JPS59115788A - Method and device for treating sewage - Google Patents

Method and device for treating sewage

Info

Publication number
JPS59115788A
JPS59115788A JP57230315A JP23031582A JPS59115788A JP S59115788 A JPS59115788 A JP S59115788A JP 57230315 A JP57230315 A JP 57230315A JP 23031582 A JP23031582 A JP 23031582A JP S59115788 A JPS59115788 A JP S59115788A
Authority
JP
Japan
Prior art keywords
tank
sewage
aeration
sludge
aerobic microorganisms
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
JP57230315A
Other languages
Japanese (ja)
Inventor
Shusuke Kobayashi
秀典 小林
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP57230315A priority Critical patent/JPS59115788A/en
Publication of JPS59115788A publication Critical patent/JPS59115788A/en
Pending legal-status Critical Current

Links

Classifications

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

Landscapes

  • Biological Treatment Of Waste Water (AREA)

Abstract

PURPOSE:To clean up sewage at a high rate of cleaning by using a device combining a catalytic aeration method utilizing aerobic bacteria and an activated sludge method in treating the sewage thereby making use of the advantages that both methods possess. CONSTITUTION:Sewage is once put into a storage and control tank 1 and is lifted by pumps 5, 6 into a measuring inlet 2. The sewage is supplied at the controlled flow rate from the inlet 2 into the 1st tank of plural consecutive aeration tanks 3; at the same time, the air is delivered by blowers 7, 8 and is blown through a diffusion port 9 into the sewage. The sewage flows through filter media 10 on which aerobic microorganisms stick and the pollutant in the sewage is oxidized and decomposed by the microorganism. Such operation is repeated in each tank 3 and thereafter the sewage is put into a settling tank 4 where sludge is settled and the activated sludge contg. a large amt. of the aerobic bacteria is returned by a return device 12 into the the tank 3 where the sludge is reused. The supernatant water is released after it is passed through a post treatment stage according to need.

Description

【発明の詳細な説明】 この発明は好気性微生物の働きを利用した接触曝気法と
活性汚泥法を有機的に結合した汚水処理方法及びその装
置に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a sewage treatment method that organically combines a contact aeration method using the action of aerobic microorganisms and an activated sludge method, and an apparatus therefor.

好気性微生物の働きを利用した汚水処理は汚水中に含ま
れる有機物を栄養源とする微生物に十分な酸素を与え、
その活動を助長して汚濁物質を酸化分解するもので、従
来より接触曝気法。
Sewage treatment using the action of aerobic microorganisms provides sufficient oxygen to microorganisms that use organic matter contained in wastewater as a nutrient source,
This method promotes this activity and oxidizes and decomposes pollutants, and is conventionally known as the contact aeration method.

活性汚泥法など種々知られていた。Various methods were known, including the activated sludge method.

この接触曝気法は、曝気槽内に流入した汚水を、該槽内
に配置した濾材を透してその表面に棲息する好気性微生
物に接触させて酸化処理するもので、好気性微生物の活
動範囲が限られているため、流入汚水が少ない場合の処
理とか。
In this contact aeration method, wastewater that has flowed into an aeration tank is oxidized by being brought into contact with aerobic microorganisms living on the surface of the filter medium placed in the tank, and the range of activity of aerobic microorganisms is Since there is a limited amount of wastewater, it is necessary to treat when there is little inflow of wastewater.

BOD濃度が低い場合の処理には適するが、この逆即ち
、流入汚水が多く、BOD濃度が高い場合あるいは油脂
類を多く含む汚水処理などには不適であった。これに対
して活−性汚泥法は。
Although it is suitable for treatment when the BOD concentration is low, it is unsuitable for the opposite case, that is, when there is a large amount of inflowing sewage and the BOD concentration is high, or for the treatment of sewage containing a large amount of oils and fats. On the other hand, the activated sludge method

曝気槽内の汚水中に好気性微生物を多量に含む汚泥を浮
遊させておき、ブロワ−によって空気とともに混合し好
気性微生物に接触させて酸化処理するもので、好気性微
生物の活動が活発であることから流入汚水が多い場合で
も、高濃度のBOD負荷にも強い反面、過剰曝気などに
よって栄養−生物の平衡がくずれ浄化率を低下させる所
謂、解体現象や糸状菌の異品発生により沈澱力が低下す
る所謂、膨化現象を起こし易いという問題があった。
Sludge containing a large amount of aerobic microorganisms is suspended in wastewater in an aeration tank, mixed with air by a blower, and brought into contact with aerobic microorganisms for oxidation treatment, which increases the activity of aerobic microorganisms. Therefore, even when there is a large amount of inflowing wastewater, it is resistant to high concentrations of BOD loads, but on the other hand, excessive aeration disrupts the nutrient-organism balance and reduces the purification rate. There has been a problem in that the so-called swelling phenomenon, which is a decrease in the amount of water, tends to occur.

