JPH10118629A - Apparatus and method for cleaning water - Google Patents

Apparatus and method for cleaning water

Info

Publication number
JPH10118629A
JPH10118629A JP8297340A JP29734096A JPH10118629A JP H10118629 A JPH10118629 A JP H10118629A JP 8297340 A JP8297340 A JP 8297340A JP 29734096 A JP29734096 A JP 29734096A JP H10118629 A JPH10118629 A JP H10118629A
Authority
JP
Japan
Prior art keywords
water
water purification
purification
raw
activated carbon
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP8297340A
Other languages
Japanese (ja)
Inventor
Kunio Mizuno
邦雄 水野
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.)
DIA GOMME KK
Dia Rubber Co Ltd
Original Assignee
DIA GOMME KK
Dia Rubber 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 DIA GOMME KK, Dia Rubber Co Ltd filed Critical DIA GOMME KK
Priority to JP8297340A priority Critical patent/JPH10118629A/en
Publication of JPH10118629A publication Critical patent/JPH10118629A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage

Landscapes

  • Water Treatment By Sorption (AREA)
  • Biological Treatment Of Waste Water (AREA)
  • Physical Water Treatments (AREA)
  • Removal Of Specific Substances (AREA)

Abstract

PROBLEM TO BE SOLVED: To purify water of a basin, a lake or rivers a basin, a lake or rivers of which a problem of water pollution is raised. SOLUTION: Raw water is supplied to a purifying tank and fine bubbles are raised toward the surface of raw water from the bottom part of this purifying tank and waste refuse, org. matter or bacteria in raw water are stuck to these air bubbles to be accompanied by air bubbles and a part of raw water to which waste refuse is stuck to be allowed to overflow from the upper end surface of the purifying tank or filtered by a filter agent such as zeolite to be primarily filtered. This primarily filtered treated water is supplied to a water purifying tank filled with a solid oxygen generator such as calcium peroxide and passed through a purifying tank to be purified. This treated water is supplied to a water purifying tank packed with activated carbon to be further purified. By this constitution, treated water free from waste refuse, having oxygen sufficiently dissolved therein and decolored and deodorized is obtaned.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、池、湖及び河川等
の水質を浄化するための水質浄化装置及び水質浄化方法
に関する。本発明の水質浄化装置は、固形酸素発生剤を
含有する水質浄化剤により構成される水質浄化層を備え
ている。そのため、酸素が十分に溶存した処理水が得ら
れ、オルトリン酸イオン濃度の低下等、特定の水質浄化
の効果が奏される。また、活性炭を含有する水質浄化剤
により構成される水質浄化層をも備え、有機物等が除去
されるとともに脱色、脱臭等もなされる。
The present invention relates to a water purification apparatus and a water purification method for purifying water quality of ponds, lakes, rivers, and the like. The water purification device of the present invention includes a water purification layer composed of a water purification agent containing a solid oxygen generating agent. Therefore, treated water in which oxygen is sufficiently dissolved can be obtained, and specific water purification effects such as a decrease in orthophosphate ion concentration can be obtained. In addition, a water purification layer composed of a water purification agent containing activated carbon is also provided, so that organic substances and the like are removed, and decolorization and deodorization are performed.

【0002】[0002]

【従来の技術】現在、多くの公園、ゴルフ場等におい
て、池、湖などの水質汚濁が深刻となっている。また、
河川などでも中下流域では大量の工業排水、生活排水に
よって水質の悪化が問題になっている。これらは美観を
損ねるばかりでなく、悪臭の発生、鯉の死亡等大きな問
題になっている。その対策として各種の浄化設備、資材
等が実用に供されている。しかし、これら従来の設備、
資材などでは、塵埃等の除去はなされるものの、十分な
酸素を溶存させた処理水を得ることについてはまったく
配慮されていない。
2. Description of the Related Art At present, in many parks, golf courses, and the like, water pollution of ponds, lakes, and the like has become serious. Also,
Even in rivers and the like, the deterioration of water quality has become a problem in the middle and lower basins due to large amounts of industrial and domestic wastewater. These not only spoil the aesthetics but also cause serious problems such as generation of foul odors and death of carp. As a countermeasure, various purification equipment, materials, and the like have been put to practical use. However, these conventional equipment,
For materials and the like, dust and the like are removed, but no consideration is given to obtaining treated water in which sufficient oxygen is dissolved.

【0003】[0003]

【発明が解決しようとする課題】本発明の水質浄化装置
は、上記従来の水質浄化設備、資材等の問題点を解決す
るものであり、特に微細な塵埃、有機物、微生物等の除
去に加え、十分な酸素が溶存し、且つ脱色、脱臭された
処理水を得るための水質浄化装置を提供する。また、本
発明は、原水を濾過して水質を浄化した後、或いは原水
中を上昇する微細な気泡に塵埃等を付着、同伴させて水
質を浄化した後、この処理水を、固形酸素発生剤により
構成される水質浄化層に導入し、透過させて、十分な酸
素を溶存させる水質浄化方法を提供する。更に、これら
の水質浄化に加え、活性炭により構成される水質浄化層
に処理水を導入し、透過させて、有機物を除去し、且つ
脱色、脱臭等をする水質浄化方法を提供する。
The water purifying apparatus of the present invention solves the problems of the above-mentioned conventional water purifying equipment, materials and the like. In particular, in addition to the removal of fine dust, organic substances, microorganisms, etc. Provided is a water purification device for obtaining treated water in which sufficient oxygen has been dissolved and decolorized and deodorized. In addition, the present invention provides a method for purifying water quality by filtering raw water to purify water quality, or purifying water quality by adhering and accompanying dust and the like to fine bubbles rising in raw water, and then treating the treated water with a solid oxygen generating agent. The present invention provides a water purification method for introducing and permeating into a water purification layer constituted by the above and dissolving sufficient oxygen. Furthermore, in addition to these water purifications, a water purification method is provided in which treated water is introduced into a water purification layer made of activated carbon, is allowed to permeate to remove organic substances, and is decolorized and deodorized.

【0004】[0004]

【課題を解決するための手段】第1発明の水質浄化装置
は、固形酸素発生剤を含有する第1の水質浄化剤により
構成される第1の水質浄化層を備えることを特徴とす
る。また、第2発明の水質浄化装置は、固形酸素発生剤
を含有する第1の水質浄化剤により構成される第1の水
質浄化層と、活性炭を含有する第2の水質浄化剤により
構成される第2の水質浄化層とを備えることを特徴とす
る。
According to a first aspect of the present invention, there is provided a water purification apparatus including a first water purification layer comprising a first water purification agent containing a solid oxygen generating agent. Further, the water purification device of the second invention is constituted by a first water purification layer composed of a first water purification agent containing a solid oxygen generating agent, and a second water purification agent containing activated carbon. And a second water purification layer.

