JP2000317481A - Septic tank - Google Patents

Septic tank

Info

Publication number
JP2000317481A
JP2000317481A JP13325399A JP13325399A JP2000317481A JP 2000317481 A JP2000317481 A JP 2000317481A JP 13325399 A JP13325399 A JP 13325399A JP 13325399 A JP13325399 A JP 13325399A JP 2000317481 A JP2000317481 A JP 2000317481A
Authority
JP
Japan
Prior art keywords
chamber
septic tank
sewage
aeration
aeration 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
JP13325399A
Other languages
Japanese (ja)
Inventor
Soetsu Kitamura
総謁 北村
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 JP13325399A priority Critical patent/JP2000317481A/en
Publication of JP2000317481A publication Critical patent/JP2000317481A/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

  • Treatment Of Biological Wastes In General (AREA)
  • Biological Treatment Of Waste Water (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a septic tank low in manufacturing cost and maintenance cost and having stable purification capacity sufficient for purifying sewage. SOLUTION: In an aeration chamber 5, countless fluidized carriers 9 on whose each surface aerobic bacteria are supported are filled to circulate by convection up and down together with the sewage by the air supplied through an air diffusing pipe 10. A partition member 13 is provided between the aeration chamber 5 and a precipitation chamber 6 to guide each carrier 9 to the convection direction and obstruct the outflow of each carrier 9. In the precipitation chamber 6, the sewage is circulated by convection together with the carriers 9 by the air supplied through the air diffusing pipe 10 to transfer solids on the bottom of the precipitation chamber 6 to the aeration chamber 5.

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】本発明は浄化槽に関する。こ
の浄化槽は、屎尿の浄化が可能な単独浄化槽や屎尿の他
に雑排水の浄化も可能な合併浄化槽に利用できる。
The present invention relates to a septic tank. This septic tank can be used for a single septic tank capable of purifying human waste and a combined septic tank capable of purifying miscellaneous wastewater in addition to human waste.

【0002】[0002]

【従来の技術】従来、屎尿や雑排水等からなる汚水を浄
化する一般的な浄化槽として、接触曝気方式の曝気室と
沈殿室とを有するものが知られている。この曝気室に
は、上方に濾材(接触材)が固定され、下方には空気等
の酸素含有ガスを送り込むブロアと接続された散気管が
設けられている。なお、この曝気室には下端が底部に開
口して上方に垂直に延在する筒状の清掃筒が設けられ得
る。また、曝気室の下方には同様のブロアに接続されて
酸素含有ガスを供給する逆洗管も設けられ得る。さら
に、曝気室の上流側に隔壁により仕切られた嫌気室を有
する合併浄化槽にあっては、曝気室の底部に一端が開口
し、他端が嫌気室に開口する移送管も設けられ得る。他
方、曝気室の下流側には底部が連通する隔壁により仕切
られた沈殿室が隣接されている。
2. Description of the Related Art Heretofore, as a general purification tank for purifying sewage water consisting of human waste and miscellaneous wastewater, a purification tank having a contact aeration type aeration chamber and a sedimentation chamber is known. In the aeration chamber, a filter medium (contact material) is fixed on the upper side, and a diffuser pipe connected to a blower for feeding an oxygen-containing gas such as air is provided below. The aeration chamber may be provided with a cylindrical cleaning cylinder whose lower end is opened at the bottom and extends vertically upward. A backwash tube connected to a similar blower and supplying an oxygen-containing gas may be provided below the aeration chamber. Further, in a combined septic tank having an anaerobic chamber partitioned by a partition on the upstream side of the aeration chamber, a transfer pipe having one end opened at the bottom of the aeration chamber and the other end opened to the anaerobic chamber may be provided. On the other hand, on the downstream side of the aeration chamber, a sedimentation chamber separated by a partition wall whose bottom communicates is adjacent.

【0003】この種の浄化槽では、曝気室内に汚水が上
方から供給されるようになっており、この汚水は、濾材
の間隙を流れるとともに、濾材の表面に住みついた好気
性バクテリアによって汚れの分解を受ける。この間、散
気管は好気性バクテリアに酸素を供給する。なお、逆洗
管を備えた浄化槽にあっては、必要の都度逆洗管が供給
する酸素含有ガスにより、濾材にくっついて繁殖した余
分な好気性バクテリア(固形物)を濾材から剥離させる
ことができる。こうして曝気室内にはある程度浄化され
た処理水が貯留され、この処理水は下流側の沈殿室内に
おいて未だ含有する固形物を沈殿し、上澄みの水が所望
により消毒水の添加を受けて排出されることとなる。
In this type of septic tank, sewage is supplied into the aeration chamber from above. The sewage flows through the gap between the filter media, and is also decomposed by aerobic bacteria living on the surface of the filter media. receive. During this time, the air diffuser supplies oxygen to the aerobic bacteria. In the case of a septic tank equipped with a backwash tube, extra aerobic bacteria (solid matter) that adhered to the filter medium and propagated by the oxygen-containing gas supplied from the backwash tube whenever necessary can be separated from the filter medium. it can. The treated water thus purified to some extent is stored in the aeration chamber, and the treated water precipitates solids still contained in the downstream settling chamber, and the supernatant water is discharged with the addition of disinfecting water as desired. It will be.

【0004】沈殿室内に残留する固形物は、沈殿室と曝
気室とが底部において連通しているため、曝気室におい
て好気性バクテリアによる再度の汚れの分解を受けるこ
ととなる。そして、移送管を備えた合併浄化槽にあって
は、同様のブロアから供給された酸素含有ガスにより発
せられた水流を移送管が取り込むことから、曝気室に残
留する固形物はこの移送管により上流側の嫌気室に移送
され、嫌気室において嫌気性バクテリアによって汚れの
分解を受けることとなる。固形物が曝気室に残留する場
合、清掃筒に業者がホースを挿入し、ホースによりその
固形物を引き抜くこととなる。
The solids remaining in the sedimentation chamber are subject to the re-decomposition of the dirt by the aerobic bacteria in the aeration chamber, since the sedimentation chamber and the aeration chamber communicate at the bottom. In a combined septic tank equipped with a transfer pipe, the transfer pipe takes in the water flow generated by the oxygen-containing gas supplied from the same blower, so that the solid matter remaining in the aeration chamber is upstream from the transfer pipe. The anaerobic chamber is transported to the anaerobic chamber, where the anaerobic bacteria undergoes the decomposition of dirt. If the solid remains in the aeration chamber, the trader inserts a hose into the cleaning cylinder and pulls the solid through the hose.

