JP3688828B2 - Pumping device - Google Patents

Pumping device Download PDF

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Publication number
JP3688828B2
JP3688828B2 JP29234696A JP29234696A JP3688828B2 JP 3688828 B2 JP3688828 B2 JP 3688828B2 JP 29234696 A JP29234696 A JP 29234696A JP 29234696 A JP29234696 A JP 29234696A JP 3688828 B2 JP3688828 B2 JP 3688828B2
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JP
Japan
Prior art keywords
liquid
pumping
screen panel
nitrification
bucket
Prior art date
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Expired - Fee Related
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JP29234696A
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Japanese (ja)
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JPH10141215A (en
Inventor
護 皆方
成人 有松
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Maezawa Industries Inc
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Maezawa Industries Inc
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Priority to JP29234696A priority Critical patent/JP3688828B2/en
Publication of JPH10141215A publication Critical patent/JPH10141215A/en
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Description

【0001】
【発明の属する技術分野】
本発明は、揚液装置に関し、詳しくは、液中に浮遊物が存在する液を浮遊物を分離しながら揚液するための揚液装置であって、例えば、硝化槽担体投入型活性汚泥循環法による排水処理装置の硝化液循環用として用いるのに適した揚液装置に関する。
【0002】
【従来の技術】
従来から、排水中の窒素分を除去する方法として、脱窒槽と硝化槽とを備えた循環式硝化脱窒法が広く採用されている。この循環式硝化脱窒法は、基本的には、前段が無酸素条件下の脱窒槽、後段が好気性条件下の硝化槽で構成され、硝化槽で生成した硝酸性窒素及び亜硝酸性窒素を含む硝化液を前段の脱窒槽へ返流循環して原水と接触させ、原水中のBODを利用して脱窒菌(嫌気性細菌)の働きで脱窒を図る処理方法である。
【0003】
従来、硝化槽から脱窒槽に硝化液を返流させる手段としては、一般的な渦巻ポンプ等の揚水ポンプが用いられていたが、循環式硝化脱窒法では、通常、硝化槽から脱窒槽に返流させる硝化液の量を原水の1〜3倍、多いときには約6倍にまで設定しているために硝化液の返流量が極めて多く、ポンプの消費エネルギーが多大であり、ランニングコストに大きく影響していた。また、硝化槽と脱窒槽とは、通常、同じレベルで設けられているため、ポンプ自体の性能(揚程等)も過剰であり、コストアップの一因となっていた。
【0004】
このため、硝化槽における全面曝気用空気のエアリフト効果を利用して硝化槽から脱窒槽に硝化液を返流させることも行われている。すなわち、硝化槽内を好気性条件下とするために散気装置から発生する空気泡を処理水中に含ませることにより、処理水の見掛けの比重を小さくして比重差に相当する分だけ水位を上昇させることに加えて、空気泡の上昇に伴う液面上昇を利用して硝化槽内の水位を脱窒槽の水位より高くすることで処理水(硝化液)を脱窒槽に流下させるようにしている。
【0005】
【発明が解決しようとする課題】
しかし、硝化槽に供給する空気泡は、硝化槽内を好気性条件下とするためのものであって、エアリフト効果による揚水は二次的なものであるため、エアリフト効果だけでは、処理水の流入量や流出量が変化すると所定の返流量を確保することが不可能になることがあり、しかも、揚水量が水位に影響されるために返流量の調節が困難であるという問題もあった。
【0006】
さらに、いずれの返流手段においても、硝化槽内に硝化菌固定化担体を投入した場合は、返流水等に担体が同伴されることを防止するため、固定スクリーン等の固液分離装置を設置しているが、スクリーン等に担体が詰まったり、流入水中に残ったし渣の絡み付きによる閉塞の可能性があった。
【0007】
そこで本発明は、このような硝化槽担体投入型活性汚泥循環法による排水処理装置における硝化液循環用として用いるのに適し、揚液量の制御が容易で、担体等の固形物の分離も確実に行うことができる揚液装置を提供することを目的としている。
【0008】
【課題を解決するための手段】
上記目的を達成するため、本発明の揚液装置は、液中から液面上にわたって設置される無端状のスクリーンパネルと、該スクリーンパネルを回転駆動する駆動源と、スクリーンパネルの内周部両側の少なくとも液中部分を閉塞する塞ぎ板と、スクリーンパネルの内周側に設けられた揚液バケットと、該揚液バケットの上昇側内周部の液面より上方に設けられた液受けとを備え、前記揚液バケットは、前記液受け側に流出口を有するとともに、液受けは、液中から液受け上方に向かって上昇する揚液バケットの流出口を閉塞する揚液板を備えていることを特徴としている。また、前記スクリーンパネルの内側から外側に向けて圧力流体を噴出するノズルを設けたことを特徴としている。
【0009】
【発明の実施の形態】
以下、本発明を、図面を参照してさらに詳細に説明する。図1は本発明の揚液装置の一例を示す概略側面図、図2は揚液装置の正面図、図3は同じく横断面図、図4は要部の斜視図、図5は循環式硝化脱窒法による排水処理装置への設置例を示す概略平面図である。
【0010】
この揚液装置は、液中から液面上にわたって設置される無端状のスクリーンパネル1と、このスクリーンパネル1の内周側に設けられた揚液バケット2と、この揚液バケット2の上昇側内周部の液面より上方に設けられた液受け3と、スクリーンパネル1の内側から外側に向けて圧力流体を噴出するノズル4とを有するもので、スクリーンパネル1と揚液バケット2とは、エンドレスチェーン5により保持され、スクリーンパネル1の内周部両側を閉塞する塞ぎ板6等に設けられたガイド及びスプロケット(図示せず)により回転可能に支持されており、駆動源である電動機7により回転駆動されている。
【0011】
揚液バケット2は、液受け3側の一側に流出口2aとなる開口を形成した箱状のものであって、液受け3には、液中から液受け上部に向かって上昇する揚液バケット2の流出口2aを閉塞する揚液板3aが垂直方向に設けられている。
【0012】
このように形成した揚液装置を図1に示す矢印方向に回転させると、図1左側を液中から上昇する揚液バケット2内の水等は、該揚液バケット2の流出口2aが揚液板3aにより閉塞されているため、揚液バケット2と揚液板3aとに囲まれた部分の量が汲み上げられ、揚液バケット2が揚液板3aより上方に移動することによって液受け3内に流下し、該液受け3に接続した適宜な流路を介して所望の設備に送られることになる。
【0013】
また、汲み上げられる水等は、両側が塞ぎ板6で塞がれているため、スクリーンパネル1を通過してスクリーンパネル1の内周部に流入するので、液中の浮遊物が侵入することがなく、揚液バケット2により水等のみを汲み上げることができる。このとき、スクリーンパネル1に捕捉された浮遊物は、スクリーンパネル1の傾斜及びノズル4から噴出する水等の圧力流体によりスクリーンパネル1から除去されて再び液中に戻される。
【0014】
この揚液装置は、揚液バケット2の容積及びその設置数と、その回転速度とにより揚液量を決定することができるので、運転中の流量変更も、回転速度を調節することにより容易に制御することができる。
【0015】
このように形成した揚液装置は、例えば、図5に示す循環式硝化脱窒法による排水処理装置の硝化槽11内に設置されて硝化液の返流と排出とを行うのに適している。この排水処理装置は、原水及び硝化液が流入する脱窒槽12と、脱窒槽12の処理水が流入する前記硝化槽11とを有するもので、揚液装置Aの液受け3には、硝化槽11内の処理水を脱窒槽12に返流する硝化液返流用流路13と、処理水を次の処理工程に送出する処理水送出流路14とが接続されている。
【0016】
原水流入部15から脱窒槽12に流入した原水は、硝化液返流用流路13から流入する1〜6倍量の循環硝化液と混合して撹拌機で撹拌されながら無酸素条件下で脱窒処理された後、流路16から硝化槽11内に流入し、散気装置から供給される空気により撹拌されながら好気状態で硝化菌固定化担体に担持された硝化菌により硝化処理される。
【0017】
そして、硝化槽11の処理水は、揚液装置Aで液受け3に揚液された後、硝化液返流用流路13と処理水送出流路14とに所定量が分岐して流れ、一部が処理水送出流路14から次工程に送出され、その1〜6倍量が脱窒槽12に送り返される。
【0018】
このように、上記構成の揚液装置Aを用いることにより、エアリフト効果を利用した硝化液の返流に比べて安定した流量で硝化液を脱窒槽12に戻すことができ、循環量を増加させて脱窒効率を向上させることもでき、また、一般的な揚水ポンプに比べてコストの低減が図れる。
