JPS6038028A - Instantaneous mixing method of particulate material and liquid - Google Patents

Instantaneous mixing method of particulate material and liquid

Info

Publication number
JPS6038028A
JPS6038028A JP58145561A JP14556183A JPS6038028A JP S6038028 A JPS6038028 A JP S6038028A JP 58145561 A JP58145561 A JP 58145561A JP 14556183 A JP14556183 A JP 14556183A JP S6038028 A JPS6038028 A JP S6038028A
Authority
JP
Japan
Prior art keywords
cyclone chamber
liquid
particulate materials
powder
charged
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
JP58145561A
Other languages
Japanese (ja)
Inventor
Masatoshi Kawano
川野　正敏
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP58145561A priority Critical patent/JPS6038028A/en
Publication of JPS6038028A publication Critical patent/JPS6038028A/en
Pending legal-status Critical Current

Links

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/10—Mixing by creating a vortex flow, e.g. by tangential introduction of flow components

Abstract

PURPOSE:To make it possible to perform instantaneous mixing, by charging two kinds or more of airborn particulate materials into a cyclone chamber along with carrier air from a tangential direction to revolve the same in a floated state. CONSTITUTION:Particulate materials are transported to a cylindrical cyclone chamber 2 by air transport pipes 1, 1' and tangentially charged into the upper interior of the cyclone chamber 2 by nozzles 3, 3'. The charged particulate materials are subjected to revolving motion while floated in the air stream within the cyclone chamber 2 and gradually transferred to the lower part of the cyclone chamber 2. When the particulate materials are humidified by a liquid, a spray bozzle 4 is provided to a position lower than the particulate material spray nozzle 3 and water or a desired liquid is tangentially sprayed into the cyclone chamber 2 in a fine mist state from the spray nozzle 4.

Description

【発明の詳細な説明】 本弁明は気流輛送用能な直径２０χ桂艮以下の粉粒体を
１１こして混合あるいは加湿せしめる方法に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for mixing or humidifying powder or granular material having a diameter of 20×Kayen or less that can be passed through air flow.

本発明の目的は従来の混練タイプの加湿法に比べ嵐の大
小を間わず瞬時加湿でき、しかも水分比無人化でき、更
には粉粒体あるいは液体同志の櫨々の化量での混合も出
来るという新しい楕想による粉粒体、液体の瞬時混合方
法を提供せんとするものである。The purpose of the present invention is that compared to conventional kneading type humidification methods, it is possible to humidify instantly regardless of the size of a storm, and the moisture ratio can be controlled unattended, and furthermore, it is possible to mix powders, granules, or liquids in similar amounts. The purpose of this project is to provide a method for instant mixing powder, granular materials, and liquid based on a new elliptical concept.

この発明は空気輸送１ｉ（１）　、　（１）’ｆこよっ
て粉粒体を円鈴形すイクロン菟（２）まで気流権送し、
ノズ／ｌ／　ｅ１１＋　＜ｓｆによ゛りてサイクロン基
（２ンのｅ」部上方にクンゼンシャルに空気とともに投
入する。投入された粉粒体はサイクロン室（２）内を空
気流にの２で浮遊しながら旋回連動し、サイクロン室（
２）の１方に徐々に移行する。そのため窒気との接触面
積はその粒体、粉体の最大値を示す状態となっている。This invention uses pneumatic transport 1i (1), (1)'f to transport powder and granules to a circular cylinder (2),
The nozzle /l/e11+ <sf is used to inject the powder and granules into the cyclone chamber (2) above the e section with air. It rotates while floating, and the cyclone chamber (
Gradually shift to one of 2). Therefore, the area of contact with nitrogen gas is at its maximum value for the granules and powder.

