JPH0720596B2 - Contaminated water treatment method - Google Patents

Contaminated water treatment method

Info

Publication number
JPH0720596B2
JPH0720596B2 JP14559989A JP14559989A JPH0720596B2 JP H0720596 B2 JPH0720596 B2 JP H0720596B2 JP 14559989 A JP14559989 A JP 14559989A JP 14559989 A JP14559989 A JP 14559989A JP H0720596 B2 JPH0720596 B2 JP H0720596B2
Authority
JP
Japan
Prior art keywords
water
aeration
area
stirring
particles
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 - Fee Related
Application number
JP14559989A
Other languages
Japanese (ja)
Other versions
JPH0312300A (en
Inventor
一 伊藤
秀実 長川
忠洋 森
Original Assignee
日立機電工業株式会社
忠洋 森
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 日立機電工業株式会社, 忠洋 森 filed Critical 日立機電工業株式会社
Priority to JP14559989A priority Critical patent/JPH0720596B2/en
Publication of JPH0312300A publication Critical patent/JPH0312300A/en
Publication of JPH0720596B2 publication Critical patent/JPH0720596B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、汚濁した河口域、河川、湖沼、池、堀等の水
域を効率的に浄化する汚濁水域の処理法に関するもので
ある。
TECHNICAL FIELD The present invention relates to a method for treating a polluted water area for efficiently purifying a polluted estuary area, a river, a lake, a pond, a moat, or the like.

〔従来の技術〕[Conventional technology]

河口域、河川、湖沼、池、堀等の汚濁した水域におい
て、外部から流入する汚染物質と、水底に堆積した泥か
ら溶出する汚濁物質が起因となって水質汚濁が進行す
る。特に、水底に堆積した泥が分解すると窒素、燐など
の栄養塩が溶出し、藻類が多量に発生し易い状況を生み
出す。その結果、透視度を著しく低下させ、さらに、こ
れらの藻類は沈澱して水底に堆積し、それが分解すると
溶出する栄養塩のために再び藻類が増殖するという悪循
環を繰り返している。
In polluted waters such as estuaries, rivers, lakes, ponds, and moats, water pollution progresses due to pollutants flowing in from the outside and pollutants eluted from mud accumulated on the bottom of the water. In particular, when the mud deposited on the bottom of the water is decomposed, nutrient salts such as nitrogen and phosphorus are eluted, and a large amount of algae is likely to be generated. As a result, the visibility is remarkably reduced, and further, these algae precipitate and accumulate on the bottom of the water, and when they decompose, the algae grow again due to the nutrient salts that elute, which repeats a vicious cycle.

水中の酸素は好気性バクテリアが汚濁物質を分解すると
きに多量に消費される。酸素は日中、藻類の光合成によ
って水中に供給されるが、雨天時や夜間は光合成が停止
し、呼吸のみ行なうようになり、逆に酸素が消費され、
水底に堆積した泥が嫌気的になり、汚濁が進行する。
Oxygen in water is consumed in large quantities when aerobic bacteria decompose pollutants. Oxygen is supplied to the water during the daytime by photosynthesis of algae, but during rainy weather or at night, photosynthesis stops and only breathing occurs, and oxygen is consumed on the contrary,
Mud accumulated on the bottom of the water becomes anaerobic and pollution progresses.

また、この水域内における水中の有機物質を好気性分解
処理するため、水域内の水を曝気、攪拌する方法が「曝
気による河川浄化に関する研究」(第26回下水道研究発
表会講演集)に示すように提案され、河川の自浄係数向
上、臭気発生防止などに効果があることが実証されてい
る。
Moreover, in order to aerobically decompose the organic substances in the water in this water area, the method of aerating and stirring the water in the water area is shown in "Study on river purification by aeration" (The 26th Sewer Research Conference Lecture) It has been demonstrated that it is effective in improving the self-cleaning coefficient of rivers and preventing odors.

〔発明が解決しようとする課題〕[Problems to be Solved by the Invention]

上記方式によれば、水、水域内において、曝気と攪拌を
同時に行なうことにより、水及び水底に堆積した泥に酸
素を供給することができるので、そこに存在する汚濁物
質、とくに有機物の好気性分解を促進することができ
る。
According to the above method, oxygen can be supplied to the water and the mud accumulated on the bottom by simultaneously performing aeration and stirring in the water and the water area. The decomposition can be accelerated.

