JP2002370097A - Nitrate nitrogen treatment apparatus and treatment method using the same - Google Patents

Nitrate nitrogen treatment apparatus and treatment method using the same

Info

Publication number
JP2002370097A
JP2002370097A JP2001178976A JP2001178976A JP2002370097A JP 2002370097 A JP2002370097 A JP 2002370097A JP 2001178976 A JP2001178976 A JP 2001178976A JP 2001178976 A JP2001178976 A JP 2001178976A JP 2002370097 A JP2002370097 A JP 2002370097A
Authority
JP
Japan
Prior art keywords
water
nitrate nitrogen
water tank
treated
material layer
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.)
Granted
Application number
JP2001178976A
Other languages
Japanese (ja)
Other versions
JP4772216B2 (en
Inventor
Toshiaki Miyanaga
俊明 宮永
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.)
Nippon Steel Chemical and Materials Co Ltd
Original Assignee
Nippon Steel Chemical 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 Nippon Steel Chemical Co Ltd filed Critical Nippon Steel Chemical Co Ltd
Priority to JP2001178976A priority Critical patent/JP4772216B2/en
Publication of JP2002370097A publication Critical patent/JP2002370097A/en
Application granted granted Critical
Publication of JP4772216B2 publication Critical patent/JP4772216B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Classifications

    • Y02W10/12

Landscapes

  • Farming Of Fish And Shellfish (AREA)
  • Removal Of Specific Substances (AREA)
  • Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
  • Filtration Of Liquid (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a nitrate nitrogen treatment apparatus capable of simply removing nitrate nitrogen in a large-sized water tank or a closed system such a lakes and marshes or the like at a low cost. SOLUTION: The nitrate nitrogen treatment apparatus, which is constituted so that a water stream generation member like an air bubble generator is provided and a nitrate nitrogen removing material bed comprising a sulfur/ calcium carbonate component is arranged on the way of a water stream route formed from the water stream generation member and, if necessary, a dissolved oxygen lowering member comprising a water permeable material is arranged in the periphery thereof, is sunk in a system wherein water to be treated is housed in a water tank or the like to perform denitrification.

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】本発明は養魚槽等における閉
鎖系水域における硝酸性窒素の除去方法に関するもので
ある。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for removing nitrate nitrogen in closed water bodies in a fish tank or the like.

【0002】[0002]

【従来の技術】近年、閉鎖水域における硝酸性窒素処理
が問題になっている。例えば水槽における魚介類飼育の
場合、ホビー用の小規模なものから陸上養殖のような大
規模飼育に至るまで共通して硝酸性窒素処理が問題とな
っている。また、自然界においても、例えば水の入れ替
えに乏しい閉鎖系湾や湖沼の場合、年々硝酸性窒素濃度
が高まりつつあり、水産環境に少なからず悪影響を与え
つつある。
2. Description of the Related Art In recent years, nitrate nitrogen treatment in a closed water area has become a problem. For example, in the case of fish and shellfish breeding in an aquarium, nitrate nitrogen treatment is a common problem from small-scale hobby breeding to large-scale breeding such as land farming. Also, in the natural world, for example, in the case of closed bays and lakes where water replacement is poor, the concentration of nitrate nitrogen is increasing year by year, and this is exerting a considerable adverse effect on the marine environment.

【0003】ところが従来の硝酸性窒素処理技術では、
このような閉鎖系水域を対象とした場合、水素供与体を
投入が必要であったり、水の循環装置を持ちいらねばな
らないなど、本来の脱窒効率が低効率ゆえに大規模装置
且つ多大な費用がかかりがちであり、このような閉鎖水
域条件での硝酸性窒素処理対策が不充分な状況であっ
た。
However, in the conventional nitrate nitrogen treatment technology,
When targeting such closed waters, large-scale equipment and enormous cost are required because the original denitrification efficiency is low, such as the need to input a hydrogen donor and the need to have a water circulation device. And the measures for nitrate nitrogen treatment under such closed water conditions were insufficient.

【0004】硝酸性窒素処理という点では、WO00/186
94号公報には、硫黄とカルシウム系成分からなる窒素除
去材料を使用した硫黄酸化細菌による安価、且つ効率的
な硝酸性窒素処理が提案されている。この方法は、微生
物の働きにより脱窒を行うものであるため、環境の異な
る閉鎖系水域における硝酸性窒素処理への適用可能性に
は疑問があるものであった。
In terms of nitrate nitrogen treatment, WO 00/186
No. 94 proposes an inexpensive and efficient nitrate nitrogen treatment by a sulfur-oxidizing bacterium using a nitrogen-removing material composed of sulfur and a calcium-based component. Since this method performs denitrification by the action of microorganisms, its applicability to nitrate nitrogen treatment in closed water bodies with different environments was questionable.

【0005】[0005]

【発明が解決しようとする課題】本発明はこのような事
情に鑑みて開発されたものであって、上記課題を解決
し、必要且つ最小限の硫黄とカルシウム系からなる窒素
除去材料を用いて、閉鎖系水域における硝酸性窒素体を
効果的に除去することを可能とする安価で実用的な閉鎖
系水域における硝酸性窒素体の処理方法を提供するもの
である。
DISCLOSURE OF THE INVENTION The present invention has been developed in view of such circumstances, and solves the above-mentioned problems by using a necessary and minimum nitrogen-removing material comprising sulfur and calcium. Another object of the present invention is to provide an inexpensive and practical method for treating nitrate nitrogen in closed water bodies that enables effective removal of nitrate nitrogen in closed water bodies.

