JPH09220591A - Waste water treatment apparatus - Google Patents

Waste water treatment apparatus

Info

Publication number
JPH09220591A
JPH09220591A JP2881996A JP2881996A JPH09220591A JP H09220591 A JPH09220591 A JP H09220591A JP 2881996 A JP2881996 A JP 2881996A JP 2881996 A JP2881996 A JP 2881996A JP H09220591 A JPH09220591 A JP H09220591A
Authority
JP
Japan
Prior art keywords
scum
reaction tank
wastewater treatment
skimmer
treatment device
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.)
Pending
Application number
JP2881996A
Other languages
Japanese (ja)
Inventor
Taku Menju
卓 毛受
Kazuo Shibazaki
和夫 柴崎
Shigeru Kobayashi
茂 小林
Nobuyuki Ashikaga
伸行 足利
Hiroshi Tamura
博 田村
Ichiro Yamanashi
伊知郎 山梨
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.)
Toshiba Corp
Original Assignee
Toshiba Corp
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 Toshiba Corp filed Critical Toshiba Corp
Priority to JP2881996A priority Critical patent/JPH09220591A/en
Publication of JPH09220591A publication Critical patent/JPH09220591A/en
Pending legal-status Critical Current

Links

Classifications

    • Y02W10/12

Abstract

PROBLEM TO BE SOLVED: To provide a waste water treatment apparatus capable of continuing the good treatment even of waste water generating scum while holding the amt. of bacteria in a reaction tank and preventing generated scum from flowing out along with treated water to facilitate the discarding of scum. SOLUTION: A waste water treatent apparatus biologically purifying waste water in an unaerobic reaction tank 2 is constituted of the gas-solid-liquid separation device 6 arranged to the upper part of the reaction tank 2 and opened to the liquid phase part of the reaction tank at both ends thereof, the skimmer 9 arranged in the vicinity of the liquid surface of the upper part of the reaction tank 2 and a barrier plate 10 arranged in order to limit the generation place of sucm formed in the reaction tank 2 on the liquid surface. By generating the scum formed in the reaction tank 2 at a specific place by the barrier plate 10 to scrape off the scum by the skimmer 9 without pushing out the same to a flooding part, scum can be prevented from flowing out along with treated water to be easily discarded and treated water good in quality can be obtained.

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】本発明は、下水及び産業廃水
などの廃水を嫌気性微生物によって処理する廃水処理装
置に関する。
TECHNICAL FIELD The present invention relates to a wastewater treatment apparatus for treating wastewater such as sewage and industrial wastewater with anaerobic microorganisms.

【0002】[0002]

【従来の技術】下水,産業廃水,汚泥等の廃水中の有機
物を処理する方法の一つに、嫌気性処理がある。嫌気性
処理は有機物が高濃度に含まれる廃水に適用でき、また
汚泥発生量が少ないことや、発酵ガスがメタンガスを主
成分としているためエネルギが回収できるなどの利点が
ある。
BACKGROUND ART Anaerobic treatment is one of the methods for treating organic matter in wastewater such as sewage, industrial wastewater, and sludge. Anaerobic treatment has advantages that it can be applied to wastewater containing a high concentration of organic substances, that the amount of sludge generated is small, and that the fermentation gas is mainly composed of methane gas, so that energy can be recovered.

【0003】図8は一般的に広く普及している汚泥床型
嫌気性廃水処理装置(UASB型)の構成図である。同
図に示すように、廃水は原水ポンプ1によって反応槽2
の下方から槽内に供給される。反応槽2内には沈降性の
菌体が層となっており、廃水中の有機物がこの嫌気性微
生物層3を上昇しながら分解される。分解された有機物
はメタンガスまたは炭酸ガスとなって上澄液層4を上昇
する。反応槽2内の菌体は、発酵ガスが付着したり発酵
ガスの上昇による同伴流によって反応槽2液相中を上昇
するが、反応槽2液相上部に設けた気固液分離装置6な
どの気液界面で発酵ガスと分離し、嫌気性微生物層3へ
と上澄液層4を沈降する。この気固液分離装置6の働き
により反応槽2内の菌体量は保持され良好な処理が継続
できる。
FIG. 8 is a block diagram of a sludge bed type anaerobic wastewater treatment device (UASB type) which is generally widely used. As shown in the figure, the wastewater is fed to the reaction tank 2 by the raw water pump 1.
Is supplied into the tank from below. The reaction tank 2 has a layer of sedimentable cells, and organic substances in the wastewater are decomposed while rising in the anaerobic microorganism layer 3. The decomposed organic matter becomes methane gas or carbon dioxide gas and rises in the supernatant liquid layer 4. The bacteria in the reaction tank 2 rise in the liquid phase of the reaction tank 2 due to the accompanying flow due to the attachment of the fermentation gas or the rise of the fermentation gas, but the gas-solid separation device 6 provided above the liquid phase of the reaction tank 2 etc. Is separated from the fermentation gas at the gas-liquid interface, and the supernatant liquid layer 4 is settled into the anaerobic microorganism layer 3. Due to the function of the gas-solid separation device 6, the amount of the bacterial cells in the reaction tank 2 is maintained, and good processing can be continued.

