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JP5250921B1 - Pressurized floating scum separation treatment device - Google Patents

Pressurized floating scum separation treatment device Download PDF

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JP5250921B1
JP5250921B1 JP2012185838A JP2012185838A JP5250921B1 JP 5250921 B1 JP5250921 B1 JP 5250921B1 JP 2012185838 A JP2012185838 A JP 2012185838A JP 2012185838 A JP2012185838 A JP 2012185838A JP 5250921 B1 JP5250921 B1 JP 5250921B1
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scum
separation tank
tank
casing
air
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JP2014012263A (en
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利保 東
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San Ei KK
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Abstract

【課題】浮上分離槽で浮上するスカムを圧縮作用で脱水しながら掻揚排出することにより排出後の搬送が省エネのもとに可能となりしかも搬送先でのスカムと水分との分離工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提供する。
【解決手段】収集したスカム含有汚水を加圧式空気溶解装置45により発生する水とともに浮上分離槽2内に噴出させてスカムを同浮上分離槽2内に浮上させ、掻揚スクリュウ23とスカムガイド19付きスカム取込口20および掻揚スクリュウ用回転駆動手段40とを有したスクリュウコンベア17で浮上したスカムを排出する。
【選択図】図1
[PROBLEMS] By removing the scum that floats in the levitation separation tank by means of compression and dewatering while dewatering, it is possible to transport the scum after discharge while saving energy and simplifying the separation process of scum and moisture at the transport destination as much as possible. There is provided a pressure levitation type scum separation processing apparatus adapted to be able to be realized.
The collected scum-containing sewage is spouted into the levitation separation tank 2 together with water generated by a pressurized air dissolving device 45 to levitate the scum into the levitation separation tank 2, and the cradle screw 23 and the scum guide 19 The scum that floats on the screw conveyor 17 having the attached scum intake 20 and the rotary screw rotation drive means 40 is discharged.
[Selection] Figure 1

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噴出させて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 will be discharged from the top by spraying under reduced pressure with water in which air is dissolved by pressurization and promoting scum ascent. The pressurized levitation method 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された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、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、浮上したスカムが水分を充分に含んだまま排出されるため、スカム処理施設への搬送に無駄な電力が消費し、しかも搬送先でスカムと水分とを再度分離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 is designed to smoothly convey the scum that has been levitated to the scum treatment facility far away from the scum that has been discharged from the pressurized levitation and concentration tank. The means consists of a scraper, which is a chain with a scraping plate protruding from the outer periphery, and a discharger with a scraping blade that moves along a curved surface and rotates around the rotation axis. The scum from the discharger is discharged into the scum. Therefore, since the scum that floated is discharged with sufficient moisture, wasteful power is consumed for transport to the scum treatment facility, and the scum and moisture are transported to the transport destination. And it will be necessary to separate them again.

本発明は、こうした問題を解決しようとするものであり、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工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提供することを目的とする。  The present invention is intended to solve these problems. The scum that floats in the levitation separation tank is raked and discharged while draining by a compression action, thereby enabling transportation after discharge while saving energy and transport destination. It is an object of the present invention to provide a pressure levitation type scum separation processing apparatus capable of simplifying the separation process of scum and moisture in the process as much as possible.

本発明は上記目的を達成するため、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により空気を溶解させる加圧式空気溶解装置により発生する水とともに浮上分離槽内に噴出させてスカムを同浮上分離槽内に浮上させるとともに浮上したスカムをスカム排出装置により排出するように構成し、前記スカム排出装置は、掻揚スクリュウとスカム取込口付きケーシングおよび掻揚スクリュウ用回転駆動手段とを有し、前記ケーシングは、浮上分離槽において傾斜状に設置されてその傾斜方向下部が浮上分離槽に支持される一方傾斜方向上部が水面より高い浮上分離槽外に位置してケーシングに形成した排出口を通じて掻き揚げスカムを排出可能とされるとともに、前記スカム取込口は、ケーシングにおける傾斜方向下部の下周りにおいて開設されて浮上してくるスカムを斜面ガイド付きスカムガイドを介して取り込み可能に構成されている加圧浮上式スカム分離処理装置において、少なくともスカム取込口に対応する掻揚スクリュウの周縁部には、前記傾斜方向上方へ向けて突出する掬い揚げ突条が設けられていることを特徴とする In order to achieve the above-mentioned object, the invention according to claim 1 is configured such that the collected scum-containing sewage is jetted into a floating separation tank together with water generated by a pressurized air dissolving device that dissolves air by pressurization. The scum is floated in the floating separation tank, and the floated scum is discharged by a scum discharge device. The scum discharge device includes a lifting screw, a casing with a scum intake, and a rotary drive means for the lifting screw The casing is installed in an inclined manner in the floating separation tank, and the lower part in the inclined direction is supported by the floating separation tank, while the upper part in the inclined direction is located outside the floating separation tank higher than the water surface and is formed in the casing. The discharged scum can be discharged through the discharged outlet, and the scum intake opening is located below the lower part of the casing in the inclined direction. In the pressurized levitation scum separation processing device that is configured to be able to take in the scum that is established and floats through the scum guide with the slope guide, at least the peripheral portion of the lifting screw corresponding to the scum intake port A scooping ridge projecting upward in the tilt direction is provided .

