JPS59186689A - Process and device for eliminating turbidity of turbid water by flocculation - Google Patents

Process and device for eliminating turbidity of turbid water by flocculation

Info

Publication number
JPS59186689A
JPS59186689A JP6254683A JP6254683A JPS59186689A JP S59186689 A JPS59186689 A JP S59186689A JP 6254683 A JP6254683 A JP 6254683A JP 6254683 A JP6254683 A JP 6254683A JP S59186689 A JPS59186689 A JP S59186689A
Authority
JP
Japan
Prior art keywords
tank
water
turbid water
perforated plates
turbidity
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
JP6254683A
Other languages
Japanese (ja)
Other versions
JPH0215275B2 (en
Inventor
Yoichi Hirose
洋一 広瀬
Nobuya Ishio
石尾 暢弥
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.)
Fuso Kensetsu Kogyo KK
Original Assignee
Fuso Kensetsu Kogyo 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 Fuso Kensetsu Kogyo KK filed Critical Fuso Kensetsu Kogyo KK
Priority to JP6254683A priority Critical patent/JPS59186689A/en
Publication of JPS59186689A publication Critical patent/JPS59186689A/en
Publication of JPH0215275B2 publication Critical patent/JPH0215275B2/ja
Granted legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D21/00Separation of suspended solid particles from liquids by sedimentation
    • B01D21/0039Settling tanks provided with contact surfaces, e.g. baffles, particles
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D21/00Separation of suspended solid particles from liquids by sedimentation
    • B01D21/003Sedimentation tanks provided with a plurality of compartments separated by a partition wall
    • B01D21/0033Vertical, perforated partition walls
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D21/00Separation of suspended solid particles from liquids by sedimentation
    • B01D21/02Settling tanks with single outlets for the separated liquid
    • B01D21/08Settling tanks with single outlets for the separated liquid provided with flocculating compartments
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D21/00Separation of suspended solid particles from liquids by sedimentation
    • B01D21/24Feed or discharge mechanisms for settling tanks
    • B01D21/2433Discharge mechanisms for floating particles
    • B01D21/2438Discharge mechanisms for floating particles provided with scrapers on the liquid surface for removing floating particles

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Separation Of Suspended Particles By Flocculating Agents (AREA)
  • Physical Water Treatments (AREA)

Abstract

PURPOSE:To eliminate turbidity from turbid water stably by allowing turbid water incorporated with a flucculating agent to flow downward through a floc forming tank provided with many arranged perforated plates to straighten the flow and to settle generated floc, then allowing the scum to float up by pressurization in a floatation tank. CONSTITUTION:Turbid water is supplied to a mixing tank 1 and stirred immediately and quickly together with a chemical such as flocculating agent (a) injected into the tank 1 using a quick stirring device 2. The stirred turbid water is supplied to a floc forming tank 4 through an orifice at the bottom of a partition wall 3. Many perforated plates 5 are provided vertically with an optional distance in the floc forming tank 4 in the direction for inhibiting downward flow of the turbid water. When the turbid water flows down through the group of the perforated plates, suspended matters in the turbid water are flocculated by the effect of the flocculating agent and flow downward through each hole of the perforated plates. When supernatant water in a flow straightening and settling tank 6 is supplied to the next floatation tank 8, suspended matters which are not settled in the settling tank 6 are floated by the effect of air bubbles released from pressurized water to form scum and are discharged out of the tank.

Description

【発明の詳細な説明】 本発町は上水道、工業用水路、下水道あるいは土木排水
、し尿処理、産業廃水処理等の懸濁水の凝集除濁全行う
方法及びその装置に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method and apparatus for the complete coagulation and turbidity removal of suspended water in water supplies, industrial waterways, sewers, civil engineering drainage, human waste treatment, industrial wastewater treatment, etc.

濁水中の濁質には無機性のものと有機性のもの(藻類等
)とがあシ、無機性のものは密度が大きいので沈降しや
すいが、有機性のものf′i密度が小さく離沈降性で、
むしろ浮上しやすい性質金もっている。通常の河川水で
は無機性の濁質が大半全占め、反対に湖沼水や冨栄養化
した貯留水では有機性の濁質が大半を占める場合が多い
。河川水であっても、渇水期、集中象雨時等により、季
節的に濁度が変化する場合がある。
There are two kinds of suspended matter in turbid water: inorganic matter and organic matter (algae, etc.); inorganic matter has a high density and tends to settle, but organic matter has a small Sedimentary,
Rather, it has the property of being easy to float. In normal river water, inorganic turbidity makes up most of the water, while in lake water and nutrient-rich reservoir water, organic turbidity often makes up the majority. Even in river water, the turbidity may change seasonally due to periods of drought, heavy rainfall, etc.

