JPH0985269A - Sewage treatment apparatus - Google Patents

Sewage treatment apparatus

Info

Publication number
JPH0985269A
JPH0985269A JP24939195A JP24939195A JPH0985269A JP H0985269 A JPH0985269 A JP H0985269A JP 24939195 A JP24939195 A JP 24939195A JP 24939195 A JP24939195 A JP 24939195A JP H0985269 A JPH0985269 A JP H0985269A
Authority
JP
Japan
Prior art keywords
chamber
filter
scum
opening
clarification
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
JP24939195A
Other languages
Japanese (ja)
Inventor
Seiichiro Nakamoto
政一郎 仲本
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.)
Sekisui Chemical Co Ltd
Original Assignee
Sekisui Chemical 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 Sekisui Chemical Co Ltd filed Critical Sekisui Chemical Co Ltd
Priority to JP24939195A priority Critical patent/JPH0985269A/en
Publication of JPH0985269A publication Critical patent/JPH0985269A/en
Pending legal-status Critical Current

Links

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  • Treatment Of Biological Wastes In General (AREA)
  • Removal Of Floating Material (AREA)

Abstract

PROBLEM TO BE SOLVED: To prevent the discharge of a suspended substance such as a scum to the outside of an apparatus even when the inflow amt. of sewage per a unit time fluctuates suddenly. SOLUTION: Sewage flows from an aeration decomposition chamber 10 to a sedimentation chamber 19 through an opening part 14 provided in the vicinity of the water surface of a partition wall 13 partitioning both chambers 10, 19 and a filter 17 is provided to the opening part 14 on the side of the aeration decomposition chamber 10 in a detachable manner and a scum skimmer 22 and an air lift pump 25 cooperating therewith are provided on the side of the sedimentation chamber 19.

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】本発明は、汚水処理装置に関
し、詳しくは、汚水処理装置の最終段階である消毒室に
至るまでの間で、汚水中に混入している浮遊物質を確実
に捕捉して除去することにより、放流水の水質改善を図
り得る汚水処理装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a sewage treatment apparatus, and more specifically, it reliably captures suspended matter mixed in sewage before reaching the disinfection chamber, which is the final stage of the sewage treatment apparatus. The present invention relates to a sewage treatment apparatus that can improve the water quality of discharged water by removing it.

【0002】[0002]

【従来の技術】従来の汚水処理装置、例えば接触曝気式
浄化槽では、汚水取入れ口から槽内に流入した汚水が、
固液分離沈澱室または嫌気濾床室、曝気分解室、沈澄室
(沈澱室)等を通過する間に、段階的に処理が重ねら
れ、沈澄室の上澄液を越流堰により取水して消毒室へ流
入させ、該消毒室に設けた排水口から逐次排水させるよ
うになっている。
2. Description of the Related Art In a conventional sewage treatment apparatus, for example, a contact aeration type septic tank, the sewage flowing into the tank from the sewage inlet is
While passing through the solid-liquid separation settling room or the anaerobic filter bed room, the aeration decomposition room, the precipitation room (precipitation room), etc., the treatment is repeated step by step, and the supernatant liquid of the precipitation room is taken by the overflow weir. Then, it is made to flow into the disinfection chamber and is sequentially drained from the drain port provided in the disinfection chamber.

【0003】ところが、汚水取入れ口から槽内に流入す
る単位時間当たりの汚水量は、常時一定ではなく、生活
排水の使用が最も多い朝の時間帯に偏重し勝ちである。
従って、槽内での汚水の移流も不安定となり、一時的に
急激な水の流れが生じ、その際には、曝気分解室や沈澄
室の汚水も消毒室を経て大量に槽外に排水されるのであ
る。
However, the amount of sewage flowing into the tank from the sewage inlet per unit time is not always constant, and tends to be concentrated in the morning hours when the domestic wastewater is most used.
Therefore, the advection of sewage in the tank becomes unstable, and a sudden rapid flow of water occurs.At that time, a large amount of sewage in the aeration decomposition chamber and the sedimentation chamber is also discharged outside the tank through the disinfection chamber. Is done.

【0004】このとき、曝気分解室や沈澄室では、濾床
や槽壁等に付着していた生物膜が剥離したり、或いは沈
降中の浮遊物質や既に沈澱分離されていた汚泥、剥離生
物膜等の微細遊離体(これらを纏めて以下単に「スカム
等」という)が、水流の勢いで巻き上げられたりして水
面上に浮上し、消毒室から槽外に流出するのである。
At this time, in the aeration decomposition chamber and the sedimentation chamber, the biofilm adhering to the filter bed, the tank wall, or the like is peeled off, or the floating substances in the sedimentation, the sludge that has been separated by sedimentation, and the peeled biofilm are separated. The microscopic loose bodies (collectively referred to as "scums" hereinafter) are floated on the surface of the water by being swirled up by the force of the water flow and flow out of the disinfection chamber to the outside of the tank.

【0005】このようにして、本来は汚水内のスカム等
を自然に沈降させて上澄液のみを消毒室内に送り込む為
に設けられた部屋である筈の沈澄室が、実際にはスカム
等が浮遊し易く、放流水中に混入して排出されることが
あり、このようなスカム等は高いBOD値を示すところ
から、放流水の水質維持の為には、出来るだけ捕捉・排
除する必要があった。
In this way, the settling chamber, which is supposed to be a room originally designed to naturally settle the scum and the like in the sewage and send only the supernatant into the disinfecting chamber, is actually the scum and the like. Are easily floated and may be mixed in the discharged water and discharged. Since such scums have a high BOD value, it is necessary to capture and eliminate them as much as possible to maintain the quality of the discharged water. there were.

【0006】そこで、この問題解決の為に従来より種々
の工夫がなされてきたが、例えば実公平1−4469号
公報には、沈澄室の中程に繊維体で形成されたフィルタ
ーを配設し、曝気分解室からのスカム等を濾過・捕捉
し、放流水への混入を防止する技術が開示されている。
Therefore, various measures have been conventionally made to solve this problem. For example, in Japanese Utility Model Publication No. 1-4469, a filter made of a fibrous body is arranged in the middle of the sedimentation chamber. However, a technique is disclosed in which scum or the like from the aeration decomposition chamber is filtered and captured to prevent the scum from being mixed into the discharged water.

