JPS6028549B2 - Continuous centrifugal concentrator - Google Patents

Continuous centrifugal concentrator

Info

Publication number
JPS6028549B2
JPS6028549B2 JP3079579A JP3079579A JPS6028549B2 JP S6028549 B2 JPS6028549 B2 JP S6028549B2 JP 3079579 A JP3079579 A JP 3079579A JP 3079579 A JP3079579 A JP 3079579A JP S6028549 B2 JPS6028549 B2 JP S6028549B2
Authority
JP
Japan
Prior art keywords
cylindrical body
stock solution
solids
outer cylindrical
discharged
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
Application number
JP3079579A
Other languages
Japanese (ja)
Other versions
JPS55121853A (en
Inventor
康雄 桑元
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.)
Kubota Corp
Original Assignee
Kubota Corp
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 Kubota Corp filed Critical Kubota Corp
Priority to JP3079579A priority Critical patent/JPS6028549B2/en
Publication of JPS55121853A publication Critical patent/JPS55121853A/en
Publication of JPS6028549B2 publication Critical patent/JPS6028549B2/en
Expired legal-status Critical Current

Links

Description

【発明の詳細な説明】 本発明は化学プラントや下水処理施設等から生ずる汚泥
の如き固形物を含む原液を濃縮固形物と清澄水とに連続
して分離するこの出来来る連続式遠心濃縮機に関するも
のである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a continuous centrifugal concentrator that can continuously separate stock solutions containing solids such as sludge generated from chemical plants, sewage treatment facilities, etc. into concentrated solids and clear water. It is something.

固形物を含む原液を処理する場合は固形物と清澄水すな
わち固液を分離して処理する必要があり、この際固形物
をいかに濃縮して効率よく固液を分離するかが重要な課
題となる。
When processing a stock solution containing solids, it is necessary to separate the solids from clear water, i.e. solid-liquid, and an important issue at this time is how to concentrate the solids and efficiently separate the solid-liquid. Become.

そこで従来の遠心濃縮機は、上端を越流堰にした閉口部
を形成し下端を有底にした立型回転筒体に原液を投入し
て固液分離を行なっている。この方法は、筒体内に投入
された原液に遠心力を与えて固形物を筒体内周面に濃縮
堆積させ、一方固形物が分離した清澄水は上端関口部よ
り溢水排出させて固液を分離するものである。しかしこ
の場合固形物は筒体内から自動的に排出することが出来
ないので一旦原液の供給を停止した後、回転を落しスキ
ムパィプ等を筒体内に押入して吸引し筒体外に固形物を
排出していた。この様に従来の遠心濃縮機は高速回転で
原液供給と固形物を濃縮する工程と、回転を低速に又は
停止して固形物を排出する工程のバッチ運転であり効率
が悪く、また操業の安定性を欠くものであった。本発明
は上記の点を鑑み、装置の効率化と操業の安定を図るた
め、原液供聯合中であっても筒体内の固形物の排出が出
釆るようにしたもので、連続的に固液の分離を行ない得
るようにしたものである。
Therefore, in conventional centrifugal concentrators, solid-liquid separation is performed by charging the stock solution into a vertical rotary cylinder whose upper end forms a closed section with an overflow weir and whose lower end is bottomed. In this method, centrifugal force is applied to the stock solution put into the cylinder to concentrate and deposit the solids on the periphery of the cylinder, while the clear water from which the solids have been separated is discharged overflowing from the upper end to separate the solids and liquids. It is something to do. However, in this case, the solids cannot be automatically discharged from the cylinder, so after stopping the supply of the stock solution, the rotation is slowed down and a skim pipe is inserted into the cylinder to suction it and the solids are discharged from the cylinder. was. As described above, conventional centrifugal concentrators operate in batches, with the process of supplying the stock solution and concentrating the solids at high speed, and the process of slowing down or stopping the rotation to discharge the solids, resulting in poor efficiency and unstable operation. It lacked sex. In view of the above points, in order to improve the efficiency of the device and stabilize the operation, the present invention is designed so that the solids in the cylinder can be discharged even during the undiluted liquid supply, so that solids can be continuously solidified. It is designed to allow liquid separation.

以下本発明の実施例を図面に基づいて詳細に説明する。Embodiments of the present invention will be described in detail below based on the drawings.

