JP3273358B2 - Lake and swamp purification method and apparatus - Google Patents
Lake and swamp purification method and apparatusInfo
- Publication number
- JP3273358B2 JP3273358B2 JP22257597A JP22257597A JP3273358B2 JP 3273358 B2 JP3273358 B2 JP 3273358B2 JP 22257597 A JP22257597 A JP 22257597A JP 22257597 A JP22257597 A JP 22257597A JP 3273358 B2 JP3273358 B2 JP 3273358B2
- Authority
- JP
- Japan
- Prior art keywords
- water
- powder
- lakes
- suction pipe
- lake
- 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
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- Separation Of Suspended Particles By Flocculating Agents (AREA)
Description
【0001】[0001]
【発明の属する技術分野】この発明は、湖、沼底に沈積
している汚泥等を固液分離して、分離個体と液体とを別
々に処理し、湖、沼を浄化することを目的とした湖、沼
浄化方法及び装置に関するものである。The present invention has an object to purify lakes and marshes by separating solid and liquid sludge and the like deposited on the bottoms of lakes and marshes, treating separated solids and liquids separately. The present invention relates to a method and an apparatus for purifying a lake or swamp.
【0002】[0002]
【従来の技術】従来湖、沼の浄化については、浚渫又は
間欠空気揚水装置による浄化が知られている(特開昭3
−7440号)。2. Description of the Related Art Conventionally, as for purification of lakes and marshes, purification by dredging or intermittent air pumping apparatus is known (Japanese Unexamined Patent Publication No. Sho 3).
-7440).
【0003】[0003]
【発明により解決しようとする課題】前記従来の浚渫
は、湖、沼等の水深回復について効果があるが、浄水に
ついて十分の効果が期待できない問題点があった。The above-mentioned conventional dredging is effective in recovering the water depth of lakes and swamps, but has a problem that it cannot be expected to have a sufficient effect in purifying water.
【0004】また間欠空気揚水装置は、比較的水深の深
いダム、湖、沼等に有効であるが、水深が浅く、かつ永
年有機物、無機物が積層し、汚泥化した湖、沼の浄水は
困難になるという問題点があった。The intermittent air pumping apparatus is effective for dams, lakes, and swamps having a relatively deep water depth. However, it is difficult to purify sludge of lakes and swamps, which have a shallow depth of water and have accumulated organic and inorganic substances for many years. There was a problem of becoming.
【0005】[0005]
【課題を解決するための手段】この発明は、湖、沼に沈
積した汚泥を水と共に採取し、貝化石粉末を加えた後固
液を分離することにより、比較的浅い湖、沼において浚
渫しつつ処理することになり、前記従来の問題点を解決
したのである。SUMMARY OF THE INVENTION According to the present invention, sludge deposited on lakes and swamps is collected together with water, and after adding shell fossil powder, solid and liquid are separated, thereby dredging in relatively shallow lakes and swamps. Thus, the conventional problem is solved.
【0006】即ち方法の発明は、湖、沼底から採取する
汚泥水等に貝化石粉末を混合し、ついで浮遊固形物、沈
殿固形物及び水に固液分離し、前記浮遊固形物と、沈殿
固形物は別々に分離して夫々脱水処理すると共に、分離
水は湖、沼に放流することを特徴とした湖、沼浄化方法
である。また汚泥水等と、貝化石粉末との混合は、汚泥
水等の吸入採取時貝化石粉末を添加し、又は吸入採取し
た後に貝化石粉末を混入することを特徴としたものであ
り、汚泥水等を給送する間に、比重分離を行ない比重の
大きい大粒固形物と小粒固形物を夫々分離することを特
徴としたものである。[0006] That is, the invention of the method is to mix fossil shell powder with sludge water collected from the bottom of a lake or marsh, and then to separate solid and liquid into suspended solids, precipitated solids and water. This is a lake and swamp purification method characterized in that solids are separately separated and dewatered, and the separated water is discharged to lakes and swamps. The mixing of sludge water etc. with shell fossil powder is characterized by adding shell fossil powder at the time of inhalation sampling of sludge water or the like, or mixing shell fossil powder after inhalation sampling. And the like, while separating the large solids and the small solids, which have a large specific gravity, while feeding.
