JP2873387B2 - Closed water purification facility - Google Patents

Closed water purification facility

Info

Publication number
JP2873387B2
JP2873387B2 JP2081619A JP8161990A JP2873387B2 JP 2873387 B2 JP2873387 B2 JP 2873387B2 JP 2081619 A JP2081619 A JP 2081619A JP 8161990 A JP8161990 A JP 8161990A JP 2873387 B2 JP2873387 B2 JP 2873387B2
Authority
JP
Japan
Prior art keywords
water
breakwater
tide level
seawater
area
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
JP2081619A
Other languages
Japanese (ja)
Other versions
JPH03278885A (en
Inventor
千明 丹羽
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.)
Shimizu Construction Co Ltd
Original Assignee
Shimizu 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 Shimizu Construction Co Ltd filed Critical Shimizu Construction Co Ltd
Priority to JP2081619A priority Critical patent/JP2873387B2/en
Publication of JPH03278885A publication Critical patent/JPH03278885A/en
Application granted granted Critical
Publication of JP2873387B2 publication Critical patent/JP2873387B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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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

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  • Revetment (AREA)
  • Biological Treatment Of Waste Water (AREA)

Description

【発明の詳細な説明】 「産業上の利用分野」 本発明は、閉鎖性水域の浄化に適した海水、河水、湖
水等の浄化施設に関する。
Description: TECHNICAL FIELD The present invention relates to a purification facility for seawater, river water, lake water, etc., which is suitable for purifying closed water bodies.

「従来の技術」 先に本発明者らは特願平1−137298号において、港湾
等の海水等の浄化に適した施設を提案した。
"Prior art" The present inventors have previously proposed in Japanese Patent Application No. 1-137298 a facility suitable for purifying seawater in a port or the like.

第4図は、発明者らが提案した浄化施設である。この
浄化施設は、重力式消波堤をなす函状のケーソン1の内
部に接触材としての礫2…が充填されたものである。ケ
ーソン1の上部には、該ケーソン1の前面側および天面
側に開口した多数の湾曲水路からなるマルチセル型導水
部3が設けられている。この導水部3の前面側の開口は
海水の流入口4とされ、天面側の開口は噴き上げ口5と
なっている。噴き上げ口5の後方には、噴き上げ口5か
ら噴き上げられた海水をケーソン1内部に取り入れる上
部取水口6が形成されている。この上部取水口6は、満
潮位以上の位置に設けられている。またケーソン1の下
部には、ケーソン1内を通過した海水を後方の海域に導
出させる導出口7…が形成されている。
FIG. 4 shows a purification facility proposed by the inventors. In this purification facility, a caisson 1 in the form of a gravity type breakwater is filled with gravel 2... As a contact material. At the upper part of the caisson 1, there is provided a multi-cell type water guide section 3 composed of a large number of curved water passages opened on the front side and the top side of the caisson 1. The opening on the front side of the water guiding section 3 is an inlet 4 for seawater, and the opening on the top side is a spout 5. Behind the jet port 5, an upper intake port 6 for taking in the seawater spouted from the jet port 5 into the caisson 1 is formed. The upper intake port 6 is provided at a position higher than the high tide level. At the lower part of the caisson 1, there are formed outlets 7 for drawing seawater that has passed through the caisson 1 to the sea area behind.

この浄化施設では、前方海域の海水が波力によって流
入口4…から導水部3に流入する。導水部3に流入した
海水は、進行方向を上方に湾曲されて噴き上げ口5から
上方に噴き上げられ、これにより曝気され溶存酸素が増
加する。こうして曝気された海水は。上部取水部6から
ケーソン1内部に入り、礫2…の表面に付着した微生物
によって好気的に浄化される。そしてこのように浄化さ
れた海水は、導出口7からかケーソン1の後部へ流出す
る。
In this purification facility, the seawater in the front sea area flows into the water guide section 3 from the inflow ports 4. The seawater that has flowed into the water guide section 3 is curved upward in the traveling direction and is blown upward from the blow-up port 5, thereby being aerated and the dissolved oxygen being increased. The seawater aerated in this way. The caisson 1 enters the caisson 1 through the upper water intake 6 and is aerobically purified by microorganisms attached to the surface of the gravel 2. The purified seawater flows out from the outlet 7 to the rear of the caisson 1.

