JP2001310193A - Sewage treatment apparatus - Google Patents

Sewage treatment apparatus

Info

Publication number
JP2001310193A
JP2001310193A JP2000133473A JP2000133473A JP2001310193A JP 2001310193 A JP2001310193 A JP 2001310193A JP 2000133473 A JP2000133473 A JP 2000133473A JP 2000133473 A JP2000133473 A JP 2000133473A JP 2001310193 A JP2001310193 A JP 2001310193A
Authority
JP
Japan
Prior art keywords
carrier
tank
water
filtration
filter
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.)
Granted
Application number
JP2000133473A
Other languages
Japanese (ja)
Other versions
JP4198299B2 (en
Inventor
Takahiro Sakatani
孝宏 酒谷
Osamu Tsuchida
理 土田
Hiroshi Yamazaki
宏史 山崎
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.)
AMUZU KK
Original Assignee
AMUZU 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 AMUZU KK filed Critical AMUZU KK
Priority to JP2000133473A priority Critical patent/JP4198299B2/en
Publication of JP2001310193A publication Critical patent/JP2001310193A/en
Application granted granted Critical
Publication of JP4198299B2 publication Critical patent/JP4198299B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related 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

Abstract

PROBLEM TO BE SOLVED: To provide a means for simply lowering the water level of a carrier filter tank at the time of washing of a filter carrier and a carrier separator hard to block up, capable of obtaining stable separation action and good in workability at the time of maintenance, in a sewage treatment apparatus using a carrier on which microorganisms are fixed. SOLUTION: At the time of washing of a filter carrier, the water level in an upstream tank positioned on the upstream side of the carrier filter tank is lowered by the forcible transfer of the filter carrier and the treated water in the carrier filter tank is transferred to the upstream tank to lower the water level in the carrier filter tank and, thereafter, the filter carrier in the carrier filter tank is washed. The surface of the filter screen of the carrier separator is arranged at the central part in the vicinity of the water surface of the tank in parallel to the water flow at the water surface part of the revolving flow in the carrier filter tank at an angle of 30<-<90 deg. with respect to the horizontal surface. Since the surface of the screen is arranged at the central part in the vicinity of the water surface, visual confirmation is easily performed and cleaning work by a brush, or the like, is easy.

Description

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

【0001】[0001]

【発明の属する技術分野】この発明は、汚水処理装置に
関し、特に移送汚水からの担体の分離と濾過担体を充填
した担体濾過槽の担体の洗浄に特徴のある上記装置に関
するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a sewage treatment apparatus and, more particularly, to the above-mentioned apparatus characterized by separating a carrier from transferred sewage and washing a carrier in a carrier filtration tank filled with a filtration carrier.

【0002】[0002]

【従来の技術】担体濾過槽に充填した濾過担体で固形物
を除去する場合、長期間の運転により濾過担体が閉塞す
るおそれがある。通常これを防止するため、定期的に濾
過担体を洗浄し、濾過した固形物を除去する必要がある
が、曝気または機械撹拌により担体を洗浄すれば、槽内
水面が上昇し、分離した固形物が次槽へ移流するおそれ
がある。次槽への移流を防止するため、一般には担体濾
過槽の水位を予め低下させておき、次に洗浄を行ってい
る。
2. Description of the Related Art When removing solids with a filter carrier filled in a carrier filter tank, the filter carrier may be clogged by long-term operation. Normally, to prevent this, it is necessary to periodically wash the filtration carrier and remove the filtered solids, but if the carrier is washed by aeration or mechanical stirring, the water level in the tank rises and the separated solids May be transferred to the next tank. In general, in order to prevent advection to the next tank, the water level in the carrier filtration tank is lowered in advance, and then washing is performed.

【0003】従来、担体濾過槽の水位を低下させる手段
として、緩衝室を槽内に設けておき、水位低下に見合う
容量を一時ストックする構造が実用されている。
Hitherto, as a means for lowering the water level of a carrier filtration tank, a structure has been put to practical use in which a buffer chamber is provided in the tank and a capacity corresponding to the water level drop is temporarily stored.

