JPH07204685A - Tertiary treatment apparatus for drainage - Google Patents

Tertiary treatment apparatus for drainage

Info

Publication number
JPH07204685A
JPH07204685A JP6005994A JP599494A JPH07204685A JP H07204685 A JPH07204685 A JP H07204685A JP 6005994 A JP6005994 A JP 6005994A JP 599494 A JP599494 A JP 599494A JP H07204685 A JPH07204685 A JP H07204685A
Authority
JP
Japan
Prior art keywords
water
denitrification
filter medium
tank
treated 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
JP6005994A
Other languages
Japanese (ja)
Inventor
Shigekazu Kurata
繁和 倉田
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.)
NAGANO EKIKA KK
Original Assignee
NAGANO EKIKA KK
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 NAGANO EKIKA KK filed Critical NAGANO EKIKA KK
Priority to JP6005994A priority Critical patent/JPH07204685A/en
Publication of JPH07204685A publication Critical patent/JPH07204685A/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)
  • Removal Of Specific Substances (AREA)
  • Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)

Abstract

PURPOSE:To conduct denitrification and dephosphorization of drainage at high yields without remodeling an existing purification apparatus. CONSTITUTION:An impeller 4 is installed on the water surface in the denitrification vessel 1 of an apparatus main body A, and the impeller 4 is rotated by treated water discharged from a purification apparatus B. A lot of magnet grains 5 are fixed on the surface of the impeller 4; denitrification bacteria activated by the magnetic force of the magnet grains are exposed alternately to the hydrosphere and the atmosphere so that the colonies of the bacteria grow in a favorable environment to obtain efficient denitrification function. The iron components in water to be treated which is sent from a denitrification vessel 2 to a dephosphorization vessel 3 are attracted by the magnet grains fixed on the surface of a cylindrical filter medium 7 set in the dephosphorization vessel 3; phosphorus, which is apt to adhere to the iron components, is positively removed by being attracted by the magnet grains with the iron components.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、浄化装置で一次処理、
二次処理された処理水を、更に三次処理して高い栄養塩
類(窒素及びリン)除去率を得る排水三次処理装置に関
する。
BACKGROUND OF THE INVENTION The present invention relates to a primary treatment in a purifying device,
The present invention relates to a waste water tertiary treatment device that obtains a high nutrient salt (nitrogen and phosphorus) removal rate by subjecting the treated water that has been subjected to the secondary treatment to a third treatment.

【0002】[0002]

【従来の技術】一般的に、排水中に含まれている有機汚
濁物の大部分は、浄化装置で沈澱分離(一次処理)、及
び生物処理(二次処理)されて除去される。また、有機
性窒素の大部分が硝化され、更には嫌気性処理と好気性
処理を繰返すことにより脱窒されると共に、リンも余剰
汚泥と共に抜き出して、清澄化された処理水が公共用水
域に放出される。
2. Description of the Related Art Generally, most of organic pollutants contained in waste water are removed by sedimentation (primary treatment) and biological treatment (secondary treatment) in a purification device. In addition, most of the organic nitrogen is nitrified and further denitrified by repeating anaerobic treatment and aerobic treatment, and phosphorus is also extracted together with excess sludge, and the clarified treated water is placed in public water areas. Is released.

【0003】[0003]

【発明が解決しようとする課題】ところで、排水中に含
まれている栄養塩類(窒素及びリン)による富栄養化の
限界濃度は極めて低く、湖沼、内湾、内海等の閉鎖性水
域では、放出される二次処理水に含まれている微量の栄
養塩類の影響でプランクトンの過剰繁殖を惹起する等、
水質悪化に結びつく様々な弊害が生じ得る。
By the way, the critical concentration of eutrophication by nutrient salts (nitrogen and phosphorus) contained in wastewater is extremely low, and it is released in closed water areas such as lakes, inner bays and inland seas. Inducing overgrowth of plankton due to the effect of trace amounts of nutrients contained in the secondary treated water
Various adverse effects that lead to deterioration of water quality can occur.

