JP3130743B2 - Washing equipment for sedimentation separation equipment - Google Patents

Washing equipment for sedimentation separation equipment

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Publication number
JP3130743B2
JP3130743B2 JP06275211A JP27521194A JP3130743B2 JP 3130743 B2 JP3130743 B2 JP 3130743B2 JP 06275211 A JP06275211 A JP 06275211A JP 27521194 A JP27521194 A JP 27521194A JP 3130743 B2 JP3130743 B2 JP 3130743B2
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Japan
Prior art keywords
sedimentation
air
diffuser
tube
pipe
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.)
Expired - Lifetime
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JP06275211A
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Japanese (ja)
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JPH08131712A (en
Inventor
豊 石丸
睦生 山根
養藏 坂本
茂明 大原
Original Assignee
神鋼パンテツク株式会社
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Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は、液体、特に水、下水、
廃水などの処理において、懸濁粒子を含む被処理液体中
から懸濁粒子を両者の比重差を利用して沈降分離する装
置の洗浄装置に関する。
The present invention relates to liquids, in particular water, sewage,
The present invention relates to a cleaning device for a device that sediments and separates suspended particles from a liquid to be treated containing suspended particles by using a difference in specific gravity between the two in the treatment of wastewater or the like.

【0002】[0002]

【従来の技術および発明が解決しようとする課題】流通
する被処理液体中からの懸濁粒子の沈降を妨げる撹乱流
の発生を防止し、また液体中の懸濁粒子が流域の底部に
沈着するまでに降下しなければならない距離を減少する
ことにより、分離液の清澄度の向上、分離時間の短縮な
どの効果を得ることを目的として、多数の細長い管状通
路を一定の管断面の規則的配列のもとに互いに平行させ
て密集した集合体を傾斜させて沈殿槽内に配置し、この
管巣状集合体を通して被処理液体を流過させる傾斜管沈
降分離装置が知られている(例えば、特公昭55−37
927号公報参照)。この傾斜管沈降分離装置は、液体
より比重の大きい懸濁粒子の沈降分離および液体より比
重の小さい粒子の浮上分離のいずれにも用いられてお
り、多くの場合、懸濁物質は固体微粒子である。
2. Description of the Related Art The generation of a turbulent flow which hinders the settling of suspended particles from a flowing liquid to be treated is prevented, and the suspended particles in the liquid are deposited at the bottom of a basin. In order to improve the clarity of the separation liquid and shorten the separation time by reducing the distance that must be lowered, a large number of elongated tubular passages are regularly arranged in a fixed cross section. A slanted tube sedimentation / separation device is known in which a group of densely arranged parallel to each other is inclined and arranged in a sedimentation tank, and a liquid to be treated flows through the tube-shaped group of aggregates (for example, Tokiko Sho 55-37
927). This inclined tube sedimentation separation device is used for both sedimentation separation of suspended particles having a higher specific gravity than liquid and flotation separation of particles having a lower specific gravity than liquid, and in many cases, suspended solids are solid fine particles. .

【0003】次に、本発明の理解を容易にするために、
上記した特公昭55−37927号公報に記載された従
来の傾斜管沈降分離装置に関して、被処理液体中からこ
れより比重の大きい固体微粒子の懸濁物質を沈降分離す
る場合について、図5を参照しながら説明する。
Next, in order to facilitate understanding of the present invention,
Regarding the conventional inclined tube sedimentation and separation apparatus described in Japanese Patent Publication No. 55-37927, a case where a suspended substance of solid fine particles having a higher specific gravity is sedimented and separated from the liquid to be treated, with reference to FIG. I will explain it.

