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JPH0519603B2 - - Google Patents
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JPH0519603B2 - - Google Patents

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Publication number
JPH0519603B2
JPH0519603B2 JP60144902A JP14490285A JPH0519603B2 JP H0519603 B2 JPH0519603 B2 JP H0519603B2 JP 60144902 A JP60144902 A JP 60144902A JP 14490285 A JP14490285 A JP 14490285A JP H0519603 B2 JPH0519603 B2 JP H0519603B2
Authority
JP
Japan
Prior art keywords
water
flocculant
algaecide
shallow
water pump
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 - Lifetime
Application number
JP60144902A
Other languages
Japanese (ja)
Other versions
JPS626010A (en
Inventor
Masahiko Makino
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.)
Kaiyo Kogyo KK
Original Assignee
Kaiyo 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 Kaiyo Kogyo KK filed Critical Kaiyo Kogyo KK
Priority to JP14490285A priority Critical patent/JPS626010A/en
Publication of JPS626010A publication Critical patent/JPS626010A/en
Publication of JPH0519603B2 publication Critical patent/JPH0519603B2/ja
Granted legal-status Critical Current

Links

Description

【発明の詳細な説明】 (産業上の利用分野) この発明は比較的浅水域(例えば水深3m位)
の湖・沼又は池・河川或いは浄水する為の貯水場
などにおける浄水方法に関する。
[Detailed description of the invention] (Industrial application field) This invention is applicable to relatively shallow waters (for example, about 3 m deep).
This invention relates to water purification methods in lakes, ponds, ponds, rivers, and water storage facilities for water purification.

(従来の技術) 従来、ダム・湖・沼、或いは河川等において
は、水温の上昇と共に、藻類が繁殖し、水中の酸
欠による魚類の死滅、悪臭の発生その他の原因に
よる水質低下が生じていたが、有効な防止方法が
なく、例えば活性炭による濾過などが考えられて
いた。また水深の大きなダム・湖沼などにおいて
は、間欠空気揚水装置によつてダム等の水を上下
方向に強制対流させることにより、藻類の死滅と
溶存酸素量を増加する試みがなされ、相当の成果
を収めていた。
(Prior art) Conventionally, in dams, lakes, marshes, rivers, etc., as water temperature rises, algae breeds, fish die due to lack of oxygen in the water, bad odors occur, and water quality deteriorates due to other causes. However, there was no effective prevention method, and for example, filtration using activated carbon was considered. In addition, in deep dams, lakes, etc., attempts have been made to kill algae and increase the amount of dissolved oxygen by forcing the water in the dam to move upward and downward using intermittent air pumping devices, with considerable success. It was contained.

前記水深が大きい場合には、表層の水と、深層
の水とが滞留することによつて、表層に多生する
藻類を水底の暗所に送り込み、藻類の弱化及び死
滅によりその繁殖を防ぎ、殺藻の目的をも達成で
きた。
When the water depth is large, surface water and deep water stagnate, sending algae that grow abundantly on the surface to a dark place at the bottom of the water, weakening and killing the algae to prevent their proliferation, The purpose of algaecide was also achieved.

(発明によつて解決すべき問題点) 然るに浅水域に揚水筒を設置し、水を対流させ
ても、水面の藻類が若干下方へ移るだけで、これ
を死滅させることは不可能である。また汚水の大
部分は水中に微細固形物が浮遊している為である
が、これを効率よく沈澱させる手段がなく、かつ
酸欠改善の手段もなかつた。
(Problems to be Solved by the Invention) However, even if a water pump is installed in shallow water and water is convected, the algae on the water surface will only move slightly downward, and it will be impossible to kill them. Furthermore, most of the sewage is caused by fine solid matter floating in the water, but there is no way to efficiently precipitate this, and there is no way to improve oxygen deficiency.