すなわち、渇水期には有機性の濁質が混在もしくは大部
分全方め、また集中豪雨等による濁度上昇時には濁質は
無機性のものが大部分である。凝集除濁装置としては凝
集沈澱装置が一般的に汎用されているが有機性の濁質が
混在する場合、難沈降性のフロックが処理水中に流出す
る現象がしばしばみられ、急速ろ過装置を後設する場合
、この流出フロックによってろ過装置の目詰まpを早め
る原因となっている。また従来の凝集沈澱装置が薬品混
和、フロック形成を含めて、4時間程度の滞留時間を必
要とする。
That is, during dry periods, organic turbidity is mixed or almost everywhere, and when turbidity increases due to localized heavy rain, most of the turbidity is inorganic. A coagulation-sedimentation device is generally used as a coagulation and clarification device, but when organic turbidity is present, difficult-to-settlement flocs often flow out into the treated water, and the rapid filtration device is not used after the rapid filtration device. When installed, the outflow flocs cause the filtration device to become clogged more quickly. Further, the conventional coagulation-sedimentation apparatus requires about 4 hours of residence time, including chemical mixing and floc formation.

本発明はこれに練みて従来の凝集沈澱装置にて濁水全処
理しでいる同程度の水質の処理を6〜数分の1の短時間
でしかも低濁度原水から高濁度原水1で、またさらに有
機性・無機性の濁)jlj、を問わず安定して除濁処理
を行わんとするもので、懸濁水に凝集剤を注入し、急速
撹拌せしめた後、これを多孔板を多数配列せしめたフロ
ック形成槽を流下せしめて所望のフロック形成し、次に
これを整流沈降せしめて一次除濁を行ない、且上澄水を
浮上分離槽へ導びき核種でスカム分を加圧浮上分離せし
めて濁質の二次除濁を行わしめるようになしたことを%
徴とする第一の発明と、濁水に凝集剤を注入し急速攪拌
するようになした混和槽に、多孔板を多数配列せしめた
多孔板フロック形成槽全瞬接し、核種Ic 7 口2り
を沈降せしめて一次除濁を行う整流沈降槽を設けると共
にこの整流沈降槽の上澄水を導びくようにして浮上分離
槽を配設し、該浮上分離槽にスカム分の浮上を助けるた
めの減圧気泡発生装置及び浮上スカムの掻寄掻取シによ
り二次除濁を行う汚泥掻取装置を設けて成ること全特徴
とする第二の発明とよシ成るものである。
The present invention takes advantage of this to achieve the same level of water quality as conventional coagulation and sedimentation equipment, which can treat all of the turbid water in 6 to 1/2 times the time, and with low to high turbidity raw water. In addition, the aim is to stably remove turbidity regardless of whether the turbidity is organic or inorganic, by injecting a flocculant into the suspended water and stirring it rapidly. The arrayed floc formation tanks are allowed to flow down to form desired flocs, which are then rectified and settled to perform primary clarification, and the supernatant water is led to a flotation tank where the scum is floated and separated under pressure using nuclides. % to perform secondary clarification of turbidity.
The first invention characterized in that a perforated plate flock forming tank in which a large number of perforated plates are arranged are brought into instant contact with a mixing tank in which a coagulant is injected into turbid water and rapidly stirred, and two ports of nuclide Ic 7 are collected. A rectifying sedimentation tank is provided to perform primary turbidity removal by sedimentation, and a flotation tank is installed to guide the supernatant water of this rectification sedimentation tank, and reduced-pressure bubbles are provided in the flotation tank to help float the scum. This invention is similar to the second invention, which is characterized in that it includes a generator and a sludge scraping device that performs secondary turbidity removal by scraping and scraping floating scum.

