JP2015077587A - Pressure floatation type scrum separation apparatus - Google Patents

Pressure floatation type scrum separation apparatus Download PDF

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JP2015077587A
JP2015077587A JP2013228727A JP2013228727A JP2015077587A JP 2015077587 A JP2015077587 A JP 2015077587A JP 2013228727 A JP2013228727 A JP 2013228727A JP 2013228727 A JP2013228727 A JP 2013228727A JP 2015077587 A JP2015077587 A JP 2015077587A
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scum
levitation
screw
tank
separation tank
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JP5605490B1 (en
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東 利保
Toshiyasu Azuma
利保 東
利光 東
Toshimitsu Azuma
利光 東
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Suna Co Ltd
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Suna Co Ltd
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  • Treatment Of Sludge (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a pressure floatation type scum separation apparatus which makes efficient scraping and dehydration of floating scum within a screw conveyor.SOLUTION: A floating separation tank 1 carrying out floating separation of sewage has a communication cylinder e for collecting scum guided by an oblique scum guide. On the upper side of the floating separation tank, a screw conveyor type scum discharge device 17 is fixed obliquely, and the scrum discharge apparatus has a casing in which a rectangular scum intake port 20 opened on the lower side of the inclination is communicated with the communication cylinder and fixed and which can discharges scum through a discharge port 35 opened on the upper side of the inclination, a scraping screw and dehydration means which is provided in the upper part of the casing and compresses scrum to remove moisture. The water level of sewage in the floating separation tank is set to be 1/2 of the diameter of the scraping screw high relative to the lower end part of the lower periphery on the upper side of the inclination of the scum intake port.

Description

本発明は、加圧浮上式スカム分離処理装置に関する。  The present invention relates to a pressurized floating scum separation processing apparatus.

収集したスカム含有汚水を浮上分離槽に導入するに当って加圧によりエアーを溶解させた水を伴って減圧下で分離槽内に噴出させスカムの浮上を促進させることにより浮上したスカムを上部より排出するようにした加圧浮上方式は既に知られている技術である。そうした技術に関連するものとして、特許文献1に開示された技術がある。  When the collected scum-containing sewage is introduced into the levitation separation tank, the scum that has been levitated from the upper part by spouting the scum by urging the scum into the separation tank under reduced pressure with water in which air is dissolved by pressurization is introduced. The pressure levitation method for discharging is a known technique. As a technique related to such a technique, there is a technique disclosed in Patent Document 1.

特許第4238297号Japanese Patent No. 4238297

上記特許文献1による技術は、浮上したスカムを加圧浮上濃縮槽(浮上分離槽)に設けられたスカム排出トラフに向けて掻寄せるスクレーパと、前記加圧浮上濃縮槽の槽壁上部で、かつ、湾曲中心位置がその加圧浮上濃縮槽側に位置するように形成された湾曲面と、回転軸を有するとともに、その回転軸に羽根を有する、前記スクレーパで掻寄せられたスカムを前記スカム排出トラフに排出する前記湾曲面近くに設けられた排出機と、前記排出機の回転軸を回転駆動するとともに、その回転数を調整する機能を有する駆動源と、を有することを特徴とする。
このスカム加圧浮上濃縮装置は、浮上したスカムを加圧浮上濃縮槽から排出するとともにこれらのスカムを遠く離れたスカム処理施設へ円滑に搬送できるようにしたものであるが、ここで浮上させたスカムを排出する手段は、掻寄板を外周に突設したチェーンであるスクレーパと、湾曲面に添って運動する掻上羽根付きで回転軸回りを回転する排出機とでなり、排出機からのスカムをスカム排出トラフへ排出するようにしたものであり、従って、浮上したスカムは水分を充分に含んでいて重くなっておりそれをそのまま排出するため、スカム処理施設への搬送に無駄な電力が消費されることになり、しかも搬送先でスカムから水分を分離除去して所定の目的に供し得るようにする必要が出てくる。
The technique according to Patent Document 1 includes a scraper that scrapes the floated scum toward a scum discharge trough provided in a pressurized flotation concentration tank (flotation separation tank), an upper tank wall of the pressurized flotation concentration tank, and The scum discharged by the scraper having a curved surface formed so that the center position of the curve is located on the pressurized flotation concentration tank side and a rotating shaft and blades on the rotating shaft is discharged from the scum. A discharger provided near the curved surface for discharging to the trough, and a drive source having a function of rotating the rotation shaft of the discharger and adjusting the number of rotations thereof.
This scum pressurized levitation concentrator discharges the scum that has floated from the pressurized levitation concentration tank and allows the scum to be smoothly transported to a scum treatment facility far away. The means for discharging the scum consists of a scraper that is a chain with a scraping plate protruding from the outer periphery, and a discharger that rotates around the rotation axis with a scraping blade that moves along the curved surface. The scum is discharged to the scum discharge trough. Therefore, the floating scum contains sufficient moisture and is heavy and is discharged as it is. In addition, it is necessary to separate and remove moisture from the scum at the transport destination so that it can be used for a predetermined purpose.

そうした問題、即ち、浮上分離槽で浮上するスカムを圧縮作用で水切りしながら掻揚排出することにより排出後の搬送を省エネのもとに可能とししかも搬送先でのスカムと水分との分離行程を極力簡略化することができるようにした加圧浮上式スカム分離処理装置を本出願人は先に提案した(特願2012−185838)。
その提案内容の一つは、図1ないし図3に示されている。
この加圧浮上式スカム分離処理装置において、1は浮上分離装置で、上方を開放状とし上からみて矩形槽とした浮上分離槽2を備えている。浮上分離槽2は、槽本体3と分離水槽5とを仕切り壁4を介して有し、これら槽本体3と分離水槽5内には、汚水6および分離水7が同じレベルHとなるように溜められるようになっている。
8は連通管で、槽本体3と分離水槽5とをつなぐパイプで、前後端にフィルター9を備えて浄化された水が分離水7として分離水槽5内に導入されるようになっている。10はオーバーフロー口で、前記水位Hを決めるものである。
分離水槽5内の分離水7は、このオーバーフロー口10を通じて外部に排出される一方、分離水槽5の底部からは、給水ポンプ12の作動により給水管11を通じて分離水7が引き抜かれ後述する加圧式空気溶解装置45に導入されるようになっている。
Such a problem, that is, the scum that floats in the levitation separation tank is evacuated and discharged while being drained by the compression action, so that the post-discharge transportation can be performed with energy savings, and the separation process of scum and moisture at the transport destination can be reduced. The present applicant has previously proposed a pressure levitation type scum separation processing apparatus that can be simplified as much as possible (Japanese Patent Application No. 2012-185838).
One of the proposals is shown in FIGS.
In this pressurized levitation scum separation processing apparatus, reference numeral 1 denotes a levitation separation apparatus, which is provided with a levitation separation tank 2 which is open from the top and is a rectangular tank as viewed from above. The floating separation tank 2 has a tank body 3 and a separation water tank 5 via a partition wall 4, and the sewage 6 and the separation water 7 are at the same level H in the tank body 3 and the separation water tank 5. It can be stored.
8 is a communication pipe that connects the tank body 3 and the separation water tank 5, and the purified water having the filter 9 at the front and rear ends is introduced into the separation water tank 5 as the separation water 7. Reference numeral 10 denotes an overflow port for determining the water level H.
The separated water 7 in the separated water tank 5 is discharged to the outside through the overflow port 10, while the separated water 7 is pulled out from the bottom of the separated water tank 5 through the water supply pipe 11 by the operation of the water supply pump 12, which will be described later. It is introduced into the air dissolving device 45.

