JPH11262753A - Method and apparatus for water treatment - Google Patents
Method and apparatus for water treatmentInfo
- Publication number
- JPH11262753A JPH11262753A JP6739098A JP6739098A JPH11262753A JP H11262753 A JPH11262753 A JP H11262753A JP 6739098 A JP6739098 A JP 6739098A JP 6739098 A JP6739098 A JP 6739098A JP H11262753 A JPH11262753 A JP H11262753A
- Authority
- JP
- Japan
- Prior art keywords
- water
- treated
- tank
- oxygen
- nitrogen
- 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
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/20—Treatment of water, waste water, or sewage by degassing, i.e. liberation of dissolved gases
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/46—Treatment of water, waste water, or sewage by electrochemical methods
- C02F1/461—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
- C02F1/46104—Devices therefor; Their operating or servicing
- C02F1/4618—Devices therefor; Their operating or servicing for producing "ionised" acidic or basic water
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/72—Treatment of water, waste water, or sewage by oxidation
-
- 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
- Aeration Devices For Treatment Of Activated Polluted Sludge (AREA)
- Physical Water Treatments (AREA)
- Water Treatment By Electricity Or Magnetism (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は水処理装置に係り、
特に、湖沼、河川、運河、貯水池、あるいは水槽等に対
する水処理装置に関する。TECHNICAL FIELD The present invention relates to a water treatment device,
In particular, the present invention relates to a water treatment device for a lake, a river, a canal, a reservoir, a water tank, or the like.
【0002】[0002]
【従来の技術】従来より、微生物が担持された処理層を
湖沼や水槽等の閉鎖水域中に浸積し、処理層の中央部に
立設された集水管にて周囲の水を吸引することにより、
処理層に被処理水を通過させる水質浄化装置が知られて
いる。この装置では、空気圧縮機から供給された圧縮空
気を、空気噴出部から集水管内に噴出させることによ
り、集水管内に水流を形成し、かつ被処理水に酸素を供
給している。2. Description of the Related Art Conventionally, a treatment layer carrying microorganisms has been immersed in a closed water area such as a lake or a water tank, and the surrounding water has been sucked by a water collection pipe provided in the center of the treatment layer. By
2. Description of the Related Art There is known a water purification device that allows treated water to pass through a treatment layer. In this device, the compressed air supplied from the air compressor is jetted from the air jetting section into the water collecting pipe, thereby forming a water flow in the water collecting pipe and supplying oxygen to the water to be treated.
【0003】[0003]
【発明が解決しようとする課題】ところで、上記水域に
おける水質低下の結果、アオコと呼ばれる藻類の発生が
問題となっている。また、アオコの発生を促進する要因
としては、水中の窒素、リン、二酸化炭素、及び有機化
合物の濃度の他、水温や水中の光量等が挙げられる。し
かしながら、上記水質浄化装置では、アオコの発生を防
止するために大量の微生物が必要となり、また、微生物
の活性が低下する冬場等には、十分に浄化処理を行うこ
とができなくなるという問題が生じている。本発明は上
記事情に鑑みてなされたもので、特に、水中の二酸化炭
素量を減少させてアオコの発生を防止することをその目
的としている。However, as a result of the deterioration of the water quality in the above-mentioned water area, the occurrence of algae called blue-green algae has become a problem. In addition, factors that promote the occurrence of blue water include the concentration of nitrogen, phosphorus, carbon dioxide, and organic compounds in water, the temperature of water, the amount of light in water, and the like. However, the water purification apparatus requires a large amount of microorganisms to prevent the occurrence of blue water, and there is a problem that purification treatment cannot be performed sufficiently in winter or the like when the activity of microorganisms decreases. ing. The present invention has been made in view of the above circumstances, and has as its object, in particular, to reduce the amount of carbon dioxide in water to thereby prevent the occurrence of blue-green algae.