【0004】脂質やタンパク質などの生物難分解性有機
物を多量に含む廃水を処理する場合、スカムが発生し反
応槽2内の気液界面に蓄積する。スカムは保持力のある
微細な泡が集積したものである。スカムが反応槽2内の
気液界面に蓄積すると、発酵ガスと共に上澄液層4を上
昇してきた菌体はスカムに付着してしまい、嫌気性微生
物層3へ沈降せず蓄積していく。また、蓄積量の増加に
よりスカムは処理水と共に反応槽溢流部5から付着した
菌体を伴って流出するため、反応槽2内の菌体保持量が
減少してゆく。このように菌体の減少が進むと、反応槽
2は充分な処理ができなくなるという問題が生じる。こ
のような問題を解決するために反応槽内にスキマーまた
はシャワーを設置した廃水処理装置が用いられている。
[0004] When treating wastewater containing a large amount of biodegradable organic substances such as lipids and proteins, scum is generated and accumulated at the gas-liquid interface in the reaction tank 2. The scum is a collection of fine bubbles having a holding power. When scum accumulates on the gas-liquid interface in the reaction tank 2, the bacterial cells that have risen in the supernatant layer 4 together with the fermentation gas adhere to the scum and accumulate in the anaerobic microorganism layer 3 without settling. Further, since the accumulated amount of scum flows out together with the treated water from the reaction tank overflow portion 5 along with the bacterial cells attached thereto, the bacterial cell retention amount in the reaction tank 2 decreases. As the number of bacterial cells decreases, the reaction tank 2 cannot be sufficiently treated. In order to solve such a problem, a wastewater treatment device having a skimmer or a shower installed in a reaction tank is used.

【0005】図9はスキマーを設置した円筒形反応槽を
備えた従来の廃水処理装置の概略図である。同図に示す
ように、反応槽2の液面を掻くようにスキマー9を設置
し、このスキマー9を反応槽2上部に取り付けたモータ
8により回転させる。スカムポケット7を反応槽2の液
面よりわずか高くに開口するように設置し、スキマー9
によって掻き寄せられてきたスカムのみをスカムポケッ
ト7に掻き落す。スカムポケット7に掻き落とされたス
カムは、下部から反応槽2外部へ取り出され廃棄され
る。しかし、この方法ではスキマー9はスカムの一部を
溢流部5へ掻き落しているので、処理水質の低下の原因
となっていた。また、スカムは脱水性が非常に悪く、脱
水機で容易に減容することができず、廃棄が困難であっ
た。
FIG. 9 is a schematic view of a conventional wastewater treatment apparatus equipped with a cylindrical reaction tank in which a skimmer is installed. As shown in the figure, a skimmer 9 is installed so as to scratch the liquid surface of the reaction tank 2, and the skimmer 9 is rotated by a motor 8 attached to the upper part of the reaction tank 2. The scum pocket 7 is installed so as to open slightly higher than the liquid surface of the reaction tank 2, and the skimmer 9
Only the scum that has been scraped by is scraped off into the scum pocket 7. The scum scraped off in the scum pocket 7 is taken out of the reaction tank 2 from the lower part and discarded. However, in this method, the skimmer 9 scrapes off a part of the scum to the overflow portion 5, which causes the deterioration of the treated water quality. Further, the scum has a very poor dehydration property and cannot be easily reduced in volume by a dehydrator, so that it is difficult to dispose of it.

