JPS6022912A - Solid separating apparatus - Google Patents

Solid separating apparatus

Info

Publication number
JPS6022912A
JPS6022912A JP12798483A JP12798483A JPS6022912A JP S6022912 A JPS6022912 A JP S6022912A JP 12798483 A JP12798483 A JP 12798483A JP 12798483 A JP12798483 A JP 12798483A JP S6022912 A JPS6022912 A JP S6022912A
Authority
JP
Japan
Prior art keywords
liquid
solids
tank
treated
solid
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.)
Pending
Application number
JP12798483A
Other languages
Japanese (ja)
Inventor
Tetsuo Nishida
哲夫 西田
Fumiyoshi Murakami
村上 文祥
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP12798483A priority Critical patent/JPS6022912A/en
Publication of JPS6022912A publication Critical patent/JPS6022912A/en
Pending legal-status Critical Current

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  • Separation Of Suspended Particles By Flocculating Agents (AREA)

Abstract

PURPOSE:To obtain a compact settling tank by providing a circular tank, a discharge mechanism of a solid-contg. liquid, and a treated liquid discharge mechanism, scraping together the solids accumulated in the central recess of the circular tank by a rake, and transferring the solids to a storage tank by a pump. CONSTITUTION:The liquid to be treated is supplied into a circular tank 1 from an inflow port 4 through an inflow passage 3. The liquid to be treated circulates rapidly at the central part and slowly at the outer circumference by a rake 19 of a scraping machine 16, and the sand, etc. having a larger sp. gr. flows toward the center along the bottom 5 of the tank. The solids settled on the bottom 5 of the tank are accumulated in a recess 6 at the central part. The solids are discharged by a pump 9 together with a liquid as the solid-contg. liquid contg. a large quantity of solids. Meanwhile, the treated liquid free from solids is sucked by a pump 14, and sent to the next stage.

Description

【発明の詳細な説明】 本発明は下水又は雨水処理において沈砂などの粉粒状固
形物又はスラッジ状の固形物を含む被処理液から固形物
を分離して清浄な処理済液を得るための固形物分離装置
に関するものである。 従来この様な被処理液の固形物
分離を行なう場合には、特に大量の被処理液を扱う雨水
処理の場合には大きな沈殿槽(或いは沈殿池)の中に被
処理液を導き、固形物を重力により沈殿せしめ、得られ
た清浄な処理済液を別の貯留槽(又は貯留池)に導き、
貯留槽から改めてポンプなどの排出桟構により排出して
いた。〜・方水底に分離沈殿した沈砂などの固形物を取
除くには、掻寄機によって掻寄せた後、掻」−磯で掻り
げ、コンベヤ逆どの輸送機構により池面に移送していた
。 このような従来の方法においては次の如外欠点を有
する。
DETAILED DESCRIPTION OF THE INVENTION The present invention is a method for separating solids from a treated liquid containing powdery solids such as sediment or sludge-like solids in sewage or rainwater treatment to obtain a clean treated liquid. This relates to a material separation device. Conventionally, when separating the solids from the liquid to be treated, especially in the case of rainwater treatment where a large amount of liquid to be treated is handled, the liquid to be treated is introduced into a large sedimentation tank (or sedimentation pond) to separate the solids. is allowed to settle by gravity, and the resulting clean treated liquid is led to another storage tank (or reservoir),
The water was once again discharged from the storage tank using a discharge structure such as a pump. - To remove solid matter such as sediment that has separated and settled on the bottom of the pond, it is first raked with a raking machine, then raked with a rock and transported to the pond surface with a transport mechanism such as a conveyor or reverse. . This conventional method has the following disadvantages.

(1)重力沈殿により分離を行なうので連続運転かで外
ない。
(1) Since separation is carried out by gravity precipitation, continuous operation is sufficient.

(2)従って処理時間が長くなる。(2) Therefore, processing time becomes longer.

(:()処理時間を短くするには、広い沈殿槽を要し、
そのために広い敷地人ペースを必要とする。
(:() To shorten the processing time, a wide sedimentation tank is required.
This requires a large space for people to work on the site.

