JP3309465B2 - Septic tank membrane treatment device and septic tank - Google Patents
Septic tank membrane treatment device and septic tankInfo
- Publication number
- JP3309465B2 JP3309465B2 JP03022993A JP3022993A JP3309465B2 JP 3309465 B2 JP3309465 B2 JP 3309465B2 JP 03022993 A JP03022993 A JP 03022993A JP 3022993 A JP3022993 A JP 3022993A JP 3309465 B2 JP3309465 B2 JP 3309465B2
- Authority
- JP
- Japan
- Prior art keywords
- septic tank
- liquid
- pipe
- treated
- membrane
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
- Treatment Of Biological Wastes In General (AREA)
Description
【0001】[0001]
【産業上の利用分野】本発明は浄化槽にそのまま付加で
きる膜処理装置とこの膜処理装置を組み込んだ浄化槽に
関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a membrane treatment apparatus which can be directly added to a septic tank and a septic tank incorporating the membrane treatment apparatus.
【0002】[0002]
【従来の技術】生物処理と膜分離処理を組み合わせた廃
水処理装置として、特開昭63−209793号公報に
開示されるものがある。この廃水処理装置は嫌気性処理
槽によって処理した被処理液を一旦調整槽に貯留し、こ
の調整槽から取り出した被処理液を好気性処理槽と固液
分離装置を備えた循環処理ラインに流して処理するよう
にしたものである。2. Description of the Related Art A wastewater treatment apparatus combining biological treatment and membrane separation treatment is disclosed in Japanese Patent Application Laid-Open No. 63-209793. This wastewater treatment apparatus temporarily stores the liquid to be treated processed by the anaerobic treatment tank in a regulating tank, and flows the liquid to be treated taken out of the regulating tank into a circulation treatment line equipped with an aerobic treatment tank and a solid-liquid separator. Processing.
【0003】[0003]
【発明が解決しようとする課題】上述したように、嫌気
性処理、好気性処理及び固液分離処理を行なうことで浄
化能力は大幅に向上するのであるが、既に設置されてい
る浄化槽はし尿を処理する嫌気性処理室と沈澱室のみを
備えたものであり、この浄化槽を好気性処理と固液分離
処理が可能な浄化槽に交換するには、既に設置している
設備が無駄になる。また、単に好気性処理室と固液分離
処理装置をつなげただけでは浄化槽自体が大型化する。As described above, the purifying ability is greatly improved by performing the anaerobic treatment, the aerobic treatment and the solid-liquid separation treatment. It has only an anaerobic treatment chamber and a sedimentation chamber to be treated. To replace this septic tank with a septic tank capable of aerobic treatment and solid-liquid separation treatment, the equipment already installed is wasted. Further, simply connecting the aerobic treatment chamber to the solid-liquid separation treatment apparatus increases the size of the septic tank itself.
【0004】[0004]
【課題を解決するための手段】上記課題を解決すべく本
願の第1発明は、ポンプにつながる被処理液の吸引パイ
プと、ポンプから伸びる被処理液の供給パイプと、被処
理液の供給パイプに接続される分離膜と、この分離膜か
ら透過液を取り出す透過液パイプと、分離膜から濃縮液
を取り出す濃縮液パイプと、濃縮液パイプに接続される
エジェクターと、エジェクターに接続される散気装置と
によって膜処理装置を構成した。In order to solve the above-mentioned problems, a first invention of the present application comprises a suction pipe for a liquid to be treated connected to a pump, a supply pipe for the liquid to be treated extending from the pump, and a supply pipe for the liquid to be treated. , A permeate pipe for extracting the permeate from the separation membrane, a concentrate pipe for extracting the concentrate from the separation membrane, an ejector connected to the concentrate pipe, and a diffuser connected to the ejector The apparatus constituted a film processing apparatus.