【0019】
さらに、スクリーンパネル1の内周側にノズル4を設け、このノズル4から水や空気等をスクリーンパネル1の外側に向けて噴出させることにより、スクリーンパネル1に付着した担体やし渣等をより確実にスクリーンパネル1から除去することができるので、担体の流出を防止できるとともにスクリーンパネル1の閉塞を防止でき、スクリーン面積を小さくすることもできる。
【0020】
なお、スクリーンパネルや揚液バケットの形状等は、上記実施例に限るものではなく、例えば、スクリーンパネルと揚液バケットとを一体的に形成することもでき、全体を円形状に回転させることもできる。また、スクリーンパネルは、図示のように山形に形成することが、スクリーンパネルからの捕捉物の除去の点で好ましいが、平面状に形成することもできる。さらに、揚液装置の用途も、上記排水処理装置に限らず、様々な設備・装置の揚液手段として用いることができる。
【0021】
【発明の効果】
以上説明したように、本発明の揚液装置によれば、液中の浮遊物を分離しながら安定した状態で揚液することができ、揚液量の調節も容易である。特に、スクリーンに付着した浮遊物を簡単に除去することができるので、運転中にスクリーンが閉塞することがなく、スクリーン面積を小さくすることができる。
【図面の簡単な説明】
【図1】 本発明の揚液装置の一例を示す概略側面図である。
【図2】 揚液装置の正面図である。
【図3】 同じく横断面図である。
【図4】 要部の斜視図である。
【図5】 揚液装置の設置例を示す概略平面図である。
【符号の説明】
1…スクリーンパネル、2…揚液バケット、2a…流出口、3…液受け、3a…揚液板、4…ノズル、5…エンドレスチェーン、6…塞ぎ板、7…電動機
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a pumping device, and more particularly, a pumping device for pumping a liquid in which a floating substance exists in the liquid while separating the floating substance, for example, a nitrification tank carrier input type activated sludge circulation TECHNICAL FIELD The present invention relates to a pumping device suitable for use as a nitrifying solution circulation in a wastewater treatment device by the method.
[0002]
[Prior art]
Conventionally, a circulating nitrification denitrification method including a denitrification tank and a nitrification tank has been widely adopted as a method for removing nitrogen content in waste water. This circulatory nitrification denitrification method basically consists of a denitrification tank under anaerobic conditions in the first stage and a nitrification tank under aerobic conditions in the first stage, and nitrate nitrogen and nitrite nitrogen produced in the nitrification tank are used. This is a treatment method in which the nitrifying liquid contained is returned to the preceding denitrification tank and brought into contact with raw water, and denitrification is performed by the action of denitrifying bacteria (anaerobic bacteria) using BOD in the raw water.
[0003]
Conventionally, as a means for returning the nitrification solution from the nitrification tank to the denitrification tank, a general pump such as a centrifugal pump has been used. However, in the circulation type nitrification denitrification method, the nitrification tank is usually returned from the nitrification tank to the denitrification tank. The amount of nitrating liquid to be flowed is set to 1 to 3 times the raw water, and to about 6 times when it is large, so the flow rate of nitrating liquid is extremely large, the energy consumption of the pump is enormous, and the running cost is greatly affected. Was. In addition, since the nitrification tank and the denitrification tank are usually provided at the same level, the performance of the pump itself (lift head, etc.) is excessive, which contributes to an increase in cost.
[0004]
For this reason, the nitrification liquid is also returned from the nitrification tank to the denitrification tank by utilizing the air lift effect of the entire aeration air in the nitrification tank. In other words, by adding air bubbles generated from the diffuser to make the inside of the nitrification tank aerobic, the apparent specific gravity of the treated water is reduced and the water level is adjusted by an amount corresponding to the specific gravity difference. In addition to raising the water level, the water level in the nitrification tank is made higher than the water level in the denitrification tank using the rise in liquid level accompanying the rise of air bubbles so that the treated water (nitrification liquid) flows down to the denitrification tank. Yes.
[0005]
[Problems to be solved by the invention]
However, the air bubbles supplied to the nitrification tank are for making the inside of the nitrification tank aerobic, and the pumping by the air lift effect is secondary. If the inflow or outflow changes, it may not be possible to secure a predetermined return flow rate, and there is also a problem that it is difficult to adjust the return flow rate because the pumped amount is affected by the water level. .
[0006]
Furthermore, in any return means, when a nitrifying bacteria-immobilized carrier is introduced into the nitrification tank, a solid-liquid separation device such as a fixed screen is installed to prevent the carrier from being entrained in the return water. However, there is a possibility of clogging due to tangling of the residue remaining in the inflowing water or the carrier clogged in the screen or the like.
