JP2000218286A - Membrane septic tank - Google Patents
Membrane septic tankInfo
- Publication number
- JP2000218286A JP2000218286A JP11021294A JP2129499A JP2000218286A JP 2000218286 A JP2000218286 A JP 2000218286A JP 11021294 A JP11021294 A JP 11021294A JP 2129499 A JP2129499 A JP 2129499A JP 2000218286 A JP2000218286 A JP 2000218286A
- Authority
- JP
- Japan
- Prior art keywords
- membrane
- tank
- aeration
- aeration tank
- raw water
- 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.)
- Pending
Links
- 239000012528 membrane Substances 0.000 title claims abstract description 48
- 238000005273 aeration Methods 0.000 claims abstract description 39
- 244000005700 microbiome Species 0.000 claims abstract description 7
- 239000000969 carrier Substances 0.000 claims abstract description 4
- 239000006260 foam Substances 0.000 claims description 7
- 239000007788 liquid Substances 0.000 claims description 2
- 238000000926 separation method Methods 0.000 claims description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 13
- 238000000967 suction filtration Methods 0.000 abstract description 3
- 239000010840 domestic wastewater Substances 0.000 abstract description 2
- 238000000151 deposition Methods 0.000 abstract 1
- 239000002689 soil Substances 0.000 abstract 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 4
- 238000004140 cleaning Methods 0.000 description 4
- 239000001301 oxygen Substances 0.000 description 4
- 229910052760 oxygen Inorganic materials 0.000 description 4
- 239000000463 material Substances 0.000 description 3
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 3
- 239000002028 Biomass Substances 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 238000004659 sterilization and disinfection Methods 0.000 description 2
- 230000004913 activation Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000010800 human waste Substances 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000007689 inspection Methods 0.000 description 1
- 230000000813 microbial effect Effects 0.000 description 1
- 230000020477 pH reduction Effects 0.000 description 1
- 229920000098 polyolefin Polymers 0.000 description 1
- 230000006641 stabilisation Effects 0.000 description 1
- 238000011105 stabilization Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Classifications
-
- 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
Landscapes
- Biological Treatment Of Waste Water (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
- Treatment Of Biological Wastes In General (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、膜処理型浄化槽に
関するものである。[0001] The present invention relates to a membrane treatment type septic tank.
【0002】[0002]
【従来の技術】従来から、膜処理型浄化槽にあっては膜
エレメントによる吸引濾過による膜の目詰まりを防ぐた
め、曝気槽下部に配設した散気管から曝気を行い、曝気
による回流で膜面に付着した生物膜を洗浄しつつ吸引を
行っている。2. Description of the Related Art Conventionally, in a membrane treatment type septic tank, aeration is performed from a diffuser pipe provided at a lower portion of an aeration tank to prevent clogging of the membrane due to suction filtration by a membrane element. Suction is performed while cleaning the biofilm attached to the surface.
【0003】[0003]
【発明が解決しようとする課題】しかしながら、上記従
来の技術においては、膜面洗浄のため、通常の生物処理
に必要な酸素供給に必要な曝気量以上に曝気を過大にす
る必要があり、必然的に曝気用ブロアは大きくなるの
で、その運転には多くの電力負荷がかかるという問題が
あった。However, in the above-mentioned conventional technology, it is necessary to increase the amount of aeration for cleaning the surface of the membrane, which is more than the amount of aeration necessary for supplying oxygen necessary for ordinary biological treatment. Since the blower for aeration is large in size, there is a problem that a large power load is required for the operation.
【0004】又、生物処理に必要量以上の酸素が供給さ
れることによる過曝気状態を引き起こし、曝気槽内の生
物処理反応によって窒素酸化物が多く生成され、槽内の
酸性化がすすむなどの影響があった。[0004] In addition, overaeration is caused by supply of oxygen in an amount more than necessary for biological treatment, and a large amount of nitrogen oxides is generated by the biological treatment reaction in the aeration tank, and acidification in the tank proceeds. Affected.
