JPH06328002A - Precipitation classifying method and apparatus therefor - Google Patents
Precipitation classifying method and apparatus thereforInfo
- Publication number
- JPH06328002A JPH06328002A JP12574393A JP12574393A JPH06328002A JP H06328002 A JPH06328002 A JP H06328002A JP 12574393 A JP12574393 A JP 12574393A JP 12574393 A JP12574393 A JP 12574393A JP H06328002 A JPH06328002 A JP H06328002A
- Authority
- JP
- Japan
- Prior art keywords
- classified
- classification
- liquid
- classification tank
- tank
- 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.)
- Granted
Links
Landscapes
- Separation Of Solids By Using Liquids Or Pneumatic Power (AREA)
Abstract
(57)【要約】
【目的】 細胞塊等のように生育段階毎に種々の群が存
在する被分級物を多群に、かつ多量に分級できる沈降式
分級方法及び装置の提供を目的としている。
【構成】 軸方向が水平に配置された円筒状の分級槽4
の下部軸方向に複数の仕切部6を配列する。分級槽4の
一方の開口部端に、上部が一定の高さに保たれ、下部が
外方に向かって斜めに立ち上がり、先端部が開口した第
1の斜円錐状管路2を接続する。分級槽4の他方の開口
部端に、下部が一定の高さに保たれ、上部が外方に向か
って斜めに立ち下がり、先端部が開口した第2の斜円錐
状管路10を接続する。第1の斜円錐管路2の先端部2
aから被分級物の混入液体を流入させ、第2の斜円錐管
路10の先端部10aから液体を流出させ、被分級物の
落下する終端速度の差により被分級物を仕切部6に分級
するようにした。
(57) [Summary] [Purpose] It is an object of the present invention to provide a sedimentation-type classification method and apparatus capable of classifying a large number of classified substances having various groups such as cell clumps at each growth stage into a large number. . [Structure] Cylindrical classification tank 4 arranged axially horizontally
A plurality of partition portions 6 are arranged in the lower axial direction of. The first inclined conical pipe line 2 whose upper portion is kept at a constant height and whose lower portion rises obliquely outward and whose front end portion is open is connected to one opening end of the classification tank 4. At the other opening end of the classification tank 4, a second inclined conical pipe line 10 whose lower part is kept at a constant height and whose upper part is inclined downward toward the outside and whose front end is open is connected. . Tip 2 of the first oblique conical conduit 2
The mixed liquid of the object to be classified flows in from a, the liquid flows out from the tip portion 10a of the second oblique conical conduit 10, and the object to be classified is classified into the partition part 6 due to the difference in the terminal speed of the falling of the object to be classified. I decided to do it.
Description
【0001】[0001]
【産業上の利用分野】本発明は、沈降式分級方法及び装
置に係り、詳しくは液体中に混入された被分級物の終端
速度の差を利用して、多種類の分級物を多量に分級する
沈降式分級方法及び装置に関し、特に細胞塊等の分級に
好適な沈降式分級方法及び装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a settling type classification method and apparatus, and more particularly, to classify many kinds of classified materials in large quantities by utilizing the difference in terminal speed of classified objects mixed in a liquid. The present invention relates to a sedimentation-type classification method and device, particularly to a sedimentation-type classification method and device suitable for classification of cell aggregates and the like.
【0002】[0002]
【従来の技術】従来から、粉粒体状の微小物体を選別す
る方法として、篩を用いた篩分けの方法、あるいは遠心
分離器による方法、又は流体中における沈降速度の差を
利用して物体を大きさ又は密度の異なる群に分級する分
級装置を用いた方法等が考えられている。2. Description of the Related Art Conventionally, as a method for selecting minute objects in the form of powder or granules, a method of sieving using a sieve, a method of using a centrifuge, or a method utilizing a difference in sedimentation velocity in a fluid is used. There has been considered a method using a classifying device for classifying the A. into groups having different sizes or densities.
【0003】例えば、特公昭52−47715号及び特
開平2−247541号に記載の発明は、遠心分離器を
用いて精密な分級を可能としている。しかし、この方法
は回分法であるため連続的な選別はできず、また細胞塊
を分級するような場合には、遠心分離器へ出し入れする
際に雑菌や不純物に汚染される虞もある。For example, the inventions described in JP-B-52-47715 and JP-A-2-247541 enable precise classification using a centrifugal separator. However, since this method is a batch method, continuous selection cannot be performed, and in the case of classifying cell aggregates, there is a risk that contaminants and impurities will be contaminated when the cells are put into and taken out from the centrifuge.
【0004】また、次のような分級装置も提案されてい
る。すなわち、実開昭63−99259号記載の考案
は、分級槽内で物体を自由落下させ、槽の底に設置され
た巻取りベルトにより、ベルト上に落下した物体から順
に取り出し分級を行う装置である。しかしながら、この
装置では連続的な分級は不可能であり、ベルトより分級
した物体を取り出すのに手間がかかるため、大量に分級
することもできない。また、ベルトの巻取り部分から発
生する油分、金属粉等の不純物が混入する可能性があ
り、細胞塊の分級には不適当である。The following classifying device has also been proposed. That is, the device described in Japanese Utility Model Laid-Open No. 63-99259 is a device for free fall of objects in a classification tank, and a take-up belt installed at the bottom of the tank to take out the objects in order from the objects falling on the belt and perform classification. is there. However, continuous classification is not possible with this apparatus, and it takes time to take out the classified objects from the belt, so that it is not possible to classify a large amount. Further, there is a possibility that impurities such as oil and metal powder generated from the winding portion of the belt may be mixed in, which is not suitable for classifying cell aggregates.
【0005】このような問題が生じないものとして、特
公平3−99号、特開昭59−196760号及び特開
平3−178352号に記載の発明がある。特公平3−
99号記載の発明は、分級する物体を含む物体群を流体
中に分散させた分散液を底部が上下に摺動できるピスト
ンを備えた容器中に入れ、一定の速度でその容器の底部
を押し上げることにより、乱流を防止した上昇流を作り
出し、その押し上げ速度より小さい沈降速度を有する粒
子を容器上部より溢流させることにより高精度な分級を
行えるようになっている。The inventions described in JP-B-3-99, JP-A-59-196760 and JP-A-3-178352 are those which do not cause such a problem. Special Fairness 3-
In the invention described in No. 99, a dispersion liquid in which an object group including an object to be classified is dispersed in a fluid is put into a container equipped with a piston whose bottom part can slide up and down, and the bottom part of the container is pushed up at a constant speed. As a result, an upward flow that prevents turbulent flow is created, and particles having a sedimentation velocity lower than the pushing-up velocity are caused to overflow from the upper part of the container, so that highly accurate classification can be performed.
