JP2020058986A - Centrifugal separator - Google Patents

Centrifugal separator Download PDF

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JP2020058986A
JP2020058986A JP2018192615A JP2018192615A JP2020058986A JP 2020058986 A JP2020058986 A JP 2020058986A JP 2018192615 A JP2018192615 A JP 2018192615A JP 2018192615 A JP2018192615 A JP 2018192615A JP 2020058986 A JP2020058986 A JP 2020058986A
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cleaning liquid
discharge port
centrifugal separator
liquid storage
continuous discharge
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JP7199901B2 (en
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裕二 佐野
Yuji Sano
裕二 佐野
尚史 桶谷
Hisafumi Oketani
尚史 桶谷
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Mitsubishi Kakoki Kaisha Ltd
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Abstract

To provide a centrifugal separator configured so that a nozzle and the like is prevented from clogging.SOLUTION: A centrifugal separator comprises: a rotary container 103; an intermittent discharge port 112a and a continuous discharge port 211 which discharge separated solid components intermittently or continuously; and a washing liquid storage part 201a which stores washing liquid 203 outside the rotary container 103 and to which the continuous discharge port 211 opens. In an inner opening part 213, communicated with the continuous discharge port 211, which opens to inside of the rotary container 103, a distance from a rotation center is longer than the liquid level of the washing liquid 203 which is stored in the washing liquid storage part 201a when contents in a rotating body are totally discharged so that total volumes of the contents are discharged through the intermittent discharge port 112a.SELECTED DRAWING: Figure 1

Description

本発明は、被処理液体中に含まれる固形成分を分離する遠心分離装置に関するものである。   The present invention relates to a centrifugal separator that separates solid components contained in a liquid to be treated.

遠心分離装置には、分離された固形成分を排出する機構が設けられている。そのような機構としては、例えば、固形成分を間欠的に纏めて排出するものや、比較的小さなノズル等から連続的に排出するものなどがある。また、これらの排出機構を併せ持つ分離板型遠心分離機も知られている(例えば、特許文献1参照。)。   The centrifugal separator is provided with a mechanism for discharging the separated solid component. Examples of such a mechanism include a mechanism for intermittently discharging solid components and a mechanism for continuously discharging solid components from a relatively small nozzle or the like. A separation plate type centrifuge having both of these discharge mechanisms is also known (for example, refer to Patent Document 1).

特開2001−239184号公報JP 2001-239184 A

しかしながら、上記のような固形成分を比較的小さなノズル等から連続的に排出する排出機構は、ノズル等が詰まりがちであり、詰まった場合には、装置を分解清掃等する作業が必要になる。   However, in the discharge mechanism for continuously discharging the solid component from the relatively small nozzle or the like as described above, the nozzle or the like is apt to be clogged, and when clogged, it is necessary to disassemble and clean the device.

本発明は、上記の点に鑑み、遠心分離装置において、被処理液体から分離された固形成分を連続的に排出するノズル等の閉塞防止を目的としている。   In view of the above points, the present invention has an object to prevent clogging of a nozzle or the like that continuously discharges a solid component separated from a liquid to be treated in a centrifugal separator.

上記の目的を達成するため、本発明は、
回転容器と、上記回転容器の内部に所定の間隔を空けて積層された複数の分離板とを有し、被処理液体に含まれる固形成分を遠心力により分離して排出する遠心分離装置であって、
上記回転容器の内側外周部に堆積された固形成分を間欠的に排出する間欠排出口と、
上記回転容器の内側外周部に開口する内側開口部に連通し、上記回転容器の内側外周部に堆積される固形成分を連続的に排出する連続排出口と、
上記回転容器の外側に設けられて洗浄液を貯留するとともに、内部に上記連続排出口が開口する洗浄液貯留部と、
を有し、
上記内側開口部は、上記回転容器の回転中心からの距離が、上記間欠排出口から固形成分が排出される時の上記洗浄液貯留部に貯留されている洗浄液の液面における上記回転中心からの距離よりも長い位置に設けられていることを特徴とする。
In order to achieve the above object, the present invention provides
A centrifugal separator having a rotating container and a plurality of separation plates laminated at predetermined intervals inside the rotating container, for separating and discharging solid components contained in the liquid to be treated by centrifugal force. hand,
An intermittent discharge port for intermittently discharging the solid component accumulated on the inner peripheral portion of the rotating container,
A continuous discharge port that communicates with an inner opening portion that opens to the inner outer peripheral portion of the rotating container and continuously discharges solid components accumulated on the inner outer peripheral portion of the rotating container,
A cleaning liquid storage unit provided outside the rotary container to store the cleaning liquid, and the continuous discharge port opening inside,
Have
The inner opening has a distance from the rotation center of the rotation container in the liquid level of the cleaning liquid stored in the cleaning liquid storage unit when the solid component is discharged from the intermittent discharge port. It is characterized in that it is provided at a position longer than that.

