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JP3692893B2 - Aerobic treatment tank - Google Patents
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JP3692893B2 - Aerobic treatment tank - Google Patents

Aerobic treatment tank Download PDF

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JP3692893B2
JP3692893B2 JP2000056997A JP2000056997A JP3692893B2 JP 3692893 B2 JP3692893 B2 JP 3692893B2 JP 2000056997 A JP2000056997 A JP 2000056997A JP 2000056997 A JP2000056997 A JP 2000056997A JP 3692893 B2 JP3692893 B2 JP 3692893B2
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area
carrier
treated
water
tank
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JP2001239291A (en
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正芳 佐久間
秀行 諏訪
真 田中
直道 森
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日立プラント建設株式会社
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    • 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

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  • Aeration Devices For Treatment Of Activated Polluted Sludge (AREA)

Description

【0001】
【発明の属する技術分野】
本発明は好気性処理槽に係り、特に被処理水と粒状の担体とを流動状態で接触させる好気性処理槽に関する。
【0002】
【従来の技術】
図11に従来の技術に係る好気性処理槽の一例を示す。槽10内には微生物を保持した担体12が投入されている。また、槽10の中央部には槽内を平面的に2つのエリアに区分する隔壁14が配設されている。隔壁14はその上部及び下部が欠落しており、一方のエリア16と他方のエリア18とはその上下が連通している。エリア16の中段位置には曝気用の空気を上方に向けて吹き出す散気装置20が設置されている。
【0003】
被処理水は流入管22から槽10内に供給され、一定の水位を維持して被処理水が張り込まれている。この状態で前記散気装置20から空気を吹き出すと、吹き出された空気のリフト作用によって被処理水に上昇流が生じ、被処理水をエリア16とエリア18との間に右廻りに循環させる循環流Xが形成される。被処理水の循環流Xに乗って前記担体12も槽10内を流動しながら循環する。
【0004】
被処理水と担体12が流動状態で接触しつつ所定時間循環する過程で、前記曝気による好気条件下で担体12に保持された微生物の作用により被処理水は浄化処理される。処理水は担体12の流出を防止するためのスクリーン24をすり抜けて流出管26から槽外に排出される。
【0005】
上記好気性処理槽においては、比重がなるべく被処理水に近い担体を適度の濃度で投入し、被処理水と均一に混合接触させながら循環することが処理効率を向上させる上で重要である。被処理水の密度は温度によっても変化するので、担体の比重を被処理水と一致させることは困難である。このため、担体の原材料として高分子系の材料を用いる場合には、その取扱性や製造上の制約、価格等の観点から担体の比重は1.01〜1.08程度のものが好ましく用いられる。
【0006】
【発明が解決しようとする課題】
しかしながら、この種の好気性処理槽では担体を被処理水と均一に混合接触させながら循環するにはかなりの高度な技術が必要であることが判明した。すなわち、発明者の経験によれば上記比重が1.01〜1.08程度の担体を用いた場合においては、図11に示すように担体12がエリア18の右端底部に沈降堆積する現象が見られた。このような担体の沈降堆積現象は、反応に寄与しない担体の割合が大きくなり、担体と被処理水との接触効率が低下して、処理性能が悪化する原因となる。また、沈降堆積した担体に付着した微生物が嫌気状態下で腐敗したり、担体が相互に固着して悪影響をもたらす場合もある。まして、担体の比重が例えば活性炭のように2.0程度の場合には担体の沈降堆積現象がより一層顕著となり、処理性能の低下や運転操作上のトラブルを引き起こすことが懸念された。
【0007】
本発明の目的は、上記従来技術の問題点を改善し、槽の底部に担体が沈降堆積しにくく、担体と被処理水との接触効率を向上させることができる好気性処理槽を提供することにある。
【0008】
【課題を解決するための手段】
