JPS5823145B2 - Classifier - Google Patents
ClassifierInfo
- Publication number
- JPS5823145B2 JPS5823145B2 JP49028638A JP2863874A JPS5823145B2 JP S5823145 B2 JPS5823145 B2 JP S5823145B2 JP 49028638 A JP49028638 A JP 49028638A JP 2863874 A JP2863874 A JP 2863874A JP S5823145 B2 JPS5823145 B2 JP S5823145B2
- Authority
- JP
- Japan
- Prior art keywords
- compartment
- inlet
- container
- precipitation
- settling
- 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
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D19/00—Degasification of liquids
- B01D19/0042—Degasification of liquids modifying the liquid flow
- B01D19/0052—Degasification of liquids modifying the liquid flow in rotating vessels, vessels containing movable parts or in which centrifugal movement is caused
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D17/00—Separation of liquids, not provided for elsewhere, e.g. by thermal diffusion
- B01D17/02—Separation of non-miscible liquids
- B01D17/0217—Separation of non-miscible liquids by centrifugal force
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D45/00—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces
- B01D45/12—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by centrifugal forces
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04B—CENTRIFUGES
- B04B1/00—Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04B—CENTRIFUGES
- B04B1/00—Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles
- B04B1/10—Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles with discharging outlets in the plane of the maximum diameter of the bowl
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Centrifugal Separators (AREA)
- Separation Of Solids By Using Liquids Or Pneumatic Power (AREA)
- Combined Means For Separation Of Solids (AREA)
Description
【発明の詳細な説明】 本発明は分級装置(分類装置)に関する。[Detailed description of the invention] The present invention relates to a classification device (classification device).
それは特に複数個の成分を含む流体混合物を分級するた
めの装置に関する。It particularly relates to a device for classifying fluid mixtures containing a plurality of components.
該成分は、三相、即ち、気体、液体及び固体のいずれで
もよい。The components may be three-phase, ie, gas, liquid, and solid.
該混合物は、かくして、液−気、液−固、気−固、液−
液或はその他任意の流体である同様の混合物であってよ
G)。The mixture is thus liquid-gas, liquid-solid, gas-solid, liquid-
liquid or any other similar mixture of fluids.
本発明は、複数個の沈殿用隔室をもつ容器から成り、流
体混合の分級を乱流を可及的に防止して、良好な分級を
行なうようにすることを目的とした分級装置を提供する
もので、その特徴とする所は、その特許請求の範囲に記
載の通りである。The present invention provides a classification device that is composed of a container having a plurality of sedimentation compartments and is intended to prevent turbulence as much as possible during classification of fluid mixtures and perform good classification. Its features are as described in the claims.
次に更に本発明装置につき詳述する。Next, the apparatus of the present invention will be further explained in detail.
本発明装置は、夫々同じ物理的特性を有する混合物成分
を集めるための上下方向に間隔を存して複数個配設した
沈殿用隔室を有し且つ垂直回転軸のまわりを回転可能な
截頭円錐形でその小径入口端を下向きとして配した容器
と、該容器のその下端入口端の外周を包囲し且つ内部に
流体混合物を収容した貯溜室と、該容器内に、各段の沈
殿用隔室に対応してその各入口の下位に容器の上向きに
開拡した各側壁に対向して半径方向に延びて該回転軸に
夫々固設されたバッフルとから成り、該回転軸の回転に
より、各バッフルと容器の回転を生ぜしめ、貯溜室内の
流体混合物を容器内に入口端から導入せしめると共に容
器内で該流体混合物に遠心力を与えてその側壁に沿い上
動せしめてその。The device of the present invention has a truncated head rotatable around a vertical axis of rotation, and has a plurality of precipitation compartments arranged vertically at intervals for collecting mixture components having the same physical properties. A container having a conical shape with its small-diameter inlet end facing downward; a storage chamber surrounding the outer periphery of the lower inlet end of the container and containing a fluid mixture therein; A baffle is provided below each inlet of the chamber and extends in a radial direction opposite to each upwardly expanding side wall of the container and is fixed to the rotating shaft, and when the rotating shaft rotates, Rotation of each baffle and the container is caused to cause the fluid mixture within the reservoir to be introduced into the container from the inlet end and to apply a centrifugal force to the fluid mixture within the container causing it to move up along the side walls thereof.
