JPH0773642B2 - Solid-liquid separation device - Google Patents
Solid-liquid separation deviceInfo
- Publication number
- JPH0773642B2 JPH0773642B2 JP61147815A JP14781586A JPH0773642B2 JP H0773642 B2 JPH0773642 B2 JP H0773642B2 JP 61147815 A JP61147815 A JP 61147815A JP 14781586 A JP14781586 A JP 14781586A JP H0773642 B2 JPH0773642 B2 JP H0773642B2
- Authority
- JP
- Japan
- Prior art keywords
- solid
- liquid
- inner diameter
- plate
- threaded body
- 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.)
- Expired - Lifetime
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Description
【発明の詳細な説明】 〔産業上の利用分野〕 本発明は固液分離装置に関し、特にアルミニユームの切
粉を液体中から分離させて回収するのに適したものであ
る。TECHNICAL FIELD The present invention relates to a solid-liquid separator, and is particularly suitable for separating aluminum chips from a liquid and collecting the chips.
従来、工作機械から生じる金属切粉を液体中から分離す
るについては、金網ですという方法が主流であるが、
頻繁に目詰まりを生ずるため、逆洗装置を附設して常時
これを駆動させておく必要があり、また、スクレーパー
によつて詰りを掻き取る際に往々にして金網が破れると
いう欠点がある。Conventionally, wire mesh is the mainstream method for separating metal chips generated from machine tools from liquid,
Since it frequently causes clogging, it is necessary to attach a backwashing device to drive it continuously, and there is a drawback that the wire mesh is often broken when scraping the clogging with a scraper.
本発明の目的は、詰りを生じることがなく、逆洗装置や
スクレーパーの附設を必要としない固液分離装置を提供
することにある。An object of the present invention is to provide a solid-liquid separation device that does not cause clogging and does not require a backwash device or a scraper.
本発明に係る固液分離装置では、固液収容函から排出口
へ至る間において、内径面が後記螺施体の山部外周から
谷部外周に沿つて偏心状に嵌合するよう穿孔された複数
枚の可動環状板を軸方向へ積層状に配列させ、内径面が
後記螺施体の山部外周とほぼ同心状に嵌合するよう穿孔
された複数枚の環状間板を上記可動環状板の積層間に介
在させて固定体に支承させ、これら可動環状板または環
状間板の板面要所に間隔保持用摺動凸子を配設すること
により、隣接板面間において内径方向から外径方向へ至
る狭隙状の液体流出溝を形成せしめ、原動機で駆動され
る芯材を横軸としてその外周に螺状フィンを巻装させて
なる螺施体を固液収容函内から排出口の開口方向へ伸延
させて螺施繰出機溝を構成すると共に上記螺施体の伸延
部を可動環状板および環状間板の中心孔に貫挿させるこ
とにより、螺施体の山部外周が可動環状板の内径面を押
圧しつつ環状間板の内径面に沿つて回転して可動環状板
に偏心回転運動を行わせるよう構成し、螺施繰出機溝の
駆動時に固液収容函内の固液が軸方向に移送せしめられ
て液体は液体流出溝から外側へ流出せしめられると共に
固形物は前方の排出口から排出せしめられ、且つ、液体
流出溝に入り込んだ微小固形物は可動環状板の偏心回転
運動に伴なう前記摺動凸子の摺動作用と液体の流出作用
によつて除却せられるよう構成したのである。In the solid-liquid separation device according to the present invention, the inner diameter surface is perforated so as to be fitted eccentrically along the outer circumference of the ridge portion of the screwed body from the outer circumference of the ridge portion between the solid-liquid storage box and the outlet. The plurality of movable annular plates are arranged in a stacked manner in the axial direction, and the plurality of annular interstitial plates are punched so that the inner diameter surface is fitted substantially concentrically with the outer periphery of the threaded portion of the threaded body described later. Of the movable annular plate or annular interstitial plate, and by disposing the spacing-holding sliding protrusions at key points on the plate surface of the movable annular plate or annular interstitial plate, the space between the adjacent plate surfaces is removed from the inner diameter direction. A threaded body formed by forming a narrow gap-shaped liquid outflow groove extending in the radial direction and winding a spiral fin around the outer circumference of the core material driven by the prime mover is discharged from the solid-liquid storage box. To form a screw-feeding machine groove in the opening direction, and the extension portion of the screw-applied body is provided with a movable annular plate or And the center hole of the annular disc, the outer periphery of the threaded portion of the threaded body rotates along the inner surface of the annular disc while pressing the inner surface of the movable annular plate, causing eccentric rotation of the movable annular plate. When the screw feeding and feeding machine groove is driven, the solid-liquid in the solid-liquid storage box is transferred in the axial direction so that the liquid flows out to the outside from the liquid outflow groove and the solid matter is discharged to the front. The fine solids discharged from the outlet and entering the liquid outflow groove are removed by the sliding action of the sliding protrusions and the outflow action of the liquid accompanying the eccentric rotational movement of the movable annular plate. I configured it.
