JP2003181483A - Method for treating septic tank and the septic tank - Google Patents
Method for treating septic tank and the septic tankInfo
- Publication number
- JP2003181483A JP2003181483A JP2001384647A JP2001384647A JP2003181483A JP 2003181483 A JP2003181483 A JP 2003181483A JP 2001384647 A JP2001384647 A JP 2001384647A JP 2001384647 A JP2001384647 A JP 2001384647A JP 2003181483 A JP2003181483 A JP 2003181483A
- Authority
- JP
- Japan
- Prior art keywords
- tank
- water
- partition plate
- aerobic treatment
- 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
Links
Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
Landscapes
- Biological Treatment Of Waste Water (AREA)
- Treatment Of Biological Wastes In General (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、汚水浄化槽装置に
おける好気処理部(生物処理槽部)の処理方法及びその
処理方法を実施する浄化槽に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for treating an aerobic treatment section (biological treatment tank section) in a sewage treatment tank apparatus and a septic tank for carrying out the method.
【0002】[0002]
【従来の技術】従来、好気処理槽と沈殿槽を仕切板で仕
切った構造の組み合わせは、以下に示す4タイプが存在
する。
好気処理槽はばっ気槽(活性汚泥)で、通常のスロッ
ト型の沈殿槽。
好気処理槽は接触ばっ気槽で、通常のスロット型の沈
殿槽。
好気処理槽は担体流動床で、通常のスロット型の沈殿
槽。
好気処理槽は生物濾過槽で、通常のスロット型の沈殿
槽。
そして、何れのタイプも、図5に示すように、好気処理
槽9と沈殿槽10を仕切る仕切板11は、その下端面が
槽本体の底面から離して設置され、仕切板11の下側で
好気処理槽9と沈殿槽10が連通されている。2. Description of the Related Art Conventionally, there are the following four types of combinations of a structure in which an aerobic treatment tank and a precipitation tank are partitioned by a partition plate. The aerobic treatment tank is an aeration tank (activated sludge), which is a normal slot type sedimentation tank. The aerobic treatment tank is a contact aeration tank and is an ordinary slot type precipitation tank. The aerobic treatment tank is a carrier fluidized bed and is an ordinary slot type sedimentation tank. The aerobic treatment tank is a biological filtration tank, which is an ordinary slot type sedimentation tank. And in any type, as shown in FIG. 5, the partition plate 11 for partitioning the aerobic treatment tank 9 and the precipitation tank 10 is installed such that the lower end surface thereof is separated from the bottom surface of the tank main body, and the partition plate 11 is underside. The aerobic treatment tank 9 and the precipitation tank 10 are communicated with each other.
【0003】その為、上記構成には次のような問題点が
ある。
微細なSSが沈殿槽へ流出し、そのまま放流される。
沈殿槽底部に汚泥が堆積し、腐敗して浮上し、スカム
が大量発生する。
浄化槽への流入汚水の量が多くなると、沈殿槽では固
液分離が十分行なわれなくなり、汚泥が槽外へ流出され
る。
上記理由から、沈殿槽は容量的には好気処理槽に対し
て30%程度が必要とされ、かなりの大容量が必要であ
った。Therefore, the above structure has the following problems. Fine SS flows into the settling tank and is discharged as it is. Sludge accumulates on the bottom of the settling tank, decomposes and floats, and a large amount of scum is generated. When the amount of wastewater flowing into the septic tank increases, solid-liquid separation is not sufficiently performed in the settling tank, and sludge flows out of the tank. For the above reason, the settling tank needs to have a capacity of about 30% with respect to the aerobic treatment tank, and a considerably large capacity.
