JP2011218266A - Microbubble sewage regenerating apparatus having scum mechanism - Google Patents

Microbubble sewage regenerating apparatus having scum mechanism Download PDF

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JP2011218266A
JP2011218266A JP2010088251A JP2010088251A JP2011218266A JP 2011218266 A JP2011218266 A JP 2011218266A JP 2010088251 A JP2010088251 A JP 2010088251A JP 2010088251 A JP2010088251 A JP 2010088251A JP 2011218266 A JP2011218266 A JP 2011218266A
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water
scum
treatment tank
water treatment
microbubble
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Yuji Maeda
勇司 前田
Tamio Igarashi
民夫 五十嵐
Yoshihiro Nobutomo
義弘 信友
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Hitachi Ltd
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Abstract

PROBLEM TO BE SOLVED: To provide a microbubble sewage regenerating apparatus having a scum mechanism that can discharge scum effectively.SOLUTION: The microbubble sewage regenerating apparatus having a scum mechanism includes: a water treatment tank 1 in which water to be treated flows; a plurality of partition plates 2 disposed in the water treatment tank 1; an ozone gas injection device 4 in which a part of the water to be treated in the water treatment tank 1 is extracted and mixed with ozone gas; a high pressure pump 5 in which the gas-liquid two-phase flow mixed by the ozone gas injection device 4 raises voltage; a microbubble generator 6 in which the gas-liquid two phase flow with raised pressure by the high pressure pump 5 is jetted from a plurality of small holes to generate microbubbles; and a scum outlet 10 in which a helical water stream guide is provided inside to remove generated scum during the microbubbles generated by the microbubble generator 6 flow down in the water treatment tank 1.

Description

本発明は、マイクロバブル下水再生装置に付属したスカム排出口の壁面に付着したスカムや、肥大化して排出口の縁を乗り越えられないスカムを残存しないように除去できるスカム機構を具備したマイクロバブル下水再生装置に関する。   The present invention relates to a microbubble sewage system provided with a scum mechanism capable of removing scum adhering to a wall surface of a scum discharge port attached to a microbubble sewage regeneration apparatus and a scum that is enlarged and cannot get over the edge of the discharge port. The present invention relates to a playback device.

マイクロバブル下水再生装置は、オゾンを微細気泡にして処理水を浄化する装置である。   The microbubble sewage reclaiming device is a device that purifies treated water by making ozone into fine bubbles.

〔非特許文献1〕によれば、微細気泡は、直径が50マイクロメータ以下の気泡のことであり、一般にマイクロバブルと呼ばれる。このようなサイズの気泡は、周囲の流体に溶け込み、液中で縮小していくことによって約2分で完全に溶解する。微細気泡は、周囲の液体に溶け込み、その直径が減少するため、表面張力が大きくなる効果により高温で高圧となる。又、気泡は微細になるほど体積に対する表面積比が大きくなるため、溶解効率が高くなり、気体の圧力に比例して溶解度が増加するヘンリーの法則にしたがって溶解がさらに促進される。微細気泡は、その消滅時に殺菌力を有するラジカルを発生し、このラジカルによって、殺菌,有機物の分解ができるため、浄化,殺菌,消毒できるとされている。   According to [Non-Patent Document 1], fine bubbles are bubbles having a diameter of 50 micrometers or less and are generally called microbubbles. Bubbles of such a size dissolve completely in the surrounding fluid and are completely dissolved in about 2 minutes by shrinking in the liquid. The fine bubbles are dissolved in the surrounding liquid and the diameter thereof is reduced, so that the pressure becomes high at a high temperature due to the effect of increasing the surface tension. In addition, since the surface area ratio with respect to the volume increases as the bubbles become finer, the dissolution efficiency increases, and the dissolution is further promoted according to Henry's law in which the solubility increases in proportion to the pressure of the gas. It is said that fine bubbles generate radicals having sterilizing power when they disappear, and these radicals can sterilize and decompose organic substances, so that they can be purified, sterilized and disinfected.

