JP2000126790A - Aerobic treatment apparatus - Google Patents

Aerobic treatment apparatus

Info

Publication number
JP2000126790A
JP2000126790A JP30731698A JP30731698A JP2000126790A JP 2000126790 A JP2000126790 A JP 2000126790A JP 30731698 A JP30731698 A JP 30731698A JP 30731698 A JP30731698 A JP 30731698A JP 2000126790 A JP2000126790 A JP 2000126790A
Authority
JP
Japan
Prior art keywords
air
amount
treated
water
groups
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP30731698A
Other languages
Japanese (ja)
Other versions
JP3451964B2 (en
Inventor
Makoto Tanaka
真 田中
Masayoshi Sakuma
正芳 佐久間
Hideyuki Suwa
秀行 諏訪
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.)
Hitachi Plant Technologies Ltd
Original Assignee
Hitachi Plant Technologies 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 Hitachi Plant Technologies Ltd filed Critical Hitachi Plant Technologies Ltd
Priority to JP30731698A priority Critical patent/JP3451964B2/en
Publication of JP2000126790A publication Critical patent/JP2000126790A/en
Application granted granted Critical
Publication of JP3451964B2 publication Critical patent/JP3451964B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime 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

Landscapes

  • Activated Sludge Processes (AREA)
  • Biological Treatment Of Waste Water (AREA)

Abstract

PROBLEM TO BE SOLVED: To prevent the lowering of treatment capacity by uniformizing the concn. distribution of the microorganism carrier in a treatment tank. SOLUTION: A plurality of air diffusion plates 26 supplying air into water to be treated to form an aerobic condition are arranged to the bottom part in a treatment tank 14 and an air supply line 30 supplying air to a plurality of the air diffusion plates 26 is divided into a plurality of groups from the air diffusion plate 26 on the side of an inflow port 18 to the air diffusion plate 26 on the side of an outflow port 22. Flow rate adjusting valves 32 controlling the amount air supplied to the air diffusion plates 26 of the respective groups are provided to indivisually control the air diffusion amount from the air diffusion plates 26 at groups.

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、好気性処理装置に
係り、特に、下水、し尿、産業排水等の有機性排水にエ
アを散気しながら微生物担体を利用して生物学的に処理
する好気性処理装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an aerobic treatment apparatus, and more particularly to a biological treatment using an microorganism carrier while diffusing air into organic wastewater such as sewage, human waste, and industrial wastewater. The present invention relates to an aerobic treatment device.

【0002】[0002]

【従来の技術】下水、し尿、産業排水等の有機性排水の
浄化処理する装置としては、好気性条件下で微生物、例
えば硝化菌を固定化した微生物担体を利用して生物学的
に処理する好気性処理装置がある。この好気性散気装置
は、処理槽の流入口から流入した被処理水が処理槽の底
部に設けられた散気板からのエアによる好気性条件下で
微生物担体と接触して生物学的に処理された後、処理槽
の流出口から流出する。散気板は、処理槽の底面全面に
均等に配置されており、コンプレッサからのエア量が散
気板全体に均等に供給されて散気板からエアが処理槽全
体に均一に散気されるようにしている。
2. Description of the Related Art As an apparatus for purifying organic wastewater such as sewage, human waste, industrial wastewater, etc., a biological treatment is carried out under aerobic conditions using a microorganism carrier having immobilized microorganisms, for example, nitrifying bacteria. There is an aerobic treatment device. In this aerobic diffusion device, the water to be treated flowing from the inlet of the treatment tank contacts the microbial carrier under aerobic conditions with air from a diffuser plate provided at the bottom of the treatment tank to biologically treat the water. After the treatment, it flows out of the outlet of the treatment tank. The diffuser plate is evenly arranged on the entire bottom surface of the processing tank, and the amount of air from the compressor is evenly supplied to the entire diffuser plate, and the air is uniformly diffused from the diffuser plate to the entire processing tank. Like that.