【0005】上記「固形酸素発生剤」の主原料は、本発
明の目的を達成することができる範囲で種々選択するこ
とができ、例えば過酸化カルシウム等を例示することが
できる。また、この固形酸素発生剤は粉末状、粒状、ペ
レット状いずれの形状、大きさでもよく、より粒径の大
きい塊状物であってもよい。また、上記「活性炭」とし
ては、通常、水質浄化に使用されるものを特に制限され
ることなく用いることができる。この活性炭は、銀、
銅、亜鉛、錫等が担持され、抗菌性が付与されたもので
あってもよい。
[0005] The main raw material of the "solid oxygen generator" can be variously selected within a range in which the object of the present invention can be achieved, and examples thereof include calcium peroxide. The solid oxygen generating agent may be in the form and size of powder, granule or pellet, or may be a lump having a larger particle size. Moreover, as the above-mentioned "activated carbon", those usually used for water purification can be used without particular limitation. This activated carbon is silver,
Copper, zinc, tin or the like may be supported and may have antibacterial properties.

【0006】上記「第1の水質浄化剤」及び上記「第2
の水質浄化剤」は、それぞれ固形酸素発生剤或いは活性
炭のみからなるものとすることが好ましい。それによっ
て固形酸素発生剤及び活性炭それぞれ特有の浄水効果が
十分に且つ効率よく奏される。しかし、第1の水質浄化
剤及び第2の水質浄化剤の所要の浄水効果が損なわれな
い範囲内で、ゼオライト、パーライト等の水質浄化作用
のある他の多孔質体を混合して用いてもよい。また、こ
れらの多孔質体は2種以上を併用することもできる。
[0006] The "first water purification agent" and the "second water purification agent"
It is preferable that each of the "water purification agents" is composed of only a solid oxygen generator or activated carbon. Thereby, the water purifying effect specific to each of the solid oxygen generator and the activated carbon is sufficiently and efficiently achieved. However, as long as the required water purification effect of the first water purification agent and the second water purification agent is not impaired, other porous materials having a water purification effect such as zeolite and perlite may be mixed and used. Good. Further, two or more of these porous bodies can be used in combination.

【0007】上記の固形酸素発生剤及び活性炭は、通
常、粒体又は粉体からなり、特に活性炭は微細な粉体で
ある場合が多い。そのため、上記「第1の水質浄化層」
及び上記「第2の水質浄化層」は、通常、固形酸素発生
剤及び活性炭、場合によって併用されるゼオライト等
を、例えば金属、プラスチック、繊維強化プラスチック
等からなる容器中に充填することにより形成される。ま
た、特に活性炭などは流通する水によって容易に移送さ
れてしまうことがある。このような活性炭などの容器か
らの流出を防止するため、この容器の被処理水の流入口
と流出口には、通常、活性炭等が被処理水によって流出
してしまわないように金網、多孔質フィルム等からなる
フィルタが装着される。
[0007] The above-mentioned solid oxygen generator and activated carbon are usually composed of granules or powder, and especially activated carbon is often a fine powder. Therefore, the "first water purification layer"
And the above-mentioned "second water purification layer" is usually formed by filling a container made of, for example, metal, plastic, fiber-reinforced plastic, or the like with a solid oxygen generator and activated carbon, zeolite or the like optionally used, and the like. You. In particular, activated carbon and the like may be easily transported by flowing water. In order to prevent such activated carbon from flowing out of the container, a wire mesh and a porous material are usually provided at the inlet and outlet of the water to be treated so that the activated carbon and the like do not flow out by the water to be treated. A filter made of a film or the like is mounted.

【0008】また、第2発明における、第1の水質浄化
層と、第2の水質浄化層とは、それぞれ別個の容器に固
形酸素発生剤、活性炭等を充填し、これら容器を配管に
よって接続した構成としてもよい。更に、同一容器中に
隔壁を隔てて第1及び第2の水質浄化層を形成し、一方
の水質浄化層を透過して浄化された処理水を、配管を用
いることなく、容器の底面と隔壁の下端面との間の空間
或いは隔壁そのものに設けられた透孔等を通過させて、
他方の水質浄化層に流通させ、この浄化層を透過させて
更に浄化する構成とすることもできる。
In the second invention, the first water purification layer and the second water purification layer are each filled with a solid oxygen generating agent, activated carbon and the like in separate containers, and these containers are connected by piping. It may be configured. Further, the first and second water purification layers are formed in the same container with a partition therebetween, and the treated water that has passed through one of the water purification layers and has been purified can be separated from the bottom surface of the container and the partition without using piping. Through the space between the lower end surface of the or through holes provided in the partition itself,
A configuration may also be adopted in which the water is circulated through the other water purification layer, and the water is purified through the purification layer.

【0009】上記の隔壁は、その下端近傍のみから処理
水が流通することができる板状体とすることができる。
この場合、容器の底面と板状体の下端面との間におい
て、板状体の全幅に渡って処理水が流通し得る空間を設
けたものとしてもよい。また、板状体の下端近傍のみに
固形酸素発生剤又は活性炭の粒径に応じて、適宜大きさ
及び個数の透孔、スリット等を設けたものであってもよ
い。この隔壁は、充填された水質浄化剤の重量或いは水
流などによって容易に変形しないだけの剛性が必要であ
り、例えばステンレススチール等の金属、ポリプロピレ
ン、ABS樹脂等のプラスチック或いは繊維強化プラス
チック等からなる板状体によって構成することができ
る。また、隔壁は、上記の透孔、スリット等を板状体の
全面に均等に設けたものとすることもできる。
The partition may be a plate-like body through which the treated water can flow only from the vicinity of the lower end.
In this case, a space may be provided between the bottom surface of the container and the lower end surface of the plate-shaped body through which the treated water can flow over the entire width of the plate-shaped body. Further, the plate-shaped body may be provided with through holes, slits, etc. of an appropriate size and number only in the vicinity of the lower end of the plate according to the particle diameter of the solid oxygen generating agent or activated carbon. The partition wall must have rigidity such that it is not easily deformed by the weight of the filled water purification agent or the flow of water. For example, a plate made of metal such as stainless steel, plastic such as polypropylene, ABS resin, or fiber-reinforced plastic is used. It can be constituted by a shape. Further, the partition wall may have the above-mentioned through-holes, slits and the like provided evenly on the entire surface of the plate-like body.

