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JPH0461687B2 - - Google Patents
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JPH0461687B2 - - Google Patents

Info

Publication number
JPH0461687B2
JPH0461687B2 JP61140993A JP14099386A JPH0461687B2 JP H0461687 B2 JPH0461687 B2 JP H0461687B2 JP 61140993 A JP61140993 A JP 61140993A JP 14099386 A JP14099386 A JP 14099386A JP H0461687 B2 JPH0461687 B2 JP H0461687B2
Authority
JP
Japan
Prior art keywords
solid particles
impact
powder
particles
surface modification
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
JP61140993A
Other languages
Japanese (ja)
Other versions
JPS62298443A (en
Inventor
Yorioki Nara
Masumi Koishi
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.)
Nara Machinery Co Ltd
Original Assignee
Nara Machinery Co Ltd
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 Nara Machinery Co Ltd filed Critical Nara Machinery Co Ltd
Priority to JP61140993A priority Critical patent/JPS62298443A/en
Priority to DE8686112228T priority patent/DE3687219T2/en
Priority to EP86112228A priority patent/EP0224659B1/en
Priority to SU864028279A priority patent/RU2047362C1/en
Priority to CN 86106765 priority patent/CN1007127B/en
Priority to KR1019860010468A priority patent/KR900001366B1/en
Publication of JPS62298443A publication Critical patent/JPS62298443A/en
Priority to US07/183,297 priority patent/US4915987A/en
Publication of JPH0461687B2 publication Critical patent/JPH0461687B2/ja
Granted legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F35/00Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
    • B01F35/71Feed mechanisms
    • B01F35/714Feed mechanisms for feeding predetermined amounts
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2/00Processes or devices for granulating materials, e.g. fertilisers in general; Rendering particulate materials free flowing in general, e.g. making them hydrophobic
    • B01J2/006Coating of the granules without description of the process or the device by which the granules are obtained
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/50Mixing liquids with solids
    • B01F23/565Mixing liquids with solids by introducing liquids in solid material, e.g. to obtain slurries
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F27/00Mixers with rotary stirring devices in fixed receptacles; Kneaders
    • B01F27/60Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a horizontal or inclined axis
    • B01F27/70Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a horizontal or inclined axis with paddles, blades or arms
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F33/00Other mixers; Mixing plants; Combinations of mixers
    • B01F33/80Mixing plants; Combinations of mixers
    • B01F33/836Mixing plants; Combinations of mixers combining mixing with other treatments
    • B01F33/8363Mixing plants; Combinations of mixers combining mixing with other treatments with coating
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F35/00Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
    • B01F35/71Feed mechanisms
    • B01F35/717Feed mechanisms characterised by the means for feeding the components to the mixer
    • B01F35/7173Feed mechanisms characterised by the means for feeding the components to the mixer using gravity, e.g. from a hopper
    • B01F35/71731Feed mechanisms characterised by the means for feeding the components to the mixer using gravity, e.g. from a hopper using a hopper
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F35/00Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
    • B01F35/71Feed mechanisms
    • B01F35/717Feed mechanisms characterised by the means for feeding the components to the mixer
    • B01F35/71805Feed mechanisms characterised by the means for feeding the components to the mixer using valves, gates, orifices or openings
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F35/00Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
    • B01F35/75Discharge mechanisms
    • B01F35/754Discharge mechanisms characterised by the means for discharging the components from the mixer
    • B01F35/7547Discharge mechanisms characterised by the means for discharging the components from the mixer using valves, gates, orifices or openings
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B9/00Making granules
    • B29B9/16Auxiliary treatment of granules
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/60Mixing solids with solids
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F35/00Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
    • B01F35/71Feed mechanisms
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B9/00Making granules
    • B29B9/16Auxiliary treatment of granules
    • B29B2009/163Coating, i.e. applying a layer of liquid or solid material on the granule

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Dispersion Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Processes Of Treating Macromolecular Substances (AREA)
  • Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
  • Glanulating (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)

Description

【発明の詳細な説明】 a 産業上の利用分野 本発明は、核となる粒子(以下母粒子という)
として、その表面形態が各種形状の凹凸や、孔
状、溝状の形状をもつ粒子を用いて、この母粒子
の表面や凹部にあらかじめ他の微粒子(以下子粒
子という)を付着、埋め込みをしておき、衝撃打
撃手段を用いてこの母粒子の凸部を軟化、溶融、
変形させ、母粒子の中に子粒子を包み込んで母粒
子の表面改質を行う方法に関する。
[Detailed description of the invention] a. Industrial application field The present invention is directed to core particles (hereinafter referred to as base particles).
As a method, particles with various surface shapes such as irregularities, pores, and grooves are used to attach and embed other particles (hereinafter referred to as child particles) in advance on the surface and recesses of the mother particles. The protrusions of the base particles are then softened, melted, and
This invention relates to a method for surface modification of mother particles by deforming the mother particles and enveloping child particles in the mother particles.

b 従来の技術 従来、一般に固体粒子の固結防止、変色変質防
止、分散性の向上、流動性の改善、触媒効果の向
上、消化・吸収の制御、磁気特性の向上、発色性
の改善、耐光性の向上などを目的として各種の表
面改質が、物理吸着法、化学吸着法、真空蒸着
法、静電付着法、熔解物質の被覆法、特殊スプレ
ードライング法などの方法で行なわれて来た。こ
れらのうち、特に固体粒子の表面を固体粒子で、
即ち、粉体の表面を粉体で表面改質する場合は、
公知の各種ミキサー型やボールミル型の攪拌機を
使つて長時間(数時間〜数十時間)攪拌し、攪拌
に伴なつて生ずる静電現象やメカノケミカル現象
を応用して改質を行なつて来た。
b Conventional technology Conventionally, in general, prevention of caking of solid particles, prevention of discoloration and deterioration, improvement of dispersibility, improvement of fluidity, improvement of catalytic effect, control of digestion and absorption, improvement of magnetic properties, improvement of color development, and light resistance. Various surface modifications have been carried out for the purpose of improving properties, such as physical adsorption, chemical adsorption, vacuum evaporation, electrostatic adhesion, molten substance coating, and special spray drying. . Among these, in particular, the surface of solid particles is
In other words, when modifying the surface of powder with powder,
Modification has been carried out by stirring for a long time (several hours to several tens of hours) using various known mixer type or ball mill type stirrers, and applying the electrostatic and mechanochemical phenomena that occur with stirring. Ta.