【0004】図6は、緩衝室として水面下にエアタンク
25を設けておき、洗浄前にタンク内の空気を槽内の汚
水と置換することにより、水位を下げる構造の例であ
る。エアタンクが水面下にあり、水位低下の必要のない
時間帯は、常に浮力が発生しており、エアタンクの固定
部に強度が求められる。
FIG. 6 shows an example of a structure in which an air tank 25 is provided below the water surface as a buffer chamber, and the water level is lowered by replacing the air in the tank with sewage in the tank before washing. When the air tank is below the surface of the water and there is no need to lower the water level, buoyancy is constantly generated, and strength is required for the fixed portion of the air tank.

【0005】流量調整部を備えた汚水処理装置であれ
ば、流量調整部を緩衝室として用いることができる。流
量調整部が満水にならない時間帯に担体濾過槽内の処理
水を流量調整部に移動し、担体濾過槽の水位を低下させ
て濾過担体の洗浄を行なう。これは余分な構造を槽内に
設ける必要がないが、流量調整部を備えた汚水処理装置
でなければ採用し難い。
In a sewage treatment apparatus provided with a flow rate adjusting section, the flow rate adjusting section can be used as a buffer chamber. During the time when the flow control unit is not full, the treated water in the carrier filtration tank is moved to the flow control unit to lower the water level in the carrier filtration tank to wash the filtration support. It is not necessary to provide an extra structure in the tank, but it is difficult to adopt this unless the sewage treatment apparatus has a flow rate adjusting unit.

【0006】また、担体反応槽に充填される担体は浮遊
・流動しており、次槽、例えば上記担体濾過槽へ処理水
のみを移送するために、濾過スクリーンを備えた担体分
離装置が必要不可欠である。従来、担体分離装置の濾過
スクリーンは、水平面に対して垂直または水平面とほぼ
同角度をもつもの、上向流から水平流または水平流から
下向流に転ずる途中の斜向流に平行に配置したものなど
が採用されている。
Further, the carrier to be filled in the carrier reaction tank is floating and flowing, and a carrier separation device equipped with a filtration screen is indispensable for transferring only the treated water to the next tank, for example, the carrier filtration tank. It is. Conventionally, a filtration screen of a carrier separation device has a filter screen that is perpendicular to the horizontal plane or has substantially the same angle as the horizontal plane, and is arranged in parallel to the oblique flow on the way from the upward flow to the horizontal flow or from the horizontal flow to the downward flow. Things have been adopted.

【0007】担体分離装置のスクリーン面を垂直に配置
すると、旋回流とスクリーン面とがクロスフローとな
り、スクリーン面は常に流れにより洗浄されて目詰まり
を軽減できるが、一方でメンテナンス時には視線とスク
リーン面とが同一方向になるため、上部からのスクリー
ン面の目視確認が困難である。
When the screen surface of the carrier separation device is vertically arranged, the swirling flow and the screen surface cross-flow, and the screen surface is constantly washed by the flow to reduce clogging. Are in the same direction, it is difficult to visually check the screen surface from above.

【0008】一方、スクリーン面を上向流から水平流ま
たは水平流から下向流に転ずる途中の斜向流に平行に配
置したものは、スクリーン面が水流に対し平行となって
おり、前記の従来構造と同様にクロスフローにより目詰
まりを防止しているが、斜向流が得られる部位は比較的
槽の側部であり、通常は槽の上部中央に設けられる開口
からのメンテナンスに支障をきたす場合がある。
On the other hand, when the screen surface is arranged parallel to the oblique flow in the course of turning from the upward flow to the horizontal flow or from the horizontal flow to the downward flow, the screen surface is parallel to the water flow. As with the conventional structure, clogging is prevented by cross flow, but the oblique flow is obtained relatively on the side of the tank, which usually hinders maintenance from the opening provided in the upper center of the tank. May be harmful.

【0009】[0009]

【発明が解決しようとする課題】本発明は、従来の技術
に見られた構造上の問題点や装置上の制約を排し、簡便
な方法で濾過担体洗浄時の担体濾過槽の水位を低下させ
る手段を提供することを第1の課題としている。
DISCLOSURE OF THE INVENTION The present invention eliminates the structural problems and the restrictions on the apparatus found in the prior art, and reduces the water level of the carrier filtration tank during the filtration carrier washing by a simple method. It is a first object to provide a means for causing this to occur.

【0010】本発明の第2の課題は、従来の担体分離装
置に見られたメンテナンス上の問題点を解決し、閉塞し
難く安定した分離作用が得られ、メンテナンス時の作業
性も良好な担体分離装置を提供することである。
[0010] A second object of the present invention is to solve the problem of maintenance in the conventional carrier separation device, to obtain a carrier which is hardly clogged, has a stable separation action, and has good workability during maintenance. It is to provide a separating device.