【0004】[0004]
【発明が解決しようとする課題】本発明は、上記した従
来の技術が有する問題点に鑑みてなされたもので、その
目的とするところは、沈殿槽へのSSの流出及び沈殿槽
底部に汚泥が堆積せず、活性汚泥濃度を高く保ちながら
の運転を可能とする処理方法及び浄化槽を提供すること
にある。SUMMARY OF THE INVENTION The present invention has been made in view of the problems of the above-mentioned prior art, and its purpose is to discharge SS into the settling tank and sludge at the bottom of the settling tank. (EN) It is intended to provide a treatment method and a septic tank which can be operated while keeping the activated sludge concentration at a high level without accumulating.
【0005】[0005]
【課題を解決するための手段】上記目的を達成する為に
本発明が講じた技術的手段は、好気処理槽と沈殿槽を仕
切板で仕切った浄化槽の処理方法であって、好気処理槽
に浮遊担体を充填し、通常のばっ気状態で汚水と担体を
共に旋回させ、その際、好気処理槽と沈殿槽を完全に仕
切る仕切板に取り付けた通水用膜に沿って上昇させて、
前記通水用膜に付着した生物膜を剥ぎ落とし、通水用膜
の閉塞を防止することを特徴とする(請求項1)。この
方法により、スカムの発生はなく、汚泥の流出も無くな
り、固液分離を行なう必要が無くなるため、沈殿槽(処
理水槽)の容積をコンパクト化することが可能となる。The technical means taken by the present invention to achieve the above-mentioned object is a method for treating a septic tank in which an aerobic treatment tank and a sedimentation tank are separated by a partition plate. Fill the tank with floating carrier and swirl the sewage and carrier together in a normal aeration state, while raising it along the water passage membrane attached to the partition plate that completely separates the aerobic treatment tank and the sedimentation tank. hand,
The biofilm attached to the water-permeable membrane is peeled off to prevent the water-permeable membrane from being blocked (claim 1). By this method, scum is not generated, sludge does not flow out, and solid-liquid separation is not necessary, so that the volume of the sedimentation tank (treated water tank) can be made compact.
【0006】上記処理方法を実施する浄化槽は、浄化槽
における好気処理槽と沈殿槽を仕切板で完全に仕切り、
その好気処理槽内に浮遊担体を充填すると共に、仕切板
の下部付近に散気管を配置し、更に前記仕切板に、好気
処理槽から沈殿槽へ処理汚水が通過し得る通水用膜を設
け、処理汚水が前記通水用膜を通過する時、汚水中の汚
泥が捕捉され、水分と超微細SSのみが該通水用膜を通
過するようにしたことを特徴とする(請求項2)。即
ち、好気処理槽と沈殿槽を仕切る仕切板は槽本体の底面
に密着させて両槽を完全に仕切り、少なくとも両槽が仕
切板の下側で連通しないようにする。そして、該仕切板
の高さ方向中程より上側の位置に、通水用膜を設ける。
上記構成により、好気処理槽に充填した浮遊担体は、散
気管から放出された気泡が仕切板に沿いながら上昇する
上昇流にのって通水用膜にぶつかり、通水用膜の表面に
付着した生物膜を効率よく剥ぎ取り、長期に亘って安定
した処理機能を維持できる。The septic tank for carrying out the above treatment method is a partition plate that completely separates the aerobic treatment tank and the sedimentation tank in the septic tank.
A floating membrane is filled in the aerobic treatment tank, an air diffuser is arranged near the lower part of the partition plate, and a water passage membrane through which treated wastewater can pass from the aerobic treatment tank to the sedimentation tank on the partition plate. When the treated sewage passes through the water-permeable membrane, sludge in the sewage is captured, and only water and ultrafine SS pass through the water-permeable membrane. 2). That is, the partition plate for partitioning the aerobic treatment tank and the precipitation tank is brought into close contact with the bottom surface of the tank body to completely partition both tanks so that at least both tanks do not communicate with each other below the partition plate. Then, a water-permeable membrane is provided at a position above the middle of the partition plate in the height direction.
