JPH0647084B2 - centrifuge - Google Patents

centrifuge

Info

Publication number
JPH0647084B2
JPH0647084B2 JP60121084A JP12108485A JPH0647084B2 JP H0647084 B2 JPH0647084 B2 JP H0647084B2 JP 60121084 A JP60121084 A JP 60121084A JP 12108485 A JP12108485 A JP 12108485A JP H0647084 B2 JPH0647084 B2 JP H0647084B2
Authority
JP
Japan
Prior art keywords
liquid
meniscus
centrifuge
diameter side
guide
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
Application number
JP60121084A
Other languages
Japanese (ja)
Other versions
JPS61278370A (en
Inventor
丈夫 風間
Original Assignee
石川島播磨重工業株式会社
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 石川島播磨重工業株式会社 filed Critical 石川島播磨重工業株式会社
Priority to JP60121084A priority Critical patent/JPH0647084B2/en
Publication of JPS61278370A publication Critical patent/JPS61278370A/en
Publication of JPH0647084B2 publication Critical patent/JPH0647084B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B04CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04BCENTRIFUGES
    • B04B11/00Feeding, charging, or discharging bowls
    • B04B11/08Skimmers or scrapers for discharging ; Regulating thereof
    • B04B11/082Skimmers for discharging liquid
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B04CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04BCENTRIFUGES
    • B04B1/00Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles
    • B04B1/20Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles discharging solid particles from the bowl by a conveying screw coaxial with the bowl axis and rotating relatively to the bowl
    • B04B2001/2083Configuration of liquid outlets

Landscapes

  • Centrifugal Separators (AREA)

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は、運転中に外部から自由に液面位置の調整がで
き、且つ有圧状態の液排出を可能にした遠心分離機に関
するものである。
TECHNICAL FIELD The present invention relates to a centrifuge in which the liquid surface position can be freely adjusted from the outside during operation and the liquid can be discharged under pressure. is there.

[従来の技術] 第6図は従来のスクリューデカンタ形遠心分離機の概略
を示すものであり、一端がテーパ状の回転円筒1の中に
スクリューコンベヤ2が同心状に配設され、回転円筒1
及びスクリューコンベヤ2は、それぞれ別個に単独で回
転し得るように支持されている。スクリューコンベヤ2
の中空軸には、吐出口4が穿設され、中空軸内部にはフ
ィードパイプ3が装入されている。一方前記回転円筒1
の小径側には、分離された固形分を排出するための排出
口5が設けられ、他端大径側に設けた排出口6には、清
澄液排出用の堰板6aが備えられている。
[Prior Art] FIG. 6 shows an outline of a conventional screw decanter type centrifugal separator, in which a screw conveyor 2 is concentrically arranged in a rotary cylinder 1 having one end tapered.
The screw conveyor 2 and the screw conveyor 2 are supported so that they can rotate independently of each other. Screw conveyor 2
The hollow shaft is provided with a discharge port 4, and the feed pipe 3 is inserted inside the hollow shaft. On the other hand, the rotating cylinder 1
The discharge port 5 for discharging the separated solid content is provided on the small diameter side of the, and the discharge port 6 provided on the other end large diameter side is provided with a weir plate 6a for discharging the clarified liquid. .

上記遠心分離機において、フィードパイプ3より供給さ
れたスラリーは、スクリューコンベヤ2の中空軸に設け
られた吐出口4より回転円筒1内に放出され、ここで清
澄液と固形分に分離される。固形分はスクリューコンベ
ヤ2により回転円筒小径側の排出口5より機外に排出さ
れ、清澄液は回転円筒大径側排出口6の堰板6aをオーバ
ーフローする。
In the above centrifuge, the slurry supplied from the feed pipe 3 is discharged into the rotary cylinder 1 through the discharge port 4 provided in the hollow shaft of the screw conveyor 2, and is separated into a clarified liquid and a solid content there. The solid content is discharged to the outside of the machine from the discharge port 5 on the small diameter side of the rotating cylinder by the screw conveyor 2, and the clarified liquid overflows the weir plate 6a of the discharge port 6 on the large diameter side of the rotating cylinder.

