JP2002102882A - Sewage cleaning method and apparatus - Google Patents

Sewage cleaning method and apparatus

Info

Publication number
JP2002102882A
JP2002102882A JP2000301660A JP2000301660A JP2002102882A JP 2002102882 A JP2002102882 A JP 2002102882A JP 2000301660 A JP2000301660 A JP 2000301660A JP 2000301660 A JP2000301660 A JP 2000301660A JP 2002102882 A JP2002102882 A JP 2002102882A
Authority
JP
Japan
Prior art keywords
backwashing
sludge
sewage
tank
treatment tank
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
JP2000301660A
Other languages
Japanese (ja)
Inventor
Shigeyuki Yamaguchi
重行 山口
Hideki Minoura
秀樹 箕浦
Shinya Hirota
伸也 広田
Hiroshi Kano
広志 加納
Kenji Sato
賢志 佐藤
Takayoshi Nakaoka
敬善 中岡
Mineo Itagaki
峯尾 板垣
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.)
Panasonic Electric Works Co Ltd
Original Assignee
Matsushita Electric Works 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 Matsushita Electric Works Ltd filed Critical Matsushita Electric Works Ltd
Priority to JP2000301660A priority Critical patent/JP2002102882A/en
Publication of JP2002102882A publication Critical patent/JP2002102882A/en
Pending legal-status Critical Current

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  • Treatment Of Biological Wastes In General (AREA)
  • Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a sewage cleaning method and apparatus capable of always stably cleaning sewage corresponding to a temporary change in the discharge amount of the sewage. SOLUTION: In the sewage cleaning method, a high water level position (HWL) and a low water level position (LWL) are provided in the upper part of an anaerobic treatment tank 2 to form a sewage flow rate adjusting part 3 between both positions. An aerobic treatment tank 5 equipped with a filter medium 6, a sedimentation tank 10 and a disinfection tank 11 are arranged on the downstream side of the anaerobic treatment tank 2 in this order, and a backwashing pipe 8 for back washing the filter medium 6 and an air lift pump 9 for returning sludge peeled by backwashing the filter medium 6 are provided to constitute the sewage cleaning tank A. When the liquid level of sewage in the flow rate adjusting part 3 is set in the vicinity of the lower water level position, the return of sludge is performed intermittently.

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、汚水浄化方法に関
する。さらに詳しくは、嫌気性処理槽の上部を汚水の流
量調整部とし、上記嫌気性処理槽の下流に設けられた好
気性処理槽からの汚泥返送を間欠的に行うことにより、
汚水排水量の時間的な変動に対処して、汚水処理を効率
的に行うことができる汚水浄化方法、及びそのための汚
水浄化槽に関する。
The present invention relates to a method for purifying sewage. More specifically, the upper part of the anaerobic treatment tank is a wastewater flow rate adjustment unit, by intermittently performing sludge return from the aerobic treatment tank provided downstream of the anaerobic treatment tank,
The present invention relates to a sewage purification method capable of efficiently performing sewage treatment by coping with a temporal change in sewage drainage amount, and a sewage purification tank therefor.

【0002】[0002]

【従来の技術】従来、一般家庭等から排出される汚水
を、活性汚泥を用いて浄化する方法は公知であり、嫌気
性処理された汚水を引き続き好気性処理し、剥離した汚
泥を分離して汚水を浄化する方法が一般的に行われてい
る。上記の方法に関しては、たとえば、特開昭58−1
43884号、実開平3−86094号、実開平4−2
15892号、特開平4−99295号、特開平11−
77071号等各公報に、各種の先行技術が開示されて
いる。
2. Description of the Related Art Conventionally, a method for purifying sewage discharged from general households or the like using activated sludge is known, and anaerobic treated sewage is continuously subjected to aerobic treatment, and separated sludge is separated. A method for purifying sewage is generally used. Regarding the above method, for example, Japanese Patent Application Laid-Open No. 58-1
43888, Heikai 3-86094, Heikai 4-2
15892, JP-A-4-99295, JP-A-11-
Various publications such as 77071 disclose various prior arts.

【0003】ところで、一般家庭等における汚水の排出
パターンは、人間の生活時間と密接に関係しており、排
出量の時間的変動、すなわち、朝は汚水の排出量がピー
クに達するのに対し、昼間、深夜には排出量が極端に減
るという現象が一般的にみられる。上記した排出量の時
間的変動への対処がないと、汚水の排出量が汚水浄化槽
の処理能力を一時的に上回る場合、浄化処理をされてい
ない汚水がそのまま、オーバーフローして排出したり、
浄化処理槽中に沈殿している汚泥が排水とともに排出さ
れ、水質を汚染するという問題が生じる。
By the way, the discharge pattern of sewage in general households and the like is closely related to the life time of human beings, and the temporal fluctuation of the discharge amount, that is, the discharge amount of sewage peaks in the morning, In the daytime and late at night, it is common to see a dramatic decrease in emissions. If there is no response to the above-mentioned temporal fluctuation of the discharge amount, if the discharge amount of the sewage temporarily exceeds the treatment capacity of the sewage septic tank, the sewage that has not been subjected to the sewage treatment overflows and is discharged,
There is a problem that the sludge settled in the purification tank is discharged together with the wastewater and pollutes the water quality.

