JP2000037697A - Water treatment method and apparatus - Google Patents

Water treatment method and apparatus

Info

Publication number
JP2000037697A
JP2000037697A JP10223589A JP22358998A JP2000037697A JP 2000037697 A JP2000037697 A JP 2000037697A JP 10223589 A JP10223589 A JP 10223589A JP 22358998 A JP22358998 A JP 22358998A JP 2000037697 A JP2000037697 A JP 2000037697A
Authority
JP
Japan
Prior art keywords
water
sludge
aeration
purification
area
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
JP10223589A
Other languages
Japanese (ja)
Inventor
Kazuo Fujita
一男 藤田
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.)
Nihon Kentetsu Co Ltd
Original Assignee
Nihon Kentetsu 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 Nihon Kentetsu Co Ltd filed Critical Nihon Kentetsu Co Ltd
Priority to JP10223589A priority Critical patent/JP2000037697A/en
Publication of JP2000037697A publication Critical patent/JP2000037697A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage

Abstract

PROBLEM TO BE SOLVED: To keep treatment capacity in a water treatment method and apparatus by aeration type gravel purification, to allow excessive sludge generated between gravels to flow out of the system aerlier and to prevent the spoilage of sludge or the clogging between gravels to enhance treatment capacity. SOLUTION: A water tank is divided into a plurality of purifying areas 11, 12, 13 and a final stage single sludge area 14, and gravels 2 and air diffusers 3 are arranged to the purifying areas 11, 12, 13 and water is allowed to flow successively from the upstream side and treated water is introduced into the sludge area 14 to sediment sludge to allow supernatant water to flow out and aeration is collectively performed in the purifying areas 11, 12, 13 successively and cyclically from the upstream 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】本発明は都市排水や河川水な
どの原水(被処理水)を浄化するため内部にレキが敷設
された水槽からなる曝気式レキ間浄化を行なう水処理方
法及び装置の改良に関する。この種の水処理装置はとり
わけ低BOD排水、例えばBODが100mg/L以下
の排水の処理に好適に用いられる。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a water treatment method and apparatus for purifying raw water (to-be-treated water) such as city drainage or river water, which is an aeration type water purifier comprising a water tank in which water is laid. Regarding improvement. This type of water treatment apparatus is particularly suitably used for treating low BOD wastewater, for example, wastewater having a BOD of 100 mg / L or less.

【0002】[0002]

【従来の技術】従来、レキを用いる水処理装置は図4に
示すように、基本的には、原水を導入、浄化するための
水槽1と、該水槽内に敷設されたレキ2と、該レキ2の
下に配置される散気装置3によって構成される。水槽1
の一端には原水の導入管4が備えられ及び水槽1の他端
に処理水の流出管5が設置される。散気装置3には配管
を介してブロワ−6が接続される。
2. Description of the Related Art Conventionally, as shown in FIG. 4, a water treatment apparatus using a rake basically comprises a water tank 1 for introducing and purifying raw water, a rake 2 laid in the water tank, and a water tank. It is constituted by an air diffuser 3 arranged below the rake 2. Aquarium 1
Is provided with an inlet pipe 4 for raw water and an outlet pipe 5 for treated water at the other end of the water tank 1. A blower 6 is connected to the air diffuser 3 via a pipe.

【0003】導入管4を通って水槽1内に導入された原
水はその中に滞留する汚泥微生物によって浄化される。
水槽1内ではブロワ−6から挿入される空気が散気装置
3を通して放出され、レキ2の間を通って曝気(エアレ
−ション)が行なわれ、生物処理を促進する。即ち、レ
キ2に生息する微生物及び浮遊する微生物によって原水
中の異物が生物学的酸化処理を受け、原水は汚泥と処理
水に分離し、処理水は流出管5から流出するようになっ
ている。
[0003] Raw water introduced into the water tank 1 through the introduction pipe 4 is purified by sludge microorganisms staying therein.
In the water tank 1, air inserted from the blower 6 is released through the air diffuser 3, and aeration (aeration) is performed between the rakes 2 to promote biological treatment. That is, the foreign matter in the raw water undergoes the biological oxidation treatment by the microorganisms inhabiting the reki 2 and the floating microorganisms, the raw water is separated into sludge and the treated water, and the treated water flows out from the outflow pipe 5. .

