JPH04100554A - Centrifugal separator of liquid - Google Patents

Centrifugal separator of liquid

Info

Publication number
JPH04100554A
JPH04100554A JP21575190A JP21575190A JPH04100554A JP H04100554 A JPH04100554 A JP H04100554A JP 21575190 A JP21575190 A JP 21575190A JP 21575190 A JP21575190 A JP 21575190A JP H04100554 A JPH04100554 A JP H04100554A
Authority
JP
Japan
Prior art keywords
liquid
fixed container
container
rotating
rotating cylinder
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP21575190A
Other languages
Japanese (ja)
Inventor
Shiro Takahashi
四郎 高橋
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
TAKAHASHI NETSURIYUUTAI RES YUGEN
Original Assignee
TAKAHASHI NETSURIYUUTAI RES YUGEN
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by TAKAHASHI NETSURIYUUTAI RES YUGEN filed Critical TAKAHASHI NETSURIYUUTAI RES YUGEN
Priority to JP21575190A priority Critical patent/JPH04100554A/en
Publication of JPH04100554A publication Critical patent/JPH04100554A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To effectively separate the content such as the solid in a liquid by generating a revolving stream in the liquid within a hermetically closed vertical cylindrical fixed container and passing the liquid through the gaps between rotary discs to guide the same into a rotary cylinder. CONSTITUTION:A liquid supply port 14 is provided to the bottom plate part of a hermetically closed vertical cylindrical fixed container 1 and a rotary cylinder 7 whose upper part protrudes above the fixed container 1 is concentrically arranged in the fixed container 1 in the axial direction of the container 1. Further, rotary discs 8 generating a swirl in the liquid within the fixed container 1 are horizontally provided to the rotary cylinder 7 so as to provide intervals in a vertical direction and liquid passing ports 11 are provided to the outer wall of the rotary cylinder 7 so as to be positioned between the adjacent rotary discs 8. Liquid discharge ports 12 are arranged to the part upwardly protruding from the fixed container 1 of the rotary cylinder 7 and liquid drain pipes 16-19 are connected to the fixed container 1. As a result, the content such as the solid in the liquid can be effectively separated.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、自然汚濁水の浄化処理、又は工場内で発生す
る無機系、有機系及び植物系等の固液混合体乃至軽量質
液混合体の処理に当って、液の浄化、排出重質液中の水
分乃至油分の含有率減少化、含有固形微細粉の回収利用
、比重差に基づく液の分級化等を行う液状体の遠心分離
装置に関する。
Detailed Description of the Invention [Industrial Application Field] The present invention is applicable to the purification treatment of naturally polluted water, or solid-liquid mixtures or light solid-liquid mixtures of inorganic, organic, and plant-based substances generated in factories. Centrifugal separation of liquids to purify the liquid, reduce the content of water or oil in the discharged heavy liquid, collect and use the solid fine powder contained, and classify the liquid based on the difference in specific gravity. Regarding equipment.

(従来の技術〕 従来、液状体の遠心分離処理には、水平円筒型又は垂直
円筒型の回転体が最も広く利用されている。
(Prior Art) Conventionally, horizontal cylindrical or vertical cylindrical rotating bodies have been most widely used for centrifugal separation of liquid materials.

〔発明が解決しようとする課題〕[Problem to be solved by the invention]

前記の従来の回転円筒型の遠心分離方式は、容器内の液
状体はすべて回転しつつ外周部に近づ(はどその遠心力
が大きくなり、その有する遠心骨Ml!能は高いが、円
筒型容器を回転するための支持機構、駆動機構等の諸要
素を必要とするため、処理能力が小さい装置の場合も、
また特にその処理能力の増大を計る装置の場合も、処理
量当りの設備費用が大きくなり易いという問題がある。
In the conventional rotating cylindrical centrifugal separation method described above, all the liquid in the container rotates and approaches the outer periphery (the centrifugal force of the container becomes large, and the centrifugal force of the container is high, but the cylindrical Since various elements such as a support mechanism and a drive mechanism are required to rotate the mold container, even in the case of equipment with small processing capacity,
Furthermore, especially in the case of an apparatus designed to increase its throughput, there is a problem in that the equipment cost per throughput tends to increase.