これにより、間欠排出口から回転体内の内容物を全量排出するトータル排出時に、上記洗浄液貯留部に貯留されている洗浄液が、上記連続排出口から上記内側開口部に流れる圧力が作用し、上記連続排出口等が洗浄される。   As a result, at the time of total discharge in which the entire amount of the content in the rotating body is discharged from the intermittent discharge port, the pressure of the cleaning liquid stored in the cleaning liquid storage section from the continuous discharge port to the inner opening acts, and The outlet etc. are cleaned.

本発明によれば、遠心分離装置において、被処理液体から分離された固形成分を連続的に排出するノズル等の閉塞防止ができる。   According to the present invention, in a centrifugal separator, it is possible to prevent clogging of a nozzle or the like that continuously discharges a solid component separated from a liquid to be treated.

遠心分離装置の正面断面図である。It is a front sectional view of a centrifuge. 固形成分を排出する動作の例を示すタイミングチャートである。6 is a timing chart showing an example of an operation of discharging a solid component. 固形成分が連続的に排出される状態の例を模式的に示す説明図である。It is explanatory drawing which shows typically the example of the state which a solid component is discharged continuously. 回転体内の内容物を全量排出するトータル排出時の例を模式的に示す説明図である。It is explanatory drawing which shows typically the example at the time of the total discharge which discharges all the contents in a rotary body.

以下、本発明の実施形態として、例えば船舶用ディーゼルエンジン機関の燃料油および潤滑油等の被処理流体である原液の清浄化に用いられる分離板型遠心分離機である遠心分離装置について説明する。この分離板型遠心分離機は、回転体内に截頭円錐形状の薄板からなる分離板を案内筒の軸方向に沿って小間隙を有して多数積層して装着した竪型の遠心分離機であって、回転体内で分離・堆積されるスラッジを弁シリンダの開閉によって外部に排出する機構を有している。上記スラッジは、被処理液体に含まれる固形物等であって、より詳しくは、遠心力で回転体内の最外径部側に分離・堆積される固形分である。   Hereinafter, as an embodiment of the present invention, a centrifuge which is a separation plate type centrifuge used for cleaning a stock solution which is a fluid to be processed such as fuel oil and lubricating oil of a marine diesel engine will be described. This separation plate type centrifuge is a vertical type centrifuge in which a large number of separation plates made of frustoconical thin plates are stacked in the rotating body along the axial direction of the guide cylinder with a small gap. Therefore, it has a mechanism for discharging sludge separated and accumulated in the rotating body to the outside by opening and closing the valve cylinder. The sludge is a solid matter or the like contained in the liquid to be treated, and more specifically, a solid content separated and accumulated on the outermost diameter side of the rotor by centrifugal force.

(分離板型遠心分離機101の概略構成)
分離板型遠心分離機101は、図1に示すように、
回転軸102に取り付けられて高速回転する回転容器103と、
上記回転容器103の中心部上部に設けられ、原液が外部から供給される液入口管104と、
上記原液を回転容器103内の最下部に向けて末広がりに導く案内筒105と、
上記原液におけるスラッジ等の各成分を比重差により分離するために、上記案内筒105の軸方向に小間隙を有して多数積層されて装着された分離板113、および水取板152を有する分離領域と回転容器103内の最外径部(内側外周部)のスラッジ堆積領域とから形成される分離室151と、
上記回転容器103内の下部に設けられ、作動水の水圧に応じて上下動制御され、スラッジを堆積させる時に上昇して(図1の左半分)外周部上縁が弁パッキン107に圧接されて間欠排出部112の間欠排出口112aを閉じる一方、スラッジを排出する時に下降して(図1の右半分)間欠排出口112aを開く弁シリンダ106と、
上記分離室151で分離されたスラッジをそれぞれ連続排出口211を介して連続して外部へ排出する複数の連続排出部201と、
上記分離室151で分離された清浄油(軽液)等を外部に排出するための液抜き出し部154・156と、
を備えている。
(Schematic configuration of separation plate type centrifugal separator 101)
The separation plate type centrifuge 101, as shown in FIG.
A rotating container 103 attached to the rotating shaft 102 and rotating at high speed;
A liquid inlet pipe 104, which is provided in the upper part of the central portion of the rotary container 103 and to which the undiluted liquid is supplied from the outside,
A guide tube 105 that guides the above-mentioned undiluted solution toward the bottom of the rotary container 103 toward the bottom,
In order to separate each component such as sludge in the undiluted solution by the difference in specific gravity, a separation plate 113 and a water removal plate 152, which are mounted by stacking a large number with a small gap in the axial direction of the guide cylinder 105, are installed. A separation chamber 151 formed from a region and a sludge accumulation region of the outermost diameter portion (inner outer peripheral portion) in the rotary container 103;
It is provided in the lower part of the rotary container 103 and is controlled to move up and down according to the hydraulic pressure of the working water, and rises when sludge is accumulated (the left half of FIG. 1) and the upper edge of the outer peripheral portion is pressed against the valve packing 107. A valve cylinder 106 that closes the intermittent discharge port 112a of the intermittent discharge part 112 while lowering when discharging sludge (right half of FIG. 1) to open the intermittent discharge port 112a.
A plurality of continuous discharge units 201 for continuously discharging the sludge separated in the separation chamber 151 to the outside through continuous discharge ports 211,
Liquid withdrawing parts 154 and 156 for discharging the clean oil (light liquid) or the like separated in the separation chamber 151 to the outside,
It has.