この発明は上記の点に鑑み、接触曝気法及び活性汚泥法
がそれぞれ持つ長所を生かし、短所とするところを除去
して好気性微生物の解体。
In view of the above points, this invention takes advantage of the advantages of the contact aeration method and the activated sludge method, eliminates their disadvantages, and disassembles aerobic microorganisms.

膨化をなくシ、浄化率及び沈澱力の向上を図り、良水質
の放流水が安定的に得られるようにした汚水処理方法及
びその装置を提供することを目的としている。
The object of the present invention is to provide a sewage treatment method and apparatus that eliminate swelling, improve purification efficiency and settling power, and stably obtain effluent of good quality.

次ぎに、この発明を添付図面に示す一実施例にもとづい
て説明する。
Next, the present invention will be described based on an embodiment shown in the accompanying drawings.

1は汚水源(図示せず)から排出した汚水を貯留する調
整槽、2は計量枡、3は曝気槽、4は沈澱槽である。
1 is an adjustment tank for storing wastewater discharged from a wastewater source (not shown), 2 is a measuring cell, 3 is an aeration tank, and 4 is a settling tank.

前記調整槽l内には複数基(図においては二基の場合を
示しているが、これ以上であってもよい)のポンプ51
,6が配置され、前記計量枡2に汚水を汲上げるように
なっている。該計量枡2は曝気槽3に流送する汚水量を
調節するもので、装置によってはかかる調節をポンプ自
体にて行わせ、計量枡2を設置しない場合もある。前記
曝気槽3は図においては三種連続した場合を示している
が、これに限らない。これら曝気槽3の各種には好気性
微生物を付着させるための濾材10がそれぞれ配置され
ている。また、各種には複数基(図においては二基の場
合を示しているが、それ以上であってもよい)のブロワ
−7,8から大気中の空気が槽内設置した吐出口9を通
して供給できるようになっている。この空気の供給は前
記濾材表面に棲息する好気性微生物および後記する返送
された活性汚泥に十分な酸素を与え、好気性微生物の繁
殖を促すとともにその活動を活発化させるため必要なも
のである。前記曝気槽3において十分に曝気された汚水
はその槽上部より沈澱槽4に流送され、該沈澱槽4内に
おいて沈降分離し、上澄水は必要に応じて行われる後処
理工程を経て放流される一方、沈降した汚泥は好気性微
生物を多量に含むことから返送装置19を介して前記濾
材を配置した曝気槽3内に戻されるようになっている。
There are a plurality of pumps 51 (the figure shows two pumps, but there may be more) in the adjustment tank l.
, 6 are arranged to pump up wastewater into the measuring cell 2. The measuring cell 2 is used to adjust the amount of sewage flowing into the aeration tank 3, and depending on the device, such adjustment may be performed by the pump itself, and the measuring cell 2 may not be installed. Although the figure shows a case where three types of aeration tanks 3 are installed in succession, the aeration tank 3 is not limited to this. Each type of aeration tank 3 is provided with a filter medium 10 for adhering aerobic microorganisms. In addition, for each type, atmospheric air is supplied from multiple blowers 7 and 8 (two blowers are shown in the figure, but more may be used) through a discharge port 9 installed in the tank. It is now possible to do so. This air supply is necessary in order to provide sufficient oxygen to the aerobic microorganisms living on the surface of the filter medium and the returned activated sludge, which will be described later, to promote the reproduction of the aerobic microorganisms and to activate their activities. The sewage that has been sufficiently aerated in the aeration tank 3 is sent from the upper part of the tank to a settling tank 4, where it is sedimented and separated, and the supernatant water is discharged after undergoing a post-treatment process if necessary. On the other hand, since the settled sludge contains a large amount of aerobic microorganisms, it is returned to the aeration tank 3 in which the filter medium is arranged via a return device 19.

前記調整槽l内に配置した二基のポンプ5゜6は図示し
ないフロートスイッチによって、流入汚水が基準水位に
達したときに稼動するようになっている。また、前記ブ
ロワ−7,8は前記ポンプ5.6に連動して駆動するよ
うになっている。そして前記ブロワ−7,8は図示しな
い電子タイマーの作用でポンプ停止後も一定時間延長し
て稼動を継続できるようになっている。
The two pumps 5 and 6 arranged in the regulating tank 1 are operated by a float switch (not shown) when the inflowing wastewater reaches a reference water level. Further, the blowers 7 and 8 are driven in conjunction with the pump 5.6. The blowers 7 and 8 can continue to operate for a certain period of time even after the pumps have been stopped by the action of an electronic timer (not shown).

