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JP2727411B2 - Separator centrifuge - Google Patents

Separator centrifuge

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Publication number
JP2727411B2
JP2727411B2 JP10199194A JP10199194A JP2727411B2 JP 2727411 B2 JP2727411 B2 JP 2727411B2 JP 10199194 A JP10199194 A JP 10199194A JP 10199194 A JP10199194 A JP 10199194A JP 2727411 B2 JP2727411 B2 JP 2727411B2
Authority
JP
Japan
Prior art keywords
heavy liquid
liquid
heavy
light liquid
impeller
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 - Fee Related
Application number
JP10199194A
Other languages
Japanese (ja)
Other versions
JPH07284693A (en
Inventor
正宏 森口
一夫 野嶋
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.)
Mitsubishi Kakoki Kaisha Ltd
Original Assignee
Mitsubishi Kakoki Kaisha Ltd
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 Mitsubishi Kakoki Kaisha Ltd filed Critical Mitsubishi Kakoki Kaisha Ltd
Priority to JP10199194A priority Critical patent/JP2727411B2/en
Publication of JPH07284693A publication Critical patent/JPH07284693A/en
Application granted granted Critical
Publication of JP2727411B2 publication Critical patent/JP2727411B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は、分離板型遠心分離機に
関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a separator centrifuge.

【0002】[0002]

【従来の技術】固形物及び水分を含む潤滑油、燃料油等
の清浄には調節板式分離板型遠心分離機が従来使用され
ており、これによると分離室内の水分(以下重液とい
う)と油分(以下軽液という)との界面が分離板の所定
の半径上に安定して維持されるように、重液通路の出口
部に環状出口堰(以下調節板という)を設けている。
2. Description of the Related Art Conventionally, an adjusting plate type centrifugal separator has been used for cleaning lubricating oil, fuel oil and the like containing solid matter and moisture. An annular outlet weir (hereinafter referred to as a control plate) is provided at the outlet of the heavy liquid passage so that the interface with the oil (hereinafter referred to as the light liquid) is stably maintained at a predetermined radius of the separation plate.

【0003】しかしながら、この種の遠心分離機では、
処理油(以下原液という)の比重が変わる場合には、こ
れに応じてその調節板を重液−軽液の界面の変動に応じ
て所定の半径上に位置せしめるよう最適の直径の調節板
に変更しなければならないので取扱いが厄介である。そ
こで本出願人は、先に特開昭61−78451号で調節
板方式に代わるものとして、遠心分離機から排出される
軽液中の水分を検知し、これによって重液の排出を制御
する手段を提案した。
However, this type of centrifuge has
When the specific gravity of the treated oil (hereinafter referred to as “stock solution”) changes, the adjusting plate is adjusted to an optimal diameter so that it can be positioned on a predetermined radius in accordance with the fluctuation of the heavy liquid-light liquid interface. Handling is cumbersome because it must be changed. Accordingly, the present applicant has previously proposed a method of controlling the discharge of the heavy liquid by detecting the moisture in the light liquid discharged from the centrifuge as an alternative to the adjusting plate method in Japanese Patent Application Laid-Open No. 61-78451. Suggested.

【0004】すなわち、軽液の排出管路に静電容量型の
水分検出器を設け、回転胴内の分離室に所定量以上の水
分が分離堆積すると、軽液側に水分がキャリーオーバー
する現象を利用し、同水分検出器により軽液中の水分を
検出すれば、制御器を介して回転胴のスラッジ排出用主
弁(以下、主弁という)を開閉することで堆積水分を外
部に排出する方法である。
[0004] That is, when a capacitance type moisture detector is provided in a light liquid discharge pipe and a predetermined amount or more of water is separated and deposited in a separation chamber in a rotary drum, the carryover of water to the light liquid side occurs. When the moisture detector detects moisture in the light liquid, the main valve for discharging sludge of the rotating drum (hereinafter referred to as the main valve) is opened and closed via the controller to discharge accumulated moisture to the outside. How to

【0005】[0005]

【発明が解決しようとする課題】しかしながら静電容量
型水分検出器は高価格であるとともに、維持管理にも労
力を要するため、比較的低コストの維持管理の容易な水
分検出手段の開発が要望されている。本発明はこのよう
な事情に鑑みて提案されたもので、維持管理が容易で分
離性能の高い比較的低コストの経済的な分離板型遠心分
離機を提供することを目的とする。
However, since the capacitance type moisture detector is expensive and requires maintenance work, there is a need for the development of a relatively low-cost and easy-to-maintain moisture detection means. Have been. The present invention has been proposed in view of such circumstances, and an object of the present invention is to provide a relatively low-cost economical separator-type centrifuge that is easy to maintain and has high separation performance.