【0005】本発明は、上記事由に鑑みてなしたもの
で、その目的とするところは、少ない曝気量でも膜面洗
浄が効率的に行うことのできる膜処理型浄化槽を提供す
ることにある。The present invention has been made in view of the above circumstances, and an object of the present invention is to provide a membrane treatment type septic tank that can efficiently perform membrane surface cleaning even with a small amount of aeration.
【0006】[0006]
【課題を解決するための手段】上記目的を達成するため
に、本発明の膜処理型浄化槽にあっては、固液分離する
膜エレメントが内部に複数配設されている曝気槽を備え
た膜処理型浄化槽において、隣接する膜エレメント同士
の間隔よりも小さい直径で微生物を担持することのでき
る担体が曝気槽に多数混入されたことを特徴としてい
る。この場合、曝気による回流で担体が曝気槽内を移動
し、膜面と接触することにより膜面の洗浄を行う。In order to achieve the above object, a membrane treatment type septic tank according to the present invention has a membrane provided with an aeration tank in which a plurality of membrane elements for solid-liquid separation are arranged. The treatment type septic tank is characterized in that a large number of carriers capable of supporting microorganisms with a diameter smaller than the distance between adjacent membrane elements are mixed in the aeration tank. In this case, the carrier moves in the aeration tank by circulating by aeration and comes into contact with the membrane surface to clean the membrane surface.
【0007】また、上記担体は柔軟な発泡体で構成され
ていることが好ましい。この場合、担体と膜面との接触
はソフトに行われ、また担体の内部に微生物が住みつき
易くなる。It is preferable that the carrier is formed of a flexible foam. In this case, the contact between the carrier and the membrane surface is performed softly, and the microorganisms easily live in the carrier.
【0008】[0008]
【発明の実施の形態】図1は、本発明の請求項1又は2
に対応する一実施の形態を示した断面図である。図2
は、請求項1又は2に対応する一実施の形態を示した要
部断面図である。以下、図1により本発明の実施例を説
明する。DESCRIPTION OF THE PREFERRED EMBODIMENTS FIG. 1 shows a first or second embodiment of the present invention.
FIG. 2 is a cross-sectional view showing an embodiment corresponding to FIG. FIG.
FIG. 1 is a sectional view of a main part showing an embodiment corresponding to claim 1 or 2. Hereinafter, an embodiment of the present invention will be described with reference to FIG.
【0009】この実施の形態の膜処理型浄化槽1は、地
中に埋設固定されており、外界からの点検はマンホール
2で遮蔽された開口部3を経由して行われる。し尿や生
活雑排水(以下、原水4という)は、膜処理型浄化槽1
の片端に設けられた流入口5より流入し、濾材23、夾
雑物除去槽24を経て夾雑物が除去された状態となり、
移送ポンプ6により曝気槽7に送られる。The septic tank 1 of this embodiment is buried and fixed in the ground, and inspection from the outside is performed through an opening 3 shielded by a manhole 2. Human waste and domestic wastewater (hereinafter referred to as raw water 4) are supplied to the membrane treatment type septic tank 1
From the inflow port 5 provided at one end of the filter material, the filter material 23, the foreign matter removal tank 24, the state where impurities are removed,
It is sent to the aeration tank 7 by the transfer pump 6.
【0010】この曝気槽7においては、酸素により微生
物を活性化させ有機物の分解を促進するために、その下
部にその酸素を供給するための散気管8が備えられてい
る。この散気管8からは、膜処理型浄化槽1の外部に設
置された制御部9を備えた曝気用ブロア10から送気配
管11を経由して取り込まれた空気が一定間隔で曝気さ
れる。一定間隔をあけることで、微生物活動の活性化お
よび量の安定化を図ることが可能となる。In the aeration tank 7, a diffusion tube 8 for supplying oxygen is provided below the aeration tank 7 in order to activate microorganisms by oxygen and promote decomposition of organic substances. From the air diffuser 8, air taken in via an air supply pipe 11 from an aeration blower 10 having a control unit 9 installed outside the membrane treatment type septic tank 1 is aerated at regular intervals. At regular intervals, activation of microbial activity and stabilization of the amount can be achieved.