また、〔非特許文献2〕によれば、マイクロバブルの表面に油粒子が吸着され、油粒子とともに浮上していくことが報告されている。   According to [Non-Patent Document 2], it is reported that oil particles are adsorbed on the surface of microbubbles and float along with the oil particles.

マイクロバブルを用いた下水再生装置においても、下水中に含まれる細かな濁質の膜(以下、スカムという)が形成されるのが観測できる。良質な再生水を提供するためには、定期的にこのスカムを除去する必要がある。   Even in a sewage recycling apparatus using microbubbles, it can be observed that a fine turbid film (hereinafter referred to as scum) contained in sewage is formed. In order to provide good quality recycled water, it is necessary to remove this scum periodically.

「水の特性と新しい利用技術」、株式会社エヌ・ティー・エス、2004年"Characteristics of water and new utilization technology", NTS Corporation, 2004 「微細気泡の最新技術」、株式会社エン・ティー・エス、2006年"The latest technology of fine bubbles", ENTS Co., Ltd., 2006

マイクロバブルを用いた下水再生装置では、スカム除去装置が設けられるが、スカム排出口では、処理水槽の壁面に付着したスカム、或いは肥大化したスカムが排出口を乗り越えられないという問題があり、スカムが残存し、スカム排出口付近に付着して排出できなくなるという問題がある。   In the sewage recycling device using microbubbles, a scum removing device is provided. However, at the scum discharge port, there is a problem that the scum adhering to the wall surface of the treated water tank or the enlarged scum cannot get over the discharge port. Remains, adheres to the vicinity of the scum outlet and cannot be discharged.

本発明の目的は、スカムを効果的に排出できるスカム機構を具備したマイクロバブル下水再生装置を提供することにある。   An object of the present invention is to provide a microbubble sewage recycling apparatus having a scum mechanism that can effectively discharge scum.

上記目的を達成するために、本発明のスカム機構を具備したマイクロバブル下水再生装置は、被処理水を流入する水処理槽と、水処理槽内に設置された複数の仕切板と、水処理槽内の被処理水の一部を抽水してオゾンガスと混合するオゾンガス注入装置と、オゾンガス注入装置により混合された気液二相流を昇圧する高圧ポンプと、高圧ポンプで昇圧された気液二相流を小さな複数の孔から噴出してマイクロバブルを発生する微細気泡生成装置と、微細気泡生成装置で生成されたマイクロバブルを水処理槽内を流下させる際に発生するスカムを除去するための内側にらせん状の水流ガイドを設けたスカム排出口を備えたものである。   In order to achieve the above object, a microbubble sewage regeneration apparatus equipped with a scum mechanism of the present invention includes a water treatment tank into which water to be treated flows, a plurality of partition plates installed in the water treatment tank, and a water treatment An ozone gas injection device that extracts a portion of the water to be treated in the tank and mixes it with ozone gas, a high-pressure pump that boosts the gas-liquid two-phase flow mixed by the ozone gas injection device, and a gas-liquid two boosted by the high-pressure pump A microbubble generator that generates microbubbles by ejecting a phase flow from a plurality of small holes, and a scum that is generated when the microbubbles generated by the microbubble generator flow down the water treatment tank. It has a scum outlet with a spiral water flow guide on the inside.

本発明によれば、スカム排出口で、排水に渦流を発生させてスカム排出口付近のスカムを効果的に除去することができ、スカムをスムーズに排出できる。   According to the present invention, a vortex can be generated in the drainage at the scum discharge port to effectively remove the scum near the scum discharge port, and the scum can be discharged smoothly.

マイクロバブル下水再生装置の構成図。The block diagram of a micro bubble sewage reproduction | regeneration apparatus. スカム排出口を拡大した斜視図。The perspective view which expanded the scum discharge port. スカムを排出する時の処理フロー図。The processing flowchart when discharging scum.

