JP2001179272A - Combined treatment device - Google Patents

Combined treatment device

Info

Publication number
JP2001179272A
JP2001179272A JP36952899A JP36952899A JP2001179272A JP 2001179272 A JP2001179272 A JP 2001179272A JP 36952899 A JP36952899 A JP 36952899A JP 36952899 A JP36952899 A JP 36952899A JP 2001179272 A JP2001179272 A JP 2001179272A
Authority
JP
Japan
Prior art keywords
septic tank
biological reaction
wastewater
treatment
treatment septic
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.)
Granted
Application number
JP36952899A
Other languages
Japanese (ja)
Other versions
JP4119994B2 (en
Inventor
Atsushi Hibino
淳 日比野
Masaki Date
正記 伊達
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.)
Showa Denko Materials Co Ltd
Original Assignee
Hitachi Chemical Co Ltd
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 Hitachi Chemical Co Ltd filed Critical Hitachi Chemical Co Ltd
Priority to JP36952899A priority Critical patent/JP4119994B2/en
Publication of JP2001179272A publication Critical patent/JP2001179272A/en
Application granted granted Critical
Publication of JP4119994B2 publication Critical patent/JP4119994B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Treatment Of Biological Wastes In General (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a combined treatment septic tank, which can solve a disposal problem of an existing individual treatment septic tank and treat domestic miscellaneous wastewater at a cost lower than a cost required for newly purchasing a combined treatment septic tank by effectively utilizing the individual treatment septic tank. SOLUTION: A combined treatment device has a biological reaction part for carrying out aerobic treatment and a filtration part for filtering the drain on the downstream side of the biological reaction part. Piping connection to the individual treatment septic tank comprises a transfer pipe that makes the drain just before flowing into a sterilizing chamber of the individual treatment septic tank flow into the biological reaction part, a waste washing water transfer pipe that transfers washing water after washing the filtration part to an anaerobic treatment part or a sedimentation separation chamber of the individual treatment septic tank, and a return pipe that returns the waste water of the downstream side of the filtration part to the sterilizing chamber of the individual treatment septic tank. Bath drain piping for making a drain of a bath tub flow into the biological reaction part is mounted to the biological reaction part or the transfer pipe.

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、合併処理化装置に
関する。
The present invention relates to a merge processing apparatus.

【0002】[0002]

【従来の技術】従来から、屎尿の浄化を行う装置として
は、単独処理浄化槽を用いている。図5は、分離接触ば
っ気方式の単独処理浄化槽を示す概略断面図である。屎
尿は、流入口2から沈殿分離室3へと流入し、固液分離
及び嫌気処理が行われ、接触ばっ気室4へと移流する。
接触ばっ気室4内では、移流した水が散気管7から散気
される空気の泡により攪拌されて接触材8に接触し、栄
養基質の酸化除去が徐々に行われる。接触材8は、攪拌
を継続していると生物膜が厚く堆積し閉塞するので、定
期的に逆洗管9より空気泡を吐出することで生物膜を剥
離させる。接触ばっ気室4を通過した水は、沈殿室5に
て固形分の沈殿分離を行ってから、分離した上澄み液を
消毒室6へと移流させ、滅菌処理を施した後に流出口1
0より放流される。
2. Description of the Related Art Conventionally, a single treatment septic tank has been used as an apparatus for purifying human waste. FIG. 5 is a schematic cross-sectional view showing a separate contact aeration type single treatment septic tank. Human waste flows into the sedimentation separation chamber 3 from the inflow port 2, is subjected to solid-liquid separation and anaerobic treatment, and is transferred to the contact aeration chamber 4.
In the contact aeration chamber 4, the transferred water is agitated by the bubbles of air diffused from the diffuser tube 7 and comes into contact with the contact material 8, whereby the nutrient substrate is gradually oxidized and removed. If the contact material 8 is continuously stirred, the biofilm is thickly deposited and clogged. Therefore, the biofilm is peeled off by periodically discharging air bubbles from the backwash tube 9. After the water that has passed through the contact aeration chamber 4 is subjected to sedimentation and separation of solids in the sedimentation chamber 5, the separated supernatant liquid is transferred to the disinfection chamber 6, sterilized, and subjected to the outlet 1.
Released from 0.