With the above configuration, the floating carrier filled in the aerobic treatment tank hits the water-permeable membrane on the surface of the water-permeable membrane by the upward flow of bubbles emitted from the air diffuser along the partition plate. The adhered biofilm can be stripped off efficiently and a stable processing function can be maintained for a long period of time.
【0007】又、上記仕切板に設ける通水用膜は、穴径
が0.02〜0.07mmで、好気処理槽に充填した浮
遊担体がぶつかっても破損しない素材とする(請求項
3)。通水用膜の穴径を上記の範囲とすることで、通常
の汚泥等(生物膜のフロック等)の通過を阻止できる。
また、膜の材質は、ポリエステル等の不織布又はステン
レス製針金やナイロンの平織等が挙げられる。更に、上
記通水用膜は、仕切板に対して着脱自在としてもよい
(請求項4)。上記通水用膜は長期間使用している間に
は油分等の付着により、散気管から放出される気泡の上
昇流や浮遊担体との接触による微細なSSの掻き取りが
不十分になり、通水用膜が閉塞する場合も考えられる
が、前記構成により通水用膜部分を取り外して洗浄でき
ると共に、新品との交換も可能で、目詰まり解消、メン
テナンスを容易に行なうことができる。Further, the water-permeable membrane provided on the partition plate has a hole diameter of 0.02 to 0.07 mm and is made of a material which is not damaged even if the floating carrier filled in the aerobic treatment tank hits (claim 3). ). By setting the hole diameter of the water-permeable membrane within the above range, it is possible to prevent the passage of ordinary sludge or the like (flock of biological membrane, etc.).
Examples of the material of the film include non-woven fabric such as polyester, stainless wire or plain weave of nylon. Further, the water-permeable membrane may be detachable from the partition plate (claim 4). The above water-permeable membrane is adhered with oil or the like during long-term use, resulting in insufficient scraping of fine SS due to contact with the upward flow of air bubbles discharged from the air diffusing tube or floating carrier, Although the water-permeable membrane may be blocked, the water-permeable membrane portion can be removed and cleaned by the above-described configuration, and the water-permeable membrane can be replaced with a new one, so that clogging can be eliminated and maintenance can be easily performed.
【0008】また、上記仕切板は好気処理槽側に傾いて
取り付け、且つその取付角度を15度〜45度とすると
よい(請求項5)。これにより、散気管から放出された
気泡は通水用膜を伝いながら上昇することになり、その
結果、通水用膜にバイブレーションが与えられる。それ
により、膜表面に付着した微生物膜は剥離され、該通水
用膜が閉塞するのを防止する。Further, it is preferable that the partition plate is attached so as to be inclined toward the aerobic treatment tank side, and the attachment angle thereof is 15 to 45 degrees (claim 5). As a result, the bubbles released from the air diffusing pipe ascend while traveling along the water-permeable membrane, and as a result, vibration is imparted to the water-permeable membrane. As a result, the microbial membrane attached to the membrane surface is peeled off and the water-permeable membrane is prevented from being blocked.
【0009】[0009]
【発明の実施の形態】以下、本発明の実施の形態を図面
に基いて説明する。図1は本発明に係る浄化槽の一例を
示し、その浄化槽Aは、汚水等の流入口a側に前処理槽
A1が区画形成され、その前処理槽A1と流出口bとの
間に好気処理槽A2が配置され、その好気処理槽A2内
には流出口bとの間を二室に完全に仕切る仕切板1が設
置されて処理水槽A3が区画形成され、更に好気処理槽
A2内には浮遊担体4が充填されている。BEST MODE FOR CARRYING OUT THE INVENTION Embodiments of the present invention will be described below with reference to the drawings. FIG. 1 shows an example of a septic tank according to the present invention. In the septic tank A, a pretreatment tank A1 is sectioned and formed on the side of an inlet a of sewage or the like, and an aerobic gas is provided between the pretreatment tank A1 and the outlet b. A treatment tank A2 is disposed, and a partition plate 1 that completely separates the outflow port b into two chambers is installed in the aerobic treatment tank A2 to form a treated water tank A3. The floating carrier 4 is filled inside.