【0011】[0011]

【課題を解決するための手段】上記第1の課題を解決す
るため、本発明では、強制移送により汚水処理の流れの
上流側に位置する前槽6の水位を下げ、次いで担体濾過
槽8内の処理水を上流側に位置する槽5、6に移送して
担体濾過槽の水位を低下させ、その後担体濾過槽内の濾
過担体の洗浄を行なうことを特徴としている。
In order to solve the above-mentioned first problem, according to the present invention, the water level of the front tank 6 located on the upstream side of the flow of the sewage treatment is lowered by forced transfer. Is transferred to tanks 5 and 6 located on the upstream side to lower the water level in the carrier filtration tank, and thereafter, the filtration carrier in the carrier filtration tank is washed.

【0012】上記手段では、濾過担体の洗浄に必要な空
間を得るための緩衝室を処理流れの上流側にある前槽6
の液面を低下させることにより作り出し、ここに担体濾
過槽の処理水を貯留することにより、担体濾過槽の水位
を低下させて洗浄を行う。これにより、簡便なシステム
で洗浄時の水面の盛り上がりによる固形物の次槽への移
流を防止できる。
In the above means, a buffer chamber for obtaining a space necessary for washing the filter carrier is provided in the front tank 6 upstream of the processing flow.
The cleaning is performed by lowering the liquid level of the carrier filtration tank and storing the treated water in the carrier filtration tank to lower the water level in the carrier filtration tank. This makes it possible to prevent the solid material from flowing to the next tank due to the swelling of the water surface during washing with a simple system.

【0013】上記手段によれば、エアタンク等の構造物
が不要であり、更に流量調整槽を持たない汚水処理装置
にも適用が可能である。
According to the above-mentioned means, a structure such as an air tank is not required, and the present invention can be applied to a sewage treatment apparatus having no flow rate adjusting tank.

【0014】また上記第2の課題を解決するため、本発
明では、担体分離装置の濾過スクリーン面21を槽の水
面付近の中央部に配置し、槽内の旋回流の水面部分にお
ける水流の方向と直交する水平面に対して30度を越
え、かつ90度未満の角度で濾過スクリーン24を設置
している。
In order to solve the second problem, according to the present invention, the filtration screen surface 21 of the carrier separating device is disposed at a central portion near the water surface of the tank, and the direction of the water flow in the water surface portion of the swirling flow in the tank. The filtration screen 24 is installed at an angle of more than 30 degrees and less than 90 degrees with respect to a horizontal plane orthogonal to the above.

【0015】上記構造の担体分離装置は、水面付近中央
部に配置されるため、上部開口からの閉塞状況等の目視
確認が行いやすく、またブラシ等によるスクリーン面の
掃除の際にも作業が容易である。更に、既製品の配管部
材等で製造する場合には、水平にスクリーン面を設ける
場合に比べ、スクリーン面積を大きくできるため、単位
面積あたりの透過水量を低く設定でき、これにより安定
した分離作用と閉塞防止作用が発揮される。
Since the carrier separation device having the above structure is arranged in the center near the water surface, it is easy to visually check the state of blockage from the upper opening, and the work is easy when cleaning the screen surface with a brush or the like. It is. Furthermore, in the case of manufacturing with a ready-made pipe member or the like, since the screen area can be increased as compared with the case where the screen surface is provided horizontally, the amount of permeated water per unit area can be set low, thereby achieving a stable separation action. The effect of preventing blockage is exhibited.

【0016】担体反応槽では曝気によりまず上昇流が起
こり、次いで水面付近では水平流、そして徐々に下向流
に転ずる旋回流が形成されている。担体分離装置は水面
付近の中央部に位置しており、水平流によりスクリーン
面が洗浄され目詰まりを起こしにくい構造となってい
る。
In the carrier reaction tank, an upward flow is first generated by aeration, and then a horizontal flow is formed near the water surface, and a swirling flow gradually turning downward is formed. The carrier separating device is located at the center near the water surface, and has a structure in which the screen surface is washed by the horizontal flow and is hardly clogged.