【0006】また、特開昭59−196760号及び特
開平3−178352号に記載の発明は、流体の密度を
調整することにより、調整した密度より大きな密度をも
つ物体を沈降させ、小さな密度をもつ物体を浮上させ、
二群に分級するものである。また更に、特公昭57−5
582号は微小物体を含む懸濁液を槽内で静置し、沈降
させ、懸濁液抜き出し管により抜き出し、分級する方法
である。上述したものは、いずれも被分級物を二群に分
流するものである。Further, in the inventions disclosed in JP-A-59-196760 and JP-A-3-178352, the density of the fluid is adjusted so that an object having a density higher than the adjusted density is settled, and a small density is set. Levitate an object with
It is classified into two groups. Furthermore, Japanese Patent Publication No. 57-5
No. 582 is a method in which a suspension containing microscopic objects is allowed to stand in a tank, is allowed to settle, is extracted by a suspension withdrawal tube, and is classified. In all of the above, the material to be classified is divided into two groups.
【0007】特公昭53−16933号に記載の発明
は、直立円筒体と拡開円筒体とを交互に組み合わせたも
ので、その構造により乱流を防ぎ、かつ多群に分級でき
るようにしたものである。The invention described in Japanese Examined Patent Publication No. Sho 53-16933 is a combination of upright cylinders and expanding cylinders which are alternately combined, the structure of which prevents turbulence and enables classification into multiple groups. Is.
【0008】また更に、実開昭58−166882号に
記載の考案は、粉粒物の分級装置であって、流れる気体
中に上部から被分級物である粉粒物を供給し、粉粒物の
降下速度差を利用して、落下位置の違いにより分級する
ものである。Furthermore, the device described in Japanese Utility Model Application Laid-Open No. 58-166882 is a classifier for powders and granules, in which the powders and granules to be classified are supplied from above to a flowing gas, By using the descent speed difference of, the classification is performed according to the difference of the falling position.
【0009】[0009]
【発明が解決しようとする課題】しかしながら、これら
の方法の多くは物体を二群に分けるだけであり、細胞塊
を生育段階毎に多群に分けるような分級はできず、また
管内に乱流が発生するため、細胞塊などのような物体に
適した分級精度は期待できない。また、特公昭53−1
6933号に記載の発明は、物体の回収口の入り口が狭
く、また拡開円筒体部で管内流速と等しい沈降速度であ
る物体は回収できないため、全体的に物体の回収効率が
悪く、大量に分級できないという問題がある。また、実
開昭58−166882号に記載の考案は、分級する物
体にかかる風力,重力,摩擦抵抗が分級中に釣り合わな
いため、物体は曲線を描いて落下するので、落下軌跡が
不安定となり落下位置が正確に把握できず分級精度がで
ない。また、細胞塊のように培養液中にて培養・生育さ
せるものでは、分級・選別も液体中で行う必要があり、
この装置のような気体中での分級は適さない。However, most of these methods only divide the object into two groups and cannot classify the cell mass into multiple groups according to the growth stage, and turbulent flow in the tube. Therefore, classification accuracy suitable for objects such as cell clusters cannot be expected. In addition, Japanese Patent Publication Sho 53-1
The invention described in No. 6933 has a narrow entrance of an object recovery port and cannot recover an object having a sedimentation velocity equal to the in-pipe flow velocity in the expanding cylindrical body part, so that the recovery efficiency of the object as a whole is poor and a large amount of There is a problem that you cannot classify. Further, in the device described in Japanese Utility Model Publication No. 58-166882, since the wind force, gravity, and frictional resistance applied to the object to be classified do not balance during classification, the object falls in a curved line, and the falling trajectory becomes unstable. The falling position cannot be accurately grasped and the classification accuracy is poor. Also, in the case of culturing / growing in a culture medium like a cell mass, it is necessary to perform classification / selection in a liquid,
Classification in a gas like this device is not suitable.
【0010】本発明は、細胞塊等のように生育段階毎に
種々の群が存在する被分級物を多群に、かつ多量に分級
できる沈降式分級装置の提供を目的としている。It is an object of the present invention to provide a sedimentation type classifying apparatus capable of classifying a large number of classified substances having various groups such as cell clumps at each growth stage into a large number.
【0011】[0011]
【課題を解決するための手段】本発明に係る沈降式分級
方式は、被分級物が混入された液体を等速で流し、液体
中を沈降していく被分級物の終端速度に基づく落下位置
の違いにより被分級物を分級するようにしたことを特徴
としている。A settling type classification method according to the present invention is a dropping position based on a terminal velocity of a classified substance in which a liquid mixed with the classified substance is caused to flow at a constant velocity and settles in the liquid. The feature is that the objects to be classified are classified according to the difference of.
【0012】また、本発明に係る沈降式分級方式は、等
速で流れる液体中に被分級物を落とし、液体中を沈降し
ていく被分級物の終端速度に基づく落下位置の違いによ
り被分級物を分級するようにしたことを特徴としてい
る。Further, in the sedimentation type classification method according to the present invention, the object to be classified is dropped in the liquid flowing at a constant speed, and the classified object is classified by the difference in the falling position based on the terminal velocity of the object to be settled in the liquid. It is characterized by classifying things.
【0013】また、本発明に係る沈降式分級装置は、軸
方向が水平に配置された円筒状の分級槽と、該分級槽の
下部軸方向に配列され、弁を開とすることにより他の装
置と連通する複数の仕切部と、該分級槽の一方の開口部
端に接続され、側面視、上部が一定の高さに保たれ、下
部が外方に向かって斜めに立ち上がり、先端部が開口し
た第1の斜円錐状管路と、該分級槽の他方の開口部端に
接続され、側面視、下部が一定の高さに保たれ、上部が
外方に向かって斜めに立ち下がり、先端部が開口した第
2の斜円錐状管路とを備え、前記第1の斜円錐状管路の
先端部から被分級物の混入液体を流入させ、前記第2の
斜円錐状管路の先端部から液体を流出させるようにした
ことを特徴としている。Further, the sedimentation type classifying apparatus according to the present invention has a cylindrical classifying tank whose axial direction is horizontally arranged and a lower axial direction of the classifying tank, which is arranged by opening a valve to obtain another type. A plurality of partition parts communicating with the device and one end of the opening of the classification tank are connected, the upper part is kept at a constant height in a side view, the lower part rises obliquely outward, and the tip part is It is connected to the opened first oblique conical pipe line and the other opening end of the classification tank, the lower part is kept at a constant height in a side view, and the upper part is inclined downward toward the outside. A second oblique conical conduit having an open tip, and the mixed liquid of the material to be classified is caused to flow into the second oblique conical conduit from the distal end of the first oblique conical conduit. The feature is that the liquid is made to flow out from the tip.