【0005】また、第1発明に係る膜処理装置を付加し
た浄化槽としては、膜処理装置の分離膜を浄化槽本体の
上方に配置し、前記膜処理装置の被処理液の吸引パイプ
を沈澱室に、透過液パイプを消毒室に臨ませ、更に散気
装置を生物処理室内に配置した。Further, as a septic tank to which the membrane treatment apparatus according to the first invention is added, a separation membrane of the membrane treatment apparatus is disposed above a septic tank main body, and a suction pipe for a liquid to be treated of the membrane treatment apparatus is provided in a precipitation chamber. Then, the permeate pipe was made to face the disinfection room, and the air diffuser was placed in the biological treatment room.
【0006】[0006]
【作用】第1発明に係る膜処理装置を浄化槽に付設する
には、浄化槽の点検口を開け、点検口から浄化槽内にエ
ジェクターと散気装置を入れる。 [Act] To attaching a film processing apparatus according to the first invention septic tank, opening the access door of the septic tank, Ru placed ejector and air diffuser in the septic tank through the sight port.
【0007】[0007]
【実施例】以下に本発明の実施例を添付図面に基づいて
説明する。図1は第1発明に係る浄化槽用膜処理装置の
全体図であり、この膜処理装置はカバー1内に管状の分
離膜2とポンプ3を配設し、このポンプ3につながる被
処理液の吸引パイプ4の一部をカバー1外に導出し、ポ
ンプ3から伸びる被処理液の供給パイプ5を前記分離膜
2の一次側に接続している。Embodiments of the present invention will be described below with reference to the accompanying drawings. FIG. 1 is an overall view of a membrane treatment apparatus for a septic tank according to the first invention. In this membrane treatment apparatus, a tubular separation membrane 2 and a pump 3 are disposed in a cover 1, and a liquid to be treated connected to the pump 3 is removed. A part of the suction pipe 4 is led out of the cover 1, and a supply pipe 5 for the liquid to be treated extending from the pump 3 is connected to the primary side of the separation membrane 2.
【0008】また、分離膜2の二次側には透過液を取り
出す透過液パイプ6を接続し、この透過液パイプ6の一
部をカバー1外に導出し、更に分離膜2の一次側には濃
縮液を取り出す濃縮液パイプ7を接続している。そし
て、濃縮液パイプ7の途中にはカバー1に保持されるエ
ジェクター8を接続し、このエジェクター8から延びる
気液導入パイプ9の先端に散気管10を取り付けてい
る。Further, a permeate pipe 6 for extracting a permeate is connected to the secondary side of the separation membrane 2, a part of the permeate pipe 6 is led out of the cover 1, and further connected to the primary side of the separation membrane 2. Is connected to a concentrate pipe 7 for taking out a concentrate. An ejector 8 held by the cover 1 is connected in the middle of the concentrated liquid pipe 7, and an air diffuser 10 is attached to a distal end of a gas-liquid introduction pipe 9 extending from the ejector 8.
【0009】図2は上記の膜処理装置を付加した浄化槽
の正面図、図3は同浄化槽の平面図であり、浄化槽は既
に地中等に埋設されている既存のものであり、槽本体
(タンク)11の地表に露出した上面に膜処理装置を付
設している。FIG. 2 is a front view of a septic tank to which the above-mentioned membrane treatment apparatus is added, and FIG. 3 is a plan view of the septic tank. The septic tank is an existing one which is already buried underground or the like. A film processing apparatus is attached to the upper surface exposed on the surface of 11).
【0010】浄化槽の槽本体11は内部を隔壁12,1
3にて第1処理室S1、第2処理室S2及び沈殿室S3
に区画され、沈殿室S3は底部で第2処理室S2と連通
し、また沈殿室S3上部には消毒室S4を設けている。
そして、第1処理室S1には導入管14を介して被処理
液が導入され、第1処理室S1内の被処理液は連通路1
5を介して第2処理室S2に送られ、沈殿室S3の上澄
み液が消毒室S4で消毒された後、排出管16を介して
外部に取り出される。A tank main body 11 of a septic tank has a partition wall 12, 1 inside.
3, the first processing chamber S1, the second processing chamber S2, and the sedimentation chamber S3
The sedimentation chamber S3 communicates with the second processing chamber S2 at the bottom, and a disinfection chamber S4 is provided above the sedimentation chamber S3.