本発明の一実施例を図1から図3を用いて説明する。図1は、本実施例の水処理設備の構成図である。   An embodiment of the present invention will be described with reference to FIGS. FIG. 1 is a configuration diagram of the water treatment facility of this embodiment.

水処理槽1は、複数の仕切板2a〜2cが設置され、水処理槽1内が複数のゾーンに仕切られている。仕切板2は、上部を固定した仕切板2a,2cと下部を固定した仕切板2bが交互に設置され、仕切板2aの上流側の水処理槽1の上部側から下水処理水(以下、被処理水という)が流入する。   The water treatment tank 1 is provided with a plurality of partition plates 2a to 2c, and the water treatment tank 1 is partitioned into a plurality of zones. The partition plate 2 has partition plates 2a and 2c with fixed upper portions and partition plates 2b with fixed lower portions alternately installed. From the upper side of the water treatment tank 1 on the upstream side of the partition plate 2a, sewage treated water (hereinafter, covered) Treated water).

水処理槽1の外部には、オゾン発生装置3、オゾン発生装置3で発生したオゾンガスをオゾンガス注入装置4に導くための配管16、水処理槽1下部から一部抽水された被処理水を取り入れ、配管16で導かれたオゾンガスを被処理水中に混合するオゾンガス注入装置4、オゾンガス注入装置4で混合された気液二相流を昇圧する高圧ポンプ5、高圧ポンプ5で昇圧された気液二相流を配管17で導き、小さな複数の孔から噴出してマイクロバブルを発生する微細気泡生成装置6、微細気泡発生装置6で発生したマイクロバブルを水処理槽1の仕切板2aの上流側に導く配管18が設置されている。   Outside of the water treatment tank 1, the ozone generator 3, the pipe 16 for guiding the ozone gas generated by the ozone generator 3 to the ozone gas injection device 4, and the water to be treated partially extracted from the lower part of the water treatment tank 1 are taken in. The ozone gas injection device 4 that mixes ozone gas guided by the pipe 16 into the water to be treated, the high-pressure pump 5 that boosts the gas-liquid two-phase flow mixed by the ozone gas injection device 4, and the gas-liquid two that is pressurized by the high-pressure pump 5 The microbubble generation device 6 that guides the phase flow through the pipe 17 and ejects from a plurality of small holes to generate microbubbles, and the microbubbles generated by the microbubble generation device 6 to the upstream side of the partition plate 2 a of the water treatment tank 1. A pipe 18 for guiding is installed.

ここで、オゾンガス注入装置4には、エゼクタ方式のもの、散気管方式のもの、直接混合する気液混合方式のものが適用され、高圧ポンプ5は、渦流ポンプが二相流吐き出し性能に優れるので望ましいが、一般のポンプも使用可能である。   Here, the ozone gas injection device 4 is of an ejector type, a diffuser type, or a gas-liquid mixing type that directly mixes, and the high pressure pump 5 has a vortex pump excellent in two-phase flow discharge performance. Although desirable, common pumps can also be used.

仕切板2aと仕切板2cとの間の仕切板2bの上部には、スカム排出口10が設置され、スカム排出口10の中央部には排出管20が設けられ、排出管20にはスカム排出弁11が取り付けられている。スカム排出口10には、図2に示すように、らせん状のガイド30が設けられている。スカム排出弁11は配管22により排水ピット24に接続されている。   A scum discharge port 10 is installed in the upper part of the partition plate 2b between the partition plate 2a and the partition plate 2c, a discharge pipe 20 is provided in the center of the scum discharge port 10, and a scum discharge is provided in the discharge pipe 20. A valve 11 is attached. As shown in FIG. 2, the scum discharge port 10 is provided with a spiral guide 30. The scum discharge valve 11 is connected to a drain pit 24 by a pipe 22.

