JPS61249711A - Heat treatment device - Google Patents

Heat treatment device

Info

Publication number
JPS61249711A
JPS61249711A JP60090946A JP9094685A JPS61249711A JP S61249711 A JPS61249711 A JP S61249711A JP 60090946 A JP60090946 A JP 60090946A JP 9094685 A JP9094685 A JP 9094685A JP S61249711 A JPS61249711 A JP S61249711A
Authority
JP
Japan
Prior art keywords
powder
airflow
air stream
diffusion
nozzle
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP60090946A
Other languages
Japanese (ja)
Inventor
Tsutomu Iwamoto
勉 岩本
Atsushi Saito
篤志 斉藤
Kazuhiro Kubouchi
窪内 一博
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.)
Konica Minolta Inc
Original Assignee
Konica Minolta 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 Konica Minolta Inc filed Critical Konica Minolta Inc
Priority to JP60090946A priority Critical patent/JPS61249711A/en
Publication of JPS61249711A publication Critical patent/JPS61249711A/en
Pending legal-status Critical Current

Links

Classifications

    • 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

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Developing Agents For Electrophotography (AREA)
  • Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)

Abstract

PURPOSE:To contrive to obtain at high yield granule and powder in small and uniform diameter by providing a rotating nozzle exhausting dispersion air stream and a dispersion air stream feeding mechanism feeding diffusion air stream inside of said rotating nozzle. CONSTITUTION:The mechanism 29 feeding air stream for diffusion is composed of the diffusion air stream nozzles 30 provided on the peripheral wall of a rotating nozzle 28 so as to be connected to the inside of said nozzle 28, and the diffusion air stream feeding part feeding the diffusion air stream to said nozzles 30. The diffusion air stream nozzles 30 are arranged in the positions almost symmetrical in relation with the axial direction of the rotating nozzle 28. These diffusion air stream nozzles 30 are arranged in such a manner that the diffusion air streams are, for instance, supplied in the directions crossing mutually downward obliqualy in relation to the axis of the rotating nozzle 28 inside of said nozzle 28. From the opening of the rotating nozzle 28, the dispersion air stream of powder and granule is exhausted downward while swirling at the state where the thickness D of the air stream layer of an empty cone shape is increased. Consequently, the space density of the powder and granule in the dispersion air stream is decreased, whereby the powder and granule are fully dispersed in low density.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、粉体または粒体よりなる粉粒体を熱処理して
所望の形態の粒子粉末を得るために用いられる熱処理装
置に関するものである。さらに詳しくは、熱可塑性樹脂
などを主成分とする粉粒体が分散された気流を旋回させ
ながら吐出する旋回ノズルを設け、この旋回ノズルの内
方に拡散用気流を供給する拡散用気流供給機構を配設し
、前記旋回ノズルから吐出された旋回気流を加熱する加
熱機構を設けることにより、凝着による粒子の粗大化を
防止することができて小径で粒径の揃った粒子粉末を高
い収率で得ることができるようにした熱処理装置に関す
るものである。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a heat treatment apparatus used for heat treating powder or granules to obtain particulate powder in a desired form. . More specifically, a diffusion airflow supply mechanism includes a swirling nozzle that swirls and discharges an airflow in which powder particles mainly composed of thermoplastic resin or the like are dispersed, and supplies a diffusion airflow inside the swirling nozzle. By providing a heating mechanism that heats the swirling airflow discharged from the swirling nozzle, coarsening of particles due to adhesion can be prevented, and a high yield of small and uniformly sized powder particles can be achieved. The present invention relates to a heat treatment apparatus that can obtain heat treatment at a high rate.

〔従来技術〕[Prior art]

例えば乾式の電子写真複写機においては、感光体上に形
成された静電潜像牽現像するためにトナーと称される粒
子粉末が用いられる。斯かるトナーは、通常、熱可塑性
樹脂を主成分とする粉粒体を熱処理して所望の形態即ち
所望の粒径及び所望の形状の粒子粉末に成形されて製造
される。
For example, in a dry type electrophotographic copying machine, powder particles called toner are used to develop and develop an electrostatic latent image formed on a photoreceptor. Such a toner is usually manufactured by heat-treating a powder or granular material containing a thermoplastic resin as a main component and molding it into powder particles having a desired shape, that is, a desired particle size and shape.

