JP2003181465A - Engineering method for decontaminating water bottom - Google Patents
Engineering method for decontaminating water bottomInfo
- Publication number
- JP2003181465A JP2003181465A JP2001380581A JP2001380581A JP2003181465A JP 2003181465 A JP2003181465 A JP 2003181465A JP 2001380581 A JP2001380581 A JP 2001380581A JP 2001380581 A JP2001380581 A JP 2001380581A JP 2003181465 A JP2003181465 A JP 2003181465A
- Authority
- JP
- Japan
- Prior art keywords
- water
- pond
- treated
- coagulant
- circulating
- 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.)
- Withdrawn
Links
Landscapes
- Separation Of Suspended Particles By Flocculating Agents (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】この発明は、湖沼、池、河
川、港湾等の水底に沈殿しているヘドロ、汚泥、土砂や
水に浮遊しているアオコなどの藻類、懸濁固形分(S
S)、汚濁物質、悪臭原因物質などを凝集分離して、水
底の浄化を行うとともに水の清澄性を高める水底浄化工
法に関し、特に処理に際して産業廃棄物を発生しないよ
うにしたものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to sludge, sludge, sedimented algae such as water and water-blooming algae suspended on the bottom of water such as lakes, ponds, rivers and harbors, and suspended solids (S
S), a pollutant, an offensive odor-causing substance, and the like are aggregated and separated to purify the water bottom and improve the clarity of the water, and in particular, the industrial waste is not generated during the treatment.
【0002】[0002]
【従来の技術】港湾、湖沼、河川、池、掘割等において
は、時間の経過とともに水底に堆積していく土砂、ゴ
ミ、ヘドロなどを浚渫して取り除くことで、水深の確
保、悪臭発生の防止、水生生物の保護などを図ることが
なされている。この浚渫の際に発生する浚渫底泥は、含
水率に高い半固体状態のものであり、その処分が必要と
なる。2. Description of the Related Art In ports, lakes, lakes, rivers, ponds, excavations, etc., the depth of water and the prevention of offensive odors are secured by dredging and removing sediment, dust, and sludge that accumulate on the bottom of the water over time. , Protection of aquatic organisms has been made. The dredged bottom mud generated during this dredging is in a semi-solid state with a high water content and must be disposed of.
【0003】このような浚渫底泥の処分の1つの方法と
して、浚渫底泥を沈殿槽などに一旦貯め、この浚渫底泥
に硫酸バンド、PAC(ポリ塩化アルミニウム)やポリ
アクリレートなどの高分子系凝集剤などの各種凝集剤を
添加し、撹拌混合して、泥中の固形分を凝集させて沈殿
分離し、上澄水を港湾等に戻し、沈殿物を産業廃棄物と
して廃棄するものがある。As one method of disposing such dredged bottom mud, the dredged bottom mud is temporarily stored in a sedimentation tank or the like, and a sulfuric acid band, a polymer system such as PAC (polyaluminum chloride) or polyacrylate is added to the dredged bottom mud. There is a method in which various coagulants such as a coagulant are added, and the mixture is stirred and mixed to coagulate the solid content in the mud for precipitation separation, and the supernatant water is returned to a port or the like, and the precipitate is discarded as industrial waste.
【0004】しかしながら、この処分方法では、使用す
る凝集剤の種類によっては、上澄水のpHが酸側あるい
はアルカリ側に傾き、これを中和する必要があること、
固形分の沈殿に長時間を要し、処理に時間がかかるこ
と、沈殿物を産業廃棄物として廃棄処分することが現実
に困難であることなどの問題点がある。However, in this disposal method, depending on the type of the coagulant used, the pH of the supernatant water tends to the acid side or the alkali side, which needs to be neutralized.
There are problems that it takes a long time to precipitate the solid content, it takes a long time to process, and it is actually difficult to dispose of the precipitate as industrial waste.
【0005】また、沈殿物の減容を行うために沈殿物を
脱水処理することもあるが、脱水された分離水に汚濁物
質が含まれ、この分離水の廃水処理が改めて必要にな
る。さらに、従来の浚渫法では、水中に浮遊している藻
類、懸濁固形分などは除去されず、水は濁ったままの状
態で清澄化されないなどの不都合もある。Although the precipitate may be dehydrated in order to reduce the volume of the precipitate, the dehydrated separated water contains pollutants, and the waste water treatment of this separated water is required again. Further, the conventional dredging method has a disadvantage that algae suspended in water, suspended solids and the like are not removed, and the water is not clarified in a turbid state.