【0004】図5において、懸濁粒子を含む原水に化学
的凝集剤が添加されて撹拌混合され、この混合物がフロ
ック形成槽21に導入され、凝集剤のフロックは懸濁微
粒子と結合して比重の大きい大粒化された沈殿性のよい
粒子を形成し、この原水は傾斜管沈降分離装置22の流
入端に導かれる。傾斜管沈降分離装置22は、多数の細
長い管状通路を一定の管断面の規則的配列のもとに互い
に平行させて密集した集合体を水平に対して角度αをも
って傾斜配置したものである。上記原水は沈降分離装置
22の各管状通路を通って斜め上向きに分流し、その間
に懸濁粒子と結合したフロックは沈殿し、上記傾斜角度
αが沈殿物質の安息角より大きい角度とされているた
め、沈殿物質は管の底面上を液体の流れと反対方向に滑
り落ちて傾斜管沈降分離装置22の流入端のところで排
出されて汚泥集合タンク23の下部に集積され、周期的
にあるいは連続的にそこから除去される。他方、傾斜管
沈降分離装置22の上端から流出した清澄された液体は
容器24にあつめられ、そこから送り出される。
In FIG. 5, a chemical flocculant is added to raw water containing suspended particles, and the mixture is stirred and mixed. The mixture is introduced into a floc forming tank 21, and the floc of the flocculant is combined with the suspended fine particles to have a specific gravity. The raw water is led to the inflow end of the inclined pipe sedimentation / separation device 22. The inclined tube sedimentation / separation device 22 is a device in which a large number of elongated tubular passages are arranged parallel to each other under a regular arrangement of a fixed tube cross section, and a dense assembly is arranged at an angle α to the horizontal. The raw water diverges obliquely upward through each of the tubular passages of the sedimentation / separation device 22, during which the flocs combined with the suspended particles settle, and the inclination angle α is set to an angle larger than the angle of repose of the sedimented material. Therefore, the sedimented substance slides down on the bottom surface of the pipe in the direction opposite to the liquid flow, is discharged at the inflow end of the inclined pipe sedimentation / separation device 22, is collected in the lower part of the sludge collection tank 23, and is periodically or continuously. To be removed from there. On the other hand, the clarified liquid flowing out from the upper end of the inclined pipe sedimentation / separation device 22 is collected in the container 24 and sent out therefrom.

【0005】このように、傾斜管沈降分離装置は、一般
に原水の流路が多数の管状通路に分割されることによ
り、液体流に対する整流効果、懸濁粒子の沈降距離の短
縮および沈降面積の増大を図り、もって懸濁粒子の分離
効果を向上させたものであり、液体流中の懸濁粒子の有
効な沈殿分離を実現するためには、管状通路の液体流の
乱流化は避けねばならない。乱流条件の下では懸濁粒子
の沈降が著しく阻害されるからである。そこで、本出願
人は先に、組立が容易で、変形しにくく、沈殿物質の分
離が円滑に行われる構造の沈降分離装置として、図6に
示すように、略矢羽根形の管状通路断面25を有する懸
濁物質沈降分離装置に関する発明を特許出願した(特願
平5−334331号)。
[0005] As described above, in the inclined tube sedimentation / separation apparatus, the flow of raw water is generally divided into a large number of tubular passages, so that a rectifying effect on the liquid flow, a reduction in the settling distance of the suspended particles, and an increase in the settling area. In order to achieve effective sedimentation and separation of suspended particles in the liquid flow, turbulence of the liquid flow in the tubular passage must be avoided in order to achieve effective separation of suspended particles in the liquid flow . This is because sedimentation of suspended particles is significantly inhibited under turbulent conditions. Therefore, as shown in FIG. 6, the present applicant has previously described a sedimentation / separation device having a structure that is easy to assemble, hardly deforms, and smoothly separates sedimentary substances, as shown in FIG. (Japanese Patent Application No. 5-334331).

【0006】しかしながら、このような傾斜管沈降分離
装置においては、沈降分離されなかった懸濁物質が使用
期間を経るにつれて傾斜管表面に徐々に堆積する結果生
じる汚泥や付着藻類を適当なタイミングで洗浄しなけれ
ば、通過流路が閉塞されて偏流を起こすことがあり、効
果的な分離作業ができなくなってしまう。特に、夏期な
ど藻類が発生しやすい時期には、頻繁に洗浄を行わなけ
ればならない。この洗浄方法としては、例えば、以下に
示すような方式のものが知られている。
However, in such an inclined tube sedimentation / separation apparatus, sludge and attached algae resulting from the sedimentation of suspended substances that have not been settled and separated gradually on the surface of the inclined tube over a period of use are washed at an appropriate timing. Otherwise, the passage may be blocked, causing a drift, and an effective separation operation may not be performed. In particular, washing must be performed frequently during the period when algae are likely to occur, such as in summer. As this cleaning method, for example, the following method is known.