従来、泥水槽内に凝集剤を混入し、固形物をフ
ロツク化して沈澱させる技術は知られていたが、
何百万トン以上という大水量の湖、沼では凝集剤
等を攪拌混合する手段がなかつたので、前記技術
を実用化することはできなかつた。
Conventionally, the technology of mixing a flocculant into a muddy water tank to flocculate and precipitate solids was known, but
Since there was no means to stir and mix flocculants and the like in lakes and ponds with large water volumes of millions of tons or more, it was not possible to put the above technology into practical use.

(問題点解決の手段) そこでこの発明は、湖・沼又は貯水場などの所
定の水深の位置に(たまたま深い場所があればそ
の位置、なければ人工的に造成する。例えば2m
以上であれば可能)揚水筒を設置し、前記揚水筒
によつて水を循環流動させる過程で凝集剤又は殺
藻剤、或いは凝集剤と殺藻剤とを拡散させること
により、浮遊固形物を凝集沈澱させ、又は固形物
を沈澱させると共に、藻類を死滅させて、比較的
容易に浄水目的を達成したものである。
(Means for Solving Problems) Therefore, the present invention aims to create a water depth at a predetermined depth such as a lake, a pond, or a water storage field (if there is a deep place by chance, then artificially create it at that location, for example, 2m).
(Possible if the above is possible) By installing a water pump and dispersing the flocculant or algaecide, or the flocculant and algaecide during the process of circulating and flowing water through the water pump, suspended solids can be removed. The purpose of water purification is achieved relatively easily by coagulating sedimentation or precipitating solid matter and killing algae.

前記における凝集剤としては、例えば硫酸アル
ミニウム、ポリ塩化アルミニウムその他の高分子
凝集剤が考えられ、殺藻剤としては、硫酸銅又は
塩化銅が考えられる。
Examples of the flocculant mentioned above include aluminum sulfate, polyaluminum chloride, and other polymer flocculants, and examples of the algaecide include copper sulfate or copper chloride.

また揚水筒は、水の対流循環上、水深2m以上
の所においてより効率よく動作するので、例えば
第1図図示のように、表層部と下層部とが対流し
易い形状であることが望ましい。そこで水深を必
要深さとする為に人工的に水底を堀削して(例え
ばサンドポンプなど利用)第1図図示のような水
底形状とすることもできる。
In addition, since the water pump operates more efficiently in water depths of 2 m or more due to the convective circulation of water, it is desirable that the top layer and the lower layer have a shape that facilitates convection, as shown in FIG. 1, for example. Therefore, in order to make the water depth the required depth, the water bottom can be artificially excavated (for example, by using a sand pump) to form the water bottom shape as shown in FIG.

前記凝集剤又は殺藻剤が液体として与えられる
時には、第1図図示のように、揚水筒の一部に給
液管を臨ませ、所定量宛の前記液剤を供給すれ
ば、目的を達成することもできる。前記において
は、湖・沼等の中へ揚水筒を設置することについ
て説明したけれども、湖・沼又は河川から必要量
の処理水を貯水場に導き、該貯水場内へ揚水筒を
設置して、固形物を沈澱させ、又は固形物の沈澱
と殺藻とを同時に、或いは順次に行わせる場合も
ある。
When the flocculant or algaecide is applied as a liquid, the purpose can be achieved by placing a liquid supply pipe facing a part of the water pump and supplying a predetermined amount of the liquid as shown in Figure 1. You can also do that. In the above, we explained about installing a water pump in a lake, pond, etc., but it is also possible to lead the required amount of treated water from the lake, pond or river to a water storage field, install a water pump in the water storage field, The solids may be precipitated, or the solids may be precipitated and algaecide simultaneously or sequentially.

また凝集剤が固形で与えられる時には、揚水筒
の上方に、薬剤入りの容器を浮遊させておき、適
宜溶解して拡散するようにしておくと、必要な濃
度に拡散させることができる。
Further, when the flocculant is given in solid form, it is possible to diffuse it to the required concentration by floating a container containing the agent above the water pump and dissolving and dispersing it as appropriate.

尚、殺藻剤の濃度は0.2ppm〜1.0ppmが適当で
ある。この程度の濃度ならば、魚などが殺すこと
なく、殺藻目的を達成することが確認された。
In addition, the appropriate concentration of the algaecide is 0.2 ppm to 1.0 ppm. It was confirmed that at this level of concentration, the purpose of algaecide was achieved without killing fish etc.

