JP2003117562A - Active cleaning equipment for water and bottom sediment of water area - Google Patents

Active cleaning equipment for water and bottom sediment of water area

Info

Publication number
JP2003117562A
JP2003117562A JP2001318891A JP2001318891A JP2003117562A JP 2003117562 A JP2003117562 A JP 2003117562A JP 2001318891 A JP2001318891 A JP 2001318891A JP 2001318891 A JP2001318891 A JP 2001318891A JP 2003117562 A JP2003117562 A JP 2003117562A
Authority
JP
Japan
Prior art keywords
water
agent
mixing
tank
separation
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
JP2001318891A
Other languages
Japanese (ja)
Inventor
Ryoichi Maeda
涼一 前田
Etsuro Moriyama
越郎 森山
Susumu Yoshida
將 吉田
Koji Yokoyama
浩司 横山
Ichiro Osugi
一郎 大杉
Kenji Naeki
謙二 苗木
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.)
Toray Engineering Co Ltd
Original Assignee
Toyo Construction Co Ltd
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 Toyo Construction Co Ltd filed Critical Toyo Construction Co Ltd
Priority to JP2001318891A priority Critical patent/JP2003117562A/en
Publication of JP2003117562A publication Critical patent/JP2003117562A/en
Pending 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

Abstract

PROBLEM TO BE SOLVED: To provide an equipment for performing an active cleaning treatment of water and bottom sediment in watersides existing nearby in living, such as ponds of shrines, temples and parks, moats, reservoirs, and lakes and ponds, or in water areas, such as ponds of golf courses. SOLUTION: This equipment for active cleaning of the water and bottom sediment of the water areas is used by injecting a water active cleaning agent O into raw water containing the pollutants of the water areas, such as the ponds, mixing and agitating the raw water to flocculate the organic matter and nutrient salts mainly suspended and dissolved in the water, injecting fine air bubbles to floc to float and separate the floc by the fine air bubbles onto the water surface and to separate an remove the pollutants from the inside of the water and recovering and treating the floc.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明が属する技術分野】本願発明は主に池、堀、溜池
等の水域から汚濁物質を含む水質を活性浄化処理し、併
せて池底等に溜まる汚泥、浮遊泥等の底質を活性浄化処
理する技術の分野に属する。
TECHNICAL FIELD The present invention mainly purifies water containing pollutants from water bodies such as ponds, moats, and reservoirs, and purifies bottom sediment such as sludge and suspended mud. Belongs to the field of processing technology.

【0002】[0002]

【従来の技術】排水処理技術は、工場排水、家庭排水、
下水等の排水中から汚濁物質を除去して、排水基準値以
下にすることである。汚濁物質は、有機性あるいは無機
性物質、懸濁性あるいは溶解性物質、有害性の有無、あ
るいは無機栄養塩類等があるが、これらの汚濁物質の性
質や濃度に応じて、各種の、例えば、物理化学的処理や
生物学的処理、あるいはこれらの組み合わせ的な処理が
行われてきた。
2. Description of the Related Art Wastewater treatment technologies include factory wastewater, domestic wastewater,
It is to remove pollutants from wastewater such as sewage so that the wastewater falls below the standard value. Pollutants include organic or inorganic substances, suspending or dissolving substances, presence or absence of harmfulness, inorganic nutrient salts, etc., depending on the nature and concentration of these pollutants, various, for example, Physicochemical treatment, biological treatment, or a combination of these treatments has been performed.

【0003】これらの処理により、固液分離、有機物や
還元性物質の酸化、PHの調節、有害物質や無機栄養塩
類(主としてリン、窒素化合物)の除去、生成汚泥の処
理、処分が行われることとなる。例えば、有機性排水で
は、先ず懸濁性物質を含む場合には、固液分離により懸
濁性物質を除去し、除去後に汚濁性物質の濃度が基準値
を超えている場合には通常は生物学的処理を行う。まだ
基準値を超えている場合は更に物理化学的処理を行う。
いかなる場合でも放流時には大腸菌群が基準値以下とす
るべく殺菌処理を行う。
By these treatments, solid-liquid separation, oxidation of organic substances and reducing substances, adjustment of PH, removal of harmful substances and inorganic nutrient salts (mainly phosphorus and nitrogen compounds), treatment and disposal of produced sludge. Becomes For example, in organic wastewater, when a suspending substance is contained first, the suspending substance is removed by solid-liquid separation, and when the concentration of the pollutant substance exceeds the standard value after the removal, it is usually a biological substance. Biological processing. If the standard value is still exceeded, further physicochemical treatment is performed.
In any case, sterilization is performed so that the coliform bacteria will be below the standard value at the time of discharge.

【0004】無機性排水では、懸濁性物質がある場合に
は固液分離を行い、更に有害物質がある場合は物理化学
的処理を施してその有害物質を固形物として分離する
か、無害化する。更に汚濁物質が基準値を超えている場
合は、吸着処理やイオン交換などの高度処理を行うこと
が必要になる。最終的には、排水基準の強化と共に、ダ
イオキシン、環境ホルモン等の微量有害物質の除去へと
排水処理の対象を拡大してゆくものである。
In the case of inorganic waste water, solid-liquid separation is carried out when there is a suspended substance, and physicochemical treatment is further carried out when there is a harmful substance to separate the harmful substance as a solid substance or to render it harmless. To do. Further, when the pollutant exceeds the standard value, it is necessary to perform advanced treatment such as adsorption treatment or ion exchange. Ultimately, along with strengthening wastewater standards, we will expand the scope of wastewater treatment to remove trace amounts of harmful substances such as dioxins and environmental hormones.

【0005】このように排水処理では、汚濁物質の濃度
や種類に応じて段階的に処理が行われ、便宜的に一次処
理、二次処理、三次処理(高度処理)と呼ばれている。
一次処理では主として懸濁性物質を物理的に除去する処
理、二次処理では生物学的に有機性物質を分解する処
理、三次処理では、二次処理で除去できなかったBO
D,COD、リン、窒素等を処理することを目指す。処
理コストは、高次処理ほど高価になるので、放流先の排
水基準に応じた処理プロセス選択することが重要であ
る。また設備の選定に当たっては、建設費、設備面積、
許容される設置面積、運転費、維持管理費、処理時間の
長短等の難易を考慮する必要がある。やたらに高度処理
を目指しても、コストや除去汚濁物質あたりの投入エネ
ルギーが高くなったり、プロセスの環境負荷を増大させ
る結果となることもある。
As described above, in the wastewater treatment, the treatment is performed stepwise according to the concentration and type of the pollutant, and for convenience, it is called primary treatment, secondary treatment, or tertiary treatment (advanced treatment).
The primary treatment mainly removes suspended solids physically, the secondary treatment biologically decomposes organic substances, and the tertiary treatment cannot remove BO by the secondary treatment.
Aim to treat D, COD, phosphorus, nitrogen, etc. Since the treatment cost becomes higher as the higher-order treatment is performed, it is important to select the treatment process according to the discharge standard of the discharge destination. When selecting equipment, construction cost, equipment area,
It is necessary to consider the difficulty such as allowable installation area, operating cost, maintenance cost, and length of processing time. Even if a high-level treatment is aimed at, the cost and the input energy per removed pollutant may increase and the environmental load of the process may increase.

