JP2002205095A - Sludge transporting apparatus - Google Patents

Sludge transporting apparatus

Info

Publication number
JP2002205095A
JP2002205095A JP2001000890A JP2001000890A JP2002205095A JP 2002205095 A JP2002205095 A JP 2002205095A JP 2001000890 A JP2001000890 A JP 2001000890A JP 2001000890 A JP2001000890 A JP 2001000890A JP 2002205095 A JP2002205095 A JP 2002205095A
Authority
JP
Japan
Prior art keywords
sludge
pipe
tank
discharge
air
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
JP2001000890A
Other languages
Japanese (ja)
Other versions
JP4618899B2 (en
Inventor
Yasunobu Okajima
康信 岡島
Masaharu Nurishi
雅治 塗師
Tatsuya Uejima
達也 上島
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.)
Kubota Corp
Original Assignee
Kubota 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 Kubota Corp filed Critical Kubota Corp
Priority to JP2001000890A priority Critical patent/JP4618899B2/en
Publication of JP2002205095A publication Critical patent/JP2002205095A/en
Application granted granted Critical
Publication of JP4618899B2 publication Critical patent/JP4618899B2/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

Abstract

PROBLEM TO BE SOLVED: To provide a sludge transporting apparatus, in which the clogging of a diffuser is prevented and failure hardly occurs. SOLUTION: The sludge transporting apparatus has a sludge transporting pipe 3 dipped in a vessel, arranged in a horizontal direction and communicating with a blower 6 at the base end side, plural sludge suction pipes 4 communicating with the sludge transporting pipe 3 and formed so that each tip part extended on both sides of the sludge transporting pipe 3 is opened at the lower position of the sludge transporting pipe 3 as a sludge suction port 5, a sludge discharge pipe 7 communicating with the tip part side of the sludge transporting pipe 3 at one end and opened at another end as a discharge port 9 to the outside and a discharge valve 10 provided in the sludge discharge pipe 7.

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、汚泥移送装置に関
し、膜分離活性汚泥法等において槽内混合液もしくは余
剰汚泥を移送する技術に係るものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a sludge transfer apparatus, and more particularly to a technique for transferring a mixed liquid in a tank or excess sludge in a membrane separation activated sludge method or the like.

【0002】[0002]

【従来の技術】従来、汚水処理施設は前処理槽、流量調
整槽、脱窒槽、硝化槽、処理水槽などを各機能毎に別途
の槽として有しており、これらの多くには汚水攪拌用の
散気装置と汚水移送用ポンプを設置し、例えば脱窒槽の
槽内混合液をポンプで硝化槽へ供給し、あるいは硝化槽
の槽内混合液をポンプで脱窒槽へ返送している。
2. Description of the Related Art Conventionally, a sewage treatment facility has a pretreatment tank, a flow control tank, a denitrification tank, a nitrification tank, a treatment water tank, and the like as separate tanks for each function. For example, an aeration device and a sewage transfer pump are installed. For example, a liquid mixture in a tank of a denitrification tank is supplied to a nitrification tank by a pump, or a liquid mixture in a tank of a nitrification tank is returned to a denitrification tank by a pump.

【0003】また、膜分離活性法では、硝化槽に膜分離
装置を浸漬し、膜分離装置の下方に配置した散気装置か
ら空気を散気し、空気のエアリフト作用で生起する固気
液混合の上向流によって膜面を洗浄している。
In the membrane separation activation method, a membrane separation device is immersed in a nitrification tank, air is diffused from an air diffuser arranged below the membrane separation device, and a solid-gas-liquid mixture generated by an air lift action of the air. The membrane surface is washed by upward flow.

【0004】[0004]

【発明が解決しようとする課題】しかし、上記した構成
において、移送ポンプや散気装置が故障すると機能不全
となるので、定期的なメンテナンスによってその故障を
未然に防止することが必要となる。
However, in the above configuration, if the transfer pump or the air diffuser breaks down, it will malfunction, so it is necessary to prevent the breakdown by regular maintenance.

【0005】本発明は上記した課題を解決するものであ
り、散気装置の閉塞を未然に防止するとともに、機械的
構成要素が少なく簡略な構造を有することで故障の発生
し難い汚泥移送装置を提供することを目的とする。
The present invention has been made to solve the above-mentioned problems, and it is an object of the present invention to provide a sludge transfer device which prevents the air diffuser from being obstructed, and has a simple structure with few mechanical components, so that it is difficult to cause a failure. The purpose is to provide.

【0006】[0006]

【課題を解決するための手段】上記課題を解決するため
に、請求項1に係る本発明の汚泥移送装置は、槽内に浸
漬して水平方向に配置し、基端側が空気供給源に連通す
るとともに、下面に複数の汚泥吸込口を有する汚泥移送
管と、一端が汚泥移送管の先端側に連通するとともに、
他端が槽外に排出口として開口する汚泥排出管と、汚泥
排出管に設けた排出バルブとを有するものである。
According to a first aspect of the present invention, there is provided a sludge transfer device according to the present invention, wherein the sludge transfer device is immersed in a tank and arranged in a horizontal direction, and has a base end communicating with an air supply source. And a sludge transfer pipe having a plurality of sludge suction ports on the lower surface, and one end communicating with the tip side of the sludge transfer pipe,
It has a sludge discharge pipe whose other end opens as a discharge port outside the tank, and a discharge valve provided on the sludge discharge pipe.