(作用) 即ちこの発明によれば、凝集剤と殺藻剤とを同
時又は別々に拡散させるので、水中の微細固形物
が沈澱し、藻類が死滅し、かつ揚水筒の作用によ
り水中溶存酸素量を向上させることができる。
(Function) That is, according to the present invention, since the flocculant and the algaecide are diffused simultaneously or separately, fine solids in the water are precipitated, algae are killed, and the amount of dissolved oxygen in the water is reduced by the action of the water pump. can be improved.

実施例 1 次にこの発明の実施例を第1図乃至第3図につ
いて説明する。
Embodiment 1 Next, an embodiment of the present invention will be described with reference to FIGS. 1 to 3.

第1図において、水深5m(鎖線37)の水底
を実線図示37aのように堀削し、最深部を7m
とし、該部へ揚水筒1を設置する。この揚水筒1
の設置場所は、水量、水深および水底の形状によ
つて異なるが、例えば水量30万トン〜50万トン毎
に直径50cmの揚水筒1基を設置する。第1図の場
合に、揚水は矢示38,38aのように左右へ拡
散され、水面から水底に下降し、水底をはつて揚
水筒1に到つて当初のように再び揚水され、これ
を繰返すことになる。また第2図は湖40に対す
る揚水筒1,1a,1b,1cの設置位置を示
す。次に第3図は湖41の一側へ鎖線43より放
水路42に亘る間に人工水路39を作り、該部の
みへ揚水筒1,1aを設置したのいである。何れ
にしても通過する水を全部浄水しようという構成
になつている。
In Figure 1, the bottom of the water at a depth of 5 m (dashed line 37) is excavated as shown by the solid line 37a, and the deepest part is 7 m.
Then, the water pumping cylinder 1 is installed in that part. This water pump 1
The installation location varies depending on the water volume, water depth, and shape of the water bottom, but for example, one water pump with a diameter of 50 cm is installed for every 300,000 to 500,000 tons of water volume. In the case of Fig. 1, the pumped water is spread to the left and right as shown by arrows 38 and 38a, descends from the water surface to the bottom, crawls through the bottom, reaches pumping tube 1, is pumped up again as before, and repeats this process. It turns out. Further, FIG. 2 shows the installation positions of the pumping cylinders 1, 1a, 1b, and 1c with respect to the lake 40. Next, as shown in FIG. 3, an artificial waterway 39 is created extending from the chain line 43 to the discharge channel 42 on one side of the lake 41, and the water pumps 1, 1a are installed only in this area. In any case, the system is designed to purify all the water that passes through it.

実施例 2 次にこの発明の実施例を第4図乃至第6図に示
す装置に基いて説明する。
Embodiment 2 Next, an embodiment of the present invention will be described based on the apparatus shown in FIGS. 4 to 6.