【0005】[0005]

【発明が解決しようとする課題】しかし、上記従来の一
般的な浄化槽にあっては、曝気室内に濾材が固定されて
いるため、濾材の表面の好気性バクテリアによって汚れ
を分解する際、濾材に余分な好気性バクテリア(固形
物)からなる目詰まりを生じ易い。このため、その浄化
槽は、そのままでは浄化能力の低下を生じてしまう。ま
た、逆洗管により余分な固形物を濾材から剥離して浄化
能力の回復を図らんとすれば、逆洗管の分だけ製造コス
ト及び維持コストの高騰化を生じてしまう。
However, in the above-mentioned conventional general septic tank, since the filter medium is fixed in the aeration chamber, when the dirt is decomposed by the aerobic bacteria on the surface of the filter medium, the filter medium is removed. Clogging is likely to occur due to extra aerobic bacteria (solids). For this reason, the purification tank will cause a reduction in the purification ability as it is. Further, if an attempt is made to recover the purification ability by removing extra solid matter from the filter medium by the backwash tube, the production cost and the maintenance cost are increased by the amount of the backwash tube.

【0006】この点、出願人が先に提案した特願平10
−123072号及び特願平10−123073号のよ
うに、曝気室内に無数の流動担体を充填した浄化槽とす
ることが考えられる。かかる浄化槽では、表面に好気性
バクテリアが担持された各流動担体が散気管から供給さ
れる酸素含有ガスにより汚水とともに上下に対流するた
め、上記のような目詰まりによる浄化能力の低下を生じ
ることはない。むしろ、酸素含有ガスにより好気性バク
テリアに安定して酸素を供給しつつ、好気性バクテリア
と汚水とが接触し易くなる。また、各流動担体が互いに
衝突・干渉・当接して表面にくっついて繁殖した余分な
固形物を剥離させることができる。こうして汚水は、好
気性バクテリアによって汚れが分解されやすく、浄化能
力が高まる。また、逆洗管が不要になり、製造コスト及
び維持コストの低廉化を実現できる。
[0006] In this regard, Japanese Patent Application No. Hei 10
As in JP-A-123072 and Japanese Patent Application No. 10-123073, a septic tank in which an aeration chamber is filled with a myriad of fluid carriers can be considered. In such a septic tank, since each fluid carrier having an aerobic bacterium on the surface convects up and down together with the sewage by the oxygen-containing gas supplied from the air diffuser, the purification ability due to the clogging described above may not be reduced. Absent. Rather, the oxygen-containing gas makes it easier for the aerobic bacteria to come into contact with the sewage while stably supplying oxygen to the aerobic bacteria. In addition, each of the fluid carriers collides, interferes, and abuts on each other, and sticks to the surface, so that extra solid matter that has propagated can be separated. In this way, the sewage is easily decomposed by the aerobic bacteria, and the purification ability is enhanced. In addition, a backwash tube is not required, and the manufacturing cost and the maintenance cost can be reduced.

【0007】しかしながら、かかる流動担体を用いた曝
気室を有する浄化槽であっても、沈殿室内に残留する固
形物が曝気室において好気性バクテリアにより汚れの分
解を受け難いのであれば、結果的に満足できる汚水の浄
化能力が安定して得られ難い。本発明は、上記従来の実
状に鑑みてなされたものであって、製造コスト及び維持
コストの低廉化を実現しつつ、満足できる汚水の浄化能
力を安定して発揮可能な浄化槽を提供することを解決す
べき課題としている。
[0007] However, even in a septic tank having an aeration chamber using such a fluid carrier, if the solid matter remaining in the sedimentation chamber is hardly decomposed by aerobic bacteria in the aeration chamber, the result is satisfactory. It is difficult to obtain stable sewage purification ability. The present invention has been made in view of the above conventional situation, and provides a septic tank capable of stably exhibiting a satisfactory sewage purification ability while realizing low production costs and low maintenance costs. It is an issue to be solved.

【0008】[0008]

【課題を解決するための手段】本発明の浄化槽は、貯留
した汚水中に酸素含有ガスを供給する散気管が設けら
れ、該汚水を好気性バクテリアにより浄化する曝気室
と、底部が連通する隔壁により仕切られつつ該曝気室に
隣接し、該汚水を沈殿により固形物と水とに分離する沈
殿室とを有する浄化槽において、前記曝気室内には、表
面に前記好気性バクテリアが担持され、前記散気管から
供給される前記酸素含有ガスにより前記汚水とともに上
下に対流する無数の流動担体が充填され、該曝気室と前
記沈殿室との間には、各該流動担体を対流方向に案内し
つつ各該流動担体の流出を阻止する分離部材が設けら
れ、該沈殿室は、該散気管から供給される該酸素含有ガ
スで各該流動担体とともに対流する該汚水により、該沈
殿室内の底部の固形物を該曝気室に移送可能になされて
いることを特徴とする。
A septic tank according to the present invention is provided with a diffuser pipe for supplying oxygen-containing gas to stored sewage, and an aeration chamber for purifying the sewage with aerobic bacteria, and a partition communicating with a bottom. A septic tank having a sedimentation chamber adjacent to the aeration chamber while being separated by water and separating the sewage into solids and water by sedimentation, wherein the aerobic bacteria are supported on the surface of the aeration chamber, The oxygen-containing gas supplied from the trachea is filled with countless fluid carriers that convect up and down together with the wastewater, and between the aeration chamber and the precipitation chamber, each fluid carrier is guided in the convection direction while A separating member is provided for preventing the outflow of the fluidized carrier, and the sedimentation chamber is provided with a solid substance at the bottom of the sedimentation chamber by the sewage convection with the fluidized carrier with the oxygen-containing gas supplied from the air diffuser. To Characterized in that it is adapted to allow transfer to the aeration chamber.