混合物流体を各段の隔室に供給せしめ、その混合物成分
の物理的特性に応じ各隔室に於て実質上同じ物理的特性
の混合物粒子成分の沈殿を行なうようにする。A mixture fluid is supplied to each stage of compartments to effect precipitation of mixture particle components of substantially the same physical properties in each compartment depending on the physical properties of the mixture components.
物理的特性は、大きさ、形状、比重、密度その他適当な
物理的特性である。Physical properties include size, shape, specific gravity, density, and other suitable physical properties.
沈殿用隔室。は縦方向に間隔を存せしめられたバンク内
に形成され、各バンクは、該容器の回転軸のまわりに異
なった高さで円周上に間隔を存せしめられた複数個の隔
室を含む。Sedimentation compartment. are formed in longitudinally spaced banks, each bank including a plurality of circumferentially spaced compartments at different heights about the axis of rotation of the container. .
このように該容器は上方に開拡される側壁を有するので
、各バルブで混合物流体。The container thus has upwardly widening side walls so that the mixture fluid at each valve.
に遠心力を与えるときはこれを該側壁に沿って可及的に
層流状態としてその各上位外周の各隔室に流入せ、しめ
ることが出来る。When a centrifugal force is applied to the tube, the centrifugal force can be caused to flow as laminarly as possible along the side wall into each of the compartments on the upper periphery of the tube.
該沈殿用隔室は色々な異なった高さ位置で該容器から突
出し得る。The settling compartment may protrude from the vessel at various different heights.
高さ位置の増大につれ該沈殿用隔室の端末は一層半シ径
方向に突出するようにしてもよい。As the height increases, the ends of the settling compartments may protrude more radially.
該沈殿用隔室(円周上に1個又は複数個から成る)は沈
殿分級された成分を通過排出せしめる閉塞可能オリフィ
スを設ける。The settling chamber (consisting of one or more circumferential chambers) is provided with a closable orifice through which the precipitated and classified components are discharged.
該オリフィスは成分の隔室からの排出を制御するに適す
べく作られた弁装置を具備シする。The orifice includes a valve arrangement adapted to control the discharge of components from the compartment.
該弁は沈殿隔室の容量に応答するようにする。The valve is made responsive to the volume of the settling compartment.
これら弁は該沈殿用隔室の夫々に或はそのいくつかに感
知器に応答し而して電気的、機械的或は流体圧的装置に
より作動せしめられる。These valves are actuated by electrical, mechanical or hydraulic devices in response to sensors in each or several of the settling compartments.
これらは、交るかわる時間経過に応答し或は手で作動し
、得る。These may be responsive to alternating passages of time or may be manually actuated.
弁はバタフライ型或はスルース型弁が都合がよいが又分
離せられるべき成分に依存するその他適宜の弁であシ得
る。The valve is conveniently a butterfly or sluice type valve, but may also be any other suitable valve depending on the components to be separated.
又、該沈殿用隔室は、その内側端の入口からその外側端
の閉塞可能なオリフィスに向い漸次狭幅。The settling chamber has a progressively narrower width from the inlet at its inner end to the closable orifice at its outer end.
に集中するように構成される。configured to focus on
かかる構成によシ、沈殿成分が排出される時に、該沈殿
用隔室の残余の部分への水の供給に対する妨害を最小限
にとどめると共に、分級並びに沈殿操作に対する妨害を
最小限にとどめることができて連続的操作を可能とする
効果をもたらす。With this configuration, when the precipitated components are discharged, it is possible to minimize interference with the water supply to the remaining part of the precipitation compartment, and to minimize interference with the classification and precipitation operations. This has the effect of allowing continuous operation.
さらに該沈殿用隔室はその被処理混合流体の入口側の高
さよシも、該入口から該オリフィスまでの深さを大きく
構成される。Furthermore, the settling chamber is constructed so that the height from the inlet side of the mixed fluid to be treated is greater than the depth from the inlet to the orifice.