【0006】[0006]

【課題を解決するための手段】本発明は、水槽内の被処
理水等の閉鎖系において、水流発生部材を備え、該水流
発生部材によって形成された水流経路の途中に、硫黄と
炭酸カルシウム系成分からなる硝酸性窒素除去材料層を
設けた硝酸性窒素の処理装置である。また、本発明は、
前記硝酸性窒素除去材料層の周囲に、透水性素材からな
る溶存酸素低下部材を配置した硝酸性窒素の処理装置で
ある。更に、本発明は前記硝酸性窒素除去材料層の上流
側に、ろ過部材を設けてなる硝酸性窒素の処理装置であ
る。ここで、前記溶存酸素低下部材が、サンゴ砂又はロ
ックウールからなる多孔質材料であることが有利であ
る。
According to the present invention, there is provided a closed system for water to be treated in a water tank, comprising a water flow generating member, wherein a sulfur and calcium carbonate system is provided in the water flow path formed by the water flow generating member. This is a nitrate nitrogen treatment apparatus provided with a nitrate nitrogen removal material layer composed of components. Also, the present invention
An apparatus for treating nitrate nitrogen, wherein a dissolved oxygen reducing member made of a water-permeable material is arranged around the nitrate nitrogen removal material layer. Further, the present invention is an apparatus for treating nitrate nitrogen, comprising a filtration member provided upstream of the nitrate nitrogen removal material layer. Here, it is advantageous that the dissolved oxygen reducing member is a porous material made of coral sand or rock wool.

【0007】また、本発明は、水槽内の被処理水等の閉
鎖系において、水流発生部材より循環水流を形成させる
ことにより、水槽中の水を、硫黄と炭酸カルシウム系成
分からなる硝酸性窒素除去材料層を通過させた後、再び
水槽中に放出、循環する硝酸性窒素の処理方法である。
更に、本発明は、大型水槽又は湖沼等の水を上記水槽中
に導入し、上記水槽中の水又は処理水の少なくとも一部
を大型水槽又は湖沼等に戻す前記の硝酸性窒素の処理方
法である。
Further, in the present invention, in a closed system such as water to be treated in a water tank, a circulating water flow is formed by a water flow generating member so that water in the water tank is converted into nitrate nitrogen containing sulfur and calcium carbonate-based components. This is a method for treating nitrate nitrogen that is released and circulated again into the water tank after passing through the removal material layer.
Further, the present invention relates to the method for treating nitrate nitrogen, wherein water in a large water tank or a lake is introduced into the water tank, and at least a part of the water in the water tank or the treated water is returned to the large water tank or the lake. is there.

【0008】次に、本発明の好ましい態様のいくつかを
示す。 a) 水槽又は被処理水中に、少なくとも一部が透水性
固体壁で構成された容器状体を浸漬した構造を有し、該
容器状体の下部からはほぼ垂直に上昇する上昇管であっ
て、管の内部に上昇水流を発生させるための気体発生部
を有し、管の先端が容器状体から突出して容器状体上部
にある水中に達する上昇管を設置し、且つ、該容器状体
の内部には硫黄と炭酸カルシウム系成分からなる硝酸性
窒素除去材料層を設けた閉鎖系水域内の硝酸性窒素の処
理装置。ここで、上昇管と気体発生部は、前記水流発生
部材の一例である。また、透水性固体壁は、前記酸素低
下部材の一例ともなる。
Next, some preferred embodiments of the present invention will be described. a) a rising pipe which has a structure in which a container having at least a part of a water-permeable solid wall is immersed in a water tank or water to be treated, and which rises almost vertically from a lower portion of the container; A gas generating portion for generating a rising water flow inside the pipe, a rising pipe having a tip end of the pipe protruding from the container and reaching the water at the upper part of the container; An apparatus for treating nitrate nitrogen in a closed system water body provided with a nitrate nitrogen removal material layer composed of sulfur and calcium carbonate-based components inside. Here, the riser and the gas generating unit are examples of the water flow generating member. The water permeable solid wall is also an example of the oxygen reducing member.

【0009】b) 容器状体の下部を下層濾過板とし、
この上に硝酸性窒素除去材料層を設けると共に、任意の
位置に1又は2以上の上昇管を設けてなる硝酸性窒素の
処理装置。ここで、透水性固体壁が、砂利、サンゴ砂、
不織布及びロックウールのいずれか若しくはそれらの混
合物又はこれらを充填した多孔質材料であること、又は
透水性固体壁が、ロックウール層を有する多孔質材料で
あり、多孔質材料が透水性の膜、フィルム、金網又ガラ
スであることが有利である。また、下層濾過板と硫黄と
カルシウム系成分からなる硝酸性窒素除去材料層の間に
ロックウール層を有することも有利である。
B) The lower part of the container is a lower filter plate,
An apparatus for treating nitrate nitrogen, wherein a nitrate nitrogen removal material layer is provided thereon, and one or more risers are provided at arbitrary positions. Here, the permeable solid wall is gravel, coral sand,
Any of nonwoven fabric and rock wool or a mixture thereof or a porous material filled with them, or the water-permeable solid wall is a porous material having a rock wool layer, and the porous material is a water-permeable membrane, Advantageously, it is a film, wire mesh or glass. It is also advantageous to have a rock wool layer between the lower filter plate and the nitrate nitrogen removing material layer composed of sulfur and calcium components.

【0010】d) 上昇水流を発生させるための気体発
生部を有する上昇管を、硝酸性窒素除去材料層の中心部
に配置した硝酸性窒素の処理装置。ここで、上昇水流を
発生させるための気体発生部を有する上昇管を、硝酸性
窒素除去材料層の中心部に配置するように上昇管の下端
部を折り曲げて又は折り曲げずして中心部に配置し、該
中心部の上昇管に透水性の複数の穴を設けること、ある
いは上昇水流を発生させるための気体発生部を有する上
昇管を2つ以上設けることが有利である。
D) An apparatus for treating nitrate nitrogen in which a riser tube having a gas generating section for generating a rising water flow is disposed at the center of the nitrate nitrogen removal material layer. Here, a riser having a gas generating portion for generating a rising water flow is disposed at the center by bending or not bending the lower end of the riser so as to be disposed at the center of the nitrate nitrogen removing material layer. It is advantageous to provide a plurality of water-permeable holes in the central riser, or to provide two or more risers having a gas generator for generating a rising water flow.