【0004】[0004]
【課題を解決するための手段】本発明は上記事情に鑑み
てなされたもので、上記被処理水の処理に際し、被処理
水を酸性化する行程と、酸性化された上記被処理水を窒
素で曝気する行程と、窒素曝気後の上記被処理水を中和
する行程と、中和された上記被処理水を酸素で曝気する
行程とを備えることを特徴としている。SUMMARY OF THE INVENTION The present invention has been made in view of the above circumstances, and in the treatment of the above-mentioned water to be treated, a step of acidifying the water to be treated and a step of converting the acidified water to be treated with nitrogen. , A process of neutralizing the water to be treated after nitrogen aeration, and a process of aerating the neutralized water to be treated with oxygen.
【0005】ここで、酸性水とアルカリ水とを生成する
電解水生成装置を用意し、上記酸性水を用いて上記被処
理水を酸性化し、上記アルカリ水を用いて上記被処理水
を中和してもよい。[0005] Here, an electrolytic water generator for producing acidic water and alkaline water is prepared, the water to be treated is acidified by using the acidic water, and the water to be treated is neutralized by using the alkaline water. May be.
【0006】また、空気から窒素と酸素とを分離する気
体分離装置を用意し、分離された窒素を用いて上記被処
理水を窒素で曝気し、分離された酸素を用いて上記被処
理水を酸素で曝気してもよい。[0006] Further, a gas separation device for separating nitrogen and oxygen from air is prepared, and the water to be treated is aerated with nitrogen using the separated nitrogen, and the water to be treated is separated using the separated oxygen. It may be aerated with oxygen.
【0007】[0007]
【発明の実施の形態】以下、図面に基づき本発明の実施
形態について説明する。本発明に係る水処理装置の構造
の例を図1に示す。符号3は被処理水2を導水する管路
で、管路3には、上流側からフィルタ4及びポンプ5が
設けられ、かつ管路3の最下流側には、被処理水2から
酸性水とアルカリ水とを生成する電解水生成装置6が設
けられている。Embodiments of the present invention will be described below with reference to the drawings. FIG. 1 shows an example of the structure of the water treatment apparatus according to the present invention. Reference numeral 3 denotes a pipeline for guiding the water 2 to be treated. The pipeline 3 is provided with a filter 4 and a pump 5 from the upstream side. And an electrolyzed water generator 6 for generating alkaline water.
【0008】符号7は処理槽で、処理槽7内は隔壁8,
9により第一槽10、第二槽11、及び第三槽12に分
割され、かつ隔壁8の高さは隔壁9より高く設定されて
いる。また、第一槽10には、電解水生成装置6から酸
性水13供給用の管路14が延び、かつ第二槽11に
は、電解水生成装置6からアルカリ水15供給用の管路
16が延びている。一方、第三槽12には、開閉自在な
排出口17が設けられている。Reference numeral 7 denotes a processing tank.
The partition 9 is divided into a first tank 10, a second tank 11, and a third tank 12, and the height of the partition 8 is set higher than that of the partition 9. In the first tank 10, a pipe 14 for supplying the acidic water 13 from the electrolyzed water generator 6 extends, and in the second tank 11, a pipe 16 for supplying the alkaline water 15 from the electrolyzed water generator 6. Is extending. On the other hand, the third tank 12 is provided with a discharge port 17 that can be freely opened and closed.
【0009】符号18は、空気から窒素と酸素とを分離
する気体分離装置である。気体分離装置18からは、第
一槽10に向け窒素供給用の管路19が延び、管路19
の先端部19aは第一槽10の下端部にて水平に延設さ
れ、かつ先端部19aには、その延設方向に沿って複数
のノズル20が上方に向け形成されている。同様に、気
体分離装置18からは、第三槽12に向け酸素供給用の
管路21が延び、管路21の先端部21aは第三槽12
の下端部にて水平に延設され、かつ先端部21aには、
その延設方向に沿って複数のノズル22が上方に向け形
成されている。そして、上記フィルタ4、ポンプ5、電
解水生成装置6、処理槽7、気体分離装置18、及び管
路3,14,16,19,21から、水処理装置1が概
略構成されている。Reference numeral 18 denotes a gas separation device for separating nitrogen and oxygen from air. A line 19 for supplying nitrogen extends from the gas separation device 18 toward the first tank 10.
