JPH07237Y2 - Sewage treatment equipment - Google Patents
Sewage treatment equipmentInfo
- Publication number
- JPH07237Y2 JPH07237Y2 JP4226889U JP4226889U JPH07237Y2 JP H07237 Y2 JPH07237 Y2 JP H07237Y2 JP 4226889 U JP4226889 U JP 4226889U JP 4226889 U JP4226889 U JP 4226889U JP H07237 Y2 JPH07237 Y2 JP H07237Y2
- Authority
- JP
- Japan
- Prior art keywords
- sewage treatment
- air
- tank
- filter layer
- sewage
- 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
- Treatment Of Biological Wastes In General (AREA)
Description
【考案の詳細な説明】 〔産業上の利用分野〕 この考案の汚水処理装置に関し、詳しくは接触ばっ気室
を有する汚水処理装置の改良に関する。DETAILED DESCRIPTION OF THE INVENTION [Industrial field of application] The present invention relates to a sewage treatment apparatus, and more particularly to an improvement of a sewage treatment apparatus having a contact aeration chamber.
従来、汚水処理装置として分離接触ばっ気方式、及び嫌
気ろ床接触ばっ気方式などの汚水処理装置が知られてい
る。Conventionally, as a sewage treatment apparatus, a separation contact aeration method, an anaerobic filter contact aeration method, and the like are known.
ところで、これら汚水処理装置において、接触ばっ気室
内での生物膜が季節的性状変動時、あるいは長期経過後
などに剥離し、浮遊する現象が生じ、微細で沈降し難い
浮遊汚泥はそのまま放流水に混ざって流出することが有
り、SS,SS性BODの上昇を来す不具合が有った。By the way, in these sewage treatment devices, the biofilm in the contact aeration chamber peels and floats when seasonal properties change or after a long period of time. There was a problem that they could mix and flow out, causing an increase in SS and SS sex BOD.
このような不具合を解消するため、従来の汚水処理装置
では、放流水を再び濾過装置に導びき三次処理を行なう
方式としたり、あるいは放流水に対し、もう一段の酸化
処理槽を設けて三次処理を行なうことなどが実施されて
いる。In order to eliminate such a problem, in the conventional wastewater treatment equipment, the effluent water is guided to the filtration device again to carry out the tertiary treatment, or the effluent water is provided with a third-stage oxidization treatment tank for the tertiary treatment. Is carried out.
しかし、上記三次処理を行なう方法は、いずれにして
も、汚水処理装置としての浄化槽の他に三次処理設備を
要し、また、これらに対するブロア、ポンプなどの駆動
設備を付設しなければならないので、占有容積が増大す
る他、運転管理も複雑となり、家庭用として実施が困難
となる問題が有った。However, in any case, the method for performing the above-mentioned tertiary treatment requires tertiary treatment equipment in addition to the septic tank as the sewage treatment device, and since it is necessary to attach drive equipment such as a blower and a pump to these, In addition to increasing the occupied volume, operation management becomes complicated, and there is a problem that it is difficult to implement for home use.
この考案は、上記問題点に鑑み、一の浄化槽のみで、SS
の流出が防止でき,さらに昼夜を通じ、汚水処理の効率
を一定となし得る、浄化効率の良い汚水処理装置を提供
することを目的としてなされたものである。In consideration of the above-mentioned problems, this device has only one septic tank, and SS
The purpose of the present invention is to provide a sewage treatment apparatus which can prevent the outflow of sewage and can keep the efficiency of sewage treatment constant throughout the day and night and which has good purification efficiency.
即ち、この考案の汚水処理装置は、接触ばっ気槽を有す
る汚水処理装置において、沈殿槽に濾過層が設けられ、
該濾過層下部には、前記接触ばっ気槽への空気供給管と
は別系統とされた逆洗用散気管が設けられていると共
に、濾過層上部には、前記逆洗用散気管と同時に給気さ
れる処理汚水を汚水原水の流入室へ返送するエアリフト
ポンプが設けられ、前記空気供給管へ給気するブロアー
装置は運転制御用タイマーが付設されて成ることを特徴
とする汚水処理装置。That is, the sewage treatment apparatus of the present invention is a sewage treatment apparatus having a contact aeration tank, wherein a settling tank is provided with a filter layer,
A backwash air diffuser, which is a separate system from the air supply pipe to the contact aeration tank, is provided in the lower portion of the filter layer, and at the same time, the backwash air diffuser pipe is provided in the upper portion of the filter layer. An sewage treatment apparatus comprising an air lift pump for returning the treated sewage to be supplied to the inflow chamber of the sewage raw water, and a blower device for supplying air to the air supply pipe is provided with an operation control timer.