図面において、1は軸心を鉛直方向にして回転が与えら
れる筒体外である。原液はこの外筒体1内で遠心力を受
けて固液の分離が行なわれる。外筒体1の底部は縮蓬し
た頭斜周壁laを成しており濃緒された固形物Aが上方
に滑って移動しやすいように形成されている。外筒体1
の上下両端は端板2,3が設けられ各端板2,3には中
央に開□部4.5が設けらている。上端開口部4からは
原液供給管6と固形物引抜管7が挿入配設されており、
原液の供給と共に濃縮された固形物Aが排出される。ま
た下端関口部5は分離液を排出する越流堰となる。原液
供聯合管6の先端下方にはボス付きの円形案内板8が外
筒体と一体回転する様に設けられており、原液はこの案
内板8により受け止められて遠心力が与えられ外筒体1
の内壁に向けて均等に送出される。外筒体1と案内板8
との間には下端開□部4に向けて拡摩した内筒体9が外
筒体1と一体回転する様に設けてあり、案内板8から送
出された原液は更にここで受け止めて外筒体1内に原液
の乱れを防ぐと共に、固形物はこの内筒体9の煩斜した
周壁を滑って外筒体1の底部周壁laに移行しやすい様
に形成されている。10は外筒体1のケーシングである
In the drawings, reference numeral 1 indicates the outside of the cylindrical body, which is rotated with its axis in the vertical direction. The stock solution is subjected to centrifugal force within this outer cylindrical body 1 to separate solid and liquid. The bottom of the outer cylindrical body 1 forms a slanted circumferential wall la, which is formed so that the solid material A can easily slide upward. Outer cylinder body 1
End plates 2 and 3 are provided at both upper and lower ends of the board, and each end plate 2 and 3 is provided with an opening 4.5 in the center. A stock solution supply pipe 6 and a solid material withdrawal pipe 7 are inserted from the upper end opening 4.
Concentrated solid material A is discharged together with supply of the stock solution. Further, the lower end entrance portion 5 serves as an overflow weir for discharging the separated liquid. A circular guide plate 8 with a boss is provided below the tip of the undiluted solution supply joint tube 6 so as to rotate together with the outer cylinder, and the undiluted solution is received by this guide plate 8 and centrifugal force is applied to the outer cylindrical body. 1
is evenly distributed towards the inner wall of the Outer cylinder body 1 and guide plate 8
An inner cylindrical body 9 whose friction is enlarged toward the lower end opening 4 is provided between the cylindrical body 9 and the outer cylindrical body 1 so as to rotate together with the outer cylindrical body 1. The tube body 1 is formed in such a manner that it prevents the undiluted solution from being disturbed, and also allows solid matter to easily slide along the oblique peripheral wall of the inner tube body 9 and move to the bottom circumferential wall la of the outer tube body 1. 10 is a casing of the outer cylindrical body 1.