【0007】[0007]

【発明が解決しようとする課題】しかしながら、この従
来技術の場合、沈澄室に配設されるフィルターは嵩高で
あるため、沈澄室の有効容量がそれだけ減少してその機
能が低下するばかりでなく、フィルターの密度が高いこ
とによる目詰まりが起こり易いので、逆洗設備も必要と
した。
However, in the case of this prior art, since the filter provided in the clarification chamber is bulky, the effective capacity of the clarification chamber is reduced to that extent and its function is deteriorated. However, since the filter density is high and clogging is likely to occur, a backwash facility was also required.

【0008】この逆洗設備は、曝気分解室に使用してい
る散気管を、上端を軸にして随時回動し、沈澄室下部よ
り散気してフィルターを洗う方法である。しかし、逆洗
後沈澄室上部に浮遊したスカム等を完全に排除するに
は、フィルターを水面まで引き上げてスカム等の消毒室
への移流を防止すると共に沈澄室での再沈降を待たねば
ならず、浄化槽の機能が回復するまでに時間を要すると
いう問題があった。
This backwashing equipment is a method for washing the filter by rotating the air diffuser pipe used in the aeration decomposition chamber at any time with the upper end as an axis to diffuse air from the lower portion of the sedimentation chamber. However, in order to completely remove scum floating in the upper part of the sedimentation chamber after backwashing, the filter should be raised to the surface of the water to prevent advection of scum to the disinfection chamber and wait for re-sedimentation in the sedimentation chamber. However, there is a problem that it takes time to restore the function of the septic tank.

【0009】本発明は、上述のようなスカム等の処理上
の問題点を解決し、変動の激しい流入汚水にも追従して
スカム等が槽外に排出されるのを確実に防止できる汚水
処理装置を提供することを目的とする。
The present invention solves the above-mentioned problems in the treatment of scum and the like, and can reliably prevent the scum and the like from being discharged outside the tank by following the influent wastewater that fluctuates greatly. The purpose is to provide a device.

【0010】[0010]

【課題を解決するための手段】請求項1記載の発明の汚
水処理装置は、「移流方向に少なくとも曝気分解室、沈
澄室及び消毒室を有してなる汚水処理装置において、曝
気分解室から沈澄室への移流が両室を仕切る隔壁の水面
付近に設けられた開口部によって可能となされ、この開
口部の曝気分解室側にはフィルターが嵌脱可能に装着さ
れ、沈澄室側にはスカムスキマ及びこれと連動するエア
リフトポンプが付設されてなること」を特徴とするもの
であり、このことにより上記目的が達成される。
The sewage treatment apparatus according to the first aspect of the present invention is a sewage treatment apparatus having at least an aeration decomposition chamber, a sedimentation chamber and a disinfection chamber in the advection direction. Advection to the sedimentation chamber is made possible by the opening provided near the water surface of the partition that separates both chambers.A filter is removably attached to the aeration decomposition chamber side of this opening, and it is attached to the sedimentation chamber side. Is provided with a scum skimmer and an air lift pump that works in conjunction with the scum skimmer. ”This achieves the above object.

【0011】また、請求項2記載の発明の汚水処理装置
は、「移流方向に少なくとも曝気分解室、沈澄室及び消
毒室を有してなる汚水処理装置において、沈澄室が隔壁
により移流方向に向けて第一沈澄室と第二沈澄室に区画
され、隔壁の中程には上方に向け第一沈澄室側に傾斜し
た傾斜面が形成されると共にこの傾斜面に開口部が設け
られ、第一沈澄室から第二沈澄室への移流がこの開口部
によって可能となされ、開口部の第一沈澄室側にはフィ
ルターが装着され、第二沈澄室側にはスカムスキマ及び
これと連動するエアリフトポンプが付設されてなるこ
と」を特徴とするものであり、このことによっても上記
目的が達成される。
According to the second aspect of the present invention, there is provided a sewage treatment apparatus having at least an aeration decomposition chamber, a clarification chamber and a disinfection chamber in the advection direction. Is divided into a first simmering chamber and a second simmering chamber, and an inclined surface inclined upward toward the first simmering chamber is formed in the middle of the partition wall and an opening is formed in this inclined surface. Provided, advection from the first clarification chamber to the second clarification chamber is enabled by this opening, a filter is mounted on the first clarification chamber side of the opening, and on the second clarification chamber side The scum skimmer and an air lift pump that works together with the scum skimmer are additionally provided. "This also achieves the above object.

【0012】[0012]

【発明の実施の形態】以下、本発明の汚水処理装置の実
施の形態について、図面を参照しながら詳細に説明す
る。尚、図面に示す例は、本発明の汚水処理装置を家庭
用小型合併処理浄化槽に採用した場合について示すもの
である。
BEST MODE FOR CARRYING OUT THE INVENTION Hereinafter, embodiments of a wastewater treatment apparatus of the present invention will be described in detail with reference to the drawings. In addition, the example shown in the drawings shows a case where the sewage treatment apparatus of the present invention is adopted in a small household combined treatment septic tank.

【0013】図1は請求項1記載の発明の汚水処理装置
の一例について、その全体構造を示す縦断面図である。
FIG. 1 is a longitudinal sectional view showing the entire structure of an example of the sewage treatment apparatus according to the first aspect of the invention.

【0014】同図において、1は嫌気濾床第一室、2は
第一濾材、3は第一仕切り板、4は第一移流口、5は嫌
気濾床第二室であり、同じく第二濾材6、第二仕切り板
7及び第二移流口8を有する。
In the figure, 1 is an anaerobic filter bed first chamber, 2 is a first filter medium, 3 is a first partition plate, 4 is a first advection port, 5 is an anaerobic filter bed second chamber, and the second chamber is also the same. It has a filter medium 6, a second partition plate 7, and a second advection port 8.

