JP2002119987A - Flow rate adjusting tank, anaerobic treatment tank and sewage cleaning tank - Google Patents

Flow rate adjusting tank, anaerobic treatment tank and sewage cleaning tank

Info

Publication number
JP2002119987A
JP2002119987A JP2000319505A JP2000319505A JP2002119987A JP 2002119987 A JP2002119987 A JP 2002119987A JP 2000319505 A JP2000319505 A JP 2000319505A JP 2000319505 A JP2000319505 A JP 2000319505A JP 2002119987 A JP2002119987 A JP 2002119987A
Authority
JP
Japan
Prior art keywords
tank
treatment tank
flow control
anaerobic treatment
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.)
Granted
Application number
JP2000319505A
Other languages
Japanese (ja)
Other versions
JP4712953B2 (en
Inventor
Atsushi Hibino
淳 日比野
Nobuyoshi Katagai
信義 片貝
Hiroshi Yamashita
宏 山下
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 JP2000319505A priority Critical patent/JP4712953B2/en
Publication of JP2002119987A publication Critical patent/JP2002119987A/en
Application granted granted Critical
Publication of JP4712953B2 publication Critical patent/JP4712953B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Classifications

    • Y02W10/12

Abstract

PROBLEM TO BE SOLVED: To provide a compact sewage cleaning tank further enhanced in capacity than before and capable of stably treating sewage. SOLUTION: A flow rate adjusting tank is divided into an upper effective part and a lower effective part by the horizontal surface of a water level half the maximum water level to be formed into a top-heavy shape wherein the volume of the lower effective part is 10-90% that of the upper effective part and the shape of an anaerobic treatment tank is bisected in the same way to be formed into each a fan shape wherein the volume of an upper effective part is 20-90% of the volume of a lower effective part, and these two tanks are provided side by side, and further, an aerobic treatment tank and a disinfection tank are provided to form the sewage cleaning tank.

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、流量調整槽、嫌気
処理槽及び汚水浄化槽に関する。更に詳しくは、し尿や
雑排水などの汚水又は排水を処理する汚水浄化槽の槽内
に設けられ、特にその形状に特徴がある流量調整槽及び
嫌気処理槽並びにこの流量調整槽及び嫌気処理槽を槽内
に組み込んだ汚水浄化槽に関する。
The present invention relates to a flow control tank, an anaerobic treatment tank, and a sewage purification tank. More specifically, a flow control tank and an anaerobic treatment tank provided in a tank of a sewage purification tank for treating sewage or wastewater such as night soil and gray water, and particularly characterized in its shape, and the flow control tank and the anaerobic treatment tank The present invention relates to a sewage septic tank incorporated in a tank.

【0002】[0002]

【従来の技術】汚水浄化槽は、従来から種々知られてい
る。これらのうちの一例は、図5に示すように上流側か
ら順に、嫌気濾床槽(第1室)、嫌気濾床槽(第2
室)、好気処理槽、沈殿槽及び消毒槽が配置され、か
つ、嫌気処理槽の上方部に流量調整部(図5のH.W.
L.とL.W.L.とで挟まれる部分)が設けられた汚
水浄化槽である(特開平4−367793号公報)。
2. Description of the Related Art Various types of sewage treatment tanks have been known. One example of these is an anaerobic filter tank (first chamber) and an anaerobic filter tank (second chamber) in this order from the upstream side as shown in FIG.
Chamber), an aerobic treatment tank, a sedimentation tank, and a disinfecting tank, and a flow control unit (HW.
L. And L. W. L. (A part sandwiched between the two) is provided (see Japanese Patent Application Laid-Open No. 4-367933).

【0003】ここで、流量調整部の目的は、槽内へ多量
の汚水が流入した場合であっても汚水処理を安定に行う
こと、すなわち、槽内へ流入した多量の汚水を一時的に
貯留しながら、これを下流側の処理槽へ所定の流速で供
給(送液)して、汚水浄化槽における汚水処理を安定に
行うことである。また、汚水の液面は、通常、最高水位
(HWL)と最低水位(LWL)との間の流量調整域を
上下する。ここで、最低水位よりも下の空間を無駄にす
ることは、高効率化・小型化を狙った汚水浄化槽の設計
では避けなければならない。上記の特開平4−3677
93号公報の例では、流量調整部の下方を嫌気処理槽と
することでこの問題に対処している。
Here, the purpose of the flow rate adjusting section is to stably treat sewage even when a large amount of sewage flows into the tank, that is, to temporarily store a large amount of sewage flowing into the tank. Meanwhile, this is to be supplied (liquid sending) to the downstream processing tank at a predetermined flow rate so as to stably perform the sewage treatment in the sewage purification tank. In addition, the liquid level of the sewage generally rises and falls in a flow rate adjustment region between the highest water level (HWL) and the lowest water level (LWL). Here, wasting space below the minimum water level must be avoided in the design of a sewage purification tank aiming at high efficiency and miniaturization. JP-A-4-3677 mentioned above
In the example of Japanese Patent Publication No. 93, this problem is dealt with by providing an anaerobic treatment tank below the flow rate adjusting unit.