【0004】従って、これらの弊害を防止するために
は、排水中から栄養塩類を完全に除去した後に、公共用
水域へ放出することが望ましいが、一次処理、二次処理
で完全に除去するためには、大規模な浄化槽を装備しな
ければならず、コスト高となり実現性に乏しい。
Therefore, in order to prevent these adverse effects, it is desirable to completely remove the nutrient salts from the wastewater and then release them into the public water area, but in order to completely remove them by the primary treatment and the secondary treatment. Must be equipped with a large-scale septic tank, resulting in high costs and poor feasibility.

【0005】また、既存の浄化槽で対処するには改修工
事が必要となり、その間の処理浄化に支障を来すため迅
速に対応することができない。
Further, repair work is required to cope with the existing septic tank, and the treatment and purification during that period will be hindered, so that it cannot be promptly dealt with.

【0006】本発明は、上記事情に鑑みてなされたもの
で、既存の浄化槽を利用して高い栄養塩類除去率を低コ
ストで実現することができると共に、簡単で取扱い性の
良い排水三次処理装置を提供することを目的としてい
る。
The present invention has been made in view of the above circumstances, and it is possible to realize a high nutrient salt removal rate at a low cost by using an existing septic tank, and a simple and easy-to-handle wastewater tertiary treatment device. Is intended to provide.

【0007】[0007]

【課題を解決するための手段】上記目的を達成するため
本発明は、浄化装置の下流に連通して処理水の脱窒及び
脱リンを行う排水三次処理装置において、装置本体に、
バッフルを介して互いに連通する脱窒槽と脱リン槽とを
設け、上記脱窒槽の水面に、下部を処理水に浸漬し且つ
上記放水管から放出された処理水の水流を受けて回転す
ると共に表面に帯磁性部材を装着する羽根車を設け、一
方上記脱リン槽に、表面に帯磁性部材を装着する筒状濾
材を交換自在に没入し、さらにこの筒状濾材の内部と次
の処理槽とを移流管を介して連通したことを特徴とす
る。
In order to achieve the above object, the present invention provides a waste water tertiary treatment apparatus for denitrifying and dephosphorizing treated water, which is connected to a downstream of a purifying apparatus.
A denitrification tank and a dephosphorization tank, which communicate with each other through a baffle, are provided, the lower surface of the denitrification tank is immersed in treated water, and the surface of the denitrification tank is rotated while receiving the water flow of the treated water discharged from the water discharge pipe. An impeller for mounting the magnetically permeable member is provided on the other hand, and a tubular filter medium for mounting the magnetically permeable member on the surface is exchangeably immersed in the dephosphorization tank. Is communicated via an advection tube.

【0008】[0008]

【作 用】本発明では、浄化装置から放出された処理水
を脱窒槽に流入すると、この処理水の水流で羽根車が回
転する。この羽根車の表面には帯磁性部材が取付けられ
ており、表面に菌叢を生成する脱窒菌が上記帯磁性部材
の磁力を受けて活性化され、しかも、この羽根車が回転
することで水圏と気圏とを交互に入換わるため、最適な
環境下で脱窒槽内の処理水を脱窒する。
[Operation] In the present invention, when the treated water discharged from the purification device flows into the denitrification tank, the impeller rotates by the water flow of the treated water. A magnetic susceptibility member is attached to the surface of this impeller, and the denitrifying bacteria that generate bacterial flora on the surface are activated by the magnetic force of the above magnetic susceptibility member. Since the atmosphere and the atmosphere are alternately switched, the treated water in the denitrification tank is denitrified under the optimum environment.

【0009】次いで、この処理水が脱窒槽からバッフル
を介して隣の脱リン槽に流入されると、この流入された
処理水は、この脱リン槽に没入されている筒状濾材を通
り移流管を経て隣の処理槽へ流出する。
Next, when this treated water flows from the denitrification tank through the baffle into the adjacent dephosphorization tank, the inflowed treated water flows through the cylindrical filter media immersed in the dephosphorization tank. It flows out to the next processing tank through the pipe.

【0010】上記筒状濾材には、その表面に設けた帯磁
性部材の磁力により鉄分が吸着され、この鉄分に付着さ
れているリンを同時に吸着する。その結果、筒状濾材を
通過する間に、処理水からほとんどのリンが積極的に除
去される。なお、上記筒状濾材を交換することで、この
筒状濾材の表面に吸着されたリンは他の余剰汚泥と共に
抜き出すことができる。
Iron is adsorbed to the cylindrical filter medium by the magnetic force of the magnetically permeable member provided on the surface thereof, and phosphorus adhering to the iron is adsorbed at the same time. As a result, most of the phosphorus is actively removed from the treated water during passage through the tubular filter media. By exchanging the tubular filter medium, the phosphorus adsorbed on the surface of the tubular filter medium can be extracted together with other excess sludge.