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により空気を溶解させる加圧式空気溶解装置により発生する水とともに浮上分離槽内に噴出させてスカムを同浮上分離槽内に浮上させるとともに浮上したスカムをスカム排出装置により排出するように構成し、前記スカム排出装置は、掻揚スクリュウとスカム取込口付きケーシングおよび掻揚スクリュウ用回転駆動手段とを有し、前記ケーシングは、浮上分離槽において傾斜状に設置されてその傾斜方向下部が浮上分離槽に支持される一方傾斜方向上部が水面より高い浮上分離槽外に位置してケーシングに形成した排出口を通じて掻き揚げスカムを排出可能とされるとともに、前記スカム取込口は、ケーシングにおける傾斜方向下部の下周りにおいて開設されて浮上してくるスカムを斜面ガイド付きスカムガイドを介して取り込み可能に構成されている加圧浮上式スカム分離処理装置において、少なくともスカム取込口に対応する掻揚スクリュウの周縁部には、前記傾斜方向上方へ向けて突出する掬い揚げ突条が設けられていることを特徴とするので、浮上分離槽で浮上するスカムを圧縮作用で脱水しながら掻揚排出することにより排出後の搬送が省エネのもとに可能となりしかも搬送先でのスカムと水分との分離工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提供することができる。特に、回転してくる掬い揚げ突条が、浮上してきたスカムを確実に掬い揚げることによって掻き揚げ作用を確実かつ多量化し、掬い揚げミスをなくすことができるとともに、圧縮作用によるスカムの脱水作用を積極的なものとし、さらに掬い揚げ突条の存在はスクリュウコンベアの補強にもなる。As described above, according to the first aspect of the present invention, the collected scum-containing sewage is jetted into the floating separation tank together with water generated by a pressurized air dissolving device that dissolves air by pressurization, and the scum is floated in the floating separation tank. And the scum discharging device is configured to discharge the scum that has floated in the scum by a scum discharging device, the scum discharging device has a lifting screw, a casing with a scum intake, and a rotation driving means for the lifting screw, The casing is installed in an inclined manner in the floating separation tank, and the lower part in the inclined direction is supported by the floating separation tank, while the upper part in the inclined direction is positioned outside the floating separation tank higher than the water surface and is raked up through a discharge port formed in the casing. The scum can be discharged, and the scum intake port is opened and floated around the lower part of the casing in the inclined direction. In the pressurized flotation type scum separation processing apparatus configured to be able to take in the coming scum through the scum guide with a slope guide, at least the peripheral portion of the lifting screw corresponding to the scum intake port is directed upward in the inclination direction. It is characterized by a ridge that protrudes toward the surface, so that the scum that floats in the levitation separation tank is raked and discharged while dewatering by compression action, so that transportation after discharge can be saved In addition, it is possible to provide a pressure-flotation type scum separation processing apparatus that is capable of simplifying the separation process of scum and moisture at the conveyance destination as much as possible. In particular, the rotating scooping ridge makes sure that the scum that has been lifted is scooped up reliably, thereby increasing the amount of fisting action, eliminating mistakes in scooping, and reducing the scum dehydrating action due to the compression action. In addition, the presence of the scooping ridges also reinforces the screw conveyor.