「発明が解決しようとする課題」 先に提案した浄化施設にあっては、礫2…によって形
成された広い表面によって多量の微生物膜が保持されて
おり、極めて高い水質浄化効果を期待できる。
[Problems to be Solved by the Invention] In the purification facility proposed above, a large amount of microbial membranes is held by the wide surface formed by the pebbles 2, and an extremely high water purification effect can be expected.

しかしながら前記浄化施設では波浪の強弱によってケ
ーソン1内に入る海水の量が変動するので、この浄化施
設を用いて所定の海域を周辺海域から仕切り閉鎖性海域
を形成すると、閉鎖性海域に取り込める海水量が極めて
不安定となり、波が穏やかなときには海水取り込み量が
不足ことが懸念される。また閉鎖性海域を浄化する能力
に付いても安定性に欠ける不安があった。
However, since the amount of seawater entering the caisson 1 fluctuates depending on the strength of the waves in the purification facility, if a predetermined sea area is partitioned from the surrounding sea area to form a closed sea area using this purification facility, the amount of seawater that can be taken into the closed sea area Becomes extremely unstable, and when the waves are calm, there is a concern that the intake of seawater may be insufficient. There was also a lack of stability regarding the ability to purify closed sea areas.

本発明は前記事情に鑑みてなされたもので、周辺水域
の水を安定に閉鎖性海域へ取り込むことができると共
に、閉鎖性水域内の水質を良好に保つことができる閉鎖
性水域の浄化施設を提供することを目的とする。
The present invention has been made in view of the above-mentioned circumstances, and a purification facility for closed water bodies capable of stably taking water in surrounding water bodies into closed sea areas and maintaining good water quality in closed water areas. The purpose is to provide.

「課題を解決するための手段」 本発明の閉鎖性水域の浄化施設は、満潮位以上の高さ
に上部取水口を有する消波堤の後側に、内部水域と周辺
水域とを仕切る仕切り堤が連設され、これら消波堤およ
び仕切り堤の内部に微生物が付着し得る接触材が充填さ
れ、消波堤と仕切り堤との隔壁に干潮位以下に位置する
連通孔が穿設され、仕切り堤の内部水域側の壁部に干潮
位以上、中等潮位以下に位置する処理水導出口が穿設さ
れると共に、周辺水域から仕切り堤内部に直接周辺水域
の水を取り入れる直接取水部が満潮位以下、中等潮位以
上の位置に間欠的に設けられたものである。
"Means for Solving the Problems" The purification facility for closed water bodies of the present invention is a partition wall that separates an internal water area from a surrounding water area behind a breakwater having an upper intake at a height higher than the high tide. The breakwater and the partition wall are filled with a contact material to which microorganisms can adhere, and the partition wall between the breakwater and the partition wall is provided with a communication hole located at a low tide or lower, and the partition wall is formed. A treated water outlet located at a low tide level and below the middle tide level is drilled in the wall on the inner water body side of the dike, and a direct intake part that takes in water from the surrounding water area directly from the surrounding water area to the inside of the dike is at high tide. Below, it is provided intermittently at a position above the middle tide level.

ここで閉鎖性水域とは、周辺水域と完全に仕切られた
内部水域のみでなく、水位をコントロールできる状態で
周辺水域と一部連通されたような内部水域も含むものと
する。
Here, the closed water area includes not only an internal water area completely separated from the surrounding water area, but also an internal water area partially connected to the peripheral water area in a state where the water level can be controlled.

前記接触材としては、かき殻等の貝殻、波板等のプラ
スチック成形体、コンクリートブロック等の無機物の成
形体、砂利、、砕石、玉石など微生物膜が成長するもの
であれば、各種のものを利用できる。
Examples of the contact material include shells such as oysters, plastic molded articles such as corrugated sheets, inorganic molded articles such as concrete blocks, gravel, crushed stones, crushed stones, and other materials that can grow microbial membranes such as boulders. Available.

またここで中等潮位とは、平均満潮位と平均干潮位と
の和の1/2の高さ位置を示すものとする。
Here, the medium tide level indicates a height position that is half the sum of the average high tide level and the average low tide level.