【0015】9は汚水取り入れ口であって、ここから流
入した汚水は、嫌気濾床第一室1に入り、第一濾材2内
を通過後上昇する。そして第一仕切り板3の上端近傍に
設けられた第一移流口4を通って嫌気濾床第二室5に入
る。同様にして第二濾材6を通過後上昇する。そして第
二仕切り板7の上端近傍に設けられた第二移流口8から
曝気分解室10へ移流する。
Numeral 9 is a sewage intake, from which sewage enters the anaerobic filter bed first chamber 1, passes through the first filter medium 2 and rises. Then, it enters the anaerobic filter bed second chamber 5 through the first advection port 4 provided near the upper end of the first partition plate 3. Similarly, after passing through the second filter medium 6, it rises. Then, it is admitted to the aeration decomposition chamber 10 from the second advection port 8 provided near the upper end of the second partition plate 7.

【0016】11は接触材、12は散気管であって、何
れも曝気分解室10内に組み込まれている。散気管12
は図示しない送風機に連結され、該送風機からの圧縮空
気によりそのノズルから微細気泡を噴出し、室内に汚水
の上昇水流を形成する。この上昇水流は水面に達すると
下降水流となることにより、曝気分解室10の中に時計
回りの旋回流を形成する。
Reference numeral 11 is a contact material, and 12 is an air diffuser, both of which are incorporated in the aeration decomposition chamber 10. Air diffuser 12
Is connected to a blower (not shown), and fine air bubbles are ejected from the nozzle by compressed air from the blower to form an upward flow of sewage in the room. When this rising water flow reaches the water surface, it becomes a descending water flow, thereby forming a clockwise swirling flow in the aeration decomposition chamber 10.

【0017】一方、接触材11の表面に付着生成した生
物膜が肥厚すると、この旋回流によって剥離し、嫌気濾
床第二室5から流入してきたスカム等と一緒になって一
部は底部に沈降・堆積すると共に残りは旋回するように
なる。
On the other hand, when the biofilm adhering to the surface of the contact material 11 is thickened, it is separated by this swirling flow, and a part of the biofilm adheres to the bottom of the anaerobic filter bed 5 together with scum and the like. As it settles and accumulates, the rest turns.

【0018】13は曝気分解室10と後述する沈澄室と
を仕切る隔壁であり、その下端は槽の底壁に接続されて
両室を区画している。また、隔壁13の上縁は水面から
15〜20cm程度突き出ており、その水面付近にはや
や大きめの、正面視が方形を呈する開口部14が設けら
れ、曝気分解室10から沈澄室への移流が、この開口部
14によって可能となされている。
Reference numeral 13 is a partition wall for partitioning the aeration decomposition chamber 10 and a sedimentation chamber, which will be described later, and the lower end of the partition wall is connected to the bottom wall of the tank to define both chambers. Further, the upper edge of the partition wall 13 projects about 15 to 20 cm from the water surface, and a slightly larger opening 14 having a square shape when viewed from the front is provided in the vicinity of the water surface, and from the aeration decomposition chamber 10 to the sedimentation chamber. Advection is made possible by this opening 14.

【0019】図2(イ)は、この開口部14とこれに装
着されたフィルターとを取り出して示す一部切欠分解斜
視図であり、同図(ロ)は、その内フィルターのみを取
り出して示す斜視図である。
FIG. 2A is a partially cutaway exploded perspective view showing the opening 14 and the filter attached to the opening 14, and FIG. 2B shows only the inner filter. It is a perspective view.

【0020】開口部14の曝気分解室10側には、該開
口部14よりも大寸法にして、上縁が欠如された額縁状
の保持枠15が突設され、隔壁13の壁面との間に後述
するフィルターの嵌脱可能な嵌挿溝16が形成されてい
る。
On the side of the aeration decomposition chamber 10 of the opening 14, a frame-shaped holding frame 15 having a size larger than that of the opening 14 and lacking the upper edge is provided so as to project between the wall surface of the partition wall 13. Further, a fitting insertion groove 16 into which a filter described later can be fitted and removed is formed.

【0021】17はフィルターであって、ポリエチレン
繊維からなる0.5〜1mm程度の厚みの不織布を重ね
合わせ、約5mmの厚みの板状にしたものである。嵌挿
溝16の溝面に接する外周縁はゴムスポンジ製の縁枠1
8で縁取りすることにより、その縁部の補強、嵌脱の容
易性及びパッキンの機能を付与しており、汚水中のスカ
ム等が嵌挿溝16の溝面と縁枠18との間から浸入しな
いように配慮されている。
Reference numeral 17 denotes a filter, which is formed by laminating non-woven fabrics made of polyethylene fibers and having a thickness of about 0.5 to 1 mm, and forming a plate shape having a thickness of about 5 mm. The outer peripheral edge in contact with the groove surface of the fitting groove 16 is an edge frame 1 made of rubber sponge.
By edging at 8, the edge portion is reinforced, the fitting / removal is facilitated, and the packing function is provided, and scum in the dirty water enters from between the groove surface of the fitting insertion groove 16 and the edge frame 18. It is considered not to do so.

【0022】このフィルター17は、開口部14の曝気
分解室10側に設ける必要がある。沈澄室側に設けたの
では、フィルター交換時にスカム等が該沈澄室に混入し
易くなる。また、フィルターの交換は定期的に行って水
質維持を図り、またその交換の作業性を良くする為に、
その上縁を水面から突き出るようになし、その部分を交
換時の把持部とするのがよく、また、予め複数個の新品
もしくは清掃済みのフィルターを準備しておけば、交換
は瞬時に行うことができる。
This filter 17 must be provided on the side of the aeration decomposition chamber 10 of the opening 14. If the filter is provided on the side of the sedimentation chamber, scum or the like is easily mixed in the sedimentation chamber when the filter is replaced. Also, in order to maintain the water quality by regularly replacing the filter and improve the workability of the replacement,
The upper edge should be projected from the surface of the water, and that part should be used as a grip for replacement.Also, if you have prepared multiple new or cleaned filters in advance, replacement should be done instantly. You can

【0023】19は沈澄室、20は越流堰、21は消毒
室、22はスカムスキマである。このスカムスキマ22
は、沈澄室19の水面より約5mm程度低い位置に、越
流堰20と相対するようにして開口部14の沈澄室19
側に取り付けられている。
Reference numeral 19 is a sedimentation chamber, 20 is an overflow weir, 21 is a disinfection chamber, and 22 is a scum skimmer. This scum gap 22
Is located at a position about 5 mm lower than the water surface of the sedimentation chamber 19 so as to face the overflow weir 20.
It is attached to the side.