【0004】[0004]

【発明が解決しようとする課題】一方、近年、し尿と生
活排水を単一の槽で処理する、いわゆる合併処理浄化槽
が一般家庭に普及しつつあるが、合併処理浄化槽は、そ
のコンパクトさゆえに、上記の問題点を有している。汚
水の排出量の時間的変動に対応するためには、一時的に
汚水を貯留する貯留槽を設け、その貯留槽から一定量の
汚水を常に上記合併処理浄化槽に移送するようにすれ
ば、活性汚泥による嫌気性処理、好気性処理を安定して
行うことができる。しかしながら、合併処理浄化槽に上
記貯留槽を付設すると、装置自体が大型となり、また、
用地の確保という面でも問題が生じる。したがって、一
般家庭用としては、小型で設置面積も少なく、また、汚
水の排出量の時間的変動に十分適応して、汚水を処理す
ることができる浄化装置が求められている。本発明は上
記課題を解決して、一般家庭等から排出される汚水の時
間的な変動に対処して、常に、安定して汚水を浄化する
ことが可能な汚水浄化方法及び、そのためのコンパクト
な汚水浄化槽を提供することをその課題とする。
On the other hand, in recent years, so-called combined treatment septic tanks, which treat human waste and domestic wastewater in a single tank, are becoming popular in ordinary households. It has the above problems. In order to respond to temporal fluctuations in the amount of sewage discharge, if a storage tank for temporarily storing sewage is provided, and a certain amount of sewage is constantly transferred from the storage tank to the merger treatment / purification tank, Anaerobic and aerobic treatment with sludge can be performed stably. However, if the above-mentioned storage tank is attached to the merged treatment septic tank, the device itself becomes large,
Problems also arise in terms of securing land. Therefore, there is a need for a general household use of a purification device that is small in size, has a small installation area, and is capable of treating sewage in a manner that is sufficiently adapted to temporal fluctuations in sewage discharge. Solution to Problem The present invention solves the above problems, copes with temporal fluctuations of sewage discharged from general households, etc., and can always and stably purify sewage, and a compact sewage purification method therefor. It is an object to provide a sewage septic tank.

【0005】[0005]

【課題を解決するための手段】すなわち、本発明によれ
ば、嫌気性処理槽の上部に高水位位置と低水位位置を設
けてその間を汚水の流量調整部とし、当該嫌気性処理槽
の下流に濾過材を具備した好気性処理槽と、沈殿槽と、
消毒槽をこの順に配列し、上記濾過材を逆洗するための
逆洗管及び、上記濾過材を逆洗することによって剥離し
た汚泥を返送するための汚泥返送用エアリフトポンプと
を、備えた汚水浄化槽において、上記、流量調整部にお
ける汚水の液面が低水位位置付近にあるとき、汚泥の返
送を間欠的に行うことを特徴とする汚水浄化方法が提供
される。
That is, according to the present invention, a high water level position and a low water level position are provided at the upper part of the anaerobic treatment tank, between which a wastewater flow rate adjusting part is provided, and the downstream of the anaerobic treatment tank is provided. An aerobic treatment tank equipped with a filtering material, a sedimentation tank,
A sewage system comprising a disinfecting tank arranged in this order, a backwash pipe for backwashing the filter medium, and an air lift pump for returning sludge separated by backwashing the filter medium for returning sludge. In the septic tank, there is provided a sewage purification method characterized by intermittently returning sludge when the liquid level of the sewage in the flow control section is near the low water level position.