(4)沈殿作用を乱さないために処理済液を導く貯留槽
を別に必要とし、広い敷地スペースを必要とする。
(4) In order not to disturb the sedimentation process, a separate storage tank is required to guide the treated liquid, and a large site space is required.

(5)沈殿した固形物を取出すために、掻寄機、掻に機
、コンベヤなどの装置を必要とし、設備費、運転費のほ
か保守にも手間がかかり、スペースも必要となる。
(5) In order to take out the precipitated solids, devices such as scrapers, scrapers, and conveyors are required, which requires equipment costs, operating costs, and maintenance, and requires space.

(6) これらの機器による固形物取出し作業は、沈殿
動作と同時に行なうことができないので、処理時間は一
層長くなる。
(6) Since the solid matter removal operation using these devices cannot be carried out simultaneously with the precipitation operation, the processing time becomes even longer.

などの欠、係である。It is a matter of lack of such things.

本発明は従来のものの」二記の欠点を除き、雨水処理の
如と大量の被処理液の固形物分離動作であってもこれを
連続的に行ない、しかも装置が小型であってスペースを
要さず、複雑な機器を要さず設備費、運転費及び保守の
手間を軽減できる固形物分離装置を提供することを目的
とするものである。
The present invention eliminates the two drawbacks of the conventional ones, and allows continuous separation of solid matter from a large amount of liquid to be treated, such as rainwater treatment.Moreover, the device is small and requires space. It is an object of the present invention to provide a solid matter separator that does not require complicated equipment and can reduce equipment costs, operating costs, and maintenance efforts.

本発明はほぼ円筒状の周壁な有する円形槽と、沈殿分離
した固形物を多量に含む固形分液を吸出して排出する固
形分液排出機構と、固形物を分離した後の処理済液を排
出する処理済液排出機構とを備え、前記円形槽の周壁に
は、被処理液を流入せしめる流入路を設け、前記円形槽
の槽底のほぼ中央部に凹所を設け、前記固形分液排出機
構の固形分液吸込1」を前記凹所に臨ましめ、1iij
記円形槽のにぼ中央に、垂直軸を中心に回転する掻板を
有する攪はん機構を備えたことを特徴とする固形物分離
装置である。
The present invention includes a circular tank having a substantially cylindrical peripheral wall, a solid liquid discharge mechanism that sucks out and discharges a solid liquid containing a large amount of precipitated and separated solids, and a solid liquid discharge mechanism that discharges the treated liquid after separating the solid substances. A treated liquid discharge mechanism is provided, the peripheral wall of the circular tank is provided with an inflow path through which the liquid to be treated flows in, a recess is provided approximately in the center of the bottom of the circular tank, and the solid liquid is discharged. Make the solid liquid suction 1 of the mechanism face the recess, and
This solid matter separator is characterized in that it is equipped with a stirring mechanism having a scraper rotating around a vertical axis in the center of the circular tank.

本発明の実施例を第1図及び第2図により説明する。Embodiments of the present invention will be described with reference to FIGS. 1 and 2.

1は、はぼ円筒状め周壁2を有する円形槽であり、周壁
2の一部に、被処理液を流入せしめる流入路3が流入口
4に開口している。流入口4の位置は、円形槽1の中央
に向かうようにしてもよく、また、周壁2に灯して接線
方向に流入するようにしてもよい。円形槽1の槽底5の
ほぼ中央には凹んでいる凹所6が形成されている。
Reference numeral 1 denotes a circular tank having a circumferential wall 2 having a substantially cylindrical shape, and an inflow passage 3 through which a liquid to be treated flows into a part of the circumferential wall 2 opens into an inflow port 4 . The inlet 4 may be positioned toward the center of the circular tank 1, or may be directed toward the peripheral wall 2 so that the inlet 4 flows tangentially. A recess 6 is formed approximately in the center of the tank bottom 5 of the circular tank 1.

