JPH0531404A - Suction type liquid-solid separator - Google Patents

Suction type liquid-solid separator

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Publication number
JPH0531404A
JPH0531404A JP21261491A JP21261491A JPH0531404A JP H0531404 A JPH0531404 A JP H0531404A JP 21261491 A JP21261491 A JP 21261491A JP 21261491 A JP21261491 A JP 21261491A JP H0531404 A JPH0531404 A JP H0531404A
Authority
JP
Japan
Prior art keywords
solid
valve
liquid
pump
storage tank
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.)
Granted
Application number
JP21261491A
Other languages
Japanese (ja)
Other versions
JP3127008B2 (en
Inventor
Kenji Ishimaru
健二 石丸
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.)
NIPPON RABARU KK
Original Assignee
NIPPON RABARU KK
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 NIPPON RABARU KK filed Critical NIPPON RABARU KK
Priority to JP03212614A priority Critical patent/JP3127008B2/en
Publication of JPH0531404A publication Critical patent/JPH0531404A/en
Application granted granted Critical
Publication of JP3127008B2 publication Critical patent/JP3127008B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

PURPOSE:To prevent abrasion of a pump without impairing the original performance of a centrifugal force type liquid-solid separator by providing this liquid- solid separator to the suction side of a pump. CONSTITUTION:The suction side of a pump 40 is connected to the outflow side of a liquid-solid separator 10. The discharge side of solid material in the liquid-solid separator is connected to the upper part of a storage tank 42 via a valve V1. The storage tank is provided with both a lower discharge port 48 having a valve V2 and an air vent pipe 50 having a valve 4. The interval between the discharge side of the pump and the storage tank is connected by a branched pipe 54 having a valve V3. The respective valves are controlled by a valve controlling device 56. While a suction type liquid-solid separator is ordinarily operated, the valve V1 is opened and the valves V2-V4 are closed. The valve V1 is closed and the valves V2-V4 are opened at a time for mode for discharging the stored material.

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、ポンプの吸引側に遠心
力を利用した固液分離機を組み合わせたサクション型固
液分離装置に関するものである。更に詳しく述べると、
それらポンプ及び固液分離機に、固形物排出用の貯留槽
と分岐管及び複数の弁を組み合わせることにより、固液
分離機の性能維持とポンプ保護の両方の効果をもたせる
ようにしたサクション方式の固液分離システムに関する
ものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a suction type solid-liquid separation device in which a suction-side pump is combined with a solid-liquid separator utilizing centrifugal force. More specifically,
By combining these pumps and solid-liquid separators with a storage tank for discharging solids, a branch pipe, and multiple valves, a suction-type suction system is designed to have the effects of both maintaining the performance of the solid-liquid separators and protecting the pumps. The present invention relates to a solid-liquid separation system.

【0002】[0002]

【従来の技術】遠心力を利用した固液分離機自体は従来
公知であり、サイクロン方式など幾つかの形式がある。
なかでも現在、液体中に含まれている固形粒子などを分
離する優れた性能をもつ代表的な装置として、図3に示
すような固液分離機がある。この固液分離機10は、分
離筒12の上部と下部にそれぞれ外側バレル14,16
を設け、上部の外側バレル14の側面に流入口18を、
また分離筒12内の上方から外側バレル14の上面を貫
通して流出管20を配置して流出口21を設け、下部の
外側バレル16の下方に固形物排出口22を設けた外観
構造である。
2. Description of the Related Art A solid-liquid separator using centrifugal force has been publicly known, and there are several types such as a cyclone type.
Among them, there is a solid-liquid separator as shown in FIG. 3 as a typical device having excellent performance for separating solid particles contained in a liquid. This solid-liquid separator 10 includes outer barrels 14 and 16 at the upper and lower portions of a separation cylinder 12, respectively.
And an inlet port 18 on the side surface of the upper outer barrel 14,
Further, it is an external structure in which the outflow pipe 20 is arranged by penetrating the upper surface of the outer barrel 14 from above in the separation cylinder 12 to provide an outflow port 21, and a solid matter discharge port 22 is provided below the lower outer barrel 16. .

