JPH02194824A - Mixer of granules - Google Patents
Mixer of granulesInfo
- Publication number
- JPH02194824A JPH02194824A JP1014364A JP1436489A JPH02194824A JP H02194824 A JPH02194824 A JP H02194824A JP 1014364 A JP1014364 A JP 1014364A JP 1436489 A JP1436489 A JP 1436489A JP H02194824 A JPH02194824 A JP H02194824A
- Authority
- JP
- Japan
- Prior art keywords
- section
- dispersion section
- opening
- dispersion
- mixer
- 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.)
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- Adjustment And Processing Of Grains (AREA)
Abstract
Description
【発明の詳細な説明】 産業上の利用分野 本発明は、米等の粒体の混合装置に関する。[Detailed description of the invention] Industrial applications The present invention relates to a mixing device for grains such as rice.
従来の技術とその問題点
例えば、精米工場から出荷される白米は、複数の品種を
ブレンドしたものとされることがある。Conventional techniques and their problems For example, white rice shipped from a rice mill is sometimes a blend of multiple varieties.
この場合は、精米工程を経た白米が品種毎にタンクに収
容され、これらのタンクの下方を順次移動するスクリュ
ーコンベアに適宜排出され、該スクリューコンベアによ
り攪拌され混合せられることとなる。しかしながら、こ
のスクリューコンベアのみでは十分な攪拌が得られず、
品質の均一化が図れないという問題があった。In this case, the polished rice that has undergone the rice milling process is stored in tanks for each type, and is appropriately discharged to a screw conveyor that sequentially moves below these tanks, and is stirred and mixed by the screw conveyor. However, this screw conveyor alone cannot provide sufficient agitation;
There was a problem that it was not possible to achieve uniform quality.
この他、複数種の粒体を混合する手段として回転ドラム
中に粒体を収容して攪拌する方法などが採られていたが
、この場合はドラムの駆動装置等が必要であり、設備が
複雑化、大形化するという問題があった。In addition, a method of mixing multiple types of granules has been adopted, such as storing the granules in a rotating drum and stirring them, but this requires a drum drive device, etc., and the equipment is complicated. There was a problem of increasing size and size.
本発明は、これらの問題点を解決し、小形でかつ簡単な
構造により十分な混合を行なうことができる粒体の混合
装置を提供することを目的とする。An object of the present invention is to solve these problems and provide a granule mixing device that is small and has a simple structure and can perform sufficient mixing.
問題点を解決するための手段
本発明の前記目的は、頂部を上にして配置された円錐又
は多角錐形状の分散部と、該分散部の頂部に臨む開口を
備えたホッパと、前記分散部の下部を囲繞するように設
けられ該ホッパから前記分散部を経て流下した粒体を集
めて下方へ案内する振り分け部とを備え、前記分散部は
その傾斜面の途中に、該傾斜面を流下する粒体の一部を
通す開口を有し、前記振り分け部は、前記分散部の傾斜
面上を流下した粒体を下方へ案内する通路と、該通路の
下方に設けられた収集面とを備え、前記通路は、前記粒
体を前記分散部の半径方向へ振り分けるように多数個が
案内方向を少なくとも2つの異なる方向として前記分散
部の周方向に並設されており、前記収集面は、前記分散
部の開口及び前記通路から放出される粒体を集めて下方
へ案内する収集面とを備えていることを特徴とする粒体
の混合装置により達成される。Means for Solving the Problems The object of the present invention is to provide a dispersing section having a conical or polygonal pyramid shape arranged with its top facing upward, a hopper having an opening facing the top of the dispersing section, and a dispersing section. a distributing section that is provided to surround a lower part of the hopper and collect particles flowing down from the hopper through the dispersion section and guide them downward; The distribution section has an opening through which part of the particles are passed through, and the distribution section has a passage that guides the particles that have flowed down on the slope of the dispersion section downward, and a collection surface provided below the passage. A plurality of the passages are arranged in parallel in the circumferential direction of the dispersion section with guiding directions in at least two different directions so as to distribute the particles in the radial direction of the dispersion section, and the collection surface includes: This is achieved by a granule mixing device characterized in that it comprises an opening of the dispersion section and a collection surface that collects and guides the granules discharged from the passageway downward.