上記回転容器103は、上部に設けられた略截頭円錐台形部である回転体蓋103aと、下部に設けられた上記截頭円錐台形部の外径よりも大きな内径を有する大径円柱部である回転胴103bとが、リングナット103cによって一体化した形状をしている。回転容器103は回転軸102と一体化されて高速回転(例えば7000〜9000min-1)できるように固定されている。   The rotary container 103 is composed of a rotary body lid 103a, which is a substantially truncated cone-shaped portion provided at an upper portion, and a large-diameter cylindrical portion having an inner diameter larger than the outer diameter of the truncated truncated cone portion provided at a lower portion. A certain rotating drum 103b is integrated with a ring nut 103c. The rotary container 103 is integrated with the rotary shaft 102 and is fixed so as to rotate at high speed (for example, 7,000 to 9000 min −1).

上記のような分離板型遠心分離機101の分離室151内に導入された原液は、分離板113間の間隙を上昇して流れていくうちに比重の大きい固形分はスラッジ堆積領域へ、油(軽液)は回転容器103の中心側へと分離され、分離水は回転容器103の上部に設けられた液抜き出し部156より排出される。   The undiluted solution introduced into the separation chamber 151 of the separation plate type centrifugal separator 101 as described above rises in the gap between the separation plates 113 and flows, while the solid content having a large specific gravity is transferred to the sludge accumulation region to the oil accumulation area. The (light liquid) is separated toward the center of the rotary container 103, and the separated water is discharged from the liquid extraction unit 156 provided on the upper part of the rotary container 103.

上記スラッジ堆積領域に堆積したスラッジは、間欠排出部112から間欠的に排出させることもできるし、連続排出部201から連続的に排出させることもできる。   The sludge accumulated in the sludge accumulation region can be discharged intermittently from the intermittent discharge part 112 or continuously discharged from the continuous discharge part 201.