槽本体3内の下部には、減圧弁を兼ねた複数のノズル13を備える供給管14が槽本体3の前後方向に軸心を向けるようにして単一本あるいは複数本配備されている。槽本体3と分離水槽5とでなる浮上分離槽2の上部には、スカム排出装置であるスクリュウコンベア17が約15度傾斜した状態で固定設置されている。
スクリュウコンベア17は、内径約300mmの円筒状をなすケーシング18を備えるとともに、このケーシング18の傾斜方向下部一端(テール側)は、閉止したものとされて槽本体3の前側(図1の左側)に固定支持される一方、傾斜方向上部一端(ヘッド側)は、同じく閉止したものとされて浮上分離槽2の後側(図1の右側)に張り出した状態で固定されている。
In the lower part of the tank body 3, a single supply pipe 14 or a plurality of supply pipes 14 provided with a plurality of nozzles 13 that also serve as pressure reducing valves are arranged so that the axial center is directed in the front-rear direction of the tank body 3. A screw conveyor 17 that is a scum discharge device is fixedly installed at an upper portion of the floating separation tank 2 including the tank body 3 and the separated water tank 5 in an inclined state of about 15 degrees.
The screw conveyor 17 includes a cylindrical casing 18 having an inner diameter of about 300 mm, and a lower end (tail side) in the inclination direction of the casing 18 is closed and the front side of the tank body 3 (left side in FIG. 1). On the other hand, one upper end (head side) in the inclined direction is also closed and fixed in a state of protruding to the rear side (right side in FIG. 1) of the floating separation tank 2.

20はスカム取込口で、ケーシング18の傾斜方向下部一端から傾斜方向上方へ離れた下周り位置に下からみると矩形の開口として形成されたもので、汚水6上に浮上してくるスカムSを取り込むのに適応した位置に設けられている。
22はスクリュウ軸(あるいはパイプ)で、ケーシング18の中心を通りその両端は軸受で回転自在に支持されるとともに、同スクリュウ軸22の外周には掻揚スクリュウ23が設けられている。掻揚スクリュウ23は、板をラセン状にしたスクリュウ本体23aを備え、この本体23aは、上端がケーシング18の上部端から70cm程度手前に端部があるように形成されている。
Reference numeral 20 denotes a scum intake port, which is formed as a rectangular opening when viewed from below at a lower peripheral position away from the lower end of the casing 18 in the inclination direction, and the scum S that floats on the sewage 6. It is provided at a position suitable for taking in.
A screw shaft (or pipe) 22 passes through the center of the casing 18 and both ends thereof are rotatably supported by bearings, and a screw screw 23 is provided on the outer periphery of the screw shaft 22. The lifting screw 23 includes a screw main body 23a having a spiral plate, and the main body 23a is formed so that the upper end is about 70 cm away from the upper end of the casing 18.

スクリュウ本体23aのスカム取込口20に対応する長さ以上の長さLに亘る周縁部には、前記傾斜方向上方へ向けて突出する掬い揚げ突条23bがラセン帯板として一体に設けられている。ここで、図1〜図3の19はスカムガイドを示す。浮上分離槽2の槽本体3は、その上方を開放したままにしてその槽内全面が水面となるようにして汚水6を溜めておきそこにスカムSを浮上させる方式にしておくと、スカム取込口20へのスカムSの取り込みは消極的なものになる。
そこで、汚水6から微細気泡とともに浮上してくるスカムSをスカム取込口20に確実かつ積極的に取り込めるようにスカムガイド19を設けたものである。
A scooping ridge 23b that protrudes upward in the inclined direction is integrally provided as a spiral strip at the peripheral edge of the screw main body 23a that extends over a length L that is equal to or longer than the scum inlet 20 of the screw body 23a. Yes. Here, reference numeral 19 in FIGS. 1 to 3 denotes a scum guide. If the tank body 3 of the levitation separation tank 2 is left open so that the entire surface of the tank becomes a water surface and the sewage S is floated on the scum S, Incorporation of the scum S into the inlet 20 becomes passive.
Therefore, the scum guide 19 is provided so that the scum S floating along with the fine bubbles from the sewage 6 can be reliably and positively taken into the scum inlet 20.

スカムガイド19は、図3にその詳細を示すように、前・後の斜面ガイドa、bおよび左・右の斜面ガイドcによる逆四角錐状のものとされて槽本体3内に周縁を隙間なく接することで固定されている。これら4面の斜面ガイドa〜cの上部中央には、四角な連通筒eが一体に設けられている。  As shown in detail in FIG. 3, the scum guide 19 is formed in an inverted quadrangular pyramid shape by front and rear slope guides a and b and left and right slope guides c. It is fixed by touching. A square communication tube e is integrally provided at the center of the upper part of these four inclined guides a to c.

この連通筒eは、左右の傾斜板状の対向壁fと前後の壁g、hとを有する上下貫通状の筒部となっており、対向壁fは、図3のケーシング18のスカム取込口20の外縁に添って溶接されるように構成される一方、前後のうち前側の壁gは低く後側hを高くしてその上側に半円より短い円弧形の嵌合受溝i、jを形成することで、これら嵌合受溝i、jにスカム取込口20の前後の外縁部が嵌まり込んで溶接されるようになっている。
このように連通筒eがスカム取込口20の外縁に適合することで、浮上してきたスカムSが途中で詰まったりすることなく取り込まれることになる。図1、図2におけるHは、汚水6の水面を示し、この水面Hは、連通筒eの嵌合受溝jの溝底高さ程度とされている。
This communicating cylinder e is a vertically penetrating cylindrical part having left and right inclined plate-like opposing walls f and front and rear walls g, h. The opposing wall f is taken in the scum of the casing 18 of FIG. While being configured to be welded along the outer edge of the port 20, the front wall g of the front and rear is low, the rear h is high, and an arcuate fitting receiving groove i shorter than a semicircle on the upper side, By forming j, the outer edge portions of the front and rear of the scum inlet 20 are fitted into these fitting receiving grooves i and j and are welded.
In this way, the communication tube e is fitted to the outer edge of the scum inlet 20, so that the scum S that has risen is taken in without being clogged in the middle. 1 and 2 indicates the water surface of the sewage 6, and the water surface H is about the height of the groove bottom of the fitting receiving groove j of the communication tube e.

スクリュウ軸22の傾斜方向上部周りには、脱水手段の受板を構成する圧縮受盤26が装備されている。圧縮受盤26は、掻揚スクリュウ23によって掻き揚げられてくるスカムSを圧縮したのち排出口35から排出するように反発バネ33を備えて進退自在なものとされている。排出口35には、搬送コンベア36上のコンテナ37内に圧縮済みのスカムを落とし込むためのシュート38が設けられている。図1の40は減速モーターである駆動源(駆動手段)で、伝導手段41を介してスクリュウ軸22を図2の矢印R方向に回転駆動させるようになっている。  Around the upper portion of the screw shaft 22 in the inclination direction, a compression receiving plate 26 constituting a receiving plate of the dehydrating means is provided. The compression receiving plate 26 is provided with a repulsion spring 33 so as to be freely advanced and retracted so that the scum S lifted up by the lifting screw 23 is compressed and then discharged from the discharge port 35. The discharge port 35 is provided with a chute 38 for dropping compressed scum into a container 37 on the transport conveyor 36. Reference numeral 40 in FIG. 1 denotes a driving source (driving means) which is a reduction motor, which rotates the screw shaft 22 in the direction of arrow R in FIG.