この閉鎖性水域の浄化施設には、内部水域の水を周辺
水域へ排出する排出路を別途設けてると良い。そして内
部水域の水位を中等潮位を中心として周辺海域の干満潮
位の範囲内で変動させるように制御すると良い。
The purification facility for closed water bodies may be provided with a separate discharge path for discharging water from the internal water bodies to surrounding water bodies. Then, it is preferable to control the water level of the internal water area so as to fluctuate within the range of the ebb and tide level of the surrounding sea area centering on the middle tide level.

前記排出路には、閉鎖性水域の海水を適宜な時期に適
宜な時間放流できるように、電磁弁を設けると良い。ま
た排出路からの放流量は、内部水域と周辺水域との水位
差、排出路の解放時間等によって制御されるが、制御に
際しては希望する海水の交換率や潮位変動パターン、閉
鎖性水域内の汚濁物の内部生産や自己分解、浄化施設の
浄化能力や汚泥負荷のバランス等を考慮する必要があ
る。
The discharge passage may be provided with an electromagnetic valve so that seawater in the closed water area can be discharged at an appropriate time and for an appropriate time. The discharge rate from the discharge channel is controlled by the water level difference between the internal water area and the surrounding water area, the release time of the discharge channel, etc.In controlling, the desired seawater exchange rate, tide level fluctuation pattern, It is necessary to consider the internal production and self-decomposition of pollutants, the purification capacity of the purification facility, and the balance of sludge load.

また前記制御の際には、閉鎖性水域の透明度(透視
度)、化学的酸素要求量(COD)、塩分濃度等のうち少
なくとも1つを指標として、その値が所定の範囲内に入
るように、排出路の開口時間帯、開口時間を調整し海水
交換率を管理することが望ましい。
At the time of the control, at least one of transparency (transparency), chemical oxygen demand (COD), salt concentration and the like of the closed water area is used as an index so that the value falls within a predetermined range. It is desirable to control the seawater exchange rate by adjusting the opening time zone and opening time of the discharge channel.

「作用」 本発明の閉鎖性水域の浄化施設では、満ち潮時など、
周辺水域の水位が上昇して中等潮位以上の所定の高さに
なると、直接取水部を介して周辺水域の海水が消波堤の
後側に設けられた仕切り堤に流入する。そしてこの仕切
り堤内で接触材に付着した微生物により浄化され、その
後、仕切り堤の内部水域側の壁部に設けられた処理水導
出口から内部水域へ流出する。
"Action" In the closed water purification facility of the present invention,
When the water level in the surrounding water area rises and reaches a predetermined height equal to or higher than the middle tide level, the seawater in the surrounding water area flows into the partition embankment provided behind the breakwater via the direct water intake section. Then, the water is purified by microorganisms attached to the contact material in the partition, and then flows out to the internal water from a treated water outlet provided in a wall on the internal water side of the partition.

他方、波浪エネルギーによって消波堤上部の取水口か
ら消波堤内に入る溶存酸素が付加された海水は、消波堤
内の接触材表面に成長した微生物により浄化され、つい
で消波堤と仕切り堤と間の隔壁の連通孔を介して仕切り
堤に流入する。この後海水は仕切り堤内で微生物による
浄化を受け、処理水導出口から内部水域へ流出する。
On the other hand, seawater to which dissolved oxygen added into the breakwater from the intake at the top of the breakwater due to wave energy is purified by microorganisms that have grown on the surface of the contact material in the breakwater, and then the breakwater and the partition wall It flows into the partition embankment through the communication hole of the partition between them. Thereafter, the seawater is purified by microorganisms in the partition embankment, and flows out from the treated water outlet into the internal water area.

このように本発明の浄化施設では、波浪エネルギーに
加えて潮位差によるエネルギーによっても周辺水域の海
水が内部水域に取り込まれるので、本発明の浄化施設に
よれば、周辺水域の海水を効率良く閉鎖性水域へ取り込
むことができる。
As described above, in the purification facility of the present invention, the seawater in the surrounding water area is taken into the internal water area by the energy due to the tidal level in addition to the wave energy. Therefore, according to the purification facility of the present invention, the seawater in the surrounding water area is efficiently closed. Can be taken into sexual waters.

「実施例」 以下、図面を参照して本発明の閉鎖性水域の浄化施設
を詳しく説明する。なお前記従来例と同一構成部分に
は、同一符号を附して説明を簡略化する。
"Example" Hereinafter, a purification facility for closed water bodies of the present invention will be described in detail with reference to the drawings. The same components as those of the conventional example are denoted by the same reference numerals, and the description will be simplified.