装置のコンパクト化のためには、装置の外筒を固定し、
容器内の液状体を回転軸を心とする回転体外周部の回転
面と接触させてその旋回を促す方式の構成も考えられた
が、外筒固定による旋回流に対するブレーキに対し、限
定された面積の前記の回転体外周部の回転面との接触に
よる旋回駆動力が小さいために、遠心分離作用が微弱と
なり実用化に至っていない。
In order to make the device more compact, it is necessary to fix the outer cylinder of the device and
A configuration in which the liquid in the container is brought into contact with the rotating surface of the outer periphery of the rotating body around the rotation axis to encourage its swirling has been considered, but this approach has limited ability to brake the swirling flow by fixing the outer cylinder. Since the turning driving force due to the contact with the rotating surface of the outer periphery of the rotating body is small, the centrifugal separation effect is weak and it has not been put to practical use.

また、前記従来の回転円筒型の方式においては、遠心分
離処理された液状体をその比重差に応して分別排出しよ
うとする時、容器全体が高速回転しているために、この
分別排出口の各段設備については、装置上の困難が伴う
ことになり、遠心分離装置として、軽質液、重質液の三
者分離だけでなく、比重差に応しての分別排出を容易化
することも問題点となっている。
In addition, in the conventional rotating cylindrical type system, when the centrifuged liquid is to be separated and discharged according to the difference in specific gravity, the whole container is rotating at high speed, so the separation outlet Regarding each stage of equipment, there are difficulties in terms of the equipment, so it is necessary to use a centrifugal separator not only to separate the light liquid and heavy liquid, but also to facilitate the separation and discharge according to the difference in specific gravity. is also a problem.

本発明は従来の遠心分離装置0以上の問題点を解決しよ
うとするものである。
The present invention seeks to solve more than zero problems with conventional centrifugal separators.

(課題を解決するための手段〕 本発明の液状体の遠心分離装置は、密閉された竪型の円
筒形の固定容器、前記固定容器の底板部に設けられた液
状体の給液口、前記固定容器内にその軸心方向に同心に
設けられ上部が前記固定容器の上方に突出する回転円筒
、前記回転円筒に互いに上下方向に間隔をおいて水平に
取付けられ固定容器内の液状体に旋回流を発生させる回
転板、隣接する前記回転板の間に位置して前記回転円筒
の外壁に設けられた通液口、前記回転円筒の前記固定容
器から上方に突出する部分に設けられた放液口、及び前
記固定容器に接続された排1&管を備えた。
(Means for Solving the Problems) A liquid centrifugal separator of the present invention includes a sealed vertical cylindrical fixed container, a liquid supply port provided on a bottom plate of the fixed container, A rotating cylinder provided concentrically in the axial direction within a fixed container and having an upper portion protruding above the fixed container, which is attached horizontally to the rotating cylinder at intervals in the vertical direction and rotates around the liquid in the fixed container. a rotating plate that generates a flow; a liquid passage port located between the adjacent rotating plates and provided on the outer wall of the rotating cylinder; a liquid discharge port provided in a portion of the rotating cylinder that projects upward from the fixed container; and an exhaust pipe connected to the fixed container.