【0011】e) 水槽又は被処理水中に、少なくとも
一部が透水性固体壁で構成された容器状体を浸漬し、該
容器状体の下部からはほぼ垂直に上昇する上昇管であっ
て、管の内部に上昇水流を発生させるための気体発生部
を有し、管の先端が容器状体から突出して容器状体上部
にある水中に達する上昇管の気体発生部に、気体を外部
から導入し、それにより上昇管から水を吸い上げて循環
水流を水槽中に形成させ、水槽中の水を透水性固体壁を
通して、該容器状体の内部に充填された硫黄と炭酸カル
シウム系成分からなる硝酸性窒素除去材料層を通過さ
せ、これを上昇管から吸い上げて水槽中に放出、循環す
る硝酸性窒素の処理方法。
E) a rising pipe which is immersed in a water tank or to-be-treated water at least partially comprising a water-permeable solid wall, and which rises almost vertically from a lower part of the container; A gas generator is provided inside the pipe to generate a rising water flow, and gas is introduced from the outside into the gas generator of the riser pipe, where the tip of the pipe protrudes from the container and reaches the water at the top of the container. Then, water is sucked up from the riser to form a circulating water flow in the water tank, and the water in the water tank is passed through the water-permeable solid wall, and the sulfuric acid and the nitric acid composed of the calcium carbonate-based component filled in the container are filled. A method for treating nitrate nitrogen, which is passed through a layer of nitrogen-removing material, sucked up from a riser, released into a water tank, and circulated.

【0012】本発明の処理装置は、硝酸性窒素除去材料
層と該層を通過する水流発生部材を有するものであれば
よいが、硝酸性窒素除去材料層を所定の厚みに維持する
ため、容器状体に硝酸性窒素除去材料層を配置すること
が好ましい。容器状体の形状は任意であるが、直方体形
状が製作の容易さから有利であるが、円筒形等であって
もよい。また、これらの処理装置は水槽中に1つである
必要は無く、目的に応じて複数使用してもよい。その使
用方法は、例えば、直列に連結したタイプや並列に並べ
たタイプであってもよい。更には並列タイプの場合、気
泡発生装置がそれぞれに設置されていても良い。また、
円筒形と直方体形状を併用してもよいし、並べ方も並列
でもよいし直列でもよい。また、水流発生部材として
は、容器状体から水中に突出する上昇管と気泡発生部を
有することがよい。
The treatment apparatus of the present invention may be any one having a nitrate nitrogen removing material layer and a water flow generating member passing through the layer. In order to maintain the nitrate nitrogen removing material layer at a predetermined thickness, a container is required. It is preferable to dispose a nitrate nitrogen removing material layer on the shape. The shape of the container is arbitrary, but a rectangular parallelepiped is advantageous from the viewpoint of ease of manufacture, but may be a cylinder or the like. Further, it is not necessary to provide one of these treatment devices in the water tank, and a plurality of treatment devices may be used according to the purpose. The method of use may be, for example, a type connected in series or a type arranged in parallel. Furthermore, in the case of a parallel type, a bubble generating device may be provided for each. Also,
The cylindrical shape and the rectangular parallelepiped shape may be used together, and the arrangement may be parallel or serial. Further, it is preferable that the water flow generating member has a riser tube and a bubble generating portion that protrude into the water from the container.

【0013】容器状体は上部が開放されているか、少な
くとも一部が透水性固体壁で構成されているが、水槽中
の水が所定速度で、硝酸性窒素除去材料層を通るように
するため透水性固体壁で構成される部分や、透水性材料
が選定される。通常、容器状体は水中に沈められた状態
で使用され、容器状体中の硝酸性窒素除去材料層を通過
した水は上昇管から、水槽に戻される。この際、水槽を
2つ以上に仕切り、上昇管から水槽に戻される水を優先
的に他の大型水槽等に戻すことも有利である。
The container is open at the top or at least partially formed of a water-permeable solid wall. The water in the water tank passes through the nitrate-nitrogen removing material layer at a predetermined speed. A portion composed of a water-permeable solid wall and a water-permeable material are selected. Usually, the container is used in a state of being submerged in water, and the water that has passed through the layer of the nitrate-nitrogen removing material in the container is returned to the water tank from the riser. At this time, it is also advantageous to divide the water tank into two or more tanks, and to preferentially return the water returned from the rising pipe to the water tank to another large water tank or the like.

【0014】ここで、透水性固体壁は、網状体や多孔質
体からなっていてもよく、それに接して砂利、サンゴ
砂、不織布及びロックウール等の粒状物又は繊維状物を
有していてもよい。これらの少なくとも一部が溶存酸素
低下部材を兼ねることが好ましい。有利にはサンゴ砂又
はロックウールであり、これは溶存酸素を消費して脱窒
菌の活動を高めると共に、BODを減少させることがで
きる酸化菌の繁殖に有効なためである。これらが粒状物
等である場合は、外側を透水性の膜、繊維、フィルム、
金網又ガラスで包むことが有利である。また、下層濾過
板を設け、SS分を除去することも有利である。更に、
透水性固体壁と硝酸性窒素除去材料層の間にロックウー
ル層を設けて、脱窒菌の繁殖場を広げることも有利であ
る。
Here, the water-permeable solid wall may be made of a net or a porous body, and has a granular or fibrous material such as gravel, coral sand, nonwoven fabric and rock wool in contact therewith. Is also good. It is preferable that at least a part of these also serve as a dissolved oxygen lowering member. Preference is given to coral sand or rock wool, because it consumes dissolved oxygen to increase the activity of denitrifying bacteria and is effective for the propagation of oxidizing bacteria which can reduce BOD. When these are granular materials and the like, the outside is a water-permeable membrane, fiber, film,
It is advantageous to wrap in wire mesh or glass. It is also advantageous to provide a lower filter plate to remove SS. Furthermore,
It is also advantageous to provide a rock wool layer between the water permeable solid wall and the nitrate nitrogen removing material layer to widen the breeding ground for denitrifying bacteria.

