JP5812237B2 - Precipitation device for sediment in water tank - Google Patents

Precipitation device for sediment in water tank Download PDF

Info

Publication number
JP5812237B2
JP5812237B2 JP2010229054A JP2010229054A JP5812237B2 JP 5812237 B2 JP5812237 B2 JP 5812237B2 JP 2010229054 A JP2010229054 A JP 2010229054A JP 2010229054 A JP2010229054 A JP 2010229054A JP 5812237 B2 JP5812237 B2 JP 5812237B2
Authority
JP
Japan
Prior art keywords
screw
water
sediment
separation
pressure
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.)
Active
Application number
JP2010229054A
Other languages
Japanese (ja)
Other versions
JP2012066233A (en
Inventor
井上 虎男
虎男 井上
Original Assignee
井上 虎男
虎男 井上
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by 井上 虎男, 虎男 井上 filed Critical 井上 虎男
Priority to JP2010229054A priority Critical patent/JP5812237B2/en
Publication of JP2012066233A publication Critical patent/JP2012066233A/en
Application granted granted Critical
Publication of JP5812237B2 publication Critical patent/JP5812237B2/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Landscapes

  • Treatment Of Sludge (AREA)

Description

本発明は一般水槽や水処理設備の沈殿分離槽内の沈殿物を槽外に排除する装置に関するものである。  The present invention relates to an apparatus for removing precipitates in a sedimentation separation tank of a general water tank or a water treatment facility.

水槽内の沈殿物を排除、或いは回収するためには、チェーンやロープに掻き板を取付け一定方向に掻き寄せ、或いは、上半を開放したケースとスクリューで構成するスクリューコンベヤーで一定方向に移送集積した後、遠心ポンプや容積形ポンプで吸引、或いは垂直や傾斜して配設したスクリューコンベヤーを用いて水槽外に排除する等の方法がある。  In order to eliminate or collect sediment in the water tank, a scraper is attached to the chain or rope, scraped in a certain direction, or transported and accumulated in a certain direction by a screw conveyor consisting of a case and screw with the upper half open. After that, there is a method of suctioning with a centrifugal pump or a positive displacement pump, or removing it outside the water tank using a screw conveyor arranged vertically or inclined.

特開2001−347103  JP 2001-347103 A 特開2003−334404  JP 2003-334404 A 特開2005−342568  JP-A-2005-342568 特開2008−12528  JP2008-12528

集積した沈殿物汚泥を遠心ポンプや容積形ポンプを使用して水槽外に排出する方法にあっては、集積汚泥量とポンプ排出量を終始一致させることは、検出技術が発達した今日においても非常に困難なことであり、沈殿物を沈殿状態以下の水分量で排除回収することは至難なことであり、結局、余分な水分も吸入させて排除しているのが現状である。  In the method of discharging accumulated sediment sludge to the outside of the water tank using a centrifugal pump or positive displacement pump, it is very important that the accumulated sludge amount matches the pump discharge amount throughout the day even when the detection technology has developed. It is difficult to eliminate and recover the precipitate with a water content below the precipitation state. In the present situation, excess water is also inhaled and removed.

垂直方向、或いは、傾斜したスクリューコンベヤーを用いる方法にあっても、凝集剤を使用して沈降分離するような軽質、微細粒子の沈殿物の場合においては、沈殿状態水分量のままでの排除は困難であり、スクリュー詰りも生じやすい。  Even in the case of using a screw conveyor that is vertical or inclined, in the case of a light and fine particle precipitate that is settled and separated using a flocculant, the moisture content in the precipitated state is not excluded. It is difficult and screw clogging is likely to occur.

沈殿物汚泥の水分量を減らすために、水平移送用スクリューコンベヤーの先端部に加圧部とフイルター機構を連接して、絞り機能を備えたものにあっては、取扱調整が煩雑であるばかりでなく、特に微細粒子を取扱う設備ではフイルタートラブルが多く好ましくない。  In order to reduce the amount of water in the sediment sludge, the handling and adjustment are just cumbersome if the pressurizing part and the filter mechanism are connected to the tip of the screw conveyor for horizontal transfer and have a throttling function. In particular, facilities that handle fine particles are not preferable because of many filter troubles.