実施例の図面において、1は上面に固液投入口2を開口
させた固液収容函、3は固液収容函1から所定の間隔を
隔てて前方に開設された排出口、4は固液収容函1の後
方に設置せられたモーター等の原動機、5は原動機4に
より低速に回転される螺施体であつて、例えば第2図
〔イ〕に見られるよう1本の芯材6aを横軸としてその外
周に螺状フィン7aを巻付け、或いは第2図〔ロ〕に見ら
れるよう定間隔に並列させた複数本の芯材6b……6bを横
軸としてその外周に螺状フィン7bを巻付けて、山部と谷
部を有する螺施体となし、該螺施体5を固液収容函1内
から排出口3の開口方向へ伸延させることにより螺施繰
出機溝8が構成される。9……9は金属薄板で作られた
可動環状板であつて、固液収容函1から排出口3へ至る
間において複数枚を軸方向へ積層状に配列し、内径面を
前記螺施体5の山部外周から谷部外周に沿つて偏心状に
嵌合させるため、内径bが螺施体5の山径Mよりも小径
で谷径Gよりは大径となるよう穿孔せられている。10…
…10は金属薄板で作られた環状間板であつて、上記可動
環状間板9……9の積層間に介在させた状態により固定
体11に支承せられ、内径面を前記螺施体5の山部外周と
ほぼ同心状に嵌合させるため、内径Bが螺施体5の山径
Mと同径かまたはそれよりも僅かに大径となるよう穿孔
せられている。そしてこれら可動環状板9……9または
環状間板10……10の板面要所に、固体過粒径を規正す
るための間隔保持用摺動凸子12……12を配設することに
より、隣接板面間において内径方向から外径方向へ至る
狭隙状の液体流出溝13……13を形成せしめるのである。
間隔保持用摺動凸子12……12の凸設態様としては、第7
図〔イ〕に見られるごとく可動環状板9……9の両面に
凸設させてもよく、或いは第7図〔ロ〕に見られるごと
く可動環状板9……9および環状間板10……10の夫々の
片面同一方向に凸設させてもよい。前記螺施体5の伸延
部は可動環状板9……9および環状間板10……10の中心
孔に貫挿されるのであるが、既述のように可動環状板9
の内径bと環状間板10の内径Bとに直径差が附せられて
いるので、螺施体5が回転すればその山部外周が可動環
状板9の内径面を押圧しつつ環状間板10の内径面に沿つ
て回転し、可動環状板9は偏心回転運動を行わせられる
ことになる。In the drawings of the embodiment, 1 is a solid-liquid container with a solid-liquid inlet 2 opened on the upper surface, 3 is a discharge port opened forward from the solid-liquid container 1 at a predetermined interval, and 4 is solid liquid. A prime mover 5 such as a motor installed at the rear of the housing box 1 is a screw body rotated at a low speed by the prime mover 4, and for example, one core member 6a is provided as shown in FIG. A spiral fin 7a is wound around the outer periphery as the horizontal axis, or a plurality of core materials 6b ... 6b arranged in parallel at regular intervals as seen in FIG. 7b is wound to form a threaded body having ridges and valleys, and the threaded body 5 is extended from the inside of the solid-liquid storage box 1 in the opening direction of the discharge port 3 to form the threading feeder groove 8. Composed. Reference numeral 9 indicates a movable annular plate made of a thin metal plate, and a plurality of the movable annular plates are arranged in the axial direction in a laminated manner between the solid-liquid storage box 1 and the discharge port 3, and the inner diameter surface is formed by the threaded body. 5 is eccentrically fitted from the outer circumference of the crest portion to the outer circumference of the trough portion, so that the inner diameter b is perforated such that the inner diameter b is smaller than the mountain diameter M of the threaded body 5 and larger than the valley diameter G. . Ten…
Reference numeral 10 denotes an annular spacer made of a thin metal plate, which is supported by the fixed body 11 in a state of being interposed between the movable annular spacers 9 ... In order to fit the outer periphery of the crest portion substantially concentrically, the inner diameter B is perforated such that the inner diameter B is the same as or slightly larger than the crest diameter M of the threaded body 5. Then, by disposing the sliding projections 12 ... 12 for maintaining the spacing for regulating the solid particle diameter in the plate surface points of the movable annular plates 9 ... 9 or the annular spacers 10. , Narrow gap-shaped liquid outflow grooves 13 are formed between the adjacent plate surfaces from the inner diameter direction to the outer diameter direction.
