JPH06278681A - Raw water treatment device - Google Patents
Raw water treatment deviceInfo
- Publication number
- JPH06278681A JPH06278681A JP5092164A JP9216493A JPH06278681A JP H06278681 A JPH06278681 A JP H06278681A JP 5092164 A JP5092164 A JP 5092164A JP 9216493 A JP9216493 A JP 9216493A JP H06278681 A JPH06278681 A JP H06278681A
- Authority
- JP
- Japan
- Prior art keywords
- raw water
- container
- water
- partition plate
- air
- 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.)
- Withdrawn
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
【0001】[0001]
【産業上の利用分野】本発明は、船舶のビルジ水や陸上
の含油廃水(特に乳化油を含む廃水)のごとき汚濁成分
を有する原水について、浄化処理を行なうための装置に
関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an apparatus for purifying raw water having pollutant components such as bilge water of ships and oil-containing wastewater on land (especially wastewater containing emulsified oil).
【0002】[0002]
【従来の技術】図5に示す従来の円筒型流動床式生物処
理装置について説明すると、流動床装置本体としての容
器1の内部には、微生物等を付着させる粒子としての付
着担体fを含んだ水が満たされている。そして、微生物
や、その他の汚濁成分を含む原水cが原水流入管4を通
じて容器1内へ流入するようになっている。容器1の内
部は仕切板5によって分割されており、これにより下部
で相互に連通した流動部Aと沈殿部Bとが形成されてい
る。2. Description of the Related Art A conventional cylindrical fluidized bed type biological treatment apparatus shown in FIG. 5 will be described. Inside a container 1 as a fluidized bed apparatus main body, an adhering carrier f as particles for adhering microorganisms and the like is included. The water is full. Then, raw water c containing microorganisms and other pollutant components flows into the container 1 through the raw water inflow pipe 4. The inside of the container 1 is divided by a partition plate 5, whereby a fluidized portion A and a sedimented portion B which are in communication with each other are formed in the lower portion.
【0003】また、容器1の流動部Aには、円筒管3a
で形成されたエアリフト部3と、その下方に配置された
空気管2とが設けられ、空気管2から噴き上げられた空
気aがエアリフト部3により上方へ案内されるようにな
っている。そして、空気aがエアリフト部3内を上昇す
る際に生じる駆動力によって、流動部Aの混合液bと付
着担体fとが上昇し、やがて水面に達すると下方に向か
って流れることによって流動部A内は混合される。その
間、空気aの中の酸素が混合液bに溶解する。これに対
し、原水cは、原水流入管4から流入して混合されなが
ら、それに含まれる汚濁成分(有機物,油分)を分解除
去される。Further, in the flow section A of the container 1, a cylindrical tube 3a is provided.
The air lift portion 3 formed in 1 and the air pipe 2 arranged below the air lift portion 3 are provided, and the air a blown up from the air pipe 2 is guided upward by the air lift portion 3. Then, due to the driving force generated when the air a rises in the air lift unit 3, the mixed liquid b and the adhering carrier f of the flow unit A rise, and when they reach the water surface, they flow downward so that they flow. The inside is mixed. During that time, oxygen in the air a is dissolved in the mixed liquid b. On the other hand, the raw water c flows through the raw water inflow pipe 4 and is mixed with the raw water c while decomposing and removing the pollutant components (organic substances and oil components) contained therein.
【0004】流動部A内の混合液bの大部分は、このよ
うにして循環・混合されるが、その一部は沈殿部Bに流
入する。沈殿部Bは仕切板5によって流動部Aと区画さ
れているが、その下部は連通しているので、流動部A内
の一部の分離液dは、沈殿部Bを上昇しながらやがて水
面に達し、溢流堰6から溢流して処理水トラフ7で処理
水eとなって合流したのち、処理水管8を介して排出さ
れる。なお分離液dと混在する付着担体fが沈殿部Bを
上昇するとき、水よりも比重の大きい粒子としての付着
担体fは、沈殿部Bの下部で沈降し、分離液dと分離す
る。Most of the mixed liquid b in the flow section A is circulated and mixed in this way, but a part thereof flows into the precipitation section B. The settling section B is partitioned by the partition plate 5 from the fluidized section A, but since the lower part thereof communicates, a part of the separated liquid d in the fluidized section A rises up in the settling section B and eventually reaches the water surface. After reaching and overflowing from the overflow weir 6 to form the treated water e in the treated water trough 7, the treated water e is combined and then discharged through the treated water pipe 8. When the adhering carrier f mixed with the separation liquid d rises in the precipitation part B, the adhesion carrier f as particles having a larger specific gravity than water settles in the lower part of the precipitation part B and separates from the separation liquid d.