【0006】[0006]

【課題を解決するための手段】そのために請求項1の装
置の発明は、回転胴内に設けられたスラッジ排出用主弁
と、軽液排出流路に設けられた軽液インペラーと、重液
排出流路に設けられた重液インペラーとを有する分離板
型遠心分離機において、出口端が閉塞された重液インペ
ラーに付設され同重液インペラーの内部圧を検出する圧
力検出器と、上記圧力検出器の出力に応動して主弁開閉
用作動水の制御弁を開閉する制御器とを具えるととも
に、その重液インペラー径を軽液自由表面径より大きく
したことを特徴とする。
For this purpose, an apparatus according to the first aspect of the present invention comprises: a main valve for discharging sludge provided in a rotary drum; a light liquid impeller provided in a light liquid discharge passage; In a separator centrifuge having a heavy liquid impeller provided in a discharge channel, a pressure detector attached to the heavy liquid impeller having an outlet end closed and detecting an internal pressure of the heavy liquid impeller; and A controller for opening and closing the control valve for the main valve opening / closing hydraulic water in response to the output of the detector, and having a heavy liquid impeller diameter larger than a light liquid free surface diameter.

【0007】[0007]

【作用】本発明の分離板型遠心分離機の作用、特に回転
胴内での重・軽液成分の分離の進行について、本発明の
原理図である図2に基づいて説明する。 (1)同図(A)に示すように、原液の導入を開始す
る。 (2)軽液インペラーから軽液が流出するとともに、重
液流路には重液インペラー出口が閉塞されているため、
軽液が滞留する。 (3)重液が徐々に回転胴の内面に堆積し、重・軽液界
面D2 が仕切板の先端D1 に達する。 (4)重・軽液界面D2 が同図(B)に示すように、仕
切板の先端D1 より内径側に至ると、重液流路には点線
で図示されるような、重液と軽液の界面が仕切板径D1
より若干内径寄りに形成される。
The operation of the centrifugal separator of the present invention, in particular, the progress of separation of heavy and light liquid components in the rotary drum will be described with reference to FIG. 2 which is a principle diagram of the present invention. (1) As shown in FIG. 1A, the introduction of a stock solution is started. (2) Since the light liquid flows out of the light liquid impeller and the heavy liquid impeller outlet is closed in the heavy liquid flow path,
Light liquid stays. (3) heavy liquid is deposited on the inner surface of the slowly rotating cylinder, the heavy and light liquid interface D 2 reaches tip D 1 of the partition plate. (4) such that the heavy and light liquid interface D 2 shown in FIG. (B), reaches the inner diameter side from the tip end D 1 of the partition plate, such as the heavy liquid flow path is illustrated in dotted lines, heavy liquid The interface between the liquid and the light liquid is the partition plate diameter D 1
It is formed slightly closer to the inner diameter.

【0008】(5)回転胴内の重液の堆積量が徐々に増
すにつれて、重液流路中の軽液自由表面が内径側に移動
し、やがて同図(B)に示すように、重・軽液の比重差
により、回転胴内の軽液面との間にレベル差δが生ず
る。 (6)このレベル差δと下記の理由により重液インペラ
ーの内部圧力が急増し、これを圧力検出器が検知して重
液が回転胴内に溜まったことが検出され、排出信号によ
り主弁が開いて溜まった重液を排出孔より外部へ排出す
る。 (7)運転を継続し(1)に戻る。
(5) As the amount of heavy liquid accumulated in the rotating drum gradually increases, the free surface of the light liquid in the heavy liquid flow path moves toward the inner diameter side, and as shown in FIG. -A level difference δ is generated between the light liquid level in the rotary drum and the specific gravity difference of the light liquid. (6) Due to this level difference δ and the following reason, the internal pressure of the heavy liquid impeller suddenly increases, and this is detected by a pressure detector, and it is detected that heavy liquid has accumulated in the rotary drum. Opens and discharges the accumulated heavy liquid to the outside through the discharge hole. (7) Continue the operation and return to (1).

