JPH0487699A - Method for purifying polluted water region - Google Patents
Method for purifying polluted water regionInfo
- Publication number
- JPH0487699A JPH0487699A JP2199897A JP19989790A JPH0487699A JP H0487699 A JPH0487699 A JP H0487699A JP 2199897 A JP2199897 A JP 2199897A JP 19989790 A JP19989790 A JP 19989790A JP H0487699 A JPH0487699 A JP H0487699A
- Authority
- JP
- Japan
- Prior art keywords
- water
- tank
- flocculant
- sludge
- pond
- 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
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 63
- 238000000034 method Methods 0.000 title claims description 8
- 239000010802 sludge Substances 0.000 claims abstract description 28
- 238000005273 aeration Methods 0.000 claims abstract description 10
- 238000005086 pumping Methods 0.000 claims abstract description 3
- 238000000108 ultra-filtration Methods 0.000 claims description 11
- 239000007788 liquid Substances 0.000 claims description 6
- 238000002156 mixing Methods 0.000 abstract description 14
- 239000012528 membrane Substances 0.000 abstract description 9
- 238000000926 separation method Methods 0.000 abstract description 4
- 239000012510 hollow fiber Substances 0.000 abstract description 2
- 244000144992 flock Species 0.000 abstract 2
- 239000003344 environmental pollutant Substances 0.000 description 6
- 231100000719 pollutant Toxicity 0.000 description 6
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 5
- 230000000694 effects Effects 0.000 description 5
- 229910052760 oxygen Inorganic materials 0.000 description 5
- 239000001301 oxygen Substances 0.000 description 5
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 4
- 229910052698 phosphorus Inorganic materials 0.000 description 4
- 239000011574 phosphorus Substances 0.000 description 4
- 239000003463 adsorbent Substances 0.000 description 3
- 238000007790 scraping Methods 0.000 description 3
- 238000004062 sedimentation Methods 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- 238000005345 coagulation Methods 0.000 description 2
- 230000015271 coagulation Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000000605 extraction Methods 0.000 description 2
- 238000005188 flotation Methods 0.000 description 2
- 238000002347 injection Methods 0.000 description 2
- 239000007924 injection Substances 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 238000005192 partition Methods 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 238000011282 treatment Methods 0.000 description 2
- 239000003643 water by type Substances 0.000 description 2
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 1
- 235000011941 Tilia x europaea Nutrition 0.000 description 1
- 238000005276 aerator Methods 0.000 description 1
- 238000005054 agglomeration Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 238000011001 backwashing Methods 0.000 description 1
- 239000000701 coagulant Substances 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000018044 dehydration Effects 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000012851 eutrophication Methods 0.000 description 1
- 239000000706 filtrate Substances 0.000 description 1
- 238000007667 floating Methods 0.000 description 1
- 239000008394 flocculating agent Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 239000004571 lime Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000002957 persistent organic pollutant Substances 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 239000008213 purified water Substances 0.000 description 1
- 238000009287 sand filtration Methods 0.000 description 1
- 239000013049 sediment Substances 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 230000008719 thickening Effects 0.000 description 1
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
- Separation Of Suspended Particles By Flocculating Agents (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は汚濁した湖沼、池、堀等の水域を効果的に浄化
する方法に関するものである。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a method for effectively purifying polluted water bodies such as lakes, ponds, and moats.
従来、汚濁水域を直接浄化する方法としては、間欠式空
気揚水筒と呼ばれる曝気機を用いる方法、石灰や凝集剤
を散布する方法等がある。Conventionally, methods for directly purifying polluted water bodies include a method using an aerator called an intermittent air pump, a method of spraying lime or a flocculant, and the like.
しかしながら前者は、水域全体を好気化することにより
嫌気性腐敗を防止する効果があるものの、有機性汚濁物
を直接分解したり、水域外に排除する機能をもたないた
め、汚濁物を処理する効果は少ない。また、後者は一時
的には透視度の向上など顕著な効果を示すものの、沈澱
物が蓄積して徐々に嫌気性腐敗が進むため、汚濁水の恒
久的な処理にはならない。However, although the former has the effect of preventing anaerobic decay by aerobizing the entire water body, it does not have the function of directly decomposing organic pollutants or removing them from the water body, so it is necessary to treat the pollutants. It has little effect. Furthermore, although the latter method temporarily shows remarkable effects such as improved visibility, it is not a permanent treatment for polluted water because sediment accumulates and anaerobic decomposition gradually progresses.