【0007】上記した構成により、汚泥移送時には、汚
泥移送管に空気源から所定圧力の空気を供給する状態で
排出バルブを開栓し、汚泥移送管に供給する空気を汚泥
排出管を通して排出口から排出する。
[0007] With the above configuration, at the time of sludge transfer, the discharge valve is opened while supplying air at a predetermined pressure from the air source to the sludge transfer pipe, and the air supplied to the sludge transfer pipe is discharged from the discharge port through the sludge discharge pipe. Discharge.

【0008】このとき、排出口が汚泥移送管の上方位置
に開口し、汚泥吸込口が汚泥移送管の下方位置に開口す
ることで、空気の流れの主流がより抵抗の小さい排出口
へ向かうことになり、管内の静圧の低下による管外の汚
泥吸込口近傍との圧力差によって余剰汚泥もしくは槽内
混合液が汚泥吸込口を通して汚泥移送管内に流入し、流
入した槽内混合液は空気とともに汚泥排出管を通って排
出口から排出される。
[0008] At this time, since the discharge port is opened at a position above the sludge transfer pipe and the sludge suction port is opened at a position below the sludge transfer pipe, the main flow of air flows toward the discharge port with lower resistance. Due to the pressure difference between the outside of the pipe and the vicinity of the sludge suction port due to the decrease in the static pressure inside the pipe, excess sludge or the mixed liquid in the tank flows into the sludge transfer pipe through the sludge suction port, and the mixed liquid in the tank together with air It is discharged from the discharge port through the sludge discharge pipe.

【0009】一方、排出バルブを閉栓した状態では、空
気源から所定圧力で供給する空気が汚泥移送管の汚泥吸
込口を通して槽内に噴出し、汚泥移送管に残留する槽内
混合液が管外へ排出される。汚泥吸込口から噴出する空
気は槽内混合液を曝気する曝気空気として作用するの
で、別途に散気装置を設ける必要がない。また、散気に
よって汚泥吸込口の付近で汚泥が乾燥して閉塞の原因と
なるが、この乾燥した汚泥は汚泥移送時に洗浄される。
On the other hand, when the discharge valve is closed, air supplied at a predetermined pressure from the air source is blown into the tank through the sludge suction port of the sludge transfer pipe, and the mixed liquid remaining in the sludge transfer pipe is discharged outside the pipe. Is discharged to The air ejected from the sludge suction port acts as aeration air for aerating the mixed solution in the tank, so that there is no need to provide a separate air diffuser. Further, the diffused air dries the sludge in the vicinity of the sludge suction port and causes blockage. The dried sludge is washed when the sludge is transferred.

【0010】つまり、汚泥移送時に汚泥移送管内では槽
内混合液が空気の通気を阻害する抵抗として作用し、空
気の流れが脈動して汚泥移送管内の圧力が急激な増減を
繰り返して変化するので、汚泥排出管の排出口から空気
と槽内混合液が断続的に排出されるとともに、汚泥吸込
口を通して汚泥移送管内に汚泥が断続的に流入する。
That is, when the sludge is transferred, the mixed liquid in the tank acts as a resistance to impede the air flow in the sludge transfer pipe, and the air flow pulsates, and the pressure in the sludge transfer pipe repeatedly changes rapidly. At the same time, the air and the mixture in the tank are intermittently discharged from the discharge port of the sludge discharge pipe, and the sludge intermittently flows into the sludge transfer pipe through the sludge suction port.

【0011】この汚泥吸込口を通した急速な槽内混合液
の流入が反復的に生じることで、汚泥移送管の内部に付
着した汚泥を効果的に洗浄する。汚泥移送管の内部に付
着した汚泥は散気時の空気によって乾燥しているが、槽
内混合液が汚泥に浸潤することで汚泥の剥離を促進し、
剥離した汚泥は槽内混合液とともに空気の排出に伴って
排出口から排出する。
The sludge adhering to the inside of the sludge transfer pipe is effectively washed by the repetitive flow of the mixed liquid in the tank through the sludge suction port repeatedly. Sludge adhering to the inside of the sludge transfer pipe is dried by the air at the time of aeration, but the mixed solution in the tank infiltrates the sludge to promote sludge separation,
The separated sludge is discharged from the discharge port together with the mixed liquid in the tank with the discharge of air.

【0012】したがって、汚泥移送時に汚泥吸込口、汚
泥移送管の内部を洗浄できるので、乾燥性汚泥による閉
塞を未然に防止することができ、汚泥移送と散気を交互
に行うことで特別なメンテナンスを要することなく汚泥
の移送および散気を常に円滑に行うことができる。
Therefore, the sludge suction port and the inside of the sludge transfer pipe can be washed when transferring the sludge, so that the obstruction due to the drying sludge can be prevented beforehand, and the special maintenance is performed by alternately performing the transfer of the sludge and the air diffusion. It is possible to always smoothly transfer and diffuse the sludge without the need for the above.

