JPS61274798A - Apparatus for treating organic waste water - Google Patents
Apparatus for treating organic waste waterInfo
- Publication number
- JPS61274798A JPS61274798A JP11661785A JP11661785A JPS61274798A JP S61274798 A JPS61274798 A JP S61274798A JP 11661785 A JP11661785 A JP 11661785A JP 11661785 A JP11661785 A JP 11661785A JP S61274798 A JPS61274798 A JP S61274798A
- Authority
- JP
- Japan
- Prior art keywords
- tank
- air
- partition plate
- waste water
- treatment
- 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
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/30—Aerobic and anaerobic processes
- C02F3/301—Aerobic and anaerobic treatment in the same reactor
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Biodiversity & Conservation Biology (AREA)
- Microbiology (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業の技術分野〕
本発明は、有機物水処理浄化槽で、上部と下部に槽内を
区切って、下部に有機廃水を注入して嫌−1気性処理を
し、次に上部で好気□性処理をし、該上部と下部の境界
に仕切板を配置し、該仕切板に多数の噴流孔を設け、下
部で処理したものを上部に空気とともに噴流し、一槽で
嫌気性処理と好気性処理をする浄化槽装置に関する。[Detailed description of the invention] [Technical field of industry] The present invention is an organic water treatment septic tank, in which the inside of the tank is divided into an upper part and a lower part, and organic wastewater is injected into the lower part for anaerobic treatment. Aerobic treatment is carried out in the upper part, a partition plate is placed at the boundary between the upper part and the lower part, a large number of jet holes are provided in the partition plate, and the material treated in the lower part is jetted into the upper part with air, and one tank is heated. This article relates to septic tank equipment that performs anaerobic and aerobic treatment.
通常の有機物水処理槽装置では、一槽内で嫌気性処理を
したものを他の楢で好気性処理をするのが、在来の通常
の方法である。そして供給汚水にスクリーンを通して空
気を吹きこんで好気性処理をする。嫌気性処理で酸素の
ない状態で有機物分子は酵素(以下、バクテリアおよび
同様の微生物を酵素と一括して呼ぶ。)による加水分解
反応を作用されて分解し次に生物細胞中の溶解性成分の
酸化還元を受けるが、最終生成iは好気性処理による生
成物よシも酸化の程度が少ない。嫌気極処理の酵素と好
気性処理の酵素とは生物の種類が異なるが共存できない
ことはない。しかし好気性処理による分解は酸素かに′
くなるまで行われ、酸素がなくなると嫌気硅酵素゛が急
速に増加し嫌気性処理が行われる。嫌気住処−によると
、アンモニア−メタンガス、硫化水素、および水素が発
生し、悪臭を放ち、可燃性ガスを生成する。この欠点は
あるが、利点として、深い場所で行うことができ、エア
レーションをする必要がないし、また表匍積を大にする
必要がない。これは好気性処理では得られない。好気性
処理の利点は、残留BODが多い嫌気性処理に対しBO
Dが少なく浄化液の着色が著しく少ないし、有機物濃度
が少ない場合には嫌気性処理コストより低い。これらの
欠点と長所とを勘案して、一槽内の深部で先ず嫌気性処
理をし、次に仕切板の多数の小孔を通して空気とともに
上部に噴流しエアレーションによる好気性処理を行うよ
うにし、生成スラジを処理水とともに上部から取り出す
ことができる処理装置を提供するという課題が存在する
。この際、嫌気部に被処理水を供給し、好気部へ生成ス
ラジを含む被処理物を送水するかなどを定めることも課
題である。In conventional organic water treatment tank systems, the conventional method is to perform anaerobic treatment in one tank and aerobic treatment in another oak. Air is then blown into the supplied wastewater through a screen for aerobic treatment. In anaerobic treatment, in the absence of oxygen, organic molecules undergo a hydrolysis reaction by enzymes (hereinafter, bacteria and similar microorganisms are collectively referred to as enzymes), and are then decomposed into soluble components in biological cells. Although undergoing redox, the final product i is less oxidized than the product from aerobic treatment. Although the enzymes for anaerobic electrode treatment and the enzymes for aerobic treatment are different types of organisms, they cannot coexist. However, decomposition due to aerobic treatment is caused by oxygen