本発明は、被処理水とこの被処理水よりも比重が大きい粒状の担体とを流動状態で接触させる好気性処理槽において、槽内を平面的に区分した一方のエリアに空気を吹き出す散気装置を配置し、この吹き出された空気のリフト作用によって前記被処理水と担体とを前記一方のエリアと他方のエリアとの間に循環させ、前記他方のエリアには前記被処理水と担体とを分離するためのスクリーンを配設するとともに、前記他方のエリアには循環流を内回りの循環流X と前記スクリーン面に沿った外回りの循環流X に分ける案内部材を設け、前記循環流X 槽の側壁に沿って槽底部に導くようにしたことを特徴とする。
【0009】
前記循環流X 循環路の入口開口面積と出口開口面積の比は1〜5であることが望ましい。
【0011】
また、本発明は前記処理槽内に前記一方のエリアと他方のエリアとを仕切る隔壁が配設されたことが望ましい
【0012】
また、本発明は前記案内部材の下端を変形自在にすることによって、前記循環流X 循環路の出口開口面積が調整可能にされたことを特徴とする。
【0013】
また、本発明は前記一方のエリアに配置される散気装置が外側と内側に区分され、外側の散気装置から散気される空気のリフト作用が、内側のそれよりも大きくなるように調整されたことが望ましい
【0014】
【発明の実施の形態】
本発明の実施の形態を図面に即して説明する。以下に示す図面において、前掲の図11と同一の符号を付したものは図11に示したと同様又は類似の機能を持つ要素であり、その説明を省略することがある。
【0015】
図1は本発明の第1の実施例を示す断面図であり、図2は図1のD−D矢視図である。この実施例では他方のエリア18に案内板30が設けられている。案内板30はスクリーン24面に対して所定の間隔を有して、スクリーン24面と略平行に設けられ、また、案内板30の下端は側壁28に近接した位置まで延びている。
【0016】
上記の構成において、エリア16からの循環流Xは、他方のエリア18において前記案内板30の存在によって案内板30の上端位置で循環流X0と循環流X1に2分される。循環流X0は隔壁14と案内板30との間を通る内回りの流れとなって隔壁14の下方から一方のエリア16に戻る。
【0017】
一方、循環流X1は前記案内板30によって区画され、案内板30とスクリーン24面、側壁28との間に形成された循環路32内を側壁28に沿って下方に流れ、循環流X2として槽底部34に導かれる。循環路32の入口開口面積A1と出口開口面積A2との比は1〜5の範囲、好ましくは1.5〜3の範囲に設定される。すなわち、入口開口面積A1に比べて出口開口面積A2を同一、又は小さくすることによって、循環流X2の流速が相対的に大きくなり、被処理水と担体12とを槽底部34に沿って強く流し出す。このため、槽底部34に担体12が沈降堆積することを防止することができる。
【0018】
前記循環路32の入口開口面積A1と出口開口面積A2との比が1未満であると、循環流X2の流速を大きくすることができなくなり、槽底部34に担体14が沈降堆積し易くなる。また、上記の比が5を超えると循環流X1に対する循環流X2の流速比率を大きくできるが、循環路32の出口開口での通水抵抗が大きくなって循環路32における循環流量が低下する。
【0019】
上述のように、この第1の実施例によれば他方のエリア18に被処理水と担体12とを槽の側壁28に沿って槽底部34に導く案内板30を設けたので、被処理水と担体12とを槽底部34に沿って強く流し出すことができ、槽底部34に担体12が沈降堆積することを防止することができる。また、循環路32の入口開口面積A1と出口開口面積A2との比が1〜5の範囲、好ましくは1.5〜3の範囲に設定されるので、循環流X2の流速を槽底部34に担体12が沈降堆積しない適度な大きさにできる。また、案内板30はスクリーン24面に対して所定の間隔を有しスクリーン24面と略平行に設けられているので、循環流X1はスクリーン24面に沿って安定な流れを形成し、担体12によるスクリーン24面の洗浄作用が期待できる。また、処理槽内には一方のエリア16と他方のエリア18とを仕切る隔壁14が設けられているので、相互のエリアを短絡する流れを少なくでき、槽全体としてダイナミックな安定した循環流を形成できる。
【0020】
図3は本発明の第2の実施例を示す断面図である。本実施例では被処理水と担体12とを槽の側壁28に沿って槽底部34に導く断面が多角形の案内部材36が設けられている。一方のエリアからの循環流は、他方のエリア18では案内部材36の上端位置で循環流X0と循環流X1に2分される。循環流X1はスクリーン24面及び槽の側壁28に沿って循環路32内を流れ、下部では狭い出口開口面積A2を保持しつつ早い速度の循環流X2が側壁28、コーナー傾斜部38、槽底部34の順に流れる。
【0021】
この第2の実施例によれば、被処理水と担体12とを早い速度の循環流X2で確実に槽底部34に導くような形状とされているので、槽底部34に担体12が沈降堆積することをより確実に防止することができる。
【0022】
図4は本発明の第3の実施例を示す断面図である。本実施例では案内部材である案内板40、42が上下2段に離れて設けられている。一方のエリアからの循環流は他方のエリア18の上部で循環流X0、循環流X1、循環流X3に別れ、循環路32内では循環流X1、循環流X3が合流した後、循環流X2となって槽底部34に向けて流れる。この実施例においても出口開口面積A2が狭くされているので、早い速度の循環流X2が得られ、槽底部34に担体12が沈降堆積することを防止することができる。
【0023】
この第3の実施例によれば、循環流X1が循環路32を流れる過程でスクリーン24から処理水がすり抜けるので、循環流X1の流量がその分減少する。この減少量を循環流X3が補うことになり、循環流X2の流速を安定して維持できる。
