JPS6031838A - Semi-wet finely crushing machine - Google Patents

Semi-wet finely crushing machine

Info

Publication number
JPS6031838A
JPS6031838A JP14208883A JP14208883A JPS6031838A JP S6031838 A JPS6031838 A JP S6031838A JP 14208883 A JP14208883 A JP 14208883A JP 14208883 A JP14208883 A JP 14208883A JP S6031838 A JPS6031838 A JP S6031838A
Authority
JP
Japan
Prior art keywords
classification section
airflow
nozzle
agglomeration
pulverized
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
JP14208883A
Other languages
Japanese (ja)
Inventor
宏 坂本
満 山本
薫 増田
四元 弘毅
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.)
National Institute of Advanced Industrial Science and Technology AIST
Original Assignee
Agency of Industrial Science and Technology
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 Agency of Industrial Science and Technology filed Critical Agency of Industrial Science and Technology
Priority to JP14208883A priority Critical patent/JPS6031838A/en
Publication of JPS6031838A publication Critical patent/JPS6031838A/en
Pending legal-status Critical Current

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Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 機能性材料に関連して、物理的あるいは化学的に多様な
特性をもつ微粒子が、エレクト四二りス素材、ファイン
セラミックスなど各方面で重要視されつつある。
DETAILED DESCRIPTION OF THE INVENTION In relation to functional materials, fine particles having various physical or chemical properties are becoming important in various fields such as electrified materials and fine ceramics.

この発明はこのようなニーズに応えるための微粉砕機に
関するものである。
The present invention relates to a pulverizer that meets these needs.

従来の高速気流を利用した粉砕機においては構成されに
くかった。
It was difficult to construct a conventional crusher using high-speed airflow.

この発明は高速気流を利′用して粉砕した産物の1部を
凝集還流して粉砕産物の滞留時間を長く取り、粉砕産物
を微粉化することをねらいとしている0 この発明を図面にもとづいて説明すると、第1図におい
て、半湿式微粉砕機本体は大きくわけて粉砕部1と凝集
分級部2から構成される。粉砕部には円筒型の粉砕室3
の内部に圧縮気体を導入するノズル4を粉砕室の側壁に
配置し4.そのノズルの方向を粉砕室内に設けた気流上
昇ロート5の円周に接するように固定する。また、粉砕
室の各ノズルの上方に試料供給装置6を設は供給された
試料を各ノズルの高速気流に乗せるようにする。凝集分
級部は円筒部7と円錐部8とを連設して密閉構造に形成
し、上記円筒部に噴霧状の気流を圧入する気流導入口9
を設は気流を接線方向に導入し、該凝集分級部内で粉砕
産物の粗粒部分を凝集および微粒部分を分級せしめ、そ
れぞれ凝集物は凝集分級部と粉砕室の境界部に設けた粗
粒子戻しロート(兼気流上昇ロート)5に沿って粉砕室
に戻し再び粉砕する。また、微粉は凝集分級部上部に設
けた気流上昇管10より排出され捕集される。
This invention aims to pulverize a part of the pulverized product by coagulating and refluxing a part of the pulverized product using high-speed airflow, thereby increasing the residence time of the pulverized product and pulverizing the pulverized product. To explain, in FIG. 1, the main body of a semi-wet type pulverizer is broadly divided into a crushing section 1 and an agglomeration/classification section 2. The crushing section has a cylindrical crushing chamber 3.
4. A nozzle 4 for introducing compressed gas into the interior of the grinding chamber is arranged on the side wall of the grinding chamber. The direction of the nozzle is fixed so as to be in contact with the circumference of the airflow ascending funnel 5 provided in the grinding chamber. Further, a sample supply device 6 is provided above each nozzle in the grinding chamber so that the supplied sample is carried on the high-speed airflow of each nozzle. The aggregation and classification section has a cylindrical section 7 and a conical section 8 arranged in series to form a sealed structure, and an air flow inlet 9 for pressurizing a spray-like air flow into the cylindrical section.
The airflow is introduced in the tangential direction to agglomerate the coarse particles and classify the fine particles of the pulverized product in the agglomeration and classification section, and the agglomerates are returned to the coarse particle return provided at the boundary between the agglomeration and classification section and the grinding chamber. It is returned to the grinding chamber along the funnel (also known as an airflow ascending funnel) 5 and is ground again. Further, the fine powder is discharged and collected from the airflow riser pipe 10 provided above the agglomeration and classification section.

この発明はノズルから高速気流を円筒の中心方向に集め
、粉砕室上部の試料供給装置から供給された砕料を高速
で衝突させて粉砕するものである。
In this invention, a high-speed airflow is collected from a nozzle toward the center of a cylinder, and the crushed material supplied from a sample supply device in the upper part of the crushing chamber is collided with the sample at high speed to be crushed.