このような粉粒体の熱処理工程に用いられる熱処理装置
としては、従来、加圧熱気体の噴出流に、その外側から
或いは互いに交叉する方向から熱可塑性樹脂を主成分と
する粉粒体の分散気流を吹き込むことにより、当該粉粒
体の熱処理を行うようにした構成の熱処理装置が知られ
ている。
Conventionally, heat treatment equipment used in such a heat treatment process for powder and granules has been used to disperse powder and granules mainly composed of thermoplastic resin into a jet stream of pressurized hot gas from the outside or in directions that intersect with each other. 2. Description of the Related Art A heat treatment apparatus is known that is configured to perform heat treatment on the powder or granular material by blowing an air flow into it.

〔発明が解決しようとする問題点〕[Problem that the invention seeks to solve]

しかしながら、斯かる構成の装置においては、加圧熱気
体の噴出流に対して粉粒体の分散気流を均一に混合させ
ることが困難であり、従って熱処理にムラが生じて凝着
による粗大粒子が発生したり、或いは熱処理不足の粒子
が発生したりして、結局小径で粒径の揃った粒子粉末を
高い収率で得ることが困難である。
However, in an apparatus with such a configuration, it is difficult to uniformly mix the dispersion airflow of powder and granules with the jet flow of pressurized hot gas, which results in uneven heat treatment and coarse particles due to aggregation. As a result, it is difficult to obtain small and uniformly sized powder particles with a high yield.

このようなことから、粉粒体の分散気流を旋回ノズルか
ら旋回させながら吐出させることにより当該気流による
空円錐状の旋回気流を形成し、この空円錐状の旋回気流
の外側から加熱気流を同方向に旋回させながら混合して
熱処理を行うようにした構成の熱処理装置が提案された
。斯かる構成の装置によれば、粉粒体の分散気流と、加
熱気流とが略均−に混合されるようになるが、しかしな
がら旋回気流が遠心力により旋回ノズルの内壁近傍に集
中するためその層が薄くなり、粉粒体の供給量を増大せ
しめる場合には、旋回気流層における粉粒体の密度が高
くなり、従って粉粒体同志の凝着が起こり易くて粗大粒
子が発生し易い問題点を有している。
For this reason, by discharging the dispersion airflow of powder and granular material while swirling it from a swirling nozzle, a hollow cone-shaped swirling airflow is formed by the airflow, and a heated airflow is simultaneously generated from the outside of this hollow cone-shaped swirling airflow. A heat treatment apparatus has been proposed in which the heat treatment is performed by mixing the materials while rotating them in the same direction. According to the device having such a configuration, the dispersion airflow of the powder and the heated airflow are almost evenly mixed. However, the swirling airflow is concentrated near the inner wall of the swirling nozzle due to centrifugal force, When the layer becomes thinner and the amount of powder and granules supplied increases, the density of the powder and granules in the swirling airflow bed increases, which tends to cause the particles to stick together, resulting in the formation of coarse particles. It has points.

〔発明の目的〕[Purpose of the invention]

本発明は、以上の如き事情に基いてなされたものであっ
て、その目的は、粉粒体を小さな密度で良好に分散せし
めることができて粗大粒子の発生を抑止することができ
、その結果小径で粒径の揃った粒子粉末を高い収率で得
ることができる熱処理装置を提供することにある。
The present invention has been made based on the above-mentioned circumstances, and its object is to be able to disperse powder and granules well at a small density, to suppress the generation of coarse particles, and as a result, to suppress the generation of coarse particles. It is an object of the present invention to provide a heat treatment apparatus capable of obtaining powder particles having a small diameter and uniform particle size at a high yield.