【0010】また、特に活性炭等が微細である場合な
ど、この金属或いはプラスチック等からなる隔壁の下端
近傍の処理水が流通する箇所或いは隔壁の全面に透孔等
を設けた場合は、その片面又は両面の全面に、水は容易
に透過するが活性炭等は透過しない多孔質シートを配設
することが好ましい。このような多孔質シートとして
は、金網、不織布、多孔質フィルム等が挙げられる。不
織布としては、ポリエステル、ナイロン、ポリプロピレ
ン繊維等からなる厚さ0.5〜2mm、例えば1mm程
度の市販のものを特に制限されることなく使用すること
ができる。多孔質フィルムとしては、ポリエチレン、ポ
リプロピレン等からなる適宜厚さ及び孔径のものを用い
ることができる。
In addition, particularly in the case where activated carbon or the like is fine, when a through hole or the like is provided in a place where the treated water flows near the lower end of the partition wall made of metal or plastic, or in the entire surface of the partition wall, It is preferable to dispose a porous sheet that easily transmits water but does not transmit activated carbon or the like on the entire surface on both sides. Examples of such a porous sheet include a wire mesh, a nonwoven fabric, a porous film, and the like. As the nonwoven fabric, a commercially available nonwoven fabric having a thickness of 0.5 to 2 mm, for example, about 1 mm, made of polyester, nylon, polypropylene fiber or the like can be used without any particular limitation. As the porous film, a film having an appropriate thickness and pore diameter made of polyethylene, polypropylene, or the like can be used.

【0011】更に、本発明では、多孔質体に固定した好
気性微生物の浄化作用を併用することもできる。多孔質
体としては、天然のゼオライト、パーライト等の多孔質
体、各種酸化物等を焼成して得られる多孔質セラミック
スなどを使用することができる。多孔質体の孔径が大き
い方が微生物が固定され易く、適当な孔径を有し、且つ
物理的な濾過機能にも優れる木炭の使用が好ましい。こ
の好気性微生物を固定した多孔質体を配設する位置は特
に限定されない。第1の水質浄化層と第2の水質浄化層
との間に、この多孔質体からなる水質浄化層を設けるこ
ともできるし、多孔質体を、それが容易に流出しない網
状体等に収容し、この網状体を、第1及び第2の水質浄
化層の処理水の流入口近傍或いは流出口近傍に配設する
こともできる。
Further, in the present invention, the purifying action of aerobic microorganisms fixed on the porous body can be used in combination. As the porous body, a porous body such as natural zeolite and pearlite, a porous ceramic obtained by firing various oxides, and the like can be used. It is preferable to use charcoal having a large pore size of the porous body, because microorganisms are easily fixed thereto, have an appropriate pore size, and are excellent in physical filtration function. The position at which the porous body on which the aerobic microorganisms are fixed is not particularly limited. A water purification layer composed of this porous body can be provided between the first water purification layer and the second water purification layer, and the porous body is housed in a mesh or the like that does not easily flow out. Then, the net-like body may be disposed near the inlet or outlet of the treated water of the first and second water purification layers.

【0012】好気性微生物としては、属名ゲオトリッチ
ャム他の酵母、ノカルディア他の放射菌、バチルス他の
細菌及びアルペルギルス(有用糸状菌)等からなる放射
菌と特殊な細菌の共生作用を利用したもの等を使用でき
る。この微生物には、更に、特殊処理した硫酸第一鉄な
どの無機成分と、醗酵済みの動物性有機物、腐食酸など
を配合することもでき、このようにすれば生物的及び化
学的に作用し相乗効果が発揮される。
As the aerobic microorganisms, those utilizing the symbiotic effect of radioactive bacteria consisting of yeasts such as the genus Geotricham and others, radioactive bacteria such as Nocardia and others, bacteria such as Bacillus and alpergillus (useful filamentous fungi) and special bacteria. Etc. can be used. The microorganisms can also be blended with specially treated inorganic components such as ferrous sulfate, fermented animal organics, corrosive acids, etc., which can act biologically and chemically. A synergistic effect is exhibited.

【0013】第3発明の水質浄化装置は、第1発明或い
は第2発明の水質浄化装置に、塵埃等を除去するための
特定の構成の浄水装置を組み合わせたものであり、浄水
槽本体、該浄水槽本体の上部より原水を供給するための
原水供給管、供給された原水中に、上記浄水槽本体の底
部より微細な気泡を混入させるための気泡供給手段、及
び処理水流出管を備える第1の浄水装置、並びに固形酸
素発生剤を含有する第1の水質浄化剤により構成される
第1の水質浄化層と、活性炭を含有する第2の水質浄化
剤により構成される第2の水質浄化層とを備える第2の
浄水装置からなることを特徴とする。
The water purification apparatus of the third invention is obtained by combining the water purification apparatus of the first invention or the second invention with a water purification apparatus having a specific structure for removing dust and the like. A raw water supply pipe for supplying raw water from the top of the water purification tank main body, a bubble supply means for mixing fine bubbles from the bottom of the water purification tank main body into the supplied raw water, and a treated water outflow pipe. 1 water purification apparatus, a first water purification layer composed of a first water purification agent containing a solid oxygen generating agent, and a second water purification composed of a second water purification agent containing activated carbon. And a second water purification device having a layer.

【0014】第3発明の上記「第1の浄水装置」のよう
に、原水中の微細な塵埃、有機物等を微細な気泡に付着
させ、気泡に同伴させて除去する装置は、簡易な構造で
あって、しかも大量の原水を短時間に処理することがで
きる。そのため、特に池、河川等、大量の水を浄化する
場合に好適である。上記「微細な気泡」は、通常、その
径が数μm、特に2〜5μm、例えば平均径が4μm程
度のものであればよい。このように微細な気泡は、原水
中を上昇する間に原水中に含まれる非常に微細な塵埃、
有機物等を容易に捕捉する。この塵埃等を捕捉し、これ
を同伴して水面に浮き出た気泡及び同伴された塵埃など
は、オーバーフローする原水の一部とともに除去され
る。
An apparatus for attaching fine dust, organic matter, and the like in raw water to fine bubbles and removing the fine particles and organic substances in the raw water along with the bubbles, as in the above-mentioned "first water purification apparatus" of the third invention, has a simple structure. In addition, a large amount of raw water can be treated in a short time. Therefore, it is particularly suitable for purifying a large amount of water such as a pond or a river. The above "fine bubbles" usually have a diameter of several μm, particularly 2 to 5 μm, for example, an average diameter of about 4 μm. Such fine bubbles are very fine dust contained in raw water while rising in raw water,
Easily captures organic matter. The dust and the like are captured, and the air bubbles that float on the water surface accompanying the dust and the accompanying dust are removed together with a part of the raw water that overflows.

