JP2892888B2 - Septic tank - Google Patents

Septic tank

Info

Publication number
JP2892888B2
JP2892888B2 JP19176092A JP19176092A JP2892888B2 JP 2892888 B2 JP2892888 B2 JP 2892888B2 JP 19176092 A JP19176092 A JP 19176092A JP 19176092 A JP19176092 A JP 19176092A JP 2892888 B2 JP2892888 B2 JP 2892888B2
Authority
JP
Japan
Prior art keywords
tank
water
contact
treated
aeration
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.)
Expired - Lifetime
Application number
JP19176092A
Other languages
Japanese (ja)
Other versions
JPH0631288A (en
Inventor
八郎 佐藤
広佳 中島
良人 北井
大 原田
勝己 浜田
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.)
Kubota Corp
Original Assignee
Kubota 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 Kubota Corp filed Critical Kubota Corp
Priority to JP19176092A priority Critical patent/JP2892888B2/en
Publication of JPH0631288A publication Critical patent/JPH0631288A/en
Application granted granted Critical
Publication of JP2892888B2 publication Critical patent/JP2892888B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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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)
  • Treatment Of Biological Wastes In General (AREA)

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は、嫌気濾床槽の下流に接
触ばっ気槽を設けた浄化槽に関する。
The present invention relates to a septic tank provided with a contact aeration tank downstream of an anaerobic filter bed tank.

【0002】[0002]

【従来の技術】従来、この種の浄化槽においては、例え
ば接触ばっ気槽の下流に沈殿槽を設け、その沈殿槽から
の上澄液を消毒槽に導き、ここで消毒した後、放流する
構成になっていた。
2. Description of the Related Art Conventionally, in this type of septic tank, for example, a sedimentation tank is provided downstream of a contact aeration tank, and the supernatant from the sedimentation tank is guided to a disinfection tank, where it is disinfected and then discharged. Had become.

【0003】[0003]

【発明が解決しようとする課題】ところが、このような
浄化槽において、処理能力を大きくしたいときには、接
触ばっ気槽を多段設ける等、浄化槽自体を大型化する必
要があり、そのため、スペースの制約があるところ等に
おいて対応しにくい欠点があった。
However, when it is desired to increase the processing capacity of such a septic tank, it is necessary to increase the size of the septic tank itself, for example, by providing multiple stages of contact aeration tanks, thereby limiting the space. However, there were drawbacks that were difficult to cope with.

【0004】そこで、本発明の目的は、浄化槽全体の占
めるスペースを実質的に大きくすることなく、汚水の処
理能力を高め、コンパクトで処理能力の大きい浄化槽を
提供することにある。
[0004] It is therefore an object of the present invention to provide a compact septic tank having a large treatment capacity without substantially increasing the space occupied by the entire septic tank and increasing the treatment capacity of sewage.

【0005】[0005]

【課題を解決するための手段】この目的を達成するため
の本願発明による浄化槽の特徴構成は、嫌気濾床槽の下
流に、接触材を内装してある接触ばっ気槽を設けた浄化
槽であって、前記接触ばっ気槽内に、濾材を充填してあ
る充填層を備え、上側に被処理水を取り込み可能な開口
部を設けた生物濾過槽を浸漬配置すると共に、その生物
濾過槽の底部に、濾液排出装置の濾液取り入れ口とばっ
気装置とを配設してあることにある。
Means for Solving the Problems] characterizing feature of the septic tank according to the present invention for achieving this object, under the anaerobic filter bed tank
The flow, a septic tank contact materials were provided aeration tank contact touch you have decorated, the contact aeration tank, filled with a filter medium tare
With an opening that can take in water to be treated
While immersed placed the biological filtration tank provided with parts, the organism
The bottom of the filtration tank is flush with the filtrate inlet of the filtrate discharge device.
And a ventilation device .

【0006】[0006]