【0003】[0003]

【発明が解決しようとする課題】しかしながら、単独処
理浄化槽は、処理すべき水の種類が屎尿に限定され、台
所排水、洗濯排水、洗面排水及び浴槽排水等の生活雑排
水を処理できないとの課題を有している。このような問
題は、既設の単独処理浄化槽を撤去して新たに合併処理
浄化槽を設置することで解決できるが、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、不要となった単独処理浄化槽の処分に
関しても新たな問題を発生させる。また、単独処理浄化
槽を掘り起こすことなく、埋め殺す場合には、処分に関
する問題が発生しないものの、土地の有効活用ができな
いとの別の問題を発生させる。
However, the single treatment septic tank has a problem that the type of water to be treated is limited to human waste, and it is not possible to treat household wastewater such as kitchen wastewater, laundry wastewater, washbasin wastewater and bathtub wastewater. have. This problem can be solved by removing the existing single treatment septic tank and installing a new merged treatment septic tank. However, not only is the construction cost high, but also many single treatment septic tanks are made of FRP. Therefore, a new problem arises with respect to disposal of the single treatment septic tank that is no longer required. In addition, when burying a single treatment septic tank without excavating it, there is no problem with disposal, but another problem arises that land cannot be used effectively.

【0004】本発明は、上記のような課題に鑑みてなさ
れたものであり、既設の単独処理浄化槽を有効利用する
ことで、単独処理浄化槽の処分問題を解決すると共に、
新たに合併処理浄化槽を購入するよりも安価に生活雑排
水を処理可能な合併処理化装置を提供することを目的と
する。
[0004] The present invention has been made in view of the above problems, and solves the disposal problem of the single treatment septic tank by effectively utilizing the existing single treatment septic tank.
It is an object of the present invention to provide a merger treatment system capable of treating household wastewater at a lower cost than purchasing a merger treatment septic tank.

【0005】[0005]

【課題を解決するための手段】本発明は、次のものに関
する。 (1)単独処理浄化槽に配管接続することにより、排水
の合併処理を可能とする合併処理化装置において、その
合併処理化装置が、好気処理を行うための生物反応部
と、その生物反応部の下流側にて排水の濾過を行うため
の濾過部とを有し、単独処理浄化槽との配管接続が、単
独処理浄化槽の消毒室に流入する直前の排水を上記生物
反応部へと流入させる移流管と、上記濾過部を洗浄した
排水を単独処理浄化槽の嫌気処理部又は沈殿分離室へと
移送する洗浄排水移送管と、上記濾過部の下流側の排水
を単独処理浄化槽の消毒室に返送する返送管とによりな
され、浴槽からの排水を上記生物反応部へと流入させる
浴槽排水配管が、上記生物反応部又は移流管に設けられ
た合併処理化装置。 (2)浴槽排水配管が、流量調整弁を備えている上記
(2)に記載の合併処理化装置。 (3)生物反応部が、その上流側に流量調整槽を有し、
単独処理浄化槽及び浴槽からの排水が上記流量調整槽を
介して生物反応部へと流入する上記(1)又は(2)に
記載される合併処理化装置。
The present invention relates to the following. (1) In a merged treatment device that enables a merged treatment of wastewater by connecting a pipe to a single treatment septic tank, the merged treatment device includes a biological reaction section for performing aerobic treatment, and a biological reaction section thereof. A filtration unit for filtering wastewater on the downstream side of the process, and a pipe connection to the single treatment septic tank, the advection to flow the wastewater immediately before flowing into the disinfection chamber of the single treatment septic tank into the biological reaction unit A pipe, a washing drainage transfer pipe for transferring the wastewater from which the filtration section has been washed to the anaerobic treatment section or the sedimentation separation chamber of the single treatment septic tank, and returning the wastewater downstream of the filtration section to the disinfection chamber of the single treatment septic tank. A merging treatment device, wherein a bathtub drainage pipe is provided in the biological reaction section or the advection pipe, which is formed by a return pipe and allows drainage from the bathtub to flow into the biological reaction section. (2) The merging treatment device according to (2), wherein the bathtub drainage pipe is provided with a flow control valve. (3) The biological reaction section has a flow control tank on its upstream side,
The combined treatment apparatus according to (1) or (2), wherein the wastewater from the single treatment septic tank and the bathtub flows into the biological reaction section via the flow rate adjusting tank.