Then, the liquid to be treated is introduced into the first processing chamber S1 through the introduction pipe 14, and the liquid to be treated in the first processing chamber S1 is communicated with the communication path 1.
5, is sent to the second processing chamber S2, and the supernatant liquid of the precipitation chamber S3 is disinfected in the disinfection chamber S4, and then taken out through the discharge pipe 16.
【0011】ここで、膜処理装置を付加する前の浄化槽
はし尿のみを処理する単独浄化槽であり、第1処理室S
1及び第2処理室S2では共に嫌気性処理を施してい
た。Here, the septic tank before the addition of the membrane treatment apparatus is a single septic tank for treating only night soil, and the first treatment chamber S
Anaerobic treatment was performed in both the first and second processing chambers S2.
【0012】一方、膜処理装置を付加した浄化槽は、槽
本体11の上面の点検口17を介して、膜処理装置のエ
ジェクター8及び気液導入パイプ9と散気管10からな
る散気装置をそれぞれ第1処理室S1及び第2処理室S
2内に配置し、第1処理室S1及び第2処理室S2を共
に好気性処理が可能な室に変更している。尚、第1処理
室S1及び第2処理室S2を必ずしも好気性処理室にす
る必要はなく、エジェクター8において導入する空気の
量を無くすか、大幅に絞るか、あるいは間欠的に曝気を
することによって嫌気性処理室となる。また、浄化槽の
沈殿室S3内には膜処理装置の吸引パイプ4を臨ませ、
消毒室S4には透過液パイプ6を臨ませている。On the other hand, the septic tank to which the membrane treatment device is added is provided with an ejector 8 of the membrane treatment device and an air diffuser comprising a gas-liquid introduction pipe 9 and an air diffusion tube 10 via an inspection port 17 on the upper surface of the tank body 11. First processing chamber S1 and second processing chamber S
2, the first processing chamber S1 and the second processing chamber S2 are both changed to a chamber capable of performing aerobic processing. Note that the first processing chamber S1 and the second processing chamber S2 do not necessarily have to be aerobic processing chambers, and the amount of air introduced into the ejector 8 is eliminated, greatly reduced, or intermittently aerated. It becomes an anaerobic treatment room. In addition, the suction pipe 4 of the membrane processing apparatus faces the sedimentation chamber S3 of the septic tank,
The permeated liquid pipe 6 faces the disinfection chamber S4.
【0013】以上において、導入管14を介して第1処
理室S1に被処理液を導入する。被処理液としては、し
尿の他に生ごみを含む台所排水、風呂、洗面或いは洗濯
排水等の雑排水も同時に導入する。ここで、第1処理室
S1ではエジェクター8への空気の取り込みを絞って嫌
気性処理を行ない、第2処理室S2ではエジェクター8
へ空気を取り込んで好気性処理を行なうものとする。In the above, the liquid to be treated is introduced into the first processing chamber S1 through the introduction pipe 14. As the liquid to be treated, miscellaneous wastewater such as kitchen wastewater, bath, washing surface, or washing wastewater containing garbage is also introduced in addition to night soil. Here, in the first processing chamber S1, anaerobic processing is performed by reducing the intake of air into the ejector 8, and in the second processing chamber S2, the ejector 8 is discharged.
The aerobic treatment is performed by taking in air.
【0014】すると、第1処理室S1に導入された被処
理液は、先ず酸生成菌によって被処理液中の有機物が酢
酸(CH3COOH)やプロピオン酸(CH3CH2CO
OH)等の有機酸に低分子化され、更にこれら有機酸は
分解され、メタン菌などによってメタン(CH4)や二
酸化炭素(CO2)のガスに変換される。また、タンパ
ク質や尿素などの窒素分の分解物であるアンモニア態窒
素(NH4+)が生成される。Then, in the liquid to be treated introduced into the first processing chamber S1, the organic matter in the liquid to be treated is first converted to acetic acid (CH 3 COOH) or propionic acid (CH 3 CH 2 CO
OH) and the like, and these organic acids are further decomposed and converted into methane (CH 4 ) or carbon dioxide (CO 2 ) gas by methane bacteria or the like. Also, ammonia nitrogen (NH 4 +), which is a decomposition product of nitrogen such as protein and urea, is generated.