図1における45は加圧式空気溶解装置で、複数の空気溶解槽46…を備える。各空気溶解槽46には、並列式の入側配管47を通じて前記給水管11が連通されるとともに、出側配管48とそれをまとめた合流管49を通じて前記供給管14に連通式に接続がなされている。各空気溶解槽46の入側と出側には自動弁50,51が設けられている。
空気溶解槽46内には、その下部一側寄りに空気ノズル53が設けられ、循環仕切板54の周りを空気が循環運動しながら内水に空気が溶解するようになっている。空気ノズル53は、各空気パイプ55を通じてブロア56またはコンプレッサーなどの給気手段に接続されている。また、空気パイプ55のそれぞれには空気自動弁57が制御自在に設けられている。
60は汚水受槽で、沈澱池や濃縮槽などからの収集されたスカム含有汚水61が導入されてくる。同受槽60と前記合流管49との間は汚水供給管62で接続され、その管上には汚水ポンプ63が設けられている。
In FIG. 1, reference numeral 45 denotes a pressurized air dissolving apparatus including a plurality of air dissolving tanks 46. The water supply pipe 11 communicates with each air dissolution tank 46 through a parallel inlet pipe 47 and is connected to the supply pipe 14 through an outlet pipe 48 and a junction pipe 49 that integrates the outlet pipe 48. ing. Automatic valves 50 and 51 are provided on the entry side and the exit side of each air dissolution tank 46.
In the air dissolution tank 46, an air nozzle 53 is provided on the lower side of the air dissolution tank 46 so that the air dissolves in the internal water while the air circulates around the circulation partition plate 54. The air nozzle 53 is connected to air supply means such as a blower 56 or a compressor through each air pipe 55. Each of the air pipes 55 is provided with an air automatic valve 57 in a controllable manner.
Reference numeral 60 denotes a sewage receiving tank into which scum-containing sewage 61 collected from a sedimentation basin or a concentration tank is introduced. The receiving tank 60 and the junction pipe 49 are connected by a sewage supply pipe 62, and a sewage pump 63 is provided on the pipe.

この加圧浮上式スカム分離処理装置の作用を説明する。入側自動弁50(空気あるいは電動作動式)を開放したもとで、給水ポンプ12を運転して分離水槽5内の分離水7を一方の空気溶解槽(加圧水タンク)46へ供給する。次に、一方の空気溶解槽46に対応する自動弁57を開くとともにブロア56あるいはコンプレッサを運転して空気ノズル53によって微細化空気を空気溶解槽46内に噴入することにより一方の空気溶解槽46内の圧力を高めかつ内水を循環流とすることにより微細空気を内水に溶解させる。
その後、汚水ポンプ63を運転してスカム含有汚水61を汚水供給管62まで送ると、それと同時に一方の空気溶解槽46に対応する出側自動弁51を開き、それによりスカム含有汚水と空気の溶解した加圧水とを混合させ、その混合したものが、合流管49および供給管14からノズル13…を通じて浮上分離槽2の槽本体3内に減圧された形で送り込まれる。
The operation of this pressurized floating scum separation processing device will be described. With the inlet side automatic valve 50 (air or electrically operated) opened, the water supply pump 12 is operated to supply the separated water 7 in the separated water tank 5 to one air dissolving tank (pressurized water tank) 46. Next, the automatic valve 57 corresponding to one of the air dissolution tanks 46 is opened, and the blower 56 or the compressor is operated so that fine air is injected into the air dissolution tank 46 by the air nozzle 53. The fine air is dissolved in the internal water by increasing the pressure in 46 and using the internal water as a circulating flow.
Thereafter, when the sewage pump 63 is operated to send the scum-containing sewage 61 to the sewage supply pipe 62, the outlet automatic valve 51 corresponding to one of the air dissolution tanks 46 is opened at the same time, thereby dissolving the scum-containing sewage and air. The mixed pressurized water is mixed, and the mixture is fed into the tank body 3 of the floating separation tank 2 from the junction pipe 49 and the supply pipe 14 through the nozzles 13.

送り込まれた混合水からの微細気泡はスカムを付着して浮上してゆく。浮上したスカムSは、スカムガイド19による斜面ガイドにより円滑に案内されながらスカム取込口20に取り込まれ、掻揚スクリュウ23に付した掬い揚げ突条23bによる掬い揚げ機能により確実に掬い揚げられることになる。掬い揚げられて軸方向に送られてゆくスカムSは、背部から反発バネ33による反発を受けながら後退してゆく圧縮受盤26により脱水作用を受けたのち排出口35よりシュート38を経てコンテナ37へと排出されるようになっている。  The fine bubbles from the mixed water that has been sent in will float with scum. The floated scum S is taken into the scum inlet 20 while being smoothly guided by the slope guide by the scum guide 19, and is reliably lifted by the scooping function by the scooping ridge 23b attached to the lifting screw 23. become. The scum S which is scooped up and sent in the axial direction is dehydrated by the compression receiving plate 26 which is retracted while being repelled by the repulsion spring 33 from the back, and then passes through the chute 38 from the discharge port 35 to the container 37. To be discharged.

ところで、図1ないし図3に示す加圧浮上式スカム分離処理装置においては、浮上分離槽2内の水位Hが分離水槽5の水位に応じて一定に規定され、その水位Hが、連通筒eの後側の嵌合受溝jの溝底高さに略対応するレベルに規定され、そのレベルHは、掻揚スクリュウ23に対しては低いレベルとされ、図示のように、掻揚スクリュウ23の下回りにくる一部のみがスカム上層域に没する程度のごく浅目に設定されていた。
スカムSはスカム取込口20の傾斜方向上方開口縁であるn点を越えたところまで掻き込みされればあとはケーシング18の全周を備えた部分に差し掛かることになることから順当に掻き揚げられるようになるが、前記のように掻揚スクリュウ23の下周りのごく一部しか没していない浅い水位Hであれば、掻揚スクリュウ23の面はその下周りにおいてのみスカムSを掻く程度になって実際にはスカムSは図2の矢印Xのように連通筒e内において掻き送られる運動を繰り返すのみとなり、その結果、スカムSは掻きこぼし現象を発生してスカム取込口20を越えて本来目的とするケーシング18内へと掻き揚げられにくく、従って、確実かつ効率的に掻き揚げができず、その後の圧搾脱水作用の向上も図りにくくなるという問題が発生することとなっていた。
By the way, in the pressurized flotation type scum separation processing apparatus shown in FIG. 1 to FIG. 3, the water level H in the flotation separation tank 2 is defined to be constant according to the water level of the separation water tank 5, and the water level H is The level H is set to a level substantially corresponding to the height of the groove bottom of the rear fitting receiving groove j, and the level H is set to a low level with respect to the lifting screw 23, and as shown in the drawing, the lifting screw 23 It was set so shallow that only a part of the lower part of the scum sunk in the upper scum area.
Since the scum S is scraped up to a point beyond the point n that is the upper opening edge in the inclination direction of the scum intake port 20, the scum S is scraped in a proper manner since the scum S reaches the portion having the entire circumference of the casing 18. If it is a shallow water level H in which only a small portion around the bottom of the lifting screw 23 is submerged as described above, the surface of the lifting screw 23 scratches the scum S only around the bottom. Actually, the scum S only repeats the motion of being scraped in the communication tube e as indicated by the arrow X in FIG. 2, and as a result, the scum S generates a scraping phenomenon and the scum inlet 20 Therefore, there is a problem that it is difficult to rake up into the originally intended casing 18 and therefore cannot be raked up reliably and efficiently, and it is difficult to improve the subsequent pressing and dehydrating action. It has been a thing.

本発明は、上記問題を解決しようとするものであり、浮上スカムのスクリュウコンベア内で掻き揚げが十分確実かつ効率的に行われ脱水作用も効率化されるようにした加圧浮上式スカム分離処理装置を提供することを目的とする。  The present invention is intended to solve the above-mentioned problem, and is a pressure floating type scum separation process in which the lifting is performed sufficiently reliably and efficiently in the screw conveyor of the floating scum and the dewatering action is also made efficient. An object is to provide an apparatus.

