終の処理手段が分散手段
の場合、この分散処理手段を微粒子高分散処理手段群の
最終処理手段という。又、準微粒子高分散処理手段群の
最終の処理手段が、準微粒子高分散処理手段の最終の分
散手段へ、高分散芯粒子粉体の粒子・気体混合物選択処
理工程時に於いて低分散状態であったために選択分離さ
れた部分を搬送するフィードバック手段を備えた高分散
芯粒子粉体の粒子・気体混合物選択手段、又は最終の分
散手段より前の処理手段に、高分散芯粒子粉体の粒子・
気体混合物選択処理工程時に於いて低分散状態であった
ために選択分離された部分を搬送するフィードバック手
段を備えた高分散芯粒子粉体の粒子・気体混合物選択手
段の場合、この高分散芯粒子粉体の粒子・気体混合物選
択手段を準微粒子高分散処理手段群の最終処理手段とい
う。
Final Treatment Means When the final treatment means of the semi-fine particle high dispersion treatment means group is a dispersion means, this dispersion treatment means is referred to as the final treatment means of the fine particle high dispersion treatment means group. Also, the final processing means of the quasi-fine particle high dispersion processing means group is added to the final dispersion means of the quasi-fine particle high dispersion processing means in a low dispersion state at the time of the particle / gas mixture selective processing step of the highly dispersed core particle powder. The particles / gas mixture selection means of the highly dispersed core particle powder provided with the feedback means for conveying the selected and separated portion, or the treatment means before the final dispersion means, the particles of the highly dispersed core particle powder.・
In the case of the particle / gas mixture selecting means of the highly dispersed core particle powder, which is provided with the feedback means for conveying the selectively separated portion due to the low dispersion state in the gas mixture selection treatment step, this highly dispersed core particle powder The means for selecting a body particle / gas mixture is referred to as the final treatment means of the quasi-fine particle high dispersion treatment means group.

【0054】尚、準微粒子高分散処理手段群の最終処理
手段であるフィードバック手段を備えた高分散芯粒子粉
体の粒子・気体混合物選択手段より前に設ける(例え
ば、このフィードバック手段を備えた高分散芯粒子粉体
の粒子・気体混合物選択手段と最終分散手段の間、或い
は最終分散手段より前)高分散芯粒子粉体の粒子・気体
混合物選択手段は、フィードバック手段の有無にかかわ
らず微粒子高分散処理手段群の構成要素である。
It should be noted that it is provided before the particle / gas mixture selecting means of the highly dispersed core particle powder, which is provided with the feedback means which is the final processing means of the quasi-fine particle high dispersion processing means group. Between the particle / gas mixture selection means of the dispersed core particle powder and the final dispersion means, or before the final dispersion means) The particle / gas mixture selection means of the highly dispersed core particle powder is fine particle height regardless of the presence or absence of the feedback means. It is a component of the distributed processing means group.

【0055】分散手段 分散するために用いる手段を分散手段という。少しでも
或いは僅かでも分散効果を有するものは分散手段として
使用可能であり、本発明ではこれを分散手段とする。例
えば、一般に供給手段として用いる空気輸送用のロータ
リーフィーダーやインジェクションフィーダー(粉体工
学会編:“粉体工学便覧”、日刊工業新聞社(198
6)P568、P571)は、分散効果も有するので、
分散目的の手段として使用する場合は分散手段である。
後述の分散維持・促進手段も分散目的で(βを高める目
的で)使用する場合は分散手段となる。
Dispersing Means The means used to disperse are called dispersing means. Those having a dispersion effect even if only a little or a little can be used as the dispersion means, and this is referred to as the dispersion means in the present invention. For example, pneumatically-used rotary feeders and injection feeders that are generally used as supply means (edited by Japan Society of Powder Engineering: “Powder Engineering Handbook”, Nikkan Kogyo Shimbun (198)
6) Since P568 and P571) also have a dispersion effect,
When used as a means for dispersion purpose, it is a dispersion means.
When the dispersion maintaining / promoting means described later is also used for the purpose of dispersion (to increase β), it becomes a dispersion means.

【0056】本発明において、準微粒子高分散処理手段
群は、芯粒子粉体の粒子の加速及び/又は速度勾配に置
く気流による分散、芯粒子粉体の粒子の静止障害物及び
/又は回転体である障害物への衝突による分散、芯粒子
粉体の粒子の流動層及び/又は脈流及び/又は回転ドラ
ム及び/又は振動及び/又は掻取りからなる機械的解砕
による分散の内の選択された一種以上の分散の機構を備
えたものである。
In the present invention, the group of means for high-dispersion quasi-fine particles include core particle powder particles dispersed by an air stream placed in an acceleration and / or velocity gradient, stationary particles of core particle powder, and / or rotating bodies. A dispersion by collision with an obstacle, a fluidized bed of particles of the core particle powder and / or a pulsating flow and / or a rotating drum and / or a mechanical disintegration consisting of vibration and / or scraping. It is equipped with one or more types of distributed mechanism.

【0057】具体的には、準微粒子高分散処理手段群
は、エジェクタ型分散機、ベンチュリ型分散機、細管、
撹拌機、気流中の障害物を利用した分散機、ジェットの
吹付けを利用した分散機、螺旋管、回転羽根を利用した
分散機、回転するビンを利用した分散機(ケージミ
ル)、流動層型分散機、脈流を利用した分散機、回転ド
ラムを利用した分散機、振動を利用した分散機、振動ふ
るい、スクレーパによる掻き取りを利用した分散機、SA
EI、Gonell式分散機、中条式分散機、Roller式分散機、
オリフィス型分散機、B.M式分散機、Timbrell式分散
機、Wright式分散機の内の選択された一種以上からなる
分散手段を備えた物である。(粉体工学会編:“粉体工
学便覧”、日刊工業新聞社(1986)P430)。
Specifically, the quasi-fine particle high dispersion treatment means group includes an ejector type disperser, a venturi type disperser, a capillary tube,
Stirrer, Disperser that uses obstacles in the air flow, Disperser that uses jet spraying, Spiral tube, Disperser that uses rotating blades, Disperser that uses a rotating bottle (cage mill), fluidized bed type Disperser, Disperser using pulsating flow, Disperser using rotating drum, Disperser using vibration, Vibration sieve, Disperser using scraping by scraper, SA
EI, Gonell type disperser, Nakajo type disperser, Roller type disperser,
It is provided with a dispersing means composed of one or more selected from an orifice type disperser, a BM type disperser, a Timbrell type disperser, and a Wright type disperser. (Powder Engineering Society: “Powder Engineering Handbook”, Nikkan Kogyo Shimbun (1986) P430).

【0058】また、特開昭56−1336号に記載の撹
拌羽根を利用した分散機、特開昭58−163454号
に記載の高速気流と分散ノズルを利用した分散機、特開
昭59−199027号に記載の回転羽根による分散作
用とプラズマイオンによる分散作用を利用した分散機、
特開昭59−207319号に記載のプラズマイオンに
よる分散作用を利用した分散機、特開昭59−2166
16号に記載のエジェクタとプラズマイオンによる分散
作用を利用した分散機、特開昭59−225728号に
記載のエジェクタとイオン流の分散作用を利用した分散
機、特開昭59−183845号に記載のプラズマイオ
ンの分散作用を利用した分散機、特開昭63−1664
21号に記載の分散羽根と圧力気体による分散作用を利
用した分散機、特開昭62−176527号に記載のラ
イン状又はリング状スリット型噴出口を用いた分散機、
特開昭63−221829号に記載の網状羽根を利用し
た分散機、特開昭63−1629号に記載の噴射ノズル
からの高速気流による分散作用を利用した分散機、実開
昭63−9218号に記載の多数の細孔を利用した分散
機、実開昭62−156854号に記載のエジェクタ型
分散機、実開昭63−6034号に記載の細孔とオリフ
ィスを利用した分散機等に記載のものも使用可能であ
る。
Further, a disperser using a stirring blade described in JP-A-56-1336, a disperser using a high-speed air stream and a dispersion nozzle described in JP-A-58-163454, and JP-A-59-199027. Disperser utilizing the dispersing action by the rotating blade and the dispersing action by plasma ions described in No.
A disperser utilizing the dispersing action of plasma ions described in JP-A-59-207319, and JP-A-59-2166.
No. 16, a disperser utilizing the dispersing action of an ejector and plasma ions, No. 59-225728, a disperser utilizing the dispersing action of an ejector and an ion flow, and No. 59-183845. Disperser utilizing the dispersing action of plasma ions of JP-A-63-1664
No. 21, a disperser utilizing a dispersing action by a dispersion blade and a pressure gas, a disperser using a line-shaped or ring-shaped slit type jet outlet described in JP-A-62-176527,
A disperser using a mesh blade described in JP-A No. 63-221829, a disperser using a dispersing action by a high-speed air stream from an injection nozzle described in JP-A No. 63-1629, No. Sho 63-9218. Described in the disperser using a large number of pores described in No. 6, the ejector type disperser described in Japanese Utility Model Publication No. 62-156854, and the disperser using the pores and orifices described in Japanese Utility Model Publication No. 63-6034. The thing of can also be used.

【0059】準微粒子高分散処理手段群に好適な分散手
段として、特願昭63−311358号、特願平1−7
1071号、特願平2−218537号等に記載の装置
が挙げられる。
Dispersing means suitable for the group of means for high-dispersion quasi-fine particles include Japanese Patent Application No. 63-311358 and Japanese Patent Application No. 1-7.
The apparatus described in Japanese Patent Application No. 1071 and Japanese Patent Application No. 2-218537 can be used.

【0060】高分散芯粒子粉体の粒子・気体混合物選択
手段 芯粒子粉体の粒子・気体混合物のなかから、主に単一粒
子状態の粒子を含む高分散芯粒子粉体の粒子・気体混合
物以外の低分散芯粒子粉体部分を分離し、主に単一粒子
状態の粒子を含む高分散芯粒子粉体の粒子・気体混合物
を選択する手段をいう。一次粒子の集合体である凝集粒
子は、見かけの粒子径が一次粒子の粒子径に比べ大きく
なることから、例えば乾式分級手段により分離が可能で
ある。この高分散芯粒子粉体の粒子・気体混合物選択手
段の例としては、重力を利用した分級手段、慣性力を利
用した分級手段、遠心力を利用した分級手段、静電気を
利用した分級手段、流動層を利用した分級手段等から一
種以上選択された乾式分級手段が挙げられる。
Highly-dispersed core particle powder / gas mixture selection means: Highly-dispersed core particle powder / gas mixture mainly containing particles in a single particle state among core particle powder / gas mixture Means for separating the low-dispersion core particle powder portion other than and selecting the particle / gas mixture of the high-dispersion core particle powder mainly containing particles in a single particle state. Aggregated particles, which are aggregates of primary particles, have an apparent particle diameter larger than the particle diameter of primary particles, and therefore can be separated by, for example, a dry classification means. Examples of the particle / gas mixture selecting means for the highly dispersed core particle powder include a classification means using gravity, a classification means using inertial force, a classification means using centrifugal force, a classification means using static electricity, and a flow method. Examples include dry classification means selected from one or more of classification means using layers.

【0061】この高分散芯粒子粉体の粒子・気体混合物
選択手段の例としては、重力分級機、慣性分級機、遠心
分級機、サイクロン、エアセパレータ、ミクロンセパレ
ータ、ミクロプレックス、ムルチプレックス、ジグザグ
分級機、アキュカット、コニカルセパレータ、ターボク
ラシファイア、スーパセパレータ、ディスパージョンセ
パレータ、エルボジェット、流動層分級機、バーチュア
ルインパクタ、O-Sepa、ふるい、バイブレーティングス
クリーン、シフタ(粉体工学会編:“粉体工学便覧”日
刊工業新聞社、P514(1986))等が挙げられ
る。
Examples of means for selecting a particle / gas mixture of this highly dispersed core particle powder include a gravity classifier, inertia classifier, centrifugal classifier, cyclone, air separator, micron separator, microplex, multiplex, zigzag classification. Machine, Accu-Cut, Conical separator, Turbo classifier, Super separator, Dispersion separator, Elbow jet, Fluidized bed classifier, Virtual impactor, O-Sepa, Sieve, Vibrating screen, Shifter (Powder Engineering Society: “Powder Engineering” Engineering Handbook "Nikkan Kogyo Shimbun, P514 (1986)) and the like.

【0062】芯粒子粉体の粒子・気体混合物 芯粒子粉体の粒子・気体混合物とは、(a)芯粒子粉体の
粒子が気中に一様に浮遊した均質流れ(一様な浮遊流
れ)、(b)芯粒子粉体の粒子が気中のある領域で非一様
な分布を示す不均質流れ(非均質浮遊流れ)、(c)芯粒
子粉体の粒子の摺動層を伴う流れ(摺動流れ)、又は
(d)芯粒子粉体の粒子の静止層を伴う流れをいう。
Particle / gas mixture of core particle powder The particle / gas mixture of core particle powder is (a) a homogeneous flow in which particles of the core particle powder are uniformly suspended in air (a uniform floating flow). ), (B) Inhomogeneous flow (non-homogeneous floating flow) in which particles of the core particle powder show a non-uniform distribution in a certain area in the air, (c) accompanied by a sliding layer of particles of the core particle powder Flow (sliding flow), or
(d) A flow with a stationary layer of particles of core particle powder.

【0063】低分散芯粒子粉体の粒子・気体混合物 芯粒子粉体の粒子・気体混合物の内、芯粒子粉体の粒子
が主に単一粒子状態以外の状態で気中に存在する芯粒子
粉体の粒子・気体混合物をいう。
Low-dispersion core particle powder particle / gas mixture Core particle powder particle / gas mixture mainly exists in the air in a state other than a single particle state. A powder particle / gas mixture.

【0064】高分散芯粒子粉体の粒子・気体混合物 芯粒子粉体の粒子が主に単一粒子状態で気中に存在する
芯粒子粉体の粒子・気体混合物をいう。高分散芯粒子粉
体の粒子・気体混合物は、極めて高分散であっても、実
際には凝集粒子を含む。低分散芯粒子粉体の粒子・気体
混合物は、実際には、凝集していない単粒子を含み、選
択分離して低分散芯粒子粉体の粒子・気体混合物と高分
散芯粒子粉体の粒子・気体混合物に分けられる。低分散
芯粒子粉体の粒子・気体混合物は、凝集粒子の選択分離
及び/又は再分散により、高分散芯粒子粉体の粒子・気
体混合物となる。
Particle / gas mixture of highly dispersed core particle powder This is a particle / gas mixture of core particle powder in which the particles of the core particle powder mainly exist in the air in a single particle state. The particle-gas mixture of the highly dispersed core particle powder actually contains agglomerated particles, even though it is extremely highly dispersed. The particles / gas mixture of the low-dispersion core particle powder actually contains non-aggregated single particles, and the particles / gas mixture of the low-dispersion core particle powder and the particles of the high-dispersion core particle powder are selectively separated. -Divided into gas mixtures. The particle / gas mixture of the low-dispersion core particle powder becomes a particle / gas mixture of the high-dispersion core particle powder by selectively separating and / or re-dispersing the agglomerated particles.

【0065】回収手段 被覆空間で被覆した被覆準微粒子を取り出す手段を回収
手段という。回収手段の内で回収処理の行われる部分を
回収部という。被覆空間の被覆開始領域を通過して被覆
した被覆準微粒子は、気中から直接取り出して回収する
か、又は気中から取り出して一時的に蓄えてから回収す
るか、又は、気体と共に回収される。回収手段の回収部
としては、隔壁(障害物)を利用した回収手段の回収
部、重力を利用した回収手段の回収部、慣性力を利用し
た回収手段の回収部、遠心力を利用した回収手段の回収
部、帯電による引力を利用した回収手段の回収部、熱泳
動力を利用した回収手段の回収部、ブラウン拡散を利用
した回収手段の回収部、ガスの背圧や減圧等による吸引
力を利用した回収手段の回収部等が利用可能である。こ
の回収手段の回収部の好適な例として、重力集塵機、慣
性集塵機、遠心力集塵機、濾過集塵機、電気集塵機、洗
浄集塵機、粒子充填層、サイクロン、バグフィルター、
セラミックスフィルター、スクラバー等が挙げられる。
Collecting Means The means for taking out the coated quasi-fine particles coated in the coating space is called collecting means. The part of the recovery means that performs the recovery process is called the recovery part. The coated quasi-fine particles coated by passing through the coating start region of the coating space are directly taken out from the air and collected, or taken out from the air and temporarily stored and then collected, or are collected together with the gas. . As the collecting unit of the collecting unit, a collecting unit of a collecting unit using a partition wall (obstacle), a collecting unit of a collecting unit using gravity, a collecting unit of a collecting unit using inertial force, a collecting unit using centrifugal force Collection part, collection part of collection means using attractive force due to electrification, collection part of collection means using thermophoretic force, collection part of collection means using Brownian diffusion, suction force by back pressure or decompression of gas, etc. It is possible to use the recovery unit of the recovery means used. As a preferred example of the recovery unit of this recovery means, gravity dust collector, inertial dust collector, centrifugal dust collector, filtration dust collector, electric dust collector, washing dust collector, particle packed bed, cyclone, bag filter,
Examples include ceramics filters and scrubbers.

【0066】準微粒子高分散処理手段群の図の説明 図2(a)は本発明の準微粒子高分散処理手段群の基本的
な構成の一例を表すブロック図である。芯粒子粉体の粒
子を分散させる最終の分散手段A、最終の分散手段以前
の分散処理手段群の構成要素dで構成されている。ε
は、芯粒子粉体の粒子の内、主に単一粒子状態で気中に
存在する高分散芯粒子粉体の粒子・気体混合物である。
構成要素dとしては、分散手段、供給手段、高分散芯粒
子粉体の粒子・気体混合物選択手段等任意の処理手段を
単独又は組み合わせて使用できる。構成要素dは、必ず
しも設けなくとも良い。準微粒子高分散処理手段群
は、、最終の処理手段である分散手段Aの処理後、
(1)体積基準頻度分布で平均粒子径が10μmを越え
20μm以下の芯粒子粉体に対し、分散度がβで80%
以上、又は(2)体積基準頻度分布で平均粒子径が20
μmを越え50μm以下の芯粒子粉体に対し、分散度が
βで90%以上、又は(3)体積基準頻度分布で平均粒
子径が50μmを越え300μm以下の芯粒子粉体に対
し、分散度がβで95%以上、又は(4)体積基準頻度
分布で平均粒子径が300μmを越え800μm以下の
芯粒子粉体に対し、分散度がβで97%以上、又は
(5)体積基準頻度分布で平均粒子径が800μmを越
える芯粒子粉体に対し、分散度がβで99%以上を実現
できる構成のものである。
FIG. 2A is a block diagram showing an example of the basic configuration of the quasi-particulate high dispersion processing means group of the present invention. It is composed of the final dispersion means A for dispersing the particles of the core particle powder and the constituent element d of the dispersion processing means group before the final dispersion means. ε
Is a particle / gas mixture of the highly dispersed core particle powder, which is mainly present in the air in the form of a single particle among the particles of the core particle powder.
As the constituent element d, any treatment means such as a dispersion means, a supply means, a particle / gas mixture selection means of highly dispersed core particle powder can be used alone or in combination. The component d does not necessarily have to be provided. The quasi-fine particle high dispersion treatment means group is, after the treatment of the dispersion means A, which is the final treatment means,
(1) With respect to the core particle powder having a volume-based frequency distribution and an average particle size of more than 10 μm and 20 μm or less, the dispersity is β = 80%
Or (2) the volume-based frequency distribution has an average particle size of 20
The dispersity is 90% or more in β with respect to the core particle powder of more than μm and 50 μm or less. Is 95% or more in β, or (4) the core particle powder having an average particle size exceeding 300 μm and 800 μm or less in the volume standard frequency distribution, the dispersity is 97% or more in β, or (5) the volume standard frequency distribution With respect to the core particle powder having an average particle diameter of more than 800 μm, the dispersity β can be 99% or more.

