JP4381557B2 - Merger processing equipment - Google Patents

Merger processing equipment Download PDF

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Publication number
JP4381557B2
JP4381557B2 JP2000102870A JP2000102870A JP4381557B2 JP 4381557 B2 JP4381557 B2 JP 4381557B2 JP 2000102870 A JP2000102870 A JP 2000102870A JP 2000102870 A JP2000102870 A JP 2000102870A JP 4381557 B2 JP4381557 B2 JP 4381557B2
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treatment
septic tank
tank
treated water
chamber
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JP2001239289A (en
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正記 伊達
淳 日比野
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Housetec Inc
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Housetec Inc
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Description

【0001】
【発明の属する技術分野】
本発明は、合併処理化装置に関する。
【0002】
【従来の技術】
屎尿の浄化処理は、単独処理浄化槽を用いて行っている。
【0003】
図4は、従来の分離接触曝気方式の単独処理浄化槽を示す縦断側面図である。この単独処理浄化槽1は、屎尿を流入口2から沈殿分離室3へ流入させて固液分離および嫌気処理を行い、接触曝気室4へ移流する。接触曝気室4は、移流した処理水を散気管7から散気した空気の泡によって撹拌して接触材8に接触させ、栄養基質を酸化させて徐々に除去する。接触材8は、撹拌を継続すると生物膜が厚く堆積して閉塞するので、定期的に逆洗管9から空気泡を吐出することにより接触材8から生物膜を剥離させる。接触曝気室4を通過した処理水は、沈殿室5にて固形分の沈殿分離を行い、上澄み液を消毒槽6へ移流させて滅菌処理して流出口10から放流する。なお、11は消毒剤容器である。
【0004】
【発明が解決しようとする課題】
この単独処理浄化槽は、処理すべき汚水の種類が屎尿に限定され、台所排水,洗濯排水,洗面排水および浴槽排水などの生活排水を処理することができないという問題がある。
【0005】
この問題は、既設の単独処理浄化槽を撤去して新たな合併処理浄化槽を設置することにより解決することができるが、施工費用が高額となるばかりでなく、多くの単独処理浄化槽がFRP製であることから、不要になった単独処理浄化槽の処分に関しても新たな問題が発生する。
【0006】
また、単独処理浄化槽を掘り起こすことなく埋め殺すようにすれば廃棄物処分の問題は生じないものの土地の有効活用ができなくなる問題がある。
【0007】
本発明の目的は、既設の単独処理浄化槽を有効活用して合併処理浄化槽を実現させることができる合併処理化装置を提案することにある。
【0008】
【課題を解決するための手段】
本発明は、嫌気処理室と接触曝気室と沈殿室と消毒槽とを備えた屎尿専用の既設の単独処理浄化槽に配管接続することにより、屎尿に加えて、台所排水、洗濯排水、洗面排水などの汚水を合併処理することができる合併処理浄化槽を構成する合併処理化装置において、好気処理を行うための生物反応部と、この生物反応部の下流側で処理水の濾過を行うための濾過部とを備え、単独処理浄化槽との配管接続は、前記既設の単独処理浄化槽の消毒槽に流入する直前の処理水を前記生物反応部へ移流させる移流管と、濾過部を洗浄した処理水を前記既設の単独処理浄化槽の嫌気処理部または沈殿分離室へ移送する返送管により行ない、前記汚水の内、台所排水(ディスポーザ排水を含む)、洗濯排水、洗面排水については前記既設の単独浄化槽の流入口から流入させ、前記既存の単独浄化槽及び前記合併処理化装置を通過させて合併処理し、浴槽排水については前記既設の単独処理浄化槽及び前記合併処理浄化装置を通過することなく系外に放出するように構成してなることを特徴とする。
【0009】
前記生物反応部の上流側に流量調整槽を備え、単独処理浄化槽からの処理水をこの流量調整槽を介して生物反応部へ流入させるようにしたことを特徴とする。
【0010】
【発明の実施の形態】
本発明の合併処理化装置を接続して合併処理浄化槽を構成する単独処理浄化槽は、少なくとも、嫌気処理室または沈殿分離室と、消毒室を備えたものであることが必要であり、具体的には、従来の技術で説明したように、流入口および流出口を備え、内部に上流側から沈殿分離室,接触曝気室,沈殿室,消毒槽を備えたものが好適である。
【0011】
本発明の合併処理化装置は、少なくとも、好気処理を行うための生物反応部と処理水の濾過を行う濾過部を備えたものであれば良い。