【0009】本発明の浄化槽にあっては、曝気室内にお
いて、表面に好気性バクテリアが担持された無数の流動
担体が散気管から供給される酸素含有ガスにより汚水と
ともに上下に対流するため、従来の接触曝気方式の曝気
室を有する浄化槽のような濾材の目詰まりによる浄化能
力の低下を生じることはない。むしろ、酸素含有ガスに
より好気性バクテリアに安定して酸素を供給しつつ、好
気性バクテリアと汚水とが接触し易くなる。また、各流
動担体が互いに衝突・干渉・当接して表面にくっついて
繁殖した余分な固形物を剥離させることができる。こう
して汚水は、好気性バクテリアによって汚れが分解され
やすく、浄化能力が高まる。また、逆洗管が不要にな
り、製造コスト及び維持コストの低廉化を実現できる。
In the septic tank according to the present invention, in the aeration chamber, a myriad of fluid carriers carrying aerobic bacteria on the surface are convected up and down together with the sewage by the oxygen-containing gas supplied from the air diffuser. There is no reduction in the purification capacity due to clogging of the filter medium as in a septic tank having a contact aeration type aeration chamber. Rather, the oxygen-containing gas makes it easier for the aerobic bacteria to come into contact with the sewage while stably supplying oxygen to the aerobic bacteria. In addition, each of the fluid carriers collides, interferes, and abuts on each other, and sticks to the surface, so that extra solid matter that has propagated can be separated. In this way, the sewage is easily decomposed by the aerobic bacteria, and the purification ability is enhanced. In addition, a backwash tube is not required, and the manufacturing cost and the maintenance cost can be reduced.

【0010】また、この浄化槽にあっては、沈殿室にお
いて、散気管から供給される酸素含有ガスで各流動担体
とともに対流する汚水により、沈殿室内の底部の固形物
を曝気室に移送可能になされている。例えば、沈殿室を
底部側に向かうほど狭く形成することにより、沈殿室の
底部側が曝気室内を対流する汚水で負圧になり、沈殿室
内の底部の固形物が曝気室に吸い込まれるように移送さ
れる(スロット効果)。この際、曝気室と沈殿室との間
には分離部材が設けられ、この分離部材が各流動担体の
流出を阻止する。また、分離部材は各流動担体を対流方
向に案内することから、各流動担体は流出しようとして
分離部材と衝突してもその対流が阻止されず、スロット
効果を効果的に生じることとなる。このため、沈殿室内
に残留する固形物が曝気室において好気性バクテリアに
より汚れの分解を受け易く、結果的に満足できる汚水の
浄化能力が安定して得られる。
Further, in this septic tank, the solid matter at the bottom of the sedimentation chamber can be transferred to the aeration chamber in the sedimentation chamber by the sewage convection with each fluid carrier with the oxygen-containing gas supplied from the air diffuser. ing. For example, by forming the sedimentation chamber narrower toward the bottom side, the bottom side of the sedimentation chamber becomes negative pressure due to the sewage convection in the aeration chamber, and the solid matter at the bottom in the sedimentation chamber is transferred so as to be sucked into the aeration chamber. (Slot effect). At this time, a separating member is provided between the aeration chamber and the settling chamber, and the separating member prevents outflow of each fluid carrier. Further, since the separating member guides each fluid carrier in the convection direction, even if each fluid carrier tries to flow and collides with the separating member, the convection is not prevented, and the slot effect is effectively generated. For this reason, the solid matter remaining in the sedimentation chamber is easily susceptible to the decomposition of dirt by the aerobic bacteria in the aeration chamber, and as a result, a satisfactory sewage purification ability can be stably obtained.

【0011】分離部材としては、各流動担体の対流方向
に延在し、各流動担体と当接可能なガイド部を有するも
のを採用することができる。この分離部材では、ガイド
部が各流動担体と当接して各流動担体を対流方向に案内
する。この分離部材はガイド部と交差する補強部を有す
ることが好ましい。浄化槽はこの分離部材を設けた後か
ら各流動担体を充填することにより製造される。かかる
各流動担体の充填の際、分離部材には各流動担体の衝突
力が作用する。また、製造した浄化槽は曝気室内に各流
動担体を充填した状態で出荷、搬送されることとなる。
かかる出荷等の際、分離部材にはやはり各流動担体の自
重による衝突力が作用する。さらに、浄化槽の運転の
際、各流動担体は対流し、汚水とともに分離部材に衝突
力を及ぼす。分離部材が補強部を有しておれば、それら
の際に生じる衝突力に確実に耐えることができる。かか
る補強部は曝気室側に突出していないことが好ましい。
曝気室側に補強部が突出しておれば、各流動担体を案内
する際の抵抗が大きくなるからである。
As the separating member, a member extending in the direction of convection of each fluid carrier and having a guide portion capable of contacting each fluid carrier can be employed. In this separation member, the guide portion comes into contact with each fluid carrier and guides each fluid carrier in the convection direction. This separating member preferably has a reinforcing portion that intersects the guide portion. The septic tank is manufactured by filling each fluid carrier after providing the separation member. When filling each of the fluid carriers, a collision force of each fluid carrier acts on the separation member. In addition, the manufactured septic tank is shipped and transported in a state where each fluid carrier is filled in the aeration chamber.
At the time of such shipping or the like, a collision force due to the weight of each fluid carrier also acts on the separation member. Furthermore, during operation of the septic tank, each fluid carrier convects and exerts a collision force on the separation member together with the waste water. If the separating member has the reinforcing portion, it can surely withstand a collision force generated at that time. It is preferable that such a reinforcing portion does not protrude toward the aeration chamber.
This is because if the reinforcing portion protrudes toward the aeration chamber, the resistance when guiding each fluid carrier increases.

【0012】ガイド部は、各流動担体との接触面積が小
さく、これにより各流動担体を案内する際の抵抗を小さ
くできる形状のものが好ましい。このようなガイド部と
しては、軸直角方向の断面形状が一般的な円形のものの
他、楕円形や三角形、四角形等の多角形であるものを採
用することができる。軸直角方向の断面形状が円形のガ
イド部であれば、購入が容易であり、浄化槽の製造コス
トの低廉化を実現できる。また、軸直角方向の断面形状
が多角形のガイド部であれば、その多角形の頂角が曝気
室側に位置すれば、各流動担体を案内しやすく、各流動
担体を案内する際の抵抗も小さくしやすい。
The guide portion is preferably of a shape which has a small contact area with each fluid carrier and can thereby reduce the resistance when guiding each fluid carrier. As such a guide portion, a polygonal shape such as an elliptical shape, a triangular shape, a quadrangular shape, or the like can be employed in addition to a general circular shape having a cross-sectional shape in a direction perpendicular to the axis. If the guide section has a circular cross section in the direction perpendicular to the axis, it is easy to purchase, and the manufacturing cost of the septic tank can be reduced. Further, if the cross-sectional shape in the direction perpendicular to the axis is a polygonal guide portion, if the apex angle of the polygon is located on the aeration chamber side, it is easy to guide each fluid carrier, and the resistance at the time of guiding each fluid carrier is improved. Also easy to make small.