この際固形分の脱液を良くするためには、液面Lを外径
側にすることによって回転円筒1の脱液部分1bを長くす
る必要がある。他面排出液の清澄度を良くするために
は、液面Lを内径側にすることによって、液のホールド
量を増やすことが必要である。
At this time, in order to improve the drainage of the solid content, it is necessary to lengthen the drainage portion 1b of the rotary cylinder 1 by setting the liquid surface L on the outer diameter side. In order to improve the clarity of the liquid discharged on the other surface, it is necessary to increase the liquid hold amount by setting the liquid surface L to the inner diameter side.

この液面Lを調整するために、上記従来装置においては
遠心分離機を一時停止して、堰板6aの交換をおこなわな
ければならないため、操作が繁雑であると云う問題があ
る。
In order to adjust the liquid level L, in the above-mentioned conventional apparatus, the centrifuge must be temporarily stopped and the weir plate 6a must be replaced, which causes a problem that the operation is complicated.

上記問題を解決するための従来装置としては、第7図
(イ)(ロ)、第8図(イ)(ロ)に示すように、スキミングパイプ
を使用したものや、第9図(イ)(ロ)に示すように求心ポン
プを使用したもの(例えば特公昭50-6667号)がある。
As a conventional device for solving the above problem, FIG.
(A) (b), those using a skimming pipe as shown in FIG. 8 (a) (b), and those using a centripetal pump as shown in FIG. 9 (a) (b) (for example, Japanese Patent Publication No. 50-6667).

第7図(イ)(ロ)に示す方式は、回転円筒1の内側に先端が
突出するようにした吸入管22を、ケーシング23に回転自
在にとりつけ、吸入管22を回動することによってその先
端を変化せしめ、液面Lの調整を図るものである。
In the system shown in FIGS. 7 (a) and 7 (b), the suction pipe 22 having a tip protruding inside the rotary cylinder 1 is rotatably mounted on the casing 23, and the suction pipe 22 is rotated to rotate the suction pipe 22. The tip is changed to adjust the liquid level L.

第8図(イ)(ロ)に示す方式は、回転円筒1の内側に、先端
を突出させた吸入管24をその軸心方向に伸縮させてその
先端を変位せしめ、液面調整を図るものである。
The method shown in FIGS. 8 (a) and 8 (b) is for adjusting the liquid level by expanding and contracting the suction pipe 24 having a protruding end inside the rotating cylinder 1 in the axial direction thereof to displace the end thereof. Is.

第9図(イ)(ロ)に示す方式は、回転円筒内に回動自在に支
持された円板25を回動して、該円板に備えられた吸入路
口25aを変位させ、液面Lの調整を図るものである。
In the system shown in FIGS. 9 (a) and 9 (b), the circular plate 25 rotatably supported in the rotary cylinder is rotated to displace the suction passage port 25a provided in the circular plate, and It is intended to adjust L.

[発明が解決しようとする問題点] しかしながら、上記従来装置にあっては、次のような種
々の問題がある。
[Problems to be Solved by the Invention] However, the above-described conventional device has the following various problems.

すなわち、第7図(イ)(ロ)に示すものでは、液の自由表面
の曲率と吸入管の曲率が流体力学上理想的になるのは、
1点のみであり、従ってその1点以外の位置では液流の
乱れが大きく、吸入管の流路抵抗は非常に大きくなる。
That is, in FIGS. 7A and 7B, the curvature of the free surface of the liquid and the curvature of the suction pipe are ideal in terms of hydrodynamics.
Since there is only one point, the turbulence of the liquid flow is large at positions other than that point, and the flow path resistance of the suction pipe becomes very large.

又、第8図(イ)(ロ)に示すものでは、吸入管の曲率を液の
自由表面の曲率に合致せしめることが不可能であり、液
流が乱れるため、吸入管の流路抵抗が非常に大きくな
る。
Further, in the case shown in FIGS. 8 (a) and (b), it is impossible to match the curvature of the suction pipe with the curvature of the free surface of the liquid, and the liquid flow is disturbed. Grows very large.