【0007】特開昭52−82862号公報には、原水
の流れを止め、沈殿槽内の原水を噴流発生装置によって
傾斜板間に噴射し、この噴射流と対流によって傾斜板沈
降装置内に堆積した汚泥や付着した微生物を強制剥離さ
せることを特徴とする、傾斜板沈降装置の洗浄方法とそ
の装置に関する発明が開示されている。しかし、この場
合、洗浄作業中は、沈降分離作業を休止する必要があ
る。また、一定の洗浄効果を得るためには、噴流発生用
のポンプ容量をある程度大きくする必要があり、ポンプ
が大型になると、吐出流が乱れ、一様に洗浄できないこ
とがある。
Japanese Patent Application Laid-Open No. 52-82862 discloses that the flow of raw water is stopped, the raw water in a sedimentation tank is jetted between inclined plates by a jet generator, and the jet flow and convection are accumulated in the inclined plate sedimentation device. There is disclosed an invention relating to a method for cleaning an inclined plate sedimentation apparatus, which is characterized by forcibly separating sludge and attached microorganisms, and an apparatus relating to the method. However, in this case, it is necessary to suspend the sedimentation separation operation during the washing operation. Further, in order to obtain a certain cleaning effect, it is necessary to increase the capacity of the pump for generating the jet flow to some extent. If the pump is large, the discharge flow may be disturbed and the cleaning may not be performed uniformly.

【0008】また、特開昭52−135461号公報に
は、傾斜板式沈降分離装置の傾斜板の上方に、層の列に
沿って配置された水噴射ノズルと水吸入管を一体に走行
可能に配設し、傾斜板面上に付着した汚泥を除去洗浄す
ることを特徴とする、傾斜板式沈降分離装置用自己洗浄
装置に関する発明が開示されている。しかし、この方式
では、走行台車・水中ポンプ等の設備コストが高く、ま
たこの台車やポンプ等の機械設備の保守点検作業が定期
的に必要となる。また、洗浄作業中は沈降分離作業を休
止する必要がある。
Japanese Patent Application Laid-Open No. 52-135461 discloses that a water injection nozzle and a water suction pipe arranged along a row of layers can be integrally moved above an inclined plate of an inclined plate type sedimentation / separation device. Disclosed is an invention relating to a self-cleaning device for an inclined plate type sedimentation separation device, which is disposed and removes and cleans sludge adhering to the inclined plate surface. However, in this method, the equipment cost of the traveling trolley, the submersible pump, and the like is high, and the maintenance and inspection work of the mechanical equipment such as the trolley and the pump is periodically required. In addition, it is necessary to suspend the sedimentation and separation operation during the washing operation.

【0009】さらに、特開昭62−79814号公報に
は、沈殿池内に吊り下げまたは桁上に支持する支持金具
が設けられ、その支持金具に加振機が装着されるように
して、傾斜沈降装置に付着堆積した汚泥を自動的に除去
することを特徴とする、傾斜沈降装置の洗浄方法および
装置に関する発明が開示されている。しかし、この方式
では、加振機の機械的振動が支持金具を経て傾斜沈降装
置に伝達されるため、これらを支持する部材の強度を高
める必要があり、設備コストが高くなる。
Further, Japanese Patent Application Laid-Open No. Sho 62-79814 discloses a method in which a support bracket is provided to be suspended or supported on a girder in a sedimentation basin, and a vibrator is mounted on the support bracket. There is disclosed an invention relating to a method and an apparatus for cleaning an inclined sedimentation apparatus, wherein sludge adhering to the apparatus is automatically removed. However, in this method, the mechanical vibration of the vibrator is transmitted to the inclined sedimentation device via the support fitting, so that it is necessary to increase the strength of the members supporting these, and the equipment cost increases.

【0010】本発明は従来の技術の有するこのような問
題点に鑑みてなされたものであって、その目的は、沈降
分離作業を中断することなく、効率よく均一に洗浄する
ことが可能な、低コストの沈降分離装置用洗浄装置を提
供することにある。
[0010] The present invention has been made in view of such problems of the prior art, and an object thereof is to enable efficient and uniform cleaning without interrupting the sedimentation / separation operation. An object of the present invention is to provide a low-cost settling / separation apparatus cleaning apparatus.