【0012】
生物反応部および濾過部についてより具体的に述べると、一例としては、槽内に担体を充填して担体層を形成し、その担体槽の下部および内部に散気管を設け、担体層の内部に設置した散気管より上側の担体層により主として好気処理を行い、担体層の内部に設置した散気管より下側の担体層により主として濾過を行うように構成する。また、他の例としては、通水板により区画した上下2段の担体層を形成すると共に各担体層の下部に散気管を設置し、通水するときに上流側となる担体層を生物反応部となし、下流側の担体層を濾過部とするように構成する。
【0013】
生物反応部に用いる担体は、微生物を多く保持可能にすることから、網様円筒状,骨格様球状,へちま状,小円筒状,波板状,チューブ状,繊維絡み状などの合成樹脂製の成形体、独立気泡体または連通気泡体を有する合成樹脂製の成形体、アンスラサイト(無煙炭),珪砂,セラミックなどの無機体を好適に用いることかできる。
【0014】
濾過部に使用する担体(濾材)は、生物反応部と同様に担体を使用したものを好適に使用することができる。使用する担体としては、生物反応部で使用したものと同じ形態でも異なる形態でも良い。濾過部の底部に配置する散気管は、通常状態では空気泡の吐出を行うことなく、担体が静止状態を保って濾過が行い易い環境を維持させるが、継続して濾過を行うことによって担体に厚く堆積した生物膜を剥離するために、定期的に空気泡を吐出させて該担体の撹拌を行って担体から生物膜を剥離する。剥離した生物膜は、洗浄排水移送管によって、単独処理浄化槽の嫌気処理室または沈殿分離室へ移送するようにすることが好ましい。
【0015】
移流管は、単独処理浄化槽から生物反応部へ処理水を移流させるものであり、単独処理浄化槽からの処理水は、消毒室に流入する直前の処理水とする。具体的には、単独処理浄化槽の接触曝気室または沈殿室から処理水を抜き取り、生物反応部へと移流させることが好ましい。また、生物反応部の上流側に流量調整槽を設ける場合は、単独処理浄化槽からの処理水を一旦流量調整槽へ移流させてから生物反応部へ移流するようにする。
【0016】
排水洗浄移送管は、合併処理化装置の濾過部を洗浄した処理水を単独処理浄化槽の嫌気処理部または沈殿分離室へ移送するものであり、主として、濾過部の担体から剥離した生物膜を多く含む処理水を移送する。
【0017】
返送管は、濾過部の下流側の汚水を単独処理浄化槽の消毒室に返送するものであり、返送された処理水は、滅菌処理を行って系外へ放流される。
【0018】
合併処理化装置は、生物反応部の上流に流量調整槽を備え、合併処理化装置に流入する処理水を一旦流量調整槽に溜め、そこから生物反応部へ流入させても良く、これにより、安定した浄化処理を行うことができる。
【0019】
第1の実施の形態
図1は、合併処理化装置を単独処理浄化槽に配管接続して構成した合併処理浄化槽であり、(a)は平面図、(b)は縦断側面図である。
【0020】
単独処理浄化槽1は、既設の単独処理浄化槽であり、上流側から、第1流入口2,嫌気処理室(沈殿分離室)3,接触曝気室4,沈殿室5,消毒槽6,第1流出口10を備える。
【0021】
合併処理化装置20は、第2流入口21から処理水を流入させる生物濾過槽22を備え、この生物濾過槽22は、槽の上下に担体の通過を妨げ、処理水を通過させる通水部材23,24,25を設置し、通水部材23,24間に担体を充填して形成した上側の担体層によって生物反応部26を構成し、通水部材24,25間に担体を重点して形成した下側の担体層によって濾過部27を構成する。生物反応部26の下部に設けた散気部材28は、好気処理を行うために使用するものであり、常に空気泡の吐出を行うようにするが、濾過部27の下部に設けた散気部材29は、生物膜の剥離を行う洗浄のために使用するものであり、1日1回の空気泡の吐出を1〜30分程度行うようにする。
【0022】
この濾過部27の下流側には、処理水貯留部30を設け、この処理水貯留部30には第2流出口31を設け、底部に洗浄排水移送管32を開口させる。
【0023】
単独処理浄化槽1と合併処理化装置20の配管接続は、沈殿室5と第2流入口21を移流管33によって接続し、単独処理浄化槽1の沈殿室5の処理水を合併処理化装置20の生物濾過槽22に移流する。また、第2流出口31と消毒室6を返送管34によって接続し、処理水貯留部30の上澄み液を消毒室6に移流する。そして、洗浄排水引き抜き管32は、移送ポンプ35と洗浄排水移送管36を介して嫌気処理室3に接続する。
【0024】
ここで、汚水(処理水)の流れについて説明する。家庭から排出される屎尿,台所排水(ディスポーザ排水を含む),洗面排水,洗濯排水および浴槽排水等(以下、排水aという)は、単独処理浄化槽1の第1流入口2から嫌気処理室2へ流入する。嫌気処理室2は、処理水の固液分離および嫌気処理を行って接触曝気室4に移流する。接触曝気室4は、処理水の栄養基質を酸化して除去して沈殿室5に移流する。沈殿室5は、処理水の固形分を沈殿させて分離し、上澄み液を移流管33によって合併処理化装置20の第2流入口21から生物濾過槽22内に移流する。
【0025】
合併処理化装置20の生物濾過槽22は、流入した処理水を、先ず、生物反応部26において散気部材28からの空気泡によって好気処理し、その後、濾過部27において生物反応部26からの持込み酸素により好気処理を行いながら固形物質の除去を行い、処理水貯留部30に移流する。
【0026】
