JP3056407B2 - Defoaming equipment for wastewater treatment equipment - Google Patents

Defoaming equipment for wastewater treatment equipment

Info

Publication number
JP3056407B2
JP3056407B2 JP7300628A JP30062895A JP3056407B2 JP 3056407 B2 JP3056407 B2 JP 3056407B2 JP 7300628 A JP7300628 A JP 7300628A JP 30062895 A JP30062895 A JP 30062895A JP 3056407 B2 JP3056407 B2 JP 3056407B2
Authority
JP
Japan
Prior art keywords
defoaming
watering
wastewater treatment
equipment
water
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
JP7300628A
Other languages
Japanese (ja)
Other versions
JPH09117606A (en
Inventor
邦昭 平野
正 鈴木
昭典 斉藤
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Denka Consultant and Engineering Co Ltd
Original Assignee
Denka Consultant and Engineering Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Denka Consultant and Engineering Co Ltd filed Critical Denka Consultant and Engineering Co Ltd
Priority to JP7300628A priority Critical patent/JP3056407B2/en
Publication of JPH09117606A publication Critical patent/JPH09117606A/en
Application granted granted Critical
Publication of JP3056407B2 publication Critical patent/JP3056407B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

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  • Degasification And Air Bubble Elimination (AREA)

Description

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

【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 an apparatus for mechanically destroying bubbles generated in a closed type wastewater treatment apparatus or 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 air bubbles in a closed type wastewater treatment apparatus, a method of adding a defoaming agent such as a silicon-based or wax emulsion or spray water alone or in combination has been used. The former requires the provision of a storage tank in addition to the cost of the defoamer, and the latter requires a large pump because it requires a large amount of water.

【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。
SUMMARY OF THE INVENTION An object of the present invention is to provide a defoaming apparatus which does not use an antifoaming agent and can save or reduce the installation space for 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 present invention, there is provided a cylindrical defoaming cylinder mounted through the upper part of a closed type wastewater treatment tank, wherein an annular spout with a water spout is formed at an inner edge of a lower end of the cylinder. A sprinkling disc with a lower blade attached to a vertical drive shaft is provided above the gutter and formed with a sprinkling drop gap between the spout and the inner wall of the body, and defoaming sprinkling on the sprinkling disc is provided. It is configured to be supplied. The watering gap between the watering disc and the body wall is such that water from around the disc can effectively flow down into the annular gutter, and the outer peripheral edge of the disc is located above the inner wall of the gutter. Good degree to do. The water spout of the annular gutter may be provided on the side surface in addition to the bottom surface of the gutter.

【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。
DESCRIPTION OF THE PREFERRED EMBODIMENTS FIG. 1 is an overall view in which the apparatus is applied to a three-phase fluidized tank. Reference numeral 1 denotes a three-phase fluidized vessel, in which waste liquid to be treated is supplied by aeration with a microorganism-immobilized carrier. It is circulating inside. 3 is an aeration device, 4 is a buffer plate,
Reference numeral 5 denotes a current plate, reference numeral 6 denotes an overflow weir, and reference numeral 7 denotes a hood that seals an upper portion of the tank. Reference numeral 10 denotes a device of the present invention, and a cylindrical defoaming cylinder 11 is fixedly provided through the hood 7 as shown in FIG. 12 is a foam scattering prevention cylinder provided with a vent 12a,
13 is a motor stand, and 14 is a variable speed motor. 1
Reference numeral 5 denotes a rotating shaft, which penetrates the center of the bubble scattering prevention chamber 12 and has an intermediate portion provided with a foam stopper plate or a radial support frame 1 having a vent hole 16a.
The shaft end reaches the inside of the defoaming cylinder 11. A sprinkling disk 20 having a defoaming blade 21 on the lower surface is axially attached to the shaft end. The diameter of the disk is such that the outer periphery of the disk has a gutter inner wall 2 to be described later so as to form an annular gap P with the body wall.
It is good to be located just above the number 6. The blade 21 is formed by forming an L-shaped or flat plate on the lower surface of the disk 20 by 5 to 6 axial symmetries or FIG.
It is fixed in an eccentric radial manner as shown in FIG. 23 is the torso 1
An annular gutter 25 is formed on the inner edge of the lower end opening 24 at the inner edge of the lower end opening 24 by an inner wall 26 integrally connected to the body, and a water spout 27 is drilled at the bottom of the gutter. I have. Reference numeral 30 denotes a watering supply pipe, which is connected to a pump (not shown) and sprays water from a water discharge port 31 opened on the watering disk 20. In the above apparatus, the rotation speed of the watering disc is in a range where the circumferential speed of the blade tip is 3 to 6 m / s. It is not preferable because it scatters. Further, a watering amount of 10 to 50 L / Hr is sufficient. Further, when the superficial velocity of the air in the body becomes 0.7 m / s or more, the bubbles are lifted to the upper part of the main 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 device, the foam generated in the tank rises from the opening 24 and is crushed by the rotating blade 21, and the crushed small pieces try to rise through the gap P but move on the watering disc 20 by centrifugal force. Since the flowing water flows down from the peripheral edge through the gap, it is caught by the water and flows down into the receiving gutter 25 to be dropped from the water spouting port 27 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 three-phase fluidized total wastewater treatment apparatus having an effective volume of 56 m 3 and an aeration rate of 11 Nm 3 / min was supplied with a superficial velocity of 0.5 m / m.
The apparatus shown in FIG. 2 and FIG. 3 in which the throat diameter D was set to 0.7 m so as to be sec. was used to treat wastewater from a water-soluble ink manufacturing plant. 5.23 m / s circumferential speed of rotating blades
(Motor rotation speed: 166 rpm), and by operating at a water spraying rate of 20 L / Hr, foam generated in the tank could be defoamed without using an antifoaming agent. The amount of water used when defoaming the wastewater by the spray method is 14,000 L / H.
r, a large amount of water and water supply is saved according to the invention.