【0015】また、第3発明において、第1の浄水装置
と上記「第2の浄水装置」とは、その配置の順序は特に
限定はされない。しかし、通常は、先ず、塵埃等を除去
して物理的に浄化された処理水とした後、酸素の付与及
び脱臭、脱色等を行うことが好ましい。更に、固形酸素
発生剤を含む第1の水質浄化層と活性炭を含む第2の水
質浄化層の配置の順序も特に限定はされない。いずれが
先であっても、固形酸素発生剤によって処理水に十分な
酸素を溶存させる効果、及び活性炭によって脱臭、脱色
し、且つ有機物等を除去する効果は同様に奏される。
[0015] In the third invention, the order of arrangement of the first water purification device and the above-mentioned "second water purification device" is not particularly limited. However, it is usually preferable to first remove dust and the like to obtain physically purified treated water, and then apply oxygen, deodorize and decolorize. Further, the order of disposing the first water purification layer containing the solid oxygen generating agent and the second water purification layer containing the activated carbon is not particularly limited. In either case, the effect of dissolving sufficient oxygen in the treated water by the solid oxygen generating agent and the effect of deodorizing and decoloring by the activated carbon and removing organic substances and the like are similarly exhibited.

【0016】しかし、一般に固形酸素発生剤に比べて微
細な粒子からなる活性炭を含む水質浄化層を先に配設し
た場合は、隔壁の構成によっては活性炭が固形酸素発生
剤を含む水質浄化層へ流入することがある。少量の活性
炭が流入しても、固形酸素発生剤の水質浄化の性能には
大きな影響はない。しかし、大量に流入した場合は、水
質浄化性能の変動もあり得るし、水質浄化剤を洗浄した
り、取り替えたりする際に、作業し難い、作業周辺が汚
損される等の問題がある。尚、この第1及び第2の水質
浄化層の配置の順序については、第2発明においても上
記と同様のことがいえる。
However, when the water purification layer containing activated carbon composed of finer particles than the solid oxygen generator is generally disposed first, the activated carbon is transferred to the water purification layer containing the solid oxygen generator depending on the configuration of the partition walls. May flow in. The inflow of a small amount of activated carbon does not have a significant effect on the water purification performance of the solid oxygen generator. However, when the water flows in a large amount, there is a possibility that the water purification performance may fluctuate, and when cleaning or replacing the water purification agent, there is a problem that the work is difficult and the surroundings of the work are soiled. In addition, about the order of arrangement | positioning of this 1st and 2nd water quality purification layer, it can be said that it is the same as the above also in 2nd invention.

【0017】第4発明の水質浄化方法は、原水中の異物
を浄水手段によって除去し、その後、この異物が除去さ
れた一次処理水を、固形酸素発生剤を含有する第1の水
質浄化剤により構成される第1の水質浄化層による第1
の浄化によって二次浄化することを特徴とする。また、
第5発明の水質浄化方法は、原水中の異物を浄水手段に
よって除去し、その後、この異物が除去された一次処理
水を、固形酸素発生剤を含有する第1の水質浄化剤によ
り構成される第1の水質浄化層による第1の浄化及び活
性炭を含有する第2の水質浄化剤により構成される第2
の水質浄化層による第2の浄化の一方を先に、他方をそ
の後に行って二次浄化することを特徴とする。
According to the water purification method of the fourth invention, the foreign matter in the raw water is removed by the water purification means, and then the primary treated water from which the foreign matter has been removed is treated with the first water purification agent containing the solid oxygen generating agent. First composed by the first water purification layer
It is characterized in that secondary purification is performed by purification. Also,
In the water purification method of the fifth invention, foreign matter in the raw water is removed by water purification means, and then the primary treated water from which the foreign matter has been removed is constituted by a first water purification agent containing a solid oxygen generating agent. The first purification by the first water purification layer and the second purification by the second water purification agent containing activated carbon.
One of the second purification by the water purification layer is performed first, and the other is performed thereafter to perform secondary purification.

【0018】尚、上記の第5発明において、第1と第2
の水質浄化層のいずれの処理を先にするかは特に限定さ
れないが、第2及び第3発明におけると同様に、固形酸
素発生剤を含む第1の水質浄化層による浄化を先に行う
ことが好ましい。また、第2発明におけると同様に、上
記の第1及び第2の水質浄化層は、一つの容器内に設け
てもよいし、それぞれを別個の容器内に設け、それら容
器を配管によって接続するようにしてもよい。更に、上
記「異物」には、上記「原水」中の固形物、浮遊物など
も含まれ、また、有機物も無機物も含まれるものとす
る。
In the above-mentioned fifth invention, the first and the second
It is not particularly limited which treatment of the water purification layer is performed first, but similarly to the second and third inventions, the purification by the first water purification layer containing the solid oxygen generating agent can be performed first. preferable. Further, as in the second invention, the first and second water purification layers may be provided in one container, or may be provided in separate containers, and the containers are connected by piping. You may do so. Further, the “foreign matter” includes solids and suspended matters in the “raw water”, and also includes organic substances and inorganic substances.

【0019】第4及び第5発明において、上記「浄水手
段」は、第6発明のように濾過によって異物を除去する
ものとすることができる。このような濾過は、ゼオライ
ト、パーライト等の多孔質体であって、浄水作用を有す
る無機粉粒体等からなる濾過剤によって行うことがで
き、これら濾過剤は2種以上を併用することもできる。
また、濾過は、各種酸化物等を焼成して得られる多孔質
セラミックス、ポリエチレン、ポリプロピレンなどから
なる多孔質フィルム及び多孔質中空糸膜などの濾過材に
よって行うこともできる。尚、第1及び第2発明の水質
浄化装置には、これらの濾過によって異物を除去する浄
水装置を組み合わせて使用することができる。
In the fourth and fifth inventions, the "water purification means" may remove foreign matter by filtration as in the sixth invention. Such filtration can be performed using a porous agent such as zeolite or perlite, and a filtering agent composed of an inorganic powder or the like having a water-purifying effect. These filtering agents can be used in combination of two or more. .
Further, the filtration can also be performed using a filtering material such as a porous film obtained by firing various oxides or the like, a porous film made of polyethylene, polypropylene, or the like, and a porous hollow fiber membrane. It should be noted that the water purification devices of the first and second inventions can be used in combination with a water purification device for removing foreign substances by filtration.