また、重力式沈殿分離法の一種である横流れ方式の沈殿分離装置は、分離水槽内に、通水方向に対して平行で、通水方向に直角な平面内では大きく傾斜させた分離板を層状に多数配列して沈殿分離を早めるようにした装置であり、傾斜分離板下方には沈殿物貯留部を設けるのであるが、傾斜分離板を密集させた分離板間の被処理液の通水流路よりも、抵抗の少ない被処理水の流水路となるために、これを防止すべく通水方向に直角な粗流板を複数配列して区画する。  In addition, the cross-flow type sedimentation separation device, which is a type of gravity sedimentation separation method, has a layered separation plate in the separation water tank that is largely inclined in a plane parallel to the water flow direction and perpendicular to the water flow direction. In order to speed up the precipitation separation, a sediment reservoir is provided below the inclined separation plate, but the flow path of the liquid to be treated between the separation plates in which the inclined separation plates are closely packed In order to provide a flow channel for water to be treated with less resistance, a plurality of rough flow plates perpendicular to the water flow direction are arranged and partitioned to prevent this.

しかし、連続操業のできる装置とするためには、分離板長さ全範囲にわたる沈殿物の掻き寄せ等の移送設備が必要であり、該移送設備には、やむなく生じる通水方向の貫通したスペースがあり、流水抵抗も比較的少なくなりやすいために充分な沈降分離がなされないばかりでなく、傾斜分離板から沈降する分離汚泥を再混入させる流路(以下“くぐり水路”と呼ぶ)となり、傾斜分離板終端近くに再流入(以下“くぐり水”と呼ぶ)して処理水に混合流出し、分離性能を低下させる問題が実験結果から判明している。  However, in order to obtain a device that can be operated continuously, it is necessary to have a transfer facility such as scraping of sediment over the entire length of the separation plate, and the transfer facility has an unavoidably penetrating space in the water passage direction. In addition, since the resistance to running water is relatively low, not only is sufficient sedimentation separated, but it also becomes a channel that re-mixes the separated sludge that settles from the inclined separation plate (hereinafter referred to as “recessed channel”). From the experimental results, it has been found that there is a problem that the re-inflow near the end of the plate (hereinafter referred to as “kug water”) flows out into the treated water and deteriorates the separation performance.

沈殿分離水槽等の水槽底にほぼ水平に配設した移送用のスクリューコンベヤーは、ケースの上半が開放された長さ範囲では、水や沈殿物を移送する能力はあるけれども圧力を発生させることはできないが、スクリュー外周が全周囲われた状態では幾分かの圧力を発生させることができ、スクリューの断面積を漸減させることや、スクリューピッチを漸減させること等で更に加圧力を得ることができることは、スクリュー式ポンプやスクリュー式脱水濃縮機等の技術から容易に理解できるところである。  The screw conveyor for transfer installed almost horizontally at the bottom of the water tank such as a sedimentation water tank is capable of transporting water and sediment within the length range where the upper half of the case is open, but generates pressure. However, some pressure can be generated when the outer periphery of the screw is completely surrounded, and additional pressure can be obtained by gradually reducing the cross-sectional area of the screw or gradually decreasing the screw pitch. What can be done is easily understood from techniques such as a screw-type pump and a screw-type dewatering concentrator.