【0067】図2(b)は、本発明の準微粒子高分散処理
手段群の基本的な構成の他の一例を表すブロック図であ
る。芯粒子粉体の粒子を分散させる最終の分散手段A、
最終の分散手段Aへ芯粒子粉体の粒子が、主に単一粒子
状態で気中に存在する高分散芯粒子粉体の粒子・気体混
合物、以外の低分散芯粒子粉体の粒子・気体混合物ηを
フィードバックさせるフィードバック手段Cを備えた最
終の高分散芯粒子粉体の粒子・気体混合物選択手段B、
最終の分散手段以前の分散処理手段群の構成要素d、最
終分散手段と最終選択手段の間の準微粒子高分散処理手
段群の構成要素eで構成されている。εは、芯粒子粉体
の粒子の内、主に単一粒子状態で気中に存在する高分散
芯粒子粉体の粒子・気体混合物である。構成要素dとし
ては、分散手段、供給手段、選択手段等任意の処理手段
を単独又は組み合わせて使用できる。構成要素eとして
は、分散手段以外の処理手段、例えば供給手段、選択手
段等任意の処理手段を単独又は組み合わせて使用でき
る。構成要素d及びeは、必ずしも設けなくとも良い。
準微粒子高分散処理手段群は、最終の処理手段である選
択手段Bによる処理後、前記平均粒子径の芯粒子粉体に
対し前記分散度を実現できる構成のものである。
FIG. 2B is a block diagram showing another example of the basic constitution of the quasi-fine particle high dispersion treatment means group of the present invention. The final dispersing means A for dispersing the particles of the core particle powder,
To the final dispersion means A, particles of the high-dispersion core particle powder in which the particles of the core particle powder mainly exist in the air in a single particle state, and particles / gas of the low-dispersion core particle powder other than Particle / gas mixture selecting means B of the final highly dispersed core particle powder provided with a feedback means C for feeding back the mixture η,
It is composed of the constituent element d of the dispersion processing means group before the final dispersion means and the constituent element e of the quasi-fine particle high dispersion processing means group between the final dispersion means and the final selection means. [epsilon] is a particle / gas mixture of highly dispersed core particle powder, which exists in the air mainly in a single particle state among particles of the core particle powder. As the constituent element d, any processing means such as a dispersing means, a supplying means, a selecting means can be used alone or in combination. As the component e, a processing means other than the dispersion means, for example, an arbitrary processing means such as a supply means and a selection means can be used alone or in combination. The components d and e do not necessarily have to be provided.
The quasi-fine particle high-dispersion processing means group has a configuration capable of realizing the above-mentioned degree of dispersion with respect to the core particle powder having the above-mentioned average particle diameter after the processing by the selecting means B which is the final processing means.

【0068】図2(c)は、本発明の準微粒子高分散処理
手段群の基本的な構成の他の一例を表すブロック図であ
る。芯粒子粉体の粒子を分散させる最終の分散手段A、
最終の分散手段Aより前の処理手段へ芯粒子粉体の粒子
が、主に単一粒子状態で気中に存在する高分散芯粒子粉
体の粒子・気体混合物、以外の低分散芯粒子粉体の粒子
・気体混合物ηをフィードバックさせるフィードバック
手段Cを備えた高分散芯粒子粉体の粒子・気体混合物選
択手段B、最終の分散手段以前の準微粒子高分散処理手
段群の構成要素d、最終の分散手段と最後の選択手段の
間の準微粒子高分散処理手段群の構成要素eで構成され
ている。εは、芯粒子粉体の粒子の内、主に単一粒子状
態で気中に存在する高分散芯粒子粉体の粒子・気体混合
物である。構成要素dとしては、分散手段、供給手段、
選択手段等任意の処理手段を単独又は組み合わせて使用
できる。構成要素dとしては、分散手段以外の処理手
段、例えば供給手段、選択手段等任意の処理手段を単独
又は組み合わせて使用できる。構成要素d及びeは、必
ずしも設けなくとも良い。準微粒子高分散処理手段群
は、最終の処理手段である選択手段Bによる処理後、前
記平均粒子径の芯粒子粉体に対し前記分散度を実現でき
る構成のものである。
FIG. 2C is a block diagram showing another example of the basic constitution of the quasi-fine particle high dispersion treatment means group of the present invention. The final dispersing means A for dispersing the particles of the core particle powder,
To the processing means before the final dispersing means A Low-dispersion core particle powder other than a particle / gas mixture of highly dispersed core particle powder in which the particles of the core particle powder are mainly present in the air in a single particle state Highly dispersed core particle powder particle / gas mixture selection means B provided with a feedback means C for feeding back the body particle / gas mixture η, component d of the quasi-fine particle high dispersion treatment means group before the final dispersion means, and final It is composed of the constituent element e of the quasi-fine particle high dispersion treatment means group between the dispersion means and the last selection means. [epsilon] is a particle / gas mixture of highly dispersed core particle powder, which exists in the air mainly in a single particle state among particles of the core particle powder. As the component d, a dispersion means, a supply means,
Any processing means such as selection means can be used alone or in combination. As the constituent element d, any processing means other than the dispersion means, for example, an arbitrary processing means such as a supply means and a selection means can be used alone or in combination. The components d and e do not necessarily have to be provided. The quasi-fine particle high-dispersion processing means group has a configuration capable of realizing the above-mentioned degree of dispersion with respect to the core particle powder having the above-mentioned average particle diameter after the processing by the selecting means B which is the final processing means.

【0069】なお、以上のような構成であるから、供給
槽、芯粒子生成手段等の粉体の供給源も本準微粒子高分
散処理手段群の構成に含めてもよい。例えば図2(c)の
場合、フィードバック手段Cのフィードバック先を供給
槽とする構成も高分散処理手段群の構成として良いこと
は言うまでもない。又、準微粒子高分散処理手段群の分
散工程の前に、芯粒子粉体の粒子を解砕及び/又は粉砕
する解砕工程を入れても良いことは言うまでもない。
Because of the above-mentioned structure, the powder supply source such as the supply tank and the core particle generating means may be included in the structure of the semi-fine particle high dispersion processing means group. For example, in the case of FIG. 2C, it goes without saying that the configuration in which the feedback destination of the feedback means C is the supply tank may be the configuration of the high dispersion processing means group. Needless to say, a crushing step of crushing and / or crushing particles of the core particle powder may be added before the dispersing step of the quasi-fine particle high dispersion treatment means group.

【0070】上記した準微粒子高分散処理手段群の基本
的な構成をより詳細にしたブロック図に基づいて更に詳
しく説明することにする。
The basic structure of the above-mentioned quasi-fine particle high dispersion processing means group will be described in more detail with reference to a more detailed block diagram.

【0071】構成1 図3(a)は、本発明の準微粒子高分散処理手段群の第1
の構成を説明するブロック図であって図2(a)に対応す
るものである。本例は、被覆される芯粒子粉体を供給す
る供給槽100、被覆される芯粒子粉体を分散させる最
終分散手段Aから構成されている。εは、芯粒子粉体の
粒子の内、主に単一粒子状態で気中に存在する高分散芯
粒子粉体の粒子・気体混合物である。
Structure 1 FIG. 3 (a) shows a first group of quasi-fine particle high dispersion treatment means group of the present invention.
2 is a block diagram for explaining the configuration of FIG. 2 and corresponds to FIG. This example comprises a supply tank 100 for supplying the core particle powder to be coated, and a final dispersion means A for dispersing the core particle powder to be coated. [epsilon] is a particle / gas mixture of highly dispersed core particle powder, which exists in the air mainly in a single particle state among particles of the core particle powder.

【0072】構成2 図3(b)は、本発明の準微粒子高分散処理手段群の第2
の構成を説明するブロック図であって図2(a)に対応す
るものである。本例は、被覆される芯粒子粉体を供給す
る供給槽100、被覆される芯粒子粉体を分散させる分
散手段a、被覆される芯粒子粉体を分散させる最終分散
手段Aから構成されている。εは、芯粒子粉体の粒子の
内、主に単一粒子状態で気中に存在する高分散芯粒子粉
体の粒子・気体混合物である。
Structure 2 FIG. 3 (b) shows the second semi-fine particle high dispersion treatment means group of the present invention.
2 is a block diagram for explaining the configuration of FIG. 2 and corresponds to FIG. This example comprises a supply tank 100 for supplying the core particle powder to be coated, a dispersing means a for dispersing the core particle powder to be coated, and a final dispersing means A for dispersing the core particle powder to be coated. There is. [epsilon] is a particle / gas mixture of highly dispersed core particle powder, which exists in the air mainly in a single particle state among particles of the core particle powder.

【0073】構成3 図3(c)は、本発明の準微粒子高分散処理手段群の第3
の構成を説明するブロック図であって図2(b)に対応す
るものである。本例は、被覆される芯粒子粉体を供給す
る供給槽100、被覆される芯粒子粉体を分散させる分
散手段a、分散手段aで分散させた芯粒子粉体の粒子・
気体混合物のうちから主に単一粒子状態で気中に存在す
る高分散芯粒子粉体の粒子・気体混合物、以外の低分散
芯粒子粉体の粒子・気体混合物ηを分散手段aへフィー
ドバックさせるフィードバック手段C、主に高分散芯粒
子粉体の粒子・気体混合物を最終の分散手段Aへ導入す
る高分散芯粒子粉体の粒子・気体混合物選択手段b、被
覆される芯粒子粉体を分散させる最終分散手段A、から
構成されている。εは、芯粒子粉体の粒子の内、主に単
一粒子状態で気中に存在する高分散芯粒子粉体の粒子・
気体混合物である。
Structure 3 FIG. 3 (c) shows a third group of quasi-fine particle high dispersion treatment means group of the present invention.
2 is a block diagram for explaining the configuration of FIG. 2 and corresponds to FIG. In this example, a supply tank 100 for supplying the core particle powder to be coated, a dispersing means a for dispersing the core particle powder to be coated, and particles of the core particle powder dispersed by the dispersing means a.
From the gas mixture, the particles / gas mixture of the low-dispersion core particle powder other than the particles / gas mixture of the high-dispersion core particle powder mainly existing in the air in a single particle state are fed back to the dispersing means a. Feedback means C, mainly particle / gas mixture of highly dispersed core particle powder for introducing the particle / gas mixture of highly dispersed core particle powder into the final dispersion means A, dispersion of core particle powder to be coated It is composed of a final dispersion means A. ε is the particle of the highly dispersed core particle powder that exists mainly in the air in the form of a single particle among the particles of the core particle powder.
It is a gas mixture.

【0074】構成4 図3(d)は、本発明の準微粒子高分散処理手段群の第4
の構成を説明するブロック図であって図2(b)に対応す
るものである。本例は、被覆される芯粒子粉体を供給す
る供給槽100、被覆される芯粒子粉体を分散させる最
終分散手段A、最終分散手段Aで分散させた芯粒子粉体
の粒子・気体混合物のうちから主に単一粒子状態で気中
に存在する高分散芯粒子粉体の粒子・気体混合物、以外
の低分散芯粒子粉体の粒子・気体混合物ηを分散手段A
へフィードバックするフィードバック手段C、高分散芯
粒子粉体の粒子・気体混合物を放出する最終の高分散芯
粒子粉体の粒子・気体混合物選択手段Bから構成されて
いる。εは、芯粒子粉体の粒子の内、主に単一粒子状態
で気中に存在する高分散芯粒子粉体の粒子・気体混合物
である。
Structure 4 FIG. 3 (d) shows a fourth example of the quasi-fine particle high dispersion treatment means group of the present invention.
2 is a block diagram for explaining the configuration of FIG. 2 and corresponds to FIG. In this example, a supply tank 100 for supplying the core particle powder to be coated, a final dispersion means A for dispersing the core particle powder to be coated, and a particle / gas mixture of the core particle powder dispersed by the final dispersion means A. Of the above, particles / gas mixture of high-dispersion core particle powder existing mainly in the air in the form of a single particle and particles / gas mixture η of low-dispersion core particle powder other than A are dispersed by means A.
It comprises a feedback means C for feeding back to, and a final particle / gas mixture selecting means B for discharging the highly dispersed core particle powder particle / gas mixture. [epsilon] is a particle / gas mixture of highly dispersed core particle powder, which exists in the air mainly in a single particle state among particles of the core particle powder.

【0075】構成5 図3(e)は、本発明の準微粒子高分散処理手段群の第5
の構成を説明するブロック図であって図2(b)に対応す
るものである。本例は、被覆される芯粒子粉体を供給す
る供給槽100、被覆される芯粒子粉体を分散させる分
散手段a、被覆される芯粒子粉体を分散させる最終分散
手段A、最終分散手段Aで分散させた芯粒子粉体の粒子
・気体混合物のうちから主に単一粒子状態で気中に存在
する高分散芯粒子粉体の粒子・気体混合物、以外の低分
散芯粒子粉体の粒子・気体混合物ηを分散手段Aへフィ
ードバックするフィードバック手段C、高分散芯粒子粉
体の粒子・気体混合物を放出する最終の高分散芯粒子粉
体の粒子・気体混合物選択手段Bから構成されている。
εは、芯粒子粉体の粒子の内、主に単一粒子状態で気中
に存在する高分散芯粒子粉体の粒子・気体混合物であ
る。
Structure 5 FIG. 3 (e) shows the fifth semi-fine particle high dispersion treatment means group of the present invention.
2 is a block diagram for explaining the configuration of FIG. 2 and corresponds to FIG. In this example, a supply tank 100 for supplying the core particle powder to be coated, a dispersing means a for dispersing the core particle powder to be coated, a final dispersing means A for dispersing the core particle powder to be coated, and a final dispersing means. Of the low-dispersion core particle powder other than the high-dispersion core particle powder particle / gas mixture mainly existing in the air in the form of a single particle among the particle / gas mixture particles of the core particle powder dispersed in A. It comprises a feedback means C for feeding back the particle / gas mixture η to the dispersing means A, and a final particle / gas mixture selecting means B for releasing the particle / gas mixture of the highly dispersed core particle powder. There is.
[epsilon] is a particle / gas mixture of highly dispersed core particle powder, which exists in the air mainly in a single particle state among particles of the core particle powder.

【0076】構成6 図3(f)は、本発明の準微粒子高分散処理手段群の第6
の構成を説明するブロック図であって図2(b)に対応す
るものである。本例は、被覆される芯粒子粉体を供給す
る供給槽100、芯粒子粉体の粒子・気体混合物のうち
から主に低分散芯粒子粉体の粒子・気体混合物を取り除
き、主に高分散芯粒子粉体の粒子・気体混合物を分散手
段Aへ導入する高分散芯粒子粉体の粒子・気体混合物選
択手段b、選択分離された芯粒子粉体の粒子を分散させ
る最終分散手段A、最終分散手段Aで分散させた芯粒子
粉体の粒子・気体混合物のうちから主に単一粒子状態で
気中に存在する高分散芯粒子粉体の粒子・気体混合物、
以外の低分散芯粒子粉体の粒子・気体混合物ηを分散手
段Aへフィードバックさせるフィードバック手段C、高
分散芯粒子粉体の粒子・気体混合物を放出する最終の高
分散芯粒子粉体の粒子・気体混合物選択手段Bから構成
されている。εは、芯粒子粉体の粒子の内、主に単一粒
子状態で気中に存在する高分散芯粒子粉体の粒子・気体
混合物である。
Structure 6 FIG. 3 (f) shows the sixth embodiment of the quasi-fine particle high dispersion treatment means group of the present invention.
2 is a block diagram for explaining the configuration of FIG. 2 and corresponds to FIG. In this example, a low-dispersion core particle powder / gas mixture is mainly removed from the supply tank 100 for supplying the core particle powder to be coated, and a particle / gas mixture of the core particle powder is removed, and mainly high dispersion is performed. Highly dispersed core particle powder particle / gas mixture selecting means b for introducing the particle / gas mixture of the core particle powder into the dispersing means A, final dispersing means A for dispersing the particles of the core particle powder selected and separated, and finally Of the particles / gas mixture of the core particle powder dispersed by the dispersing means A, the particles / gas mixture of highly dispersed core particle powder mainly present in the air in a single particle state,
Feedback means C for feeding back particles / gas mixture η of low-dispersion core particle powder to dispersion means A, particles of high-dispersion core particle powder / final particles of high-dispersion core particle powder releasing gas mixture / It is composed of a gas mixture selecting means B. [epsilon] is a particle / gas mixture of highly dispersed core particle powder, which exists in the air mainly in a single particle state among particles of the core particle powder.

【0077】構成7 図3(g)は、本発明の準微粒子高分散処理手段群の第7
の構成を説明するブロック図であって図2(c)に対応す
るものである。本例は、被覆される芯粒子粉体を供給す
る供給槽100、被覆される芯粒子粉体を分散させる分
散手段a、被覆される芯粒子粉体を分散させる最終分散
手段A、最終分散手段Aで分散させた芯粒子粉体の粒子
・気体混合物のうちから主に単一粒子状態で気中に存在
する高分散芯粒子粉体の粒子・気体混合物、以外の低分
散芯粒子粉体部分ηを分散手段aへフィードバックする
フィードバック手段C、高分散芯粒子粉体の粒子・気体
混合物を放出する最終の高分散芯粒子粉体の粒子・気体
混合物選択手段Bから構成されている。εは、芯粒子粉
体の粒子の内、主に単一粒子状態で気中に存在する高分
散芯粒子粉体の粒子・気体混合物である。
Structure 7 FIG. 3 (g) shows the seventh embodiment of the semi-fine particle high dispersion treatment means group of the present invention.
2 is a block diagram for explaining the configuration of FIG. 2 and corresponds to FIG. In this example, a supply tank 100 for supplying the core particle powder to be coated, a dispersing means a for dispersing the core particle powder to be coated, a final dispersing means A for dispersing the core particle powder to be coated, and a final dispersing means. A low-dispersion core particle powder portion other than the high-dispersion core particle powder particles / gas mixture mainly existing in the air in a single particle state from the particle / gas mixture of the core particle powder dispersed in A. It comprises a feedback means C for feeding back η to the dispersion means a, and a final particle / gas mixture selection means B for highly dispersed core particle powder, which releases the highly dispersed core particle powder particle / gas mixture. [epsilon] is a particle / gas mixture of highly dispersed core particle powder, which exists in the air mainly in a single particle state among particles of the core particle powder.

【0078】このようにして達成された準微粒子の高分
散状態を維持するために、気中分散維持手段を準微粒子
高分散処理手段群に付加することもできる。ここで気中
分散維持手段とは、気中に分散担持された芯粒子粉体の
粒子の再凝集を防止して分散度βを維持する手段をい
う。又、このようにして達成された芯粒子の高分散状態
を促進するために、気中分散促進手段を微粒子高分散処
理手段群と被覆室の間に付加することもできる。ここで
いう気中分散促進手段とは、気中に分散担持された芯粒
子粉体の粒子のうち主に再凝集した粒子の再分散を促進
し、分散状態の低下を鈍らせたり、一旦低下した分散状
態を元の高分散の状態まで回復するように再分散を促す
手段をいう。この気中分散維持手段又は気中分散促進手
段の好適な例としては、パイプ振動装置、パイプ加熱装
置、プラズマ発生装置、荷電装置等が挙げられる。
In order to maintain the highly dispersed state of the quasi-fine particles thus achieved, the air dispersion maintaining means may be added to the quasi-fine particle high dispersion treatment means group. Here, the air dispersion maintaining means refers to means for preventing reaggregation of particles of the core particle powder dispersed and carried in air to maintain the dispersity β. Further, in order to promote the highly dispersed state of the core particles thus achieved, an air dispersion promoting means can be added between the fine particle high dispersion treatment means group and the coating chamber. The air dispersion promoting means here promotes redispersion of mainly reaggregated particles among particles of the core particle powder dispersed and carried in the air, and slows down the deterioration of the dispersed state, or once decreases It means a means for promoting re-dispersion so as to recover the dispersed state to the original highly dispersed state. Suitable examples of the air dispersion maintaining means or the air dispersion promoting means include a pipe vibrating device, a pipe heating device, a plasma generating device, a charging device and the like.

