JPH04118198U - Sewage septic tank - Google Patents

Sewage septic tank

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Publication number
JPH04118198U
JPH04118198U JP3121991U JP3121991U JPH04118198U JP H04118198 U JPH04118198 U JP H04118198U JP 3121991 U JP3121991 U JP 3121991U JP 3121991 U JP3121991 U JP 3121991U JP H04118198 U JPH04118198 U JP H04118198U
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JP
Japan
Prior art keywords
tank
chamber
filter bed
contact aeration
anaerobic filter
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
JP3121991U
Other languages
Japanese (ja)
Other versions
JP2543839Y2 (en
Inventor
八郎 佐藤
丈衛 佐藤
良人 北井
大 原田
和之 本田
Original Assignee
株式会社クボタ
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Filing date
Publication date
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Priority to JP3121991U priority Critical patent/JP2543839Y2/en
Publication of JPH04118198U publication Critical patent/JPH04118198U/en
Application granted granted Critical
Publication of JP2543839Y2 publication Critical patent/JP2543839Y2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Abstract

(57)【要約】 (修正有) 〔目的〕 コンパクトでありながら別途三次処理槽を設
けたものと同等の浄化効率が得られしかも脱窒効率も優
れる、主として5〜30人槽用の汚水浄化槽の改良を目的
とする。 〔構成〕 嫌気濾床槽第一室2Aと同第二室2B、接触
ばっ気槽第一室3Aと同第二室3B、沈殿槽4及び消毒
槽5を一体に有し、前記接触ばっ気槽第一室3Aの槽内
液を常時嫌気濾床槽第一室2Aへ返送する循環ポンプ6
Aと前記接触ばっ気槽第二室3Bの槽内液を不定期に嫌
気濾床槽第一室2Aへ返送する循環ポンプ6Bが設けら
れて構成され、接触ばっ気槽第一室3Aで発生する剥離
汚泥を常時嫌気濾床槽第一室2Aへ返送することによっ
て負荷を軽減し浄化効率を高める。
(57) [Summary] (with amendments) [Purpose] A sewage septic tank that is compact but has the same purification efficiency as a separate tertiary treatment tank and also has superior denitrification efficiency, mainly for use in tanks for 5 to 30 people. The purpose is to improve. [Configuration] It has an anaerobic filter bed tank first chamber 2A and a second chamber 2B, a contact aeration tank first chamber 3A and a second chamber 3B, a sedimentation tank 4 and a disinfection tank 5, and the contact aeration tank Circulation pump 6 that constantly returns the tank liquid in the tank first chamber 3A to the anaerobic filter bed tank first chamber 2A
A and a circulation pump 6B that irregularly returns the tank liquid in the contact aeration tank second chamber 3B to the anaerobic filter bed tank first chamber 2A, and the liquid generated in the contact aeration tank first chamber 3A is By constantly returning the peeled sludge to the anaerobic filter bed tank first chamber 2A, the load is reduced and the purification efficiency is increased.

Description

【考案の詳細な説明】[Detailed explanation of the idea]

【0001】0001

【産業上の利用分野】[Industrial application field]

この考案は汚水浄化槽に関し、詳しくは三次処理槽を有する汚水浄化槽の改良 に関する。 This idea is related to sewage septic tanks, and more specifically, improvement of sewage septic tanks with tertiary treatment tanks. Regarding.

【0002】0002

【従来の技術】[Conventional technology]

従来汚水浄化槽として、汚水を嫌気性微生物及び好気性微生物による生物学的 作用により汚水を順次浄化処理していく方式のものが広く知られており、通常こ れら汚水浄化槽は構造により5〜30人槽、あるいは31人槽以上のものと区別され ている。 上記において、容量5〜30人槽の場合の汚水浄化槽にあっては通常嫌気濾床槽 第一室と同第二室、接触ばっ気槽、沈殿槽及び消毒槽を一体に有する構造とされ 、最終的に排出される浄化処理水のBODが20mg/l以下となるように排出基準が 定められている。 そして、浄化処理水の目標水質が上記基準よりきびしいBOD10mg/l以下が要 求される場合は、さらに上記汚水浄化槽に三次汚水処理槽を設け、これらの連接 構造によって汚水処理を行う構造とされている(例えば実願平1-147524号、同14 7526、同149541号明細書及び図面等) 。 Traditionally, sewage septic tanks are used to treat sewage through biological treatment by anaerobic microorganisms and aerobic microorganisms. A system that sequentially purifies wastewater through action is widely known, and this method is usually used. These sewage septic tanks are classified into tanks for 5 to 30 people, or tanks for 31 people or more depending on their structure. ing. In the above, sewage septic tanks with a capacity of 5 to 30 people are usually anaerobic filter beds. It has a structure that integrates the first chamber, the second chamber, a contact aeration tank, a sedimentation tank, and a disinfection tank. , the discharge standards are set so that the BOD of the purified water that is finally discharged is 20 mg/l or less. It is determined. The target water quality of purified water must be BOD 10 mg/l or less, which is stricter than the above standards. If required, a tertiary sewage treatment tank should be installed in addition to the above sewage septic tank, and these should be connected. It is said that the structure is designed to treat sewage depending on the structure (for example, Utility Model Application No. 1-147524; 7526, 149541 specification and drawings, etc.).