処理水貯留部30内の処理水の上澄み液は、返送管34によって消毒室6へ移流し、ここで消毒滅菌処理した後に第1流出口10から放流する。
【0027】
合併処理化装置20の濾過部27は、継続して濾過を行うと、担体に生物膜が厚く堆積して閉塞するので、散気部材29から定期的に空気泡を吐出させて担体を撹拌することにより、担体から生物膜の剥離を行う。そして、剥離した生物膜は、移送ポンプ35を稼働させて洗浄排水引き抜き管32によって引き抜いて洗浄排水移送管36を介して嫌気処理室3に移送する。
【0028】
このような合併処理浄化槽によれば、単独処理浄化槽1を有効に利用して屎尿,台所排水,洗面排水,洗濯排水等を合併処理することができる。
【0029】
第2の実施の形態
図2は、本発明の第2の実施の形態における合併処理浄化槽の縦断側面および配管を示す図である。この実施の形態は、図1に示した第1の実施の形態の合併処理浄化槽における合併処理化装置20に流量調整槽40を一体的に設け、この流量調整槽40内の処理水をポンプ41により生物濾過槽22に移流するようにした構成である。その他の構成は、第1の実施の形態と同様であるので、同一符号を付して重複する説明を省略する。
【0030】
浴槽排水は、数分間に約200〜300リットルという大量の排水量になる。そのために、合併処理化装置20の生物濾過槽22の容量を十分に大きく確保することができない場合には、処理が不十分な処理水を放流してしまうことになりかねない。
【0031】
そこで、この実施の形態は、汚れの少ない浴槽排水は排水aとは別に排水するように浴槽排水管42で配管し、移流管33の途中で合流させて流量調整槽40に流入させて貯留し、この流量調整槽40からポンプ41を使用して適量の処理水を生物濾過槽22へ移流させるように構成した。
【0032】
このような合併処理浄化槽によれば、単独処理浄化槽1における屎尿,台所排水,洗面排水,洗濯排水の処理機能を低下させることなく安定した浄化処理を行うことができる。
【0033】
第3の実施の形態
図3は、本発明の第3の実施の形態における合併処理浄化槽の縦断側面および配管を示す図である。この実施の形態は、図2に示した第2の実施の形態の合併処理浄化槽における合併処理化装置に設けた流量調整槽を別体に形成した構成である。その他の構成は、第2の実視の形態と同様であるので、同一符号を付して重複する説明を省略する。
【0034】
この実施の形態では、流量調整槽40は、合併処理化装置20とは別体に形成して地中に埋設するように構成し、第3流入口43に移流管33を接続して処理水を流入させる。そして、この流量調整槽40内に貯留する処理水をポンプ41により移送管44を介して合併処理化装置20の第2流入口21に移流するように配管接続する。
【0035】
このような合併処理浄化槽によれば、合併処理化装置20は地上に設置することが可能となって施工費用を低減することができる。
【0036】
その他の実施の形態
このような合併処理浄化槽は、浄化槽を新設するときには、新しい単独処理浄化槽を単独で新設し、またはこの新しい既存の単独処理浄化槽と合併処理化装置を組み合わせて使用することにより合併処理浄化槽を構成して新設することができるので、単独処理浄化槽と合併処理浄化槽の生産効率を高めることができる。
【0037】
【発明の効果】
本発明は、既設の単独処理浄化槽を利用して合併処理浄化槽を構成することができるので、既設の単独処理浄化槽を処分して新たな合併処理浄化槽を設置するよりも安価に実現することができ、単独処理浄化槽を廃棄する必要もなくなる。
【0038】
また、単独処理浄化槽の消毒室を利用することにより、合併処理化装置の構成を簡単にすることができる。
【0039】
また、浴槽排水配管を別配管にすることにより、他の生活排水に比較して量が多いために浄化処理を不安定にしていた浴槽排水を直接または合併処理化装置による処理のみまたは消毒滅菌のみを行って系外に放流することができ、浄化処理を安定に行うことができる。
【0040】
更に、浴槽排水が既設の単独処理浄化槽を通過せずに、直接系外に放出するように構成すれば、既設の単独処理浄化槽の容量を大きくしなくても汚泥の流出を防止することができると共に生物濾過処理を効率的に行うことができるので、生物濾過槽の容量をコンパクトにすることができ、システム全体を小型化することが可能となる。
【0041】
更に、合併処理化装置に流量調整槽を設けた場合には、安定した浄化処理を行うことができ、特に合併処理化装置と流量調整槽を別体にして配管接続するようにすれば、合併処理化装置を地上設置することにより施工費用を低減することができる。
【0042】
また、本発明は、新しい単独処理浄化槽と合併処理化装置を使用して合併処理浄化槽を新設することもできるので、単独処理浄化槽と合併処理浄化槽の生産効率を高めることができる。
【図面の簡単な説明】
【図1】本発明の第1の実施の形態を示す合併処理化装置を単独処理浄化槽に配管接続して構成した合併処理浄化槽であり、(a)は平面図、(b)は縦断側面図である。
【図2】本発明の第2の実施の形態における合併処理浄化槽の縦断側面および配管を示す図である。
【図3】本発明の第3の実施の形態における合併処理浄化槽の縦断側面および配管を示す図である。
【図4】従来の分離接触曝気方式の単独処理浄化槽を示す縦断側面図である。
【符号の説明】
1…単独処理浄化槽、3…嫌気処理室、4…接触曝気室、5…沈殿室、6…消毒槽、20…合併処理化装置、22…生物濾過槽、26…生物反応部、27…濾過部。