【0004】図6に、他の従来例の汚水浄化槽を示す。
上流側から、嫌気濾床槽2、好気処理槽4、沈殿槽5及
び消毒槽6が配置され、かつ、嫌気処理槽2内の上部の
一画に沈降分離室14が設けられた汚水浄化槽である
(実開昭54−120165号公報)。
FIG. 6 shows another conventional sewage treatment tank.
A sewage purification tank in which an anaerobic filter bed tank 2, an aerobic treatment tank 4, a sedimentation tank 5, and a disinfection tank 6 are arranged from the upstream side, and a sedimentation separation chamber 14 is provided in an upper part of the anaerobic treatment tank 2. (Japanese Utility Model Laid-Open No. 54-120165).

【0005】ここで、嫌気処理槽の目的は、汚水浄化槽
に流入した汚水の固液分離を行ない、上澄液を次槽に送
液し、沈降した固体分(堆積汚泥)を嫌気処理すること
である。この嫌気処理を効率よく進行させるためには、
堆積汚泥に酸素を供給させない、すなわち流入水を堆積
汚泥に接触させないようにしなければならない。また、
流入水ショックによる堆積汚泥の流出を防止しなければ
ならない。
[0005] The purpose of the anaerobic treatment tank is to perform solid-liquid separation of the sewage flowing into the sewage purification tank, send the supernatant to the next tank, and perform anaerobic treatment of the settled solids (sedimented sludge). It is. In order for this anaerobic process to proceed efficiently,
Oxygen must not be supplied to the sediment sludge, i.e. the influent water must not contact the sediment sludge. Also,
Outflow of sediment sludge due to inflow water shock must be prevented.

【0006】上記の実開昭54−120165号公報の
例では、嫌気処理槽の上部に沈降分離室を設けることで
この問題に対処している。
In the example of Japanese Utility Model Application Laid-Open No. 54-120165, this problem is dealt with by providing a sedimentation separation chamber above the anaerobic treatment tank.

【0007】[0007]

【発明が解決しようとする課題】本発明の課題は、流量
調整槽又は嫌気処理槽を備える汚水浄化槽であって、従
来の汚水浄化槽よりも更にその性能を向上させ、コンパ
クトで、汚水を安定に処理できる汚水浄化槽を提供する
こと、あるいはそのような汚水浄化槽に好適に使用され
る流量調整槽又は嫌気処理槽を提供することである。
An object of the present invention is a sewage purification tank having a flow control tank or an anaerobic treatment tank. The performance of the sewage purification tank is improved more than the conventional sewage purification tank, and the sewage purification tank is compact and can stably discharge sewage. An object of the present invention is to provide a sewage purification tank that can be treated, or to provide a flow control tank or an anaerobic treatment tank suitably used for such a sewage purification tank.

【0008】[0008]

【課題を解決するための手段】上記課題を達成するた
め、本発明の汚水浄化槽では次の構成をとった。
In order to achieve the above object, the sewage purifying tank of the present invention has the following configuration.

【0009】すなわち、本発明は、先ず、汚水浄化槽内
に設けられる流量調整槽であって、その最高水位(HW
L)の半分の水位(以下、HWL/2と略す)の水平面
によってこの流量調整槽を有効な上部と有効な下部とに
二分するとき、前記有効な下部の容積は前記有効な上部
の容積(これを100とする。)に対して10%〜90
%(好ましくは15%〜75%、更に好ましくは20%
〜60%)であることを特徴とする流量調整槽3であ
る。
That is, the present invention firstly relates to a flow control tank provided in a sewage purification tank, which has a maximum water level (HW).
L), when the flow control tank is divided into an effective upper part and an effective lower part by a horizontal plane at a half water level (hereinafter, abbreviated as HWL / 2), the effective lower part volume is equal to the effective upper part volume (HWL / 2). 10 to 90%.
% (Preferably 15% to 75%, more preferably 20%
6060%).

【0010】言い換えれば、HWL/2の水平面によっ
て槽を上部と下部に二分するとき、前記下部(底面から
HWL/2まで)の容積は前記上部(HWL/2からH
WLまで)の容積の10%〜90%(好ましくは15%
〜75%、更に好ましくは20%〜60%)となるよう
に、その形状を下に絞り込んだ構造(頭でっかち又は逆
L字状の構造)とした流量調整槽3である。なお、前記
下部の容積が前記上部の容積の10%未満の場合は、エ
アリフトポンプ等の送液ポンプの揚水管を配するスペー
スが狭すぎて、好ましくない。
In other words, when the tank is divided into an upper portion and a lower portion by the horizontal plane of HWL / 2, the volume of the lower portion (from the bottom surface to HWL / 2) is equal to that of the upper portion (from HWL / 2 to HWL / 2).
10% to 90% (preferably 15%) of the volume
流量 75%, more preferably 20% 6060%) is a flow control tank 3 having a structure narrowed downward (a head-shaped or inverted L-shaped structure). If the volume of the lower part is less than 10% of the volume of the upper part, the space for disposing the pumping pipe of the liquid feed pump such as an air lift pump is too small, which is not preferable.

【0011】ここで、流量調整槽3の四周は、通常、汚
水浄化槽の外壁8と一又は二以上の仕切壁9とによって
囲い、その仕切壁9の少なくとも一は途中に屈曲部(絞
り部)9bを有して立設してなる仕切壁が好ましい。
Here, the four circumferences of the flow control tank 3 are usually surrounded by an outer wall 8 of the sewage purification tank and one or more partition walls 9, and at least one of the partition walls 9 has a bent portion (throttle portion) in the middle. A partition wall which is erected with 9b is preferable.