【0006】図10はシャワーを設置した円筒形反応槽
を備えた従来の廃水処理装置の概略図である。同図に示
すように、シャワーノズル12を反応槽2の天井に設
け、清水を噴出させることによってスカムを破壊もしく
はスカムに衝撃を与えることにより付着した菌体を分離
する。しかし、この方法ではスカムの発生量が大量の場
合、必要となる清水も多量となるため費用がかかり過ぎ
るという問題がある。清水を用いるのは懸濁固形物等が
シャワー水に混入した場合、ノズルの閉塞を引き起こす
ことを回避するためである。
FIG. 10 is a schematic view of a conventional wastewater treatment apparatus equipped with a cylindrical reaction tank equipped with a shower. As shown in the figure, a shower nozzle 12 is provided on the ceiling of the reaction tank 2, and fresh water is jetted to destroy the scum or to give an impact to the scum to separate the adhered bacterial cells. However, this method has a problem in that when the amount of scum generated is large, the amount of fresh water required is also large and therefore it is too expensive. The reason for using clear water is to avoid clogging of the nozzle when suspended solids and the like are mixed in the shower water.

【0007】[0007]

【発明が解決しようとする課題】本発明の請求項1乃至
請求項6は、上記事情に鑑みてなされたもので、その目
的はスカムの処理水への流出を軽減し、発酵ガスもしく
はスカムと菌体との分離性を向上させ、スカムが発生す
る廃水でも反応槽内に菌体量を保持し良好な処理を継続
できると同時に、発生したスカムを減容または分離し廃
棄を容易にする廃水処理装置を提供することにある。
SUMMARY OF THE INVENTION Claims 1 to 6 of the present invention have been made in view of the above circumstances, and the purpose thereof is to reduce the outflow of scum into the treated water, and to use fermentation gas or scum. Wastewater that improves separability from bacterial cells and keeps the amount of bacterial cells in the reaction tank even in wastewater where scum is generated so that good processing can be continued, and at the same time reduces the volume of scum generated and separates it to facilitate disposal. It is to provide a processing device.

【0008】[0008]

【課題を解決するための手段】上記目的を達成するため
に、本発明の請求項1は、廃水を嫌気性反応槽で生物学
的に浄化処理する廃水処理装置において、前記反応槽の
上部に設置され、両端が反応槽液相部に開口している気
固液分離装置と、前記反応槽上部の液面近傍に設置され
たスキマーと、前記反応槽中で生成したスカムの液面で
の発生場所を限定させるために設置された邪魔板とから
構成されることを特徴とする。
In order to achieve the above object, the first aspect of the present invention is to provide a wastewater treatment apparatus for biologically purifying wastewater in an anaerobic reaction tank. Installed gas-solid separation device with both ends open to the liquid phase part of the reaction tank, a skimmer installed near the liquid surface above the reaction tank, and a liquid level of scum generated in the reaction tank. It is characterized by being configured with a baffle installed to limit the place of occurrence.

【0009】本発明の請求項2は、廃水を嫌気性反応槽
で生物学的に浄化処理する廃水処理装置において、前記
反応槽の上部に設置され、両端が反応槽液相部に開口し
ている気固液分離装置と、前記反応槽気相部に設置した
噴水装置と、前記反応槽で浄化した廃水の一部を噴水に
利用するために浄化した廃水の懸濁固形物等を取り除く
浄化装置とから構成されることを特徴とする。
According to a second aspect of the present invention, in a wastewater treatment apparatus for biologically purifying wastewater in an anaerobic reaction tank, the wastewater treatment apparatus is installed above the reaction tank, and both ends are opened to a liquid phase portion of the reaction tank. Gas-liquid separation device, a water spouting device installed in the gas phase of the reaction tank, and purification for removing suspended solids of the waste water purified to use part of the waste water purified in the reaction tank for fountain And a device.

【0010】本発明の請求項3は、請求項1記載の廃水
処理装置において、前記反応槽でスキマーにより掻き取
ったスカムを貯め、減圧装置により前記スカムを消泡さ
せる槽を設けることを特徴とする。
According to a third aspect of the present invention, in the wastewater treatment apparatus according to the first aspect, there is provided a tank for storing scum scraped by a skimmer in the reaction tank and defoaming the scum by a decompression device. To do.

【0011】本発明の請求項4、請求項1記載の廃水処
理装置において、前記反応槽でスキマーにより掻き取っ
たスカムを貯め、消泡剤により前記スカムを消泡させる
槽を設けることを特徴とする。
In the wastewater treatment apparatus according to claims 4 and 1 of the present invention, a scum scraped by a skimmer is stored in the reaction tank, and a tank for defoaming the scum with a defoaming agent is provided. To do.

【0012】本発明の請求項5は、請求項1記載の廃水
処理装置において、前記反応槽でスキマーにより掻き取
ったスカムを貯め、加温することにより前記スカムを消
泡させる槽を設けることを特徴とする。
According to a fifth aspect of the present invention, in the wastewater treatment apparatus according to the first aspect, there is provided a tank for storing scum scraped by a skimmer in the reaction tank and heating the scum to defoam the scum. Characterize.