すなわち、上記間欠的な排出は、例えば原液の処理量や、そのスラッジの含有量から、回転容器103内に堆積したスラッジの堆積量が所定量になる時間が推定され、タイマー等により制御される所定のタイミングで、開閉弁作動水供給部材111の閉弁作動水供給ノズル121または開弁作動水供給ノズル131から開閉弁作動水受部材110に閉弁作動水または開弁作動水が供給されて行われる。より詳しくは、閉弁作動水供給ノズル121から閉弁作動水が供給されると、その閉弁作動水は閉弁作動水供給路122を介して閉弁作動水圧室123に導入され、遠心力によって外周側に押し付けられることによって生じる圧力により弁シリンダ106が上昇して弁パッキン107に圧接され、間欠排出口112aが閉じられる。また、開弁作動水供給ノズル131から開弁作動水が供給されると、その開弁作動水は開弁作動水供給路132を介して弁体133を遠心力に抗して内周側にスライドさせ、閉弁作動水圧室123内の閉弁作動水を開弁作動水排水流路134から開弁作動水排出孔135を介して放出させることにより弁シリンダ106が下降して間欠排出口112aを開き、スラッジの排出が行われる。その後、直ちに開弁作動水の供給は停止され、再び閉弁作動水が閉弁作動水圧室123に供給されると、弁シリンダ106は上方に押し上げられ、間欠排出口112aがシールされる。   That is, the intermittent discharge is estimated from the amount of the undiluted solution treated and the sludge content, for example, and the time when the accumulated amount of sludge accumulated in the rotary container 103 reaches a predetermined amount is controlled by a timer or the like. At a predetermined timing, the valve closing water or valve opening water is supplied from the valve closing water supply nozzle 121 or the valve opening water supply nozzle 131 of the valve opening / closing water supply member 111 to the valve opening / closing valve water receiving member 110. Done. More specifically, when the valve-closing working water is supplied from the valve-closing working water supply nozzle 121, the valve-closing working water is introduced into the valve-closing working water pressure chamber 123 via the valve-closing working water supply passage 122 and centrifugal force is applied. The pressure generated by being pressed to the outer peripheral side of the valve cylinder 106 causes the valve cylinder 106 to rise and come into pressure contact with the valve packing 107, thereby closing the intermittent discharge port 112a. Further, when the valve-opening water is supplied from the valve-opening water supply nozzle 131, the valve-opening water flows through the valve-opening water supply passage 132 to the valve body 133 against the centrifugal force to the inner peripheral side. By sliding the valve closing hydraulic water in the valve operating hydraulic pressure chamber 123 from the valve operating water drainage channel 134 through the valve operating water discharge hole 135, the valve cylinder 106 descends and the intermittent discharge port 112a. Open and sludge is discharged. Immediately thereafter, the supply of the valve-opening working water is stopped, and when the valve-closing working water is supplied again to the valve-closing working water pressure chamber 123, the valve cylinder 106 is pushed upward, and the intermittent discharge port 112a is sealed.

また、上記連続的な排出は、所定の内径に設定されたノズルとして作用する連続排出口211が、回転体蓋103aに形成された連続排出流路212を介して、回転体蓋103aの内面に開口する内側開口部213に連通することによって、回転容器103の回転による遠心力によって、スラッジ堆積領域に堆積するスラッジが、徐々に、連続的に排出されるようになっている。   Further, in the above continuous discharge, the continuous discharge port 211 acting as a nozzle set to a predetermined inner diameter is provided on the inner surface of the rotor lid 103a via the continuous discharge flow passage 212 formed in the rotor lid 103a. By communicating with the inner opening 213 that opens, the sludge accumulated in the sludge accumulation region is gradually and continuously discharged by the centrifugal force generated by the rotation of the rotary container 103.

(連続排出口211の洗浄について)
回転体蓋103aの外側には、連続排出口211を囲むように洗浄液貯留部201aが設けられ、連続排出口211や連続排出流路212を洗浄する例えば清浄な水等の洗浄液203が、貯留されるようになっている。より具体的には、例えば洗浄液受部201bがリングナット103cにボルト202によって取り付けられ、回転体蓋103aの外壁と洗浄液受部201bとで囲まれる空間に、洗浄液203が貯留されるようになっている。上記洗浄液203は、例えば、回転容器103の外方に設けられた支持板221に取り付けられた給水管222(洗浄液供給部)により給水バルブ223を介して供給されるようになっている。上記洗浄液受部201bには、回転容器103の外周側に向けて開口する排出孔201cが設けられ、洗浄液貯留部201aの内部に連続排出口211から排出されたスラッジが徐々に外方側に流れ出し得るようになっている。また、上記洗浄液貯留部201aに貯留される洗浄液203の液面の位置は、前記のように間欠排出口112aから回転体内の内容物を全量排出するトータル排出される時において、上記内側開口部213よりも回転容器103の回転中心に近い位置になるように設定されている。
(About cleaning of continuous discharge port 211)
A cleaning liquid storage portion 201a is provided outside the rotary body lid 103a so as to surround the continuous discharge port 211, and a cleaning liquid 203 such as clean water for cleaning the continuous discharge port 211 and the continuous discharge flow path 212 is stored therein. It has become so. More specifically, for example, the cleaning liquid receiving portion 201b is attached to the ring nut 103c by a bolt 202, and the cleaning liquid 203 is stored in a space surrounded by the outer wall of the rotor lid 103a and the cleaning liquid receiving portion 201b. There is. The cleaning liquid 203 is supplied, for example, via a water supply valve 223 by a water supply pipe 222 (cleaning liquid supply unit) attached to a support plate 221 provided outside the rotary container 103. The cleaning liquid receiving portion 201b is provided with a discharge hole 201c opening toward the outer peripheral side of the rotary container 103, and the sludge discharged from the continuous discharge port 211 gradually flows to the outer side inside the cleaning liquid storage portion 201a. I'm supposed to get it. In addition, the position of the liquid surface of the cleaning liquid 203 stored in the cleaning liquid storage portion 201a is the inner opening 213 when the total amount of the content in the rotating body is completely discharged from the intermittent discharge port 112a as described above. It is set so as to be closer to the rotation center of the rotary container 103.