〔作 用] 本発明では、固定容器内にその底板部の給液口から供給
された液状体は、回転円筒と共に回転する回転板によっ
て旋回流となって固定容器内を上昇し、この間に混在す
る固形物等の内容物の遠心分離が行われる。内容物の遠
心分離が行なわれて軽質となった液状体は、回転円筒の
通液口を通って回転円筒内へ流入し、同回転円筒内を上
昇して固定容器から上方に突出する部分に設けられた放
液口から排出される。一方、遠心分離された内容物を含
む重質の液状体は固定容器の排液管から排出される。前
記のように、液状体は、固定容器内を旋回しながら回転
板の外周部から回転円筒の通液口に至るために、その間
に大きい時間経過が与えられ、液状体に混在する固形物
等の内容物は効果的に遠心分離される。また、以上のよ
うに、本発明では、充分な時間経過をもって遠心分離が
行なわれるために、固定容器の壁面付近では旋回流の強
さが弱まっているにも拘らず、充分な遠心分離作用が奏
せられ、また回転円筒の回転数を下げることができ、駆
動に要する動力が低減する。しかも、容器を回転させて
いないために、機構も簡単化される。
[Function] In the present invention, the liquid supplied into the fixed container from the liquid supply port on the bottom plate becomes a swirling flow and rises inside the fixed container by the rotary plate that rotates together with the rotating cylinder, and during this time, the liquid is mixed and The contents, such as solid matter, are centrifuged. The liquid, which has become lighter after centrifugation of the contents, flows into the rotating cylinder through the liquid passage port of the rotating cylinder, rises inside the rotating cylinder, and reaches the part that protrudes upward from the fixed container. It is discharged from the provided liquid discharge port. On the other hand, the heavy liquid containing the centrifuged contents is discharged from the drain pipe of the stationary container. As mentioned above, the liquid flows from the outer periphery of the rotary plate to the liquid passage port of the rotating cylinder while swirling inside the fixed container, so a long period of time passes during that time, and solids etc. mixed in the liquid flow. The contents of the are effectively centrifuged. Furthermore, as described above, in the present invention, since centrifugation is performed after a sufficient period of time has elapsed, sufficient centrifugal separation effect is achieved even though the strength of the swirling flow is weakened near the wall surface of the fixed container. The rotation speed of the rotating cylinder can be lowered, and the power required for driving is reduced. Moreover, since the container is not rotated, the mechanism is also simplified.

〔実施例〕〔Example〕

本発明の一実施例を、第1図によって説明する。 An embodiment of the present invention will be described with reference to FIG.

lは円筒状の竪型の密閉された固定容器であり、円筒形
の側壁2.傾斜した截頭円錐形の側壁3及び水平な上蓋
板4と底板5を備えている。固定容器l内には、その軸
心と同心に上下方向へ延びる回転円筒7が設けられ、同
回転円筒7の上部は固定容器1の上蓋板4を貫通して上
方に突出しており、その上端にはモーター22によって
駆動される回転軸6が取付けられでいる。前記回転軸6
は軸受20で支持され、また前記回転円筒7の下部の延
長部7′は、底板5の下方の軸受21Qこよって支持さ
れている。前記回転円筒7には上下方向に間隔をおいて
複数の円板又は転翅等の固定容器1内の液状体に旋回流
を発生させる回転板8が水平に取付けられており、最上
段と最下段の回転板8の上方と下方の固定容器1内には
、前記回転板8より径の大きい最上部の回転板9及び最
底部の回転板IOが、それぞれ回転円筒7に水平に取付
けられている0回転円筒7の外壁の隣接する回転板8,
9.10の中間の位置には、同外壁を貫通する複数の通
液口11が設けられ、また、同回転円筒の固定容器1よ
り上方に突出する部分には複数の放液口12が設けられ
ている。
1 is a cylindrical vertical sealed fixed container, and has a cylindrical side wall 2. It has an inclined frustoconical side wall 3 and a horizontal top cover plate 4 and bottom plate 5. A rotating cylinder 7 is provided inside the fixed container l and extends vertically concentrically with the axis of the fixed container l. A rotating shaft 6 driven by a motor 22 is attached to the upper end. The rotating shaft 6
is supported by a bearing 20, and the lower extension 7' of the rotating cylinder 7 is supported by a bearing 21Q below the bottom plate 5. Rotating plates 8, which generate swirling flow in the liquid in the fixed container 1, such as a plurality of discs or rotary blades, are horizontally attached to the rotating cylinder 7 at intervals in the vertical direction. In the fixed container 1 above and below the lower rotary plate 8, a top rotary plate 9 and a bottom rotary plate IO having a larger diameter than the rotary plate 8 are respectively attached horizontally to the rotary cylinder 7. The adjacent rotary plate 8 on the outer wall of the 0-rotation cylinder 7,
9. A plurality of liquid passage ports 11 are provided at the intermediate position of the same outer wall, and a plurality of liquid discharge ports 12 are provided at a portion of the rotating cylinder that protrudes upward from the fixed container 1. It is being

