JPS59193195A - Fixed bed type sewage cleaning up tank - Google Patents

Fixed bed type sewage cleaning up tank

Info

Publication number
JPS59193195A
JPS59193195A JP58068099A JP6809983A JPS59193195A JP S59193195 A JPS59193195 A JP S59193195A JP 58068099 A JP58068099 A JP 58068099A JP 6809983 A JP6809983 A JP 6809983A JP S59193195 A JPS59193195 A JP S59193195A
Authority
JP
Japan
Prior art keywords
tank
water level
flow rate
gas
water
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP58068099A
Other languages
Japanese (ja)
Inventor
Hiroshi Hoshikawa
星川 寛
Satoshi Nishikata
西方 聡
Yasunari Sasaki
康成 佐々木
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.)
Fuji Electric Co Ltd
Original Assignee
Fuji Electric Co Ltd
Fuji Electric Corporate Research and Development Ltd
Fuji Electric Manufacturing Co Ltd
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 Fuji Electric Co Ltd, Fuji Electric Corporate Research and Development Ltd, Fuji Electric Manufacturing Co Ltd filed Critical Fuji Electric Co Ltd
Priority to JP58068099A priority Critical patent/JPS59193195A/en
Publication of JPS59193195A publication Critical patent/JPS59193195A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage

Landscapes

  • Biological Treatment Of Waste Water (AREA)

Abstract

PURPOSE:To prevent the rise in a water level owing to progression of clogging by providing a detector for the watr level in a tank and a device for diffusing gas into an outflow pipe and controlling the flow rate of said gas, and changing the flow rate of the gas into a water flow pipe according to a change in the water level. CONSTITUTION:When the operation of a cleaning up tank is continuously performed, the clogging in a packing material 3 is progressed by thickening of biological membrane and the water level in the tank rises graudally until the level arrives at a preset position, then a water level controller constituted of the 2nd air diffuser 15, a flow rate regulating valve 16 and a float 17 operates to maintain the water level. More specifically, the 2nd air diffuser 15 has the function of an air lift pump together with an outflow pipe 6, and the suction power thereof increases or decreases according to the flow rate of the gas diffused from the diffuser 15. When the water level rises to lift the float 17, the valve 16 is opened and the gas is discharged from the diffuser 15 to suck and discharge treated water 5.

Description

【発明の詳細な説明】 〔発明の属する技術分野〕 この発明は、汚水を充填材表面に付着生育した微生物の
働きにより浄化処理する固定床形汚水浄化装置における
水位制御に関する。
DETAILED DESCRIPTION OF THE INVENTION [Technical field to which the invention pertains] This invention relates to water level control in a fixed bed type sewage purification device that purifies sewage through the action of microorganisms grown on the surface of a filler.

〔従来技術とその問題点〕[Prior art and its problems]

汚水を微生物の働きにより浄化処理する方法の一つとし
て従来より固定床法がよく知られている。
The fixed bed method has been well known as one of the methods for purifying wastewater using the action of microorganisms.

固定床法は、密閉された槽内にプラスチック製の波板、
網などで形成した充填材を収納してこれに汚水を流入せ
しめ、機械攪拌装置または散気によるエアーリフトを用
いて汚水を攪拌し、前記充填材の表面に付着生育した微
生物と循環接触させることにより汚水を浄化処理するも
のである。このような処理を行なう装置としては攪拌方
法や充填材の設置位置などの違いにより、種々の形式の
ものが使用されているが、最も一般的に使用されている
装置は、槽の中央部に攪拌部を有し、槽内壁と攪拌部と
の間に充填材を設置した形式のもので、その縦断面を第
1図に示す。
The fixed bed method uses corrugated plastic plates in a sealed tank.
A filling material formed of a net or the like is housed and sewage is allowed to flow into it, and the sewage is agitated using a mechanical stirring device or an air lift using aeration, and brought into circulation contact with microorganisms that have grown on the surface of the filling material. This is to purify wastewater. Various types of equipment are used for this type of treatment, depending on the stirring method and the location of the filler, but the most commonly used equipment is one that is installed in the center of the tank. It has a stirring section and a filler is installed between the inner wall of the tank and the stirring section, and its vertical cross section is shown in FIG. 1.