c 発明が解決しようとする問題点 前記従来の方法は、母粒子の囲りに子粒子が付
着されるだけで母粒子に対する子粒子の密着性が
十分でなく、そのため改質後の粉体を次工程で混
合、混練、分散、ペースト化等の加工をする場
合、子粒子が簡単に脱落したり、成分偏柝を生じ
たりしてその操作条件を著しく制限するばかりで
なく、加工後の生産品の品質にバラツキが生じる
最大の原因となつていた。
c Problems to be Solved by the Invention In the conventional method, the child particles are only attached to the surroundings of the mother particles, and the adhesion of the child particles to the mother particles is not sufficient. When processing processes such as mixing, kneading, dispersing, and pasting are performed in the next process, the child particles may easily fall off or the components may become unbalanced, which not only severely limits the operating conditions, but also severely limits the production efficiency after processing. This was the biggest cause of variations in product quality.

さらにまた、物質の除放性制御をする場合も
種々のマイクロカプセル化法が用いられてきた
が、すべて湿式法であり、次の工程として乾燥工
程が必要となるばかりでなく技術の適用分野も限
定されたもので汎用性に乏しかつた。
Furthermore, various microencapsulation methods have been used to control the sustained release of substances, but all of them are wet methods, and not only do they require a drying process as the next step, but the field of application of the technology is also limited. It was limited and lacked versatility.

本発明は前記事情に鑑みてなされたもので、従
来技術の前記問題点を解消した固体粒子の表面改
質方法を提供しようとするものである。
The present invention has been made in view of the above-mentioned circumstances, and it is an object of the present invention to provide a method for surface modification of solid particles that solves the above-mentioned problems of the prior art.

d 問題点を解決するための手段 本発明は前記問題点を解決するため、第1図に
示す如く、乾式、機械的手段により母粒子に子粒
子をまぶし、さらに母粒子の一部を軟化、溶融、
あるいは変形させて母粒子の中に子粒子を包み込
み、極めて短時間(数秒〜数分間)のうちに均一
な安定した粉体粒子の表面改質を行ない、それに
よつて機能性複合材料(ハイブリツドパウダー)
を得ることができる方法を提供するもので、その
要旨は、衝撃室内に、衝撃ピンを周設した回転盤
を配置すると共に、該衝撃ピンの最外周軌道面に
沿い、かつそれに対して一定の空間を置いて衝突
リングを配置し、前記衝撃ピンの回転によつて発
生した気流を、前記衝撃室と、前記衝撃突リング
の一部から前記回転盤の中心部付近の前カバーに
開口する循環回路とに誘導・循環させ、該気流と
共に表面に各種形状の凹凸や孔、溝をもつ平均粒
子径100〜0.1μmの固体粒子と、該固体粒子の凹
部や孔、溝の内部に入り込むことができる程度の
大きさの他の微小固体粒子とから構成される粉体
粒子群の全量を、繰り返し前記衝撃室と前記循環
回路とを通過させ、前記衝撃ピンと、前記衝突リ
ングとの間で前記固体粒子を粉砕しない範囲の機
械的打撃により、該固体粒子の凹部や孔、溝の内
部に前記他の微小固体粒子を付着、埋め込ませな
がら、または、付着、埋め込ませた後、前記固体
粒子の凸部を変形させ、さらに継続した機械的打
撃または該機械的打撃により発生した熱エネルギ
ーにより、前記固体粒子の凸部を軟化・溶融また
はさらに変形させて、該固体粒子の内部に前記他
の微小固体粒子を包み込んだ状態で複合化するこ
とを特徴とする固体粒子の表面改質方法にある。
d. Means for Solving the Problems In order to solve the above-mentioned problems, the present invention, as shown in FIG. melting,
Alternatively, by deforming the mother particles and enveloping the child particles in the mother particles, the surface of the powder particles can be uniformly and stably modified in an extremely short period of time (several seconds to several minutes), thereby producing functional composite materials (hybrid powders). )
The purpose is to provide a method that can obtain the following: A rotary disk surrounding an impact pin is placed in an impact chamber, and a rotational disk is provided along the outermost orbital surface of the impact pin, and at a constant distance with respect to the outermost orbital surface of the impact pin. A collision ring is arranged with a space therebetween, and airflow generated by the rotation of the impact pin is circulated through the impact chamber and a part of the impact ring to the front cover near the center of the rotary disk. The airflow is guided and circulated through a circuit, and together with the airflow, solid particles with an average particle diameter of 100 to 0.1 μm have irregularities, holes, and grooves of various shapes on the surface, and it is possible to enter the inside of the recesses, holes, and grooves of the solid particles. The entire amount of powder particles consisting of other fine solid particles of a size as large as possible is repeatedly passed through the impact chamber and the circulation circuit, and the solid particles are removed between the impact pin and the collision ring. While or after adhering and embedding the other microscopic solid particles inside the recesses, holes, and grooves of the solid particles, the convexity of the solid particles is caused by mechanical impact within a range that does not crush the particles. The convex portions of the solid particles are softened, melted, or further deformed by continuous mechanical impact or thermal energy generated by the mechanical impact, and the other fine solid particles are formed inside the solid particles. The present invention provides a method for surface modification of solid particles, which is characterized by forming a composite in a state in which the particles are encapsulated.