【0010】前処理槽A1は、沈殿分離層、嫌気濾床槽
等、何れでもよい。何れにしても、この前処理槽A1で
油分、固形物を除去された汚水が、好気処理槽A2に流
入するように構成されている。The pretreatment tank A1 may be any of a precipitation separation layer, an anaerobic filter bed tank and the like. In any case, the wastewater from which the oil content and the solid matter have been removed in the pretreatment tank A1 is configured to flow into the aerobic treatment tank A2.
【0011】好気処理槽A2内に設置する仕切板1は、
その下端面を槽の底面に密着させて配置して好気処理槽
A2と処理水槽A3を完全に仕切り、仕切板の下側で両
槽が連通しないようにしてある。そして、この仕切板1
の高さ方向の中程位置から上端の間で、且つ該仕切板1
の幅方向の中央部には開口5が開設され、その開口5に
通水用膜2が着脱可能に設けられている。又、上記仕切
板1は、その上端側が好気処理槽A2側に傾けて取り付
けられている。その仕切板1の傾きの角度としては、1
5度〜45度程度が好ましい。そして、この仕切板1に
沿って好気処理槽A2側に散気管3が配設されている。
これにより、散気管3から放出された気泡は仕切板1に
沿って上昇し、通水用膜2にバイブレーションを与え、
その結果、通水用膜2の表面に付着した微生物膜を剥離
させる働きをする。The partition plate 1 installed in the aerobic treatment tank A2 is
The lower end surface is placed in close contact with the bottom surface of the tank to completely partition the aerobic treatment tank A2 and the treated water tank A3 so that both tanks do not communicate with each other under the partition plate. And this partition board 1
Between the middle position and the upper end in the height direction of the partition plate 1
An opening 5 is opened in the center portion in the width direction of, and the water-permeable membrane 2 is detachably provided in the opening 5. Further, the partition plate 1 is attached such that its upper end side is inclined to the aerobic treatment tank A2 side. The angle of inclination of the partition plate 1 is 1
About 5 to 45 degrees is preferable. An air diffuser 3 is arranged along the partition plate 1 on the aerobic treatment tank A2 side.
Thereby, the bubbles released from the air diffuser 3 rise along the partition plate 1 and impart vibration to the water-permeable membrane 2,
As a result, it functions to peel off the microbial membrane attached to the surface of the water-permeable membrane 2.
【0012】上記通水用膜2は、穴径が0.02mm〜
0.07mm程度で、通常の汚泥等(生物膜のフロック
等)は通過できない膜とし、且つその強度は浮遊担体が
接触した場合でも、破損することがない強度のものとす
る。その通水用膜2の材質としては、ポリエステル等の
不織布、またはステンレス製針金、ナイロン等の平織等
が挙げられ、その膜2が枠体6に張設されている。尚、
通水用膜2を張設した枠体6は、前記仕切板1の開口5
の縁に沿って取り付けた差し枠7にスライド自在に装着
されている。The water-permeable membrane 2 has a hole diameter of 0.02 mm to
The membrane has a thickness of about 0.07 mm and cannot pass ordinary sludge and the like (such as flocs of biofilm), and its strength is such that it will not be damaged even when the floating carrier comes into contact with it. Examples of the material for the water-permeable membrane 2 include non-woven fabric such as polyester, stainless steel wire, plain weave such as nylon, and the membrane 2 is stretched around the frame 6. still,
The frame body 6 having the water-permeable membrane 2 stretched is the opening 5 of the partition plate 1.
It is slidably mounted on the frame 7 mounted along the edge of the.
