JP2547290Y2 - Wastewater treatment equipment - Google Patents

Wastewater treatment equipment

Info

Publication number
JP2547290Y2
JP2547290Y2 JP1991079811U JP7981191U JP2547290Y2 JP 2547290 Y2 JP2547290 Y2 JP 2547290Y2 JP 1991079811 U JP1991079811 U JP 1991079811U JP 7981191 U JP7981191 U JP 7981191U JP 2547290 Y2 JP2547290 Y2 JP 2547290Y2
Authority
JP
Japan
Prior art keywords
filter medium
water
partition plate
layer
wastewater treatment
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.)
Expired - Lifetime
Application number
JP1991079811U
Other languages
Japanese (ja)
Other versions
JPH0522097U (en
Inventor
範晴 星
知行 山下
Original Assignee
株式会社西原環境衛生研究所
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 株式会社西原環境衛生研究所 filed Critical 株式会社西原環境衛生研究所
Priority to JP1991079811U priority Critical patent/JP2547290Y2/en
Publication of JPH0522097U publication Critical patent/JPH0522097U/en
Application granted granted Critical
Publication of JP2547290Y2 publication Critical patent/JP2547290Y2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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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)

Description

【考案の詳細な説明】[Detailed description of the invention]

【0001】[0001]

【産業上の利用分野】この考案は、有機物あるいは窒素
成分を含む廃水などの被処理水を生物学的に濾過する廃
水処理装置に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a wastewater treatment apparatus for biologically filtering water to be treated such as wastewater containing organic substances or nitrogen components.

【0002】[0002]

【従来の技術】図2は、従来の廃水処理装置を示す構成
図であり、図において1は、断面が円形又は矩形の槽、
2bは比重が1.0よりも大きな濾材bの層、3は廃水
(被処理水)、4は逆洗気体を送り出す逆洗ブロワ、5
は濾材bに酸素を供給する曝気ブロワ、6は逆洗水を送
り出す逆洗ポンプ、7は逆洗排水槽、8は処理水槽であ
る。廃水等の被処理水中に含まれる有機物の除去として
のバイオフィルタは、微生物膜を付着させた比重が1.
0よりも大きな例えばセラミックのような濾材bを槽1
内の仕切板9上に配置し、廃水3を上部から流入させ前
記濾材bに着生した微生物膜の働きによって、廃水3中
の有機物を生物学的に分解除去している。
2. Description of the Related Art FIG. 2 is a block diagram showing a conventional wastewater treatment apparatus, in which 1 is a tank having a circular or rectangular cross section.
2b is a layer of the filter medium b having a specific gravity larger than 1.0, 3 is waste water (water to be treated), 4 is a backwash blower for sending backwash gas, and 5
Is an aeration blower for supplying oxygen to the filter medium b, 6 is a backwash pump for sending backwash water, 7 is a backwash drain tank, and 8 is a treated water tank. A biofilter for removing organic matter contained in water to be treated such as wastewater has a specific gravity of 1.
A filter medium b larger than 0, such as ceramic,
The organic matter in the wastewater 3 is biologically decomposed and removed by the action of the microbial membrane deposited on the filter medium b by allowing the wastewater 3 to flow in from above and disposed on the inner partition plate 9.

【0003】しかしながら、廃水3の処理を継続すると
微生物の肥大化、廃水3中の懸濁物質の堆積等により、
前記濾材bの層2bが目詰まりを起こし、所定の通水量
が確保出来なくなったり、好気性微生物処理の場合は微
生物の嫌気化が発生したりして処理水質が悪化するの
で、洗浄操作を行っている。
[0003] However, if the treatment of the wastewater 3 is continued, the microorganisms will enlarge and the suspended solids in the wastewater 3 will accumulate.
The layer 2b of the filter medium b is clogged, and a predetermined amount of water cannot be secured. ing.

【0004】次に動作について説明する。廃水3の最高
水位をHWL、最低水位をLWLとする。水位がLWL
からHWL迄変化し、HWLになると、濾材bの層2b
の下部から、逆洗ブロワ4により逆洗気体を、逆洗ポン
プ6により逆洗水を流入して、濾材bの層2bの目詰ま
りを解消する、いわゆる洗浄操作を行っている。
Next, the operation will be described. The highest level of the wastewater 3 is HWL, and the lowest level is LWL. Water level is LWL
From HWL to HWL, and when HWL is reached, the layer 2b of the filter medium b
A backwashing blower 4 and a backwashing pump 6 flow backwash gas from the lower portion of the filter medium b, thereby performing a so-called washing operation for eliminating clogging of the layer 2b of the filter medium b.