本発明の方法で表面処理できる代表的母粒子粉
体としては、一般にその平均粒子径が0.1μm〜
100μm程度で、かつ粒子表面形態が各種形状の凹
凸や孔状、溝状であるナイロンパウダー、ポリエ
チレンパウダー、アクリルパウダー、スチレンパ
ウダー、ABSパウダー、ポリプロピレンパウダ
ー、ゼラチン、各種ワツクス類、硫黄、銅粉、銀
粉等の有機物、無機物、金属類で、また代表的子
粒子粉体としては一般的に平行粒子径が0.01μm
〜10μm程度であるところの二酸化チタン、カー
ボン、酸化鉄などの顔料、エポキシパウダー、ナ
イロンパウダー、アクリルパウダーなどの高分子
材料、すず、銀、銅などの金属類、デンプン、セ
ルロース、シルクパウダー、セラミツクス類など
の天然材料や種々の粉末香料などである。しか
し、本発明はこれら材料に限定されることなく、
各種化学工業、電気、磁気材料工業、化粧品、塗
料、印刷インキ、及びトナー、色材、繊維、医
薬、食品、ゴム、プラスチツクス、窯業などの工
業界で使用されている各種材料の各組合わせ成分
に適用することができる。
Typical base particle powders that can be surface-treated by the method of the present invention generally have an average particle diameter of 0.1 μm to
Nylon powder, polyethylene powder, acrylic powder, styrene powder, ABS powder, polypropylene powder, gelatin, various waxes, sulfur, copper powder, which are approximately 100μm in size and have various surface shapes such as irregularities, holes, and grooves. Organic substances, inorganic substances, metals such as silver powder, and typical child particle powders generally have a parallel particle diameter of 0.01 μm.
Pigments such as titanium dioxide, carbon, and iron oxide with a diameter of ~10μm, polymeric materials such as epoxy powder, nylon powder, and acrylic powder, metals such as tin, silver, and copper, starch, cellulose, silk powder, and ceramics. These include natural materials such as herbs and various powdered fragrances. However, the present invention is not limited to these materials;
Combinations of various materials used in various chemical industries, electrical industries, magnetic materials industries, cosmetics, paints, printing inks, toners, coloring materials, textiles, pharmaceuticals, foods, rubber, plastics, ceramics, and other industries. Can be applied to ingredients.

以下、本発明の実施例について図面を参照しな
がら詳細に説明する。
Hereinafter, embodiments of the present invention will be described in detail with reference to the drawings.

第2図及び第3図は本発明の方法を実施するた
めの衝撃式打撃手段として衝撃式粉砕機を用いた
例を示す。仝図において、1は本発明方法を実施
するために使用する粉体衝撃装置(代表的な衝撃
式粉砕機)のケーシング、2はその後カバー、3
はその前カバー、4はケーシング1内にあつて高
速回転する回転盤、5は回転盤4の外周に所定間
隔を置いて放射状に周設された複数の衝撃ピンで
あり、これは一般にハンマー型またはプレート型
のものである。6は回転盤4をケーシング1内に
回転可能に軸支持する回転軸、8は衝撃ピン5の
最外周軌道面に沿い、かつそれに対して一定の空
間を置いて周設された衝突リングであり、これ
は、各種形状の凹凸型または円周平板型のものを
用いる。9は衝突リングの一部を切欠いて設けた
改質粉体排出用の開閉弁で、これは場合によつて
は前カバーや後カバーの粉砕室に面した一部を切
欠いて設けてもよい。10は開閉弁9の弁軸、1
1は弁軸10を介して開閉弁9を操作するアクチ
ユエーター、13は一端が衝突リング8の内壁の
一部に開口し、他端が回転盤4の中心部付近の前
カバー3に開口して閉回路を形成する循環回路、
14は原料ホツパー、15は原料ホツパー14と
循環回路13とを連結する原料供給用のシユー
ト、16は原料計量フイーダー、17は原料貯槽
である。18は回転盤4の外周と衝突リング8と
の間に設けられた衝撃室、19は循環回路13へ
の循環口を夫々示す。20は改質粉体排出シユー
ト、21はサイクロン、22はロータリーバル
ブ、23はバツグフイルター、24はロータリー
バルブ、25は排風機、31は本発明の運転を制
御する時限制御装置、32はあらかじめ母粒子の
表面に子粒子を付着させる必要のある場合に使用
する各種ミキサー、電動乳鉢等公知のプレプロセ
ツサーを夫々示す。
FIGS. 2 and 3 show an example in which an impact crusher is used as impact impact means for carrying out the method of the present invention. In the figure, 1 is a casing of a powder impacting device (a typical impact crusher) used to carry out the method of the present invention, 2 is a cover afterwards, and 3
4 is a front cover, 4 is a rotary disk that rotates at high speed inside the casing 1, and 5 is a plurality of impact pins radially arranged at predetermined intervals around the outer circumference of the rotary disk 4, which are generally hammer-shaped. Or a plate type one. Reference numeral 6 designates a rotating shaft that rotatably supports the rotary disk 4 within the casing 1, and 8 designates a collision ring disposed around the outermost orbital surface of the impact pin 5 with a certain space therebetween. , this uses various shapes of concave and convex type or circumferential flat plate type. Reference numeral 9 denotes an on-off valve for discharging modified powder, which is provided by cutting out a part of the collision ring, and in some cases, this may be provided by cutting out a part of the front cover or rear cover facing the grinding chamber. . 10 is the valve shaft of the on-off valve 9, 1
1 is an actuator that operates the on-off valve 9 via the valve shaft 10; 13 has one end opening in a part of the inner wall of the collision ring 8, and the other end opening in the front cover 3 near the center of the rotary disk 4; a circular circuit that forms a closed circuit,
14 is a raw material hopper, 15 is a raw material supply chute that connects the raw material hopper 14 and the circulation circuit 13, 16 is a raw material measuring feeder, and 17 is a raw material storage tank. Reference numeral 18 indicates a shock chamber provided between the outer periphery of the rotary disk 4 and the collision ring 8, and reference numeral 19 indicates a circulation port to the circulation circuit 13. 20 is a modified powder discharge chute, 21 is a cyclone, 22 is a rotary valve, 23 is a bag filter, 24 is a rotary valve, 25 is an exhaust fan, 31 is a time control device for controlling the operation of the present invention, and 32 is a preset Various types of mixers, electric mortars, and other known preprocessors used when it is necessary to attach child particles to the surface of particles are shown.