【0003】0003

【従来技術の問題点】[Problems with conventional technology]

しかしながら、上記の汚水浄化槽は汚水浄化槽本体を設置した後、相互のレベ ルを調整しながらさらに三次処理槽を別に設置する必要があり、施工費用が多く なり、また大きな設置面積を必要とする欠点があった。 さらに、三次処理槽が本体汚水浄化槽と別体となっているので、この三次処理 槽の槽内液を本体汚水浄化槽側へ返送するには前置槽との水位差分高い揚程の返 送ポンプが必要となり、エアリフトポンプの場合多量のエア量が必要で効率が悪 かった。 However, after installing the sewage septic tank mentioned above, It is necessary to install a separate tertiary treatment tank while adjusting the This also has the disadvantage of requiring a large installation area. Furthermore, since the tertiary treatment tank is separate from the main sewage septic tank, the tertiary treatment To return the liquid in the tank to the main sewage septic tank, a return head with a higher water level than the front tank is used. A feed pump is required, and air lift pumps require a large amount of air and are inefficient. won.

【0004】0004

【考案が解決しようとする課題】[Problem that the idea aims to solve]

この考案は上記問題点に鑑み、コンパクトでありながら三次処理槽を設けたも のと同等の浄化効率が得られしかも脱窒効率も優れる、主として5〜30人槽用の 汚水浄化槽の改良を目的としたものである。 In view of the above problems, this idea was designed to be compact but equipped with a tertiary treatment tank. It is mainly used for tanks with 5 to 30 people, and has a purification efficiency equivalent to that of The purpose is to improve sewage septic tanks.

【0005】[0005]

【課題を解決するための手段】[Means to solve the problem]

即ち、この考案の汚水浄化槽は、汚水が流入される嫌気濾床槽第一室と以下処 理水が順次自然移流されていく嫌気濾床槽第二室、接触ばっ気槽第一室と同第二 室、沈殿槽及び消毒槽を一体に有し、前記接触ばっ気槽第一室の槽内液を常時嫌 気濾床槽第一室へ返送する循環ポンプと、前記接触ばっ気槽第二室の槽内液を不 定期に嫌気濾床槽第一室へ返送する循環ポンプとが設けられてなることを特徴と するものである。 That is, the sewage septic tank of this invention has a first chamber of the anaerobic filter bed tank into which sewage flows, and a chamber below. Anaerobic filter bed tank 2nd room, contact aeration tank 1st room and 2nd room where the water is naturally advected It has a chamber, a sedimentation tank, and a disinfection tank, and the liquid in the first chamber of the contact aeration tank is constantly abated. A circulation pump that returns the liquid to the first chamber of the air filter bed tank and a tank liquid that returns the liquid in the second chamber of the contact aeration tank. It is characterized by being equipped with a circulation pump that periodically returns the water to the first chamber of the anaerobic filter bed tank. It is something to do.

【0006】[0006]