【0006】上記汚水処理槽においては、主として、好
気性処理槽内において好気性微生物により汚水の浄化を
行う。好気性微生物は通常、濾過材の表面に付着して使
用されており、長時間汚水の処理を行うと、濾過材の表
面に微生物膜が生成し、肥厚してくる。この肥厚が進む
と汚水の通過が困難となるため、逆洗処理により空気を
吹き込み、濾過材を激しく攪拌して微生物膜を剥離させ
る必要がある。この逆洗処理は定期的に行われるが、本
発明においては、深夜等、汚水の排出が極端に減少する
ときに行う。逆洗処理により剥離した微生物膜は、汚泥
として槽の底部に沈殿するが、この汚泥は、排水ととも
に下流に同伴されないよう、嫌気性処理槽に返送され
る。本発明においては、この汚泥返送を、間欠的に行う
ことを特徴としている。間欠的に汚泥返送を行うことに
より、好気性処理槽内における水位位置の変動を最低限
に抑え、効率的に返送運転を行うことができる。同時に
最低の水位位置変動幅で好気性処理を行うため、汚水を
高度に、安定して浄化することができる。
In the above-mentioned sewage treatment tank, sewage is purified mainly by aerobic microorganisms in the aerobic treatment tank. The aerobic microorganisms are usually used by adhering to the surface of the filter medium, and if the sewage treatment is performed for a long time, a microbial membrane is formed on the surface of the filter medium and thickens. If the thickening progresses, it becomes difficult to pass the sewage, so it is necessary to blow air by backwashing treatment and vigorously agitate the filter medium to remove the microbial membrane. This backwashing process is performed periodically, but in the present invention, it is performed when the discharge of sewage is extremely reduced, such as at midnight. The microbial membrane peeled off by the backwashing process precipitates at the bottom of the tank as sludge, and this sludge is returned to the anaerobic treatment tank so as not to be entrained downstream together with the wastewater. The present invention is characterized in that the sludge is returned intermittently. By intermittently returning sludge, fluctuations in the water level position in the aerobic treatment tank can be minimized, and the return operation can be performed efficiently. At the same time, since the aerobic treatment is performed with the minimum water level position fluctuation width, the sewage can be highly and stably purified.

【0007】さらに発明によれば、嫌気性処理槽の上部
に高水位位置と低水位位置を設けてその間を汚水の流量
調整部とし、当該嫌気性処理槽の下流に濾過材を具備し
た好気性処理槽と、沈殿槽と、消毒槽をこの順に配列
し、上記濾過材を逆洗するための逆洗管及び、上記濾過
材を逆洗することによって剥離した汚泥を返送するため
の汚泥返送用エアリフトポンプとを、備えた汚水浄化槽
において、汚泥の返送を間欠的に行う汚泥返送手段を備
えたことを特徴とする汚水浄化槽が提供される。
Further, according to the present invention, an aerobic process having a high water level and a low water level at the upper part of the anaerobic treatment tank and a flow rate adjusting part between the high water level and the low water level, and a filtering material provided downstream of the anaerobic treatment tank. A treatment tank, a sedimentation tank, and a disinfection tank are arranged in this order, a backwash tube for backwashing the filter material, and a sludge return for returning sludge separated by backwashing the filter material. A sewage treatment tank provided with an air lift pump and a sludge return means for intermittently returning sludge is provided.

【0008】[0008]

【発明の実施の形態】以下、本発明の好ましい実施の形
態について、図面を参照してより詳細に説明する。図1
は、本発明にかかる汚水浄化槽Aの断面図である。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Preferred embodiments of the present invention will be described below in detail with reference to the drawings. FIG.
1 is a sectional view of a sewage purification tank A according to the present invention.

【0009】まず、本発明の汚水浄化方法について説明
する。一般家庭から排出される、し尿、生活排水等の汚
水は、汚水入口1から嫌気性処理槽2に流入し、沈殿物
を分離するとともに、嫌気性処理が行われる。嫌気性処
理槽2の上部には、高水位位置(HWL)と低水位位置
(LWL)が設けられ、両者の間が流量調整部3とされ
ている。流入した汚水が貯まり、水位位置が上昇すると
高水位位置(HWL)を検知する検知手段(図示せず)
が作動して汚水移送ポンプ4が作動し、汚水は好気性処
理槽5に移送される。
First, the sewage purification method of the present invention will be described. Sewage such as night soil and domestic wastewater discharged from general households flows into the anaerobic treatment tank 2 from the sewage inlet 1 to separate sediment and perform anaerobic treatment. A high water level (HWL) and a low water level (LWL) are provided in the upper part of the anaerobic treatment tank 2, and a flow rate adjusting unit 3 is provided between the two. Detecting means (not shown) for detecting the high water level (HWL) when the inflowed sewage accumulates and the water level rises
Operates to operate the sewage transfer pump 4, and the sewage is transferred to the aerobic treatment tank 5.