【0006】[0006]
【発明が解決しようとする課題】よって、本発明におけ
る課題は、水底に堆積している土砂、ヘドロ、汚泥等だ
けではなく、水中に浮遊している藻類、懸濁固形分など
を凝集、沈降させて処理することができ、沈降した固形
分等を産業廃棄物として改めて廃棄する必要がなく、さ
らには分離水の二次処理が不要である水底浄化工法を得
ることにある。Therefore, the object of the present invention is to aggregate and settle not only sediment, sludge, sludge, etc. accumulated on the bottom of the water, but also algae suspended in water, suspended solids, etc. The present invention is to obtain a water bottom purification method in which the precipitated solids and the like do not have to be discarded as industrial waste again and the secondary treatment of separated water is unnecessary.
【0007】[0007]
【課題を解決するための手段】かかる課題を解決するた
め、請求項1にかかる発明は、処理対象水域に浮かべた
作業船に水底の泥水を汲み上げ、これに凝集剤を添加、
混合し、この泥水をそのまま処理対象水域に戻すことを
特徴とする水底浄化工法である。請求項2にかかる発明
は、処理対象水域にこの水域を循環する循環水流を形成
し、この循環水流に凝集剤を添加することを特徴とする
水底浄化工法である。In order to solve such a problem, the invention according to claim 1 pumps up mud water at the bottom of a work vessel floated in a water area to be treated, and adds a coagulant thereto.
This is a water bottom purification method characterized by mixing and returning this muddy water as it is to the water area to be treated. The invention according to claim 2 is a water bottom purification method characterized in that a circulating water flow that circulates in the water body to be treated is formed, and a coagulant is added to the circulating water flow.
【0008】[0008]
【発明の実施の形態】以下、本発明を実施の形態に基づ
いて詳しく説明する。図1は、請求項1にかかる発明の
水底浄化工法の例を示すもので、処理対象水域が池の例
である。この池1には、1隻の以上の作業船2が浮かべ
られている。この作業船2は台船などであり、この船上
には、吸引装置3、吸引ポンプ4、凝集剤投入装置5、
撹拌槽6、発電機7などが搭載されている。BEST MODE FOR CARRYING OUT THE INVENTION Hereinafter, the present invention will be described in detail based on embodiments. FIG. 1 shows an example of the water bottom purification method of the invention according to claim 1, wherein the water area to be treated is an example of a pond. One or more work boats 2 are floated on this pond 1. The work boat 2 is a pier or the like, and a suction device 3, a suction pump 4, a flocculant charging device 5,
The stirring tank 6, the generator 7, etc. are mounted.
【0009】上記吸引装置3には池1の底にまで伸びる
吸引パイプ8が接続されている。この吸引パイプ8の先
端にはケージ9が取り付けられており、吸引ポンプ4の
動作で吸引装置3による池底の堆積物およびその周囲の
水(以下、泥水と言う。)が吸引されるようになってい
る。A suction pipe 8 extending to the bottom of the pond 1 is connected to the suction device 3. A cage 9 is attached to the tip of the suction pipe 8 so that the suction pump 4 operates to suck the sediment on the pond bottom and the water around it (hereinafter referred to as muddy water) by the suction device 3. Has become.
【0010】この吸引装置3に吸引された泥水は、乱流
状態でパイプ10を介して撹拌槽6に送り込まれるよう
になっている。この撹拌槽6は、通常の撹拌翼を有する
容量1〜5立方メートル程度のタンクなどであり、この
内部に凝集剤投入装置5から供給される粉末状の凝集剤
が添加されるようになっている。The muddy water sucked by the suction device 3 is sent to the stirring tank 6 through the pipe 10 in a turbulent state. The stirring tank 6 is a tank having a normal stirring blade and a capacity of about 1 to 5 cubic meters, and the like, into which the powdery coagulant supplied from the coagulant feeding device 5 is added. .
【0011】この凝集剤投入装置5は、撹拌槽6の上部
に設けられており、粉末状の凝集剤を貯蔵する貯蔵タン
クと、この貯蔵タンクの底部から落下する凝集剤を定量
的に送り出すスクリューフィダーなどのフィダーを有す
るもので、制御部からの制御信号により凝集剤の撹拌槽
6への添加量を制御できるようになっている。The coagulant feeding device 5 is provided at the upper part of the stirring tank 6, and a storage tank for storing the powdery coagulant and a screw for quantitatively feeding the coagulant falling from the bottom of the storage tank. A feeder such as a feeder is provided, and the amount of the flocculant added to the stirring tank 6 can be controlled by a control signal from the controller.