上記目的達成のため、請求項1に記載の発明は、収集したスカム含有汚水を加圧空気を伴って供給する浮上誘導装置を備えた浮上分離槽と、この浮上分離槽に連通して清澄水を分離水として貯留するとともにその貯留水が浮上分離槽内の水位と同じレベルの水位とされてその排水も可能とされた分離水槽とを有し、浮上分離槽は、前記浮上誘導装置から浮上しつつ傾斜状のスカムガイドに案内されてきたスカムを集める連通筒をその槽上部に備えるとともに、前記浮上分離槽の上側には、スクリュウコンベア式スカム排出装置がその一端を低く他端を高くして傾斜状をなして固定され、前記スカム排出装置は、円筒状でその傾斜方向下側の下周りに開設した矩形状のスカム取込口を前記連通筒に連通状をなすように連結固定されるとともに傾斜方向上側の下周りに開設した排出口を通じてスカムを排出可能とされたケーシングと、このケーシングに内装されてスカムを傾斜上方へ掻き揚げるように設けられた掻揚スクリュウと、前記ケーシングの上部内に設けられていて掻き揚げられてくるスカムを圧縮して水分を除去するための脱水手段とを有する加圧浮上式スカム分離処理装置において、前記浮上分離槽内の汚水は、スカム取込口の傾斜方向上方の下周り下端部を基準として掻揚スクリュウのスクリュウ径Dの1/2よりも高いレベルを水面として設定されていることを特徴とする。
請求項2に記載の発明は、請求項1に記載のものにおいて、スクリュウコンベアの掻揚スクリュウは、スカム取込口に対応する長さ部分に設けられたスクリュウ部分が他のスクリュウ部分よりも長いピッチとして形成されている。
請求項3に記載の発明は、請求項1または2に記載のものにおいて、浮上誘導装置は、上端開口がスカム取込口に向くようにして浮上分離槽の槽底部から垂直に立てられた浮上誘導パイプと、外部からの汚水を浮上誘導パイプ内に導入する配管と、空気供給源からの空気を浮上誘導パイプ内に供給する散気装置とを備え、この散気装置は、供給管とその先端の散気装置本体とを備えるとともにこれら供給管と散気装置本体とは1つのユニットとして浮上分離槽と浮上誘導パイプとをつなぐ脱着ガイドパイプを通じて脱着可能とされている。
In order to achieve the above object, the invention described in claim 1 is a flotation separation tank provided with a flotation induction device for supplying collected scum-containing sewage with pressurized air, and clarified water communicating with the flotation separation tank. Is stored as separated water, and the stored water is at the same level as the water level in the levitation separation tank, and the effluent separation tank is levitated from the levitation induction device. In addition, a communicating cylinder for collecting the scum guided by the inclined scum guide is provided at the upper part of the tank, and a screw conveyor type scum discharging device has a lower end and a higher end at the upper side of the floating separation tank. The scum discharge device is connected and fixed so that the rectangular scum intake opening formed in the lower part of the lower side in the inclination direction is connected to the communication cylinder so as to communicate with the communication cylinder. And lean A casing capable of discharging the scum through a discharge opening opened around the lower side in the direction, a lifting screw provided in the casing so as to lift the scum upward and inclined, and an upper part of the casing. In the pressurized flotation type scum separation processing apparatus having a dewatering means for removing moisture by compressing the scum that is provided and scraped, the sewage in the flotation separation tank is inclined at the scum intake port. The water surface is set to a level higher than ½ of the screw diameter D of the lifting screw with reference to the lower lower end portion in the upper direction.
The invention according to claim 2 is the one according to claim 1, wherein the screw conveyor of the screw conveyor has a longer screw portion provided in a length portion corresponding to the scum intake port than the other screw portions. It is formed as a pitch.
According to a third aspect of the present invention, in the first or second aspect of the present invention, the levitation guidance device is a levitation that stands vertically from the bottom of the levitation separation tank so that the upper end opening faces the scum intake port. An induction pipe, a pipe for introducing sewage from the outside into the levitation induction pipe, and an air diffuser for supplying air from an air supply source into the levitation induction pipe. The air diffuser main body at the tip is provided, and the supply pipe and the air diffuser main body can be detached as a unit through a desorption guide pipe that connects the floating separation tank and the floating guide pipe.

上述したように請求項1に記載の発明は、収集したスカム含有汚水を加圧空気を伴って供給する浮上誘導装置を備えた浮上分離槽と、この浮上分離槽に連通して清澄水を分離水として貯留するとともにその貯留水が浮上分離槽内の水位と同じレベルの水位とされてその排水も可能とされた分離水槽とを有し、浮上分離槽は、前記浮上誘導装置から浮上しつつ傾斜状のスカムガイドに案内されてきたスカムを集める連通筒をその槽上部に備えるとともに、前記浮上分離槽の上側には、スクリュウコンベア式スカム排出装置がその一端を低く他端を高くして傾斜状をなして固定され、前記スカム排出装置は、円筒状でその傾斜方向下側の下周りに開設した矩形状のスカム取込口を前記連通筒に連通状をなすように連結固定されるとともに傾斜方向上側の下周りに開設した排出口を通じてスカムを排出可能とされたケーシングと、このケーシングに内装されてスカムを傾斜上方へ掻き揚げるように設けられた掻揚スクリュウと、前記ケーシングの上部内に設けられていて掻き揚げられてくるスカムを圧縮して水分を除去するための脱水手段とを有する加圧浮上式スカム分離処理装置において、前記浮上分離槽内の汚水は、スカム取込口の傾斜方向上方の下周り下端部を基準として掻揚スクリュウのスクリュウ径Dの1/2よりも高いレベルを水面として設定されていることを特徴とするので、浮上スカムのスクリュウコンベア内で掻き揚げが十分確実かつ効率的に行われ脱水作用も効率化されるようにした加圧浮上式スカム分離処理装置を提供することができる。
請求項2に記載の発明は、請求項1に記載のものにおいて、スクリュウコンベアの掻揚スクリュウは、スカム取込口に対応する長さ部分に設けられたスクリュウ部分が他のスクリュウ部分よりも長いピッチとして形成されているので、浮上スカムのスクリュウコンベア内で掻き揚げが十分確実かつ効率的に行われ脱水作用も効率化されるようにした加圧浮上式スカム分離処理装置を提供することができる。
請求項3に記載の発明は、請求項1または2に記載のものにおいて、浮上誘導装置は、上端開口がスカム取込口に向くようにして浮上分離槽の槽底部から垂直に立てられた浮上誘導パイプと、外部からの汚水を浮上誘導パイプ内に導入する配管と、空気供給源からの空気を浮上誘導パイプ内に供給する散気装置とを備え、この散気装置は、供給管とその先端の散気装置本体とを備えるとともにこれら供給管と散気装置本体とは1つのユニットとして浮上分離槽と浮上誘導パイプとをつなぐ脱着ガイドパイプを通じて脱着可能とされているので、散気装置本体を定期的な保守点検により常に正常な散気機能を発揮できる状態に保つことができ、その結果、スカムの浮上を常に効果的なものとしスカム掻揚が十分確実かつ効率的に行われるようにした加圧浮上式スカム分離処理装置を提供することができる。
As described above, the invention described in claim 1 is a flotation separation tank provided with a flotation induction device that supplies collected scum-containing sewage with pressurized air, and separates the clarified water in communication with the flotation separation tank. A separation water tank that stores water as a water level that is the same level as the water level in the floating separation tank and that allows the drainage of the water, and the floating separation tank floats from the floating guide device. A communicating cylinder for collecting the scum guided by the inclined scum guide is provided at the upper part of the tank, and a screw conveyor type scum discharge device is inclined above the floating separation tank with one end lowered and the other raised. The scum discharge device is cylindrically connected and fixed so that a rectangular scum intake opening formed in a lower part around the lower side in the inclination direction is connected to the communication cylinder so as to communicate with the communication cylinder. Inclination direction A casing capable of discharging the scum through a discharge opening opened around the lower side of the side, a scraping screw installed in the casing so as to lift the scum upward and inclined, and provided in the upper part of the casing In the pressurized flotation type scum separation processing apparatus having a dewatering means for removing the moisture by compressing the scum that has been swept up, the sewage in the flotation separation tank is in the direction of inclination of the scum inlet Since the water surface is set to a level that is higher than 1/2 of the screw diameter D of the lifting screw with the lower lower end of the upper part as a reference, it is possible to sufficiently lift up the screw in the screw conveyor of the floating scum. In addition, it is possible to provide a pressurized flotation type scum separation processing apparatus that is efficiently performed and the dehydrating action is also improved.
The invention according to claim 2 is the one according to claim 1, wherein the screw conveyor of the screw conveyor has a longer screw portion provided in a length portion corresponding to the scum intake port than the other screw portions. Since it is formed as a pitch, it is possible to provide a pressure levitation scum separation processing device that is sufficiently reliably and efficiently scraped in the screw conveyor of the levitation scum and has an improved dewatering effect. .
According to a third aspect of the present invention, in the first or second aspect of the present invention, the levitation guidance device is a levitation that stands vertically from the bottom of the levitation separation tank so that the upper end opening faces the scum intake port. An induction pipe, a pipe for introducing sewage from the outside into the levitation induction pipe, and an air diffuser for supplying air from an air supply source into the levitation induction pipe. The air diffuser main body is provided with a tip diffuser main body and the supply pipe and the air diffuser main body can be detached as a single unit through a desorption guide pipe that connects the floating separation tank and the floating guide pipe. Can be kept in a state where a normal aeration function can always be performed by regular maintenance and inspection, and as a result, the scum can be lifted effectively and the scum can be lifted sufficiently reliably and efficiently. The pressurized flotation above equation scum separation processing apparatus can be provided.