【0079】パイプ振動装置は、発振器を設置したパイ
プの振動により、気中に分散している粒子に分散機とは
言えない振動を与えることで、再凝集を抑制し高分散状
態を維持する手段又は再凝集した粒子の分散を促進する
手段である。パイプ加熱装置は、加熱したパイプにより
搬送気体の外側から熱を加えて搬送気体を膨張させ、分
散機とは言えないほどに流速を加速して再凝集を抑制
し、再凝集した粒子の分散を促進する手段である。
The pipe vibrating device is a means for suppressing re-agglomeration and maintaining a high dispersion state by giving vibrations, which cannot be regarded as a disperser, to the particles dispersed in the air by the vibration of the pipe in which the oscillator is installed. Alternatively, it is a means for promoting the dispersion of reaggregated particles. The pipe heating device expands the carrier gas by applying heat from the outside of the carrier gas by the heated pipe, accelerates the flow velocity so that it can not be called a disperser, suppresses reaggregation, and disperses the reaggregated particles. It is a means to promote.

【0080】プラズマ発生装置は、芯粒子粉体を分散担
持している気中にプラズマを発生させ、そのプラズマイ
オンと芯粒子との衝突により、再凝集を抑制し高分散状
態を維持する手段又は再凝集した粒子の分散を促進する
手段である。荷電装置は、芯粒子粉体を分散担持してい
る気中に、コロナ放電、電子ビーム、放射線等の方法で
単極イオンを発生させ、単極イオン雰囲気中を通過させ
ることで粒子を単極に帯電させ、静電気の斥力により再
凝集を抑制し高分散状態を維持する手段又は再凝集した
粒子の分散を促進する手段である。
The plasma generator is a means for generating plasma in the air carrying the core particle powder in a dispersed state and suppressing re-aggregation by the collision of the plasma ions with the core particles to maintain a high dispersion state. It is a means of promoting the dispersion of reaggregated particles. The charging device uses a method such as corona discharge, electron beam, or radiation to generate unipolar ions in the air carrying the core particle powder, and the particles are unipolar by passing through the unipolar ion atmosphere. It is a means for suppressing re-aggregation by repulsive force of static electricity to maintain a high dispersion state or a means for promoting dispersion of re-aggregated particles.

【0081】このようにして形成された準微粒子の高分
散状態の芯粒子粉体は粒子の表面を被覆形成物質で被覆
するために被覆室に送られる。この被覆室には被覆開始
領域を含む被覆空間が設けられている。
The highly dispersed core particle powder of the quasi-fine particles thus formed is sent to the coating chamber for coating the surface of the particles with the coating forming substance. A coating space including a coating start area is provided in the coating chamber.

【0082】準微粒子高分散処理手段群と被覆室とは直
結することが望ましいが、搬送に不可避の中空部材及び
/又はパイプを使って接続しても良い。この場合にも、
被覆開始領域での分散度βを上記した範囲の値とするこ
とが不可欠である。準微粒子高分散処理手段群と被覆室
を別々に置いてその間を連結する場合は、芯粒子粉体を
その分散状態のまま被覆室へ導入してやれば良い。その
ためには、この間に芯粒子粉体の分散状態を維持するた
めの装置である気中分散維持手段及び/又は分散状態を
高めるための装置である気中分散促進手段及び/又は芯
粒子粉体の粒子・気体混合物から、低分散芯粒子粉体部
分を分離し、主に単一粒子状態の粒子を含む高分散芯粒
子粉体の粒子・気体混合物を選択する高分散芯粒子粉体
の粒子・気体混合物選択手段を設けることもできる。
Although it is desirable that the quasi-fine particle high dispersion treatment means group and the coating chamber are directly connected, they may be connected by using a hollow member and / or a pipe which is inevitable for transportation. Also in this case,
It is indispensable to set the dispersion degree β in the coating start region to a value within the above range. When the quasi-fine particle high dispersion treatment means group and the coating chamber are separately placed and connected to each other, the core particle powder may be introduced into the coating chamber in the dispersed state. For that purpose, the air dispersion maintaining means and / or the air dispersion promoting means and / or the core particle powder which is an apparatus for maintaining the dispersed state of the core particle powder during this period. High-dispersion core particle powder particles that separate the low-dispersion core particle powder part from the particle-gas mixture and select the high-dispersion core particle powder particle / gas mixture that mainly contains particles in a single particle state -Gas mixture selection means can also be provided.

【0083】準微粒子高分散処理手段群において気中分
散された直後の芯粒子粉体の中から、主に凝集した粒子
からなる低分散状態の粒子と主に一次粒子からなる高分
散状態の芯粒子粉体を選択分離し、高分散状態の部分の
みを被覆室に送り出す高分散芯粒子粉体の粒子・気体混
合物選択手段を介して、準微粒子高分散処理手段群を被
覆室へ接続すれば、効果的に被覆処理を行うことができ
る。又、本発明においては、準微粒子高分散処理手段群
が、(1)被覆室、又は(2)被覆空間、又は(3)被覆開始
領域と一部以上空間を共有することもできる。
From the core particle powder immediately after being dispersed in the air in the quasi-fine particle high dispersion treatment means group, particles in a low dispersion state mainly composed of agglomerated particles and cores in a high dispersion state mainly composed of primary particles By connecting the quasi-fine particle high dispersion treatment means group to the coating chamber through the particle / gas mixture selection means of the highly dispersed core particle powder which selectively separates the particle powder and sends only the highly dispersed state to the coating chamber The coating treatment can be effectively performed. Further, in the present invention, the quasi-fine particle high dispersion treatment means group may share a part or more of the space with (1) the coating chamber, (2) the coating space, or (3) the coating start region.

【0084】すなわち、準微粒子高分散処理手段群中の
分散空間と被覆室とを、または準微粒子高分散処理手段
群中の分散空間と被覆開始領域を有する被覆空間とを、
または準微粒子高分散処理手段群中の分散空間と被覆開
始領域とを、空間的に共有することもできる。ここで被
覆開始領域とは、(1)体積基準頻度分布で平均粒径が1
0μmを越え20μm以下の芯粒子粉体にあっては粒子
の分散度βが80%以上、(2)体積基準頻度分布で平均
粒径が20μmを越え50μm以下の芯粒子粉体にあっ
ては粒子の分散度βが90%以上、又は(3)体積基準頻
度分布で平均粒径が50μmを越え300μm以下の芯
粒子粉体にあっては粒子の分散度βが95%以上、
(4)体積基準頻度分布で平均粒径が300μmを越え
800μm以下の芯粒子粉体にあっては粒子の分散度β
が97%以上、(5)体積基準頻度分布で平均粒径が8
00μmを越える芯粒子粉体にあっては粒子の分散度β
が99%以上である分散状態で搬送された高分散状態の
芯粒子粉体に気相を経て生成する被覆形成物質前駆体及
び/又は気相状態の被覆形成物質前駆体が接触及び/又
は衝突し、被覆を開始する領域を指し、次の図4(a)〜
(e)で示される態様が考慮される。
That is, the dispersion space and the coating chamber in the quasi-fine particle high dispersion treatment means group, or the dispersion space and the coating space having the coating start region in the quasi-fine particle high dispersion treatment means group,
Alternatively, the dispersion space in the quasi-fine particle high dispersion treatment means group and the coating start region can be spatially shared. Here, the coating start region is (1) the volume standard frequency distribution and the average particle size is 1
For the core particle powder having a particle size of more than 0 μm and 20 μm or less, the particle dispersity β is 80% or more, The dispersity β of the particles is 90% or more, or (3) the core particle powder having an average particle size of more than 50 μm and 300 μm or less in the volume standard frequency distribution has a particle dispersity β of 95% or more,
(4) In the core particle powder having a volume-based frequency distribution and an average particle size of more than 300 μm and 800 μm or less, the degree of particle dispersion β
Is 97% or more, and (5) volume-based frequency distribution has an average particle size of 8
In the case of core particle powder exceeding 00 μm, the degree of particle dispersion β
And / or collision of a coating-forming substance precursor produced in the vapor phase and / or a coating-forming substance precursor in the vapor phase with a highly dispersed core particle powder conveyed in a dispersed state of 99% or more. The area where the coating is to be started, as shown in FIG.
The embodiment shown in (e) is considered.

【0085】すなわち、図4(a)〜(e)において被覆開
始領域は2で示される領域である。図4(a)において、
芯粒子の平均粒子径に応じて上記した分散度βの分散状
態で被覆を始める被覆空間の被覆開始領域2を準微粒子
高分散処理手段群又は準微粒子高分散処理手段群の一
部、好適には準微粒子高分散処理手段群の放出部1を覆
って設ける。図4(b)において準微粒子高分散処理手段
群又は準微粒子高分散処理手段群の一部、好適には準微
粒子高分散処理手段群の放出部1から放出される芯粒子
粉体の粒子4が全て通る前記被覆空間の被覆開始領域2
を設ける。上記の構成により、全ての芯粒子粉体の粒子
は上記した分散度βの分散状態で被覆始められる。図4
(c)において準微粒子高分散処理手段群又は準微粒子高
分散処理手段群の一部で好適には準微粒子高分散処理手
段群の放出部1から放出される芯粒子粉体の粒子4の
内、回収部5に入る粒子は必ず通過する前記被覆空間の
被覆開始領域2を設ける。図4(d)において回収部5を
囲む前記被覆空間の被覆開始領域2を設ける。図4(e)
において高分散芯粒子粉体の粒子・気体混合物の粒子の
みが到達可能な位置に回収部5を設ける。従って、ここ
での領域6は重力を利用した選択手段となる。回収部に
入る高分散芯粒子粉体の粒子・気体混合物の粒子が、必
ず通過する前記被覆空間の被覆開始領域2を図の斜線部
のように設ける。このようにすることで上記した分散度
βの分散状態で被覆始めた芯粒子のみ回収でき、被覆開
始領域を通っていない芯粒子と被覆開始領域を通過した
被覆準微粒子とは混ざることはない。
That is, the coating start region is the region indicated by 2 in FIGS. In FIG. 4 (a),
According to the average particle diameter of the core particles, the coating start region 2 of the coating space in which the coating is started in the dispersed state of the dispersity β described above is a semi-fine particle high dispersion treatment means group or a part of the semi-fine particle high dispersion treatment means group, preferably Is provided so as to cover the emission part 1 of the quasi-fine particle high dispersion treatment means group. In FIG. 4 (b), particles 4 of the core particle powder discharged from the quasi-particulate high-dispersion processing means group or a part of the quasi-particulate high-dispersion processing means group, preferably from the discharge part 1 of the quasi-fine particle high-dispersion processing means group. Coating start region 2 of the coating space where all pass
To provide. With the above configuration, all the particles of the core particle powder are started to be coated in the dispersed state of the degree of dispersion β described above. Figure 4
In (c), the quasi-particulate high-dispersion processing means group or a part of the quasi-fine-particle high-dispersion processing means group is preferably among the particles 4 of the core particle powder discharged from the discharge part 1 of the quasi-fine particle high-dispersion processing means group. A coating start region 2 of the coating space is provided through which particles that enter the recovery unit 5 always pass. In FIG. 4D, a coating start region 2 of the coating space that surrounds the recovery unit 5 is provided. Figure 4 (e)
In the above, the recovery unit 5 is provided at a position where only the particles of the highly dispersed core particle powder and the particles of the gas mixture can reach. Therefore, the area 6 here is a selecting means utilizing gravity. The coating start region 2 of the coating space through which the particles of the highly dispersed core particle powder / particles of the gas mixture that enter the recovery section must pass is provided as shown by the hatched portion in the figure. By doing so, only the core particles that have begun to be coated in the dispersed state of the above-described dispersity β can be recovered, and the core particles that have not passed through the coating start region and the coated quasi-fine particles that have passed through the coating start region do not mix.

【0086】上記したところから、本発明を実施する装
置は、準微粒子高分散処理手段群と被覆室又は準微粒子
高分散処理手段群と被覆室と回収手段から構成されるも
のであるが、これらの装置の構成要素は、種々の組み合
わせ方をすることが可能で、これらの装置の構成例を図
面にもとづいて説明するとつぎのとおりである。
From the above, the apparatus for carrying out the present invention comprises the quasi-fine particle high dispersion treatment means group and the coating chamber or the quasi-fine particle high dispersion treatment means group, the coating chamber and the recovery means. The constituent elements of the device can be combined in various ways, and the configuration examples of these devices will be described below with reference to the drawings.

【0087】装置の構成1 図5(a)は、本発明を実施する第一の装置の構成を説明
するブロック図である。本例のこの装置は、被覆装置の
製造装置本体2−A、被覆室2−B1、被覆空間2−B
2、被覆開始領域2−B3、準微粒子高分散処理手段群
2−C1、回収手段2−Dから構成されている。準微粒
子高分散処理手段群2−C1は、被覆室2−B1に直結
してある。
Device Configuration 1 FIG. 5 (a) is a block diagram illustrating the configuration of a first device for carrying out the present invention. This apparatus of this example includes a manufacturing apparatus main body 2-A of a coating apparatus, a coating chamber 2-B1, a coating space 2-B.
2, coating start region 2-B3, quasi-fine particle high dispersion treatment means group 2-C1, and recovery means 2-D. The quasi-fine particle high dispersion treatment means group 2-C1 is directly connected to the coating chamber 2-B1.

【0088】装置の構成2 図5(b)は、本発明を実施する第二の装置の構成を説明
するブロック図である。本例のこの装置は、被覆装置の
製造装置本体2−A、被覆室2−B1、被覆空間2−B
2、被覆開始領域2−B3、準微粒子高分散処理手段群
2−C1、不可避の中空部材2−C2、回収手段2−D
から構成されている。準微粒子高分散処理手段群2−C
1は、被覆室2−B1に不可避の中空部材2−C2を介
して接続してある。
Device Configuration 2 FIG. 5 (b) is a block diagram for explaining the configuration of the second device for carrying out the present invention. This apparatus of this example includes a manufacturing apparatus main body 2-A of a coating apparatus, a coating chamber 2-B1, a coating space 2-B.
2, coating start region 2-B3, semi-fine particle high dispersion treatment means group 2-C1, unavoidable hollow member 2-C2, recovery means 2-D
It consists of Semi-fine particle high dispersion treatment means group 2-C
1 is connected to the coating chamber 2-B1 via an unavoidable hollow member 2-C2.

【0089】装置の構成3 図5(c)は、本発明を実施する第三の装置の構成を説明
するブロック図である。本例のこの装置は、被覆装置の
製造装置本体2−A、被覆室2−B1、被覆空間2−B
2、被覆開始領域2−B3、準微粒子高分散処理手段群
2−C1、気中分散維持手段2−C3、回収手段2−D
から構成されている。準微粒子高分散処理手段群2−C
1は、被覆室2−B1に気中分散維持手段2−C3を介
して接続してある。
Device Configuration 3 FIG. 5 (c) is a block diagram for explaining the configuration of the third device for carrying out the present invention. This apparatus of this example includes a manufacturing apparatus main body 2-A of a coating apparatus, a coating chamber 2-B1, a coating space 2-B.
2, coating start region 2-B3, semi-fine particle high dispersion treatment means group 2-C1, aerial dispersion maintenance means 2-C3, recovery means 2-D
It consists of Semi-fine particle high dispersion treatment means group 2-C
1 is connected to the coating chamber 2-B1 via the air dispersion maintaining means 2-C3.

【0090】装置の構成4 図5(d)は、本発明を実施する第四の装置の構成を説明
するブロック図である。本例のこの装置は、被覆装置の
製造装置本体2−A、被覆室2−B1、被覆空間2−B
2、被覆開始領域2−B3、準微粒子高分散処理手段群
2−C1、回収手段2−Dから構成されている。準微粒
子高分散処理手段群2−C1は、被覆室2−B1と空間
を共有している。
Device Configuration 4 FIG. 5D is a block diagram illustrating the configuration of a fourth device for carrying out the present invention. This apparatus of this example includes a manufacturing apparatus main body 2-A of a coating apparatus, a coating chamber 2-B1, a coating space 2-B.
2, coating start region 2-B3, quasi-fine particle high dispersion treatment means group 2-C1, and recovery means 2-D. The quasi-fine particle high dispersion treatment means group 2-C1 shares a space with the coating chamber 2-B1.

【0091】装置の構成5 図5(e)は、本発明を実施する第五の装置の構成を説明
するブロック図である。本例のこの装置は、被覆装置の
製造装置本体2−A、被覆室2−B1、被覆空間2−B
2、被覆開始領域2−B3、準微粒子高分散処理手段群
2−C1、回収手段2−Dから構成されている。準微粒
子高分散処理手段群2−C1は、被覆室2−B1中に設
けている。
Device Configuration 5 FIG. 5 (e) is a block diagram illustrating the configuration of a fifth device for carrying out the present invention. This apparatus of this example includes a manufacturing apparatus main body 2-A of a coating apparatus, a coating chamber 2-B1, a coating space 2-B.
2, coating start region 2-B3, quasi-fine particle high dispersion treatment means group 2-C1, and recovery means 2-D. The quasi-fine particle high dispersion treatment means group 2-C1 is provided in the coating chamber 2-B1.

【0092】装置の構成6 図5(f)は、本発明を実施する第六の装置の構成を説明
するブロック図である。本例のこの装置は、被覆装置の
製造装置本体2−A、被覆室2−B1、被覆空間2−B
2、被覆開始領域2−B3、準微粒子高分散処理手段群
2−C1、回収手段2−Dから構成されている。準微粒
子高分散処理手段群2−C1の分散空間中に、被覆室2
−B1を設けている。
Device Configuration 6 FIG. 5 (f) is a block diagram illustrating the configuration of a sixth device for carrying out the present invention. This apparatus of this example includes a manufacturing apparatus main body 2-A of a coating apparatus, a coating chamber 2-B1, a coating space 2-B.
2, coating start region 2-B3, quasi-fine particle high dispersion treatment means group 2-C1, and recovery means 2-D. In the dispersion space of the quasi-fine particle high dispersion treatment means group 2-C1, the coating chamber 2
-B1 is provided.

【0093】装置の構成7 図5(g)は、本発明を実施する第七の装置の構成を説明
するブロック図である。本例のこの装置は、被覆装置の
製造装置本体2−A、被覆室2−B1、被覆空間2−B
2、被覆開始領域2−B3、準微粒子高分散処理手段群
2−C1、回収手段2−D、再被覆供給手段2−Eから
構成されている。回収手段2−Dから被覆後の被覆準微
粒子を高分散処理手段群2−C1に再被覆供給手段2−
Eにより搬送して、繰り返して被覆処理が行える。かか
る構成の装置のすべてが本発明に含まれるものである。
Device Configuration 7 FIG. 5 (g) is a block diagram illustrating the configuration of a seventh device for carrying out the present invention. This apparatus of this example includes a manufacturing apparatus main body 2-A of a coating apparatus, a coating chamber 2-B1, a coating space 2-B.
2, coating start region 2-B3, quasi-fine particle high dispersion treatment means group 2-C1, recovery means 2-D, re-coating supply means 2-E. The coated quasi-fine particles after coating from the collecting means 2-D are re-coated and supplied to the high dispersion treatment means group 2-C1.
It can be conveyed by E and can be repeatedly coated. All the devices having such a configuration are included in the present invention.

