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JPH10323694A - Method for removing nitrogen in water containing nitrate and denitrification bioreactor - Google Patents

Method for removing nitrogen in water containing nitrate and denitrification bioreactor

Info

Publication number
JPH10323694A
JPH10323694A JP9150049A JP15004997A JPH10323694A JP H10323694 A JPH10323694 A JP H10323694A JP 9150049 A JP9150049 A JP 9150049A JP 15004997 A JP15004997 A JP 15004997A JP H10323694 A JPH10323694 A JP H10323694A
Authority
JP
Japan
Prior art keywords
membrane
nitrate
denitrification
hydrogen donor
containing water
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
JP9150049A
Other languages
Japanese (ja)
Inventor
Toshiko Hashimoto
敏子 橋本
Hirobumi Izawa
博文 井澤
Hiroshi Okamoto
拓 岡本
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.)
Hiroshima Prefecture
Original Assignee
Hiroshima Prefecture
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 Hiroshima Prefecture filed Critical Hiroshima Prefecture
Priority to JP9150049A priority Critical patent/JPH10323694A/en
Publication of JPH10323694A publication Critical patent/JPH10323694A/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

  • Biological Treatment Of Waste Water (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)
  • Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)

Abstract

PROBLEM TO BE SOLVED: To solve operational problems and enable nitrogen removal performance to be improved by conducting nitrogen removal (membrane separation nitrogen removal) at a level of a single body apparatus by using a membrane container in which hydrogen donors are enclosed as a nitrogen removal bioreactor of a cartridge-type. SOLUTION: Water containing nitrate and methanol 2 provided from the outside are membrane-separated in the water containing nitrate. The methanol 2 is allowed to permeate through a membrane 11 to activate a denitrification reaction on a biofilm generated on the surface of the membrane 11. A nitrogen removal bioreactor X includes a membrane container 1 made by forming a polyethylene membrane material 11 into a bag or a tube and in which the methanol 2 is enclosed. The methanol 2 can be supplied from the outside. The nitrogen removal bioreactor X is provided as a cartridge able to be used repeatedly as a single body.

Description

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

【0001】[0001]

【本発明の属する技術分野】本発明は、バイオリアクタ
ーによる硝酸塩含有水中の窒素除去方法及び脱窒バイオ
リアクターに関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for removing nitrogen from nitrate-containing water by a bioreactor and a denitrification bioreactor.

【0002】[0002]

【従来の技術】従来より、富栄養化による水質汚濁が進
行している水域の水質改善において、汚濁原因の一つと
なっている生活排水や工場排水中の含有硝酸塩(硝酸性
窒素)を脱窒素菌(Hyphomicrobium) により生物化学的
に窒素ガスに還元する脱窒バイオリアクターが知られて
いる。〔硝化脱窒方法〕
2. Description of the Related Art Conventionally, in the improvement of water quality in a water area in which water pollution is progressing due to eutrophication, nitrate (nitrate nitrogen) contained in domestic wastewater or industrial wastewater, which is one of the causes of pollution, is denitrified. A denitrification bioreactor that biochemically reduces nitrogen gas by bacteria (Hyphomicrobium) is known. (Nitrification and denitrification method)

【0003】従来方法は、図4(a)に示すように、同
一液相内に水素供与体(有機炭素化合物)を投入するも
の〔混合脱窒〕であり、脱窒後この有機炭素化合物を別
途除去する処理が必要であった。この場合、清澄な(有
機炭素濃度が低い)水であっても一旦有機炭素化合物を
添加し、脱窒素菌を繁殖させて、脱窒をおこない、その
後に有機炭素化合物を別途除去処理することになる。
In the conventional method, as shown in FIG. 4 (a), a hydrogen donor (organic carbon compound) is charged into the same liquid phase (mixed denitrification). A separate removal process was required. In this case, even in clear (low organic carbon concentration) water, an organic carbon compound is once added, a denitrifying bacterium is propagated, denitrification is performed, and then the organic carbon compound is separately removed. Become.