しかし、上記方法によっても、水中に浮遊している汚濁
物や藻類は互いの粒子がその表面に同じ電荷(通常は
負)を帯びているため、粒子は互いに反発し合って沈澱
することがないので、透視度は改善しないという問題点
を有していた。
However, even by the above method, the particles and the algae floating in water have the same electric charge (usually negative) on the surface, so that the particles do not repel each other and precipitate. Therefore, there is a problem that the transparency is not improved.

本発明は、汚濁した水域の水中に浮遊している汚濁物や
藻類等の極めて沈降しにくく水の透視度を低下させる粒
子をフロック化して沈澱させ、沈澱した沈澱物を好気的
に分解して透明な水質を得ることを可能にする汚濁水域
の処理方法を提供することを目的とする。
The present invention flocculates particles suspended in the water of a polluted water area such as pollutants and algae that are extremely difficult to settle and reduces the transparency of water to precipitate them, and aerobically decomposes the precipitated precipitates. It is an object of the present invention to provide a method for treating a polluted water area, which makes it possible to obtain transparent water quality.

〔課題を解決するための手段〕[Means for Solving the Problems]

上記目的を達成するため、本発明の汚濁水域の処理法
は、汚濁した水域の水中に設置した曝気攪拌装置により
水平方向の水流を起こして曝気と攪拌を同時に行ない溶
解性有機物等の汚濁物質を分解するとともに、水中に浮
遊している汚濁物や藻類等の極めて沈降しにくく水の透
視度を低下させる粒子に対し、前記曝気攪拌装置の急速
攪拌領域に凝集剤を添加し、水域内の緩速攪拌領域で前
記粒子をフロック化して沈澱させ、沈澱した沈澱物を好
気的に分解して透明な水質を得ることを要旨とする。
In order to achieve the above object, the method for treating a polluted water area of the present invention is a method for causing a horizontal water flow by an aeration stirring device installed in the water of a polluted water area to simultaneously perform aeration and stirring to dissolve pollutants such as soluble organic substances. For particles that decompose and are less likely to sediment such as pollutants and algae that are suspended in water and reduce the transparency of water, add a coagulant to the rapid stirring area of the aeration stirrer to reduce the The gist of the present invention is to flocculate the particles in a rapid stirring region to cause precipitation, and aerobically decompose the precipitated precipitate to obtain transparent water quality.

〔実施例〕〔Example〕

以下本発明を図示の実施例に基づいて説明する。 The present invention will be described below based on the illustrated embodiments.

図において1は池で、幅28m、長さ30mの大きさを有し、
この池1内に第1図に示すように池内の水を攪拌し、水
平方向の水流を起こして循環水流が生じるよう池の対角
線上に2台の曝気攪拌装置2,2を設置する。
In the figure, 1 is a pond having a width of 28 m and a length of 30 m,
As shown in FIG. 1, water in the pond is stirred in the pond 1 and two aeration stirring devices 2, 2 are installed on the diagonal of the pond so that a horizontal water flow is generated and a circulating water flow is generated.

この曝気攪拌装置2は水域の水の曝気をも行なわしめる
もので、各種のものを採用できる。この曝気攪拌装置2
のモータ容量を2,2KWとすると、曝気攪拌装置の汚水の
攪拌部又は攪拌直後の領域での流速は1m/secとなり、急
速攪拌される。また他の水域内での流速は15cm/secの緩
速攪拌領域となる。そして曝気攪拌装置2のモータをイ
ンバータ制御等により、その回転数を制御することによ
り各領域の流速を調整可能とする。
This aeration and agitation device 2 also aerates the water in the water area, and various types can be adopted. This aeration stirring device 2
If the motor capacity of 2 is set to 2.2 KW, the flow velocity in the agitating part of the aeration agitating device or the region immediately after agitation becomes 1 m / sec, and rapid agitation is performed. In addition, the flow velocity in other water areas is a slow stirring area of 15 cm / sec. Then, the motor of the aeration and agitation device 2 is controlled by an inverter or the like to control the number of revolutions thereof so that the flow velocity in each region can be adjusted.