【0010】一方、好気性処理槽5内には、好気性微生
物を付着させた濾過材6が具備されており、散気管7を
通して常時吹き込まれる曝気用空気によって好気性とさ
れた雰囲気で、汚水の浄化を行う。汚水の浄化を継続し
て行うと、濾過材6の表面に上記微生物の膜が生成、肥
厚して、汚水の通過を妨げるため、定期的に逆洗する。
逆洗は、空気供給装置B(送風機)から逆洗用空気ライ
ン13を経由して供給された空気を逆洗管8で散気し、
処理水中に吹き込んで濾過材6を激しく流動、攪拌させ
ることによって行う。濾過材6の表面から剥離した微生
物膜は汚泥として、好気性処理槽5の底部に沈殿する。
一方、空気供給装置Bからエアリフト用空気ライン14
を経由して供給された空気は、汚泥返送用エアリフトポ
ンプ9に吹き込まれ、沈殿した汚泥はエアリフトによ
り、嫌気性浄化槽2に返送される。
On the other hand, the aerobic treatment tank 5 is provided with a filter material 6 to which aerobic microorganisms are adhered, and the sewage in an atmosphere made aerobic by aeration air constantly blown through a diffuser 7. Perform purification. If the purification of the sewage is performed continuously, a film of the microorganisms is generated and thickened on the surface of the filter medium 6 to prevent the passage of the sewage.
In the backwash, the air supplied from the air supply device B (blower) via the backwash air line 13 is diffused in the backwash pipe 8,
This is performed by blowing into the treated water to vigorously flow and stir the filter medium 6. The microbial membrane peeled off from the surface of the filter material 6 precipitates as sludge on the bottom of the aerobic treatment tank 5.
On the other hand, the air line 14
Is supplied to the air lift pump 9 for returning sludge, and the settled sludge is returned to the anaerobic purification tank 2 by an air lift.

【0011】好気性浄化槽5において浄化処理された処
理水は、ついで、沈殿槽10に移動し、沈殿物を分離し
た後、オーバーフローして、消毒槽11で消毒される。
かくして、浄化処理をされた排水は排水出口12から放
流される。
The treated water purified in the aerobic purification tank 5 is then moved to a sedimentation tank 10 where the sediment is separated, overflows and is disinfected in a disinfection tank 11.
Thus, the purified wastewater is discharged from the wastewater outlet 12.

【0012】空気供給装置Bには、逆洗用空気調節弁V
1及びそれを制御するためのタイマT1また、エアリフト
用空気調節弁V2及びそれを制御するためのタイマT2
備えられており、それぞれ、逆洗用空気送風時間、及び
エアリフト用空気送風時間をオン・オフ制御する。
[0012] The air supply device B includes an air control valve V for backwashing.
1 and a timer T 1 for controlling the same, an air lift air control valve V 2 and a timer T 2 for controlling the air control valve V 2 are provided, respectively. Controls time on / off.

【0013】[0013]

【実施例】図1に示した汚水浄化装置A、空気供給装置
Bを用い、上記した方法にしたがって、本発明の方法を
実施した。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS The method of the present invention was carried out according to the above-mentioned method using the sewage purification apparatus A and the air supply apparatus B shown in FIG.

【0014】[0014]

【実施例1】一般家庭において、汚水の排出量が極端に
減少する深夜に本発明の方法を実施した。深夜において
は、嫌気性処理槽2の水位位置は、流量調整部3の下限
近辺にあり、この状態において、図2に示すパターンで
逆洗及び汚泥の返送を行った。すなわち、まず、図3に
示す空気供給装置Bに備えられた逆洗用空気調節弁V 1
を逆洗用空気調節弁制御タイマT1によって所定時間、
開となるように制御し、空気を所定時間、逆洗管8に送
風し、逆洗を行った。逆洗により微生物膜は剥離し、好
気性浄化槽5の底部に沈殿した。符号Xは、好気性浄化
槽5の底部に沈殿した剥離汚泥を示す。また、L1は、
逆洗を開始した時点における水位位置を示す。
[Example 1] Extreme discharge of sewage in ordinary households
The method of the present invention was performed at decreasing midnight. At midnight
Is the water level position of the anaerobic treatment tank 2
In this state, in the state shown in FIG.
Backwashing and sludge return were performed. That is, first, FIG.
Backwash air control valve V provided in the air supply device B shown in FIG. 1
The backwashing air control valve control timer T1By predetermined time,
Control to open, and send air to backwash tube 8 for a predetermined time.
Winded and backwashed. The microbial membrane is peeled off by back washing,
It settled at the bottom of the temper septic tank 5. Symbol X is aerobic purification
The separated sludge settled at the bottom of the tank 5 is shown. Also, L1Is
This shows the water level position at the time when backwashing was started.