上記装置を用いて、本発明の粉体表面改質の方
法を実施する場合、次の要領で操作する。
When carrying out the powder surface modification method of the present invention using the above apparatus, the following procedure is performed.

まず、改質粉体排出用の開閉弁9を閉鎖した状
態としておき、必要に応じて不活性ガスを装置内
に導入しながら、駆動手段(図示せず)によつて
回転軸6を駆動し、改質処理すべき物質の性質に
より5m/sec〜160m/secの周速度で回転盤4を
回転させる。この際、回転盤4外周の衝撃ピン5
の回転に伴つて急激な空気・不活性ガスの気流が
生じ、この気流の遠心力に基づくフアン効果によ
つて衝撃室18に開口する循環回路13の循環口
19から循環回路13を巡つて回転盤4の中心部
に戻る気流の循環流れ、即ち完全な自己循環の流
れが形成される。しかもこの際発生する単位時間
当りの循環風量は、衝撃室と循環系の全容積に較
べて著しく多量であるため、短時間のうちに莫大
な回数の気流循環サイクルが形成されることにな
る。
First, the on-off valve 9 for discharging the reformed powder is kept in a closed state, and the rotating shaft 6 is driven by a driving means (not shown) while introducing inert gas into the apparatus as necessary. The rotary disk 4 is rotated at a circumferential speed of 5 m/sec to 160 m/sec depending on the properties of the substance to be modified. At this time, the impact pin 5 on the outer periphery of the rotary disk 4
A sudden air/inert gas airflow is generated as the airflow rotates, and due to the fan effect based on the centrifugal force of this airflow, the airflow rotates around the circulation circuit 13 from the circulation port 19 of the circulation circuit 13 that opens into the shock chamber 18. A circulating flow of airflow returning to the center of the plate 4, that is, a completely self-circulating flow is formed. Furthermore, since the amount of circulating air generated per unit time is significantly larger than the total volume of the shock chamber and circulation system, an enormous number of air circulation cycles are formed in a short period of time.

次に、一定量の母粒子の(凹部)に例えば静電
現象を利用して子粒子を付着させた被処理粉体
を、計量フイーダー16より原料ホツパー14に
短時間で投入する。プレプロセツサー32を使用
する必要のない場合は、母粒子、子粒子を夫々
別々に計量して原料ホツパー14に投入する。被
処理粉体は原料ホツパー14からシユート15を
通り衝撃室18に入る。衝撃室18へ送入された
粉体粒子群は、ここで高速回転する回転盤4の多
数の衝撃ピン5によつて瞬間的な打撃作用を受
け、さらに周辺の衝突リング8に衝突して再度衝
撃作用と強度の圧縮作用を受ける。そして同時に
前記循環ガスの流れに同伴して被処理粉体は循環
回路13を循環して再び衝撃室18へ戻り、再度
打撃作用を受ける。
Next, a powder to be treated, in which child particles are attached to the recesses of a predetermined amount of mother particles using, for example, an electrostatic phenomenon, is fed into the raw material hopper 14 from the metering feeder 16 in a short time. If it is not necessary to use the preprocessor 32, the mother particles and child particles are weighed separately and placed into the raw material hopper 14. The powder to be processed passes from the raw material hopper 14 through the chute 15 and enters the shock chamber 18 . The powder particles sent into the impact chamber 18 are instantaneously impacted by the many impact pins 5 of the rotary disk 4 that rotates at high speed, and then collide with the surrounding impact ring 8 to be struck again. Subject to impact action and strong compression action. At the same time, the powder to be treated is circulated through the circulation circuit 13 along with the flow of the circulating gas, returns to the impact chamber 18, and is again subjected to the impact action.

この様な衝撃作用が短時間のうちに連続して何
回も繰り返され、母粒子表面、特に母粒子凸部は
衝撃、打撃作用および該作用による(熱)エネル
ギーを受けることにより、短時間のうちに軟化、
溶融、変形され、母粒子に子粒子を包み込んだ状
態で母粒子による膜が母粒子表面に形成される。
そしてこの一連の衝撃作用は、母粒子の全表面が
所望の融着状態になるまで継続させるが、衝撃室
と循環系の全容積に較べて多量のガス(空気及び
不活性ガス)が系内を循環するため、ガスと同伴
して循環する被処理粉体(母粒子と子粒子)は極
めて短時間のうちに莫大な衝撃回数を受けること
になる。一回分の処理量にもよるが、この表面改
質に要する時間は被処理粉体の供給時間を含めて
も一般に数秒乃至数分の極めて短時間で終了す
る。
Such an impact action is repeated many times in a short period of time, and the surface of the base particle, especially the convex part of the base particle, receives the impact, impact action, and (thermal) energy from this action, resulting in a short period of time. Softening inside,
The mother particles are melted and deformed, and a film of the mother particles is formed on the surface of the mother particles in a state where the child particles are encapsulated in the mother particles.
This series of impact actions is continued until the entire surface of the base particles is in the desired fused state, but a large amount of gas (air and inert gas) is inside the system compared to the total volume of the impact chamber and circulation system. As a result, the powder to be treated (mother particles and child particles) that circulates together with the gas is subjected to a huge number of impacts in an extremely short period of time. Although it depends on the amount of treatment per batch, the time required for this surface modification is generally completed within an extremely short time of several seconds to several minutes, even including the time for supplying the powder to be treated.

第1図にモデル図を示す。図においてaは母粒
子で、その表面形態は各種形状の凹凸や、孔状、
溝状の形状を有するものである。bは子粒子であ
る。仝図1は原料系、仝図2は母粒子の凹部に子
粒子を付着させた状態を示す。この状態において
前記衝撃、打撃作用を与えることにより母粒子の
一部(凸部)が軟化溶融あるいは変形し、粒子は
仝図3,4と移行し、母粒子の中に子粒子が包み
込まれることになる。
Figure 1 shows a model diagram. In the figure, a is the base particle, and its surface morphology includes various shapes of unevenness, pores, etc.
It has a groove-like shape. b is a child particle. Figure 1 shows the raw material system, and Figure 2 shows the state in which the child particles are attached to the concave portions of the mother particles. In this state, by applying the above-mentioned impact or impact action, a part (convex part) of the base particle softens, melts, or deforms, and the particle moves as shown in Figures 3 and 4, and the child particles are wrapped in the base particle. become.