【0012】その場合、前記屈曲部9bは、好ましく
は、最低水位(LWL)又はその近傍の高さに形成す
る。ここで「近傍」とは流量調整槽の最高水位(HW
L)時の水深の概ね20%以内を意味する。
In this case, the bent portion 9b is preferably formed at a minimum water level (LWL) or at a height in the vicinity thereof. Here, “near” means the maximum water level (HW
L) means within approximately 20% of the water depth at the time.

【0013】また、この流量調整槽3における流量調整
装置は、好ましくは、エアリフトポンプ10及び移送管
11からなるものである。
The flow control device in the flow control tank 3 preferably comprises an air lift pump 10 and a transfer pipe 11.

【0014】また、最高水位(HWL)と最低水位(L
WL)との間の槽内には、好ましくは、充填材を充填し
た濾床13を形成させる。
Further, the highest water level (HWL) and the lowest water level (L
WL), a filter bed 13 filled with a filler is preferably formed.

【0015】本発明は、また、汚水浄化槽内に設けられ
る嫌気処理槽、すなわち、その最高水位(HWL)の半
分の水位の水平面によってこの嫌気処理槽を有効な上部
と有効な下部とに二分するとき、前記有効な上部の容積
は前記有効な下部の容積(これを100とする。)に対
して20%〜90%(好ましくは30%〜80%、更に
好ましくは40%〜70%)であることを特徴とする嫌
気処理槽2にも関する。なお、上記有効な上部の容積
が、有効な下部の容積の20%未満では、堆積汚泥がス
カム化して浮上した場合、このスカムを貯留するスペー
スが狭すぎて好ましくない。
The present invention also divides the anaerobic treatment tank into an effective upper part and an effective lower part by an anaerobic treatment tank provided in the sewage purification tank, that is, a horizontal plane at half the level of the highest water level (HWL). At this time, the effective upper volume is 20% to 90% (preferably 30% to 80%, more preferably 40% to 70%) with respect to the effective lower volume (referred to as 100). The present invention also relates to an anaerobic treatment tank 2 having a certain feature. When the effective upper volume is less than 20% of the effective lower volume, when the accumulated sludge is scummed and floats, the space for storing the scum is undesirably too narrow.

【0016】ここで、嫌気処理槽2の四周は、通常、汚
水浄化槽の外壁8と一又は二以上の仕切壁9とによって
囲われ、仕切壁9の少なくとも一は、好ましくは、前記
仕切壁の少なくとも一は途中に屈曲部9bを有して立設
してなる仕切壁である。
Here, the four circumferences of the anaerobic treatment tank 2 are usually surrounded by an outer wall 8 of the sewage purification tank and one or more partition walls 9, and at least one of the partition walls 9 is preferably formed of the partition wall. At least one is a partition wall having a bent portion 9b in the middle and standing upright.

【0017】また、上記嫌気処理槽2の槽内の上部の一
画には沈降分離室を設置し、汚水をこの沈降分離室で受
け、受けた沈降性固形物を沈降分離室の下部から嫌気処
理槽の底部へ落として堆積させる構造が好ましい。
Further, a sedimentation separation chamber is provided in a part of the upper part of the anaerobic treatment tank 2 in which sewage is received in the sedimentation separation chamber, and the received sedimentable solids are anaerobically collected from the lower part of the sedimentation separation chamber. A structure in which the liquid is deposited on the bottom of the processing tank and deposited is preferable.

【0018】本発明は、更に、上記のいずれかの流量調
整槽3と、上記のいずれかの嫌気処理槽2とを、上流側
から任意の順に並設した汚水浄化槽にも関する。
The present invention further relates to a sewage purifying tank in which any one of the flow control tanks 3 and any one of the anaerobic treatment tanks 2 are arranged in any order from the upstream side.

【0019】ここで、流量調整槽3と嫌気処理槽2とは
共通の仕切壁で隔てることが好ましい。
Here, it is preferable that the flow control tank 3 and the anaerobic treatment tank 2 are separated by a common partition wall.

【0020】また、上記流量調整槽3及び嫌気処理槽2
の下流側には、更に好気処理槽及び消毒槽を配置するこ
とが好ましい。
Further, the above-mentioned flow control tank 3 and anaerobic treatment tank 2
It is preferable to further arrange an aerobic treatment tank and a disinfection tank on the downstream side of.

【0021】[0021]

【作用】本発明の流量調整槽3においては、その有効な
下部の容積は、有効な上部の容積よりも小さく、また最
低水位は、通常、屈曲部(絞り部)又はその近傍に存在
するため、最低水位以下の空間、つまり送液不能な無駄
な空間は小さい。そのため流量調整槽がコンパクトにな
る。
In the flow control tank 3 of the present invention, the effective lower volume is smaller than the effective upper volume, and the lowest water level is usually at the bent portion (throttle portion) or in the vicinity thereof. The space below the minimum water level, that is, a wasteful space where liquid cannot be sent, is small. Therefore, the flow control tank becomes compact.

【0022】本発明の嫌気処理槽2においては、その有
効な上部の容積は、有効な下部の容積よりも小さいの
で、汚水の流入時に堆積汚泥に接触する確率が低いまま
に、上澄液を次槽に送液できる。また、流入水ショック
による堆積汚泥の流出も少ない。
In the anaerobic treatment tank 2 of the present invention, the effective upper volume is smaller than the effective lower volume. Liquid can be sent to the next tank. In addition, the outflow of sediment sludge due to the inflow water shock is small.