第1図において槽1は上部開口部が覆蓋2によって密閉
されており、内部には側壁に沿ってプラスチック製の波
板や網などで形成された充填材3が配置され、この充填
材3の中心部に攪拌部4が形成される。浄化槽1の側壁
上部を貫通して流入管5が設けられ、この流入管5に対
向した側壁で流入管5より僅かに低い位置でかつ充填材
3の上面より高い位置を貫通して流出管6が設けられて
いる。
In FIG. 1, the upper opening of a tank 1 is sealed with a cover 2, and a filling material 3 made of corrugated plastic sheet, net, etc. is placed inside along the side wall. A stirring section 4 is formed in the center. An inflow pipe 5 is provided passing through the upper part of the side wall of the septic tank 1, and an outflow pipe 6 is provided at a position slightly lower than the inflow pipe 5 and higher than the top surface of the filler 3 on the side wall opposite to the inflow pipe 5. is provided.

流出管6の一端は槽内の充填材3を上部から内部を貫通
して充填材3の下面まで配vびれており、他力の流出側
先端は槽外にて気液分離器7に接続されている。覆蓋2
を貫通する配管8は槽外に設置された第1のコンプレッ
サ9の入側に接続され、このコンプレッサ9の出側に接
続された配管8aは、覆蓋2を貫通して槽内攪拌部4を
通り槽底部に近い所で先端が散気装置10に接続されて
いる。
One end of the outflow pipe 6 passes through the filling material 3 in the tank from the top to the bottom of the filling material 3, and the other end of the outflow side is connected to the gas-liquid separator 7 outside the tank. has been done. cover 2
A pipe 8 that penetrates the tank is connected to the inlet side of a first compressor 9 installed outside the tank, and a pipe 8a connected to the outlet side of the compressor 9 penetrates the cover 2 and connects the tank agitation section 4. The tip is connected to the air diffuser 10 near the bottom of the tank.

また槽底部に近い槽側壁を貫通して槽内部に逆洗用散気
装置11が設けられ、この逆洗用散気装置11は槽外に
ある第2のコンプレッサ12に接続されている。また槽
の最底部には排泥管13が取付けられ、その先端には排
泥弁14が設けられている。
Further, a backwashing air diffuser 11 is provided inside the tank by penetrating the tank side wall near the bottom of the tank, and this backwashing air diffuser 11 is connected to a second compressor 12 located outside the tank. Further, a sludge drain pipe 13 is attached to the bottom of the tank, and a sludge drain valve 14 is provided at the tip thereof.

上述した構造の固定床形汚水浄化槽における汚水の処理
工程を説明すると、まず汚水Fは流入管5より槽内に流
入し貯溜される。浄化槽1内で生成するメタンガスを主
成分とした嫌気性ガスは第1のコンプレッサ9の作用で
配管8より吸入されて配管8aに送出され、先端の散気
装置10より攪拌部4に送出される。Cれにより汚水は
攪拌され、充填材3の表面に付着生育し生物膜を形成し
た微生物と接触することにより浄化される。浄化された
水は充填材3の下面から充填材3を貫通して配管された
流出管6を通過して気液分離器7に処理水Tとして流出
する。
To explain the process of treating sewage in the fixed bed type sewage septic tank having the above-described structure, first, sewage F flows into the tank through the inflow pipe 5 and is stored therein. Anaerobic gas mainly composed of methane gas generated in the septic tank 1 is sucked into the pipe 8 by the action of the first compressor 9, sent to the pipe 8a, and sent to the stirring section 4 from the aeration device 10 at the tip. . The sewage is agitated by carbon and is purified by coming into contact with microorganisms that have adhered to and grown on the surface of the filler 3 to form a biofilm. The purified water passes through an outflow pipe 6 piped through the filling material 3 from the lower surface of the filling material 3, and flows out into the gas-liquid separator 7 as treated water T.