【0004】[0004]

【発明が解決しようとする課題】このような従来の水処
理装置は水槽1の内部が単一の槽であり、その中の汚泥
微生物が同一種の微生物となるため発生する余剰汚泥量
が多くなると共に、時間の経過によりレキ間における抵
抗の少ない箇所から多く曝気し、汚泥が多く滞留して抵
抗の大きな箇所からの曝気がなくなる。従って曝気が不
均一になり、エアの出にくい所に余剰汚泥が蓄積されて
長時間滞留し、その部分が嫌気性になり、レキ間に目詰
りを生じ、処理性能が低下した。特に降雨期には多量の
砂泥がレキ間に入って目詰りを起し、処理性能が大幅に
低下する傾向があった。
In such a conventional water treatment apparatus, the inside of the water tank 1 is a single tank, and the amount of surplus sludge generated is large because the sludge microorganisms therein are the same kind of microorganism. At the same time, as time elapses, more aeration is performed from places with low resistance between the rakes, and a large amount of sludge stays and aeration from places with high resistance is stopped. Therefore, the aeration became uneven, and the excess sludge was accumulated in places where air was difficult to flow out and stayed for a long time, and that portion became anaerobic, clogging occurred between the rolls, and the processing performance was reduced. Especially during the rainy season, a large amount of sand and mud was caught in the gaps, causing clogging, and the treatment performance tended to be significantly reduced.

【0005】本発明の目的は上記従来技術の問題点を解
消することであって、それ故、レキを用いる水処理装置
の処理性能を維持し且つレキ間に発生する余剰汚泥を早
めに系外に流出し、汚泥の腐敗やレキ間の目詰りを防
ぎ、装置全体の処理性能を高め且つ性能を長期間安定さ
せることである。
[0005] An object of the present invention is to solve the above-mentioned problems of the prior art, and therefore, it is necessary to maintain the treatment performance of a water treatment apparatus using a reki and quickly remove excess sludge generated between the rekis. The purpose of the present invention is to prevent the sludge from being rotted and clogging between reeds, to enhance the processing performance of the entire apparatus and to stabilize the performance for a long period of time.

【0006】[0006]

【課題を解決するための手段】上記本発明の目的を達成
するため、本発明による水処理方法の特徴は、水槽内に
導入した原水を曝気式レキ間浄化する方法において、前
記水槽内の区分された区域に順次に原水を流通して各前
記区域における曝気を上流側の区域(前段)より順次に
行なってレキ間曝気を行ない、最終段の前記区域の処理
水を汚泥区域に導入して該処理水中の汚泥を沈降するこ
とであり、曝気を水槽内の1つの区域ごとに集中して行
なうことにより、レキ間の目詰りを除去し、処理性能を
保つ。
In order to achieve the object of the present invention, a water treatment method according to the present invention is characterized in that, in a method of purifying raw water introduced into a water tank between aeration tanks, there is provided a method for purifying raw water. Raw water is sequentially circulated through the divided areas, and aeration in each of the above sections is sequentially performed from the upstream section (previous stage) to perform aeration between the rakes, and the treated water in the last section is introduced into the sludge section. This is to settle the sludge in the treated water, and by performing aeration intensively for each area in the water tank, the clogging between the rakes is removed and the treatment performance is maintained.

【0007】また、上記方法を実施するための本発明に
よる装置は、内部が複数の浄化区域と流出側の単一の汚
泥区域とに区分され且つ浄化すべき原水が一方の浄化区
域から後続の前記区域に順次に流通するようになってい
る水槽と、各浄化区域に敷設されたレキ及び該レキの下
に設置された散気装置と、各散気装置に接続された分岐
管及びそれらの分岐管に接続された共通の管とからなる
配管と、曝気用エアを送るため前記共通の管に接続され
たブロワ−と、一連の浄化区域での曝気を順次に行なう
のを可能にするため各分岐管に設置された自動弁とを含
むことを特徴とし、好適には水槽内には3、4又は5つ
の前記浄化区域が設けられている。
Further, the apparatus according to the present invention for carrying out the above-mentioned method is characterized in that the inside is divided into a plurality of purification zones and a single sludge zone on the outflow side, and raw water to be purified is supplied from one purification zone to the subsequent one. A water tank that is sequentially circulated to the area, a rake laid in each purification area and an air diffuser installed under the rake, a branch pipe connected to each air diffuser, and a A pipe consisting of a common pipe connected to a branch pipe, a blower connected to the common pipe for sending air for aeration, and to enable successive aeration in a series of purification zones. And an automatic valve installed in each branch pipe, and preferably three, four or five said purifying sections are provided in the water tank.