【0013】請求項2に係る本発明の汚泥移送装置は、
槽内に浸漬して水平方向に配置し、基端側が空気供給源
に連通する汚泥移送管と、汚泥移送管に連通するととも
に、汚泥移送管の両側に張り出す各先端が汚泥移送管の
下方位置で汚泥吸込口として開口する複数の汚泥吸込管
と、一端が汚泥移送管の先端側に連通するとともに、他
端が槽外に排出口として開口する汚泥排出管と、汚泥排
出管に設けた排出バルブとを有するものである。
[0013] The sludge transfer device of the present invention according to claim 2 comprises:
The sludge transfer pipe is immersed in the tank and placed horizontally, and the base end communicates with the air supply source, and the sludge transfer pipe communicates with the sludge transfer pipe. A plurality of sludge suction pipes that open as sludge suction ports at positions, a sludge discharge pipe having one end communicating with the tip side of the sludge transfer pipe, and another end opening as a discharge port outside the tank, and a sludge discharge pipe are provided. And a discharge valve.

【0014】上記した構成により、汚泥移送時には、汚
泥移送管に空気源から所定圧力の空気を供給する状態で
排出バルブを開栓し、汚泥移送管に供給する空気を汚泥
排出管を通して排出口から排出する。
With the above configuration, when transferring sludge, the discharge valve is opened while supplying air of a predetermined pressure from the air source to the sludge transfer pipe, and the air supplied to the sludge transfer pipe is discharged from the discharge port through the sludge discharge pipe. Discharge.

【0015】このとき、排出口が汚泥移送管の上方位置
に開口し、汚泥吸込管の汚泥吸込口が汚泥移送管の下方
位置に開口することで、空気の流れの主流がより抵抗の
小さい排出口へ向かうことになり、管内の静圧の低下に
よる汚泥吸込口近傍との圧力差によって余剰汚泥もしく
は槽内混合液が汚泥吸込口を通して汚泥吸込管および汚
泥移送管内に流入し、流入した槽内混合液は空気ととも
に汚泥排出管を通って排出口から排出される。
At this time, the discharge port is opened at a position above the sludge transfer pipe, and the sludge suction port of the sludge suction pipe is opened at a position below the sludge transfer pipe, so that the main flow of air flow has a smaller resistance. The excess sludge or the mixed liquid in the tank flows into the sludge suction pipe and the sludge transfer pipe through the sludge suction port due to a pressure difference between the sludge suction port and the vicinity of the sludge suction port due to a decrease in the static pressure in the pipe. The mixed solution is discharged from the outlet through the sludge discharge pipe together with air.

【0016】汚泥吸込管が汚泥移送管の両側へ張り出す
ことで汚泥吸込口が槽内に広く分散して存在するので、
槽底部に沈降した汚泥を広い範囲にわたって均一に吸い
込むことができる。
Since the sludge suction pipe protrudes to both sides of the sludge transfer pipe, the sludge suction ports are widely dispersed in the tank.
Sludge settled at the bottom of the tank can be uniformly sucked over a wide range.

【0017】一方、排出バルブを閉栓した状態では、空
気源から所定圧力で供給する空気が汚泥吸込管の汚泥吸
込口を通して槽内に噴出し、汚泥移送管および汚泥吸込
管に残留する槽内混合液が管外へ排出される。汚泥吸込
口から噴出する空気は槽内混合液を曝気する曝気空気と
して作用し、汚泥吸込管が汚泥移送管の両側へ張り出す
ことで汚泥吸込口が槽内に広く分散して存在するので、
広い範囲にわたって均一な曝気を行うことができ、別途
に散気装置を設ける必要がない。また、散気によって汚
泥吸込口の付近で汚泥が乾燥して閉塞の原因となるが、
この乾燥した汚泥は汚泥移送時に洗浄される。
On the other hand, when the discharge valve is closed, air supplied from the air source at a predetermined pressure is blown into the tank through the sludge suction port of the sludge suction pipe, and the mixing in the tank remaining in the sludge transfer pipe and the sludge suction pipe is performed. The liquid is discharged out of the tube. The air spouted from the sludge suction port acts as aeration air to aerate the mixed liquid in the tank, and the sludge suction pipe protrudes to both sides of the sludge transfer pipe so that the sludge suction port is widely dispersed in the tank.
Uniform aeration can be performed over a wide range, and there is no need to provide a separate diffuser. Also, the sludge dries near the sludge suction port due to aeration and causes blockage,
The dried sludge is washed when transferring the sludge.

【0018】つまり、汚泥移送時に汚泥移送管内では槽
内混合液が空気の通気を阻害する抵抗として作用し、空
気の流れが脈動して汚泥移送管内の圧力が急激な増減を
繰り返して変化するので、汚泥排出管の排出口から空気
と槽内混合液が断続的に排出されるとともに、汚泥吸込
口を通して汚泥吸込管および汚泥移送管内に汚泥が断続
的に流入する。
In other words, the liquid mixture in the tank acts as a resistance to impede the air flow in the sludge transfer pipe during sludge transfer, and the air flow pulsates and the pressure in the sludge transfer pipe repeatedly changes rapidly. In addition, the air and the mixture in the tank are intermittently discharged from the outlet of the sludge discharge pipe, and the sludge intermittently flows into the sludge suction pipe and the sludge transfer pipe through the sludge suction port.