【0004】こうした栄養塩除去機能をもたせた生物学
的処理方法〔硝化脱窒方法〕は、水質浄化対策におい
て、環境水に対して直接おこなうよりも発生源レベルで
おこなうほうが費用対効果が大きいという有利性があ
り、こでまでに装置開発もなされてきた。
[0004] Biological treatment methods (nitrification and denitrification method) having such a nutrient removal function are more cost-effective to perform at the source level than directly to environmental water in water purification measures. It has advantages, and the device has been developed so far.

【0005】[0005]

【発明が解決しようとする課題】しかしながら、装置全
体として運用上の転換を図らなければならず、結果的に
既設装置や既存施設に適用できない場合が多く、これら
のところでは栄養塩の負荷削減対策が遅滞することを余
儀無くされているという問題があった。
However, the operation of the entire apparatus must be changed, and as a result, it cannot be applied to existing equipment and existing facilities in many cases. Had to be delayed.

【0006】本発明はこのような事情に鑑みなされたも
のであって、水素供与体を封入した膜体容器をカートリ
ッジ型の脱窒バイオリアクターとして使用することによ
り、脱窒〔膜分離脱窒〕を単体装置レベルで進行させ、
運用上の問題を解消するとともに脱窒性能を向上可能な
硝酸塩含有水中の窒素除去方法及び脱窒バイオリアクタ
ーを提供するものである。
SUMMARY OF THE INVENTION The present invention has been made in view of the above-mentioned circumstances, and uses a membrane container enclosing a hydrogen donor as a cartridge-type denitrification bioreactor to denitrify (membrane separation denitrification). At the single device level,
An object of the present invention is to provide a method for removing nitrogen from nitrate-containing water and a denitrification bioreactor capable of solving operational problems and improving denitrification performance.

【0007】[0007]

【課題を解決するための手段】課題を解決するために本
発明は、単体の脱窒バイオリアクターによる硝酸塩含有
水中の窒素除去方法であって、硝酸塩含有水中で、該硝
酸塩含有水と外部投入される水素供与体とを膜分離し、
かつ、該膜を介して水素供与体を透過させ、膜表面に生
成する生物膜での脱窒反応を活性化することを特徴とす
るものである。
SUMMARY OF THE INVENTION In order to solve the problems, the present invention is a method for removing nitrogen from nitrate-containing water by a single denitrification bioreactor. Membrane separation from the hydrogen donor
In addition, the present invention is characterized in that a hydrogen donor is permeated through the membrane to activate a denitrification reaction in a biofilm formed on the membrane surface.

【0008】また、脱窒バイオリアクターであって、硝
酸塩含有水中で閉区画を形成し、記閉区画に水素供与体
を封入するとともに、少なくとも1区画壁を水素供与体
透過膜により構成した膜体容器からなり、該膜体容器を
単体で反復使用可能にカートリッジ化したことを特徴と
するものである。
A denitrification bioreactor, wherein a closed compartment is formed in nitrate-containing water, a hydrogen donor is sealed in the closed compartment, and at least one partition wall is constituted by a hydrogen donor permeable membrane. The membrane container is made into a cartridge which can be used repeatedly by itself.

【0009】[0009]

【発明の実施の形態】本発明の実施の形態は、上記構成
における水素供与体がメタノールであり、水素供与体透
過膜がポリエチレン膜であり、ポリエチレン製の膜素材
を袋状又はチューブ状に形成した膜体容器にメタノール
を封入し、カートリッジ型の脱窒バイオリアクターを構
成している。
DESCRIPTION OF THE PREFERRED EMBODIMENTS In the embodiment of the present invention, the hydrogen donor in the above structure is methanol, the hydrogen donor permeable membrane is a polyethylene membrane, and a polyethylene membrane material is formed in a bag or a tube. Methanol is sealed in the membrane container thus formed to constitute a cartridge type denitrification bioreactor.