かかる構成によシ、該混合流体の該沈殿用隔室内での乱
流現象を可及的に最小限度にすると共に、該沈殿用隔室
内の奥部に迄到達している粒子を該内側端の入口又はそ
の近傍に存在するいかなる渦又は小過によっても影響を
受けさせることなく良好に安定にその沈殿物を集中でき
るので、該オリフィスの常閉弁を適時開弁じて核集中し
た沈殿物粒子を拡散することなく、集中的に且つ効能率
に分離採取することができる効果を有する。With this configuration, turbulence of the mixed fluid in the settling compartment is minimized as much as possible, and particles that have reached the deep part of the settling compartment are removed from the inner end. Since the precipitate can be concentrated in a good and stable manner without being affected by any vortices or small filtration existing at or near the inlet of the orifice, the normally closed valve of the orifice can be opened in a timely manner to remove the concentrated precipitate particles. It has the effect of being able to concentrate and efficiently separate and collect the substances without dispersing them.
又、上記の弁を作動して沈殿物を排出することによって
、乱流等を防止する該沈殿用隔室の高さと深さの比を実
質的に維持することができる。Furthermore, by operating the valve to discharge the precipitate, it is possible to substantially maintain the height-to-depth ratio of the precipitating compartment, which prevents turbulence and the like.
又、沈殿用隔室から排出された沈殿成分を各別に集める
ための捕集装置も設けることが出来る。A collection device may also be provided to separately collect the precipitated components discharged from the precipitate compartment.
本発明を添附図面を参考にその1例を下記詳述する。An example of the present invention will be described in detail below with reference to the accompanying drawings.
図面に於て、10は、縦軸13のまわりを回転、駆動せ
しめられるようにつくられた狭い方の端を容器の底とし
た截頭円錐形の容器12から成る分級装置を総括的に示
す。In the drawings, 10 generally indicates a classification device consisting of a truncated conical container 12 with the narrow end as the bottom of the container, which is made to be rotated and driven around a vertical axis 13. .
該容器12は、入口端14と該入口端の傍にそれる側壁
16を有する。The container 12 has an inlet end 14 and a sidewall 16 extending beside the inlet end.
複数個の沈殿用隔室30が軸方向に間隔を存したバンク
83.84.85内に高さを異にして設けられる。A plurality of settling chambers 30 are provided at different heights in axially spaced banks 83, 84, 85.
軸20が適当なベアリング17により支持された枠22
上に回転自在に設置され且つ、駆動モータ26に接続さ
れたベルト駆動プーリー24を備える。a frame 22 with a shaft 20 supported by suitable bearings 17;
A belt drive pulley 24 is rotatably installed thereon and connected to a drive motor 26.
該容器12は放射状腕28により駆動軸20に接続され
る。The container 12 is connected to the drive shaft 20 by a radial arm 28.
又、各段の沈殿用隔室30の入口32に対応してその各
下位の容器側壁10に対向して、放射状に延びるバッフ
ル29が該容器12の軸20と側壁16に固着されてい
る。Further, a radially extending baffle 29 is fixed to the shaft 20 and side wall 16 of the container 12, corresponding to the inlet 32 of each stage of the precipitation compartment 30, and facing the container side wall 10 below each stage.
第1図及び第2図から分るように、該沈殿用隔室30は
、異なった高さに、長さ方向に間隔を存して設けられた
バンク83,84.85内に設けられ、且つ閉塞し得る
オリフィス31を有する。As can be seen in FIGS. 1 and 2, the settling chambers 30 are provided in longitudinally spaced banks 83, 84, 85 at different heights; It also has an orifice 31 that can be closed.
感知器33が沈殿用隔室30内に設けられ且つオリフィ
ス31内の弁32と作動的に連結される。A sensor 33 is provided within settling compartment 30 and is operatively connected to valve 32 within orifice 31 .