【0007】次に装置の発明は、湖、沼底からの汚泥水
等の採取手段、採取汚泥水等の移送動力手段、貝化石粉
末と汚泥水等との混合手段、混合物の固液分離手段及び
分離固形物と液体との処理手段を順次連結したことを特
徴とする湖、沼浄化装置であり、採取手段は、船体等水
上支持装置から調節自在に突出させ吸入管の基端側にポ
ンプの吸入側を連結し、前記吸入管により吸引採取した
ものである。また移送動力手段は、ポンプ使用又はジェ
ット流体使用としたものであり、貝化石粉末と汚泥水等
との混合手段は、吸入管に貝化石粉末の注入管を添設
し、又は混合槽に貝化石粉末の供給装置を設けたもので
ある。更に固液分離手段は、底板を斜設した分離槽の上
部に浮遊物掬取装置を設け、中間上部に排水管を連結
し、下部に沈殿物の排出装置を臨ませたものであり、分
離固形物の処理手段は、振動篩の下部に集水槽を設けて
水切り装置としたものである。Next, the invention of the apparatus is intended to provide means for collecting sludge water and the like from a lake or a swamp bottom, means for transporting the collected sludge water or the like, means for mixing shell fossil powder with sludge water, and means for solid-liquid separation of a mixture. And a purification device for a lake or swamp, wherein treatment means for separating solids and liquid are sequentially connected, and the sampling means is adjusted to protrude from a water support device such as a hull and a pump is provided at a base end side of a suction pipe. Are connected to each other, and are suctioned and collected by the suction pipe. The transfer power means uses a pump or a jet fluid, and the mixing means of the shell fossil powder and the sludge water is provided by adding an injection pipe of the shell fossil powder to the suction pipe, or a shell for the mixing tank. A fossil powder supply device is provided. Further, the solid-liquid separation means is provided with a suspended matter scooping device at the upper part of the separation tank having the bottom plate obliquely connected, a drainage pipe connected to the middle upper part, and a sediment discharge device facing the lower part. The means for treating solids is a drainage device provided with a water collecting tank below the vibrating sieve.
【0008】[0008]
【発明の実施の形態】この発明は、湖、沼から採取した
汚泥水等に貝化石粉末を加えた後、固液分離して夫々処
理し、分離浄水を湖、沼に戻すことの繰り返えしによっ
て、浚渫と浄水とを同時平行して行う方法である。DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention is a repetition of adding shell fossil powder to sludge water collected from lakes and swamps, separating them into solids and liquids, treating them separately, and returning the separated purified water to lakes and swamps. In this method, dredging and water purification are performed simultaneously in parallel.
【0009】また前記方法を実施する為に、汚泥水等の
採取手段、貝化石粉末との混合手段、固液分離手段及び
分離固形物の処理手段と分離液の処理手段を連結した
湖、沼浄化装置である。In order to carry out the above-mentioned method, a means for collecting sludge water or the like, a means for mixing with fossil shell powder, a means for separating solid and liquid, a means for treating separated solid matter and a means for treating separated liquid are connected to lakes and swamps. It is a purification device.
【0010】前記装置は、移動可能としてあり、湖、沼
等の岸から一定距離(例えば1km)程度中心部に向け
て処理し、湖、沼等の中央部に残った未処理部は船上処
理を行うなど、湖、沼の立地条件に応じ効率のよい手段
を選定して実施することができる。The above-mentioned apparatus is movable and processes a certain distance (for example, 1 km) from the shore of a lake, a swamp, etc. toward the center, and the unprocessed portion remaining in the center of the lake, a swamp, etc., is processed on board. For example, efficient means can be selected and implemented according to the location conditions of lakes and swamps.
【0011】[0011]
【実施例1】この発明の実施例を図1について説明す
る。Embodiment 1 An embodiment of the present invention will be described with reference to FIG.
【0012】湖、沼から沈殿している汚泥等を水と共に
採取し(水分70〜80%)、これに貝化石粉末0.1
〜0.5%(重量)を加えて均一に混合した後移送し、
又は汚泥水等を移送中に貝化石粉末を混合し、或いは汚
泥水等を混合槽に入れて貝化石粉末を混合する。Sludge and the like precipitated from lakes and swamps are collected together with water (water content: 70-80%), and the fossil shell powder 0.1
~ 0.5% (by weight), add uniform mixing and transfer
Alternatively, the shell fossil powder is mixed while the sludge water or the like is being transferred, or the shell fossil powder is mixed by putting the sludge water or the like into a mixing tank.