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模式図。The schematic diagram which shows one Embodiment of the pressurization floating type scum separation processing apparatus of this invention. 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2のIII−III線に沿う拡大断面図。The expanded sectional view which follows the III-III line of FIG. 図1のスカムガイドの詳細をスクリュウコンベアとの関係において示す分解斜視図。The disassembled perspective view which shows the detail of the scum guide of FIG. 1 in relation to a screw conveyor. 掬い揚げ突条の他の実施形態を示す断面図。Sectional drawing which shows other embodiment of a deep-fried protrusion. 図1のB部を拡大して示す断面図。Sectional drawing which expands and shows the B section of FIG. 図6のVII−VII線断面図。VII-VII line sectional drawing of FIG. 空気溶解槽についての他の実施形態を示す模式断面図。The schematic cross section which shows other embodiment about an air dissolution tank.

以下、本発明である加圧浮上式スカム分離処理装置の一実施形態を図1ないし4に基づいて説明する。尚、以下、浮上分離装置や加圧水発生装置などは金属材料、特にステンレス材を使用することを基本とするが、そのことに限定されない。  Hereinafter, an embodiment of a pressure levitation type scum separation processing apparatus according to the present invention will be described with reference to FIGS. In the following description, the floating separator and the pressurized water generator are based on the use of a metal material, particularly stainless steel, but are not limited thereto.

図1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を備える。浮上分離槽2は、槽本体3と分離槽5とを仕切り壁4を介して有し、これら槽本体3と分離槽5内には、レベルHまで汚水6および分離水7が溜められる。8は連通管で、槽本体3と分離槽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、その水位Hは可動堰により上下に調節可能としてもよい。分離槽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に導入するようになっている。  In FIG. 1, reference numeral 1 denotes a levitation separation apparatus, which includes a levitation separation tank 2 that 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 tank 5 via a partition wall 4, and the sewage 6 and the separated water 7 are stored up to level H in the tank body 3 and the separation tank 5. A communication pipe 8 is a pipe that connects the tank body 3 and the separation tank 5, and purified water having a filter 9 at the front and rear ends is introduced into the separation tank 5 as separated water 7. An overflow port 10 determines the water level H. The water level H may be adjusted up and down by a movable weir. The separation water 7 in the separation tank 5 is discharged to the outside through the overflow port 10, while the separation water 7 is drawn from the bottom of the separation tank 5 through the water supply pipe 11 by the operation of the water supply pump 12, which will be described later. The air 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。この供給管14には減圧弁を備えてもよい。
槽本体3と分離槽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。この傾斜角度は、20度、30度…のように変更することがある。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. The supply pipe 14 may be provided with a pressure reducing valve.
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 separation tank 5 in an inclined state of about 15 degrees. This inclination angle may be changed to 20 degrees, 30 degrees, and so on. 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.

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。図3のように、この掬い揚げ突条23bの突出量W1は、スクリュウ本体23aの外径Dを300mmとした場合、50mm前後とされるが、W2のように75mm前後としてもよく、また100mm前後と大きく突出させることもある。この掬い揚げ突条23bは、図3の右欄のようにアングル材をラセン状に形成した別体ものをスクリュウ本体23aの周縁に溶接あるいは止着固定してもよい。また、掬い揚げ突条23bは、図5に示すように、丸ロッドや丸パイプあるいは角パイプ状のものにして溶接一体化するようにしてもよい。さらに、同掬い揚げ突条23bは、Lに限定して一部に設けられているが、スクリュウ本体23aの全長に亘って設けてもよい。A scooping ridge 23b that protrudes upward in the inclined direction is integrally provided as a spiral strip at the peripheral edge of the main body 23a extending over a length L that is equal to or longer than the length corresponding to the scum inlet 20. . As shown in FIG. 3, the protrusion amount W1 of the scooping ridge 23b is about 50 mm when the outer diameter D of the screw body 23a is 300 mm, but may be about 75 mm as in W2, or 100 mm. It may protrude greatly from front to back. The scooping ridges 23b may be welded or fixed to the periphery of the screw body 23a, as shown in the right column of FIG. Further, as shown in FIG. 5 , the scooping ridges 23b may be round rods, round pipes or square pipes and welded together. Furthermore, although the scooping ridge 23b is provided in a part limited to L, it may be provided over the entire length of the screw body 23a.

