JPH1119668A - Small-sized combined purifying tank - Google Patents

Small-sized combined purifying tank

Info

Publication number
JPH1119668A
JPH1119668A JP9179645A JP17964597A JPH1119668A JP H1119668 A JPH1119668 A JP H1119668A JP 9179645 A JP9179645 A JP 9179645A JP 17964597 A JP17964597 A JP 17964597A JP H1119668 A JPH1119668 A JP H1119668A
Authority
JP
Japan
Prior art keywords
tank
water
aeration
small
chamber
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
JP9179645A
Other languages
Japanese (ja)
Inventor
Yasuyoshi Sugiyama
靖芳 杉山
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.)
Inax Corp
Original Assignee
Inax Corp
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 Inax Corp filed Critical Inax Corp
Priority to JP9179645A priority Critical patent/JPH1119668A/en
Publication of JPH1119668A publication Critical patent/JPH1119668A/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

  • Separation Using Semi-Permeable Membranes (AREA)
  • Treatment Of Biological Wastes In General (AREA)
  • Activated Sludge Processes (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a small-sized combined purifying tank capable of preventing sludge from being excessively drawn and also capable of preventing the sludge from flowing out in the case where a large quantity of water flows rapidly. SOLUTION: The inside of an aeration tank 51 is divided into a first chamber 51a and a second chamber 51b by a partition plate 52 low in height and a screen 53 and a membrane module 57 is arranged in the second chamber 51. A manhole 75 is provided on the upward of the first chamber 51a. A presettling tank 66 is provided so as to be separated by the partition plate 65 and the water flowing over an upper limit water level H.H.W.L. is made so as to flow out to the pre-settling tank 66. The water in the pre-settling tank 66 overflows a tank wall 70, flows into a pre-disinfecting tank 71, after being sterilized by coming to contact with a sterilizing agent, the water overflows the tank wall 70 and flows into a disinfecting tank 62 to be discharged.

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】本発明は生活排水などを浄化
処理するための小型合併浄化槽に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a small-sized combined septic tank for purifying domestic wastewater and the like.

【0002】[0002]

【従来の技術】生活排水などを処理する装置は、特開平
7−299490号公報及び特開平7−299491号
公報などに示されるように、被処理水をスクリーン濾過
した後、曝気処理し、次いで濾過膜で濾過した後、殺菌
し、放流するものが広く用いられている。
2. Description of the Related Art As disclosed in JP-A-7-299490 and JP-A-7-299491, an apparatus for treating domestic wastewater and the like is provided with an aeration treatment after subjecting water to be treated to screen filtration, followed by aeration treatment. After being filtered through a filtration membrane, those that are sterilized and discharged are widely used.

【0003】第3,4図は上記の特開平7−29949
1号公報に記載の従来例を示すものであり、第3図の汚
水処理装置1は、被処理水供給管2より導入される被処
理水を好気条件下で活性汚泥により生物学的に処理する
曝気室3と、この曝気室3と隔壁4を介して分離された
濾液室5とで構成されており、濾液室5には排出管6が
設けられている。
FIGS. 3 and 4 show the above-mentioned Japanese Patent Application Laid-Open No. 7-29949.
FIG. 3 shows a conventional example, in which a sewage treatment apparatus 1 shown in FIG. 3 biologically converts treated water introduced from a treated water supply pipe 2 by activated sludge under aerobic conditions. It comprises an aeration chamber 3 to be treated, and a filtrate chamber 5 separated from the aeration chamber 3 via a partition 4, and the filtrate chamber 5 is provided with a discharge pipe 6.

【0004】曝気室3内には、被処理水供給管2の開口
部を覆って、スクリーン7などを備えた濾過部8が設け
られるとともに、上部に室内の活性汚泥混合液の液位を
測定する液位計9が、タイマー機能をも備えた制御装置
9aに接続して設けられている。また、隔壁4の近傍
に、室内の自然水頭を駆動圧として活性汚泥混合液を固
液分離する浸漬型の膜分離装置10が設けられている。
In the aeration chamber 3, a filtration unit 8 provided with a screen 7 and the like is provided so as to cover the opening of the water supply pipe 2 to be treated, and the liquid level of the activated sludge mixed liquid in the room is measured at the upper part. The liquid level gauge 9 is connected to a control device 9a having a timer function. In addition, an immersion type membrane separation device 10 is provided in the vicinity of the partition 4 for solid-liquid separation of the activated sludge mixture by using the natural head in the room as a driving pressure.

【0005】膜分離装置10は、上下が開口する箱状の
ケーシング11の内部に膜カートリッジ12を適当間隔
で並列に配置しており、各膜カートリッジ12の膜透過
側に連通させて吸引チューブ13と吸引ヘッダー管14
とを順次設けている。そして、吸引ヘッダー管14に一
端を連通させて濾液管15が設けられていて、この濾液
管15の他端は隔壁4を貫通して濾液室5内に導かれて
いる。濾液管15の他端部には、制御装置9aに接続す
る電磁弁16が設けられている。膜カートリッジ12の
下方には、被処理水に曝気空気を供給する曝気装置17
がブロワ18に接続して設けられている。
[0005] In the membrane separation device 10, membrane cartridges 12 are arranged in parallel in a box-shaped casing 11 which is open at the top and bottom at appropriate intervals, and a suction tube 13 is connected to the membrane permeation side of each membrane cartridge 12. And suction header tube 14
Are sequentially provided. A filtrate tube 15 is provided with one end communicating with the suction header tube 14, and the other end of the filtrate tube 15 penetrates the partition wall 4 and is guided into the filtrate chamber 5. The other end of the filtrate tube 15 is provided with an electromagnetic valve 16 connected to the control device 9a. An aeration device 17 for supplying aeration air to the water to be treated is provided below the membrane cartridge 12.
Are connected to the blower 18.

