JPS6182894A - Apparatus for fluidized bed type biological treatment of waste water - Google Patents
Apparatus for fluidized bed type biological treatment of waste waterInfo
- Publication number
- JPS6182894A JPS6182894A JP59200566A JP20056684A JPS6182894A JP S6182894 A JPS6182894 A JP S6182894A JP 59200566 A JP59200566 A JP 59200566A JP 20056684 A JP20056684 A JP 20056684A JP S6182894 A JPS6182894 A JP S6182894A
- Authority
- JP
- Japan
- Prior art keywords
- fluidized bed
- nozzles
- wastewater
- group
- carrier particles
- 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
Links
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)
Abstract
Description
【発明の詳細な説明】
(産業上の利用分野)
この発明は処理槽内に設けた流動床に下から廃水を供給
して槽内に上昇流を形成し、この上昇流によって流動床
を構成する坦体粒子を流動化し、坦体粒子が坦持する微
生物で廃水を嫌気的又は好気的に処理する流動床式生物
処理装置に関する。Detailed Description of the Invention (Industrial Application Field) This invention supplies wastewater from below to a fluidized bed provided in a treatment tank to form an upward flow in the tank, and this upward flow forms a fluidized bed. The present invention relates to a fluidized bed biological treatment device that fluidizes carrier particles and treats wastewater anaerobically or aerobically with microorganisms supported by the carrier particles.
(従来の技術)
従来の装置では流動床下部にできるだけ均一に液を供給
して坦体粒子を良好に流動させるため、砂濾過における
支持層の様に、流動床の下に粒径の異なる砂利を用いた
支持床を設け、支持床中での砂利の粒度分布は下のもの
ほど大きく、上に向かつて次第て小さくシていた。(Prior art) In conventional equipment, in order to supply liquid as uniformly as possible to the bottom of the fluidized bed to ensure good fluidization of carrier particles, gravel of different particle sizes is placed under the fluidized bed, like a support layer in sand filtration. The particle size distribution of gravel in the support bed was larger at the bottom and gradually smaller towards the top.
(発明が解決すべき問題点)
上記により流動床下部に均一に液を供給することはで・
きるが、成る一定期間運転を経続すると坦体粒子上の微
生物と同種の増殖した微生物によって支持床を構成する
砂利相互の間隙が塞がれて支持床は閉塞し、その結果、
坦体粒子の流動が損われるばかりか、圧力上昇によって
運転の継続も不可能となる。(Problems to be solved by the invention) As described above, it is not possible to uniformly supply the liquid to the lower part of the fluidized bed.
However, if the operation continues for a certain period of time, the gaps between the gravels that make up the support bed will be clogged by the same type of microorganisms that have grown on the carrier particles, and the support bed will become clogged.
Not only is the flow of the carrier particles impaired, but the increased pressure also makes it impossible to continue operation.
このため、処理槽の底部に中底状に支持板を設けてその
上に流動床を形成し、上記支持板にノズルを分散して取
付け、ノズルを通じ流動床下部に液を供給する試みもあ
るが、この場合は支持板上のノズル相互の隣接間隔がデ
ッドスペースになってこ\に坦体粒子が沈積し、沈積し
た坦体粒子は坦持している微生物で互いに固着してデッ
ドスペースを次第に拡大すると言う問題点がある。For this reason, some attempts have been made to provide a mid-bottom support plate at the bottom of the treatment tank, form a fluidized bed on top of it, install nozzles in a distributed manner on the support plate, and supply liquid to the bottom of the fluidized bed through the nozzles. However, in this case, the space between adjacent nozzles on the support plate becomes a dead space, where carrier particles are deposited, and the deposited carrier particles stick to each other due to the microorganisms they carry, gradually filling the dead space. There is a problem with expanding.
(問題点を解決するための手段)
そこで本発明は処理槽の底部に液体を噴出する複数のノ
ズルを配置し、上記複数のノズルを複数の群に編成し、
各群に順次液体を供給する手段を設けたことを特徴とす
る。(Means for solving the problem) Therefore, the present invention arranges a plurality of nozzles that eject liquid at the bottom of a processing tank, organizes the plurality of nozzles into a plurality of groups,
It is characterized by providing means for sequentially supplying liquid to each group.