実施例
以下、本発明を白米の混合装置に適用した場合を例にと
って添付図面に基づき説明する。EXAMPLE Hereinafter, a case where the present invention is applied to a mixed machine for polished rice will be explained based on the accompanying drawings.
第1図に示すように、混合装置(10)は、収納タンク
(61)、 (62)、 (63)、 (64)
からスクリューコンベア(70)、昇降コンベア(80
)を経て送られる白米を受取るように配置されている。As shown in Fig. 1, the mixing device (10) includes storage tanks (61), (62), (63), (64).
From screw conveyor (70), lifting conveyor (80
) is arranged to receive the white rice sent through the station.
各収納タンクには種類の異なる白米が収容されており、
下部の吐出口から白米がスクリューコンベア(70)に
供給される。スクリューコンベア(70)により搬送さ
れた白米は、昇降コンベアのパケット(81)により上
昇せられ、混合装置(10)に送られる。混合装置(1
0)は、頂部を上にして配置された円錐形状の分散部(
20)と、該分散部の頂部に臨む下部開口を備えたホッ
パ(30)と、分散部(20)の下部を囲繞するように
設けられた振り分け部(40)とを備えている。この例
では、昇降コンベア(80)により搬送された白米をホ
ッパ(30)が受取る。Each storage tank stores different types of white rice.
Polished rice is supplied to the screw conveyor (70) from the lower discharge port. The polished rice conveyed by the screw conveyor (70) is lifted up by the packet (81) of the elevating conveyor and sent to the mixing device (10). Mixing device (1
0) is a conical dispersion section (
20), a hopper (30) having a lower opening facing the top of the dispersing section, and a sorting section (40) provided so as to surround the lower part of the dispersing section (20). In this example, the hopper (30) receives polished rice conveyed by the lifting conveyor (80).
この供給装置は、自動化のために有利なものであるが、
この他ベルトコンベアや人手操作によるもの等、混合装
置のホッパへの供給には適宜の手段を採用することがで
きる。This feeding device is advantageous for automation, but
In addition, any suitable means such as a belt conveyor or manual operation may be used for supplying the mixture to the hopper of the mixing device.
ホッパ(30)は側壁にレベル計(31)を備え、下端
部には該レベル計に連動するシャッタ(32)が装着さ
れている。これにより、ホッパ内に所定量が蓄積すると
シャッタ(32)が開かれ、白米が流下することとなる
。シャッタ(32)の下には、流下した白米が飛散しな
いように分散部の傾斜面に沿って、カバー(33)が設
けられている。シャッタ(32)から流下した白米は分
散部(20)に沿って流れる。分散部(第2図に一点鎖
線で示す)の円錐面の傾斜は、適用される粒体の種類に
応じて決められるが、円滑な流下をなすためには、その
粒体の安息角より大きい傾斜角とするのが望ましく、粒
体が1層の面をなして流れるように過大な傾斜角としな
いのが望ましい。The hopper (30) is equipped with a level meter (31) on the side wall, and a shutter (32) interlocked with the level meter is attached to the lower end. As a result, when a predetermined amount of rice is accumulated in the hopper, the shutter (32) is opened and the polished rice flows down. A cover (33) is provided below the shutter (32) along the slope of the dispersion section so that the polished rice that flows down is not scattered. The polished rice flowing down from the shutter (32) flows along the dispersion section (20). The slope of the conical surface of the dispersion section (shown by the dashed line in Figure 2) is determined depending on the type of particles to which it is applied, but in order to achieve smooth flow, it must be larger than the angle of repose of the particles. It is preferable to use an inclination angle, and it is preferable not to make the inclination angle too large so that the grains flow in one layer.