【0006】[0006]

【発明の実施の形態】本発明の合併処理化装置を配管接
続する単独処理浄化槽は、少なくとも嫌気処理部又は沈
殿分離室と、消毒室とを有するものであれば特に限定さ
れるものではなく、具体的には、従来技術にて説明した
ように、流入口及び流出口を有し、内部に上流側から沈
殿分離室、接触ばっ気室、沈殿室、消毒室を設けたもの
を好適に用いることができる。
BEST MODE FOR CARRYING OUT THE INVENTION The single treatment septic tank to which the combined treatment apparatus of the present invention is connected by piping is not particularly limited as long as it has at least an anaerobic treatment section or a sedimentation separation chamber and a disinfection chamber. Specifically, as described in the related art, a device having an inflow port and an outflow port, and provided with a sedimentation separation chamber, a contact aeration chamber, a sedimentation chamber, and a disinfection chamber from the upstream side is preferably used. be able to.

【0007】本発明に用いる合併処理化装置は、少なく
とも好気処理を行う生物反応部と排水の濾過を行う濾過
部とを有するものであれば特に限定されるものではな
い。生物反応部及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、その担体層の下部及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て主に好気
処理を行い、担体層の内部に設置した散気管より下側の
担体層にて主に濾過を行うことができる。また、別の例
としては、通水板により区画した上下2段の担体層を形
成すると共に各々の担体層の下部に散気管を設置し、水
を通水する際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ことができる。
[0007] The combined treatment apparatus used in the present invention is not particularly limited as long as it has at least a biological reaction section for performing aerobic treatment and a filtration section for filtering wastewater. To describe the biological reaction section and the filtration section more specifically, as an example, a carrier is filled in a tank to form a carrier layer, and a diffuser is provided below and inside the carrier layer. Aerobic treatment can be performed mainly in the carrier layer above the installed diffuser, and filtration can be mainly performed in the carrier layer below the diffuser installed inside the carrier layer. Further, as another example, an upper and lower carrier layer separated by a water flow plate is formed, and an air diffuser is provided below each carrier layer, so that the carrier layer which is on the upstream side when water flows is provided. As a biological reaction section, and the carrier layer on the downstream side can be used as a filtration section.

【0008】生物反応部に用いる担体は、微生物を多く
保持可能であることから、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、繊維絡み状等
の合成樹脂製の成形体、独立気泡体又は連通気泡体を有
した合成樹脂製の成形体、アンスラサイト(無煙炭)、
珪砂、セラミック等の無機体を好適に用いることができ
る。
[0008] Since the carrier used in the bioreaction section can hold a large amount of microorganisms, it can be synthesized in the form of a net-like cylinder, a skeleton-like sphere, a streak, a small cylinder, a corrugated plate, a tube, a fiber entanglement, or the like. Molded articles made of resin, molded articles made of synthetic resin having closed cells or communicating cells, anthracite (anthracite),
An inorganic substance such as silica sand or ceramic can be suitably used.

【0009】濾過部に用いる担体(濾材)は、生物反応
部に用いた担体と同様の担体を好適に使用することがで
きるが、異なるものでもよい。濾過を行う部分の底部に
配置した散気管は、通常状態で継続的に空気泡の吐出を
行うことがなく、担体が静止状態を保ち濾過の行いやす
い環境を維持させるが、継続して濾過を行っていると担
体に生物膜が厚く堆積するので、定期的に空気泡を吐出
させて担体の攪拌を行い、担体から生物膜の剥離を行
う。担体の洗浄により剥離させた生物膜は、単独処理浄
化槽の嫌気処理部又は沈殿分離室へと、洗浄排水移送管
により移送させることが好ましい。
As the carrier (filter medium) used in the filtration section, the same carrier as the carrier used in the biological reaction section can be suitably used, but may be different. The air diffuser arranged at the bottom of the part to be filtered does not continuously discharge air bubbles in the normal state, and the carrier keeps the stationary state and maintains an environment that facilitates filtration. Since the biofilm is deposited thickly on the carrier when it is performed, the carrier is agitated by periodically discharging air bubbles, and the biofilm is separated from the carrier. The biofilm separated by washing the carrier is preferably transferred to an anaerobic treatment section or a sedimentation separation chamber of a single treatment septic tank by a washing drainage transfer pipe.

【0010】本発明に用いる移流管は、単独処理浄化槽
から生物反応部へと排水を移流させるものであり、単独
処理浄化槽からの排水は、消毒室に流入する直前の排水
とする。具体的には、単独処理浄化槽の接触ばっき室又
は沈殿室から排水を抜き取り、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
整槽を設ける場合には、単独処理浄化槽からの排水を一
旦流量調整槽へ移流させてから生物反応部へと移流させ
るようにする。
[0010] The advection tube used in the present invention transfers wastewater from the single treatment septic tank to the biological reaction section, and the wastewater from the single treatment septic tank is the wastewater immediately before flowing into the disinfection room. Specifically, it is preferable to drain the wastewater from the contacting chamber or sedimentation chamber of the single treatment septic tank, and to transfer the wastewater to the biological reaction section. When a flow control tank is provided on the upstream side of the biological reaction section, the wastewater from the single treatment / purification tank is once transferred to the flow control tank and then to the biological reaction section.