【0003】この固液分離機の内部構造並びに作動原理
は次の通りである。 液体と固形物(固形粒子など)は、流入口18から接
線方向で上部チャンバー24内に流入し渦流状になる。 その液体と固形物は、接線方向に設けられたスリット
状の特殊回転機構26を通過することによって加速され
分離筒12の内側へ勢いよく流れ込む。 液体より重い固形物は、遠心力により分離筒12の内
壁に当たり、固形物と液体との分離(1次分離)が始ま
る。 固形物は、分離筒12の内壁に沿ってゆっくりと沈降
していき、下部チャンバー28に溜まる。 回転渦となって下降してきた液体は、下部案内羽根機
構30によって瞬間的に急減速され、速度エネルギーが
圧力エネルギーに変わり、更に固液分離(2次分離)が
行われる。 固形物を含まない液体は中心の渦(負圧地帯)によっ
て急上昇し、流出管20を通り、流出口21から外部へ
流出する。 下部チャンバー28に堆積した固形物は、必要に応じ
て定期的に、あるいは連続的に固形物排出口22から排
出する。
The internal structure and operating principle of this solid-liquid separator are as follows. Liquid and solid matter (solid particles and the like) flow into the upper chamber 24 in a tangential direction from the inflow port 18 to form a vortex. The liquid and solid matter are accelerated by passing through the slit-shaped special rotation mechanism 26 provided in the tangential direction, and are vigorously flown into the separation cylinder 12. The solid matter heavier than the liquid hits the inner wall of the separation cylinder 12 by centrifugal force, and the separation of the solid matter and the liquid (primary separation) starts. The solid matter slowly settles along the inner wall of the separation cylinder 12 and collects in the lower chamber 28. The liquid that has descended as a rotating vortex is suddenly decelerated by the lower guide vane mechanism 30, the velocity energy is changed to pressure energy, and further solid-liquid separation (secondary separation) is performed. The liquid that does not contain solids rapidly rises due to the central vortex (negative pressure zone), passes through the outflow pipe 20, and flows out from the outlet 21 to the outside. The solid matter accumulated in the lower chamber 28 is discharged from the solid matter discharge port 22 regularly or continuously as needed.

【0004】従来、上記のような遠心力を利用した固液
分離機を用いる場合は、固液分離機に分離すべき液体/
固形物を送り込むポンプを、固液分離機の流入側に設置
している。つまりポンプの吐出側と固液分離機の流入側
とを配管で接続する構成が採られている。原液(固形物
を含んだ液体)はポンプを通り、該ポンプで加圧されて
固液分離機に送られ、ここで清浄化される。
Conventionally, when a solid-liquid separator utilizing centrifugal force as described above is used, the liquid / liquid to be separated into the solid-liquid separator is
A pump for feeding solid matter is installed on the inflow side of the solid-liquid separator. That is, the discharge side of the pump and the inflow side of the solid-liquid separator are connected by piping. The stock solution (liquid containing solid matter) passes through a pump, is pressurized by the pump, is sent to a solid-liquid separator, and is purified there.

【0005】[0005]

【発明が解決しようとする課題】ポンプを固液分離機の
流入側に設置すると、該ポンプには分離すべき液体と固
形物とが通るためポンプが摩耗し易く寿命が短くなる欠
点がある。上記のような固液分離機は、それを通過する
液体の回転によって生じる遠心力を利用して固形物を分
離するのであるから、液体の通過が流入口からの押し込
み力によるものであるか、流出口での吸い込み力による
ものであるかにかかわらず、一定量以上の液体が通過し
さえすれば遠心力を生じ性能を発揮する。そこで、固液
分離機を意図的にポンプの吸引側に設置することによっ
て、固形物を分離した清浄な液体のみを吸い込むように
し、ポンプの保護を図ることが考えられる。
When the pump is installed on the inflow side of the solid-liquid separator, the pump has a drawback that the liquid to be separated and the solid matter pass through the pump and the pump is easily worn and its life is shortened. Since the solid-liquid separator as described above separates the solid matter by utilizing the centrifugal force generated by the rotation of the liquid passing therethrough, whether the passage of the liquid is due to the pushing force from the inlet, Regardless of the suction force at the outlet, centrifugal force is exerted as long as a certain amount of liquid or more passes through, and performance is exhibited. Therefore, it is conceivable to intentionally install the solid-liquid separator on the suction side of the pump so that only the clean liquid separated from the solid matter is sucked in to protect the pump.