【0015】本発明において使用する硫黄と炭酸カルシ
ウム系成分からなる硝酸性窒素除去材料は、前記WO00
/18694号公報等で公知のものを使用することができる。
好ましくは、硫黄と石灰石粉末等の炭酸カルシウム粉末
を、約1:2〜2:1の割合で混合し、硫黄を溶融させ
て一体化させ、これを冷却し、所定の粒度に粉砕したも
のが挙げられる。また、硝酸性窒素除去材料層の構造や
量などは、処理水量や窒素分濃度に応じて窒素除去材料
充填量の構造や量を設計することが可能である。一般に
は流入水(kg)に対して0.05〜2倍量(kg)の充填量と
することが好ましく、より望ましくは0.1〜1倍量で
あることが好ましい。その他の処理条件はWO00/18694
号公報に準じて設計すれば良い。上記硝酸性窒素除去材
料の粒子形状に制限はないが、好ましくは20mm以下の
不定形状である。粒子形状が20mm以上でも脱窒効果は
発現できるが、ときとして処理槽内の効果的な水の流れ
を得られない場合が発生することも生ずることもある。
上記硝酸性窒素除去材料の充填方法には特に制限ない
が、かさ比重0.5以上で充填されていることが望まし
い。かさ比重が0.5より小さく充填されると、ときと
して無機充填層内を流れる水の流れが偏流を生ずる場合
があるために効果的な脱窒が得られない場合が生ずるこ
ともある。
The nitrate nitrogen removing material comprising sulfur and calcium carbonate-based components used in the present invention is the above-mentioned WO 00
/ 18694 and the like can be used.
Preferably, sulfur and calcium carbonate powder such as limestone powder are mixed at a ratio of about 1: 2 to 2: 1, and the sulfur is melted and integrated, cooled, and pulverized to a predetermined particle size. No. The structure and amount of the nitrate-nitrogen removing material layer can be designed in accordance with the amount of treated water and the concentration of nitrogen content. Generally, the filling amount is preferably 0.05 to 2 times the amount (kg) of the inflow water (kg), and more preferably 0.1 to 1 times the amount. Other processing conditions are WO00 / 18694
The design may be made in accordance with the publication of Japanese Patent Application Laid-Open Publication No. H10-209,878. The particle shape of the nitrate nitrogen removing material is not limited, but preferably has an irregular shape of 20 mm or less. Although the denitrification effect can be exhibited even if the particle shape is 20 mm or more, sometimes the case where an effective flow of water in the treatment tank cannot be obtained may occur.
The method for filling the nitrate nitrogen removing material is not particularly limited, but it is preferable that the material is filled with a bulk specific gravity of 0.5 or more. If the bulk specific gravity is less than 0.5, effective denitrification may not be obtained because sometimes the flow of water flowing in the inorganic packed bed may cause a drift.

【0016】被処理水は、硝酸性窒素(NO2 -又はNO3 -
が含まれた水であれば任意であるが、本発明の装置は閉
鎖系水域中の水、例えば養魚用の水槽、プール、池など
の水に適する。被処理水中の硝酸性窒素は数ppmから数
千ppmまで対応可能である。本発明においては、気泡発
生に用いられる気体は、特に制限されるものではなく、
通常の空気で差し支えない。但し硫黄酸化脱窒細菌を用
いるために、窒素ガスによる気泡発生により処理効果が
高まる場合がある。なお、本発明における硝酸性窒素処
理の原理は、上記硝酸性窒素除去材料と硫黄酸化脱窒細
菌によるものであるため、処理槽の温度は10〜50℃
であることが好ましく、より望ましくは20〜40℃で
ある。処理槽の温度が10℃よりも低くなったり、逆に
50℃よりも高くなると、硫黄酸化脱窒細菌の活性が低
下するために好ましくない。
The water to be treated, nitrate nitrogen (NO 2 - or NO 3 -)
The device of the present invention is suitable for water in a closed system water area, for example, a water tank for fish farming, a pool, a pond, and the like. The nitrate nitrogen in the water to be treated can correspond to several ppm to several thousand ppm. In the present invention, the gas used for bubble generation is not particularly limited,
Normal air is fine. However, due to the use of sulfur oxidizing and denitrifying bacteria, the treatment effect may be enhanced by the generation of bubbles by nitrogen gas. Since the principle of the nitrate nitrogen treatment in the present invention is based on the nitrate nitrogen removal material and the sulfur oxidizing and denitrifying bacteria, the temperature of the treatment tank is 10 to 50 ° C.
And more preferably 20 to 40 ° C. If the temperature of the treatment tank is lower than 10 ° C. or higher than 50 ° C., it is not preferable because the activity of the sulfur oxidizing and denitrifying bacteria decreases.

【0017】[0017]

【発明の実施の態様】以下、本発明の装置及びこの装置
を用いた処理方法について、参照図を用いて更に詳しく
説明する。図1は本発明の装置の容器状体と上昇管部分
を示す断面図である。容器状体は透水性の固体壁1と下
層濾過板(3)とから形成されている。容器状体の内部
には硝酸性窒素除去材料層(2)が設けられている。ま
た、容器状体の下層濾過板(3)からほぼ真上に上昇管
(4)が立設されており、上昇管低部には上昇水流を発
生するための気体吹き込み装置(6)が設けられてい
る。この装置は図示されない水槽中に沈められ、上昇管
(4)の上端が水中に没する水位となっている。
DESCRIPTION OF THE PREFERRED EMBODIMENTS The apparatus of the present invention and a processing method using the apparatus will be described below in more detail with reference to the drawings. FIG. 1 is a sectional view showing a container-like body and a riser portion of the apparatus of the present invention. The container comprises a water-permeable solid wall 1 and a lower filter plate (3). A nitrate-nitrogen removing material layer (2) is provided inside the container. An ascending pipe (4) is provided almost directly above the lower filter plate (3) of the container, and a gas blowing device (6) for generating an ascending water flow is provided at a lower portion of the ascending pipe. Have been. This device is submerged in a water tank (not shown), and the upper end of the riser (4) has a water level at which it is submerged in water.