【0011】本発明に用いる洗浄排水移送管は、合併処
理化装置の濾過部を洗浄した排水を単独処理浄化槽の嫌
気処理部又は沈殿分離室へと移送させるものであり、主
には、濾過部の担体から剥離させた生物膜を多く含む排
水の移送をする。
The washing and drainage transfer pipe used in the present invention transfers wastewater from the filtration section of the combined treatment apparatus to the anaerobic treatment section or the sedimentation separation chamber of the single treatment / purification tank. The wastewater containing a large amount of biofilm separated from the carrier is transferred.

【0012】本発明に用いる返送管は、濾過部の下流側
の排水を、単独処理浄化槽の消毒室に返送するものであ
り、返送された排水は、滅菌処理を行われて系外へと放
流される。
The return pipe used in the present invention returns wastewater downstream of the filtration section to the disinfection chamber of the single treatment septic tank, and the returned wastewater is subjected to a sterilization treatment and discharged to the outside of the system. Is done.

【0013】本発明に用いる浴槽排水配管は、浴槽及び
浴室からの排水を生物反応部へと流入させるものであ
り、浴槽及び浴室の排水を直接生物反応部へと流入させ
ても、一旦流量調整槽へ流入させてから生物反応部へと
流入させるようにしてもよい。また、浴槽排水配管に通
す排水は、少なくとも浴槽及び浴室の排水を含むもので
あり、浴槽排水以外に、汚れの程度が低い洗濯排水を流
してもよい。
The bathtub drainage pipe used in the present invention is for draining the wastewater from the bathtub and the bathroom into the biological reaction section. Even if the wastewater from the bathtub and the bathroom flows directly into the biological reaction section, the flow rate is once adjusted. You may make it flow into a biological reaction part after flowing into a tank. Further, the wastewater passing through the bathtub drainage pipe includes at least the wastewater from the bathtub and the bathroom, and in addition to the bathtub drainage, washing wastewater with a low degree of dirt may flow.

【0014】浴槽排水配管には、流量調整弁を設けるこ
とが好ましく、このようにすることで、一時に大量に発
生する浴槽及び浴室の排水を徐々に生物反応部へと流入
させ、安定した処理を行えるようになる。また、流量調
整弁を設ける代わりに、生物反応部の上流に流量調整槽
を設け、合併処理化装置へと流入する排水を一旦流量調
整槽に溜め、そこから生物反応部へと流入させるように
することも、安定した排水処理を行え好ましい。
[0014] It is preferable to provide a flow control valve in the bathtub drainage pipe. In this way, a large amount of wastewater from the bathtub and the bathroom generated at a time is gradually flown into the biological reaction section, and stable treatment is performed. Can be performed. Also, instead of providing a flow control valve, a flow control tank is provided upstream of the biological reaction section, and the wastewater flowing into the combined treatment device is temporarily stored in the flow control tank, and then flows into the biological reaction section. It is also preferable to perform stable wastewater treatment.

【0015】[0015]

【実施例】以下図面を用いて、本発明の実施例を説明す
る。図1は、本発明の実施例を示す、合併処理化装置を
単独処理浄化槽に配管接続したものであり、(a)は概
略平面図を示し、(b)は概略側断面図を示す。単独処
理浄化槽1は、既設のものであり、その内部構造は、上
流側から第1流入口11、嫌気処理室22、接触ばっ気
室4、沈殿室29、消毒室16、第1流出口12を設け
ている。そして、上記単独処理浄化槽1を用いて合併処
理可能とするには、新たに本発明の合併処理化装置15
を設置する。
Embodiments of the present invention will be described below with reference to the drawings. FIG. 1 shows an embodiment of the present invention, in which a combined treatment apparatus is connected to a single treatment septic tank by piping. (A) shows a schematic plan view, and (b) shows a schematic sectional side view. The single treatment septic tank 1 is an existing one, and its internal structure includes a first inflow port 11, an anaerobic treatment chamber 22, a contact aeration chamber 4, a sedimentation chamber 29, a disinfection chamber 16, a first outflow port 12 from the upstream side. Is provided. Then, in order to be able to carry out the merger treatment using the single treatment septic tank 1, the merger treatment apparatus 15 of the present invention is newly added.
Is installed.