又、該沈殿用隔室30は、その内側端の入口82からそ
の外側端の閉塞可能なオリフィス31に向い漸次狭幅に
集中し、該入口82側の高さ80よりも該入口82から
該オリフィス31までの深さ81を大きくするよう構成
される。Further, the settling chamber 30 gradually becomes narrower and more concentrated from the inlet 82 at its inner end toward the closable orifice 31 at its outer end, and the width from the inlet 82 is lower than the height 80 on the inlet 82 side. It is configured to increase the depth 81 to the orifice 31.
固定外筐34は該容器12を包囲して設けられる。A fixed outer casing 34 is provided to surround the container 12.
バッフル板36は該外筐34に、排出分級された成分の
流れに向って設けられる。A baffle plate 36 is provided in the outer casing 34 facing the flow of the discharged and classified components.
軸20と該容器12の入口端14を包囲し且つシール3
7を有する固定貯溜室15が更に設けられる。A seal 3 surrounds the shaft 20 and the inlet end 14 of the container 12.
A fixed reservoir 15 having 7 is further provided.
又内部拘束壁50が混合物を該沈殿用隔室内へ導入する
ことを助けるために、図面の点線示の如く設けるこきが
出来る。An internal restraining wall 50 may also be provided as shown in dotted lines in the drawings to assist in introducing the mixture into the settling compartment.
該拘束壁50を設ける場合は、遠心力によシ側壁16に
堆積する沈殿層を極めて薄くなり、その結果沈殿物の良
好な分離、分級効果をもたらすに役立つ。When the restraining wall 50 is provided, the sediment layer deposited on the side wall 16 due to centrifugal force becomes extremely thin, and as a result, it helps to bring about a good separation and classification effect of the sediment.
使用に於て、例えば水中懸濁された砂粒から成る混合物
が貯溜室15内に用意され次で回転軸20の回転に伴な
い椀状容器の入口端14内に供給される。In use, a mixture consisting of, for example, sand grains suspended in water is provided in the reservoir 15 and then fed into the inlet end 14 of the bowl as the rotating shaft 20 rotates.
バックル29の攪拌により遠心力が容器12内に供給さ
れた混合物流体に与えられ而してそれは該椀状容器の回
転の際該容器12の側壁16に沿って矢38示方向に上
方に変位される。The agitation of the buckle 29 imparts a centrifugal force to the mixture fluid supplied in the container 12, causing it to be displaced upwardly along the side wall 16 of the container 12 in the direction of arrow 38 upon rotation of the bowl. Ru.
砂のより重い或はより大きいサイズのフラクションは、
より低位の沈殿用隔室内に沈殿され又より軽い或はより
小さいフラクションは、より上位の沈殿用隔室内に沈殿
され事実上固体のない水が40で溢流する。The heavier or larger size fraction of sand is
The lighter or smaller fractions are precipitated in the lower settling compartments and the substantially solids-free water overflows at 40.
砂の予定容量が該隔室内に沈殿したとき、これは感知器
33により検出され而して弁32は開かれる。When the predetermined volume of sand has settled into the compartment, this is detected by sensor 33 and valve 32 is opened.
遠心力により、砂の夫々のフラクションは、夫々の異な
った高さで適当な装置(図示しない)により制御される
固定のバッフル板36上に排出される。Due to centrifugal force, the respective fractions of sand are discharged at different heights onto a fixed baffle plate 36 controlled by suitable devices (not shown).
使用中、該装置は水中懸濁物からメツシュ325より小
さい砂粒を実質上分離した。In use, the device substantially separated sand grains smaller than Mesh 325 from the water suspension.
沈殿用隔室の幅、それらの高さ、長さ方向のバンク内の
隔室の数、或は回転速度等を変えることにより、フラク
ションの数及び質を変えることが出来る。By varying the width of the settling compartments, their height, the number of compartments in a longitudinal bank, or the speed of rotation, the number and quality of the fractions can be varied.