【0015】ついで図2に示すパターンにしたがって、
逆洗を終了した後に、汚泥を嫌気性処理槽2に一定間隔
で間欠的に返送した。すなわち、空気供給装置Bに備え
られたエアリフト用空気調節弁V2をエアリフト用空気
調節弁制御タイマT2によって所定時間、一定間隔で開
とするようにオン・オフ制御し、空気を汚泥返送用エア
リフトポンプ9に送風し、汚泥の返送を間欠的に行っ
た。その状況を模式的に図4に示す。本実施例において
は、短時間のエアリフトを間欠的に行ったため、好気性
処理槽5内の水位位置低下を抑制して汚泥返送を効率的
に行うことができた。すなわち、間欠運転を行ったた
め、好気性処理槽5内の水位位置は比較的高い位置に保
たれ、したがって、エアリフトポンプの揚程が小さくな
り、短時間のエアリフトポンプの運転で、効率よく汚泥
を返送することができた。なお、図4において、L2
本発明の間欠返送を実施した場合の最低水位位置を示
し、L3は、従来法の連続運転を実施した場合の最低水
位位置を示す。間欠返送を実施したとき、好気性処理槽
5内の水位位置は上記L2と、図3におけるL1の間で変
動し、その巾を最低とすることができたため、好気性処
理槽5における汚水の浄化を、高度に、安定して行うこ
とができた。
Next, according to the pattern shown in FIG.
After the backwash was completed, the sludge was intermittently returned to the anaerobic treatment tank 2 at regular intervals. That is, a predetermined time air lift air regulating valve V 2 provided in the air supply device B by airlift air regulating valve control timer T 2, and the on-off control to open at regular intervals, for the air sludge return The air was blown to the air lift pump 9 and the sludge was returned intermittently. FIG. 4 schematically shows the situation. In this embodiment, since the air lift was performed intermittently for a short time, it was possible to suppress the lowering of the water level position in the aerobic treatment tank 5 and efficiently return the sludge. That is, since the intermittent operation is performed, the water level position in the aerobic treatment tank 5 is maintained at a relatively high position, so that the head of the air lift pump is reduced, and the sludge is efficiently returned by the operation of the air lift pump for a short time. We were able to. Incidentally, in FIG. 4, L 2 represents the lowest level position when carrying out the intermittent return of the present invention, L 3 represents the lowest level position when carrying out the continuous operation of the conventional method. When carrying out the intermittent return water level position of aerobic treatment tank 5 from the above L 2, since varied between L 1 in FIG. 3 could be the width and the lowest, in the aerobic treatment tank 5 Purification of sewage could be performed highly and stably.

【0016】[0016]

【実施例2】実施例1において、逆洗と汚泥返送のパタ
ーンを図5に変更した以外、他の条件は同じとして本発
明の方法を実施した。図5からよくわかるように、逆洗
の間欠運転と汚泥返送の間欠運転を同一周期、同一位相
で行った。この場合、空気供給装置B(送風機)から逆
洗管8と、エアリフトポンプ9への送風の制御を同時に
行うので、制御機構を簡略化できた。また逆洗を間欠的
に行ったため、剥離汚泥が好気性処理槽5内に均一に分
布され、汚泥返送水の水質が均等化された。さらに逆洗
も複数回行ったため、濾過材から微生物膜の除去を十分
におこなうことができ、汚水の処理能力が大巾に向上し
た。
Example 2 The method of the present invention was carried out in the same manner as in Example 1, except that the backwashing and sludge return patterns were changed to those shown in FIG. As can be clearly understood from FIG. 5, the intermittent operation of the backwash and the intermittent operation of returning the sludge were performed in the same cycle and in the same phase. In this case, since the control of the air supply from the air supply device B (blower) to the backwash pipe 8 and the air lift pump 9 is performed simultaneously, the control mechanism can be simplified. In addition, since the backwash was performed intermittently, the separated sludge was uniformly distributed in the aerobic treatment tank 5, and the quality of the sludge return water was equalized. Furthermore, since the backwashing was also performed a plurality of times, the removal of the microbial membrane from the filter medium could be sufficiently performed, and the treatment capacity of the sewage was greatly improved.

【0017】[0017]

【実施例3】実施例1において、逆洗と汚泥返送のパタ
ーンを図6に変更した以外、他の条件は同じとして本発
明の方法を実施した。図6からよくわかるように、逆洗
の後に汚泥返送を位相をずらせて行った。ただし、汚泥
返送の間欠運転は、逆洗と同一周期で行うパターンとし
た。その結果、逆洗の終了後に汚泥返送を行うので、剥
離した汚泥を効率的に嫌気性処理槽2に返送することが
でき、逆洗と汚泥返送に関連する機器の稼働時間を短縮
することができた。
Example 3 The method of the present invention was carried out in the same manner as in Example 1, except that the backwashing and sludge return patterns were changed to those shown in FIG. As can be clearly seen from FIG. 6, after the backwashing, the sludge was returned with the phase shifted. However, the intermittent operation of returning sludge was performed in the same cycle as the backwash. As a result, since the sludge is returned after the backwashing is completed, the separated sludge can be efficiently returned to the anaerobic treatment tank 2, and the operation time of the equipment related to the backwashing and the sludge return can be reduced. did it.