【0011】[0011]

【課題を解決するための手段】上記目的を達成するため
に本発明は、沈殿槽内に設置した傾斜板または傾斜管内
を流通する、懸濁粒子を含む被処理液体から該懸濁粒子
を両者の比重差を利用して沈降分離する沈降分離装置に
用いる洗浄装置であって、上記沈殿槽の底部にスラッジ
を掻き取るための台車を走行自在に設け、該台車に該台
車とともに移動することが可能な多数のエア吐出口を有
する散気管を具備したことを特徴とする沈降分離装置用
洗浄装置を第一の発明とし、上記第一の発明において、
上記エア吐出口より散気管内に短管を装入し、該短管に
散気管内壁面頂部位置より下位となるようにエア流入用
の小孔を形成したことを特徴とする沈降分離装置用洗浄
装置を第二の発明とし、沈殿槽内に設置した傾斜板また
は傾斜管内を流通する、懸濁粒子を含む被処理液体から
該懸濁粒子を両者の比重差を利用して沈降分離する沈降
分離装置に用いる洗浄装置であって、上記沈殿槽の底部
を走行自在の台車に、該台車とともに移動することが可
能な多数のエア吐出口を有する散気管を具備し、エア吐
出口より散気管内に短管を装入し、該短管に散気管内壁
面頂部位置より下位となるようにエア流入用の小孔を形
成したことを特徴とする沈降分離装置用洗浄装置を第三
の発明とする。
In order to achieve the above object, the present invention provides a method for converting both suspended particles from a liquid to be treated containing suspended particles flowing through an inclined plate or inclined tube installed in a settling tank. A sedimentation separation apparatus for sedimentation separation using a specific gravity difference, wherein a bogie for scraping sludge is provided at the bottom of the sedimentation tank so as to be able to run freely, and the bogie can be moved together with the bogie. The first invention is a sedimentation / separation device cleaning device characterized by having an air diffuser having a large number of air discharge ports, and in the first invention,
A sedimentation separation device, wherein a short pipe is inserted into the diffuser from the air discharge port, and a small hole for air inflow is formed in the short pipe so as to be lower than the top position of the inner wall of the diffuser. The washing apparatus according to the second aspect of the present invention, in which the suspended particles are settled from the liquid to be treated containing the suspended particles by utilizing the difference in the specific gravity of the liquid to be treated, which flows through the inclined plate or the inclined tube installed in the sedimentation tank. A washing device used for a separation device, comprising: a carriage that can travel on the bottom of the sedimentation tank; and an air diffuser having a large number of air discharge ports that can move together with the carriage. A third aspect of the present invention is a washing apparatus for a sedimentation separation device, wherein a short pipe is inserted into the pipe, and a small hole for air inflow is formed in the short pipe so as to be lower than the top position of the inner wall of the diffuser pipe. And

【0012】[0012]

【作用】沈殿槽の底部を常時一定の速度で走行しながら
底部に溜まったスラッジを掻き取ることができる台車に
具備した散気管から所定量のエアを吐出することによ
り、沈降分離作業を中断することなく、傾斜板または傾
斜管表面に付着・堆積した汚泥や藻類を除去することが
できる。エア吐出口より散気管内に装入した短管に散気
管内壁面頂部位置より下位となるようにエア流入用の小
孔を形成することにより、散気管内の水は散気管に送給
されたエアの圧力により押し下げられ、水面が小孔のレ
ベル以下になった後、始めて短管内にエアは流入する。
その後、傾斜板または傾斜管内を洗浄するために必要な
所定量のエアを散気管内に給気しなければならないが、
そのとき給気されたエアは小孔を通過する際に抵抗を受
け、小孔から吐出されるエア量より散気管に供給される
エア量が多くなるため、散気管内の圧力が高くなり、散
気管内の水位はさらに下がり、一定水位で安定する。こ
のとき全ての小孔は散気管内の水面より上部に位置する
ので、散気管の据え付けレベルに多少の誤差があって
も、散気管の複数の小孔から均一にエアを吐出すること
ができる。
The sedimentation and separation operation is interrupted by discharging a predetermined amount of air from an air diffuser provided on a truck capable of scraping sludge accumulated at the bottom while constantly running at the constant speed at the bottom of the sedimentation tank. Without removing sludge and algae attached and deposited on the surface of the inclined plate or inclined tube. Water in the diffuser is supplied to the diffuser by forming a small hole for air inflow in the short pipe inserted into the diffuser from the air discharge port so that it is lower than the top position of the inner wall of the diffuser. Only after the water is pushed down by the pressure of the air and the water level falls below the level of the stoma, the air flows into the short pipe.
After that, a predetermined amount of air necessary for cleaning the inside of the inclined plate or the inclined pipe must be supplied into the diffuser pipe,
The air supplied at that time receives resistance when passing through the small hole, and the amount of air supplied to the diffuser tube is larger than the amount of air discharged from the small hole, so the pressure in the diffuser tube increases, The water level in the air diffuser falls further and stabilizes at a constant water level. At this time, all the small holes are located above the water surface in the air diffuser, so that even if there is some error in the installation level of the gas diffuser, air can be uniformly discharged from the plural small holes of the gas diffuser. .