【0006】濾液室5内には、排出管6の開口部を覆っ
て、滅菌器19を備えた消毒部20が設けられるととも
に、室5内の被処理水を消毒部20へ導くポンプ21が
設けられている。
In the filtrate chamber 5, a disinfecting section 20 provided with a sterilizer 19 is provided so as to cover the opening of the discharge pipe 6, and a pump 21 for guiding the water to be treated in the chamber 5 to the disinfecting section 20 is provided. Is provided.

【0007】また、装置の天部には保守管理のための開
口部22,23が形成され、それぞれに蓋22a,23
aが設けられている。
[0007] Openings 22 and 23 for maintenance are formed in the top of the apparatus, and lids 22a and 23 are provided respectively.
a is provided.

【0008】このように構成された汚水処理装置におい
て、被処理水供給管2より被処理水を導入すると、被処
理水は濾過部8を通過する間にスクリーン7などによっ
てきょう雑物が除去され、次いで曝気室3内の活性汚泥
混合液に混合される。そして、被処理水は、ブロワ18
より曝気装置17を通じて曝気空気が供給される好気的
条件下、曝気空気の気泡流により撹拌されつつ活性汚泥
の作用により生物学的に処理され、被処理水中に含まれ
ていた有機物や窒素分が除去される。
In the sewage treatment apparatus configured as described above, when water to be treated is introduced from the water supply pipe 2, foreign matter is removed from the water to be treated by the screen 7 while passing through the filtration unit 8. Then, it is mixed with the activated sludge mixture in the aeration chamber 3. The water to be treated is blower 18
Under aerobic conditions in which aerated air is supplied through the aeration device 17, biological treatment is performed by the action of activated sludge while being stirred by the bubble flow of the aerated air, and organic matter and nitrogen contained in the water to be treated are removed. Is removed.

【0009】また、曝気室3内の活性汚泥混合液は、自
然水頭を駆動圧として、膜カートリッジ12により固液
分離される。そして、活性汚泥は室内に維持され、濾過
膜を透過した濾液は吸引チューブ13と吸引ヘッダー管
14とを経て濾液管15より濾液室5へ送られる。
The activated sludge mixture in the aeration chamber 3 is solid-liquid separated by the membrane cartridge 12 using the natural head as a driving pressure. Then, the activated sludge is maintained in the room, and the filtrate that has passed through the filtration membrane is sent from the filtrate tube 15 to the filtrate chamber 5 through the suction tube 13 and the suction header tube 14.

【0010】なお、制御装置9aによって電磁弁16が
開閉制御され、曝気室3内の水位が低水位L.W.L.
と高水位H.W.L.との間に維持される。
The electromagnetic valve 16 is controlled to open and close by the control device 9a, and the water level in the aeration chamber 3 is set to a low water level L.P. W. L.
And high water level H. W. L. Is maintained between.

【0011】濾液室5に流入した被処理水は、ポンプ2
1によって消毒部20へ導かれ、滅菌器19により消毒
された後に排出管6より装置の外部へ排出される。
The treated water flowing into the filtrate chamber 5 is supplied to the pump 2
The liquid is guided to a disinfecting section 20 by 1 and sterilized by a sterilizer 19 and then discharged from the discharge pipe 6 to the outside of the apparatus.

【0012】第4図の汚水処理装置においては、被処理
水供給管31より被処理水を導入して、スクリーン32
などを設けた濾過部33を通過させる間にきょう雑物を
除去し、この被処理水を受入室34に貯留するととも
に、その適当量をエアリフトポンプ35などにより曝気
室36に導いている。
[0014] In the sewage treatment apparatus shown in FIG.
The foreign matter is removed during the passage through the filtration unit 33 provided with a filter, etc., and the water to be treated is stored in the receiving chamber 34, and an appropriate amount thereof is guided to the aeration chamber 36 by an air lift pump 35 or the like.

【0013】そして、被処理水を曝気室36内の活性汚
泥混合液と混合し、ブロワ37などの給気手段より曝気
装置38を通じて曝気空気を供給する好気的条件下に曝
気空気の気泡流を利用して撹拌しながら、活性汚泥の作
用によって被処理水中の有機物や窒素分を除去してい
る。また、活性汚泥混合液中に浸漬して設けた膜分離装
置39の濾液側にポンプ40により吸引負圧を供給し、
濾過膜の表裏に圧力差を生ぜしめることによって、濾過
膜により固液分離を行い、活性汚泥を室内に残留させる
とともに、濾過膜を通過した濾液を取り出している。
Then, the water to be treated is mixed with the activated sludge mixture in the aeration chamber 36, and aerated air is supplied under aerobic conditions through an aeration device 38 through an aeration device 38 such as a blower 37. The organic sludge and the nitrogen content in the water to be treated are removed by the action of the activated sludge while stirring with the use of water. Further, suction negative pressure is supplied by the pump 40 to the filtrate side of the membrane separation device 39 provided by immersion in the activated sludge mixture,
By generating a pressure difference between the front and back of the filtration membrane, solid-liquid separation is performed by the filtration membrane, the activated sludge remains in the room, and the filtrate that has passed through the filtration membrane is taken out.

【0014】そして、この濾液を消毒部41に導いて滅
菌器42で衛生上支障のないように消毒し、その後、濾
液室43を経て浄化処理水44として装置の外部へ流出
させている。
The filtrate is guided to a disinfecting section 41 and disinfected by a sterilizer 42 so as not to impair sanitation. Thereafter, the filtrate is discharged to the outside of the apparatus as a purified water 44 through a filtrate chamber 43.