【0094】上記のようにして芯粒子粉体を被覆形成物
質で被覆した被覆準微粒子について、再び被覆形成物質
で被覆すること、またはこの再被覆を反復することがで
きる。この場合、被覆準微粒子は再被覆供給手段に送ら
れる。ここで、再被覆供給手段とは、再被覆を行うため
に被覆後の被覆準微粒子を準微粒子高分散処理手段群へ
搬送する手段をいう。具体的には、(a)被覆準微粒子を
回収する回収手段、及び(b)回収手段から準微粒子高分
散処理手段群に被覆準微粒子を搬送する被覆粒子搬送手
段を備えた手段である。または、(a)被覆準微粒子を回
収する回収手段、(b)回収手段から準微粒子高分散処理
手段群に被覆準微粒子を搬送する被覆粒子搬送手段、
(c)及び被覆後の被覆準微粒子を分級する被覆粒子分級
手段を備えた手段である。被覆量が多い場合、被覆前の
芯粒子粉体の粒子の粒度分布と被覆後の被覆準微粒子の
粒度分布は変わってしまう。そこで、被覆後の被覆準微
粒子の粒度分布を被覆粒子分級手段により調整し、再被
覆処理を行えば効果的である。
The coated quasi-fine particles obtained by coating the core particle powder with the coating forming substance as described above can be coated with the coating forming substance again, or this recoating can be repeated. In this case, the coated quasi-fine particles are sent to the recoating supply means. Here, the re-coating supply means means for conveying the coated quasi-fine particles after coating to the quasi-fine particle high dispersion treatment means group for performing re-coating. Specifically, it is a means provided with (a) a collecting means for collecting the coated quasi-fine particles, and (b) a coated particle conveying means for conveying the coated quasi-fine particles from the collecting means to the quasi-fine particle high dispersion treatment means group. Alternatively, (a) a collecting means for collecting the coated quasi-fine particles, (b) a coated particle conveying means for conveying the coated quasi-fine particles from the collecting means to the quasi-fine particle high dispersion treatment means group,
(c) and means for classifying the coated quasi-fine particles after coating to classify the coated particles. When the coating amount is large, the particle size distribution of the core particle powder before coating and the particle size distribution of the coated quasi-fine particles after coating change. Therefore, it is effective to adjust the particle size distribution of the coated quasi-fine particles after coating by the coated particle classification means and perform the recoating treatment.

【0095】この再被覆処理は、必要によって繰り返す
ことが出来、そして被覆形成物質の被覆量を所望のもの
に設定することが出来る。更に、この被覆形成物質の種
類を変えてこの被覆処理を繰り返すことが出来、このよ
うにして複数成分の物質を被覆形成物質として多重被覆
することも出来る。
This recoating process can be repeated if necessary, and the coating amount of the coating forming substance can be set to a desired value. Further, this coating treatment can be repeated by changing the type of the coating forming substance, and in this way, it is also possible to multiply coat a substance of a plurality of components as a coating forming substance.

【0096】本発明に適用する被覆準微粒子の製造装置
は、被覆形成物質が、気相を経る気相法によって、芯粒
子粉体の粒子表面に被覆される被覆準微粒子の製造装置
であれば制限はない。例えば、化学蒸着(CVD)装置
としては、熱CVD装置、プラズマCVD装置、電磁波
を利用したCVD(可視光線CVD、レーザCVD、紫
外線CVD、赤外線CVD、遠赤外線CVD)装置、M
OCVD装置等、或いは、物理蒸着(PVD)装置とし
ては、真空蒸着装置、イオンスパッタリング装置、イオ
ンプレーティング装置等が適用可能である。より具体的
には、例えば、特開平3−75302号公報の超微粒子
で表面が被覆された粒子およびその製造方法に記載の被
覆粒子製造装置が好適である。
The apparatus for producing coated quasi-fine particles applied to the present invention is an apparatus for producing coated quasi-fine particles in which the coating-forming substance is coated on the particle surface of the core particle powder by a vapor phase method in which a gas phase is passed. There is no limit. For example, as a chemical vapor deposition (CVD) apparatus, a thermal CVD apparatus, a plasma CVD apparatus, a CVD (visible light CVD, laser CVD, ultraviolet CVD, infrared CVD, far infrared CVD) apparatus using electromagnetic waves, M
As the OCVD device or the like or the physical vapor deposition (PVD) device, a vacuum vapor deposition device, an ion sputtering device, an ion plating device, or the like can be applied. More specifically, for example, a particle whose surface is coated with ultrafine particles disclosed in JP-A-3-75302 and a coated particle manufacturing apparatus described in the manufacturing method thereof are suitable.

【0097】以上述べた通り、本発明では準微粒子芯粒
子粉体、又は主に準微粒子からなる芯粒子粉体の粒子を
被覆空間に投入し気相を経て生成する被覆形成物質前駆
体及び/又は気相状態の被覆形成物質前駆体をこの芯粒
子粉体の粒子に接触及び/又は衝突させてこの芯粒子粉
体の粒子の表面を被覆形成物質で被覆する被覆準微粒子
が製造されるが、本発明の基本的な工程を要約すると次
の通りである。
As described above, in the present invention, the particles of the quasi-fine particle core particle powder or the particles of the core particle powder mainly composed of quasi-fine particles are charged into the coating space and the precursor of the coating forming substance and // Alternatively, coated quasi-fine particles can be produced in which a coating-form substance precursor in a gas phase is brought into contact with and / or collides with the particles of the core-particle powder to coat the surface of the particles of the core-particle powder with the coating-form substance. The basic steps of the present invention are summarized as follows.

【0098】I (A) 準微粒子高分散処理手段群により、体積基準頻
度分布で平均粒子径が10μmを越える準微粒子芯粒子
粉体の粒子又は主に準微粒子からなる芯粒子粉体の粒子
を、気中に分散させて高分散芯粒子粉体の粒子・気体混
合物とする分散工程、(B) この分散工程で分散させ
た高分散芯粒子粉体の粒子・気体混合物の芯粒子粉体の
粒子を、その平均粒子径が10μmを越え20μm以下
のときには分散度βが80%以上、20μmを越え50
μm以下のときには分散度βが90%以上、50μmを
越え300μm以下のときには分散度βが95%以上、
300μmを越え800μm以下のときには分散度βが
97%以上、800μmを越えるときには分散度βが9
9%以上、の分散状態で、被覆空間の被覆開始領域にお
いて被覆形成物質前駆体と接触及び/又は衝突させて被
覆を開始する被覆工程、を設けた被覆法。
I (A) The particles of the quasi-fine particle core particle powder having an average particle diameter of more than 10 μm in the volume-based frequency distribution or the particles of the core particle powder mainly composed of quasi-fine particles are processed by the group of means for highly dispersing quasi-fine particles. A dispersion step of dispersing in air to form a particle / gas mixture of highly dispersed core particle powder, (B) a particle / gas mixture of highly dispersed core particle powder dispersed in this dispersing step, When the average particle size of the particles is more than 10 μm and less than 20 μm, the dispersity β is 80% or more, and more than 20 μm and 50
When it is less than μm, the dispersity β is 90% or more, and when it is more than 50 μm and less than 300 μm, the dispersity β is 95% or more,
When it exceeds 300 μm and 800 μm or less, the dispersion degree β is 97% or more, and when it exceeds 800 μm, the dispersion degree β is 9%.
A coating method comprising a coating step of contacting and / or colliding with a coating forming material precursor in a coating starting region of a coating space in a dispersed state of 9% or more to start coating.

【0099】II (A) 体積基準頻度分布で平均粒子径が10μmを越
え20μm以下の準微粒子芯粒子粉体の粒子又は主に準
微粒子からなる芯粒子粉体の粒子を、準微粒子高分散処
理手段群により分散させた高分散芯粒子粉体の粒子・気
体混合物の芯粒子粉体の粒子の分散度βが80%以上を
実現する準微粒子高分散処理手段群、体積基準頻度分布
で平均粒子径が20μmを越え50μm以下の準微粒子
芯粒子粉体の粒子又は主に準微粒子からなる芯粒子粉体
の粒子を、準微粒子高分散処理手段群により分散させた
高分散芯粒子粉体の粒子・気体混合物の芯粒子粉体の粒
子の分散度βが90%以上を実現する準微粒子高分散処
理手段群、体積基準頻度分布で平均粒子径が50μmを
越え300μm以下の準微粒子芯粒子粉体の粒子又は主
に準微粒子からなる芯粒子粉体の粒子を、準微粒子高分
散処理手段群により分散させた高分散芯粒子粉体の粒子
・気体混合物の芯粒子粉体の粒子の分散度βが95%以
上を実現する準微粒子高分散処理手段群、体積基準頻度
分布で平均粒子径が300μmを越え800μm以下の
準微粒子芯粒子粉体の粒子又は主に準微粒子からなる芯
粒子粉体の粒子を、準微粒子高分散処理手段群により分
散させた高分散芯粒子粉体の粒子・気体混合物の芯粒子
粉体の粒子の分散度βが97%以上を実現する準微粒子
高分散処理手段群、体積基準頻度分布で平均粒子径が8
00μmを越える準微粒子芯粒子粉体の粒子又は主に準
微粒子からなる芯粒子粉体の粒子を、準微粒子高分散処
理手段群により分散させた高分散芯粒子粉体の粒子・気
体混合物の芯粒子粉体の粒子の分散度βが99%以上を
実現する準微粒子高分散処理手段群、により気中に分散
させて高分散芯粒子粉体の粒子・気体混合物とする分散
工程、(B) この分散工程で分散させた高分散芯粒子
粉体の粒子・気体混合物の芯粒子粉体の粒子を、その平
均粒子径が10μmを越え20μm以下のときには分散
度βが80%以上、20μmを越え50μm以下のとき
には分散度βが90%以上、50μmを越え300μm
以下のときには分散度βが95%以上、300μmを越
え800μm以下のときには分散度βが97%以上、8
00μmを越えるときには分散度βが99%以上、の分
散状態で、被覆空間の被覆開始領域において被覆形成物
質前駆体と接触及び/又は衝突させて被覆を開始する被
覆工程、を設けた被覆法。
II (A) Particles of quasi-fine particle core particle powder having an average particle diameter of more than 10 μm and 20 μm or less in volume-based frequency distribution or particles of core particle powder mainly composed of quasi-fine particles are subjected to a quasi-fine particle high dispersion treatment. High-dispersion core particles dispersed by means of means, core particles of a gas mixture, core particles of quasi-fine particle high-dispersion treatment means realizing a degree of dispersion β of particles of powder of 80% or more, average particles by volume-based frequency distribution Particles of highly dispersed core particle powder in which particles of quasi-fine particle core particle powder having a diameter of more than 20 μm and not more than 50 μm or particles of core particle powder mainly composed of quasi-fine particles are dispersed by a quasi-fine particle high dispersion treatment means group. -A group of quasi-fine particle high-dispersion treatment means that achieves a particle dispersity β of 90% or more in a core particle powder of a gas mixture, and a quasi-fine particle core particle powder having an average particle size of more than 50 μm and 300 μm or less in a volume-based frequency distribution Particles or mainly quasi-fine particles Particles of highly dispersed core particles obtained by dispersing the particles of the core particle powder made of (1) by means of the quasi-fine particle high dispersion treatment means group achieve a dispersity β of the particles of the core particle powder of the gas mixture of 95% or more. Quasi-fine particle high dispersion treatment means group, quasi-fine particle core particle powder particles having an average particle diameter of more than 300 μm and 800 μm or less in the volume standard frequency distribution or core particle powder mainly composed of quasi-fine particles Particles of highly dispersed core particles dispersed by the processing means group, quasi-particulate high dispersion processing means group that realizes a dispersity β of the particles of the core particle powder of the gas / gas mixture of 97% or more, averaged by volume-based frequency distribution Particle size is 8
Particles of highly dispersed core particle powder obtained by dispersing particles of quasi-fine particle core particle powder having a diameter of more than 00 μm or particles of core particle powder mainly composed of quasi-fine particles by a group of quasi-fine particle high dispersion treatment means Dispersing step of dispersing in air into a particle / gas mixture of high-dispersion core particle powder by means of a group of quasi-fine particle high-dispersion processing means that realizes a particle dispersity β of 99% or more in the particle powder, (B) When the average particle size of the particles of the highly dispersed core particle powder / the particles of the gas mixture core particle powder dispersed in this dispersion step is more than 10 μm and less than 20 μm, the dispersity β is 80% or more and more than 20 μm. When it is less than 50 μm, the dispersity β is 90% or more, more than 50 μm and 300 μm
When the dispersity β is 95% or more when it is below, and when the dispersity β is more than 300 μm and 800 μm or less, the dispersity β is 97% or more, 8
A coating method comprising a coating step of starting coating by contacting and / or colliding with the coating material precursor in the coating start region of the coating space in a dispersed state with a dispersity β of 99% or more when it exceeds 00 μm.

【0100】III (A) 体積基準頻度分布で平均粒子径が10μmを越
え20μm以下の準微粒子芯粒子粉体の粒子又は主に準
微粒子からなる芯粒子粉体の粒子を、準微粒子高分散処
理手段群により分散させた高分散芯粒子粉体の粒子・気
体混合物の芯粒子粉体の粒子の分散度βが80%以上を
実現する準微粒子高分散処理手段群、体積基準頻度分布
で平均粒子径が20μmを越え50μm以下の準微粒子
芯粒子粉体の粒子又は主に準微粒子からなる芯粒子粉体
の粒子を、準微粒子高分散処理手段群により分散させた
高分散芯粒子粉体の粒子・気体混合物の芯粒子粉体の粒
子の分散度βが90%以上を実現する準微粒子高分散処
理手段群、体積基準頻度分布で平均粒子径が50μmを
越え300μm以下の準微粒子芯粒子粉体の粒子又は主
に準微粒子からなる芯粒子粉体の粒子を、準微粒子高分
散処理手段群により分散させた高分散芯粒子粉体の粒子
・気体混合物の芯粒子粉体の粒子の分散度βが95%以
上を実現する準微粒子高分散処理手段群、体積基準頻度
分布で平均粒子径が300μmを越え800μm以下の
準微粒子芯粒子粉体の粒子又は主に準微粒子からなる芯
粒子粉体の粒子を、準微粒子高分散処理手段群により分
散させた高分散芯粒子粉体の粒子・気体混合物の芯粒子
粉体の粒子の分散度βが97%以上を実現する準微粒子
高分散処理手段群、体積基準頻度分布で平均粒子径が8
00μmを越える準微粒子芯粒子粉体の粒子又は主に準
微粒子からなる芯粒子粉体の粒子を、準微粒子高分散処
理手段群により分散させた高分散芯粒子粉体の粒子・気
体混合物の芯粒子粉体の粒子の分散度βが99%以上を
実現する準微粒子高分散処理手段群、により気中に分散
させて高分散芯粒子粉体の粒子・気体混合物とする分散
工程、(B) この分散工程で分散させた高分散芯粒子
粉体の粒子・気体混合物の芯粒子粉体の粒子を、被覆工
程に直接搬送する搬送工程、(C) この搬送工程で搬
送した高分散芯粒子粉体の粒子・気体混合物の芯粒子粉
体の粒子を、その平均粒子径が10μmを越え20μm
以下のときには分散度βが80%以上、20μmを越え
50μm以下のときには分散度βが90%以上、50μ
mを越え300μm以下のときには分散度βが95%以
上、300μmを越え800μm以下のときには分散度
βが97%以上、800μmを越えるときには分散度β
が99%以上、の分散状態で、被覆空間の被覆開始領域
において被覆形成物質前駆体と接触及び/又は衝突させ
て被覆を開始する被覆工程、を設けた被覆法。
III (A) Quasi-fine particle high-dispersion treatment of particles of quasi-fine particle core particle powder having an average particle size of more than 10 μm and 20 μm or less in volume-based frequency distribution or core particle powder mainly composed of quasi-fine particles High-dispersion core particles dispersed by means of means / particles Core particles of gas mixture Core particles of quasi-particulate high-dispersion treatment means realizing a degree of dispersion β of 80% or more, average particles by volume-based frequency distribution Particles of highly dispersed core particle powder in which particles of quasi-fine particle core particle powder having a diameter of more than 20 μm and 50 μm or less or particles of core particle powder mainly composed of quasi-fine particles are dispersed by a group of quasi-fine particle high dispersion treatment means. -A group of quasi-fine particle high-dispersion treatment means that achieves a particle dispersity β of 90% or more in a core particle powder of a gas mixture, and a quasi-fine particle core particle powder having an average particle size of more than 50 μm and 300 μm or less in a volume-based frequency distribution Particles or mainly quasi-fine particles Particles of highly dispersed core particles obtained by dispersing the particles of the core particle powder made of (1) by the quasi-fine particle high dispersion treatment means group achieves a dispersity β of the particles of the core particle powder of the gas / gas mixture of 95% or more. Quasi-fine particle high dispersion treatment means group, quasi-fine particle core particle powder particles having an average particle size of more than 300 μm and 800 μm or less in the volume standard frequency distribution, or core particle powder mainly consisting of quasi-fine particles Particles of highly dispersed core particles dispersed by the processing means group, particles of the gas / core mixture of the gas mixture, the degree of dispersion β of the particles of the powder of the quasi-particulate high dispersion processing means group achieving 97% or more, averaged by volume-based frequency distribution Particle size is 8
Particles of a highly dispersed core particle powder obtained by dispersing particles of a quasi-fine particle core particle powder having a diameter of more than 00 μm or particles of a core particle powder mainly composed of quasi-fine particles by a group of quasi-fine particle high dispersion treatment means (B) a dispersion step of dispersing in air into a particle / gas mixture of highly dispersed core particle powder by means of a quasi-fine particle high dispersion treatment means group that realizes a particle dispersibility β of the particle powder of 99% or more; A conveying step of directly conveying the particles of the highly dispersed core particle powder / the core particle powder of the gas mixture dispersed in this dispersion step to the coating step, (C) the highly dispersed core particle powder conveyed in this conveying step Core particles of body particles / gas mixture Powder particles with an average particle size of more than 10 μm and 20 μm
When the dispersity β is 80% or more, when it is more than 20 μm and not more than 50 μm, the dispersity β is 90% or more, 50 μ or less.
When the value exceeds m and is 300 μm or less, the dispersity β is 95% or more, and when the value exceeds 300 μm and 800 μm or less, the dispersity β is 97% or more, and the dispersity β is more than 800 μm.
Of 99% or more in a dispersed state, a coating step of starting coating by contacting and / or colliding with the coating material precursor in the coating start region of the coating space.