本発明では、水槽底にほぼ水平に配設したスクリューコンベヤーの上半が開放された範囲で水槽内沈殿物を先端側に移送集積し、スクリュー先端の一定長さ範囲を少ない隙間を設けた加圧ケースで囲い加圧力を得る構成にして、該加圧ケース端にはポンプやスクリューコンベヤー等の加圧、または、掻き揚げ手段を設けない排泥管を上方向に伸延させて連接し、上端を水槽内水位よりも高い位置で水槽外に開放する。
排泥管内水位は無加圧の状態では水槽内水位と同等であり、スクリューコンベヤーの稼動により幾分上昇する。
排泥管内に集積した沈殿物を水槽外に排出するためには、“排泥管水頭×排泥管内液の密度−水槽の水頭×水槽内液の密度+排泥管の流動抵抗”以上の加圧力が必要であるが、液頭差が主体の比較的小さな加圧力で沈殿物の排出を行うことができる。
In the present invention, the sediment in the water tank is transported and accumulated on the tip side within the range where the upper half of the screw conveyor disposed almost horizontally at the bottom of the water tank is opened, and the fixed length range of the screw tip is reduced. The pressure case is configured to obtain a pressurizing pressure, and the end of the pressurization case is connected to the pressurization of a pump, screw conveyor, etc. Is opened outside the water tank at a position higher than the water level in the water tank.
The water level in the drainage pipe is equivalent to the water level in the tank in the non-pressurized state, and rises somewhat due to the operation of the screw conveyor.
In order to discharge the sediment accumulated in the sludge pipe to the outside of the water tank, it must be greater than or equal to “the sludge pipe head × the density of the liquid in the sludge pipe−the water head × the density of the liquid in the tank + the flow resistance of the sludge pipe”. Although a pressing force is required, the sediment can be discharged with a relatively small pressing force mainly composed of a liquid head difference.

スクリューコンベヤーにより移送され、排泥管内に集積される沈殿物汚泥は、スクリューの加圧力と沈殿物汚泥の自重によって圧蜜される。
圧蜜とともに沈殿物汚泥は粘度が上り、スクリューとケース間隙間の漏れ量減少の影響もあって加圧力は更に上昇しやすくなり、排泥管上端より濃縮された沈殿物汚泥が排出される。
The sediment sludge transferred by the screw conveyor and accumulated in the sludge pipe is crushed by the pressure of the screw and the weight of the sediment sludge.
Along with the nectar, the sediment sludge increases in viscosity, and the pressure increases more easily due to the effect of a decrease in leakage between the screw and the case gap, and the concentrated sludge is discharged from the upper end of the exhaust pipe.

更に、水分量の少ない沈殿物汚泥を得るためには、ケース内のスクリュー先端に軸流ポンプの羽根車様の加圧羽根車を装着して、沈殿物の押し込み効果を高める。  Furthermore, in order to obtain a sediment sludge with a small amount of water, a pressure impeller like an impeller of an axial flow pump is attached to the screw tip in the case to enhance the effect of pushing the sediment.

横流れ方式の沈殿分離水槽においても前述と同様に、加圧部を備えたスクリューコンベヤーを分離水槽底に配設すると共に排泥管を連接し、沈殿物貯留部を区画する複数の阻流板下方端にはスクリュー外周に近接させた孔を開窄してスクリューを貫通させ、スクリューの移送方向を分離水槽の被処理水の通水方向と逆行する方向とすることにより、くぐり水に対向する水流を発生させてくぐり水を防止し、装置の分離精度の低下が防止できる。  Also in the cross-flow type sedimentation separation water tank, as described above, a screw conveyor equipped with a pressurizing unit is arranged at the bottom of the separation water tank, and a sludge pipe is connected, and a plurality of flow blocking plates below the sediment storage part. At the end, a hole close to the outer periphery of the screw is opened to allow the screw to pass therethrough, and the flow direction of the screw is opposite to the direction of water flow of the water to be treated in the separation water tank. Can be prevented from passing through water to prevent the separation accuracy of the apparatus from being lowered.

上述したように本発明装置は、加圧部を設けた水平方向の移送用スクリューコンベヤーのみで、垂直方向の揚送用ポンプやスクリューコンベヤー設備を用いる場合よりも濃縮された沈殿物を排除回収することができ、後段の運搬、脱水、乾燥、焼却等に与える省エネルギー効果、経済効果は大きい。
加えて、横流れ方式の沈殿分離装置においては、くぐり水を防止して装置の分離精度を向上できる効果は大きく、水処理分野装置のコンパクト化に大きく貢献できるものである。
As described above, the apparatus of the present invention eliminates and collects concentrated precipitates only by using a horizontal transfer screw conveyor provided with a pressurizing unit, as compared with the case of using a vertical pump and screw conveyor equipment. The energy saving effect and economic effect on transportation, dehydration, drying, incineration, etc. in the latter stage are great.
In addition, in the cross-flow type sedimentation separation apparatus, the effect of preventing the passing water and improving the separation accuracy of the apparatus is great, and can greatly contribute to the downsizing of the apparatus in the water treatment field.