【0019】この汚泥吸込口を通した急速な槽内混合液
の流入が反復的に生じることで、汚泥吸込管の内部に付
着した汚泥を効果的に洗浄する。汚泥吸込管の内部に付
着した汚泥は散気時の空気によって乾燥しているが、槽
内混合液が汚泥に浸潤することで汚泥の剥離を促進し、
剥離した汚泥は槽内混合液とともに空気の排出に伴って
排出口から排出する。
The sludge adhering to the inside of the sludge suction pipe is effectively washed by the repetitive flow of the mixed liquid in the tank through the sludge suction port repeatedly. Sludge adhering to the inside of the sludge suction pipe is dried by the air at the time of aeration, but the mixed solution in the tank infiltrates the sludge to promote sludge separation,
The separated sludge is discharged from the discharge port together with the mixed liquid in the tank with the discharge of air.

【0020】したがって、汚泥移送時に汚泥吸込口、汚
泥吸込管、汚泥移送管の内部を洗浄できるので、乾燥性
汚泥による閉塞を未然に防止することができ、汚泥移送
と散気を交互に行うことで特別なメンテナンスを要する
ことなく汚泥の移送および散気を常に円滑に行うことが
できる。
Therefore, the sludge suction port, the sludge suction pipe, and the inside of the sludge transfer pipe can be washed during the transfer of the sludge, so that the obstruction due to the drying sludge can be prevented beforehand, and the transfer of the sludge and the air diffusion are performed alternately. Thus, the transfer and the air diffusion of the sludge can be always performed smoothly without requiring any special maintenance.

【0021】請求項3に係る本発明の汚泥移送装置は、
汚泥排出管が他端に排出口とは別途に排気バルブを介し
て分岐した排気管を有し、排気管が槽内の液面上もしく
は液中に排気口として開口するものである。
The sludge transfer device of the present invention according to claim 3 is
The sludge discharge pipe has, at the other end, an exhaust pipe branched via an exhaust valve separately from the discharge port, and the exhaust pipe opens as an exhaust port on the liquid surface in the tank or in the liquid.

【0022】上記した構成により、排気バルブを閉栓し
た状態で排出バルブを開栓することで汚泥移送を行い、
排出バルブおよび排気バルブを閉栓することで散気を行
い、排出バルブを閉栓した状態で排気バルブを開栓する
ことで洗浄のみを行う。
With the above configuration, sludge transfer is performed by opening the discharge valve while the exhaust valve is closed,
Aeration is performed by closing the discharge valve and the exhaust valve, and only cleaning is performed by opening the exhaust valve with the discharge valve closed.

【0023】[0023]

【発明の実施の形態】以下、本発明の実施の形態を図面
に基づいて説明する。図1〜図4において、硝化槽(曝
気槽)1の内部には散気装置を兼ねた汚泥移送装置2と
汚泥移送装置2の上部に配置する膜分離装置1aとを浸
漬している。膜分離装置1aは硝化槽1に必須のもので
はないが、本実施の形態に係る膜分離活性汚泥法では活
性汚泥の分離手段として使用する。
Embodiments of the present invention will be described below with reference to the drawings. In FIG. 1 to FIG. 4, a sludge transfer device 2 also serving as a diffuser and a membrane separation device 1 a disposed above the sludge transfer device 2 are immersed in a nitrification tank (aeration tank) 1. The membrane separation device 1a is not essential for the nitrification tank 1, but is used as a means for separating activated sludge in the membrane separation activated sludge method according to the present embodiment.

【0024】膜分離装置1aは、例えば有機平膜形、チ
ューブ形、セラミック形の各種の分離膜を使用すること
ができるが、ここでは有機平膜形の分離膜を使用した複
数の膜カートリッジを鉛直方向に沿って、かつ所定間隔
をあけて平行に配置したものであり、隣接する膜カート
リッジ間に流路を形成している。各膜カートリッジは膜
透過液流路(図示省略)に連通し、槽内の水頭(重力)
もしくはポンプ吸引圧を駆動圧として作動する。
The membrane separation device 1a can use various types of separation membranes, for example, an organic flat membrane type, a tube type, and a ceramic type. Here, a plurality of membrane cartridges using the organic flat membrane type separation membrane are used. They are arranged in parallel in the vertical direction and at a predetermined interval, and form a flow path between adjacent membrane cartridges. Each membrane cartridge communicates with a membrane permeate flow path (not shown), and the water head (gravity) in the tank
Alternatively, it operates using the pump suction pressure as the driving pressure.

【0025】汚泥移送装置2は水平方向に配置した所定
口径の大径管からなる汚泥移送管3と、汚泥移送管3の
下方に配置した所定口径の小径管からなる複数の汚泥吸
込管4とからなる。汚泥吸込管4は逆T字形をなし、上
部の一端で汚泥移送管3に連通するとともに、汚泥移送
管3の両側に張り出した両側の先端が汚泥吸込口5とし
て開口している。
The sludge transfer device 2 includes a sludge transfer pipe 3 formed of a large-diameter pipe having a predetermined diameter disposed horizontally and a plurality of sludge suction pipes 4 formed of a small-diameter pipe having a predetermined diameter disposed below the sludge transfer pipe 3. Consists of The sludge suction pipe 4 has an inverted T-shape, communicates with the sludge transfer pipe 3 at one upper end, and has both ends protruding on both sides of the sludge transfer pipe 3 opening as sludge suction ports 5.