【0012】撹拌槽6において、凝集剤が添加、撹拌さ
れた泥水は、池底からの新たな泥水の吸引に伴って、撹
拌槽6の上部の排出口に接続された排出パイプ11から
再び池1に戻されるようになっている。ここで使用され
る凝集剤としては、無機系のシリカを主体とした粉末状
のもので、中性域で凝集速度の速いものが用いられる。
なお、発電機7は、吸引ポンプ4、撹拌槽6、凝集剤投
入装置5などに電力を供給するもので、池1が小さく、
その岸からこれら機器に直接配電可能であれば不要であ
る。The muddy water to which the flocculant has been added and stirred in the stirring tank 6 is re-drained from the discharge pipe 11 connected to the discharge port at the upper portion of the stirring tank 6 as new muddy water is sucked from the bottom of the pond. It is set back to 1. As the aggregating agent used here, a powdery one mainly composed of inorganic silica and having a high aggregating rate in a neutral region is used.
The generator 7 supplies electric power to the suction pump 4, the stirring tank 6, the coagulant feeding device 5, etc., and the pond 1 is small,
It is not necessary if the equipment can be directly distributed from the shore.
【0013】次に、この作業船2を用いた浄化方法を説
明する。池底から吸引ポンプ4により吸引装置3に吸引
された泥水を撹拌槽6に送り、ここで凝集剤投入装置5
から凝集剤を添加する。凝集剤の泥水への添加量は、泥
水中に含まれる汚泥等の種類、濃度等によって左右され
るが、通常泥水1000リットルに対して凝集剤60〜
150g程度とされる。Next, a purification method using this work boat 2 will be described. The muddy water sucked from the bottom of the pond by the suction pump 4 to the suction device 3 is sent to the stirring tank 6, where the coagulant feeding device 5
Add flocculant from. The amount of the flocculant added to the muddy water depends on the type and concentration of sludge contained in the muddy water, but usually 60 to 60 liters of the flocculant is added to 1000 liters of the muddy water.
It is about 150 g.
【0014】泥水中の汚泥、懸濁固形分などの濃度が1
0%を越えると、凝集剤の有効範囲を超えるため、希釈
して10%以内にする必要がある。この希釈には、泥水
を吸引する際に、池底の水を多量に吸い込むように、吸
引パイプ8の先端のケージ9の位置を調整する方法や、
処理後の撹拌槽6から排出される水を利用してこれを吸
引装置3に戻す方法がある。The concentration of sludge and suspended solids in mud water is 1
If it exceeds 0%, it exceeds the effective range of the coagulant, so it is necessary to dilute it to within 10%. For this dilution, when sucking muddy water, a method of adjusting the position of the cage 9 at the tip of the suction pipe 8 so that a large amount of water at the bottom of the pond is sucked,
There is a method of returning the water to the suction device 3 using the water discharged from the stirred tank 6 after the treatment.
【0015】撹拌槽6において、凝集剤が添加された泥
水は、撹拌翼で撹拌混合されたのち、順次撹拌槽6から
そのまま、すなわち凝集された固形分を沈殿、脱水等し
て分離することなく、水に懸濁した状態のまま、排出パ
イプ11から処理泥水として池1に戻される。このよう
に泥水に凝集剤を添加し、混合したものをそのまま池に
戻すところが本発明の特徴点であり、処理プロセスが極
めて簡単で済む効果が得られる。In the stirring tank 6, the muddy water to which the flocculant is added is stirred and mixed by the stirring blades, and then, as it is from the stirring tank 6 as it is, that is, without aggregating solid components by precipitation, dehydration or the like. While being suspended in water, it is returned from the discharge pipe 11 to the pond 1 as treated mud water. The feature of the present invention is that the coagulant is added to the muddy water and the mixture is returned to the pond as it is, and the treatment process can be extremely simple.
【0016】そして、このようにして撹拌槽6におい
て、泥水に上記凝集剤を添加すると、泥水に浮遊する
土、砂粒子や懸濁固形分などに結合していた毛管水が、
切り離され、自由水として分離される。この凝集現象に
より、泥水中に浮遊していた土砂粒子、懸濁固形分など
の固形分が相互に吸着しあい、フロック化して、小さな
塊となり、瞬時に沈降を開始する。When the above coagulant is added to the muddy water in the stirring tank 6 in this manner, the capillary water which has been bound to the soil, the sand particles and the suspended solids floating in the muddy water becomes
Separated and separated as free water. Due to this agglomeration phenomenon, solid particles such as sediment particles and suspended solid particles suspended in mud water are mutually adsorbed to form flocs and become small lumps, and immediately start to settle.