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a merger processing apparatus.
[0002]
[Prior art]
The purification process of manure is performed using a single treatment septic tank.
[0003]
FIG. 4 is a longitudinal sectional side view showing a single processing septic tank of a conventional separation contact aeration method. In the single treatment septic tank 1, manure is allowed to flow from the inlet 2 into the precipitation separation chamber 3 to perform solid-liquid separation and anaerobic treatment, and then transferred to the contact aeration chamber 4. In the contact aeration chamber 4, the treated water agitated is agitated by the bubbles of air diffused from the diffuser tube 7 and brought into contact with the contact material 8, and the nutrient substrate is oxidized and gradually removed. If the contact material 8 is continuously stirred, the biofilm accumulates thickly and closes. Therefore, the biofilm is peeled from the contact material 8 by periodically discharging air bubbles from the backwash tube 9. The treated water that has passed through the contact aeration chamber 4 is subjected to precipitation separation of solids in the sedimentation chamber 5, sterilized by transferring the supernatant liquid to the disinfection tank 6, and discharged from the outlet 10. In addition, 11 is a disinfectant container.
[0004]
[Problems to be solved by the invention]
In this single treatment septic tank, the type of sewage to be treated is limited to manure, and there is a problem that domestic wastewater such as kitchen wastewater, laundry wastewater, bathroom wastewater and bathtub wastewater cannot be treated.
[0005]
This problem can be solved by removing the existing single processing septic tank and installing a new merged processing septic tank, but not only the construction cost is high, but many single processing septic tanks are made of FRP. Therefore, a new problem also arises regarding the disposal of the single processing septic tank that has become unnecessary.
[0006]
Moreover, if the single treatment septic tank is buried without being dug up, there is a problem that the land cannot be effectively used although the problem of waste disposal does not occur.
[0007]
An object of the present invention is to propose a merger processing apparatus capable of effectively utilizing an existing single processing septic tank and realizing a merged processing septic tank.