【0017】[0017]

【発明の実施の形態】以下、図1ないし図3に示す実施
例を参照して、この発明をより詳細に説明する。図示実
施例の汚水処理装置1の内部は、隔壁2、3、4により
固液分離槽5、嫌気濾床槽6、担体反応槽7、担体濾過
槽8に区画されており、担体濾過槽8の上部中央に消毒
槽9が設けられている。装置の上部には図2に点線で示
すメンテナンス用の開口10が設けられている。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Hereinafter, the present invention will be described in more detail with reference to the embodiments shown in FIGS. The inside of the sewage treatment apparatus 1 of the illustrated embodiment is divided into a solid-liquid separation tank 5, an anaerobic filter bed tank 6, a carrier reaction tank 7, and a carrier filtration tank 8 by partitions 2, 3, and 4. A disinfection tank 9 is provided at the center of the upper part. In the upper part of the apparatus, a maintenance opening 10 indicated by a dotted line in FIG. 2 is provided.

【0018】嫌気濾床槽6の中央部分には、濾材11が
充填されている。担体反応槽7には比重がほぼ1の担体
12が充填されており、底部の偏心位置に散気管13が
配置されている。この散気管からの曝気により、担体反
応槽には槽の一方の側壁で上昇し、上層部分で水平に流
れ、反対の側壁に沿って下降する旋回流が生成される。
担体はこの旋回流に乗って浮遊し、担体の表面や内部に
着床した好気性微生物により、汚水の浄化が行われる。
The central part of the anaerobic filter bed tank 6 is filled with a filter medium 11. The carrier reaction tank 7 is filled with a carrier 12 having a specific gravity of about 1, and an air diffuser 13 is disposed at an eccentric position at the bottom. Due to the aeration from the air diffuser, a swirling flow is generated in the carrier reaction tank which rises on one side wall of the tank, flows horizontally in the upper layer portion, and descends along the opposite side wall.
The carrier floats on this swirling flow, and sewage is purified by aerobic microorganisms that have landed on the surface or inside of the carrier.

【0019】担体濾過槽8には比重の軽い濾過担体26
が充填され、中間より若干下方の部分に大量の空気を曝
気可能な洗浄用散気管14が配置されている。通常の運
転状態においては、洗浄用散気管からは曝気が行われて
おらず、濾過担体26は層の上層に浮力により密集して
おり、処理水がこの密集層を通過する間に担体に着床し
た微生物により、固形分が捕捉される。濾過担体26
は、適時洗浄用散気管14から空気を曝気して流動させ
ることにより洗浄を行なって、表面に付着した固形分を
分離沈降させる。沈降した汚泥は、エアリフトポンプを
備えた汚泥返送管15により固液分離槽5に返送され
る。
The carrier filtration tank 8 has a filtration carrier 26 having a low specific gravity.
And a diffuser 14 for washing capable of aerating a large amount of air is disposed in a portion slightly below the middle. In the normal operation state, aeration is not performed from the cleaning air diffuser, and the filtration carrier 26 is densely packed on the upper layer by buoyancy, and the treated water is deposited on the carrier while passing through the dense layer. The solid content is captured by the microorganisms that have been deposited. Filtration carrier 26
The washing is performed by aerating and flowing air from the washing air diffuser 14 as needed to separate and settle solids attached to the surface. The settled sludge is returned to the solid-liquid separation tank 5 by a sludge return pipe 15 provided with an air lift pump.

【0020】固液分離槽と嫌気濾床槽の間の隔壁2及び
嫌気濾床槽と担体反応槽の間の隔壁3の水面部分には、
隔壁を貫通する移流口16が設けられており、固液分離
槽には汚水の流入管17が開口し、消毒槽9には放流管
18が設けられている。また嫌気濾床槽6には、エアリ
フトポンプを備えた強制移送管19が設けられている。
この強制移送管19の吸入口20は、嫌気濾床槽6の水
面近くで開口しており、エアリフトポンプの必要な揚程
を得るために一旦下方に下がり、再び上方に導かれたあ
と、吐出口が担体反応槽の上部に開口している。
The water surface of the partition wall 2 between the solid-liquid separation tank and the anaerobic filter bed tank and the partition wall 3 between the anaerobic filter bed tank and the carrier reaction tank are:
An advection port 16 penetrating the partition wall is provided, an inflow pipe 17 of sewage is opened in the solid-liquid separation tank, and a discharge pipe 18 is provided in the disinfection tank 9. The anaerobic filter tank 6 is provided with a forced transfer pipe 19 provided with an air lift pump.
The suction port 20 of this forced transfer pipe 19 is open near the water surface of the anaerobic filter bed tank 6, and once lowers in order to obtain the required lift of the air lift pump, is guided again upward, and then is discharged again. Open at the top of the carrier reaction tank.