【実施例】【Example】

次にこの考案の実施例を説明する。 図1はこの考案の実施例の断面図である。 この考案の汚水浄化槽1は、汚水が流入される嫌気濾床槽第一室2Aと以下処 理水が順次自然移流されていく嫌気濾床槽第二室2B、接触ばっ気槽第一室3A と同第二室3B、沈殿槽4及び消毒槽5を一体に有し、接触ばっ気槽第一室3A の槽内液を常時嫌気濾床槽第一室へ返送する循環ポンプ6Aが設けられていると 共に、接触ばっ気槽第二室3Bの槽内液を不定期に嫌気濾床槽第一室へ返送する 循環ポンプ6Bが設けられて構成されている。 上記において、循環ポンプ6A、6Bにはエアリフトポンプが使用され、また その流量調整のためエアリフトポンプ6Aへの空気供給管にはオリフィス板等か らなる調整装置が設けられている。 また、図中7A、7Bは夫々の接触ばっ気槽第一室、第二室内の接触材の逆洗 を行う散気管を、8A、8Bは夫々の接触ばっ気槽第一室、第二室内に散気を行 う散気管を示す。 また接触ばっ気槽第二室3Bの返送用循環ポンプ6Bは図示は省略するがタイ マー装置などにより間歇的に駆動操作されるように構成されている。 Next, an example of this invention will be described. FIG. 1 is a sectional view of an embodiment of this invention. The sewage septic tank 1 of this invention consists of an anaerobic filter bed tank first chamber 2A into which sewage flows, and a Anaerobic filter bed tank second chamber 2B, contact aeration tank first chamber 3A, where water is naturally advected in sequence It has the same second chamber 3B, sedimentation tank 4 and disinfection tank 5 as one unit, and a contact aeration tank first chamber 3A. A circulation pump 6A is provided to constantly return the liquid in the tank to the first chamber of the anaerobic filter bed tank. In addition, the tank liquid in the contact aeration tank second chamber 3B is returned to the anaerobic filter bed tank first chamber at irregular intervals. A circulation pump 6B is provided. In the above, air lift pumps are used as the circulation pumps 6A and 6B, and In order to adjust the flow rate, there is an orifice plate etc. in the air supply pipe to the air lift pump 6A. An adjusting device consisting of: In addition, 7A and 7B in the figure indicate backwashing of the contact material in the first and second chambers of the contact aeration tank, respectively. The air diffusers 8A and 8B are used to diffuse air into the first and second chambers of the contact aeration tank, respectively. Showing the diffuser tube. Also, the return circulation pump 6B of the contact aeration tank second chamber 3B is not shown, but It is configured to be driven and operated intermittently by a marketing device or the like.

【0007】[0007]

【作用】[Effect]

この考案の汚水浄化槽1において、汚水は嫌気濾床槽第一室2Aへ流入され、 順次嫌気濾床槽第二室2B、接触ばっ気槽第一室3A、同第二室3Bへと自然移 流により移流しつつ浄化されていく。 この場合流入水は嫌気濾床槽第一室2A及び同第二室2Bで粗大浮遊物が除去 され、嫌気性微生物の作用により分解される。次いで接触ばっ気槽第一室3Aへ 移流すれば好気性微生物の作用により水中の有機物、アンモニアは酸化分解され 、接触ばっ気槽第二室3Bで同じ処理が行われてさらにBOD値が低くなり硝化 が進行する。 この処理過程が長期続けられると接触ばっ気槽第一室3Aには微生物の生物膜 が剥離しこれが浮遊した状態となるが、槽内液は常時循環ポンプ6で嫌気濾床槽 第一室へ返送されているので、この水流によって上記剥離生物膜は返送され接触 ばっ気槽第一室3Aでの増加が防止される。 従って、接触ばっ気槽第一室3Aでの移流有機物の負荷が低く保持され、以後 の接触ばっ気槽第二室3Bでも安定したBOD除去が可能となり、容易にBOD ≦10ppm が達成され、さらに硝化効率も良くなる。 また、接触ばっ気槽第一室からの硝化液の常時返送と第2室からの間欠返送に より嫌気濾床槽では脱室が進行する。 さらに接触ばっ気槽第一室3A及び同第二室3Bは一体とされているので移流 の際の両者のレベル差が小さくできる。 In the sewage septic tank 1 of this invention, sewage flows into the anaerobic filter bed tank first chamber 2A, Naturally transferred sequentially to anaerobic filter bed tank second chamber 2B, contact aeration tank first chamber 3A, and second chamber 3B. It is purified while being advected by the current. In this case, coarse suspended matter is removed from the inflow water in the first chamber 2A and second chamber 2B of the anaerobic filter bed tank. and decomposed by the action of anaerobic microorganisms. Next, go to the contact aeration tank first chamber 3A. When advected, organic matter and ammonia in the water are oxidized and decomposed by the action of aerobic microorganisms. , the same treatment is carried out in the second chamber 3B of the contact aeration tank, and the BOD value further decreases, resulting in nitrification. progresses. If this treatment process continues for a long time, a biofilm of microorganisms will form in the first chamber 3A of the contact aeration tank. The liquid will peel off and become suspended in the tank, but the liquid in the tank will be constantly circulated through the anaerobic filter bed tank by the circulation pump 6. Since the water is returned to the first chamber, the detached biofilm is returned and contacted by this water flow. Increase in the aeration tank first chamber 3A is prevented. Therefore, the load of advective organic matter in the first chamber 3A of the contact aeration tank is kept low, and henceforth Stable BOD removal is possible even in the contact aeration tank second chamber 3B, making it easy to remove BOD. ≦10ppm is achieved, and the nitrification efficiency is further improved. In addition, it is possible to constantly return nitrifying liquid from the first chamber of the contact aeration tank and intermittent return from the second chamber. In the anaerobic filter bed tank, chamber escape progresses. Furthermore, since the contact aeration tank first chamber 3A and the second chamber 3B are integrated, advection The level difference between the two can be reduced.