【0006】[0006]

【発明が解決しようとする課題】このような事情に鑑
み、本願発明は、有機質に富んだ池、堀や溜池等の水域
で、簡単な装置で、しかも迅速に汚濁物質を除去して水
質を改善し、併せて池底の泥質等をも改善して、水域の
水質および底質を活性浄化する装置を提供することを目
的とするものである。
In view of the above circumstances, the present invention provides a water device such as a pond, a moat, or a pond rich in organic matter with a simple device and quickly removes pollutants to improve the water quality. It is an object of the present invention to provide an apparatus for improving the water quality and bottom quality of a water area by improving the water quality and bottom quality of the pond.

【0007】[0007]

【課題を解決するための手段】課題を解決するための本
願発明の第1のものは、水質活性浄化剤と、水質活性
浄化剤注入装置2と、混合攪拌装置4と、微細気泡発生
装置6と、浮上分離凝集物回収装置9とを少なくとも具
備する池等の水域の水質底質活性浄化装置であって、水
質活性浄化剤は、析出浄化剤01または凝集分離剤0
3を含み、水質活性浄化剤注入装置2は、析出浄化剤0
1または凝集分離剤03を選択的にまたは同時に注入可
能であって、水質に応じて、析出浄化剤01または凝集
分離剤03の一方または両者を同時に、または一方の後
に他方を順序付けて水域の汚濁物質を含む原水中に注入
し、混合攪拌装置4により混合攪拌することにより、汚
濁物質である水中のアオコ、有機物、土粒子等の懸濁粒
子を凝集し、溶解している有機物、栄養塩類を析出凝集
して、大粒の塊である凝集物(フロック)化し、微細気
泡発生装置6は、微細気泡を発生し、前記微細気泡を水
面方向に付勢する方向で処理水中に導入して、凝集を促
進させると共に、前記凝集物を浮上分離凝集物10とし
て水面上に浮上分離させることにより水中から汚濁物質
を分離させ、浮上分離凝集物回収装置9により、前記浮
上分離凝集物10を回収する水域の水質底質活性浄化装
置である。
The first aspect of the present invention for solving the problem is to provide a water quality active cleaning agent 0 , a water quality active cleaning agent injecting device 2, a mixing and stirring device 4, and a fine bubble generating device. 6 and a flotation / separation / aggregate collection device 9 at least, which is a water bottom active purification device for a water area such as a pond, wherein the water purification agent 0 is a precipitation purification agent 01 or a flocculation separation agent 0.
3, the water quality active purifying agent injecting device 2 includes a precipitation purifying agent 0
1 or the coagulation / separation agent 03 can be selectively or simultaneously injected, and depending on the water quality, one or both of the precipitation purification agent 01 or the coagulation / separation agent 03 can be injected simultaneously, or one after the other can be sequenced to pollute the water area. By injecting into raw water containing a substance and mixing and stirring with a mixing and stirring device 4, suspended particles such as water-bloom, organic matter, and soil particles, which are pollutants, are aggregated to dissolve dissolved organic matter and nutrient salts. Precipitated and agglomerated to form agglomerates (flocs) that are large lumps, and the fine bubble generator 6 generates fine bubbles and introduces the fine bubbles into the treated water in a direction to urge the fine bubbles toward the water surface to agglomerate. And the flotation separation flocculates 10 are floated and separated on the water surface to separate contaminants from the water, and the flotation separation flocculates recovery device 9 causes the flotation separation flocculates 10 to be separated. A water sediment activity purification device of water for recovering.

【0008】課題を解決するための本願発明の第2のも
のは、水質活性浄化剤と、水質活性浄化剤注入装置2
と、混合攪拌装置4と、微細気泡発生装置6と、浮上分
離凝集物回収装置9と、原水汲上げ装置81と、清水放
流装置82と、混合攪拌槽51と、微細気泡付加槽52
と、浮上分離回収槽53とを少なくとも具備する池等の
水域の水質底質活性浄化装置であって、水質活性浄化剤
0は、析出浄化剤01または凝集分離剤03を含み、原
水汲上げ装置81は、汚濁物質を含む水域の原水や他の
排水を混合攪拌槽51中に汲入れ可能であり、水質活性
浄化剤注入装置2は、析出浄化剤01または凝集分離剤
03を選択的にまたは同時に注入可能であって、水質に
応じて、析出浄化剤01または凝集分離剤03の一方ま
たは両者を同時に、または一方の後に他方を順序付け
て、混合攪拌槽51中において、汚濁物質を含む原水中
に注入し、混合攪拌装置4により混合攪拌することによ
り、汚濁物質である水中のアオコ、有機物、土粒子等の
懸濁粒子を凝集し、溶解している有機物、栄養塩類を析
出凝集して大粒の塊である凝集物(フロック)化し、微
細気泡発生装置6は、微細気泡を発生し、混合攪拌槽5
1に隣接する微細気泡付加槽52において、前記微細気
泡を水面方向に付勢する方向で処理水中に導入して、凝
集を促進させると共に、前記凝集物を浮上分離凝集物1
0として水面上に浮上分離させることにより、処理水中
から汚濁物質を分離させ、浮上分離凝集物回収装置9
は、微細気泡付加槽52に隣接する浮上分離回収槽53
において、前記浮上分離凝集物10を回収して処理水中
から除去し、清水放流装置82は、汚濁物質の除去され
た清水を元の池等の水域や放水路に放流する水域の水質
底質活性浄化装置である。
A second aspect of the present invention for solving the problem is a water activity purifying agent 0 and a water activity purifying agent injector 2.
A mixing and stirring device 4, a fine bubble generating device 6, a flotation and separation agglomerate collecting device 9, a raw water pumping device 81, a fresh water discharge device 82, a mixing and stirring tank 51, and a fine bubble adding tank 52.
And a flotation / separation tank 53, which is a water bottom active purification device for a water area such as a pond, wherein the water active purification agent 0 contains a precipitation purification agent 01 or a coagulation separation agent 03, and a raw water pumping apparatus Reference numeral 81 is capable of pumping raw water in a water area containing pollutants or other drainage into the mixing and stirring tank 51, and the water activity purifying agent injecting device 2 selectively uses the precipitation purifying agent 01 or the coagulation separating agent 03. It is possible to inject at the same time, and according to the water quality, one or both of the precipitation purification agent 01 and the aggregation / separation agent 03 are simultaneously or one after the other, and the other is ordered, and in the mixing and stirring tank 51, the raw water containing pollutants is added. By injecting into water and mixing and stirring with the mixing and stirring device 4, suspended particles such as water-bloom, organic matter, and soil particles, which are pollutants, are aggregated, and dissolved organic matter and nutrient salts are precipitated and aggregated into large particles. Chunk of Turned into some aggregates (flocs), fine bubble generator 6 generates microbubbles, mixing and stirring tank 5
In the micro-bubble adding tank 52 adjacent to No. 1, the micro-bubbles are introduced into the treated water in the direction of urging in the water surface direction to promote coagulation, and the flocculates are floated and separated.
As a result, the contaminants are separated from the treated water by being floated and separated on the water surface as 0, and the flotation separation aggregate collecting device 9
Is a floating separation collection tank 53 adjacent to the fine bubble addition tank 52.
In the above, the floating separation aggregate 10 is collected and removed from the treated water. It is a purification device.