【0016】合併処理化装置15は、その内部に生物濾
過槽17を有し、その生物濾過槽17は、槽の上下に担
体の通過を妨げ排水を通過させる通水部材30、31、
32の設置を行い、上記通水部材30、31間及び通水
部材31、32間に担体を充填し、上側の担体層を生物
反応部18となし、下側の担体層を濾過部19としてい
る。生物反応部18及び濾過部19の下部には、散気部
材20、21が設けられている。生物反応部18の下部
に設けられた散気部材20は、好気処理を行うために使
用されるものであり、常時空気泡の吐出を行っている
が、濾過部19の下部に設けられた散気部材21は、生
物膜の剥離を行う洗浄の際に使用されるもので、1日1
回の空気泡の吐出を1〜30分程度行う。また、濾過部
19の下流側には、処理水貯留部34を設けている。
The combined treatment apparatus 15 has a biological filtration tank 17 inside thereof, and the biological filtration tank 17 has water passing members 30, 31, which prevent the carrier from passing above and below the tank and allow the waste water to pass through.
The carrier is filled between the water-permeable members 30 and 31 and between the water-permeable members 31 and 32, the upper carrier layer is formed as the biological reaction section 18, and the lower carrier layer is formed as the filtration section 19. I have. Air diffusion members 20 and 21 are provided below the biological reaction unit 18 and the filtration unit 19. The air diffusing member 20 provided at the lower part of the biological reaction part 18 is used for performing aerobic treatment and constantly discharges air bubbles, but is provided at the lower part of the filtering part 19. The air diffusing member 21 is used at the time of cleaning for removing the biofilm, and is used once a day.
The air bubbles are discharged for about 1 to 30 minutes. Further, a treated water storage unit 34 is provided downstream of the filtration unit 19.

【0017】単独処理浄化槽1と合併処理化装置15と
の配管接続は、沈殿室29と第2流入口13とを移流管
37により接続することで行われ、上記移流管37は、
排水を単独処理浄化槽1から合併処理化装置15へと移
流させる以外に、浴槽排水配管26を用いることで、浴
槽及び浴室の排水を合併処理化装置15へと移流させ
る。また、第2流出口と消毒室16とは、返送管38に
より配管接続され、処理水貯留部34から消毒室16へ
と排水を返送する。
The pipe connection between the single treatment septic tank 1 and the combined treatment apparatus 15 is performed by connecting the sedimentation chamber 29 and the second inflow port 13 with an advection pipe 37.
In addition to diverting the wastewater from the single treatment septic tank 1 to the merger treatment device 15, the drainage of the bathtub and the bathroom is diverted to the merger treatment device 15 by using the bathtub drainage pipe 26. In addition, the second outlet and the disinfection chamber 16 are connected by a return pipe 38 so as to return wastewater from the treated water storage section 34 to the disinfection chamber 16.

【0018】水の流れについて説明すると、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)、
洗面排水及び洗濯排水(以下まとめて排水aと言う)
は、第1流入口11から嫌気処理室22へと流入して固
液分離及び嫌気処理を行われ、接触ばっ気室4にて栄養
基質の酸化除去が行われる。接触ばっ気室4を通過した
排水aは、沈殿室29内で固形分の沈殿分離を行われ、
第1流出口12を介して移流管37へと流入する。
The flow of water will be described. Human waste discharged from home, kitchen wastewater (including disposer wastewater),
Wash drainage and laundry drainage (hereinafter collectively referred to as drainage a)
Flows into the anaerobic treatment chamber 22 from the first inlet 11 to be subjected to solid-liquid separation and anaerobic treatment, and the oxidative removal of nutrient substrates is performed in the contact aeration chamber 4. The waste water a that has passed through the contact aeration chamber 4 is subjected to sedimentation separation of solids in the sedimentation chamber 29,
It flows into the advection tube 37 via the first outlet 12.