このブロワ−の延長時間は電子タイマーのセントの仕方
によるが、汚水の流入量、BODの負荷量により長時間
にしたり短時間にすることができる。このセント時間は
多くの場合、30分〜1時間程度で満足できる。
The extended time of this blower depends on how the electronic timer is set, but it can be made longer or shorter depending on the amount of inflow of sewage and the amount of BOD load. In most cases, this cent time of about 30 minutes to 1 hour is satisfactory.

さらに前記ブロワ−7,8のいずれか一方または双方は
前記フロートスイッチとは別個に図示しないタイマーに
よって一定時間ごとに稼動するようになっている。これ
は流入汚水の負荷量によって一日数回一定時間ごとブロ
ワ−を稼動させたり、一つのブロワ−を24時間連続稼
動することが必要な場合があるからである。
Further, one or both of the blowers 7 and 8 are operated at regular intervals by a timer (not shown) separately from the float switch. This is because, depending on the load of inflowing sewage, it may be necessary to operate the blower at regular intervals several times a day, or to operate one blower continuously for 24 hours.

なお3図中11は第四曝気槽で、該第四曝気槽11は前
記沈澱層4の上澄水を更に曝気する予備的なもので、前
記曝気槽3と同様に好気性微生物を付着させるための濾
材lOと前記ブロワ−7,8に連通ずる空気吐出口9を
備えているが、ハソフル13を設置し、上澄水が動揺し
ないようにしている。この第四曝気槽11は必ずしも設
けなければならないものではない。
In addition, 11 in Fig. 3 is a fourth aeration tank, and the fourth aeration tank 11 is a preliminary tank for further aerating the supernatant water of the sediment layer 4, and like the aeration tank 3, it is used to attach aerobic microorganisms. The filter medium 10 is provided with an air outlet 9 that communicates with the blowers 7 and 8, and a hasoflu 13 is installed to prevent the supernatant water from stirring. This fourth aeration tank 11 does not necessarily have to be provided.

この発明は以上の如<、調整槽よりポンプを介して曝気
槽内に流入した汚水を、該槽内に配置して濾材を透して
その表面に棲息する好気性微生物に接触曝気して後、沈
澱槽において沈降分離した汚泥を前記濾材を配置した曝
気槽に返送することを特徴としているから、i気槽内は
濾材表面に棲息する好気性微生物のほか、汚泥とともに
返送される好気性微生物によって充満することとなる。
As described above, the present invention is as follows: wastewater flowing into an aeration tank from a regulating tank via a pump is placed in the tank, passes through a filter medium, contacts aerobic microorganisms living on the surface of the tank, and is then aerated. Since the sludge that has been settled and separated in the settling tank is returned to the aeration tank in which the filter medium is placed, the i-air tank contains aerobic microorganisms living on the surface of the filter medium as well as aerobic microorganisms that are returned together with the sludge. It will be filled with.

この槽内に浮遊する好気性微生物は必要な酸素の供給に
より、活発に活動して汚濁物質を吸着酸化するが、もと
もと、生物であり、その酸化能力に限界があって2通常
では解体および膨化現象を起こして酸化能力をな(した
り、沈澱力を失わせることがあるが、かかる酸化能力に
限界を生15た微生物が槽内配置の濾材表面に付着する
と濾材表面の酸化能力のある微生物と置換する結果、槽
内は審に高い酸化能力を持つ微生物によって保たれるこ
ととなる。
The aerobic microorganisms floating in this tank become active and adsorb and oxidize pollutants by supplying the necessary oxygen, but they are originally living organisms and have a limited oxidizing ability, so they usually disintegrate and expand. If microorganisms that limit the oxidizing ability adhere to the surface of the filter media placed in the tank, the microorganisms with the oxidizing ability on the surface of the filter media may As a result, the inside of the tank will be maintained by microorganisms with high oxidizing ability.

従って、この発明方法及び装置によれば汚水量が多量で
あったり、BOD負荷が高い場合であっても、また汚水
量が時間帯、季節などによって集中したり、はとんどな
くなったりするような場合であっても、そのあらゆる現
場の条件に対応し、良水質の放流水が安定して得られる
というすぐれた効果を奏するものである。
Therefore, according to the method and device of the present invention, even if the amount of sewage is large or the BOD load is high, the amount of sewage can be concentrated or disappear depending on the time of day, season, etc. Even in such cases, it is compatible with all site conditions and has the excellent effect of stably obtaining effluent water of good quality.