【0005】[0005]

【考案が解決しようとする課題】従来の廃水処理装置は
以上のように構成されているので、濾材bの層2bの洗
浄に際し、濾材層を円滑に流動化させる為には、相当大
きな流速の水及び/又は空気が必要であり、大きな動力
が消費される。そのため濾材bの層の厚さに限界があ
り、従って、1)水深が浅く曝気による酸素溶解効率が
低い、2)濾過速度が遅い、3)処理継続時間が短か
い、4)高濃度排水に対応できない等の課題があった。
Since the conventional wastewater treatment apparatus is constructed as described above, a considerably large flow rate is required to smoothly fluidize the filter medium layer when washing the layer 2b of the filter medium b. Requires water and / or air and consumes significant power. Therefore, there is a limit to the thickness of the layer of the filter medium b. Therefore, 1) the water depth is low and the oxygen dissolving efficiency by aeration is low, 2) the filtration speed is slow, 3) the treatment duration is short, and 4) high-concentration wastewater is discharged. There were issues such as inability to respond.

【0006】この考案は上記のような課題を解消するた
めになされたもので、処理性能を向上するとともに洗浄
に要する動力を少なくし、かつ装置自体を縮小すること
ができる廃水処理装置を得ることを目的とする。
SUMMARY OF THE INVENTION The present invention has been made to solve the above-mentioned problems, and an object of the present invention is to provide a wastewater treatment apparatus capable of improving the processing performance, reducing the power required for cleaning, and reducing the size of the apparatus itself. With the goal.

【0007】[0007]

【課題を解決するための手段】この考案に係る廃水処理
装置は、比重が1.0よりも小さくて、被処理水中で浮
上する層と比重が1.0よりも大きくて、槽内下部に形
成する層の2層の濾材槽に分離し、しかも仕切板により
上部の濾材と下部の濾材は決して混わらないように構成
した。
The wastewater treatment apparatus according to the present invention has a specific gravity of less than 1.0, a layer floating in the water to be treated, and a specific gravity of more than 1.0. The filter medium was separated into two layers of filter medium tanks to be formed, and the upper filter medium and the lower filter medium were never mixed by a partition plate.

【0008】又、分割した濾材2層の間に、下層の濾材
が通過しない仕切板を槽側面全体、あるいは部分的に配
置し、前記仕切板を通過した排水を逆洗排水槽に流出す
る排水口と、該排水口の開閉調節をする排水口弁を備え
たものである。
In addition, a partition plate through which the lower filter medium does not pass is disposed on the whole or part of the tank side between the two divided filter media layers, and the wastewater passing through the partition plate flows into the backwash drain tank. It has a mouth and a drain valve for opening and closing the drain.

【0009】[0009]

【作用】この考案における廃水処理装置は、特に高濃度
排水を大量に効率良く濾過処理し、濾過処理が速く、継
続時間を長くすることができる。
The wastewater treatment apparatus according to the present invention can efficiently and efficiently filter particularly high-concentration wastewater in a large amount, so that the filtration process is fast and the duration is long.

【0010】上部の濾材の洗浄は、排水口を開にして、
抜水するだけで可能であり、又、下部の濾材の洗浄は、
上部の濾材部の廃水を抜水した状態で行うことができる
[0010] To clean the upper filter medium, open the drain port,
It is possible only by draining water.
Can be performed with drainage of wastewater from upper filter media

【0011】[0011]