【0019】移流管37では、浴槽排水配管26から流
入する浴槽及び浴室の排水(以下排水bという)と排水
aとが合流して、第2流入口13より合併処理化装置1
5へと移流する。排水a、bは、生物反応部18にて散
気部材20からの空気泡の吐出による好気処理がなさ
れ、その後濾過部19にて生物反応部18からの持込み
酸素で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34へと移流する。排水a、bは、処理水
貯留部34から返送管38を介して消毒室16へと流入
し、滅菌処理を行われた後に第1流出口12から放流さ
れる。
In the advection pipe 37, the drainage from the bathtub and the bathroom (hereinafter referred to as drainage b) flowing from the bathtub drainage pipe 26 and the drainage a merge, and the merged treatment apparatus 1 is supplied through the second inlet 13.
Advancing to 5 The wastewaters a and b are subjected to aerobic treatment by discharging air bubbles from the diffusing member 20 in the biological reaction unit 18, and then performing aerobic treatment with oxygen brought in from the biological reaction unit 18 in the filtration unit 19. , Remove solid matter,
It flows to the treated water storage unit 34. The wastewaters a and b flow into the disinfection chamber 16 from the treated water storage section 34 via the return pipe 38, and are discharged from the first outlet 12 after being subjected to the sterilization processing.

【0020】濾過部19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、定期的に散気
部材21から空気泡を吐出させて担体の攪拌を行い、担
体から生物膜を剥離させる。剥離された生物膜は、移送
ポンプ23を稼働させることで、洗浄排水移送管24よ
り引き抜き、嫌気処理室22へと返送する。
If filtration is continued, the filtration section 19 will thicken the biofilm on the carrier and close it, so that air bubbles are periodically discharged from the air diffusing member 21 to stir the carrier, The biofilm is stripped from the By operating the transfer pump 23, the separated biofilm is pulled out from the washing drainage transfer pipe 24 and returned to the anaerobic treatment chamber 22.

【0021】図2は、図1に示す浴槽排水配管に流量調
整弁を設けた合併処理化装置の概略平面図を示す。排水
bは、浴槽及び浴室の排水であるために、数分間に約2
00〜300lという大量の排水を発生させる。そのた
め、生物濾過槽17の容量を十分に大きく確保していな
い場合には、処理の行われない排水をそのまま放流する
ことになりかねない。そのため、生物濾過槽17の容量
を十分に確保できない場合には、浴槽排水配管26に流
量調整弁27を設けることで、少量づつ排水bを生物濾
過槽17へと流入させ、安定した処理を行うようにす
る。
FIG. 2 is a schematic plan view of a combined treatment apparatus in which a flow control valve is provided in the bathtub drainage pipe shown in FIG. The drainage b is about 2 minutes in a few minutes because it is bathtub and bathroom drainage.
Generates a large amount of wastewater of 00 to 300 l. Therefore, if the capacity of the biological filtration tank 17 is not sufficiently large, the wastewater that is not treated may be discharged as it is. Therefore, when the capacity of the biological filtration tank 17 cannot be sufficiently ensured, the drainage b is flowed into the biological filtration tank 17 little by little by providing a flow control valve 27 in the bathtub drain pipe 26 to perform a stable treatment. To do.

【0022】図3は、本発明の合併処理化装置に、流量
調整槽を設けた場合の概略側断面図を示す。本実施例で
は、排水a、bを一旦流量調整槽28に流入させ、そこ
からポンプ35を用いて生物濾過槽17へと移流させて
いる。上記流量調整槽28を用いる場合には、図2に示
すような流量調整弁27を用いずに安定した処理を行う
ことができる。
FIG. 3 is a schematic sectional side view showing a case where a flow rate adjusting tank is provided in the combined processing apparatus of the present invention. In the present embodiment, the drainage waters a and b are once flowed into the flow control tank 28, and are then transferred to the biological filtration tank 17 using the pump 35. When the flow rate adjusting tank 28 is used, stable processing can be performed without using the flow rate adjusting valve 27 as shown in FIG.

【0023】図4は、合併処理化装置と流量調整槽とを
一体化せずに配管接続した合併処理化装置の概略側断面
図を示す。このような構成であれば、地中に埋設するの
は流量調整槽36だけで済み、合併処理化装置15は地
上設置することが可能となる。
FIG. 4 is a schematic cross-sectional side view of the merged processing apparatus in which the merged processing apparatus and the flow rate control tank are connected to each other without being integrated. With such a configuration, only the flow rate adjusting tank 36 needs to be buried in the ground, and the merger processing apparatus 15 can be installed on the ground.