ここで、図1、図2および図4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。  Here, reference numeral 19 in FIGS. 1, 2 and 4 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4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。尚、斜面ガイドcは、直板を斜めにしたものであるが、湾曲した板材を使ってもよい。  As shown in detail in FIG. 4, 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. The inclined surface guide c is a straight plate that is slanted, but a curved plate material may be used.

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4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および図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。The communication tube e is a vertically penetrating tube portion having left and right inclined plate-like opposing walls f and front and rear walls g and h, and the opposing wall f takes 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 indicate the water surface of the sewage 6, and the water surface H is approximately the height of the groove bottom of the fitting receiving groove j of the communication tube e.

尚、図4の右上に示すように、左右の壁fには取付フランジkを設けて止着具mによりケーシング18に脱着可能に構成してもよい。取付作業が簡略になるとともにメンテナンスも至便になる。前後の壁g,hの湾曲する縁部に沿った湾曲板状をした取付フランジを設けて同じく脱着可能にしてもよい。  As shown in the upper right of FIG. 4, the left and right walls f may be provided with mounting flanges k so as to be detachable from the casing 18 by the fasteners m. Installation work is simplified and maintenance is convenient. A mounting flange having a curved plate shape along the curved edges of the front and rear walls g, h may be provided so as to be removable.

スクリュウ軸22の傾斜方向上部周りには、図6および図7に示すように、圧縮受盤26が装備されている。圧縮受盤26は、ケーシング18の内径よりも少し小さい外径をもった円板状の受板27を本体として備え、同受板27の中心に備えた中央ボス28に滑動しやすい円筒樹脂製の内スライダ29を備えてスクリュウ軸22周りを軸方向に進退自在とし、さらに受板27の外周にも滑動しやすい円筒樹脂製の外スライダ30を備え付けてケーシング18内周に添って進退自在にしてある。そして、受板27の背部には、複数のガイドパイプ31を突設する一方、ケーシング18の端面側に突設したガイドバー32を各ガイドパイプ31に摺動自在に嵌め入れてある。ガイドバー32周りには弾発手段である反発バネ33を備えて掻揚スクリュウ23によって掻き揚げられてきたスカムに圧縮作用を加えるべく圧縮受盤26に反発力を常時与えるように構成されている。As shown in FIGS. 6 and 7, a compression receiving plate 26 is provided around the upper portion of the screw shaft 22 in the inclination direction. The compression receiving plate 26 includes a disk-shaped receiving plate 27 having an outer diameter slightly smaller than the inner diameter of the casing 18 as a main body, and is made of a cylindrical resin that is easily slidable on a central boss 28 provided at the center of the receiving plate 27. The inner slider 29 is provided so that the screw shaft 22 can be moved forward and backward in the axial direction, and the outer periphery of the receiving plate 27 is provided with an outer slider 30 made of a cylindrical resin which is slidable so as to be movable forward and backward along the inner periphery of the casing 18. It is. A plurality of guide pipes 31 project from the back portion of the receiving plate 27, and guide bars 32 projecting from the end face side of the casing 18 are slidably fitted into the guide pipes 31. The guide bar 32 is provided with a repulsion spring 33 as a resilient means so that a repulsive force is constantly applied to the compression receiving plate 26 so as to apply a compression action to the scum that has been lifted up by the lifting screw 23. .

35排出口で、ケーシング18の傾斜方向上部下周りに開設され、同排出口35の傾斜方向下端開口縁よりも傾斜方向下方寄り位置に復帰時の圧縮受盤26が位置するようになっている。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6の矢印方向に回転駆動させるようになっている。
尚、図1の右上に示すように、掻揚スクリュウ23を傾斜方向上方の端まで設けたものをここで排除するものではない。
また、シュート38からのスカムは、ベルトなどのコンベアで直接搬送することもあるし、コンベアによらず移動可能なコンテナ37に収集して搬送することもある。
35 is a discharge port, which is opened around the upper lower part of the casing 18 in the inclination direction, and the compression receiving plate 26 at the time of return is positioned at a lower position in the inclination direction than the lower opening edge of the discharge port 35 in the inclination direction. . 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 the arrow in FIG .
In addition, as shown in the upper right of FIG. 1, what provided the lifting screw 23 to the upper end of the inclination direction is not excluded here.
Further, the scum from the chute 38 may be directly conveyed by a conveyor such as a belt, or may be collected and conveyed in a container 37 that can be moved regardless of the conveyor.