【0005】図6には従来の角型の流動床式生物処理装
置の構造を示す。その構造は、原理的には図5の円筒型
と全く同じであるが、主な相違点は次のとおりである。
すなわち、図5におけるエアリフト部3が、図6では流
動床本体1とエアリフト板3’aとで囲まれたエアリフ
ト部3’に相当する。また図5の溢流堰6は円筒型の容
器1と同心円状に配置されているが、図6では溢流堰6
がエアリフト部3’と反対側の部分にのみ配設されてい
る。FIG. 6 shows the structure of a conventional prismatic fluidized bed type biological treatment apparatus. Its structure is in principle the same as that of the cylindrical type shown in FIG. 5, but the main differences are as follows.
That is, the air lift portion 3 in FIG. 5 corresponds to the air lift portion 3 ′ surrounded by the fluidized bed body 1 and the air lift plate 3′a in FIG. Further, the overflow weir 6 in FIG. 5 is arranged concentrically with the cylindrical container 1, but in FIG.
Are disposed only on the portion opposite to the air lift portion 3 '.
【0006】[0006]
【発明が解決しようとする課題】前述のような従来の装
置を船舶のビルジ水等の処理に使用する場合、以下のよ
うな課題がある。 (1) 従来の装置では仕切板5が固定されている。しかし
ビルジ水を生物処理するにつれて、粒子としての付着担
体fが、肥大化して粒子径が増加し、流動部Aと沈殿部
Bとの連通部に付着担体fが積層し、詰まる現象が発生
した。またそれによって流動部Aにおける付着担体fの
濃度が減少し、処理性能が安定しないという課題があっ
た。 (2) 船舶に搭載すると、航行中の船の上下動の揺れによ
って沈殿部Bでの付着担体fが巻き上がる。そのため沈
殿部Bで水dと付着担体fとが完全には分離せず、最悪
の場合は付着担体fが水dと共に処理水eに漏出する。When the above-mentioned conventional apparatus is used for treating bilge water of a ship, there are the following problems. (1) In the conventional device, the partition plate 5 is fixed. However, as the bilge water is biologically treated, the adhering carrier f as particles is enlarged and the particle size is increased, and the adhering carrier f is laminated at the communication part between the fluidized section A and the settling section B to cause a phenomenon of clogging. . Further, there is a problem that the concentration of the adhered carrier f in the fluidized section A is reduced and the processing performance is not stable. (2) When mounted on a ship, the adhered carrier f in the sedimentation part B is rolled up due to the vertical swing of the ship during navigation. Therefore, the water d and the adhesive carrier f are not completely separated in the settling section B, and in the worst case, the adhesive carrier f leaks into the treated water e together with the water d.