【0024】[0024]

【発明の効果】本発明は、既設の単独処理浄化槽を利用
することにより合併処理を可能としたので、単独処理浄
化槽を処分して新たに合併処理浄化槽を設置するより
も、安価に合併処理を行うことが可能であり、単独処理
浄化槽を処分する必要もなくなる。また、浴槽排水配管
に流量調整弁を設けた場合には、生物反応部及び濾過部
の容量を大きくする必要がなくなり、合併処理化装置全
体を小型化することが可能となる。更に、合併処理化装
置に流量調整槽を設けた場合には、安定した排水処理を
行うことができ、特に合併処理化装置と流量調整槽とを
一体化せずに配管接続するのであれば、合併処理化装置
を地上設置することで施工費用を低く抑えることが可能
となる。
According to the present invention, the merger treatment can be performed by using the existing single treatment septic tank, so that the merger treatment can be performed at a lower cost than disposing the single treatment septic tank and newly installing the merger treatment septic tank. It is possible to do so, and there is no need to dispose of a single treatment septic tank. In addition, when the flow rate control valve is provided in the bathtub drainage pipe, it is not necessary to increase the capacities of the biological reaction section and the filtration section, and it is possible to reduce the size of the combined processing apparatus. Furthermore, in the case where the flow control tank is provided in the merged processing device, stable drainage treatment can be performed, especially if the piping is connected without integrating the merged processing device and the flow control tank. The installation cost can be kept low by installing the merged processing equipment on the ground.

【0025】本発明は、単独処理浄化槽を通過した排水
を単純に合併処理化装置へと流入させ、合併処理を行っ
ているのではなく、単独処理浄化槽の消毒室に流入する
直前の排水を合併処理化装置へと流入させ、その後、上
記消毒室へと返送するので、合併処理化装置に消毒室を
設けることなく、既存の単独処理浄化槽に付設する消毒
室を活用することが可能であり、部材点数を低減し且つ
資源の有効活用を行える。
According to the present invention, the wastewater that has passed through the single treatment septic tank is simply flowed into the merger and the wastewater immediately before flowing into the disinfection chamber of the single treatment septic tank is not merged. Since it flows into the treatment device and then returns to the disinfection chamber, it is possible to utilize the disinfection room attached to the existing single treatment septic tank without providing a disinfection room in the combined treatment device. The number of members can be reduced and resources can be effectively used.

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

【図1】本発明の実施例を示す、合併処理化装置であ
り、(a)は概略平面図を示し、(b)は概略側断面図
を示す。
BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a merge processing apparatus showing an embodiment of the present invention, wherein (a) shows a schematic plan view and (b) shows a schematic side sectional view.

【図2】図1に示す浴槽排水配管に流量調整弁を設けた
合併処理化装置の概略平面図を示す。
FIG. 2 is a schematic plan view of a combined treatment apparatus in which a flow control valve is provided in a bathtub drainage pipe shown in FIG.

【図3】合併処理化装置に、流量調整槽を設けた概略側
断面図を示す。
FIG. 3 is a schematic side cross-sectional view in which a flow control tank is provided in the combined processing apparatus.

【図4】合併処理化装置と流量調整槽とを一体化せずに
配管接続した概略側断面図を示す。
FIG. 4 is a schematic cross-sectional side view in which the merging treatment apparatus and the flow rate adjusting tank are connected to each other without being integrated.

【図5】従来例を示す、分離接触ばっ気方式の単独処理
浄化槽の概略断面図。
FIG. 5 is a schematic cross-sectional view of a separate contact aeration type single treatment septic tank showing a conventional example.

【符号の説明】[Explanation of symbols]

1.単独処理浄化槽 2.流入口 3.沈殿分離室 4.接触ばっ
気室 5.沈殿室 6.消毒室 7.散気管 8.接触材 9.逆洗管 10.流出口 11.第1流入口 12.第1流
出口 13.第2流入口 14.第2流
出口 15.合併処理化装置 16.消毒室 17.生物濾過槽 18.生物反
応部 19.濾過部 20.散気部
材 21.散気部材 22.嫌気処
理室 23.移送ポンプ 24.洗浄排
水移送管 26.浴槽排水配管 27.流量調
整弁 28.流量調整槽 29.沈殿室 30.通水部材 31.通水部
材 32.通水部材 34.処理水
貯留部 35.ポンプ 36.流量調
整槽 37.移流管 38.返送管
1. Separate treatment septic tank 2. Inlet 3. Sedimentation separation chamber 4. 4. Contact aeration chamber Settling chamber 6. Disinfection room 7. 7. diffuser tube Contact material 9. Backwash tube 10. Outlet 11. First inlet 12. First outlet 13. Second inlet 14. Second outlet 15. Merger processing device 16. Disinfection room 17. Biological filtration tank 18. Biological reaction section 19. Filtration unit 20. Diffuser member 21. Diffuser member 22. Anaerobic treatment chamber 23. Transfer pump 24. Cleaning drainage transfer pipe 26. Bathtub drainage piping 27. Flow control valve 28. Flow control tank 29. Sedimentation chamber 30. Water passing member 31. Water passing member 32. Water passing member 34. Treated water storage unit 35. Pump 36. Flow control tank 37. Advection tube 38. Return pipe