第1実施例装置の重力式沈殿分離水槽の側断面図。The sectional side view of the gravity type precipitation separation water tank of a 1st Example apparatus. 図1のA−A断面図。AA sectional drawing of FIG. (イ)は図1のB−B断面詳細図、(ロ)は図1のA−A断面におけるスクリュー部詳細図。(A) is a BB cross-section detailed drawing of FIG. 1, (B) is a screw part detailed drawing in the AA cross section of FIG. 第2実施例装置の横流れ方式重力沈殿水槽の側断面図。The sectional side view of the transverse flow type gravity precipitation water tank of the 2nd example device. (ハ)は図4のC−C断面図、(ニ)はC−C断面におけるスクリュー部の詳細図。(C) is a cross-sectional view taken along the line CC in FIG. 図4のD−D視図。DD view of FIG. スクリュー先端に加圧羽根車を取付けた実施例の部分詳細断面図。The partial detail sectional view of the Example which attached the pressure impeller to the screw front-end | tip. 図7のE−E断面視詳細図。EE sectional detail drawing of FIG.

以下、本発明の実施形態を図1〜図8に基づいて説明する。  Hereinafter, embodiments of the present invention will be described with reference to FIGS.

本発明の第1実施例装置の重力式沈殿分離水槽である図1〜図3において、分離水槽1の流入樋2から流入した浮遊物を含む被処理水は分離エリアaで沈降分離され、流出樋3に流出する。
沈降する混入浮遊物は沈殿物貯留部bに沈殿し、上半を開放したスクリューコンベヤー11によって反駆動方向に移送され、筒状の加圧ケース5内を通り排泥管6のc部に吐出される。
排泥管6の上部は、上下方向に摺動可能にパッキング10で止水された上部排泥管7を備えて、上端を開放し、排泥管内における沈殿物自重での圧蜜と、水面より上方のd部分での脱水作用で濃縮された沈殿物汚泥が吐出され、シュート8から滑落排出する。
In FIG. 1 to FIG. 3 which are gravity type precipitation separation water tanks of the first embodiment apparatus of the present invention, the water to be treated including suspended matters flowing from the inflow tank 2 of the separation water tank 1 is settled and separated in the separation area a It flows out to 樋 3.
The settled suspended matter settled in the sediment reservoir b, transferred in the counter-drive direction by the screw conveyor 11 with the upper half open, passed through the cylindrical pressure case 5 and discharged to the c portion of the sludge discharge pipe 6. Is done.
The upper part of the mud pipe 6 is provided with an upper mud pipe 7 that is slidable in the up and down direction and stopped by the packing 10, the upper end is opened, and the nectar with the sediment weight in the mud pipe and the water surface The sediment sludge concentrated by the dehydrating action in the upper part d is discharged and slides out from the chute 8.

スクリューコンベヤー11先端部の加圧ケース5内に内包されるスクリュー部分は、必要に応じてスクリューピッチを漸減させることや、スクリュー11と加圧ケース5の断面積を漸減させて加圧力の増加を図ることができる。  The screw part enclosed in the pressure case 5 at the tip of the screw conveyor 11 gradually reduces the screw pitch as necessary, or gradually decreases the cross-sectional area of the screw 11 and the pressure case 5 to increase the pressurizing force. Can be planned.

上部排泥管7の上端開放位置は、沈殿物の性状に合せて、排出が可能な範囲でなるべく高く設定し、排出汚泥水分量の低減を計る。  The upper end open position of the upper sludge pipe 7 is set as high as possible within the range where discharge is possible in accordance with the properties of the sediment, and the amount of discharged sludge moisture is reduced.