第1図ないし第3図は本発明の閉鎖性水域の浄化施設
の一実施例を示すもので、図中符号10は消波堤である。
この消波堤10は、前記従来の浄化施設で用いたケーソン
1…によって形成されている。
1 to 3 show an embodiment of a purification facility for closed water bodies according to the present invention, wherein reference numeral 10 denotes a breakwater.
The breakwater 10 is formed by caissons 1 used in the conventional purification facility.

この消波堤10の後側には、内部海域11と周辺海域12を
仕切る仕切り堤13が連設されている。この仕切り堤13の
内部には、礫2…が充填されている。
Behind the breakwater 10, a partition wall 13 that partitions the internal sea area 11 and the surrounding sea area 12 is provided continuously. The inside of the partition wall 13 is filled with gravel 2.

この仕切り堤13と消波堤10との間の隔壁14には、互い
の内部を連通する連通孔15…が穿設されている。この連
通孔15…は、干潮位A以下の位置に設けられている。ま
た仕切り堤10の内部海域11側の壁部16には、この浄化施
設で処理された海水が流出する処理水導出口17…が形成
されている。この処理水導出口17…は、干潮位A以上、
中等潮位B以下の位置に設けられている。
In the partition wall 14 between the partition wall 13 and the breakwater 10, communication holes 15 communicating with each other are formed. The communication holes 15 are provided at positions below the low tide level A. A treated water outlet 17 through which seawater treated in the purification facility flows out is formed in the wall 16 on the inner sea area 11 side of the partition wall 10. This treated water outlet 17 ...
It is provided at a position below the middle tide level B.

またこの浄化施設では、周辺海域12から仕切り堤10内
に直接外海水を取り入れる直接取水部18…が消波堤10を
貫いて3箇所設けられている。この直接取水部18…は、
満潮位C以下、中等潮位B以上の位置に設けられてい
る。
Further, in this purification facility, there are provided three direct water intake portions 18 for directly taking in outside seawater from the surrounding sea area 12 into the partition wall 10 through the breakwater 10. This direct water intake section 18…
It is provided at a position below the high tide level C and above the middle tide level B.

前記処理水導出口17…は、この直接取水部18…および
前記連通孔15…に対して水平方向にずれた位置に設けら
れている。
The treated water outlets 17 are provided at positions displaced in the horizontal direction with respect to the direct water intake portions 18 and the communication holes 15.

またこの浄化施設には、内部海域11の海水を周辺海域
12に放出するための排出路が設けられている(図示せ
ず)。そしてこの排出口には、電磁弁が設けられており
所望のタイミングで内部海域11の海水を放流できるよう
になっている。
In addition, this purification facility uses seawater from the inner sea area 11
A discharge path is provided for discharge to 12 (not shown). The discharge port is provided with an electromagnetic valve so that seawater in the internal sea area 11 can be discharged at a desired timing.

この閉鎖性水域の浄化施設では、満ち潮時、周辺海域
12の水位が上昇して所定の高さになると、第1図中矢印
で示すように、満潮位C以下、中等潮位B以上の高さに
設けられた直接取水部18を介して周辺海域12の海水が仕
切り堤13に直接流入する。そしてこの仕切り堤13内を下
降しつつ礫2…の表面に棲息する微生物により浄化さ
れ、その後、壁部16の処理水導出口17から内部海域11へ
流出する。
At the time of high tide, this purification facility in closed water
When the water level rises and reaches a predetermined height, as shown by the arrow in FIG. 1, the surrounding sea area 12 passes through a direct water intake section 18 provided at a height below the high tide level C and above the middle tide level B. Of seawater flows directly into the partition wall 13. The microorganisms living on the surface of the pebbles 2 are purified while falling down the partition wall 13, and then flow out from the treated water outlet 17 of the wall 16 into the internal sea area 11.