固定容器1の上蓋板4上に連接して回転円筒7の固定容
器1からの突出部を取囲んで貯液円筒13が設けられて
いる。同貯液円筒13の下部は、上蓋板4に回転円ti
7を取囲んで設けられた通入4aを介して固定容器1の
上部と連通しており、また貯液円筒13の側壁には軽質
の液状体の排液管15が接続されている。
A liquid storage cylinder 13 is provided on the top cover plate 4 of the fixed container 1 so as to surround the protrusion of the rotating cylinder 7 from the fixed container 1 . The lower part of the liquid storage cylinder 13 is connected to the upper cover plate 4 by a rotating circle ti.
It communicates with the upper part of the fixed container 1 through a passage 4a provided surrounding the liquid storage cylinder 13, and a drain pipe 15 for a light liquid is connected to the side wall of the liquid storage cylinder 13.

固定゛容器1の底板5の最底部回転板10の下方の位置
には給液ポンプ23をもつ固形物等の内容物が混在する
液状体の給液管14が接続され、同底板19の側壁2寄
りの外方の位置には重質の液状体の排液管19が接続さ
れ、更に、側壁2の上部には中質液の排出管18が、ま
た傾斜した側壁3には中質の液状体の排液管16.17
がそれぞれ接続されている。
A liquid supply pipe 14 with a liquid supply pump 23 for a liquid mixed with contents such as solids is connected to a position below the bottom rotary plate 10 of the bottom plate 5 of the fixed container 1, and the side wall of the bottom plate 19 is A heavy liquid drain pipe 19 is connected to the outer position near 2, and a medium liquid drain pipe 18 is connected to the upper part of the side wall 2, and a medium liquid drain pipe 18 is connected to the inclined side wall 3. Liquid drain pipe 16.17
are connected to each other.

なお、後記する液状体の流れの方向を第1図中矢印で示
す。
Note that the flow direction of the liquid, which will be described later, is indicated by an arrow in FIG.

以上のように構成された本実施例では、給液ポンプ23
によって給液管】4から固定容器1内に液状体が供給さ
れ、液状体は最下段の回転板10に沿って、水平方向外
方へ向って流れた後、固定容器l内で回転板8,9.1
0によって旋回流が与えられ、旋回しつつ固定容器1内
を上昇する。次いで液状体は回転板8.9.10の間を
旋回しながら内方へ流れて、通液口11を経て回転円筒
7内へ入って同筒7内を上昇する。このように液状体は
、固定容器1内で旋回流となり、かつ、回転板8,9.
10の外周部から回転円筒7の通液口11へ向って流れ
るために、時間経通が長くなり、これによって、液状体
内の固形物等の内容物の遠心分離を十分に行なうことが
できる。なお、この際に固定容器1の側壁面付近では旋
回流の強さが弱まっているが、本実施例では、前記のよ
うに通液口11へ入る迄の時間経過を長くすることによ
って、所要の遠心分離を行なうことができる。
In this embodiment configured as described above, the liquid supply pump 23
A liquid is supplied into the fixed container 1 from the liquid supply pipe 4, and after flowing outward in the horizontal direction along the rotary plate 10 at the lowest stage, the liquid flows to the rotary plate 8 in the fixed container l. ,9.1
0 gives a swirling flow, which rises inside the fixed container 1 while swirling. The liquid then flows inwardly while swirling between the rotating plates 8, 9, 10, enters the rotating cylinder 7 through the liquid passage port 11, and rises within the rotating cylinder 7. In this way, the liquid becomes a swirling flow within the fixed container 1, and the rotating plates 8, 9...
Since the liquid flows from the outer periphery of the liquid body 10 toward the liquid passage port 11 of the rotating cylinder 7, the passage time becomes longer, and thereby the contents such as solids in the liquid body can be sufficiently centrifuged. At this time, the strength of the swirling flow is weakened near the side wall surface of the fixed container 1, but in this embodiment, the required amount of time is increased by lengthening the time elapsed until the liquid enters the liquid passage port 11 as described above. can be centrifuged.