【0013】本発明の請求項6は、請求項1記載の廃水
処理装置において、前記反応槽でスキマーにより掻き取
ったスカムを貯め、脂質分解に適した微生物によって前
記スカムを処理する槽を設けることを特徴とする。
According to a sixth aspect of the present invention, in the wastewater treatment apparatus according to the first aspect, there is provided a tank for storing scum scraped by a skimmer in the reaction tank and treating the scum with a microorganism suitable for lipid decomposition. Is characterized by.

【0014】[0014]

【発明の実施の形態】以下、本発明の実施の形態を図を
参照して説明する。図1は本発明の嫌気性水処理装置の
第1実施例(請求項1対応)の構成図である。
Embodiments of the present invention will be described below with reference to the drawings. FIG. 1 is a configuration diagram of a first embodiment (corresponding to claim 1) of the anaerobic water treatment apparatus of the present invention.

【0015】同図において、嫌気性水処理装置の主たる
構成は反応槽2であり、この反応槽2は廃水中の有機物
を分解しバイオガスを発生する嫌気性微生物層3と上澄
液層4とからなる。廃水は原水ポンプ1により反応槽2
の下部から流入し、嫌気性微生物層3で浄化された後、
上澄液層4を経て溢流部5から反応槽2外へ流出する。
廃水中の有機物は嫌気性微生物によって主にメタン及び
炭酸ガスからなるバイオガスに分解され反応槽2内を上
昇し、反応槽2上部から回収される。
In the figure, the main structure of the anaerobic water treatment apparatus is a reaction tank 2, and this reaction tank 2 decomposes organic substances in waste water to generate biogas, and an anaerobic microbial layer 3 and a supernatant layer 4. Consists of. Waste water is sent from the raw water pump 1 to the reaction tank 2
After flowing in from the bottom of the plant and being purified by the anaerobic microbial layer 3,
After passing through the supernatant layer 4, the overflow portion 5 flows out of the reaction tank 2.
Organic substances in the wastewater are decomposed into biogas mainly composed of methane and carbon dioxide by anaerobic microorganisms, rise in the reaction tank 2, and are recovered from the upper portion of the reaction tank 2.

【0016】反応槽2内部の上部には気固液分離装置6
が設置されており、バイオガスの上昇に伴い上澄液層4
を上昇した嫌気性微生物の一部を気固液分離装置6に衝
突させることにより嫌気性微生物層3へと沈降させる。
A gas-solid separation device 6 is provided in the upper part of the reaction tank 2.
Is installed, and as the biogas rises, the supernatant layer 4
The part of the anaerobic microorganisms having risen in temperature is caused to collide with the gas-solid separation device 6 to settle into the anaerobic microorganism layer 3.

【0017】廃水中に脂質やタンパク質を多く含む場合
には、バイオガスの気泡が破裂しにくくなり液面にスカ
ムを形成する。このスカムを除去するため反応槽2上部
水面近傍にはスカムポケット7及び反応槽2上部に取り
付けたモータ8によって回転するスキマー9が設置され
ている。スキマー9の回転により水面のスカムはスカム
ポケット7に掻き落とされる。また、スカムがスキマー
9で掻き取ることができる範囲に発生し留まるようにス
キマー9と溢流部5の間にはスカム邪魔板10が設置さ
れている。
When the wastewater contains a large amount of lipids and proteins, the bubbles of biogas are less likely to burst and scum is formed on the liquid surface. In order to remove this scum, a scum pocket 7 and a skimmer 9 which is rotated by a motor 8 attached to the upper part of the reaction tank 2 are installed near the water surface above the reaction tank 2. By the rotation of the skimmer 9, the scum on the water surface is scraped off by the scum pocket 7. Further, a scum baffle plate 10 is installed between the skimmer 9 and the overflow portion 5 so that the scum is generated and stays in a range where it can be scraped by the skimmer 9.

【0018】図2(a)及び(b)は、それぞれ図1の
反応槽2の液面平面図及び反応槽2上部の拡大図図であ
る。同図に示すように、気固液分離装置6の形状を、ス
カムがスカム邪魔板10内に発生するようにし、発生し
たスカムを掻き取ることにより溢流部5からの処理水質
を向上させるようにしたものである。
FIGS. 2A and 2B are a plan view of the liquid surface of the reaction tank 2 and an enlarged view of the upper portion of the reaction tank 2 in FIG. 1, respectively. As shown in the figure, the gas-solid separation device 6 is shaped so that scum is generated in the scum baffle plate 10 and the generated scum is scraped off to improve the quality of treated water from the overflow portion 5. It is the one.