他方、第2図中矢印で示すように、波浪エネルギーに
よって消波堤10の上部取水口6から消波堤10内に入った
海水は、消波堤10内を堤の延長方向に流動しつつ下降し
消波堤10内の礫2…表面に棲息する微生物により浄化さ
れ、ついで消波堤10と仕切り堤13との隔壁14に設けられ
た連通孔15を介して仕切り堤13に流入する。そして、仕
切り堤13内を堤の延長方向に流動しつつ上昇し微生物に
よる浄化を受けたあと、処理水導出口17から内部海域11
へ流出する。
On the other hand, as indicated by the arrow in FIG. 2, seawater that has entered the breakwater 10 from the upper intake 6 of the breakwater 10 due to the wave energy flows in the breakwater 10 in the extension direction of the breakwater. The rubble 2 descends and is purified by microorganisms living on the surface of the breakwater 10, and then flows into the partition wall 13 through a communication hole 15 provided in a partition 14 between the breakwater 10 and the partition wall 13. After flowing through the partitioning levee 13 in the direction of extension of the levee and ascending and being purified by microorganisms, the treated water outlet 17 passes through the inner sea area 11
Leaks to

このようにこの浄化施設では、波浪エネルギーに加え
て潮位差によるエネルギーによっても周辺海域12の海水
が内部海域11に取り込まれるので、波浪の弱い日でも内
部海域11に海水を十分取り込むことができ、周辺海域12
から内部海域11へ取り込める海水量を安定させることが
できる。
Thus, in this purification facility, since the seawater in the surrounding sea area 12 is taken into the inner sea area 11 by the energy due to the tidal level in addition to the wave energy, it is possible to sufficiently take in the seawater into the inner sea area 11 even on a weak wave day, Surrounding sea area 12
It is possible to stabilize the amount of seawater that can be taken into the internal sea area 11 from the sea.

またこの浄化施設では、消波堤10の上部取水口6が満
潮位C以上の高さに設けられ、消波堤10と仕切り堤13と
の間の隔壁14の連通孔15が干潮位A以下の位置に設けら
れ、仕切り堤13の内部海域11側の壁部16の処理水導出口
17が干潮位A以上、中等潮位B以下の位置に設けられ、
周辺海域12から仕切り堤13内部に直接外海水を取り入れ
る直接取水部18が満潮位C以下、中等潮位B以上の位置
に設けられているので、上部取水口6から流入した海水
が消波堤10内を堤の延長方向に流動しつつ下降し次いで
仕切り堤13内を堤の延長方向に流動しつつ上昇したあと
処理水導出口17から内部海域11へ流出する一方、直接取
水部18から取り入れられた海水が消波堤10内を堤の延長
方向に流動しつつ下降したあと処理水導出口17から内部
海域11へ流出する。従ってこの浄化施設では上部取水口
6から取り入れられた海水も直接取水部18から取り入れ
られた海水も礫2…の表面に成長した微生物と長時間接
触し十分浄化されるので、内部海域11の水質を良好に保
つことができる。
In this purification facility, the upper intake port 6 of the breakwater 10 is provided at a height higher than the high tide level C, and the communication hole 15 of the partition wall 14 between the breakwater 10 and the partition wall 13 is lower than the low tide level A. And the treated water outlet of the wall 16 on the inner sea area 11 side of the partition wall 13
17 is provided at a low tide level A or higher and a middle tide level B or lower,
Since the direct water intake section 18 for directly taking in outside seawater from the surrounding sea area 12 to the inside of the partition wall 13 is provided at a position lower than the high tide level C and higher than the middle tide level B, the seawater flowing from the upper intake port 6 is subjected to the breakwater 10. It flows down in the direction of extension of the levee and descends, and then rises while flowing in the partition levee 13 in the direction of extension of the levee, and then flows out of the treated water outlet 17 into the internal sea area 11, while being taken in directly from the water intake section 18. The seawater descends while flowing in the breakwater 10 in the direction of extension of the breakwater, and then flows out from the treated water outlet 17 into the internal sea area 11. Therefore, in this purification facility, the seawater taken in from the upper intake port 6 and the seawater taken in directly from the intake section 18 come into contact with the microorganisms grown on the surface of the pebbles 2 for a long time and are sufficiently purified. Can be kept good.

なお前記実施例では、浄化施設で入り江の部分を仕切
った例を記載したが、本発明の閉鎖性水域の浄化施設は
河口を仕切る河口堰等にも利用できる。
In the above-mentioned embodiment, an example in which the inlet is partitioned by the purification facility is described. However, the purification facility of the closed water area according to the present invention can be used also for an estuary weir partitioning an estuary.