【0013】前記のようにした貝化石粉末を均一に混合
した後、沈殿槽に移送する。前記汚泥水等は、貝化石粉
末により凝集、吸着、酸化などの作用を受けて、比重の
軽い有機物(例えばアオコ、その他の藻類)は浮遊し、
比重の重い有機物、無機物は沈殿する。そこで分離水
(浄水)は湖、沼に放流し、沈殿物は取り出して脱水処
理した後、集積する。この沈殿物には貝化石粉末が比較
的多く含まれているので、酸素の供給、PHの調整その
他好気性菌の繁殖を助長する(空気にも接触しているの
で酸素は十分供給される)。前記有機物は、好気性菌に
よって急速に分解され、無機物(砂など)がより多くな
って急速に乾燥できる。特に有機物が多い場合には、発
酵熱も乾燥を助長する。このように処理した土は、土質
改良土又は埋立土として使用できる。After the shell fossil powder as described above is uniformly mixed, it is transferred to a sedimentation tank. The sludge water and the like are subjected to actions such as aggregation, adsorption, and oxidation by the shell fossil powder, and organic substances having a low specific gravity (e.g., blue-green algae, other algae) float,
Organic substances and inorganic substances having a high specific gravity precipitate. The separated water (purified water) is discharged to lakes and swamps, and the sediment is taken out, dehydrated, and then accumulated. The sediment contains a relatively large amount of shell fossil powder, which contributes to the supply of oxygen, adjustment of pH, and the propagation of aerobic bacteria. (Since it is in contact with air, oxygen is sufficiently supplied.) . The organic matter is rapidly decomposed by aerobic bacteria, and can be rapidly dried due to an increase in inorganic matter (such as sand). Especially when there are many organic substances, the heat of fermentation also promotes drying. The soil thus treated can be used as soil improvement soil or landfill soil.
【0014】前記浮遊物には、藻類などの有機物が多い
ので、掬い出して集積すれば、脱水と発酵が進行し(貝
化石粉末の効用による)、必要に応じ他の材料(例えば
カルシウムなど)を添加して家畜の飼料とし、又は鶏糞
などを混入して肥料とすることができる。Since the suspended matter contains many organic substances such as algae, if it is scooped out and accumulated, dehydration and fermentation proceed (depending on the effect of shell fossil powder), and if necessary, other materials (eg, calcium, etc.) Can be used as feed for livestock, or can be mixed with chicken manure to produce fertilizer.
【0015】前記のように、水中の有機物、水底の沈殿
物を同時平行して処理できると共に浄水は湖、沼に放流
するので、湖、沼の未処理水に対しては浄水の加入によ
る希釈作用が期待できると共に、浄水に混入している貝
化石粉末の作用により、未処理水に影響を与え、浄化処
理の促進を図ることができる。As described above, the organic matter in the water and the sediment at the bottom of the water can be treated simultaneously and in parallel, and the purified water is discharged to the lake and the swamp. Therefore, the untreated water in the lake and the swamp is diluted by adding the purified water. The action can be expected, and the action of the shell fossil powder mixed into the purified water affects the untreated water, thereby promoting the purification treatment.
【0016】[0016]
【実施例2】この発明の装置の実施例を図2、3、4に
基づいて説明する。Embodiment 2 An embodiment of the apparatus according to the present invention will be described with reference to FIGS.
【0017】浚渫船1の一側に吸入管2を斜設し、吸入
管2はクレーン3で吊下すると共に、ホース4を介して
ポンプ5の吸入側へ連結する。そこでクレーン3によ
り、吸入管2の吸入端を前後左右に移動する場合にもホ
ース4が屈曲、伸縮して自由に操作することができる。
ポンプ5の吐出側は移送管6に連結し、移送管6は、機
械室7などの上部を通過し、浮体8、8に支承されて、
湖岸9に達する。湖岸9には、混合槽10が架構11上
に設置してあり、前記混合槽10の一側へ前記移送管6
端を噴射室12に開口させると共に、貝化石粉末(例え
ば100〜200メッシュ)を噴射させる。混合槽10
内には、流下案内板13、14が斜設され、各流下案内
板13、14及び底板15上には突片16、16が夫々
設けてある。そこで前記噴射室10で貝化石粉末と混合
した汚泥水等は、流下案内板13、14と底板15上を
流下する間に撹拌作用を受けて均一に混合し、排出口1
7から沈殿槽18内へ排出される。A suction pipe 2 is obliquely provided on one side of the dredger 1, and the suction pipe 2 is suspended by a crane 3 and connected to a suction side of a pump 5 via a hose 4. Therefore, even when the suction end of the suction pipe 2 is moved back and forth and right and left by the crane 3, the hose 4 can be freely operated by bending and expanding and contracting.