[0007]
Therefore, the present invention is suitable for use as a nitrification liquid circulation in a wastewater treatment apparatus using such a nitrification tank carrier input type activated sludge circulation method, can easily control the amount of pumped liquid, and reliably separate solids such as a carrier. An object of the present invention is to provide a liquid pumping apparatus that can be used for the above.
[0008]
[Means for Solving the Problems]
In order to achieve the above object, a liquid pumping apparatus according to the present invention includes an endless screen panel installed from the liquid to the liquid surface, a drive source for rotationally driving the screen panel, and both sides of the inner peripheral portion of the screen panel. A closing plate that closes at least the liquid portion, a pumping bucket provided on the inner peripheral side of the screen panel, and a liquid receiver provided above the liquid level on the inner peripheral portion on the rising side of the pumping bucket. The liquid bucket has an outlet on the liquid receiver side, and the liquid receiver has a pumping plate for closing the outlet of the liquid bucket that rises upward from the liquid toward the liquid receiver. It is characterized by that. Further, a nozzle for ejecting a pressure fluid from the inside to the outside of the screen panel is provided.
[0009]
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, the present invention will be described in more detail with reference to the drawings. 1 is a schematic side view showing an example of the liquid pumping apparatus of the present invention, FIG. 2 is a front view of the liquid pumping apparatus, FIG. 3 is a cross-sectional view, FIG. 4 is a perspective view of the main part, and FIG. It is a schematic plan view which shows the example of installation to the waste water treatment equipment by a denitrification method.
[0010]
The pumping device includes an endless screen panel 1 installed from the liquid to the liquid surface, a pumping bucket 2 provided on the inner peripheral side of the screen panel 1, and a rising side of the pumping bucket 2. It has a liquid receiver 3 provided above the liquid surface of the inner peripheral part and a nozzle 4 for ejecting a pressure fluid from the inside to the outside of the screen panel 1. The motor 7 is supported by the endless chain 5 and is rotatably supported by a guide and a sprocket (not shown) provided on a closing plate 6 that closes both sides of the inner peripheral portion of the screen panel 1. It is driven by rotation.
[0011]
The pumping bucket 2 is a box-like shape in which an opening serving as an outlet 2a is formed on one side of the liquid receiver 3, and the liquid receiver 3 is a pumped liquid that rises from the liquid toward the upper part of the liquid receiver. A liquid lifting plate 3a for closing the outlet 2a of the bucket 2 is provided in the vertical direction.
[0012]
When the pumping device formed in this way is rotated in the direction of the arrow shown in FIG. 1, water in the pumping bucket 2 that rises from the liquid on the left side of FIG. Since it is closed by the liquid plate 3a, the amount of the portion surrounded by the pumping bucket 2 and the pumping plate 3a is pumped up, and the liquid receiver 3 is moved by moving the pumping bucket 2 upward from the pumping plate 3a. Then, the liquid flows down and is sent to a desired facility through an appropriate flow path connected to the liquid receiver 3.
[0013]
Further, since the water or the like to be pumped is closed on both sides by the closing plate 6, it passes through the screen panel 1 and flows into the inner peripheral portion of the screen panel 1, so that floating substances in the liquid may enter. In addition, only the water or the like can be pumped by the pumping bucket 2. At this time, the suspended matter captured by the screen panel 1 is removed from the screen panel 1 by pressure fluid such as the inclination of the screen panel 1 and water ejected from the nozzle 4 and returned to the liquid again.
[0014]
Since the pumping device can determine the pumping amount based on the volume of the pumping bucket 2, the number of the pumping buckets 2 installed, and the rotation speed thereof, it is easy to change the flow rate during operation by adjusting the rotation speed. Can be controlled.