【0020】また、第7発明のように、浄水手段とし
て、第3発明における第1の浄水装置を使用することも
できる。この浄水装置を用いる場合は、例えば浄水槽の
上部から原水を連続的に供給し、供給された原水中に、
浄水槽の底部より微細な気泡を供給し、原水中の塵埃、
有機物等の異物を、原水中を上昇する気泡に付着させ、
同伴させて、この異物を原水の水面に浮上させた後、原
水の一部とともに浄水槽の上端面からオーバーフローさ
せて除去することができる。
Further, as in the seventh invention, the first water purification device in the third invention can be used as the water purification means. When using this water purification device, for example, raw water is continuously supplied from the upper part of a water purification tank, and the supplied raw water is
Supply fine air bubbles from the bottom of the water purification tank,
Foreign substances such as organic substances are attached to bubbles rising in raw water,
After the foreign substances are caused to float on the surface of the raw water together with the raw water, they can be removed by overflowing from the upper end surface of the water purification tank together with a part of the raw water.

【0021】更に、本発明の水質浄化方法では、第8発
明のように、浄化すべき原水を、閉鎖水域から取水し、
第4〜7発明の方法によって浄化した後、処理水を再び
取水した閉鎖水域に戻す方法とすることができる。上記
「閉鎖水域」とは、池、湖、湾などの他、河川等であっ
ても、水流に乏しく、水が停滞している箇所をも意味す
るものとする。このような閉鎖水域において、本発明の
方法によって特に連続的に水質浄化を実施した場合、そ
の浄水効果に優れ、非常に好ましい。
Further, according to the water purification method of the present invention, as in the eighth invention, raw water to be purified is taken from a closed water area,
After the purification by the method of the fourth to seventh inventions, the treated water can be returned to the closed water area from which the treated water has been taken again. The “closed water area” means a pond, a lake, a bay, or the like, as well as a river or the like, where the water flow is poor and the water is stagnant. In such a closed water area, when the water purification is performed particularly continuously by the method of the present invention, the water purification effect is excellent and it is very preferable.

【0022】水質汚濁が深刻になっていることは前記の
通りであるが、水質の有機汚濁化として定義、把握され
ている現象として富栄養化の問題がある。特に湖水、池
水など閉鎖水域の富栄養化の原因である藻類の繁殖に必
要な栄養として知られているのが、リン及び窒素成分で
ある。そして、一般に藻類の繁殖はリン成分の量によっ
て制限を受けるとされているが、従来の水質浄化装置で
は、このリン成分の除去は十分ではなかった。本発明に
おいて、好適な固形酸素発生剤として使用される過酸化
カルシウムは、この水中のリン成分を除去する優れた効
果をも有する。そのため、本発明の水質浄化装置を使用
して水質を浄化すれば、藻類の繁殖が制限され、富栄養
化現象の発生が抑えられる。
As described above, water pollution has become serious, but there is a problem of eutrophication as a phenomenon defined and understood as organic pollution of water quality. In particular, phosphorus and nitrogen components are known as nutrients necessary for the propagation of algae which cause eutrophication in closed water areas such as lake water and pond water. It is generally said that the growth of algae is limited by the amount of the phosphorus component. However, the removal of the phosphorus component was not sufficient in the conventional water purification device. In the present invention, calcium peroxide used as a suitable solid oxygen generator also has an excellent effect of removing the phosphorus component in the water. Therefore, if the water quality is purified using the water purification device of the present invention, the propagation of algae is restricted, and the occurrence of the eutrophication phenomenon is suppressed.

【0023】[0023]

【発明の実施の形態】以下、実施例によって本発明を更
に詳しく説明する。 実施例 図1は、第3発明に対応する水質浄化装置の縦断面図で
ある。 (1) 第1の浄水装置 図1において、1は第1の浄水装置であり、2は第2の
浄水装置である。また、11は浄水槽本体であり、その
横断面は円形である。111は浄水槽本体外壁、112
は浄水槽本体底板、113は外筒、114は内筒、11
5は浮上異物排水配管である。外筒113及び内筒11
4の横断面も円形である。3は原水供給管である。
DESCRIPTION OF THE PREFERRED EMBODIMENTS Hereinafter, the present invention will be described in more detail by way of examples. Embodiment FIG. 1 is a longitudinal sectional view of a water purification apparatus according to a third invention. (1) First Water Purifier In FIG. 1, reference numeral 1 denotes a first water purifier, and 2 denotes a second water purifier. Reference numeral 11 denotes a water purification tank main body, and its cross section is circular. 111 is the outer wall of the water purification tank main body, 112
Is the bottom plate of the water purification tank main body, 113 is the outer cylinder, 114 is the inner cylinder, 11
5 is a floating foreign matter drainage pipe. Outer cylinder 113 and inner cylinder 11
The cross section of No. 4 is also circular. 3 is a raw water supply pipe.

【0024】4は気泡混入ポンプ、41は浄水槽本体底
板112に取り付けられた気泡発生器である。5は処理
水を第1の浄水装置1から第2の浄水装置2へ移送する
ための送水管である。尚、外筒113は支持棒等によっ
て、浄水槽本体外壁111或いは浄水槽本体底板112
等に固定し、支えてもよいし、上部から吊り下げる形態
としてもよい。
4 is an air bubble mixing pump, and 41 is an air bubble generator attached to the bottom plate 112 of the water purification tank main body. Reference numeral 5 denotes a water pipe for transferring the treated water from the first water purification device 1 to the second water purification device 2. Note that the outer cylinder 113 is supported by a support rod or the like and the outer wall 111 of the water purification tank main body or the bottom plate 112 of the water purification tank main body.
Or the like, and may be supported, or may be suspended from above.

【0025】(2) 第2の浄水装置 21は第2の浄水装置の本体であり、この本体21の横
断面も円形である。211は外壁、212は底板、21
3は隔壁である。6は処理水流出管である。この隔壁2
13によって横断面が半円形に二分された二つの浄水槽
には、それぞれ固形酸素発生剤粉末(過酸化カルシウム
粉末、大同ほくさん株式会社製、商品名「オーツーパワ
ー」)及び活性炭(銀が担持された浄水用の市販品)が
充填されている。214は固形酸素発生剤が充填された
浄水槽であり、固形酸素発生剤7が充填されている。2
15は活性炭が充填された浄水槽であり、活性炭8が充
填されている。
(2) The second water purifier 21 is a main body of the second water purifier, and the main body 21 has a circular cross section. 211 is an outer wall, 212 is a bottom plate, 21
3 is a partition. Reference numeral 6 denotes a treated water outflow pipe. This partition 2
13, two oxygen purifier powders (calcium peroxide powder, manufactured by Daido Hokusan Co., Ltd., trade name "Auto Two Power") and activated carbon (silver) are carried in two water purification tanks each having a semicircular cross section. (A commercial product for water purification). Reference numeral 214 denotes a water purification tank filled with a solid oxygen generating agent, which is filled with the solid oxygen generating agent 7. 2
Reference numeral 15 denotes a water purification tank filled with activated carbon, which is filled with activated carbon 8.