【0008】[0008]

【発明の実施の形態】次に図面を参照のもとに実施例に
より本発明に関し説明する。図1及び図2に示すよう
に、本発明による水処理装置も基本的には水槽10と、
その内に敷設されるレキ2と、該水槽内で曝気を行なう
ための散気装置3によって構成され、導入管4を通して
水槽10内に導入された原水は該水槽内に生息する汚泥
微生物による接触酸化作用によって浄化される。
BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a block diagram showing a first embodiment of the present invention; As shown in FIGS. 1 and 2, the water treatment apparatus according to the present invention basically includes a water tank 10,
The raw water introduced into the water tank 10 through the introduction pipe 4 is constituted by a rake 2 laid therein and an air diffuser 3 for performing aeration in the water tank, and is contacted by sludge microorganisms living in the water tank. Purified by oxidation.

【0009】この水処理方法で用いられる水槽10はそ
の長手方向に沿って槽内が適当数の区域に区分されてお
り、且つ最終段、即ち最も下流側の区域が汚泥沈降用の
汚泥区域になっており、及び該汚泥区域を除く各区域を
1つの区域ごとに順次に曝気し得るように構成される。
このような水槽を用いることにより、この水処理方法は
原水を水槽内の上流側の区域より順次に各区域に流通し
て最終段の汚泥区域で汚泥を沈降し上澄水たる処理水を
流出すると共に、曝気を各区域ごとに上流側より順次に
行なうことを特徴とし、その区域の散気装置を通して曝
気を集中して行なうことによって、レキ間を閉塞してい
る汚泥を上昇、剥離して再生(洗浄)する特長を有する
ものである。
In the water tank 10 used in this water treatment method, the inside of the tank is divided into an appropriate number of sections along the longitudinal direction, and the last stage, that is, the most downstream area is a sludge area for sludge sedimentation. And each zone except the sludge zone is configured to be able to be sequentially aerated for each zone.
By using such a water tank, this water treatment method circulates raw water sequentially to each area from the upstream area in the water tank, sediments the sludge in the sludge area at the final stage, and discharges treated water as supernatant water. In addition, the aeration is performed sequentially from the upstream side for each area, and the aeration is concentrated through the air diffuser in that area, so that the sludge blocking the space between the rakes is lifted, separated, and regenerated. (Cleaning).

【0010】この水処理装置につき、図1及び図2に関
し詳記すると、図示の例では水槽10の内部は3つの仕
切り7、8、9によって4つの区域に区分され、前段の
区域11とそれに続く2つの区域12、13は浄化区域
として用いられ、最終段の区域14が汚泥区域として用
いられる。導入管4から水槽内の区域11に導入された
原水は好適には図示のようにオ−バ−フロ−によって順
次、後続の区域に移流するようになっている。この場
合、各仕切りは仕切壁として構成される。
The water treatment apparatus will be described in detail with reference to FIGS. 1 and 2. In the illustrated example, the inside of the water tank 10 is divided into four sections by three partitions 7, 8, 9, and the preceding section 11 and the preceding section 11 are divided into four sections. The next two zones 12, 13 are used as a purification zone, and the last stage zone 14 is used as a sludge zone. The raw water introduced from the introduction pipe 4 into the area 11 in the water tank is preferably transferred to the subsequent area by an overflow as shown in the figure. In this case, each partition is configured as a partition wall.