次に、この考案の実施例を説明する。 Next, an embodiment of this invention will be described.
第1図はこの考案の実施例の断面図、第2図は第1図の
要部拡大図である。FIG. 1 is a sectional view of an embodiment of the present invention, and FIG. 2 is an enlarged view of a main part of FIG.
この考案の汚水処理装置1は一つの槽を多槽に仕切り、
汚水原水の流入される沈殿分離室又は嫌気ろ床第1槽、
あるいは第2槽1A,1B、接触ばっ気槽1C、沈殿槽1D及び
消毒槽1Eとし、汚水を順次移送していく汚水処理装置に
おいて、沈殿槽1Dにれき、砂層又は樹脂繊維層など2Aよ
り成る濾過層2が設けられ、この濾過層2の下部には接
触ばっ気槽1C内の散気管3へ給気を行なうブロアー4及
び給気管5とは別系統として、逆洗用散気管6が設けら
れていると共に、濾過層2上部には逆洗用散気管6への
空気供給管7に逆洗時処理汚水を汚水原水の流入槽1Aへ
返送するエアリフトポンプ8が接続され、さらに空気供
給管7へ給気するブロアー9には運転制御用タイマー10
が付設されて構成されている。The sewage treatment apparatus 1 of this invention divides one tank into multiple tanks,
Sedimentation separation chamber or anaerobic filter bed first tank into which raw wastewater flows
Alternatively, the second tank 1A, 1B, the contact aeration tank 1C, the settling tank 1D and the disinfectant tank 1E, and in the wastewater treatment device that sequentially transfers the wastewater, the settling tank 1D is composed of 2A such as gravel, sand layer or resin fiber layer. A filter layer 2 is provided, and a backwash air diffuser pipe 6 is provided below the filter layer 2 as a system separate from the blower 4 and the air supply pipe 5 for supplying air to the air diffuser pipe 3 in the contact aeration tank 1C. At the same time, an air lift pump 8 for returning the backwash treated wastewater to the inflow tank 1A of the wastewater raw water is connected to the air supply pipe 7 for the backwash diffuser pipe 6 above the filter layer 2, and the air supply pipe is further provided. The blower 9 that supplies air to 7 has a timer 10 for operation control.
Is attached.
なお、図中1Fは、沈殿室1Dより消毒室1Eへ処理水を移送
する流量調整用エアリフトポンプを示す。In addition, 1F in the figure shows a flow rate adjusting air lift pump that transfers the treated water from the precipitation chamber 1D to the disinfection chamber 1E.
上記実施例において、タイマー10は一昼夜を通じ、例え
ば、深夜の一定時間のみブロアー9を作動させ、以外の
時間帯は、休止する制御を行なう構成とされる。In the above-described embodiment, the timer 10 is configured to operate the blower 9 only for a fixed time at midnight throughout the day and night, and to stop the blower 9 at other times.
又、上記において、濾過層を構成する濾材は、上記の他
細砂、粗大砂、及び礫などの他、樹脂粒子なども使用可
能である。Further, in the above, as the filter medium constituting the filter layer, in addition to the above fine sand, coarse sand, gravel and the like, resin particles and the like can be used.
この考案において、通常時においては、接触ばっ気槽1C
より沈殿室1Dへ移流した処理汚水は、消毒槽1Eへ至るま
でに、濾過層2を経るため、この部分でSSはほぼ完全に
濾過され、除去される。In this device, the contact aeration tank 1C is normally used.
The treated sewage transferred to the settling chamber 1D passes through the filter layer 2 before reaching the disinfecting tank 1E, so that SS is almost completely filtered and removed in this portion.
従って、流出水中へのSSが減少しSS性BOD値が低下す
る。Therefore, SS in runoff water decreases and SS BOD value decreases.
一方、濾過層2で濾過された浮遊汚泥は、濾過層2に滞
留するため、放置すれば目詰まりの原因となる。On the other hand, the floating sludge filtered in the filtration layer 2 stays in the filtration layer 2, and if left unattended, it causes clogging.
しかし、タイマー10により間歇的に作動する逆洗用散気
管6によって、これらは逆洗により再浮遊し、これが濾
過層2上部のエアリフトポンプ8により汚水原水の流入
する槽1Aへ返送され、自動的に除去されるのである。However, by the backwash air diffuser 6 which is intermittently operated by the timer 10, these are re-suspended by backwash, and this is returned to the tank 1A into which the raw wastewater flows by the air lift pump 8 above the filtration layer 2 and automatically. Will be removed.