以上の固定化作業が終了した後、改質粉体排出
用の開閉弁9を鎖線で示す位置に移動させて開
き、固定化処理された粉体を排出する。この固定
化処理された粉体は、それ自身に作用している遠
心力(処理粉体に遠心力が作用しているところで
あれば排出弁9の位置は別のところでも良い。)
と、排風機25の吸引力によつて短時間(数秒
間)で衝撃室18及び循環回路13から排出さ
れ、シユート20を通つてサイクロン21及び循
環回路13から排出され、シユート20を通つて
サイクロン21及びバツグフイルター23などの
粉末捕集装置に誘導された後捕集され、ロータリ
ーバルブ22,24を介して系外に排出される。
After the above immobilization work is completed, the on-off valve 9 for discharging the modified powder is moved to the position shown by the chain line and opened, and the powder subjected to the immobilization process is discharged. This fixed powder is affected by the centrifugal force acting on itself (the discharge valve 9 may be located at a different location as long as the centrifugal force is acting on the treated powder).
Then, it is discharged from the shock chamber 18 and the circulation circuit 13 in a short period of time (several seconds) by the suction force of the exhaust fan 25, and is discharged from the cyclone 21 and circulation circuit 13 through the chute 20. 21 and a bag filter 23, the powder is collected and discharged to the outside of the system via rotary valves 22 and 24.

固定化処理された粉体を排出後、開閉弁9は直
ちに閉鎖され、再び計量フイダー16から、次回
以降の一定量の被処理粉体が衝撃室に供給されて
同様な工程を経て固定化処理された粉体が次々と
生産される。なお、これら一連の回分固定化処理
操作は、関連機器の動作時間に関連して、予め時
限設定された時限制御装置31によつて制御され
継続される。
After discharging the immobilized powder, the on-off valve 9 is immediately closed, and a certain amount of the powder to be treated for the next time is supplied to the shock chamber from the metering feeder 16 again and undergoes the same process to be immobilized. powder is produced one after another. Note that these series of batch fixing processing operations are controlled and continued by a time limit control device 31 whose time limit is set in advance in relation to the operating time of related equipment.

母粒子表面での母粒子による軟化溶融、成膜処
理が部分的局部的固定処理でよい場合、第2図の
粉体衝撃装置をワンパス式の連続処理システムと
して使用することも出来る。その場合は第2図に
おける循環口19を閉鎖し、開閉弁9を開とした
状態で被処理粉体を原料ホツパー15から連続的
に供給すれば良い。
If the softening, melting, and film-forming treatment by the base particles on the surface of the base particles can be carried out by local fixation, the powder impact apparatus shown in FIG. 2 can also be used as a one-pass continuous processing system. In that case, the powder to be treated may be continuously supplied from the raw material hopper 15 with the circulation port 19 in FIG. 2 closed and the on-off valve 9 open.

また、本発明による表面改質処理操作中、熱的
処理を補助的に併用する必要のある場合は、衝突
リング8や循環回路13をジヤケツト構造とし、
各種の熱媒や冷媒を通して被処理粉体の表面改質
処理に都合のよい温度条件を設定することができ
る。
In addition, during the surface modification treatment operation according to the present invention, if it is necessary to use thermal treatment as an auxiliary, the collision ring 8 and circulation circuit 13 may have a jacket structure.
Temperature conditions convenient for surface modification treatment of the powder to be treated can be set through various heating mediums and coolants.

また、本発明の実施に用いる粉体衝撃装置にお
いては、前記回転盤4に補助羽根を装着し、ある
いは循環回路13の途中に、たとえば遠心力型プ
レートフアンなどを配置して循環流に更に強制力
を与えることもできる。すなわち、循環風量を増
大させれば単位時間内の循環回数が増加し、従つ
て粉体粒子の衝突回数も増加するので、表面改質
処理時間を短縮することができる。
In addition, in the powder impacting device used for carrying out the present invention, auxiliary blades are attached to the rotary disk 4, or a centrifugal plate fan or the like is placed in the middle of the circulation circuit 13 to further force the circulating flow. It can also be empowering. That is, if the circulating air volume is increased, the number of times of circulation within a unit time increases, and therefore the number of collisions of powder particles also increases, so that the surface modification treatment time can be shortened.

さらにまた、本発明の実施に用いる粉体衝撃装
置は、上述した循環回路を与えたもののみでな
く、第2図および第3図の装置において循環回路
を取除いた構造のものも、これを使用することが
できる。
Furthermore, the powder impacting apparatus used in the practice of the present invention is not limited to the one provided with the above-mentioned circulation circuit, but also includes one having a structure in which the circulation circuit is removed from the apparatus shown in FIGS. 2 and 3. can be used.

また本発明を実施する雰囲気に空気中はもち論
のこと、粒子の組合せによつて酸化劣化の防止、
発火や爆発を防止する目的で窒素ガスや各種の不
活性ガスを使用する場合もある。
In addition, the atmosphere in which the present invention is carried out is in the air, and the combination of particles prevents oxidative deterioration.
Nitrogen gas or various inert gases may be used to prevent ignition or explosion.

第4図は本発明の実施にも用いる粉体衝撃装置
において、この不活性ガスを使用する実施例を示
す。なおこの実施例の説明に際し、前記実施例と
同一部材については同一符号を付し、説明を省略
する。第4図において、26は原料ホツパー14
の下部に設けた原料供給弁、27は原料供給用の
シユート15に開口する不活性ガスの供給弁、2
8は不活性ガス供給源、29は不活性ガスの供給
路を示す。尚、この実施例では循環回路13をケ
ーシング1内に収納した態様を示す。
FIG. 4 shows an example in which this inert gas is used in a powder impacting device which is also used in the practice of the present invention. In the description of this embodiment, the same members as in the previous embodiment are designated by the same reference numerals, and the explanation thereof will be omitted. In FIG. 4, 26 is the raw material hopper 14
27 is an inert gas supply valve that opens into the raw material supply chute 15;
Reference numeral 8 indicates an inert gas supply source, and 29 indicates an inert gas supply path. Note that this embodiment shows an embodiment in which the circulation circuit 13 is housed within the casing 1.