【0023】[0023]

【発明の実施の形態】以下、発明の実施の形態を添付図
面により更に具体的に説明する。図1は本発明の第一実
施形態の汚水浄化槽の構成略図である。上流側から、流
量調整槽3、嫌気処理槽2、好気処理槽4、沈殿槽5及
び消毒槽6の順に配列されている。流量調整槽3の仕切
はその3面が汚水浄化槽の外壁(外槽)8で兼用され、
残る1面が嫌気処理槽2との間の仕切壁9(9a/9b
/9c)が使われている。流量調整槽3に流入した汚水
は、流量調整槽3に配置された流量調整装置によって、
下流側の嫌気処理槽2に送液される。
Embodiments of the present invention will be described below more specifically with reference to the accompanying drawings. FIG. 1 is a schematic diagram of a configuration of a sewage purification tank according to a first embodiment of the present invention. From the upstream side, the flow control tank 3, the anaerobic treatment tank 2, the aerobic treatment tank 4, the sedimentation tank 5, and the disinfection tank 6 are arranged in this order. As for the partition of the flow control tank 3, its three surfaces are also used as the outer wall (outer tank) 8 of the sewage purification tank,
The remaining one is a partition 9 between the anaerobic treatment tank 2 (9a / 9b).
/ 9c) is used. The sewage flowing into the flow rate adjusting tank 3 is flown by the flow rate adjusting device arranged in the flow rate adjusting tank 3.
The liquid is sent to the anaerobic treatment tank 2 on the downstream side.

【0024】流量調整槽3の仕切壁9は垂直部9a/9
cと屈曲部(絞り部)9bとからなり、その屈曲部(絞
り部)9bのレベルにLWLが形成されている。図には
示さなかったが、最高水位(HWL)の半分の水位(H
WL/2)も屈曲部(絞り部)9b又はその近傍にあ
る。また、図1から分かるように、屈曲部(絞り部)9
bよりも上の部分は嫌気処理槽2側に向かって張り出し
ており(言い換えれば、屈曲部9bよりも下の部分で嫌
気処理槽2が流量調整槽3側に向かって張り出してお
り)、流量調整槽3におけるLWL以下の容積は小さい
(逆に、隣接する嫌気処理槽2の下部の容積が大き
い)。
The partition wall 9 of the flow control tank 3 has a vertical portion 9a / 9.
c and a bent portion (restricted portion) 9b, and LWL is formed at the level of the bent portion (restricted portion) 9b. Although not shown in the figure, the water level (H
WL / 2) is also at or near the bent portion (throttle portion) 9b. In addition, as can be seen from FIG.
The portion above b extends toward the anaerobic treatment tank 2 side (in other words, the anaerobic treatment tank 2 extends below the bent portion 9b toward the flow control tank 3 side), and the flow rate increases. The volume below the LWL in the adjustment tank 3 is small (conversely, the volume below the adjacent anaerobic treatment tank 2 is large).

【0025】また、流量調整槽3の最高水位(HWL)
と最低水位(LWL)の間には充填材を充填した濾床1
3が形成されている。使用される充填材としては、網様
円筒状、骨格様球状、板状ヘチマ様、小円筒状、波板状
等がある。流量調整槽3に濾床13を設けることは必須
ではないが、濾床13があれば、これが汚水中への水没
と空気中への露出とを繰り返し、流量調整槽3中におい
ても好気生物反応を進行させうるので好ましい。この好
気生物反応には、特別な部材及び装置(例えば、散気部
材からの曝気)を必要としない。
The maximum water level (HWL) of the flow control tank 3
Filter bed 1 filled with packing material between the low water level (LWL)
3 are formed. Examples of the filler used include a net-like cylindrical shape, a skeleton-like spherical shape, a plate-like luffa-like shape, a small cylindrical shape, and a corrugated shape. Although it is not essential to provide the filter bed 13 in the flow control tank 3, if the filter bed 13 is provided, the filter bed 13 repeats submersion in sewage and exposure to the air. This is preferable because the reaction can proceed. This aerobic reaction does not require special components and equipment (eg, aeration from diffuser components).

【0026】ここで、流量調整装置は、汚水揚水用のエ
アリフトポンプ10と移送管11とで構成され、分水計
量マス12も付設されているものである。エアリフトポ
ンプの代わりに、汎用の電動ポンプを使うこともでき
る。
Here, the flow rate adjusting device is composed of an air lift pump 10 for pumping sewage and a transfer pipe 11, and is also provided with a water distribution measuring mass 12. A general-purpose electric pump can be used instead of the air lift pump.