【0026】本実施の形態では汚泥吸込管4に汚泥吸込
口5を設けているが、図5に示すように、汚泥移送管3
の下面に汚泥吸込口5を直接に設けることも可能であ
る。汚泥移送管3は基端側が空気供給源であるブロア6
に連通しており、先端側に汚泥排出管7を接続してい
る。汚泥排出管7は先端側が脱窒槽(もしくは汚泥貯留
槽)8の内部において汚泥移送管3の上方位置で排出口
9として開口しており、途中に排出バルブ10を設けて
いる。汚泥排出管7は排出口9とは別途に排気バルブ1
1を介して分岐した排気管12を有し、排気管12は硝
化槽1の内部の液面上に排気口13として開口してい
る。本実施の形態では排気口13が水面上の大気圧下に
開口しているが、排気口13を水面下に配置することも
可能である。
In this embodiment, the sludge suction pipe 4 is provided with the sludge suction port 5, but as shown in FIG.
It is also possible to provide the sludge suction port 5 directly on the lower surface of the. The sludge transfer pipe 3 has a blower 6 whose base end is an air supply source.
And a sludge discharge pipe 7 is connected to the tip side. The sludge discharge pipe 7 has an opening at the tip side as a discharge port 9 at a position above the sludge transfer pipe 3 inside a denitrification tank (or a sludge storage tank) 8, and a discharge valve 10 is provided in the middle. The sludge discharge pipe 7 is provided separately from the discharge port 9 with the exhaust valve 1
1, the exhaust pipe 12 is opened as an exhaust port 13 on the liquid level inside the nitrification tank 1. In the present embodiment, the exhaust port 13 is opened under atmospheric pressure above the water surface, but it is also possible to arrange the exhaust port 13 below the water surface.

【0027】以下、上記した構成における作用を説明す
る。汚泥移送時には、排気バルブ11を閉栓した状態で
排出バルブ10を開栓し、汚泥移送管3にブロア6から
所定圧力の空気を供給し、汚泥移送管3に供給する空気
を汚泥排出管7を通して排出口9から排出する。
The operation of the above configuration will be described below. At the time of sludge transfer, the discharge valve 10 is opened with the exhaust valve 11 closed, air of a predetermined pressure is supplied to the sludge transfer pipe 3 from the blower 6, and air supplied to the sludge transfer pipe 3 is passed through the sludge discharge pipe 7. It is discharged from the discharge port 9.

【0028】このとき、排出口9が汚泥移送管7の上方
位置に開口し、汚泥吸込管4の汚泥吸込口5が汚泥移送
管3の下方位置に開口することで、空気の流れがより抵
抗の小さい排出口9へ向かうことになり、図3に示すよ
うに、圧力差P0−P1によって硝化槽1の槽内混合液
(もしくは余剰汚泥)が汚泥吸込口5を通して汚泥吸込
管4および汚泥移送管3の内部に流入し、流入した槽内
混合液は空気とともに汚泥排出管7を通って排出口9か
ら脱窒槽8へ排出される。
At this time, the discharge port 9 opens at a position above the sludge transfer pipe 7 and the sludge suction port 5 of the sludge suction pipe 4 opens at a position below the sludge transfer pipe 3, so that the flow of air is reduced. As shown in FIG. 3, the mixed liquid (or excess sludge) in the nitrification tank 1 passes through the sludge suction port 5 and the sludge suction pipe 4 and the sludge transfer as shown in FIG. 3 due to the pressure difference P0-P1. The mixed liquid in the tank which flows into the pipe 3 and flows into the pipe 3 is discharged to the denitrification tank 8 from the discharge port 9 through the sludge discharge pipe 7 together with air.

【0029】汚泥吸込管4は汚泥移送管3の両側へ張り
出しているので汚泥吸込口5が硝化槽1の槽底部に広く
分散して存在することになり、槽底部に沈降した汚泥を
広い範囲にわたって均一に吸い込むことができる。
Since the sludge suction pipe 4 projects on both sides of the sludge transfer pipe 3, the sludge suction ports 5 are widely dispersed at the bottom of the nitrification tank 1, and the sludge settled at the bottom of the nitrification tank 1 is spread over a wide area. Can be inhaled uniformly.

【0030】一方、排出バルブ10および排気バルブ1
1を閉栓した状態では、ブロア6から所定圧力で供給す
る空気が汚泥吸込管4の汚泥吸込口5を通して硝化槽1
の内部に噴出し、汚泥移送管3および汚泥吸込管4に残
留する槽内混合液が管外へ排出される。
On the other hand, the exhaust valve 10 and the exhaust valve 1
1 is closed, air supplied at a predetermined pressure from the blower 6 flows through the sludge suction port 5 of the sludge suction pipe 4 to the nitrification tank 1.
And the mixed liquid in the tank remaining in the sludge transfer pipe 3 and the sludge suction pipe 4 is discharged out of the pipe.

【0031】汚泥吸込口5から噴出する空気は槽内混合
液を曝気する曝気空気として作用し、汚泥吸込管4が汚
泥移送管3の両側へ張り出すことで汚泥吸込口5が槽内
に広く分散して存在するので、広い範囲にわたって均一
な曝気を行うことができ、別途に散気装置を設ける必要
がない。
The air ejected from the sludge suction port 5 acts as aeration air for aerated the mixed solution in the tank, and the sludge suction pipe 4 projects to both sides of the sludge transfer pipe 3 so that the sludge suction port 5 is widened in the tank. Since they are dispersed, uniform aeration can be performed over a wide range, and there is no need to separately provide an air diffuser.