本発明は以上の如き構成であるから、原液供V給管6か
ら供給された原液は案内板8によって内筒体9に向けて
均等に送出される。内筒体9は、原液を供給する際の外
筒体1内の原液の流れを乱さないようにして、固形物A
層の乱れを防止すると共に、内筒体9内の固形物を外筒
体1の煩斜周壁laに向けて移行させる。従って固形物
の外筒体1での滞留時間が長くなり十分な濃縮が得られ
、外筒体1の煩斜周壁laを滑って外節体1の上端に移
行し、固形物引抜管7により吸引されて外筒体1外に排
出される。一方固形物が分離された分離液は下端開口部
5より溢水排水され排出口11より装置外に排出される
。従って固形物排出時の原液の乱れの影響を殆んど受け
ないから連続して固液の分離を行なうことが出来る。本
発明は以上説明した如く実施されるものであり、原液は
一旦案内板で受止めて内筒体に供給し、このに内筒体よ
って固形物を外筒体の底部の方向に移行させると共に原
液供聯合時の濃縮固形物層の乱れを防ぎ、固形物の排出
は上端から、また分離液の排出は下端から行なうから固
形物は十分に濃縮され、一方分離液の排出は固形物排出
時の影響を受けないから、連続して濃縮率の高い固液分
離を行なうことが出来るものであり、装置の効率を向上
させまた操業を安定させることが出来る。
Since the present invention has the above-described configuration, the stock solution supplied from the stock solution supply V supply pipe 6 is evenly delivered toward the inner cylinder body 9 by the guide plate 8. The inner cylindrical body 9 handles the solid matter A without disturbing the flow of the undiluted solution in the outer cylindrical body 1 when supplying the undiluted solution.
Disturbance of the layers is prevented, and the solid matter in the inner cylinder 9 is moved toward the oblique peripheral wall la of the outer cylinder 1. Therefore, the residence time of the solids in the outer cylinder body 1 becomes longer, sufficient concentration is obtained, the solids slide on the oblique peripheral wall la of the outer cylinder body 1, migrate to the upper end of the outer segment body 1, and are transferred to the solid substance drawing pipe 7. It is sucked and discharged outside the outer cylinder body 1. On the other hand, the separated liquid from which solids have been separated is drained from the lower end opening 5 and discharged from the apparatus through the discharge port 11. Therefore, solid-liquid separation can be carried out continuously because it is hardly affected by disturbance of the stock solution when solids are discharged. The present invention is carried out as described above, and the stock solution is once received by the guide plate and supplied to the inner cylinder, and the solid material is transferred to the bottom of the outer cylinder by the inner cylinder. This prevents disturbance of the concentrated solids layer when the raw solution is supplied, and the solids are discharged from the upper end, and the separated liquid is discharged from the lower end, so the solids are sufficiently concentrated.On the other hand, the separated liquid is discharged when the solids are discharged. Since it is not affected by the effects of water, it is possible to perform solid-liquid separation with a high concentration rate continuously, improving the efficiency of the device and stabilizing the operation.

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

図面は本発明の実施例を示す断面図である。 1・・・・・・外筒体、2,3・・・・・・端板、4,
5・・・・・・開口部、6・・・・・・原液供繋合管、
7…・・・固形物引抜管、8・・・・・・案内板、9・
・・・・・内筒体。
The drawings are cross-sectional views showing embodiments of the present invention. 1... Outer cylinder body, 2, 3... End plate, 4,
5... Opening part, 6... Stock solution supply connection tube,
7... Solid material drawing pipe, 8... Guide plate, 9.
...Inner cylindrical body.

Claims (1)

【特許請求の範囲】[Claims] 1 中央に開口が形成された端板を軸心方向両端に有す
る外筒体を、その軸心を鉛直方向にして軸心回りに回動
自在に設け、前記外筒体の径方向内側に同心状に下端側
に向けて拡径した内筒体を設け、上端開口に原液供給管
を固形物引抜管を配設し、原液供給管先端下方に原液を
前記内筒体に向けて送出する案内板を設けたことを特徴
とする連続式遠心濃縮装置。
1. An outer cylindrical body having end plates with an opening formed in the center at both ends in the axial direction is provided so as to be rotatable around the axis with its axis in the vertical direction, and a concentric outer cylindrical body is provided on the radially inner side of the outer cylindrical body. An inner cylindrical body whose diameter is enlarged toward the lower end in the form of a shape, a stock solution supply pipe and a solid material withdrawal pipe arranged at the upper end opening, and a guide for sending the stock solution toward the inner cylinder body below the tip of the stock solution supply pipe. A continuous centrifugal concentrator characterized by the provision of a plate.
JP3079579A 1979-03-15 1979-03-15 Continuous centrifugal concentrator Expired JPS6028549B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3079579A JPS6028549B2 (en) 1979-03-15 1979-03-15 Continuous centrifugal concentrator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3079579A JPS6028549B2 (en) 1979-03-15 1979-03-15 Continuous centrifugal concentrator

Publications (2)

Publication Number Publication Date
JPS55121853A JPS55121853A (en) 1980-09-19
JPS6028549B2 true JPS6028549B2 (en) 1985-07-05

Family

ID=12313608

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3079579A Expired JPS6028549B2 (en) 1979-03-15 1979-03-15 Continuous centrifugal concentrator

Country Status (1)

Country Link
JP (1) JPS6028549B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0659159U (en) * 1993-01-28 1994-08-16 静岡化成株式会社 Mobile stand for holding long objects

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0659159U (en) * 1993-01-28 1994-08-16 静岡化成株式会社 Mobile stand for holding long objects

Also Published As

Publication number Publication date
JPS55121853A (en) 1980-09-19

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