【0003】[0003]

【発明が解決しようとする課題】しかしながら、処理槽
内には、流入口から流出口に至る被処理水の流れが形成
されるため、上記したような従来型の好気性処理装置の
場合には、時間がたつにつれて被処理水中における微生
物担体の濃度分布に偏りを生じる。この結果、被処理水
と微生物担体との接触効率が悪くなるので、生物学的な
処理性能が極端に低下してしまうという欠点がある。
However, since the flow of the water to be treated is formed from the inlet to the outlet in the treatment tank, the above-mentioned conventional aerobic treatment apparatus is not used. As the time elapses, the concentration distribution of the microorganism carrier in the water to be treated becomes uneven. As a result, the contact efficiency between the water to be treated and the microorganism carrier is deteriorated, and there is a disadvantage that the biological treatment performance is extremely reduced.

【0004】本発明は、このような事情に鑑みてなされ
たもので、処理槽内の微生物担体の濃度分布を均一化し
て処理性能の低下を防止することができる好気性処理装
置を提供することを目的とする。
[0004] The present invention has been made in view of such circumstances, and provides an aerobic treatment apparatus capable of uniforming the concentration distribution of microorganism carriers in a treatment tank and preventing a decrease in treatment performance. With the goal.

【0005】[0005]

【課題を解決するための手段】本発明は前記目的を達成
するために、被処理水を流入口から流入して流出口から
流出させる間に微生物を固定化した多数の微生物担体と
接触させ前記被処理水を生物学的に処理する処理槽と、
前記処理槽内の底部に、前記被処理水中にエアを供給し
て好気性条件を形成する散気板を複数配設すると共に、
該複数の散気板にエアを供給するエア供給ラインを前記
流入口側の散気板から前記流出口側の散気板にかけて複
数のグループにグループ分けしたエア散気装置と、前記
各グループの散気板から散気される散気量をグループご
とに個別に制御する制御手段と、を備えたことを特徴と
する。
According to the present invention, in order to achieve the above object, the present invention is characterized in that microorganisms are brought into contact with a large number of immobilized microorganism carriers while water to be treated flows in from an inlet and flows out from an outlet. A treatment tank for biologically treating the water to be treated,
At the bottom of the treatment tank, a plurality of diffuser plates are provided to supply air into the water to be treated and form aerobic conditions,
An air diffuser that divides an air supply line for supplying air to the plurality of diffuser plates into a plurality of groups from the diffuser plate on the inlet side to the diffuser plate on the outlet side; Control means for individually controlling the amount of air diffused from the air diffuser plate for each group.

【0006】本発明によれば、処理槽内の底部に被処理
水中にエアを供給して好気性条件を形成する散気板を複
数配設すると共に、該複数の散気板にエアを供給するエ
ア供給ラインを流入口側の散気板から流出口側の散気板
にかけて複数のグループにグループ分けした。そして、
各グループの散気板に供給するエア量を制御する制御手
段を設けて、散気板からの散気量をグループごとに個別
に制御できるようにした。これにより、散気板から散気
される気泡による微生物担体の拡散程度を、流入口側と
流出口側とで異なるようにすることができる。従って、
流入口から流出口に至る被処理水の流れの影響で微生物
担体の分布濃度が大きくなる場所の散気量を多くし、分
布濃度が小さくなる場所の散気量を小さくすることによ
り、処理槽内の微生物担体の分布濃度を均一化させるこ
とができる。
According to the present invention, a plurality of air diffusers are provided at the bottom of a processing tank to supply air into the water to be treated to form aerobic conditions, and air is supplied to the plurality of air diffusers. The air supply lines were divided into a plurality of groups from the diffuser plate on the inlet side to the diffuser plate on the outlet side. And
Control means for controlling the amount of air supplied to the diffuser plates of each group is provided so that the amount of air diffused from the diffuser plates can be individually controlled for each group. Thereby, the degree of diffusion of the microorganism carrier by the bubbles diffused from the diffuser plate can be made different between the inflow side and the outflow side. Therefore,
By increasing the amount of air diffused in places where the concentration of microbial carriers increases due to the effect of the flow of the water to be treated from the inlet to the outlet, and by reducing the amount of air diffused in places where the concentration of distribution decreases, The distribution concentration of the microorganism carrier in the inside can be made uniform.