【0024】
図5は本発明の第4の実施例を示す断面図である。本実施例では案内板44の上部が一方のエリア16にまで延長され、その端部46が散気装置20を平面的に2分する位置に下向きに設けられている。このため、散気装置20のaゾーンからの上昇流はそのまま循環流X1となって案内板44の外側を通り、bゾーンからの上昇流はそのまま循環流X0となって案内板44の内側を通ることになる。この実施例においても出口開口面積A2が狭くされており、かつ、循環流X1の流量が確実に確保される構造とされているので、早い速度の循環流X2が確実に得られ、槽底部34に担体12が沈降堆積することを確実に防止することができる。
【0025】
なお、図5においては一方のエリア16と他方のエリア18との境界が判然としない。したがって、本実施例では槽10内を仮想線Yで区分し、この仮想線Yの左側である散気装置20が配置された側を一方のエリア16とし、仮想線Yの右側である案内板44の主体部分が配置された側を他方のエリア18として理解するものとし、仮想線Yの位置は適宜左右に移動して理解し得るものとする。また、前掲の図3や図4並びに後掲の図7においても上記と同様の考え方で一方のエリア16と他方のエリア18との境界を仮想し得るものとする。
【0026】
図6は本発明の第5の実施例を示す断面図である。本実施例では案内板48の下部が側壁28と平行に垂下しており、その下端が槽底部34との間で循環路32の出口開口を形成している。この実施例においても出口開口面積A2が狭くされているので、早い速度の循環流X2が確実に得られ、槽底部34に担体12が沈降堆積することを防止することができる。
【0027】
図7は本発明の第6の実施例を示す断面図である。本実施例ではスクリーン24が一方のエリア16の側に設けられ、被処理水は他方のエリア18の側に設けた流入管22から供給され、処理水は一方のエリア16の側に設けた流出管26から排出される。案内板50の下部は傾斜して側壁28との間隔が下方に進にしたがって狭められ、その下端がコーナー傾斜部38との間で循環路32の出口開口を形成している。この実施例においても出口開口面積A2が狭くされているので、早い速度の循環流X2が得られ、槽底部34に担体12が沈降堆積することを防止することができる。
【0028】
図8は本発明の第7の実施例を示す断面図である。本実施例では中心線Zに対して左右対称に構成されている。中心線Zから右側の部分は前掲図1に示した第1の実施例とほぼ同一の構造であり、第1の実施例の場合と同様の循環流を形成して槽底部に担体が沈降堆積することを防止する。また、中心線Zから左側の部分についても、右側の部分と対象の循環流を形成して槽底部に担体が沈降堆積することを防止する。本実施例は被処理水に流量が多い大型の槽に好適である。
【0029】
図9は本発明の第8の実施例を示す案内部材の要部説明図である。
図9(イ)では案内部材52の下端52Aがヒンジ54を介して矢印方向に回動自在にされている。このため、必要な時期に下端52Aを回動させた後、固定することによって、循環路32の出口開口面積A2を最も好ましい値に調整できる。また、図9(ロ)の場合には案内部材56の下端56Aが矢印方向に摺動自在にされている。このため、必要な時期に下端56Aを摺動させた後、固定することによって、循環路32の出口開口面積A2を最も好ましい値に調整できる。
【0030】
図10は本発明の第9の実施例を示す断面図である。本実施例では散気装置20が第1の散気装置58と第2の散気装置60に分離している。第1の散気装置58は槽10の外側(側壁寄り)に配置され、この第1の散気装置58からの上昇流は循環路32を経由する主に外回りの循環流を形成する。また、第2の散気装置60は槽10の内側(中央寄り)に配置され、この第2の散気装置60からの上昇流は循環路32を経由しない主に内回りの循環流を形成する。
【0031】
本実施例では各散気装置用の流量調整弁62、64の開度を調節して、第1の散気装置58に多くの空気を送り込み、第1の散気装置58から散気される空気のリフト作用が、第2の散気装置60のそれよりも大きくなるようにする。このように調整することによって、循環流X1の流量が確実に確保されることになり、早い速度の循環流X2が確実に得られ、槽底部に担体が沈降堆積することを防止することができる。
【0032】
【発明の効果】
上述のとおり、本発明に係る好気性処理槽によれば槽の底部に担体が沈降堆積すること抑えることができる。このため、担体と被処理水との接触効率を向上させることができる。
【図面の簡単な説明】
【図1】本発明の第1の実施例を示す断面図
【図2】図1のD−D矢視図
【図3】本発明の第2の実施例を示す断面図
【図4】本発明の第3の実施例を示す断面図
【図5】本発明の第4の実施例を示す断面図
【図6】本発明の第5の実施例を示す断面図
【図7】本発明の第6の実施例を示す断面図
【図8】本発明の第7の実施例を示す断面図
【図9】本発明の第8の実施例を示す案内部材の要部説明図
【図10】本発明の第9の実施例を示す断面図
【図11】従来技術に係る好気性処理槽の一例を示す断面図
【符号の説明】
10……槽
12……担体
14……隔壁
16……一方のエリア
18……他方のエルア
20……散気装置
24……スクリーン
28……側壁
30……案内板
32……循環路
34……槽底部
36……案内部材
38……コーナー傾斜部
58……第1の散気装置
60……第2の散気装置
