JPS588522A - Method and apparatus for refining powder - Google Patents
Method and apparatus for refining powderInfo
- Publication number
- JPS588522A JPS588522A JP56107338A JP10733881A JPS588522A JP S588522 A JPS588522 A JP S588522A JP 56107338 A JP56107338 A JP 56107338A JP 10733881 A JP10733881 A JP 10733881A JP S588522 A JPS588522 A JP S588522A
- Authority
- JP
- Japan
- Prior art keywords
- hole
- filter
- powder
- filtration filter
- raw material
- 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
Links
Landscapes
- Filtration Of Liquid (AREA)
Abstract
Description
【発明の詳細な説明】 置に関するものである。[Detailed description of the invention] It's about location.
従来、粉体を精製する方法として、ソックスレー抽出方
法がパ知られている。この方法は、濾過フイルタを設け
た容器に原料粉体を入れ、これを最下方連通管に接続し
、この最下方連通管の注液孔よりf方に一方の孔を設け
、最下方連通管の上方に他方の孔を設けた蒸気上昇通路
を接続し、この蒸気上昇通路の上方の孔よりも上方に冷
却部を有し、蒸気上昇通路の下方の孔よりも下方に液部
を設けた装置において、液部を加熱して蒸発した液体を
蒸気上昇通路より冷却部に導びき、この冷却部で冷却し
、この冷却された液体で粉体を洗浄して連通管から排出
するもので、高純度の洗浄液で繰り返し粉体の精−を行
なっている。Conventionally, the Soxhlet extraction method has been known as a method for refining powder. In this method, raw material powder is placed in a container equipped with a filtration filter, connected to the lowest communicating pipe, one hole is provided in the direction f from the liquid injection hole of this lowest communicating pipe, and the lowest communicating pipe is A steam rising passage with another hole provided above is connected, a cooling part is provided above the hole above the steam rising passage, and a liquid part is provided below the hole below the steam rising passage. In the device, the liquid part is heated and the evaporated liquid is guided to the cooling part through the vapor rising passage, cooled in this cooling part, and the powder is washed with the cooled liquid and discharged from the communication pipe. The powder is repeatedly cleaned using a high-purity cleaning solution.
しかしながら、この方法はバッチ方式であるため、粉体
の供給、取出し及び装置の組立て準備を1回の精製ごと
に行なう必要があり、従って、この方法では、1つの装
置で原料供給から排液工程までの精製を一環して得るこ
とはできず、更に攪拌工程がないために、一定洗浄液量
当りの精製効率が悪いという欠点があり、精製のバラツ
キが大きいという欠点があった。However, since this method is a batch method, it is necessary to perform powder supply, removal, and equipment assembly preparation for each purification process. Furthermore, since there is no stirring step, there is a drawback that the purification efficiency per fixed amount of washing liquid is low, and there is a large variation in purification.
本発明は、上記従来例の欠点を解消するために、−原料
供給工程、洗浄溶剤注入工程、攪拌工程、排液工程、乾
燥工程、粉砕工程、粉体取出し工程を一環して行なうこ
とを特徴とし、その目的は精製の度ごとに装置の組立準
備を必要とせず、かつ攪拌工程の採用により一定洗浄液
量当りの精製効率が良く、即ち同一純度を得るために従
来方法より供給洗浄液量が少なくて済み、均一な精製が
行なえる粉体精製方法及び装置を提供するものである。In order to eliminate the drawbacks of the conventional example, the present invention is characterized in that - raw material supply process, cleaning solvent injection process, stirring process, draining process, drying process, pulverization process, and powder removal process are carried out in one step. The purpose of this method is to eliminate the need to assemble and prepare equipment for each purification process, and to achieve high purification efficiency per fixed amount of washing liquid by using a stirring process.In other words, to obtain the same purity, the amount of washing liquid supplied is smaller than with conventional methods. The purpose of the present invention is to provide a powder refining method and apparatus that can perform uniform refining without having to perform the following steps.
以下、図面により実施例を詳細に説明する。Hereinafter, embodiments will be described in detail with reference to the drawings.