汚濁水域を効果的に浄化するためには、溶解性の汚濁物
質は直接分解するか、吸着剤に吸着または不溶化させて
吸着剤あるいは汚泥を他の固形物とともに回収し、水域
外に排出する必要がある。特に富栄養化の原因物質であ
るリンに対しては、従来の凝集沈澱により汚濁水を浄化
する方法が考えられるが、通常の水域の水は、汚濁水域
であっても通常凝集沈澱を用いている下水処理水等の水
に比べると、リンf度が低いため凝集フロックが脆弱で
あり、沈澱分離が難しいという問題がある。また、後段
に砂濾過を設けたとしても微細な凝集フロックが濾槽の
深部に達して逆洗が難しくなる。In order to effectively purify polluted water bodies, it is necessary to directly decompose soluble pollutants, or to adsorb or insolubilize them onto adsorbents, collect the adsorbents or sludge along with other solids, and discharge them out of the water area. There is. In particular, for phosphorus, which is a cause of eutrophication, the conventional method of purifying polluted water by coagulation and sedimentation is considered. Compared to water such as treated sewage water, the degree of phosphorus is low, so the flocs are weak and sedimentation is difficult. Further, even if sand filtration is provided at the latter stage, fine flocs reach the deep part of the filter tank, making backwashing difficult.
本発明は、汚濁物を含む水に凝集剤を加えて汚泥フロッ
クを形成させ、固液分離を行って清澄な水を水域に戻す
ことにより、水域を効果的に浄化することを目的とする
。The present invention aims to effectively purify water bodies by adding a flocculant to water containing pollutants to form sludge flocs, performing solid-liquid separation, and returning clear water to the water bodies.
本発明は上記目的を達成するためになしたもので、汚濁
水域の水を揚水して曝気を行い、凝集剤等を添加して凝
集した汚泥を限外濾過により固液分離し、濾過水を汚濁
水域に戻すことによって、水域を浄化することを要旨と
する。The present invention was made to achieve the above object, and involves pumping water from a polluted water area, aerating it, adding a coagulant, etc., and separating the flocculated sludge into solid and liquid by ultrafiltration. The purpose is to purify water bodies by returning them to polluted waters.
汚濁水域の水を揚水して、凝集剤等を添加して汚泥を生
成させ、限外濾過装置を用いて固液分離し、汚泥を回収
して系外に搬出するとともに、分離した浄化水を水域に
戻すことによって、汚濁水域を効果的に浄化することが
できる。Water from polluted areas is pumped up, flocculants are added to produce sludge, solid-liquid separation is performed using an ultrafiltration device, the sludge is collected and transported out of the system, and the separated purified water is By returning the water to the water, the polluted water area can be effectively purified.
以下本発明を図示の実施例にもとづいて説明する。 The present invention will be explained below based on the illustrated embodiments.
図においてLは、汚濁水域の例として小規模の池を示し
たもので、池の端部には揚水ポンプ1が設けられる。揚
水した池の水は、曝気槽2においてコンプレッサ3、あ
るいはブロワ−からの空気を底部の散気装置[4から散
気することにより曝気される。また、凝集剤タンク5か
ら注入ポンプ6により曝気槽2に凝集剤が添加され池の
水と混合される。さらに、次の混和槽7において撹拌機
9により緩速撹拌される。混和槽上部には浮上汚泥の掻
取装N8、底部には沈澱汚泥を引抜くための配管を設け
、汚泥引抜ポンプ10により汚汀渡縮槽]】に送洗する
。In the figure, L indicates a small-scale pond as an example of a polluted water area, and a water pump 1 is provided at the end of the pond. The pumped pond water is aerated in the aeration tank 2 by dispersing air from a compressor 3 or a blower through an aeration device [4] at the bottom. Further, a flocculant is added from the flocculant tank 5 to the aeration tank 2 by an injection pump 6 and mixed with pond water. Furthermore, in the next mixing tank 7, the mixture is slowly stirred by a stirrer 9. A scraping device N8 for floating sludge is provided at the top of the mixing tank, and piping for drawing out the settled sludge is provided at the bottom, and the sludge is sent to the sludge coagulation tank by a sludge drawing pump 10.