【0017】また、池1に戻された処理水でもこのよう
な凝集反応がさらに進行し、結果的に圧密性が高く、含
水比が低い処理土が池1の底に堆積する。これにより水
の透明度が上がり、清澄な水が得られるさらに、池1に
戻された処理水から凝集剤の一部が周囲の池の水に拡散
していき、そこにおいても上述の凝集反応が進行する。Further, even in the treated water returned to the pond 1, such a coagulation reaction further progresses, and as a result, treated soil having a high compaction property and a low water content is deposited on the bottom of the pond 1. As a result, the transparency of the water increases and clear water is obtained. Furthermore, a part of the flocculant diffuses from the treated water returned to the pond 1 into the water in the surrounding ponds, and the above-mentioned flocculation reaction also occurs there. proceed.
【0018】また、土砂粒子、懸濁固形分等の凝集、沈
殿と同時に泥水に浮遊しているアオコ等の藻類、有機物
質、悪臭原因物質などが上述のフロックに吸着して取り
込まれ、沈殿する。さらに、処理後の分離水は、無機系
の凝集剤を使用することで、そのpHが中性であり、そ
のまま排出しても環境に何ら悪影響を与えることがな
い。At the same time as agglomeration and sedimentation of sediment particles, suspended solids and the like, algae such as water-bloom and the like, organic substances and malodor causing substances that are floating in muddy water are adsorbed by the flocs described above and settled. . Furthermore, the separated water after treatment has a neutral pH by using an inorganic flocculant, and does not adversely affect the environment even if it is discharged as it is.
【0019】かくして、池1の底には、圧密性が高く、
含水比が低い処理土が堆積し、池水は清澄となる。そし
て、作業船2を池1内で巡航させることで、あるいは複
数の作業船2、2・・を使用することで、池1全体を浄
化することができる。Thus, the bottom of the pond 1 has high compaction,
Treated soil with a low water content is deposited and the pond water becomes clear. The entire pond 1 can be purified by cruising the work boat 2 in the pond 1 or by using a plurality of work boats 2, 2 ...
【0020】このような浄化工法では、凝集反応に伴っ
て発生する処理土が処理前に比べて減容されて池底に戻
されるため、処理土が産業廃棄物となることがなく、そ
の廃棄処分の手間が不要になるという実用上極めて有用
な効果が得られる。産業廃棄物の最終処分場がほとんど
ない現状では、産業廃棄物が発生しないことは実に大き
なメリットとなるものである。In such a purification method, the treated soil generated by the coagulation reaction is reduced in volume as compared with that before the treatment and is returned to the bottom of the pond, so that the treated soil does not become an industrial waste and is discarded. A practically extremely useful effect is obtained in that the labor of disposal is unnecessary. In the present situation where there is almost no final disposal site for industrial waste, the fact that no industrial waste is generated is a great advantage.
【0021】また、このように処理土の二次処理が不要
であることは、そのための脱水設備などの設備、乾燥場
所などのスペース、処理土の搬出運搬などの費用等が不
要となり、近隣に対して悪臭を放たないなど、これによ
るトータルの処理コストも大きく低減されるとともに狭
い公園や河川敷などでも近隣の民家に不快感を与えるこ
とがなく、浄化作業を進行することができる。さらに、
分離水が中性であるので二次処理が不要であり、これに
要するコストも不要となる。In addition, the fact that the secondary treatment of the treated soil is unnecessary in this manner eliminates the need for equipment such as a dehydration facility, a space such as a drying place, and a cost for carrying out and transporting the treated soil. On the other hand, it does not give off a bad odor, so that the total treatment cost is greatly reduced, and the purification work can be carried out even in a small park or riverbed without causing discomfort to neighboring private houses. further,
Since the separated water is neutral, no secondary treatment is required, and the cost required for this is also unnecessary.
【0022】図2は、請求項2にかかる発明の工法の一
例を示すものである。この例では、池1の周囲の水面に
複数(7台)の循環ポンプ21、21・・・が分散して
水中に沈められて配置されている。この循環ポンプ21
を一斉に動作させて、大量の池水を各循環ポンプ21か
ら噴出させて、池1内に図中矢印方向の池水の流速0.