上記の装置の作動に於て、各沈殿用隔室29の入口82
に直接対向せしめることなくその下位に容器の側壁16
に対向してバッフル29を設けたので、バッフル29の
回転により混合物流体を該隔室29の入口82に直接流
入供給せしめることなく、一旦その側壁16に沿わせて
上動せしめ可及的に層流として流入供給でき、更に、各
隔室29は、入口82側の高さ80よシも該入口82か
ら該オリフィス31までの深さ81を大きく構成したの
で、各隔室29内での乱流を可及的に最・不眠となし得
られると共に粒子を該入口82近傍に生ずる渦又は小過
に影響されることなく安定な沈殿を行なわせることが出
来ると共に一旦沈殿した粒子は攪乱されることなく安定
にその沈殿状態を保持する効果をもたらす。In operation of the apparatus described above, the inlet 82 of each settling compartment 29
The side wall 16 of the container is placed below the side wall 16 of the container without directly facing it.
Since the baffle 29 is provided opposite to the baffle 29, the rotation of the baffle 29 does not cause the mixture fluid to flow directly into the inlet 82 of the compartment 29, but rather allows it to move upward along the side wall 16 of the compartment 29, thereby forming a layer as much as possible. Furthermore, each compartment 29 has a depth 81 from the inlet 82 to the orifice 31 that is larger than the height 80 on the inlet 82 side, so that turbulence within each compartment 29 is reduced. The flow can be made as smooth as possible, and the particles can be allowed to settle stably without being affected by the vortices or small turbulence generated near the inlet 82, and the particles once settled can be disturbed. This has the effect of stably maintaining the precipitated state without causing any problems.
本発明の実施の態様は例えば次の通りである。Examples of embodiments of the present invention are as follows.
(1)夫々の沈殿用隔室は、複数個の円周上に配置され
た室から成り、夫々の室は一点に集中し、閉塞可能なオ
リフィスと弁が夫々のその集中する一点に設けられた特
許請求の範囲第1項に記載の装置。(1) Each precipitation compartment consists of a plurality of circumferentially arranged chambers, each chamber is concentrated at one point, and a closable orifice and valve are provided at each concentrated point. An apparatus according to claim 1.
(2)該容器は、該容器内の該混合物を攪拌するための
内部フィンを有する特許請求の範囲第1項に記載の装置
。(2) The apparatus of claim 1, wherein the container has internal fins for stirring the mixture within the container.
第1図は本発明実施の1例の線図的裁断側面図、第2図
は第1図の■−■線截線面断面図す。
10・・・・・・分級装置、12・・・・・・容器、1
3・・・・・・垂直軸、14・・・・・・流入口端、1
6・・・・・・側壁、30・・・・・・沈殿用隔室、8
0・・・・・・沈殿用隔室の入口側の高さ、81・・・
・・・沈殿用隔室の入口からオリフィスまでの深さ、2
9・・・・・・バッフル、82・・・・・・入口、83
.84.85・・・・・・バンク。FIG. 1 is a diagrammatic cutaway side view of one embodiment of the present invention, and FIG. 2 is a cross-sectional view taken along the line ■--■ in FIG. 10... Classifying device, 12... Container, 1
3... Vertical axis, 14... Inlet end, 1
6... Side wall, 30... Sedimentation compartment, 8
0...Height on the inlet side of the precipitation compartment, 81...
...Depth from the entrance of the settling compartment to the orifice, 2
9...Baffle, 82...Inlet, 83
.. 84.85... Bank.