【0026】尚、第1の浄水装置1の浄水槽本体11及
び第2の浄水装置の本体21は、いずれも繊維強化塩化
ビニル樹脂製であり、浮上異物排水配管115、原水供
給管3、送水管5及び処理水流出管6はステンレススチ
ール製である。また、図示はしていないが、送水管5の
固形酸素発生剤が充填された浄水槽214への入口及び
活性炭が充填された浄水槽215から処理水流出管6へ
の出口には、水は容易に透過するが、固形酸素発生剤7
及び活性炭8は容易に透過しない大きさの透孔を有する
フィルタが装着されている。
The water purifying tank main body 11 of the first water purifying apparatus 1 and the main body 21 of the second water purifying apparatus are both made of fiber-reinforced vinyl chloride resin. The water pipe 5 and the treated water outflow pipe 6 are made of stainless steel. Although not shown, water is supplied to the inlet of the water supply pipe 5 into the water purification tank 214 filled with the solid oxygen generating agent and the outlet from the water purification tank 215 filled with activated carbon to the treated water outflow pipe 6. Easily permeates, but solid oxygen generator 7
In addition, the activated carbon 8 is provided with a filter having a through hole having a size that does not easily transmit.

【0027】(3) 浄水方法 原水供給管3から浄水槽本体11中に流入した原水は、
浄水槽本体底板112に向かって流れ、この原水の流れ
と対向して気泡発生器41から微細な気泡が上昇する。
この際、気泡には原水中の微小な塵埃、有機物等が付着
し、気泡はこれらを同伴して水面まで上昇する。水面ま
で上昇したこの気泡及び塵埃、有機物等は浄水槽本体外
壁111の上端面からオーバーフローする原水とともに
浮上異物排水配管115中に流下し、廃棄される。一
方、浄化された原水、即ち一次処理水は、浄水槽本体底
板112と外筒113の下端面との空隙から、外筒11
3と内筒114によって形成される流路に流入し、その
流路を上昇し、内筒114の上端面から内筒114内に
流入し、そのまま送水管5を通って第2の浄水装置2へ
移送される。
(3) Water Purification Method The raw water flowing into the water purification tank main body 11 from the raw water supply pipe 3 is:
The water flows toward the water purification tank main body bottom plate 112, and fine bubbles rise from the bubble generator 41 in opposition to the flow of the raw water.
At this time, fine dust, organic matter and the like in the raw water adhere to the bubbles, and the bubbles rise to the surface of the water accompanied by these. The bubbles, dust, organic matter, etc., which have risen to the water surface, flow down into the floating foreign matter drain pipe 115 together with the raw water overflowing from the upper end surface of the water purification tank main body outer wall 111, and are discarded. On the other hand, the purified raw water, that is, the primary treated water, is supplied from the gap between the water purification tank main body bottom plate 112 and the lower end surface of the outer cylinder 113 to the outer cylinder 11.
3 and the inner tube 114, flows up the channel, flows into the inner tube 114 from the upper end surface of the inner tube 114, and passes through the water supply pipe 5 as it is to the second water purification device 2 Transferred to

【0028】一次処理水は送水管5から固形酸素発生剤
6が充填された浄水槽214へ流入する。隔壁213
は、第2の浄水装置本体21と同一の材質であり、第2
の浄水装置の本体21の底板212と、この隔壁213
の下端面との間には、隔壁213の全幅に渡って空間2
16が設けられている。また、この空間216には不織
布が配設されており、固形酸素発生剤7と活性炭8とが
混ざり合わないようになっている。固形酸素発生剤7か
らなる第1の水質浄化層を透過し、酸素が付与された処
理水は、空間216に配設された不織布を透過し、活性
炭8が充填された浄水層215に流入する。この活性炭
からなる第2の水質浄化層を透過し、脱色、脱臭され、
且つ有機物等が更に除去された二次処理水は処理水流出
管8から流出し、この塵埃、有機物等が除去され、十分
な酸素が溶存し、且つ脱色、脱臭された処理水は、原水
を取水した池等の、原水を取り入れる箇所とは適宜離れ
た箇所に送り返される。
The primary treated water flows from the water supply pipe 5 into the water purifying tank 214 filled with the solid oxygen generating agent 6. Partition wall 213
Is the same material as the second water purification device main body 21, and the second
The bottom plate 212 of the main body 21 of the water purification device and the partition wall 213
Between the lower end surface of the partition 213 and the entire width of the partition 213.
16 are provided. Further, a nonwoven fabric is provided in the space 216 so that the solid oxygen generator 7 and the activated carbon 8 do not mix. The treated water that has passed through the first water purification layer made of the solid oxygen generator 7 and has been provided with oxygen permeates through the nonwoven fabric provided in the space 216 and flows into the water purification layer 215 filled with activated carbon 8. . It permeates through the second water purification layer made of activated carbon, and is decolorized and deodorized.
The secondary treated water from which organic substances and the like have been further removed flows out from the treated water outflow pipe 8, and the dust, organic substances and the like have been removed, sufficient oxygen has been dissolved, and the decolorized and deodorized treated water has the same effect as the raw water It is sent back to a place, such as a pond where water is taken, away from the place where raw water is taken.

【0029】実験例 富栄養化現象の原因である藻類の繁殖に必要な栄養の一
種であるオルトリン酸が、固形酸素発生剤によって、ど
の程度除去されるか検討した。試験は、蒸留水にオルト
リン酸を溶解して、イオン濃度42ppm、26ppm
及び4.5ppmの水溶液を調製し、この中に図2〜4
に示すようにイオン濃度に応じて所定量の固形酸素発生
剤(実施例と同じものを用いた。)を投入し、初期濃度
の経時変化を測定することにより実施した。
Experimental Example It was examined how much orthophosphoric acid, a kind of nutrient necessary for the propagation of algae, which causes eutrophication, is removed by a solid oxygen generator. The test was performed by dissolving orthophosphoric acid in distilled water, and ion concentrations of 42 ppm and 26 ppm.
And a 4.5 ppm aqueous solution was prepared, in which FIGS.
As shown in Table 2, a predetermined amount of a solid oxygen generating agent (the same one as in Example was used) was charged according to the ion concentration, and the change over time in the initial concentration was measured.