[0008]
[Means for Solving the Problems]
In addition to human waste, kitchen wastewater, laundry wastewater, bathroom drainage, etc. in addition to human waste by piping connection to an existing single treatment septic tank dedicated to human waste, which includes an anaerobic treatment chamber, a contact aeration chamber, a sedimentation chamber, and a disinfection tank In a merger treatment apparatus that constitutes a merger treatment septic tank capable of performing merger treatment of wastewater, a biological reaction part for performing an aerobic treatment, and a filtration for filtering treated water downstream of the biological reaction part And a pipe connection with the single treatment septic tank, the advection pipe for advancing the treated water immediately before flowing into the sterilization tank of the existing single treatment septic tank, and the treated water having washed the filtration part performed by return pipe to transfer to the anaerobic treatment section or precipitation separation chamber of said existing single processing septic tank, among the wastewater (including disposer waste water) kitchen waste water, washing waste water, for wash drainage alone septic tank of the existing Allowed to flow from the inlet, the existing single septic tank and passed through the merger processing apparatus merged treated, the tub wastewater is discharged out of the system without passing through a single processing septic tank and the combined treatment purifier of the existing It is characterized by comprising as follows.
[0009]
A flow rate adjustment tank is provided on the upstream side of the biological reaction unit, and treated water from the single treatment septic tank is allowed to flow into the biological reaction unit via the flow rate adjustment tank.
[0010]
DETAILED DESCRIPTION OF THE INVENTION
The single treatment septic tank that constitutes the merger treatment septic tank by connecting the merger treatment apparatus of the present invention is required to have at least an anaerobic treatment chamber or a sedimentation separation chamber, and a disinfection chamber. As described in the prior art, it is preferable to have an inlet and an outlet, and a precipitation separation chamber, a contact aeration chamber, a precipitation chamber, and a disinfection tank from the upstream side.
[0011]
The merger processing apparatus of this invention should just be provided with the filtration part which filters the biological reaction part for performing an aerobic process, and treated water at least.
[0012]
More specifically, the biological reaction section and the filtration section are described. As an example, a tank is filled with a carrier to form a carrier layer, and a diffuser pipe is provided at the bottom and inside of the carrier tank. The aerobic treatment is mainly performed by the carrier layer above the installed diffuser tube, and the filtration is mainly performed by the carrier layer below the diffuser tube installed inside the carrier layer. As another example, an upper and lower two-stage carrier layer partitioned by a water flow plate is formed, and an aeration tube is installed at the lower part of each carrier layer. The downstream carrier layer is configured as a filtration part.
[0013]
Since the carrier used in the biological reaction part can hold many microorganisms, it is made of synthetic resin such as a net-like cylindrical shape, a skeleton-like spherical shape, a square shape, a small cylindrical shape, a corrugated plate shape, a tube shape, or a fiber entangled shape. An inorganic body such as a molded body, a molded body made of a synthetic resin having closed cells or open cells, anthracite (anthracite), silica sand, and ceramic can be preferably used.
[0014]
As the carrier (filter medium) used in the filtration part, a carrier using a carrier can be suitably used as in the biological reaction part. The carrier to be used may be the same form as that used in the biological reaction part or a different form. The air diffuser arranged at the bottom of the filtration unit does not discharge air bubbles in the normal state, and maintains an environment in which the carrier can be easily filtered while maintaining a stationary state. In order to peel the biofilm deposited thickly, air bubbles are discharged periodically and the carrier is stirred to peel the biofilm from the carrier. The peeled biofilm is preferably transferred to the anaerobic treatment chamber or the precipitation separation chamber of the single treatment septic tank by a washing drainage transfer pipe.
[0015]
The advection pipe transfers the treated water from the single treatment septic tank to the biological reaction section, and the treated water from the single treatment septic tank is treated water immediately before flowing into the disinfection chamber. Specifically, it is preferable to remove the treated water from the contact aeration chamber or settling chamber of the single treatment septic tank and transfer it to the biological reaction section. When a flow rate adjustment tank is provided upstream of the biological reaction unit, the treated water from the single treatment purification tank is once transferred to the flow rate adjustment tank and then transferred to the biological reaction unit.
[0016]
The drainage washing transfer pipe is used to transfer the treated water that has washed the filtration unit of the combined treatment apparatus to the anaerobic treatment unit or the sedimentation separation chamber of the single treatment septic tank. Transfer the treated water.