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。尚、空気溶解槽46は、2本配備されているが、後述するスカム含有汚水の収集量に適応すべく3本以上設けることがある。  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. Although two air dissolution tanks 46 are provided, three or more air dissolution tanks 46 may be provided to adapt to the amount of scum-containing sewage collected later.

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(給気手段)56に接続されている。ブロア56はコンプレッサーに代えることができる。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。  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 a blower (air supply means) 56 through each air pipe 55. The blower 56 can be replaced with a compressor. Each of the air pipes 55 is provided with an air automatic valve 57 in a controllable manner.

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。  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。給水ポンプ12を運転して分離槽5内の分離水7を利用して一方の空気溶解槽46へ給水する。空気溶解槽46への流入は入側自動弁50(空気あるいは電動作動式)を開放してなされる。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またはコンプレッサー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が開き、それによりスカム含有汚水と空気の溶解した加圧水とが混合し、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の本体槽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. The water supply pump 12 is operated to supply water to one air dissolution tank 46 using the separated water 7 in the separation tank 5. The inflow into the air dissolution tank 46 is made by opening the inlet side automatic valve 50 (air or electrically operated type). 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 the air nozzle 53 injects the atomized air into the air dissolution tank 46, thereby causing one of the air dissolution tanks. 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 pressurized water is mixed, and the mixture is fed into the main body tank 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はスカム取込口20を通じて取り込まれて掻き揚げられてゆくが、スカム取込口20へのスカムSの取り込みは、スカムガイド19による斜面ガイドにより円滑かつ確実になされる。スカム取込口20からのスカムSは、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。掬い揚げられたスカムSは、反発バネ33に抗して圧縮受盤26を押上げてゆき、図6の仮想線で示す圧縮受盤26の位置より手前位置まで移動させながら脱水作用をし、さらに圧縮受盤26を仮想線位置まで押上げてゆくことで排出口35よりシュート38へと排出する。一方、浮上分離槽2の本体槽3内の分離水は、その底部のフィルター9付き連通管8を通じて分離槽5内に導入されてオーバーフロー口10を通じて排水される一方、前記のように加圧水として再利用される。  The fine bubbles from the mixed water that has been sent in will float with scum. The floated scum S is taken in and scraped up through the scum inlet 20, but the scum S is taken into the scum inlet 20 smoothly and reliably by the slope guide by the scum guide 19. The scum S from the scum inlet 20 is surely scooped up by the scooping function by the scooping ridge 23b attached to the lifting screw 23. The scooped scum S pushes up the compression receiving plate 26 against the repulsion spring 33 and dehydrates it while moving it from the position of the compression receiving plate 26 indicated by the phantom line in FIG. Further, the compression receiving plate 26 is pushed up to the imaginary line position and discharged from the discharge port 35 to the chute 38. On the other hand, the separated water in the main body tank 3 of the floating separation tank 2 is introduced into the separation tank 5 through the communication pipe 8 with the filter 9 at the bottom and drained through the overflow port 10. Used.

空気溶解槽46が複数槽設けられていると、スカム含有汚水が多量化した場合に活用される。即ち、スカム含有汚水が通常量の場合には、一方の空気溶解槽46のみで充足できるが、多量化した場合にはそれだけでは応じきれないので、他方の空気溶解槽46も並行して運転し、図例の2本槽の場合には、一方の空気溶解槽46において給水から加圧溶解をしさらに排出運転がなされる間それに時間差をもって並行して他方の空気溶解槽46において同じ給水→加圧溶解→排出運転をすることで排出工程を連続して行うことができるものである。例えば、一方の空気溶解槽46からの排出が終わるタイミングに他方の空気溶解槽46からの排出開始タイミングを略合わせることで行われる。3本以上の空気溶解槽46を構成した場合も同様のタイミングを設定する。  When a plurality of air dissolution tanks 46 are provided, it is utilized when the amount of scum-containing sewage increases. That is, when the scum-containing sewage is in a normal amount, it can be satisfied with only one air dissolution tank 46, but when it is increased in quantity, it cannot be satisfied with it alone. In the case of the two tanks shown in the figure, the pressure is dissolved from the water supply in one air dissolution tank 46 and the discharge operation is further performed. The discharge process can be performed continuously by performing pressure dissolution → discharge operation. For example, it is performed by substantially matching the discharge start timing from the other air dissolution tank 46 with the timing at which the discharge from one air dissolution tank 46 ends. The same timing is set when three or more air dissolution tanks 46 are configured.