【0009】前記した図2(A)に示される状態におい
て、重液チャンバー内のインペラー径をD3 ,軽液の自
由表面径をD4 とすると、インペラー外端における圧力
34は次の(1) 式で表される。 P34=(γω2 /8g)(D3 2−D4 2)(kg/cm2 )・・・(1) 自由表面径D4 が同図(B)に示すように、D5 になる
と、圧力P35は次の(2)式で表される。 P35=(γω2 /8g)(D3 2−D5 2)(kg/cm2 )・・・(2) ここで、γは軽液の比重,ωは回転体の角速度である。 (亀井三郎著、化学機械の理論と計算、産業図書、P42
7,1970)
In the state shown in FIG. 2A, assuming that the impeller diameter in the heavy liquid chamber is D 3 and the free surface diameter of the light liquid is D 4 , the pressure P 34 at the outer end of the impeller is as follows: 1) It is expressed by the formula. P 34 = (γω 2 / 8g ) (D 3 2 -D 4 2) (kg / cm 2) ··· (1) as shown in the free surface diameter D 4 is the drawing (B), becomes the D 5 , the pressure P 35 is represented by the following equation (2). P 35 = (γω 2 / 8g ) (D 3 2 -D 5 2) (kg / cm 2) ··· (2) where, gamma is the specific gravity of the light liquid, omega is the angular velocity of the rotating body. (Saburo Kamei, Chemical Machine Theory and Calculations, Industrial Books, P42
7,1970)

【0010】このように原液処理の進行に伴い徐々に分
離重液の量が増え、D2 が内向き半径方向に移動し、や
がてD2 <D1 となると、仕切板の上方の軽液は内向き
半径方向に移動し、δが発生し、D5 <D4 となり、前
記式よりP35>P34となり、これを上端が閉塞されたイ
ンペラー内の圧力を測定することにより、検出すること
ができる。
As described above, the amount of the separated heavy liquid gradually increases with the progress of the undiluted liquid treatment, and D 2 moves inward in the radial direction. When D 2 <D 1 , the light liquid above the partition plate is removed. Moving in the inward radial direction, δ is generated, and D 5 <D 4 , P 35 > P 34 according to the above equation, and this is detected by measuring the pressure in the impeller closed at the upper end. Can be.

【0011】 以上から重液インペラー径Dは、レベ
ル差δを検知するためには軽液の自由表面径Dより大
きくする必要があるが、 の径が大きすぎると重液チ
ャンパー内における重液インペラーに対する軽液の抵抗
が大きくなり回転体を回転させているモータ本体の必要
動力が大きくなるので注意が必要であるまた重・軽液
境界面径Dが分離板4の外径と仕切り板径Dの間の
好適な位置になるよう前記式により、重液チャンパー内
軽液自由表面径Dを求めれば、重・軽液境界面径D
を好適位置に維持して運転できることが判る.
[0011] The heavy liquid impeller diameter D 3 from above, level
Although in order to detect the Le difference δ should be larger than the free surface diameter D 0 of the light liquid, heavy liquid Ji when the diameter of D 3 is too large
Resistance of light liquid to heavy liquid impeller in jumper
Motor body that rotates the rotating body
Care must be taken because the power is increased . Also by the equation so that the heavy and light liquid boundary surface diameter D 2 becomes a suitable position between the outer diameter and the partition plate diameter D 1 of the separating plate 4, the heavy liquid Chanpa <br/> light liquid free surface diameter D 5 is obtained, the heavy-light liquid interface diameter D 2
It can be seen that the vehicle can be operated while maintaining a suitable position.

【0012】[0012]

【実施例】本発明の一実施例を図面について説明する
と、図1はその全体縦断面図である。図1において、1
は図示せざる駆動手段により鉛直方向軸心の周りに高速
回転する回転胴で、上部には回転体蓋2が締付リングに
よって嵌着されている。3は回転体蓋2の上部に付設さ
れた軽液チャンバー、4は案内筒6の周りに適宜すきま
をもって積層された截頭円錐状の複数の分離板、5は回
転胴1の内周下部に鉛直方向に摺動可能に挿入された主
弁、7は回転胴1の外周にそれぞれ半径方向に摺動可能
に設けられた複数の副弁、25は各副弁7の下方に設け
られ開弁作動水を機外に排出するためのドレン孔、8は
軽液チャンバー3内に水平に挿入された軽液インペラー
で、回転胴1及び回転体蓋2の一体的高速回転とは無関
係に静止位置に取付けられている。
BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is an overall vertical sectional view of an embodiment of the present invention. In FIG. 1, 1
Is a rotating body which rotates at high speed around a vertical axis by a driving means (not shown), and a rotating body lid 2 is fitted on the upper part thereof by a tightening ring. 3 is a light liquid chamber attached to the upper part of the rotating body lid 2, 4 is a plurality of frusto-conical separation plates laminated around the guide cylinder 6 with an appropriate clearance, and 5 is a lower part of the inner periphery of the rotating drum 1. A main valve 7 slidably inserted in the vertical direction, a plurality of sub-valves 7 provided on the outer periphery of the rotary drum 1 so as to be slidable in the radial direction, and a valve 25 provided below each sub-valve 7 and opened A drain hole 8 for discharging the working water out of the machine is a light liquid impeller 8 horizontally inserted into the light liquid chamber 3, and is at a stationary position irrespective of the integral high-speed rotation of the rotating body 1 and the rotating body lid 2. Mounted on

