JP4187889B2 - Aerobic filter bed tank and septic tank - Google Patents
Aerobic filter bed tank and septic tank Download PDFInfo
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- JP4187889B2 JP4187889B2 JP32091499A JP32091499A JP4187889B2 JP 4187889 B2 JP4187889 B2 JP 4187889B2 JP 32091499 A JP32091499 A JP 32091499A JP 32091499 A JP32091499 A JP 32091499A JP 4187889 B2 JP4187889 B2 JP 4187889B2
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- 238000002347 injection Methods 0.000 claims description 27
- 239000007924 injection Substances 0.000 claims description 27
- 238000005406 washing Methods 0.000 claims description 22
- 239000010865 sewage Substances 0.000 claims description 18
- 238000001914 filtration Methods 0.000 claims description 15
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 12
- 238000006243 chemical reaction Methods 0.000 claims description 10
- 239000007788 liquid Substances 0.000 claims description 8
- 238000004659 sterilization and disinfection Methods 0.000 claims description 6
- 230000000249 desinfective Effects 0.000 claims description 5
- 239000000126 substance Substances 0.000 claims 1
- 238000005273 aeration Methods 0.000 description 18
- 238000004140 cleaning Methods 0.000 description 16
- 239000000969 carrier Substances 0.000 description 10
- 239000002351 wastewater Substances 0.000 description 8
- 238000010586 diagram Methods 0.000 description 5
- 238000009792 diffusion process Methods 0.000 description 5
- 238000000746 purification Methods 0.000 description 5
- 229910052760 oxygen Inorganic materials 0.000 description 4
- MYMOFIZGZYHOMD-UHFFFAOYSA-N oxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 4
- 239000001301 oxygen Substances 0.000 description 4
- 239000000463 material Substances 0.000 description 3
- 238000005192 partition Methods 0.000 description 2
- 238000011144 upstream manufacturing Methods 0.000 description 2
- 210000003608 Feces Anatomy 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- QGZKDVFQNNGYKY-UHFFFAOYSA-N ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 239000010871 livestock manure Substances 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 230000001954 sterilising Effects 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
Description
【0001】
【発明の属する技術分野】
本発明は、好気濾床槽及び汚水浄化槽並びに好気濾床槽の濾過層の洗浄方法に関し、更に詳しくは、屎尿や雑排水等の汚水処理に好適に用いられる好気濾床槽、及びその好気濾床槽を備える汚水浄化槽、並びにその好気濾床槽の濾過層の洗浄方法に関するものである。
【0002】
【従来の技術】