〔問題点を解決するための手段〕[Means for solving problems]

本発明熱処理装置は、粉粒体を気流中で熱処理する熱処
理装置であって、粉粒体の分散気流を旋回せしめる旋回
機構と、この旋回機構よりの旋回された粉粒体の分散気
流を加熱する加熱機構とを有し、前記旋回機構は、分散
気流を吐出する旋回ノズルと、この旋回ノズルの内方に
拡散用気流を供給する拡散用気流供給機構とを具えてな
ることを特徴とする。
The heat treatment apparatus of the present invention is a heat treatment apparatus for heat-treating powder and granular materials in an air stream, and includes a swirling mechanism that swirls an airflow dispersing the powder and granules, and a swirling mechanism that heats the swirled dispersion airflow of the powder and granular materials. The heating mechanism is characterized in that the swirling mechanism includes a swirling nozzle that discharges a dispersed airflow, and a diffusion airflow supply mechanism that supplies a diffusion airflow to the inside of the swirling nozzle. .

斯かる装置によれば、粉粒体の分散気流は旋回ノズルの
内部において旋回しながら拡散用気流により乱されて拡
散されるようになるため、粉粒体が小さな密度で良好に
分散された状態で旋回ノズルから吐出されるようになる
。従って熱処理においてば粉粒体同志の凝着による粗大
化が抑制され、結局小径で粒径の揃った粒子粉末を高い
収率で得ることができる。
According to such a device, the dispersion airflow of the powder and granules is disturbed and diffused by the diffusion airflow while swirling inside the rotating nozzle, so that the powder and granules are well dispersed with a small density. It will now be discharged from the rotating nozzle. Therefore, during the heat treatment, coarsening due to adhesion of the powder particles to each other is suppressed, and as a result, particles of small diameter and uniform particle size can be obtained at a high yield.

〔実施例〕〔Example〕

以下、本発明の一実施例を図面を参照しながら詳細に説
明する。
Hereinafter, one embodiment of the present invention will be described in detail with reference to the drawings.

第1図は熱処理装置の一例の概略を示す説明図であり、
■は熱処理用容器、2は旋回機構、3は加熱機構、4は
冷却風供給機構、5はサイクロン、6は集塵機、7は排
気機構である。
FIG. 1 is an explanatory diagram showing an outline of an example of a heat treatment apparatus,
2 is a heat treatment container, 2 is a rotating mechanism, 3 is a heating mechanism, 4 is a cooling air supply mechanism, 5 is a cyclone, 6 is a dust collector, and 7 is an exhaust mechanism.

前記旋回機構2は、第2図及び第3図に拡大して示すよ
うに、エゼクタ部21と、旋回部22とよりなり、エゼ
クタ部21は、圧縮気流導入口23と、粉粒体の供給口
24と、混合室25と、スロート部26とよりなる。旋
回部22は、旋回室27と、旋回ノズル28と、拡散用
気流供給機構29とよりなる。
As shown enlarged in FIGS. 2 and 3, the turning mechanism 2 includes an ejector section 21 and a turning section 22, and the ejector section 21 has a compressed air flow inlet 23 and a powder supply port It consists of a mouth 24, a mixing chamber 25, and a throat portion 26. The swirling section 22 includes a swirling chamber 27, a swirling nozzle 28, and a diffusion air flow supply mechanism 29.

前記拡散用気流供給機構29は、第2図及び第3図に拡
大して示すように、旋回ノズル28の周壁に当該旋回ノ
ズル28の内部に連通ずるよう設けた拡散用気流ノズル
30と、この拡散用気流ノズル30に拡散用気流を供給
する拡散用気流供給部(図示せず)とよりなる。この例
においては、拡散用気流ノズル30は合計4個配設され
、これらの4個の拡散用気流ノズノL;30は旋回ノズ
ル28の軸方向に関して略対称の位置に配置され、そし
てこれらの拡散用気流ノズル30は、拡散用気流が旋回
ノズル28内に例えば当該旋回ノズル28の軸に対して
斜め下方に向かって交叉する方向に供給されるよう配置
されている。拡散用気流の圧力或いは拡散用気流の吐出
方向は特に限定されず自由に選定することができる。
As shown enlarged in FIGS. 2 and 3, the diffusion air flow supply mechanism 29 includes a diffusion air flow nozzle 30 provided on the peripheral wall of the swirl nozzle 28 so as to communicate with the interior of the swirl nozzle 28, and It consists of a diffusion airflow supply section (not shown) that supplies diffusion airflow to the diffusion airflow nozzle 30. In this example, a total of four diffusion airflow nozzles 30 are arranged, and these four diffusion airflow nozzles L; The airflow nozzle 30 is arranged so that the diffusion airflow is supplied into the swirling nozzle 28 in a direction diagonally downward and intersecting the axis of the swirling nozzle 28, for example. The pressure of the diffusion airflow or the discharge direction of the diffusion airflow is not particularly limited and can be freely selected.