【0010】上記構成の脱窒バイオリアクターの機能
は、容器内部のメタノールが膜を透過し表面に達した時
点で脱窒素菌に取り込まれて硝酸性窒素を還元し窒素ガ
スとして気散させる。このため、膜表面に脱窒素菌が高
密度に固定化された生物膜が生成し、ここでの脱窒反応
が活性化される。〔膜分離脱窒〕
The function of the denitrification bioreactor having the above structure is that when the methanol inside the container permeates the membrane and reaches the surface, it is taken in by the denitrifying bacterium to reduce nitrate nitrogen and diffuse it as nitrogen gas. For this reason, a biofilm in which the denitrifying bacteria are immobilized at a high density is generated on the membrane surface, and the denitrification reaction is activated here. (Membrane separation denitrification)

【0011】また、上記構成の脱窒バイオリアクターは
単体構成であることから必要箇所での脱窒を単体装置レ
ベルで進行させることができる。
Further, since the denitrification bioreactor having the above configuration is a single unit, denitrification at a required place can be advanced at a single unit level.

【0012】したがって、既設の浄化槽にも付設するこ
とができ、カートリッジ型であることから反復使用がで
きる。
Therefore, it can be attached to an existing septic tank, and since it is a cartridge type, it can be used repeatedly.

【0013】[0013]

【実施例】本発明の実施例について添付図面を参照して
以下説明する。
Embodiments of the present invention will be described below with reference to the accompanying drawings.

【0013】図1は本発明方法〔膜分離脱窒〕を模式的
に示す説明図である。
FIG. 1 is an explanatory view schematically showing the method (membrane separation and denitrification) of the present invention.

【0014】図2は本発明の脱窒バイオリアクターの構
成概要図である。
FIG. 2 is a schematic diagram showing the structure of the denitrification bioreactor of the present invention.

【0015】図示するように、脱窒バイオリアクター
(X)は、ポリエチレン製の膜素材(11)を袋状又はチ
ューブ状に形成した膜体容器(1)にメタノール(2)
を封入したものである。この場合、容器(1)内に網を
入れ、容器の保形とメタノール(2)の浮揚偏在の抑制
を図っている。なお、図中のチューブは外部からメタノ
ール(2)を補充するためのものであり、コックは封止
(栓止)用であり、シャックルは重り又は槽底掛止用で
ある。
As shown in the figure, a denitrification bioreactor (X) comprises a membrane container (1) in which a polyethylene membrane material (11) is formed in a bag shape or a tube shape.
Is enclosed. In this case, a net is put in the container (1) to maintain the shape of the container and to suppress the floating and uneven distribution of the methanol (2). The tube in the figure is for externally replenishing methanol (2), the cock is for sealing (plugging), and the shackle is for weight or for hanging the bottom of the tank.

【0016】したがって、脱窒バイオリアクター(X)
をカートリッジ化できる。
Therefore, the denitrification bioreactor (X)
Can be made into a cartridge.

【0017】そして、この脱窒バイオリアクター(X)
を硝酸塩含有水中に設置することにより、硝酸塩含有水
とメタノールとを膜分離し、かつ、該膜を介してメタノ
ールを透過させ、膜表面に膜表面に脱窒素菌を高密度に
固定化して生物膜を生成し、脱窒反応を活性化すること
ができる。
The denitrification bioreactor (X)
Is placed in the nitrate-containing water to separate the membrane from the nitrate-containing water and methanol, and to permeate the methanol through the membrane. A film can be formed to activate the denitrification reaction.

【0018】ここで、実験的事実に基づく本発明の作用
効果について以下結論のみを述べる。
Here, only the following conclusions will be made regarding the operation and effect of the present invention based on experimental facts.

【0019】脱窒はほぼ膜面のみでおこなわれる。 脱窒速度はメタノールのポリエチレン膜透過特性に依
存する。( いずれも温度依存)
The denitrification is performed almost only on the film surface. The denitrification rate depends on the characteristics of methanol permeation through the polyethylene membrane. (Both temperature dependent)

【0020】また、図3に脱窒バイオリアクターを既設
の実浄化槽(例えばし尿浄化槽)に適用した例を示す。
図示するように、脱窒バイオリアクター(X)は沈澱槽
に設置される。
FIG. 3 shows an example in which the denitrification bioreactor is applied to an existing actual septic tank (eg, human waste septic tank).
As shown, the denitrification bioreactor (X) is installed in a settling tank.

【0021】なお、図4は(a)従来方法〔混合脱窒〕
と(b)本発明方法〔膜分離脱窒〕との特徴の相違を模
式的に示す比較説明図である。
FIG. 4 (a) shows a conventional method (mixed denitrification).
And (b) is a comparative explanatory view schematically showing the difference between the features of the method of the present invention (membrane separation and denitrification).