上記のように設定されていることによって、例えば以下のようにして連続排出口211の洗浄が行われる。   With the above settings, the continuous discharge port 211 is cleaned as follows, for example.

まず、例えば、回転容器103が所定の回転速度で回転している状態で、図2に示すように閉弁作動水が供給されると間欠排出部112の間欠排出口112aが閉じて、内部のスラッジ堆積領域にスラッジが堆積する。堆積したスラッジのうちの一部は、内側開口部213から連続排出流路212を介して連続排出口211から排出され、さらに排出孔201cから回転容器103の外方側に流れ出す。すなわち、遠心力によって各部に作用する圧力の関係を図3に示すように水頭圧を模して表すと、例えば間欠排出部112における水頭圧をHとした場合、連続排出口211には水頭圧h1(または洗浄液貯留部201aに、排出孔201cから排出され切らないスラッジが貯留されている場合には、その液面の位置に応じた水頭圧h2)が作用する。そこで、上記水頭圧に応じて、回転容器103内のスラッジが連続排出口211から排出される。   First, for example, when the rotary container 103 is rotating at a predetermined rotation speed and the valve-closing working water is supplied as shown in FIG. 2, the intermittent discharge port 112a of the intermittent discharge part 112 is closed, and Sludge accumulates in the sludge accumulation area. Part of the accumulated sludge is discharged from the continuous discharge port 211 from the inner opening 213 through the continuous discharge flow path 212, and further flows out from the discharge hole 201c to the outside of the rotary container 103. That is, when the relationship between the pressures exerted on the respective parts by the centrifugal force is represented by imitating the hydrohead pressure as shown in FIG. 3, for example, when the hydrohead pressure in the intermittent discharge part 112 is H, the hydrohead pressure is applied to the continuous discharge port 211. h1 (or a head pressure h2 corresponding to the position of the liquid surface when sludge that is not completely discharged from the discharge hole 201c is stored in the cleaning liquid storage unit 201a) acts. Therefore, the sludge in the rotary container 103 is discharged from the continuous discharge port 211 according to the head pressure.

やがて、スラッジ堆積領域に所定量のスラッジが堆積することが見込まれるタイミングで間欠排出部112の間欠排出口112aが開放される際には、その開放に所定の時間だけ先立って、給水管222から洗浄液203が供給され、洗浄液貯留部201aに溜められた後に間欠排出口112aが開放される。この場合、回転容器103内の被処理液体が比較的短時間に間欠排出部112から排出されて回転容器103が完全に、またはほぼ空になると、図4に示すように、間欠排出部112における水頭圧Hは0となり、連続排出口211に連通する内側開口部213には、洗浄液203の液面から内側開口部213の位置までの距離に応じた水頭圧h3が作用する。そこで、洗浄液貯留部201aに貯留された洗浄液203は連続排出流路212を逆流し、これによって、連続排出口211、連続排出流路212、および内側開口部213が洗浄される。   Eventually, when the intermittent discharge port 112a of the intermittent discharge part 112 is opened at a timing when a predetermined amount of sludge is expected to be accumulated in the sludge accumulation area, the water supply pipe 222 is opened for a predetermined time before the opening. After the cleaning liquid 203 is supplied and stored in the cleaning liquid storage portion 201a, the intermittent discharge port 112a is opened. In this case, when the liquid to be treated in the rotary container 103 is discharged from the intermittent discharge part 112 in a relatively short time, and the rotary container 103 becomes completely or almost empty, as shown in FIG. The water head pressure H becomes 0, and a water head pressure h3 corresponding to the distance from the liquid surface of the cleaning liquid 203 to the position of the inner opening 213 acts on the inner opening 213 communicating with the continuous discharge port 211. Therefore, the cleaning liquid 203 stored in the cleaning liquid storage portion 201a flows back through the continuous discharge flow path 212, whereby the continuous discharge port 211, the continuous discharge flow path 212, and the inner opening 213 are cleaned.