【0007】[0007]

【発明の実施の形態】以下、添付図面に従って本発明に
係る好気性処理装置の好ましい実施の形態について詳説
する。図1は、本発明に係る好気性処理装置10の側面
断面図である。図1に示すように、本発明の好気性処理
装置10は、主として、好気性の微生物、例えば硝化菌
を包括固定或いは付着固定した多数の微生物担体12、
12…が添加された処理槽14と、処理槽14内に好気
性条件を形成する散気装置16とで構成される。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Preferred embodiments of the aerobic treatment apparatus according to the present invention will be described below in detail with reference to the accompanying drawings. FIG. 1 is a side sectional view of an aerobic treatment device 10 according to the present invention. As shown in FIG. 1, the aerobic treatment apparatus 10 of the present invention mainly includes a large number of microorganism carriers 12 in which aerobic microorganisms, for example, nitrifying bacteria are comprehensively fixed or adhered,
12 are added, and a diffuser 16 for forming an aerobic condition in the processing tank 14.

【0008】処理槽14は、横長な直方体状に形成さ
れ、その一端側(図1の左側)下部の流入口18には被
処理水を処理槽14に流入させる原水配管20が接続さ
れると共に、その他端側(図1の右側)上部の流出口2
2には処理水配管24が接続される。流出口22には微
生物担体12が被処理水に同伴して流出しないようにス
クリーン27が配設される。
The treatment tank 14 is formed in a horizontally long rectangular parallelepiped shape, and a raw water pipe 20 through which water to be treated flows into the treatment tank 14 is connected to an inflow port 18 below one end (left side in FIG. 1). , Outlet 2 on the other end (right side in FIG. 1)
2 is connected to a treated water pipe 24. A screen 27 is provided at the outlet 22 so that the microorganism carrier 12 does not flow out along with the water to be treated.

【0009】散気装置16は、処理槽14の略底部全面
に、処理槽14の流入口18側から流出口22側にかけ
て配列配置された複数の散気板26、26…と、処理槽
14外に設けたコンプレッサ28との間をエア供給ライ
ン30で繋いで構成される。このエア供給ラインは、本
管30Aから複数の枝管30B、30B…に分岐され、
更に枝管30Bから分岐した複数の接続管30Cと散気
板26とが接続される。そして、それぞれの枝管30B
に流量調整バルブ32が設けられる。これにより、処理
槽14の流入口18側の散気板26から流出口22側の
散気板26にかけて、即ち、処理槽14の流入口18か
ら流入した被処理水が流出口22に流れる流れ方向にか
けて、図2に示すように、例えばA〜Jの10グループ
にグループ分けし、各グループA〜Jに属する散気板2
6からの散気量をグループごとに個別に制御できるよう
にした。
The air diffuser 16 includes a plurality of air diffusers 26, 26... Arranged from the inlet 18 side to the outlet 22 side of the processing tank 14 over substantially the entire bottom of the processing tank 14. An air supply line 30 connects the compressor 28 provided outside. This air supply line is branched from the main pipe 30A into a plurality of branch pipes 30B, 30B,.
Further, a plurality of connection pipes 30C branched from the branch pipe 30B and the diffuser plate 26 are connected. And each branch pipe 30B
Is provided with a flow control valve 32. As a result, the flow of the water to be processed flowing from the air diffuser plate 26 on the inlet 18 side of the processing tank 14 to the air diffuser plate 26 on the outlet 22 side, that is, In the direction, as shown in FIG. 2, for example, the air diffusers 2 are divided into ten groups A to J and belong to the respective groups A to J.
The amount of air diffused from No. 6 can be individually controlled for each group.