【0009】[0009]

【発明の実施の形態】本願発明は、神社、寺や公園の
池、お堀、溜め池、湖沼等の生活の身近に存在する水
辺、あるいはゴルフ場の池等の水域の水質および底質を
活性浄化処理する装置に関する。このような水域は、比
較的に小規模で、湧水等も少なく、他から閉鎖されてい
るケースが多い。上野の不忍池等の比較的に広い場所で
は、適宜に小区画に仕切り、各小区画を連続的に、また
は回分的に順次処理することができる。仕切は、本願発
明の活性浄化処理の速度が速いので、必ずしも密閉する
必要はなく、水の移動である水流に対して、ある程度の
抵抗となるように仕切られていれば良い。
BEST MODE FOR CARRYING OUT THE INVENTION The present invention determines the water quality and bottom quality of water bodies existing in everyday life such as shrines, temples and parks, moats, reservoir ponds, lakes and marshes, or water areas such as golf course ponds. The present invention relates to a device for active purification treatment. Such water areas are relatively small, have little spring water, and are often closed from other areas. In a relatively large area such as Shinobazu Pond in Ueno, it is possible to partition into small blocks as appropriate and to process each small block continuously or batchwise. Since the partition has a high speed of the active purification treatment of the present invention, it is not always required to be hermetically sealed, and it may be partitioned so as to have a certain resistance to the water flow which is the movement of water.

【0010】このような場所の水は、生活排水が流れ込
んだりし易く、また流れのない止まり水であり、水深も
浅く、環境や季節的な影響を受け易く、湧水等が少ない
場合には、有機物の懸濁物質や溶解物の濃度が高くな
り、また土粒子や、アオコ等が多量に存在したり、発生
したりして透明度も低く、美観を損ねるものである。ま
た季節によっては、微生物が大発生したり、透明度が低
下したり、悪臭を発生したりすることも少なくない。従
って活性浄化処理に当たっては、 短期間で処理が終了
する必要があり、処理設備も、設置場所が確保し難いの
で、小型、小規模にする必要があり、運転資金等もリー
ズナブルである必要がある。更に回収された有機物等の
回収物質も、土壌、肥料等で再利用できれば更に良い。
The water in such a place is a stop water in which domestic wastewater easily flows in, and there is no flow. The depth of the water is shallow, and it is easily affected by the environment and the seasons. In addition, the concentration of suspended solids and dissolved substances of organic matter becomes high, and a large amount of soil particles, water-bloom, etc. are present or generated, so that the transparency is low and the appearance is spoiled. In addition, depending on the season, a large amount of microorganisms, a decrease in transparency, and a bad odor are often generated. Therefore, it is necessary to finish the treatment in a short period of time for the active purification treatment, and it is difficult to secure the installation location for the treatment equipment.Therefore, it is necessary to make it small and small, and it is necessary that the operating capital etc. be reasonable. . Further, it is more preferable that the collected substances such as the collected organic substances can be reused in soil, fertilizers and the like.

【0011】図1は、本願発明の第1の実施の形態の模
式図であり、対象水域の原位置に直接設置し、当該位置
で処理するタイプのものである。(a)は、対象水域に
対して、水質活性浄化剤を添加し、混合する過程であ
る。(b)は析出凝集、凝集過程である。(c)は微細
気泡注入過程であり、凝集を促進すると共に、汚濁物を
浮上分離凝集物10として、水面上に浮上分離させる過
程である。(d)はこの浮上分離凝集物10を回収して
処分する過程である。ここで、は水質活性浄化剤であ
り、析出浄化剤01と凝集分離剤03とからなる。2は
ポンプ等からなる水質浄化活性剤注入装置、4はポンプ
等からなる混合攪拌装置、6は微細気泡発生装置、9は
浮上分離凝集物回収装置、10は浮上分離凝集物であ
る。
FIG. 1 is a schematic diagram of a first embodiment of the present invention, which is of a type that is installed directly at an original position in a target water area and treated at that position. (A) is a process of adding and mixing the water quality active purifying agent 0 to the target water area. (B) is precipitation aggregation and aggregation process. (C) is a process of injecting fine bubbles, which is a process of promoting aggregation and causing the contaminants to float as flotation / separation aggregates 10 on the water surface. (D) is a process of collecting and disposing of the floating separated aggregate 10. Here, 0 is a water quality active purifying agent, and is composed of a precipitation purifying agent 01 and an aggregation separating agent 03. Reference numeral 2 is a water purification activator injection device such as a pump, 4 is a mixing and stirring device such as a pump, 6 is a fine bubble generating device, 9 is a flotation-separated aggregate collection device, and 10 is a flotation-separated aggregate.

【0012】水質活性浄化剤は、析出浄化剤01と凝
集分離剤03とを包含する。析出浄化剤01は、例えば
シーマロックス(商品名)を用いる。シーマロックス
は、一般にはロックウオーター(あるいはロックスウオ
ーター:岩水)と呼ばれているものの一種である。即ち
ロックウオータは、シーマロックスを包含し、岩石から
溶出した薬液の総称である。ロックウォーターは、多種
の金属酸化物および非金属酸化物を含む鉱物の腐食岩
(「サブロライト」)またはこの腐食岩が更に風化され
た土壌を無機酸溶液に溶解して得た、多数の金属塩およ
び非金属塩のミネラル成分を主成分として含有する酸性
添加剤より主としてなり、水処理用水質活性浄化剤とし
て広く使用されている(例えば特開昭58−21670
5号公報参照)。
The water activity purifying agent 0 includes a precipitation purifying agent 01 and an aggregating / separating agent 03. As the precipitation cleaning agent 01, for example, Cima Rocks (trade name) is used. Cima Rocks is a type of what is generally called Rock Water (or Rocks Water: Iwamizu). In other words, rock water is a generic name for chemicals that include seamarox and are eluted from rocks. Rockwater is a large number of metal salts obtained by dissolving mineral corrosive rocks containing various metal oxides and non-metal oxides (“sabbrolite”) or soils further weathered in inorganic acid solutions. It is mainly composed of an acidic additive containing a mineral component of a non-metal salt as a main component, and is widely used as a water activity purifying agent for water treatment (for example, JP-A-58-21670).
(See Japanese Patent Publication No. 5).

【0013】またロックウォーターは、天然の鉱物から
ミネラル諸元素を抽出した無機液であり、毒性が全くな
いことが証明されている。主要成分は、Al,Fe,Mg,K,Ti,
Ca,Mn,Na,V,Rb,Si,Zn,W,Co,Li,Cu等である。この豊富な
無機質を含有していることにより、処理水の水質を活性
化し、浄化することができる。使用対象たる被処理水
は、自然物の腐敗成分を溶解している排水がよく、石油
製品やメッキ等の産業排水の処理には、あまり期待でき
ない。具体的には、厨房排水、食品工業の排水、家畜排
水、製紙排水等である。なお前処理として、無機質系や
高分子系凝集剤を使用すれば、無機質系の懸濁物質や溶
解物質をも凝集化処理することができる。
Rock water is an inorganic liquid obtained by extracting mineral elements from natural minerals, and it has been proved that it has no toxicity. The main components are Al, Fe, Mg, K, Ti,
They are Ca, Mn, Na, V, Rb, Si, Zn, W, Co, Li, Cu and the like. By containing this abundant inorganic substance, the water quality of the treated water can be activated and purified. The water to be treated, which is the target of use, is often wastewater in which spoilage components of natural substances are dissolved, and it cannot be expected to treat industrial wastewater such as petroleum products and plating. Specifically, it includes kitchen drainage, food industry drainage, livestock drainage, papermaking drainage, and the like. If an inorganic or polymeric flocculant is used as the pretreatment, the inorganic suspended substance or dissolved substance can also be subjected to the flocculation treatment.