【0024】図3は図1に示す汚水処理装置の点検蓋を
取り外して内部を示す要部のみの平面図である。
FIG. 3 is a plan view of only the main part showing the inside of the sewage treatment apparatus shown in FIG. 1 with the inspection lid removed.

【0025】スカムスキマ22は、図2(ハ)及び図3
にも示すように、平面視が長方形にして漏斗状を呈する
杓子部23と、そのほぼ中央部から垂下された吸込管2
4とからなっている。杓子部23の長手方向の寸法が、
越流堰20のそれに対して約1/2となされ、出来るだ
け水面全体からスカム等を吸い寄せられるようになって
いる。
The scum skimmer 22 is shown in FIGS.
As also shown, the scooping part 23 having a rectangular shape in a plan view and having a funnel shape, and the suction pipe 2 suspended from substantially the center part thereof.
It consists of 4. The longitudinal dimension of the ladle 23 is
It is made about 1/2 of that of the overflow weir 20, so that scum etc. can be sucked from the entire water surface as much as possible.

【0026】25はエアリフトポンプであって、揚水管
26と、その下端に接続された空気圧送管27と、図示
しない空気調整用バルブ及びコンプレッサー等の圧縮空
気源とからなり、スカムスキマ22にほぼ接して配設さ
れている。
An air lift pump 25 is composed of a pumping pipe 26, an air pressure feeding pipe 27 connected to the lower end of the pump 26, and a compressed air source such as an air adjusting valve and a compressor (not shown), which is almost in contact with the scum skimmer 22. Are arranged.

【0027】スカムスキマ22とエアリフトポンプ25
とは、連携してその機能を発揮するものであり、図2
(ハ)に示すように、吸込管24の下端が揚水管26の
中程に接続され、エアリフトポンプ25を駆動すれば、
揚水管26から常時5〜10リットルの汚水が揚水でき
るようになっている。
The scum skimmer 22 and the air lift pump 25
Is a function that works in cooperation with each other.
As shown in (c), if the lower end of the suction pipe 24 is connected to the middle of the pumping pipe 26 and the air lift pump 25 is driven,
5 to 10 liters of sewage can be pumped from the pumping pipe 26 at all times.

【0028】このようにして、スカムスキマ22の杓子
部23で捕集された汚水は、エアリフトポンプ25の駆
動により吸込管24内に吸い込まれ、揚水管26の上部
まで揚水されるのである。
In this way, the dirty water collected by the scooping portion 23 of the scum skimmer 22 is sucked into the suction pipe 24 by the drive of the air lift pump 25, and is pumped up to the upper part of the pump pipe 26.

【0029】28、28は返送管、29は曝気分解室1
0の沈降・堆積したスカム等の返送用エアリフトポンプ
の揚水管であって、該返送用エアリフトポンプは、この
揚水管と、図示しない空気圧送管、空気調整用バルブ及
びコンプレッサー等の圧縮空気源とからなる。尚、この
エアリフトポンプは、常時作動させて一定量、例えば沈
澄室19への流入汚水の2〜5倍程度常時返送しておれ
ば、汚水の脱窒効果も向上する。
28, 28 are return pipes, 29 is aeration decomposition chamber 1
0 is a pumping pipe of a return air lift pump for settling / accumulating scum and the like, and the returning air lift pump includes this pumping pipe and a compressed air source such as an air pressure feeding pipe, an air adjusting valve and a compressor. Consists of. In addition, if this air lift pump is operated at all times and constantly returns a fixed amount, for example, about 2 to 5 times the inflowing wastewater into the sedimentation chamber 19, the denitrification effect of the wastewater is also improved.

【0030】かくして、揚水管26の上部まで揚水され
たスカムスキマ22の汚水は、横引きチーズのところで
横引きされ、返送管28に送られると共に、揚水管29
により圧送されてきた曝気分解室10の返送スカム等と
合流し、嫌気濾床第一室1に返送されるようになってい
る。
Thus, the sewage of the scum skimmer 22 pumped up to the upper portion of the pumping pipe 26 is laterally drawn at the sideways cheese and sent to the return pipe 28 and the pumping pipe 29.
It joins with the return scum and the like of the aeration decomposition chamber 10 that has been pressure-fed by and is returned to the anaerobic filter bed first chamber 1.

【0031】上述の請求項1記載の発明の汚水処理装置
の主な作用について纏めて述べると、嫌気濾床第一室1
及び嫌気濾床第二室5で処理された汚水は、汚水濃度が
平均化されて曝気分解室10に流入する。散気管12か
らの空気により旋回流を発生し、有機質成分が好気性菌
により分解処理されると共に、沈降・堆積したスカム等
は嫌気濾床第一室1に返送される。
The main operation of the sewage treatment apparatus according to the first aspect of the present invention will be summarized below. The anaerobic filter bed first chamber 1
The sewage treated in the anaerobic filter bed second chamber 5 flows into the aeration decomposition chamber 10 after the sewage concentration is averaged. A swirl flow is generated by the air from the air diffuser 12, the organic components are decomposed by aerobic bacteria, and the scum and the like that have settled and accumulated are returned to the anaerobic filter bed first chamber 1.

【0032】一方、上澄み液はフィルター17を通っ
て、開口部14から沈澄室19に流入する。このとき上
澄み液中のスカム等は、曝気分解室10内でフィルター
17により捕捉される。即ち、曝気分解室10で処理さ
れた汚水は、このフィルター17を通らなければ、沈澄
室19、消毒室21へと移流することができない。従っ
て、短時間に大量の汚水が流入した場合でも、曝気分解
室10でのスカム等はこのフィルター17によって捕捉
することができる。
On the other hand, the supernatant passes through the filter 17 and flows into the precipitation chamber 19 through the opening 14. At this time, scum and the like in the supernatant liquid are captured by the filter 17 in the aeration decomposition chamber 10. That is, the wastewater treated in the aeration decomposition chamber 10 cannot be admitted to the clarification chamber 19 and the disinfection chamber 21 unless it passes through the filter 17. Therefore, even if a large amount of dirty water flows in in a short time, scum in the aeration decomposition chamber 10 can be captured by the filter 17.