When the oxygen is exhausted, anaerobic silica enzyme rapidly increases and anaerobic treatment is performed. Anaerobic habitats produce ammonia-methane gas, hydrogen sulfide, and hydrogen, producing malodorous and flammable gases. Despite this drawback, the advantage is that it can be carried out in deep places, there is no need for aeration, and there is no need to increase the surface volume. This cannot be achieved with aerobic treatment. The advantage of aerobic treatment is that BO
Since D is low, the coloring of the purified liquid is significantly less, and when the concentration of organic matter is low, the cost is lower than that of anaerobic treatment. Taking these disadvantages and advantages into consideration, we first perform anaerobic treatment in the deep part of one tank, and then perform aerobic treatment by aeration by jetting it to the upper part with air through a large number of small holes in the partition plate. The problem exists of providing a treatment device in which the produced sludge can be removed from the top together with the treated water. At this time, it is also a problem to decide whether to supply water to be treated to the anaerobic section and to send water to be treated including generated sludge to the aerobic section.
本発明は、在来の課題解決をするために上部と下部とを
中間に多数の所要形状寸法の多孔中間仕切板を設けて、
嫌気性処理の下部と好気性処理の上部とを一槽内に形成
し、槽の最下部から被処理M機物廃水を注入し、該廃水
通路を多孔噴出板で仕切って供給する。槽下部で嫌気性
処理をした水を前記多孔中間仕切板の多孔から空気ポン
プで供給する空気を噴出し、この上方への噴出と前記被
処理有機物廃水の注入圧による流水で、槽上部に送くら
れ、好気性処理をし、上部から処理液と生成スラジを分
離装置に送水しスラジを除去する。In order to solve the conventional problem, the present invention provides a large number of porous intermediate partition plates with required shapes and dimensions between the upper and lower parts,
A lower part for anaerobic treatment and an upper part for aerobic treatment are formed in one tank, and M machinery wastewater to be treated is injected from the lowest part of the tank, and the wastewater passage is partitioned with a porous spout plate and supplied. The water that has been anaerobically treated in the lower part of the tank is sent to the upper part of the tank by blowing out air supplied by an air pump through the holes in the porous intermediate partition plate, and using this upward jet and flowing water due to the injection pressure of the organic wastewater to be treated. The treated liquid and generated sludge are sent from the upper part to a separator to remove the sludge.
注入廃水供給多孔噴出板と中間多孔板とは重要な構成要
素である。The injection wastewater supply perforated spout plate and the intermediate perforated plate are important components.
本発明を一実施例について図面に基づいて説明する。第
1図は本発明の一実施例の一部拡大正面図である。第2
図は好気性処理部での通気率と総括酸素移動容量係数と
の関係図である。A線が本発明のものでB線が在来法に
よるものである。An embodiment of the present invention will be explained based on the drawings. FIG. 1 is a partially enlarged front view of an embodiment of the present invention. Second
The figure is a diagram showing the relationship between the ventilation rate and the overall oxygen transfer capacity coefficient in the aerobic treatment section. Line A is the one made by the present invention, and line B is made by the conventional method.