【0019】図3は本発明の嫌気性水処理装置の第2実
施例(請求項2対応)の構成図であり、図1に示す第1
実施例と同一部分には同一の符号を付してその詳細な説
明は省略する。
FIG. 3 is a block diagram of a second embodiment (corresponding to claim 2) of the anaerobic water treatment apparatus of the present invention, which is the first shown in FIG.
The same parts as those in the embodiment are designated by the same reference numerals, and detailed description thereof will be omitted.

【0020】同図に示すように、本実施例は、反応槽2
で浄化した廃水の一部を清澄ろ過槽11によって清澄に
し、これをシャワー水としてシャワーノズル12から反
応槽2内に発生したスカムに噴射し、スカムを破壊また
は衝撃を与える。スカムは蓄積して層状になると嫌気性
微生物の付着など処理上の障害を引き起こすため、シャ
ワーによる粉砕が効果的である。また、シャワーに清水
(通常、水道水を用いる)を使わず浄化した廃水の一部
を利用するとコスト低減につながる。
As shown in the figure, in this embodiment, the reaction tank 2
A part of the waste water purified in (1) is clarified by the clarification filtration tank 11, and this is sprayed as shower water from the shower nozzle 12 to the scum generated in the reaction tank 2 to destroy or impact the scum. If scum accumulates and becomes layered, it causes processing obstacles such as adhesion of anaerobic microorganisms, so crushing with a shower is effective. In addition, if a portion of the wastewater purified without using fresh water (usually tap water) is used for the shower, it will lead to cost reduction.

【0021】図4は本発明の嫌気性水処理装置の第3実
施例(請求項3対応)の構成図であり、図1に示す第1
実施例と同一部分には同一符号を付してその詳細な説明
は省略する。
FIG. 4 is a block diagram of a third embodiment (corresponding to claim 3) of the anaerobic water treatment apparatus of the present invention, which is the first shown in FIG.
The same parts as those in the embodiment are designated by the same reference numerals, and detailed description thereof will be omitted.

【0022】同図に示すように、本実施例では上記第1
実施例にさらにスカム槽13を追加設置したものであ
る。スカムポケット7から掻き落としたスカムをスカム
槽13に受け、スカム槽13内を真空ポンプ14で減圧
することによりスカムを減容し廃棄処分を容易にするこ
とができる。スカムは微細な気泡の集合物であるため、
消泡すると減容される。また、気圧を低下すると気泡は
膨脹し膜を維持できなくなり破泡するのでスカムは減容
される。
As shown in the figure, in this embodiment, the first
The scum tank 13 is additionally installed in the embodiment. The scum scraped from the scum pocket 7 is received by the scum tank 13, and the inside of the scum tank 13 is decompressed by the vacuum pump 14, so that the scum volume can be reduced and disposal can be facilitated. Since scum is a collection of fine bubbles,
When defoaming, the volume is reduced. Further, when the atmospheric pressure is lowered, the bubbles expand and cannot maintain the film, and the bubbles are broken, so that the scum volume is reduced.

【0023】図5は本発明の嫌気性水処理装置の第4実
施例(請求項4対応)の構成図であり、図4に示す第3
実施例と同一部分には同一符号を付してその詳細な説明
は省略する。
FIG. 5 is a constitutional view of a fourth embodiment (corresponding to claim 4) of the anaerobic water treatment apparatus of the present invention, and the third embodiment shown in FIG.
The same parts as those in the embodiment are designated by the same reference numerals, and detailed description thereof will be omitted.

【0024】同図に示すように、上記第4実施例では真
空ポンプ14により減圧してスカムを減容したが、本実
施例ではスカム槽13の上部に消泡剤ノズル15を設置
したものである。本実施例によると、スカムポケット7
から掻き落としたスカムを収納したスカム槽13に、消
泡剤ノズル15から消泡剤を噴霧することによりスカム
を破泡するので減容される。
As shown in the figure, in the fourth embodiment, the vacuum pump 14 is used to reduce the pressure to reduce the scum volume, but in the present embodiment, the defoaming agent nozzle 15 is installed above the scum tank 13. is there. According to this embodiment, the scum pocket 7
By spraying the defoaming agent from the defoaming agent nozzle 15 into the scum tank 13 containing the scum scraped off from the scum, the scum is broken and the volume is reduced.