次に液体と粉粒体を加湿する場合は噴島ノスル（旬を粉
粒体のノズル（３）より下位に設けて同噴霧ノズルより
水又は所望の液体を微細化しｔコ状態でサイクロン室（
２）ＰＪにタンセンシャルに噴霧する。尚水鳴襄の場合
噴霧粒子を微細にする為蒸気又はｈこの様にサイクロン
室、　（２）　Ｖ３にタンゼンシャルに投入された粒体
、粉体又は微細化された肢体粒子は互に最大の接触面積
を保らながら絢突、分散して瞬時に混合あるいは加湿で
きるものである。適正に配合あるいは加湿された粉体、
粒体、液体肴はサイクロン室（２）の土部排出シニート
（５）より排出さＪＬ、次工程へ移行する。Next, when humidifying liquid and granular material, install the Fujima nozzle (shun) below the powder nozzle (3), atomize water or the desired liquid from the same spray nozzle, and leave it in the cyclone chamber (
2) Spray tansentially on PJ. In the case of Shang Suimei, in order to make the spray particles finer, steam or a cyclone chamber is used in this way. It spreads and disperses while maintaining its surface area, allowing for instant mixing or humidification. Properly blended or humidified powder,
The granules and liquid appetizers are discharged from the cyclone chamber (2) through the soil outlet (5) and transferred to the next process.

ａｔ＋記次期工程において気流−送と加湿用液体の噴霧
に使用した堅気が不必要な場合はサイクロン室（２）円
のＰ」簡（６Ｊを経て空気のみ分組して大気又は適当な
機器へ排出する。又削記望気が次期工程において必要あ
るいは存在しても支障のない場合はサイクロン室（２）
内には内筒（６）は設置しなくてよい。If the air used for air flow and spraying of humidifying liquid is not needed in the at+recording process, the air should be separated through the cyclone chamber (2) (6J) and discharged to the atmosphere or to appropriate equipment. In addition, if the desired air is required in the next process or there is no problem with its existence, the cyclone room (2)
There is no need to install an inner cylinder (6) inside.

尚図中（７）、　（８月よ粉粒体気流輸送装置、（９〕
は粕水管である。In addition, (7) in the figure, (August, powder and granule pneumatic transport device, (9)
is Kasuzu pipe.

以上の様に本発明によれば下記の通りの優れｔζ効來を
得ることが出来る。As described above, according to the present invention, the following excellent tζ effect can be obtained.

（１）　従来の親線タイプの加ＩＭ器に比較してホの大
小を問わず瞬時加湿ができる。(1) Compared to conventional main wire type humidifiers, instant humidification is possible regardless of the size of the hole.

（２）　クローズドタイプの為非富に南生的である。(2) Because it is a closed type, it is southern in wealth.

（３）　加湿作業が無人でできる。(3) Humidification work can be done unattended.

（４）　水分比率は水８＋−ノズルの水魁調抑により自
由自在１こ友史できる。(4) The water ratio can be adjusted freely by adjusting the water ratio of the water 8+- nozzles.

（５）　加湿工程に機械作動部分がない為、メンテナン
スフリーである。(5) There are no mechanically moving parts in the humidification process, so it is maintenance-free.

（６）　本発明は粉粒体の加湿ばかりでなく二Ｓ類の粉
粒外同志あるいは二極類の散体同志の均−且つ瞬間的間
合も行える。(6) The present invention is capable of not only humidifying powder or granules, but also uniformly and instantaneously interspersing two S types of particles outside the powder or two polar types of dispersions.

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

第１因は本発明粉粒体、液体の一時混合方沃を示す説明
１、第２１はサイクロン室内部にお（）る粉粒体、液粒
子の運動を示す説明１である。The first factor is Explanation 1 showing the temporary mixing of the granular material and liquid of the present invention, and the 21st factor is Explanation 1 showing the movement of the granular material and liquid particles inside the cyclone chamber.

Claims (1)

【特許請求の範囲】[Claims] ｌ）少くとも二油以上の気体輸送された粉粒体又は微粒
化された液体を輔送気体とともに日向形サイクロン室内
にタンセンシャルに投入し、投入された粉粒体又は微細
化された液体をサイクロン室Ｐｊに浮遊状態に＆卸させ
て、粉粒体又は微粗化された液体同志を間合、崗英、分
散せしめて１８時に配合状態あるいは加湿状態にするこ
とを特徴とする粉粒体、液体のべ丙混合方法。l) At least two or more gas-transported powders or atomized liquids are tangentially charged into a sun-shaped cyclone chamber with a supporting gas, and the introduced powders or granules or atomized liquids are Powder and granule material is suspended and distributed in a cyclone chamber Pj, and the powder and granule material or finely coarsened liquid are separated, dispersed, and brought into a blended state or a humidified state at 6 p.m. , how to mix liquids.
JP58145561A 1983-08-08 1983-08-08 Instantaneous mixing method of particulate material and liquid Pending JPS6038028A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58145561A JPS6038028A (en) 1983-08-08 1983-08-08 Instantaneous mixing method of particulate material and liquid