【0013】[0013]

【実施例】以下に本発明の実施例を図面を参照しながら
説明する。図1は沈殿槽の側断面図である。図1におい
て、1は矢示方向に沿ってこの沈殿槽の底部を自在に走
行してスラッジを掻き取ることができる台車である。2
は高圧のエアを送給するエアホースであり、このエアホ
ースは、沈殿槽のほぼ中央部に沿って敷設したガイドレ
ール3内に配した、ホース支持案内装置であるケーブル
ベヤ4にガイドされながら、台車1とともに沈殿槽内を
矢示方向に移動することができる。5は多数設置した傾
斜管であり、この傾斜管内を懸濁粒子を含む被処理水が
下方から上方に向けて流過しつつ懸濁粒子が沈降分離さ
れる。
Embodiments of the present invention will be described below with reference to the drawings. FIG. 1 is a side sectional view of a sedimentation tank. In FIG. 1, reference numeral 1 denotes a bogie that can freely travel along the bottom of the sedimentation tank along the direction of the arrow to scrape sludge. 2
Is an air hose for supplying high-pressure air. The air hose is guided by a cable carrier 4 which is a hose supporting and guiding device disposed in a guide rail 3 laid along substantially the center of the sedimentation tank. At the same time, it can move in the settling tank in the direction of the arrow. Reference numeral 5 denotes a plurality of inclined pipes, in which the water to be treated containing suspended particles flows upward from below in the inclined pipe, and the suspended particles are settled and separated.

【0014】図2は傾斜管を除いた沈殿槽の平面図であ
る。図2において、6は台車1に付設した散気管であ
り、その詳細は図3に示す通りである。図3において、
エアホースの先端は、矢示7で示すように散気管6に接
続されており、エアホースを経て散気管6内に流入した
エアは、短管11から上方に向けて吐出される。供給す
るエア量は短管11の1個当たり3L/min.の条件であ
る。なお、供給するエア量が多いほど傾斜管に衝突する
エア量が多くなり洗浄効果はよくなる。ただし、エア量
が短管11の1個当たり5L/min.より多いと、大量の
気泡が傾斜管に衝突し、傾斜管が過剰に振動して破損す
ることがあり、さらに必要以上にエア供給動力が必要で
ランニングコスト増大につながる。また、1L/min.よ
り少ないと、傾斜管に衝突するエア量が少なくなり、傾
斜管に適度の振動を与えることができず、洗浄効果が減
少する。さらに、散気管内のエアの圧力が小さくなるた
め、散気管内の水位が上昇し、いくつかの小孔は水没し
てしまい、すべての小孔から均一にエアを吐出させるこ
とができない。よって供給するエア量は、短管11の1
個当たり1L/min.〜5L/min.が好ましい。散気管6
からエアを吐出する方式として、図4(b)に示すよう
に、散気管6の頂部に形成したエア吐出口9を経てエア
を吐出する方式では、散気管6内の水の脈動10が激し
く、エア吐出口が水で塞がれることがあり、複数の各エ
ア吐出口から均一にエアを吐出することができない。
FIG. 2 is a plan view of the sedimentation tank without the inclined tube. In FIG. 2, reference numeral 6 denotes an air diffuser attached to the truck 1, the details of which are as shown in FIG. In FIG.
The end of the air hose is connected to the diffuser 6 as indicated by an arrow 7, and the air that has flowed into the diffuser 6 via the air hose is discharged upward from the short pipe 11. The amount of air supplied is 3 L / min. Per one short pipe 11. It should be noted that the greater the amount of air supplied, the greater the amount of air colliding with the inclined tube, and the better the cleaning effect. However, if the amount of air is more than 5 L / min. Per one of the short pipes 11, a large amount of air bubbles collide with the inclined pipe, and the inclined pipe may be excessively vibrated and damaged, and furthermore, the air supply more than necessary. Power is required, leading to increased running costs. If the flow rate is less than 1 L / min., The amount of air colliding with the inclined tube is reduced, so that an appropriate vibration cannot be given to the inclined tube, and the cleaning effect is reduced. Further, since the pressure of the air in the air diffuser is reduced, the water level in the air diffuser rises, and some small holes are submerged, so that air cannot be uniformly discharged from all the small holes. Therefore, the amount of air supplied is one of the short pipes 11.
It is preferably 1 L / min. To 5 L / min. Diffuser 6
As shown in FIG. 4B, in the method of discharging air from the air diffuser 6 through an air discharge port 9 formed at the top of the diffuser 6, the pulsation 10 of water in the diffuser 6 is severe. In some cases, the air discharge ports are blocked by water, and the air cannot be discharged uniformly from the plurality of air discharge ports.