このように水域に曝気攪拌装置2を設け、水域内の水を
攪拌曝気すると、水中に酸素が供給され、これにより溶
解性有機物等の懸濁物質は好気分解を受ける。
As described above, when the aeration and agitation device 2 is provided in the water area and the water in the water area is agitated and aerated, oxygen is supplied into the water, whereby suspended substances such as soluble organic substances undergo aerobic decomposition.

ところで、水中に浮遊している汚濁物や藻類等の粒子
は、その表面に同じ電荷(通常は負)を帯びているた
め、互いに反発し合って浮遊し、なかなか沈澱しない。
この沈澱を促進するため、曝気攪拌装置2の急速攪拌領
域3において、すなわち、曝気攪拌装置2の曝気部に凝
集剤4を添加し、急速攪拌と同時に曝気を行なうことに
より粒子と凝集剤を効率よく接触させて粒子表面の電荷
を中和する。その後、緩速攪拌領域で粒子をフロック化
させ、曝気攪拌装置2の停止により沈澱させる。沈澱物
は放置しておけば分解し、汚濁物質が溶出し、水質汚濁
の悪循環を繰り返すことになるが、曝気攪拌装置2より
供給される酸素によって、沈澱した沈殿物は好気的に分
解され、汚濁物質や窒素、燐などの栄養塩の溶出を阻止
して、藻類の増殖を抑制できるものである。
By the way, since particles such as pollutants and algae floating in water have the same electric charge (usually negative) on their surfaces, they repel each other and float, and do not easily settle.
In order to accelerate this precipitation, the flocculant 4 is added in the rapid stirring region 3 of the aeration stirring device 2, that is, to the aeration part of the aeration stirring device 2, and the aeration is performed simultaneously with the rapid stirring, so that the particles and the aggregating agent are efficiently treated. Contact well to neutralize the charge on the particle surface. After that, the particles are flocculated in the slow-speed stirring region, and the particles are precipitated by stopping the aeration and stirring device 2. The precipitate decomposes if left to stand, pollutants elute and the vicious cycle of water pollution repeats. However, the oxygen supplied from the aeration and agitation device 2 decomposes the precipitate aerobically. It is possible to suppress the elution of pollutants and nutrient salts such as nitrogen and phosphorus to suppress the growth of algae.

なお、急速攪拌領域3での凝集剤4の添加は約1〜2時
間行ない、添加終了後、曝気攪拌装置2を約1時間運転
して緩速攪拌を行なった後、曝気攪拌装置3を停止す
る。
The flocculating agent 4 is added in the rapid stirring region 3 for about 1 to 2 hours, and after the addition is completed, the aeration stirring device 2 is operated for about 1 hour to perform slow stirring, and then the aeration stirring device 3 is stopped. To do.

急速攪拌領域3にて凝集剤4を添加して急速攪拌する時
間T1[H]及び添加終了後、曝気攪拌装置を停止させる
までの緩速攪拌時間T2[H]は水の性状に応じて適正に
調整するものとする。
The time T1 [H] for adding the flocculant 4 in the rapid stirring area 3 and rapid stirring and the slow stirring time T2 [H] for stopping the aeration stirring device after the addition is appropriate according to the nature of water. Shall be adjusted.

急速攪拌時間T1[H]は水域内の水が全て攪拌部と接触
する時間と考えることができる。
The rapid stirring time T1 [H] can be considered as the time during which all the water in the water area contacts the stirring section.

攪拌部での流速v[m/sec]、流路断面をφD[m]と
すると、攪拌流量Q[m3H]は、 水域の水容量をV[m3]とするとT1[H] 緩速攪拌時間T2[H]は、実験室規模での実験によると
約10分で殆どフロック化が終了しており、20分以上に設
定すれば充分フロック化が行なわれる。
Assuming that the flow velocity v [m / sec] in the stirring section and the flow passage cross section is φD [m], the stirring flow rate Q [m 3 H] is If the water capacity of the water area is V [m 3 ], then T 1 [H] According to the experiment on a laboratory scale, the slow stirring time T2 [H] almost completes the flocculation in about 10 minutes, and if it is set to 20 minutes or more, the flocculation is sufficiently performed.