【0010】次に上記の如く構成された本発明の好気性
処理装置10における散気方法について説明する。原水
配管20を介して流入口18から処理槽14内に流入し
た被処理水は、散気装置16からのエアによる好気性条
件下で処理槽14内を流出口22側に流れる間に微生物
担体12と接触し、生物学的に処理される。処理された
処理水は流出口22のスクリーン27で微生物が分離さ
れた後、処理水配管24を通って装置10外に排出され
る。
Next, a method for diffusing air in the aerobic treatment apparatus 10 of the present invention configured as described above will be described. The water to be treated which has flowed into the treatment tank 14 from the inlet 18 through the raw water pipe 20 flows through the treatment tank 14 to the outlet 22 under aerobic conditions by air from the diffuser 16 while the microorganism carrier 12 and is biologically treated. The treated water is discharged out of the apparatus 10 through the treated water pipe 24 after the microorganisms are separated by the screen 27 of the outlet 22.

【0011】この生物学的処理において、被処理水と微
生物担体12との接触効率を上げるためには、処理槽1
4内における微生物担体12の濃度分布を如何に均一に
するかが重要となる。そこで、本発明の好気性処理装置
10では、上記した複数のグループA〜Jのうち、最大
散気量で散気する散気板26のグループが時間の経過と
ともに流出口22側(被処理水の流れの下流側)から流
入口18側(被処理水の流れの上流側)に順次変化する
ように各グループA〜Jの流量調整バルブ32を制御す
るようにした。
In this biological treatment, in order to increase the contact efficiency between the water to be treated and the microorganism carrier 12, the treatment tank 1
It is important how to make the concentration distribution of the microbial carrier 12 in 4 uniform. Therefore, in the aerobic treatment apparatus 10 of the present invention, of the plurality of groups A to J, the group of the diffuser plates 26 that diffuses at the maximum amount of diffused air with the passage of the outlet 22 side (the water to be treated) as time passes. The flow control valves 32 of each of the groups A to J are controlled so as to sequentially change from the downstream side of the flow of (1) to the inlet 18 side (upstream of the flow of the water to be treated).

【0012】図3(a)は、各グループA〜Jから処理
槽14内に均一な散気量で散気する従来の好気性処理装
置での散気方法を示したものであり、図3(b)〜
(j)は本発明の好気性処理装置での散気方法を示した
ものである。また、図4(a)〜(j)は、図3(a)
〜(j)の散気方法における処理槽14内の微生物担体
12の濃度分布を示したものである。微生物担体12の
濃度と図4の黒色の濃淡との関係を示す濃淡バーのよう
に、黒色が濃い程、微生物担体12の濃度が大きいこと
を示し、最も濃い黒色部分における微生物担体12の濃
度が15%であることを示している。
FIG. 3A shows an air diffusion method in a conventional aerobic processing apparatus in which air is diffused from each of the groups A to J into the processing tank 14 at a uniform amount. (B) ~
(J) shows a method of diffusing air in the aerobic treatment device of the present invention. FIGS. 4A to 4J correspond to FIGS.
7 shows the concentration distribution of the microorganism carrier 12 in the treatment tank 14 in the aeration method of (j). As shown by a gray bar indicating the relationship between the concentration of the microorganism carrier 12 and the shade of black in FIG. 4, the darker the black, the greater the concentration of the microorganism carrier 12 is. The concentration of the microorganism carrier 12 in the darkest black portion is 15%.