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58145561A JPS6038028A (en) 1983-08-08 1983-08-08 Instantaneous mixing method of particulate material and liquid

Publications (1)

Publication Number Publication Date
JPS6038028A true JPS6038028A (en) 1985-02-27

Family

ID=15387986

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58145561A Pending JPS6038028A (en) 1983-08-08 1983-08-08 Instantaneous mixing method of particulate material and liquid

Country Status (1)

Country Link
JP (1) JPS6038028A (en)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4797001A (en) * 1986-07-30 1989-01-10 Mitsubishi Denki Kabushiki Kaisha Substrate bias generator for use in dynamic random access memory
JPH01112158A (en) * 1987-10-26 1989-04-28 Tokuyama Soda Co Ltd Production of insoluble carrier particle immobilized with antibody or antigen
US5158427A (en) * 1990-06-15 1992-10-27 Aisin Seiki Kabushiki Kaisha Centrifugal supercharger
US5207148A (en) * 1990-06-25 1993-05-04 Caffe Acorto, Inc. Automated milk inclusive coffee apparatus
WO1998016307A1 (en) * 1996-10-16 1998-04-23 Yasunobu Yoshida Method and apparatus for manufacturing chemical sub-substance by catalytic reaction and the like of reactive fluid
US6019497A (en) * 1995-04-20 2000-02-01 Valtion Teknillinen Tutkimuskeskus Mixing
JP2006001957A (en) * 2004-06-15 2006-01-05 Sumitomo Chemical Co Ltd Manufacturing process of polyolefin resin composition
US20150283780A1 (en) * 2012-10-09 2015-10-08 Ohio Blow Pipe Co. Wet cyclone dust filtration system

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5031471A (en) * 1973-07-21 1975-03-27

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5031471A (en) * 1973-07-21 1975-03-27

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4797001A (en) * 1986-07-30 1989-01-10 Mitsubishi Denki Kabushiki Kaisha Substrate bias generator for use in dynamic random access memory
JPH01112158A (en) * 1987-10-26 1989-04-28 Tokuyama Soda Co Ltd Production of insoluble carrier particle immobilized with antibody or antigen
JPH07111434B2 (en) * 1987-10-26 1995-11-29 株式会社トクヤマ Method for producing insoluble carrier particles on which antibody or antigen is immobilized
US5158427A (en) * 1990-06-15 1992-10-27 Aisin Seiki Kabushiki Kaisha Centrifugal supercharger
US5207148A (en) * 1990-06-25 1993-05-04 Caffe Acorto, Inc. Automated milk inclusive coffee apparatus
US5509349A (en) * 1990-06-25 1996-04-23 Caffe Acorto, Inc. Beverage valve venturi apparatus
US6019497A (en) * 1995-04-20 2000-02-01 Valtion Teknillinen Tutkimuskeskus Mixing
WO1998016307A1 (en) * 1996-10-16 1998-04-23 Yasunobu Yoshida Method and apparatus for manufacturing chemical sub-substance by catalytic reaction and the like of reactive fluid
GB2337009B (en) * 1996-10-16 2001-04-11 Yoshida Yasunobu Method and apparatus for manufacturing chemical sub-substance by catalytic reaction and the like of reactive fluid
JP2006001957A (en) * 2004-06-15 2006-01-05 Sumitomo Chemical Co Ltd Manufacturing process of polyolefin resin composition
US20150283780A1 (en) * 2012-10-09 2015-10-08 Ohio Blow Pipe Co. Wet cyclone dust filtration system
US9815252B2 (en) * 2012-10-09 2017-11-14 Ohio Blow Pipe Co. Wet cyclone dust filtration system

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