5〜5m/秒程度の循環水流Aを形成する。この速い循
環水流Aにより池底に沈んでいた土砂、ヘドロ等が巻き
上がり、循環水流Aに乗って移動する。FIG. 2 shows an example of the construction method of the invention according to claim 2. In this example, a plurality of (seven) circulation pumps 21, 21, ... Are dispersed and submerged on the water surface around the pond 1 and arranged. This circulation pump 21
Are operated simultaneously, and a large amount of pond water is ejected from each circulation pump 21, and the pond water flow velocity of 0.
A circulating water flow A of about 5 to 5 m / sec is formed. Due to this rapid circulating water flow A, the sediment, sludge, etc. that have sunk at the bottom of the pond roll up and move along with the circulating water flow A.
【0023】そして、この状態において、岸の近くに浮
かべた作業船22から凝集剤を循環水流Aに対して投入
する。投入された凝集剤は、循環流Aの中で池水に混合
され、拡散していく。作業船22には凝集剤投入装置2
3が設置されている。凝集剤には、先の例で使用された
ものと同じ粉末状の無機系のものが用いられる。Then, in this state, the coagulant is injected into the circulating water flow A from the work boat 22 floated near the shore. The introduced coagulant is mixed with the pond water in the circulation flow A and diffuses. The work vessel 22 has a flocculant injection device 2
3 are installed. As the aggregating agent, the same powdery inorganic material as that used in the previous example is used.
【0024】この循環水流Aに対する凝集剤の投入を、
例えば3〜5日程度連続して続けることで、池水の中で
先の例と同様な凝集反応が行われ、やがて池底には処理
された圧密性の高い、含水比の低い処理土が堆積してい
き、池水は徐々に清澄化し、浄化が行われる。The addition of the coagulant to the circulating water flow A
For example, by continuing for about 3 to 5 days continuously, the same agglutination reaction as in the previous example is performed in the pond water, and eventually the treated soil with high compaction and low water content is deposited on the bottom of the pond. The pond water is gradually clarified and purified.
【0025】この例の工法においても、先の例の工法と
同様に、凝集処理に伴う産業廃棄物が発生しないと言う
大きなメリットが得られるとともに同様の作用効果が得
られるものである。また、作業船22には凝集剤投入装
置23を設置するだけでよく、設備が簡単である利点が
ある。In the construction method of this example as well, similar to the construction method of the previous example, a great merit that no industrial waste is generated due to the coagulation treatment is obtained and the same action and effect are obtained. Further, it is sufficient to install the flocculant charging device 23 on the work boat 22, which is advantageous in that the facility is simple.
【0026】以上の説明においては、池を処理対象水域
としたが、本発明ではこれに限定されず、港湾、湖沼、
河川、池、掘割等を対象水域とすることができる。ま
た、作業船に、レジャーボートのような外観を有するも
のを用いれば、作業が人目につかず、例えば貸しボート
などが営業中でも浄化作業を実施することができる。In the above description, the pond is the treated water area, but the present invention is not limited to this.
Rivers, ponds, excavations, etc. can be targeted water areas. Further, if a work boat having an appearance like a leisure boat is used, the work is invisible, and the cleaning work can be performed even when a rental boat is in business.
【0027】[0027]
【発明の効果】以上説明したように、この発明の水底浄
化工法によれば、処理土が産業廃棄物となることがな
く、その廃棄処分の手間が不要になるという実用上極め
て有用な効果が得られる。また、処理土の二次処理が不
要であるため、そのための脱水設備などの設備、乾燥場
所などのスペース、処理土の搬出運搬などの費用等が不
要となり、近隣に対して悪臭を放たないなど、これによ
るトータルの処理コストも大きく低減されるとともに狭
い公園や河川敷などでも近隣の民家に不快感を与えるこ
とがなく、浄化作業を進行することができるなどの効果
が得られる。As described above, according to the water bottom purification method of the present invention, the treated soil does not become an industrial waste, and there is no need to dispose of it, which is extremely useful in practice. can get. In addition, since the secondary treatment of treated soil is not required, there is no need for equipment such as dehydration equipment, space for drying places, transportation costs for carrying out treated soil, etc. As a result, the total processing cost can be greatly reduced, and the purification work can be performed without causing discomfort to neighboring private houses even in a narrow park or riverbed.
【図1】本発明の第1の例を示す概略構成図である。FIG. 1 is a schematic configuration diagram showing a first example of the present invention.
【図2】本発明の第2の例の概略構成を示す平面図であ
る。FIG. 2 is a plan view showing a schematic configuration of a second example of the present invention.