【0022】[0022]

【発明の効果】本発明は以上の構成よりなるものであ
り、これによれば脱窒バイオリアクター単体で脱窒機能
を発現できるので、必要の都度、任意の場所に設置する
ことで効率的に窒素除去を図ることができる。
According to the present invention, the denitrification bioreactor alone can exhibit the denitrification function according to the above constitution, so that it can be efficiently installed at any place whenever necessary Nitrogen can be removed.

【0023】したがって、浄化槽による排水処理だけで
なく河川水や地下水に対する浄化システムの一端を担う
構成要素として適用範囲が拡大できる。
Therefore, the range of application can be expanded as a component that plays a part in a purification system for river water and groundwater as well as wastewater treatment by a septic tank.

【0024】また、従来的な用地の確保や脱窒槽の建設
などの設備投資が不要となり、装置の製造コストも廉価
であるので、初期投資(設置コスト)の低減等多大な経
済効果を奏することが期待できる。しかも、設置後はそ
のまま放置するだけでよく、維持管理が省力化できる。
In addition, capital investment such as conventional securing of land and construction of a denitrification tank is not required, and the manufacturing cost of the apparatus is low, so that a great economic effect such as a reduction in initial investment (installation cost) can be achieved. Can be expected. In addition, it is only necessary to leave the apparatus as it is after installation, so that maintenance can be saved.

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

【図1】本発明方法〔膜分離脱窒〕を模式的に示す説明
図である。
FIG. 1 is an explanatory view schematically showing a method of the present invention (membrane separation and denitrification).

【図2】脱窒バイオリアクターの構成概要図である。FIG. 2 is a schematic structural diagram of a denitrification bioreactor.

【図3】脱窒バイオリアクターを既設の実浄化槽に適用
した例を示す説明図である。
FIG. 3 is an explanatory diagram showing an example in which a denitrification bioreactor is applied to an existing actual septic tank.

【図4】(a)従来方法〔混合脱窒〕と(b)本発明方
法〔膜分離脱窒〕との相違を模式的に示す比較説明図で
ある。
FIG. 4 is a comparative explanatory diagram schematically showing the difference between (a) the conventional method (mixed denitrification) and (b) the method of the present invention (membrane separation and denitrification).

【符号の説明】[Explanation of symbols]

1 膜体容器 11 ポリエチレン膜 2 メタノール X 脱窒バイオリアクター 1 Membrane container 11 Polyethylene membrane 2 Methanol X Denitrification bioreactor

───────────────────────────────────────────────────── 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 (5)