【0025】図6は本発明の嫌気性水処理装置の第5実
施例(請求項5対応)の構成図であり、図4に示す第3
実施例と同一部分には同一符号を付してその詳細な説明
は省略する。
FIG. 6 is a constitutional view of a fifth embodiment (corresponding to claim 5) of the anaerobic water treatment apparatus of the present invention, and shows a third embodiment shown in FIG.
The same parts as those in the embodiment are designated by the same reference numerals, and detailed description thereof will be omitted.

【0026】同図に示すように、上記第3実施例では減
圧によりスカムを減容したが、本実施例ではスカム槽1
3にスチームを吹き込むスチームライン16を設置した
ものである。本実施例によると、スカム槽13にスチー
ムライン16からスチームを吹き込みスカムを加温し膨
張させることにより破泡し、減容する。
As shown in the figure, in the third embodiment, the scum volume was reduced by reducing the pressure, but in this embodiment, the scum tank 1 is used.
The steam line 16 for injecting steam into the 3 is installed. According to the present embodiment, steam is blown into the scum tank 13 from the steam line 16 to heat and expand the scum to break the bubbles and reduce the volume.

【0027】図7は本発明の嫌気性水処理装置の第6実
施例(請求項6対応)の構成図であり、図4に示す第3
実施例と同一部分には同一符号を付してその詳細な説明
は省略する。
FIG. 7 is a constitutional view of a sixth embodiment (corresponding to claim 6) of the anaerobic water treatment apparatus of the present invention, and the third embodiment shown in FIG.
The same parts as those in the embodiment are designated by the same reference numerals, and detailed description thereof will be omitted.

【0028】同図に示すように、上記第3実施例ではス
カムの減容を機械的操作によって行うが、本実施例では
スカム分解に適した微生物をスカム槽13内に保持し、
このスカム分解菌層17によりスカムの分解除去を行い
減容するものである。
As shown in the figure, in the third embodiment, the volume of scum is reduced by mechanical operation. In this embodiment, microorganisms suitable for scum decomposition are held in the scum tank 13,
The scum-decomposing bacteria layer 17 decomposes and removes scum to reduce the volume.

【0029】[0029]

【発明の効果】以上説明したように、本発明によれば下
記に示す効果を奏する。すなわち、本発明の請求項1に
よれば、反応槽内で生成するスカムを邪魔板によって特
定の場所に発生させ、これを溢流部に押し出さずにスキ
マーで掻き取ることによりスカムが処理水と共に流出す
ることを防止し廃棄を容易にできるため、良好な処理水
質が得られる。
As described above, the present invention has the following effects. That is, according to claim 1 of the present invention, scum generated in the reaction tank is generated at a specific location by the baffle plate, and the scum is scraped together with the treated water by scraping off with a skimmer without pushing it out to the overflow portion. Good treated water quality can be obtained because it can be prevented from flowing out and easily discarded.

【0030】本発明の請求項2によれば、スカムと菌体
の分離を処理するために噴出するシャワー水は、反応槽
で生成した廃水の一部を浄化装置で懸濁固形物等を除去
して利用することできるので、シャワー用の液は新たに
清水を用いるのではなく浄化した廃水を清澄にして使用
するため、清水のコストや放流水の増加によるコスト増
加が軽減される。
According to the second aspect of the present invention, the shower water jetted for treating the separation of scum and bacterial cells removes suspended solids and the like from a part of the waste water produced in the reaction tank by a purifying device. Since the liquid for the shower is used by clarifying the purified waste water instead of newly using the fresh water, the cost of the fresh water and the increase of the cost due to the increase of the discharged water can be reduced.

【0031】本発明の請求項3によれば、反応槽上部で
スキマーにより掻き取ったスカムを貯留し減圧ポンプで
気相部を減圧し、スカムを減容させ廃棄を容易にするこ
とができる。
According to the third aspect of the present invention, the scum scraped by the skimmer is stored in the upper part of the reaction tank, and the gas phase part is depressurized by the depressurization pump to reduce the volume of the scum and facilitate disposal.

【0032】本発明の請求項4によれば、反応槽上部で
スキマーにより掻き取ったスカムを消泡剤の添加により
消泡し、スカムを減容させ廃棄を容易にすることができ
る。本発明の請求項5によれば、反応槽上部でスキマー
により掻き取ったスカムを貯留し加温することで、スカ
ムを減容させ廃棄を容易にすることができる。
According to the fourth aspect of the present invention, the scum scraped off by the skimmer in the upper part of the reaction vessel can be defoamed by adding the defoaming agent, and the scum can be reduced in volume to facilitate disposal. According to the fifth aspect of the present invention, by storing the scum scraped by the skimmer in the upper part of the reaction tank and heating the scum, the scum can be reduced in volume and can be easily discarded.