The discharge side of the pump 5 is connected to the transfer pipe 6, which passes through the upper part of the machine room 7 and the like, is supported by the floating bodies 8, 8,
Reach Lakeshore 9. On the lake shore 9, a mixing tank 10 is installed on a frame 11, and the transfer pipe 6 is connected to one side of the mixing tank 10.
The end is opened to the injection chamber 12, and shell fossil powder (for example, 100 to 200 mesh) is injected. Mixing tank 10
Downflow guide plates 13 and 14 are obliquely provided therein, and projecting pieces 16 and 16 are provided on each of the downflow guide plates 13 and 14 and the bottom plate 15, respectively. Then, the sludge water mixed with the shell fossil powder in the spray chamber 10 is uniformly mixed by the stirring action while flowing down the flow guide plates 13 and 14 and the bottom plate 15.
7 and discharged into the sedimentation tank 18.
【0018】前記沈殿槽18は、底板18aが進行方向
へ低く斜設されている。前記沈殿槽18の一側上に前記
排出口17が臨ませてあり、他側に浄水の排出口19
と、沈殿物20の吸入管21の先端とが設置してある。
また沈殿槽18の上部には、浮遊物22を掬上げる為の
ネットコンベア23の下部が斜に突入設置され、ネット
コンベア23の上部は、搬出コンベア24上へ臨ませて
ある(図7)。図中50はホッパー、51はネットコン
ベアの動力、52は水受けである。The sedimentation tank 18 has a bottom plate 18a which is inclined downward in the traveling direction. The discharge port 17 faces one side of the sedimentation tank 18 and the purified water discharge port 19
And the tip of the suction pipe 21 for the sediment 20 are provided.
In addition, a lower part of a net conveyor 23 for scooping up the suspended matter 22 is installed obliquely in the upper part of the sedimentation tank 18, and an upper part of the net conveyor 23 faces the unloading conveyor 24 (FIG. 7). In the figure, 50 is a hopper, 51 is a power of a net conveyor, and 52 is a water receiver.
【0019】前記吸入管21には吸引ポンプ25の吸入
端が連結され、吸引ポンプ25の吐出側には、移送管2
6の一端が連結され、移送管26の中間部には分離匣2
7、28が直列に連結される。前記分離匣27、28
は、ホッパー29、30と連結され、ホッパー29、3
0と連結され、ホッパー29、30の出口には、自動又
は手動の開閉蓋31、32が設置される。図8は自動の
開閉蓋31、32であって、集積した砂利などの重量が
スプリング33、34の弾力より大きくなると、軸3
5、36を中心にして矢示37、38の方向へ回転し、
矢示39、40のように砂利又は砂をコンベア41、4
2上へ排出する。前記放出により砂利などの重量が小さ
くなると、前記開閉蓋31、32は、スプリング33、
34の弾力により前記と逆に回転し、ホッパーの出口を
閉鎖する。A suction end of a suction pump 25 is connected to the suction pipe 21, and a transfer pipe 2 is connected to a discharge side of the suction pump 25.
6 are connected to each other.
7, 28 are connected in series. Separation boxes 27, 28
Are connected to the hoppers 29 and 30,
Automatic or manual opening / closing lids 31 and 32 are installed at the outlets of the hoppers 29 and 30, respectively. FIG. 8 shows automatic opening / closing lids 31 and 32. When the weight of the accumulated gravel becomes larger than the elasticity of the springs 33 and 34, the shaft 3
Rotate in the directions of arrows 37 and 38 around 5, 36,
Gravel or sand as shown by arrows 39 and 40 on conveyors 41 and 4
2 Discharge up. When the weight of the gravel or the like is reduced by the release, the opening / closing lids 31 and 32 are
With the resiliency of 34, it rotates in the opposite direction, closing the outlet of the hopper.