周壁2としては円形のほか、長円形、楕円形、スパイラ
ル状など、後述の如く攪はん機構の旋回作用によって被
処理液が、周壁2に沿って円滑に旋回して流れるような
形状ならよい。また、凹所6は図の如く中央部のみが一
段と深く凹んでいて、もよく、また、槽底5の中央部の
みが凹んで、凹所6を形成し、他の部は平坦であっても
五〇。また、槽底5の全体が傾斜して形ItLされて゛
もより、゛中央部のみが一部平になって11でもよ0゜
吸込ロア、吸込管8、ポンプ9、吐出管101こより固
形分液排出機構が形成され、後述の如く凹所6に集積す
る沈砂などの固形物を、固形物を多量に含む固形分液と
して吸出し、貯槽11或νA1土離れた位置にある次工
程の装置に送るよう1こなっている。固形分液を有効に
排出するために吸込ロアは凹所6に臨んで設けられて0
る。
The peripheral wall 2 may be circular, oval, elliptical, spiral, etc. as long as it allows the liquid to be treated to smoothly swirl and flow along the peripheral wall 2 due to the swirling action of the stirring mechanism as described later. . Further, as shown in the figure, only the central part of the recess 6 may be recessed deeper, or only the central part of the tank bottom 5 may be recessed to form the recess 6, and the other parts may be flat. Also fifty. In addition, since the entire tank bottom 5 is slanted and shaped, only the center part is partially flattened, so that the solids can be drawn from the suction lower, suction pipe 8, pump 9, and discharge pipe 101 at an angle of 0°. A discharge mechanism is formed, and as described later, solid matter such as sediment accumulated in the recess 6 is sucked out as a solid liquid containing a large amount of solid matter, and sent to the storage tank 11 or νA1 to a device for the next process located at a distance. It's going well. In order to effectively discharge the solid liquid, the suction lower is provided facing the recess 6.
Ru.

吸込「]12、吸込管13、ポンプ14、吐出管15に
より処理済液排出機構が形成され、固形分を分離した後
の清浄な処理酒液を吸出して次−r程に送るようになっ
ている。
The suction pipe 12, the suction pipe 13, the pump 14, and the discharge pipe 15 form a treated liquid discharge mechanism, which sucks out the clean processed liquor liquid after solids have been separated and sends it to the next stage. There is.

16は攪はん機構であり、モータ17により駆動される
垂直な回転軸11Nこより回転する掻板19を有する。
Reference numeral 16 denotes a stirring mechanism, which has a stirring plate 19 rotated by a vertical rotation shaft 11N driven by a motor 17.

掻板19の高さは最低水位のときにも攪はんがで鰺るよ
うな高さに選ぶ。最高水位のときにもぐってしまっても
よし)。また、昇降調節可能としてもより)。
The height of the scraper plate 19 is selected so that it can be stirred even at the lowest water level. (You don't have to worry about it slipping in when the water is at its highest level.) It is also possible to raise and lower it (adjustable).

作用につき説明する。The effect will be explained.

被処理液は流入路3を通り、流入1」4より円形槽1に
流入する。流入して円形槽1内に収容さitた被処理液
は、掻はん機構16の掻板191こよ暫)矢印20の向
きに中心部は早く外周はゆるく循環し、この際掻板19
の遠心作用により液面(=I近の液の流れは外力に向か
い、中心のFカでは矢印22の如く吸込みの流れを生ず
る。その結果矢印23.24.22の如き二次的な循環
流を生じ、比重の大きい砂などは槽底5に沿−)ては中
心に向かう矢印24の如き流れとなる。
The liquid to be treated passes through the inflow path 3 and flows into the circular tank 1 from the inflow 1''4. The liquid to be treated that flows in and is stored in the circular tank 1 circulates through the scraping plate 191 of the scraping mechanism 16 in the direction of the arrow 20, faster at the center and looser at the outer periphery.
Due to the centrifugal action of the liquid surface (=I), the liquid flow near the liquid surface (=I) is directed toward the external force, and at the center F, a suction flow is generated as shown by the arrow 22.As a result, a secondary circulation flow is generated as shown by the arrows 23, 24, and 22. , and sand with a large specific gravity flows along the tank bottom 5 as shown by an arrow 24 toward the center.

槽底5に沈殿する固形物は、この二次流れにより中心に
集められ中央イ」近の凹所6に婁仔ける。
The solids that settle on the tank bottom 5 are collected in the center by this secondary flow and are dumped into the recess 6 near the center.