またこの拡散用気流の圧力或いは拡散用気流の吐出方向
さらには拡散用気流ノズル30の数によって、粉粒体の
熱処理性能例えば造粒度、収率、粒径分布などが影響を
受けるので、例えば電子写真複写機に用いられるトナー
の製造工程における熱処理工程に用いることができる熱
処理装置を構成する場合には、トナニは通常粒径が6〜
20μmの範囲内の小径でかつ粒径が揃った粒子粉末で
あることが必要であり、従って得られる粒子粉末の粒径
が上記の範囲内に入り、かつ当該範囲内において粒径が
揃ったものとなるように、拡散用気流の圧力或いは拡散
用気流の吐出方向さらには拡散用気流ノズル30の数を
選定することが好ましい。この拡散用気流の温度は特に
限定されない。また拡散用気流ノズル30を設ける代わ
りに旋回ノズル28の周方向に沿って伸びる円環状のス
リットを設けてこのスリットを介して拡散用気流を旋回
ノズル28内に供給するように構成してもよい。
In addition, the heat treatment performance of the powder or granules, such as granulation degree, yield, particle size distribution, etc., is affected by the pressure of this diffusion airflow, the discharge direction of the diffusion airflow, and the number of diffusion airflow nozzles 30. When configuring a heat treatment device that can be used in the heat treatment process in the manufacturing process of toner used in electrophotographic copying machines, toner particles usually have a particle size of 6 to 6.
It is necessary that the particle powder has a small diameter within the range of 20 μm and the particle size is uniform, so the particle size of the obtained powder powder falls within the above range and the particle size is uniform within the range. It is preferable to select the pressure of the diffusion airflow, the discharge direction of the diffusion airflow, and the number of diffusion airflow nozzles 30 so that The temperature of this diffusion airflow is not particularly limited. Alternatively, instead of providing the diffusion airflow nozzle 30, an annular slit extending along the circumferential direction of the swirling nozzle 28 may be provided, and the diffusion airflow may be supplied into the swirling nozzle 28 through this slit. .

加熱機構3は、例えば、送気部31と、この送気部31
から供給される気流を加熱するヒータ一部32と、この
ヒータ一部32よりの加熱気流を容器1内に導入する加
熱気流導入部33とよりなる。この加熱気流導入部33
には整流部34が設けられていて、この整流部34によ
り、加熱気流は旋回ノズル28の開口から吐出された粉
粒体の分散気流を包囲するよう旋回ノズル28の開口の
外周全体に向かって供給される。
The heating mechanism 3 includes, for example, an air supply section 31 and an air supply section 31.
It consists of a heater part 32 that heats the airflow supplied from the heater part 32, and a heated airflow introducing part 33 that introduces the heated airflow from the heater part 32 into the container 1. This heated air flow introducing section 33
is provided with a rectifier 34, and the rectifier 34 directs the heated air flow toward the entire outer periphery of the opening of the swirl nozzle 28 so as to surround the dispersed airflow of powder and granules discharged from the opening of the swirl nozzle 28. Supplied.