【0027】次に、汚水の流れを図1で説明する。汚水
は、先ず、流入口1から流量調整槽3に入り、エアリフ
トポンプ10により揚水され、分水計量マス12によっ
て分水計量後、移送管11を経て嫌気処理槽2へ送液さ
れる。嫌気処理槽2では、夾雑物の除去と共に汚水は嫌
気分解を受け、次に好気処理槽4へ移流する。好気処理
槽4では、曝気により有機物の酸化・分解とアンモニア
の硝化が行われ、沈殿槽5へと移流する。そして、消毒
槽6で滅菌され、流出口7から放流される。
Next, the flow of sewage will be described with reference to FIG. First, the sewage enters the flow control tank 3 from the inflow port 1, is pumped by the air lift pump 10, is weighed by the weighing mass 12, and is sent to the anaerobic treatment tank 2 via the transfer pipe 11. In the anaerobic treatment tank 2, the sewage undergoes anaerobic decomposition together with the removal of contaminants, and then flows to the aerobic treatment tank 4. In the aerobic treatment tank 4, oxidation and decomposition of organic matter and nitrification of ammonia are performed by aeration, and the mixture is transferred to the precipitation tank 5. Then, it is sterilized in the disinfection tank 6 and discharged from the outlet 7.

【0028】図2は本発明の第二実施形態の汚水浄化槽
の構成略図である。図1の汚水浄化槽と異なる点は、流
量調整槽3と嫌気処理槽2との順序を逆に配置させた点
である。すなわち、第1槽を嫌気処理槽2とし、第2槽
を流量調整槽3とし、第3槽以降は図1と同様で、好気
処理槽4、沈殿槽5及び消毒槽6の順で配列されてい
る。嫌気処理槽2の仕切はその3面が汚水浄化槽の外壁
8(外槽)で兼用され、残る1面が流量調整槽3との間
の仕切壁9(9a/9b/9c)である。
FIG. 2 is a schematic view of the configuration of a sewage purification tank according to a second embodiment of the present invention. The difference from the sewage purification tank in FIG. 1 is that the flow control tank 3 and the anaerobic treatment tank 2 are arranged in reverse order. That is, the first tank is an anaerobic treatment tank 2, the second tank is a flow control tank 3, and the third and subsequent tanks are the same as in FIG. 1, arranged in the order of an aerobic treatment tank 4, a sedimentation tank 5 and a disinfection tank 6. Have been. The three walls of the anaerobic treatment tank 2 are also used as the outer wall 8 (outer tank) of the sewage purification tank, and the remaining one is a partition wall 9 (9a / 9b / 9c) between the anaerobic treatment tank 2 and the flow control tank 3.

【0029】嫌気処理槽2の上部に比べて下部の容積が
大きいと、嫌気処理槽2の底部に堆積される汚泥(堆積
汚泥)は液の流れの影響を受けにくく、堆積汚泥が次槽
へ流出することなくそこで嫌気生物反応が進行しやす
い。堆積汚泥の嫌気生物反応が進行すると堆積汚泥が消
化されるため、堆積汚泥の貯留に必要な容量は小さくて
すむ。
When the volume of the lower part is larger than that of the upper part of the anaerobic treatment tank 2, the sludge (sedimented sludge) deposited on the bottom of the anaerobic treatment tank 2 is hardly affected by the flow of the liquid, and the accumulated sludge is transferred to the next tank. The anaerobic reaction easily proceeds there without spilling. As the anaerobic reaction of the sedimentary sludge proceeds, the sedimentary sludge is digested, so that the capacity required for storing the sedimentary sludge is small.

【0030】図2における汚水の流れは、先ず、汚水原
水が流入口1から嫌気処理槽2に入り、固液分離され、
嫌気処理を受けて流量調整槽3へ移流する。流量調整槽
3に入った汚水は、エアリフトポンプ10により揚水さ
れ、移送管11を経て好気処理槽4へ送液される。好気
処理槽4以降は、図1の説明と同様である。
In the flow of sewage in FIG. 2, raw sewage first enters an anaerobic treatment tank 2 from an inlet 1 and is separated into solid and liquid.
After being subjected to the anaerobic treatment, it is transferred to the flow control tank 3. The sewage entering the flow control tank 3 is pumped by an air lift pump 10 and sent to the aerobic treatment tank 4 via a transfer pipe 11. The process after the aerobic treatment tank 4 is the same as the description of FIG.

【0031】図3は、本発明の第三実施形態の汚水浄化
槽の構成略図である。図2の汚水浄化槽と異なる点は、
嫌気処理槽2の上部に沈降分離室14が設置されている
点である。
FIG. 3 is a schematic diagram of a configuration of a sewage purification tank according to a third embodiment of the present invention. The difference from the sewage treatment tank of FIG.
The point is that a sedimentation separation chamber 14 is provided above the anaerobic treatment tank 2.

【0032】沈降分離室14は2枚の区画板15(15
a/15b)から構成されており、側面から見ると、こ
の区画板15の一方の15aが「く」の字型、他方の1
5bが逆「く」の字型であり、互いに向き合って下方が
上方より狭まっている漏斗形状をなしている。そして、
他方の15bの下端は、一方の15aの下端よりも下側
に入り込む形状になっているため、堆積汚泥がスカム化
して浮上しても、この沈降分離室14内に浮上すること
はない。
The sedimentation separation chamber 14 has two partition plates 15 (15
a / 15b), and when viewed from the side, one 15a of the partitioning plate 15 has a
5b is an inverted "C" shape, and has a funnel shape in which the lower part is narrower than the upper part facing each other. And
Since the lower end of the other 15b is shaped to enter below the lower end of the one 15a, even if the deposited sludge is scummed and floats, it does not float in the settling / separation chamber 14.