更に第7図(イ)(ロ)、第8図(イ)(ロ)いずれの方式も機構上
吸入管の占めるスペースの制約、多数個の吸入管を設け
た場合の吸入口位置を、同期同調させるのが構造的に困
難と云う制約などがあり、吸入管路断面積を拡大でき
ず、吸入管流路抵抗の軽減は不可能である。
Further, in both of FIG. 7 (a) (b) and FIG. 8 (a) (b), the space occupied by the suction pipes on the mechanism is restricted, and the suction port position when multiple suction pipes are provided is synchronized. There are restrictions such that it is structurally difficult to tune them, the cross-sectional area of the suction pipe cannot be expanded, and it is impossible to reduce the suction pipe flow resistance.

更に又第9図(イ)(ロ)に示すものでは、吸入路の液面に対
する角度αの変化にともない液の流入状態に影響を与え
るが、液流の乱れが少いのは、第9図(ロ)に示す位置関
係にある場合のみで、他の位置では液流の乱れが大きく
なり、流入口抵抗が大となる。第7図〜第9図のいずれ
の場合も、液流の乱れが大きいと、発泡性の液を取扱う
場合に、泡を生じ易く後工程で消泡操作を行う必要が生
じる。遠心分離機内のスラリー液は、回転円筒と共に、
通常2000〜4000r.p.m.の高速で回転しているが、第9図
(イ)(ロ)に示すように円板25がその液中に深く侵入すると
スラリー液中に大きな撹乱を引き起して、遠心分離機の
分離性能を低下させる。この方式も機構上吸入口は一ヶ
所しか設けることができないので前記スキミングパイプ
方式と同様に吸入路断面積を増大できず、スラリー供給
量が増加すると液面が変動するが遠心分離機の分離性能
と固形物の脱水性能を維持するために、液面を一定させ
る必要があり吸入管吸入口の位置を頻繁に調整しなけれ
ばならない。
Furthermore, in the case shown in FIGS. 9 (a) and 9 (b), the inflow state of the liquid is affected by the change of the angle α with respect to the liquid surface of the suction passage, but the turbulence of the liquid flow is small. Only in the case of the positional relationship shown in the figure (b), the turbulence of the liquid flow becomes large and the inlet resistance becomes large at other positions. In any of FIGS. 7 to 9, if the turbulence of the liquid flow is large, bubbles are liable to be generated when handling the foaming liquid, and it is necessary to perform the defoaming operation in the subsequent step. The slurry liquid in the centrifuge, along with the rotating cylinder,
It usually rotates at a high speed of 2000 to 4000 rpm, but Fig. 9
(A) When the disc 25 deeply penetrates into the liquid as shown in (b), a large disturbance is caused in the slurry liquid, and the separation performance of the centrifugal separator is deteriorated. Since only one intake port can be provided in this system due to the mechanism, the cross-sectional area of the intake passage cannot be increased as in the skimming pipe system, and the liquid level fluctuates as the slurry supply increases, but the separation performance of the centrifuge is increased. In order to maintain the dehydration performance of solids, it is necessary to keep the liquid level constant and the position of the suction pipe suction port must be adjusted frequently.

本発明は上記の実情に鑑み運転中に外部から液面位置を
自由に調整し得るようにし、且つ清澄液の加圧排出を行
い得るようにすることを目的としたものである。
SUMMARY OF THE INVENTION The present invention has been made in view of the above circumstances, and an object thereof is to allow the liquid surface position to be freely adjusted from the outside during operation, and to allow the clear liquid to be discharged under pressure.

[問題点を解決するための手段] 本発明では回転円筒の大径端部に排液室を設け、該排液
室内に排液吸入口を開口する求心ポンプを前記回転円筒
大径部外側に配設し、求心ポンプは、排液通路と半月板
案内溝を備えた半月板ガイドを前記回転円筒大径端部に
配設し、半月板案内溝には排液吸入口を備えた半月板14
を滑合せしめ、半月板14背面より突出したピンを案内す
るカム溝を備えた駆動円板を、前記半月板ガイドのボス
外周に例えばハンドルにより回転し得るように嵌合して
形成したものである。
[Means for Solving the Problems] In the present invention, a centripetal pump, which is provided with a drainage chamber at the large-diameter end of the rotary cylinder and has a drainage inlet opening in the drainage chamber, is provided outside the rotary cylinder large-diameter portion. The centripetal pump is provided with a meniscus guide having a drainage passage and a meniscus guide groove at the large diameter end of the rotating cylinder, and a meniscus having a drainage suction port in the meniscus guide groove. 14
And a drive disk having a cam groove for guiding a pin projecting from the rear surface of the meniscus 14 is fitted to the outer periphery of the boss of the meniscus guide so as to be rotatable by a handle, for example. is there.