【0011】図1及び図2に示すように、各浄化区域1
1、12、13はその内で汚泥微生物による浄化作用を
行なうため、それぞれ内部にレキ2が敷設され、及びそ
れぞれレキ2の下に散気装置3a、3b、3cが設置さ
れる。これらの浄化用の区域11、12、13は好まし
くは同じ容量に構成される。レキ2としては従来のもの
と同じであってもよい。また各区域内の散気装置はそれ
ぞれ適当数の散気管によって構成される。それらの散気
管のエア放出孔がレキ2によって閉塞されるのを防ぐた
め多孔板などの気体透過性の被いを介在させてもよい。
As shown in FIG. 1 and FIG.
In order to perform a purification action by sludge microorganisms in the insides 1, 12, and 13, a wrench 2 is laid inside, and air diffusers 3a, 3b, and 3c are installed below the wrecks 2, respectively. These purifying zones 11, 12, 13 are preferably configured to the same volume. The rake 2 may be the same as the conventional one. The air diffuser in each area is constituted by an appropriate number of air diffusers. A gas-permeable covering such as a perforated plate may be interposed to prevent the air discharge holes of the air diffusers from being closed by the recess 2.

【0012】各区域の散気装置はそれぞれの分岐管を介
し、即ち散気装置3aはその分岐管15aを介し、散気
装置3bはその分岐管15bを介して及び散気装置3c
は分岐管15cを介してそれぞれ共通の管15に接続さ
れ、該共通の管15の一端にブロワ−6が設置されてい
る。従って、これらの分岐管と共通の管15によってブ
ロワ−6と各散気装置との間の配管が構成される。
The air diffusers in each zone are via their respective branch pipes, ie the air diffuser 3a is via its branch pipe 15a, the air diffuser 3b is via its branch pipe 15b and the air diffuser 3c.
Are connected to a common pipe 15 via a branch pipe 15c, and a blower 6 is installed at one end of the common pipe 15. Therefore, a pipe between the blower 6 and each air diffuser is constituted by the common pipe 15 with these branch pipes.

【0013】この水処理装置の特徴は上記のように水槽
内が適当数の区域に区分されると共に各区域ごとに曝気
を行ない得るように構成されることであり、そのため各
分岐管に、適当なコントロ−ラ又はタイマ−等によって
自動的に開閉される自動弁が設置される。即ち、図示の
ように、分岐管15aに自動弁16aが、分岐管15b
に自動弁16bが、分岐管15cに自動弁16cがそれ
ぞれ設置される。これらの自動弁としては任意の型又は
構造のものであってよいが、一例では電磁弁が用いられ
る。
The feature of this water treatment apparatus is that the inside of the water tank is divided into an appropriate number of sections as described above, and that the aeration can be performed in each section. An automatic valve which is automatically opened and closed by a controller or a timer is installed. That is, as shown, an automatic valve 16a is provided in the branch pipe 15a,
The automatic valve 16b is installed in the branch pipe 15c, respectively. These automatic valves may be of any type or structure. In one example, a solenoid valve is used.

【0014】なお、汚泥区域14はその前段での処理水
を受け入れてそこに含まれる汚泥を沈降分離する役割を
果すものであって、従ってその区域にはレキ2及び散気
装置は設置されない。この汚泥区域14には図1に示す
ように、その底部の近くに汚泥引抜き用の開口17が設
けられ、及び該開口に汚泥引抜管18が接続される。こ
の汚泥引抜管18はバッキュ−ムカ−などの真空源(図
示せず)に接続され、該汚泥区域で沈降した汚泥は定期
的に抜き取られるようになっている。
The sludge section 14 serves to receive the treated water in the preceding stage and settle and separate the sludge contained therein. Therefore, no recoil 2 and a diffuser are installed in the section. As shown in FIG. 1, the sludge section 14 is provided with an opening 17 for drawing sludge near the bottom thereof, and a sludge drawing pipe 18 is connected to the opening. The sludge withdrawal pipe 18 is connected to a vacuum source (not shown) such as a vaccum car, and the sludge settled in the sludge area is periodically withdrawn.