【0014】また、本発明に係る沈降式分級装置は、軸
方向が水平に配置された円筒状の分級槽と、該分級槽の
下部軸方向に配列され、弁を開とすることにより他の装
置と連通する複数の仕切部と、該分級槽の一方の開口部
端に接続され、外方に向かって細くなり、先端部が開口
した第1の円錐状管路と、該分級槽の他方の開口部端に
接続され、外方に向かって細くなり、先端部が開口した
第2の円錐状管路と、前記分級槽の前記一方の開口部端
近傍に配置された整流格子とを備え、前記第1の円錐状
管路の先端部から液体を流入させ、前記第2の円錐状管
路の先端部から液体を流出させるようにするとともに、
前記分級槽の前記一方の開口部端近傍の上部に設けた投
入口から被分級物を投入するようにしたことを特徴とし
ている。Further, the settling type classifying apparatus according to the present invention has a cylindrical classifying tank whose axial direction is arranged horizontally and a lower axial direction of the classifying tank, and is opened by opening a valve. A plurality of partition parts communicating with the device, a first conical conduit connected to one opening end of the classification tank, narrowing outward, and having an open tip, and the other of the classification tanks A second conical pipe line connected to the end of the opening of the container, narrowing outward, and having an open tip, and a rectifying grid disposed near the end of the one opening of the classification tank. , Letting the liquid flow in from the tip of the first conical conduit and letting the liquid flow out from the tip of the second conical conduit,
It is characterized in that an object to be classified is introduced through an introduction port provided in an upper portion of the classification tank near the end of the one opening.
【0015】また更に、本発明に係る沈降式分級方法及
び装置で分級する被分級物は細胞塊であることを特徴と
している。Furthermore, the object to be classified by the sedimentation type classification method and apparatus according to the present invention is characterized in that it is a cell mass.
【0016】[0016]
【作用】本発明は、上述のように、被分級物が混入され
た液体を等速で流し、あるいは等速で流れる液体中に被
分級物を落すので、被分級物はその物体にかかる重力,
浮力,液体との摩擦抵抗が釣り合って液体中を等速で沈
降していく。この速度を終端速度といい、被分級物の密
度,質量,体積,形状等の相違によって異なる。被分級
物は、この終端速度と液体の流速とにより斜め下方に直
線状の軌跡を描いて落下する。この落下位置の違いによ
り被分級物は、その密度,質量等の差に分級される。As described above, according to the present invention, the liquid mixed with the substance to be classified is caused to flow at a constant velocity, or the substance to be classified is dropped into the liquid flowing at a constant velocity. ,
The buoyancy and the frictional resistance with the liquid balance each other, and the liquid settles at a constant speed. This speed is called the terminal speed, and it depends on the density, mass, volume, shape, etc. of the material to be classified. The object to be classified falls along a linear trajectory obliquely downward due to the terminal velocity and the flow velocity of the liquid. The objects to be classified are classified according to the difference in density, mass, etc. due to the difference in the falling position.
【0017】また本発明は、第1の斜円錐状管路の先端
部から被分級物の混入液体を流入させ、第2の斜円錐状
管路の先端部から液体を流出させるようにすると、液体
中に混入されている被分級物は、その終端速度の差に従
って、分級槽の下部軸方向に配列された仕切部に順に入
る。これらの仕切部に繋がる弁を開とすることにより、
仕切部内に分級されて入った被分級物は他の装置へと運
ばれる。Further, according to the present invention, when the mixed liquid of the substance to be classified is caused to flow in from the tip of the first oblique conical conduit and the liquid is caused to flow out from the tip of the second oblique conical conduit, The substances to be classified mixed in the liquid sequentially enter the partition section arranged in the lower axial direction of the classification tank according to the difference in the terminal speed. By opening the valves connected to these partitions,
The objects to be classified that have been classified into the partition section are carried to another device.
【0018】また更に、第1の円錐状管路の先端部から
液体を流入させ、第2の円錐状管路の先端部から液体を
流出させるようにするとともに、分級槽の前記一方の開
口部端近傍の上部に設けた投入口から被分級物を投入す
ると、被分級物は整流格子により乱流の少ない液体中を
一定の速度で沈降し、分級槽の下部軸方向に配列された
仕切部に順に入る。これらの仕切部に繋がる弁を開とす
ることにより、仕切部内に分級されて入った被分級物は
他の装置へと運ばれる。Furthermore, the liquid is allowed to flow in from the tip of the first conical conduit and the liquid is allowed to flow from the tip of the second conical conduit, and the one opening of the classification tank is also used. When the material to be classified is introduced from the inlet provided at the upper part near the end, the material to be classified is settled at a constant speed in the liquid with less turbulence by the rectifying grid, and the partition part arranged in the lower axial direction of the classification tank. Go into order. By opening the valves connected to these partition parts, the objects to be classified that have been classified into the partition parts are carried to another device.
【0019】[0019]
【実施例】以下、本発明の実施例を図面に基づき説明す
る。その前に、重力を用いた沈降分級装置の原理につい
て説明する。物体を静止液体中で自由落下させたとき、
物体にかかる重力,浮力,流体との摩擦抵抗が釣り合
い、やがて物体は等速で落下するようになる。この速度
を終端速度といい、物体の質量,体積,密度,形状等の
性質によって異なる。この操作を、水平方向に一定で、
流路内のどの場所でも同じ流速である水平方向に延びた
管路内にて行うと、終端速度に差がある2物体は、図3
に示すように、落下開始位置から落下終了位置までの水
平移動距離に差が生じる。このときに生じる水平移動距
離の差により物体を分級することが重力を用いた沈降式
分級方法である。Embodiments of the present invention will be described below with reference to the drawings. Before that, the principle of the sedimentation classifier using gravity will be described. When an object freely falls in a stationary liquid,
Gravity, buoyancy, and frictional resistance with fluid balance the object, and eventually the object will fall at a constant velocity. This velocity is called the terminal velocity, and it depends on the properties such as the mass, volume, density, and shape of the object. This operation is constant in the horizontal direction,
When performed in a pipe extending in the horizontal direction where the flow velocity is the same at any place in the flow path, two objects with different terminal velocities are
As shown in, there is a difference in the horizontal movement distance from the drop start position to the drop end position. Classifying an object by the difference in the horizontal movement distance generated at this time is a sedimentation type classification method using gravity.