[作用] ハンドルにより駆動円板を回転させると、カム溝によっ
てピンが案内されるため、半月板は半月板ガイドの案内
溝に沿って放射方向に移動し、半月板に備えられている
吸入口の位置を、内径側から外径側まで連続的に変化さ
せる。
[Operation] When the drive disc is rotated by the handle, the pin is guided by the cam groove, so that the meniscus moves in the radial direction along the guide groove of the meniscus guide, and the suction port provided in the meniscus. The position of is continuously changed from the inner diameter side to the outer diameter side.

[実施例] 以下本発明の実施例を添付図面を参照しつつ説明する。Embodiments Embodiments of the present invention will be described below with reference to the accompanying drawings.

第1図〜第5図は本発明の一実施例であり、回転円筒1
の大径端部の側面に、回転円筒1から排出口6を経て排
出された清澄液を留める排液室10を設け、該排液室10か
ら吸入された液を集液室12に送る求心ポンプ11を回転円
筒1に同心状に回転円筒1の大径側端部外側に配設す
る。
1 to 5 show an embodiment of the present invention, which is a rotary cylinder 1
A drainage chamber 10 is provided on the side surface of the large-diameter end portion of the rotary cylinder 1 for holding the clarified liquid discharged from the rotary cylinder 1 through the discharge port 6, and centripetal that sends the liquid sucked from the drainage chamber 10 to the liquid collection chamber 12. The pump 11 is arranged concentrically with the rotary cylinder 1 outside the large diameter side end of the rotary cylinder 1.

求心ポンプ11の詳細について説明すると、排液室10から
集液室12に至る排液通路15aを備えた半月板ガイド15の
ボス外周に、例えばハンドル17により回転させ得るよう
にした駆動円板16を嵌合せしめ、該駆動円板16には第3
図、第4図に示すように円板内周側から外周側へ向けて
延びる曲線状のカム溝16aを設け、前記半月板ガイド15
の案内溝15bに、吸入口14bを備えた2枚1対の半月板
14を、案内溝15bに沿って放射方向へ摺動し得るように
嵌合せしめ、前記一対の半月板14にピン14aを突出せし
めて、該ピン14aを前記駆動円板16のカム溝16aに嵌入
せしめ、前記駆動円板16の回転角変位をカム溝16a及び
ピン14aを介し半月板14の放射方向変位に転換し得るよ
うにする。カム溝16aは、駆動円板16の回転角変位と半
月板14の放射方向への変位が正比例するようなカーブに
なっている。
Explaining the details of the centripetal pump 11, the drive disk 16 that can be rotated by, for example, a handle 17 is provided on the boss outer circumference of the meniscus guide 15 having a drainage passage 15a from the drainage chamber 10 to the liquid collection chamber 12. The drive disc 16 with a third
As shown in FIGS. 4 and 5, a curved cam groove 16a extending from the inner peripheral side of the disc toward the outer peripheral side is provided, and the meniscus guide 15 is provided.
A pair of meniscus with a suction port 14b in its guide groove 15b
14 is fitted so as to be slidable in the radial direction along the guide groove 15b, and the pin 14a is projected to the pair of meniscus plates 14, and the pin 14a is fitted in the cam groove 16a of the drive disk 16. It is fitted so that the rotational angle displacement of the drive disc 16 can be converted into the radial displacement of the meniscus 14 via the cam groove 16a and the pin 14a. The cam groove 16a is curved so that the rotational angle displacement of the drive disc 16 and the radial displacement of the meniscus 14 are directly proportional.