第1図の処理槽SSは殊に下部槽S1が地表面GL下に
埋設されるように設けられ、有機廃棄物を含む廃水Wは
供給管5で下部槽S1に図示のように供給板2から注入
される。槽壁7は通常は円筒形で上部に図示のごとく傾
斜板10i付したものであるが、角形など用途に応じ任
意に選定して使用することができる。下部槽Slは地下
に深く埋込まれ、外気及び光を遮断した状態で嫌気性処
理をし、該下部槽S1の上部に上部槽S2を設けここに
は地表から光及空気を多量に供給して好気性処理をする
。上部槽S2の下端であって下部槽8.1の上端との間
に仕切板1を設け、空気ポンプ3から連結配管4で仕切
板1に槽S2で好気性処理をするだめの加圧吹込空気を
供給し、仕切板1に備えた多数の微小孔から分散させて
上方に向けて空気泡を噴出させる。嫌気性処理された廃
水8は噴出空気とともに、下底からの廃水Wの供給量に
応じて、槽S1から槽S2に移動され好気性処理される
。下部槽S1と上部槽S2は仕切板1で、仕切られるこ
とによって嫌気性処理と好気性処理とが仕切板で完全に
境界され画処理容積をそれだけ増大する。第3図に一部
拡大断面図で示す仕切板1はアルミナ製板で厚さ20i
uxで、直径が例えば150ミクロン程度の多数の孔1
1を有し前記空気泡13を噴出する。嫌気性処理をした
廃水通路孔12の直径より小であり、滓が流過し得る最
小許容形状寸法であるのがのぞましい。また直径IU程
度の廃水8の流通孔12t−備える。The treatment tank SS in FIG. 1 is particularly provided with a lower tank S1 buried below the ground surface GL, and wastewater W containing organic waste is supplied to the lower tank S1 via a supply pipe 5 to a supply plate 2 as shown in the figure. injected from. The tank wall 7 is usually cylindrical and has an inclined plate 10i attached to the upper part as shown in the figure, but it can be arbitrarily selected depending on the purpose, such as a rectangular shape. The lower tank S1 is buried deep underground and performs anaerobic treatment while blocking outside air and light, and an upper tank S2 is provided above the lower tank S1 to which a large amount of light and air is supplied from the ground surface. and aerobic treatment. A partition plate 1 is provided between the lower end of the upper tank S2 and the upper end of the lower tank 8.1, and pressurized air is blown into the partition plate 1 from an air pump 3 via a connecting pipe 4 to perform aerobic treatment in the tank S2. Air is supplied, dispersed through a large number of micropores provided in the partition plate 1, and air bubbles are ejected upward. The anaerobically treated wastewater 8 is moved together with the ejected air from the tank S1 to the tank S2 according to the amount of wastewater W supplied from the bottom, where it is aerobically treated. The lower tank S1 and the upper tank S2 are separated by a partition plate 1, whereby anaerobic processing and aerobic processing are completely separated by the partition plate, thereby increasing the image processing volume accordingly. The partition plate 1 shown in a partially enlarged sectional view in Fig. 3 is made of alumina and has a thickness of 20 mm.
ux, with a large number of holes 1 with a diameter of, for example, about 150 microns.
1 and ejects the air bubbles 13. Preferably, the diameter is smaller than the diameter of the anaerobically treated wastewater passage hole 12, and is the minimum allowable shape and size through which the slag can flow. It is also provided with a flow hole 12t for the waste water 8 having a diameter of about IU.
上部槽S2と下部槽S1から成る処理槽SSの容積は例
えば100−で、有効散気面積比は約10%で、槽SS
の深さは例えば3.6mで、上部槽S2と下部槽S1は
同一直径の内筒形である。The volume of the treatment tank SS consisting of the upper tank S2 and the lower tank S1 is, for example, 100-, the effective aeration area ratio is about 10%, and the tank SS
The depth of the tank is, for example, 3.6 m, and the upper tank S2 and the lower tank S1 have an inner cylindrical shape with the same diameter.
同一のDO値と廃棄物滓との被処理廃水に適用した場合
、第2図に示す結果が得られた。すなわち、通気率と総
括酸素移動容量係数の関係は、処理前のDOが2.0で
あったものを、空気を中間板1から吹きこんでDOを1
.3に低下させた場合、第2図に示すA線になり在来法
Bによるものと比較しエアレーション用ポンプ等の電力
効率が約35%の向上した。When applied to treated wastewater with the same DO value and waste slag, the results shown in FIG. 2 were obtained. In other words, the relationship between the ventilation rate and the overall oxygen transfer capacity coefficient is that if the DO before treatment was 2.0, then the DO was 1 by blowing air through the intermediate plate 1.
