JPH09117606A - Defoaming device for waste water treatment device - Google Patents
Defoaming device for waste water treatment deviceInfo
- Publication number
- JPH09117606A JPH09117606A JP30062895A JP30062895A JPH09117606A JP H09117606 A JPH09117606 A JP H09117606A JP 30062895 A JP30062895 A JP 30062895A JP 30062895 A JP30062895 A JP 30062895A JP H09117606 A JPH09117606 A JP H09117606A
- Authority
- JP
- Japan
- Prior art keywords
- water
- disk
- foam
- defoaming
- scattering
- 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.)
- Granted
Links
Landscapes
- Degasification And Air Bubble Elimination (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】この発明は、密閉型廃水処理
装置又は曝気槽において発生する泡を機械的に破壊する
装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a closed wastewater treatment device or a device for mechanically destroying bubbles generated in an aeration tank.
【0002】[0002]
【従来の技術】従来密閉型廃水処理装置内の気泡を消泡
する手段としてシリコン系又はワックスエマルジョン等
の消泡剤を添加する方法やスプレー水を単独で又は併用
することが行なわれているが、前者は消泡剤のコストの
他に貯槽を設ける必要があり、後者は多量の水を必要と
するので大型ポンプを設置する必要がある。2. Description of the Related Art Conventionally, as a means for defoaming bubbles in a closed type wastewater treatment apparatus, a method of adding a defoaming agent such as a silicone type or wax emulsion, or spray water alone or in combination has been carried out. The former requires a storage tank in addition to the cost of the defoamer, and the latter requires a large amount of water, so a large pump must be installed.
【0003】[0003]
【発明が解決しようとする課題】本発明は、消泡剤を用
いずに低コストで貯槽又はポンプ等の消泡関係装置の設
置スペースを不用又は節減できる消泡装置を提供するも
のである。DISCLOSURE OF THE INVENTION The present invention provides a defoaming device which does not use an antifoaming agent and which can reduce the installation space of defoaming-related devices such as a storage tank or a pump at low cost.
【0004】[0004]
【課題を解決するための手段】本発明装置は、密閉型廃
水処理槽上部を貫通して取付けられた円筒消泡胴の下端
内縁に散水口付環状受樋が形成されると共に前記胴内に
垂直駆動軸に軸着された下面ブレード付散水円板が前記
受樋上部に位置し且つ前記胴内壁との間に散水落下間隙
を形成して設けられ、前記散水円板上に消泡散水が供給
されるように構成されている。散水円板と胴壁との間の
散水落下間隙は、円板周辺からの散水が有効に環状受樋
内に流下する程度の間隙であって、円板外周端が受樋内
壁の上方に位置する程度がよい。環状受樋の散水口は受
樋底面の他に側面に設けてもよい。According to the apparatus of the present invention, an annular gutter with a water spout is formed on the inner edge of the lower end of a cylindrical defoaming cylinder mounted so as to penetrate through the upper part of a closed type wastewater treatment tank, and at the same time, inside the cylinder. A sprinkler disc with a lower surface blade axially attached to a vertical drive shaft is provided at the upper part of the gutter and is provided with a sprinkling drop gap formed between the sprinkler disc and the inner wall of the trunk. Is configured to be supplied. The sprinkling drop gap between the sprinkling disc and the shell wall is such that the sprinkling from the disc periphery effectively flows down into the annular gutter, and the outer edge of the disc is located above the gutter inner wall. Good to do. The spout of the annular trough may be provided on the side surface in addition to the bottom surface of the trough.