(作用)
複数の群が例えば第11第2の2群であるとすると、運
転中の成る時期は第1群のノズルに切換手段で液体を供
給して噴出させ、これとより流動床を流動化する。そし
て次の成る時期は第2群のノズルに切換手段で液体を供
給して噴出させ、これにより流動床を流動化し、これが
終れば再び第1群のノズルに液体を供給して噴出させる
。(Function) If the plurality of groups are, for example, the 11th, 2nd, and 2nd groups, during operation, liquid is supplied to the nozzles of the 1st group by the switching means and ejected, and this causes the fluidized bed to flow. become Then, at the next time, the switching means supplies the liquid to the nozzles of the second group and makes it eject, thereby fluidizing the fluidized bed, and when this is finished, the liquid is again supplied to the nozzles of the first group and makes it eject.
(実施例)
図示の各実施例において、lは処理槽、2は流動′床、
3α・・・は第1群のノズル、3b・・・は第2群のノ
ズル、μは両群のノズルに液体を切換えて供給するため
の切換パルプとして例示した切換手段を示し、切換手段
が各群のノズルに供給する液体は廃水の原液でもよいし
、処理槽内の循環液の一部でもよい。(Example) In each illustrated example, 1 is a treatment tank, 2 is a fluidized bed,
3α... indicates the nozzles of the first group, 3b... indicates the nozzles of the second group, μ indicates a switching means exemplified as a switching pulp for switching and supplying liquid to the nozzles of both groups, and the switching means is The liquid supplied to each group of nozzles may be an undiluted solution of wastewater, or may be a part of the circulating liquid in the treatment tank.
第1,2図の第1実施例では処理槽lの底部に中底状の
支持板jを設け、第1群と第2群のノズル3α・・・と
3b・・・とを全体として分散状に配置し、つまり第1
詳のノズル3αを均一に分散して配置し、第1ノズル群
のノズルの隣接間隔に第2群のノズル3btl−均一に
分散して配置する。In the first embodiment shown in Figs. 1 and 2, a mid-bottom support plate j is provided at the bottom of the processing tank l, and the nozzles 3α and 3b of the first and second groups are dispersed as a whole. In other words, the first
The detailed nozzles 3α are uniformly distributed and arranged, and the nozzles 3btl of the second group are uniformly distributed and arranged at adjacent intervals of the nozzles of the first nozzle group.
そして・第1群のノズル3α・・・に配管を接続したヘ
ッダー6αと、第2群のノズル3b・・・に配管を接続
したヘッダー6bを切換パルプ弘に接続し、運転中は切
換パルプを操作し第1群のノズル3α・・・に廃水の原
液又は槽内の循環液の一部を供給して噴出させ、流動床
を流動したら、次には第2群のノズル3b・・・に液を
供給して噴出させ、流動床を流動する。Then, the header 6α with piping connected to the first group of nozzles 3α... and the header 6b with piping connected to the second group of nozzles 3b... are connected to the switching pulp valve, and the switching pulp is switched off during operation. After operating the first group of nozzles 3α... to supply the undiluted waste water or a part of the circulating liquid in the tank and ejecting it to flow the fluidized bed, the second group of nozzles 3b... The liquid is supplied and ejected to flow the fluidized bed.
これにより、一方の群のノズルで流動床を流動化させて
いるとき、坦体粒子は上記一方のノズルの隣接間隔の支
持板上に沈積する傾向があるが、次に切換えて他方の群
のノズルで流動床を流動化する際に沈積した坦体粒子は
容易に流動化し、こうしてノズルの群に交互に、或いは
順番に廃水を供給し、微生物の増殖に起因する沈積した
坦体粒子相互の固着現象を確実に防止できる。This ensures that when one group of nozzles is fluidizing the fluidized bed, the carrier particles tend to deposit on the support plates at adjacent intervals of said one group, but then switch to the other group of nozzles. During fluidization of the fluidized bed in the nozzles, the deposited carrier particles are easily fluidized, thus feeding the groups of nozzles alternately or sequentially with wastewater, and preventing the deposited carrier particles from interacting with each other due to microbial growth. Sticking phenomenon can be reliably prevented.