運転開始に際して、まず、原料供給弁26を閉
じ、開閉弁9を開いたあと、不活性ガスの供給弁
27を開き衝撃室18及び循環回路13内に不活
性ガスを充満させておく。この固定化作業開始に
先立つて行なう衝撃室及び循環回路内への不活性
ガスの置換は、通常数分以内で終了する。
When starting the operation, first, the raw material supply valve 26 is closed, the on-off valve 9 is opened, and then the inert gas supply valve 27 is opened to fill the shock chamber 18 and circulation circuit 13 with inert gas. The substitution of inert gas into the shock chamber and circulation circuit prior to the start of this immobilization work is usually completed within a few minutes.

次に開閉弁9と供給弁27とを同時に閉じたあ
と、直ちに原料供給弁26を開いて、予め計量さ
れた被処理粉体をシユート15を通じて衝撃室1
8に供給する。なお供給後、供給弁26は直ちに
閉の状態に戻し、その信号を受けて計量フイーダ
ー16は原料ホツパー14に次回の被処理粉体を
計量し供給しておく。
Next, after closing the on-off valve 9 and the supply valve 27 at the same time, the raw material supply valve 26 is immediately opened, and the pre-measured powder to be processed is passed through the chute 15 into the shock chamber 1.
Supply to 8. After supplying, the supply valve 26 is immediately returned to the closed state, and upon receiving this signal, the weighing feeder 16 measures and supplies the next powder to be processed to the raw material hopper 14.

以後は、不活性ガスと共に前記実施例の場合と
同様に被処理粉体の衝撃を行ない、被処理粉体は
循環回路13内を循環しながら不活性ガスとの十
分な接触を保ちつつ改質処理される。次に開閉弁
9と供給弁27とを開くと固定化処理された粉体
は、衝撃室18及び循環回路13からシユート2
0へ排出され、同時に衝撃室18及び循環回路1
3は新らしい不活性ガスで置換される。排出され
た表面改質粉体は前記実施例と同様に処理され
る。
Thereafter, the powder to be treated is bombarded with an inert gas in the same manner as in the above embodiment, and the powder to be treated is reformed while being circulated in the circulation circuit 13 while maintaining sufficient contact with the inert gas. It is processed. Next, when the on-off valve 9 and the supply valve 27 are opened, the immobilized powder is transferred from the shock chamber 18 and the circulation circuit 13 to the chute 2.
0 and at the same time shock chamber 18 and circulation circuit 1.
3 is replaced with a new inert gas. The discharged surface-modified powder is treated in the same manner as in the previous example.

以後は開閉弁9及び供給弁27を閉じて原料供
給弁26を開とすれば、次回分の改質処理操作が
進行する。なお、不活性ガスの供給、停止を含む
これら一連の回分固定化操作は、前記実施例と同
様に時限制御装置31によつて制御され継続され
る。
Thereafter, by closing the on-off valve 9 and the supply valve 27 and opening the raw material supply valve 26, the next reforming operation will proceed. Note that this series of batch fixing operations including supply and stop of the inert gas are controlled and continued by the time control device 31 as in the previous embodiment.

なお母粒子の軟化、溶融、あるいは変形が局所
的部分の処理でよい場合は、第4図の粉体衝撃装
置をワンパス室の連続処理システムとして使用す
ることができる。その場合は第4図における循環
回路13を閉塞し、原料供給弁26及び不活性ガ
スの供給弁27並びに開閉弁9を開とした状態で
被処理粉体を原料ホツパー14から連続的に一定
量の割合で供給すればよい。この際、排風機(第
2図の25)出口の不活性ガスを原料供給シユー
ト15へ戻す方式を採れば不活性ガスの使用量を
節減することになり経済的である。
If the softening, melting, or deformation of the base particles only needs to be done in a localized area, the powder impacting apparatus shown in FIG. 4 can be used as a continuous treatment system in a one-pass chamber. In that case, the circulation circuit 13 shown in FIG. It should be supplied at a ratio of . At this time, if a method is adopted in which the inert gas at the outlet of the exhaust fan (25 in FIG. 2) is returned to the raw material supply chute 15, the amount of inert gas used can be reduced, which is economical.

上述の如く、本願発明に係る固体(粉体)粒子
の表面改質方法の特長は、衝撃式打撃手段として
の衝撃式粉砕機構の微小粉体粒子に対する強力な
衝撃力と、使用する母粒子の表面形態に着目し、
衝撃力を利用しながら、母粒子で子粒子を母粒子
内に包み込んでしまうところにある。
As mentioned above, the features of the method for surface modification of solid (powder) particles according to the present invention are that the impact-type crushing mechanism as an impact-type impact means has a strong impact force on the fine powder particles, and the Focusing on surface morphology,
The process involves using impact force to envelop child particles within the parent particle.

また、第1図に示す如く本発明の方法によれ
ば、各種材料の母粒子に対する子粒子の包み込み
は単なる一成分子粒子によるものにとどまらず、
二成分以上の子粒子の包み込みも可能である。ま
た子粒子の形状も球状、不定形、繊維状などその
形状はとわない。
Furthermore, as shown in FIG. 1, according to the method of the present invention, the envelopment of the child particles into the mother particles of various materials is not limited to just one-component molecular particles;
It is also possible to encapsulate child particles of two or more components. Further, the shape of the child particles is not restricted, such as spherical, amorphous, and fibrous.