【0013】分離部材は、散気管に向かって下り勾配と
なるように傾斜又は湾曲されていることが好ましい。こ
れにより、曝気室の底部において、沈殿室側で沈んでく
る各流動担体が分離部材に案内されて散気管により再度
浮上させられることとなり、各流動担体の対流が規則的
になるとともに、スロット効果を生じ易い。したがっ
て、本発明の浄化槽では、製造コスト及び維持コストの
低廉化を実現しつつ、満足できる汚水の浄化能力を安定
して発揮することができる。
Preferably, the separating member is inclined or curved so as to have a downward slope toward the air diffuser. Thereby, at the bottom of the aeration chamber, each fluid carrier settling on the sedimentation chamber side is guided by the separating member and floated again by the diffuser tube, so that the convection of each fluid carrier becomes regular and the slot effect is obtained. Tends to occur. Therefore, in the septic tank of the present invention, a satisfactory purification performance of sewage can be stably exhibited while realizing a reduction in manufacturing cost and maintenance cost.

【0014】[0014]

【発明の実施の形態】以下、本発明を具体化した実施形
態1〜8を図面を参照しつつ説明する。 (実施形態1)実施形態1では本発明の浄化槽を家庭用
合併浄化槽に具体化している。この浄化槽では、図1に
示すように、FRP製のケーシング1内に垂直方向に延
在するFRP製の隔壁2及び隔壁3が固定され、ケーシ
ング1の前内面と隔壁2とにより嫌気室4が形成され、
ケーシング1の内側面と隔壁2、3とにより曝気室5が
形成され、ケーシング1の後内面と隔壁3とにより沈殿
室6が形成されている。
DESCRIPTION OF THE PREFERRED EMBODIMENTS Embodiments 1 to 8 embodying the present invention will be described below with reference to the drawings. (Embodiment 1) In Embodiment 1, the septic tank of the present invention is embodied as a household combined septic tank. In this septic tank, as shown in FIG. 1, an FRP partition 2 and a partition 3 extending vertically are fixed in an FRP casing 1, and an anaerobic chamber 4 is formed by the front inner surface of the casing 1 and the partition 2. Formed,
An aeration chamber 5 is formed by the inner surface of the casing 1 and the partitions 2 and 3, and a sedimentation chamber 6 is formed by the rear inner surface of the casing 1 and the partition 3.

【0015】嫌気室4は、濾材を入れない沈殿分離室
(腐敗室)であってもよく、濾材を入れる嫌気濾床室で
あってもよい。この嫌気室4に汚水を流入する流入口7
回りにはバッフル8がケーシング1に固定されている。
曝気室5内には、無数の流動担体9が曝気室5の容積の
20〜80%程度の容積で充填されている。これらの流
動担体9は比重が0.93のポリエチレンにより形成さ
れ、大きな表面積を確保しつつ、気泡を捕捉しない外形
をなしている。また、曝気室5の最底部における隔壁2
側には、隔壁2と平行かつ水平に柱状の散気管10が設
けられており、散気管10は上方に延在する配管11に
よりバルブ11aを介して酸素含有ガスとしての空気を
送り込むブロア12と接続されている。曝気室4内には
図示しない清掃筒も設けられている。
The anaerobic chamber 4 may be a sedimentation / separation chamber (rot chamber) in which a filter medium is not inserted or an anaerobic filter bed chamber in which a filter medium is inserted. Inflow port 7 through which sewage flows into the anaerobic chamber 4
A baffle 8 is fixed around the casing 1.
The aeration chamber 5 is filled with countless fluid carriers 9 in a volume of about 20 to 80% of the volume of the aeration chamber 5. These fluid carriers 9 are formed of polyethylene having a specific gravity of 0.93, and have an outer shape that does not trap air bubbles while securing a large surface area. The partition 2 at the bottom of the aeration chamber 5
On the side, a column-shaped air diffuser 10 is provided in parallel with and horizontal to the partition wall 2. It is connected. A cleaning cylinder (not shown) is also provided in the aeration chamber 4.

【0016】隔壁3の底部は幅方向全体に開放されてお
り、曝気室5と沈殿室6とは底部において連通されてい
る。そして、沈殿室6は、ケーシング1の下部後壁が前
方に傾斜した傾斜面1aとされているため、底部側に向
かうほど狭く形成されている。隔壁3の下端には、図2
及び図3に詳細を示すように、曝気室5と沈殿室6との
連通口を垂直方向で覆う分離部材13がブラケット14
により固定されている。この分離部材13は、図3に示
すように、上下に延在する複数本のガイド部13aと、
各ガイド部13aの上下端に固定された枠体13bとか
らなる。各ガイド部13aは、図4に示すように、軸直
角方向の断面形状が円形であり、図3に示すように、隣
り合うガイド部13aの間隔は各流動担体9の外径より
小さくされている。
The bottom of the partition 3 is open in the entire width direction, and the aeration chamber 5 and the sedimentation chamber 6 communicate with each other at the bottom. Since the lower rear wall of the casing 1 has an inclined surface 1a that is inclined forward, the sedimentation chamber 6 is formed narrower toward the bottom. At the lower end of the partition 3, FIG.
As shown in detail in FIG. 3, a separating member 13 that vertically covers a communication port between the aeration chamber 5 and the sedimentation chamber 6 is a bracket 14.
It is fixed by. As shown in FIG. 3, the separation member 13 includes a plurality of guide portions 13a extending vertically.
And a frame 13b fixed to the upper and lower ends of each guide portion 13a. As shown in FIG. 4, each of the guide portions 13a has a circular cross section in the direction perpendicular to the axis, and as shown in FIG. 3, the interval between the adjacent guide portions 13a is smaller than the outer diameter of each of the fluid carriers 9. I have.