[0015]
The pumping device formed in this way is suitable for, for example, installing in the nitrification tank 11 of the wastewater treatment device by the circulating nitrification denitrification method shown in FIG. 5 to return and discharge the nitrification solution. This waste water treatment apparatus has a denitrification tank 12 into which raw water and nitrification liquid flow and a nitrification tank 11 into which treated water from the denitrification tank 12 flows. 11 is connected to a nitrification liquid return flow path 13 for returning the treated water in the denitrification tank 12 and a treated water delivery flow path 14 for delivering the treated water to the next treatment step.
[0016]
The raw water flowing into the denitrification tank 12 from the raw water inflow section 15 is mixed with 1 to 6 times the amount of circulating nitrification liquid flowing in from the nitrification liquid return flow path 13 and dehydrated under anoxic conditions while being stirred by a stirrer. After being subjected to nitriding treatment, it flows into the nitrification tank 11 from the flow path 16 and is nitrified by the nitrifying bacteria carried on the nitrifying bacteria immobilization support in an aerobic state while being agitated by the air supplied from the air diffuser. .
[0017]
Then, the treated water in the nitrification tank 11 is pumped to the liquid receiver 3 by the pumping device A, and then a predetermined amount branches and flows into the nitrifying liquid return flow path 13 and the treated water delivery flow path 14, A part is sent from the treated water delivery channel 14 to the next process, and 1 to 6 times the amount is sent back to the denitrification tank 12.
[0018]
Thus, by using the pumping apparatus A having the above-described configuration, the nitrification liquid can be returned to the denitrification tank 12 at a stable flow rate compared with the return flow of the nitrification liquid using the air lift effect, and the circulation rate is increased. Thus, the denitrification efficiency can be improved, and the cost can be reduced as compared with a general pump.
[0019]
Furthermore, a nozzle 4 is provided on the inner peripheral side of the screen panel 1, and water, air, or the like is ejected from the nozzle 4 toward the outside of the screen panel 1, thereby further removing the carrier, residue, etc. attached to the screen panel 1. Since it can be reliably removed from the screen panel 1, it is possible to prevent the carrier from flowing out, to prevent the screen panel 1 from being blocked, and to reduce the screen area.
[0020]
The shape of the screen panel and the liquid bucket is not limited to the above embodiment, and for example, the screen panel and the liquid bucket can be integrally formed, and the whole can be rotated into a circular shape. it can. Further, the screen panel is preferably formed in a mountain shape as shown in the drawing, from the viewpoint of removal of trapped substances from the screen panel, but can also be formed in a flat shape. Furthermore, the use of the pumping device is not limited to the waste water treatment device, and can be used as a pumping means for various facilities and devices.
[0021]
【The invention's effect】
As described above, according to the liquid pumping apparatus of the present invention, liquid can be pumped in a stable state while separating suspended matters in the liquid, and the amount of liquid pumping can be easily adjusted. In particular, since floating substances adhering to the screen can be easily removed, the screen is not blocked during operation, and the screen area can be reduced.
[Brief description of the drawings]
FIG. 1 is a schematic side view showing an example of a liquid pumping apparatus according to the present invention.
FIG. 2 is a front view of a pumping device.
FIG. 3 is a cross-sectional view of the same.
FIG. 4 is a perspective view of a main part.
FIG. 5 is a schematic plan view showing an installation example of a liquid pumping apparatus.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 ... Screen panel, 2 ... Pumping liquid bucket, 2a ... Outlet, 3 ... Liquid receptacle, 3a ... Pumping plate, 4 ... Nozzle, 5 ... Endless chain, 6 ... Closing plate, 7 ... Electric motor