又、仕切板2aと仕切板2cとの間には、スカム排出口10より高い位置にフロート式の水位計13aが設置されており、水位がスカム排出口位置13bに達したかどうかを検出している。   A float type water level gauge 13a is installed between the partition plate 2a and the partition plate 2c at a position higher than the scum discharge port 10, and detects whether the water level has reached the scum discharge port position 13b. ing.

水処理槽1の上部は、被処理水と反応しなかったオゾンを回収するための屋根(図示せず)が設けられており、集められた排オゾンは、排オゾン配管7を介して活性炭層8に導入され、活性炭で吸収させた後、排気ファン9により大気放出される。   The upper part of the water treatment tank 1 is provided with a roof (not shown) for collecting ozone that has not reacted with the water to be treated, and the collected exhaust ozone passes through an exhaust ozone pipe 7 and is an activated carbon layer. 8 is absorbed by activated carbon and then released into the atmosphere by an exhaust fan 9.

水処理槽1で処理された処理水は、再生水弁12,配管23を介して再生水として貯留槽25に貯留される。   The treated water treated in the water treatment tank 1 is stored in the storage tank 25 as reclaimed water via the reclaimed water valve 12 and the pipe 23.

制御装置14には水位計13aの信号がフィードバックされ、高圧ポンプ5のインバータを駆動するための信号、スカム排出弁11を開閉制御するための信号、再生水弁12を開閉制御するための信号が出力するようになっている。   A signal from the water level gauge 13a is fed back to the control device 14, and a signal for driving the inverter of the high-pressure pump 5, a signal for controlling the opening and closing of the scum discharge valve 11, and a signal for controlling the opening and closing of the regenerative water valve 12 are output. It is supposed to be.

下水処理設備から被処理水が水処理槽1に注入され、オゾン発生装置3,高圧ポンプ5が駆動されると、水処理槽1の下部から一部抽水された被処理水に、オゾンガス注入装置4でオゾン発生装置3からのオゾンガスが混合されて気液二相流となって、高圧ポンプ5に吸い込まれ、昇圧された後、微細気泡生成装置6に流入する。   When water to be treated is injected into the water treatment tank 1 from the sewage treatment facility and the ozone generator 3 and the high pressure pump 5 are driven, an ozone gas injection device is added to the water to be partially extracted from the lower part of the water treatment tank 1. 4, the ozone gas from the ozone generator 3 is mixed to form a gas-liquid two-phase flow, which is sucked into the high-pressure pump 5 and pressurized, and then flows into the fine bubble generating device 6.

高圧ポンプ5から吐き出されたオゾンガスが混入した気液二相流は、昇圧されてオゾンガスの一部が液中に溶解しながら、微細気泡生成装置6に達し、微細気泡生成装置6に設けられた複数の小さな孔から流出する。この小さな孔部を通過する時に圧力損失が生じ、流速が増加するので、ベルヌーイの定理から分かるように、圧力が急激に低下して減圧されるので、加圧溶解していた気泡が微細気泡、いわゆるマイクロバブルとなって、水処理槽1内に吹き込まれる。なお、下流側では流路面積が増加するため、圧力は回復するが、急激な流路面積の変化によって圧力が不安定となり、気泡はさらに微細気泡へと崩壊する。   The gas-liquid two-phase flow mixed with the ozone gas discharged from the high pressure pump 5 reaches the fine bubble generating device 6 while being partially pressurized and dissolved in the liquid, and is provided in the fine bubble generating device 6. Out of several small holes. When passing through this small hole, pressure loss occurs and the flow rate increases, so as can be seen from Bernoulli's theorem, the pressure rapidly decreases and the pressure is reduced. The so-called microbubbles are blown into the water treatment tank 1. In addition, since the flow path area increases on the downstream side, the pressure recovers, but the pressure becomes unstable due to a sudden change in the flow path area, and the bubbles further collapse into fine bubbles.