【0008】[0008]

【考案の効果】[Effect of the idea]

この考案は以上説明したように、従来別体としていた三次処理槽を一体化した ので容積が非常にコンパクト化され5〜30人槽の小型化が達成されると共に、従 来必要としていた長尺の移流管が不要となりさらに放流管底を浅く設計できるの で設置の制約が少なくなり設置作業も容易となる。 また、接触ばっ気槽第一室より嫌気槽第一室への処理水常時返送と接触ばっ気 槽第二室よりの間欠返送によりBODの低減化、PH中性化など水質が安定化され 、さらに脱窒効率も良く、接触ばっ気槽第二室による処理によりBOD≦10PPm 、T−N≦20PPm など非常に良い浄化処理水とすることが可能となるのである。 As explained above, this idea integrates the tertiary treatment tank, which was previously separated. As a result, the volume is extremely compact, achieving a miniaturization of the tank for 5 to 30 people. This eliminates the need for long advection pipes that were previously required, and allows the bottom of the discharge pipe to be designed shallower. This reduces installation restrictions and makes installation work easier. In addition, the treated water is constantly returned from the first room of the contact aeration tank to the first room of the anaerobic tank, and the contact aeration tank is Intermittent return from the second chamber of the tank stabilizes water quality by reducing BOD and neutralizing pH. Furthermore, the denitrification efficiency is also good, and BOD≦10PPm due to treatment in the second chamber of the contact aeration tank. , it becomes possible to obtain very good purified water such as T-N≦20PPm.

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

【図1】この考案の実施例の断面図である。FIG. 1 is a sectional view of an embodiment of the invention.

【符号の説明】[Explanation of symbols]

1 汚水浄化槽 2A 嫌気濾床槽第一室 2B 嫌気濾床槽第二室 3A 接触ばっ気槽第一室 3B 接触ばっ気槽第二室 4 沈殿槽 5 消毒槽 6 循環ポンプ 1 Sewage septic tank 2A Anaerobic filter bed tank first room 2B Anaerobic filter bed tank second chamber 3A Contact aeration tank first chamber 3B Contact aeration tank second chamber 4 Sedimentation tank 5 Disinfection tank 6 Circulation pump

───────────────────────────────────────────────────── フロントページの続き (72)考案者 原田 大 滋賀県甲賀郡甲西町高松2番地の1 株式 会社クボタ滋賀工場内 (72)考案者 本田 和之 滋賀県甲賀郡甲西町高松2番地の1 株式 会社クボタ滋賀工場内 ──────────────────────────────────────────────── ─── Continuation of front page (72) Creator Dai Harada 2-1 Takamatsu, Kosai-machi, Koka-gun, Shiga Prefecture Stocks Inside Kubota Shiga Factory (72) Creator Kazuyuki Honda 2-1 Takamatsu, Kosai-machi, Koka-gun, Shiga Prefecture Stocks Inside Kubota Shiga Factory

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 【請求項1】 汚水が流入される嫌気濾床槽第一室と以
下処理水が順次自然移流されていく嫌気濾床槽第二室、
接触ばっ気槽第一室と同第二室、沈殿槽及び消毒槽を一
体に有し、前記接触ばっ気槽第一室の槽内液を常時嫌気
濾床槽第一室へ返送する循環ポンプと、前記接触ばっ気
槽第二室の槽内液を不定期に嫌気濾床槽第一室へ返送す
る循環ポンプとが設けられてなることを特徴とする汚水
浄化槽。
Claim 1: A first chamber of the anaerobic filter bed tank into which sewage flows, and a second chamber of the anaerobic filter bed tank into which the treated water is sequentially naturally advected;
A circulation pump that integrally includes a first chamber and a second chamber of a contact aeration tank, a settling tank, and a disinfection tank, and constantly returns the tank liquid in the first chamber of the contact aeration tank to the first chamber of an anaerobic filter bed tank. and a circulation pump for irregularly returning the liquid in the tank in the second chamber of the contact aeration tank to the first chamber of the anaerobic filter bed tank.
JP3121991U 1991-04-05 1991-04-05 Sewage septic tank Expired - Lifetime JP2543839Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3121991U JP2543839Y2 (en) 1991-04-05 1991-04-05 Sewage septic tank

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3121991U JP2543839Y2 (en) 1991-04-05 1991-04-05 Sewage septic tank

Publications (2)

Publication Number Publication Date
JPH04118198U true JPH04118198U (en) 1992-10-22
JP2543839Y2 JP2543839Y2 (en) 1997-08-13

Family

ID=31914573

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3121991U Expired - Lifetime JP2543839Y2 (en) 1991-04-05 1991-04-05 Sewage septic tank

Country Status (1)

Country Link
JP (1) JP2543839Y2 (en)

Also Published As

Publication number Publication date
JP2543839Y2 (en) 1997-08-13

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