【0033】嫌気処理槽2の上部に沈降分離室14を設
置することにより、さらに、堆積汚泥は液の流れの影響
を受けにくくなり、堆積汚泥が次槽へ流出することなく
そこで嫌気生物反応が進行する。
By installing the sedimentation separation chamber 14 above the anaerobic treatment tank 2, the sedimentary sludge is hardly affected by the flow of the liquid, and the anaerobic reaction is performed without the sedimentation sludge flowing out to the next tank. proceed.

【0034】なお、図1〜図3の例では、流量調整槽3
を囲う四周の仕切壁の少なくとも一を垂直に立ち上がる
垂直部と斜めに立ち上がる屈曲部とからなるものとした
が、これに代わり、図4のように、平板状又は略平板状
の仕切を斜めに配置して(断面形状は略台形となる)、
下部の容積を上部の容積の10%〜90%とすることも
できる。この場合、上記したような明確な垂直部及び屈
曲部(絞り部)は存在しない。
Incidentally, in the example of FIGS.
At least one of the four circumferential partition walls surrounding the vertical section and the bent section that rises obliquely, but instead of this, as shown in FIG. Place it (the cross-sectional shape will be approximately trapezoidal)
The lower volume may be 10% to 90% of the upper volume. In this case, there are no clear vertical portions and bent portions (throttle portions) as described above.

【0035】[0035]

【発明の効果】本発明の流量調整槽によれば、最低水位
よりも下の空間を無駄なく有効に利用できる。最高水位
と最低水位の間に濾床を設ければ、特別な部材及び装置
(例えば、散気部材からの曝気)を設けることなく、そ
こで好気生物反応も促進させることができる。本発明の
嫌気処理槽によれば、槽底の堆積汚泥が汚水の流入によ
る液乱れの影響を受けにくく、また次槽に流出しにく
く、嫌気生物反応も進みやすい。また、嫌気処理槽の上
部に沈降分離室を設置すれば、更に、槽底の堆積汚泥は
液流の影響を受けにくく、次槽に流出しにくく、嫌気生
物反応も進みやすい。本発明の汚水浄化槽によれば、そ
の性能は更に向上し、コンパクトで、汚水を安定に処理
できる。
According to the flow regulating tank of the present invention, the space below the minimum water level can be effectively used without waste. Providing a filter bed between the highest and lowest water levels can also promote aerobic reactions therewithout having to provide special components and equipment (eg, aeration from a diffuser). ADVANTAGE OF THE INVENTION According to the anaerobic treatment tank of this invention, the sediment sludge of a tank bottom is hard to be affected by the liquid turbulence by the inflow of sewage, it is hard to flow out to the next tank, and an anaerobic biological reaction also advances easily. If a sedimentation separation chamber is installed in the upper part of the anaerobic treatment tank, the sediment sludge at the bottom of the tank is hardly affected by the liquid flow, hardly flows out to the next tank, and the anaerobic reaction easily proceeds. According to the sewage treatment tank of the present invention, the performance is further improved, and the sewage treatment tank can be compactly treated stably.

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

【図1】本発明の第一実施形態の汚水浄化槽の構成略図
(正面から見た図)である。
FIG. 1 is a schematic diagram (viewed from the front) of a sewage purification tank according to a first embodiment of the present invention.

【図2】本発明の第二実施形態の汚水浄化槽の構成略図
(正面から見た図)である。
FIG. 2 is a schematic structural view (view from the front) of a sewage purification tank according to a second embodiment of the present invention.

【図3】本発明の第三実施形態の汚水浄化槽の構成略図
で、(a)は正面から見た図、(b)は嫌気処理槽部を
側面から見た図である。
FIGS. 3A and 3B are schematic diagrams of a configuration of a sewage purification tank according to a third embodiment of the present invention, in which FIG. 3A is a front view and FIG. 3B is a side view of an anaerobic treatment tank.

【図4】本発明の第四実施形態の汚水浄化槽の構成略図
(正面から見た図)である。
FIG. 4 is a schematic diagram (viewed from the front) of a configuration of a sewage purification tank according to a fourth embodiment of the present invention.

【図5】従来例の汚水浄化槽の構成略図である。FIG. 5 is a schematic diagram of a configuration of a conventional sewage purification tank.

【図6】他の従来例の汚水浄化槽の構成略図である。FIG. 6 is a schematic diagram of the configuration of another conventional sewage purification tank.

【符号の説明】[Explanation of symbols]

1:流入口 2:嫌気処理槽 3:流量調整槽 4:好気処理槽 5:沈殿槽 6:消毒槽 7:流出口 8:汚水浄化槽の外壁(外槽) 9:仕切壁 9a,9c:仕切壁の垂直部 9b:仕切壁の屈曲部(絞り部) 10:エアリフトポンプ 11:移送管 12:分水計量マス 13:濾床 14:沈降分離室 15a,15b:区画板 16: 散気部材(散気管) 17:濾床 1: Inlet 2: Anaerobic treatment tank 3: Flow control tank 4: Aerobic treatment tank 5: Sedimentation tank 6: Disinfection tank 7: Outlet 8: Outer wall (outer tank) of sewage purification tank 9: Partition wall 9a, 9c: Vertical part of partition wall 9b: Bent part of partition wall (throttle part) 10: Air lift pump 11: Transfer pipe 12: Water separation measuring mass 13: Filter bed 14: Settling separation chamber 15a, 15b: Partition plate 16: Air diffuser (Aeration tube) 17: Filter bed

Claims (11)