この例では約45° (白米の安息角:約30°)とさ
れている。この傾斜角の選択は、分散部を多角錐形状と
する場合にも当てはまる。また分散部(20)の頂部は
、適度の丸みを持たせるのが望ましい。これは、該頂部
が尖鋭であると、ホッパ(30)の排出口とこれに臨む
頂部との間の流下抵抗がホッパ内の収容量によって太き
(変化する場合があるから・である。一方、この頂部の
丸みは、流下を円滑にするように適度に小さい曲率半径
とされるのが望ましく、この例では、これらを勘案して
曲率半径的5mmの丸みとされている。分散部(20)
の傾斜面の上部には、該傾斜面を流下する白米の一部を
通すための開口が形成されている。この実施例では鎖孔
は白米よりやや径の大きい多数の小孔(21)とされて
いる。もっとも、該開口は種々の形態とすることができ
、例えば分散部(20)の周方向に連続するように形成
された間隙、或いは該周方向に設けられ複数の白米を一
度に通過させ得る比較的大きな孔とすることができる。In this example, it is approximately 45° (the angle of repose of white rice: approximately 30°). This selection of the inclination angle also applies to the case where the dispersion section has a polygonal pyramid shape. Further, it is desirable that the top of the dispersion section (20) be appropriately rounded. This is because if the top is sharp, the flow resistance between the outlet of the hopper (30) and the top facing it will be thick (and may change) depending on the capacity inside the hopper. It is desirable that the radius of curvature of this top part is appropriately small to make the flow smooth, and in this example, taking these into consideration, the radius of curvature is rounded to 5 mm. )
An opening is formed in the upper part of the sloping surface to allow a portion of the polished rice flowing down the sloping surface to pass through. In this embodiment, the chain holes are a number of small holes (21) whose diameter is slightly larger than that of polished rice. However, the opening can have various forms, for example, a gap formed continuously in the circumferential direction of the dispersion section (20), or a gap formed in the circumferential direction and allowing a plurality of polished rice to pass through at once. It can be made with a large hole.
また、第4図に示すように、上部が開いた殻状のガイド
(22)を小孔(21)の下部に設けることもでき、こ
れにより小孔(21)への流入をより確実にすることが
できる。振り分け部(40)は、第2図に縦断面を示す
ように、カップ形状の外壁(41)の内周部に上下に延
びる分割壁(42)を多数設け、該分割壁の上下の中間
部に分散部(20)の円錐の底面が接するようにしたも
のである。したがって、振り分け部(40)の内部には
、分割壁(42)で分割されて形成された通路が周方向
に多数並び、各々の開口部は分散部(20)に臨んでい
る。振り分け部(40)の内部には、さらに内底面(4
3)が備えられている。該内底面は、分散部(20)よ
り下方にある分割壁(42)の下端からやや下降しなが
ら半径方向内方へ延び中央部に開口(44)を形成して
いる。内底面(43)はまた、周方向に並ぶ通路に対し
1つ置きに該通路の底部を形成するように、やや上昇し
つつ半径方向外方へ延びている。Furthermore, as shown in Fig. 4, a shell-shaped guide (22) with an open top can be provided at the bottom of the small hole (21), thereby making the flow into the small hole (21) more reliable. be able to. As shown in the vertical cross section in FIG. 2, the distribution part (40) is provided with a large number of vertically extending dividing walls (42) on the inner circumference of a cup-shaped outer wall (41), and the upper and lower intermediate parts of the dividing walls are The bottom surface of the cone of the dispersion section (20) is in contact with the dispersion section (20). Therefore, inside the distribution part (40), a large number of passages divided by the dividing wall (42) are lined up in the circumferential direction, and each opening faces the distribution part (20). Inside the distribution part (40), there is further an inner bottom surface (4
3) is provided. The inner bottom surface extends radially inward while slightly descending from the lower end of the dividing wall (42) located below the dispersion portion (20), and forms an opening (44) in the center. The inner bottom surface (43) also extends radially outwardly with a slight rise to form the bottom of every other circumferentially aligned passageway.
したがって、該底部を有する通路(45a)と、該底部
がなく底面を開放された通路(45b)とが、交互に配
置されている。外壁(41)の下部は下降しつつ半径方
向内方へ延び中央部に開口(46)を形成し、その傾斜
面は流下する白米を集めて下方へ案内する収集面(47
)となっている。Therefore, passages (45a) having the bottom and passages (45b) having an open bottom without the bottom are arranged alternately. The lower part of the outer wall (41) extends radially inward while descending to form an opening (46) in the center, and its sloped surface forms a collection surface (47) that collects the flowing polished rice and guides it downward.
).
振り分け部(40)の開口(46)には、スクリューコ
ンベア(90)が臨んでいる。該コンベアは、受取った
白米をスクリューによってさらに攪拌し混合させながら
搬送し、排出口(91)から次工程に送る。A screw conveyor (90) faces the opening (46) of the sorting section (40). The conveyor conveys the received polished rice while further stirring and mixing it with a screw, and sends it to the next process from the discharge port (91).