【0033】また、フィルタ17の目を透過して浸入し
た微細なスカム等や、フィルター17の交換中に通過し
たスカム等、或いは短時間に大量の汚水が流入した場合
に、沈澄室19内で舞い上がったスカム等については、
スカムスキマ22によって捕捉され、エアリフトポンプ
25との共働により嫌気濾床第一室1に返送されるので
ある。
Further, in the case where a fine scum which has penetrated through the eyes of the filter 17 or the like, a scum which has passed through during the replacement of the filter 17, or a large amount of dirty water has flowed in in a short time, the inside of the sedimentation chamber 19 For the scum that came up in,
It is captured by the scum skimmer 22 and returned to the anaerobic filter bed first chamber 1 in cooperation with the air lift pump 25.

【0034】このように、請求項1記載の発明の場合、
スカム等の除去設備はフィルター17と、スカムスキマ
22及びエアリフトポンプ25とからなる二段構えにな
っているので、スカム等が確実に除去された汚水とな
り、沈澄室19から越流堰20を経由して消毒室21に
移流し、消毒剤による殺菌を受けた後、排水口30より
逐次放流されるのである。
Thus, in the case of the invention according to claim 1,
The removal equipment for scum and the like has a two-stage structure consisting of a filter 17, a scum skimmer 22 and an air lift pump 25, so that scum and the like is reliably removed and becomes wastewater from the sedimentation chamber 19 through the overflow weir 20. Then, it is admitted to the disinfection chamber 21, and after being sterilized by the disinfectant, it is sequentially discharged from the drainage port 30.

【0035】請求項1記載の発明に係る上記例では、フ
ィルターは、ポリエチレン繊維からなる不織布で製せら
れた例を示したが、必ずしもこれに限定されず、その他
各種天然繊維や合成繊維からなる織布、網布、不織布等
の繊維状の板状構成体が採用される。また、より効果的
なフィルターを得る方法の一つとして、下流側に向けて
順次網目の細かい板状構成体を重ね合わせる方法があ
る。
In the above-mentioned example according to the invention described in claim 1, the filter is made of a non-woven fabric made of polyethylene fiber, but the present invention is not limited to this, and it is made of various other natural fibers and synthetic fibers. A fibrous plate-like structure such as a woven cloth, a net cloth, or a non-woven cloth is used. Further, as one of the methods for obtaining a more effective filter, there is a method of sequentially laminating plate-like structural bodies having fine meshes toward the downstream side.

【0036】フィルターの素材の他の具体例として、ポ
リエチレン、ポリプロピレン、ウレタン、ポリ塩化ビニ
ル等の合成樹脂、或いは天然ゴムやクロロプレン、シリ
コン、ブタジエンアクリロニトリルゴム(NBR)、エ
チレンプロピレンゴム(EPR)等の合成ゴム製の板状
を呈する連続気泡発泡体が挙げられる。要は、液体を通
過させ且つ濾過させるところの、凡そ0.1〜5mm以
下の通水孔を有するものであれば、特に材質は限定され
ない。
Other specific examples of the material of the filter include synthetic resins such as polyethylene, polypropylene, urethane and polyvinyl chloride, natural rubber, chloroprene, silicon, butadiene acrylonitrile rubber (NBR) and ethylene propylene rubber (EPR). An open-cell foam having a plate shape made of synthetic rubber can be used. In short, the material is not particularly limited as long as it has water passage holes of about 0.1 to 5 mm or less through which the liquid is passed and filtered.

【0037】開口部の大きさ及びフィルタの種類、濾過
する目の大きさ等は、最も使用水量の多い朝の時間帯の
流入水によって、異常に水位が上昇して次の処理室での
処理工程に短絡を起こし、未処理水が移流することがな
いように、各汚水処理装置について個別に実験し、最適
のものを設計乃至選定して使用するのが好ましい。
Regarding the size of the opening, the type of filter, the size of the filter eye, etc., the water level rises abnormally due to the inflow of water during the morning when the amount of water used is the largest, and the treatment in the next treatment chamber is performed. In order to prevent short-circuiting in the process and advection of untreated water, it is preferable to individually test each sewage treatment apparatus and design or select the optimal one for use.

【0038】フィルター選定の一つの目安としては、通
常の一日の平均流入汚水量を求め、その6〜10倍位の
汚水が、10分程度の間に連続して流入しても、短絡が
起こらない程度のものを選定すれば充分に安全性が保た
れる。
As one guideline for selecting a filter, a normal daily average inflow sewage amount is obtained, and even if 6 to 10 times the average inflow sewage flow continuously for about 10 minutes, a short circuit will occur. Sufficient safety will be maintained if a material that does not occur is selected.

【0039】図4は請求項2記載の発明の汚水処理装置
の一例について、その全体構造を示す縦断面図である。
尚、上述の請求項1記載の発明の汚水処理装置と同一部
分には同一符号を付し、重複する説明は省略する。
FIG. 4 is a vertical cross-sectional view showing the entire structure of an example of the wastewater treatment apparatus of the second aspect of the invention.
The same parts as those of the sewage treatment apparatus according to the first aspect of the present invention will be designated by the same reference numerals, and overlapping description will be omitted.

【0040】31は隔壁、32は第一沈澄室、33は第
二沈澄室であって、隔壁31により曝気分解室10と第
一沈澄室32とが区画されているが、隔壁31の下端縁
は、槽の底壁から遊離され、間隙34が形成されてい
る。また、該隔壁31の水面下2cmのところに返送口
35が設けられ、該返送口35に沿って返送板36が突
設されている。
Reference numeral 31 is a partition wall, 32 is a first clarification chamber, and 33 is a second clarification chamber. The partition wall 31 divides the aeration decomposition chamber 10 and the first clarification chamber 32. The lower end edge of is separated from the bottom wall of the tank to form a gap 34. A return port 35 is provided 2 cm below the water surface of the partition wall 31, and a return plate 36 is provided so as to project along the return port 35.