1・・・池、2・・・作業船、3・・・吸引装置、4・
・・吸引ポンプ、5・・・凝集剤投入装置、6・・・撹
拌槽、8・・・吸引パイプ、11・・・排出パイプ、2
1・・・循環ポンプ、22・・・作業船、23・・・凝
集剤投入装置。1 ... Pond, 2 ... Workboat, 3 ... Suction device, 4 ...
..Suction pump, 5 ... Flocculant charging device, 6 ... Stirring tank, 8 ... Suction pipe, 11 ... Discharge pipe, 2
1 ... Circulation pump, 22 ... Work boat, 23 ... Coagulant feeding device.
Claims (2)
水を汲み上げ、これに凝集剤を添加、混合し、この泥水
をそのまま処理対象水域に戻すことを特徴とする水底浄
化工法。1. A method for purifying a bottom of a water, which is characterized in that mud at the bottom of a water is pumped up to a work boat floated in the water to be treated, a coagulant is added to and mixed with this, and the mud is returned to the water to be treated as it is.
流を形成し、この循環水流に凝集剤を添加することを特
徴とする水底浄化工法。2. A water bottom purification method characterized in that a circulating water flow circulating in the water body to be treated is formed and a coagulant is added to the circulating water flow.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2001380581A JP2003181465A (en) | 2001-12-13 | 2001-12-13 | Engineering method for decontaminating water bottom |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2001380581A JP2003181465A (en) | 2001-12-13 | 2001-12-13 | Engineering method for decontaminating water bottom |
Publications (1)
Publication Number | Publication Date |
---|---|
JP2003181465A true JP2003181465A (en) | 2003-07-02 |
Family
ID=27591569
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2001380581A Withdrawn JP2003181465A (en) | 2001-12-13 | 2001-12-13 | Engineering method for decontaminating water bottom |
Country Status (1)
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JP (1) | JP2003181465A (en) |
Cited By (7)
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WO2006082875A1 (en) * | 2005-02-04 | 2006-08-10 | Nihon University | System and method for purification of water |
KR100779423B1 (en) | 2006-08-16 | 2007-11-29 | 주식회사 선양 | Post processing ship with electrolysis device for seawater sludge and method for treating the same |
JP2011524802A (en) * | 2008-12-24 | 2011-09-08 | クリスタル・ラグーンズ・コーポレーション・エルエルシー | Efficient filtration process of water in aquarium for recreational facilities and decorative use, where filtration is performed on a small amount of water and not on the total volume of aquarium water process |
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WO2019187169A1 (en) * | 2018-03-27 | 2019-10-03 | 正佳 近藤 | Vacuum consolidation dredging method, tower air-tight loading caisson, and dedicated work ship |
CN110863475A (en) * | 2019-12-16 | 2020-03-06 | 浙江华东建设工程有限公司 | Water recycling mechanism for landscape of ecological park |
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-
2001
- 2001-12-13 JP JP2001380581A patent/JP2003181465A/en not_active Withdrawn
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2006082875A1 (en) * | 2005-02-04 | 2006-08-10 | Nihon University | System and method for purification of water |
JP4997389B2 (en) * | 2005-02-04 | 2012-08-08 | 学校法人日本大学 | Water purification system and water purification method |
KR100779423B1 (en) | 2006-08-16 | 2007-11-29 | 주식회사 선양 | Post processing ship with electrolysis device for seawater sludge and method for treating the same |
JP2011524802A (en) * | 2008-12-24 | 2011-09-08 | クリスタル・ラグーンズ・コーポレーション・エルエルシー | Efficient filtration process of water in aquarium for recreational facilities and decorative use, where filtration is performed on a small amount of water and not on the total volume of aquarium water process |
WO2019187169A1 (en) * | 2018-03-27 | 2019-10-03 | 正佳 近藤 | Vacuum consolidation dredging method, tower air-tight loading caisson, and dedicated work ship |
CN108975479A (en) * | 2018-06-25 | 2018-12-11 | 卢勇军 | A kind of Industrial Wastewater Treatment recovery system recycled based on trade effluent |
CN110863475A (en) * | 2019-12-16 | 2020-03-06 | 浙江华东建设工程有限公司 | Water recycling mechanism for landscape of ecological park |
CN110863475B (en) * | 2019-12-16 | 2020-06-02 | 浙江华东建设工程有限公司 | Water recycling mechanism for landscape of ecological park |
CN111592061A (en) * | 2020-06-03 | 2020-08-28 | 济南鸿泰华丰机械有限公司 | Ecological environment restoration method |
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