【0007】[0007]
【課題を解決するための手段】本発明の原水処理装置
は、微生物等を付着させる粒子としての付着担体を含ん
だ水を満たされる容器と、同容器に原水を流入させる原
水流入部と、上記容器の底部内で上方へ空気を噴き上げ
るように配設された空気管と、同空気管から噴出する空
気を上方へ案内するエアリフト部と、同エアリフト部の
上部から上記容器の底部へ内部液を流動させる流動部
と、同流動部から仕切板で仕切られながら同仕切板の下
方の連通口で同流動部と連通するように同流動部に隣接
して配設された沈殿部と、同沈殿部の上部で上記容器の
壁部上縁に形成された溢流堰とをそなえ、上記容器の底
部内で上記仕切板の下端のレベルにより規制される上記
連通口の開口面積を調整すべく、上記仕切板の昇降機構
が設けられたことを特徴としている。The raw water treatment apparatus of the present invention comprises a container filled with water containing an adherent carrier as particles for adhering microorganisms and the like, and a raw water inflow section for introducing raw water into the container. An air pipe arranged to blow air upward in the bottom of the container, an air lift portion that guides the air ejected from the air pipe upward, and an internal liquid from the top of the air lift portion to the bottom of the container. The fluidizing part to be fluidized, the sedimentation part which is arranged adjacent to the fluidizing part so that the fluidizing part is separated from the fluidizing part by the partition plate and communicates with the fluidizing part at the communication port below the partition plate. With an overflow weir formed on the upper edge of the wall of the container at the upper part of the portion, in order to adjust the opening area of the communication port regulated by the level of the lower end of the partition plate in the bottom of the container, A special feature is that the partition plate lifting mechanism is provided. It is set to.
【0008】[0008]
【作用】上述の本発明の原水処理装置では、次のような
作用が行なわれる。 (1) 流動部と沈殿部との間の仕切板を上下に移動調節し
て、流動部と沈殿部との連通口を所要の開口面積に設定
する。 (2) ビルジ水等の原水を導入し始めた当初には連通口の
開口面積を小さくし、生物処理が進行して付着担体が肥
大化し粒子径が増加するにつれて、連通口の開口面積を
大きく設定する。これによって連通口における水の通過
速度は低下し、付着担体どうしが分散する。 (3) 本装置が船体等に装備されて揺動を生じた場合、連
通口の開口面積を小さくすることにより、流動部内の混
合液と付着担体の揺動が沈殿部内へ伝播して影響を及ぼ
す程度は少なくなる。The raw water treatment apparatus of the present invention described above has the following actions. (1) The partition plate between the fluidizing section and the sedimentation section is moved up and down to adjust the communication port between the fluidizing section and the sedimentation section to a desired opening area. (2) At the beginning of introducing raw water such as bilge water, the opening area of the communication port was made small, and the opening area of the communication port was increased as the biological treatment progressed and the adhering carrier enlarged and the particle size increased. Set. As a result, the speed at which water passes through the communication port decreases, and the adhering carriers are dispersed. (3) When this device is mounted on a hull or the like and causes rocking, the rocking of the mixed liquid in the flow part and the adherent carrier propagates into the sedimentation part to reduce the influence by reducing the opening area of the communication port. The effect is small.
【0009】[0009]
【実施例】以下、図面により本発明の第1実施例として
の原水処理装置について説明すると、図1はその縦断面
図、図2はその平面図であって、本装置は円筒型の流動
床式生物処理手段として構成され、図1,2に示された
流動部A,沈殿部B,空気管a,混合液b,原水c,分
離液d,処理水eおよび付着担体fは、図5に同符号で
示されたものとほぼ同じものである。すなわち、微生物
等を付着させる粒子としての付着担体fを含んだ水を満
たされる容器1に、原水流入部としての原水流入管4が
接続されており、また同容器1の底部内で上方へ空気を
噴き上げるように配設された空気管2と、同空気管2か
らの空気を上方へ案内する円筒管3aで形成されたエア
リフト部3が設けられている。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS A raw water treatment apparatus as a first embodiment of the present invention will be described below with reference to the drawings. FIG. 1 is a longitudinal sectional view thereof, FIG. 2 is a plan view thereof, and the apparatus is a cylindrical fluidized bed. The fluidized portion A, the sedimentation portion B, the air pipe a, the mixed liquid b, the raw water c, the separated liquid d, the treated water e and the adhering carrier f shown in FIGS. Are almost the same as those indicated by the same reference numerals. That is, a raw water inflow pipe 4 as a raw water inflow part is connected to a container 1 filled with water containing an adherent carrier f as particles for adhering microorganisms and the like. An air lift portion 3 formed by an air pipe 2 arranged to blow up the air and a cylindrical pipe 3a for guiding the air from the air pipe 2 upward is provided.