【0011】[0011]

【実施例】以下、図面に基づいて本発明の実施例を説明
する。
Embodiments of the present invention will be described below with reference to the drawings.

【0012】図1に示す排水三次処理装置の装置本体A
には、上流側から脱窒槽1と脱リン槽2とが隣接形成さ
れ、この両槽1,2がバッフル3を介して連通されてい
る。
Apparatus main body A of the waste water tertiary treatment apparatus shown in FIG.
A denitrification tank 1 and a dephosphorization tank 2 are formed adjacent to each other from the upstream side, and both tanks 1 and 2 are connected via a baffle 3.

【0013】上記脱窒槽1の水面には複数の羽根車4が
水流に沿って回転自在に横設されており、この羽根車4
の下部が処理水中に浸漬されている。図2に示すよう
に、この羽根車4の表面には、帯磁性部材の一例である
磁石粒5が多数取付られている。また、この羽根車4の
上方の一方へ偏倚したい位置に、排水を一次処理及び二
次処理する浄化装置Bの放水管B1に連通する流入管6
が臨まされている。
On the water surface of the denitrification tank 1, a plurality of impellers 4 are rotatably provided along the water flow.
The lower part of is immersed in treated water. As shown in FIG. 2, on the surface of the impeller 4, a large number of magnet particles 5 as an example of a magnetically permeable member are attached. Further, at a position where it is desired to be biased to one side above the impeller 4, an inflow pipe 6 communicating with a water discharge pipe B1 of a purifying device B for performing primary treatment and secondary treatment of wastewater.
Is facing.

【0014】一方、上記脱リン槽2は、処理水の流れに
沿って上流から下流方向へ複数の処理槽2a及び終処理
槽2bに分割されており、各処理槽2aには、交換自在
な筒状濾材7が立設されている。図3に示すように、こ
の筒状濾材7の表面には、帯磁性部材の一例である磁石
粒5が多数取付けられている。また、この筒状濾材7の
内部には、いわゆる鹿沼土を代表とする軽石風化粒など
の内部濾材が充填されている。
On the other hand, the dephosphorization bath 2 is divided into a plurality of treatment baths 2a and a final treatment bath 2b from the upstream side to the downstream side along the flow of the treated water, and the treatment baths 2a are exchangeable. The tubular filter material 7 is erected. As shown in FIG. 3, a large number of magnet particles 5, which are an example of a magnetically permeable member, are attached to the surface of the tubular filter material 7. Further, the inside of the cylindrical filter medium 7 is filled with an internal filter medium such as pumice weathered particles typified by so-called Kanuma soil.

【0015】また、この筒状濾材7の低部の上流方向に
指向する側面に流入口7aが穿設されており、処理水
は、この流入口7aから内部に流入して上昇される。さ
らに、この筒状濾材7の上部の下流方向に指向する側面
に、この筒状濾材7の内部に連通する移流管8が連設さ
れ、この移流管8の吐出口が隣の処理槽2aに開口され
ている。また、最下流に位置する処理槽2aに立設され
た筒状濾材7に連通する移流管8が終処理槽2bに開口
され、この終処理槽2bの水面に放流管9が開口されて
いる。
An inflow port 7a is formed in a side surface of the lower portion of the cylindrical filter medium 7 which faces the upstream direction, and the treated water flows into the inflow port 7a and rises. Further, an advection pipe 8 communicating with the inside of the tubular filter medium 7 is connected to the side surface of the upper portion of the tubular filter medium 7 which is directed in the downstream direction, and the discharge port of the advection pipe 8 is connected to the adjacent processing tank 2a. It is open. Further, an advection pipe 8 communicating with a cylindrical filter medium 7 standing upright in the treatment tank 2a located at the most downstream side is opened in the final treatment tank 2b, and a discharge pipe 9 is opened in the water surface of the final treatment tank 2b. .

【0016】次に、上記構成による実施例の作用につい
て説明する。
Next, the operation of the embodiment having the above structure will be described.