旋回機構2においては、圧縮気流導入口23から混合室
25内に圧縮気流が導入されると共に供給口24から粉
粒体が混合室25内に供給されると、粉粒体が分散され
た高圧の気流がスロート部26を介して旋回室27内に
導入され、この旋回室27内で高圧の粉粒体の分散気流
が旋回しながらその圧力により旋回ノズル28の内壁に
沿って下降するようになる。しかしてこの旋回気流は、
拡散用気流ノズル30より旋回ノズル28内に供給され
た拡散用気流と衝突してその流れが乱されるため、旋回
ノズル28の内壁に沿って流れていた旋回気流が旋回ノ
ズル28の内方側に拡散されながら、当該旋回ノズル2
8の開口から下方に向かって吐出される。一方加熱機構
3により加熱気流が容器1内に供給されると、加熱気流
導入部33により当該加熱気流は旋回ノズル28の開口
の外周全体から粉粒体の分散気流に会合するようになり
、これにより当該分散気流内の粉粒体はその表面が溶融
されて球形化されると共に、微小な粉粒体が造粒されて
新たな粒状体となる。その後冷却風供給機構4から供給
された冷却風により冷却されて固化し、次いで固化粒体
がサイクロン5内に送られて当該サイクロン5により固
化粒体が分離されて粒子粉末が補集器内に補集される。
In the swirling mechanism 2, when compressed airflow is introduced into the mixing chamber 25 from the compressed airflow inlet 23 and powder and granules are supplied into the mixing chamber 25 from the supply port 24, the high pressure in which the powder and granules are dispersed is generated. The airflow is introduced into the swirling chamber 27 through the throat portion 26, and the high-pressure dispersed airflow of powder and granules swirls within the swirling chamber 27, so that the pressure causes it to descend along the inner wall of the swirling nozzle 28. Become. However, the swirling airflow of the lever is
Because the flow is disturbed by colliding with the diffusion airflow supplied from the diffusion airflow nozzle 30 into the swirling nozzle 28, the swirling airflow that was flowing along the inner wall of the swirling nozzle 28 is directed to the inner side of the swirling nozzle 28. The rotating nozzle 2
It is discharged downward from the opening 8. On the other hand, when the heated airflow is supplied into the container 1 by the heating mechanism 3, the heated airflow comes to join the dispersed airflow of the powder and granular material from the entire outer periphery of the opening of the swirling nozzle 28 by the heated airflow introduction part 33. As a result, the surfaces of the powder and granules in the dispersed air flow are melted and spherical, and fine powder and granules are granulated to form new granules. Thereafter, the solidified granules are cooled and solidified by the cooling air supplied from the cooling air supply mechanism 4, and then the solidified granules are sent into the cyclone 5, where the solidified granules are separated and the particles are placed in the collector. It will be supplemented.

一方サイクロン5の上部の気流出口からは排気流が排出
される。
On the other hand, an exhaust flow is discharged from the air outlet at the upper part of the cyclone 5.