【0014】凝集分離剤03は、例えばポリ塩化アルミ
ニウムが用いられる。ポリ塩化アルミニウムはポピュラ
ーな無機凝集剤の一種で、一般的には単に凝集剤、沈降
剤等呼ばれている。浮遊したり溶解している土粒子など
の無機あるいは有機物を凝集させる効果があり、無機質
系の前処理剤として使用することもできる。水質活性浄
化剤の注入は、水質活性化浄化剤注入装置2で行う
が、処理水の水質、汚染の程度、処理の効果、経済的観
点からみて、析出浄化剤01と凝集分離剤03のうち、
いずれか一方または両者同時に、または一方の後に他方
を順序を付けて注入することができる。
As the flocculating and separating agent 03, for example, polyaluminum chloride is used. Polyaluminum chloride is a kind of popular inorganic coagulant, and is generally called simply as coagulant or sedimentation agent. It has the effect of aggregating inorganic or organic substances such as soil particles that are floating or dissolved, and can also be used as an inorganic pretreatment agent. The water-purifying agent 0 is injected by the water-purifying agent injecting device 2, but in view of the water quality of the treated water, the degree of pollution, the effect of the treatment, and the economical viewpoint, the precipitation purifying agent 01 and the coagulant separating agent 03 are treated. home,
Either one or both can be injected simultaneously, or one after the other, in sequence.

【0015】汚染の激しい水質では、最初に安価な凝集
分離剤03を使用して、浮遊したり溶解している土粒子
などの無機あるいは有機物を凝集させて、その凝集物を
前処理として浮上分離させ、次いで高価な析出浄化剤0
1を注入して、凝集分離剤03では除去できない物質を
二次浮上分離することができる。もちろん同時に両者を
注入することもできる。処理の効果としては、析出浄化
剤01は高価であるが、水質の活性と浄化の双方が可能
であり、凝集分離剤03は安価であるが、水質を浄化
し、その改善を図ることができるものである。
In the case of severely polluted water quality, an inexpensive coagulation / separation agent 03 is first used to coagulate inorganic or organic matter such as suspended or dissolved soil particles, and the coagulation is subjected to flotation as pretreatment. And then an expensive precipitation purification agent 0
By injecting 1, the substance that cannot be removed by the flocculating and separating agent 03 can be secondarily floated and separated. Of course, both can be injected at the same time. As for the effect of the treatment, although the precipitation purification agent 01 is expensive, it is possible to both activate and purify the water quality, and the aggregation separating agent 03 is inexpensive, but it is possible to purify the water quality and improve it. It is a thing.

【0016】微細気泡発生装置6は、微細気泡を発生す
る。その微細気泡(マイクロバブル)を処理水中に導入
し凝集物に作用させると、凝集物に微細気泡が付着し、
あるいは微細気泡の周りに凝集物が付着し、その浮力に
より凝集物を水面に持ち上げる、即ち浮上分離が行われ
る。微細気泡を処理水中に導入するに当っては、水面方
向に付勢するような成分を付して行うと、浮上分離がよ
り効率的に行われることとなる。またその微細気泡の噴
流を導入して、水域底面近傍の浮遊泥、汚泥を攪拌すれ
ば、水質活性浄化剤の混合攪拌作用も促進されること
となり、更には混合攪拌機の機能も兼ね備えることがで
き、底質の改善、活性浄化を図ることもできる。ここで
微細気泡発生装置6により発生する微細気泡は、その大
きさが5μm以下の直径を有するものである。
The fine bubble generator 6 generates fine bubbles. When the fine bubbles (micro bubbles) are introduced into the treated water to act on the aggregate, the fine bubbles adhere to the aggregate,
Alternatively, agglomerates are attached around the fine bubbles, and the buoyancy lifts the agglomerates to the water surface, that is, floating separation. When the fine bubbles are introduced into the treated water, if a component that biases in the water surface direction is added, the floating separation will be performed more efficiently. If the jet of fine bubbles is introduced to stir the floating mud and sludge near the bottom of the water area, the mixing and stirring action of the water-purifying agent 0 can be promoted, and it can also have the function of a mixing stirrer. It is also possible to improve bottom sediment and purify activity. Here, the fine bubbles generated by the fine bubble generator 6 have a diameter of 5 μm or less.

【0017】このように水質活性浄化剤の添加によ
り、被処理水中の有機物や土粒子、アオコ等の懸濁物質
を非分散性の大粒の凝塊(フロック)に成長させて、溶
解している有機物や栄養塩類を析出凝集せしめて、ある
いは前記凝塊物と共に凝集化させ、微細気泡により、水
面に浮上分離凝集物10として浮上せしめて、汚濁物質
を水中から分離除去することができる。またミネラル成
分や微細気泡の酸素を水中に付加することとなるので水
と、生物とを活性浄化させ、生態系の復元を図ることが
できる。
As described above, by adding the water activity purifying agent 0 , suspended substances such as organic matter, soil particles, and water-blooms in the water to be treated are grown into non-dispersible large-sized agglomerates (flocs) and dissolved. It is possible to separate and remove the pollutants from the water by precipitating and aggregating the organic substances and nutrient salts present therein, or by aggregating with the agglomerates, and floating them as floating separation agglomerates 10 on the water surface by fine bubbles. Further, since mineral components and oxygen of fine bubbles are added to the water, the water and living organisms can be actively purified, and the ecosystem can be restored.

【0018】更に底層の処理水を好気性に改善し、底泥
の分解を促進し、栄養塩類の溶出を低減することができ
る。溶存酸素の増加、ミネラル質の作用により水質だけ
でなく、底泥も活性浄化され、処理水は処理後汚濁し難
くなる。浮上分離凝集物回収装置9は、縄、ロープ等、
あるいはレーキ(掻取り具)、シルトプロテクター、バ
キュームポンプ、スカム回収器等が適宜用いられ、水面
上に浮上した浮上分離凝集物10を容易に回収すること
ができる。この凝集物からなる回収物は、天日干し等で
簡単に乾燥でき、有機肥料として再利用可能であり、条
件に応じて販売することもできるものである
Further, the treated water in the bottom layer can be improved to be aerobic, the decomposition of the bottom mud can be promoted, and the elution of nutrient salts can be reduced. Due to the increase of dissolved oxygen and the action of minerals, not only the water quality but also the bottom mud is activated and purified, and the treated water is less likely to be polluted after the treatment. The flotation separation aggregate collection device 9 includes ropes, ropes, etc.
Alternatively, a rake (scraping tool), a silt protector, a vacuum pump, a scum collector, etc. are used as appropriate, and the flotation-separated aggregate 10 that has floated above the water surface can be easily collected. The collected product consisting of this aggregate can be easily dried by sun-drying, can be reused as an organic fertilizer, and can be sold depending on the conditions.