【0015】また、図1及び図2には示されていない
が、所望により、各区域内における原水導入側の近くに
バッフル板(そらせ板)が設けられ、該バッフル板によ
り導入直後の原水を下降して原水がそのまま出口側に流
れるのを防ぎ、その区域において原水が汚泥微生物によ
る処理を受けるのに充分な時間にわたり滞留するのを確
保する。
Although not shown in FIGS. 1 and 2, if desired, a baffle plate (deflecting plate) is provided near the raw water introduction side in each area, and the raw water immediately after introduction is provided by the baffle plate. Descends to prevent the raw water from flowing directly to the outlet side, ensuring that the raw water remains in the area for a sufficient time to be treated by the sludge microorganisms.

【0016】この水処理装置では原水は導入管4から水
槽10内の浄化区域11に入り、そこから次の浄化区域
12に、さらに浄化区域13に流通し、該区域13から
オーバ−フロ−により汚泥区域14に流入し、その区域
での上澄水が流出管5から排出されると共に、各浄化区
域11、12、13において上流側より順次に曝気が行
なわれる。即ち、先ず、浄化区域11の自動弁16aの
みを開き、他の自動弁16b、16cを閉として、ブロ
ワ−6からのエア−をすべて、共通の管15及び分岐管
15aを介し散気装置3aに送り、そこから集中して放
出する。
In this water treatment apparatus, raw water enters the purifying section 11 in the water tank 10 from the introduction pipe 4, and then flows to the next purifying section 12 and further to the purifying section 13, from which the overflow water flows. The water flows into the sludge section 14, and the supernatant water in the section is discharged from the outflow pipe 5, and the aeration is sequentially performed from the upstream side in each of the purification sections 11, 12, and 13. That is, first, only the automatic valve 16a of the purification section 11 is opened, the other automatic valves 16b and 16c are closed, and all the air from the blower 6 is diffused through the common pipe 15 and the branch pipe 15a. , And release it from there.

【0017】このように浄化区域11での曝気が一定時
間、例えば1時間を経過すると、その自動弁16aを閉
じ、浄化区域13の自動弁16cは閉じたままで次の浄
化区域12の自動弁16bを開き、該区域12において
散気装置3bからエアを放出して一定時間にわたり曝気
を行なう。次いで自動弁16aは閉のままにして浄化区
域12の自動弁16bを閉じ、及び浄化区域13の自動
弁16cを開き、該区域13において散気装置3cから
エアを放出して曝気を行なう。該区域13における曝気
を一定時間行なうと、自動弁16cを閉じ、及び浄化区
域11の自動弁16aを開いて、上記動作がくり返され
る。なお、各区域での曝気時間は装置の構造、原水の状
態、処理条件などによって適当な時間がとられる。
As described above, when the aeration in the purification section 11 has passed for a certain period of time, for example, one hour, the automatic valve 16a of the next purification section 12 is closed while the automatic valve 16c of the purification section 13 remains closed. Is opened, air is released from the air diffuser 3b in the area 12, and aeration is performed for a certain period of time. Next, the automatic valve 16a is kept closed, the automatic valve 16b of the purification section 12 is closed, and the automatic valve 16c of the purification section 13 is opened. In the section 13, air is released from the air diffuser 3c to perform aeration. When the aeration in the zone 13 is performed for a certain period of time, the automatic valve 16c is closed and the automatic valve 16a in the purification zone 11 is opened, and the above operation is repeated. The aeration time in each area is appropriately set according to the structure of the apparatus, the state of raw water, the treatment conditions, and the like.

【0018】なお、原水のBODが低い場合、例えばB
OD5〜10mg/Lの場合には最も下流側の浄化区域
13での曝気を省き、それより上流側の浄化区域11、
12で順次に曝気をくり返し、該区域13を沈降部とし
て用いてもよい。この場合、浄化区域13におけるレキ
間の余剰汚泥や砂泥を除去するため例えば1ケ月に1回
程度の間隔で、その散気装置3cからエアを放出するこ
とが行なわれ、濃縮された汚泥を汚泥区域14に効率的
に移送することができるので、維持管理面及び処理性能
面で有効に活用できる。
When the BOD of raw water is low, for example, B
When the OD is 5 to 10 mg / L, the aeration in the most downstream purification section 13 is omitted, and the upstream purification section 11,
Aeration may be repeated sequentially at 12, and the area 13 may be used as a settling section. In this case, air is released from the air diffuser 3c at intervals of, for example, about once a month in order to remove excess sludge and sand mud between the rakes in the purification area 13, and the concentrated sludge is removed. Since it can be efficiently transferred to the sludge area 14, it can be effectively used in terms of maintenance and processing performance.