【0018】[0018]

【実施例4】実施例1において、逆洗と汚泥返送のパタ
ーンを図7に変更した以外、他の条件は同じで本発明の
方法を実施した。図7からよくわかるように、まず、汚
泥返送を行い、ついで、位相をずらせて間欠的に上記逆
洗を汚泥返送と同一周期で行った。ただし、上記逆洗に
おける間欠運転の停止時間を、剥離した汚泥が沈殿する
のに十分な時間とした。その結果、沈殿している汚泥の
返送を最初に行うので、汚泥を効率的に嫌気性処理槽2
に返送することができ、逆洗と汚泥返送に関連する機器
の稼働時間を短縮することができた。
Example 4 The method of the present invention was carried out in the same manner as in Example 1, except that the backwashing and sludge return patterns were changed to those shown in FIG. As can be clearly understood from FIG. 7, first, the sludge was returned, and then the above-mentioned backwash was performed intermittently at the same cycle as the return of the sludge by shifting the phase. However, the stop time of the intermittent operation in the backwash was set to a time sufficient for the separated sludge to settle. As a result, the sludge that has settled is returned first, so that the sludge is efficiently removed from the anaerobic treatment tank 2.
The operation time of equipment related to backwashing and sludge return could be shortened.

【0019】以上いずれの実施例においても、嫌気性処
理槽2に返送された汚泥は、沈殿され、たとえば定期的
に抜き取る等、公知の手段により処理される。
In any of the embodiments described above, the sludge returned to the anaerobic treatment tank 2 is settled and treated by a known means, for example, periodically withdrawing.

【0020】[0020]

【発明の効果】本発明における汚水浄化方法は、嫌気性
処理槽の上部に高水位位置と低水位位置を設けてその間
を汚水の流量調整部とし、当該嫌気性処理槽の下流に濾
過材を具備した好気性処理槽と、沈殿槽と、消毒槽をこ
の順に配列し、上記濾過材を逆洗するための逆洗管及
び、上記濾過材を逆洗することによって剥離した汚泥を
返送するための汚泥返送用エアリフトポンプとを、備え
た汚水浄化槽において、上記、流量調整部における汚水
の液面が低水位位置付近にあるとき、汚泥の返送を間欠
的に行うことを特徴とする。
According to the sewage purification method of the present invention, a high water level and a low water level are provided at the upper part of an anaerobic treatment tank, and a wastewater flow control part is provided between them. An aerobic treatment tank provided, a sedimentation tank, and a disinfection tank are arranged in this order, and a backwash tube for backwashing the filter material, and for returning sludge separated by backwashing the filter material. In the sewage purification tank provided with the sludge returning air lift pump, the sludge is intermittently returned when the liquid level of the sewage in the flow rate adjusting section is near the low water level position.

【0021】本発明の方法においては、嫌気性浄化槽の
上部を流量調整槽とし、汚泥返送を間欠的に行うため、
好気性浄化槽における水位位置変動幅を最低に抑え、好
気性処理を行うことができる。その結果、汚水の排出量
の時間的変動に十分対応して、汚水の浄化処理を高度
に、かつ、安定して行うことができる。したがって、一
般家庭等から排出される汚水の時間的な変動に対処し
て、常に、安定して汚水を浄化することが可能な汚水浄
化方法を提供することができる。
In the method of the present invention, the upper part of the anaerobic purification tank is used as a flow control tank, and the sludge is returned intermittently.
The aerobic treatment can be performed by minimizing the fluctuation range of the water level position in the aerobic septic tank. As a result, sewage purification processing can be performed highly and stably in response to temporal fluctuations in sewage discharge. Therefore, it is possible to provide a sewage purification method capable of always stably purifying sewage by coping with temporal fluctuation of sewage discharged from general households and the like.

【0022】さらに、本発明の方法において、上記汚泥
返送を間欠的におこなうとともに、上記逆洗を間欠的に
行うことができる。このようにすれば、汚泥返送水の水
質が均等化され、さらに逆洗も複数回行うことになるた
め、濾過材から微生物膜を十分に除去することができ、
汚水の処理能力が大巾に向上する。また、汚泥返送と逆
洗の間欠運転は、特別な制御機器を必要とせず、汚泥返
送用エアリフトポンプ及び逆洗管に送入する空気をタイ
マ等の手段によりオン・オフ制御するだけで簡単に行う
ことができる。また、本発明の方法を実施するための汚
水浄化槽も、一般家庭において使用可能なコンパクトな
ものとすることができる。
Further, in the method of the present invention, the sludge can be returned intermittently and the backwash can be performed intermittently. In this way, the quality of the sludge return water is equalized, and the backwashing is also performed a plurality of times, so that the microbial membrane can be sufficiently removed from the filter medium,
Wastewater treatment capacity is greatly improved. In addition, the intermittent operation of sludge return and backwashing can be easily performed by simply turning on and off the air fed to the sludge return air lift pump and the backwash pipe by means of a timer or the like, without requiring any special control equipment. It can be carried out. Also, the sewage treatment tank for carrying out the method of the present invention can be made compact so that it can be used in ordinary households.

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

【図1】本発明にかかる汚水浄化装置の断面図である。FIG. 1 is a sectional view of a sewage purification apparatus according to the present invention.

【図2】実施例1の運転パターンを示す図である。FIG. 2 is a diagram showing an operation pattern according to the first embodiment.