【0030】自然界の池、湖等におけるオルトリン酸イ
オン濃度はある程度の幅があるものと思われる。例えば
東京都大田区の洗足池の全有機リン化合物の量から推定
されるイオン濃度は4〜10ppm程度である。従っ
て、上記のイオン濃度42ppm及び26ppmの試験
は、通常、自然界では考えられない高濃度での試験であ
る。それでも図2及び図3の結果によれば、試験水10
リットル当たり1gの酸素発生剤によって、僅か3日で
イオン濃度は当初の1/10程度にまで低下しているこ
とが分かる。また、図4の結果によれば、当初濃度が低
い場合は、当初濃度が高い場合ほどの著しい濃度低下は
みられないが、イオン濃度の絶対値は非常に小さく、こ
れらの試験により、固形酸素発生剤の優れたオルトリン
酸除去効果が裏付けられた。
It is considered that the concentration of orthophosphate ions in ponds, lakes and the like in the natural world has a certain range. For example, the ion concentration estimated from the amount of all the organic phosphorus compounds in the Senzoku pond in Ota-ku, Tokyo is about 4 to 10 ppm. Therefore, the above-mentioned tests at ion concentrations of 42 ppm and 26 ppm are tests at high concentrations which are not considered in nature. Nevertheless, according to the results of FIGS. 2 and 3, the test water 10
It can be seen that the ion concentration is reduced to about 1/10 of the initial value in only 3 days by 1 g of the oxygen generating agent per liter. According to the results of FIG. 4, when the initial concentration is low, the concentration does not decrease as much as when the initial concentration is high, but the absolute value of the ion concentration is very small. The excellent orthophosphoric acid removal effect of the generator was supported.

【0031】尚、図2〜4において、○は10リットル
の水溶液に1.0gの固形酸素発生剤を投入した場合、
△は10リットルの水溶液に3.0gの固形酸素発生剤
を投入した場合、及び図2の□は10リットルの水溶液
に5.0gの固形酸素発生剤を投入した場合の試験結果
を表す。
In FIGS. 2 to 4, ○ indicates that 1.0 g of a solid oxygen generator was added to a 10 liter aqueous solution.
Δ indicates the test results when 3.0 g of the solid oxygen generator was added to a 10 liter aqueous solution, and □ in FIG. 2 indicates the test results when 5.0 g of the solid oxygen generator was added to a 10 liter aqueous solution.

【0032】[0032]

【発明の効果】第1発明の水質浄化装置によれば、これ
までの水質浄化において特に考慮はされていなかった被
処理水への酸素の付与がなされる。このように十分な酸
素が溶存した処理水とすることにより、富栄養化の防止
等、特定の水質浄化の効果が奏される。また、第2発明
のように、活性炭を含有する水質浄化層を併用すること
により、更に脱色、脱臭された処理水とすることができ
る。更に、第3発明のように、多量の原水の塵埃等を効
率よく除去することができる水質浄化装置を組み合わせ
ることにより、第1発明及び第2発明の水質浄化の効果
をより高めることができる。
According to the water purification apparatus of the first invention, oxygen is added to the water to be treated, which has not been particularly considered in the conventional water purification. By using such treated water in which sufficient oxygen is dissolved, specific water purification effects such as prevention of eutrophication can be achieved. Further, as in the second invention, by using a water purification layer containing activated carbon in combination, it is possible to obtain decolorized and deodorized treated water. Further, by combining a water purification device capable of efficiently removing a large amount of dust and the like of raw water as in the third invention, the effect of the water purification of the first invention and the second invention can be further enhanced.

【0033】また、第4及び第5発明の水質浄化方法に
よれば、塵埃等を除去する浄水手段と、少なくとも処理
水に十分な酸素を溶存させるための浄水手段とが組み合
わせられる。それによって、各浄水手段が有する特定の
水質浄化の効果が併せ奏せられ、塵埃等を含まず、十分
な酸素が溶存し、且つ脱色、脱臭がなされた処理水を容
易に得ることができる。本発明の水質浄化方法によれ
ば、上記のように十分な酸素が溶存した処理水とするこ
とができると同時に、オルトリン酸イオン濃度の低下
等、特定の効果が併せ奏される。
According to the water purification methods of the fourth and fifth inventions, the water purification means for removing dust and the like and the water purification means for dissolving at least sufficient oxygen in the treated water are combined. As a result, the specific water purification effect of each water purification means can be obtained, and it is possible to easily obtain treated water that does not contain dust and the like, has sufficient oxygen dissolved therein, and is decolorized and deodorized. According to the water purification method of the present invention, it is possible to obtain treated water in which sufficient oxygen is dissolved as described above, and at the same time, specific effects such as a decrease in the concentration of orthophosphate ions are exerted.

【0034】更に、塵埃等を除去する浄水手段として
は、第6発明の濾過手段の他、第7発明のように、第3
発明に対応する浄水手段とすることができる。このよう
に、本発明の水質浄化方法では、各種の浄水手段を適宜
組み合わせることができる。更に、本発明では、第8発
明のように、池、湖等の閉鎖水域において、その浄水効
果が顕著であり、水質汚濁が大きな問題となっている、
これら池、湖等の水質を十分に浄化することができる。
Further, as the water purifying means for removing dust and the like, in addition to the filtering means according to the sixth invention, a third water purifying means as in the seventh invention is used.
Water purification means corresponding to the invention can be provided. Thus, in the water purification method of the present invention, various water purification means can be appropriately combined. Further, in the present invention, as in the eighth invention, the water purification effect is remarkable in closed water areas such as ponds and lakes, and water pollution is a major problem.
The water quality of these ponds and lakes can be sufficiently purified.

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

【図1】第3発明に対応する水質浄化装置の縦断面図で
ある。
FIG. 1 is a vertical sectional view of a water purification device according to a third invention.

【図2】初期リン酸イオン濃度を42ppmとした場合
の、リン酸イオン濃度の経時変化を表すグラフである。
FIG. 2 is a graph showing a change over time in a phosphate ion concentration when an initial phosphate ion concentration is 42 ppm.

【図3】初期リン酸イオン濃度を26ppmとした場合
の、リン酸イオン濃度の経時変化を表すグラフである。
FIG. 3 is a graph showing a change over time in a phosphate ion concentration when an initial phosphate ion concentration is 26 ppm.

【図4】初期リン酸イオン濃度を4.5ppmとした場
合の、リン酸イオン濃度の経時変化を表すグラフであ
る。
FIG. 4 is a graph showing a change over time of a phosphate ion concentration when an initial phosphate ion concentration is 4.5 ppm.