【0013】図3(a)のように、各グループA〜Jか
ら均一な散気量で散気する従来の場合には、図4(a)
のように、流出口22側ほど微生物担体12の濃度分布
が大きくなり、処理槽14内において微生物担体12の
分布濃度に大きな偏りが発生する。特に、多数の微生物
担体12が処理槽14のスクリーン27下方に滞留しす
る傾向がある。
As shown in FIG. 3A, in the case of a conventional case where air is diffused from each of the groups A to J with a uniform amount of air, FIG.
As shown in the figure, the concentration distribution of the microorganism carrier 12 becomes larger toward the outlet 22, and the distribution concentration of the microorganism carrier 12 in the treatment tank 14 is greatly biased. In particular, many microbial carriers 12 tend to stay below the screen 27 of the processing tank 14.

【0014】次に、この従来における微生物担体12の
濃度分布の状態から本発明の散気方法を行った。即ち、
図3(b)に示すように、流出口22に一番近いグルー
プJの散気量を最大にし、グループIの散気量を2番目
に大きくし、他のグループA〜Hの散気量を同じで最小
にした。次に、図3(c)に示すように、グループIの
散気量を最大にし、グループH及びJの散気量を2番目
に大きくし、他のグループA〜Gの散気量を同じで最小
にした。次に、図3(d)に示すように、グループHの
散気量を最大にし、グループG及びIの散気量を2番目
に大きくし、他のグループA〜F及びグループJの散気
量を同じで最小にした。このように、最大散気量のグル
ープを流出口22側から流入口18側に時間の経過とと
もに順次変化させるようにし、図3(j)のように、グ
ループBの散気量を最大、グループA及びCの散気量を
2番目、他のグループD〜Jの散気量を同じで最小にし
たら、再び図3(b)の散気状態に戻るようにした。
Next, the aeration method of the present invention was performed from the state of the conventional concentration distribution of the microorganism carrier 12. That is,
As shown in FIG. 3B, the amount of air diffused in the group J closest to the outlet 22 is maximized, the amount of air diffused in the group I is made second largest, and the amount of air diffused in the other groups A to H is increased. Was the same and minimized. Next, as shown in FIG. 3C, the amount of air diffusion of the group I is maximized, the amount of air diffusion of the groups H and J is made the second largest, and the amount of air diffusion of the other groups A to G is the same. To minimize it. Next, as shown in FIG. 3D, the amount of air diffused in the group H is maximized, the amount of air diffused in the groups G and I is made the second largest, and the air diffused in the other groups A to F and the group J. The amount was the same and minimized. In this manner, the group with the maximum air diffusion amount is sequentially changed from the outlet 22 side to the inlet 18 side with the passage of time, and as shown in FIG. When the amount of air diffused in A and C was the second and the amount of air diffused in the other groups D to J was the same and minimized, the air diffused state was returned to the state shown in FIG. 3B again.

【0015】図4(b)〜(j)から分かるように、最
大散気量のグループを流出口22側から流入口18側に
時間の経過とともに変化させることにより、処理槽14
内に流入口18から流出口22に至る被処理水の流れが
形成されても、流出口22側に滞留していた微生物担体
12(図4の濃黒色部分)は流入口18側に移動しなが
ら、次第に拡散される。これにより、処理槽14内の微
生物担体12の濃度分布を均一化させることができる。
As can be seen from FIGS. 4 (b) to 4 (j), by changing the group of the maximum amount of diffused air from the outlet 22 to the inlet 18 over time, the processing tank 14
Even if the flow of the water to be treated from the inlet 18 to the outlet 22 is formed therein, the microorganism carrier 12 (the dark black portion in FIG. 4) that has stayed at the outlet 22 moves to the inlet 18 side. Meanwhile, it is gradually spread. Thereby, the concentration distribution of the microorganism carrier 12 in the treatment tank 14 can be made uniform.