【0015】受入室34内の上部と膜分離装置39の上
方とにそれぞれ液位計45,46を設け、これらの液位
計45,46により測定される液位に基づいて、被処理
水31の流入量とポンプ40により引き抜く濾液量との
調整を行うとともに、濾過膜を浸漬状態に維持する活性
汚泥混合液の最低液位Lを確保するようにしている。
Level gauges 45 and 46 are provided above the receiving chamber 34 and above the membrane separator 39, and the water 31 to be treated is determined based on the level measured by the level gauges 45 and 46. And the amount of filtrate drawn out by the pump 40 is adjusted, and the minimum liquid level L of the activated sludge mixed liquid for maintaining the filtration membrane in the immersion state is ensured.

【0016】[0016]

【発明が解決しようとする課題】上記従来の装置におい
て、汚泥が過剰になった場合、マンホール蓋をあけてバ
キュームカーのホースを曝気室内に差し込み汚泥を引き
抜く(吸引排出する)が、ホースを曝気室3,36の底
部にまで差し込んでおくと曝気室3,36内の汚泥がす
べて抜き出されてしまい、運転再開後に汚泥が極端に不
足し、処理水質が悪化してしまう。また、膜分離装置が
目詰りし易くなる。汚泥量を調節して引き抜くこともで
きなくはないが、手間と熟練を要す。
In the conventional apparatus described above, when the sludge becomes excessive, the manhole cover is opened, a hose of a vacuum car is inserted into an aeration chamber, and the sludge is pulled out (sucked and discharged). If it is inserted into the bottom of the chambers 3 and 36, all the sludge in the aeration chambers 3 and 36 will be extracted, and the sludge will be extremely short after the restart of operation, and the treated water quality will deteriorate. Further, the membrane separation device is easily clogged. It is not impossible to remove sludge by adjusting the amount of sludge, but it requires time and skill.

【0017】また、上記従来の装置において、急激に多
量の被処理水が流入してきた場合、曝気室3,36の水
が濾液室5,43に溢れ出し、そのまま放流されてしま
う。
Further, in the above-mentioned conventional apparatus, when a large amount of water to be treated suddenly flows in, the water in the aeration chambers 3, 36 overflows into the filtrate chambers 5, 43 and is discharged as it is.

【0018】本発明は、上記従来の問題点を解決すべく
なされたものであり、汚泥の過剰な引き抜きが防止され
る小型合併浄化槽を提供することを目的とする。また、
本発明は、急激に多量の水が流入してきた場合に汚泥の
流出を防止できるようにした小型合併浄化槽を提供する
ことを目的とする。
The present invention has been made to solve the above-mentioned conventional problems, and an object of the present invention is to provide a small-sized combined clarification tank in which excessive extraction of sludge is prevented. Also,
An object of the present invention is to provide a small-sized combined septic tank that can prevent sludge from flowing out when a large amount of water flows in abruptly.

【0019】[0019]

【課題を解決するための手段】請求項1の小型合併浄化
槽は、槽体内に被処理水を曝気処理する曝気槽が設けら
れると共に、この曝気槽内に設置された膜モジュールに
よって曝気処理水を膜濾過し、濾過水を消毒槽で殺菌し
た後排出する小型合併浄化槽において、該曝気槽内の底
面から仕切壁を立ち上げて曝気槽内の下部を複数室に区
画したことを特徴とするものである。
According to a first aspect of the present invention, there is provided a small-sized combined clarification tank, wherein an aeration tank for aerating the water to be treated is provided in the tank body, and the aeration-treated water is supplied by a membrane module installed in the aeration tank. A small combined septic tank that discharges after filtering membrane water and sterilizing the filtered water in a disinfection tank, wherein a partition wall is set up from the bottom in the aeration tank and the lower part in the aeration tank is divided into a plurality of chambers. It is.

【0020】かかる小型合併浄化槽にあっては、マンホ
ールからホースを差し込んで汚泥の引き抜きを行う場
合、膜モジュールを設けた室内の下部(仕切壁上端より
も下方領域)の汚泥は引き抜かれずに残留するようにな
る。
In such a small-sized combined septic tank, when a sludge is pulled out by inserting a hose from a manhole, the sludge in the lower part (the area below the upper end of the partition wall) in the room provided with the membrane module remains without being drawn out. Become like

【0021】請求項2の小型合併浄化槽は、槽体内に被
処理水を曝気処理する曝気槽が設けられると共に、この
曝気槽内に設置された膜モジュールによって曝気処理水
を膜濾過し、濾過水を消毒槽で殺菌した後排出する小型
合併浄化槽において、該曝気槽内の水が所定水位以上に
なると溢流して流入してくる予備沈殿槽を設けたことを
特徴とするものである。
According to a second aspect of the present invention, there is provided a small-sized combined clarification tank, wherein an aeration tank for aerating the water to be treated is provided in the tank body, and the aeration-treated water is subjected to membrane filtration by a membrane module installed in the aeration tank. In a small-sized combined septic tank that discharges after sterilizing in a disinfecting tank, a preliminary sedimentation tank that overflows and flows in when the water in the aeration tank reaches or exceeds a predetermined water level is provided.

【0022】かかる小型合併浄化槽にあっては、曝気槽
から予備沈殿槽に流出した汚泥はこの予備沈殿槽で沈降
分離処理されるようになり、小型合併浄化槽外への流出
が防止される。
In such a small-sized combined septic tank, the sludge flowing out of the aeration tank into the preliminary settling tank is subjected to sedimentation / separation treatment in the preliminary settling tank, and is prevented from flowing out of the small combined combined septic tank.