尚、一方の空気溶解槽46からの排出が終わったあと一定の時間差をおいて他方の空気溶解槽46の排出が開始されるようにタイミングをとってもよい。
また、空気溶解槽46は、図8に示すように、多孔板や網状材などのエアー噴出材66を外カバー67の下開口に装着して微細エアーを導入可能にしてもよい。この場合、空気溶解槽46内の残留分をドレンしたあとで空気噴出材66を通じて空気を吹き込むことにより同空気噴出材66の目詰まりを除去することができる。前記分離槽5には補給水管を通じて分離水を補充可能にしてもよい。
It should be noted that a timing may be taken so that the discharge of the other air dissolution tank 46 is started after a certain time difference after the discharge from one air dissolution tank 46 ends.
Further, as shown in FIG. 8, the air dissolving tank 46 may be provided with an air blowing material 66 such as a perforated plate or a net-like material in a lower opening of the outer cover 67 so that fine air can be introduced. In this case, clogging of the air blowing material 66 can be removed by blowing the air through the air blowing material 66 after draining the residue in the air dissolution tank 46. The separation tank 5 may be replenished with separated water through a makeup water pipe.

1…浮上分離装置 2…浮上分離槽 3…槽本体 5…分離槽 17…スクリュウコンベア 18…ケーシング 19…スカムガイド 20…スカム取込口 22…スクリュウ軸 23…掻揚スクリュウ 23a…スクリュウ本体 23b…掬い揚げ突条 26…圧縮受盤 33…反発バネ 35…排出口 40…駆動源(駆動手段) 45…加圧式空気溶解装置 46…空気溶解槽 DESCRIPTION OF SYMBOLS 1 ... Levitation separation apparatus 2 ... Levitation separation tank 3 ... Tank main body 5 ... Separation tank 17 ... Screw conveyor 18 ... Casing 19 ... Scum guide 20 ... Scum intake 22 ... Screw shaft 23 ... Lifting screw 23a ... Screw main body 23b ... Crawling ridge 26 ... Compression receiving plate 33 ... Repulsion spring 35 ... Discharge port 40 ... Driving source (driving means) 45 ... Pressurized air dissolving device 46 ... Air dissolving tank

Claims (1)

収集したスカム含有汚水を加圧により空気を溶解させる加圧式空気溶解装置により発生する水とともに浮上分離槽内に噴出させてスカムを同浮上分離槽内に浮上させるとともに浮上したスカムをスカム排出装置により排出するように構成し、前記スカム排出装置は、掻揚スクリュウとスカム取込口付きケーシングおよび掻揚スクリュウ用回転駆動手段とを有し、前記ケーシングは、浮上分離槽において傾斜状に設置されてその傾斜方向下部が浮上分離槽に支持される一方傾斜方向上部が水面より高い浮上分離槽外に位置してケーシングに形成した排出口を通じて掻き揚げスカムを排出可能とされるとともに、前記スカム取込口は、ケーシングにおける傾斜方向下部の下周りにおいて開設されて浮上してくるスカムを斜面ガイド付きスカムガイドを介して取り込み可能に構成されている加圧浮上式スカム分離処理装置において、少なくともスカム取込口に対応する掻揚スクリュウの周縁部には、前記傾斜方向上方へ向けて突出する掬い揚げ突条が設けら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。The collected scum-containing sewage is jetted into the floating separation tank together with water generated by a pressurized air dissolving device that dissolves air by pressurization, and the scum is floated in the floating separation tank and the scum that floated is The scum discharge device has a lifting screw, a casing with a scum intake port, and a rotation driving means for the lifting screw, and the casing is installed in an inclined manner in the floating separation tank. The lower part in the inclined direction is supported by the floating separation tank, while the upper part in the inclined direction is located outside the floating separation tank higher than the water surface, and the scum can be discharged through the discharge port formed in the casing. The mouth is a scum guide with a slope guide that is opened around the lower part of the lower part of the casing in the inclination direction and rises. In the pressurized levitation type scum separation processing device configured to be able to be taken in via the scum, a scooping ridge projecting upward in the inclined direction at least on the peripheral portion of the lifting screw corresponding to the scum taking-in port Is provided with a pressure levitation type scum separation processing device.
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