図は、本発明の一実施例の装置の概略構成を示した図で
、1は中空容器、2は中空容器1の内部を上下に分割す
るフィルタ取付部1′で装置された濾過フィルタ、3は
中空容器lの頂部に設けられたシャフト挿入孔4から挿
入されたシャフト3′の先端に設けられたプロペラ、S
は中空容器1の上部の側壁に設けられ、開、閉手段5′
を持つ第1の孔、6は第1の孔5より上部の側壁に設け
られ、開閉手段6′を持つ第2の孔、マは濾過フィルタ
2の上部に接して中空容器1の側壁に設けられ、開閉手
段ゲを持つ第3の孔、8は濾過フィルタ2より下部の側
壁に設けられ、開閉手段8′を有jる第4の孔、9は中
空容器1の底部に設けられ、開閉手段9′を持つ排液孔
であり、中空容器1は使用する溶剤により腐食やその他
の反応あるいは膨潤等の化学的または物理的改質を起こ
さず、粉体供給から粉体取出し工程までの操作工程にお
ける条件変化に対して充分な物理的強度を保ち得る材料
で、密着シール性が良く、気液洩れの生じ難い材料であ
れば、全て使用することができる。これらの材料黄銅等
の金属、テフロン内装金属のような複合材料等がある。The figure shows a schematic configuration of an apparatus according to an embodiment of the present invention, in which 1 is a hollow container, 2 is a filtration filter installed at a filter attachment part 1' that divides the interior of the hollow container 1 into upper and lower parts, and 3 S is a propeller provided at the tip of a shaft 3' inserted from a shaft insertion hole 4 provided at the top of a hollow container L;
is provided on the upper side wall of the hollow container 1, and an opening/closing means 5'
A first hole 6 having an opening/closing means 6' is provided in the side wall above the first hole 5, and a second hole 6 having an opening/closing means 6' is provided in the side wall of the hollow container 1 in contact with the upper part of the filter 2. A third hole 8 having an opening/closing means is provided on the side wall below the filtration filter 2, and a fourth hole 9 having an opening/closing means 8' is provided at the bottom of the hollow container 1 and has an opening/closing means 8'. The hollow container 1 is provided with a drainage hole having a means 9', and the hollow container 1 does not undergo chemical or physical modification such as corrosion or other reactions or swelling due to the solvent used, and can be operated from the powder supply to the powder removal process. Any material can be used as long as it maintains sufficient physical strength against changes in process conditions, has good sealing properties, and is resistant to gas-liquid leakage. These materials include metals such as brass and composite materials such as Teflon-coated metal.
このように構成した本実施例の装置では、まず第1の孔
5から原料が供給され、第4の孔8から洗浄溶剤が注入
され、シャフト3′に接続されたプロペラ3で攪拌しな
がら洗浄する。一定時間洗浄後、中空容器1の底部に設
けられた第5の孔9から洗浄溶剤を排出する。この洗浄
溶剤を排出後、第5の孔9を通して減圧しながら第2の
孔6より加熱された気体を送り込み、またプロペラ3で
原料を攪拌しながら乾燥する。またこの乾燥を行なって
いる時、プロペラ3で原料を攪拌しながら粉砕する。こ
の乾燥粉砕を一定時間行なった後、第3の孔〒より精製
された粉体を取・り出す。In the apparatus of this embodiment configured in this way, the raw material is first supplied through the first hole 5, the cleaning solvent is injected through the fourth hole 8, and the cleaning solvent is stirred by the propeller 3 connected to the shaft 3'. do. After cleaning for a certain period of time, the cleaning solvent is discharged from the fifth hole 9 provided at the bottom of the hollow container 1. After discharging this cleaning solvent, heated gas is fed through the second hole 6 while reducing the pressure through the fifth hole 9, and the raw material is dried while being stirred by the propeller 3. Further, during this drying, the raw material is pulverized while being stirred by the propeller 3. After this dry pulverization is carried out for a certain period of time, the purified powder is taken out from the third hole.
以上のように、各工程を繰り返し行なうことにより、均
一に精製された粉体を取り出すことができる。また、上
記の工程において、原料を供給した後の洗浄溶剤の注入
、プロペラによる攪拌、洗浄溶剤の排出のみを繰り返す
ことにより、より精製された粉体を取りなすことができ
る。As described above, by repeating each step, uniformly purified powder can be taken out. Further, in the above process, by repeating only the injection of the cleaning solvent after supplying the raw materials, stirring by a propeller, and discharge of the cleaning solvent, a more refined powder can be obtained.
なお、原料の供給は中空容器lを減圧して供給すること
が望ましく、この減圧は第5の孔9を通して行なうこと
ができる。また洗浄溶剤は加圧してぶ入してもよいし、
−中空容器1内を減圧して注入してもよい。液量の制御
は中空容器1が透明であれば、目視制御が可舞であるが
、中空容器1の所望の位置にセンサ(温度、電流、液圧
等)を設けて検知、制御すればよい。また精製効率や精
度のバラツキは攪拌が原因することが多いが、これはモ
ータによる回転数及びプロペラ3の形状により制御する
ことができる。更に、第5の孔9がらの排液は減圧下で
行なうことにより、より作業を早く行なうことができる
。乾燥工程では、第2の孔6より気体を送り込み、第5
の孔9から減圧しながら乾、燥を行なうが、乾燥速度を
向上させるために、気体は加熱されていることが望まし
く、また粉体の液化を防止するために、気体は02やC
O2を除いたN2などの使用が望ましい。また粉砕工程
中の粉砕効率や精度はモータによるシャフト3′の回転
数やプロペラの形状で制御することができ、またこの工
程では、粉体の熱反応を防止するため、気体は加熱され
ず、不活性であることが望ましい。Note that it is desirable to supply the raw material by reducing the pressure in the hollow container 1, and this pressure reduction can be performed through the fifth hole 9. Additionally, the cleaning solvent may be introduced under pressure.