また、本発明の方法によれば、各母粒子に対す
る含有子粒子の割合(比率)がそれ程厳密でなく
ともよい場合(即ち、全体としての成分比率が一
定であればよい場合)は、各種ミキサー、電動乳
鉢などのプレプロセツサーを使用せず、別々に計
量された母粒子粉体と子粒子粉体を直接衝撃室に
供給して母粒子表面に対する子粒子の固定化処理
を行なうことができる。
In addition, according to the method of the present invention, when the ratio (ratio) of the contained child particles to each base particle does not need to be so strict (that is, when the overall component ratio only needs to be constant), various types of mixers can be used. It is possible to immobilize the child particles on the surface of the mother particle by directly supplying separately measured mother particle powder and child particle powder to the impact chamber without using a preprocessor such as an electric mortar.

実施例 1 回転盤に周設された8枚のプレート型衝撃ピン
の外径が235mm、循環回路の直径が54.9mmである
第2図の粉体衝撃装置を使用した。母粒子として
平均粒径dp50=19μmのポーラス状ナイロン6に
平均粒径dp50=0.03μmのアセチレンブラツクを
子粒子としてあらかじめミキサーで混合付着さ
せ、次に上記処理装置にて回転数6540rpm、粉体
仕込量120g、運転時間2minという条件で処理し
たところ、ナイロン粒子(母粒子)の中にアセチ
レンブラツク(子粒子)を包み込み、さらにその
表面をナイロン6で覆つているという表面改質粉
体を得た。
Example 1 The powder impact device shown in FIG. 2 was used, in which the outer diameter of eight plate-type impact pins disposed around a rotary disk was 235 mm, and the diameter of the circulation circuit was 54.9 mm. Acetylene black with an average particle diameter of dp 50 = 0.03 μm was mixed and adhered as a child particle to porous nylon 6 with an average particle diameter of dp 50 = 19 μm as a base particle in advance using a mixer, and then powdered at a rotation speed of 6540 rpm using the above processing device. When processed under the conditions of 120 g of body charge and 2 min of operation time, a surface-modified powder was created in which acetylene black (child particles) were wrapped in nylon particles (mother particles), and the surface was further covered with nylon 6. Obtained.

なお、前記実施例に用いた粉体サンプルの粉体
の走査型電子顕微鏡写真を第5図に示す。
Incidentally, a scanning electron micrograph of the powder sample used in the above example is shown in FIG.

e 発明の効果 以上のように、本願発明に係る固体粒子の表面
改質方法によれば各種粉体材料の組合わせから成
る母粒子に対してその表面形態を利用し他の子粒
子を母粒子中に包み込んでしまう表面の改質処理
を行ない、均一で安定した特性を有する機能性複
合・混成粉体材料(コンポジツトまたはハイブリ
ツドパウダー)を極めて短時間で効率よく生産す
ることができる。
e Effects of the Invention As described above, according to the method for surface modification of solid particles according to the present invention, the surface morphology of the mother particles made of a combination of various powder materials is utilized to transform other child particles into the mother particles. By performing a surface modification treatment that envelops the material, it is possible to efficiently produce a functional composite/hybrid powder material (composite or hybrid powder) with uniform and stable properties in an extremely short time.

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

第1図1〜4は本発明に係る方法で処理される
各種改質前粉体と改質後の粉体の態様を示す概念
的な説明図、第2図は、本発明の実施に用いた粉
体衝撃装置を、その前後装置とともに系統的に示
した概念的な説明図、第3図は第2図の側断面説
明図、第4図は同じく不活性ガスを用いる場合の
他の装置の説明図であり、第5図は実施例に用い
た粉体サンプルの粒子構造の走査型電子顕微鏡写
真を示し、仝図1は前記実施例に用いたポーラス
状ナイロン原料(2000倍)、2は母粒子に子粒子
を付着させたもの(5000倍)、3は衝撃打撃手段
により表面改質を行い子粒子を母粒子内に包み込
んだ状態(5000倍)を示す。 a……母粒子、b……子粒子、1……衝撃式粉
砕機。
1 to 4 are conceptual explanatory diagrams showing the aspects of various pre-modified powders and modified powders treated by the method according to the present invention, and FIG. A conceptual explanatory diagram systematically showing the powder impacting device that was used, along with its front and rear devices, Figure 3 is a side cross-sectional diagram of Figure 2, and Figure 4 is another device that also uses inert gas. FIG. 5 shows a scanning electron micrograph of the particle structure of the powder sample used in the example, and FIG. 1 shows the porous nylon raw material (2000x) used in the example, 3 shows a state in which child particles are attached to a mother particle (5000 times), and 3 shows a state in which the child particles are encapsulated within the mother particle after surface modification by impact impact means (5000 times). a...Mother particle, b...Child particle, 1...Impact type crusher.

Claims (1)