【0011】また、該曝気槽7内には原水4に複数の膜
エレメント12が浸漬されており、原水4はこの膜面1
3に付着した生物膜14によって濾過され、この濾過に
より膜内に現れた濾過水15が吸引ポンプ16により吸
い出され、パイプ17を経て消毒槽18につながる濾過
水取出口19から取り出される。消毒槽18により最終
の浄化を終えた濾過水15は、外部につながる放流口2
0より放流される。In the aeration tank 7, a plurality of membrane elements 12 are immersed in raw water 4, and the raw water 4
Filtration is performed by the biofilm 14 attached to the filter 3, and filtered water 15 that has appeared in the membrane by the filtration is sucked out by a suction pump 16 and taken out from a filtered water outlet 19 that is connected to a disinfection tank 18 through a pipe 17. The filtered water 15 that has been finally purified by the disinfection tank 18 is discharged to the discharge port 2 connected to the outside.
Released from 0.
【0012】吸引濾過されることによる膜の目詰まりを
取り除くため、本実施例では図2に示す通り、曝気によ
る曝気槽7内の原水4の回流により、あらかじめ曝気槽
7内に混入された担体21を流動させ、膜面13と接触
させることで生物膜14の洗浄を行っている。その結
果、曝気による気泡22の回流のみで膜面に付着した生
物膜14を洗浄していた従来の方法にくらべ、さらに少
ない曝気量でも同様の効果を得られた。従って従来にく
らべ曝気量を大幅に減らせるため、曝気用ブロア10の
小型化とそれに伴う省電力化が可能となる。In order to remove the clogging of the membrane due to the suction filtration, in this embodiment, as shown in FIG. 2, the carrier mixed in the aeration tank 7 in advance by the circulation of the raw water 4 in the aeration tank 7 by aeration. The biofilm 14 is washed by flowing the fluid 21 and bringing it into contact with the membrane surface 13. As a result, compared to the conventional method in which the biofilm 14 attached to the membrane surface was washed only by the circulation of the bubbles 22 by aeration, the same effect was obtained even with a smaller amount of aeration. Therefore, the amount of aeration can be greatly reduced as compared with the conventional case, so that the size of the aeration blower 10 can be reduced and power consumption can be reduced accordingly.
【0013】担体21は隣接する膜エレメント12間に
入り込めるように、担体21の直径が膜エレメント12
間の寸法よりも小さいものであることは言うまでもない
が、本実施例においては、隣接する膜エレメント12の
間を7ミリメートルとし、担体21は5ミリメートル角
のサイコロ状の連続発泡体を使用した。The diameter of the carrier 21 is adjusted so that the carrier 21 can enter between the adjacent membrane elements 12.
Needless to say, the size is smaller than the size between them, but in this embodiment, the distance between the adjacent membrane elements 12 is 7 mm, and the carrier 21 is a 5-mm square continuous foam.
【0014】担体21は原水4の中を流動できるもので
あればどのような素材から構成されていてもよいが、生
物膜14と接触するため、生物膜14の損傷を防ぐため
できるだけ柔軟なものが望ましい。本実施例では、ポリ
オレフィンのスポンジを用いたが生物膜14の損傷はみ
られず、良好な洗浄結果を得られた。また、空洞を多く
有する発泡体であるため担体21の内部に微生物が住み
つき易くなり、生物量の増加が見られ処理効率が向上
し、ひいては曝気槽7の容量を小さくすることも可能と
なる。The carrier 21 may be made of any material as long as it can flow in the raw water 4. However, since the carrier 21 is in contact with the biofilm 14, it is as flexible as possible to prevent the biofilm 14 from being damaged. Is desirable. In this example, a sponge made of polyolefin was used, but no damage to the biofilm 14 was observed, and good cleaning results were obtained. In addition, since the foam is a foam having many cavities, microorganisms can easily live in the carrier 21, an increase in biomass can be seen, the treatment efficiency can be improved, and the capacity of the aeration tank 7 can be reduced.
【0015】[0015]
【発明の効果】本発明の膜処理型浄化槽は、上述の実施
態様の如く実施されて、曝気による回流で担体が曝気槽
内を移動し、膜面と接触することにより膜面の洗浄を行
うができる。The membrane treatment type septic tank of the present invention is implemented as in the above-described embodiment, and the carrier moves in the aeration tank by circulating flow by aeration and is cleaned by contact with the membrane surface. Can be.