以上の実施例によれば、旋回ノズル28の内方に拡散用
気流を供給する拡散用気流供給機構29を設けているた
め、粉粒体の分散気流は旋回ノズル28の内部において
拡散用気流ノズル30から供給される拡散用気流と衝突
してその流れが乱され、従って遠心力により旋回ノズル
28の内壁に沿って偏って流れていた旋回気流が旋回ノ
ズル28の内方側にも拡散されるようになって、旋回ノ
ズル28の開口からは空円錐状の気流層の厚さDが増加
した状態で粉粒体の分散気流が旋回しながら下方に吐出
されるようになり、この結果分散気流中の粉粒体の空間
濃度が低くなって粉粒体が小さな密度で良好に分散され
た状態となる。従って加熱気流により加熱されるときに
は、粉粒体同志の凝着による粗大化が防止されて造粒度
が小さく抑えられ、結局小径で粒径の揃った粒子粉末を
高い収率で得ることができる。そしてこのように粉粒体
を空間濃度が低い状態で分散せしめることができるので
、粉粒体の供給量を増加せしめて一層高い収率で粉粒体
の熱処理を行うこともできる。そして粉粒体の分散気流
は、拡散用気流により速度が低減化された状態で旋回ノ
ズル28の開口から吐出されるようになるので、加熱気
流との熱的な会合時間が長くなり、従って熱処理不足の
粒子を招来せずに良好な熱処理を行うことができる。そ
して加熱気流は、加熱気流導入部33により旋回ノズル
28の外壁上部から当該旋回ノズル28の開口の外周全
体に向かって供給されるため、旋回ノズル28の開口か
ら吐出された粉粒体の分散気流は加熱気流に包囲されな
がら加熱される状態となり、従って粉粒体の飛散が生し
にくくて装置内の汚染を伴わずに粉粒体の熱処理を施す
ことができる。
According to the embodiments described above, since the diffusion air flow supply mechanism 29 that supplies the diffusion air flow inside the swirl nozzle 28 is provided, the dispersion air flow of the powder and granules is supplied to the diffusion air flow nozzle inside the swirl nozzle 28. It collides with the diffusion airflow supplied from the swirling nozzle 30 and the flow is disturbed, and therefore, the swirling airflow that was flowing unevenly along the inner wall of the swirling nozzle 28 due to centrifugal force is also diffused to the inner side of the swirling nozzle 28. As a result, the dispersion airflow of powder particles is discharged downward from the opening of the swirling nozzle 28 with the thickness D of the empty conical airflow layer increasing, and as a result, the dispersion airflow The spatial concentration of the powder and granules therein becomes low and the powder and granules are well dispersed with a small density. Therefore, when heated by a heated air stream, coarsening due to adhesion of powder and granules is prevented, and the granulation degree is kept small, resulting in a high yield of small and uniformly sized powder particles. . Since the powder and granules can be dispersed at a low spatial concentration in this manner, the supply amount of the powder and granules can be increased and the powder and granules can be heat-treated at a higher yield. Since the dispersion airflow of the powder particles is discharged from the opening of the swirling nozzle 28 with its speed reduced by the diffusion airflow, the thermal association time with the heated airflow becomes longer, and therefore the heat treatment Good heat treatment can be performed without introducing insufficient particles. Since the heated airflow is supplied from the upper part of the outer wall of the swirling nozzle 28 toward the entire outer periphery of the opening of the swirling nozzle 28 by the heated airflow introduction part 33, the powder and granular material discharged from the opening of the swirling nozzle 28 is dispersed. is in a state where it is heated while being surrounded by a heated air current, so that the powder particles are less likely to scatter, and the powder particles can be heat-treated without contaminating the inside of the apparatus.

以上本発明をトナーの熱処理工程に用いる場合について
説明゛したが、本発明の熱処理装置はトナー以外の粉粒
体の熱処理を行う場合にも用いることができる。
Although the present invention has been described above with respect to the case where it is used in a toner heat treatment process, the heat treatment apparatus of the present invention can also be used when heat treating powder or granular materials other than toner.

〔発明の効果〕〔Effect of the invention〕

以上のように、本発明は、粉粒体を気流中で熱処理する
熱処理装置であって、粉粒体の分散気流を旋回せしめる
旋回機構と、この旋回機構よりの旋回された粉粒体の分
散気流を加熱する加熱機構とを有し、前記旋回機構は、
分散気流を吐出する旋回ノズルと、この鯵回ノズルの内
方に拡散用気流を供給する拡散用気流供給機構とを具え
てなることを特徴とする熱処理装置であるから、粉粒体
の分散気流は旋回ノズルの内部において旋回しながら拡
散用気流により乱されて拡散されるようになるため、粉
粒体が小さな密度で良好に分散された状態で旋回ノズル
から吐出されるようになる。
As described above, the present invention provides a heat treatment apparatus for heat-treating powder and granular materials in an air stream, which includes a swirling mechanism for swirling an airflow for dispersing powder and granular materials, and a dispersion of the swirled powder and granular materials by the swirling mechanism. and a heating mechanism that heats the airflow, and the swirling mechanism includes:
The heat treatment apparatus is characterized by comprising a swirling nozzle that discharges a dispersion airflow, and a diffusion airflow supply mechanism that supplies the dispersion airflow to the inside of the swirling nozzle. The particles are swirled inside the swirling nozzle and are disturbed and diffused by the diffusion airflow, so that the powder particles are discharged from the swirling nozzle in a well-dispersed state with a small density.