「発明の効果」 以上説明したように本発明の閉鎖性水域の浄化施設
は、満潮位以上の高さに上部取水口を有する消波堤の後
側に、内部水域と周辺水域とを仕切る仕切り堤が連設さ
れ、これら消波堤および仕切り堤の内部に微生物が付着
し得る接触材が充填され、消波堤と仕切り堤との隔壁に
干潮位以下に位置する連通孔が穿設され、仕切り堤の内
部水域側の壁部に干潮位以上、中等潮位以下に位置する
処理水導出口が穿設されると共に、周辺水域から仕切り
堤内部に直接周辺水域の水を取り入れる直接取水部が満
潮位以下、中等潮位以上の位置に間欠的に設けられた施
設である。
[Effect of the Invention] As described above, the enclosed water purification facility of the present invention is provided with a partition for separating the internal water area and the surrounding water area behind a breakwater having an upper intake at a height higher than the high tide. A breakwater is continuously provided, the inside of the breakwater and the partition wall is filled with a contact material to which microorganisms can adhere, and a communication hole located at a low tide level or lower is formed in a partition wall between the breakwater and the partition wall, A treated water outlet located at a low tide level or higher and a lower level than the middle tide level is bored in the wall on the side of the internal water area of the partition, and the direct intake section that takes in water from the surrounding water area directly into the partition wall from the surrounding water area. This facility is provided intermittently at a location below the middle tide level and above the middle tide level.

このような構成を備えた本発明の閉鎖性水域の浄化施
設では、満ち潮時、周辺水域の水位が上昇して所定の高
さになると、直接取水部を介して周辺水域の海水が消波
堤の後側に設けられた仕切り堤に流入する。そしてこの
仕切り堤内で浄化された後内部水域に流入する。
In the closed water purifying facility of the present invention having such a configuration, at the time of high tide, when the water level of the surrounding water area rises and reaches a predetermined height, the seawater in the surrounding water area is directly disintegrated by the breakwater. Flows into the partition wall provided on the rear side of. After being purified within the partition, the water flows into the internal water area.

他方、波浪エネルギーによって消波堤上部の取水口か
ら消波堤内に入った海水は、消波堤内で浄化されたあと
仕切り堤に流入し再び浄化された後、処理水導出口から
内部水域に導出する。
On the other hand, seawater that enters the breakwater from the intake above the breakwater due to the wave energy is purified in the breakwater, flows into the partition, is purified again, and is drawn out from the treated water outlet to the internal water area. I do.

このように本発明の浄化施設では、波浪エネルギーに
加えて潮位差によるエネルギーによっても周辺水域の水
が内部水域に取り込まれるので、波浪の弱い日でも内部
水域に十分水を取り込むことができ、閉鎖性水域への水
取り込み量を安定させることができる。
As described above, in the purification facility of the present invention, the water in the surrounding water area is taken into the internal water area by the energy due to the tidal level in addition to the wave energy. It is possible to stabilize the amount of water taken into a sexual water area.

また本発明の浄化施設では、消波堤の上部取水口が満
潮位以上の高さに設けられ、消波堤と仕切り堤との隔壁
の連通孔が干潮位以下の位置に設けられ、仕切り堤の内
部水域側の壁部の処理水導出口が干潮位以上、中等潮位
以下の位置に設けられ、周辺水域から仕切り堤内部に直
接周辺水域の水を取り入れる直接取水部が満潮位以下、
中等潮位以上の位置に設けられているので、上部取水口
から流入した海水は消波堤内を下降しついで仕切り堤内
を上昇したあと処理水導出口に達する一方、直接取水部
から取り入れられた海水は消波堤内を下降したあと処理
水導出口に達する。従って本発明の浄化施設では上部取
水口から取り入れられた海水も直接取水部から取り入れ
られた海水も堤の延長方向に流動すると共に上下方向へ
も導水されて接触材の表面に成長した微生物と長時間接
触し十分浄化されるので、内部水域の水質を良好に保つ
ことができる。
Further, in the purification facility of the present invention, the upper intake of the breakwater is provided at a height higher than the high tide level, and the communication hole of the partition wall between the breakwater and the partition wall is provided at a position lower than the low tide level. The treated water outlet on the wall on the side of the internal water area is located at a low tide level or higher and a middle tide level or lower, and the direct intake section that takes in water from the surrounding water area directly into the partition wall from the surrounding water area is below the high tide level.
Since the seawater is located at the middle tide level or higher, the seawater flowing in from the upper intake descends in the breakwater and then rises in the partition, reaches the treated water outlet, while the seawater taken in from the direct intake is After descending inside the breakwater, it reaches the treated water outlet. Therefore, in the purification facility of the present invention, the seawater taken in from the upper intake port and the seawater taken in directly from the intake section flow in the extension direction of the levee, and are also guided in the vertical direction, and the microorganisms that grow on the surface of the contact material and the length of the microorganism. Since the water is sufficiently contacted for a long time, the water quality in the internal water area can be kept good.