【0020】前記分離匣27、28内は、移送管26の
断面積よりも広い断面積となり、流速が低下するので、
比較的大きい砂利、砂などは順次沈下してホッパー2
9、30内に堆積し、小さい土粒等は矢示43のように
送られて、振動篩44内へ放出される。振動篩44によ
って固液が分離され、水は排水管45を矢示49のよう
に経て湖、沼に放流され、土等はコンベア46により矢
示47のように運ばれ、集積地に堆積土48となる。前
記土等に有機物が混入している場合には、堆積中に微生
物により発酵分解し、土等の乾燥を助長する。この乾燥
した土等は水分30%以下であって、埋立地の土又は土
質改良土などに有用な土質であり、臭気がないことは勿
論、取扱いも容易であって、掘削土等と同様に使用する
ことができる。Since the inside of the separation boxes 27 and 28 has a larger cross-sectional area than the cross-sectional area of the transfer pipe 26 and the flow velocity decreases,
Relatively large gravel, sand, etc. settle down one after another and hopper 2
The small soil particles and the like that are deposited in the sifters 9 and 30 are sent as indicated by arrows 43 and discharged into the vibrating sieve 44. The solid and liquid are separated by the vibrating sieve 44, the water is discharged to the lake or swamp through the drain pipe 45 as shown by arrow 49, and the soil and the like are carried by the conveyor 46 as shown by arrow 47, and the soil is deposited on the accumulation area. 48. When organic matter is mixed in the soil or the like, it is fermented and decomposed by microorganisms during deposition to promote drying of the soil or the like. This dried soil has a water content of 30% or less and is useful soil for landfill or soil improvement soil. It has no odor and is easy to handle. Can be used.
【0021】前記実施装置は、汚泥水等の処理の一例を
示すものであって、固液分離後の水、浮遊有機物、その
他の固形物等の処理は従来公知の技術を採用することが
できる。要は汚泥水等に貝化石粉末を添加混合し、貝化
石粉末の優れた特性によって、汚泥水等を効率よく処理
し、浄水、有用有機物(飼料、肥料)及び有用土に変化
させることであり、湖、沼の浄化と、汚泥水等の有用化
が最大の目的となるものである。The above-mentioned embodiment shows an example of the treatment of sludge water and the like, and the treatment of water, suspended organic matter, other solid matter and the like after solid-liquid separation can employ a conventionally known technique. . The point is to add and mix shell fossil powder to sludge water, etc., and to efficiently treat sludge water, etc. by the excellent properties of shell fossil powder, and to convert it into purified water, useful organic matter (feed, fertilizer) and useful soil. Purification of lakes and marshes and utilization of sludge water are the most important objectives.
【0022】前記沈殿物移送中に分離した砂利又は砂
は、土木、建築に用いるコンクリートの優れた粗骨材、
細骨材として使用することができる。The gravel or sand separated during the transfer of the sediment is an excellent coarse aggregate of concrete used for civil engineering and construction,
It can be used as fine aggregate.
【0023】[0023]
【実施例3】この発明の他の実施例を図9に基づいて説
明する。実施例2は、吸入した泥・土・水の混合物と貝
化石粉末とを混合槽で混合したが、この実施例は移送中
に混合しようとしたものである。Embodiment 3 Another embodiment of the present invention will be described with reference to FIG. In Example 2, the inhaled mixture of mud, soil, and water was mixed with shell fossil powder in a mixing tank. In this example, mixing was attempted during transfer.
【0024】即ち浚渫船1の一側に吸入管2を斜設し、
吸入管2はクレーン3で吊下すると共に、ホース4を介
してポンプ5の吸入側へ連結する。前記吸入管2の適所
に、貝化石粉末の吹込み匣50が設けられ、エアにより
貝化石粉末を吹き込むべく、ノズル(図示していない)
が吸入管2内へ突入されている。前記ポンプ5の吐出側
は、移送管6に連結し、移送管6は、機械室7などの上
部を通過し、浮体8、8に支承されて、湖岸9に達す
る。前記移送管6が機械室7の上部を通り、下降するこ
とにより、一定の水圧が掛り爾後の移送管内を混合物が
円滑かつ容易に移動する。図中60は混合物を加速する
為に加圧エアを吹込むジェット匣である。That is, the suction pipe 2 is obliquely provided on one side of the dredger 1,
The suction pipe 2 is suspended by a crane 3 and connected to a suction side of a pump 5 via a hose 4. An injection box 50 for shell fossil powder is provided at an appropriate position of the suction pipe 2, and a nozzle (not shown) for blowing shell fossil powder with air.