[0017]
The return pipe returns sewage downstream of the filtration unit to the disinfection chamber of the single treatment septic tank, and the returned treated water is sterilized and discharged outside the system.
[0018]
The merger treatment apparatus may be provided with a flow rate adjustment tank upstream of the biological reaction unit, and the treated water flowing into the merger treatment unit may be temporarily stored in the flow rate adjustment tank and then flowed into the biological reaction unit from this, A stable purification process can be performed.
[0019]
First Embodiment FIGS. 1A and 1B are merged treatment septic tanks constructed by connecting a merger treatment apparatus to a single process septic tank, wherein FIG. 1A is a plan view and FIG. 1B is a longitudinal side view.
[0020]
The single processing septic tank 1 is an existing single processing septic tank. From the upstream side, the first inlet 2, the anaerobic processing chamber (precipitation separation chamber) 3, the contact aeration chamber 4, the precipitation chamber 5, the disinfection tank 6, and the first flow An outlet 10 is provided.
[0021]
The combined treatment apparatus 20 includes a biological filtration tank 22 that allows treated water to flow in from the second inlet 21, and this biological filtration tank 22 prevents water from passing through the top and bottom of the tank and allows the treated water to pass therethrough. 23, 24, 25 are installed, and the biological reaction part 26 is constituted by the upper carrier layer formed by filling the carrier between the water-permeable members 23, 24. The carrier is emphasized between the water-permeable members 24, 25. The lower support layer thus formed constitutes the filtration unit 27. The air diffuser 28 provided at the lower part of the biological reaction unit 26 is used for performing the aerobic treatment and always discharges air bubbles. However, the air diffuser provided at the lower part of the filter unit 27 is used. The member 29 is used for cleaning to remove the biofilm, and discharges air bubbles once a day for about 1 to 30 minutes.
[0022]
A treated water storage unit 30 is provided on the downstream side of the filtration unit 27, a second outlet 31 is provided in the treated water storage unit 30, and a cleaning drainage transfer pipe 32 is opened at the bottom.
[0023]
The pipe connection between the single treatment septic tank 1 and the merger treatment apparatus 20 is that the sedimentation chamber 5 and the second inlet 21 are connected by the advection pipe 33, and the treated water in the precipitation chamber 5 of the single treatment septic tank 1 is connected to the merge treatment apparatus 20. Transfer to the biological filtration tank 22. Further, the second outlet 31 and the sterilization chamber 6 are connected by the return pipe 34, and the supernatant liquid of the treated water storage unit 30 is transferred to the sterilization chamber 6. The cleaning / drainage extraction pipe 32 is connected to the anaerobic treatment chamber 3 via a transfer pump 35 and a cleaning / drainage transfer pipe 36.
[0024]
Here, the flow of sewage (treated water) will be described. For manure, kitchen wastewater (including disposer wastewater), bathroom wastewater, laundry wastewater and bathtub wastewater (hereinafter referred to as wastewater a) discharged from the home to the anaerobic treatment chamber 2 from the first inlet 2 of the single treatment septic tank 1 Inflow. The anaerobic treatment chamber 2 performs solid-liquid separation and anaerobic treatment of the treated water and moves to the contact aeration chamber 4. The contact aeration chamber 4 oxidizes and removes the nutrient substrate of the treated water and transfers it to the precipitation chamber 5. The sedimentation chamber 5 precipitates and separates the solid content of the treated water, and the supernatant is transferred from the second inlet 21 of the combined treatment apparatus 20 into the biological filtration tank 22 through the transfer pipe 33.
[0025]
The biological filtration tank 22 of the merger processing apparatus 20 first aerobically treats the treated water that has flowed in with the air bubbles from the air diffuser 28 in the biological reaction unit 26, and then the biological reaction unit 26 in the filtration unit 27. The solid substance is removed while performing an aerobic treatment with the oxygen brought in, and then advected to the treated water storage unit 30.
[0026]
The supernatant of the treated water in the treated water storage unit 30 is transferred to the sterilization chamber 6 through the return pipe 34 and is discharged from the first outlet 10 after sterilization treatment.
[0027]
When the filtration unit 27 of the merger processing apparatus 20 continuously performs filtration, the biofilm accumulates thickly on the carrier and closes, so that air bubbles are periodically discharged from the air diffuser 29 to stir the carrier. As a result, the biofilm is peeled off from the carrier. Then, the peeled biofilm is pulled out by the cleaning drainage pipe 32 by operating the transfer pump 35 and transferred to the anaerobic treatment chamber 3 through the cleaning drainage transfer pipe 36.