従来の加圧浮上式スカム分離処理装置の一例を示す断面模式図。  FIG. 6 is a schematic cross-sectional view showing an example of a conventional pressurized floating scum separation processing apparatus. 図1のA部を拡大して示す断面図。  Sectional drawing which expands and shows the A section of FIG. 図1のスカムガイドの詳細を示す斜視図。  The perspective view which shows the detail of the scum guide of FIG. 本発明の加圧浮上式スカム分離処理装置の一実施形態を示す断面模式図。  The cross-sectional schematic diagram which shows one Embodiment of the pressurization floating type scum separation processing apparatus of this invention. 図4の装置の要部拡大断面図。  The principal part expanded sectional view of the apparatus of FIG. 加圧式空気溶解装置を装置外に設けた他の実施形態を示す拡大断面図。  The expanded sectional view which shows other embodiment which provided the pressurization type air dissolution apparatus outside the apparatus. スクリュウコンベアを水平に対し30度の角度に設定した実施形態を示す断面図。  Sectional drawing which shows embodiment which set the screw conveyor to the angle of 30 degree | times with respect to the horizontal. スカム取込口および連通筒についての他の実施形態を示す横断面図。  The cross-sectional view which shows other embodiment about a scum intake and a communicating cylinder. 図4のM部の拡大図。  The enlarged view of the M section of FIG. 図9のX−X線拡大断面図  XX expanded sectional view of FIG. 図9のXI−XI線拡大断面図。  XI-XI line expanded sectional view of FIG. 他の実施形態を示す浮上分離装置の断面模式図。  The cross-sectional schematic diagram of the floating separation apparatus which shows other embodiment. 図12の要部拡大図。  The principal part enlarged view of FIG.

図4は本発明の一実施形態を示している。この実施形態において浮上分離装置1は本発明の要部である一部を除いて図1の従来例と同様であるので同様な部分については同一の符号を付して説明に代える。浮上分離装置1の槽本体3は、設置基盤から一定高さ(例えば、2m前後)の架台66上に脱着可能に載せ付けられている。図4における架台66は、4本の脚台67と矩形枠状をした載置台68が図示されている。  FIG. 4 shows an embodiment of the present invention. In this embodiment, the levitating / separating apparatus 1 is the same as the conventional example of FIG. 1 except for a part which is a main part of the present invention. The tank body 3 of the levitation separator 1 is detachably mounted on a gantry 66 having a certain height (for example, around 2 m) from the installation base. The gantry 66 in FIG. 4 shows four leg bases 67 and a mounting base 68 having a rectangular frame shape.

槽本体3の底壁70には、スカム取込口20の下方に同心状に対応するように浮上誘導装置の要部である浮上誘導パイプ71が脱着可能に載置固定されている。この浮上誘導パイプ71は、直径350mm程度の丸形の筒体であるが、三角筒形や四角筒形でもよく、上部の絞り部72を有する上端開口73が下からスカム取込口20に同心状に向くようにして垂直に立てられている。  On the bottom wall 70 of the tank body 3, a levitation guide pipe 71, which is a main part of the levitation guidance device, is detachably mounted and fixed so as to correspond concentrically below the scum inlet 20. The levitation guide pipe 71 is a round cylinder having a diameter of about 350 mm, but may be a triangle cylinder or a square cylinder, and an upper end opening 73 having an upper throttle portion 72 is concentric with the scum inlet 20 from below. Standing vertically so that it faces the shape.

浮上誘導パイプ71の下部中央位置には、先端をエルボ形のラッパ式にした汚水供給管62が浮上分離槽2を通じて接続されている。75はガイド筒で、上下をラッパ状にした円筒体で浮上誘導パイプ71の下部に汚水供給管62の先端と同心状をなすように固定設置されるとともに浮上誘導パイプ71との間に隙間を設けておくことで沈降物が発生した場合それらを下方へ導いて自動弁を介して適宜外部に排出し得るようにしてある。  A sewage supply pipe 62 whose tip is an elbow-shaped trumpet type is connected to the center of the lower part of the levitation guide pipe 71 through the levitation separation tank 2. Reference numeral 75 denotes a guide cylinder, which is a cylindrical body having a trumpet shape on the top and bottom. If sediments are generated by providing them, they can be guided downward and discharged appropriately through an automatic valve.

77は散気装置であり、この散気装置77は、浮上誘導パイプ71の下部中央に位置する散気装置本体78を備え、この散気装置本体78は、図9に示すように下向きから上方へと圧縮空気を噴出する脱着式多孔板79とケーシング80とを備える。82は脱着ガイドパイプで、前後を貫通状とし散気装置本体78よりも大きな内径を有する丸(あるいは角)パイプでなり、その一端は浮上誘導パイプ71に連通させ他端は浮上分離槽2外にフランジを介して連通するように水平に固定されている。  Reference numeral 77 denotes an air diffuser, and the air diffuser 77 includes an air diffuser main body 78 positioned at the lower center of the levitation guide pipe 71. The air diffuser main body 78 is upward from below as shown in FIG. A detachable perforated plate 79 for ejecting compressed air and a casing 80 are provided. Reference numeral 82 denotes a desorption guide pipe, which is a round (or square) pipe having a front and rear penetration and a larger inner diameter than the diffuser main body 78, one end communicating with the levitation guide pipe 71 and the other end outside the levitation separation tank 2. It is fixed horizontally so as to communicate with each other through a flange.