【0013】前記好気処理槽A2に充填する浮遊担体4
は、比重が1近くで、大きさは5mm〜20mm程度
の、水流と共に旋回し得る粒状のもので、比表面積が大
きいものならよい。また、充填する量は、好気処理槽A
2の容量に対して30〜50%程度とする。Floating carrier 4 filled in the aerobic treatment tank A2
Is a granular material having a specific gravity of about 1 and a size of about 5 mm to 20 mm, which can swirl with a water flow, and may have a large specific surface area. In addition, the filling amount is the aerobic treatment tank A
It is about 30 to 50% with respect to the capacity of 2.
【0014】次に、その処理動作について説明する。先
ず最初に前処理槽A1で油分、固形物が除去された汚水
が好気処理槽A2に流入する。この好気処理槽A2で
は、高濃度の活性汚泥と浮遊担体中の微生物により、汚
水中の有機物が効率的に分解除去される。汚水中の有機
物で増殖した微生物は、MLSS濃度が10,000m
g/l程度となる。更に、長時間後には、MLSS濃度
はそれ以上となる場合もあるが、その場合には好気処理
槽A2内の汚泥の引抜を行なう。Next, the processing operation will be described. First, sewage from which oil and solids have been removed in the pretreatment tank A1 flows into the aerobic treatment tank A2. In this aerobic treatment tank A2, organic matter in wastewater is efficiently decomposed and removed by the high concentration of activated sludge and the microorganisms in the floating carrier. Microorganisms grown in organic matter in wastewater have MLSS concentrations of 10,000 m
It is about g / l. Further, after a long time, the MLSS concentration may become higher than that, but in that case, the sludge in the aerobic treatment tank A2 is extracted.
【0015】一方、好気処理槽A2に流入した汚水は、
仕切板1の上部に取り付けられている通水用膜2の表面
に接触した時、汚水中の汚泥(生物フロック)が捕捉さ
れ、水分と超微細SSのみが該通水用膜2を通過する。
そして、通水用膜2の下方には散気管3が設置され、空
気泡が上昇流となって発生放出されているため、この上
昇流に伴って前記通水用膜2にバイブレーションがかか
り、通水用膜2に捕捉された汚泥は前記バイブレーショ
ンにより強制的に剥離される。このようにして、好気処
理槽A2内は漸次MLSS濃度が高くなってゆくことに
なる。On the other hand, the sewage flowing into the aerobic treatment tank A2 is
When the surface of the water passage membrane 2 attached to the upper part of the partition plate 1 is contacted, sludge (biological flocs) in the wastewater is captured, and only water and ultrafine SS pass through the water passage membrane 2. .
An air diffuser 3 is installed below the water-permeable membrane 2, and air bubbles are generated and released as an upward flow, so that the water-permeable membrane 2 is vibrated along with the upward flow, The sludge captured by the water-permeable membrane 2 is forcibly separated by the vibration. In this way, the MLSS concentration in the aerobic treatment tank A2 gradually increases.
【0016】又、好気処理槽A2内に流入する汚水中に
油分が多い場合や、何らかの他の原因で、前記通水用膜
2が目詰まりを起こした場合は、ばっ気を停止して好気
処理槽A2内を静置し、固液分離が起こり汚泥が好気処
理槽A2の底部に堆積したのを確認した上で、通水用膜
2の全体が見えるまで上澄水を引き抜き、その後通水用
膜2を引き抜き、水道水で十分に洗浄を行った後、仕切
板1に取り付ける。尚、万一、修復が不可能と思われる
場合には、枠体6の通水用膜2を新しい膜と張り替え、
交換を行なう。Further, when the wastewater flowing into the aerobic treatment tank A2 contains a large amount of oil or when the water passage membrane 2 is clogged due to some other cause, the aeration is stopped. After leaving the aerobic treatment tank A2 stationary and confirming that solid-liquid separation has occurred and sludge has accumulated on the bottom of the aerobic treatment tank A2, the supernatant water is drawn out until the entire water-permeable membrane 2 is visible, After that, the water-permeable membrane 2 is pulled out, washed sufficiently with tap water, and then attached to the partition plate 1. Incidentally, if it seems impossible to repair, replace the water-permeable membrane 2 of the frame 6 with a new membrane,
Exchange.