【作用】接触ばっ気槽内に上側に被処理水を取り込み可
能な開口部を設け濾材を充填し、上側に被処理水を取
り込み可能な開口部を設けた生物濾過槽を浸漬配置する
と共に、その生物濾過槽の底部に、濾液排出装置の濾液
取り入れ口とばっ気装置とを配設してあるので、前記接
触ばっ気槽内の被処理水は、前記開口部から生物濾過槽
に流入して前記濾材と接触しながら底部に達し、前記濾
液排出装置の濾液取り入れ口から生物濾過槽外へ排出さ
れる。詳述すれば、このばっ気装置で常時少量散気して
生物濾過槽内の濾材に成育する好気性微生物に必要な酸
素を補足しながら、前記濾液排出装置の濾液取り入れ口
から生物濾過槽外へ濾液を排出することによって、生物
濾過槽内に充填された濾材の間隙を下方に被処理水が通
過し、被処理水中の浮遊懸濁物を濾過によって物理的に
捕捉すると共に、物理的に捕捉できないような微小な有
機物まで濾材に生息する微生物に捕捉させてこれらを分
解処理できるばかりでなく、物理的な濾過処理では原理
的に捕らえられない溶液として存在する有機物まで分解
処理することができる。又、前記ばっ気装置によって、
比較的多量のエアーを必要に応じ短時間バブリングさせ
る所謂逆洗を行うことにより、下方から上方に向かうエ
アーにより、濾材に付着した過剰の生物膜等が剥離させ
られ、そのエアーとともに上方側に除去させられる。そ
のため、濾材に過剰の生物膜等が付着して目詰まりを起
こすことを防止することができる。このとき逆洗により
除去された生物膜等は、汚泥として被処理水中に浮遊す
ることになるのであるが、前記生物処理槽は、前記接触
ばっ気槽内に浸漬されているから、上方側に浮遊させら
れた前記汚泥は、容易に前記接触ばっ気槽内へ浮遊して
再度処理されることになる。
[Function] The water to be treated can be taken into the upper part of the contact aeration tank.
Function opening , fill the filter medium, and take the water to be treated on the upper side.
The biological filtration tank having a interrupt enable opening while immersed placed on the bottom of the biological filtration tank, since the filtrate inlet of the filtrate discharge device and the aeration device and are arranged, the contact
The water to be treated in the contacting aeration tank flows from the opening through the biological filtration tank.
To the bottom while contacting the filter media,
Drained out of the biological filtration tank through the filtrate inlet of the liquid discharger
It is. More specifically, the aeration device constantly diffuses a small amount of gas to supplement the oxygen required for the aerobic microorganisms growing on the filter medium in the biological filtration tank. by discharging the filtrate, the water to be treated under the gap filter media filled in the biological filtration tank through the
In addition to physically trapping suspended suspensions in the water to be treated by filtration, not only can microorganisms living in the filter medium be trapped by micro-organisms that cannot be physically trapped, but also these can be decomposed, In a physical filtration treatment, it is possible to decompose an organic substance present as a solution that cannot be trapped in principle. Also, by the aeration device,
By performing a so-called backwashing bubbling short optionally a relatively large amount of air, e directed from bottom to top
Removes excess biofilm and the like adhering to the filter media
And is removed upward along with the air. So
Therefore, it is possible to prevent an excessive biofilm or the like from adhering to the filter medium and causing clogging. At this time,
The removed biofilm, etc. floats in the water to be treated as sludge.
However, the biological treatment tank is
Because it is immersed in the aeration tank,
The sludge that has been collected floats easily into the contact aeration tank.
It will be processed again.

【0007】[0007]

【発明の効果】従来の浄化槽では、沈殿槽において、沈
殿分離によるSSの除去だけしかできなかったのに比
し、本願発明による浄化槽は、沈殿槽を設けることな
く、生物濾過槽での濾過によってSSの除去や微小な有
機物の除去ができながら、生物処理も同時に行うことが
できるので、浄化槽全体の占めるスペースを最小限に抑
えながら、その処理能力を高め、SSやBODを、より
効果的に低減することができる。尚、生物濾過槽を接触
ばっ気槽から切り離してその下流に設ける構成も考えら
れるが、このように切り離した構成では浄化槽全体の占
めるスペースが大きくなるばかりでなく、生物濾過槽を
逆洗したときに剥離する剥離汚泥等を流入側の接触ばっ
気槽に戻すための返送路が必要となるのに比べ、本願発
明の構成による場合は、逆洗時の前記剥離汚泥が接触ば
っ気槽内の循環水に混入して処理されるため、このよう
な返送路を設けなくてもよく、全体をコンパクトなもの
に形成できるという利点もある。
According to the conventional septic tank, only the SS can be removed by sedimentation separation in the sedimentation tank. On the other hand, the septic tank according to the present invention does not require a sedimentation tank, but is filtered by a biological filtration tank. Biological treatment can be performed at the same time as removal of SS and minute organic matter, so the processing capacity is increased while minimizing the space occupied by the entire septic tank, and SS and BOD are more effectively reduced. Can be reduced. In addition, a configuration in which the biological filtration tank is separated from the contact aeration tank and provided downstream thereof is also conceivable. However, such a separated configuration not only increases the space occupied by the entire septic tank, but also results when the biological filtration tank is backwashed. In contrast to the necessity of a return path for returning the separated sludge and the like to be separated to the inflow side contact aeration tank, in the case of the configuration of the present invention, the separated sludge at the time of backwashing is in the contact aeration tank. Since it is mixed with circulating water and treated, there is no need to provide such a return path, and there is an advantage that the whole can be formed into a compact one.