Project into the suction pipe 2. The discharge side of the pump 5 is connected to a transfer pipe 6. The transfer pipe 6 passes through an upper portion such as a machine room 7, is supported by floating bodies 8, 8 and reaches a lake shore 9. When the transfer pipe 6 passes through the upper part of the machine room 7 and descends, a certain water pressure is applied, and the mixture moves smoothly and easily in the transfer pipe after that. In the figure, reference numeral 60 denotes a jet box for blowing pressurized air to accelerate the mixture.
【0025】前記湖岸9に達した移送管6は支脚51に
高く支持されており、ついで分離匣52、53、54を
所定間隔で直列に連結してある。従って泥・土・水の混
合物は、分離匣52で大粒砂を分離し、ついで分離匣5
3で中粒砂を分離し、更に分離匣54で小粒砂を分離
し、沈殿槽55に入り、微粒土等58が沈殿する。そこ
で微粒土は排土管56から外界へ取出し、乾燥して肥料
(青子その他の有機物と、貝化石粉末との混合物なので
肥料効果がある。)などにしたり、土質改良土に使用す
る。前記上澄液59は排水管57を介して湖へ戻す。The transfer pipe 6 reaching the lake shore 9 is supported at a high level by a supporting leg 51, and separation casings 52, 53 and 54 are connected in series at predetermined intervals. Therefore, the mixture of mud, soil, and water separates large sand particles in the separation box 52, and then separates the
In 3, the medium sand is separated, and the small sand is further separated in the separation box 54. Then, the fine soil is taken out from the discharge pipe 56 to the outside world, and dried to be used as fertilizer (a fertilizer effect because it is a mixture of aoko and other organic matter and shell fossil powder) and used as soil improvement soil. The supernatant 59 is returned to the lake via the drain pipe 57.
【0026】前記実施例によれば、泥・土・水の混合物
の移送中に、貝化石粉末を供給するので、移送中に均一
に混合することができる。従って混合槽が不必要にな
り、装置の簡易化ができる。また分離匣52、53、5
4を直列設置したので、砂利等を粒度別に分別すること
ができる。従って砂、砂利等の分別物を、夫々別々に集
積し、コンクリートなどの骨材として販売することがで
きる。According to the above embodiment, the shell fossil powder is supplied during the transfer of the mixture of mud, soil and water, so that the mixture can be uniformly mixed during the transfer. Therefore, a mixing tank is not required, and the apparatus can be simplified. Separate boxes 52, 53, 5
Since 4 were installed in series, gravel and the like can be separated according to particle size. Therefore, separated materials such as sand and gravel can be separately collected and sold as aggregates such as concrete.
【0027】[0027]
【実験例】湖、沼の水に貝化石粉末を混入し、水質浄化
の試験をした所、表1の結果を得た。[Experimental example] A fossil shell powder was mixed into the water of a lake or a swamp, and a water purification test was carried out. The results shown in Table 1 were obtained.
【0028】[0028]
【表1】 [Table 1]
【0029】※なしは管理基準値をまだ調べていない。* For none, the management reference value has not been examined yet.
【0030】※1リットル当り粉末凝 剤1g、3g、
5g、水1リットルに対し砂100g添加剤3gを実験
してみた。* 1 g of powder coagulant per liter, 3 g,
5 g, 1 liter of water, 100 g of sand and 3 g of additive were tested.
【0031】 実験の結果 1 透視度 5cmだったものが30cmとなり、約6倍の効果が認められ た。 2 色 度 165だったものが10となり、約91.3%減少した。 3 濁度 93だったものが4となり、約96%の減少となった。 4 大腸菌群 17000が230となり、約98.6%減少した。 5 浮遊物 110だったものが3となり、約97%除去できた。 6 COD 40だったものが6.5となり、約84%減少した。 7 DO 基準値以内 8 PH 9.0だったものが7.7となり、常に中性である。As a result of the experiment, 1 the visibility was changed from 5 cm to 30 cm, and the effect of about 6 times was recognized. Chromaticity was 165, which was 165, a decrease of about 91.3%. 3 The turbidity was 93, which was 93, a decrease of about 96%. 4 The number of E. coli 17000 was 230, a decrease of about 98.6%. 5 Floating matter was changed from 110 to 3, and approximately 97% was removed. What was 6 COD 40 was 6.5, a decrease of about 84%. 7 DO Within the standard value 8 PH 9.0 was changed from 9.0 to 7.7, which is always neutral.
【0032】前記のように、貝化石粉の添加により、水
の浄化について大腸菌及びCODの減少、浮遊物の除去
など著しい効果が認められた。As mentioned above, the addition of fossil shell powder reduces water purification , reduces E. coli and COD, and removes suspended matter.