【0005】[0005]
【発明の実施態様】図1は装置を三相流動槽に適用した
全体図であって、1は三相流動槽であり、供給される被
処理廃液が微生物固定化担体を伴って曝気によって槽内
を循環流動している。3は曝気装置、4はバッファ板、
5は整流板、6は溢流堰、7は槽上部を密閉しているフ
ードである。10は本発明装置であって、図2に示す如
く円筒状の消泡胴11がフード7を貫通して固設されて
いる。12は通気口12aが設けられた泡飛散防止筒、
13はモータスタンド、14は可変速モータである。1
5は回転軸であって、泡飛散防止室12の中心を貫通し
て中間部を通気孔16a付泡止め板又は放射状支持枠1
6によって支持17され、軸端は消泡胴11内に達して
いる。軸端には下面に消泡ブレード21を備えた散水円
板20が軸着されている。円板直径は胴壁との間に環状
間隙Pを形成するように円板外周が後述する受樋内壁2
6の直上に位置する程度がよい。ブレード21はL型又
は平型の板を円板20の下面に5〜6ケ軸対称又は図3
の如く偏心放射状に固定したものである。23は、胴1
1の槽挿入側ノド部であって下端開口24の内縁には環
状受樋25が胴と一体的に連設する内壁26によって形
成されると共に受樋底部には散水口27が穿設されてい
る。30は散水供給管であって、図示しないポンプに接
続され散水円板20上に開口している吐水口31から散
水する。上記装置において、散水円板の回転速度は、ブ
レード先端の円周速度が3〜6m/sになる範囲であっ
て、6m/s以上では泡の飛び跳ねが多くなり、円板上
方にまで泡が飛散するようになるので好ましくない。ま
た、散水量は10〜50L/Hrで充分である。さら
に、胴内の空気の空塔速度が0.7m/s以上になると
泡が胴上部にまで持ち上げられるので空塔速度を0.3
m/s〜0.7m/sの範囲になるようにノド部径Dを
設定するのがよい。上記装置において、槽内に発生した
泡は開口24から上昇するが回転するブレード21によ
って破砕され、破砕された小片は間隙Pを通って上昇し
ようとするが散水円板20上を遠心力によって移動して
きた流水が周縁から間隙を通って流下しているのでこれ
によって捕捉されて受樋25内に流下して散水口27か
ら液滴となって槽内に落下する。この液滴は水面上の泡
を破砕することにも寄与する。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS FIG. 1 is an overall view of the apparatus applied to a three-phase flow tank, in which 1 is a three-phase flow tank, and the waste liquid to be treated to be supplied is aerated by aeration with a microorganism-immobilized carrier. It circulates inside. 3 is an aerator, 4 is a buffer plate,
5 is a current plate, 6 is an overflow weir, and 7 is a hood that seals the upper part of the tank. Reference numeral 10 is a device of the present invention, and as shown in FIG. 2, a cylindrical defoaming cylinder 11 is fixedly installed through the hood 7. 12 is a bubble scattering prevention tube provided with a vent 12a,
Reference numeral 13 is a motor stand, and 14 is a variable speed motor. 1
Reference numeral 5 denotes a rotary shaft, which penetrates the center of the bubble scattering prevention chamber 12 and has an intermediate portion at a foam stop plate with a vent hole 16a or a radial support frame 1
It is supported 17 by 6, and the shaft end reaches the inside of the defoaming cylinder 11. A sprinkling disc 20 having a defoaming blade 21 on the lower surface is axially attached to the shaft end. The disk diameter is such that the outer circumference of the disk is a trough inner wall 2 which will be described later so as to form an annular gap P with the trunk wall.
It is better to be located just above 6. The blade 21 is an L-shaped or flat-shaped plate on the lower surface of the circular plate 20 having 5 to 6 axial symmetry or FIG.
It is fixed eccentrically and radially. 23 is the body 1
An annular gutter 25 is formed at an inner edge of the lower end opening 24 of the tank insertion side of No. 1 by an inner wall 26 integrally connected to the trunk, and a spout 27 is bored at a bottom part of the gutter. There is. A sprinkling supply pipe 30 sprinkles water from a spout 31 which is connected to a pump (not shown) and which is opened on the sprinkling disc 20. In the above device, the rotational speed of the sprinkling disk is within a range in which the circumferential speed of the blade tip is 3 to 6 m / s, and when the speed is 6 m / s or more, the bubbles jump frequently and the bubbles reach above the disk. It is not preferable because it will scatter. The amount of water sprayed is 10 to 50 L / Hr. Furthermore, when the superficial velocity of the air in the body is 0.7 m / s or more, bubbles are lifted up to the upper part of the body.
It is preferable to set the throat portion diameter D so as to be in the range of m / s to 0.7 m / s. In the above apparatus, the bubbles generated in the tank rise through the opening 24 but are crushed by the rotating blade 21, and the crushed small pieces try to rise through the gap P, but move on the sprinkling disk 20 by centrifugal force. The flowing water flowing down from the peripheral edge through the gap is trapped by the flowing water and flows down into the trough 25 to form droplets from the sprinkling port 27 and drop into the tank. The droplets also contribute to breaking bubbles on the water surface.
【0006】[0006]
【実施例】有効容積56m3、曝気量11Nm3/分の密
閉型三相流動総廃水処理装置に、空塔速度が0.5m/
secになるようにノド径部Dを0.7mに設定した図
2,図3のような装置を設置して水溶性インキ製造工場
の廃水を処理した。回転羽根の円周速度5.23m/s
(モータ回転数166rpm)、散水量20L/Hrと
して運転することによって消泡剤を使用せずに槽内で発
生した泡を消泡できた。因に、上記廃水をスプレー法に
よって消泡する場合の水の使用量は14,000L/H
rであって、本発明によれば大量の水及び給水設備が節
約される。Example A closed type three-phase fluidized total wastewater treatment device with an effective volume of 56 m 3 and an aeration rate of 11 Nm 3 / min was used, and the superficial velocity was 0.5 m / min.