[0028]
According to such a merger treatment septic tank, the single treatment septic tank 1 can be effectively used to perform merger treatment of manure, kitchen drainage, wash drainage, laundry drainage, and the like.
[0029]
Second Embodiment FIG. 2 is a view showing a longitudinal side surface and piping of a merged treatment septic tank according to a second embodiment of the present invention. In this embodiment, a flow rate adjusting tank 40 is integrally provided in the merger processing apparatus 20 in the merged processing septic tank of the first embodiment shown in FIG. 1, and treated water in the flow rate adjusting tank 40 is pumped 41. Therefore, the advection to the biological filtration tank 22 is performed. Since other configurations are the same as those of the first embodiment, the same reference numerals are given and redundant description is omitted.
[0030]
The bathtub drainage becomes a large amount of drainage of about 200 to 300 liters in several minutes. For this reason, if the capacity of the biological filtration tank 22 of the combined treatment apparatus 20 cannot be secured sufficiently large, treated water that is insufficiently processed may be discharged.
[0031]
Therefore, in this embodiment, the bathtub drainage with little dirt is piped by the bathtub drainage pipe 42 so as to be drained separately from the drainage a, and merged in the middle of the advection pipe 33 to flow into the flow rate adjusting tank 40 and stored. A proper amount of treated water was transferred from the flow rate adjustment tank 40 to the biological filtration tank 22 using a pump 41.
[0032]
According to such a combined treatment septic tank, stable purification treatment can be performed without deteriorating the treatment functions of manure, kitchen wastewater, wash effluent, and laundry wastewater in the single treatment septic tank 1.
[0033]
Third Embodiment FIG. 3 is a view showing a longitudinal side surface and piping of a merged treatment septic tank according to a third embodiment of the present invention. In this embodiment, the flow rate adjusting tank provided in the merger processing apparatus in the merged processing septic tank of the second embodiment shown in FIG. 2 is formed separately. Other configurations are the same as those in the second embodiment, and thus the same reference numerals are given and duplicate descriptions are omitted.
[0034]
In this embodiment, the flow rate adjusting tank 40 is formed separately from the merger processing apparatus 20 and is embedded in the ground, and the advection pipe 33 is connected to the third inlet 43 to treat the treated water. Inflow. Then, a pipe connection is made so that the treated water stored in the flow rate adjusting tank 40 is transferred by the pump 41 via the transfer pipe 44 to the second inlet 21 of the merger processing apparatus 20.
[0035]
According to such a merger treatment septic tank, the merger treatment apparatus 20 can be installed on the ground, and construction costs can be reduced.
[0036]
Other Embodiments When a septic tank is newly established, such a merged septic tank can be merged by installing a new single septic tank alone or by combining this new existing septic tank with a combined processing unit. Since a processing septic tank can be constructed and newly installed, the production efficiency of the single processing septic tank and the merged processing septic tank can be increased.
[0037]
【The invention's effect】
Since the present invention can configure the merged treatment septic tank using the existing single treatment septic tank, it can be realized at a lower cost than disposing the existing single treatment septic tank and installing a new merged treatment septic tank. In addition, it is not necessary to discard the single treatment septic tank.
[0038]
Moreover, the structure of a merger processing apparatus can be simplified by utilizing the disinfection chamber of a single processing septic tank.
[0039]
In addition, by using a separate bathtub drainage pipe, the wastewater from the bathtub, which has been destabilized due to its large volume compared to other domestic wastewater, can be treated directly or by disinfection sterilization only directly or by a combined treatment device. Can be discharged out of the system, and the purification treatment can be performed stably.
[0040]
Furthermore, if the bathtub drainage is configured to be discharged directly out of the system without passing through the existing single treatment septic tank, sludge can be prevented from flowing out without increasing the capacity of the existing single treatment septic tank. At the same time, since the biological filtration treatment can be performed efficiently, the capacity of the biological filtration tank can be made compact, and the entire system can be miniaturized.
[0041]
Furthermore, when the flow control tank is provided in the merger processing apparatus, stable purification treatment can be performed. In particular, if the merger processing apparatus and the flow control tank are separated and connected by piping, the merger Construction cost can be reduced by installing the processing equipment on the ground.
[0042]
Moreover, since this invention can also newly establish a merged process septic tank using a new single process septic tank and a merger processing apparatus, the production efficiency of a single process septic tank and a merged process septic tank can be improved.