【0006】しかし、遠心力を利用した固液分離機の場
合、その固液分離機を単にポンプの吸引側に設置しただ
けの構成では、運転中に固形物排出口が開になると、そ
こから空気を吸い込み、固液分離機内部の渦流に乱れが
生じてしまう。そのため固液分離機本来の性能を発揮で
きなくなる問題が生じる。この問題を解決するには、固
形物排出時に、一旦固液分離動作を中断せざるを得ない
が、そうすると運転効率が低下するばかりでなく、運転
再開時の分離性能の低下も避けられない。
However, in the case of a solid-liquid separator utilizing centrifugal force, if the solid-liquid separator is simply installed on the suction side of the pump, when the solid material discharge port opens during operation, Air is sucked in, causing turbulence in the vortex inside the solid-liquid separator. Therefore, there arises a problem that the original performance of the solid-liquid separator cannot be exhibited. In order to solve this problem, the solid-liquid separation operation has to be interrupted once when the solid matter is discharged. However, this not only lowers the operation efficiency but also the separation performance when the operation is restarted.

【0007】本発明の目的は、上記のような従来技術の
欠点を解消し、遠心力を利用した固液分離機本来の性能
を損なうことなく、該固液分離機をポンプ吸引側に設置
できるようにし、それによってポンプの摩耗を防止した
サクション型固液分離装置を提供することである。
The object of the present invention is to solve the above-mentioned drawbacks of the prior art and to install the solid-liquid separator on the suction side of the pump without impairing the original performance of the solid-liquid separator utilizing centrifugal force. In this way, the suction-type solid-liquid separation device in which the wear of the pump is prevented is provided.

【0008】[0008]

【課題を解決するための手段】本発明は、遠心力を利用
した固液分離機の流出側にポンプの吸引側を接続すると
共に、前記固液分離機の固形物排出側を第1の開閉弁を
介して貯留槽の上部に接続し、該貯留槽に、第2の開閉
弁を有する下部排出口と、空気抜き管を設け、前記ポン
プの吐出側と前記貯留槽との間を第3の開閉弁を有する
分岐管で接続したサクション型固液分離装置である。通
常、第1、第2、及び第3の開閉弁は自動開閉弁であ
り、各自動開閉弁を制御する弁制御装置を具備してい
る。該弁制御装置は、通常運転中は第1の自動開閉弁を
開、第2及び第3の自動開閉弁を閉とし、貯留物排出モ
ード時に第1の自動開閉弁を閉、第2及び第3の自動開
閉弁を開とする制御を行う。
According to the present invention, a suction side of a pump is connected to an outflow side of a solid-liquid separator utilizing centrifugal force, and a solid matter discharge side of the solid-liquid separator is first opened and closed. It is connected to the upper part of the storage tank via a valve, and the storage tank is provided with a lower discharge port having a second on-off valve and an air vent pipe, and a third space is provided between the discharge side of the pump and the storage tank. It is a suction type solid-liquid separation device connected by a branch pipe having an on-off valve. Usually, the first, second, and third on-off valves are automatic on-off valves, and are equipped with a valve control device that controls each automatic on-off valve. The valve control device opens the first automatic opening / closing valve and closes the second and third automatic opening / closing valves during normal operation, and closes the first automatic opening / closing valve in the stored-material discharge mode, and closes the second and third automatic opening / closing valves. Control for opening the automatic on-off valve 3 is performed.

【0009】また特に貯留槽が大型の場合には、空気抜
き管に第4の自動開閉弁を設け、前記弁制御装置によ
り、通常運転中は閉、貯留物排出モード時に開とする制
御を行うのが好ましい。
Further, particularly when the storage tank is large, a fourth automatic opening / closing valve is provided in the air vent pipe, and the valve control device controls the valve to be closed during normal operation and opened during the stored material discharge mode. Is preferred.