ノズルの群に交互に、或いは順番に廃水を供給する時間
は約1分以上60分以内が好ましい。It is preferable that the time period for supplying wastewater to the groups of nozzles alternately or sequentially is about 1 minute or more and 60 minutes or less.
上記第1実施例は支持板上に第1群と第2nのノズルを
個々に取付けたが、第3図、第4゜5図の実施例の様に
支持板5を設けないで実施することもできる。In the first embodiment described above, the first group and the 2n nozzle were individually mounted on the support plate, but it can be carried out without providing the support plate 5 as in the embodiments shown in Figs. 3 and 4-5. You can also do it.
第3図の実施例は処理槽の底部l′に二本の十字形の中
空管7αと7bを処理槽の中心で約45°交叉させて配
置し、一方の中空管7αに第1群のノズル3α・・・を
設け、他方の中空管76に第2群のノズル3b・・・を
設は切換パルプψから容管7αと7b−に廃水を切換え
て供給する様にしたものである。。In the embodiment shown in FIG. 3, two cross-shaped hollow tubes 7α and 7b are arranged at the bottom l' of the treatment tank, crossing each other at an angle of about 45 degrees at the center of the treatment tank, and one hollow tube 7α has a first A group of nozzles 3α... are provided, and a second group of nozzles 3b... are provided in the other hollow pipe 76 to switch and supply wastewater from the switching pulp ψ to the container pipes 7α and 7b-. It is. .
又、第4,5図の実施例は処理槽の底部l′を断面三角
状の平行な谷部に構成し、この谷部内に平行に多数の中
空管lを敷設し、その一本置きの管tα・・・に第1群
のノズル3α・・・を設け、残りの一本置きの管rb・
・・に第2群のノズル3b・・・を設け、管tα・・・
はヘッダー6αで、管rb・・・はヘッダー6bで切換
パルプ44に接続したものである。この場合、各ノズル
3a・・・、 3bは溝の底に向かって液体を噴出する
様に取付けるとよい。容管のノズルから噴出した廃水が
流動床を流動化する領域を拡げることができるからであ
る。In addition, in the embodiment shown in Figs. 4 and 5, the bottom l' of the processing tank is formed into a parallel valley with a triangular cross section, and a large number of hollow tubes l are laid in parallel within this valley. The first group of nozzles 3α... are installed in the pipes tα..., and every other tube rb...
A second group of nozzles 3b... is provided in..., and a pipe tα...
is a header 6α, and pipes rb... are connected to the switching pulp 44 through a header 6b. In this case, each nozzle 3a, . . . , 3b may be installed so as to eject liquid toward the bottom of the groove. This is because it is possible to expand the area where the wastewater spouted from the nozzle of the container fluidizes the fluidized bed.
第3図、第4,5図の実施例の運転は第1実施例と同様
に行う。The embodiments shown in FIGS. 3, 4 and 5 are operated in the same manner as the first embodiment.
(効果)
以上の様に本発明によれば処理槽の底部で廃水を噴出し
て流動床を流動化するノズルをvII数の群に編成し、
各群のノズルから交互に又は順番に廃水を噴出する様に
したので流動床をは!均一に流動化できると共に、沈積
した坦体粒子が微生物で固着してデッドスペースを生じ
ることも防止できる。(Effects) As described above, according to the present invention, the nozzles that eject wastewater at the bottom of the treatment tank to fluidize the fluidized bed are organized into vII groups,
The wastewater is jetted out alternately or sequentially from each group of nozzles, creating a fluidized bed! In addition to uniform fluidization, it is possible to prevent the deposited carrier particles from becoming stuck with microorganisms and creating dead spaces.