【0041】散気管12が、隔壁31の下端近辺の曝気
分解室10側に組み込まれており、微細気泡の噴出によ
る汚水の上昇水流を形成する。この上昇水流は水面付近
で返送板36に当たって移流方向とは逆方向に流れ、全
体として反時計回りの旋回流を形成する。このとき、第
一沈澄室32の水面のスカム等は返送口35を通って曝
気分解室10に返送される。
The air diffuser 12 is incorporated near the lower end of the partition wall 31 on the side of the aeration decomposition chamber 10 and forms an upward flow of sewage due to the ejection of fine bubbles. This rising water flow hits the return plate 36 near the water surface and flows in the direction opposite to the advection direction, and forms a counterclockwise swirling flow as a whole. At this time, the scum on the water surface of the first sedimentation chamber 32 is returned to the aeration decomposition chamber 10 through the return port 35.

【0042】また、曝気分解室10の沈降・堆積したス
カム等の返送用エアリフトポンプの揚水管29が設けら
れているが、前述の請求項1記載の発明の例とその機能
がほぼ同じであるから詳細な説明を省略する。
Further, although the pumping pipe 29 of the air lift pump for returning the settled / accumulated scum in the aeration decomposition chamber 10 is provided, its function is almost the same as the example of the invention described in claim 1. The detailed description will be omitted.

【0043】また、隔壁31の下端には整流板37が設
けられ、曝気分解室10の旋回流により第一沈澄室32
の底部に堆積したスカム等を吸い寄せて曝気分解室10
側に返送されるようになっている。38は遮蔽板であっ
て、曝気分解室10の旋回流が、第二移流口8に逆流す
るのを防止する為のものである。
Further, a rectifying plate 37 is provided at the lower end of the partition wall 31, and the swirling flow of the aeration decomposition chamber 10 causes the first precipitation chamber 32 to flow.
Aeration decomposition chamber 10 by attracting scum accumulated on the bottom of
It is supposed to be returned to the side. Reference numeral 38 is a shield plate for preventing the swirling flow of the aeration decomposition chamber 10 from flowing back to the second advection port 8.

【0044】39は第一沈澄室32と第二沈澄室33と
を区画する隔壁であり、その中程、水深の約1/2程度
の深さのところで、上方に向け第一沈澄室32側に約4
5°傾斜した高さ約25cmの傾斜面40が形成され、
この傾斜面40に高さ20×幅50cmの開口部41が
設けられている。
Reference numeral 39 is a partition wall for partitioning the first clarification chamber 32 and the second clarification chamber 33. In the middle thereof, at a depth of about ½ of the water depth, the first clarification chamber is directed upward. About 4 on the room 32 side
An inclined surface 40 having a height of about 25 cm inclined by 5 ° is formed,
The inclined surface 40 is provided with an opening 41 having a height of 20 and a width of 50 cm.

【0045】図5はスカムスキマとエアリフトポンプ、
並びに開口部41とフィルターの配設状態及びその作動
を説明する為の斜視図である。
FIG. 5 shows a scum skimmer and an air lift pump,
FIG. 6 is a perspective view for explaining the arrangement state of the opening 41 and the filter and the operation thereof.

【0046】この開口部41には、ポリエチレン製繊維
の不織布からなるフィルター42が第一沈澄室32側に
ビス止めにより取着されている。尚、このフィルター4
2は、請求項1記載の発明に係る前記例のように嵌脱可
能にすることは任意である。
A filter 42 made of polyethylene fiber non-woven fabric is attached to the opening 41 on the first clarification chamber 32 side with screws. In addition, this filter 4
It is optional that the item 2 can be inserted and removed as in the example according to the first aspect of the invention.

【0047】第一沈澄室32から第二沈澄室33への移
流は、この開口部41によって可能である。43は、フ
ィルター41の目詰まり時に作動させる逆洗管である。
スカムスキマ22、エアリフトポンプ25等は、前述の
請求項1記載の発明の例とその機能がほぼ同じであるか
ら詳細な説明を省略する。
Advection from the first clarification chamber 32 to the second clarification chamber 33 is possible by this opening 41. Reference numeral 43 is a backwash pipe that is activated when the filter 41 is clogged.
The functions of the scum skimmer 22 and the air lift pump 25 and the like are almost the same as those of the example of the invention described in claim 1, and therefore detailed description thereof will be omitted.

【0048】上述の請求項2記載の発明の汚水処理装置
の主な作用について纏めて述べると、嫌気濾床第一室1
及び嫌気濾床第二室5で処理された汚水は、汚水濃度が
平均化されて曝気分解室10に流入する。散気管12か
らの空気により反時計回りの旋回流を発生し、有機質成
分が好気性菌により分解処理されると共に、沈降・堆積
したスカム等は揚水管29により嫌気濾床第一室1に返
送される。
The main operation of the sewage treatment apparatus according to the second aspect of the present invention will be summarized below. The anaerobic filter bed first chamber 1
The sewage treated in the anaerobic filter bed second chamber 5 flows into the aeration decomposition chamber 10 after the sewage concentration is averaged. A counterclockwise swirling flow is generated by the air from the air diffuser 12 and the organic components are decomposed by aerobic bacteria, and the settled / accumulated scum and the like are returned to the anaerobic filter bed first chamber 1 by the pumping pipe 29. To be done.