83は供給管で、空気供給源56からの空気を浮上誘導パイプ71内へと散気装置77を介して導入するためのパイプで、この空気供給管83の周りには、図8ないし図10に示すように、逆流防止用の前シール板84と後閉止板85の他に脱着ガイドパイプ82内を進退スライドできる振れ止め板86を備えるとともに、空気供給管83の先端には連通状に散気装置本体78を備えている。前シール板84は、脱着ガイドパイプ82内でシールパッキン(図示省略)を介して内外を遮断するが、脱着ガイドパイプ82内に添ってそのまま進退することもできるようになっている。後閉止板85は脱着ガイドパイプ82の外部端のフランジに止着具を介して水密状に取り付けられ必要に応じて取り外しも可能なようになっている。  Reference numeral 83 denotes a supply pipe, which is a pipe for introducing air from the air supply source 56 into the levitation induction pipe 71 via the air diffuser 77, and around the air supply pipe 83, FIGS. As shown in FIG. 4, in addition to the front seal plate 84 and the rear closing plate 85 for preventing backflow, there is provided a steady plate 86 capable of sliding back and forth in the attachment / detachment guide pipe 82, and at the tip of the air supply pipe 83 is scattered in a continuous manner. A gas device body 78 is provided. The front seal plate 84 shuts off the inside and outside of the desorption guide pipe 82 via seal packing (not shown), but can also advance and retreat as it is along the desorption guide pipe 82. The rear closing plate 85 is attached to a flange at the outer end of the attachment / detachment guide pipe 82 in a watertight manner via a fastener, and can be removed as necessary.

止着具を外して後閉止板85を脱着ガイドパイプ82から外し外向きに抜くと散気装置本体78は脱着ガイドパイプ82内を通過することができ、その際、振れ止め板86や前シール板84は脱着ガイドパイプ82内にスライドしてゆくことで散気装置本体78が落ち込むことなく同心状に支持されながら円滑に外部へと取り出されることになる。図9に仮想線で示すように、散気装置77の特に空気供給管83や多孔板79など異物の詰まりやすい部材や部品を簡単に点検整備したり交換することもできるようになる。点検整備等の終えた散気装置77は、前シール板84を脱着ガイドパイプ82内に入れてスライドさせてゆけば容易に元の状態に戻すことができ、前シール板84と後閉止板85が脱着ガイドパイプ82に対し水密状になることでシール性の高い散気装置を得ることができるようになっている。  When the fastener is removed and the rear closing plate 85 is removed from the attachment / detachment guide pipe 82 and pulled outward, the diffuser main body 78 can pass through the attachment / detachment guide pipe 82, and at that time, the steady plate 86 and the front seal The plate 84 slides into the attachment / detachment guide pipe 82, so that the diffuser body 78 is smoothly taken out while being supported concentrically without dropping. As indicated by phantom lines in FIG. 9, members and parts that are likely to be clogged with foreign substances such as the air supply pipe 83 and the porous plate 79 of the air diffuser 77 can be easily inspected and serviced or replaced. The air diffuser 77 that has been inspected and maintained can be easily restored to its original state by inserting the front seal plate 84 into the attachment / detachment guide pipe 82 and sliding it, and the front seal plate 84 and the rear closing plate 85. As a result of being watertight with respect to the desorption guide pipe 82, it is possible to obtain an air diffuser with high sealing performance.

図4では汚水と空気溶解・浮上とを浮上誘導パイプ71内で行うようにしてあったが、図5に示すように、槽2外でスカム含有汚水と過飽和微細空気混じり水とを合流させてのち槽2内の浮上誘導パイプ71内に導入するように構成する場合もある。即ち、88は加圧式空気溶解装置で、その本体である空気溶解槽89には空気微細化ユニット90とバネ付勢式開閉弁91とが脱着交換整備可能に内装され、槽89の一端にはコンプレッサでなる空気供給源92が接続されるとともに分離水槽5からの給水管11がユニット90の下流側に連通するように接続されている。この装置88で作られた過飽和微細空気混合水はスカム含有汚水62と合流されて浮上誘導パイプ82内に導入されてスカムSを浮上分離させるように構成されている。  In FIG. 4, sewage and air dissolution / levitation are performed in the levitation guide pipe 71. However, as shown in FIG. 5, scum-containing sewage and supersaturated fine air mixed water are combined outside the tank 2. There may be a case where it is configured to be introduced into the levitation guide pipe 71 in the tank 2 later. That is, 88 is a pressurized air dissolving device, and an air refining unit 90 and a spring-biased on-off valve 91 are installed in the main body of the air dissolving tank 89 so as to be able to be attached / detached and replaced. An air supply source 92 made of a compressor is connected, and a water supply pipe 11 from the separation water tank 5 is connected to communicate with the downstream side of the unit 90. The supersaturated fine air-mixed water produced by the device 88 is combined with the scum-containing sewage 62 and introduced into the levitation guide pipe 82 to levitate and separate the scum S.

一方、分離水槽5は、図4に示すように、その上端前後が半円状凹欠部95とされ、この凹欠部95を介してケーシング18をセットすることにより図示しない連結具により相互を連結固定してスクリュウコンベア17の安定化を図っている。
そして、この場合の分離水槽5には、側壁に固定した回転支持具96にエルボ型のオーバーフローパイプ97を回転操作可能に取り付けることにより、適宜回転角度でロックも可能な回転操作ハンドル98によりパイプ口98を上下調節可能に構成したもので、これにより、分離水槽5内の水位を自由に変更できるようにすることができる。
On the other hand, as shown in FIG. 4, the separation water tank 5 has a semicircular concave notch 95 at the front and back of the upper end. The screw conveyor 17 is stabilized by connecting and fixing.
In this case, the separation water tank 5 is provided with a rotary operation handle 98 that can be locked at an appropriate rotation angle by attaching an elbow overflow pipe 97 to a rotary support 96 fixed to the side wall so as to be rotatable. 98 is configured to be adjustable up and down, whereby the water level in the separation water tank 5 can be freely changed.

この場合の望む水位は図1の水位Hを基準にすればH+Aとされる。Hは、スカム取込口20の傾斜方向上方の下周り下端部の高さを示すもので、Aは、掻揚スクリュウ23のスクリュウ径Dの1/2よりも高い、この実施形態ではスクリュウ径Dと略同じ寸法(高さ)とされる。
従って、浮上分離槽2上のケーシング18内の水面レベルもH+Aと同一に調整される。ここで、掻き揚げの好ましい条件として、図5のレベルラインのようにAをスクリュウ径Dの1/2よりも高くする。スカム取込口20の傾斜方向上方の下周り下端部nを基準としてその垂直上方へD/2程度以上に水位を設定しておけばスカムSも同レベルまで浮上して及び、そうするとn点を境に傾斜方向前後に亘るQの範囲もスカムSが浮上し溜まってくることになるから、スクリュウ部分q1とq2が回転すればこれらQ部分のスカムSはケーシング18のスカム取込口20より上方の円筒内であるY方向に確実に掻き揚げられることになる。掻き揚げが確実化・効率化するとその後の圧搾脱水作用も効果的に行われるようになる。
The desired water level in this case is H + A based on the water level H in FIG. H indicates the height of the lower lower end of the scum intake port 20 in the inclination direction, and A is higher than ½ of the screw diameter D of the lifting screw 23. In this embodiment, the screw diameter The dimension (height) is substantially the same as D.
Therefore, the water level in the casing 18 on the floating separation tank 2 is also adjusted to be the same as H + A. Here, as a preferable condition for the raking, A is set to be higher than ½ of the screw diameter D as shown in the level line of FIG. If the water level is set to about D / 2 or more vertically upward with respect to the lower lower end n of the scum intake port 20 above the inclination direction, the scum S also rises to the same level, and then the n point is set. Since the scum S also floats and accumulates in the Q range in the front and rear of the tilt direction at the boundary, the scum S of these Q parts is above the scum inlet 20 of the casing 18 when the screw parts q1 and q2 rotate. It is surely lifted up in the Y direction in the cylinder. If the fried food is made reliable and efficient, the subsequent dewatering action is effectively performed.