なお、上記急速攪拌領域3で添加される凝集剤4として
はカチオン系合成ポリマー、アニオン系合成ポリマー、
ノニオン系合成ポリマー、キトサン等が使用され、この
凝縮剤の添加濃度に対する透明度との関係を第3図に示
す。この判定結果により凝集剤の濃度は最も上澄水の透
明度が良くなる2mg/l前後の価とするが、これは使用す
する凝集剤の種別や汚水濃度によっても変わるものであ
る。
As the aggregating agent 4 added in the rapid stirring region 3, a cationic synthetic polymer, an anionic synthetic polymer,
Nonionic synthetic polymers, chitosan and the like are used, and the relationship between the added concentration of the condensing agent and the transparency is shown in FIG. Based on this determination result, the concentration of the flocculant is set to a value of around 2 mg / l, which gives the best clarity of the supernatant water, but this varies depending on the type of flocculant used and the concentration of sewage.

第3図より、前記の如き水域の水に対してはカチオン系
合成ポリマーとキトサンが有効であるが、最も透明度が
良くなる添加率においてカチオン系合成ポリマーはキト
サンの2倍必要であり、経済性においてキトサンが優れ
ている。
As shown in FIG. 3, the cationic synthetic polymer and chitosan are effective for the water in the above-mentioned water area, but the cationic synthetic polymer needs to be twice as much as the chitosan at the addition rate that gives the best transparency, and the economical efficiency is improved. Chitosan is excellent in.

このキトサンはエビやカニの殻等に含まれる生体高分子
キチンをアルカリ処理したもので、魚類等、生物に対す
る毒性が全く無く生態系で分解され易く、他の合成ポリ
マーに比べ安全性が高いものである。
This chitosan is made by treating the biopolymer chitin contained in the shells of shrimp and crab with alkali, has no toxicity to living organisms such as fish, is easily decomposed in the ecosystem, and has a higher safety than other synthetic polymers. Is.

なお、凝集剤として前述の如き合成ポリマーが使用され
るが、水域に対する安全性及び経済性を考慮するとカニ
の甲羅等から抽出されて生成される天然高分子凝集剤キ
トサンを使用することが好ましい。
Although the synthetic polymer as described above is used as the flocculant, it is preferable to use the natural polymer flocculant chitosan, which is produced by being extracted from the shell of a crab or the like, in consideration of the safety and the economical efficiency for water bodies.

さらに、急速攪拌時に曝気を併用することにより、第5
図に示すように凝集性を向上させることができる。
Furthermore, by using aeration together with rapid stirring, the fifth
As shown in the figure, the cohesiveness can be improved.

水域の底部に沈澱した粒子は、水域の中央等に集まるよ
うに曝気攪拌装置2の起こす水流の方向を調整し、この
沈澱物(汚泥)を水中ポンプ等にて吸泥排出することも
可能である。
It is also possible to adjust the direction of the water flow caused by the aeration and agitation device 2 so that the particles settled at the bottom of the water area gather in the center of the water area, and this sediment (sludge) can be absorbed and discharged by an underwater pump or the like. is there.

〔発明の効果〕 本発明によれば、曝気攪拌装置の急速攪拌領域に凝集剤
を添加するため水中に浮遊している粒子と凝集剤を効率
よく接触させることができ、さらに、この粒子を水域内
の緩速攪拌領域でフロック化して沈澱させ、沈澱した沈
澱物を曝気攪拌装置より供給される酸素によって好気的
に分解することができ、これにより、溶解性有機物等の
曝気処理を行いながら、簡易な方法で汚濁水域の透視度
を向上することができる。
[Effect of the Invention] According to the present invention, since the flocculant is added to the rapid stirring region of the aeration stirrer, the particles floating in water and the flocculant can be efficiently brought into contact with each other. Flocculates and precipitates in the slow stirring area inside, and the precipitated precipitate can be aerobically decomposed by the oxygen supplied from the aeration stirring device, which enables aeration treatment of soluble organic substances, etc. The transparency of polluted water can be improved by a simple method.