従って熱処理においてiよ粉粒体同意の凝着による粗大
化が抑制され、結局小径で粒径の揃った粒子粉末を高い
収率で得ることができる。
Therefore, during the heat treatment, coarsening due to cohesion of the powder particles is suppressed, and as a result, particles with small diameters and uniform particle sizes can be obtained at a high yield.

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

第1図は本発明熱処理装置の一実施例を概略的に示す説
明図、第2図及び第3図はそれぞれ旋回機構の要部を拡
大して示す説明用縦断正面図及び説明用底面図である。 1・・・熱処理用容器   2・・・旋回機構3・・・
加熱機構     4・・・冷却風供給機構5・・・サ
イクロン    6・・・集塵機7・・・排気機構  
   21・・・エゼクタ部22・・・旋回部    
  23・・・圧縮気流導入口24・・・供給口   
   25・・・混合室26・・・スロート部    
27・・・旋回室28・・・旋回ノズル    29・
・・拡散用気流供給機構30・・・拡散用気流ノズル 
31・・・送気部     ′32・・・ヒータ一部 
   33・・・加熱気流導入部34・・・整流部
FIG. 1 is an explanatory diagram schematically showing an embodiment of the heat treatment apparatus of the present invention, and FIGS. 2 and 3 are an explanatory longitudinal sectional front view and an explanatory bottom view, respectively, showing enlarged main parts of the turning mechanism. be. 1... Heat treatment container 2... Rotating mechanism 3...
Heating mechanism 4... Cooling air supply mechanism 5... Cyclone 6... Dust collector 7... Exhaust mechanism
21...Ejector part 22...Swivel part
23... Compressed air flow introduction port 24... Supply port
25...Mixing chamber 26...Throat part
27... Turning chamber 28... Turning nozzle 29.
...Diffusion airflow supply mechanism 30...Diffusion airflow nozzle
31... Air supply section '32... Part of the heater
33... Heated air flow introduction section 34... Rectification section

Claims (1)

【特許請求の範囲】 1)粉粒体を気流中で熱処理する熱処理装置であって、 粉粒体の分散気流を旋回せしめる旋回機構と、この旋回
機構よりの旋回された粉粒体の分散気流を加熱する加熱
機構とを有し、 前記旋回機構は、分散気流を吐出する旋回ノズルと、こ
の旋回ノズルの内方に拡散用気流を供給する拡散用気流
供給機構とを具えてなることを特徴とする熱処理装置。 2)加熱機構は、旋回ノズルの開口の外周から加熱気流
を導入する加熱気流導入部を有することを特徴とする特
許請求の範囲第1項記載の熱処理装置。
[Scope of Claims] 1) A heat treatment device for heat-treating powder and granular material in an air stream, comprising: a swirling mechanism that swirls an airflow dispersing the powder and granular material; and a dispersion airflow of the powder and granular material swirled by the swirling mechanism. a heating mechanism that heats the air, and the swirling mechanism includes a swirling nozzle that discharges a dispersed airflow, and a diffusion airflow supply mechanism that supplies a diffusion airflow to the inside of the swirling nozzle. Heat treatment equipment. 2) The heat treatment apparatus according to claim 1, wherein the heating mechanism has a heated air flow introduction section that introduces the heated air flow from the outer periphery of the opening of the rotating nozzle.
JP60090946A 1985-04-30 1985-04-30 Heat treatment device Pending JPS61249711A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60090946A JPS61249711A (en) 1985-04-30 1985-04-30 Heat treatment device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60090946A JPS61249711A (en) 1985-04-30 1985-04-30 Heat treatment device

Publications (1)

Publication Number Publication Date
JPS61249711A true JPS61249711A (en) 1986-11-06

Family

ID=14012629

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60090946A Pending JPS61249711A (en) 1985-04-30 1985-04-30 Heat treatment device

Country Status (1)

Country Link
JP (1) JPS61249711A (en)

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