.. 3, line A is shown in FIG. 2, and compared to conventional method B, the power efficiency of aeration pumps, etc. is improved by about 35%.
本発明は、地下に遮光状態に埋設した下部槽S1で嫌気
性処理をした廃水8を、一槽SS中を薄い仕切板1で薄
層の境界をし、この仕切板1の微小孔から空気を吹きこ
み、上部槽S2で好気性処理をするようにしたから、嫌
気性処理と好気性処理とが効率良く行なえ、処理効率が
顕著に向上した。嫌気性処理をすることで発生する悪臭
と可燃性ガス発生を好気性処理を同一槽SS内で中間仕
切板を設けて、槽下部と槽上部とでつづけて処理し、中
間仕切機に備えた微小孔から空気を吹きこみ処理をする
ことで処理槽の容積利用効率を高め処理効率を高め、単
位槽容積当シの効率向上し、処理水の透明度を高めるこ
とができる。こうして処理コストヲ顕著に低下させるこ
とができ実用効果が犬である。4+p!I−+、b俸切
−抜初−−粘埃ハ昨1訃。In the present invention, wastewater 8 that has been anaerobically treated in a lower tank S1 buried underground in a light-shielded state is separated into thin layers by a thin partition plate 1 in one tank SS, and air is aired through the micropores of this partition plate 1. Since this was injected and aerobic treatment was performed in the upper tank S2, anaerobic treatment and aerobic treatment could be performed efficiently, and the treatment efficiency was significantly improved. The bad odor and combustible gas generated by anaerobic treatment are treated aerobically by installing an intermediate partition plate in the same tank SS, and treating the lower part of the tank and the upper part of the tank continuously, and is equipped with an intermediate partition machine. By blowing air through micropores during treatment, it is possible to increase the volume utilization efficiency of the treatment tank, increase treatment efficiency, improve efficiency per unit tank volume, and improve the transparency of treated water. In this way, the processing cost can be significantly reduced and the practical effects are significant. 4+p! I-+, b salary cut-out first--sticky dust died last year.
第1図は本発明の一実施例の説明用一部拡大正面断面図
。第2図は通気率と総括酸素移動容量係数との関係図。
茅3困)まl>切板の一訃4八大J什面1目。
SS・・・処理槽
1・・・中間仕切板兼空気吹込部
2・・・被処理廃水注入口
3・・・空気ポンプ 4・・・空気配管5・・・廃
水供給管 6・・・処理水排出樋7・・・下部槽周
壁 8・・・嫌気性処理水9・・・好気性処理水
A・・・本発明線 B・・・在来法線T・・・処
理水 W・・・被処理廃水S1・・・下部槽
S2・・・土部槽11・・・空気吹出孔 12
・・・廃水通路孔13・・・吹込空気泡
特許出願人 株式会社井上ジャパックス研究所代
理 人 弁理士 中 西 −
111図
一〇
〜2
匍 2!!1
遺1キ
’ II 3 @’
一Nmり2, H
手続補正書
昭和60年6月28日FIG. 1 is a partially enlarged front sectional view for explaining one embodiment of the present invention. Figure 2 is a diagram showing the relationship between air permeability and overall oxygen transfer capacity coefficient.茅 3 troubles) M > Kiriita no Ichiban 48 Daij 1st item. SS...Treatment tank 1...Intermediate partition plate/air blowing part 2...Wastewater inlet to be treated 3...Air pump 4...Air piping 5...Wastewater supply pipe 6...Processing Water discharge gutter 7...lower tank surrounding wall 8...anaerobic treated water 9...aerobic treated water A...invention line B...conventional normal line T...treated water W...・Wastewater to be treated S1...lower tank
S2... Dobe tank 11... Air outlet 12
...Wastewater passage hole 13... Blown air bubbles patent applicant Inoue Japax Laboratory Co., Ltd.