- The inside of the hollow container 1 may be depressurized and injected. If the hollow container 1 is transparent, the liquid volume can be controlled visually, but it is also possible to detect and control the amount by installing a sensor (temperature, current, liquid pressure, etc.) at a desired position in the hollow container 1. . Further, variations in purification efficiency and accuracy are often caused by stirring, but this can be controlled by the rotation speed of the motor and the shape of the propeller 3. Furthermore, by draining the liquid from the fifth hole 9 under reduced pressure, the work can be carried out more quickly. In the drying process, gas is sent through the second hole 6 and the fifth
Drying is performed while reducing the pressure from the hole 9 of the powder.In order to improve the drying speed, it is desirable that the gas be heated, and in order to prevent the powder from liquefying, the gas should be heated.
It is desirable to use N2, etc., excluding O2. Furthermore, the crushing efficiency and accuracy during the crushing process can be controlled by the rotation speed of the shaft 3' by the motor and the shape of the propeller.In addition, in this process, the gas is not heated to prevent thermal reactions of the powder. Preferably inert.
更に、粉体を取り出すには、第3の孔7を通して減圧し
ながら、第2の孔6より加熱されない不活性気体を送風
して行なわれる。またフィルタ2は所定の時間使用した
後、中空容器1のフィルタ板付部1を外して交換される
。Furthermore, the powder is taken out by blowing unheated inert gas through the second hole 6 while reducing the pressure through the third hole 7. Further, after the filter 2 has been used for a predetermined period of time, the filter plate attaching portion 1 of the hollow container 1 is removed and the filter 2 is replaced.
以上説明したように、本発明によれば、原料供給工程、
洗浄溶剤注入工程、攪拌工程、排液工程、乾燥工程、粉
砕工程、粉体取出し工程を順次行なうことにより、精製
された粉体を効率よく、−環した操作で行なうことがで
き、更に上記工程において、′洗浄溶剤注入工程、攪拌
工程、排液工程のみを繰り返すこ7とにより、より精製
された粉体を取り出すことができる。 。As explained above, according to the present invention, the raw material supply step,
By sequentially performing the cleaning solvent injection step, stirring step, draining step, drying step, pulverization step, and powder removal step, the purified powder can be efficiently processed in a circular operation, and the above steps can be carried out efficiently. In step 7, by repeating only the washing solvent injection step, stirring step, and draining step 7, more purified powder can be taken out. .
図は、本発明の一実施例の装置の概略構成図である。
1・・・中空容器、2・・・濾過フィルタ、3・・・プ
ロペラ、3・・・シャフト、4・・・シャフト挿入孔、
5・・・第1の孔、6・・・第2の孔、7・・・第3の
孔、8・・・第4の孔、9・・・第5の孔、5′、6′
、7′、8′、9′・・・開閉手段。
特許出願人 株式会社 リ コ −The figure is a schematic configuration diagram of an apparatus according to an embodiment of the present invention. 1... Hollow container, 2... Filtration filter, 3... Propeller, 3... Shaft, 4... Shaft insertion hole,
5...First hole, 6...Second hole, 7...Third hole, 8...Fourth hole, 9...Fifth hole, 5', 6'
, 7', 8', 9'... opening/closing means. Patent applicant Rico Co., Ltd. −
Claims (3)
、ルタの上部に設けられた第1、第2、第3の孔と前記
濾過フィルタの下部に設けられた第4、第5の孔と、前
記濾過フィルタの上部に設けられた攪拌翼を有する中空
容器において、前記濾過フィルタの上方の前記第1の孔
からの原料供給工程と、前記済過フィルタの下方の前記
第4の孔からの洗浄溶剤注入工程と、前記攪拌翼による
攪拌工程と、前記濾過フィルタの下方の前記第5の孔か
らの洗浄後溶剤の排液工程と、前記濾過フィルタの上方
の第2の孔からの送風と前記排液工程を継続することに
よる乾燥工程と、前記排液工程と前記乾燥工程における
攪拌工程継続による粉砕工程と、前記濾過フィルタの上
部に接する第3の孔からの粉体取出し工程とを順次行な
うことを特徴とする粉体精製方法。(1) A filtration filter is provided inside, and the filtration filter has first, second, and third holes provided at the top of the filter, and fourth and fifth holes provided at the bottom of the filtration filter. , in a hollow container having a stirring blade provided above the filtration filter, a step of supplying the raw material from the first hole above the filtration filter, and a step of supplying the raw material from the fourth hole below the filtration filter; a cleaning solvent injection step, a stirring step using the stirring blade, a draining step of the post-cleaning solvent from the fifth hole below the filtration filter, and an air blowing step from the second hole above the filtration filter. A drying process by continuing the liquid draining process, a pulverizing process by continuing the stirring process in the liquid draining process and the drying process, and a powder extraction process from the third hole in contact with the upper part of the filtration filter are sequentially performed. A powder refining method characterized by:
攪拌工程、前記洗浄後溶剤の排液工程を繰り返し順次行
なうことを特徴とする特許請求の範囲第1項記載の粉体
精製方法。(2) The powder refining method according to claim 1, wherein in the step, the washing solvent injection step, the stirring step, and the post-washing solvent draining step are repeatedly performed in sequence.