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to an aerobic treatment tank, and more particularly to an aerobic treatment tank in which water to be treated and a granular carrier are brought into contact in a fluid state.
[0002]
[Prior art]
FIG. 11 shows an example of an aerobic treatment tank according to a conventional technique. A carrier 12 holding microorganisms is placed in the tank 10. In addition, a partition wall 14 that divides the inside of the tank into two areas in a planar manner is disposed at the center of the tank 10. The upper part and the lower part of the partition wall 14 are missing, and the upper and lower sides communicate with one area 16 and the other area 18. An air diffuser 20 that blows out aeration air upward is installed at the middle position of the area 16.
[0003]
The water to be treated is supplied into the tank 10 from the inflow pipe 22, and the water to be treated is filled with maintaining a constant water level. When the air is blown out from the air diffuser 20 in this state, an upward flow is generated in the water to be treated by the lift action of the blown air, and the water to be treated is circulated clockwise between the areas 16 and 18. A stream X is formed. The carrier 12 also circulates while flowing in the tank 10 on the circulating flow X of the water to be treated.
[0004]
In the process of circulating for a predetermined time while the water to be treated and the carrier 12 are in contact with each other in a fluid state, the water to be treated is purified by the action of the microorganisms held on the carrier 12 under aerobic conditions by the aeration. The treated water passes through the screen 24 for preventing the carrier 12 from flowing out and is discharged out of the tank through the outflow pipe 26.
[0005]
In the aerobic treatment tank, it is important for improving the treatment efficiency that a carrier having a specific gravity as close as possible to the water to be treated is introduced at an appropriate concentration and circulated while being uniformly mixed and contacted with the water to be treated. Since the density of the water to be treated varies depending on the temperature, it is difficult to make the specific gravity of the carrier coincide with that of the water to be treated. For this reason, when a high molecular weight material is used as a raw material for the carrier, a carrier having a specific gravity of about 1.01 to 1.08 is preferably used from the viewpoints of handleability, manufacturing restrictions, cost, and the like. .