下部に空気室2を設けた揚水筒1の上方へ(例
えば水面と揚水筒1の上端との中間)、硫酸銅容
器3および凝集剤容器3aを円形状に配置し、浮
子4によつて硫酸銅および凝集剤容器3,3aを
所定の水深に安定させる。例えば硫酸銅および凝
集剤容器3,3aの下側と揚水筒1の上端とを索
条5で連結し、浮子4と硫酸銅および凝集剤容器
3,3aとを索条6で連結して設置位置を定め
る。硫酸銅および凝集剤容器3,3aはリング状
の内外枠7,7aの内側へ網袋8を固定して形成
され、網袋8内へ硫酸銅および凝集剤9,9aが
収容されている。硫酸銅および凝集剤9,9aの
量は、揚水筒1を設置するダム10(又は湖・沼
等)の水量と水質、揚水筒の数とによつて決める
が、溶解度との関係で、一度に必要以上の濃度に
溶解しないように網目を密にする。即ち計算通り
の速度で溶解するならば、水量に0.2ppmを乗じ
た量でよいけれども、通常は溶解度の早いことを
考慮して必要量の数分の1乃至数十分の1宛取付
けることが好ましい。揚水筒による撹拌効率と殺
藻剤又は凝集剤の拡散速度を考慮し、設置殺藻剤
が全部溶解した時に殺藻剤がダムの全水域に行渡
れば理想的である。
A copper sulfate container 3 and a flocculant container 3a are arranged in a circular shape above a water pump 1 having an air chamber 2 at the bottom (for example, between the water surface and the upper end of the water pump 1), and a float 4 is used to collect sulfuric acid. The copper and flocculant containers 3, 3a are stabilized at a predetermined water depth. For example, the lower side of the copper sulfate and flocculant containers 3, 3a and the upper end of the water pump 1 are connected with a cable 5, and the float 4 and the copper sulfate and flocculant containers 3, 3a are connected with a cable 6. Determine the position. The copper sulfate and flocculant containers 3, 3a are formed by fixing a mesh bag 8 to the inside of ring-shaped inner and outer frames 7, 7a, and the mesh bag 8 accommodates copper sulfate and flocculant 9, 9a. The amounts of copper sulfate and flocculants 9, 9a are determined depending on the water volume and quality of the dam 10 (or lake, marsh, etc.) where the pumping tube 1 is installed, and the number of pumping tubes. Make the mesh dense so that it does not dissolve at a concentration higher than necessary. In other words, if it dissolves at the calculated rate, the amount of water multiplied by 0.2 ppm will suffice, but considering the rapid solubility, it is usually recommended to install it at a fraction of the required amount. preferable. Considering the agitation efficiency of the water pump and the diffusion rate of the algaecide or coagulant, it would be ideal if the algaecide would be distributed throughout the entire water area of the dam when all of the installed algaecide is dissolved.

この発明の殺藻剤容器は、第5図で図示し、前
記に説明したようにリング状内外枠7,7aの内
側へ網袋8を固定し、網袋8内へ硫酸銅又は凝集
剤を収容したものであり、揚水筒1内を上昇した
水が第4図中矢示11,11のように四方へ流動
する時、前記網袋8内を通過して硫酸銅又は凝集
剤を溶解するのであるが、このような容器では溶
解度の調節がむつかしく、予め網目によつて過度
の溶解ができないようにしておく必要がある。
The algaecide container of the present invention is illustrated in FIG. 5, and as described above, a mesh bag 8 is fixed inside the ring-shaped inner and outer frames 7, 7a, and copper sulfate or a flocculant is poured into the mesh bag 8. When the water rising in the water pumping tube 1 flows in all directions as shown by arrows 11 and 11 in FIG. 4, it passes through the mesh bag 8 and dissolves the copper sulfate or flocculant. However, it is difficult to adjust the solubility in such containers, and it is necessary to prevent excessive dissolution by using a mesh in advance.

前記実施例においては、揚水筒の上部周辺へ殺
藻剤および凝集剤容器を設置することによつて、
必要濃度の殺藻剤および凝集剤を発生拡散させた
が、殺藻剤および凝集剤が液状で与えられる場合
には、揚水筒1の中間部内側へ殺藻剤用のノズル
を設置し、パイプ13を介して必要量の殺藻剤等
を供給すればよいことになる。この場合に先ず凝
集剤を送り、次いで殺藻剤を送ることができる。
図中12は薬液タンクである。
In the above embodiment, by installing algaecide and flocculant containers around the upper part of the water pump,
The required concentration of algaecide and flocculant was generated and diffused. However, if the algaecide and flocculant are to be given in liquid form, an algaecide nozzle is installed inside the middle part of the water pump 1, and the pipe The required amount of algaecide, etc. may be supplied through the 13. In this case, the flocculant can be fed first and then the algaecide.
In the figure, 12 is a chemical tank.