以下本発明全図示の実施例に基づいて巳明するO 下水−産業・工業・土木用廃水などの懸濁水(原水)全
混和槽1へ供給すると共に該槽内に注入される凝集剤等
の薬剤と急速攪拌装M2にて急速攪拌する。3はこの混
和槽1と瞬接された次のフロック形成槽4との間に設け
られた隔壁で、隔壁下部は開口され、混和槽1にて凝集
剤と攪拌された濁水をこの隔壁下部の開口より7oツク
Jfi成’fl’へ供給するようになす。このフロック
形成槽4には濁水の流下を妨げる方向に多数の多孔@5
が任意の間隔で垂設され、この多孔板5の群を流下する
時、濁水中の濁質はその凝集剤の作用にてフロック化さ
れつつしかもそのフロック化粧を成長させつつ多孔板の
各孔内全流下する。この場合多孔板の大きさ、形状は任
意とする。例えばフロック化しやすいように混和槽に近
い上流側の孔径を小、整流沈降槽に近い下流側の孔径を
大となるよう多孔板の上流側よシ下流側に向ってその孔
径を順次小径より大径となるようにして多孔板を配列し
たpl又は同じ孔径の多孔板をフロック形成槽の上流側
と下流°側に於て不等間隔となるように配列した9、各
板の穿孔位置全夫々異なるように配列したplさらには
穿孔位置を揃えたりして配列するが、この配列法もその
一例で限定されるものではない。この多数の多孔板が配
列されたフロック形成槽4の下流側には整流沈降槽6を
瞬接し・濁水中の濁質がフロック化粧としてフロック形
成槽4よリー該整−流沈降槽6へ供給されるようになす
。この整流沈降槽の底部には沈降したフロック化濁質を
槽外へ排出するための排泥v7を設置し、沈澱5死が一
定量に達すると定期的もしくは選択的任意に排出するよ
うになす。
The following description will be made based on the fully illustrated embodiments of the present invention. Sewage - Suspended water (raw water) such as industrial, industrial, and civil engineering wastewater is supplied to the mixing tank 1, and flocculants, etc., are injected into the tank. Rapidly stir the drug using rapid stirring device M2. Reference numeral 3 denotes a partition wall provided between this mixing tank 1 and the next flocculation tank 4 that is brought into instant contact. It is made to supply from the opening to the 7-hole Jfi input 'fl'. This floc formation tank 4 has many porous holes @ 5 in the direction that prevent the flow of turbid water.
are vertically arranged at arbitrary intervals, and when flowing down the group of perforated plates 5, the suspended solids in the turbid water are turned into flocs by the action of the coagulant, and the flocs are grown while flowing through each pore of the perforated plate. The entire inside flows down. In this case, the size and shape of the perforated plate are arbitrary. For example, in order to facilitate flocculation, the pore diameter is made smaller on the upstream side near the mixing tank, and the pore diameter on the downstream side near the rectification settling tank is made larger, so that the pore diameters are gradually made larger from the upstream side of the perforated plate toward the downstream side. PL, in which perforated plates are arranged so as to have the same diameter, or perforated plates with the same hole diameter are arranged at unequal intervals on the upstream and downstream sides of the flocculation tank 9, all the perforation positions on each plate. The differently arranged PLs are arranged by aligning the perforation positions, but this arrangement method is only one example and is not limited to this. A rectifying sedimentation tank 6 is connected instantaneously to the downstream side of the flocculation tank 4 in which a large number of perforated plates are arranged, and the turbidity in the turbid water is supplied from the flocculation tank 4 to the rectification sedimentation tank 6 as floc makeup. Do what you want. A sludge v7 is installed at the bottom of this rectification sedimentation tank to discharge the flocculated suspended solids out of the tank, and when a certain amount of sedimentation is reached, it is discharged periodically or selectively. .