[0006]
[Problems to be solved by the invention]
However, it has been found that in this type of aerobic treatment tank, a considerably high level of technology is required to circulate the carrier while being in uniform mixed contact with the water to be treated. That is, according to the inventor's experience, when a carrier having a specific gravity of about 1.01 to 1.08 is used, a phenomenon in which the carrier 12 settles and accumulates at the bottom of the right end of the area 18 as shown in FIG. It was. Such a sedimentation phenomenon of the carrier increases the proportion of the carrier that does not contribute to the reaction, lowers the contact efficiency between the carrier and the water to be treated, and causes the treatment performance to deteriorate. In addition, microorganisms adhering to the sedimented carrier may rot under anaerobic conditions, or the carriers may adhere to each other and cause adverse effects. Furthermore, when the specific gravity of the carrier is about 2.0, such as activated carbon, the sedimentation phenomenon of the carrier becomes even more prominent, and there is a concern that the processing performance may be lowered and trouble in operation may be caused.
[0007]
An object of the present invention is to provide an aerobic treatment tank that improves the above-mentioned problems of the prior art, makes it difficult for the carrier to settle and deposit on the bottom of the tank, and can improve the contact efficiency between the carrier and the water to be treated. It is in.
[0008]
[Means for Solving the Problems]
The present invention relates to an aerobic treatment tank in which water to be treated and a granular carrier having a specific gravity larger than that of the water to be treated are brought into contact with each other in a fluidized state, and a diffuser that blows out air into one area divided in a plane. An apparatus is disposed, and the treated water and the carrier are circulated between the one area and the other area by the lift action of the blown air, and the treated water and the carrier are circulated in the other area. with arranging a screen for separating, said the other area is provided a guide member to separate the circulation flow X 1 of the outer loop along the screen surface in the circulation flow and the circulation flow X 0 of the inward turning, the circulation flow the X 1 along the side wall of the vessel, characterized in that to guide the tank bottom.
[0009]
The ratio of the inlet opening area and the outlet opening area of the circulation path of the circulating flow X 1 is desirably 1 to 5.
[0011]
In the present invention, it is desirable that a partition wall for partitioning the one area and the other area is disposed in the processing tank.
[0012]
Further, the present invention is characterized in that by a deformable lower end of the guide member, the outlet opening area of the circulation path of the circulating flow X 1 is adjustable.
[0013]
In the present invention, the air diffuser arranged in the one area is divided into an outer side and an inner side, and the lift action of the air diffused from the outer air diffuser is adjusted to be larger than that of the inner side. It is desirable that
[0014]
DETAILED DESCRIPTION OF THE INVENTION
Embodiments of the present invention will be described with reference to the drawings. In the drawings shown below, components having the same reference numerals as those in FIG. 11 described above are elements having the same or similar functions as those shown in FIG. 11, and description thereof may be omitted.
[0015]
FIG. 1 is a cross-sectional view showing a first embodiment of the present invention, and FIG. 2 is a view taken along the line DD in FIG. In this embodiment, a guide plate 30 is provided in the other area 18. The guide plate 30 has a predetermined interval with respect to the screen 24 surface and is provided substantially parallel to the screen 24 surface. The lower end of the guide plate 30 extends to a position close to the side wall 28.
[0016]
In the above configuration, the circulating flow X from the area 16 is divided into the circulating flow X 0 and the circulating flow X 1 at the upper end position of the guide plate 30 by the presence of the guide plate 30 in the other area 18. The circulating flow X 0 returns to one area 16 from below the partition wall 14 as an inward flow passing between the partition wall 14 and the guide plate 30.
[0017]
On the other hand, circulation X 1 is partitioned by the guide plate 30, flows downward guide plate 30 and the screen 24 side, the circulation path 32 formed between the side walls 28 along the side wall 28, circulating flow X 2 To the tank bottom 34. The ratio of the inlet opening area A 1 and the outlet opening area A 2 of the circulation path 32 is set to a range of 1 to 5, preferably 1.5 to 3. That is, by making the outlet opening area A 2 the same or smaller than the inlet opening area A 1 , the flow rate of the circulating flow X 2 becomes relatively large, and the water to be treated and the carrier 12 are moved along the tank bottom 34. And flush out strongly. For this reason, it is possible to prevent the carrier 12 from being deposited on the tank bottom 34.