粉砕された砕料は上昇気流に乗り気流上昇ロートによっ
て凝集分級部に導びかれる。凝集分級部においては上昇
気流導入口より噴霧気流を圧入して凝集分級部内に旋回
流を作り、粉砕された粉砕産物を遠心効果を利用して分
級する。凝集分級部において、粗粒部分は遠心力により
凝集分級部の側壁方向に押し出される。また、噴霧気流
中の水滴も遠心力を受け粗粒部分と同じように側壁方向
に押しやられるので、粗粒部分はこの過程で凝集し、さ
らに大粒子とな>〕側携を伝わり下方へ落ち粗粒子戻し
ロー1に沿って粉砕室に還流され、再び粉砕される。ま
た、微粒部分は遠心効果にあまり左右されず、中心に集
まり、上昇気流に乗って凝集□分級の上部に付設された
気流上昇管より糸外に排出され、捕集装置によって回収
される。
The pulverized material rides on the updraft and is guided to the aggregation and classification section by the airflow ascending funnel. In the aggregation and classification section, a spray airflow is forced into the updraft inlet to create a swirling flow in the aggregation and classification section, and the pulverized products are classified using the centrifugal effect. In the agglomeration and classification section, the coarse particles are pushed out toward the side wall of the aggregation and classification section by centrifugal force. In addition, the water droplets in the spray airflow are also subjected to centrifugal force and are pushed toward the side wall in the same way as the coarse particles, so the coarse particles aggregate during this process and become even larger particles. The particles are returned to the grinding chamber along the coarse particle return row 1 and ground again. In addition, the fine particles are not affected much by the centrifugal effect, gather at the center, ride the rising air current, are discharged out of the thread from the airflow riser pipe attached to the top of the agglomeration□ classifier, and are collected by the collection device.

以上説明したようにこの発明は高速気流を利用して粉砕
し、その粉砕産物の一部を凝集還流して微粒化するもの
である。
As explained above, the present invention utilizes high-speed airflow to pulverize, and a part of the pulverized product is coagulated and refluxed to atomize it.

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

半湿式微粉砕機の実施例を第1図及び第2図に示す。 以下に本装置の代表的な部分の説明を示す。 1粉砕部、2凝集分級部、3.粉砕室 本ノズル、5.気流上昇ロート、6.試料供給装置?0
円筒部、a円錐部、9.気流導入口10気流上昇管 特許出願人 工業技術院長 川 1)裕 部 5−
An example of a semi-wet type pulverizer is shown in FIGS. 1 and 2. Below is a description of typical parts of this device. 1 crushing section, 2 agglomeration and classification section, 3. Grinding chamber main nozzle, 5. Airflow ascending funnel, 6. Sample supply device? 0
Cylindrical part, a conical part, 9. Airflow introduction port 10 Airflow riser pipe Patent applicant: Director of the Agency of Industrial Science and Technology Kawa 1) Yube 5-

Claims (3)

【特許請求の範囲】[Claims] (1) 円筒型の粉砕室の側壁に圧縮気体を導入するノ
ズルを中心方向に向けて配置し、そのノズルから凝集分
級部の気体上昇管の円周に対して接する方向に気体を導
入して、粉砕室上方で且つ各ノズルの上方に付けた試料
供給装置より供給された試料を高速気流に乗せて粉砕す
る装置。
(1) A nozzle for introducing compressed gas is arranged on the side wall of the cylindrical crushing chamber, facing toward the center, and the gas is introduced from the nozzle in a direction tangent to the circumference of the gas riser pipe of the aggregation and classification section. A device that crushes the sample supplied from the sample supply device attached above the crushing chamber and above each nozzle by placing it on a high-speed airflow.
(2) 粉砕された試料粉末を凝集分級部に導入し、分
級部入口より噴霧状の気流を圧入して、粉砕産物の粗粒
部分を凝集及び微粒子の分級を同時に行なうことを特徴
とする特許請求の範囲第1項の装置。
(2) A patent characterized in that the pulverized sample powder is introduced into an agglomeration and classification section, and a spray-like airflow is forced into the inlet of the classification section to simultaneously agglomerate the coarse particles of the pulverized product and classify the fine particles. Apparatus according to claim 1.
(3) 凝集分級部と粉砕室の境界部に粉砕産物導入及
び凝集粒子並びに粗粒子戻しロートを付設することを特
徴とする特許請求の範囲第1項の装置。
(3) The apparatus according to claim 1, characterized in that a funnel for introducing pulverized products and for returning agglomerated particles and coarse particles is attached to the boundary between the agglomeration and classification section and the pulverization chamber.
JP14208883A 1983-08-03 1983-08-03 Semi-wet finely crushing machine Pending JPS6031838A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP14208883A JPS6031838A (en) 1983-08-03 1983-08-03 Semi-wet finely crushing machine

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP14208883A JPS6031838A (en) 1983-08-03 1983-08-03 Semi-wet finely crushing machine

Publications (1)

Publication Number Publication Date
JPS6031838A true JPS6031838A (en) 1985-02-18

Family

ID=15307146

Family Applications (1)

Application Number Title Priority Date Filing Date
JP14208883A Pending JPS6031838A (en) 1983-08-03 1983-08-03 Semi-wet finely crushing machine

Country Status (1)

Country Link
JP (1) JPS6031838A (en)

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5784756A (en) * 1980-11-13 1982-05-27 Hosokawa Micron Kk Air current type crusher

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5784756A (en) * 1980-11-13 1982-05-27 Hosokawa Micron Kk Air current type crusher

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