【0019】図2は、本願発明の第2の実施の形態であ
るプラントタイプのもので、原水汲上げ装置81と、清
水放流装置82と、混合攪拌槽51と、微細気泡付加槽
52、浮上分離回収槽53とを少なくとも付加して具備
するものであり、対象水域の近傍に設置して運転する。
また車上に設置すれば移動も簡単に可能となり、巡回的
に各地の水域の活性浄化処理を図ることができる。ここ
で、1は流量計、6は微細気泡噴射ノズル、7は清水吸
引口、8は仕切壁、9は掻き取り装置からなる浮上分離
凝集物回収装置、11は回収装置、12は回収袋、13
は清水排出口、14は堰、15は開口、16は二次浮上
分離凝集物回収装置、51は混合攪拌槽、52は微細気
泡付加槽、53は浮上分離回収槽、54は清水放流槽、
55は二次浮上分離回収槽である。
FIG. 2 shows a plant type which is a second embodiment of the present invention. It is a raw water pumping device 81, a fresh water discharge device 82, a mixing and stirring tank 51, a fine bubble addition tank 52, and a floater. It is provided with at least the separation and recovery tank 53, and is installed and operated near the target water area.
In addition, if it is installed on the vehicle, it can be easily moved, and the active purification treatment of the water bodies in various places can be planned cyclically. Here, 1 is a flow meter, 6 is a fine bubble injection nozzle, 7 is a fresh water suction port, 8 is a partition wall, 9 is a flotation / separation aggregate recovery device consisting of a scraping device, 11 is a recovery device, 12 is a recovery bag, Thirteen
Is a fresh water discharge port, 14 is a weir, 15 is an opening, 16 is a secondary flotation separation aggregate collection device, 51 is a mixing and stirring tank, 52 is a fine bubble addition tank, 53 is a floating separation collection tank, 54 is a fresh water discharge tank,
55 is a secondary flotation separation recovery tank.

【0020】このタイプのものは、原水汲上げ装置81
により汚濁原水を連続的、または回分的に混合攪拌槽5
1に汲入れ、第1の実施の形態のものと同様に、水質活
性浄化剤を、水質活性浄化剤注入装置2により注入し
て、ラインミキサー、ドロップシャフト等の同様な混合
攪拌装置4により混合することができる。各処理は、第
1の実施の形態のものと異なり、仕切壁8で仕切られた
それぞれの処理をを行う各処理槽で行われるようになっ
ており、各処理槽では異なる処理をほぼ同時に行うこと
ができる。
This type has a raw water pumping device 81
Contaminated raw water is continuously or batchwise mixed by the stirring tank 5
1, the water quality active cleaning agent 0 is injected by the water quality active cleaning agent injecting device 2 in the same manner as in the first embodiment, and the same mixing and stirring device 4 such as a line mixer or a drop shaft is used. Can be mixed. Different from the first embodiment, each processing is performed in each processing tank that performs each processing partitioned by the partition wall 8, and each processing tank performs different processing almost at the same time. be able to.

【0021】各処理槽への処理水の導入の仕方は、各仕
切壁8に応じて、下方に設けられた開口15や上方に設
けられた堰14によって行われる。堰14は3角堰、4
角堰、全幅堰等各種あり、流量によって、その種類や開
口15の大きさ等を適宜選択することができる図3によ
り、処理水の流向制御の概略を説明する。混合攪拌槽5
1と微細気泡付加槽52との間には仕切壁8が設けられ
ており、下方には開口15が形成されている。原水に水
質活性浄化剤を添加された処理水は、攪拌混合され
て、汚濁物が析出凝集して凝集物化され、この下方の開
口15からに微細気泡付加槽52中に導入される。
The method of introducing the treated water into each treatment tank is carried out by an opening 15 provided at the bottom and a weir 14 provided at the top, depending on each partition wall 8. Weir 14 is a triangular weir, 4
There are various types such as a square weir and a full width weir, and the type and size of the opening 15 can be appropriately selected according to the flow rate, and the flow direction control of the treated water will be outlined with reference to FIG. Mixing and stirring tank 5
A partition wall 8 is provided between 1 and the fine bubble addition tank 52, and an opening 15 is formed below. The treated water to which the water activity purifying agent 0 is added to the raw water is agitated and mixed, and the contaminants are precipitated and aggregated to be aggregated, and introduced into the fine bubble addition tank 52 through the opening 15 below.

【0022】ここに微細気泡噴射ノズル5から微細気泡
が噴射されると、この凝集物化を促進しつつ、微細気泡
が付着されて浮上方向と進行方向の成分に応じて、浮上
分離凝集物10として浮上しつつ次の槽の方に進行す
る。微細気泡付加槽52と浮上分離回収槽53との間に
は仕切壁8が設けられており、上方には堰14が形成さ
れているから、その方向に処理水の流れは制御されて、
堰14を越えて浮上分離回収槽53に導入される。ここ
で処理水は、水面には汚濁物質が浮上分離凝集物10が
存在し、従って下方には清水が存在する。水面の浮上分
離凝集物10は掻き取り装置等の浮上分離凝集物回収装
置9により回収され、回収装置11を介して回収袋12
に収納される。
When fine bubbles are jetted from the fine bubble jet nozzle 5 to the above, the fine bubbles are adhered, and the fine bubbles are attached to the floating separation aggregate 10 depending on the components in the floating direction and the traveling direction. While levitating, proceed to the next tank. Since the partition wall 8 is provided between the fine bubble addition tank 52 and the floating separation collection tank 53, and the weir 14 is formed above, the flow of the treated water is controlled in that direction.
It is introduced into the floating separation recovery tank 53 over the weir 14. Here, in the treated water, contaminants are floated and separated on the surface of the water, and the agglomerate 10 is present, and thus, fresh water is present below. The floating separation aggregates 10 on the water surface are collected by the floating separation aggregates collecting device 9 such as a scraping device, and the collecting bag 12 is collected via the collecting device 11.
Is stored in.

【0023】浮上分離凝集物回収装置9で回収された浮
上分離凝集物10は本願発明の第1の実施の形態のもの
と同じ様に処理してよい。下方の清水は隣接する二次分
離浮上槽55との境界である仕切壁8の下方にある開口
15を介して、二次分離浮上槽55に導入される。析出
凝集に時間のかかる汚濁物は、この槽で浮上分離して二
次分離浮上凝集物回収装置16により回収することがで
きる。下方の清水は一部は清水吸引口7より微細気泡発
生装置6に導かれ、その清水を利用して微細気泡を発生
する。清水の他の大部分は、清水放流槽54に導入さ
れ、清水放流装置82により元の池や放水路に放流され
ることとなる。
The flotation separated agglomerates 10 recovered by the flotation separated agglomerate recovery apparatus 9 may be treated in the same manner as in the first embodiment of the present invention. The fresh water below is introduced into the secondary separation floating tank 55 through the opening 15 below the partition wall 8 which is the boundary with the adjacent secondary separation floating tank 55. The contaminant, which takes a long time for precipitation and aggregation, can be floated and separated in this tank and collected by the secondary separation floating flocculent collection device 16. Part of the lower fresh water is introduced from the fresh water suction port 7 to the fine bubble generator 6, and the fine water is used to generate fine bubbles. Most of the fresh water is introduced into the fresh water discharge tank 54 and discharged into the original pond or discharge channel by the fresh water discharge device 82.

【0024】図4は、このプラントタイプのものの処理
のフローを示すものである。即ち原水汲上げ、水質
活性浄化剤の注入、混合攪拌、析出凝集、微細
気泡噴射、析出凝集物浮上分離、分離回収、袋詰
め脱水、二次分離浮上、▲10▼清水放流、▲11▼有機
肥料化、廃棄物処理となる。また混合攪拌槽51の大き
さ等量的関係を勘案して、また流量計1等の各種計測装
置が簡単に使用できるので、凝集物を形成するのに、点
滴ポンプ、流量計1等を使用して、量的関係や、現在の
系の状態がが容易に把握でき、各処理を最適値に制御す
ることができる。
FIG. 4 shows a processing flow of this plant type. That is, pumping raw water, injecting water-purifying agent 0 , mixing and agitation, precipitation agglomeration, injection of fine bubbles, flotation separation of precipitation agglomerates, separation and collection, bagging dehydration, secondary separation flotation, (10) discharge of fresh water, (11) It becomes organic fertilizer and waste treatment. In addition, in consideration of the size-equal relationship of the mixing and stirring tank 51, and because various measuring devices such as the flow meter 1 can be easily used, a drip pump, the flow meter 1 or the like is used to form the aggregate. Then, the quantitative relationship and the current system state can be easily grasped, and each process can be controlled to the optimum value.