第1図は本発明の第1実施例の縦断側面図、第2図は同
上の平面図、第3図は第2実施例の平面図、第4図は他
の一実施例の平面図、第5図は同上の要部の拡大縦断側
面図で、図中、/は処理槽、2は流動床、3αは第1群
のノズル、3bは第2群のノズル、弘は切換手段を示す
。
手続補正書相幻
昭和59年10月26日FIG. 1 is a longitudinal sectional side view of a first embodiment of the present invention, FIG. 2 is a plan view of the same as above, FIG. 3 is a plan view of a second embodiment, and FIG. 4 is a plan view of another embodiment. FIG. 5 is an enlarged longitudinal sectional side view of the main parts of the same as above, in which / indicates a processing tank, 2 indicates a fluidized bed, 3α indicates a first group of nozzles, 3b indicates a second group of nozzles, and Hiroshi indicates a switching means. . Procedural amendment minister Gengen October 26, 1982
Claims (3)
槽内に上昇流を形成し、この上昇流によつて流動床を構
成する坦体粒子を流動化し、坦体粒子が坦持する微生物
で廃水を処理する廃水の流動床式生物処理装置において
、 処理槽の底部に液体を噴出する複数のノズ ルを配置し、上記複数のノズルを複数の群に編成し、各
群に順次液体を供給する切換手段を設けたことを特徴と
する廃水の流動床式生物処理装置。(1) Wastewater is supplied from below to the fluidized bed installed in the treatment tank to form an upward flow in the tank, and this upward flow fluidizes the carrier particles that make up the fluidized bed. In a fluidized bed biological treatment device for wastewater that treats wastewater with supported microorganisms, multiple nozzles that eject liquid are placed at the bottom of the treatment tank, the multiple nozzles are organized into multiple groups, and each group is A fluidized bed biological treatment device for wastewater, characterized in that it is provided with switching means for sequentially supplying liquid.
液又は槽内循環液である廃水の流動床式生物処理装置。(2) A fluidized bed biological treatment device for wastewater in the device according to claim (1), wherein the wastewater is an undiluted solution or a circulating fluid in the tank.
、複数の全部の群のノズルの全体は処理槽の底部に均等
に分散して配置されている廃水の流動床式生物処理装置
。(3) In the device according to claim (1) or (2), all of the plurality of groups of nozzles are evenly distributed and arranged at the bottom of the treatment tank, a fluidized bed biological treatment device for wastewater. .
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP59200566A JPH0613118B2 (en) | 1984-09-27 | 1984-09-27 | Fluidized bed biological treatment equipment for wastewater |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP59200566A JPH0613118B2 (en) | 1984-09-27 | 1984-09-27 | Fluidized bed biological treatment equipment for wastewater |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS6182894A true JPS6182894A (en) | 1986-04-26 |
JPH0613118B2 JPH0613118B2 (en) | 1994-02-23 |
Family
ID=16426449
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP59200566A Expired - Fee Related JPH0613118B2 (en) | 1984-09-27 | 1984-09-27 | Fluidized bed biological treatment equipment for wastewater |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0613118B2 (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0240292A (en) * | 1988-07-27 | 1990-02-09 | Japan Organo Co Ltd | Apparatus for anaerobically treating upward flow |
JP2002192179A (en) * | 2000-12-22 | 2002-07-10 | Asahi Eng Co Ltd | Liquid dispersing nozzle |
JP2006346580A (en) * | 2005-06-16 | 2006-12-28 | Hitachi Zosen Corp | Water treatment method and apparatus of ammonia-containing wastewater |
-
1984
- 1984-09-27 JP JP59200566A patent/JPH0613118B2/en not_active Expired - Fee Related
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0240292A (en) * | 1988-07-27 | 1990-02-09 | Japan Organo Co Ltd | Apparatus for anaerobically treating upward flow |
JP2002192179A (en) * | 2000-12-22 | 2002-07-10 | Asahi Eng Co Ltd | Liquid dispersing nozzle |
JP2006346580A (en) * | 2005-06-16 | 2006-12-28 | Hitachi Zosen Corp | Water treatment method and apparatus of ammonia-containing wastewater |
Also Published As
Publication number | Publication date |
---|---|
JPH0613118B2 (en) | 1994-02-23 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
LAPS | Cancellation because of no payment of annual fees |