【0016】図5は、本発明の好気性処理装置10によ
る別の散気方法を示したものであり、流入口18側のグ
ループから流出口22側グループにいくにしたがって散
気板26から散気される散気量が段階的に大きくなるよ
うに各グループの流量調整バルブ32を制御するように
したものである。即ち、各グループA〜Jのうち、流入
口18側のグループAからの散気量を最小にし、流出口
22側のグループJにいくにしたがって散気量を段第的
に大きくする散気方法を定常的に行うようにしたもので
ある。
FIG. 5 shows another air diffusion method by the aerobic treatment apparatus 10 of the present invention. The air diffusion plate 26 diffuses from the group on the inlet 18 side to the group on the outlet 22 side. The flow control valves 32 of each group are controlled so that the amount of diffused air gradually increases. That is, of the groups A to J, an air diffusion method in which the amount of air diffused from the group A on the inflow port 18 side is minimized, and the amount of air diffused gradually increases toward the group J on the outflow port 22 side. Is performed regularly.

【0017】この本発明の好気性処理装置による別の散
気方法によれば、図6に示すように処理槽14内には反
時計回りの旋回流(図6の矢印)が形成されるので、処
理槽14内に流入口18から流出口22に至る被処理水
の流れ(図6の実線)が形成されても、微生物担体12
が流出口22側に滞留することなく処理槽14全体に拡
散される。これにより、処理槽14内の微生物担体12
の濃度分布を均一化させることができる。
According to another aeration method using the aerobic treatment apparatus of the present invention, a counterclockwise swirling flow (arrow in FIG. 6) is formed in the treatment tank 14 as shown in FIG. Even if the flow of the water to be treated from the inlet 18 to the outlet 22 (solid line in FIG. 6) is formed in the treatment tank 14, the microorganism carrier 12
Is diffused throughout the processing tank 14 without staying at the outlet 22 side. Thereby, the microorganism carrier 12 in the treatment tank 14 is
Can be made uniform.

【0018】尚、本発明の実施の形態では、散気板のグ
ループをA〜Jの10グループにグループ化した例で説
明したが、このグループ数に限定されるものではない。
また、本発明の実施の形態では、処理槽の形状を直方体
状で説明したが、これに限定されるものではなく、処理
槽内において流入口から流出口に至る被処理水の流れが
形成される構造の処理槽であれば、本発明を適用するこ
とができる。
In the embodiment of the present invention, an example has been described in which the groups of diffuser plates are grouped into ten groups A to J, but the number of groups is not limited to this.
Further, in the embodiment of the present invention, the shape of the treatment tank is described as a rectangular parallelepiped.However, the present invention is not limited to this, and the flow of the water to be treated from the inlet to the outlet is formed in the treatment tank. The present invention can be applied to a processing tank having a structure as described above.

【0019】[0019]

【発明の効果】以上説明したように、本発明の好気性処
理装置によれば、処理槽内の微生物担体の濃度分布を均
一化させることができるので、被処理水と微生物担体と
の接触効率を向上させることができる。これにより、好
気性処理装置の性能を向上させることができる。
As described above, according to the aerobic treatment apparatus of the present invention, the concentration distribution of the microorganism carrier in the treatment tank can be made uniform, so that the contact efficiency between the water to be treated and the microorganism carrier is improved. Can be improved. Thereby, the performance of the aerobic treatment device can be improved.

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

【図1】本発明の好気性処理装置の全体構成を説明する
側面断面図
FIG. 1 is a side cross-sectional view illustrating an overall configuration of an aerobic treatment device of the present invention.

【図2】散気板のグループ分けの一例を説明した説明図FIG. 2 is an explanatory view illustrating an example of grouping of diffuser plates;

【図3】本発明の好気性処理装置による散気方法を説明
する説明図
FIG. 3 is an explanatory view for explaining an air diffusion method by the aerobic treatment device of the present invention.

【図4】本発明の好気性処理装置による散気方法を行っ
た時の処理槽内における微生物担体の濃度分布を説明す
る説明図
FIG. 4 is an explanatory view for explaining a concentration distribution of a microorganism carrier in a treatment tank when a diffuser method is performed by the aerobic treatment device of the present invention.