【図3】実施例1における逆洗を示す模式図である。FIG. 3 is a schematic diagram showing backwashing in Example 1.

【図4】実施例1における汚泥の返送を示す模式図であ
る。
FIG. 4 is a schematic diagram showing return of sludge in the first embodiment.

【図5】実施例2の運転パターンを示す図である。FIG. 5 is a diagram illustrating an operation pattern according to a second embodiment.

【図6】実施例3の運転パターンを示す図である。FIG. 6 is a diagram showing an operation pattern according to a third embodiment.

【図7】実施例4の運転パターンを示す図である。FIG. 7 is a diagram showing an operation pattern of a fourth embodiment.

【符号の説明】[Explanation of symbols]

1 汚水入口 2 嫌気性処理槽 3 流量調整部 4 汚水移送ポンプ 5 好気性処理槽 6 濾過材 7 散気管 8 逆洗管 9 汚泥返送用エアリフトポンプ 10 沈殿槽 11 消毒槽 12 排水出口 13 逆洗用空気ライン 14 エアリフト用空気ライン A 汚水浄化槽 B 空気供給装置 L1 実施例1において逆洗を開始した時点での水位
位置 L2 実施例1において汚泥を間欠返送したときの最
低水位位置 L3 従来法の汚泥を連続返送したときの最低水位位
置 V1 逆洗用空気調節弁 V2 エアリフト用空気調節弁 T1 逆洗用空気調節弁制御タイマ T2 エアリフト用空気調節弁制御タイマ X 汚泥
Reference Signs List 1 sewage inlet 2 anaerobic treatment tank 3 flow rate adjustment unit 4 sewage transfer pump 5 aerobic treatment tank 6 filter material 7 diffuser pipe 8 backwash pipe 9 air lift pump for returning sludge 10 sedimentation tank 11 disinfection tank 12 drainage outlet 13 for backwash Air line 14 Air lift air line A Sewage treatment tank B Air supply device L 1 Water level position at the time of starting backwashing in Example 1 L 2 Minimum water level position when sludge is intermittently returned in Example 1 L 3 Conventional method minimum level position V 1 backwash air regulating valve V 2 airlift air regulating valve T 1 backwash air regulating valve control timer T 2 airlift air regulating valve control timer X sludge when the sludge was continuously returned

───────────────────────────────────────────────────── フロントページの続き (72)発明者 広田 伸也 大阪府門真市大字門真1048番地松下電工株 式会社内 (72)発明者 加納 広志 大阪府門真市大字門真1048番地松下電工株 式会社内 (72)発明者 佐藤 賢志 大阪府門真市大字門真1048番地松下電工株 式会社内 (72)発明者 中岡 敬善 大阪府門真市大字門真1048番地松下電工株 式会社内 (72)発明者 板垣 峯尾 大阪府門真市大字門真1048番地松下電工株 式会社内 Fターム(参考) 4D027 AB07 AB14 4D040 BB42 BB82 BB91  ──────────────────────────────────────────────────続 き Continued on the front page (72) Inventor: Shinya Hirota 1048 Kadoma, Kadoma, Osaka Prefecture Inside Matsushita Electric Works Co., Ltd. (72) 72) Inventor Kenshi Sato 1048 Kadoma, Kadoma, Osaka Prefecture Inside Matsushita Electric Works, Ltd. (72) Inventor Takayoshi Nakaoka 1048 Odaka, Kazuma, Kadoma, Osaka Prefecture Inside Matsushita Electric Works, Ltd. 1048 Kadoma, Kadoma, Fumonma-shi Matsushita Electric Works F-term (reference) 4D027 AB07 AB14 AB14 4D040 BB42 BB82 BB91

Claims (6)