【0013】9は回転体蓋2の上端開口を通して軸心方
向に挿入された原液供給管、10は回転胴1の外周に適
宜間隔で半径方向に穿設された複数のスラッジ排出孔、
15は重液インペラーの上部室の内圧を検出する圧力検
出器14の検出値に基づいて、開弁作動水制御弁23を
制御する制御器である。20は軽液チャンバー3の上部
に付設され、重液流路18と連通し、内部には重液イン
ペラー19が水平に挿入される重液チャンバーである。
Reference numeral 9 denotes a stock solution supply pipe inserted in the axial direction through an upper end opening of the rotating body lid 2; 10 denotes a plurality of sludge discharge holes formed in the outer periphery of the rotating drum 1 at appropriate intervals in a radial direction;
Reference numeral 15 denotes a controller that controls the valve-opening working water control valve 23 based on the detection value of the pressure detector 14 that detects the internal pressure of the upper chamber of the heavy liquid impeller. Reference numeral 20 denotes a heavy liquid chamber which is attached to the upper part of the light liquid chamber 3 and communicates with the heavy liquid flow path 18 and into which a heavy liquid impeller 19 is horizontally inserted.

【0014】このような装置において、遠心分離機が定
速回転に達したのち、原液供給管9より原液を案内筒6
を経て供給すると、原液は分離板4上で遠心分離され、
比重差によって外径側より内向き半径方向に固形分,重
液,軽液の順に分離室16内に層成される。
In such an apparatus, after the centrifugal separator reaches a constant speed, the undiluted solution is supplied from the undiluted solution supply pipe 9 to the guide cylinder 6.
And the undiluted solution is centrifuged on the separation plate 4,
The solid content, heavy liquid, and light liquid are formed in the separation chamber 16 in the radial direction inward from the outer diameter side due to the specific gravity difference.

【0015】重液は回転胴内の分離室16に徐々に溜ま
ってゆき、その重・軽液界面径D2 が仕切板17の径D
1 を越えて内向き半径方向に移動するに伴い、重液流路
18中の軽液は重液チャンバー20に入り、上端が閉塞
された重液インペラー19の上部圧が上昇する。
The heavy liquid gradually accumulates in the separation chamber 16 in the rotating drum, and its heavy / light liquid interface diameter D 2 is equal to the diameter D of the partition plate 17.
As it moves inward in the radial direction beyond 1 , the light liquid in the heavy liquid flow path 18 enters the heavy liquid chamber 20, and the upper pressure of the heavy liquid impeller 19 whose upper end is closed rises.

【0016】ちなみに、図2(A)において、回転数N
=9500rpm (ω=995),γ=900×10-6kg
/cm3 ,D3 =12cm,D4 =9cmとすると、式(1)
により P34=7.15kg/cm2 となり、同図(B)のように、自由液面径の変化δを5
mmとしてD5 =8.5cm とすれば、式(2)により、 P35=8.14kg/cm2 となるから、Δp=P35−P34=1kg/cm2 となり、慣
用の圧力検出器で十分検出できる。
By the way, in FIG. 2A, the rotational speed N
= 9500 rpm (ω = 995), γ = 900 × 10 -6 kg
/ Cm 3 , D 3 = 12 cm, D 4 = 9 cm, equation (1)
As a result, P 34 = 7.15 kg / cm 2 , and as shown in FIG.
if D 5 = 8.5 cm as mm, by the equation (2), P 35 = 8.14kg / cm 2 because made, Δp = P 35 -P 34 = 1kg / cm 2 , and the well in conventional pressure detector Can be detected.