この混合装置は、次のように作用する。ホッパ(30)
に所定量の白米が蓄積するとレベル計の作動に応じてシ
ャッタ(32)が開かれ、白米は分散部(20)の傾斜
面上を流下する。その一部は、第2図に矢印Cで示すよ
うに、小孔(21)から落下し、直接に開口(46)か
ら、或いは収集面(47)を経て開口(46)から排出
される。This mixing device works as follows. Hopper (30)
When a predetermined amount of polished rice has accumulated, the shutter (32) is opened in response to the operation of the level meter, and the polished rice flows down on the slope of the dispersion section (20). A portion thereof falls through the small hole (21) and is discharged either directly through the opening (46) or via the collection surface (47) through the opening (46), as shown by arrow C in FIG.
このように傾斜面の途中から落下する白米は他の白米よ
り早(排出されることとなり、これにより他の白米との
間の混合がなされる。傾斜面を最後まで流下する白米は
、該傾斜面を薄い層状となって流れる。この流れは、前
述のように望ましくは1層の流れとされる。この層状化
により、ホッパ内で塊状となっていた同一品種の白米は
分散部の周方向に沿って分散する。傾斜面を最後まで流
下した白米は、さらに通路(45a)又は通路(45b
)に流入する。通路(45a)に流入した白米は、矢印
Aで示すように、先ず内底壁(43)に案内されて半径
方向内方へ向かって流れて開口(44)から落下し、直
接その下の開口(46)。In this way, the white rice that falls from the middle of the slope is discharged faster than other white rice, and as a result, it mixes with other white rice. It flows in a thin layer on the surface.As mentioned above, this flow is preferably a single layer flow.By this layering, the white rice of the same variety that has become lumps in the hopper is spread in the circumferential direction of the dispersion section. The white rice that has flown down the slope to the end is further distributed along the passage (45a) or the passage (45b).
). As shown by arrow A, the polished rice that has flowed into the passageway (45a) is first guided by the inner bottom wall (43), flows radially inward, falls from the opening (44), and directly falls into the opening below. (46).
に、又は収集面(47)上を経て開口(46)に至る。or over the collection surface (47) to the opening (46).
一方、通路(45b)に流入した白米は、矢印Bで示す
ように、該通路を下方へ通過し収集面(47)上を滑降
して開口(46)に至る。このように分散部(20)の
傾斜面を最後まで流下する白米は、分散部(20)でそ
の円錐形状の周方向に分散され、ついで振り分け部(4
0)でそのカップ形状の半径方向に振り分けられて分散
するというように、相互に交わる方向に分散させられる
こととなる。したがって、混合装置(10)を通過する
白米は、これら分散部における落下開始時期の相違及び
振り分け部を経た相交わる方向への分散により、充分な
混合が行なわれる。また、振り分け部(40)を経る際
の混合作用には、−旦傾斜の緩やかな内底壁(43)を
経る場合と、直接収集面(47)に至る場合との流下速
度の相違による収集の時間差乃至多段化も寄与している
と思われる。On the other hand, the polished rice that has flowed into the passageway (45b) passes downwardly through the passageway, as shown by arrow B, and slides down on the collection surface (47) to reach the opening (46). In this way, the polished rice flowing down the slope of the dispersion section (20) to the end is dispersed in the circumferential direction of the conical shape in the dispersion section (20), and is then distributed in the distribution section (4).
At 0), the particles are distributed in the radial direction of the cup shape and are dispersed, and thus the particles are dispersed in directions that intersect with each other. Therefore, the polished rice passing through the mixing device (10) is sufficiently mixed due to the difference in the falling start timing in these dispersion sections and the dispersion in mutually intersecting directions through the distribution section. In addition, the mixing effect when passing through the distribution section (40) is due to the difference in the flow rate between when passing through the gently sloped inner bottom wall (43) and when directly reaching the collection surface (47). It is thought that the time difference or multi-stage structure also contributes.