【0023】請求項3の小型合併浄化槽は、請求項2に
おいて、前記予備沈殿槽内の水が所定水位以上になると
溢流して流入してくる予備消毒槽を設け、前記消毒槽に
対し該予備消毒槽の水を流出させるようにしたことを特
徴とするものである。
According to a third aspect of the present invention, there is provided the small-sized combined septic tank according to the second aspect, further comprising a preliminary disinfecting tank that overflows and flows in when the water in the preliminary sedimentation tank reaches or exceeds a predetermined water level. It is characterized in that the water in the disinfection tank is allowed to flow out.

【0024】かかる小型合併浄化槽においては、予備沈
殿槽からの流出水が予備消毒槽で消毒を受け、十分に消
毒された後排出されるようになる。
In such a small-sized combined septic tank, the effluent from the preliminary sedimentation tank is disinfected in the preliminary disinfection tank and discharged after being sufficiently disinfected.

【0025】請求項4の小型合併浄化槽は、請求項2又
は3において、前記予備沈殿槽の水を曝気槽に返送する
ポンプを設けたことを特徴とするものである。
In a fourth aspect of the present invention, there is provided the small-sized combined clarification tank according to the second or third aspect, further comprising a pump for returning the water in the preliminary settling tank to the aeration tank.

【0026】かかる小型合併浄化槽においては、予備沈
殿槽で沈降した汚泥やその他の固形分が曝気槽に返送さ
れるため、曝気槽の汚泥濃度を高く維持することができ
ると共に、流出固形分量を著しく少なくすることができ
る。
In such a small-sized combined septic tank, the sludge and other solids settled in the preliminary sedimentation tank are returned to the aeration tank, so that the sludge concentration in the aeration tank can be maintained at a high level and the amount of solids flowing out can be significantly reduced. Can be reduced.

【0027】請求項5の小型合併浄化槽は、槽体内に被
処理水を曝気処理する曝気槽が設けられると共に、この
曝気槽内に設置された膜モジュールによって曝気処理水
を膜濾過し、濾過水を消毒槽で殺菌した後排出する小型
合併浄化槽において、該槽体の流入口近傍に該曝気槽内
の水位が所定水位以上になったときに流入するオーバー
フロー流入口を設け、該オーバーフロー流入口を前記消
毒槽に連通する導管を設けたことを特徴とするものであ
る。
According to a fifth aspect of the present invention, there is provided the small-sized combined clarification tank, wherein an aeration tank for aerating the water to be treated is provided in the tank body, and the aeration-treated water is subjected to membrane filtration by a membrane module installed in the aeration tank. In the small-sized combined septic tank that is sterilized and discharged after disinfection, an overflow inlet is provided near the inlet of the tank body when the water level in the aeration tank is equal to or higher than a predetermined water level, and the overflow inlet is provided. A conduit communicating with the disinfection tank is provided.

【0028】かかる小型合併浄化槽においては、急激に
多量の水が流入してきたときにこの水を短絡的に消毒槽
へ導かれるようになり、曝気槽からの汚泥の流出が防止
される。
In such a small-sized combined septic tank, when a large amount of water suddenly flows in, the water is short-circuited to the disinfecting tank, thereby preventing sludge from flowing out of the aeration tank.

【0029】このオーバーフロー流入口は、請求項6の
通り、スクリーンの下流側に設け、ある程度の除渣処理
後の水を消毒槽へ導くようにするのが好ましい。
This overflow inlet is preferably provided on the downstream side of the screen, as described in claim 6, so that water after a certain amount of residue removal treatment is guided to the disinfection tank.

【0030】[0030]

【発明の実施の形態】第1図は実施の形態に係る小型合
併浄化槽の断面図であり、被処理水は槽体50の流入口
51’から曝気槽51内に流入し、曝気処理される。こ
の曝気槽51内は背の低い仕切壁52とスクリーン53
とにより第1室51aと第2室51bとに区画されてお
り、各室51a,51bにそれぞれ散気管54,55が
配置され、ブロワ56から空気が供給される。なお、散
気管54はスクリーン53に沿って気泡を上昇させるよ
うに仕切板52に沿って配置されている。このスクリー
ン53は第1室51a側へ若干傾いている。
DESCRIPTION OF THE PREFERRED EMBODIMENTS FIG. 1 is a sectional view of a small-sized combined septic tank according to an embodiment. Water to be treated flows into an aeration tank 51 from an inlet 51 'of a tank body 50 and is subjected to aeration treatment. . Inside the aeration tank 51, a short partition wall 52 and a screen 53 are provided.
Thus, a first chamber 51a and a second chamber 51b are defined, and diffuser tubes 54 and 55 are arranged in the respective chambers 51a and 51b, and air is supplied from a blower 56. The air diffuser 54 is arranged along the partition plate 52 so as to raise bubbles along the screen 53. The screen 53 is slightly inclined toward the first chamber 51a.

【0031】散気管55は膜モジュール57に沿って気
泡を上昇させるように膜モジュール57の下側に配置さ
れている。
The air diffuser 55 is disposed below the membrane module 57 so as to raise bubbles along the membrane module 57.

【0032】膜モジュール57の濾過水は、パイプ6
0、ポンプ61によって消毒槽62に導入され、殺菌剤
63と接触して殺菌された後、放流口64から放流され
る。なお、レベルセンサ(図示略)によって曝気槽51
内の水位が検知され、この検知信号に基づいてポンプ6
1が作動される。これにより、曝気槽51内の水位が低
水位L.W.L.と高水位H.W.L.との間に維持さ
れる。
The filtered water of the membrane module 57 is supplied to the pipe 6
After being introduced into the disinfection tank 62 by the pump 61 and contacted with the disinfectant 63 to be sterilized, it is discharged from the discharge port 64. Note that the aeration tank 51 is controlled by a level sensor (not shown).
The water level in the pump is detected, and the pump 6
1 is activated. Thereby, the water level in the aeration tank 51 becomes low water level L. W. L. And high water level H. W. L. Is maintained between.