【0008】[0008]

【実施例】以下、本発明の実施例について説明する。図
1に示すように、上流側から、嫌気濾床槽第1室N1及
び嫌気濾床槽第2室N2からなる嫌気濾床槽N、接触ば
っ気槽Eを、被処理液が自然移流によりこの順に流れる
ように設けて浄化槽を構成してある。
Embodiments of the present invention will be described below. As shown in FIG. 1, an anaerobic filter bed tank N composed of an anaerobic filter bed tank first chamber N1 and an anaerobic filter bed tank second chamber N2, and a contact aeration tank E are flowed from the upstream side by natural advection. A septic tank is provided so as to flow in this order.

【0009】前記嫌気濾床槽Nには、被処理水中の有機
物を嫌気分解する嫌気性微生物を生育してその生物膜を
定着させるために、濾床F1、F2を設けてある。前記
接触ばっ気槽Eは、被処理水中の残りの有機物の分解や
アンモニア性窒素の硝化反応等を行う好気性微生物を定
着させるために、プラスチック製の接触材Cを、ネット
自体の目巾が10mm角で、平面視で目巾50〜80m
mのハニカムチューブネットに一体成形して設けると共
に、槽内に被処理水の循環流を生ぜしめ、前記接触材C
に定着させた好気性微生物に、有機物を含む被処理水を
よく接触させて、この好気性微生物に必要な酸素を与え
るエアーを供給するために、PVC製パイプに多数の上
向き散気孔を形成した1対の散気管D1、D1を、嫌気
濾床槽第2室N2側の隔壁Wと接触材Cとの間に形成さ
れた間隙の底部に、前記隔壁に沿って水平に配し、エア
ー供給用ブロワーに連通接続してある。散気管D1、D
1からの散気量並びに前記隔壁Wと接触材C間の間隙の
広さは、この間隙を上昇する被処理水の流速が30cm
/s程度、前記接触材C内を下降する被処理水の流速が
10cm/s程度の循環流になるようにしてある。
The anaerobic filter bed tank N is provided with filter beds F1 and F2 in order to grow anaerobic microorganisms that anaerobically decompose organic substances in the water to be treated and to fix their biofilms. The contact aeration tank E is used to fix aerobic microorganisms that decompose the remaining organic matter in the water to be treated and perform nitrification of ammoniacal nitrogen. 10 mm square, eye width 50 to 80 m in plan view
m is formed integrally with the honeycomb tube net of m, and a circulating flow of the water to be treated is generated in the tank.
A large number of upward air diffusion holes were formed in a PVC pipe in order to contact the aerobic microorganisms fixed in the well with the water to be treated containing organic matter and to supply air for supplying oxygen necessary for the aerobic microorganisms. A pair of air diffusers D1, D1 are horizontally arranged along the partition wall at the bottom of the gap formed between the partition wall W and the contact material C on the anaerobic filter bed second chamber N2 side to supply air. Connected to a blower for air. Air diffuser D1, D
1 and the width of the gap between the partition wall W and the contact material C, the flow rate of the water to be treated rising through this gap is 30 cm.
/ S, and the flow rate of the water to be treated descending in the contact material C is set to a circulation flow of about 10 cm / s.

【0010】又、接触材Cに過剰の生物膜等が付着して
目詰まりを起こすことを防止するため、常時又は間欠的
に、必要に応じ、エアーをバブリングさせて、過剰の生
物膜等を剥離汚泥として剥離するための逆洗管Rを接触
材Cの下方に設けてある。尚、接触ばっ気槽E内の浮遊
懸濁物濃度やBOD等が大きくなりすぎることを防ぐた
め、接触ばっ気槽E内の被処理液の一部を常時又は間欠
的に前記嫌気濾床槽第1室N1に返送して脱窒処理等を
促進することができるように、エアーリフトポンプAを
接触ばっ気槽Eの底部から立ち上がらせ、エアーリフト
ポンプAから嫌気濾床槽第1室N1に通ずる返送路Bを
設けてある。
In order to prevent clogging due to excessive biofilms and the like adhering to the contact material C, air is constantly or intermittently bubbled as necessary to remove the excess biofilms and the like. A backwash pipe R for stripping as stripped sludge is provided below the contact material C. In order to prevent the concentration of suspended solids, BOD, etc. in the contact aeration tank E from becoming too large, a part of the liquid to be treated in the contact aeration tank E is constantly or intermittently removed from the anaerobic filter bed tank. The air lift pump A rises from the bottom of the contact aeration tank E so that the air can be returned to the first chamber N1 to accelerate the denitrification treatment and the like. A return path B is provided.