【0015】このアンモニア態窒素(NH4+)及び未分
解の有機物を含んだ被処理液は連通路15を介して第2
処理室S2に送られる。この第2処理室S2では散気管
10を通して吹込まれたエア(酸素)を利用して硝化菌
によりアンモニア態窒素(NH4+)が硝酸態窒素(NO
3-)や亜硝酸態窒素(NO2-)に酸化分解され、また未
分解有機物は、好気性菌の集合体である生物膜によって
酸化分解される。そして、硝酸態窒素(NO3-)や亜硝
酸態窒素(NO2-)を含む処理水の一部は吸引パイプ
4,分離膜2を介して濃縮液と共に濃縮液パイプ7,気
液導入パイプ9を介して第1処理室S1に戻り、脱窒素
菌等により脱窒素処理される。また、好気性処理された
後の処理水は沈殿室3に流入し、吸引パイプ4を介して
分離膜2へ供給され、透過液は透過液パイプ6から消毒
室S4を介して放流される。The liquid to be treated containing the ammonia nitrogen (NH 4 +) and undecomposed organic substances is passed through the communication passage 15 to the second liquid.
It is sent to the processing chamber S2. In the second processing chamber S2, ammonia nitrogen (NH 4 +) is converted into nitrate nitrogen (NO) by nitrifying bacteria utilizing air (oxygen) blown through the air diffuser 10.
3- ) and nitrite nitrogen (NO 2- ) are oxidatively decomposed, and undecomposed organic matter is oxidatively decomposed by a biofilm, which is an aggregate of aerobic bacteria. Part of the treated water containing nitrate nitrogen (NO 3 −) or nitrite nitrogen (NO 2 −) passes through the suction pipe 4 and the separation membrane 2 together with the concentrate and the concentrate pipe 7, the gas-liquid introduction pipe Then, the process returns to the first processing chamber S1 via 9 and is denitrified by denitrifying bacteria or the like. The treated water after the aerobic treatment flows into the precipitation chamber 3 and is supplied to the separation membrane 2 via the suction pipe 4, and the permeate is discharged from the permeate pipe 6 via the disinfection chamber S 4.
【0016】第1発明に係る浄化槽にあっては第2処理
室S2から取り出した被処理液を濃縮して再び処理室に
戻すようにしている。In the septic tank according to the first invention, the liquid to be treated taken out of the second processing chamber S2 is concentrated and returned to the processing chamber.
【0017】[0017]
【発明の効果】以上に説明したように本発明に係る浄化
槽用膜処理装置は、既存の単一浄化槽に何らの変更を加
えることなく、そのまま付加することができ、極めて経
済的である。また、本発明に係る浄化槽用膜処理装置が
付加された浄化槽は、好気性処理と膜分離処理を行なう
ことができるので、し尿に限らず生ごみを含む台所排
水、風呂、洗面或いは洗濯排水なども同時に処理するこ
とができるので浄化能力が大幅にアップする。As described above, the membrane treatment apparatus for a septic tank according to the present invention can be added to an existing single septic tank without any change, and is extremely economical. In addition, the septic tank to which the septic tank membrane treatment device according to the present invention is added can perform aerobic treatment and membrane separation treatment, so that kitchen wastewater including not only human waste but also kitchen garbage, a bath, a washing surface, or a washing wastewater is used. Can be treated at the same time, so that the purification ability is greatly improved.
【図1】第一発明に係る浄化槽用膜処理装置の全体図FIG. 1 is an overall view of a septic tank membrane treatment apparatus according to a first invention.
【図2】第一発明に係る浄化槽用膜処理装置を付加した
浄化槽の正面図FIG. 2 is a front view of a septic tank to which a septic tank membrane treatment apparatus according to the first invention is added.
【図3】図2に示した浄化槽の平面図FIG. 3 is a plan view of the septic tank shown in FIG.