混和槽7において凝集した汚泥フロックは、清澄な水と
ともに混和槽中段から引抜かれ加圧ポンプ12により加
圧されて、限外濾過装置13に送られる。限外濾過膜N
13は、限外濾過膜が管状、中空糸状、平膜状等のモジ
ュールが組込まれ、膜を透過した清澄な濾過水15は、
池の別の場所に返送される。濾過水15が短絡して揚水
されることのないよう、池には仕切壁16を設けるとと
もに、揚水ポンプ1からできるだけ離れた位置に濾過水
を戻す方が効果的である。限外濾過膜を透過しない汚泥
フロックは、濃縮され返送配管14により混和槽7へと
返送される。The sludge flocs coagulated in the mixing tank 7 are pulled out from the middle stage of the mixing tank together with clear water, pressurized by a pressure pump 12, and sent to an ultrafiltration device 13. Ultrafiltration membrane N
13 is a module in which the ultrafiltration membrane has a tubular shape, a hollow fiber shape, a flat membrane shape, etc., and the clear filtered water 15 that has passed through the membrane is
It is sent back to another part of the pond. In order to prevent the filtered water 15 from being pumped due to a short circuit, it is more effective to provide a partition wall 16 in the pond and to return the filtered water to a position as far away from the water pump 1 as possible. Sludge flocs that do not pass through the ultrafiltration membrane are concentrated and returned to the mixing tank 7 via the return pipe 14.
次に本発明の作用について説明する。Next, the operation of the present invention will be explained.
曝気槽2では、池の水に酸素を供給することで溶存酸素
を高めるとともに添加した凝集剤等と短時間で混合する
機能を持つ。ただし、凝集剤等を添加する位置は必ずし
も曝気槽2に限定されるものではなく、混和槽7に流入
する直前等で添加することも可能である。The aeration tank 2 has the function of increasing dissolved oxygen by supplying oxygen to the pond water and mixing it with the added flocculant etc. in a short time. However, the location where the flocculant and the like are added is not necessarily limited to the aeration tank 2, and it is also possible to add the flocculant etc. immediately before flowing into the mixing tank 7.
添加する薬剤は、溶解性リンを凝集する凝集剤の以外に
、他の汚濁成分を除去する吸着剤等対象成分により選定
する。次の混和槽7では緩速撹拌を行うことにより、フ
ロックの凝集が促進される。汚泥フロックが水とともに
限外濾過装置13に送水される時に加圧され、混和槽7
に戻ってきた時には再び常圧に戻るため、水中に溶解し
ていた空気の一部が微細な気泡として析出し、汚泥フロ
ックに付着して汚泥を浮上させる力が働く、浮上した汚
泥は上部の掻取装N8により集められ、槽外に搬出され
る。従って、混和槽7の前段で曝気を行うことは、浮上
分離作用を促進するとともに、池に返送する濾過水の溶
存酸素濃度が高くなるため、池の水を好気状態に保つと
いう機能を持っている。また限外濾過膜N13により濃
縮された汚泥は、混和槽7に返送しているが、返送する
ことによってリンの除去率が高まるとともに汚泥フロッ
クの固液分離性も向上する。The chemicals to be added are selected depending on the target components, such as a flocculant that flocculates soluble phosphorus, and an adsorbent that removes other pollutant components. In the next mixing tank 7, slow stirring is performed to promote agglomeration of flocs. When the sludge flocs are sent to the ultrafiltration device 13 together with water, they are pressurized and mixed into the mixing tank 7.
When the water returns to normal pressure, some of the air dissolved in the water precipitates out as fine bubbles, adheres to the sludge flocs, and works to lift the sludge to the surface. It is collected by scraping device N8 and carried out of the tank. Therefore, performing aeration before the mixing tank 7 not only promotes flotation and separation, but also increases the dissolved oxygen concentration in the filtered water returned to the pond, which has the function of keeping the pond water in an aerobic state. ing. Furthermore, the sludge concentrated by the ultrafiltration membrane N13 is returned to the mixing tank 7, and by returning the sludge, the removal rate of phosphorus is increased and the solid-liquid separability of the sludge flocs is also improved.
一方、混和槽内の汚泥フロックのうち、粒子が大きく重
いものは次第に沈降していく。沈澱効果を高めるために
は、定期的に撹拌I19を停止して静置させることが望
ましい。沈澱した汚泥は活況引抜ポンプにより引抜かれ
、濃縮槽11において1%以上の4度に濃縮して槽外に
排出され、脱水等の処理を行って処分される。また、濃
縮槽11からオーバーフローする分離水は、溶存酸素が
低下しているためIIl気槽2に返送され再び処理され
る。On the other hand, among the sludge flocs in the mixing tank, those with large and heavy particles gradually settle. In order to enhance the precipitation effect, it is desirable to periodically stop stirring I19 and allow the mixture to stand still. The precipitated sludge is pulled out by a live extraction pump, concentrated to 1% or more at 4 degrees Celsius in a thickening tank 11, discharged outside the tank, and subjected to treatments such as dehydration and then disposed of. Further, the separated water overflowing from the concentration tank 11 is returned to the IIl gas tank 2 and treated again because dissolved oxygen has decreased.