Claims (2)

液中から液面上にわたって設置される無端状のスクリーンパネルと、該スクリーンパネルを回転駆動する駆動源と、スクリーンパネルの内周部両側の少なくとも液中部分を閉塞する塞ぎ板と、スクリーンパネルの内周側に設けられた揚液バケットと、該揚液バケットの上昇側内周部の液面より上方に設けられた液受けとを備え、前記揚液バケットは、前記液受け側に流出口を有するとともに、液受けは、液中から液受け上方に向かって上昇する揚液バケットの流出口を閉塞する揚液板を備えていることを特徴とする揚液装置。An endless screen panel installed from the liquid surface to the liquid surface, a drive source for rotationally driving the screen panel, a blocking plate for closing at least the liquid portion on both sides of the inner periphery of the screen panel, A pumping liquid provided on the inner peripheral side, and a liquid receiver provided above the liquid surface of the inner peripheral part on the rising side of the pumping bucket, the pumping bucket being an outlet on the liquid receiving side The liquid receiver includes a pumping plate that closes an outlet of the pumping bucket that rises from the liquid toward the upper side of the liquid receiver. 前記スクリーンパネルの内側に、スクリーンパネルの外側に向けて圧力流体を噴出するノズルを設けたことを特徴とする請求項1記載の揚液装置。2. The liquid pumping apparatus according to claim 1, wherein a nozzle for ejecting a pressure fluid toward the outside of the screen panel is provided inside the screen panel.
JP29234696A 1996-11-05 1996-11-05 Pumping device Expired - Fee Related JP3688828B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP29234696A JP3688828B2 (en) 1996-11-05 1996-11-05 Pumping device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP29234696A JP3688828B2 (en) 1996-11-05 1996-11-05 Pumping device

Publications (2)

Publication Number Publication Date
JPH10141215A JPH10141215A (en) 1998-05-26
JP3688828B2 true JP3688828B2 (en) 2005-08-31

Family

ID=17780618

Family Applications (1)

Application Number Title Priority Date Filing Date
JP29234696A Expired - Fee Related JP3688828B2 (en) 1996-11-05 1996-11-05 Pumping device

Country Status (1)

Country Link
JP (1) JP3688828B2 (en)

Also Published As

Publication number Publication date
JPH10141215A (en) 1998-05-26

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