【符号の説明】1… カバー、 2…分離膜、 3…ポンプ、 4…被処
理液の吸引パイプ、5…被処理液の供給パイプ、 6…
透過液パイプ、 7…濃縮液パイプ、 8…エジェクタ
ー、 10…散気管。[Description of Signs] 1 ... cover, 2 ... separation membrane, 3 ... pump, 4 ... suction pipe for liquid to be treated, 5 ... supply pipe for liquid to be treated, 6 ...
Permeate pipe 7 Concentrate pipe 8 Ejector 10 Aeration tube
───────────────────────────────────────────────────── フロントページの続き (72)発明者 三浦 勲 福岡県北九州市小倉北区中島2丁目1番 1号 東陶機器株式会社内 (56)参考文献 特開 平4−247295(JP,A) 特開 平4−87694(JP,A) 実開 平4−99300(JP,U) 実開 平4−110196(JP,U) 実開 平4−134492(JP,U) (58)調査した分野(Int.Cl.7,DB名) C02F 3/00,1/44 ──────────────────────────────────────────────────続 き Continuation of the front page (72) Inventor Isao Miura 2-1-1, Nakajima, Kokurakita-ku, Kitakyushu-shi, Fukuoka Prefecture Totoki Kiki Co., Ltd. (56) References JP-A-4-247295 (JP, A) JP-A-4-87694 (JP, A) JP-A-4-99300 (JP, U) JP-A-4-110196 (JP, U) JP-A-4-134492 (JP, U) (Int.Cl. 7 , DB name) C02F 3 / 00,1 / 44
Claims (2)
と、ポンプから伸びる被処理液の供給パイプと、被処理
液の供給パイプに接続される分離膜と、分離膜から透過
液を取り出す透過液パイプと、分離膜から濃縮液を取り
出す濃縮液パイプと、濃縮液パイプに接続されるエジェ
クターと、エジェクターに接続される散気装置とを備え
たことを特徴とする浄化槽用膜処理装置。1. A suction pipe for a liquid to be treated connected to a pump, a supply pipe for the liquid to be treated extending from the pump, a separation membrane connected to a supply pipe for the liquid to be treated, and a permeate for extracting the permeate from the separation membrane. A membrane treatment apparatus for a septic tank, comprising: a pipe; a concentrate pipe for extracting a concentrate from a separation membrane; an ejector connected to the concentrate pipe; and an air diffuser connected to the ejector.
の分離膜を槽本体の上方に配置し、前記膜処理装置の被
処理液の吸引パイプを沈澱室に、透過液パイプを消毒室
に臨ませ、更に散気装置を生物処理室内に配置してなる
ことを特徴とする浄化槽。2. The separation membrane of the membrane treatment apparatus for a septic tank according to claim 1, wherein the separation membrane is disposed above the tank body, the suction pipe for the liquid to be treated of the membrane treatment apparatus is disposed in a precipitation chamber, and the permeate pipe is disposed in a disinfection chamber. And a diffuser is placed in the biological treatment chamber.
A septic tank characterized by that .
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP03022993A JP3309465B2 (en) | 1993-02-19 | 1993-02-19 | Septic tank membrane treatment device and septic tank |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP03022993A JP3309465B2 (en) | 1993-02-19 | 1993-02-19 | Septic tank membrane treatment device and septic tank |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH06238287A JPH06238287A (en) | 1994-08-30 |
JP3309465B2 true JP3309465B2 (en) | 2002-07-29 |
Family
ID=12297889
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP03022993A Expired - Fee Related JP3309465B2 (en) | 1993-02-19 | 1993-02-19 | Septic tank membrane treatment device and septic tank |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP3309465B2 (en) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP4848139B2 (en) * | 2005-05-23 | 2011-12-28 | 隆喜 栂 | Aeration tank structure |
JP5648387B2 (en) * | 2010-09-16 | 2015-01-07 | 三菱レイヨン株式会社 | Aeration device and method of operating membrane separation device |
-
1993
- 1993-02-19 JP JP03022993A patent/JP3309465B2/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
JPH06238287A (en) | 1994-08-30 |
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