【特許請求の範囲】 1 衝撃室内に、衝撃ピンを周設した回転盤を配
置すると共に、該衝撃ピンの最外周軌道面に沿
い、かつそれに対して一定の空間を置いて衝突リ
ングを配置し、前記衝撃ピンの回転によつて発生
した気流を、前記衝撃室と、前記衝突リングの一
部から前記回転盤の中心部付近の前カバーに開口
する循環回路とに誘導・循環させ、該気流と共に
表面に各種形状の凹凸や孔、溝をもつ平均粒子径
100〜0.1μmの固体粒子と、該固体粒子の凹部や
孔、溝の内部に入り込むことができる程度の大き
さの他の微小固体粒子とから構成される粉体粒子
群の全量を、繰り返し前記衝撃室と前記循環回路
とを通過させ、前記衝撃ピンと、前記衝突リング
との間で前記固体粒子を粉砕しない範囲の機械的
打撃により、該固体粒子の凹部や孔、溝の内部に
前記他の微小固体粒子を付着、埋め込ませなが
ら、または、付着、埋め込ませた後、前記固体粒
子の凸部を変形させ、さらに継続した機械的打撃
または該機械的打撃により発生した熱エネルギー
により、前記固体粒子の凸部を軟化・溶融または
さらに変形させて、該固体粒子の内部に前記他の
微小固体粒子を包み込んだ状態で複合化すること
を特徴とする固体粒子の表面改質方法。 2 固体粒子の隣合う凸部の全部あるいは一部を
互いに融着させることを特徴とする特許請求の範
囲第1項に記載の固体粒子の表面改質方法。 3 予め固体粒子の凹部や孔、溝の内部に、他の
微小固体粒子を付着させておくことを特徴とする
特許請求の範囲第1項または第2項に記載の固体
粒子の表面改質方法。 4 補助手段として加熱し、固体粒子の隣合う凸
部を互いに融着させることを特徴とする特許請求
の範囲第1項〜第3項のいずれかに記載の固体粒
子の表面改質方法。 5 不活性ガス雰囲気下で行うことを特徴とする
特許請求の範囲第1項〜第4項のいずれかに記載
の固体粒子の表面改質方法。
[Scope of Claims] 1. A rotary disk surrounding an impact pin is arranged in an impact chamber, and a collision ring is arranged along the outermost orbital surface of the impact pin and with a certain space therebetween. , the airflow generated by the rotation of the impact pin is guided and circulated through the impact chamber and a circulation circuit that opens from a part of the impact ring to the front cover near the center of the rotary disk; In addition, the average particle size has various shapes of unevenness, pores, and grooves on the surface.
The entire amount of the powder particle group consisting of solid particles of 100 to 0.1 μm and other minute solid particles of a size that can fit inside the recesses, holes, and grooves of the solid particles is repeatedly removed as described above. The solid particles are passed through the impact chamber and the circulation circuit, and the solid particles are mechanically hit within a range that does not crush the solid particles between the impact pin and the collision ring, so that the solid particles are inside the recesses, holes, and grooves of the solid particles. While adhering and embedding fine solid particles, or after adhering and embedding, the convex portions of the solid particles are deformed, and the solid particles are further deformed by continuous mechanical impact or thermal energy generated by the mechanical impact. A method for surface modification of solid particles, which comprises softening, melting, or further deforming the convex portions of the solid particles to form a composite in a state in which the other fine solid particles are encapsulated inside the solid particles. 2. The method for surface modification of solid particles according to claim 1, characterized in that all or part of adjacent convex portions of the solid particles are fused to each other. 3. The method for surface modification of solid particles according to claim 1 or 2, which comprises adhering other fine solid particles to the inside of the recesses, holes, and grooves of the solid particles in advance. . 4. The method for surface modification of solid particles according to any one of claims 1 to 3, characterized in that heating is used as an auxiliary means to fuse adjacent convex portions of the solid particles to each other. 5. A method for surface modification of solid particles according to any one of claims 1 to 4, characterized in that the method is carried out under an inert gas atmosphere.
JP61140993A 1985-05-07 1986-06-17 Method for reforming surface of solid particle Granted JPS62298443A (en)

Priority Applications (7)

Application Number Priority Date Filing Date Title
JP61140993A JPS62298443A (en) 1986-06-17 1986-06-17 Method for reforming surface of solid particle
DE8686112228T DE3687219T2 (en) 1985-10-07 1986-09-04 METHOD FOR IMPROVING THE SURFACE QUALITY OF SOLID PARTICLES AND DEVICE THEREFOR.
EP86112228A EP0224659B1 (en) 1985-10-07 1986-09-04 Method of improving quality of surface of solid particles and apparatus thereof
SU864028279A RU2047362C1 (en) 1985-10-07 1986-10-03 Method and device for treating solid particle surface
CN 86106765 CN1007127B (en) 1985-05-07 1986-10-06 Method for improving quality of surface of solid particles and apparatus
KR1019860010468A KR900001366B1 (en) 1985-12-13 1986-12-08 Surface treating method of the solid particles and apparatus there for
US07/183,297 US4915987A (en) 1985-10-07 1988-04-11 Method of improving quality of surface of solid particles and apparatus thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61140993A JPS62298443A (en) 1986-06-17 1986-06-17 Method for reforming surface of solid particle

Publications (2)

Publication Number Publication Date
JPS62298443A JPS62298443A (en) 1987-12-25
JPH0461687B2 true JPH0461687B2 (en) 1992-10-01

Family

ID=15281656

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61140993A Granted JPS62298443A (en) 1985-05-07 1986-06-17 Method for reforming surface of solid particle

Country Status (1)

Country Link
JP (1) JPS62298443A (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6177550A (en) * 1984-09-25 1986-04-21 Mazda Motor Corp Brake system of car
EP1964875B1 (en) * 2005-12-14 2012-11-07 Ube Industries, Ltd. Powder composed of inorganic compound-loaded polyamide porous particle
JP2008050592A (en) * 2006-07-28 2008-03-06 Kyodo Printing Co Ltd Powder-integrated resin particles, granulation method thereof, particle-containing molded body, particle-containing sheet material, and molding methods thereof
WO2008013266A1 (en) * 2006-07-28 2008-01-31 Kyodo Printing Co., Ltd. Resin particle with powder united thereto and method of forming the same, particle-containing molded object, particle-containing sheet material, and method of forming these, and functional sheet and process for producing functional sheet
JP5089521B2 (en) * 2008-07-31 2012-12-05 学校法人 中村産業学園 Powder plasma processing method
US9539543B2 (en) * 2009-01-29 2017-01-10 Basf Corporation Mechanically fused materials for pollution abatement in mobile and stationary sources
JP2010185028A (en) * 2009-02-13 2010-08-26 Ube Ind Ltd Resin particle, method of production thereof and cosmetic
JP5603298B2 (en) * 2011-07-06 2014-10-08 株式会社Nbcメッシュテック Antiviral agent
JP2013188674A (en) * 2012-03-13 2013-09-26 Fuji Electric Co Ltd Particle structure and manufacturing method thereof
JP2013209338A (en) * 2012-03-30 2013-10-10 Nbc Meshtec Inc Bactericide

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62221434A (en) * 1986-03-22 1987-09-29 Nara Kikai Seisakusho:Kk Treatment of making micro-solid particle globular and device therefor
JPS62140636A (en) * 1985-12-13 1987-06-24 Nara Kikai Seisakusho:Kk Method and device for reforming surface of solid grain

Also Published As

Publication number Publication date
JPS62298443A (en) 1987-12-25

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