【0019】このように、各浄化区域11、12、13
を上流側の区域より順次、曝気することによって各区域
内のレキ2間の余剰汚泥や砂泥が順次、後続の区域に移
送され、最終的には汚泥区域14に導入されてそこで沈
降し、開口17及び汚泥引抜管18を介して外部に排出
される。汚泥区域14における上澄水が処理水として流
出管5を通して放流される。
Thus, each of the purification zones 11, 12, 13
By sequentially aeration from the upstream area, excess sludge and sand mud between the rakes 2 in each area are sequentially transferred to the subsequent area, finally introduced into the sludge area 14 and settled there, It is discharged to the outside through the opening 17 and the sludge extraction pipe 18. The supernatant water in the sludge section 14 is discharged through the outlet pipe 5 as treated water.

【0020】また、図1及び図2に示すように、浄化区
域間の仕切り7、8も仕切壁として構成し、それらの区
域間の移流もオ−バ−フロ−によって行なえば、それら
の浄化区域において互いに異なる生物相が形成され、従
って食物連鎖が進み、余剰汚泥の発生を少なくし、処理
性能を向上する利点がある.
As shown in FIGS. 1 and 2, the partitions 7 and 8 between the purification sections are also constituted as partition walls, and if the advection between these sections is also carried out by overflow, the purification of those sections is performed. Different biota are formed in the area, so the food chain is advanced, and there is an advantage that the generation of excess sludge is reduced and the treatment performance is improved.

【0021】なお、浄化区域間の仕切り7、8は必ずし
も仕切壁である必要はなく、液透過性の平面材、例えば
図3に示すように、メッシュで構成してもよく、この場
合、各区域における導入側にバッフル板19が設置され
るのが好ましい。この場合にも上流側の区域から順次に
曝気が行なわれることは云うまでもない。
The partitions 7 and 8 between the purification sections need not necessarily be partition walls, and may be formed of a liquid-permeable flat material, for example, a mesh as shown in FIG. A baffle plate 19 is preferably provided on the introduction side in the area. In this case as well, it goes without saying that aeration is performed sequentially from the upstream area.

【0022】上記の実施例では水槽内の最終段に汚泥区
域14があるほか、水槽内に3つの浄化区域が備えられ
ているが、場合によっては浄化区域はそれ以外の個数で
あってもよいが、好適には浄化区域は3、4又は5つが
備えられる。その個数であれば、最少の浄化区域で処理
性能を効果的に向上し、且つオ−バ−フロ−により移流
する場合にも適当数の異なる生物相が生じるが、それ以
上に区分しても設備費の高騰を招くのみで、コスト的ニ
−ズにマッチしなくなり、且つそれに相応した処理性能
の向上が期待し得ない。
In the above embodiment, the sludge area 14 is provided at the last stage in the water tank, and three purification areas are provided in the water tank. However, in some cases, the number of purification areas may be other. Preferably, however, three, four or five purification zones are provided. With that number, the treatment performance is effectively improved in the minimum purification area, and an appropriate number of different biota will be generated even when advection is performed by overflow. Only incurring a rise in equipment costs, it does not match the cost needs, and the corresponding improvement in processing performance cannot be expected.

【0023】なお、図示の実施例では各区域ごとに順次
に行なわれる曝気を各分岐管の自動弁の開閉操作によっ
て行なっているが、場合により他の方式で行なってもよ
く、例えば共通の管15を用いないで各浄化区域の散気
装置ごとにブロワ−を設け、コントロ−ラによりそれら
のブロワ−をオン・オフ制御することによって行なって
もよい。特に水槽の容量が大きい場合には、このような
方式も有効である。
In the illustrated embodiment, the aeration performed sequentially for each section is performed by opening and closing the automatic valve of each branch pipe. However, the aeration may be performed by another method in some cases. Instead of using the air blower 15, a blower may be provided for each air diffuser in each purification area, and the blowers may be turned on and off by a controller. Especially when the capacity of the water tank is large, such a method is also effective.