一般によく知られた汚水浄化槽は、通常、仕切壁で仕切られた嫌気処理槽(第一室及び第二室)、好気処理槽(好気濾床槽)、沈殿槽(又は処理水槽)及び消毒槽等からなる。流入口から供給された汚水は、嫌気処理槽第一室から下流へ順次移流され、最後に消毒槽で消毒されて、流出口から外部へ放流される。
【0003】
汚水浄化槽における好気濾床槽の構造は、従来、いくつか知られているが、出願人は先に、図6に示すように、多孔性板材(図示せず)を間に挟んで好気濾床槽を上濾床(生物反応層、又はRゾーン)1と下濾床(濾過層、又はFゾーン)2とに分け、濾床層に粒状担体を充填し、それぞれの濾床の下に散気管4a,4bを設置するとともに、好気濾床槽Cの下部に移送ポンプ(エアリフトポンプ)5の液吸込口となる洗浄排水引抜口5aを設置する構造を提案した(特開平9−248584号公報)。この汚水浄化槽における好気濾床槽Cの洗浄時には、2つの濾床の下の散気管4a,4bから曝気した後に、移送ポンプ(エアリフトポンプ)5を介して好気濾床槽下部の洗浄排水引抜口5aから洗浄排水を引き抜き、嫌気処理槽(第一室)の上部へ移送させると共に、その移送に伴って押し出された嫌気処理槽(第二室)からの移流水を好気濾床槽Cの上濾床へ導入している。
【0004】
そして、その洗浄の際に曝気によって下濾床を均一に流動させるとともに、下濾床に捕捉されていた浮遊性懸濁物(生物膜剥離汚泥ともいう。以下、SSと略す。)を剥離させ、移送ポンプ(エアリフトポンプ)5を介して洗浄排水引抜口5aから嫌気処理槽(第一室)へ洗浄排水として返送している。このとき、引抜かれる洗浄排水の量は、好気濾床槽C底面の面積とその底面を通過する洗浄排水の速度によって決まるものである。
【0005】
【発明が解決しようとする課題】
しかし、好気濾床槽Cにおける下濾床2の下端とその底面との距離が離れている場合、洗浄排水引抜口5aから遠いSSは洗浄排水引抜口5aへ吸引される力よりも沈降力が勝って、底面上に沈降する傾向となる。また、沈降したSSは、その場所に留まって嫌気化し、汚水処理の性能に悪い影響を及ぼす。本発明は、このような問題を解消しようとするものであり、その目的とするところは、下濾床2の下端と濾床底面との距離が離れている場合であっても、好気濾床槽Cの底にSSが留まらず、汚水処理の性能を良好に維持できる好気濾床槽及び汚水浄化槽、あるいは好気濾床槽の下濾床(濾過層)の洗浄方法を提供することである。
【0006】
【課題を解決するための手段】
上記目的を達成するため、本発明の好気濾床槽では次の構成をとった。すなわち、本発明は、第1に、生物反応層1と濾過層2の2つの濾床を有し、各濾床の下(下部又は下方を意味する。以下、同じ。)にそれぞれ散気管4a,4bを有する好気濾床槽Cであって、前記濾過層2の下方の散気管4bの下方であって、前記濾過層と前記好気濾床槽の底面との間に更に空気噴射管6が配置されていることを特徴とする、好気濾床槽Cである。
【0007】
ここで、生物反応層1と濾過層2の2つの濾床は、生物反応層1を前濾床とし濾過層2を後濾床として横に並べて配置することも可能であるが、好ましくは、生物反応層1を上濾床とし濾過層2を下濾床として縦に配置された(すなわち、二重床を形成する。)好気濾床槽Cである。
【0008】
また、散気管4bの下方に配置される空気噴射管6は、底面に沈降したSSを十分舞い上げるよう、噴射される空気流が水平流(すなわち、底面と並行な流れ)を形成する空気噴射口6aをもつ管とする。また、空気噴射口6aの所在部位は、好気濾床槽Cの底面の中心部もしくは中心部近辺で、底面に接するように(あるいは、底面から50mm以上を離さない位置に)することが好ましい。
【0009】
また、上記好気濾床槽Cにおいて、濾過層2の下方か、あるいは濾過層2の上方もしくは生物反応層1の下方のいずれかには、更に移送ポンプ(通常は、エアリフトポンプ)5の液吸込口となる洗浄排水引抜口5aが配置されていることが好ましい。
【0010】
本発明は、第2に、上記した好気濾床槽を備える汚水浄化槽、すなわち、上流から順に、嫌気濾床槽(第一室A及び第二室B)、上記した好気処理槽C、沈殿槽(又は処理水槽)D及び消毒槽Eを備えることを特徴とする汚水浄化槽である。
【0013】
【作用】
好気濾床槽の下濾床の洗浄時、その下濾床の液は散気管からの上下方向の曝気流とともに、空気噴射管(その空気噴射口)からの水平方向の噴射流によって効率よく撹拌される。そして、液中に存在するSSは底面に沈降することなく洗浄排水引抜口から引き抜かれ、移送ポンプ(エアリフトポンプ)を介して嫌気濾床槽第一室へ返送される(図1参照)。
【0014】
【発明の実施の形態】
以下、発明の実施の形態を図面により更に具体的に説明する。
図1は本発明に係る一例の好気濾床槽の概略構成図であり、図2は図1の好気濾床槽を底面下方から見上げた図である。これらの図には、洗浄時の曝気流(矢印)も付記した。
好気濾床槽Cには生物担体(生物の棲み家となる。接触材、濾材とも呼ばれる)を充填して濾床を形成させる。この濾床は、上濾床(生物反応層)1と下濾床(濾過層)2とに分けられ、上濾床1と下濾床2との間に通水性の多孔性板材(生物担体を通さないが水や空気を自由に通すもの)を挟んで区画する。また、上濾床1の上にも下濾床2の下にも、それぞれ通水性の多孔性板材を配置し、生物担体が流出しないように保持している。
【0015】
上濾床1の下に散気管4aを設け、下濾床2の下にも散気管4bを設け、また、好気濾床槽Cの下部には移送ポンプ(エアリフトポンプ)5の液吸込口となる洗浄排水引抜口5aが設けられている。