【0025】生成された凝集物と微細気泡との関係は第
1の実施の態様と同様であるが、導入方向と気泡の量的
関係等により最適値に制御することができる。水面に浮
上した凝集物の回収も、第1の実施の態様と同様の装置
を用いて容易に行うことが可能であり、回収した凝集物
を袋詰めにすれば回収過程中で、同時に脱水過程も行わ
れることとなり、より短時間で有機肥料化し易い。
The relationship between the agglomerates generated and the fine bubbles is the same as in the first embodiment, but can be controlled to an optimum value by the quantitative relationship between the introduction direction and the bubbles. It is possible to easily collect the agglomerates floating on the water surface by using the same device as in the first embodiment. If the collected agglomerates are packed in a bag, the agglomerates can be simultaneously dehydrated during the recovery process. Will also be carried out, and it will be easier to turn it into an organic fertilizer in a shorter time.

【0026】[0026]

【 表 1】 表1には、上野不忍池における処理の実験結果を示す。
ここで、「SS」Suspended Solid:水中に懸濁してい
る有機系、無機系の物質で、汚れを示す指標。スクリー
ン等で除去できる大型のものは含まない。「濁度」:水
の濁り具合を示す指標。「クロロフィル」:植物性プラ
ンクトンの溶存量を示す。水中の葉緑素の量を測定して
求める。「COD」Chemical Oxygen Demand:化学的酸
素要求量。排水中の被酸化性物質を酸化剤によって酸化
させるのに必要な酸素量で、有機性物質による汚れの指
標。基準値は通常、過マンガン酸カリウム法による分析
値を用いる。「T−N」Total Nitrogen:全窒素量。無
機性窒素(アンモニア性窒素、亜硝酸性及び硝酸性窒
素)及び有機性窒素(タンパク質や種々の有機化合物の
窒素)の総量を表す。「T−P」Total Phosphorus:全
リン量。水中のリン化合物の総量をそのリンの量で表し
たものである。
[Table 1] Table 1 shows the experimental results of the treatment in Ueno Shinobazuike.
Here, "SS" Suspended Solid: An organic or inorganic substance suspended in water, which is an index indicating dirt. Does not include large items that can be removed with a screen. "Turbidity": An index showing the degree of turbidity of water. "Chlorophyll": Indicates the dissolved amount of phytoplankton. It is determined by measuring the amount of chlorophyll in water. "COD" Chemical Oxygen Demand: Chemical oxygen demand. The amount of oxygen required to oxidize oxidizable substances in wastewater with an oxidizer, which is an index of contamination by organic substances. As the reference value, an analysis value by the potassium permanganate method is usually used. "TN" Total Nitrogen: Total nitrogen content. It represents the total amount of inorganic nitrogen (ammonia nitrogen, nitrite and nitrate nitrogen) and organic nitrogen (nitrogen of proteins and various organic compounds). "TP" Total Phosphorus: Total phosphorus content. The total amount of phosphorus compounds in water is represented by the amount of phosphorus.

【0027】以下に運転状況を見るに、図1のもので
は、例えば20トンの汚濁水を5kWの微細気泡発生装
置6で処理した場合は以下の程度の処理状況である。資
材機材等の設備がコンパクトで簡単なので、設備搬入後
30分程度で活性浄化処理作業を開始することができ
る。対象水域に水処理用水質活性浄化剤0を注入すると
10分程度で凝集化が開始され、水中ポンプで対象水域
内の水を循環し混合すると、汚濁物質は10分程度で凝
集物質化される。
Looking at the operation status below, in the case of FIG. 1, for example, when 20 tons of polluted water is processed by the 5 kW fine bubble generator 6, the processing status is as follows. Since the equipment such as materials and equipment is compact and simple, it is possible to start the activity purification treatment work in about 30 minutes after the equipment is loaded. When the water purification agent for water treatment 0 for water treatment is injected into the target water area, coagulation starts in about 10 minutes, and when water in the target water area is circulated and mixed by the submersible pump, the pollutant is converted into coagulated material in about 10 minutes. .

【0028】それから微細気泡を注入すると50分程度
で凝集物が浮上分離する。この浮上分離した凝集物を1
0分程度で回収して乾燥し、有機肥料とするか廃棄物と
して処理することができる。乾燥は、天日干しでも、1
日あれば充分である。処理状況は、見る間に透明度が向
上するので、即効的で目にも分かり易い。
Then, when fine bubbles are injected, the aggregates float and separate in about 50 minutes. This flotation-separated aggregate is 1
It can be collected in about 0 minutes, dried and used as organic fertilizer or treated as waste. Even if it is dried in the sun, 1
One day is enough. Since the transparency of the processing status improves during viewing, it is immediately effective and easy to see.

【0029】[0029]

【発明の効果】水質活性浄化剤の酸化作用により、水
溶性有機物、栄養塩類等の汚濁物質を系外に除去するこ
とができるので、水質および底質が活性浄化される。水
質活性浄化剤0に含まれるミネラル分と活性酸素とが、
水質および底質を活性浄化させる。水質活性浄化剤
微細気泡を使用して、汚濁物質を析出凝集して分離する
ため、短時間で活性浄化処理が可能であり、見る間に透
明度が向上する。また原水の汚濁物質の変化や量的な変
化にも柔軟に対応することができる。
EFFECTS OF THE INVENTION Oxidizing action of the water quality active purifying agent 0 can remove pollutants such as water-soluble organic substances and nutrient salts to the outside of the system. Minerals and active oxygen contained in the water quality purification agent 0
Actively purifies water and bottom sediment. The water purification agent 0 and fine bubbles are used to deposit and aggregate pollutants to separate them, so that the purification treatment can be carried out in a short time, and the transparency is improved during viewing. In addition, it is possible to flexibly respond to changes in pollutants of raw water and quantitative changes.

【0030】活性浄化された水はミネラル分を多く含
み、生態系の復元に大いに寄与する。また底質が改善さ
れるのでワムシ等の底性生物の成育が活性浄化される。
水質活性浄化剤の効果により不快な臭気を除去し、作
業中も悪臭が発生し難い。底水層を好気性に改善して底
層からの栄養塩類の溶出を低減する。また特に第1の実
施態様では、底層の浮遊泥、汚泥を攪拌して、浮上分離
して系外に除去処理することが可能である。
Actively purified water contains a large amount of minerals and greatly contributes to the restoration of the ecosystem. In addition, since the sediment quality is improved, the growth of benthic organisms such as rotifers is actively purified.
Due to the effect of the water quality active purifying agent 0, an unpleasant odor is removed, and an offensive odor is less likely to occur during work. The bottom water layer is improved to be aerobic to reduce the elution of nutrients from the bottom layer. Further, in particular, in the first embodiment, it is possible to stir the floating mud and sludge in the bottom layer, float and separate them, and remove them outside the system.