【0010】[0010]

【作用】通常運転中、固液分離機と貯留槽とは内部で連
通し一体となり、且つ貯留槽は他からは隔絶され内部が
完全に液体で満たされているため、固液分離機は本来の
優れた固液分離性能を発揮する。分離した固形物は貯留
槽へと沈降する。貯留物排出モードの時は、第1の開閉
弁を閉とすることで固液分離機は貯留槽から完全に切り
離されるから、固液分離機単独で、それ本来の優れた固
液分離性能を発揮し、分離した固形物を下部チャンバー
に集積する。他方、貯留槽では、固液分離機とは関係な
く、内部に貯留した固形物を排出できる。排出後、再び
内部を完全に液体で満たした状態で固液分離機に接続す
ることで、通常運転に戻る。従って本発明のシステムで
は通常運転中も固形物排出モードの時も、固液分離機は
固液分離動作を継続して実行できる。
[Function] During normal operation, the solid-liquid separator and the storage tank communicate with each other inside and are integrated, and the storage tank is isolated from the others and the inside is completely filled with liquid. Excellent solid-liquid separation performance. The separated solid matter settles in the storage tank. In the stored material discharge mode, the solid-liquid separator is completely separated from the storage tank by closing the first opening / closing valve, so that the solid-liquid separator alone can provide the original excellent solid-liquid separation performance. It exerts and accumulates the separated solids in the lower chamber. On the other hand, in the storage tank, the solid matter stored inside can be discharged regardless of the solid-liquid separator. After discharging, by connecting to the solid-liquid separator again with the inside completely filled with liquid, normal operation is resumed. Therefore, in the system of the present invention, the solid-liquid separator can continuously perform the solid-liquid separation operation during the normal operation and the solids discharge mode.

【0011】[0011]

【実施例】図1は本発明に係るサクション型固液分離装
置の一実施例を示す全体説明図である。この装置は、主
として遠心力を利用した固液分離機10と、それに液体
を流通させるポンプ40と、固形物を貯留するための貯
留槽42、及び数個の自動開閉弁などから構成されてい
る。
DESCRIPTION OF THE PREFERRED EMBODIMENTS FIG. 1 is an overall explanatory view showing an embodiment of a suction type solid-liquid separation device according to the present invention. This device is mainly composed of a solid-liquid separator 10 utilizing centrifugal force, a pump 40 for circulating a liquid therein, a storage tank 42 for storing solid matter, and several automatic opening / closing valves. .

【0012】ここで固液分離機10は、前記図3で述べ
たのと同様の構造である。この固液分離機10の流出口
21をポンプ40の吸引側に本管44で接続する。固液
分離機10の固形物排出口22は、手動開閉弁46及び
第1の自動開閉弁V1 を介して貯留槽42の上部に接続
する。貯留槽42の下部には第2の自動開閉弁V2 を備
えた排出口48を設け、上部には空気抜き管50を取り
付ける。また前記ポンプ40の吐出側の本管52と前記
貯留槽42の上部との間を、第3の自動開閉弁V3 を有
する分岐管54で接続する。更に前記空気抜き管50に
は第4の自動開閉弁V4 を設置する。そして、これら各
自動開閉弁V1 〜V4 は弁制御装置56からの信号で開
閉制御されるようにする。
Here, the solid-liquid separator 10 has the same structure as that described in FIG. The outlet 21 of the solid-liquid separator 10 is connected to the suction side of the pump 40 by a main pipe 44. The solid matter discharge port 22 of the solid-liquid separator 10 is connected to the upper part of the storage tank 42 via a manual opening / closing valve 46 and a first automatic opening / closing valve V 1 . A discharge port 48 provided with a second automatic opening / closing valve V 2 is provided in the lower portion of the storage tank 42, and an air vent pipe 50 is attached to the upper portion. A branch pipe 54 having a third automatic opening / closing valve V 3 is connected between the main pipe 52 on the discharge side of the pump 40 and the upper part of the storage tank 42. Further, a fourth automatic opening / closing valve V 4 is installed in the air vent pipe 50. The automatic opening / closing valves V 1 to V 4 are controlled to open / close by a signal from the valve control device 56.

【0013】更に本実施例では、ポンプ40の吐出側の
本管52に圧力調整用の手動弁58が設けられてあり、
固液分離機10の流入側と流出側、及びポンプ40の吐
出側本管52の手動弁58の前後に、それぞれ圧力計G
1 〜G4 を設置している。
Further, in this embodiment, a manual valve 58 for pressure adjustment is provided in the main pipe 52 on the discharge side of the pump 40,
Pressure gauges G are respectively provided on the inflow side and the outflow side of the solid-liquid separator 10 and before and after the manual valve 58 of the discharge side main pipe 52 of the pump 40.
1 to G 4 are installed.