【0021】担体反応槽と担体濾過槽を区画する隔壁4
の水面直下には、担体反応層側の開口端にスクリーン面
21を備えた担体分離装置22が設けられている。この
担体分離装置は、担体反応槽7の水面付近の中央部に配
置されており、その担体反応槽側の開口端は、その開口
部分における槽内の水流と平行で、かつ水平面に対して
30ないし45度の角度をなす面で斜めに切断され、当
該斜めの面に多数の水平方向に細長い濾過孔23を備え
たスクリーン24が取付けられている。
A partition 4 for partitioning the carrier reaction tank and the carrier filtration tank
A carrier separation device 22 having a screen surface 21 at the opening end on the carrier reaction layer side is provided directly below the water surface. This carrier separation device is disposed at the center of the carrier reaction tank 7 near the water surface, and the open end on the carrier reaction tank side is parallel to the water flow in the tank at the opening portion and 30 ° with respect to the horizontal plane. A screen 24 having a large number of horizontally elongated filtration holes 23 is attached to the diagonally cut surface at an angle of 45 to 45 degrees.

【0022】このスクリーンは、担体反応槽の水面直下
に位置しており、散気管13の曝気により生成される担
体反応槽の旋回流は、図5に矢印で示すように、このス
クリーンの濾過孔23の長手方向に流れる。担体分離装
置22の担体濾過槽8側の端部は、正常運転時の担体濾
過槽の水面直下に開口している。
This screen is located just below the water surface of the carrier reaction tank, and the swirling flow of the carrier reaction tank generated by the aeration of the diffuser 13 causes the filtration holes of the screen to pass through as shown by arrows in FIG. 23 flows in the longitudinal direction. The end of the carrier separation device 22 on the side of the carrier filtration tank 8 is opened just below the water surface of the carrier filtration tank during normal operation.

【0023】定常運転時においては、強制移送管19の
エアリフトポンプ及び洗浄用散気管14の曝気は停止し
ている。固液分離槽5に流入した原水は、移流口16、
16を経て、嫌気濾床槽6を通り担体反応槽7へと溢流
して行く。担体反応槽7では担体12に着床した好気性
微生物により、処理水の浄化が行われ、スクリーン24
によって担体を分離された処理水が担体濾過槽8へと流
れる。そして、担体濾過槽の担体26で濾過が行われ、
消毒槽を経て放流される。担体濾過槽8の底部に沈降し
た濾過汚泥は、適時汚泥返送管15のエアリフトポンプ
を運転することによって、固液分離槽5に返送される。
During normal operation, the air lift pump of the forced transfer pipe 19 and the aeration of the cleaning air diffuser 14 are stopped. The raw water flowing into the solid-liquid separation tank 5 is supplied to the advection port 16,
After 16, the water overflows through the anaerobic filter bed tank 6 to the carrier reaction tank 7. In the carrier reaction tank 7, the treated water is purified by the aerobic microorganisms that have landed on the carrier 12, and the screen 24 is cleaned.
The treated water from which the carrier has been separated flows into the carrier filtration tank 8. Then, filtration is performed on the carrier 26 of the carrier filtration tank,
Released through the disinfection tank. The filtered sludge settled at the bottom of the carrier filtration tank 8 is returned to the solid-liquid separation tank 5 by operating the air lift pump of the sludge return pipe 15 as appropriate.