[0018]
If the ratio of the inlet opening area A 1 and the outlet opening area A 2 of the circulation path 32 is less than 1, the flow rate of the circulating flow X 2 cannot be increased, and the carrier 14 is deposited and deposited on the tank bottom 34. It becomes easy. Further, when the ratio exceeds 5, the flow rate ratio of the circulation flow X 2 to the circulation flow X 1 can be increased, but the water flow resistance at the outlet opening of the circulation path 32 increases and the circulation flow rate in the circulation path 32 decreases. To do.
[0019]
As described above, according to the first embodiment, the guide plate 30 that guides the water to be treated and the carrier 12 to the tank bottom 34 along the side wall 28 of the tank is provided in the other area 18. And the carrier 12 can be strongly flowed out along the tank bottom 34, and the carrier 12 can be prevented from being deposited on the tank bottom 34. Further, since the ratio of the inlet opening area A 1 and the outlet opening area A 2 of the circulation path 32 is set in the range of 1 to 5, preferably in the range of 1.5 to 3 , the flow rate of the circulating flow X 2 is set to the tank. The carrier 12 can be of an appropriate size that does not settle and deposit on the bottom 34. Further, since the guide plate 30 has a predetermined interval with respect to the screen 24 surface and is provided substantially parallel to the screen 24 surface, the circulating flow X 1 forms a stable flow along the screen 24 surface, and the carrier 12 can be expected to clean the screen 24 surface. Further, since the partition wall 14 for partitioning the one area 16 and the other area 18 is provided in the processing tank, the flow for short-circuiting each other area can be reduced, and a dynamic and stable circulation flow is formed as the entire tank. it can.
[0020]
FIG. 3 is a sectional view showing a second embodiment of the present invention. In this embodiment, a guide member 36 having a polygonal cross section for guiding the water to be treated and the carrier 12 to the tank bottom 34 along the side wall 28 of the tank is provided. The circulating flow from one area is divided into the circulating flow X 0 and the circulating flow X 1 at the upper end position of the guide member 36 in the other area 18. The circulation flow X 1 flows in the circulation path 32 along the surface of the screen 24 and the side wall 28 of the tank, and at the lower part, the circulation flow X 2 at a high speed maintains the narrow outlet opening area A 2 and the side flow 28 and the corner inclined portion 38. , And flows in the order of the tank bottom 34.
[0021]
According to the second embodiment, since the water to be treated and the carrier 12 are reliably guided to the tank bottom 34 by the circulation flow X 2 at a high speed, the carrier 12 settles on the tank bottom 34. Accumulation can be prevented more reliably.
[0022]
FIG. 4 is a sectional view showing a third embodiment of the present invention. In the present embodiment, guide plates 40 and 42 which are guide members are provided in two separate upper and lower stages. The circulating flow from one area is separated into a circulating flow X 0 , a circulating flow X 1 , and a circulating flow X 3 in the upper part of the other area 18, and after the circulating flow X 1 and the circulating flow X 3 are merged in the circulation path 32. Then, it becomes a circulation flow X 2 and flows toward the tank bottom 34. Also in this embodiment, since the outlet opening area A 2 is narrowed, the circulating flow X 2 at a high speed can be obtained, and the carrier 12 can be prevented from being settled and deposited on the tank bottom 34.
[0023]
According to the third embodiment, the treated water passes through the screen 24 while the circulating flow X 1 flows through the circulating path 32, so the flow rate of the circulating flow X 1 decreases accordingly. This decrease amount is supplemented by the circulation flow X 3 , and the flow velocity of the circulation flow X 2 can be stably maintained.