なお、上記排出孔201cから流れ出し得るスラッジの量は、連続排出口211から排出されるスラッジの量よりも多ければ、給水管222から清浄な洗浄液203が供給されたときに洗浄液受部201bに貯留される洗浄液203のスラッジ濃度を低く抑えやすい点で好ましいが、洗浄液受部201bからスラッジや洗浄液203が溢れたとしても特に差し支えはなく、給水管222から十分な洗浄液203が供給されるなどすれば、以下のような連続排出口211等の洗浄を十分行わせることはできる。また、洗浄液203の清浄程度は相対的なもので、連続排出口211等の洗浄が可能な程度に清浄であればよい。   If the amount of sludge that can flow out from the discharge hole 201c is larger than the amount of sludge discharged from the continuous discharge port 211, it is stored in the cleaning liquid receiving portion 201b when the clean cleaning liquid 203 is supplied from the water supply pipe 222. It is preferable in that the sludge concentration of the cleaning liquid 203 to be kept low can be easily suppressed, but even if the sludge or the cleaning liquid 203 overflows from the cleaning liquid receiving portion 201b, there is no particular problem, and if sufficient cleaning liquid 203 is supplied from the water supply pipe 222, for example. It is possible to sufficiently wash the continuous discharge port 211 and the like as described below. The cleaning liquid 203 is relatively clean, and may be clean enough to clean the continuous discharge port 211 and the like.

(連続排出口211からのスラッジ排出量(排出速度)の調整について)
連続排出口211から排出されるスラッジの量は、回転容器103の回転速度や、被処理液体中の固形成分濃度、連続排出口211のオリフィス径などの他、連続排出口211における水頭圧(図3のh1やh2)によっても変化する。そこで、図1に併せて示すように、回転容器103の回転中心からの距離が異なる複数の位置に連通し得るように連続排出流路212を設け、何れかの位置に選択的に連続排出口211を設けることによって、連続排出口211から排出されるスラッジの量を調整することが容易にできる。それゆえ、連続排出口211のオリフィス径の共通化を図ったり、オリフィス径を過度に小さく設定することなく、排出量を小さく設定するなど、連続排出口より排出されるスラッジの排出流速(量)を簡易的に可変することが容易にできる。
(Regarding adjustment of sludge discharge amount (discharge speed) from continuous discharge port 211)
The amount of sludge discharged from the continuous discharge port 211 includes the rotational speed of the rotary container 103, the concentration of solid components in the liquid to be treated, the orifice diameter of the continuous discharge port 211, and the head pressure at the continuous discharge port 211 (see FIG. It also changes depending on h1 and h2) of 3. Therefore, as also shown in FIG. 1, a continuous discharge passage 212 is provided so as to be able to communicate with a plurality of positions at different distances from the rotation center of the rotary container 103, and a continuous discharge port is selectively provided at any position. By providing 211, the amount of sludge discharged from the continuous discharge port 211 can be easily adjusted. Therefore, the discharge flow rate (amount) of the sludge discharged from the continuous discharge port can be reduced by making the orifice size of the continuous discharge port 211 common or by setting the discharge amount small without setting the orifice size excessively small. Can be easily changed.

ここで、上記のように連続排出口211の位置を種々に設定する場合、それに対応するように洗浄液203の液面の位置を設定するためには、例えば図1に仮想線で示すように、連続排出部201に代えて洗浄液受部201bの長さが異なる連続排出部201’を取り付けたり、支持板221上での取り付け位置が異なる給水管222’を用いるようにしたりしてもよい。また、洗浄液受部201bを伸縮可能にしたり、給水管222をスライド可能にしたりしてもよい。   Here, in the case where the position of the continuous discharge port 211 is set variously as described above, in order to set the position of the liquid surface of the cleaning liquid 203 so as to correspond thereto, for example, as shown by a phantom line in FIG. Instead of the continuous discharge part 201, a continuous discharge part 201 ′ having a different length of the cleaning liquid receiving part 201b may be attached, or a water supply pipe 222 ′ having a different attachment position on the support plate 221 may be used. Further, the cleaning liquid receiving portion 201b may be made expandable and contractable, or the water supply pipe 222 may be made slidable.

(その他の事項)
なお、洗浄液受部201bは、リングナット103cに取り付けるのに限らず、回転体蓋103aや回転胴103bに取り付けられるなどしてもよい。また、リングナット103cや、回転体蓋103a、回転胴103bの2つ以上に取り付け得るようにされてもよい。
(Other matters)
The cleaning liquid receiving portion 201b is not limited to being attached to the ring nut 103c, but may be attached to the rotating body lid 103a or the rotating body 103b. Further, the ring nut 103c, the rotary body lid 103a, and the rotary drum 103b may be attached to two or more.