The spacing protrusions 12 ...
As shown in FIG. 7 (b), the movable annular plates 9 ... 9 may be projected on both sides, or, as shown in FIG. 7 (b), the movable annular plates 9 ... 9 and the annular spacer 10 ... Each of the ten surfaces may be convexly provided in the same direction. The extending portion of the threaded body 5 is inserted into the center holes of the movable annular plates 9 ... 9 and the annular interphase plates 10 ... 10, but as described above, the movable annular plates 9 ...
Since there is a difference in diameter between the inner diameter b of the annular disc 10 and the inner diameter B of the annular disc 10, when the threaded body 5 rotates, the outer periphery of the mountain portion presses the inner diameter surface of the movable annular plate 9 while the annular disc is rotated. By rotating along the inner diameter surface of 10, the movable annular plate 9 is caused to perform an eccentric rotation motion.
可動環状板9……9の外径aは、環状間板10……10の内
径Bよりも大径で外径Aよりは小径となし、螺施体5の
谷部外周によつて可動環状板9……9が環状間板10……
10の外周からはみ出さないよう規正される。The outer diameter a of the movable annular plates 9 ... 9 is larger than the inner diameter B of the annular interstitial plates 10 ... 10 and smaller than the outer diameter A, and is movable by the outer circumference of the valley portion of the threaded body 5. Plate 9 ... 9 is an annular plate 10 ...
It is regulated so that it does not protrude from the outer periphery of 10.
可動環状板9と環状間板10との最も望ましい寸法比率を
第3図および第4図について説明すると、 a=A−α 〔注〕α:外径差 α<W W=W′ ということになる。αがWより大きくなると、過物の
粒径の規正が行えなくなる。また、WがW′よりも大き
くなれば液体流出溝13……13のクリーニング効果が低下
するし、W′がWよりも大きくなれば可動環状板9を破
損するおそれがある。環状間板10の内径Bは、螺施体5
の回転が円滑に行われるよう螺施体の山径Mよりも僅か
に大径とすることが望ましい。螺施体の山径Mと可動環
状板の内径bとの差が、可動環状板9の半径方向への摺
動量となる。そして可動環状板9が過大に偏心しないよ
うに、螺施体の谷径Gを設定するのである。The most desirable dimensional ratio between the movable annular plate 9 and the annular spacer 10 will be described with reference to FIGS. 3 and 4. a = A-α [Note] α: outer diameter difference α <W W = W ′ Become. If α is larger than W, it becomes impossible to regulate the particle size of the excess material. Further, if W is larger than W ', the cleaning effect of the liquid outflow grooves 13 ... 13 is deteriorated, and if W'is larger than W, the movable annular plate 9 may be damaged. The inner diameter B of the annular spacer 10 is 5
It is desirable that the diameter is slightly larger than the thread diameter M of the threaded body so that the rotation can be performed smoothly. The difference between the thread diameter M of the threaded body and the inner diameter b of the movable annular plate is the amount of sliding of the movable annular plate 9 in the radial direction. The root diameter G of the threaded body is set so that the movable annular plate 9 is not excessively eccentric.