【0101】IV (A) 体積基準頻度分布で平均粒子径が10μmを越
え20μm以下の準微粒子芯粒子粉体の粒子又は主に準
微粒子からなる芯粒子粉体の粒子を、準微粒子高分散処
理手段群により分散させた高分散芯粒子粉体の粒子・気
体混合物の芯粒子粉体の粒子の分散度βが80%以上を
実現する準微粒子高分散処理手段群、体積基準頻度分布
で平均粒子径が20μmを越え50μm以下の準微粒子
芯粒子粉体の粒子又は主に準微粒子からなる芯粒子粉体
の粒子を、準微粒子高分散処理手段群により分散させた
高分散芯粒子粉体の粒子・気体混合物の芯粒子粉体の粒
子の分散度βが90%以上を実現する準微粒子高分散処
理手段群、体積基準頻度分布で平均粒子径が50μmを
越え300μm以下の準微粒子芯粒子粉体の粒子又は主
に準微粒子からなる芯粒子粉体の粒子を、準微粒子高分
散処理手段群により分散させた高分散芯粒子粉体の粒子
・気体混合物の芯粒子粉体の粒子の分散度βが95%以
上を実現する準微粒子高分散処理手段群、体積基準頻度
分布で平均粒子径が300μmを越え800μm以下の
準微粒子芯粒子粉体の粒子又は主に準微粒子からなる芯
粒子粉体の粒子を、準微粒子高分散処理手段群により分
散させた高分散芯粒子粉体の粒子・気体混合物の芯粒子
粉体の粒子の分散度βが97%以上を実現する準微粒子
高分散処理手段群、体積基準頻度分布で平均粒子径が8
00μmを越える準微粒子芯粒子粉体の粒子又は主に準
微粒子からなる芯粒子粉体の粒子を、準微粒子高分散処
理手段群により分散させた高分散芯粒子粉体の粒子・気
体混合物の芯粒子粉体の粒子の分散度βが99%以上を
実現する準微粒子高分散処理手段群、により気中に分散
させて高分散芯粒子粉体の粒子・気体混合物とする分散
工程、(B) この分散工程で分散させた高分散芯粒子
粉体の粒子・気体混合物の芯粒子粉体の粒子を、搬送に
不可避の、中空部材、中空を形成する部材からなる中間
部材、及びパイプから選択される1種類又はそれ以上の
部材を介して搬送する搬送工程、(C) この搬送工程
で搬送した高分散芯粒子粉体の粒子・気体混合物の芯粒
子粉体の粒子を、その平均粒子径が10μmを越え20
μm以下のときには分散度βが80%以上、20μmを
越え50μm以下のときには分散度βが90%以上、5
0μmを越え300μm以下のときには分散度βが95
%以上、300μmを越え800μm以下のときには分
散度βが97%以上、800μmを越えるときには分散
度βが99%以上、の分散状態で、被覆空間の被覆開始
領域において被覆形成物質前駆体と接触及び/又は衝突
させて被覆を開始する被覆工程、を設けた被覆法。
IV (A) Particles of quasi-fine particle core particle powder having an average particle size of more than 10 μm and 20 μm or less in a volume-based frequency distribution or particles of core particle powder mainly composed of quasi-fine particles are subjected to quasi-fine particle high dispersion treatment. High-dispersion core particles dispersed by means of means, core particles of a gas mixture, core particles of quasi-fine particle high-dispersion treatment means realizing a degree of dispersion β of particles of powder of 80% or more, average particles by volume-based frequency distribution Particles of highly dispersed core particle powder in which particles of quasi-fine particle core particle powder having a diameter of more than 20 μm and not more than 50 μm or particles of core particle powder mainly composed of quasi-fine particles are dispersed by a quasi-fine particle high dispersion treatment means group. -A group of quasi-fine particle high-dispersion treatment means that achieves a particle dispersity β of 90% or more in a core particle powder of a gas mixture, and a quasi-fine particle core particle powder having an average particle size of more than 50 μm and 300 μm or less in a volume-based frequency distribution Particles or mainly quasi-fine particles Particles of highly dispersed core particles obtained by dispersing the particles of the core particle powder made of (1) by means of the quasi-fine particle high dispersion treatment means group achieve a dispersity β of the particles of the core particle powder of the gas mixture of 95% or more. Quasi-fine particle high dispersion treatment means group, quasi-fine particle core particle powder particles having an average particle diameter of more than 300 μm and 800 μm or less in the volume standard frequency distribution or core particle powder mainly composed of quasi-fine particles Particles of highly dispersed core particles dispersed by the processing means group, quasi-particulate high dispersion processing means group that realizes a dispersity β of the particles of the core particle powder of the gas / gas mixture of 97% or more, averaged by volume-based frequency distribution Particle size is 8
Particles of a highly dispersed core particle powder obtained by dispersing particles of a quasi-fine particle core particle powder having a diameter of more than 00 μm or particles of a core particle powder mainly composed of quasi-fine particles by a group of quasi-fine particle high dispersion treatment means Dispersing step of dispersing in air into a particle / gas mixture of high-dispersion core particle powder by means of a group of quasi-fine particle high-dispersion processing means that realizes a particle dispersity β of 99% or more in the particle powder, (B) The particles of the high-dispersion core particle powder and the particles of the core particle powder of the gas mixture dispersed in this dispersion step are selected from a hollow member unavoidable for transportation, an intermediate member including a member forming a hollow, and a pipe. A carrying step of carrying through one or more kinds of members, (C) the particles of the highly dispersed core particle powder and the particles of the core particle powder of the gas mixture carried in this carrying step have an average particle diameter of 20 over 10 μm
When it is less than μm, the dispersity β is 80% or more, and when it is more than 20 μm and less than 50 μm, the dispersity β is 90% or more, 5
When it is more than 0 μm and less than 300 μm, the dispersion degree β is 95
% And more than 300 μm and less than 800 μm, the dispersity β is 97% or more, and when more than 800 μm, the dispersity β is 99% or more in contact with the precursor of the coating forming material in the coating start region of the coating space. And / or a coating step of causing collision to start coating.

【0102】V (A) 体積基準頻度分布で平均粒子径が10μmを越
え20μm以下の準微粒子芯粒子粉体の粒子又は主に準
微粒子からなる芯粒子粉体の粒子を、準微粒子高分散処
理手段群により分散させた高分散芯粒子粉体の粒子・気
体混合物の芯粒子粉体の粒子の分散度βが80%以上を
実現する準微粒子高分散処理手段群、体積基準頻度分布
で平均粒子径が20μmを越え50μm以下の準微粒子
芯粒子粉体の粒子又は主に準微粒子からなる芯粒子粉体
の粒子を、準微粒子高分散処理手段群により分散させた
高分散芯粒子粉体の粒子・気体混合物の芯粒子粉体の粒
子の分散度βが90%以上を実現する準微粒子高分散処
理手段群、体積基準頻度分布で平均粒子径が50μmを
越え300μm以下の準微粒子芯粒子粉体の粒子又は主
に準微粒子からなる芯粒子粉体の粒子を、準微粒子高分
散処理手段群により分散させた高分散芯粒子粉体の粒子
・気体混合物の芯粒子粉体の粒子の分散度βが95%以
上を実現する準微粒子高分散処理手段群、体積基準頻度
分布で平均粒子径が300μmを越え800μm以下の
準微粒子芯粒子粉体の粒子又は主に準微粒子からなる芯
粒子粉体の粒子を、準微粒子高分散処理手段群により分
散させた高分散芯粒子粉体の粒子・気体混合物の芯粒子
粉体の粒子の分散度βが97%以上を実現する準微粒子
高分散処理手段群、体積基準頻度分布で平均粒子径が8
00μmを越える準微粒子芯粒子粉体の粒子又は主に準
微粒子からなる芯粒子粉体の粒子を、準微粒子高分散処
理手段群により分散させた高分散芯粒子粉体の粒子・気
体混合物の芯粒子粉体の粒子の分散度βが99%以上を
実現する準微粒子高分散処理手段群、により気中に分散
させて高分散芯粒子粉体の粒子・気体混合物とする分散
工程、(B) この分散工程で分散させた高分散芯粒子
粉体の粒子・気体混合物の芯粒子粉体の粒子を、この分
散性能で気中に分散させた高分散芯粒子粉体の粒子・気
体混合物の芯粒子粉体の粒子の気中分散状態を維持する
気中分散維持手段、この高分散芯粒子粉体の粒子・気体
混合物の芯粒子粉体の粒子の気中分散状態を高める気中
分散促進手段、芯粒子粉体の粒子と気体との混合物にお
いて低分散芯粒子粉体の粒子・気体混合物を分離し、芯
粒子粉体の粒子が主に単一粒子状態で気中に存在する高
分散芯粒子粉体の粒子・気体混合物を選択する高分散芯
粒子粉体の粒子・気体混合物選択手段の1種類又はそれ
以上を介して搬送する搬送工程、(C) この搬送工程
で搬送した高分散芯粒子粉体の粒子・気体混合物の芯粒
子粉体の粒子を、その平均粒子径が10μmを越え20
μm以下のときには分散度βが80%以上、20μmを
越え50μm以下のときには分散度βが90%以上、5
0μmを越え300μm以下のときには分散度βが95
%以上、300μmを越え800μm以下のときには分
散度βが97%以上、800μmを越えるときには分散
度βが99%以上、の分散状態で、被覆空間の被覆開始
領域において被覆形成物質前駆体と接触及び/又は衝突
させて被覆を開始する被覆工程、を設けた被覆法。
V (A) Particles of quasi-fine particle core particle powder having an average particle size of more than 10 μm and 20 μm or less in a volume-based frequency distribution or particles of core particle powder mainly composed of quasi-fine particles are subjected to quasi-fine particle high dispersion treatment. High-dispersion core particles dispersed by means of means, core particles of a gas mixture, core particles of quasi-fine particle high-dispersion treatment means realizing a degree of dispersion β of particles of powder of 80% or more, average particles by volume-based frequency distribution Particles of highly dispersed core particle powder in which particles of quasi-fine particle core particle powder having a diameter of more than 20 μm and not more than 50 μm or particles of core particle powder mainly composed of quasi-fine particles are dispersed by a quasi-fine particle high dispersion treatment means group. -A group of quasi-fine particle high-dispersion treatment means that achieves a particle dispersity β of 90% or more in a core particle powder of a gas mixture, and a quasi-fine particle core particle powder having an average particle size of more than 50 μm and 300 μm or less in a volume standard frequency distribution Particles or mainly quasi-fine particles Particles of highly dispersed core particles obtained by dispersing the particles of the core particle powder made of (1) by the quasi-fine particle high dispersion treatment means group achieves a dispersity β of the particles of the core particle powder of the gas / gas mixture of 95% or more. Quasi-fine particle high dispersion treatment means group, quasi-fine particle core particle powder particles having an average particle size of more than 300 μm and 800 μm or less in the volume standard frequency distribution, or core particle powder mainly consisting of quasi-fine particles Particles of highly dispersed core particles dispersed by the processing means group, particles of the gas / core mixture of the gas mixture, the degree of dispersion β of the particles of the powder of the quasi-particulate high dispersion processing means group achieving 97% or more, averaged by volume-based frequency distribution Particle size is 8
Particles of highly dispersed core particle powder obtained by dispersing particles of quasi-fine particle core particle powder having a diameter of more than 00 μm or particles of core particle powder mainly composed of quasi-fine particles by a group of quasi-fine particle high dispersion treatment means Dispersing step of dispersing in air into a particle / gas mixture of high-dispersion core particle powder by means of a group of quasi-fine particle high-dispersion processing means that realizes a particle dispersity β of 99% or more in the particle powder, (B) Particles of highly dispersed core particles powder / gas mixture core particles dispersed in this dispersion step, particles of highly dispersed core particles powder / gas mixture core dispersed in the air with this dispersion performance In-air dispersion maintaining means for maintaining in-air dispersion state of particles of particle powder, in-air dispersion promoting means for increasing in-air dispersion state of particles of core particle powder of particles / gas mixture of highly dispersed core particle powder , Core particles powder in a mixture of particles and gas, low dispersion core particles powder Highly-dispersed core particles Powder particles / gas mixture that separates particles / gas mixture, and particles of core particles powder mainly exist in the air in single particle state Highly-dispersed core particles Powder particles A carrying step of carrying through one or more kinds of gas mixture selecting means, (C) particles of the highly dispersed core particle powder carried in this carrying step, and particles of the core particle powder of the gas mixture are averaged. Particle size exceeds 10μm 20
When it is less than μm, the dispersity β is 80% or more, and when it is more than 20 μm and less than 50 μm, the dispersity β is 90% or more, 5
When it is more than 0 μm and less than 300 μm, the dispersion degree β is 95
% And more than 300 μm and less than 800 μm, the dispersity β is 97% or more, and when more than 800 μm, the dispersity β is 99% or more in contact with the precursor of the coating forming material in the coating start region of the coating space. And / or a coating step of causing collision to start coating.

【0103】以上、1〜Vの全てにおいて、好適には、
体積基準頻度分布で平均粒子径が10μmを越え20μ
m以下の準微粒子芯粒子粉体の粒子又は主に準微粒子か
らなる芯粒子粉体の粒子を、準微粒子高分散処理手段群
により分散させた高分散芯粒子粉体の粒子・気体混合物
の芯粒子粉体の粒子の分散度βが80%以上を実現する
空間領域、体積基準頻度分布で平均粒子径が20μmを
越え50μm以下の準微粒子芯粒子粉体の粒子又は主に
準微粒子からなる芯粒子粉体の粒子を、準微粒子高分散
処理手段群により分散させた高分散芯粒子粉体の粒子・
気体混合物の芯粒子粉体の粒子の分散度βが90%以上
を実現する空間領域、体積基準頻度分布で平均粒子径が
50μmを越え300μm以下の準微粒子芯粒子粉体の
粒子又は主に準微粒子からなる芯粒子粉体の粒子を、準
微粒子高分散処理手段群により分散させた高分散芯粒子
粉体の粒子・気体混合物の芯粒子粉体の粒子の分散度β
が95%以上を実現する空間領域、体積基準頻度分布で
平均粒子径が300μmを越え800μm以下の準微粒
子芯粒子粉体の粒子又は主に準微粒子からなる芯粒子粉
体の粒子を、準微粒子高分散処理手段群により分散させ
た高分散芯粒子粉体の粒子・気体混合物の芯粒子粉体の
粒子の分散度βが97%以上を実現する空間領域、体積
基準頻度分布で平均粒子径が800μmを越える準微粒
子芯粒子粉体の粒子又は主に準微粒子からなる芯粒子粉
体の粒子を、準微粒子高分散処理手段群により分散させ
た高分散芯粒子粉体の粒子・気体混合物の芯粒子粉体の
粒子の分散度βが99%以上を実現する空間領域の内の
高分散芯粒子粉体の粒子・気体混合物中の芯粒子粉体の
粒子の全ての粒子が通過する面を含む空間領域に、被覆
空間の被覆開始領域を位置させるか、又は、体積基準頻
度分布で平均粒子径が10μmを越え20μm以下の準
微粒子芯粒子粉体の粒子又は主に準微粒子からなる芯粒
子粉体の粒子を、準微粒子高分散処理手段群により分散
させた高分散芯粒子粉体の粒子・気体混合物の芯粒子粉
体の粒子の分散度βが80%以上を実現する空間領域、
体積基準頻度分布で平均粒子径が20μmを越え50μ
m以下の準微粒子芯粒子粉体の粒子又は主に準微粒子か
らなる芯粒子粉体の粒子を、準微粒子高分散処理手段群
により分散させた高分散芯粒子粉体の粒子・気体混合物
の芯粒子粉体の粒子の分散度βが90%以上を実現する
空間領域、体積基準頻度分布で平均粒子径が50μmを
越え300μm以下の準微粒子芯粒子粉体の粒子又は主
に準微粒子からなる芯粒子粉体の粒子を、準微粒子高分
散処理手段群により分散させた高分散芯粒子粉体の粒子
・気体混合物の芯粒子粉体の粒子の分散度βが95%以
上を実現する空間領域、体積基準頻度分布で平均粒子径
が300μmを越え800μm以下の準微粒子芯粒子粉
体の粒子又は主に準微粒子からなる芯粒子粉体の粒子
を、準微粒子高分散処理手段群により分散させた高分散
芯粒子粉体の粒子・気体混合物の芯粒子粉体の粒子の分
散度βが97%以上を実現する空間領域、体積基準頻度
分布で平均粒子径が800μmを越える準微粒子芯粒子
粉体の粒子又は主に準微粒子からなる芯粒子粉体の粒子
を、準微粒子高分散処理手段群により分散させた高分散
芯粒子粉体の粒子・気体混合物の芯粒子粉体の粒子の分
散度βが99%以上を実現する空間領域の内の回収手段
の回収部に回収する全てに粒子が通過する面を含む空間
領域に、被覆空間の被覆開始領域を位置させて行うもの
である。
In all of the above 1 to V, preferably,
Volume-based frequency distribution with average particle size exceeding 10 μm and 20 μm
Particles of highly dispersed core particle powder obtained by dispersing particles of quasi fine particle core particle powder of m or less or particles of core particle powder mainly composed of quasi fine particles by a group of quasi fine particle high dispersion treatment means Spatial region that achieves a particle dispersity β of 80% or more, a quasi-fine particle core having an average particle size of more than 20 μm and not more than 50 μm in a volume-based frequency distribution, or a quasi-fine particle core or a core mainly made of quasi-fine particles Particles of high-dispersion core particle powder in which particles of particle powder are dispersed by a group of quasi-fine particle high-dispersion processing means.
Spatial region in which the degree of dispersion β of the core particle powder of the gas mixture is 90% or more, the volume standard frequency distribution has an average particle size of more than 50 μm and 300 μm or less Particles of highly dispersed core particles obtained by dispersing particles of finely divided core particles by means of a quasi-fine particle high dispersion treatment means group.
Of 95% or more in a spatial region, volume-based frequency distribution, and average particle diameter of more than 300 μm and 800 μm or less of quasi-fine particles core particles powder or particles of core particles mainly composed of quasi-fine particles A space region in which the degree of dispersion β of the particles of the particles / gas mixture of the high-dispersion core particle powder dispersed by the high-dispersion treatment means group is 97% or more, and the average particle diameter in the volume-based frequency distribution is Particles of highly dispersed core particle powder obtained by dispersing particles of quasi-fine particle core particle powder exceeding 800 μm or particles of core particle powder mainly consisting of quasi-fine particles by a group of quasi-fine particle high dispersion treatment means Highly dispersed core particles in a space region where the degree of particle dispersion β of the particle powder is 99% or more-including a surface through which all the particles of the core particle powder in the gas mixture pass. In the space area, the coating start area of the coating space Particles of the quasi-fine particle core particle powder having an average particle diameter of more than 10 μm and 20 μm or less in the volume-based frequency distribution or particles of the core particle powder mainly composed of quasi-fine particles are treated with a quasi-fine particle high dispersion treatment means. A space region in which the degree of dispersion β of the particles of the highly dispersed core particle powder and the particles of the core particle powder of the gas mixture dispersed by the group is 80% or more,
Volume-based frequency distribution with average particle size exceeding 20 μm and 50 μm
Particles of highly dispersed core particle powder obtained by dispersing particles of quasi fine particle core particle powder of m or less or particles of core particle powder mainly composed of quasi fine particles by a group of quasi fine particle high dispersion treatment means Spatial region where the degree of dispersion β of the particles of the particle powder is 90% or more, the average particle diameter in the volume-based frequency distribution is more than 50 μm and 300 μm or less, quasi-fine particle core A space region in which the degree of dispersion β of the particles of the highly dispersed core particle powder / gas mixture of the core particle powder of the highly dispersed core particle powder in which the particles of the particle powder are dispersed by the quasi-fine particle high dispersion treatment means group is 95% or more, Particles of a quasi-fine particle core particle powder having an average particle diameter of more than 300 μm and 800 μm or less in a volume-based frequency distribution or particles of a core particle powder mainly consisting of quasi-fine particles are dispersed by a quasi-fine particle high dispersion treatment means group. Dispersed core particles Powder particles / gas A space region where the degree of dispersion β of the compound core particle powder is 97% or more, a quasi-fine particle having an average particle size of more than 800 μm in a volume standard frequency distribution, or mainly quasi-fine particles. A space region in which the degree of dispersion β of the particles of the highly dispersed core particle powder / gas mixture of the core particle powder of the highly dispersed core particle powder in which the particles of the core particle powder are dispersed by means of the quasi-fine particle high dispersion treatment means group is 99% or more. The coating start region of the coating space is located in a space region including a surface through which particles pass through all of the recovery means of the recovery means.