特に、図4、図5にH+Aで示すようにAをスクリュウ径Dと略同じ程度の高さ寸法に水位を設定しておけばスカムSが更に高いレベルにまで浮上して及びn点以上の浮上スカムSは全周がケーシング18に包囲された形になるので矢印Yのような掻き揚げがより一層確実で能率的になされるようになるだけでなく、n点より傾斜方向下方にもスカムSが多量に浮上して円筒内一杯に溜まることになるのでそれらスカムS分が前記n点以上のスカムSを掻き揚げ作用して掻き揚げが全体として確実かつ能率的なものになる。前記Aは限りなく高くすればよい訳ではなく、脱水手段の構成部材が没すると脱水機能が確保できなくなるため、脱水手段の下端の構成部材である圧縮受盤26より十分傾斜方向下方に水位を設定するようにすべきである。
尚、分離水槽5にH+Aの高さに図1のように定位置開口型のオーバーフロー口を開けておき水位は一定化したものにすることもできる。
前記掬い揚げ突条23bはスクリュウ自体の掻き揚げ機能の向上により、省略することができる。
In particular, as shown by H + A in FIGS. 4 and 5, if the water level is set to a height approximately the same as the screw diameter D, the scum S rises to a higher level and is higher than n points. The levitation scum S is surrounded by the casing 18 so that the levitation scum S is not only more reliably and efficiently lifted up as indicated by the arrow Y, but also scum below the n point in the inclination direction. Since a large amount of S floats and accumulates in the cylinder as a whole, the scum S portion lifts up the n or more scums S, so that the entire rake is surely and efficient. The above-mentioned A does not have to be increased as much as possible. Since the dewatering function cannot be secured when the dehydrating means is submerged, the water level should be sufficiently lower than the compression receiving plate 26, which is the lower end of the dehydrating means. Should be set.
In addition, the water level can be made constant by opening a fixed-position opening type overflow opening as shown in FIG.
The scooping ridge 23b can be omitted due to the improvement of the scooping function of the screw itself.

図7は他の実施形態を示すもので、この実施形態は、スクリュウコンベア17が水平線を基準にして30°に立ち上がった例を示し、この場合、矢印Zのように脱水分である水の切れが良くなる利点がある。
図8は他の実施形態を示すもので、この実施形態は、ケーシング18の半円部分を切り欠いて広い角度範囲のスカム取込口20とすることでスカムSがスクリュウコンベア内により多く容易に入り込めるようにしたものである。連通筒eはスカム取込口20の形状に応じてケーシング18の両脇高さまで立ち上がって連結されている。
FIG. 7 shows another embodiment, and this embodiment shows an example in which the screw conveyor 17 rises to 30 ° with respect to the horizontal line. Has the advantage of improving.
FIG. 8 shows another embodiment. In this embodiment, the semi-circular portion of the casing 18 is cut out to form a scum intake port 20 in a wide angle range, so that the scum S can be more easily increased in the screw conveyor. It was designed to enter. The communication cylinder e rises up to both side heights of the casing 18 according to the shape of the scum inlet 20 and is connected.

図12および図13は他の実施形態を示している。従来の加圧浮上式スカム分離処理装置においては、図2に示すようにスカムSはスカム取込口20を越えた該口20の傾斜上方以上のところまで掻き込みができればあとはケーシング18が外まわりにあることから順に掻き揚げることができるが、図2のH程度の浅い水位であってしかも掻揚スクリュウ23の面が全て15°程度の立ち上がった面となっていると、掻揚スクリュウ23の面により掻き揚げられるスカムSが図2の矢印Xのように斜め側方である連通筒e内に掻き送る運動を繰り返すのみとなり、その結果、スカムSは掻きこぼしされることからスカム取込口20の開口縁を越えて傾斜上方のケーシング18の全円筒部分へと掻き揚げにくく、従って、掻き揚げが確実にかつ効率的に行えずその後の圧搾脱水も所定通りに行えなくなるという問題があった。  12 and 13 show another embodiment. In the conventional pressurized levitation type scum separation processing apparatus, as shown in FIG. 2, the scum S can be swept beyond the scum intake port 20 beyond the inclination of the port 20, and then the casing 18 is turned around. However, if the surface of the cradle screw 23 is all about 15 °, the surface of the cradle screw 23 is The scum S swept up by the surface only repeats the movement of scraping into the communicating tube e that is obliquely sideways as indicated by the arrow X in FIG. 2, and as a result, the scum S is spilled and the scum intake port It is difficult to scrape over the opening edge of 20 to the entire cylindrical part of the casing 18 at the upper side of the slope. Therefore, the scraping cannot be reliably and efficiently performed, and the subsequent pressing and dewatering can be performed as prescribed. There is a problem that Kunar.

そこで、この実施形態では、スカム取込口20の傾斜方向の長さBを図面上では55mmとし、このスカム取込口20の寸法Bに対応する部分より少し長い寸法分の長ピッチスクリュウ本体23cとし、残りの大部分の短ピッチスクリュウ本体23aにしてラセン状に互いをつないでスクリュウ本体を形成したものである。短ピッチスクリュウ本体23aは1/2×P2(1/2ピッチ)は図面上では12mmである一方長ピッチスクリュウ本体23cは1/2×P1(1/2ピッチ)は図面上ではその5倍の6mmとされている。  Therefore, in this embodiment, the length B in the inclination direction of the scum inlet 20 is 55 mm in the drawing, and the long pitch screw main body 23c is slightly longer than the portion corresponding to the dimension B of the scum inlet 20. The remaining short pitch screw main body 23a is connected to each other in a spiral shape to form a screw main body. The short pitch screw body 23a has a size of 1/2 × P2 (1/2 pitch) of 12 mm in the drawing, while the long pitch screw body 23c has a size of 1/2 × P1 (1/2 pitch) of 5 times that in the drawing. It is set to 6 mm.

長ピッチスクリュウ本体23cには掬い揚げ突条23bが付されて掻き揚げ効果が上がるようにされている。長ピッチスクリュウ本体23cは図13に示すようにその羽根の外周接線とスクリュウコンベア17を横断する面とのなす角度は45°とされることで前記のように他よりも長いピッチ部分をスカム取込口20に対応させて回転掻揚自在としたので、スカム取込口20から浮上してくるスカムSを切って図2のようなX方向でなく図13のようなY方向(軸方向)に掻き揚げることにより掻き揚げが確実かつ能率的になされるとともにその後の脱水作用も効果的になされるようになった。また、長ピッチスクリュウ本体23cは短ピッチスクリュウ本体23aよりも1回転当たりのスカム送り量が数倍多くなり、その結果、短ピッチスクリュウ本体23a側へのスカムの送りが多くなることから脱水(圧縮)作用がより積極的になされるようになる。  The long pitch screw main body 23c is provided with scooping ridges 23b so as to increase the filing effect. As shown in FIG. 13, the long pitch screw body 23c has a 45 ° angle between the outer peripheral tangent line of its blades and the surface crossing the screw conveyor 17 so that the longer pitch portion can be scummed as described above. Since the rotation can be swung freely corresponding to the inlet 20, the scum S rising from the scum inlet 20 is cut, and the Y direction (axial direction) as shown in FIG. 13 instead of the X direction as shown in FIG. In this way, it is possible to surely and efficiently carry out the filing and to effectively perform the subsequent dehydration. Further, the long pitch screw body 23c has several times more scum feed per rotation than the short pitch screw body 23a, and as a result, more scum is fed to the short pitch screw body 23a side, resulting in dehydration (compression). ) The action becomes more active.