【0020】図1には、本発明に係る沈降式分級装置の
第1の実施例が示されている。図において、4は軸方向
が水平に配置された内側が滑らかな円筒状の分級槽であ
り、該分級槽4の一方の開口部端には、側面視、上部が
一定の高さに保たれ、下部が外方に向かって斜めに立ち
上がり、先端部2aが開口した第1の斜円錐状管路2
が、フランジ5を利用してビスで取付けられている。こ
の第1の斜円錐状管路2は、先端部2aから見ると液体
が乱流にならない程度に分級槽4に向かって次第に拡開
している。FIG. 1 shows a first embodiment of the sedimentation type classifying apparatus according to the present invention. In the figure, reference numeral 4 is a cylindrical classification tank having a smooth inner side, which is arranged horizontally in the axial direction, and one end of the opening of the classification tank 4 is kept at a constant height in a side view from the top. , The first oblique conical conduit 2 whose lower portion rises obliquely outward and whose tip 2a is open
Are attached with screws using the flange 5. The first inclined conical conduit 2 gradually expands toward the classification tank 4 to the extent that the liquid does not become a turbulent flow when viewed from the tip 2a.
【0021】この第1の斜円錐状管路部2の先端部2a
には、ユニオン3を用いてパイプ1が着脱可能に取り付
けられており、該パイプ1には分級を行う細胞塊の微小
物体を含む懸濁液を送り込むためのポンプ等が接続され
ている。分級槽4の下部には下方に狭くなる筒状の仕切
部6(6a,6b,・・)が分級槽4の軸方向に配列さ
れており、これら仕切部6の最下部にはそれぞれハーフ
ユニオン7が接続されていて、それぞれシリコン等のチ
ューブ8が簡単に着脱できるようになっている。なお、
シリコン等のチューブ8の開閉をピンチコック9にて行
われる。The tip portion 2a of the first oblique conical conduit portion 2
1, a pipe 1 is detachably attached using a union 3, and the pipe 1 is connected with a pump or the like for feeding a suspension containing minute objects of cell mass to be classified. At the bottom of the classification tank 4, cylindrical partition parts 6 (6a, 6b, ...) that narrow downward are arranged in the axial direction of the classification tank 4, and at the bottom of these partition parts 6 there are half unions. 7 are connected, and tubes 8 made of silicon or the like can be easily attached and detached. In addition,
The tube 8 made of silicon or the like is opened and closed by the pinch cock 9.
【0022】また、分級槽4の他方の開口部端には、乱
流にならない程度に内側が滑らかで、側面視、上部が外
方に向かって斜めに立ち上がり、下部が一定の高さに保
たれ、先端部10aが開口した第2の斜円錐状管路10
が、フランジ11を利用してビス止め11されている。
この第2の斜円錐状管路10の先端部10aには、ユニ
オン12にてパイプ13が着脱可能に取付けられてい
る。At the other end of the opening of the classification tank 4, the inside is smooth to the extent that turbulent flow does not occur, the upper part rises obliquely outward, and the lower part is kept at a constant height in side view. The second oblique conical conduit 10 with the tip end 10a opened
However, it is screwed 11 using the flange 11.
A pipe 13 is detachably attached to a tip portion 10a of the second oblique conical conduit 10 by a union 12.
【0023】次に、この装置の動作について説明する。
分級する微小物体を細胞塊として、液体を培養液などの
密度が1g/cm3 の液とするとき、培養タンクからパイ
プ1内を一定流量で液体とともに流れてきた細胞塊は、
先ず第1の斜円錐状管路2に入る。液体は密度が1g/
cm3 であり、また細胞塊の密度は1g/cm3 をわずかに
上回る程度なので、本例液体中では細胞塊にかかる重力
と浮力と摩擦抵抗が即座に釣合い、鉛直方向の動きのみ
に注目すると、落下開始直後に等速となって落下する。
なお、このときの細胞塊の速度を終端速度と呼ぶ。Next, the operation of this device will be described.
When the minute object to be classified is a cell mass and the liquid is a liquid having a density of 1 g / cm 3 such as a culture solution, the cell mass flowing from the culture tank in the pipe 1 at a constant flow rate with the liquid is
First, the first inclined conical conduit 2 is entered. Liquid has a density of 1g /
Since it is cm 3 , and the density of the cell mass is slightly higher than 1 g / cm 3 , in the liquid of this example, gravity, buoyancy, and frictional resistance applied to the cell mass are immediately balanced, and if we focus only on the vertical movement, , Immediately after the fall starts, it falls at a constant speed.
The velocity of the cell mass at this time is called the terminal velocity.
【0024】第1の斜円錐状管路2中で、細胞塊は鉛直
方向に等速で落下するが、管路が次第に拡開しているた
め液体は水平方向の流速は漸減するので、細胞塊は図の
ように放物線を描いて落下する。細胞塊が第1の斜円錐
状管路2から分級槽4に入ると、分級槽4では槽内のど
の地点でも水平方向に一定で等しい流速で流れるため、
細胞塊は図のような斜め下向きの直線を描いて落下し、
分級槽4の下部の仕切部6内に入り、シリコンチューブ
8を通り、それぞれ次の工程へ輸送される。このとき、
終端速度の速い、形状の大きな細胞塊ほど図において左
側の仕切部6aの方へ入り、終端速度の遅い、形状の小
さな細胞塊ほど右側の仕切部6dの方へ入り、細胞塊の
大きさ、生育段階により分級できる。仕切部6d内に入
らないほど終端速度の遅い細胞塊は液体とともに第2の
斜円錐状管路10、パイプ13を通り培養タンクへ戻さ
れ、再び培養される。In the first oblique conical conduit 2, the cell mass falls in the vertical direction at a constant velocity, but since the conduit gradually expands, the liquid flow velocity gradually decreases in the horizontal direction. The mass falls in a parabola as shown. When the cell mass enters the classification tank 4 through the first oblique conical conduit 2, the classification tank 4 flows horizontally at a constant and equal flow rate at any point in the tank.
The cell clumps fall in a diagonal straight line as shown in the figure,
The particles enter the partition section 6 at the bottom of the classification tank 4, pass through the silicon tube 8, and are transported to the next step. At this time,
The larger the cell mass with the faster terminal velocity and the larger shape, the closer to the partition 6a on the left side in the figure, and the smaller the cell velocity with the lower terminal speed and the smaller the shape, the closer to the partition 6d on the right side. It can be classified according to the growth stage. The cell mass having a slow terminal velocity that does not enter the partition 6d is returned together with the liquid to the culture tank through the second oblique conical conduit 10 and the pipe 13, and is cultured again.