【0015】しかし、図4(a)に示すように、エア吐
出口9より散気管6内に短管11を装入し、この短管1
1に散気管内壁面頂部位置より下位となるように小孔1
2を形成し、短管11内へはこの小孔12を経てエアが
通入されるようにすれば、散気管6内に送給されたエア
の圧力により散気管6内の水面が押し下げられ、この水
面が上部の小孔12のレベル以下になった後、始めて短
管11内にエアは流入する。従って、図4(b)のよう
に、散気管6内に激しい水の脈動が生じることはなく、
図4(a)に示すように、散気管6内の水面レベルはほ
ぼ水平となる。
However, as shown in FIG. 4A, a short pipe 11 is inserted into the air diffuser 6 from the air discharge port 9 and
A small hole 1 is located below the top of the inner wall of the diffuser tube.
2 is formed and air is allowed to flow into the short pipe 11 through the small holes 12, so that the water surface in the diffusion pipe 6 is pushed down by the pressure of the air supplied into the diffusion pipe 6. Only after this water level falls below the level of the upper small hole 12 does air flow into the short pipe 11. Therefore, as shown in FIG. 4B, there is no strong pulsation of water in the air diffuser 6.
As shown in FIG. 4A, the water surface level in the air diffuser 6 is substantially horizontal.

【0016】その結果、作用の項で述べたごとく、複数
の短管11から均一にエアを吐出することができる。
As a result, air can be uniformly discharged from the plurality of short tubes 11 as described in the section of operation.

【0017】また、散気管6内に流入したエアの圧力が
かなり高い場合は、下部の小孔12のレベルまで水面が
押し下げられた後、上部と下部の両方の小孔12から短
管11内にエアは流入する。本実施例では、短管11に
上部の小孔と下部の小孔からなる2個の小孔を設けた
が、小孔の数はこれに限定されず、1個でも3個以上で
もよい。すなわち、エアがその小孔を通過する際に抵抗
を受けるような小孔を短管11に設ければよいのであ
る。
When the pressure of the air flowing into the air diffuser 6 is considerably high, the water surface is pushed down to the level of the small holes 12 at the lower part. Air flows into the air. In the present embodiment, the short tube 11 is provided with two small holes including the upper small hole and the lower small hole, but the number of small holes is not limited to this, and may be one or three or more. That is, a small hole may be provided in the short tube 11 so that the air receives resistance when passing through the small hole.

【0018】なお、本発明の沈降分離装置用洗浄装置
は、本実施例で示すように、被処理水を下方から上方に
向けて通す傾斜管を洗浄するだけでなく、被処理水を上
方から下方に向けて通す傾斜管、または被処理水を横方
向に通す傾斜板等を洗浄することも可能である。
As shown in the present embodiment, the washing apparatus for a sedimentation / separation apparatus of the present invention not only cleans an inclined pipe through which water to be treated is passed upward from below, but also cleans the water to be treated from above. It is also possible to wash a sloped pipe that passes downward, or a sloped plate that horizontally passes water to be treated.