よって、濾過層2の目詰まりは、充分に予防される。Therefore, the clogging of the filtration layer 2 is sufficiently prevented.
さらに、このエアリフトポンプ8による汚泥返送は、汚
水原水の流入の無い深夜時間帯とされるから、次回の汚
水流入ピーク時に備え、再循環により汚水の再処理を行
うので、ピーク時の流入水勢による未処理汚水の流出も
防止できるのである。Further, since the sludge return by the air lift pump 8 is performed at midnight time when the raw water of the wastewater does not flow in, the wastewater is reprocessed by recirculation in preparation for the next peak of the wastewater inflow. Outflow of untreated sewage can also be prevented.
また、槽の全液面を流量調整用エアリフトポンプ1Fで調
整する場合、深夜時間帯は低水位になり逆洗時汚水の流
出は完全に防ぐことが出来る。Also, when the total liquid level in the tank is adjusted by the flow rate adjusting air lift pump 1F, the water level becomes low during the midnight time and the outflow of dirty water during backwashing can be completely prevented.
この考案は以上説明したように、接触ばっ気槽におい
て、浮遊汚泥が発生しても、これらは、沈殿槽の濾過層
でほぼ完全に除去されるので、流出水中にSSが混入する
おそれがなく、また、タイマー制御によって濾過層のSS
を再浮遊させ、これをエアリフトポンプで汚水原水の流
入口へ返送するため流出水のBOD値上昇も有効に防止で
きるのである。As explained above, even if floating sludge is generated in the contact aeration tank, it is almost completely removed by the filtration layer of the sedimentation tank, so there is no risk of SS being mixed into the outflow water. , Also, SS of the filtration layer by timer control
Is re-suspended and returned to the inflow port of the wastewater by the air lift pump, which effectively prevents the rise of the BOD value of the outflow water.
さらに全体が一つの槽内に収められるので、コンパクト
化され、設置も容易となるなど種々の実用的効果を有す
る。Further, since the whole is stored in one tank, it has various practical effects such as compactness and easy installation.
第1図はこの考案の断面図、第2図は第1図の要部拡大
図である。FIG. 1 is a sectional view of the present invention, and FIG. 2 is an enlarged view of a main part of FIG.
Claims (1)
て、沈殿槽に濾過層が設けられ、該濾過層下部には、前
記接触ばっ気槽への空気供給管とは別系統とされた逆洗
用散気管が設けられていると共に、濾過層上部には、前
記逆洗用散気管と同時に給気される処理汚水を汚水原水
の流入室へ返送するエアリフトポンプが設けられ、前記
空気供給管へ給気するブロアー装置は運転制御用タイマ
ーが付設されて成ることを特徴とする汚水処理装置。1. A sewage treatment apparatus having a contact aeration tank, wherein a settling tank is provided with a filter layer, and a lower part of the filter layer is provided with a system separate from an air supply pipe to the contact aeration tank. In addition to the air diffuser for washing, an air lift pump for returning the treated sewage, which is supplied at the same time as the air diffuser for backwashing, to the inflow chamber of the sewage raw water is provided in the upper part of the filter layer, and the air supply pipe The blower device for supplying air to the equipment is provided with a timer for operation control, which is a sewage treatment device.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4226889U JPH07237Y2 (en) | 1989-04-11 | 1989-04-11 | Sewage treatment equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4226889U JPH07237Y2 (en) | 1989-04-11 | 1989-04-11 | Sewage treatment equipment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH02133496U JPH02133496U (en) | 1990-11-06 |
| JPH07237Y2 true JPH07237Y2 (en) | 1995-01-11 |
Family
ID=31553662
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP4226889U Expired - Fee Related JPH07237Y2 (en) | 1989-04-11 | 1989-04-11 | Sewage treatment equipment |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH07237Y2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2016159290A (en) * | 2015-03-05 | 2016-09-05 | 株式会社クボタ | Septic tank |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2679531B2 (en) * | 1992-05-28 | 1997-11-19 | 株式会社イナックス | Filtration device |
| JP4979531B2 (en) * | 2007-10-01 | 2012-07-18 | 株式会社ハウステック | Aerobic filter bed and method for operating the aerobic filter bed |
-
1989
- 1989-04-11 JP JP4226889U patent/JPH07237Y2/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2016159290A (en) * | 2015-03-05 | 2016-09-05 | 株式会社クボタ | Septic tank |
| WO2016140084A1 (en) * | 2015-03-05 | 2016-09-09 | 株式会社クボタ | Sewage treatment tank |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH02133496U (en) | 1990-11-06 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| LAPS | Cancellation because of no payment of annual fees |