【符号の説明】[Explanation of symbols]

1;第1の浄水装置、11;浄水槽本体、111;浄水
槽本体外壁、112;浄水槽本体底板、113;外筒、
114;内筒、115;浮上異物排水配管、2;第2の
浄水装置、21;第2の浄水装置の本体、211;外
壁、212;底板、213;隔壁、214;固形酸素発
生剤が充填された浄水槽、215;活性炭が充填された
浄水槽、216、空間、3;原水供給管、4;気泡混入
ポンプ、41;気泡発生器、5;送水管、6;処理水流
出管、7;固形酸素発生剤、8;活性炭。
1; first water purification device, 11; water purification tank main body, 111; water purification tank main body outer wall, 112; water purification tank main body bottom plate, 113;
114; inner cylinder, 115; floating foreign matter drainage pipe, 2; second water purification device, 21; main body of second water purification device, 211; outer wall, 212; bottom plate, 213; partition wall, 214; Purified water tank, 215; water tank filled with activated carbon, 216, space, 3; raw water supply pipe, 4; bubble mixing pump, 41; bubble generator, 5; water supply pipe, 6; treated water outflow pipe, 7 Solid oxygen generator, 8; activated carbon.

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 FI C02F 3/10 C02F 3/10 Z ──────────────────────────────────────────────────続 き Continued on the front page (51) Int.Cl. 6 Identification code FI C02F 3/10 C02F 3/10 Z

Claims (8)

【特許請求の範囲】[Claims] 【請求項1】 固形酸素発生剤を含有する第1の水質浄
化剤により構成される第1の水質浄化層を備えることを
特徴とする水質浄化装置。
1. A water purification apparatus comprising: a first water purification layer comprising a first water purification agent containing a solid oxygen generating agent.
【請求項2】 固形酸素発生剤を含有する第1の水質浄
化剤により構成される第1の水質浄化層と、活性炭を含
有する第2の水質浄化剤により構成される第2の水質浄
化層とを備えることを特徴とする水質浄化装置。
2. A first water purification layer composed of a first water purification agent containing a solid oxygen generating agent, and a second water purification layer composed of a second water purification agent containing activated carbon. A water purification device comprising:
【請求項3】 浄水槽本体、該浄水槽本体の上部より原
水を供給するための原水供給管、供給された原水中に、
上記浄水槽本体の底部より微細な気泡を混入させるため
の気泡供給手段、及び処理水流出管を備える第1の浄水
装置、並びに固形酸素発生剤を含有する第1の水質浄化
剤により構成される第1の水質浄化層と、活性炭を含有
する第2の水質浄化剤により構成される第2の水質浄化
層とを備える第2の浄水装置からなることを特徴とする
水質浄化装置。
3. A water purification tank main body, a raw water supply pipe for supplying raw water from an upper portion of the water purification tank main body,
A first water purification device having a bubble supply means for mixing fine bubbles from the bottom of the water purification tank main body, a treated water outflow pipe, and a first water purification agent containing a solid oxygen generating agent. A water purification device comprising: a second water purification device including a first water purification layer and a second water purification layer including a second water purification agent containing activated carbon.
【請求項4】 原水中の異物を浄水手段によって除去
し、その後、この異物が除去された一次処理水を、固形
酸素発生剤を含有する第1の水質浄化剤により構成され
る第1の水質浄化層による第1の浄化によって二次浄化
することを特徴とする水質浄化方法。
4. A method for removing foreign matter in raw water by water purification means, and then removing the foreign matter from the first treated water to a first water quality comprising a first water purification agent containing a solid oxygen generating agent. A water purification method, wherein secondary purification is performed by first purification by a purification layer.
【請求項5】 原水中の異物を浄水手段によって除去
し、その後、この異物が除去された一次処理水を、固形
酸素発生剤を含有する第1の水質浄化剤により構成され
る第1の水質浄化層による第1の浄化及び活性炭を含有
する第2の水質浄化剤により構成される第2の水質浄化
層による第2の浄化の一方を先に、他方をその後に行っ
て二次浄化することを特徴とする水質浄化方法。
5. A method for removing foreign matter in raw water by means of water purification means, and then removing the foreign matter from the primary treated water by a first water purification agent comprising a first water purification agent containing a solid oxygen generating agent. Performing one of the first purification by the purification layer and the second purification by the second water purification layer composed of the second water purification agent containing activated carbon first, and then performing the other to perform secondary purification. A water purification method characterized by the following.
【請求項6】 上記浄水手段が、上記原水を濾過するこ
とによって、該原水中の上記異物を濾別し、除去するも
のである請求項4又は5記載の水質浄化方法。
6. The water purification method according to claim 4, wherein the water purification means filters and removes the foreign matter in the raw water by filtering the raw water.
【請求項7】 上記浄水手段が、上記原水中を移動する
気泡に、該原水中の異物を付着させ、同伴させて、上記
気泡及び該気泡に同伴する上記異物を、上記原水の一部
とともに除去するものである請求項4又は5記載の水質
浄化方法。
7. The water purification means attaches foreign substances in the raw water to the bubbles moving in the raw water and causes the foreign substances to accompany the bubbles, and removes the air bubbles and the foreign substances accompanying the bubbles together with a part of the raw water. The water purification method according to claim 4 or 5, wherein the water quality is removed.
【請求項8】 上記原水は、閉鎖水域から取水され、浄
化後、再び該閉鎖水域に戻される請求項4乃至7のいず
れか1項に記載の水質浄化方法。
8. The water purification method according to claim 4, wherein the raw water is taken from a closed water area, and after being purified, returned to the closed water area.
JP8297340A 1996-10-18 1996-10-18 Apparatus and method for cleaning water Pending JPH10118629A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8297340A JPH10118629A (en) 1996-10-18 1996-10-18 Apparatus and method for cleaning water

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8297340A JPH10118629A (en) 1996-10-18 1996-10-18 Apparatus and method for cleaning water

Publications (1)

Publication Number Publication Date
JPH10118629A true JPH10118629A (en) 1998-05-12

Family

ID=17845260

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8297340A Pending JPH10118629A (en) 1996-10-18 1996-10-18 Apparatus and method for cleaning water

Country Status (1)

Country Link
JP (1) JPH10118629A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100413000B1 (en) * 2001-10-25 2003-12-31 이희권 Wastewater disposal device
JP2005007257A (en) * 2003-06-18 2005-01-13 Ataka Construction & Engineering Co Ltd Phosphorus recovering apparatus and method for treating phosphorus-containing organic wastewater
JP2006239583A (en) * 2005-03-03 2006-09-14 Mie Univ Sintered body for water purification, and production method

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100413000B1 (en) * 2001-10-25 2003-12-31 이희권 Wastewater disposal device
JP2005007257A (en) * 2003-06-18 2005-01-13 Ataka Construction & Engineering Co Ltd Phosphorus recovering apparatus and method for treating phosphorus-containing organic wastewater
JP2006239583A (en) * 2005-03-03 2006-09-14 Mie Univ Sintered body for water purification, and production method

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