該フィルタの上部に設けられた攪拌翼と、前記中空容器
の上部側壁に設けられた開閉手段を有する気体送風孔と
、該気体送風孔より下方の側壁に対向して設けられた開
閉手段を有する原料供給孔と、前記フィルタの上部に接
し“て側壁に設けられた粉体取出し孔と、前記フィルタ
の下部の前記粉体取出し孔に対向する側壁に設けられた
開閉手段を有する注液孔と、前記中空容器の底部に鰻け
た開閉手段を有する排液孔とからなる粉体精製装置。(3) a filter provided near the middle part of the hollow container;
A stirring blade provided at the upper part of the filter, a gas blowing hole having an opening/closing means provided on the upper side wall of the hollow container, and an opening/closing means provided opposite to the side wall below the gas blowing hole. a raw material supply hole, a powder extraction hole provided on a side wall in contact with the upper part of the filter, and a liquid injection hole having an opening/closing means provided on a side wall opposite to the powder extraction hole at the lower part of the filter. A powder refining device comprising: a drain hole having an opening/closing means provided at the bottom of the hollow container;
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP56107338A JPS588522A (en) | 1981-07-09 | 1981-07-09 | Method and apparatus for refining powder |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP56107338A JPS588522A (en) | 1981-07-09 | 1981-07-09 | Method and apparatus for refining powder |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS588522A true JPS588522A (en) | 1983-01-18 |
Family
ID=14456515
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP56107338A Pending JPS588522A (en) | 1981-07-09 | 1981-07-09 | Method and apparatus for refining powder |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS588522A (en) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS61245807A (en) * | 1985-02-15 | 1986-11-01 | グラッソス コニンクリイケ マシネファブリィケン ナ−ムロ−ゼ フェンノ−トチャップ | Device and method for separating solid particle from liquid suspension and/or purifying or lixiviating solid particle |
JPS62156310U (en) * | 1986-03-25 | 1987-10-05 | ||
US9808595B2 (en) | 2007-08-07 | 2017-11-07 | Boston Scientific Scimed, Inc | Microfabricated catheter with improved bonding structure |
US9901706B2 (en) | 2014-04-11 | 2018-02-27 | Boston Scientific Scimed, Inc. | Catheters and catheter shafts |
CN108905323A (en) * | 2018-07-28 | 2018-11-30 | 赣州市翔义科技有限公司 | A kind of coating filtering device convenient for improving discharging efficiency |
US10207077B2 (en) | 2003-03-27 | 2019-02-19 | Boston Scientific Scimed, Inc. | Medical device |
-
1981
- 1981-07-09 JP JP56107338A patent/JPS588522A/en active Pending
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS61245807A (en) * | 1985-02-15 | 1986-11-01 | グラッソス コニンクリイケ マシネファブリィケン ナ−ムロ−ゼ フェンノ−トチャップ | Device and method for separating solid particle from liquid suspension and/or purifying or lixiviating solid particle |
JPS62156310U (en) * | 1986-03-25 | 1987-10-05 | ||
US10207077B2 (en) | 2003-03-27 | 2019-02-19 | Boston Scientific Scimed, Inc. | Medical device |
US9808595B2 (en) | 2007-08-07 | 2017-11-07 | Boston Scientific Scimed, Inc | Microfabricated catheter with improved bonding structure |
US9901706B2 (en) | 2014-04-11 | 2018-02-27 | Boston Scientific Scimed, Inc. | Catheters and catheter shafts |
CN108905323A (en) * | 2018-07-28 | 2018-11-30 | 赣州市翔义科技有限公司 | A kind of coating filtering device convenient for improving discharging efficiency |
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