内容物が分離され軽質化された液状体は、前記のように
、回転円筒7内を上昇し、放液口12から貯液円筒13
内へ流入する。液状体内の固形物等の内容物は、同好円
筒13内で更に重力分離を受けて分離され、液状体は更
に軽質化され、固形物等の内容物が十分に分離された液
状体は排液管15より排出される。
The liquid whose contents have been separated and lightened rises in the rotating cylinder 7 and flows from the liquid discharge port 12 to the liquid storage cylinder 13, as described above.
flow inward. The solids and other contents in the liquid are further separated by gravity separation in the cylinder 13, the liquid is further lightened, and the liquid from which the solids and other contents have been sufficiently separated is drained. It is discharged from the pipe 15.

一方、貯液円筒13で分離された内容物を含む液状体は
、透穴4aを通って固定容器1の上部へ還流し、同容器
1内の前記の旋回流となって、内容物の分離作用を受け
る。
On the other hand, the liquid containing the contents separated in the liquid storage cylinder 13 flows back to the upper part of the fixed container 1 through the through hole 4a, becomes the above-mentioned swirling flow in the container 1, and separates the contents. be affected.

前記のように、最上段と最下段の回転板9,1゜は、回
転板8より径が大きく形成されているために、回転板8
に沿って流れる液状体が固定容器lの軸方向へ流れるこ
とが阻止され、給液管14より固定容器1内へ流入する
液状体と貯液円筒13から固定容器1内へ流入する液状
体は、同回転板9,1゜に沿って円滑に外方へ向って流
れた上、固定容器1内の旋回流となり、内容物の遠心分
離が確実に行なわれる。
As mentioned above, since the uppermost and lowermost rotary plates 9 and 1° are formed to have a larger diameter than the rotary plate 8,
The liquid flowing along the axis is prevented from flowing in the axial direction of the fixed container l, and the liquid flowing into the fixed container 1 from the liquid supply pipe 14 and the liquid flowing into the fixed container 1 from the liquid storage cylinder 13 are prevented from flowing in the axial direction of the fixed container l. In addition to smoothly flowing outward along the rotary plates 9 and 1°, the flow becomes a swirling flow within the fixed container 1, and centrifugal separation of the contents is reliably performed.

一方、固定容器1内で分離された内容物を含むを含む中
質の液状体は排液管16.17.18から排出される。
On the other hand, the medium liquid containing the separated contents in the fixed container 1 is discharged from the drain pipe 16, 17, 18.

また、本実施例では、容器を回転させず、回転円筒と回
転板だけを回転しており、また液状体が回転円筒へ流入
する時間経過を大きくしたことによって、回転板の回転
を遅くしても、固定容器1内で充分な遠心作用を得るこ
とができるために、所要の駆動動力を低減することがで
きる。
In addition, in this example, only the rotating cylinder and rotating plate were rotated without rotating the container, and by increasing the time elapsed for the liquid to flow into the rotating cylinder, the rotation of the rotating plate was slowed down. Also, since sufficient centrifugal action can be obtained within the fixed container 1, the required driving power can be reduced.

前記の実施例を利用した繊維質の微細汚濁物を含む水液
の処理設備を、第2図に示す。
FIG. 2 shows a treatment facility for an aqueous liquid containing fine fibrous contaminants using the above-described embodiment.

前実施例に係る遠心分離装置を2個設けて、これを−次
遠心分離装置101と二次遠心分動装置102とする。
Two centrifugal separators according to the previous embodiment are provided, and these are referred to as a secondary centrifugal separator 101 and a secondary centrifugal separation device 102.