以上の実施例では、通路(45a)、(45b)という
ように2個の通路を1単位としたが、3個以上の通路を
1単位とし、1単位内の通路の案内方向を相互に半径方
向に異ならせ、該単位を繰返し配置したものとしてもよ
く、或いは通路の案内方向を特定の単位を形成すること
なく半径方向に異ならせてもよい。3個を1単位とする
場合は、第3図に振り分け部(40−)の概略を示すよ
うに、2つの内底壁(43a)、(43b)が設けられ
収集壁(47)を含めて3段の構成となる。In the above embodiment, two passages such as the passages (45a) and (45b) are regarded as one unit, but three or more passages are regarded as one unit, and the guiding directions of the passages within one unit are set to be radial from each other. The units may be arranged repeatedly in different directions, or the guiding directions of the passages may be different in the radial direction without forming specific units. When three pieces are used as one unit, two inner bottom walls (43a) and (43b) are provided, including the collecting wall (47), as shown schematically in FIG. 3 of the sorting part (40-). It has a three-stage configuration.
流下する白米は、分散部(20)の途中から落下する流
れ(D)、及び分散部(20)を流下したのち、分割壁
(42)で仕切られた通路を通る流れ(A)、(B)、
(C)の合計4種の流れとなり、より良好な混合が行な
われる。The flowing polished rice is divided into a flow (D) that falls from the middle of the dispersion section (20), and a flow (A) and (B) that flows down the dispersion section (20) and then passes through a passage partitioned by a dividing wall (42). ),
There are a total of four types of flows (C), and better mixing is achieved.
以上、白米を例にとって説明したが、同様にして各種の
穀類、豆類、その他の粒体の混合に、本発明装置を適用
できるのは勿論である。Although the above explanation has been made using polished rice as an example, it goes without saying that the apparatus of the present invention can be similarly applied to mixing various grains, beans, and other grains.
発明の効果
以上から明らかなように、本発明によれば、次の効果を
奏する粒体の混合装置を提供することができる。すなわ
ち、円錐又は多角錐形状の分散部の頂部にホッパから流
下した粒体は、先ず分散部の傾斜面の途中から落下する
ものと傾斜面を最後まで流下するものとに分けられ、こ
の落下時期の相違により、収集面又は下部開口への到達
時期がずれて排出時点での混合が行なわれ。また傾斜面
を流下した粒体はその傾斜面上を滑降するときに薄い層
状となって錐体の周方向に分散し、振り分け部の通路を
通過する際には半径方向に振り分けられて該方向に分散
し、これら合い交わる方向への分散後に収集面により集
められるので、ここでも混合が行なわれることとなる。Effects of the Invention As is clear from the above, according to the present invention, it is possible to provide a granule mixing device that exhibits the following effects. In other words, the particles that flow down from the hopper to the top of the conical or polygonal pyramid-shaped dispersion section are divided into those that first fall halfway down the slope of the dispersion section and those that flow all the way down the slope. Due to this difference, the timing of reaching the collection surface or lower opening is delayed, resulting in mixing at the time of discharge. In addition, when the particles flow down the slope, they form a thin layer and are dispersed in the circumferential direction of the cone, and when they pass through the passage in the distribution section, they are distributed in the radial direction. Mixing occurs here as well, as the particles are dispersed in the opposite directions and collected by the collection surface after dispersion in the intersecting directions.
したがって、粒体の流下に伴うこれら両温合作用により
、十分な混合が行なわれるのである。またこのための構
造は、駆動源や動きを伴う部材を必要とすることのない
簡単なものとなっている。Therefore, due to these warming effects as the particles flow down, sufficient mixing is achieved. Moreover, the structure for this is simple and does not require a driving source or moving members.
図は本発明の実施例を示すもので、第1図は混合装置を
その給排装置と共に示す正面図、第2図は混合装置にお
ける振り分け部を縦断した状態で示す斜視図、第3図は
混合装置の他の例を概略的に示す縦断端面図、第4図は
分散部の他の例を一部切り欠いて示す斜視図である。
(10)・・・・・・混合装置
(20)・・・・・・分散部
(21)・・・・・・小孔(開口)
(30)・・・・・・ホッパ
(40)、(4CI)・・・・・・振り分け部(42)
・・・・・・分割壁
(43)、 (43a)、 (43b)−・内底壁
(44)・・・・・・開口
(45a) 、 (45b) −通路(46)・・・
・・・開口
(47)・・・・・・収集面
(以 上)
第
図
第
図
3゜
ホッパ
・開口
40、 40’・ 扱つ%lす部
45a、 45b−
通路
9.介粋1璧
・・關OThe figures show an embodiment of the present invention; FIG. 1 is a front view showing the mixing device together with its supply/discharge device, FIG. 2 is a perspective view showing the distribution section of the mixing device in a longitudinal section, and FIG. FIG. 4 is a vertical cross-sectional end view schematically showing another example of the mixing device, and FIG. 4 is a partially cutaway perspective view showing another example of the dispersion section. (10)...Mixing device (20)...Dispersion section (21)...Small hole (opening) (30)...Hopper (40), (4CI)...Distribution section (42)
...Dividing walls (43), (43a), (43b) - Inner bottom wall (44) ... Openings (45a), (45b) - Passage (46)...