【0049】一方、汚水は間隙34を通って第一沈澄室
32に入り、更にフィルター42を通過して開口部41
から第二沈澄室33に入る。このとき上澄み液中のスカ
ム等はフィルター42で捕捉される。即ち、曝気分解室
10で処理された汚水は、このフィルター42を経由し
て開口部41を通らなければ、第二沈澄室32、消毒室
21へと移流することができない。従って、短時間に大
量の汚水が流入した場合でも、曝気分解室10でのスカ
ム等はこのフィルター42によって捕捉することができ
る。
On the other hand, the sewage enters the first clarification chamber 32 through the gap 34, further passes through the filter 42 and the opening 41.
Then, the second sedimentation chamber 33 is entered. At this time, scum or the like in the supernatant is captured by the filter 42. That is, the sewage treated in the aeration decomposition chamber 10 cannot be transferred to the second clarification chamber 32 and the disinfection chamber 21 unless it passes through the opening 41 through the filter 42. Therefore, even if a large amount of dirty water flows in in a short time, scum in the aeration decomposition chamber 10 can be captured by the filter 42.

【0050】また、フィルター42の目を透過して浸入
したスカム等、或いは短時間に大量の汚水が流入した際
に、第二沈澄室33内で舞い上がったスカム等について
は、スカムスキマ22によって捕捉され、エアリフトポ
ンプ25との共働により嫌気濾床第一室1に返送され
る。
The scum skimmer 22 captures scum that has penetrated through the eyes of the filter 42, or scum that has risen in the second sedimentation chamber 33 when a large amount of dirty water has flowed in in a short time. Then, it is returned to the anaerobic filter bed first chamber 1 in cooperation with the air lift pump 25.

【0051】フィルター42は深いところにあり、しか
も固定式であるから、若し目詰まりを起こしたならば、
逆洗管43を作動させて洗い落とせばよく、その作動中
もフィルター42から離脱したスカム等は第二沈澄室3
3には流入しないので、汚水処理装置の機能は低下する
ことがない。
Since the filter 42 is located deep and is of a fixed type, if it is clogged,
It suffices to operate the backwash pipe 43 to wash it off, and scum and the like separated from the filter 42 during the operation are removed from the second clarification chamber 3
Since it does not flow into No. 3, the function of the sewage treatment apparatus does not deteriorate.

【0052】このように、請求項1記載の発明の場合と
同様に、スカム等の除去設備はフィルター42と、スカ
ムスキマ22及びエアリフトポンプ25とからなる二段
構えになっているので、スカム等が確実に除去された汚
水が、第二沈澄室33から越流堰20を経由して消毒室
21に移流し、消毒剤による殺菌を受けた後、排水口3
0より逐次放流されるのである。
As described above, as in the case of the first aspect of the present invention, the scum removing device has a two-stage structure including the filter 42, the scum skimmer 22 and the air lift pump 25. The sewage that has been reliably removed is transferred from the second sedimentation chamber 33 to the disinfection chamber 21 via the overflow weir 20, and after being sterilized by the disinfectant, the drainage port 3
It is released successively from 0.

【0053】尚、フィルターの素材や構造、開口部の大
きさとの関連、選定の目安等は、前述の請求項1記載の
発明の場合と同様であるから省略する。
The material and structure of the filter, the relationship with the size of the opening, the standard of selection, etc. are the same as in the case of the above-mentioned invention of claim 1, and therefore will be omitted.

【0054】[0054]

【発明の効果】本発明の汚水処理装置は、曝気分解室か
ら沈澄室、或いは第一沈澄室から第二沈澄室への移流の
際、それぞれを区画する隔壁に設けた開口部のみを必ず
通るようになし、しかもこの開口部にはフィルターを装
着したので、特に、大量の汚水が短時間に流入する朝の
時間帯等において、曝気分解室や第一沈澄室での急激な
水質低下があっても、スカム等の消毒室への流出をフィ
ルターで効果的に捕捉できるので、排水の水質低下を防
止できる。
The sewage treatment apparatus of the present invention has only the opening provided in the partition wall for partitioning each of the aeration decomposition chamber and the sedimentation chamber or the first sedimentation chamber to the second sedimentation chamber when advancing. Since a filter is attached to this opening, there is a sudden increase in the aeration decomposition chamber and the first sedimentation chamber, especially in the morning hours when a large amount of dirty water flows in in a short time. Even if the water quality deteriorates, the outflow of scum or the like to the disinfection chamber can be effectively captured by the filter, so that the deterioration of the water quality of the wastewater can be prevented.

【0055】また、フィルターの目詰まり対策として、
請求項1記載の発明の場合は、フィルターを嵌脱可能と
したので、交換が円滑に且つ速やかになされ、交換時に
浄化槽としての機能を殆ど低下することなくそのまま持
続させることが出来る。また、請求項2記載の発明の場
合は、逆洗管の設置によりその洗浄操作が簡単に実施で
き、しかも逆洗後のスカム等の流出防止に格別の操作等
を必要としない。
As a measure against clogging of the filter,
In the case of the invention described in claim 1, since the filter can be fitted and removed, replacement can be smoothly and promptly performed, and the function as a septic tank can be maintained as it is at the time of replacement without being substantially deteriorated. In the case of the second aspect of the invention, the washing operation can be easily performed by installing the backwash pipe, and no special operation or the like is required to prevent outflow of scum after the backwash.

【0056】また更に、フィルターの交換時や逆洗時等
で、万が一、第一沈澄室や第二沈澄室でスカム等が侵入
乃至浮上することを配慮して、スカムスキマとエアリフ
トポンプとからなる捕捉装置を付設し、スカム等の捕集
手段を二段構えとしたので、水質改善をより確実に行う
ことができ、安心して排水することができる汚水処理装
置となっている。
Furthermore, in consideration of scum and the like invading or floating in the first clarification chamber and the second clarification chamber when the filter is replaced or backwashed, the scum skimmer and the air lift pump should be taken into consideration. Since the following trapping device is attached and the trapping means such as scum is provided in two stages, the water quality can be improved more reliably and the wastewater treatment device can be discharged with peace of mind.

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

【図1】請求項1記載の発明の汚水処理装置の一例につ
いて、その全体構造を示す縦断面図である。
FIG. 1 is a vertical cross-sectional view showing the entire structure of an example of a sewage treatment apparatus according to the first aspect of the invention.