【0010】そして、エアリフト部3の下端から上記空
気により円筒管3aの内部を通って上方へ誘導された原
水を含む内部液が、エアリフト部3の上部から容器1の
底部へ流動するように、流動部Aが形成されるととも
に、同流動部Aから仕切板5で仕切られながら同仕切板
5の下方の連通口5aで同流動部Aと連通する沈殿部B
が、流動部Aに隣接して配設されている。また、沈殿部
Bの上部で容器1の壁部上縁に形成された溢流堰6が設
けられている。さらに、本発明では容器1の底部内で仕
切板5の下端のレベルにより規制される連通口5aの開
口面積を調整できるように、仕切板5の昇降機構が設け
られている。Then, the internal liquid containing the raw water, which is guided upward from the lower end of the air lift portion 3 through the inside of the cylindrical pipe 3a by the air, flows from the upper portion of the air lift portion 3 to the bottom portion of the container 1, The flow section A is formed, and the settling section B which is partitioned from the flow section A by the partition plate 5 and communicates with the flow section A at the communication port 5a below the partition plate 5.
Is disposed adjacent to the flow section A. Further, an overflow weir 6 formed on the upper edge of the wall portion of the container 1 is provided above the precipitation portion B. Further, in the present invention, a lifting mechanism for the partition plate 5 is provided so that the opening area of the communication port 5a regulated by the level of the lower end of the partition plate 5 in the bottom of the container 1 can be adjusted.
【0011】すなわち、上記昇降機構として、仕切板5
と同仕切板5に固定された接続金具9とを懸吊するラッ
ク式軸10が設けられるとともに、同ラック式軸10を上下
動させるラック式駆動部11が設けられている。なお、本
実施例では連通口5aが仕切板5の下端と容器1の傾斜
壁1aとの間に形成されるようになっているが、この傾
斜壁1aの代りに棚板状の部材を容器1の内壁から突設
してもよく、要する仕切板5の昇降により連通口5aの
開口面積が増減するように形成されていればよい。That is, the partition plate 5 is used as the lifting mechanism.
A rack type shaft 10 for suspending and a connection fitting 9 fixed to the partition plate 5 is provided, and a rack type drive unit 11 for vertically moving the rack type shaft 10 is provided. In this embodiment, the communication port 5a is formed between the lower end of the partition plate 5 and the inclined wall 1a of the container 1. However, instead of the inclined wall 1a, a shelf plate-shaped member is used for the container. It may be provided so as to project from the inner wall of No. 1 and may be formed so that the opening area of the communication port 5a is increased or decreased by the required elevation of the partition plate 5.
【0012】仕切板5を上下方向に移動させる場合、ラ
ック式駆動部11を回転作動させることによって、ラック
式軸10を上方または下方に移動させる。そして、ラック
式軸10の移動は接続金具9を介して仕切板5に伝えら
れ、仕切板5が上方または下方に移動することになる。
なお、駆動部11は手動式または電動式のいずれでも実施
可能である。流動部A内の一部の分離液dは、沈殿部B
を上昇しながらやがて水面に達し、溢流堰6から溢流し
て処理水トラフ7で処理水eとなって合流したのち、処
理水管8を介して排出される。なお分離液dと混在する
付着担体fが沈殿部Bを上昇するとき、水よりも比重の
大きい粒子としての付着担体fは、沈殿部Bの下部で沈
降し、分離液dと分離する。When the partition plate 5 is moved in the vertical direction, the rack type driving unit 11 is rotated to move the rack type shaft 10 upward or downward. Then, the movement of the rack shaft 10 is transmitted to the partition plate 5 via the connection fitting 9, and the partition plate 5 moves upward or downward.
It should be noted that the drive unit 11 can be implemented either manually or electrically. A part of the separated liquid d in the fluidized section A is
After reaching the water surface while rising, the water overflows from the overflow weir 6 and becomes the treated water e in the treated water trough 7 and joins, and then is discharged through the treated water pipe 8. When the adhering carrier f mixed with the separation liquid d rises in the precipitation part B, the adhesion carrier f as particles having a larger specific gravity than water settles in the lower part of the precipitation part B and separates from the separation liquid d.