【0033】急激に多量の水が曝気槽51に流入し、高
水位H.W.L.を超える水位上昇が発生したときのた
めに、曝気槽51と仕切板65によって隔てられるよう
にして予備沈殿槽66が設けられており、上限水位H.
H.W.L.を超える水を該予備沈殿槽60へ流出させ
るようにしている。この予備沈殿槽66内には仕切板5
8と平行に移流壁67が上下方向に延設されており、仕
切板65を溢流してきた水が移流壁67によって予備沈
殿槽66内の下部に導かれる。予備沈殿槽66の底面部
66aは傾斜面となっており、沈殿物が予備沈殿槽66
の最深部66bへ集まるよう構成されている。
A large amount of water suddenly flows into the aeration tank 51, and the high water level H.p. W. L. When a rise in the water level exceeding the maximum water level occurs, a preliminary sedimentation tank 66 is provided so as to be separated by the aeration tank 51 and the partition plate 65.
H. W. L. Is discharged to the pre-settling tank 60. In the preliminary sedimentation tank 66, the partition plate 5
An advection wall 67 extends in the vertical direction in parallel with 8, and water overflowing the partition plate 65 is guided to a lower part in the pre-sedimentation tank 66 by the advection wall 67. The bottom surface portion 66a of the pre-sedimentation tank 66 is an inclined surface, and
At the deepest part 66b.

【0034】予備沈殿槽66内の水位が上限水位H.
H.W.L.を超えると、この予備沈殿槽66内の水が
槽壁70を溢流して予備消毒槽71に流入し、殺菌剤7
2と接触して殺菌された後、槽壁73を溢流して消毒槽
62に流入し、放流される。
The water level in the pre-settling tank 66 is equal to the upper limit water level H.
H. W. L. Is exceeded, the water in the preliminary sedimentation tank 66 overflows the tank wall 70 and flows into the preliminary disinfection tank 71, where the disinfectant 7
After being sterilized by contact with the tank 2, the water overflows the tank wall 73, flows into the disinfection tank 62, and is discharged.

【0035】前記最深部66b付近から立ち上がるよう
にしてエアリフトポンプ68が設けられており、ブロワ
56から供給された空気をノズル68aから吐出させる
ことにより、予備沈殿槽66内の水をパイプ69を介し
て曝気槽51へ返送可能としている。これは、曝気槽5
1内の水位が高水位H.W.L.よりも低下してきたと
きに予備沈殿槽66内の水を曝気槽51へ戻して処理す
るためである。
An air lift pump 68 is provided so as to rise from the vicinity of the deepest portion 66b. The air supplied from the blower 56 is discharged from a nozzle 68a, so that water in the pre-sedimentation tank 66 is passed through a pipe 69. And can be returned to the aeration tank 51. This is aeration tank 5
1 is high water level H. W. L. This is because the water in the preliminary sedimentation tank 66 is returned to the aeration tank 51 for processing when the water level falls below the threshold.

【0036】このように構成された小型合併浄化槽にお
いて、汚泥引き抜きを行うには、曝気槽第1室51aの
上方の槽体50上面に設けられたマンホール75を開
け、バキュームカーのホースを該第1室51a内に差し
込み、汚泥を引き抜く。
In the small-sized combined clarification tank constructed as described above, to remove sludge, the manhole 75 provided on the upper surface of the tank body 50 above the first chamber 51a of the aeration tank is opened, and the hose of the vacuum car is connected to the first tank 51. The sludge is pulled out by inserting it into the first chamber 51a.

【0037】この小型合併浄化槽においては、仕切板5
2によって曝気槽51内が第1,2室51a,51bに
区画されているため、汚泥引き抜きしても第2室51b
内の水位は仕切板52の上端よりも低下しない。即ち、
汚泥引き抜きを行っても曝気槽第2室51b内には仕切
板52で囲まれた部分に汚泥が残留する。従って、その
後水処理を再開した場合にも十分に排水を曝気により浄
化することができる。
In this small-sized combined septic tank, the partition plate 5
2 separates the inside of the aeration tank 51 into first and second chambers 51a and 51b.
The water level inside does not drop below the upper end of the partition plate 52. That is,
Even when the sludge is extracted, the sludge remains in the portion surrounded by the partition plate 52 in the aeration tank second chamber 51b. Therefore, even when the water treatment is restarted thereafter, the wastewater can be sufficiently purified by aeration.

【0038】また、第2室51b内に汚泥が残留すると
ころから、膜モジュールが急速に詰まることも防止され
る。なお、仕切板52により槽体50が補強されるとい
う効果も得られる。
Further, it is possible to prevent the membrane module from being rapidly clogged due to the sludge remaining in the second chamber 51b. The effect that the tank body 50 is reinforced by the partition plate 52 is also obtained.

【0039】この小型合併浄化槽においては、予備沈殿
槽66が設けられているので、曝気槽51を溢れた水が
直ちに放流されることがない。また、この予備沈殿槽6
6から水が溢れる場合、この水は予備沈殿槽66で沈降
分離処理を受けたものであり、固形物の流出が少ない。
さらに、この予備沈殿槽66からの水は予備消毒槽71
及び消毒槽62によって十分に消毒される。なお、予備
沈殿槽66内の水が予備消毒槽71を経由して流出する
ところから、汚泥の流出も減少する。
In this small-sized combined clarification tank, since the preliminary settling tank 66 is provided, the water overflowing the aeration tank 51 is not immediately discharged. In addition, this preliminary sedimentation tank 6
When the water overflows from 6, the water has been subjected to the sedimentation separation treatment in the pre-sedimentation tank 66, and the outflow of solids is small.
Further, the water from the preliminary sedimentation tank 66 is supplied to the preliminary disinfection tank 71.
And, it is sufficiently disinfected by the disinfection tank 62. In addition, since the water in the pre-sedimentation tank 66 flows out via the pre-sterilization tank 71, the outflow of sludge is also reduced.