この発明に使用する揚水装置は、揚水筒1の下
端部に空気室2を設け、これに加圧空気を送気管
16より矢示17のように送入する。然る時に、
加圧空気は先ず外筒室18内へ送り込まれ、外筒
室18の頂部より逐次溜つて、外筒室18内の水
位を下降させると共に、仕切筒19の上部に設け
た透孔20より矢示21のように中間室22に入
り、中間室22の水位を下げる。次いで水位が第
6図中鎖線23の位置に達すると、中間室内の加
圧空気は内筒24の下端部に設けた連通孔25を
経て矢示26のように内筒室27内へ入り、内筒
室27を矢示28のように上昇し、その上部より
連通孔29を経て矢示30のように揚水筒1内へ
噴出する。従つて加圧空気は空気団31となつて
揚水筒内を上昇するので、揚水筒の下部の水は空
気団の上昇につれて矢示15のように上昇し、揚
水筒1の上端より吹き出し、矢示11のように横
方向へ流動するが(第4図)、この水の一部は硫
酸銅又は凝集剤容器内を通過するので、内容硫酸
銅等を逐次溶解し、その溶解液は水の流れにつれ
て拡散し、かつ上下対流につれて矢示33,33
aのように水底側へも下降し、水底付近に下降し
て弱化した藻類を更に弱め、遂には殺すことにな
る。図中32は加圧空気のホース、35は重錘、
36は揚水筒1の上端部に設けた浮子である。
The water pumping device used in this invention has an air chamber 2 at the lower end of a water pumping cylinder 1, into which pressurized air is fed from an air pipe 16 as shown by an arrow 17. When the time comes,
The pressurized air is first sent into the outer cylinder chamber 18, and is gradually accumulated from the top of the outer cylinder chamber 18, lowering the water level in the outer cylinder chamber 18, and flowing through the through hole 20 provided in the upper part of the partition cylinder 19. The water enters the intermediate chamber 22 as shown in Fig. 21 and lowers the water level in the intermediate chamber 22. Next, when the water level reaches the position indicated by the chain line 23 in FIG. The water rises through the inner cylinder chamber 27 as shown by the arrow 28, and is ejected from the upper part of the tank through the communication hole 29 into the water pumping cylinder 1 as shown by the arrow 30. Therefore, the pressurized air becomes an air mass 31 and rises inside the water pump, so the water at the bottom of the water pipe rises as the air mass rises as shown by arrow 15, blows out from the upper end of the water pipe 1, and rises as shown by the arrow 15. As shown in Figure 11, it flows in the horizontal direction (Figure 4), but some of this water passes through the copper sulfate or flocculant container, so the copper sulfate, etc. contained therein is sequentially dissolved, and the dissolved liquid is mixed with water. Diffusion as the flow progresses, and arrows 33, 33 as the vertical convection
As shown in a, it also descends to the bottom of the water, further weakening the weakened algae as it descends near the bottom, and eventually kills them. In the figure, 32 is a pressurized air hose, 35 is a weight,
36 is a float provided at the upper end of the water pump 1.

(発明の効果) 即ちこの発明によれば、揚水筒の揚水循環を利
用して水を上下循環流動させ、の過程で殺藻剤お
よび/または凝集剤を入れてこれを拡散させたの
で、曝気と同時に薬剤を拡散し、溶存酸素量の増
大と、微細固形物の沈澱および藻類の死滅によつ
て、大量水を容易、確実に浄水し得る効果があ
る。
(Effects of the Invention) That is, according to the present invention, water is circulated up and down using the water pumping cycle of the water pump, and in the process, algaecide and/or flocculant are added and dispersed, so that no aeration is required. At the same time, it has the effect of easily and reliably purifying large amounts of water by diffusing chemicals, increasing the amount of dissolved oxygen, precipitation of fine solids, and killing algae.