【0011】次に、本願発明の独特の構成を示すところ
の生物濾過槽1について説明する。生物濾過槽1は、接
触材Cの上面付近から下面付近にわたる長さの円筒状の
ケーシング2内に30mm径以内のプラスチック製小型
濾材を多数一様に充填してなる充填層3を収容したもの
で、これが4脚を有する支持台4上に載置された状態で
前記接触材Cの略中央に鉛直に配設されている。ケーシ
ング2は底5を設けてあるが、その上端は接触材Cの上
端のレベル付近で開放して被処理水を取り込むための開
口部6に形成してある。生物濾過槽1には、更に、充填
層3の下方に濾液取り入れ口7を有する濾液排出装置た
る濾液排出エアーリフト管8を生物濾過槽1の内壁又は
外壁に沿って立ち上がらせて消毒槽Qに連通させ、この
濾液排出エアーリフト管8の下端近くにエアーリフト用
エアー供給管9を前記ブロワーから連通配管してある。
生物濾過槽1には、又、充填層3に成育させる好気性微
生物に酸素を補足するための散気管と、充填層3の目詰
まりを防ぐための逆洗管とを兼ねるばっ気装置10とし
て、PVC製パイプに多数の上向き散気孔を形成したも
のを、前記ブロワーに連通接続して、充填層3の下方に
水平に配設してある。ばっ気装置10に供給されるエア
ー流量は、通常の散気時の小さい流量と、間欠的に行う
逆洗時の大きい流量とに簡単に切替えられるように、切
替えバルブを設けてある。尚、充填層3に成育させる好
気性微生物に酸素を供給するための散気管と、充填層3
の目詰まりを防ぐための逆洗管とを兼用しないで、別個
に設ける構成にしてもよい。
Next, a biological filtration tank 1 showing a unique configuration of the present invention will be described. The biological filtration tank 1 accommodates a packed layer 3 formed by uniformly filling a large number of small plastic filter media having a diameter of 30 mm or less into a cylindrical casing 2 having a length extending from near the upper surface to near the lower surface of the contact material C. The contact member C is vertically disposed substantially at the center of the contact member C in a state where the contact member C is placed on a support base 4 having four legs. The casing 2 is provided with a bottom 5 whose upper end is formed in an opening 6 for opening near the upper end level of the contact material C to take in the water to be treated. In the biological filtration tank 1, a filtrate discharge air lift pipe 8, which is a filtrate discharge device having a filtrate intake port 7 below the packed bed 3, rises along the inner wall or the outer wall of the biological filtration tank 1, and enters the disinfection tank Q. An air supply pipe 9 for air lift is connected near the lower end of the filtrate discharge air lift pipe 8 from the blower.
The biological filtration tank 1 also has an aeration device 10 serving as a diffuser tube for supplementing oxygen to aerobic microorganisms grown in the packed bed 3 and a backwashing tube for preventing clogging of the packed bed 3. A large number of upwardly diffusing holes formed in a PVC pipe are connected to the blower and horizontally disposed below the packed bed 3. A switching valve is provided so that the flow rate of air supplied to the aeration apparatus 10 can be easily switched between a small flow rate during normal air diffusion and a large flow rate during intermittent backwashing. In addition, an air diffuser for supplying oxygen to the aerobic microorganisms grown in the packed bed 3 and a packed bed 3
May be provided separately without being used as a backwash tube for preventing clogging.

【0012】エアーリフト管8からの揚水量は、浄化槽
への原水の平均流入量の1.5〜2倍程度になるよう
に、且つ充填層3を下降する被処理水の流速が5cm/
s程度以下になるように、エアーリフト管8への供給エ
アー流量や充填槽3の断面積等を設定すると共に、接触
ばっ気層E内の水位が管理下限水位迄下がるとエアーリ
フト管8への供給エアーが自動的に止まるようにレベル
センサーと、これに連動して開閉する電磁バルブを設け
てある。
The amount of water to be pumped from the air lift pipe 8 is set to be about 1.5 to 2 times the average amount of raw water flowing into the septic tank, and the flow rate of the water to be treated descending the packed bed 3 is 5 cm /
The flow rate of air supplied to the air lift tube 8 and the cross-sectional area of the filling tank 3 are set so as to be about s or less, and when the water level in the contact aeration layer E falls to the lower control limit water level, the air lift tube 8 A level sensor and an electromagnetic valve that opens and closes in conjunction with the level sensor are provided so that the supplied air automatically stops.