【0031】第2の実施態様では、各種計測装置を搭載
して各要素の量的関係を把握できるので、最適の状態で
制御された運転が可能である。何れも装置がコンパクト
なので、狭い場所でも設置、処理可能であり、しかも修
景を損なわない。また移動可能とすることができるの
で、ゴルフ場の池等で、必要に応じて短時間作業し、作
業後は撤収することも簡単にできる。車載のものでは、
広範囲の各地での作業が、定期的に巡回して行なうこと
ができる。また微細気泡を、処理水中に導入するに当
り、水面方向に付勢するような成分を付して行うので、
浮上分離がより効率的に行われることとなり、攪拌混合
にも好都合である。
In the second embodiment, since various measuring devices are mounted and the quantitative relationship between the respective elements can be grasped, the controlled operation in the optimum state is possible. Both of them are compact in size, so they can be installed and processed even in a narrow space, and they do not impair the landscape. Further, since it can be moved, it is possible to easily work at a golf course pond or the like for a short time and to withdraw it after the work. In the car,
Work in a wide range of places can be patroled regularly. In addition, when introducing fine air bubbles into the treated water, a component that urges them toward the water surface is added,
Float separation is performed more efficiently, which is also convenient for stirring and mixing.

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

【図1】本願発明の第1の実施の形態における水域原位
置の模式図である。(a)水質活性浄化剤の注入と混
合攪拌過程、(b)汚濁物質の析出凝縮過程、(c)微
細気泡注入と凝縮物の浮上分離過程、(d)凝集物の回
収、処分過程。
FIG. 1 is a schematic diagram of an original position of a water area according to a first embodiment of the present invention. (A) Injecting the water activity purifier 0 and mixing and stirring process, (b) Precipitating and condensing process of pollutants, (c) Injecting fine bubbles and floating separation process of condensate, (d) Collecting and disposing process of aggregates.

【図2】本願発明の第2の実施の形態におけるプラント
全体の斜視図である。
FIG. 2 is a perspective view of an entire plant according to a second embodiment of the present invention.

【図3】プラント内部における処理水の流向制御の概略
を説明する図である。
FIG. 3 is a diagram illustrating an outline of flow direction control of treated water inside a plant.

【図4】本願発明の第2の実施の形態におけるプラント
内における処理のフローを示す図である。
FIG. 4 is a diagram showing a flow of processing in a plant according to a second embodiment of the present invention.

【符号の説明】 ・・・水質活性浄化剤 01・・・析出質浄化剤 03・・・凝集分離剤 1・・・流量計 2・・・水質活性浄化剤注入装置 4・・・混合攪拌装置 5・・・微細気泡噴射ノズル 6・・・微細気泡発生装置 7・・・清水吸引口 8・・・仕切壁 9・・・浮上分離凝集物回収装置 10・・・浮上分離凝集物 11・・・回収装置1 12・・・回収袋 13・・・清水排出口 14・・・堰 15・・・開口 16・・・二次浮上分離凝集物回収装置 51・・・混合攪拌槽 52・・・微細気泡付加槽 53・・・浮上分離回収槽 55・・・二次分離浮上槽 54・・・清水放流槽 81・・・原水汲上げ装置 82・・・清水放流装置[Explanation of Codes] 0 ... Water purification agent 01 ... Precipitation purification agent 03 ... Aggregation / separation agent 1 ... Flowmeter 2 ... Water activation agent injection device 4 ... Mixing stirring Device 5 ... Fine bubble injection nozzle 6 ... Fine bubble generator 7 ... Fresh water suction port 8 ... Partition wall 9 ... Flotation separated aggregate collection device 10 ... Flotation separated aggregate 11 ... ..Recovery device 112 ... recovery bag 13 ... fresh water outlet 14 ... weir 15 ... opening 16 ... secondary flotation separated aggregate collection device 51 ... mixing stirring tank 52 ...・ Fine bubble addition tank 53 ・ ・ ・ Floating separation recovery tank 55 ・ ・ ・ Secondary separation floating tank 54 ・ ・ ・ Clean water discharge tank 81 ・ ・ ・ Raw water pumping device 82 ・ ・ ・ Clean water discharge device

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) C02F 1/40 C02F 1/40 C E 1/68 510 1/68 510Z 520 520K 540 540Z 3/20 3/20 Z 11/02 11/02 11/14 11/14 B (72)発明者 吉田 將 東京都千代田区麹町一丁目10番地東洋建設 株式会社内 (72)発明者 横山 浩司 東京都千代田区麹町一丁目10番地東洋建設 株式会社内 (72)発明者 大杉 一郎 東京都千代田区麹町一丁目10番地東洋建設 株式会社内 (72)発明者 苗木 謙二 東京都千代田区麹町一丁目10番地東洋建設 株式会社内 Fターム(参考) 4D015 BA19 BA22 BB05 BB08 BB09 CA20 DA03 DA31 DC02 DC04 EA33 4D029 AA01 AB05 BB11 4D037 AA05 AB02 AB04 BA03 CA07 CA08 CA13 4D051 AA04 AB07 CA01 CA02 EB08 4D059 AA30 BA03 BJ09 DA51 DA70─────────────────────────────────────────────────── ─── Continuation of front page (51) Int.Cl. 7 Identification code FI theme code (reference) C02F 1/40 C02F 1/40 CE E 1/68 510 1/68 510Z 520 520K 540 540Z 3/20 3 / 20 Z 11/02 11/02 11/14 11/14 B (72) Inventor Masayoshi Yoshida 1-10 Kojimachi, Chiyoda-ku, Tokyo Within Toyo Construction Co., Ltd. (72) Koji Yokoyama 1-chome, Kojimachi, Chiyoda-ku, Tokyo 10 Toyo Construction Co., Ltd. (72) Inventor Ichiro Osugi 1-10 Kojimachi, Chiyoda-ku, Tokyo Toyo Construction Co., Ltd. (72) Inventor Kenji Naegi 1-10 Kojimachi, Chiyoda-ku, Tokyo Toyo Construction Co., Ltd. F Term (reference) 4D015 BA19 BA22 BB05 BB08 BB09 CA20 DA03 DA31 DC02 DC04 EA33 4D029 AA01 AB05 BB11 4D037 AA05 AB02 AB04 BA03 CA07 CA08 CA13 4D051 AA04 AB07 CA01 CA02 EB08 4D059 AA30 BA03 BJ09 DA51 DA70