また、連続排出口211の位置が同一に設定される場合でも、洗浄液受部201bの長さ等を異ならせるなどして、洗浄液203の液面の位置を種々に設定可能にしてもよい。この場合には、図4における水頭圧h3を種々に設定し得ることになるので、これに応じて連続排出口211等の洗浄程度を設定することができる。   Even when the positions of the continuous discharge ports 211 are set to be the same, the position of the liquid surface of the cleaning liquid 203 may be set variously by changing the length of the cleaning liquid receiving portion 201b and the like. In this case, since the head pressure h3 in FIG. 4 can be set variously, the cleaning degree of the continuous discharge port 211 and the like can be set accordingly.

また、洗浄液203の液面の位置を設定するためには、洗浄液受部201bにおける回転容器103の回転中心からの距離が異なる複数の位置に洗浄液203を溢れさせる開口部を設け、それらの開口部を選択的に閉塞させ得るようにしてもよい。   Further, in order to set the position of the liquid surface of the cleaning liquid 203, openings for overflowing the cleaning liquid 203 are provided at a plurality of positions in the cleaning liquid receiving portion 201b at different distances from the rotation center of the rotary container 103, and those openings are provided. May be selectively occluded.

101 分離板型遠心分離機
102 回転軸
103 回転容器
103a 回転体蓋
103b 回転胴
103c リングナット
104 液入口管
105 案内筒
106 弁シリンダ
107 弁パッキン
110 開閉弁作動水受部材
111 開閉弁作動水供給部材
112 間欠排出部
112a 間欠排出口
113 分離板
121 閉弁作動水供給ノズル
122 閉弁作動水供給路
123 閉弁作動水圧室
131 開弁作動水供給ノズル
132 開弁作動水供給路
133 弁体
134 開弁作動水排水流路
135 開弁作動水排出孔
151 分離室
152 水取板
154・156 液抜き出し部
201 連続排出部
201’ 連続排出部
201a 洗浄液貯留部
201b 洗浄液受部
201c 排出孔
202 ボルト
203 洗浄液
211 連続排出口
212 連続排出流路
213 内側開口部
221 支持板
222 給水管
222’ 給水管
223 給水バルブ
101 Separation Plate Centrifuge 102 Rotating Shaft 103 Rotating Container 103a Rotating Body Lid 103b Rotating Body 103c Ring Nut 104 Liquid Inlet Pipe 105 Guide Tube 106 Valve Cylinder 107 Valve Packing 110 Open / Close Valve Operating Water Receiving Member 111 Open / Close Valve Operating Water Supply Member 112 intermittent discharge part 112a intermittent discharge port 113 separation plate 121 valve closing working water supply nozzle 122 closing valve working water supply path 123 valve closing working water pressure chamber 131 opening valve working water supply nozzle 132 opening valve working water supply path 133 valve body 134 opening Valve-operated water drainage channel 135 Valve-operated water discharge hole 151 Separation chamber 152 Water removal plate 154/156 Liquid extraction part 201 Continuous discharge part 201 ′ Continuous discharge part 201a Cleaning liquid storage part 201b Cleaning liquid receiving part 201c Discharge hole 202 Bolt 203 Cleaning liquid 211 Continuous discharge port 212 Continuous discharge flow path 13 inner opening 221 supporting plate 222 water supply tube 222 'the water supply pipe 223 water supply valve

Claims (6)