固液収容函1内へ充填された固液は螺施体5に沿つて前
後方向へ流れ込み、積層された可動環状板9……9およ
び環状間板10……10の中心孔へ流入する。そして螺施繰
出機溝8を低速駆動させると、固液は螺施体5に沿つて
軸方向へ前進せしめられ、液体は液体流出溝13……13よ
り外側へ流出せしめられると共に固形物は前方の排出口
3より排出せしめられる。そして液体流出溝13……13に
入り込んだ微小固形物は、摺動凸子12……12の摺動作用
と液体の流出作用によつて除却せられることになるが、
固体過粒径の規正、つまり、排出口3から排出させる
固形物と液体流出溝13……13から流下させる微小固形物
との選り分けは、液体流出溝13……13の溝の深さ即ち間
隔保持用摺動凸子12……12の高さtによつて設定され
る。従つて、凸子12……12の高さを異にした交換用の可
動環状板9……9を予め各種用意しておき、これを適宜
差し替えることによつて固体過粒径の規正基準を任意
に変更することができるのである。The solid-liquid filled in the solid-liquid storage box 1 flows in the front-rear direction along the threaded body 5, and flows into the center holes of the stacked movable annular plates 9 ... When the screw-feeding machine groove 8 is driven at a low speed, the solid liquid is advanced in the axial direction along the screw-applying body 5, the liquid is caused to flow out from the liquid outflow grooves 13 ... 13 and the solid matter is moved forward. It is discharged from the discharge port 3 of. The fine solid matter that has entered the liquid outflow grooves 13 ... 13 can be removed by the sliding action of the sliding protrusions 12 ... 12 and the outflow action of the liquid.
The regulation of the solid over-particle size, that is, the selection of the solid matter discharged from the discharge port 3 and the minute solid matter flowing down from the liquid outflow groove 13 ... 13 is performed by the depth or interval of the liquid outflow groove 13 ... 13. It is set by the height t of the holding sliding protrusion 12 ... 12. Therefore, various movable annular plates 9 ... 9 for exchange having different heights of the convex elements 12 ... 12 are prepared in advance, and by appropriately replacing them, the regulation standard of the solid over-particle diameter is determined. It can be changed arbitrarily.
本発明装置においては、螺施体5の駆動に伴う可動環状
板9……9の偏心回転運動により、固液分離作用と同時
にクリーニング作用が行われるので目詰まりを生ずるこ
とがなく、逆洗装置やスクレーパーを必要としないとい
う利点がある。しかも固体過粒径の規正、つまり排出
口3から排出させる固形物と液体流出溝13……13から流
下させる微小固形物との選り分けを、流体流出溝13……
13の溝の深さ即ち間隔保持用摺動凸子12……12の高さt
によつて設定するという方式であるから、凸子12……12
の高さを異にした交換用の可動環状板9……9を予じめ
各種用意しておけば、これを差し替えることによつて固
体過粒径の規正基準を任意に変更することができ、極
めて便利である。また、本発明装置における螺施体5
は、単なるリボンスクリューではなく、芯材を横軸とし
てその外周に螺状フィンを巻装させた強固な構成である
ため、濃度の高い固液や粘性の強い固液の中においても
変形することなく有効に過機能を果し得るのである。In the device of the present invention, since the cleaning action is performed simultaneously with the solid-liquid separation action by the eccentric rotation movement of the movable annular plates 9 ... 9 accompanying the driving of the screw applying body 5, clogging does not occur, and the backwashing device does not occur. It has the advantage that no scraper or scraper is required. Moreover, the regulation of the solid particle size, that is, the selection of the solid matter discharged from the discharge port 3 and the minute solid matter flowing down from the liquid outflow groove 13 ...
The depth of the groove of 13, that is, the height t of the sliding protrusion 12 ...
Since it is a method of setting by using,
If various kinds of movable annular plates 9 for replacement with different heights are prepared in advance, by replacing them, it is possible to arbitrarily change the regulation standard for the solid particle size. , Very convenient. Further, the threaded body 5 in the device of the present invention
Is not a mere ribbon screw, but has a rigid structure with a spiral fin wound around the core with the horizontal axis as the horizontal axis, so it can be deformed even in a solid liquid with high concentration or a solid liquid with high viscosity. Without it, it can effectively perform overfunction.