【0019】[0019]

【発明の効果】本発明は上記のとおり構成されているの
で、次の効果を奏する。 請求項1記載の発明によれば、既設の台車に散気管
を付設するだけでよいから、設備コストを低減すること
ができるが、もちろん、新設の場合も台車に散気管を取
り付けるだけの構成でよいから、設備コストは低減でき
る。
Since the present invention is configured as described above, the following effects can be obtained. According to the first aspect of the present invention, it is only necessary to attach an air diffuser to an existing truck, so that equipment costs can be reduced. Because it is good, equipment costs can be reduced.

【0020】また、洗浄箇所が散気管上に限定されるの
で、フロック等の巻き上げの発生範囲が局所的であり、
巻き上げられたフロックの量も少ないので、処理水中に
混入したとしても、処理水質を悪化させることがないた
め、沈降分離作業を続行しながら洗浄することが可能で
ある。
Further, since the washing point is limited on the air diffuser, the range of the roll-up of the flocks or the like is local,
Since the amount of the wound up flocks is small, the quality of the treated water is not deteriorated even if it is mixed in the treated water, so that it is possible to wash while continuing the sedimentation and separation work.

【0021】さらに、散気管が台車とともに移動しつつ
洗浄を行う方式であるから、一度に多量の空気を使用す
ることがなく、傾斜管全体を洗浄できる。また、必要空
気量が比較的少量ですみ、所要動力が少なくなるという
効果が期待できる。
Furthermore, since the cleaning is performed while the air diffuser moves with the carriage, the entire inclined pipe can be cleaned without using a large amount of air at a time. In addition, an effect that a relatively small amount of air is required and the required power is reduced can be expected.

【0022】 請求項2、3記載の発明によれば、散
気管の各エア吐出口から吐出されるエアのばらつきが少
なくなるので、洗浄効率が一層改善される。
According to the second and third aspects of the present invention, the variation in the air discharged from each air discharge port of the air diffuser is reduced, so that the cleaning efficiency is further improved.

【図面の簡単な説明】[Brief description of the drawings]

【図1】沈殿槽の側断面図である。FIG. 1 is a side sectional view of a sedimentation tank.

【図2】傾斜管を除いた沈殿槽の平面図である。FIG. 2 is a plan view of the sedimentation tank without an inclined tube.

【図3】本発明の散気管の正面図である。FIG. 3 is a front view of the air diffuser according to the present invention.

【図4】図4(a)は小孔を有する短管をエア吐出口よ
り散気管内に装入した状態を示す側断面図、図4(b)
は散気管の頂部にエア吐出口を設けた場合を示す側断面
図である。
FIG. 4 (a) is a side sectional view showing a state in which a short pipe having a small hole is inserted into an air diffuser from an air discharge port, and FIG. 4 (b).
FIG. 4 is a side sectional view showing a case where an air discharge port is provided at the top of an air diffuser.

【図5】従来の傾斜管沈降分離装置の概略構成図であ
る。
FIG. 5 is a schematic configuration diagram of a conventional inclined pipe sedimentation separation apparatus.

【図6】従来の傾斜管沈降分離装置の管状通路の断面を
示す図である。
FIG. 6 is a view showing a cross section of a tubular passage of a conventional inclined pipe sedimentation separation apparatus.

【符号の説明】[Explanation of symbols]

1…台車 5…傾斜管 6…散気管 9…エア吐出口 11…短管 12…小孔 DESCRIPTION OF SYMBOLS 1 ... Dolly 5 ... Inclined pipe 6 ... Diffusion pipe 9 ... Air discharge port 11 ... Short pipe 12 ... Small hole

───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 平6−63321(JP,A) 特開 昭63−1408(JP,A) 特開 昭57−48309(JP,A) 特開 昭55−18227(JP,A) 実開 昭56−34507(JP,U) (58)調査した分野(Int.Cl.7,DB名) B01D 21/00 - 21/34 ──────────────────────────────────────────────────続 き Continuation of front page (56) References JP-A-6-63321 (JP, A) JP-A-63-1408 (JP, A) JP-A-57-48309 (JP, A) JP-A 55-48 18227 (JP, A) Japanese Utility Model Showa 56-34507 (JP, U) (58) Fields investigated (Int. Cl. 7 , DB name) B01D 21/00-21/34