【0013】本実施例の原水処理装置は上述のように構
成されているので、流動部Aと沈殿部Bとの間の仕切板
5を上下に移動調節して、流動部Aと沈殿部Bとの連通
口5aが所要の開口面積に設定されるが、ビルジ水等の
原水を導入し始めた当初には仕切板5を下降させて連通
口5aの開口面積を小さくする。そして生物処理が進行
して付着担体fが肥大化し粒子径が増加するにつれて、
仕切板5の上昇により連通口5aの開口面積を大きく設
定する。このように開口面積を大きくすると、連通口5
aにおける水の通過速度は低下し、付着担体fどうしが
分散するようになる。また本装置が船体に装備されて機
関室ビルジ水などの処理に用いられる場合、船体の動揺
時には連通口5aの開口面積を小さくすることにより、
流動部A内の混合液bと付着担体fの揺動が沈殿部B内
へ伝播するのを抑制することができる。Since the raw water treatment apparatus of this embodiment is constructed as described above, the partition plate 5 between the fluidizing section A and the sedimenting section B is vertically moved to adjust the fluidizing section A and the sedimentation section B. The opening area of the communication port 5a is set to a required opening area, but at the beginning of introducing raw water such as bilge water, the partition plate 5 is lowered to reduce the opening area of the communication port 5a. Then, as the biological treatment progresses and the adherent carrier f is enlarged and the particle size is increased,
By raising the partition plate 5, the opening area of the communication port 5a is set large. When the opening area is increased in this way, the communication port 5
The passing speed of water in a decreases and the adhering carriers f are dispersed. Further, when this device is mounted on a hull and used for treatment of engine room bilge water, by reducing the opening area of the communication port 5a when the hull sways,
It is possible to suppress the oscillation of the mixed liquid b and the adhering carrier f in the fluidized portion A from propagating into the sedimented portion B.
【0014】なお、本装置の使用に際し、生物馴致を開
始するときおよび通常運転を継続するときは、連通口5
aの開口面積は水の通過速度が2m/h以下となるように
設定される。また付着担体fが肥大化するにつれて、仕
切板5の下方への移動により、連通口5aの開口面積
は、水の通過速度が1m/h以下となるように設定され
る。船体の動揺に伴い本装置の揺動が始まったときは、
連通口5aの開口面積は、水の通過速度が0.5m/h以下
となるように設定される。When using this apparatus, when starting the biocompatibility and continuing the normal operation, the communication port 5
The opening area of a is set so that the water passing speed is 2 m / h or less. Further, as the adhering carrier f is enlarged, the partition plate 5 is moved downward so that the opening area of the communication port 5a is set such that the water passage speed is 1 m / h or less. When the device starts rocking due to the motion of the hull,
The opening area of the communication port 5a is set so that the water passage speed is 0.5 m / h or less.
【0015】次に、本発明の第2実施例を図3(縦断面
図)および図4(平面図)に示す。この第2実施例は角
型の流動床式生物処理手段として構成され、基本的構造
は図1,2の円筒型のものと同じであるが、主な相違点
は次のとおりである。すなわち、図1のエアリフト部3
は、図3で流動床本体としての容器1の壁部とエアリフ
ト板3’aとで囲まれたエアリフト部3’に相当する。
また図1の溢流堰6は円筒型の容器1と同心円状に配置
されているが、図3では溢流堰6がエアリフト部3’と
反対側の部分にのみ配設されている。なお連通口5aの
開口面積の設定手段については、第1実施例とほぼ同様
に仕切板5の昇降機構10,11として構成されている。そ
して、この第2実施例の場合も、第1実施例と同様の作
用効果を得ることができる。Next, a second embodiment of the present invention is shown in FIG. 3 (longitudinal sectional view) and FIG. 4 (plan view). The second embodiment is configured as a prismatic fluidized bed type biological treatment means, and the basic structure is the same as that of the cylindrical type of FIGS. 1 and 2, but the main differences are as follows. That is, the air lift portion 3 of FIG.
Corresponds to the air lift portion 3 ′ surrounded by the wall portion of the container 1 as the fluidized bed body and the air lift plate 3′a in FIG.