更に、散気管4bの下方には空気噴射口6aを有する空気噴射管6(空気噴射用横管6b)が配置され、底面と並行な空気噴射流をつくることができる。なお、先の散気管4a,4bに穿けられる散気孔は、通常、SS等の沈降物による詰まりを防止するため、管の下部に設けるのが普通である。
【0016】
好気濾床槽Cにおける水処理は、上濾床(生物反応層)1においては、被処理水は、散気管4aから曝気・導入される空気(溶存酸素)の存在下に、生物担体中に生息する好気性微生物によって好気処理される。すなわち、ここでは主として、生物化学的酸素要求量(BOD)の酸化・分解と、アンモニアの硝化が進行する。
また、下濾床2においては、通常の運転(洗浄時以外の運転)では散気管4bからは曝気しない。上濾床1からの流下液の持ち越み酸素(溶存酸素)を消費しつつ引き続き好気処理すると共に、静止状態の生物担体を利用してSSを効率よく捕捉(濾過)する機能がある。それゆえ、下濾床2は、捕捉されたSSによって徐々に詰まってくる。この詰まりを解除するため、好気濾床槽C(特に、下濾床2)を定期的に(通常は、1日に1回で、1〜30分間程度、夜間)洗浄する。この洗浄の際は、下濾床2の下に設けている散気管4bから曝気すると共に、それと同時に、その空気噴射口6aからも曝気し、生物担体からSSを遊離させる。前記曝気と同時に、又はその曝気の後に、SSを含んだ洗浄排水を洗浄排水引抜口5aから引き抜く。この引き抜きには、エアリフトポンプが好ましく用いられる。
【0017】
空気噴射管6の空気噴射口6aからの曝気は、通常、散気管4bからの曝気(すなわち、洗浄・吸引)と同時に行うが、散気管4bからの曝気に先立って行ってもよい。その場合、前日の洗浄時に排出されずに底面に沈降していたSSを、予め舞き上げ、これを散気管4bからの曝気(すなわち、洗浄・吸引)と共に引き抜くわけである。
また、洗浄中の上濾床1の散気管4aからの曝気(すなわち、連続曝気)は、その間、一時停止させてもよい。
【0018】
洗浄は、タイマー等の使用によって自動的に行うことができる。時刻、時間及び頻度は、任意に設定できることが好ましい。
【0019】
また、図1及び図2に示したような空気噴射管に限らず、種々の形状の空気噴射管を使用できる。図3及び図4に、他の例の空気噴射管及び好気濾床槽を示した。いずれの図も好気濾床槽を底面下方から見上げた図で、図3は空気噴射管が途中で分枝している例、図4は先端が開放されているほかに管の途中で小穴があけられている例である。
【0020】
なお、図1〜図4の例は、上濾床と下濾床との上下の2層構造の例としたが、上下ではなく横2列の直列構造とすることも可能である。
【0021】
図5は、本発明の好気濾床槽を利用した汚水浄化槽(概略構成図)の例である。
この汚水浄化槽は、上流側から、嫌気濾床槽第一室A、嫌気濾床槽第二室B、好気濾床槽C(上濾床1及び下濾床2を有する)、処理水槽D、消毒槽Eの各槽に分画されている。
嫌気濾床槽第一室A及び嫌気濾床槽第二室Bには、網様円筒状濾材等の生物担体を充填することができ、好気濾床槽Cの上濾床1及び下濾床2には、スポンジ担体等の生物担体を充填することができる。
処理水槽Dには、好気濾床槽Cの下濾床2を洗浄する際に必要なエアリフトポンプ5が設けられ、エアリフトポンプの液吸込口は好気濾床槽C下部に設けられている。ここから引き抜かれた洗浄排水は、嫌気濾床槽第一室Aへ返送される構造である。また、処理水槽Dには、空気噴射用縦管6cも配置されている。
【0022】
洗浄の動作の例は、次の通り。汚水浄化槽の通常運転時には、上濾床1の下方の散気管4aに空気を供給し、下濾床2の下方の散気管4b及びエアリフトポンプ5には空気を供給しない。洗浄時には、下濾床2の下方の散気管4b、エアリフトポンプ5及び空気噴射管6に空気を供給する。
【0023】
下濾床2の下部の空気噴射管6は次のように設置する。好気濾床槽Cの下部で処理水槽D寄りの好気濾床槽側壁面に移流口7を設け、この移流口の上部には洗浄排水引抜口5aを配置し、この洗浄排水引抜口5aの下方に処理水槽D側から底面を這わせるように空気噴射用横管6bを差し込む。その際、好気濾床槽C底面の中心部に空気噴射口6aがくるようにする。空気噴射管6に空気を供給し、その空気噴射口6aから空気を吐出させると、下濾床2の下方及び好気濾床槽Cの底面付近が撹拌され、SSは底に留まることなく洗浄排水と共に洗浄排水引抜口5aから引き抜かれる。
【0024】
本発明の好気濾床槽又は汚水浄化槽によれば、下濾床の下端と好気濾床槽底面との距離が離れている場合であっても、好気濾床槽の底にSSが留まることが少ない。
【図面の簡単な説明】
【図1】本発明に係る好気濾床槽の概略構成図。洗浄時の曝気流も矢印で付記した。
【図2】図1の好気濾床槽を底面下方から見上げた図。矢印は、空気噴射口からの噴射流を示す。
【図3】本発明に係る他の例の好気濾床槽を底面下方から見上げた図。空気噴射管は途中で分枝している例。
【図4】本発明に係る別の例の好気濾床槽を底面下方から見上げた図。空気噴射管の先端が開放されているほかに管の途中で小穴があけられている。
【図5】本発明に係る汚水浄化槽の概略構成図。
【図6】従来例の好気濾床槽の概略構成図。
【符号の説明】
1:上濾床(生物反応層) 2:下濾床(濾過層)
3: 仕切壁
4a:散気管 4b:散気管
5:エアリフトポンプ
5a:洗浄排水引抜口(エアリフトポンプ吸込口)
5b:エアリフトポンプ揚水管
6:空気噴射管 6a:空気噴射口
6b:空気噴射用横管 6c:空気噴射用縦管
7:移流口
A:嫌気濾床槽第一室