【0017】図1に示すように、曝気室5内には、隔壁
3に対面して上下に移送管15が延在されており、移送
管15の途中には配管16が接続され、配管16はバル
ブ16aを介して酸素含有ガスとしての空気を送り込む
ブロア12と接続されている。図2〜4に示すように、
移送管15の一端は分離部材13の2本のガイド部13
a間で壁面1a側に突出するように屈曲され、その開口
15aは曝気室5における沈殿室6側の底部において壁
面1aに向かって開いている。他方、図1に示すよう
に、移送管5の他端は隔壁2を上方で跨いで延在してお
り、その開口15bは嫌気室4のバッフル8内に開いて
いる。
As shown in FIG. 1, a transfer pipe 15 extends vertically in the aeration chamber 5 so as to face the partition wall 3. Is connected to a blower 12 for feeding air as an oxygen-containing gas through a valve 16a. As shown in FIGS.
One end of the transfer pipe 15 is connected to two guide portions 13 of the separation member 13.
The opening 15a is opened toward the wall 1a at the bottom of the aeration chamber 5 on the side of the sedimentation chamber 6 between the openings a. On the other hand, as shown in FIG. 1, the other end of the transfer pipe 5 extends over the partition 2 upward, and the opening 15 b is open in the baffle 8 of the anaerobic chamber 4.

【0018】沈殿室6には浄化した水を流出する流入口
17が設けられている。以上のように構成された浄化槽
では、流入口7により汚水がまず嫌気室4に流入され
る。嫌気室4内では貯留した汚水を嫌気性バクテリアに
より浄化する。嫌気室4内の汚水は隔壁2に設けられた
図示しない連通口により曝気室5内に移動する。
The sedimentation chamber 6 is provided with an inlet 17 through which purified water flows out. In the septic tank configured as described above, sewage first flows into the anaerobic chamber 4 through the inflow port 7. In the anaerobic chamber 4, the stored wastewater is purified by anaerobic bacteria. The sewage in the anaerobic chamber 4 moves into the aeration chamber 5 through a communication port (not shown) provided in the partition 2.

【0019】そして、曝気室5内では、散気管10から
一定量の空気が連続的に供給されており、表面に好気性
バクテリアが担持された各流動担体9が散気管10から
供給される空気により汚水とともに上下に対流してい
る。このため、従来の接触曝気方式の曝気室を有する浄
化槽のような濾材の目詰まりによる浄化能力の低下を生
じることはない。むしろ、空気により好気性バクテリア
に安定して酸素を供給しつつ、好気性バクテリアと汚水
とが接触し易くなる。また、各流動担体9が互いに衝突
・干渉・当接して表面にくっついて繁殖した余分な固形
物を剥離させることができる。こうして汚水は、好気性
バクテリアによって汚れが分解されやすく、浄化能力が
高まる。また、逆洗管が不要になり、製造コスト及び維
持コストの低廉化を実現できる。
In the aeration chamber 5, a constant amount of air is continuously supplied from the air diffuser 10, and each fluid carrier 9 having aerobic bacteria carried on the surface thereof is supplied from the air diffuser 10. And convection up and down together with the sewage. For this reason, there is no decrease in the purification ability due to clogging of the filter medium as in a conventional septic tank having a contact aeration type aeration chamber. Rather, the aerobic bacteria and the sewage are more likely to come into contact with each other while supplying oxygen stably to the aerobic bacteria by air. In addition, each of the fluid carriers 9 collides, interferes, and abuts on each other, and sticks to the surface, so that extra solid matter that has propagated can be separated. In this way, the sewage is easily decomposed by the aerobic bacteria, and the purification ability is enhanced. In addition, a backwash tube is not required, and the manufacturing cost and the maintenance cost can be reduced.

【0020】そして、曝気室5にはある程度浄化された
処理水が貯留され、この処理水は下流側の沈殿室6内に
おいて未だ含有する固形物を沈殿する。沈殿室6内に残
留する固形物は、沈殿室6と曝気室5とが底部において
連通しているため、曝気室5において好気性バクテリア
による再度の汚れの分解を受けることとなる。この際、
この浄化槽にあっては、沈殿室6が壁面1aによって底
部側に向かうほど狭く形成されていることから、沈殿室
6内の固形物がその壁面1aに案内されて曝気室5側へ
移動しやすい。
The aerated chamber 5 stores treated water purified to some extent, and the treated water precipitates solids still contained in the settling chamber 6 on the downstream side. The solid matter remaining in the sedimentation chamber 6 is subjected to the decomposition of the dirt again by the aerobic bacteria in the aeration chamber 5 because the sedimentation chamber 6 and the aeration chamber 5 communicate with each other at the bottom. On this occasion,
In this septic tank, since the sedimentation chamber 6 is formed narrower toward the bottom by the wall surface 1a, the solid matter in the sedimentation chamber 6 is guided by the wall surface 1a and easily moves to the aeration chamber 5 side. .

【0021】特に、沈殿室6において、散気管10から
供給される空気で各流動担体9とともに対流する汚水に
より、沈殿室6内の底部の固形物が曝気室5に移送され
る。つまり、沈殿室6の底部側が曝気室5内を対流する
汚水で負圧になり、沈殿室6内の底部の固形物が曝気室
5に吸い込まれるように移送される(スロット効果)。
これにより沈殿室6内に残留する固形物が曝気室5にお
いて好気性バクテリアにより汚れの分解を受け易く、結
果的に満足できる汚水の浄化能力が安定して得られる。
In particular, in the sedimentation chamber 6, the solid matter at the bottom in the sedimentation chamber 6 is transferred to the aeration chamber 5 by sewage convection with each fluid carrier 9 by air supplied from the air diffuser 10. That is, the bottom side of the sedimentation chamber 6 becomes negative pressure due to the sewage convection in the aeration chamber 5, and the solid matter at the bottom in the sedimentation chamber 6 is transferred so as to be sucked into the aeration chamber 5 (slot effect).
As a result, the solid matter remaining in the sedimentation chamber 6 is easily susceptible to decomposition of dirt by the aerobic bacteria in the aeration chamber 5, and as a result, a satisfactory purification performance of sewage is stably obtained.