【0024】担体濾過槽の担体26の洗浄は、夜間等の
原水の流入のない時間帯を見計らって行われる。まず強
制移送管19のエアリフトポンプを運転して、嫌気濾床
槽6の汚水を強制的に担体反応槽7の処理能力を超えな
い流量で移送する。これにより、嫌気濾床槽6の水位が
低下する。次に汚泥返送管15のエアリフトポンプを運
転して、担体濾過槽8の処理水を固液分離槽5に返送す
る。返送された処理水は嫌気濾床槽6に溢流するが、嫌
気濾床槽6の水位が予め低下しているため、担体反応槽
には流れない。そのため、担体濾過槽8の水位が低下す
るから、そこで洗浄用散気管14から大量の空気を曝気
して、濾過担体26を洗浄する。洗浄により分離沈降し
た汚泥は、汚泥返送管15により固液分離槽5に返送さ
れる。
The washing of the carrier 26 in the carrier filtration tank is performed in consideration of a time period during which raw water does not flow, such as at night. First, the air lift pump of the forced transfer pipe 19 is operated to forcibly transfer the sewage in the anaerobic filter bed tank 6 at a flow rate not exceeding the processing capacity of the carrier reaction tank 7. Thereby, the water level of the anaerobic filter bed tank 6 decreases. Next, the air lift pump of the sludge return pipe 15 is operated to return the treated water in the carrier filtration tank 8 to the solid-liquid separation tank 5. The returned treated water overflows into the anaerobic filter bed tank 6, but does not flow into the carrier reaction tank because the water level in the anaerobic filter bed tank 6 has been lowered in advance. As a result, the water level in the carrier filtration tank 8 decreases, so that a large amount of air is aerated from the cleaning air diffuser 14 to wash the filtration carrier 26. The sludge separated and settled by the washing is returned to the solid-liquid separation tank 5 by the sludge return pipe 15.

【0025】この洗浄処理はタイマなどによって設定し
た時間行われ、洗浄が終了したら、通常の運転操作に戻
る。
This cleaning process is performed for a time set by a timer or the like. When the cleaning is completed, the operation returns to the normal operation.

【0026】担体分離装置22のスクリーン面21は、
装置上部のメンテナンス用の開口10を開いて視認する
ことができる。汚泥の付着が認められるときは、当該開
口からブラシを差し込んでスクリーン面を掃除する。ス
クリーン面の汚泥が除去されたかどうかは、当該開口か
ら容易に確認できる。
The screen surface 21 of the carrier separation device 22
The maintenance opening 10 at the top of the apparatus can be opened and visually recognized. If sludge adheres, clean the screen by inserting a brush through the opening. Whether or not sludge on the screen surface has been removed can be easily confirmed from the opening.

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

【図1】実施例の汚水処理装置の断面側面図FIG. 1 is a cross-sectional side view of a sewage treatment apparatus according to an embodiment.

【図2】図1の断面平面図FIG. 2 is a cross-sectional plan view of FIG.

【図3】図1のA−A断面図FIG. 3 is a sectional view taken along line AA of FIG. 1;

【図4】担体分離装置の断面図FIG. 4 is a sectional view of a carrier separation device.

【図5】図4の平面図FIG. 5 is a plan view of FIG. 4;

【図6】従来装置を模式的に示した図FIG. 6 schematically shows a conventional apparatus.

【符号の説明】[Explanation of symbols]

5 固液分離槽 6 嫌気濾床槽 7 担体反応槽 8 担体濾過槽 12 担体 14 洗浄用散気管 19 強制移送管 21 スクリーン面 22 担体分離装置 26 濾過担体 5 Solid-liquid separation tank 6 Anaerobic filter bed tank 7 Carrier reaction tank 8 Carrier filtration tank 12 Carrier 14 Cleaning diffuser tube 19 Forced transfer tube 21 Screen surface 22 Carrier separation device 26 Filtration carrier

───────────────────────────────────────────────────── フロントページの続き (72)発明者 山崎 宏史 石川県金沢市西泉3丁目92番地 アムズ株 式会社内 Fターム(参考) 4D003 AA12 AB02 BA02 CA02 CA03 CA08 DA09 DA11 EA01 EA28 4D027 AA01 AA02 AA12 AA14 AB06 AB07 AB12 AB14  ────────────────────────────────────────────────── ─── Continuing on the front page (72) Inventor Hiroshi Yamazaki 3-92 Nishiizumi, Kanazawa-shi, Ishikawa F-term (reference) within AMS Corporation 4D003 AA12 AB02 BA02 CA02 CA03 CA08 DA09 DA11 EA01 EA28 4D027 AA01 AA02 AA12 AA14 AB06 AB07 AB12 AB14