【0033】本発明の請求項6によれば、反応槽上部で
スキマーにより掻き取って貯留したスカムを、スカムの
分解に適した脂質分解菌によって処理することによりス
カムを減容させ廃棄を容易にすることができる。
According to claim 6 of the present invention, the scum scraped by the skimmer in the upper part of the reaction tank and stored therein is treated with a lipid-degrading bacterium suitable for decomposing the scum to reduce the volume of the scum and facilitate disposal. can do.

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

【図1】本発明の廃水処理装置の第1実施例の構成図。FIG. 1 is a configuration diagram of a first embodiment of a wastewater treatment device of the present invention.

【図2】図1の反応槽2上部の部分拡大図。FIG. 2 is a partially enlarged view of the upper part of the reaction tank 2 in FIG.

【図3】本発明の廃水処理装置の第2実施例の構成図。FIG. 3 is a configuration diagram of a second embodiment of the wastewater treatment apparatus of the present invention.

【図4】本発明の廃水処理装置の第3実施例の構成図。FIG. 4 is a configuration diagram of a third embodiment of the wastewater treatment apparatus of the present invention.

【図5】本発明の廃水処理装置の第4実施例の構成図。FIG. 5 is a configuration diagram of a fourth embodiment of a wastewater treatment device of the present invention.

【図6】本発明の廃水処理装置の第5実施例の構成図。FIG. 6 is a configuration diagram of a fifth embodiment of the wastewater treatment device of the present invention.

【図7】本発明の廃水処理装置の第6実施例の構成図。FIG. 7 is a configuration diagram of a sixth embodiment of the wastewater treatment apparatus of the present invention.

【図8】従来の嫌気性水処理装置の構成図。FIG. 8 is a configuration diagram of a conventional anaerobic water treatment device.

【図9】従来の他の嫌気性水処理装置の構成図。FIG. 9 is a configuration diagram of another conventional anaerobic water treatment device.

【図10】従来のさらに他の嫌気性水処理装置の構成
図。
FIG. 10 is a configuration diagram of still another conventional anaerobic water treatment device.

【符号の説明】[Explanation of symbols]

1…原水ポンプ、2…反応槽、3…嫌気性微生物層、4
…上澄液層、5…溢流部、6…気固液分離装置、7…ス
カムポケット、8…モータ、9…スキマー、10…スカ
ム邪魔板、11…清澄ろ過槽、12…シャワーノズル、
13…スカム槽、14…真空ポンプ、15…消泡ノズ
ル、16…スチームライン、17…スカム分離菌槽、1
8…ガストラップ。
1 ... Raw water pump, 2 ... Reaction tank, 3 ... Anaerobic microbial layer, 4
… Supernatant layer, 5… Overflow part, 6… Gas-solid separation device, 7… Scum pocket, 8… Motor, 9… Skimmer, 10… Scum baffle plate, 11… Clarification filtration tank, 12… Shower nozzle,
13 ... scum tank, 14 ... vacuum pump, 15 ... defoaming nozzle, 16 ... steam line, 17 ... scum separation bacterial tank, 1
8 ... Gas trap.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 足利 伸行 東京都府中市東芝町1番地 株式会社東芝 府中工場内 (72)発明者 田村 博 東京都港区芝浦一丁目1番1号 株式会社 東芝本社事務所内 (72)発明者 山梨 伊知郎 東京都府中市東芝町1番地 株式会社東芝 府中工場内 ─────────────────────────────────────────────────── --- Continuation of front page (72) Nobuyuki Ashikaga Nobuyuki Ashikaga 1st Toshiba Town, Fuchu, Tokyo Inside the Toshiba Fuchu factory (72) Inventor Hiroshi Tamura 1-1-1, Shibaura, Minato-ku, Tokyo Toshiba Headquarters Co., Ltd. In the office (72) Inventor Ichiro Yamanashi 1st Toshiba Town, Fuchu City, Tokyo Inside the Fuchu Factory, Toshiba Corporation

Claims (6)