このようにして生成された微細気泡は、水処理槽1の壁面と仕切板2aとの間、仕切板2aと仕切板2bとの間、仕切板2bと仕切板2cとの間を順次流れる間に、被処理水に含まれる濁質に付着して水面へ浮上し、集積した濁質、すなわちスカムとして仕切板2bの上部に溜まる。   While the fine bubbles generated in this manner sequentially flow between the wall surface of the water treatment tank 1 and the partition plate 2a, between the partition plate 2a and the partition plate 2b, and between the partition plate 2b and the partition plate 2c. In addition, it adheres to the turbidity contained in the water to be treated and floats on the water surface, and accumulates on the upper part of the partition plate 2b as accumulated turbidity, that is, scum.

この溜まったスカムを定期的に除去する処理手順を図3に示す。ステップ100で、制御装置14は、再生水弁12を閉じる。再生水弁12を閉じることによって、水処理槽1内の水位が上昇する。   A processing procedure for periodically removing the accumulated scum is shown in FIG. In step 100, the control device 14 closes the regeneration water valve 12. By closing the regeneration water valve 12, the water level in the water treatment tank 1 rises.

ステップ101で、水位計13aの信号をフィードバックした制御装置14は、水位がスカム排出口10より高いかどうかを判断する。水位がスカム排出口10より高くなると、ステップ102で、制御装置14は、スカム排出弁11を開き、水処理槽1内の被処理水をスカム排出口10から排水させる。スカム排出口10には、らせん状のガイド30が設けられているので、排水により渦流が発生して水処理槽1内の壁面及びスカム排出口付近に付着したスカムを渦流のエネルギーにより効果的に除去することができる。   In step 101, the control device 14 that has fed back the signal from the water level gauge 13 a determines whether or not the water level is higher than the scum outlet 10. When the water level becomes higher than the scum discharge port 10, in step 102, the control device 14 opens the scum discharge valve 11 and drains the water to be treated in the water treatment tank 1 from the scum discharge port 10. Since the spiral guide 30 is provided in the scum discharge port 10, the scum adhering to the wall surface in the water treatment tank 1 and in the vicinity of the scum discharge port is effectively generated by the energy of the vortex flow due to the drainage. Can be removed.

制御装置14は、ステップ103で、スカム排出時間を計測し、設定された時間が経過すると、ステップ104で、再生水弁12を開いて水位を下げ、ステップ105で、スカム排出弁を閉じる。   The controller 14 measures the scum discharge time in Step 103, and when the set time has elapsed, in Step 104, the regeneration water valve 12 is opened to lower the water level, and in Step 105, the scum discharge valve is closed.

このように、本実施例によれば、スカム排出口の内側にらせん状の水流ガイドを設けているので、排水時に渦流を発生させて、水処理槽壁面及びスカム排出口付近に付着するスカムを効果的に除去することができる。   As described above, according to the present embodiment, the spiral water flow guide is provided inside the scum discharge port, so that a vortex flow is generated during drainage, and the scum adhering to the water treatment tank wall surface and the vicinity of the scum discharge port is removed. It can be effectively removed.

1 水処理槽
2 仕切板
3 オゾン発生装置
4 オゾンガス注入装置
5 高圧ポンプ
6 微細気泡生成装置
10 スカム排出口
11 スカム排出弁
12 再生水弁
13 水位計
14 制御装置
DESCRIPTION OF SYMBOLS 1 Water treatment tank 2 Partition plate 3 Ozone generator 4 Ozone gas injection device 5 High pressure pump 6 Fine bubble production | generation apparatus 10 Scum discharge port 11 Scum discharge valve 12 Reclaimed water valve 13 Water level meter 14 Control device

Claims (2)