【0016】そして、曝気による回流のみで膜面に付着
した生物膜を洗浄していた従来の方法にくらべ、少ない
曝気量でも同様の効果を得られたので、曝気用ブロアの
小型化とそれに伴う省電力化が可能となる。[0016] Compared with the conventional method in which the biofilm adhered to the membrane surface is washed only by circulation by aeration, the same effect can be obtained with a small amount of aeration. Power saving can be achieved.
【0017】また、柔軟な発泡体で構成されている担体
は、膜面との接触がソフトに行われるため、生物膜の損
傷はみられず、良好な洗浄結果を得られる。また発泡体
のため空洞を多く有する該担体の内部には微生物が住み
つき易くなるので、生物量の増加が見られ処理効率が向
上し、ひいては曝気槽の容量を小さくすることも可能と
なる。Further, the carrier made of a flexible foam is softly contacted with the membrane surface, so that the biofilm is not damaged and a good washing result can be obtained. In addition, since the microorganisms easily live in the carrier having many cavities due to the foam, the biomass is increased, the treatment efficiency is improved, and the capacity of the aeration tank can be reduced.
【図1】本発明の一実施形態である膜処理型浄化槽を示
す断面図である。FIG. 1 is a cross-sectional view showing a membrane treatment type septic tank according to one embodiment of the present invention.
【図2】同膜処理型浄化槽の一要部を示す断面図であ
る。FIG. 2 is a cross-sectional view showing a main part of the membrane treatment type septic tank.
1 膜処理型浄化槽 7 曝気槽 12 膜エレメント 21 担体 DESCRIPTION OF SYMBOLS 1 Membrane treatment type septic tank 7 Aeration tank 12 Membrane element 21 Carrier
Claims (2)
配設されている曝気槽を備えた膜処理型浄化槽におい
て、隣接する膜エレメント同士の間隔よりも小さい直径
で微生物を担持することのできる担体が曝気槽に多数混
入されたことを特徴とする膜処理型浄化槽。1. In a membrane treatment type septic tank provided with an aeration tank in which a plurality of membrane elements for solid-liquid separation are arranged, microorganisms can be carried with a diameter smaller than the distance between adjacent membrane elements. A membrane treatment type septic tank wherein a large number of carriers are mixed in an aeration tank.
を特徴とする請求項1記載の膜処理型浄化槽。2. The membrane treatment type septic tank according to claim 1, wherein the carrier is made of a flexible foam.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11021294A JP2000218286A (en) | 1999-01-29 | 1999-01-29 | Membrane septic tank |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11021294A JP2000218286A (en) | 1999-01-29 | 1999-01-29 | Membrane septic tank |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JP2000218286A true JP2000218286A (en) | 2000-08-08 |
Family
ID=12051136
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP11021294A Pending JP2000218286A (en) | 1999-01-29 | 1999-01-29 | Membrane septic tank |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2000218286A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR100339017B1 (en) * | 2000-04-03 | 2002-05-31 | 한상배 | Advanced Wate Water Treatment System of Package Type |
| KR100402289B1 (en) * | 2001-11-05 | 2003-10-22 | (주)동호이씨엠 | Method and apparatus for treatment of sewage and waste-water |
| US6863817B2 (en) | 2002-12-05 | 2005-03-08 | Zenon Environmental Inc. | Membrane bioreactor, process and aerator |
-
1999
- 1999-01-29 JP JP11021294A patent/JP2000218286A/en active Pending
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR100339017B1 (en) * | 2000-04-03 | 2002-05-31 | 한상배 | Advanced Wate Water Treatment System of Package Type |
| KR100402289B1 (en) * | 2001-11-05 | 2003-10-22 | (주)동호이씨엠 | Method and apparatus for treatment of sewage and waste-water |
| US6863817B2 (en) | 2002-12-05 | 2005-03-08 | Zenon Environmental Inc. | Membrane bioreactor, process and aerator |
| US7022236B2 (en) | 2002-12-05 | 2006-04-04 | Zenon Environmental Inc. | Membrane bioreactor, process and aerator |
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