【0017】そこで、圧力検出器14はインペラー上部
圧を検出し、これが設定値に達すると、その出力信号を
制御器15に送り、制御器15は制御弁23を開き、開
弁作動水を副弁7に導入する。これにより、副弁7は内
向き半径方向に摺動し、主弁水室11の作動水は副弁7
を経て排出され、主弁5は分離室16の内圧により開
き、回転胴1内の固形物及び重液は排出孔10から外部
に排出される。排出後タイマーの作用により、開弁作動
水の供給は停止し、副弁7内の作動水はドレン孔25か
らすべて排出され、副弁7は遠心力により外向き半径方
向に摺動して閉じるとともに、閉弁作動水が常に主弁水
室11に供給されているので、主弁5はその水圧により
押し上げられ回転体蓋2の下端に装着されたパッキンに
当接し、排出孔10は閉じ、回転胴内の重液の排出は停
止する。
Therefore, the pressure detector 14 detects the impeller upper pressure, and when the pressure reaches a set value, sends an output signal to the controller 15, and the controller 15 opens the control valve 23 and supplies the valve-opening operating water to the auxiliary. Introduce to valve 7. As a result, the sub-valve 7 slides inward in the radial direction, and the working water in the main valve water chamber 11 is supplied to the sub-valve 7.
The main valve 5 is opened by the internal pressure of the separation chamber 16, and the solids and heavy liquid in the rotary drum 1 are discharged to the outside through the discharge holes 10. By the action of the timer after the discharge, the supply of the valve-opening operation water is stopped, the operation water in the sub-valve 7 is all discharged from the drain hole 25, and the sub-valve 7 slides outward and closes radially by centrifugal force. At the same time, since the valve-closing operating water is always supplied to the main valve water chamber 11, the main valve 5 is pushed up by the water pressure and comes into contact with the packing mounted on the lower end of the rotating body lid 2, and the discharge hole 10 is closed. The discharge of heavy liquid in the rotating drum stops.

【0018】ここで圧力検出器14は慣用される通常の
ものでよく、例えば長円形断面を有する円弧状の管に、
内圧が働くと管が変形することを検出するブルドン型等
が特に適している。図1に示すように、軽液インペラー
8から流出する軽液は、そのまま図示はされないサービ
スタンク又はサンプタンクへ流入する。
Here, the pressure detector 14 may be a conventional one, for example, an arc tube having an oval cross section.
A Bourdon type or the like which detects that the tube is deformed when an internal pressure is applied is particularly suitable. As shown in FIG. 1, the light liquid flowing out of the light liquid impeller 8 directly flows into a service tank or a sump tank (not shown).

【0019】なお、上記実施例において、圧力検出器の
代わりに、減圧弁で減圧した0.1 kg/cm2 程度の空気を
重液チャンバーの軽液液面にノズルで吹きつけ、そのノ
ズルに圧力スイッチを付設する手段を採ることもでき
る。そうすると、軽液自由液面が内向き半径方向へ移動
してノズル先端に達すると、上記減圧空気の流出が液面
により阻止されるので、その圧力が若干上昇する。そこ
で、この圧力上昇を圧力計で検出することにより、重液
の堆積を検知することができる。
In the above embodiment, instead of the pressure detector, about 0.1 kg / cm 2 of air depressurized by a pressure reducing valve is blown to the light liquid surface of the heavy liquid chamber by a nozzle, and a pressure switch is applied to the nozzle. Means for attaching a key may be employed. Then, when the light liquid free liquid level moves inward in the radial direction and reaches the nozzle tip, the outflow of the decompressed air is prevented by the liquid level, so that the pressure slightly increases. Therefore, by detecting this pressure rise with a pressure gauge, the accumulation of heavy liquid can be detected.

【0020】[0020]

【発明の効果】以上説明した構成と作用を有する本発明
によれば、高価な静電容量型水分検出器の代わりに、比
較的低価格の装置でもって、分離板型遠心分離機内部に
堆積する重液の界面を感知することができるので、遠心
分離機を効率よく運転できるとともに、分離精製した軽
液(油)の品位を一定にできる効果が得られる。
According to the present invention having the above-described structure and operation, instead of using an expensive capacitance-type moisture detector, a relatively low-priced device is used to accumulate in a separator centrifuge. Since the interface of the heavy liquid is detected, the centrifuge can be operated efficiently, and the effect of keeping the quality of the separated and purified light liquid (oil) constant can be obtained.

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

【図1】本発明の実施例を示す全体縦断面図。FIG. 1 is an overall vertical sectional view showing an embodiment of the present invention.