【0025】以上のことから、本発明実施例の沈降式分
級方法及び装置を用いることにより、微小物体を連続し
て大量に多群に分級可能となる。また、分級は外部と隔
離された管路内で行われるため雑菌や不純物に汚染され
ることがなく、また装置は分解可能であるため装置の洗
浄、滅菌が簡単に行えることから細胞塊等の物体にも有
効である。また、流体として液体を用いているため、気
体のように分級する物体にかかる風力,重力,摩擦抵抗
が分級中に釣り合わず物体が曲線を描いて落下し、落下
軌跡が不安定となって、落下位置が正確に把握できず分
級精度がでないという欠点がない。また、細胞塊のよう
に培養液中にて培養・生育させるものでは、分級・選別
も液体中で行う必要があるので、本実施例のような装置
が分級に好適である。From the above, by using the sedimentation type classification method and apparatus of the embodiment of the present invention, it is possible to continuously classify a large amount of minute objects into a large number of groups. In addition, since classification is performed in a pipeline isolated from the outside, it is not contaminated with various bacteria and impurities, and since the device can be disassembled, the device can be easily washed and sterilized. It is also effective for objects. Also, because liquid is used as the fluid, the wind force, gravity, and frictional resistance applied to the object to be classified like gas are not balanced during classification, the object falls in a curved line, and the fall trajectory becomes unstable. There is no drawback that the falling position cannot be accurately grasped and the classification accuracy is poor. Further, in the case of culturing / growing in a culture solution such as a cell mass, classification / selection also needs to be performed in the liquid, and thus the apparatus according to this example is suitable for classification.
【0026】次に、本発明の第2の実施例について説明
する。なお、第1の実施例で説明したものと同一または
相当する部分には同一符号を付す。図2には、本発明に
係る沈降式粉流物分級装置の第2の実施例が示されてい
る。図において、4は軸方向が水平に配置された内側が
滑らかな円筒状の分級槽であり、該分級槽4の一方の開
口部端には、外方に向かって細くなり、先端部15aが
開口した第1の円錐状管路15がフランジ5を利用して
ビスで取付けられている。この第1の斜円錐状管路15
は、先端部15aから見ると液体が乱流にならない程度
に分級槽4に向かって次第に拡開している。Next, a second embodiment of the present invention will be described. The same or corresponding parts as those described in the first embodiment are designated by the same reference numerals. FIG. 2 shows a second embodiment of the sedimentation type powder flow material classifying apparatus according to the present invention. In the figure, 4 is a cylindrical classification tank in which the axial direction is horizontally arranged and the inside is smooth. At one end of the opening of the classification tank 4, the classification tank 4 is tapered outward and has a tip 15a. An open first conical conduit 15 is attached with screws using the flange 5. This first oblique conical conduit 15
Is gradually expanded toward the classification tank 4 so that the liquid does not become a turbulent flow when viewed from the tip portion 15a.
【0027】また、該分級槽4の他方の開口部端には、
外方に向かって細くなり、先端部17aが開口した第2
の円錐状管路17がフランジ5を利用してビスで取付け
られている。この第2の斜円錐状管路17も、先端部1
7aから見ると液体が乱流にならない程度に分級槽4に
向かって次第に拡開している。At the other end of the opening of the classification tank 4,
The second taper toward the outside, with the tip 17a opened
The conical conduit 17 is attached with screws using the flange 5. This second oblique conical conduit 17 also has a tip portion 1.
When viewed from 7a, the liquid gradually expands toward the classification tank 4 to the extent that the liquid does not become a turbulent flow.
【0028】前記第1の斜円錐状管路15の先端部15
aには、ユニオン3を用いてパイプ1が着脱可能に取り
付けられており、前記第2の斜円錐状管路17の先端部
17aにも、ユニオン12によりパイプ13が接続され
ていて、該パイプ13は一周して前記パイプ1と接続さ
れているが、パイプ13→パイプ1のライン中に順にド
レイン18、ポンプ19、流量調整バルブ20、流量計
21が接続されている。The tip portion 15 of the first oblique conical conduit 15
A pipe 1 is detachably attached to a by using a union 3, and a pipe 13 is connected to a tip portion 17a of the second oblique conical conduit 17 by a union 12. Although the circuit 13 is connected to the pipe 1 after making one round, a drain 18, a pump 19, a flow rate adjusting valve 20, and a flow meter 21 are sequentially connected in the line of the pipe 13 → the pipe 1.
【0029】また、前記分級槽4の前記一方の開口部端
近傍には整流格子16が配置されており、該整流格子1
6は極めて薄い材料にて格子状に形成されていて、着脱
可能な嵌め込み式にて取り付けられている。該整流格子
16は、前記第1の円錐状管路15から流入した液体を
整流して乱流とならないようにするものである。また、
分級槽4の前記一方の開口部端近傍の上部には被分級物
を投入するための投入孔4aが設けられており、該投入
孔4aには、鉛直方向に延びたパイプ27がユニオン2
8を用いて接続されている。該パイプ27の中間にはボ
ールバルブ(ON、OFFバルブ)29が配置されてお
り、上端部には分級を行う細胞塊等の微小物体を含む懸
濁液が入った容器(不図示)が接続されている。図4に
は、本装置の具体的な形状が示されており、(a)は平
面図、(b)は側面図であり、図2に示す符号を付して
説明を省略する。A rectifying grid 16 is arranged near the end of the one opening of the classifying tank 4, and the rectifying grid 1 is provided.
6 is made of an extremely thin material in a lattice shape, and is attached by a detachable fitting type. The rectifying grid 16 rectifies the liquid that has flowed in from the first conical conduit 15 so that it does not become a turbulent flow. Also,
A charging hole 4a for charging a material to be classified is provided in the upper part of the classification tank 4 in the vicinity of the one end of the opening, and a pipe 27 extending vertically is provided in the charging hole 4a.
8 are used for connection. A ball valve (ON / OFF valve) 29 is arranged in the middle of the pipe 27, and a container (not shown) containing a suspension containing minute objects such as cell clusters for classification is connected to the upper end. Has been done. FIG. 4 shows a specific shape of the present device, (a) is a plan view and (b) is a side view, and the reference numerals shown in FIG.
【0030】また、分級槽4の下部には、実施例1の場
合と同様、下方に狭くなる筒状の複数個仕切部6(6
a,6b,・・)が設けられており、これら仕切部6の
最下部にはそれぞれハーフユニオン7が接続されてい
て、それぞれシリコン等のチューブ8が簡単に着脱でき
るようになっている。なお、シリコン等のチューブ8の
開閉をピンチコック9にて行われる。シリコン等のチュ
ーブ12のもう一方の端はそれぞれ各次工程と接続され
ている。Further, in the lower part of the classification tank 4, as in the case of the first embodiment, a plurality of cylindrical partition parts 6 (6, which are narrowed downward, are formed.
a), 6b, ...) are provided, and half unions 7 are connected to the lowermost portions of the partition portions 6, respectively, so that tubes 8 made of silicon or the like can be easily attached and detached. The tube 8 made of silicon or the like is opened and closed by the pinch cock 9. The other end of the tube 12 made of silicon or the like is connected to each subsequent step.