The tip 19a of the first tank 10 extends horizontally at the lower end of the first tank 10, and a plurality of nozzles 20 are formed on the tip 19a upward along the extending direction. Similarly, a line 21 for supplying oxygen extends from the gas separation device 18 toward the third tank 12, and a distal end 21 a of the line 21 is connected to the third tank 12.
Is extended horizontally at the lower end of the
A plurality of nozzles 22 are formed upward along the extension direction. The filter 4, pump 5, electrolyzed water generator 6, treatment tank 7, gas separator 18, and pipelines 3, 14, 16, 19, and 21 constitute a water treatment apparatus 1 in a schematic manner.
【0010】次に、上記構成を有する水処理装置1の動
作について説明する。被処理水2は、ポンプ5の作用に
より管路3内に導入され、フィルタ4を通過後、電解水
生成装置6にて、酸性水13とアルカリ水15とに分離
される。分離された酸性水13は管路14を介して第一
槽10に供給されるとともに、分離されたアルカリ水1
5は管路16を介して第ニ槽11に供給される。Next, the operation of the water treatment apparatus 1 having the above configuration will be described. The water to be treated 2 is introduced into the pipe 3 by the action of the pump 5, passes through the filter 4, and is separated into the acidic water 13 and the alkaline water 15 by the electrolytic water generator 6. The separated acidic water 13 is supplied to the first tank 10 through a pipe 14 and the separated alkaline water 1
5 is supplied to the second tank 11 via the pipe 16.
【0011】また、第一槽10には、気体分離装置18
から管路19を介して窒素が供給されている。この窒素
は、ノズル20から細かな気泡23となって第一槽10
内に噴出され、その結果、第一槽10内に貯留された酸
性水13が窒素で曝気され、酸性水13中の二酸化炭素
及び酸素が大気中に放出される。The first tank 10 includes a gas separation device 18.
Is supplied through a line 19 with nitrogen. This nitrogen forms fine bubbles 23 from the nozzle 20 and
As a result, the acidic water 13 stored in the first tank 10 is aerated with nitrogen, and carbon dioxide and oxygen in the acidic water 13 are released to the atmosphere.
【0012】曝気後の酸性水13は、隔壁8を越えて第
ニ槽11に流入し、第二槽11に供給されたアルカリ水
15と混合される。その結果、第ニ槽11内にて、酸性
水13がアルカリ水15により中和される。中和された
水は、隔壁9を越えて第三槽12に流入する。The acid water 13 after aeration flows into the second tank 11 over the partition 8 and is mixed with the alkaline water 15 supplied to the second tank 11. As a result, the acidic water 13 is neutralized by the alkaline water 15 in the second tank 11. The neutralized water flows into the third tank 12 over the partition wall 9.
【0013】また、第三槽12には、気体分離装置18
から管路21を介して酸素が供給されている。この酸素
は、ノズル22から細かな気泡24となって第三槽12
内に噴出され、その結果、第三槽12に貯留された水が
酸素で曝気され、水中の酸素が富化される。第三槽12
における貯水量が一定値を越えると、排出口17が開
き、第三槽12内の、二酸化炭素濃度が低く酸素濃度が
高い水(処理水)が、被処理水域に還流される。Further, a gas separating device 18 is provided in the third tank 12.
Is supplied through a pipe 21 from the oxygen supply. This oxygen is converted into fine bubbles 24 from the nozzle 22 to form the third tank 12.
As a result, the water stored in the third tank 12 is aerated with oxygen, and the oxygen in the water is enriched. Third tank 12
When the amount of water stored in exceeds the predetermined value, the outlet 17 is opened, and water (treated water) having a low carbon dioxide concentration and a high oxygen concentration in the third tank 12 is returned to the water area to be treated.