... Opening (47) ... Collection surface (above) Fig. Fig. 3゜Hopper Opening 40, 40' Handling section 45a, 45b - Passage 9. The best person...Kan O
Claims (1)
分散部と、該分散部の頂部に臨む開口を備えたホッパと
、前記分散部の下部を囲繞するように設けられ該ホッパ
から前記分散部を経て流下した粒体を集めて下方へ案内
する振り分け部とを備え、前記分散部はその傾斜面の途
中に、該傾斜面を流下する粒体の一部を通す開口を有し
、前記振り分け部は、前記分散部の傾斜面上を流下した
粒体を下方へ案内する通路と、該通路の下方に設けられ
た収集面とを備え、前記通路は、前記粒体を前記分散部
の半径方向へ振り分けるように多数個が案内方向を少な
くとも2つの異なる方向として前記分散部の周方向に並
設されており、前記収集面は、前記分散部の開口及び前
記通路から放出される粒体を集めて下方へ案内する収集
面とを備えていることを特徴とする粒体の混合装置。(1) A conical or polygonal pyramid-shaped dispersion section arranged with the top up, a hopper equipped with an opening facing the top of the dispersion section, and a hopper provided so as to surround the lower part of the dispersion section from which the hopper is disposed. and a distribution section that collects the particles flowing down through the dispersion section and guides them downward, and the dispersion section has an opening in the middle of the slope thereof, through which a part of the particles flowing down the slope passes. , the sorting section includes a passage that guides the particles flowing down on the inclined surface of the dispersion section downward, and a collection surface provided below the passage, and the passage allows the particles to be distributed in the dispersion section. A plurality of collecting surfaces are arranged in parallel in the circumferential direction of the dispersion section with guiding directions in at least two different directions so as to be distributed in the radial direction of the dispersion section, and the collecting surface is discharged from the opening of the dispersion section and the passage. A granule mixing device characterized by comprising a collection surface that collects granules and guides them downward.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1014364A JPH02194824A (en) | 1989-01-23 | 1989-01-23 | Mixer of granules |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1014364A JPH02194824A (en) | 1989-01-23 | 1989-01-23 | Mixer of granules |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH02194824A true JPH02194824A (en) | 1990-08-01 |
| JPH0525532B2 JPH0525532B2 (en) | 1993-04-13 |
Family
ID=11859004
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1014364A Granted JPH02194824A (en) | 1989-01-23 | 1989-01-23 | Mixer of granules |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH02194824A (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2015157252A (en) * | 2014-02-24 | 2015-09-03 | シャープ株式会社 | Mixture producing apparatus |
| CN108114622A (en) * | 2018-01-15 | 2018-06-05 | 浙江大学 | A kind of method of the prismatic cover dispersive element of interlayer and dispersion phase |
| CN108211421A (en) * | 2018-01-24 | 2018-06-29 | 浙江大学 | A kind of dual channel taper extraction element and the method for percolation extraction |
| CN108245929A (en) * | 2018-01-15 | 2018-07-06 | 浙江大学 | A kind of method of interlayer cone cover dispersive element and dispersion phase |
-
1989
- 1989-01-23 JP JP1014364A patent/JPH02194824A/en active Granted
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2015157252A (en) * | 2014-02-24 | 2015-09-03 | シャープ株式会社 | Mixture producing apparatus |
| CN108114622A (en) * | 2018-01-15 | 2018-06-05 | 浙江大学 | A kind of method of the prismatic cover dispersive element of interlayer and dispersion phase |
| CN108245929A (en) * | 2018-01-15 | 2018-07-06 | 浙江大学 | A kind of method of interlayer cone cover dispersive element and dispersion phase |
| CN108211421A (en) * | 2018-01-24 | 2018-06-29 | 浙江大学 | A kind of dual channel taper extraction element and the method for percolation extraction |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0525532B2 (en) | 1993-04-13 |
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