第1図は本発明装置の外観側面図、第2図は本発明装置
における螺施体の構造例を示した外観側面図であつて、
〔イ〕は横軸に凸条を螺施状に巻付けて山部と谷部を有
する螺施体を構成した事例、〔ロ〕は螺施状に巻回され
たリボンスクリューの内側要所に底板を当接して山部と
谷部を有する螺施体を構成した事例である。第3図は本
発明装置における可動環状板の正面図、第4図は本発明
装置における環状間板の正面図である。第5図は本発明
装置における可動環状板および環状間板と螺施体の関係
を示した要部縦断側面図であつて、〔イ〕は第2図
〔イ〕の螺施体を用いた事例、〔ロ〕は第2図〔ロ〕の
螺施体を用いた事例である。第6図〔イ〕は第5図
〔イ〕のY−Y線における縦断正面図、第6図〔ロ〕は
第5図〔ロ〕のY−Y線における縦断正面図である。第
7図〔イ〕は間隔保持用摺動凸子を可動環状板の両面に
凸設させた事例を示す要部縦断側面図、第7図〔ロ〕は
間隔保持用摺動凸子を可動環状板および環状間板の夫々
の片面同一方向に凸設させた事例を示す要部縦断側面図
である。第8図は本発明装置における環状間板の支承態
様を例示した要部縦断正面図である。 1……固液収容函、3……排出口、4……原動機、5…
…螺施体、8……螺施繰出機溝、9……可動環状板、10
……環状間板、12……間隔保持用摺動凸子、13……流体
流出溝。FIG. 1 is an external side view of the device of the present invention, and FIG. 2 is an external side view showing a structural example of a threaded body in the device of the present invention.
[A] is a case where a screw is wound around the horizontal axis to form a threaded body having ridges and valleys, and [B] is the inner side of a ribbon screw wound in a threaded shape. This is an example in which a bottom plate is brought into contact with and a threaded body having peaks and valleys is formed. FIG. 3 is a front view of a movable annular plate in the device of the present invention, and FIG. 4 is a front view of an annular plate in the device of the present invention. FIG. 5 is a vertical sectional side view of a main part showing the relationship between the movable annular plate and the annular interstitial plate and the threaded body in the device of the present invention, [a] using the threaded body of FIG. 2 [a]. The case [B] is a case using the threaded body of FIG. FIG. 6B is a vertical sectional front view taken along the line YY of FIG. 5B, and FIG. 6B is a vertical sectional front view taken along the line YY of FIG. 5B. FIG. 7 (a) is a vertical sectional side view of a main part showing an example in which the spacing holding sliding protrusions are provided on both sides of the movable annular plate, and FIG. 7 (b) shows the spacing holding sliding protrusions movable. It is a principal part longitudinal cross-sectional view which shows the example in which the annular plate and the annular interstitial plate were made to project in the same direction on one side. FIG. 8 is a vertical cross-sectional front view of a main part illustrating the bearing mode of the annular disc in the device of the present invention. 1 ... Solid-liquid storage box, 3 ... Discharge port, 4 ... Motor, 5 ...
… Screwed body, 8 …… Screwed feeding machine groove, 9 …… Movable annular plate, 10
…… Annular disc, 12 …… Sliding protrusions for maintaining spacing, 13 …… Fluid outflow groove.