【特許請求の範囲】[Claims] 【請求項1】 嫌気性処理槽の上部に高水位位置と低水
位位置を設けてその間を汚水の流量調整部とし、当該嫌
気性処理槽の下流に濾過材を具備した好気性処理槽と、
沈殿槽と、消毒槽をこの順に配列し、上記濾過材を逆洗
するための逆洗管及び、上記濾過材を逆洗することによ
って剥離した汚泥を返送するための汚泥返送用エアリフ
トポンプとを、備えた汚水浄化槽において、上記、流量
調整部における汚水の液面が低水位位置付近にあると
き、汚泥の返送を間欠的に行うことを特徴とする汚水浄
化方法。
An aerobic treatment tank provided with a high water position and a low water position at the upper part of an anaerobic treatment tank, between which a wastewater flow rate adjusting part is provided, and a filtering material provided downstream of the anaerobic treatment tank,
A sedimentation tank and a disinfection tank are arranged in this order, a backwash tube for backwashing the filter medium, and a sludge return air lift pump for returning sludge separated by backwashing the filter medium. Wherein the sludge is returned intermittently when the liquid level of the wastewater in the flow rate adjusting section is near the low water level position in the wastewater purification tank provided.
【請求項2】 上記逆洗を間欠的に行うとともに、この
逆洗の間欠運転を上記汚泥返送と同一周期、同一位相で
行う請求項1記載の汚水浄化方法。
2. The sewage purification method according to claim 1, wherein the backwashing is performed intermittently, and the intermittent backwashing operation is performed in the same cycle and in the same phase as the sludge return.
【請求項3】 上記逆洗を間欠的に行うとともに、逆洗
の後に汚泥返送の位相をずらせて間欠的に上記逆洗と同
一周期で行う請求項1記載の方法。
3. The method according to claim 1, wherein the backwashing is performed intermittently, and the phase of sludge return is shifted after the backwashing so as to be performed intermittently in the same cycle as the backwashing.
【請求項4】 上記逆洗を間欠的に行うとともに、逆洗
の前に汚泥返送の位相をずらせて間欠的に上記逆洗と同
一周期で行い、かつ上記逆洗と上記汚泥返送の間欠運転
の停止時間を同一の所定時間とした請求項1記載の汚水
浄化方法。
4. An intermittent operation in which the backwashing is performed intermittently, the sludge return phase is shifted before the backwashing, and intermittently in the same cycle as the backwashing, and the backwashing and the sludge return are performed intermittently. 2. The sewage purification method according to claim 1, wherein the stop time of the sewage is the same predetermined time.
【請求項5】 上記汚泥返送と上記逆洗の間欠運転を当
該汚泥返送用エアリフトポンプ及び当該逆洗管に送入す
る空気をオン・オフ制御することによって行う請求項1
乃至4のいずれか1項に記載の汚水浄化方法。
5. The sludge returning and the intermittent operation of the backwashing are performed by controlling on / off of air fed into the sludge returning air lift pump and the backwashing pipe.
The sewage purification method according to any one of claims 1 to 4.
【請求項6】 嫌気性処理槽の上部に高水位位置と低水
位位置を設けてその間を汚水の流量調整部とし、当該嫌
気性処理槽の下流に濾過材を具備した好気性処理槽と、
沈殿槽と、消毒槽をこの順に配列し、上記濾過材を逆洗
するための逆洗管及び、上記濾過材を逆洗することによ
って剥離した汚泥を返送するための汚泥返送用エアリフ
トポンプとを、備えた汚水浄化槽において、汚泥の返送
を間欠的に行う汚泥返送手段を備えたことを特徴とする
汚水浄化槽。
6. An aerobic treatment tank provided with a high water position and a low water position at the upper part of the anaerobic treatment tank and a flow rate adjusting portion between the high water position and the low water position, and provided with a filtering material downstream of the anaerobic treatment tank;
A sedimentation tank and a disinfection tank are arranged in this order, a backwash tube for backwashing the filter medium, and a sludge return air lift pump for returning sludge separated by backwashing the filter medium. A wastewater purification tank provided with sludge return means for intermittently returning sludge.
JP2000301660A 2000-10-02 2000-10-02 Sewage cleaning method and apparatus Pending JP2002102882A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2000301660A JP2002102882A (en) 2000-10-02 2000-10-02 Sewage cleaning method and apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2000301660A JP2002102882A (en) 2000-10-02 2000-10-02 Sewage cleaning method and apparatus

Publications (1)

Publication Number Publication Date
JP2002102882A true JP2002102882A (en) 2002-04-09

Family

ID=18783154

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2000301660A Pending JP2002102882A (en) 2000-10-02 2000-10-02 Sewage cleaning method and apparatus

Country Status (1)

Country Link
JP (1) JP2002102882A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1734014A1 (en) * 2005-06-14 2006-12-20 PDL Development SL Device and method for filtration of fluids
CN105084594A (en) * 2015-08-20 2015-11-25 孙源 Urban sewage treatment method
CN106587347A (en) * 2015-10-19 2017-04-26 李天源 Intelligent movable rural domestic sewage treatment method and device
CN110372165A (en) * 2019-08-18 2019-10-25 邱学尧 A marks septic tank
CN110981117A (en) * 2019-12-30 2020-04-10 巫溪县绿荫环保有限公司 Integrated domestic sewage treatment device

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1734014A1 (en) * 2005-06-14 2006-12-20 PDL Development SL Device and method for filtration of fluids
CN105084594A (en) * 2015-08-20 2015-11-25 孙源 Urban sewage treatment method
CN106587347A (en) * 2015-10-19 2017-04-26 李天源 Intelligent movable rural domestic sewage treatment method and device
CN110372165A (en) * 2019-08-18 2019-10-25 邱学尧 A marks septic tank
CN110981117A (en) * 2019-12-30 2020-04-10 巫溪县绿荫环保有限公司 Integrated domestic sewage treatment device

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