【0104】又は、前記I及びIIにおいて、好適には、
体積基準頻度分布で平均粒子径が10μmを越え20μ
m以下の準微粒子芯粒子粉体の粒子又は主に準微粒子か
らなる芯粒子粉体の粒子を、準微粒子高分散処理手段群
により分散させた高分散芯粒子粉体の粒子・気体混合物
の芯粒子粉体の粒子の分散度βが80%以上を実現する
準微粒子高分散処理手段群、体積基準頻度分布で平均粒
子径が20μmを越え50μm以下の準微粒子芯粒子粉
体の粒子又は主に準微粒子からなる芯粒子粉体の粒子
を、準微粒子高分散処理手段群により分散させた高分散
芯粒子粉体の粒子・気体混合物の芯粒子粉体の粒子の分
散度βが90%以上を実現する準微粒子高分散処理手段
群、体積基準頻度分布で平均粒子径が50μmを越え3
00μm以下の準微粒子芯粒子粉体の粒子又は主に準微
粒子からなる芯粒子粉体の粒子を、準微粒子高分散処理
手段群により分散させた高分散芯粒子粉体の粒子・気体
混合物の芯粒子粉体の粒子の分散度βが95%以上を実
現する準微粒子高分散処理手段群、体積基準頻度分布で
平均粒子径が300μmを越え800μm以下の準微粒
子芯粒子粉体の粒子又は主に準微粒子からなる芯粒子粉
体の粒子を、準微粒子高分散処理手段群により分散させ
た高分散芯粒子粉体の粒子・気体混合物の芯粒子粉体の
粒子の分散度βが97%以上を実現する準微粒子高分散
処理手段群、体積基準頻度分布で平均粒子径が800μ
mを越える準微粒子芯粒子粉体の粒子又は主に準微粒子
からなる芯粒子粉体の粒子を、準微粒子高分散処理手段
群により分散させた高分散芯粒子粉体の粒子・気体混合
物の芯粒子粉体の粒子の分散度βが99%以上を実現す
る準微粒子高分散処理手段群、により気中に分散させて
高分散芯粒子粉体の粒子・気体混合物とする分散工程の
一部以上と前記被覆工程の一部以上とを、空間を一部以
上共有して行うものである。
Alternatively, in the above I and II, preferably,
Volume-based frequency distribution with average particle size exceeding 10 μm and 20 μm
Particles of highly dispersed core particle powder obtained by dispersing particles of quasi fine particle core particle powder of m or less or particles of core particle powder mainly composed of quasi fine particles by a group of quasi fine particle high dispersion treatment means A group of quasi-fine particle high-dispersion treatment means that realizes a particle dispersity β of 80% or more, particles of a quasi-fine particle core particle powder having an average particle size of more than 20 μm and 50 μm or less in a volume-based frequency distribution, or mainly Particles of core particle powder composed of quasi-fine particles are dispersed by means of a quasi-fine particle high dispersion treatment means group. Achievement of quasi-fine particle high-dispersion treatment means group, average particle diameter exceeding 50 μm in volume-based frequency distribution 3
Particles of highly dispersed core particle powder obtained by dispersing particles of quasi-fine particle core particle powder having a diameter of 00 μm or less or particles of core particle powder mainly composed of quasi-fine particles by a group of quasi-fine particle high dispersion treatment means A group of quasi-fine particle high-dispersion treatment means that achieves a particle dispersity β of 95% or more, a particle of quasi-fine particle core particle powder having an average particle size of more than 300 μm and 800 μm or less in a volume-based frequency distribution, or mainly Particles of highly dispersed core particle powder obtained by dispersing particles of core particle powder composed of quasi-fine particles by means of a quasi-fine particle high dispersion treatment means group have a degree of dispersion β of 97% or more Realized quasi-fine particle high-dispersion treatment means group, average particle diameter of 800μ in volume-based frequency distribution
Particles of a highly dispersed core particle powder in which particles of a quasi-fine particle core particle powder exceeding m or particles of a core particle powder mainly composed of quasi-fine particles are dispersed by a group of quasi-fine particle high dispersion treatment means Part of the dispersion process of dispersing particles in the air to form a particle-gas mixture of highly dispersed core particle powder by means of a quasi-fine particle high dispersion treatment means group that realizes a particle dispersibility β of the particle powder of 99% or more. And a part or more of the coating step are performed by sharing a part or more of the space.

【0105】次いで本発明を実施例によって更に詳細に
説明することにする。
The invention will now be described in more detail by way of examples.

【0106】実施例1 以下、図5(a)に示した構成の装置の具体例としての図
6およびその部分拡大図である図7に示した本発明の実
施例に基づいて詳細に説明する。
Embodiment 1 Hereinafter, a detailed description will be given based on the embodiment of the present invention shown in FIG. 6 as a specific example of the apparatus having the configuration shown in FIG. 5A and its partially enlarged view of FIG. 7. ..

【0107】本例の装置は、プラズマトーチ3−A、プ
ラズマ室3−a、被覆形成物質前駆体生成室の冷却槽3
−B、被覆形成物質前駆体生成室3−b、狭義の被覆室
冷却槽3−C、狭義の被覆室3−c、被覆準微粒子冷却
室の冷却槽3−D、被覆準微粒子冷却室3−d、被覆形
成物質の原料の供給側に、供給装置3−E1、芯粒子粉
体の供給側に、撹拌式分散機3−F1とエジェクター式
分散機3−H1、細管分散機107及び被覆準微粒子回
収部3−Gより成る。供給装置3−E1は被覆形成物質
の原料粉体の供給槽112に、撹拌式分散機3−F1は
芯粒子粉体の供給槽を備えた供給機111にそれぞれ結
合される。本例における被覆室は、定義ではプラズマ室
3−a、被覆形成物質前駆体生成室3−b、狭義の被覆
室3−c、被覆準微粒子冷却室3−dから構成されてお
り、ここではこれらを広義の被覆室と称する。広義の被
覆室の内、主に被覆処理の行われる室3−cを狭義の被
覆室と称する。
The apparatus of this example comprises a plasma torch 3-A, a plasma chamber 3-a, and a cooling tank 3 for the coating-formation-material precursor producing chamber.
-B, coating forming substance precursor generation chamber 3-b, narrowly-defined coating chamber cooling tank 3-C, narrowly-defined coating chamber 3-c, coating quasi-fine particle cooling chamber cooling tank 3-D, coating quasi-fine particle cooling chamber 3 -D, a supply device 3-E1 on the supply side of the raw material of the coating forming substance, a stirring type dispersion machine 3-F1 and an ejector type dispersion machine 3-H1, a capillary tube dispersion machine 107 and a coating on the supply side of the core particle powder. The quasi-fine particle recovery unit 3-G. The supply device 3-E1 is connected to the supply tank 112 for the raw material powder of the coating-forming substance, and the stirring-type disperser 3-F1 is connected to the supply device 111 equipped with the supply tank for the core particle powder. By definition, the coating chamber in this example is composed of a plasma chamber 3-a, a coating forming substance precursor generation chamber 3-b, a coating chamber 3-c in a narrow sense, and a coating quasi-fine particle cooling chamber 3-d. These are called a coating room in a broad sense. Of the coating chambers in the broad sense, the chamber 3-c in which the coating process is mainly performed is called the coating chamber in the narrow sense.

【0108】本準微粒子高分散処理手段群αは、供給槽
を備えた供給機111、撹拌式分散機3−F1とエジェ
クター式分散機3−H1及び内径4mmのステンレス製細
管分散機107で構成されており、図2(a)の準微粒子
高分散処理手段群の構成である。準微粒子高分散処理手
段群は、DM=40μmの(〔DM/5,5DM〕,≧9
0%)の粉体に対して出力時β≧90%を実現できるよ
うに構成されている。準微粒子高分散処理手段群の最終
処理手段である細管107は被覆室3−Cに直結してあ
り、被覆空間の3−L2の被覆開始領域3−L1におい
てDM=40μmの(〔DM/5,5DM〕,≧90%)
の粉体に対しβ≧90%を実現できるように構成されて
いる。
This semi-fine particle high dispersion treatment means group α comprises a feeder 111 having a feed tank, a stirring type dispersing machine 3-F1, an ejector type dispersing machine 3-H1 and a stainless steel thin tube dispersing machine 107 having an inner diameter of 4 mm. This is the structure of the quasi-fine particle high dispersion treatment means group in FIG. 2 (a). The quasi-fine particle high dispersion treatment means group has a D M = 40 μm ([D M / 5,5D M ], ≧ 9.
It is configured such that β ≧ 90% can be achieved at the time of output for 0%) powder. The thin tube 107, which is the final processing means of the quasi-fine particle high dispersion processing means group, is directly connected to the coating chamber 3-C, and D M = 40 μm ([D M / 5,5D M ], ≧ 90%)
It is configured so that β ≧ 90% can be realized for the powder of

【0109】プラズマトーチ3−Aは、例えば、内径4
4mm、長さ200mmの石英管を主体とし、外側に高周波
発振用のコイルが取り付けられ、その外側には冷却用の
外套管が設けられている。プラズマトーチ3−Aの上部
には噴出方向が接線方向、軸方向及び半径方向のガス噴
出口101が設けられている。プラズマトーチ3−Aの
下部は被覆形成物質の原料の供給口104が設けられ、
被覆形成物質の原料の供給槽を備えた供給機112から
供給される被覆形成物質の原料の粉体がキャリアガス1
03に担持されてプラズマ焔中に導入される構成であ
る。
The plasma torch 3-A has, for example, an inner diameter of 4
A quartz tube having a length of 4 mm and a length of 200 mm is mainly used, a coil for high-frequency oscillation is attached to the outside, and a jacket tube for cooling is provided on the outside. On the upper part of the plasma torch 3-A, a gas ejection port 101 whose ejection direction is tangential, axial and radial is provided. At the bottom of the plasma torch 3-A, a supply port 104 for the raw material of the coating forming material is provided.
The powder of the raw material of the coating forming substance supplied from the feeder 112 equipped with the supply tank of the raw material of the coating forming substance is the carrier gas 1.
It is a structure which is carried by 03 and introduced into the plasma flame.

【0110】被覆形成物質前駆体生成室3−bは、内径
120mm、長さ200mmの石英管と、その外側の冷却用
外套管3−Bとから成る。狭義の被覆室3−cは、内径
120mm、長さ100mmの内管とその外側の冷却用の外
套管3−Cとから成る。狭義の被覆室3−cは、芯粒子
粉体の供給槽を備えた供給機111から供給される芯粒
子が、撹拌式分散機3−F1、エジェクター式分散機3
−H1及び細管分散機107からなる準微粒子高分散処
理手段群αにより分散させて、狭義の被覆室3−cの中
央部に設けられた芯粒子粉体の供給口から導入される構
成である。被覆空間3−L2及び被覆空間の被覆開始領
域は、狭義の被覆室3−c内に設けてある。被覆準微粒
子冷却室3−dは、内径440mm、長さ800mmの管1
16とその外側の冷却用の外套管3−Dとから成る。被
覆準微粒子の回収部3−Gの出口部109は、真空ポン
プに連結され、被覆準微粒子がフィルター110上に集
められ取り出される構成である。
The coating material precursor producing chamber 3-b comprises a quartz tube having an inner diameter of 120 mm and a length of 200 mm, and a cooling outer tube 3-B outside the quartz tube. The covering chamber 3-c in a narrow sense is composed of an inner tube having an inner diameter of 120 mm and a length of 100 mm and an outer jacket tube 3-C for cooling the outer tube. In the narrowly-defined coating chamber 3-c, the core particles supplied from the feeder 111 equipped with the core particle powder supply tank are the stirring type disperser 3-F1 and the ejector type disperser 3.
-H1 and a fine particle high-dispersion treatment means group α composed of a fine tube disperser 107 and dispersed from a core particle powder supply port provided in the central portion of the coating chamber 3-c in a narrow sense. . The coating space 3-L2 and the coating start region of the coating space are provided in the coating chamber 3-c in a narrow sense. The coated quasi-fine particle cooling chamber 3-d is a tube 1 having an inner diameter of 440 mm and a length of 800 mm.
16 and a cooling mantle 3-D on the outside thereof. The outlet 109 of the coated quasi-fine particle collecting unit 3-G is connected to a vacuum pump so that the coated quasi-fine particles are collected on the filter 110 and taken out.

【0111】本発明の、実施例の被覆準微粒子の製造装
置により、芯粒子粉体の粒子として、DM=40μmで
(〔DM/5,5DM〕,≧90%)分布のダイヤモンド
の準微粒子粉体の粒子に、被覆形成物質として酸化けい
素を被覆した。プラズマトーチ3−Aの上部に設けられ
たガス噴出口101に供給源102からアルゴンガスを
20リットル/分の割合で供給する。このアルゴンガス
は印加された高周波によってプラズマ化され、プラズマ
トーチ3−A内プラズマ室3−aでプラズマ焔を形成す
る。
With the apparatus for producing coated quasi-fine particles according to the embodiment of the present invention, diamond particles having a distribution of D M = 40 μm ([D M / 5,5D M ], ≧ 90%) were obtained as core particle powder particles. The particles of the quasi-fine particle powder were coated with silicon oxide as a coating forming substance. Argon gas is supplied at a rate of 20 liters / minute from the supply source 102 to the gas ejection port 101 provided at the upper part of the plasma torch 3-A. The argon gas is turned into plasma by the applied high frequency, and forms a plasma flame in the plasma chamber 3-a in the plasma torch 3-A.

【0112】被覆形成物質の原料の供給槽を備えた供給
機112から供給した被覆形成物質の原料である酸化け
い素粉末は、5リットル/分のキャリアガス103に担
持されて、プラズマトーチ3−Aの下部に設けられた被
覆形成物質の原料の投入口104から、プラズマ焔中に
0.5g/分の割合で導入され、プラズマ焔の熱により
蒸発し、被覆形成物質前駆体生成室3−bで急冷、凝縮
して被覆形成物質前駆体となる。
The silicon oxide powder, which is the raw material of the coating forming substance, supplied from the feeder 112 equipped with the supply tank of the raw material of the coating forming substance is carried on the carrier gas 103 of 5 liter / min, and the plasma torch 3- From the inlet 104 for the raw material of the coating forming substance provided in the lower part of A, it is introduced into the plasma flame at a rate of 0.5 g / min, is evaporated by the heat of the plasma flame, and the precursor chamber for forming coating substance 3- It is rapidly cooled and condensed in b to become a coating material precursor.

【0113】芯粒子粉体の供給槽を備えた供給機111
から1.5g/分で供給されるダイヤモンドの芯粒子
は、撹拌式分散機3−F1により分散せしめ、5リット
ル/分の割合で供給されるキャリアガス105により担
持され、10リットル/分の流量の分散ガス106によ
るエジェクター式分散機3−H1及び細管分散機107
により気中に分散させる。
Feeder 111 equipped with a supply tank for core particle powder
The core particles of diamond supplied at 1.5 g / min from the above are dispersed by the stirring type disperser 3-F1 and carried by the carrier gas 105 supplied at a rate of 5 l / min, and the flow rate is 10 l / min. Ejector Disperser 3-H1 and Capillary Disperser 107
To disperse in the air.

【0114】本実施例の供給槽を備えた供給機111、
撹拌式分散機3−F1とエジェクター式分散機3−H1
及び細管分散機107で構成される準微粒子高分散処理
手段群αは、体積基準の頻度分布として、DM=40μ
mの(〔DM/5,5DM〕,≧90%)分布の芯粒子粉
体の粒子を、最終処理手段である細管分散機107で、
分散度β=94%に分散できる。又、被覆空間の被覆開
始領域3−L1で、分散度β=94%の分散状態で被覆
が始められる。
A feeder 111 having the feeding tank of this embodiment,
Stirring Disperser 3-F1 and Ejector Disperser 3-H1
The quasi-fine particle high-dispersion processing means group α constituted by the fine tube disperser 107 has a volume-based frequency distribution of D M = 40 μm.
m ([D M / 5,5D M ], ≧ 90%) distribution of particles of the core particle powder is treated with a fine tube disperser 107 which is a final treatment means.
The degree of dispersion β can be dispersed to 94%. Further, in the coating start region 3-L1 of the coating space, coating is started in the dispersed state with the dispersion degree β = 94%.

【0115】このようにして生成した、被覆形成物質で
表面が被覆された被覆準微粒子は、気体と共に被覆準微
粒子冷却室3−dを降下し、被覆準微粒子回収部3−G
に至る。この被覆準微粒子からなる製品は、フィルター
110により気体と分離し、集められ取り出される。
The coated quasi-fine particles having their surfaces coated with the coating-forming substance, which have been generated in this manner, move down together with the gas in the coated quasi-fine particle cooling chamber 3-d, and the coated quasi-fine particle recovery section 3-G.
Leading to. The product composed of the coated quasi-fine particles is separated from the gas by the filter 110, collected, and taken out.

【0116】得られた被覆準微粒子である、酸化けい素
で表面を被覆したダイヤモンド準微粒子を走査型電子顕
微鏡で観察したところ、図8に示す通り、一次粒子であ
る個々のダイヤモンド準微粒子に酸化けい素が超微粒子
状に被覆したものであった。
Observation of the obtained coated quasi-fine particles, that is, the diamond quasi-fine particles whose surface was coated with silicon oxide, by a scanning electron microscope revealed that as shown in FIG. It was an ultrafine particle coated with silicon.

【0117】比較例 分散手段を設けず、準微粒子粉体を供給機111から直
接被覆室3−cに導入するようにした点を除いて本実施
例で用いた装置とは同一の構成の装置を用い、本実施例
で用いたものと全く同じダイヤモンド準微粒子粉体を、
被覆形成物質の酸化けい素で被覆した。被覆室への投入
口におけるダイヤモンド準微粒子の分散度βは75%で
あった。得られた被覆粒子である、酸化けい素で表面を
被覆したダイヤモンド準微粒子を走査型電子顕微鏡で観
察したところ、図9に示すとおり部分的に酸化けい素が
被覆していない酸化けい素被覆ダイヤモンド準微粒子し
か得られなかった。
Comparative Example An apparatus having the same configuration as the apparatus used in this Example except that the dispersing means was not provided and the quasi-fine particle powder was introduced directly from the feeder 111 into the coating chamber 3-c. Using the same diamond quasi-fine particle powder used in this example,
It was coated with the coating forming material silicon oxide. The dispersion degree β of the quasi-fine diamond particles at the inlet to the coating chamber was 75%. The obtained coated particles, that is, the quasi-fine particles of diamond whose surface was coated with silicon oxide, were observed by a scanning electron microscope. As shown in FIG. 9, the silicon oxide-coated diamond in which silicon oxide was not partially coated was observed. Only quasi fine particles were obtained.

【0118】実施例2 図10およびその部分拡大図である図11に示した装置
は、図5(d)に示した構成の装置の1つの具体例であ
る。
Example 2 The apparatus shown in FIG. 10 and its partially enlarged view shown in FIG. 11 is one specific example of the apparatus having the configuration shown in FIG. 5 (d).

【0119】本例の被覆形成物質前駆体を生成せしめる
装置の構成は実施例1と同一である。準微粒子高分散処
理手段群αは、供給槽を備えた供給機214、撹拌式分
散機5−F1、細管分散機211及び衝突板を利用した
分散機5−H2で構成されており、図2(a)の準微粒子
高分散処理手段群の構成の一例である。細管分散機21
1は、内径4mmのステンレス製である。準微粒子高分散
処理手段群αの最終分散手段である衝突板を利用した分
散機5−H2は、SiC製の衝突板213がステンレス
製のホルダー212により設置された構成である。この
衝突板を利用した分散機5−H2は狭義の被覆室5−c
の中に設けられており、準微粒子高分散処理手段群αと
狭義の被覆室5−cは共有の空間を有している。また、
被覆空間5−L1及び被覆空間の被覆開始領域5−L2
は、狭義の被覆室5−c内に設けてある。本装置の準微
粒子高分散処理手段群によれば、体積基準頻度分布とし
て、DM=200μmの(〔DM/5,5DM〕,≧90
%)分布に相当する芯粒子粉体の粒子を、最終の分散処
理である衝突板を利用した分散機5−H2の衝突板21
5を衝突直後、分散度β≧95%に分散できる。したが
って、分散度β≧95%の状態で被覆が開始される。
The structure of the apparatus for producing the coating material precursor of this example is the same as that of the first embodiment. The quasi-fine particle high dispersion treatment means group α is composed of a feeder 214 having a feed tank, a stirring type dispersing machine 5-F1, a narrow tube dispersing machine 211, and a dispersing machine 5-H2 using a collision plate, as shown in FIG. It is an example of the constitution of the quasi-fine particle high dispersion treatment means group of (a). Capillary disperser 21
1 is made of stainless steel with an inner diameter of 4 mm. The disperser 5-H2 using a collision plate, which is the final dispersion means of the quasi-fine particle high dispersion treatment means group α, has a structure in which a collision plate 213 made of SiC is installed by a holder 212 made of stainless steel. The dispersion machine 5-H2 using this collision plate is a coating chamber 5-c in a narrow sense.
And the coating chamber 5-c in a narrow sense have a common space. Also,
Covering space 5-L1 and coating start region 5-L2 of the covering space
Is provided in the narrowly-defined coating chamber 5-c. According to the quasi-fine particle high-dispersion processing means group of the present apparatus, as the volume-based frequency distribution, D M = 200 μm ([D M / 5,5D M ], ≧ 90
%) Particles of the core particle powder corresponding to the distribution, the collision plate 21 of the disperser 5-H2 using the collision plate which is the final dispersion treatment.
Immediately after the collision, No. 5 can be dispersed to a dispersity β ≧ 95%. Therefore, the coating is started in the state of the dispersity β ≧ 95%.