B:嫌気濾床槽第二室
C:好気濾床槽
D:処理水槽
E:消毒槽[0001]
BACKGROUND OF THE INVENTION
The present invention relates to an aerobic filter bed tank, a sewage purification tank, and a method for cleaning the filtration layer of the aerobic filter bed tank, and more specifically, an aerobic filter bed tank suitably used for sewage treatment such as manure and miscellaneous waste water, and The present invention relates to a sewage purification tank equipped with the aerobic filter bed tank and a method for cleaning the filtration layer of the aerobic filter bed tank.
[0002]
[Prior art]
Generally well-known sewage septic tanks are usually anaerobic treatment tanks (first chamber and second chamber) partitioned by a partition wall, an aerobic treatment tank (aerobic filter bed tank), a precipitation tank (or treated water tank) and It consists of a disinfection tank. The sewage supplied from the inflow port is sequentially transferred from the first chamber of the anaerobic treatment tank to the downstream, finally sterilized in the disinfection tank, and discharged from the outflow port to the outside.
[0003]
Several structures of the aerobic filter bed tank in the sewage septic tank are conventionally known. However, as shown in FIG. 6, the applicant previously aerobically sandwiched a porous plate (not shown). The filter bed tank is divided into an upper filter bed (biological reaction layer or R zone) 1 and a lower filter bed (filter layer or F zone) 2, and the filter bed layer is filled with a granular carrier, A structure is proposed in which aeration pipes 4a and 4b are installed in the air and a washing drainage outlet 5a which is a liquid suction port of the transfer pump (air lift pump) 5 is installed in the lower part of the aerobic filter bed tank C (Japanese Unexamined Patent Publication No. Hei 9-1993). No. 248584). At the time of washing the aerobic filter bed tank C in this sewage septic tank, after aeration from the diffuser pipes 4a and 4b under the two filter beds, the washing drainage of the lower part of the aerobic filter bed tank via a transfer pump (air lift pump) 5 The washing waste water is withdrawn from the extraction port 5a and transferred to the upper part of the anaerobic treatment tank (first chamber), and the advection water from the anaerobic treatment tank (second chamber) pushed out with the transfer is aerobic filter bed tank C is introduced into the upper filter bed.