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 単独処理浄化槽に配管接続することによ
り、排水の合併処理を可能とする合併処理化装置におい
て、その合併処理化装置が、好気処理を行うための生物
反応部と、その生物反応部の下流側にて排水の濾過を行
うための濾過部とを有し、単独処理浄化槽との配管接続
が、単独処理浄化槽の消毒室に流入する直前の排水を上
記生物反応部へと流入させる移流管と、上記濾過部を洗
浄した排水を単独処理浄化槽の嫌気処理部又は沈殿分離
室へと移送する洗浄排水移送管と、上記濾過部の下流側
の排水を単独処理浄化槽の消毒室に返送する返送管とに
よりなされ、浴槽からの排水を上記生物反応部へと流入
させる浴槽排水配管が、上記生物反応部又は移流管に設
けられた合併処理化装置。
Claims: 1. A merger treatment device which enables a merger treatment of wastewater by connecting a pipe to a single treatment septic tank, wherein the merger treatment device comprises a biological reaction section for performing aerobic treatment, and a biological reaction part thereof. A filtration section for filtering the wastewater downstream of the reaction section, and a pipe connection to the single treatment septic tank, and the wastewater immediately before flowing into the disinfection chamber of the single treatment septic tank flows into the biological reaction section. An advection pipe to be washed, a washing wastewater transfer pipe for transferring the wastewater washed from the filtration section to the anaerobic treatment section or the sedimentation separation chamber of the single treatment septic tank, and a wastewater downstream of the filtration section to the disinfection chamber of the single treatment septic tank. A return pipe for returning the bath, and a bathtub drainage pipe for allowing drainage from the bathtub to flow into the biological reaction section is provided in the biological reaction section or the advection pipe.
【請求項2】 浴槽排水配管が、流量調整弁を備えてい
る請求項1に記載の合併処理化装置。
2. The combined treatment apparatus according to claim 1, wherein the bathtub drainage pipe is provided with a flow control valve.
【請求項3】 生物反応部が、その上流側に流量調整槽
を有し、単独処理浄化槽及び浴槽からの排水が上記流量
調整槽を介して生物反応部へと流入する請求項1又は2
に記載される合併処理化装置。
3. The biological reaction section has a flow control tank on the upstream side thereof, and the wastewater from the single treatment septic tank and the bath tub flows into the biological reaction section through the flow control tank.
Merger processing device described in.
JP36952899A 1999-12-27 1999-12-27 Merger processing equipment Expired - Lifetime JP4119994B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP36952899A JP4119994B2 (en) 1999-12-27 1999-12-27 Merger processing equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP36952899A JP4119994B2 (en) 1999-12-27 1999-12-27 Merger processing equipment

Publications (2)

Publication Number Publication Date
JP2001179272A true JP2001179272A (en) 2001-07-03
JP4119994B2 JP4119994B2 (en) 2008-07-16

Family

ID=18494657

Family Applications (1)

Application Number Title Priority Date Filing Date
JP36952899A Expired - Lifetime JP4119994B2 (en) 1999-12-27 1999-12-27 Merger processing equipment

Country Status (1)

Country Link
JP (1) JP4119994B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2376618A (en) * 2001-06-21 2002-12-24 Durand Technology Ltd Expandable plant container
CN109867403A (en) * 2017-12-01 2019-06-11 中国水利水电科学研究院 A kind of processing unit and sewage water treatment method of dispersing type sewage

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5000594B2 (en) * 2008-07-07 2012-08-15 株式会社ハウステック Merger processing septic tank

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2376618A (en) * 2001-06-21 2002-12-24 Durand Technology Ltd Expandable plant container
CN109867403A (en) * 2017-12-01 2019-06-11 中国水利水电科学研究院 A kind of processing unit and sewage water treatment method of dispersing type sewage
CN109867403B (en) * 2017-12-01 2023-09-22 中国水利水电科学研究院 Decentralized sewage treatment device and sewage treatment method

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