The waste water of the water-soluble ink manufacturing plant was treated by installing the apparatus shown in FIGS. 2 and 3 in which the throat diameter portion D was set to 0.7 m so that the time became sec. Circumferential velocity of the rotating blade 5.23m / s
By operating (motor rotation speed 166 rpm) and water sprinkling amount of 20 L / Hr, the bubbles generated in the tank could be defoamed without using the defoaming agent. The amount of water used for defoaming the waste water by the spray method is 14,000 L / H.
r, the present invention saves a large amount of water and water supply equipment.
【0007】[0007]
【効果】本発明は、従来必要であった大量の水を節約で
き、又は消泡剤を全く使用しないので処理コストを大幅
に低減できて経済的である他、特別の給水施設も貯槽も
不要であって設備面積も節約できる効果がある。[Effect] The present invention can save a large amount of water, which is conventionally required, or does not use an antifoaming agent at all, so that the treatment cost can be greatly reduced and it is economical, and no special water supply facility or storage tank is required. Therefore, there is an effect that the equipment area can be saved.
【図1】本発明装置を三相流動槽上に設置した全体図。FIG. 1 is an overall view of the apparatus of the present invention installed on a three-phase flow tank.
【図2】本発明装置の要部断面図。FIG. 2 is a sectional view of an essential part of the device of the present invention.
【図3】図2のA−A線断面矢視図。FIG. 3 is a sectional view taken along line AA of FIG. 2;
11 消泡胴 12 泡飛散防止室 16 泡止め板 20 散水円板 21 消泡回転羽根 23 胴のノド部 24 開口 25 環状受樋 26 内壁 27 散水口 30 散水供給管 31 吐出口 11 Defoaming cylinder 12 Foam scattering prevention chamber 16 Foam stop plate 20 Sprinkling disk 21 Defoaming rotary blade 23 Throat throat 24 Opening 25 Annular gutter 26 Inner wall 27 Sprinkling port 30 Sprinkling supply pipe 31 Discharging port
Claims (2)
られた円筒消泡胴の下端内縁に散水口付環状受樋が形成
されると共に前記胴内に垂直駆動軸に軸着された下面ブ
レード付散水円板が前記受樋上部に位置し且つ前記胴内
壁との間に散水落下間隙を形成して設けられ、前記散水
円板上に消泡散水が供給されることを特徴とする廃水処
理装置用消泡装置。1. A lower surface of a cylindrical defoaming cylinder mounted penetrating an upper part of a closed type waste water treatment tank, wherein an annular gutter with a water spout is formed on an inner edge of a lower end of the cylindrical defoaming cylinder, and a vertical drive shaft is axially attached to the cylinder. A waste water characterized in that a water sprinkling disc with a blade is located above the trough and is provided with a sprinkling drop gap between it and the inner wall of the trunk, and defoaming water sprinkling is supplied onto the water sprinkling disc. Defoaming device for processing equipment.
ねた泡止め板を介して泡飛散防止室が設けられてなる請
求項1記載の消泡装置。2. The defoaming device according to claim 1, wherein a bubble scattering prevention chamber is provided above the water sprinkling disk via a foam stopping plate which also serves as a bearing support for the drive shaft.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP7300628A JP3056407B2 (en) | 1995-10-25 | 1995-10-25 | Defoaming equipment for wastewater treatment equipment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP7300628A JP3056407B2 (en) | 1995-10-25 | 1995-10-25 | Defoaming equipment for wastewater treatment equipment |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH09117606A true JPH09117606A (en) | 1997-05-06 |
JP3056407B2 JP3056407B2 (en) | 2000-06-26 |
Family
ID=17887156
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP7300628A Expired - Fee Related JP3056407B2 (en) | 1995-10-25 | 1995-10-25 | Defoaming equipment for wastewater treatment equipment |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP3056407B2 (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2003305305A (en) * | 2002-04-16 | 2003-10-28 | Copros Co Ltd | Defoaming device in wastewater treatment tank |
CN107140707A (en) * | 2017-07-07 | 2017-09-08 | 四川西普石油物资装备有限公司 | Realize the bubble removing method of desulfurization wastewater concentration tower |
-
1995
- 1995-10-25 JP JP7300628A patent/JP3056407B2/en not_active Expired - Fee Related
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2003305305A (en) * | 2002-04-16 | 2003-10-28 | Copros Co Ltd | Defoaming device in wastewater treatment tank |
CN107140707A (en) * | 2017-07-07 | 2017-09-08 | 四川西普石油物资装备有限公司 | Realize the bubble removing method of desulfurization wastewater concentration tower |
Also Published As
Publication number | Publication date |
---|---|
JP3056407B2 (en) | 2000-06-26 |
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