【0014】この水処理装置1では、被処理水2に由来
する酸性水13を第一槽10内にて窒素で曝気すること
により、水中の二酸化炭素が大気中に放出される。従っ
て、処理水の二酸化炭素濃度が低下し、アオコの発生が
抑制される。また、酸性水13は第二槽11内にて同じ
く被処理水2に由来するアルカリ水15で中和処理され
るため、処理水のpHが環境基準内に維持される。In the water treatment apparatus 1, the acidic water 13 derived from the water to be treated 2 is aerated in the first tank 10 with nitrogen, whereby carbon dioxide in the water is released into the atmosphere. Therefore, the concentration of carbon dioxide in the treated water is reduced, and the occurrence of blue water is suppressed. The acidic water 13 is also neutralized in the second tank 11 with the alkaline water 15 derived from the water 2 to be treated, so that the pH of the treated water is maintained within the environmental standard.
【0015】一方、第一槽10内における曝気に伴い酸
性水13中の酸素も大気中に放出されるが、第三槽12
内における曝気により供給された酸素により、処理水の
酸素濃度が高められる。従って、被処理水域における好
気性水性生物の生育が、処理水の供給により阻害される
ことはない。On the other hand, with the aeration in the first tank 10, oxygen in the acidic water 13 is also released into the atmosphere.
Due to the oxygen supplied by aeration in the inside, the oxygen concentration of the treated water is increased. Therefore, the growth of aerobic aquatic organisms in the water area to be treated is not hindered by the supply of treated water.
【0016】なお、電解水生成装置6を用いて酸性水1
3とアルカリ水15とを得る代わりに、酸及びアルカリ
を第一槽10及び第二槽11にそれぞれ供給し、被処理
水2の酸性化及び中和を行ってもよい。It is to be noted that the acidic water 1 is
Instead of obtaining 3 and the alkali water 15, an acid and an alkali may be supplied to the first tank 10 and the second tank 11, respectively, to acidify and neutralize the water 2 to be treated.
【0017】また、気体分離装置18として、酸素とそ
れ以外の気体とを分離する装置を用いてもよい。この場
合、第一槽10内の酸性水13には、酸素分離後の空
気、すなわち窒素と二酸化炭素とが供給されるが、二酸
化炭素は第一槽10内における曝気に伴い大気中に放出
されるため、二酸化炭素の供給による悪影響はない。Further, as the gas separating device 18, a device for separating oxygen from other gases may be used. In this case, air after oxygen separation, that is, nitrogen and carbon dioxide, is supplied to the acidic water 13 in the first tank 10, but the carbon dioxide is released into the atmosphere with the aeration in the first tank 10. Therefore, there is no adverse effect due to the supply of carbon dioxide.
【0018】[0018]
【発明の効果】以上説明した通り、本発明によれば、被
処理水中の二酸化炭素を大気中に放出することにより、
アオコの発生要因の一つである被処理水中の二酸化炭素
の濃度が低下する。よって、被処理水域におけるアオコ
の発生が抑制可能となる。As described above, according to the present invention, by releasing carbon dioxide in the water to be treated into the atmosphere,
The concentration of carbon dioxide in the water to be treated, which is one of the causes of blue water, decreases. Therefore, it is possible to suppress the occurrence of blue water in the water area to be treated.
【0019】また、被処理水を酸素で曝気することによ
り、被処理水の酸素濃度が高められるため、被処理水域
における好気性水性生物の生育が、処理された水の供給
により阻害されることはない。In addition, the oxygen concentration of the water to be treated is increased by aerating the water to be treated with oxygen, so that the growth of aerobic aquatic organisms in the water area to be treated is inhibited by the supply of the treated water. There is no.
【図1】 本発明に係る水処理装置の構造の例を示す図
である。FIG. 1 is a diagram showing an example of the structure of a water treatment apparatus according to the present invention.