【図2】同図(イ)は同上装置のうち、開口部及びこの
開口部に対するフィルターの取付状態を示す一部切欠斜
視図であり、同図(ロ)はフィルターのみを示す斜視図
であり、同図(ハ)はスカムスキマとエアリフトポンプ
の配設状態及びその作動を説明する為の斜視図である。
FIG. 2 (a) is a partially cutaway perspective view showing an opening and a mounting state of a filter with respect to the opening in the same apparatus, and FIG. 2 (b) is a perspective view showing only the filter. FIG. 3C is a perspective view for explaining the disposition state of the scum skimmer and the air lift pump and the operation thereof.

【図3】図1に示す汚水処理装置の点検蓋を取り外して
内部を示す要部のみの平面図である。
FIG. 3 is a plan view of only a main part showing the inside of the sewage treatment apparatus shown in FIG. 1 with an inspection lid removed.

【図4】請求項2記載の発明の汚水処理装置の一例につ
いて、その全体構造を示す縦断面図である。
FIG. 4 is a vertical cross-sectional view showing the entire structure of an example of the sewage treatment apparatus according to the second aspect of the invention.

【図5】同上においてスカムスキマとエアリフトポン
プ、並びに開口部とフィルターの配設状態及びその作動
を説明するための斜視図である。
FIG. 5 is a perspective view for explaining a disposition state of a scum skimmer and an air lift pump, an opening portion and a filter, and an operation thereof in the above.

【符号の説明】[Explanation of symbols]

1 嫌気濾床第一室 5 嫌気濾床第二室 9 汚水取入れ口 10 曝気分解室 11 接触材 13、31、39 隔壁 14、41 開口部 15 保持枠 16 嵌挿溝 17、42 フィルター 19 沈澄室 21 消毒室 22 スカムスキマ 23 杓子部 24 吸込管 25 エアリフトポンプ 26、29 揚水管 27 空気圧送管 30 排水口 32 第一沈澄室 33 第二沈澄室 34 間隙 40 傾斜面 42 逆洗管 1 Anaerobic filter bed 1st chamber 5 Anaerobic filter bed 2nd chamber 9 Sewage intake 10 Aeration decomposition chamber 11 Contact material 13, 31, 39 Partition wall 14, 41 Opening 15 Holding frame 16 Fitting groove 17, 42 Filter 19 Sedimentation Room 21 Disinfection room 22 Scum skimmer 23 Scoop 24 Suction pipe 25 Air lift pump 26, 29 Pumping pipe 27 Air pressure feeding pipe 30 Drain 32 First clarification chamber 33 Second clarification chamber 34 Gap 40 Slope 42 Backwash pipe

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 移流方向に少なくとも曝気分解室、沈澄
室及び消毒室を有してなる汚水処理装置において、曝気
分解室から沈澄室への移流が両室を仕切る隔壁の水面付
近に設けられた開口部によって可能となされ、この開口
部の曝気分解室側にはフィルターが嵌脱可能に装着さ
れ、沈澄室側にはスカムスキマ及びこれと連動するエア
リフトポンプが付設されてなることを特徴とする汚水処
理装置。
1. In a sewage treatment apparatus having at least an aeration decomposition chamber, a clarification chamber and a disinfection chamber in the advection direction, advection from the aeration decomposition chamber to the clarification chamber is provided near the water surface of a partition wall separating both chambers. It is made possible by the opened opening, a filter is removably mounted on the side of the aeration decomposition chamber of this opening, and a scum skimmer and an air lift pump linked with this are attached on the side of the sedimentation chamber. Sewage treatment equipment to be.
【請求項2】 移流方向に少なくとも曝気分解室、沈澄
室及び消毒室を有してなる汚水処理装置において、沈澄
室が隔壁により移流方向に向けて第一沈澄室と第二沈澄
室に区画され、隔壁の中程には上方に向け第一沈澄室側
に傾斜した傾斜面が形成されると共にこの傾斜面に開口
部が設けられ、第一沈澄室から第二沈澄室への移流がこ
の開口部によって可能となされ、開口部の第一沈澄室側
にはフィルターが装着され、第二沈澄室側にはスカムス
キマ及びこれと連動するエアリフトポンプが付設されて
なることを特徴とする汚水処理装置。
2. A sewage treatment apparatus comprising at least an aeration decomposition chamber, a clarification chamber and a disinfection chamber in the advection direction, wherein the clarification chamber is divided by a partition wall toward the advection direction and the first clarification chamber and the second clarification chamber are provided. It is divided into chambers, and an inclined surface is formed in the middle of the partition wall so as to incline upward toward the first sedimentation chamber and an opening is provided in this inclined surface. Advection to the chamber is enabled by this opening, a filter is attached to the first clarification chamber side of the opening, and a scum skimmer and an air lift pump linked with this are attached to the second clarification chamber side. A sewage treatment device characterized by the above.
JP24939195A 1995-09-27 1995-09-27 Sewage treatment apparatus Pending JPH0985269A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP24939195A JPH0985269A (en) 1995-09-27 1995-09-27 Sewage treatment apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP24939195A JPH0985269A (en) 1995-09-27 1995-09-27 Sewage treatment apparatus

Publications (1)

Publication Number Publication Date
JPH0985269A true JPH0985269A (en) 1997-03-31

Family

ID=17192305

Family Applications (1)

Application Number Title Priority Date Filing Date
JP24939195A Pending JPH0985269A (en) 1995-09-27 1995-09-27 Sewage treatment apparatus

Country Status (1)

Country Link
JP (1) JPH0985269A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002011464A (en) * 2000-06-30 2002-01-15 Hitachi Chem Co Ltd Septic tank
JP2005185892A (en) * 2003-12-24 2005-07-14 Fuji Clean Kogyo Kk Sewage treatment device
JP2007117908A (en) * 2005-10-28 2007-05-17 Kubota Corp Septic tank
KR101414519B1 (en) * 2013-01-04 2014-07-16 한국원자력연구원 Apparatus for treatment of wastewater including pre-adjustment zone

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002011464A (en) * 2000-06-30 2002-01-15 Hitachi Chem Co Ltd Septic tank
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
JP2007117908A (en) * 2005-10-28 2007-05-17 Kubota Corp Septic tank
KR101414519B1 (en) * 2013-01-04 2014-07-16 한국원자력연구원 Apparatus for treatment of wastewater including pre-adjustment zone

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