Claims (1)
して回転可能に設けられた截頭円錐形の容器と;該容器
の側壁に設けられた入口開口のまわりで該容器と密着し
、外側に延び、且つ沈殿用隔室内側端の該入口から該沈
殿用隔室の外側端の閉塞可能なオリフィスに向い漸次狭
幅に集中する同じ沈殿特性を有するそれら成分の沈殿の
ための、該容器の側壁に軸方向に間隔を置いて直列に設
けられた複数個の沈殿用隔室と;該オリフィスを常閉す
ると共に所定周期で所定時間それらのオリフィスを自動
的に開口するための弁と;該容器の入口端を包囲し且つ
流体混合物を収容する貯溜室と;各沈殿用隔室の入口に
対応して、該各人口の下方に該回転軸に固設され且つ半
径方向に設置された混合物に遠心力を与えるためのバッ
フルと;該沈殿用隔室から排出された沈殿成分を集める
ために該容器のまわりに設けられた固定外筐とを有し;
且つ該沈殿用隔室は該流動の方向の該沈殿用隔室の入口
側の高さよりも該入口から該オリフィスまでの深さを大
きく構成したことから成る運搬流体を伴う混合流体から
の複数個の物理的に分離可能な成分の分級装置。1 a frusto-conical container rotatably mounted for rotation around an axis of rotation with the narrow end as the bottom of the container; , for the precipitation of those components having the same precipitation characteristics extending outwardly and concentrating in progressively narrower widths from the inlet at the inner end of the precipitation compartment towards the obstructable orifice at the outer end of the precipitation compartment; a plurality of settling compartments arranged in series at axial intervals on the side wall of the vessel; a valve for normally closing the orifices and automatically opening the orifices for a predetermined period at a predetermined period; a reservoir surrounding the inlet end of the vessel and containing the fluid mixture; and corresponding to the inlet of each settling compartment, fixed to the rotating shaft and radially disposed below the respective settling compartment; a baffle for applying a centrifugal force to the separated mixture; and a fixed outer casing provided around the container for collecting the precipitated components discharged from the precipitating compartment;
and the sedimentation chamber is configured such that the depth from the inlet to the orifice is greater than the height of the inlet side of the sedimentation chamber in the flow direction. classification equipment for physically separable components.
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| ZA731965A ZA731965B (en) | 1973-03-20 | 1973-03-20 | Classifying means |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS50111662A JPS50111662A (en) | 1975-09-02 |
| JPS5823145B2 true JPS5823145B2 (en) | 1983-05-13 |
Family
ID=25566120
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP49028638A Expired JPS5823145B2 (en) | 1973-03-20 | 1974-03-14 | Classifier |
Country Status (5)
| Country | Link |
|---|---|
| JP (1) | JPS5823145B2 (en) |
| CA (1) | CA986072A (en) |
| ES (1) | ES424379A1 (en) |
| GB (1) | GB1465311A (en) |
| ZA (1) | ZA731965B (en) |
Families Citing this family (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5237896A (en) * | 1975-09-17 | 1977-03-24 | Toray Industries | Multiifilament yarn for water jet loom and fabric weaving method |
| GB2128903B (en) * | 1982-09-30 | 1986-04-16 | British Nuclear Fuels Ltd | Separating impurities from a gas |
| US4515689A (en) * | 1982-12-03 | 1985-05-07 | Clasicon (Proprietary) Limited | Classifying means |
| MXPA98001208A (en) * | 1995-07-13 | 2005-07-25 | V Knelson Benjamin | Separating intermixed materials of different specific gravity. |
| CA2238897C (en) * | 1998-05-26 | 2004-05-04 | Steven A. Mcalister | Flow control valve for continuous discharge centrifugal concentrators |
| RU2151006C1 (en) * | 1999-06-29 | 2000-06-20 | Ивженко Андрей Петрович | Centrifugal separator |
| RU2164172C1 (en) * | 1999-06-29 | 2001-03-20 | Ивженко Андрей Петрович | Centrifugal separator |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB1304106A (en) * | 1970-10-14 | 1973-01-24 |
-
1973
- 1973-03-20 ZA ZA731965A patent/ZA731965B/en unknown
-
1974
- 1974-03-01 GB GB942174A patent/GB1465311A/en not_active Expired
- 1974-03-14 JP JP49028638A patent/JPS5823145B2/en not_active Expired
- 1974-03-18 ES ES424379A patent/ES424379A1/en not_active Expired
- 1974-03-19 CA CA195,389A patent/CA986072A/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| CA986072A (en) | 1976-03-23 |
| DE2409224A1 (en) | 1974-09-26 |
| ES424379A1 (en) | 1976-06-01 |
| JPS50111662A (en) | 1975-09-02 |
| DE2409224B2 (en) | 1976-06-16 |
| ZA731965B (en) | 1974-11-27 |
| GB1465311A (en) | 1977-02-23 |
| AU6649574A (en) | 1975-09-11 |
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