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 濾過担体(26)を充填して固液分離を行う
担体濾過槽(8)を備え、曝気により定期的に濾過担体(2
6)を洗浄して捕捉した浮遊物質を除去する洗浄用散気管
(14)を備えた汚水処理装置において、処理水の流れの上
流側に位置する前槽(6)から下流側に位置する次槽(7)に
強制的に処理水を移送する強制移送装置(19)を備え、濾
過担体(26)の洗浄前に強制移送装置(19)を運転して前槽
の水位を下げ、次に担体濾過槽(8)の水を上流側に位置
する槽(5,6,7)に送ることにより担体濾過槽(8)の水位を
低下させた後に濾過担体(26)の洗浄を行う、汚水処理装
置。
1. A carrier filtration tank (8), which is filled with a filtration carrier (26) to perform solid-liquid separation, and is periodically aerated by aeration.
6) Cleaning air diffuser to remove trapped suspended matter by cleaning
In the sewage treatment apparatus provided with (14), a forced transfer device (forcibly transferring the treated water from the front tank (6) located on the upstream side of the flow of the treated water to the next tank (7) located on the downstream side) Before the washing of the filter carrier (26), the forced transfer device (19) is operated to lower the water level of the front tank, and then the water in the carrier filtration tank (8) is located upstream of the tank (5). Sewage treatment apparatus for washing the filtration carrier (26) after lowering the water level of the carrier filtration tank (8) by sending it to the carrier filtration tank (8).
【請求項2】 担体(12)を充填して酸素を含有するガス
を吹き込むことにより充填担体を旋回させて汚水を浄化
する担体反応槽(7)と、担体反応槽から次槽へと担体(1
2)を分離して処理水を移流する担体分離装置(22)とを備
えた汚水処理装置において、担体反応槽(7)内の水平流
が惹起する部位に、スクリーン面(21)を水平面に対して
30度を超えかつ90度未満の角度にして担体分離装置
(22)を設けた、汚水処理装置。
2. A carrier reaction tank (7) for filling a carrier (12) and blowing a gas containing oxygen to swirl the filled carrier to purify waste water, and a carrier (7) from the carrier reaction tank to the next tank. 1
In a sewage treatment device provided with a carrier separation device (22) for separating 2) and transferring treated water, a screen surface (21) is placed on a horizontal surface at a site where a horizontal flow is caused in the carrier reaction tank (7). Carrier separation device at an angle of more than 30 degrees and less than 90 degrees
A sewage treatment apparatus provided with (22).
JP2000133473A 2000-05-02 2000-05-02 Sewage treatment equipment Expired - Fee Related JP4198299B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2000133473A JP4198299B2 (en) 2000-05-02 2000-05-02 Sewage treatment equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2000133473A JP4198299B2 (en) 2000-05-02 2000-05-02 Sewage treatment equipment

Publications (2)

Publication Number Publication Date
JP2001310193A true JP2001310193A (en) 2001-11-06
JP4198299B2 JP4198299B2 (en) 2008-12-17

Family

ID=18641962

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2000133473A Expired - Fee Related JP4198299B2 (en) 2000-05-02 2000-05-02 Sewage treatment equipment

Country Status (1)

Country Link
JP (1) JP4198299B2 (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005185892A (en) * 2003-12-24 2005-07-14 Fuji Clean Kogyo Kk Sewage treatment device
JP2006116463A (en) * 2004-10-22 2006-05-11 Kubota Corp Operation method for sewage treatment device, and sewage treatment device
JP2007237147A (en) * 2006-03-13 2007-09-20 Hitachi Housetec Co Ltd Aerobic treatment tank and septic tank containing it
JP2007260621A (en) * 2006-03-29 2007-10-11 Kubota Corp Septic tank
CN117654120A (en) * 2024-02-01 2024-03-08 安徽清朗环保科技有限公司 Horizontal flow sedimentation tank

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109612138A (en) * 2018-11-15 2019-04-12 安徽兆拓新能源科技有限公司 A kind of solar water heater water tank with cleaning function

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005185892A (en) * 2003-12-24 2005-07-14 Fuji Clean Kogyo Kk Sewage treatment device
JP4554194B2 (en) * 2003-12-24 2010-09-29 フジクリーン工業株式会社 Sewage treatment equipment
JP2006116463A (en) * 2004-10-22 2006-05-11 Kubota Corp Operation method for sewage treatment device, and sewage treatment device
JP2007237147A (en) * 2006-03-13 2007-09-20 Hitachi Housetec Co Ltd Aerobic treatment tank and septic tank containing it
JP2007260621A (en) * 2006-03-29 2007-10-11 Kubota Corp Septic tank
CN117654120A (en) * 2024-02-01 2024-03-08 安徽清朗环保科技有限公司 Horizontal flow sedimentation tank

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