Further, the overflow weir 6 in FIG. 1 is arranged concentrically with the cylindrical container 1, but in FIG. 3 the overflow weir 6 is arranged only in a portion opposite to the air lift portion 3 ′. The means for setting the opening area of the communication port 5a is constructed as the lifting mechanisms 10 and 11 for the partition plate 5 in substantially the same manner as in the first embodiment. Also in the case of the second embodiment, it is possible to obtain the same effects as those of the first embodiment.
【0016】[0016]
【発明の効果】以上詳述したように、本発明の原水処理
装置によれば、次のような効果が得られる。 (1) 流動部Aと沈殿部Bとの仕切板5が昇降可能に構成
されて、流動部Aと沈殿部Bとの連通口5aの開口面積
を自在に設定できるようにしたので、船舶のビルジ水等
の処理のための流動床式生物処理手段として使用するこ
とが可能となる。 (2) 上記連通口5aの開口面積を広くして同連通口にお
ける水の通過速度を下げることにより、肥大化した付着
担体fが積層する現象を抑制することができる。これに
よって流動部Aの付着担体fの濃度はほぼ一定となり、
処理性能を安定化させるという効果が得られる。 (3) 本装置を船舶等に用いた場合の動揺時に、連通口5
aの開口面積を小さくすることで、流動部A内の付着担
体fの揺動が沈殿部B内へ伝播するのを抑制できるとい
う効果が生じる。As described in detail above, according to the raw water treatment apparatus of the present invention, the following effects can be obtained. (1) Since the partition plate 5 between the flow section A and the settling section B is configured to be able to move up and down, and the opening area of the communication port 5a between the flow section A and the settling section B can be freely set. It can be used as a fluidized bed type biological treatment means for treating bilge water and the like. (2) By widening the opening area of the communication port 5a to reduce the passage speed of water through the communication port, it is possible to suppress a phenomenon in which the enlarged adherent carriers f are stacked. As a result, the concentration of the adhered carrier f in the fluidized portion A becomes almost constant,
The effect of stabilizing the processing performance can be obtained. (3) The communication port 5 is
By reducing the opening area of a, it is possible to suppress the swing of the adhering carrier f in the fluidized portion A from propagating into the sedimented portion B.
【0017】またこの場合肥大化した付着担体fは、流
動部Aにおける混合液の揺動により連通口5aの付近で
は分散されるという効果も生じる。これによって、流動
部A内の付着担体fが処理水e中に流入することを防止
でき、安定した処理水水質が得られる。Further, in this case, the enlarged adhering carrier f also has the effect of being dispersed in the vicinity of the communication port 5a due to the rocking of the mixed liquid in the flow section A. This can prevent the adhering carrier f in the fluidized section A from flowing into the treated water e, and a stable treated water quality can be obtained.
【図1】本発明の第1実施例として原水処理装置の縦断
面図である。FIG. 1 is a vertical sectional view of a raw water treatment apparatus as a first embodiment of the present invention.
【図2】図1の原水処理装置の平面図である。FIG. 2 is a plan view of the raw water treatment device of FIG.
【図3】本発明の第2実施例としての原水処理装置の縦
断面図である。FIG. 3 is a vertical sectional view of a raw water treatment device as a second embodiment of the present invention.
【図4】図3の原水処理装置の平面図である。FIG. 4 is a plan view of the raw water treatment device of FIG.
【図5】従来の原水処理装置の一例を示す縦断面図であ
る。FIG. 5 is a vertical sectional view showing an example of a conventional raw water treatment device.
【図6】従来の原水処理装置の他の例を示す縦断面図で
ある。FIG. 6 is a vertical sectional view showing another example of a conventional raw water treatment device.