【0013】前記濾液排出エアーリフト管8からの放出
液は消毒槽Qに導かれる。消毒槽Qの入口には、固形消
毒剤を収容した薬筒Tが配設されており、薬筒Tには、
その下部に被処理水流入流出用のスリット状開口を複数
形成してある。薬筒T中の消毒剤と接触した被処理水は
消毒槽の中程に設けられた邪魔板の下をくぐり、溢流し
て放流されるようにしてある。
The liquid discharged from the filtrate discharge air lift pipe 8 is guided to a disinfection tank Q. At the entrance of the disinfecting tank Q, a cartridge T containing a solid disinfectant is disposed.
A plurality of slit-shaped openings for inflow and outflow of the water to be treated are formed in a lower portion thereof. The water to be treated that has come into contact with the disinfectant in the cartridge T passes under a baffle provided in the middle of the disinfection tank, and overflows and is discharged.

【0014】尚、特許請求の範囲の項に図面との対照を
便利にするために符号を記すが、該記入により本発明は
添付図面の構成に限定されるものではない。
In the claims, reference numerals are provided for convenience of comparison with the drawings, but the present invention is not limited to the configuration shown in the attached drawings.

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

【図1】実施例における浄化槽の縦断側面図FIG. 1 is a vertical sectional side view of a septic tank in an embodiment.

【符号の説明】[Explanation of symbols]

E 接触ばっ気槽 N 嫌気濾床槽 1 生物濾過槽 7 濾液取り入れ口 8 濾液排出装置 10 ばっ気装置 E contact aeration tank N anaerobic filter bed tank 1 biological filtration tank 7 filtrate inlet 8 filtrate discharge device 10 aeration device

───────────────────────────────────────────────────── フロントページの続き (72)発明者 原田 大 滋賀県甲賀郡甲西町高松2番地の1 株 式会社クボタ 滋賀工場内 (72)発明者 浜田 勝己 滋賀県甲賀郡甲西町高松2番地の1 株 式会社クボタ 滋賀工場内 (56)参考文献 特開 平3−232588(JP,A) 実開 平3−83695(JP,U) 実開 平2−125799(JP,U) (58)調査した分野(Int.Cl.6,DB名) C02F 3/00 ──────────────────────────────────────────────────続 き Continuing on the front page (72) Dai Harada, Inventor 2 at Takamatsu, Kosai-cho, Koga-gun, Shiga Prefecture Inside the Kubota Shiga Plant. Kubota Corporation Shiga Factory (56) References JP-A-3-232588 (JP, A) JP-A-3-83695 (JP, U) JP-A-2-125799 (JP, U) (58) Field (Int.Cl. 6 , DB name) C02F 3/00

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 嫌気濾床槽(N)の下流に、接触材
(C)を内装してある接触ばっ気槽(E)を設けた浄化
槽であって、 前記接触ばっ気槽(E)内に、濾材を充填してある充填
層(3)を備え、上側に被処理水を取り込み可能な開口
部(6)を設けた生物濾過槽(1)を浸漬配置すると共
に、その生物濾過槽(1)の底部に、濾液排出装置
(8)の濾液取り入れ口(7)とばっ気装置(10)と
を配設してある浄化槽。
A contact material is provided downstream of an anaerobic filter tank (N).
A septic tank provided with aeration tank (E) against touch of the (C) are then furnished to the contact aeration tank (E) filling, it is filled with filter media
Opening provided with layer (3) and capable of taking in water to be treated on the upper side
A biological filtration tank (1) provided with a part (6) is immersed and arranged, and a filtrate inlet (7) of a filtrate discharge device (8) and an aeration device (10) are provided at the bottom of the biological filtration tank (1). And a septic tank.
JP19176092A 1992-07-20 1992-07-20 Septic tank Expired - Lifetime JP2892888B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP19176092A JP2892888B2 (en) 1992-07-20 1992-07-20 Septic tank

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP19176092A JP2892888B2 (en) 1992-07-20 1992-07-20 Septic tank

Publications (2)

Publication Number Publication Date
JPH0631288A JPH0631288A (en) 1994-02-08
JP2892888B2 true JP2892888B2 (en) 1999-05-17

Family

ID=16280058

Family Applications (1)

Application Number Title Priority Date Filing Date
JP19176092A Expired - Lifetime JP2892888B2 (en) 1992-07-20 1992-07-20 Septic tank

Country Status (1)

Country Link
JP (1) JP2892888B2 (en)

Also Published As

Publication number Publication date
JPH0631288A (en) 1994-02-08

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