【0018】水槽中の水は、固体壁1から硝酸性窒素除
去材料層(2)を通過した後、下層濾過板(3)を通過
して、上昇管(4)を通って上昇し、処理水(5)とな
って水槽中に合流する。その際、硝酸性窒素は硝酸性窒
素除去材料と脱窒菌の作用により無害な窒素ガスに変化
する。濾過板(3)は泡ガラスのようなものであること
が可能であり、硝酸性窒素除去材料層を通過した水の一
部は濾過板(3)から直接水槽中に合流してもよい。
The water in the water tank passes through the nitrate nitrogen removing material layer (2) from the solid wall 1, passes through the lower filter plate (3), rises through the riser (4), and is treated. It becomes water (5) and merges into the water tank. At that time, the nitrate nitrogen changes into harmless nitrogen gas by the action of the nitrate nitrogen removal material and the denitrifying bacteria. The filter plate (3) can be like foam glass, and a portion of the water that has passed through the nitrate nitrogen removal material layer may merge directly from the filter plate (3) into the water tank.

【0019】閉鎖水域における硝酸性窒素体処理では、
処理槽の中に被処理水を流入させる必要がある。従っ
て、従来方法ではポンプによる被処理水の吸引や循環装
置、攪拌装置の設置など、本来の処理以外の付帯装置が
大掛かりとなるために、一般に望まれる安価且つシンプ
ルな装置設計が難しい。そこで本発明においては、当該
装置の中心部に存在する管の中に、内部に気泡発生装置
(6)を設置することにより、気泡発生による管内の上
昇水流の発生によって、それに伴う硫黄とカルシウム系
成分からなる硝酸性窒素除去材料層への上部透水性固体
壁(1)からの被処理水の引水を可能としている。
In the treatment of nitrate nitrogen in a closed water area,
It is necessary to flow the water to be treated into the treatment tank. Therefore, in the conventional method, ancillary equipment other than the original treatment, such as suction of the water to be treated by a pump, installation of a circulation device, and a stirrer, becomes large-scale. Therefore, in the present invention, by installing an air bubble generating device (6) inside a pipe existing at the center of the apparatus, the rising water flow in the pipe due to the generation of air bubbles causes the sulfur and calcium-based The water to be treated can be drained from the upper permeable solid wall (1) to the nitrate-nitrogen removing material layer composed of the components.

【0020】なお、図1における水が浸透できる固体層
とは特に制限はないが、砂利、サンゴ砂、不織布、ロッ
クウールのいずれか若しくはそれらの混合物であること
が好ましく、より望ましくはロックウールである。ロッ
クウールはその微細な空隙性を有する故に、脱窒菌の繁
殖等に最適であることから特に優れた硝酸性窒素効果を
得ることが可能である。これらが所定の形状を保持する
ことができない場合は、多孔質の樹脂、金網、泡ガラス
等で外側形状又は外側形状と内側形状を作ることがよ
い。
The water-permeable solid layer in FIG. 1 is not particularly limited, but is preferably any of gravel, coral sand, nonwoven fabric, rock wool or a mixture thereof, and more preferably, rock wool. is there. Since rock wool has fine voids, it is most suitable for the propagation of denitrifying bacteria and the like, so that a particularly excellent nitrate nitrogen effect can be obtained. When these cannot maintain a predetermined shape, it is preferable to form the outer shape or the outer shape and the inner shape with a porous resin, wire mesh, foam glass, or the like.

【0021】上昇管の上部構造は開口部を有する限り制
限はないが、図2に示すようなL字形状や図3に示すT
字形状が有利である。上昇管の長さや太さを特に制限す
るものではなく、水槽の場合は水槽の高さに準じて設計
され、また池や沼の場合は水深に応じて設計することが
可能である。更に、下層濾過板の構造や大きさについて
も特に制限を設けるものではなく、市販の下層濾過装置
を使用できる。この下層濾過板に垂直に設置された上昇
管の設置位置や本数についても特に制限を設けるもので
はない。
The upper structure of the riser is not limited as long as it has an opening, but it has an L-shape as shown in FIG.
The letter shape is advantageous. There is no particular limitation on the length and thickness of the riser. In the case of a water tank, the riser can be designed according to the height of the water tank, and in the case of a pond or swamp, it can be designed according to the water depth. Further, the structure and size of the lower filter plate are not particularly limited, and a commercially available lower filter device can be used. There is no particular limitation on the installation position or the number of risers installed vertically to the lower filter plate.

【0022】図4は本発明の他の態様を示す断面図であ
り、下層濾過板(3)と硝酸性窒素除去材料層(2)の
間にロックウール層(7)を存在させた例を示す。この
ような構造とすると、硝酸性窒素処理に対してより優れ
た効果を得ることが可能となる。なお、図中の他の符号
は図1と同じである。
FIG. 4 is a sectional view showing another embodiment of the present invention, in which an example in which a rock wool layer (7) is present between a lower filter plate (3) and a nitrate nitrogen removing material layer (2). Show. With such a structure, it is possible to obtain a more excellent effect on the nitrate nitrogen treatment. The other symbols in the figure are the same as those in FIG.

【0023】図5は本発明の他の態様を示す断面図であ
り、容器状体(10)は上部に透水性固体壁を有さず、
被処理水は直接、硝酸性窒素除去材料層(2)の表面
(8)から内部に進入し、接触して脱窒され、管の下部
(9)より気体吹き込み装置(6)から気体により上昇
し、処理水(5)として流出する構造となっている。
FIG. 5 is a cross-sectional view showing another embodiment of the present invention, wherein the container (10) does not have a water-permeable solid wall at the top,
The water to be treated directly enters the inside from the surface (8) of the nitrate-nitrogen removing material layer (2), contacts and is denitrified, and rises from the lower part (9) of the pipe by gas from the gas blowing device (6). And flows out as treated water (5).