[Brief description of the drawings]
BRIEF DESCRIPTION OF DRAWINGS FIG. 1 is a merged treatment septic tank constructed by connecting a merger treatment apparatus showing a first embodiment of the present invention to a single treatment septic tank, wherein (a) is a plan view and (b) is a longitudinal side view. It is.
FIG. 2 is a view showing a longitudinal side surface and piping of a merged treatment septic tank according to a second embodiment of the present invention.
FIG. 3 is a view showing a longitudinal side surface and piping of a merged treatment septic tank according to a third embodiment of the present invention.
FIG. 4 is a vertical side view showing a conventional single-treatment septic tank using a separation contact aeration method.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 ... Single processing septic tank, 3 ... Anaerobic processing chamber, 4 ... Contact aeration chamber, 5 ... Precipitation chamber, 6 ... Disinfection tank, 20 ... Combined treatment apparatus, 22 ... Biofiltration tank, 26 ... Biological reaction part, 27 ... Filtration Department.

Claims (2)

嫌気処理室と接触曝気室と沈殿室と消毒槽とを備えた屎尿専用の既設の単独処理浄化槽に配管接続することにより、屎尿に加えて、台所排水、洗濯排水、洗面排水などの汚水を合併処理することができる合併処理浄化槽を構成する合併処理化装置において、好気処理を行うための生物反応部と、この生物反応部の下流側で処理水の濾過を行うための濾過部とを備え、単独処理浄化槽との配管接続は、前記既設の単独処理浄化槽の消毒槽に流入する直前の処理水を前記生物反応部へ移流させる移流管と、濾過部を洗浄した処理水を前記既設の単独処理浄化槽の嫌気処理部または沈殿分離室へ移送する返送管により行ない、前記汚水の内、台所排水(ディスポーザ排水を含む)、洗濯排水、洗面排水については前記既設の単独浄化槽の流入口から流入させ、前記既存の単独浄化槽及び前記合併処理化装置を通過させて合併処理し、浴槽排水については前記既設の単独処理浄化槽及び前記合併処理浄化装置を通過することなく系外に放出するように構成してなることを特徴とする合併処理化装置。In addition to manure, sewage such as kitchen wastewater, laundry wastewater, and wash drainage is merged by connecting to an existing single treatment septic tank dedicated to human waste with an anaerobic treatment chamber, contact aeration chamber, sedimentation chamber, and disinfection tank In a merger treatment apparatus that constitutes a merged treatment septic tank that can be treated, it comprises a biological reaction part for performing aerobic treatment, and a filtration part for filtering treated water downstream of the biological reaction part. In addition, the pipe connection with the single treatment septic tank is a transfer pipe for advancing the treated water immediately before flowing into the sterilization tank of the existing single treatment septic tank to the biological reaction unit, and the treated water that has washed the filtration unit is used as the existing single unit. performed by return pipe to transfer to the anaerobic treatment section or precipitation separation chamber of the processing septic tank, of the sewerage (including disposer waste water) kitchen waste water, washing waste water, from the inlet of a single septic tank of the existing for wash wastewater ON Toe, the existing single septic tank and by passing the combined treatment apparatus and combined treatment, the bath drainage to discharge out of the system without passing through a single processing septic tank and the combined treatment purifier of the existing A merger processing apparatus characterized by comprising. 請求項1において、前記生物反応部の上流側に流量調整槽を備え、単独処理浄化層からの処理水をこの流量調整槽を介して生物反応部へ流入させるようにしたことを特徴とする合併処理化装置。The merger according to claim 1, wherein a flow rate adjusting tank is provided upstream of the biological reaction unit, and treated water from the single treatment purification layer is allowed to flow into the biological reaction unit through the flow rate adjusting tank. Processing equipment.
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Publication number Priority date Publication date Assignee Title
JP2008279446A (en) * 2008-07-07 2008-11-20 Hitachi Housetec Co Ltd Combination treatment septic tank

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CN100340502C (en) * 2004-12-27 2007-10-03 中国科学院成都生物研究所 Processing plant for regenerating and using sewage
CN102020401B (en) * 2010-12-23 2012-07-04 成都大学 An anti-impact load livestock farm sewage treatment device and treatment method thereof

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008279446A (en) * 2008-07-07 2008-11-20 Hitachi Housetec Co Ltd Combination treatment septic tank

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