1 容器 1a 傾斜壁 2 空気管 3,3’ エアリフト部 3a 円筒管 3’a エアリフト板 4 原水流入管 5 仕切板 6 溢流堰 7 処理水トラフ 8 処理水管 9 ラック式軸 10 ラック式駆動部 A 流動部 B 沈殿部 a 空気 b 混合液 c 原水 d 分離液 e 処理水 f 付着担体 1 Container 1a Inclined wall 2 Air pipe 3,3 'Airlift part 3a Cylindrical pipe 3'a Airlift plate 4 Raw water inflow pipe 5 Partition plate 6 Overflow weir 7 Treated water trough 8 Rack type shaft 10 Rack type drive part A Flowing part B Precipitating part a Air b Mixed liquid c Raw water d Separated liquid e Treated water f Adhesive carrier
フロントページの続き (72)発明者 大川 義昭 神戸市兵庫区小松通五丁目1番16号 株式 会社神菱ハイテック内Front Page Continuation (72) Inventor Yoshiaki Okawa 5-16 Komatsudori, Hyogo-ku, Kobe Inside Shinryo High-Tech Co., Ltd.
Claims (1)
担体を含んだ水を満たされる容器と、同容器に原水を流
入させる原水流入部と、上記容器の底部内で上方へ空気
を噴き上げるように配設された空気管と、同空気管から
噴出する空気を上方へ案内するエアリフト部と、同エア
リフト部の上部から上記容器の底部へ内部液を流動させ
る流動部と、同流動部から仕切板で仕切られながら同仕
切板の下方の連通口で同流動部と連通するように同流動
部に隣接して配設された沈殿部と、同沈殿部の上部で上
記容器の壁部上縁に形成された溢流堰とをそなえ、上記
容器の底部内で上記仕切板の下端のレベルにより規制さ
れる上記連通口の開口面積を調整すべく、上記仕切板の
昇降機構が設けられたことを特徴とする、原水処理装
置。1. A container filled with water containing an adherent carrier as particles for adhering microorganisms and the like, a raw water inflow part for allowing raw water to flow into the container, and air blown upward in the bottom part of the container. An air pipe arranged, an air lift part for guiding the air ejected from the air pipe upward, a flow part for flowing the internal liquid from the upper part of the air lift part to the bottom part of the container, and a partition plate from the flow part. While being partitioned by the partition plate, a settling section disposed adjacent to the fluidizing section so as to communicate with the fluidizing section at the lower communication port of the partitioning plate, and on the upper edge of the wall of the container above the settling section. A lifting mechanism for the partition plate is provided in order to adjust the opening area of the communication port, which is provided with an overflow weir and is regulated by the level of the lower end of the partition plate in the bottom of the container. Characteristic raw water treatment equipment.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP5092164A JPH06278681A (en) | 1993-03-26 | 1993-03-26 | Raw water treatment device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP5092164A JPH06278681A (en) | 1993-03-26 | 1993-03-26 | Raw water treatment device |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH06278681A true JPH06278681A (en) | 1994-10-04 |
Family
ID=14046794
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP5092164A Withdrawn JPH06278681A (en) | 1993-03-26 | 1993-03-26 | Raw water treatment device |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH06278681A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2009050750A (en) * | 2007-08-23 | 2009-03-12 | Ihi Corp | Fluidized-bed method and facility for treating waste water aerobically |
JP2009166902A (en) * | 2009-04-20 | 2009-07-30 | Hitachi Ltd | Purification water supply system |
WO2012155467A1 (en) * | 2011-05-17 | 2012-11-22 | 南京大学 | Resin ion exchange and adsorption reactor of continuous-flow internal circulation simulated fluidized bed |
-
1993
- 1993-03-26 JP JP5092164A patent/JPH06278681A/en not_active Withdrawn
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2009050750A (en) * | 2007-08-23 | 2009-03-12 | Ihi Corp | Fluidized-bed method and facility for treating waste water aerobically |
JP2009166902A (en) * | 2009-04-20 | 2009-07-30 | Hitachi Ltd | Purification water supply system |
WO2012155467A1 (en) * | 2011-05-17 | 2012-11-22 | 南京大学 | Resin ion exchange and adsorption reactor of continuous-flow internal circulation simulated fluidized bed |
US8758608B2 (en) | 2011-05-17 | 2014-06-24 | Nanjing University | Continuously flowing, inner circulatory, quasi-fluidized-bed reactor for resin ion exchange and adsorption |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
A300 | Withdrawal of application because of no request for examination |
Free format text: JAPANESE INTERMEDIATE CODE: A300 Effective date: 20000530 |