【0024】図6は本発明の他の態様を示す断面図であ
り、被処理水は透水性固体壁(11)から流入し、内部
の窒素除去材料充填層(2)を通過して、複数の穴が空
いた上昇管(12)の穴部分に入り込んだ後、気体吹き
込み装置(6)により管の下部から上部にむけて移動
し、処理水(5)として閉鎖系水域に合流する。図6に
示す装置においてもより効果的な結果を得ることが可能
である上記透水性固体壁(11)は、透水性を有する限
り制限するものではないが、ロックウールであることが
好ましい。ロックウールは脱窒菌などの生物菌の存在に
優れた効果を示すために、より効果的な硝酸性窒素体処
理を行うことが可能となる。また、ロックウールの繊維
構造により、水浸透の偏析などを防ぐ役割も得られる。
更に、ロックウールは他の繊維やプラスチックや金属等
と組合せて使用されて強度を高めることもできる。
FIG. 6 is a cross-sectional view showing another embodiment of the present invention. The water to be treated flows from the water-permeable solid wall (11), passes through the nitrogen-removing material-filled layer (2) inside, and becomes a plurality of pieces. After entering the hole portion of the riser pipe (12) having the hole, the gas moves from the lower part to the upper part of the pipe by the gas blowing device (6), and merges into the closed system water area as the treated water (5). The water-permeable solid wall (11) capable of obtaining more effective results also in the apparatus shown in FIG. 6 is not limited as long as it has water permeability, but is preferably rock wool. Since rock wool has an excellent effect on the presence of biological bacteria such as denitrifying bacteria, it is possible to perform more effective nitrate nitrogen treatment. Further, the role of preventing segregation of water permeation can be obtained by the fiber structure of rock wool.
Further, rock wool can be used in combination with other fibers, plastics, metals, etc. to increase strength.

【0025】図7は本発明の他の態様を示す断面図であ
り、被処理水は透水性固体壁(11)から流入し、内部
の窒素除去材料充填層(2)、次いでロックウール層
(13)を通過して、複数の穴が空いた上昇管(12)
の穴部分に入り込んだ後、気体吹き込み装置(6)によ
り上昇して、処理水(5)となる。
FIG. 7 is a cross-sectional view showing another embodiment of the present invention. The water to be treated flows from the water-permeable solid wall (11), and the nitrogen-removing material-filled layer (2) inside, and then the rock wool layer ( 13) Passing pipe with multiple holes (12)
After entering the hole, the water is raised by the gas blowing device (6) to become treated water (5).

【0026】図8及び図9は本発明の他の態様を示す断
面図であり、被処理水は透水性固体壁(11)から流入
し、内部の窒素除去材料充填層(2)を通過して又は次
いでロックウール層(13)を通過して、複数の穴が空
いた上昇管(12)の穴部分に入り込んだ後、気体吹き
込み装置(6)により上昇して、処理水(5)となる。
図8及び図9に示す態様では上昇管(12)は下部にお
いて水平に曲げられて横型の窒素除去材料充填層(2)
と大きい接触面積を有している。
FIGS. 8 and 9 are sectional views showing another embodiment of the present invention. The water to be treated flows from the water-permeable solid wall (11) and passes through the nitrogen-removing material-filled layer (2) inside. After passing through the rock wool layer (13) and entering the hole portion of the riser pipe (12) having a plurality of holes, it rises by the gas blowing device (6), and is treated with the treated water (5). Become.
In the embodiment shown in FIGS. 8 and 9, the riser (12) is bent horizontally at the lower part to form a horizontal nitrogen-removing material-filled layer (2).
And has a large contact area.

【0027】図10及び図11は本発明の他の態様を示
す断面図であり、被処理水は透水性固体壁(11)から
流入し、内部の窒素除去材料充填層(2)を通過して又
は次いでロックウール層(13)を通過して、複数の穴
が空いた上昇管(12)の穴部分に入り込んだ後、気体
吹き込み装置(6)により上昇して、処理水(5)とな
る。図10及び図11に示す実施態様では窒素除去材料
充填層(2)で接続した上昇管が2つある例である。上
昇管を2つ以上設けることにより、水の循環量を増や
し、処理能力を向上することができる。
FIGS. 10 and 11 are cross-sectional views showing another embodiment of the present invention. The water to be treated flows from the water-permeable solid wall (11) and passes through the nitrogen-removing material-filled layer (2) inside. After passing through the rock wool layer (13) and entering the hole portion of the riser pipe (12) having a plurality of holes, the riser pipe (6) rises by the gas blowing device (6) to form the treated water (5). Become. The embodiment shown in FIGS. 10 and 11 is an example in which there are two risers connected by a nitrogen-removing-material-filled layer (2). By providing two or more risers, the amount of circulating water can be increased and the processing capacity can be improved.

【0028】図4〜図11に示す態様においても装置へ
の処理水の引水原理や管の上部構造についても図2や図
3に示す形状が採用され得る。また、図1の装置で説明
したような各種の変形が可能である。上記各図に示した
ように本発明の装置は、各種の態様が可能である。例え
ば、横型タイプや縦型タイプの他、上昇管を2以上有す
るタイプ、透水性固体壁を有しないタイプ、下層濾過板
を有しないタイプなど多数ある。本発明の装置を使用し
て被処理水を処理する方法には格別制限はないが、被処
理水とは別の水槽で処理する方法、被処理水のある水槽
や池等に配置し直接処理する方法などがある。
In the embodiments shown in FIGS. 4 to 11, the principle shown in FIGS. 2 and 3 can be adopted for the principle of drawing treated water into the apparatus and the upper structure of the pipe. Further, various modifications as described in the apparatus of FIG. 1 are possible. As shown in the above figures, the device of the present invention can be in various modes. For example, there are many types such as a horizontal type and a vertical type, a type having two or more risers, a type having no permeable solid wall, and a type not having a lower filter plate. There is no particular limitation on the method of treating the water to be treated using the apparatus of the present invention, but a method of treating the water in a water tank separate from the water to be treated, a method of directly disposing the water in a water tank or pond having the water to be treated, There are ways to do that.