【0040】第2図(a)は別の実施の形態に係る小型
合併浄化槽の断面図であり、被処理水は槽体80の流入
口81からスクリーン槽82に流入し、スクリーン83
を通過して溢流壁84を乗り越えて曝気槽85に流入す
る。なお、スクリーン83の下部に沿って設けられた散
気管83aに対しブロワ83bから空気を供給し、気泡
をスクリーン83に沿って上昇させることによりスクリ
ーン83の目詰りを防止するよう構成されている。
FIG. 2 (a) is a sectional view of a small-sized combined septic tank according to another embodiment, in which water to be treated flows into a screen tank 82 from an inlet 81 of a tank 80 and a screen 83.
And flows over the overflow wall 84 into the aeration tank 85. Air is supplied from a blower 83b to an air diffuser 83a provided along the lower part of the screen 83, and bubbles are raised along the screen 83 to prevent the screen 83 from being clogged.

【0041】曝気槽85内に流入した水は、散気管86
からの噴出空気によって曝気処理される。曝気処理され
た水は、膜モジュール87によって濾過処理され、濾過
水は濾過水パイプ88、ポンプ89によって消毒槽90
に導入され、殺菌剤91と接触して殺菌された後、放流
口92から放流される。
The water that has flowed into the aeration tank 85 is
Is aerated by the air ejected from the air. The aerated water is filtered by a membrane module 87, and the filtered water is filtered by a filtered water pipe 88 and a pump 89 in a disinfection tank 90.
After being brought into contact with the germicide 91 and sterilized, it is discharged from the discharge port 92.

【0042】このポンプ89は曝気槽85内の水位が所
定の低水位L.W.L.と高水位H.W.L.との間に
あるように制御装置(図示略)によって制御される。
The pump 89 has an aeration tank 85 having a predetermined low water level L.W. W. L. And high water level H. W. L. Is controlled by a control device (not shown).

【0043】なお、膜モジュール87の下側にも散気管
93が設置されており、散気管86,93に対しブロワ
94から空気が供給される。膜モジュール87に近接し
て仕切板96が槽体80の底面から立ち上げられ、曝気
槽85内が第1室85aと第2室85bとに区画されて
いる。膜モジュール87は第2室85bに配置されてい
る。
A diffuser tube 93 is also provided below the membrane module 87, and air is supplied to the diffuser tubes 86 and 93 from a blower 94. A partition plate 96 is raised from the bottom of the tank body 80 near the membrane module 87, and the inside of the aeration tank 85 is partitioned into a first chamber 85a and a second chamber 85b. The membrane module 87 is disposed in the second chamber 85b.

【0044】前記スクリーン槽82の下側には、開口9
7を介して該スクリーン槽82に連通した、し渣濃縮貯
留槽98が設けられている。
An opening 9 is provided below the screen tank 82.
A residue concentrate storage tank 98 is provided, which communicates with the screen tank 82 via.

【0045】スクリーン83は、第2図(b)に示すよ
うに例えばパンチ孔径2mmのパンチングメタル(微細
目スクリーン)83aと、スリット幅3〜30mm程度
のスリット板(細目スクリーン)83bとからなる。ス
リット板83bには、上下方向に延在するスリット83
cが設けられている。
As shown in FIG. 2 (b), the screen 83 comprises, for example, a punched metal (fine-grained screen) 83a having a punch hole diameter of 2 mm and a slit plate (fine-grained screen) 83b having a slit width of about 3 to 30 mm. A slit 83 extending in the vertical direction is provided in the slit plate 83b.
c is provided.

【0046】通常の流入水量のときは、水はすべてパン
チングメタル83aを通過し溢流壁84を溢流するが、
急激に多量の水が流入してくることによりスクリーン槽
82及び曝気槽85内の水位が溢流壁84の上端よりも
高くなり、スリット板83bにまで達すると、この水は
スリット83cを通り抜ける。
When the amount of inflow water is normal, all water passes through the punching metal 83a and overflows the overflow wall 84.
When a large amount of water suddenly flows in, the water levels in the screen tank 82 and the aeration tank 85 become higher than the upper end of the overflow wall 84, and when the water reaches the slit plate 83b, this water passes through the slit 83c.

【0047】ところで、このように急激に多量の水が流
入してきた場合、曝気槽85内の水位が前記高水位H.
W.L.よりも高くなることがある。このような場合、
曝気槽85内の汚泥が消毒槽90へ流入することを防止
するために、スクリーン83よりも下流側且つスクリー
ン83の直近のスクリーン槽82側面にオーバーフロー
流入口100を設け、消毒槽90側面にオーバーフロー
流出口102を設け、これらオーバーフロー流入口10
0とオーバーフロー流出口102とをオーバーフロー導
管101で連通している。これにより、流入してきた水
が該導管101を通って短絡的に消毒槽90へ導かれる
ようになり、曝気槽85からの汚泥の流出が防止され
る。
When a large amount of water flows in abruptly, the water level in the aeration tank 85 becomes higher than the high water level H.
W. L. May be higher. In such a case,
In order to prevent the sludge in the aeration tank 85 from flowing into the disinfection tank 90, an overflow inlet 100 is provided on the side of the screen tank 82 downstream of the screen 83 and immediately adjacent to the screen 83, and overflows on the side of the disinfection tank 90. An outlet 102 is provided and these overflow inlets 10 are provided.
0 and the overflow outlet 102 are communicated by an overflow conduit 101. As a result, the inflowing water is short-circuited to the disinfecting tank 90 through the conduit 101, and the outflow of sludge from the aeration tank 85 is prevented.