[0004]
Then, during the washing, the lower filter bed is caused to flow uniformly by aeration, and floating suspension (also referred to as biofilm peeling sludge, hereinafter abbreviated as SS) trapped in the lower filter bed is peeled off. Then, the waste water is returned from the washing drain outlet 5a to the anaerobic treatment tank (first chamber) through the transfer pump (air lift pump) 5 as washing waste water. At this time, the amount of the cleaning waste water to be drawn is determined by the area of the bottom surface of the aerobic filter bed tank C and the speed of the cleaning waste water passing through the bottom surface.
[0005]
[Problems to be solved by the invention]
However, when the distance between the lower end of the lower filter bed 2 and the bottom surface of the lower filter bed 2 in the aerobic filter bed tank C is long, the SS far from the washing drain outlet 5a has a settling force than the force sucked into the washing drain outlet 5a. Tends to settle and settle on the bottom. Moreover, the settled SS stays in the place and becomes anaerobic, which adversely affects the performance of sewage treatment. The present invention is intended to solve such a problem, and the object of the present invention is to perform aerobic filtration even when the lower end of the lower filter bed 2 and the bottom of the filter bed are separated. To provide a cleaning method for an aerobic filter bed tank and a sewage septic tank, or a lower filter bed (filter layer) in an aerobic filter bed tank, in which SS does not stay at the bottom of the floor tank C and the performance of sewage treatment can be maintained well. It is.
[0006]
[Means for Solving the Problems]
In order to achieve the above object, the aerobic filter bed of the present invention has the following configuration. That is, the present invention firstly has two filter beds of the biological reaction layer 1 and the filter layer 2, and each of the diffuser tubes 4a under each filter bed (which means the lower part or the lower part, hereinafter the same). , an aerobic filter bed tank C with 4b, a lower diffusing tube 4b under side of the filtration layer 2, further air jet between the bottom of the aerobic filter bed tank and the filtering layer The aerobic filter bed tank C is characterized in that the pipe 6 is arranged.
[0007]
Here, the two reaction beds of the bioreaction layer 1 and the filtration layer 2 can be arranged side by side with the bioreaction layer 1 as a front filter bed and the filtration layer 2 as a rear filter bed. The aerobic filter bed tank C is arranged vertically (that is, forms a double bed) with the biological reaction layer 1 as the upper filter bed and the filter layer 2 as the lower filter bed.
[0008]
In addition, the air injection pipe 6 disposed below the air diffusion pipe 4b is an air injection in which the injected air flow forms a horizontal flow (that is, a flow parallel to the bottom surface) so that the SS settling on the bottom surface is sufficiently raised. It is assumed that the tube has a mouth 6a. Moreover, it is preferable that the location where the air injection port 6a is located is in the center of the bottom of the aerobic filter bed C or in the vicinity of the center so as to be in contact with the bottom (or at a position not separated from the bottom by 50 mm or more). .
[0009]
Further, in the aerobic filter bed C, a liquid of a transfer pump (usually an air lift pump) 5 is further provided below the filtration layer 2 or above the filtration layer 2 or below the biological reaction layer 1. It is preferable that a cleaning drainage outlet 5a serving as a suction inlet is disposed.
[0010]
The present invention secondly, a sewage purification tank equipped with the above-described aerobic filter bed tank, that is, an anaerobic filter bed tank (first chamber A and second chamber B) in order from the upstream, the above-described aerobic treatment tank C, A sewage septic tank comprising a sedimentation tank (or treated water tank) D and a disinfection tank E.
[0013]
[Action]
When washing the lower filter bed in the aerobic filter bed, the liquid in the lower filter bed is efficiently used by the horizontal jet stream from the air jet pipe (its air jet port) along with the vertical aeration from the diffuser pipe. Stir. Then, the SS present in the liquid is drawn out from the washing drainage outlet without sinking to the bottom surface, and returned to the first chamber of the anaerobic filter bed tank via the transfer pump (air lift pump) (see FIG. 1).
[0014]
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, embodiments of the present invention will be described more specifically with reference to the drawings.
FIG. 1 is a schematic configuration diagram of an example of an aerobic filter bed tank according to the present invention, and FIG. 2 is a view of the aerobic filter bed tank of FIG. In these figures, an aeration air flow (arrow) at the time of cleaning is also appended.