【0032】また、散気によって汚泥吸込口5の付近で
汚泥が乾燥して閉塞の原因となるが、この乾燥した汚泥
は汚泥移送時に洗浄される。つまり、汚泥移送時に汚泥
移送管3の内部では槽内混合液が空気の通気を阻害する
抵抗として作用し、空気の流れが脈動して汚泥移送管3
の内部圧力が急激な増減を繰り返して変化するので、汚
泥排出管7の排出口9から空気と槽内混合液が断続的に
排出されるとともに、汚泥吸込口5を通して汚泥吸込管
4および汚泥移送管3の内部に汚泥が断続的に流入す
る。
Further, the sludge dries near the sludge suction port 5 due to the aeration and causes a blockage. The dried sludge is washed when the sludge is transferred. In other words, the liquid mixture in the tank acts as a resistance to impede the ventilation of air inside the sludge transfer pipe 3 during the sludge transfer, and the air flow pulsates and the sludge transfer pipe 3
Since the internal pressure of the sludge repeatedly changes rapidly, air and the mixture in the tank are intermittently discharged from the discharge port 9 of the sludge discharge pipe 7, and the sludge suction pipe 4 and the sludge transfer through the sludge suction port 5. Sludge intermittently flows into the pipe 3.

【0033】この汚泥吸込口5を通した急速な槽内混合
液の流入が反復的に生じることで、汚泥吸込管4の内部
に付着した汚泥を効果的に洗浄する。汚泥吸込管4の内
部に付着した汚泥は散気時の空気によって乾燥している
が、槽内混合液が汚泥に浸潤することで汚泥の剥離を促
進し、剥離した汚泥は槽内混合液とともに空気の排出に
伴って排出口9から排出する。
The rapid inflow of the mixture in the tank through the sludge suction port 5 repeatedly causes the sludge adhering to the inside of the sludge suction pipe 4 to be effectively washed. The sludge adhering to the inside of the sludge suction pipe 4 is dried by air at the time of aeration, but the mixed liquid in the tank infiltrates the sludge to promote the separation of the sludge, and the separated sludge is mixed with the mixed liquid in the tank. The air is discharged from the discharge port 9 as the air is discharged.

【0034】したがって、汚泥移送時に汚泥吸込口5、
汚泥吸込管4、汚泥移送管3の内部を洗浄できるので、
乾燥性汚泥による閉塞を未然に防止することができ、汚
泥移送と散気を交互に行うことで特別なメンテナンスを
要することなく汚泥の移送および散気を常に円滑に行う
ことができ、移送機能を簡略な構造で実現するので故障
を低減して維持管理費を抑制することができる。
Therefore, the sludge suction port 5,
Since the inside of the sludge suction pipe 4 and the sludge transfer pipe 3 can be washed,
Blockage due to drying sludge can be prevented beforehand, and sludge transfer and air diffusion are performed alternately, so that sludge transfer and air diffusion can be performed smoothly without any special maintenance, and the transfer function can be performed. Since it is realized with a simple structure, failures can be reduced and maintenance costs can be reduced.

【0035】また、必要であれば、排出バルブ10を閉
栓した状態で排気バルブ11を開栓することで、汚泥吸
込口5から吸い込んだ槽内混合液を汚泥吸込管4、汚泥
移送管3、排気管12を通して排気口13から硝化槽1
に排出し、洗浄のみを行うこともできる。
If necessary, by opening the exhaust valve 11 with the discharge valve 10 closed, the mixed liquid in the tank sucked from the sludge suction port 5 is fed to the sludge suction pipe 4, the sludge transfer pipe 3, Nitrification tank 1 from exhaust port 13 through exhaust pipe 12
And only washing can be performed.

【0036】また、遠隔地から操作する場合には液位計
を脱窒槽8に設け、その変位を通信回線を通して検出す
ることで汚泥移送の有無を確認し、水位変動や汚泥粘度
上昇などによって汚泥移送および管内洗浄が行われない
状態を回避する。
When operating from a remote place, a liquid level gauge is provided in the denitrification tank 8, and its displacement is detected through a communication line to confirm the presence or absence of sludge transfer. Avoid situations where transfer and flushing are not performed.

【0037】また、自動化を行う場合には、各バルブを
電動弁もしくは電磁弁とし、タイマー等で開閉時間を制
御して汚泥の移送量を設定する。
When automation is performed, each valve is an electric valve or a solenoid valve, and the opening and closing time is controlled by a timer or the like to set the amount of sludge to be transferred.

【0038】[0038]

【発明の効果】以上のように本発明によれば、汚泥移送
時には汚泥吸込口を通して槽内混合液を吸い込んで移送
することができ、汚泥吸込管が汚泥移送管の両側へ張り
出して汚泥吸込口が槽内に広く分散して存在することで
槽底部に沈降した汚泥を広い範囲にわたって均一に吸い
込むことができ、排出バルブを閉栓した状態で汚泥吸込
口から噴出する空気で槽内混合液を曝気することができ
るので別途に散気装置を設ける必要がなく、汚泥移送時
に管内部を洗浄できるので汚泥移送と散気を交互に行う
ことで特別なメンテナンスを要することなく汚泥の移送
および散気を常に円滑に行うことができる。
As described above, according to the present invention, at the time of sludge transfer, the mixed liquid in the tank can be sucked and transferred through the sludge suction port, and the sludge suction pipe projects to both sides of the sludge transfer pipe and the sludge suction port. Is widely dispersed in the tank so that the sludge settled at the bottom of the tank can be sucked in uniformly over a wide range, and the mixed liquid in the tank is aerated with the air ejected from the sludge suction port with the discharge valve closed. It is not necessary to provide a separate air diffuser, and the inside of the pipe can be washed at the time of transferring the sludge. It can always be done smoothly.