【0022】また、曝気室5と沈殿室6との間には分離
部材13が設けられ、この分離部材13が各流動担体9
の流出を阻止する。また、分離部材13のガイド部13
aは各流動担体9と小さな接触面積で当接して対流方向
に案内することから、各流動担体9は流出しようとして
分離部材13と衝突してもその対流が阻止されず、スロ
ット効果を効果的に生じることとなる。このため、沈殿
室6内に残留する固形物が曝気室5において好気性バク
テリアにより汚れの分解を受け易く、結果的に満足でき
る汚水の浄化能力が安定して得られる。
A separating member 13 is provided between the aeration chamber 5 and the sedimentation chamber 6, and the separating member 13
To prevent the outflow. Also, the guide portion 13 of the separation member 13
Since a is in contact with each of the fluid carriers 9 with a small contact area and is guided in the convection direction, even if each of the fluid carriers 9 collides with the separating member 13 to flow out, the convection is not prevented, and the slot effect is effectively prevented. Will occur. For this reason, the solid matter remaining in the sedimentation chamber 6 is easily susceptible to decomposition of dirt by the aerobic bacteria in the aeration chamber 5, and as a result, a satisfactory purification performance of sewage is stably obtained.

【0023】そして、ブロア12から供給された空気に
より発せられた水流を移送管15が取り込むことから、
曝気室5に残留する固形物はこの移送管15により上流
側の嫌気室4に移送される。この際、曝気室5における
沈殿室6側の底部において壁面1aに向かって移送管1
5の一端の開口15aが開いていることから、曝気室5
に移動する固形物は、好適にその開口15a内に取り込
まれ、好適に嫌気室4に移送されることとなる。また、
移送管15の一端の開口15aが分離部材13よりも壁
面1a側に突出しているため、分離部材13に阻害され
ずに沈殿室6内の固形物が開口15a内に取り込まれ、
好適に嫌気室4に移送される。これにより曝気室5内に
残留する固形物が嫌気室4において嫌気性バクテリアに
より汚れの分解を受け易く、結果的に満足できる汚水の
浄化能力が安定して得られる。
Since the transfer pipe 15 takes in the water flow generated by the air supplied from the blower 12,
The solid matter remaining in the aeration chamber 5 is transferred by the transfer pipe 15 to the anaerobic chamber 4 on the upstream side. At this time, at the bottom of the aeration chamber 5 on the sedimentation chamber 6 side, the transfer pipe 1 is moved toward the wall surface 1a.
Since the opening 15a at one end of the opening 5 is open,
Is preferably taken into the opening 15a and is preferably transferred to the anaerobic chamber 4. Also,
Since the opening 15a at one end of the transfer pipe 15 protrudes more toward the wall surface 1a than the separating member 13, solid matter in the sedimentation chamber 6 is taken into the opening 15a without being hindered by the separating member 13,
It is preferably transferred to the anaerobic chamber 4. As a result, the solid matter remaining in the aeration chamber 5 is liable to be decomposed by the anaerobic bacteria in the anaerobic chamber 4 and, as a result, a satisfactory sewage purification ability can be stably obtained.

【0024】そして、沈殿室6では、上澄みの水が所望
により消毒水の添加を受けて流出口17により排出され
ることとなる。固形物が曝気室5に残留する場合、清掃
筒に業者がホースを挿入し、ホースによりその固形物を
引き抜くこととなる。したがって、実施形態1の浄化槽
では、製造コスト及び維持コストの低廉化を実現しつ
つ、満足できる汚水の浄化能力を安定して発揮すること
ができる。また、分離部材13として、軸直角方向の断
面形状が一般的な円形のガイド部13aを採用している
ため、分離部材13の購入は容易であり、この点で浄化
槽の製造コストの低廉化を実現している。
In the sedimentation chamber 6, the supernatant water is discharged through the outlet 17 with the addition of disinfecting water as required. If the solids remain in the aeration chamber 5, a trader inserts a hose into the cleaning cylinder and pulls out the solids with the hose. Therefore, in the septic tank of the first embodiment, it is possible to stably exhibit satisfactory sewage purification ability while realizing low production costs and low maintenance costs. In addition, since the separation member 13 employs the guide portion 13a having a generally circular cross section in the direction perpendicular to the axis, it is easy to purchase the separation member 13, and in this regard, the production cost of the septic tank can be reduced. Has been realized.

【0025】なお、上記実施形態1の浄化槽では、嫌気
室4は1室であるが、第1の嫌気室と、この第1の嫌気
室の下流に位置する第2の嫌気室とで嫌気室4を構成す
ることもできる。 (実施形態2)実施形態2の浄化槽では、図5に示すよ
うに、移送管15の一端の開口15aが分離部材13か
ら突出していない。他の構成は実施形態1の浄化槽と同
一である。
In the septic tank of the first embodiment, the anaerobic chamber 4 is one, but the first anaerobic chamber and the second anaerobic chamber located downstream of the first anaerobic chamber are anaerobic chambers. 4 can also be configured. (Embodiment 2) In the septic tank of Embodiment 2, the opening 15a at one end of the transfer pipe 15 does not protrude from the separation member 13, as shown in FIG. Other configurations are the same as the septic tank of the first embodiment.

【0026】この浄化槽では、移送管15の一端の開口
15aが分離部材13より突出していないため、沈殿室
6内の固形物を開口15a内に取り込む際、それが分離
部材13にやや阻害されるものの、他の作用効果を実施
形態1の浄化槽と同様に奏することができる。 (実施形態3)実施形態3の浄化槽では、図6に示すよ
うに、分離部材13の下端が散気管10側に近接してお
り、曝気室5と沈殿室6との連通口を散気管10に向か
って下り勾配で覆っている。他の構成は実施形態1の浄
化槽と同一である。
In this septic tank, since the opening 15a at one end of the transfer pipe 15 does not protrude from the separating member 13, when the solid matter in the sedimentation chamber 6 is taken into the opening 15a, it is slightly obstructed by the separating member 13. However, other effects can be obtained in the same manner as the septic tank of the first embodiment. (Embodiment 3) In the septic tank according to Embodiment 3, as shown in FIG. 6, the lower end of the separation member 13 is close to the air diffuser 10 side, and the communication port between the aeration chamber 5 and the sedimentation chamber 6 is connected to the air diffuser 10. It is covered with a downward slope toward. Other configurations are the same as the septic tank of the first embodiment.