この場合沈降フロック化濁質を集泥しやすいように僧底
部を船底形その他の形状とする。この整流沈降槽では高
濁度で沈降しゃすい無機性の濁質が主となる。そしてこ
の整流沈降槽でフロック化した濁質は沈降されて一次除
濁が行われるが、低濁度で有機性の濁質や沈降しなかっ
た濁質等は該沈降槽の上澄濁水を次の浮上分離槽8へ供
給する。この浮上分離槽8へ供給される上澄濁水は、浮
上分離槽の上流側に設けた隔板?内へ供給される。そし
てこの隔板9の下部は開口され、この開口よυ浮上分離
槽内へ導びかれるが、この場合核種の隔板下方に減圧気
泡発生装置10全設け、これに槽外に設けた加圧貯水槽
11よp加圧水を供給する。この加圧貯水槽11には浮
上分離槽にて浮上濁Ji(スカム)を除去した処理水又
は清浄水金加圧ポンプ12にて加圧して供給し、核種1
1にコンプレッサ−16よシ加圧空気を供給し、加圧下
にて空気を溶存せしめ、これ全加圧水供給管14を経て
減圧気泡装flit 10より分離槽内へ噴出せしめる
と加圧水中に溶存していた空気は減圧によって気泡とな
シ分離槽内を浮上する。この時上澄濁水中に含1れる低
濁度で有機性の濁質が浮上し槽上液面に浮遊しスカムと
なる。この浮遊スカムは浮上分離槽上部に設けられた汚
泥(スカム)掻寄装置15にて掻き寄せられ、槽外へ排
出さレルと共にこの濁質全分離した処理水はストレーナ
16を介して排水されるものである。
In this case, the bottom part is shaped like a ship's bottom or some other shape to facilitate the collection of settled flocculated suspended solids. In this rectified sedimentation tank, the main material is inorganic turbid matter that has high turbidity and settles easily. The flocculated turbidity is settled in this rectification sedimentation tank and primary clarification is carried out, but organic turbidity with low turbidity and turbidity that has not settled is transferred to the upper clear turbid water of the sedimentation tank. is supplied to the flotation separation tank 8. The supernatant turbid water supplied to this flotation tank 8 is separated by a partition plate provided on the upstream side of the flotation tank. supplied within. The lower part of the partition plate 9 is opened, and the nuclide is guided into the υ flotation separation tank through this opening. Pressurized water is supplied from the water storage tank 11. This pressurized water storage tank 11 is supplied with treated water from which floating turbidity Ji (scum) has been removed in a flotation separation tank or purified water pressurized with a gold pressurization pump 12, and is supplied with nuclide 1.
1 is supplied with pressurized air from a compressor 16, the air is dissolved under pressure, and when the air is blown out into the separation tank from the vacuum bubble device flit 10 through the pressurized water supply pipe 14, the air is dissolved in the pressurized water. Due to the reduced pressure, the air becomes bubbles and floats up inside the separation tank. At this time, organic turbid substances with low turbidity contained in the supernatant turbid water float to the surface and become scum on the upper liquid surface of the tank. This floating scum is scraped up by a sludge scraping device 15 installed at the top of the flotation separation tank and discharged to the outside of the tank.The treated water from which all turbidity has been separated is drained through a strainer 16. It is something.

実施例 上表の処理条件で濁水を処理するように設定し混和槽よ
りフロック形成槽、整流沈降槽、浮上分離槽を順次流下
せしめて濁水処理全行った結果法の如き効果を得た。
EXAMPLE The treatment conditions of the above table were set to treat turbid water, and the flow was sequentially flowed from the mixing tank to the flocculation tank, the rectifying sedimentation tank, and the flotation separation tank to completely treat the turbid water. As a result, an effect similar to that of the method was obtained.

而して本発明による時は従来法に比べ極めて短時間に濁
水の処理が行えると共に低濁度原水から高濁度原水まで
、有機性・無機性とい9濁寅のIii、ヲ問わず、安定
して除濁がイテえる等の利点を有する。
Therefore, when using the present invention, it is possible to treat turbid water in an extremely short time compared to conventional methods, and it is stable regardless of whether it is organic or inorganic, from low turbidity raw water to high turbidity raw water. It has the advantage of being able to remove turbidity.

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

図面は本発明濁水の凝集除濁装置を示す概略図である。 1・・・混和槽 2・・・@速攪拌装置 6、9・・・ViA壁 4・・・ブロック形成槽 5・・・多孔板 6・・・整流沈降槽 7・・・排泥管 8・・・浮上分離槽 10・・・減圧気泡発生装置 11・・・加圧貯水槽 12・・・カロ圧ホ゛ンブ 1ろ・・・コンプレッサー 14・・・加圧水供給管 15・・・汚泥掻寄装置 16・・・ストレーナ (外1名 The drawing is a schematic view showing the apparatus for coagulating and removing turbidity of turbid water according to the present invention. 1...Mixing tank 2...@speed stirring device 6, 9...ViA wall 4...Block forming tank 5... Perforated plate 6... Rectifier settling tank 7...Sludge drainage pipe 8...Flotation separation tank 10... Decompression bubble generator 11... Pressurized water tank 12...Calorie pressure horn 1ro...compressor 14... Pressurized water supply pipe 15...Sludge scraping device 16...Strainer (1 other person

Claims (2)