And other remarkable effects.
【0033】[0033]
【発明の効果】この発明は、湖、沼から採取した汚泥水
等に貝化石粉末を混入するので、汚泥処理と水質改善を
同時並行的に行い、有機物を好気性菌で分解処理した浄
水は湖、沼に放流し、汚泥等は有用な砂利、砂、土にし
て諸目的に使用し、浮遊有機物は処理して飼料、肥料、
その他(例えば土質改良材)に使用し得るなどの諸効果
がある。According to the present invention, since shell fossil powder is mixed into sludge water or the like collected from lakes and swamps, sludge treatment and water quality improvement are performed simultaneously in parallel , and organic substances are decomposed by aerobic bacteria. Water is discharged into lakes and swamps, sludge is used as useful gravel, sand, and soil for various purposes, and suspended organic matter is processed for feed, fertilizer,
There are various effects such as may be used for other (e.g., soil break Ryozai).
【0034】また使用物が貝化石粉末であるから、浄
水、土などに残しても公害を発生するおそれなく、却っ
て浄水又は土質改善に継続的に効力を発揮する効果があ
る。Further, since the used substance is shell fossil powder, there is no danger of causing pollution even if it is left in purified water or soil, and it has an effect of continuously exerting an effect on water purification or soil quality improvement.
【図1】この発明の方法の実施例のブロック図。FIG. 1 is a block diagram of an embodiment of the method of the present invention.
【図2】同じく装置の実施例の概念図。FIG. 2 is a conceptual diagram of an embodiment of the apparatus.
【図3】同じく採取と移送装置を示す拡大正面図。FIG. 3 is an enlarged front view showing the collection and transfer device.
【図4】同じく平面図。FIG. 4 is a plan view of the same.
【図5】同じく混合槽の拡大正面図。FIG. 5 is an enlarged front view of the mixing tank.
【図6】同じく一部拡大平面図。FIG. 6 is a partially enlarged plan view.
【図7】同じく沈殿槽の拡大正面図。FIG. 7 is an enlarged front view of the sedimentation tank.
【図8】同じく砂利分離装置の一部を破切した拡大図。FIG. 8 is an enlarged view of a part of the gravel separation device.
【図9】同じく他の実施例の概念図。FIG. 9 is a conceptual diagram of another embodiment.
1 浚渫船 2 吸入管 3 クレーン 4 ホース 5 ポンプ 6 移送管 7 機械室 8 浮体 9 湖岸 10 混合槽 11 架構 12 噴射室 13、14 流下案内板 15 底板 16 突片 17 排出口 18 沈殿槽 18a 底板 19 排出口 20 沈殿物 21 吸入管 22 浮遊物 23 ネットコンベア 24 搬出コンベア 25 吸引ポンプ 26 移送管 27、28 分離匣 29、30 ホッパー 31、32 開閉蓋 33、34 スプリング 35、36 軸 41、42 コンベア 44 振動篩 45 排水管 46 コンベア 48 堆積土 50 吹込み匣 51 支脚 52、53、54 分離匣 55 沈殿槽 56 排土管 57 排水管 58 微粒土等 59 上澄液 60 ジェット匣 DESCRIPTION OF SYMBOLS 1 Dredge ship 2 Suction pipe 3 Crane 4 Hose 5 Pump 6 Transfer pipe 7 Machine room 8 Floating body 9 Lake shore 10 Mixing tank 11 Frame 12 Injection chamber 13, 14 Downflow guide plate 15 Bottom plate 16 Projection 17 Drain 18 Sedimentation tank 18a Bottom plate 19 Discharge Outlet 20 Precipitate 21 Suction pipe 22 Suspended material 23 Net conveyor 24 Unloading conveyor 25 Suction pump 26 Transfer pipe 27, 28 Separation box 29, 30 Hopper 31, 32 Opening lid 33, 34 Spring 35, 36 Shaft 41, 42 Conveyor 44 Vibration Sieve 45 drain pipe 46 conveyor 48 sedimentary soil 50 blowing box 51 supporting legs 52, 53, 54 separation box 55 sedimentation tank 56 drain pipe 57 drain pipe 58 fine soil etc. 59 supernatant liquid 60 jet box
フロントページの続き (56)参考文献 特開 平9−187776(JP,A) 特開 平2−268884(JP,A) 特開 昭57−91786(JP,A) 特開 昭51−141457(JP,A) 特開 平7−327544(JP,A) 特開 平7−100460(JP,A) 特開 昭47−20945(JP,A) 特開 平6−178983(JP,A) 特開 平5−111697(JP,A) 特開 平6−134499(JP,A) (58)調査した分野(Int.Cl.7,DB名) C02F 1/52 - 1/56 C02F 11/00 - 11/20 Continuation of the front page (56) References JP-A-9-187776 (JP, A) JP-A-2-268888 (JP, A) JP-A-57-91786 (JP, A) JP-A-51-141457 (JP, A) JP-A-7-327544 (JP, A) JP-A-7-100460 (JP, A) JP-A-47-20945 (JP, A) JP-A-6-178983 (JP, A) 5-111697 (JP, A) JP-A-6-134499 (JP, A) (58) Fields investigated (Int. Cl. 7 , DB name) C02F 1/52-1/56 C02F 11/00-11 / 20