【実施例】以下、この考案の一実施例を図について図2
の従来の装置と同一の部分については省略して説明す
る。図1において、2aは比重が1.0よりも小さな濾
材aの層、2bは比重が1.0よりも大きな濾材bの層
であり、濾材aの層2aは仕切板A(9a)で支持さ
れ、濾材bの層2bは仕切板B(9b)で支持されてい
る。仕切板A(9a)により、濾材aと濾材bは決して
混わらない。9cは濾材bの層2bの上面より上で、前
記仕切板A(9a)よりも下に位置し、槽側面体あるい
は部分的に配置され、水は通過し、かつ、前記濾材bは
通過しない多孔的な構造の仕切板C、10は仕切板C
(9c)を通過した排水を逆洗排水槽7に流出する排水
口、11は排水口10の開閉調節をする排水口弁であ
る。運転中の水位は、濾材aの槽2aの上面より廃水の
最低水位LWLが低くなった処理水位範囲X,Y及び大
型化して、最低水位LWLの時に、既に濾材aの槽2a
の下面が仕切板A(9a)から浮上した処理水位範囲Z
等の範囲で運転できるように、処理水槽8に設けられた
水位調整ゲ−ト12で任意に調整する。
BRIEF DESCRIPTION OF THE DRAWINGS FIG.
The description of the same parts as those of the conventional apparatus will be omitted. In FIG. 1, 2a is a layer of a filter medium a having a specific gravity of less than 1.0, 2b is a layer of a filter medium b having a specific gravity of more than 1.0, and a layer 2a of the filter medium a is supported by a partition plate A (9a). The layer 2b of the filter medium b is supported by the partition plate B (9b). The filter medium a and the filter medium b are never mixed by the partition plate A (9a). 9c is located above the upper surface of the layer 2b of the filter medium b and below the partition plate A (9a), is disposed on the tank side surface or partially, and allows water to pass through and does not pass through the filter medium b. The partition plate C having a porous structure and the partition plate 10 are
A drain port 11 for draining the drain water passing through (9c) into the backwash drain tank 7 is a drain valve for opening and closing the drain port 10. During operation, the water level ranges X and Y where the minimum water level LWL of the wastewater is lower than the upper surface of the tank 2a of the filter medium a, and the water level is increased, and the tank 2a of the filter medium a is already at the minimum water level LWL.
Water level range Z in which the lower surface of the surface floats from the partition plate A (9a)
The water level is adjusted arbitrarily by a water level adjusting gate 12 provided in the treated water tank 8 so that the operation can be performed within the range of the above.

【0012】次に動作について説明する。濾材aのみの
洗浄は、仕切板A(9a)を設けたことにより、排水口
弁11を開にして、抜水するだけで可能である。
Next, the operation will be described. Washing of only the filter medium a can be performed only by opening the drain valve 11 and draining water by providing the partition plate A (9a).

【0013】濾材bの洗浄は、濾材bの層2bの下部か
ら、逆洗ブロワ4による逆洗気体を一定時間、送出した
あと、逆洗気体と共に逆洗ポンプ6による逆洗水を流入
し、一定時間オ−バ−ラップした後、逆洗気体の送出を
停止し、逆洗水のみの流入を行う。すなわち1)逆洗気
体送出工程、2)逆洗気体・逆洗水流工程、3)逆洗水
流入工程からなる。なお全工程中、排水口弁11は開の
状態にしておく。
In the washing of the filter medium b, a backwash gas from the backwash blower 4 is sent out from the lower portion of the layer 2b of the filter medium b for a certain period of time, and then backwash water from the backwash pump 6 flows together with the backwash gas. After overlapping for a certain period of time, the delivery of the backwash gas is stopped and only the backwash water flows. That is, there are 1) a backwash gas sending step, 2) a backwash gas / backwash water flow step, and 3) a backwash water inflow step. During the entire process, the drain valve 11 is kept open.

【0014】以上のように、洗浄のための逆洗水・逆洗
気体用の動力としては、濾材bのためのもののみでよ
く、しかも濾材2層(濾材aは浮遊している為、処理水
位範囲が広い)により、水深が深く曝気による酸素溶解
効率が高く、かつ濾過速度が速く、さらに処理継続時間
が長く、特に高濃度廃水に効果がある。
As described above, the power for backwash water / backwash gas for washing only needs to be for the filter medium b, and two layers of the filter medium (since the filter medium a is floating, (Wide range of water level is wide), the water depth is deep, the oxygen dissolving efficiency by aeration is high, the filtration speed is high, and the treatment duration is long.

【0015】[0015]

【考案の効果】以上のように、この発明によれば、被処
理水中浮上した濾材aの層2aと下部の濾材bの層2b
の2層を形成し、しかも仕切板により濾材aと濾材bは
決して混わらないように構成したので、水深を深くする
ことが出来、曝気による酸素溶解効率が高く、かつ、濾
過速度が速く、さらに処理継続時間を長くすることが出
来、処理性能を向上させることができる効果がある。
As described above, according to the present invention, the layer 2a of the filter medium a and the layer 2b of the lower filter medium b floated in the water to be treated.
Since the filter medium a and the filter medium b are never mixed by the partition plate, the water depth can be increased, the oxygen dissolving efficiency by aeration is high, and the filtration speed is high. Further, there is an effect that the processing continuation time can be lengthened and the processing performance can be improved.