【特許請求の範囲】[Claims] (1)懸濁水に凝集剤を注入し、急速攪拌せしめた後・
これを多孔板を多数配列せしめたフロック形成槽を流下
せしめて所望のフロックを形成し、次にこれを整流沈降
せしめて一次除濁を行ない・且上澄水を浮上分離槽へ導
びき核種でスカム分を加圧浮上分離せしめて濁質の二次
除濁を行わしめるようになしたことを特徴とする濁水の
凝集除濁法。
(1) After injecting the flocculant into the suspended water and stirring rapidly,
This is flowed down a floc formation tank with a large number of perforated plates arranged to form the desired flocs, and then rectified and settled to perform primary clarification.The supernatant water is then led to a flotation separation tank to scum with nuclides. A coagulation and clarification method for turbid water, characterized in that secondary clarification of turbidity is carried out by flotation separation under pressure.
(2)濁水に凝集剤全注入し急速攪拌するようになした
混和槽に、多孔板全多数配列せしめた多孔板フロック形
成槽を臨接し、核種にフロックを沈降せしめて一次除濁
を行う整流沈降槽を設けると共にこの整流沈降槽の上澄
水を導ひくようにして浮上分離槽を配設し、該【フニ上
分喘槽にスカム分の浮上を助けるための減圧気泡発生装
置及び浮上スカムの掻寄掻取シによシニ次除濁を行う汚
泥掻取装置を設けて成る濁水の凝集除濁装置。
(2) A perforated plate flocculation tank in which a large number of perforated plates are arranged is placed adjacent to a mixing tank in which all of the coagulant is injected into turbid water and rapidly stirred, and rectification is performed to precipitate flocs on nuclides and perform primary clarification. A sedimentation tank is provided, and a flotation separation tank is installed to guide the supernatant water of this rectification sedimentation tank, and a decompression bubble generator to help float the scum to the upper separation tank and a floating scum removal tank are installed. A turbid water coagulation and clarification device that is equipped with a sludge scraping device that performs sludge removal using a scraper.
JP6254683A 1983-04-08 1983-04-08 Process and device for eliminating turbidity of turbid water by flocculation Granted JPS59186689A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6254683A JPS59186689A (en) 1983-04-08 1983-04-08 Process and device for eliminating turbidity of turbid water by flocculation

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6254683A JPS59186689A (en) 1983-04-08 1983-04-08 Process and device for eliminating turbidity of turbid water by flocculation

Publications (2)

Publication Number Publication Date
JPS59186689A true JPS59186689A (en) 1984-10-23
JPH0215275B2 JPH0215275B2 (en) 1990-04-11

Family

ID=13203339

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6254683A Granted JPS59186689A (en) 1983-04-08 1983-04-08 Process and device for eliminating turbidity of turbid water by flocculation

Country Status (1)

Country Link
JP (1) JPS59186689A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH09327601A (en) * 1996-06-12 1997-12-22 Maezawa Ind Inc Method and apparatus for solid-liquid separation
JP2010527286A (en) * 2007-05-18 2010-08-12 オテヴェ・ソシエテ・アノニム Water treatment facility and method by flotation separation
CN102774922A (en) * 2012-08-20 2012-11-14 宜兴市富陶环境保护设备有限公司 Gas floating device
JP2013146685A (en) * 2012-01-19 2013-08-01 Nippon Solid Co Ltd Transverse flow sedimentation basin in which ceiling is lidded
JP6584688B1 (en) * 2018-04-13 2019-10-02 三菱電機株式会社 Water circulation circuit system
JP2021013881A (en) * 2019-07-11 2021-02-12 株式会社楢崎製作所 Turbid water treatment device and turbid water treatment method

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH09327601A (en) * 1996-06-12 1997-12-22 Maezawa Ind Inc Method and apparatus for solid-liquid separation
JP2010527286A (en) * 2007-05-18 2010-08-12 オテヴェ・ソシエテ・アノニム Water treatment facility and method by flotation separation
JP2013146685A (en) * 2012-01-19 2013-08-01 Nippon Solid Co Ltd Transverse flow sedimentation basin in which ceiling is lidded
CN102774922A (en) * 2012-08-20 2012-11-14 宜兴市富陶环境保护设备有限公司 Gas floating device
JP6584688B1 (en) * 2018-04-13 2019-10-02 三菱電機株式会社 Water circulation circuit system
WO2019198227A1 (en) * 2018-04-13 2019-10-17 三菱電機株式会社 Foreign matter trapping device and water circulation circuit comprising foreign matter trapping device
JP2021013881A (en) * 2019-07-11 2021-02-12 株式会社楢崎製作所 Turbid water treatment device and turbid water treatment method

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