Claims (2)
取時又は吸入採取後に、前記汚泥水等の0.1〜0.5
%(重量)の貝化石粉末を混合し、ついで前記汚泥水等
の移送中に比重分離を行って浮遊固形物、沈殿固形物及
び水に固液分離し、前記分離した浮遊固形物と、沈殿固
形物は別々に取出し、有機物は好気性菌により分解さ
れ、夫々脱水処理すると共に、分離水は好気性菌が含ま
れたまま湖、沼に放流されることを特徴とした湖、沼浄
化方法。1. Inhalation sampling of sludge water collected from lakes and swamp bottoms
At the time of collection or after inhalation sampling, 0.1 to 0.5 of the sludge water etc.
% (Weight) of shell fossil powder and then the sludge water etc.
During the transfer , solid-liquid separation is performed into suspended solids, precipitated solids and water, and the separated suspended solids and precipitated solids are separately taken out, and organic substances are decomposed by aerobic bacteria.
Are, together with the respective dehydrating, separation water contains aerobic bacteria
A method for purifying lakes and swamps, characterized by being discharged into lakes and swamps as they are.
装置から、吸入管を調節自在に突出させ、該吸入管の吐
出側に、ポンプ又はジェット液体による移送動力手段を
連結し、前記吸入管に貝化石粉末の注入管を添設し、又
は前記吸入管の吐出側に設置した混合槽に貝化石粉末の
供給装置を設けて、貝化石粉末と汚泥水等の混合手段と
し、前記混合槽の排出側に分離槽の一側を連結し、前記
分離槽に、浮遊物採取装置と、沈殿物の排出装置を設置
すると共に、前記浮遊物採取装置及び沈殿物の排出装置
に夫々脱水処理手段を順次連結したことを特徴とする
湖、沼浄化装置。 2. A water support such as a hull provided on the water of a lake or swamp.
The suction pipe is adjustably protruded from the device, and the discharge of the suction pipe is performed.
On the outlet side, transfer power means by pump or jet liquid
Connected, an inlet pipe for shell fossil powder is attached to the suction pipe,
Is a mixture of fossil shell powder in a mixing tank installed on the discharge side of the suction pipe.
Provide a supply device, and mixing means of fossil shell powder and sludge water
Then, one side of the separation tank is connected to the discharge side of the mixing tank,
Separation tank is equipped with a suspended solids collection device and a sediment discharge device
And the apparatus for collecting the suspended matter and the apparatus for discharging the sediment
Characterized in that dewatering treatment means are sequentially connected to each other
Lake and swamp purification equipment.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP22257597A JP3273358B2 (en) | 1997-08-19 | 1997-08-19 | Lake and swamp purification method and apparatus |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP22257597A JP3273358B2 (en) | 1997-08-19 | 1997-08-19 | Lake and swamp purification method and apparatus |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH1157738A JPH1157738A (en) | 1999-03-02 |
JP3273358B2 true JP3273358B2 (en) | 2002-04-08 |
Family
ID=16784624
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP22257597A Expired - Lifetime JP3273358B2 (en) | 1997-08-19 | 1997-08-19 | Lake and swamp purification method and apparatus |
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Country | Link |
---|---|
JP (1) | JP3273358B2 (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR20040066210A (en) * | 2003-01-17 | 2004-07-27 | 장성완 | A Hydrophobic solidification isolated solution for wastewater treating |
-
1997
- 1997-08-19 JP JP22257597A patent/JP3273358B2/en not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
JPH1157738A (en) | 1999-03-02 |
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