【0029】[0029]

【実施例】本発明の実施例を以下に説明する。 実施例1 60cm×30cm×30cmの海水貯槽水槽を2つ用
意し、それぞれに50Lの海水を入れて、図1及び図4
の形状の硝酸性窒素体処理装置を設置した。装置は下層
濾過板はニッソー製のバイオフィルター60を使用し、
5〜20mm範囲である不定形状の硫黄50重量部と炭
酸カルシウム50重量部からなる溶融混合窒素除去材料
粒1kgからなる窒素除去材料充填槽と、新日化ロック
ウール株式会社製の7m厚みのロックウールシートを使
用した。なお、気泡発生機はニッソー製のシーター12
00を使用した。また、海水はすべて閉鎖系で循環して
いる。処理槽の温度は30℃設定とした。この海水貯槽
に大塚化学製のOK−F−2を硝酸性窒素濃度100m
g/Lとなるように投入して、硝酸性窒素濃度の経時変
化を調べた。これより、硝酸性窒素体の良好な除去状況
が把握できる。硝酸性窒素(NO3)の濃度変化(mg/
L)を表1に示す。
Embodiments of the present invention will be described below. Example 1 Two 60 cm × 30 cm × 30 cm seawater storage tanks were prepared, and 50 L of seawater was added to each tank.
Was installed. The device uses a biofilter 60 made of Nissor for the lower filter plate,
A nitrogen-removing material filling tank composed of 1 kg of molten mixed nitrogen-removing material particles comprising 50 parts by weight of irregularly shaped sulfur and 50 parts by weight of calcium carbonate having a range of 5 to 20 mm, and a lock having a thickness of 7 m made by Shin Nikka Rockwool Co. Wool sheets were used. The bubble generator is a Nisso sheeter 12.
00 was used. All seawater is circulating in a closed system. The temperature of the processing tank was set at 30 ° C. In this seawater storage tank, OK-F-2 manufactured by Otsuka Chemical Co.
g / L, and the change with time of the nitrate nitrogen concentration was examined. From this, it is possible to grasp a favorable removal state of the nitrate nitrogen body. Nitrate nitrogen (NO 3 ) concentration change (mg /
L) is shown in Table 1.

【0030】[0030]

【表1】 [Table 1]

【0031】実施例2 実施例1と同じ形状の水槽を3つ準備し、同じく50L
の海水を入れて、図5、図6および図7の形状の硝酸性
窒素体処理装置を設置した。図5に順ずる装置では、ア
クリル製の10cm×10cm×高さ25cmの容器を
使用して、その中に5〜20mm範囲である不定形状の
硫黄50重量部と炭酸カルシウム50重量部からなる溶
融混合窒素除去材料粒1kgからなる窒素除去材料を充
填し、管としてVU13の塩ビ管を使用した。一方、図
6および図7に順ずる装置では、新日化ロックウール株
式会社製の7m厚みのロックウールシートを使用し、5
〜20mm範囲である不定形状の硫黄50重量部と炭酸
カルシウム50重量部からなる溶融混合窒素除去材料粒
1kgからなる窒素除去材料を充填した。なお、気泡発
生機は、ニッソー製のシーター1200を使用した。ま
た、海水はすべて閉鎖系で循環している。処理槽の温度
は30℃設定とした。この海水貯槽に大塚化学製のOK
−F−2を硝酸性窒素濃度200mg/Lとなるように
投入して、硝酸性窒素濃度の経時変化を調べたこれよ
り、硝酸性窒素体の良好な除去状況が把握できる。硝酸
性窒素体(NO3)濃度変化(mg/L)を表2に示す。
Example 2 Three water tanks having the same shape as in Example 1 were prepared, and 50 L
, And a nitrate nitrogen treatment apparatus having the shape shown in FIGS. 5, 6 and 7 was installed. In the apparatus according to FIG. 5, a 10 cm × 10 cm × 25 cm height container made of acryl is used, and 50 parts by weight of irregular shaped sulfur and 50 parts by weight of calcium carbonate having a range of 5 to 20 mm are contained therein. A nitrogen removing material consisting of 1 kg of the mixed nitrogen removing material particles was filled, and a VU13 PVC pipe was used as a pipe. On the other hand, in the apparatus according to FIGS. 6 and 7, a 7 m-thick rock wool sheet manufactured by Shin Nikka Rock Wool Co., Ltd. is used.
A nitrogen-removing material consisting of 1 kg of molten mixed nitrogen-removing material particles consisting of 50 parts by weight of irregularly shaped sulfur and 50 parts by weight of calcium carbonate having a range of about 20 mm was filled. In addition, a sheeter 1200 manufactured by Nisso was used as the bubble generator. All seawater is circulating in a closed system. The temperature of the processing tank was set at 30 ° C. In this seawater storage tank, OK
-F-2 was charged so as to have a nitrate nitrogen concentration of 200 mg / L, and the change with time of the nitrate nitrogen concentration was examined. From this, it is possible to grasp a favorable removal state of the nitrate nitrogen body. Table 2 shows the change in the concentration of nitrate nitrogen (NO 3 ) (mg / L).

【0032】[0032]

【表2】 [Table 2]

【0033】[0033]

【発明の効果】本発明によれば、通常、大規模且つ多大
な費用を必要とする水槽や海水中の硝酸性窒素処理問題
に対して、簡便且つ低コスト、効率的な硝酸性窒素処理
を実現できる。発明の効果は顕著である。
According to the present invention, a simple, low-cost, and efficient nitrate nitrogen treatment can be effectively applied to the problem of treating a large-scale and large-cost nitrate nitrogen in a tank or seawater. realizable. The effect of the invention is remarkable.

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

【図1】 本発明の処理装置の断面図FIG. 1 is a sectional view of a processing apparatus of the present invention.

【図2】 上昇管の説明図FIG. 2 is an explanatory view of a riser.

【図3】 他の上昇管の説明図FIG. 3 is an explanatory view of another riser pipe.

【図4】 本発明の他の処理装置の断面図FIG. 4 is a sectional view of another processing apparatus of the present invention.

【図5】 本発明の他の処理装置の断面図FIG. 5 is a sectional view of another processing apparatus of the present invention.

【図6】 本発明の他の処理装置の断面図FIG. 6 is a sectional view of another processing apparatus of the present invention.

【図7】 本発明の他の処理装置の断面図FIG. 7 is a sectional view of another processing apparatus of the present invention.

【図8】 本発明の他の処理装置の断面図FIG. 8 is a sectional view of another processing apparatus of the present invention.

【図9】 本発明の他の処理装置の断面図FIG. 9 is a sectional view of another processing apparatus of the present invention.

【図10】 本発明の他の処理装置の断面図FIG. 10 is a sectional view of another processing apparatus of the present invention.