Claims (3)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 沈殿槽内に設置した傾斜板または傾斜管
内を流通する、懸濁粒子を含む被処理液体から該懸濁粒
子を両者の比重差を利用して沈降分離する沈降分離装置
に用いる洗浄装置であって、上記沈殿槽の底部にスラッ
ジを掻き取るための台車を走行自在に設け、該台車に
台車とともに移動することが可能な多数のエア吐出口を
有する散気管を具備したことを特徴とする沈降分離装置
用洗浄装置。
The present invention is applied to a sedimentation / separation apparatus which sediments and separates suspended particles from a liquid to be treated containing suspended particles by using a specific gravity difference between the liquids to be treated, which flows through an inclined plate or inclined tube installed in a sedimentation tank. A washing device, which is provided with a sludge on the bottom of the sedimentation tank.
A washing device for a sedimentation separation device, comprising: a carriage for scraping a jig, which is provided so as to be freely movable, and the carriage having an air diffuser having a large number of air discharge ports capable of moving together with the carriage .
【請求項2】 上記エア吐出口より散気管内に短管を装
入し、該短管に散気管内壁面頂部位置より下位となるよ
うにエア流入用の小孔を形成したことを特徴とする請求
項1記載の沈降分離装置用洗浄装置。
2. A short pipe is inserted from the air discharge port into the diffuser pipe, and a small hole for air inflow is formed in the short pipe so as to be lower than the top position of the inner wall of the diffuser pipe. The washing device for a sedimentation separation device according to claim 1.
【請求項3】 沈殿槽内に設置した傾斜板または傾斜管
内を流通する、懸濁粒子を含む被処理液体から該懸濁粒
子を両者の比重差を利用して沈降分離する沈降分離装置
に用いる洗浄装置であって、上記沈殿槽の底部を走行自
在の台車に、該台車とともに移動することが可能な多数
のエア吐出口を有する散気管を具備し、エア吐出口より
散気管内に短管を装入し、該短管に散気管内壁面頂部位
置より下位となるようにエア流入用の小孔を形成したこ
を特徴とする沈降分離装置用洗浄装置。
3. A sedimentation / separation apparatus which sediments and separates suspended particles from a liquid to be treated, which contains suspended particles, through a slant plate or a slant tube installed in a sedimentation tank by utilizing a specific gravity difference between the two. a cleaning apparatus, the carriage freely traveling bottom of the settling tank, comprising a diffuser tube having a number of air discharge opening which can be moved together with the該台vehicle, from the air discharge port
A short tube is inserted into the diffuser tube, and the short tube is placed at the top of the inner wall of the diffuser tube.
Small holes for air inflow are formed below
And a washing device for a sedimentation separation device.
JP06275211A 1994-11-09 1994-11-09 Washing equipment for sedimentation separation equipment Expired - Lifetime JP3130743B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP06275211A JP3130743B2 (en) 1994-11-09 1994-11-09 Washing equipment for sedimentation separation equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP06275211A JP3130743B2 (en) 1994-11-09 1994-11-09 Washing equipment for sedimentation separation equipment

Publications (2)

Publication Number Publication Date
JPH08131712A JPH08131712A (en) 1996-05-28
JP3130743B2 true JP3130743B2 (en) 2001-01-31

Family

ID=17552250

Family Applications (1)

Application Number Title Priority Date Filing Date
JP06275211A Expired - Lifetime JP3130743B2 (en) 1994-11-09 1994-11-09 Washing equipment for sedimentation separation equipment

Country Status (1)

Country Link
JP (1) JP3130743B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0475075U (en) * 1990-11-13 1992-06-30

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5518227A (en) * 1978-07-24 1980-02-08 Ebara Infilco Co Ltd Waste water treating apparatus
JPS5634507U (en) * 1979-08-28 1981-04-04
JPS5748309A (en) * 1980-09-08 1982-03-19 Japan Organo Co Ltd Washing apparatus for precipitation promoting material
JPS631408A (en) * 1986-06-23 1988-01-06 Hitachi Ltd Washing appratus for slanted part in settling apparatus
JP2599538B2 (en) * 1992-08-14 1997-04-09 日本碍子株式会社 Inclined plate type sedimentation tank and method for preventing clogging thereof

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0475075U (en) * 1990-11-13 1992-06-30

Also Published As

Publication number Publication date
JPH08131712A (en) 1996-05-28

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