【0017】以上のようにして通水用膜2を通過した処
理水は、処理水槽A3に一旦貯溜され、消毒装置8で滅
菌された後、放流される。又、本装置で窒素除去も行な
う場合には、処理水槽A3内にエアリフトポンプ(図示
省略)を設置し、流入水量の3〜4倍量の処理水を、前
処理槽A1へ常時循環させる。それにより、処理水中の
硝化された硝酸性窒素を、前処理槽A1内の脱窒菌によ
り脱窒を行なう。The treated water that has passed through the water-permeable membrane 2 as described above is temporarily stored in the treated water tank A3, sterilized by the disinfection device 8, and then discharged. When nitrogen removal is also performed by this apparatus, an air lift pump (not shown) is installed in the treated water tank A3 to constantly circulate the treated water in an amount of 3 to 4 times the inflow water amount to the pretreatment tank A1. Thereby, the nitrified nitrate nitrogen in the treated water is denitrified by the denitrifying bacteria in the pretreatment tank A1.
【0018】[0018]
【発明の効果】本発明の浄化槽の処理方法は請求項1記
載の構成により、好気処理槽内の活性汚泥濃度を高く保
ちながらの運転を可能とし、スカムの発生はなく、汚泥
の流出を防止できる。又、請求項2記載の構成により、
前記した処理方法を効果的に実行でき、前記した従来の
問題点を解消することができる。更に、請求項3記載の
構成により、通常の汚泥等(生物膜のフロック等)の通
過を阻止できる。また、請求項4記載の構成により、仮
に通水用膜が閉塞した場合でも、仕切板から膜を取り付
けた部材を取り外すことで、簡単に洗浄、交換すること
ができる。更に、請求項5記載の構成により、散気管か
ら放出される気泡は通水用膜を伝いながら上昇すること
により、膜にバイブレーションが与えられ、通水用膜に
付着した微生物膜を効率よく剥離することができ、長期
に亘って安定した通水用膜の機能を維持することができ
る。According to the method for treating a septic tank of the present invention, according to the constitution of claim 1, the operation can be performed while keeping the concentration of activated sludge in the aerobic treatment tank high, scum is not generated, and sludge can be discharged. It can be prevented. Further, according to the configuration of claim 2,
The above-described processing method can be effectively executed, and the above-mentioned conventional problems can be solved. Further, with the structure according to the third aspect, passage of ordinary sludge or the like (flock or the like of biofilm) can be prevented. Further, according to the structure of claim 4, even if the water-permeable membrane is closed, it can be easily washed and replaced by removing the member to which the membrane is attached from the partition plate. Further, according to the configuration of claim 5, the bubbles released from the air diffusing pipe ascend while being transmitted through the water-permeable membrane, whereby the membrane is vibrated, and the microbial membrane attached to the water-permeable membrane is efficiently separated. Therefore, the stable function of the water-permeable membrane can be maintained for a long period of time.
【図1】本発明の実施の形態の一例を示す浄化槽の断面
図である。FIG. 1 is a cross-sectional view of a septic tank showing an example of an embodiment of the present invention.
【図2】同縦断側面図である。FIG. 2 is a vertical sectional side view of the same.
【図3】仕切板より通水用膜を取り外す状態を示す同断
面図である。FIG. 3 is a cross-sectional view showing a state in which a water-permeable membrane is removed from a partition plate.
【図4】通水用膜部分を示す拡大斜視図である。FIG. 4 is an enlarged perspective view showing a water-permeable membrane portion.
【図5】従来構造を示す断面図である。FIG. 5 is a cross-sectional view showing a conventional structure.