第2実施例の横流れ方式の重力沈殿水槽装置を図4〜図6で説明する。
本実施例の場合、排泥管6の上下方向調整は不要なものの例であり、原水投入管17から投入された被処理水は、分離水槽1内に配設した傾斜分離板21を通過する間に沈降分離され、処理水は流出樋3に流出し、分離汚泥は沈殿物貯留部bに沈降する。
沈殿物貯留部b内は被処理水のくぐり水を防止するために、通水方向に直交した複数の阻流板23によって区画し、最下部にはスクリューコンベヤー11の回動に支障のない大きさの孔を開窄し、スクリュー11を貫通させる。
A lateral flow type gravity sedimentation tank apparatus according to the second embodiment will be described with reference to FIGS.
In the case of the present embodiment, the vertical adjustment of the sludge pipe 6 is unnecessary, and the water to be treated introduced from the raw water introduction pipe 17 passes through the inclined separation plate 21 provided in the separation water tank 1. In the meantime, it is settled and separated, the treated water flows out to the outflow basin 3, and the separated sludge settles in the sediment reservoir b.
The sediment reservoir b is partitioned by a plurality of baffle plates 23 orthogonal to the direction of water flow to prevent the treated water from passing through, and the bottom is large enough to prevent the screw conveyor 11 from rotating. The hole is opened and the screw 11 is penetrated.

本実施例装置の阻流板23は、沈殿物貯留部bを完全区画して分離精度を維持したいのであるが、スクリュー11と阻流板23間の隙間、及び、スクリュー11のスクリュー自体の羽根ピッチ間の空隙からのくぐり水が生じるのであるが、スクリューコンベヤーの移送方向を被処理水の通水方向と逆方向とすることで、沈殿物の移送と共に、くぐり水と逆行する水流を発生させることによって、くぐり水を防止して装置の分離精度を維持する。  The baffle plate 23 of the apparatus of this embodiment is intended to completely separate the sediment reservoir b and maintain the separation accuracy. However, the gap between the screw 11 and the baffle plate 23 and the blade of the screw 11 itself. The squeezed water is generated from the gaps between the pitches. By moving the direction of the screw conveyor in the direction opposite to the direction of the water to be treated, the flow of sediment is generated along with the transport of the precipitate. Therefore, it is possible to prevent the passing water and maintain the separation accuracy of the apparatus.

図7及び図8に示す実施例は、スクリュー11先端に3枚の羽根を持つ軸流ポンプの羽根車様の加圧羽根車31を装着し、ナット32で固定したものの実施態様を示す。
加圧羽根車31は、回転数の低い本実施例装置の場合、水力学的ポンプ作用よりも沈殿物汚泥を排泥管6内にヘラで押し込むような働きを期待するものであり、スクリュー11と別体に作ることによって、羽根枚数と羽根角度を自由に選べること、耐摩耗性の良い材質で製作できる利点がある。
The embodiment shown in FIGS. 7 and 8 shows an embodiment in which an impeller-like pressure impeller 31 of an axial flow pump having three blades at the tip of a screw 11 is mounted and fixed with a nut 32.
The pressurizing impeller 31 is expected to act to push the sediment sludge into the sludge pipe 6 with a spatula rather than the hydraulic pump action in the case of the apparatus of this embodiment having a low rotation speed. By making them separately, there are advantages that the number of blades and the blade angle can be freely selected, and that the material can be manufactured with a material having good wear resistance.

また、本発明装置の稼動停止時においては、排泥管6内に排除されない沈殿物汚泥が残る問題が発生するけれども、装置の稼動停止前に、一時的にスクリュー11の回転数を高くすることで、加圧羽根車31の水力学的加圧力を増大させ、軸流ポンプの羽根車が小水量ほど高い(締切り点で250〜300%)加圧力を示す特性もあり、排泥管内の沈殿物汚泥を排除することができる。  Further, when the apparatus of the present invention is stopped, there is a problem that the sediment sludge that is not excluded remains in the sludge pipe 6. However, before the apparatus is stopped, the rotational speed of the screw 11 is temporarily increased. Therefore, the hydraulic pressure of the pressure impeller 31 is increased, and the impeller of the axial flow pump has a characteristic that the pressure increases as the amount of water decreases (250 to 300% at the cutoff point). Waste sludge can be eliminated.