【0048】なお、オーバーフロー流入口100をスク
リーン83の下流側に設けているため、槽体80への流
入水は、粗大固形分がスクリーン83で分離された後、
消毒槽90へ導かれる。
Since the overflow inlet 100 is provided on the downstream side of the screen 83, the water flowing into the tank 80 is separated after the coarse solids are separated by the screen 83.
It is led to the disinfection tank 90.

【0049】このように構成された小型合併浄化槽にお
いても、汚泥引き抜きを行うには、曝気槽第1室85a
の上方の槽体80上面に設けられたマンホール99を開
け、バキュームカーのホースを該第1室85a内に差し
込み、汚泥を引き抜くが、仕切板96によって曝気槽8
5内が第1,2室85a,85bに区画されているた
め、第2室85b内の水位は汚泥引き抜きしても仕切板
96の上端よりも低下しない。即ち、汚泥引き抜きを行
っても曝気槽第2室85b内には仕切板96で囲まれた
部分に汚泥が残留する。従って、その後水処理を再開し
た場合にも十分に排水を曝気により浄化することができ
る。また、膜モジュール87が急速に詰まることも防止
される。なお、仕切板96によって槽体80が補強され
るという効果も奏される。さらに曝気槽第1室85aの
下部は散気管86によりスポット的に曝気し撹拌するこ
とにより、部分的に嫌気状態となるので、脱室の効果も
ある。
Even in the small-sized combined septic tank constructed as described above, in order to perform the sludge extraction, the first chamber 85a of the aeration tank is required.
The manhole 99 provided on the upper surface of the tank body 80 above is opened, a hose of a vacuum car is inserted into the first chamber 85a, and the sludge is pulled out.
Since the inside of 5 is partitioned into the first and second chambers 85a and 85b, the water level in the second chamber 85b does not drop below the upper end of the partition plate 96 even when the sludge is drawn out. That is, even if the sludge is extracted, the sludge remains in the portion surrounded by the partition plate 96 in the aeration tank second chamber 85b. Therefore, even when the water treatment is restarted thereafter, the wastewater can be sufficiently purified by aeration. Also, it is possible to prevent the membrane module 87 from being rapidly clogged. In addition, the effect that the tank body 80 is reinforced by the partition plate 96 is also exerted. Furthermore, the lower part of the aeration tank first chamber 85a is partially anaerobic by aerating and agitating it in a spot by a diffuser tube 86, so that there is also an effect of removing the chamber.

【0050】[0050]

【発明の効果】以上の通り、本発明の小型合併浄化槽に
よると、槽体内からの汚泥の過剰な引き抜きが確実に防
止され、処理水質を常に良好なものとすることができ
る。
As described above, according to the small-sized combined septic tank of the present invention, excessive extraction of sludge from the tank can be reliably prevented, and the quality of treated water can always be improved.

【0051】また、本発明によると、曝気槽からの汚泥
の流出も防止されるようになり、処理水質を常に良好な
ものとすることができる。
Further, according to the present invention, the outflow of sludge from the aeration tank can be prevented, and the quality of treated water can always be improved.

【0052】本発明では、急激に多量の水が流入してき
た場合にも消毒を十分に行うことも可能である。
In the present invention, even when a large amount of water suddenly flows in, it is possible to sufficiently perform disinfection.

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

【図1】実施の形態に係る小型合併浄化槽の断面図であ
る。
FIG. 1 is a sectional view of a small-sized combined septic tank according to an embodiment.

【図2】別の実施の形態に係る小型合併浄化槽の断面図
である。
FIG. 2 is a cross-sectional view of a small-sized combined septic tank according to another embodiment.

【図3】従来例を示す断面図である。FIG. 3 is a sectional view showing a conventional example.

【図4】別の従来例を示す断面図である。FIG. 4 is a sectional view showing another conventional example.

【符号の説明】[Explanation of symbols]

50,80 槽体 51,85 曝気槽 51a,85a 第1室 51b,85b 第2室 52,96 仕切板 57,87 膜モジュール 62,90 消毒槽 66 予備沈殿槽 71 予備消毒槽 75,99 マンホール 83 スクリーン 100 オーバーフロー流入口 101 オーバーフロー導管 102 オーバーフロー流出口 50,80 Tank body 51,85 Aeration tank 51a, 85a First chamber 51b, 85b Second chamber 52,96 Partition plate 57,87 Membrane module 62,90 Disinfection tank 66 Preliminary sedimentation tank 71 Preliminary disinfection tank 75,99 Manhole 83 Screen 100 overflow inlet 101 overflow conduit 102 overflow outlet

Claims (6)