回転容器と、上記回転容器の内部に所定の間隔を空けて積層された複数の分離板とを有し、被処理液体に含まれる固形成分を遠心力により分離して排出する遠心分離装置であって、
上記回転容器の内側外周部に堆積された固形成分を間欠的に排出する間欠排出口と、
上記回転容器の内側外周部に開口する内側開口部に連通し、上記回転容器の内側外周部に堆積される固形成分を連続的に排出する連続排出口と、
上記回転容器の外側に設けられて洗浄液を貯留するとともに、内部に上記連続排出口が開口する洗浄液貯留部と、
を有し、
上記内側開口部は、上記回転容器の回転中心からの距離が、上記間欠排出口から固形成分が排出される時の上記洗浄液貯留部に貯留されている洗浄液の液面における上記回転中心からの距離よりも長い位置に設けられていることを特徴とする遠心分離装置。
A centrifugal separator that has a rotary container and a plurality of separation plates that are stacked inside the rotary container with a predetermined space therebetween, and that separates solid components contained in the liquid to be treated by centrifugal force and discharges the liquid. hand,
An intermittent discharge port for intermittently discharging the solid component accumulated on the inner peripheral portion of the rotating container,
A continuous discharge port that communicates with an inner opening portion that opens to the inner outer peripheral portion of the rotating container and continuously discharges solid components accumulated on the inner outer peripheral portion of the rotating container,
A cleaning liquid storage unit provided outside the rotary container to store the cleaning liquid, and the continuous discharge port opening inside,
Have
The inner opening has a distance from the center of rotation of the rotary container, and a distance from the center of rotation of the liquid level of the cleaning liquid stored in the cleaning liquid storage unit when the solid component is discharged from the intermittent discharge port. A centrifugal separator characterized in that it is provided at a position longer than that.
請求項1の遠心分離装置であって、
さらに、上記洗浄液貯留部に洗浄液を供給する洗浄液供給部を備えたことを特徴とする遠心分離装置。
The centrifugal separator according to claim 1, wherein
Furthermore, the centrifugal separation apparatus provided with the cleaning liquid supply part which supplies a cleaning liquid to the said cleaning liquid storage part.
請求項2の遠心分離装置であって、
上記間欠排出口から回転体内の内容物を全量排出するトータル排出されるのに先立って、上記洗浄液供給部によって上記洗浄液が上記洗浄液貯留部に貯留されることを特徴とする遠心分離装置。
The centrifugal separator according to claim 2, wherein
A centrifugal separator, wherein the cleaning liquid is stored in the cleaning liquid storage unit by the cleaning liquid supply unit before the total amount of the contents in the rotor is completely discharged from the intermittent discharge port.
請求項1から請求項3のうち何れか1項の遠心分離装置であって、
上記洗浄液貯留部には、上記連続排出口から上記洗浄液貯留部に排出される固形成分を上記洗浄液貯留部の外部に排出する排出孔が設けられていることを特徴とする遠心分離装置。
The centrifugal separator according to any one of claims 1 to 3,
The centrifugal separator, wherein the cleaning liquid storage part is provided with a discharge hole for discharging the solid component discharged from the continuous discharge port to the cleaning liquid storage part to the outside of the cleaning liquid storage part.
請求項1から請求項4のうち何れか1項の遠心分離装置であって、
上記洗浄液貯留部に貯留される洗浄液の液面の位置を可変に設定可能にされていることを特徴とする遠心分離装置。
The centrifugal separator according to any one of claims 1 to 4,
A centrifugal separator, wherein the position of the liquid surface of the cleaning liquid stored in the cleaning liquid storage section can be variably set.
請求項1から請求項5のうち何れか1項の遠心分離装置であって、
上記連続排出口における、上記回転容器の回転中心からの距離が可変に構成されていることを特徴とする遠心分離装置。
The centrifugal separator according to any one of claims 1 to 5,
The centrifugal separator, wherein the distance from the center of rotation of the rotary container at the continuous discharge port is variable.
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Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2557629A (en) * 1946-02-21 1951-06-19 Alais & Froges & Camarque Cie Method and apparatus for continuous centrifugal separation
JPS60104255U (en) * 1983-12-20 1985-07-16 三菱化工機株式会社 Cleaning device for separation plate centrifuge
JPH01224062A (en) * 1988-01-27 1989-09-07 Westfalia Separator Ag Centrifugal separator for separating liquid mixture
JP2001239184A (en) * 2000-02-29 2001-09-04 Mitsubishi Kakoki Kaisha Ltd Separation plate type centrifugal separator
US20070117706A1 (en) * 2003-12-11 2007-05-24 Alfa Laval Corporate Ab Centrifugal separator

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2557629A (en) * 1946-02-21 1951-06-19 Alais & Froges & Camarque Cie Method and apparatus for continuous centrifugal separation
JPS60104255U (en) * 1983-12-20 1985-07-16 三菱化工機株式会社 Cleaning device for separation plate centrifuge
JPH01224062A (en) * 1988-01-27 1989-09-07 Westfalia Separator Ag Centrifugal separator for separating liquid mixture
JP2001239184A (en) * 2000-02-29 2001-09-04 Mitsubishi Kakoki Kaisha Ltd Separation plate type centrifugal separator
US20070117706A1 (en) * 2003-12-11 2007-05-24 Alfa Laval Corporate Ab Centrifugal separator
JP2007513756A (en) * 2003-12-11 2007-05-31 アルファ ラヴァル コーポレイト アクチボラゲット centrifuge

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