【0016】又、濾材2層の間に、濾材bが通過しない
仕切板と排水口を設けることにより、濾材aの洗浄は、
排水口を開にして、抜水するだけで可能であり、洗浄の
ための濾材a用逆洗水・逆洗気体用の動力は不要であ
り、処理能力に比較し、省パワーとなる効果がある。
Further, by providing a partition plate and a drain port through which the filter medium b does not pass between the two layers of the filter medium, the filter medium a can be washed.
It is possible only by opening the drain port and draining water. Power for backwash water and backwash gas for the filter medium a for cleaning is unnecessary, and the effect of power saving compared with the processing capacity is achieved. is there.

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

【図1】この考案の一実施例による廃水処理装置を示す
構成図である。
FIG. 1 is a configuration diagram showing a wastewater treatment apparatus according to an embodiment of the present invention.

【図2】従来の廃水処理装置を示す構成図である。FIG. 2 is a configuration diagram showing a conventional wastewater treatment device.

【符号の説明】[Explanation of symbols]

1 槽 2b 濾材bの層 3 廃水(被処理水) 7 逆洗排水槽 9a 仕切板A 9b 仕切板B 9c 仕切板C 10 排水口 11 排水口弁 Reference Signs List 1 tank 2b layer of filter medium b 3 wastewater (water to be treated) 7 backwash drainage tank 9a partition plate A 9b partition plate B 9c partition plate C 10 drain port 11 drain valve

Claims (2)

(57)【実用新案登録請求の範囲】(57) [Scope of request for utility model registration] 【請求項1】 微生物をその表面に着生させた濾材を槽
内1に充填して、濾材層を形成し、当該濾材層に被処理
水を流入して、被処理水を生物学的に濾過する廃水処理
装置において、比重が1.0よりも小さくて、前記被処
理水中で浮上し、上部の層を形成する濾材aと、比重が
1.0よりも大きくて、前記槽内下部に、仕切板Bで支
持され下部の層を形成する濾材bと、前記濾材aと前記
濾材bを仕切り、水及び空気は通過する仕切板Aとを備
えた廃水処理装置。
1. A filter medium on which microorganisms have formed on its surface is filled in a tank 1, a filter medium layer is formed, and water to be treated flows into the filter medium layer, and the water to be treated is biologically separated. In the wastewater treatment apparatus for filtering, the specific gravity is smaller than 1.0, the filter medium a which floats in the water to be treated and forms an upper layer, and the specific gravity is larger than 1.0, and A wastewater treatment apparatus comprising: a filter medium b supported by a partition plate B to form a lower layer; and a partition plate A that partitions the filter medium a and the filter medium b and through which water and air pass.
【請求項2】 濾材bの層の上面より上で、前記仕切板
Aより下に位置し、槽側面全体、あるいは部分的に配置
され、水は通過し、かつ、前記濾材bは通過しない多孔
的な構造の仕切板Cと、前記仕切板Cを通過した排水を
逆洗排水槽7に流出する排水口と、前記排水口の開閉調
節をする排水口弁とを備えたことを特徴とする請求項第
1項記載の廃水処理装置。
2. A porous member which is located above the upper surface of the layer of the filter medium b and below the partition plate A, and is disposed entirely or partially on the side of the tank, and allows water to pass therethrough and does not allow the filter medium b to pass therethrough. Plate C having a conventional structure, a drain port for draining the drain water passing through the partition plate C to the backwash drain tank 7, and a drain valve for opening and closing the drain port. The wastewater treatment device according to claim 1.
JP1991079811U 1991-09-06 1991-09-06 Wastewater treatment equipment Expired - Lifetime JP2547290Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1991079811U JP2547290Y2 (en) 1991-09-06 1991-09-06 Wastewater treatment equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1991079811U JP2547290Y2 (en) 1991-09-06 1991-09-06 Wastewater treatment equipment

Publications (2)

Publication Number Publication Date
JPH0522097U JPH0522097U (en) 1993-03-23
JP2547290Y2 true JP2547290Y2 (en) 1997-09-10

Family

ID=13700598

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1991079811U Expired - Lifetime JP2547290Y2 (en) 1991-09-06 1991-09-06 Wastewater treatment equipment

Country Status (1)

Country Link
JP (1) JP2547290Y2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2012004893A1 (en) * 2010-07-09 2012-01-12 小川 弘 Wastewater treatment device
JP2015142885A (en) * 2014-01-31 2015-08-06 三菱重工業株式会社 Biofilm filter device, desalination system, and method for cleaning biofilm filter device

Also Published As

Publication number Publication date
JPH0522097U (en) 1993-03-23

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