本発明の水槽内沈殿物の排除装置は、自然な沈殿状態よりも濃縮した沈殿物汚泥を水槽外に排出することができ、加えて、従来必要とされていた沈殿物を槽外に排出するためのポンプや、垂直、或いは傾斜スクリューコンベヤーを不要にするものであり、水処理装置の沈殿水槽を始めとし、沈殿物の発生するあらゆる水槽や、河川、湖沼の汚泥の堆積しやすい場所にも利用することができる。  The apparatus for removing sediment in the water tank of the present invention can discharge the sediment sludge that is more concentrated than the natural sediment state to the outside of the water tank, and additionally discharges the sediment that has been conventionally required to the outside of the tank. Pumps and vertical or inclined screw conveyors are not required, including sedimentation tanks for water treatment equipment, any tank where sediment is generated, and places where sludge is likely to accumulate in rivers and lakes. Can be used.

1 分離水槽
2 流入樋
3 流出樋
4 スクリューコンベヤーのケース
5 加圧ケース
6 排泥管
7 上部排泥管
8 排泥用シュート
9 処理水接続口
10 パッキング
11 スクリューコンベヤーのスクリュー
12 軸受ケース
13 ベアリング
14 シール
15 スクリュー駆動用のモーター
16 チェーン
17 原水投入管
21 傾斜分離板
22 分離板押え
23 阻流板
31 加圧羽根車
32 加圧羽根車31の締付ナット
a 分離エリア
b 沈殿物貯留部
c 排泥管始端部
d 排泥管終端部
e 流入エリア
f 流出エリア
DESCRIPTION OF SYMBOLS 1 Separation water tank 2 Inflow tank 3 Outflow tank 4 Screw conveyor case 5 Pressurizing case 6 Drain pipe 7 Upper mud pipe 8 Mud chute 9 Treated water connection port 10 Packing 11 Screw conveyor screw 12 Bearing case 13 Bearing 14 Seal 15 Screw drive motor 16 Chain 17 Raw water input pipe 21 Inclined separation plate 22 Separation plate retainer 23 Block plate 31 Pressure impeller 32 Clamping nut a of pressure impeller 31 Separation area b Precipitate storage part c Drainage Mud pipe start end d Waste mud pipe end e Inflow area f Outflow area

Claims (3)

横流れ方式の沈殿分離水槽において、傾斜分離板下方の沈殿物貯留部内を、通水方向に直交して区画する複数の阻流板の最深部に、該阻流板を貫通する形で、上半を開放したケースとスクリューで構成するスクリューコンベヤーを、被処理水の通水方向に逆行する方向に沈殿物を移送するように配設し、スクリュー送出側端部の一定長さを筒状の加圧ケース内に挿入して加圧部を構成すると共に、該加圧ケース端には上方向に伸延する排泥管を連接し、上端を分離水槽水位より高い位置で開放するようにした、沈殿物の排除装置。 In the horizontal flow type sedimentation separation tank, the upper half of the sediment storage part below the inclined separation plate penetrates the baffle plates to the deepest part of a plurality of baffle plates that are divided perpendicular to the water flow direction. A screw conveyor consisting of a case and a screw with an open end is arranged so as to transfer sediment in a direction reverse to the direction of water flow of the water to be treated , and a fixed length at the end of the screw delivery side is added to the cylinder. The pressure part is inserted into the pressure case to constitute a pressurizing part, and a sludge pipe extending upward is connected to the end of the pressure case, and the upper end is opened at a position higher than the separation water tank water level. Exclusion device. スクリューコンベヤーのスクリュー先端に、軸流ポンプの羽根車様の加圧羽根車を装着した請求項1に記載する沈殿物の排除装置。 2. The precipitate eliminating device according to claim 1, wherein an impeller-like pressure impeller of an axial flow pump is attached to a screw tip of a screw conveyor. 装置の停止前、或いは、排泥管詰りを防止するために、一時的にスクリュー回転数を増大させるようにした請求項1及び請求項2のいずれか1項に記載する沈殿物の排除装置。

The apparatus for removing precipitates according to any one of claims 1 and 2, wherein the rotational speed of the screw is temporarily increased before the apparatus is stopped or in order to prevent clogging of the drainage pipe.