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

図はこの発明の実施例を示す略示的断面図で1−・−調
整槽、      3−曝気槽5.6−ポンプ、   
  7.8−プロワ−9−・返送装置、      1
0−濾材代理人  弁理士   羽  村  行  弘
手続ネ甫正書(方式) 昭和58年 4月28日 特許庁長官  若 杉 和 夫  殿 1、事件の表示 昭和57年特許願第230315号 2−発明の名称 汚水処理方法及びその装置 3−補正をする者 事件との関係  特許出願人 住所  山梨県甲府市東光寺町4−383氏名  小 
 林  秀  典 4−代理人 ■151 住所  東京都渋谷区代々木2丁目5番1号6−補正の
対象 願書及び明細書 7−補正の内容
The figure is a schematic cross-sectional view showing an embodiment of the present invention, and includes: 1--adjustment tank, 3-aeration tank, 5.6-pump,
7.8-Prower-9-・Return device, 1
0-Filter agent agent Patent attorney Yuki Hamura Ko procedure Neho (method) April 28, 1980 Commissioner of the Japan Patent Office Kazuo Wakasugi 1, Indication of case 1988 Patent application No. 230315 2- Invention Name of sewage treatment method and its device 3 - Relationship with the case of the person making the amendment Patent applicant address 4-383 Tokoji-cho, Kofu City, Yamanashi Prefecture Name Small
Hidenori Hayashi 4 - Agent ■ 151 Address 6-2-5-1 Yoyogi, Shibuya-ku, Tokyo - Application and specification subject to amendment 7 - Contents of amendment

Claims (1)

【特許請求の範囲】 (11開整槽よりポンプを介して曝気槽内に流入した汚
水を、該槽内に配置した濾材を透してその表面に棲息す
る好気性微生物に接触曝気して後、沈澱槽において、沈
降分離した汚泥を前記濾材を配置した曝気槽に返送する
ことを特徴とする汚水処理方法。 (2)好気性微生物を付着させるための濾材を配置した
曝気槽と、該曝気槽内にて曝気後の汚水を沈降分離する
沈澱槽と、該沈澱槽内に沈降した好気性微生物を含む汚
泥を前記濾材を配置した曝気槽に返送する返送装置とを
備えたことを特徴とする汚水処理装置。
[Claims] (After the sewage that flows into the aeration tank from the 11-open adjustment tank via a pump passes through a filter medium placed in the tank and comes into contact with aerobic microorganisms living on the surface of the tank, it is aerated. A sewage treatment method characterized by returning the sludge that has been settled and separated in the settling tank to an aeration tank in which the filter medium is arranged. (2) An aeration tank in which a filter medium is arranged for adhering aerobic microorganisms, and the aeration tank. It is characterized by comprising a settling tank that sediments and separates sewage after aeration in the tank, and a return device that returns the sludge containing aerobic microorganisms settled in the settling tank to the aeration tank in which the filter medium is arranged. sewage treatment equipment.
JP57230315A 1982-12-24 1982-12-24 Method and device for treating sewage Pending JPS59115788A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57230315A JPS59115788A (en) 1982-12-24 1982-12-24 Method and device for treating sewage

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57230315A JPS59115788A (en) 1982-12-24 1982-12-24 Method and device for treating sewage

Publications (1)

Publication Number Publication Date
JPS59115788A true JPS59115788A (en) 1984-07-04

Family

ID=16905901

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57230315A Pending JPS59115788A (en) 1982-12-24 1982-12-24 Method and device for treating sewage

Country Status (1)

Country Link
JP (1) JPS59115788A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20020060114A (en) * 2002-05-16 2002-07-16 주식회사 씨에치케이엔비론 Apparatus and method for processing sewage and wastewater having a pack tower
KR100415588B1 (en) * 2000-08-01 2004-01-31 (주)맑은물 Sewage/wastewater treatment plant
KR100437642B1 (en) * 2001-11-12 2004-06-30 주식회사 한성와이엠 Sewage Purifier
KR100443407B1 (en) * 2002-04-02 2004-08-11 곽종운 Water purification device using a microorganism media
KR100456346B1 (en) * 2002-04-18 2004-11-09 (주)한일이에스티 The sewage and waste water treatment plant by microorganism contact oxidation

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100415588B1 (en) * 2000-08-01 2004-01-31 (주)맑은물 Sewage/wastewater treatment plant
KR100437642B1 (en) * 2001-11-12 2004-06-30 주식회사 한성와이엠 Sewage Purifier
KR100443407B1 (en) * 2002-04-02 2004-08-11 곽종운 Water purification device using a microorganism media
KR100456346B1 (en) * 2002-04-18 2004-11-09 (주)한일이에스티 The sewage and waste water treatment plant by microorganism contact oxidation
KR20020060114A (en) * 2002-05-16 2002-07-16 주식회사 씨에치케이엔비론 Apparatus and method for processing sewage and wastewater having a pack tower

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