【0024】[0024]

【発明の効果】上記のように、本発明によれば、水槽内
の区分された区域ごとに上流側より一定時間ごとに順次
にレキ間曝気が集中して行なわれるので、曝気強度が高
まり、レキ間に滞留した汚泥や砂泥を剥離することがで
き、目詰りを防止できるので、長期にわたり安定した処
理性能が維持される。特に従来、降雨期の初めに多量の
砂泥が流入するとレキ間に目詰りを起したが、そのよう
な場合にも砂泥を順次に次の区域に移流し、目詰りを防
ぐことができる。また、この水処理装置では、曝気用の
ブロワ−は水槽内の全体にわたり曝気する場合に比し、
小容量のもので可能になる。
As described above, according to the present invention, the aeration between the rakes is sequentially concentrated from the upstream side at regular time intervals for each of the divided areas in the water tank, so that the aeration intensity increases. Sludge and sand mud staying between the rakes can be removed and clogging can be prevented, so that stable treatment performance can be maintained for a long period of time. Particularly, conventionally, when a large amount of sand and mud flowed in at the beginning of the rainy season, clogging occurred between the legs, but even in such a case, the sand and mud are sequentially transferred to the next area, and clogging can be prevented. . Further, in this water treatment apparatus, the blower for aeration is compared with the case where aeration is performed in the entire water tank,
It becomes possible with a small capacity.

【0025】水槽内に区分される浄化区域の個数を3、
4又は5とすることにより、各区域を効果的に活用で
き、とりわけ設備上のコストの上昇を招くこともなく、
経済性の点で最も好ましい区分数になっている。なお、
各区域間の移流をオ−バ−フロ−によって行なう場合、
各区域の生物相を独立したものにし、余剰汚泥の発生、
滞留を少なくする利点があるが、このような場合にも3
ないし5の浄化区域に区分することは最適数の区分にな
っている。
The number of purification zones divided in the water tank is 3,
By setting it to 4 or 5, each area can be effectively used, and especially without increasing the equipment cost.
This is the most favorable number of categories in terms of economy. In addition,
When advection between the sections is performed by overflow,
Independent biota in each area, generating excess sludge,
This has the advantage of reducing stagnation.
The division into five to five purification zones is the optimal number of divisions.

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

【図1】本発明による水処理装置の一例を概略的に示す
側断面図である。
FIG. 1 is a side sectional view schematically showing an example of a water treatment apparatus according to the present invention.

【図2】図1に示す水処理装置の概略的な平面図であ
る。
FIG. 2 is a schematic plan view of the water treatment apparatus shown in FIG.

【図3】本発明の他の実施例を概略的に示す側断面図で
ある。
FIG. 3 is a side sectional view schematically showing another embodiment of the present invention.

【図4】従来のレキ間曝気式の水処理装置を概略的に示
す側断面図である。
FIG. 4 is a side sectional view schematically showing a conventional water treatment device of the aeration type between rakes.

【符号の説明】[Explanation of symbols]

2:レキ、3a、3b、3c:散気装置、6:ブロワ
−、10:水槽、11、12、13:浄化区域、14:
汚泥区域、15:共通の管、15a、15b、15c:
分岐管、16a、16b、16c:自動弁
2: Reki, 3a, 3b, 3c: diffuser, 6: blower, 10: water tank, 11, 12, 13: purification area, 14:
Sludge area, 15: common pipe, 15a, 15b, 15c:
Branch pipe, 16a, 16b, 16c: automatic valve