JP2010229054A 2010-09-21 2010-09-21 Precipitation device for sediment in water tank Active JP5812237B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2010229054A JP5812237B2 (en) 2010-09-21 2010-09-21 Precipitation device for sediment in water tank

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2010229054A JP5812237B2 (en) 2010-09-21 2010-09-21 Precipitation device for sediment in water tank

Publications (2)

Publication Number Publication Date
JP2012066233A JP2012066233A (en) 2012-04-05
JP5812237B2 true JP5812237B2 (en) 2015-11-11

Family

ID=46164132

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2010229054A Active JP5812237B2 (en) 2010-09-21 2010-09-21 Precipitation device for sediment in water tank

Country Status (1)

Country Link
JP (1) JP5812237B2 (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104225977A (en) * 2013-06-15 2014-12-24 颜可仁 Automatic sediment cleaning device for slurry basin
KR101384854B1 (en) * 2013-12-31 2014-04-29 허종형 Sludge excharging device for settling pond
CN105854357B (en) * 2016-05-04 2018-03-06 上海大学 Skeleton symbol double buffering baffling sedimentation basin
CN108970184B (en) * 2018-09-21 2020-11-24 江苏广域化学有限公司 Gravity settling separation equipment for chemical mixed liquid

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5331371U (en) * 1976-08-25 1978-03-17
JPS53105059A (en) * 1977-02-23 1978-09-12 Sadao Shimazaki Device for automatically discharging sludge in purifying tank
JPS6150610A (en) * 1984-08-16 1986-03-12 Toru Matsuoka Apparatus for treating waste water

Also Published As

Publication number Publication date
JP2012066233A (en) 2012-04-05

Similar Documents

Publication Publication Date Title
JP5812237B2 (en) Precipitation device for sediment in water tank
CN201305491Y (en) Water purifier
JP2008136934A (en) Grit separation
JP5944721B2 (en) Sand settling equipment
CN104806183B (en) Oil field flushing returns discharge opeing blood pressure lowering except device for silt
CN205461179U (en) Sedimentation basin
CN208832087U (en) A kind of device of energy-saving online removal working solution sediment
KR100922231B1 (en) Oil separator for waste water treatment handling equipment
FR2820734A1 (en) WATER TREATMENT FACILITY BY FLOCKS LASTED BY A GRANULAR MATERIAL, COMPRISING INTEGRATED MEANS FOR DEGREASING
CN105431384B (en) Sewage disposal device
KR100533523B1 (en) Settling tank having buffers for removing scum
KR20050009976A (en) Method and device for flocculating setting
JP4247840B2 (en) Sludge dewatering unit and sludge suction and dewatering device using the same
KR100824707B1 (en) Waste-water Sedimentation Processing Apparatus Having Vertical-feeding Decanter
CN204034338U (en) Multi-functional sedimentation basin
CN202107583U (en) Downhole treatment device for sewage of mine
CN210974372U (en) Industrial wastewater sludge treatment device
KR100986634B1 (en) Pretreatment equipment of sludge or sewage
RU2465944C2 (en) Device to separate phases in water-oil mix and inclined settler
CN203403506U (en) Tail end rainwater purification well of flow splitting rainwater discharge system
CN106669273A (en) Self-decompression belt type oil-water separation device
CN106669266A (en) Rapid belt type oil-water separation apparatus
CN204162537U (en) For the heavy water treating equipment of dense medium speed of underground coal mine
CN104841157B (en) Countercurrent extraction pumping equipment
CN217246995U (en) Desander with filtering performance

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20130909

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20140827

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20140916

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20141030

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20150414

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20150529

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20150901

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20150908

R150 Certificate of patent or registration of utility model

Ref document number: 5812237

Country of ref document: JP

Free format text: JAPANESE INTERMEDIATE CODE: R150

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250