【0120】本例の被覆準微粒子の製造装置により、芯
粒子粉体の粒子として、体積基準の平均粒子径DM=2
00μmで(〔DM/5,5DM〕,≧90%)分布の酸
化アルミニウムの準微粒子粉体の粒子に、被覆形成物質
として金属アルミニウムを被覆した。プラズマトーチ5
−Aの上部に設けられたガス噴出口201に供給源20
2から20リットル/分のアルゴンガスを供給する。こ
のアルゴンガスは印加された高周波によってプラズマ化
され、プラズマトーチ5−A内プラズマ室5−aでプラ
ズマ焔を形成する。
With the apparatus for producing coated quasi-fine particles of this example, the volume-based average particle diameter D M = 2 as the particles of the core particle powder.
Particles of a quasi-fine particle powder of aluminum oxide having a distribution of 00 [mu] m ([D M / 5,5D M ], ≧ 90%) were coated with metallic aluminum as a coating forming substance. Plasma torch 5
The gas supply port 201 is provided on the upper part of -A
Supply 2 to 20 liters / minute of argon gas. The argon gas is turned into plasma by the applied high frequency, and forms a plasma flame in the plasma chamber 5-a inside the plasma torch 5-A.

【0121】被覆形成物質の原料の供給槽を備えた供給
機215から0.5g/分で供給した被覆形成物質の原
料である金属アルミニウム粉末は、5リットル/分のキ
ャリアガス203に担持されて、プラズマトーチ5−A
の下部に設けられた被覆形成物質の原料の投入口204
から、プラズマ焔中に導入され、プラズマ焔の熱により
蒸発し、被覆形成物質前駆体生成室5−bで急冷、凝縮
して被覆形成物質前駆体となる。
The metal aluminum powder as the raw material of the coating forming material, which was supplied at 0.5 g / min from the feeder 215 equipped with the supply tank of the raw material of the coating forming material, was carried on the carrier gas 203 at 5 liters / minute. , Plasma torch 5-A
Feeding port 204 for the raw material of the coating forming material provided at the bottom of
Is introduced into the plasma flame, evaporated by the heat of the plasma flame, and rapidly cooled and condensed in the coating forming substance precursor generating chamber 5-b to become the coating forming substance precursor.

【0122】芯粒子粉体の供給槽を備えた供給機214
から2.0g/分で供給される酸化アルミニウムの芯粒
子は、撹拌式分散機5−F1により分散せしめ、20リ
ットル/分の割合で供給されるキャリアガス205によ
り担持され、細管分散機211を経て衝突板を利用した
分散機5−H2によって、分散度β=97%に気中に分
散せしめる。被覆室の中で分散せしめた芯粒子を、被覆
空間5−L2の被覆開始領域5−L1で分散度β=97
%の分散状態で被覆し始める。このようにして生成し
た、被覆形成物質で表面が被覆された被覆準微粒子は、
気体と共に被覆準微粒子冷却室5−dを降下し、被覆準
微粒子回収部5−Gに至る。この被覆準微粒子からなる
製品は、フィルター210により気体と分離し、集めら
れ取り出される。
Feeder 214 equipped with a supply tank for core particle powder
Aluminum oxide core particles supplied at a rate of 2.0 g / min from the above are dispersed by a stirring type disperser 5-F1 and carried by a carrier gas 205 supplied at a rate of 20 liters / min. After that, it is dispersed in the air to a dispersion degree β = 97% by a disperser 5-H2 using a collision plate. The core particles dispersed in the coating chamber are dispersed in the coating start region 5-L1 of the coating space 5-L2 to have a dispersity β = 97.
Start coating with a% dispersion. The thus-produced coated quasi-fine particles whose surface is coated with a coating-forming substance,
Along with the gas, the coated quasi-fine particle cooling chamber 5-d descends to reach the coated quasi-fine particle recovery section 5-G. The product composed of the coated quasi-fine particles is separated from the gas by the filter 210 and collected and taken out.

【0123】得られた被覆準微粒子である、金属アルミ
ニウムで表面を被覆した酸化アルミニウム準微粒子は、
走査型電子顕微鏡で観察したところ、一次粒子である個
々の酸化アルミニウム準微粒子に金属アルミニウムが被
覆したものである。被覆形態は実施例1で得たものと同
様であった。
The obtained coated quasi-fine particles, aluminum oxide quasi-fine particles whose surface was coated with metallic aluminum, were:
Observation with a scanning electron microscope reveals that individual aluminum oxide quasi-fine particles, which are primary particles, are coated with metallic aluminum. The coating morphology was similar to that obtained in Example 1.

【0124】実施例3 図12およびその部分拡大図である図13に示した装置
は、図5(b)に示した構成の装置の1つの具体例であ
る。
Example 3 The apparatus shown in FIG. 12 and a partially enlarged view of FIG. 13 is one specific example of the apparatus having the configuration shown in FIG. 5 (b).

【0125】本例の被覆形成物質前駆体を生成せしめる
装置の構成は、実施例1と同一である。準微粒子高分散
処理手段群αは、供給槽を備えた供給機313、分散手
段である撹拌式分散機6−F1、高分散芯粒子粉体の粒
子・気体混合物選択手段であるサイクロン6−Iで構成
されており、図2(b)のブロック図の構成の一例であ
る。サイクロン6−Iの高分散芯粒子粉体の粒子・気体
混合物の放出部は、搬送に不可避のパイプ307で狭義
の被覆室6−cへ接続してあり、低分散芯粒子粉体の粒
子・気体混合物の放出部は、ホッパー6−J、ロータリ
ーバルブ6−Kを介して搬送管310で撹拌式分散機6
−F1へ接続してある。本装置の準微粒子高分散処理手
段群によれば、体積基準の粒度分布として、DM=15
μmの(〔DM/5,5DM〕,≧90%)分布に相当す
る芯粒子粉体の粒子を、最終の処理手段であるサイクロ
ン6−Iの高分散芯粒子粉体流の放出部で、分散度β≧
90%に分散できる。狭義の被覆室6−cに図のごとく
被覆空間6−L2及び被覆空間の被覆開始領域6−L1
が設けてある。6−Cと6−Dを結合するフランジ部の
制約による不可避のパイプ307による分散度βの低下
は少なくとどめられる。したがって、被覆開始領域にお
いて、分散度β≧80%で被覆が開始される。
The structure of the apparatus for producing the coating material precursor of this example is the same as that of the first embodiment. The quasi-fine particle high dispersion treatment means group α includes a feeder 313 having a supply tank, a stirring type dispersing machine 6-F1 which is a dispersing means, and a cyclone 6-I which is a means for selecting a particle / gas mixture of highly dispersed core particle powder. And is an example of the configuration of the block diagram of FIG. The discharge part of the particles / gas mixture of the high-dispersion core particle powder of the cyclone 6-I is connected to the coating chamber 6-c in a narrow sense by a pipe 307 which is inevitable for transportation, and the particles of the low-dispersion core particle powder / The discharge portion of the gas mixture is provided with a carrier pipe 310 through a hopper 6-J and a rotary valve 6-K, and a stirring type disperser 6 is used.
-Connected to F1. According to the quasi-fine particle high dispersion treatment means group of this apparatus, D M = 15 as the volume-based particle size distribution.
of [mu] m ([D M / 5,5D M], ≧ 90%) of the particles in the powder of core particles corresponding to the distribution, release of the highly dispersed core particles in the cyclone 6-I which is the final processing means powder stream And the degree of dispersion β ≧
It can be dispersed to 90%. As shown in the drawing, the coating space 6-L2 and the coating start region 6-L1 of the coating space are provided in the coating chamber 6-c in a narrow sense.
Is provided. The decrease of the dispersion degree β due to the unavoidable pipe 307 due to the restriction of the flange portion connecting 6-C and 6-D can be limited. Therefore, in the coating start region, the coating starts with the dispersity β ≧ 80%.

【0126】本例の被覆準微粒子の製造装置により、芯
粒子粉体の粒子として、DM=15μmの(〔DM/5,
5DM〕,≧90%)分布の立方晶窒化硼素の準微粒子
粉体の粒子に、被覆形成物質として金属アルミニウムを
被覆した。プラズマトーチ6−Aの上部に設けられたガ
ス噴出口301に供給源302からアルゴンガスを20
リットル/分で供給する。このアルゴンガスは印加され
た高周波によってプラズマ化され、プラズマトーチ6−
A内プラズマ室6−aでプラズマ焔を形成する。
With the apparatus for producing coated quasi-fine particles of this example, as particles of the core particle powder, D M = 15 μm ([[D M / 5,5
5D M ], ≧ 90%) of cubic boron nitride quasi-fine grain powder particles were coated with metallic aluminum as a coating forming substance. Argon gas was supplied from the supply source 302 to the gas jet port 301 provided on the upper portion of the plasma torch 6-A.
Supply in liters / minute. This argon gas is turned into plasma by the applied high frequency, and the plasma torch 6-
A plasma flame is formed in the plasma chamber 6-a in A.

【0127】被覆形成物質の原料の供給槽を備えた供給
機314から0.5g/分で供給した被覆形成物質の原
料である金属アルミニウム粉末は、5リットル/分のキ
ャリアガス303に担持されて、プラズマトーチ6−A
の下部に設けられた被覆形成物質の原料の投入口304
から、プラズマ焔中に導入され、プラズマ焔の熱により
蒸発し、被覆形成物質前駆体生成室6−bで急冷、凝縮
して被覆形成物質前駆体となる。
Metallic aluminum powder, which is a raw material of the coating forming material, was supplied at 0.5 g / min from a feeder 314 equipped with a supply tank of the raw material of the coating forming material, and was supported on a carrier gas 303 of 5 liters / minute. , Plasma torch 6-A
Feeding port 304 for the raw material of the coating forming material provided at the bottom of the
Is introduced into the plasma flame, evaporated by the heat of the plasma flame, and rapidly cooled and condensed in the coating forming substance precursor generation chamber 6-b to become the coating forming substance precursor.

【0128】芯粒子粉体の供給槽を備えた供給機313
から1.7g/分で供給される立方晶窒化硼素の芯粒子
は、撹拌式分散機6−F1により分散させ、15リット
ル/分のキャリアガス305により担持されパイプ30
6を介してサイクロン6−Iに搬送される。サイクロン
6−Iは、微粉側の最大粒子径が20μmとなるように
調節されており、単一粒子を主に含む高分散芯粒子粉体
の粒子・気体混合物は、搬送に不可避のパイプ307を
介し放出口308から狭義の被覆室6−cに放出させ
る。一方、サイクロン6−Iにより選択分離した主に凝
集粒子からなる低分散芯粒子粉体の粒子・気体混合物分
散芯粒子粉体流は、ホッパー6−J、ロータリーバルブ
6−Kを経て、10リットル/分のキャリアガス309
によりパイプ310中を搬送され、撹拌式分散機6−F
1へフィードバックせしめる。準微粒子高分散処理手段
群αからの放出部であるサイクロン6−Iの高分散芯粒
子粉体の粒子・気体混合物の放出部での分散度は分散度
β=90%であり、被覆空間の被覆開始領域6−L1で
の分散度は、β=85%である。このようにして生成し
た、被覆形成物質で表面が被覆された被覆準微粒子は、
気体と共に被覆準微粒子冷却室6−dを降下し、被覆準
微粒子回収部6−Gに至る。この被覆準微粒子からなる
製品は、フィルター312により気体と分離し、集めら
れ取り出される。
Feeder 313 equipped with a supply tank for core particle powder
The cubic boron nitride core particles supplied at a rate of 1.7 g / min from 1 to 30 g are dispersed by the stirring type disperser 6-F1 and carried by the carrier gas 305 at 15 liters / min.
It is conveyed to cyclone 6-I via 6. The cyclone 6-I is adjusted so that the maximum particle size on the fine powder side is 20 μm, and the particle / gas mixture of the highly dispersed core particle powder mainly containing single particles flows through the pipe 307 which is inevitable for transportation. Through the discharge port 308, it is discharged to the coating chamber 6-c in a narrow sense. On the other hand, the particle / gas mixture-dispersed core particle powder flow of the low-dispersion core particle powder mainly composed of agglomerated particles selectively separated by the cyclone 6-I is passed through the hopper 6-J and the rotary valve 6-K to obtain 10 liters. Carrier gas 309 / min
Is carried in the pipe 310 by the stirring type dispersing machine 6-F.
Give feedback to 1. The degree of dispersion of the particles / gas mixture of the cyclone 6-I highly dispersed core particle powder, which is the discharge portion from the quasi-fine particle high dispersion treatment means group α, is the dispersion degree β = 90%, The degree of dispersion in the coating start region 6-L1 is β = 85%. The thus-produced coated quasi-fine particles whose surface is coated with a coating-forming substance,
Along with the gas, the coated quasi-fine particle cooling chamber 6-d descends to reach the coated quasi-fine particle recovery unit 6-G. The product composed of the coated quasi-fine particles is separated from the gas by the filter 312, collected and taken out.

【0129】得られた被覆準微粒子である、金属アルミ
ニウムで表面を被覆した立方晶窒化硼素準微粒子は、走
査型電子顕微鏡で観察したところ、一次粒子である個々
の立方晶窒化硼素準微粒子に金属アルミニウムが被覆し
たものである。被覆形態は実施例1と同様であった。
The obtained coated quasi-fine particles, which were cubic boron nitride quasi-fine particles whose surface was coated with metallic aluminum, were observed by a scanning electron microscope. It is coated with aluminum. The coating form was the same as in Example 1.

【0130】[0130]

【発明の効果】本発明の、被覆準微粒子の製造方法およ
び装置によって、準微粒子芯粒子粉体の粒子又は主に準
微粒子からなる芯粒子粉体の粒子であっても個々の粒子
に被覆形成物質を被覆可能となり、凝集体の表面を被覆
形成物質で被覆した被覆凝集体を生成することによる未
被覆の粒子や未被覆を持つ粒子を生成することが無くな
った。これにより、未被覆の芯粒子或いは未被覆部分を
有する芯粒子が存在しなくなり工業生産上のメリット
は、頗る大きい。
According to the method and apparatus for producing coated quasi-fine particles of the present invention, individual particles can be coated even if they are particles of quasi-fine particle core particle powder or particles of core particle powder mainly composed of quasi-fine particles. It became possible to coat the substance, and there was no longer the generation of uncoated particles or particles with uncoated particles by forming coated agglomerates in which the surface of the agglomerates was coated with a coating-forming substance. As a result, uncoated core particles or core particles having an uncoated portion do not exist, and the merit in industrial production is extremely large.

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

【図1】粉体粒子の分布図であり、(a)は本来の分散度
βを表わし、(b)は粒径D1〜D2の範囲の粒子が体積で
90%を占める粉体の粒径対体積基準頻度を表わす。
FIG. 1 is a distribution chart of powder particles, (a) shows the original dispersity β, and (b) shows the distribution of particles having a particle size range of D 1 to D 2 occupying 90% by volume. Represents particle size vs. volume based frequency.

【図2】(a)〜(c)は準微粒子高分散処理手段群の基本
構成を示すブロック図。
2A to 2C are block diagrams showing a basic configuration of a quasi-fine particle high dispersion treatment means group.

【図3】(a)〜(g)は準微粒子高分散処理手段群の構成
をより詳細に説明するブロック図。
3 (a) to 3 (g) are block diagrams for explaining the configuration of a quasi-fine particle high dispersion treatment means group in more detail.

【図4】(a)〜(e)は芯粒子粉体に被覆が開始される態
様を示す図。
FIGS. 4A to 4E are views showing a mode in which coating of core particle powder is started. FIG.

【図5】(a)〜(g)は本発明の装置の構成を説明するブ
ロック図。
5A to 5G are block diagrams illustrating the configuration of the device of the present invention.

【図6】実施例1の装置を示す図。FIG. 6 is a diagram showing an apparatus of Example 1.

【図7】実施例1の装置の部分拡大図。FIG. 7 is a partially enlarged view of the device according to the first embodiment.

【図8】実施例1の装置で得られた被覆準微粒子の走査
型電子顕微鏡写真。
8 is a scanning electron micrograph of coated quasi-fine particles obtained by the apparatus of Example 1. FIG.

【図9】比較例で得られた被覆準微粒子の走査型電子顕
微鏡写真。
FIG. 9 is a scanning electron micrograph of coated quasi-fine particles obtained in a comparative example.

【図10】実施例2の装置を示す図。FIG. 10 is a diagram showing an apparatus of Example 2.

【図11】実施例2の装置の部分拡大図。FIG. 11 is a partially enlarged view of the device according to the second embodiment.

【図12】実施例3の装置を示す図。FIG. 12 is a diagram showing an apparatus according to a third embodiment.

【図13】実施例3の装置の部分拡大図。FIG. 13 is a partially enlarged view of the device according to the third embodiment.