【0027】この浄化槽では、曝気室5の底部におい
て、沈殿室6側で沈んでくる各流動担体9が分離部材1
3に案内されて散気管10により再度浮上させられるこ
ととなり、各流動担体9の対流が規則的になるととも
に、スロット効果を生じ易い。他の作用効果は実施形態
1の浄化槽と同様である。 (実施形態4)実施形態4の浄化槽では、図7に示すよ
うに、移送管15の一端の開口15aが壁面1aと平行
である。他の構成は実施形態1、3の浄化槽と同一であ
る。
In this septic tank, at the bottom of the aeration chamber 5, each of the fluid carriers 9 sinking on the sedimentation chamber 6 side is separated from the separation member 1.
As a result, the convection of each fluid carrier 9 becomes regular, and the slot effect easily occurs. Other functions and effects are the same as those of the septic tank of the first embodiment. (Embodiment 4) In the septic tank of Embodiment 4, as shown in FIG. 7, an opening 15a at one end of the transfer pipe 15 is parallel to the wall surface 1a. Other configurations are the same as the septic tanks of the first and third embodiments.

【0028】この浄化槽では、沈殿室6内の固形物と曝
気室5内の固形物とをほぼ同程度開口15a内に取り込
みやすい。他の作用効果は実施形態1、3の浄化槽と同
様である。 (実施形態5)実施形態5の浄化槽では、図8に示すよ
うに、移送管15の一端を屈曲させることなく、その開
口15aを壁面1aと平行としている。他の構成は実施
形態1、3、4の浄化槽と同一である。
In this septic tank, the solid matter in the sedimentation chamber 6 and the solid matter in the aeration chamber 5 can be easily taken into the opening 15a to almost the same extent. Other functions and effects are the same as those of the septic tanks of the first and third embodiments. (Embodiment 5) In the septic tank of Embodiment 5, as shown in FIG. 8, the opening 15a of the transfer pipe 15 is parallel to the wall surface 1a without bending one end of the transfer pipe 15. Other configurations are the same as the septic tanks of the first, third, and fourth embodiments.

【0029】この浄化槽では、移送管15の成形が容易
であり、製造コストの低廉化を実現可能である。他の作
用効果は実施形態4の浄化槽と同様である。 (実施形態6)実施形態6の浄化槽では、図9及び図1
0に示すように、分離部材13として、ガイド部13a
と直交する補強部13cを有するものを採用している。
他の構成は実施形態1等の浄化槽と同一である。
In this septic tank, the transfer tube 15 can be easily formed, and the production cost can be reduced. Other functions and effects are the same as those of the septic tank of the fourth embodiment. (Embodiment 6) In the septic tank of Embodiment 6, FIGS.
As shown in FIG.
What has the reinforcement part 13c orthogonal to this is employ | adopted.
Other configurations are the same as those of the septic tank of the first embodiment and the like.

【0030】この浄化槽では、分離部材13を設けた後
から各流動担体9を充填する際、曝気室5内に各流動担
体9を充填した状態で出荷、搬送する際及び浄化槽の運
転時において、分離部材13が補強部13cを有してい
ることから、それらの際に生じる衝突力に確実に耐える
ことができる。他の作用効果は実施形態1等の浄化槽と
同様である。 (実施形態7)実施形態7の浄化槽では、図11に示す
ように、曝気室5側に突出していない補強部13dをも
つ分離部材13を採用している。他の構成は実施形態6
の浄化槽と同一である。
In this septic tank, when each of the fluid carriers 9 is filled after the separation member 13 is provided, when the aeration chamber 5 is shipped and transported with each of the fluid carriers 9 filled, and when the septic tank is operated, Since the separating member 13 has the reinforcing portion 13c, it can surely withstand a collision force generated at that time. Other functions and effects are the same as those of the septic tank of the first embodiment and the like. (Embodiment 7) In the septic tank of Embodiment 7, as shown in FIG. 11, a separation member 13 having a reinforcing portion 13d that does not project toward the aeration chamber 5 is employed. Another configuration is the sixth embodiment.
It is the same as the septic tank.

【0031】この浄化槽では、補強部13dが曝気室5
側に突出しておらず、各流動担体9を案内する際の抵抗
を小さくしている。他の作用効果は実施形態6の浄化槽
と同様である。 (実施形態8)実施形態8の浄化槽では、図12に示す
ように、ケーシング1が比較的容積の大きな沈殿室18
を有する場合、下方が沈殿室18側に屈曲した隔壁19
をそのケーシング1に固定し、これにより沈殿室18を
底部側に向かうほど狭く形成している。他の構成は実施
形態1の浄化槽と同一である。
In this septic tank, the reinforcing portion 13d is provided in the aeration chamber 5
It does not protrude to the side and reduces the resistance when guiding each fluid carrier 9. Other functions and effects are the same as those of the septic tank of the sixth embodiment. (Eighth Embodiment) In the septic tank of the eighth embodiment, as shown in FIG.
In the case of having a partition wall 19, the lower side is bent toward the settling chamber 18 side.
Is fixed to the casing 1 so that the sedimentation chamber 18 is formed narrower toward the bottom. Other configurations are the same as the septic tank of the first embodiment.

【0032】この浄化槽においても、実施形態1の浄化
槽と同様の作用効果を奏することができる。
In this septic tank, the same operation and effect as those of the septic tank of the first embodiment can be obtained.

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

【図1】実施形態1の合併浄化槽の縦模式断面図であ
る。
FIG. 1 is a vertical cross-sectional view of a combined septic tank according to a first embodiment.

【図2】実施形態1の合併浄化槽に係り、要部拡大図断
面図である。
FIG. 2 is an enlarged cross-sectional view of a main part of the combined septic tank according to the first embodiment.

【図3】実施形態1の合併浄化槽に係り、要部拡大背面
図である。
FIG. 3 is a main part enlarged rear view of the combined septic tank according to the first embodiment.

【図4】実施形態1の合併浄化槽に係り、分離部材等の
軸直角方向断面図である。
FIG. 4 is a cross-sectional view at right angles to an axis of a separation member and the like according to the combined septic tank of the first embodiment.

【図5】実施形態2の合併浄化槽に係り、要部拡大図断
面図である。
FIG. 5 is an enlarged cross-sectional view of a main part of the combined septic tank according to the second embodiment.

【図6】実施形態3の合併浄化槽に係り、要部拡大図断
面図である。
FIG. 6 is an enlarged cross-sectional view of a main part of the combined septic tank according to the third embodiment.

【図7】実施形態4の合併浄化槽に係り、要部拡大図断
面図である。
FIG. 7 is an enlarged cross-sectional view of a main part of a combined septic tank according to a fourth embodiment.