[0024]
FIG. 5 is a cross-sectional view showing a fourth embodiment of the present invention. In the present embodiment, the upper portion of the guide plate 44 extends to one area 16, and its end 46 is provided downward at a position that bisects the air diffuser 20. For this reason, the upward flow from the a zone of the air diffuser 20 passes through the outside of the guide plate 44 as it is as the circulating flow X 1, and the upward flow from the b zone becomes the circulating flow X 0 as it is. You will pass inside. Also in this embodiment, the outlet opening area A 2 is narrowed and the flow rate of the circulating flow X 1 is reliably ensured, so that a fast circulating flow X 2 can be reliably obtained, It is possible to reliably prevent the carrier 12 from being deposited on the tank bottom 34.
[0025]
In FIG. 5, the boundary between one area 16 and the other area 18 is not obvious. Therefore, in the present embodiment, the inside of the tank 10 is divided by the virtual line Y, the side on which the air diffuser 20 on the left side of the virtual line Y is disposed is set as one area 16, and the guide plate on the right side of the virtual line Y It is assumed that the side on which the main part 44 is arranged is understood as the other area 18, and the position of the virtual line Y can be understood by moving right and left as appropriate. 3 and 4 described above and FIG. 7 described later can assume a boundary between one area 16 and the other area 18 in the same way as described above.
[0026]
FIG. 6 is a cross-sectional view showing a fifth embodiment of the present invention. In the present embodiment, the lower portion of the guide plate 48 hangs down in parallel with the side wall 28, and the lower end thereof forms an outlet opening of the circulation path 32 with the tank bottom portion 34. Also in this embodiment, since the outlet opening area A 2 is narrowed, a high-speed circulation flow X 2 can be obtained with certainty, and the carrier 12 can be prevented from being deposited on the tank bottom 34.
[0027]
FIG. 7 is a cross-sectional view showing a sixth embodiment of the present invention. In this embodiment, the screen 24 is provided on the one area 16 side, the water to be treated is supplied from the inflow pipe 22 provided on the other area 18 side, and the treated water is discharged on the one area 16 side. It is discharged from the tube 26. The lower portion of the guide plate 50 is inclined so that the distance from the side wall 28 is gradually reduced, and the lower end thereof forms an outlet opening of the circulation path 32 with the corner inclined portion 38. Also in this embodiment, since the outlet opening area A 2 is narrowed, the circulating flow X 2 at a high speed can be obtained, and the carrier 12 can be prevented from being settled and deposited on the tank bottom 34.
[0028]
FIG. 8 is a cross-sectional view showing a seventh embodiment of the present invention. In this embodiment, it is configured symmetrically with respect to the center line Z. The portion on the right side from the center line Z has substantially the same structure as that of the first embodiment shown in FIG. 1, and the carrier is settled and deposited on the bottom of the tank by forming a circulating flow similar to the case of the first embodiment. To prevent. Further, the left part from the center line Z also forms a target circulation flow with the right part to prevent sedimentation and deposition of the carrier on the bottom of the tank. This embodiment is suitable for a large tank having a large flow rate for water to be treated.
[0029]
FIG. 9 is an explanatory view of a main part of a guide member showing an eighth embodiment of the present invention.
In FIG. 9A, the lower end 52A of the guide member 52 is rotatable in the direction of the arrow through a hinge 54. For this reason, the outlet opening area A 2 of the circulation path 32 can be adjusted to the most preferable value by rotating and fixing the lower end 52A at a necessary time. In the case of FIG. 9B, the lower end 56A of the guide member 56 is slidable in the direction of the arrow. For this reason, the outlet opening area A 2 of the circulation path 32 can be adjusted to the most preferable value by sliding and fixing the lower end 56A at a necessary time.
[0030]
FIG. 10 is a cross-sectional view showing a ninth embodiment of the present invention. In this embodiment, the air diffuser 20 is separated into a first air diffuser 58 and a second air diffuser 60. The first air diffuser 58 is disposed on the outside (close to the side wall) of the tank 10, and the upward flow from the first air diffuser 58 mainly forms an external circulation flow via the circulation path 32. Further, the second air diffuser 60 is disposed on the inner side (near the center) of the tank 10, and the upward flow from the second air diffuser 60 mainly forms an inward circulation flow that does not pass through the circulation path 32. .