かくてこのような処理が数ケ月連続して行なわれると、
生物膜の厚さが厚くなり、ついに生物膜自体を充填材3
0表面上に支えきれなくなって剥離し、処理水Tに混入
して水質悪化を招く。また生物膜は充填材3の隙間に増
殖するため、次第に隙間が少なくなり目詰まりを起こし
槽内の水の循環が悪くなり浄化作用が悪化する。この対
策としては周期的に逆洗を行なう。このためには第2の
コンプレッサ12を運転し、槽内の充填材3の下方に設
けられた逆洗用散気装置11より空気を吹込む。これに
より、気泡が充填材3の隙間を通過し、肥厚した生物膜
を剥離する。剥離した生物膜は、−第2のコンプレッサ
12の停止後に浄化槽2底部に沈積するので、排泥弁1
4を開弁すれば排泥管13を経て槽外に排出される。な
お逆洗および排泥中は第1のコンプレッサ9の運転は行
なわない0 以上は正常な場合の処理工程を述べたが、従来の汚水浄
化槽においては、充填材3の目詰まりが進行するに従い
、処理水排出位置と槽内水位に高落差が生じ浄化槽1内
の水位が上昇し汚水Fの流入位置と処理水Tの流出位置
の上下寸法差が小さいときには、処理水Tが流入管5を
通して逆流する欠点があった。通常の固定床形汚水浄化
プロセスにおいては複数台の固定床形汚水浄化槽を直列
に連結して使用しているため、前述した逆流現象は、目
詰まりした槽の前段の槽にも水位上昇を招き、そのため
真に目詰まりが進行して水位が上昇している槽と、目詰
まりせずに水位が上昇している檜の区別ができず、真に
逆洗を必要とする槽がいずれであるか正確に知ることは
困難であった。
If this kind of treatment is carried out continuously for several months,
The thickness of the biofilm increases until the biofilm itself becomes a filler3.
0 It can no longer be supported on the surface and peels off, contaminating the treated water T and causing deterioration of water quality. Furthermore, since the biofilm grows in the gaps in the filler 3, the gaps gradually become smaller and become clogged, which impairs the circulation of water in the tank and deteriorates the purification effect. As a countermeasure against this problem, backwashing should be carried out periodically. For this purpose, the second compressor 12 is operated to blow air from the backwashing air diffuser 11 provided below the filler 3 in the tank. As a result, the air bubbles pass through the gaps in the filler 3 and peel off the thickened biofilm. The separated biofilm is deposited on the bottom of the septic tank 2 after the second compressor 12 is stopped, so the sludge valve 1
When the valve 4 is opened, the sludge is discharged to the outside of the tank through the drainage pipe 13. Note that the first compressor 9 is not operated during backwashing and sludge removal. The processing steps above are for a normal case, but in a conventional sewage septic tank, as the filler 3 becomes clogged, When there is a height difference between the treated water discharge position and the water level in the tank, the water level in the septic tank 1 rises, and the vertical dimension difference between the inflow position of sewage F and the outflow position of treated water T is small, the treated water T flows back through the inflow pipe 5. There was a drawback. In a normal fixed-bed sewage purification process, multiple fixed-bed sewage septic tanks are connected in series, so the above-mentioned backflow phenomenon causes the water level to rise in the tank preceding the clogged tank. Therefore, it is impossible to distinguish between a tank that is truly clogged and the water level is rising, and a hinoki tank that is not clogged and the water level is rising, and which tanks truly require backwashing. It was difficult to know exactly.