【図面の簡単な説明】 第1図ないし第3図は本発明の閉鎖性水域の浄化施設の
一実施例を示すもので、第1図は第3図中I−I線に沿
う断面図、第2図は第3図中II−II線に沿う断面図、第
3図は平面図、第4図は本発明者らが先に提案した浄化
施設を示す斜視図である。 A……干潮位、B……中等潮位、C……満潮位、2……
礫(接触材)、6……上部取水口、10……消波堤、11…
…内部海域、12……周辺海域、13……仕切り堤、14……
隔壁、15……連通孔、16……壁部、17……処理水導出
口、18……直接取水部
BRIEF DESCRIPTION OF THE DRAWINGS FIGS. 1 to 3 show an embodiment of a purification facility for closed water bodies according to the present invention. FIG. 1 is a sectional view taken along the line II in FIG. FIG. 2 is a sectional view taken along the line II-II in FIG. 3, FIG. 3 is a plan view, and FIG. 4 is a perspective view showing a purification facility previously proposed by the present inventors. A: Low tide, B: Medium tide, C: High tide, 2 ...
Gravel (contact material), 6 ... Upper intake, 10 ... Breakwater, 11 ...
… Inner sea area, 12 …… Surrounding sea area, 13 …… Partition embankment, 14 ……
Partition wall, 15: communication hole, 16: wall, 17: treated water outlet, 18, direct water intake

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】満潮位以上の高さに上部取水口を有する消
波堤の後側に、内部水域と周辺水域とを仕切る仕切り堤
が連設され、これら消波堤および仕切り堤の内部に微生
物が付着し得る接触材が充填され、消波堤と仕切り堤と
の隔壁に干潮位以下に位置する連通孔が穿設され、仕切
り堤の内部水域側の壁部に干潮位以上、中等潮位以下に
位置する処理水導出口が穿設されると共に、周辺水域か
ら仕切り堤内部に直接周辺水域の水を取り入れる直接取
水部が満潮位以下、中等潮位以上の位置に間欠的に設け
られたことを特徴とする閉鎖性水域の浄化施設。
Claims: 1. A breakwater that separates an internal water area from a surrounding water area is provided continuously behind a breakwater having an upper intake at a height equal to or higher than a high tide level. A contact material to which microorganisms can adhere is filled, a communication hole located below the low tide level is formed in the partition wall between the breakwater and the partition wall, and a low tide level and a middle tide level are formed in the wall on the internal water body side of the partition wall. The following treated water outlets have been drilled, and the direct water intake that takes in the water from the surrounding water area directly into the partition from the surrounding water area has been intermittently provided at a position below the high tide level and above the medium tide level. A closed water purification facility characterized by:
JP2081619A 1990-03-29 1990-03-29 Closed water purification facility Expired - Lifetime JP2873387B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2081619A JP2873387B2 (en) 1990-03-29 1990-03-29 Closed water purification facility

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2081619A JP2873387B2 (en) 1990-03-29 1990-03-29 Closed water purification facility

Publications (2)

Publication Number Publication Date
JPH03278885A JPH03278885A (en) 1991-12-10
JP2873387B2 true JP2873387B2 (en) 1999-03-24

Family

ID=13751345

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2081619A Expired - Lifetime JP2873387B2 (en) 1990-03-29 1990-03-29 Closed water purification facility

Country Status (1)

Country Link
JP (1) JP2873387B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP6814108B2 (en) * 2017-08-10 2021-01-13 日立造船株式会社 Breakwater system

Also Published As

Publication number Publication date
JPH03278885A (en) 1991-12-10

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