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 水槽内に導入した原水を曝気式レキ間浄
化する方法において、前記水槽内の区分された区域に順
次に原水を流通して各前記区域における曝気を上流側の
区域より順次に行なってレキ間曝気を行ない、下流側の
前記区域の処理水を汚泥区域に導入して該処理水中の汚
泥を沈降することを特徴とする水処理方法。
1. A method for purifying raw water introduced into a water tank between aeration tanks, wherein the raw water is sequentially circulated through divided areas in the water tank, and aeration in each of the sections is sequentially performed from an upstream area. A water treatment method comprising: performing aeration between rakes to introduce treated water in the downstream section into a sludge section to settle sludge in the treated water.
【請求項2】 内部が複数の浄化区域と流出側の単一の
汚泥区域に区分され且つ浄化すべき原水が一方の浄化区
域から後続の前記区域に順次に流通するようになってい
る水槽と、各浄化区域に敷設されたレキ及び該レキの下
に設置された散気装置と、各散気装置に接続された分岐
管及びそれらの分岐管に接続された共通の管とからなる
配管と、曝気用エアを送るため前記共通の管に接続され
たブロワ−と、一連の浄化区域での曝気を順次に行なう
のを可能にするため各分岐管に設置された自動弁とを含
むことを特徴とする水処理装置。
2. A water tank having an interior divided into a plurality of purification sections and a single sludge section on an outflow side, and raw water to be purified is sequentially passed from one purification section to the subsequent section. A pipe consisting of a rake laid in each purification area and an air diffuser installed under the rake, a branch pipe connected to each air diffuser, and a common pipe connected to those branch pipes. Including a blower connected to said common pipe for delivering air for aeration, and an automatic valve installed on each branch pipe to enable sequential aeration in a series of purification zones. Characterized water treatment equipment.
【請求項3】 前記水槽内には3、4又は5つの前記浄
化区域が設けられていることを特徴とする請求項2に記
載の水処理装置。
3. The water treatment apparatus according to claim 2, wherein three, four or five purifying sections are provided in the water tank.
JP10223589A 1998-07-23 1998-07-23 Water treatment method and apparatus Pending JP2000037697A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10223589A JP2000037697A (en) 1998-07-23 1998-07-23 Water treatment method and apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10223589A JP2000037697A (en) 1998-07-23 1998-07-23 Water treatment method and apparatus

Publications (1)

Publication Number Publication Date
JP2000037697A true JP2000037697A (en) 2000-02-08

Family

ID=16800544

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10223589A Pending JP2000037697A (en) 1998-07-23 1998-07-23 Water treatment method and apparatus

Country Status (1)

Country Link
JP (1) JP2000037697A (en)

Similar Documents

Publication Publication Date Title
JP2875765B2 (en) High-concentration wastewater treatment equipment
US6190548B1 (en) Multi-chambered treatment filter
US4818391A (en) Integral Clarifier
JPH02131194A (en) Purifier
WO2002096806A3 (en) Method, apparatus and biomass support element for biological wastewater treatment
US1286017A (en) Purification of sewage and analogous liquids.
KR101767032B1 (en) Wastewater Treatment System For Dairy Farming
KR20090100962A (en) Stock raising onsite wastewater treatment apparatus
US8012353B2 (en) Method and apparatus for simultaneous clarification and endogenous post denitifrication
JP2006289153A (en) Method of cleaning sewage and apparatus thereof
JP2000084578A (en) Contact aeration tank
US6258274B1 (en) Method for reducing sludge within a river or the like
JPH11244891A (en) Method for denitrification treating waste water and treating system
JP2000037697A (en) Water treatment method and apparatus
JPS61157396A (en) Aeration type high performance waste water treatment apparatus
CN217398702U (en) Multidirectional-circulation efficient denitrification sewage treatment equipment
JP2697801B2 (en) Septic tank
US4652371A (en) Integral clarifier
JPS61227894A (en) Batch device for treating filthy water
JPH10337584A (en) Sewage treatment tank
SU958325A1 (en) Filter for purifying farm fecal liquors from organic impurities
JP2663809B2 (en) Wastewater treatment equipment
JPH07256286A (en) Water treatment apparatus
JP3716461B2 (en) Concentration method in the receiving tank for biological filtration backwash wastewater
KR890006973Y1 (en) Tank for treatment of sewage

Legal Events

Date Code Title Description
FPAY Renewal fee payment (prs date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090601

Year of fee payment: 15

EXPY Cancellation because of completion of term