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 水質活性浄化剤()と、水質活性浄化
剤注入装置(2)と、混合攪拌装置(4)と、微細気泡
発生装置(6)と、浮上分離凝集物回収装置(9)とを
少なくとも具備する池等の水域の水質底質活性浄化装置
であって、 水質活性浄化剤()は、析出浄化剤(01)または凝
集分離剤(03)を含み、 水質活性浄化剤注入装置(2)は、析出浄化剤(01)
または凝集分離剤(03)を選択的にまたは同時に注入
可能であって、水質に応じて、析出浄化剤(01)また
は凝集分離剤(03)の一方または両者を同時に、また
は一方の後に他方を順序付けて水域の汚濁物質を含む原
水中に注入し、混合攪拌装置(4)により混合攪拌する
ことにより、汚濁物質である水中のアオコ、有機物、土
粒子等の懸濁粒子を凝集し、溶解している有機物、栄養
塩類を析出凝集して、大粒の塊である凝集物(フロッ
ク)化し、 微細気泡発生装置(6)は、微細気泡を発生し、前記微
細気泡を水面方向に付勢する方向で処理水中に導入し
て、凝集を促進させると共に、前記凝集物を浮上分離凝
集物(10)として水面上に浮上分離させることにより
水中から汚濁物質を分離させ、 浮上分離凝集物回収装置(9)により、前記浮上分離凝
集物(10)を回収する水域の水質底質活性浄化装置。
1. An active water purification agent ( 0 ), an active water purification agent injecting device (2), a mixing and stirring device (4), a fine bubble generating device (6), and a flotation separation aggregate collecting device (9). ) Is provided at least in a water body such as a pond, wherein the water-purifying agent ( 0 ) contains a precipitation purifying agent (01) or a coagulation separating agent (03). The injection device (2) is a precipitation purification agent (01).
Alternatively, the coagulation-separating agent (03) can be selectively or simultaneously injected, and one or both of the precipitation purification agent (01) and the coagulation-separating agent (03) can be injected simultaneously or one after the other, depending on the water quality. By ordering and injecting into raw water containing pollutants in the water area, and mixing and stirring with a mixing and stirring device (4), suspended particles such as water-bloom, organic matter, and soil particles in water that are pollutants are aggregated and dissolved. Agglomerates (flocs) that are large-sized lumps by precipitating and aggregating organic substances and nutrient salts that are present, and the fine bubble generator (6) generates fine bubbles, and urges the fine bubbles toward the water surface. Is introduced into the treated water to promote coagulation, and at the same time, the agglomerates are floated and separated on the surface of the water as flotation and separation agglomerates (10) to separate pollutants from the water. ) To Ri, the flotation aggregate (10) Water sediment activity purification device of water for recovering.
【請求項2】 水質活性浄化剤()と、水質活性浄化
剤注入装置(2)と、混合攪拌装置(4)と、微細気泡
発生装置(6)と、浮上分離凝集物回収装置(9)と、
原水汲上げ装置(81)と、清水放流装置(82)と、
混合攪拌槽(51)と、微細気泡付加槽(52)と、浮
上分離回収槽(53)とを少なくとも具備する池等の水
域の水質底質活性浄化装置であって、 水質活性浄化剤()は、析出浄化剤(01)または凝
集分離剤(03)を含み、 原水汲上げ装置(81)は、汚濁物質を含む水域の原水
や他の排水を混合攪拌槽(51)中に汲入れ可能であ
り、 水質活性浄化剤注入装置(2)は、析出浄化剤(01)
または凝集分離剤(03)を選択的にまたは同時に注入
可能であって、水質に応じて、析出浄化剤(01)また
は凝集分離剤(03)の一方または両者を同時に、また
は一方の後に他方を順序付けて、混合攪拌槽(51)中
において、汚濁物質を含む原水中に注入し、混合攪拌装
置(4)により混合攪拌することにより、汚濁物質であ
る水中のアオコ、有機物、土粒子等の懸濁粒子を凝集
し、溶解している有機物、栄養塩類を析出凝集して大粒
の塊である凝集物(フロック)化し、 微細気泡発生装置(6)は、微細気泡を発生し、混合攪
拌槽(51)に隣接する微細気泡付加槽(52)におい
て、前記微細気泡を水面方向に付勢する方向で処理水中
に導入して、凝集を促進させると共に、前記凝集物を浮
上分離凝集物(10)として水面上に浮上分離させるこ
とにより、処理水中から汚濁物質を分離させ、 浮上分離凝集物回収装置(9)は、微細気泡付加槽(5
2)に隣接する浮上分離回収槽(53)において、前記
浮上分離凝集物(10)を回収して処理水中から除去
し、 清水放流装置(82)は、汚濁物質の除去された清水を
元の池等の水域や放水路に放流する水域の水質底質活性
浄化装置。
2. A water activity purifying agent ( 0 ), a water activity purifying agent injection device (2), a mixing and stirring device (4), a fine bubble generating device (6), and a flotation separation aggregate collecting device (9). )When,
A raw water pumping device (81), a fresh water discharge device (82),
An apparatus for purifying water bottom sediment in a water area such as a pond, which comprises at least a mixing and stirring tank (51), a fine air bubble addition tank (52), and a flotation separation recovery tank (53), the water activity purifying agent ( 0 ) Contains a precipitation purification agent (01) or a coagulation separation agent (03), and a raw water pumping device (81) pumps raw water in a water area containing pollutants or other waste water into a mixing stirring tank (51). It is possible that the water activity purifying agent injection device (2)
Alternatively, the coagulation-separating agent (03) can be selectively or simultaneously injected, and one or both of the precipitation purification agent (01) and the coagulation-separating agent (03) can be injected simultaneously or one after the other, depending on the water quality. By ordering and pouring into raw water containing pollutants in the mixing and stirring tank (51) and mixing and stirring with the mixing and stirring device (4), suspended water such as water-bloom, organic matter, and soil particles, which are pollutants, are suspended. The turbid particles are aggregated, and dissolved organic substances and nutrient salts are precipitated and aggregated to form aggregates (flocs) that are large lumps, and the fine bubble generator (6) generates fine bubbles, and mixes and stirs the tank ( In the fine bubble addition tank (52) adjacent to 51), the fine bubbles are introduced into the treated water in a direction of urging them toward the water surface to promote aggregation, and at the same time, the aggregates are floated and separated aggregates (10). On the water surface By floating and separating, contaminants are separated from the treated water, and the flotation and separation agglomerate recovery device (9) includes a fine bubble addition tank (5
In the flotation separation recovery tank (53) adjacent to 2), the flotation separation aggregate (10) is recovered and removed from the treated water, and the fresh water discharge device (82) returns the fresh water from which the pollutants have been removed to the original water. An active purification device for water bottom sediment in water areas such as ponds and water areas that are discharged into discharge channels.
JP2001318891A 2001-10-17 2001-10-17 Active cleaning equipment for water and bottom sediment of water area Pending JP2003117562A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2001318891A JP2003117562A (en) 2001-10-17 2001-10-17 Active cleaning equipment for water and bottom sediment of water area

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2001318891A JP2003117562A (en) 2001-10-17 2001-10-17 Active cleaning equipment for water and bottom sediment of water area

Publications (1)

Publication Number Publication Date
JP2003117562A true JP2003117562A (en) 2003-04-22

Family

ID=19136516

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Link
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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004307257A (en) * 2003-04-07 2004-11-04 Toyo Constr Co Ltd Method of manufacturing shell recycled block and shell recycled block
CN102126822A (en) * 2011-01-20 2011-07-20 北京城市排水集团有限责任公司 Active sludge floatation thickening device and method for membrane biological reaction tank process
JP2012106212A (en) * 2010-11-19 2012-06-07 Reo Laboratory Co Ltd Drainage treatment method
JP2020116515A (en) * 2019-01-23 2020-08-06 有限会社アルファサービス Microcystis concentration and recovery system

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004307257A (en) * 2003-04-07 2004-11-04 Toyo Constr Co Ltd Method of manufacturing shell recycled block and shell recycled block
JP2012106212A (en) * 2010-11-19 2012-06-07 Reo Laboratory Co Ltd Drainage treatment method
CN102126822A (en) * 2011-01-20 2011-07-20 北京城市排水集团有限责任公司 Active sludge floatation thickening device and method for membrane biological reaction tank process
JP2020116515A (en) * 2019-01-23 2020-08-06 有限会社アルファサービス Microcystis concentration and recovery system

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