【図11】 本発明の他の処理装置の断面図FIG. 11 is a sectional view of another processing apparatus of the present invention.

【符号の説明】[Explanation of symbols]

1:透水性固体壁 2:硝酸性窒素除去材料層 3:濾過板 4:上昇管 6:気体吹き込み装置 1: Permeable solid wall 2: Nitrate nitrogen removal material layer 3: Filter plate 4: Up pipe 6: Gas blowing device

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) B01D 35/027 C02F 1/58 T C02F 1/58 3/28 A 3/28 B01D 35/02 C G ──────────────────────────────────────────────────の Continued on the front page (51) Int.Cl. 7 Identification code FI Theme coat ゛ (Reference) B01D 35/027 C02F 1/58 T C02F 1/58 3/28 A 3/28 B01D 35/02 CG

Claims (6)

【特許請求の範囲】[Claims] 【請求項1】 水槽内の被処理水等の閉鎖系において、
水流発生部材を備え、該水流発生部材によって形成され
た水流経路の途中に、硫黄と炭酸カルシウム系成分から
なる硝酸性窒素除去材料層を設けたことを特徴とする硝
酸性窒素の処理装置。
In a closed system such as water to be treated in a water tank,
An apparatus for treating nitrate nitrogen, comprising a water flow generation member, and a nitrate nitrogen removal material layer comprising sulfur and calcium carbonate-based components provided in the middle of a water flow path formed by the water flow generation member.
【請求項2】 前記硝酸性窒素除去材料層の周囲に、透
水性素材からなる溶存酸素低下部材を配置したことを特
徴とする請求項1記載の硝酸性窒素の処理装置。
2. The apparatus for treating nitrate nitrogen according to claim 1, wherein a dissolved oxygen reducing member made of a water-permeable material is arranged around the nitrate nitrogen removal material layer.
【請求項3】 前記硝酸性窒素除去材料層の上流側に、
ろ過部材を設けてなる請求項1記載の硝酸性窒素の処理
装置。
3. An upstream side of the nitrate nitrogen removing material layer,
The apparatus for treating nitrate nitrogen according to claim 1, further comprising a filtration member.
【請求項4】 前記溶存酸素低下部材が、サンゴ砂又は
ロックウールからなる多孔質材料である請求項1記載の
硝酸性窒素の処理装置。
4. The apparatus for treating nitrate nitrogen according to claim 1, wherein the dissolved oxygen reducing member is a porous material made of coral sand or rock wool.
【請求項5】 水槽内の被処理水等の閉鎖系において、
水流発生部材より循環水流を形成させることにより、水
槽中の水を、硫黄と炭酸カルシウム系成分からなる硝酸
性窒素除去材料層を通過させた後、再び水槽中に放出、
循環することを特徴とする硝酸性窒素の処理方法。
5. In a closed system such as water to be treated in a water tank,
By forming a circulating water flow from the water flow generating member, the water in the water tank is allowed to pass through the nitrate nitrogen removing material layer composed of sulfur and calcium carbonate-based components, and then discharged again into the water tank,
A method for treating nitrate nitrogen, comprising circulating.
【請求項6】 大型水槽又は湖沼等の水を上記水槽中に
導入し、上記水槽中の水又は処理水の少なくとも一部を
大型水槽又は湖沼等に戻す請求項5記載の硝酸性窒素の
処理方法。
6. The nitrate nitrogen treatment according to claim 5, wherein water from a large water tank or a lake is introduced into the water tank, and at least a part of the water or the treated water in the water tank is returned to the large water tank or the lake. Method.
JP2001178976A 2001-06-13 2001-06-13 Nitrate nitrogen treatment apparatus and treatment method Expired - Fee Related JP4772216B2 (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006015320A (en) * 2004-06-01 2006-01-19 Nippon Steel Chem Co Ltd Nitrate nitrogen treatment material and wastewater treatment method
US7276164B2 (en) 2004-10-07 2007-10-02 Exxonmobil Research And Engineering Company Nitrate removal in a purge stream using constructed wetlands

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0295498A (en) * 1988-09-30 1990-04-06 Nikko Eng Kk Method and apparatus for treating water
JPH0564531A (en) * 1991-09-05 1993-03-19 Hatanaka Masanobu Water-tank apparatus for ornamentation
JPH0947611A (en) * 1995-08-07 1997-02-18 Horimizu Seisakusho:Kk Filter in water
JPH11285377A (en) * 1998-04-02 1999-10-19 Hiroshi Masujima Composition provided with microbial activity, and its production
JP2000093997A (en) * 1998-09-25 2000-04-04 Nitchitsu Co Ltd Nitrate nitrogen denitrifying substrate
JP2001104993A (en) * 1999-10-01 2001-04-17 Nitchitsu Co Ltd Nitrate nitrogen denitrifying composition and production thereof

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0295498A (en) * 1988-09-30 1990-04-06 Nikko Eng Kk Method and apparatus for treating water
JPH0564531A (en) * 1991-09-05 1993-03-19 Hatanaka Masanobu Water-tank apparatus for ornamentation
JPH0947611A (en) * 1995-08-07 1997-02-18 Horimizu Seisakusho:Kk Filter in water
JPH11285377A (en) * 1998-04-02 1999-10-19 Hiroshi Masujima Composition provided with microbial activity, and its production
JP2000093997A (en) * 1998-09-25 2000-04-04 Nitchitsu Co Ltd Nitrate nitrogen denitrifying substrate
JP2001104993A (en) * 1999-10-01 2001-04-17 Nitchitsu Co Ltd Nitrate nitrogen denitrifying composition and production thereof

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006015320A (en) * 2004-06-01 2006-01-19 Nippon Steel Chem Co Ltd Nitrate nitrogen treatment material and wastewater treatment method
JP4602025B2 (en) * 2004-06-01 2010-12-22 新日鐵化学株式会社 Nitrate nitrogen treatment material and waste water treatment method
US7276164B2 (en) 2004-10-07 2007-10-02 Exxonmobil Research And Engineering Company Nitrate removal in a purge stream using constructed wetlands

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