【0014】弁制御装置56による各自動開閉弁V1
4 の開閉動作のタイミングを図2に示す。通常運転中
は、第1の自動開閉弁V1 を開とし、それ以外の自動開
閉弁V2 〜V4 を全て閉としてある。ポンプ40による
吸引力により原液(固形物を含む液体)は先ず固液分離
機10に入る。固液分離機10では、前述したような動
作原理で固液分離が行われ、固形物は貯留槽42内まで
沈降し集積される。清浄化された液体は流出口21から
本管44を通ってポンプ40に吸い込まれ、吐出側の本
管52から吐出する。
Each automatic opening / closing valve V 1 by the valve controller 56
The timing of the opening / closing operation of V 4 is shown in FIG. During normal operation, the first automatic open / close valve V 1 is open and the other automatic open / close valves V 2 to V 4 are all closed. The stock solution (liquid containing solid matter) first enters the solid-liquid separator 10 by the suction force of the pump 40. In the solid-liquid separator 10, solid-liquid separation is performed according to the above-described operation principle, and the solid matter is settled and accumulated in the storage tank 42. The purified liquid is sucked into the pump 40 from the outlet 21 through the main pipe 44, and is discharged from the main pipe 52 on the discharge side.

【0015】貯留槽42内に固形物がある程度集積した
ならば、貯留物排出モードでの運転に切り換える。先ず
第1の自動開閉弁V1 を閉として、固液分離機10を貯
留槽42から切り離す。これによって固液分離機10は
そのまま継続して固液分離動作を行える。他方、第2の
自動開閉弁V2 を開とすると、貯留槽42内に溜まった
固形物を排出できる。その際に、第3の自動開閉弁V3
を開とすると、ポンプ40の吐出側から高圧の清浄な液
体の一部が分岐管54を通って貯留槽42に流入し、該
貯留槽42に堆積している固形物を押し出すようにして
貯留槽42を清掃する。分岐管54への通液の背圧調整
は、手動弁58の開閉度合いの制御によって行う。清掃
後に、第2の自動開閉弁V2 を閉じ、空気抜き管50の
第4の自動開閉弁V4 を開く。第3の自動開閉弁V3
引続き開を維持しているため、清浄な液体が貯留槽42
内に溜まる。空気抜き管50を通って液体が外部に噴出
するまで液体が溜まったら第4の自動開閉弁V4 を閉
じ、第3の自動開閉弁V3 を閉じる。これによって固形
物の排出動作が完了する。
When the solids are accumulated to some extent in the storage tank 42, the operation is switched to the storage discharge mode. First, the first automatic open / close valve V 1 is closed to disconnect the solid-liquid separator 10 from the storage tank 42. Thereby, the solid-liquid separator 10 can continue the solid-liquid separation operation as it is. On the other hand, when the second automatic opening / closing valve V 2 is opened, the solid matter accumulated in the storage tank 42 can be discharged. At that time, the third automatic opening / closing valve V 3
Is opened, a part of the high-pressure clean liquid flows from the discharge side of the pump 40 into the storage tank 42 through the branch pipe 54, and the solid matter accumulated in the storage tank 42 is pushed out and stored. The tank 42 is cleaned. The back pressure of the liquid passing through the branch pipe 54 is adjusted by controlling the opening / closing degree of the manual valve 58. After cleaning, the second automatic opening / closing valve V 2 is closed, and the fourth automatic opening / closing valve V 4 of the air vent pipe 50 is opened. Since the third automatic opening / closing valve V 3 is kept open, the clean liquid is stored in the storage tank 42.
Accumulate inside. When the liquid has accumulated until it is ejected to the outside through the air vent pipe 50, the fourth automatic opening / closing valve V 4 is closed and the third automatic opening / closing valve V 3 is closed. This completes the operation of discharging the solid matter.

【0016】その後、再び第1の自動開閉弁V1 を開、
それ以外の自動開閉弁V2 〜V4 を全て閉として通常運
転モードに戻る。この時、貯留槽42の内部は液体で満
たされ、空気が混入することはないため、固液分離機の
分離性能が損なわれることはない。
After that, the first automatic on-off valve V 1 is opened again,
All other automatic on-off valves V 2 to V 4 are closed and the normal operation mode is returned to. At this time, the inside of the storage tank 42 is filled with liquid and air is not mixed in, so the separation performance of the solid-liquid separator is not impaired.