この集積した固形物を、吸込1−17からポンプ9によ
り、j夜と共に固形物を多く含んだ固形fF液として吸
出し、損出する。
This accumulated solid matter is sucked out from the suction 1-17 by the pump 9 as a solid fF liquid containing a large amount of solid matter, and is lost.

−・力、固形物を除去した被処理液は吸込1i112か
らポンプ14により吸上げられて次」二程に送られる。
- The liquid to be treated from which solid matter has been removed is sucked up by the pump 14 from the suction 1i112 and sent to the next step.

本発明の固形物分#IIU装置は、化学プロセスにおけ
る固液分離、産業廃水処理におけるスラッジ除去プロセ
ス、汚水・雨水処理におけるスラッジ除去や沈砂プロセ
スなどに適用することがで終る。
The solid content #IIU device of the present invention can be applied to solid-liquid separation in chemical processes, sludge removal processes in industrial wastewater treatment, sludge removal and sand settling processes in sewage/rainwater treatment, etc.

本発明により、次の如き顕著な利点を有する固形物分離
装置を提供することができ、実用上極めて大なる効果を
奏することがで外る。
According to the present invention, it is possible to provide a solid matter separator having the following remarkable advantages, and it can be seen that it has extremely great practical effects.

(1)被処理水を連続的に流入せしめても、沈殿する固
形物を連続的に中央に集め、固形分液排出機構により連
続的に排出し、かつ処理済液を処理済液排出(幾構によ
り連続的に排出するので、連続的に固形物分離を行なう
ことかできる。
(1) Even if the water to be treated is allowed to flow in continuously, the precipitated solids are continuously collected in the center, and the solids are continuously discharged by the solid liquid discharge mechanism, and the treated liquid is discharged (somehow). Since the system discharges continuously, solids can be separated continuously.

(2)従って分離槽の大静さを極めて小さくすることか
で外る。
(2) Therefore, the problem can be solved by making the separation tank extremely quiet.

(3)分離速度が速いことも相まって、短時間で多量の
被処理液の処理ができる。
(3) Coupled with the high separation speed, a large amount of liquid to be processed can be processed in a short time.

(4)沈殿と、固形分液排出と、処理済液排出とが同時
にでとるので、処理済液排出用の貯留槽を分離槽で兼J
llすることができ、別途排出用槽を設ける必要がない
(4) Since precipitation, solid liquid discharge, and treated liquid discharge are performed at the same time, the storage tank for treated liquid discharge can also be used as a separation tank.
ll, and there is no need to provide a separate discharge tank.

(5)固形物の排出のための固形物掻集め、掻−ヒげ、
輸送などの多数の付帯設41iiなどを不要となし、簡
単な固形分液排出機構により固形物排出を行なうことが
で外る。
(5) raking and scraping of solids for the purpose of discharging solids;
A large number of ancillary facilities 41ii for transportation and the like are not required, and the solids can be discharged by a simple solids liquid discharge mechanism.

(6)以上の理由により、必要なスペースが極めて小さ
くなり、機器の数量も著しく減り、敷地費、設備費、保
守費、運転費などを軽減せしめ、機器が甲、純であって
故障も少なく、信頼性が入て゛ある。
(6) For the above reasons, the required space is extremely small, the quantity of equipment is also significantly reduced, site costs, equipment costs, maintenance costs, operating costs, etc. are reduced, and the equipment is simple and has fewer failures. , reliability is included.

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

第1図及び第2図は、本発明の実施例の平面図及びその
縦断面正面図である。 1・・円形槽、2・・周壁、3・・流入路、4・・流入
1上 5・・槽底、6・・凹所、7・・吸込l]、8・
・吸込管、9・・ポンプ、10・・吐出管、11・・貯
槽、12・・吸込11.13・・吸込管、14・・ポン
プ、15・・111出管、16・・攪はん機構、17・
・モータ、18・・同転軸、19・・掻板、20,22
,23.24・・矢印。
FIGS. 1 and 2 are a plan view and a vertical cross-sectional front view of an embodiment of the present invention. 1...Circular tank, 2...Peripheral wall, 3...Inflow channel, 4...Inflow 1 top, 5...Bottom of the tank, 6...Recess, 7...Suction l], 8...
・Suction pipe, 9... Pump, 10... Discharge pipe, 11... Storage tank, 12... Suction 11.13... Suction pipe, 14... Pump, 15... 111 Outlet pipe, 16... Stirring Mechanism, 17.
・Motor, 18... Co-rotating shaft, 19... Scraping plate, 20, 22
,23.24...Arrow.