【特許請求の範囲】[Claims] 【請求項1】汚水浄化槽内に設けられる流量調整槽であ
って、その最高水位(HWL)の半分の水位の水平面に
よってこの流量調整槽を有効な上部と有効な下部とに二
分するとき、前記有効な下部の容積は前記有効な上部の
容積に対して10%〜90%である流量調整槽。
1. A flow control tank provided in a sewage purifying tank, wherein the flow control tank is divided into an effective upper part and an effective lower part by a horizontal plane at a half level of the highest water level (HWL). The flow regulating tank, wherein the effective lower volume is 10% to 90% of the effective upper volume.
【請求項2】その四周は汚水浄化槽の外壁と一又は二以
上の仕切壁とによって囲われ、前記仕切壁の少なくとも
一は途中に屈曲部を有して立設してなるものである、請
求項1の流量調整槽。
2. The four circumferences are surrounded by an outer wall of a sewage purification tank and one or more partition walls, and at least one of the partition walls is provided upright with a bent portion in the middle. Item 1. The flow control tank of Item 1.
【請求項3】屈曲部は最低水位(LWL)又はその近傍
の高さに形成されている、請求項2の流量調整槽。
3. The flow rate adjusting tank according to claim 2, wherein the bent portion is formed at a height at or near the lowest water level (LWL).
【請求項4】流量調整槽における流量調整装置は、エア
リフトポンプ及び移送管からなるものである、請求項1
〜3のいずれかの流量調整槽。
4. The flow control device in the flow control tank comprises an air lift pump and a transfer pipe.
3. The flow control tank according to any one of (1) to (3).
【請求項5】槽内の最高水位と最低水位との間に充填材
を充填した濾床が形成されている、請求項1〜4のいず
れかの流量調整槽。
5. The flow control tank according to claim 1, wherein a filter bed filled with a filler is formed between the highest water level and the lowest water level in the tank.
【請求項6】汚水浄化槽内に設けられる嫌気処理槽であ
って、その最高水位(HWL)の半分の水位の水平面に
よってこの嫌気処理槽を有効な上部と有効な下部とに二
分するとき、前記有効な上部の容積は前記有効な下部の
容積に対して20%〜90%である嫌気処理槽。
6. An anaerobic treatment tank provided in a sewage purification tank, wherein said anaerobic treatment tank is divided into an effective upper part and an effective lower part by a horizontal plane at a half level of the highest water level (HWL). An anaerobic treatment tank wherein the effective upper volume is 20% to 90% of the effective lower volume.
【請求項7】その四周は汚水浄化槽の外壁と一又は二以
上の仕切壁とによって囲われ、前記仕切壁の少なくとも
一は途中に屈曲部を有して立設してなるものである、請
求項6の嫌気処理槽。
7. The four circumferences are surrounded by an outer wall of a sewage treatment tank and one or more partition walls, and at least one of the partition walls is provided upright with a bent portion in the middle. Item 6. Anaerobic treatment tank.
【請求項8】その槽内の上部の一画には沈降分離室が設
置されてなる請求項6又は7の嫌気処理槽。
8. The anaerobic treatment tank according to claim 6, wherein a sedimentation separation chamber is provided in an upper part of the tank.
【請求項9】請求項1〜5のいずれかの流量調整槽と、
請求項6〜8のいずれかの嫌気処理槽とが、上流側から
任意の順に並設されている汚水浄化槽。
9. The flow control tank according to claim 1, wherein:
A sewage purification tank in which the anaerobic treatment tank according to any one of claims 6 to 8 is arranged in any order from the upstream side.
【請求項10】流量調整槽と嫌気処理槽とは共通の仕切
壁で隔てられている、請求項9の汚水浄化槽。
10. The sewage treatment tank according to claim 9, wherein the flow control tank and the anaerobic treatment tank are separated by a common partition wall.
【請求項11】下流側に更に好気処理槽及び消毒槽が配
置されている、請求項9又は10の汚水浄化槽。
11. The sewage treatment tank according to claim 9, wherein an aerobic treatment tank and a disinfection tank are further disposed downstream.
JP2000319505A 2000-06-30 2000-10-19 Wastewater septic tank Expired - Fee Related JP4712953B2 (en)

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002159804A (en) * 2000-11-24 2002-06-04 Hitachi Chem Co Ltd Sedimentation and separation chamber, sludge concentration tank and sewage cleaning tank equipped therewith
JP2008119562A (en) * 2006-11-08 2008-05-29 Fuji Clean Kogyo Kk Water treating device and water treatment method
CN114853171A (en) * 2022-05-17 2022-08-05 成都市兴蓉环境股份有限公司 Adjustable rural sewage treatment method