尚、水位は、図2のHのように浅くしても前記掻き揚げ効果が得られるが、より確実に掻き揚げ効果を得ることを目的とする場合には、図13のH+Aのように高くすれば長ピッチスクリュウ本体23cの全体を水没状態にして同様にレベルの高いスカムS域の中に該本体23cを没して掻き揚げを確実にすることができる。スクリュウ径をDとした場合、Aは0からD/2の範囲にしたり、D/2〜Dの範囲のいずれかにすることができる。しかし、この実施形態では、図13のQの範囲、即ち、少なくともn点からD/2程度高くなったレベルに水位を設定確保することでスカムSを掻きこぼしなく矢印Yのようにスカム取込口20からケーシング18の全円筒部分内へと確実に掻き揚げられるように構成する。Aをスクリュウ径D程度に高くすることでより確実な掻き揚げができるようになる。
図12の100は縦長状のオーバーフロー口、101は高さ調節堰、102は堰木ガイドである。前記スクリュウの角度は40ないし50°の範囲でもよい。
The water level can be obtained even if it is shallow as shown in FIG. 2H. However, when the water level is intended to obtain the effect more reliably, it is as high as H + A in FIG. Then, the entire long pitch screw main body 23c can be submerged, and the main body 23c can be submerged in the scum S region having a high level to ensure the lifting. When the screw diameter is D, A can be in the range of 0 to D / 2, or can be in the range of D / 2 to D / 2. However, in this embodiment, the water level is set and secured within the range of Q in FIG. 13, that is, at least about D / 2 from the point n, so that the scum S is taken in as indicated by the arrow Y without scraping. It is configured so as to be surely lifted from the mouth 20 into the entire cylindrical portion of the casing 18. By raising A to about the screw diameter D, it becomes possible to more reliably fry up.
In FIG. 12, 100 is a vertically long overflow port, 101 is a height adjusting weir, and 102 is a weir guide. The angle of the screw may be in the range of 40 to 50 °.

1…浮上分離装置 2…浮上分離槽 3…槽本体 5…分離水槽 17…スクリュウコンベア 18…ケーシング 26、33…脱水手段 20…スカム取込口 22…スクリュウ軸 23…掻揚スクリュウ 35…排出口 40…駆動源(駆動手段)。  DESCRIPTION OF SYMBOLS 1 ... Levitation separation apparatus 2 ... Levitation separation tank 3 ... Tank main body 5 ... Separation water tank 17 ... Screw conveyor 18 ... Casing 26, 33 ... Dehydration means 20 ... Scum intake port 22 ... Screw shaft 23 ... Lifting screw 35 ... Discharge port 40: Drive source (drive means).

Claims (3)

収集したスカム含有汚水を加圧空気を伴って供給する浮上誘導装置を備えた浮上分離槽と、この浮上分離槽に連通して清澄水を分離水として貯留するとともにその貯留水が浮上分離槽内の水位と同じレベルの水位とされてその排水も可能とされた分離水槽とを有し、浮上分離槽は、前記浮上誘導装置から浮上しつつ傾斜状のスカムガイドに案内されてきたスカムを集める連通筒をその槽上部に備えるとともに、前記浮上分離槽の上側には、スクリュウコンベア式スカム排出装置がその一端を低く他端を高くして傾斜状をなして固定され、前記スカム排出装置は、円筒状でその傾斜方向下側の下周りに開設した矩形状のスカム取込口を前記連通筒に連通状をなすように連結固定されるとともに傾斜方向上側の下周りに開設した排出口を通じてスカムを排出可能とされたケーシングと、このケーシングに内装されてスカムを傾斜上方へ掻き揚げるように設けられた掻揚スクリュウと、前記ケーシングの上部内に設けられていて掻き揚げられてくるスカムを圧縮して水分を除去するための脱水手段とを有する加圧浮上式スカム分離処理装置において、前記浮上分離槽内の汚水は、スカム取込口の傾斜方向上方の下周り下端部を基準として掻揚スクリュウのスクリュウ径Dの1/2よりも高いレベルを水面として設定されていることを特徴とする加圧浮上式スカム分離処理装置。  A floating separation tank equipped with a levitation induction device that supplies collected scum-containing sewage with pressurized air, and stores clarified water as separated water in communication with the floating separation tank, and the stored water is stored in the floating separation tank. A separation water tank that has the same water level as that of the water level and can also be drained, and the floating separation tank collects the scum that has been guided by the inclined scum guide while floating from the levitation guide device. A communicating cylinder is provided at the top of the tank, and on the upper side of the floating separation tank, a screw conveyor type scum discharge device is fixed in an inclined shape with its one end lowered and the other end raised, and the scum discharge device is A rectangular scum intake port that is formed in a cylindrical shape in the lower part on the lower side in the tilt direction is connected and fixed so as to communicate with the communication tube, and is formed through a discharge port that is provided in the lower part on the upper side in the tilt direction. A casing capable of discharging a vacuum, a scraping screw provided in the casing so as to scrape up the scum, and a scum that is lifted up in the upper part of the casing. In the pressurized flotation scum separation processing apparatus having a dewatering means for compressing and removing water, the sewage in the flotation separation tank is scraped with reference to the lower lower end portion of the scum intake port at the upper part in the inclination direction. A pressure levitation scum separation treatment apparatus characterized in that a level higher than ½ of a screw diameter D of a lifting screw is set as a water surface. 請求項1に記載のものにおいて、スクリュウコンベアの掻揚スクリュウは、スカム取込口に対応する長さ部分に設けられたスクリュウ部分が他のスクリュウ部分よりも長いピッチとして形成されている加圧浮上式スカム分離処理装置。  2. The flotation screw of a screw conveyor according to claim 1, wherein the screw portion provided on the length portion corresponding to the scum intake port is formed with a longer pitch than the other screw portions. Type scum separation processing device. 請求項1または2に記載のものにおいて、浮上誘導装置は、上端開口がスカム取込口に向くようにして浮上分離槽の槽底部から垂直に立てられた浮上誘導パイプと、外部からの汚水を浮上誘導パイプ内に導入する配管と、空気供給源からの空気を浮上誘導パイプ内に供給する散気装置とを備え、この散気装置は、供給管とその先端の散気装置本体とを備えるとともにこれら供給管と散気装置本体とは1つのユニットとして浮上分離槽と浮上誘導パイプとをつなぐ脱着ガイドパイプを通じて脱着可能とされている加圧浮上式スカム分離処理装置。  The levitation guidance device according to claim 1 or 2, wherein the levitation guidance device is configured to cause a levitation guide pipe standing vertically from a bottom of the levitation separation tank so that an upper end opening faces the scum intake port, and sewage from the outside. A pipe to be introduced into the levitation induction pipe and an air diffuser for supplying air from the air supply source into the levitation induction pipe. The air diffuser includes a supply pipe and an air diffuser main body at the tip thereof. In addition, the pressure levitation type scum separation processing apparatus is configured such that the supply pipe and the diffuser main body are detachable as a unit through a detachment guide pipe that connects the levitation separation tank and the levitation guide pipe.
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CN113185013A (en) * 2021-04-08 2021-07-30 王彦婕 Coating wastewater treatment system
CN113185013B (en) * 2021-04-08 2023-12-26 重庆吉江环保产业集团有限公司 Coating wastewater treatment system

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