又半月板14には、液流の乱れを最小に抑えて液を吸入し
得るように形成した渦巻き状の液通路14cが設けられ、
排液室10から吸入口14bを介して液通路14cへ吸入され
た液は、該液通路14cから液通路15aを通り集液室12に
送られるようになっている。
Further, the meniscus 14 is provided with a spiral liquid passage 14c formed so as to minimize the turbulence of the liquid flow and suck the liquid.
The liquid sucked into the liquid passage 14c from the drainage chamber 10 through the suction port 14b is sent to the liquid collection chamber 12 from the liquid passage 14c through the liquid passage 15a.

ハンドル17を操作して駆動円板16を回転させると、カム
溝16aによりピン14aが案内されるため、半月板14は半
月板ガイド15の案内溝15bに沿って放射方向へ移動し、
半月板14に設けられた吸入口14bの位置は第3図に示す
内径側から第4図に示す外径側まで連続的に変えられ
る。従って運転中に液面は自由に変えられ、吸入口14b
がいかなる位置にある場合でも液通路14cを通る液の乱
れは最小になる。
When the drive disk 16 is rotated by operating the handle 17, the pin 14a is guided by the cam groove 16a, so that the meniscus 14 moves in the radial direction along the guide groove 15b of the meniscus guide 15,
The position of the suction port 14b provided in the meniscus 14 can be continuously changed from the inner diameter side shown in FIG. 3 to the outer diameter side shown in FIG. Therefore, the liquid level can be changed freely during operation, and the suction port 14b
The turbulence of the liquid passing through the liquid passage 14c is minimized regardless of the position of the liquid.

なお、本発明の実施例においては半月板の移動をピン及
びカム溝により行う場合について説明したが、これに限
らず種々のカム機構を採用し得ること、その他、本発明
の要旨を逸脱しない範囲内で種々変更を加え得ること、
等は勿論である。
In addition, in the embodiment of the present invention, the case where the movement of the meniscus is performed by the pin and the cam groove has been described. However, not limited to this, various cam mechanisms can be adopted, and the scope of the present invention is not deviated. That you can make various changes within
Of course, etc.

[発明の効果] 本発明の遠心分離機は、上述のような構成を有するので
下記の如き種々の優れた効果を奏し得る。
[Effects of the Invention] Since the centrifuge of the present invention has the configuration as described above, it can exhibit various excellent effects as described below.

(I)運転中に停止する必要なく外部から自由に液面の調
整ができる。
(I) The liquid level can be freely adjusted from the outside without the need to stop during operation.

(II)吸入口がいかなる位置にある場合でも乱流発生を最
小にして液排出ができる。
(II) Regardless of the position of the suction port, turbulent flow can be minimized and liquid can be discharged.

(III)吸入口を2ヶ所に設けることができるので大流量
を流す場合にも液面に変化が少い。
(III) Since the suction ports can be provided at two places, there is little change in the liquid level even when a large flow rate is passed.

(IV)液中に侵入するのは、半月板のごく一部分のみであ
るから液を撹乱して分離性能を阻害しない。
(IV) Since only a small part of the meniscus penetrates into the liquid, it does not disturb the separation performance by disturbing the liquid.

(V)求心ポンプ内蔵形式となるので、有圧排液が得られ
高所への液の配送に、別途加圧装置を必要としない。
(V) Since it has a centripetal pump built-in type, it does not require a separate pressurizing device to obtain pressurized drainage and deliver the fluid to a high place.

【図面の簡単な説明】[Brief description of drawings]