被処理水を流入する水処理槽と、該水処理槽内に設置された複数の仕切板と、前記水処理槽内の被処理水の一部を抽水してオゾンガスと混合するオゾンガス注入装置と、該オゾンガス注入装置により混合された気液二相流を昇圧する高圧ポンプと、該高圧ポンプで昇圧された気液二相流を小さな複数の孔から噴出してマイクロバブルを発生する微細気泡生成装置と、該微細気泡生成装置で生成されたマイクロバブルを前記水処理槽内を流下させる際に発生するスカムを除去するための内側にらせん状の水流ガイドを設けたスカム排出口を備えたスカム機構を具備したマイクロバブル下水再生装置。   A water treatment tank into which the water to be treated flows, a plurality of partition plates installed in the water treatment tank, an ozone gas injection device for extracting a part of the water to be treated in the water treatment tank and mixing it with ozone gas; , A high-pressure pump that boosts the gas-liquid two-phase flow mixed by the ozone gas injection device, and microbubble generation that generates microbubbles by ejecting the gas-liquid two-phase flow pressurized by the high-pressure pump from a plurality of small holes And a scum having a scum discharge port provided with a spiral water flow guide on the inside for removing scum generated when the microbubbles generated by the fine bubble generating device flow down in the water treatment tank A microbubble sewage recycling device equipped with a mechanism. 前記水処理槽が、再生水を排出する配管を開閉制御する再生水弁と、水位を検出する水位計と、前記スカム排出口に接続される排出管を開閉制御するスカム排出弁を具備し、前記スカムを除去する時には、制御装置は、前記再生水弁を閉じ、前記水位計により計測された水位が前記スカム排出口より高いと判断されたときに、前記スカム排出弁を設定時間開状態に制御する請求項1に記載のスカム機構を具備したマイクロバブル下水再生装置。   The water treatment tank includes a reclaimed water valve for opening and closing a pipe for discharging reclaimed water, a water level meter for detecting a water level, and a scum discharge valve for opening and closing a discharge pipe connected to the scum discharge port, When removing the water, the control device closes the regeneration water valve and controls the scum discharge valve to be in an open state for a set time when it is determined that the water level measured by the water level gauge is higher than the scum discharge port. A microbubble sewage recycling apparatus comprising the scum mechanism according to Item 1.
JP2010088251A 2010-04-07 2010-04-07 Microbubble sewage regenerating apparatus having scum mechanism Pending JP2011218266A (en)

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JP2014213215A (en) * 2013-04-22 2014-11-17 中村物産有限会社 Sterilization apparatus and sterilization method
JP2016150314A (en) * 2015-02-18 2016-08-22 千代田化工建設株式会社 Water treatment method
JP2017131893A (en) * 2017-05-15 2017-08-03 住友精密工業株式会社 Method and system for treating high-concentration organic wastewater
CN111760533A (en) * 2020-07-08 2020-10-13 刘帆 Ultrasonic micro-airflow biomass production line system

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2014094322A (en) * 2012-11-07 2014-05-22 Sumitomo Precision Prod Co Ltd Multistage organic waste water treatment system
JP2014213215A (en) * 2013-04-22 2014-11-17 中村物産有限会社 Sterilization apparatus and sterilization method
JP5584869B1 (en) * 2013-12-06 2014-09-10 中村物産有限会社 Sterilization treatment apparatus and sterilization treatment method
JP2015110205A (en) * 2013-12-06 2015-06-18 中村物産有限会社 Sterilization device and sterilization method
JP2016150314A (en) * 2015-02-18 2016-08-22 千代田化工建設株式会社 Water treatment method
JP2017131893A (en) * 2017-05-15 2017-08-03 住友精密工業株式会社 Method and system for treating high-concentration organic wastewater
CN111760533A (en) * 2020-07-08 2020-10-13 刘帆 Ultrasonic micro-airflow biomass production line system
CN111760533B (en) * 2020-07-08 2021-10-29 刘帆 Ultrasonic micro-airflow biomass production line system

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