【特許請求の範囲】[Claims] 【請求項1】 バイオリアクターによる硝酸塩含有水中
の窒素除去方法において、硝酸塩含有水中で、該硝酸塩
含有水と外部投入される水素供与体とを膜分離し、か
つ、該膜を介して水素供与体を透過させ、膜表面に生成
する生物膜での脱窒反応を活性化することを特徴とする
硝酸塩含有水中の窒素除去方法。
In a method for removing nitrogen from nitrate-containing water by a bioreactor, the nitrate-containing water is separated from the externally supplied hydrogen donor by membrane in the nitrate-containing water, and the hydrogen donor is passed through the membrane. A method for removing nitrogen from nitrate-containing water, wherein the nitrogen is permeated to activate a denitrification reaction in a biofilm formed on the membrane surface.
【請求項2】 水素供与体が有機炭素化合物であり、膜
が樹脂製の水素供与体透過膜である請求項1記載の硝酸
塩含有水中の窒素除去方法。
2. The method for removing nitrogen from nitrate-containing water according to claim 1, wherein the hydrogen donor is an organic carbon compound, and the membrane is a resin-made hydrogen donor permeable membrane.
【請求項3】 有機炭素化合物がメタノールであり、樹
脂製の水素供与体透過膜がポリエチレン膜である請求項
2記載の硝酸塩含有水中の窒素除去方法。
3. The method for removing nitrogen from nitrate-containing water according to claim 2, wherein the organic carbon compound is methanol and the resin-made hydrogen donor permeable membrane is a polyethylene membrane.
【請求項4】 硝酸塩含有水中で、該硝酸塩含有水と外
部投入される水素供与体とを膜分離し、かつ、該膜を介
して水素供与体を透過させ、膜表面に生成する生物膜で
の脱窒反応を活性化するための脱窒バイオリアクターで
あって、硝酸塩含有水中で閉区画を形成し、該閉区画に
水素供与体を封入するとともに、少なくとも1区画壁を
水素供与体透過膜により構成した膜体容器からなり、該
膜体容器を単体で反復使用可能なカートリッジとしたこ
とを特徴とする脱窒バイオリアクター。
4. A biofilm formed on the surface of a membrane by separating the nitrate-containing water and an externally supplied hydrogen donor by membrane in the nitrate-containing water and allowing the hydrogen donor to pass through the membrane. A denitrification bioreactor for activating a denitrification reaction of a gas, comprising forming a closed compartment in nitrate-containing water, enclosing a hydrogen donor in the closed compartment, and forming at least one compartment wall with a hydrogen donor permeable membrane. A denitrification bioreactor comprising a membrane container constituted by the above (1), wherein the membrane container is a cartridge that can be repeatedly used alone.
【請求項5】 水素供与体がメタノールであり、水素供
与体透過膜がポリエチレン膜であり、膜体容器が前記ポ
リエチレン製の膜素材を袋状又はチューブ状に形成し前
記メタノールを封入してなるものである請求項4記載の
脱窒バイオリアクター。
5. A hydrogen donor is methanol, a hydrogen donor permeable membrane is a polyethylene membrane, and a membrane container is formed by forming the polyethylene membrane material into a bag or a tube and enclosing the methanol. 5. The denitrification bioreactor according to claim 4, wherein
JP9150049A 1997-05-23 1997-05-23 Method for removing nitrogen in water containing nitrate and denitrification bioreactor Pending JPH10323694A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9150049A JPH10323694A (en) 1997-05-23 1997-05-23 Method for removing nitrogen in water containing nitrate and denitrification bioreactor

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9150049A JPH10323694A (en) 1997-05-23 1997-05-23 Method for removing nitrogen in water containing nitrate and denitrification bioreactor

Publications (1)

Publication Number Publication Date
JPH10323694A true JPH10323694A (en) 1998-12-08

Family

ID=15488393

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
JP (1) JPH10323694A (en)

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WO2000066502A1 (en) * 1999-04-30 2000-11-09 Dautais Jean Pierre Active purifying structures for lining and forming compact physico-biological filters
WO2003033420A1 (en) * 2001-10-12 2003-04-24 Eiwa Country Environment Co., Ltd. Soil water purifier
JP2007289912A (en) * 2006-03-30 2007-11-08 Central Res Inst Of Electric Power Ind Treatment method of wastewater containing selenate compound by microorganisms
JP2008012461A (en) * 2006-07-07 2008-01-24 Central Res Inst Of Electric Power Ind Method for treating liquid containing selenate compound using microorganisms
JP2008023488A (en) * 2006-07-24 2008-02-07 Central Res Inst Of Electric Power Ind Method and apparatus for supplying electron donor to microorganism and bioreactor using the same
JP2008149233A (en) * 2006-12-15 2008-07-03 Central Res Inst Of Electric Power Ind Deoxygenation method and apparatus
JP2008246269A (en) * 2006-07-24 2008-10-16 Central Res Inst Of Electric Power Ind Soil purification method
US7575686B2 (en) 2005-12-23 2009-08-18 University Of Massachusetts Process for autotrophic perchlorate reduction using elemental sulfur and mollusk shells
JP2011005380A (en) * 2009-06-24 2011-01-13 Central Res Inst Of Electric Power Ind Device for supplying electron donor to microorganism and method of using the device
JP2013039571A (en) * 2005-06-15 2013-02-28 Central Research Institute Of Electric Power Industry Method of supplying microorganism activity control substance, apparatus therefor, and method of cleaning environment and bioreactor using the same
JP2013121595A (en) * 2013-02-12 2013-06-20 Central Research Institute Of Electric Power Industry Device for supplying electron donor to microorganism and method of using the device
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Citations (3)

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