第1図は、本発明の遠心分離機の一実施例の説明図、第
2図は、本発明の遠心分離機に使用する求心ポンプの部
分の詳細図、第3図は第2図のA−A矢視図で、半月板
が縮小した状態の説明図、第4図は、同半月板が拡大し
た状態の説明図、第5図は、本発明の遠心分離機に使用
する求心ポンプ構成部品の立体図、第6図は、従来のス
クリューデカンタ形遠心分離機の説明図、第7図(イ)(ロ)
及び第8図(イ)(ロ)は、スキミングパイプを使用した従来
の遠心分離機の一例の説明図、第9図(イ)(ロ)は求心ポン
プを使用した従来の遠心分離機の一例の説明図である。 図中1は回転円筒、2はスクリューコンベヤ、3はフィ
ードパイプ、10は排液室、11は求心ポンプ、12は集液
室、14は半月板、14aはピン、14bは吸入口、14cは液
通路、15は半月板ガイド、15aは排液通路、15bは案内
溝、16は駆動円板、16aはカム溝、17はハンドルを示
す。
FIG. 1 is an explanatory view of an embodiment of the centrifuge of the present invention, FIG. 2 is a detailed view of a centripetal pump used in the centrifuge of the present invention, and FIG. 3 is an A of FIG. FIG. 4 is an explanatory view of the state where the meniscus is contracted, FIG. 4 is an explanatory view of the state where the meniscus is enlarged, and FIG. 5 is a centripetal pump configuration used in the centrifuge of the present invention. Fig. 6 is a three-dimensional view of the parts, Fig. 6 is an explanatory view of a conventional screw decanter type centrifuge, and Fig. 7 (a) (b).
8 (a) and (b) are explanatory views of an example of a conventional centrifuge using a skimming pipe, and FIG. 9 (a) (b) is an example of a conventional centrifuge using a centripetal pump. FIG. In the figure, 1 is a rotating cylinder, 2 is a screw conveyor, 3 is a feed pipe, 10 is a draining chamber, 11 is a centripetal pump, 12 is a collecting chamber, 14 is a meniscus, 14a is a pin, 14b is an inlet, 14c is Liquid passage, 15 is a meniscus guide, 15a is a drain passage, 15b is a guide groove, 16 is a drive disc, 16a is a cam groove, and 17 is a handle.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】回転円筒大径部側端部に、該回転円筒と同
心状に、外部からの操作により回転し得るようにした駆
動円板を配設し、該駆動円板の中空部内周に、回転円筒
放射方向へ延びる案内溝を有する半月板ガイドを嵌合せ
しめ、該半月板ガイドの案内溝に、回転円筒大径部側か
ら外部へ液を排出する液通路を備えた半月板を摺動自在
に嵌合せしめ、該半月板を前記案内溝に沿って回転円筒
放射方向へ移動させるカム機構を前記駆動円板と半月板
との間に設けたことを特徴とする遠心分離機。
1. A drive disk, which is concentric with the rotary cylinder and is rotatable by an external operation, is arranged at an end of the rotary cylinder on the large-diameter side, and an inner circumference of a hollow part of the drive disk is provided. , A meniscus guide having a guide groove extending in the radial direction of the rotating cylinder is fitted, and a meniscus having a liquid passage for discharging liquid from the large diameter side of the rotating cylinder to the outside is fitted in the guide groove of the meniscus guide. A centrifuge characterized in that a cam mechanism, which is slidably fitted and moves the meniscus along the guide groove in a radial direction of the rotating cylinder, is provided between the drive disc and the meniscus.
JP60121084A 1985-06-04 1985-06-04 centrifuge Expired - Lifetime JPH0647084B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60121084A JPH0647084B2 (en) 1985-06-04 1985-06-04 centrifuge

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60121084A JPH0647084B2 (en) 1985-06-04 1985-06-04 centrifuge

Publications (2)

Publication Number Publication Date
JPS61278370A JPS61278370A (en) 1986-12-09
JPH0647084B2 true JPH0647084B2 (en) 1994-06-22

Family

ID=14802464

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60121084A Expired - Lifetime JPH0647084B2 (en) 1985-06-04 1985-06-04 centrifuge

Country Status (1)

Country Link
JP (1) JPH0647084B2 (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DK176946B1 (en) 2007-05-09 2010-06-14 Alfa Laval Corp Ab Centrifugal separator and a liquid phase drain port element
CN102125894B (en) * 2010-12-21 2013-01-09 莫珉珉 Improved horizontal decanter centrifuge
JP5832828B2 (en) * 2011-08-30 2015-12-16 巴工業株式会社 Variable dam of centrifuge and centrifuge
CN107088475A (en) * 2017-05-27 2017-08-25 宜兴市华鼎机械有限公司 A kind of horizontal centrifuge of the adjustable centripetal discharge pump of band

Also Published As

Publication number Publication date
JPS61278370A (en) 1986-12-09

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