A…浄化槽 A1…前処理槽 A2…好気処理槽 A3…処理水槽 1…仕切板 2…通水用膜 3…散気管 4…浮遊担体 A ... Septic tank A1 ... Pretreatment tank A2 ... Aerobic treatment tank A3 ... Treated water tank 1 ... Partition plate 2 ... Water-permeable membrane 3 ... Air diffuser 4 ... Floating carrier
フロントページの続き Fターム(参考) 4D003 AA12 AB04 BA01 BA02 CA02 CA04 DA11 DA18 DA19 DA21 EA01 EA19 FA01 4D027 AA02 AA12 AA14 AB06 AB12 AB14 Continued front page F-term (reference) 4D003 AA12 AB04 BA01 BA02 CA02 CA04 DA11 DA18 DA19 DA21 EA01 EA19 FA01 4D027 AA02 AA12 AA14 AB06 AB12 AB14
Claims (5)
浄化槽の処理方法であって、好気処理槽に浮遊担体を充
填し、通常のばっ気状態で汚水と担体を共に旋回させ、
その際、好気処理槽と沈殿槽を仕切る仕切板に取り付け
た通水用膜に沿って上昇させて、前記通水用膜に付着し
た生物膜を剥ぎ落とし、通水用膜の閉塞を防止すること
を特徴とする浄化槽の処理方法。1. A method for treating a septic tank in which an aerobic treatment tank and a sedimentation tank are separated by a partition plate, wherein the aerobic treatment tank is filled with a floating carrier, and the waste water and the carrier are swirled together in a normal aeration state. ,
At that time, it is raised along the water passage membrane attached to the partition plate that separates the aerobic treatment tank and the sedimentation tank, and the biological membrane adhering to the water passage membrane is peeled off to prevent clogging of the water passage membrane. A method for treating a septic tank, which comprises:
切板で完全に仕切り、その好気処理槽内に浮遊担体を充
填すると共に、仕切板の下部付近に散気管を配置し、更
に前記仕切板に、好気処理槽から沈殿槽へ処理汚水が通
過し得る通水用膜を設け、処理汚水が前記通水用膜を通
過する時、汚水中の汚泥が捕捉され、水分と超微細SS
のみが該通水用膜を通過するようにしたことを特徴とす
る浄化槽。2. An aerobic treatment tank and a sedimentation tank in a septic tank are completely partitioned by a partition plate, the aerobic treatment tank is filled with a floating carrier, and an air diffuser is arranged near the lower part of the partition plate. The partition plate is provided with a water passage membrane that allows treated wastewater to pass from the aerobic treatment tank to the sedimentation tank.When the treated wastewater passes through the water passage membrane, sludge in the wastewater is trapped, and water and ultrafine particles are trapped. SS
A septic tank characterized in that only the water is passed through the water-permeable membrane.
径が0.02〜0.07mmで、好気処理槽に充填した
浮遊担体がぶつかっても破損しない素材である請求項2
記載の浄化槽。3. The water-permeable membrane provided on the partition plate has a hole diameter of 0.02 to 0.07 mm and is a material that is not damaged even if the floating carrier filled in the aerobic treatment tank hits it.
The described septic tank.
在である請求項2又は3記載の浄化槽。4. The septic tank according to claim 2 or 3, wherein the water-permeable membrane is detachable from the partition plate.