The aerobic filter bed tank C is filled with a biological carrier (becomes a living organism, also called a contact material or a filter material) to form a filter bed. This filter bed is divided into an upper filter bed (biological reaction layer) 1 and a lower filter bed (filter layer) 2, and a water-permeable porous plate (biological carrier) between the upper filter bed 1 and the lower filter bed 2. Compartment that sandwiches water and air freely. Further, a water-permeable porous plate material is disposed on both the upper filter bed 1 and the lower filter bed 2 so as to prevent the biological carrier from flowing out.
[0015]
A diffuser pipe 4a is provided below the upper filter bed 1, a diffuser pipe 4b is also provided below the lower filter bed 2, and a liquid suction port of a transfer pump (air lift pump) 5 is provided below the aerobic filter bed tank C. A cleaning drain outlet 5a is provided.
Further, an air injection pipe 6 (air injection horizontal pipe 6b) having an air injection port 6a is disposed below the air diffusion pipe 4b, and an air injection flow parallel to the bottom surface can be created. Note that the diffuser holes formed in the diffuser tubes 4a and 4b are usually provided at the lower portion of the tube in order to prevent clogging due to sediment such as SS.
[0016]
Water treatment in the aerobic filter bed tank C is performed in the biological carrier in the presence of air (dissolved oxygen) aerated and introduced from the diffuser 4a in the upper filter bed (biological reaction layer) 1. It is aerobic treated by aerobic microorganisms that inhabit. That is, mainly, oxidation / decomposition of biochemical oxygen demand (BOD) and nitrification of ammonia proceed.
Further, in the lower filter bed 2, in the normal operation (operation other than during washing), aeration is not performed from the air diffusing tube 4b. While continuing the aerobic treatment while consuming the carry-over oxygen (dissolved oxygen) of the falling liquid from the upper filter bed 1, there is a function of efficiently capturing (filtering) SS using a stationary biological carrier. Therefore, the lower filter bed 2 is gradually clogged with the captured SS. In order to release this clogging, the aerobic filter bed C (particularly the lower filter bed 2) is periodically washed (usually once a day for about 1 to 30 minutes at night). At the time of this washing, aeration is performed from the air diffuser 4b provided under the lower filter bed 2, and at the same time, aeration is also performed from the air injection port 6a to release SS from the biological carrier. Simultaneously with the aeration or after the aeration, the cleaning waste water containing SS is extracted from the cleaning drain outlet 5a. An air lift pump is preferably used for this drawing.
[0017]
The aeration from the air injection port 6a of the air injection tube 6 is normally performed simultaneously with the aeration (that is, cleaning / suction) from the diffusion tube 4b, but may be performed prior to the aeration from the diffusion tube 4b. In this case, the SS that has settled on the bottom surface without being discharged at the time of washing the previous day is swollen in advance, and this is pulled out together with aeration (that is, washing / suction) from the aeration tube 4b.
Further, the aeration (that is, continuous aeration) from the air diffuser 4a of the upper filter bed 1 during the cleaning may be temporarily stopped during that time.
[0018]
Cleaning can be performed automatically by using a timer or the like. It is preferable that the time, time, and frequency can be set arbitrarily.
[0019]
Moreover, not only an air injection pipe as shown in FIG.1 and FIG.2, but an air injection pipe of various shapes can be used. 3 and 4 show another example of an air injection pipe and an aerobic filter bed tank. Each figure is a view of the aerobic filter bed tank as viewed from below the bottom surface. FIG. 3 shows an example in which the air injection pipe branches in the middle. FIG. 4 shows a small hole in the middle of the pipe in addition to the open end. This is an example where is opened.
[0020]
In addition, although the example of FIGS. 1-4 was taken as the example of the upper and lower two layers structure of the upper filter bed and the lower filter bed, it is also possible to set it as the serial structure of two horizontal rows instead of upper and lower.
[0021]
FIG. 5 is an example of a sewage purification tank (schematic configuration diagram) using the aerobic filter bed tank of the present invention.
This sewage septic tank has an anaerobic filter bed first chamber A, an anaerobic filter bed second chamber B, an aerobic filter bed C (having an upper filter bed 1 and a lower filter bed 2), and a treated water tank D from the upstream side. The sterilization tank E is divided into each tank.