【0017】弁制御装置56はタイマーを内蔵してお
り、上記のシーケンスを自動的に実行する。また通常運
転モードと固形物排出運転モードとの切替えも自動的に
実施可能である。勿論、手動スイッチ操作により、必要
に応じて上記運転モードの切替えを行わせることもでき
る。
The valve control device 56 has a built-in timer and automatically executes the above sequence. Further, it is possible to automatically switch between the normal operation mode and the solid matter discharge operation mode. Needless to say, the operation mode can be switched as necessary by operating the manual switch.

【0018】以上、本発明の好ましい一実施例について
詳述したが、本発明はこのような構成のみに限定される
ものではない。上記実施例では全て自動開閉弁を使用
し、弁制御装置で開閉を制御する構成になっている。こ
の構成は簡便で好ましいが、場合によっては全て手動で
行うようにしてもよい。空気の混入を防ぐためには空気
抜き管に開閉弁を設けることが好ましいが、特に小規模
のシステムの場合は、開閉弁を省略してもあまり支障は
生じない。また本発明は図3に示すような固液分離機に
限らず、遠心力を利用した全ての形式の固液分離機に適
用できる。
The preferred embodiment of the present invention has been described above in detail, but the present invention is not limited to such a configuration. In the above-described embodiments, the automatic opening / closing valve is used in all, and opening / closing is controlled by the valve control device. This configuration is simple and preferable, but in some cases it may be performed manually. It is preferable to provide an opening / closing valve on the air vent pipe in order to prevent the entry of air, but especially in the case of a small-scale system, omission of the opening / closing valve does not cause much trouble. Further, the present invention is not limited to the solid-liquid separator as shown in FIG. 3, but can be applied to all types of solid-liquid separators utilizing centrifugal force.

【0019】[0019]

【発明の効果】本発明は上記のようにポンプの吸引側に
固液分離機を設置したため、ポンプに流れる液体は既に
固形物が分離除去されており、ポンプの摩耗を防止する
ことができポンプの長寿命化を図ることができる。そし
て本発明では固液分離機に貯留槽を接続し、数個の開閉
弁の制御で固液分離機側に空気が吸い込まれないように
工夫しているため、遠心力を利用した固液分離機の分離
性能が損なわれることもない。本発明装置では、固形物
排出モードの時でも固液分離動作を続行できるから、運
転効率もよい。
As described above, according to the present invention, since the solid-liquid separator is installed on the suction side of the pump as described above, the solid matter has already been separated and removed from the liquid flowing through the pump, and the wear of the pump can be prevented. It is possible to extend the life of the. And in the present invention, a storage tank is connected to the solid-liquid separator, and by devising such that air is not sucked into the solid-liquid separator by controlling several on-off valves, solid-liquid separation using centrifugal force is performed. The separation performance of the machine is not impaired. In the device of the present invention, since the solid-liquid separation operation can be continued even in the solid matter discharge mode, the operation efficiency is good.

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

【図1】本発明に係るサクション型固液分離装置の全体
構成図。
FIG. 1 is an overall configuration diagram of a suction type solid-liquid separator according to the present invention.

【図2】その各自動開閉弁の開閉タイミングを示す説明
図。
FIG. 2 is an explanatory view showing opening / closing timings of the respective automatic opening / closing valves.

【図3】遠心力を利用した固液分離機の代表例の構造と
動作の説明図。
FIG. 3 is an explanatory view of the structure and operation of a typical example of a solid-liquid separator using centrifugal force.