り付けられ、且つその取付角度が15度〜45度である
ことを特徴とする請求項2乃至4のいずれか1項記載の
浄化槽。5. The partition plate according to claim 2, wherein the partition plate is mounted so as to be inclined toward the aerobic treatment tank, and the mounting angle is 15 degrees to 45 degrees. Septic tank.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2001384647A JP2003181483A (en) | 2001-12-18 | 2001-12-18 | Method for treating septic tank and the septic tank |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2001384647A JP2003181483A (en) | 2001-12-18 | 2001-12-18 | Method for treating septic tank and the septic tank |
Publications (1)
Publication Number | Publication Date |
---|---|
JP2003181483A true JP2003181483A (en) | 2003-07-02 |
Family
ID=27594327
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2001384647A Pending JP2003181483A (en) | 2001-12-18 | 2001-12-18 | Method for treating septic tank and the septic tank |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2003181483A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2010201378A (en) * | 2009-03-04 | 2010-09-16 | Kubota Corp | Water-purifier tank and method for operating the same |
ITPI20090078A1 (en) * | 2009-06-19 | 2010-12-19 | Zetaplast S P A | MODULAR TANK FOR WASTEWATER TREATMENT |
CN104118944A (en) * | 2014-08-12 | 2014-10-29 | 石家庄市源生园环保有限公司 | Draw-water ecological base system for purifying tail water from urban sewage treatment plants |
CN105884020A (en) * | 2016-05-16 | 2016-08-24 | 东华大学 | Low-energy-consumption fouling-resistant anaerobic membrane bioreactor |
-
2001
- 2001-12-18 JP JP2001384647A patent/JP2003181483A/en active Pending
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2010201378A (en) * | 2009-03-04 | 2010-09-16 | Kubota Corp | Water-purifier tank and method for operating the same |
ITPI20090078A1 (en) * | 2009-06-19 | 2010-12-19 | Zetaplast S P A | MODULAR TANK FOR WASTEWATER TREATMENT |
WO2011004226A3 (en) * | 2009-06-19 | 2011-05-26 | Zetaplast S.P.A. | Wastewater treatment tank |
CN104118944A (en) * | 2014-08-12 | 2014-10-29 | 石家庄市源生园环保有限公司 | Draw-water ecological base system for purifying tail water from urban sewage treatment plants |
CN105884020A (en) * | 2016-05-16 | 2016-08-24 | 东华大学 | Low-energy-consumption fouling-resistant anaerobic membrane bioreactor |
CN105884020B (en) * | 2016-05-16 | 2019-06-21 | 东华大学 | A kind of low energy consumption anti-pollution type anaerobic membrane bioreactor |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
JPH07155758A (en) | Waste water treating device | |
JP4119997B2 (en) | Wastewater septic tank | |
KR101037888B1 (en) | Hybrid wastewater treatment equipment with sedimentation, biological degradation, filtration, phosphorus removal and uv disinfection system in a reactor | |
JPH11197685A (en) | Method for treating membrane-separated activated sludge | |
JP2003181483A (en) | Method for treating septic tank and the septic tank | |
JP3700932B2 (en) | Method and apparatus for cleaning filter using ozone | |
CA2565052A1 (en) | System for improved dissolved air floatation with a biofilter | |
JPH06142668A (en) | Purifying treatment device for organic sewage | |
JP6834733B2 (en) | Wastewater treatment equipment | |
JP2002096090A (en) | Septic tank | |
JP2001079576A (en) | Private sewage treatment tank | |
JPH11216307A (en) | Overflow pipe of filtration tank | |
JP4124957B2 (en) | Filter body washing method and apparatus | |
JP3721092B2 (en) | Solid-liquid separation method and apparatus for activated sludge | |
JP3975393B2 (en) | Wastewater septic tank | |
JPH0418988A (en) | Biomembrane filter device for organic sewage | |
JP4346985B2 (en) | Middle water equipment, wastewater treatment equipment | |
JPH0350969Y2 (en) | ||
JP2006055852A (en) | Cleaning method and equipment for filter element | |
KR100305361B1 (en) | Household sewage treatment device | |
JP2008000720A (en) | Purification apparatus | |
JP3716461B2 (en) | Concentration method in the receiving tank for biological filtration backwash wastewater | |
JP2001129579A (en) | Waste water treating method and waste water treating apparatus | |
JP2002001375A (en) | Waste water treating apparatus | |
JPH03296494A (en) | Treatment apparatus for organic polluted water |