The first chamber A and the second chamber B of the anaerobic filter bed tank can be filled with a biological carrier such as a mesh-like cylindrical filter medium, and the upper filter bed 1 and the lower filter of the aerobic filter bed tank C. The floor 2 can be filled with a biological carrier such as a sponge carrier.
The treated water tank D is provided with an air lift pump 5 necessary for washing the lower filter bed 2 of the aerobic filter bed tank C, and a liquid suction port of the air lift pump is provided at the lower part of the aerobic filter bed tank C. . The washing waste water extracted from here is returned to the first chamber A of the anaerobic filter bed tank. In addition, an air jet vertical pipe 6c is also disposed in the treated water tank D.
[0022]
An example of the cleaning operation is as follows. During normal operation of the sewage septic tank, air is supplied to the diffusing pipe 4 a below the upper filter bed 1, and no air is supplied to the diffusing pipe 4 b below the lower filter bed 2 and the air lift pump 5. At the time of washing, air is supplied to the air diffusion pipe 4b, the air lift pump 5 and the air injection pipe 6 below the lower filter bed 2.
[0023]
The air jet pipe 6 below the lower filter bed 2 is installed as follows. At the lower part of the aerobic filter bed C, an advection port 7 is provided on the side wall surface of the aerobic filter bed tank close to the treated water tank D, and a washing drain outlet 5a is arranged above the advection port, and this washing drain outlet 5a. The horizontal pipe 6b for air injection is inserted so that the bottom surface is made to flow from the treated water tank D side below. At that time, the air injection port 6a is arranged at the center of the bottom surface of the aerobic filter bed C. When air is supplied to the air injection pipe 6 and air is discharged from the air injection port 6a, the lower part of the lower filter bed 2 and the vicinity of the bottom of the aerobic filter bed tank C are stirred, and the SS is washed without staying at the bottom. It is pulled out from the cleaning drainage outlet 5a together with the drainage.
[0024]
According to the aerobic filter bed tank or the sewage purification tank of the present invention, even if the distance between the lower end of the lower filter bed and the bottom surface of the aerobic filter bed tank is long, SS is present at the bottom of the aerobic filter bed tank. it is not small to stay.
[Brief description of the drawings]
FIG. 1 is a schematic configuration diagram of an aerobic filter bed tank according to the present invention. The aeration air flow at the time of washing is also indicated by an arrow.
FIG. 2 is a view of the aerobic filter bed tank of FIG. The arrow indicates the jet flow from the air jet port.
FIG. 3 is a view of another example of an aerobic filter bed tank according to the present invention as viewed from below the bottom surface. An example in which the air injection pipe branches on the way.
FIG. 4 is a view of another example of an aerobic filter bed tank according to the present invention as viewed from below the bottom surface. In addition to the open end of the air jet tube, a small hole is made in the middle of the tube.
FIG. 5 is a schematic configuration diagram of a sewage septic tank according to the present invention.
FIG. 6 is a schematic configuration diagram of a conventional aerobic filter bed tank.
[Explanation of symbols]
1: Upper filter bed (biological reaction layer) 2: Lower filter bed (filter layer)
3: Partition wall 4a: Air diffuser 4b: Air diffuser 5: Air lift pump 5a: Cleaning drain outlet (air lift pump suction port)
5b: Air lift pump pumping pipe 6: Air injection pipe 6a: Air injection port 6b: Horizontal pipe for air injection 6c: Vertical pipe for air injection 7: Advection port A: Anaerobic filter bed first chamber B: Anaerobic filter bed first Two rooms C: Aerobic filter bed D: Treated water tank E: Disinfection tank
Claims (4)
Priority Applications (1)
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JP32091499A JP4187889B2 (en) | 1999-11-11 | 1999-11-11 | Aerobic filter bed tank and septic tank |
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JP32091499A JP4187889B2 (en) | 1999-11-11 | 1999-11-11 | Aerobic filter bed tank and septic tank |
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JP4187889B2 true JP4187889B2 (en) | 2008-11-26 |
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CN105836895A (en) * | 2016-06-12 | 2016-08-10 | 广西飞扬环保科技有限公司 | Integrated sewage purification system |
CN110526398B (en) * | 2019-08-27 | 2022-03-08 | 南京环保产业创新中心有限公司 | Micro-polluted water treatment reactor and method thereof |
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