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

第1図は閉鎖性水域に曝気攪拌装置を設置した状態の平
面図、第2図はその縦断面図、第3図は凝集剤の添加率
と透明度との関係を示すグラフ図、第4図は閉鎖性水域
での水の汚濁を説明するフローチャート、第5図は曝気
の有無と凝集性との関係を示すグラフである。 1は池、2は曝気攪拌装置、3は急速攪拌領域、4は凝
集剤。
FIG. 1 is a plan view showing a state where an aeration and agitation device is installed in a closed water area, FIG. 2 is a longitudinal sectional view thereof, and FIG. 3 is a graph showing the relationship between the coagulant addition rate and transparency, and FIG. Is a flow chart for explaining water pollution in a closed water area, and FIG. 5 is a graph showing the relationship between the presence or absence of aeration and cohesiveness. 1 is a pond, 2 is an aeration stirring device, 3 is a rapid stirring region, 4 is a flocculant.

───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 昭61−136496(JP,A) 特開 昭63−171699(JP,A) ─────────────────────────────────────────────────── --Continued from the front page (56) References JP-A-61-136496 (JP, A) JP-A-63-171699 (JP, A)

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】汚濁した水域の水中に設置した曝気攪拌装
置により水平方向の水流を起こして曝気と攪拌を同時に
行ない溶解性有機物等の汚濁物質を分解するとともに、
水中に浮遊している汚濁物や藻類等の極めて沈降しにく
く水の透視度を低下させる粒子に対し、前記曝気攪拌装
置の急速攪拌領域に凝集剤を添加し、水域内の緩速攪拌
領域で前記粒子をフロック化して沈澱させ、沈澱した沈
澱物を好気的に分解して透明な水質を得ることを特徴と
する汚濁水域の処理法。
1. An aeration and agitation device installed in the water of a polluted water area causes a horizontal water flow to aerate and agitate simultaneously to decompose pollutants such as soluble organic substances, and
For particles such as contaminants and algae that are suspended in water that are extremely unlikely to settle and reduce the visibility of water, add a coagulant to the rapid stirring area of the aeration stirring device, and in the slow stirring area within the water area. A method for treating a polluted water area, characterized in that the particles are flocculated and precipitated, and the precipitated precipitate is aerobically decomposed to obtain transparent water quality.
JP14559989A 1989-06-08 1989-06-08 Contaminated water treatment method Expired - Fee Related JPH0720596B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP14559989A JPH0720596B2 (en) 1989-06-08 1989-06-08 Contaminated water treatment method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP14559989A JPH0720596B2 (en) 1989-06-08 1989-06-08 Contaminated water treatment method

Publications (2)

Publication Number Publication Date
JPH0312300A JPH0312300A (en) 1991-01-21
JPH0720596B2 true JPH0720596B2 (en) 1995-03-08

Family

ID=15388788

Family Applications (1)

Application Number Title Priority Date Filing Date
JP14559989A Expired - Fee Related JPH0720596B2 (en) 1989-06-08 1989-06-08 Contaminated water treatment method

Country Status (1)

Country Link
JP (1) JPH0720596B2 (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH06285462A (en) * 1992-05-01 1994-10-11 Mito Kogyo Kk Apparatus for purifying reservoir
KR100360542B1 (en) * 1999-08-05 2002-11-13 보성중공업주식회사 method for purificationing a waste water and apparatus for performing the same
JP4655279B2 (en) * 2006-02-15 2011-03-23 特定非営利活動法人まちなみ育成会 Natural material water purification coagulating sedimentation agent
JP6258277B2 (en) * 2014-10-15 2018-01-10 アクアサービス株式会社 Water purification method and water purification system

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61136496A (en) * 1984-12-06 1986-06-24 Ebara Infilco Co Ltd Apparatus for preventing eutrophication
JPS63171699A (en) * 1987-01-07 1988-07-15 Shin Meiwa Ind Co Ltd Aeration system for pond or the like

Also Published As

Publication number Publication date
JPH0312300A (en) 1991-01-21

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