Citations (18)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS51126967A (en) * 1975-04-17 1976-11-05 Fmc Corp High pressure thermohydrilysis for decomposing triazines in acidic waste streams
JPS52151674A (en) * 1976-06-14 1977-12-16 Takasago Thermal Engineering Method of pelletizing high viscous fluid
JPS54120165A (en) * 1978-03-08 1979-09-18 Hitachi Kiden Kogyo Ltd Article holding method for equal-capacity separate winch type grab bucket crane
JPS559240A (en) * 1978-06-30 1980-01-23 Matsushita Electric Works Ltd Electronic desk calculator for illumination calculation
JPS55111596A (en) * 1979-02-19 1980-08-28 Nippon Telegraph & Telephone Mechanical excavation shielding
JPS59131294A (en) * 1983-01-17 1984-07-28 Victor Co Of Japan Ltd Speaker diaphragm
JPH02107396A (en) * 1988-10-18 1990-04-19 Kubota Ltd Waste water purification tank
JPH0437596A (en) * 1990-06-01 1992-02-07 Toshiba Corp Printed wiring board device
JPH04200792A (en) * 1990-11-30 1992-07-21 Zenkoku Jiyoukasou Kogyo Kumiai Purifying tank for household small combined treatment
JPH04317796A (en) * 1991-04-17 1992-11-09 Nishihara Neo Kogyo Kk Purifying vessel for sewage and its driving method
JPH04367793A (en) * 1991-06-14 1992-12-21 Nishihara Neo Kogyo Kk Flow adjustment of purification tank
JPH07275877A (en) * 1994-04-13 1995-10-24 Suiken Kiko:Kk Small-scaled combined purifying tank
JPH07308683A (en) * 1994-05-16 1995-11-28 Toto Ltd Septic tank
JPH0824880A (en) * 1994-07-20 1996-01-30 Miyoshi Shokai:Kk Combined treatment and purification tank
JPH08323378A (en) * 1995-06-02 1996-12-10 Hitachi Chem Co Ltd Sewage septic tank
JPH1034176A (en) * 1996-07-29 1998-02-10 Matsushita Electric Works Ltd Purifying tank
JPH10296251A (en) * 1997-04-28 1998-11-10 Sekisui Chem Co Ltd Method for regulating sludge in sewage treatment tank
JP2001079576A (en) * 1999-09-17 2001-03-27 Kubota Corp Private sewage treatment tank

Family Cites Families (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS51126967U (en) * 1975-04-09 1976-10-14
JPS5735440Y2 (en) * 1975-06-05 1982-08-05
JPS5541352Y2 (en) * 1976-05-13 1980-09-27
JPS5626879Y2 (en) * 1978-02-07 1981-06-25
JPS5627996Y2 (en) * 1978-06-30 1981-07-03
JPS55111596U (en) * 1979-01-29 1980-08-05
JPS59131294U (en) * 1983-02-22 1984-09-03 株式会社西原環境衛生研究所 Sewage purification equipment
JP2525123Y2 (en) * 1990-06-15 1997-02-05 株式会社クボタ Sewage septic tank
JPH0437596U (en) * 1990-07-24 1992-03-30

Patent Citations (18)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS51126967A (en) * 1975-04-17 1976-11-05 Fmc Corp High pressure thermohydrilysis for decomposing triazines in acidic waste streams
JPS52151674A (en) * 1976-06-14 1977-12-16 Takasago Thermal Engineering Method of pelletizing high viscous fluid
JPS54120165A (en) * 1978-03-08 1979-09-18 Hitachi Kiden Kogyo Ltd Article holding method for equal-capacity separate winch type grab bucket crane
JPS559240A (en) * 1978-06-30 1980-01-23 Matsushita Electric Works Ltd Electronic desk calculator for illumination calculation
JPS55111596A (en) * 1979-02-19 1980-08-28 Nippon Telegraph & Telephone Mechanical excavation shielding
JPS59131294A (en) * 1983-01-17 1984-07-28 Victor Co Of Japan Ltd Speaker diaphragm
JPH02107396A (en) * 1988-10-18 1990-04-19 Kubota Ltd Waste water purification tank
JPH0437596A (en) * 1990-06-01 1992-02-07 Toshiba Corp Printed wiring board device
JPH04200792A (en) * 1990-11-30 1992-07-21 Zenkoku Jiyoukasou Kogyo Kumiai Purifying tank for household small combined treatment
JPH04317796A (en) * 1991-04-17 1992-11-09 Nishihara Neo Kogyo Kk Purifying vessel for sewage and its driving method
JPH04367793A (en) * 1991-06-14 1992-12-21 Nishihara Neo Kogyo Kk Flow adjustment of purification tank
JPH07275877A (en) * 1994-04-13 1995-10-24 Suiken Kiko:Kk Small-scaled combined purifying tank
JPH07308683A (en) * 1994-05-16 1995-11-28 Toto Ltd Septic tank
JPH0824880A (en) * 1994-07-20 1996-01-30 Miyoshi Shokai:Kk Combined treatment and purification tank
JPH08323378A (en) * 1995-06-02 1996-12-10 Hitachi Chem Co Ltd Sewage septic tank
JPH1034176A (en) * 1996-07-29 1998-02-10 Matsushita Electric Works Ltd Purifying tank
JPH10296251A (en) * 1997-04-28 1998-11-10 Sekisui Chem Co Ltd Method for regulating sludge in sewage treatment tank
JP2001079576A (en) * 1999-09-17 2001-03-27 Kubota Corp Private sewage treatment tank

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002159804A (en) * 2000-11-24 2002-06-04 Hitachi Chem Co Ltd Sedimentation and separation chamber, sludge concentration tank and sewage cleaning tank equipped therewith
JP2008119562A (en) * 2006-11-08 2008-05-29 Fuji Clean Kogyo Kk Water treating device and water treatment method
CN114853171A (en) * 2022-05-17 2022-08-05 成都市兴蓉环境股份有限公司 Adjustable rural sewage treatment method

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