その対策としては汚水の流入位置を処理水の流出位置に
対して十分高い位置に設けれはよいが、これは浄化槽自
体の容積が必要以上に大きくなるばかりでなく、汚水浄
化プロセスを構成する直列連結された浄化槽の各種間の
高低差が犬きくなシプロセス自体の体積効率が悪化し、
さらにそのため各種の逆洗が頻繁になり、過剰な逆洗エ
ネルギーの使用と処理水質の悪化をもたらす欠点があっ
た前記の如く浄化槽の充填材に目詰まりが生じ、槽の水
位が上昇すると処理水排出位置と槽内水位に高落差を生
ずるが、これを第1図に示すようにΔPにて表わすと、
ΔPは目詰まシによる圧力損失と考えられる。したがっ
てΔPは目詰まシに比例して増加していくから、この状
態で槽内水位を一定に保つためには、逆に処理水排出位
置を低い位置に下げればよい。しかしながら実際には槽
の構造と配管上の問題から処理水排出位置を移動させ順
次低い位置に下げ、充填材3の上部に排水位置を設ける
ことは、浄化槽の容積増大なくしては困難な問題である
As a countermeasure against this problem, it would be good to install the sewage inflow position at a sufficiently high position relative to the treated water outflow position, but this would not only make the volume of the septic tank itself unnecessarily large but also The difference in height between each type of connected septic tank causes the volumetric efficiency of the process itself to deteriorate,
Furthermore, as a result, various types of backwashing become more frequent, which has the disadvantage of using excessive backwashing energy and deteriorating the quality of treated water. A height difference occurs between the discharge position and the water level in the tank, and this is expressed as ΔP as shown in Figure 1.
ΔP is considered to be a pressure loss due to clogging. Therefore, ΔP increases in proportion to clogging, so in order to keep the water level in the tank constant in this state, the treated water discharge position should be lowered to a lower position. However, in reality, due to tank structure and piping problems, it is difficult to move the treated water discharge position and gradually lower it to a lower position without increasing the volume of the septic tank. be.

〔発明の目的〕[Purpose of the invention]

この発明は上述の欠点を除去し、浄化槽の充填材に目づ
まシが進行しても槽内の水位上昇を招くことなく、汚水
処理を続行することを可能ならしめる固定床形汚水浄化
槽を提供することを目的とする。
The present invention eliminates the above-mentioned drawbacks and provides a fixed bed type sewage septic tank that makes it possible to continue sewage treatment without causing a rise in the water level in the tank even if the filling material of the septic tank becomes clogged. The purpose is to

〔発明の要点〕[Key points of the invention]

この発明は槽内水位を検知する装置と、流出管中に気体
を散気させかつその気体流量を制御する装置とを備え、
水位の変化に応じて流出管中への気体流量を変化させて
処理水を吸引排水することによシ槽内水位をほぼ一定に
保つようにするものである。
This invention includes a device for detecting the water level in the tank, a device for diffusing gas into the outflow pipe and controlling the gas flow rate,
The water level in the tank is kept almost constant by changing the flow rate of gas into the outflow pipe in response to changes in the water level and suctioning and draining the treated water.

〔発明の実施例〕[Embodiments of the invention]

以下この発明の実施例を図面に基づいて説明する。第2
図はこの発明の一実施例である固定床形汚水浄化槽の縦
断面図で、従来構造の浄化槽と同じ部分2部品に対して
は同一の符号を付し、説明を省略する。この浄化槽は従
来構造の槽内の配管8aから分岐する配管8bを設けて
、これを充填材3の中を貫通する流出管6の中に通し、
その先端部(充填材3の下部付近)に第2の散気装置1
5を取付ける。また配管8bの分岐個所近辺に流量調整
弁16を設けて、この流量調整弁16に水面に浮かぶフ
ロート17を連動させる構造とする。
Embodiments of the present invention will be described below based on the drawings. Second
The figure is a longitudinal cross-sectional view of a fixed bed type sewage septic tank that is an embodiment of the present invention, and two parts that are the same as those of a septic tank of a conventional structure are given the same reference numerals and explanations thereof will be omitted. This septic tank is provided with a pipe 8b branching from a pipe 8a in the tank of a conventional structure, which is passed into an outflow pipe 6 penetrating through the filling material 3.
A second air diffuser 1 is installed at the tip (near the bottom of the filler 3).
Install 5. Further, a flow rate adjustment valve 16 is provided near the branch point of the pipe 8b, and a float 17 floating on the water surface is linked to this flow rate adjustment valve 16.