【0031】次に、この装置の動作について説明する。
装置内は液体で満たされ、その液体はポンプ19にて装
置内を循環する。流れの向きは分級槽4内では図におい
て左から右である。また、分級槽4内の流速はポンプ1
9の下流の流量調整バルブ20により制御され、その速
度は流量調整バルブ20下流の流量計21の値を測定す
ることにより知ることができる。また、分級槽4内の液
体が管路の急拡大、急縮小により乱流になるのを防止す
るため、分級槽4の左右に第1の円錐状管路15、第2
の円錐状管路17を接続し、更に整流格子16にて分級
槽4内の流れをどの地点であっても水平方向で一定で等
しい流速に保っている。また、装置は洗浄、滅菌が容易
に行えるよう、部品は着脱可能となっている。Next, the operation of this device will be described.
The inside of the device is filled with a liquid, and the liquid is circulated in the device by a pump 19. The flow direction is from left to right in the figure in the classification tank 4. Also, the flow velocity in the classification tank 4 is
It is controlled by the flow rate adjusting valve 20 downstream of 9, and its speed can be known by measuring the value of the flow meter 21 downstream of the flow rate adjusting valve 20. Further, in order to prevent the liquid in the classification tank 4 from becoming a turbulent flow due to the sudden expansion and contraction of the conduit, the first conical conduit 15 and the second conical conduit 15 are provided on the left and right of the classification tank 4.
The conical pipe line 17 is connected, and the flow in the classification tank 4 is maintained at a constant and equal flow rate in the horizontal direction at any point by the rectifying grid 16. The parts are removable so that the device can be easily cleaned and sterilized.
【0032】例として分級を行う微小物体を細胞塊、液
体を培養液として説明する。先ず、細胞塊はパイプ27
を自由落下して、分級槽4に供給される。このとき、液
体である培養液と細胞塊の密度の関係は細胞塊の方が培
養液より若干密度が大であるため液体内を落下する細胞
塊は落下直後に細胞塊にかかる重力と浮力と摩擦抵抗力
が釣合い即座に等速で落下する。この時の速度を終端速
度と呼ぶ。As an example, a minute object for classification will be described as a cell mass and a liquid as a culture solution. First, the cell mass is pipe 27
Is dropped and supplied to the classification tank 4. At this time, the relationship between the density of the liquid culture medium and the cell mass is that the density of the cell mass is slightly higher than that of the culture liquid, so that the cell mass falling in the liquid has gravity and buoyancy applied to the cell mass immediately after falling. The frictional resistance balances out and it immediately drops at a constant speed. The speed at this time is called the terminal speed.
【0033】細胞塊はパイプ27中を落下して分級槽4
内に落下した時点には終端速度に達し、以後等速で落下
する。分級槽4内では、液体は水平方向に一定流速で流
れているため、分級槽4内に入った細胞塊は図のように
斜め下向きの直線を描いて落下し、分級槽4下部の仕切
部6(6a,6b,・・・)に入り、分級される。この
とき、終端速度の速い形状の大きな細胞塊ほど、左の仕
切部6aの方へ入り、終端速度の遅い形状の小さな細胞
塊になるにつれて右の仕切部6bの方へ入るようにな
る。このようにして、細胞塊を形状の大きさ、すなわち
生育段階により分級選別できる。各仕切部6内に入った
細胞塊はシリコン等のチューブ8を通ってそれぞれ次工
程に移される。The cell clumps fall through the pipe 27 and the classification tank 4
When it falls inside, it reaches the terminal speed, and thereafter it drops at a constant speed. Since the liquid flows horizontally in the classifying tank 4 at a constant flow velocity, the cell clumps entering the classifying tank 4 fall in a slanting downward straight line as shown in the figure, and the partitioning section at the lower part of the classifying tank 4 falls. 6 (6a, 6b, ...) Enter and be classified. At this time, a larger cell mass having a shape with a higher terminal speed enters the left partition 6a, and a smaller cell mass having a shape with a lower terminal speed enters the right partition 6b. In this way, the cell mass can be classified and sorted according to the size of the shape, that is, the growth stage. The cell mass that has entered each partition 6 is transferred to the next step through a tube 8 made of silicon or the like.
【0034】図4に示すように、分級槽4内部の直径を
R、液体の流速をV、分級する微小物体の鉛直下向きの
終端速度U、微小物体の水平方向の移動距離をX、微小
物体が落下するのにかかる時間(水平移動距離Xに達す
るまでの時間)をtとすると、微小物体は水平、鉛直方
向共に等速で移動するため、 t=R/U ・・・・・・・・ t=X/V ・・・・・・・・ の関係にある。As shown in FIG. 4, the inside diameter of the classification tank 4 is R, the flow velocity of the liquid is V, the vertical downward velocity U of the minute object to be classified, the horizontal moving distance of the minute object is X, and the minute object is Let t be the time it takes for the object to fall (time to reach the horizontal movement distance X), since a minute object moves at a constant velocity in both horizontal and vertical directions, t = R / U ..・ T = X / V ...
【0035】上記,より水平移動距離Xは、 X=RV/U・・・・・・・・ となる。したがって、微小物体の水平移動距離は、分級
槽4内部の直径と流速、物体の終端速度が分かれば、計
算により簡単に求められる。このため、分級を行う物体
の終端速度が分かれば、計算により分級に最適な分級槽
4の直径、水平方向の長さ、流速、仕切部6を設けるた
めの仕切り板の位置を設定してやることができる。From the above, the horizontal movement distance X is X = RV / U .... Therefore, the horizontal moving distance of the minute object can be easily obtained by calculation if the diameter and flow velocity inside the classification tank 4 and the terminal velocity of the object are known. Therefore, if the terminal speed of the object to be classified is known, the diameter of the classification tank 4, the length in the horizontal direction, the flow velocity, and the position of the partition plate for providing the partition 6 can be set by calculation. it can.