【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。
According to the present invention, a large amount of water required conventionally can be saved, or the treatment cost can be greatly reduced because no defoaming agent is used. Therefore, no special water supply facility or storage tank is required. This has the effect of saving the equipment area.

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

【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 fluidized vessel.

【図2】本発明装置の要部断面図。FIG. 2 is a sectional view of a main 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;

【符号の説明】[Explanation of symbols]

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 DESCRIPTION OF SYMBOLS 11 Defoaming cylinder 12 Foam scattering prevention room 16 Antifoaming plate 20 Sprinkling disc 21 Defoaming rotating blade 23 Body throat 24 Opening 25 Annular gutter 26 Inner wall 27 Sprinkling port 30 Sprinkling supply pipe 31 Discharge port

───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 昭53−39260(JP,A) 特開 昭56−150407(JP,A) 特開 昭49−87564(JP,A) 実開 平6−70802(JP,U) 実開 昭62−1709(JP,U) 実開 昭59−93605(JP,U) 実開 昭57−39605(JP,U) (58)調査した分野(Int.Cl.7,DB名) B01D 19/02 ──────────────────────────────────────────────────続 き Continuation of the front page (56) References JP-A-53-39260 (JP, A) JP-A-56-150407 (JP, A) JP-A-49-87564 (JP, A) 70802 (JP, U) Japanese Utility Model Showa 62-1709 (JP, U) Japanese Utility Model Showa 59-93605 (JP, U) Japanese Utility Model Showa 57-39605 (JP, U) (58) Field surveyed (Int. 7 , DB name) B01D 19/02

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 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環状受樋に囲まれた開口24
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 cylindrical defoaming cylinder mounted through the upper part of a closed type wastewater treatment tank, having an annular gutter with a sprinkling port formed at an inner edge of a lower end thereof and a lower surface axially mounted on a vertical drive shaft in the cylinder. A watering disc with a blade is located above the opening 24 surrounded by the annular gutter and is provided so as to form a watering drop gap with the inner wall of the body, and defoaming watering is supplied onto the watering disc. A defoaming device for a wastewater treatment device, characterized in that:
【請求項2】 散水円板の上方に駆動軸の軸受支持を兼
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 foam scattering prevention chamber is provided above the watering disc via a foam stopper plate also serving as a bearing support for the drive shaft.
JP7300628A 1995-10-25 1995-10-25 Defoaming equipment for wastewater treatment equipment Expired - Fee Related JP3056407B2 (en)

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 JPH09117606A (en) 1997-05-06
JP3056407B2 true 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)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP3733484B2 (en) * 2002-04-16 2006-01-11 株式会社コプロス 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
JPH09117606A (en) 1997-05-06

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