【図8】実施形態5の合併浄化槽に係り、要部拡大図断
面図である。
FIG. 8 is an enlarged cross-sectional view of a main part of a combined septic tank according to a fifth embodiment.

【図9】実施形態6の合併浄化槽に係り、要部拡大背面
図である。
FIG. 9 is an enlarged rear view of a relevant part of the combined septic tank according to the sixth embodiment.

【図10】実施形態6の合併浄化槽に係り、分離部材の
軸直角方向断面図である。
FIG. 10 is a cross-sectional view in the direction perpendicular to the axis of a separation member according to the combined septic tank of the sixth embodiment.

【図11】実施形態7の合併浄化槽に係り、分離部材の
軸直角方向断面図である。
FIG. 11 is a cross-sectional view in a direction perpendicular to an axis of a separating member according to the combined septic tank of the seventh embodiment.

【図12】実施形態8の合併浄化槽の縦模式断面図であ
る。
FIG. 12 is a schematic vertical sectional view of a combined septic tank according to an eighth embodiment.

【符号の説明】[Explanation of symbols]

4…嫌気室 2、3…隔壁 10…散気管 5…曝気室 6…沈殿室 15…移送管 15a…開口 9…流動担体 13…分離部材 13a…ガイド部 13c、13d…補強部 1a…壁面 DESCRIPTION OF SYMBOLS 4 ... Anaerobic chamber 2, 3 ... Partition wall 10 ... Aeration pipe 5 ... Aeration chamber 6 ... Sedimentation chamber 15 ... Transfer pipe 15a ... Opening 9 ... Fluid carrier 13 ... Separation member 13a ... Guide part 13c, 13d ... Reinforcement part 1a ... Wall surface

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】貯留した汚水中に酸素含有ガスを供給する
散気管が設けられ、該汚水を好気性バクテリアにより浄
化する曝気室と、底部が連通する隔壁により仕切られつ
つ該曝気室に隣接し、該汚水を沈殿により固形物と水と
に分離する沈殿室とを有する浄化槽において、 前記曝気室内には、表面に前記好気性バクテリアが担持
され、前記散気管から供給される前記酸素含有ガスによ
り前記汚水とともに上下に対流する無数の流動担体が充
填され、該曝気室と前記沈殿室との間には、各該流動担
体を対流方向に案内しつつ各該流動担体の流出を阻止す
る分離部材が設けられ、該沈殿室は、該散気管から供給
される該酸素含有ガスで各該流動担体とともに対流する
該汚水により、該沈殿室内の底部の固形物を該曝気室に
移送可能になされていることを特徴とする浄化槽。
An aeration tube for supplying oxygen-containing gas to stored sewage is provided, and an aeration chamber for purifying the sewage with aerobic bacteria and an aeration chamber adjacent to the aeration chamber while being separated by a partition having a bottom communicating therewith. A septic tank having a sedimentation chamber that separates the sewage into solids and water by sedimentation.In the aeration chamber, the surface of the aerobic bacteria is carried, and the oxygen-containing gas supplied from the air diffusion tube is used. Innumerable fluid carriers that convect up and down together with the sewage are filled, and a separation member between the aeration chamber and the sedimentation chamber that guides each fluid carrier in the convection direction and prevents the fluid carriers from flowing out. The sedimentation chamber is provided such that solids at the bottom of the sedimentation chamber can be transferred to the aeration chamber by the sewage convection with the respective fluid carriers with the oxygen-containing gas supplied from the aeration tube. Iko A septic tank characterized by the following.
【請求項2】分離部材は、各流動担体の対流方向に延在
し、各該流動担体と当接可能なガイド部を有するもので
あることを特徴とする請求項1記載の浄化槽。
2. The septic tank according to claim 1, wherein the separation member has a guide portion extending in a convection direction of each fluid carrier and capable of contacting each fluid carrier.
【請求項3】分離部材はガイド部と交差する補強部を有
することを特徴とする請求項2記載の浄化槽。
3. The septic tank according to claim 2, wherein the separating member has a reinforcing portion intersecting with the guide portion.
【請求項4】ガイド部は軸直角方向の断面形状が円形で
あることを特徴とする請求項2又は3記載の浄化槽。
4. The septic tank according to claim 2, wherein the guide has a circular cross section in a direction perpendicular to the axis.
【請求項5】分離部材は、散気管に向かって下り勾配と
なるように傾斜又は湾曲されていることを特徴とする請
求項1、2、3又は4記載の浄化槽。
5. The septic tank according to claim 1, wherein the separation member is inclined or curved so as to have a downward slope toward the air diffuser.
JP13325399A 1999-05-13 1999-05-13 Septic tank Pending JP2000317481A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP13325399A JP2000317481A (en) 1999-05-13 1999-05-13 Septic tank

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP13325399A JP2000317481A (en) 1999-05-13 1999-05-13 Septic tank

Publications (1)

Publication Number Publication Date
JP2000317481A true JP2000317481A (en) 2000-11-21

Family

ID=15100298

Family Applications (1)

Application Number Title Priority Date Filing Date
JP13325399A Pending JP2000317481A (en) 1999-05-13 1999-05-13 Septic tank

Country Status (1)

Country Link
JP (1) JP2000317481A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005185892A (en) * 2003-12-24 2005-07-14 Fuji Clean Kogyo Kk Sewage treatment device
CN105585125A (en) * 2016-03-09 2016-05-18 李林 Structure integration biological membrane reactor
JP2020179380A (en) * 2019-04-26 2020-11-05 株式会社ハウステック Aerobic rocking filter bed tank, septic tank equipped with the same, and method for operating the same

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005185892A (en) * 2003-12-24 2005-07-14 Fuji Clean Kogyo Kk Sewage treatment device
JP4554194B2 (en) * 2003-12-24 2010-09-29 フジクリーン工業株式会社 Sewage treatment equipment
CN105585125A (en) * 2016-03-09 2016-05-18 李林 Structure integration biological membrane reactor
JP2020179380A (en) * 2019-04-26 2020-11-05 株式会社ハウステック Aerobic rocking filter bed tank, septic tank equipped with the same, and method for operating the same
JP7416567B2 (en) 2019-04-26 2024-01-17 株式会社ハウステック Aerobic rocking filter tank, septic tank equipped with the same, and method of operating an aerobic rocking filter tank

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