【特許請求の範囲】[Claims] 【請求項1】 廃水を嫌気性反応槽で生物学的に浄化処
理する廃水処理装置において、前記反応槽の上部に設置
され、両端が反応槽液相部に開口している気固液分離装
置と、前記反応槽上部の液面近傍に設置されたスキマー
と、前記反応槽中で生成したスカムの液面での発生場所
を限定させるために設置された邪魔板とから構成される
ことを特徴とする廃水処理装置。
1. A wastewater treatment device for biologically purifying wastewater in an anaerobic reaction tank, the gas-solid separation apparatus being installed above the reaction tank and having both ends open to a liquid phase portion of the reaction tank. And a skimmer installed near the liquid surface above the reaction tank, and a baffle installed to limit the location of scum generated in the reaction tank on the liquid surface. Wastewater treatment equipment.
【請求項2】 廃水を嫌気性反応槽で生物学的に浄化処
理する廃水処理装置において、前記反応槽の上部に設置
され、両端が反応槽液相部に開口している気固液分離装
置と、前記反応槽気相部に設置した噴水装置と、前記反
応槽で浄化した廃水の一部を噴水に利用するために浄化
した廃水の懸濁固形物等を取り除く浄化装置とから構成
されることを特徴とする廃水処理装置。
2. A wastewater treatment device for biologically purifying wastewater in an anaerobic reaction tank, the gas-solid separating apparatus being installed above the reaction tank and having both ends open to a liquid phase portion of the reaction tank. And a fountain device installed in the gas phase portion of the reaction tank, and a purifying device for removing suspended solids of the waste water purified for using a part of the waste water purified in the reaction tank as a fountain. A wastewater treatment device characterized by the above.
【請求項3】 請求項1記載の廃水処理装置において、
前記反応槽でスキマーにより掻き取ったスカムを貯め、
減圧装置により前記スカムを消泡させる槽を設けること
を特徴とする廃水処理装置。
3. The wastewater treatment device according to claim 1,
Store the scum scraped by the skimmer in the reaction tank,
A wastewater treatment device comprising a tank for defoaming the scum by a decompression device.
【請求項4】 請求項1記載の廃水処理装置において、
前記反応槽でスキマーにより掻き取ったスカムを貯め、
消泡剤により前記スカムを消泡させる槽を設けることを
特徴とする廃水処理装置。
4. The wastewater treatment device according to claim 1,
Store the scum scraped by the skimmer in the reaction tank,
A wastewater treatment device comprising a tank for defoaming the scum with an antifoaming agent.
【請求項5】 請求項1記載の廃水処理装置において、
前記反応槽でスキマーにより掻き取ったスカムを貯め、
加温することにより前記スカムを消泡させる槽を設ける
ことを特徴とする廃水処理装置。
5. The wastewater treatment device according to claim 1,
Store the scum scraped by the skimmer in the reaction tank,
A wastewater treatment device comprising a tank for defoaming the scum by heating.
【請求項6】 請求項1記載の廃水処理装置において、
前記反応槽でスキマーにより掻き取ったスカムを貯め、
脂質分解に適した微生物によって前記スカムを処理する
槽を設けることを特徴とする廃水処理装置。
6. The wastewater treatment device according to claim 1,
Store the scum scraped by the skimmer in the reaction tank,
A wastewater treatment device comprising a tank for treating the scum with a microorganism suitable for lipid decomposition.
JP2881996A 1996-02-16 1996-02-16 Waste water treatment apparatus Pending JPH09220591A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2881996A JPH09220591A (en) 1996-02-16 1996-02-16 Waste water treatment apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2881996A JPH09220591A (en) 1996-02-16 1996-02-16 Waste water treatment apparatus

Publications (1)

Publication Number Publication Date
JPH09220591A true JPH09220591A (en) 1997-08-26

Family

ID=12259020

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2881996A Pending JPH09220591A (en) 1996-02-16 1996-02-16 Waste water treatment apparatus

Country Status (1)

Country Link
JP (1) JPH09220591A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003266094A (en) * 2002-03-13 2003-09-24 Hideken Sekkei:Kk Anaerobic digestion tank and operation method therefor
JP2006297394A (en) * 2006-08-08 2006-11-02 Toshiba Corp Anaerobic wastewater treatment apparatus
CN102153197A (en) * 2011-04-13 2011-08-17 芜湖慧安水处理科技有限公司 Internal circulation anaerobic reactor
JP2011206657A (en) * 2010-03-29 2011-10-20 Chugoku Electric Power Co Inc:The Gas-liquid separator

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003266094A (en) * 2002-03-13 2003-09-24 Hideken Sekkei:Kk Anaerobic digestion tank and operation method therefor
JP2006297394A (en) * 2006-08-08 2006-11-02 Toshiba Corp Anaerobic wastewater treatment apparatus
JP2011206657A (en) * 2010-03-29 2011-10-20 Chugoku Electric Power Co Inc:The Gas-liquid separator
CN102153197A (en) * 2011-04-13 2011-08-17 芜湖慧安水处理科技有限公司 Internal circulation anaerobic reactor

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