【特許請求の範囲】[Claims] 【請求項1】 槽体内に被処理水を曝気処理する曝気槽
が設けられると共に、この曝気槽内に設置された膜モジ
ュールによって曝気処理水を膜濾過し、濾過水を消毒槽
で殺菌した後排出する小型合併浄化槽において、 該曝気槽内の底面から仕切壁を立ち上げて曝気槽内の下
部を複数室に区画したとを特徴とする小型合併浄化槽。
An aeration tank for aerating water to be treated is provided in the tank body, and the aeration-treated water is subjected to membrane filtration by a membrane module installed in the aeration tank, and the filtered water is sterilized in a disinfection tank. A small combined septic tank for discharging a small combined septic tank, wherein a partition wall is raised from a bottom surface in the aeration tank and a lower portion in the aeration tank is divided into a plurality of chambers.
【請求項2】 槽体内に被処理水を曝気処理する曝気槽
が設けられると共に、この曝気槽内に設置された膜モジ
ュールによって曝気処理水を膜濾過し、濾過水を消毒槽
で殺菌した後排出する小型合併浄化槽において、 該曝気槽内の水が所定水位以上になると溢流して流入し
てくる予備沈殿槽を設けたことを特徴とする小型合併浄
化槽。
2. An aeration tank for aerating the water to be treated is provided in the tank body, and the aeration-treated water is subjected to membrane filtration by a membrane module installed in the aeration tank, and the filtered water is sterilized in a disinfection tank. A small-sized combined septic tank, which comprises a preliminary settling tank that discharges and discharges when the water in the aeration tank reaches or exceeds a predetermined water level.
【請求項3】 請求項2において、前記予備沈殿槽内の
水が所定水位以上になると溢流して流入してくる予備消
毒槽を設け、前記消毒槽に対し該予備消毒槽の水を流出
させるようにしたことを特徴とする小型合併浄化槽。
3. The pre-disinfection tank according to claim 2, further comprising a pre-disinfection tank that overflows and flows in when the water in the pre-settling tank reaches or exceeds a predetermined water level. A small-sized combined septic tank characterized by the above.
【請求項4】 請求項2又は3において、前記予備沈殿
槽の水を曝気槽に返送するポンプを設けたことを特徴と
する小型合併浄化槽。
4. The small-sized combined purification tank according to claim 2, further comprising a pump for returning water from the pre-settling tank to the aeration tank.
【請求項5】 槽体内に被処理水を曝気処理する曝気槽
が設けられると共に、この曝気槽内に設置された膜モジ
ュールによって曝気処理水を膜濾過し、濾過水を消毒槽
で殺菌した後排出する小型合併浄化槽において、 該槽体の流入口近傍に該曝気槽内の水位が所定水位以上
になったときに流入するオーバーフロー流入口を設け、
該オーバーフロー流入口を前記消毒槽に連通する導管を
設けたことを特徴とする小型合併浄化槽。
5. An aeration tank for aerating the water to be treated is provided in the tank body, and the aeration treatment water is subjected to membrane filtration by a membrane module installed in the aeration tank, and the filtered water is sterilized in a disinfection tank. In the small-sized combined septic tank to be discharged, an overflow inlet is provided near the inlet of the tank body when the water level in the aeration tank becomes equal to or higher than a predetermined water level,
A small-sized combined septic tank, wherein a conduit communicating the overflow inlet with the disinfecting tank is provided.
【請求項6】 請求項5において、前記槽体内の流入口
の近傍に流入水が通過するスクリーンが設けられてお
り、前記オーバーフロー流入口は該スクリーンよりも下
流側に設けられていることを特徴とする小型合併浄化
槽。
6. The screen according to claim 5, wherein a screen through which inflow water passes is provided near the inflow port in the tank body, and the overflow inflow port is provided downstream of the screen. Small merger septic tank.
JP9179645A 1997-07-04 1997-07-04 Small-sized combined purifying tank Pending JPH1119668A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9179645A JPH1119668A (en) 1997-07-04 1997-07-04 Small-sized combined purifying tank

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9179645A JPH1119668A (en) 1997-07-04 1997-07-04 Small-sized combined purifying tank

Publications (1)

Publication Number Publication Date
JPH1119668A true JPH1119668A (en) 1999-01-26

Family

ID=16069400

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9179645A Pending JPH1119668A (en) 1997-07-04 1997-07-04 Small-sized combined purifying tank

Country Status (1)

Country Link
JP (1) JPH1119668A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007190488A (en) * 2006-01-19 2007-08-02 Mitsubishi Rayon Eng Co Ltd Membrane separation activated sludge treatment apparatus
JP2010137216A (en) * 2008-11-11 2010-06-24 Kobelco Eco-Solutions Co Ltd Membrane separation activated sludge treatment apparatus and membrane separation activated sludge treatment method

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007190488A (en) * 2006-01-19 2007-08-02 Mitsubishi Rayon Eng Co Ltd Membrane separation activated sludge treatment apparatus
JP2010137216A (en) * 2008-11-11 2010-06-24 Kobelco Eco-Solutions Co Ltd Membrane separation activated sludge treatment apparatus and membrane separation activated sludge treatment method

Similar Documents

Publication Publication Date Title
JPH07155758A (en) Waste water treating device
KR20010033596A (en) Vapor/liquid mixer and polluted water purification apparatus using the mixer
JP4892390B2 (en) Water treatment apparatus having a solid-liquid separator
JPH1119668A (en) Small-sized combined purifying tank
JP3124197B2 (en) Sewage treatment equipment
JP3773360B2 (en) Septic tank with membrane separation
JP3171746B2 (en) Domestic wastewater treatment equipment
JPH0523687A (en) Sewage treating device
JPH09103791A (en) Septic tank
JP3181523B2 (en) Sewage purification equipment
KR100469317B1 (en) System for Advanced Wastewater Treatment using ozone
JP3105140B2 (en) Sewage treatment equipment
AU2005200936A1 (en) The treatment of waste water
JP3186921B2 (en) Sewage treatment equipment
JP2005074345A (en) Sewage treatment method
JP3181468B2 (en) Sewage treatment equipment
JP2001252679A (en) Waste water treating device and method
JPS586555B2 (en) human waste septic tank
JP2004305926A (en) Immersion membrane separation type activated sludge treatment method
JP2003181483A (en) Method for treating septic tank and the septic tank
KR970003588Y1 (en) Waste-water purifier
JP3414609B2 (en) Operating method of sewage treatment equipment
KR890006973Y1 (en) Tank for treatment of sewage
KR100579117B1 (en) Apparatus for purificating of closed water area by dissolved air flotation
JP4338853B2 (en) Aerobic filter bed tank and sewage septic tank with a diffuser for cleaning