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】 芯粒子粉体を被覆空間に投入し、気相を
経て生成する被覆形成物質前駆体及び/又は気相状態の
被覆形成物質前駆体を、この芯粒子粉体の粒子に接触及
び/又は衝突させて、芯粒子粉体の粒子の表面を被覆形
成物質で被覆する被覆準微粒子の製造方法において、 (A) 準微粒子高分散処理手段群の最終処理手段が、
(a) この芯粒子粉体の粒子を気中に分散させる分散
手段、及び(b) 芯粒子粉体の粒子を気中に分散させ
た芯粒子粉体の粒子と気体との混合物において低分散芯
粒子粉体部分を分離し、芯粒子粉体の粒子が主に単一粒
子状態で気中に存在する高分散芯粒子粉体の粒子・気体
混合物を選択する高分散芯粒子粉体の粒子・気体混合物
選択手段とこの高分散芯粒子粉体の粒子・気体混合物選
択手段により選択分離された低分散芯粒子粉体部分を準
微粒子高分散処理手段群中の分散手段の内の最終分散手
段及び/又は最終分散手段以前の処理手段に搬送するフ
ィードバック手段とを備えた高分散芯粒子粉体の粒子・
気体混合物選択手段、から選ばれる準微粒子高分散処理
手段群により、体積基準頻度分布で平均粒子径が10μ
mを越える準微粒子芯粒子粉体の粒子又は主に準微粒子
からなる芯粒子粉体の粒子を、気中に分散させて高分散
芯粒子粉体の粒子・気体混合物とする分散工程、 (B) この分散工程で分散させた芯粒子粉体の粒子
を、 その平均粒子径が10μmを越え20μm以下のときに
は分散度βが80%以上、 20μmを越え50μm以下のときには分散度βが90
%以上、 50μmを越え300μm以下のときには分散度βが9
5%以上、 300μmを越え800μm以下のときには分散度βが
97%以上、そして800μmを越えるときには分散度
βが99%以上の分散状態で、被覆空間の被覆開始領域
において被覆形成物質前駆体と接触及び/又は衝突させ
て被覆を開始する被覆工程、を設けたことを特徴とす
る、被覆準微粒子の製造方法。
1. A core-particle powder is put into a coating space, and a coating-forming substance precursor and / or a gas-phase coating-forming substance precursor produced through a gas phase are brought into contact with the particles of the core-particle powder. And / or colliding to coat the surface of the particles of the core particle powder with the coating forming substance, in the method for producing coated quasi-fine particles,
(A) Dispersing means for dispersing the particles of the core particle powder in the air, and (b) Low dispersion in a mixture of the particles of the core particle powder and the gas in which the particles of the core particle powder are dispersed in the air. Highly dispersed core particle powder particles that separate the core particle powder part and select the particle / gas mixture of highly dispersed core particle powder in which the particles of the core particle powder mainly exist in the air in a single particle state. The gas dispersion selection means and the particles of the highly dispersed core particle powder, and the low dispersion core particle powder portion selectively separated by the gas mixture selection means are the final dispersion means of the dispersion means in the quasi-fine particle high dispersion treatment means group. And / or feedback means for conveying to the processing means before the final dispersing means, particles of highly dispersed core particle powder,
The average particle diameter is 10 μm in the volume-based frequency distribution by means of the quasi-fine particle high dispersion treatment means group selected from the gas mixture selecting means.
a dispersion step of dispersing particles of the quasi-fine particle core particle powder exceeding m or particles of the core particle powder mainly consisting of quasi-fine particles into the air to form a particle / gas mixture of the highly dispersed core particle powder; The particles of the core particle powder dispersed in this dispersion step have a dispersity β of 80% or more when the average particle size is more than 10 μm and 20 μm or less, and a dispersity β of 90 when the average particle size is more than 20 μm and 50 μm or less.
% And more than 50 μm and less than 300 μm, the dispersity β is 9
When the dispersity β is 97% or more when it is 5% or more and 300 μm or more and 800 μm or less, and the dispersity β is 99% or more when it is more than 800 μm, it is in contact with the coating material precursor in the coating start region of the coating space. And / or a coating step of causing collision to start coating, and a method for producing coated quasi-fine particles.
【請求項2】 体積基準頻度分布で平均粒子径が10μ
mを越え20μm以下の芯粒子粉体を、準微粒子高分散
処理手段群の最終処理により気中に分散させて高分散芯
粒子粉体の粒子・気体混合物とし、その芯粒子粉体の粒
子の分散度βを80%以上とする分散性能を有する準微
粒子高分散処理手段群、又は体積基準頻度分布で平均粒
子径が20μmを越え50μm以下の芯粒子粉体を、準
微粒子高分散処理手段群の最終処理により気中に分散さ
せて高分散芯粒子粉体の粒子・気体混合物とし、その芯
粒子粉体の粒子の分散度βを90%以上とする分散性能
を有する準微粒子高分散処理手段群、又は体積基準頻度
分布で平均粒子径が50μmを越え300μm以下の芯
粒子粉体を、準微粒子高分散処理手段群の最終処理によ
り気中に分散させて高分散芯粒子粉体の粒子・気体混合
物とし、その芯粒子粉体の粒子の分散度βを95%以上
とする分散性能を有する準微粒子高分散処理手段群、又
は体積基準頻度分布で平均粒子径が300μmを越え8
00μm以下の芯粒子粉体を、準微粒子高分散処理手段
群の最終処理により気中に分散させて高分散芯粒子粉体
の粒子・気体混合物とし、その芯粒子粉体の粒子の分散
度βを97%以上とする分散性能を有する準微粒子高分
散処理手段群、又は体積基準頻度分布で平均粒子径が8
00μmを越える芯粒子粉体を、準微粒子高分散処理手
段群の最終処理により気中に分散させて高分散芯粒子粉
体の粒子・気体混合物とし、その芯粒子粉体の粒子の分
散度βを99%以上とする分散性能を有する準微粒子高
分散処理手段群による分散工程を設け、準微粒子高分散
処理手段群により分散させた高分散芯粒子粉体の粒子・
気体混合物を被覆工程に直接放出するか、又は分散工程
と被覆工程の間に、準微粒子高分散処理手段群により分
散させた高分散芯粒子粉体の粒子・気体混合物を放出す
る放出部から、搬送に不可避の、中空部材、中空を形成
せしめる部材からなる中間部材、及びパイプから選択さ
れる一種類又はそれ以上の部材を介して搬送するか、及
び/又は、前記分散性能で気中に分散させた高分散芯粒
子粉体の粒子・気体混合物中の粒子の気中分散状態を維
持する気中分散維持手段、前記分散性能で気中に分散さ
せた高分散芯粒子粉体の粒子・気体混合物中の粒子の気
中分散状態を高める気中分散促進手段、芯粒子粉体の粒
子と気体との混合物の内の、低分散芯粒子粉体部分を分
離し、芯粒子粉体の粒子が主に単一粒子状態で気中に存
在する高分散芯粒子粉体の粒子・気体混合物を選択する
高分散芯粒子粉体の粒子・気体混合物選択手段の一種類
又はそれ以上を介して搬送する、搬送工程を設けること
を特徴とする、請求項1に記載の被覆準微粒子の製造方
法。
2. The volume-based frequency distribution has an average particle diameter of 10 μm.
A core particle powder having a particle size of more than 20 μm and not more than m is dispersed in the air by the final treatment of the quasi-fine particle high dispersion treatment means group to obtain a particle / gas mixture of the highly dispersed core particle powder. High-dispersion treatment means group for quasi-fine particles having a dispersibility β of 80% or more, or a core particle powder having an average particle diameter of more than 20 μm and 50 μm or less in a volume standard frequency distribution. Quasi-particulate high-dispersion treatment means having a dispersibility in which the particle / gas mixture of the highly-dispersed core particle powder is dispersed in the air by the final treatment of the above, and the degree of dispersion β of the particles of the core-particle powder is 90% or more. Core particles having a mean particle size of more than 50 μm and not more than 300 μm in a group or volume-based frequency distribution are dispersed in the air by the final treatment of the quasi-fine particle high-dispersion treatment means group to form particles of high-dispersion core particle powder. As a gas mixture, the core particle powder Quasi particle group of means for high dispersion treatment with a dispersion capability of the dispersity β of 95% or more of the particles, or beyond the average particle size of 300μm by volume frequency distribution 8
The core particle powder having a particle size of 00 μm or less is dispersed in the air by the final treatment of the quasi-fine particle high dispersion treatment means group to form a particle / gas mixture of the highly dispersed core particle powder, and the degree of dispersion β of the particles of the core particle powder Of 97% or more for the quasi-fine particle high dispersion treatment means having a dispersion performance, or the volume-based frequency distribution has an average particle diameter of 8
The core particle powder having a particle size of more than 00 μm is dispersed in the air by the final treatment of the quasi-fine particle high dispersion treatment means group to obtain a particle / gas mixture of the highly dispersed core particle powder, and the degree of dispersion β of the particles of the core particle powder. Particles of high-dispersion core particles which are dispersed by means of a group of quasi-fine particle high-dispersion treatment means having a dispersion performance of 99% or more.
The gas mixture is directly discharged to the coating step, or between the dispersion step and the coating step, from the discharge part for discharging the particle / gas mixture of the highly dispersed core particle powder dispersed by the quasi-fine particle high dispersion treatment means group, It is conveyed through one or more members selected from a hollow member, an intermediate member composed of a member for forming a hollow, and a pipe, which is unavoidable for carrying, and / or dispersed in the air with the above-mentioned dispersion performance. Air-dispersion maintaining means for maintaining the air-dispersed state of particles in a particle / gas mixture of highly dispersed core particle powder, particles / gas of highly-dispersed core particle powder dispersed in air with the above-mentioned dispersion performance In-air dispersion promoting means for increasing the air-dispersed state of particles in the mixture, in the mixture of particles and gas of the core particle powder, the low-dispersion core particle powder portion is separated, and the particles of the core particle powder are Highly dispersed core particles mainly present in the air in the form of single particles Highly dispersed core particles for selecting a powder particle / gas mixture A transfer step is provided for transferring the powder / particle mixture through one or more kinds of powder particle / gas mixture selecting means. Method for producing coated quasi-fine particles.
【請求項3】 体積基準頻度分布で平均粒子径が10μ
mを越え20μm以下の芯粒子粉体を、準微粒子高分散
処理手段群の最終処理により気中に分散させて高分散芯
粒子粉体の粒子・気体混合物とし、その芯粒子粉体の粒
子の分散度βを80%以上とする分散性能を有する準微
粒子高分散処理手段群、又は体積基準頻度分布で平均粒
子径が20μmを越え50μm以下の芯粒子粉体を、準
微粒子高分散処理手段群の最終処理により気中に分散さ
せて高分散芯粒子粉体の粒子・気体混合物とし、その芯
粒子粉体の粒子の分散度βを90%以上とする分散性能
を有する準微粒子高分散処理手段群、又は体積基準頻度
分布で平均粒子径が50μmを越え300μm以下の芯
粒子粉体を、準微粒子高分散処理手段群の最終処理によ
り気中に分散させて高分散芯粒子粉体の粒子・気体混合
物とし、その芯粒子粉体の粒子の分散度βを95%以上
とする分散性能を有する準微粒子高分散処理手段群、又
は体積基準頻度分布で平均粒子径が300μmを越え8
00μm以下の芯粒子粉体を、準微粒子高分散処理手段
群の最終処理により気中に分散させて高分散芯粒子粉体
の粒子・気体混合物とし、その芯粒子粉体の粒子の分散
度βを97%以上とする分散性能を有する準微粒子高分
散処理手段群、又は体積基準頻度分布で平均粒子径が8
00μmを越える芯粒子粉体を、準微粒子高分散処理手
段群の最終処理により気中に分散させて高分散芯粒子粉
体の粒子・気体混合物とし、その芯粒子粉体の粒子の分
散度βを99%以上とする分散性能を有する準微粒子高
分散処理手段群による分散工程の一部以上と前記被覆工
程の一部以上とを、空間を一部以上共有して行うことを
特徴とする、請求項1に記載の被覆準微粒子の製造方
法。
3. The volume-based frequency distribution has an average particle size of 10 μm.
A core particle powder having a particle size of more than 20 μm and not more than m is dispersed in the air by the final treatment of the quasi-fine particle high dispersion treatment means group to obtain a particle / gas mixture of the highly dispersed core particle powder. High-dispersion treatment means group for quasi-fine particles having a dispersibility β of 80% or more, or a core particle powder having an average particle diameter of more than 20 μm and 50 μm or less in a volume standard frequency distribution. Quasi-particulate high-dispersion treatment means having a dispersibility in which the particle / gas mixture of the highly-dispersed core particle powder is dispersed in the air by the final treatment of the above, and the degree of dispersion β of the particles of the core-particle powder is 90% or more. Core particles having a mean particle size of more than 50 μm and not more than 300 μm in a group or volume-based frequency distribution are dispersed in the air by the final treatment of the quasi-fine particle high-dispersion treatment means group to form particles of high-dispersion core particle powder. As a gas mixture, the core particle powder Quasi particle group of means for high dispersion treatment with a dispersion capability of the dispersity β of 95% or more of the particles, or beyond the average particle size of 300μm by volume frequency distribution 8
The core particle powder having a particle size of 00 μm or less is dispersed in the air by the final treatment of the quasi-fine particle high dispersion treatment means group to form a particle / gas mixture of the highly dispersed core particle powder, and the degree of dispersion β of the particles of the core particle powder Of 97% or more for the quasi-fine particle high dispersion treatment means having a dispersion performance, or the volume-based frequency distribution has an average particle diameter of 8
The core particle powder having a particle size of more than 00 μm is dispersed in the air by the final treatment of the quasi-fine particle high dispersion treatment means group to obtain a particle / gas mixture of the highly dispersed core particle powder, and the degree of dispersion β of the particles of the core particle powder. Characterized in that a part or more of the dispersion step and a part or more of the coating step by the quasi-fine particle high dispersion treatment means group having a dispersion performance of 99% or more are performed by sharing a part or more of the space. The method for producing coated quasi-fine particles according to claim 1.
【請求項4】 体積基準頻度分布で平均粒子径が、10
μmを越え20μm以下の芯粒子粉体を、準微粒子高分
散処理手段群の最終処理により気中に分散させて高分散
芯粒子粉体の粒子・気体混合物とし、その芯粒子粉体の
粒子の分散度βを80%以上とする空間領域、 体積基準頻度分布で平均粒子径が、20μmを越え50
μm以下の芯粒子粉体を、準微粒子高分散処理手段群の
最終処理により気中に分散させて高分散芯粒子粉体の粒
子・気体混合物とし、その芯粒子粉体の粒子の分散度β
を90%以上とする空間領域、 体積基準頻度分布で平均粒子径が、50μmを越え30
0μm以下の芯粒子粉体を、準微粒子高分散処理手段群
の最終処理により気中に分散させて高分散芯粒子粉体の
粒子・気体混合物とし、その芯粒子粉体の粒子の分散度
βを95%以上とする空間領域、 体積基準頻度分布で平均粒子径が、300μmを越え8
00μm以下の芯粒子粉体を、準微粒子高分散処理手段
群の最終処理により気中に分散させて高分散芯粒子粉体
の粒子・気体混合物とし、その芯粒子粉体の粒子の分散
度βを97%以上とする空間領域、 体積基準頻度分布で平均粒子径が、800μmを越える
芯粒子粉体を、準微粒子高分散処理手段群の最終処理に
より気中に分散させて高分散芯粒子粉体の粒子・気体混
合物とし、その芯粒子粉体の粒子の分散度βを99%以
上とする空間領域の内の、高分散芯粒子粉体の粒子・気
体混合物中の芯粒子粉体の粒子の全ての粒子が通過する
面を含む空間領域に、被覆空間の被覆開始領域を位置せ
しめるか、又は体積基準頻度分布で平均粒子径が、10
μmを越え20μm以下の芯粒子粉体を、準微粒子高分
散処理手段群の最終処理により気中に分散させて高分散
芯粒子粉体の粒子・気体混合物とし、その芯粒子粉体の
粒子の分散度βを80%以上とする空間領域、 体積基準頻度分布で平均粒子径が20μmを越え50μ
m以下の芯粒子粉体を、準微粒子高分散処理手段群の最
終処理により気中に分散させて高分散芯粒子粉体の粒子
・気体混合物とし、芯粒子粉体の粒子の分散度βを90
%以上とする空間領域、 体積基準頻度分布で平均粒子径が、50μmを越え30
0μm以下の芯粒子粉体を準微粒子高分散処理手段群の
最終処理により気中に分散させて高分散芯粒子粉体の粒
子・気体混合物とし、その芯粒子粉体の粒子の分散度β
を95%以上とする空間領域、 体積基準頻度分布で平均粒子径が、300μmを越え8
00μm以下の芯粒子粉体を、準微粒子高分散処理手段
群の最終処理により気中に分散させて高分散芯粒子粉体
の粒子・気体混合物とし、その芯粒子粉体の粒子の分散
度βを97%以上とする空間領域、 体積基準頻度分布で平均粒子径が、800μmを越える
芯粒子粉体を準微粒子高分散処理手段群の最終処理によ
り気中に分散させて高分散芯粒子粉体の粒子・気体混合
物とし、その芯粒子粉体の粒子の分散度βを99%以上
とする空間領域の内の、回収手段の回収部に回収する全
ての粒子が通過する面を含む空間領域に、被覆空間の被
覆開始領域を位置せしめることを特徴とする、請求項
1、2又は3に記載の被覆準微粒子の製造方法。
4. The volume-based frequency distribution has an average particle size of 10
A core particle powder having a particle size of more than 20 μm and more than 20 μm is dispersed in the air by the final treatment of the quasi-fine particle high dispersion treatment means group to obtain a particle / gas mixture of the highly dispersed core particle powder. Spatial region where dispersity β is 80% or more, average particle size exceeds 20 μm in volume standard frequency distribution 50
The core particle powder having a particle size of μm or less is dispersed in the air by the final treatment of the quasi-fine particle high dispersion treatment means group to obtain a particle / gas mixture of the highly dispersed core particle powder, and the degree of dispersion β of the particle of the core particle powder
Of 90% or more, the average particle size exceeds 50 μm in the volume-based frequency distribution, and 30
The core particle powder having a particle size of 0 μm or less is dispersed in the air by the final treatment of the quasi-fine particle high dispersion treatment means group to form a particle / gas mixture of the highly dispersed core particle powder, and the degree of dispersion β of the particles of the core particle powder Of 95% or more, the volume-based frequency distribution has an average particle size of more than 300 μm and 8
The core particle powder having a particle size of 00 μm or less is dispersed in the air by the final treatment of the quasi-fine particle high dispersion treatment means group to form a particle / gas mixture of the highly dispersed core particle powder, and the degree of dispersion β of the particles of the core particle powder Of 97% or more in a space region, and a core particle powder having an average particle size of more than 800 μm in a volume-based frequency distribution is dispersed in the air by the final treatment of the quasi-fine particle high-dispersion treatment means group to obtain a highly dispersed core particle powder. Particles of a highly dispersed core particle powder / particles of a core particle powder in a gas mixture in a spatial region where the degree of dispersion β of the particles of the core particle powder is 99% or more as a body particle / gas mixture. The coating start region of the coating space is located in the space region including the surface through which all the particles pass, or the average particle diameter is 10 in the volume standard frequency distribution.
A core particle powder having a particle size of more than 20 μm and more than 20 μm is dispersed in the air by the final treatment of the quasi-fine particle high dispersion treatment means group to obtain a particle / gas mixture of the highly dispersed core particle powder. Spatial region with dispersity β of 80% or more, volume-based frequency distribution with average particle size exceeding 20 μm and 50 μm
The core particle powder having a particle size of m or less is dispersed in the air by the final treatment of the quasi-fine particle high dispersion treatment means group to obtain a particle / gas mixture of the highly dispersed core particle powder, and the degree of dispersion β of the particles of the core particle powder is 90
% Or more in the spatial region, and the average particle size in the volume standard frequency distribution exceeds 50 μm and is 30
The core particle powder having a particle size of 0 μm or less is dispersed in the air by the final treatment of the quasi-fine particle high dispersion treatment means group to form a particle / gas mixture of the highly dispersed core particle powder, and the degree of dispersion β of the particles of the core particle powder
Of 95% or more, the volume-based frequency distribution has an average particle size of more than 300 μm and 8
The core particle powder having a particle size of 00 μm or less is dispersed in the air by the final treatment of the quasi-fine particle high dispersion treatment means group to form a particle / gas mixture of the highly dispersed core particle powder, and the degree of dispersion β of the particles of the core particle powder Of 90% or more in a spatial region, and a core particle powder having an average particle size of more than 800 μm in a volume-based frequency distribution is dispersed in the air by the final treatment of the quasi-fine particle high dispersion treatment means group to obtain a highly dispersed core particle powder. In the space area including the surface through which all particles to be recovered by the recovery unit of the recovery means pass, in the space area in which the degree of dispersion β of the particles of the core particle powder is 99% or more. The method for producing coated quasi-fine particles according to claim 1, 2 or 3, wherein a coating start region of the coating space is positioned.
【請求項5】 芯粒子粉体の粒子の粒度分布が、平均粒
子径をDMとしたとき、体積基準頻度分布で(〔DM
5,5DM〕,≧90%)であることを特徴とする、請
求項1、2、3又は4に記載の被覆準微粒子の製造方
法。
5. The particle size distribution of the powder of core particles of particles, when the average particle diameter is D M, by volume frequency distribution ([D M /
5,5D M ], ≧ 90%), The method for producing coated quasi-fine particles according to claim 1, 2, 3 or 4.
JP21926993A 1993-08-12 1993-08-12 Method for producing coated quasi-fine particles Expired - Fee Related JP3545784B2 (en)

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