[0031]
In the present embodiment, the opening degree of the flow rate adjusting valves 62 and 64 for each air diffuser is adjusted, a large amount of air is sent to the first air diffuser 58, and air is diffused from the first air diffuser 58. The lift action of air is made larger than that of the second air diffuser 60. By adjusting in this way, the flow rate of the circulating flow X 1 is surely ensured, and the circulating flow X 2 at a high speed is surely obtained, and the carrier is prevented from sedimentation and accumulation at the bottom of the tank. Can do.
[0032]
【The invention's effect】
As described above, according to the aerobic treatment tank according to the present invention, it is possible to prevent the carrier from being deposited on the bottom of the tank. For this reason, the contact efficiency of a support | carrier and to-be-processed water can be improved.
[Brief description of the drawings]
FIG. 1 is a sectional view showing a first embodiment of the present invention. FIG. 2 is a sectional view taken along the line DD in FIG. 1. FIG. 3 is a sectional view showing a second embodiment of the invention. FIG. 5 is a cross-sectional view showing a fourth embodiment of the present invention. FIG. 6 is a cross-sectional view showing a fifth embodiment of the present invention. FIG. 8 is a cross-sectional view showing a seventh embodiment of the present invention. FIG. 9 is an explanatory view of a main part of a guide member showing an eighth embodiment of the present invention. Sectional view showing a ninth embodiment of the present invention. FIG. 11 is a sectional view showing an example of an aerobic treatment tank according to the prior art.
DESCRIPTION OF SYMBOLS 10 ... Tank 12 ... Carrier 14 ... Bulkhead 16 ... One area 18 ... The other ELER 20 ... Air diffuser 24 ... Screen 28 ... Side wall 30 ... Guide plate 32 ... Circulation path 34 ... ... tank bottom 36 ... guide member 38 ... corner inclined part 58 ... first air diffuser 60 ... second air diffuser

Claims (2)

被処理水とこの被処理水よりも比重が大きい粒状の担体とを流動状態で接触させる好気性処理槽において、槽内を平面的に区分した一方のエリアに空気を吹き出す散気装置を配置し、この吹き出された空気のリフト作用によって前記被処理水と担体とを前記一方のエリアと他方のエリアとの間に循環させ、前記他方のエリアには前記被処理水と担体とを分離するためのスクリーンを配設するとともに、前記他方のエリアには循環流を内回りの循環流Xと前記スクリーン面に沿った外回りの循環流Xに分ける案内部材を設け、前記循環流Xを槽の側壁に沿って槽底部に導くようにしたことを特徴とする好気性処理槽。In an aerobic treatment tank in which the water to be treated and a granular carrier having a specific gravity greater than that of the water to be treated are brought into contact in a fluid state, an air diffuser that blows out air is arranged in one area that is divided in a plane. In order to circulate the treated water and the carrier between the one area and the other area by the lift action of the blown air, and to separate the treated water and the carrier in the other area bath with said the other area is provided a guide member to separate the circulation flow X 1 of the outer loop along the screen surface in the circulation flow and the circulation flow X 0 of the inward turning, the circulation flow X 1 to dispose the screen An aerobic treatment tank characterized by being guided to the bottom of the tank along the side wall. 前記案内部材の下端を変形自在にすることによって、前記循環流Xの循環路の出口開口面積が調整可能にされたことを特徴とする請求項1に記載の好気性処理槽。The aerobic treatment tank according to claim 1, wherein an outlet opening area of the circulation path of the circulation flow X 1 is adjustable by making the lower end of the guide member deformable.
JP2000056997A 2000-03-02 2000-03-02 Aerobic treatment tank Expired - Lifetime JP3692893B2 (en)

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KR100456087B1 (en) * 2002-03-20 2004-11-06 유한회사 그린환경 Aeration apparatus for sewage treatment plant
CN101076498B (en) * 2004-11-22 2012-06-06 努比亚水系统有限公司 A kind of ventilation type biological filtration system and its wastewater treatment method
JP4994349B2 (en) * 2008-12-01 2012-08-08 メタウォーター株式会社 Nitrification carrier circulation method in deep tank aeration tank
KR101337620B1 (en) 2010-11-29 2013-12-06 유한회사 그린환경 Aeration apparatus for sewage treatment and operation methods of the same
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