この構造においても汚水浄化プロセスは従来と全く同じ
であり、この運転を連続的に行なうと生物膜の肥厚によ
シ充填材30目詰まりが進行し、それに伴い槽内水位は
次第に上昇するが、この水位が予め設定された位置まで
達すると、第2の散気装置15.流量調整弁16.フロ
ート17によシ構成された水位制御装置の働きによりそ
の水位が維持される。
In this structure, the sewage purification process is exactly the same as the conventional one, and if this operation is performed continuously, the filling material 30 will become clogged due to the thickening of the biofilm, and the water level in the tank will gradually rise. When this water level reaches a preset position, the second air diffuser 15. Flow rate adjustment valve 16. The water level is maintained by the action of a water level control device constituted by the float 17.

ここで前述の水位制御装置の作用を詳細に説明すると、
第2の散気装置15は流出管6とともにエアリフトポン
プの機能をもち、その吸引能力は第2の散気装置15か
ら吐出されるガス流量に応じて増減するので、水位が上
昇してフロート17を押し上げると流量調整弁16が開
き、ガスが第2の散気装置15から吐出され、前述のエ
アリフトポンプ機能が働き、処理水Tを吸引排出する。
Here, the operation of the water level control device mentioned above will be explained in detail.
The second air diffuser 15 has the function of an air lift pump together with the outflow pipe 6, and its suction capacity increases or decreases depending on the gas flow rate discharged from the second air diffuser 15, so the water level rises and the float 17 When pushed up, the flow rate adjustment valve 16 opens, gas is discharged from the second diffuser 15, the above-mentioned air lift pump function is activated, and the treated water T is sucked and discharged.

その結果ΔPが減少して水位の上昇は停止する。As a result, ΔP decreases and the water level stops rising.

第3図は、この発明の他の実施例を示すもので水位検出
用電極18.制御ユニット19.電動弁20を用いて水
位を制御するものである。すなわち槽内水位がWH4で
上昇すると水位検出用電極18で検出され、制御ユニッ
ト19からの信号により電動弁20が開弁し、ガスが第
2の散気装置15から吐出して処理水Tを吸引排出する
。その結果、槽内水位は下降し、WLのレベルになると
水位検出用電極18で検出され、電動弁20が閉弁し、
処理水Tの吸引排出も停止するので槽内水位は再び上昇
を始める。この動作のくり返しにより槽内水位はWHと
WLの間を上下するが、WHとWLの間隔を数鑵位にす
れば実用上問題ない。
FIG. 3 shows another embodiment of the present invention, in which the water level detection electrode 18. Control unit 19. The water level is controlled using an electric valve 20. That is, when the water level in the tank rises at WH4, it is detected by the water level detection electrode 18, the electric valve 20 is opened in response to a signal from the control unit 19, and gas is discharged from the second diffuser 15 to discharge the treated water T. Suction and discharge. As a result, the water level in the tank decreases, and when it reaches the level WL, it is detected by the water level detection electrode 18, and the electric valve 20 closes.
Since the suction and discharge of the treated water T also stops, the water level in the tank starts to rise again. By repeating this operation, the water level in the tank fluctuates between WH and WL, but this does not pose a practical problem as long as the interval between WH and WL is set to several digits.