Claims (1)

【特許請求の範囲】[Claims] 1、 はぼ円筒状の周壁を有する円形槽と、沈殿分離し
た固形物を多量に含む固形分液を吸出して排出する固形
分液排出機構と、固形物を分離した後の処理済液を排出
する処理済液排出桟構とを備え、前記円形槽の周壁には
、被処理液を流入せしめる流入路を設け、前記円形槽の
槽底のほぼ中央部に西面を設け、前記固形分液排出機構
の固形分液吸込口を前記凹所に臨ましめ、前記円形槽の
ほぼ中央に、唾直軸を中心に回転する掻板を有する攪は
ん機構を備えたことを特徴とする固形物分離装置。
1. A circular tank with a roughly cylindrical peripheral wall, a solids liquid discharge mechanism that sucks out and discharges a solid liquid containing a large amount of precipitated and separated solids, and a system that discharges the treated liquid after separating the solids. The peripheral wall of the circular tank is provided with an inflow path through which the liquid to be treated flows in, and the west face is provided at approximately the center of the bottom of the circular tank, and the solid liquid is discharged from the solid liquid. The solid liquid suction port of the discharge mechanism faces the recess, and a stirring mechanism is provided approximately in the center of the circular tank, the stirring mechanism having a scraping plate that rotates around the vertical axis of the saliva. material separation equipment.
JP12798483A 1983-07-15 1983-07-15 Solid separating apparatus Pending JPS6022912A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP12798483A JPS6022912A (en) 1983-07-15 1983-07-15 Solid separating apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12798483A JPS6022912A (en) 1983-07-15 1983-07-15 Solid separating apparatus

Publications (1)

Publication Number Publication Date
JPS6022912A true JPS6022912A (en) 1985-02-05

Family

ID=14973565

Family Applications (1)

Application Number Title Priority Date Filing Date
JP12798483A Pending JPS6022912A (en) 1983-07-15 1983-07-15 Solid separating apparatus

Country Status (1)

Country Link
JP (1) JPS6022912A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61278311A (en) * 1985-06-04 1986-12-09 Ebara Corp Solid/liquid separator
JPS6249919A (en) * 1985-08-29 1987-03-04 Tetsuo Nishida Solid-liquid separator
JPS62171720A (en) * 1986-01-24 1987-07-28 Tetsuo Nishida Solid-liquid separator

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4910551A (en) * 1972-05-29 1974-01-30
JPS5318247A (en) * 1976-08-02 1978-02-20 Aida Some Koujiyou Goushi Sewage treating apparatus
JPS5347153A (en) * 1976-10-09 1978-04-27 Tadayuki Yoshida Separation of mud and sand from drain sludge

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4910551A (en) * 1972-05-29 1974-01-30
JPS5318247A (en) * 1976-08-02 1978-02-20 Aida Some Koujiyou Goushi Sewage treating apparatus
JPS5347153A (en) * 1976-10-09 1978-04-27 Tadayuki Yoshida Separation of mud and sand from drain sludge

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61278311A (en) * 1985-06-04 1986-12-09 Ebara Corp Solid/liquid separator
JPH0371162B2 (en) * 1985-06-04 1991-11-12 Ebara Mfg
JPS6249919A (en) * 1985-08-29 1987-03-04 Tetsuo Nishida Solid-liquid separator
JPH0371163B2 (en) * 1985-08-29 1991-11-12 Tetsuo Nishida
JPS62171720A (en) * 1986-01-24 1987-07-28 Tetsuo Nishida Solid-liquid separator
JPH0112525B2 (en) * 1986-01-24 1989-03-01 Tetsuo Nishida

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