【図5】本発明の好気性処理装置による別の散気方法を
説明する説明図
FIG. 5 is an explanatory view for explaining another air diffusing method by the aerobic treatment device of the present invention.

【図6】本発明の好気性処理装置による別の散気方法を
行った時の処理槽内における被処理水の流動状態を説明
する説明図
FIG. 6 is an explanatory diagram for explaining a flow state of water to be treated in a treatment tank when another aeration method is performed by the aerobic treatment device of the present invention.

【符号の説明】[Explanation of symbols]

10…好気性処理装置 12…微生物担体 14…処理槽 16…散気装置 18…流入口 20…原水配管 22…流出口 24…処理水配管 26…散気板 27…スクリーン 28…コンプレッサ 30…エア供給ライン 32…流量調整バルブ DESCRIPTION OF SYMBOLS 10 ... Aerobic treatment apparatus 12 ... Microorganism carrier 14 ... Treatment tank 16 ... Aperture apparatus 18 ... Inlet 20 ... Raw water pipe 22 ... Outflow port 24 ... Treatment water pipe 26 ... Aperture plate 27 ... Screen 28 ... Compressor 30 ... Air Supply line 32: Flow control valve

───────────────────────────────────────────────────── フロントページの続き Fターム(参考) 4D003 AA12 AB02 BA02 CA02 CA07 DA11 DA18 DA20 EA01 FA05 4D028 BB02 BC12 BD06 CA09 CB08 ──────────────────────────────────────────────────続 き Continued on the front page F term (reference) 4D003 AA12 AB02 BA02 CA02 CA07 DA11 DA18 DA20 EA01 FA05 4D028 BB02 BC12 BD06 CA09 CB08

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】被処理水を流入口から流入して流出口から
流出させる間に微生物を固定化した多数の微生物担体と
接触させ前記被処理水を生物学的に処理する処理槽と、 前記処理槽内の底部に、前記被処理水中にエアを供給し
て好気性条件を形成する散気板を複数配設すると共に、
該複数の散気板にエアを供給するエア供給ラインを前記
流入口側の散気板から前記流出口側の散気板にかけて複
数のグループにグループ分けしたエア散気装置と、 前記各グループの散気板から散気される散気量をグルー
プごとに個別に制御する制御手段と、 を備えたことを特徴とする好気性処理装置。
A treatment tank for biologically treating the water to be treated by bringing microorganisms into contact with a number of microorganism carriers immobilized while the water to be treated flows in from an inlet and flows out from an outlet; At the bottom of the treatment tank, a plurality of diffuser plates are provided to supply air into the water to be treated and form aerobic conditions,
An air diffuser that divides an air supply line that supplies air to the plurality of diffuser plates from the diffuser plate on the inlet side to the diffuser plate on the outlet side into a plurality of groups; Control means for individually controlling the amount of air diffused from the air diffuser plate for each group, and an aerobic treatment device comprising:
【請求項2】前記各グループの散気板から散気される散
気量のうち、最大散気量のグループが時間の経過ととも
に流出口側から流入口側に順次変化するように前記制御
手段を制御することを特徴とする請求項1の好気性処理
装置。
2. The control means so that a group having a maximum amount of air diffused from the air diffuser plates of each of the groups sequentially changes from an outlet side to an inlet side with the passage of time. The aerobic treatment device according to claim 1, wherein
【請求項3】前記流入口側グループから前記流出口側グ
ループにいくにしたがって散気板から散気される散気量
が段階的に大きくなるように前記制御手段を制御するこ
とを特徴とする請求項1の好気性処理装置。
3. The control means is controlled such that the amount of air diffused from the air diffuser plate increases stepwise from the inlet side group to the outlet side group. The aerobic treatment device according to claim 1.
JP30731698A 1998-10-28 1998-10-28 Aerobic treatment equipment Expired - Lifetime JP3451964B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP30731698A JP3451964B2 (en) 1998-10-28 1998-10-28 Aerobic treatment equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP30731698A JP3451964B2 (en) 1998-10-28 1998-10-28 Aerobic treatment equipment