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 B01D 33/58 ─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 6 Identification code Office reference number FI technical display location B01D 33/58
Claims (1)
いて、内径面が後記螺施体(5)の山部外周から谷部外周
に沿つて偏心状に嵌合するよう穿孔された複数枚の可動
環状板(9)……(9)を軸方向へ積層状に配列させ、内径面
が後記螺施体(5)の山部外周とほぼ同心状に嵌合するよ
う穿孔された複数枚の環状間板(10)……(10)を上記
可動環状板(9)……(9)の積層間に介在させて固定体(1
1)に支承させ、これら可動環状板(9)……(9)または環
状間板(10)の板面要所に間隔保持用摺動凸子(12)…
…(12)を配設することにより、隣接板面間において内
径方向から外径方向へ至る狭隙状の流体流出溝(13)…
…(13)を形成せしめ、原動機(4)で駆動される芯材を
横軸としてその外周に螺状フィンを巻装してなる螺施体
(5)を固液収容函(1)内から排出口(3)の開口方向へ伸延
させて螺施繰出機溝(8)を構成すると共に上記螺施体(5)
の伸延部を可動環状板(9)……(9)および環状間板(10)
……(10)の中心孔に貫挿させることにより、螺施体
(5)の山部外周が可動環状板(9)……(9)の内径面を押圧
しつつ環状間板(10)……(10)の内径面に沿つて回転
して可動環状板(9)……(9)に偏心回転運動を行わせるよ
う構成し、螺施繰出機溝(8)の駆動時に固液収容函(1)内
の固液が軸方向に移送せしめられて液体は液体流出溝
(13)……(13)から外側へ流出せしめられると共に固
形物は前方の排出口(3)から排出せしめられ、且つ液
体流出溝(13)……(13)に入り込んだ微小固形物は可
動環状板(9)……(9)の偏心回転運動に伴なう前記摺動凸
子(12)……(12)の摺動作用と液体の流出作用によつ
て除去せられるよう構成したことを特徴とする固液分離
装置。1. From the solid-liquid storage box (1) to the discharge port (3), the inner diameter surface is eccentrically fitted along the threaded body (5) described below from the ridge outer circumference to the valley outer circumference. Plural movable annular plates (9) ... (9) are arranged in a stack in the axial direction so that the inner diameter surface fits almost concentrically with the outer periphery of the threaded body (5) described below. A plurality of annular discs (10) ... (10) perforated as shown in the figure are interposed between the movable annular plates (9).
It is supported by 1), and the sliding protrusions (12) for maintaining spacing are provided on the plate surface points of the movable annular plates (9).
By arranging (12), a narrow gap-shaped fluid outflow groove (13) extending from the inner diameter direction to the outer diameter direction between adjacent plate surfaces.
... (13) is formed, and a core is driven by the prime mover (4), and a spiral fin is wound around the outer periphery of the core as a horizontal axis.
(5) is extended from the inside of the solid-liquid storage box (1) in the opening direction of the discharge port (3) to form a screw-feeding machine groove (8), and the above-mentioned screw-threaded body (5).
The extension part of the movable ring plate (9) …… (9) and ring plate (10)
...... By inserting it into the center hole of (10), the threaded body
The outer periphery of the mountain portion of (5) rotates along the inner diameter surface of the annular plate (10) …… (10) while pressing the inner diameter surface of the movable annular plate (9) …… (9). 9) ... (9) is configured to perform an eccentric rotary motion, and when the screw feeding and feeding machine groove (8) is driven, the solid-liquid in the solid-liquid storage box (1) is transferred in the axial direction and the liquid is removed. The liquid outflow groove (13) …… (13) flows out to the outside and the solid matter is discharged from the front discharge port (3), and the fine solids that have entered the liquid outflow groove (13) …… (13). Items can be removed by the sliding action of the sliding protrusions (12) ... (12) and the outflow action of the liquid accompanying the eccentric rotation of the movable annular plate (9). A solid-liquid separation device characterized by being configured.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP61147815A JPH0773642B2 (en) | 1986-06-24 | 1986-06-24 | Solid-liquid separation device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP61147815A JPH0773642B2 (en) | 1986-06-24 | 1986-06-24 | Solid-liquid separation device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS634815A JPS634815A (en) | 1988-01-09 |
| JPH0773642B2 true JPH0773642B2 (en) | 1995-08-09 |
Family
ID=15438849
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP61147815A Expired - Lifetime JPH0773642B2 (en) | 1986-06-24 | 1986-06-24 | Solid-liquid separation device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0773642B2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2007090237A (en) * | 2005-09-28 | 2007-04-12 | Amukon Kk | Solid-liquid separator |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2012034357A1 (en) | 2010-09-16 | 2012-03-22 | 中国石油化工股份有限公司 | Catalyst carrier for olefin polymerization, solid catalyst component and catalyst |
| CN107936154B (en) | 2017-12-01 | 2020-11-06 | 中国石油天然气股份有限公司 | Alkoxy magnesium catalyst carrier and preparation method and application thereof |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0570482A (en) * | 1991-09-12 | 1993-03-23 | Hitachi Chem Co Ltd | Peptide and its salt |
-
1986
- 1986-06-24 JP JP61147815A patent/JPH0773642B2/en not_active Expired - Lifetime
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2007090237A (en) * | 2005-09-28 | 2007-04-12 | Amukon Kk | Solid-liquid separator |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS634815A (en) | 1988-01-09 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| EXPY | Cancellation because of completion of term |