【0036】次に、この装置を用いて行った実験例を図
5を参照して説明する。 (実験例)長軸長が1〜4mmのニンジン不定胚(ニン
ジンの生体の一部を切取り、培養することにより生じた
将来芽と根になる部分を持つ細胞塊)を長軸長1〜2m
m,2〜3mm,3〜4mmの3群のニンジン不定胚に
分級するとする。この分級を行うのに、分級槽4内部の
直径を300mm、流速を3mm/sec、液体を0.1
%アルギン酸ナトリウム水溶液とした。先ず、長軸長1
〜2mm,2〜3mm,3〜4mmのニンジン不定胚の
終端速度はそれぞれ平均1.772 、2.443 、3.503 mm/
secであるので、前述の式より水平移動距離はそれぞ
れ507.9 、368.4 、256.9 mmである。このことから、
仕切部6を設けるための仕切り板の位置をパイプ27の
中心より256.9 〜368.4 mmの中央と、368.4 〜507.9
mmの中央とに設けた。これによりに、生育の揃った3
群の不定胚を得ることができた。Next, an example of an experiment conducted using this apparatus will be described with reference to FIG. (Experimental example) A carrot somatic embryo having a major axis length of 1 to 4 mm (a cell mass having a part to be a future sprout and a root produced by cutting out a part of a carrot living body and culturing) and having a major axis length of 1 to 2 m
It is assumed that the carrot somatic embryos of 3 groups of m, 2 to 3 mm, and 3 to 4 mm are classified. To carry out this classification, the diameter inside the classification tank 4 is 300 mm, the flow rate is 3 mm / sec, and the liquid is 0.1
% Aqueous solution of sodium alginate. First, major axis length 1
Terminal velocities of carrot somatic embryos of ~ 2 mm, 2-3 mm, 3-4 mm average 1.772, 2.443, 3.503 mm /, respectively.
Since it is sec, the horizontal movement distances are 507.9, 368.4, and 256.9 mm from the above equation, respectively. From this,
The position of the partition plate for providing the partition portion 6 is set to the center of 256.9 to 368.4 mm from the center of the pipe 27 and 368.4 to 507.9.
It was provided at the center of mm. As a result, 3
A group of somatic embryos could be obtained.
【0037】[0037]
【発明の効果】以上説明したように、本発明によれば、
細胞塊等のように生育段階毎に種々の群が存在する被分
級物を、多群に、かつ多量に分級することができ、かつ
雑菌等の不純物による汚染を防止することができる。As described above, according to the present invention,
It is possible to classify an object to be classified such as a cell clump that has various groups at each growth stage into a large number of groups and prevent contamination with impurities such as various bacteria.
【図1】本発明の第1の実施例の側面図である。FIG. 1 is a side view of a first embodiment of the present invention.
【図2】本発明の第2の実施例の側面図である。FIG. 2 is a side view of the second embodiment of the present invention.
【図3】沈降による分級原理を説明する図である。FIG. 3 is a diagram illustrating a classification principle by sedimentation.
【図4】第2の実施例に係る沈降式分級装置の具体的外
観を示す図で、(a)は平面図、(b)は側面図であ
る。4A and 4B are views showing a specific external appearance of a sedimentation type classification device according to a second embodiment, FIG. 4A being a plan view and FIG. 4B being a side view.
【図5】図2に示す第2の実施例の原理を説明する図で
ある。5 is a diagram illustrating the principle of the second embodiment shown in FIG.
【図6】実験例を説明するための図である。FIG. 6 is a diagram for explaining an experimental example.
1 パイプ 2 第1の斜円錐状管路 3 ユニオン 4 分級槽 4a 投入孔 5 フランジ 6 仕切 7 ハーフユニオン 8 シリコンチューブ 9 ピンチコック 10 第2の斜円錐状管路 11 フランジ 12 ユニオン 13 パイプ 15 第1の円錐状管路 16 整流格子 17 第2の円錐状管路 1 Pipe 2 1st Inclined Conical Pipe 3 Union 4 Classification Tank 4a Input Hole 5 Flange 6 Partition 7 Half Union 8 Silicon Tube 9 Pinch Cock 10 Second Oblique Conical Pipe 11 Flange 12 Union 13 Pipe 15 1st Conical conduit 16 Straightening grid 17 Second conical conduit
Claims (5)
し、液体中を沈降していく被分級物の終端速度に基づく
落下位置の違いにより被分級物を分級するようにしたこ
とを特徴とする沈降式分級方法。1. A method in which a liquid mixed with an object to be classified is caused to flow at a constant velocity and the object to be classified is classified according to a difference in a drop position based on a terminal velocity of the object to be classified that is settling in the liquid. A characteristic sedimentation type classification method.
し、液体中を沈降していく被分級物の終端速度に基づく
落下位置の違いにより被分級物を分級するようにしたこ
とを特徴とする沈降式分級方法。2. The object to be classified is dropped in a liquid flowing at a constant velocity, and the object to be classified is classified according to the difference in the drop position based on the terminal velocity of the object to be settled in the liquid. Settling type classification method.
槽と、 該分級槽の下部軸方向に配列され、弁を開とすることに
より他の装置と連通する複数の仕切部と、 該分級槽の一方の開口部端に接続され、側面視、上部が
一定の高さに保たれ、下部が外方に向かって斜めに立ち
上がり、先端部が開口した第1の斜円錐状管路と、 該分級槽の他方の開口部端に接続され、側面視、下部が
一定の高さに保たれ、上部が外方に向かって斜めに立ち
下がり、先端部が開口した第2の斜円錐状管路とを備
え、 前記第1の斜円錐状管路の先端部から被分級物の混入液
体を流入させ、前記第2の斜円錐状管路の先端部から液
体を流出させるようにしたことを特徴とする沈降式分級
装置。3. A cylindrical classification tank whose axial direction is arranged horizontally, and a plurality of partition portions which are arranged in the lower axial direction of the classification tank and which communicate with other devices by opening a valve, A first oblique conical conduit which is connected to one opening end of the classification tank, has an upper part kept at a constant height in a side view, and has a lower part rising outward obliquely and having an open end. And a second oblique cone connected to the other opening end of the classification tank, the lower part of which is kept at a constant height in a side view, the upper part of which falls obliquely outward, and the end part of which is open. And a liquid pipe, and a liquid mixed with the substance to be classified is caused to flow in from a tip portion of the first oblique conical pipe passage, and a liquid is caused to flow out from a tip portion of the second oblique conical pipe passage. A sedimentation classifier characterized by the following.
槽と、 該分級槽の下部軸方向に配列され、弁を開とすることに
より他の装置と連通する複数の仕切部と、 該分級槽の一方の開口部端に接続され、外方に向かって
細くなり、先端部が開口した第1の円錐状管路と、 該分級槽の他方の開口部端に接続され、外方に向かって
細くなり、先端部が開口した第2の円錐状管路と、 前記分級槽の前記一方の開口部端近傍に配置された整流
格子とを備え、 前記第1の円錐状管路の先端部から液体を流入させ、前
記第2の円錐状管路の先端部から液体を流出させるよう
にするとともに、前記分級槽の前記一方の開口部端近傍
の上部に設けた投入口から被分級物を投入するようにし
たことを特徴とする沈降式分級装置。4. A cylindrical classification tank whose axial direction is arranged horizontally, and a plurality of partition sections which are arranged in the lower axial direction of the classification tank and which communicate with other devices by opening a valve, A first conical pipe line connected to one opening end of the classification tank, narrowing outward, and having an open tip, and connected to the other opening end of the classification tank A second conical pipe line that narrows toward the end and has an open tip, and a rectifying grid that is arranged near the one opening end of the classification tank, and the first conical pipe line of the first conical pipe line is provided. The liquid is made to flow in from the tip portion, and the liquid is made to flow out from the tip portion of the second conical conduit, and classification is performed from an input port provided in the upper portion of the classification tank near the one end of the opening. A sedimentation type classifier characterized in that it is adapted to throw in a substance.