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

【図1】本発明の実施の形態における汚泥移送装置を示
す正面図である。
FIG. 1 is a front view showing a sludge transfer device according to an embodiment of the present invention.

【図2】同汚泥移送装置の斜視図である。FIG. 2 is a perspective view of the sludge transfer device.

【図3】同汚泥移送装置の要部断面図である。FIG. 3 is a sectional view of a main part of the sludge transfer device.

【図4】同汚泥移送装置の要部拡大図である。FIG. 4 is an enlarged view of a main part of the sludge transfer device.

【図5】本発明の他の実施の形態における汚泥移送装置
の要部拡大図である。
FIG. 5 is an enlarged view of a main part of a sludge transfer device according to another embodiment of the present invention.

【符号の説明】[Explanation of symbols]

1 硝化槽(曝気槽) 1a 膜分離装置 2 汚泥移送装置 3 汚泥移送管 4 汚泥吸込管 5 汚泥吸込口 6 ブロア 7 汚泥排出管 8 脱窒槽(もしくは汚泥貯留槽) 9 排出口 10 排出バルブ 11 排気バルブ 12 排気管 13 排気口 DESCRIPTION OF SYMBOLS 1 Nitrification tank (aeration tank) 1a Membrane separation apparatus 2 Sludge transfer apparatus 3 Sludge transfer pipe 4 Sludge suction pipe 5 Sludge suction port 6 Blower 7 Sludge discharge pipe 8 Denitrification tank (or sludge storage tank) 9 Discharge port 10 Discharge valve 11 Exhaust Valve 12 Exhaust pipe 13 Exhaust port

フロントページの続き (72)発明者 上島 達也 大阪府大阪市浪速区敷津東一丁目2番47号 株式会社クボタ内 Fターム(参考) 4D028 BC11 BC24 BC26 4D029 AA01 AB07 DD01 4D059 AA04 CB01 Continuation of the front page (72) Inventor Tatsuya Uejima 2-47 Shishizu Higashi, Namiwa-ku, Osaka-shi, Osaka F-term in Kubota Corporation (Reference) 4D028 BC11 BC24 BC26 4D029 AA01 AB07 DD01 4D059 AA04 CB01

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 槽内に浸漬して水平方向に配置し、基端
側が空気供給源に連通するとともに、下面に複数の汚泥
吸込口を有する汚泥移送管と、一端が汚泥移送管の先端
側に連通するとともに、他端が槽外に排出口として開口
する汚泥排出管と、汚泥排出管に設けた排出バルブとを
有することを特徴とする汚泥移送装置。
1. A sludge transfer pipe having a plurality of sludge suction ports on its lower surface and a bottom end communicating with an air supply source, and one end of the sludge transfer pipe being immersed in a tank and arranged horizontally. And a sludge discharge pipe having the other end open as a discharge port outside the tank, and a discharge valve provided on the sludge discharge pipe.
【請求項2】 槽内に浸漬して水平方向に配置し、基端
側が空気供給源に連通する汚泥移送管と、汚泥移送管に
連通するとともに、汚泥移送管の両側に張り出す各先端
が汚泥移送管の下方位置で汚泥吸込口として開口する複
数の汚泥吸込管と、一端が汚泥移送管の先端側に連通す
るとともに、他端が槽外に排出口として開口する汚泥排
出管と、汚泥排出管に設けた排出バルブとを有すること
を特徴とする汚泥移送装置。
2. A sludge transfer pipe having a base end side communicating with an air supply source and a sludge transfer pipe communicating with the sludge transfer pipe, and each end projecting to both sides of the sludge transfer pipe. A plurality of sludge suction pipes that open as sludge suction ports at a position below the sludge transfer pipe, a sludge discharge pipe having one end communicating with the tip side of the sludge transfer pipe, and the other end opening as a discharge port outside the tank; A sludge transfer device comprising: a discharge valve provided in a discharge pipe.
【請求項3】 汚泥排出管が他端に排出口とは別途に排
気バルブを介して分岐した排気管を有し、排気管が槽内
の液面上もしくは液中に排気口として開口することを特
徴とする請求項1又は2に記載の汚泥移送装置。
3. The sludge discharge pipe has, at the other end, an exhaust pipe branched via an exhaust valve separately from the discharge port, and the exhaust pipe is opened as an exhaust port on the liquid surface in the tank or in the liquid. The sludge transfer device according to claim 1 or 2, wherein:
JP2001000890A 2001-01-09 2001-01-09 Sludge transfer device Expired - Lifetime JP4618899B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2001000890A JP4618899B2 (en) 2001-01-09 2001-01-09 Sludge transfer device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2001000890A JP4618899B2 (en) 2001-01-09 2001-01-09 Sludge transfer device

Publications (2)

Publication Number Publication Date
JP2002205095A true JP2002205095A (en) 2002-07-23
JP4618899B2 JP4618899B2 (en) 2011-01-26