【0017】浄化装置Bで所定に一次処理、二次処理さ
れた処理水が装置本体Aの流入管6から、脱窒槽1の水
面に横設する羽根車4に吐出されると、この羽根車4が
回転し、この羽根車4の表面に菌叢を生成する脱窒菌が
水圏と気圏とを交互に入れ替り、良好な脱窒環境を作る
と共に、上記脱窒菌は上記羽根車4の表面に取付けた磁
石粒5の磁力を受けて活性化されており、上記脱窒槽1
に流入した処理水を良好な環境下で脱窒する。
When the treated water, which has been subjected to a predetermined primary treatment and a secondary treatment in the purifying device B, is discharged from the inflow pipe 6 of the main body A of the device to the impeller 4 laterally provided on the water surface of the denitrification tank 1, this impeller 4 rotates, the denitrifying bacteria that generate a flora on the surface of the impeller 4 alternate between the hydrosphere and the atmosphere to create a good denitrifying environment, and the denitrifying bacteria are attached to the surface of the impeller 4. The denitrification tank 1 is activated by receiving the magnetic force of the magnet particles 5.
Denitrify the treated water that has flowed into the system under a favorable environment.

【0018】そして、この脱窒槽1からバッフル3を介
して隣の脱リン槽2の処理槽2aに流入された処理水
は、ゆっくりと下降し、この処理槽2に立設する筒状濾
材7の下部側面に穿設した流入口7aから、この筒状濾
材7の内部に流入され、この内部を上昇する。その間、
この筒状濾材7の表面に装着した多数の磁石粒5によっ
て鉄分が吸着されると同時に、この鉄分に付着するリン
が吸着される。さらに、この筒状濾材7に充填した軽石
風化粒などの内部濾材によって、リン及び他の汚濁物が
効率よく除去される。
The treated water that has flowed from the denitrification tank 1 through the baffle 3 into the treatment tank 2a of the adjacent dephosphorization tank 2 slowly descends, and the cylindrical filter medium 7 standing upright in this treatment tank 2 is provided. From the inflow port 7a formed in the lower side surface of the cylindrical filter medium 7, it flows into the inside of the cylindrical filter medium 7 and rises inside thereof. in the meantime,
Iron is adsorbed by the large number of magnet particles 5 mounted on the surface of the tubular filter material 7 and, at the same time, phosphorus adhering to the iron is adsorbed. Further, phosphorus and other contaminants are efficiently removed by the internal filter medium such as weathered pumice particles filled in the tubular filter medium 7.

【0019】その結果、上記処理水中の窒素及びリンの
ほとんどが、各処理槽1,2aを流れる間に除去され、
終処理槽2bでは、鉄分及び栄養塩類除去率のきわめて
高い清澄な処理水(三次処理水)が得られる。
As a result, most of the nitrogen and phosphorus in the treated water are removed while flowing through the treatment tanks 1 and 2a,
In the final treatment tank 2b, clear treated water (tertiary treated water) having an extremely high iron and nutrient salt removal rate can be obtained.

【0020】また、上記筒状濾材7は交換自在なカート
リッジタイプであり、この筒状濾材7に余剰汚泥と共に
吸着されたリンは、この筒状濾材7自体を交換すること
で、簡単に抜き出すことができる。
The tubular filter medium 7 is a replaceable cartridge type, and the phosphorus adsorbed on the tubular filter medium 7 together with the excess sludge can be easily extracted by replacing the tubular filter medium 7 itself. You can

【0021】さらに、この排水三次処理装置は外部動力
が不要であるため、経済的であり、既存の浄化装置5を
改修することなく、簡単な増設工事で対応することがで
きるので、迅速な対応が可能となり、しかも取扱い性が
良い。
Furthermore, since this waste water tertiary treatment device does not require external power, it is economical, and it can be dealt with by a simple extension work without modifying the existing purification device 5, so that a quick response is possible. It is possible and easy to handle.

【0022】[0022]

【発明の効果】以上、説明したように本発明によれば、
浄化装置の下流に併設するだけて、栄養塩類除去率のき
わめて高い清澄な三次処理水を得ることができる。
As described above, according to the present invention,
Only by installing it downstream of the purification device, it is possible to obtain clear tertiary treated water with extremely high nutrient salt removal rate.