とする請求項1,2,3又は4記載の沈降式分級方法及
び装置。5. The sedimentation type classification method and apparatus according to claim 1, 2, 3 or 4, wherein the material to be classified is a cell mass.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP12574393A JP2967894B2 (en) | 1993-05-27 | 1993-05-27 | Sedimentation type classification method and apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP12574393A JP2967894B2 (en) | 1993-05-27 | 1993-05-27 | Sedimentation type classification method and apparatus |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH06328002A true JPH06328002A (en) | 1994-11-29 |
| JP2967894B2 JP2967894B2 (en) | 1999-10-25 |
Family
ID=14917702
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP12574393A Expired - Lifetime JP2967894B2 (en) | 1993-05-27 | 1993-05-27 | Sedimentation type classification method and apparatus |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2967894B2 (en) |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0753348A1 (en) * | 1995-07-10 | 1997-01-15 | Yazaki Corporation | Apparatus for classifying objects by sedimentation |
| US5720394A (en) * | 1994-07-15 | 1998-02-24 | Yazaki Corporation | Sample supply unit for settling classification system |
| US7802686B2 (en) | 2004-09-22 | 2010-09-28 | Fuji Xerox Co., Ltd. | Method and device for classifying fine particles |
| WO2011049229A1 (en) * | 2009-10-22 | 2011-04-28 | Jfeスチール株式会社 | Ferromagnetic material separation apparatus |
| WO2013093954A1 (en) * | 2011-12-19 | 2013-06-27 | ヤマハ発動機株式会社 | Object selecting device and object selecting method |
| CN116689081A (en) * | 2023-06-12 | 2023-09-05 | 苏州华天国科电力科技有限公司 | Method for separating carbon and silicon from primary polysilicon and device for using same |
| WO2025169978A1 (en) * | 2024-02-08 | 2025-08-14 | 日機装株式会社 | Cell aggregate recovery system |
-
1993
- 1993-05-27 JP JP12574393A patent/JP2967894B2/en not_active Expired - Lifetime
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5720394A (en) * | 1994-07-15 | 1998-02-24 | Yazaki Corporation | Sample supply unit for settling classification system |
| EP0753348A1 (en) * | 1995-07-10 | 1997-01-15 | Yazaki Corporation | Apparatus for classifying objects by sedimentation |
| US5875899A (en) * | 1995-07-10 | 1999-03-02 | Yazaki Corporation | Apparatus for classifying objects by sedimentation |
| US7802686B2 (en) | 2004-09-22 | 2010-09-28 | Fuji Xerox Co., Ltd. | Method and device for classifying fine particles |
| WO2011049229A1 (en) * | 2009-10-22 | 2011-04-28 | Jfeスチール株式会社 | Ferromagnetic material separation apparatus |
| WO2013093954A1 (en) * | 2011-12-19 | 2013-06-27 | ヤマハ発動機株式会社 | Object selecting device and object selecting method |
| JPWO2013093954A1 (en) * | 2011-12-19 | 2015-04-27 | ヤマハ発動機株式会社 | Object sorting apparatus and object sorting method |
| US9194865B2 (en) | 2011-12-19 | 2015-11-24 | Yamaha Hatsudoki Kabushiki Kaisha | Object selecting device and object selecting method |
| CN116689081A (en) * | 2023-06-12 | 2023-09-05 | 苏州华天国科电力科技有限公司 | Method for separating carbon and silicon from primary polysilicon and device for using same |
| WO2025169978A1 (en) * | 2024-02-08 | 2025-08-14 | 日機装株式会社 | Cell aggregate recovery system |
Also Published As
| Publication number | Publication date |
|---|---|
| JP2967894B2 (en) | 1999-10-25 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US9365815B2 (en) | Particle separation device and method of separating particles | |
| US20120202289A1 (en) | Separator device, deposition device and system for handling of somatic plant embryos | |
| JPH06328002A (en) | Precipitation classifying method and apparatus therefor | |
| Barlow et al. | Two-phase velocity measurements in dense particle-laden jets | |
| Xu et al. | Classification of ultrafine particles using a novel 3D-printed hydrocyclone with an arc inlet: experiment and CFD modeling | |
| JP3226201B2 (en) | Sedimentation classifier | |
| CN106140450B (en) | Microsphere separation device and separation method thereof | |
| JP2905507B2 (en) | Particle classification method and apparatus | |
| JPH0838930A (en) | Sample collection device for sedimentation classifier | |
| Jones et al. | Slip velocity of particulate solids in vertical tubes | |
| Han et al. | Flow visualization inside a water model virtual impactor | |
| CN214811660U (en) | A kind of fine particle classification device | |
| CN101085689A (en) | Accelerated sedimentation separation device and method for turbid water particles | |
| US5267653A (en) | Sorting method and sorting device | |
| CN208824085U (en) | Adjustable inertia separator | |
| JPH0824706A (en) | Sample feeder for sedimentation classifier | |
| US2330423A (en) | Separator | |
| JPH08332407A (en) | Wet classification device and wet classification method | |
| CN206139323U (en) | Microsphere separation device | |
| RU2140327C1 (en) | Method of enriching fine-fraction concentrates | |
| CN204933657U (en) | Super fine powder classifier | |
| US3446352A (en) | Method and apparatus for washing and grading swarf,for use in the mining or the mineral-oil industry | |
| JP3368519B2 (en) | Opening / closing mechanism of sample collection line in sedimentation classifier | |
| JPH0558779B2 (en) | ||
| CN221132653U (en) | Hydraulic classifier for mineral separation |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| A01 | Written decision to grant a patent or to grant a registration (utility model) |
Free format text: JAPANESE INTERMEDIATE CODE: A01 Effective date: 19990713 |
|
| FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20080820 Year of fee payment: 9 |
|
| FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20090820 Year of fee payment: 10 |
|
| FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20090820 Year of fee payment: 10 |
|
| FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20100820 Year of fee payment: 11 |
|
| FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20110820 Year of fee payment: 12 |
|
| FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20120820 Year of fee payment: 13 |
|
| FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20130820 Year of fee payment: 14 |
|
| EXPY | Cancellation because of completion of term |