Family

ID=18869588

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2001000890A Expired - Lifetime JP4618899B2 (en) 2001-01-09 2001-01-09 Sludge transfer device

Country Status (1)

Country Link
JP (1) JP4618899B2 (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008168295A (en) * 2002-12-19 2008-07-24 Kato Construction Co Ltd Sludge treatment method for wetland-type water purification apparatus
KR100865920B1 (en) 2008-05-07 2008-10-29 한남환경엔지니어링(주) Apparatus and mode for sequencing batch reactor
CN104512961A (en) * 2013-09-26 2015-04-15 三菱丽阳株式会社 Air diffusion apparatus and water treatment apparatus
JP2016137469A (en) * 2015-01-29 2016-08-04 三菱レイヨン株式会社 Method and device for cleaning air diffusion pipe, and activated sludge treatment method and activated sludge treatment system

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS54168052U (en) * 1978-05-17 1979-11-27
JPS5613087A (en) * 1979-07-11 1981-02-07 Mitsui Miike Mach Co Ltd Preventing device for clogging of floating type activated sludge air diffusion device
JPH04134495U (en) * 1991-05-30 1992-12-15 株式会社クボタ Sewage septic tank
JPH07116698A (en) * 1993-10-28 1995-05-09 Toho Gas Co Ltd Recovering device for precipitated sludge
JPH10128380A (en) * 1996-10-29 1998-05-19 Kansai Kako Kk Liquid lifting pipe for air-left
JP2000197893A (en) * 1999-01-08 2000-07-18 Hitachi Chem Co Ltd Air supply device for septic tank
JP2000334433A (en) * 1999-05-27 2000-12-05 Cleanup Corp Garbage treating system and its treatment

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS54168052U (en) * 1978-05-17 1979-11-27
JPS5613087A (en) * 1979-07-11 1981-02-07 Mitsui Miike Mach Co Ltd Preventing device for clogging of floating type activated sludge air diffusion device
JPH04134495U (en) * 1991-05-30 1992-12-15 株式会社クボタ Sewage septic tank
JPH07116698A (en) * 1993-10-28 1995-05-09 Toho Gas Co Ltd Recovering device for precipitated sludge
JPH10128380A (en) * 1996-10-29 1998-05-19 Kansai Kako Kk Liquid lifting pipe for air-left
JP2000197893A (en) * 1999-01-08 2000-07-18 Hitachi Chem Co Ltd Air supply device for septic tank
JP2000334433A (en) * 1999-05-27 2000-12-05 Cleanup Corp Garbage treating system and its treatment

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008168295A (en) * 2002-12-19 2008-07-24 Kato Construction Co Ltd Sludge treatment method for wetland-type water purification apparatus
KR100865920B1 (en) 2008-05-07 2008-10-29 한남환경엔지니어링(주) Apparatus and mode for sequencing batch reactor
CN104512961A (en) * 2013-09-26 2015-04-15 三菱丽阳株式会社 Air diffusion apparatus and water treatment apparatus
JP2016137469A (en) * 2015-01-29 2016-08-04 三菱レイヨン株式会社 Method and device for cleaning air diffusion pipe, and activated sludge treatment method and activated sludge treatment system

Also Published As

Publication number Publication date
JP4618899B2 (en) 2011-01-26

Similar Documents

Publication Publication Date Title
ES2282329T3 (en) AIR DIFFUSER AND CLEANING METHOD OF THE SAME.
JP5062140B2 (en) Method of operating diffuser and diffuser
JP2001212587A (en) Method and apparatus for diffusing air of membrane separation activated sludge method
AU1852102A (en) Multistage immersion type membrane separator and high-concentration wastewater treatment facility using same
JP2002205095A (en) Sludge transporting apparatus
JP4530621B2 (en) Cleaning method for air diffuser
JP2002166290A (en) Diffuser and method for washing the same
JP3744425B2 (en) Membrane separation wastewater treatment equipment
JP2001276875A (en) Air diffuser for dipping type membrane separation device
JPH11138190A (en) Operation method of diffuser and diffuser practicizing operation
EP0523498A1 (en) Sewage treatment apparatus
JP2001170677A (en) Air diffuser for high-concentration sewage
JP3920725B2 (en) Aeration method and aeration system
JP2004337787A (en) Membrane separation activated sludge treatment tank
JP5235632B2 (en) Aeration device and method
JP3859447B2 (en) Aeration method and apparatus
JP2002186991A (en) Air diffuser
JP4274903B2 (en) Cleaning method for air diffuser
JP4017339B2 (en) Underwater aeration equipment
JP2001087792A (en) Diffuser
JP2004066025A (en) Difer
WO2017122678A1 (en) Air diffusion device and air diffusion hole cover
JPH0696153B2 (en) Sewage purification device
KR100626296B1 (en) Apparatus for manufacturing Ozone sterilized water
JP2761463B2 (en) Drain pumping device

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20070925

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20090310

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20100928

A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20101026

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

Free format text: PAYMENT UNTIL: 20131105

Year of fee payment: 3

R150 Certificate of patent or registration of utility model

Ref document number: 4618899

Country of ref document: JP

Free format text: JAPANESE INTERMEDIATE CODE: R150

Free format text: JAPANESE INTERMEDIATE CODE: R150

EXPY Cancellation because of completion of term