1 水処理装置 2 被処理水 6 電解水生成装置 13 酸性水 15 アルカリ水 18 気体分離装置 DESCRIPTION OF SYMBOLS 1 Water treatment apparatus 2 Treated water 6 Electrolyzed water generation apparatus 13 Acid water 15 Alkaline water 18 Gas separation apparatus
Claims (3)
れた前記被処理水を窒素で曝気する行程と、窒素曝気後
の前記被処理水を中和する行程と、中和された前記被処
理水を酸素で曝気する行程とを有することを特徴とする
水処理方法。A step of acidifying the water to be treated, a step of aerating the acidified water to be treated with nitrogen, and a step of neutralizing the water to be treated after nitrogen aeration. A process of aerating the water to be treated with oxygen.
被処理水を窒素で曝気し、窒素曝気後の前記被処理水を
中和し、中和された前記被処理水を酸素で曝気する水処
理装置において、酸性水とアルカリ水とを生成する電解
水生成装置を備え、前記酸性水を用いて前記被処理水を
酸性化し、前記アルカリ水を用いて前記被処理水を中和
することを特徴とする水処理装置。2. The water to be treated is acidified, the acidified water to be treated is aerated with nitrogen, the water to be treated after aeration with nitrogen is neutralized, and the water to be neutralized is treated with oxygen. In the water treatment device for aeration, an electrolytic water generation device for producing acidic water and alkaline water is provided, the treated water is acidified using the acidic water, and the treated water is neutralized using the alkaline water. A water treatment apparatus, comprising:
被処理水を窒素で曝気し、窒素曝気後の前記被処理水を
中和し、中和された前記被処理水を酸素で曝気する水処
理装置において、空気から窒素と酸素とを分離する気体
分離装置を備え、分離された窒素を用いて前記被処理水
を窒素で曝気し、分離された酸素を用いて前記被処理水
を酸素で曝気することを特徴とする水処理装置。3. The water to be treated is acidified, the acidified water to be treated is aerated with nitrogen, the water to be treated after aeration with nitrogen is neutralized, and the neutralized water to be treated is treated with oxygen. In the water treatment device for aeration, a gas separation device for separating nitrogen and oxygen from air is provided, the treated water is aerated with nitrogen using separated nitrogen, and the treated water is separated using separated oxygen. A water treatment device characterized by aerating oxygen with oxygen.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6739098A JPH11262753A (en) | 1998-03-17 | 1998-03-17 | Method and apparatus for water treatment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6739098A JPH11262753A (en) | 1998-03-17 | 1998-03-17 | Method and apparatus for water treatment |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH11262753A true JPH11262753A (en) | 1999-09-28 |
Family
ID=13343616
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP6739098A Pending JPH11262753A (en) | 1998-03-17 | 1998-03-17 | Method and apparatus for water treatment |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH11262753A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2003047950A (en) * | 2001-08-01 | 2003-02-18 | Kurita Water Ind Ltd | Deoxygenation and decarboxylation treatment apparatus and treatment method |
WO2009083489A1 (en) * | 2007-12-21 | 2009-07-09 | Compagnie Gervais Danone | Method for enriching water with oxygen by an electrolytic process, oxygen enriched water or beverage and uses thereof |
CN104556281A (en) * | 2014-12-15 | 2015-04-29 | 中国第一重型机械股份公司 | Method for removing carbon dioxide contained in water |
-
1998
- 1998-03-17 JP JP6739098A patent/JPH11262753A/en active Pending
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2003047950A (en) * | 2001-08-01 | 2003-02-18 | Kurita Water Ind Ltd | Deoxygenation and decarboxylation treatment apparatus and treatment method |
WO2009083489A1 (en) * | 2007-12-21 | 2009-07-09 | Compagnie Gervais Danone | Method for enriching water with oxygen by an electrolytic process, oxygen enriched water or beverage and uses thereof |
US8709231B2 (en) | 2007-12-21 | 2014-04-29 | Compagnie Gervais Danone | Method for enriching water with oxygen by an electrolytic process, oxygen enriched water or beverage and uses thereof |
CN104556281A (en) * | 2014-12-15 | 2015-04-29 | 中国第一重型机械股份公司 | Method for removing carbon dioxide contained in water |
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