【0023】また、無動力であるため、経済的で、しか
も保守管理が容易となり、既存の浄化装置に、低コスト
で簡単に増設することができる。
Moreover, since it is non-powered, it is economical and maintenance is easy, and it can be easily added to an existing purification device at low cost.

【0024】更に、筒状濾材が交換自在なカートリッジ
タイプであるため、この筒状濾材を交換することで、リ
ンを他の余剰汚泥と共に簡単に抜き出すことができて、
取扱い性がよい。
Furthermore, since the tubular filter medium is a replaceable cartridge type, phosphorus can be easily extracted together with other excess sludge by exchanging the tubular filter medium.
Good handleability.

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

【図1】排水三次処理装置の概略断面図FIG. 1 Schematic cross-sectional view of a wastewater tertiary treatment device

【図2】羽根車の斜視図FIG. 2 is a perspective view of an impeller.

【図3】筒状濾材の斜視図FIG. 3 is a perspective view of a tubular filter medium.

【符号の説明】[Explanation of symbols]

1 脱窒槽 2 脱リン槽 3 バッフル 4 羽根車 5 帯磁性部材 7 筒状濾材 8 移流管 A 装置本体 B 浄化装置 1 denitrification tank 2 dephosphorization tank 3 baffle 4 impeller 5 magnetic member 7 tubular filter material 8 advection tube A device body B purification device

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 C02F 3/08 A ─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 6 Identification code Internal reference number FI technical display area C02F 3/08 A

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 浄化装置の下流に連通して処理水の脱窒
及び脱リンを行う排水三次処理装置において、 装置本体に、バッフルを介して互いに連通する脱窒槽と
脱リン槽とを設け、 上記脱窒槽の水面に、下部を処理水に浸漬し且つ上記放
水管から放出された処理水の水流を受けて回転すると共
に表面に帯磁性部材を装着する羽根車を設け、 一方上記脱リン槽に、表面に帯磁性部材を装着する筒状
濾材を交換自在に没入し、 さらにこの筒状濾材の内部と次の処理槽とを移流管を介
して連通したことを特徴とする排水三次処理装置。
1. A waste water tertiary treatment device for denitrifying and dephosphorizing treated water communicating with a downstream of a purification device, wherein a denitrification tank and a dephosphorization tank communicating with each other via a baffle are provided in the main body of the device. On the water surface of the denitrification tank, there is provided an impeller whose lower part is immersed in treated water and which is rotated by receiving the water flow of the treated water discharged from the water discharge pipe and which is equipped with a magnetically permeable member on the surface thereof. A drainage tertiary treatment device characterized in that a tubular filter medium having a magnetically permeable member mounted on the surface is replaceably immersed, and the inside of the tubular filter medium is communicated with the next treatment tank through an advection pipe. .
JP6005994A 1994-01-24 1994-01-24 Tertiary treatment apparatus for drainage Pending JPH07204685A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6005994A JPH07204685A (en) 1994-01-24 1994-01-24 Tertiary treatment apparatus for drainage

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6005994A JPH07204685A (en) 1994-01-24 1994-01-24 Tertiary treatment apparatus for drainage

Publications (1)

Publication Number Publication Date
JPH07204685A true JPH07204685A (en) 1995-08-08

Family

ID=11626347

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6005994A Pending JPH07204685A (en) 1994-01-24 1994-01-24 Tertiary treatment apparatus for drainage

Country Status (1)

Country Link
JP (1) JPH07204685A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003245687A (en) * 2002-02-26 2003-09-02 Fumio Maekawa Method for promoting biological denitrification by magnetic field
CN113941438A (en) * 2021-10-20 2022-01-18 广东顺博铝合金有限公司 Aluminum products recovery processing is with broken lump material deironing device

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003245687A (en) * 2002-02-26 2003-09-02 Fumio Maekawa Method for promoting biological denitrification by magnetic field
CN113941438A (en) * 2021-10-20 2022-01-18 广东顺博铝合金有限公司 Aluminum products recovery processing is with broken lump material deironing device
CN113941438B (en) * 2021-10-20 2024-03-12 广东顺博铝合金有限公司 Broken piece material deironing device for aluminum product recovery processing

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