Publications (2)

Publication Number Publication Date
JP2000126790A true JP2000126790A (en) 2000-05-09
JP3451964B2 JP3451964B2 (en) 2003-09-29

Family

ID=17967688

Family Applications (1)

Application Number Title Priority Date Filing Date
JP30731698A Expired - Lifetime JP3451964B2 (en) 1998-10-28 1998-10-28 Aerobic treatment equipment

Country Status (1)

Country Link
JP (1) JP3451964B2 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2018164894A (en) * 2017-03-28 2018-10-25 住友重機械エンバイロメント株式会社 Arrangement method of water treatment system and diffuser
JPWO2020161825A1 (en) * 2019-02-06 2021-04-30 三菱電機株式会社 Water treatment equipment and water treatment method
JP2022027846A (en) * 2019-02-06 2022-02-14 三菱電機株式会社 Water treatment apparatus and water treatment method

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2018164894A (en) * 2017-03-28 2018-10-25 住友重機械エンバイロメント株式会社 Arrangement method of water treatment system and diffuser
JPWO2020161825A1 (en) * 2019-02-06 2021-04-30 三菱電機株式会社 Water treatment equipment and water treatment method
JP2022027846A (en) * 2019-02-06 2022-02-14 三菱電機株式会社 Water treatment apparatus and water treatment method
JP7282149B2 (en) 2019-02-06 2023-05-26 三菱電機株式会社 Water treatment device and water treatment method
JP7424997B2 (en) 2019-02-06 2024-01-30 三菱電機株式会社 water treatment equipment

Also Published As

Publication number Publication date
JP3451964B2 (en) 2003-09-29

Similar Documents

Publication Publication Date Title
US7563363B2 (en) System for treating wastewater
US7794599B2 (en) Bioreactor system for multi-stage biological wastewater treatment
KR101884448B1 (en) advanced water treating apparatus using ozone
CN107265636A (en) A kind of BBE biological high-efficiencies processing pond
JP3451964B2 (en) Aerobic treatment equipment
KR101879740B1 (en) Advanced water-treating apparatus
KR101617426B1 (en) Advanced water-treating apparatus
KR101044826B1 (en) An operation method to increase advanced treatment efficiency in membrane bio reacter and an advanced treatment appartus there of
KR102289941B1 (en) water treating apparatus for sewage and wastewater
JPH04135699A (en) Biological treating device
CN213771729U (en) Sewage biochemical treatment system with multiple process modes
CN205061691U (en) Biological sewage treatment system of not sectionalized membrane
JPS5912797A (en) Intermittently aerating denitrification device
CN209602205U (en) MBR integrated sewage disposal reactor
JP7002977B2 (en) Wastewater treatment equipment
JP3269722B2 (en) Sewage treatment tank
CN204958685U (en) MBR sewage processor
JPH1170391A (en) Waste water treatment method and apparatus therefor
CN113845212B (en) MBR integrated sewage purification device and method
CN211570249U (en) Multistage A-O-MBR sewage treatment system of segmentation water intaking
CN109133352A (en) A kind of integral type nitrogen removing device and denitrogenate method
JPH05220491A (en) Waste water treating equipment
JP2023151175A (en) Operation control system of aerator
CN104761103B (en) Sewage treatment device and method
JPH06304588A (en) Waste water treatment by biological membrane method

Legal Events

Date Code Title Description
S533 Written request for registration of change of name

Free format text: JAPANESE INTERMEDIATE CODE: R313533

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20080718

Year of fee payment: 5

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090718

Year of fee payment: 6

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090718

Year of fee payment: 6

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20100718

Year of fee payment: 7