【図2】本発明の原理図。FIG. 2 is a principle view of the present invention.

【符号の説明】[Explanation of symbols]

1;回転胴、2;回転体蓋、3;軽液チャンバー、4;
分離板、5;主弁、6;案内筒、7;副弁、8;軽液イ
ンペラー、9;原液供給管、10;排出孔、11;主弁
水室、13;軽液流路、14;圧力検出器、15;制御
器、16;分離室、17;仕切板、18;重液流路、1
9;重液インペラー、20;重液チャンバー、22;重
液室、23;制御弁、25;ドレン孔、D0 ;軽液自由
表面径、D1 ;仕切板径、D2 ;境界面径、D3 ;重液
インペラー径、D4 ,D5 ;重液チャンバー内軽液自由
表面径。
1; rotating body, 2; rotating body lid, 3; light liquid chamber, 4;
Separating plate, 5; main valve, 6; guide cylinder, 7; sub-valve, 8; light liquid impeller, 9; raw liquid supply pipe, 10; discharge hole, 11; main valve water chamber, 13; light liquid flow path, 14 A pressure detector, 15; a controller, 16; a separation chamber, 17; a partition plate, 18;
9; heavy liquid impeller, 20; heavy liquid chamber, 22; heavy liquid chamber, 23; control valve, 25; drain hole, D 0 : light liquid free surface diameter, D 1 : partition plate diameter, D 2 : boundary surface diameter , D 3 : heavy liquid impeller diameter, D 4 , D 5 : light liquid free surface diameter in heavy liquid chamber.

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】回転胴内に設けられたスラッジ排出用主弁
と、軽液排出流路に設けられた軽液インペラーと、重液
排出流路に設けられた重液インペラーとを有する分離板
型遠心分離機において、出口端が閉塞された重液インペ
ラーに付設され同重液インペラーの内部圧を検出する圧
力検出器と、上記圧力検出器の出力に応動して主弁開閉
用作動水の制御弁を開閉する制御器とを具えるととも
に、その重液インペラー径を軽液自由表面径より大きく
したことを特徴とする分離板型遠心分離機。
1. A separation plate having a main valve for discharging sludge provided in a rotary drum, a light liquid impeller provided in a light liquid discharge channel, and a heavy liquid impeller provided in a heavy liquid discharge channel. In a centrifugal separator, a pressure detector attached to the heavy liquid impeller whose outlet end is closed and detecting the internal pressure of the heavy liquid impeller, and a hydraulic valve for opening and closing the main valve in response to the output of the pressure detector A separation plate type centrifuge comprising a controller for opening and closing a control valve and having a heavy liquid impeller diameter larger than a light liquid free surface diameter.
JP10199194A 1994-04-15 1994-04-15 Separator centrifuge Expired - Fee Related JP2727411B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10199194A JP2727411B2 (en) 1994-04-15 1994-04-15 Separator centrifuge

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10199194A JP2727411B2 (en) 1994-04-15 1994-04-15 Separator centrifuge

Publications (2)

Publication Number Publication Date
JPH07284693A JPH07284693A (en) 1995-10-31
JP2727411B2 true JP2727411B2 (en) 1998-03-11

Family

ID=14315308

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10199194A Expired - Fee Related JP2727411B2 (en) 1994-04-15 1994-04-15 Separator centrifuge

Country Status (1)

Country Link
JP (1) JP2727411B2 (en)

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
SE528387C2 (en) * 2005-03-08 2006-10-31 Alfa Laval Corp Ab Centrifugal separator and method for separating a product into at least a relatively heavy phase and a relatively light phase
SE529562C2 (en) * 2006-02-13 2007-09-18 Alfa Laval Corp Ab Ways of monitoring centrifugal separator
CN100434185C (en) * 2006-09-07 2008-11-19 宋蜀江 Centrifugal machine
JP4794647B2 (en) * 2009-04-17 2011-10-19 定男 篠原 Separator plate centrifuge, its separator plate and solid-liquid separation method
JP4921521B2 (en) * 2009-05-29 2012-04-25 定男 篠原 Separation plate manufacturing method for separation plate type centrifuge
DK2366457T3 (en) * 2010-03-19 2013-06-10 Alfa Laval Corp Ab DEVICE AND PROCEDURE FOR MONITORING AND ADJUSTING A RADIAL POSITION OF A INTERFACE LAYER IN A CENTRIFUGE

Also Published As

Publication number Publication date
JPH07284693A (en) 1995-10-31

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