【符号の説明】[Explanation of symbols]

10 固液分離機 21 流出口 22 固形物排出口 40 ポンプ 42 貯留槽 44 本管 48 固形物排出口 50 空気抜き配管 54 分岐管 V1 第1の自動開閉弁 V2 第2の自動開閉弁 V3 第3の自動開閉弁 V4 第4の自動開閉弁10 Solid-Liquid Separator 21 Outlet 22 Solid Discharge Port 40 Pump 42 Storage Tank 44 Main Pipe 48 Solid Discharge Port 50 Air Vent Pipe 54 Branch Pipe V 1 First Automatic Open / Close Valve V 2 Second Automatic Open / Close Valve V 3 3rd automatic opening / closing valve V 4 4th automatic opening / closing valve

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 遠心力を利用した固液分離機の流出側に
ポンプの吸引側を接続すると共に、前記固液分離機の固
形物排出側を第1の開閉弁を介して貯留槽の上部に接続
し、該貯留槽には、第2の開閉弁を有する下部排出口
と、空気抜き管を設け、前記ポンプの吐出側と前記貯留
槽との間を第3の開閉弁を有する分岐管で接続したこと
を特徴とするサクション型固液分離装置。
1. A suction side of a pump is connected to an outflow side of a solid-liquid separator utilizing centrifugal force, and a solid discharge side of the solid-liquid separator is connected to an upper part of a storage tank via a first opening / closing valve. The storage tank is provided with a lower outlet having a second opening / closing valve and an air vent pipe, and a branch pipe having a third opening / closing valve is provided between the discharge side of the pump and the storage tank. A suction-type solid-liquid separator characterized by being connected.
【請求項2】 第1、第2、及び第3の開閉弁は自動開
閉弁であり、各自動開閉弁を制御する弁制御装置を具備
し、該弁制御装置は、通常運転中は第1の自動開閉弁を
開、第2及び第3の自動開閉弁を閉とし、貯留物排出モ
ードの時に第1の自動開閉弁を閉、第2及び第3の自動
開閉弁を開とする制御を行う請求項1記載の固液分離装
置。
2. The first, second, and third on-off valves are automatic on-off valves, each of which is provided with a valve control device that controls each of the automatic on-off valves. Control to open the automatic open / close valve, close the second and third automatic open / close valves, and close the first automatic open / close valve and open the second and third automatic open / close valves in the stored-material discharge mode. The solid-liquid separation device according to claim 1, which is performed.
【請求項3】 空気抜き管に第4の自動開閉弁を設け、
弁制御装置により、通常運転中は閉、貯留物排出モード
の時に開とする制御を行う請求項2記載の固液分離装
置。
3. An air vent pipe is provided with a fourth automatic opening / closing valve,
The solid-liquid separation device according to claim 2, wherein the valve control device performs control such that the valve control device is closed during normal operation and opened during the stored-material discharge mode.
JP03212614A 1991-07-30 1991-07-30 Suction-type solid-liquid separator Expired - Fee Related JP3127008B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP03212614A JP3127008B2 (en) 1991-07-30 1991-07-30 Suction-type solid-liquid separator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP03212614A JP3127008B2 (en) 1991-07-30 1991-07-30 Suction-type solid-liquid separator

Publications (2)

Publication Number Publication Date
JPH0531404A true JPH0531404A (en) 1993-02-09
JP3127008B2 JP3127008B2 (en) 2001-01-22

Family

ID=16625602

Family Applications (1)

Application Number Title Priority Date Filing Date
JP03212614A Expired - Fee Related JP3127008B2 (en) 1991-07-30 1991-07-30 Suction-type solid-liquid separator

Country Status (1)

Country Link
JP (1) JP3127008B2 (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007111587A (en) * 2005-10-18 2007-05-10 Ohbayashi Corp Solid separating device
JP2007296451A (en) * 2006-04-28 2007-11-15 Nikuni:Kk Liquid treatment apparatus
US7569267B2 (en) 2003-10-22 2009-08-04 Kureha Corporation Laminate and production process thereof
US7608339B2 (en) 2003-10-22 2009-10-27 Kureha Corporation Multilayer film
CN112189116A (en) * 2018-03-29 2021-01-05 福瑞科有限公司 Removal device with flow control

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7569267B2 (en) 2003-10-22 2009-08-04 Kureha Corporation Laminate and production process thereof
US7608339B2 (en) 2003-10-22 2009-10-27 Kureha Corporation Multilayer film
JP2007111587A (en) * 2005-10-18 2007-05-10 Ohbayashi Corp Solid separating device
JP2007296451A (en) * 2006-04-28 2007-11-15 Nikuni:Kk Liquid treatment apparatus
CN112189116A (en) * 2018-03-29 2021-01-05 福瑞科有限公司 Removal device with flow control

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