〔発明の効果〕〔Effect of the invention〕

この発明によれば、浄化槽内水位の変化に応じて流出管
中に散気するガス流量を変化させ、処理水を吸引排水す
ることにより、槽内水位を一定に保つようにしたので、
充填材の目詰まりが進行しても処理水が流入管から逆流
することもないし、汚水の流入位置と処理水の流出位置
の高低差を大きくすることも不必要となるため浄化槽の
小形化が可能であシ、とくに複数台の浄化槽を直列連結
して使用する固定床形汚水浄化プロセスにおいては各浄
化槽間の高低差を縮少できるのでプロセスの体積効率を
改善することができる。また充填材上面と浄化槽底部間
の水圧差または電動弁の作動状況とチェックすることに
よシ逆洗時期を判断するため、逆洗時期を正確に検知で
き、逆洗操作も自動化が容易となる効果がある。
According to this invention, the water level in the septic tank is maintained constant by changing the gas flow rate diffused into the outflow pipe according to changes in the water level in the septic tank and sucking and draining the treated water.
Even if the filler becomes clogged, the treated water will not flow back from the inflow pipe, and there is no need to increase the height difference between the inflow position of sewage water and the outflow position of treated water, making it possible to downsize the septic tank. It is possible, especially in a fixed-bed sewage purification process in which a plurality of septic tanks are connected in series, the height difference between each septic tank can be reduced, and the volumetric efficiency of the process can be improved. In addition, the backwashing time is determined by checking the water pressure difference between the top surface of the filler and the bottom of the septic tank or the operating status of the electric valve, so the backwashing time can be accurately detected and backwashing operations can be easily automated. effective.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は従来構造の固定床形汚水浄化槽の縦断面図、第
2図はこの発明の実施例の縦断面図、第3図はこの発明
の異なる実施例の縦断面図である。 1・槽、3・・充填材、6・・流出管、15・第2の散
気装置、16・流量調整弁、17・ フロート、18 
・水位検出用電極、19・・制御ユニット、20・・電
動弁。 手続補正書(自船 昭和58年い30日 特許庁 長官  若(工和夫 殿 1、事件の表示   特願昭(さ−68099住  所
  川崎市川崎区田辺新田1番1号7、補正の対象 卯
記の□1.iA’11−ツ7ン](・つ9でfllQ徂
明A1!l囚の几しJ一つ;1′j″〔説明の項8、補
正の内容  別紙の通り 1、明細書の特許請求の範囲を下紙のとおり補正する。 1)内部に充填材を有する槽に汚水を流入さぜ、前記充
填材の表面に付着生育した微生物により汚水を処理し、
処理水を前記充填材の下面より充填材を貫通して槽の側
壁面より槽外部に導出する流出管より排出する固定床形
汚水浄化槽において、槽内水位を検出する装置と、前記
流出管中に気体を散気させかつその気体流量を制御する
装置とを備え、水位の変化に応じて流出管中への気体流
量を変化させて処理水を吸引排出することにより槽内水
位をほぼ一定に保つようにしたことを特徴とする固定床
形汚水浄化槽。 2、特許請求の範囲第1項記載のものにおいて、槽内水
位を検出する装置としてフロートを用い、流出管に散気
させる気体流量の制御は前記フロートに連動している流
量調整弁により行なうようにしたことを特徴とする固定
床形汚水浄化槽。 3)特許請求の範囲第1項記載のものにおいて、槽内水
位を検出する′装置として電極形水位検出器を用い、流
出管に散気させる気体流量の制御は自1−記電極形水位
検出器により作動される電動弁に1行なうようにしたこ
とを特徴とする固定床形汚水浄化槽。 2、明細書の第4頁第8行「いる。」の次に下記を云″
加する。
FIG. 1 is a vertical cross-sectional view of a conventional fixed-bed sewage septic tank, FIG. 2 is a vertical cross-sectional view of an embodiment of the present invention, and FIG. 3 is a vertical cross-sectional view of a different embodiment of the present invention. 1. Tank, 3. Filling material, 6. Outflow pipe, 15. Second diffuser, 16. Flow rate adjustment valve, 17. Float, 18
- Water level detection electrode, 19... Control unit, 20... Electric valve. Procedural amendment (own ship dated 30th 1980, Director General of the Japan Patent Office, Mr. Waka (Kuwao 1), case description Tokkun Sho (Sa-68099 address: 1-1-7 Tanabeshinden, Kawasaki-ku, Kawasaki City, subject of amendment) Uki's □1. , amend the claims of the specification as shown below: 1) Sewage is caused to flow into a tank having a filler inside, and the sewage is treated with microorganisms grown on the surface of the filler,
In a fixed bed type sewage septic tank in which treated water is discharged from an outflow pipe that penetrates the filling material from the bottom surface of the filling material and leads out of the tank from the side wall surface of the tank, a device for detecting a water level in the tank; The tank is equipped with a device that diffuses gas and controls the gas flow rate, and the water level in the tank is kept almost constant by changing the gas flow rate into the outflow pipe according to changes in the water level and suctioning and discharging the treated water. A fixed bed type sewage septic tank characterized by being designed to maintain 2. In the device described in claim 1, a float is used as a device for detecting the water level in the tank, and the flow rate of gas diffused into the outflow pipe is controlled by a flow rate regulating valve linked to the float. A fixed bed type sewage septic tank characterized by: 3) In the product described in claim 1, an electrode-type water level detector is used as a device for detecting the water level in the tank, and the control of the gas flow rate to be diffused into the outflow pipe is performed by the electrode-type water level detector described in item 1. A fixed bed type sewage septic tank characterized in that one electric valve is operated by a container. 2. On page 4, line 8 of the specification, after "Iru.", say the following:
Add.