液槽103内の繊III賞の微細汚濁物を含む水液を給
液ポンプ104によって、1次遠心分離装置101へ送
り、間装W101で微細汚濁物が分離された水液を液1
103へ戻すか、清浄液として系外へ排出する。一方、
分離された微細汚濁物を含む水液は、二次遠心分離装置
102へ送られ、ここで清浄化された水液を貯槽103
へ戻し、分離された微細汚濁物を含む濃縮液を適宜の処
理装置へ排出する。
The aqueous liquid containing the fine contaminants of Sensai III Award in the liquid tank 103 is sent to the primary centrifugal separator 101 by the liquid supply pump 104, and the aqueous liquid from which the fine contaminants have been separated in the interlayer W101 is converted into liquid 1.
Either return it to 103 or discharge it out of the system as a cleaning liquid. on the other hand,
The separated aqueous liquid containing fine contaminants is sent to a secondary centrifugal separator 102, where the purified aqueous liquid is transferred to a storage tank 103.
The concentrated liquid containing the separated fine pollutants is discharged to an appropriate processing device.

前記の実施例を利用した油分・水分・固形物の分離処理
設備を、第3図に示す。
FIG. 3 shows an equipment for separating oil, water, and solids using the above-mentioned embodiment.

廃棄有機物の乾溜処理によって生ずる有機ガスを液化処
理した給液が、前記実施例に係る遠心分離装置である一
次遠心分離装2201.軽質液分離装置202及び重質
液分離装置203へ弁開度を調節して排出量バランスを
とるように導入される。−次遠心分離装置201で得ら
れた軽質の液は、軽質液分離装置202へ導入され、こ
こに供給されている給液と共に分離作用を受け、軽質油
は排液管205(前記実施例の排液管15)から、中賞
油は排液管206(前記実施例の排液管16.17)か
ら、重質油は排液管207(前記実施例の排液管18)
から排出される。一方、前記分離装置201.で分離さ
れた固形物等を含む重質の液は、底部の排液管から重質
液分離装置203へ導入され、ここで分離処理を受け、
清浄化された水液は軽質液分離装置202へ導入され、
分離された内容物を含むスラリーは適宜の処理装置へ送
られる。
The feed liquid obtained by liquefying the organic gas produced by the dry distillation treatment of waste organic matter is fed to the primary centrifugal separator 2201, which is the centrifugal separator according to the above embodiment. The liquid is introduced into the light liquid separation device 202 and the heavy liquid separation device 203 so as to balance the discharge amount by adjusting the valve opening degree. - The light liquid obtained in the next centrifugal separator 201 is introduced into the light liquid separator 202, where it is subjected to a separation action together with the liquid supplied here, and the light oil is removed from the drain pipe 205 (as in the previous embodiment). Medium oil is drained from the drain pipe 15), medium oil is drained from the drain pipe 206 (drain pipe 16, 17 in the above embodiment), and heavy oil is drained from the drain pipe 207 (drain pipe 18 in the above embodiment).
is discharged from. On the other hand, the separation device 201. The heavy liquid containing solids etc. separated in is introduced from the bottom drain pipe to the heavy liquid separation device 203, where it is subjected to separation treatment,
The purified water liquid is introduced into the light liquid separator 202,
The slurry containing the separated contents is sent to appropriate processing equipment.