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

第1図はこの発明の実施状態における断面図、
第2図は同じく湖沼へ直接装置を設置した平面
図、第3図は同じく湖沼に浄水部を設けた場合の
平面図、第4図は揚水筒の上方に薬剤容器を設置
した正面図、第5図は殺藻剤および凝集剤容器の
一部を破切した拡大正面図、第6図は同じく空気
室の一部拡大断面図である。 1,1a,1b,1c……揚水筒、2……空気
室、3,3a……硫酸銅および凝集剤容器、4
0,41……湖、42……放水路。
FIG. 1 is a sectional view of the present invention in its implementation state;
Figure 2 is a plan view of the device installed directly in a lake, Figure 3 is a plan view of a water purification section installed in a lake, Figure 4 is a front view of a drug container installed above the water pump, FIG. 5 is an enlarged front view with a portion of the algaecide and flocculant container cut away, and FIG. 6 is a partially enlarged sectional view of the air chamber. 1, 1a, 1b, 1c... Water tank, 2... Air chamber, 3, 3a... Copper sulfate and flocculant container, 4
0,41... Lake, 42... Spillway.

Claims (1)

【特許請求の範囲】 1 湖・沼・貯水池又は河川などの被処理水中
に、揚水筒により水を上下循環流動させる過程
で、凝集剤および殺藻剤を入れて水流により拡散
させ、これにより浮遊固形物を凝集沈澱させおよ
び藻類を死滅させて淨水処理すると共に、水中の
溶存酸素量を向上させることを特徴とした浅水域
における淨水方法。 2 湖・沼・貯水池又は河川などの被処理水中
に、揚水筒により水を上下循環流動させる過程
で、凝集剤又は殺藻剤を入れて水流により拡散さ
せ、これにより浮遊固形物を凝集沈澱させ、又は
藻類を死滅させて浄水処理すると共に、水中の溶
存酸素量を向上させることを特徴とした浅水域に
おける浄水方法。 3 凝集剤又は殺藻剤は同時に拡散させ、又は個
別に順次拡散させた特許請求の範囲第1項記載の
浅水域における浄水方法。 4 凝集剤はポリ塩化アルミニウム、硫酸アルミ
ニウム又はその他の高分子凝集剤とした特許請求
の範囲第1項記載の浅水域における浄水方法。 5 殺藻剤は硫酸銅又は塩化銅とした特許請求の
範囲第1項記載の浅水域における淨水方法。
[Claims] 1. In the process of circulating water up and down in a water pump such as a lake, marsh, reservoir, or river, a flocculant and an algaecide are added and dispersed by the water flow, thereby causing suspension. A method for effusion in shallow water, characterized by treating effluent by coagulating and precipitating solids and killing algae, and improving the amount of dissolved oxygen in water. 2 In the process of circulating water up and down in water to be treated, such as lakes, marshes, reservoirs, or rivers, using water pumps, a flocculant or algaecide is added and dispersed by the water flow, which causes suspended solids to coagulate and settle. , or a water purification method for shallow water, characterized by purifying water by killing algae and improving the amount of dissolved oxygen in the water. 3. The water purification method in shallow waters according to claim 1, wherein the flocculant or algaecide is diffused simultaneously or individually sequentially. 4. The water purification method in shallow waters according to claim 1, wherein the flocculant is polyaluminum chloride, aluminum sulfate, or other polymer flocculant. 5. The method for sterilizing water in shallow waters according to claim 1, wherein the algaecide is copper sulfate or copper chloride.
JP14490285A 1985-07-02 1985-07-02 Clarification of water in sharrow water area Granted JPS626010A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP14490285A JPS626010A (en) 1985-07-02 1985-07-02 Clarification of water in sharrow water area

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP14490285A JPS626010A (en) 1985-07-02 1985-07-02 Clarification of water in sharrow water area

Publications (2)

Publication Number Publication Date
JPS626010A JPS626010A (en) 1987-01-13
JPH0519603B2 true JPH0519603B2 (en) 1993-03-17

Family

ID=15372964

Family Applications (1)

Application Number Title Priority Date Filing Date
JP14490285A Granted JPS626010A (en) 1985-07-02 1985-07-02 Clarification of water in sharrow water area

Country Status (1)

Country Link
JP (1) JPS626010A (en)

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS59118913A (en) * 1982-12-22 1984-07-09 Kaiyo Kogyo Kk Prevention of freezing of water surface

Also Published As

Publication number Publication date
JPS626010A (en) 1987-01-13

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