Claims (1)

【特許請求の範囲】 1)内部に充填材を有する密閉された槽に汚水を流入さ
せ、前記充填材の表面に付着生育した微生物により汚水
を処理し、処理水を前記充填材の下面より充填材を貫通
して榴の側壁面より槽外部に導出する流出管より排出す
る固定床形汚水浄化槽において、槽内水位を検出する装
置と、前記流出管中に気体を散気させかつその気体流量
を制御する装置とを備え、水位の変化に応じて流出管中
への気体流量を変化させて処理水を吸引排出することに
より槽内水位をほぼ一定に保つようにしたことを特徴と
する固定床形汚水浄化槽。 2、特許請求の範囲第1項記載のものにおいて、槽内水
位を検出する装置としてフロートを用い、流出管に散気
させる気体流量の制御は前記フロートに連動している流
量調整弁により行なうようにしたことを特徴とする固定
床形汚水浄化槽。 3)特許請求の範囲第1項記載のものにおいて、槽内水
位を検出する装置として電極形水位検出器を用い、流出
管に散気させる気体流量の制御は前記電極形水位検出器
により作動される電動弁にて行なうようにしたことを特
徴とする固定床形汚水浄化槽。
[Claims] 1) Sewage is caused to flow into a sealed tank having a filler inside, the wastewater is treated with microorganisms grown on the surface of the filler, and the treated water is filled from the bottom surface of the filler. A fixed bed type sewage septic tank that discharges water from an outflow pipe that penetrates the material and leads out of the tank from the side wall surface of the tank. The fixing device is characterized in that the water level in the tank is kept almost constant by suctioning and discharging treated water by changing the flow rate of gas into the outflow pipe according to changes in the water level. Floor-shaped sewage septic tank. 2. In the device described in claim 1, a float is used as a device for detecting the water level in the tank, and the flow rate of gas diffused into the outflow pipe is controlled by a flow rate regulating valve linked to the float. A fixed bed type sewage septic tank characterized by: 3) In the device described in claim 1, an electrode type water level detector is used as a device for detecting the water level in the tank, and control of the flow rate of gas diffused into the outflow pipe is operated by the electrode type water level detector. A fixed bed type sewage septic tank characterized by being operated by an electric valve.
JP58068099A 1983-04-18 1983-04-18 Fixed bed type sewage cleaning up tank Pending JPS59193195A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58068099A JPS59193195A (en) 1983-04-18 1983-04-18 Fixed bed type sewage cleaning up tank

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58068099A JPS59193195A (en) 1983-04-18 1983-04-18 Fixed bed type sewage cleaning up tank

Publications (1)

Publication Number Publication Date
JPS59193195A true JPS59193195A (en) 1984-11-01

Family

ID=13363949

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58068099A Pending JPS59193195A (en) 1983-04-18 1983-04-18 Fixed bed type sewage cleaning up tank

Country Status (1)

Country Link
JP (1) JPS59193195A (en)

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