本発明による時は、汚濁水域の水を揚水して曝気しなが
ら凝集剤等を添加して汚濁物を凝集して汚泥フロックを
生成させ、限外濾過装置を用いて固液分離した濾過水を
該汚濁水域に戻すとともに、浮上分離と沈澱を組合わせ
て汚泥を回収し処分するため、従来の技術に比べて汚濁
物の除去効果が高く、清澄で溶存酸素の高い水を返送す
ることによって、汚濁水域を効果的に浄化することがで
きる。According to the present invention, water in a polluted area is pumped up, a flocculant is added while aerating the water, the pollutants are coagulated to form sludge flocs, and the filtrate is separated into solid and liquid using an ultrafiltration device. In addition to returning the sludge to the polluted water area, the sludge is recovered and disposed of using a combination of flotation and sedimentation, which is more effective in removing pollutants than conventional technology, and by returning clear water with high dissolved oxygen, Polluted waters can be effectively purified.
第1図は本発明汚濁水域の浄化方法を実施する装置の説
明図である。
1は揚水ポンプ、2は曝気槽、3はコンプレッサ、4は
散気装置、5は凝集剤タンク、6は注入ポンプ、7は混
和槽、8は汚′&掻取装置、9は撹拌機、10は汚泥引
抜ポンプ、11は汚泥渡縮槽、12は加圧ポンプ、13
は限外濾過装置、】4は返送配管、15は濾過水、16
は仕切壁。FIG. 1 is an explanatory diagram of an apparatus for carrying out the method for purifying polluted water areas of the present invention. 1 is a water pump, 2 is an aeration tank, 3 is a compressor, 4 is an aeration device, 5 is a flocculant tank, 6 is an injection pump, 7 is a mixing tank, 8 is a dirt & scraping device, 9 is an agitator, 10 is a sludge extraction pump, 11 is a sludge transfer tank, 12 is a pressurizing pump, 13
is an ultrafiltration device, ]4 is a return pipe, 15 is filtered water, 16
is a partition wall.
Claims (1)
添加して凝集した汚泥を限外濾過により固液分離し、濾
過水を汚濁水域に戻すことによつて、水域を浄化するこ
とを特徴とする汚濁水域の浄化方法。(1) Purify the water area by pumping water from the polluted water area, performing aeration, adding a flocculant, etc., separating the flocculated sludge from solid-liquid through ultrafiltration, and returning the filtered water to the polluted water area. A method for purifying polluted water bodies, characterized by:
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2199897A JPH0487699A (en) | 1990-07-27 | 1990-07-27 | Method for purifying polluted water region |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2199897A JPH0487699A (en) | 1990-07-27 | 1990-07-27 | Method for purifying polluted water region |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH0487699A true JPH0487699A (en) | 1992-03-19 |
Family
ID=16415425
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2199897A Pending JPH0487699A (en) | 1990-07-27 | 1990-07-27 | Method for purifying polluted water region |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0487699A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH06285462A (en) * | 1992-05-01 | 1994-10-11 | Mito Kogyo Kk | Apparatus for purifying reservoir |
EP0995483A1 (en) * | 1998-10-23 | 2000-04-26 | The Procter & Gamble Company | A cross-flow filtration apparatus |
KR100408484B1 (en) * | 2000-12-20 | 2003-12-06 | 주식회사 앤바이오 | Treatment Equipment of Wastewater |
US20120228232A1 (en) * | 2007-07-31 | 2012-09-13 | Aquafiber Technologies Corp. | Water Remediation and Biosolids Collection System and Associated Methods |
-
1990
- 1990-07-27 JP JP2199897A patent/JPH0487699A/en active Pending
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH06285462A (en) * | 1992-05-01 | 1994-10-11 | Mito Kogyo Kk | Apparatus for purifying reservoir |
EP0995483A1 (en) * | 1998-10-23 | 2000-04-26 | The Procter & Gamble Company | A cross-flow filtration apparatus |
WO2000024499A1 (en) * | 1998-10-23 | 2000-05-04 | The Procter & Gamble Company | A cross-flow filtration apparatus |
KR100408484B1 (en) * | 2000-12-20 | 2003-12-06 | 주식회사 앤바이오 | Treatment Equipment of Wastewater |
US20120228232A1 (en) * | 2007-07-31 | 2012-09-13 | Aquafiber Technologies Corp. | Water Remediation and Biosolids Collection System and Associated Methods |
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