〔発明の効果〕〔Effect of the invention〕

以上説明したように、本発明は、密閉された竪型の円筒
形の固定容器内において、液状体に旋回流を発生させ、
これを回転板の間を通して回転円筒内へ導くことによっ
て、十分な時間経過をもって液状体の遠心分離を行ない
、同液状体に混在する固形物等の内容物を効果的に分離
することができる。また、回転駆動されるものは、回転
円筒と回転板に限られ、駆動に要する動力を低減するこ
とができると共に、装置が簡単で軽量化され設備費を低
廉にすることができる。
As explained above, the present invention generates a swirling flow in a liquid in a sealed vertical cylindrical fixed container,
By guiding this into the rotating cylinder through the rotating plates, the liquid can be centrifuged after a sufficient period of time has elapsed, and solids and other contents mixed in the liquid can be effectively separated. In addition, what is rotationally driven is limited to the rotating cylinder and the rotating plate, and the power required for driving can be reduced, and the device is simple and lightweight, making it possible to reduce equipment costs.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は本発明の一実施例の縦断図、第2図及び第3図
は同実施例を用いた遠心分離設備の例をそれぞれ示す系
統図である。 1・・・固定容器、     2.3・・・側壁。 4・・・上蓋板、      5・・・底板7・・・回
転円筒、     8・・・回転板。 9・・・最上部回転板、10・・・最底部回転板11・
・・通液口、12・・・放液口 13・・・貯液円筒、     14・・・給液管15
、16.17.18.19・・・排液管22・・・モー
ター、23・・・給液ポンプ。
FIG. 1 is a longitudinal sectional view of one embodiment of the present invention, and FIGS. 2 and 3 are system diagrams showing examples of centrifugal separation equipment using the same embodiment. 1...Fixed container, 2.3...Side wall. 4... Upper cover plate, 5... Bottom plate 7... Rotating cylinder, 8... Rotating plate. 9... Top rotating plate, 10... Bottom rotating plate 11.
...Liquid passage port, 12...Liquid discharge port 13...Liquid storage cylinder, 14...Liquid supply pipe 15
, 16.17.18.19...Drainage pipe 22...Motor, 23...Liquid supply pump.

Claims (1)

【特許請求の範囲】[Claims] 密閉された竪型の円筒形の固定容器、前記固定容器の底
板部に設けられた液状体の給液口、前記固定容器内にそ
の軸心方向に同心に設けられ上部が前記固定容器の上方
に突出する回転円筒、前記回転円筒に互いに上下方向に
間隔をおいて水平に取付けられ固定容器内の液状体に旋
回流を発生させる回転板、隣接する前記回転板の間に位
置して前記回転円筒の外壁に設けられた通液口、前記回
転円筒の前記固定容器から上方に突出する部分に設けら
れた放液口、及び前記固定容器に接続された排液管を備
えたことを特徴とする液状体の遠心分離装置。
A sealed vertical cylindrical fixed container, a liquid supply port provided on the bottom plate of the fixed container, a liquid supply port provided in the fixed container concentrically in the axial direction thereof, and the upper part thereof is above the fixed container. a rotating cylinder that protrudes from the rotating cylinder; a rotating plate that is horizontally attached to the rotating cylinder at intervals in the vertical direction and generates a swirling flow in the liquid in the fixed container; and a rotating plate that is located between the adjacent rotating plates and that A liquid that is characterized by comprising a liquid passage port provided on an outer wall, a liquid discharge port provided in a portion of the rotating cylinder that projects upward from the fixed container, and a drain pipe connected to the fixed container. Body centrifuge.
JP21575190A 1990-08-17 1990-08-17 Centrifugal separator of liquid Pending JPH04100554A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP21575190A JPH04100554A (en) 1990-08-17 1990-08-17 Centrifugal separator of liquid

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP21575190A JPH04100554A (en) 1990-08-17 1990-08-17 Centrifugal separator of liquid

Publications (1)

Publication Number Publication Date
JPH04100554A true JPH04100554A (en) 1992-04-02

Family

ID=16677618

Family Applications (1)

Application Number Title Priority Date Filing Date
JP21575190A Pending JPH04100554A (en) 1990-08-17 1990-08-17 Centrifugal separator of liquid

Country Status (1)

Country Link
JP (1) JPH04100554A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012516773A (en) * 2009-02-05 2012-07-26 アルファ・ラバル・コーポレイト・エービー Apparatus for separating oil from a gas mixture and method for separating oil from a gas mixture

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012516773A (en) * 2009-02-05 2012-07-26 アルファ・ラバル・コーポレイト・エービー Apparatus for separating oil from a gas mixture and method for separating oil from a gas mixture
JP2015120157A (en) * 2009-02-05 2015-07-02 アルファ・ラバル・コーポレイト・エービー Apparatus for separating oil from gas mixture, and method for separating oil from gas mixture

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