Attorney Patent Attorney Nakanishi - 111 Figure 10-2 匍 2! ! 1 Remains 1 Ki' II 3 @' 1 Nmri 2, H Procedural Amendment June 28, 1985
Claims (1)
で、地下に遮光埋設した前記下部槽に被処理廃水の注入
部を設けて嫌気性水処理をし、該下部槽で嫌気性水処理
をした廃水を前記中間仕切板に備えた通路孔から空気と
ともに地上の上部槽に噴出し好気性水処理をするように
設けたものである有機物水処理装置。 2 通路孔を流通する廃水中に分散気泡を噴出混合する
空気吹出孔を設けた中間仕切板を備えた特許請求の範囲
の第1項に記載の有機物水処理装置。[Scope of Claims] 1. A wastewater treatment tank consisting of a lower tank, an upper tank, and an intermediate partition plate, in which an inlet for wastewater to be treated is provided in the lower tank, which is buried underground to block light, for anaerobic water treatment. An organic water treatment device that is installed so that wastewater that has been subjected to anaerobic water treatment in a lower tank is spouted together with air from a passage hole provided in the intermediate partition plate to an above-ground upper tank for aerobic water treatment. 2. The organic water treatment device according to claim 1, comprising an intermediate partition plate provided with air blowing holes for blowing and mixing dispersed air bubbles into the wastewater flowing through the passage holes.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP11661785A JPS61274798A (en) | 1985-05-31 | 1985-05-31 | Apparatus for treating organic waste water |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP11661785A JPS61274798A (en) | 1985-05-31 | 1985-05-31 | Apparatus for treating organic waste water |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS61274798A true JPS61274798A (en) | 1986-12-04 |
Family
ID=14691613
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP11661785A Pending JPS61274798A (en) | 1985-05-31 | 1985-05-31 | Apparatus for treating organic waste water |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS61274798A (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE9305922U1 (en) * | 1993-04-20 | 1993-08-19 | Bischof, Franz, Dipl.-Ing., 90489 Nürnberg | Multi-stage reactor module with integrated stirring and gassing system |
NL1004455C2 (en) * | 1996-11-06 | 1998-05-08 | Pacques Bv | Device for the biological treatment of waste water. |
EP0995793A1 (en) * | 1998-09-25 | 2000-04-26 | GSF-Forschungszentrum für Umwelt und Gesundheit GmbH | Apparatus for the culture and the concentration of non-adherent cells and for the coculture of two distinct sort of cells |
WO2009096797A1 (en) * | 2008-01-28 | 2009-08-06 | Ntnu Technology Transfer As | Method and device for the treatment of waste water |
JP2009291719A (en) * | 2008-06-05 | 2009-12-17 | Sumiju Kankyo Engineering Kk | Biological wastewater treatment apparatus |
-
1985
- 1985-05-31 JP JP11661785A patent/JPS61274798A/en active Pending
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE9305922U1 (en) * | 1993-04-20 | 1993-08-19 | Bischof, Franz, Dipl.-Ing., 90489 Nürnberg | Multi-stage reactor module with integrated stirring and gassing system |
NL1004455C2 (en) * | 1996-11-06 | 1998-05-08 | Pacques Bv | Device for the biological treatment of waste water. |
WO1998019971A1 (en) * | 1996-11-06 | 1998-05-14 | Paques B.V. | Apparatus for the biological purification of waste water |
US6063273A (en) * | 1996-11-06 | 2000-05-16 | Paques B.V. | Apparatus for the biological purification of waste water |
EP0995793A1 (en) * | 1998-09-25 | 2000-04-26 | GSF-Forschungszentrum für Umwelt und Gesundheit GmbH | Apparatus for the culture and the concentration of non-adherent cells and for the coculture of two distinct sort of cells |
WO2009096797A1 (en) * | 2008-01-28 | 2009-08-06 | Ntnu Technology Transfer As | Method and device for the treatment of waste water |
US9133044B2 (en) | 2008-01-28 | 2015-09-15 | Biowater Technology AS | Method and device for the treatment of waste water |
JP2009291719A (en) * | 2008-06-05 | 2009-12-17 | Sumiju Kankyo Engineering Kk | Biological wastewater treatment apparatus |
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